Handbook of organic solvent properties Ian M. Smallwood Consultant
A member of the Hodder Headline Group
LONDON SYDNEY...
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Handbook of organic solvent properties Ian M. Smallwood Consultant
A member of the Hodder Headline Group
LONDON SYDNEY AUCKLAND Copublished in the Americas by Halsted Press an imprint of John Wdey & Sons Inc. NEW YORK TORONTO
First published in Great Britain 1996 by Amold, a member of the Hodder Headline Group, 338 Euston Road, London NW1 3BH
Copublished in the Americas by Halsted Press an imprint of John Wley & Sons Inc., 605 Third Avenue, New York, NY 10158
CD 1996 Ian M. Smallwood All rights reserved. No part of this publication may be reproduced or transmitted in any form or by any means, elactronically or mechanically, including photocopying, recording or any information stomge or retrieval system, without either prior permission in writing from the publisher or a licence permitting restricted copying. In the United Kingdom Such licences are issued by the Copyright Licensing Agency: 90 Tottenham Court Road, London W1P 9HE. Whilst the advice and information in this book is believed to be true and accurate at the date of going to press, neither the author nor the publisher can accept any legal responsibilityof liability for any errors or omissions that may be made. British Library Cataloguing in Publication Data A catalogue record for this book is available from the British Library
Library of Congress Cataloging-in-PublicationData A catalog record for this book is available from the Library of Congress ISBN 0 340 64578 4 ISBN 0 470 23608 6 in the Americas only produced by Gray Publishing, Tunbridge Wells, Kent Printed in Great Britain by The Bath Press, Avon and bound by Hunter & Foulis Ltd, Edinburgh
c
It goes without saying that a solvent will be chosen to do its job effectively and economically, and it is usually possible to choose a short list of solvents which will do this without requiring a large amount of experimental work provided that reference books, setting out the properties of commonly used solvents, are available. Almost always the choice will lean towards a solvent that is already used on the site, or to one of which the researcher has experience. Today, however, there are other criteria than solvent power and volatility which need to be considered. Regulations covering the exposure to solvent vapours of makers of the product and its users are much stricter than in times past and, as knowledge of the potential dangers improve, are likely to become even stricter. No longer is it possible to protect the makers and users by improved ventilation to draw the solvent fumes away and to discharge them, heavily diluted, into the atmosphere. Solvents’ effects on both high- and low-level ozone in the atmosphere are now unacceptable; although it is not widely appreciated by the general public that solvents contribute a large part of the volatile organic compounds (VOCs) in European industrial countries, as much as the whole arisings from road transport uses. This has a significant influence on solvent choice, since any solvents that evaporate in industrial operations have either to be recaptured or destroyed rather than passing unchanged into the atmosphere. The economics of solvent choice may now allow an expensive solvent to be used many times over rather than a cheap one only once, always provided that the expensive one can
be recovered in a fit state for reuse. A low-cost solvent may be difficult to destroy by incineration in an environmentally acceptable way, perhaps because its molecule contains chlorine, nitrogen or sulphur so that its disposal cost may exceed its purchase cost. Another factor of considerable importance is the need to avoid changing the solvent to be used in a process. This even applies to the earliest stages of the development of a new product since the temptation to stay with a solvent that appears to be working well in the laboratory is great. The longer during the development stages that toxicity, environmental damage and overall economics are not considered in detail, the more difficult it is to make a change. Once production is started long and difficult negotiations with regulatory bodies, which often need to re-approve an altered process, may be involved and a change of solvent becomes almost impossible. All these considerations make the optimum selection of a solvent for a process a matter of importance. Fortunately much information is available in the literature concerning both the properties of the old solvents (e.g. benzene, carbon tetrachloride) which were often byproducts of other processes and of the newer ones (e.g. tetrahydrofuran, dimethylacetamide) which are purpose-made for their desirable solvent effects. This book is a collection of the physical properties of most commonly used solvents along with information on their behaviour in the environment during and after use and their health and fire hazards.
Name It cannot be stressed too strongly that the name of a solvent should be easily used and recognized by all, from the graduate in the research laboratory to the plant operator who may have difficulty in reading a language which is not his or her own. Once a name, or worse still a set of initials, has become standard usage on a site it is very difficult to make a change. The use, for instance, of IPA for isopropanol or isopropyl acetate of tri or TC for trichloroethylene or 1,1,1-trichloroethane can lead to errors that are very serious. Highly toxic benzene can all too easily be confused, in dealings with Europe, for benzin, a comparatively low toxicity material.
Hazchem code This is a code informing U.K. emergency services of the action to be taken when dealing with transport emergencies and can be a useful method of labelling storage tanks on a site where many different solvents are handled. It consists of a number and one or two letters (see Table 1). Explanation: It can be seen that breathing apparatus (BA) should be available in all cases. E after the code indicates that evacuation of people should be considered. ‘Contain’ means that any spillage should not enter water courses or drains. ‘Dilute’ means that a spillage should be washed away to drain with plenty of water.
Molecular weight On many occasions the effectiveness of a solvent will be compared on a molar rather than on a weight or volume basis. Purchases are, however, always by weight or by volume so that a low molecular weight solvent may have a significant cost advantage in use. On the other hand the low molecular weight of water,
Table 1 Hazchem codes Number
Firefighting medium
1 2 3 4
Water jets Water fog Foam Dry agent
Explosion Letter risk Personal protection P R S
(SI T (TI W X Y (Y) Z
(Z)
Yes No Yes Yes No No Yes No Yes Yes No No
BA + Full BA Full BA Gloves BA (fire only) BA + Gloves BA (fire only) BA + Full BA Full BA Gloves BA (fire only) BA Gloves BA (fire only)
+
+
+ + +
+ Gloves + Gloves + Gloves + Gloves
Action Dilute Dilute Dilute Dilute Dilute Dilute Contain Contain Contain Contain Contain Contain
present in all solvents at parts per million level at least, may be surprisingly damaging when processing, for instance, high molecular weight Grignard reagents or urethanes. When a solvent is used at a high mole fraction, as for instance in extractive distillation where solvent mole fractions of 0.9 are common, the cost-effectiveness of a low molecular weight solvent such as monoethylene glycol can be remarkable in comparison with some other entrainers.
Boiling point Many operations with solvents involve boiling the liquid solvent and this requires a heating medium (hot oil or steam) at a temperature 15 or 20°C above the solvent’s boiling point. It should be borne in mind that some solvents (e.g. DMF and DMSO) are not stable at their atmospheric boiling points and if necessary must be boiled at reduced pressure.
The normal factory steam pressure is about 10 bar and this should yield a temperature of 160°C at the point of use and boil a solvent at 140145°C. If a higher temperature than this is necessary hot oil, stable to 30O/32O0C, will provide heat usable at 270/280"C. A solvent in which an involatile solute is dissolved will boil at a higher temperature than the pure material. Typically, the boiling point will be raised from 140 to 150°C if the mole fraction of the solvent in the mixture is reduced by 20%. If solvents need to be separated by distillation it is not a reliablgguide to assume that because their boiling points are widely different the split will be easy, particularly when water may be present.
Freezing point Several solvents (e.g. dimethyl sulphoxide and cyclohexanol) are solid at ambient temperature and therefore need to be stored and handled in heated storage and pipelines and particularly with heated tank vents. For certain materials, such as benzene, that combine a high freezing point with high toxicity, the thawing of blocked pipelines can be a difficult and potentially dangerous task. It should be noted that some solvents even when solid give off an explosive vapour. Thus, the vapour pressure of solid benzene is given by loglo p (mmHg) = 9.85
- 2309/T
and the concentration of benzene at 0°C is 7600 ppm, which is well above its lower explosive limit. Air-cooled condensers can be severely damaged if some of their tubes become blocked while others are still handling hot vapour causing high stresses in the tube bundle. Drums of solid flammable solvents pose handling and emptying problems.
Specific gravity Storage tanks and their surrounding bunds are normally tested using water and are designed for
a liquid of density 1.0. While most solvents have specific gravities below this, the chlorinated solvents are much denser (e.g. perchloroethylene, specific gravity 1.62) and tanks may need to be derated if switched to storing such materials. For the same reason 200-litre drums of chlorinated solvents may be too heavy to handle, either manually or palletized on a fork-lift truck and existing pumps may be overloaded. On the other hand, a change to a less dense solvent may mean that a full tanker load of solvent cannot be accommodated in an existing tank built with a denser solvent in mind. When compositions are quoted as percentages it is important to know whether these are by mole, weight-by-weight (w/w), volume-by-volume (v/v) or weight-by-volume (w/v) and, in the last case to appreciate that the sum of the components will not add up to 100.
Liquid expansion coefficient Organic solvents have an expansion coefficient five to seven times greater than water. The increase in volume when a high boiling solvent is heated from cold to its boiling point is significant and has been known to cause damage in batch-still operations when sufficisnt ullage has not been allowed. When purchasing solvents by volume rather than weight it may be necessary to use temperature correction.
Flash point and explosive limits The lower explosive limit (LEL) of a solvent corresponds to the vapour concentration above the liquid at its flash point at which a source of ignition will set off an explosion. The upper explosive limit (UEL) is the vapour concentration that is just too rich to explode and an 'upper flash point' of a pure solvent can be calculated if the UEL and the Antoine constants are known. If the atmosphere should be enriched with oxygen it will form an explosive mixture over a wider range than that between LEL and UEL and if the 'air' is less than 8-10% oxygen, depending on the solvent, no explosion can take place at any
solvent content. It is common when the likely ambient temperature lies in the range between the two explosive limits to blanket the vapour space in a storage tank with inert gas. For safety a gas with about 3% oxygen is used, but it should be remembered that this 'nitrogen' is not free of oxygen so that solvents that form peroxides very readily (e.g. ethers) can be damaged if pure nitrogen is not used as the blanket over them. Testing for flash point is carried out using laboratory equipment of a range of designs. Those that are easier to use do not necessarily correspond to the standard test methods laid down by regulatory authorities, but are adequate for internal purposes on site. The standard methods are difficult to use for an inexperienced operator, but all common mistakes tend to give a test result lower than it should be and therefore err on the side of safety. The figures quoted here are ones using the tag closed cup method which tend to give rather lower results than the tag open cup and the Cleveland open cup methods. There is no reliable conversion factor between the various methods. Mixtures of two or more solvents may, because of the presence of azeotropes, have a lower flash point than their components have separately. When handling solvent-laden air, as is common in activated charcoal recovery plants, it is normal to operate with a flammable solvent content in the range of 2540% of LEL. If information on the flash point of a mixture is not available the great majority of solvents have an LEL of 10,000 ppm (1%) with a few in the range of 7000-10,000 ppm. The flash point of straight run hydrocarbon solvents (e.g. white spirit) can be estimated from their initial boiling point (IBP) flash point = 0.73 x IBP - 72.6 where both temperatures are in "C. Common practice in United States is to quote petroleum temperatures in "E
Autoignition temperature While generally a spark or flame is needed to set a flammable liquid on fire, almost all solvents can
be ignited by a very hot surface and some by heat sources that are commonly met on industrial sites such as steam mains, hot oil pipelines and items heated by electricity, including laboratory heating mantles. Steam pipes routinely have temperatures between 160 and 200°C and may be considerably hotter where high pressure steam is used. Hot oil reaches 300°C or a little higher. Solvents such as ether with an autoignition temperature of 160°C and dioxane (180°C) are therefore liable to catch fire if dripped on to a heating medium line. Their use on a site may require major changes to plant layout. Carbon disulphide has an autoignition temperature of 100°C and cannot safely be used except in a purpose-built plant. The glycol ethers also present a hazard when hot oil heating is used. Electrical apparatus that is correctly described as flameproof can reach the autoignition points of some solvents and a change of solvent in a manufacturingfacility should not take place without this being considered.
Electrical conductivity When solvents are moved in contact with another phase static electricity is generated. This can occur in a number of circumstances in industrial operations such as
1. A hydrocarbon/water mixture is pumped in a pipe. 2. A solvent is stirred or pumped in contact with a powder. 3. A solvent is sprayed into air. 4. A solvent is contacted with an immiscible liquid (e.g. water) in an agitator. If the static produces a spark which contains enough energy and if the vapour phase in contact with the liquid is between its LEL and UEL an explosion may occur. It is also possible that a fine mist of flammable liquid below its LEL can be ignited by a static spark. The chance of such an explosion depends largely on the electrical conductivity of the solvent (see also the section on Dipole moment) since a
high conductivity allows the charge to leak away. Some solvents have naturally high conductivities and a few develop high conductivity over time in storage, although the latter cannot be relied on as a safety measure. It is also possible to add a proprietary anti-static additive at a level of about 0.15%. Small impurities of alcohols in esters or of inorganic salts can also increase conductivity by orders of magnitude. Freshly distilled water has a conductance of 5.0 x lo-* siemen, but this rapidly increases as it picks up CO2 from the air. The conductivity limit that is usually regarded as safe is 1.0 x 10-l' siemen/cm (100 picosiemen/cm) and above this level it is not necessary to earth the equipment handling the solvent. Resistivity, the reciprocal of conductivity, is also often quoted and the danger limit in various resistivity units is
100 megohm metre (Ma m) 1.0x megohm cm (MR cm) 1.0x ohm cm (acm). In general, all hydrocarbons and ethers (but not glycol ethers) have conductivities of 1 picosiemen/cm or less and are liable to generate static electricity. The higher molecular weight esters are at or near the limit. The unit used in the tables is siemen/cm. The minimum ignition energy of the spark required to cause an ignition for most solvents lies in the range of 0.2-1.5mJ, but carbon disulphide which has a very low conductivity (1.0x siemen/cm) also has a very low minimum ignition energy (about 0.015mJ) and a very wide range between LEL and UEL. It thus represents an exceptionally high electrostatic hazard.
Immediate danger to life and health (IDLH) The IDLH value represents a maximum vapour concentration from which a person can escape within 30 min without irreversible health damage or effects that would impair the ability to escape. Such information is clearly important in
rescues and emergencies. It should be compared with the LEL and the saturated vapour concentration at the ambient temperature. Since a spark might cause an explosion in an atmosphere within the flammable range even if the IDLH is greater than the LEL other considerations than the IDLH may prohibit entering a solvent-laden atmosphere.
Occupational exposure standard
(OW An OES is the exposure to a solvent in air at which there is no indication that injury is caused to people, even if it takes place on a day-after-day basis. The long-term exposure limit to solvent vapours sets a limit for the average exposure over an 8-h working day. It applies to workers in a plant and not to people living in the neighbourhood. The short-term exposure limit (STEL) also applies to some solvents and refers to an average over a peak period of 15 min. This is meant for the type of exposure that occurs when cleaning a filter press or doing other regular, but short-term tasks. The average over the peak would be counted as part of the 8-h exposure. The limits vary from country to country and are constantly being reviewed in the light of experience. The figures quoted in this book are those applicable in the U.K. in 1996 and are expressed in ppm. Where a British figure is not available U.S. TLV-TWA figures are used.
Odour threshold This is extremely subjective and hard to define accurately. In one reported test 10% of those taking part could detect an odour at 1 ppm while 50% could do so at 25 ppm. At 500 ppm there was still 10% of those exposed who could not detect it. There is further a difference between identifying a smell and just detecting it so that complaints of an odour are hard to refute reliably and smell cannot be relied upon as a warning of potentially dangerous exposure. This is particularlytrue in the
case of long periods of exposure since the nose becomes desensitized. The figures quoted here are for concentrations where all the people exposed could detect, although not identify, an odour. Solvents are not, as a class, very odiferous materials and few can be detected at much below a 1 ppm level unlike mercaptans (which can be smelt at the low ppb level), sulphides and aldehydes. The latter are often detectable in solvents that have been recovered and recycled and make such recovered solvents unacceptable for use in household formulations. Some solvents, such as dimethylformamide (DMF), have very low odours themselves but contain trace quantities of impurity (dimethylamine in the case of DMF) which are much easier to detect. Others, e.g. dimethylsulfoxide, produce very unpleasant smells when they are degraded biologically so that even small quantities getting into an aqueous effluent are unacceptable.
Saturated vapour concentration (SVCI The concentration of vapour in equilibrium with liquid (or solid) solvent is important for a number of reasons: 1. Fire and explosion. 2. Toxicity. 3. Smell. 4. Loss in handling. Vapour concentration can be expressed in mgm/m3, ppm or %. The former lends itself to ventilation calculations where the quantity of solvent being evaporated into a body of air is known. Both ppm and percentage figures are based on volumes of solvent vapour in air and the conversion is given by ppm = mgm/m3 x 24.04/solvent molecular weight.
All the SVC quoted here are at 21°C (equivalent to 70°F). 1. Fire and explosion. The concentration leading to a fire hazard is very much greater than
that leading to a health hazard. It is unusual for someone exposed to a fire hazard not to be able to detect solvent odour by nose although, since all solvents are denser than air, the concentration at floor level may be very much greater than that at head height. 2. Toxicity. This is discussed elsewhere. Above the normally quoted health levels asphyxiation can take place at an SVC of about 150,000 ppm. A high concentration of inert gas (or C02) used for blanketing the vapour space in a tank can also be dangerous in this way. 3. Smell. This is discussed in the section on Odour threshold. 4. Loss in handling. Every time a bulk liquid is transferred between road tanker and storage tank or between storage and process there is a potential discharge of vapour. In addition, solvent vapours are discharged when the storage tank ‘breathes’ with the daily change of temperature. Increasingly it is becoming unacceptable that this discharge goes directly into the atmosphere and the alternatives are to return the vapour to the vapour space of the vessel from which the liquid comes or to pass the solvent-rich ventings to recovery or destruction. The linking of vents and recovery can become very complicated if more than one solvent is involved in the system and destruction of the solvent in the ventings before their discharge to atmosphere is the most common solution. The loss of solvent is no greater than it would be if the ventings were discharged directly but, to design a destruction plant, the amount of discharge must be known. The most volatile solvents (pentane, ether, dichloromethane) can lose 0.3% of the liquid transferred on each occasion and in a good recovery system the handling loss can be the largest contribution to the total losses of solvent.
Vapour density relative to air This is the ratio between the molecular weight of the solvent and the molecular weight of air. Apart from methanol which has the lowest vapour density, all organic solvents are much heavier than air.
This means that spillages, whether on a small scale in the laboratory or on a large scale in an industrial plant, will give rise to vapour at a low level. Ventilation should therefore be designed to draw from this level and tests for flammable or toxic concentrations should be made at a low point. Heavy vapours can spread for long distances in ditches, pipe tracks and drainage pipes and can accumulate in bunded areas, particularly if the bund walls are high. The manual clearing of sludges and deposits in the bottoms of storage tanks which have contained low-flash point solvents is particularly hazardous if low-level ventilation is not provided.
Photochemical ozone creation potential (POCP) POCP is an arbitrary scale of atmospheric chemical activity based on ethylene at 100 and the very stable organics at 0. The ‘natural’ products such as alpha-pinene and dipentene have a POCP of about 50. A significantly large contribution to the total of volatile organic compounds (VOCs) in industrial countries is derived from the use of solvents. Since VOCs are an essential ingredient of smog both legislation and public opinion will lead to the choice of solvents which have a low POCF! This is particularly true for paints and for domestic uses where recapture and recovery of the used solvent or its destruction before discharge are impractical. Since there is little correlation between the toxicity, evaporation rate, solvent power and POCP of solvents this entails a further independent restriction to the choice of solvent for domestic purposes. The POCP should not be confused with the ozone depletion potential (ODP) which depends on the extreme stability of various halogenated solvents in the atmosphere, but, because POCP is a measure of reactivity in the complex chemistry of the lowest level of the atmosphere, solvents with a high ODP (see Table 2) do have a very low POCI?
Table 2
ODP
POCP CFCll3 Methylene chloride l,l,l-Trichloroethane Chloroform Perchloroethylene Carbon tetrachloride Trichloroethylene
0.80 <0.05 0.15
0.9 0.1 1.o 0.5
0 1.04 0
6.6
The class of solvents with particularly high POCP is made up off aromatic hydrocarbonswith methyl sidechains such as trimethyl benzenes and the xylenes. Legislation has restricted their use in Los Angeles for many years and their widespread use in paint formulations is qteadily being reduced. Developments in the resins used in paints will reduce the proportion of solvents and demand increased use of more sophisticated solvents and of water in their place. If such improvements cannot replace, say, xylenes, careful fractionation can, at a price, reduce the POCP as Table 3 shows. Since rn-xylene is usually the most common isomer in solvent C8 aromatics, the improvement may be considerable. Table 3
POCP Ethylbenzene o-xylene p-xylene m-xylene
59.3 66.6 88.8 99.3
Methyl sidechains on paraffins or naphthenes do not have the same harmful effect. The replacement of acetone (POCP 17.8) by methyl acetate (POCP 2.5) or the use of isobutyl acetate (POCP 33.2) for MlBK (POCP 63.3) is typical of what may be achieved in reducing the adverse impact of solvents on the environment.
Miscibility with water All solvents are at least partially miscible with water and most of those with a polarity of more
than 36 (on a scale of water = 100) are wholly so. Moisture levels as low as 200 ppm can easily be measured by the Karl Fischer method. Only solvents with a very low solubility in water and densities of less than 1.00 should be tested by the Dean and Stark method. The requirementsfor dryness in a solvent range from the low ppm for a Grignard reagent solvent to 2 or 3% for cellulose paint thinners or gun washes. While most can be dried by various forms of distillation, there are also many solid dessicants using chemisorption or hydration effects, although none of these dessicants are general purpose. Molecular sieves are very effective and are suitable to dry the great majority of solvents. However, unless regeneration plant is used to recover the molecular sieve, their cost is about €10,000/ tonne of water removed. Many solvents are hygroscopic and if moisture is to be kept at a very low level, the vents of storage tanks should be fitted with silica gel or molecular sieve-filled canisters. For the removal of small amounts of solvents from water see the section on log activated carbon partition. Knowledge of the solubility of solvents in water is useful in predicting their behaviour in several fields. Highly water-soluble solvents carry materials and migrate themselves into the biosphere.
They are both more easily leached from soil and less easily volatilized into air. The large number of solvents that are not fully miscible with water at 25°C is a measure of the high difference between the polarity of water and that of many organic solvents. Table 4 lists a number of other solvent pairs that have an upper critical solution temperature at a temperature within normal industrial operating range. The polarity of the non-polar solvents are all less than 6.5 (on the scale of water = 1001, while the polar solvents have a polarity of 30 or more.
loglo activated carbon partition While aqueous effluents containing highly volatile solvents can be stripped using air or steam preparatory to being discharged, the less volatile and particularly those that are polar, are difficult to strip and are more economically removed from dilute solution using activated carbon- or ionexchange resins. To get an idea of the effectiveness of activated carbon adsorption, one can use the following equation as a preliminary guide, although an experiment using the grade of carbon to be used is vital to get a sound design
Table 4 Upper critical solution temperature (“C) Methanol Ethanol EGME
nC5
nC6
nC7
nCs
14.8 <-78
35 -65 28 -32 12 -39 3 68 -4 69 20 -25 77 92 51
51 -60 49 -12 25 -28 4 73 -8 70 18 -22 85 94 60
67
EEE Carbitol Acetone Acetophenone DMF Acetic acid Aniline Nitrobenzene Pyridine Acetonitrile Furfurill Phenol
63 72 25 60 57
nC9
nClo
c6
CSz
2,2,4-TMP
76 -15
45 -16
36 -24 25
42.5 -70 40 -15 28 -34 14
-60
<-1 -6
-6 10
19 72 20
29 75 22
41 78 24
92
100
108
-40
3.9
-29 -16 50 7 30 -4 -36 77 66
7 80 29 -15 81 101
x 1 PAC=-.m c xlm is the weight of adsorbate in mg per kg of charcoal, c is the concentration in ppb of the solute remaining in the effluent, and PACis the activated charcoal partition coefficient. The values of PACare usually quoted in logarithms to the base 10. For a rough preliminary estimate
where S is the solubility of the solvent in water in ppb. This relationship is not valid if the solute is wholly water miscible, and clearly shows that the more water-soluble a solvent is the less easy it is to remove it from water by adsorption. The partition coefficient is affected by temperature, pH and the type of activated charcoal used.
Loglo partition between octanol and water A great deal of work on the partition of solutes between water and other solvents has been done by Pomona College. The main solvent used is noctanol giving the relationship P,w
=
concentration of solute in n-octanol concentration of solute in water
Originally the work was done as a guide to the biological effect of the solute. A high value of P (i.e. log P > 1.51, corresponding to a low concentration in water, means that the material in solution cannot easily invade living organisms and therefore has a low biological effect. On the other hand, a negative value of log P indicates a very hydrophilic compound, difficult to extract from water using any third solvent, not just noctanol. The values of Po, are expressed as logarithms to base 10 and the logarithms have a range of -1.93 to +4.15, a range of a million. A reasonable estimate for P, if experimental results are not available, is
log Pow = 6.75 - 0.75 log S where S is the solubility of the solute in water in PPb.
Oxygen demand The biodegradability of solvents to the simplest molecules, primarily CO2 and water in a given time (here the quoted biological oxygen demand figure is for five days except for a few instances where 10 days are quoted) vary widely and the correlation between laboratory and plant-scale results for the amount of oxygen removed from the aqueous phase is not very reliable. The theoretical oxygen demand (ThOD), is solely the oxygen needed on a stochiometric basis to oxidize the solvent completely, and is thus the worst possible effect, but may be useful if no laboratory results are available. In this book the values of ThOD do not include for the oxidation of the nitrogen where it exists in the solvent's molecule. This tends to be a slow reaction and seldom is represented in the five-day BOD test. BOD depends on the effectiveness of the organisms that may be present and which may be killed by a change of the solvent in the effluent and starved to death by a lack of the solvent to which it is accustomed. Results for BOD can be measured over a time period measured in days, usually five or 10, and is clearly a time-consuming test. A high BOD solvent sparingly miscible in water and with no solvent-rich phase present to replenish the aqueous phase may be less harmful than a low BOD solvent that is readily soluble in water.
Antoine vapour pressure equation There is one very widely used equation for estimating the vapour pressure of organic liquids, the Antoine equation lOgP= A--
B C+T
where A , B and C are constants.
P is the vapour pressure of the solvent at temperature T which can be expressed in a number of pressure units which, of course, refer to different values of A. It is therefore most important to know what pressure units are in use when getting values of the constants from the literature. In this book logarithms to base 10, mmHg and "C are used.
knowledge of its solubility parameter can be of considerable assistance. A resin, a polymer or any other non-electrolyte is likely to be most easily soluble in a solvent if the solubility parameters of the solvent and the solute are similar. It follows that two solvents with similar parameters will have similar dissolving powers for a given resin
S=[L+)
112
Cox chart equation As an alternative to using the Antoine equation it is possible to employ an equation' based on the Cox chart log P = A -
B T +230
These constants are not the same as the Antoine ones although they tend to coincide when C = 230. In this book the same units for P and T are used and the logarithms are also to base 10. Since another correlation gives a value for C of
C = 2 3 9 - 0.19Tb A and B from the two systems will be close together for solvents boiling near 50°C. Since both Cox and Antoine equations are based on the ClausiusXlaypeyron equation the values for B are related to the latent heat of the solvent. The Cox equation lends itself to calculating relative volatilities
s = A1 - 4 - 4-4
log a* = log-
4
230+ T
and the sensitivity of the value of the relative volatility to temperature tends to be high when the difference in latent heats is high. Alcohols tend to have higher molal latent heats than other groups of solvents and therefore to have large changes in a* with changes of temperature and pressure.
Solubr'lity parameter
03)
In choosing a solvent for a particular duty,
where L is the molal latent heat of the solvent, T the absolute temperature and V its molar volume. The value of is normally expressed in units of call' cm-3/2. The solubility parameter is a blendable property so its value for a blend can be calculated and a blend of solvents can be made to suit the solute more closely if necessary. While the value of Scan be calculated knowing only readily available information, it can also be found experimentally for hydrocarbons and chlorinated hydrocarbons by measuring the Kauri Butanol number (KB) since
KB = 5 0 6 - 3 4 5 (for KB > 35). Just as a solute with a similar value of 6 to the solvent will dissolve so two solvents of similar S will be miscible, The limit of difference beyond which total miscibility will not be achieved at 2 9 8 K is about 2.5, but as the values of UCST show (Miscibility with water section), at higher temperature miscibility becomes easier.
Dipole moment The figures quoted here are for liquids at 2 9 8 K. The dipole moment is proportional to 1/T where T is the absolute temperature. Along with a number of other properties, dipole moment contributes to the 'polarity' of a solvent.
Dielectric constant The dielectric constant of a solvent reflects its molecular symmetry and is comparatively easy to
measure. It can thus be used to calculate molar polarization and, from it, dipole moment (PI.
An approximate relationship between the two scales is
p=- E-1 V &+2
B = 15lE
where E is the dielectric constant and V the molecuIar vol ume. Dielectric constant is also a factor in considering a solvent's electrostatic hazard. A solvent's relaxation time, which is a measure of the rate at which an electrostatic charge will decay, is a product of dielectric constant and resistivity. The higher this product the higher the relaxation time. However, the range of values of the dielectric constant is about 2-180, which is a small range compared to the range of resistivity (see Electrical conductivity section). Nonetheless if a solvent is being changed in an existing process the possible increased risk of electrostatic problems should not be ignored.
Polarity Polarity is a widely discussed and quoted property of a solvent but it is used loosely to cover a number of different effects, including those covered by dielectric constant and dipole. The figures quoted here are comprehensively discussed in reference 14 of the bibliography.
Evaporation time There is no satisfactory method of calculating the rate of evaporation of a solvent, since it depends on the equipment in which evaporation takes place as well as a number of properties of the solvent. There are two widely used standard solvents diethyl ether and butyl acetate - against which other solvents' evaporation times can be compared. Somewhat confusingly, a low rate of evaporation on the ether scale corresponds to a high number (i.e. the time it takes to evaporate is many times the time ether takes), while on the butyl acetate scale a low rate of evaporationcorresponds to a low number (i.e. the rate of evaporation is lower than that of butyl acetate).
where B and E are the butyl acetate and ether numbers.
Nett heat of combustion For the eventual disposal of used solvent, whether in liquid or vapour form, the preferred method is usually burning. This may involve using the solvent as a fuel, possibly in a cement or lime kiln in which it may be used as a replacement for a more conventional, and more costly fuel. Alternatively, to reduce VOCs to a very low level in solvent-laden air, combustion in an incinerator, with or without added fuel, may be used. A less common alternative is oxidation in the liquid phase which also gives rise to heat. In all cases the heat of combustion of the solvent to be destroyed needs to be known. Since in almost every case the water generated in the destruction will be discharged as vapour, the lower or nett calorific value is the appropriate one to use and it is the one quoted here.
Heat of fusion It may be theoretically important to know how much heat will be required to thaw out the solvent should it freeze, but the most frequent use of the heat of fusion is to estimate the freezing point depression when the solvent dissolves a solute. The freezing point depression per gram-mole in 100 grams of solvent can be adequately calculated up to a mole fraction of solute of 0.10 by the expression
R T~ lOOH where R is the gas constant (1.987 cal/g units), H is the latent heat of fusion in cal/g and Tis the freezing point of the pure solvent in K.
For some commonly used solvents with high melting points the freezing point depression coefficients are listed below. Acetic acid Benzene &Butanol Cyclohexane Cyclohexanol Dimethylsulphoxide 1,4-Dioxane Nitrobenzene Phenol Sulfolane Water
39.0 49.0 80.6 208 420 40.9 46 70 74 64 1 18.6
Azeotropes The presence of an azeotrope between solvent components can have three important effects:
1. It makes the recovery by distillation of one of the solvents to a high degree of purity and a high yield difficult. Azeotropic mixtures should therefore be avoided if possible in pharmaceutical productionwhere recovery is important. 2. It increases the rate of evaporation in the great majority of cases since the azeotrope is usually a low boiling one in which the boiling point of the azeotrope is below that of both pure components. 3. It decreases the flash point of the mixture and can therefore have an important influence on safety when the solvent mixture may be used at a temperature about ambient. It is important, therefore, to know when an azeotrope exists and also when its absence is confirmed. In this book binary azeotropes mostly drawn from Horsley's Azeotropic Data are listed. There are a great number of possible ternary or more complex mixtures of solvents that are used, and some ternary azeotropes have been recorded. It is extremely rare for a ternary azeotrope to occur if all three binary mixtures which its components can form are not also azeotropic. In the absence of information on the existence of an azeotrope in a binary mixture of solvents it
is possible to estimate whether an azeotrope will exist if activity coefficients at infinite dilution ( f ) and pure vapour pressures of the solvents (P) are available. In an ideal vapour-liquid system of two solvents the relative volatility (a*)is equal to the ratio of the vapour pressure of the components and is not affected by composition P1/Pp = a*
An azeotrope occurs in a non-ideal system when the vapour phase and the liquid phase in equilibrium with it have the same composition
a=--~14- a a * = 1 , 0 Y2p2 Y2 The values of yvary throughout the concentration range. By definition n = 1.0 for pure component 1 at the composition at which component 2 is infinitely dilute and has an activity coefficient y; and vice versa. A low-boiling azeotrope (much the more common) will occur if y: > a*, while a high-boiling azeotrope will occur if l/a* > yy.
Activity coefficients Activity coefficients are described as a measure of the relative escaping tendency of a compound. This may be escape from a liquid phase to a vapour phase (which can also be quantified by Henry's law coefficient) or from one liquid phase to another, which is the basis of liquid-liquid extraction. The data sheets list the experimental values of f which are obtained by a variety of methods. These can show an appreciable difference one from another, particularly when the mixtures they refer to are very non-ideal with values of f of lo3 or more. There is also a considerabletemperature effect on values of y The two major sources of the values listed here are references 2a and 2c. Those from 2a, which have reference numbers 1/1 to 8/381 are derived from distillation data and are at temperatures near
boiling point, although these may be at pressures lower than atmospheric for high boiling or unstable solvents. Those from 2c are measured at 25°C and have reference numbers commencing 1X. The latter are more useful for liquid-liquid extraction calculations. If no experimental results are available for particular soluteholvent mixtures UNIFAC provides a method of calculating u‘ values.
Partition coefficient (K) There are an almost unlimited number of systems which can involve solvent extraction, but those listed here are restricted to the ones which have water as phase 1, an extraction solvent, sparingly soluble with water, as phase 2 and a solute partitioned between the two phases.
K=
molar concentration of solute in water molar concentration of solute in X
If the objective is to remove the solute from phase 2 and concentrate it in phase 1, K needs to be as high as possible and a target minimum of 5.0 is appropriate. On the other hand, if the solute needs to be removed from the water phase, K should be 0.2 or less. The values of partition coefficient listed are for 25°C and the most dilute solutions for which information was available. K is temperature dependent and tends to 1.Oas the concentrations of solute in the two phases increase. Since the two phases each containing solute are in equilibrium, the product of the mole fraction of solute and its activity coefficient in each phase is the same. Hence
For dilute solutions the activity coefficients can be used to assess the likely performance of the system. Thus for the system water (1)-heptane (2)MEK (solute)
This would indicate that it was possible to remove MEK from water using heptane as an extraction solvent. The references which give the source of the information are from three sources in the bibliography. These are:
1. CEH: Perry’s Chemical Engineering Handbook 2b. V2, 3 and 4: Dechema Liquidlliquid Data Collection 17 P: Pomona College Collection.
Henry’s law constant (HI Particularly in dilute solutions in water, solvents tend to behave in a very non-ideal way and their equilibrium vapour pressure has to be calculated either using an activity coefficient or Henry’s law constant (HI. The literature contains compilations of the latter for aqueous solutions but they are reported in several different units, all of which are a pressure divided by a concentration, Le. H = P/x, where P is the vapour pressure of the pure solvent at the solution temperature and x its concentration in the liquid phase. In this book H is expressed in atmospheres divided by mole fractions. Alternative units are
1. Atmospheres per g-mole of solvent per 100 m3 of water. Convert by multiplying by 106/18. 2. Kilopascals per g-mole of solvent per 100 m3 of water. Convert by multiplying by 548. 3. Atmospheres per Ib-mole per ft3. Convert by multiplying by 6.25 x The value of H increases with temperature and the figures here are for the system temperature of 25°C. Figures for H quoted in the literature for apparently identical systems vary widely, sometimes by an order of magnitude or more, but, if the information is available there are two ways of checking it.
1. Since H is only suitable for use in dilute solutions
H
= Pf
If therefore figures for the activity coefficient at infinite dilution and 25°C and the Antoine coefficients are available, the value of H can be compared. 2. Many solvents, particularly hydrocarbons, chlorinated, and the higher molecular weight oxygenated ones, are so insoluble in water that their aqueous solutions are always dilute. At saturation, therefore H = PIS where S is the solubility of the solvent in water expressed as a mole fraction. High values of H (e.g. > 50) indicate a dis solved solvent that can be stripped easily either
by air or steam. Such a solvent will also evaporate quickly from water. H can also be used to calculate the composition of solvent-laden air in contact with water at levels appropriate to TLV calculations thus
C = (TLV in ppm).(mol. wt of solvent) Ha18
where C is the concentration of solvent in water which corresponds to the TLV. Similarly the flash point of a dilute aqueous solution can be seen to be above or below 25°C given a value for the LEL of the pure solvent.
Introduction
vii
Key to tables
ix
Section I Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-Trimethyl pentane Cyclohexane Benzene Toluene Ethylbenzene Xylene (mixed isomers) C9 Aromatics TetraIin
1 3 7 11 15 19 23 27 31 35 39 43 47 51 55
Section 2 Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alcohol i-Amyl alcohol Cyclohexanol n-Octanol Ethanediol Diethylene glycol 1,2-PropanedioI
59 61 65 69 73 77 81 85 89 93 97 101 105 109 113
Section 3 Glycol ethers Propylene glycol methyl ether Ethylene glycol methyl ether Ethylene glycol ethyl ether Ethylene glycol monobutyl ether
117 119 123 127 131
Section 4 Chlorinated solvents Methylene chloride Chloroform Carbon tetrachloride 1,2-DichIoroethane
135 137 141 145 149
1,I ,1-Trichloroethane Trichloroethylene Perchloroethylene Monochlorobenzene
153 157 161 165
Section 5 Ketones Acetone Methyl ethyl ketone Methyl isobutyl ketone Cyclohexanone n-Methyl-2-pyrrolidone Acetophenone
169 171 175 179 183 187 191
Section 6 Ethers Diethyl ether Diisopropyl ether Dibutyl ether Methyl tert butyl ether 1,4-Dioxane Tetrahydrofuran
195 197 201 205 209 213 217
Section 7 Esters Methyl acetate Ethyl acetate Isopropyl acetate n-Butyl acetate Cellosolve acetate
22 1 223 227 23 1 235 239
Section 8 Miscellaneous solvents Dimethylformamide Dimethylacetamide Dimethylsulphoxide Sulfolane Carbon disulphide Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
243 245 249 2 53 257 261 265 269 273 277 281 285 289 293 297 301
Bibliography
305
Hydrocarbons
n-Pentane Alternative names Below 40°C, petroleum ether Reference codes CAS number UN number
109 66 0 1265
Hazchem code EPA code
3Y
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
72 C5H12 36 -129 0.626
Cubic expansion coeff (per oC x 103) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (20°C)
1.52
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
-40 260 2E-10
Lower explosive limit (ppm) Upper explosive limit (ppm)
15000 78000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
5000 600 750 900
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
768000 2.5 442 41
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) Log1Oactivated carbon partition Log1Opartition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
16 0.235 1.358
38E-4 120E-4 +3.23 3.56
Vapour pressure equation constants (Log1O,mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
7.0 0 1.844 0.9
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/molrC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
6120 776 40.32 3.31 470 2008 3.825 3.316 115.0
6.87632 1075.780 233.205 6.82847 1050.1 Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
28 1.0 13
Hydrocarbons
~~
Azeotrope X% Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TM P Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics TetraIin Alcohols Methanol Ethanol n-Propanol i- Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-PropanedioI
"C
WIW
Reference
Solute
Reference
-
-
-
-
None None
0.9 0.8 1.2
6d123 6a1127 1x311149
None None None
9742 9741
1.1 1.6 3.5
6all19 6a118 6d160
8 31 95 34 None 94 35 None None None
2055 4062 6484 6370
19.0 13.6
2e/l32 2d375
8.5
2b1169
8.7
2ff529
2.4
6a1100
8327 8228
\one Vone
Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,1,1-TCA TCE Perk. MCB Hydrocarbons
51 3 lone
1571 1482
Partition coefficient
Reference
~~
keotrope :% Solute Yetones ketone M EK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,CDioxane THF
"C
Reference
CW/W
30
32
5368
32
33
8296
Vone
Esters 78 Me acetate Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetatr
34
5536
89 36 None
1256 3156
None
9740
Solute Y
Reference
7.1 5.3
3+4/190 1x/3/1149
4.8 2.2
1x/3/1149 1x/3/1149
22.0
6aI102
Partition coefficient
Reference
0.91
vu475
Miscellaneous DMF DMAc DMSO Sulfolane cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
90
35
2792
99
35
462
Hydrocarbons
b
n-Hexane Alternative names 62/68 Hexane Reference codes CAS number UN number
110 543 1208
Hazchem code EPA code
3YE
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
86 C6Hl4 69 -95 0.659
Cubic expansion coeff (per oC x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
1.3 18.4 0.31 1.372
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
-22 225 1.0E-16
Lower explosive limit (ppm) Upper explosive limit (ppm)
12000 75000
5000 20
Vapour concentration @21°C ppm Vapour density {relative to air) Vapour pressure @21°C mmHg POCP
170000 2.99 128 42
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm) Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition Log1Opartition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
9.5E-4 110E-4 +3.80 0.04 (7) 3.53
Vapour pressure equation constants (Log1o. mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
6.9 0 1.9 0.9
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/molfC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
6880 921 42.0 3.03 507.5 3119 4.50 3.86 130.5
6.91058 1189.64 226.28 6.9386 1212.1 Kauri butanol value Evaporation time (ether = 1) Evaporation time (BuAc = 1)
30 1.4 8.4
Hydrocarbons
Azeotrope
K% Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics TetraIin Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol l-Octanol Ethanediol DEG 1,2-PropanedioI Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,1,l-TCA TCE Perk. MCB Hydrocarbons
"C
Reference
Solute f
-
-
-
None None
12133 12134
0.9 0.5
6a1604 6a16 13
None
11690 10861 12131
1.1 1.4 1.4
6al273 6d535 6d59 1
1.5
6a1605
39.1 12.3 22.4 10.5 11.2 13 9.5
2d253 2d453 2d584 2b197 2b1200 2b1320 2 bl2 50
6.0
2fl532
575.0
2bl295
1.3 1.2
6d426 6d403
1.3 1.5 1.4 1.8
64473 64463 6a1453 6d529
WIW
None
None None None
72 79 96 77 97 98 92 None None None
50 59 66 63 68 68 67
None 66 95
None 16 60 None None 67 71 None None None
2087 4106 6506 6390 8163 8354 8242 9758 9845
8442
1575 1495 2730b 2330 22 17a 10519
0.9
Reference 6a1123
-
Partition coefficient
Reference
-
38.1 0.74 1.00 0.04
P383 V21577 VU6 16 V31121
Azeotrope Solute Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,CDioxane TH F
X% wlw
."C
41 71
50 64
cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
5385 7376
Solute f
Reference
4.2 3.5
3+41225 3+4/302
17.6 None 47 67 98 50
Esters Me acetate 39 Et acetate 62 i-Propyl acetate 91 n-Butyl acetate Cellosolve acetatc Miscellaneous DMF DMAc DMSO Sulfolane
Reference
7588 9297
1Xl311240 3+4/472 1Xl311240
2.6
515 14
6d332 12
None 95 68 None None
1274 3184 11151 10708
None 97 69 72 52
6284 2800
62
VU487 V3126
3bl451
1.2 3.0 1.6
None None
94
0.8 0.13
Reference
12128
60 63 52 65 69
Partition coefficient
0.16
24.8
vu547
9.2
V2/282
1.91
P1659
1~/3/12,0
13.4 11.6 14.5
51152 6al580 6d532
7.4
6a/5 10
570
fydrocarbons
n-Heptane Alternative names Reference codes CAS number UN number
142 82 5 1206
Hazchem code EPA code
3YE
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
100 C7Hl6 98 -91 0.664
Cubic expansion coeff (per oC x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive Index (25°C)
1.3 19.3 0.41 1.385
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
-4 215 1.0E-16
Lower explosive limit (ppm) Upper explosive limit (ppm)
10000 70000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
4250 400 500 150
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
55000 3.57 40 53
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
3E-4 lOOE-4 +3.5 0(7) 3.52
Vapour pressure equation constants (Log1o. mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
7.5 0.0 1.924 1.2
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/"C) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
7560 1067 52 2.74 540 3378 5.17 4.40 147.5
6.89386 1264.370 216.64 7.04265 1365.1 Kauri butanol value Evaporation time (ether = 1) Evaporation time (BuAc = 1)
31 3.0 3.3
Hydrocarbons
Azeotrope X%
Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes Cg Aromatics Tetralin Alcohols Methanol Ethanol n-Propanol iPropano I n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2- Propanedio1 Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC l,l,l-TCA TCE Perk. MCB Hydrocarbons
"C
WIW
Reference
None
12133
-
-
None None 0.7 80 None None None
Solute f' 1.3 0.9
-
Reference 6al127 6al604
-
1.o
6bl196
13809 11697 10876 13027 13807 13808
1.0 1.1 1.3 1.4 1.7 1.4 1.3
6bl197 6d304 6bl123 6bll69 6d489 6d497 6bl200
18.4 11.6 15.5 14.5 7.6 8.0 19.0
2d243 2al498 2al596 2blll3 2bl218 2dl378 2dl281 2fl382
23.7 8.2
2fl4 19 2f/535
10.0
1x/1/359
59 51 64 50 82 73 62 Azeo 93 None
49 71 88 76 94 91 89
2101 4139 6514 6399 8182 8368 8248
98
9869 11727
97
98
4312
77 86
92 97
6592 846 1
None 24 81
1167 3009
2.2 1.3 1.2 2.3
None
2335
1.3
1x/3/1328
None
10531
1.7
6blll9
lx/1/357 6bl77 6 bl67 6d444
Partition coefficient
Reference
-
-
<0.001 0.003 <0.001 <0.001
P1487 P2290 P2877 P2877
5.41 0.46 1.18
V21376 V21583 V21620
0.90
P3982
~
Azeotrope ~
X%
Solute
"C
wlw
Reference
Solute f
Reference
3.1 3.9 2.5 3.8 10.2
3+4/242 3+4/311 3b1550 3b1509 3bl460
Partition coefficient
Reference
~
Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane TH F
10 30 87
56 77 98
None 56
12196 92
Esters Me acetate 3 57 Et acetate 6 77 i-Propyl acetate 33 88 n-Butyl acetate None Cellosolve acetatf Miscellaneous DMF DMAc DMSO Sulfolane cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
95
6393 7384 11801
7552
5558 7594 9302 11826a
97
None
1278
None
11179
75 79 54 95 None 87
96 95 69 98 79
8860 6289 2803 8781 10936 654
1.2 4.2 1.o 1.2 2.7 1.4
1x/3/1330 3+4/559 3 +41592 1x/3/133 1 3+4/478 1x/311330
4.2 3.5
1x/1/358 1x/1/359
2.0
51591
17.0
6b198
108 1.3 18.1 13.1 3.1 5.0 25.7 10.6 20.0
1x/3/1330 1x/1/357 51175 6bl161 6bl116 6bl100 6b179 3+4150 2fl400
0.66 0.13
v3129
0.08
V4/240
10.4 0.20
V4/2 01 P1722
1.3
P1657
CEH
iydrocarbons
n-Octane Alternative names Reference codes CAS number UN number
111 65 9 1262
Hazchem code EPA code
3YE
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
114 C8H18 126 -57 0.703
Cubic expansion coeff (per oC x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
1.2 21.7 0.50 1.395
13.3 220
Lower explosive limit (ppm) Upper explosive limit (ppm)
10000 65000
3750 300 375 200
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
15700 4.1 12 49
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm) Aqueous effluent Solubility in water (25°C %wlw) Solubility of water in (25°C %wlw) LoglO activated carbon partition LoglO partition in octanollwater (wlw) Biological oxygen demand wlw (days) Theoretical oxygen demand wlw
O.63E-4 BOE-4
Vapour pressure equation constants (Log1o. mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
1.2
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/molf'C) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
8265 1213 59.3 2.49 568 4926 5.85 4.93 163.5
6.93142 1358.800 209.855 7.14736 1518.9 Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
1.23
Hydrocarbons
Azeotrope Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TM P Cyclohexane Benzene Toluene Ethylbenzene Xylenes Cg Aromatics Tetralin Alcohols Methanol Ethanol n-PropanoI i- Propano1 n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol l-Octanol Ethanediol DEG 112-Propanediol Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC l,l, 1-TCA TCE Perk. MCB Hydrocarbons
X% w/w
"C
Reference
12133
None
Solute f
1.o 0.9 1.o
Reference 1x/1/395 6a/6 13 6b1196
-
Partition coefficient
Reference
-
-
-
-
None None 0.7 80 None 88 126 None
13809 11697 10876 13027 14101 14120
0.9 1.o 1.2 1.1 1.2 1.2
6b1283 6al323 6b/242 6b1261 6b1273 6b/275
15.4 21.9 3.7 7.0 4.8
2c/249 2c/462 2c/576 2b/115 2f/207
6.42 1.18 2.55 1.02
V2/385 V2/585 VU622 P960
26.7 4.1
1x/3/1368 2f/383
0.24
P1270
4.5 5.0
2b/302 2b1432
0.93
P3982
2.2 1.4 1.o 2.9
1x/1/393 1x/1/393 6b/234 1x/1/393
37 29 64 50 82 73 89 Azeo 93 None
72 98 88 76 94 91 62
2113 4139 6514 6399 8182 8368 8284
98
9869 11727
97
98
4312
82 123 77 93 86 97 None
10002 6592 846 1
None 24 81
1168a 3009
8 None
2227 10531
121
-
Azeotrope Solute Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DIPE Dibutyl ether MTBE 1,CDioxane THF
X% w/w
"C
10 30 87
56 77 98
Reference
None 56
92
7552
5558 7594 9302 11826a
Azeo
CS2
Acetic acid An iIine Nitrobenzene Morpholine Pyridine &Nitropropane ketonitrile u: rfuraIdehyde )hen01 Nater
83 95 None
3204 11197
75
8860 6289 2810 878 1 10936 734
90
Reference
6.1 3.3 2.1
3bI224 3 +4/3 17 1x/1/395
14.4
lx/3/1368
Partition coefficient
Reference
0.30
V21507
12196
Esters Me acetate 3 57 Et acetate 6 77 i-Propyl acetate 33 88 n-Butyl acetate None Cellosolve acetate Miscellaneous DMF DMAc DMSO Sulfolane
5393 7384 11801
Solute f
96 95 77 98
34 5 Vone 75 90
2.5 1.5
3 +4/480 1x/1/394
2.4
1x/1/394
16.5
1x/3/1367
1.3
1x/1/393
6.2 2.5
51189 6bl241
2.9
6bl239
31.3 8.5 8.9
1x/1/393 3a1137 2bI382
Hydrocarbons
n-Nonane Alternative names Reference codes CAS number UN number
1920
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
128 CgH2o 151 -53 0.718
Cubic expansion coeff (per oC x 103) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
31 205
Lower explosive limit (ppm) Upper explosive limit (ppm)
8700 29000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
300
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
5263 4.4 4 47
0.4
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) Log1Oactivated carbon partition Log1Opartition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
Hazchem code EPA code
1.1 22.9 0.67 1.403
O.2E-4 79E-4
3.50
Vapour pressure equation constants (Loglo. mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
0.9
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/molfC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Wa:als' surface area Molar volume
9037 1359 71 2.31 595 3690 6.52 5.48 178.3
6.93442 1429.459 201.820 7.24534 1662.9 Kauri butanol value Evaporation time (ether = 1) Evaporation time (BuAc = 1)
Hydrocarbons
Azeotrope Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics TetraIin Alcohols Methanol Ethanol n-PropanoI i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-PropanedioI Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,1,l-TCA TCE Perk. MCB Hydrocarbons
X% w/w
"C Reference
Solute g
1.o 0.8 0.8
-
-
17
64
2
97
29
116
128
Reference
-
-
6.16 1.25 2.1 1
V2B9 1 V2/586 V2/623
1x/3/1387
14106 14118
2119
8203
6.7 4.2 9.5 12.0 5.6
50
Partition coefficient
1xf311387 1~/3/1387 lxf311387
-
1.o
None 19 144
Reference
8493
2~4398 2d505 2f/95 2f/209 lxf311387
rzeotrope ~
:%
Solute
"C Reference
YIW
Vetones ketone MEK MlBK Zyclohexanone NMP ketophenone
Solute f
6.4
Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane THF
Reference
Partition coefficient
Reference
3bl236
13.7
1x/3/1387
2.2
3+4/481
16.1
1x/3/1387
Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetatf Miscellaneous DMF DMAc DMSO Sulfolane cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
31 57
113 149
3230 11210
10 25
115 118 80
8870 6293 2812
40
95
789
2.4
6bI352
Hydrocarbons
n-Decane Alternative names Reference codes CAS number UN number Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4) Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
Hazchem code EPA code
142 CloH22 174 -30 0.730
Cubic expansion coeff (per oC x 103) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
1.06
44
Lower explosive limit (ppm) Upper explosive limit (ppm)
8000 25000
Vapour concentration @21°C ppm Vapour density {relative to air) Vapour pressure @21°C mmHg POCP
1980 4.9 1.5 46.4
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm) Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
O.O2E-4 72E-4
3.49
Vapour pressure equation constants (Loglo. mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric Constant (20°C) Polarity (water 100) Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol!'C) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
1.408
6.7
7.44000 1843.12 230.220 7.33946 1801.3
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
0.9
1504 2.11 617 6864 7.20 6.02 195
Hydrocarbons
Azeotrope K%
Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes C, Aromatics Tetralin Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol l-Octanol Ethanediol DEG 1,2-PropanedioI Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,1,1-TCA TCE Perk. MCB Hydrocarbons
"C
Reference
w/w
Solute f' 1.o 1.o 1.o 1.o
-
-
0.9 0.8 1.3
75
166
Partition coefficient
Reference
-
-
0.06
V3/133
1x/4/14 10 1x/4/1411 1x/4/14 12 1x/4/14 12
1x/4/1411 6d574 1x/4/1411
15033
2126
None None None None 92
Reference
8213
None
77
161
4434
8
123
6628
0.6 3.3 5.8 5.1 12.4
2e/l93 2a/508 2a/606 2b/118 2b1236
1.1
2d/285
7.1
2f/542
1.3
6b/392
seotrope %
iolute (etones ketone d EK ABK 2yclohexanone IMP ketophenone
"C Reference
IIW
5396
lone lone
Fthers liethyl ether IIPE Iibutyl ether WTBE 1,4-Dioxane THF
Solute f 1.2 3.8
Reference
Partition coefficient
Reference
+
3 41247 3bl396
12.6
1x/4/14 10
3.2
1x/4/14 10
15.5
1x/4/14 10
Esters Me acetate Et acetate i-Propyl acetate v-Butyl acetate Cellosolve acetal Miscellaneous DMF DMAc DMSO Sulfolane CS2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
20 54
117 167
None
3237 11230
1.1 5.3
6d57 1 51191
8872
1.7
6bl386
81
2815
168 97
11016 842
4.5
65
3 i4/59
Hydrocarbons
2,2,4-Trimethyl pentane Alternative names ISO-Octane, ISOPAR C, 2,2,4-TMP Reference codes CAS number UN number
540 84 1
Hazchem code EPA code
3YE
114 C8Hl8 99 -107 0.692
Cubic expansion coeff (per oC x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
1.00
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
-12 418
Lower explosive limit (ppm) Upper explosive limit (ppm)
11000 60000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
400
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
4.1 41
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
3.51
Vapour pressure equation constants (Log1o. mmHg) Antoine equation A B C Cox chart A B
6.80304 1252.59 220.119 7.04642 1370.5
Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100) Thermal information Latent heat (car/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/molfC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
18.33 0.477 1.389
2.2E-4 0.011
7.4
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
27
7396 1211 55.6 2.59 544 2157 5.85 5.01 166.1
Hvdrocarbons
~~
Azeotrope ~
K% Solute
"C Reference
w/w
Solute f
Reference
Partition coefficient
Reference
-
-
20.1 31.2
V2/139 V2/386
~~
Hydrocarbons +Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes Cg Aromatics TetraIin Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol l-Octanol Ethanedio1 DEG 112-Propanediol
None None
13809 14715
-
-
None 2 80 None None
11699a 10880 13040
1.o 1.o 0.7
-
1xJ1/398 6b/197 6b/283
-
1.4 1.4 1.4
6a1328 6b/304 6b/323 6b/333
1.9
47 58 59 16
59 72 85 77
2114 4167 6524 6419
16.6 29.3 11.2 4.4
2a/250 2a/503 2d500 2b/l16
73 56
92 88
8378 8254
5.2
2b/284
35
99
9882
2.1 1.5 1.2
1x/1/397 1x/1/397 6b/285
Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1 1I 1-TCA TCE Perk. MCB Hydrocarbons
Vone
1168b
keotrope :%
Solute Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone
Reference
Partition coefficient
Reference
2.4 3.7
3b/225 3b/395
0.11 0.10
V3/30 CEH
1.4
1x/1/398
3.1
1x/1/398
1.3
1x/1/397
11196
6.5
6b/318
8868 6292 281 1
7.5
6b/297
"C Reference
V/W
)O
Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,CDioxane THF Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetate
Solute T
Miscellaneous DMF DMAc DMSO Sulfolane cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
lone 77 79
LO
96 95 69
keo lone 39 79
31.5 13.1 17.3
1x/1/397 3+4/55 2b1383
734a
Yydrocarbons
Cyclohexane Alternative names Hexamethylene, benzene hydride Reference codes CAS number UN number
11082 1145
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
7
Hazchem code EPA code
3YE
84 C6Hl2 81 +6.5 0.778
Cubic expansion coeff (per oC x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
1.2 24.98 0.980 1.424
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
-17 260 7.0E-18
Lower explosive limit (ppm) Upper explosive limit (ppm)
13000 84000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
10000 100 300 400
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
155700 2.9 78.8 25
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
0.0055 0.01 +4.15 0.6
(5)
3.43
Vapour pressure equation constants (Log10l mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric Constant (20°C) Polarity (water 100)
8.2 0.3 2.01 0.6
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/molrC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der W~als' volume Van der Waals' surface area Molar volume
7140 874 36.4 4.07 553 627 4.05 3.24 108.57
6.85146 1206.470 223.136 7.04736 1295.8 Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
50 3.4 5.6
Hydrocarbons
~
Azeotrope X%
Solute
"C Reference
WIW
Solute r"
Reference
Partition coefficient
Reference ~~
Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics Tetralin Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol D EG 1,2-PropanedioI Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,1,l-TCA TCE Perk. MCB Hydrocarbons
~
None None
11690 11697
None
11699a
1.2 4.0 0.9 1.7
1.o
-
-
6d205 6al283 6d3 10 6d3 11
c0.01 c0.01
V31278 v31340
20.9 13.0 10.0 12.0 9.0 9.9 4.5 16.7
2al239 2d430 2al579 2f/69 2fll79 2fl3 17 2fl234 1V3I122 7
14.8 23.0 6.6 8.0 1.8
P159 v21350 P639 V2/613 P950
22.1
2b/128 1.4
P3977
-
50 77 None
10854 11694
1.4 1.5 1.7 2.0
62 70 80 68 96. 86 82 None None None
2079 4087 6495 6384 8146 8338 8234 9752 9834 11684
None
4255
85 77 None
6572 8430
6al328
-
-
54 65 74 69 80 78 76
6d119 6a/273 6a/304 6al323
-
None None 50 74
1490 1159 300 1
1.1 2.6
6d159
None
2328
1.5
6d155
Vone
10515
1.71
6d202
6a/142
Azeotrope (%
Solute
"C Reference
NlW
Solute 4"
Reference
Partition coefficient
Reference
Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone
33
50
53 72
rlone
5378 7374 11685
4.7 2.8 2.7 2.7 9.4
3+4/213 3 +41297 3 413 54 3 +4/33 7 3b1447
1.o
3+41555
1.3 3.0 1.6
1xi31122 7 3+41468 1x/3/1227
3.4 2.7
51393 51506
2.1
51585
+
1.95 0.13
P492 V3l2 5
Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane TH F
75
Esters 17 Me acetate 16 Et acetate 75 i-Propyl acetate n-Butyl acetate Cellosolve acetate
80
75 0
55 73 79
534 1 7583 9296
Miscellaneous DMF DMAc DMSO Sulfolane cs2
Acetic acid Ani Iine Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
rlone 9 79 lone lone
30 IO lone
81 62
1269 3173 11148 8846 6283 2797 8763
19.2 11.2
1x/3/1226 1x/1/271
90.0 1.1 15.6 4.7 9.9
1xi311227 6all54 51146 6a1255 6a1203
2.8 6.9
6all77 1x/1/270
16.7
3+4145
12.8 0.2
1.59 31
70
V21259 P1713
P1622
522
Hydrocarbons
Benzene Alternative names Benzole, benzol, not benzine Reference codes CAS number UN number
71 43 2 1114
Hazchem code EPA code
3WE UO19
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
78 C6H6 80 +5.5 0.879
Cubic expansion coeff (per °C x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
1.24 28.9 0.65 1.498
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
-11 592 4.4E-17
Lower explosive limit (ppm) Upper explosive limit (ppm)
13000 71000
2000 5
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
117000 2.8 78 19
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
300
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) Log1o activated carbon partition Log1o partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
0.18 0.063 3.6 +2.13 1.2 (10) 3.08
Vapour pressure equation constants (LOglO. mmHg) Antoine equation A B C Cox chart A B
6.87987 1196.760 219.161 7.04500 1290.9
Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
9.2 0 2.28 11.1
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/molrC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
7340 749 31 4.9 562 2375 3.19 2.40 89.41
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
112 2.6
Hydrocarbons
Azeotrope
X% Solute Hydrocarbons n-Pentane n-Hexa ne n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes Cg Aromatics Tetra1in Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-PropanedioI Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,l ,l-TCA TCE Perk. MCB Hydrocarbons
"C
Solut2 y
WIW
Reference
None 5 68 0.7 80 None
9741 1086 1 10876 10879
1.8 1.5 1.7 1.2
6d118
None 98 80 50 77
10880 10854
1.1 1.5 1.5
6c/574 6bl304 6a1205
-
-
None None None None
10871 10878a
61 68 83 67 None 92 85 None None None
10882a
57 68 77 72 79 79
2066 4073 649 1 6375 8136 8333 8232 9748 982 1 10856
None None None
4239 8520 6654
None None
6567 8425
None None 82 80
1486 1154 2999
None None None
2326 10509
-
0.9 1.o 1.o 2.2
9.7 13.2 5.7 6.9 4.3 116.0 3.6
5.7
0.9 0.9 1.1 1.0 1.o 1.o 1.3 1.o
Reference
Partition coefficient
Reference
-
-
2.3 8.0 1.3 0.86 0.19 0.24 0.33 0.15
v21121 P379 P636 V21595 V3/118 V3/142 V31129 P1268
1.42
P3978
6a1535 6b1123 6b1242
-
71823 71306 713 10 71322
2a1205 2a1399 2a1556 2f165 2fll69 2f13 16 2f1227
2b1127
1xf11225 7/80 717 71142 71121 711 14 711 12 71243
Azeotrope
X% Solute Ketones Acetone MEK MIBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane THF
"C
WIW
Reference
Solute T
Reference
None 55 78 None
5374 7369 10857
1.9 1.3 1.1 0.7 1.0
3+4/195 3+41284 3 +4/35 1 3b1503 3 b144 1
None None 88
12
Esters Me acetate 0.3 43 Et acetate 6 77 i-Propyl acetate None n-Butyl acetate None Cellosolve acetate Miscellaneous DMF DMAc DMSO Sulfolane
cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Aceton itriI e Furfuraldehyde Phenol Water
Partition coefficient
Reference
0.43
P497
0.001
P2745
8293 10863
0.7 1.2
3 +4/5 16 3+41553
7537
1.1 0.8
3 41465 1x/3/1183
0.24 0.06
v3172
1.3 3.7
513 75 51502
0.08 0.02
P518 P863
0.9
51583
<0.01
V31279
4.6 3.4 3.3 3.8 1.3 5.1 1.5 1.5
1x/1/226 1x/1/227 71169 71191 71100 51127 71263 71253
3.33
V21542
0.53
V3188
21.0 0.12
P30 1 P1716
1.2 2.2 3.0 1.8 4.8
71220 71186 71124 3 4/44 2b1359
2.49 0.09
V3/105 P1104
0.03 0.05 0.08
V21182 V3/190 V31265
5537 7580 9294 10859
None
5863
None
4184
None 98 80 None None
1265 3163 10850 10703
None None 66 73 None None 91 69
884 1 6281 2795 8760
+
+
V41238
486
Hydrocarbons
Toluene Alternative names Toluol, methylbenzene, methyl benzol Reference codes CAS number UN number
108 88 3 1294
Hazchem code EPA code
3YE U220
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
92 C7H8 110.6 -95 0.867
Cubic expansion coeff (per oC x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
1.1 28.5 0.59 1.494
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
4 480 8.0E-16
Lower explosive limit (ppm) Upper explosive limit (ppm)
12700 70000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
2000 50 150 40
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour Pressure @21°C mmHg POCP
31000 3.2 23.2 56
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
0.052 0.033 2.9 +2.69 1.19 (5) 3.13
Vapour pressure equation constants (Loglo. mmHg) Antoine equation A B C Cox chart A B
6.95087 1342.31 219.187 7.12773 1448.2
Solvent properties Solubility parameter Dipole (D) Dielectric Constant (20°C) Polarity (water 100)
8.9 0.4 2.38 9.9
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol!'C) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
7985 892 41.0 4.22 591.8 1580 3.92 2.97 106.85
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
105 6.1 2.0
Hydrocarbons
AzeotroDe X% Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TM P Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics Tetra1in Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-PropanedioI Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,l,l-TCA TCE Perk. MCB Hydrocarbons
"C
Solute 1p"
WIW
Reference
None None None
12131 13027 13041
1.3 1.4 1.2 1.3
6d160 6d591 6b1169 6bl261
None None None
13043 11694 10871
1.4 1.2 1.o
6b1323 6a1283 71283
-
-
None None
13029 13030
64 31 77 32 93 51 81 31 106 68 101 55 45 95 None 90 110 None
2098 4120 6512 6397 8170 836 1 8246 9760 9852 11720
110 93 None 98 110
4285 853 1 6658
None 74 106 89 110 None
9978 6586 8450
None None None
1498 1166 3006
None None
2220 10524
-
1.1 0.83
Reference
-
Partition coefficient
Reference
-
-
20.8 11.6 1.05 1.16 0.17
V21135 V21372 V2/580 V2/6 19 CEH
0.20
V31130
0.78
P3980
71443 71444
6.3 5.3 4.3 3.9 10.3 3.8 3.3
2d268 2d477 2d592 2f178 2f1190 2b1289 2dl276
45.9
2f134 1
3.9 1.4
2f1337 2fl440
0.9 1.2 1.o 1.o
1x/3/317 71352 71332 71380
0.9
713 70
1.o
714 16
Azeotrope X%
Solute Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,CDioxane TH F Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetate Miscellaneous DMF DMAc DMSO Sulfolane cs2
Acetic acid Ani Iine Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
"C
WIW
Reference
None None 97 111
539 1 7382 11799
Partition coefficient
Reference
0.40
P501
2.22
V41223
2.97 0.03
V41190 P1719
71406
0.14
P1109
71373 3a1135 2fl393
0.07 0.03 0.12
V21191 V41258 P 1644
Solute f
Reference
1.8 1.4 1.2 1.4 0.3
3+4/236 3 +4/308 3+41356 3+41339 3b1456
1.2
3+41558
7550
1.3
3+4/375
None None None None
7591 9300 11825 11913
1.2
515 16
1.1
51586
None
5893a
1.9
713 90
None 72 101 None None
1276 3194 11167 10718
8.3 140.4 1.1 9.4 1.7 1.9
71386 71399 71361 51159 71426 71422
68 108 82 110 24 81 None None 80 85
8858 6285 280 1 8776 10920
1.8
None
20
8304
102
None
3.8 2.6 2.4 610
iydrocarbons
Ethylbenzene Alternative names Phenyl ethane Reference codes CAS number UN number
100 41 4 1175
Hazchem code EPA code
3YE ZO48
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
106 CSHlO 136 -94 0.867
Cubic expansion coeff (per oC x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
1.03 29.2 0.72 1.493
15 435
Lower explosive limit (ppm) Upper explosive limit (ppm)
10000 67000
2000 100 125 125
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
9960 3.7 8.0 59
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm) Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
0.020 0.033 3.1 +2.76 0.028 (5) 3.17
Vapour pressure equation constants (Loglo. mmHg) Antoine equation A B C Cox chart A B
6.96580 1429.550 213.767 7.19691 1579.7
Solvent properties Solubility Parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100) Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/molrC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
8.9 0.4 2.41
Kauri butanol value Evaporation time (ether = 1) Evaporation time (BuAc = 1)
8.8 0.84
8491 1038 43 3.74 617 4.60 3.51 123.1
Hydrocarbons
Azeotrope X%
Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TM P Cyclohexane Benzene Toluene Ethylbenzene Xylenes Cg Aromatics TetraIin Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol l-Octanol Ethanediol DEG 1,2-PropanedioI Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,l,1-TCA TCE Perk. MCB Hydrocarbons
"C
wlw
Reference
Solute r"
Reference
None 12 126 None
13807 14101 14106
1.7 1.2
6d489 6bl273
1.5 1.2 1.o 1.0
6bl333 6 d 3 10 71306 71443
None None None
10878a 13029
-
-
None
14098
None None 9 None 33 20 None 60 51
2106 4144 6517 6402 8185 837 1 8251 9765 987 1
97 115 107 130 126
B7 Azeo
133
432 1 8545
BO 49 57 4
135 117 126 140
9991 6596 8463
None
1167a
None
2225
-
-
6.5 6.1 3.3 2.0 2.7
2d245 2d460 2d601 2dl95 2bl228
3.1 2.9
2bl132 2bl299
0.9 0.7
71464 7/466
1.o
71469
Partition coefficient
Reference
-
-
2.0
V2162 1
2.0 0.85
V31158 P3977
~~
keotrope Reference
Solute Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane THF
Vone Vone Vone
11802
None
14102
Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate None Cellosolve acetate None Miscellaneous DMF DMAc DMSO Sulfolane
65
Reference
2.1 1.4
3b1217 3 413 16
1.1
3 +41563
0.9
51540
5.0 2.0 1.6 1.5
51178 714 74 714 70 3+4/482
2.5 3.0
71465 3+4/51
Partition coefficient
Reference
0.07
V41268
+
11828 12007 134
cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
Solute f
34 115 None
3206 11183
None 8 120 None 95 132 None 67 92
886 1 6290 2804 8783 10943 676
Hydrocarbons
Xylenes (mixed isomers) Alternative names Dimethyl benzenes, xylol Reference codes CAS number UN number
1330 20 7 1307
Hazchem code EPA code
3Y U239
106 C8HlO 136*
Cubic expansion coeff (per oC x 103) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
1.0 28.6 0.7* 1.496
Physical properties* Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
0.870
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
23* 480 8.0E-16
Lower explosive limit (ppm) Upper explosive limit (ppm)
11400 70000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
10000 100 150 1.0
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure@ 21°C mmHg POCP
9180 3.7 7.0 85*
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
0.02 0.05 4.3 3.0 0.1 (5) 3.17
Vapour pressure equation constants (Loglo. mmHg)* Antoine equation A B C Cox chart A B
6.99053 1453.43 215.310 7.20807 1601.1
Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
8.9 1.3 2.3 7.4
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/molfC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
8692 1035 42 3.55 623 3180 4.66 3.54 121.84
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
98 13.5 0.76
*Typical mixture of isomers Hydrocarbons
Azeotrope X% Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2 2,4-TM P Cyclohexane Benzene Toluene Ethylbenzene Xylenes Cg Aromatics Tetralin Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i- Buta no1 s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-0ctanol Ethanediol DEG 1,2-PropanedioI Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 112-EDC l1ll1-TCA TCE Perk. MCB Hydrocarbons
"C
Reference
wlw
None None None 81
144
None None None
13808 14120 14118
13030 14098
-
-
Solute f
Reference
1.5 1.2 1.4 1.3
1x/1/369 6d605 6d497 6bl275
1.5 1.o 1.1
6al3 11 713 10 71444
-
-
6.6 5.3 3.3 2.6 3.1 2.6 2.7
2d247 2d500 2d575 241229 2bl229 2bl292 2dl282
Partition coefficient
Reference
-
-
3.08
v21379
0.56
P3979
None
None None 7 97 None 27 115 12 108 None
2108 4146 6519 6402 8186
90 140 None 11 93 135 Azeo
11730 4113 4323
6.3
2fl536
73 45 50 4
9994 6598 8465 12235
4.0 4.2
2 bll34 2fl4 16
None
137 120 128 144
8252
0.85
1x/1/369
0.9 1.1
71480 71490
0.9
71508
1167c
Azeotrope X%
Solute
Yetones ketone M EK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,CDioxane TH F
"C
Reference
WIW
None None
22
142
Esters Me acetate None Et acetate i-Propyl acetate None n-Butyl acetate Cellosolve acetatf None Miscellaneous DMF DMAc DMSO Sulfolane
cs2
Acetic acid Ani Iine Nitrobenzene Morpholine Pyridine 2-Nitropropane AcetonitriIe Furfuraldehyde Phenol Water
Reference
2.4 1.2 1.3 1.2 1.9
3131222 3bl382 3bl553 3b/511 3bl462
1.1
1x/3/1348
1.3
1x/3/1350
1.6
51541
2.5
71481
1.1 3.8
1x/1/369 5118 1
1.4
5.1 2.9
Partition coefficient
Reference
0.29
,V2/506
14.1 0.1.1
P310 P1718
71482
0.08
P1108
1x/1/369 3 +4/52
0.38
v21193
0.12
P1642
14117
7594 11829 12009 136
5894
22 116 None
3208 11185
80
Solute
None 90 139 None 63 93
2805 8785 10944 677
Hydrocarbons
C9 Aromatics Alternative names Reference codes CAS number UN number Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4) Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
2325
Hazchem code EPA code
Cubic expansion coeff (per °C x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
0.89 28 1.153
55 425
Lower explosive limit (ppm) Upper explosive limit (ppm)
9000 65000
8000 25 75 0.4
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
5200 4.2 4 84*
120 CgHl2 152* 0.876
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
0.0058* 0.035*
3.20
Vapour pressure equation constants (LoglOt mmHg)* Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water lOO)
7.1
Thermal information* Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol!'C) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (caVmol) Van der Waals' volume Van der Waals' surface area Molar volume
8952 1179 48 3.21 631 1680 5.30 4.04 139
7.0764 1571.0 209.7 7.25282 1670.2
Kauri butanol value Evaporation time (ether = 1) Evaporation time (BuAc = 1)
*Typical mixture of isomers Hydrocarbons
keotrope I(%
Solute
"C
U/W
Reference
Solute
Reference
None
10882a
1.1
71322
-
-
-
2.6
2d197
2.2
2fl241
3.3
2d/131
~~
Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n- Decane 2,2,4-TM P Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics TetraIin Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG lI2-Propanediol
-
2116 4173 6529 6422 820 1 8382
None None None None None None ? ? 50 156 None 85 153
9886 11750 14729 4372
148 122 134 160
10008 6618 8484 12252
Glycol ethers PGME EGME EEE EGBE
30 15 10 20
Chlorinated MDC Chloroform Carbon tet. lI2-EDC 1,1,1-TCA TCE Perk. MCB
None
Hydrocarbons
-
10566
Partition coefficient
Reference
zeotrope .%
Solute Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone
"C Reference
//W
?
152
Solute f
Reference
Partittion coefficient
Reference
0.33
V2/508
11374 2.8
3b/463
Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,6Dioxane TH F Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetate !5 Miscellaneous DMF DMAc DMSO Sulfolane cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
155
12024
lone 30
167
3225 11205
40 20 50
152 158 95
8805 10971 767
Leo
2.8 52.1
2b/385 1b/286
0.02
V3/301
Although individual C9 aromatics can be obtained commercially the mixture used as a solvent usually contains a mixture of up to eight isomers with atmospheric boiling points in the range of 152-176°C. In many cases some isomers form azeotropes with other solvents while others do not. If any azeotropes are reported they are included in the above table. Hydrocarbons
Tetralin Alternative names Tetrahydronaphthalene, tetranap Reference codes CAS number UN number
119642
Hazchem code EPA code
132 CloHl2 205 -31 0.974
Cubic expansion coeff (per oC x 103) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
1.0 35.5 2.0 1.539
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
74 225
Lower explosive limit (ppm) Upper explosive limit (ppm)
8000 50000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
25
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
526 4.6 0.4
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
4.8 O (5) 3.15
Vapour pressure equation constants (LOglO. mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100) Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/molfC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
0 2.77 9.3
7.52287 2019.3 Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
200
10098 1289 0.53 3.65 447 2978
136
Hydrocarbons
zeotrope ~
1% Solute
"C Reference
//W
Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics Tetra Iin Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol l-Octanol Ethanediol DEG 1,2-PropanedioI Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,1,l-TCA TCE Perk. MCB Hydrocarbons
13
~~
194
Solute T
Reference
1.9 1.9
1x/4/1398 1x/4/1398
1.4 1.o
W4t1398 1x/4/1398
-
-
2.2
2b/235
2.1
2f/54 1
Partition coefficient
Reference
rzeotrope Solute
1% ilw
"C Reference
Solute f'
Reference
Partition coefficient
Reference
4.6
V2/3 10
Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,CDioxane THF Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetate Miscellaneous DMF DMAc DMSO Sulfolane cs2
Acetic acid Ani Iine Nitrobenzene Morpholine Pyridine 2-N itropropane Acetonitrile Furfuraldehyde Phenol Water
!O
99
806
Hydrocarbons
Section 2
Alcohols
Methanol Alternative names Methyl alcohol, wood alcohol, carbinol, not methylated spirit Reference codes CAS number UN number
67 56 1 1230
Hazchem code EPA code
2PE U154
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
32 ClH4Ol 64 -98 0.792
Cubic expansion coeff (per oC x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
1.2 22.6 0.6 1.326
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
15 470 1.5E-9
Lower explosive limit (ppm) Upper explosive limit (ppm)
60000 365000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
25000 200 250 6000
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
156000 1.11 103 12.3
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
Total Total 0.86 -0.82 1.12 (5) 1.5
Vapour pressure equation constants (LOglO' mmHg) Antoine equation A B C Cox chart A B
8.08097 1582.271 239.726 8.23606 1579.9
Solvent properties Solubility parameter Dipole (D) ,
14.5 1.7
Dielectric constant (20°C) Polarity (water 100)
32.6 76.2
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/molfC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' .surface area Molar volume
8426 150 19.5 7.96 513 758 1.43 1.43 40.4
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
380 6.3 4.1
Alcohols
Azeotrope
X% wlw
"C
Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes Cg Aromatics Tetra1in
8 50 52 72 83 None 53 38 39 69 None None None
31 68 59 63 64
Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol l-Octanol Ethanediol DEG 1,2-PropanedioI Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. l12-EDC 1,1,1-TCA TCE Perk. MCB Alcohols
Reference
Solute r"
Reference
2055 2087 2101 2113 2120 2126 2114 2079 2066 2098 2106 2108 2116
11.2 16.0 22.1 45.1 38.6 49.7 28.1 18.3 7.4 8.4 10.3 10.3
2d132 24253 2d243 2d249 2d191 2d250 2a/239 24205 2a1268 2d245 2c/247
-
-
-
-
None None None None None
1944
59 54 58 64
1978a 2015
1.o 1.3 0.9 1.3 1.3 0.7 1.4 1.4
2d193
2450 2al122 24123 2a/169 2a/171 2d128 2a1202 2a1201
None None
2056
None
1945
2a162
None
1979
2d98
93 B7 79 32 22 38 64 None
38 38 56 61 56 59 64
1544 1430 1090 1930 1923 1915 1914 2063
2.1 2.7 7.0 5.4
2a/24 2d23 241 2d44
8.3 17.9 7.8
2a140 2437 2al204
Partition coefficient
Reference
Azeotrope X%
Solute Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane THF
Reference
12 56 70 64 None
1963 1993 2084
98 24
2091a
cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
62 57
10 51 None 31 59
Esters 19 Me acetate 46 Et acetate i-Propyl acetate 80 n-Butyl acetate Cellosolve acetate Miscellaneous DMF DMAc DMSO Sulfolane
"C
W/W
54 62 65
2058 1998 1996 1967 1999 2046
None
29 40 None
1175 1933
None
2065
None None 19 64
2024 1977 1925
None
213
Solute
Reference
1.8 2.1 3.3
2d68 2a/133 2d248
3.2 4.3 10.6 3.1 2.2 2.2
2a/170 2d261
2.9 2.8
2d92
5.8
2 d 2 13
0.8
2all15
0.25 4.0 12.2 0.9
2d62 2d125 2a/35 2d48
1.0
2al183
2.4 1.o
2a143
1.5
1/49
Partition coefficient
Reference
2d160 2d148 2 d l 41
2d154
2d140
Alcohols
Ethanol Alternative names Ethyl alcohol, grain alcohol, methylated spirits, IMS Reference codes CAS number UN number
64 17 5 1170
Hazchem code EPA code
2SE UOOl
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
46 C2H60l 78 -114 0.789
Cubic expansion coeff (per oC x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
1.1 22.3 1.08 1.359
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
13 419 1.4E-9
Lower explosive limit (ppm) Upper explosive limit (ppm)
33000 190000
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
64000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour Threshold (ppm)
1000 6000
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition Loglo partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
1.6 45.7 ?7
Total Total 1.35 -0.32 0.92 (5) 2.09
Vapour pressure equation constants (LoglO, mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D), Dielectric constant (20°C) Polarity (water 100)
13.4 1.7 22.4 65.4
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol!'C) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
9200 296 27 6.39 516 1198 2.11 1.97 58.68
8.11220 1592.864 226.184 8.24183 1651.2
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
325 8.3 2.4
Alcohols
Azeotrope X%
Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TM P Cyclohexane Benzene Toluene Ethylbenzene Xylenes Cg Aromatics Tetralin Alcohols Methanol Ethanol n-PropanoI i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol l-Octanol Ethanediol DEG 1,2-Propanediol Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,P-EDC 1,l ,l-TCA TCE Perk. MCB
"C
W/W
Reference
Solute 4"
Reference
6.9 8.9 11.3 15.1 24.5 14.5 10.8 7.5 4.0 5.9 6.4 7.7
2c/375 2a1353 2a/498 2d462 2d398 2d508 2d503 2a/430 2d399 2d477 2c/460 2d500
5 21 72 78
34 59 98 77
4062 4106 4139 4165
40 31 32 63 None None None
72 65 68 77
4167 4087 4073 4120 4144 4146 4175
None
1944
-
-
None None None None None None None None None None None None
3981 3980 4026 4029a 4027 4063 1066
None None None
3982 4032
1.1
-
2a/60
-
1.1 1.o 1.o
2d236 2d341 2a1365
1.o 1.1 1.3 2.3
2a/366 2d396 2d395 2d42 1
6.5
2c/297
1.9
2c/319
2c/350
40 59 65 70
1551 1442 1105 2964
1.7 2.0 4.7 3.6
2d283 2d285 2d276 2a/299
28 71 63 77 None
2286 2162 4070
4.7 6.1 5.6
2d295 2c/285 2d397
2 7 16 37
Partition coefficient
Reference
~
Azeotrope X%
Solute Ketones Acetone MEK MIBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane THF
"C
wlw
Reference
Solute f
Reference
None 39 74 None
3965 4005 4101
1.8 1.7 2.1
2a1321 2a1343 2d423
None 17 64 None
4029 4110 4170
2.6 4.1 5.0
2d375 2a1459 2d391
>98 7 8
4011 4009
2.2 1.5
2a1348 2a1328
3969 4012 4054
1.9 2.4 2.1 3.1
2d335 2d351 2d391 2d426
0.7
2d37 1
8.1 6.5 0.7 4.9
2d344 2a1281 2d293 2a1427
0.6 1.o
2d345 2d355
1.9 5.5
2d298 2d383
2.7
11165
10
Esters Me acetate 3 57 26 72 Et acetate 77 i-Propyl acetate 52 n-Butyl acetate None Cellosolve acetate Miscellaneous DMF DMAc DMSO Sulfolane cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane ketonitri le Furfuraldehyde Phenol Water
None
9
43
1189
None None
4075 4072
None 94 78 56 73 None
4038 3978 2760
96
78
242
Partition coefficient
Reference
Alcohols
n-Propanol Alternative names Propan-1-ol, n-propyl alcohol, 1-propanol, ethyl carbinol Reference codes CAS number UN number
71 23 8 1274
Hazchem code EPA code
2SE
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
60 C3H80l 97 -127 0.804
Cubic expansion coeff (per oC x 103) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
0.96 23.7 1.72 1.383
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
25 440 9.0E-9
Lower explosive limit (ppm) Upper explosive limit (ppm)
21000 135000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
4000 200 250 45
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
18000 2.07 13.4 45
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C o;oW/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
Total Total 1.67 +0.34 1.5 2.40
Vapour pressure equation constants (LoglOs mmHg) Antoine equation A B C Cox chart A B
8.37895 1788.020 227.438 8.25022 1755.8
Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
11.9 1.7 20.1 61.7
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/molfC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
9780 438 34 5.10 537 1240 2.78 2.51 75.14
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
250 9.0 1.0
Alcohols
~~
Azeotrope Solute
X% w/w
Hydrocarbons n-Pentane n- Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes Cg Aromatics Tetra1in
None 4 36 70 98 None 41 20 17 49 91 93 None
Alcohols Methanol Ethanol n-Propanol iPropanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-Propanediol Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC l,l,l-TCA TCE Perk. MCB Alcohols
"C
Reference
66 88 94 97 85 74 77 93 7 97
None None
6484 6505 6514 6523 6524 6495 649 1 6512 6517 6519 6529
3981
-
-
13.3 5.0 6.6 8.3 8.7 6.5 3.8 3.3 3.3 3.8 4.0
2a/584 2a/596 2a1576 2d505 2al606 2d500 2al579 2a.556 2a/592 2a160 1 2c/575
1.1 1.1
2a/122 2a/336
-
Partition coefficient
Reference
1.2
CEH
-
-
-
2d53 1 2a/539 2a/541
0.07
CEH
6486
1.0 1.0 1.8
2d47 1 2a/548 2d414
4195a
6.2
2c/483
2.9
2c/491
1.3
2c/490
2.7
2d416
3.3 2.4
2a/509 2a/520
5.9
2a1518
3.5
2a1552
6465 6463
None
None
73 81 73 82 94 97
Reference
1.1 1.1 1.1
None None None None None None
None None 8 19 7 17 48 80
Solute f
1454 1116 297 1 2296 2177 6489
Azeotrope
K% Solute
Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,CDioxane THF
"C
WIW
Reference
None None 35 94
5320 6445
None None
6464
55 None
6447
Esters None Me acetate None Et acetate i-Propyl acetate n-Butyl acetate 40 94 Cellosolve acetate Miscellaneous DMF DMAc DMSO Sulfolane CSZ Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
Solute f
Reference
1.6
2c/496
0.2
2d461
3.6 3.2
2a1586
1.8 1.2
2d533 2d497
3.6 1.7
2d530 2d536
14.5
2d484
0.4
2d454
46
1209
3.6 0.9
2d417 2a/525
2c/512
28
6469 627 1 2768
0.8
96 81
3.0
2~4430
71
87
293
3.95
11301
5
\one
75
Partition coefficient
Reference
Alcohols
i-Propanol Alternative names Propan-2-ol, isopropyl alcohol, IPA -avoid
confusion with IP acetate
Reference codes CAS number UN number
67 63 0 1219
Hazchem code EPA code
2SE
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
60 C3H80l 82 -88 0.786
Cubic expansion coeff (per oC x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
1.05 21.7 2.0 1.375
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
12 425 6.0E-8
Lower explosive Upper explosive
23000 127000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
20000 400 500 60
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
Total Total 1.46 +0.26 1.59 2.40
Vapour pressure equation constants (LoglOt mmHg) Antoine equation A B C Cox chart A B
8.87829 2010.33 252.636 8.24362 1673.2
Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
11.5 1.66 18.3 54.6
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol!'C) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
9540 433 37 4.76 508 1282 2.78 2.51 76.92
limit (ppm) limit (ppm)
Kauri butanol value Evaporationtime (ether = I) Evaporationtime (BuAc = I)
46000 2.07 35.1 15
230 11 1.5
Alcohols
Azeotrope Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics Tetrali n Alcohols Methanol Ethanol n-Propanol i-Propanol &Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-PropanedioI
X% w/w
"C
6 23 51 84 Azeo None 54 32 33 69 None None None
35 63 76 82
6370 6390 6399 6418
77 69 72 81
6419 6384 6375 6397 6402 6404 6423
Reference
None None None
1978a 3980
-
-
None None None None None None None None None None
Solute f
Reference
5.0 7.4 7.8 7.9 6.6 4.8 4.7 4.0 3.8 5.3 5.0 5.0
2b197 2bll13 2bll15 2f195 2b1118 2b/l16 2 b/84 2b/65 2b1108 2d/95 2d/96 2d197
0.9 1.1 1.02
2d123 2d341 2f/47
1.6 1.o 1.1 0.82
24/55 2d/56 2b/62 2f163
2.6
2d/47
2.31 1.6 3.3
2f/36 2d/40 2b136
4.0 5.7 4.9
2d/43 2d/42 24/64
-
Partition coefficient
Reference
-
Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,1,l-TCA TCE Perk. MCB Alcohols
None 4 18 43 None 30 70 None
61 69 75 75 82
1561 1453 1115 2970 2729 2295 2176 6373
-
Azeotrope Solute Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane THF Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetate Miscellaneous DMF DMAc DMSO Sulfolane
cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropan Acetonitrile Furfuraldehyde Phenol Water
X% w/w
"C
Reference
Solute Ip"
Reference
2.4 1.5 1.7
2 b143 2 b154 2b/96
2.9 3.9
2b1101
6337 6335a
1.7 1.4
2b/56 2b155
5516 6338 6363
2.5 1.7 1.77 2.0
2b150 2b159 2f/59 2d175
None 32 78 None
5319 6335 6386
None 15 66
6351 6391
None None None 25 75 52 80 None
Partition coefficient
Reference
None
8
44
2.5 13.6
2f139 2d/53
0.6
2d144
1208
0.9
2d157
96 48
82 75
6270 2767
2.57
2f140
88
80
292
3.2
11334
Alcohols
n-Butanol Alternative names Butyl alcohol, 1-butanol, butanol, propyl carbinol Reference codes CAS number UN number
71 36 3 1120
Hazchem code EPA code
3Y UO31
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
74 C4HlOOl 118 -80 0.810
Cubic expansion coeff (per oC x 103) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
0.79 24.6 3.0 1.397
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
35 360 9.1E-9
Lower explosive limit (ppm) Upper explosive limit (ppm)
14000 112000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
8000 50 50 5000
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
6300 2.55 4.8 55
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
7.3 20.4 2.36 +0.88 1.15(5) 2.21
Vapour pressure equation constants (Log10r mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
11.4 1.66 18.2 60.2
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/molfC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
10434 586 41 4.41 563 2215 3.45 3.05 91.97
7.83800 1558.19 196.881 8.25925 1871.7
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
225 33 0.47
Alcohols
Azeotrope
X% Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TM P Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics Tetralin Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-PropanedioI Glycol ethers PGME EGME EEE EGBE Chlorinated M DC Chloroform Carbon tet. 1,2-EDC 1,1,l-TCA TCE Perk. MCB Alcohols
"C
Reference
Solute
Reference
68 94 110 116
8163 8182 8194 8203
4.1 2.8 4.2 6.6 10.0 8.9
2bl169 2bl200 2b1218 1x/3/107 5 2fl209 2131236
80
8146 8136 8170 8185 8186 8198
WIW
None 3 18 50 72 8 4 None 28 67 73 None
105 115 115
None None None None
2015 4026
-
-
None None None None None
8103 8102
None None
None 3 None 3 30 56
8106 8106
77
1133 2984
87 109 115
2306 2186 8133
3.3 2.1 2.3 2.7 2.7
2bl188 2f/169 2bl207 2b1228 2b1229
3.1
2b1235
1.3 1.0 1.o 1.o
2at169 2a/365 2at539 2dl55
-
Partition coefficient
Reference
0.84 0.34 0.12 0.24
V2t99 V4l2 05 V4t226 V2/590
-
-
-
1.o 0.9 1.o 1.1 1.2
2bl161 2bl154 2b1173 2b1170 2b1193
0.07
V31110
2.6 1.8 1.8
2dl6 2d1174 2d1137
1-10
V21420
1.1
2fll89
1.9 1.5 2.4 2.3 2.0 2.8 3.1 2.5
1x/1/130 2b1136 2b1135 2b1137 2f/123 2f/l2 1 2d1155 2b1175
Azeotrope X%
Solute Ketones Acetone MEK MIBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane THF Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetatf Miscellaneous DMF DMAc DMSO Sulfolane cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane ketonitrile Furfuraldehyde Phenol Nater
"C
WIW
Reference
Solute T
Reference
None None 30 114
5344 7357 8152
1.1 2.0 1.8
2b1140 2b1143 241193
None None 83 118
8104
1.7 2.4 2.4
1x/3/1072 2b1202 2d123 1
1.1 1.2
2bl147 2b1146
1.o 1.8
2f1137 2bl148
1.7
2bl197
0.5
2f1131
8195
None None
None None 63 1 None
8121 8153 8160
None None 57 120 None None
1233 3135 8138 8135
2.6 1.o
2fl120 2dll58
70 119 48 112 None
8109 6275
0.7
2b1166
4.1 3.2
2dll56 2f1155
5.1
11407
58
93
372
Partition coefficient
Reference
0.31 0.14
V21469 V41237
0.20
P307
Alcohols
i-Butanol Alternative names Isopropyl carbinol, isobutyl alcohol, IBA, 2-me-1-propanol Reference codes CAS number UN number
73 83 1 1120
Hazchem code EPA code
3Y U140
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
74 C4HlOOl 108 -108 0.802
Cubic expansion coeff (per oC x !03) Surface tension (@20°C dyn/cm) Absolute Viscosity (@25°C cP) Refractive index (25°C)
0.95 22.8 3.96 1.394
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
25 390 1.6E-8
Lower explosive Upper explosive
16000 109000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
8000 50 75 80
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
8.7 15. 2.1 +0 1.6 2.6
Vapour pressure equation constants (LOglO, mmHg) Antoine equation A B C Cox chart A B
8.53516 1950.94 237.147 8.25506 1816.5
Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100) Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/molfC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
10.7 1.7 17.7 55.2
limit (ppm) limit (ppm)
11500 2.56 8.6 40
O 6 .74 2
Kauri butanol value Evaporationtime {ether = 1) Evaporationtime {BuAc = 1)
25 0.6
10220 585 53 4.30 548 3.45 3.05 92.91
Alcohols
Azeotrope X% Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes Cg Aromatics Tetralin Alcohols Methanol Ethanol n-Propanol i-Propano1 n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-PropanedioI Blycol ethers PGME EGME EEE EGBE 2hlorinated MDC zhloroform zarbon tet. 1,2-EDC l,l, 1-TCA TCE 'erk. WCB Alcohols
oc
Reference
Solute Y
Reference
68 91 104
8327 8354 8368 8377
5.3 4.0
2f/320 2f1326
92 78 79 101 107 107
8378 8338 8333 836 1 837 1 8373
3.2 3.4 2.7
2f/3 17 2f/3 16 2b1289
2.8
2b1292
0.9
2f150 2d156 2fll53
WIW
None 2 27
27 14 8 45 80 88
None None None None None
4029a 6465 8103
-
-
8328
None
2.3
None None
6548 8306
9 40 53
-
1.o 0.9
None None None
None 5 6
1.o 1.o
-
2fl223 2f/3 11
2f/l2
76 83
1475 1137 2988
2.1
2b1272
85 103 107
2309 2189 833 1
2.5
24/357
Partition coefficient
Reference
0.24
VU552
-
-
Azeotrope
X% Solute
Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane THF Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetate Miscellaneous DMF DMAc DMSO Sulfolane
cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile FurfuraIdehyde Phenol Water
"C
WIW
Reference
Solute .p"
Reference
None None 91
5347 7360 8343
1.4
2f1304
1.5
2b1278
108
101
None None None None
7522
7570 8318 8345 8352
None
0.03
P864
0.4
2bl275
1.o
2f1302
0.21
P308
0.03
P1107
None Azeo
1236
None 67 105 None
8307 6278 2779
0.7
2f1307
3.4
2f1300
376
4.8
11440
57
Reference
8379
None 4
Partition coefficient
89
Alcohols
s-Butanol Alternative names 2-Butanol, methyl ethyl carbinol, 2-hydroxy-butane Reference codes CAS number UN number
78 92 2 1120
Hazchem code EPA code
3Y
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
74 C4HlOOl 99.5 -115 0.807
Cubic expansion coeff (per oC x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
0.91 23.0 3.7 1.395
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
21 405 <1.0E-7
Lower explosive limit {ppm) Upper explosive limit {ppm)
17000 98000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
10,000 100 150 75
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
17600 2.56 13.2 55
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C o;oW/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
19.8 65.1 +0.61 1.87 2.59
Vapour pressure equation constants (Log1o. mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole {D) Dielectric constant {20°C) Polarity {water 100) Thermal information Latent heat {cal/mol) Nett heat of combustion {kcal/gmol) Specific heat {cal/molfC) Critical pressure {MN/m2) Critical temperature {K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
10.8 1.7 16.56 50.6
7.47429 1314.188 186.500 8.25102 1766.8 Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
195 13.0 0.9
9916 583 40 4.20 536
91.70
Alcohols
~~ ~~
Azeotrope X% Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n- Decane 2,2,4-TM P Cyclohexane Benzene Toluene Ethylbenzene Xylenes Cg Aromatics Tetralin
"C
WIW
Reference
Solute r"
Reference
None 8 67 37 88
8228 8242 8248
4.3 3.8
2bl250 2fl239
34 18 15 55 None None
8254 8234 8232 8246 8251 8252
2.6 4.1 1.6 1.8 2.1
2bl285 2bl284 2fl234 2fl22 7 2bl276
2.7 3.4
2bl282 2fl24 1
0.9 1.2
2d128 2d366
8102
1.1 0.9
-
2bl62 2bl154 2fl223
-
88 76 79 95
Alcohols Methanol Ethanol n-Propano1 iPropanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-PropanedioI
-
-
Glycol ethers PGME EGME EEE EGBE
lone
6547
None 8 74 12 82
1472 1134 2985
2.2 2.2
2fl2 17 2fl220
15 84 57 97 None
2307 2187 8230
2.1 4.0 2.7
2fl2 19 2bl240 2bl258
Chlorinated M DC Chloroform Carbon tet. 1,2-EDC 1,l ,l-TCA TCE Perk. MCB Alcohols
None None None None None None
4027 6463
1.o
Partition coefficient
Reference
LzeotroDe (%
olute
"C)
Solute
Reference
VIW
Reference
Partition coefficient
Reference
~
etones ,cetane
1EK 1IBK :yclohexanone IMP cetophenone
'thers biethyl ether )IPE )ibutyl ether ATBE ,4- Dioxane 'H F
7358
(one
40
99
1.4
2b1239
6.0
2b1251
4.8 0.9 3.8 12.5
2f/2 18 2f122 1 2bl265 2f1226
0.8
2fl224
2.3
2 bl24 1
7.3
11420
7520
:sten Ae acetate 3 acetate -Propyl acetate ,-Butyl acetate :ellosolve acetat
None
7568
None
8237
Aiscellaneous IMF >MAC IMSO Mfolane
>Sp ketic acid Wine q itrobenzene vlorpholine 'yridine !-Nitropropane ketonitrile :u rfuraldehyde 'henol Nater
None
823 1
None 82 99
8217 6276
73
87
373
0.20
P309
Alcohols
n-Amyl alcohol Alternative names 1-Pentanol, pentyl alcohol, butyl carbinol Reference codes CAS number UN number
71 41 0 1105
Hazchem code EPA code
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
88 C5Hl2Ol 138 -78 0.815
Cubic expansion coeff (per oC x 103) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
0.92
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
48 360
Lower explosive limit (ppm) Upper explosive limit (ppm)
11000 laaaaa
150 10
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
4030 3.1 3.0
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm) Aqueous effluent Solubility in water (25°C o;oW/w) Solubility of water in (25°C o;oW/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
25.6 4.0 1.408
1.7 9.2 2.74 +1.40
2.73
Vapour pressure equation constants (Loglo. mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
1.7 13.9 56.8
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/molrC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
10613 733 37 3.84 586 2345 4.13 3.59 108.6
7.3982 1435.57 179.8
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
0.3
Alcohols
Azeotrope X% Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2 2,4-TM P Cyclohexane Benzene Toluene Ethylbenzene Xylenes C, Aromatics Tetra1in Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 112-Propanediol Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 112-EDC 1,l 1-TCA TCE Perk. MCB lcohols
"C
w/w
Reference
None Azeo
9758
Solute f
Reference
3.8 3.7 4.8 3.7 4.5
1x/3/1154 1x/3/1155 21382 2f1383 lx/3/1156
Partition coefficient
Reference
122
9769
None None None 40 130 42 131
9752 9748 9760 9765 9766
3.3 2.6 3.1
1X13/1155 lx/3/1155 1x/3/1156
None None None None None
2056 4063
1.3 1.5 1.o 0.9 0.8 1.o
2d202 2d396 2d47 1 2f/63 2b/173 2fl3 11
0.14 0.50
VU1 17 V2/348
-
-
-
-
-
-
None
9746a
4.4
2d/8
2.7
VU423
1.7
2d/139
1.8 1.3 1.7 1.2
1x/3/1153 lxf311153 2f1375 2fB73
None
None None
6560 8419
None
15 25
1147a
117 126
220 1 9747
Azeotrope
K% Solute Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane TH F
"C
Reference
wlw
Azeo
50
135
Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate None Cellosolve acetate
Solute *p"
Reference
2.1 1.8 1.7
1x/3/1154 1x/311154 2fl380
1.7
1x/3/1154
2.1
1x/3/1154
2.0
2fl37 1
Reference
0.22
P313
0.05 co.01
V31186 P1649
9770
9754
Miscellaneous DMF DMAc DMSO Sulfolane a 2
None
1257
Acetic acid Ani Iine Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
None 15 120
8836 6280
None 46
Partition coefficient
96
9749 464
3.4
1d383
Alcohols
i-Amyl alcohol Alternative names Fusel oil, 3-methyl-l-butanol,
isopentyl alcohol, isobutyl carbinol
Reference codes CAS number UN number Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
123 51 3
Hazchem code EPA code
88 C5Hl2Ol 130 -134 0.810
Cubic expansion coeff (per oC x 103) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
46 365
Lower explosive limit (ppm) Upper explosive limit (ppm)
8000 100 125 15
Vapour concentration @21°C ppm Vapour density (relative to air} Vapour pressure @21°C mmHg POCP
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm) Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C o;oW/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/"C) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
4.2 1.4014
12000 90000
3140 3.06 2.4
2.75
+1.16 2.73
Vapour pressure equation constants (LOglO. mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
1.12 23.8
1.8 15.2 56.5
7.382 1373.8 174.3
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
62
10542 792 47.3 583 4.13 3.59 109.2
Alcohols
azeotrope K%
Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics Tetralin Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-PropanedioI Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,1,l-TCA TCE Perk. MCB Alcohols
"C
W/W
Reference
Solute .p"
Reference
None 7 98 35 120
9845 9869 9881
4.8
1x/3/1151
5 99 None None 10 110 49 126 52 126 None
9882 9834 9821 9852 987 1 9873 9887
3.0
1~/3/1151
None None None
4066 6486
1.2 1.2 1.o
2d201 2d395 2a/548
None None
1.o
2b/170
8328
-
-
-
-
None
422 1
4.1
2d17
1.7
2d/138
None None None None
9816 6562 8420
None None
1149 2995
None 19 116 34 124
232 1 2203 9819
Partition coefficient
Reference
0.50 0.12 0.07
V2/347 V21566 V2/592
0.08
V3/139
-
-
ueotrope :%
"C
Solute
V/W
Reference
Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone
4one
9836
Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane THF
i5
130
Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetate Jone
Solute f
Reference
1.8
1x/3/1151
2.1
1x/3/1151
Partition coefficient
Reference
0.07
V3/185
9883
9842
Miscellaneous DMF DMAc DMSO Sulfolane
cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane AcetonitriIe Furfuraldehyde Phenol Water
$4 Jone
133
3156a 9824
(one
8838
Jone
9822 468
io
95
1.9
1a/382
Alcohols
Cyclohexanol Alternative names Hexalin, cyclohexyl alcohol Reference codes CAS number UN number Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4) Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
108 93 0
Hazchem code EPA code
100 C6Hl2Ol 161 +25 0.949
Cubic expansion
68 300
Lower explosive limit (ppm) Upper explosive limit (ppm)
20000
3500 50
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
1500 3.45 1.14
1
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
coeff (per oC x !03)
Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
0.82 32 52.7 1.465
4.3 11.8 +1.23 0.08 (5) 2.83
Vapour pressure equation constants (Loglo. mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
11.4 1.8 15.0 50.0
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/"C) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
10900 892 50 3.7 625 419 4.35 3.51 103.43
8.35237 2258.560 251.624 8.27876 2110.6 Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
150 0.08
Alcohols
Azeotrope
X% Solute Hydrocarbons n-Pentane +Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes Cg Aromatics Tetralin Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol l-Octanol Ethanediol DEG 1,2-PropanedioI Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,1,l-TCA TCE Perk. MCB 'cohols
"C Reference
Solute T
Reference
None None
11727
5.5 5.7 6.8
1XJ311232 lxJ11272 2fl4 19
None None None
11684 10856 11720
3.4 2.7
1V11272 1XJ11272
WIW
10 40
140
11730 11750
None None None None
-
-
Vane
4257
Vone
9967
Uone
11712
lone
Partition coefficient
Reference
2f1536
1.2 3.9
2d42 1 2d414
1.o
2bl193
-
-
2.3
2dl14
1.6
2131393
-
-
0.02
P3974
Lzeotrope
:% Solute
"C
Reference
VIW
Solute r"
Reference
3.8
2d5 10
0.5
2W395 2fl4 11
1.4
2d511
1.3
2fl4 17
1.4
2fl4 16
Part coefficient
Reference
0.24
VI260
0.05
v31234
.i
Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,CDioxane THF
lone 11357
lone
lone
11745
lone
7543
Esters Me acetate lone Et acetate i-Propyl acetate lone n-Butyl acetate Cellosolve acetate Miscellaneous DMF DMAc DMSO Sulfolane cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile FurfuraIdehyde Phenol Water
11149
rlone
35 13 30
156 183 98
8764 10895 528
2.8 4.5
2bl385 11514
Alcohols
n-Octanol Alternative names Octyl alcohol, heptyl carbinol Reference codes CAS number UN number Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4) Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
I11 87 5
Hazchem code EPA code
130 CgHl8Ol 194 -16 0.827
Cubic expansion coeff (per OCx !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
0.99 27.5 7.5 1.427
81
Lower explosive limit (ppm) Upper explosive limit (ppm)
30000
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
186 4.5 0.14
1.4E-7
0.5
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
0.6 3.15 2.95 (5) 2.95
Vapour pressure equation constants (Log1o. mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100) Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/molfC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
10.4 1.9
6.5422 1139.45 115.9 8.29377 2295.1 Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
54.3 12675 1167 65 2.69 659 6.15 5.21 158.4
Alcohols
~~
~
keotrope :%
Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics Tetralin Alcohols Methanol Ethanol n-Propanol i- Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-0ctano1 Ethanediol DEG l12-Propanediol
"C Reference
VIW
14113 14728
lone lone 194
184
Solute 4"
Reference
2.6 2.8 3.1 3.4
1x/1/401 1x/1/402 1x/1/402 1x/1/402
2.8
2f1542
2.1 2.1 2.5 2.4 2.7 1.4
1x/1/401 1x/1/402 1x/1/402 1x/1/402 1x/1/402 2f541
1.1
1x/3/1371
-
-
Alcohols
Reference
c0.01 c0.01 c0.01 c0.01
P1483 P2286 P2874 P2876
0.76 0.29 0.06
P155 P367 P636
0.02 0.03 0.03 c0.01 c0.01 c0.01
P947 P964 P973 P1266 P1273 P1894
-
-
0.48 0.01
PlOOO P3976
4356
Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,l,l-TCA TCE Perk. MCB
Partition coefficient
1.6 1.o 1.7
1x/1/401 1x/1/401 1x/1/401
c0.01
P87
c0.01
P1377
keotrope I
L
Solute Ketones Acetone MEK MIBK Cyclohexanone NMP Acetophenone
"C
Reference
V/W
37
195
Reference
2.6 2.0
1x/1/401 1x/1/401
13909
Ethers Diethyl ether DIPE Dibutyl ether MTBE 1,4-Dioxane TH F Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetate Miscellaneous DM F DMAc DMSO Sulfolane
1.2
1x/3/1371
2.4
1x/1/401
1.23
2f/527
1.8
CS2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
Solute f
17 Jone
184
195 99
8789 10962 741
Reference
0.24 0.07
P491 P852
0.02
P1839
<0.01
P2743
0.04
P986
0.09
P515
0.82 14.8
P931 P386
0.24 0.02 <0.01 1.66 0.07
P282 P1710 P1438 P932 V3/234
1x/1/401
11200 10754
7.5 Jone 37 LO
Partition coefficient
1x/1/401
0.30
P260
eo.01
P1617
Alcohc
Ethanediol Alternative names Glycol, monoethyleneglycol, !,2-dihydroxyethane,
MEG, not ethyl glycol
Reference codes CAS number UN number
!072!
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
62 C2H6O2 !98 -!3 !.!!5
Cubic expansion coeff (per oC x !03) Surface tension (@20°C dynlcm) Absolute viscosity (@25°C cP) Refractive index (25°C)
0.64
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
!!! 4!3 !.2E-6
Lower explosive limit (ppm) Upper explosive limit (ppm
32000
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
153 2.15 0.12
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
!
60 !25
Aqueous effluent Solubility in water (25°C o;oW/w) Solubility of water in (25°C %wlw) LoglO activated carbon partition LoglO partition in octanollwater (w/w) Biological oxygen demand wlw (days) Theoretical oxygen demand wlw
Hazchem code EPA code
46.5 20 1.429
Total Total !.!6 -!.93 0.!6 (5) !.29
Vapour pressure equation constants (Loglo. mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
14.6 2.31 37.7 79.0
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/molfC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
12524 250 35 7.7 647 2682 2.41 2.25 55.92
8.09083 2088.936 203.454
Kauri butanol value Evaporation time (ether = 1) Evaporation time (BuAc = 1)
1550
Alcohols
Azeotrope
X% Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics Tetralin Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol l-Octanol Ethanediol DEG 1,2-PropanedioI Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,1,l-TCA TCE Perk. MCB Alcohols
"C
Solute .p"
Reference
4434
229.0 384.0 806.0 1170.0 1710.0 1970.0
1x11133 1x11135 1x11/35 1x11136 1x11137 1x11137
None None 6 110 13 133 16 140 160
4255 4239 4285 432 1 4323 4372
148.0 45.7 76.9 86.7 110.0 200
1x11/34 lx/l/34 1x11135 1x/1136 1x11136 1x11137
None None None
1946 4195a
None
4213
WIW
Reference
None 3 98 11 124
4265 4312 4353
23
161
None None None 36 184
-
422 1 4257 4356
-
2.1 4.4 6,6
2.5
2dl6 2fll2
4.1 3.3 2.3
2d/8 2d/7 2dl14
-
1.9 0.9
None
4222
None
4268
None 6 119 6 130
2287 2163 4233
2a162 2c/297 2c/483
2f113 2b112
Partition coafficient
Reference
Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane THF
Solute
Reference
6.2 8.4
1xl3/971 1x/3/97 1
0.44
2f/17
4206 4204a
3.60
2d/3
4258 4261
6.9
2d/l5
1.5
2b/8
0.5
2bP
3.9
2bl16
5.1
2f/l
1.1 0.72
2d/ll ld173
Reference
Solute
52
186
4316
10
140
4354
None None
Esters Me acetate Et acetate i-Propyl acetate None n-Butyl acetate Cellosolve acetate None Miscellaneous DMF DMAc DMSO Sulfolane
Partition coefficient
Reference
cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-N itropropane Acetonitrile Furfuraldehyde Phenol Water
24 59
181 186
4242 4238
None
4215
None 199 78 None
4214 4240 244
Alcohols
Diethylene glycol Alternative names DEG, 2,2-oxydiethanol Reference codes CAS number UN number
111 46 6
Hazchem code EPA code
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
106 C4HlOOJ 245 -8 1.118
Cubic expansion coeff (per oC x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
0.63
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
124 229 6E-7
Lower explosive limit (ppm) Upper explosive limit (ppm)
16000 108000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
25
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
Total Total 1.86 -1.98 0.06 (5) 1.51
Vapour pressure equation constants (Loglo. mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole {D} Dielectric constant {20°C} Polarity {water 100} Thermal information Latent heat {cal/mol} Nett heat of combustion {kcal/gmol) Specific heat {cal/mol!'C} Critical pressure {MN/m2) Critical temperature {K) Latent heat of fusion {cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
2.31 31.7 71.3
48.5 34 1.445
3.68 0.019
12.83 7046.4 463.2
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
15900 567 58.4 4.7 680 4.00 3.57 94.8
Alcohols
lzeotrope (%
Solute
N/W ~
Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics Tetralin Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-Propanediol Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,1,1-TCA TCE Perk. MCB Alcohols
~~
"C Reference
Solute
Reference
64.1 91.5 95.6 139.8 200.3 287.1 195.0 32.1 5.8 12.3 14.9 17.0 25.0
1x/1/139 lx/l/l41 lx/l/142 lx/1/144 1xJ11144 1x/1/145 1x/1/144 lx/l/l40 1x111139 2f/34 1 1x/1/143 1x/1/143 1x/1/144
Partition coefficient
Reference
~
Jone Jone \ZeO \zeo
8520 8531 8545 8547
-
-
0.92 1.3 1.5 1.4 1.9 1.7
1x/3/1079 1x/3/1079 1x/3/1079 1x/3/1080 1x/3/1080 1x/3/1080
2.5
1x/3/1080
-
e
e
~
zeotrope %
;01ute Yetones ketone M EK UlBK 2yclohexanone NMP ketophenone
"C
Reference
I/W
Solute
Reference
3.1 3.7 8.0
1x/3/ 1079 1x/3/1080 1x/3/1081
2.5
1x/3/1080
3.4 5.3
1x/3/107 9 1x/3/1080
Partition coefficient
Reference
8538
lone
Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,bDioxane THF Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetatf Miscellaneous DMF DMAc DMSO Sulfolane cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
10
rlone
210
8518
386
0.6 2.3
2f/339 1a/353
Alcohols
1,2-Propanediol Alternative names Propylene glycol, not propyl glycol Reference codes CAS number UN number
57 55 6
Hazchem code EPA code
Physical properties Molecular weight Empirical formula Boiling point {OC) Freezing point {OC) Specific gravity {20/4)
76 C3H802 187 -60 1.0362
Cubic expansion coeff (per °C x 103) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
0.72
Fire hazards Flash point {closed cup °C) Autoignition temperature {OC) Electrical conductivity
99 421 6.0E-7
Lower explosive limit (ppm) Upper explosive limit (ppm)
26000 125000
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
212 2.52 0.16
Health hazards IDLH {ppm) OES-TWA OES-STEL Odour threshold {ppm)
150
Aqueous effluent Solubility in water {25°C o;oW/w) Solubility of water in {25°C %w/w) LoglO activated carbon partition Loglo partition in octanol/water {w/w) Biological oxygen demand w/w {days) Theoretical oxygen demand w/w
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/molfC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
54 1.431
Total Total 1.43 -1.35
1.68
Vapour pressure equation constants (LOglO1mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
72
8.9545 2692.2 255.2
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
0.01
72.2 12844 436 45 6.1 624 3.28 2.78 73.7
Alcohols
zeotrotn? P/o
Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics TetraI in Alcohols Methanol Ethanol n-Propanol iPropano1 n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-0ctanol Ethanediol DEG 1,2-PyopanedioI Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC l,l,l-TCA TCE Perk. MCB Alcohols
"C
Reference
dw
Jone 2
110
6654 6658
.o
136
6665
-
-
Solute .p"
Reference
120 170 246
1x11168 1x11168 1xl1168
58.9 16.2 26.4
-
Partition coefficient
Reference
1x11168 1x11168 1x11168
1.1 1.4 1.5 1.7
2c/319 2c/491 2d147 2d1137
2.2 1.7
2d1139 2d/138
0.9
2b112
-
e e e
beotrope (% iolute
"C
UM
(etones ketone dEK dlBK $clohexanone JMP ketophenone 3hers Iiethyl ether IIPE Iibutyl ether ATBE 1,4-Dioxane THF
Reference
183
6664
136
6668
Esters Me acetate Et acetate i-Propyl acetate ?-Butyl acetate None %ellosolve acetate None
Solute f
Reference
3.1
2d/135
1.2
lx/3/1013
Partition coefficient
Reference
6655a 6656
~iscellaneous DMF DMAc DMSO Sulfolane 3 2
ketic acid 4niline Nitrobenzene Morpholine vridine &Nitropropane ketonitrile furfuraldehyde Phenol Water
43
None
180
6655
296
Alcohols
Section 3
Glycol ethers
Propylene glycol methyl ether Alternative names I-Methoxy-2-propanol,
PM, PGME
Reference codes CAS number UN number
107982
Hazchem code EPA code
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
90 C4HlOO2 121 -139 0.924
Cubic expansion coeff (per oC x 103) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
32 290 4.5E-7
Lower explosive limit (ppm) Upper explosive limit (ppm)
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
100 300
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) Log1Oactivated carbon partition Log1Opartition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
1.03 27.0 1.9 1.407
11000 3.1 8.3 80
Total Total
0.16 (5) 1.95
Vapour pressure equation constants (Loglo. mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole {D) Dielectric constant {20°C) Polarity {water 100) Thermal information Latent heat {cal/mol) Nett heat of combustion {kcal/gmol) Specific heat {cal/mol/"C) Critical pressure {MN/m2) Critical temperature {K) Latent heat of fusion {cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
14.3 1.67
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
22 0.66
9180 682 49.5 552
97.4
Glycol ethers
hotrope (%
Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics Tetra1in Alcohols Methanol Ethanol n-PropanoI iPropano1 n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-PropanedioI Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,1,l-TCA TCE Perk. MCB ;/ycol ethers
"C Reference
VIW
30
qone
107
8512
6650a
-
Solute f
Reference
Partition coefficient
Reference
ueotrope :%
solute
"C Reference
vlw
Solute
Reference
Partition coefficient
Reference
Yetones ketone WEK MIBK Zyclohexanone VMP ketophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,CDioxane TH F Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetate Miscellaneous DMF DMAc DMSO Sulfolane
cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
55
97
384
Glycol ethers
Ethylene glycol methyl ether Alternative names Methyl cellosolve, EGME, 2-methoxyethanol,
ME, methyl glycol
Reference codes CAS number UN number
109 86 4 1188
Hazchem code EPA code
2(5)
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
76 C3HBO2 125 -85 0.966
Cubic expansion coeff (per oC x 103) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
0.92
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
38 288 1.0E-6
Lower explosive limit (ppm) Upper explosive limit (ppm)
25000 198000
2000 5
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
9300 2.6 7
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
90
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) Log1Oactivated carbon partition Log1Opartition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w Vapour pressure equation constants (LoglQ, mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100) Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/molfC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
10.8 2.0 16.9 66.7
33.0 1.6 1.400
Total Total 1.50 -0.77 0.50 (5) 1.68
7.8498 1793.982 236.877
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
34 0.47
9424 399 43 5.1 565
78.7
Glycol ethers
keotrope Solute Yydrocarbons ?-Pentane ?-Hexane ?-Heptane 7-Octane 7-Nonane ?-Decane 2,2 4-T MP Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics Tetralin rllcohols Methanol Ethanol n-Propanol i- Propanol n-Butanol i-Butanol s-Butanol n-Amyl aAlc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG l12-Propanediol
:% u/w
"C
!3 18 32
Reference
Solute f
Reference
93 110
6592 6614
13.1 4.4 28.4
1x/3/10 12 1x/1/67 1x/3/10 12
123
6628
78
6572 6567 6586 6596 6598
5.7 2.3 3.6 2.9 3.1 3.8
2b/128 2b/127 1x/3/1012 2b/132 2b/134 2d/l3 1
lone lone
1979 3982
1.1
1x/3/10 12
1.7
2c/490
lone lone lone lone Vone
6546 6548 6547 6560 6562
15 qone
!5 51 55
106 117 120
Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 112-EDC 1 1I 1-TCA TCE Perk. MCB Glycol ethers
-
-
24 47
109 119
2178 6566
3.1
2fI99
2.4
2d/120
Partition coefficient
Reference
4zeotrope Y
Solute
"C Reference
Jv/W ~~
Solute
Reference
1.6 2.0
2dlll3 2b/122
1.5
1x/3/10 12
1.7
2bf126
2.4
2dl122
2.2
2fl103
1.7
2d/109
Partition coefficient
Reference
~
Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone
25
114
657 5
Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane THF
58
122
6615
654 1
Yone
Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate 48 Cellosolve acetatc Vone
119
6576 6583
Miscellaneous DMF DMAc DMSO Sulfolane cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
Vone
6550
lone lone 19
6549 6568 294
99
Glycol ethers
Ethylene glycol ethyl ether Alternative names Cellosolve, EGEE, 2-ethoxyethanol, EE, ethyl glycol Reference codes CAS number UN number
110 80 5 1711
Hazchem code EPA code
25
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
90 C4HloO2 135 -70 0.931
Cubic expansion coeff (per °C x 103) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
0.97 28.2 2.5 1.405
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
43 235 9.3E-8
Lower explosive limit (ppm) Upper explosive limit (ppm)
18000 140000
6000 5
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
5300 3.1 4 75
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
50
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in(25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w Vapour pressure equation constants (Log1O,mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100) Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der.Waals' volume Van der Waals' surface area Molar volume
10.0 1.69 5.3 62.7
Total Total 1.95 -0.54 0.67 (5) 1.86
7.81910 1801.90 230
Kauri butanol value Evaporationtime {ether = 1) Evaporationtime {BuAc = 1)
43 0.32
9540 503 52
3.70 3.29 97.41
Glycol ethers
lzeotrope Reference
Solute ?/*
Reference
66 97 116 128
8442 846 1 8478 8493
6.0
2b1295
5.5
2b1302
None 11 109 43 126 50 128
8425 8450 8463 8465
2.0 2.4 2.9
2f/337 2d1299 2fI338
None
4032
None None
8105 8306
None None
8419 8420
-
-
-
-
Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics Tetra1in Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-PropanedioI Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC l,l,l-TCA TCE Perk. MCB Glycol ethers
5 14 38 50
16 32
116 127
2190 8423
2dl396
Partition coefficient
Reference
~
Azeotrope
K% Solute
"C Reference
w/w
Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone
None
Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane THF
50
Solute
Reference
1.o 1.6
2f1332 2f1334
757 1
1.5
2f1335
8434 8400
1.6
2bl294
1.9
11450
Partition coefficient
Reference
8433
127
Esters Me acetate Et acetate None i-Propyl acetate n-Butyl acetate 13 126 Cellosolve acetate None
8479
Miscellaneous DMF DMAc DMSO Sulfolane cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile FuduraIdehyde Phenol Water
Yone 15 Vone Vone 13
8407 119
98
6279 8406 8426 382
Glycol ethers
Ethylene glycol monobutyl ether Alternative names Butyl glycol, butyl cellosolve, EB, 2-butoxyethanol,
EGBE
Reference codes CAS number UN number
I11 76 2 2369
Hazchem code EPA code
2R
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
118 C6H14O2 171 -75 0.902
Cubic expansion coeff (per oC x 103) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
0.92 27.4 6.4 1.417
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
68 214 4.3E-7
Lower explosive limit (ppm) Upper explosive limit (ppm)
11000 106000
700 25
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
922 4.07 0.7 75
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
0.5
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) Log1Oactivated carbon partition Log1Opartition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w Vapour pressure equation constants (Loglo. mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100) Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/moI/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
8.9 1.80 5.3 60.2
2.40 +0.83 0.60 (5) 2.3 7.8448 1988.90 230.00
Kauri butanol value Evaporation time (ether = 1) Evaporation time (BuAc = 1)
119 0.06
10266 778 55 3.2 641 5.05 4.37 131.84
Glycol ethers
ueotrope :%
Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2 2 4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes Cg Aromatics Tetra1in Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol l-Octanol Ethanediol DEG 112-Propanediol
Glycol ethers
Reference
4one
36 140 lone !O 160
8166
lone
11712
-
Jone Jone
Solute f
Reference
3.3
2bl432
1.3
2fl440
1.1
2fi89
-
-
12235 12252
lone
Glycol ethers PGME EGME EEE EGBE Chlorinafed MDC Chloroform Carbon tet. 112-EDC 1 1 1-TCA TCE Perk. MCB
"C
VIW
2218 10521
Partition coefficient
Reference
keotrope (%
Solute
"C Reference
VIW
Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,CDioxane THF
Solute Y
Reference
1.4
2bl430
0.73
11526
Partition coefficient
Reference
12247
lone
Esters Me acetate Et acetate lone i-Propyl acetate n-Butyl acetate Jone Cellosolve acetate lone
7590 11823 11989
Miscellaneous DMF DMAc DMSO Sulfolane cs2
Acetic acid Ani Iine Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
11153 10710
Jone Jone
.2 17 !1
161 186 99
8769 10904 584
Glycol ethers
Chlorinated solvents
Methylene chloride Alternative names Dichloromethane, MDC, methylene dichloride, not methyl chloride Reference codes CAS number UN number
75092 1593
Hazchem code EPA code
2Z UO80
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
85 C1H2CI2 40 -95 1.326
Cubic expansion coeff (per oC x 103) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
1.37 28.1 0.44 1.4211
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
None 605 4.3E-11
Lower explosive limit (ppm) Upper explosive limit (ppm)
130000 220000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
5000 50 300 250
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
495000 2.95 376 0.9
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) Log1Oactivated carbon partition Log1Opartition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
1.30 0.20 2.9 +1.25 O
(5)
0.56
Vapour pressure equation constants (Log1Q, mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
9.7 1.8 9.1 30.9
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
6715 122 24 6.08 510 1436 2.26 1.99 64.50
7.0803 1138.91 231.45 6.91821 1090.1
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
136 1.8 25.0
Chlorinated solvents
beotrow
t% Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TM P Cyclohexane Benzene Toluene Ethylbenzene Xylenes Cg Aromatics Tetralin Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-Propanediol
"C
NlW
Reference
$9 36 lone
1571 1575
33 35 lone
38 40
Solute r"
Reference
2.9
6allOO
4.1
1x/3/923
1.o
1d31923
Partition coefficient
Reference
2d24 2d283 2d416 2fl36
9.28
V4/118
1561
7.9 43.7 4.1 4.1
-
-
-
-
-
1544 1551
Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,1,l-TCA TCE Perk. MCB Chlorinated solvents
Jone
1426
0.7 0.9 1.o 1.2 1.5 0.9
a202 8/62 81263 1xl31923 1x/31923 81256
keotrope (%
"C
Solute f
Reference
Solute
VlW
Reference
Ketones Acetone MEK
lone lone
1553 1564
1.1 0.4
3b127 3 +4/26 1
1566
0.7
3 +41492
0.4
1x/3/92 3 0.09
0.5 0.4
51347 51449
0.8
W265
0.45 0.8
81264 81266
4.2
5164
0.6
81267
1.2 1.2
81258 3a/115
Partition coefficient
Reference
0.39
V41120
3.24
V2136
MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane THF
70
41
Esters 1557
Me acetate lone Et acetate i-Propyl acetate n-Butyt acetate Cellosolve acetate Miscellaneous DMF DMAc DMSO Sulfolane cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
55
36
1546
lone
39
1170
38
208
1324.0
111
Chlorinated solvents
Chloroform Alternative names Trichloromethane Reference codes CAS number UN number
67 66 3 1888
Hazchem code EPA code
2Z UO44
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
119 C1HICI3 61 -23 1.480
Cubic expansion coeff (per oC x 103) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
1.29 27.16 0.57 1.444
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
None None <1.0E-10
Lower explosive limit (ppm) Upper explosive limit (ppm)
None None
1000 2
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
300
Aqueous effluent Solubility in water (25°C %wlw) Solubility of water in (25°C %wlw) Log1Oactivated carbon partition Log1Opartition in octanollwater (wlw) Biological oxygen demand wlw (days) Theoretical oxygen demand wlw
0.82 0.072 3.6 +1.97 0.02 (5) 1.35
Vapour pressure equation constants (LoglOt mmHg) Antoine equation A B C Cox chart A B
6.95465 1170.966 226.232 6.97909 1192.6
Solvent properties Solubility parameter Dipole (D} Dielectric constant (20°C} Polarity (water 100}
9.3 1.1 4.8 25.9
Thermal information Latent heat (cal/mol} Nett heat of combustion (kcal/gmol} Specific heat (cal/mol/OC} Critical pressure (MN/m2} Critical temperature (K} Latent heat of fusion (cal/mol} Van der Waals' volume Van der Waals' surface area Molar volume
70.21 91 27 2.38 536 2097 2.87 2.41 80.41
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
286000 4.13 169 1.0
1.9
Chlorinated solvents
AzeotroDe
X% Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics Tetra1in Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol iButa no1 s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol l-Octanol Ethanediol DEG 1,2-Propanediol
"C
WIW
Reference
Solute f'
Reference
None 83 60 None
1482 1495 1500
2.1 1.9 1.4 2.1
1x/3/992 6al426 6bl77 1x/3/922
None None None
1490 1486 1498
0.86 0.75
1x/1/4 71352
87 53 93 59 None 61 96
1430 1442 1454 1453
7.4 4.3
2d23 2d285
6.6 2.7
2dl40 2bl136
None None
1475 1472
Partition coefficient
Reference
3.5 1.07 0.24 0.34 0.05 0.07 0.08
P160 P373 P640 P65 1 P952 P964 P976
-
-
Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,1,1-TCA TCE Perk. MCB
None
1426
0.8
81202
-
-
-
-
None None
1086 1435
None None
1431 1484
1.1 1.1 1.o 1.1 1.2 0.8
8/56 1x/3/92 1 1x/3/92 1 1x/3/92 1 812 15 81244
Chlorinafed solvents
Azeotrope Solute
X% w/w
"C
Reference
Solute
Reference
Partition coefficient
Reference
~
Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane THF
78 64 17 80 None
1443 1460 1492
0.06
3bl426
1474 1496 1501a
0.4 0.5 0.4
3+4/486 3+4/537 3 4/59 1
None 66 73
1465 1464
0.3 0.25
3 +4/44 1 1x/1/4
1448 1466
0.43 0.23
51341 51443
1493
0.41
51574
Miscellaneous DMF DMAc DMSO Su lfolane Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Fudura ldehyde Phenol Water
3 4/90 3+4/260 3 +4/343
None 36 71 None
Esters Me acetate 77 65 Et acetate 28 78 i-Propyl acetate n-Butyl acetate None Cellosolve acetate
cs2
+
0.5 0.4 0.3
None None
1169 1437
None
1485
None
1480a
None None
1433 1480
97
56
P493
0.03
V41115
0.32
v41113
1.04 0.007
V2118 P1714
0.006
P1102
0.07
P1627
+
0.18
81229
1.3 4.2
812 13 5162
0.35
81240
1.2 10.7
0.03
812 17 3+4/36
207
Chlorinated solvents
Carbon tetrachloride Alternative names Carbon tet., CTET, tetrachloromethane Reference codes CAS number UN number
56 23 5 1846
Hazchem code EPA code
2Z U211
Physical properties Molecular weight Empirical formula 8oiling point (OC) Freezing point (OC) Specific gravity (20/4)
154 ClCI4 76 -23 1.58
Cubic expansion coeff (per oC x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
1.27 27 0.97 1.459
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
None None 4.0E-18
Lower explosive limit (ppm) Upper explosive limit (ppm)
None None
300 2
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
96
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
0.077 0.008 4.3 +2.64 0 (5) 0.21
Vapour pressure equation constants (Log10t mmHg) Antoine Equation A B C Cox chart A B
6.84083 1210.595 229.664 7.02433 1267.9
Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
8.6 0 2.24 5.2
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
7238 62 32 4.56 556 784 3.39 2.91 97.5
Chlorinated solvents
Kauri butanol value Evaporationtime (ether = 1) EvaporationTime (BuAc = 1)
150900 5.34 99.6
1.8
Azeotrope
K% Solute Hydrocarbons n-Pentane n- Hexane n-Heptane n-Octane n-Nonane n- Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes Cg Aromatics Tetra1in Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol D EG lI2-Propanediol
"C
Chlorinated solvents
Reference
2d276 2d509
4.76
P382
2b136
2.45 0.32
Val0
0.05
P1269
-
-
Reference
None None None
1162 1167 1168a
1.3 1.3 1.o
6a/403 6b/67 6b/234
None None None None None None
1168b 1159 1154 1166 1167a 1167c
1.4 1.1 1.1 1.o 0.9 0.9
6bl285 6d142 717 71332 71464 71480
1090 1105 1116 1115 1133 1137 1134 1147a 1149
10.3 20.5 14.5 6.7 9.5
79 54 92 52 98 95 92 None None
56 65 73 67 77 76 75
Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC l,l,l-TCA TCE Perk. MCB
Partition coefficient
wlw
1086
Vone 30 be0 Vone Vone Vone
75
1098 1093 1091 1152
Solute f
5.4
Reference
2d1
2fl109 2f/2 17
4.9
2f199
1.1 1.o
8/63 8/55
-
1.5 1.2 0.7 1.o 1.4
P958
-
8/96 8/82 8/80 8/78 81164
AzeotroDe X%
Solute Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,CDioxane THF Esters Me acetate Et acetate i-Propyl acetate v-Butyl acetate Cellosolve acetatc
"C Reference
WIW
12 71
56 74
1108 1121
None None
1136 1163
None
1124
None 57 75 None None
1110 1125 1145 1161
Miscellaneous DMF DMAc DMSO Sulfolane 2S2
4cetic acid Wine Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
None 98 76 None None
1153
None 83 65 None None 96 66
1114 1095 1140 1155 205
1085 1099
Solute f
Reference
+ +
Partition coefficient
Reference
0.26
P502
0.06
V41107
0.05
P519
2.3 1.8
3 4/80 3 41259
0.9
3bl495
1.1
3+4/529
1.6 0.9
3 41440 3+4/429
1.6 1.4
51339 51436
0.8
51573
5.4
8/117
5.9
V41106
18.5
81107
3.8
P387
1.2 12.2 6.0 0.7
8/76 5/59 81174 81168
6.0 0.07
v2112 P1720
2.0 3.2 9.6 3.8 3.4
81141 81120 8/86 3+4/35 2bl355
0.04 0.31
P1652
+
Chlorinated solvents
1,2-Dichloroethane Alternative names Ethylene dichloride, EDC Reference codes CAS number UN number
107 06 2 1184
Hazchem code EPA code
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
99 C2H4CI2 83.5 -36 1.253
Cubic expansion coeff (per oC x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
13 413 4E-11
Lower explosive limit (ppm) Upper explosive limit (ppm)
62000 169000
1000 5
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
94000 3.4 71
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
400
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) Log1Oactivated carbon partition Log1Opartition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
0.81 0.15 3.8 3.6 0.002 (5) 0.97
Vapour pressure equation constants (Loglo. mmHg) Antoine equation A B C Cox chart A B
7.02530 1271.254 222.927 7.04532 1303.5
Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
9.8 1.8 10.45 32.7
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
7623 269 31 5.38 563 2091 2.93 2.53 78.87
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
2YE UO77
1.16 32.2 0.9 1.444
2.7
Chlorinated solvents
Azeotrope
K% Solute Hydrocarbons n-Pentane n-Hexane n-Heptane +Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics Tetralin Alcohols Methanol Ethanol n-Propanol iPropanol n-Butanol i-Butanol s-Butanol n-Amyl alc. /-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-Propanediol
"C
b41W
Reference
None 76 81
3003 3009
50 74 20 80 None
3001 2999 3006
58 53 Vone 57 \one 34 38
1930 2964 2971 2970 2984 2988 2985
61 71 73 83 82
Vone
2995
qone
1435 1098
Solute f
Reference
4.8 3.6 3.4
1x/1/18 1x/1/19 6c/444
3.4 3.1 1.1 1.1 1.o 1.3
lxll/l9 6all59 71142 71380 71466 71490
11.2 4.9 5.1 4.9 3.2 4.2 2.7 3.6
2d44 2a1299 2d520 1x/1/18 2b l l 3 7 2b1272 2f1220 2fl375
1.0 1.o 1.8
a263 1x/3/957 1x/3/957
Partition coefficient
Reference
7.9
V2183
1.2
V21207
-
-
Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. l12-EDC 1 1,l-TCA TCE Perk. MCB Chlorinated solvents
!O 57
75
82
-
2281
-
1.6 1.4 1.7
-
a363 81351 a340
keotrope (%
Solute ~~
"C
ulw
Reference
Solute
Reference
lone
2966 2977
0.8 0.8 0.8
3+4/144 3bl271 3bl519
Partition coefficient
Reference
<0.01
P2746
0.98
V4/180
1.61 <0.01
vu202 P1721
0.14
V4118 1
~~
Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,440xane TH F Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetatc
beo
Jone lone
2987 3004
lone
2979
0.9 0.7
3+4/447 W31957
Jone lone
2980 2992
0.8
lx/l/l8
lone
2961
2.6 4.4
lx/lll7 5/74
0.9
1x/1/18
1.4 1.1
8/364 3alll9
Miscellaneous DMF DMAc DMSO Sulfolane
cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
il
11
79 72
2757 227
Chlorinated solvents
1,1,1-Tricloroethane Alternative names Methyl chloroform, TCA, chlorothene, M.C., not 1,1,2-trichloroethane Reference codes CAS number UN number
71 55 6 2831
Hazchem code EPA code
2Z U226
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
133 C2H3CI3 74 -30 1.338
Cubic expansion coeff (per oC x 103) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
1.3 30 0.65 1.438
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
None 537 7.3E-9
Lower explosive limit (ppm) Upper explosive limit (ppm)
65000 155000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
350 450 300
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
154700 4.62 101.8 0.1
Aqueous effluent Solubility in water (25°C o;oW/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
0.13 0.03 4.3 4.0 0.48
Vapour pressure equation constants (Log1o. mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
7.7 1.7 7.25 17.0
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
7780 233 32 4.4 550 651.7 3.54 3.03 100.4
6.90633 1211.31 226.816 7.01846 1257.7
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
124 2.6 6.0
Chlorinated solvents
4zeotrope
t% Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes Cg Aromatics Tetra1in Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-PropanedioI
"C Reference
N/W
29
78
67
56
Solute f
2730b
Reference
1.3
6d473
1.o
7112 1
1.6
2f/123
24.8
2fI373
Partition coefficient
Reference
0.11
V4/158
-
-
1923
Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,1,l-TCA TCE Perk. MCB Chlorinated solvents
Leo 4one
2729
-
1.o 1.1 1.2
-
1.o
1x/3/948 8/82 1x/3/948
-
1x/3/948
~~
keotrope
K% Solute
"C
Reference
NlW
Solute
Reference
Partition coefficient
Reference
0.04
V41160
0.04
V41159
Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane THF Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetate Miscellaneous DMF DMAc DMSO Sulfolane cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile FurfuraIdehyde Phenol Water
96
65
Chlorinated solvents
Trichloroethylene Alternative names 1 ,2,2-trichloroethylene,
trike, TCE, triclene, trilane, trichloroethene, not trichlorethane
Reference codes CAS number UN number
7901 1710
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
Hazchem code EPA code
2Z U228
131 C2HlCI3 87 -86 1.464
Cubic expansion coeff (per oC x 103) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
1.17 29.5 0.57 1.475
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
32* 420 8E-12
Lower explosive limit (ppm) Upper explosive limit (ppm)
80000 105000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
500 100 150 200
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
80260
6
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C o;oW/w) Log1Oactivated carbon partition Loglo partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/OC) Critical pressure {MN/m2) Critical temperature (K) Latent heat of fusion (car/mol) Van der Waals' volume Van der Waals' surface area Molar volume
56.5 6.6
0.11 0.033 5.0 +2.29 0.61
Vapour pressure equation constants (Loglo. mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
4.55
8.0 0.9 3.42 16.0
6.51827 1018.603 192.731
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
130 3.1 4.9
7467 206 30 4.90 571 3.31 2.86 90.01
*Very resistant to flashing. Chlorinated solvents
Azeotrope Solute
X% wlw
Reference
Solute T
Reference
None None None
1482 2330 2335
1.5
6a1463
17 80 None
2328 2326
1.3 1.o 0.8
6dl55 71114 71370
62 71 83 70 97 91 85
1915 2286 2296 2295 2306 2309 2307
6.9 7.3 2.7 3.1 3.7
2a140 2al295 2 d 5 18 2dl43 2fl121
3.8
2fl2 17
1.1 1.o 1.4 1.o
1xl31943 1xl31943 813 5 1 1xl31943
Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TM P Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics TetraIin Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-PropanedioI
"C
59 72 82 75 87 85 84
None
232 1
None
2287
None 33 82
1093 2281
-
-
Partition coefficient
Reference
8.9 2.03 0.24
V2/79 CEH V41152
0.08
v41154
-
-
Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,1,l-TCA TCE Perk. MCB
Chlorinated solvents
-
-
1.6
813 2 6
Azeotrope Solute Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxa ne THF
X% wlw
"C Reference
Solute f
Reference
None None
2289 2299
1.o 1.3 1.1
3b15 1 3 +4/264 3bl517
None
2331
None
2301
Esters Me acetate None Et acetate i-Propyl acetate None n-Butyl acetate Cellosolve acetatc
Partition coefficient
Reference
0.05
v21157
0.05
V41151
1.o
51454
0.6
51575
2282
4.7
5172
2.7
v21151
2280
5.5 3.1
81349 3+4137
0.03
V4l155
2302 2317
Miscellaneous DMF DMAc DMSO Sulfolane
cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
96
71 94
86
75 73
218
Chlorinated solvents
Perchloroethylene Alternative names Tetrachloroethylene, perk, tetrachloroethene Reference codes CAS number UN number
127 18 4 1897
Hazchem code EPA code
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
166 C2CI4 122 -36 1.63
Cubic expansioncoeff (per oC x !03) Surfacetension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractiveindex (25°C)
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
None None 5.5E-4
Lower explosive limit (ppm) Upper explosive limit (ppm)
None None
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
400 50 150 300
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
20600 5.8 15.4 0.5
Aqueous effluent Solubility in water (25°C o;oW/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
1.02 32 0.88 1.504
0.015 0.0105 5.4 +2.60 0.06 (5) 0.39
Vapour pressure equation constants (LoglOt mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
2Z U210
4.5 0 2.3
7.62930 1803.96 258.976
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
90 6.0 2.6
8316 162 35 4.48 613 3.89 3.40 101.84
Chlorinated
solvents
Azeotrope Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes C, Aromatics Tetralin Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-Propanediol Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,,l-TCA l TCE Perk. MCB Chlorinated solvents
X% w/w
OC
Reference
2217a
None 92
120
6a1453
1.3
71112
Reference
2.6
CEH
21.7
CEH
-
-
2227
36 37 30 52 71 60 43 85 81
64 77 82 94 109 103 97 117 116
1914 2162 2176 2177 2186 2189 2187 2201 2203
94
119
2163
95 76 54 None
121 110 116
2205 2178 2190 2218
-
1.5
Partition coefficient
2220 2225 1167c
None None None
None None
Reference
1431 1091
-
16.4 5.4
2af37 2~1285
5.9 3.8
2d/42 2d/l55
3.3
2d1240
1.1 1.2 1.o 2.0
8/2 56 812 15
1.1
-
8/78 81340 W327
-
Azeotrope
K% Solute Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane THF
"C
wlw
Reference
Solute .p"
Reference
Part coefficient
Reference
None
2168
2.6
3bl49
4.2
CEH
0.08
v41149
48
114
2209
2181
None
Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate 79 Cellosolve acetate
120
2210
51
107
2158
52
113
2192
2.0
81346
2191
4.3
34117
Miscellaneous DMF DMAc DMSO Sulfolane 1.4
cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
Vone
34
88
8.316 7.25
v21147
0.05
v41150
217
.
~~
Chlor sted solvents
Monochlorobenzene Alternative names Chlorobenzene, MCB, phenyl chloride Reference codes CAS number UN number
108 90 7 1134
Hazchem code EPA code
2Y UO37
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
113 C6H5Cil 132 -46 1.106
Cubic expansion coeff (per oC x 103) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
0.98 33 0.8 1.523
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
29 640 7E-11
Lower explosive limit (ppm) Upper explosive limit (ppm)
13000 71000
2400 50
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour Pressure @21°C mmHg POCP
12650 3.9 9.5
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
1
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) Log1Oactivated carbon partition Log1Opartition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
0.049 0.033 4.9 +2.84 0.03 (5) 2.05
Vapour pressure equation constants (Log10t mmHg) Antoine equation A B C Cox chart A B
7.17294 1549.200 229.260 7.18576 1558.4
Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
9.5 1.3 5.62 18.8
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
8814 754 35 4.52 632 2305 3.81 2.84 102.24
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
90 10.0
Chlorinated solvents
Azeotrope X% Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane &Decane 2 2 4-T MP Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics Tetrali n Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-PropanedioI
Chlorinated MDC Chloroform Carbon tet. 112-EDC 1 1,l-TCA TCE Perk. MCB
Reference
Solute Y
Reference
None None None
10519 10531 10536
1.6 1.8 2.2
6d529 6bll19 lX13I1175
1.5
6b1392
None None None None None
10515 10509 10524 10532 10534
1.3 1.o 1.o 1.o 0.9
6aI202 71243 714 16 71469 71508
None None 20 None 44 37 None 75 66 None
2063 4070 6489 6273 8133 833 1 8230 9747 9819
4.9 4.2 3.0 3.4 2.5 2.8 2.8
2d204 2d397 2d552 2d164 2b175 2dl357 2 b1258
2.6
2b1395
3.4
2d1120
94
Glycol ethers PGME EGME EEE EGBE
"C
wlw
97 115 107 126 124 130
4233
None 53 119 68 127 None
9960 6566 8423 10521
1484 1152
None None
-
Chlorinated solvents
-
1.2 1.2
81244 81166
-
-
Partition coefficient
Reference
0.16
P3988
-
-
keotrope (%
Solute Ketones Acetone MEK MIBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane THF
"C Reference
N/W
5372
\one \one \one \one
10512
None
10537
Esters Me acetate None Et acetate i-Propyl acetate None n-Butyl acetate Cellosolve acetate Miscellaneous DMF DMAc DMSO Sulfolane CS2 Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
7578
Reference
1.3 1.3 1.1
3+41192 3 +4/283 3131543
0.9
1x/311175
1.2 1.4
51374 51492
1.8 1.1
a1527 1x/3/1175
Partition coefficient
Reference
0.17 0.08
vu477 V3122
3.7
CEH
0.08
V31226
0.32 0.01
VU176 V41255
10516
41 115 None None
None None None 72
Solute f
90
3160 10511 10508
2794a 8758 10510 484
3.3
81381
Chlorinafed solvents
Section 5
Ketones
Acetone Alternative names Propan-2-one, dimethyl ketone Reference codes CAS number UN number
67 64 1 1090
Hazchemcode EPAcode
2YE UOO2
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
58 C3H60l 56 -95 0.790
Cubic expansion coeff (per oC x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
1.4 23.3 0.33 1.357
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
-18 465 5E-9
Lower explosive limit (ppm) Upper explosive limit (ppm)
26000 128000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
20000 750 1500 300
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
342800 2.0 194 17.8
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) Loglo activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
Total Total 1.74 -0.24
1.22
(5)
2.21
Vapour pressure equation constants (Loglo. mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
10.0 2.9 20.6 35.5
Thermal information Latent heat (cal/mol) Nett heat of combustion {kcal/gmol) Specific heat (cal/mol/OC) Critical pressure {MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
7076 395 30 4.8 508 1358 2.57 2.34 73.4
7.11714 1210.596 229.664 7.18990 1232.4
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
1.8 5.6
Ketones
Azeotrope Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TM P Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics Tetralin Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-PropanedioI Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC l,l, 1-TCA TCE Perk. MCB Ketones
X% w/w
"C
21 59 90 None None None None 67 None None None None None
32 50 56
Reference
Solute ?p"
Reference
5368 5385 5393 5395
5.8 5.1 5.5 8.4 6.2 6.7 8.2 4.3 1.4 1.6 2.1 2.6 1.6
3+4/190 3+4/225 3+4/242 3b/224 3b1236 3 +4/247 3b/225 3 412 13 3 +4/195 3+4/236 3b1217 3b/222 3b1233
1.8 1.7
2a/68 2a/32 1
2.4 1.6 1.2
2 b/43 2 b/l40 2f/304
None
4.6
2d/510
None
2.9 1.o
2dIll3 2f1332
5396 53
5378 5374 539 1
88 55 None None None None None
1963 3965 5320 5319 5344 5347
+
None 22 64 89 56 None
1553 1443 1108 2966
0.7 0.6 2.3 1.0
3 b/2 7 3 4/90 3 4/80 3+4/144
None None None
2289 2168 5372
2.7 3.7 1.6
3b149
+
+
3 b/5 1 3+4/192
Partition coefficient
Referenc
Azeotrope
K% Solute
Ketones Acetone MEK MIBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,CDioxane TH F Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetate Miscellaneous DMF DMAc DMSO Sulfolane cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
"C
N/W
Reference
Solute T
Reference
-
-
-
-
None None
5330 5382
0.9 1.1
3+4/173 3b1196
None 61 54
5346 5386
1.4
3+4/177
None
5333
1.4
1x/3/991
50 55 None None None
5310 5334 5365 5383
1.3 1.2
3+4/159 3+4/176
1.1
3bl197
None
3.1
3 41164
None
1.2
3 b/80
Partition coefficient
Reference
+
33 39 None None
1194 3101
3.6 1.4 0.9
3+4/132 3+4/148 3b/183
None
5353
2.1
3+4/181
None
2762
1.o
3+4/143
None None
5375 269
5.3
1x/3/993
Ketones
Methyl ethyl ketone Alternative names MEK, butan-2-one Reference codes CAS number UN number
78 93 3 1193
Hazchem code EPA code
2YE U159
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
72 C4H8Ql 80 -87 0.805
Cubic expansion coeff (per oC x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
1.3 24.6 0.41 1.377
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
-6 485 3.6E-9
Lower explosive limit (ppm) Upper explosive limit (ppm)
18000 100000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
3000 200 300 30
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
112000 2.50 75.3 42.3
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
26 12.0 2.25 +0.29 2.14 (5) 2.44
Vapour pressure equation constants (Loglo. mmHg) Antoine equation A B C Cox chart A B
7.06356 1261.340 221.969 7.22242 1345.9
Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
9.3 2.8 18.5 32.7
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
7848 540 38 4.16 535 1790 3.25 2.88 89.44
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
2.5 4.6
Ketones
Azeotrope Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes Cg Aromatics Tetralin Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-PropanedioI Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,1,l-TCA TCE Perk. MCB Ketones
X% wlw
"C
29 70
64 77
None None 40 72 45 78 None None
30 64 61 74 None 68 78 None None None
Reference
Solute
Reference
7376 7384
3.4 2.9 3.2 6.0
1x/3/1044 3+4/302 3+4/311 3 +4/3 17
7374 7369 7382
5.0 4.3 3.3 1.2 1.6 1.9 1.3
3bl396 3bI395 3 +4/297 3+4/284 3+4/308 3 +4/3 16 3bl382
2.0 2.3 1.6 1.6 0.9
2al133 2al343 2c/496 2bl54 2fl144
1.3
2bl239
1993 4005 6445 6335 7357 7360 7358
None
1.8 1.6 2.4
2b/122 2fl334 2b/430
+
None 93 80 29 74 24
1564 1460 1121 2977
0.6 0.5 1.5 0.7
3 41/26 1 3+4/260 3 412 59 3bl271
None
2299
1.1 2.5 1.5
3+4/264 3bl265 3 +4/283
None
+
Partition coefficient
Reference
0.12
CEH
0.25
v31225
0.22
v3117
8.16
V214 18
0.08
CEH
Leotrope Reference
Solute Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane THF
lone
Vone
Esters Vone Me acetate 12 77 Et acetate i-Propyl acetate Vone n-Butyl acetate Cellosolve acetatf
5330
cs2
16 46 None
0.9
Reference
+
3 41173
-
-
1.o
3+4/300
1.5
3bl357
7344
1.2
1x/3/1044
5519 7345 7366
1.o 1.1
3 412 7 1 3+41278
1.4
3bJ289
3.0 1.6
1x/1/97 3 41269
1.5
3b1316
1.1
1x/1/98
1.2
3b1268
0.1 6.9
2b1358 1x/1/99
-
Miscellaneous DMF DMAc DMSO Sulfolane Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
Solute g
1216 3117
None 73
6272
None B9 73
7370 338
Partition coefficient
Reference
0.30
V412 15
0.21
P326
-
-
+
+
Ketones
Methyl isobutyl ketone Alternative names 4-Methyl-2-pentanone,
MIBK
Reference codes CAS number UN number
108101 1245
Hazchem code EPA code
U161
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
100 C6Hl2Ol 116 -84 0.801
Cubic expansion coeff (per oC x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
0.94 23.6 0.61 1.394
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
13 459 5E-8
Lower explosive limit (ppm) Upper explosive limit (ppm)
14000 75000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
50 8
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition Loglo partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
21700 3.47 16.5 63.3
1.7 1.9 3.05
2.06 2.2
Vapourpressure equation constants (Log1o.mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
8.4 2.81 13.1 27
6.67272 1168.408 191.944 7.27155 1519.2 Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
5.6 1.4
8500 672 46 3.27 571.5 4.60 3.95 125.8
Ketones
Azeotrope
K% Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes Cg Aromatics Tetralin Alcohols Methanol Ethanol n-Propanol i- Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol l-Octanol Ethanediol DEG 1,2-Propanediol Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,l ,l-TCA TCE Perk. MCB Ketones
"C
Reference
w/w
13 65
Solute r"
Reference
2.3 2.5 2.1 2.0
1x/3/1233 1x/1/273 3bl550 1VU273
1.9 1.2 1.o 1.1
1x/1/373 3 +4/354 3 4/35 1 3 +4/356
1.6
3bl553
98 113
11801 11805
None None 3 111 None None
11685 10857 11799 11802
None None
2084 4101
2.1 2.5
2al248 2c/423
None 70 114 9 108
6386 8152 8343
1.5 2.5
2b/96 2b/193
30.2
2fl380
None
9836
75 114 None
6575 8433
None
1492
52 Yone
114
2209
Partition coefficient
Reference
8.65
V2l430
+
0.5 1.1 0.8 0.9 1.1
3+4/343 1x/3/1233 3bl519 1x/3/1233 3bl517
1.o
3bI543
~
rzeotrope :%
olute
etones cetone 1 EK 1IBK yclohexanone IMP cetophenone
"C
VIW
Reference
(one
5382
Solute f 1.2
1.1
-
-
Reference 1x/1/273 3 +41300
-
Partition coefficient
0.12
-
Reference V21485
-
then liethyl ether IIPE libutyl ether ITBE ,4-Dioxane 'HF
1.2
3bl523
1.9
3bl527
1272 3175
1.8
3+4/345
8849
1.o
3bl53 1
sten Ae acetate :t acetate .Propyl acetate t-Butyl acetate :ellosolve acetatc Aiscellaneous )MF )MAC IMSO iulfolane :Sp \cetic acid hiline rlitrobenzene dorpholine vridine !-Nitropropane ketonitrile %rFuraldehyde 'henol Nater
None None
40
76
115
88
537
1.4
3al126
10.6
1bl337
0.32
V21285
0.08 0.03 co.01
V21183 v31193 v31295
Ketones
Cyclohexanone Alternative names Cyclohexyl ketone, sextone Reference codes CAS number UN number
108941 1915
Hazchem code EPA code
3Y UO57
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
98 C6HIOOl 156 -32 0.948
Cubic expansion coeff (per oC x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
0.94
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
43 420 5E-18
Lower explosive limit (ppm) Upper explosive limit (ppm)
11000 94000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
5000 25 100 1
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
3963 3.40 3.1
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) Log1Oactivated carbon partition Log1Opartition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
2.3 8.0 3.0 +0.81 1.23 2.61
Vapour pressure equation constants (Log1o. mmHg) Antoine equation A B C Cox chart A B
7.47050 1832.200 244.200 7.32768 1716.5
Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100) Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
9.9 3.1 18.2 28
Kauri butanol value Evaporation time (ether = 1) Evaporation time (BuAc = 1)
34.5 2.2 1.448
41 0.25
9016 788 48 3.8 629 4.14 3.34 104.2
Ketones
Leotrope (%
Solute Hydrocarbons +Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TM P Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics Tetralin Alcohols Methanol Ethanol n-Propano1 i- Propano1 n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol l-Octanol Ethanediol DEG 1,2-PropanedioI
u/w
"C Reference
Uone Uone
qone
11367
Solute
Reference
3.7 4.1 4.4 4.9
1x/ 11257 1x/1/258 3b/509 1x/3/12 10
1.6 0.9
1.o
3b/505 3b/503 3+4/339
1.5
3bl511
2.1
1x/3/1210
Ketones
0.4 0.3 1.2
(one
Reference
3.4
V2/428
0.03
P3981
11357
Glycol ethers .PGME EGME EEE EGBE Chlorinated M DC Chloroform Carbon tet. 1,2-EDC 1,1,l-TCA TCE Perk. MCB
Partition coefficient
10512
1x/1/256 1x/1/256 3b/495
~
zeotrope %
Solute
"C
I/W
Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone
Reference
-
Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane THF Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetatc Miscellaneous DMF DMAc DMSO Sulfolane cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
rlone
11144
rlone !8 185 96 $3
8762 10889 506
Solute f
Reference
1.3 1.o
1x/1/256 1x/3/1210
-
-
2.5
3b/506
1.o
1x/3/12 10
1.3
1x/1/256
1.8
3b/500
1.9
1x/1/356
1.4
1x/1/256
0.1 5.93
2b/368 1/5 11
Partition coefficient
Reference
Ketones
n-Methyl-2-pyrrolidone Alternative names M-pyrol, NMR 1-methyl pyrrolidone Reference codes CAS number UN number
872 50 4
Hazchem code EPA code
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
99 CsHgN1Ol 202 -24 1.03
Cubic expansion coeff (per oC x 103] Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
0.9 40.7 1.8 1.468
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
95 287 2E-8
Lower explosive limit (ppm) Upper explosive limit (ppm)
21800 122400
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
395 3.44 0.3
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
100
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
Total Total
1.1 (5) 2.18
Vapour pressure equation constants (LoglOt mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water lOO) Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/moI/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
11.0 4.1 32.2 36
8.27890 2570.30 273.150
Kauri butanol value Evaporation time (ether = 1) Evaporation time (BuAc = 1)
0.04
12600 667 40 722 6207 3.98 3.20 96.1
Ketones
4zeotrope (%
Solute
N/W
"C Reference
Solute Ip" ~
Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TM P Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics TetraIin Alcohols Methanol Ethanol n-Propanol i- Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol l-Octanol Ethanediol DEG 1,2-PropanedioI
Reference
~~
10.2 11.3 10.5 12.1 13.9 15.9 14.4 5.9 1.2 1.5 1.8 1.8 2.0
lx/1/17 1 1x/1/174 lx/l/176 1x/1/176 1x/1/177 1x/1/177 1x/1/177 1x/1/173 1x/1/172 1x/1/175 1x/1/176 lx/l/1125 3b/463
0.5 0.6 0.7 0.75 0.7 0.7
1x/1/169 1x/1/169 1x/3/1118 lx/l/169 1x/3/1119 1x/3/1119
0.6
2f/4 11
0.05
2f/17
0.4 0.4 2.3
1x/3/1117 1x/3/1117 lx/3/1117
Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,1,l-TCA TCE Perk. MCB Ketones
Partition coefficient
Reference
I rzeotrope :%
Solute
VIW
Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone
-
"C
Reference
-
Solute Y
Reference
1.3 1.4
1x/11169 1x/11170
-
-
1.2
1x/3/1119
1.6 1.9
1x/1/169 1x/311119
1.15
la1379
Ethers Diethyl ether DIPE Dibutyl ether MTBE 1,CDioxane TH F Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetate
Partition coefficient
Reference
Miscellaneous DMF DMAc DMSO Sulfolane cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
Vone
416a
I
Ketones
Acetophenone Alternative names Acetylbenzene, methyl phenyl ketone Reference codes CAS number UN number
98 86 2
Hazchem code EPA code
Physical properties Molecular weight Empirical formula Boiling point {OC) Freezing point {OC) Specific gravity {20/4)
120 C8H80l 202 + 19.6 1.024
Cubic expansion coeff (per °C x 103) Surface tension (@30°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
Fire hazards Flash point {closed cup °C) Autoignition temperature {OC) Electrical conductivity
82 570 3E-9
Lower explosive limit (ppm) Upper explosive limit (ppm)
1.0
Vapour concentration @21°C ppm Vapour density {relative to air) Vapour pressure @21°C mmHg POCP
Health hazards IDLH {ppm) OES-TWA OES-STEL Odour threshold {ppm)
10
Aqueous effluent Solubility in water {25°C %w!w) Solubility of water in {25°C %w!w) LoglO activated carbon partition LoglO partition in octanol/water {w!w) Biological oxygen demand w/w {days) Theoretical oxygen demand w/w
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
461 4.17 0.35
0.55 1.70 3.84
2.53
Vapour pressure equation constants (LoglOt mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
0.84 12 1.74 1.532
2.9 17.4 30.6
7.2273 1774.6 206.3
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
0.03
10032 949 54 3.8 428 4.69 3.61 117.4
Ketones
hotrope (%
Solute
"C
M/W
Reference
Wydrocarbons v-Pentane v - Hexane v- Heptane a-Octane n-Nonane n-Decane 2,2,4-TM P Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics Tetra1in Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-Propanediol
None
13 195 48 186 None 184
Solute ?p"
Reference
5.4 6.4 6.0 7.6 7.3
1x/1/363 1x/1/363 1x/1/363 lx/3/1345 1x/1/364
4.7 1.6 1.3 1.7 1.8
1x/1/363 1x/1/363 1x/3/1345 1x/1/363 1x/1/364
3.5 3.3
1x/1/362 1x/3/1345
1.1
2b/251
0.6 0.6 1.7
1x/1/362 1x/1/362 1x/1/362
13909 4316 8538 6664
Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,1,l-TCA TCE Perk. MCB Ketones
Partition coefficient
Reference
keotrope :%
Solute
"C) Reference
vlw
Ketones Acetone M EK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,CDioxane TH F
Solute
Reference
1.oo
1x/3/1345
-
-
0.9
1x/3/1345
2.1
l.x/1/362
1.7
1x/1/362
0.5 6.44
2fl402 1a1460
Partition coefficient
Reference
-
Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetate Miscellaneous DMF DMAc DMSO Sulfolane cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
10733
done
0.02 .8
98
671
v31205
Ketones
Section 6
Ethers
Diethyl ether Alternative names Ethyl ether, ethoxy ethane, ether, ethyl oxide, sulfuric ether, not petroleum ether Reference codes CAS number UN number
60 29 7 1155
Hazchem code EPA code
3YE Ul17
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
74 C4HlOOl 34.5 -116 0.715
Cubic expansion coeff (per oC x 103) Surface tension (@20°C dyn/cm) Ab~olute viscosity (@25°C cP) Refractive index (25°C)
1.6 17 0.24 1.352
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
-45 160 3E-16
Lower explosive limit (ppm) Upper explosive limit (ppm)
18500 360000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
19000 400 500 1
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
610000 2.57 462 60
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
6.9 1.3 +0.77 0.03 (5) 2.59
Vapour pressure equation constants (Log1o, mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water lOO)
7.4 1.3 4.3 11.7
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
6216 598 40 3.61 473 1735 3.39 3.02 103.5
6.98472 1090.64 231.20 7.00353 1088.4
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
1.0 28.0
Ethers
keotrope I(%
Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TM P Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics Tetra1in Alcohols Methanol Ethanol n-Propanol iPropano1 n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-PropanedioI
"C
N/W
Reference
58 33 None
8296 830 1
Yone Vone
8293 8304
2 62 Yone Yone Yone Vone
4029 6464 6351 8104
Solute
Reference
1.5
1x/3/1077
0.9 1.2
3 415 16 1x13/1077
4.8 3.8
2all70 2d375
Ethers
2.9 1.75 0.18 0.44
P157 V2l34 1 P678 P649
1.3
P1274
55.7 13.4
P1004 P657
1.61 1.22
30 41 Vone Vone Vone
1566 1474 1136 2987
0.6 0.4
Reference
+
Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,1,l-TCA TCE Perk. MCB
Partition coefficient
+ +
3 41492 3 41486
P655 PlOOl
~~~
~
Azeotrope
X% Solute Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DIPE Dibutyl ether MTBE 1,4-Dioxane THF
"C
wlw
Reference
None
5346
-
-
None
8305
Esters Me acetate None Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetate
Solute 9" 2.2 1.9
Reference
+
2.0
1X/3/1077
1.1
3 +415 13
5527
Miscellaneous DMF DMAc DMSO Sulfolane cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
V21470
<0.01
P2744
-
-
0.08 0.03
24.3
34 99 None
1235 3136
None
8297
None
1.6 2.6
2778
2.5
375
28.6
3+4/495 3+4/502
3 +41499
34
P516 P860
P594
0.41 0.03
V21228 P1710
0.20
P1101
0.40
P261
<0.01 99
Reference
0.28
3 4117 7 1~/311077
-
-
Partition coefficient
P1617
la1257
Ethers
Diisopropyl ether Alternative names Isopropyl ether, DIPE Reference codes CAS number UN number
108203 1159
Hazchemcode EPAcode
3YE
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
102 C6Hl4Ol 68 -86 0.724
Cubic expansion coeff (per oC x 103) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
1.4 18 0.33 1.367
-28 430
Lower explosive limit (ppm) Upper explosive limit (ppm)
14000 79000
10000 250 310 0.1
Vapour concentration@ 21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
193000 3.58 123
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
1.2 0.62 2.9 +2.0 0.19 2.83
Vapour pressure equation constants (Log1a. mmHg) Antoine equation A B C Cox chart A B
6.84953 1139.34 231.742 7.09624 1256.2
Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water lOO) Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
6.9 1.2
(5)
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
1.6 8.1
6936 885 52 3.14 500 2631 4.74 4.09 142.3
Ethers
beotrm (%
Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2 4-TM P Cyclohexane Benzene Toluene Ethylbenzene Xylenes Cg Aromatics Tetralin Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol l-Octanol Ethanediol DEG 1,2-PropanedioI
"C
VW
Reference
67 53 qone
12128 12196
Jone
10863
76 33
57 64
2091a 4110
35
66
639 1
54 Jone Jone
71
1496 1163 3004
Solute
Reference
1.1 1.3
3+4/559 lx/3/1243
1.0 1.2 1.1 1.4
3+4/555 3+4/553 3 +4/558 3+4/563
3.3 5.0 3.5 4.5 3.0
2al261 2al459 2al586 2b1101 2b1202
0.5 1.1
3+4/537 3+4/529
Partition coefficient
Reference
0.5
V2/6 18
Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1 1 1-TCA TCE Perk. MCB
rlone
233 1
..1
Ethers
~
.
keotrope (%
Solute Yetones ketone MEK MlBK Syclohexanone NMP ketophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane THF
"C
Reference
VIW
39 keo
54
5386 3bl357
7548
Reference
2.8
3b1357
1.7
3b1506
-
Uone
Solute
2.2
-
Partition coefficient
Reference
-
-
4.5
V3l103
0.6
VU282
0.01
P1656
1x/3/1243
Esters Me acetate Et acetate i-Propyl acetate a-Butyl acetate Cellosolve acetate Miscellaneous DMF DMAc DMSO Sulfolane cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
Uone
35
62
3185
3.2
579
19.2
3+41544
11525
Ethers
Dibutyl ether Alternative names Butyl ether Reference codes CAS number UN number Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
142 96 1
Hazchem code EPA code
130 C8Hl8Ol 142 -95 0.769
Cubic expansion coeff (per °C x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
1.15 1.4 0.63 1.397
25 194
Lower explosive limit (ppm} Upper explosive limit (ppm}
15000 76000
7377 4.48 5.5
0.5
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21 °C mmHg POCP
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm) Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
0.03 0.20 4.59
2.95
Vapour pressure equation constants (LoglOt mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100) Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
7.2 1.2
6.7963 1297.29 191.03 7.31357 1649.0 Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
7.1 8944 1182 66.0 307 6.09 5.18 170.4
Ethers
Azeotrope Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics Tetra1in Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 112-Propanediol Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 112-EDC l,l, 1-TCA TCE Perk. MCB Ethers
X% w/w
"C Reference
None 78 142
Solute T
Reference
1.o
1.o 1.o 1.1
1x/3/1370 1x/3/1370 1x/3/1370 1x/3/1370
1.o 0.9 1.o
1x/3/1370 1x/3/1370 1x/3/1370
Partition coefficient
Reference
14102 14117
None
4170
3.5
2d391
0.98
VU389
17 118 None
8195 8379
0.7
2d/23 1
0.04
V3/122
50 135 35 130 None
9770 9883 11745
0.5 0.8 1.2 0.8
1x/3/1370 1x/3/1370 1x/3/1370 1x/3/13 70
140
4354
136
6668
63 138 32 122 50 127 None
10003 6615 8479 12247
90
None
None
1501a
10537
Leotrope (% Solute
"C
ulw
Reference
Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane TH F Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetate Miscellaneous DMF DMAc DMSO Sulfolane CS2 Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
qone
126
qone done
30 done 57
Reference
2.3
1x/3/1370
-
-
2.1
1x/3/1370
Partition coefficient
Reference
0.07
CEP
-
-
5.0
V3/104
1.o
V2/304
8305
-
5
Solute 4"
11333
3220 11198
138
93
8788 10960 735
4.2
3d139
Ethers
Methyl tert butyl ether Alternative names Tert butyl methyl ether, MTBE Reference codes CAS number UN number Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4) Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
1634044
Hazchem code EPA code
88 C5Hl2Ol 55 -109 0.741
Cubic expansion coeff (per oC x 103) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (20°C)
18.3 0.35 1.369
-34 460
Lower explosive limit (ppm) Upper explosive limit (ppm)
16000 84000
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
372000 3.06 206
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm) Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
4.3 1.4
2.75
Vapour pressure equation constants (Loglo. mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100) Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
7.4 1.2 4.5 14.8
7.06046 1191.2 Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
1.6 8.4
7030 740
4.07 3.63 119.0
Ethers
zeotrope % Solute
"C Reference
//W
Yydmcarbons +Pentane hexane ?-Heptane ?-Octane a-Nonane a-Decane 2 2,4-TM P Cyclohexane Benzene Toluene Ethylbenzene Xylenes Cg Aromatics TetraIin Alcohols Methanol Ethanol n-Propano1 i- Propano1 n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-Propanediol Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. l12-EDC 1 1 1-TCA TCE Perk. MCB Ethers
51
2058
Solute +f'
Reference
1.2 0.9
1x/3/1152 1x/3/1152
1.1
1x/3/1152
3.0 3.0 2.9 2.6
2d160
Partition coefficient
Reference
lzeotrope (%
Solute
"C
ulw
Reference
-
-
Solute f
Reference
Partition coefficient
Reference
Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,CDioxane THF Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetate Miscellaneous DMF DMAc DMSO Sulfolane
cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
97
52
466
Ethers
1,4-Dioxane Alternative names Glycol ethylene ether, p-dioxane, diethylene dioxide, diethylene oxide Reference codes CAS number UN number
123 91 1 1185
Hazchem code EPA code
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
88 C4H802 101 + 12 1.034
Cubic expansion coeff (per °C x 103) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
12 180 5E-15
Lower explosive limit (ppm) Upper explosive limit (ppm)
20000 222000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
200 25 100 170
Vapour concentration @21°C ppm Vapour density (relative to air} Vapour pressure @21°C mmHg POCP
41000 3.06 32
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) Log1Oactivated carbon partition Log1Opartition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
2SE
1.1 40 1.3 1.420
Total Total -0.42 0 1.82
Vapour pressure equation constants (LoglOr mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
10.0 0.4 2.21 16.4
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
8510 567 36 5.21 588 3080 3.19 2.64 85.1
7.43155 1554.679 240.337 7.19047 1426.5
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
7.3 2.2
Ethers
Azeotrope Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TM P Cyclohexane Benzene Toluene Ethylbenzene Xylenes Cg Aromatics Tetralin Alcohols Methanol Ethanol n-Propanol i- Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol l-Octanol Ethanediol DEG lI2-Propanediol Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,1,l-TCA TCE Perk. MCB Ethers
X% w/w
"C
2 44
25 12
Reference
Solute
Reference
60 92 100
7547 7552 7554
3.3 4.0 7.4 4.7
3+4/472 lx/3/1052 1x/3/1052 3 +4/48 1
80 82 102
7540 7537 7550
2.6 1.1 1.2
3 +41468 3 -k 41465 1x/3/1052
None 9 78 45 95 None None 96 101 60 99
1998 4011 6447 6337 7519 7522 7520
1.6 2.5 1.7 1.2 1.5 1.4
2d148 1x/3/1052 2d53 1 2b/56 2b/147 2b/278
None
7543
None
4206
None
654 1
Vone \one Vone
1465 1124 2979
0.46 1.2 1.4
3+4/441 1x/3/1052 3 41447
Vone Vone
230 1 2181
80
+
Partition coefficient
Reference
zeotrope :%
Solute Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,CDioxane TH F
"C Solute
Reference
1.3 1.6
1x/3/1052 3b1523
-
-
-
7514 7527
1.1
3+41455
1.7
3 4- 41454
2.2
3i-41450
2.4 2.3
3i-41446 3i-41448
4.1
11382
JlW
Reference
lone
5333
Jone
7539
ione
7548
Esters Me acetate done Et acetate (one i-Propyl acetate n-Butyl acetate Cellosolve acetate Miscellaneous DMF DMAc DMSO Sulfolane cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
!3
119
119
Jone
7524
Jone
2769a
32
88
349
Partition coefficient
Reference
Ethers
Tetrahydrofuran Alternative names THF, tetra methylene oxide, 1,4-epoxybutane, oxacyclopentane Reference codes CAS number UN number
109999 2056
Hazchem code EPA code
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
72 C4H80l 66 -109 0.888
Cubic expansion coeff (per oC x 103) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
-15 212 4.5 E-5
Lower explosive UoDer, explosive
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
100 200 30
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' yolume Van der Waals' surface area Molar volume
limit (ppm) limit (ppm)
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP Total Total
1.1 28 0.55 1.404
23000 118000
230000 2.5 133 70
Lower critical solution temperature 72°C
+0.46 2.59
Vapour pressure equation constants (Loglo. mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
2SE U213
9.1 1.75 7.6 21
6.99515 1202.29 226.254 7.09092 1246.2 Kauri butanol value Evaporation time (ether = 1) Evaporation time (BuAc = 1)
2.3 6.3
6664 601 36 5.2 541 2.94 2.72 81.08
Ethers
Azeotrope X% Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes Cg Aromatics TetraI in Alcohols Methanol Ethanol n-Propanol i- Propano1 n-Butanol i-Butanol s-Butanol n-Amyl ak. i-Amyl alc. Cyclohexanol l-Octanol Ethanediol DEG 1,2-PropanedioI
"C
W h
Reference
Solute f
Reference
None 50 63
7407
2.0 1.9
1x/3/1046 1x/3/1046
1.7
1x/3/1047
1.7 0.84 0.85 0.90
1x/3/1046 1~!3/1046 1x/3/1046 1x/3/1047
0.9
1x/3/1047
2.4 1.9 1.4 1.4 1.2
2a/141 2C4328 2~4497 2W55 2b/146
6.6
2d/3
0.5 0.25 0.75 0.60
lx/l/lOO 1x/3/1046 3 4/429 1x/3/ 1046
97
60
69 61 90 66 None None None
1996 4009
None
4204a
34 72 None
1464
6335a
Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,P-EDC 1,1,1-TCA TCE Perk. MCB Ethers
+
Partition coefficient
Reference
Azeotrope X%
Solute Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane TH F
"C
wlw 8
Reference
Solute f
-
-
Partition coefficient
Reference
-
-
2.05
V21396
64
-
Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetate Miscellaneous DMF DMAc DMSO Sulfolane
Reference
None
1.1
1x/3/1046
-
1.1
1x/311046
4.6
3+41433
cs2
Acetic acid AniIine Nitrobenzene Morpho1ine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
6273
None
96
64
345
10.4
11367
Ethers
Esters
Methyl acetate Alternative names Acetic acid I methyl ester Reference codes CAS number UN number
79 20 9 1231
Hazchem code EPA code
2SE
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
74 C3H602 57 -98 0.927
Cubic expansion coeff (per °C x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
1.4 24 0.37 1.360
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
-10 500 3.4E-6
Lower explosive limit {ppm) Upper explosive limit {ppm)
31000 160000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
10000 200 250 200
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
290000 2.57 171 2.5
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
24.5 8.2 1.85 +0.18 1.51
Vapour pressure equation constants (Loglo. mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100) Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
9.6 1.7 6.7 29
7.06524 1157.63 219.726 7.25014 1254.0
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
2.1 9.5
7178 348 37 4.6 507 2.80 2.58 79.8
Esters
keotrope ~~~
:% Solute
"C
VIW
Reference
Solute
Reference
Partition coefficient
Reference
3.81
V2l4 16
~~~~~
Hydrocarbons n-Pentane n- Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TM P Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics Tetralin Alcohols Methanol Ethanol n-Propanol i- Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol l-Octanol Ethanediol DEG 1,2-PropanedioI
!2 53 36
34 52 57
5536 5554 5558
5.5
1xJ31994
30
55 57
5541 5537
3.6 1.4
51393 51375
31 54 37 57 lone lone
1967 3969
2.7 1.9 2.8 2.2 2.3
2d92 2d335 2d530 2b150 2f1137
0.3
5516
Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC l,l, 1-TCA TCE Perk. MCB Esters
lone !3 65 lone
1557 1448 1110
0.6 0.6 1.7
51347 51341 51339
1.2
51374
~~
Azeotrope X%
Solute Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,CDioxane THF
"C
Partition coefficient
Reference
3+4/159 3+4/271
0.37
V21463
-
-
-
-
0.8
51357
1.2
51397
0.41
V41183
WIW
Reference
Solute
Reference
50 55 None
5310 5519
1.3 1.o
None
5527
5521a
Esters Me acetate Et acetate None i-Propyl acetate n-Butyl acetate None Cellosolve acetatc Miscellaneous DMF DMAc DMSO Sulfolane
cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-N itropropane Acetonitrile Furfuraldehyde Phenol Water
30 40 None
1198 3101a
2.7 1.1
51349 5/82
lone
2763
1.4
51354
276
8.5
11264
37
56
Esters
Ethyl acetate Alternative names ETAC, acetic ester, EtOAc, ethyl ethanoate, acetic acid, ethyl ester Reference codes CAS number UN number
141 78 6 1173
Hazchem code EPA code
3YE Ul12
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
88 C4H802 77 -84 0.895
Cubic expansion coeff (per oC x 103) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
1.39 24 0.46 1.370
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
-4 484 1.0E-9
Lower explosive limit (ppm) Upper explosive limit (ppm)
22000 115000
laaaa 400
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
50
Aqueous effluent Solubility in water (25°C %wlw) Solubility of water in (25°C %wlw) Log1Oactivated carbon partition Log1Opartition in octanollwater (wlw) Biological oxygen demand wlw (days) Theoretical oxygen demand wlw
7.7 3.3 2.31 +0.73 1.2 1.82
Vapour pressure equation constants (Log1o. mmHg) Antoine equation A B C Cox chart A B
7.10179 1244.95 217.881 7.30648 1358.7
Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
9.1 1.7 6.02 23
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/moI/OC) Critical pressure (MN/m1 Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
7744 493 40 3.84 523 2494 3.48 3.12 98.5
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
114000 3.04 78 21.8
3.0 4.2
Esters
Azeotrope Solute
X% w/w
I
"C Reference
Solute rP
Reference
Partition coefficient
Reference
I Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes Cg Aromatics Tetralin Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-PropanedioI Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,1,l-TCA TCE Perk. MCB Esters
38
65
7588
3.1 2.4 2.9 3.1
1x/1/105 515 14 1W3I105 1 1x/3/105 1
I
I 54 72 None None
7583 7580 7591
None
7594
1.5 2.3 3.1 1.2 1.8 1.6
1V3I105 1 51506 51502 515 16 51540 5/54 1
1
I
I
56 62 69 72 None 75 76 None None None
1999 4012 6448 6338 7567 7570 7568
2.7 2.2 1.9 1.6 2.3
3.5
None
1x111103 2a/351 2a/536 2bl59 2bl148
2dl5 11
1.08 0.41 0.19 0.17 0.03 0.04 0.07
V2193 CEH V21549 CEH V3150 v3/54 V3/52
I
I
I
I
I
None None
757 1 7590
2.0 2.2
2b1126 2f/33 5
1x/1/103 l-x/11103 1x/1/103 1x/1/103
72 78 43 75 None
1466 1125 2980
0.5 0.5 1.3 0.8
None
2302
0.9
51454
None
7578
1.4
51492
I
I
I
I
I
keotrope :%
Solute
"C
Reference
VIW
Solute 1p
Reference
1.2 2.0 0.6
3 41176 3+41278 3bl527
1.o
3 +4/513
1.1 1.1
3 41455 1xJ11104
Partition coefficient
Reference
~
Ketones ketone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,CDioxane THF
lone 32 77
5334 7345
7514
Uone
Esters Uone Me acetate Et acetate Vone i-Propyl acetate \one n-Butyl acetate Cellosolve acetatt
5521a
-
Acetic acid Ani Iine Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
0.14
CEH
+
51357
-
-
1.o
51487
3.9
5/46 1
-
-
7585
Miscellaneous DMF DMAc DMSO Sulfolane
cs2
1.1
+
1.85
V3148
3 46 None
1220 3120
2.7 7.0
1xJ11103 51104
0.29
V41184
None 77 75 None
6274 2770 7574
1.6 1.7
1xJ11103 3al123
0.17 0.03 eo.01
v21175 vu57 v4124 1
352
9.7
11393
91.5
70
Esters
Isopropyl acetate Alternative names Sec propyl acetate, 2-propyl acetate, acetic acid, isopropyl ester Reference codes CAS number UN number
108 21 4 1220
Hazchem code EPA code
3YE
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
102 C5HIO02 89 -69 0.874
Cubic expansion coeff (per oC x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
1.31 22.1 0.46 1.375
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
3 460 5.7E-7
Lower explosive limit (ppm) Upper explosive limit (ppm)
18000 80000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
16000 250 200 30
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
66000 3.5 47 21.5
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) Log1Oactivated carbon partition Log1Opartition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
2.9 3.2 2.63
2.04
Vapour pressure equation constants (Logl(), mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100) Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/moI/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
8.5 2.7
7.3340 1436.53 233.7 7.34068 1422.7
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
8262 534 50 3.65 538 4.15 3.65 117.8
Esters
Azeotrope
K% Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TM P Cyclohexane Benzene Toluene Ethylbenzene Xylenes Cg Aromatics Tetralin Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 112-Propanediol
wlw
9 67
I
"C Reference
69 88
Esters
Reference
9297 9302
Reference
I
I 25 79 None None
9296 9294 9300
I I (
65 77
2046 4054
48 80 None
6363 8121
20 48
1.9
2d391
1.7
2fI59
(
I
I
I
I
Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 112-EDC 1 1 1-TCA TCE Perk. MCB
Solute
Partition coefficient
I
(
None None
1145 2992
None
2317
I
I
keotrope (%
Solute Yetones ketone MEK MIBK Syclohexanone NMP ketophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane THF
"C
MIW
Reference
lone \(one
5365 7366
Vone
7527
Esters Me acetate Vone Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetatt
Solute .P
1.o
Reference
51487
-
-
-
1251 3147
1.4
51123
Partition coefficient
Reference
-
-
Miscellaneous DMF DMAc DMSO Sulfolane
cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
None None
20 90
80
2788
77
439
0.36
V2/236
<0.01
V41264
Est e n
n-Butyl acetate Alternative names BuAc, n-butyl ethanoate, BuOAc, acetic acid, butyl ester Reference codes CAS number UN number
123 86 4 1123
Hazchem code EPA code
3YE
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
116 C6Hl2O2 126 -73 0.876
Cubic expansion coeff (per oC x 103) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
1.16 25.1 0.73 1.392
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
22 407 1.6E-8
Lower explosive limit (ppm) Upper explosive limit (ppm)
17000 150000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
laaaa 150 200 15
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
14200 4.03 10.6 32.3
Aqueous effluent Solubility in water (25°C %wlw) Solubility of water in (25°C %wlw) LoglO activated carbon partition LoglO partition in octanollwater (wlw) Biological oxygen demand wlw (days) Theoretical oxygen demand wlw
).7 1.3 3.04 +1.7 1.15 2.21
Vapour pressure equation constants (Loglo. mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100) Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
8.6 1.8
7.02845 1368.50 204.00 7.44951 1626.5 Kauri butanol value Evaporation time (ether = 1) Evaporation time (BuAc = 1)
11.8 1.0
24.1 8584 784 58 3.05 579 4.83 4.20 132.5
Esters
Azeotrope ~~
X% Solute
"C Reference
Solute f
Reference
None 52 119
11826a 11832
1.8
5/59 1
None None
11687 10859
1.5 0.9 1.o
51585 51583 51586
None None
11828 11830
5.8 2.1 1.2 1.8 1.4
2c/213 2c/426 2d484 2dD5 2 bll97
1.5
2fl4 17
6.9
2dll5
9968 6576 8434 11823
2.3 1.8
2d1122 2b1294
1493 1161
0.7 1.2
51574 51573
0.7
51575
WIW
Partition coefficient
Reference
1.12 0.61 0.11
V21131 VU363 V21574
0.03
V4l253
~~~
Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2 2 4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes C, Aromatics Tetra I in Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-PropanedioI
None
4258
None
6655a
Glycol ethers PGME EGME EEE EGBE
None 52 119 87 126 None
Chlorinated MDC Chloroform Carbon tet. 112-EDC 1 1 1-TCA TCE Perk. MCB Esters
None None 60 94 None 37 116 None None None 82 126 None
None None
21 120 None
8153 8345 8237 9754 9837
2210 10516
Azeotrope X%
Solute Ketones Acetone MEK MIBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DIPE Dibutyl ether MTBE 1,CDioxane THF
"C
Reference
WIW
5383
None
95
126
Esters None Me acetate None Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetatt None
Solute f
Reference
1.4
3b1197
1.2
51397
-
-
2.1
51147
2.3 1.8 0.5 6.7
51577 3 +4146 2b/373 11516
Part coefficient
0.14
Reference CEH
11833
7585
-
-
-
11821
Miscellaneous DMF DMAc DMSO Sulfolane
cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile FurfuraIdehyde Phenol Water
None
3177
None
8850
Azeo 71
90
10896 542
0.23
V41185
0.07 0.02 <0.01
V2/184 V3/194 V3/297
Esters
Cellosolve acetate Alternative names Ethylene glycol monoethyl acetate, 2-ethoxy ethyl acetate Reference codes CAS number UN number
111 15 9 1172
Hazchem code EPA code
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
132 C6Hl2O3 156 -62 0.973
Cubic expansion coeff (per oC x 103) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (20°C)
52 345
Lower explosive limit (ppm) Upper explosive limit (ppm)
17000 82000
2500 5
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
2108 4.6 1.5 60
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
0.1
1.12 28.2
Aqueous effluent Solubility in water (25°C %w/w) 22.9 Solubility of water in (25°C %w/w) 6.5 LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w 1.82 Vapour pressure equation constants (Loglo. mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D)constant (20°C) . Dielectric
8.6 1.8
6.8246 1291.3 170.97 7.542 1799.3 Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
57 0.2
Polarity (water 100) Thermal information Latent heat (car/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
9768 754 63.9 3.0 607
135.7
Esters
~~
Azeotrope X% Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes C, Aromatics Tetra Iin Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-0ctanol Ethanediol DEG 112-Propanediol Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. l12-EDC 1I 1 1-TCA TCE Perk. MCB Esters
"C
wlw
Reference
None None None
11913 12007 12009
None None
8160 8352
None
9842
None
4261
None
6665
13 151 None None None
9969 6583 8440 11989
Solute f
Reference
Partition coefficient
Reference
heotrope (%
Solute
"C Reference
YIW
Solute
Reference
Partition coefficient
Reference
Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DIPE Dibutyl ether MTBE 1,CDioxane THF
38
142
Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate lone Cellosolve acetatf
12021
11821
-
-
Miscellaneous DMF DMAc DMSO Sulfolane cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
Vone 28
50
185 97
8766 10898 559
Esters
Miscellaneous solvents
Dimethylformamide Alternative DMF
names
Reference codes CAS number UN number Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4) Fire hazards Flash point (closed
cup °C)
Autoignition temperature Electrical conductivity Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold
(OC)
(ppm)
68 12 2 2265
Hazchem code EPA code
2P
73 C3H7N1O1 153 -61 0.945
Cubic expansion coeff (per oC x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
1.03 35 0.82 1.427
62 445 6.0E-8
Lower explosive limit {ppm) Upper explosive limit {ppm)
22000 160000
3500 10 20 100
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
3700 2.53 3.8
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) Log1Oactivated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
Total Total
-0.74 0.9 1.86
Vapourpressure equation constants (Loglo. mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D} Dielectric constant (20°C} Polarity (water 100} Thermal information Latent heat (cal/mol} Nett heat of combustion (kcal/gmol} Specific heat (cal/mol/OC} Critical pressure (MN/m2} Critical temperature (K} Latent heat of fusion (cal/mol} Van der Waals' volume Van der Waals' surface area Molar volume
12.1 3.8 36.7 40.4
7.10850 1537.78 210.390
Kauri butanol value Evaporationtime (ether = I ) Evaporationtime (BuAc = I)
120 0.17
10074 423 36 4.48 647 3.09 2.74 77.43 Miscellaneous solvents
Leotrope (%
Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes Cg Aromatics Tetra Iin Alcohols Methanol Ethanol n-Propanol iPropanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-PropanedioI
"C Reference
M/W
5
Jone Jone 15
!O
Jone Jone
97
5893 5893a 134 136
5894
Solute f
Reference
12.8 17.2 8.3 18.6 22.0 25.3 30.1 5.4 1.2 2.0 2.2 2.7
lx/1/58 6c/332 6V98 1x/1/61 1~l311005 1x/3/1005 1x/1/61 1x/1/59 1x/1/59 1x/1/60 1x/3/1003 7/48 1
0.6 0.6
2a/115 2c/371
1.2 1.0
2f1527 2b/8
0.9
81265 0.29 8/117
Partition coefficient
Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,1,1-TCA TCE Perk. MCB Miscellaneous solvents
1.8
0.4
0.04 0.02
Reference
rzeotrope :%
Solute
VIW
"C
Reference
Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane TH F Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetate Miscellaneous DMF DMAc DMSO Sulfolane
-
cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
Solute f
Reference
0.9 1.3
3+41164 3bl289
1.2
3bl500
1.3
3+41454
1.6
1x/3/999
-
-
1.2
81407
4.4
1x/1/57
0.3
81428
1.08
11276
Partition coefficient
Reference
kzeo
Jone Jone
2765
Miscellaneous solvents
Dimethylacetamide Alternative names DMAc Reference codes CAS number UN number Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4) Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
127 195
Hazchem code EPA code
87 C4HgNlOl 166 -20 0.945
Cubic expansion coeff (per oC x 103) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
0.95 34 0.92 1.436
70 491
Lower explosive limit (ppm) Upper explosive limit (ppm)
15000 115000
400 10 20 50
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm) Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
1.0
Total Total
-0.77
Vapour pressure equation constants (LoglOt mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water lOO)
1316 3.02
11.0 3.8 37.8 40.1
7.76228 1889.1 221.00
Kauri butanol value Evaporationtime (ether = I) Evaporationtime (BuAc = I)
172 0.14
10360 569 42 4.08 658 3.53 2.97 92.1
Miscellaneous solvents
zeotrope % Solute
I/W
"C Reference
Solute f
Reference
8.3 17.0 20.0 13.0
lx/1/118 lx/l/118 1x.W 18 lx/3/1168
2.3 3.0 1.6 1.6
l~W118 W1/118 1x/3/1168 1x/3/1168
0.5 0.5 0.3
lV3/1065 1x/3/1068 2d454
~~
Yydrocarbons ?-Pentane ?-Hexane heptane v0ctane 7-Nonane ?-Decane 2,2,4-TM P Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics Tetralin Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-PropanedioI Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,l ,l-TCA TCE Perk. MCB discellaneous solvents
Partition coefficient
Reference
rzeotrope ~~
:%
jolute
"C Solute
Reference
1.1 1.1
1x/3/1168 1x/3/1168
1.2
1x/3/1168
1.3 1.3
1x/3/1168 1x/3/1168
-
-
-
3133
0.2
5/115
1.o
1d 4 0 2
Reference
vlw
Vetones ketone MEK MlBK Qclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,CDioxane THF Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetatc Miscellaneous DMF DMAc DMSO Sulfolane
cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
79
None
171
Partition coefficient
Miscelr
Reference
eous solvents
Dimethylsulphoxide Alternative names DMSO, sulfinyl-bis-methane,
DIMSO
Reference codes CAS number UN number
67 68 5
Hazchem code EPA code
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
78 C2H6OlSl 189 + 18.5 1.101
Cubic expansion coeff (per oC x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
1.0 43.7 2.0 1.476
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
95 255 2E-9
Lower explosive Upper explosive
30000 420000
1000
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm) Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
(ppm) (ppm)
650 2.7 0.7
Total Total
Vapour pressure equation constants (LoglQ, mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
limit limit
13.0 3.96 46.6 44.4
6.88076 1541.52 191.797
Kauri butanol value Evaporationtime {ether = 1) Evaporationtime {BuAc = 1)
1500
12636 441 36
3221 2.83 2.47 71.3
Miscellaneous solvents
Leotrope ~~
(%
Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TM P Cyclohexane Benzene Toluene Ethylbenzene Xylenes Cg Aromatics Tetra Iin Alcohols Methanol Ethanol n-Propanol i- Propanol n-Butanol i-Butanol +Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol l-Octanol Ethanediol DEG 1,2-PropanedioI
vlw
"C
Referenc
Solute f
Reference
25.9 38.6 33.4 43.5 55.9 70.7 61.2 15.5 2.7 4.1 4.6 7.5
1x/1/29 1x/1/30 1x/1/31 1x/1/3 1 1x/1/3 1 1x/1/32 1x/1/31 1x/1/30 71169 71386 1x/1/31 1x/3/969
0.4 0.8
2d62 1x/3/96 7
1.5 0.7 0.9
2fl39 2fl131 2bl275
ione
0.2
2 b17
lone lone lone
0.6 0.7 4.0
81264 8122 9 81107
lone
done ione
4184
4183a
Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Ehloroform Earbon tet. 1,2-EDC lI1,1-TCA TCE Perk. MCB
Miscellaneous solvents
Partition coefficient
Reference
I rzeotrope :%
Solute
Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1.CDioxane
I
"C
Solute f
Reference
ione
1.8 2.5
3bl80 1x/3/967
lone lone
1.5 2.5
3+4/450 3 41433
3.2 3.3
1x/3/967 5146 1
1.1
81407
-
-
-
243
0.5
11119
f1W
Reference
THF Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetate Miscellaneous DMF DMAc DMSO Sulfolane
rlone
Partition coefficient
Reference
+
-
cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
\one
L
Miscellaneous solvents
Sulfolane Alternative names (Cyclo)tetramethylene sulphone, thiolane-1 , 1-dioxide Reference codes CAS number UN number Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4) Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
126 33 0
Hazchem code EPA code
120 C4H8O2S 285 +27.4 1.26
Cubic expansion coeff (per oC x !03) Surface tension (@30°C dyn/cm) Absolute viscosity (@30°C cP) Refractive index (30°C)
0.7 35.5 10.3 1.471
177
Lower explosive limit (ppm) Upper explosive limit (ppm)
54000
Vapour concentration @21°C ppm Vapour density {relative to air) Vapour pressure @21°C mmHg POCP
65.8 4.17 0.05
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm) Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C o;oW/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w Vapour pressure equation constants (Log1()1mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
4.69 44 41
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
14720 595 55 5.32 801 1063 4.04 3.20 95.3
Total Total
7.40800 2255.469 211.393
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
Miscellaneous
solvents
keotrope
(96 Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes Cg Aromatics Tetra1in
N/W
keo
4zeo
Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-Propanediol Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,1,l-TCA TCE Perk. MCB
None
Miscellaneous solvents
"C Reference
Solute
Reference
33.2 48.2 51.4 66.0 87.3 115.0 53.2 19.3 2.7 1.5 4.9 5.1 6.7
1x/1/109 lx/l/lll lx/l/112 lx/1/113 lx/1/114 ldl/114 lx/llll3 lx/l/llO 7/191 71399 ldllll2 l x / l / l 12 1x/3/1063
0.8 3.3 3.5 4.9 4.6 4.3
2d125 2~4344 1x/3/1054 2d/53 1x/3/1055 1x/3/1055
1.7
2f/l03
0.9 1.1 5.0 1.3
8/266 1x/3/1053 1x/3/1053 1x/3/10 53
Partition coefficient
Reference
~
Azeotrope
Y% Solute
N/W
Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane THF Esters Me acetate Et acetate :-Propyl acetate ?-Butyl acetate :el losolve acetatt Uiscellaneous IMF IMAc IMSO julfolane >Sp \cetic acid Wine litrobenzene Aorpholine 'yridine !-Nitropropane ketonitrile :urfuraIdehyde 'henol Vater
lone
"C Reference
Solute
Reference
1.5 2.1 3.7
1x/3/1054 1x/3/1055 1x/3/1058
3.3
lx/3/1055
1.7 2.8
1x/3/1054 1x/3/1055
-
-
2.1
1x/3/1065
Partition coefficient
Reference
Miscellaneous solvents
Carbon disulphide Alternative names Carbon bisulphide Reference codes CAS number UN number
75 150 1131
Hazchem code EPA code
PO22
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
76 C1S2 46 -111 1.26
Cubic expansion coeff (per oC x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
1.4 32 0.36 1.628
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
-30 102 1.0E-16
Lower explosive limit (ppm) Upper explosive limit (ppm)
13000 500000
500 10
vapour concentration @21°c ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
685000 2.7 309
Health hazards Idlh (ppm) OES-TWA OES-STEL Odour threshold (ppm)
0.2
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) Log1Oactivated carbon partition Log1Opartition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
0.21 0.014
2.0
Vapour pressure equation constants (Loglo. mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole {D) Dielectric constant {20°C) Polarity {water 100)
10.0 0 2.64 6.5
Thermal information Latent heat {cal/mol) Nett heat of combustion {kcal/gmol) Specific heat {cal/mol/OC) Critical pressure {MN/m2) Critical temperature {K) Latent heat of fusion {cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
6460 246 18 7.62 546 1050 2.06 1.65 60.65
6.94279 1169.11 241.59
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
1.8 10.9
Miscellaneous solvents
Azeotrope X% Solute Hydrocarbons, n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n- Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes Cg Aromatics Tetra1in Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol l-Octanol Ethanediol DEG 1,2-PropanedioI
"C
Reference
WIW
11
36
None None
None None None
71 91 95 92 None None None None
40 43 46 44
Solute f'
Reference
35 36 None None
Miscellaneous solvents
Reference
16.4
P385
1256 1274 1278 2.0
1V31938
1.5
6d57 1
1269 1265 1276
0.4 1.4 1.1
6all54 71100 71361
1175 1189 1209 1208 1233 1236 1260 1257
6.3 84.4 13.7
2a135 2a/281 2d417
11.3
2f1120
24.8 8.7
2d1239 2fl37 1
1170 1169 1085
1.4 1.4
812 14 8176
1.7
813 18
Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,l ,l-TCA TCE Perk. MCB
Partition coefficient
keotrope :%
Solute Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane TH F
"C
39 j7 46 34 lone
1194 1216 1272
7.0 4.4
3 +41132 1xl31938
34
1235
2.0
3+41495
3.3
3+41446
6.6
51349
13
Miscellaneous DMF DMAc DMSO Sulfolane Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
Reference
vlw
Esters 40 70 Me acetate 46 33 Et acetate Uone i-Propyl acetate n-Butyl acetate Cellosolve acetatf
cs2
Solute f
Reference
1198 1220 1251
-
-
1180
Uone
26.6
38
Partition coefficient 0.78
P506
0.15
P520
-
-
127.2
P333
81320 0.43
37
43
Reference
P1663
207
Miscellaneous solvents
Acetic Acid Alternative names Ethanoic acid, glacial acetic acid Reference codes CAS number UN number
64 19 7 1842
Hazchem code EPA code
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
60 C2H4O2 118 + 17 1.051
Cubic expansion coeff (per oC x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
40 427 6E-9
Lower explosive limit (ppm) Upper explosive limit (ppm)
54000 160000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
1000 10 15 2
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
17400 2.08 13
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C o;oW/w) Log1Oactivated carbon partition Log1Opartition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
1.370
Total 1.80 -0.24
1.07
10.1 1.7 .6.2
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
1.13
Total
Vapour pressure equation constants (Loglo. mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
1.14 27.4
7.5596 1644.05 233.5 7.4565 1592.4 Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
64.8 5800 188 29.4 5.8 595 2800 2.20 2.07 57.5
Miscellaneous solvents
keotrope Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2 2 4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics Tetralin Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-Propanediol
(96 ulw
"C
Reference
Solute ?
Reference
9.0 20 16
51152 51175 51189
31
51191
Vone 6 25 53 59 79
68 93 105 113 117
3156 3184 3204 3219 3230 3237
10 2 34 56 73
79 80 105 115 116
3173 3163 3194 3206 3208
4.9 3.3 7.6 7.9 5.6
51146 51127 51159 51178 51181
1933 3090 3109
0.9 0.7 0.9 0.8 1.o 1.1 1.2
221148 2c/293 2211525 2d184 2d1158 2fl302 2f122 1
1.9 2.6 5.4 2.6
5164 5/62 5/59 5174
3.3
5/72
Vone Yone Yone 43
120
3135
16
133
3156a
76
1437 1099 2961
118 107 115
2282 2158 3160
Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 112-EDC 1 1 1-TCA TCE Perk. MCB
None 2 \one
4 39 59
liscellaneous solvents
Partition coefficient
Reference
Azeotrope
X% Solute Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,bDioxane THF
Reference
Solute r"
Reference
None None None
3101 3117 3175
1.o 1.1 1.5
3 +4/148 3+4/269 3+4/345
None None None
3136 3185 3220
1.9 2.4
3 41502 3 +4/544
3119
0.9
3 +41448
3101a 3120 3147 3177
1.1 1.2 1.6 1.8
5/82 51104 51123 51147
3133
0.1
5.115
-
-
0.04
511 ia
1.4
11102
78
Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetate
None None None None
Miscellaneous DMF DMAc DMSO Sulfolane
21
cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
"C
WIW
119
171
None
Reference
+
1180
-
-
None None
3164 3162
51
Partition coefficient
138
3139
None None
2758a 3138
None
23 1
Miscellaneous solvents
Aniline Alternative names Aminobenzene, benzeneamine, phenylamine Reference codes CAS number UN number
62 53 3 1547
Hazchem code EPA code
UO12
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
93 C6H7Nl 184 -6 1.022
Cubic expansion coeff (per oC x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
0.9 45.5 4.4 1.583
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
76 770 2.4E-8
Lower explosive limit (ppm) Upper explosive limit (ppm)
13000 110000
100 0.5
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
380
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
0.5
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
3.5 5.1 2.78 +0.94 1.50 (5) 2.67
Vapour pressure equation constants (Log1~ mmHg) Antoine equation A B C Cox chart A B
7.46441 1840.79 216.92 7.55756 1936.2
Solvent properties Solubility parameter Dipole (D} Dielectric constant (30°C} Polarity (water 100}
10.3 1.56 6.7 42.0
Thermal information Latent heat (cal/mol} Nett heat of combustion (kcal/gmol} Specific heat (cal/mol/OC} Critical pressure (MN/m2} Critical temperature (K} Latent heat of fusion (cal/mol} Van der Waals' volume Van der Waals' surface area Molar volume
10602 773 48 5.30 699 2519 3.72 2.82 91.53
3.23 0.26
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
Miscellaneous solvents
Azeotrope
X%
"C
Solute
WlW
Reference
Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics Tetra1in
None None None 13 149 36 167 None None None None None None
11151 11179 11197 11210 11230 11196 11148 10850 11167 11183 11185
A Icohols Methanol Ethanol n-Propanol iPropan01 n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-Propanediol
Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC l,l,l-TCA TCE Perk. MCB
Solute f
Reference
17.4 6.8 11.0 38 26
1x/1/240 6a1580 6b1161 lx/3/1194 1x/1/242
6.0 4.1 1.4 1.6 2.3 3.1
6b1318 6al255 71263 71426 71474 1x/3/1194
None
4075
2.2 3.3
1x/3/1192 2a1427
None
8138
2.3
1x/3/1193
2.9
2b1265
1.6
2bl395
3.6
2b116
1.4 1.5 3.8
1x/1/239 1x/1/239 81174
1.8
81527
None None 83 76
184 181
9824 11149 11200 4242
57
186
6655
None
9963
None
11153
None
None
Miscellaneous solvents
10511
Partition coefficient
Reference
4zeotrope (%
Solute Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane TH F
"C Reference
Solute
Reference
1.3 0.6
3b1183 1x/3/1192
0.4
1x/3/1192
1.4
1x/1/239
0.3
81428
3.5
1x/1/239
-
-
-
10704
6.4
81540
\zeo?
?
81500
Jone
0.9
81385
4.5
11499
MIW
Jone Jone
11144
Jone
11182
Jone
11198
Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetate Miscellaneous DMF DMAc DMSO Sulfolane
cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
Leo?
qone 3
!5
3164
180
81
488
Partition coefficient
Reference
-
-
0.05
V31233
0.01
V3l290
Miscellaneous solvents
Nitrobenzene Alternative names Oil of mirbane, nitrobenzol Reference codes CAS number UN number
98 95 3 1662
Hazchem code EPA code
2Y U169
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
123 C6H6N1O2 211 +6 1.204
Cubic expansion coeff (per oC x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
0.96 43.9 1.80 1.550
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
88 496 2E-10
Lower explosive limit (ppm) Upper explosive limit (ppm)
18000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
200 1 2 6
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
272 4.27 0.21
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) Log1Oactivated carbon partition Log1Opartition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w Vapour pressure equation constants (Loglo. mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C)' Polarity (water 100)
10.0 4.0 34.8 32.4
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
10455 706 44 4.82 720 2768 4.08 3.10 102.7
0.19 +1.86 1.82 7.13043 1751.36 201.34
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
Miscellaneous solvents
4zeotroDe I(%
Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TM P Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics Tetra1in Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-Propanediol Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,1,l-TCA TCE Perk. MCB
"C
N/W
Reference
None None
9740 10708
Solute Ip"
Reference
7.0 8.7 6.7 3.9 8.0
1x/1/222 6a1532 1x/1/223 6b1241 1x/1/223 1x/1/223 6a1203 712 53 71422 71470 1x/1/223
None None
10703 10718
11.8 9.6 1.1 1.5 1.6 1.8
None None
2065 4072
10.4 10.7
1x/1/220 1x/11220
None
8135
None
823 1
16.0
2f1226
None 41 186 90 210
10754 4238 8518
None
10710
None None
1485 1153
1.0 1.0 1.8 1.1
1x/11220 1111220 81168 1x/11220
None
10508
1.1
lx/3/1180
Miscellaneous solvents
Partition coefficient
Reference
5.9 3.5
P165 V2l349
0.02
V31257
~
botrope (%
Solute
"C Reference
ulw
Solute g
Reference
Partition coefficient
Reference
~
Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane THF
rlone
10733
lone
8297
Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetatt Miscellaneous DMF DMAc DMSO Sulfolane cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-N itropropane Acetonitrile Furfuraldehyde Phenol Water
None 97 180
-
12
99
3162 10704
-
1.2 1.1
lxJ11221 3bl316
0.8
1x/3/1180
1.4
1x/11221
2.6
1x/1/220
1.o
81540
-
-
1.7
1x/11220
3.9 0.01
P311 V31260
-
-
0.02
V3/259
485
Miscellaneous solvents
Morpholine Alternative names Tetrahydro. p. oxazine, diethyeneimide oxide, tetrahydro-1,4-isoxazine Reference codes CAS number UN number
110 91 8 2054
Hazchem code EPA code
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
87 C4HgN1Ol 129 -5 1.00
Cubic expansion coeff (per oC x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
38 310 6E-10
Lower explosive limit (ppm) Upper explosive limit (ppm)
18000 108000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
20 30 1
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
10500 3.0 7.9
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C o;oW/w) Log1Oactivated carbon partition Log1Opartition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
Thermal information Latent heat (cal/mol} Nett heat of combustion (kcal/gmol} Specific heat (cal/mol/OC} Critical pressure (MN/m2} Critical temperature (K} Latent heat of fusiQn (cal/mol} Van der Waals' volume Van der Waals' surface area Molar volume
1.1 37.5 2.2 1.455
Total Total -1.08 2.11
Vapour pressure equation constants (Log1o. mmHg) Antoineequation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D} Dielectric constant (20°C} Polarity (water 100}
2P
1.56 7.4 31.8
7.1603 1447.7 210.0
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
9510 42 5.5 618
3.47 2.80 87.5
Miscellaneous solvents
hotrope (%
Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics Tetralin
VIW
lone
Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-Propanediol Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. l12-EDC 1 1,l-TCA TCE Perk. MCB Miscellaneous solvents
"C Reference
Solute f'
Reference
27.0
1x111123
3.3
1x111123
1.9
3 41482
0.9
2d345
+
8057
Partition coefficient
Reference
beotrope ~
[Yo
Solute
~~
"C Reference
vlw
Solute f
Reference
Partition coefficient
Reference
Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,CDioxane TH F
73
127
8058
Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetatc Miscellaneous DMF DMAc DMSO Sulfolane cs2
Acetic acid AniIine Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Fudura Idehyde Phenol Water
-
-
-
-
None
367
2.0
la1327
-
Miscellaneous solvents
Pyridine Alternative names Reference codes CAS number UN number
11086 1252
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
1
Hazchem code EPA code
2WE U196
79 C5H6Nl 115 -42 0.983
Cubic expansion coeff (per °C x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
1.0 36.6 0.88 1.507
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
20 522 4E-8
Lower explosive limit (ppm) Upper explosive limit (ppm)
18000 124000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
3600 5 10 0.03
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
22000
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w Vapour pressure equation constants (Loglo. mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100) Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/moI/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
10.7 2.3 12.9 30.2
2.74 16.6
Total Total 2.26 +0.64 1.47 (5) 3.03
7.01328 1356.93 212.655
Kauri butanol value Evaporation time (ether = 1) Evaporation time (BuAc = 1)
12.7
8374 617 34 5.64 620 3.00 2.11 80.86
Miscellaneous solvents
Azeotrope X%
"C
Solute
wlw
Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes Cg Aromatics Tetra1in
None 25 96 56 110 90 115 None 23 96 None None 21 110 None None
8860 8867 8870 8872 8868 8846 884 1 8858 886 1 8863
None 44 None
73
2024 2760 6469
119
8109
Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol iButa no1 s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol l-Octanol Ethanediol DEG 1,2-PropanedioI Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,l ,l-TCA TCE Perk. MCB
30
Reference
None None None
8217 8836 8838
None
4215
None None
6550 8407
None None None
1480a
48
Miscellaneous solvents
113
2192
Solute
Reference
7.2 4.8 4.6 3.9 4.2 3.8 10.3 2.5 1.3 1.5
1YJ3l1092 lYJ3l1092 6b1116 6b1239 6b1354 6b1386 6b1297 6a1177 71220 71406
1.3
71482
1.1 1.1 0.9 1.1 1.o 0.4 0.9
2a/183 2d355 2d512 2d157 2b1166 2fl307 2bl255
0.6 0.44 1.5
81267 W240 81140
1.9
81346
Partition coefficient
Reference
keotrope :%
Solute
"C Reference
V/W
Reference
Solute
Partition coefficient
Reference
~~
Ketones ketone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,CDioxane THF
j0
115
qone
Esters Me acetate Et acetate i-Propyl acetate lone n-Butyl acetate Cellosolve acetatt
+
8849
1.2 1.o 1.o
3 41181 1X/3/1092 3b/53 1
2769a
1.o
1X/3/ 1092
0.09 0.4
51118 81500
-
-
2.8
11469
5353
Jone
8850
Miscellaneous DMF DMAc DMSO Sulfolane cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-N itropropane Acetonitrile Furfuraldehyde Phenol Water
69 Vone
138
-
-
2779b
None
13 57
3139
183 94
8842 395
Miscellaneous solvents
2-Nitropropane Alternative names 2NR sec nitropropane Reference codes CAS number UN number
79 46 9 2608
Hazchem code EPA code
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
89 C3H7N1O2 120 -93 0.992
Cubic expansion coeff (per oC x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
28 428 5E-7
Lower explosive limit (ppm) Upper explosive limit (ppm)
26000 110000
2300 5
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
22000 3.18 16
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
300
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) Log1Oactivated carbon partition Log1Opartition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
1.1 30 0.74 1.392
1.76 0.5
1.35
Vapour pressure equation constants (Loglo. mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100)
2Y U171
10.4 1.9 25.5 37.3
7.4211 1625.43 237.6
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
10 1.5
8811 441 42 618 3.36 2.94 90.1
Miscellaneous solvents
keotrope I(%
Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TM P Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics Tetralin Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-Propanediol Glycol ethers PGME EGME EEE EGBE
Chlorinated MDC Chloroform Carbon tet. 1,2-EDC l,l,l-TCA TCE Perk. MCB
"C Reference
NIW
68 95 111 118
6284 6289 6291 6293
21 95 10 81 None 18 110 92 120
6292 6283 6281 6285 6290
None 6 78 25 96 4 82 52 112 33 105 18 99 85 120
1977 3978 627 1 6270 6275 6278 6276 6280
85
6279
3 21 47 75
None
Miscellaneous solvents
119
1114
Solute ?p"
Reference
6.5 6.6 4.0
1x/1/63 6a/510 6b/100
5.7 1.3
lxJ1163 71186
8.4 8.4
1x/1/63 1x/1/63
0.9 0.9 2.3
lx/1/63 1x/1/63 1x/1/63
Partition coefficient
Reference
1.10
V2186
~
ueotrope
:% Solute
"C Reference
VIW
Solute f
Reference
Partition coefficient
Reference
~
Ketones ketone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane THF
(one
6272
Jone
6282
Uone
6273
Esters Me acetate \one Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetatt
6274
Miscellaneous DMF DMAc DMSO Sulfolane
cs2
Acetic acid Ani Iine Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
-
-
71
89
4.0
1x/1/63
-
-
290
Miscellaneous solvents
Acetonitrile Alternative names Methyl cyanide, ACN, ethane nitrile, cyanomethane Reference codes CAS number UN number
75 05 8 1648
Hazchem code EPA code
2WE UOO3
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (20/4)
41 C2H3Nl 81.6 -44 0.782
Cubic expansion coeff (per oC x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
1.4 29.1 0.38 1.342
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
6 524 6E-10
Lower explosive limit (ppm) Upper explosive limit (ppm)
44000 160000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
4000 40 60 40
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
96000 1.42 71
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C o;oW/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
-0.34 1.22 2.15
Vapour pressure equation constants (Loglo. mmHg) Antoine equation A B C Cox Chart A B
7.33986 1482.29 250.523 7.12578 1322.7
Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100) Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
Total Total
11.9 3.2 37.5 46
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
2.04
7134 289 22 4.83 548 1.87 1.72 52.86
Miscellaneous solvents
~
Azeotrope
X% Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes Cg Aromatics TetraIin Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl ale. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-PropanedioI
"C
Reference
Solute 4"
Reference
35 57 69 77 80 82 69 62 73 81
2792 2800 2803 2810 2812 2815 281 1 2797 2795 2801 2804 2805
21.3 27 32.8 57 86
lxB1953 lx/lll5 6bD9 lx/l/l6 1x/1/16
44 22.0 2.5 4.5 5.0 5.5 7.3
lx/l/l6 lx/1/14 71124 71373 71465 71499 W31955
64 73 81 75
1925 2760 2768 2767
3.0 3.7 6.5 2.4 4.8 3.3 2.7
2d43 2a/298 1x/3/95 1
2f140
9.2
2f11
1.7
2dl109
wlw 11 28 46 66 41 33 34 76 None None
81 44 72 52 None None
2779
Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,1,l-TCA TCE Perk. MCB
2dll56 2fl300 2dl24 1
\one lone 17 65 79 49
1546 1433 1095 2757
1.2 1.4 4.4 1.4
81258 812 17 8/86 8/364
29
2280
3.4
81349
2794a
2.8
a381
Vone
Miscellaneous solvents
75
Partition coefficient
Reference
keotrope :%
Solute Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane THF
"C
VIW
Reference
Solute r"
Reference
lone !7
2762
1.o 1.2
3 41143 3W268
Jone
2778
3.2
3+4/499
Jone
2769a
1.4
1x/3/95 1
2763 2770 2788
1.1 1.6
51354 51455
1.8
51577
17.9
81320
1.o
81385
Esters Vone Me acetate 75 23 Et acetate 80 i-Propyl acetate 50 n-Butyl acetate Cellosolve acetatf Miscellaneous DMF DMAc DMSO Sulfolane CS2 Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
Vone
2765
Vone
2758a
2779b
1.8
1x/1/14
-
-
-
-
6.1
1181
76
226
Reference
+
Vone
34
Partition coefficient
Miscellaneous solvents
Furfuraldehyde Alternative names Furfural, furfurol. 2-furaldehyde, fural Reference codes CAS number UN number
9801 1199
Physical properties Molecular weight Empirical formula Boiling point {OC) Freezing point {OC) Specific gravity {20/4) Fire hazards Flash point {closed cup °C) Autoignition temperature {OC) Electrical conductivity Health hazards IDLH {ppm) OES-TWA OES-STEL Odour threshold {ppm)
1
Hazchem code EPA code
U125
96 C5H402 162 -37 1.160
Cubic expansion coeff (per oC x !03) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
1.06 45 1.4 1.524
62 315
Lower explosive Upper explosive
21000 193000
250 2 10 0.2
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
Aqueous effluent Solubility in water {25°C %w/w) Solubility of water in {25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water {w/w) Biological oxygen demand w/w {days) Theoretical oxygen demand w/w Vapour pressure equation constants (Loglo. mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole (D) Dielectric constant (20°C) Polarity (water 100) Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
11.2 3.6 41.9
limit (ppm) limit (ppm)
2400 3.33 1.81
8.4 5.0 +0.23 0.77 (5) 1.67
8.40200 2338.49 261.638
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
75
9216 539 36 5.03 660 3.17 2.48 83.23
Miscellaneous solvents
Azeotrope Solute Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes Cg Aromatics Tetralin Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-0ctanol Ethanediol DEG 1,2-PropanedioI Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. lI2-EDC 1,l,1-TCA TCE Perk. MCB
X% w/w
5 None
"C Reference
98
None None None None 10 139 60 155
878 1 8797
8763 8760 8776 8783 8785 8805
None None
Solute .9"
8764 8789 4214
14 151 None None 88 161
8753 6549 8406 8769
None None
1480 1140
3 4/50 3d137
11.7 8.9 8.0 1.6 1.7 2.5 2.8
3 4/59 3+4/55 3+4/45 3 +4/44 3d135 3+4/51 3 4/52
1.o 3.8
2c/140 2a1383
None None
Miscellaneous solvents
2191 8758
0.9 0.9 3.6 1.1 2.1 2.4
Partition coefficient
Reference
0.21 0.78 0.12 0.06
V2/558 V2/59 1 V3/115 V3/137
0.82
V2/42 1
+
7.1 6.0
2.4
5 156 None None
Reference
+
+
2f/l55
3d115 3+4/36 3+4/35
3d119 3+4/37
3d117
Azeotrope Solute Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,bDioxane THF
X% wlw
"C Reference
None
20
Solute
Reference
2.8
3d121
1.6
3d126
8788
6.1
3aI139
7574
1.6
3d123
1.6
3 +4/46
Partition coefficient
Reference
0.25 0.11
v2/47 1 v3/2 1
1.13
v2/539
0.34
V2/230
0.08
V3/182
-
-
8762
138
Esters Me acetate Et acetate None i-Propyl acetate n-Butyl acetate Cellosolve acetate None
8766
Miscellaneous DMF DMAc DMSO Sulfolane cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane ketonitrile Furfuraldehyde Phenol Water
None
3138
-
-
-
-
None 35
8761 394
0.8
11455
98
Miscellaneous solvents
Phenol Alternative names Hydroxy benzene, carbolic acid Reference codes CAS number UN number
108 95 2 1671
Hazchem code EPA code
Physical properties Molecular weight Empirical formula Boiling point (OC) Freezing point (OC) Specific gravity (41/4)
94 C6H60l 182 +41 1.058
Cubic expansion coeff (per °C x !03) Surface tension (@55°C dyn/cm) Absolute viscosity (@43°C cP) Refractive index (4! °C)
0.9 36.5 4.3 1.542
Fire hazards Flash point (closed cup OC) Autoignition temperature (OC) Electrical conductivity
79 715 2.7E-8
Lower explosive limit {ppm) Upper explosive limit {ppm)
17000 86000
Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
100 5 10 20
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
815
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) LoglO activated carbon partition LoglO partition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w
3.26 0.62
8.4 28.7 4.0 +1.47
2.38
Vapour pressure equation constants (Loglo. mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter Dipole {D) @40°C .2.2 Dielectric constant {60°C) .10.0 Polarity {water 100)
94.8
Thermal information Latent heat {cal/mol) Nett heat of combustion {kcal/gmol) Specific heat {cal/mol/OC) Critical pressure {MN/m2) Critical temperature {K) Latent heat of fusion {cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
6768 700 52 6.13 694 2750 3.55 2.68 83.14
11.3
6.9305 1382.65 159.5 7.84460 2045.1 Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
Miscellaneous solvents
seotrope .%
Solute Hydrocarbons n-Pentane n-Hexane +Heptane n-Octane n-Nonane n-Decane 2,2,4=TMP Cyclohexane Benzene Toluene Ethylbenzene Xylenes C9 Aromatics Tetralin Alcohols Methanol Ethanol n-Propanol i-Propanol +Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol l-Octanol Ethanediol DEG 1,2-PropanedioI Glycol ethers PGME EGME EEE EGBE Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1,l,1-TCA TCE Perk. MCB
"C Reference
I/W
1
125
10936 10959
15
168
11016
Sone
done done done
10920 10943 10944
Uone Uone 37 183 13 195 22 199
9749 9822 10895 10962 4240
36 183 Vone None 53 186
9962 6568 8426 10904
None
1155
None
10510
Miscellaneous solvents
Solute
Reference
10.9 13.6 12.8 19.8 26.8
1x/1/23 1 1x/1/233 1x/1/234 2x/382 1x/1/235
3.0 7.1 2.6 2.8
2b1383 1x/1/232 1x/1/231 1x/1/233
3.2 2.0
1x/1/234 2b/385
0.3
2b1370
2.6 0.8
2d/11
1.7 1.8 4.2 2.1
1x/1/230 1x/1/230 1x/1/230 1x/1/230
2fl339
Partition coefficient
Reference
0.37
VU125
0.13
V2/606
Azeotrope Solute Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane THF
X% w/w
"C Reference
None None
Solute 4"
Reference
5375 7370
0.33
2b/358
72
185
10889
0.11
2bl368
8
202
10939
0.3
2 b/38 1
0.46
2b/373
3.2
1x/1/230
Partition coefficient
Reference
10960
None
Esters Me acetate Et acetate i-Propyl acetate None n-Butyl acetate 185 Cellosolve acetatt 72
10896 10898
Miscellaneous DMF DMAc DMSO Sulfolane
cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Furfuraldehyde Phenol Water
42
185
10883
87
183
8842 8761
None
-
-
9
99
487
-
-
12.5
11496
Miscellaneous solvents
Water Alternative names Reference codes CAS number UN number Physical properties Molecular weight Empirical formula Boiling point (oC) Freezing point (oC) Specific gravity (20/4)
Hazchem code EPA code 18 H2O1 100 a 0.998
Cubic expansion coeff (per °C x 103) Surface tension (@20°C dyn/cm) Absolute viscosity (@25°C cP) Refractive index (25°C)
0.21 72.75 0.89 1.332
Fire hazards Flash point (closed cup °C) Lower explosive limit (ppm) Autoignition temperature (09 Upper explosive limit (ppm) Electrical conductivity (xl0siemen/cm) 5.0 (see Key to tables) Health hazards IDLH (ppm) OES-TWA OES-STEL Odour threshold (ppm)
Vapour concentration @21°C ppm Vapour density (relative to air) Vapour pressure @21°C mmHg POCP
25000 0.625 19
Aqueous effluent Solubility in water (25°C %w/w) Solubility of water in (25°C %w/w) Log1Oactivated carbon partition Log1Opartition in octanol/water (w/w) Biological oxygen demand w/w (days) Theoretical oxygen demand w/w Vapour pressure equation constants (Loglo. mmHg) Antoine equation A B C Cox chart A B Solvent properties Solubility parameter (call/2 cm312) Dipole (D) Dielectric constant (20°C) Polarity (water 100)
23.4 1.87 79.7 100
Thermal information Latent heat (cal/mol) Nett heat of combustion (kcal/gmol) Specific heat (cal/mol/OC) Critical pressure (MN/m2) Critical temperature (K) Latent heat of fusion (cal/mol) Van der Waals' volume Van der Waals' surface area Molar volume
9703 11.5 18 22.1 647 1432 0.92 1.40 18.02
8.07131 1730.63 233.426
Kauri butanol value Evaporationtime (ether = 1) Evaporationtime (BuAc = 1)
Miscellaneous solvents
4zeotrope I(%
Solute
"C
ulw
Hydrocarbons n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane 2,2,4-TM P Cyclohexane Benzene Toluene Ethylbenzene Xylenes Cg Aromatics Tetralin
1.4 5.6 13 25 40 51 11 8.4 8.8 19 33 40 :.50 80
Alcohols Methanol Ethanol n-Propanol i-Propanol n-Butanol i-Butanol s-Butanol n-Amyl alc. i-Amyl alc. Cyclohexanol 1-Octanol Ethanediol DEG 1,2-PropanedioI
None 4.0 28 12.6 42 33 27 54 50 70 90 None None None
Glycol ethers PGME EGME EEE EGBE
35 78 87 79
Chlorinated MDC Chloroform Carbon tet. 1,2-EDC 1I 1,l-TCA TCE Perk. MCB
1.5 2.8 4 8.7 4 6.2 16.5 28
Miscellaneous solvents
35 62 79 90 95 97 79 69 69 85 92 95 96 99
78 88 80 93 90 87 96 95 98 99
97 100 98 99 38 56 66 72 65 73 88 90
blubility of solite in X (ppm) B25"C 38 9.5 3 0.6 0.2 0.02 2.2 55 1800 520 165 200
Total Total Total Total 73000 87000 198000 17000 43000 6000 Total Total Total Total Total Total Total* 13000 8200 770 8100 1300 1100 150 490
Solute f
Reference
870 4500 11000 96 100
1~l411656 1x1411658 1x1411659 1x1411659
2150 9700 24000 3630
1x/4/1657 1x/4/1658 1x1411659 1x14/1659
2.18 5.80 15.0 13.7 114.1 42.3 24.9 22.7 60.6 115.4
1140 11153 11286 11329 11407 11440 11420 1x/4/1656 1d382 11514
H atrn/mole fraction 70250 71730 150000 274000 330000 262000 186000 10700 309 3 53 447 313
0.39 0.45 0.51 0.62 0.44 0.35 0.60 0.68
Upper CST, "C
306
<-23 <-23 127 129 110 182 184.7
0.88 0.23 2.23 0.61
6.9 14.8
ld173 1a/353 la1337
<20 <20 <20
la1450 11526
<20 <20 128
336 665 6400 626 5500 5100
1x1411644 1x1411644 1x/4/1648 1x/4/1647 1x1411646
3000
1x1411657
111
138 225 1634 65 1666 648 1492 25.2
>220
Azeotrope
X% Solute
"C
WIW
hlubility of solite in X (ppm) 925°C
Solute +f
Reference
10.2 27.2 15.1 38.3 1.6 1277
11237 11363 1bl337 1/511 1d379 1/46
98.2 4.3
la1257 11525
8.2 24.3
11382 1xl411653
0.38 6.0
23.6 108 242 995
11264 1%I411653 1x/4/1656 11516
5.15
Ketones Acetone MEK MlBK Cyclohexanone NMP Acetophenone
11 24 55
73 88 96
None 82
98
Tota I !60000t 17000 23000 Tota I 5500
Ethers Diethyl ether DlPE Dibutyl ether MTBE 1,4-Dioxane THF
1.3 4.5 33 3 18 5.3
34 62 93 52 88 64
69000 12000 300 43000 Total Total$
Esters Me acetate Et acetate i-Propyl acetate n-Butyl acetate Cellosolve acetate
5 8.5 10 29 50
56 70 77 90 97
'45000 77000 29000 7000 '29000
Miscellaneous DMF DMAc DMSO Sulfolane
None None None None
cs2
Acetic acid Aniline Nitrobenzene Morpholine Pyridine 2-Nitropropane Acetonitrile Fudura ldehyde Phenol
None
2.8
Total Total Total TotaI
43
None
41 87 86 99 None 43 94 29 89 15.2 76 65 98 91 100
Total
35000 1900 Total Total 17600 Total 84000 84000
2.2 1.6 0.43 14.8 2100 3.6 22.6
11276 1d402 11199 ld316 3300 11102 11499
1.05 42.8
la1327 11469
32.5 50.6 44.0
1/81 11455 11496
H AtmIMole fraction
2.38 2.42 3.0 0.82
Upper CST, "C
<-11 139
220 48.3 96.3
202
C-1 5 138
108
<25 1XI411646 0.07 0.16 1.03
0.61 6720 1.12 2.35
1067 C-27 167
-0.9 122 66
Lower critical solution temperatures *Butyl cellosolve (DEGBE) 55°C tMethyl ethyl ketone (MEK) -6°C STetrahydrofuran (THF) 72°C Miscellaneous solvents
1. Perry's Chemical Engineers' Handbook.
5. Weast, R. C. (1975) CRC Handbook of
McGraw-Hill, New York. The most complete collection of information on industrial chemical properties and chemical engineering theory and practice. 2. Dechema Chemistry Data Series. Frankfurt. a. Volume I. Vapor-Liquid Equilibrium Data Collection. Nineteen parts by 1996. A very large collection of binary and ternary vapour-liquid data and activity coefficients for organic materials commonly used in industry. The majority of the VLE of binary mixtures are shown in graphic form. All solvents listed have their Antoine constants included and the values of their Van der Waals surface area and volume. b. Volume V. Liquid-Liquid Equilibrium Data Collection. Four parts by 1996. The liquid ternary mixtures are shown in graphic form which allow the possibility of extraction of a solute from one solvent to another to be estimated. c. Volume IX. Activity Coefficients at lnfinite Dilution. Four parts by 1996. A very large collection of activity coefficients of liquid solutes in commonly used solvents and stationary phases. In all the above 2 7 books the references cover the original research paper. Each book contains about 550 pages. 3. Riddick, J. A. and Burger, W. B. (1986) Organic Solvents, 4th edn. Volume 2 of Techniques of Chemistry Series. John Wiley, New York. A good source of physical data and laboratory purification methods for solvents. Hazards and stabilizershnhibitors for laboratory work are included. 4. Horsley, L. H. (1973) Azeotropic data 111. Advances in Chemistry Series No. 116. American Chemical Society, Washington DC. A most comprehensive collection of azeotropes with the original research papers for all azeotropes listed.
Chemistry and Physics (The Rubber Handbook). CRC Press, Boca Raton, FL. Although many later editions have been printed those numbered 55 and less contain information on solvent azeotropes which are not included in later editions. However, the later editions contain a large amount of useful information on solvents. Dreisbach, R. R. (1952) Pressure-VolumeTemperature Relationships of Organic Compounds, 3rd edn. Handbook Publishers. Contains Cox chart constants and tables of pressure-temperature data for individual compounds. Horvath, A. L. (1982) Halogenated Hydrocarbons Solubility and Miscibility with Water. Marcel Dekker, New York. A comprehensive coverage of water-chlorinated hydrocarbons and the mechanism of their miscibility. Flick, F. W. (1993) lndustrial Solvents Handbook, 4th edn. Noyes Data Corporation, Park Ridge, NJ. A collection of information of the physical properties of commercial solvents, but nothing on their fire and health hazards. De Renzo, D. J. (1986) Solvents Safety Handbook. Noyes Data Corporation, Park Ridge, NJ. For every commonly used solvent this book lists the essential physical properties, health data and transport safety information. Sax, N. I. (1984) Dangerous Properties of lndustrial Materials, 6th edn. Van Nostrand Reinhold, New York. The definitive book on the toxicity of solvents and other organic chemicals. Lide, D. R. (1995) Handbook of Organic Solvents. CRC Press, Boca Raton, FL. A compilation of many commonly used solvents with particular stress on analysis and thermodynamic properties.
6.
7.
8.
9.
10.
11.
12. Gallant, R. W. (1993)Physical Properties of Hydrocarbons. Gulf Publishing Co. Three volumes. All the properties of the simpler solvents and hydrocarbons up to Clo that are required for engineering design purposes plotted over normal working temperature ranges. 13. Solubility Data Series (1979 and continuing). Pergamon, Oxford. Over 30 volumes. Very detailed survey of the solubility of materials in water including paraffins, aromatic hydrocarbons, esters and alcohols and of the solubility of water in them. 14. Reichardt, C. (1988)Solvents and Solvent Effects in Organic Chemistry, 2nd edn. VCH Verlagsgeseilschaft, Weihheim. Useful for comparing the effects of various solvents and their method of action.
15. Reid, R. C., Prausssnitz, J. M. and Poling, B. E. (1987)Properties of Gases and Liquids, 4th edn. McGraw-Hill, New York. Very useful basis for methods of estimating properties that are not available from experiment. 16. Verschueren. Handbook of Environmental Data on Organic Chemicals. Van Nostrand Reinhold, New York. A comprehensive collection on the fate of materials in the environment. 17. Hansch, C. and Leo, A. (1979)Substituent Constants for Correlation Analysis in Chemistry and Biology. John Wiley, New York. Pomona College loglo P listings.