- InChI
- InChI=1S/C7H14O2/c1-3-4-5-6-7(8)9-2/h3-6H2,1-2H3
- InChI Key
- NUKZAGXMHTUAFE-UHFFFAOYSA-N
- Formula
- C7H14O2
- SMILES
- CCCCCC(=O)OC
- Molecular Weight1
- 130.18
- CAS
- 106-70-7
- Other Names
-
- Caproic acid, methyl ester
- Methyl caproate
- Methyl capronate
- Methyl ester of hexanoic acid
- Methyl hexanoate
- Methyl hexoate
- Methyl hexylate
- Methyl n-hexanoate
- Methyl n-hexoate
- NSC 5023
- n-Caproic acid methyl ester
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase 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).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (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).
- 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.
- csound,fluid : Speed of sound in fluid (m/s).
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- λ : Liquid thermal conductivity (W/m×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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Contents
- Physical Properties
- Temperature Dependent Properties
- Pressure Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | [-4215.00; -4184.00] | kJ/mol |
|
| ΔcH°liquid | -4184.00 ± 0.40 | kJ/mol | NIST |
| ΔcH°liquid | -4215.00 ± 0.60 | kJ/mol | NIST |
| ΔfG° | -225.86 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -494.00 ± 2.00 | kJ/mol | NIST |
| ΔfH°liquid | -540.20 ± 1.00 | kJ/mol | NIST |
| ΔfusH° | 16.67 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [46.00; 48.70] | kJ/mol |
|
| ΔvapH° | 48.40 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 47.70 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 47.90 | kJ/mol | NIST |
| ΔvapH° | 48.20 | kJ/mol | NIST |
| ΔvapH° | 47.80 ± 0.50 | kJ/mol | NIST |
| ΔvapH° | 48.70 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 48.04 ± 0.12 | kJ/mol | NIST |
| ΔvapH° | 48.00 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | Outlier 46.00 ± 1.00 | kJ/mol | NIST |
| ΔvapH° | 46.20 | kJ/mol | NIST |
| log10WS | [-2.00; -1.87] |
|
|
| log10WS | -2.00 | Aq. Sol... | |
| log10WS | -1.87 | Estimat... | |
| logPoct/wat | 1.740 | Crippen Calculated Property | |
| McVol | 116.930 | ml/mol | McGowan Calculated Property |
| Pc | 2940.89 | kPa | Joback Calculated Property |
| Inp | [142.00; 938.00] |
|
|
| Inp | 907.00 | NIST | |
| Inp | 907.00 | NIST | |
| Inp | 908.30 | NIST | |
| Inp | 923.40 | NIST | |
| Inp | 922.60 | NIST | |
| Inp | 921.80 | NIST | |
| Inp | 908.00 | NIST | |
| Inp | 904.00 | NIST | |
| Inp | 905.00 | NIST | |
| Inp | 913.00 | NIST | |
| Inp | 902.00 | NIST | |
| Inp | 902.00 | NIST | |
| Inp | 913.00 | NIST | |
| Inp | 910.00 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | 911.00 | NIST | |
| Inp | 909.00 | NIST | |
| Inp | 909.00 | NIST | |
| Inp | 910.00 | NIST | |
| Inp | 905.00 | NIST | |
| Inp | 913.00 | NIST | |
| Inp | 905.00 | NIST | |
| Inp | 907.00 | NIST | |
| Inp | 931.00 | NIST | |
| Inp | 910.00 | NIST | |
| Inp | 915.00 | NIST | |
| Inp | 902.00 | NIST | |
| Inp | 925.00 | NIST | |
| Inp | 915.00 | NIST | |
| Inp | 936.00 | NIST | |
| Inp | 924.00 | NIST | |
| Inp | 938.00 | NIST | |
| Inp | 911.00 | NIST | |
| Inp | 925.00 | NIST | |
| Inp | 903.00 | NIST | |
| Inp | 923.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 933.00 | NIST | |
| Inp | 904.00 | NIST | |
| Inp | 934.00 | NIST | |
| Inp | 905.00 | NIST | |
| Inp | 904.00 | NIST | |
| Inp | 904.00 | NIST | |
| Inp | 904.00 | NIST | |
| Inp | 908.50 | NIST | |
| Inp | 907.40 | NIST | |
| Inp | 908.00 | NIST | |
| Inp | 908.00 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | 909.00 | NIST | |
| Inp | 927.00 | NIST | |
| Inp | 910.00 | NIST | |
| Inp | 907.00 | NIST | |
| Inp | 922.50 | NIST | |
| Inp | 931.40 | NIST | |
| Inp | 914.00 | NIST | |
| Inp | 932.00 | NIST | |
| Inp | 924.00 | NIST | |
| Inp | 931.00 | NIST | |
| Inp | 925.00 | NIST | |
| Inp | 918.00 | NIST | |
| Inp | 916.00 | NIST | |
| Inp | 922.00 | NIST | |
| Inp | 905.00 | NIST | |
| Inp | 905.00 | NIST | |
| Inp | 907.00 | NIST | |
| Inp | 925.00 | NIST | |
| Inp | 907.00 | NIST | |
| Inp | 916.00 | NIST | |
| Inp | 919.00 | NIST | |
| Inp | 927.00 | NIST | |
| Inp | 930.00 | NIST | |
| Inp | 929.00 | NIST | |
| Inp | 924.00 | NIST | |
| Inp | 924.00 | NIST | |
| Inp | 928.00 | NIST | |
| Inp | 925.00 | NIST | |
| Inp | 924.00 | NIST | |
| Inp | 923.20 | NIST | |
| Inp | 927.00 | NIST | |
| Inp | 915.00 | NIST | |
| Inp | 936.00 | NIST | |
| Inp | 936.00 | NIST | |
| Inp | 909.00 | NIST | |
| Inp | 927.00 | NIST | |
| Inp | 927.00 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | 905.00 | NIST | |
| Inp | 910.00 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | 907.00 | NIST | |
| Inp | 907.00 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | 910.00 | NIST | |
| Inp | 914.00 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | 907.00 | NIST | |
| Inp | 907.00 | NIST | |
| Inp | 905.00 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | 921.00 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | 923.00 | NIST | |
| Inp | 927.00 | NIST | |
| Inp | 911.00 | NIST | |
| Inp | 924.00 | NIST | |
| Inp | 929.00 | NIST | |
| Inp | 911.00 | NIST | |
| Inp | 927.00 | NIST | |
| Inp | 936.00 | NIST | |
| Inp | 925.00 | NIST | |
| Inp | 924.00 | NIST | |
| Inp | 922.00 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | 931.00 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | 902.00 | NIST | |
| Inp | 922.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | 911.00 | NIST | |
| Inp | 934.00 | NIST | |
| Inp | 934.00 | NIST | |
| Inp | 934.00 | NIST | |
| Inp | 934.00 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | 907.00 | NIST | |
| Inp | 902.00 | NIST | |
| Inp | 914.00 | NIST | |
| Inp | 904.00 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | 905.00 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | Outlier 142.00 | NIST | |
| Inp | Outlier 148.05 | NIST | |
| Inp | 919.00 | NIST | |
| Inp | 924.00 | NIST | |
| Inp | 927.00 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | 910.00 | NIST | |
| Inp | 905.00 | NIST | |
| I | [1142.00; 1208.00] |
|
|
| I | 1183.00 | NIST | |
| I | 1177.00 | NIST | |
| I | 1184.00 | NIST | |
| I | 1177.00 | NIST | |
| I | 1188.00 | NIST | |
| I | 1184.00 | NIST | |
| I | 1190.00 | NIST | |
| I | 1182.00 | NIST | |
| I | 1180.00 | NIST | |
| I | 1180.00 | NIST | |
| I | 1176.00 | NIST | |
| I | 1186.00 | NIST | |
| I | 1176.00 | NIST | |
| I | 1173.00 | NIST | |
| I | 1175.00 | NIST | |
| I | 1173.00 | NIST | |
| I | 1175.00 | NIST | |
| I | 1189.00 | NIST | |
| I | 1197.00 | NIST | |
| I | 1181.00 | NIST | |
| I | 1187.00 | NIST | |
| I | 1183.00 | NIST | |
| I | 1172.00 | NIST | |
| I | 1177.00 | NIST | |
| I | 1184.00 | NIST | |
| I | 1183.00 | NIST | |
| I | 1190.00 | NIST | |
| I | 1171.00 | NIST | |
| I | 1189.00 | NIST | |
| I | Outlier 1208.00 | NIST | |
| I | 1204.00 | NIST | |
| I | 1202.00 | NIST | |
| I | 1194.00 | NIST | |
| I | 1197.00 | NIST | |
| I | 1185.00 | NIST | |
| I | 1172.00 | NIST | |
| I | 1197.00 | NIST | |
| I | 1184.00 | NIST | |
| I | 1191.00 | NIST | |
| I | 1178.00 | NIST | |
| I | 1178.00 | NIST | |
| I | 1191.00 | NIST | |
| I | Outlier 1142.00 | NIST | |
| I | Outlier 1154.00 | NIST | |
| I | 1193.00 | NIST | |
| I | 1182.00 | NIST | |
| I | 1184.00 | NIST | |
| I | 1186.00 | NIST | |
| I | 1185.00 | NIST | |
| I | 1184.00 | NIST | |
| I | 1202.00 | NIST | |
| I | 1192.00 | NIST | |
| I | 1174.00 | NIST | |
| I | 1188.00 | NIST | |
| I | 1185.00 | NIST | |
| I | 1177.00 | NIST | |
| I | 1200.00 | NIST | |
| I | 1180.00 | NIST | |
| I | 1187.00 | NIST | |
| I | Outlier 1208.00 | NIST | |
| I | 1172.00 | NIST | |
| I | 1192.00 | NIST | |
| I | 1197.00 | NIST | |
| I | 1177.00 | NIST | |
| I | 1188.00 | NIST | |
| I | 1197.00 | NIST | |
| I | 1177.00 | NIST | |
| I | 1183.00 | NIST | |
| I | 1183.00 | NIST | |
| I | 1200.00 | NIST | |
| Tboil | 435.85 | K | Joback Calculated Property |
| Tc | 612.24 | K | Joback Calculated Property |
| Tfus | [202.20; 203.60] | K |
|
| Tfus | 203.60 ± 0.05 | K | NIST |
| Tfus | 202.20 ± 0.50 | K | NIST |
| Vc | 0.452 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [238.65; 299.73] | J/mol×K | [435.85; 612.24] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 240 250 260 270 280 290 300 450 500 550 600 | ||||
| Cp,gas | 238.65 | J/mol×K | 435.85 | Joback Calculated Property |
| Cp,gas | 249.76 | J/mol×K | 465.25 | Joback Calculated Property |
| Cp,gas | 260.50 | J/mol×K | 494.65 | Joback Calculated Property |
| Cp,gas | 270.86 | J/mol×K | 524.04 | Joback Calculated Property |
| Cp,gas | 280.85 | J/mol×K | 553.44 | Joback Calculated Property |
| Cp,gas | 290.48 | J/mol×K | 582.84 | Joback Calculated Property |
| Cp,gas | 299.73 | J/mol×K | 612.24 | Joback Calculated Property |
| Cp,liquid | [246.40; 269.60] | J/mol×K | [303.15; 373.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 245 250 255 260 265 270 320 340 360 | ||||
| Cp,liquid | 246.40 | J/mol×K | 303.15 | Heat ca... |
| Cp,liquid | 248.80 | J/mol×K | 313.15 | Heat ca... |
| Cp,liquid | 251.50 | J/mol×K | 323.15 | Heat ca... |
| Cp,liquid | 254.60 | J/mol×K | 333.15 | Heat ca... |
| Cp,liquid | 257.90 | J/mol×K | 343.15 | Heat ca... |
| Cp,liquid | 261.50 | J/mol×K | 353.15 | Heat ca... |
| Cp,liquid | 265.50 | J/mol×K | 363.15 | Heat ca... |
| Cp,liquid | 269.60 | J/mol×K | 373.15 | Heat ca... |
| η | [0.0002656; 0.0031909] | Pa×s | [240.81; 435.85] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 250 300 350 400 | ||||
| η | 0.0031909 | Pa×s | 240.81 | Joback Calculated Property |
| η | 0.0016480 | Pa×s | 273.32 | Joback Calculated Property |
| η | 0.0009795 | Pa×s | 305.82 | Joback Calculated Property |
| η | 0.0006434 | Pa×s | 338.33 | Joback Calculated Property |
| η | 0.0004549 | Pa×s | 370.84 | Joback Calculated Property |
| η | 0.0003401 | Pa×s | 403.34 | Joback Calculated Property |
| η | 0.0002656 | Pa×s | 435.85 | Joback Calculated Property |
| ΔvapH | [45.20; 46.40] | kJ/mol | [325.00; 350.00] |
|
| ΔvapH | 46.40 ± 0.10 | kJ/mol | 325.00 | NIST |
| ΔvapH | 45.30 | kJ/mol | 349.00 | NIST |
| ΔvapH | 45.20 | kJ/mol | 350.00 | NIST |
| Pvap | [0.03; 96.03] | kPa | [262.64; 422.29] |
|
|
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 300 350 400 | ||||
| Pvap | 0.03 | kPa | 262.64 | Experim... |
| Pvap | 0.08 | kPa | 272.74 | Experim... |
| Pvap | 0.14 | kPa | 280.70 | Transpi... |
| Pvap | 0.16 | kPa | 282.84 | Experim... |
| Pvap | 0.17 | kPa | 283.60 | Transpi... |
| Pvap | 0.18 | kPa | 284.60 | Transpi... |
| Pvap | 0.21 | kPa | 286.60 | Transpi... |
| Pvap | 0.22 | kPa | 287.60 | Transpi... |
| Pvap | 0.26 | kPa | 289.50 | Transpi... |
| Pvap | 0.28 | kPa | 290.50 | Transpi... |
| Pvap | 0.27 | kPa | 290.50 | Transpi... |
| Pvap | 0.31 | kPa | 292.50 | Transpi... |
| Pvap | 0.34 | kPa | 292.87 | Experim... |
| Pvap | 0.34 | kPa | 293.30 | Transpi... |
| Pvap | 0.35 | kPa | 293.40 | Transpi... |
| Pvap | 0.34 | kPa | 293.50 | Transpi... |
| Pvap | 0.39 | kPa | 295.40 | Transpi... |
| Pvap | 0.42 | kPa | 296.40 | Transpi... |
| Pvap | 0.46 | kPa | 298.30 | Transpi... |
| Pvap | 0.47 | kPa | 298.40 | Transpi... |
| Pvap | 0.54 | kPa | 300.30 | Transpi... |
| Pvap | 0.65 | kPa | 303.30 | Transpi... |
| Pvap | 0.73 | kPa | 304.30 | Transpi... |
| Pvap | 0.89 | kPa | 307.63 | Experim... |
| Pvap | 0.90 | kPa | 307.90 | Experim... |
| Pvap | 0.89 | kPa | 308.30 | Transpi... |
| Pvap | 0.92 | kPa | 309.30 | Transpi... |
| Pvap | 1.05 | kPa | 312.30 | Transpi... |
| Pvap | 1.15 | kPa | 312.30 | Transpi... |
| Pvap | 1.46 | kPa | 316.30 | Transpi... |
| Pvap | 1.60 | kPa | 317.65 | Experim... |
| Pvap | 1.76 | kPa | 320.40 | Transpi... |
| Pvap | 2.22 | kPa | 324.40 | Transpi... |
| Pvap | 2.68 | kPa | 328.40 | Transpi... |
| Pvap | 3.18 | kPa | 331.40 | Transpi... |
| Pvap | 3.53 | kPa | 332.72 | Experim... |
| Pvap | 7.13 | kPa | 347.57 | Experim... |
| Pvap | 13.06 | kPa | 362.19 | Experim... |
| Pvap | 23.11 | kPa | 377.31 | Experim... |
| Pvap | 38.94 | kPa | 392.48 | Experim... |
| Pvap | 62.31 | kPa | 407.40 | Experim... |
| Pvap | 96.03 | kPa | 422.29 | Experim... |
| n0 | [1.37490; 1.41212] | [278.15; 358.15] |
|
|
|
T(K) Refractive Index 1.38 1.39 1.4 1.41 300 350 | ||||
| n0 | 1.41212 | 278.15 | Thermop... | |
| n0 | 1.40984 | 283.15 | Thermop... | |
| n0 | 1.40757 | 288.15 | Thermop... | |
| n0 | 1.40529 | 293.15 | Thermop... | |
| n0 | 1.40300 | 298.15 | Thermop... | |
| n0 | 1.40480 | 298.15 | Vapor-L... | |
| n0 | 1.40480 | 298.15 | Vapor-L... | |
| n0 | 1.40070 | 303.15 | Thermop... | |
| n0 | 1.39841 | 308.15 | Thermop... | |
| n0 | 1.39610 | 313.15 | Thermop... | |
| n0 | 1.39373 | 318.15 | Thermop... | |
| n0 | 1.39136 | 323.15 | Thermop... | |
| n0 | 1.38902 | 328.15 | Thermop... | |
| n0 | 1.38667 | 333.15 | Thermop... | |
| n0 | 1.38432 | 338.15 | Thermop... | |
| n0 | 1.38169 | 343.15 | Thermop... | |
| n0 | 1.37961 | 348.15 | Thermop... | |
| n0 | 1.37725 | 353.15 | Thermop... | |
| n0 | 1.37490 | 358.15 | Thermop... | |
| ρl | 879.76 | kg/m3 | 298.15 | Densiti... |
| λ | [0.12; 0.15] | W/m×K | [263.83; 368.50] |
|
|
T(K) Liquid thermal conductivity (W/m×K) 0.12 0.13 0.13 0.14 0.14 0.15 0.15 300 350 | ||||
| λ | 0.15 | W/m×K | 263.83 | Experim... |
| λ | 0.15 | W/m×K | 268.65 | Experim... |
| λ | 0.14 | W/m×K | 273.70 | Experim... |
| λ | 0.14 | W/m×K | 278.59 | Experim... |
| λ | 0.14 | W/m×K | 283.75 | Experim... |
| λ | 0.14 | W/m×K | 288.67 | Experim... |
| λ | 0.14 | W/m×K | 293.64 | Experim... |
| λ | 0.14 | W/m×K | 298.72 | Experim... |
| λ | 0.14 | W/m×K | 303.63 | Experim... |
| λ | 0.13 | W/m×K | 308.61 | Experim... |
| λ | 0.13 | W/m×K | 313.60 | Experim... |
| λ | 0.13 | W/m×K | 321.08 | Experim... |
| λ | 0.13 | W/m×K | 328.54 | Experim... |
| λ | 0.13 | W/m×K | 333.52 | Experim... |
| λ | 0.13 | W/m×K | 338.55 | Experim... |
| λ | 0.13 | W/m×K | 343.49 | Experim... |
| λ | 0.12 | W/m×K | 348.48 | Experim... |
| λ | 0.12 | W/m×K | 353.70 | Experim... |
| λ | 0.12 | W/m×K | 358.38 | Experim... |
| λ | 0.12 | W/m×K | 363.41 | Experim... |
| λ | 0.12 | W/m×K | 368.50 | Experim... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 325.20 | K | 2.00 | NIST |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 294.86 | 105.00 | 0.0009 |
| 294.75 | 5079.00 | 0.0009 |
| 294.63 | 9980.00 | 0.0010 |
| 294.34 | 15024.00 | 0.0010 |
| 293.98 | 19999.00 | 0.0011 |
| 293.48 | 25055.00 | 0.0011 |
| 292.99 | 29973.00 | 0.0012 |
| 303.12 | 107.00 | 0.0008 |
| 303.09 | 5026.00 | 0.0008 |
| 303.05 | 10031.00 | 0.0009 |
| 303.01 | 15014.00 | 0.0009 |
| 302.98 | 19967.00 | 0.0009 |
| 302.89 | 24988.00 | 0.0010 |
| 302.79 | 29963.00 | 0.0010 |
| 312.74 | 103.00 | 0.0007 |
| 312.70 | 4988.00 | 0.0007 |
| 312.71 | 10033.00 | 0.0008 |
| 312.69 | 15010.00 | 0.0008 |
| 312.69 | 20046.00 | 0.0008 |
| 312.62 | 24986.00 | 0.0008 |
| 312.57 | 29951.00 | 0.0009 |
| 322.29 | 98.00 | 0.0006 |
| 322.29 | 5048.00 | 0.0006 |
| 322.08 | 9972.00 | 0.0007 |
| 322.32 | 15008.00 | 0.0007 |
| 322.12 | 19979.00 | 0.0007 |
| 322.14 | 24972.00 | 0.0008 |
| 321.96 | 29975.00 | 0.0008 |
| 331.89 | 9984.00 | 0.0006 |
| 331.83 | 14994.00 | 0.0006 |
| 331.93 | 20001.00 | 0.0007 |
| 331.80 | 25008.00 | 0.0007 |
| 331.74 | 30010.00 | 0.0007 |
| 341.39 | 20015.00 | 0.0006 |
| 341.41 | 25042.00 | 0.0006 |
| 341.38 | 29965.00 | 0.0006 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 100.00 | 884.48 |
| 293.15 | 1000.00 | 884.65 |
| 293.15 | 3000.00 | 886.42 |
| 293.15 | 5000.00 | 887.67 |
| 293.15 | 10000.00 | 891.64 |
| 293.15 | 15000.00 | 895.33 |
| 293.15 | 20000.00 | 898.81 |
| 293.15 | 25000.00 | 902.28 |
| 293.15 | 30000.00 | 905.55 |
| 293.15 | 35000.00 | 908.69 |
| 293.15 | 40000.00 | 911.73 |
| 293.15 | 50000.00 | 917.83 |
| 293.15 | 60000.00 | 923.06 |
| 303.15 | 100.00 | 874.56 |
| 303.15 | 1000.00 | 875.42 |
| 303.15 | 3000.00 | 877.13 |
| 303.15 | 5000.00 | 878.76 |
| 303.15 | 10000.00 | 882.75 |
| 303.15 | 15000.00 | 886.63 |
| 303.15 | 20000.00 | 890.21 |
| 303.15 | 25000.00 | 893.78 |
| 303.15 | 30000.00 | 897.24 |
| 303.15 | 35000.00 | 900.52 |
| 303.15 | 40000.00 | 903.67 |
| 303.15 | 50000.00 | 909.79 |
| 303.15 | 60000.00 | 915.57 |
| 313.15 | 100.00 | 865.26 |
| 313.15 | 1000.00 | 865.64 |
| 313.15 | 3000.00 | 867.5 |
| 313.15 | 5000.00 | 869.26 |
| 313.15 | 10000.00 | 873.55 |
| 313.15 | 15000.00 | 877.59 |
| 313.15 | 20000.00 | 881.48 |
| 313.15 | 25000.00 | 885.29 |
| 313.15 | 30000.00 | 888.86 |
| 313.15 | 35000.00 | 892.33 |
| 313.15 | 40000.00 | 895.54 |
| 313.15 | 50000.00 | 901.99 |
| 313.15 | 60000.00 | 907.83 |
| 323.15 | 100.00 | 855.18 |
| 323.15 | 1000.00 | 856.16 |
| 323.15 | 3000.00 | 858.01 |
| 323.15 | 5000.00 | 859.89 |
| 323.15 | 10000.00 | 864.44 |
| 323.15 | 15000.00 | 868.76 |
| 323.15 | 20000.00 | 872.98 |
| 323.15 | 25000.00 | 876.76 |
| 323.15 | 30000.00 | 880.55 |
| 323.15 | 35000.00 | 884.15 |
| 323.15 | 40000.00 | 887.68 |
| 323.15 | 50000.00 | 894.33 |
| 323.15 | 60000.00 | 900.65 |
| 333.15 | 100.00 | 845.43 |
| 333.15 | 1000.00 | 846.26 |
| 333.15 | 3000.00 | 848.43 |
| 333.15 | 5000.00 | 850.38 |
| 333.15 | 10000.00 | 855.15 |
| 333.15 | 15000.00 | 859.63 |
| 333.15 | 20000.00 | 864.0 |
| 333.15 | 25000.00 | 868.18 |
| 333.15 | 30000.00 | 871.99 |
| 333.15 | 35000.00 | 875.8 |
| 333.15 | 40000.00 | 879.63 |
| 333.15 | 50000.00 | 886.48 |
| 333.15 | 60000.00 | 892.97 |
| 343.15 | 100.00 | 835.2 |
| 343.15 | 1000.00 | 836.39 |
| 343.15 | 3000.00 | 838.54 |
| 343.15 | 5000.00 | 840.78 |
| 343.15 | 10000.00 | 845.7 |
| 343.15 | 15000.00 | 850.49 |
| 343.15 | 20000.00 | 855.28 |
| 343.15 | 25000.00 | 859.46 |
| 343.15 | 30000.00 | 863.7 |
| 343.15 | 35000.00 | 867.75 |
| 343.15 | 40000.00 | 871.46 |
| 343.15 | 50000.00 | 878.77 |
| 343.15 | 60000.00 | 885.3 |
| 353.15 | 100.00 | 825.57 |
| 353.15 | 1000.00 | 826.5 |
| 353.15 | 3000.00 | 828.96 |
| 353.15 | 5000.00 | 831.13 |
| 353.15 | 10000.00 | 836.55 |
| 353.15 | 15000.00 | 841.75 |
| 353.15 | 20000.00 | 846.44 |
| 353.15 | 25000.00 | 851.08 |
| 353.15 | 30000.00 | 855.46 |
| 353.15 | 35000.00 | 859.68 |
| 353.15 | 40000.00 | 863.59 |
| 353.15 | 50000.00 | 871.08 |
| 353.15 | 60000.00 | 878.16 |
| 363.15 | 100.00 | 815.64 |
| 363.15 | 1000.00 | 816.87 |
| 363.15 | 3000.00 | 819.47 |
| 363.15 | 5000.00 | 821.87 |
| 363.15 | 10000.00 | 827.32 |
| 363.15 | 15000.00 | 833.11 |
| 363.15 | 20000.00 | 837.93 |
| 363.15 | 25000.00 | 842.64 |
| 363.15 | 30000.00 | 847.27 |
| 363.15 | 35000.00 | 851.7 |
| 363.15 | 40000.00 | 856.02 |
| 363.15 | 50000.00 | 863.88 |
| 363.15 | 60000.00 | 871.24 |
| Reference | ||
Speed of sound, m/s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Speed of sound, m/s - Liquid |
| 297.83 | 110.00 | 1225.1 |
| 306.48 | 110.00 | 1182.9 |
| 317.92 | 100.00 | 1137.0 |
| 327.21 | 110.00 | 1090.2 |
| 336.91 | 100.00 | 1055.2 |
| 346.90 | 100.00 | 1021.1 |
| 357.28 | 100.00 | 970.4 |
| 367.48 | 100.00 | 938.2 |
| 377.88 | 110.00 | 903.5 |
| 387.73 | 100.00 | 866.5 |
| 398.60 | 90.00 | 827.8 |
| 407.93 | 100.00 | 799.0 |
| 417.52 | 110.00 | 764.3 |
| 298.76 | 1010.00 | 1231.7 |
| 308.59 | 1010.00 | 1186.9 |
| 318.30 | 1000.00 | 1142.6 |
| 327.58 | 1010.00 | 1097.9 |
| 337.95 | 1000.00 | 1065.3 |
| 346.56 | 1010.00 | 1029.7 |
| 357.85 | 1010.00 | 989.8 |
| 367.24 | 1010.00 | 947.2 |
| 377.91 | 1010.00 | 910.8 |
| 387.01 | 1010.00 | 874.2 |
| 397.64 | 1010.00 | 842.1 |
| 406.65 | 1010.00 | 810.8 |
| 417.08 | 1010.00 | 775.9 |
| 427.06 | 1000.00 | 746.0 |
| 436.99 | 1010.00 | 714.9 |
| 447.88 | 1000.00 | 672.6 |
| 457.84 | 990.00 | 642.8 |
| 466.46 | 1010.00 | 613.5 |
| 478.01 | 1010.00 | 570.1 |
| 417.21 | 5010.00 | 808.2 |
| 427.25 | 5000.00 | 786.5 |
| 437.07 | 5000.00 | 751.6 |
| 447.00 | 4990.00 | 723.0 |
| 456.84 | 5000.00 | 695.3 |
| 466.28 | 5000.00 | 663.1 |
| 478.34 | 5010.00 | 623.4 |
| 487.67 | 5000.00 | 595.0 |
| 497.36 | 5000.00 | 568.5 |
| 507.11 | 5010.00 | 535.1 |
| 517.60 | 5010.00 | 504.9 |
| 528.29 | 5000.00 | 472.6 |
| 538.26 | 5010.00 | 439.9 |
| 547.96 | 5000.00 | 406.1 |
| 558.34 | 5000.00 | 378.3 |
| 567.58 | 5000.00 | 346.5 |
| 575.39 | 5000.00 | 317.9 |
| 586.99 | 5010.00 | 275.0 |
| 298.35 | 7010.00 | 1261.9 |
| 308.90 | 7000.00 | 1221.1 |
| 317.60 | 7010.00 | 1175.8 |
| 327.38 | 7010.00 | 1130.2 |
| 337.21 | 7010.00 | 1102.7 |
| 347.43 | 7000.00 | 1067.3 |
| 357.33 | 7010.00 | 1033.1 |
| 367.18 | 7000.00 | 989.6 |
| 377.97 | 7000.00 | 961.0 |
| 387.07 | 7000.00 | 922.0 |
| 397.54 | 7020.00 | 891.4 |
| 406.79 | 7020.00 | 857.7 |
| 416.99 | 7010.00 | 835.1 |
| 427.33 | 7000.00 | 805.5 |
| 487.58 | 1000.00 | 535.4 |
| 497.17 | 1010.00 | 499.6 |
| 506.88 | 1000.00 | 464.6 |
| 516.99 | 1010.00 | 426.2 |
| 298.85 | 3000.00 | 1240.3 |
| 309.19 | 3010.00 | 1197.6 |
| 319.17 | 3010.00 | 1152.2 |
| 327.90 | 3000.00 | 1107.9 |
| 337.97 | 3000.00 | 1078.0 |
| 347.71 | 3010.00 | 1040.3 |
| 356.24 | 3010.00 | 1011.9 |
| 366.38 | 3010.00 | 970.6 |
| 377.25 | 3000.00 | 927.9 |
| 386.63 | 3000.00 | 894.6 |
| 396.70 | 3000.00 | 862.0 |
| 406.78 | 3010.00 | 828.8 |
| 417.12 | 3000.00 | 796.9 |
| 427.25 | 3000.00 | 770.6 |
| 439.30 | 3000.00 | 727.5 |
| 446.68 | 3010.00 | 706.2 |
| 456.61 | 3000.00 | 673.8 |
| 466.22 | 3010.00 | 642.9 |
| 478.43 | 3010.00 | 596.3 |
| 487.67 | 3010.00 | 565.4 |
| 497.43 | 3010.00 | 534.1 |
| 506.49 | 3000.00 | 503.9 |
| 517.56 | 3000.00 | 468.7 |
| 529.52 | 3000.00 | 426.0 |
| 538.04 | 3000.00 | 396.8 |
| 547.56 | 3000.00 | 362.7 |
| 557.68 | 3000.00 | 321.9 |
| 566.56 | 3010.00 | 285.3 |
| 576.45 | 3010.00 | 241.0 |
| 437.97 | 6990.00 | 771.5 |
| 447.38 | 7000.00 | 744.5 |
| 457.10 | 7010.00 | 715.1 |
| 466.30 | 7000.00 | 689.7 |
| 478.28 | 7000.00 | 646.3 |
| 487.69 | 7000.00 | 617.0 |
| 497.38 | 7000.00 | 591.6 |
| 506.97 | 7010.00 | 563.3 |
| 517.52 | 7010.00 | 531.6 |
| 528.46 | 7000.00 | 504.0 |
| 538.26 | 7000.00 | 472.1 |
| 548.26 | 7000.00 | 446.0 |
| 557.89 | 7010.00 | 423.0 |
| 567.72 | 7010.00 | 390.1 |
| 576.35 | 7000.00 | 365.2 |
| 587.76 | 7000.00 | 334.6 |
| 298.17 | 10000.00 | 1274.4 |
| 308.58 | 10010.00 | 1227.8 |
| 317.52 | 10010.00 | 1181.0 |
| 327.40 | 10010.00 | 1143.2 |
| 337.71 | 10010.00 | 1111.9 |
| 346.92 | 10020.00 | 1081.3 |
| 356.68 | 10010.00 | 1048.7 |
| 366.89 | 10000.00 | 1005.5 |
| 377.70 | 10000.00 | 974.3 |
| 386.85 | 10000.00 | 945.8 |
| 397.25 | 10010.00 | 909.9 |
| 406.89 | 10000.00 | 885.7 |
| 417.21 | 10020.00 | 864.4 |
| 427.38 | 10010.00 | 833.5 |
| 438.10 | 9980.00 | 802.1 |
| 447.21 | 10010.00 | 776.0 |
| 456.81 | 9990.00 | 747.0 |
| 586.48 | 3000.00 | 197.5 |
| 298.56 | 5000.00 | 1252.4 |
| 309.13 | 5010.00 | 1210.5 |
| 318.41 | 5010.00 | 1160.9 |
| 327.64 | 5010.00 | 1120.6 |
| 337.21 | 5000.00 | 1091.3 |
| 347.75 | 5010.00 | 1054.8 |
| 357.35 | 5000.00 | 1022.1 |
| 366.68 | 5000.00 | 980.4 |
| 377.72 | 5000.00 | 939.5 |
| 387.29 | 5000.00 | 908.4 |
| 397.83 | 5000.00 | 875.5 |
| 406.99 | 5010.00 | 841.7 |
| 466.30 | 10010.00 | 720.4 |
| 478.28 | 10000.00 | 677.8 |
| 487.71 | 10000.00 | 653.5 |
| 497.44 | 10000.00 | 629.4 |
| 507.02 | 10020.00 | 599.2 |
| 517.63 | 10010.00 | 571.0 |
| 528.65 | 10010.00 | 547.3 |
| 538.35 | 10000.00 | 516.1 |
| 548.18 | 9980.00 | 498.8 |
| 558.07 | 10000.00 | 472.6 |
| 565.69 | 10010.00 | 446.4 |
| 577.04 | 10010.00 | 420.8 |
| 588.07 | 10030.00 | 393.2 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [315.12; 449.30] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.49142e+01 | |||
| Coefficient B | -3.75133e+03 | |||
| Coefficient C | -5.86470e+01 | |||
| Temperature range, min. | 315.12 | |||
| Temperature range, max. | 449.30 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
| Pvap | 1.33 | kPa | 315.12 | Calculated Property |
| Pvap | 2.98 | kPa | 330.03 | Calculated Property |
| Pvap | 6.12 | kPa | 344.94 | Calculated Property |
| Pvap | 11.70 | kPa | 359.85 | Calculated Property |
| Pvap | 21.05 | kPa | 374.76 | Calculated Property |
| Pvap | 35.93 | kPa | 389.66 | Calculated Property |
| Pvap | 58.55 | kPa | 404.57 | Calculated Property |
| Pvap | 91.65 | kPa | 419.48 | Calculated Property |
| Pvap | 138.44 | kPa | 434.39 | Calculated Property |
| Pvap | 202.65 | kPa | 449.30 | Calculated Property |
Similar Compounds
Find more compounds similar to Hexanoic acid, methyl ester.
Mixtures
- Hexanoic acid, methyl ester + Water
- Acetonitrile + Hexanoic acid, methyl ester
- Propanenitrile + Hexanoic acid, methyl ester
Sources
- Crippen Method
- Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
- High-pressure liquid densities of fatty acid methyl esters: Measurement and prediction with the PC-SAFT equation of state
- Experimental vapor pressures (from 1 Pa to 100 kPa) of six saturated Fatty Acid Methyl Esters (FAMEs): Methyl hexanoate, methyl octanoate, methyl decanoate, methyl dodecanoate, methyl tetradecanoate and methyl hexadecanoate
- Densities and interfacial tensions for fatty acid methyl esters (from methyl formate to methyl heptanoate) + water demixed mixtures at atmospheric pressure conditions
- Experimental investigations on the liquid thermal conductivity of five saturated fatty acid methyl esters components of biodiesel
- Heat capacities and thermal diffusivities of some n-alkanoic acid methyl esters
- Thermophysical properties of fatty acid methyl and ethyl esters
- Liquid viscosities for methyl hexanoate, methyl heptanoate, methyl caprylate, and methyl nonanoate at high pressures
- Measurement of Speed of Sound in Methyl Hexanoate from 297.83 to 588.07 K and up to 10 MPa
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 8. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
- Vapor-Liquid Equilibrium Data for the Binary Methyl Esters (Butyrate, Pentanoate, and Hexanoate) (1) + Acetonitrile (2) Systems at 93.32 kPa
- Experimental Study of Thermodynamic Properties of Mixtures Containing Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate Using Gas-Liquid Chromatography and Transpiration Method
- Vapor-Liquid Equilibrium Data for the Binary Methyl Esters (Butyrate, Pentanoate, and Hexanoate) (1) + Propanenitrile (2) Systems at 93.32 kPa
- Joback Method
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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