Chemical Properties of Hexanoic acid, ethyl ester (CAS 123-66-0)

Hexanoic acid, ethyl ester

InChI
InChI=1S/C8H16O2/c1-3-5-6-7-8(9)10-4-2/h3-7H2,1-2H3
InChI Key
SHZIWNPUGXLXDT-UHFFFAOYSA-N
Formula
C8H16O2
SMILES
CCCCCC(=O)OCC
Molecular Weight1
144.21
CAS
123-66-0
Other Names
  • 8068-81-3
  • Acetic acid, butyl-, ethyl ester
  • Caproic acid ethyl ester
  • Ethyl butyl acetate
  • Ethyl caproate
  • Ethyl ester of hexanoic acid
  • Ethyl hexanoate
  • Ethyl hexoate
  • Ethyl n-hexanoate
  • NSC 8882
  • n-Caproic acid ethyl ester
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Physical Properties

Property Value Unit Source
ω 0.5236 Relay (1.0) Calculated Property
Δf -217.44 kJ/mol Joback Calculated Property
Δfgas -528.00 ± 2.00 kJ/mol NIST
Δfliquid -579.10 ± 1.10 kJ/mol NIST
Δfus 19.26 kJ/mol Joback Calculated Property
Δvap [50.60; 52.00] kJ/mol Show Hide
Δvap 50.60 ± 0.40 kJ/mol NIST
Δvap 52.00 ± 1.00 kJ/mol NIST
Δvap 51.10 kJ/mol NIST
Δvap 51.50 ± 1.30 kJ/mol NIST
Δvap 51.72 ± 0.10 kJ/mol NIST
IE 9.72 eV Relay (1.0) Calculated Property
log10WS -2.35 Estimated Solubility
logPoct/wat 2.130 Crippen Calculated Property
McVol 131.020 ml/mol McGowan Calculated Property
Pc 2657.03 kPa Joback Calculated Property
Inp [159.00; 1014.00]   Show Hide
Inp 982.90 NIST
Inp 979.00 NIST
Inp 989.00 NIST
Inp 1000.00 NIST
Inp 982.00 NIST
Inp 981.00 NIST
Inp 976.00 NIST
Inp 976.00 NIST
Inp 980.00 NIST
Inp 980.00 NIST
Inp 986.00 NIST
Inp 1000.00 NIST
Inp 983.00 NIST
Inp 990.00 NIST
Inp 986.00 NIST
Inp 994.00 NIST
Inp 991.00 NIST
Inp 986.00 NIST
Inp 992.00 NIST
Inp 986.00 NIST
Inp 986.00 NIST
Inp 985.00 NIST
Inp 988.00 NIST
Inp 982.00 NIST
Inp 982.00 NIST
Inp 1000.00 NIST
Inp 998.00 NIST
Inp 999.00 NIST
Inp 991.00 NIST
Inp 991.00 NIST
Inp 976.00 NIST
Inp 999.00 NIST
Inp 1000.00 NIST
Inp 997.00 NIST
Inp 996.00 NIST
Inp 976.00 NIST
Inp 996.00 NIST
Inp 1010.00 NIST
Inp 1000.00 NIST
Inp 1000.00 NIST
Inp 1002.00 NIST
Inp 996.00 NIST
Inp 996.00 NIST
Inp 1000.00 NIST
Inp 1000.00 NIST
Inp 995.00 NIST
Inp 997.00 NIST
Inp 1000.00 NIST
Inp 980.00 NIST
Inp 1001.00 NIST
Inp 999.00 NIST
Inp 981.00 NIST
Inp 996.00 NIST
Inp 1003.00 NIST
Inp 979.00 NIST
Inp 997.00 NIST
Inp 981.00 NIST
Inp 981.00 NIST
Inp 1014.00 NIST
Inp 1000.00 NIST
Inp 985.00 NIST
Inp 1002.00 NIST
Inp 1003.00 NIST
Inp 1005.00 NIST
Inp 996.00 NIST
Inp 1002.00 NIST
Inp 1003.00 NIST
Inp 1003.00 NIST
Inp 979.00 NIST
Inp 1002.00 NIST
Inp 1003.00 NIST
Inp 1003.00 NIST
Inp 980.00 NIST
Inp 980.00 NIST
Inp 1011.00 NIST
Inp 1000.00 NIST
Inp 993.00 NIST
Inp 979.00 NIST
Inp 998.40 NIST
Inp 998.00 NIST
Inp 1001.00 NIST
Inp 996.00 NIST
Inp 994.00 NIST
Inp 994.00 NIST
Inp 998.00 NIST
Inp 996.00 NIST
Inp 1000.00 NIST
Inp 1000.00 NIST
Inp 1001.00 NIST
Inp 1003.00 NIST
Inp 1006.00 NIST
Inp 1001.00 NIST
Inp 1002.00 NIST
Inp 992.00 NIST
Inp 996.00 NIST
Inp 995.00 NIST
Inp 1001.00 NIST
Inp 998.00 NIST
Inp 999.00 NIST
Inp 989.00 NIST
Inp 998.00 NIST
Inp 997.00 NIST
Inp 1003.00 NIST
Inp 996.00 NIST
Inp 1002.00 NIST
Inp 999.00 NIST
Inp 1002.00 NIST
Inp 1002.00 NIST
Inp 1005.00 NIST
Inp 998.00 NIST
Inp 982.00 NIST
Inp 990.00 NIST
Inp 996.00 NIST
Inp 997.00 NIST
Inp 1011.00 NIST
Inp 998.00 NIST
Inp 1001.00 NIST
Inp 1000.00 NIST
Inp 998.00 NIST
Inp 998.00 NIST
Inp 998.00 NIST
Inp 999.00 NIST
Inp 1004.00 NIST
Inp 981.00 NIST
Inp 1010.00 NIST
Inp 1005.00 NIST
Inp 1001.00 NIST
Inp 1010.00 NIST
Inp 996.00 NIST
Inp 1003.00 NIST
Inp 1002.00 NIST
Inp 1001.00 NIST
Inp 988.00 NIST
Inp 985.00 NIST
Inp 987.00 NIST
Inp 994.00 NIST
Inp 998.00 NIST
Inp 1000.00 NIST
Inp 1002.00 NIST
Inp 997.00 NIST
Inp 1000.00 NIST
Inp 990.00 NIST
Inp 983.00 NIST
Inp 1004.00 NIST
Inp 996.00 NIST
Inp 1004.00 NIST
Inp 982.00 NIST
Inp 993.00 NIST
Inp 998.00 NIST
Inp 1002.00 NIST
Inp 1003.00 NIST
Inp 1003.00 NIST
Inp 996.00 NIST
Inp 981.00 NIST
Inp 980.00 NIST
Inp 984.00 NIST
Inp 979.00 NIST
Inp 996.00 NIST
Inp 983.00 NIST
Inp 986.00 NIST
Inp 988.00 NIST
Inp 981.00 NIST
Inp 991.00 NIST
Inp 982.00 NIST
Inp 975.00 NIST
Inp 985.00 NIST
Inp 1000.00 NIST
Inp 1001.00 NIST
Inp 985.00 NIST
Inp 975.00 NIST
Inp 998.00 NIST
Inp 999.00 NIST
Inp 975.00 NIST
Inp 1007.00 NIST
Inp 995.00 NIST
Inp 999.00 NIST
Inp 1007.00 NIST
Inp 999.00 NIST
Inp 998.00 NIST
Inp 1010.00 NIST
Inp 999.00 NIST
Inp 977.00 NIST
Inp 959.00 NIST
Inp 976.00 NIST
Inp 1000.00 NIST
Inp 1000.00 NIST
Inp 983.00 NIST
Inp 984.00 NIST
Inp 976.00 NIST
Inp 999.00 NIST
Inp 996.00 NIST
Inp 994.00 NIST
Inp 975.00 NIST
Inp 975.00 NIST
Inp 996.00 NIST
Inp 984.00 NIST
Inp 999.00 NIST
Inp 994.00 NIST
Inp 1002.00 NIST
Inp 1002.00 NIST
Inp 981.00 NIST
Inp 981.00 NIST
Inp 996.00 NIST
Inp 999.00 NIST
Inp 983.00 NIST
Inp 1000.00 NIST
Inp 1001.00 NIST
Inp 1001.00 NIST
Inp 997.00 NIST
Inp 997.00 NIST
Inp 983.00 NIST
Inp 1001.00 NIST
Inp 997.00 NIST
Inp 1001.00 NIST
Inp 1001.00 NIST
Inp 999.00 NIST
Inp 997.00 NIST
Inp 995.00 NIST
Inp 997.00 NIST
Inp 1003.00 NIST
Inp 999.00 NIST
Inp 999.00 NIST
Inp 974.00 NIST
Inp 980.00 NIST
Inp 1003.00 NIST
Inp 983.00 NIST
Inp 980.00 NIST
Inp 984.00 NIST
Inp 1000.00 NIST
Inp 1000.00 NIST
Inp 1002.00 NIST
Inp 1000.00 NIST
Inp 980.00 NIST
Inp 981.00 NIST
Inp 981.00 NIST
Inp 983.00 NIST
Inp 983.00 NIST
Inp 981.00 NIST
Inp Outlier 159.00 NIST
Inp 1000.00 NIST
Inp 991.00 NIST
Inp 985.00 NIST
I [1183.00; 1271.00]   Show Hide
I 1231.00 NIST
I Outlier 1267.00 NIST
I 1220.00 NIST
I 1229.00 NIST
I 1229.00 NIST
I 1226.00 NIST
I 1223.00 NIST
I 1223.00 NIST
I 1236.00 NIST
I 1258.00 NIST
I 1241.00 NIST
I 1246.00 NIST
I 1241.00 NIST
I 1241.00 NIST
I 1230.00 NIST
I 1213.00 NIST
I 1216.00 NIST
I 1232.00 NIST
I 1220.00 NIST
I 1222.00 NIST
I 1241.00 NIST
I 1244.00 NIST
I 1232.00 NIST
I 1244.00 NIST
I 1240.00 NIST
I 1240.00 NIST
I 1240.00 NIST
I 1246.00 NIST
I 1236.00 NIST
I 1248.00 NIST
I 1239.00 NIST
I 1237.00 NIST
I 1236.00 NIST
I 1230.00 NIST
I 1227.00 NIST
I 1247.00 NIST
I 1253.00 NIST
I 1221.00 NIST
I 1224.00 NIST
I 1242.00 NIST
I 1258.00 NIST
I Outlier 1267.00 NIST
I 1231.00 NIST
I 1245.00 NIST
I 1221.00 NIST
I 1232.00 NIST
I 1224.00 NIST
I 1244.00 NIST
I 1224.00 NIST
I 1232.00 NIST
I 1233.00 NIST
I 1226.00 NIST
I 1241.00 NIST
I 1223.00 NIST
I 1229.00 NIST
I 1212.00 NIST
I 1229.00 NIST
I 1233.00 NIST
I 1222.00 NIST
I 1241.00 NIST
I 1225.00 NIST
I Outlier 1271.00 NIST
I 1241.20 NIST
I 1224.00 NIST
I 1225.00 NIST
I 1240.00 NIST
I 1238.00 NIST
I 1238.00 NIST
I 1228.00 NIST
I 1230.00 NIST
I 1238.00 NIST
I 1237.00 NIST
I 1220.00 NIST
I 1230.00 NIST
I 1220.00 NIST
I 1223.00 NIST
I Outlier 1261.00 NIST
I 1224.00 NIST
I 1228.00 NIST
I 1238.00 NIST
I 1242.00 NIST
I 1251.00 NIST
I 1234.00 NIST
I 1230.00 NIST
I 1230.00 NIST
I 1220.00 NIST
I 1220.00 NIST
I 1248.00 NIST
I 1235.00 NIST
I 1235.00 NIST
I 1220.00 NIST
I 1240.00 NIST
I 1258.00 NIST
I 1223.00 NIST
I 1251.00 NIST
I 1230.00 NIST
I 1230.00 NIST
I 1237.00 NIST
I 1251.00 NIST
I 1240.00 NIST
I 1240.00 NIST
I 1230.00 NIST
I 1212.00 NIST
I 1249.00 NIST
I Outlier 1205.00 NIST
I 1226.00 NIST
I 1244.00 NIST
I 1235.00 NIST
I 1241.00 NIST
I 1232.00 NIST
I 1238.00 NIST
I 1234.00 NIST
I 1226.00 NIST
I 1223.00 NIST
I Outlier 1205.00 NIST
I 1232.00 NIST
I 1231.00 NIST
I 1232.00 NIST
I Outlier 1208.00 NIST
I 1251.00 NIST
I 1236.00 NIST
I 1221.00 NIST
I 1243.00 NIST
I 1244.00 NIST
I 1235.00 NIST
I 1223.00 NIST
I 1235.00 NIST
I 1231.00 NIST
I 1235.00 NIST
I 1217.00 NIST
I 1254.00 NIST
I 1234.00 NIST
I 1222.00 NIST
I 1251.00 NIST
I Outlier 1270.00 NIST
I 1233.00 NIST
I 1248.00 NIST
I 1233.00 NIST
I 1229.00 NIST
I 1229.00 NIST
I 1258.00 NIST
I 1225.00 NIST
I Outlier 1259.00 NIST
I 1233.00 NIST
I 1224.00 NIST
I 1224.00 NIST
I 1244.00 NIST
I 1232.00 NIST
I 1244.00 NIST
I 1221.00 NIST
I 1220.00 NIST
I 1252.00 NIST
I Outlier 1259.00 NIST
I 1222.00 NIST
I 1227.00 NIST
I 1236.00 NIST
I 1223.00 NIST
I 1253.00 NIST
I 1238.00 NIST
I 1239.00 NIST
I 1238.00 NIST
I 1238.00 NIST
I 1238.00 NIST
I Outlier 1183.00 NIST
I 1248.00 NIST
I 1209.00 NIST
I Outlier 1199.00 NIST
I 1231.00 NIST
I 1218.00 NIST
I 1231.30 NIST
I 1223.00 NIST
I 1236.00 NIST
I 1228.00 NIST
I 1228.00 NIST
I 1228.00 NIST
I 1223.00 NIST
I 1227.00 NIST
I 1223.00 NIST
I 1227.00 NIST
I 1223.00 NIST
I 1227.00 NIST
I 1223.00 NIST
I 1227.00 NIST
I 1227.00 NIST
I 1245.00 NIST
I 1241.00 NIST
I 1223.00 NIST
I 1244.00 NIST
I 1236.00 NIST
I 1238.00 NIST
I 1238.00 NIST
I 1240.00 NIST
I 1233.00 NIST
I 1252.00 NIST
I 1237.00 NIST
I 1241.00 NIST
I 1241.00 NIST
I 1242.00 NIST
I 1258.00 NIST
I 1258.00 NIST
I 1241.00 NIST
I 1240.00 NIST
I 1242.00 NIST
I 1221.00 NIST
I 1221.00 NIST
I 1238.00 NIST
I 1223.00 NIST
I 1244.00 NIST
I Outlier 1205.00 NIST
I 1244.00 NIST
I 1229.00 NIST
I 1238.00 NIST
I 1242.00 NIST
I 1232.00 NIST
I 1232.00 NIST
I 1224.00 NIST
I 1226.00 NIST
I 1244.00 NIST
I 1243.00 NIST
I 1246.00 NIST
I 1224.00 NIST
I 1233.00 NIST
I 1229.00 NIST
I 1241.00 NIST
I 1241.00 NIST
I 1243.00 NIST
I 1230.00 NIST
I 1226.00 NIST
I 1235.00 NIST
I 1236.00 NIST
I 1216.00 NIST
I 1250.00 NIST
I 1226.00 NIST
I 1243.00 NIST
I Outlier 1259.00 NIST
I 1250.00 NIST
I 1223.00 NIST
I 1243.00 NIST
I 1222.00 NIST
I 1223.00 NIST
I 1248.00 NIST
I 1224.00 NIST
I 1229.00 NIST
I 1229.00 NIST
I Outlier 1199.00 NIST
I 1255.00 NIST
I 1232.00 NIST
I 1217.00 NIST
I 1223.00 NIST
I 1248.00 NIST
I 1223.00 NIST
I 1245.00 NIST
I 1223.00 NIST
I 1229.00 NIST
I 1245.00 NIST
I 1245.00 NIST
I 1238.00 NIST
I 1225.00 NIST
I 1225.00 NIST
I 1223.00 NIST
I 1231.00 NIST
I 1244.00 NIST
I 1235.00 NIST
I 1246.00 NIST
I 1232.00 NIST
I 1223.00 NIST
I 1241.00 NIST
I 1238.00 NIST
I 1229.00 NIST
I 1224.00 NIST
I 1243.00 NIST
I 1216.00 NIST
I 1250.00 NIST
I 1248.00 NIST
I 1255.00 NIST
I 1223.00 NIST
I 1245.00 NIST
I 1231.00 NIST
I 1230.00 NIST
I 1235.00 NIST
I 1251.00 NIST
I 1240.00 NIST
I Outlier 1205.00 NIST
I 1232.00 NIST
I 1246.00 NIST
I 1236.00 NIST
I 1221.00 NIST
I 1244.00 NIST
I 1233.00 NIST
I 1241.20 NIST
I 1220.00 NIST
Tboil [435.00; 441.20] K Show Hide
Tboil 441.20 K NIST
Tboil 440.06 ± 0.30 K NIST
Tboil 439.80 ± 1.00 K NIST
Tboil 439.80 ± 1.50 K NIST
Tboil 435.00 ± 5.00 K NIST
Tc [615.20; 615.22] K Show Hide
Tc 615.22 K Development of a Predictive Equation of State for CO2 + Ethyl Ester Mixtures Based on Critical Points Measurements
Tc 615.20 ± 0.60 K NIST
Tfus 205.51 ± 0.30 K NIST
Vc 0.505 m3/kmol Relay (1.0) Calculated Property

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,gas [279.70; 346.77] J/mol×K [458.73; 633.80] Show Hide
Cp,gas 279.70 J/mol×K 458.73 Joback Calculated Property
Cp,gas 291.94 J/mol×K 487.91 Joback Calculated Property
Cp,gas 303.75 J/mol×K 517.09 Joback Calculated Property
Cp,gas 315.14 J/mol×K 546.26 Joback Calculated Property
Cp,gas 326.10 J/mol×K 575.44 Joback Calculated Property
Cp,gas 336.64 J/mol×K 604.62 Joback Calculated Property
Cp,gas 346.77 J/mol×K 633.80 Joback Calculated Property
η [0.0004290; 0.0011020] Pa×s [288.15; 343.15] Show Hide
η 0.0011020 Pa×s 288.15 Densities and Viscosities of Binary Mixtures of Isoamyl Acetate, Ethyl Caproate, Ethyl Benzoate, Isoamyl Butyrate, Ethyl Phenylacetate, and Ethyl Caprylate with Ethanol at T = (288.15, 298.15, 308.15, and 318.15) K
η 0.0008160 Pa×s 293.15 Density and Viscosity of Binary Mixtures of Ethyl-2-methylbutyrate and Ethyl Hexanoate with Methanol, Ethanol, and 1-Propanol at (293.15, 303.15, and 313.15) K
η 0.0008160 Pa×s 293.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0007570 Pa×s 298.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0009400 Pa×s 298.15 Densities and Viscosities of Binary Mixtures of Isoamyl Acetate, Ethyl Caproate, Ethyl Benzoate, Isoamyl Butyrate, Ethyl Phenylacetate, and Ethyl Caprylate with Ethanol at T = (288.15, 298.15, 308.15, and 318.15) K
η 0.0007040 Pa×s 303.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0007040 Pa×s 303.15 Density and Viscosity of Binary Mixtures of Ethyl-2-methylbutyrate and Ethyl Hexanoate with Methanol, Ethanol, and 1-Propanol at (293.15, 303.15, and 313.15) K
η 0.0006560 Pa×s 308.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0008140 Pa×s 308.15 Densities and Viscosities of Binary Mixtures of Isoamyl Acetate, Ethyl Caproate, Ethyl Benzoate, Isoamyl Butyrate, Ethyl Phenylacetate, and Ethyl Caprylate with Ethanol at T = (288.15, 298.15, 308.15, and 318.15) K
η 0.0006140 Pa×s 313.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0006140 Pa×s 313.15 Density and Viscosity of Binary Mixtures of Ethyl-2-methylbutyrate and Ethyl Hexanoate with Methanol, Ethanol, and 1-Propanol at (293.15, 303.15, and 313.15) K
η 0.0005760 Pa×s 318.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0007110 Pa×s 318.15 Densities and Viscosities of Binary Mixtures of Isoamyl Acetate, Ethyl Caproate, Ethyl Benzoate, Isoamyl Butyrate, Ethyl Phenylacetate, and Ethyl Caprylate with Ethanol at T = (288.15, 298.15, 308.15, and 318.15) K
η 0.0005410 Pa×s 323.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0005090 Pa×s 328.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0004820 Pa×s 333.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0004560 Pa×s 338.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η 0.0004290 Pa×s 343.15 Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
ΔvapH [47.40; 51.80] kJ/mol [294.00; 422.50] Show Hide
ΔvapH 50.80 ± 0.40 kJ/mol 294.00 NIST
ΔvapH 48.60 kJ/mol 338.00 NIST
ΔvapH 47.40 ± 0.30 kJ/mol 359.50 NIST
ΔvapH 51.80 kJ/mol 422.50 NIST
Pvap [3.44e-03; 174.60] kPa [253.41; 462.43] Show Hide
Pvap 3.44e-03 kPa 253.41 Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap 0.01 kPa 263.26 Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap 0.07 kPa 283.06 Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap 0.14 kPa 293.05 Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap 0.29 kPa 303.03 Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap 0.56 kPa 313.15 Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap 1.02 kPa 323.18 Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap 1.78 kPa 333.11 Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap 2.98 kPa 343.09 Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap 4.55 kPa 351.97 Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap 7.18 kPa 362.10 Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap 10.93 kPa 372.13 Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap 11.35 kPa 373.15 Isothermal Vapor Liquid Equilibria of n-Tetradecane + Ethyl Hexanoate, Ethyl Decanoate, and Ethyl Tetradecanoate
Pvap 16.07 kPa 382.15 Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap 16.69 kPa 383.15 Isothermal Vapor Liquid Equilibria of n-Tetradecane + Ethyl Hexanoate, Ethyl Decanoate, and Ethyl Tetradecanoate
Pvap 23.19 kPa 392.23 Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap 23.94 kPa 393.15 Isothermal Vapor Liquid Equilibria of n-Tetradecane + Ethyl Hexanoate, Ethyl Decanoate, and Ethyl Tetradecanoate
Pvap 32.56 kPa 402.19 Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap 33.59 kPa 403.15 Isothermal Vapor Liquid Equilibria of n-Tetradecane + Ethyl Hexanoate, Ethyl Decanoate, and Ethyl Tetradecanoate
Pvap 44.90 kPa 412.21 Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap 46.18 kPa 413.15 Isothermal Vapor Liquid Equilibria of n-Tetradecane + Ethyl Hexanoate, Ethyl Decanoate, and Ethyl Tetradecanoate
Pvap 60.62 kPa 422.19 Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap 62.32 kPa 423.15 Isothermal Vapor Liquid Equilibria of n-Tetradecane + Ethyl Hexanoate, Ethyl Decanoate, and Ethyl Tetradecanoate
Pvap 80.76 kPa 432.28 Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap 82.69 kPa 433.15 Isothermal Vapor Liquid Equilibria of n-Tetradecane + Ethyl Hexanoate, Ethyl Decanoate, and Ethyl Tetradecanoate
Pvap 105.57 kPa 442.29 Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap 108.02 kPa 443.15 Isothermal Vapor Liquid Equilibria of n-Tetradecane + Ethyl Hexanoate, Ethyl Decanoate, and Ethyl Tetradecanoate
Pvap 136.73 kPa 452.34 Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap 139.11 kPa 453.15 Isothermal Vapor Liquid Equilibria of n-Tetradecane + Ethyl Hexanoate, Ethyl Decanoate, and Ethyl Tetradecanoate
Pvap 174.60 kPa 462.43 Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
n0 [1.37754; 1.41438]   [278.15; 358.15] Show Hide
n0 1.41438 278.15 Thermophysical properties of fatty acid methyl and ethyl esters
n0 1.41210 283.15 Thermophysical properties of fatty acid methyl and ethyl esters
n0 1.40982 288.15 Thermophysical properties of fatty acid methyl and ethyl esters
n0 1.40753 293.15 Thermophysical properties of fatty acid methyl and ethyl esters
n0 1.40525 298.15 Thermophysical properties of fatty acid methyl and ethyl esters
n0 1.40295 303.15 Thermophysical properties of fatty acid methyl and ethyl esters
n0 1.40063 308.15 Thermophysical properties of fatty acid methyl and ethyl esters
n0 1.39829 313.15 Thermophysical properties of fatty acid methyl and ethyl esters
n0 1.39594 318.15 Thermophysical properties of fatty acid methyl and ethyl esters
n0 1.39360 323.15 Thermophysical properties of fatty acid methyl and ethyl esters
n0 1.39128 328.15 Thermophysical properties of fatty acid methyl and ethyl esters
n0 1.38897 333.15 Thermophysical properties of fatty acid methyl and ethyl esters
n0 1.38667 338.15 Thermophysical properties of fatty acid methyl and ethyl esters
n0 1.38438 343.15 Thermophysical properties of fatty acid methyl and ethyl esters
n0 1.38210 348.15 Thermophysical properties of fatty acid methyl and ethyl esters
n0 1.37983 353.15 Thermophysical properties of fatty acid methyl and ethyl esters
n0 1.37754 358.15 Thermophysical properties of fatty acid methyl and ethyl esters
ρl [865.59; 866.29] kg/m3 [298.15; 298.15] Show Hide
ρl 866.29 kg/m3 298.15 Refractive Indices and Surface Tensions of Binary Mixtures of Isoamyl Acetate, Ethyl Caproate, Ethyl Benzoate, Isoamyl Butyrate, Ethyl Phenylacetate, and Ethyl Caprylate with Ethanol at (288.15, 298.15, 308.15, and 318.15) K
ρl 865.59 kg/m3 298.15 Ebulliometric Determination and Prediction of Vapor Liquid Equilibria for Binary Mixtures of Ethanol and Ethyl Hexanoate
csound,fluid [592.40; 1220.10] m/s [294.37; 473.82] Show Hide
csound,fluid 1220.10 m/s 294.37 Speed of sound measurement and prediction of ethyl hexanoate and ethyl octanoate at temperatures from (293.15 to 473.15) K and pressures from (0.1 to 10) MPa
csound,fluid 1191.00 m/s 301.55 Speed of sound measurement and prediction of ethyl hexanoate and ethyl octanoate at temperatures from (293.15 to 473.15) K and pressures from (0.1 to 10) MPa
csound,fluid 1152.70 m/s 313.34 Speed of sound measurement and prediction of ethyl hexanoate and ethyl octanoate at temperatures from (293.15 to 473.15) K and pressures from (0.1 to 10) MPa
csound,fluid 1115.10 m/s 324.26 Speed of sound measurement and prediction of ethyl hexanoate and ethyl octanoate at temperatures from (293.15 to 473.15) K and pressures from (0.1 to 10) MPa
csound,fluid 1077.60 m/s 333.16 Speed of sound measurement and prediction of ethyl hexanoate and ethyl octanoate at temperatures from (293.15 to 473.15) K and pressures from (0.1 to 10) MPa
csound,fluid 1046.10 m/s 343.20 Speed of sound measurement and prediction of ethyl hexanoate and ethyl octanoate at temperatures from (293.15 to 473.15) K and pressures from (0.1 to 10) MPa
csound,fluid 1010.00 m/s 353.08 Speed of sound measurement and prediction of ethyl hexanoate and ethyl octanoate at temperatures from (293.15 to 473.15) K and pressures from (0.1 to 10) MPa
csound,fluid 975.00 m/s 363.12 Speed of sound measurement and prediction of ethyl hexanoate and ethyl octanoate at temperatures from (293.15 to 473.15) K and pressures from (0.1 to 10) MPa
csound,fluid 942.00 m/s 373.14 Speed of sound measurement and prediction of ethyl hexanoate and ethyl octanoate at temperatures from (293.15 to 473.15) K and pressures from (0.1 to 10) MPa
csound,fluid 905.40 m/s 383.76 Speed of sound measurement and prediction of ethyl hexanoate and ethyl octanoate at temperatures from (293.15 to 473.15) K and pressures from (0.1 to 10) MPa
csound,fluid 870.10 m/s 393.30 Speed of sound measurement and prediction of ethyl hexanoate and ethyl octanoate at temperatures from (293.15 to 473.15) K and pressures from (0.1 to 10) MPa
csound,fluid 834.90 m/s 402.64 Speed of sound measurement and prediction of ethyl hexanoate and ethyl octanoate at temperatures from (293.15 to 473.15) K and pressures from (0.1 to 10) MPa
csound,fluid 800.80 m/s 413.59 Speed of sound measurement and prediction of ethyl hexanoate and ethyl octanoate at temperatures from (293.15 to 473.15) K and pressures from (0.1 to 10) MPa
csound,fluid 764.00 m/s 423.96 Speed of sound measurement and prediction of ethyl hexanoate and ethyl octanoate at temperatures from (293.15 to 473.15) K and pressures from (0.1 to 10) MPa
csound,fluid 730.30 m/s 433.99 Speed of sound measurement and prediction of ethyl hexanoate and ethyl octanoate at temperatures from (293.15 to 473.15) K and pressures from (0.1 to 10) MPa
csound,fluid 697.60 m/s 443.55 Speed of sound measurement and prediction of ethyl hexanoate and ethyl octanoate at temperatures from (293.15 to 473.15) K and pressures from (0.1 to 10) MPa
csound,fluid 661.00 m/s 452.90 Speed of sound measurement and prediction of ethyl hexanoate and ethyl octanoate at temperatures from (293.15 to 473.15) K and pressures from (0.1 to 10) MPa
csound,fluid 628.80 m/s 463.10 Speed of sound measurement and prediction of ethyl hexanoate and ethyl octanoate at temperatures from (293.15 to 473.15) K and pressures from (0.1 to 10) MPa
csound,fluid 592.40 m/s 473.82 Speed of sound measurement and prediction of ethyl hexanoate and ethyl octanoate at temperatures from (293.15 to 473.15) K and pressures from (0.1 to 10) MPa
γ [0.02; 0.03] N/m [288.15; 358.15] Show Hide
γ 0.03 N/m 288.15 Densities, Viscosities, Refractive Indices, and Surface Tensions for 12 Flavor Esters from T ) 288.15 K to T ) 358.15 K
γ 0.03 N/m 298.15 Densities, Viscosities, Refractive Indices, and Surface Tensions for 12 Flavor Esters from T ) 288.15 K to T ) 358.15 K
γ 0.02 N/m 308.15 Densities, Viscosities, Refractive Indices, and Surface Tensions for 12 Flavor Esters from T ) 288.15 K to T ) 358.15 K
γ 0.02 N/m 318.15 Densities, Viscosities, Refractive Indices, and Surface Tensions for 12 Flavor Esters from T ) 288.15 K to T ) 358.15 K
γ 0.02 N/m 328.15 Densities, Viscosities, Refractive Indices, and Surface Tensions for 12 Flavor Esters from T ) 288.15 K to T ) 358.15 K
γ 0.02 N/m 338.15 Densities, Viscosities, Refractive Indices, and Surface Tensions for 12 Flavor Esters from T ) 288.15 K to T ) 358.15 K
γ 0.02 N/m 348.15 Densities, Viscosities, Refractive Indices, and Surface Tensions for 12 Flavor Esters from T ) 288.15 K to T ) 358.15 K
γ 0.02 N/m 358.15 Densities, Viscosities, Refractive Indices, and Surface Tensions for 12 Flavor Esters from T ) 288.15 K to T ) 358.15 K
λ [0.12; 0.15] W/m×K [254.29; 383.37] Show Hide
λ 0.15 W/m×K 254.29 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ 0.14 W/m×K 264.08 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ 0.14 W/m×K 274.02 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ 0.14 W/m×K 283.95 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ 0.14 W/m×K 293.74 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ 0.14 W/m×K 303.70 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ 0.13 W/m×K 313.76 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ 0.13 W/m×K 323.67 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ 0.13 W/m×K 333.63 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ 0.12 W/m×K 343.56 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ 0.12 W/m×K 353.55 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ 0.12 W/m×K 363.41 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ 0.12 W/m×K 373.40 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ 0.12 W/m×K 383.37 Measurement of the thermal conductivity of five aliphatic esters in the liquid phase

Correlations

Property Value Unit Temperature (K) Source
Pvap [1.33; 202.67] kPa [329.12; 468.56] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Pvp) = A + B/(T + C)
Coefficient A1.48813e+01
Coefficient B-3.87622e+03
Coefficient C-6.35120e+01
Temperature range, min.329.12
Temperature range, max.468.56
Pvap 1.33 kPa 329.12 Calculated Property
Pvap 2.98 kPa 344.61 Calculated Property
Pvap 6.12 kPa 360.11 Calculated Property
Pvap 11.72 kPa 375.60 Calculated Property
Pvap 21.08 kPa 391.09 Calculated Property
Pvap 35.98 kPa 406.59 Calculated Property
Pvap 58.62 kPa 422.08 Calculated Property
Pvap 91.73 kPa 437.57 Calculated Property
Pvap 138.51 kPa 453.07 Calculated Property
Pvap 202.67 kPa 468.56 Calculated Property

Similar Compounds

ethyl hexanoate-d11. Heptanoic acid, ethyl ester. Tetradecanoic acid, ethyl ester. Docosanoic acid, ethyl ester. Heptadecanoic acid, ethyl ester. Octadecanoic acid, ethyl ester. Ethyl tetracosanoate. Ethyl tridecanoate. Eicosanoic acid, ethyl ester. Undecanoic acid, ethyl ester. Octanoic acid, ethyl ester. ethyl octacosanoate. Nonadecanoic acid, ethyl ester. ethyl nonacosanoate. ethyl tricosanoate.

Find more compounds similar to Hexanoic acid, ethyl ester.

Mixtures

Sources

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Outlier This icon means that the value is more than 2 standard deviations away from the property mean.