- 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 acetate
- Hexyl alcohol, acetate
- Hexyl ester of acetic acid
- Hexyl ethanoate
- Hexylester kyseliny octove
- N-HEXYL ACETATE
- N-HEXYL ETHANOATE
- NSC 7323
- ethanoic acid, hexyl ester
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔfG° | -217.44 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -453.25 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 19.26 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [51.90; 52.10] | kJ/mol |
|
| ΔvapH° | 51.90 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 52.10 | kJ/mol | NIST |
| log10WS | -2.46 | Aq. Sol... | |
| logPoct/wat | 2.130 | Crippen Calculated Property | |
| McVol | 131.020 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 2 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | 2657.03 | kPa | Joback Calculated Property |
| Inp | [979.20; 1025.00] |
|
|
| 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 | |
| I | [1235.00; 1311.00] |
|
|
| I | 1277.00 | NIST | |
| I | 1255.00 | NIST | |
| I | 1286.00 | NIST | |
| I | 1295.00 | NIST | |
| I | 1277.00 | NIST | |
| I | Outlier 1299.00 | NIST | |
| I | Outlier 1301.00 | NIST | |
| I | 1262.00 | NIST | |
| I | 1268.00 | NIST | |
| I | 1276.00 | NIST | |
| I | 1276.00 | NIST | |
| I | 1276.00 | NIST | |
| I | 1274.00 | NIST | |
| I | 1276.00 | NIST | |
| I | 1296.00 | NIST | |
| I | 1278.00 | NIST | |
| I | 1280.00 | NIST | |
| I | Outlier 1305.00 | NIST | |
| I | 1270.00 | NIST | |
| I | 1270.00 | NIST | |
| I | 1269.00 | NIST | |
| I | 1272.00 | NIST | |
| I | 1266.00 | NIST | |
| I | 1279.00 | NIST | |
| I | 1280.00 | NIST | |
| I | 1275.00 | NIST | |
| I | 1269.00 | NIST | |
| I | 1275.00 | NIST | |
| I | 1279.00 | NIST | |
| I | 1265.00 | NIST | |
| I | 1275.00 | NIST | |
| I | 1268.00 | NIST | |
| I | 1254.00 | NIST | |
| I | 1293.00 | NIST | |
| I | Outlier 1311.00 | NIST | |
| I | 1271.00 | NIST | |
| I | 1282.00 | NIST | |
| I | 1277.00 | NIST | |
| I | 1265.00 | NIST | |
| I | 1270.00 | NIST | |
| I | 1261.00 | NIST | |
| I | 1267.00 | NIST | |
| I | 1251.00 | NIST | |
| I | 1264.00 | NIST | |
| I | 1265.00 | NIST | |
| I | 1264.00 | NIST | |
| I | 1267.00 | NIST | |
| I | 1272.00 | NIST | |
| I | 1275.00 | NIST | |
| I | 1295.00 | NIST | |
| I | 1295.00 | NIST | |
| I | 1295.00 | NIST | |
| I | 1265.00 | NIST | |
| I | 1267.00 | NIST | |
| I | Outlier 1248.00 | NIST | |
| I | 1257.00 | NIST | |
| I | 1264.00 | NIST | |
| I | 1269.00 | NIST | |
| I | 1272.00 | NIST | |
| I | Outlier 1308.00 | NIST | |
| I | 1285.00 | NIST | |
| I | 1279.00 | NIST | |
| I | 1251.00 | NIST | |
| I | 1258.00 | NIST | |
| I | 1258.00 | NIST | |
| I | 1286.00 | NIST | |
| I | 1275.00 | NIST | |
| I | 1263.00 | NIST | |
| I | 1251.00 | NIST | |
| I | 1275.00 | NIST | |
| I | 1268.00 | NIST | |
| I | Outlier 1307.00 | NIST | |
| I | 1276.00 | NIST | |
| I | 1282.00 | NIST | |
| I | 1280.00 | NIST | |
| I | 1269.00 | NIST | |
| I | 1272.00 | NIST | |
| I | 1277.00 | NIST | |
| I | 1270.00 | NIST | |
| I | 1270.00 | NIST | |
| I | 1257.00 | NIST | |
| I | 1275.00 | NIST | |
| I | 1282.00 | NIST | |
| I | 1274.00 | NIST | |
| I | 1254.00 | NIST | |
| I | 1254.00 | NIST | |
| I | 1270.00 | NIST | |
| I | 1274.00 | NIST | |
| I | 1263.00 | NIST | |
| I | 1276.00 | NIST | |
| I | 1291.00 | NIST | |
| I | Outlier 1307.00 | NIST | |
| I | 1274.00 | NIST | |
| I | 1259.00 | NIST | |
| I | 1278.00 | NIST | |
| I | 1271.00 | NIST | |
| I | 1274.00 | NIST | |
| I | 1269.00 | NIST | |
| I | 1271.00 | NIST | |
| I | 1272.00 | NIST | |
| I | Outlier 1235.00 | NIST | |
| I | 1289.00 | NIST | |
| I | 1290.00 | NIST | |
| I | 1268.00 | NIST | |
| I | 1262.00 | NIST | |
| I | 1267.00 | NIST | |
| I | 1273.00 | NIST | |
| I | 1271.00 | NIST | |
| I | 1267.00 | NIST | |
| I | 1280.00 | NIST | |
| I | 1265.00 | NIST | |
| I | 1279.00 | NIST | |
| I | 1277.00 | NIST | |
| I | 1270.00 | NIST | |
| I | Outlier 1307.00 | NIST | |
| I | 1270.00 | NIST | |
| I | 1290.00 | NIST | |
| I | 1264.00 | NIST | |
| I | 1265.00 | NIST | |
| I | 1264.00 | NIST | |
| I | 1265.00 | NIST | |
| I | 1272.00 | NIST | |
| I | 1272.00 | NIST | |
| I | 1264.00 | NIST | |
| I | 1265.00 | NIST | |
| I | 1264.00 | NIST | |
| I | 1265.00 | NIST | |
| I | 1275.00 | NIST | |
| I | 1272.00 | NIST | |
| I | 1281.00 | NIST | |
| I | 1271.00 | NIST | |
| I | 1276.00 | NIST | |
| I | 1266.00 | NIST | |
| I | 1276.00 | NIST | |
| I | 1281.00 | NIST | |
| I | 1283.00 | NIST | |
| I | 1274.00 | NIST | |
| I | 1279.00 | NIST | |
| I | 1292.00 | NIST | |
| I | 1259.00 | NIST | |
| I | 1259.00 | NIST | |
| I | 1278.00 | NIST | |
| I | 1265.00 | NIST | |
| I | 1287.00 | NIST | |
| I | 1269.00 | NIST | |
| I | 1271.00 | NIST | |
| I | 1283.00 | NIST | |
| I | 1287.00 | NIST | |
| I | 1283.00 | NIST | |
| I | 1279.00 | NIST | |
| I | Outlier 1308.00 | NIST | |
| I | 1258.00 | NIST | |
| I | 1268.00 | NIST | |
| I | 1276.00 | NIST | |
| I | 1267.00 | NIST | |
| I | 1281.00 | NIST | |
| I | 1278.00 | NIST | |
| I | 1283.00 | NIST | |
| I | Outlier 1303.00 | NIST | |
| I | 1267.00 | NIST | |
| I | 1273.00 | NIST | |
| I | 1272.00 | NIST | |
| I | 1275.00 | NIST | |
| I | 1282.00 | NIST | |
| I | 1283.00 | NIST | |
| I | 1275.00 | NIST | |
| I | 1260.00 | NIST | |
| I | 1283.00 | NIST | |
| I | 1265.00 | NIST | |
| I | 1269.00 | NIST | |
| I | 1278.00 | NIST | |
| I | 1294.00 | NIST | |
| I | 1283.00 | NIST | |
| I | 1264.00 | NIST | |
| I | 1268.00 | NIST | |
| I | 1283.00 | NIST | |
| I | 1266.00 | NIST | |
| I | 1269.00 | NIST | |
| I | 1283.00 | NIST | |
| I | 1282.00 | NIST | |
| I | 1281.00 | NIST | |
| I | 1270.00 | NIST | |
| I | 1270.00 | NIST | |
| I | 1264.00 | NIST | |
| I | 1262.00 | NIST | |
| I | 1274.00 | NIST | |
| I | Outlier 1305.00 | NIST | |
| I | 1266.00 | NIST | |
| I | 1279.00 | NIST | |
| I | 1275.00 | NIST | |
| I | 1265.00 | NIST | |
| I | 1287.00 | NIST | |
| I | 1268.00 | NIST | |
| I | 1283.00 | NIST | |
| I | 1269.00 | NIST | |
| I | 1270.00 | NIST | |
| Tboil | [429.15; 464.00] | K |
|
| Tboil | 444.63 | K | KDB |
| 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 | 633.80 | K | Joback Calculated Property |
| Tfus | [192.30; 212.25] | K |
|
| Tfus | 212.25 | K | KDB |
| Tfus | 192.85 | K | Aq. Sol... |
| Tfus | 212.10 ± 0.05 | K | NIST |
| Tfus | 192.30 ± 0.50 | K | NIST |
| Vc | 0.507 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [279.70; 346.77] | J/mol×K | [458.73; 633.80] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 280 290 300 310 320 330 340 350 500 550 600 | ||||
| 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 | [0.0005790; 0.0011180] | Pa×s | [293.15; 343.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 6.00e-4 7.00e-4 8.00e-4 9.00e-4 1.00e-3 1.10e-3 300 320 340 | ||||
| η | 0.0011180 | Pa×s | 293.15 | Density... |
| η | 0.0010360 | Pa×s | 298.15 | Density... |
| η | 0.0009620 | Pa×s | 303.15 | Density... |
| η | 0.0008950 | Pa×s | 308.15 | Density... |
| η | 0.0008360 | Pa×s | 313.15 | Density... |
| η | 0.0007820 | Pa×s | 318.15 | Density... |
| η | 0.0007330 | Pa×s | 323.15 | Density... |
| η | 0.0006890 | Pa×s | 328.15 | Density... |
| η | 0.0006490 | Pa×s | 333.15 | Density... |
| η | 0.0006120 | Pa×s | 338.15 | Density... |
| η | 0.0005790 | Pa×s | 343.15 | Density... |
| ΔfusH | [19.83; 19.83] | kJ/mol | [212.10; 212.10] |
|
| 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] |
|
| 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] |
|
|
T(K) Vapor pressure (kPa) 0 20 40 60 80 300 350 400 | ||||
| Pvap | 0.03 | kPa | 274.50 | Vapour ... |
| Pvap | 0.03 | kPa | 277.70 | Vapour ... |
| Pvap | 0.04 | kPa | 280.80 | Vapour ... |
| Pvap | 0.05 | kPa | 283.80 | Vapour ... |
| Pvap | 0.07 | kPa | 286.90 | Vapour ... |
| Pvap | 0.08 | kPa | 289.90 | Vapour ... |
| Pvap | 0.10 | kPa | 291.90 | Vapour ... |
| Pvap | 0.12 | kPa | 294.00 | Vapour ... |
| Pvap | 0.15 | kPa | 297.00 | Vapour ... |
| Pvap | 0.18 | kPa | 300.00 | Vapour ... |
| Pvap | 0.23 | kPa | 303.10 | Vapour ... |
| Pvap | 0.27 | kPa | 306.10 | Vapour ... |
| Pvap | 0.33 | kPa | 309.10 | Vapour ... |
| Pvap | 25.00 | kPa | 397.97 | Phase E... |
| Pvap | 30.00 | kPa | 403.36 | Phase E... |
| Pvap | 35.00 | kPa | 408.02 | Phase E... |
| Pvap | 40.00 | kPa | 412.14 | Phase E... |
| Pvap | 45.00 | kPa | 416.02 | Phase E... |
| Pvap | 50.00 | kPa | 419.47 | Phase E... |
| Pvap | 55.00 | kPa | 422.59 | Phase E... |
| Pvap | 60.00 | kPa | 425.57 | Phase E... |
| Pvap | 65.00 | kPa | 428.26 | Phase E... |
| Pvap | 70.00 | kPa | 430.93 | Phase E... |
| Pvap | 75.00 | kPa | 433.38 | Phase E... |
| Pvap | 80.00 | kPa | 435.68 | Phase E... |
| Pvap | 85.00 | kPa | 437.92 | Phase E... |
| Pvap | 90.00 | kPa | 439.98 | Phase E... |
| n0 | 1.40960 | 293.15 | Liquid-... | |
| ρl | [855.00; 868.52] | kg/m3 | [298.15; 313.15] |
|
|
T(K) Liquid Density (kg/m3) 854 856 858 860 862 864 866 868 300 305 310 | ||||
| ρl | 868.52 | kg/m3 | 298.15 | Experim... |
| ρl | 868.30 | kg/m3 | 298.15 | Densiti... |
| ρl | 868.52 | kg/m3 | 298.15 | Surface... |
| ρl | 863.90 | kg/m3 | 303.15 | Densiti... |
| ρl | 859.80 | kg/m3 | 308.15 | Densiti... |
| ρl | 855.00 | kg/m3 | 313.15 | Densiti... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [334.82; 468.91] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.54294e+01 | |||
| Coefficient B | -4.08917e+03 | |||
| Coefficient C | -6.47630e+01 | |||
| Temperature range, min. | 334.82 | |||
| Temperature range, max. | 468.91 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
| 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 | [8.33e-07; 2452.89] | kPa | [192.25; 618.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 8.03443e+01 | |||
| Coefficient B | -8.74286e+03 | |||
| Coefficient C | -9.31977e+00 | |||
| Coefficient D | 3.93049e-06 | |||
| Temperature range, min. | 192.25 | |||
| Temperature range, max. | 618.00 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 200 400 600 | ||||
| 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 |
Similar Compounds
Find more compounds similar to Acetic acid, hexyl ester.
Mixtures
- Heptane + Acetic acid, hexyl ester
- Benzene + Acetic acid, hexyl ester
- Acetic acid, hexyl ester + Water
- Acetic acid + Acetic acid, hexyl ester
- 1-Hexanol + Acetic acid, hexyl ester
- Acetic acid + Acetic acid, hexyl ester + Water
- Tetrahydrofuran + Acetic acid, hexyl ester
- 1,4-Dioxane + Acetic acid, hexyl ester
- Anisole + Acetic acid, hexyl ester
- Butane, 1-(ethenyloxy)- + Acetic acid, hexyl ester
- Formamide, N,N-dimethyl- + Acetic acid, hexyl ester
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Vapour pressures and enthalpies of vaporization of a series of the linear n-alkyl acetates
- Experimental and theoretical study of surface tension of binary mixtures of (n-alkyl acetates + heptane, benzene, and toluene)
- 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
- Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
- Phase Equlibria for Hexyl Acetate Reactive Distillation
- Densities, Viscosities, and Sound Speed of Binary Mixtures of Hexyl Acetate with Tetrahydrofuran, 1,4-Dioxane, Anisole, and Butyl Vinyl Ether
- Surface Tension and Surface Properties of Binary Mixtures of 1,4-Dioxane or N,N-Dimethyl Formamide with n-Alkyl Acetates
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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