Chemical Properties of Ethyl Acetate (CAS 141-78-6)

Ethyl Acetate

InChI
InChI=1S/C4H8O2/c1-3-6-4(2)5/h3H2,1-2H3
InChI Key
XEKOWRVHYACXOJ-UHFFFAOYSA-N
Formula
C4H8O2
SMILES
CCOC(C)=O
Molecular Weight1
88.11
CAS
141-78-6
Other Names
  • 1-Acetoxyethane
  • Acetic acid, ethyl ester
  • Acetic ether
  • Acetidin
  • Acetoxyethane
  • Aethylacetat
  • CH3COOC2H5
  • Essigester
  • Ethyl acetic ester
  • Ethyl ester of acetic acid
  • Ethylacetaat
  • Ethyle (acetate d')
  • Ethylester kyseliny octove
  • Etile (acetato di)
  • NSC 70930
  • Rcra waste number U112
  • UN 1173
  • Vinegar naphtha
  • ac. acetic ethyl ester
  • ethyl ethanoate
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Physical Properties

Property Value Unit Source
ω [0.3610; 0.3630]   Show Hide
ω 0.3630 PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω 0.3610 ChemSep v8.3 pure component data Compiled value
ω 0.3620 KDB
PAff 835.70 kJ/mol NIST
Tig [699.15; 699.82] K Show Hide
Tig 699.82 K KDB
Tig 699.15 K NCMS SOLV-DB
BasG [799.90; 804.70] kJ/mol Show Hide
BasG 804.70 kJ/mol NIST
BasG 799.90 ± 0.20 kJ/mol NIST
ΔcH°liquid [-2256.00; -2235.40] kJ/mol Show Hide
ΔcH°liquid -2238.54 ± 0.48 kJ/mol NIST
ΔcH°liquid -2235.40 ± 3.90 kJ/mol NIST
ΔcH°liquid -2256.00 kJ/mol NIST
ΔcH°liquid -2246.00 kJ/mol NIST
μ [1.78; 1.90] debye Show Hide
μ 1.78 debye ChemSep v8.3 pure component data Compiled value
μ 1.90 debye KDB
η [0.0004260; 0.0004370] Pa×s Show Hide
η 0.0004370 Pa×s A volumetric and viscosity study for the binary mixtures of 1-hexyl-3-methylimidazolium tetrafluoroborate with some molecular solvents
η 0.0004274 Pa×s Densities and Viscosities of Binary Liquid Mixtures of Trichloroethylene and Tetrachloroethylene with Some Polar and Nonpolar Solvents
η 0.0004260 Pa×s Densities and Viscosities of Ternary Mixtures of Cyclohexane + Cyclohexanone + Some Alkyl Acetates at 298.15 K
εr 6.02 NCMS SOLV-DB
LFL 2.20 % in Air KDB
UFL 9.00 % in Air KDB
Tflash,cc [269.15; 285.93] K Show Hide
Tflash,cc 285.93 K KDB
Tflash,cc 269.15 K NCMS SOLV-DB
Tflash,oc 268.71 K KDB
ΔfG° [-328.00; -327.60] kJ/mol Show Hide
ΔfG° -328.00 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfG° -327.60 kJ/mol KDB
Rg 3.3480 KDB
ΔfH°gas [-446.90; -443.20] kJ/mol Show Hide
ΔfH°gas -444.50 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfH°gas -443.20 kJ/mol KDB
ΔfH°gas -445.43 ± 0.84 kJ/mol NIST
ΔfH°gas -444.80 ± 0.40 kJ/mol NIST
ΔfH°gas -443.80 kJ/mol NIST
ΔfH°gas -446.90 kJ/mol NIST
ΔfH°liquid [-482.00; -478.82] kJ/mol Show Hide
ΔfH°liquid -480.57 ± 0.79 kJ/mol NIST
ΔfH°liquid -479.86 ± 0.46 kJ/mol NIST
ΔfH°liquid -478.82 ± 0.73 kJ/mol NIST
ΔfH°liquid -482.00 ± 4.00 kJ/mol NIST
ΔfusH° 10.48 kJ/mol Joback Calculated Property
ΔvapH° [32.30; 35.69] kJ/mol Show Hide
ΔvapH° 35.61 kJ/mol NCMS SOLV-DB
ΔvapH° 35.69 kJ/mol NIST
ΔvapH° 35.00 kJ/mol NIST
ΔvapH° 35.10 kJ/mol NIST
ΔvapH° 35.10 ± 0.20 kJ/mol NIST
ΔvapH° 35.10 kJ/mol NIST
ΔvapH° 35.60 ± 0.10 kJ/mol NIST
ΔvapH° 35.10 ± 0.20 kJ/mol NIST
ΔvapH° 35.10 ± 0.20 kJ/mol NIST
ΔvapH° Outlier 32.30 ± 0.42 kJ/mol NIST
IE [9.90; 10.45] eV Show Hide
IE 10.01 ± 0.05 eV NIST
IE 10.01 ± 0.05 eV NIST
IE 10.00 ± 0.10 eV NIST
IE 10.16 eV NIST
IE 9.90 ± 0.05 eV NIST
IE 10.24 eV NIST
IE 10.11 ± 0.02 eV NIST
IE 10.09 ± 0.02 eV NIST
IE Outlier 10.45 eV NIST
IE 9.90 eV NIST
log10WS [-0.04; -0.04]   Show Hide
log10WS -0.04 Aq. Solubility Prediction
log10WS -0.04 Estimated Solubility
logPoct/wat 0.730 NCMS SOLV-DB
McVol 74.660 ml/mol McGowan Calculated Property
NFPA Fire [%!d(float64=3); %!d(float64=3)]   Show Hide
NFPA Fire 3 KDB
NFPA Fire 3 NCMS SOLV-DB
NFPA Health 1 NCMS SOLV-DB
NFPA Safety 0 NCMS SOLV-DB
Pc [3830.00; 4280.00] kPa Show Hide
Pc 3900.00 kPa Critical Properties of the Reacting Mixture in the Esterification of Acetic Acid with Ethanol
Pc 3870.00 kPa IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Pc 3830.09 kPa PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc 3830.00 kPa ChemSep v8.3 pure component data Compiled value
Pc 3882.00 kPa KDB
Pc 3882.00 ± 3.87 kPa NIST
Pc 3830.00 ± 81.06 kPa NIST
Pc 3851.70 ± 40.00 kPa NIST
Pc 4018.00 ± 202.65 kPa NIST
Pc Outlier 4280.00 ± 405.30 kPa NIST
Ptriple 1.43e-03 kPa ChemSep v8.3 pure component data Compiled value
ρc [299.29; 308.10] kg/m3 Show Hide
ρc 307.66 ± 5.29 kg/m3 NIST
ρc 308.10 ± 4.41 kg/m3 NIST
ρc 299.29 ± 5.29 kg/m3 NIST
Inp [554.00; 634.00]   Show Hide
Inp 611.00 NIST
Inp 602.00 NIST
Inp 584.00 NIST
Inp 608.00 NIST
Inp 592.00 NIST
Inp 615.00 NIST
Inp 600.00 NIST
Inp 620.00 NIST
Inp Outlier 568.00 NIST
Inp 612.00 NIST
Inp 600.00 NIST
Inp 600.00 NIST
Inp 605.00 NIST
Inp 600.00 NIST
Inp 578.95 NIST
Inp 600.00 NIST
Inp 609.70 NIST
Inp 604.40 NIST
Inp 611.70 NIST
Inp 605.10 NIST
Inp 600.80 NIST
Inp 599.30 NIST
Inp 597.30 NIST
Inp Outlier 563.00 NIST
Inp 600.00 NIST
Inp 607.50 NIST
Inp 605.70 NIST
Inp 602.40 NIST
Inp 607.00 NIST
Inp 577.00 NIST
Inp 607.00 NIST
Inp 613.00 NIST
Inp 577.00 NIST
Inp Outlier 572.00 NIST
Inp 590.00 NIST
Inp 594.00 NIST
Inp Outlier 567.00 NIST
Inp 595.70 NIST
Inp 596.00 NIST
Inp 592.00 NIST
Inp 592.00 NIST
Inp 602.00 NIST
Inp Outlier 571.00 NIST
Inp 587.00 NIST
Inp 600.00 NIST
Inp 601.00 NIST
Inp 600.00 NIST
Inp 595.00 NIST
Inp 618.00 NIST
Inp 600.00 NIST
Inp 579.00 NIST
Inp 580.00 NIST
Inp 611.00 NIST
Inp 600.00 NIST
Inp 589.00 NIST
Inp 592.00 NIST
Inp 612.00 NIST
Inp 612.00 NIST
Inp 610.00 NIST
Inp 577.00 NIST
Inp 613.00 NIST
Inp 612.00 NIST
Inp 605.00 NIST
Inp 615.00 NIST
Inp 615.00 NIST
Inp 615.00 NIST
Inp 608.00 NIST
Inp 612.00 NIST
Inp 596.00 NIST
Inp 598.00 NIST
Inp 609.00 NIST
Inp 578.00 NIST
Inp 609.10 NIST
Inp 615.00 NIST
Inp 581.00 NIST
Inp 581.00 NIST
Inp 612.00 NIST
Inp 599.00 NIST
Inp 601.00 NIST
Inp 581.00 NIST
Inp 581.00 NIST
Inp 614.00 NIST
Inp 601.00 NIST
Inp 626.00 NIST
Inp 614.00 NIST
Inp 617.00 NIST
Inp 612.00 NIST
Inp 597.00 NIST
Inp 600.00 NIST
Inp 601.00 NIST
Inp 602.00 NIST
Inp 620.00 NIST
Inp 600.00 NIST
Inp 599.00 NIST
Inp 602.00 NIST
Inp 594.00 NIST
Inp 624.00 NIST
Inp 603.00 NIST
Inp 603.00 NIST
Inp 613.00 NIST
Inp 578.00 NIST
Inp 621.00 NIST
Inp 610.00 NIST
Inp 614.00 NIST
Inp 623.00 NIST
Inp 605.00 NIST
Inp Outlier 628.00 NIST
Inp 612.00 NIST
Inp 612.00 NIST
Inp 600.00 NIST
Inp 590.00 NIST
Inp 594.00 NIST
Inp 593.00 NIST
Inp 591.00 NIST
Inp 590.00 NIST
Inp 587.00 NIST
Inp 594.00 NIST
Inp 598.00 NIST
Inp 608.00 NIST
Inp Outlier 554.00 NIST
Inp 611.00 NIST
Inp 612.00 NIST
Inp 606.00 NIST
Inp 604.00 NIST
Inp 607.00 NIST
Inp 602.00 NIST
Inp 605.00 NIST
Inp 593.00 NIST
Inp Outlier 628.00 NIST
Inp 614.00 NIST
Inp 584.00 NIST
Inp 594.00 NIST
Inp 597.00 NIST
Inp 584.00 NIST
Inp 608.00 NIST
Inp 608.00 NIST
Inp 584.00 NIST
Inp Outlier 628.00 NIST
Inp Outlier 628.00 NIST
Inp 615.00 NIST
Inp 592.00 NIST
Inp 615.00 NIST
Inp 612.00 NIST
Inp Outlier 630.00 NIST
Inp 595.00 NIST
Inp 615.00 NIST
Inp 614.00 NIST
Inp 614.00 NIST
Inp 596.00 NIST
Inp 600.00 NIST
Inp 600.00 NIST
Inp 601.82 NIST
Inp 615.00 NIST
Inp 597.00 NIST
Inp 588.00 NIST
Inp 620.00 NIST
Inp 583.00 NIST
Inp 592.00 NIST
Inp 601.00 NIST
Inp 602.00 NIST
Inp Outlier 568.00 NIST
Inp 580.00 NIST
Inp 590.00 NIST
Inp 600.00 NIST
Inp 614.00 NIST
Inp 612.00 NIST
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Inp 600.00 NIST
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Inp 600.00 NIST
Inp 600.00 NIST
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Inp 594.00 NIST
Inp 595.00 NIST
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Inp 604.00 NIST
Inp 600.00 NIST
Inp 600.00 NIST
Inp 605.00 NIST
Inp 605.00 NIST
Inp 615.00 NIST
Inp 603.00 NIST
Inp 610.00 NIST
Inp Outlier 633.00 NIST
Inp 607.00 NIST
Inp 599.00 NIST
Inp Outlier 628.00 NIST
Inp 609.00 NIST
Inp 605.00 NIST
Inp 616.00 NIST
Inp 592.00 NIST
Inp 600.00 NIST
Inp 613.00 NIST
Inp 584.00 NIST
Inp 589.00 NIST
Inp 613.00 NIST
Inp 592.00 NIST
Inp 605.00 NIST
Inp 592.00 NIST
Inp 612.00 NIST
Inp Outlier 634.00 NIST
Inp 605.00 NIST
Inp 615.00 NIST
Inp 615.00 NIST
Inp 602.00 NIST
Inp 609.00 NIST
Inp 611.00 NIST
Inp 612.00 NIST
Inp 612.00 NIST
Inp 621.00 NIST
Inp 595.00 NIST
Inp 613.00 NIST
Inp 611.00 NIST
Inp 613.00 NIST
Inp 613.00 NIST
Inp 592.00 NIST
Inp 615.00 NIST
Inp 592.00 NIST
Inp 595.00 NIST
Inp 601.00 NIST
Inp 600.00 NIST
Inp 609.00 NIST
Inp 602.00 NIST
Inp 598.00 NIST
Inp 620.00 NIST
Inp 590.00 NIST
Inp 615.00 NIST
Inp 616.00 NIST
Inp 602.00 NIST
Inp 604.00 NIST
Inp 600.00 NIST
Inp 603.00 NIST
Inp 598.00 NIST
Inp 596.00 NIST
Inp 600.00 NIST
Inp 600.00 NIST
Inp 614.00 NIST
Inp 600.00 NIST
Inp 595.00 NIST
Inp 595.00 NIST
Inp 595.00 NIST
Inp 603.00 NIST
Inp 593.00 NIST
Inp 600.00 NIST
Inp 611.00 NIST
Inp 616.00 NIST
Inp 596.00 NIST
Inp 607.00 NIST
Inp 578.00 NIST
Inp 614.00 NIST
Inp 601.00 NIST
Inp 587.00 NIST
Inp 595.00 NIST
Inp 589.00 NIST
Inp Outlier 633.00 NIST
Inp 616.00 NIST
Inp 598.00 NIST
Inp 603.00 NIST
Inp 596.00 NIST
Ip [850.00; 921.00]   Show Hide
Ip 902.00 NIST
Ip 875.00 NIST
Ip 908.00 NIST
Ip 881.00 NIST
Ip 880.00 NIST
Ip 906.00 NIST
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Ip 890.00 NIST
Ip 885.00 NIST
Ip 884.00 NIST
Ip 887.00 NIST
Ip 906.00 NIST
Ip 874.00 NIST
Ip 880.00 NIST
Ip 880.00 NIST
Ip 870.00 NIST
Ip Outlier 856.00 NIST
Ip Outlier 858.00 NIST
Ip 882.00 NIST
Ip 889.00 NIST
Ip 895.00 NIST
Ip 900.00 NIST
Ip Outlier 917.00 NIST
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Ip 863.00 NIST
Ip 891.00 NIST
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Ip 887.00 NIST
Ip 888.00 NIST
Ip 888.00 NIST
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Ip 884.00 NIST
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Ip 870.00 NIST
Ip 872.00 NIST
Ip 867.00 NIST
Ip 867.00 NIST
Ip 881.00 NIST
Ip 890.00 NIST
Ip 893.00 NIST
Ip Outlier 854.00 NIST
Ip 882.00 NIST
Ip 892.00 NIST
Ip 881.00 NIST
Ip 866.00 NIST
Ip 899.00 NIST
Ip 893.00 NIST
Ip 891.00 NIST
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Ip 904.00 NIST
Ip 900.00 NIST
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Ip 888.00 NIST
Ip 912.40 NIST
Ip 900.00 NIST
Ip 868.00 NIST
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Ip 878.00 NIST
Ip 903.00 NIST
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Ip 900.00 NIST
Ip 905.00 NIST
Ip 872.00 NIST
Ip 900.00 NIST
Ip 899.00 NIST
Ip 890.00 NIST
Ip 890.00 NIST
Ip Outlier 856.00 NIST
Ip 885.00 NIST
Ip 891.00 NIST
Ip 901.00 NIST
Ip 892.00 NIST
Ip 890.00 NIST
Ip 903.00 NIST
Ip Outlier 921.00 NIST
Ip 882.00 NIST
Ip 893.00 NIST
Ip Outlier 850.00 NIST
Ip 884.00 NIST
Ip 889.00 NIST
Ip Outlier 920.00 NIST
Ip 890.00 NIST
Ip 885.00 NIST
Ip Outlier 850.00 NIST
Ip Outlier 850.00 NIST
Ip 861.00 NIST
Ip 870.00 NIST
Ip 882.00 NIST
Ip 894.00 NIST
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Ip 885.00 NIST
Ip 908.00 NIST
Ip Outlier 854.00 NIST
Ip 878.00 NIST
Ip 890.00 NIST
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Ip 912.00 NIST
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Ip 872.70 NIST
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Ip 888.00 NIST
Ip 891.00 NIST
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Ip 872.00 NIST
Ip 880.00 NIST
Ip 883.00 NIST
Ip 882.00 NIST
Ip Outlier 857.00 NIST
Ip Outlier 858.00 NIST
Ip 862.00 NIST
Ip 907.00 NIST
Ip 870.00 NIST
Ip 885.00 NIST
Ip 870.00 NIST
Ip Outlier 915.00 NIST
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Ip 909.00 NIST
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Ip 878.00 NIST
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Ip 866.00 NIST
Ip 866.00 NIST
Ip 898.00 NIST
Ip Outlier 853.00 NIST
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Ip 898.00 NIST
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Ip 889.00 NIST
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Ip 870.00 NIST
Ip 872.00 NIST
Ip 890.00 NIST
Ip 874.00 NIST
Ip Outlier 858.00 NIST
Ip Outlier 917.00 NIST
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S°gas 362.75 J/mol×K NIST
S°liquid 259.40 J/mol×K NIST
Tboil [346.65; 375.00] K Show Hide
Tboil 350.27 K Vapor liquid equilibria for the quaternary reactive system ethyl acetate + ethanol +water + acetic acid and some of the constituent binary systems at 101.3 kPa
Tboil 350.24 K Vapor liquid equilibria for the binary mixtures of 2,3-butanediol with n-butanol, n-butyl acetate, and ethyl acetate at 101.3 kPa
Tboil 350.24 K Liquid-liquid equilibria of water + 3-hydroxy-2-butanone + ethyl ethanoate
Tboil 350.20 K Solubility and tie-line data for ternary aqueous mixtures of cyclopentanol with organic solvents at T = 298.2 K: Experiments and NRTL model
Tboil 350.15 K The isobaric vapor liquid equilibria of ethyl acetate p acetonitrile p bis(trifluoromethylsulfonyl)imide-based ionic liquids at 101.3 kPa
Tboil 350.29 K Isobaric vapor-liquid equilibrium of a ternary system of ethyl acetate + propyl acetate + dimethyl sulfoxide and binary systems of ethyl acetate + dimethyl sulfoxide and propyl acetate + dimethyl sulfoxide at 101.3 kPa
Tboil 350.35 K Isobaric Vapor - Liquid Equilibrium for Ethyl acetate + Methanol + Ionic Liquids Ternary systems at 101.3 kPa
Tboil 350.16 K Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil 350.20 K Isobaric Vapor Liquid Equilibrium for Three Binary Systems of Acetaldehyde + Ethanol, Ethyl Acetate, 1-Butanol at 101.3 kPa
Tboil 349.95 K Effect of Ionic Liquids on the Binary Vapor-Liquid Equilibrium of Ethyl Acetate + Methanol System at 101.3 kPa
Tboil 350.28 K Isobaric Vapor-Liquid Phase Equilibrium Measurements for Allyl Alcohol with Chloroform, Ethyl Acetate, and Methyl Propionate at 101.3 kPa
Tboil 350.25 K Isobaric Vapor-Liquid Equilibria and Excess Quantities for Binary Mixtures of an Ethyl Ester + tert-Butanol and a New Approach to VLE Data Processing
Tboil 350.15 K Vapor-Liquid Equilibrium of Binary Mixtures Containing Ethyl Acetate + 2-Methyl-1-propanol and Ethyl Acetate + 2-Methyl-1-butanol at 101.3 kPa
Tboil 350.21 K Volumetric Behavior and Saturated Pressure for Carbon Dioxide + Ethyl Acetate at a Temperature of 313.15 K
Tboil 350.15 K Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Tboil 350.19 K Experimental Determination of Vapor Liquid Equilibria. Binary Systems of Methyl Acetate, Ethyl Acetate, and Propyl Acetate with 1-Propanol at 0.6 MPa
Tboil 350.21 K ChemSep v8.3 pure component data Compiled value
Tboil 350.26 K KDB
Tboil 350.21 K NCMS SOLV-DB
Tboil 350.13 ± 0.30 K NIST
Tboil 350.20 K NIST
Tboil 350.00 K NIST
Tboil 350.25 ± 0.30 K NIST
Tboil 349.25 ± 0.30 K NIST
Tboil 350.25 ± 0.30 K NIST
Tboil 350.25 ± 0.30 K NIST
Tboil 350.30 ± 0.20 K NIST
Tboil 350.30 K NIST
Tboil 350.30 ± 0.50 K NIST
Tboil 350.25 ± 0.30 K NIST
Tboil 350.19 ± 0.50 K NIST
Tboil 350.25 ± 0.30 K NIST
Tboil 350.30 ± 0.20 K NIST
Tboil 350.30 ± 0.30 K NIST
Tboil Outlier 375.00 ± 2.00 K NIST
Tboil 350.35 K NIST
Tboil 350.05 ± 0.30 K NIST
Tboil 350.21 ± 0.50 K NIST
Tboil 350.25 ± 0.50 K NIST
Tboil 350.25 ± 0.30 K NIST
Tboil 350.00 ± 2.00 K NIST
Tboil 350.29 ± 0.15 K NIST
Tboil 350.15 ± 2.00 K NIST
Tboil 350.25 ± 0.30 K NIST
Tboil 350.25 ± 0.30 K NIST
Tboil 350.25 ± 0.50 K NIST
Tboil 350.25 ± 0.30 K NIST
Tboil 350.65 ± 2.00 K NIST
Tboil 349.65 ± 2.00 K NIST
Tboil 352.15 ± 2.00 K NIST
Tboil 350.25 ± 1.00 K NIST
Tboil 350.30 ± 1.00 K NIST
Tboil 350.30 ± 1.00 K NIST
Tboil 349.97 ± 2.00 K NIST
Tboil 351.15 ± 2.00 K NIST
Tboil 350.45 ± 1.00 K NIST
Tboil 350.25 ± 1.00 K NIST
Tboil 350.30 ± 0.40 K NIST
Tboil 349.15 ± 2.00 K NIST
Tboil 349.65 ± 2.50 K NIST
Tboil 350.26 ± 0.06 K NIST
Tboil 350.30 ± 0.15 K NIST
Tboil 350.00 ± 2.00 K NIST
Tboil 350.30 ± 0.50 K NIST
Tboil 350.15 ± 2.00 K NIST
Tboil 349.95 ± 2.00 K NIST
Tboil 350.20 ± 0.50 K NIST
Tboil 350.30 ± 0.20 K NIST
Tboil 350.25 ± 0.50 K NIST
Tboil 350.21 ± 0.50 K NIST
Tboil 349.65 ± 2.00 K NIST
Tboil 350.30 ± 0.50 K NIST
Tboil 350.30 ± 0.50 K NIST
Tboil 350.30 ± 0.50 K NIST
Tboil 350.45 ± 0.60 K NIST
Tboil 350.30 ± 0.30 K NIST
Tboil 350.25 ± 1.00 K NIST
Tboil 350.30 ± 0.20 K NIST
Tboil 350.25 ± 1.00 K NIST
Tboil 349.90 ± 0.20 K NIST
Tboil 350.30 ± 0.50 K NIST
Tboil 350.30 ± 0.20 K NIST
Tboil 350.30 ± 0.50 K NIST
Tboil 350.30 ± 2.00 K NIST
Tboil 350.20 ± 2.00 K NIST
Tboil 350.30 ± 2.00 K NIST
Tboil 350.10 ± 2.00 K NIST
Tboil 350.70 ± 2.00 K NIST
Tboil 350.65 ± 2.00 K NIST
Tboil 346.65 ± 3.00 K NIST
Tboil 347.45 ± 2.00 K NIST
Tboil 347.45 ± 2.00 K NIST
Tc [513.00; 548.90] K Show Hide
Tc 523.29 K Development of a Predictive Equation of State for CO2 + Ethyl Ester Mixtures Based on Critical Points Measurements
Tc 523.30 K IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Tc 523.20 K PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc 523.20 K ChemSep v8.3 pure component data Compiled value
Tc 523.30 K KDB
Tc 523.20 K NIST
Tc 523.30 ± 0.05 K NIST
Tc 523.30 ± 1.00 K NIST
Tc 523.30 ± 1.00 K NIST
Tc Outlier 548.90 ± 20.00 K NIST
Tc 522.70 ± 2.00 K NIST
Tc 513.00 ± 6.00 K NIST
Tfus [189.15; 190.77] K Show Hide
Tfus 189.15 K Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus 189.60 K ChemSep v8.3 pure component data Compiled value
Tfus 189.50 K KDB
Tfus 189.25 K Aq. Solubility Prediction
Tfus 189.55 K NCMS SOLV-DB
Tfus 189.55 K NIST
Tfus 189.18 ± 0.05 K NIST
Tfus 189.35 ± 0.30 K NIST
Tfus 189.55 ± 0.10 K NIST
Tfus 189.77 ± 0.30 K NIST
Tfus Outlier 190.77 ± 0.20 K NIST
Tfus 190.00 ± 2.00 K NIST
Ttriple [182.56; 189.60] K Show Hide
Ttriple 182.56 K Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple 189.60 K ChemSep v8.3 pure component data Compiled value
Ttriple 189.30 ± 0.05 K NIST
Ttriple 189.30 ± 0.20 K NIST
Ttriple 189.30 ± 0.20 K NIST
UQi 3.12 ChemSep v8.3 pure component data Compiled value
URi 3.48 ChemSep v8.3 pure component data Compiled value
Vc [0.286; 0.286] m3/kmol Show Hide
Vc 0.286 m3/kmol IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Vc 0.286 m3/kmol PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc 0.286 m3/kmol ChemSep v8.3 pure component data Compiled value
Vc 0.286 m3/kmol KDB
Zc [0.2520000; 0.2551730]   Show Hide
Zc 0.2550000 IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Zc 0.2520000 ChemSep v8.3 pure component data Compiled value
Zc 0.2551730 KDB
Zra 0.25 KDB

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,gas [125.82; 149.47] J/mol×K [360.00; 450.00] Show Hide
Cp,gas 125.82 J/mol×K 360.00 NIST
Cp,gas 131.06 J/mol×K 380.00 NIST
Cp,gas 136.22 J/mol×K 400.00 NIST
Cp,gas 142.80 J/mol×K 425.00 NIST
Cp,gas 149.47 J/mol×K 450.00 NIST
Cp,liquid [157.70; 170.59] J/mol×K [290.00; 303.61] Show Hide
Cp,liquid 157.70 J/mol×K 290.00 NIST
Cp,liquid 169.20 J/mol×K 293.60 NIST
Cp,liquid 169.50 J/mol×K 298.10 NIST
Cp,liquid 168.94 J/mol×K 298.15 NIST
Cp,liquid 169.30 J/mol×K 298.15 NIST
Cp,liquid 169.06 J/mol×K 298.15 NIST
Cp,liquid 169.60 J/mol×K 298.15 NIST
Cp,liquid 169.60 J/mol×K 298.15 NIST
Cp,liquid 167.40 J/mol×K 298.15 NIST
Cp,liquid 170.59 J/mol×K 298.32 NIST
Cp,liquid 168.82 J/mol×K 303.61 NIST
η [0.0002750; 0.0004520] Pa×s [293.15; 343.15] Show Hide
η 0.0004520 Pa×s 293.15 Density, dynamic viscosity, and derived properties of binary mixtures of methanol or ethanol with water, ethyl acetate, and methyl acetate at T = (293.15, 298.15, and 303.15) K
η 0.0004520 Pa×s 293.15 Dynamic Viscosities, Densities, and Speed of Sound and Derived Properties of the Binary Systems Acetic Acid with Water, Methanol, Ethanol, Ethyl Acetate and Methyl Acetate at T = (293.15, 298.15, and 303.15) K at Atmospheric Pressure
η 0.0004430 Pa×s 293.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0004210 Pa×s 298.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0004260 Pa×s 298.15 Density, dynamic viscosity, and derived properties of binary mixtures of methanol or ethanol with water, ethyl acetate, and methyl acetate at T = (293.15, 298.15, and 303.15) K
η 0.0004280 Pa×s 298.15 Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for Alkyl (Methyl, Ethyl, Butyl, and Isoamyl) Acetates + Glycols at Different Temperatures
η 0.0004260 Pa×s 298.15 Dynamic Viscosities, Densities, and Speed of Sound and Derived Properties of the Binary Systems Acetic Acid with Water, Methanol, Ethanol, Ethyl Acetate and Methyl Acetate at T = (293.15, 298.15, and 303.15) K at Atmospheric Pressure
η 0.0004260 Pa×s 298.15 NCMS SOLV-DB
η 0.0004030 Pa×s 303.15 Dynamic Viscosities, Densities, and Speed of Sound and Derived Properties of the Binary Systems Acetic Acid with Water, Methanol, Ethanol, Ethyl Acetate and Methyl Acetate at T = (293.15, 298.15, and 303.15) K at Atmospheric Pressure
η 0.0003990 Pa×s 303.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0004030 Pa×s 303.15 Density, dynamic viscosity, and derived properties of binary mixtures of methanol or ethanol with water, ethyl acetate, and methyl acetate at T = (293.15, 298.15, and 303.15) K
η 0.0003806 Pa×s 303.15 Densities, Viscosities, and Speeds of Sound of Binary Liquid Mixtures of Sulfolane with Ethyl Acetate, n-Propyl Acetate, and n-Butyl Acetate at Temperature of (303.15, 308.15, and 313.15) K
η 0.0003790 Pa×s 303.15 Volumetric and Transport Properties of Binary Liquid Mixtures of Phenylacetonitrile with Aliphatic Esters at Temperatures of (303.15 to 313.15) K
η 0.0003810 Pa×s 308.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0003870 Pa×s 308.15 Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for Alkyl (Methyl, Ethyl, Butyl, and Isoamyl) Acetates + Glycols at Different Temperatures
η 0.0003610 Pa×s 308.15 Volumetric and Transport Properties of Binary Liquid Mixtures of Phenylacetonitrile with Aliphatic Esters at Temperatures of (303.15 to 313.15) K
η 0.0003622 Pa×s 308.15 Densities, Viscosities, and Speeds of Sound of Binary Liquid Mixtures of Sulfolane with Ethyl Acetate, n-Propyl Acetate, and n-Butyl Acetate at Temperature of (303.15, 308.15, and 313.15) K
η 0.0003630 Pa×s 313.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0003426 Pa×s 313.15 Densities, Viscosities, and Speeds of Sound of Binary Liquid Mixtures of Sulfolane with Ethyl Acetate, n-Propyl Acetate, and n-Butyl Acetate at Temperature of (303.15, 308.15, and 313.15) K
η 0.0003440 Pa×s 313.15 Volumetric and Transport Properties of Binary Liquid Mixtures of Phenylacetonitrile with Aliphatic Esters at Temperatures of (303.15 to 313.15) K
η 0.0003460 Pa×s 318.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0003300 Pa×s 323.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0003150 Pa×s 328.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0003010 Pa×s 333.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0002880 Pa×s 338.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0002750 Pa×s 343.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
ΔfusH [10.48; 10.48] kJ/mol [189.30; 189.30] Show Hide
ΔfusH 10.48 kJ/mol 189.30 NIST
ΔfusH 10.48 kJ/mol 189.30 NIST
ΔfusH 10.48 kJ/mol 189.30 NIST
ΔfusH 10.48 kJ/mol 189.30 NIST
ΔvapH [31.00; 36.70] kJ/mol [313.00; 363.00] Show Hide
ΔvapH 34.60 ± 0.10 kJ/mol 313.00 NIST
ΔvapH 35.70 kJ/mol 319.50 NIST
ΔvapH 34.00 kJ/mol 320.00 NIST
ΔvapH 36.70 kJ/mol 322.00 NIST
ΔvapH 33.80 ± 0.10 kJ/mol 326.00 NIST
ΔvapH 33.40 ± 0.10 kJ/mol 331.00 NIST
ΔvapH 31.40 ± 0.10 kJ/mol 343.00 NIST
ΔvapH 32.40 ± 0.10 kJ/mol 344.00 NIST
ΔvapH 34.10 kJ/mol 345.00 NIST
ΔvapH 32.22 kJ/mol 349.80 KDB
ΔvapH 31.90 kJ/mol 350.00 NIST
ΔvapH 31.94 kJ/mol 350.30 NIST
ΔvapH 31.90 ± 0.10 kJ/mol 351.00 NIST
ΔvapH 31.00 ± 0.10 kJ/mol 363.00 NIST
Pvap [11.89; 1500.00] kPa [297.17; 462.75] Show Hide
Pvap 11.89 kPa 297.17 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 12.49 kPa 298.15 NCMS SOLV-DB
Pvap 16.04 kPa 303.35 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 18.33 kPa 306.25 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 20.64 kPa 308.86 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 21.72 kPa 310.00 Isobaric Vapor-Liquid Equilibria for Ethyl Acetate + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap 22.44 kPa 310.67 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 24.34 kPa 312.53 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 24.78 kPa 313.00 Isobaric Vapor-Liquid Equilibria for Ethyl Acetate + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap 25.30 kPa 313.15 Isothermal Vapor-Liquid Equilibria of ethyl acetate + dibromomethane, or + bromochloromethane or + 1,2-dichloroethane or +1-bromo-2-chloroethane at T = 313.15 K
Pvap 25.08 kPa 313.15 Total Vapor Pressure Measurements for 2-Ethoxyethanol with Methyl Acetate, Ethyl Acetate, Propyl Acetate, and Ethyl Propionate at 313.15 K and for 2-Ethoxyethanol with Methyl Formate at 308.15 K
Pvap 27.63 kPa 315.44 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 28.18 kPa 316.00 Isobaric Vapor-Liquid Equilibria for Ethyl Acetate + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap 31.37 kPa 318.40 Vapour liquid equilibrium for the ethyl ethanoate + 1-butene, +cis-2-butene, +trans-2-butene, +2-methylpropene, +n-butane and +2-methylpropane
Pvap 31.33 kPa 318.46 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 31.95 kPa 319.00 Isobaric Vapor-Liquid Equilibria for Ethyl Acetate + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap 34.85 kPa 321.01 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 36.12 kPa 322.00 Isobaric Vapor-Liquid Equilibria for Ethyl Acetate + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap 38.43 kPa 323.47 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 40.00 kPa 324.44 Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
Pvap 40.61 kPa 324.80 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 40.73 kPa 325.00 Isobaric Vapor-Liquid Equilibria for Ethyl Acetate + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap 44.98 kPa 327.41 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 45.80 kPa 328.00 Isobaric Vapor-Liquid Equilibria for Ethyl Acetate + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap 45.95 kPa 328.15 Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
Pvap 49.27 kPa 329.77 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 50.00 kPa 330.01 Isobaric Vapor Liquid Equilibria for Binary Mixtures of Isoamyl Acetate + Ethyl Acetate at 50 and 100 kPa
Pvap 51.36 kPa 331.00 Isobaric Vapor-Liquid Equilibria for Ethyl Acetate + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap 52.56 kPa 331.51 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 53.33 kPa 331.90 Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
Pvap 55.72 kPa 333.07 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 57.46 kPa 334.00 Isobaric Vapor-Liquid Equilibria for Ethyl Acetate + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap 59.91 kPa 335.02 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 62.83 kPa 336.33 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 64.13 kPa 337.00 Isobaric Vapor-Liquid Equilibria for Ethyl Acetate + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap 66.49 kPa 337.91 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 66.66 kPa 337.99 Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
Pvap 69.34 kPa 339.09 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 71.40 kPa 340.00 Isobaric Vapor-Liquid Equilibria for Ethyl Acetate + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap 72.26 kPa 340.23 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 76.02 kPa 341.69 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 79.32 kPa 343.00 Isobaric Vapor-Liquid Equilibria for Ethyl Acetate + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap 79.83 kPa 343.03 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 79.99 kPa 343.18 Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
Pvap 82.56 kPa 344.11 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 86.85 kPa 345.53 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 87.93 kPa 346.00 Isobaric Vapor-Liquid Equilibria for Ethyl Acetate + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap 90.81 kPa 346.86 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 93.32 kPa 347.70 Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
Pvap 94.63 kPa 348.09 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 96.74 kPa 348.75 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 97.26 kPa 349.00 Isobaric Vapor-Liquid Equilibria for Ethyl Acetate + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap 98.97 kPa 349.45 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 100.00 kPa 349.53 Isobaric Vapor Liquid Equilibria for Binary Mixtures of Isoamyl Acetate + Ethyl Acetate at 50 and 100 kPa
Pvap 99.36 kPa 349.56 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 100.07 kPa 349.76 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 100.68 kPa 349.93 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 101.30 kPa 349.95 Effect of Ionic Liquids on the Binary Vapor-Liquid Equilibrium of Ethyl Acetate + Methanol System at 101.3 kPa
Pvap 101.32 kPa 350.15 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 101.30 kPa 350.15 The isobaric vapor liquid equilibria of ethyl acetate p acetonitrile p bis(trifluoromethylsulfonyl)imide-based ionic liquids at 101.3 kPa
Pvap 101.30 kPa 350.28 Isobaric Vapor-Liquid Phase Equilibrium Measurements for Allyl Alcohol with Chloroform, Ethyl Acetate, and Methyl Propionate at 101.3 kPa
Pvap 101.30 kPa 350.29 Isobaric vapor-liquid equilibrium of a ternary system of ethyl acetate + propyl acetate + dimethyl sulfoxide and binary systems of ethyl acetate + dimethyl sulfoxide and propyl acetate + dimethyl sulfoxide at 101.3 kPa
Pvap 101.30 kPa 350.35 Isobaric Vapor - Liquid Equilibrium for Ethyl acetate + Methanol + Ionic Liquids Ternary systems at 101.3 kPa
Pvap 104.65 kPa 351.12 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 106.84 kPa 351.77 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 107.36 kPa 352.00 Isobaric Vapor-Liquid Equilibria for Ethyl Acetate + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap 108.13 kPa 352.12 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 111.21 kPa 352.94 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 111.76 kPa 353.15 Vapor Liquid Equilibrium and Excess Enthalpy Data for Systems Containing N,N-Dimethylacetamide
Pvap 114.65 kPa 353.91 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 116.46 kPa 354.43 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 118.56 kPa 354.93 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 118.27 kPa 355.00 Isobaric Vapor-Liquid Equilibria for Ethyl Acetate + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap 120.68 kPa 355.50 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 122.31 kPa 355.91 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 124.00 kPa 356.37 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 127.89 kPa 357.35 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 130.00 kPa 357.92 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 130.03 kPa 358.00 Isobaric Vapor-Liquid Equilibria for Ethyl Acetate + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap 133.45 kPa 358.74 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 134.15 kPa 359.00 Isobaric Vapor-Liquid Equilibria for Ethyl Acetate + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap 136.34 kPa 359.44 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 139.07 kPa 360.03 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 142.55 kPa 360.88 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 146.37 kPa 361.73 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 150.43 kPa 362.62 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 155.58 kPa 363.72 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 157.94 kPa 364.25 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 160.53 kPa 364.81 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 163.99 kPa 365.52 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 167.81 kPa 366.29 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 171.33 kPa 367.00 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 174.65 kPa 367.64 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 176.37 kPa 367.98 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 180.88 kPa 368.83 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 184.43 kPa 369.49 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 187.47 kPa 370.07 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 190.92 kPa 370.69 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 195.35 kPa 371.50 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 205.70 kPa 373.00 Isothermal (vapour + liquid) equilibrium (VLE) for binary mixtures containing diethyl carbonate, phenyl acetate, diphenyl carbonate, or ethyl acetate
Pvap 202.90 kPa 373.15 Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
Pvap 557.10 kPa 412.80 Isothermal (vapour + liquid) equilibrium (VLE) for binary mixtures containing diethyl carbonate, phenyl acetate, diphenyl carbonate, or ethyl acetate
Pvap 687.53 kPa 423.15 Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
Pvap 1222.70 kPa 452.30 Isothermal (vapour + liquid) equilibrium (VLE) for binary mixtures containing diethyl carbonate, phenyl acetate, diphenyl carbonate, or ethyl acetate
Pvap 1500.00 kPa 462.75 Measurement and modeling of high pressure VLE for methyl acetate or ethyl acetate with 2-butanol. Isobaric data at 1.5 MPa
n0 [1.35368; 1.37519]   [288.15; 328.15] Show Hide
n0 1.37519 288.15 Density, Speed of Sound, and Refractive Index of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate with Acetone, Methyl Acetate, and Ethyl Acetate at Temperatures from (278.15 to 328.15) K
n0 1.37490 288.20 Experimental and calculated liquid-liquid equilibrium data for water + furfural + solvents
n0 1.37200 293.15 Distribution of Butyric Acid between Water and Several Solvents
n0 1.35880 293.15 Solubilities of Methyldiphenylphosphine Oxide in Selected Solvents
n0 1.37240 293.15 A novel static analytical apparatus for phase equilibrium measurements
n0 1.35880 293.15 Solubilities of Triphenylphosphine Oxide in Selected Solvents
n0 1.37010 293.15 Liquid-Liquid Equilibrium of (Water + Pentane-2,4-dione + Ethyl Ethanoate) and (Water + Pentane-2,4-dione + Cyclohexane) at (298.15 and 313.15) K
n0 1.37190 293.15 Solubilities of Phosphorus-Containing Compounds in Selected Solvents
n0 1.37241 293.15 Thermodynamic Properties of Ionic Liquids in Organic Solvents from (293.15 to 303.15) K
n0 1.37190 293.15 Solubilities of Some Phosphaspirocyclic Compounds in Selected Solvents
n0 1.37241 293.15 Mixing properties of binary mixtures presenting azeotropes at several temperatures
n0 1.37020 293.20 Vapor liquid equilibria for the ternary system of carbon dioxide + ethanol + ethyl acetate at elevated pressures
n0 1.36977 298.15 Mixing properties of binary mixtures presenting azeotropes at several temperatures
n0 1.37270 298.15 Effects of the presence of ethylacetate or benzene on the densities and volumetric properties of mixture (styrene + N,N-dimethylformamide)
n0 1.37000 298.15 Correlation and prediction of mixing thermodynamic properties of ester-containing systems: Ester + alkane and ester + ester binary systems and the ternary dodecane + ethyl pentanoate + ethyl ethanoate
n0 1.37000 298.15 NCMS SOLV-DB
n0 1.36994 298.15 Density, Speed of Sound, and Refractive Index of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate with Acetone, Methyl Acetate, and Ethyl Acetate at Temperatures from (278.15 to 328.15) K
n0 1.36983 298.15 Physical Properties of Binary and Ternary Mixtures of Ethyl Acetate, Ethanol, and 1-Octyl-3-methyl-imidazolium Bis(trifluoromethylsulfonyl)imide at 298.15 K
n0 1.36980 298.15 Vapor-Liquid Equilibrium Data for Binary Mixtures of Dimethyl Carbonate with Methyl Acetate, Ethyl Acetate, n-Propyl Acetate, Isopropyl Acetate, n-Butyl Acetate, and Isoamyl Acetate at 93.13 kPa
n0 1.37244 298.15 Isobaric Vapor-Liquid Equilibrium Data for Binary Systems of Anisole with Methyl Acetate, Ethyl Acetate, n-Propyl Acetate, and Isopropyl Acetate at 93.9 kPa
n0 1.36981 298.15 Measurement of VLE Data by Using an Experimental Installation with Automatic Control: Modeling of Binary Systems of Methyl Acetate or Ethyl Acetate with n-Heptane or 2,2,4-Trimethylpentane at Both 0.1 and 1.5 MPa
n0 1.36980 298.15 Density, Refractive Index, and Speed of Sound at 298.15 K and Vapor-Liquid Equilibria at 101.3 kPa for Binary Mixtures of Ethyl Acetate + 1-Pentanol and Ethanol + 2-Methyl-1-propanol
n0 1.37130 298.15 Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of 1,4-Dioxane with Different Organic Liquids at (298.15, 303.15, and 308.15) K
n0 1.37120 298.15 Determination and Correlation of Vapor Liquid Equilibrium Data for the Ethyl Acetate + Hexamethyl Disiloxane System at 101.3 kPa
n0 1.36920 298.15 Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) I: HE and V E for 25 binary mixtures {xCu-1H2u-1CO2C2H5 + (1-x)a,x-ClCH2(CH2)v-2CH2Cl}, where u = 1 to 5, a = 1 and v = x = 2 to 6
n0 1.36990 298.15 Densities, Viscosities, and Refractive Indices for Binary and Ternary Mixtures of N,N-Dimethylacetamide (1) + 2-Methylbutan-2-ol (2) + Ethyl Acetate (3) at 298.15 K for the Liquid Region and at Ambient Pressure
n0 1.37000 298.15 Vapor-Liquid Equilibria for Ethyl Acetate + Methanol at (0.1, 0.5, and 0.7) MPa. Measurements with a New Ebulliometer
n0 1.36978 298.15 Density, Refractive Index, Speed of Sound at 298.15 K, and Vapor-Liquid Equilibria at 101.3 kPa for Binary Mixtures of Ethyl Acetate + Ethyl Lactate and Methyl Acetate + Ethyl Lactate
n0 1.36978 298.15 Liquid-Liquid Equilibrium Diagrams of Ethanol + Water + (Ethyl Acetate or 1-Pentanol) at Several Temperatures
n0 1.36977 298.15 Ternary (liquid + liquid) equilibria of the azeotrope (ethyl acetate + 2-propanol) with different ionic liquids at T = 298.15 K
n0 1.37000 298.15 Molecular interactions in (2,4,6-trimethyl-1,3,5-trioxane + n-alkyl acetates) at T=(298.15, 303.15, and 308.15) K
n0 1.36977 298.15 Thermodynamic Properties of Ionic Liquids in Organic Solvents from (293.15 to 303.15) K
n0 1.36977 298.15 Properties of ionic liquid HMIMPF6 with carbonates, ketones and alkyl acetates
n0 1.36712 303.15 Mixing properties of binary mixtures presenting azeotropes at several temperatures
n0 1.36720 303.15 Density, refraction index and vapor-liquid equilibria of N-methyl-2-hydroxyethylammonium butyrate plus (methyl acetate or ethyl acetate or propyl acetate) at several temperatures
n0 1.36730 303.15 Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of 1,4-Dioxane with Different Organic Liquids at (298.15, 303.15, and 308.15) K
n0 1.36712 303.15 Thermodynamic Properties of Ionic Liquids in Organic Solvents from (293.15 to 303.15) K
n0 1.36640 303.15 Densities, speeds of sound, isentropic compressibilities, refractive indexes, and viscosities of tetrahydrofuran with haloalkane or alkyl ethanoate at T = 303.15 K
n0 1.36750 303.15 Liquid-liquid equilibrium for ternary systems of ethyl acetate/isopropyl acetate + 2,2,3,3-tetrafluoro-1-propanol + water at 298.15, 318.15 K
n0 1.36720 303.20 Experimental and calculated liquid-liquid equilibrium data for water + furfural + solvents
n0 1.36460 308.15 Density, Speed of Sound, and Refractive Index of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate with Acetone, Methyl Acetate, and Ethyl Acetate at Temperatures from (278.15 to 328.15) K
n0 1.36310 308.15 Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of 1,4-Dioxane with Different Organic Liquids at (298.15, 303.15, and 308.15) K
n0 1.35970 318.15 Thermodynamic properties of (an ester + an alkane). XVI. Experimental HEm and V Em values and a new correlation method for (an alkyl ethanoate + an n-alkane) at 318.15 K
n0 1.35919 318.15 Density, Speed of Sound, and Refractive Index of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate with Acetone, Methyl Acetate, and Ethyl Acetate at Temperatures from (278.15 to 328.15) K
n0 1.35940 318.20 Experimental and calculated liquid-liquid equilibrium data for water + furfural + solvents
n0 1.35368 328.15 Density, Speed of Sound, and Refractive Index of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate with Acetone, Methyl Acetate, and Ethyl Acetate at Temperatures from (278.15 to 328.15) K
ρl [830.62; 906.55] kg/m3 [288.15; 348.15] Show Hide
ρl 906.55 kg/m3 288.15 Excess molar enthalpies of diethyl malonate+ (1-butanol, 2-methyl-1-propanol, 1-pentanol, n-heptane, and ethyl acetate) at T= (288.2, 298.2, 313.2, 328.2, 338.2, and 348.2 K) and p = 101.3 kPa
ρl 901.00 kg/m3 293.00 KDB
ρl 900.48 kg/m3 293.15 Liquid-liquid equilibria and COSMO-SAC modeling of organic solvent/ ionic liquid - hydroxyacetone - water mixtures
ρl 900.44 kg/m3 293.15 Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
ρl 900.88 kg/m3 293.15 Volumetric and FT-IR Studies of the Binary Liquid Mixtures of Tributylamine and Alkyl Ester (C1-C5)
ρl 900.57 kg/m3 293.15 Study on thermo physical and excess molar properties of binary systems of ionic liquids. I: [Cnmim][PF6] (n = 6, 8) and alkyl acetates
ρl 900.26 kg/m3 293.15 Volumetric properties of binary mixtures of N-ethylformamide with tetrahydrofuran, 2-butanone and ethylacetate from (293.15 to 313.15) K
ρl 900.57 kg/m3 293.20 Liquid-liquid equilibrium data for ternary systems of water + acetic acid + acetate esters at 293.2 K and 303.2 K and ~ 95 kPa
ρl 894.50 kg/m3 298.15 (Liquid + liquid) equilibria for mixtures of dodecane and ethanol with alkylsulfate-based ionic liquids
ρl 894.51 kg/m3 298.15 Standard partial molar volumes of some electrolytes in ethylene carbonate based mixtures
ρl 897.72 kg/m3 298.15 Effect of Inorganic Salts on the Isobaric Vapor Liquid Equilibrium of the Ethyl Acetate Ethanol System
ρl 894.36 kg/m3 298.15 Liquid-liquid equilibria and COSMO-SAC modeling of organic solvent/ ionic liquid - hydroxyacetone - water mixtures
ρl 894.37 kg/m3 298.15 Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
ρl 899.50 kg/m3 298.15 Isobaric Vapor-liquid Equilibrium for Three Binary Systems of Ethyl Acetate + Propyl Acetate, Ethyl Acetate + Propylene Carbonate, and Propyl Acetate + Propylene Carbonate at 101.3 kPa
ρl 894.60 kg/m3 298.15 Experimental Determination of Densities and Isobaric Vapor Liquid Equilibria of Methyl Acetate and Ethyl Acetate with Alcohols (C3 and C4) at 0.3 MPa
ρl 894.70 kg/m3 298.15 Ternary Excess Molar Volumes of {Methyltrioctylammonium Bis[(trifluoromethyl)sulfonyl]imide + Methanol + Methyl Acetate or Ethyl Acetate} Systems at (298.15, 303.15, and 313.15) K
ρl 894.40 kg/m3 298.15 Liquid-Liquid Equilibrium in Ternary Systems Containing Ethylene Glycol, Monofunctional Benzene Derivative, and Ethyl Acetate
ρl 894.79 kg/m3 298.15 Volumetric and FT-IR Studies of the Binary Liquid Mixtures of Tributylamine and Alkyl Ester (C1-C5)
ρl 894.40 kg/m3 298.15 Apparent molar volume and apparent molar isentropic compressibility for thebinary systems {methyltrioctylammoniumbis(trifluoromethylsulfonyl)imide + ethyl acetate or ethanol} at different temperatures underatmospheric pressure
ρl 894.14 kg/m3 298.15 Volumetric properties of binary mixtures of N-ethylformamide with tetrahydrofuran, 2-butanone and ethylacetate from (293.15 to 313.15) K
ρl 894.40 kg/m3 298.15 Measurement and correlation of solubility and solution thermodynamics of 1,3-dimethylurea in different solvents from T = (288.15 to 328.15) K
ρl 893.40 kg/m3 298.15 Solubility and solution thermodynamics of sorbic acid in eight pure organic solvents
ρl 894.40 kg/m3 298.15 Revision of the volumetric method for measurements of liquid liquid equilibria in binary systems
ρl 894.38 kg/m3 298.15 Excess molar enthalpies of diethyl malonate+ (1-butanol, 2-methyl-1-propanol, 1-pentanol, n-heptane, and ethyl acetate) at T= (288.2, 298.2, 313.2, 328.2, 338.2, and 348.2 K) and p = 101.3 kPa
ρl 894.47 kg/m3 298.15 Study on thermo physical and excess molar properties of binary systems of ionic liquids. I: [Cnmim][PF6] (n = 6, 8) and alkyl acetates
ρl 893.90 kg/m3 298.40 Vapor Liquid Equilibrium at 350 K, Excess Molar Enthalpies at 298 K, and Excess Molar Volumes at 298 K of Binary Mixtures Containing Ethyl Acetate, Butyl Acetate, and 2-Butanol
ρl 888.35 kg/m3 303.15 Study on thermo physical and excess molar properties of binary systems of ionic liquids. I: [Cnmim][PF6] (n = 6, 8) and alkyl acetates
ρl 888.50 kg/m3 303.15 Apparent molar volume and apparent molar isentropic compressibility for thebinary systems {methyltrioctylammoniumbis(trifluoromethylsulfonyl)imide + ethyl acetate or ethanol} at different temperatures underatmospheric pressure
ρl 888.26 kg/m3 303.15 Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
ρl 888.19 kg/m3 303.15 Liquid-liquid equilibria and COSMO-SAC modeling of organic solvent/ ionic liquid - hydroxyacetone - water mixtures
ρl 888.75 kg/m3 303.15 Excess Volumes and Excess Isentropic Compressibilities of Binary Liquid Mixtures of Trichloroethylene with Esters at 303.15 K
ρl 888.66 kg/m3 303.15 Volumetric and FT-IR Studies of the Binary Liquid Mixtures of Tributylamine and Alkyl Ester (C1-C5)
ρl 887.85 kg/m3 303.15 Volumetric properties of binary mixtures of N-ethylformamide with tetrahydrofuran, 2-butanone and ethylacetate from (293.15 to 313.15) K
ρl 888.42 kg/m3 303.15 Studies of viscosities of dilute solutions of alkylamine in non-electrolyte solvents. II. Haloalkanes and other polar solvents
ρl 888.50 kg/m3 303.15 Volumetric and transport properties of ternary mixtures containing 1-propanol + ethyl ethanoate + cyclohexane or benzene at 303.15 K: Experimental data, correlation and prediction by ERAS model
ρl 888.50 kg/m3 303.15 Volumetric and transport properties of ternary mixtures containing 1-alkanol + ethyl ethanoate + cyclohexane at 303.15 K: Experimental data, correlation and prediction by ERAS model
ρl 888.50 kg/m3 303.15 Ternary Excess Molar Volumes of {Methyltrioctylammonium Bis[(trifluoromethyl)sulfonyl]imide + Methanol + Methyl Acetate or Ethyl Acetate} Systems at (298.15, 303.15, and 313.15) K
ρl 881.52 kg/m3 308.15 Volumetric properties of binary mixtures of N-ethylformamide with tetrahydrofuran, 2-butanone and ethylacetate from (293.15 to 313.15) K
ρl 882.70 kg/m3 308.15 Apparent molar volume and apparent molar isentropic compressibility for thebinary systems {methyltrioctylammoniumbis(trifluoromethylsulfonyl)imide + ethyl acetate or ethanol} at different temperatures underatmospheric pressure
ρl 881.98 kg/m3 308.15 Liquid-liquid equilibria and COSMO-SAC modeling of organic solvent/ ionic liquid - hydroxyacetone - water mixtures
ρl 882.09 kg/m3 308.15 Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
ρl 882.48 kg/m3 308.15 Volumetric and FT-IR Studies of the Binary Liquid Mixtures of Tributylamine and Alkyl Ester (C1-C5)
ρl 882.17 kg/m3 308.15 Study on thermo physical and excess molar properties of binary systems of ionic liquids. I: [Cnmim][PF6] (n = 6, 8) and alkyl acetates
ρl 875.73 kg/m3 313.15 Liquid-liquid equilibria and COSMO-SAC modeling of organic solvent/ ionic liquid - hydroxyacetone - water mixtures
ρl 875.81 kg/m3 313.15 Excess molar enthalpies of diethyl malonate+ (1-butanol, 2-methyl-1-propanol, 1-pentanol, n-heptane, and ethyl acetate) at T= (288.2, 298.2, 313.2, 328.2, 338.2, and 348.2 K) and p = 101.3 kPa
ρl 875.10 kg/m3 313.15 Ternary Excess Molar Volumes of {Methyltrioctylammonium Bis[(trifluoromethyl)sulfonyl]imide + Methanol + Methyl Acetate or Ethyl Acetate} Systems at (298.15, 303.15, and 313.15) K
ρl 876.30 kg/m3 313.15 Apparent molar volume and apparent molar isentropic compressibility for thebinary systems {methyltrioctylammoniumbis(trifluoromethylsulfonyl)imide + ethyl acetate or ethanol} at different temperatures underatmospheric pressure
ρl 875.88 kg/m3 313.15 Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
ρl 875.95 kg/m3 313.15 Study on thermo physical and excess molar properties of binary systems of ionic liquids. I: [Cnmim][PF6] (n = 6, 8) and alkyl acetates
ρl 875.14 kg/m3 313.15 Volumetric properties of binary mixtures of N-ethylformamide with tetrahydrofuran, 2-butanone and ethylacetate from (293.15 to 313.15) K
ρl 876.25 kg/m3 313.15 Volumetric and FT-IR Studies of the Binary Liquid Mixtures of Tributylamine and Alkyl Ester (C1-C5)
ρl 876.10 kg/m3 313.20 Liquid-liquid equilibrium data for ternary systems of water + acetic acid + acetate esters at 293.2 K and 303.2 K and ~ 95 kPa
ρl 869.62 kg/m3 318.15 Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
ρl 869.68 kg/m3 318.15 Study on thermo physical and excess molar properties of binary systems of ionic liquids. I: [Cnmim][PF6] (n = 6, 8) and alkyl acetates
ρl 863.36 kg/m3 323.15 Study on thermo physical and excess molar properties of binary systems of ionic liquids. I: [Cnmim][PF6] (n = 6, 8) and alkyl acetates
ρl 863.30 kg/m3 323.15 Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
ρl 856.81 kg/m3 328.15 Excess molar enthalpies of diethyl malonate+ (1-butanol, 2-methyl-1-propanol, 1-pentanol, n-heptane, and ethyl acetate) at T= (288.2, 298.2, 313.2, 328.2, 338.2, and 348.2 K) and p = 101.3 kPa
ρl 851.36 kg/m3 332.70 Isothermal vapor liquid equilibria for different binary mixtures involved in the alcoholic distillation
ρl 843.86 kg/m3 338.15 Excess molar enthalpies of diethyl malonate+ (1-butanol, 2-methyl-1-propanol, 1-pentanol, n-heptane, and ethyl acetate) at T= (288.2, 298.2, 313.2, 328.2, 338.2, and 348.2 K) and p = 101.3 kPa
ρl 830.62 kg/m3 348.15 Excess molar enthalpies of diethyl malonate+ (1-butanol, 2-methyl-1-propanol, 1-pentanol, n-heptane, and ethyl acetate) at T= (288.2, 298.2, 313.2, 328.2, 338.2, and 348.2 K) and p = 101.3 kPa
ΔfusS [55.27; 55.27] J/mol×K [189.30; 189.30] Show Hide
ΔfusS 55.27 J/mol×K 189.30 NIST
ΔfusS 55.27 J/mol×K 189.30 NIST
csound,fluid [1058.00; 1187.92] m/s [288.15; 318.15] Show Hide
csound,fluid 1187.92 m/s 288.15 Densities and Speeds of Sound of Binary Liquid Mixtures of Some n-Alkoxypropanols with Methyl Acetate, Ethyl Acetate, and n-Butyl Acetate at T = (288.15, 293.15, 298.15, 303.15, and 308.15) K
csound,fluid 1165.80 m/s 293.15 Densities and Speeds of Sound of Binary Liquid Mixtures of Some n-Alkoxypropanols with Methyl Acetate, Ethyl Acetate, and n-Butyl Acetate at T = (288.15, 293.15, 298.15, 303.15, and 308.15) K
csound,fluid 1143.23 m/s 298.15 Densities and Speeds of Sound of Binary Liquid Mixtures of Some n-Alkoxypropanols with Methyl Acetate, Ethyl Acetate, and n-Butyl Acetate at T = (288.15, 293.15, 298.15, 303.15, and 308.15) K
csound,fluid 1119.00 m/s 303.15 Density and Speed of Sound of Binary Mixtures of N-Methylacetamide with Ethyl Acetate, Ethyl Chloroacetate, and Ethyl Cyanoacetate in the Temperature Interval (303.15 to 318.15) K
csound,fluid 1120.80 m/s 303.15 Densities and Speeds of Sound of Binary Liquid Mixtures of Some n-Alkoxypropanols with Methyl Acetate, Ethyl Acetate, and n-Butyl Acetate at T = (288.15, 293.15, 298.15, 303.15, and 308.15) K
csound,fluid 1098.00 m/s 308.15 Density and Speed of Sound of Binary Mixtures of N-Methylacetamide with Ethyl Acetate, Ethyl Chloroacetate, and Ethyl Cyanoacetate in the Temperature Interval (303.15 to 318.15) K
csound,fluid 1098.43 m/s 308.15 Densities and Speeds of Sound of Binary Liquid Mixtures of Some n-Alkoxypropanols with Methyl Acetate, Ethyl Acetate, and n-Butyl Acetate at T = (288.15, 293.15, 298.15, 303.15, and 308.15) K
csound,fluid 1081.00 m/s 313.15 Density and Speed of Sound of Binary Mixtures of N-Methylacetamide with Ethyl Acetate, Ethyl Chloroacetate, and Ethyl Cyanoacetate in the Temperature Interval (303.15 to 318.15) K
csound,fluid 1058.00 m/s 318.15 Density and Speed of Sound of Binary Mixtures of N-Methylacetamide with Ethyl Acetate, Ethyl Chloroacetate, and Ethyl Cyanoacetate in the Temperature Interval (303.15 to 318.15) K
γ [0.02; 0.03] N/m [298.15; 323.20] Show Hide
γ 0.02 N/m 298.15 Concentration Dependence of Surface Tension for Very Dilute Aqueous Solutions of Organic Non-Electrolytes
γ 0.02 N/m 298.15 Surface Tension Data of Aqueous Binary Mixtures of Methyl, Ethyl, Propyl, and Butyl Acetates at 298.15 K
γ 0.02 N/m 298.15 NCMS SOLV-DB
γ 0.03 N/m 323.20 KDB
λliquid [0.12; 0.16] W/m×K [249.13; 348.46] Show Hide
λliquid 0.16 W/m×K 249.13 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid 0.16 W/m×K 253.89 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid 0.16 W/m×K 260.17 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid 0.15 W/m×K 268.04 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid 0.15 W/m×K 274.35 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid 0.15 W/m×K 281.34 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid 0.15 W/m×K 285.31 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid 0.15 W/m×K 290.42 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid 0.14 W/m×K 295.44 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid 0.14 W/m×K 298.52 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid 0.14 W/m×K 303.53 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid 0.14 W/m×K 308.44 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid 0.14 W/m×K 313.45 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid 0.13 W/m×K 318.40 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid 0.13 W/m×K 323.25 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid 0.13 W/m×K 328.39 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid 0.13 W/m×K 333.37 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid 0.13 W/m×K 338.34 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid 0.13 W/m×K 343.27 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid 0.12 W/m×K 345.43 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid 0.12 W/m×K 348.46 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase

Pressure Dependent Properties

Property Value Unit Pressure (kPa) Source
Tboil(P) [332.82; 369.50] K [54.99; 185.00] Show Hide
Tboil(P) 332.82 K 54.99 Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil(P) 335.16 K 59.98 Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil(P) 339.42 K 70.00 Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil(P) 340.92 K 75.00 Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil(P) 343.18 K 80.00 Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil(P) 344.93 K 84.99 Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil(P) 346.58 K 89.91 Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil(P) 348.20 K 95.01 Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil(P) 351.26 K 104.99 Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil(P) 352.67 K 109.98 Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil(P) 355.36 K 119.90 Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil(P) 356.62 K 124.98 Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil(P) 357.86 K 129.93 Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil(P) 359.08 K 134.95 Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil(P) 360.24 K 139.96 Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil(P) 362.48 K 149.95 Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil(P) 363.56 K 154.97 Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil(P) 364.60 K 159.96 Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil(P) 365.64 K 164.99 Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil(P) 367.61 K 174.99 Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil(P) 368.58 K 180.00 Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil(P) 369.50 K 185.00 Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil

Datasets

Mass density, kg/m3

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
298.15 100.00 894.0
298.15 1000.00 894.7
298.15 2000.00 895.7
298.15 3000.00 896.7
298.15 3800.00 897.4
298.15 5000.00 898.8
298.15 10000.00 903.4
298.15 15000.00 907.7
298.15 20000.00 912.0
298.15 25000.00 916.1
298.15 30000.00 921.1
298.15 35000.00 926.3
303.15 100.00 887.6
303.15 1000.00 888.5
303.15 2000.00 889.5
303.15 3000.00 890.5
303.15 3800.00 891.3
303.15 5000.00 892.7
303.15 10000.00 897.5
303.15 15000.00 902.0
303.15 20000.00 906.3
303.15 25000.00 910.7
303.15 30000.00 915.9
303.15 35000.00 921.2
308.15 100.00 881.4
308.15 1000.00 882.3
308.15 2000.00 883.3
308.15 3000.00 884.4
308.15 3800.00 885.3
308.15 5000.00 886.7
308.15 10000.00 891.7
308.15 15000.00 896.4
308.15 20000.00 900.9
308.15 25000.00 905.4
308.15 30000.00 910.7
308.15 35000.00 916.2
313.15 100.00 875.2
313.15 1000.00 876.1
313.15 2000.00 877.2
313.15 3000.00 878.3
313.15 3800.00 879.2
313.15 5000.00 880.6
313.15 10000.00 885.8
313.15 15000.00 890.7
313.15 20000.00 895.4
313.15 25000.00 899.8
313.15 30000.00 905.3
313.15 35000.00 910.9
318.15 100.00 868.8
318.15 1000.00 869.8
318.15 2000.00 871.0
318.15 3000.00 872.2
318.15 3800.00 873.1
318.15 5000.00 874.5
318.15 10000.00 880.0
318.15 15000.00 885.1
318.15 20000.00 889.8
318.15 25000.00 894.5
318.15 30000.00 900.1
318.15 35000.00 905.9
323.15 100.00 862.7
323.15 1000.00 864.0
323.15 2000.00 865.1
323.15 3000.00 866.2
323.15 3800.00 867.1
323.15 5000.00 868.6
323.15 10000.00 874.2
323.15 15000.00 879.4
323.15 20000.00 884.3
323.15 25000.00 889.2
323.15 30000.00 895.0
323.15 35000.00 900.9
328.15 100.00 856.4
328.15 1000.00 857.8
328.15 2000.00 859.2
328.15 3000.00 860.5
328.15 3800.00 861.5
328.15 5000.00 862.5
328.15 10000.00 868.4
328.15 15000.00 873.9
328.15 20000.00 879.0
328.15 25000.00 884.1
328.15 30000.00 890.1
328.15 35000.00 896.2
333.15 100.00 850.4
333.15 1000.00 851.7
333.15 2000.00 853.0
333.15 3000.00 854.4
333.15 3800.00 855.4
333.15 5000.00 856.8
333.15 10000.00 862.9
333.15 15000.00 868.5
333.15 20000.00 873.8
333.15 25000.00 879.0
333.15 30000.00 885.2
333.15 35000.00 891.4
338.15 100.00 844.0
338.15 1000.00 845.4
338.15 2000.00 846.8
338.15 3000.00 848.2
338.15 3800.00 849.3
338.15 5000.00 850.8
338.15 10000.00 857.1
338.15 15000.00 863.0
338.15 20000.00 868.5
338.15 25000.00 873.9
338.15 30000.00 880.3
338.15 35000.00 886.7
343.15 100.00 837.5
343.15 1000.00 839.1
343.15 2000.00 840.6
343.15 3000.00 842.0
343.15 3800.00 843.2
343.15 5000.00 844.5
343.15 10000.00 851.2
343.15 15000.00 857.3
343.15 20000.00 863.0
343.15 25000.00 868.5
343.15 30000.00 875.1
343.15 35000.00 881.6
348.15 100.00 829.4
348.15 1000.00 830.5
348.15 2000.00 832.3
348.15 3000.00 833.8
348.15 3800.00 835.0
348.15 5000.00 836.8
348.15 10000.00 845.5
348.15 15000.00 851.8
348.15 20000.00 857.7
348.15 25000.00 863.5
348.15 30000.00 870.2
348.15 35000.00 877.0
353.15 1000.00 824.3
353.15 2000.00 826.0
353.15 3000.00 827.5
353.15 3800.00 828.8
353.15 5000.00 830.6
353.15 10000.00 837.7
353.15 15000.00 844.3
353.15 20000.00 850.4
353.15 25000.00 856.1
353.15 30000.00 862.7
353.15 35000.00 869.6
358.15 1000.00 818.4
358.15 2000.00 820.0
358.15 3000.00 821.6
358.15 3800.00 822.8
358.15 5000.00 824.7
358.15 10000.00 832.1
358.15 15000.00 838.9
358.15 20000.00 845.2
358.15 25000.00 851.0
358.15 30000.00 857.6
358.15 35000.00 864.7
363.15 1000.00 811.8
363.15 2000.00 813.5
363.15 3000.00 815.3
363.15 3800.00 816.6
363.15 5000.00 818.5
363.15 10000.00 826.3
363.15 15000.00 833.3
363.15 20000.00 839.7
363.15 25000.00 845.8
363.15 30000.00 852.9
363.15 35000.00 860.2
368.15 1000.00 804.9
368.15 2000.00 806.8
368.15 3000.00 808.6
368.15 3800.00 810.0
368.15 5000.00 812.1
368.15 10000.00 820.2
368.15 15000.00 827.5
368.15 20000.00 834.3
368.15 25000.00 840.6
368.15 30000.00 848.0
368.15 35000.00 855.5
373.15 1000.00 798.5
373.15 2000.00 800.4
373.15 3000.00 802.4
373.15 3800.00 803.8
373.15 5000.00 806.0
373.15 10000.00 814.4
373.15 15000.00 822.0
373.15 20000.00 829.0
373.15 25000.00 835.5
373.15 30000.00 843.0
373.15 35000.00 850.6
378.15 1000.00 791.8
378.15 2000.00 793.8
378.15 3000.00 795.8
378.15 3800.00 797.3
378.15 5000.00 799.6
378.15 10000.00 808.5
378.15 15000.00 816.5
378.15 20000.00 823.7
378.15 25000.00 830.5
378.15 30000.00 838.4
378.15 35000.00 846.3
383.15 1000.00 784.8
383.15 2000.00 787.1
383.15 3000.00 789.1
383.15 3800.00 790.8
383.15 5000.00 793.2
383.15 10000.00 802.4
383.15 15000.00 810.7
383.15 20000.00 818.2
383.15 25000.00 825.3
383.15 30000.00 833.5
383.15 35000.00 841.6
388.15 1000.00 778.2
388.15 2000.00 780.5
388.15 3000.00 782.7
388.15 3800.00 784.4
388.15 5000.00 786.9
388.15 10000.00 796.4
388.15 15000.00 805.1
388.15 20000.00 813.0
388.15 25000.00 820.3
388.15 30000.00 828.8
388.15 35000.00 837.2
393.15 1000.00 771.0
393.15 2000.00 773.5
393.15 3000.00 775.9
393.15 3800.00 777.7
393.15 5000.00 780.4
393.15 10000.00 790.5
393.15 15000.00 799.4
393.15 20000.00 807.6
393.15 25000.00 815.2
393.15 30000.00 823.9
393.15 35000.00 832.4
Reference

Correlations

Property Value Unit Temperature (K) Source
Cp,gas [100.13; 266.84] J/mol×K [200.00; 1500.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is Cp,gas in J/mol×K, T in K
Coefficient A9.71830e+01
Coefficient B-1.12140e+03
Coefficient C6.91924e+00
Coefficient D-1.23430e-03
Coefficient E3.61580e-07
Temperature range, min.200.00
Temperature range, max.1500.00
Cp,gas 100.13 J/mol×K 200.00 Calculated Property
Cp,gas 123.79 J/mol×K 344.44 Calculated Property
Cp,gas 158.04 J/mol×K 488.89 Calculated Property
Cp,gas 188.28 J/mol×K 633.33 Calculated Property
Cp,gas 211.18 J/mol×K 777.78 Calculated Property
Cp,gas 227.83 J/mol×K 922.22 Calculated Property
Cp,gas 240.17 J/mol×K 1066.67 Calculated Property
Cp,gas 249.93 J/mol×K 1211.11 Calculated Property
Cp,gas 258.48 J/mol×K 1355.56 Calculated Property
Cp,gas 266.84 J/mol×K 1500.00 Calculated Property
Property Value Unit Temperature (K) Source
Cp,liquid [162.57; 197.54] J/mol×K [189.30; 391.65] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is Cp,liquid in J/mol×K, T in K
Coefficient A1.29430e+02
Coefficient B9.61920e+02
Coefficient C-7.03470e+00
Coefficient D3.47450e-02
Coefficient E-3.13460e-05
Temperature range, min.189.30
Temperature range, max.391.65
Cp,liquid 162.57 J/mol×K 189.30 Calculated Property
Cp,liquid 161.24 J/mol×K 211.78 Calculated Property
Cp,liquid 162.24 J/mol×K 234.27 Calculated Property
Cp,liquid 164.81 J/mol×K 256.75 Calculated Property
Cp,liquid 168.61 J/mol×K 279.23 Calculated Property
Cp,liquid 173.38 J/mol×K 301.72 Calculated Property
Cp,liquid 178.93 J/mol×K 324.20 Calculated Property
Cp,liquid 185.02 J/mol×K 346.68 Calculated Property
Cp,liquid 191.34 J/mol×K 369.17 Calculated Property
Cp,liquid 197.54 J/mol×K 391.65 Calculated Property
Property Value Unit Temperature (K) Source
η [0.0011331; 0.0000913] Pa×s [220.00; 473.15] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is η in Pa×s, T in K
Coefficient A1.64280e+01
Coefficient B-2.19290e+02
Coefficient C-4.12400e+00
Coefficient D6.05680e-07
Coefficient E2.00000e+00
Temperature range, min.220.00
Temperature range, max.473.15
η 0.0011331 Pa×s 220.00 Calculated Property
η 0.0007786 Pa×s 248.13 Calculated Property
η 0.0005520 Pa×s 276.26 Calculated Property
η 0.0004022 Pa×s 304.38 Calculated Property
η 0.0003001 Pa×s 332.51 Calculated Property
η 0.0002287 Pa×s 360.64 Calculated Property
η 0.0001776 Pa×s 388.77 Calculated Property
η 0.0001402 Pa×s 416.89 Calculated Property
η 0.0001124 Pa×s 445.02 Calculated Property
η 0.0000913 Pa×s 473.15 Calculated Property
Property Value Unit Temperature (K) Source
ΔvapH [41.61; 13.43] kJ/mol [189.60; 505.74] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc
Y is ΔvapH in kJ/mol, T in K
Coefficient A4.95270e+01
Coefficient B3.70290e-01
Coefficient C7.26850e-02
Coefficient D-7.74930e-02
Coefficient E1.73810e-02
Critical temperature, Tc (K)5.23200e+02
Temperature range, min.189.60
Temperature range, max.505.74
ΔvapH 41.61 kJ/mol 189.60 Calculated Property
ΔvapH 39.82 kJ/mol 224.73 Calculated Property
ΔvapH 37.91 kJ/mol 259.85 Calculated Property
ΔvapH 35.84 kJ/mol 294.98 Calculated Property
ΔvapH 33.59 kJ/mol 330.11 Calculated Property
ΔvapH 31.08 kJ/mol 365.23 Calculated Property
ΔvapH 28.21 kJ/mol 400.36 Calculated Property
ΔvapH 24.81 kJ/mol 435.49 Calculated Property
ΔvapH 20.42 kJ/mol 470.61 Calculated Property
ΔvapH 13.43 kJ/mol 505.74 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [1.33; 202.64] kPa [258.37; 372.76] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.47020e+01
Coefficient B-3.08216e+03
Coefficient C-4.45420e+01
Temperature range, min.258.37
Temperature range, max.372.76
Pvap 1.33 kPa 258.37 Calculated Property
Pvap 2.99 kPa 271.08 Calculated Property
Pvap 6.17 kPa 283.79 Calculated Property
Pvap 11.81 kPa 296.50 Calculated Property
Pvap 21.26 kPa 309.21 Calculated Property
Pvap 36.24 kPa 321.92 Calculated Property
Pvap 58.97 kPa 334.63 Calculated Property
Pvap 92.12 kPa 347.34 Calculated Property
Pvap 138.81 kPa 360.05 Calculated Property
Pvap 202.64 kPa 372.76 Calculated Property
Pvap [1.28e-03; 3814.55] kPa [189.60; 523.20] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is Pvap in kPa, T in K
Coefficient A8.62609e+01
Coefficient B-7.07329e+03
Coefficient C-1.06598e+01
Coefficient D8.16528e-06
Coefficient E2.00000e+00
CommentRange stopped at Tc; ChemSep gives it to 523.3 K.
Temperature range, min.189.60
Temperature range, max.523.20
Pvap 1.28e-03 kPa 189.60 Calculated Property
Pvap 0.10 kPa 226.67 Calculated Property
Pvap 1.79 kPa 263.73 Calculated Property
Pvap 14.22 kPa 300.80 Calculated Property
Pvap 65.98 kPa 337.87 Calculated Property
Pvap 213.81 kPa 374.93 Calculated Property
Pvap 542.18 kPa 412.00 Calculated Property
Pvap 1158.61 kPa 449.07 Calculated Property
Pvap 2194.19 kPa 486.13 Calculated Property
Pvap 3814.55 kPa 523.20 Calculated Property
Pvap [1.39e-03; 3810.53] kPa [189.60; 523.30] KDB Vapor Pressure Data Show Hide
Equationln(Y) = A + B/T + C·ln(T) + D·T² + E/T²
Y is Pvap in kPa, T in K
Coefficient A8.09498e+01
Coefficient B-6.86243e+03
Coefficient C-9.83731e+00
Coefficient D7.27641e-06
Coefficient E0.00000e+00
Temperature range, min.189.60
Temperature range, max.523.30
Pvap 1.39e-03 kPa 189.60 Calculated Property
Pvap 0.10 kPa 226.68 Calculated Property
Pvap 1.81 kPa 263.76 Calculated Property
Pvap 14.29 kPa 300.83 Calculated Property
Pvap 66.14 kPa 337.91 Calculated Property
Pvap 214.41 kPa 374.99 Calculated Property
Pvap 544.22 kPa 412.07 Calculated Property
Pvap 1163.18 kPa 449.14 Calculated Property
Pvap 2199.72 kPa 486.22 Calculated Property
Pvap 3810.53 kPa 523.30 Calculated Property
Pvap [7.84; 97.27] kPa [288.73; 348.98] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.43407e+01
Coefficient B-2.86833e+03
Coefficient C-5.51890e+01
ReferencePolák and Mertl, 1965
CommentCoefficents calculated by NIST from author's data.
Temperature range, min.288.73
Temperature range, max.348.98
Pvap 7.84 kPa 288.73 Calculated Property
Pvap 11.03 kPa 295.42 Calculated Property
Pvap 15.25 kPa 302.12 Calculated Property
Pvap 20.72 kPa 308.81 Calculated Property
Pvap 27.72 kPa 315.51 Calculated Property
Pvap 36.54 kPa 322.20 Calculated Property
Pvap 47.52 kPa 328.90 Calculated Property
Pvap 61.03 kPa 335.59 Calculated Property
Pvap 77.47 kPa 342.29 Calculated Property
Pvap 97.27 kPa 348.98 Calculated Property
Property Value Unit Temperature (K) Source
ρl [1009.09; 328.13] kg/m3 [189.60; 523.20] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A / B^(1 + (1 − T/C)^D)
Y is ρl in kg/m3, T in K
Coefficient A6.95379e+01
Coefficient B2.42950e-01
Coefficient C5.23260e+02
Coefficient D2.57620e-01
CommentRange stopped at Tc; ChemSep gives it to 523.25 K.
Temperature range, min.189.60
Temperature range, max.523.20
ρl 1009.09 kg/m3 189.60 Calculated Property
ρl 971.81 kg/m3 226.67 Calculated Property
ρl 932.46 kg/m3 263.73 Calculated Property
ρl 890.57 kg/m3 300.80 Calculated Property
ρl 845.38 kg/m3 337.87 Calculated Property
ρl 795.77 kg/m3 374.93 Calculated Property
ρl 739.74 kg/m3 412.00 Calculated Property
ρl 673.29 kg/m3 449.07 Calculated Property
ρl 585.48 kg/m3 486.13 Calculated Property
ρl 328.13 kg/m3 523.20 Calculated Property
Property Value Unit Temperature (K) Source
γ [0.04; 0.02] N/m [189.15; 350.15] Jasper (1972), surface tension of pure liquid compounds Compiled value Show Hide
EquationY = A + B·T + C·T² + D·T³ + E·T⁴
Y is γ in N/m, T in K
Coefficient A5.80027e-02
Coefficient B-1.16100e-04
Coefficient C0.00000e+00
Coefficient D0.00000e+00
Coefficient E0.00000e+00
Temperature range, min.189.15
Temperature range, max.350.15
γ 0.04 N/m 189.15 Calculated Property
γ 0.03 N/m 207.04 Calculated Property
γ 0.03 N/m 224.93 Calculated Property
γ 0.03 N/m 242.82 Calculated Property
γ 0.03 N/m 260.71 Calculated Property
γ 0.03 N/m 278.59 Calculated Property
γ 0.02 N/m 296.48 Calculated Property
γ 0.02 N/m 314.37 Calculated Property
γ 0.02 N/m 332.26 Calculated Property
γ 0.02 N/m 350.15 Calculated Property
γ [0.04; 0.00] N/m [189.60; 505.74] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is γ in N/m, T in K
Coefficient A-2.53310e-02
Coefficient B1.27150e+01
Coefficient C-2.64430e+00
Coefficient D-5.93700e-04
Coefficient E-2.76690e-06
Temperature range, min.189.60
Temperature range, max.505.74
γ 0.04 N/m 189.60 Calculated Property
γ 0.03 N/m 224.73 Calculated Property
γ 0.03 N/m 259.85 Calculated Property
γ 0.02 N/m 294.98 Calculated Property
γ 0.02 N/m 330.11 Calculated Property
γ 0.02 N/m 365.23 Calculated Property
γ 0.01 N/m 400.36 Calculated Property
γ 0.01 N/m 435.49 Calculated Property
γ 0.00 N/m 470.61 Calculated Property
γ 0.00 N/m 505.74 Calculated Property
Property Value Unit Temperature (K) Source
λgas [0.00; 0.11] W/m×K [189.60; 990.21] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A·T^B / (1 + C/T + D/T²)
Y is λgas in W/m×K, T in K
Coefficient A2.32640e-07
Coefficient B1.90200e+00
Coefficient C1.02580e+02
Coefficient D-1.70150e+04
Temperature range, min.189.60
Temperature range, max.990.21
λgas 0.00 W/m×K 189.60 Calculated Property
λgas 0.01 W/m×K 278.56 Calculated Property
λgas 0.02 W/m×K 367.51 Calculated Property
λgas 0.02 W/m×K 456.47 Calculated Property
λgas 0.03 W/m×K 545.43 Calculated Property
λgas 0.04 W/m×K 634.38 Calculated Property
λgas 0.06 W/m×K 723.34 Calculated Property
λgas 0.07 W/m×K 812.30 Calculated Property
λgas 0.09 W/m×K 901.25 Calculated Property
λgas 0.11 W/m×K 990.21 Calculated Property
Property Value Unit Temperature (K) Source
λliquid [0.18; 0.13] W/m×K [189.60; 350.21] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is λliquid in W/m×K, T in K
Coefficient A4.07710e-02
Coefficient B-1.27250e+02
Coefficient C-2.69950e-01
Coefficient D-5.57530e-03
Coefficient E9.93630e-07
Temperature range, min.189.60
Temperature range, max.350.21
λliquid 0.18 W/m×K 189.60 Calculated Property
λliquid 0.18 W/m×K 207.45 Calculated Property
λliquid 0.17 W/m×K 225.29 Calculated Property
λliquid 0.16 W/m×K 243.14 Calculated Property
λliquid 0.16 W/m×K 260.98 Calculated Property
λliquid 0.15 W/m×K 278.83 Calculated Property
λliquid 0.14 W/m×K 296.67 Calculated Property
λliquid 0.14 W/m×K 314.52 Calculated Property
λliquid 0.13 W/m×K 332.36 Calculated Property
λliquid 0.13 W/m×K 350.21 Calculated Property

Similar Compounds

Acetic acid, fluoro-, ethyl ester. Acetic acid, iodo-, ethyl ester. Acetic acid, bromo-, ethyl ester. Acetic acid, chloro-, ethyl ester. 1,2-Ethanediol, diacetate. Ethanol, 2-bromo-, acetate. Carbonocyanidic acid, ethyl ester. Ethanol, 2-chloro-, acetate. .beta.-Iodoethyl acetate. Ethyl cyanoacetate. Acetic acid, difluoro-, ethyl ester. Ethyl propiolate. Acetic acid, dichloro-, ethyl ester. 2-Ethoxyethyl acetate. 1,2-Ethanediol, monoacetate.

Find more compounds similar to Ethyl Acetate.

Mixtures

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Sources

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