INDUSTRIAL SOLVENTS HANDBOOK Fifth Edition
Edited by
Ernest W. Flick
NOYES DATA CORPORATION Westwood, New Jersey, U.S...
121 downloads
1467 Views
44MB Size
Report
This content was uploaded by our users and we assume good faith they have the permission to share this book. If you own the copyright to this book and it is wrongfully on our website, we offer a simple DMCA procedure to remove your content from our site. Start by pressing the button below!
Report copyright / DMCA form
INDUSTRIAL SOLVENTS HANDBOOK Fifth Edition
Edited by
Ernest W. Flick
NOYES DATA CORPORATION Westwood, New Jersey, U.S.A.
Copyright 8 1998 by Ernest W.Rick No part of this book may be reproduced or utilized in any form or by any means, electronic or mechanical, including photocopying, recording or by any information storage and retrieval system, without permission in writing from the Publisher. Library of Congress Catalog Card Number: 98-5137 ISBN: 0-8155-1413-1 Printed in the United States Published in the United States of America by Noyes Data Carporation Fairview Avenue, Westwood, New Jersey 07675
10 9 8 7 6 5 4 3 2 1
Industrial solvents handbook / edited by Ernest W. Rick. -- 5th ed. p. an. Includes bibliographical references and index. ISBN 0-8155-1413-1 1. Solvents--Handbook, manuals, etc 1. Rick, Ernest W. TP247.5.153 1998 661'.807--dc21
98-5137
CIP
NOTICE To the best of our knowledge the information in this publication is accurate; however, the Publisher does not assume any responsibility or liability for the accuracy or completeness of, or consequences arising from, such information. This book does not purport to contain detailed user instructions, and by its range and scope could not possibly do so. Mention of trade names or commercial products does not constitute endorsement or recommendation for use by the Author or Publisher. industrial solvents could be toxic, and therefore due caution should always be exercised in the use of these potentially hazardous materials. Final determination of the suitability of any information or product for use contemplated by any user, and the manner of that use, is the sole responsibility of the user. We strongly recommend that users seek and adhere to a manufacturer's or supplier's current instructions for handling each material they use. The reader is cautioned to consult the supplier in case of questions regarding current availability.
viii
Foreword Completely revised, and vastly expanded, this well-established and successful reference volume is designed principally for the chemical and other process industries, but will be found useful by anyone needing the latest pertinent data on industrial solvents. This Fifth Edition is uniquely helpful when it becomes necessary to select a new solvent on a competitive or comparative basis: when the customary solvent, employed hitherto, might no longer be available, or can no longer be used because of environmental reasons; or when prices have risen to such an extent that an existing process must be redesigned to make it economically feasible again. The over 1,200 tables in this book contain basic data on the physical properties of most solvents and on the solubilities of a variety of materials in these solvents. Even phase diagrams for multicomponent systems are included. Particularly valuable are the HPLC and UV data for various solvents provided in the last chapter. The contents of the tables were selected by the editor mainly from manufacturers' literature at no cost to, nor influence from, the manufacturers or distributors of these solvents. The source of each table is indicated by a reference number following the title. A complete set of references is found at the end of the book, as well as a trade name index. The vast amount of information contained in the book is evidenced at once in the large table of contents, which is organized by chemical groups and also serves as the index. An abbreviated summary of the contents is given below, indicating the number of tables in each category. Hydrocarbon Solvents ........................ 143 Halogenated Hydrocarbons .................... 64 Nitroparaffins .............................. 10 Organic Sulfur Compounds .................... 34 Mononhydric Alcohols ........................ 182 Polyhydric Alcohols .......................... 227 Phenols . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 1 Aldehydes ................................ 13 Ethers . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 49 Glycol Ethers .............................. 80 Ketones .................................. 50 Acids .................................... 21 Amines .................................. .193 Esters ................................... 84 HPLC and UV Data. ......................... 84 Advanced composition and production methods developed by Noyes Data Corporation are employed to bring this durably bound book to you in a minimum of time. Special techniques are used to close the gap between "manuscript" and "completed book." In order to keep the price of the book to a reasonable level, it has been partially reproduced by photo-offset directly from the original material and the cost saving passed on to the reader. Due to this method of publishing, certain portions of the book may be less legible than desired.
vii
Contents and Subject Index .................................................................................. HYDROCARBON SOLVENTS ........................................................................ Paraffins .................................................................................... 2.1 Methane ......................................................................... 2.2 Ethane ........................................................................... 2.3 Propane .......................................................................... 2.4 lsobutane ......................................................................... 2.5 n-Butane ......................................................................... 2.6 2.2-Dimethylpropane ................................................................ 2.7 lsopentane ........................................................................ 2.8 n-Pentane ........................................................................ 2.9 2. 2-Dimethylbutane ................................................................. 2.10 2.3-Dimethylbutane ................................................................. 2.11 2-Methylpentane ................................................................... 2.12 3-Methylpentane ................................................................... 2.13 n-Hexane ....................................................................... 2.14 2.4-Dimethylpentane ............................................................... 2.15 2.3-Dimethylpentane ............................................................... 2.16 3-Methylhexane .................................................................. 2.17 n-Heptane ....................................................................... 2.18 2.2. 4-Trimethylpentane ............................................................. 2.19 2.3. 4-Trimethylpentane ............................................................. 2.20 Mixed Trimethylpentanes ............................................................ 2.21 Mixed Dimethylhexanes ............................................................. 2.22 n-Oxtane ........................................................................ 2.23 2.2. 5-Trimethylhexane .............................................................. 2.24 n-Nonane ....................................................................... 2.25 n-Decane ....................................................................... 2.26 n-Undecane ..................................................................... 2.27 n-Dodecane ..................................................................... 2.28 n-Tridecane ...................................................................... 2.29 n-Tetradecane .................................................................... 2.30 n-Pentadecane ................................................................... 2.31 n-Hexadecane ................................................................... 2.32 n-Heptadecane ................................................................... 2.33 n-Octadecane .................................................................... 2.34 n-Nonadecane ................................................................... 2.35 n-Elcosane ...................................................................... Cycloparaffins ............................................................................... 2.36 Cyclopentane ..................................................................... 2.37 Methylcyclopentane ................................................................ 2.38 Cyclohexane ..................................................................... 2.39 1.1-Dimethylcyclopentane ........................................................... 2.40 1.2- and 1.3-Dimethylcyclopentane .................................................... 2.41 Methylcyclohexane ................................................................. 2.42 trans-I. &Dimethylcyclohexane ....................................................... 2.43 cis-1 4-Dimethylcyclohexane ......................................................... 2.44 Mixed 1.4-Dimethylcyclohexanes ...................................................... 2.45 trans-1 2-Dimethylcyclohexane ....................................................... 2.46 cis-I 2-Dimethylcyclohexane ......................................................... 2.47 Mixed 1.2-Dimethylcyclohexane ....................................................... 2.48 Ethylcyclohexane .................................................................. 2.49 lsopropylcyclohexane ............................................................... Olefins ..................................................................................... 2.50 Ethylene ........................................................................ INTRODUCTION
. ..
1 3 3 3 3 4 4 5
5 6 7 7 8 8 9 10 11 11 12 12 12 13 13 13 14 14 15 15 16 16 17 17 17 18 18 18 18 19 19 19 20 20 21 22 22 23 23 23 24 24 25 25 26 27 27
x
Contents and Subject Index 2.51 2.52 2.53 2.54 2.55 2.56 2.57 2.58 2.59 2.60 2.61 2.62 2.63 2.64 2.65 2.66 2.67 2.68 2.69 2.70 2.71 2.72 2.73 2.74 2.75 2.76 2.77 2.78 2.79 2.80 2.81 2.82 2.83 2.84 2.85 2.86 2.87 2.88 2.89 2.90 2.91 2.92 2.93 2.94 2.95
....................................................................... ...................................................................... ........................................................................ ................................................................... ..................................................................... .................................................................. ................................................................. ................................................................. ................................................................... ....................................................................... .................................................................... .................................................................. ................................................................. .............................................................. .......................................................... ................................................................ ............................................................. ........................................................... ................................................................ ................................................................ ....................................................................... ................................................................. ........................................................... .......................................................................
Propylene Isobutylene Butene-1 trans-Butene-2 cis-Butene-2 Mixed 2-Butenes 3-Methylbutene-1 2-Methylbutene-1 Methylbutene-2 Pentene-1 cis-Pentene-2 trans-Pentene-2 Mixed 2-Pentenes 3.3-Dimethylbuten e-1 Mixed 2.3-Dimethylbutenes 4-Methylpentene-1 cis-4-Methylpentene-2 trans-4-Methylpentene-2 Mixed 4-Methyl-2-Pentenes ......................................................... 2-Methylpentene-1 2-Methylpentene-2 Hexene-1 cis-Hexene-2 .................................................................... Mixed 2-Hexenes Mixed 2- and 3-Hexenes Heptene-1 cis-Heptene-2 .................................................................... Mixed 2-Heptenes ................................................................. Mixed 3-Heptenes 2.4.4-Trirnethylpentene-1 2.4.4-Trirnethylpenten e-2 ........................................................... Mixed Diisobutylenes . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . Octene-1 cis-Octene-2 ..................................................................... Mixed 2-Octenes Mixed Octenes Nonene-1 Decene-1 Undecene-1 ..................................................................... Dodecene-1 ..................................................................... Tridecene-1 Tetradecene-1 Butadiene-13 Isoprene Piperylene
................................................................. ...........................................................
........................................................................ .................................................................. .................................................................... ....................................................................... .......................................................................
...................................................................... .................................................................... .................................................................... ........................................................................ ....................................................................... Cycloolefins ................................................................................. 2.96 Cyclopentene ..................................................................... 2.97 Cyclohexene . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2.98 4-Vinylcyclohexene-1 .............................................................. 2.99 Mixed Methylcyclohexenes ........................................................... 2.100 Cyclooctadiene-1. 5 ................................................................ Aromatics .................................................................................. 2.101 Benzene ........................................................................ 2.102 Toluene ......................................................................... 2.103 Ethylbenzene ..................................................................... 2.104 p-Xylene ......................................................................... 2.105 rn-Xylene ....................................................................... 2.106 o-Xylene ........................................................................ 2.107 Curnene . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2.108 n-Propylbenzene .................................................................. 2.109 Pseudocurnene ................................................................... 2.110 n-Butylbenzene ................................................................... 2.111 lsobutylbenzene ................................................................... 2.112 Hydrocarbon Solvents .............................................................. sec-Butylbenvene 2.113 tert-Butylbenzene .................................................................
27 27 28 28 28 29 29
30 31 31 32 32 32 33 33 33
34 35 35 36 36 37 37 37 38 38 38 39 39 39 40 40 41 41 41 42 42 42 42 42 43 43 43 44 44 44 44 45 46 46 47 47 47 48 48 49 49 50 50 51 51 51 52 53
53
Contents and Subject Index 2.114 1-Phenylbutene-2 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2.115 sec-Amylbenzene . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2.116 Mixed Amylbenzenes . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . Terpenes . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2.1 17 DIPENTENE No. 122 Terpene Solvent . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2.1 18 SOLVENOL 2 Terpene Solvent ....................................................... 2.1 19 SOLVENOL 226 Terpene Solvent . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2.120 HERCULES Steam-Distilled Wood Turpentine . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2.121 HERCULES alpha-Pinene . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2.122 Selected Properties of Some Common Terpene Solvents . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2.123 Arizona Terpene Products . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . ComparativeData . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . Amoco PANASOLSolvents . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2.124 2.125 Ashland Aliphatic and Aromatic Solvents ................................................ 2.126 Chemcentral Solvents (Aliphatic and Aromatic) ............................................ 2.127 Crowley Solvents . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2.128 Dynaloy Solvents . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2.129 Eastman Solvents and Diluents ....................................................... 2.130 Exxon Hydrocarbon Solvefits . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2.131 Fina Aromatic Solvents . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2.132 Hoechst Celanese Methyl Isobutyl Ketone . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2.133 KendalVAmalie. Wlco Special Solvents . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2.134 Mobil Oil Aliphatic and Aromatic Solvents . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2.135 Penreco Hydrocarbon Solvents . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2.136 Phillips 66 Hibh P u r i i Hydrocarbon . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2.137 Shell Chemical Solvents . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2.138 Sunoco Chemicals Solvents . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2.139 3M SCOTCH-GRIP Solvents No. 2 and No. 3 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2.140 Total Petroleum Special Solvent . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2.141 UCARSolvents . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2.142 Unocal Aliphatic and Aromatic Hydrocarbons . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2.143 VistaLPASolvents . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
HALOGENATED HYDROCARBONS . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . ChlorlnatedHydrocarbons . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3.1 AllylChlorice . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3.2 n-Amyl Chloride . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3.3 Mixed Amyl Chlorides . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3.4 Benzyl Chloride . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3.5 n-Butyl Chloride . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3.6 sec-Butyl Chloride . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3.7 Butyryl Chloride . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3.8 Caprylyl Chloride . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3.9 Carbon Tetrachloride . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3.10 Chlorinated Butane Derivatives . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3.1 1 Chlorinated Hydrocarbons . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3.12 Chlorinated Organic Solvents . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3.13 CHLOROWAX Liquid Chlorinated Paraffins. Waxes and Alpha Olefins ......................... 3.14 Chlorobenzenes-Vapor Pressures . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3.16 Chloromethylene Compounds . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 0- and p-Chlorotoluenes . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3.17 3.18 p-Chlorotoluene . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . HALSO99 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3.19 3.20 HALSOAG 125 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3.21 o-Dichlorobenzene . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3.22 p-Dichlorobenzene . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3.23 Dichlorodiisopropyl Ether . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3.24 Dichloroethylene . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3.25 Dichloroethyl Ether . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3.26 Dichlorohydrin . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3.27 Dichloromethane . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3.28 Dichloropentanes . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3.29 2.4-Dichlorotoluene . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3.30 Epichlorohydrin . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3.31 Ethyl Chloride . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
xi 54
54 54 55 55 55 56 56 57 57 58 61 61 62 63 64 65 68 73 74 74 75 78 81 81 82 90 93 93 96 99 101 103 103 103 103 103 104 104 104 105 105 106 107 107 107 108 111 113 114 114 115 115 116 116 117 117 118 118 119 120 120 121 121
xii
Contents and Subject Index Ethylene Chlorohydrin . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . Ethylene Dichloride ............................................................... 3.34 2-Ethylhexyl Chloride .............................................................. 3.35 Glycerol a-Monochlorohydrin 3.36 Hexachloroethane ................................................................ 3.37 n-Hexyl Chloride ................................................................. 3.38 Methylene Chloride 3.39 Isopropyl Chloride 3.40 Methyl Chloride . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3.41 Monochlorohydrin ................................................................. 3.42 Pentachloroethane 3.43 Perchloroethylene 3.44 Propylene Chlorohydrin 3.45 Propylene Dichloride .............................................................. 3.46 1.1.2. 2-Tetrachloroethane .......................................................... 3.47 Tetrachloroethylene ............................................................... 3.48 Trichlorobenzenes ................................................................ 3.49 1.1. 1-Trichloroethane .............................................................. 3.50 1 1 2-Trichloroethane .............................................................. 3.51 Trichloroethylene ................................................................. 3.52 Density of Chlorinated Solvents ...................................................... 3.53 Vapor Pressure of Chlorinated Solvents 3.54 Trichloropropane 3.55 Triglycol Dichloride 3.56 Vinylchloride .................................................................... 3.57 Vinylidene Chloride ............................................................... ComparativeData 3.58 Alpha Cleaning Solvents . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3.59 Ashland Chlorinated Solvents ........................................................ 3.60 Chemcentral Chlorinated Solvents .................................................... 3.61 Dow Chemical Chlorinated Solvents 3.62 Vertrel Cleaning Agents ............................................................ 3.63 Occidental Chemical (OXSOL Solvents) . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3.64 3M Hydrofluorether
123 123 124 124 125 126 126 127 127 130 130 130 132 132 133 134 136 136 142 142 145 145 146 146 147 147 149 149 150 150 151 160 169 195
Industrial Amines Ranked in Order of Decreasing Base Strength .............................. Comparing Amines for Safety ........................................................ NlPAR640 ...................................................................... COMSOL 101-X ................................................................. COMSOL280 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . COMSOL 820 ...................................................................
211 211 212 213 214 215 215 216 218 220 221
3.32
3.33
........................................................
............................................................... ................................................................
................................................................ ................................................................ ............................................................
..
................................................ ................................................................. ................................................................
........................................................................... ...................................................
............................................................... NITROPARAFFINS .............................................................................. 4.1 Angus Nitroparaffins ............................................................... 4.2 Angus NitroAlcohols .............................................................. 4.3 Angus Primary Amino Alcohols ....................................................... 4.4 Angus DMAP-80 ................................................................. 4.5 4.6 4.7 4.8 4.9 4.10
..................................................................
ORGANIC SULFUR COMPOUNDS 5.1 Carbon Disulfide . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.2 Typical DMSO Properties ........................................................... 5.3 Vapor Pressure vs Temperature for DMSO .............................................. 5.4 Specific Gravity of DMSO as a Function of Temperature .................................... 5.5 DMSO Viscosity as a Function of Temperature ........................................... 5.6 Comparative Hygroscopicities of DMSO at Various Relative Humidities at 22°C 5.7 Initial Sorption Rates of DMSO at Various Relative Humidities at 22% ......................... 5.8 Freezing Temperatures for DMSO-Solvent Binary System .................................. 5.9 Freezing Point for DMSO-Water Solutions . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.10 Freezing Point Curves for DMSO-Water Solutions ....................................... 5.11 Heat of Mixing of DMSC-4-40 System at 22°C .......................................... 5.12 Specific Gravity of DMSO-Water Solutions ............................................. 5.13 Viscosity of DMSO-Water Solutions .................................................. 5.14 Results of Reflux of DMSO for 24 Hours with Various Compounds ............................ 5.15 Thermal Stabiliof DMSO .......................................................... 5.16 Refluxing of DMSO and Mixtures for Shorter Periods ...................................... 5.17 Effect of Heating DMSO with Concentrated Acids .........................................
222 222 223 224 224 224 225 225 225 226 226 226 227 227 227 228 228 228
...................
Contents and Subject Index 5.18 5.19 5.20 5.21 5.22 5.23 5.24 5.25 5.26 5.27 5.28 Sulfolane 5.29 5.30
5.31 5.32 5.33 5.34
................................................ ............................................... .............................. ................................................
Solubility of Organic Materials in DMSO Solubility of Resins and Polymers in DMSO ............................................. Solubility of Inorganic Materials in DMSO Solubility of Gases in DMSO at Atmospheric Pressure and 20% Solubility Parameters of Strong Solvents DMSO as a Solvent Replacement . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . Hansen Solubility Parameters of Polymer Envelopes ....................................... Polymer Solvency of DMSO/Tetralin Mixtures ............................................ Polymer Solvency of DMSO/MIKE Mixtures Solvent Viscosities ................................................................ Solvent Evaporation Times ..........................................................
..............................................
..................................................................................
.............................................................
Properties ofSulfolane Solubility of Sulfolane in Various Chemical Compounds .................................... Solubility of Various Chemical Compounds in Sulfolane .................................... Thermal Stability of Sulfolane ........................................................ Comparative Freezing Point Depression Specific Gravity ..................................................................
................................................
MONOHYDRIC ALCOHOLS ........................................................................ Methanol .................................................................................. 6.1 Physical Properties of Methanol ...................................................... 6.2 Properties of Aqueous Solutions of Methanol ............................................ 6.3 Freezing Points of Methanol-Water Solutions ............................................ 6.4 Density and Specific Gravity of Methanol-Water Solutions at 15'C ............................ Density and Specific Gravity of ethanol-Water Solutions at 30'C ............................. 6.5 Resultant Volume When Methanol and Water are Mixed .................................... 6.6 6.7 Solubility of Methanol in Gasoline from 15' to 30% ........................................ 6.8 Liquid Density of Methanol .......................................................... 6.9 Liquid Heat Capacity of Methanol ..................................................... 6.10 Vapor Heat Capacity of Methanol ..................................................... 6.11 Heat of Vaporization of Methanol ..................................................... 6.12 SurfaceTension of Methanol ........................................................ 6.13 Liquid Thermal Conductivity of Methanol ................................................ 6.14 Vapor Thermal Conductivity of Methanol ................................................ 6.15 Vapor Pressure of Methanol ......................................................... 6.16 Vapor Viscoslty of Methanol ......................................................... 6.17 Liquid Viscosity of Methanol ......................................................... 6.18 Azeotropes of Methanol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . EthylAlcohol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 6.19 Physical Properties of Anhydrous Ethyl Alcohol ........................................... 6.20 Physical Properties of 95% Ethanol .................................................... 6.21 Properties and Specifications of Ethyl Alcohol ............................................ 6.22 Conversion Tableweight and Volume Percent of Ethyl Alcohol in Ethyl Alcohol-Water Mixtures ...................................................................... Index of Refraction of Ethyl Alcohol-Water Mixtures at W'F ................................. 6.23 6.24 Heat of Solution of Ethyl Alcohol in Water 6.25 Resultant Volume When Ethyl Alcohol and Water are Mixed ................................. 6.26 Boiling Points of Ethyl Alcohol-Water Solutions ........................................... 6.27 Permanganate TimeTest ........................................................... 6.28 Freezing Points of Ethyl Alcohol-Water Mixture .......................................... 6.29 Viscosity of Ethyl Alcohol-Water Mixtures ............................................... 6.30 Flash Point of Aqueous Ethyl Alcohol Solutions 'C and 'F vs Vol % Ethanol ..................... 6.31 Specific Heat of Aqueous Solutions of Ethanol ........................................... 6.32 Surface Tension of Pure Ethanol at Various Temperatures .................................. 6.33 Latent Heat of Vaporization of Ethyl Alcohol ............................................. 6.34 Heat Capacity of Ethyl Alcohol at Various Temperatures .................................... 6.35 Volumetric Equivalents ............................................................. 6.36 Ethyl Alcohol-Water Mixtures ........................................................ 6.37 Specially Denatures Alcohols 6.38 Authorized Denaturants for SDA 388 .................................................. Denaturants Authorized for Completely Denatured Alcohol (CDA) and Specially 6.39 Denatured Alcohol (SDA) . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . Uses of Specially Denatured Alcohol .................................................. 6.40 6.41 Filmex Special Industrial Solvent Formulations ...........................................
...............................................
........................................................
xiii 229 230 232 233 233 233 234 234 235 235 235 236 236 236 236 236 237 237 238 238 238 239 239 240 241 242 242 243 243 244 244 245 245 246 246 247 247 248 249 249 249 249 250 250 251 251 251 252 252 253 254 254 254 255 255 256 256 262 277 278 279 281
xiv
Contents and Subject Index 6.42 6.43 6.44 6.45 6.46 6.47
........................................ 281 ..................................................... 281 ................................. 282 ........................... 283 ...................................... 284 .......................................................... 284 .......................................................... 285 ........................... 286 ................................... 287 ........................................................... 287 ............................................... 289 ........................................................... 289 ............................................................. 291 ........................................................................ 292 ................................................ 292 ...................................................... 293 ........................................................ 294 ....................................................... 294 ........................................................ 294 ......................................................... 294 ....................................................................... 295 ....................................... 295 ............................................ 295 296 . . . . . . . . . . . 297 .................... 297 .......................... 297 ...................................................... 298 .............................. 299 . ........................................................... 299 ....................... 299 .................... 299 .................................................................. 300 ............................................ 300 ............................................................................. 301 ................................................. 301 ................................... 302 ................................. 302 ................................. 303 ....................................................... 303 ............................................................................ 304 ................................................. 304 ....................................................... 304 ............................ 305 ........................................................................... 305 ................................................ 305 ...................................................... 305 ........................................................................... 306 ................................................ 306 306 ........................................................................ 307 ............................................. 307 ...................................................................... 307 ........................................... 307 ........................................................................... 308 ................................................ 308 ...................................................... 308 ......................................................................... 309 .............................................. 309 .................................................... 309 .................................................................... 310
Completely Denatured Alcohol (CDA) Formulations Proprietary Solvent Formulations Punctilious Specially Denatured Alcohol (SDA) Formulations Composition and Typical End Uses of Specially Denatured Alcohols Composition of Completely Denatured Alcohol (CDA) Composition of Synasol Proprietary Solvents. Anhydrol Special Industrial Solvents. and lnksolvlnk Solvents 6.48 Typical Physical Properties 6.49 Densities of Pure Ethanol-Water Mixtures at Various Temperatures Vapor Pressure of Pure Ethanol at Various Temperatures 6.50 Constant Boiling Mixtures 6.51 6.52 Proof Definitions and Conversion Factors 6.53 Proof Conversion Tables 6.54 Azeotropes of Ethanol n-PROPYLALCOHOL 6.55 Physical Properties of n-Propyl Alcohol 6.56 Azeotropes of n-Propyl Alcohol 6.57 n-Propanol-Water-Benzene 6.58 n-Propanol-Water-n-Butanol 6.59 n-Propanol-Water-Heptane 6.60 n-Propanol-Water-Hexane ISOPROPYLALCOHOL 6.61 Physical Properties of Anhydrous Isopropyl Alcohol Physical Properties of 91% Isopropyl Alcohol 6.62 6.63 Specific Gravity of Isopropyl Alcohol-Water Mixtures ...................................... Vapor-Liquid Compositions of Isopropyl Alcohol-Water Mixtures and Their Boiling Points 6.64 6.65 Refractive Index vs Composition of Isopropyl Alcohol-Water Mixtures at 25'C Isopropyl Alcohol-Water: Kinematic Viscosity vs Composition at 25°C 6.66 Azeotropes of Isopropyl Alcohol 6.67 6.68 The Effect of Isopropyl Alcohol on the Dilution Ratio of Solvents Viscosity of RS H Sec Nitrocellulose in Mixtures of Toluene. Isopropyl Alcohol and 6.69 Methyl Isobutyl Ketone 6.70 Methanol-Isopropyl Alcohol: Boiling Point vs Composition at 760 mm Hg 6.71 Methanol-Isopropyl Alcohol: tiquid-Vapor Equilibria at Atmospherii Pressure 6.72 Vapor Pressure of Isopropyl Alcohol (Anhydrous) and sec-Butyl Alcohol at Various Temperatures 6.73 Specific Gravities of Alcohols vs Temperature n-Butyl Alcohol Physical Properties of n-Butyl Alcohol 6.74 Vapor Pressure of Butyl Alcohol at Various Temperatures 6.75 6.76 Solubiliy of Water in Butyl Alcohol at Various Temperatures 6.77 Solubiliy of Butyl Alcohol in Water at Various Temperatures 6.78 Azeotropes of n-Butyl Alcohol IrobutylAlcohol 6.79 Physical Properties of Isobutyl Alcohol 6.80 Azeotropes of Isobutyl Alcohol 6.81 Relative Evaporation Rates of Various Butyl Alcohols and Acetates rec-ButylAlcohol 6.82 Physical Properties of =-Butyl Alcohol 6.83 Azeotropes of sec-Butyl Alcohol tert-ButylAlcohol 6.84 Physical Properties of tert-Butyl Alcohol 6.85 Azeotropes of tert-Butyl Alcohol ...................................................... PrlmaryAmylAlcohol 6.86 Physical Properties of Primary Amyl Alcohol Prlmaryn-AmylAlcohol 6.87 Physical Properties of Primary n-Amyl Alcohol SSC-AmylAlCOhOl 6.88 Physical Properties of sec-Amyl Alcohol 6.89 Azeotropes of sec-Amyl Alcohol rec-n-AmylAlcohol 6.90 Physical Properties of sec-n-Amyl Alcohol 6.91 Azeotropes of sec-n-Amyl Alcohol tert-Amyl Alcohol, Reflned
Contents and Subject Index
..........................................
Physical Properties of Refined tert-Amyl Alcoho 6.92 Azeotropes of tert-Amyl Alcohol ...................................................... 6.93 IroamylAlcohol ............................................................................. 6.94 Physical Properties of Isoamyl Alcohol
................................................. ....................................................... ......................................................................... .............................................. ........................................................................... ................................................ .......................................................................... .............................................. ......................................................................... .............................................. ............................................................................ ................................................. .................................................. .......................................................... .......................................................................... ............................................... ..................................................... .............................................................................. .................................................. ........................................................ ............................................................................ ................................................ ............................................................................ ................................................ ......................................................................... ............................................. ............................................................................. ................................................. ....................................................... ........................................................................... ................................................ ..................................................... ............................................................................. ................................................. .............................................................................. ................................................................... ....................................... .............................................................................. ................................................... ............................................................................ ................................................. ............................................................................ ................................................. ............................................................. .............................................. ................................................. ............................................. ........................................................................... ................................................................. .............................................................. ......................................................... ........................................................... ......................................................... .................................................... ............................................................ ............................................................ ............................................................................... .................................................... .........................................................
Azeotropes of Isoamyl Alcohol 6.95 ActhreAmylAlcohol Physical Properties of Active Amyl Alcohol 6.96 FuselOll. Rellned Physical Properties of Refined Fusel Oil 6.97 YethylamylAlcohol Physical Properties of Methylamyl Alcohols 6.98 2-EthylbutylAlcohol Physical Properties of 2-Ethylbutyl Alcohol 6.99 n-HexylAlcohol 6.100 Physical Properties of n-Hexyl Alcohol 6.101 Solubility of Water in n-Hexyl Alcohol 6.102 Azeotropes ofexyl Alcohol CyclohexylAlcohol Physical Properties of Cyclohexyl Alcohol 6.103 6.104 Azeotropes of Cyclohexyl Alcohol HeptylAlcohol Physical Properties of Heptyl Alcohol 6.105 6.106 Azeotropes of Heptyl Alcohol 2-HeptylAlcohol 6.107 Physical Properties of 2-Hem Alcohol 3-HeptylAlcohol 6.108 Physical Properties of 3-Heptyl Alcohol 2-EthylhexylAlcohol Physical Properties of 2-Ethylhexyl Alcohol 6.109 n-OctylAlcohol 6.1 10 Physical Properties of n-Octyl Alcohol Azeotropes ofn-Octyl Alcohol 6.111 SW-OctylAlCOhOl 6.1 12 Physical Propetties of sec-Odyl Alcohol Azeotropes of sec-Octyl Alcohol 6.113 lsooctyl Alcohol 6.1 I4 Physical Properties of lsooctyl Alcohol Nonyl Alcohol Physical Properties of Nonyl Alxoholx319 6.115 3b..TrimethylhexylAlcohol 6.1 16 Physical Properties of 3.5.5-Trimethylhexyl Alcohol DecylAlcohol Physical Properties of Decyl Alcohol 6.117 IrodecylAlcohol 6.1 18 Physical Properties of lsodecyl Alcohol TrldecylAlcohol Physical Properties of Tridecyl Alcohol 6.1 19 OtherAlcoholsandAlcoholBlends 6.120 ALFOL Alcohol Low Range Blends C,-C, ALFOL Alcohol Pure Homologs C,-C, 6.121 ALFOL Alcohol High Range Blends C,o-&, 6.122 ALFOLTypical properties ........................................................... 6.123 ComparatlveData 6.124 Ashland Alcohols Chemcentral Alcohols 6.125 6.126 CPSChemicalAlcohol99% Eastman Latent Solvents 6.127 6.128 Hoechst Celanese Alcohols Procter and Gamble Fatty Alcohols 6.129 6.130 Shell Chemical Alcohols Union Carbide Alcohols 6.131 AllylAlcohol 6.132 Physical Properties of Allyl Alcohol 6.133 Azeotropes ofAlkylAlcohol +
xv 310 310 311 311 311 312 312 312 312 313 313 313 313 314 314 314 314 315 315 315 316 316 316 316 316 317 317 317 317 317 317 318 318 318 318 319 319 319 320 320 320 320 321 321 321 321 322 322 322 323 324 325 325 325 326 327 329 330 331 332 333 333
333
mi
Contents and Subject Index Crotyl Alcohol .............................................................................. 334 Physical Properties of Crotyl Alcohol .................................................... 334 6.134 MethylbutynylAlcohol........................................................................ 334 Physical Properties of Methylbutynyl Alcohol ............................................. 334 6.135 M~hylpentynylAlcohol....................................................................... 335 335 Physical Properties of Methylpentynyl Alcohol 6.136 Higher UnraturatedAlcoholr .................................................................. 335 6.137 Unsaturated Aliphatic Alcohols ....................................................... 335 DIa~toneAlcohol........................................................................... 335 335 6.138 Physical Properties of Diacetone Alcohol ............................................... 2-Merc~ptoethylAlcohol...................................................................... 336 6.139 Physical Properties of 2-Mercaptoethyl Alcohol .......................................... 336 2-EthylsulfonylethylAlcohol ................................................................... 336 Physical Properties of 2-Ethylsulfonylethyl Alcohol 336 6.140 l,l, I-TrHluoroethylAlcohol .................................................................... 336 6.141 Trifluoroethanol Physical Properties 336 337 6.142 Polymer Solubilities in Trifluoroethanol ................................................. 6.143 Salt Solubility (wt %) in Trifluoroethanol at 25% .......................................... 337 337 6.144 Solubility of Gases in Trifluoroethanol at 27°C ............................................ 337 6.145 Vapor Pressure vs Temperature ...................................................... 338 6.146 Freezing Point: Trifluoroethanol-Water 6.147 Infrared Spectrum ................................................................ 338 338 1H,IH$H-Tetrafluoro- I-Propyl Alcohol .......................................................... 6.148 Physical Properties of lH.lH.3H-Tetrafluoro- I-Propyl Alcohol ............................... 338 lH,1H,5H-Octafluoro- I-Pentyl Alcohol ........................................................... 339 339 6.149 Physical Properties of 1H.lH.JH-Octafluoro- 1-Pentyl Alcohol BenzylAlcohol ............................................................................. 339 339 6.150 Physical Properties of Benzyl Alcohol .................................................. 6.151 VELSICOL Benzyl Alcohol .......................................................... 339 Furfuryl Alcohol ............................................................................ 340 6.152 Physical Properties of Furfuryl Alcohol ................................................. 340 341 6.153 Vapor Pressure of Furfuryl Alcohol .................................................... 341 6.154 Pounds per Gallon of Furfuryl Alcohol at Various Temperatures .............................. 6.155 Density of Furfuryl Alcohol-Water Solutions as a Function of Composition (at 25'C. 77OF) . . . . . . . . . . . 342 342 6.156 Vapor Pressure of Furfuryl Alcohol as a Function of Temperature ............................. 343 6.157 Solubility of tiquid Organic Compounds in Furfuryl Alcohol (at 25%. 77OF) ...................... 6.158 Solubility of Solid Organic Compounds in Furfuryl Alcohol (at 25 "C. 77'F) ...................... 343 6.159 Solubility of Thermoplastic Resins in Furfuryl Alcohol (at Room Temperature) .................... 344 6.160 Effect of Time at Elevated Temperature on Certain Characteristics of Furfuryl Alcohol (Under Neutral Conditions) ........................................................ 344 6.161 Stabiliation of Furfuryl Alcohol With an Amine (at 150'C in Glass) ............................ 345 6.162 Antoxidation of Furfuryl Alcohol ....................................................... 345 TetrahydrofurfurylAlcohol .................................................................... 346 6.163 Physical Properties of Tetrahydrofurfuryl Alcohol .......................................... 346 6.164 Solubility of Various Substances in Tetrahydrofurfuryl Alcohol ................................ 346 6.165 Vapor-tiquid Equilibria in the Tetrahydrofurfuryl Alcohol-Water System ........................ 347 6.166 Specific Gravity and Pounds per Gallon of Tetrahydrofurfuryl Alcohol at Various Temperatures . . . . . . . 347 6.167 Vapor Pressure of Tetrahydrofurfuryl Alcohol ............................................ 347 6.168 Vapor-tiquid Equilibria Curve of the THFA-Water System at the Boiling Point 348 6.169 The System THFA-Water Composition Curve ............................................ 348 6.170 Specific Gravity and Pounds per Gallon ................................................ 349 6.171 Vapor Pressure (Boiling Point Method) ................................................. 349 6.172 HERCO and YARMOR Pine Oil ...................................................... 349 6.173 Hercules TERPINEOL ............................................................. 352 Other Data ................................................................................. 354 6.174 Solubility Data for Alcohols .......................................................... 354 6.1 75 Melting Points of Saturated Monohydric Alcohols ......................................... 355 355 6.176 Rate of Evaporation of Various Solvents at Room Temperature ............................... 6.177 Comparative Evaporation Rates of Alcohols ............................................. 355 6.178 Vapor Pressure of Alcohols at Various Temperatures 356 6.179 Freezing Points (Initial Crystallization) of Aqueous Solution of Alcohols ......................... 356 6.180 Specific Gravity of Aqueous Solution of Alcohols at 20'C ................................... 357 6.181 Viscosity of Ethyl Cellulose in Alcohol-Hydrocarbon Mixtures ................................ 357 358 6.1 82 Evaporation Data for Various Solvents .................................................
............................................
........................................ ...................................................
..
...............................
...................
......................................
Contents and Subject Index
xvii
POLYHYDRICALCOHOLS . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 359 EthyleneGlycol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 359 359 7.1 Physical Properties and Specifications of Ethylene Glycol ................................... 363 7.2 Boiling Points of Aqueous Ethylene Glycol Solutions ....................................... 7.3 Density of Aqueous Ethylene Glycol Solutions . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 363 7.4 Specific Gravity at 60°F of Aqueous Ethylene Glycol Solution vs Composition .................... 361 361 7.5 Freezing Points of Aqueous Ethylene Glycol Solutions . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 362 7.6 Specific Heat of Aqueous Ethylene Glycol Solutions ....................................... 362 Vapor-tiquid Composition Curves for Aqueous Ethylene Glycol Solutions ....................... 7.7 363 7.8 Vapor Pressure of Aqueous Ethylene Glycol Solutions ..................................... 7.9 Viscosity of Aqueous Ethylene Glycol Solutions . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 363 364 7.10 Relative Humectant Values of Aqueous Solutions of Ethylene Glycol . . . . . . . . . . . . . . . . . . . . . . . . . . . 7.1 1 Water Vapor Dew Points Over Aqueous Ethylene Glycol Solutions ............................ 364 7.12 Key Hygroscopictty Curve for Ethylene Glycol ............................................ 365 365 Moisture Absorption of Ethylene Glycol at Various Relative Humidities .......................... 7.13 365 7.14 Moisture Absorption of Ethylene Glycol at Various Absolute Humidities ......................... 7.15 Kinematic Viscosity of Anhydrous Ethylene Glycol and Trimethylene Glycol Solutions . . . . . . . . . . . . . . 366 Freezing Points of Anhydrous Ethylene Glycol and Trimethylene Glycol Solutions . . . . . . . . . . . . . . . . . 366 7.16 366 7.17 Azeotropes of Ethylene Glycol ....................................................... PropyleneGlycol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 367 367 7.18 Physical Properties of Propylene Glycol ................................................ 368 7.19 Propylene Glycol Specifications . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 368 Boiling Points of Aqueous Propylene Glycol Solutions ...................................... 7.20 369 7.21 Conversion Chart for Aqueous Propylene Glycol Solutions . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 369 7.22 Density of Aqueous Propylene Glycol Solutions (Percent by Weight) . . . . . . . . . . . . . . . . . . . . . . . . . . . Effect of Aqueous Propylene Glycol Solutions on Dew Points at Various Contact Temperatures . . . . . . . 370 7.23 7.24 Freezing Points of Aqueous Propylene Glycol Solutions . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 370 7.25 Heat of Vaporization of Propylene Glycol at Various Temperatures . . . . . . . . . . . . . . . . . . . . . . . . . . . . 371 371 Refractive Indices of Aqueous Propanediol Solutions at 20". 30".and 40°C ...................... 7.26 372 7.27 Relative Humectant Values of Propylene Glycol. N.F. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 7.28 Specific Gravity of Aqueous Propylene Glycol Solutions at Various Temperatures . . . . . . . . . . . . . . . . .372 373 7.29 Specific Heat of Aqueous Propylene Glycol Solutions ...................................... 7.30 Thermal Conductivity of Aqueous Propylene Glycol Solutions at Various Temperatures . . . . . . . . . . . . . 373 7.31 Total Pressure over Aqueous Propylene Glycol Solutions Versus Temperatures . . . . . . . . . . . . . . . . . . 373 373 7.32 Vapor-Liquid Composition Curves for Aqueous Propylene Glycol Solutions ...................... 374 7.33 Vapor Pressures of Aqueous Propylene Glycol Solutions ................................... 374 7.34 Viscosities of Aqueous Propylene Glycol Solutions . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 374 7.35 Azeotropes of Propylene Glycol ...................................................... If-Propanedlol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 375 375 7.36 Physical Properties of 1.3-Propanediol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 375 Freezing Points of Aqueous Solutions of 1.3-Propanediol ................................... 7.37 376 7.38 Specific Gravity of Aqueous Solutions of 1.3-Propanediol at 20' and 40% ...................... 376 1,2-Butanedlol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 376 7.39 Physical Properties of 1.2-Butanediol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 377 7.40 Specific Gravity of Aqueous 1.2-Butanediol Solutions at 20" and 40°C ......................... 377 7.41 Absolute Viscostty of Aqueous 1.2-Butanediol Solutions at 20' and 40°C ....................... 1,3-Butanediol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 377 377 7.42 Physical Properties of lb-Butanediol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 378 7.43 Freezing Point of Aqueous Solutions of 1.3-Butanediol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 378 7.44 Refractive Index and Freezing Point of Aqueous Solutions of 1.3-Butanediol .................... 378 Specific Gravity of Aqueous 1.3-Butanediol Solutions at 20" and 40°C ......................... 7.45 378 7.46 Viscosity of Aqueous Solutions of 1.3-Butanediol ......................................... 378 7.47 Absolute Viscosity of Aqueous 1.3-Butanediol Solutions at 20" and 40% . . . . . . . . . . . . . . . . . . . . . . . 379 1,4-Butanediol .............................................................................. 379 7.48 Physical Properties of 1.4-Butanediol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 379 Absolute Viscosity of Aqueous 1.4-Butanediol Solutions at 20' and 40% ....................... 7.49 379 7.50 Specific Gravity of Aqueous 1.4-Butanediol Solutions at 20" and 40°C ......................... Pf-Butanediol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 380 380 7.51 Physical Properties of 2.3-Butanediol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 7.52 Boiling Points of Aqueous levo-2. 3-Butanediol Solutions at Atmospheric Pressure . . . . . . . . . . . . . . . . 380 381 7.53 Boiling Points of Aqueous levo-2.3-Butanedio I-Ethanol Solutions ............................ 381 7.54 Boiling Points of Aqueous levo-2.3-Butanedio l-hiethanol Solutions ........................... 381 7.55 Freezing Points of Aqueous levo-2. 3-Butanediol Solutions .................................. 382 7.56 Freezing Points of Aqueous meso-dextro-2. 3-Butanediol Solutions ...........................
xviii
Contents and Subject Index
..... ..................... ..........................
Effect of meso.2. 3.Butanediol on the Freezing Point of Aqueous levo-2. 3.Butanediol Solutions 382 Freezing Points of Aqueous levo-2.3.Butanedio l.Ethanol Solutions ........................... 383 Freezing Points of Aqueous levo-2.3.Butanedio LEthylene Glycol Solutions 383 Freezing Points of Aqueous levo-2.3.Butanedio l.Methano1 Solutions 383 Freezing Points of Aqueous levo-2.3.Butanedio l.Tetrahydrofurfuryl Alcohol Solutions . . . . . . . . . . . . . 383 Kinematic Viscosity of Aqueous levo-2. 3.Butanediol Solutions. Expressed Logarithmically. as a Function of Concentration and Temperature ........................................... 384 Solutions in Relation to Concentration Kinematic Viscosity of Aqueous levo.2. 3.Butanediol 7.63 and Temperature ............................................................... 384 Kinematic Viscosity of 60% levo-2.3.Butanediol. Glycerol and Ethylene Glycol Solutions at Low 7.64 Temperatures 384 Solutions at 20°C. Expressed in Kinematic Viscosity of Aqueous levo-2.3.Butanedio l.Ethanol 7.65 Centistokes .................................................................... 384 Kinematic Viscosity of Aqueous levo-2.3.Butanedio l.Methanol Solutions at 20°C. Expressed in 7.66 Centistokes 385 l.Ethylene Glycol Solutions in 20'C Kinematic Viscosity of Aqueous levo.2.3.Butanedio 7.67 385 Expressed incentistokes ......................................................... 7.68 Kinematic Viscosity of Aqueous levo-2.3.Butanedio l.Tetrahydrofurfuryl Alcohol Solutions at 20'C. Expressed in Centistokes 385 Absolute Viscosity of Aqueous Solutions of Ethylene Glycol. levo.2.3.Butanediol. meso-dextro7.69 2.3.Butanediol and Glycerol at 20°C ................................................. 385 Optical Rotatory Power of Aqueous levo.2. 3.Butanediol Solutions at 20°C ...................... 386 7.70 Effects of Concentration and Temperature on the Specific Rotatory Power of Aqueous levo-237.71 Butanediol Solutions 386 386 7.72 Refractive Indices of Aqueous levo.2. 3.Butanediol Solutions at Different Temperatures 386 7.73 Refractive Indices of Aqueous Solutions of meso- and levo.2. 3.Butanediol at 25'C Specific Gravity of Aqueous levo-2. 3.Butanediol Solutions at 20'. 30'. and 40% . . . . . . . . . . . . . . . . . 387 7.74 387 7.75 Specific Gravity of Aqueous meso.2. 3.Butanedol Solutions at 20'. 30'. and 4O'C 7.76 Surface Tension of Aqueous Solutions of levo-2. 3.Butanediol and Ethylene Glycol . . . . . . . . . . . . . . . 387 Butanediois . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 388 388 Refractive Indices of Aqueous Butanediol Solutions at 20". 30'. and 40°C ....................... 7.77 388 Kinematic Viscosity of Aqueous Butanediol Solutions at 20" and 40°C. in Centistokes 7.78 2.Butene.1, 4.dioi 388 ............................................... 388 7.79 Physical Properties of 2.Butene-1. 4.diol 2.Butyne.1, Cdioi ........................................................................... 389 389 7.80 Physical Properties of 2.Butyne.l. 4.diol IC-Pentanedlol 389 7.81 Physical Properties of 1.5.Pentanediol 389 390 7.82 Absolute Viscosity of Aqueous 1.5.Pentanediol Solutions at 20" and 40°C 390 7.83 Specific Gravity of Aqueous 1.5-Pentanediol Solutions at 20" and 40°C 2,CPen.nediol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 390 ................................................. 390 7.84 Physical Properties of 2.4.Pentanediol NeopentylGlycol ............................................................................ 390 7.85 Physical Properties of Neopentyl Glycol 390 Pentanediols 391 7.86 Kinematic Viscostly of Aqueous Pentanediol Solutions at 20" and 40%. in Centistokes 391 7.87 Refractive Indices of Aqueous Pentanediol Solutions at 20' and 4Q°C .......................... 391 IS-Hexanediol 392 392 7.88 Physical Properties of 1.6.Hexanediol 2,5.Hexanediol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 392 7.89 Physical Properties of 1.5.Hexanediol ................................................. 392 HexyleneGiycol ............................................................................. 392 7.90 Physical Properties and Specifications of Hexylene Glycol 392 393 7.91 Freezing Points of Hexylene Glycol-Water Mixtures 393 7.92 Specific Gravity and Freezing Point of Hexylene Glycol-Water Mixtures Pinacol 394 394 7.93 Physical Properties of Pinacol 22-Diethyl-I f-Propanedloi 394 7.94 Physical Properties of 2.2.Diethyl.l. 3.Propanediol 394 2.Ethyl.1, 3.Hexanedlol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 394 7.95 Physical Properties of 2.Ethyl.l. 3.Hexanediol 394 2,5.Dimethyl.3.Hexyne.2,5 .diol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 395 5.diol .................................... 395 7.96 Physical Properties of 2.5.Dimethyl.3.Hexyne-2. 1,4.Cyclohexanedimethanol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 395 7.57 7.58 7.59 7.60 7.61 7.62
..................................................................
....................................................................
....................................................
............................................................. ............ ............... ................
.............. ...........................................................................
............................................... ............................................................................. ................................................. ...................... ........................
................................................ ............................................................................... ............. ............................................................................. .................................................
.................................. ....................................... ........................ ................................................................................... ........................................................ ................................................................... ....................................... ...........................................
Contents and Subject Index
xiu
7.97 Properties of 1.4-Cyclohexanedimethanol .............................................. 395 p-XylyieneGlycol ........................................................................... 397 Physical Properties of p-Xylylene Glycol ................................................ 397 7.98 2-Ethyl-2-Butyl-1, 3-Propanedlol ............................................................... 397 397 7.99 Physical Properties of 2-Ethyl-2-Butyl-1. 3-Propanediol ................................... 3,6-Mmethyl4Octyne-3,6-dlol ................................................................ 397 7.1 00 Physical Properties of 3.6-Dimethyl4Octyne-3. 6-diol .................................... 397 Thiodiglycol ................................................................................ 398 7.1 01 Physical Properties of Thiodiglycol .................................................... 398 7.102 Vapor Pressure of Thiodiglycol at Various Temperatures .................................... 398 MiscellaneousGlycolr ........................................................................ 399 Hydrates of Aliphatic Glycols ........................................................ 399 7.1 03 7.104 Hydrates of Cyclic Glycols .......................................................... 400 7.105 Freezing Points of Aqueous Ethylene Glycol and Propylene Glycol Solutions ..................... 401 7.1 06 Freezing Points of Various Aqueous Glycol Solutions. "C ................................... 402 Freezing Points of Various Aqueous Alcohols. Glycols and Glycerol ........................... 402 7.107 402 7.1 08 Compatibility of Coupling Solvents with Carbon Tetrachloride and Water ........................ 403 7.1 09 Key Hygroscopicity Curve ........................................................... 7.1 10 Surface Tension of Glycol-Water Systems .............................................. 403 7.1 11 Vapor Pressure of Glycols .......................................................... 403 7.112 Viscosityof Glycols ............................................................... 404 404 7.113 Water Absorption by Glycols as a Function of Time ....................................... Water Absorption by Glycols as a Function of Relative Humidity .............................. 404 7.1 14 7.1 15 Refractive Index. Specific Gravity. and Boiling Point Measurements of Various Glycols . . . . . . . . . . . . . 404 7.1 16 Relative Solvent Properties of Glycols .................................................. 405 Effect of Various Glycols on Synthetic Rubber Samples-Results Reported as % Volume and 7.117 % Weight Increase .............................................................. 405 406 7.1 18 Solubility of Cellulose Deriiatiies in Glycols ............................................. 406 Compatibility of Film Cast from 80/20 Toluene/Alcohol ...................................... 7.1 19 406 7.1 20 Relative Humectant Values .......................................................... 407 7.121 Water Vapor Dew Points Over Aqueous Ethylene Glycol Solutions ............................ Water Vapor Dew Points Over Aqueous Diethylene Glycol Solutions ........................... 407 7.122 7.123 Water Vapor Dew Points Over Aqueous Triethylene Glycol Solutions .......................... 407 7.124 Water Vapor Dew Points Over Aqueous Propylene Glycol Solutions 407 408 Water Vapor Dew Points Over Aqueous Dipropylene Glycol Solutions .......................... 7.125 408 7.126 Boiling Points of Glycols at 50 mm Hg ................................................. 408 7.127 Total Pressure Over Aqueous Ethylene Glycol Solutions M Temperature ....................... Total Pressure Over Aqueous Diethylene Glycol Solutions M Temperature ...................... 408 7.128 409 Total Pressure Over Aqueous Triethylene Glycol Solutions vs Temperature ...................... 7.129 409 7.130 Total Pressure Over Aqueous Propylene Glycol Solutions vs Temperature ...................... 7.131 Total Pressure Over Aqueous Dipropylene Glycol Solutions vs Temperature ..................... 409 410 7.132 Vapor-Liquid Composition Curves for Aqueous Ethylene Glycol Solutions ....................... 7.133 Vapor-tiquid Composition Curves for Aqueous Diethylene Glycol Solutions ..................... 410 Vapor-Liquid Composition Curves for Aqueous Triethylene Glycol Solutions ..................... 411 7.134 411 7.135 Vapor-Liquid Composition Curves for Aqueous Propylene Glycol Solutions ...................... 7.136 Vapor-tiquid Composition Curves for Aqueous Dipropylene Glycol Solutions .................... 412 412 7.137 Pour Points of Glycols ............................................................. 412 7.138 Viscosities of Anhydrous Glycols ..................................................... 7.139 Viscosities of Aqueous Ethylene Glycol Solutions ......................................... 413 7.140 Viscosities of Aqueous Diethylene Glycol Solutions ........................................ 413 7.141 Viscosities of Aqueous Triethylene Glycol Solutions 414 7.142 Viscosities of Aqueous Tetraethylene Glycol Solutions ..................................... 414 414 7.143 Viscosities of Aqueous Propylene Glycol Solutions ........................................ 414 7.144 Viscosities of Aqueous Dipropylene Glycol Solutions ....................................... 415 7.145 Viscosities of Aqueous Tripropylene Glycol Solutions ...................................... 415 7.146 Freezing Points of Aqueous Glycol Solutions ............................................ 7.147 Specific Heat of Anhydrous Glycols ................................................... 415 7.148 Specific Heats of Aqueous Glycol Solutions (BtuAbPF) ..................................... 416 7.149 Densities of Aqueous Ethylene Glycol Solutions (% by wt) 416 417 Densities of Aqueous Diethylene Glycol Solutions (% by wt) ................................. 7.1 50 7.151 Densities of Aqueous Triethylene Glycol Solutions (% by wt) ................................ 417 7.152 Densities of Aqueous Tetraethylene Glycol Solutions (% by wt) .............................. 418 7.153 Densities of Aqueous Propylene Glycol Solutions (% by wt) ................................. 418 419 Densities of Aqueous Dipropylene Glycol Solutions (% by wt) ................................ 7.154 419 7.155 Densities of Aqueous Tripropylene Glycol Solutions (% by wt) ...............................
...........................
.......................................
..................................
Contents and Subject Index
xx
.................................. 419 ............................................................. 420 ............................... 420 ................................... 420 .................................. 420 .................................. 421 ................................ 421 .................................. 421 ................................. 421 ................................ 422 ...................................... 422 .............................................. 423 ....................................................... 424 ................................................... 424 ............................................... 425 ........................................................ 425 ............................................. 426 . .................... 426 .............. 426 . . . . . . . . . . . . . . 427 .............. 427 ....................... 428 ................................. 428 ........................................... 429 ................................................ 429 ............................................................ 430 ................................................................ 430 ........................................... 430 ..................................... 431 .................................................................. 431 .............................................................. 432 ................................................ 433 .......................................................... 433 .......................................................................... 434 ......................................... 434 ........................... 434 ................................... 434 .......................................................... 435 ............................................. 436 ............................................. 437 ...................................... 437 ................................. 438 ................................. 438 ........................... 438 ................... 439 ............................................. 439 .................................................. 440 ......................................... 441 ........................................................... 441 .......................................................... 441 ............................................. 441 ............................................ 442 ........................................................................... 443 .......................................................... 443 ......................................................... 443 ............................................................ 444 ............................................................................ 444 ................................................ 444 ............................................................................ 445 ................................................ 445 ...................................... 445 .................................................. 445 ........................................ 446 ..................................................... 446 ....................................... 446
7.1 56 Surface Tensions of Aqueous Solutions of Glycols at 7 p F 7.157 Flammability of Glycols Refractive Indices of Aqueous Glycol Solutions at 7 p F (25%) 7.158 7.159 Conversion Chart for Aqueous Ethylene Glycol Solutions 7.160 Conversion Chart for Aqueous Diethylene Glycol Solutions Conversion Chart for Aqueous Triethylene Glycol Solutions 7.161 7.162 Conversion Chart for Aqueous Tetraethylene Glycol Solutions 7.163 Conversion Chart for Aqueous Propylene Glycol Solutions 7.164 Conversion Chart for Aqueous Dipropylene Glycol Solutions 7.1 65 Conversion Chart for Aqueous Tripropylene Glycol Solutions Freeze Points and Burst Points of Aqueous Solutions 7.166 7.167 Solubility of Various Compounds in Glycols 7.168 viscosity of Anhydrous Glycols 7.169 Specific Heat of Anhydrous Glycols 7.1 70 Technical Data: Ethylene Glycol Products 7.171 Ethylene Glycol Compatibility 7.172 Weight per Gallon at Various Temperatures 7.173 Weight Percent vs Volume Percent Aq Monoethylene Glycol Solutions. 20'C 7.174 Specific Gravity vs Composition @ Various Temperatures of Aqueous MEG Solutions 7.175 Specific Gravity vs Composition @ Various Temperatures of Aqueous DEG Solutions Specific Gravity vs Composition @ Various Temperatures of Aqueous TEG Solutions 7.176 7.177 Boiling Point @ 760 mm Hg vs Composition of Aqueous Glycol Solutions 7.178 Freezing Point vs Cornposition of Aqueous Glycol Solutions 7.179 Vapor Pressure vs Temperature of the Glycols 7.180 Viscosity vs Temperature of the Glycols 7.181 Fire Hazard Information 7.182 AcuteOralToxicity 7.183 Environmental Considerations. Biodegradation 7.1 84 Ethylene Glycols: Products. Grades and Specifications 7.185 Ashland Glycols 7.186 Chemcentral Polyols 7.187 Hoechst Celanese 1.3-Butylene Glycol 7.188 Occidental Ethylene Glycol Giycerol(Giyc8rine) 7.189 Physical Properties and Specifications of Glycerol Boiling Points and Specific Gravities of Aqueous Glycerol Solutions 7.190 7.191 Conversion Chart for Aqueous Glycerol Solutions (25%) 7.192 Density of Glycerol-Water 7.193 Freezing Points of Glycerol-Water Solutions 7.194 Freezing Points of Glycerol-Water Solutions 7.195 Viscosity of Aqueous Glycerol Solutions. Centipoises Hygroscopicity Curves for Glycerol and 1.3-Butylene Glycol 7.196 7.197 Hygroscopicity Curves for Glycerol and 2.3-Butyiene Glycol 7.198 Relative Humidities Over Aqueous Glycerol Solutions. 20' to 100'C Solubility of Sucrose and Dextrose in Aqueous Glycerol at 15'. 24'. and 35% 7.199 7.200 Solubility of Various Compounds in Glycerol 7.201 Specific Gravity and Percent Glycerol 7.202 Specific Gravities of Glycerol and Glycol Mixtures 7.203 Specific Heat of Glycerol 7.204 Vapor Pressure of Glycerol 7.205 Vapor Pressure of Glycerol-Water Solutions Viscosity of Glycerol Solutions in Centipoises 7.206 ComprrativeDatr 7.207 Emery CP/USP Glycerines 7.208 Procter & Gamble Glycerine 7.209 Witco Refined Glycerine 13.4-Butanetrioi 7.210 Physical Properties of 1.2.4-Butanetriol lP.6-Hexrnetrloi 7.21 1 Physical Properties of 1.2.6-Hexanetriol 7.212 Freezing Points of 1.2.6-Hexanetrio I-Water Mixtures 7.213 Vapor Pressure of 1.2.6-Hexanetriol 7.214 Solubility of 1.2. 6-Hexanetriol in Organic Solvents 7.21 5 Compatibility of 1.2. 6-Hexanetriol viscosities and Freezing Points of 1.2. 6-Hexanetriol 7.216
.
Contents and Subject Index
lnri
.......................................................................... 447 ............................................... 447 .............................................................................. 447 447 ................................................................................... 448 ....................................................... 448 ..................................................... 448 .................... 449 ...................... 449 ......................... 450 ...................................... 450 ........................ 450 ............................................................................. 451 ............................................... 451 .............................................................. 452 ...................................................... 452 PHENOLS ..................................................................................... 454 454 8.1 Phenol ......................................................................... ALDEHYDES ................................................................................... 455 Furfural ................................................................................... 455 9.1 Properties of PureFurfural .......................................................... 455 9.2 Typical Properties and Specifiiations of Furfural .......................................... 456 9.3 Solubility of Various Substances in Furfural .............................................. 457 9.4 Solubility of Selected Thermoplastic Resins in Furfural ..................................... 457 458 9.5 Specific Gravity and Pounds per Gallon of Furfural ........................................ 458 9.6 CornpositiodDensity of Furfural-Water Solutions ......................................... 459 9.7 Vapor Pressure of Furfural .......................................................... 9.8 Solution Temperature of Furfural-Water System .......................................... 459 9.9 Temperature-Composition Diagram of Furfural-Water System ............................... 460 9.10 Vapor-Liquid Equilibrium In the Furfural-Water System .................................... 460 9.11 Vapor-Liquid Composition of Furfural-Water System ...................................... 461 OtherAldehydsr ............................................................................ 461 9.12 Vapor Pressures of Various Aldehydes ................................................. 461 9.13 Physical Properties of Various Aldehydes ............................................... 462 ETHERS ...................................................................................... 463 10.1 Dimethyl Ether ................................................................... 463 10.2 Chlorodimethyl Ether .............................................................. 464 10.3 Chloromethyl Ethyl Ether ........................................................... 465 465 10.4 Ethyl Ether ...................................................................... 466 10.5 Flammability of Ethyl Ether-Oxygen-Helium Mixture ....................................... 10.6 Dichloroethyl Ether ................................................................ 466 IsopropylEther ............................................................................. 467 10.7 Properties of Pure Isopropyl Ether .................................................... 467 10.8 Vapor Pressure of Isopropyl Ether .................................................... 467 10.9 Isopropyl Ether-Water Solubility ...................................................... 467 10.10 Mutual Solubility for the System: Isopropyl Ether-Isopropyl Alcohol-Water at 25'C. % wt . . . . . . . . . . . 468 10.11 Conjugate Solutions in the System: Isopropyl Ether-Isopropyl Alcohol-Water at 25'C. % wt . . . . . . . . . 469 10.12 Miscibility of Isopropyl Ether-Isopropyl Alcohol-Water at 25% ............................... 469 Azeotropic Information-Isopropyl Ether ................................................. 470 10.13 10.14 Vapor Pressure of Isopropyl Ether at Various Temperatures ................................. 471 10.15 Specific Gravity of sopropyl Ether vs Temperature ........................................ 471 Mutual Solubility and Specific Gravity of Isopropyl Ether. Water and Isopropyl Alcohol at 25'C . . . . . . . . 471 10.16 472 10.17 n-Butyl Ether .................................................................... 10.18 Diamyl Ether .................................................................... 473 10.19 n-Hexyl Ether ................................................................... 473 474 10.20 Solubility Data for Various Ethers ..................................................... 474 10.21 Comparative Evaporation Rates of Various Ethers ........................................ 475 10.22 Specific Gravities of Various Ethers ................................................... 476 10.23 Vapor Pressure of Various Ethers ..................................................... 10.24 Ethylene Oxide .................................................................. 478 10.25 Enthalpy and Entropy of Ethylene Oxide ................................................ 478 Trlmethyolpropane Physical Properties of Trimethylolpropane 7.217 Pentaerythritol 7.218 Physical Properties of Pentaerythritol .................................................. Sorbitol 7.219 Physical Properties ofSorbiito1 Boiling Point of Sorbitol Solutions 7.220 7.221 Hydrogenolysis of Sorbitol and Glycerol at a Hydrogen Pressure of 2.000 psi 7.222 Hydrogenolysis of Sorbitol at 215% and a Hydrogen Pressure of 2.000 psi Phase Diagram of Sorbitol Solubility in Hydroalcoholic Liquids at 35% 7.223 7.224 Solubility of Sorbitol in Hydroalcoholic Liquids at 25°C 7.225 . Viscosity Curve for Pure d-Sorbitol Solutions of Various Concentrations SugarAlcoholr 7.226 Physical Properties of the Sugar Alcohols Mircellan~urPolyhydrlcAlcoholr 7.227 Hydrates of Polyhydric Alcohols
xxii
Contents and Subject Index 10.26 10.27 10.28 10.29 10.30 10.31 10.32 10.33 10.34 10.35 10.36 10.37 10.38 10.39 10.40 10.41 10.42 10.43 10.44 10.45 10.46 10.47 10.48 10.49
................................................................. .......................... ............................................................... .............................................................. ....................................................................... ................................................................ .................................................................. ........................................................... .................................................................. ............................................................... .................................................. ............................................................... ................................................................... .................................................................. ......................................................
Propylene Oxide Freezing Points of Solutions of Ethylene Oxide and Propylene Oxide 1.2.Butylene Oxide CARDOUTENC-513 I. 4-Dioxane .................................................................... Trioxane VinylMethyl Ether VinylEthylEther Vinyl 2-Chloroethyl Ether Vinyl Butyl Ether Vinyllsobutyl Ether Vinyl 2-Ethylhexyl Ether ............................................................ Typical Properties of the vinyl Ethers Phenyl Methyl Ether Dibenzyl Ether Diphenyl "Oxide Miscellaneous Alkyl Aryl Ethers Furan .......................................................................... 2-Methylfuran ................................................................... Tetrahydrofuran .................................................................. 2.3-Dihydropyran Tetrahydropyran Tetrahydropyran-2-Methanol ........................................................ Terpinyl Methyl Ether ..............................................................
................................................................. ..................................................................
GLYCOLETHERS ............................................................................... 11 1 ARCOSOLV Ethylene and Propylene Glycol Ethers ....................................... 11.2 Ashland Glycol Ethers 11.3 Chemcentral Glycol Ethers 11.4 DOWANOL Glycol Ethers and Acetates 11.5 Eastman Chemicals Glycol Ethers 11.6 Grant Chemical Glycol Diethers (GLYMES) 11.7 Occidental Ethylene Glycol Ethers and Glycol Ether Acetates 11.8 Olin Chemicals Poly-Sob Propylene Glycol Ethers ........................................ 11.9 Union Carbide Glycol Ethers Methylal 11.10 Physical Properties of Methylal ....................................................... EthyleneGlycols Ethylene Glycol Monomethyl Ether 11.11 11.12 Ethylene Glycol Monoethyl Ether ..................................................... 11 13 Ethylene Glycol Dimethyl Ether ....................................................... 11 I 4 Ethylene Glycol Diethyl Ether ........................................................ 11.15 Ethylene Glycol Monopropyl Ether .................................................... 11 16 Ethylene Glycol Monobutyl Ether 11.17 Water Solubiliy of Ethylene Glycol n-Butyl Ether Ethylene Glycol Monoisobutyl Ether 11.18 11.19 Ethylene Glycol Dibutyl Ether 11.20 Ethylene Glycol Monophenyl Ether .................................................... 11.21 Ethylene Glycol Monobenql Ether 11.22 Terpinyl Ethylene Glycol Ether 11.23 Ethylene Glycol Butylphenyl Ethers .................................................... 11.24 Ethylene Glycol Monohexyl Ether 11.25 Ethylene Glycol Ethyl Hexyl Ether 11.26 Diethylene Glycol 11.27 Diethylene Glycol Monomethyl Ether 11.28 Diethylene Glycol Monoethyl Ether .................................................... 11.29 Diethylene Glycol Monoethyl EthedEthylene Glycol ........................................ 11-30 Diethylene Glycol Monobutyl Ether .................................................... 11.31 Diethylene Glycol Monopropyl Ether ................................................... 11.32 Diethylene Glycol Dimethyl Ether 11.33 Diethylene Glycol Monoethyl Ether (Special Grade) 11.34 Diethylene Glycol Monohexyl Ether 113 5 Diethylene Glycol Divinyl Ether 11.36 Diethylene Glycol Monoisobutyl Ether 11.37 Triethylene Glycol ................................................................
.
. . .
............................................................. .......................................................... ................................................ .................................................... .............................................. ................................ ......................................................... ................................................................................... ............................................................................ .....................................................
..................................................... ......................................... ................................................... ........................................................ .................................................... ....................................................... ..................................................... ..................................................... ................................................................. ...................................................
..................................................... ........................................ .................................................... ........................................................ ..................................................
479 479 480 480 481 481 482 482 482 482
483 483
483 484 485 485 486 486 486 487 493 493 494 494 496 496 498 499 500 503 504 506 512 513 514 514 514 514 515 515 516 516 516 517 517 518 519 520 520 521 521 521 522 523 523 523 524 524 524 525 525 525 526 526
Contents and Subject Index 11.38 Triethylene Glycol Monomethyl Ether . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.39 Triethylene Glycol Monoethyl Ether . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.40 Triethylene Glycol Dimethyl Ether . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.41 Triethylene Glycol Monomethyl Ether/Highers . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.42 Triethylene Glycol Monobutyl Ether/Highers . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.43 Tetraethylene Glycol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.44 Triethylene Glycol Dimethyl Ether . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . PropyleneGlycols . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.45 Propylene Glycol Monomethyl Ether . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . Propylene Glycol Monophenyl Ether . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.46 11.47 Propylene Glycol Monopropyl Ether . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.48 Propylene Glycol Monobutyl Ether . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.49 Propylene Glycol tert-Butyl Ether . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.50 Propylene Glycol Monobutoxyethyl Ether . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.51 Propylene Glycol Isobutyl Ether and Higher Homologs . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.52 Propylene Based Glycol Ether Blends . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.53 Propylene Based Glycol Ether Blend . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.54 Dipropylene Glycol Monomethyl Ether . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.55 Dipropylene Glycol Monopropyl Ether . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.56 Dipropylene Glycol Monobutyl Ether . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.57 Dipropylene Glycol Tertiary Butyl Ether . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.58 Tripropylene Glycol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.59 Tripropylene Glycol Monomethyl Ether . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.60 Aromatic Based Glycol Ether . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . Triglycols . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.61 Methoxytriglycol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.62 Ethoxytriglycol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.63 Butoxytriglycol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . MiscellaneousGlycolData . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.64 ARCOSOLV Evaporation Characteristics. Resin Compatibility and Other Data .................... 11.65 DOWANOL Miscibility. Solubility. Evaporation Rates. Vapor Pressure. Density. Surface Tension and Other Data . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.66 GLYME Azeotropic Vapor Pressure and Solubility Data ..................................... 11.67 Union Carbide Glycol Ethers . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . PolyethyleneGlycols. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.68 Ashland Polyethylene Glycols . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.69 BASF Pluracol E Polyethylene Glycols . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.70 CARBOWAX Polyethylene Glycols . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.71 Dow Polyglycols . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . PolypropyleneGlycols . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.72 Ashland Polypropylene Glycols . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11-73 Dow Polypropylene Glycols and Polyglycol Copolymers ..................................... Polyols . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.74 Properties of PLURONIC and TETRONIC Block Copolymer Surfactants ........................ GlycerineEthers . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.75 Glyceryl a-Monomethyl Ether . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.76 Glyceryl a.y-Dimethyl Ether . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.77 Glyceryl a-Mono-n-Butyl Ether . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.78 Glyceryl a-Monoisoamyl Ether . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.79 Glyceryl a.y-Diisoamyl Ether . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.80 Miscellaneous Glycerine Ethers . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
miii 527 527 528 528 528 529 529 530 530 530 531 531 532 532 532 533 533 533 534 534 534
535 536 536 536 536 537 537 537 537
548 574 576 581 581 581 582 599 611 611 612 622 622 623 623 623 623 623 624 624
KETONES . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 625 Acetone . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 625 625 12.1 Physical Properties of Acetone . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 12.2 625 Low Temperature Characteristics of Aqueous Solutions of Acetone ............................ 626 12.3 Solubility of Various Materials in Acetone . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 626 12.4 Specific Gravity of Aqueous Solutions of Acetone at Different Temperatures . . . . . . . . . . . . . . . . . . . . . 12.5 Surface Tension of Aqueous Solutions of Acetone at 25°C .................................. 627 627 12.6 Viscosity of Aqueous Acetone Solutions at 25% . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 628 12.7 Refractive Index of Aqueous Solutions of Acetone at 25°C . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 12.8 Liquid-Vapor Equilibria for Aqueous Solutions of Acetone at Different Pressures . . . . . . . . . . . . . . . . . . 628 629 12.9 Freezing Point of Aqueous Solutions of Acetone . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . MethylEthylKetone . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 629
xxiv
Contents and Subject Index 12.10 Physical Properties of Methyl Ethyl Ketone .............................................. 629 630 12.1 1 Methyl Ethyl Ketone and Water ...................................................... Methyln-propylKetone 630 Properties of Methyl n-Propyl Ketone .................................................. 630 12.12 Methyln-ButylKetone ....................................................................... 631 631 12.13 properties of Methyl n-Butyl Ketone ................................................... Solubility of Dry Half-Second R.S. Nitrocellulose in a System of Methyl Butyl Ketone-sec12.14 Butanol-Toluene ................................................................ 632 MethyllsobutylKetone ....................................................................... 632 632 12.15 Properties of Methyl Isobutyl Ketone ................................................... 633 Solubility of Miscellaneous Materials in Methyl Isobutyl Ketone at 20" to 25°C .................... 12.16 Methyln-AmylKetone 634 12.17 Properties of Methyl n-Amyl Ketone ................................................... 634 MethylIsoamylKetone 634 12.18 Properties of Methyl Isoamyl Ketone ................................................... 634 635 Properties of Methyl Isoamyl Ketone vs Other Solvents ..................................... 12.19 12.20 Butyrate-Acrylic Wood Lacquer-ubstituting Isoamyl Ketone for 2-Ethoxyethyl Acetate . . . . . . . . . . . 635 Methyl HexylKetone 636 12.21 Properties of Methyl Hexyl Ketone 636 MethylHeptyl Ketone ........................................................................ 636 636 12.22 Properties of Methyl Heptyl Ketone .................................................... EthylbutylKetone ........................................................................... 637 637 12.23 Properties of Ethylbutyl Ketone ....................................................... Ethyl Amyl Ketone ........................................................................... 637 637 12.24 Properties of Ethyl Amyl Ketone ...................................................... Dl-n-PropylKetone ......................................................................... 638 638 12.25 Properties of Di-n-Propyl Ketone DllsobutylKetone ........................................................................... 638 638 12.26 Properties of Diisobutyl Ketone Cyclohexanone 639 639 12.27 Properties of Cyclohexanone ........................................................ 640 12.28 Resin Solubility in Cyclohexanone MethylCyclohexanone ....................................................................... 641 641 12.29 Properties of Methyl Cyclohexanone ................................................... MethylAcetone ............................................................................. 641 DlacetoneAlcohol ........................................................................... 642 642 12.30 Physical Properties of Acetone-Free Diacetone Alcohol .................................... AcetonylAcetone ........................................................................... 642 643 12.31 Properties of Acetonyl Acetone MesltylOxlde ............................................................................... 643 12.32 Properties of Mesityl Oxide .......................................................... 643 lsophorone ................................................................................ 644 12.33 Properties oflsophorone ........................................................... 644 Fenchone .................................................................................. 644 12.34 Properties of Fenchone ............................................................ 644 Beta-Proplolactone 645 645 12.35 Physical Properties of Beta-Propiolactone Gamma-Butyrolactone ....................................................................... 645 645 12.36 Properties of Gamma-Butyrolactone ................................................... ComparatlveData 648 12.37 Ashland Ketones 648 12.38 Chemcentral Ketones and Miscellaneous Active Solvents ................................... 649 650 12.39 Eastman Chemical Ketones 650 12.40 Exxon Ketones . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 651 12.41 Hoechst-Celanese Ketones 651 12.42 Shell Chemical Ketones 652 12.43 Union Carbide Ketones ............................................................ 657 12.44 Vapor Pressure of Various Ketones at Different Temperatures ............................... 658 12.45 Specific Gravities of etones ......................................................... 659 12.46 Solubility of Ketones in Water 659 12.47 Solubility of Water in Ketones ........................................................ 660 12.48 Relative Evaporation of Ketones-Fast to Intermediate Evaporating Liquids 660 12.49 Relative Evaporation of Ketones-lntermediate to Slow Evaporating Liquids ..................... 12.50 Viscosity vs Concentration of Chlorinated Rubber (Hercules PARLON S-20) in MEK . . . . . . . . . . . . . . . 661
......................................................................
....................................................................... .......................................................................
......................................................................... ....................................................
..................................................... ....................................................... ............................................................................. ....................................................
.......................................................
.......................................................................... ..............................................
........................................................................... ................................................................. ......................................................... ......................................................... ............................................................
........................................................ .....................
ACIDS
Contents and Subject Index
m
. . . . . . . . ................................................................................ 13.1 Acetic Acid ...................................................................... Viscosity of Acetic Acid and Acetic Anhydride Mixtures at 15' and 76.5"C ....................... 13.2 Butyric Acid ..................................................................... 13.3 Viscosity of Aqueous Butyric Acid Solution at 25'C ........................................ 13.4 ButyricAnhydride . . . . . . . . . . . . . . . . . ............................................... 13.5
662 662 662 663 663
i
13.6 13.7 13.8 13.9 13.10 13.1 1 13.12 13.13 13.14 13.15 13.16 13.17 13.18 13.19 13.20 13.21
................................. ................................................................. ................................................................ ...................................................................... ................................................................ .......................................... .......................................... ..............................................
Solubility of Water in Caproic Acid at Various Temperatures 2-Ethylbutyric Acid 2-Ethylhexoic Acid Solubility of Water in Ethylhexoic Acid. Ethylbutyraldehyde and Ethylpropylacrolein . . . . . . . . . . . . . . . . Lactic Acid Triftuoroacetic Acid Vapor Pressure of Organic Acids and Anhydrides at Various Temperatures ..................... Fatty Acid Composition of Various Fats and Oils Arizona Chemical ACTINOL Tall Oil Fatty Acids Eastman Chemicals Acids and Anhydrides Halocarbon Products BIOGRADE Triiuoroacetic Acid ...................................... EMERY Fatty and Dibasic Acids ...................................................... INDUSTRENE and HYSTRENE Fatty and Dibasic Acids .................................... NEO-FATFattyAcids ............................................................. Procter 81Gamble Fatty Acids ........................................................ Union Carbide Acids
.............................................................. AMINES ....................................................................................... AlkylAmines ............................................................................... 14.1 Monomethylamine ................................................................ 14.2 Dimethylamine ................................................................... 14.3 Trimethylamine ................................................................... 14.4 Freezing Points of Aqueous Methylamine Solutions ....................................... 14.5 Binary Azeotropes of Methylamines ................................................... 14.6 Solubility Data for Methylamines ...................................................... 14.7 Monoethylamine .................................................................. 14.8 Diethylamine .................................................................... 14.9 Triethylamine .................................................................... 14.10 n-Propylamine ................................................................... 14.11 Di-n-Propylamine ................................................................ Mutual Solubility of Di-n-Propylamine and Water at Various Temperatures ...................... 14.12 ....................... 14.13 Solubility Curve at 25" for the System Di-n-Propylamine-Water-Ethanol 14.14 Isopropylamine ................................................................... 14.15 Di-lsopropylamine ................................................................ 14.16 14.17 14.18 14.19 14.20 14.21 14.22 14.23 14.24 14.25 14.26 14.27 14.28 14.29 14.30 14.31 14.32 14.33 14.34 14.35 14.36 14.37 14.38 14.39
n-Butylamine .................................................................... n-Dibutylamine .................................................................. n-Tributylamine .................................................................. lsobutylamine .................................................................... Diisobutylamine .................................................................. sec-Butylamine Mono-n-Butyl Diamylamine ......................................................... n-Amylamine .................................................................... sec-Amylamine Diamylamine (Mixed Isomers) Triamylamine (Mixed Isomers) ....................................................... sec-Hexylamine 2-Ethylbutylamine n-Heptylarnine ................................................................... 2-Ethylhexylamine Di-2-Ethylhexylamine Cyclohexylamine ................................................................. Dicyclohexylamine AUQUAT Fatty Quaternary Ammonium Chloride .......................................... KEMAMINE Fatty Quaternary Ammonium Chlorides ....................................... High Molecular Weight Aliphatic Amines Solubilities of Pure Dodecyl- and Octadecyl-Trimethylammonium Chlorides in Grams per 100 grams ofsolvent ..................................................................... Solubilities of Organic Compounds in Aliphatic Amines at 25' f 5'C Vapor Pressure of Various Amines
..................................................................
.................................................................. ........................................................ .................................................................. ................................................................ ................................................................ ............................................................. ................................................................
................................................
........................... ....................................................
663 664 664 664
664 665 666
668 669 670 671 671 672 676 681
683 684 686 686 686
686 687 688
688 689 690 690 691 691 691 692 692 692 693 693 693 694 694
694 695 695
695 696 696 696 697 697 697 697 697 698 698
699 699 700 700 701 705
m i
Contents and Subject Index
14.40 Vapor Pressure of Sharples Amines . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . AlkyleneDlamlnes . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.41 Ethylene Diamine . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . Boiling Point Composition Curves for Aqueous Ethylenediamine Solutions . . . . . . . . . . . . . . . . . . . . . . . 14.42 14.43 Diethylenetriamine . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.44 Boiling Point Composition Curves for Aqueous Diethylenetriarnine Solutions ..................... 14.45 Tetraethylenepentamine . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.46 Propylenediamine . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.47 Solvent Properties of Alkylene Diamines . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.48 Vapor Pressures of Alkylene Diamines and Other Amines . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.49 Density of Ethylenediamine Solutions . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.50 Density of Higher Ethylene Amines . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.51 Viscosity of Ethylenediamine Solutions . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.52 Viscosity of Higher Ethylene Amines ................................................... ComparativeData . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . Akzo ARMEEN, DUOMEEN, TRIAMEEN, ETHOMEEN, Ethoxylated Diamines, Propoxylated Amines . . . 14.53 14.54 ANGUSAmines . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.55 Ashland Amines . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.56 Chemcentral Amines . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.57 Dow Commercial Alkanolamines . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.58 Humko Amines . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.59 Procter & Gamble Tertiary Amines . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.60 Occidental Ethanolamines . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.61 Union Carbide Ethyleneamines . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.62 Union Carbide Ethanolamines ....................................................... AlkanolAmines . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.63 Monoethanolamine . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.64 Boiling Point Composition Curves for Aqueous Monoethanolamine Solutions ..................... 14.65 Viscosity of Monoethanolamine at Various Temperatures ................................... 14.66 Diethanolamine . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.67 Viscosity of Diethanolamine at Various Temperatures . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.68 Triethanolamine . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.69 Viscosity of Triethanolamine at Various Temperatures . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.70 Specific Heats of Aqueous Triethanolamine Solutions at 21% ................................ 14.71 Surface Tension of Aqueous Ethanolamine Solutions at 20°C ................................ 14.72 Viscosity of Aqueous Ethanolamine Solutions at 20°C . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.73 lsopropanolamines Mixed ........................................................... 14.74 Triisopropanolamine . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.75 2-Amino-2-Methyl-1 -Propanol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2-Amino-2-Methyl-l ,2-Propanediol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.76 14.77 2-Amino-2-Ethyl-1, 3-Propanediol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.78 2-Amino-1-Butanol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . Tris(Hydroxymethyl)Aminomethane . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.79 2-Aminoethylethanolamine . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.80 14.81 1-Diethylamino-2, 3-Propanediol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.82 Aminohydroxy Compounds . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.83 2-Diethylamino-2-Methyl-1 -Propanol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . AikylalkanolAmines . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.84 Properties of Various Alkylalkanol Amines . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . Glycol EtherAmlnes . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.85 Properties of Various Glycol Ether Amines . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . ~IAmines ................................................................................ 14.86 Aniline . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.87 Dimethylaniline . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.88 Diethylaniline . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.89 N-Mono-n-Butyl Aniline . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.90 N,N-Di- n-Butyl Aniline . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.91 n-Monoamyl Aniline (Mixed Isomers) . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.92 p-tert-Amyl Aniline . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.93 Di-tert-Amyl Aniline . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.94 N,N-Diamyl Aniline (Mixed Isomers) . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.95 Diethylbenzylamine . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.96 N-(n-Butyl)-+Naphthylamine ....................................................... imines . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
705 706 706 706 706 707 707 707 708 708 709 709 710 710 711 711 718 718 719 719 735 736 737 747 753 760 760 760 760 761 761 761 762 762 762 762 763 763 763 764 764 764 764 764 764 765 765 766 766 768 768 769 769 769 769 770 770 770 770 771 771 771 771 772
Contents and Subject Index
mii
772 Ethylene Imine . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.97 772 Propylene Imine . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.98 773 Amides . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 773 Formamide ..................................................................... 14.99 14.100 Dimethylformamide ................................................................ 773 774 14.101 Surface Tension and Density of DMF-Water Mixtures ...................................... 775 14.102 Semi-Quantitative Solubilities of Inorganic Materials in DMF at 25% . . . . . . . . . . . . . . . . . . . . . . . . . . . 776 14.103 Dimethylacetamide . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 777 14.104 Viscosities of Resins in DMAC . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 778 14.105 I-Formylpiperdine ................................................................ Nitriles., . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 780 780 14.106 n-Butyronitrile ................................................................... Heterocyclic Compounds . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 780 780 14.107 Pyrrole . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 781 14.108 2-Pyrrolidone . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 781 14.109 Phase Diagram for 2-Pyrrolidone-Water . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . ........................................................... 782 14.110 N-Methyl-2-Pyrrolidone 783 14.1 11 AcuteOralToxicity . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 783 14.1 12 Acute Dermal Toxicity . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 783 14.1 I 3 Injection Toxicity . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 783 14.1 14 Toxicity to Aqueous Organisms . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 784 14.1I 5 Infrared Absorption Spectrum . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 784 14.1I 6 Specific Heat . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 784 14.1I 7 Thermal Conductivity . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 785 14.1 I 8 Vapor Pressure . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 785 14.1 19 Comparison of Vapor Pressures of M-Pyrol and Other Aprotic Solvents . . . . . . . . . . . . . . . . . . . . . . . . 785 14.120 SurfaceTension . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 786 14.121 Freezing Point Curve . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 786 14.122 Viscosity of Anhydrous M-Pyrol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 787 14.123 Viscosity of Aqueous M-Pyrol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.124 Vapor/Liquid Equilibrium Data for M-Pyrol-Water System at Atmospheric and 400 mg Pressures . . . . . 787 787 14.125 Vapor/Liquid Equilibrium of M-Pyrol-Water Systems ....................................... 788 14.126 Hydrolytic Stability of M-Pyrol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 789 14.127 Comparison of Hydrolysis of M-Pyrol and DMF . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 789 14.128 Hydrolysis of M-Pyrol in Alkaline Salt Solutions .......................................... 789 14.129 Hygroscopicity Data . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 789 14.130 Hygroscopicity Data . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 790 14.131 Hygroscopicity Data . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 790 14.132 Effect of Temperature on Hygroscopicity . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 790 14.133 Correlation of M-Pyrol and Water Vapor Data . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 791 14.134 Vapodtiquid Equilibrium of M-Pyrol Containing 1% Water .................................. 791 14.135 Solubility of Acetylene in Various Solvents . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 792 14.136 Solubility of Sulfur Compounds and Carbon Dioxide in M-Pyrol Solvent ........................ 792 14.137 Solubility of Paraffin Hydrocarbons in M-Pyrol Solvent ..................................... 14.138 Vapor-Liquid Equilibrium Distribution Coefficients for Sulfur Compounds and Carbon Dioxide in 793 M-Pyrol Solvent 14.139 Vapor-Liquid Equilibrium Distribution Coefficients for Paraffin Hydrocarbons in M-Pyrol Solvent . . . . . . 793 14.140 Correlation of Equilibrium Distribution Coefficients for Ethane and Heavier Paraffin Hydrocarbons 794 in M-Pyrol Solvent . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.141 Classification of Equilibria in M-Pyrol Showing Relationship Between Equilibrium Distribution 794 Coefficients (K)and Solute Vapor Pressures ........................................... 795 14.142 Solubilities of Carbon Monoxide and Olefins in Anhydrous M-Pyrol Solvent ...................... 795 14.143 Solubilities of Diolefins in Anhydrous M-Pyrol Solvent ...................................... 796 14.144 Solubilities of Acetylenes in Anhydrous M-Pyrol Solvent . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.145 Vapor-tiquid Equilibrium Distribution Coefficients for Olefins and Carbon Monoxide in M-Pyrol 796 Solvent . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.146 Vapor-Liquid Equilibrium Distribution Coefficients for Diolefins in Anhydrous M-Pyrol Solvent . . . . . . . . 797 14.147 Vapor-Liquid Equilibrium Distribution Coefficients for Acetylenes in Anhydrous M-Pyrol Solvent . . . . . . 797 14.148 Effect of Water (5 wt %) in M-Pyrol Solvent on Equilibrium Distribution Coefficients for Olefins . . . . . . . 798 14.149 Effect of Water (5 wt %) in M-Pyrol Solvent on Equilibrium Distribution Coefficients for Olefins . . . . . . . 798 799 14.150 Effect of Water (5 wt %) in M-Pyrol Solvent on Equilibrium Distribution Coefficient for Methylacetylene 14.151 Effect of Water (5 wt %) in M-Pyrol Solvent on Equilibrium Distribution Coefficient for Acetylene . . . . . . 799 14.152 Classification and Correlation of Equilibria of Unsaturated Hydrocarbons in Anhydrous M-Pyrol 800 Solvent 92-10 atm. 25'-150"C range) ............................................... 14.153 Effect of Water and Elevated Pressure on Solubility of Hydrogen Sulfide in M-Pyrol Solvent . . . . . . . . . 800
.
................................................................
.
xviii
Contents and Subject Index
..... ..................... ..........................
Effect of meso.2. 3.Butanediol on the Freezing Point of Aqueous levo-2. 3.Butanediol Solutions 382 Freezing Points of Aqueous levo-2.3.Butanedio l.Ethanol Solutions ........................... 383 Freezing Points of Aqueous levo-2.3.Butanedio LEthylene Glycol Solutions 383 Freezing Points of Aqueous levo-2.3.Butanedio l.Methano1 Solutions 383 Freezing Points of Aqueous levo-2.3.Butanedio l.Tetrahydrofurfuryl Alcohol Solutions . . . . . . . . . . . . . 383 Kinematic Viscosity of Aqueous levo-2. 3.Butanediol Solutions. Expressed Logarithmically. as a Function of Concentration and Temperature ........................................... 384 Solutions in Relation to Concentration Kinematic Viscosity of Aqueous levo.2. 3.Butanediol 7.63 and Temperature ............................................................... 384 Kinematic Viscosity of 60% levo-2.3.Butanediol. Glycerol and Ethylene Glycol Solutions at Low 7.64 Temperatures 384 Solutions at 20°C. Expressed in Kinematic Viscosity of Aqueous levo-2.3.Butanedio l.Ethanol 7.65 Centistokes .................................................................... 384 Kinematic Viscosity of Aqueous levo-2.3.Butanedio l.Methanol Solutions at 20°C. Expressed in 7.66 Centistokes 385 l.Ethylene Glycol Solutions in 20'C Kinematic Viscosity of Aqueous levo.2.3.Butanedio 7.67 385 Expressed incentistokes ......................................................... 7.68 Kinematic Viscosity of Aqueous levo-2.3.Butanedio l.Tetrahydrofurfuryl Alcohol Solutions at 20'C. Expressed in Centistokes 385 Absolute Viscosity of Aqueous Solutions of Ethylene Glycol. levo.2.3.Butanediol. meso-dextro7.69 2.3.Butanediol and Glycerol at 20°C ................................................. 385 Optical Rotatory Power of Aqueous levo.2. 3.Butanediol Solutions at 20°C ...................... 386 7.70 Effects of Concentration and Temperature on the Specific Rotatory Power of Aqueous levo-237.71 Butanediol Solutions 386 386 7.72 Refractive Indices of Aqueous levo.2. 3.Butanediol Solutions at Different Temperatures 386 7.73 Refractive Indices of Aqueous Solutions of meso- and levo.2. 3.Butanediol at 25'C Specific Gravity of Aqueous levo-2. 3.Butanediol Solutions at 20'. 30'. and 40% . . . . . . . . . . . . . . . . . 387 7.74 387 7.75 Specific Gravity of Aqueous meso.2. 3.Butanedol Solutions at 20'. 30'. and 4O'C 7.76 Surface Tension of Aqueous Solutions of levo-2. 3.Butanediol and Ethylene Glycol . . . . . . . . . . . . . . . 387 Butanediois . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 388 388 Refractive Indices of Aqueous Butanediol Solutions at 20". 30'. and 40°C ....................... 7.77 388 Kinematic Viscosity of Aqueous Butanediol Solutions at 20" and 40°C. in Centistokes 7.78 2.Butene.1, 4.dioi 388 ............................................... 388 7.79 Physical Properties of 2.Butene-1. 4.diol 2.Butyne.1, Cdioi ........................................................................... 389 389 7.80 Physical Properties of 2.Butyne.l. 4.diol IC-Pentanedlol 389 7.81 Physical Properties of 1.5.Pentanediol 389 390 7.82 Absolute Viscosity of Aqueous 1.5.Pentanediol Solutions at 20" and 40°C 390 7.83 Specific Gravity of Aqueous 1.5-Pentanediol Solutions at 20" and 40°C 2,CPen.nediol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 390 ................................................. 390 7.84 Physical Properties of 2.4.Pentanediol NeopentylGlycol ............................................................................ 390 7.85 Physical Properties of Neopentyl Glycol 390 Pentanediols 391 7.86 Kinematic Viscostly of Aqueous Pentanediol Solutions at 20" and 40%. in Centistokes 391 7.87 Refractive Indices of Aqueous Pentanediol Solutions at 20' and 4Q°C .......................... 391 IS-Hexanediol 392 392 7.88 Physical Properties of 1.6.Hexanediol 2,5.Hexanediol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 392 7.89 Physical Properties of 1.5.Hexanediol ................................................. 392 HexyleneGiycol ............................................................................. 392 7.90 Physical Properties and Specifications of Hexylene Glycol 392 393 7.91 Freezing Points of Hexylene Glycol-Water Mixtures 393 7.92 Specific Gravity and Freezing Point of Hexylene Glycol-Water Mixtures Pinacol 394 394 7.93 Physical Properties of Pinacol 22-Diethyl-I f-Propanedloi 394 7.94 Physical Properties of 2.2.Diethyl.l. 3.Propanediol 394 2.Ethyl.1, 3.Hexanedlol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 394 7.95 Physical Properties of 2.Ethyl.l. 3.Hexanediol 394 2,5.Dimethyl.3.Hexyne.2,5 .diol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 395 5.diol .................................... 395 7.96 Physical Properties of 2.5.Dimethyl.3.Hexyne-2. 1,4.Cyclohexanedimethanol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 395 7.57 7.58 7.59 7.60 7.61 7.62
..................................................................
....................................................................
....................................................
............................................................. ............ ............... ................
.............. ...........................................................................
............................................... ............................................................................. ................................................. ...................... ........................
................................................ ............................................................................... ............. ............................................................................. .................................................
.................................. ....................................... ........................ ................................................................................... ........................................................ ................................................................... ....................................... ...........................................
Contents and Subject Index Ethylene Glycol Monoacetate ........................................................ 15.20 15.21 Ethylene Glycol Diacetate Ethylene Glycol Monomethyl Ether Acetate .............................................. 15.22 Ethylene Glycol Monoethyl Ether Acetate ............................................... 15.23 15.24 Ethylene Glycol Monobutyl Ether Acetate ............................................... Diethylene Glycol Monoethyl Ether Acetate . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 15.25 15.26 Diethylene Glycol Monobutyl Ether Acetate .............................................. 15.27 Propylene Glycol Monomethyl Ether Acetate ............................................. 15.28 Propylene Glycol Monoethyl Ether Acetate .............................................. 15.29 Dipropylene Glycol Monomethyl Ether Acetate (DPMA) ..................................... 15.30 Propylene-Based Glycol Ether Acetate ................................................. Propionates ................................................................................ 15.31 Methyl Propionate . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 15.32 Ethyl Propionate 15.33 N-Butyl Propionate ............................................................... Amyl Propionate 15.34 15.35 Ethyl 3-Ethoxypropionate Butyrater 15.36 Methyl Butyrate .................................................................. 15.37 Ethyl Butyrate . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 15.38 n-Butyl Butyrate 15.39 Ethyl Hydroxy-lsobutyrate .......................................................... 15.40 Isobutyl lsobutyrate ............................................................... 2.2.4-Trimethylpentanediol-l .3-Monoisobutyrate ......................................... 15.41 ComparativeData 15.42 ARCOSOLV PM Acetate and ARCOSOLV PE Acetate 15.43 Ashland Ester Solvents ............................................................ 15.44 Chemcentral Esters 15.45 CPSChemical Esters 15.46 Eastman Glycol Ether Esters 15.47 Hoechst Celanese Esters ........................................................... 15.48 Mobil OilEsters 15.49 Union Carbide Esaters ............................................................. HiOherFattyAcldEsters 15.50 Emery Methyl Esters 15.51 Procter & Gamble Methyl Esters ...................................................... 15.52 Stepan Esters Adipater 15.53 Mixture of Dimethyl Adipate and Dimethyl Glutarate Mixture of Dimethyl Adipate. Dimethyl Glutarate and Dimethyl Succinate 15.54 15.55 Dialkyl Adipate 15.56 Dioctyl Adipate ................................................................... Oxalates 15.57 DietylOxalate 15.58 Dibutyl Oxalate 15.59 Diamyl Oxalate Lactates 15.60 Methyl Lactate ................................................................... 15.61 Ethyl Lactate .................................................................... 15.62 Butyl Lactate 15.63 Amyl Lactate 15.64 Physical Properties of ctates Carbonates 15.65 Diethyl Carbonate 15.66 JEFFSOLCarbonates ............................................................. PMhalater Alkyl Benzyl Phthalates ............................................................ 15.67 15.68 Butyl Benzyl Phthalate . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 15.69 Dibutyl Phthalate . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 15.70 Di-2-Ethylhexyl Phthalate (Dioctyl Phthalate) ............................................ Phosphates 15.71 1-Butylphenyl Diphenyl Phosphate 15.72 2-Ethylhexyl Diphenyl Phosphate . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . lsodecyl Diphenyl Phosphate 15.73
...........................................................
.................................................................. .................................................................. ........................................................... ..................................................................................
..................................................................
........................................................................... ..................................... ............................................................... .............................................................. ........................................................ .................................................................. ...................................................................... .............................................................. ................................................................... .................................................................................. ....................................... ........................ ................................................................... .................................................................................. ................................................................... ................................................................... ................................................................... ...................................................................................
.................................................................... .................................................................... ......................................................... ................................................................................ ................................................................ .................................................................................
................................................................................
.................................................... ........................................................
mix 826 826 827 827 828 829 829 830 830 831 831 832 832 832 832
833 833 834 834 834 834 835 835 835 836 836 838 838 839 839 840 842
843 850 850 851 852 854 854 854 855 856 857 857 857 858 858 858 858 859 860 860 860 860 861 867 867 871 873 874 875 875 876 879
mx
Contents and Subject Index Emulsifiable Triaryl Phosphate ....................................................... 15.74 Proprietary Triaryl Phosphate Ester .................................................... 15.75 Tributoxyethyl Phosphate 15.76 Tributyl PHosphate 15.77 Triphenyl Phosphate .............................................................. 15.78 Phosphites . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . Dialkyl Hydrogen Phosphites 15.79 Trialkyl Phosphites . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 15.80 Tertiary Phosphites . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 15.81 Organophosphfies . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 15.82 Silicates ................................................................................ Ethyl Silicate .................................................................... 15.83 Plasticizers ................................................................................ Summary of Typical Properties of Plasticizers ............................................ 15.84
881 881 882 883 883 885 885 886 887 888 888 888 889 890
HPLCAND WDATA . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . GC-FiDChromatograms . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 16.1 Methylane Chloride . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . HPLC Gradient Chromatograms ................................................................ 16.2 Watervs Methanol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 16.3 Water vs Acetonitrile .............................................................. 16.4 Water vs 2-Propanol .............................................................. 16.5 Water vs Tetrahydrofuran . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 16.6 Water-01 % Trifluoroacetic Acid vs Acetonitrile-0.1 % Trifluoroacetic Acid ....................... 16.7 0.1 M Potassium Phosphate vs Acetonitrile .............................................. 16.8 0.1 M Potassium Phosphate vs Methanol ............................................... 0.05 M Potassium Phosphate vs Acetonitrile . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 16.9 0.05 M Potassium Phosphate vs Methanol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 16.10 16.11 0.01 M Potassium Phosphate vs 0.5 M Potassium Phosphate pH 6.8/6.4 ....................... 16.12 Hexane vsChloroform . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 16.13 Hexanevs Chloroform . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 16.14 Hexane vs Ethyl Acetate ........................................................... 16.15 Hexane vs2-Propanol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 16.16 HexanevsEther (Anhydrous) . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 16.17 2.2. 4-Trimethylpentane vs Chloroform ................................................. 16.18 2.2. 4-Trimethylpentane vs Methylene Chloride ........................................... 16.19 2.2. 4-Trimethylpentane vs Ethyl Acetate ............................................... 16.20 2.2. 4-Trimethylpentane vs 2-Propanol ................................................. 16.21 Methylene Chloride vs Methanol ...................................................... 16.22 Methylene Chloride vs 2-Propanol .................................................... 16.23 Methylene Chloride vs Ethyl Acetate . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 16.24 Methylene Chloride vs Ether (Anhydrous) ............................................... UitravioletSpectra . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 16.25 Acetic Acid. Glacial., . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 16.26 Acetone . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 16.27 Acetonitrile . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 16.28 Benzene . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 16.29 2-Butanol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 16.30 n-Butyl Acetate . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 16.31 n-Butyl Alcohol . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 16.32 n-Butyl Chloride . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 16.33 tert-Butyl Methyl Ether . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 16.34 Carbon Tetrachloride . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 16.35 Chlorobenzene . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 16.36 Chloroform . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 16.37 Cyclohexane .................................................................... 16.38 Cyclopentane . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 16.39 Decahydronaphthalene (Decalin) . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 16.40 o-Dichlorobenzene . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 16.41 Diethyl Carbonate ................................................................ 16.42 Dimethyl Acetamide ............................................................... 16.43 Dimethyl Formamide .............................................................. 16.44 Dimethyl Sulfoxide . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 16.45 1.4-Dioxane ....................................................................
891 891 891 892 892 893 894 894 895 896 897 897 898 899 900 900 901 901
........................................................... ................................................................ ........................................................
...
902 903
903 904 904 905 905 906 906 907 907 907 908 909 910 910 910 911 911 911 912 912 914 914 915 915 916 916 916 917 917
Contents and Subject Index 16.46 16.47 16.48 16.49 16.50 16.51 16.52 16.53 16.54 16.55 16.56 16.57 16.58 16.59 16.60 16.61 16.62 16.63 16.64 16.65 16.66 16.67 16.68 16.69 16.70 16.71 16.72 16.73 16.74 16.75 16.76 16.77 16.78 16.79 16.80 16.81 16.82 16.83 16.84
................................................................. ................................................................. .................................................................... ......................................................................
Ether. Anhydrous 2-Ethoxyethanol EthylAcetate Ethylene Dichloride ............................................................... Ethyl Ether GLYME ........................................................................ n-Heptane ...................................................................... Hexadecane .................................................................... Hexane Isobutyl Alcohol iso-Octane (2.2.4-Trimethylpentane) .................................................. Isopropyl Alcohol Isopropyl Myristate Methanol 2-Methoxyethanol 2-Methoxyethyl Acetate Methylt-Butyl Ether Methylene Chloride ............................................................... Methyl EthylKetone ............................................................... Methyl Isoamyl Ketone Methyl Isobutyl Ketone Methyl n-Propyl Ketone N-Methylpyrrolidone Pentane ........................................................................ Petroleum Ether .................................................................. beta-Phenethylamine .............................................................. 2-Propanol ..................................................................... n-Propyl Alcohol Propylene Carbonate Pyridine Tetrahydrofuran Toluene ........................................................................ 1.2. 4-Trichlorobenzene Trichloroethylene 1.1. 2-Trichlorotrifluoroethane ........................................................ Triiuoroacetic Acid ................................................................ Trimethylpentane Water ......................................................................... ortho-Xylene
........................................................................ .................................................................. ................................................................. ................................................................ ....................................................................... ................................................................ ............................................................ ............................................................... ............................................................. ............................................................. ............................................................ ..............................................................
................................................................. .............................................................. ........................................................................ .................................................................. ............................................................ .................................................................
................................................................. ....................................................................
mi 917 918 918 919 919 920 920 921 921 923 924 924 925 925 926 926 926 927 927 928 928 929 929 929 930 930 931 931 931 932 932 933 934 935 935 936 936 937 937
............................................
938
.................................................................................. TRADENAMEINDEX ............................................................................
960
APPENDM-COMPARATNE DATA FOR VARIOUS SOLVENTS REFERENCES
962
Introduction
A solution may be defined as a mixture of two or more substances which has uniform chemical and physical properties throughout. It may also be defined as a system whose component parts are two or more molecular species, there being no boundary surfaces between these parts larger than molecules. There are two components to every solutionthe solvent and the solute. As a matter of convenience, the part of a solution which i s in excess is designated as the solvent; the solute is the component which is in smaller proportion. Solvents, once used, may be recycled, reused, or discarded in an environmentally safe manner. The purpose of solvents i s to convert substances into a form suitable for a particular use. The importance of the role of solvents is brought out most clearly by the fact that many substances exhibit their greatest usefulness when in solution. Lacquer solvents, for example, are selected to produce homogeneous combinations and so selected as to impart the most desirable mechanical properties. The physical properties of a fabricated solution can be regulated a t will by the proper choice of solvents, thus adapting them to the most varied uses and methods of applications. Some of the more important uses for solvents are in the adhesives, coatings, electronics, ink, pesticide, pharmaceutical, photographic reproduction, and textile industries. Large quantities of solvents are also involved in dry cleaning, metal degreasing, oil refining and recovery, and as fuel additives. Solvents vary in their dissolving power, so that the line of demarcation between solvents, latent solvents and nonsolvents is difficult to define. Some of the factors which influence solvency are atmospheric conditions, purity and molecular association. Molecular aggregation is the explanation for increased, attenuated, or decreased solvent power or, more concisely, eccentric solvency. Any substance that will dissolve another i s called a solvent. Thus, we have a gaseous solution when a liquid or a solid is dissolved in a gas; a liquid solution when any one of these is dissolved in a liquid, and a solid solution when any one of them is dissolved in a solid. Mixing of solvents, diluents and thinners often results in change of solvent properties. Some chlorinated compounds become good solvents for cellulose esters when mixed with an alcohol. On the other hand, some active solvents for esters of cellulose lose some of their solvent power when mixed with hydrocarbons. Alcohols are added to lacquers to improve flow and to prevent blushing, although they vary considerably in these respects. Alcohols are not true or active solvents for nitrocellulose as are the active dissolvents like ethyl lactate or n-butyl acetate. The alcohol group, however, cannot be classed as nonsolvents like toluene or naphtha. When an alcohol is added to a true solvent, the solvent power of the latter is not reduced but, on the contrary, this active solvent activates the alcohol to such an extent that it too becomes a solvent. Therefore, alcohols are referred to as latent solvents, whose hidden solvent qualities are brought out by the addition of an active solvent. The presence of a latent solvent increases the tolerance of an active solvent for a nonsolvent. This group of latent solvents is also called extenders, because they increase the volume of a mixture without decreasing the solvent power. In general, simple esters and ketones activate alcohols so that they too become solvents and are capable of tolerating various proportions of diluents. This is due to the molecular aggregates formed. Two-type solvents containing both an alcohol and an active solvent group, such as an ester, ether or ketone, activate alcohol to a lesser degree. Unit volumes of a solvent will activate only a limited amount of alcohol, indicating that definite molecular aggregates are formed. A mixture of 50% n-butyl acetate and 50% n-butyl alcohol will not lose i t s solvent power until 85 to 95% of the volume is evaporated, contributing further evidence of the validity of the theory of molecular aggregates. Plasticizers, which are the high-boiling solvents, also activate alcohols. Liquids vary in their rate of evaporation. Naturally, in a mixture of liquids, some evaporate more rapidly than others. For example, if the solvent constituent of a lacquer evaporates more rapidly than the diluent, the limit of tolerance of the residual mixture is exceeded and gelling or precipitation occurs. As evaporation goes on, gigantic molecular reactions take place. Vast numbers of molecules change places as the new aggregates are formed. Some are 1
2
Industrial Solvents Handbook
replaced and some are repelled, causing immiscibility, precipitation, blushing, or one or more of the many lacquer faults. It follows that dilution ratios do not indicate tolerance during the change of solvent-nonsolvent balance which occurs during drying. In the theory of molecular aggregation, higher concentrations of cellulose derivatives contain fewer secondaryvalence bonds. Consequently, smaller amounts of diluent can be tolerated. This condition occurs during film drying. Hydroxyl-containing solvents show greater tolerance for toluene than do the simpler esters. In the case of naphtha the condition is reversed. There are, however, exceptions to this statement, among which are butyl lactate and Butyl CELLOSOLVE, which have very high naphtha tolerance. Simple esters will tolerate 50 to 100% more naphtha than will such materials as ethyl lactate, ethyl ether, ethylene glycol, diacetone alcohol, and so forth. Ethers of glycols generally have higher dilution ratios than do the butyl esters with respect to benzene, toluene, and xylene. Solutions of nitrocellulose tolerate larger quantities of nonsolvents than solutions of cellulose acetate. The "solventpower number'' i s influenced by both the nature of the diluent and the mixing of two or more solvents. Frequently, when two or more nonsolvents are mixed, they may exhibit the qualities of a good solvent. This i s especially true when one of the ingredients is an alcohol. The ether-alcohol solvent mixture for collodion is a familiar example. Another example of acquired solubility is the mixing of butyl acetate with amyl or ethyl alcohol for the less highly polymerized forms of glyceryl phthalate resins. Some of the chlorinated hydrocarbons will dissolve nitrocellulose when mixed with an alcohol. A mixture of benzene and alcohol will dissolve nitrocellulose containing up to 11% nitrogen. A toluene-ethyl alcohol solution of alkyd resin will dissolve nitrocellulose. In many cases the solvent property of esters for resins and nitrocellulose is increased by the addition of an alcohol. On the other hand, when active solvents for cellulose esters are mixed with aliphatic or aromatic hydrocarbons, the solvent power of these active solvents is decreased. These facts bring to light reasons why many of the old-type solvents have been valued for their impurities. For example, methyl acetone, made from the distillation of wood, had particularly valuable solvent properties. Actually, it i s a mixed solvent which consists of methanol, acetone, esters and higher ketones. This mixture has certain desirable properties not obtained by any of i t s component ingredients when used separately. For this reason the "synthetic methyl acetone" is made to simulate it. For this same reason commercial grades of butyl and amyl acetate contain 85% ester and the remaining portion i s the corresponding alcohol. Amyl acetate, containing i t s characteristic impurities when manufactured from fusel oil, is also valued for i t s solvent properties. The synthetic product is different because it lacks these impurities. It is made from the pentane fraction of gasoline by chlorination; the chloropentane is hydrolyzed to form amyl alcohol, and is finally esterified to the acetate. Because of today's concern with environmental pollution, chemical composition limitations of solvent formulations have been adopted by many state and local governmental agencies in the more highly industrialized areas of the country. These rules and regulations seriously affect the use of many solvents, and solvent blends must be reformulated to conform to the maximum allowable concentrations of the restricted solvents. It is necessary for the solvent user t o acquaint himself with the governmental regulations of solvent use in his particular locale.
Hydrocarbon Solvents
PARAFFINS Table 2.2: Ethane (4)
Table 2.1: Methane (4)
I I
FORMULA
PROPERTIES
FORMULA
CHI
RYM iH :;
~~~
I
PURE GRADE
PROPERTIES
I
Composition. mol per cent
I
I RE6Si:EH I
Composition. mol per cent Nitrogen Carbon Dioxide Methane Ethylene Ethane Propylene Propane
. . .
trace 99.97 0.01
0.02
Fmezim point. triple point. F Boiling point, F Specific gravity of liauid a t 60160 F n2W4 C Oensitv of liquid at 60 F. lblgal Vapor pressure et 70 F, p6a Specific gravity of mal gas at 60 F and 14.7 psia (Air = 1) Specific volume of real ga at 60 F and 14.7 psia, cu Wlb Density of real ga at 60 F and 14.7 psia, Ibdw f t Lquid volume, cu Wlb at -260 F and 13.8 p h Critical ternorretun. F Critical p m m . psia Flph point, mproximate. F Flammabilitylimits. volume K in air Lomr I Higher Heatinnvalue for mal nu at 60 F and 1 .30 in Ha. muratadblu'$ BTUl cu ft Heatingvalue for i d u l gm at GO F and 14.7 ph h. . BTUlcu ft, nm 0 hais bnir -. Saturated bldr I
I
60 F and 14.7 psia, BTUlcu h. Dry bldr Saturated bask
I 1 I
low
I I I
.
985
*Litemure valua
*Litemturn valua
3
cu3-cn3
1.0469'
13.0.
..__
17lW 1769.
I I
I
PURE GRADE
trace
0.05 99.35. 0.25 0.35
4
Industrial Solvents Handbook
Table 2.3: Propane (4)
I
FORMULA
I
PROPERTIES
RESEARCH GRADE
Compoution. mlpht p81 unt Ethane Propylene . 99.98 - .PrOP8M Imbume - -- __ 0.02- . - Norm81 Butan8 ___._. Butene2 Neopentane ___ Impentene ._____ ___ Normal Pentane
__
___
__
~
___
Purity by freezing point, mol pucent Freezing point, F Boiling point, F Specific gravity of liquid at 60/W F 10/1
-305.84' (triple poi" -43.73' 0.5077. 0.5005.
c
0.508 0.501 147.0
~
3 71 < O.OW5 60 F and 14.7 p i a (Air = 1) Specific volume of real gas at
0.510 145.9
271 C0.0005
1.5503. 8.4515' -156' _____~.
2.1' 9.5.
L "W
Higher Heatingvalue for ideal gm a t 60 F and 14.7 pi8, dry basis BTUlcu ft
t
2517'
*Literature
Table 2.4: lrobutane (4) FORMULA PROPERTIES Composition, might per u n t Ethana Propylene Proprru Imbutmu Normal B u t m Butm*Z Neopmtane Impentena NonalPentw Purity by f r w i n g point, mol print Fnuing point, F Boiling point, F Specific grrvity of liquid I W80 F
MN c
-
99.96 -255.28. a n an.
I
-
I I
0.583 0.557 119.1 4.68 45.8 72.2 111.5
0.5831. 0.5572.
__ __
. ., Sulfur content, mwt p a cent Specific p i t y of me1 c a t 80 F nd 14.7 p l (Air 1) Spncifc w l u n n of nlp a t 80 F and 14.7 p l , cu ft Ab F*lh point, tppmximat8, F Flammlility limits, wluma% in air Lam HiW Hnting value for idnl gnat 80 F and 14.7 &.dry be61 BTU/cu ft
99.5
iu.aa
0.563 0.557 119.8 4.68 45.4 72.2 111.5
< 0.m
0.m
208M15. 6.3355.
3253.
I I
I
-117
I
I -117 I
I
Hydrocarbon Solvents
5
Table 2.5: n-Butane (4)
I
FORMULA
I
PROPERTIES Composition. weight per a n t Ethane Propylene PlOp8W lrobutine Normal Butam
cna-Cnl-Cnl-cna
RESEARCH GRAOE
I
PURE GRADE
I
T E ~ ~ ~ ~ A L
~
__ __
I
0.05 99.95
I
NOOpmttn8 Iropsntane Normal Penurn
I
I
I
1
I
0.3 99.4
I
I I
I
0.1
1.0
I
97.6
I
0.2
I
0.3 0.2
I
0.2
__ U.6 ..
95.0 min
Table 2.6: 2,2-Dlmethylpropane (4) Neopentane
FORMULA
I
9
cn,+-cn, cn.
I
PROPERTIES
RESEARCH GRADE
PURE GRADE
TECHNICAL GRADE
(continued)
6
Industrial Solvents Handbook
Table 2.6: (continued)
I
PROPERTIES
100 F,pua 130 F, psia - Rdrwtwe index. 2010 Co!or, Saybolt (unless indicatedl Acidity, distillation reudue Nonvcjatile matter, gramdl00 ml Sulfur - content,we4&t per cent ._ C g. e r coy~:on_ _ - Doctor tm. _ _ - . . -Kinematic viscouty, cs at 32 F Specific gravity of real gas at 60 F and 14.7 pria (Air = 1) Specific volume of real gas at 60 F and 14.7 pua, cu Wlb Fl@ point, approximate, F Flammcbility limits. volume% in air .
.
-.
35.9 ___ -57.4
.
. ._ . .
+30
.
+30 - - neutral
.
..
- 36.7 57.1 - __ . -
-_
..
!.Was
-:
_ _ ImJral- _-
-1.-
2.622. 4.997'
. .
-85
1.4.
Low
._ .
8.3.
Higher
_
-
~
.
-85 - .-
-
Table 2.7: lsopentane (4) FORMULA RESEARCH GRADE
PROPERTIES
runE GRADE
TECHNICAL GRADE
0.1
0.2
0.1 99.4 0.4
0.1 97.1
Composition, %@t=mnt
Normal Butam ___________ cc8uto~2 2,2.-Oim*hylpropme Impentam Normal Pentane PmtenbZ Cyclopentane
60 F 8nd 14.7 psia. cu Wlb
*Literature d u n
___..
99.99 0.01
'
.-
-
+N
~. . .. 0.00115- - . - .- 0.005 - -~- . 0005 . - 1 - - - .. 1. _. - !!FE -_ - V!p" - 0.532. - - - - ._-.
__
~-
_
_..- .. . . - .
_- . -
-
.
.
-
I TEiiWil
PURE GRADE
__
-
. .
I
RESEARCH GRADE
...
-
2.8
Hydrocarbon Solvents Table 2.8: n-Pentane (4)
CH,-CH2-CH2-CH2-CH~
FORMULA RESEARCH GRADE
PROPERTIES
PURE GRADE
TECHNICAL GRADE
Comeositjon, weight per cent Norma!_Butane
->-L -.
___
~
_
.- - Z&D~mathylptopane
Imp@nfanr_ - _ N o n r l h n u n e .. . Pentene-2 -Cydopentane
_
~
0.01
-
0.5 988
0.2 99.4 0.1 0.3
99s
.
_-I____
-
99.98 Puritv by freezig pint,mCpar EInt -201.50' Frnzim PO^ F96.93' Boili oint F - __ - - ____-0istiE:on r;mF____ Initial boilingp&nt-. __ 10KCondlnrsd - . .- .____ 5oK Condenrad- - . 90KCondenred _ ._-- - o m - __ 0.6312. Specific Vity of liquid at 60l60 F . 0.62624. , _______ -e1a!!Lc--
0.5
99.2
-
__ -_
-@orprexure
__
_--
-
-
1RF,e~'1-
- .
130 F,p!
..Afmreindex.
2WO
-_ __
__-----
s-.-
9 7 -97-
___-
_____
-92.._--.
-E?!--
.
Color. Saybolt_Lunlessindicated) - _ Acldlty.distclation reudue Nonvolatile matter. pramt/lO&ml Sulfur con!en_t,ei&t per c g ! Copper c o ~ o ~ o n _ _ Doctor tM--- Kinematic viscosity, cs at 32 F Specific gravity of real gas at Fand 14.7 pria (Air = 1) - - - -60.Specific volume of real w at 60fInd 14 7 ptra, cu Wlb Flahpoint. approximate. F Flamm+ulitv limits, volume K in air -L-r Higher
_
-
-~ ~ . _ _ ,
8.56. ___ 15.57. 26.4. 13.5748-. . _ ___-
at 70 F ~ E._
~-
-
_--
AP~pmlFl!@ !- - Density pt_lipuiclat60% l b b l - .
-
0.2-
____
8.6 15.6 26.3 -
--
o s 1 0 633 0.626 _______._ 92.0 _ _ _92.7 _ _ _ . __-5.27 . 5.25
____ +30 neutral O.WO5 0.005 1 mgatm
___
____
+30
-
neutral 0.0005 0.005 1 m m
0.431.
26400. 4.9629.
-50
-57 1.4. 8.3' i
*Literature values.
Table 2.9: 2,2-Dimethyibutane (4) Neo hexa ne FORMULA
I
7%
CHa-y-CH2-CH3 CH-
I
PROPERTIES Composition, weight per u n l Impenunc Cyclopmutm 2.2-Oimrthylbutam 2,lOimoththylbutam 2Mnhylpmatm Mathylpmtm Purity by fmzirq point, mol per Unl Frwzingpoint, F Boiliq point, F Distillation r a w , F Initial boiling point Ow point
REXARCH CRAnF
I
PURE GRADE
0.2
9938 0.01 0.01
99.97 -147.77' 121.53'
99.5 0.2
ai
I
TECHNICAL GRADE
0.1 s6.4 95.0 min. 2.2 0.3
99.4 99.0min.
120.5 122.Z
-
7
8
Industrial Solvents Handbook
Table 2.9: (continued)
RESEARCH GRADE
PROPERTIES
PURE GRADE
*Litwmun dum
Table 2.10: 2,3-Dimethyibutane (4) Di isopropyl
FORMULA
I
?'a'?"'
cna-Cn-cn-cna
I
T E ~ ~ ~ ~ A L
Hydrocarbon Solvents
9
Table 2.11: 2-Methylpentane (4)
FH3 CH,-CH-CH2-CH2-CH,
FORMULA
PROPERTIES
PURE GRADE
RESEARCH GRADE
TECHNICAL GRADE
'Literature v d u n
Table 2.12: 3-Methylpentane (4)
FORMULA
?ROPERTIES
1
I
:"a CH,-CHa-CH-CH2-CH,
RESEARCH GRADE
I
WRE GRADE
I
T E ~ ~ ~ C ~ L
(continued)
IO
Industrial Solvents Handbook
Table 2.12: (continued)
I
PROPERTIES
0.6690.
Specific W i . t y of liquid at 6W60F .- - ._ -atJ@C
API gravity at 60 F Cenr;iy ofTqGdat6o_F.b&$ _._ Vapor p m r e at 70 F, psi8 100 F. pua . i3a F. psia R d r a c ~ w j d e x2 ,W O Color, Saybolt Acid&, distdlaEthylpentme ~__ _ _ - Normel Heptane Dimethylcyclopentene 0.5 Methylcyclohaxsne - _ _ ____~ n L l imethylhexane 1:2E?Ah-.. . . 2.5-Dimethylhexane Other Dimethylhexanes 2,2,4-Trimethylpentane ______-.. 2.2.3-Trimethylpentane __ 2.3.4-Trimethylpentam 2.3.3.Trimthylpenta~
__
-_.o.s
~
~~
-1m
+x---
~ l o Saybolt ~.
.-
...... ...__.
,,.."..,.I I.." "I_ ~
Nonvolatile~ matter. _ gramJlW ~ ulfur . ~ -. . .content - ....weight . . percent .. Coppw corrosion - ~ o ~ oiart -r
~
~
.
_
t
-
. . . . .
-
.
~.IJW5
0.m5
.
.. . . .
__.- . -1
...
~
negative ~. 25 Estimated
~
~~
~-
.
~
Flammabiltv limits. volume % in air I
"-,
I
I
Higher
Table 2.17: n-Heptane (4)
-
~ ~ ~ t , a p p r o - x ~ m . a ~ a.-~~-.. F . -
- .- --
..""..I.
1
Table 2.18: 2,2,4-Trimethylpentane (4) isooctane
FORMULA
I
CHl--ICHIIB-CHa
FORMULA
RESEARCH GRADE
PROPERTIES
PURE GRADE
I
PROPERTIES
CH3
CH3
1
RESEARCH GRADE ~~
Comporition,rnipht perwnt2.3-0inuthylpinta~ 2-Mathylhuana Wnhylhrxana 5Ethylpintne Normal H@ptana D imethykyclopantaw Mathylcyclohaxma
tRCl
99.8
99.99 0.01
0.2 trace
1.2-Dimrthylhlxlm 2,CDitwthylhixam 2.!LOimnhylhuam Dthw Dimnhylhexanm 2 2 1Trim.thvlamuna
Puritv. bv. fnuim_Doim . mol %
99.92
Fmzing point, F Boiling point, F I Distillation ranan. - .F Initial boiling point I .,n PY"'. I Sprific gravity of liquid at 6O/W F 2Ol4 C API orwitv et 60 F
1
Composition.weight perwnt 2.3-Oimithylpantana~ 2-Methylhuane 3-Methylhaxana >Ethylpantma Normal Heptane 0 imathylcyclopantane Methylcyclohixane 2.2.Dimthylhexane 2.44 imathylhexana 2.5-0 imethylhexane Othir Dimethylhexanes 2.2,CTritwthylpantana 2.2.3.Trirnrthylpmtana 2.3.4-Trimthvloantane
99.7 99.0 rnin
."..." 209.17.
"0,
~
Atidiw, dinillation midue Nonvoletik m m r . pmnJlW ml Sulfur conmnt, wi&t pmant C o p p corrosion ~ Doaorta F l r h point, approxinuta. F Flmmabilty limits, v o l u K % in air 1-
nah.r *LiMatun valum.
0.6118 0.684
0.6882' 0.6837k
11.1
neutral
O.ooo5 0.005 1 1lgitiW
25 I
I
, I
..-
1 fl* 7n*
*Litantun valua
CH1
CH3-d-CH2-dH-CHa
PURE GRADE -...._ -
I
__-
-_ -~ .... -
trace
0.01
____
-.
0.2
~__________ 99.99
99.8
Hydrocarbon Solvents Table 2.19: 2,3,4-Trimethylpentane (4)
Table 2.20: Mixed Trimethylpentanes (4)
FORMULA RESEARCH GRAOE
PROPERTIES
PURE GRADE
TECHNICAL GRADE
Purity by f r u i t y point, mol W F r n z i q point, F Boiling point. F Distillation range. F Initial boiling point Dry point Specific p i t y of liquid m W60 f
_-.M I A I:
API gravity at 60 F Density of liquid at 60 F, Ibdgd Vapor p r a w n m 70 F, prie io0 F. PI^ 130 F. osia Rlfnctiw index. ZWO Color Savbolt
.-
Table 2.21: Mixed Dimethylhexanes (4)
FORMULA
PROPERTIES
I I
PROPERTIES C8niI
Dklillation r a m . F GRADE
13
TECHNICAL GRADE
14
Industrial Solvents Handbook
Table 2.22: n-Oxtane (4)
FORMULA
‘Literature values.
Table 2.23: 2,2,5-Trimethylhexane (4)
*Literatun values.
CH,-lCH2Is-CII,
Hydrocarbon Solvents Table 2.24: n-Nonane (4)
FORMULA
PROPERTIES
-
Composition.weight per cant
'Litersum values.
Table 2.25: n-Decane (4)
1 I
CH3-ICH21,-CH3
GRADE
I
PURE GRADE
I
T
E
~
~
~
~
L
15
16
Industrial Solvents Handbook
Table 2.26: n-Undecane (4)
I
FORMULA
PURE GRADE
RESEARCH GRADE
PROPERTIES Composition, wekht per cent Normal Nonane Normal Decane Normal Undecane Normal DOdKane _ _ _Normal Tridecane Isoparaffins
cnp-ICH219-CHa
-
___
TECHNICAL GRADE
-~ .. ._______.
_____
___.____I____
_ 99.8_
99.6
99.1
~
.... ~
0.2
Purity by freezing point, mol K Freezing point, F Boiling point. F Distillation range, F Initial boiling point Dry Point Specific gravity of liquid at 6W60 F--..atW4 C API gravity at 60F Density of l i q u i d 6 0 F, Ibdgal Vapor prarwre at 100 F, p s i Refractive index, 2WD Color, Saybolt ____ Acidity. distillation residde Nonvolatile matter. gramdl00 ml Flash point. approximate. F
0.4
99.64 -14.07' 384.60'
0.9
99-!.99.0&~!_
_____
______._ 96.7 95.0 min
. . . . . . . . . .
__
____
..
.
__
384
-~
........... 385 .
.
0.7443. 0.74024.
0.744
.......... 0.7U
0.740 ... _58.7 ____ 6.19
.......
___
~
1.41725. +30
.................
.--0.739
A
-
.
~
1.417 +30 neutral _-__
0.0005 149
7 6.19
neutral
Table 2.27: n-Dodecane (4)
PROPERTIES
CHa-ICH21 ,O-CHa
* L i m e n valuu
I
RESEARCH GRADE
I
PURE GRADE
........
_____.
0.0005 148
.-
'Literature values
FORMULA
_
1.419 +30
I
Nf;T:E:
_
17
Hydrocarbon Solvents Table 2.28: n-Trldecane (4)
I
FORMULA
CH3-ICH*1, ,-CH3
I RESiSiEH I
PROPERTIES
I
E ; : : :
__
ComPo% .c@!Lwe*r!m-. Normal Tridecane Normal TetradKlne Normal Pentadscane ~.______ Normal Hexadecane Normal Heptadecane lroparaffins
_.
.
~
99.9
99.8
~~. .- _-
~
TECHNICAL GRADE
-
____
~
______
__ ~~.
-
0.1
-
.-
99.2
0.2
~~~
0.8
Purity by freez%point. mol K . ~. -. 99.80 - .... 99.49 99.0 min . 96.81 95Omin-_ Freezing point, F 22.29' Boiling point,______._ F 455.78. Distillation range, F ___.. __ ~___ - Initial b o i ' i n e p o i n t - - ~.~~~__ ~ _ _ 10% _ _ Condensed _____~~___ 50% Condensed ~_ - 90% Condensed Orypoint 458 ~ . _ ~ ~~. ._ -. ____ Spwificqravity -~ of liquid at 60/60 F 0.7601'. . ~ ~0.760 .~ ~.. . 0.762 . at 2014 C 0.75622' 0.756 0.758 API gravity at 80 F . -~ 54.7 54.2 A P L ! W t Y a t G O F ~ _ _ ~ . _______ ___~ Densit of li uid a t 60 F, Ibdgal 633L 6.34_.---1.42560' -__ 1.426 1.427 . -Rafr2ive A x . 2 0 1 ~ 1 _ Color, _ _ Gardner _ _ ~ Acidity, distillation residue neutral neutral Sulfur content, weight percent 0.005 0.W5 Bromine number Kinematic viscositv. cs at 77 F Flash point. approximate, F ~
~
~
~~
~~~
~
~
452
~
~
~~
~~
_____.I
_ c _
~__-
~
~
~~
~
-1 :__-~
'Literature values
Table 2.29: n-Tetradecane (4)
I
FORMULA
Table 2.30: n-Pentadscane (4)
__.__-
___
1 I:S
Sulfur content, wight percent Bromine number Kinamatic viscosity. u a t 77 F Flesh point, approximate, F 'Literature values
99
__
Purity: freezing point, mol X Freezi point, F Boiling point, F Distillation range. F Initial boiling point 10% Condensed -. - 50% Condensed 90% Condensed 0 oint O f Iiqux6SpKz:gr3Vtty at 2014 C API grwity at 80 F API gravity at 60 F Oensity of liquid at 60 F, lbdgal Refrwtive index, 2WD Color, Gardner
Composition, might percent. ~-
I
I
0.4
--
-
1
S%%&
488.33.
--__ --___-
~______~_
~
492 0.769 0.765
.
r 0.7667.y r_____0.76276'__
____-
52.5 -
6.40 1.430
1.42892.
11 I
I I
I
I
250"
I
250"
Normal Tridecana Normal Totradecane Normal Pentadecane~--~ Normal Hexadecane Normal Heptadecane lsoparaffins
Purity by frluing point. mol K Fraezinp point. F Boiling point, F Distillation range. F Initial boiling point 10% Condensed 50% Condenrad 90% Condenad Dry point Specific gravity of liquid at 60/60 F at 2014 C API gcavity at 80 F API Qrwityat 60 F Density of liquid at 60 F, Ibdpll Refnctiw index, 2WD Color, Gardner _ _Acidity. _ _ ~ distillation residui Sulfur content. wight percant Bromine number Kinematic viscosity. u at 77 F Flash point, approximate. F *Litarature values
GRADE
- ..~ -
_99.7
0.3
__
95.0 min
.______
__
CH3-ICH21,3-CH3
I
PROPERTIES
PROPERTIES
Normal Tetradecane Normal-Pentadscane Normal Hexadecane Normal Heptadecane lsoparaffint
I
FORMULA
cu3-icn1i,1-cu,
96.80 95.0 min 48.14
___
__ -
502 512 514 516 0.7721. 0.76830. 51.77' 6.43' 1.4332 s Flash point, approximate. F
50.8
_
____
48.91 6.53 _____
-_
_
____
C
L
-
0 43
300
'Literature values
Table 2.34: n-Nonadecane (4)
Table 2.33: n-Octadecane (4)
FORMULA
PROPERTIES
I I
CH1-ICH1l
,.-CHa
FORMULA
TECHNICAL GRAOE
PROPERTIES
Normal Hexadscane
Normal Octadecane Normal Nonadecane Normal Eicorne lsoparaffins
Normal OcUdecane Normal Nonadecane Normal Eicorne lsoparaffinr
tAPl gravity at 60 F iscormcted from 1WF.
CH1-ICH21,,-CH3
I
Normal Hexadscane
Purity by freezing point, mol % Freezingpoint, F Oistillation range, F Initial boiling point 10%Condensed 50%Condensed 90% Condensed 95%Condensed API gravity at 100 F API grlvity at 60 F Density of liquid at 60 F, Ibdgal Color, Grdner Bromine number Flash point, approximate, F
I I
95.95 95.0 min 81.82 5 mm Hg
302 310 312 312 313 51.8 48.0t 6.56 1
0.48 330
I
Purity by froezing point. mol % Frwzinp point, F Oistillation range, F ___ Initial boilinp point 10%Condensed 50%Condensed 90% Condensed 95%Condenmd API gravity at 100 F API gravity at 60 F Density of liquid a t 60 F. Ibdgal Color, Gradner Bromine number Flash ooint. aooroximte. F tAPl gravity at 60 F is cormctd from 1 W .
TECHNICAL GRAOE
95.37 95.0 min 87.98 5 mm Hp
320 333 336 336 336 51.0 47.3t 6.59 ¶
0.53 335
-
-
___
Hydrocarbon Solvents Table 2.35: n-Eicosane (4) I
PROPERTIES
FORMULA
I
GRADE #ox
Oinillation __- _range, - _ F.- _ - - - -5 mm_HP - - Initial boiling point 340 10% Condensed -__-_--352- - - - - 50% Condensed 354 __-___ ___ 9C% Condensed __ 355 _ _95% _ Condensed _ _ ~ _ 356-___ API pravlty at 100 F -. 49 1 API gravity at 60 F @1f---Density of liquid at- 60 3 ____--F,-Ibdgal - --y -~ Color, Gradner - -. 1 Bromine number __ 0 74 __~_ Flash point, approximate, f . - 360 ~
PROPERTIES Compst&o!. weight percent Normal H e x ~ d e p ~ e . Normal Heptadecane Normal Octadecane __ Normal Nonadwane Normal Eicosenc lvrparaffins
~
__
tAPl gravity at 60 F is corrected from 1WF.
CYCLOPARAFFINS
Table 2.36: Cyclopentane (4)
FORMULA
I
PROPERTIES
Normal Psnunn
Initial baililw mint
'Litontun v d u a '*Major impwitinsarn 2,ZTJimathylbuune and 2,3-0in*thylbutar.
CHz-CH
I CHz-C)4
'2
CH2
19
20
Industrial Solvents Handbook
Table 2.37: Methylcyclopentane (4)
Table 2.38: Cyclohexane (4)
PROPERTIES
_
I
Composition. percant _ _ wight ______ ~ Normal Hexane Msthylcyclopentlnr 2,CDimethylpentam Cyclohexane lrohsptana 3 t - 0 imethylpentm Benzene & Toluene, ppm 1.1 -Dimrthylcyclopmtane 1.2 & 1.3~Dimethylcyclopsn~~~
Purity by f m i q point, mol 96 F m i q point, F
RESEARCH GRADE
I
w.5x
08.0% GRADE
GRADE
0.5 0.1 98.8 98.0 min 0.4 0.2 200 5Wmax
0.1 99.8 99.5 min 0.1
0.01 99.98 0.01
193 5Wmar
I
99.98 43.80.
I
I
98.8
(continued)
Hydrocarbon Solvents Table 2.38: (continued)
*Literature values
Table 2.39: 1 , l -Dimethylcyclopentane (4)
CH1-CH
I
FORMULA
Cli-CH,'
PROPERTIES Composition, weight percent Normal HexaE Methylcyclopentane
I
Specific gravity of liquid at 60160 F . .
90% GRADE
_
_
_
_
p
~
~
____p_
2.4-Dimethylpentane . Cyclohexane ~__ _______ . leheptanes --____3.3.0imethylpentane Benzene & Toluene. ppm . 92' 1.1-Dimethylcyclopentane 1.2 & 1.3-Dimethvlcvclo~entane
.____
~
~
~
~
_
p p
- ..____~___
~ Color, Saybolt Acidity. distillation _____ residue -. Nonvolatile matter. gramdl00 ml ~SulfureweiphtpeGeni-Aniline point, F _ Kauri Butanol value Copper corrosion _____. Ooctor test -- Kinematic viscosity. cs at 32 F Flash point. approximate. F p
0.754 0.749
at __ 2014 C
_
API gravity at 60 F Density 01 liquid at 60 F. Ibdgal pretufre psia ~ ~Vapor _ _ _ at_ 70 _F, _ 100 F. psis 130 F. psia Refractive index, ZWO
_.
00% GRADE
PROPERTIES 'C-tCH,Il
_____ __ _.___ --__.___
117 42.9
_
< 70
- ~ . _ _ _ _ _ _ _ _
Distillation range, F
~___~_______ 'Major impurities are: Cyclohexane. 3.3-Dimethylpentane and 2.Methvlhexane.
10% Condensed 50% Condensed
9mb Condensed
-.-190p---p 190 190
-
21
22
Industrial Solvents Handbook
Table 2.40: 1,2- and 1,3-Dirnethylcyciopentane (4)
I
FORMULA
I
PROPERTIES Composition, w g h t percent Normal Hexane Methylcyclopentane 2.4-Oimethylpentane Cyclohexane - ~. Isaheptanes ______-3.3-Oimefhylpentane Benzene & Toluene. pprn 1.1 Oimethylcyclopentane 1.2 & 1.3 Oirnethylcyclopentane
- ~ _ - _ _ _
Purity by freezing point. mol % Freezing point, F Boiling point, F _ _ Oistillation range, F Initial boiling point ___ 10% Condensed __ 50% Condensed 90% Condensed ___ Dry point
ERAOC -...._ -
,CH-CH,
-
I
90%
PROPERTIES
CH+CH, I H CH,-cH,
-
Specific gravity of liquid at 60160 F at 20/4 C API grrvity at 60 F Density of liquid at 60 F, Ibdgal Vapor prstwre at 70 F, psia 100 F, psia 130 F. psia Refractive index, 2010 Color, Saybolt Acidity. distillation residue Nonvolatile matter, gramdl00 ml Sulfur content, w i g h t percent Aniline point, F Kauri Butanol value Copper corrosion Doctor tnt Kinematic viscosity. cs at 32 F Flash point. approximate, F
90% GRADE
__ _-___ _ ___ - - ~
92t
---
__ ~
_ _ _ .. ~ ~ -~ __ ..___-----
197 197 197 197
____..~-
40.5
I
I
___
PROPERTIES
RESEARCH GRADE
PURE GRADE
TECHNICAL GRADE
Composition, weight percent 1.2.Dimethylcyclopentane
Normal Heptane Methylcyclohexane Ethylcyclopentane Toluene
~
Purity by freezing point. mol %
99.86 -195.87' 213.68'
99.3 99.0 min -196.20
0.7740' API gravity at 60 F Density of liquid a t 60 F, Ibdgal Vapor pressure at 70 F. psia 1 W F, psia Refractive index, 20/0 Color. Saybolt Acidity. distillation residue Nonvolatile matter, gramdl00 ml Sulfur content, weight percent Copper corrosion Doctor test Flash point, approximate. F
0.774 0.769 6.44
1.61. 1.42312* +30
1.6 ______
1.6 1.423 +30 neutral 0.0005 0.005 1 _______________________ negative
._
I 'Literature values.
0.774 0.769
1.423
-
I
22
+30 neutral O.OOU5 0.005 1 negative
I
-
120_ _ _ _ _ - ~ ~ _ _ .
tMijor impurity is 3-Methylhexane.
.
-
_-
Table 2.41: Methylcyclohexane (4)
FORMULA
--~
--___
-__-
-
-
______ 196
.~
0.748 0.744
~.
22
< 70
.-
23
Hydrocarbon Solvents Table 2.42: trans-l,4-Dlmethylcyclohexane
(4)
Table 2.43: cis-l,4-Dimethylcyclohexane (4)
FORMUL A I
I
PROPERTIES
-
Composition. weight percent
1.2 Oimethvlcvclopentane Normal Heptane
__
-
TECHNICAL GRADE
_-__
.. -
TECHNICAL GRAOE
PROPERTIES
-
_
--
_
_ _ _ Ethylcyclopentane
Toluene tram 1.4.Dimethylcyclohrxane cit-1 .4-Oimethylcvclohexane Other Dimethylcyclohexanes trans -1.2.Oimnhylcyclohexans imethylcyclohexane ciS-l.2-0 ortho-Xylene Unidentified Impurities
___ Toluene
__-
Other Dimethylcyclohexanes
___ _~
ci~-l,2-Dimethylcyclohexane orthoXylene Unidnntified lmourities
0.11 ~
99.89 ___-
Purity by freezing point. mol % ___Freezingpoint, F Boilhepoint. F -~ _ Distillation range, F Initial boiling point .~ -- _ _ _5WCondensed Dry point ~gravity of liquid at 6W60 F - _Specific - ._____at 2om-i-
97.4 95.0 min -125.38.
_
255 78.
-
--
-
255 256 0.7872 0.7025 48.2 6.56
~
-
0.7 1.4297 +30 netural
-
0.0005
____
Sulfur-conten!, wegh! percent Copper cotrotion . ooctor test Flash point. approximate. F
..
negative----40 (0 56)
M1
Table 2.44: Mixed 1,4-Dimethylcyclohexanes (4)
I
PROPERTIES
I
FORMULA
C816
I
PROPERTIES Composition. might percent _ 1.2.Dimethylcyclopencne
I
TECHNICAL GRAOE
_
Methylcyclohexane Ethylcyclopentnni TO~UWI trans-1,CD imethylcyclohaxme cis-1.CDimethylcyclohexane 0 t h Dimethylcyclohexanes tnnr-l.2-0imlthylcyelohexne cis-1,Z-Oimlthylcyclohex8ne onh*XyleM Unidentifrd lmpuritia
Freezing point, F Boiling point, F Distillation rage, F Initial _ boiling_ point _ _ ~ _ _.___ . 50% Condensed _ _ Dry _ _point~ _ _ _ Specific gravity of liquid at Mv60 F
API gravity at 60 F Densty of liquid et 60 F, lbrlpll Vapor __ _presure _ nt 70 F. pun
~
44'0 54.9 1.1
1 95.0 min __
I
Sulfur content, m g h t prcent
250 252
-
~ Refractm _ _index. _2WD _ _ -_--_ -Color. Snybolt - _Acidity, _ dinillation rea+!
Nonvolatile matts, gamu'lW ml ____ -
TECHalCAL GRADE
I
14257 neutral
0.0005
24
Industrial Solvents Handbook
Table 2.45: trans-l,2-Dimethylcyclohexane
(4)
FORMULA
RESEARCH GRADE
PROPERTIES
I
PURE GRADE
I
TECHNICAL GRADE
Compowtion, weight percent 1.2.Dimethylcyclopenta~ Normal Hoptin8 . Methylcyclohexane _ _ - - . . Ethylcyclopmtanr - _ TolueM t r m t 1,4-Dimrthylcyclohexane cis1.CDimethylcyclohexane __ Other Dimethylcyclohexanes trans. 1,2.0imMhylcyclohexane ci~l.2-Dimethylcyclohexane ortho-Xylene Unidentified Impurities ~
-
~
99.73 -126.75' 254.15'
99.3 99.0 min -.__
I
t
I
1
Doctor t n l Flash point. approximate, F
I _ -
'LitrrMurr v a l u n
Table 2.46: cls-l,2-Dimethylcyclohexane (4)
FORMULA
'yI
cn,-cH I cn3-cn,
cnI CH./
PROPERTIES
I
PURE GRADE
(continued)
Hydrocarbon Solvents
25
Table 2.46: (continued)
Dry point Specific gravity of liquid a t 60/60 F at 2014 C API gravity at 60 F Density of liquid at 60 F. Ibu'gal Vapor a t 70 ~ F, psia _ pressure _ _ 100 F, pria Refractiveindex, 201D Color, Saybolt Acidity, distillation residue Nonvolatile matter, gramu'lW ml Sulfur content, weight percent Copper corrosion Doctor test Flash point, approximate. F
_
I
RESEARCH GRAOE
PROPERTIES
PURE GRADE ~
0.801
0.8W'
0.796
0.79627'
-
45.2 6.67
~-
0.2
0.23' 0.54' 1.43596' __ __ +30
0.5-..--
~
_____~~
1.436 +30 . _neutral ~______ 0.0005 ____-
0.005
1 nenative 60 (0 56)
-
Table 2.47: Mixed 1,2-Dirnethylcyclohexane (4)
PROPERTIES
Distillation range, F Initial boiling point Dry point Specific gravity of liquid at 60160 F at 20/4 C API gravity at 60 F Density of liquid a t 60 F, Ibu'gal Vapor pressure at 70 F, psia 1W F, pria Refractive index, 2010 Color, Saybolt Acidity, distillation residue Nonvolatile matter, gramdl00 ml Sulfur content, weiQhtDenent Copper corrosion Doctor test Flash point, approximate. F
GRAOE
_ _ _ ~ - _ _ _
Composition, weight percent -
trace tranr-1.2-Dimethylcyclohexane ctr-1.2-Dimethylcyclohexane Ethylcyclohexane Ethylbenzene Xylenes Isopropylbenzene Isopropylcyclohexane .
Unidentified ~
~~~~~
Purity by freezing point, mol % Frsszing point, F Boiling p o c
I
PROPERTIES
FORMULA
trace
_
I I 260
PURE
__
GRAPE -
-
0.792 0.789 47.2 6.59
I
I
0.6 wp 1.432 +30 neutral 0.0005 0.005 1 negative 55(D 56)
'
*Literature values.
Table 2.48: Ethylcyclohexane (4)
I
PROPERTIES
RESWCH
I
PURE GRAOE
I
TECHNICAL GRAOE
~
_
~osfion-we~htprcent Methylcyclohexane tnwl.2.D _ _tmeth@yyoheteane ~ cir-1.2-Dtmsthylcyclohexne
2.0
--
__
Ethylcyclohexane Ethylbenzene -- - Xylem __lsopropylbenzene lmpropylcyclohunr Unidmtifii
99.98
0.02
trace
99.5 0.4
96.9 0.8
01
0.3
(continued)
26
Industrial Solvents Handbook
Table 2.48: (continued)
I
PROPERTIES ~~
RESEARCH GRADE
I
PURE GRADE
I
TECHNICAL GRADE
~
99.19 99.0min 96.06 95.0 min Purity by freezing point, mol X 99.66 168.38' Fmzing poin&f 269.21. Boiling point. F -_ _ ~ Distillation range, F 266 Initial boiling point Dry point -- 269 0.793 0.793 Specific gravity of liquid at 6O/6OF ~- 0.7922' 0.788 0.788 at 20/4 C __ ___._ -- - 0.78792' 46.9 46.9 API gravity at 60 F _.__ 6.60 6.60-_Density of liquid at 60 F. lbdgal . . Vaporprercure at 70 F,psia 0._ 5.- .. 1 W F . E i L .0 . 4 8 ' 0.5 ___. _~ __ .- 1.433 1.43304' _..____ 1.433 __ -. __ ~____ -- Refractive index. 2010.. . +30 +30 +30 Color,Saybolt neutral . , ... ~ _ _ _ _ . neutral - Acidity, distillation residue. ._ 0.0005 0.0005 Nonvolatile matter. grnu'100 ml - .___ Sulfur content, -wj&hthlperEnt. .. . __ .. Copper c o n o s i ~ . - - ~- .. . ~Doctor t a l , -. , . 66 66 Fluh point. approximate. F 66
____
~
~
~
~
__
__
-
___
~
~
- __
_____
'Literature values
Table 2.49: Isopropylcyclohexane (4)
FORMULA
RESEARCH GRADE
PROPERTIES
-__Comqosfi~nLwe~hyerc_Eent -__- Methylcyclohexan?
-_
__
__
-
___
TECHNICAL GRADE
'
--
tran,~,2~imcthy~yclo~xan? cit-1.2 Dimethylcyclohexan~__ Ethylcyclohexane Ethvlbenzene Xylen!! __ _ _ lsopropylbenzene Isopropylcyclohexane __ Unidentified
PURE GRADE
~
____
Purity by freezing point. mol K _ _ Freezing point. F Boiling point. F . Distillationrange. F Initial boiling point ury point Specific gravity of liquid at 60/60 F at 20/4 C API gravity at 60 F Density of liquid at 60 F, Ibu'gsl Vapor pressure at 70 F. pw
0.8064. 06024.
_-
1WF.psia Relractive indax, 20/0 Color. Saybolt Acidity, distillation rcudue Nonvolatile matter. pramdl00 ml. Sulfur conten(,-mwht percent Copper corrosion
0.807 0.803
6.72 __
.
1.44087'
________ -
neutral 0.0005
neutral
0.0005
I I
I
_
Domrtm .____ Flash point apDroximite F 'literature values
0.807 0.803
96
I
I 96
I
96
Hydrocarbon Solvents OLEFINS
Table 2.51 : Propylene (4)
Table 2.50: Ethylene (4)
FORMULA
I
CHI
I
PROPERTIES
RESEARCH GRADE
-
CH2
I
CHI
FORMULA
98.8%
PROPERTIES
GRADE
T
GRADE
Composition. might percent Propane Propylene Ethylene Ethane Methana _ - Carbon&o_xidegpm Acetylene,epm (Iiguidl - Carbonyl, ppm @quid) - CarbonnMonox idegpm
001 99.99
Okwgem
1
CH-CH,
GRADE
0.5 99.5 99Dmin
I
~
-
-
_
_
Hydrogen. ppm Freezinai_nt, trifie poinLF _ _ __ Boilingppt, F Specific aravity otllquid a_t @/@F - -et 20/4 C AplpraviQ-at 60 F - - O g i w i ( y i d at 60 F, Ibrlgal Vaporpr-mre at 70 F. psia _ _ 100 F s i a _ _ 130 F,pua_ Sulfur content, pem &ecific gravity of real gas at 60 F and 14 7 PPI (Air = 1) Specific volume of real gat at 60 F and 14.7 pua,cu ftllb . Critical temperature, F Critical premie, psia Densify of real gas at 60 F and M J RFL~~&IL!L Flarhgozt. wproximate. F __ Iflits,vo!u-mm %in ai --Flamma&lr ----...L o m r Hiahel Heating value for ideal 01s at 60 F and 14 7 psia.BTUlcu ff, dry basis ~
-
-_-. --
_ _ I _
'Literature values
Table 2.52: Isobutylene (4)
FORMULA
PROPERTIES Composition. weight percsnt lsobutane Isobutylene Butene1 Butadienel.3 Normal Butane Butene2 AWtylMe (at Methylacetylene) ppm, wt. Wmr, ppm. wight Carbonyl (P Acetaldehyde) ppm, might Propadiens. ppm. weight
II
CH,-C
RESEARCH GRADE
0.06 99.81 0.09 0.04 tnci
74
-
PROPERTIES
CH1
I
PURE GRADE
0.1 99.3 99.0 min 0.4 0.2 true 177 nil
27
28
Industrial Solvents Handbook
Table 2.53: butene-1 (4)
FORMULA
PROPERTIES
I I
CHa-CH2-CH
RESEARCH GRADE
-
I
- Composition, might percent
0.2 99.8
lrobutylone BUtOnbl Buudienel.3 Normal Butans Butone2 Acotyleni ILI Methylacetylene) ppm, W . Water, ppm. might Carbonyl (LI Acnaldehyda) ppm, might Propdieno. ppm. might
0.1 0.3 99.4 99.0 min
8.
"Y
0.2 trace 15 25max
10 20max
4
I
20.73. 0.6013' 0.5951.
1 , W ' p '
Vapor p m r e at 70 F.. oria 100 F. pria osia_ _ _ _ _ _ _ _ _ 130 ~ _F. _ Sullur content, ppm Specific gravity of real gar at 60 F and 14.7pria (Air = 1) Specific volume of real gas at 60 F and 14.7 osia. cu ft/lb Flash point, approximate. ___ Flammability l i m - Lorn Highcr - --
trace
I
RESEARCH POLYMERIZATION GRADE GRADE
I -301.63.
Freezina Doint. F Boiling point, F Specific gravity of liquid at 6060 F at 2014 C API gravity at 60 F
POLYMERIZATION GRADE
lrobutane
I
PROPERTIES
CH1
0.601
,
I
I
103.9 C
M
-
3 . -
376
i 997 i i i 005F)
I
1
1 10max
__
i
i
1.6' I
9.3.
i
__ I
*Literature values.
Table 2.54: trans-Butene-2 (4)
H
FORMULA
CH,-C
-
C-CH9 I
H
Composition, mipht pment Buowl Normal Butlno trans-Butenb2 cieBuhnb2
0.03 0.07 99.80 0.10
99.6
97.7 95.0 min 1 .o
0.2
99.76 -157.99.
Purity by frnzing point, mol K Frnzing point, F Boiling point, F Specific gravity of liquid at 60160 F at20/4 C API gravity at 60 F Density of lipuid at 60 F. Ibdgal Vapor pnrwre at 70 F, p i a 105 F, psia 130 F, prb Flash point, approximate, F
trace 1.3
0.2
99.2 99.0 min
33.58. 0.6100. 0.6042.
______
0.610
1W.5 5.07 29.9
29.94'
.. __ 52.2 __ . 76.4 -100
0.609
100.8
-
5.07 _____ 30 52
___
.
76
-lw
Table 2.55: cis-Butene-2 (4)
FORMULA
PROPERTIES
I
H I
CH,-C
RESEARCH GRADE
-
H 1
C-CHI
GRADE
TECHNICAL GRADE
Compoaition, might prcmt Normal B u m cbButsm2
99.5
95.7 95.0 min
(continued)
Hydrocarbon Solvents
29
Table 2.55: (continued)
RESEARCH GRADE
PROPERTIES
-
Purity by freezing point, mol 96
TECHNICAL GRADE
PURE GRADE
99.92
99.4 99.0 min
-218.M. Freezingpoint, F 38.70. . Boiling point. FPP~__.~._. Specific gravity of liquid at 60160 F 0.6271. 0.627 at 2014 __ - 0.6213. APhravity at 60 F 94.2 _._ ._ _ .. Oenrity of liquid at 60 F, lbs/gal-. 5.22 Vapor Pr-re at 7_olsc ~. 27.29' ~- 27.3 105 F. pria .. . . 49.8 73.2 130 F. psi!-_.. .. . -. .. _. Flash point, approximate, F -100 ~
___
~
0.632
.c_____ ~~
-
92.4 5.26 27.8 50.8 74.8
~
~
~
.
-_______
~
~
-100
Table 2.56: Mixed 2-Butenes (4)
I
FORMULA
I
PROPERTIES
Freezingpoint, F Boiling point, F _. S p ~ i f i c ~ ~ i . ~ o ~ l a. ti 60160 q u i dF at 2014 C API.p i t y at 60 F Density of liquid at 60 F, Ibdgal M o r prspure at 70 F. p i a ._ 105 F. psia I30 F, pria . .~_____._ Flash point, approximate. F ~~
CH,-CH
-
CH-CH3
1
PURE GRADE
TECHNICAL GRADE
~
0.618 0.614 97.5 5.14 28.1 51.2 78.7 -100
0.619 0.615 97.1 5.15 28.0 51.0 76.5 -95
*Literature value%
Table 2.57: 3-Methylbutene-1 (4)
FORMULA
PROPERTIES
CH2
I
RESEARCH GRADE
I
-
7%
CH-CH-CH3
PURE GRADE
99.97
I TEOCIX:C!L 96.3 95.0 min
Pentanes-2
0.01
tme
0.5
Normal Pentane
(continued )
30
Industrial Solvents Handbook
Table 2.57: (continued)
.
9 9 4 99Omin
Purity by freegng point, mol % Fretzinppoint. F Eojlgpnt, F Distillation ranE, F_ Initialboiling point Dry point Specificpravity of lipid-at60160 F-:. at 2014 C APl g & t y a t 6 0 F -. - -. Density of liquid at 60 F, Ibdqal Vapor pressure at 70 F, p a F, pria 130 F,psia Refractive index. 20/0 Color, Saybolt Acidity, @stil+_n residue Nonvolatile matter, gramdlW ml . Flash point. approximate. F
-2l1.29. 68 11.
-
- -
0.63% 0 6272'
15,25* 26.41'
~
0633 0.628
-
-1.3643' +30
I 1
-
~~~
__
-
.
EO
~
. ~
1
13.364
1
-70
.
-
5.27 15 0
1364 +30
-70
*Literature values
Table 2.58: 2-Methylbutene-1 (4)
I
FORMULA
~~
Composition, weight percent ____ 3-Methylbutene.1 trace 2 Methylbutene-1 99.99 99 8 2 Methylbutene-2 __ trace Pentene-1 ______ -_ --4sl 01 trace Pentensr-2_ _ _ _ _ -~- _.___ . lsopentane -._ __ .- - Normal Pentane 01
03 9 7 3 95Omin 01 19 0.2
~
__
Purity by freezing point, Freezing PO% F 8 o l ~ ~ ~ w ! ! l ! __-__ L Distillations, F Initial boilinppoint -
~~
__
C
Y
E
!
99 05
_- -215 -61' __ _____ .- ___ 8809'__ ___
.--9 9 5 99Omin - ._ - __ __ .. ~~
----
___~
-
___
~
!
02
~~
._-
~
_ _
87 88 0 656 0 650 842 5 46 10 3
Specific gravity of liquid at 60/60 F 0 6557. -. 0.656 . at20/4&--0.6504:-- _ 0 650 __. API gravity at 60 F 842 _ _ --546 , Density o f liquid at 60 F, lbrlgal Vapor pressure at 70 F, pria - 10 _ 21' _ _ 103 100 F. pria 18.40. 18 8 18 8 130 F. pria 32 0 32 0 - - -____ Refractive index, 20/0 13778' 1378 1 370 --- -- - -. - - __ . Color, Saybolt . -+34 - _ _ .- +30 +M _ Acidity. distillation residue-utral __ neutral - - .- - - n eNonvolatile matter,gramdl0(l ml . O.DW5 0 0005 Flash point. approximate. F -55 -55 ~
~
__
___
___
-
~
~
'Literature valuer
~~
-
.
Hydrocarbon Solvents Table 2.59: Methylbutene-2 (4) _~
I
FORMULA
3 CHl-C=CH-CHl
RESEARCH GRADE
PROPERTIES Compo$o_n,weight percent 3Methylbutene 1 2-Methylbutenel
.
2MeWuteoe-l Pentenell-
Pentenes2
__lsopentane
-
- -
TECHNICAL GRADE
COMMERCIAL GRADE
.
_
- - __
-.
10 3 87 8
0.2
0.2
trace 99 99 trace 0.01
I
~
PURE GRADE
97.4 95 0 rnin 0.1 2.3
99.5
0.3
08 1.1
-,
Normal Pentane
Purity by f!SzinppoinJ,m>l% Freel1111I S S M I N & I I A I S I I I I I I I S
.. - . sToD.~n.D.so~~~~~E.~.. HllRRl I 1 S l l I V C N l
il
1b7I'
ii
i w-
...
~
0.7720
fir xs1.11~
,I fiH? I1 I I V
VMCI'NAI'IIIHA
I
In e ,
!7 9
I 11
HEXSOLV
I
VM h P N A P H T I I A
U460 S O L V E N l V M h P N A P l l l t l A 66
MINERALSPIRITSO8 VI40 SOLVENT 66 -
__
-
__ -
705
14
I47
n
0 21
33
166
108
n 11
11
140
ll
I,'
:::I:
14
1411
5>
I 1
I7
-
-
.-I -----
13 -~ 0.7
1411
1 4
_4 _0
(1 n __
108 __ I44
n nn
-
0.7 ._
in
-I------
spec
AROMATIC HYDROCARBON SOLVENTS
I
6 Ill
I 11
-
HI1
1.o
M l N F R A l S F A l 011
-_-_ --_BTODDA~D~OLVENL -
I
I >
..... .
105
-
R II
1 il
I46 1 V
IA( O I I F R 1111 llf N 1
__
760 mm ng
1.1'
Ilt I d N l
wmn SUIVI
-
I1 11'1
lit I ' l A N I
I A , , < > I l t 14
lndsa c 20%
uo1rac
Gravilv Per
"C
DTN7FNL
mi
TO1 V I N F
7A'iil t
11970
14670
1472 14897
14882 ' 4962 I5020
8n 806 110111
176 171 730232
63
64
Industrial Solvents Handbook
Table 2.127: Crowley Solvents (60)
METHYL NAPHTHALENE NO. 5
Specific Gravity 60'/60"F
Specifications
TYDica1
0.975/1.010
0.988
Distillation Range:
' F
"c
' F
I B P , Min. FBP, Max.
4 00 600
204 315
440 550
227 288
200
93
215
102
Flash Point, PMCC, Min. (Non-Combustible) Aromatic Content, Min. Mixed Aniline Point, ASTM, Max.
61
Color, ASTM, Max.
95%
98%
16.1
11.8
1.0
-2
Pale Straw
Color, Visual 15
Pour Point
.9279/.9465
Distillation Range OF. IBP 5% 10% 50% 70% 90% 95% EP
375 449 465 523 564 634 666 689
-10
SAF-T-SOL ZOO
AROMATIC SOLVENT 58
Specific Gravity @ 60'F.
22-
Specific Gravity @ 60/60"F
0.987
Distillation Range (ASTM D-850) 5% 50% 90%
430°F 555'F 590'F
Aniline Point, Mixed ASTM
15'C
color
Yellow
ssu
40 secs
Viscosity @ 1 0 0 ' ~
Flash Point OF.
240
Pour Point
-60'F
Yromatic Content
74%
Flash Point, COC
250'F
Color
2.0
Aromatics
98%
SSU Viscosity @ 1 0 0 ~ ~ .
46.3
Pour Point 'F.
-25
Hydrocarbon Solvents
65
Table 2.128: Dynaloy Solvents (37) DESCRIPTION Dynasolve 210 was developed to fill a widespread need for a solvent that would dissolve RTV silicones and silicone conformal coatings effectively at room temperature. Dynasolve 210 dissolves silicones quickly and effectively, but it contains methylene chloride, and may attack other polymers or coatings, such as epoxies and urethanes. Dynasolve 220.225, and 230, while not quite as fast as Dynasolve 210, contain no chlorinated solvents and are more selective. In most cases, Dynasolve 230 is fastest, followed by Dynasolve 225, and then Dynasolve 220. Dynasolve 210, 220, 225 and 230, when not contaminated by water, will not attack metai or metal components, with the exception of aluminum. However,aluminum may be etched after extended immersion in these Dynaadves. Contaminationof these Dynasdves with water will result in the formation of acids that can attack most metals and other substrates. Test data showsthat mu-metalwas untouched after a 24 hour immersion in Dynasolve 210. Dynasolve 220; 225, and 230 will not attack acrylic or polycarbonate. TYPICAL PROPERTIES Color Specific Gravity Boiling Point Flash Point PH
DYNASOLVE 210 Amber 1.272 104 F None 2.14
DYNASOLVE 220 Amber 0.828 31 1-348 F 110 F 1.70
DY NASOLVE 225 Amber 0.806 235-290 'F 52'F 1.60
DYNASOLVE
230 Amber 0.707 202-222 'F 16°F 1.30
DYNASOLVE CU-5 SAFETY CLEANING SOLVENT FOR URETHANES DESCRIPTION
Dynasolve CU-5 i s a u n i q u e s o l v e n t t h a t was developed f o r use i n c l e a n i n g urethane r e s i d u e s and c r y s t a l l i z e d i s o c y a n a t e s f r o m v a r i o u s t y p e s o f p o l y u r e t h a n e p r o c e s s i n g equipment. T Y P I C A L PROPERTIES
Color: Specific Gravity: B o i l i n g Point: Flash Point: pH :
C 1 ear 1.060 202oc 191OF CC 4 - 6
DYNASOLVE CU-6
SAFETY CLEANING SOLVENT FOR URETHANES
DESCRIPTION Dynasolve CU-6 i s a unique s o l v e n t t h a t was developed as a n o n - g e l l i n g , h i g h e r f l a s h p o i n t v e r s i o n o f Dynasolve CU-5. TYPICAL PROPERTIES Color : Specific Gravity: Boi 1i n g P o i n t : Flash Point: pH :
Clear 1.055 202oc 210OF CC 4 - 6
(continued)
66
Industrial Solvents Handbook
Table 2.128: (continued)
DYNASOLVE XD 16-4 SAFETY SOLVENT FOR REWOVAL OF SILICONE OILS AND UNCURED SILICONE POLYMERS DESCRIPTION
Dynasolve XD 16-4 i s an experimemtal solvent t h a t was developed f o r removal o f s i l i c o n e o i l s and uncured s i l i c o n e polymers from molds, molded p a r t s , and processing equipment. TYPICAL PROPERTIES Color: Specific Gravity: Boi 1i n g Point : Flash P o i n t : pH:
L i g h t Amber 1.032 >3000F 2620 F N/A
DYNASOLVE XD 22-1 SAFETY SOLVENT FOR CLEANING AND DEGREASING DESCRIPTION
Dynasolve XD 22-1 i s an experimental solvent t h a t was developed f o r use i n cleaning and degreasing a p p l i c a t i o n s . Dynasolve XD 22-1 i s a non-chlorinated, non-flanmable', non-carcinogenic, non-ozone d e p l e t i n g s o l vent TYPICAL PROPERTIES Color: Specific Gravity: Boi 1i n g Point : Flash P o i n t : pH :
C1 ear 0.780 360° F 143OF CC N/A
DYNASOLVE XD 27-2 SAFETY SOLVENT FOR CIRCUIT
BOARD CLEANING
AND DEFLUXING
DESCRIPTION
Dynasolve XD 27-2 i s an experimental solvent t h a t was developed f o r cleaning and d e f l u x i n g o f p r i n t e d c i r c u i t boards. Dynasolve XD 27-2 i s a non-chlorinated, non-flammable', non-carcinogenic, non-ozone d e p l e t i n g solvent designed as a replacement f o r CFCs. TYPICAL PROPERTIES Color: Specific Gravity: B o i 1i n g P o i n t : Flash Point : pH :
Transparent Yellow 1.000 3630 F 191OF CC 8 - 9
..
% c: cy
i
a a 3
w
a bl
3 Q
c z w >
4
5:
0
uu1
Q
e
C 'C
L
I
m 7
v)
x
w
a
L
ea U
w
I
n
w
>
>
W
53
s
n
).
Hydrocarbon Solvents
67
68
2
h
Industrial Solvents Handbook
-I
" o 9 N
v N
Hydrocarbon Solvents
69
70
Industrial Solvents Handbook
t
ai
j
. ....
. .. -
r" 01
c
Hydrocarbon Solvents
71
72
..
Q)
cv
Industrial Solvents Handbook
I
I
~
I
74
Industrial Solvents Handbook
Table 2.131 : Flna Aromatic Solvents (6)
Typical Properties Solvent Name
Flash
IXslillation De&
,
Common Apvlications
FAS 70
180
20
150 645
Warnicr climate oil well appliullwm Wood trcaling prerrvalivr
FA5 104
115
30
m-495
Down hole oil well applicahons Washoil Reaction solvent in chemical pr<xnsing Carrier solvent for spccially chemicals High oclane gasolinr hlendstwk
FAS 150
155
22
370 - 630
Very similar lo FAS 104 except higher flash Uscd in the same applications as FAS 104.
FASTX-150
155
26
w-4w
Water white (Sayboll +30) solvcnl Paint hlendslock/solvcnl Reaction solvcnt in c h r m i a l processing for spccially paint and oilfield chrmicals Oilhcld chemical solvrnl High quality wash oil
FAS Tx-200
219
11
450 - 527
Carrier for agricultural products High flash solvent applicalions in coatings Used in manufacturing specially chemicals
Toluene (90% Purity)
31
232 - 253
High oclane, low RVP gasoline hlendstock
Xylene
31
281 - 285
Many uses in solvents, gawlinr, chemical processing
Table 2.132: Hoechst Celanese Methyl Isobutyl Ketone (42)
Methyl lsobutyl Ketone IMIBK. Isobutyl melhyl ketone, Hexane, Isopropylacetone; 4-Methyl-2-pentanone)
Physical Properties AutoignitionTemperature
MO'F (449°C)
Cntical CompresstbilityFactor
0.254
Critlcal Pressure
32 3 a h
Cntical Temperalure:
298.3%
Criical Volume:
0.369 mVkmol
Dipole Moment
9.0 X 10-30cm
EvaporationRate (n-BuAc = 1):
1.54
FlammabilityLimil (vol %in air): Upper Limit: L o w Limit:
8.0 1.2
Flash Pointa gl(
60°F (16°C)
Closed Cup):
Freezing Point:
Q)
U
I
-m
Q)
I
U
m C
I
0
e
Y
p.
>
m
(R
U
W
m u,
X
W
W
iii
Q)
> w Y
.-> w
5
8 a?
C
Y
C
-a 8
Y
5
W
>
a?
N
r - w
W
I P(D
r - O P m mC9.p 0
P(D
N O
Hydrocarbon Solvents 83
H
84
Industrial Solvents Handbook
B3
.-C 0
C
c
0
1
c
I
N
2
W
-.
Hydrocarbon Solvents
5
b
a
I
E 0
%
01
I
I
x
;
I
m
0
h:
0
w
=?
I N 7
6
0
0
z
w N
85
86
Industrial Solvents Handbook
n I
el
> w
ee
a eew
m
> w
a w x
L 0
d .
E
B 7
= I
m o
n
?
Hydrocarbon Solvents
4
b b L a a a a a a I 8 000 000 t
4
2 W
$1 0
.T
2
x
c\!
I m N m m - a m N
I
4 N
I I 6
W
0
UJ
I
0 0 0 0
w 0
UJ
9
m 0
N
0 0 0 v
3
7
W 0 r
0 m
N UJ
E
00 x
V
8
-1
r:
0
z
0
c
f: W
i-
2
a
>.
v,
r
u,
-
V
X
u,
21
c
V
9
3
Y
N
I
2
I
F
0
N
0
W
z
-
0 9 h ?
2
h N
Nv!2
N 0
T
I
el 0
0 0 0
u, x
V
a
s
cl
r E
E
0
z
E
cl
0
87
88
..
k
Industrial Solvents Handbook
tn U
a"
I I I I I I I I I I I I I I I I I I I
-nu,
h m
? ? ? s
V)V)
(Dh
hr- r-h
o m
LOV)
=I
6 0 0
C
Y
.-C u
Y
..
Ih (3
c
I-
-1-1-1-1-1-1-1-1
u v c w w x
J-1-1-1-1-1-1-1-1
w z w w z a m
-1-1
o r
e x -1-1
-12
m m
gg
Hydrocarbon Solvents 89
90
Industrial Solvents Handbook
Table 2.138: Sunoco Chemicals Solvents (72) Mineral Spirits - Toledo Refinery __ Tests
Sales Specs
Typicals
c b n ~ b o r l , V d%
-
Test Method Sun GC-MS
48 0 02 74 4 17 4 a01 0 782 Mm - 0 799 hb.
0 791
D8Y I
47 4
D287 D86
MoMin-33oMax 395 Max 1.5Max
320 387
25 Mi11
30
13 I 50
Clear
Clear
V d
105 MiIl
I IO
DX,
29.0 Min - 42.0 Max
39
d1133
I20 Min
126
D61 I
loo Max
1 .o
4
d4w5
copper-
LA
D130
BromincNwlber
370
390 4w 420 475 480 510 148 154 100 Rosin (wood) .............................. ABALYN . Resin esterified SARAN** F-120 . Vinylidene >I00 with glycerine .......................... < 1 chloride-acrylonitrile ACRYLOID 6-82 -Acrylic ester >I00 SARAN F-220. Vinylidene AMBEROL 801-XLT . Phenolic ....... >I00 chloride-acrylonitrile < 1 AMBEROL ST-137-X . PhenolVELSICOL AE9 . ET0 adducts I00 VERSAMIDE 940 . Polyamide >100 BAKELITE CKR-5254 . Phenolic < 20 VlNYLlTE AYAA . Vinyl acetate >100 BECKACITE 1001 . Phenolic .......... >I00 VlNYLlTE WHH . Vinyl chloride BECKACITE 1112 . Phenolic >I00 acetate ................................... I00 PICCOPALE 100 . Polyvinyl Chloride ....................... < 1 Polyalkyl styrene .... >I00 Resin 276-V9 . *Trademark of The Dow Chemical Company 'Too viscous for further addition. **Trademark of The Dow Chemical Company overseas tSolubilities were determined by the incremental addition of solute to 100 grams of methylene chloride at room temperature. Solute was added in the following increments: 1 gram. 5 grams. 10 grams and so on in 5-gram steps up to a maximum of 100 grams Thus a notation of IO0 Resin riolubilities were obtained on uncured material suitable for use in paints. adhesives. and coatings.
.................
......
................. ....... ........ .....
......
..........
.................................... .........
...............
......................... ...........................
..................
..
.....
.
.
.
(continued)
154
0
Industrial Solvents Handbook
%I WW
0
y.
i
Y
v)
W
.-W
E
W
->.
.c
8
-6 0 r
-
5 E I
W
8
Halogenated Hydrocarbons
155
156
6
0 W
$
+
0 -?
3
Industrial Solvents Handbook
m
CI
0" .-I>: j ! i
L
0
m
'
u) 3
+ v G
-IO m
+ +
0 N
0-U + o
LL
0
0 - -
. ..
.
.. ... ..
.
.. ... ...
.
.:Pas
.. zL .A y ... * z z
Z
Z Z P P Z
.. ... .: . ..
?q
.. . ..
.
. .
S S~ .. .. .. .. .. .. .. .. . .
.
.. . ..
~
a
-0 al
C
Y
.-C 0
..
0
v
F
al
2 m
n
c
w
Halogenated Hydrocarbons
157
158
Industrial Solvents Handbook
Table 3.61 : (continued) Blending Solvdnts to Eliminate Flash Points F W Poiits ("F) -Tag Closed Tater Volume 96 Chlorinated Solvent Family
Flammable Constituent Data Source
0
10
20
30 40
50
- - - - - _ .
Alcohol
Ester
Ethanol
60
n-Butanol
106 94
NF
Butyl Acetate
84
81
76 NF
Ethyl Acetate
25
32
34
39 41 NF
21
23
21
22 NF
Octane
59
49
NF
MethylIsobutylKetone
64
64
64
Hydrocarbon Heptane Ketone
54
48 NF
62 NF
Thermal Conductivity vs. Temperature for Methylene Chloride
9 q B
Temperature, OF
3
E
Temperature, O C
C
$
v
4'
Vapor Pressure vs. Temperature for Methylene Chloride Temperature, O F
,m
1
700
500 M 300 200
3: E E
100
70
!E so 30
8 l-
2o 10
E ;
9 3 2 I
-70 -60
-so
4 0 -30
-20
-10
o + I O +2(1
Temperature, OC
+30 +40
3
so
.
-I
-60
-so
-40
-30
-20
-10
0
+ I O i 2 ( 1 +'r)
Temperature, O C
$40
is0
Halogenated Hydrocarbons Table 3.61: (continued)
Viscosity Curves for Common Secondary Refrigerants
3
I
I I I 1
X = Freezing Point
I
I
Temperature, O C Glycerol Ethanol Calcium Chloride Methanol Sodium Chloride Trichlorofluoromethane Methylene Chloride
= 64.8% Wt. (Aqueous Solution) = 56.8% Wt. (Aqueous Solution) = 29.0% Wt. (Aqueous Solution) = 38.4% Wt. (Aqueous Solution) = 2 1.O% Wt. (Aqueous Solution) = 100% Wt. = 100% Wt.
IS9
160
Industrial Solvents Handbook
Table 3.62: Vertrel Cleaning Agents (7 7) Vertrel KCD-9547 Cleaning Agent Introduction Vertrel KCD-9547 is a proprietary azeotrope-like blend of Vertrel XF hydrofluorocarbonwith trans-l,2-dichloroethylene and cyclopentane. It is ideally suited for use in vapor degreasing equipment to remove light oils, fingerprints, and particulate contaminants. Vertrel KCD-9547 is specially formulated to provide a high degree of compatibility with plastics, elastomers, and other nonferrous metals, such as in aerospace parts. Vertrel KCD9547 is nonflammable, has "zero" ozone depletion potential, and has low global warming potential. It can replace CFC-113,l ,I ,1-trichloroethane (1,I ,I -TCA), hydrochlorofluorocarbons(HCFC), and perfluorocarbons (PFC) in many applications. Physical Properties
Density and Vapor Pressure Change with Temperature
Vertrel' KCDUnits
9547
CFC-113
"C O F
37.2 99.0
47.6 117.6
Liquid Density
g/cc Ib/gal
1.29 10.8
1.56 13.1
Vapor Pressure
rnrnHg psi
414 8.0
334 6.5
Surface Tension
dyn/crn
15.3
17.3
"C OF
C-50
Physical Properties of OXSOL 100 Freezing Point, "C Boiling Point, "C Flash Point, TCC, O F Evaporation Rate at 25"C, n-BuAc = 1 Solubility Parameter ( c a l / ~ m ~ ) ' / ~ Density @ 25"C, lb/gal Kauri-Butanol Value Solubility of water in OXSOL @ 25"C, ppm Solubility of OXSOL in water 6%25"C, ppm Surface Tension @ 25"C, dynes/cm2 Heat of Combustion, BTU/lb Viscosity @ 25"C, cp CAS#
Sales Specifications Appearance Color, APHA Acidity, ppm (by specific ion probe) Alkalinity, ppm a s NaOH Water content, ppm Specific Gravity @ 25"C/25"C Non Volatile Residue, Wt. %
-36 139 109 0.9 7.3 11.2 64 240 35 25 7100 0.79 98-56-6
CFOSM 20 Max 3 Max 10 Max 150 Max 1.33-1.35 0.0020 Max
(continued)
178
..
m
:
Industrial Solvents Handbook
-
P
0
I-
E
a
a,
?!
c
5
9
0.
2
8 OD 0
In 0
0 d
0 (u
0
0
B
0
S
8
'si r 8
x
N 0
P 0
V
W
e
c 3
Q
" ki-
o
8 " F-
- 8
c
E
a
f
c
3
9
-s 9 .E
- 0
0
"
Vapor Pressure, rnm of i ig
-8
Halogenated Hydrocarbons
0
-z
179
180
Industrial Solvents Handbook
0
s!
L 3
F?
c Q)
Q
E
llJi
>
Vapor Pressure, mm of Hg
f
v
1 c
f
Halogenated Zyydrocarbons 181
182 Industrial Solvents Handbook
-1
E:X 0
u)
>
m(1)
c
c
c
I Q)
-I
m
c
P3
C .+-
c u 0
I
Halogenated Hydrocarbons
183
184
..
m
Industrial Solvents Handbook
Vapor Viscosity, centipoise
8 0
N OD
0
3 N
e N
0
0
N
: 0
m
r
0 7 W
s
0
0
2
-8 aD 0
W 0
0 t
N 0
0
N
0
0
'f
h
9
0
8
(D
v) v)
Liquid Thermal Conductivity, Btu/hr.ft."F (0
v)
8
v) v
Halogenated Hydrocarbons
Ln
2
c
-8
185
186 Industrial Solvents Handbook
Vapor Thermal Conductivity, Btu/hr,ft,"F
Halogenated Hydrocarbons
187
Table 3.63: (continued) OXSOL 2000
Chemically, OXSOL 2000 is alpha, alpha, alpha-trifluorotoluene, an HFC. OXSOL 2000 has a number of desirable properties for precision cleaning, electronics cleaning, aerosol applications, and wipe cleaning. It is a pure compound, with a relatively fast evaporation rate and toluene-like odor. In its pure form, OXSOL 2000 is a good replacement for hexane, toluene, and VM&P naphtha where a rapid evaporation rate is desirable and a flammable solvent can be used safely. In addition, OXSOL 2000 can be blended with classical solvents like trichloroethylene yielding non-flammable, very fast evaporating compositions.
Physical and Chemical Properties of OXSOL 2000: Property Chemical Formula Molecular Weight Boiling Point: "C (OF) Dielectric Constant, 25°C Flash Point, TCC "C (OF) Fire Point, TOC "C (OF) Kauri Butanol Value Evaporation Rate, n-BuAc = 1 Latent Heat of Vaporization (B.P.), BTUllb Specific Heat, Liquid 20°C (BTU/lb/"F) Density, 20°C, gm/cc Density, 20°C, Ibs/gal Vapor Pressure (20°C), mm Hg Vapor Density (Air = 1) Surface Tension in Air: Dynes/cm:2O0C Viscosity (Cp), Liquid, 20°C
C,H,F, 146.11 102 (216) 11.5 12 ( 5 4 ) 23 (74) 49 2.8 97 0 306 1185 9 88 30 5.0 23 0 56
Density of OXSOL 2000 1.26 1.24 1.22
1.20 0 0 1.18
\
cn
v
2, 1.16
.-
v)
n
1.14 1.12 1.10
1.08
1.06 -40
-20
0
20
40
60
80
100
120
Temperature (C)
(continued)
188
Industrial Solvents Handbook
Table 3.63: (continued)
Liquid Heat Capacity of OXSOL 2000 0.37
CI
n=
0.35
3
I- 0.33
9 .P 0
0.31
0" c)
L 0.29
I
Ea .g 0.27 J 0.25 -40
-20
0
20
40
60
80
100
120
Temperature (C)
OXSOL 2000 Liquid Thermal Conductivity
(continued)
Halogenated Hydrocarbons
189
Table 3.63: (continued)
OXSOL 2000 Vapor Thermal Conductivity 0.005 A
!F
f 0.005
s
2 0.004
0.002
40
-20
0
20
40
60
80
100
120
80
100
120
Temperature (C)
OXSOL 2000 Liquid Viscosity
-40
-20
0
20
40
60
Temperature (C) (continued1
190
Industrial Solvents Handbook
Table 3.63: (continued)
0.030
0 025
g- 0.020
.0 v)
$
0.015
5 L
0
>"P 0.010 0 005
t
.___-
0.000
7
:
:
:
:
1
:
-
:
---+,I
:
:
1
.
.
:
.
1
.
.
~
.
i
,
,
'
'
I
.
.
,
,
I
,
"
'
OXSOL 2000 Heat of Vaporization
c 108 --
0 .c
-40
-
-20
0
20
40
60
80
100
120
Temperature (C)
(continued1
Halogenated Hydrocarbons
191
Table 3.63: (continued)
OXSOL 2000 Liquid Vapor Pressure 1000
100
10
__
/' /
' +---
I
___
-+____
_-
2 . -
I
1 -40
-20
~___
I 0
20
40
60
80
100
120
Temperature (C)
OXSOL 2000 Liquid Surface Tension 31
29
E 0 3 27 E
h
s
c 25
.-0 v)
c
E
23
0)
0
21
; .u)
19
-I
17 15
-40
-20
0
20
40
60
80
100
120
Temperature (C)
(conti nued)
192
Industrial Solvents Handbook
Table 3.63: (continued)
Sales Specification
OXSOL"550 Soecifications
Test Appearance Color, APHA Acidity, ppm as Total Inorganic Acidity (by Specific Ion Probe) Alkalinity, ppm as NaOH Water Content, ppm Specific Gravity Q 25"C/25OC Residue on Evaporation, Wt. %
Clear, Free of Suspended Matter 30 Max. 3 Max. 10 Max. 150 Max. 1.20-1.22 0.0025 Max.
Phvsical ProDerties OXSOL 550 is a clear, colorless blend of Halogenated Aromatic solvents with a characteristic chloroaromatic odor and the following physical characteristics: Distillation Range, 0 760 mm Hg Flash Point, (TCC) Freezing Point Evaporation Rate (n-BuAc=l .O) Solubility, Q 25% Density, Q 25OC Vapor Pressure, Q 20°C !(eat of Combustion Kauri-Butanol Value
142-159°C 113'F 100.000 ppm (4 hr)
Practically non-toxic (>5g/kg) Practically non-initating Minimally irritating Not a Skin Sensitizer 600 ppm Exposure Guideline' No abnormal effects observed Not a mutagen No signs of sensitization at exposures up to 100,000 pprn In Progress In Progress
' Exposure Guideline ser by the 3M Medical Depanmrnt
3 M HFE.7100 Materials Compatibility Metals
Plastics
Elastomers
Aluminum Copper Carbon Steel 302 Stainless Steel Brass Molybdenum Tantalum Tungsten CuDe Alloy C I72 MEAlloy AZ32B
Acrylic Polyethylene Polypropylene Polycarbonate Polyester EPOXY PMMA PET ABS
Butyl Rubber* Natural Rubber Nitrile Rubber EPDM
Coniprrtihle $et. one h o w esposirre at boiling teniperrttiire. *Brrtyl Rirhber best for estended e.\-posirre > I niortth Exceptions: some swelling of PTFE und Silicone Rtrhher-. Some sirtfcrce oxidation of copper dirritig heot ttp'n,y.
3M HFE-71 DE Hydrofluoroether Azeotrope
in an azeotrope formulation 3M"" HFE-71 DE is a hydrofluoroether, Methyl Nonafluorobutyl Ethers (C,F,OCH,), with trans-l,2-dichloroethylene. This mixture is a true azeotrope, with constant vapor and liquid composition at its boiling point. This fluid is suited to medium duty cleaning and degreasing tasks, as well as specialty solvent applications, and is intended to replace ozone-depleting materials. It has zero ozone depletion potential and other favorable environmental properties. 3M HFE-71 DE has a time-weighted average exposure guideline of 600 ppm for the 3M"" HFE-7100 component, and 200 ppm for trans-l,2-dichloroethylene (8 hr average). The increased solvency and low surface tension, nonflammability and constant composition during boiling of 3M HFE-71 DE make it suitable for immersion and vapor degreasing applications. These properties also may make the azeotrope suitable for certain coating and lubricant deposition applications where increased solvency is required. 3M HFE-71DE Typical Applications Cleaning, Rinsing and Drying Agent Cleaning of oils, greases, waxes Specialty solvent applications For infomiation on other applications, contact your 3M representative or 3M authorized distributor.
(continued1
198
Industrial Solvents Handbook
Table 3.64: (continued)
General Properties Properties
3 M HFE-71DE CFC-113
Formulation Boiling Pt "C Freeze Pt "C Liquid Density' Surface Tension' Kauri-Butanol Value Flash Point Flammability Range I n Air
Azeotrope' 41 -24' 1.37 16.6 27 None None
C,Cl3F, 48 -35 1.56 17.3 31 None None
HCFC-141 b
HCFC-225 ca/cb
HFC-4310
CCl,FCH, 32 -103 1.23 19.3 56 None 7.1- 18.6"
C,CI,HF, 54 -131 1.55 16.2 31 None None
Azeotrope* 39 not avail. 1.41 15.2 NIA None NIA -
Physical Properties
3MT"HFE-7lDE lo0
-
5 >loo
50
Table 5.20: Solubility of Inorganic Materials in DMSO (36) Solubility, Grams/lWcc DMSO 25Y 90-1W'C Aluminum sulfate (18HzO) Aluminum chloride Ammonium borate (3H10) Ammonium carbonate(Hz0) Ammonium chloride Ammonium chromate Ammonium dichromate' Ammonium nitrate Ammonium thiocyanate Barium nitrate Beryllium nitrate(4HzO) Bismuth trichloride Boric acid Bromine Cadmium chloride Cadmium iodide Calcium chloride Calcium dichromate(3HzO)' Calcium nitrate(4HzO) Ceric ammonium nitrate Cobaltous chloride (6HzO)
Insol. Reacts 10 1 Insol. 1 50 80 30 1 10 1 45' Reacts 20b 30 Insol. 50 30 1 30
Cupric acetate(H4) Cupric bromideb
Insol. 1
Cupric chloride(2H20) Cupric sulfate(5H3 Cuprous iodide Ferric ammonium sulfate (12H20)
Insol.
cn
..
m
2
Monohydric Alcohols n-BUTYL ALCOHOL n-Butanol, Butanol-1,
CH3CH2CH2CH20H
Butyric Alcohol
Table 6.74: Physical Properties of n-Butyl Alcohol (37)
PHYSICAL P R O P E R T I E S O F n-BUTYL ALCOHOL Acidity a s a c e t i c acid
0.005% by w t . m a x .
Aldehydes
None
Boiling point a t 760 m m
117.7'C
Chlorides
None
Coefficient of c u b i c a l expansion p e r 'C p e r 'F
0.00093 0.00052
Coloi, Pt-Co
10 m a x .
Critical pressure
48.4 atm
Critical temperature
287'C
D i e l e c t r i c constant a t 25'C
16. I
Distillation range (including 117.7.C)
1.5.C m a x .
E l e c t r i c a l conductivity a t 25.C
9 . 1 2 x 10'' ohms
Explosive l i m i t s in a i r , Lower Upper
1.45% by vol. 1 1 . 2 5 % by vol.
Fire hazard
Moderate
F l a s h point, T a g open cup
115'F
F r e e z i n g point
-89.0.C
H e a t of combustion
8626 cal/g
Heat of fusion
29.9 cal/g
Heat of vaporization a t boiling point
141.3 cal/g
reciprocal
Ignition t e m p e r a t u r e
367'C
Iron
None
MAC
100 ppm i n a i r
Melting point
-09.8.C
Molecular weight
74.12 c a l c u l a t e d
Non-volatile m a t t e r
0 . 0 0 5 g/100 m l , m a x .
Odor
C h a r a c t e r i s t i c , nonresidual
R e f r a c t i v e index a t ZO'C, nD
I . 3992
Relative evaporation r a t e n-butyl a c e t a t e = I
0.45
I
Solubility in w a t e r a t ZO'C
7.8% by wt
Solubility of w a t e r in n-Butanol at ZO'C
2 0 . 1% by wt
Specific g r a v i t y a t ZO/ZO*C
0.8109
Specific heat of liquid a t 2O'C
0.563 cal/g
S u l f u r i c acid t e s t ( P t - C o )
25 m a x .
S u r f a c e tension a t 20'C
2 4 . 6 dynes/cm
Suspended m a t t e r
Substantially f r e e
Toxic ity
Moderately toxic by inhalation, ingestion and skin absorption
Vapor p r e s s u r e a t 20'C 40% 6O'C 75'C 100.8'C
4 . 3 9 mm Hg 18.6 mm Hg 5 9 . 2 m m Hg 1 3 1 . 3 m m Hg 4017.0 mm Hg
V i s c o s i t y a t LO'C
2.948 c e n t i p o i s e s
W a t e r content
0 . 1 0 % by w t , m a x .
Weight p e r gallon a t ZO'C
6 . 7 5 6 Ibs
301
302
..
w
Industrial Solvents Handbook
Monohydric Alcohols
303
Table 6.77: Solubility of Butyl Alcohol in Water at Various Temperatures (79)
Table 6.78: Azeotropes of n-Butyl Alcohol (37) n-BUTYL ALCOHOL FORMS BINARY AZEOTROPES WITH: B . P . of Azeotrope 'C
70
u
B .P.of Azeotrope 'C
87
Acetal
101.0
60
Methyl isovalerate
68.5
1 -Bromo-3 -methylbutane
110.7
70
4 -Methyl - 2 -pentanone
114.4
32.8
Butyl acetate
117.6
50
Octane
110.2
12
Butyl e t h e r
117.3
48
Paraldehyde
115.8
76.4
Butyl f o r m a t e
105.8
I2
u-Pinene
117.4
92.2
Butyl vinyl e t h e r
93.3
29
Pyridine
118.7
Camphene
117.8
21
Styrene
116.5
Chlorobenzene
115.3
Tetrachloroethylene
110.0
Toluene
105.6
o-Xylene p -Xylene
116.8
2 44 88
1 -Chloro-3 -methylbutane
97.0
68 73
90
Cyclohexane
79.8
25
95
Cyclohexene
82.0
32
17.5
Dibutyl e t h e r
117.6 108.5
57
1, 3-Dimethylcyclohexane
72
2, 5-Dimethylhexane
101.9
48
Ethyl borate
113.0
36 37
Ethyl butyrate
115.7
Ethyl carbonate
116.5
83
Ethyl isobutyrate
109.2
82
Heptane
93.3
37.3
Water
97
Hexane
67.0
35.3
Butyl acetate
18.2
2-Hexanone
116.5
2G
3 -Hexanone
117.2
41.8
Water
22
I -1odo- 3 -methylbutane
117.3
31
Loamy1 formate
115.9
29.3
Water
50
Iaobutyl acetate
114.5
27.7
Butyl e t h e r
115.7
n-BUTYL ALCOHOL FORMS TERNARY AZEOTROPES WITH:
k
7.9
B.P. of Azeotrope *C
Butyl chloroacetate
5L
Isobutyl e t h e r
113.5
21.3
Water
46
Isopropyl isobutyrate
115.5
68.7
Butyl formate
55
Isopropyl sulfide
112.0
86
Methylc yclohexane
95.3
Methylc yclopentane
71.8
92
116.3
3. I 85.0
89.1
93. I
91.0
83.6
Water Carbon tetrachloride
64.7
304
Industrial Solvents Handbook
ISOBUTYL ALCOHOL Isobutanol, 2-Methyl Propanol -1,
Isopropyl Carbinol
Table 6.79: Physical Properties of Isobutyl Alcohol (31)
(CH 3 )2CHCH2 O H
Table 6.80: Azeotropes of Isobutyl Alcohol (31)
Alkalinity
0 . 0 0 3 % by w t . max.
Boiling point at 760 m m
107.9.C
Coefficient of cubical '-uxpansion a t 10 to 30'C
0.95
90.7
Benzene
Color, APHA
10 max.
36.4
1 -Bromo-3 -methylbutane
Critical p r e s s u r e
48 a t m
60
Butyl formate
103.0
Critical t e m p e r a t u r e
265'C
37
Chlorobenzene
107.1
Distillation range (including 107.9.C)
78
1-Chloro-3 -methylbutane
Z'C max.
94.5
88
1 , 3-Cyclohexadiene
Electrical conductivity at 25'C
8 x lo-' mho per c m .
79.4
86
Evaporation r a t e (n-Butyl Acetate = 1 . 0 )
Cyclohexane
78.1
0.8
85.8
Cyclohexene
44
1.3-Dlmethylcyclohexane
102.2 105.5
Explosive limits in lower limit
10-3
air,
ISOBUTYL ALCOHOL FORMS BINARY AZEOTROPES WITH:
70
B . P . of Azeotrope 'C 79.9 103.4
80.5
1.68 % by volume
48
Ethyl isobutyrate
F i r e hazard
Mode rate
87
Ethyl propionate
98.9
F l a s h point, Tag open cup
103'F
91
Fluorobenzene
84.0
Heat of combustion
6382 cal/g
73
Heptane
90.8
97.5
Hexane
45
Isobutyl acetate
107.4
79.4
Isobutyl formate
97.8
93.8
Isobutyl vinyl e t h e r
27
Imopropyl sulfide
105.8 101.3
Heat of vaporization at boiling point
138 cal/g/mole
Ignition t e m p e r a t u r e
440'C
Melting point
-108'C
Molecular weight
74. I 2 calculated
Non -volatile m a t t e r
0.001 g/lOo m l , m a .
Refractive index at ZO'C, nD
1.3959
Solubility in water a t 25'C
8 . 8 m l per 100 m l
68.3
82.7
75
Methyl butyrate
68
M ethylc y c lohe xane
95
Mcthylcyclopentane
71.0
10
Methyl iaovalerate
107.5
92.6
Solubility of w a t e r in isobutyl alcohol at 25'C
20.0 m l per 100 m l
Specific gravity a t 20/2o*c
0.8034
4 -Methyl-2 -pentanone
107.9
Specific heat a t 15'C
0.716 cal/g/'C
81
L -Pentanone
101.8
Surface tension at 20.C
2 2 . 8 dynes/cm
80
3-Pentanone
101.7
Toxicity
Highly toxic by inhalation o r ingemtion
68
Pinacolone
105.5
83
Propyl acetate
101 .o
Vapor density ( A i r = 1 . 0 )
2.55
90
Propyl e t h e r
Vapor premaure at 2O.C
8.8 mm
55
Toluene
Vimcoaity at 20.C
6.68 centipoises
73
2.2.4-Trimethylpentane
Water content
0.2% by w i , max.
Weight p e r gallon a t 2O.C
6.68 lbm
9
89.5 101.2
92.0
ISOBUTYL ALCOHOL FORMS TERNARY AZEOTROPES WITH:
30.4
Water
46.5
Isobutyl acetate
33.6
Water
13.3
Isobutyl chloroacetate
17.3
Water
76
Isobutyl formate
86.8
90.2
80.2
Monohydric Alcohols
305
Table 6.81: Relative Evaporation Rates of Various Butyl Alcohols and Acetates (47)
:w -
. 0
< I>
Y
f
/h
-f
10-
1
io
0
1
1
a
io
1
0
1
io
IVAPORAIION
1
1
m
io RATE
1
io
1
r6
1 loo
1
1
r;orio
IN YlNUItS
sec-BUTYL ALCOHOL CH3CHOHCH2CHj
sec-Butanol, Butanol-2, Methyl Ethyl Carbinol
Table 6.83: Azeotropes of sec-Butyl Alcohol (37)
Table 6.82: Physical Properties of secButyl Alcohol (31) Acidity a a acetic acid Boiling point at 760 m m Coefficient of cubical expanaion at 20'C
0.003% by w t . max. 99.5-c
Color, Pt-Co (Hazen) Critical p r e a i u r e Critical temperature Diatilhtion range Fire h i z a r d
IO max.
Flaah Point, Tag open cup Tag cloaed cup Freezing point Heat of vaporization at I atm. Molecular weight Non-volatile m a t t e r Purity Refractive index at ZO'C n o Relative evaporation r a t e , n-Butyl acetate = 100 Solubility in water at 2O.C Solubility of water in, at LO'C Specific gravity at 20/20'c Specific heat at 8.5.C Surface tenaion at 20.C Tdcity Vapor preaaure at 2O.C Viacoaity at 20'C Water, preaence of
Weight per gallon at ZO'C
0 * 00101 'C
46.9 atm 265.19.C 98.0-101 .O*C Dangeroua when expoaed t o heat or name
8O'F 75.F -114.7.C 134.4 g cal/g 74.12 0 . 0 0 2 ml. m u . 99.0% min. 1.39719
#ec -BUTYL ALCOHOL FORMS BINARY AZEOTROPES WITH:
% 61 93 84.6 13.7 32 71 79 46 53 68 62 92 60
41 59
I20
88.5
22.5% by w t
77
60.0% by wt 0.8079 0.596 23.0 dynea/cm Moderate 12.1 m m 3.78 cpa. Miacible without t u r bidity with 19 vol of n-heptane at 20'C 6.73 l b
42
.
16 48 78 45
B.P. of Azeotrope 'C tert-Amyl ethyl ether tert-Amyl methyl ether Benzene mc-Butyl acetate Butyl formate 1-Chloro-3 -methylbutane Cyclohexene 2,s -Dimethylhexane Ethyl propionate Ethyl aulfide Heptane Heune Iiobutyl formate Methyl butyrate Methylc ycloheune Methylc yclopentane Methyl iaobutyrate 3 -Pentanone Pinacolone Propyl acetate Propyl ether Toluene
94.5 86.0 78.6 99.6 98.0 91.5 78.1 93.0 95.7 89.0 89.0 67.2
91.7 97.7 89.9 69.7 92.0 98.0 99.1 96.5 81.0 95.3
306
Industrial Solvents Handbook
tert-BUTYL ALCOHOL tert-Butanol,
2-Methyl Propanol-2
Table 6.84: Physical Propertleo of tertButyl Alcohol (37)
Table 6.85: Azeotropes of tertButyl Alcohol (37)
Acidity a s acetic acid
0.003% by w t . max.
Boiling point at 760 m m
82.36.C
Coefficient of cubical expansion a t 26'C
0.30132.C
63.4
Benzene
74.0
Color, Pt-Co ( H a z e n ) max.
10 m a x .
94
Carbon disulfide
45.7
Compressibility at 2O.C. between 100-500 megabara
79.6 x IO-( megadynea/cm
Critical p r e s s u r e
46 atm
Critical temperature
234.9.c
Dielectric conatant a t 19'C (audio)
I I . 4 cgs unita
Distillation range
81.5-83.0.C
Carbon tetrachloride
29.5
I -Chloro-3 -methylbutane
81.2
61.5
1 , 3 -Cyclohexadiene
73.4
63
Cyclohexane
71.3
60
Cyclohexene
73.2
93
Cyclopentane
48.2
65
Dibromodichloromethane
79.0
94
1 , I -Dichloroethane
57.1
60'F (approx. ) 48'F (approx. )
33
Diisobutyl alcohol
81.5
87
2.3-Dimethylbutane
55.3
25.57.C
10
lI3-Dimethy1cycIohexane
82.2
23
2.5-Dimethylhexane
81.5
75
Ethyl acetate
76.0
38
Ethyl n i t r a t e
78.0
30
Ethyl aulfide
79.8
69
Fluorobenzene
76.0
Heptane
78.0
Hexane
63.7
Isobutyl chloride
65.5
1.65 x 10" Dangerous when exposed t o heat o r flame
Heat of fuaion at 25.5.C Heat of aolution at I 5 * C , of the aolid alcohol in water
6290 cal/g 6302 cal/g 6426 cal/g 2 1 . 8 8 cal/g
Heat of vaporization a t 1 atm.
3.23 k g c a l 130.6 g cal/g
Melting point
25.57.C
Molecular weight
74.12
Molecular volume, 20/VM
94.3 c c
38 78 83 34 74
Non -volatile m a t t e r
0.002 g / l o o m l . max.
70
Purity
99.0% by w t . min.
Refractive index a t 20*C, nD
1.3841
Solubility a t 20.C.
Complete Complete
in water water in Specific heat a t 26'C
B.P. of Azeotrope 'C
76
F i r e hazard
Heat of combustion Liquid at constant volume constant p r e s s u r e Vapor at constant p r e s a u r e
70
41
Dipole moment
F l a s h point, Tag open cup Tag closed cup F r i e z i n g point
t e r t -BUTY L ALCOHOL FORMS BINARY AZEOTROPES WITH:
0.726 g cal/g
Specific gravity at 2 6 / 4 * ~
0.7793
Surface tension at LO'C 34.5.c 80'C
LO. 7 dynes
Toxic it y
Mode r a t e
Vapor p r e a a u r e at 3O.C
57.3 m m
19.45 dynes 14.6 dynes
Viscosity at 30'C
3.316 cpa.
Water
Miacible without turbidity with 19 vol. of n-heptane at 20.C
Weight p e r gallon a t 26'C
6.50 l b
Methylc yclohexane
78.8
Methylc yclopentane
66.6
Methylc yclopentene
69.5
Monohydric Alcohols PRIMARY AMYL ALCOHOL Primary amyl alcohol, a mixture of isomers all of which are primary alcohols, i s composed of approximately 60% pentanol-1 (CH3CH2CH2CH2CH20H); 35% 2-methyl butanol-1 (CH3CH2CH (CH3)CH20H); and 5% 3-methyl butanol -1 (CH3CH (CH3)CH2CH20H).
Table 6.86: Physical Properties of Primary Amyl Alcohol (79) Acidity as acetic acid
0.01% by w t . max.
Boiling point at 760 m m 50 m m 10 m m
133.1.C 68'C 39'C
Carbonyl, a s C, aldehyde
0.20% by wt, max.
Coefficient of expansion at 20.C
0.00092 p e r 'C
Color, R - C o
15, max.
Distillation a t 760 mm Ibp DP F i r e hazard
127.5.C 139.0.C.
max.
Mode rate
F l a s h point (open cup)
118.F
F r e e z i n g point
Sets t o glass below -9O'C
Heat of vaporization at 133.C
242 Btu/lb
P u r i t y , as p r i m a r y amyl alcohols
98.0% by
Refractive index a t 2O.C.
1.4084
nD
wt,
Solubility in water at 20.C
1.7% by wt
Solubility of water in, a t 20.C
9.2% by w t
Specific gravity at 20/20*c
0.81 34
min.
PRIMARY n-AMYL ALCOHOL Table 6.87: Physical Properties of Primary n-Amyl Alcohol (37) Acidity ( m g KOH/g)
0.06 m u .
Boiling point
137.8.C
Clarity
No turbidity or s u s pended m a t t e r
Coefficient of expansion p e r 'C
0.00092
Distillation. initial final
Not below 134.8-C Not above 140.0'C
F i r e point
140.F
F i r e hazard
Moderate
F l a s h point (open cup)
135'F
Heat of vaporization
120.6 cal/g ( c a l culated )
Melting point
-78.5.C
Molecular weight
88.15 (calculated)
Non-volatile m a t t e r a t IOO'C
5.
Refractive index at ZO'C
1.4099
Specific gravity a t 20/2o*c
0.82
o mg/100
rnl, m u .
Specific heat
0.712 cal/g
Toxicity
Highly toxic by inhalation and ingestion
Viscosity at ZS'C 60'C
3.31 cantipoises I . 33 centipoise.
Weight per gallon
6.82 lbs
307
308
0
rr: 4
5 m
G. c)
0
J
m U
u
i f u
..
00
U
W
-
m
0
U Y I.
V
D
V *
U
a V
2
U V
0
a
U
v
a * D
.-P
m m m m m o . . . . . . ?m3 nI-wm.39 -.ucImm
rUr-.uuum
2 x b 5 5 w
C
Industrial Solvents Handbook
3
2
r
0
I 0
al QD r
F
t
*
6
I.
* U m
EJ
0
2
U
U
-
X
i V V
0 0
-
7
M
\ V?
d
0 4
0
0 0
e
x
0
0
m
e u
C
I! M U
v)
v)
00m
9
r-
2-u 2 m c c
P
Monohydric Alcohols sec-n-AMYL ALCOHOL Table 6.90: Physical Properties of sec-n-Amyl Alcohol (31)
Acidity as acetic acid
0.06% max.
Boiling point
115.6.C
Coefficient of expansion p e r 'C Distillation, 95%
0.00149
F i r e hazard
Between 113.6
-
117.6.C
Mode rate 100.F
Flash point Freezing point
Less than r75.C
Heat of vaporization
96.8 cal/g (calculated)
Non -volatile at 1OO.C Refractive index a t 20.C
a . o 0 3 , ~ / 1 0 0c c max.
Specific gravity a t 2O'C
0.82
Toxicity
Highly toxic by inhalation and ingestion
Viscosity at 25.C 60'C Weight per gallon a t ZO'C
4.12 centipoires 1.09 centipoiser.
1.4098
6.81 lbs
Table 6.91: Azeotropes of sec-n-Amyl Alcohol (31)
s e c -n-AMYL ALCOHOL FORMS BINARY AZEOTROPES WITH:
%
B.P. of Azeotrope 'C
97
Cyclohexane
80.0
80
Heptane Methylcyclohexane
96.0 97.4
77
65
4-Methyl-2 -pentanone
115.0
65
Toluene
106.0
309
310
Industrial Solvents Handbook
tert-AMYL ALCOHOL, REFINED (CH3)2COHCH2CH3
2-Methyl Butanol -2, Dimethylethyl Carbinol, Amylene Hydrate, tert-Pentanol
Table 6.92: Physlcal Propertles of Refined tert-Amyl Alcohol (37) Acidity as acetic acid Boiling point Clarity
0.15% max. 101.8.C N o turbidity o r nu. pended m a t t e r
Coefficient of expansion p e r 'C Distillation. 95% between
-
0.001 33 (calculated) 98.8 103.8.C
-
F i r e hazard
Dangerous when exposed to heat or flame
F l a s h point, Open cup Freezing point
70.F
Heat of vaporization Molecular weight Neutralization value, mg KOH/g
93.4 cal/g 88.15 (calculated) 0.06 max.
Non-volatile m a t t e r
0.003 g/lOO c c . m i x .
Odor Refractive index a t 2O.C
Camphor -like
Specific gravity at 20/20*c Specific lieat
0.81
Toxicity Viscosity a t ZS'C at 63'C Water content
Moderate
None
Water tolerance, water p e r 100 c c alcohol Weight p e r gallon
6.75 lbs
-11.9-c
I .4052
- 0.82
0.753 cal/g 3.70 centipoiies 0.99 centipoises
18.0 min.
Table 6.93: Azeotropes of tert-Amyl Alcohol (37) tart-AMYL ALCOHOL FORMS BINARY AZEOTROPES WITH:
z
B . P . of Aaeotrope 'C
85 85
Bcnsene
80.0
1.3-Cycloheudiene
79.1
84
Cyclohexane Cyclohexens
80.8
83 32 50
73.5
1.3 -Dimethylcyclohe xane 2,5-Dimethylhexane
18.5 101.1 97.0 92.2
96
Heptane Heune
60
Methylcyclohe-
95 25
Methylcyclopentane &tMO
101.1
80
Propyl ether
44
Toluene
88.8 100.5
68.3 92.0 71.5
Monohydric Alcohols
31 1
ISOAMYL ALCOHOL 3-Methyl - 1 -Butanol, Primary Isoamyl Alcohol, Isobutyl Carbinol
Table 6.94: Physical Properties of Isoamyl Alcohol (31) Acidity a s acetic acid
0.01% max.
Boiling point a t 760 m m
131.4.C
Coefficient of expansion per *C per O F
0.00090 0.00050
Color, APHA
No. 1 0 m a x .
Critical t e m p e r a t u r e
307'C
Distillation range, below 128.C above 132.C
None None
Dryneaa
A 5 m l . sample is c l e a r l y miscible with a t l e a s t 19 p a r t s of 60 Be'gaaoline a t 60.F
Esters F i r e hazard
(CHS)~CHCH~CH~OH
Table 6.95: Azeotropes of Isoamyl Alcohol (37)
ISOAMYL ALCOHOL FORMS BINARY AZEOTROPES WITH:
%
Not m o r e than 0.060% a s amyl acetate Mode rate
B . P . of Azeotrope 'C
15
Bromobenzene
131.7
82.5
Butyl acetate
125.9
35
Butyl e t h e r
129.8
76
Camphene
130.9
66
Chlorobenzene
124.4
Cumene
131.6
73
1.3-Dimethylcyclohexane
116.6
85
2 . 5 -Dimethylhexane
107.6
42
Ethyl iaovalerate
130.5
93
Heptane
6
97.7
2.6
Isoamyl acetate
129.1
F l a s h point, Open cup
125'F
74.5
Isoamyl formate
123.6
Heat of combustion
794.5 g r a m caloriea per gram
88
Iaoamyl vinyl e t h e r
112.1
78
Isobutyl e t h e r
119.8
Latent heat of vaporization
105.4 g r a m calorie. per gram
28
Iaobutyl propionate
131.2
MAC
100 ppm in a i r
76
Meaityl oxide
129.2
Melting point
- I 17. Z'C
87
Methylcyclohexane
88.15
65
Octane
120.0
Molecular weight
98.2
Non-volatile m a t t e r
0.003% ma;.
78
Paraldehyde
123.5
Odor
Alcoholic , non r e s idual
26
a-Pinene
137.7
47
Propyl iaobutyrate
130.2
21
Propyl aulfide
130.5
-
Refractive index at ZO'C
1.4014
Solubility in water at 14.C
2.0% by
Specific gravity a t Z O / L O * C
0.810
- 0.813
95
2.2.4-Trimethylpentane
Specific heat a t LO'C
0.544 g r a m c a l o r i e s p e r g r a m p e r 'C
48
0-,
wt
m - , o r p-Xylene
Surface. tension a t 2O'C
2 3 . 8 dynes p e r c m
Toxic it y
Highly toxic by ingeation and inhalation
Vapor p r e s s u r e a t 20'C
2.8 m m Hg
44.8
Water
V i a c w i t y ( a b s o l u t e ) a t 23.8.C
3.86 centipoisea
24.0
Isoamyl acetate
Weight p e r gallon at ZO'C
6.76 lbs approx.
46.2
Water
99.0 125-126
ISOAMYL ALCOHOL FORMS TERNARY AZEOTROPES WITH:
%
6.5
B . P . of Azeotrope *C
Iaoamyl chloroacetate
32.4
Water
48
Isoamyl formate
93.6
95.4
89.8
312
Industrial Solvents Handbook
ACTIVE AMYL ALCOHOL Table 6.96: Physical Properties of Active Amyl Alcohol (37) Acidity ( m g KOH p e r g ) Boiling point Coefficient of expansion p e r 'C Dimtillation: 95% 30% F l a s h point, Open cup Freezing point Heat of vaporization Refractive index at ZO'C Re sidue Specific gravity a t Z0/4'C Viscomity a t 20.C 60'C Weight p e r gallon at ZO'C
0.06 max. 128'C 0.00078 Between 1 2 5 131.C min. Above 130.C max.
-
120.F Lems than -7O'C
100.0 cal/g (calculated) I .4097
0.003 g/100 cc 0.816 5.09 centipoiies 1.44 centipoiscs 6.80 lbm
FUSEL OIL, REFINED Refined fusel oil is a volatile, poisonous, oily mixture consisting largely of amyl alcohols.
Table 6.97: Physical Properties of Refined Fusel 011 (37) Acidity as acetic acid Coefficient of expansion i e r I*C
1'F Color. APHA Distillation range (ASTM) below I 1 O'C below 120.C below 130 'C above 135'C Drynesm
0.01% max.
0.00051-0.0006 0.00092- 0.001 1 No. 10 max. None Not m o r e than 1 5 % Not lems than 60% None A 5 m l . sample is clearly miscible with at l e a s t 19 p a r t s of 60' B6 gas oline at 6O'F
-
Evaporation rate at 95'F
%
Minutes 3.5 17.0 36.5 75 64.75 90 90.25 95 103.5 Moderate 5 25 50
F i r e hasard F l a s h point, Open cup Clomed cup specific gravity at ZO/ZO*C Toxicity Water molubility at ZI'C, 100 c c solvent dissolves Weight per gallon d ZO'C
123.F. approx. 106'F. approx. 0.810- 0.81 5
Highly toxic by ingestion and inhalation 9.9 c c w a t e r 6.76 6.77 lb.
-
Monohydric Alcohols
313
METHYLAMYL ALCOHOL Me thy1 lsobuty I Corb in01, 4-Me th yl pentan01-2,
MlBC
(CH-J)~CHCH~CHOHCH~
Methylamyl alcohol i s a secondary alcohol.
Table 6.98: Physical Propertles of Methylamyl Alcohol (37)
Acidity a s acetic acid
0.005% by wt. m i x .
Heat of vaporization a t I a t m .
98.6 g cal/g
MAC
2 5 ppm in a i r
Azeotrope with water: boiling point, 760 m m . * C methyl amyl alcohol, %w
94.3 55.6
Boiling point a t 760 m m
131.63
Coefficient of cubical expanaion at 2 o * c / * c
0.00103
Color, P t - C o s c a l e
10 max.
Refractive index a t ZO'C, nD
1.4081
Critical p r e s s u r e , a t m .
42.4
Solubility in water at 20.C
1.7
Critical temperature
312.C
Diatillation range, 760 m m
130.0
F i r e hazard
-
131.8.C
Molecular weight
102.17
Non-volatile m a t t e r
0.005 g/100 m l m i x .
Odor
Mild and nonreaidual
Purity, minimum
97.5% by wz
- 1.4113
- 1.87ebywt - 6.2% by wt
Solubility of water in, a t ZO'C
5.8
Specific gravity at 20/20*c
0.8079
Moderate
Specific heat at 20.C
0 . 5 2 g cal/g-'C
Flaah point, T a g open cup Tag closed cup
131.F 106.F
Surface teniion at 2O.C
22.8 dynes/cm
Suspended m a t t e r
F r e e z i n g point
Substantially f r e e
-90.C. seta t o a glass below
-
133.0.C
- 0.8080
2-ETHYLBUTYL ALCOHOL Table 6.99: Physical Propertles of 2-Ethylbutyl Alcohol (37) Acidity a s acetic acid
0.02% max.
Solubility in water at LO'C
0.43% by wt
Boiling Boilinn below below below above
147.0.C
Solubility of water in, a t LO'C
4.6% by wt
None Not m o r e than 5% Not leas than 95% None
Specific gravity at 20/20'C
0.8328
Specific heat at 25.C
0.586 cal/g
Surface tenaion a t 28'C
28.05 dynea/cm
point a t 760 m m ranne a t 760 m m 140'C 145.C 155.C
160'C
Coefficient of expansion p e r 'C Dryness at ZO'C
F l a s h point (ASTM open c u p )
0.000892 to 2O.C 0.000921 t o 55'C Miacible with 19 vol. of 60. Be' gasoline 58.C (137.F)
Heat of vaporization, 1 atm.
196 Btu/lb
Molecular weight
102.17
N m -volatile m a t t e r
0.005% max.
Refractive index at ZO'C
1.4229
Vapor p r e s s u r e aL 20.C
1.2 mm
Viscosity a t LO'C
5.63 cps.
Weight p e r gallon at LO'C
6.93 Ibs
314
Industrial Solvents Handbook
n-HEXYL ALCOHOL n-Hexanol, Hexanol-1,
Amyl Carbinol
Table 6.100: Physical Properties of n-Hexyl Alcohol (37) Acidity a s acetic acid
0.01% by wt
Refractive index a t 20.C. nD
1.4181
Boiling point a t 760 m m 50 m m 10 m m
157.1.C 89'C 60'C
Solubility in water at 2O'C
0.58% by wt
Solubility of water i n , at ZO'C
Boiling range at 760 m m
153 t o 160'C
Specific gravity at 20/20*c
7.2% by wt 0.8203 0.8208
Specific heat a t 16.9.C at 13.C
0.544 Cal/gm/'C 0.500 Cal/gm/*C
Color (F't -Co Scale )
15 max.
F i r e hazard
Moderate
F l a s h point (Open cup)
165'F
F r e e z i n g point
-44.6.C
Heat of vaporization at 1 a t m .
213 Btu/lb
Hydroxyl number
530 min.
Iodine number
1 . 2 min.
Mole c ula r weight
102.17
Odor
Mild
Table 6.101: Solubility of Water In n-Hexyl Alcohol (37)
-
Surface tension at 3n.C
23.6 dynes/cm
Suspended m a t t e r
Substantially f r e e
Vapor p r e s s u r e a t 20'C
0.43 m m
Viscosity ( a b s o l u t e ) a t 20.C
5.4 cps
Water content
Miscible without turbidity with 19 vol. of 60' API gaaoline a t 20'C
Weight p e r gallon a t 20.C
6.83 lbs
Table 6.102: Azeotropes of Hexyl Alcohol (37) HEXYL ALCOHOL FORMS BINARY AZEOTROPES WITH: B . P . of Azeotrope ' C
% 63.5
Anisole
151.0
27
Benzyl methyl e t h e r
156.7
52
Camphene
150.8
56
o -Chlorotoluene
153.5
46
p -Chlorotoluene
154.0
65
Cumeme
149.5
53
2,7-Dimethyloctane
152.5
11
Isoamyl e t h e r
157.0
40
Iaoamyl propionate
156.7
60
Isobutyl butyrate
155.0
45
Me8itylene
153.5
19
Phenetole
157.7
60
,?-Pinene
150.8
55
Propylbenrene
152.5
32
P a e udoc m e ne
156.3
77
Styrene
144.0
a5
m -Xylene
138.3
82
o-Xylene
143.6
87
p-Xylene
137.0
Monohydric Alcohols
315
CYCLOHEXYL ALCOHOL Table 6.103: Physical Properties of Cyclohexyl Alcohol (3 1) Boiling point a t 7bO m m
1 6 l . l ' C (322'F)
Boiling range a t 7 b 0 m m , 5.95%
1 56 - 1 6 3.C
Color, A P H A
10 m a y .
C r y s t a l l i z a t i o n point
-1O'C m i n .
Dielectric constant a t 25'C
15.0
E v a p o r a t i o n r a t e a t 45'C (toluene = 100)
8 approx.
F i r e hazard
Moderate
F l a s h point ( C l o s e d c u p ) (Open c u p )
145'F 154.F
F r e e z i n g point
1 8-25.15.C
Heat of c o m b u s t i o n , liquld
8893 c a l / g
Heat of fusion
4.9 c a t / g
Heat of vaporization
108 c a l / g
Ketone a s cyclohexanone
0.5% rnax.
Phenol
0.05% rnax.
R e f r a c t i v e index a t ZO'C
1.4656
Solubility in w a t e r a t 20%
3.6% by wt.
Solubility of w a t e r in a t L O T
20% by wt.
Specific g r a v i t y a t 20/4'C
0.9493
Specific heat a t 15-18'C
0.417 c a l / g m
S u r f a c e tension a t 16.2.C
34.23 dynes/cm
Toxicity
M o d e r a t e by ingestion and inhalation
Vapor density ( a i r = 1.00)
3.45
Vapor p r e s s u r e a t 20 'C 70 80 100 120 140 150 161.1
0.8 mm 15 27 78 187 398 554 760
Viscosity a t 25 'C 39.1.C 65.9'C 90 'C
49.8 20.3 5.8 2.45
Water
0.5% m a x .
Weight p e r gallon a t 20.C (68.F)
7.91 Ibs.
Table 6.104: Azeotropes of Cyclohexyl Alcohol (31) CYCLOHEXY L ALCOHOL FORMS BINARY AZEOTROPES WITH
%
B. P. of A z e o t r o p e 'C
70
Anisole
152.5
38
Benzyl m e t h y l e t h e r
159.0
59
Camphene
151.9
85
Chloroacetal
155.6
62
o-Chlorotoluene
155.5
p-Chlorotoluene
156.5
8
Cineole
160.55
72
Cumene
150.0
28
Cymene
159.5
25
Indene
160.0
22
Isoamyl ether
158.8
37
I s o a m y l propionate
157.7
80
Isobutyl b u t y r a t e
156.0
35
0-P h e l l a n d r e n e
158.0
60
Propylbenzene
153.8
83
Propyl isovalerate
155.1
40
Pseudocumene
158.0
35
@-Terpene
158.3
22
Thymene
95
rn Xylene
159.8 138.9
86
o-Xylene
143.0
45
-
centipoises cps. cps. cps.
316
Industrial Solvents Handbook
HEPTYL ALCOHOL Heptanol-1, Alcohol C-7
C7H 15 0 H
Table 6.105: Physical Properties of Heptyl Alcohol (31) Boiling point a t 765 mm
175'C
Freezing point
-34.6.C
Refractive index a t LOT, n
1.4233
D
Specific gravity at 25/4*C
0.824
Table 6.106: Azeotropes of Heptyl Alcohol (37) HEPTYL ALCOHOL FORMS BINARY AZEOTROPES WITH:
"h
B.P. of Azeotrope 'C
80
Benzyl methyl e t h e r
167.0
90
Camphene
159.3
53
Cymene
172.5
50
Dipentene
171.7
63
lsoamyl e t h e r
170.4
92
Isobutyl isovalerate
171.0
48
p -Methylaniaole
173.0
72
Phenetole
169.0
60
a-Terpinene
169.7
2-HEPTYL ALCOHOL Heptanol-2, Methylamyl Carbinol 2-Heptyl alcohol i s
CH3(CH2)4CHOHCHQ a
secondary alcohol.
Table 6.107: Physical Properties of 2-Heptyl Alcohol (37)
Acidity as acetic acid
0.03% by wt., max. 160.4.C
Boiling point a t 760 rnrn Boiling range a t 760 rnm, below below below above Color (Pt-Co r c a l e )
155% 158% 162'C 165%
None Not m o r e than 5% Not l e a s than 95% None 15, max.
Dryneas a t ZO'C
Miacible with 19 vola. 60' B6 gaaoline
F i r e hazard
Mode r a t e
Flaah point (Open cup)
160.F
Solubility i n water a t ZO'C
0.35% by wt.
Solubility of water in a t 20%
5.80% by wt.
Specific gravity a t Z ~ / Z O * ~
0.8187
Vapor p r e s a u r e a t 2O.C
1.0 rnrn
Weight p e r gallon a t 2O'C
6.81 lbr.
Monohydric Alcohols
31 7
3-HEPTYL ALCOHOL Heptanol-3
CH3CH2CH (OH )C4Hs
Table 6.108: Physical Properties of 3-Heptyl Alcohol (31) Acidity a s acetic acid
0.02% by \ut.
Boiling point a t 760 m m
156.2.C
Boiling range
153- 1S8'C
Color, APHA (Pt-Co s c a l e )
5
F i r e hazard
Mode rate
F l a s h point
140.F
Freezing point
-70.C s e t s to g l a s s below
Specific gravity at zO/ZO*C
0.8224
Vapor p r e s s u r e at 20.C
0.58 m m
Weight per gallon at 20.C
6.84 lbs.
2-ETHYLHEXYL ALCOHOL 2-Ethylhexano1, Octyl Alcohol
Table 6.109: Physical Properties of 2-Ethylhexyl Alcohol (37) Acidity a s acetic acid
O.Ol%, max.
Heat of vaporization, 1 atm.
Aldehydes
None
Molecular weight
Boiling point a t 760 m m
184.8.C
Refractive index a t 20.C.
Boiling range, below 18O'C above 192'C
None None
Solubility in water at 20.C
0.10% by wt
Solubility of water in, a t 20.C Specific gravity a t 20/20.c
0.8339
Coefficient of expansion per ' C Color, APHA
0.000875 t o 20.C 0.000902 t o 55.C 5 max.
167 Btu/lb 130.22
nD
1.4316 2.6% by wt
Specific heat a t 25.C Surface tension at 22'C
0.564 cal/gm/'C 0.2% max.
30.0 dynes/cm
Constant -boiling m i x t u r e , solvent 20% water 80%
b.p. 99.1.C
Unsaturates.
Vapor p r e s s u r e at ZO'C
0.05 m m
F i r e hazard
Slight
Viscosity at 2O.C
9 . 8 cps.
F l a s h point, Open cup
185.F
Weight p e r gallon at 2O'C
6.94 lbs
F r e e z i n g point
-70.C s e t s t o glass below
a8
ethyl hexanol
n-OCTYL ALCOHOL n-Octanol, Octanol-1
Table 6.110: Physlcal Properties of n-Octyl Alcohol (31) Acid number Boiling point a t 760 m m
0.2 max. 195'C (383.F)
Boiling range a t 760 m m
194
Color, dichromate
0.002 m i x .
E s t e r number F i r e hazard F l a s h point (Open cup)
Molecular weight
130.22
Refractive index a t 20'C, "D
1.42920
Solubility in water a t 25'C
0.059 g p e r 100 g water
1 . 3 max. Slight
Specific gravity a t 20/4'C
0.827
Viicosity at 2O.C
8.925 centipoise
195'F
Water
0.25% max.
-
197'C
Freezing point
-15.C (5.F)
Heat of combustion
9690 cal/g
Hydroxyl number
415
Iodine number
1.3 max.
- 440
318
Industrial Solvents Handbook
Table 6.111: Azeotropes of n-Octyl Alcohol (37)
OCTYL ALCOHOL FORMS BINARY AZEOTROPES WITH:
%
B . P . of Azeotrope 'C
80
N, N-Dimethyl-o-toluidine
184.8
88
Indene
182.4
85
Iaoamyl isovalerate
70
Iaobornyl methyl e t h e r
192.6 191.9
80
Iaobutyl carbonate
189.5
92
d -Limonene
177.5
20
Phorone
193.5
90
7-Terpinene
182.5
93
Thyme ne
179.6
sec-OCTYL ALCOHOL Table 6.112: Physical Properties of sec-Octyl Alcohol (37) 85% G r a d e
95% G r a d e
Boiling range f i r r t 5% 90% Denaity, I b i p e r gallon
6.8
6.8
F i r e hazard
Mode r a t e
Slight
174
173 178
- 181.5'C
-- 178'C 18L.S.C
F l a a h point
164'F
185'F
Hydroxyl n u m b e r
376
408
- 388
Melting point
-
414
-38'C
Methyl hexyl ketone content Mole,cular weight Refractive index a t ZO'C Specific gravity a t 2O'C Water content
- 15% I .4244 - 1,4252 0.814 - 0.820 1.0 - 1.2% 10
L e r i than 5%
130.23
130.23 1,4258
- 1.4262
0.818 a t 25.C
0.3
- 0.5%
Table 6.1 13: Azeotropes of sec-Octyl Alcohol (37)
s e c -0CTYL ALCOHOL FORMS BINARY AZEOTROPES WITH:
%
B . P . of Azeotrope 'C
I4
Amyl e t h e r
179.8
50
Butylbenzene
178.2
89 73.5
Butyl irovaleratc
177.4
Cineole
175.9
Cymene
174.0
56 40
Indene
176.0
28 83
Iaoamyl butyrate
180.3
h o a m y l ether
172.7
55 73
d -Limonene
174.5
a-Terpinene
171.8
43
T e rpinolene
179.0
48
Thymene
176.0
Monohydric Alcohols
319
ISOOCTYL ALCOHOL Table 6.1 14: Physical Properties of lsooctyl Alcohol (37)
Acidity a8 acetic acid Carbonyl number Cozfficient of expansion p e r 'C Color (Hazen, P t - C o ) F i r e hasard F l a a h point ( T a g open c u p ) P o u r point Purity
0.001% by wt
0.000814 5 Slight 18O'F -95'F
Refractive index at 2O.C. nD
99.5% by wt 1.4308
Solubility in w a t e r at 25.C a t 50'C
0.06 g/lOOg 0.08 g/lOOg
Solubility of w a t e r in, at 5'C ZO'C 40.C
3.4 g/IOOg 3.8 g/lOOg 4 . 1 g/lOOg
Specific gravity a t zo/2o*c 60/60*F Specific heat, 50 150.C
0.832 0.834
-
Surface tension at 20'C Vapor pressure. *C 'F 50 122 75 167 100 212 125 257 150 302 175 347 180 356 'F Viacosity. 'C 37.8 100
0.10 m g KOH/g
20.0
68
-9.4 -17.8 -31.7
15
o
-25
Water Weight p e r gallon at 60'F
0.79 cal/g/'C
NONYL ALCOHOL Table 6.115: Physical Properties of Nonyl Alcohol (37)
Aldehyde content
0.30% by
Boiling point a t 760 mm
173.3.C
Color, Saybolt Distillation (ASTM), initial
30 193'C 196'C 198'C 201.C Z06'C
5%
50% 95% max.
wt
~
F i r e hazard
Moderate
Flaah point (Open cup) F r e e z i n g point
80.C (176.F)
Heat of vaporization ( L v ) , 100.F 300'F 400 *F Mixed aniline point
-65'C 22,000 Btu/lb mole 19,000 Btu/lb mole 17,400 Btu/lb mole -15'C
Neutralization number Refractive index at LO'C, nD
0.02 m g KOH/g
Solubility in water a t 20.C
0 . 0 6 % by wt
Solubility of w a t e r in, a t 20.C Specific gravity at Z O / ~ O * ~ Vapor p r e s s u r e at 20.C
0.99% by
Viscoaity at 0.C at 20'C
56.0 cpa. 14.3 c p s .
Weight p e r gallon a t ZO'C
6.75 lba
1.4390
0.8121 0.3 m m
wt
29.5 dynca/cm mm 1.95 8.4 30 94 250 600 700 Centistoke8 6.4 12.7 51.3 84.4 224.2 0.02% by wt 6.95 lba, approx.
320
Industrial Solvents Handbook
3,5,5-TRIMETHYLHEXYL ALCOHOL Table 6.1 16: Physical Properties of 3,5,5-Trimethylhexyl Alcohol (37) Boiling point at 10 m m 760 m m
83.C ( 1 8 1 . F ) 194'C ( 3 8 I ' F )
Boiling range at 760 m m , firmt drop 90% dry Color ( APHA)
190'C 194 f 1'C 195.5.C
Flaah point (Open cup)
ZOO'F
Freezing point
Below -7O'C
2 5 max.
Molecular weight
144.25
P u r i t y (by hydroxyl n u m b e r )
97.5% min.
Refractive index at 25'C, nD
1.4300
specific gravity at tSj4.C
0.8236
Viacority at 25'C
11.06 centipoise.
Water content
0 . 1 5 % max.
Weight p e r gallon at 25'C
6.86 l b r
DECYL ALCOHOL Table 6.117: Physical Properties of Decyl Alcohol (37) Oxo Process Acidity
Fatty acid Process
0.0015% by wt.
Acid number
Solubility in water at 20'C Solubility of water in at 20%
0.20%. max.
Boiling point at 760 mm
217.3.C
231'C (448.F)
Boiling range a t 7 6 0 m m
21 9-22 1.5%
90% between 229-233.C
Coefficient of expansion a t 55.C
0.00086
Color. Hazen P t - C o
5
Specific gravity at
2.3% by wt.
~ o / ~ o * c0.837-0.840
Sulfur
Substantially f r e e
Vapor p r e s s u r e . 0.003 m u . , Dichromate
Lese than 0.1%
F i r e hazard F l a a h point (Open cup)
Slight
Slight
225.F
22 0 9 ~
Freezing point
Sets to a g l a a s
6 . P C (44.F)
Heat of combumtion
9963 cal/a
Hydroxyl number
345-365
Iodine number
0.5 max. 158.28 -95'F 99.7%-99.9% by wt.
158J8
P o u r point Purity Refractive index at 20%. nD
1.1388-1.4390
1.43682
*F mrn
"C 75 100 I25 150 175
1.3 max.
below -6o'C
0.829 at 20/4)'C
4 ppm. max.
Suspended m a t t e r
Ester. a s decyl f o r m a t e E a t e r number
Fatty Acid Process
Less than 0 . 0 1 2 by wt.
0.2 max.
Aldehydes. am decanal
Molecular weight
Oxo Process
200
167 212
2.1
257
28.2 82 225
302 347 392
'C
'F
99 20 9.4 -17.8 -31.7 -40.0 -53.9
210
Viacoslty,
-
68 I5 0 -25 -40 -65
8.4
500 Centiatokes 1.76 21 115 209 701 1649 8826
Water content
0.03-0.07%bywt.
Weight per gallon a t ZOC ' 60'F
7.03 Iba. 6.96 Iba. approx.
13.83 centipoimes
0.25%
Monohydric Alcohols
321
ISODECYL ALCOHOL Table 6.1 18: Physical Properties of lsodecyl Alcohol (37) 0.002% by wt., max.
Aridity a s a c e t i c acid Aldehydes, a s dccanal
0 . 0 5 % by wt.. max.
Boiling point at 7 6 0 mm
zzo.1.c
Boiling range a t 760 m m . Ibp DP Coefficient of expansion a t 55'C
Z25'C, max.
Z15'C, min. O.OC083
Color, ( P t - C o s c a l e )
10, m a x .
F i r e hazard F l a s h point (Open c u p )
Slight
F r e e z i n g point
S e t s to a glass below -6O.C
22O.F
Molecular weight
158.29
Odor
C h a r a c t e t i s t i c , non-petroleurn
P u r i t y , a s decanol R e f r a c t i v e index a t ZO'C.
98.5% by wt., min. n
D
1.4408
Solubility i n w a t e r a t ZO'C
L e s s than 0.01% by wt.
Solubility of w a t e r in a t 2O'C
2.4% by wt.
Specific gravity a t 20/20
0.8423
S u l f u r i c acid t e s t ( P t - C o s c a l e )
50, m a x .
Suspended m a t t e r
Substantially Cree
Vapor p r e s s u r e a t 2O'C
Less than 0.01 rnrn
Viscosity a t 20.C
18.9 c p s .
W a t e r content
0 10% by wt.. rnax.
Weight per gallon a t 2O'C
7.01 l b s .
TRIDECYL ALCOHOL Table 6.119: Physical Properties of Tridecyl Alcohol (37) Acidity a a acetic a c i d
0.002% by wt
Carbonyl n u m b e r
0.7 m g KOH/g
C o l o r , Hazen, Pt-Co
5
'C
'F
99 20 9.4 -17.8
210 68 15 0 -25 40 -65
Viscosity,
~
Distillation: initial d r y point
252'C 269'C
Fire hazard
Slight
F l a s h point ( T a g open c u p )
i8O.F
Hydroxyl n u m b e r
278 mg KoH/g
Odor
Characteristic, non-petrolcum
P o u r point
-95'F
Purity R e f r a c t i v e index at ZO'C. nD
99.6% by w t 1.4475
Specific g r a v i t y at 20.C
0.8454
Sulfur Vapor p r e s s u r e ,
'C
'F
90 100 125 150 175 200 225 250
194 212 257 311 347 401 437 491
2 PPrn mm 1.3 2.2 7.6 24 64 155 340 685
-31.7
-40.0 -53.9
-
Centipoiee8 2.61 47.5 382.2 808.3 3,692 11.081
95,433
Water
0.10% by wt.
Weigh4 p e r gallon a t 60'F
7.0 lbs.
322
Industrial Solvents Handbook
OTHER ALCOHOLS AND ALCOHOL BLENDS Table 6.120: ALFOL Alcohol Low Range Blends C6-C,, ~
.
~~
Typical I'roperties Iblal alcclh(l1,WI. '6 Molccular weigh1 distrihution (Io()% alcohol hiisis) c4 C6
~
.-
cx
~
~
100°F
Coefficient of thermal expansion Ib/gal/" F
____
. .. ... . .
610 A l W
610 ADIS X I 0
X__ I 0 lEli
YY.X
99.x
99.6
W.6
4 .X
4.8 54.4 40.1 0.7
9.0 42.1 47.8 0.5
45.1 53.2 0.5
X9.l 0.3
0.5
-
-
-
trace
-
135
I38 0 0.02 0.05 407 30 0.002
145 0 0.02 0.02 387 30 0.003
153 0
010 ~
-
43.2
~
CIO c12 C14 Average alcohol MW Calor, APHA Water, WI. %I Iodine number Hydroxyl number Carbonyl. a% ppin C=O Aciditv. as acetic acid. '6 Acid Heat Color, APHA Specific gravity at O F/" F F l s h point, (PM) O F Melting range. F Boiling range, I: Saponificationnumber Viscosity, cSt 70" F
(40)
~
S1.3
0.7 liiice I40 0 0.03
30 0.002
0 0.03 0.05 415 30 0.002
IO
-
10
0.824 77/77 I75
0.830 60/60 I75
0.829 60160 I67
0.05 40 I
1-5
1-5
0.19 II 6.4
350-460 0.27 II 6.6
35W60 0.19 II 7.1
0.00334
0.00334
0.00334
1-5 S51-459
_____XI0 A I 9Y.X 99.7
0.6
0.1 0.0 10.5 ~. 40.4 .
40.5
141 0
.
0.03 0.02 397
0.02 0.02 367
BO
BO
0.003
0.003
-
-
-
0.831 60/60 I88 3-7 401459 0.4 13.4
0.831
0.831
W60
W(fl
7.4
0.0()3!5
203 200 3-7 3-1 400-460 400-160
-
-
16.3 x.7
1.2
0.00334
0.003 17
13.5
I -
Table 6.121 : ALFOL Alcohol Pure Homologs C,-C,, __
-.___
'Qpical Properties btal alcohol, Wt.% Molecular weight distribution (100% alcohol basis) C6 C8 CIO c12 c14 C16
C18 c20 Average Molecular Weight Color, APHA Water. Wt.% Iodine number Hydroxyl number Carbonyl, as ppm C=O Acidity, as acetic acid, % Specific gravity, at F P F Flash uoinc. (PM) 'F Melting range. 'F
Boiling range, 'F saponificationnumber Viscosity, cSt 70" F 100" F Coeffcient of thermal expansion Ib/gaVF
(40) -~
10 99.8
6
8
99.4
99.9
99.4 0.6 trace trace
trace 99.9 0. I
-
-
-
-
I02 0 0.04 0.05 545 28
I30
0.001
0.8232
60/60 I30 49 3 13-3 I6 4.04
-
0 0.03 0.03 430 12 0.001 0.8293
3.5
60/60 180 1-3 381-385 4.04 10.5 6
0.00376
0.00351
5.5
0.5 99.3 0.2
158 0 0.02 0.05 351
I 0.001 0.8335 a6 i0 235 43-45 448453
4 . 0 4 14.5
9 0.00334
(continued)
Monohydric Alcohols Table 6.121: (continued) __-______ Typical Properties __ Total alcohol, WI % Molecular weight dimbution (100% alcohol haw) C6 C8 CIO c12 C14 Cl6 CI8 c20 Average Molecular Weight Color, APHA Water, WI.% Iodine number Hydroxyl number Carbonyl, as ppm C=O Acidily, as acetic acid, % Specific gravity, a( FI0 F Flah point, (PM) O F Melting range, 'F Boiling range, 'F Saponification number Vimsity, cS1 70" F IOO" F Coefficient of thermal exDansin lb/rdW
__
-
~ _ _ _ _ _ _ _
~
lGNF 99.8
12 99.8
14 998
99 8
-
-
-
-
01 99 6 0.3
trace 04
-
-
-
0.3
trace 0.3 98.7 0.7
trace 0.3 98.7 0.7
-
-
16
323
18 99 6
IRNV
99 6
-
-
0. I 0.3 98.4 0.9 27 1
187
214
242
242
0. I 0.3 98.4 0.9 27 I
5
5
5
5
5
5
0.01 0.05 299 8 0.005 0.83
0.02 0.03 258 29 0.003 0.815 12w120 290 98-1 02 567-573 0.07
0.02 0.18 227
0.02 0.18 227
64
64 0.01 1
0.02 0.33 207 24 I 0.008 0.81 I
-
0.01 I 0.813 125/125 300 118-121 626-631 0.06
-
113-122 626-63I 0.06
0.02 0.33 207 24 I 0.008 0.81 1 140/140 355 132-136 662-670 0.1
-
-
-
15
I20F/18
12OF/I8
160F/I3.5
16OF/I 3.5
0.003 17
0.003 17
0.00317
0.00309
0.00309
99.4
-
-
60/60 265 13-76 490-498 0.04 80F/ I9 12.3 0.00325
Table 6.122: ALFOL Alcohol High Range Blends C,-C,
0.813 125/125
300
140/140
355 131-140 662-670 0.1
(40)
Tv~lrvlPronetlies
lOlZIi.4
lO14CDC
1214
1214CC
1216
1216 CO
Toial Almhol, WI. 4
99.8
99
99.5
99
99
99.7
0.I 0.6 56.5
(race
0.8 68.2
0.3 64.3
0. I 0.4 67.2
42.2 0.6
30.3 0.7
24 11.4
H~rnlalugDistribution. WI. Lx
a
0.6
CIO c12
x7.5 6.X
31 36.6
C14 C16
S
31.2
0.I
C18
urn
25.3 6.8 0.2
c20 c22 C24 C26 C28 C30 Avg. Molecular Wight
Color.APHA Water. Wt. 'A Iodine nunibei Hydroxyl number carbonvl. DITTI C.0
-
164
186
I98
I95
203
198
0 0.02
0 0.05 0.07 302 123
0 0.08 0.05 284 45
0 0.06 0.05 287 21
5
5 0.04 0.08 284 47
0.04 343 31
0.0s 0. I 216 40
Spedfi Gravity "FIO F Flash Point (PM) F Melting Range, F Boiling Rangc. 'F
0.834 7272 137 354 425-525
0.836 7272 250 4145 454-545
0.838 72/72 265 7&75 518-575
0.838 7272 265 70-75 518-575
0.84 72/72 265 63-70 514-592
0.84 12/72 265 63-70
Wseosiiy, CSI
10.4 100
12.5 100
14.3 100
14.3 100
14.5 100
14.5 100
0.03321 0.I clearcolorI s r liquid
0.003 0.1
0.003 16 0. I dearcolorI s r liquid
0.00316 0.18 clear&. lcss liquid
0.00316 0.5
0.00316 0.18 dcarmlorless liquid
Temperature, F
Coeficimt of Thermal Expansion,Ib/gsVF Saponification number Appearance
dear&lsr liuid
c!armlor-
lm liquid
529-590
(continued)
324
Industrial Solvents Handbook
Table 6.122: (continued) Typical Pmpcrtin Told1 A h b l .
Wt.$I
1218DCM
1412
1416GC
1418DDU
1418GM
1618
1618CC
1618GC
20+
99.6
99.7
99.8
99.Y
99.8
99.6
99.6
9R.5
88.5
bre
Homolog Dislribution.WI.9c
-
a
lrscc
bre
CIO
c12
0.5 38.3
0.5 37.7
0. I 6.3
C14 C16 C18
30 19.8 10.8
60.6 I .2
63.4 29.8 0.4
c20 c22
0.6
-
@ace
-
0.1
0.6
tme
trace
39.5 38.7 19.6
66.4 25.6 7
I .3 61
35.7
0.6 31.9 66. I
0.6 66.2 31.4
ISM20
0.4
2
1.4
1.6bcN)
C24 C26 C28 C30 Ave. Molecular Weirlit
214
205
222
Color.APHA Water. Wt. Q Iodine number Hydmxyl number Carhyl. ppm C=O
5 0.06 0.1 I 262 48
5 0.06 0. I 274 48
Specific Gravity OF/' F
0.84 72/72 275 68-73 S25-W
0.839 72/72 270 72-75
0.819
0.835
110/110
525-585
0.822 lWl00 305 95-99 582-638
2% 97-102 598459
15.0
14.4 100
11.5
100
100
14.6 I IO
0.00313 0.18 dear &I-
0.00314 24 wt. % at 24 'C)
Slightly soluble:
Nylon 11 (0.2 wt. %)
* a duPonl "SOIuble" nylon
Table 6.143: Salt Solubillty (wt. %) In Trlfluoroethanol at 25°C (25) Salts Inorganic salts are slightly soluble trifluoroethanol containing 0.2% water. The same salts are bout 2 to 3 times more soluble in the alcohol containing 5% water. This combination of alcohol and water is convenient for conductometric titrations and organic ionic reactions. SOLUBILITY (WT.%) IN TRIFLUOROETHANOL AT 25°C Water Content
LiCl
NaCl
NaF
KI
KBr
CaCI,
0.2%
2.3
0.03
0.007
5.0%
4.2
0.08
0.02
0.9 2.1
0.3 0.6
0.04 0.12
Table 6.144: Solubility of Gases in Trifluoroethanol at 27°C (25) Gases The simple gases have solubilities in trifluoroethanol which are similar to their solubilities in water. SOLUBILITY OF GASES IN TRIFLUOROETHANOL AT 27OC (ml o f qasiml of Iiqiiid)
-
Table 6.145: Vapor Pressure vs. Temperature (25)
Industrial Solvents Handbook
338
Table 6.146: Freezing Point: Trlfluoroethanol-Water (25)
Mol % TrMluoroithanol
Table 6.147: infrared Spectrum (25) CU-' 0
a000
2'
a00
b 00
.IO
20
30 40
so a0
m I O
m 12 0 11".,.
)I.
WAVLLEMGltI LYICROIISI
PI...",.
1H,l HJH-TETRAFLUORO-1 -PROPYL ALCOHOL Table 6.148: Physical Properties of 1H,1H,3H-Tetrafluoro-l -Propyl Alcohol (37) Acid number Boiling point at 760 rnrn Denaity at LO'C Dietillation range at 760 rnrn
0.82 I09 - IlO'C 1.4853 g/ml 90% between 99.5' and 108..5'C
Fluorine content Formula weight
57.5% 132.06
Hydroxyl number
398
Melting point
-15.C
Moisture content
0.40%
Purity
> 95% 1.3197 27.6 dynes/cm
Refractive index at LO'C, nD Surface tension at ZO'C
Monohydric Alcohols
339
1Hll H15H-OCTAFLUORO-1-PENTYL ALCOHOL Table 6.149: Physical Propertles of 1H,l H15H-Octafluoro-1 -Pentyl Alcohol (37) Acid number Boiling point at 760 m m
0.70 140
Density a t ZO'C Distillation range. ASTM. at 760 mm Fluorine content
1,6641 g/ml 90% between 133.0' and 14l.O.C
-
141'C
65.5% 232.08
Formula weight Hydroxyl number Moisture content
224
Purity
> 95%
Refractive index at LO'C, nD Surface tension at LO'C
24.5 dynes/cm
0.08%
1.3190
BENZYL ALCOHOL Table 6.150: Physical Propertles of Benzyl Alcohol (37) Acidity a# benzoic .acid Aldehyde as benzaldehyde Boiling point Chlorine as benzyl chloride Dielectric conatant Distillation range, lbp 5% 90 % 95% Electrical conductivity at ZS'C
F i r e hazard Flash point (Open cup) Freezing point Heat of combuation
Latent heat of evaporation a t 204.25'C
11 1.5 8 gm ral/gm
20 5.3%
Mulecular weight Refractive index a t 2O.C.
108.13 1.5334-1.5397
0.15% m a .
Solubility in water
0.15% mu. 0.50%
mu.
n
D
1 part in 30 parts of water
1.66 195.C min. ZOCC 207.C LlO*C mu. 18 x lo-' recip. chmr.
Slight 213.F
1.044-1.058
Specific gravity at 25/25*c Specific heat at 15-2O.C
0.5402 cal/gm
Surface tension (c. g. a. unit.)
39.71 Slight
Toxicity Vapor presaure a t 30% Viacoaity at 20.C Weight per gallon at L O T
0.100 mm 0.05582 cp..
9.78 lbs.
-15.3.C 893 kg cal/mole
Table 6.151: VELSICOL Benzyl Alcohol (59) Benzyl Alcohol, Reagent Grade Benzyl Alcohol is a clear, colorless liquid with a mild, pleasant aromatic odor. It is a primary alcohol with reactive methylene and nuclear hydrogen. The reagent grade is a high purity material with analytical utility.
SPECIFICATIONS Assay, (G.C.), % minimum Solubility, in 25 ml water at 25T, g Benzaldehyde content (U.V. determination), 7% maximum Halogen (Beilstein Test) TYPICAL PROPERTIES Boiling Point, 5 mm Hg, ,'F/ 500 130(54) 7.67(.92)
Outstanding Characteristics Clear, pale color; piney odor; high solvent activity; excellent wetting, penetrating, and dispersing properties; high bactericidal activity when properly formulated; uniform.
(continued)
352
Industrial Solvents Handbook
Table 6.173: Hercules TERPINEOL (28)
TERPINEOL^^ 101
Natural Tertiary Terpene Alcohol TERPINEOLTM 101 is a natural, high-purity grade of the tertiary terpene alcohol alpha-terpineol. Derived by fractional distillation of oils extracted from pinewood, it is a water-white, oily liquid at normal temperatures with an odor suggestive of lilacs. Its chemical nature, pleasant floral odor, and surface-active properties account for its usefulness to the essential41 industry and to manufacturers of disinfectants, household and industrial soaps, detergents, cleaners, and other chemical specialties. General Sales Specifications H e r c v l n T n Mohalrucsr.d.blo
m rqu9YIy
Specific gravity at 15.6/15.6'C,min Tertiary alcohols, min, % Moisture, max, % Color, Hazen (APHA), max Appearance
0.935 94 0.6 70 EFFM'"
(a) Essesenlially Free of Foreign Mallei
Typical Properties Specific gravity at 15.6/15.6"C Tertiary alcohols, % Moisture, % Distillation range, "C(7)
0.9410 96 0.2 219 (426) 220 (428) 20 90 (194) -sE
m c)
0
cn
m
.-CIn E u?
P
%E 0-v)-
-
0
m 01 Y
Monohydric Alcohols
355
Table 6.175: Melting Points of Saturated Monohydric Alcohols (69) 120
74.0
Ti IO
3
M
*
.d
0)
u
g
20
al
-; M
W
5
-30
3
0
B
-80
-130
22
CHAIN LENGTH IN CARBONS
Table 6.176: Rate of Evaporatlon of Various Solvents at Room Temperature (19)
Table 6.177: Comparative Evaporation, Rates of Alcohols (79) (Relative Values on 5 cc Samples a t 21 "C. and
734.4 mm. Hg)
0 w I00 I-
(=sr( OH OH
HO
Glycol (a dihydroxyether ?)
Cia HIOOs
Z(2.3 -Dihydroxy-
13
129
115
103-105
---
1
195
1
HO HO'
---
n-propyl) -2hydroxy camphane
B. Tetrahydric Alcohols
6
cycloHexane-l,2, 4.5-tetrol
+ z J HO
6
8
10
-
M o H e x a n e 1.2, 4.5-tetrol
A dimethylether
of a n inositol
trans( ?)-pMenthane-l,2,6.8-
---
!OH
" o b ; OH ?
242
230
156
tetrol
(continued)
Polyhydric Alcohols Table 7.227: (continued)
Hydrate
Alcohol iiuniher of c .Atoms
10
Slwletdl Structural Formula
S:inie
p-Menthdne-1,2, 4.b-tetrol
M.p. ("C)
cmH
HO
149
100
1
1JO
___
1
I 4 1 - I 45
2
ti0
10
38
-p-&lenthane- 1,2, J,J-tetrol
cQd
HO HO
OH
2,2'-Dihydroq ti.G'-his ( g hydroxybenzhydry1)-diphenyl
308 I
OH
1
OH
C . Pentahydric Alcohols OH
G
Viburnitol (cyclohexane2,3,5/4,G-pentol)
6
Inositol hromohydrin
170-5
6
Inositol chlorohydrin
180-5
6
Scyllitol chlorohydrin
___
7
1-Metnylenecyclohexane-2.4, 6/3,5 -pent01
205
181
1
2
D. Hexahydric Alcohols G
(+)-Sorbitol
HOHzC (CHOH), CHzOH
111
._ mesa-Inositol 6
(1,2,3,5/4,6cyclohexanehexol)
225
55 15
___
1
0.5
2
OH
dV
andl-Inositols (active). .(1.3.4/2. - . . 5,s-cyclohexanehexol)
248
&H ; i
6H
'
bH
2
453
Phenols
Table 8.1: Phenol (2)
Carbolic Acid
C6H50H PHYSICAL P R O P E R T I E S O F PHENOL
Boiling point
181.6.C
Distillation r a n g e
95% d i s t i l l s within a r a n g e of 1 . 5 ' C
F l a s h point (Open c u p )
175'F
F r e e z i n g point
Not l e s s t h a n 40.C
MAC
5 ppm in a i r
Odor
Characteristic
Purity
98'10, m i n .
Solidifying point
Not l e s s than 40.7'C
Solubility in w a t e r , above 68'C at 20.C Specific gravity a t 41/4'C
In a l l proportions 8.3%
Toxicity
Highly toxic
1.058
P H E N O L FORMS BINARY AZEOTROPES WITH B.P. of Azeotrope OC.
%
B.P. of Azeotrope "C.
%
92.2
Acetophenone
202.0
28
Heptyl alcohol
185.0
22
Amyl ether
180.2
55
Indene
173.2
58
Aniline
186.2
Isoamyl ether
172.2
49 55
Benzaldehyde
185.5
85 74
Isobutyl c a r b o n a t e
192.5
Benzylamine
196.8
17
Isopropyl l a c t a t e
184.8
57
m B romotoluene
175.7
79
Mesitylene
163.5
60
o Bromotoluene
174.4
20
2 - Methylcyclohexanol
183.1
37
2-Butoxyethanol
186.4
77
Methyl f u m a r a t e
194.9
54
Butylbenzene
175.0
33
Methylheptenone
184.6
30
Butyl i s o v a l e r a t e
184.0
32
2 -0ctanone
184.5
78
Camphene
156.1
87
n-Octyl alcohol
195.4
97
o-Chlorotoluene
159.0
50
s e c - O c t y l alcohol
184.5
28
Cineole
182.9
65
a-Phellandrene
lb5.0
13 28
Cyclohexanol Cyclohexanone
183.0 184.5
82
Phorone
198.8
29
65
Decane
168.0
81
Pinacol a-Pinene
185.5 152.8
59 75
E t h y l oxalate
189.5
75
Psrudocumene
166.0
Fenchone
196.2
55
Terpinene
171.5
60
Glycol d i a c e t a t e
189.9
60
Thymene
172.3
-
-
454
Aldehydes FURFURAL CH-CH II
Furfuraldehyde Furol Pyromuc ic Aldehyde
II
cy O/C-CH=o
Table 9.1: Properties of Pure Furfural (46) Furfural(2-furaldehyde),C,H,OCHO, is a liquid aldehyde with a pungent almond-like odor Colorless when freshly distilled, it darkens on contact with air Industrial furfural is light yellow to brown in color
General Molecular weight Boiling point (at 760 mm),"C ("F) Freezing point, "C ("F) Refractive index (n 1.0) at 20" C (68" F) at 25" C ( 7 7 F) Density (d t/4) at 20" C (68" F) at 25" C (7P F) Vapor pressure Vapor density (air= 1)
96.08 161.7 (323.06) -36.5 (-33.7) 1.5261 1.5235 1.1598 1.1545 See Table 9.7
3.3
Thermodynamic properties Heat of vaporization, AHVg cal/g mole Specific heat (liquid), cal/g/deg 14 to 8 6 C (57.2to 176" F) 20 to 100"C (68to212" F) Thermal conductivity, Btu/(hr)(ft2) ("Flft) at 100"F cal/(sec) (cmz) ("Ckm) at 38" C Heat of combustion (liquid), A Hm.2 kcal/mole
11,614.6 0.401 0.416 0.1525 6.3 x 10-4 -560.3
Fluid properties Viscosity, cps, at 0" C (32"F) at 25" C (77 F) at 38" C (100.4" F) at 54" C (129.2"F) at 9 9 C (210.2"F) Surface tension, dynes/cm at 0" C (32" F) at 29.9' C (85.9 F) at 30.0"C,(86" F) Vapor diffusion coefficient, cm*/sec at 1P C (62.6"F) at 25" C (7P F) at 50" C (122" F)
455
2.48 1.49 1.35 1.09 0.68 43.5 40.7 41.1 0.076 0.087 0.107
(co ntinued)
456
Industrial Solvents Handbook
Table 9.1 : (continued)
Electrical properties Dielectric constant at 1" C (33.8"F) at 20" C (68"F) at 25"C (77"F) at 50" C (122"F) Specific conductivity, mho Minimum Maximum
46.9 41.9 38 34.9 0.26x 10-5 0.37x 10-5
Other properties Critical pre'ssure, psia kg/cm* Critical temperature, " C (" F) Molar volume, 25"C, ml/mole Molecular association Solubility in water, wt % at 20" C (68"F) alcohol ether
798 56.1 397 746.6) 83.19 1.11 8.3 m OD
Note Furfural is miscible with most common organic solvents except saturated aliphatic hydrocarbons
Flammability properties Explosive limits (% by vol ) 2.1 Lower limit (at 125"C [25P Fl and 740 mm Hg) Flash point 61.7(143) Tagclosed cup, "C (OF) 61 .7(143) Pensky-Martens, "C ("F) (Based on flash point, furfural is classified as Class Ill A * ) 393 (739) Ignition temperature, "C ("F)
Note: Furfural has a high order of thermal stability in the absence of oxygen. At temperatures as high as 230" C (446"F), exposure for many hours is required to produce detectable changes in the physical properties of furfural, with the exception of color (29). 'Refers to Code of Federal Reguiatlons, 29CFR 1910 106
Table 9.2: Typical Properties and Specifications of Furfural (2) Acidity, an acetic Boiling point Density at 60°F 1000 1500 175' 2x30 250'
3000 Distillation range (Engler) 1%, 'F (min.) End point, "F (max.) Recovery, yo (min.) Residue, yo (max.) Loss, % (max.) Explosive limit,^ lower Flash Point (Cleveland Open Cup) Freezing point Heat of Vaporization Purity
Technical 0.3% Refined 0.1% 158-162OC 1.164 1.140 1.110 1.095 1.080 1.049 1.019
300 335 98.5 0.9 0.9 2.1% at 257'F 131-5'F -34'F 107.51 cal./g 98.5% Technical 99.0-99.5% Refined
Refractive index at 6 8 7 Solubility in water at 2o'C Specific gravity at ZO/ZO'C Surface tenaion Vapor pressure at 60'F 1000 150' 175' 200' 250'
300" 350' 40000' 450'
Viscosity at l00'F 130' 210' Weight per gallon (P'C)
1.5261 8.3% 1.161 1.158-1.160Technical 1.59-1.161Refined 49 dynes/cm. 0,035Iba./aq. in. aba. 0.la Ibs./sq. in. abs. 0.540 Iba./aq. in. abs. 0.950 1bs.le.q. in. abs. 1.650Ibs./aq. in. abs. 4.40Ibs./sq. in. abs. 11.50 Ibs./sq. in. abs. 22.50 Ibs./sq. in. abs. 43.5Ibs./aq. in. a b . 77.0 Ibs./aq. in. abs. 1.35 centipoisea 1.09 centipoisea 0.68 centipoise8 9 Ibi.
Aldehydes
457
Table 9.3: Solubility of Various Substances in Furfural (46) Acetone Acids: Abietic (technical) Acetc Benzoic Butyric (technical) Cinnamic Citric Formic Lactic Maleic Naphthenic acids (practical) Oieic (U S P ) Oxalic Oxalic (anhydrous) Palmitic (technical) Phthalic Promonic (technical) Sali'cylic . Sebacic (mp 132-133°C [269.6-271.4"R) Stearic (U.S.P.) Succinic Tartaric Alcohols: Amyl n-Butyl Ethylene glycol Glycerol
S 9.4 S 14.8
S 4.1 3.6 S S R S S 4.8 3.6 1.6 17.6
S
11.0
0.8 2.1 3.0 10.9 M S S 2 .l-2.e
Isobutyl n-Octyl Amyl acetate Benzene Butyl acetate Carbon tetrachloride Castor oil Chinawood oil Chloroform Diethylene glycol monobutyl ether Diethylene glycol monoethylether Diethyl phthalate Ethyl acetate Ethylene glycol Ethylene glycol monobutyl ether Ethylene glycol monoethylether Ferric chloride Ferric chloride hexahydrate Hydrogen cyanide Linseed oil Nitrobenzene Nitrotoluene Paraldehyde Pyridine Quinoline Toluene Xylol Zinc chloride
S S M
S
M
S
M M
S
M M M
S S M M 0.55 20.0
M
M M M M
S
S S
M
20.6
S-infinitely soluble M=miscible in equal volume at room temperature R- reaction
Table 9.4: Solubility of Selected Thermoplastic Resins In Furfural (46) (At 23°C [73 4" Fl) RESIN TYPE
MANUFACTURER
SOLVENT ACTION
Nitrocellulose Ethylcellulose Cellulose acetate butyrate Polyvinyl butyral
Hercules (RS) Hercules (N-50) Eastman
vs vs vs
Vinyl acetate Vinyl acetate chloride PVC
Union Carbide (BakeliteQ) Union Carbide (BakeliteQ) Union Carbide (BakeliteQ) Uniroyal (Marvinol" VR-10)
S;VSH
S=Soluble from 1 g to 10 g per 100 g solvent VS-Soluble 10 g or more per 100 g solvent H=Temperature, 70-75°C (158-167 F); time one hour B =Cloudy 1=Less than 1 g per 100 g solvent
RESIN TYPE
YANUFACTURER
PVC
Goodrich (GeonQ 222) Du Pont (ZyteP 31) Du Pont (Elvamide) Du Pont (Alathon") Du Pont (LuciteB 140) Du Pont (Lucitee 130) DOW(PS-3)
Nylon Nylon Polyethylene Acrylic Acrylic Polystyrene
SOLVENT ACTION
458
Industrial Solvents Handbook
Table 9.5: Specific Gravity and Pounds per Gallon of Furfural (46) (Change per"C.Sp. Gr -0 00110,Ibs /gal -0 00917) SP.OR?
TEMPERATURE 'C *F
122 0 118 4 114 8 111 2 107 6 104 0 100 4 96 8 93 2 89 6 86 0 82 4 78 8 75 2 71.6 68.0 64 4 60.8
50 48 46 44 42 40 38 36 34 32 30 28 26 24 22 20 18 16
LBS /GAL.
9 403 9 421 9 440 9 458 9 476 9 494 9 502 9 531 9 549 9.568 9 586 9 604 9 623 9 631 9 660 9 678 9 696 9.715
1.127 1.129 1.131 1.134 1.136 1.138 1.140 1.142 1.145 1.147 1.149 1.151 1.153 1.156 1.158 1.160 1.162 1.164
SP.OR.'
TEMPERATURE 'C 'F
57.2 53.6 50.0 46.4 42.8 39.2 35.6 32.0 28.4 24.8 21.2 17.6 14.0 10.4 6.8 3.2 -1.6 -4.0
14 12 10 8 6 4 2 0 -2 -4 -6 -8 -10 -12 -14 -16 -18 -20
LBSJQAL.
1.167 1.169 1.171 1.173 1.175 1.178 1.180 1.182 1.184 1.186 1.189 1.191 1.193 1.195 1.197 1.200 1.202 1.204
9.733 9.752 9.770 9.788 9.807 9.825 9.833 9.861 9.879 9.898 9.916 9.935 9.953 9.971 9.990 10.008 10.027 10.045
'Referred to water at 4OC.
Table 9.6: Composltion/Density of Furfural-Water Solutions' (46)
DENSITVFURFURAL
fi BY WEIGHTI
0 0.2 0.4 0.6 0.8 1 .o
1.2 1.4 1.6 1.8 2.0 2.2 2.4 2.6 2.8 3.0 3.2 3.4 3.6 3.8 4.0 4.2 4.4
to
DENSITV-
4
2c c
0.9982 0.9986 0.9990 0.9993 0.9997 1.0001 1.0005 1.0008 1.0012 1.0016 1.0020 1.0023 1.0027 1.0031 1.0034 1.0038 1.0042 1.0046 1.0049 1.0053 1.0057 1.0060 1 .om
2sc 0.9971 0.9974 0 9978 0.9982 0.9985 0.9989 0.9993 0.9996 1 .oooo
1.0003 1.0007 1.0011 1.0014 1.0018 1.0022 1.0025 1 .0029 1.0033 1 .OC36 1.0040 1.0044 1.0047 1.0051
'Mains, G.H., Chem. & Met. Eng., 26,779 (1922). $Saturated solutjon of furfural in water at 20°C (68°F). Saturated solution of furfural in water at 250C (77OF).
FURFURAL (%BY WEIGHTI
4.6 4.8 5.0 5.2 5.4 5.6 5.8 6.0 6.2 6.4 6.6 6.8 7.0 7.2 7.4 7.6 7.8 8.0 8.2 8.32 8.4 8.65
to
4
20-c
1.0068 1.0072 1.0075 1.0079 1.0083 1.0086 1 .ow0 1 .OW4 1 .OW8 1.0101 1.0105 1.0109 1.0113 1.0116 1.0120 1.0124 1.0127 1.0131 1.0135 1.0137
-
2sc 1 .0054 1.0058 1.0062 1.0065 1.0069 1 .w73 1.0076 1 .0080 1.0084 1 BO87 1 .m1 1.0094 1 .0098 1.0102 1.0105 1.0109 1.0113 1.0116 1.0120 1.0122 1.0124 1.0127
0
c
..
2
Aldehydes
459
460 I
-e a a
r L
0)
U
I
E
5 E a
L
I
I
-n P
-E
gs
W
JP
U2!
I
Lo
aal
O L
.. 3
p i 0
c
..
2
Industrial Solvents Handbook
I (3
Aldehydes Table 9.1 1: Vapor-Liquid Composition of Furfural-Water System (46)
I I I I 02 Oh 06 0.8 MOLE FRACTION FURFURAL IN LlOUlD
1.o
OTHER ALDEHYDES Table 9.12: Vapor Pressures of Various Aldehydes (79)
B
C I
C METHACROLEIN
*IO -10
-60
-50
-40 -30 -20 O-10
0
IO 20 30 40
TEMPERATURE, *C.
60
80 X
461
462
0
v-
Industrial Solvents Handbook
P
I ' 0
0 0
v Y
Ethers Table 10.1: Dimethyl Ether (34)
C H3-0-C
Methyl Ether
H3
Physical Properities Molecular wight (calc.) . . . . . . . . 46.07 Boiling point at 760 mni . . . . . . . . -24.Y'C Vapor pressure at 20'C. . . . . . . . . 5.24 atm Freezing point . . . . . . . . . . . . - I4l.S'C Density at 20'C. . . . . . . . . . . . 0.661 g/ml Vapor density (air = 1.0). . . . . . . . I .59 Critical pressure . . . . . . . . . . . . 52.5 atm temperature . . . . . . . . . . I28.8.C density . . . . . . . . . . . .0.2714 g/ml Hcat of combustion. gas . . . . . . . . 347.6 kcal/niolc Hcit of formation, gas . . . . . . . . . -44.3 kcil/molc Heat of melting . . . . . . . . . . . . 25.621 call6 Hcat of vaporization at -24.8'C . . . . I I I .64 caI/g Flee energy of formation. 25'C . . . . . -27.3 kcal/molc Entropy at 25'C. . . . . . . . . . . . 63.72 cal/'C-molc Spccific heat ill -27.68"C . . . . . . . 0.5151 caI/g Surfacc tension. liquid-vapor intcrfacc, at -4O'C. . . . . . . . . . . . . .21 dyncr/cm -20 . . . . . . . . . . . . .. I 8 -10
101 . . . 825 . . . . . . . . . 855 Diclcctric constant at 25'C . . . . . 5.02 E.S.U. Flash point, Tag closed cup. . . . . -42°F
Viscosity of gas at O'C, q x
a
Autoignition temperature. . . . . . Explosive limits, "/. by vol. in air . . Solubility' in water at 24'C . . . . . Solubilit of water in methyl ether
..
............
at24&
662'F 3.45-26.7% 35.3% by wt. 7.0% by wt.
Solubility in gasoline (unleaded) at -4O'C. . . . . . . . .
. . . . . 647; by wt. ............ 19 ............ 7
0
25
Solubility at 25°C in: carbon tclrschloridc at 782 mm wctonc.
..... .....
benzene chlorobenzene. nuthyl acctate. . At about 5 atni.
.. .
762 761 795 704
. . . .
. . . .
. . 16.13 molt . . 11.81 . . 15.29 . . 18.55
....
I I . I7
. . . . . . . . . . . . . . 16
SOME PHYSICAL. AND THERMODYNAMIC PROPERTIES OF DIMETHYL ETHER AT VARIOUS TEMPERATURES Temperature OC
-- 3400 -20
- 10 0 10 20 30 40 50
60 70 80 90
100 110 120
Density
Vapor atrn.
0.392 0.741 1.35 1.97 2.80 3.86 5.24 7.00 9.06 11.6 14.7 18.4 22.7 27.4 33.0 39.5 46.6
I
vapor g/ml
-
0.7174 .7040 .6905 .6759 .6610 .6455 .6292 .6116 .5932 .5735 .5517 .5257 .4950 .4575 .4040
g/d
-
0.0027 .0039 .0055 .0076 .0104 ,0142 .0188 .0241 .0306 .Om5 .OW
.0623 .om0 ,1060 .1465
Dielectric :onatant
-
5.15 4.90 4.67 4.41 4.18 3.93 3.70 3.48 3.25 3.00
-
Heat of vaponzation kcal/kg
kcal/kg
3 / Y g
116.13 113.17 110.12 106.95 103.64 100.17 96.44 92.64 88.48
77.58 83.08 88.64 94.23 100.00 105.79 111.75 117.60 123.63
193.71 196.26 198.76 201.23 203.64 205.96 208.19 210.24 212.11
-
-
463
Enthalpy ..
Entropy
liquid
-
-
-
-
-
-
-
0.9342 0.9568 0.9787 1.0000 1.0206 1.0410 1.0604 1.0795
-
-
1.3996 1.3918 1.3851 1.3791 1.3744 1.3700 1.3660 1.3620
-
I
464
Industrial Solvents Handbook
Table 10.1: (continued) Binary Azeotropes Containing Dimethyl Ether
Some Properties of (CH3)20.BF3
.
Molecular weight (calc.) . Meltingpoint . . . . . B o i i g point. . . . . . Density at 20°C . . . . Vapor pressure at 30°C . at 70°C . Surface tension at 20.5% Diseociation constant . .
113.89 -12OC 128°C 1.241 g/ml 6.1 torr . 52.7torr . 33.03 dynes/. log K = (-2983)/ T 7.228
Component A
. . . .
Azeotrope Boiling Compopoint, nent A, "C Ytbywt
Boron trifluoride . . . . Hydrogen chloride . . . . Ammonia at 1 atm. . . . at 11 atm . . . Sulfur dioxide at 1 atm . at 56.1 atm at 77.1 atm at 108.7 atm Dichlorodifluoromethane at 3 atm . . . . . . .
+
. . . . . . . . . .
.
,
. . . .
127 -2 -37 25 0 6.6 12.1 26.7
. .
0
Suhibilily of Mclliyl Elhcr at Various Prcsrurcr Tcmperatu~= 25°C C';nhon lclrscbluridc
I
hlcthyl cthcr. Mole 7;
1
p,""" 112.4 127.6 ?W.I M.II 612.X
782.4 '122.7 1072.Y
0.ooo
I
Acrtonc p.nini
23.2
3.0
311.1
5.96 8.52 12.17 lh.31 IY.Y3
4113.1
-. '1 ..10
1075.0
54x.1
w.x
762.3 'JJ9.I
Methyl clhcr. Mole X 0.0 1.79 2.78 7.01 Y.23 I I.RJ 15.77 18.YS
I
knzcne
p.mn
I
Clilurolwnicnc
1
Mok 7:
2.30 372.6
503.0 634.11 761.4
913.0 1006.7
6.32 '1.32 12.2~ l5.?9 18.R4
0.0 1.75 5.0R 8.17 11.17
120.4 Jl(1.S
423.3
13.16
16.27 19.50
21.00
Table 10.2: Chlorodlmethyl Ether (2) C H3-O-CH2CI Chlorodimethyl ether i s a colorless liquid which decomposes in water and in hot ethyl alcohol. It i s soluble in acetone, carbon disulfide and concentrated hydrochloric acid. Physical Properties Boiling Point (760 mm. Hg), "C.
59
Dipole Moment In Carbon Tetrachloride D
1.88
In Benzene D
1.82
- 1.85
Melting Point, "C.
-103.5
Molecular Weight
80.52
Purity
90% min.
20 Refractive Index n D 20 Specific Gravity D 4
Methyl dcc'eliilc Methyl ether. Mole ' !:
Methyl ether,
1.39737 1.0703
60 38 42.5 56 65 60 60 60 90
Ethers Table 10.3: Chloromethyl Ethyl Ether (2) CICH2-0-CH2-C
H3
This ether i s a colorless liquid which i s an irritant to the mucous membranes. It i s used as a raw material in organic syntheses. Physical Properties Assay (chlorine)
App. 98%
Boiling Range, 760 mm. Hg, "C.
79
20 Density D 4 20 Refractive Index n D
- 83 1.03 - 1.05 1.40 - 1.41
Table 10.4: Ethyl Ether (7)(79)(23)(49) Ether Ethyl oxide Sulfuric ether Typical Properties and Specifications Apparent ignition temperature i n air
190°C.
Boiling point at 760 mm.
34.5"C.
Coefficient of expansion
0.00164 per 1°C.
Constant-boiling mixtures ("h by wt.) Ethyl ether 99% Carbon disulfide 1 .O% Ethyl ether 44.5% Methyl formate 55.5% Ethyl ether 98.9% Water 1 .l%
B.P. at 760 mm. 34.5"C. B.P. at 760 mm. 28.2"C. B.P. at 760 mm. 34.1"C.
Electrical conductivity at 25°C.
4x
Explosive l i m i t s
2.34
Flash point
-40°F.
Freezing point
-116.2"C.
Heat o f combustion
651 Cal ./mol
Heat o f vaporization
83.96 cal./g at B.P.
Refractive index at 17°C.
1.3542
Specific gravity a t 20/20°C.
0.7146
Specific heat at 30°C.
0.5476 cal ./g
.
Surface tension at 20°C.
17 .O dynes/sq
. cm .
Solubility in water a t 20°C.
6.9% by w t .
Solubility o f water in solvent at 20°C.
1.3% by wt.
Viscosity at 20°C.
0.00233 poise
Vapor pressure at 20°C.
442.0 mm. Hg
Weight per gallon at 20°C.
5.95 Ibs.
Weight per gallon a t 17°C.
5.3542 Ibs.
Acidity (as acetic)
0.002% by wt
recip. ohm
- 6.190
., max.
465
466
Industrial Solvents Handbook
Table 10.5: Flammability of Ethyl Ether-Oxygen-Helium Mixture (7) 100
90
80
70 I-
$ 60 0 (r
w
n
i
50
(3
50 40 30 20,
10
0
20
10
30 40 50 60 ETHYL ETHER, PERCENT
70
80
90
Table 10.6: Dichloroethyl Ether (2) 2,2'-Dichlorethyl Ether B,fi'-Dichlorodiethyl Ether
Acidity (as hydrochloric) Apparent ignition temperature in air Boiling point a t 760 mm. Boiling range at 760 mm. Coefficient o f expansion at 20°C. Coefficient o f expansion at 55°C. Constant boiling mixture (% by wt.) Dichlorethyl ether Water B.P. at 760 mm. Flash Point (ASTM, open cup) Flash Point (ASTM, closed cup)
CI-CH2-CH2-0-C
.
0.005% by w t max. 396°C. 178 .5"C. 170-180°C. 0.00097 (per "C .) 0.00100 (per "C.) 34.4 65.6 97.7"C. 79°C. 55°C.
H2-CH2-C
Heat of vaporization at 178°C. Refractive index at 20°C. Specific grovity at 20/20°C. Specific heat (at 20-30°C .) Surface tension at 25°C. Solubility in water at 20°C. Solubility of water in dichlorethyl ether at 20°C. Viscosity at 25°C. Vapor pressure at 20°C. Water content Weight per gal. at 20°C.
I
64.1 caI./g. 1.457 1.2220 0.369 cal 41.8 dynes/sq. cm. 1 . l % by w t .
.
.
0.28% by w t 2.0653 centipoises 0.7 mm. Hg 0.10% by w t . max. 10.17 Ibs.
Ethers
467
lSOPROPYL ETHER Table 10.7: Properties of Pure Isopropyl Ether (74) Molecular Formula CsH,,O Molecular Weight 102.172 Boiling Point. " C 68.5 Boiling Point Change. "C/mm at 760 mm 0 042 Freezing Point. " C -85.5 Density at 20°C.g/ml (in vacuo) 0.7235 at 60°F. Ib/US gal (in air) 6.07 Specific Gravity, 2O/2O0C (in air) 0.7244 Coefficient of Expansion (1) at 20°C per 'c 0.00143 Refractive Index. nO/D 1.3784 n20/D 1.36820 n30/D 1.36301 Critical Temperature, " C 288 Critical Pressure, atm 27.5 Critical Volume, cc/g 3.80 Heat of Vaporization (2,3), 760rnm, cal/g 68.16 Heat of Fusion at Melting Point (4). cal/g 25.79 Heat of Formation (5) (vapor at 25OC) k-cal/mole -77 Free Energy of Formation (4) (vapor at 25" C) k-cal/mole -31
Specific Heat (Liquid). cal/g"C (at 20°C) Thermal Conductivity (Vapor at 100°C) cal/(sec) (cm2) ("C/cm) Viscosity, cps at -20'C 0" c 20" c 50"C Surface Tension (6). 25°C. dynes/cm Dielectric Constant (7), 85 8 kHz, 25°C
1 CaIcuIaIeQirom density measurements as 7242 - 7139
7iw a io 2 CaIcuImed via Ciapyron Equation Z = 0 95 3 File h Reid In6 Eng Chem 22 513 (19%) 4 P8rkS el I I J Am Chem Soc 55 2735(1923) 5 Kharasch M S J Rwearch NO1 I Bur S14s 2 359 (1929) 6 vopel A I J C h m Soc Pari I 616 (1948) 7 KirC-Othmer Ency of Chem Tech 5 670 (1954) 0 Pelroleurn Enpinbsr JUM lY5 219
Table 10.8: Vapor Pressure of Isopropyl Ether' (74)
toc
mm Hg
1°C
mm Hg
1°C
mm Hg
-20 -15 -10 -5 0 5 10
13.4 18.4 24.9 33.3 44.0 57.3 74.0
15 20 25 30 35 40 45
94.4 119.4 149.5 185.6 228.4 278.9 338.0
50 55 60 65 70 75 80
406.6 485.8 576.7 680.3 797.8 930.1 1078.7
-
'Log VP mm Hg = 23.16817 2382.7fT 5.2545L0g T T = 273.15 + t"C
Table 10.9: Isopropyl Ether-Water Solubility (74) toc -10
0 10 20
30 40
"owt
%wt IPE in HIO
-
-
1.43 1.07 0.88 0.78
HtO in IPE 0.41 0.43 0.47 0.53 0.62 0.72
0.0000483 0.545 0.419
0.333 0.255 17.28 4 449
Other Propertlea of Commerclai IPE Autoignition Temp, OF 830 Flash Point (E), Tag Open Cup, " F (approx )+15 Tag Closed Cup, OF (approx ) -18 Flammable Limits of Vapor with Air VO vol of Compound, Upper 21 Lower 14 Relative Evaporation Rate at 25°C and OO/O R H I Shell Thin Film Evaporometer (n-BuOAc = 1 0 ) 8 04
RdHmCW
-
0.506
1" c
IPE In HtO
HIO in IPE
50
0.73 0.73 0.76 0.83 0.92 1.04
0.82 0.93 1.06 1.20 1.34 1.49
60 70
80 90 100
468
Industrial Solvents Handbook
Table 10.10: Mutual Solubility for the System: Isopropyl Ether-Isopropyl Alcohol-Water at 25%, % wt (14)
IPE
H,O
IPA
Sp. Gr.2SM0C
99.5 93.4 89.0 84.4 79.9
0.5 1.1 1.5 2.2 3.2
5.5 9.5 13.4 16.9
0.7210 0.7274 0.7326 0.7380 0.7427
74.4 72.8 70.3 68.7 65.3
4.6 4.7 5.2 5.8 6.7
21.0 22.5 24.5 25.5 28.0
0.7490 0.7509 0.7547 0.7564 0.7605
64.0 61.5 58.3 56.4 50.8
7.1 7.8 8.9 9.6 11.6
28.9 30.7 32.8 34.0 37.6
0.7620 0.7641 0.7698 0.7726 0.7812
47.6 42.6 38.6 35.7 31.5
13.0 15.5 17.8 19.7 23.0
39.4 41.9 43.6 44.6 45.5
0.7864 0.7958 0.8029 0.8091 0.8189
28.3 24.8 22.6 18.9 16.3
26.0 29.7 32.4 37.6 41.9
45.7 45.5 45.0 43.5 41.8
0.8275 0.8379 0.8450 0.8590 0.8707
14.5 12.6 12.2 10.6 8.6
45.0 48.4 49.0 52.1 55.6
40.5 39.0 38.8 37.3 35.8
0.8789 0.8884 0.8897 0.8982 0.9084
6.6 5.9 5.2 4.7 3.4
60.2 61.8 63.6 65.0 69.6
33.2 32.3 31.2 30.3 27.0
0.9200 0.9245 0.9293 0.9334 0.9437
2.2 1.6 1.3 1.2 1.o 0.9
74.8 78.3 83.3 09.4 93.8 99.1
23.0 20.1 15.4 9.4 5.2
0.9568 0.9634 0.9716 0.9796 0.9864 0.9928
Ethers
469
Table 10.11: Conjugate Solutions in the System: Isopropyl Ether-Isopropyl Alcohol-Water at 25"C, % wt (74) Upper Layer
Lower Layer
IPE 96.4 93.0 90.1 86.1 82.8
HzO 0.8 1.2 1.5 2.0 2.7
IPA 2.8 5.8 8.4 11.9 14.5
Tie Line' 1 2 3 4 5
76.3 72.1 64.2 54.2 45.4
4.0 5.0 7.0 10.2 14.0
19.7 22.9 28.8 35.6 40.6
6 7 8 9 10
1.3 1.4 1.4 1.7 2.3
80.3 77.8 74.1
16.3 17.0 18.3 20.5 23.6
36.9 31.5 25.3
18.7 23.0 29.0
44.4 45.5 45.7
11 12 13
2.9 3.7 4.7 9.8
71.2 68.3 64.6 53.3
25.9 28.0 30.7 36.9
Estimated plait point?
IPE 1.o 1.2 1.2 1.2 1.2
H2O 92.1 89.0 86.9 85.4 83.8
IPA 6.9 9.8 11.9 13.4 15.0
82.4 81.6
'See Table 10.12 2Point at which t w o layers converge into one phase. Reference: Frere, F.J., Ind. Eng. Chem. 41, 2365 (1949).
Table 10.12: Miscibility of Isopropyl Ether-Isopropyl Alcohol-Water at 25°C (74) i PE
I PA
470
Industrial Solvents Handbook
Table 10.13: Azeotropic Information-isopropyl Ether (14)
-
Ternary Azeotrope: IPA IPE (Boiling Point 61.7"C) Component
- Water
Azeotrope
Upper Layer
Lower Layer
60 89 0 50 100
5.8 93.1 1.1 95.6
10.0 1.o 89.0 4.4
IPA (Isopropyl Alc.) IPE Water o/o w
0ther Azeotropic information
Binary Azeotropes
B.P. "C 61. 62.2 70.5 69.0 4 60 61 16.3 65
-
< 20 47
Ternary Azeotropes
B.P. 'C 66 Min B.P. Nonazeotrope
Components and %wt H,O, 7.0%; Ethyl alcohol 14.7Oh; IPE 78.3% H 2 0- %; Acetone %: IPE - % H,O - Sec. Butyl alcohol IPE
IPE does not form lueotropet with Trichloroethylene 1,l-Dichloroethane 1,2-DichIoroethane 2-Chloroethanol lodoethane 2-Bromopropane Thiophene
-
-
2-Bromo-2-methyl propane 1-Chlorobutane Ethyl sulfide Diethoxymethane Benzene Hexyl Alcohol
Ethers Table 10.14: Vapor Pressure of Isopropyl Ether at Various Temperatures (8)
471
Table 10.15: Specific Gravity of Isopropyl Ether vs Temperature (8)
0.75
O.L ' 0.73
0.71
0.70
0.69
0.0
-20
Temperature. 'c
Temperature. T:
Table 10.16: Mutual Solubility and Specific Gravity of Isopropyl Ether, Water and Isopropyl Alcohol at 25°C (2)
Isopropyl Ether
Water -
99.5 93.4 89.0 84.4 79.9 74.4 72.8 70.3 68.7 65.3 64.0 61.5 58.3
0.5 1.1 1.5 2.2 3.2 4.6 4.7 5.2 5.8 6.7 7.1 7.8 8.9
Isopropyl Alcohol
-5.5 9.5 13.4 16.9 21.0 22.5 24.5 25.5 28.0 28.9 30.7 32.8
0.7210 0.7274 0.7326 0.7380 0.1427 0.7490 0.7509 0.7547 0.7564 0.7605 0.7620 0.7641 0.7698
(continued 1
472
Industrial Solvents Handbook
Table 10.16: (continued) Isopropyl Ether
56.4 50.8 47.6 42.6 38. 6 35.7 31.5 28.3 24.8 22.6 18.9 16.3 14.5 12.6 12.2 10.6 8.6 6.6 5.9 5.2 4.7 3.4 2.2 1.6 1.3 1.2 1.0 0.9
Isopropyl Alcohol
Water -
34.0 37.6 39.4 41.9 43.6 44.6 45.5 45.7 45.5 45.0 43.5 41.8 40.5 39.0 38.8 37.3 35.8 33.2 32.3 31.2 30.3 27.0 23.0 20.1 15.4 9.4 5.2
9.6 11.6 13.0 15.5 17.8 19.7 23.0 26.0 29.7 32.4 37.6 41.9 45.0 48.4 49.0 52.1 55.6 60.2 61.8 63.6 65.0 69.6 74.8 78.3 83.3 89.4 93.8 99.1
--
SG d
25°C.
0.7726 0.7812 0.7864 0.7958 0.8029 0.8091 0.8189 0.8275 0.8379 0.8450 0.8590 0.8707 0.8789 0.8884 0.8897 0.8982 0.9084 0.9200 0.9245 0.9293 0.9334 0.9437 0.9568 0.9634 0.9716 0.9796 0.9864 0.9928
Table 10.17: n-Butyl Ether (2) C4H90C4H9 n-Butyl ether i s a colorless, stable liquid, soluble i n water. Having two butyl groups, this ether i s an excellent solvent for many natural and synthetic resins, gums, oils, fats, organic acids, esters, and alkaloids. Beeswax and carnauba wax have limited solubility in butyl ether at roam temperature, but become quite soluble at higher temperatures. n-Butyl ether w i l l not dissolve cellulose acetate, benzyl cellulose, or cellulose nitrate, but when i t i s mixed with ethyl or butyl alcohol i t becomes a solvent for ethylcellulose. Butxl ether i s used as a reaction medium in organic synthesis and i n the extraction and purification of essential ails, organic acids, waxes and resins.
'I'ypicol Properlies and Specificdons
Boiling point at 760 mm 50
10 Color Flash point Heat of vaporization Freezing point Specific gravity at ZO/ZO"C Refractive index at 20°C Surface tension at 20°C Solubility in water at 20°C Solubility of water in solvent at 20°C Vapor pressure at 20°C Weight per gallon at 20°C Acidity (84 butyric) Distillation range Water content
142.4"C 63 28 Water-nhito 30.6"C 68.8 cal./g Approx. -06°C 0.7604.771
1.3W2 B.9 dynes per 5q cm 0.03% 0.19yo 48mmHg 6.4 lbs 0.05% by wt., m a l . 137-143°C 0.10% by wt., max.
Ethers
473
Table 10.18: Dlamyl Ether (2) C5H1 1OCgH11 Commercial diamyl ether consists principally of di-n-amyl ether and di-isoamyl ether, with small percentages o f isomeric amyl ethers and diamylene. I t i s a colorless to light yellow liquid which i s quite stable. I t i s insoluble i n water but soluble i n methanol, ethyl ether, ethyl acetate, acetone, aliphatic ond aromatic hydrocarbons, fixed oils, oleic and hot stearic acids, hot paraffin and carnauba waxes, the latter two solidifying when cooled. Unlike the lower aliphatic ethers, i t w i l l not dissolve nitrocellulose when admixed with ethanol. However, a mixture o f diamyl ether and 20% ethanol w i l l dissolve ethylcel lulose.
Typical Properties and Specifications Dielectric constant Flash point (open cup) Heat of vaporization Spccific gravity at 20/2O'C Specific beat Refractive index at 20°C Surfnce tension at 20°C Freezing point Vapor prcssure at 20°C Water azeotrooe at W98"C Weight per gniion at 2O'C Acidity (mg. ]99% by might 26WC 2530'C WO'C WOOC
26o.oO'c
(petuky Marten# dacd
M Acidity (u hydrorblorlc Pad) wa(u N n l h t
?hen01 combill
UO'F (11S'Cj 0001% by weight
0001% by weight 002% by might 002% by mmt
486
Industrial Solvents Handbook
Table 10.42: Miscellaneous Alkyl Aryl Ethers (2) These ethers are generally high-boiling, water insoluble liquids of pleasant odor, miscible w i t h a variety of organic solvents and commercial oils, fats, waxes and resins. Physical Properlies Formul.
2gyc
G;Kty
mim ~~. 0.993
yyp
~~
Methyl Phenyl Ether (Anisole) n-Butyl Phenyl Ether Aniyl Phenyl Ether p-tert-Amylphenyl Methyl Ether p-tert-Amylphenyl-n-Amyl Ether Amyl Benzyl Ether Amyl Tolyl Ether Amyl beta Naphthyl Ether Amyl Xylyl Ether
CHiOCJI,
15&160
120
202-212 180 C,H,OCJL 214-229 185 C,H,!OCJI, C I H ~ ~ C B ~ O C H Z235-243 210
0.929 0.924 0.942
164.1
C L H ~ ~ C ~ H I O C L285-295 I I ~ ~ 260
0.9%
234.2
CIH~IOCH~CJII CJL,OC;H,CHz CIH!tOCnH~ CsHzIOCtHz(CHds
224-239 175 %Is264 I95
320-350 310 2 S 2 6 3 205
0.912 0.916 1.01 0.907
Table 10.43: Furan (77)
HS-5H HC C H 'd Furan i s a cyclic dienic ether stabilized by benzene-like resonance. Because of its conjugated unsaturation and heteroc y c l i c atom, furan w i l l undergo many types o f reactions. I t is, therefore, o f interest as a chemical intermediate for pharmaceuticals, insecticides and fine chemicals. The heterocyclic oxygen atom i n a ring w i t h conjugated unsaturation gives furan a combination of ether, aromatic and olefinic characteristics. This polyfunctionality permits i t to undergo a variety of reactions. Compared to benzene, the furan ring has greater reactivity, and i s more susceptible to cleavage, thus resembling the vinyl ethers. Like the vinyl ethers, the furan ring i s cleaved by aqueous acids. This reaction i s accompanied by resin i f ica tion . PHYSICAL PROPERTIES Physical State Liquid Color Color l e s s Odor Characteristic ethereal S p e c i f i c G r a v i t y a t 20°/40C. 0.937 Freezing P o i n t -85 .6loC. (- 122. 10°F .) Vapor D e n s i t y 0.170 lb./cu. f t . B o i l i n g P o i n t (760 mm.) 31.3OC. (88.45'F .) F l a s h P o i n t (Tag. c l o s e d cup) -32'F. R e f r a c t i v e Index n20/D 1.4214 Molecular Weight 68.07 Flammability o r Explosive L i m i t s 2.3-14.3 v o l . % i n a i r Heat o f V a p o r i z a t i o n a t 31.2OC. 95.5 cal./gram Heat of Combustion a t constant v o l . 500.1 k g ca 1. / g r am-mo l e 2 14OC. C r i t i c a l Temperature Heat o f Formation a t 25OC. -14.9 kcal./mole S o l u b i l i t y in: Water (wt. % a t 25OC.) 1 Most o r g a n i c s o l v e n t s o o
.-
Table 10.44: 2-Methylfuran (2)
Sylvan
2-Methylfuran i s a c y c l i c diene possessing ether-like properties. It i s highly reactive w i t h many inorganic and organic compounds yielding a variety o f new derivatives which await exploration for the development of commercial applications.
(continued)
Ethers
487
Table 10.44: (continued) Appearance Odor Molecular weight 1)oilirrg point nt 760 m m Prccxing point Specific gravity, 204C./4'C. Iiidex of rcfruction, N20/D Flash point Vapor prcasurc at 15'C. (59°F) 20'C. (88'Y)
25'C. (77'F) 3O'C. ( W F ) Solubility in wnkr nt 25'C
Colorleas, tnolilc liquid 1Slhcr-like 82.098 6 2 4 ' C (144-47°F) 4 ° C (- 126.1'F) 0.816 1.434
-3O'C (-22°F) 110.5 mm 130 mm 174 mm 216 mm Less thnn 0.3 gm/IW gm
Table 10.45: Tetrahydrofuran ( 1 1)(49) Product information
Tetrahydrofuran (THF, tetramethylene oxide, diethylene oxide, 1,4-epoxybutane, tetrahydrofurane, oxolane) is an industrial solvent widely recognized for its unique combination of useful properties. DuPont THF is better than 99.9% pure with a small (0.025-0.040 wt % ) amount of butylated hydroxytoluene (BHT, 4-methyl-2,6-di-tertbutyl phenol) added as an antioxidant. Tetrahydrofuran is a cycloaliphatic ether and is not "photochemically reactive" as defined in Section k of Los Angeles County's Rule 66 (equivalent to Rule 442 of the Southern California Air Pollution Control District). THF has an ethereal odor. Physical Properties of Tetrahydrofuraq
Molecular Weight Boiling Point (760 mmHg). "C ("F) Freezing Point, "C ("F) Vapor Pressure, 20°C (68% mm Hg (kPa) Density, Liquid, 20°C (68"F), g/mL (mg/m3) Ib/gal Vapor (air = 1) Evaporation Rate In-butyl acetate = 1)
72.108 66 (151) -108.5 (-163) 143(19.1) 0.888 7.41 2.49
8.0
Viscosity, 20°C (68"F), CP(MPas)
0.48
Surface Tension in Air, 25°C (77"F), dynlcrn (mN/m) Refractive Index, n f
26.4
Heat of Vaporization (at bp), cal/g Btu/lb kJ/kg Heat of Combustion (-Aha at 25°C (77OF) liq kcal/mol Btu/lb kJ/g Specific Heat, Liquid, 20°C (68°F). cal/g.C (Btu/lb,F) kJ/kg.K 50°C (122°F). cal/g.C (Btd1b.F) kJ/kg.K Vapor, 66°C (151°F), cal/gX (Btu/lb.F) kJ/kg.K
1.4073 95 171 398 598.4 14938 34.72
Coefficient of Thermal Expansion, 10-20°C. av/"C 50-68"F. avPF Flash Point (TCC),"C
(OF)
Autoignition Temperature, "C ( O F ) Flammability Limits i'n Air, 25°C (77°F). lower upper Critical Temperature, "C ("F) Critical Pressure, atm (MPa) Dielectric Constant, E, 20°C (68°F) 30°C (86°F) Conductivity, 25°C (77°F). p mhoslcm p S/m Dipole Moment, p, 25-50°C (77-122OF1, Debye Units Solubility Parameter, 6 Hydrogen-Bonding Index, y Miscibility: water, esters, ketones, alcohols, diethyl ether; aliphatic, aromatic and chlorinated hydrocarbons
0.001 26 0.00070 -14.4 (6) 321 (610) 2 11.8 268 (514) 51.2 (5.19) 7.54 7.25 0.01 5 1.5 1.6 9.1 5.3
Infinite
0.469 1.97 0.496 2.090 0.37 1.55
(continued)
488
m
0
s
8
H
0 0 v
H
H
8 51
Industrial Solvents Handbook
C
e
J
r
g
2
::
0
5:
P
8
r c
e c c"
r
0
t J In
t
B
n
Temperature, "F
s:
0 N
s!
0
z
.t
N
rn
0 N
h
Ethers
489
Table 10.45: (continued) Flash Points o f Tetrahydrofuran-Water Solutions (by Setaflash Closed Tester)
Combustible
Flammable
100 90 80 70 60 50 40 30 20 io 0 Rei.: Culver, L. J.. "Modern Paint and C0atings:Vol. 71 (1981). No. 10. pp. 145-149. (C. A. 96(10) 70460F)
%THF
Tetrahydrofuran-Soluble Plastics. Resins, a n d Elastomers Acrylic Resins Methyl methacrylate polymers Ethyl, butyl, and other methacn/late polymers Acrylic polymers and copolymers Alkyd and Amino Resins Alkyd resins Urea formaldehyde resins (uncured) Phenol formaldehyde resins (uncured) Cellulosics Cellulose acetate Cellulose acetate butyrate Cellulose acetate stearate Ethyl cellulose Nitrocellulose Miscellaneous Resins Acrylonitrile-butadiene-styrenecopolymers Styrene-acrylonitrile copolymers Chlorinated polyethylene Polycarbonates Polysulfones Epoxy (uncured) Silicones (uncured) Polyesters (low molecular weight) Polyamides (low molecular weight) Polystyrene Styrene-butadiene copolymers (some)
Elastomers Sutadiene-acrylonitrile copolymers (some) Chlorinated rubbers Chlorosulfonated polyethylenes Polysulfides Polyurethanes (uncured) Rubber (natural, unvulcanized) Chloroprene elastomers Vinyl Resins Polyvinyl acetate Polyvinyl butyrate Polyvinyl butyrals Polyvinyl chloride Vinyl chloride copolymers Vinylidene chloride copolymers Vinyl acetate/ethylene (some) Natural Resins Congo ester Coumarone-indene Raw dammar Ester gum Manila copal Pentaerythritol ester gum Rosin Shellac (many)
(continued)
490
Industrial Solvents Handbook
Table 10.45: (continued) Vapor-Liquid Equilibria of Tetrahydrofuran
+ Water (760 mmHg)
1.0
0.8
0.6
0.4
0.2
0 0
0.2
0.4
0.8
0.6
1.o
Mole Fraction THF in Liquid
Chemical Structure (49)
Typical Properties (49) m
Tetrahydrofuran (mol. wt.
-
72.1)
C.A. No. 109999. Other common names are: Diethylene Oxide 1.4-Ep~xybutane Oxacyclopentane Oxolane The G 4 F product assays better Illan 99.8% and is stabilized with 0.025% of the antixidant BHT (4-melhyl-2,6di-left-butylphend).
Water Content (wt%)___
OMlKU __-. _-_0 015 max 0 025-0 04 005max 66"Cw,,,(151 'F) ______________ -lOsS"C(-163 F) _____ ______--_ -
--
-.
Peroxides (as THF-hydroperoxide,wt%) Statnlizer (wt%) Other Immirities
Fling Pant Freezing Pant
-
Qqud Densty (20°C) Vapor Oenslty (ar 1) Specific Grawty (20/4"C) vlscoslty (20°C) -____ Surtacc Tensm (25°C) Relractive Index (nom) cceffilent of Cutxal Expansion (lo-20°C) Flash Pant (Tag closed cup) Fbmhlity Lirmts (%mi in air 25°C) Ignition Temperature Specihc Heat (cal/g/"C) for Lquid
Specrlc Heat (cal/g/ "C) for Vapw Latent Heat 01 Vaponzatim (cal/g, 66°C) Cntical Temperature Critcal Pressure Heat 01 Cwnbustion (kgcal/mde) Heat d Formation (kgcal/mde) b p d e1(25-S"CL
_. __
-
-
-___
_.
_.
ORB8g/cc(741 Iblgal) 256calc 0886-0889 0 53 cps 26 4 dynes/cm 1 4073 Oo0129Av/°C(Ooo070Av/"F) -14 4°C (6°F) 2 (lower). 11 8 (upper) 321"C (610°F) 0 469 cak at 20°C. 0 496 calc at 50°C 0 37 calc at 66°C 98 1 Calc 2 6 8 T (514°F) 51 2 atm 597 CalC -527 calc 17Debye 758 15x10' 80 9 1 calc 53
Cdnducttwty (mhos/cm, 25°C) Evgmalion Rateln-butyl acetate 1) Wutnlity Parameter Hydrogen-Bonding Index MiscihtiW with water, alcohols, diethyl ether. esters, ketones.'allphatic, aromatic. and chlorinated hydrocarbons inlinite There &la ue
ol cwrenl p r o d u c ~ LNJI UE nd nec88mW spscl(lCall0n.
(continued)
Ethers Table 10.45: (contlnued) High Solvont Capacity for Roalna Many THF applications are based on its solvent capacity lor resins. including high-molecular-weightvinyls For example THF IS the solvent-of-choice for PVC pipe welding and bonding of other molded items Vinyl lopcoating formulations, e g lor automobile roofs and upholstery Magnetic tape binder systems Thermoplastic polyurethane coatings Printing inks for plastics Polyurethane adhesives for shoes Polyester laminating adhesives Polymer reactor cleaning
.
.. ...
PVC, CPVC, polyvinyhdene,and vinyl chloride copolymers dissolve readily in THF at room temperature Solutions wdh high solids content and workable viscosities can be prepared Many other resins, elastomers, and uncured polyurethanesand epoxies are soluble The list includes
Extradon W e n t THF is an excellent extraction solvent for many natural products, including alkaloids. fats, waxes, rubbers, and resins The following natural resins are soluble in THF Congo ester coumarone-indene ester gum dammar manila copal pentaerythritol ester gum rosin shellac A 66" boiling point allows refluxing in normal water-cooled systems without loss of THF, it also simplifies separation and recovery of the desired product Mixtures of THF and water are especially effective solvents for alkaloids, such as caffeine
Typical Range of Reain 8duMlltka In THF va MEK
Resin Type
Wt% Realn for 2500 cpa, 25.C THF MEK
Polyvinyl Chloride' Chlorinated Polyvinyl Chloridez Poly (Vinyl Chloride/VinylAcetateY Polyurethane' PolyvinylideneChloride5
13-20 16 27-40 17 44
__ - '"Exon" 654 (Firestone) "Geon" 121, 101, 103EP (Goodrich) PVC-71 Dispersion (Diamond Shamrock) WC Pearls 2200. 2250 (Escambia) "Marvinol" 10 (Uniroyal) "Vinylite" QYNV (Union Carbide) "Vygen" 1 10, 120 (General Tire)
s E
Q
f
OD
-E 0 0 OD
5
Glycol Ethers
.-B . I
c
s
509
c
510
m
4l
5
0
w
>
m
Industrial Solvents Handbook
8 rn
5
s:
.$
Y
f
F
0
r
E E 0
10
r-
@,
I
8 c-
Glycol Ethers
511
512
Industrial Solvents Handbook
Table 11.8: Olin Chemicals Poly-Solv Propylene Glycol Ethers (66)
Olin produces five ethylene glycol ethers: Poly-Solv@‘ EM, ethylene glycol monomethyl ether (CH,OCH,2CH,2OH) Poly-Soh DM, diethylene glycol monomethyl ether (CH3OC$C%OC$C%OH)
Poly-Soh DE, diethylene glycol monoethyl ether (CH3C%OC4C%OC~C&OI-l)
PolySolv TM, triethylene glycol monomethyl ether CH3(OCH&q)3 OH
Poly-Soh TE, triethylene glycol monoethyl ether
cH3c%coc%c%)3oH Typical Physical Properties EM. DM DE Boiling Point (“C) Q 760 mm Hg @50mmHg @ 1OmmHg Coefficient of Expansion @ 20°C @ 55°C I Density @ 25°C (Ib/gal) Flash Point, TCC (“C) (OF)
194 115 82
0.00095 0.00099 8.05 41 106
-
-
0.00088 8.51 87 188
0.00084 8.24 85 185
-
-
-
-85 -121
-85 -121
555.9 76.09 1.4021 Complete Complete 0.966 2.233 6.2 1.7
Flash Point, COC (“C)
(“F) Freezing Point (“C) (OF)
Heat of Vaporization @ 760 mm Hg (jouledg) Molecular Weight Refractive Index @ 20°C Solubility @ 20°C Poly-Soh in water water in Poly-Solv Specific Gravity, apparent @ 2O/2O0C Specific Heat @ 2OoC (jouledg-”C) Vapor Pressure @ 20°C (mm Hg) Viscosity, absolute @ 20°C (cp)
EM
202 121 87
124 55 27
TM
TE
249 152 126
256 158 130 -
8.50
-
-76 -105
118 245 -55 -67
124 255 -2 1 -5.8
379.1 120.15 1.4263
402.4 134.17 1.4273
327.6 164.20 1.4381
299.8 178.23 1.4376
Complete Complete 1.021 2.149 0.2 3.9
Complete Complete 0.989 2.308 0.1 4.5
Complete Complete 1.048
Complete Complete 1.022
W
I
u)
$
3c .-c0
E
51 Q
>
W
a
U m w
:
w
0
-2 0
-z -g
-5:
Q
-0
01
0
-E
3
._
E
E i=
Glycol Ethers
i'
539
540
Industrial Solvents Handbook
1::-Q)
~ 'U ~ "t) I::~~ ~
"
"'~
esQ .C:: o ~
~ 2 ~ o eO u '"' 2' Q) . 'U u
..:(\jo;
I :
666
a;
I I
a;
0>0>0>
000 1"-00
I~ ~
I Q) C
~~o "'~o "-~(Q IiI .., . ., .., '"' "t)~!::: -c S!~-J ~01-o: " ~ a: -O:U-o:
"
,"
°
c 0 --c Q»~~,,-CD
U
-CD 3 Q) c
E.
I~
~
~~-o; .c -0;
0,,"'-'"
.o
~
'5 I 01 tO 0. e
001 E' "'
:§ -0; ()
I E-EE 0.0.0. (/)(/)(/)
01
a,
0; 0; 0;,
~~~
0;0;0;
uuu
c:c:c:
Q)Q)Q)
0.0.0.
U)U)U)
I Q)1
~ ;:)
> c >
iU! Q) u < ~ :9 5 :E u
541
-0 Q) :J c: '.:; c: O .£
I I I
a>
»'>
cn:r:r z~:r >-»> 0)0)0)
::>::>::>
0:0:0:
0:0:0: 000
uuu
'"'"'"
:0:0:0
a> a> "0"0"0
000 000 I~~~
Q)I
Glycol Ethers
--I 00; c:C: ","'
~N , Q) r--c NNE Q)", =~ Q)(.) Q)Q) aJaJ
.2.2.2 -0;-0;-0; ~~~ OIOIC1 01
===1 ~~~I
l
I X;. >!D
~a: Qj
=
x
"4; c , Q) >x
000 ""n...
"0"0 1-'00= .I: .I:
1.1:.1: e' .~~8 ~rr
tO a) 00 Oa)
(.)~~ Q)~,"
''''''to ~~(') -Xa) OQ)I() ~-a.;: ~'"O) IIJOU
I
j
"' "' "'
~ Q)
~I~I~I~I~
.W
",Oa)
000
Q) I: Q) ":>, )(
~
""5 I: -
..,
EOE .0: ° rr
,
I Ln~..' ~
-oQ)-o
,~ u-u
:§G:§
<w
.>.>.
I~ >. u
cn ',9!; 0. 0. ~ (/) c '0 nI a:
ccc
:0Q) ~ c ; c o E.. ., ~ ... ... Q) :0 IG ..-
542
W
0
I
N 0
I 0
I 0
0 P
Industrial Solvents Handbook
r 8
0
U 0
-
m
h
Q-
f ln
? W ln
E a
c
E
Glycol Ethers
543
0 v)
u
m L
m
U
E .c
e
544
tu
.-t
Industrial Solvents Handbook
1
m
cnm
IN
- I N N W
mim
i
cy
L
Q
.-Io .-+ 2
3
2 0
X
a w
n
c
Q
z
0 Q
B
> J
za U
Glycol Ethers 545
546
Industrial Solvents Handbook
Table 11.64: (continued)
.Blfth Defects
Thymic Atrophy I
PNB
PTB
pph
LOAE
NOAE
1,000
N1.F
I ,OO(
1,000
1,000
N1.V
%,OOO
N/D
N/D
N/D
N/D
1,000
NLF
1,000
1,000
NI,F
370
740
?,000
N1.F
3,000
-
145
225
N/D
N/D
N/D
N/D
3,000
NLF
N/D
N/D
N/D
N/D
N/D
LOAEL NOAE
LOAEL NOAEL
145
22s
N/D
N/I)
N/D
N/D
N/D
N/D
N/D
N/D
N/I>
N/1>
N/D
N/D
mr:
3,00c
NLF
3,000
NLF
3,000
N/D
N/D
N/D
N/D
N/D
N/D
N/D
N/D
N/D
560
2,800
2800
-
14.5
560
560
NLF
2,000
NLF
2,000
NLF
N/D
N/D
N/D
N/D
N/D
N/D
N/I>
N/D
N/D
N/D
2,000
NLF
2,000
NLF
2,000
NLF
300
N/D
N/D
N/D
N/D
N/D
N/D
N/D
N/D
N/D
N/D
N/D
-1,800
NLF
-1,800
N/D
N/D
N/D
N/D
1,176
NLF
1,176
N/D
N/D
N/D
N/D
N/D
N/D
N/D
N/D
N/D
N/D
-
N/D
N/D
N/D
N/D
1,524
NLF
755
NLF
600
NLF
600
N/D
N/D
N/D
N/D
N/D
N/D
N/D
N/D
N/D
N/D
N/D
N/D
N/D
N/D
Inhalation (ppm)
N/D
N/D
N/D
N/D
700
NLF
700
Dermal (mg/kg/d) Oral (mg/kg/d)
N/D
N/D
N/D
N/D
1,140
NLF
1,140
N/D
N/D
N/D
N/D
1,000
NLF
1,000
Inhalation @pin)
990
NLF
990
NLF
709
NLF
709
Dermal (ing/kg/d) Oral (ing/kg/d)
N/D
N/D
N/D
N/D
N/D
N/D
N/D
N/D
N/D
iV/D
-
N/D
N/D
N/D
N/D
Inhalacion (ppm)
N/D
N/D
N/D
N/D
N/D
N/D
N/D
Drrinal (nig/kg/d) Oral (mg//kg/d)
N/D
N/D
N/D
N/D
1,000
NLF
1,000
N/D
N/D
N/D
-
N/D
N/D
N/D
N/D
300
NLF
300
NLF
300
NLF
300
N/D
N/D
N/D
N/D
-5,000
NLF
-5,000
hVI>
N/D
N/I)
N/D
1,000
NLF
1,000
Iiih:il;ition
DPM
NOAEL
(ppin)
Derinal (nig/kg/d) Oral ( i i i & / d )
-
(continued )
Glycol Ethers
I
DPNP
DPNB
D~TB
TPM
TPE
TPNB
EM
EE
Dennal (mg/kg/d)
N/I)
N/D
N/D
N/I>
Oral (nig/kg/iI)
N/I)
N/D
N/I)
N/D
N/I) N/I)
Inllalation (ppin)
N/I>
N/D
N/I>
N/D
N/I) N/I)
N/D
N/I)
N/I)
N/I)
910
NLF
910
NI,I‘
i,ooo
NLF
1,000
NIJ
N/D
N/I)
N/II
N/l>
N/I)
010
NLF
N/I) N/I)
Dennal (ing/kg/d)
910
NLF
910
NLI;
oK1i (mg/:/kg//d)
N/I>
N/D
N/D
N/I)
1,000
Ni,r;
Inhalation (ppin)
N/1)
N/I>
N/D
N/I>
N/I>
N/1>
N/D
N/1>
N/I)
N/lI
N/D
N/D
N/D
N/D
N/II
N/Il
N/D
N/D
N/l)
N/I)
I)ernlal (nig/kg/:/d)
N/I)
N/D
N/D
N/D
N/D
Oral (tllg//kg/
N/D
N/1)
N/I)
SA)
Inhalati~in(I,pin)
11‘1
I19
NISI:
11(J
N1.F
I20
NLF
120
NFI,
Dernul (mg/kg//d)
N/II
N/D
N/D
10,000*
N1.F
-10,000’
NLF
-10,000‘
N1.F
Oral (nig/kg/d)
N/1>
NLF N/D N/I)
N/D
N/l>
5/11
N/D
N/D
N/D
N/I>
N/I)
Inhalation (ppm)
N/D
N/D
N/I)
S/l)
N/D
WI)
N/D
N/D
N/D
N/D
N/D
N/I)
N/D
Oral (mg/kg/d)
N/D
N/D
N/D
S/I>
S/I)
N/D N/D
N/I) N/D
N/I)
Dermal (mg/kp/d)
N/I) N/D
N/D
N/D
N/I)
S/II
Inhalation (ppm)
N/D
N/D
N/D
N/Il
WD
N/D
N/D
N/D
N/II
N/Il
N/D
N/D
1,000
NIJ
N/D
N/D
N/D
N/D
N/D
N/D
N/D
1,000
N U
1,000
NLF
10
50 250
30 NVF
100
30
100
650
30 N/D
100
NNF
N/D
N/D
A’/D
250
NNF
31
io
100
10
50
“F
10
50
100
400
100
370
S/I)
N/D
NNF
-250
N/D
N/D
N/D
N/D
1 .OOO
150
300
N/D 93
N/D
NhTF
I85
N/I)
N/I)
i0i
N121:
25
77
4oi
NI,F
N/D N/D
N/D
Oral (nig/kg/d)
N/D
Inhalation ( p p i ) Deniial (mg/kg/d)
NNF
50 250
Oral (mg/kg/:/ti)
31
Inhalation (ppm)
50
10
h’/D
N/D
Dermal(mg;kg/d)
100
Dennal (mg/kg/d)
NNF
175 -250
O r d (ing/kg/d)
Nh’F
200
200
NLF
25
CO
Ilernlal(mg/kg/d)
1,176
NLF
1,176
SLI;
360
NLF
150
180
i60
NI,F
Oral (iii$kg/J)
1,180
NLF
30
100
885
NLF
80
90
88C
SLI;
Inhalation (ppni)
EB
N/D N/I)
N/II
NID = No Data NNF = No NOAEL Found (Lowest dose tested caused the effect) NLF = No LOAEL Found (Highest dose tested did not cause the effect)
547
Industrial Solvents Handbook
Glycol Ethers Table 11.65: (continued)
3
7
37
21
15
3
>loo
>loo
>loo
>loo
>io0
>loo
>loo
>loo
3
1
loo
>loo
>loa
Diethanolamine oleate
>loo,
>loo
>loo
>loo
I >loo
>1M)
Triethanolamine laurate
>1W
22
18
68
90
58
67
80
>loo
>io0
>loo
>1w
>1w
I >loo I >loo
Triethanolamine oleate
>loo
>loo
>1w
Triethanolamine stearate
15
6
5
21
13
5
.loo
37
15
>loo
>loo
>1w
>loo
>loo
Monoisopropanolamine oleate
>loo
>loo
>io0
>1w
>loo
>loo
>loo
>loo
Monoisopropanolamine stearate
1 3 1 2 1 1 1 1 1 1 5 1 4 1 < 1 1 < 1
Triethanolaminetall oil
I >loo I >loo I >io0 I >loo I >loo I
Mixed lsopropanolamine tall oil
>1w
>loo
>loo
>loo
>loo
Potassium oleate
>1w
>loo
>loo
-
>loo
loo
>1w >loo >1w >loo >loo 1
1
-
Resin Solubility+ COMPOUND
I
PM
1
DPM
I
TPM
I
PMA
I DPMA I
I
PPh
I
EB
DB
I
OM
I
EPh
Acrylic Acryloidl 6-66
D E R 657
CellUlOtlc CAP-482-0.5 CAB-381-2
Vinyl UCAR VYHH
* Tiademark 01
.. .* .. .. .. .. . . . . 0
0
0
0
.
.
The Dow Chemical Company
' Acryloid Iradomarh 01 Rohm 6 Haas Company llsdemark 01 E I OuPonl de Nemours & Comprnv Cyme1 Trademark 01 American Cyanamid Company Dermodur Trademark 01 Farbenlabriken gayer AG 5 Chempol Trademark 01 Freeman Chemical Corporalion 6 UCAR Tiademark 01 Union Carbide Corporation Soluble buI no1 rccommended lor use 2 flvxlte
0
.
0
0
0
.
.
.
*
Olssoldd gel particles Parllally so1uble many u n dlssol~ed011 particles insoluble
(continued)
549
550
Industrial Solvents Handbook
Table 11.65: (continued)
PM
1
DPM
I
TPM
I
EB
Composition of Titrant, Volume % DB DM sec-butanol
I
I
I
I
isobutanol
[
ml to couple1
n-butanol
32.8
100
I
I
I
I 7 5 1
I
2
11
I
5
41 .O
50
50 25
75
42.1
100
I
1
1 5 0 1
1
1
I 2 5 1
1
2
I I I
5
1
I I I
42.5
I
I
I
I
I
1
I
7
1
I 0
11
I
5
0
I
75
50
1
I
75
11 11 11
58.3
60.9 61.8
95.8
I
I
I
I
I
I
100
11
104.6 230.0
100 1
48.8
82 1
25
100
I
34.2
Milliliters 01 product required to titrale IO ml 01 mineral spirits and 10 ml 01 water Io a clear homogeneous solution at 25°C
Evaporation Rates of DOWANOL Products OOWANOL PM DPM TPM PMA
(BuAc = 1.00)'
OOWANOL
(BuAc = 1.00)
0.71
EC-300
0 21
0.02
E6
0 08
260 >260 >260 >260
52a
pt
Flash points measured by the closed cup method. ASTM D-56
59a 60a 61a
582
Industrial Solvents Handbook
Table 11.70: CARBOWAX Polyethylene Glycols (19)
Typical Physical Properties of CARBOWAX Polyethylene Glycols and Methoxypolye iylene Glyc 01s g/cc 80%
Welting or Freezing Range, “C
iolubility in Water a t 20°C. % bywt
Viscosity a t 210°F. cSt
Average Number of Repeating Oxyethylene Units
~~
iEl -15 I l l h -1 to h
43 58 73 15 1 10 8 15 3
400 -
380 t o 420
I 1255
I0931
1.0763 1.0766 1.0769
540 Blend (a) 600 900
468 to 534 570 to 630 855 to 945
ih) 11258 (hl
10930 10931 10926
1.0765 1.0767 1.0763
38 to 41 20 to 2 3 32 tu 36
950 to 1050 1305 t~ I595 3015 t u 3685
lh)
1.0927
1.0765 1.0761 1.0769
37 to 40
1000 1450 3350 4000 4600 _ _8000
3600
ill1
j
ill1
I
I.0‘119 1.0926
I .(I769 I .I1764
44oi
xo
17 2 26 5 90 8
Id)
1-10 4 IS3 9 S2I 7
17 i O ( 1 18)
1.03‘)2 (cl
lS.655
135 t o 365 525 IO 575 715 IC1 785
1.0173 I .05 15
I800 IO 22OI1
I.0707
4175
I0742
to
4140 t(> 5060 7000 io ‘)OOIl
Cornpciiind 20M
350 550 750 2000 5000
I
111
1.11595
5625
Surface Tension at 25°C. dvnes/cm
Product
I 06x9
Liquid
lefractive Index,
Specific Heat at 25°C.
Heat of Fusion,
I
(conti nued)
..
0
0
m
0
N 0
0
Glycol Ethers
N
0
583
584
0
r
Industrial Solvents Handbook
0
N v)
0
r
0
::
w a
wI
Glycol Ethers 585
H w N
w 0
..
0
rc F F
586 Industrial Solvents Handbook
vi 0
..
0
rc r r
PD J 0
al J
m
aO 0 o w
r
0
c
J
Glycol Ethers
8 0
5:
H 5: N
s 5:
587
588
$
8
F:
7
0
0
-
a 0
w
Industrial Solvents Handbook
450
1466
1126
917
1'14
0490
PEG 12
E900
Y(X)
14
1(x)
10
>450
a
1204
d
182
a
-
ElOOO 1000
37
El450 14',0
44
SOLID
0
>450
a
1214
a
a
PEG 20
29
>450
a
1214
a
a
PEG 6-32
d
a
PEG 75
L350
54
(13
>450
a
1224
E4500 4 W
si
180
>450
a
1224
1
rt
PEG 100
000
>500
a
1221
a
1
PEG-150
-
PEG-6 Methyl Ether
FQSO
E8000 HOW
60
Me(hoxypo1~elhylene Glycolr MPEG
CAS# 9004 74 4
MPEG 350
350
0
27
16
38
>350
1455
1097
914
138
550
20
56
30
63
>400
1461
1102
911
181
MPEG 550 MPEG 750
-
PEG-10 Methyl Ether
-
Methyl Ether
PEG-16
750
30
53
99
>450
1463
1096b
904b
d
a Designates properties not applicable for solids b At 50' ' Cosmetic Toiletry and Fragrance Association
Liquids Miscible in all Proportions with Uquld Polyethylene Glycols E200, E300, E400, E600
-
Acetaldehyde Acetlc Acid (Glacial) Acetic Anhydride Acetone' AcetyleneTet rabromide Acrylonitrile Allyl Alcohol Allyl Bromide Amyl Acetate Amyl Alcohol tert-Amyl Alcohol Anlllne Benzaldehyde Benzene Benzyl Alcohol Bromobenzene Bromoform n-ButylAcetate n-Butyl Bromide n-Butyl Phosphate n-ButylStearate o-Chloroanlline Chlorobenzene Chloroform' 0-Cresol Cyclohexanol Cyclohexanone DiacetoneAlcohol DichloroaceticAcid o-Dichlorobenzene Dichloroethyl Ether MethyleneChlorobromide' *Available from Dow (Temp.175.F)
___ Dichloroisopropyl Ether Diethanolamine' DiethyleneGlycol' 1,4-Dioxane' DiphenylOxide' DipropyleneGlycol' Ethanol(95%) Ethanolamine. Ethyl Acetate Ethyl Bromlde Ethyl Chloroacetate Ethyl Lactate EthyleneChlorohydrin EthyleneDibromide' EthyleneDichloride' EthyleneGlycol' EthylideneDichloride Formamide Furfural Glycerine' Hydrochloric Acid (conc.)' lsophorone Isopropanol(99%) Isopropyl Bromide Lactic Acid (85%) Mesityl Oxide Methanol Methyl Chloroform' (1,l,l-trichloroethane) 4-Methylcyclohexanol Methylene Bromide Methylene Chloride'
.__ --
Methyl Ethyl Ketone Methyl Formate Methyl Isobutyl Carbinol Methyl Isobutyl Ketone Methyl Salicylate. Morpholine' Nitrobenzene Nitroethane Nit romethane 1-Nitropropane 2-Nit ropropane Octyi Alcohol Paraldehyde Phenetole Phenyl Acetate Phenyl Ethyl Acetate Phenyl Ethyl Alcohol 4-Phenyl-m-Dioxane PhosphoricAcid (85%) Piperidine n-Propanol Propylene Dibromide Propylene Dichloride' Pyridine Styrene Oxide TetrahydrofurfurylAlcohol Triacetin TrimethyleneBromide TrimethyleneChlorobromide TripropyleneGlycol' Water
(continued )
600
Industrial Solvents Handbook
Table 11.71: (continued)
Liquids Insoluble or Partly Soluble in the Uquid PolyethyleneOlycols Approximate Solublllty, Volume Percent
Butyraldehyde Carbon Disulfide Carbon Tetrachlorlde' Castor Oil
Ins.
Ins.
Ins.
10%
10%
10%
Ins.
Ins.
Ins.
Ins. 25% Sol. Ins.
Ins. Ins. Ins. Ins.
Ins. Ins. Ins. Ins.
Ins. Ins. Ins. Ins.
Ins. Ins. Ins. Ins.
Ins.
% ~ _ _ Sol. _45_ -
40%
Cod Liver 011
Cottonseed Oil Cyclohexane Decahydronaphthalene Dlamylnaphthalene -~
Ins.
Ins.
Ins.
Dibutyl Sebacate
Ins.
Ins.
Ins.
Ins.
Diethylbenzene'
Ins.
10%
Diethyl Ether
Ins. 25%
25%
25 Oo/
25% 25%
Diisopropylbenzene
Ins.
Ins.
Ins.
Ins.
DodecylAlcohol
Ins.
Ins.
Ins.
Ins.
Ethylbenzene.
10%
Ethylcylohexane Gasoline . -__ ___- ______ Isopropylbenzene
Ins. Ins. Ins.
35YO Ins. . .Ins. 25___ O/o . _ I . . . . .
25%
55%
35% Sol.
Sol.
IsopropylChloride
Kerosene Lard Oil Lemon Oil Methvi Laurate alpha-Methylstyrene Ollve Oil Orange Oil
Ins.
Ins.
Ins.
Ins.
Ins. Ins. Ins. ___35YO Ins.
Ins. Ins.
~~
-
75 % Sol. Ins. Ins. ..._.___-____ Ins. Ins.
.. . .
~
Sol.
Sol. Ins. Ins. Ins. ___--______-_ Ins. Ins. Sol. Sol.
Ins. Sol. 2%
10%
30Y O
Ins.
Ins.
Ins.
Ins.
Pentachlorodiphenyl Oxide Perchloroethylene
Ins. Ins.
Sol. Ins.
Sol.
Sol.
10%
RicinoleicAcid SoyaOil
Ins.
Ins.
Ins. ins.
Ins. Ins.
25 Yo Ins. Ins.
Tetrahydronaphthalene Tributyl Aconltate Triethylbenzene
10%
45%
Ins. Ins.
25% Ins. Ins.
Ins. Ins.
10%
Xylene
10%
35%
65YO
Sol.
Sperm Oil
SOI..Solublsinall proporlions Ins.. Insoluble (Tema = 75.n
Ins. Ins. Ins.
1Yo Sol.
Ins.
'AvsllablsfromDow
Solubility of Polyethylem,alycdr
In Vatlous 3dv.nt, Acetone
__
Benzene - _ Ether
Water
E3W
€400
E(W0
m
m
m
m
-
n-Heptane -- -Methanol
-
EZOO m
ElOOO ,100 >loo
E1450
E m
60
450
1460
io60
881
200
0470
PPG-24 Glycereth-24
9082-00-2
1122
4900
- 18'
20000
lcbo
445
60
455
1455
1028
856
200
0430
PPG-66 Glycereth-12
CAS # 53637-25-5
EP530 2000
- 32'
1450
321
168
25
>420
1452
1017
846
192
-
Poloxamer181
CASU
9003-13-8
1910
Polyglycol copdm
CASU
51258-15-2 CASU
a Designates properties not applicable lor solids b At 50' * Pour Point ' Cosmetrc Tortetry and Fragrance Association
Solubility of Additional Liquids in Polypropylene Glycols Appmxlmrta Solublllty, Volumo VO
Diethanolamine' Diethylene Glycol' EthyleneGlycol'
P425 ____-___ _ _ _ _ _P1200
Glycerine'
loo > 100 43 20
_'I
Not Iwnpleieiy miuble
___
Ins
= IrlmluMe
--___
rnm
12-18 1-7
12-18 1 --7 12--18 > 24 > 24 1 -7
80
0" 70 40 50
201' Ins
HLBa Value 25' C
- ..
1-7
-_
Glycol Ethers
623
GLYCERINE ETHERS Table 11.75: Glyceryl a-Monomethyl Ether (2) &-Monomethyl Ether of Glycerine
CH30CH2CHOHCH20H
Glyceryl %-monomethyl ether i s a colorless liquid, soluble i n benzene, ethyl alcohol, glycerol and water but insoluble i n gasoline and carbon tetrachloride. I t i s a solvent for rosin, and when mixed with butyl acetate i s compatible with nitrocellulose. I t may be used as a selective solvent and i n the manufacture o f alkyd resins.
90% between 21 5-220°C
Boiling range a t 745 mm Refractive index, n
2 5"
D
1.442
Specific gravity a t 25/25"C Weight per gal
1.1 147 9.29 Ib
Table 11.76: Glyceryl a,y-Dimethyl Ether (2) 0,y-Dimethyl
H3COC H2CHOHCH20CH3
Ether of Glycerine
Glycerine &,y-dimethyl ether i s a water-white liquid soluble i n benzene, gasoline, carbon tetrachloride, ethyl alcohol, water and glycerine, but insoluble i n linseed o i l and other fixed oils. I t i s a solvent for rosin, cellulose acetate and when mixed with butyl acetate i s compatible with nitrocellulose. I t has use as a solvent and plasticizer. Iloiliny r m g c :it i 3 6 n m .
90% between 164-liO"C
Spceilic gravity at 25/25'C Weight per @iI
1
.xu
8 36 11)s
Table 11.77: Glyceryl a-Mono-n-Butyl Ether (2) 9-Mono-n-Butyl
C4H90C H2C H O H C H 2 0H
Ether of Glycerine
a-Mono-n-butyl ether of glycerine i s a colorless liquid, soluble in benzene, gasoline, ethyl alcohol and carbon tetmchloride, but only slightly soluble i n water and glycerol. I t i s a solvent for rosin and ester gum and may be used i n the preparation o f varnishes made with these substances. I3oiling range e t 18 mrn. Refractive index, n
250 D
Specific gravity at 25/25'C Weight per gal
90% between 133-137'C 1.434
0.945 7 87 Ibs
Table 11.78: Glyceryl a-Monoisoamyl Ether (2) C5H,, OCH2CHOHCH20H
a-Monoisoamyl Ether of Glyceryl
a-Monoisoamyl ether o f glyceryl i s a colorless liquid which generally contains small amounts of other amyl isomers. I t i s soluble i n benzene, ethyl alcohol, halogenated hydrocarbons, carbon tetrachloride, gasoline, linseed oil, and other fixed oils and, i n certain amounts, soluble i n glycerol and water. I t i s a solvent for rosin and, when mixed with butyl acetate, i s compatible w i t h nitrocellulose. I t may be used as a solvent i n the preparation o f alkyd resins and in the synthesis of ester derivatives. Boiling range at 745 nun Refractive index, N
E D
Specific gravity at 25L2S.C Weight per gal
90% between 252-28o"C
.a
1
OS7
8.22 Ibs
624
Industrial Solvents Handbook Table 11.79: Glyceryl a,y-Diisoamyl Ether (2) a,Y-Diisoamyl
C5H1 ,0CH2CHOHCH20C5H,
Ether o f Glycerine
Glyceryl a,y-diisoamyl ether i s a water-white liquid which may contain small quantities o f other amyl isomers. I t i s soluble in ethyl alcohol, benzene, gasoline, carbon tetrachloride and linseed oil, but insoluble in water and glycerol. It i s a solvent for ester gum and rosin and has use as a solvent and plasticizer. Boiling range a t 10 mm
9% betwean
147-153'C
D
Refractive index, n 2.5.
1.m
Specific gravity at 2.5/25% Weight par gal
7.62 Ib
0.903
Table 11.80: Miscellaneous Glycerine Ethers (2) Glycerine ethers range widely from low-boiling liquids to high-boiling =lids. The solubility varies equally from complete water miscibility to complete water insolubility. The following l i s t s these glyceryl ethers with their density and boiling points.
Glyceryl- Ether u-Isoamyl n,
7-di-koamyl
-d
b.p. (or m.p.)
0.987:; 0.908:;
137-8. 251-In 147-53s
m
u-Benzyl
1.196::
lUst
a-n-Butyl
0.946;:
l23-7-
1.063
231% 190 103-58
Cresyl u-Ethyl u ,7-di-Ethyl
tri-Ethyl Epiethylin Glycidol u-Methyl @-Methyl U ,7-di-Methyl tri-Methyl Epimethylin mono--Naphthyl mono-@-Naphthyl u-Phenyl
0.92Ch 0.886': 0.941:
1.1143,' 1.1147:: 1.003;:
181n 128-9 41 I 1loll 221n 69.5-70.5tt 164-70,-
0.937*: l.oCa,
laen, 113-4no m.p. 91-2 m.p. 109.10 185-7,s 15044
m.p. 534 287-8 m.p. 80-1 m.p. 58 m.p. 76 m.p. 83 1156.4
U ,7-di-Phenyl
u-o-CI-Phenyl U-p-CI-Phenyl mon0-2,4-di-Nitrophenyl Epiphenylin
1.03s:
u-Propyl
1.W4'
U ,7-di-Isopropyl
0.915~
:
118-22,a 112-3
U , 7-di-n-Propyl
215-7
mono-p-To1yl
m.p. 734
"C.
Ketones
ACETONE CH 3 -CO -CH 3
Dimethyl Ketone, Methylacetyl, Propanone-2
Acetone is a colorless, limpid, mobile, h y g r o s c o p i c , flammable l i q u i d h a v i n g a mint-like o d o r .
Table 12.1: Physical Properties of Acetone (47) Typical Properties Molecular Weight Color ( P t C o Scale). max Weight!Vol. IOOC, Iblgal (U. S.) kgllitre lblgal (Imperial) Solubility, 20°C. wt ?? In water Water in Evaporation Rate (n-butyl acetate = 1) Dilution Ratio, toluene VM & P na.>htha Refractive index, 20°C Vapor Pressure, 20°C. mm Hg Specific Gravity 2Oo/2O0C
Table 12.2:
Boiling Range. 760 mm. "C Initial Boiling Point. min Dry Point, max Freezing Point. OF ("C) Flash Point. Tap. Closed Cup, OF ("C) Tag Open Cup, "F ("C) Fire Point. O F ("C) Flammable Limits in Air, o/c by volume Lower Upper Autoignition Temperature (ASTM D-2 1553, OF ("C) NFPA Classification 30 DOT Classification DOT Lahels Required
58.08 5 6.59 0.79 7.91
Complete Complete 7.7 4.6 0.55 1.3589 180 0.792
Low Temperature Characteristics of Aqueous Solutions of Acetone
625
(79)
55.1 57.1 -138 (-95) -4 (-20) -2(-19) -2 (-19) 2.6 12.8 1000 (538)
IB Flammable Liquid Flammable Liquid
626
Industrial Solvents Handbook
Table 12.3: Solubllity of Various Materials in Acetone (44) S0i.r
RILITY
UI
Superfine nrenge shellac Superfine shellac T \ shellac, \ o I T \ shellnr, \ o 2 4 C gnrnet Refus Inc
_-.- -
SHEI.I.UT IN ICETONE
------
-
1
---
-
\I*TPER
I'ER('K:IITAl.E OI' AC'KToSE I\nOl,l'Bl.K
98 8 02 8 05 6 0s 8 81 '3 G3 0
I
- --
ISIN IN^
IS \ a H i O L s
PER C E , ~I,V)L~QLI ACITOII
TYPE
I
K.iui1, pide l u u r i , brou n h.iuri, I,ush llosin Ilurguiidy pitch St oc I, holm t .ti \lilstlC Ruriilnrjc .\fnd.lg~lSCLlCOlJal, f U S d
i
1 '
Chiiianood oil Coconut oil (rehned and bleached) Corn oil ( r a a ) Cottonseed oil (rehiied and bleached) Cot tonseed oil (hydrogriiated, Crisco) Cot tonseed oil ( h j drogenated) Cottoosecd oil (stearin) Cottonseed 011 (summer) Cottonseed oil (\\inter) Fish oil (herring, titu) Fish oil (h~drogeiiated) Fmh o i l (menhaden. m u ) Grease, broun Grease. garbage Grease, n hite Ihnseed oil, ran
hl' M'
97 0
M-niiscible in all proportions. M'-miscible in coneentratcd solutions with separation on dilution. SOLUBILITY OF WSTM GU\IS I N
\CETOYE
PI.
SOLUBILITY OF
~
AsPHaLTs
AND
BITUMENS I N ACETONE
5.8 58.4 62.4 70.4 62.4
F a t t y acid pitch, medium grade Gilsonite selex Grahamite Mexican petroleum asphalt, steam-distilled. medium grade Mexican petroleum asphalt, steam distilled, soft grade Petroleum *asphalt. steam distilled, Californin, rnediuin grade Residual oil froin Gulf Coast Rcsidual oil from steani distillrtion of mid-continental
hl
M hi .\I
l.3 8 998 06 4 '99 6
m
rn
51
y~8 YJ 7
0i J
4 hf .\I-rniscihle 111 all proportions rn-pnrt soluble a t 25°C is miscible in all proportions.
Trinidad pitch, relined
1MI 095
030
E> 0.85 W
u
Y-
E
on 0.75
0.70 0
10
20
30
40
50
60
ACETONE, per clnt by night
70
80
54.3 25.0 1.6 44.2 64.3
81 .0 G1 0
97.2 5.9 42.0
Table 12.4: Specific Gravity of Aqueous Solutions of Acetone at Different Temperatures (79)
5
IOL"UI1LI A 7 BOILIN0 P O l h I 01 K I T O N E
YlXllllLtTI
I
i
czvr
Arabic gum Indian gum Senegal gum Tragacanth, Allepa Tragacanth, Persian Tragacanth. Turkey
--
TIP*
Congo Manila, soft Elemi Yncca Sandarac Sierra Leone Borneo pontianac Batavia dammar Red, accrodites
8 90 :I8 i o 20 i o SOlUl,lC Soluble Solut,le !I 50 Sulul,lr RI 80
.
SOLUBII.ITY O F COPALI ~ E S I N SI N ACETONE
-.
90
100
Ketones Table 12.5: Surface Tension of Aqueous Solutions of Acetone at 25°C (79)
80
70 60 Y) (v
bc
50
r
0
=- 40 E!
E 30
v)
W
u
,4 20 a a
cn
10 r r l r l t r l r r l l l l l l l l l
1 1 1 l 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 I I I I ' I i I I I l l 1I i l I
l~Ai-t-iI
0 0
10
20
30
I i I ' I i l I ' I
40
50 60 ACETONE, per cent by weight
70
80
I l l
90
100
Table 12.6: Viscosity of Aqueous Acetone Solutions at 25°C (79)
1.50
125 u 0
v) (v
c
m
v)-
1.oo
W
E
0
c
2
0.75
W
u
g v)
0.50
0
u II
>
0.25
0.o 0
10
20
30
40
50
60
ACETONE, per cent by weight
70
80
90
100
627
628
Industrial Solvents Handbook Table 12.7: Refractive Index of Aqueous Solutions of Acetone at 25°C (19)
..".
1.36
1.35
1.34
1.33
1.32
10
0
20
30
40
50
60
70
80
90
100
ACETONE, per cent by weight
Table 12.8: Liquid-Vapor Equilibria for Aqueous Solutions of Acetone at Different Pressures
100
98
96
94
92
90 80
82
84
86
88
90
92
94
ACETONE, mol per cent in liquid phase
96
98
100
Ketones Table 12.9: Freezing Point of Aqueous Solutions of Acetone (79) 100
E 80 D
i
0 -100
-90
-80
-70
-50
-60
-30
4 0
-20
0
-10
TEMPERATURE, "C
METHYL ETHYL KETONE CH 3-CO-C2H 5
MEK, Butanone-2, Ethyl Methyl Ketone Methyl ethyl ketone is a colorless, stable, mobile,
flammable liquid with an odor like acetone
Table 12.10: Physical Properties of Methyl Ethyl Ketone (2)
Azcolropic Mizlurer % by 11.
Methyl ethyl ketone
37.5 73 84.7 29 40
40 12 60 20 70 52 55 75 45
%by It.
B.P. ( '0
62.5 27 15.3 71 60 60 82 40
78.4 77.5 45.9 73.8 73.0 72.0 77.0 74.8 77.6 77.5 79.3 79.5 55.5 70
Benzene Lcrt-Butyl alcohol Carbon disulfide Carbon tetrachloride 1,3-Cyclohexadiene Cyclohexane Ethyl acetate Ethyl alcohol Ethyl sulfide bopropyl alcohol Methyl propionate Propyl formate Propyl mercaptan Thiophene
80 30 48 45 25 55
Ternary Miztures B.P. ('0
(1) Methyl ethyl ketone (2)
Upper layer of (2) Lower layer of (2)
22.2 17.8 19.0 3.5
Water
3.0 8.9 0.4 96.4
CCL, C,HI
74.8 73.8 80.0 0.1
Typical Propertier and Specifiatim Boiling point a t 760 mm 79.0'C 0.00076 per "F Coefficient of expamion Electrical Conductivity 1.0 x 10-' ohms a t 25% Explosive limits 1.97%-10.2% Flaah point (Tag Cloaed Cup) 257 Freesing point -88.40c Heat of combustion 582 Cal./mole Latent heat of Vaporization a t P'C 108.0 cal./g Refractive Index, N P / D 1.3788 Solubility of water in solvent at P*C 10% by wt. Specific gravity a t P / P 0 C 0.805-0.837 Specific heat 0.55 cal./g Surface tension 0°C 28.9 dynes/sq cm P 24.0 40 22.3 76 18.4 Viscosity a t 15'C 0.00123 poise Weight per gallon a t P'C 6.72 Ibs. Acidity (M acetic) 0.0025 by wt. (mu.) Distillation range (ASTM) m0a.5~c 3 mg. per 100 ml. ( m u . ) Non-volatile matter Purity W O
05.7 88.9
629
630
Industrial Solvents Handbook
Table 12.11: Methyl Ethyl Ketone and Water (74)
METHYL n-PROPYL KETONE
CH~*CO*CH~*C~HS
Pentanone-2
Commercial methyl n-propyl ketone, produced synthetically by dehydrogenation of the corresponding alcohol, consists of a mixture of methyl n-propyl and diethyl ketones i n the approximate ratio of 3 to 1, and contains at least 97% of these ketones, the balance being secondary amyl alcohol. It i s a colorless liquid, soluble i n alcohol and ether but only very slightly soluble i n water.
Table 12.12: Properties of Methyl n-Propyl Ketone (41)
Typical Propertie8
Molecular Weight (C,HloO) Branched-Cham Ketones, wl % (max) Color (Pt-Co Scale), max Evaporation Rate (n-butyl acetate = 1) Weight/Vol at 20°C Ib/gal ( U S ) kglL Ib/gal (Imperial) Solubility at 20°C. wt % I n water Water in Dilution Ratio. toluene VM 8 P naphtha Refractive Index at 20°C Vapor Pressure at 20°C. m m Hg
86 13 10 15 23
6 72 0 81 8 06 31 42 39 10 1 3904
27 8
0 807 Specific Gravity at 20°/20'C Boiling Range at 760 rnm " C 101 Initial Boiling Point m i n 105 Dry Point. max -122 (-86) Freezing Point. 'F ( " C ) Flash Point. Tag Closed Cup, 'F ("C) 46 (8) 50 (10) Tag Open Cup, OF ('C) 50 (10) Fire Point O F ("C) Flammable Limits i n Air. 46 by volume 1 56 Lower, at 94OF (34°C) 8.7 Upper, at 1 4 4 O F (62°C) 840 (449) Autoignition Temperature (ASTM D 2155) OF ('C) IB NFPA Classification 30 DOT Classification Flammable Liquid Flammable Liquid DOT Labels Required
(continued)
Ketones
631
Table 12.12: (continued) Cornpariron of Solvent Power MPK vs Other Solvents
I
I
lsopropyl Acetatea
Solution Viscositv at 25°C. eP ImPa
'
25
I
. si
I
31.0
6.6
22.8
MEK
14
18.8
3.6
MPK~
16
20.8
4.5
31.5
MIE~K~
23
27.0
5.8
59.2
"an Eastman product bproduct of Du f o n t Company 'product of Uruon Carbide Corporation
METHYL n-BUTYL KETONE Hexanone-2
CH3 * C O eC4Hg
Methyl n-butyl ketone i s a colorless liquid, freely soluble i n alcohol and ether but very slightly soluble i n water.
Table 12.13: Properties of Methyl n-Butyl Ketone (41) Molecular Weight (C,H, ? O ) Melting Point, "C Boiling Point, "C, 760 mm Evaporation Rate (n-butyl acetate = I ) Weight/Vol, at 20°C Ib/gal. (U.S.) kg/liter Ib/gal. (Imperial) Solubility, 20"C, wt % In water Water in Dilution Ratio, toluene VM & P naphtha Color (Pt-Co Scale), ppm Acidity, as acetic acid, wt %
Water, w t % Branched-Chain Ketones, max, wt % Refractive Index, 20°C Flash Point (Tag Closed Cup), "F ("C) (Tag Open Cup), "F ("C) Fire Point, " F ("C) Flammable Limits in Air, % b y volume Lower Upper Autoignition Temperature (ASTM D-2 1 55), "F ("C) NFPA Classification 30:
100.16 -56.9 127 1 .o
6.75 0.8 1 8.10 1.4 2.1 4.0 1.1 5 0.0 1
ICC Labels Required Bureau of Explosives Classification
0.05 5 1.3969 77 (25) 83 (28)
86
1.3 8.0 795 (424) Flammable Liquid, Class IC None Nonhazardous Liquid
Several of the solvent characteristics of Methyl n-Butyl Ketone are listed in the following table. Similar values for other solvents are incluhed for comparison. Solution Viscosity. 25'C. cp
Eastman Solvent
Methyl n.Butyl Ketone
Blush Res., % R.H. @ 80'~ ( 2 7 0 ~ )
Evap.
Rate
I
10
I
I
1.4
I
~
'product of Hercules, Inc. 'prwluct of Firestone Plasrics Cb.
RS. 'h-Sec
~~~
8
m
0
7
Exonb
(30)
Elwire'
Cellulose Nitratea 10 wt x -~
470
2010
Zowtx
2Owt9L
2a
24
65
49
38
83
Cproducrof E, I. du Pont de Nemourr Co., Inc.
632
Industrial Solvents Handbook
Table 12.14: Solubility of Dry Half-Second R.S. Nitrocellulose in a System of Methyl Butyl Ketone-secButanol-Toluene (2)
METHYL ISOBUTYL KETONE Hexone, 4-Methylpentanone-2,
2-Methyl-4-Pentanone
CH3 * CO * C4H9
Although first prepared i n 1849, methyl isobutyl ketone was not made synthetically and on a large scale until the last decades. It i s a stable, colorless liquid classified as a medium boiler. It i s miscible with most organic solvents and with mineral and vegetable oils. When compared with butyl acetate its rate of evaporation i s somewhat faster so that i t can either replace esters or be combined with them. Its rate of evaporation i s somewhat faster than that o f butyl acetate. It i s used i n the vinyl type resins for coatings where i t helps to prevent gelling and lowers viscosity, i n nitrocellulose lacquer manufacture, i n extraction processes and i n chemical synthesis. It moy be used i n dewaxing oils.
Table 12.15: Properties of Methyl Isobutyl Ketone (47) Typical Properties Molecular Weight (C6H110) Color (Pt-Co Scale) max Weight/Vol at 20'C Ib/gal (U S ) kg/L Ib/gal (Imperial) Solubility at 2O'C wt % In water Water in Evaporation Rate (n-butyl acetate = 1) Dilution Ratio toluene VM a P naphtha Refractive Index at 20°C Vapor Pressure at 20°C mm Hg Specific Gravity at 20'/20°C Boiling Range at 760 mm " C Initial Boiling Point min Dry Point max Freezing Point. OF ( " C ) Flash Point Tag Closed Cup OF ("C) Tag Open Cup "F ("C) Fire Point OF ("C) Flammable Limits i n Air % by volume Lower at 200°F (93°C) Upper at 200'F (93°C) Autoignition Temperature (ASTM D-2155) OF ("C) NFPA Classification 30 DOT Classification DOT Labels Required
100 16 10
6 67 0 80 8 00
20 10 16 35 10 13958 15 0 802
114 117 -1 19 (-84) 60 (16) 68 (20) 70 (21) 122 7 96 840 (449)
IB Flammable Liquid Flammable Liquid
(continued1
Ketones Table 12.15: (continued)
Solution Viscosity at 25°C. CP (rnPa.9
FPC 470 Resin" 20 W t / %
Elvacrte 2010 Resfin' 20 Wt/%
30
24
80
49
38
64 83
83
46
33
77
Evap Rate
Blush Res 40 R H @ 8O'F (27°C)
RS '?-Set Cellulose Nitrate'
Methyl Isobutyl Ketone
16
78
lsobulyl Acetate
14
n-Butyl Acetate
10
Eastman Solvent
10 wt
L;
'Product of Hercules Incorporated 'Product of firestone Plastrcs Company Product of Du Pont Company
Table 12.16: Solubility of Miscellaneous Materials in Methyl Isobutyl Ketone at 20" to 25°C (2)
Acid Oleic (Technical Red Oil)
Gums Elemi Kauri (Pale Bold) Mastic Pontianak
Oils Castor, Refined Raw Cottonseed, Raw China Wood Coconut, Crude Fish, Processed Linseed, Purc Raw Mineral, 70f80 viscosity Pine Soybean, 2-3 viscosity
Resins, Natural Dammar (dewaxed) Batavia Singapore Light Rosin Sandarac
.--
Tmde N m r
-
'PYP
Modified drying type phthalic alkyd Ainterlac 80-X.. . . . . . Rosin modified maleic alkyd Amberol 801 Modified maleic Arochem 519 . . . .. Aroclor 1260 . . . . Chlorinated diphenyl Non-heat-hardening 100% para-phenylphenol resin askelite UR-254 ., Phenolic modified drying type alkyd No. 1 Solid I3eckosol Beckosol 1313. . . . . Drying type alkyd Beetle 2274.. . . . . Unmodified urea-formaldehyde Modified rosin ester Cellolyn 102 . . , , , . Rosin ester Ester gum. ...... Ethyl methacrylate . . . . . Acrylic ester Non-drying type alkyd Glyptal 2477 Melmac 245-8 . , . . , , Unmodified melamine-formaldehyde Neville R-21 (soft) . Unmodified coumaroneindene Naphthene polymers Nevillite 1 . . . . Nitrocellulose.. . . . . . . . . Cellulose rater Parlon X (ZO c p . ) . . . . . . Chlorinated rubber Phenac €48.. . . . . . . Modified phenolic Santolite K... . . . . . . . Alkyl-arybulfonamide-formaldehyde Saran F-120 . . . . . . . . . . . . Vinylidenechloride-acrylonitrilecopolymem Staybelite . , . . , . , . , . , . . , Hydrogenated rosin ester Teglac 2-152. . . . . . . . . . . . Roain modified maleic alkyd Vinylite AYAF. . . . . . . . . Polyvinyl acetate Vinylite VMCH.. , . , . . , . . Maleic modified vinyl chloride-vinyl acetats COpOlYmer8 Vinvlite VYHH. . . . . . . . . . . Vinyl chloride-vinyl acetats copolymera
633
634
Industrial Solvents Handbook
METHYL n-AMYL KETONE CH3(CH2)4-C0*CH3
Heptonone -2
This ketone is o colorless, stable liquid, miscible with most lacquer solvents ond only very slightly soluble i n water. It i s used as a high-boiling solvent for nitrocellulose and i s particularly applicable i n vinyl resin finishes, where its slow rate o f evaporotion prevents quick drying, improves the flow and gives blush resistance; also used with some effect i n insecticidal preparations.
Table 12.17: Properties of Methyl n-Amyl Ketone (47) Typical Properties
114.19 20
Molecular Welplit (C, H,,O) BrancliedChain Ketones wt % max Color ( P I C OScale), max Evaporation Rate (n-butb I acetate = 1) W e i g h t i ~ o at ~ . zoOc lbinal (L S 1 kg!L Ib/gal (Imperial) blubilit) at ?O°C, wt :: In water Water in Dilution Ratio, toluene VM & P naphtha Refracti*e Index at ZO'C Vapor Pressure at ?O°C. mm Hg
IO 0.4 6.80 0.81 8 16 0.46 1.31 3.9 1.? I.4085 2.14
Specific Cram[\ at 2O0/2O0C Boiling Range at 760 rnrn OC Initial Boiling Pomr min Dr! Pomt max Freezing Point "F e C ) Flash Point, Tap Closed Cup "F ("0 Tap Opeii Cup "F ("C) Fire Point 'F C C ) Flammable Limits in Air,% by volume Louer, at I SOOF (66'C) Upper,at 2SO'F (12I'C) Autoignition Temperature (ASTM D 215S), 'F ('C) NFPA Classification 30 DOT C l a d i c a t i o n DOT Labels Required
0817 149 153.5 -27 (-33) I O ? (39) 114 (46) 115 (46)
I I1 19
740 (393) I1 Combustible Liquid None
COMPARISON OF PROPERTIES OF HIGH-BOILING SOLVENTS
'product of Hercules Incorporated
Eastman pmducr
'prcducr of Union Carbide Curpmrron
METHYL ISOAMYL KETONE CH3-CO-CsH 1 1
MlAK
M l A K i s a retarder solvent, having an evaporation rate o f 0.5, but i t olso possesses exceptional solvent power for most film-formers. In lacquers, the low evaporation rate of MlAK promotes good flow ond leveling properties; whereas the high solvency provides low viscosities or permits a higher nonvolatile content.
Table 12.18: Properties of Methyl Isoamyl Ketone (47) Typical Properties Molecular Weight (C, H,.,O) Color ( p t C o Scale), max WeightNol, 20°C. Ib/gal (U. S.) kdlitre Iblgal (Imperial) Solubility. 2OoC, wt R I n water Water in Evaporation Rate (n-butyl a e t a t e = I ) Dilution Ratio. toluene VM & P naphtha Refractive Index. 20°C Vapor Pressure. 20°C, mm Hg Specific Gravity, 20"/20"C
114.19 10 6.76 0.8 1 8.14
0.5 1.2 0.5 4.1 I .2 1.4069 4.5 0.81 4
Boding Range, 760 mm, "C Initial Boiling Point, min Dry Point. max Freezing Point. "F e C ) Flash Point. Tag Closed Cup, "F ("C) Tag Open Cup, "F ("C) Fue Point, OF e C ) Flammable Limts in Air, R by volume Lower, at Z W F ( W c ) Upper, at ZOOOF (93°C) Autoignition Temperature (ASTM D-ZISS), O F ("C) NFPA Classification 30 DOT Classification DOT Labels Required
141 148 -101 (-74)
9 6 (36) 106(41) 107 (42) 1 .os
8.2 795 (425) IC Flammable Liquid Flammable L q u d
(continued)
Ketones
635
Table 12.18: (continued)
I
1 1
Solvent
Methyl Amyl Acetate
1
92 89 92 e4
0.5 0.5 0.4 0.2
Methyl Isoamyl Ketone Isobutyl lsobutyrate Ektarolvea EE Acetate
I
%R.H.@ RS k-Sec 80"~ ( 2 7 " ~ ) Cellulose Nitratel 10 W/%
FPC 470 Resinb
20Wt/%
128 42 128 113
I
Elvacire 2010 ResinC 2OWt/%
lnsol
lnsol
34
68
lnsol
Ins01 284
lnsol
I
,
'product of Hercules Incorporated 'product of Firestone Pksrics C0rnpzn.v Cproducr of Du Ponr Company
Table 12.19: Propertles of Methyl Isoamyl Ketone vs Other Solvents (47) Flash
Bodma
Tag Point. Open Cup, *F.
160 RanKO. mm..
Blush
Specdoc
Rate
ootutoon Ratm (Tolucnel
Methyl isobutyl ketone
1.6
3.6
08018
14
2.7
0.8728
73 90
114-117
Isobutyl acetate n-Butyl acetate
1.0
2.7
0.8109
100
116-118
Amyl acetate
0.6
2.4
0.862
93
100-150
MlAK
0.50
4.1
0.813
110
141-148
Methyl amyl acetate
0.5
1.7
0.8595
110
143-150
2-Ethoxyethanol 4-Methoxy-4-methylpentanone-2
0.3
4.9
0.931 1
130
132-136
0.3
3.1
0.904
141
147-163
Ethyl amyl ketone 2-Ethoxyethyl acetate 4-Methoxy-4-methylpentanol-2
0.2
22
94
0.822
135
156-162
0.2
2.5
91
0.9748
150
145-165
0.2
4.7
93
0.890
140
164-169
Cyclohexanone
0.2
5.8
92
0.945
129
153-160
2-Butoxyet hanol
0.06
3.33
96
0.9019
165
166-173
lsophorone
0.03
6.2
97
0.9229
205
205-220
Evaporation Solvent
Cravsty.
% R.H. a t
20IZO~C.
,
'C.
114-118
Table 12.20: Butyrate-Acrylic Wood Lacquer-Substltutlng Isoamyl Ketone for 2-Ethoxyethyl Acetate (4 7)
InKredlentr
Half-Second Butyrate
. . . . . . . . . . . . . .
Part A
Part e
wt.
wt. K
K
8.5
8.5
Acryloid 8-66 resin (40%)'
. . . . . . . . . . . . . 21.3
21.3
Santicizer 160 plasticizer'
. . . . . . . . . . . .
3.0
3.0
. . . . . . . . . .
0.01
0.01
Dow-Corning 510 (1000 cs.) fluid' Eastman lnhibttor DOBP'
.
.
.
.
.
.
.
.
Isobutyl acetate Isobutyl alcohol
.
.
0.09
0.09
26.3
36.3
. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
13.6
13.6
13.6
3.6
. . . . . . . . . . . . . .
6.8
6.8
Methyl ethyl ketone
. . . . . . . . . . . . . . . . . . . . . . . . . . .
MlAK
.
. . . . . . . . . . . . . . . . . .
Toluene
6.aA
-
7.45
7.51
I
6.8
2-Ethoxyethyl acetate
. . . . . . . . . . . . . . .
Solids.%
VISCOSlty, cp. Wt./gal., Ib. Flow out
. . . . . . . . . . . . . . . . . . . . . . . . . . . .
. . . . . . . . . . . . . . .
*Product of Rohm and Haas Company *Product of Monsanto Chernocal Company
*Product of Vow Corning Corporatoon ~2-Uydroxy-4-dodecylorybenzophenone
7.50
636
Industrial Solvents Handbook
METHYL HEXYL KETONE CH3(CH2)5CO *CH3
O c tanone-2
A colorless liquid with a characteristic odor, methyl hexyl ketone i s used as a solvent for vinyl compounds and dyes, and has been found particularly suitable i n dispersing dyes i n l i g h t petroleum oils for newsprint inks.
Table 12.21: Properties of Methyl Hexyl Ketone (2) Purity
95%, min.
Specific gravity at 20°C.
0.81 -0.83
Weight per gallon at 20°C.
6-8 Ibs
.
METHYL HEPTYL KETONE MHK 5-Methyl-2-Octanane M e t h y l heptyl ketone, a high-boiling, high-temperature baked coatings.
active solvent, imparts desirable drying characteristics i n rnony
Table 12.22: Properties of Methyl Heptyl Ketone (47) Molecular Weight (C, HI,0),calcd Melting Point. "C Boiling Range, "C, 760 mni Evaporation Rate (n-butyl acetate = I Weight/Vol. a t ?O°C Ib/gal (U.S.) kg/liter Ib/gal (Imperial) Solubility, 20°C. wt '2 In water Water in Dilution Ratio, toluene VM & P naphtha Refractive Index, 20°C
I MAK
142.24
-9 )'
183-195 0.08 6.87 0.83 8.59
0.5 0.95 3.0 1 .o
MHK
lsophorone
-
ICC Labels Required Bureau of Explosives Classification
1.422
! I EKTASOLVE@€BSolvent' I
Color (Pt-Co Scale), ppm Acidity, as acetic acid, wt 7r Water, wt % Flash Point (Tag Closed Cup), " F ("C) (Tag Open Cup), "F ("C) Fire Point, "F ("C) Flammable Limits in Air, % by volume Lower (at 180°F) Upper (at 3 13'F) Autoignition Temperature (ASTM D-2155), "F ("C) NFPA Classification 30:
0.4 0.1
1 1
3.9
I
1.2
3.4
I
2.1
0.08
3.0
0.03
6.2
I I
93 96
1 I
-F$ :; I
1.0
0.815 0.902
1 I
5-25 0.018 0.01-0.05 140 (60) I60 (71) I68 (76)
0.9 5.9 680 (360) Combustible Liquid, Class IIlA None Nonhazardous Liquid
6.80
I
7.51
I
0.827
6.87
0.922
7.68
Ketones
637
ETHYLBUTYLKETONE Heptanone -3 Ethylbutyl ketone is a stable, high-boiling solvent of special value in lacquers and synthetic resin coatings. Its evaporation rate i n relation to those of comparable solvents i s indicated i n the following tabulation: Solvent
Hours -
Methyl isobutyl ketone Butyl acetate Ethylbutyl ketone Amyl acetate Methylamyl acetate Methylamyl ketone "Ce IIosolve " acetate Diisobutyl ketone
4.5 8 14 16
17 20 38 44
The unusual combination of good solvent power with medium evaporation rate makes ethylbutyl ketone generally useful for coating solutions having adequate flow without unduly long drying time. It bakes out of films somewhat faster than other comparable ketones.
Table 12.23: Properties of Ethylbutyl Ketone (2) Boiling point Freezing point Coefficient of expansion at 20°C. Flash point Solubility i n water at 20°C. Solubility of water in at 20°C. Refractive index a t 20°C. Specific gravity at 2O/2Ooc.
147.8"C.
-36.7"C. 0.00107 125°F. 0.43% by wt. 0.78% by wt. 1.4085 0.8197
ETHYL AMYL KETONE EAK, 5-Methyl-3-Heptanone Ethyl amyl ketone, a high boiling ketone, is a colorless, stable liquid with a mild pleasant odor It is compatible with alcohols, ethers, other ketones and organic liquids. and in addition, exhiblts low water miscibility Ethyl amyl ketone's high solvency for cellulose esters, vinyl polymers
and copolymers, synthetic and natural protective coating resins, coupled with its slow evaporation rate, high blush resistance and good diluent tolerance makes i t a valued surface coating raw material
Table 12.24: Properties of Ethyl Amyl Ketone (14) Apparent specific gravity 20120'C 25125'C Color PI-Co Max Dis!illation range 'C
0 8250 824 0 816-0 820 25 156-162
Acidity (as acetx accd) % w Max Water % w Max Alcohol (as ethyl amyl carbinol) % w M a x
0 01 0 15 0 50
638
Industrial Solvents Handbook
DI-n-PROPYL KETONE Heptanone-4,
Butyrone, Amyl Ketone
(CH3CH2CH2)2CO
Di-n-propyl ketone i s a colorless, stable liquid having o pleasant odor. It i s miscible with many orgonic solvents, and dissolves a wide variety o f materials, some o f which are crude rubber, nitrocellulose, row and blown oils, many natural and synthetic resins l i k e dewaxed dammar, manila, rosin, ester gum, and waxes.
Table 12.25: Properties of Di-n-Propyl Ketone (2) Boiling point Coefficient of expansion
143.7"C. 0.001073 (per "C.) to 20°C. 0.001115 (per "C.) to 55°C. 0.8 3.1 49°C. -32.1 "C 1051 cal ./mol 75.8 cat ./g. 0.53% by w t , 1.27% by w t . 0.8162 1.4068 0.553 cal./g. 25.2 dynes/sq cm. 5.2 mm. Hg 0.0074 poise 6.79 Ibs.
Dilution ratio ("Kemsolene ") (Toluene) Flash point (ASTM Open Cup) Freezing point Heat o f combustion Latent heat o f voporization Solubility in water at 20°C. Solubility of water i n solvent at 20°C Specific gravity at 20/20°C. Refractive index o t 20°C. Specific heat at 25°C. Surface tension at 25°C. Vapor pressure a t 20°C. Viscosity a t 20°C. Weight per gallon at 20°C.
.
.
DIISOBUTYL KETONE Valerone
(C4H9)2CO
A water-white, stable liquid, miscible with most organic liquids, diisobutyl ketone has good solvency for cellulose acetate, nitrocellulose, vinyl resins, waxes, gums, natural and synthetic resins, and crude rubber. It i s used principally as a high-boiler i n nitrocellulose lacquers and vinyl resin coatings, where i t s slow evaporation rate i s advantageous.
Table 12.26: Properties of Diisobutyl Ketone (47) Typical Propertig
MoleculPr Weight (C,HI,O) Color (Ptco Scale), m Evaporation Rate (n.buty1 acelate = 1) WeIght/Vol. 20°C. Ib/gal (U. S.) kg/liter lb/gal (Imperial) Solubility, 20°C. wt W In water Water m Dilution Ratio. toluene VM & P Mphthr Refractive Index, 20'C Vapor Pressure. 2OoC, mm Hg Specific Gravity. W/2O0C
142.23
20 0.2 6.76 0.81 8.1 1 0.05
0.75 1 .5
0.8 1.4230 1.7 0.8070.814
Boding Range, 760 mm, 'C initla1 BoJmg Pomt, nun Dry Point, mu Freezlng Point. "F CC) Flash Point, Tag Closed Cup, "F CC) Tag Open Cup. 'F CC) Fue Pomt,"F CC) Flammable Lirmts m Au, 'k by wlume Lower, at 2OO"F (93OC) Upper, at 2OO'F (93OC) Autorgnitlon Temperature (ASTM D-2155).'F CC) NFPA Classificatlon 30 DOT Clasufrcation DOT Labels Required
163 173 4 3 (-42) 120 (49) 131 ( 5 5 ) 137 (58) 0.81 7.1 745 (396)
II Combustible Liquid None
(continued)
Ketones
639
Table 12.26: (continued)
I
I
E"ep
Solvent Rate
I
"."^.
..--,
$R.H Q WF (27'C)
I
I
Solution Vtrositv. 25°C. CP
RS
%-%C
cellulose Nitrate, 10 Wtl%
FPC 470 Resin'. X)Wt%
Ehcire
2010 Resinb. 2OW%
Methvl 1oamvI Ketone
0.5
89
50
34
68
Methyl Amyl Acetate
0.5
92
128
lnwl
lnsol
lmbutyl Isobutvrate
0.4
92
128
lnsol
lnwl
Diiobutvl Ketone
0.2
95
160
75
lnwl
J
CYCLOHEXANONE
"Sextone",
"Anon", Pimelin Ketone, Keto Hexamethylene
Cyclohexanone i s a colorless to pale yellow, stable liquid with an odor suggestive of peppermint. It is made by the dehydrogenotion of cyclohexanol. It i s miscible i n a l l proportions with most solvents, especially the common lacquer solvents and diluents, hydrogenated and chlorinated hydrocarbons, phenols, pyridine, and turpentine. It i s a good solvent for cellulose ethers, esters, basic dyes, latex, fats, blown oils, waxes, crude rubber, and such gums and resins as ester gum, alkyds, vinyls, coumarone, 100% and modified phenol resins, cyclohexanone resins and many natural resins. It forms constant-boiling mixtures with camphor, tetrachloroethane, and trichloropropane. It has a very high dilution ratio os compared with the coal-tar hydrocarbons, a fact which accounts for its excellence as o solvent, especially i n the lacquer industry. Its low rate of evaporation and strong solvent powers impart blush resistance, good flow and working qualities to lacquers and give films that are clear, smooth and glossy and show good adhesion. It is also used i n spraying and brushing lacquers and as a medium boiler. It i s particularly effective for blending nitrocellulose with spirit-soluble and hydrocarbon-soluble resins and oils. Its solvency for basic dyes makes i t applicable i n wood stains. Other uses are i n the a i r d r y i n g and stoving type of synthetic resins, i n plastics and molding powders, i n paint and varnish removers, i n spot and stain removers, i n metaldegreasing preparations, i n polishes, printing inks, as a leveling agent i n dyeing, i n delustering cellulose acetate, insecticides and pharmaceuticals.
Table 12.27: Properties of Cyclohexanone (2)
Boiling point Color Dielectric constant at 25OC. Evaporation rate, approximate (toluene= 100) Flash point (open cup) Freezing point Solubility i n water at 2OOC. Specific gravity at 2OOC. Specific heat 15' to 18°C. Refractive index Viscosity (SUV at 1OOOF.) Weight per gallon a t 20°C. Acidity Distillation range Purity Residue Water content
155.6"C. Waterwhite to pale yellow
18.2 20 130OF. -45OC. 8.7%
0.944-0.950 0.433 cal ,/g. 1.443 1.451 33 7.9 Ib.
-
Neutral 95% within
-
98 1OOYo
0.02% 0.2% max.
151°-1570C.
640
Industrial Solvents Handbook
Table 12.28: Resin Solubility in Cyclohexanone (79)
Resin
Acrylic ”Acryloid” 8-82 ”Elvocite” 2010 Cel lulos i c s Cellulose Acetote AB-141-95 (14% ocet.yl) Cellulose Acetate Butyrate €AB-171-2 (17% butyryl) Ce Ilu lose Acetate Butyrote EAB-381-20 (37% butyryl) Ethyl Cellulose (N-22, 24 sec.) Half Second Butyrate AB-H “Hercose” “C” Type A Nitrocellulose fRS 1’2 sec.)
Rohm 8 Hoos DuPont
2 7
32 54
Eostmon
9200
28
6.5
Eostmon
892
34
9.5
Eostmon Hercules Eostmon Hercules Hercules
5060 1408 242 806 218
>50 \50 > 50 38
>50
14 23 17 8.5 10.5
96 19
M > 50
24 14 5
> 50 > 50
7 14 5
21
65
Styrene
Polystyrene Sh4A 4000A Vinyl BAKELITE Vinyl Resin AYAF BAKELITE Vinyl Resin VYHH BAKELITE Vinyl Resin XYHL “Soron” F-120 (1000 cps ) EPOXY BAKELITE Epoxy Resin EKR 2002 Urethane ”Estone” 5701F1 “Estone” 5707Fl Rosin-Ester “Amberol” 801 L T “Cellolyn“ 104 Melamine-Formoldehyde “Cvmel” 300 Alkyd “Beckosol” li 7 “Beckosol” $31 Rubber “Porlon” S-20 (18 cps.) ”Pliolite” 5-5 Phenolic BAKELITE Phenolic Resin BKR 2620 Phenoxy BAKELITE Phenoxy Resin PKHH (1)
IC
-Sincloir
ucc ucc ucc Dow
74 68 (3) 484
UCC
21
> 50
95
282 388
14
45 2
Rohm 8 Hoos Hercules
14 20
> 50 >50
19 50
>50
Reichhold Reichhold
28 25
>M
>50
47 >50
Hercules Goodyeor
46 56
>50
UCC
23
16
5.5
-
-
Goodrich Goodrich
ucc
g r o m r r e s i n , 90 grams cyclohexanone
(2) 10 grams o f 10% r e s i n (3) Partially soluble
solution, tatrated w i t h dilusnt (en m l )
Insoluble
-
6
>H)
-
22 30
Ketones
641
METHYLCYCLOHEXANONE Methyl "Anon",
"Sextone"
B
Meta
Para
Methyl cyclohexanone i s a woter-white to pale yellow liquid with an acetone-like odor. I t i s a mixture of two isomeric cyclic ketones made by the dehydrogenation of methyl cyclohexanol It closely resembles cyclohexanone i n its physical properties, miscibility, tolerance for non-solvents and solvent action. It differs from cyclohexanone i n its somewhat slower evaporation rate and lower dilution ratios with aromatic hydrocarbons. Methyl cyclohexanone i s especially suitable for phenolic and alkyd resins, crude rubber, nitrocellulose, ester gum and kauri. It i s also an excellent agent for blending pyroxylin with resins, oils and rubber i n lacquers. It i s used i n crystalizing lacquers, where i t s low evaporation rate retards evaporation sufficiently to permit crystal growth. It i s also used i n slow-setting varnish removers and i n rubber cements.
.
Table 12.29: Properties of Methyl Cyclohexanone (2) Boiling paint Evaporation rate (approximate) (toluene= Flash paint Freezing point Refractive index at 25°C. Solubility in water at 20°C. Specific gravity at 25/4"C. Viscosity (SUV a t 100°F.) Weight per gallon Distillation range Purity Residue Water content
-
100)
169.0" 170.5"C. 20 53°C. -70°C. 1.442 1.446 2 -3% 0.91 0- 0.914 33 7.6 Ibs. 165.0" 172°C. 95% distills within 3.0" 98 100%
-
-
-
None
0.2%, max.
METHYL ACETONE Methyl Ketone Methyl acetone i s a clear, colorless, flammable, volatile liquid, obtained from the product of the destructive distillation of wood. Although i t varies i n composition i t i s generally composed of acetone 35 to 60%, methanol 20 to 40%, and m t h y l acetate 20 to 30%.
642
Industrial Solvents Handbook
DIACETONE ALCOHOL Diacetone 4-H ydrox y -4-Me thy1pentanone-2 "Pyranton A " Diacetonyl Alcohol
OH
0
II
I I
CK-C-CH~-C-CHI CIq
Diacetane alcohol i s a flammable liquid that i s colorless when pure, becoming yellow on aging; i t has a mint-like odor. Made by the condensation o f acetone, the commercial product contains up to 15% of acetone. For this reason the technical product i s superior i n its solvent power to the acetone-free grade. It i s miscible with most organic liquids, os well as with water. It i s a good solvent for cellulose acetate, nitrocellulose, cellulose acetobutyrate, cellulose ocetopropionate, hydrocarbons, oi Is, fats, resins, gums and dyes. It has only limited solvency for dammar gum, polyvinyl acetate and the petroleum resins. A high-bailing solvent, diacetone alcohol also exhibits the desirable properties of reducing the viscosities of organic solutions o f high solids content, and of minimizing temperature effects an viscosities. In most respects i t i s quite similar to acetone with the exception o f a very much slower rate o f evaporation It i s used i n cellulose ester lacquers, particularly o f the brushing type, where i t produces brilliant gloss and hard film and where its lack of odor i s desirable. It i s used i n lacquer thinners, dopes, wood stains, wood preservatives and printing pastes; i n coating compositions for paper and textiles; i n making artificial silk and leather; i n imitation gold leaf; i n celluloid cements; as a preservative for animal tissue; i n metalcleaning compounds; i n the manufacture o f photographic film; and i n hydraulic brake fluids, where i t i s usually mixed with an equal volume of castor oil Diacetone alcohol i s available i n two grades: technical, containing up to 15% acetone, and acetone-free.
Table 12.30: Physical Properties of Acetone-Free Diacetone Alcohol (2) Boiling point at 760 mm. Coefficient of expansion (Cubical) Co Ior Flash point (open cup) Heat o f combustion Melting point Specific gravity at 2O/2OoC. Refractive index a t 20°C. Viscosity (Soybolt) 11 3 seconds at 674 seconds at 1,980 seconds at Weight per gallon at 20°C. Acidity (as acetic) Distillation range a t 760 mm. Below 135°C. Below 158°C. Above 170°C. Nonvolatile matter
167.9"C.
0.000533 per
OF.
Water-white to light straw
144°F. 8,601 cal ./g
.
-47°C. 0.937 0.946 1.4235
-
-1 2°C. -30°C. -48°C.
7.83 Ibs. 0.05% None N o t more than 5% None 0.005% by wt. (max.)
ACETONYL ACETONE Hexanedione-2,5
(CH3 *CO'CH2)2
Acetonyl acetone, a diketone, i s a water-white liquid with an agreeable odor. It i s completely soluble in water, almost entirely soluble i n such substances as toluene, kauri gum and rosin, and only partly soluble i n raw linseed oil, shellac, dewaxed dammar and ester gum. It has been suggested as an intermediate i n the manufacture of rubber accelerators, dyes, inhibitors, insecticides, and pharmaceuticals and for the preparatic of derivatives of thiophene, furan and pyrrole. It may also be employed i n tanning hides and skins.
Ketones Table 12.31: Properties of Acetonyl Acetone (2) Boiling point Dilution ratio (xylene) Flash point Specific gravity at 2O/2OoC. Solubility in water at 20°C. Vapor pressure at 20°C. Weight per gallon at 20°C. Acidity (as acetic) Boiling range at 760 mm. Purity Water
191.4"C. 1.8 158°F. 0.971 0 0.9760 Complete 0.5 mm. Hg 8.10 Ibs. 0.020% by wt., mox. 185" to 195°C. 98.0% by wt., min. Miscible with 19 vol. 60" BL gasoline at 20°C.
-
MESITYL OXIDE 4-Methyl -3-Pentenone-2 Isopropylidone Acetone Methyl lsobutenyl Ketone
(CH3)2C=CH .CO* CH3
Mesityl oxide i s an unsaturated, medium-boiling ketone made by the dehydration of diacetone alcohol. It i s a colorless to strawyellow, oily liquid with a peppermint-like odor. It w i l l darken and form a solid residue on exposure and aging. It is miscible with most organic liquids and i t i s a good solvent for such substances as nitrocellulose, ethylcellulose, low-viscosity cellulose acetate, polyvinyl chloride, vinyl resins, hydrocarbons, raw linseed oil, kauri gum, rosin, ester gum and synthetic rubber. It w i l l only partly dissolve shellac and dewaxed dammar. Mesityl oxide i s used in lacquers and thinners where i t s presence in the solution lowers the viscosity and gives i t both a high tolerance for hydrocarbons and resistance to humidity. Its excellent solvent power for gums and resins i s especially applicable i n vinyl-type resins, where i t produces f i l m that are tough, glossy and hove good flow; i t s presence permits use of larger proportions of aromatic hydrocarbon diluents.
Table 12.32: Properties of Mesityl Oxide (2) Boiling point at 760 mm. Coefficient of expansion Color Dielectric constant at 20°C. Flash point (Tag closed cup) Heat of combustion Heat of vaporization Melting point Solubility in water at 25°C. Solubility of water in solvent at 20°C. Specific gravity at 20/20°C. Specific heat (21 121"C .) Refractive index at 20°C. Vapor pressure at 20°C. 30°C. 40°C. Viscosity at 25°C. Weight per gallon at 2OOC. Acidity (as acetic) Distillation range (ASTM)
-
Purity Water
129.5"C. 0.000599 per O F . Strawyellow 15.4 83°F. 846.7 Cat. per mol 85.9 cal ./g. -59°C. 3.4% by vol 3.4% by wt. 0.853 0.856 0.521 cal./g. 1.4456 8.0 mm. Hg 14.3 mm. Hg 24.5 mm. Hg 8.79 millipoises 7.12 Ibs. 0.050/, max. Below 120°C. None Above 135°C. None More than 95% distills over below 131°C. 95% by wt., min. Miscible without turbidity with 19 vols. of 60" B6 gasoline at 20°C. (approx. 0.20% by wt.)
.
-
643
644
Industrial Solvents Handbook
ISOPHORONE
lsophorone i s a stable, colorless, volatile liquid with a mild odor. It i s only slightly soluble in water, but miscible with m o s t lacquer solvents. It i s an excellent solvent for many types of cellulose esters, cellulose ethers, oils, fats, gums and resins, both natural and synthetic. It i s the most powerful solvent for nitrocellulose and "Vinylite" resins. lsophorone has one of the highest aromatic hydrocarbon dilution ratios for nitrocellulose-5.7 for toluene and 5.1 for xylene. It w i l l dissolve 30% of "Vinylite" resin without gelling. At ordinary temperatures solutions can be made of 1/2 second RS nitrocellulose containing 45% solids. lsophorone i s used i n the manufacture of coatings, inks, stencil pastes and as a thinner in synthetic resin finishes.
Table 12.33: Propertles of lsophorone (2) Boiling point at 760 mm.
2152°C.
Dilution ratios Toluene Xylene "Tro I uo i I " Mineral spirik Flash point (open cup) Freezing point Solubility in water at 20°C. Solubility of water in solvent at 20°C. Specific gravity at 20/20°C. Vapor pressure at x) "C Weight per gallon at 20°C. Acidity (as acetic) Distillation range at 760 mm. Color
5.7 5.1 1 .O 0.7 205OF. -8.1"C. 1.2% by w t . 3.8% by w t .
-
0.9200 0.9250
.
0.25 mm. Hg 7.68 Ibs. 0.02% by wt., max. 205" -220'C. Not darker than 0.05 g. K2Cr2Q7 per I. of water 98.0% by wt., min. Miscible with 19 vol. 600 B; g a d ine at 20°C.
Purity
Water content
FENCHONE Fenchone i s a liquid ketone closely resembling camphor.
fH3
Table 12.34: Properties of Fenchone (2) Boiling point
Dilution ratio: with coal-tar naphtha with hi-flash naphtha Kauri-butanol Optical activity Refractive index at 20°C. Specific gravity at 15.5"C. Aniline point (-)
191 .O°C, 1.3 final conc. 8.0 1.2 final conc. 8.2 A l l proportions in 5wo sol, with mineral spirits 131 + 7.4 1.4625 0.9457 54°C.
Distillation Range (Calculated from 50:50 Min. Spirits)
5% 10% 2w o 40% 60% 8OVo 90% 95%
193.OOC. 193.4OC. 193.8"C. 194.2 "C 194.5"C 195.4"C. 196.0"C. 197.5"C.
. .
Ketones
645
BETA-PROPIOLACTONE BPL
'
difunctionality
\
HOCH2 -C H2 -C= ,O
y---CH2-CH2-C=O
\
\
OH
Y
Hydracrylic Acid Derivatives
Beta-Propionic Acid Derivatives
Table 12.35: Physlcal Properties of Beta-Proplolactone (42)
Physical state Liquid Color Colorless Odor Pungent, acrylic 51 Boiling point at 10 mm Hg, deg C 100 mm Hg 100.0 400 mm Hg 139.7 760 mm Hg 162.3 Melting point, deg C -33.4 Refractive index n g 1.4131 Specific gravity, 20/20 C 1.1490 9.56 Pounds per gallon at 20 C 165 Flash point, Tag open cup, deg F Solubility: BPL is miscible at room temperature with most organic solvents such as ether, alcohol (reacts), benzene, acetone, and acetic acid. Solubility in water at 25 C is 37 per cent by volume, with moderately fast hydrolysis to hydroxypropionic (hydracrylic) acid.
GAMMA-BUTYROLACTONE
J-[
B LO
=o 0
Gamma-butyrolactane i s a powerful solvent and undergoes many reactions that make i t o f considerable interest i n synthesis. I t i s a colorless hygroscopic liquid over a wide temperature range. It i s soluble i n acetone, benzene, carbon tetrachloride, ethyl ether, methanal, manochlorobenzene and water in a l l proportions.
Table 12.36: Properties of Gamma-Butyrolactone (49) Appearance. . . . . . . . . . . . . . .clear liquid Color (APHA). . . . . . . . . . . . . . .40 Purity . . . . . . . . . . . . . . . . . . .99.5% min. Moisture. . . . . . . . . . . . . . . .O. 1% max. Free acid. as hydroxybutyric . . .O.I% max. Molecular wetght . . . . . . . . . . . .86 Boiling point. . . . . . . . . . . . . . .2W0C Freezing point . . . . . . . . . . . . . .-44OC Viscosity (25%). . . . . . . . . . . . .1.7 cp
Specify gravity ( d 3 . . . . . . Flash point. tag closed cup Fire point . . . . . . . . . . . . . pH (10% aqueous solution) . Refractive index (n3. . . . . . Heat of vaporization. ClausiusClapeyron (calc) . . . . . . . . . . Heat of sdution . . . . .
1124 93°C (200°F) 99OC (210°F) 45 1435 133 cal/g 598 calimol
Heat of combustion Specific heat (25OC) (60°C) Dekxtrtc cmstani (20%) Critical pressure
492 kcal/md 0 40 callgl°C 0 45 caUgl°C 39 500 psl (35 kglcm') Critical temperature 436% Solublity soluble in acetone. benzene. carbon tetrachloride, ethyl ether. methand. chlorobenzene. and water in all proportions (cont I nued )
646
Industrial Solvents Handbook
Table 12.36: (Continued) Vapor Pressure of Butyrolactone 200
150
100
50
10
1
5
50
10
100
500 760
1500
Vapor Pressure (mm Hg)
Concontration
Time (hours)
(% 1
1
1 ROOm
BLO
Dilute Tomporrtun HCI
6S°C
2
-
5
90 10 ________ 80 20
028
_ _217 __
50
0.92
6.48
99
1
98 95
50
I
1
3 T:r$rature
65OC
I
I
5
T:rgrrturo
6SqC
I
24 T:gratun
- I
-
0.34
0.32
I
0.24
0.97
-
0.73
I
0.49
2.35
-
1.23
I
0.59
4.43
102
815
915 5___ 52 __162 - - __ - - --
1598
12.10
2.57
Concentration (%)t BLO
Ha0
80
20
50
50
I I I I
65OC
-
0.56
0.97
1.21
0.68
I 1.18 I 2 53 I
1.94
3.1 1
0.99
4.87
I
3.14
5.95
-
0.54
0.42
4 07
17 92
.-
1095__ 1841
Time (hours)
I
8
24
48
-
0.33
1.7
1.7
11.1
17.4
(continued)
Ketones Table 12.36: (continued) Table 111. Bunsen Coefficients of Butyrolactone (cc gas/cc solvent converted to STP) --
____
Gam
25°C
45°C
Hydrogen Carbon Monoxide Carbon Dioxide Methyl Acetylene Acetylene Vinyl Acetylene
0.12 0.09
0
0
0.044
0
Compound
3.6 37.8 11.8 145.1 1 2 7 0 ~ 1
2.7
12.5 8 33.1
75°C
1.1 10.8 1.45 23.1 1730~1
Table IV. Solubilities of Compounds in Butyrolactone
96 (lolublo
Acrylonitrile, (high) spec. vis. 8.5’.................................... Acrylonitrile, (low) spec. vis. 3.18’ .................................... Acrylonitrile, (low) spec. vis. 2.45’.................................... Acrylonitrile, (low) spec. vis. 2.1 1‘ .................................... .“Amberot“ Resin 820 (Rohm & Haas) ................................. “Aroclor” (60% CI), chlorinated biphenyl (Monsanto) .................... Cellulose Acetate ................................................. Cellulose Acetate Butyrate ......................................... Cellulose Acetate Propionate ....................................... Cellulose Nitrate . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . “Clorafin” (70% CI), chlorinated paraffin (Hercules Powder) . . . . . . . . . . . . . .
DDT
............................................................ “Epon” 1007,epoxy resin (Shell Chemical) ............................
“Epon” 1009, epoxy resin (Shell Chemical) . . . . . . . . . . . . . . . . . . . . . . . . . . . . Ester Gum . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . Ethyl Cellulose . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . “Formvar,” polyvinyl formal resin (Monsanto) .......................... “Geon” Polyblend, polyvinyl chloride (Goodrich) ...................... : “Geon“ 102, polyvinyl chloride (Goodrich) ............................ “Geon” 202, polyvinyl chloride (Goodrich) ............................ HETAnhydride . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . Methyl Methacrylate Polymer ....................................... Methyl Vinyl Ether Polymer ......................................... “Neolyn” 23 Resin (Hercules Powder) ................................ “Parton,” chlorinated rubber (Hercules Powder) ........................ Polyvinyl Butyral . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . Pyromellitic Acid . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . “Saran“ F-120, vinylidene chloride (Dow Chemical) .................... Shellac . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . Polystyrene . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . Vinyl Acetate Polymer . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 1-Vinyl-2-Pyrrolidone Polymer . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 9-Vinylcarbazole, Monomer and Polymer . . . . . . . . . . . . . . . . . . . . . . . . . . . . . “Vinylite” VYNW, vinyl chloride resin (Union Carbide) . . . . . . . . . . . . . . . . . . . “Vinylite,” XYSG, vinyl resin (Union Carbide) .......................... 1 gram polymer dissolved in 100 ml BLO. b
Heated for 1 hour at 100°C. and then cooled to room temperature.
c
Solubility after 1 hour at 100°C.
BUTYROLACTONE refers to gamma butyrolactone
>IOb >16b 20b 20b 50 50 5‘ 10
10 25 50 50 25 25 50‘ 25‘ >5
>loc > 5‘ >lo‘ 60‘ 25 50 50
>25 25‘ 20 >I 0 25 >25 >25 >25 >25
> 5‘ 10‘
647
648
Industrial Solvents Handbook
I I
,
Ketones 649
P N v1
5
2 8
n
ir
t
3
0
,P
5 4 C
t
5
B
c
650
Industrial Solvents Handbook
Table 12.39: Eastman Chemical Ketones (47)
Acidity, as Acetic Acid Max Wt 46
Boiling Range OC
Freezing Point OC
Flash Point TCC "C (OF)
Assay Min Wt
Max
Specific Gravity @ 2Oo12O0C
5
0.792
0.004
55-57
-95
-20 (-4)
99.5
6.74
15
0.810
0.02
101-105
-86
8 (46)
90.0
1.6
6.67
10
0 802
0.01
114-117
-84
16 (60)
99.0
0.5
6.76
10
0.813
0.02
141-148
-74
36 (96)
98.0
0.4
6.80
10
0.818
0.02
147-154
-33
39 (102)
98.0
0.2 Diisobutyl Ketone (DIBK) (CH&CHCHaCOCHzCH(CH&
6.76
20
0.81I
0.02
163-176
-42
49 (120)
-
EASTMAW C-11 Ketone
7.02
75
0.84
0.10
175-250
-8
84 (184)
-
Evaporation Rate n-BuOAc=l
Lbl Gal @ 20%
Color Pt-Co
Acetone CH3COCH3
5.7
6.59
Methyl n-Propyl Ketone (MPK)~ CHjCOCjHi
2.3
Methyl Isobutyl Ketone (MIBK)~ CH3COCHzCH(CH& Methyl Isoamyl Ketone
w
(MIAK)' CHjCOCzH&H(CH&
Methyl n-Amyl Ketone ( M A K ~ ~ CH3COC5Hir
0.02
(seta-flash) aUrethane grade bKosher certified
Table 12.40: Exxon Ketones (8)
Methyl Ethyl Ketone Distillation Range, "C Specific Gravity, 20"/20"C Viscosity I@ 25"C, cp Vapor Pressure I@ 20°C mmHg Density @ 20"C, Ib/gal Flash Point, TCC "C* Acidity, wt % MAX* Evaporation Rate, n-BuAc=l 00 Purity, wt % (MIN) Hildebrand Solubility Parameter Surface Tension @ 20°C dynes/cm Water Content, wt % (MAX) Water Solubility @ 25"c, wt % In water Water in Inhalation TLVCAS Registry Number *Tag Closed Cup, ASTM D 56 *As acetic acid
Methyl Isobutyl Ketone 114-1 17
79-81 0.81 0.4 80 6.71 21 0.003 572 )99.5 9.3 25 0.1
0.6 15 6.68 62 0.01 165 )99.0 8.6 24 0.1
26.3 11.8 200 78-93-3
1.7 1.9 50 108-1 0-1
0.80
**Threshold Limit Value is a registered trademark of the ACGIH
Ketones
651
Table 12.41 : Hoechrt-Celanese Ketones (42)
Physical Properties Autoignition Temperature, OC
515.5
Heat of Combustion, kg-caVg d e
Boiling Point at 760 mm Hg, OC
79.6
Heat of Fusion, caVg mole
1.78
Boiling Point at 760 mm Hg, O F
175.3
Heat of Vaporization, btullb at 20%
212.4
Coefficient of Thermal Expansion per OC at 20%
Molecular Weight
72.11
1.126~103
Critcal Pressure, atmospheres
41.O
Critical Temperature, OC
252.5
Dielectric Constant, 20%
15.45
Specific Giavily, 2CV20OC
0.8062
Evaporation Rate (BuAc = 1)
5.7
Specific Heat of Liquid, at 20°C, caVg
,525
flammable Limits (lower limit, ~01%) (upper limit, v d %)
Surface Tension at 20%. dynedcm
24.6
2.0 11.0
Vapor Density (air = 1)
2.5
Vapor Pressure, at 2OOC, mm Hg
77.5
Rash Point, Tag Open Cup, O F Tag Closed Cup, O F
30 20
Freezing Point, O C
-86.7
582.3
Refractive Index, nf' -
1.3787
Solubili at 20% at wt % in water
26.8 12.5
water in
Vscosity at 25OC. centipoise
0.40
Weight, pounds per gallon at 20%
6.71
Table 12.42: Shell Chemical Ketones (14)
Typlcal properties of the compounds
Molecular welght Speclflc gravlty (apparent) 60/60' F 20/20oc 25/25' C Weight per U.8 gallon (in alr)
60OF
200 c 25' C Bolllng polnt @ 760 mm 'C OF
Bolllng polnt change OC/mrn @ 760 mm Vapor prerrure @ 20°C, mm Freezlng polnt @ 760 mm. OC Refmcllve Index n
20
D Heat of vaporlzatlon cal/g @ 760 mm Heat of furlon at meltlng point
cai/g Speclllc heat (Ilquld) callg 'C @ 25' C Fkrh point, tag open cup, O F approx.
tag closed cup, O F approx. Flammable tlmltr In alr % of compound, upper
lower Solubility, % wt. in water, @ 2OoC water in, @ 2OoC Azeotrope with water, %w compound Boil pt. @ 760 mm, OC Viacorlty, cps @ 20'C @ 25'C @ 30'C Surface tenrlon dynelcm 20' C
Acetone
Methyl ethyl ketone
Methyl lrobutyl ketone
Dlacetonr alcohol
58.080
72.108
100.162
116.162
0.7967 0.7925 0.7879
0.8105 0.8065 0.8023
0.8055 0.8022 0.7986
0.9441 0.9409 0.9374
6.636 6.595 6.549
6.750 6.711 6.668
6.709 6.676 6.638
7.863 7.830 7.792
56.13 133.03
79.64 175.26
116.2 241.16
169.2 336.6
0.0385
185.95 -94.897
0.04 70.21 -86.69
0.046 14.96 -83.5
0.075 0.81 -44.
1.35900
1.37880
1.3957
1.4234
122.09
105.95
82.50
90.0
23.53
24.86
0.51
15. -15.
0.51 20. 23.
0.53 79.
0.62 135. 126.
11.ov 3.0~
11.5~ 1.81v
7.5v 1.4v
complete complete
27.1 12.5
2.04 2.41
complete complete
none
88.73 73.41
75.7 87.93
12.7 98.8
0.3075
0.41 0.365
0.583 0.55
2.9
22.32
24.6
23.64
28.9
60.
652
Industrial Solvents Handbook
C
a
3
C
c 0
C
f: h
-c
2 f 0
. 0 .
:
i
n
t:
?
N
2
0
n n v 1
t. C
IC
d
!
I
I
2
r
.
!
!
t
a
8 Q) E
C
CI
I
s
Y
654
r
;
r
6
Y
*!
rll,
0
I
v)
0
Q4
U
8
0
a
e ?
.d b
0
Q4
3
0)
a
m
c
m
m
m
m
m
m
m
m
m
e
m
m
-
m
m
m
m
m
m
m
e
m
m
m
m
m
m
m
m
m
I
m
m
6
m
m
Y
5
k
-r" 2 -8
Y
5
W
m
W
8
w
Y IK
a
I 0
Y
w
> a
l-
I
c
z
W
0
a
5 W
a
~
L
0
w
2
a m o n w
Ketones
661
Table 12.50: Viscosity vs Concentratlon of Chlorinated Rubber (Hercules PARLON S-20) in MEK (8)
Percent Solldo
Table 13.1: Acetic Acid (2) Vinegar A c i d M e thone car box y Iic A c i d Ethanoic A c i d
CH3COOH
Acetic acid i s a colorless liquid with a pungent odor; i t i s made synthetically from acetylene or by the oxidation of alcohol. I t i s soluble i n water, alcohols, ethyl ether, and other organic solvents. It i s used as a precipitant for albumen, casein, and rubber latex. It i s also employed i n the manufacture of leather, cordage, linoleum, acetate solvents, acetyl derivatives, dyes, matches, printing inks, and polishes, and as an assistant i n dyeing processes.
Sptciflcnliona (Qlacial A c e l i c ) Standard
+ Laundry
Speclnl
Ace toldehydr .4citlity, as ncctir ncitl Color Formic ucid FreezinK point Son -volatile matter Water rontent Weight per yailoli ab
moc
0.&5% (minx.) W.S% (min.) Water-white 0.2% (mu*.) 15.6'C (min.)
U.S.1'. XI1
%b.5ci ( i n i i l . ! W u t e t -\v ti iI I'
IK.Roc(iniii.1 0.0265','{ (nius 0.59;, ( I I U I K . ) H.74 IIM
0.5%. (mux.) 8.74 iiw.
I
Table 13.2: Viscosity of Acetic Acid and Acetic Anhydride Mixtures at 15" and 765°C (79)
PEP CENT ACETIC ANHYDRIDE B Y WEIGHT
662
Acids
663
Table 13.3: Butyric Acid (2) Ethylacetic Acid Butanoic Acid Propyl formic Acid
CH3CH2CH2COOH
Butyric acid i s a water-white liquid having o choracteristically pronounced and highly disagreeable odor. I t i s soluble i n most organic solvents and completely soluble i n water. The importance of butyric acid i s found i n its butyrate, made with alcohols; these compounds are used as flavors because of their pleasant fruity odors. Other uses are i n the manufacture of flavor esters, plastics, drugs, i n leather tonning and for deliming hides.
Typicol Properfirs and Spcrificalionr 163.5.C 0.001026~c 0.001061 Water-rhite 3WC 0.302 I.* x 10-6 rtcip. ohm o.oo039 x 10-4 recip. ohm 17O'F 5906 0.1. (15116 20.1 cal. (1511g 1.59 cal./g -5.7.c
Boiling point a t 760 mm Caefficient of eipanaion at 20% at 55 Color Critical temperature Critical density Diasociation constant a t 25'C Electrical conductivity a t 25'C FImh point (ASTM open cup) Heat of comblution Heat of fusion Heat of vaporization Melting point
Solubility in wat.er at 2o'C Solubilitg of nater in solvent at 20'C Specific gravity at 2O/20'C Specific heat Refractive index a t 19.C Surface tenaion a t 2O'C Vapor preasure at 2O'C Viacolity at 25'C Weight per gallon at 20'C Chloridea Diatillatioa range at 760 mm Purity
Complete Complete 0.9595 0.514 (20-1oO"c) 1.3980 26.8 dynea/aq cm 0.84 mm Hg 0.01529 poiae 7.965 Iba. None leO-le-5~C W.W0by wt.,min.
Table 13.4: Viscoslty of Aqueous Butyric Acid Solution at 25°C (79)
34 32 30
2
20
3 26 4 24 22
g 7.0
g
IO
I6 14 12 10
0
E R CENT BUTYRIC ACID BY WEIGHT
Table 13.5: Butyric Anhydrlde (2)
Butyric anhydride i s a water-white liquid which hydrolyzes to butyric acid in the presence of water. Like butyric acid, i t i s used i n making butyrates, flavors, drugs and tanning agents.
Bailing point a t 760 mm. Color Flash paint Melting point Specific gravity at 20/20°C. Vapor pressure ot 2OOC.
199.5"C. Water-white
190OF. -75OC. 0.965-0.970 0.37 mm. Hg
Weight per gallon at 2OOC. Distillation range at 760 mm. Below 190°C. Above 2 0 0 O C . Below 195OC. Purity
8.1 lbs. None None N o t more than 10% 85% by wt., min.
664
Industrial Solvents Handbook
Table 13.6: Solubility of Water in Caproic Acld at Various Temperatures (79) IO
S
?!
P
re
zB
7
G3
6
I-
cz g
s 4
3
0
IO
20 30 TEMPtRATURE T.
40
50
Table 13.7: 2-Ethylbutyric Acld (2) Diethyl Acetic Acid 2-Ethylbutanoic Acid 2-Ethylbutyric ocid i s a water-white liquid, similar to butyric acid in most of i t s properties, except that i t s odor i s less strong and i t i s not as soluble in water. I t s halogenated derivatives are finding use in the manufacture of drugs. I t s esters with higher glycols are outstanding vinyl resin plasticizers. Boiling point at 760 mm.
1Y4"C.
Flash pointin water at 20°C. Solubility Solubility of water i n solvent at 20°C. Specific gravity at 20/20°C.
210°F. by wt. 0.22% 3.3% by wt. 0.9225
Vapor pressure at 20°C. Weight per gallon at 20'C. Distillation range at 760 mm. Purity
0.14 mm. Hg 7.68 Ibs. 185"-2OO0C. 90% by wt.:, min.
Table 13.8: 2-Ethylhexoic Acld (2) Octoic Acid 2-Ethylhexanoic Acid
CH3(CH2),CH(C2H5)C0OH
This acid possesses a mild odor and a high boiling point. It i s important for i t s metallic esters, the properties of which suggest usefulness as varnish driers. These metallic s a l t s are stable, mild-odored, light-colored compounds, and are soluble i n hydrocarbons. The glycol esters of this acid are excellent vinyl resin plasticizers. Boiling point at 760 mm. Flash point Solubility in water at 20°C. Solubility of water in solvent at 2OOC. Specific gravity at 20/20°C.
226.9"C. 260 O F . 0.25% by wt. 1 .% by wt.
0.9077
Vapor pressure at 2OoC. Weight per gallon at 2OoC. Distillation range at 760 mm. Purity
0.03 mm. Hg 7-55 Ibs. 220°-2300c. (90% distills within this range 95% by wt. min.
Table 13.9: Solubility of Water in Ethylhexolc Acld, Ethylbutyraldehydeand Ethylpropylacroiein (79)
TEMPERATURE Y.
Acids Table 13.10: Lactic Acid (2)
u -Hydroxypropionic Acid
CH3CHOH*COOH
Lactic acid, which i s among the oldest known organic acids, i s obtained from sour
milk by the reduction of hexose sugars or by the interaction of acetaldehyde and carbon monoxide. I t i s miscible with water and many organic reagents. Since i t has an asymmetrical carbon atom, lactic acid exists in two optical isomeric forms. Peckham states that "the nomenclature used to designate the isomeric forms was, until recently, very confusing. The form of the acid commonly known as sarcolactic, the form occurring i n blood, has (+) rotation but the I configuration. I t i s therefore correctly designated as I(+) lactic acid and its mirror image as d(-) lactic acid. The salts of the I(+) form are levorotatory and the salts of the d(-) form are dextrorotatory. &cause of the low optical rotatory power of the free acids, rotation of the pure acid or its simple salts i s not a suitable criterion for establishing the optical form of the acids, or the percentage composition i n case of a mixture". Commercial lactic acid has been determined to be a mixture of a-hydroxypropionic acid, lactyllactic acid, and water. When dilute lactic acid i s concentrated, two molecules of lactic acid unite to form loctyllactic acid and water. The lactyllactic acid splits off from the water.
~H,CHOH.COOH e CH,'CHOH~COOCH~CH,~'COOH + HI0
It
CH~C&)OCOCH(CH,)OCO
Polylactyllactic acids may also be formed by loss of water between the carboxyl and the alcohol groups, thus:
The conditions which affect the production of a lactic acid solution from lactyllactic acid are temperature, concentration and age of solution.
A graph showing the Composition of Aqueous Lactic Acid Systems at Equilibrium and at Progress States of Dehydration.
665
666
Industrial Solvents Handbook
Table 13.11: Trifiuoroacetic Acid (25)
114.03 72.5"C 105.5"C ( I ) -15.36"C (1,2) 1.4844 g/mI 12.4 Ib/gal 28.8 mm (3) 107 mm 7949 cal/mol (3) 125.5 Btu/lb 0.81 3 cp (4) 42.1 e (5) 0.026 105/cmohm (4) 13.44 dynedcm (6)
CF3COzH Mol. Wt. Boiling Point Water Azeotrope (20.6% water) Freezing Point Density a t 25°C Vapor Pressure O'C 25°C Heat of Vaporization Viscosity a t 25°C Dielectric Constant at 25°C Conductivity a t 25°C Surface Tension at 26°C
( I ) Swarts, F., Bull. Acad. Roy. Belg. Classe sci., 8, 343 (1922). (2) Cady, H.H. and Cady, G.E., J. Am. Chem. SOC., 76,915 (1954). (3) Taylor, M.D. and Templeman, M.B., J. Am. Chem. SOC., 78,2950 (1956). (4) Fialkov, Y.Y. and Zhikarev, V.S., Zh. Obshch. Khim., 33,3466,3471,3790 (1963). (5) Simons, J.H. and Lorentzen, K.E., J. Am. Chem. SOC.,72, 1426 (1950). (6) Jasper, J.J. and Wedlick, H.L., J. Chem. Eng. Data, 9, 446 (1964).
E E P
1E 20 30 40 50 60 70 TEMPERATURE 'C VAPOR PRESSURE OF TRIFLUOROACETIC ACID -10
0
10
MOL%
80
CFmH
FREEZING POINTS WATER-TRIFLUOROACETIC ACID SYSl'EM
(continued)
3
6 Q) E 0
Y
C
-
..
0
r
v
T:
2
Q)
s n
-
r
0
E
0
3
8 m
r(
8
0
0 (
E: 0
*2 0z 0
0 0
2
8
f
!2
N
8 0 0
8 N
Qm 0 0 0 P
8 P P O o D 8 s a o
0 0
33NVJl.l WSNVU lN3383d
Acids 667
3
I
-z!
C
.-wC
-8
668
Indusnial Solvents Handbook
Table 13.11: (contlnued) SOLUBILITY OF INORGANIC ACIDS
INSOLUBLE
MISCIBLE
Over 10 g
1-10 g
0.1-1 g
Leu than 0.1 g
CSCl &POI KiSO4 NH,NOs
AgF,CrO,FeCl,KCI KCrOr,KF, KI KMn04,KNO~Na0,NaCr04,NaI NaF, NaNOS Na3PO,,NaSO,
B a a z , Be C12 Cr C13 Crz (SO& MgFz NiFz
AgCI, AICI:l BaSO, C a S , FeF3 KaOr NaCI04,PbFz
SOLUBILITY OF METAL TRIFLUOROACWAm IN TRIFLUOROACETIC ACID AT 30°C
Metal Salt
AI
Ba
Ca
Cut*
Hg'*
K
Mg
Na
Ni
Fe'3*
g SaIt/lOO g acid
0.01
42
6.3
20
50
50
0.57
13
16
1.2
CO,
HBr
HCI
Ha
3.5
6.6
4.1
GlU
Clz
Trifluoroacetic Acid Water
9.3 2.1
CO 0.0 0.02
-
0.8
580
-
TEMPERATURE
423
"C.
N2
O2
SO,
8.6
0.1
0.2
23
2.5
0.02
0.03
36
0
c
P
2
'30-U3111
3lllVA NOllV314NWVS
3nlVA 3Nl001
310N3AlOdVS03VY131
31Y330NDll
310N3AlOdVS0300
310N3AlOdVS0313
310N330313
3IYV31SO313
31NV311
31W31SAXOU0AHIO
31310N131Y
31N31ONll
31310Nll
31310
1131011WlVd
3111WlVd
310NV330VlN3d
313101SlUAW
31181YAW
Acids
669
670
Industrial Solvents Handbook
Table 13.14: Arizona Chemical ACTINOL Tail Oil Fatty Acids (5) SAPONIFICATION VALUE
IODINE VALUE (WIJS)
MOISTURE .h
Asn
197
131
< 0.1
200
A
20
> 200
A
20
> 200
A
20
> 200
VlSCOSlTV
7
FA-3
I
34
0
OTHERS nv DIFFERENCE. %
SATURATED
LINOLEIC NON-CONJUGATED
95.2
7
< 0 01
FATTY ACIDS TOTAL I o
> 200 .
> 200
Acicis
671
Table 13.15: Eastman Chemicals Acids and Anhydrides (41) Cdor
Boiling
Specific Gravity @ 20.1200C
Point OC
Freezing Point OC
TOC
Form
Pt-co Max
Flash Point
Fire Point O C (OF)
A-Y Mln Wt
Glacial Acetic Acida3D*C.a (Ethanoic Acid) CHICOOH
Liquid
-
1.05
118
17
43 (109)
64 (148)
99
Acetic Anhydrided (Acetyl Oxide) (CHiCO)zO
Liquid
-
1.08
140
-73
56 (132)
58 (137)
99
Butyric Acid (Ethyl Acetic Acid) CjH7COOH
Liquid
15
0.96
164
-8
71 (160)
75 (167)
99
Butyric Anhydride (CiW0)zO
Liquid
-
0.97
195
-73
84 (183)
87 (189)
98
Crotonic Acid (2-Butenoic Acid) CHiCH:CHCOOH
Solid
15 (APHA)
0.96 (8O0/4OC)
185
70
94 (202) COC
97 (207)
99
2-Ethylhexoic Acid (2-EthylhexanoicAcid) CAHSCHIC~HSCOOH
Liquid
25
0.91
223
-118
118 (245) COC
127(260)
99
Isobutyric Acid (2-MethyipropanoicAcid) (CHi)zCHCOOH
Liquid
10
0.95
155
-47
62 (143)
67 (152)
99
Isobutyric Anhydride Cdl403
Liquid
-
0.95
182
-54
72 (161)
74 (166)
98
Propionic Acidasb9' CzH&OOH
Liquid
10
0.99
141
-22
54 (130)
58 (137)
99
-45
66 (151)
66 (151)
98
OC
(OF)
w
. I
Propionic Anhydride (CzHsCO)?O
Liquid
-
1.01
167
aAvailable in food grade bKosher cenilied 'Available in feed grade dAvailable in reagenr grade
Table 13.16: Halocarbon Products BIOGRADE Trltiuoroacetlc Acid (25)
SPECIFICATIONS: Assay by titration Trifluoroacetic Anhydride water
99.9% Min. nil 0.05% Max.
Trace Impurities (Maximums) Chloride Fluoride Sulfate Iron (Fe) Residue after evaporation
0.001% 0.001% 0.001% 0.0001% 0.0002%
Color (Platinum-Cobalt Scale) 5 Max. Ultraviolet Absorbance Maxima (0.1% in distilled water vs. distilled water in 1 cm cell path) at 230 nm 0.15% at 254.nm 0.01%
672
Industrial Solvents Handbook
Table 13.17: EMERY Fatty and Dibasic Acids (63)
Sprdflc%on8
Acid Value EmpoP 1010 Dimer Acid (polymer grade) Empol 1014 Dimer Acid Empol 1016 Dimer Acid Empol 1018 Dimer Acid Empol 1022 Dimer Acii Empol 1024 Dimer Acid Empol 1040 Trimer Acid Empol 1041 Trimer Acid Empol 1052 Polybasic Acid
Color 1963 Gardner, ma.
Compantlw Typical Comporitlon1 Short-Path High Pressure Methyl Ester Liquid Distillation Chromatography Di Poly Mono Di
Mono
Poly
194-200
1
0
97
3
4
94
2
194-198 190-198 190-198 189-197 190-198 175-192 161-181 . 250-2852
5 6 8
95
8
1 1 Tr 3 Tr
4 19 17 22 25 93
11 dark
-
-
4 6 6 9 8 2 3 33
91 76 79 77 77 18 35
5 18 15 14 15 80 62
343
633
a
80 03 75 75 7 10
-
-
90
-
Food Grade1 Fatty Acids
I
b
ma.
nm., min.
Value
53.9-54.7
3.5-5.0
88/99
205.210
2.5
0.5
50
1
40
54.5-55.5
0.5
93/99
205211
1.5
0.5
50
1
47
59.0-60.5
0.5
88199
203-206
3
0.5
26.5
1
69
Tr
65-68
1.0
84/98
1s201
1
Tr
7.5
2.5
88
1
Emenol6313 NF Low-liter Oleic Acids
6 ma.
88-93
75/98
201-204
3
Tr
5
1
Tr
3
6321 NF Low-tiler While Oleic3 Emersol6333 NF LL Oleic A~id3~0
6 max.
87-92
85/99
201-204
3
Tr
5
1
Tr
3
6
8-10
86-91
85/99
200-204
3
Tr
6.5
1
1.5
3
5.5
EmersoP 6320 DP Stearic Acid
6332 NF TP Stearic Acids-' Emersol6349 Stearic Acid Emersol6351 Stearic Acids
6
6
7
5
6
1
75
6
1
73.5
5.5
0.5
(continued)
673
Acids Table 13.17: (contlnued)
Coconut Fatty Acids
1
8-8
Color 96 Trans. Gardner W550 1963, nm., min. max.
Tvrrul rn)Oritkn'
Titer, OC
Iodine Value
23-27
5-16
3w80
Y
258268
4
5
48
20
10
2
10
1
22-26
5-10
65/96
22
2M-276
7
6
48
19
9
2
8
1
23-25
5,0 max.
1
269-273
7
6
49
19
9
7
3
E M W ~ H ~ W I V U ~ ~251 Coconut Acids
1.Omu.
1
270-276
7
6
51
18
10
7
1
1
252-258
1
0
1
1
253-259
1
3
5
E m e v 621 Coconut Fatty Acid Emery 622 Coconut Fatty Acid Emery 625 Partially Hydrogenated Coconut Fatty Acid
Fm
E ~ 627 w Low IV, HdPPd. U l n Coconut Acid
1-32 1.0
Emery 629 Stripped, Coconut Fatty Acid
27-30
Fm
6-10
o6/9(1
88/98
Acid Value
5
5
2
2 23
55
1
1
1
12
'Typical compositions determined by GLC analysis. AOCS Ce 1-62. These compositions are not manufacturing specifications. ZTypkaI property. 3Emety 7026 Kosher Grade available.
lwstearic Acids Specllcrtlons Color
46 Trans. Titer, max. 10 10
EmersolQ 871 lsostearic Acid Emersol 875 lsostearic Acid
4401550, nm., min. 30185 85/98
Iodine Value 12 max. 3 max.
OC,
Acid Value 175 min. 187-197
Oleic Acids Typical Compm Unsaturated Aclds
Saturated Acids Color
46 Trans. OC
Iodine Value
4401550 nm.. min.
Acid Value
7-12
87-95
2/30
197-204
T
ma''
88-95
199-204
Tr
3
Tr
3
Titer, EmersoP 210 Oleic Acid Emersol213 NF Low-titer Oleic hjd2,3
r
3
5
1
1
4
Tr
5
1
Tr
3
Tr
4
1
Tr
T
r
6 6
3
7
1
7
3
7
7
8
3
1 8
1
8
1
8
1
~~
Emersol233 LL
oleic Acid'
6max.
86-90
78/99
200-204
Tr
3
Tr
4
1
Tr
3
Tr
3
Tr
4
1
Tr
3
7 11
7
3 74
4
TI
1Typical compositions determined by GLC anaiysis, AOCS Ce 1-62, These compositions are not manufacturing specifications lConesponding food grade products available T o r external use only, USP XXl/NYF XVI. 4LL (bw-linokk content) oleic: polyunsaturates 5% max.
(continued1
674
Industrial Solvents Handbook Table 13.17: (continued)
Short-Chain Acids* S
~
O
n
I
S
Typlcrl CanporlUon*
Titer, OC
Iodine Value max.
Color % Trans. w 5 5 0 nm.. min.
Acid Value
35
14-16
0.2
88/99
385-390
Tr
99
1
1-6
0.3
88/99
356-366
3
56
40
1
28-31
0.5
88/99
322-326
1
97
2
Emery 650 Lauric Acid
33-35
0.4
85/97
268-272
Emery 651 Lauric Acid
41-43
0.2
w98
276-282
Tr
Emery 652 Lauric Acid
43 min.
0.2
90/98
277-281
Tr
Emery 655 Myristic Acid
52.0-53.5
0.5
90/99
243-246
Emery@657 Caprylic Acid Emery 658 Caprylic-Capric Acid Emery 659 Capric Acid
.YN 9%
s% gQ 85 “ 2 O
N
71
28
1
96
3
0.3
99
0.7
1
97
1
2
Stearic and Palmitic Acids S~llkrHOnS Unrrturated Saturated Acldr
AcldS
Color % Trans.
Titer, OC
EmersoP 110 Stearic Acid 52.8-53.5 53.7-54.7 Emersol 120 Stearic Acid2 Emersol 132 NF Lily@Stearic A ~ i d 2 ~ 354.5-55.5 ~~ Fmnrsnl 143 Palmitic Acid 58-61 63.9-65.0 Emersol 150 Stearic Acids 66.5-69.0 Emenol 152 NF Stearic Acids Emersol 153 NF Stearic Acids 67-69 52 min. Emery 400 Stearic Acid Emery 404 Stearic Acid 53.5-54.5 Emery 405 Stearic Acid’ 57 min. Emery 410 Stearic Acid 56.1-60.0 Emery 420 Stearic Acid 57.2-63.0 55.8-60.0 Emery 422 Stearic Acid
Iodine Value
E12 57 0.5 max. 1 max. 1 max. 1 max. 1 max. 9.5max.
6-9 6 max. 7 max. 1 max. 1 max.
4401550 nm.. min.
60/94 88/99 93/99 93/99 93/99 80/97 80/97 1/40 1/50 40/86 40/86
85/98 93/99
Acid Value
205-210 205-210 205-210 215-223 197-202 196-199 196-199 197-212 197-209 195-205 195209 200.207 203-209
I
35
I
39
I
5 75
~~~
25
n5 1
50
50
2 2.5
90 95
7
5
9 5
Tr
1
Tr
3
I
3 4 3
0.5 0.5 Tr
25 29 41
2 1.5 1
63 65 55
2.5
4
Tr
Tr
‘Typical composirions determined by GLC analysis, AOCS Ce 162. These compositions are not manufacturing specifications Orresponding food grade products available: SFor external use on&, USP XXUNF XVI. 4hwdered grade also available. W96 mhimum stearic m t e n t . 6Tentative specifkation.
[continued)
-
Acids
675
42
5
Table 13.17: (continued)
Slow and Modified Fatty Acids
OC EmerV.531Tallow Fatty Acid Emery 401 Fatty Acid Emery 876 Fatly Acii Emery 677 Fatty Acid Emery 878 Fatty Acid
I
36-44
Value 45-70
nm.. min. 19/81
44-53
34-44
80/95
35-45
2-6 2 max.
34-45
-
47M 7M5
IN.
Value 20&208 199-208 235-289 240-270 295-315
2.5
27
0.5
1
17
4
1
80% Monobasic acids, 2096 dibasic acids
I
SllowlCoconut Fatty Acid Blends
rrrcAcid Value 212-218 214216 216-222
EmerY. 515 Fatty Acid Emery 516 Fatty Acid Emery 517 Fatty Acid
Iodine Value
Titer, OC 3540 38-45 374.5
44-54 35-42 42 max
Emend.315 Linokk kid
Emery.610 Sova Fattv Acid Fitty Acld
Color % Trans. W550 nm., mn 72196
7w94 78194
Typlerl CompoJUon1
I
&tunlrd Arldc
5 max.
145-180
72/98
3
195-202
1525
125138
80/90
3
185205
15.23
138-145
72/98
3
197-203
0.5
I
Tr
0.5
Tr
3.5 16 11
Tr
0.5
Tr
Unulunlrd Acids
Tr
Tr
19.5
85.5
10.5
4
1
25.5
48
5
4
1 2 7 5 0
7
676
Industrial Solvents Handbook
Table 13.18: INDUSTRENE and HYSTRENE Fatty and Dibasic Acids (26)
SPECIflCATIONS
PRODUCT
lndustrene
365.
ACID DESCRIPTION [CTFA ADOPTED NAME) CAS NUMBER
Capryllc/Capric [Mlxture Caprylic/ Capric Acld) 67762-36-1
TITER C '
IODINE VALUE
6 Max
1 Max
ACID VALUE
355-369
% UNSAP MAX
1
TYPICAL CARBON CHAIN COMPOSITION XTRANS 440/550 nm,MlN
COLOR WVIBOND
MAX
SATURATED UNSATURATED OTHERS C8 ClO C l Z C14 C18 el81 C18:l
I
70/92 5.OY-0.5R 60 38
2
Available only In bulk splcal molsture levels are below 0.3%.
SPEClFlCATlONS
PRODUCT
Industrene
325
TYPICAL CARBON CHA
OMPOSITION
SATURATED C8 C10 C12 C14 C18 C i l
INSATURATED
TITER 'C
IODINE VALUE
ACID VALUE
% UNSAP MAX
Distilled Coconut (CoconutAcld) 61700-47-4
22-27
5-10
265-277
0.5
65/90 8.OY-0.8R 7
50 19 9
1
Hydrogenated Coconut [Hydrogenated Coconut Acld) 67701-05-7
23-26
3 Max 266-274
0.3
85/96 2.OY-0.2R 7
51 18 9
2
4
ACID DESCRIPTION (CTFA ADOPTED NAME) CAS NUMBER
lndustrene
223
XTRANS 44O/SSO nm.MlN
COLOR LOVIBOND
MAX
lndustrene, 328
,
Strlpped Coconut (CoconutAcld) 61700-47-4
27-30
5-10
252-260
0.5
ao/96 3 . 0 ~ 0 . 3 ~
55 24 12
Hystrene
Hydrogenated Stripped Coconut (Hydrogenated Coconut Acld) 143-07-7
26-33
1 Max
250-260
0.5
85/96 2.OY-0.2R I
55 23 12
5012
cia1
-
'HERS
95% Lauric [Lauric Acld) 143-07-7
41-44 0.5 Max 275-281 0.25
85/96 2.OY-0.2R
96 3
Hys trene 9912
99% Laurlc (Lauric Acld) 143- 07-7
43-45 0.2 Max 276-281
0.25
92/98 1.OY-0.1R
99
Hystrene
90% Mydstlc [Myrlstlc Acld) 044- 63 8
50-54 0.5 Max 238-245 0.3
85/96 2.OY-0.2R
2
92 4
2
95% Myrlstlc (MyrlstlcAcld) 044-63-0
52-54 0.5 Max 24 1-247
SP/9H
I
97 I
1
Hystrene
9512
9014 I lystrerie
9514
1
-
'bplrnl ~iiolslurelevels are below 0.3%.
0.3
1.OY-O.1R
(continued)
Acids
677
Table 13.18: (contlnued)
SPECIFICATIONS
PROWCl
Hystrene 9016
ACID DESCRIPTION (CTFA ADOPTED NAME) CAS NUMBER
90% Palmltlc (PalmltlcAcid)
TYPICAL CARBON 0
X
I COMPOSlTl
-
W P MAX
XTRANS 44O/SW nm.MIN
0.2
92/98
1.OY-O.lR Lovlbond
1
92
6
207-210
0.5
88/96
1.5Y-0.2R Lovibond
3
46
42
4.5-56.5 0.5Ma 206-210
0.2
92/98
1.OY-O.1R Lovlbond
2
51
45
2
55-57
0.2
88/96
1.5Y-0.2R Lavlbond
1
52
46
1
1
88/96
1.5Y-0.2R Lovlbond
2
44
52
2
I.OY-O.lR
2
43
52
3
TmR 'C
59-62
IODINE VALUE
ACID VALW
0 . 5 M ~ 214-219
COLOR MAX
SATURATED C14 C16 Cl8
E
-NSATURAED Ci0:I
1
57-10-3
lndustrene 5016
Double Pressed Grade (Stearic Add)
53-56
4-7
5
4
57-11-4
Hystrene 5016 NF-EXT
Triple Pressed Grade (Stark Add) 57-1 1-4
Hystrene 5016 NF-EXT-VEG
Trlple Pressed Grade (St-rlc Acid)
0.7Ma 205-210
57-11-4
lndustrene 4516
45% Palmltlc (PalmltlcAdd)
54-57
2Ma
204-209
57-11-4
Hystrene 4516
45% Palmltlc (PalmltlcAcld)
55-58
0.8Ma 203-209 0.25 92/98
Lovlbond
57-11-4
lndustrene R
Stearic Acld
52-64
10Ma
193-213
3
12 Gardner
57-63
3Mm
198-207
1
40186
3 Gardner
3
28
65
4
58-62
1M a
200-207
0.5
70192
5.OY-0.5R Lovlbond
3
28
65
4
0.5M a 200-206
0.3
92/98
I.OY-0.1R Lovlbond
2
28
66
4
195-201
0.5
70192
5.OY-0.5R lavibond
6
91
3
66.5-69 0.8Ma 195-200
0.3
92/98
1.OY-0.1R Lovlbond
4
94
2
66.5-69 0.8Ma
0.3
92/98
1.OY-0.IR Lavlbond
5 9 4
I
57-11-4
lndustrene B
Stearlc Acld 57-11-4
lndustrene 7018
70% Stearlc (Stearlc Acld) 57-11-4
Hystrene 7018
70% Stearlc (Stearlc Acld)
58-62
57-11-4
lndustrene 9018
90% Stearlc (Stearlc Acld)
65-68.5
2Ma
57-11-4
Hystrene 9718 NF-EXT
92% Stearic (Stearic Acld) 67-11-4
Hystrene 9718 NF-Em-VEG
92% Steadc (Stearlc Acld)
195-200
67-11-4
'I)rplcsl molsture levels are M o w 0.396.
(continued)
678
Industrial Solvents Handbook
Table 13.18: (continued)
SPECIFICATIONS
PRODUCT
Hysrrene 3022
TYPICAL CARBON CHAIN COMPOSlnON
X UNSAP MAX
%TRANS 440/550 m, MlN
193-20 1
1.5
50/90
60-63
178- 185
1.5
w90
68-71
169-177
1.5
50/90
27
63-67
170-180
1.5
50/90
23
72
5
67-72
165- 175
1.5
50/90
6
90
4
74-79
162- 169
2.0
ACID DESCRIPTION (CTFA ADOPTED NAME) CAS NUMBER
TITER C .
30% Arachidic
51-55
IODINE VALUE
ACID VALUE
COLOR BARDNER MAX
-
'HERS -
:14
ClE
SATURATED C l 8 C20 CZOaC22
6
30
30
30
4
14
26
55
5
C22
and Behenic (Hydrogenated Menhaden Acid) 112-85-6
Hystrene 5522
55% Arachidic
and Behenic (Hydrogenated Menhaden Acid) 112-85-6
Hystrene
60% Arachidic
6022
and Behenic (BehenicAcid)
10
60
3
112-85-6
Hystrene
70% Arachidic
7022
and Behenic (Behenic Acid) 112-85-6
Hystrene
90% Arachidic
9022
and Behenic (Behenic Acid) 112-85-6
Hys trene 9222
92% Behenic (Behenic Acid)
2
3
93
2
112-85-6
-
Typical moisture levels are below 0.3%.
SPECIFICATIONS
PRODUCT
Hystrene 2290
ACID DESCRIPTION (CTFA ADOPTED NAME) CAS NUMBER
90% Erucic 112-86-7
TYPICAL CARBON CHAIN COMPOSITION
TITER 'C
IODINE VALUE
ACID VALUE
X UNSAP MAX
27-37
65-90
160-185
2.0
COLOR GARONER MAX
5
. Cia
1
SATURATED h UNSATURATED C20 C22 C24
3
90
4
OTHERS
2
(continued)
Acidr
679
Table 13.18: (continued)
I
SPECIFICATIONS
PRODUCT
Hystrene I835
ACID DESCRIPTION (CTFA ADOPTED NAME) CAS NUMBER
Soap Blend (MtxtureTallow/ CoconuL Acld) 07701- 06 -7
TITER 'C
IODINE VALUE
ACID VALUE
X UNSAP MAX
40M;lx 36-42 214-222
45-65 201 -206
Industretie 143
Tallow lype 01790-37-2
Xb43
Industrene 145
Tallow Q p e 01700-37-2
44-41) 36-44 198-207
1
TYPICAL CARBON CHAIN COMPOSITION XTRANS 440/550 nm, MlN
MAX
78/94 4.OY-0.4R 10 Lovibond
1.5 1.0
COLOR
5 Gardner 80/93
6
18
3
33
3
5,
3 .24 17
5
43
5
3
:J
39
I
3
3
22
26 25
Typlral iiiolslure levels nre below 0 3?4$ -
-
TYPIC
SPECIFICATIONS
PRODUCT
ACID DESCRIPTION (CTFA ADOPTED NAME) CAS NUMBER
TITER *C
IODINE VALUE
ACID VALUE
X UNSAP MAX
COLOR
MAX
:ARBON CHAIN COMPOSITION
SATURATED I 4 C16 C18
Industrene 105
High-Titer Oleic (Oleic Acid) 112-80-1
14 Max
85-95
195-204
1.5
6 Gardner
6
70
Industrene 106
Oleic (Oleic Acld) 112-80-1
6 Max
95 Max
198-204
1
3 Gardner
6
72
lndustrene 205
Oleic (Oleic Acid) 112-80-1
14 Max
85-95
195-204
1.5
5.OY-0.5R Lovibond
5
72
lndustrene 206
Low-Titer Oleic (Oleic Acld) 112-80-1
6 Max
95 Max
199-204
1
7.OY-1.2R Lovibond
6
72
lndustrene 210
Canola 67701-08-0
13 Max 100- 125 190-210
10Y-1.5R Lovibond
63
Spica1 rnolsture levels are below 0.3%. 1
(continued)
680
Industrial Solvents Handbook
Table 13.18: (continued)
SPECIFICATIDNS
PRODUCT
lndustrene 120
%TRANS 440/550 m,MlN
COLOR QARDNER MAX
e
TITER .C
IODINE VALUE
ACID VALUE
% UNSAP MAX
14-18
185-200
197-202
1
5
7
4
20
16
52
I
30-38
90-112
198-206
2
4
18
10
31
32
5
4
25Mtuc
135-150
195-201
2
75/85
2
4
5
24
57
8
2
26Mm
127-138
195-203
2
70185
3
11
4
24
53
6
2
ACID DESCRIPTION (CTfA ADOPTED NAME) CAS NUMBER
Linseed (LinolenicAcld)
-
UNSATURATED
SATURATED
08424-45-3
lndustrene
OlelcLlnolelc
130
07701-00-8
Industrene 225
(Llnolelc Acld)
soya 67701-08-0
lndustrene 226
soya (LlnolelcAcld)
I I
07701-08-0
-
VpleaI molsture levels are below 0.396.
TYPIC& CARBON CHAIN COMPOSIT
SPECIFICATIONS
'RODUCT
ACID DESCRIPTION (CTFA ADOPTED NAME) CAS NUMBER KOSHER
Hystrene 45% Palmitic 4516 NF-FC (palmitic Add)
UNSAP
MAX
%TRANS W/SW nm,MIN
0.25
206-210
55-57
58-62
%
TITER 'C
55-59
UNSATURATED u)tl cmz C W 3
E
-
COLOR
IANRATED A ClE ClE
92/98
1.OY-O.1R Lovibond
, 4 4 5 4
0.2
92/98
1.OY-O.1R bvibond
1
51 45
2
0 . 5 M ~ 205-210
0.2
92/98
1.OY-O.1R Lovibond
1
52 46
1
0 . 5 M ~ 200-205
0.3
92/98
1.OY-O.1A Lovibond
2
28 66
4
IDDINE VALUE
ACID VALUE
0.6Mm 203-209
MAX
1
57-11-4
Hystrene 5016 NF-FG
Trlple Pressed Stearic (Stearlc Acld)
1.5-56.5 0.5Mm
57-1 1-4
Hystrene 5016 NF-FGVEG
Triple Pressed Stearic (StearicAcid) 57-11-4
Hystrene 7018 FG
70% Stearic (Hydrogenated Tallow Add) 57-11-4
lndustrene 87 18 FG
87% Stearic (Stearic Acld)
66-68
1M a
195-200
0.5
92/98
1.OY-O.IR Lovibond
9
89
2
56.5-69
0.5Mm
195-200
0.3
92/98
1.OY-0.1F Lovibond
4
94
2
2 6 M ~ 127-138
195-203
2
70185
3 Gardner
11
4
57-11-4
Hystrene 9718 NF-FC
92% Stearic (StearicAcld)
lndustrene 226 FG
Dlstllled Soya (Soya Acld)
57-11-4
07701-08-0 Malerials available In Kosher grade. Typlcal moisture levels are Ixlw 0.396.
24
53
6
2
(D
8 U
tt
Acids
681
682 Industrial Solvents Handbook
Acids
683
Table 13.20: Proctor 81 Gamble Fatty Adds (39)
FattyAcids
Acid V k e
Physical Properties
I
R+37.44
21.25
12 mm
2mposition (GC) raximate
50% by wt. in water; ethyl alcohol; benzene; mineral spirits
Amine component . .. . . . . . . . . . . .78% by wt Neutral equivalent as a base . .. . . . 120-126 Color, APHA.. . . . . . . . . . . . . . .. . . . . 100 (max) Flash point, Tag closed cup.. . . . . . . . . 120°F Freezing point.. . .. . . . . . . . . . . . below -20°C Specific gravity at 25/25"C.. . . . . .0.98-0.99 Viscosity at 25°C. . . . . . . . . . . . . .. . . . 7.5 cp pH ............................... 10.5-11.5 Weight per U.S. gallon.. . . .. . . . . . . . . .8.2Ib
.
Amine CS-1246" . . . .. . . . . . . . .97.5% minimum . . . ..Colorless topale yellow mobile liquid Boiling point.. . .. . ... ..... . . . . . . . . . . .73-75'C at 10 torr Neutral equivalent (calc) . . . . . ........143 Density at 2 6 C . .. . ....... . ... . . ....1.072g/mI pH of 0.1M soln. (20'C) . . . . . . . . . . . . . .10.2 Principal component
Soluble at >50% by wt. in water; ethyl alcohol; benzene; mineral spirits
ZOLDINEEZT-55
-
Typical Physical Properties of CS-1246 Specific gravity, 30/20"C . .1.085 Boiling point, "C at 15 mmHg , . 71 Freezing point, "C.. ... . . .. o Surface tension, dynedcm at 25°C . . .36.5 pH . .&9 Soluble In water, ethanol, benzene, chlorinated hydrocarbons, and acetone Flash point, Tag closed cup, OF.. ... . . 175
... .... . .. .. . ._.... .. . . ... . . ...... .. ........ .. ... .. .. . .. .. .. ... ..... .
.
Principal component . . . . .. . . .. . . . .55% solution in water Specifications Appearance .. ... . ....... . . . . . . . . . . . .Colorless topale yellow mobile liquid Melting point .. . . . . . .. .. . ... .. . , .. . . .54.5"C (active component, Purity, % by wt. . .. .. . . . .. . . . . .. .97.5 min. Neutral equivalent . . .. ... . . . . . . .. . . . ,273-278 Total Oxazolidines, % by wt. . ..99.5 min. .Density at 25'C . ... . . .... . . . . . . . . . .1.125~/ml Color, APHA.. , . . , , . , . .... ..,.. .lo0 max. pH of 0.1M soh (20°C) . ..... . . . .. .. .9.4 Water, 96 by wt. , . . . . . . .. . . . .. .0.5 m a . Active ingredient soluble at >50% by wt. in water; ethyl alcohol; at 25 gl100 ml in benzene 31 25%; at 1.2 g/lOO ml in mineral spirits' at 75°C.
. ..
. .. .. .
when anhydrous
Table 14.55: Ashland Amines (69)
Product
%?
AMP-95
0.942
Arnlne % by wt Bawd on Total Alkallnlly
Freezing
Color p1-CoScale Max 28
Flash Polnl "F Open Cup 172
*C
&Itvl Amine
0.742-0.747
76.0-81.O
97.0
- 49
0.86450.8655
Appcox. 134.5
98
15 20
30
Cvdahmyiornine
72
-18
DibutylAmlne Dlethanolomlne
(25"/25C) 0.760 1.090-1.094
155-163 Approx187
98 98.5
15 15
124 280
- 62 28.0
Lb. erGal.0 at& 7.85 (25%) 6.20 7.19 (25%) 6.32 9.14
(50mml 54.0-59.5 195215
98.5 89.093.0
15
m
CM
Kerosene
aboul 005
about 0 01
about 0.02
about 0.03
3.4
0.2
4
08
Methanol
CM
CM
CM
CM
CM
670
>m
CM
'1 1,l-Trichloroethane
about 0 6'
about
about 1.Q
about 2.5'
CM'
aboul 15'
about280'
CM'
'Methylene Chloride
CM'
IM'
CM'
CM*
CM'
about 180'
>500'
CM'
O W
I
CM CM
mtinued)
Amines
721
Table 14.57: (continued)
Mineral Oil . . . .
DI-
Monoethanolamlne
ethanolamine
about 0.06
Trlethanolamlne85
TrlethanolamlneW
MonoDllsoproIsopropanol- panolamlne amine
Trllsopropanolamine
about 0.02
about 0.03
about 0.03 0.2
0.05
Mineral Spirits . . . about 0.08 about 0.01
about 0.03
about 0.04
0.4
0.2
5
Naphtha VMP. . . . about 0.07
about 0.03
about 0.06
0.4
0.3
6
.
about 0.01
Isopropanolamlne Mlxture
about 0.4
.Y
'Perchloroethylene.. . . . . . about 0.1'
about 0.02'
about 0.1'
about 0.17'
about 0.7'
about 0.9'
about 160'
Pine Oil.. . . . . . . . CM
CM
CM
CM
CM
110
90
CM
Toluene.. . . . . . . . about 0.7
about 0.1
about 0.6
about 1.7
CM
12
340
CM
Water. . . . . . . . . . . CM
CM
CM
CM
CM
1200
>500
CM*
Refractive Indices,n,, of Aquews Ethanolamine Solutions at 7pF (2%) 1.50 1.48 1.46
3 n z w
DIETHANOLAMINE
1.44 1.42
2f 1.40 IT
B
LT
1.3 1.36 1.34 1.32
0
10
20
30
40
50
60
70
80
90
100
CONCENTRATION OF AMINE, WEIGHT %
Refractive Indices, n,, of Aqueous IsopropanolamLne Solutions at 7Pr: (25°C) 1.48
1.46
3 1.44 n z
1.42
I
&
2 1.40 lL
W
fr 1.38
1.36 1 34
0
10
20
30
40
CONCENTRATION
50
60
70
OF AMINE, WEIGHT
80 Yo
90
100
(continued)
Industrial Solvents Handbook
722
Table 14.57: (continued)
Freezing Curves of Aqueous Ethanolamine Solutions Diethanolamine 120
100
9- 80 60 40
a I I
-40
Ill=..
-40
0 -20
I
-40
I
.m
.d
-40
I
60I 0 10 20 30 4G 50 60 70 801 90 100 CONCENTRATION OF AMINE, WEIGHT Yo I
I
L.F.GJ
LF.G:
I
LL
1
-40
I
I
I
I
III
-40
I l l
-40
I I I III I I I I I I I. 1
-40
Freezing Curves of Aqueous Isopropanolamine Solutions Monoisopropanolamlne
Dilsopropanolamine
40
30
g3
10
+ao
pt
g
-10
I
w -20 I-
-30 -40
0
10
20
30
40
50
60
70
CONCENTRATION OF AMINE, WEIGHT %
80
90100 CONCENTWTION OF AMiNE. WEIGHT YO
I
&.G.-w' LF.G.- 85'
(continued)
Amines
723
Table 14.57: (continued)
Freezing Curves of Aqueous Isopropanolamine Solutions (conk.) Triisopropanolamine
Isopropanolamine Mixture 40
120 40
100
$ 8 0
U
20
G 60 ( I 3 I-
40
5a
20
a
0
20
10
10
0
O
-10
-20
-20
-30
I-
9
W
-20
-30
60
-40
-30
1
I
I 1 7
I
I
I
.
I-
I 4
10 20 30 40 50 60 70 80 CONCENTRATION OF AMINE. WEIGHT Yo 0
I
2
W
-10
-40
CONCENTRATION OF AMINE, WEIGHT %
0 w’ a 3 :
.20 .10
5 O I-
30
30
90 100
L.F.G.‘
pH Values of Aqueous Ethanolamines Diethanolamine
Monoethanolamine
12.8 12.4 12.0 s11.6 11.2 10.8
10.4 0
5
10
20
15
25
30
11.8 11.6 11.4 11.2 11.0 I,lO.S 10.6 10.4 10.2 10.0 9.8 0
5
10
15
20
25
30
CONCENTRATIONOF AMINE, WEIGHT %
CONCENTRATIONOF AMINE, WEIGHT %
Triethanolamine
11.4 11.0 10.6 I
a
10.2 9.8 9.4 0
5
10
15
20
25
30
CONCENTRATION OF AMINE, WEIGHT %
(continued)
724
.-M .Y M
8
v)
Industrial Solvents Handbook
..
rY
Amines
725
c
Industrial Solvents Handbook n
1
E 6H
UJW
r
8 3
8 '3tlflSS3tld lV101
8
0 cu
Amines
727
a
a: W a
3s
z8
728
Industrial Solvents Handbook
R
Amines
729
9 8
8 8 8
Ln
.. rf
730
Industrial Solvents Handbook
W'
d
54;
W
a
wp
..
e,
v)
cc 0
jE
0
a
Y
-2 v) 0
0
LI
0
m
Amines
731
732
8 aJ a
S
U
(3
.-
s
v
w
Y
8
Industrial Solvents Handbook
L?
0
v1
c1
-s
1 ,
c1
W
0 In
-
5:
5
g a s 8
Amines
8
733
734
1
Industrial Solvents Handbook
S
2
0
----T--
i
'
II
Amines
735
736
Industrial Solvents Handbook
Table 14.59: Proctor 81 Gamble Tertiary Amines (39)
Chemical Pmperties
AT4295
AT-1495
AT-1695
% Total Amine
AT^
AT421416
97.3 min (98.4)
97.3 min (98.4)
% Non-Terminal Amine
6.0 NIX (5.21
6.0 max (5.0)
6.0 max (5.6)
6.0 max (5.1)
(5.0 1
YONon-Amme Material
2.0 max (1.5)
2.0 mm (1.5)
2.0 max (1.7)
2.0 max (1.5)
2.0 max (1.5)
Amine Value
254-264 (2631
226-234 (232)
203-211 (2081
246-254 (2521
236-244 (243)
0.20 mm
0.20 max
0.20 max
(0.11
0.2 mox (0.11
0.2 max
Color-APHA
35 max (151
25 max (19)
35 mox (291
35 max (171
35 mox (19)
Appearance
Clear to slight haze
slight haze
Clear to
Qear to slight haze
Clear to slight hoze
Qear to
Equivalent Weight
(213)
(242)
(2701
(2231
(231 1
% Moisture
(0.11
(0.11
6.0 max
(0.11
Physical Properties
C10 d, lower c12
1.0 M
1.0 max
X
(0.0) 95.0 min
3.0 max (1.0)
(1.3)
95.0 min (9Z5)
5.0 m u (2.2)
31 Ot -1.5 (3O.d
49.0 t/-1.5 (48.9)
2.0 max (0.3)
2.0 max (1.4)
95.0 min (97.4)
1.0 max (0.81
9.5 +/-IS (911
C18 & Higher CAS No.
pi-1.5
(0.0)
(9821
C14
C16
slight haze
01 max (0.0)
1.0 max (0.31 112-18-5
112-75-4
112-69-6
41.5+/-1.5 (41.4)
112-18-5 112-75-4
112-18-5 112-754 112-69-6
Amines
737
Table 14.60: Occidental Ethanolamines (27) Ethanolamines Products, Grades and Specifications
MEA 99
DEA 99
99.0 min. 0.5 max. 15 6 1.O-62.0 0.3
1.0 max. 98.5 min. 1.0 max. 15 104-106 0.15
Miscellaneous Grades
PEA 60
PEA 85
Monoethanolamine. wt. YO Diethanolamine, wt. YO 'fi-iethanolamine. wt. YO Ethylene glycol, wt. YO Heavy ends & others, wt. YO Color (APHA) 'Lc Water, wt. O h max.
5 max. 40 max.
2 max. 15 max. 85 min. 2 max. 4 max. 1000 1.5
Specifications
Monoethanolamine. wt. YO Diethanolamine. wl. Yo Tiiethanolamine, wt. YO Color (APHA). max. Apparent equivalent wl. Water, wt. O h max.
Low Freeze Grades
Ethanolamines have relatively high freezing points, and in win~ e respecially , in northern climates. they can become too viscous to pump. For customers in
Low Freeze Grades
Monoethanolamine, wt. YO Diethanolamine, wt. Yo Triethanolamine, wt. YO Color (APHA), max. Water, wt. O h max. Freezing point, (T)
60 min. 5 max. 4ma. 1000 2
,
TEA85
TEA97HC
0.5 max. 15.0 max. 85.0 min. 50 140-145 0.2
0.5 max. 3.0 max. 97.0 min. 250 145-150 0.2
,
these areas whose applications are not sensitive to water, OxyChem offers each ethanolamine in a "Low Freeze" grade. Low freeze grade ethanolamines are produced by the addition of 15
percent by weight of deionized water. They afe blended in the delivery vessels prior to each shipment, and therefore, are not stored as finished products.
7
MEA 99 LFG DEA 99 LFG TEA85LFG TEA97LFG 84.0 min. 0.5 max. 25 15.5 -12
0.9 m a . 83.5 min. 0.9 max. 25 15.5 1
0.5 max. 13.0 max. 72.0 min. 50 15.5 -5.5
0.5 max. 2.7 max.
83.0 min. 250 15.5 -5.5
(continued)
738
Industrial Solvents Handbook
Table 14.60: (continued) Compatibility Acceptable Metals
AcceptableNon-Metals
Carbon steel (to 8OOF) Copper (to 80°F) Hastelloy B 8 Hastelloy C 8 lnconelO Monel8 Nickel Nickel resist 304 Stainless steel 316 Stainless steel 20 Cb 3 Stainless steel Tantalum Titanium
Butadiene-acrylonitrile (NBH. Uuna-NO) (MEA only) Carbon-graphite. resin impregnated Chlorinaled polyether (TEAonly) Epoxy compounds Ethylene propylene diene (EPDM) Ethylene-terefluoroethylene(ETFE. TefzelO) Fluorinated ethylene propylene (FEP) Fluoroelastomers (FKM. Viton A@. Fluorel@) Modifled phenylene oxide (NoryI8) Natural rubber Polybutadiene (Isoprene) Polyamides (Nylon@12. Nylon@66) Polychloroprene (Neoprene@) Polyester terephthalate (PET) Perfluoroalkoxy (PFA) Perfluoroelastomers (FPM. K a l r 4 . Chemraz@. Kel-F@) Polypropylene (except TEAJ Polysulfone (except T W Polyvinylidene fluoride (PVDF. K y n d ) (TEA only) Vinyl ester
Technical Data
I
Physical Properties
DEA HN(CH,CH,OH)z
61.08
105.14
149.19
Acidity/alkalinity, (pH)
11.5-12.2
10-12
10-12
Boiling point 63 760 mm Hg, (OC/"F)
170/330
Molecular weight, (g/mol)
I
TEA
MEA H N CH CH 0H
Chemical formula
N(CH,CH,OH),
268/514 (decomp.) 335/635 (decomp.)
i
44.1
Critical pressure, (Atmos.)
32.3
24.2 ~~
Critical temperature, ("C) Coefficient of cubical expansion, ( / T I applicable range, ("C)
341.3
442.1
514.3
0.00078
Q.00065
0.00055
20-30
30-40
20-30
8.487
9.104 (@3O0C/2O0C)
9.354
1.008
1.093
1.120
Dielectric constant - liquid
37.7
22.81
29.36
Equivalent weight, (g/mol)
6 1-63
104-108
140-149
Density @ 20°C. (Ibs/gal) @ 25°C. (g/ml)
Explosive limits in air, vol. Yo - lower
- upper
~
-1
5.5 17.0
Evaporation rate @ 25 "C n-butyl acetate - (=1.00) n-butyl acetate - (155 seconds)
16.2 Specific conductance, ohm-', 25"C(77"F) 18.9 x 10-5 Specific heat of liquid, cal/g. 19OC . . . . . 0.55 0.99 Btullb. 66°F . . . . . Latent heat of vaporization, cal/g, 210°C . ,400 Btu/lb. 410°F ,720 Flash point (TOC). "F . . . . . . . . . . . . . . . . ,310 " C . . . . . . . . . . . . . . . . ,154.4
Table 14.100: Dlmethylformamide ( 1 7) DMF
(CH,), NCH=O
DMF, dimethylformanide, i s a uniquely versatile and powerful solvent with the following general properties:
Appearance . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .Colorless,mobile liquid Molecular weight . . . . . . . . . . . . . . . . . . . . . . . . . . .73.09 Boiling point, 760mm. OC . , . . . . . . . . . . . . . . . . . . ,153 (307°F) Freezing point. "C . . . . . . . . . . . . . . . . . . . . . . . , . -61 (-78°F) Specific gravity Oo/4"C . . . . . . . . . . . . . . . . . , . . . . .0.9683 0.9445 25'/4OC . . . . . . . . . . . . . . . . . . . . . . . Density. Ibs/gal. 20°C . . . . . . . . . . . . . . . . . . . . , , . .7.92 Refractive index. NoZSoC . . . . . . . . . . . . . . . . . . . .1.4269 Vapor pressure. 25'C . . . . . . . . . . . . . . . . . . . . . . . .3.7mm Vircaity, ZS0C ............................ 0.802cp Surface tension. 25°C . . . . . . . . . , . . . . . . . . . . . . , .35.2 dyncs/cm Specific heat (liquid. 20°C) . . . . . . . . . . . . . , . . . . .0.49 Btu/lb/OF . . . . . . . . . . . . . . . . . . . . . . ,248 Btu/lb H u t of vaporiration H u t of combustion . . . . . . . . . . . . . . . . . . . . . . . . . ,457.5 kg cal/gm mol 11,280 Btu/lb Thermal conductivity (at 23.S'C) . . . . . . . . . . . . , ,440 d / s s cm"C
Flash point, T.O.C., OC . . . . . . . . . . . . . . . . . . . . .67 (153°F) Ignition temperature. "C . . . . . . . . . . . . . . . . . . . . . ,445 (833'F) Flammability limits in air Iowa . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2.2Vol96 upper . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 15.2vol96 Dielectric constant. Z5'C . . . . . . . . . . . . . . . . . . . . . .36.71 Dipole moment, 20°C . . . . . . . . . . . . . . . . . . . . . . . , 3 3 2 Debye Uniu Hygroscopicity. 3OoC (300 h n @ 50% RH) . . . . ,3496 gain Relative evaporation rate (butyl acetate = 100) . . . I 7 Solubility parameter . . . . . . . . . . . . . . . . . . . . . . . .12. I Ionization constant ( @ 20°C) . . . . . . . . . . . . . . . . .IO-'* Azeotropes:
DMF (18.7 w 96 ), pxylene (81.396 ) . . . . . . . . . . .135.I"C at 760mm DMF (69 w 96 ), formic acid ( 3 1 wt 96). . . . . . . . .162.4OCu 760mm DMF ( 7 wt % ), tetrachlorethylenc (93.0 wt 9%). . . . 1 1 7 . 5 T at 730mm
(cont inued )
774
Industrial Solvents Handbook
Table 14.100: (continued) Evaporation Rate Atmospheric conditions
% Evaporation
Time. Hours ~
0 20 40
0 8
16 26 34 44
60 80
100
Hem of Mixing DMF-Water . Temp
30'C. .
Wt % DMF in Aqueous Solution
Btu/lb DMF
5 10 15 20 25 30 35
09
82.5 75 73.5 70 66
64
Flash and Fire Point of DMF Water Solutions. . . Composition. DMF.H& by Wt Mixture-DMF
Flash Point 'F
100
145 165 215 210
90 70 65 60 50
Fire Point 'F
150 1 70 230 225
none
none
none
none
Table 14.101: Surface Tension and Density of DMF-Water Mixtures (77)
Amines
775
776
Industrial Solvents Handbook
Table 14.102: (continued) Polymer Solvent The principal use of DMF is as a solvent in the spinning of acrylic and polyurethane fibres. This is e s p e c i a l i d outlet but illustrates the solvent power of DMF for polymers of high moloculer weight. Various polymers which are soluble in DMF together with some which are inroluble are shown in the following liats: Soluble polyacrylonltrile oolvurethenes pol;methylmet hacrylate cellulose ecetate cellulose nitrate cellulose scotate butyrete ethylcellulou cyanoethylated cellulose polystyrene polyvinyl chloride polyvinyl elcohol polyvinyl ecetate elkyds phenol-formsldehyde resins coumarone-indene resins shellec ester g u m kauri g u m
Insoluble polyethylene oolvuropvlene polytetrafluoroethylene seturated polyesters uree-form;ldahyde resin8 neturel rubber b u t y l rubber styrene-butediene rubber nylon 66. 6, and 610
Not only does DMF allow many polymers of sparing solubility 11 be brought into soiution I t economical concentrations, but when used either alone or as a booster solvent it yields solutions with lower viscosities and higher solids content than can be obteined with other solvents. It is therefore suggested as an enrective solvent for use in the formulation of protective coatings end films, adhesives, and printing inks.
Reaction Solvent and Catalyst The use of DMF alone or as a component of e solvent system confers a number of advJntage1. the relative importance of which depends upon the particular application, but the following may be specially noted : (J) its high solvent power can increase the effective conceiltration of one of the reacting Special;
( b ) it her a high dielectric conatent:
Table 14.103: Dimethylacetamide ( I I ) DMAC PHYSICAL PROPERTIES OF DIMETHYLACETAMIDE:
B
Formula. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . CH,CN(CH,), Molecular weight. . . . . . . . . . . . . . . . . . . . . . . . . . . . .87.12 Boiling point, . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . ,165.5"C Vapor pressure at 25°C. . . . . . . . . . . . . . . . . . . . . . . .1.3 mm Freezing point. . . . Specific gravity (15.5"C) . . . . . . . . . . . . . . . . . . . 0.92 cp Refractive index . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 1.4356 Dielectric constant. . . . . . . . . . . . . . . . . . . . . . . . . . . . .37.8 Dipole moment (in dioxane). . . . . . . . . . . . . . . . . . . .3.79 Flash point (Tag Open Cup). . . . . . . . . . . . . . . . . . ..70"C Thermal conductivity (22.2"C). . . . . . . . . . . . . . . . .,416 x 10-6cal/sec/cm/oC Specific heat (liquid, 0 to 87°C). . . . . . . . . . . . . . . ..0.485 BTU/lb"F Heat of vaporization at 165°C (cal'd) . . . . . . . . . . . .10,360 cal/g mol Heat of combustion (20°C). . . . . . . . . . . . . . . . . . . .,608 k cal/g mol Flammability limits in air at 740 mm Hg and 160°C 2.0'30 by VOI Lower. . . . . . . . . . . . . . . . . . 11.5% by vol Upper . . . . . . . . . . . . . . . . . .
(continued)
Amines
777
Table 14.103: (continued) Vapor pressure:krnperahm, OC
Pmwm, mm Hg
25 40 70
1.3 3.4 18 46 108 230 460 758
90 110 130 150 165.5
Azeotrope D M A C (77.2 wt %)-acetic acid (21.1 wt %)-170.8"C
at 760 mm
Solubility-Completely miscible with water, ethers, esters, ketones, and aromatic compounds. Unsaturated aliphatics are highly soluble, but saturated aliphatics have limited solubility. Solubility at 25OC g A 0 0 0 DMAC
Iso-octane Di-isobutylene N-hexane N-Heptane Cyclohexane Cyclohexene Kerosene
33 Compl Misc "
'L
31
Compl Migc "
65%
S S S S S S
< 0.002Y0or > 80% S S S S S S S
S = soluble at 10%
S
808
Industrial Solvents Handbook
Table 14.170: Surfactant Properties of Surfadone LP Products (49) Solvent
SURFADONE' LP-100
SURFADONE' LP-300
Maximum concentration in H20 (YO) Minimum static surface tension (dynes/cm) Draves wetting time (sec.) Dynamic surface tension (dynes/cm)") HLB
0.124
0.002
28 4
26 300
29 6
N/A 3
(1) at a surface age of one second
Table 14.171: Low Concentrations of Surfadone LP Products Lower Surface Tension of Water (49) c
80
,
60 50 -
0
70
SURFADONE. LP-io0
\ \
A SURFADONE. ~P-300
40-
30 20
Table 14.172: Draves Wetting Time for Surfadone LP Products with SDS (seconds) (49) with
SURFADONE' LP-100 SURFADONE' LP-300 SDS
0.196 Solution
0.008% SDS
with 0.018% SDS
3.5 >300 17
2.4 5.4
5
P a r a f f i n oil
Cellulose n i t r a t e
25
P a r a f f i n wax (hot)
Copal g u m
>5
P i n e oil
P
D i m ethylamine
109
Resin
>5
E s t e r gum
5'
Shellac
>5 (5
Ethanol
X
Sulfur
2 -Ethylbutan01
P
Trimethylamine
Ethylene glycol
X
Turpentine
Ethyl e t h e r
1 .
P o l y v i n y l acetate
>5
Glycol e t h e r
z
Polyvinyl butyral
>5
Polyvinyl c h l o r i d e
5'
Table 14.192: N-Ethyl Morphollne (2)
34 X
Table 14.193: N-Phenyl Morpholine (2)
This cyclic tertiary amine is a water-white liquid miscible with water. It may be used as a solvent far oils, dyes and resins, and as an intermediate in the synthesis of rubber acceleraton, emulsifying agents, drugs, and dyes.
. . . . . . . . . . . . 138°C. Specific Gmvity a t 2O/2O0C. . . . 0.916 Boiling Point
Boiling Point a t 760 mm. Melting Point
. . . . . . 268OC.
. . . . . . . . . . . . 57OC.
815
Esters
FORMATES Table 15.1: Methyl Formate (2) HC OOC H3 Methyl formate i s o colorless flammable liquid with a pleasant ethereol odor. I t w i l l dissolve cellulose ethers and esters but w i l l dissolve them more readily when mixed with other solvent esters or the less volatile hologenated hydrocarbons.
Acidity Boiling point Color Distillation range Electrical conductivity a t W C Flssh point Melting point Odor initial Odor reaidual Purity Refractive index a t 20°C Solubility in water at 20'C Solubility of water in solvent a t 25°C Specific gravity a t 20/WC Vapor pressure
0°C
Neutral to mrlhyl orange (methyl formate hydrolyzes in presence of water) 31.8' C Water-white Below 31.5'C h'one Above 35.O'C None 3.6 X 10-8 reciprocal ohma -32°C
-99.8'C Pleasant, ethereal Non-residual 95% to 100% eater, by w t 1 3431
30% by vol 24% by vol 0.950 t o 0.98)
i95.0 m m 309.4 m m 400.0 m m 476.4 m m 600.0 mm 707.9 m m
10°C 16°C 20°C 25.8'C
3J'C
of Mercury of Mercury of Mercury of Mercury of Mercury of M e r c u j
Table 15.2: Ethyl Formate (2) HCOOC2H5
Fonnosol
Ethyl formate i s a water-white, highly volatile and unstable liquid with a pleasant odor resembling peach kernels. It i s portly soluble i n water and miscible with benzene. I t i s a powerful solvent for cellulose nitrate and acetate, yielding solutions of unusual low viscosity which have a tendency to c h i l l . It i s an important fumigant and larvicide for the treatment o f tobacco, cereals, dried fruit and similar products. I t i s used as a chemical intermediate i n the manufacture o f such medicinals as sulfadiazine, thiamin (Vitamin B l ) , and perfumes and synthetic flavors.
816
(continued)
Esters
817
Table 15.2: (continued) Acidity
Neutral to methyl orange (it hydrolyres in the premnce of water)
Boiling point
54.3'C
Color
Water-white
Distillation range Electrical conductivity at 25'C Flnah point Freezing point Purity Refractive index at 2O'C Specific gravity at 20/ppaC Solubility in water at 20°C Solubility of water in solvent at m-c Vapor pressure at 20.6'C at 30.20c Weight per gal at W F
51"JS'C
IRM than 1.45 X 1 0 1 recip o h m
- 19oc
-80.5"C 95% to 1% 1.3604 0.900 to 0.930 10% by vol 17o/c by vol
200 nun of Hg
300 mm of Hg 7.61 Iba
Table 15.3: Butyl Formate (2) HCOOCH2CH2CH2CHg Butyl formate i s a colorless liquid, miscible with alcohols, ethers, oils, hydrocarbons and so forth. I t w i l l dissolve cellulose nitrate, some types of cellulose acetate, and many cellulose ethers. Butyl formate w i l l also dissolve many natural and synthetic resins such as copals, dammar, elemi, mastic, shellac, cumar resins, ester gum and alkyds i n the presence of ethyl alcohol. I t i s used as an intermediate and i n perfumes. Acidity Ester content Boi Iing range Specific gmvity
0.02% max. 85% min. 96"-110°C.
0.885-0.9108
Table 15.4: Amyl Formate (2) HCOOC5H, Commercial amyl formate i s an anhydrous, colorless liquid composed of a mixture of isomeric amyl formates with the isoamyl formate in predominance. This mixture i s miscible with oils, hydrocarbons, alcohols, ketones and so forth. I t i s a solvent For cellulose esters, "Cumar", copal, gum esters, etc. I t i s able, when mixed with an alcohol, to dissolve shellac and alkyd resin. I t i s a less odoriferous and more energetic solvent than amyl acetate. I t also has both a lower boiling point and a greater speed of evaporation. n-Butyl acetate and amyl formate have similar volatility and have substantially the same solvent power which permit free interchange of these only as far as these properties allow. Acidity Boiling point Boi Iing range Flash paint Specific gravity
0.05% max. 130.4"C. 11Oo-13O0C. 80°F. 0.880-0.885
818
Industrial Solvents Handbook
ACETATES Table 15.5: Methyl Acetate (2) CH3COOCH3 Methyl acetate i s a water-white flammable, readily hydrolyzable liquid, with a fragrant odor. This low-boiling solvent was first prepared i n 1835 by reacting acetic acid and methanol. I t i s miscible with most organic solvents and w i l l completely dissolve cellulose nitrate and acetate, ethyl cellulose, resins such as ester gum, rosin, "Cumar", elemi, phenolics, and oils such as corn, linseed, castor, neatsfoot, chinawood and cottonseed. I t w i l l only partially dissolve shellac, manila, dammar, pontianac, Beckacites and alkyds. I n many respects, methyl acetate resembles acetone as a solvent, particularly as to its boiling point, solvent power and miscibility, but its tendency to hydrolyze to methanol and acetic acid, i n the presence of water, limits its wider use in the industries. Methyl acetate i s usually admixed with higher boiling solvents. It i s used i n lacquers, paints, varnishes, enamels, perfumes, dyes, dopes, plastics, and synthetic finishes as well as a substitute for acetone. Acidity (M acetic) Boiling point Dirtillation range Coefficient of expansion (per 'C) a t 20°C Color Critical temperature Critical pressure Dielectric constant a t 20°C Dilution ratiw Toluene Petroleum naphtha Electrical conductivity at W C FlMh point (A.S.T.M. Open Cup)
0.005%, mnx 58.9-c
55-5E-c 0.001390 Water-white 233.7'C 40-3 atm 7.3 f 0.2 2.9 0.9 3.4 X 10-6 mho -15°C
Freezing point Heat of combustion Heat of vaporization Non-volatile matter Refractive index nt 20'C Solubility in water a t 20°C Solubility of water in solvent a t W C Specitic gravity a t 20/WC Surface tension a t 20°C Vapor pressure a t 20°C Viscwity a t 20°C Weight per gal a t 20°C
-BB.lQC 6371 callg 104.4 cal/g 0.005 gram per 100 cc, max 1.3593 24% by wt 8% by wt 0.9353 24.0 dynes/cm 173 mm Hg 0.00381 poi7.783 Itn
Table 15.6: Ethyl Acetate (2)
Acetic Ether
CH3COOC2H5
Ethyl acetate i s a water-white, flammable liquid with a pleasant, fruity odor. The 85 to 88 per cent grade of ethyl acetate suitably denatured i s generally used for commercial purposes but 95 and 99 percent grades are also available. I t i s miscible with most organic solvents such as alcohols, ketones, esters, aromatic, aliphatic and halogenated hydrocarbons. I t dissalves such materials as nitrocellulose, camphor, oils, fats, waxes, gums and natural and synthetic resins. I t w i l l tolerate fairly large amounts of lacquer diluents and like methyl acetate i t not only has a wide range of solubilities but i t possesses the unique property of dissolving nitrocellulose, cellulose acetate and cellulose ethers yielding solutions of low viscosity. Its solvent power for cellulose derivatives i s much improved, however, by adding a small quantity of alcohol. (85 to 88%) 00170 Iiy nt, mnx Acidity (as ncrtir nrid) Blusli rrsistnnrr a t W F (10% 4 RFC. I1 S. iiitroccllulosr solution) Clrar 450/,Rclative humidity I3luish 50% Cocliicicnt of cubical r\pnnaiun (ordinary trmpernturcs) O.Mo73 per ' F 0.00132 pcr "C Color Water-a hitc Critical tcmpcrnturc 250.1"C 37 8 atmosphercs Critical pirssure Dilution rntio Toluol 3.5 Petroleum naphtha 1.1 Distillation range Below 70°C Nonc Below 72°C Not morc than 10% Above 8O'C None Miscible without turbidity with 20 volumes Dryness 60" Bd gasoline a t 20'C Electrical conductivity a t 25°C Less than 1 X IO-' reciprocal ohms Evap. rate a t OS'F (in min.) 5% t
%% % 75%
eo% 95%
1)
3f 6t 94 1lt
Flash point Freezing point Non-volatile matter Refractive index a t 20°C Solubility in water a t 25°C Solubilityof aster in solvent a t 25°C Specific gravity a t 20/20"C Viscosity a t 20°C Weight per gal a t 68'F
Acidity (as acetic) Blush resistance a t W F (10% sec. R.S. nitrocelluloae solution)
+
Coefficient of expansion per 1'F per 1'C Color Dilution ratio Toluol Petroleum hy1O( 160°C) 55-60 1O( 100OC)
>1O( 130°C) 33 37
Substance Coumarone-indene Dibutyl sebacate Dioctyl sebacate Di(2-ethylhexyl)phthalate Epichlorohydrin-bisphenol Ester gum Gum shellac HgCI, Lignin Naphthalene Ni(NO,), .6H,O Nitrocellulose Nylon, Type 8 molding powder Polyacrylonitrile Polyoxyethylene glycols Rosin, dibasic acid modified Sulfur dioxide Triethyleneglycol di-2-ethyl hexoate Tri(2-ethylhexyl) phosphate Urea Vinylidene chlorideacrylonitrile ZnCI,
>1O( 1W0C) "
07
"h
B:P OJ
-
Eluotroplc Vdum, ( E " ) (on Slllca): Polarlty Index (P
-
"0
2 00
VIKomlty (CP. 25 C):
04
Denslty (g/ml):
157
Bolllng Polnt ( C):
-
48
Percant Water Soluble In Solvent:
NIA
RmfractIva Indax (25°C):
02-
-TRr~ROi408UTANE METHYL OLtATE 296.50 308.76 TRI-CL-ALLTIC ANHYDRIOC 01-N-HUTYL SEBACATE 314.47 oieurrL * ~ ~ A C A T E 3!4,47. TETRAETHIL LEAO 323.45 338.56 N-BUTYL ULEATE e u m STCARATE 340.60 345.67 1122-TET dWOMOETMANt l.l~lr2-TtTRA~ROHOEThANE 345.71) B I S I 2 - E T n S X Y ET)5EdACATE '341.46 TR1lZ-TOLYL)PUOSPHATE 36d.36 O I ( 2 - E T n t X ) AOIPATE 370.>8 815(2-ETntX)PHTHALATE 390.57 DIETMYLHLXYL AZELATE 412.66 , ~ 1 5 ( 2 - E T r t l L H E l ) S E d ~ A C A l E +426-.66
20.0
1.3510
264.R2
266.79 ?67.33 267.83 278.35
Refract. Index
Density
-
20.0
70.0 20.0 70.0
0.0
0.8870
25,O
2.2571
?5.0 25.0 25.0 25.0 0.0 20.0 20.0 0.0 25.0 20.0 20.0 25.0 11.0 25.0 75.0
?.C220
0.8586 GsY9Y9 2.1750 2.1700 2.1724 2.1938 0.8702 1.6908 0.93b6 0.9324. 1.6590 0.tl657 0.8540
2.Y529 2.8748(-9953 1.1830 0.9220 t.9843 0.9150 (1.9120,
25.0
0.0 25.0 25.0 25.0
Melting Point
0.0 -70.0 -80.0 -39.5 -70.0
-1.1
1.6081
-15.7 2.5 -112.0 0.7
I .60d3
-7.0
1.6500
1.4724
-*>.7 1.4890 1.5012 3.0 -18.5 1.4351 1.5854 -19-0 1.6088 16.0 0.0 1.6147 1.5939 0.0 1.5976 8.1 4.2 1.7026 1.4369 -37.0 1.4369 -37.0 1.4359 5.0 1.4315 -17.0 1.3670 -110.5 0.0 -3a.O I. 6345 0.0 1.5258 0.0 -7Y.O 1.4226 -35.5 1.5933 -27.5 1.5120 1.7380 6.1 1.4926 -3>.0 1.5790 0.0 1.5670 0.0 16.9 1.5862 1.6730 2.8 13.4 I .4582 3.0 1.661R 1.660~ -Y.O I .4525 1Y.O 16.6 1.4592 11.0 1.5652 1.5608 -18.0 -1.9 1.5602 1.5680 -1Y.O 1Y.9 1.4502 0.0 0.0 1.4397 1.0 1.4415 -11.0 -136.8 1.5915 1.4680
-19.0
I .4422
26.3 0.0 0.0 -10.0
1.6323 1.0277 1.4440
20.0
1.5575 1.4474 1.4859
25.0
1.4460
25.0
1.4510
Note: Missing data i s indicated by
11.0 -07.8
-50.0 -78.0 -48.0
Boiling Point
760. 0.
143.0 242.5 ZRO.0
0.
222.2
0.
0. 6. 11. 760. 0. 0. 0. 0. 16. 9.
0. 0. 0. 760. 0. 0. 14. 4.
773. 760. 0. 0. 0. 10. 0.
0. 0. 0. 0. 760. 760. 769. 0. 0. 0. 754. 2. 80.
0. 760. 760. 21. 0. 760. 0. 0. 19. 0. 0. 0. 0. 0. 20. 5. 0. 5. 5.
0, O., or 0.0.
233.5
120.0 151.0
301.5 1R1.C 221.0 220.0
255.5 787.0 791.5 147.0 395.0 140.0
174.0 149.6 302.0 183.P 145.0 306.0
282.P 47.3 z03.1)
163.5 111.0 289.0 188.5 110.0
1R2.0 340.0 2C0.5
1Y0.5 222.2 17Y.5 360.0
257.0 752.0 1w.n
172.0 223.5 215.0 206.0 11>.5
717.0 169.0 345.0 345.0 YI.0
227.5 222.5 ?43.5 103.5 0.0
264.0 214.0 231.G 237.0 256.0
Dielec. Constant
List
G.0
85 1 852
0.0 0.0 0.0
0.0 3.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0
0.0 0.0
0.0 0.0 4.39 0.0 0.0 P.0
0.0 5.19 2.34 0.0 0.0 0.0 7.96 0.0 0.0 5.32 6.44
0.0 J.0 0.0 0.0 2.4h
6.0 0.0
0.0 0.0 0.0 0.0 0.0
0.0 3.21 0.0 4.54
4.54 0.0 4.00
3.11 7.00 0.0 0.0 0.0 0.0 5.30 0.0 4.03
NO.
857 e54
855 856 857 858 859 860 861
862 863 8 64
865 866 867 868
869 870 871 872 873 874 875 876 077 878 879 a80 881
882 883 884 8U5
88b 8R7 RHR 849 890 801
892 893 894 895 896 897 89R BY9 900 y01
902 903 904 y05
906 907 908 909 910 911
AppendixXomparative Data for Various Solvents
949
Comparison of Solvent Properties (7 7)
Poorly Hydrogen-Bonded
benzene Boiling Point, "C
80
"F
176
Freezing Point, "C "F
-r
5.4 41
Density, g/mL Img/m3) Ib/gal
088 7 34
Vapor Density (air = 1) ---
carbon tetrachloride
n-hexane
77 171
154
68
-23 -9
-96 -141
chloroform
perchloroethylene
FreonS TF
Freona MF
trichloroethylene
methyl formate
methylene chloride
61 142
121 250
48 117.6
24 74.8
87 189
31.8 89.2
39 102
6 4
-24
-83
-1 I
-35 -31
-111
-168
-73 -99
-100
-148
1 49
1 62
1 58
I 49
I3 26
0 66 5 51
12 43
1355
I3 I6
1242
28
53
2 97
41
58
-
-
4.54
6 30
12 80
13 07
6 20
1 59
146 12 22
-96 -142
-.
0 97 8 I3
133 1 1 07
21
2.93
~
Rate of Evaporation (Butyl acetate = I )
-
Viscosity, 20°C IWF), CPlmPa s) Surface Tension in Air, 20°C 168°F). dyn/cm lmN/rn) Specific Heat, Liquid, 20°C (68 Fl. caVg C (Btu/lb F) kJ/kg K
______
Heat of Vaporization Ibp) cal/g Btu/lb kJ/kg Solubility Parameter, 6
0 65
0 99
28 9
0 21 o a8
175
-
- -
0 29 18 4
26 8
0 42
10 00 11 60 280 - - ~ _ _ _ _ _ _ _ _
-
0 57
0 23
2 26
0 96
___ -
94
46
80
59
170 395
84
145 337
106
195
92
86
73
0 70
32 3
19 0
0 21 0 87
-
0 22 0 93
___
93
-
22 ~
Flash Point, TCC, "C
-1 1
"F
12
Flammable Limits, vol% Lower Upper
14 8
_2 2 - ~ 22- - -
93
NF
NF
-22 -7 12 69
22 22 - _ - __ NF
NF
041 (30°C) 058 18 7
0 35
32 0 (25°C)
0 21 0 87
35 09 63 12 146 8
43 52 78 31 182 I
72
78
0 23 096
57
NF
28 2
0 516
0 28
2 16
117 -4)
1124 202 3 4700
103
240 93
25 NF
25 NF
25
-
NF
__ NF
25 0
044
--
78 141 327
97
97
27
27
_ ? . A
_ l _ l _ -
Hydrogen Bonding Index, y
27 50
_ 1 _ 1 1 .
50 90 209
247
-36
NF
NF
NF
19 -2
M
5 23
NF
100
50
~
Threshold Limit Value," ppm
IO
5 skin
50
IO
25
L
0 88
27 2
0 54
9 87
-
1000
1000
50
ceil.
0
(continued)
950
Industrial Solvents Handbook
Moderately Hydrogen-Bonded
(continued 1
951
Appendir-Comparative Data for Various Solvents Strongly Hydrogen-Bonded cyclohexanone Boiling Point, "C "F
F'
ethyl ether
124 255
34 94
-20
-85
-4
-121
-123 -189
DMAC
315
153 307
166.1 331
-31.2 -24
4 1 -78
157
Freezing Point, "C
EGME
DMF
Density, g/mL lmg/m3) Ib/gal
0.94 7.88
0.90 7.50
0.945 7.88
0.96 8.04
0.71 5.92
Vapor Density (air = I )
3.4
2.51
3.0
2.62
Rate of Evaporation (Butyl acetate = 1)
0.23
0.17
Viscosity, 20°C (68°F). CP1mPa.s)
2.2
0.80
Surface Tension in Air. 20°C 168°F). dynlcm lrnN/m) Specific Heat, Liquid, 2 0 C I68'F). cal/g C (Btuilb F) kJ/kg K
_
_
__
-
Heat of Vaporization (bp) callg Btu/lb kJ/kq
34.5 0 49 2 05 _ _ _ ~
109 138 197 (29°C) 248 458 576
-
isopropyl alcohol
n-butyl alcohol
65 148
75.0 167
82 180
244
210 410
-98 -144
-1 28.0 -198.4
-89 -128
-89.8 -130
3 36
formamide
118
6.63
0.78 6.55
0.81 6.76
2.55
1.11
1.59
2.07
2.55
-
0.47
33.00
6.10
1.7
2.30
0.45