Chemical Properties of Acetic acid, butyl ester (CAS 123-86-4)

Acetic acid, butyl ester

InChI
InChI=1S/C6H12O2/c1-3-4-5-8-6(2)7/h3-5H2,1-2H3
InChI Key
DKPFZGUDAPQIHT-UHFFFAOYSA-N
Formula
C6H12O2
SMILES
CCCCOC(C)=O
Molecular Weight1
116.16
CAS
123-86-4
Other Names
  • 1-Acetoxybutane
  • 1-Butanol, acetate
  • 1-Butyl acetate
  • Acetate de butyle
  • Acetic acid butyl ester
  • Acetic acid n-butyl ester
  • Butile
  • Butile(acetati di)
  • Butyl ester of acetic acid
  • Butyl ester, acetic acid
  • Butylacetat
  • Butylacetaten
  • Butyle
  • Butyle (acetate de)
  • Butylester kyseliny octove
  • CH3COO(CH2)3CH3
  • NSC 9298
  • UN 1123
  • butyl acetate
  • butyl ethanoate
  • ethanoic acid, butyl ester
  • n-Butyl ethanoate
  • n-butyl acetate
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Physical Properties

Property Value Unit Source
ω [0.4070; 0.4345]   Show Hide
ω 0.4345 PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω 0.4070 ChemSep v8.3 pure component data Compiled value
ω 0.4170 KDB
Tig [677.59; 698.15] K Show Hide
Tig 677.59 K KDB
Tig 698.15 K NCMS SOLV-DB
ΔcH°liquid [-3543.00; -3467.00] kJ/mol Show Hide
ΔcH°liquid -3467.00 kJ/mol NIST
ΔcH°liquid -3543.00 kJ/mol NIST
μ [1.80; 1.84] debye Show Hide
μ 1.84 debye ChemSep v8.3 pure component data Compiled value
μ 1.80 debye KDB
η 0.0006680 Pa×s Excess Molar Volumes and Viscosity Deviations of Binary Liquid Mixtures of 1,3-Dioxolane and 1,4-Dioxane with Butyl Acetate, Butyric Acid, Butylamine, and 2-Butanone at 298.15 K
εr 5.01 NCMS SOLV-DB
LFL 1.70 % in Air KDB
UFL 7.60 % in Air KDB
Tflash,cc [295.15; 310.37] K Show Hide
Tflash,cc 310.37 K KDB
Tflash,cc 295.15 K NCMS SOLV-DB
Tflash,oc 297.04 K KDB
ΔfG° -312.30 kJ/mol ChemSep v8.3 pure component data Compiled value
Rg 4.1700 KDB
ΔfH°gas [-486.80; -485.60] kJ/mol Show Hide
ΔfH°gas -485.60 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfH°gas -486.80 kJ/mol KDB
ΔfusH° 15.67 kJ/mol Joback Calculated Property
ΔvapH° [37.50; 43.89] kJ/mol Show Hide
ΔvapH° 43.64 kJ/mol NCMS SOLV-DB
ΔvapH° 43.89 kJ/mol NIST
ΔvapH° 42.40 kJ/mol NIST
ΔvapH° 42.70 kJ/mol NIST
ΔvapH° 43.10 kJ/mol NIST
ΔvapH° 41.00 ± 0.50 kJ/mol NIST
ΔvapH° 43.60 ± 0.50 kJ/mol NIST
ΔvapH° 43.70 ± 0.20 kJ/mol NIST
ΔvapH° 43.60 ± 0.20 kJ/mol NIST
ΔvapH° 43.60 ± 0.20 kJ/mol NIST
ΔvapH° Outlier 37.50 kJ/mol NIST
IE [9.56; 10.17] eV Show Hide
IE 9.92 ± 0.05 eV NIST
IE 10.01 eV NIST
IE 9.56 ± 0.03 eV NIST
IE 10.02 ± 0.05 eV NIST
IE 10.17 eV NIST
log10WS -1.24 Aq. Solubility Prediction
logPoct/wat 2.060 NCMS SOLV-DB
McVol 102.840 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 [%!d(float64=1); %!d(float64=1)]   Show Hide
NFPA Health 1 KDB
NFPA Health 1 NCMS SOLV-DB
NFPA Safety 0 NCMS SOLV-DB
Pc [3090.00; 3141.08] kPa Show Hide
Pc 3140.00 kPa IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Pc 3141.08 kPa PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc 3090.00 kPa ChemSep v8.3 pure component data Compiled value
Pc 3140.00 kPa KDB
Pc 3090.00 ± 20.00 kPa NIST
Pc 3100.00 ± 101.32 kPa NIST
Ptriple 8.17e-05 kPa ChemSep v8.3 pure component data Compiled value
Inp [769.00; 830.10]   Show Hide
Inp 796.20 NIST
Inp 784.76 NIST
Inp 805.85 NIST
Inp 805.20 NIST
Inp 801.50 NIST
Inp 804.70 NIST
Inp 801.60 NIST
Inp 799.40 NIST
Inp 798.20 NIST
Inp 796.80 NIST
Inp 797.88 NIST
Inp 797.88 NIST
Inp 796.00 NIST
Inp 809.40 NIST
Inp 808.30 NIST
Inp 806.60 NIST
Inp 786.00 NIST
Inp Outlier 774.00 NIST
Inp 810.00 NIST
Inp 786.00 NIST
Inp Outlier 774.00 NIST
Inp 781.00 NIST
Inp 810.00 NIST
Inp 790.00 NIST
Inp 818.00 NIST
Inp 796.00 NIST
Inp 792.00 NIST
Inp Outlier 770.00 NIST
Inp 796.40 NIST
Inp 784.00 NIST
Inp 786.00 NIST
Inp 786.00 NIST
Inp 794.00 NIST
Inp 794.00 NIST
Inp 802.00 NIST
Inp 805.00 NIST
Inp 787.00 NIST
Inp 794.00 NIST
Inp 799.00 NIST
Inp 804.00 NIST
Inp 796.00 NIST
Inp 802.00 NIST
Inp 801.00 NIST
Inp 796.00 NIST
Inp 799.00 NIST
Inp 817.00 NIST
Inp 800.00 NIST
Inp 788.00 NIST
Inp 789.00 NIST
Inp 805.00 NIST
Inp 810.00 NIST
Inp 787.00 NIST
Inp 800.00 NIST
Inp Outlier 775.00 NIST
Inp 794.00 NIST
Inp 812.00 NIST
Inp 812.00 NIST
Inp 812.00 NIST
Inp 815.00 NIST
Inp 812.00 NIST
Inp 797.00 NIST
Inp 814.00 NIST
Inp 804.90 NIST
Inp 820.00 NIST
Inp 816.00 NIST
Inp 791.00 NIST
Inp 813.00 NIST
Inp 792.30 NIST
Inp 795.00 NIST
Inp 791.00 NIST
Inp 791.00 NIST
Inp 811.00 NIST
Inp 818.00 NIST
Inp Outlier 830.10 NIST
Inp 794.00 NIST
Inp 813.00 NIST
Inp 817.00 NIST
Inp 797.00 NIST
Inp 799.00 NIST
Inp 793.00 NIST
Inp 819.00 NIST
Inp 802.00 NIST
Inp 812.80 NIST
Inp 802.00 NIST
Inp 814.00 NIST
Inp 814.00 NIST
Inp 820.00 NIST
Inp 816.00 NIST
Inp 815.00 NIST
Inp 812.00 NIST
Inp 810.00 NIST
Inp 812.00 NIST
Inp 813.00 NIST
Inp 791.00 NIST
Inp 794.00 NIST
Inp 793.00 NIST
Inp 792.00 NIST
Inp 790.00 NIST
Inp 788.00 NIST
Inp 794.00 NIST
Inp 796.00 NIST
Inp 805.00 NIST
Inp Outlier 769.00 NIST
Inp 809.00 NIST
Inp 786.00 NIST
Inp 816.00 NIST
Inp 815.00 NIST
Inp 817.00 NIST
Inp Outlier 828.00 NIST
Inp 810.00 NIST
Inp 820.00 NIST
Inp 819.00 NIST
Inp Outlier 829.00 NIST
Inp 812.00 NIST
Inp 815.00 NIST
Inp 817.00 NIST
Inp 812.00 NIST
Inp 812.00 NIST
Inp 812.00 NIST
Inp 800.00 NIST
Inp 810.00 NIST
Inp 823.00 NIST
Inp 815.00 NIST
Inp 795.00 NIST
Inp 813.00 NIST
Inp 795.00 NIST
Inp 808.00 NIST
Inp 807.00 NIST
Inp 796.00 NIST
Inp 823.00 NIST
Inp 799.00 NIST
Inp 798.00 NIST
Inp 812.00 NIST
Inp 813.00 NIST
Inp 789.00 NIST
Inp 794.00 NIST
Inp 786.00 NIST
Inp 794.00 NIST
Inp 793.00 NIST
Inp 798.00 NIST
Inp 818.00 NIST
Inp 800.00 NIST
Inp 793.00 NIST
Inp 793.00 NIST
Inp 814.00 NIST
Inp 798.00 NIST
Inp 800.00 NIST
Inp 797.00 NIST
Inp 796.00 NIST
Inp 808.00 NIST
Inp 800.00 NIST
Inp 813.00 NIST
Inp 819.00 NIST
Inp 811.00 NIST
Inp Outlier 776.00 NIST
Inp 813.00 NIST
Inp 810.00 NIST
Inp 794.00 NIST
Inp 812.00 NIST
Inp 794.00 NIST
Inp 800.00 NIST
Inp 793.00 NIST
Inp 812.00 NIST
Inp 794.00 NIST
Inp 813.00 NIST
Inp 820.00 NIST
Inp 819.00 NIST
Inp 812.00 NIST
Inp 808.00 NIST
Inp 812.00 NIST
Inp 810.00 NIST
Inp 793.00 NIST
Inp 812.00 NIST
Inp 811.00 NIST
Inp 814.00 NIST
Inp 816.00 NIST
Inp 794.00 NIST
Inp 812.00 NIST
Inp 796.00 NIST
Inp 804.00 NIST
Inp 799.00 NIST
Inp 795.00 NIST
Inp 802.00 NIST
Inp 802.00 NIST
Inp 795.00 NIST
Inp 794.00 NIST
Inp 812.00 NIST
Inp 796.00 NIST
Inp 796.00 NIST
Inp 800.00 NIST
Inp 800.00 NIST
Inp 793.00 NIST
Inp 793.00 NIST
Inp 799.00 NIST
Inp 797.00 NIST
Inp 791.00 NIST
Inp 788.00 NIST
Inp 813.00 NIST
Inp 810.00 NIST
Inp 793.00 NIST
Inp 819.00 NIST
Inp 794.00 NIST
Inp 795.00 NIST
Inp 812.00 NIST
Inp 799.00 NIST
Inp 796.00 NIST
Inp 789.00 NIST
Inp 796.20 NIST
Inp 804.70 NIST
Inp 797.88 NIST
Inp 806.60 NIST
Inp Outlier 774.00 NIST
Inp 786.00 NIST
Inp 805.00 NIST
Ip [1036.00; 1114.00]   Show Hide
Ip 1077.00 NIST
Ip 1062.00 NIST
Ip 1075.00 NIST
Ip 1082.00 NIST
Ip 1053.00 NIST
Ip 1064.00 NIST
Ip 1080.00 NIST
Ip 1079.00 NIST
Ip 1091.00 NIST
Ip Outlier 1036.00 NIST
Ip 1068.00 NIST
Ip 1085.00 NIST
Ip 1078.00 NIST
Ip 1075.00 NIST
Ip 1086.00 NIST
Ip 1095.00 NIST
Ip 1078.00 NIST
Ip 1070.00 NIST
Ip 1075.00 NIST
Ip 1075.00 NIST
Ip 1070.00 NIST
Ip 1080.00 NIST
Ip 1075.00 NIST
Ip 1049.00 NIST
Ip Outlier 1100.00 NIST
Ip Outlier 1105.00 NIST
Ip Outlier 1100.00 NIST
Ip 1075.00 NIST
Ip 1057.00 NIST
Ip 1067.00 NIST
Ip 1052.00 NIST
Ip 1086.80 NIST
Ip 1072.00 NIST
Ip 1052.00 NIST
Ip 1056.00 NIST
Ip 1052.00 NIST
Ip 1078.00 NIST
Ip 1086.00 NIST
Ip 1072.00 NIST
Ip 1059.00 NIST
Ip 1072.00 NIST
Ip 1050.00 NIST
Ip 1059.00 NIST
Ip 1064.00 NIST
Ip 1066.00 NIST
Ip 1076.20 NIST
Ip 1075.20 NIST
Ip 1077.40 NIST
Ip 1074.50 NIST
Ip 1074.00 NIST
Ip 1074.40 NIST
Ip 1073.70 NIST
Ip 1074.10 NIST
Ip 1057.00 NIST
Ip 1058.00 NIST
Ip 1065.00 NIST
Ip 1077.00 NIST
Ip 1085.00 NIST
Ip 1075.00 NIST
Ip 1080.00 NIST
Ip 1062.00 NIST
Ip 1062.00 NIST
Ip 1074.00 NIST
Ip 1075.00 NIST
Ip 1080.00 NIST
Ip 1082.00 NIST
Ip 1075.00 NIST
Ip 1067.00 NIST
Ip 1082.00 NIST
Ip 1073.00 NIST
Ip 1065.00 NIST
Ip 1093.00 NIST
Ip 1068.00 NIST
Ip 1046.00 NIST
Ip 1074.00 NIST
Ip 1070.00 NIST
Ip 1077.00 NIST
Ip 1064.00 NIST
Ip 1088.00 NIST
Ip 1059.00 NIST
Ip 1066.00 NIST
Ip 1070.00 NIST
Ip 1075.00 NIST
Ip 1092.00 NIST
Ip Outlier 1105.00 NIST
Ip 1072.00 NIST
Ip 1072.00 NIST
Ip Outlier 1100.00 NIST
Ip 1047.00 NIST
Ip 1076.00 NIST
Ip 1072.00 NIST
Ip 1059.00 NIST
Ip 1071.00 NIST
Ip 1071.00 NIST
Ip 1076.00 NIST
Ip 1077.00 NIST
Ip 1070.00 NIST
Ip 1059.00 NIST
Ip 1068.00 NIST
Ip 1070.00 NIST
Ip Outlier 1114.00 NIST
Ip 1063.00 NIST
Ip 1075.00 NIST
Ip 1098.00 NIST
Ip Outlier 1040.00 NIST
Ip 1059.00 NIST
Ip 1059.00 NIST
Ip 1088.00 NIST
Ip 1077.00 NIST
Ip 1085.00 NIST
Ip 1082.00 NIST
Ip 1082.00 NIST
Ip 1065.00 NIST
Ip 1070.00 NIST
Ip 1082.00 NIST
Ip 1073.00 NIST
Ip 1074.00 NIST
Ip 1082.00 NIST
Ip 1057.00 NIST
Ip 1082.00 NIST
Ip 1060.00 NIST
Ip 1086.00 NIST
Ip 1068.00 NIST
Ip 1086.00 NIST
Ip 1086.00 NIST
Ip 1075.00 NIST
Ip 1070.00 NIST
Ip 1059.00 NIST
Ip 1091.00 NIST
Ip 1078.00 NIST
Ip 1046.00 NIST
Ip 1088.00 NIST
Ip 1092.00 NIST
Ip 1047.00 NIST
Ip 1071.00 NIST
Ip 1068.00 NIST
Ip 1082.00 NIST
Ip 1091.00 NIST
Ip 1063.00 NIST
Ip 1059.00 NIST
Ip 1073.00 NIST
Ip 1060.00 NIST
Ip 1049.00 NIST
Ip 1057.00 NIST
Ip 1052.00 NIST
Ip 1072.00 NIST
Ip 1064.00 NIST
Ip 1074.50 NIST
Tboil [397.15; 399.85] K Show Hide
Tboil 399.11 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 399.15 K Isobaric VLE data for the system of butan-1-ol + butylethanoate + 1-butyl-3-methylimidazoliumbis[(trifluoromethyl)sulfonyl]imide
Tboil 399.07 K Isobaric (vapour + liquid) equilibria of binary systems containing butyl acetate for the separation of methoxy aromatic compounds (anisole and guaiacol) from biomass fast pyrolysis oil
Tboil 399.26 K Vapour-liquid equilibrium and extractive distillation for separation of azeotrope isopropyl alcohol and diisopropyl ether
Tboil 399.09 K Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Tboil 399.15 K Measurement and Correlation of Isobaric Vapor-Liquid Equilibrium for Binary Systems of Allyl Alcohol with Isobutyl Acetate, Butyl Acetate, and Butyl Propionate at 101.3 kPa
Tboil 398.98 K Measurement and Modelization of VLE for Butyl Acetate with Methanol, Ethanol, 1-Propanol, and 1-Butanol. Experimental Data at 0.15 MPa
Tboil 399.18 K Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Tboil 399.11 K Liquid-Liquid Equilibria of Water + Acetoin + Butyl Acetate at several temperatures
Tboil 399.15 K Phase Equilibrium (VLE, LLE, and VLLE) Data of the Ternary System: Ionic Liquid [OMIM][PF6] + Butan-1-ol + Butyl Acetate
Tboil 399.11 K Liquid Liquid Equilibria of Water + 2,3-Butanediol + Butyl Acetate at T ) 298.15 K, T ) 308.15 K, and T ) 318.15 K
Tboil 399.12 K ChemSep v8.3 pure component data Compiled value
Tboil 399.20 K KDB
Tboil Outlier 397.15 K NCMS SOLV-DB
Tboil 399.10 ± 0.10 K NIST
Tboil 399.20 ± 0.40 K NIST
Tboil 398.20 K NIST
Tboil 399.70 K NIST
Tboil 399.00 K NIST
Tboil 399.20 K NIST
Tboil 399.20 ± 0.60 K NIST
Tboil 399.30 ± 0.50 K NIST
Tboil 399.00 ± 2.00 K NIST
Tboil 399.00 ± 3.00 K NIST
Tboil 399.15 K NIST
Tboil 399.85 ± 0.30 K NIST
Tboil 398.00 ± 3.00 K NIST
Tboil 398.15 ± 2.00 K NIST
Tboil 399.15 ± 0.60 K NIST
Tboil 399.24 ± 0.06 K NIST
Tboil 399.26 ± 0.11 K NIST
Tboil 398.00 ± 2.00 K NIST
Tboil 399.40 ± 0.50 K NIST
Tboil 398.00 ± 1.50 K NIST
Tboil 399.65 ± 0.25 K NIST
Tboil Outlier 397.70 ± 1.50 K NIST
Tc [560.20; 579.10] K Show Hide
Tc 575.60 K IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Tc 575.70 K PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc 579.00 K ChemSep v8.3 pure component data Compiled value
Tc 579.00 K KDB
Tc 575.40 ± 0.60 K NIST
Tc 579.00 K NIST
Tc 560.20 ± 10.00 K NIST
Tc 561.00 ± 10.00 K NIST
Tc 579.10 ± 3.00 K NIST
Tfus [195.00; 199.65] K Show Hide
Tfus 195.15 K Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus 199.65 K ChemSep v8.3 pure component data Compiled value
Tfus 195.00 K KDB
Tfus 195.15 K NCMS SOLV-DB
Tfus 199.65 K NIST
Tfus 196.35 ± 0.30 K NIST
Ttriple [196.03; 199.65] K Show Hide
Ttriple 199.65 K ChemSep v8.3 pure component data Compiled value
Ttriple 196.03 ± 0.10 K NIST
Ttriple 196.12 ± 0.05 K NIST
UQi 4.20 ChemSep v8.3 pure component data Compiled value
URi 4.83 ChemSep v8.3 pure component data Compiled value
Vc [0.400; 0.413] m3/kmol Show Hide
Vc 0.400 m3/kmol PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc 0.413 m3/kmol ChemSep v8.3 pure component data Compiled value
Vc 0.400 m3/kmol KDB
Zc [0.2530000; 0.2609000]   Show Hide
Zc 0.2530000 ChemSep v8.3 pure component data Compiled value
Zc 0.2609000 KDB
Zra [0.25; 0.26]   Show Hide
Zra 0.25 ChemSep v8.3 pure component data Compiled value
Zra 0.26 KDB

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,liquid [225.11; 242.30] J/mol×K [292.50; 298.35] Show Hide
Cp,liquid 242.30 J/mol×K 292.50 NIST
Cp,liquid 242.30 J/mol×K 292.50 NIST
Cp,liquid 225.11 J/mol×K 298.15 NIST
Cp,liquid 228.40 J/mol×K 298.15 NIST
Cp,liquid 228.11 J/mol×K 298.35 NIST
η [0.0003840; 0.0007370] Pa×s [293.15; 343.15] Show Hide
η 0.0007320 Pa×s 293.15 Density and Viscosity for a Binary Mixture of cis-3-Hexenyl Formate, Butyl Acetate, trans-2-Hexenyl Acetate, and cis-3-Hexenyl Acetate with Ethanol at Several Temperatures
η 0.0007320 Pa×s 293.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0007370 Pa×s 298.15 NCMS SOLV-DB
η 0.0006740 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 0.0006700 Pa×s 298.15 Binary mixtures of ([C4mim][NTf2] + molecular organic solvents): Thermophysical, acoustic and transport properties at various compositions and temperatures
η 0.0006770 Pa×s 298.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0006860 Pa×s 298.15 Density and Viscosity of Binary Mixtures of n-Butyl Acetate with Ketones at (298.15, 303.15, 308.15, and 313.15) K
η 0.0006250 Pa×s 303.15 Density and Viscosity of Binary Mixtures of n-Butyl Acetate with Ketones at (298.15, 303.15, 308.15, and 313.15) K
η 0.0006400 Pa×s 303.15 Binary mixtures of ([C4mim][NTf2] + molecular organic solvents): Thermophysical, acoustic and transport properties at various compositions and temperatures
η 0.0006280 Pa×s 303.15 Density and Viscosity for a Binary Mixture of cis-3-Hexenyl Formate, Butyl Acetate, trans-2-Hexenyl Acetate, and cis-3-Hexenyl Acetate with Ethanol at Several Temperatures
η 0.0006072 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 0.0006280 Pa×s 303.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0005687 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 0.0005890 Pa×s 308.15 Density and Viscosity of Binary Mixtures of n-Butyl Acetate with Ketones at (298.15, 303.15, 308.15, and 313.15) K
η 0.0005850 Pa×s 308.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0005940 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 0.0005800 Pa×s 308.15 Binary mixtures of ([C4mim][NTf2] + molecular organic solvents): Thermophysical, acoustic and transport properties at various compositions and temperatures
η 0.0005460 Pa×s 313.15 Density and Viscosity for a Binary Mixture of cis-3-Hexenyl Formate, Butyl Acetate, trans-2-Hexenyl Acetate, and cis-3-Hexenyl Acetate with Ethanol at Several Temperatures
η 0.0005460 Pa×s 313.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0005450 Pa×s 313.15 Density and Viscosity of Binary Mixtures of n-Butyl Acetate with Ketones at (298.15, 303.15, 308.15, and 313.15) K
η 0.0005340 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 0.0005700 Pa×s 313.15 Binary mixtures of ([C4mim][NTf2] + molecular organic solvents): Thermophysical, acoustic and transport properties at various compositions and temperatures
η 0.0005120 Pa×s 318.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0005300 Pa×s 318.15 Binary mixtures of ([C4mim][NTf2] + molecular organic solvents): Thermophysical, acoustic and transport properties at various compositions and temperatures
η 0.0004810 Pa×s 323.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0005000 Pa×s 323.15 Binary mixtures of ([C4mim][NTf2] + molecular organic solvents): Thermophysical, acoustic and transport properties at various compositions and temperatures
η 0.0004530 Pa×s 328.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0004280 Pa×s 333.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0004050 Pa×s 338.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0003840 Pa×s 343.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
ΔvapH [36.28; 43.00] kJ/mol [313.00; 399.20] Show Hide
ΔvapH 43.00 ± 0.10 kJ/mol 313.00 NIST
ΔvapH 41.70 ± 0.10 kJ/mol 328.00 NIST
ΔvapH 40.60 ± 0.10 kJ/mol 343.00 NIST
ΔvapH 39.40 ± 0.10 kJ/mol 358.00 NIST
ΔvapH 41.30 kJ/mol 365.00 NIST
ΔvapH 40.80 kJ/mol 365.50 NIST
ΔvapH 40.50 kJ/mol 370.00 NIST
ΔvapH 37.50 kJ/mol 398.00 NIST
ΔvapH 37.50 kJ/mol 398.00 NIST
ΔvapH 36.28 kJ/mol 399.20 NIST
Pvap [1.53; 1602.00] kPa [298.15; 531.45] Show Hide
Pvap 1.53 kPa 298.15 NCMS SOLV-DB
Pvap 8.50 kPa 328.98 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 12.50 kPa 335.89 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 17.00 kPa 346.66 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 21.00 kPa 351.77 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 25.00 kPa 355.56 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 29.77 kPa 361.65 Determination and Prediction of Vapor Liquid Equilibria for a System Containing Water + Butyl Acetate + Cyclohexane + Ethanol
Pvap 29.92 kPa 361.85 Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap 30.00 kPa 362.02 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 34.00 kPa 363.70 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 32.95 kPa 364.47 Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap 37.00 kPa 367.03 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 40.29 kPa 369.66 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 41.50 kPa 369.76 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 41.48 kPa 370.49 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 41.42 kPa 370.90 Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap 42.64 kPa 371.19 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 45.50 kPa 372.26 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 44.02 kPa 372.26 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 45.37 kPa 373.05 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 44.71 kPa 373.15 Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
Pvap 42.55 kPa 373.15 Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
Pvap 45.02 kPa 373.32 Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap 46.58 kPa 373.83 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 48.12 kPa 374.87 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 49.58 kPa 375.76 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 51.50 kPa 376.35 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 50.55 kPa 376.36 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 52.07 kPa 377.33 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 53.38 kPa 378.11 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 54.37 kPa 378.59 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 56.00 kPa 379.26 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 56.01 kPa 379.52 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 56.50 kPa 379.96 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 56.43 kPa 380.10 Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap 57.30 kPa 380.35 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 58.69 kPa 381.07 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 58.85 kPa 381.35 Determination and Prediction of Vapor Liquid Equilibria for a System Containing Water + Butyl Acetate + Cyclohexane + Ethanol
Pvap 60.07 kPa 381.84 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 60.00 kPa 381.99 Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap 60.00 kPa 382.01 Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap 60.15 kPa 382.08 Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap 61.43 kPa 382.55 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 60.50 kPa 383.00 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 62.61 kPa 383.04 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 64.03 kPa 383.86 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 65.43 kPa 384.46 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 66.73 kPa 385.13 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 67.70 kPa 385.64 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 66.50 kPa 385.97 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 69.74 kPa 386.53 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 70.74 kPa 387.08 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 72.02 kPa 387.58 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 74.50 kPa 387.78 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 72.71 kPa 388.06 Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap 73.29 kPa 388.24 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 74.70 kPa 388.78 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 76.50 kPa 389.14 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 76.06 kPa 389.46 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 77.65 kPa 390.04 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 78.73 kPa 390.60 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 80.09 kPa 391.20 Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap 79.50 kPa 391.24 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 80.42 kPa 391.29 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 81.38 kPa 391.73 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 82.99 kPa 392.35 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 83.42 kPa 392.55 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 82.00 kPa 393.08 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 86.50 kPa 393.22 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 86.83 kPa 393.89 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 87.65 kPa 394.25 Determination and Prediction of Vapor Liquid Equilibria for a System Containing Water + Butyl Acetate + Cyclohexane + Ethanol
Pvap 87.98 kPa 394.26 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 88.69 kPa 394.58 Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap 89.08 kPa 394.68 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 90.72 kPa 395.39 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 91.92 kPa 395.76 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 92.00 kPa 395.97 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 93.38 kPa 396.37 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 94.72 kPa 396.86 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 96.04 kPa 397.26 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 97.26 kPa 397.70 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 97.50 kPa 398.20 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 98.80 kPa 398.30 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 99.03 kPa 398.35 Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap 100.02 kPa 398.75 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 101.30 kPa 399.09 Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap 101.30 kPa 399.15 Phase Equilibrium (VLE, LLE, and VLLE) Data of the Ternary System: Ionic Liquid [OMIM][PF6] + Butan-1-ol + Butyl Acetate
Pvap 101.30 kPa 399.15 Isobaric VLE data for the system of butan-1-ol + butylethanoate + 1-butyl-3-methylimidazoliumbis[(trifluoromethyl)sulfonyl]imide
Pvap 101.32 kPa 399.18 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 102.59 kPa 399.56 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 104.16 kPa 400.13 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 106.99 kPa 401.02 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 108.04 kPa 401.45 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 109.22 kPa 401.76 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 110.79 kPa 402.25 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 112.04 kPa 402.73 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 113.10 kPa 403.02 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 114.64 kPa 403.56 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 116.02 kPa 403.97 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 117.33 kPa 404.32 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 118.57 kPa 404.70 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 120.05 kPa 405.20 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 121.55 kPa 405.59 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 122.71 kPa 405.99 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 124.36 kPa 406.47 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 125.41 kPa 406.72 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 126.49 kPa 407.04 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 128.01 kPa 407.47 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 129.32 kPa 407.84 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 127.00 kPa 407.93 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 130.79 kPa 408.31 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 132.03 kPa 408.66 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 133.33 kPa 408.96 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 134.61 kPa 409.37 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 136.01 kPa 409.70 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 137.57 kPa 410.13 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 138.47 kPa 410.36 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 140.29 kPa 410.86 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 141.19 kPa 411.08 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 142.69 kPa 411.53 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 144.17 kPa 411.88 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 145.56 kPa 412.24 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 146.81 kPa 412.59 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 148.01 kPa 412.90 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 149.35 kPa 413.19 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 150.84 kPa 413.61 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 152.16 kPa 413.93 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 153.49 kPa 414.27 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 154.57 kPa 414.48 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 155.00 kPa 414.72 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 155.86 kPa 414.80 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 157.54 kPa 415.25 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 158.72 kPa 415.49 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 159.80 kPa 415.75 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 161.46 kPa 416.19 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 162.90 kPa 416.51 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 164.01 kPa 416.74 Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap 195.63 kPa 423.15 Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
Pvap 188.81 kPa 423.15 Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
Pvap 191.33 kPa 423.15 Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
Pvap 195.00 kPa 423.56 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 217.00 kPa 427.54 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 220.00 kPa 428.55 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 260.00 kPa 435.40 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 275.00 kPa 437.80 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 297.00 kPa 440.65 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 295.00 kPa 440.81 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 342.00 kPa 447.05 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 377.00 kPa 451.67 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 382.00 kPa 452.25 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 407.00 kPa 455.22 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 420.00 kPa 456.75 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 457.00 kPa 460.69 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 480.00 kPa 463.25 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 492.00 kPa 464.05 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 542.00 kPa 469.05 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 583.23 kPa 473.15 Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
Pvap 592.00 kPa 473.70 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 615.00 kPa 475.55 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 637.00 kPa 477.25 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 641.00 kPa 477.55 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 670.00 kPa 479.95 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 692.00 kPa 481.70 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 712.00 kPa 483.15 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 747.00 kPa 485.75 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 790.00 kPa 488.85 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 807.00 kPa 489.95 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 842.00 kPa 492.48 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 885.00 kPa 495.15 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 915.00 kPa 496.95 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 947.00 kPa 498.95 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 970.00 kPa 500.35 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 990.00 kPa 501.65 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 997.00 kPa 501.95 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 998.00 kPa 502.15 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 1005.00 kPa 502.45 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 1012.00 kPa 502.85 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 1050.00 kPa 505.05 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 1092.00 kPa 507.35 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 1107.00 kPa 508.25 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 1135.00 kPa 509.73 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 1187.00 kPa 512.35 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 1225.00 kPa 514.25 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 1267.00 kPa 516.35 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 1307.00 kPa 518.35 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 1357.00 kPa 520.65 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 1395.00 kPa 522.45 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 1447.00 kPa 524.75 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 1472.00 kPa 525.85 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 1501.00 kPa 527.15 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 1537.00 kPa 528.65 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 1577.00 kPa 530.35 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Pvap 1602.00 kPa 531.45 Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
n0 [1.38250; 1.39510]   [293.15; 318.15] Show Hide
n0 1.39510 293.15 Liquid-liquid equilibrium for the ternary system water + 2-methyl-1-propanol + butyl acetate and water + 2-methyl-2-propanol + butyl acetate at (298.15 and 323.15) K
n0 1.39400 293.15 Isobaric Vapor Liquid Equilibrium for Binary Systems of Thioglycolic Acid with Water, Butyl Acetate, Butyl Formate, and Isobutyl Acetate at 101.3 kPa
n0 1.39180 298.15 Thermodynamic study of (alkyl esters + a,x-alkyl dihalides)III. HE m and V E m for 20 binary mixtures {xCu-1H2u-1CO2C4H9 + (1 - x)a,x-ClCH2(CH2)v-2CH2Cl}, where u = 1 to 4, a = 1 and v = x = 2 to 6
n0 1.39190 298.15 Properties of ionic liquid HMIMPF6 with carbonates, ketones and alkyl acetates
n0 1.39176 298.15 Effect of Temperature on the Change of Refractive Index on Mixing for Butyl Acetate + Aromatic Hydrocarbons
n0 1.39180 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 1.39191 298.15 Densities, speeds of sound, and refractive indices of the ternary mixtures (toluene + methyl acetate + butyl acetate) and (toluene + methyl acetate + methyl heptanoate) at 298.15 K
n0 1.39180 298.15 Densities, Excess Molar Volumes, Viscosities, and Refractive Indices of Binary Mixtures of n-Butyl Acetate with 1-Chloroalkanes (C4 C8) at 298.15 K
n0 1.39175 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 1.39160 298.15 Phase Equilibrium for the Esterification Reaction of Acetic Acid + Butan-1-ol at 101.3 kPa
n0 1.39191 298.15 Isobaric Vapor-Liquid Equilibria for the Binary Systems Benzene + Methyl Ethanoate, Benzene + Butyl Ethanoate, and Benzene + Methyl Heptanoate at 101.31kPa
n0 1.39400 298.15 NCMS SOLV-DB
n0 1.38960 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 1.39080 308.15 Topological and thermodynamic investigations of molecular interactions in binary mixtures: Molar excess volumes and molar excess enthalpies
n0 1.38250 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
ρl [849.75; 898.00] kg/m3 [273.00; 323.15] Show Hide
ρl 898.00 kg/m3 273.00 KDB
ρl 881.13 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 881.54 kg/m3 293.15 Volumetric and FT-IR Studies of the Binary Liquid Mixtures of Tributylamine and Alkyl Ester (C1-C5)
ρl 881.10 kg/m3 293.15 Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl 880.61 kg/m3 293.15 Liquid-liquid equilibria and COSMO-SAC modeling of organic solvent/ ionic liquid - hydroxyacetone - water mixtures
ρl 881.38 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 875.80 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 876.38 kg/m3 298.15 Surface Tension and Surface Properties of Binary Mixtures of 1,4-Dioxane or N,N-Dimethyl Formamide with n-Alkyl Acetates
ρl 876.00 kg/m3 298.15 Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl 876.38 kg/m3 298.15 Experimental and theoretical study of surface tension of binary mixtures of (n-alkyl acetates + heptane, benzene, and toluene)
ρl 876.00 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 873.10 kg/m3 298.15 Liquid Liquid Equilibria for the Ternary System n-Butyl Acetate + Pyrocatechol + Water at Different Temperatures at 101.3 kPa
ρl 876.40 kg/m3 298.15 Volumetric and FT-IR Studies of the Binary Liquid Mixtures of Tributylamine and Alkyl Ester (C1-C5)
ρl 875.45 kg/m3 298.15 Liquid-liquid equilibria and COSMO-SAC modeling of organic solvent/ ionic liquid - hydroxyacetone - water mixtures
ρl 876.26 kg/m3 298.20 Isothermal vapor-liquid equilibria, excess molar volume and the deviation of refractive indices for binary mixtures of 1-butanol, 1- hexanol, 3-methyl-1-butanol and butyl acetate
ρl 882.20 kg/m3 298.20 Phase Equilibrium Measurement and Thermodynamic Modeling of the 4-Methylpentan-2-one/3-Methylphenol, and 4-Methylphenol/Water Ternary Systems at 298.2, 313.2, and 323.2 K and 0.1 MPa
ρl 875.80 kg/m3 298.20 Phase equilibria of (water + butyric acid + butyl acetate) ternary systems at different temperatures
ρl 875.60 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 871.28 kg/m3 303.15 Studies of viscosities of dilute solutions of alkylamine in non-electrolyte solvents. II. Haloalkanes and other polar solvents
ρl 870.86 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 870.90 kg/m3 303.15 Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl 870.27 kg/m3 303.15 Liquid-liquid equilibria and COSMO-SAC modeling of organic solvent/ ionic liquid - hydroxyacetone - water mixtures
ρl 871.07 kg/m3 303.15 Excess Volumes and Excess Isentropic Compressibilities of Binary Liquid Mixtures of Trichloroethylene with Esters at 303.15 K
ρl 871.24 kg/m3 303.15 Volumetric and FT-IR Studies of the Binary Liquid Mixtures of Tributylamine and Alkyl Ester (C1-C5)
ρl 865.70 kg/m3 308.15 Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl 865.08 kg/m3 308.15 Liquid-liquid equilibria and COSMO-SAC modeling of organic solvent/ ionic liquid - hydroxyacetone - water mixtures
ρl 865.68 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 866.05 kg/m3 308.15 Volumetric and FT-IR Studies of the Binary Liquid Mixtures of Tributylamine and Alkyl Ester (C1-C5)
ρl 860.50 kg/m3 313.15 Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl 860.84 kg/m3 313.15 Volumetric and FT-IR Studies of the Binary Liquid Mixtures of Tributylamine and Alkyl Ester (C1-C5)
ρl 859.86 kg/m3 313.15 Liquid-liquid equilibria and COSMO-SAC modeling of organic solvent/ ionic liquid - hydroxyacetone - water mixtures
ρl 860.49 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 860.06 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 855.30 kg/m3 318.15 Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl 855.27 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 850.10 kg/m3 323.15 Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl 850.03 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 849.75 kg/m3 323.15 Liquid-Liquid Equilibria, Density, Viscosity, and Surface and Interfacial Tension of the System Water + n-Butyl Acetate + 1-Propanol at 323.15 K and Atmospheric Pressure
csound,fluid [1131.00; 1233.32] m/s [288.15; 313.15] Show Hide
csound,fluid 1233.32 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 1213.05 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 1192.35 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 1190.00 m/s 298.15 Densities, Sound Speed, and IR Studies of (Methanol + 1-Acetoxybutane) and (Methanol + 1,1-Dimethylethyl Ester) at (298.15, 303.15, 308.15, and 313.15) K
csound,fluid 1171.79 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 1173.00 m/s 303.15 Densities, Sound Speed, and IR Studies of (Methanol + 1-Acetoxybutane) and (Methanol + 1,1-Dimethylethyl Ester) at (298.15, 303.15, 308.15, and 313.15) K
csound,fluid 1151.35 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 1150.00 m/s 308.15 Densities, Sound Speed, and IR Studies of (Methanol + 1-Acetoxybutane) and (Methanol + 1,1-Dimethylethyl Ester) at (298.15, 303.15, 308.15, and 313.15) K
csound,fluid 1131.00 m/s 313.15 Densities, Sound Speed, and IR Studies of (Methanol + 1-Acetoxybutane) and (Methanol + 1,1-Dimethylethyl Ester) at (298.15, 303.15, 308.15, and 313.15) K
γ [0.02; 0.03] N/m [298.15; 313.15] Show Hide
γ 0.02 N/m 298.15 Densities, surface tensions, and derived surface thermodynamics properties of (trimethylbenzene + propyl acetate, or butyl acetate) from T = 298.15 K to 313.15 K
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 0.03 N/m 298.15 NCMS SOLV-DB
γ 0.02 N/m 303.15 Densities, surface tensions, and derived surface thermodynamics properties of (trimethylbenzene + propyl acetate, or butyl acetate) from T = 298.15 K to 313.15 K
γ 0.02 N/m 308.15 Densities, surface tensions, and derived surface thermodynamics properties of (trimethylbenzene + propyl acetate, or butyl acetate) from T = 298.15 K to 313.15 K
γ 0.02 N/m 313.15 Densities, surface tensions, and derived surface thermodynamics properties of (trimethylbenzene + propyl acetate, or butyl acetate) from T = 298.15 K to 313.15 K

Datasets

Mass density, kg/m3

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
298.15 100.00 875.7
298.15 1000.00 876.3
298.15 2000.00 877.2
298.15 3000.00 878.0
298.15 3100.00 878.1
298.15 5000.00 879.9
298.15 10000.00 883.8
298.15 15000.00 887.6
298.15 20000.00 891.3
298.15 25000.00 894.9
298.15 30000.00 899.1
298.15 35000.00 903.7
303.15 100.00 870.4
303.15 1000.00 871.1
303.15 2000.00 872.0
303.15 3000.00 872.9
303.15 3100.00 873.0
303.15 5000.00 874.7
303.15 10000.00 878.8
303.15 15000.00 882.8
303.15 20000.00 886.5
303.15 25000.00 890.2
303.15 30000.00 894.4
303.15 35000.00 899.1
308.15 100.00 865.1
308.15 1000.00 865.9
308.15 2000.00 866.9
308.15 3000.00 867.8
308.15 3100.00 867.8
308.15 5000.00 869.6
308.15 10000.00 873.9
308.15 15000.00 878.0
308.15 20000.00 881.9
308.15 25000.00 885.6
308.15 30000.00 890.0
308.15 35000.00 894.8
313.15 100.00 859.9
313.15 1000.00 860.8
313.15 2000.00 861.7
313.15 3000.00 862.7
313.15 3100.00 862.7
313.15 5000.00 864.6
313.15 10000.00 869.0
313.15 15000.00 873.2
313.15 20000.00 877.2
313.15 25000.00 881.0
313.15 30000.00 885.6
313.15 35000.00 890.5
318.15 100.00 854.9
318.15 1000.00 855.7
318.15 2000.00 856.7
318.15 3000.00 857.8
318.15 3100.00 857.9
318.15 5000.00 859.6
318.15 10000.00 864.2
318.15 15000.00 868.5
318.15 20000.00 872.6
318.15 25000.00 876.5
318.15 30000.00 881.3
318.15 35000.00 886.3
323.15 100.00 849.7
323.15 1000.00 851.0
323.15 2000.00 852.0
323.15 3000.00 853.0
323.15 3100.00 853.1
323.15 5000.00 854.6
323.15 10000.00 859.4
323.15 15000.00 863.9
323.15 20000.00 868.1
323.15 25000.00 872.3
323.15 30000.00 877.3
323.15 35000.00 882.4
328.15 100.00 844.6
328.15 1000.00 845.7
328.15 2000.00 846.8
328.15 3000.00 847.9
328.15 3100.00 848.0
328.15 5000.00 849.7
328.15 10000.00 854.6
328.15 15000.00 859.3
328.15 20000.00 863.6
328.15 25000.00 867.8
328.15 30000.00 872.5
328.15 35000.00 877.7
333.15 100.00 839.6
333.15 1000.00 840.7
333.15 2000.00 841.8
333.15 3000.00 842.9
333.15 3100.00 842.9
333.15 5000.00 844.9
333.15 10000.00 850.0
333.15 15000.00 854.8
333.15 20000.00 859.3
333.15 25000.00 863.6
333.15 30000.00 868.6
333.15 35000.00 873.9
338.15 100.00 834.5
338.15 1000.00 835.6
338.15 2000.00 836.7
338.15 3000.00 837.9
338.15 3100.00 838.0
338.15 5000.00 840.1
338.15 10000.00 845.5
338.15 15000.00 850.1
338.15 20000.00 855.0
338.15 25000.00 859.5
338.15 30000.00 864.6
338.15 35000.00 870.1
343.15 100.00 829.5
343.15 1000.00 830.5
343.15 2000.00 831.7
343.15 3000.00 832.9
343.15 3100.00 833.0
343.15 5000.00 835.2
343.15 10000.00 840.7
343.15 15000.00 845.7
343.15 20000.00 850.5
343.15 25000.00 855.1
343.15 30000.00 860.7
343.15 35000.00 866.3
348.15 100.00 824.4
348.15 1000.00 825.4
348.15 2000.00 826.7
348.15 3000.00 827.9
348.15 3100.00 828.0
348.15 5000.00 830.5
348.15 10000.00 836.1
348.15 15000.00 841.3
348.15 20000.00 846.2
348.15 25000.00 850.9
348.15 30000.00 856.6
348.15 35000.00 862.4
353.15 100.00 819.3
353.15 1000.00 820.4
353.15 2000.00 821.7
353.15 3000.00 822.9
353.15 3100.00 823.0
353.15 5000.00 825.5
353.15 10000.00 831.3
353.15 15000.00 836.7
353.15 20000.00 841.8
353.15 25000.00 846.7
353.15 30000.00 852.5
353.15 35000.00 858.4
358.15 100.00 811.6
358.15 1000.00 813.2
358.15 2000.00 813.9
358.15 3100.00 815.3
358.15 5000.00 817.7
358.15 10000.00 823.6
358.15 15000.00 829.1
358.15 20000.00 835.5
363.15 100.00 806.1
363.15 1000.00 807.5
363.15 2000.00 808.8
363.15 3000.00 810.1
363.15 3100.00 810.3
363.15 5000.00 812.8
363.15 10000.00 819.2
363.15 15000.00 824.9
363.15 20000.00 830.4
368.15 100.00 800.3
368.15 1000.00 802.1
368.15 2000.00 803.6
368.15 3000.00 804.8
368.15 3100.00 805.0
368.15 5000.00 807.7
368.15 10000.00 814.3
368.15 15000.00 820.3
368.15 20000.00 825.9
373.15 100.00 795.8
373.15 1000.00 797.2
373.15 2000.00 798.7
373.15 3000.00 800.2
373.15 3100.00 800.4
373.15 5000.00 803.1
373.15 10000.00 809.9
373.15 15000.00 815.9
373.15 20000.00 821.3
378.15 100.00 790.4
378.15 1000.00 791.9
378.15 2000.00 793.7
378.15 3000.00 795.2
378.15 3100.00 795.4
378.15 5000.00 798.0
378.15 10000.00 804.7
378.15 15000.00 810.8
378.15 20000.00 817.1
383.15 100.00 785.2
383.15 1000.00 786.7
383.15 2000.00 788.3
383.15 3000.00 789.9
383.15 3100.00 790.0
383.15 5000.00 792.9
383.15 10000.00 800.1
383.15 15000.00 806.7
383.15 20000.00 812.8
388.15 100.00 779.9
388.15 1000.00 781.6
388.15 2000.00 783.2
388.15 3000.00 785.2
388.15 3100.00 785.4
388.15 5000.00 788.4
388.15 10000.00 795.8
388.15 15000.00 802.4
388.15 20000.00 808.6
393.15 100.00 775.2
393.15 1000.00 776.4
393.15 2000.00 778.1
393.15 3000.00 779.5
393.15 3100.00 779.7
393.15 5000.00 782.8
393.15 10000.00 790.6
393.15 15000.00 797.7
393.15 20000.00 804.2
Reference

Correlations

Property Value Unit Temperature (K) Source
Cp,gas [143.60; 367.96] J/mol×K [273.00; 1200.00] 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 A9.28760e+01
Coefficient B-6.66170e+02
Coefficient C6.52424e+00
Coefficient D-6.61480e-04
Coefficient E3.06780e-07
Temperature range, min.273.00
Temperature range, max.1200.00
Cp,gas 143.60 J/mol×K 273.00 Calculated Property
Cp,gas 187.24 J/mol×K 376.00 Calculated Property
Cp,gas 225.44 J/mol×K 479.00 Calculated Property
Cp,gas 256.66 J/mol×K 582.00 Calculated Property
Cp,gas 282.03 J/mol×K 685.00 Calculated Property
Cp,gas 303.08 J/mol×K 788.00 Calculated Property
Cp,gas 321.20 J/mol×K 891.00 Calculated Property
Cp,gas 337.48 J/mol×K 994.00 Calculated Property
Cp,gas 352.83 J/mol×K 1097.00 Calculated Property
Cp,gas 367.96 J/mol×K 1200.00 Calculated Property
Property Value Unit Temperature (K) Source
Cp,liquid [213.92; 312.67] J/mol×K [202.70; 461.70] 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 A2.01710e+02
Coefficient B-1.90250e+01
Coefficient C1.11134e+00
Coefficient D6.88890e-03
Coefficient E2.15050e-06
Temperature range, min.202.70
Temperature range, max.461.70
Cp,liquid 213.92 J/mol×K 202.70 Calculated Property
Cp,liquid 217.18 J/mol×K 231.48 Calculated Property
Cp,liquid 221.33 J/mol×K 260.26 Calculated Property
Cp,liquid 226.65 J/mol×K 289.03 Calculated Property
Cp,liquid 233.47 J/mol×K 317.81 Calculated Property
Cp,liquid 242.25 J/mol×K 346.59 Calculated Property
Cp,liquid 253.62 J/mol×K 375.37 Calculated Property
Cp,liquid 268.37 J/mol×K 404.14 Calculated Property
Cp,liquid 287.58 J/mol×K 432.92 Calculated Property
Cp,liquid 312.67 J/mol×K 461.70 Calculated Property
Property Value Unit Temperature (K) Source
η [0.0014955; 0.0002523] Pa×s [250.00; 399.26] 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 A-1.70080e+01
Coefficient B1.46110e+03
Coefficient C8.42400e-01
Coefficient D1.11930e-07
Coefficient E2.00000e+00
Temperature range, min.250.00
Temperature range, max.399.26
η 0.0014955 Pa×s 250.00 Calculated Property
η 0.0010985 Pa×s 266.58 Calculated Property
η 0.0008393 Pa×s 283.17 Calculated Property
η 0.0006625 Pa×s 299.75 Calculated Property
η 0.0005376 Pa×s 316.34 Calculated Property
η 0.0004464 Pa×s 332.92 Calculated Property
η 0.0003781 Pa×s 349.51 Calculated Property
η 0.0003258 Pa×s 366.09 Calculated Property
η 0.0002848 Pa×s 382.68 Calculated Property
η 0.0002523 Pa×s 399.26 Calculated Property
Property Value Unit Temperature (K) Source
ΔvapH [53.52; 6.58] kJ/mol [199.65; 575.40] 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 A8.19257e+01
Coefficient B1.15159e+00
Coefficient C8.89674e-02
Coefficient D-1.85987e+00
Coefficient E1.11395e+00
Critical temperature, Tc (K)5.79000e+02
Temperature range, min.199.65
Temperature range, max.575.40
ΔvapH 53.52 kJ/mol 199.65 Calculated Property
ΔvapH 49.18 kJ/mol 241.40 Calculated Property
ΔvapH 45.36 kJ/mol 283.15 Calculated Property
ΔvapH 41.95 kJ/mol 324.90 Calculated Property
ΔvapH 38.80 kJ/mol 366.65 Calculated Property
ΔvapH 35.69 kJ/mol 408.40 Calculated Property
ΔvapH 32.27 kJ/mol 450.15 Calculated Property
ΔvapH 27.94 kJ/mol 491.90 Calculated Property
ΔvapH 21.47 kJ/mol 533.65 Calculated Property
ΔvapH 6.58 kJ/mol 575.40 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [1.33; 202.66] kPa [294.21; 424.78] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.46670e+01
Coefficient B-3.49621e+03
Coefficient C-5.10730e+01
Temperature range, min.294.21
Temperature range, max.424.78
Pvap 1.33 kPa 294.21 Calculated Property
Pvap 3.00 kPa 308.72 Calculated Property
Pvap 6.18 kPa 323.23 Calculated Property
Pvap 11.83 kPa 337.73 Calculated Property
Pvap 21.29 kPa 352.24 Calculated Property
Pvap 36.30 kPa 366.75 Calculated Property
Pvap 59.05 kPa 381.26 Calculated Property
Pvap 92.20 kPa 395.76 Calculated Property
Pvap 138.89 kPa 410.27 Calculated Property
Pvap 202.66 kPa 424.78 Calculated Property
Pvap [2.12e-04; 3090.00] kPa [199.65; 560.22] 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 A8.35202e+01
Coefficient B-7.62534e+03
Coefficient C-1.02228e+01
Coefficient D8.98721e-06
Coefficient E2.00000e+00
CommentRange stopped where the equation exceeds Pc; ChemSep gives it to 575.4 K.
Temperature range, min.199.65
Temperature range, max.560.22
Pvap 2.12e-04 kPa 199.65 Calculated Property
Pvap 0.02 kPa 239.71 Calculated Property
Pvap 0.53 kPa 279.78 Calculated Property
Pvap 5.13 kPa 319.84 Calculated Property
Pvap 27.86 kPa 359.90 Calculated Property
Pvap 103.96 kPa 399.97 Calculated Property
Pvap 300.77 kPa 440.03 Calculated Property
Pvap 729.94 kPa 480.09 Calculated Property
Pvap 1567.27 kPa 520.16 Calculated Property
Pvap 3090.00 kPa 560.22 Calculated Property
Pvap [1.41e-04; 3056.18] kPa [199.65; 579.15] 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 A8.07098e+01
Coefficient B-7.79009e+03
Coefficient C-9.58507e+00
Coefficient D5.19348e-06
Coefficient E0.00000e+00
Temperature range, min.199.65
Temperature range, max.579.15
Pvap 1.41e-04 kPa 199.65 Calculated Property
Pvap 0.02 kPa 241.82 Calculated Property
Pvap 0.64 kPa 283.98 Calculated Property
Pvap 6.72 kPa 326.15 Calculated Property
Pvap 37.57 kPa 368.32 Calculated Property
Pvap 138.45 kPa 410.48 Calculated Property
Pvap 383.82 kPa 452.65 Calculated Property
Pvap 871.75 kPa 494.82 Calculated Property
Pvap 1717.87 kPa 536.98 Calculated Property
Pvap 3056.18 kPa 579.15 Calculated Property
Pvap [9.20; 101.26] kPa [332.89; 399.24] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.44327e+01
Coefficient B-3.31625e+03
Coefficient C-6.13620e+01
ReferenceKliment, Fried, et al., 1964
CommentCoefficents calculated by NIST from author's data.
Temperature range, min.332.89
Temperature range, max.399.24
Pvap 9.20 kPa 332.89 Calculated Property
Pvap 12.71 kPa 340.26 Calculated Property
Pvap 17.26 kPa 347.63 Calculated Property
Pvap 23.09 kPa 355.01 Calculated Property
Pvap 30.44 kPa 362.38 Calculated Property
Pvap 39.61 kPa 369.75 Calculated Property
Pvap 50.92 kPa 377.12 Calculated Property
Pvap 64.71 kPa 384.50 Calculated Property
Pvap 81.35 kPa 391.87 Calculated Property
Pvap 101.26 kPa 399.24 Calculated Property
Property Value Unit Temperature (K) Source
ρl [962.52; 334.86] kg/m3 [199.65; 575.40] 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 A1.57836e+01
Coefficient B1.19300e-01
Coefficient C5.79000e+02
Coefficient D1.63050e-01
Temperature range, min.199.65
Temperature range, max.575.40
ρl 962.52 kg/m3 199.65 Calculated Property
ρl 927.21 kg/m3 241.40 Calculated Property
ρl 889.55 kg/m3 283.15 Calculated Property
ρl 848.98 kg/m3 324.90 Calculated Property
ρl 804.66 kg/m3 366.65 Calculated Property
ρl 755.30 kg/m3 408.40 Calculated Property
ρl 698.68 kg/m3 450.15 Calculated Property
ρl 630.34 kg/m3 491.90 Calculated Property
ρl 538.43 kg/m3 533.65 Calculated Property
ρl 334.86 kg/m3 575.40 Calculated Property
Property Value Unit Temperature (K) Source
γ [0.04; 0.01] N/m [196.15; 399.15] 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 A5.67224e-02
Coefficient B-1.06800e-04
Coefficient C0.00000e+00
Coefficient D0.00000e+00
Coefficient E0.00000e+00
Temperature range, min.196.15
Temperature range, max.399.15
γ 0.04 N/m 196.15 Calculated Property
γ 0.03 N/m 218.71 Calculated Property
γ 0.03 N/m 241.26 Calculated Property
γ 0.03 N/m 263.82 Calculated Property
γ 0.03 N/m 286.37 Calculated Property
γ 0.02 N/m 308.93 Calculated Property
γ 0.02 N/m 331.48 Calculated Property
γ 0.02 N/m 354.04 Calculated Property
γ 0.02 N/m 376.59 Calculated Property
γ 0.01 N/m 399.15 Calculated Property
γ [0.04; 8.05e-06] N/m [199.65; 574.65] 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-1.67320e-02
Coefficient B1.75590e+01
Coefficient C-2.79050e+00
Coefficient D-6.41210e-04
Coefficient E-2.91180e-06
CommentRange stopped where the equation turns negative; ChemSep gives it to 575.4 K.
Temperature range, min.199.65
Temperature range, max.574.65
γ 0.04 N/m 199.65 Calculated Property
γ 0.03 N/m 241.32 Calculated Property
γ 0.03 N/m 282.98 Calculated Property
γ 0.02 N/m 324.65 Calculated Property
γ 0.02 N/m 366.32 Calculated Property
γ 0.01 N/m 407.98 Calculated Property
γ 0.01 N/m 449.65 Calculated Property
γ 0.01 N/m 491.32 Calculated Property
γ 0.00 N/m 532.98 Calculated Property
γ 8.05e-06 N/m 574.65 Calculated Property
Property Value Unit Temperature (K) Source
λgas [0.00; 0.08] W/m×K [199.65; 800.00] 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 A5.93640e-09
Coefficient B2.37390e+00
Coefficient C-4.02220e+02
Coefficient D6.96060e+04
Temperature range, min.199.65
Temperature range, max.800.00
λgas 0.00 W/m×K 199.65 Calculated Property
λgas 0.01 W/m×K 266.36 Calculated Property
λgas 0.01 W/m×K 333.06 Calculated Property
λgas 0.02 W/m×K 399.77 Calculated Property
λgas 0.03 W/m×K 466.47 Calculated Property
λgas 0.04 W/m×K 533.18 Calculated Property
λgas 0.04 W/m×K 599.88 Calculated Property
λgas 0.05 W/m×K 666.59 Calculated Property
λgas 0.06 W/m×K 733.29 Calculated Property
λgas 0.08 W/m×K 800.00 Calculated Property
Property Value Unit Temperature (K) Source
λliquid [0.16; 0.10] W/m×K [199.65; 463.15] 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 A4.36600e-02
Coefficient B-1.25650e+02
Coefficient C-4.06860e-01
Coefficient D-5.93050e-03
Coefficient E2.41670e-06
Temperature range, min.199.65
Temperature range, max.463.15
λliquid 0.16 W/m×K 199.65 Calculated Property
λliquid 0.16 W/m×K 228.93 Calculated Property
λliquid 0.15 W/m×K 258.21 Calculated Property
λliquid 0.14 W/m×K 287.48 Calculated Property
λliquid 0.13 W/m×K 316.76 Calculated Property
λliquid 0.12 W/m×K 346.04 Calculated Property
λliquid 0.12 W/m×K 375.32 Calculated Property
λliquid 0.11 W/m×K 404.59 Calculated Property
λliquid 0.10 W/m×K 433.87 Calculated Property
λliquid 0.10 W/m×K 463.15 Calculated Property

Similar Compounds

butyl-d3 acetate. 1,4-Butanediol, diacetate. Butyl glyoxalate. Propanoic acid, butyl ester. BUTYL CYANOACETATE. pentyl-d2 acetate. pentyl-d3 acetate. Acetic acid, pentyl ester. Acetic acid, bromo-, butyl ester. Acetic acid, chloro-, butyl ester. Butyl iodoacetate. 1,4-Butanediol, dipropionate. butyl-d3 butanoate-d3. butyl-d3 butanoate. Butanoic acid, butyl ester.

Find more compounds similar to Acetic acid, butyl ester.

Mixtures

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Sources

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