Chemical Properties of Acetic acid, hexyl ester (CAS 142-92-7)

Acetic acid, hexyl ester

InChI
InChI=1S/C8H16O2/c1-3-4-5-6-7-10-8(2)9/h3-7H2,1-2H3
InChI Key
AOGQPLXWSUTHQB-UHFFFAOYSA-N
Formula
C8H16O2
SMILES
CCCCCCOC(C)=O
Molecular Weight1
144.21
CAS
142-92-7
Other Names
  • 1-Hexyl acetate
  • Acetic acid n-hexyl ester
  • FEMA No. 2565
  • Hexyl alcohol, acetate
  • Hexyl ester of acetic acid
  • Hexylester kyseliny octove
  • NSC 7323
  • ethanoic acid, hexyl ester
  • hexyl acetate
  • hexyl ethanoate
  • n-Hexyl acetate
  • n-Hexyl ethanoate
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Physical Properties

Property Value Unit Source
ω [0.4614; 0.5042]   Show Hide
ω 0.5042 PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω 0.4614 ChemSep v8.3 pure component data Compiled value
μ 1.86 debye ChemSep v8.3 pure component data Compiled value
Tflash,cc 310.15 K NCMS SOLV-DB
ΔfG° -295.40 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfH°gas -526.30 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfusH° 20.85 kJ/mol Joback Calculated Property
ΔvapH° [51.90; 52.10] kJ/mol Show Hide
ΔvapH° 51.90 ± 0.30 kJ/mol NIST
ΔvapH° 52.10 kJ/mol NIST
IE 9.77 eV Relay (1.0) Calculated Property
log10WS -2.46 Aq. Solubility Prediction
logPoct/wat 2.787 NCMS SOLV-DB
McVol 131.020 ml/mol McGowan Calculated Property
NFPA Fire 2 KDB
NFPA Health 1 KDB
Pc [2381.14; 2410.00] kPa Show Hide
Pc 2381.14 kPa PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc 2410.00 kPa ChemSep v8.3 pure component data Compiled value
Ptriple 8.52e-07 kPa ChemSep v8.3 pure component data Compiled value
Inp [979.20; 1025.00]   Show Hide
Inp 996.50 NIST
Inp 988.13 NIST
Inp 1010.21 NIST
Inp Outlier 979.20 NIST
Inp 984.60 NIST
Inp 993.00 NIST
Inp 993.10 NIST
Inp 1010.90 NIST
Inp 1009.80 NIST
Inp 1008.70 NIST
Inp 1008.00 NIST
Inp 1008.00 NIST
Inp 993.00 NIST
Inp 1000.00 NIST
Inp 1006.00 NIST
Inp 990.60 NIST
Inp 991.10 NIST
Inp 988.00 NIST
Inp 988.00 NIST
Inp 1002.00 NIST
Inp 999.00 NIST
Inp 1010.00 NIST
Inp 1004.00 NIST
Inp 1006.00 NIST
Inp 995.00 NIST
Inp 1000.00 NIST
Inp 995.00 NIST
Inp 999.00 NIST
Inp 1000.00 NIST
Inp 1002.00 NIST
Inp 1006.00 NIST
Inp 1007.00 NIST
Inp 992.00 NIST
Inp 997.00 NIST
Inp 997.00 NIST
Inp Outlier 1024.00 NIST
Inp 1004.00 NIST
Inp 1006.00 NIST
Inp 988.00 NIST
Inp Outlier 1025.00 NIST
Inp 1014.00 NIST
Inp 990.00 NIST
Inp 1008.00 NIST
Inp 1011.00 NIST
Inp 1008.00 NIST
Inp 1008.00 NIST
Inp 1006.00 NIST
Inp 1014.00 NIST
Inp 987.00 NIST
Inp 1010.00 NIST
Inp 1011.00 NIST
Inp 1000.00 NIST
Inp 989.00 NIST
Inp 993.00 NIST
Inp 993.00 NIST
Inp 1013.00 NIST
Inp 997.00 NIST
Inp 1015.00 NIST
Inp 1000.00 NIST
Inp 1002.00 NIST
Inp 1010.00 NIST
Inp 991.00 NIST
Inp 993.00 NIST
Inp 1018.00 NIST
Inp 990.00 NIST
Inp 996.00 NIST
Inp 1018.00 NIST
Inp 993.00 NIST
Inp 1007.00 NIST
Inp 1007.00 NIST
Inp 1007.00 NIST
Inp 1007.00 NIST
Inp 1019.00 NIST
Inp 1014.00 NIST
Inp 1008.00 NIST
Inp 1022.00 NIST
Inp 999.00 NIST
Inp 1005.00 NIST
Inp 1011.00 NIST
Inp 1015.00 NIST
Inp 1011.00 NIST
Inp 1011.00 NIST
Inp 1008.00 NIST
Inp 1013.00 NIST
Inp 1012.00 NIST
Inp 1004.00 NIST
Inp 996.00 NIST
Inp 1016.00 NIST
Inp 1007.00 NIST
Inp 1011.00 NIST
Inp 1013.00 NIST
Inp 1014.00 NIST
Inp 1017.00 NIST
Inp 1016.00 NIST
Inp 991.00 NIST
Inp 1014.00 NIST
Inp 1014.00 NIST
Inp Outlier 983.00 NIST
Inp 1015.00 NIST
Inp 997.00 NIST
Inp 1019.00 NIST
Inp 993.00 NIST
Inp 1015.00 NIST
Inp 1017.00 NIST
Inp 1014.00 NIST
Inp 992.00 NIST
Inp 1008.00 NIST
Inp 1008.00 NIST
Inp 995.00 NIST
Inp 1015.00 NIST
Inp 1009.00 NIST
Inp 988.00 NIST
Inp 1009.00 NIST
Inp 1020.00 NIST
Inp 999.00 NIST
Inp 1015.00 NIST
Inp 1012.00 NIST
Inp 1014.00 NIST
Inp 986.00 NIST
Inp 997.00 NIST
Inp 999.00 NIST
Inp 1007.00 NIST
Inp 991.00 NIST
Inp 1017.00 NIST
Inp 1002.00 NIST
Inp 1008.00 NIST
Inp 1009.00 NIST
Inp 1007.00 NIST
Inp 994.00 NIST
Inp 1005.00 NIST
Inp 1012.00 NIST
Inp 1010.00 NIST
Inp 1000.00 NIST
Inp 992.00 NIST
Inp 995.00 NIST
Inp 991.00 NIST
Inp 995.00 NIST
Inp 991.00 NIST
Inp 993.00 NIST
Inp 1012.00 NIST
Inp 992.00 NIST
Inp 989.00 NIST
Inp 992.00 NIST
Inp 994.00 NIST
Inp 988.00 NIST
Inp 990.00 NIST
Inp 1002.00 NIST
Inp 997.00 NIST
Inp 997.00 NIST
Inp 995.00 NIST
Inp 997.00 NIST
Inp 996.00 NIST
Inp 998.00 NIST
Inp 1007.00 NIST
Inp 1016.00 NIST
Inp 997.00 NIST
Inp 996.00 NIST
Inp 1015.00 NIST
Inp 1018.00 NIST
Inp 997.00 NIST
Inp 1009.00 NIST
Inp 1015.00 NIST
Inp 1022.00 NIST
Inp 1013.00 NIST
Inp 1007.00 NIST
Inp 988.00 NIST
Inp 1003.00 NIST
Inp 1006.00 NIST
Inp 1009.00 NIST
Inp 1013.00 NIST
Inp 1015.00 NIST
Inp 990.00 NIST
Inp 1011.00 NIST
Inp 1012.00 NIST
Inp 1010.00 NIST
Inp Outlier 1024.00 NIST
Inp 1010.00 NIST
Inp 1012.00 NIST
Inp 997.00 NIST
Inp 988.00 NIST
Inp 1009.00 NIST
Inp 1012.00 NIST
Inp 1008.00 NIST
Inp 1012.00 NIST
Inp 1011.00 NIST
Inp 992.00 NIST
Inp 1008.00 NIST
Inp 1008.00 NIST
Inp 1008.00 NIST
Inp 1008.00 NIST
Inp 995.00 NIST
Inp 1015.00 NIST
Inp 1014.00 NIST
Inp 1008.00 NIST
Inp 1012.00 NIST
Inp 1015.00 NIST
Inp 1008.00 NIST
Inp 1010.00 NIST
Inp 993.00 NIST
Inp 996.00 NIST
Inp 992.00 NIST
Inp 1003.00 NIST
Inp 995.00 NIST
Inp 997.00 NIST
Inp 992.00 NIST
Inp 995.00 NIST
Inp 995.00 NIST
Inp 1012.00 NIST
Inp 1012.00 NIST
Inp 994.00 NIST
Inp 1000.00 NIST
Inp 990.00 NIST
Inp 1007.00 NIST
Inp 1018.00 NIST
Inp 1013.00 NIST
Inp 1009.00 NIST
Inp 1012.00 NIST
Inp 997.00 NIST
Inp 1008.00 NIST
Inp 993.00 NIST
Inp 996.50 NIST
Inp 990.60 NIST
Inp 999.00 NIST
Ip [1235.00; 1311.00]   Show Hide
Ip 1277.00 NIST
Ip 1255.00 NIST
Ip 1286.00 NIST
Ip 1295.00 NIST
Ip 1277.00 NIST
Ip Outlier 1299.00 NIST
Ip Outlier 1301.00 NIST
Ip 1262.00 NIST
Ip 1268.00 NIST
Ip 1276.00 NIST
Ip 1276.00 NIST
Ip 1276.00 NIST
Ip 1274.00 NIST
Ip 1276.00 NIST
Ip 1296.00 NIST
Ip 1278.00 NIST
Ip 1280.00 NIST
Ip Outlier 1305.00 NIST
Ip 1270.00 NIST
Ip 1270.00 NIST
Ip 1269.00 NIST
Ip 1272.00 NIST
Ip 1266.00 NIST
Ip 1279.00 NIST
Ip 1280.00 NIST
Ip 1275.00 NIST
Ip 1269.00 NIST
Ip 1275.00 NIST
Ip 1279.00 NIST
Ip 1265.00 NIST
Ip 1275.00 NIST
Ip 1268.00 NIST
Ip 1254.00 NIST
Ip 1293.00 NIST
Ip Outlier 1311.00 NIST
Ip 1271.00 NIST
Ip 1282.00 NIST
Ip 1277.00 NIST
Ip 1265.00 NIST
Ip 1270.00 NIST
Ip 1261.00 NIST
Ip 1267.00 NIST
Ip 1251.00 NIST
Ip 1264.00 NIST
Ip 1265.00 NIST
Ip 1264.00 NIST
Ip 1267.00 NIST
Ip 1272.00 NIST
Ip 1275.00 NIST
Ip 1295.00 NIST
Ip 1295.00 NIST
Ip 1295.00 NIST
Ip 1265.00 NIST
Ip 1267.00 NIST
Ip Outlier 1248.00 NIST
Ip 1257.00 NIST
Ip 1264.00 NIST
Ip 1269.00 NIST
Ip 1272.00 NIST
Ip Outlier 1308.00 NIST
Ip 1285.00 NIST
Ip 1279.00 NIST
Ip 1251.00 NIST
Ip 1258.00 NIST
Ip 1258.00 NIST
Ip 1286.00 NIST
Ip 1275.00 NIST
Ip 1263.00 NIST
Ip 1251.00 NIST
Ip 1275.00 NIST
Ip 1268.00 NIST
Ip Outlier 1307.00 NIST
Ip 1276.00 NIST
Ip 1282.00 NIST
Ip 1280.00 NIST
Ip 1269.00 NIST
Ip 1272.00 NIST
Ip 1277.00 NIST
Ip 1270.00 NIST
Ip 1270.00 NIST
Ip 1257.00 NIST
Ip 1275.00 NIST
Ip 1282.00 NIST
Ip 1274.00 NIST
Ip 1254.00 NIST
Ip 1254.00 NIST
Ip 1270.00 NIST
Ip 1274.00 NIST
Ip 1263.00 NIST
Ip 1276.00 NIST
Ip 1291.00 NIST
Ip Outlier 1307.00 NIST
Ip 1274.00 NIST
Ip 1259.00 NIST
Ip 1278.00 NIST
Ip 1271.00 NIST
Ip 1274.00 NIST
Ip 1269.00 NIST
Ip 1271.00 NIST
Ip 1272.00 NIST
Ip Outlier 1235.00 NIST
Ip 1289.00 NIST
Ip 1290.00 NIST
Ip 1268.00 NIST
Ip 1262.00 NIST
Ip 1267.00 NIST
Ip 1273.00 NIST
Ip 1271.00 NIST
Ip 1267.00 NIST
Ip 1280.00 NIST
Ip 1265.00 NIST
Ip 1279.00 NIST
Ip 1277.00 NIST
Ip 1270.00 NIST
Ip Outlier 1307.00 NIST
Ip 1270.00 NIST
Ip 1290.00 NIST
Ip 1264.00 NIST
Ip 1265.00 NIST
Ip 1264.00 NIST
Ip 1265.00 NIST
Ip 1272.00 NIST
Ip 1272.00 NIST
Ip 1264.00 NIST
Ip 1265.00 NIST
Ip 1264.00 NIST
Ip 1265.00 NIST
Ip 1275.00 NIST
Ip 1272.00 NIST
Ip 1281.00 NIST
Ip 1271.00 NIST
Ip 1276.00 NIST
Ip 1266.00 NIST
Ip 1276.00 NIST
Ip 1281.00 NIST
Ip 1283.00 NIST
Ip 1274.00 NIST
Ip 1279.00 NIST
Ip 1292.00 NIST
Ip 1259.00 NIST
Ip 1259.00 NIST
Ip 1278.00 NIST
Ip 1265.00 NIST
Ip 1287.00 NIST
Ip 1269.00 NIST
Ip 1271.00 NIST
Ip 1283.00 NIST
Ip 1287.00 NIST
Ip 1283.00 NIST
Ip 1279.00 NIST
Ip Outlier 1308.00 NIST
Ip 1258.00 NIST
Ip 1268.00 NIST
Ip 1276.00 NIST
Ip 1267.00 NIST
Ip 1281.00 NIST
Ip 1278.00 NIST
Ip 1283.00 NIST
Ip Outlier 1303.00 NIST
Ip 1267.00 NIST
Ip 1273.00 NIST
Ip 1272.00 NIST
Ip 1275.00 NIST
Ip 1282.00 NIST
Ip 1283.00 NIST
Ip 1275.00 NIST
Ip 1260.00 NIST
Ip 1283.00 NIST
Ip 1265.00 NIST
Ip 1269.00 NIST
Ip 1278.00 NIST
Ip 1294.00 NIST
Ip 1283.00 NIST
Ip 1264.00 NIST
Ip 1268.00 NIST
Ip 1283.00 NIST
Ip 1266.00 NIST
Ip 1269.00 NIST
Ip 1283.00 NIST
Ip 1282.00 NIST
Ip 1281.00 NIST
Ip 1270.00 NIST
Ip 1270.00 NIST
Ip 1264.00 NIST
Ip 1262.00 NIST
Ip 1274.00 NIST
Ip Outlier 1305.00 NIST
Ip 1266.00 NIST
Ip 1279.00 NIST
Ip 1275.00 NIST
Ip 1265.00 NIST
Ip 1287.00 NIST
Ip 1268.00 NIST
Ip 1283.00 NIST
Ip 1269.00 NIST
Ip 1270.00 NIST
Tboil [429.15; 464.00] K Show Hide
Tboil 444.65 K ChemSep v8.3 pure component data Compiled value
Tboil 444.63 K KDB
Tboil 442.35 K NCMS SOLV-DB
Tboil 442.20 K NIST
Tboil 442.00 K NIST
Tboil Outlier 464.00 ± 2.00 K NIST
Tboil 441.00 ± 4.00 K NIST
Tboil 441.15 ± 1.00 K NIST
Tboil 443.65 ± 1.00 K NIST
Tboil 444.63 ± 0.30 K NIST
Tboil 429.15 ± 3.00 K NIST
Tboil 442.40 ± 1.50 K NIST
Tc [618.40; 623.50] K Show Hide
Tc 618.40 K IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Tc 618.40 K PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc 623.50 K ChemSep v8.3 pure component data Compiled value
Tfus [192.25; 212.25] K Show Hide
Tfus 193.15 K Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus 192.25 K ChemSep v8.3 pure component data Compiled value
Tfus 212.25 K KDB
Tfus 192.85 K Aq. Solubility Prediction
Tfus 193.15 K NCMS SOLV-DB
Tfus 212.10 ± 0.05 K NIST
Tfus 192.30 ± 0.50 K NIST
Ttriple 192.25 K ChemSep v8.3 pure component data Compiled value
UQi 5.28 ChemSep v8.3 pure component data Compiled value
URi 6.18 ChemSep v8.3 pure component data Compiled value
Vc [0.519; 0.524] m3/kmol Show Hide
Vc 0.524 m3/kmol PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc 0.519 m3/kmol ChemSep v8.3 pure component data Compiled value
Zc 0.2440000 ChemSep v8.3 pure component data Compiled value
Zra 0.24 ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
η [0.0005790; 0.0011180] Pa×s [293.15; 343.15] Show Hide
η 0.0011180 Pa×s 293.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0010360 Pa×s 298.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0010750 Pa×s 298.15 NCMS SOLV-DB
η 0.0009620 Pa×s 303.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0008950 Pa×s 308.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0008360 Pa×s 313.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0007820 Pa×s 318.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0007330 Pa×s 323.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0006890 Pa×s 328.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0006490 Pa×s 333.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0006120 Pa×s 338.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0005790 Pa×s 343.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
ΔfusH [19.83; 19.83] kJ/mol [212.10; 212.10] Show Hide
ΔfusH 19.83 kJ/mol 212.10 NIST
ΔfusH 19.83 kJ/mol 212.10 NIST
ΔvapH [46.20; 50.90] kJ/mol [342.50; 418.50] Show Hide
ΔvapH 48.90 kJ/mol 342.50 NIST
ΔvapH 50.90 kJ/mol 373.50 NIST
ΔvapH 46.20 kJ/mol 418.50 NIST
Pvap [0.03; 90.00] kPa [274.50; 439.98] Show Hide
Pvap 0.03 kPa 274.50 Vapour pressures and enthalpies of vaporization of a series of the linear n-alkyl acetates
Pvap 0.03 kPa 277.70 Vapour pressures and enthalpies of vaporization of a series of the linear n-alkyl acetates
Pvap 0.04 kPa 280.80 Vapour pressures and enthalpies of vaporization of a series of the linear n-alkyl acetates
Pvap 0.05 kPa 283.80 Vapour pressures and enthalpies of vaporization of a series of the linear n-alkyl acetates
Pvap 0.07 kPa 286.90 Vapour pressures and enthalpies of vaporization of a series of the linear n-alkyl acetates
Pvap 0.08 kPa 289.90 Vapour pressures and enthalpies of vaporization of a series of the linear n-alkyl acetates
Pvap 0.10 kPa 291.90 Vapour pressures and enthalpies of vaporization of a series of the linear n-alkyl acetates
Pvap 0.12 kPa 294.00 Vapour pressures and enthalpies of vaporization of a series of the linear n-alkyl acetates
Pvap 0.15 kPa 297.00 Vapour pressures and enthalpies of vaporization of a series of the linear n-alkyl acetates
Pvap 0.18 kPa 300.00 Vapour pressures and enthalpies of vaporization of a series of the linear n-alkyl acetates
Pvap 0.23 kPa 303.10 Vapour pressures and enthalpies of vaporization of a series of the linear n-alkyl acetates
Pvap 0.27 kPa 306.10 Vapour pressures and enthalpies of vaporization of a series of the linear n-alkyl acetates
Pvap 0.33 kPa 309.10 Vapour pressures and enthalpies of vaporization of a series of the linear n-alkyl acetates
Pvap 0.67 kPa 318.15 NCMS SOLV-DB
Pvap 25.00 kPa 397.97 Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap 30.00 kPa 403.36 Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap 35.00 kPa 408.02 Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap 40.00 kPa 412.14 Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap 45.00 kPa 416.02 Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap 50.00 kPa 419.47 Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap 55.00 kPa 422.59 Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap 60.00 kPa 425.57 Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap 65.00 kPa 428.26 Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap 70.00 kPa 430.93 Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap 75.00 kPa 433.38 Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap 80.00 kPa 435.68 Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap 85.00 kPa 437.92 Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap 90.00 kPa 439.98 Phase Equlibria for Hexyl Acetate Reactive Distillation
n0 [1.40900; 1.40960]   [293.15; 298.15] Show Hide
n0 1.40960 293.15 Liquid-liquid equilibria study of the (water + phosphoric acid + hexyl or cyclohexyl acetate) systems at T = (298.15, 308.15, and 318.15) K: Measurement and thermodynamic modelling
n0 1.40900 298.15 NCMS SOLV-DB
ρl [855.00; 868.52] kg/m3 [298.15; 313.15] Show Hide
ρl 868.52 kg/m3 298.15 Experimental and theoretical study of surface tension of binary mixtures of (n-alkyl acetates + heptane, benzene, and toluene)
ρl 868.30 kg/m3 298.15 Densities, Viscosities, and Sound Speed of Binary Mixtures of Hexyl Acetate with Tetrahydrofuran, 1,4-Dioxane, Anisole, and Butyl Vinyl Ether
ρl 868.52 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 863.90 kg/m3 303.15 Densities, Viscosities, and Sound Speed of Binary Mixtures of Hexyl Acetate with Tetrahydrofuran, 1,4-Dioxane, Anisole, and Butyl Vinyl Ether
ρl 859.80 kg/m3 308.15 Densities, Viscosities, and Sound Speed of Binary Mixtures of Hexyl Acetate with Tetrahydrofuran, 1,4-Dioxane, Anisole, and Butyl Vinyl Ether
ρl 855.00 kg/m3 313.15 Densities, Viscosities, and Sound Speed of Binary Mixtures of Hexyl Acetate with Tetrahydrofuran, 1,4-Dioxane, Anisole, and Butyl Vinyl Ether
γ 0.03 N/m 298.15 NCMS SOLV-DB

Correlations

Property Value Unit Temperature (K) Source
Cp,gas [182.34; 511.83] J/mol×K [273.00; 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 A7.42750e+01
Coefficient B-4.23100e+02
Coefficient C6.18024e+00
Coefficient D2.07210e-04
Coefficient E-5.67940e-08
Temperature range, min.273.00
Temperature range, max.1500.00
Cp,gas 182.34 J/mol×K 273.00 Calculated Property
Cp,gas 259.56 J/mol×K 409.33 Calculated Property
Cp,gas 319.22 J/mol×K 545.67 Calculated Property
Cp,gas 365.69 J/mol×K 682.00 Calculated Property
Cp,gas 402.85 J/mol×K 818.33 Calculated Property
Cp,gas 433.20 J/mol×K 954.67 Calculated Property
Cp,gas 458.37 J/mol×K 1091.00 Calculated Property
Cp,gas 479.43 J/mol×K 1227.33 Calculated Property
Cp,gas 497.09 J/mol×K 1363.67 Calculated Property
Cp,gas 511.83 J/mol×K 1500.00 Calculated Property
Property Value Unit Temperature (K) Source
Cp,liquid [287.14; 355.22] J/mol×K [298.00; 444.65] 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 A1.52410e+02
Coefficient B8.49230e+02
Coefficient C-3.33276e+00
Coefficient D2.40240e-02
Coefficient E-1.99640e-05
Temperature range, min.298.00
Temperature range, max.444.65
Cp,liquid 287.14 J/mol×K 298.00 Calculated Property
Cp,liquid 293.28 J/mol×K 314.29 Calculated Property
Cp,liquid 300.28 J/mol×K 330.59 Calculated Property
Cp,liquid 307.92 J/mol×K 346.88 Calculated Property
Cp,liquid 316.00 J/mol×K 363.18 Calculated Property
Cp,liquid 324.29 J/mol×K 379.47 Calculated Property
Cp,liquid 332.59 J/mol×K 395.77 Calculated Property
Cp,liquid 340.66 J/mol×K 412.06 Calculated Property
Cp,liquid 348.28 J/mol×K 428.36 Calculated Property
Cp,liquid 355.22 J/mol×K 444.65 Calculated Property
Property Value Unit Temperature (K) Source
η [0.0151173; 0.0001042] Pa×s [192.25; 573.00] 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-1.18530e+01
Coefficient B1.43790e+03
Coefficient C3.56800e-02
Coefficient D-1.58870e-07
Coefficient E2.00000e+00
Temperature range, min.192.25
Temperature range, max.573.00
η 0.0151173 Pa×s 192.25 Calculated Property
η 0.0039395 Pa×s 234.56 Calculated Property
η 0.0015478 Pa×s 276.86 Calculated Property
η 0.0007784 Pa×s 319.17 Calculated Property
η 0.0004594 Pa×s 361.47 Calculated Property
η 0.0003024 Pa×s 403.78 Calculated Property
η 0.0002153 Pa×s 446.08 Calculated Property
η 0.0001623 Pa×s 488.39 Calculated Property
η 0.0001279 Pa×s 530.69 Calculated Property
η 0.0001042 Pa×s 573.00 Calculated Property
Property Value Unit Temperature (K) Source
ΔvapH [57.64; 11.62] kJ/mol [192.25; 618.00] 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 A7.63650e+01
Coefficient B1.35350e+00
Coefficient C-2.72660e+00
Coefficient D3.01890e+00
Coefficient E-1.25160e+00
Critical temperature, Tc (K)6.23500e+02
Temperature range, min.192.25
Temperature range, max.618.00
ΔvapH 57.64 kJ/mol 192.25 Calculated Property
ΔvapH 54.90 kJ/mol 239.56 Calculated Property
ΔvapH 52.23 kJ/mol 286.86 Calculated Property
ΔvapH 49.43 kJ/mol 334.17 Calculated Property
ΔvapH 46.30 kJ/mol 381.47 Calculated Property
ΔvapH 42.72 kJ/mol 428.78 Calculated Property
ΔvapH 38.52 kJ/mol 476.08 Calculated Property
ΔvapH 33.43 kJ/mol 523.39 Calculated Property
ΔvapH 26.60 kJ/mol 570.69 Calculated Property
ΔvapH 11.62 kJ/mol 618.00 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [1.33; 202.64] kPa [334.82; 468.91] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.54294e+01
Coefficient B-4.08917e+03
Coefficient C-6.47630e+01
Temperature range, min.334.82
Temperature range, max.468.91
Pvap 1.33 kPa 334.82 Calculated Property
Pvap 2.94 kPa 349.72 Calculated Property
Pvap 6.00 kPa 364.62 Calculated Property
Pvap 11.45 kPa 379.52 Calculated Property
Pvap 20.59 kPa 394.42 Calculated Property
Pvap 35.21 kPa 409.31 Calculated Property
Pvap 57.59 kPa 424.21 Calculated Property
Pvap 90.56 kPa 439.11 Calculated Property
Pvap 137.57 kPa 454.01 Calculated Property
Pvap 202.64 kPa 468.91 Calculated Property
Pvap [3.50e-07; 2528.38] kPa [192.25; 618.00] 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 A1.28292e+02
Coefficient B-1.07780e+04
Coefficient C-1.66330e+01
Coefficient D1.01460e-05
Coefficient E2.00000e+00
Temperature range, min.192.25
Temperature range, max.618.00
Pvap 3.50e-07 kPa 192.25 Calculated Property
Pvap 7.13e-04 kPa 239.56 Calculated Property
Pvap 0.08 kPa 286.86 Calculated Property
Pvap 1.66 kPa 334.17 Calculated Property
Pvap 14.12 kPa 381.47 Calculated Property
Pvap 67.32 kPa 428.78 Calculated Property
Pvap 221.56 kPa 476.08 Calculated Property
Pvap 573.01 kPa 523.39 Calculated Property
Pvap 1266.15 kPa 570.69 Calculated Property
Pvap 2528.38 kPa 618.00 Calculated Property
Pvap [8.33e-07; 2452.89] kPa [192.25; 618.00] 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 A8.03443e+01
Coefficient B-8.74286e+03
Coefficient C-9.31977e+00
Coefficient D3.93049e-06
Coefficient E0.00000e+00
Temperature range, min.192.25
Temperature range, max.618.00
Pvap 8.33e-07 kPa 192.25 Calculated Property
Pvap 9.23e-04 kPa 239.56 Calculated Property
Pvap 0.08 kPa 286.86 Calculated Property
Pvap 1.58 kPa 334.17 Calculated Property
Pvap 13.47 kPa 381.47 Calculated Property
Pvap 66.03 kPa 428.78 Calculated Property
Pvap 223.43 kPa 476.08 Calculated Property
Pvap 585.15 kPa 523.39 Calculated Property
Pvap 1278.59 kPa 570.69 Calculated Property
Pvap 2452.89 kPa 618.00 Calculated Property
Property Value Unit Temperature (K) Source
ρl [958.15; 477.29] kg/m3 [192.25; 595.59] 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 A5.73976e+01
Coefficient B2.28280e-01
Coefficient C6.23500e+02
Coefficient D2.68790e-01
Temperature range, min.192.25
Temperature range, max.595.59
ρl 958.15 kg/m3 192.25 Calculated Property
ρl 921.61 kg/m3 237.07 Calculated Property
ρl 883.42 kg/m3 281.88 Calculated Property
ρl 843.18 kg/m3 326.70 Calculated Property
ρl 800.39 kg/m3 371.51 Calculated Property
ρl 754.25 kg/m3 416.33 Calculated Property
ρl 703.49 kg/m3 461.14 Calculated Property
ρl 645.81 kg/m3 505.96 Calculated Property
ρl 576.11 kg/m3 550.77 Calculated Property
ρl 477.29 kg/m3 595.59 Calculated Property
Property Value Unit Temperature (K) Source
γ [0.04; 0.01] N/m [192.15; 444.15] 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 A5.49355e-02
Coefficient B-9.70000e-05
Coefficient C0.00000e+00
Coefficient D0.00000e+00
Coefficient E0.00000e+00
Temperature range, min.192.15
Temperature range, max.444.15
γ 0.04 N/m 192.15 Calculated Property
γ 0.03 N/m 220.15 Calculated Property
γ 0.03 N/m 248.15 Calculated Property
γ 0.03 N/m 276.15 Calculated Property
γ 0.03 N/m 304.15 Calculated Property
γ 0.02 N/m 332.15 Calculated Property
γ 0.02 N/m 360.15 Calculated Property
γ 0.02 N/m 388.15 Calculated Property
γ 0.01 N/m 416.15 Calculated Property
γ 0.01 N/m 444.15 Calculated Property
γ [0.04; 1.39e-05] N/m [192.25; 617.57] 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-1.63810e-02
Coefficient B1.94160e+01
Coefficient C-2.82260e+00
Coefficient D-6.25580e-04
Coefficient E-2.44700e-06
CommentRange stopped where the equation turns negative; ChemSep gives it to 618 K.
Temperature range, min.192.25
Temperature range, max.617.57
γ 0.04 N/m 192.25 Calculated Property
γ 0.03 N/m 239.51 Calculated Property
γ 0.03 N/m 286.77 Calculated Property
γ 0.02 N/m 334.02 Calculated Property
γ 0.02 N/m 381.28 Calculated Property
γ 0.01 N/m 428.54 Calculated Property
γ 0.01 N/m 475.80 Calculated Property
γ 0.01 N/m 523.06 Calculated Property
γ 0.00 N/m 570.32 Calculated Property
γ 1.39e-05 N/m 617.57 Calculated Property
Property Value Unit Temperature (K) Source
λgas [0.00; 0.10] W/m×K [192.25; 1000.00] 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 A-9.69910e+01
Coefficient B-1.05350e-03
Coefficient C5.17260e+04
Coefficient D-1.01930e+09
Temperature range, min.192.25
Temperature range, max.1000.00
λgas 0.00 W/m×K 192.25 Calculated Property
λgas 0.01 W/m×K 282.00 Calculated Property
λgas 0.01 W/m×K 371.75 Calculated Property
λgas 0.02 W/m×K 461.50 Calculated Property
λgas 0.03 W/m×K 551.25 Calculated Property
λgas 0.04 W/m×K 641.00 Calculated Property
λgas 0.05 W/m×K 730.75 Calculated Property
λgas 0.07 W/m×K 820.50 Calculated Property
λgas 0.08 W/m×K 910.25 Calculated Property
λgas 0.10 W/m×K 1000.00 Calculated Property
Property Value Unit Temperature (K) Source
λliquid [0.17; 0.09] W/m×K [192.25; 533.15] 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 A7.62170e-02
Coefficient B4.32060e+02
Coefficient C-6.62170e+00
Coefficient D1.43540e-02
Coefficient E-2.13400e-05
Temperature range, min.192.25
Temperature range, max.533.15
λliquid 0.17 W/m×K 192.25 Calculated Property
λliquid 0.15 W/m×K 230.13 Calculated Property
λliquid 0.14 W/m×K 268.01 Calculated Property
λliquid 0.14 W/m×K 305.88 Calculated Property
λliquid 0.13 W/m×K 343.76 Calculated Property
λliquid 0.12 W/m×K 381.64 Calculated Property
λliquid 0.11 W/m×K 419.52 Calculated Property
λliquid 0.10 W/m×K 457.39 Calculated Property
λliquid 0.10 W/m×K 495.27 Calculated Property
λliquid 0.09 W/m×K 533.15 Calculated Property

Similar Compounds

hexyl-d3 acetate. Acetic acid, heptyl ester. nonacosyl acetate. Eicosanyl acetate. 1-Pentadecanol acetate. Triacontyl acetate. Acetic acid, octyl ester. pentacosyl acetate. 1-Docosanol, acetate. Tridecyl acetate. 1-Undecanol, acetate. Acetic acid, nonyl ester. Heneicosyl acetate. hentriacontyl acetate. Tetracosyl acetate.

Find more compounds similar to Acetic acid, hexyl ester.

Mixtures

Sources

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