- InChI
- InChI=1S/C8H16O2/c1-3-4-5-6-7-8(9)10-2/h3-7H2,1-2H3
- InChI Key
- XNCNNDVCAUWAIT-UHFFFAOYSA-N
- Formula
- C8H16O2
- SMILES
- CCCCCCC(=O)OC
- Molecular Weight1
- 144.21
- CAS
- 106-73-0
- Other Names
-
- Methyl enanthate
- Methyl ester of heptanoic acid
- Methyl heptanoate
- Methyl heptoate
- Methyl n-heptanoate
- Methyl n-heptylate
- Methyl oenanthylate
- enanthic acid, methyl ester
- methyl oenanthate
- oenanthic 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.
- 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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Contents
- Physical Properties
- Temperature Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | -4867.40 ± 0.80 | kJ/mol | NIST |
| ΔfG° | -217.44 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -517.00 ± 2.00 | kJ/mol | NIST |
| ΔfH°liquid | -567.10 ± 0.92 | kJ/mol | NIST |
| ΔfusH° | 19.26 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [49.70; 53.70] | kJ/mol |
|
| ΔvapH° | 53.20 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 51.80 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 53.40 | kJ/mol | NIST |
| ΔvapH° | 53.70 | kJ/mol | NIST |
| ΔvapH° | 53.50 | kJ/mol | NIST |
| ΔvapH° | 49.70 ± 0.50 | kJ/mol | NIST |
| ΔvapH° | 53.10 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 53.10 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 51.62 ± 0.48 | kJ/mol | NIST |
| ΔvapH° | 51.60 ± 0.50 | kJ/mol | NIST |
| ΔvapH° | 50.00 ± 1.00 | kJ/mol | NIST |
| ΔvapH° | 50.10 | kJ/mol | NIST |
| log10WS | -2.03 | Crippen Calculated Property | |
| logPoct/wat | 2.130 | Crippen Calculated Property | |
| McVol | 131.020 | ml/mol | McGowan Calculated Property |
| Pc | 2657.03 | kPa | Joback Calculated Property |
| Inp | [164.60; 1028.40] |
|
|
| Inp | 1023.90 | NIST | |
| Inp | 1023.30 | NIST | |
| Inp | 1022.90 | NIST | |
| Inp | 1005.00 | NIST | |
| Inp | 1012.00 | NIST | |
| Inp | 1002.00 | NIST | |
| Inp | 1006.00 | NIST | |
| Inp | 1011.00 | NIST | |
| Inp | 1007.00 | NIST | |
| Inp | 1026.00 | NIST | |
| Inp | 1008.60 | NIST | |
| Inp | 1008.10 | NIST | |
| Inp | 1008.00 | NIST | |
| Inp | 1027.70 | NIST | |
| Inp | 1028.40 | NIST | |
| Inp | 1021.00 | NIST | |
| Inp | 1005.00 | NIST | |
| Inp | 1004.00 | NIST | |
| Inp | 1007.00 | NIST | |
| Inp | 1007.00 | NIST | |
| Inp | 1006.00 | NIST | |
| Inp | 1026.00 | NIST | |
| Inp | 1013.00 | NIST | |
| Inp | 1013.00 | NIST | |
| Inp | 1005.00 | NIST | |
| Inp | 1009.00 | NIST | |
| Inp | 1010.00 | NIST | |
| Inp | 1006.00 | NIST | |
| Inp | 1006.00 | NIST | |
| Inp | 1006.00 | NIST | |
| Inp | 1025.00 | NIST | |
| Inp | 1005.00 | NIST | |
| Inp | 1025.00 | NIST | |
| Inp | 1021.00 | NIST | |
| Inp | 1006.00 | NIST | |
| Inp | 1006.00 | NIST | |
| Inp | 1014.00 | NIST | |
| Inp | 1005.00 | NIST | |
| Inp | 1006.00 | NIST | |
| Inp | 1006.00 | NIST | |
| Inp | 1008.00 | NIST | |
| Inp | Outlier 164.60 | NIST | |
| Inp | 1006.00 | NIST | |
| Inp | Outlier 164.60 | NIST | |
| Inp | 1025.00 | NIST | |
| Inp | 1008.00 | NIST | |
| Inp | 1009.00 | NIST | |
| Inp | 1023.90 | NIST | |
| Inp | 1002.00 | NIST | |
| I | [1241.00; 1327.00] |
|
|
| I | Outlier 1241.00 | NIST | |
| I | Outlier 1327.00 | NIST | |
| I | 1281.00 | NIST | |
| I | 1291.00 | NIST | |
| I | 1301.00 | NIST | |
| I | 1292.00 | NIST | |
| I | 1299.00 | NIST | |
| I | 1291.00 | NIST | |
| I | 1282.00 | NIST | |
| I | 1288.00 | NIST | |
| I | 1296.00 | NIST | |
| I | 1284.00 | NIST | |
| I | 1273.00 | NIST | |
| I | 1279.00 | NIST | |
| I | 1273.00 | NIST | |
| I | 1279.00 | NIST | |
| I | 1279.00 | NIST | |
| I | 1296.00 | NIST | |
| I | 1276.00 | NIST | |
| I | 1273.00 | NIST | |
| I | 1302.00 | NIST | |
| I | 1281.00 | NIST | |
| I | 1291.00 | NIST | |
| I | 1282.00 | NIST | |
| I | 1296.00 | NIST | |
| I | 1288.00 | NIST | |
| Tboil | [445.20; 446.95] | K |
|
| Tboil | 445.20 | K | NIST |
| Tboil | 446.95 ± 0.30 | K | NIST |
| Tboil | 445.30 ± 2.00 | K | NIST |
| Tc | 633.80 | K | Joback Calculated Property |
| Tfus | [217.40; 217.40] | K |
|
| Tfus | 217.40 ± 0.05 | K | NIST |
| Tfus | 217.40 ± 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 |
| Cp,liquid | [285.10; 316.90] | J/mol×K | [298.15; 373.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 285 290 295 300 305 310 315 320 300 320 340 360 | ||||
| Cp,liquid | 285.10 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 289.20 | J/mol×K | 303.15 | Heat ca... |
| Cp,liquid | 292.50 | J/mol×K | 313.15 | Heat ca... |
| Cp,liquid | 296.20 | J/mol×K | 323.15 | Heat ca... |
| Cp,liquid | 300.10 | J/mol×K | 333.15 | Heat ca... |
| Cp,liquid | 304.30 | J/mol×K | 343.15 | Heat ca... |
| Cp,liquid | 308.60 | J/mol×K | 353.15 | Heat ca... |
| Cp,liquid | 312.80 | J/mol×K | 363.15 | Heat ca... |
| Cp,liquid | 316.90 | J/mol×K | 373.15 | Heat ca... |
| η | [0.0008230; 0.0013200] | Pa×s | [283.15; 313.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 8.00e-4 9.00e-4 1.00e-3 1.10e-3 1.20e-3 1.30e-3 290 300 310 | ||||
| η | 0.0013200 | Pa×s | 283.15 | A Study... |
| η | 0.0011120 | Pa×s | 293.15 | A Study... |
| η | 0.0010230 | Pa×s | 298.15 | A Study... |
| η | 0.0009500 | Pa×s | 303.15 | A Study... |
| η | 0.0008230 | Pa×s | 313.15 | A Study... |
| ΔvapH | [46.30; 50.20] | kJ/mol | [326.00; 432.50] |
|
| ΔvapH | 50.20 ± 0.10 | kJ/mol | 326.00 | NIST |
| ΔvapH | 49.10 | kJ/mol | 350.00 | NIST |
| ΔvapH | 49.00 | kJ/mol | 367.00 | NIST |
| ΔvapH | 46.30 | kJ/mol | 432.50 | NIST |
| Pvap | [0.03; 0.47] | kPa | [278.10; 313.20] |
|
|
T(K) Vapor pressure (kPa) 0 0.1 0.2 0.3 0.4 0.5 280 290 300 310 | ||||
| Pvap | 0.03 | kPa | 278.10 | Transpi... |
| Pvap | 0.05 | kPa | 283.50 | Transpi... |
| Pvap | 0.07 | kPa | 286.40 | Transpi... |
| Pvap | 0.08 | kPa | 288.30 | Transpi... |
| Pvap | 0.09 | kPa | 290.30 | Transpi... |
| Pvap | 0.12 | kPa | 293.20 | Transpi... |
| Pvap | 0.14 | kPa | 296.20 | Transpi... |
| Pvap | 0.16 | kPa | 298.20 | Transpi... |
| Pvap | 0.19 | kPa | 300.30 | Transpi... |
| Pvap | 0.23 | kPa | 303.10 | Transpi... |
| Pvap | 0.28 | kPa | 306.10 | Transpi... |
| Pvap | 0.33 | kPa | 308.20 | Transpi... |
| Pvap | 0.38 | kPa | 310.20 | Transpi... |
| Pvap | 0.47 | kPa | 313.20 | Transpi... |
| n0 | [1.38276; 1.41865] | [278.15; 358.15] |
|
|
|
T(K) Refractive Index 1.38 1.39 1.4 1.41 1.42 300 350 | ||||
| n0 | 1.41865 | 278.15 | Thermop... | |
| n0 | 1.41643 | 283.15 | Thermop... | |
| n0 | 1.41421 | 288.15 | Thermop... | |
| n0 | 1.41199 | 293.15 | Thermop... | |
| n0 | 1.40945 | 298.15 | Densiti... | |
| n0 | 1.40976 | 298.15 | Thermop... | |
| n0 | 1.40945 | 298.15 | Isobari... | |
| n0 | 1.40753 | 303.15 | Thermop... | |
| n0 | 1.40530 | 308.15 | Thermop... | |
| n0 | 1.40301 | 313.15 | Thermop... | |
| n0 | 1.40070 | 318.15 | Thermop... | |
| n0 | 1.39841 | 323.15 | Thermop... | |
| n0 | 1.39614 | 328.15 | Thermop... | |
| n0 | 1.39389 | 333.15 | Thermop... | |
| n0 | 1.39167 | 338.15 | Thermop... | |
| n0 | 1.38946 | 343.15 | Thermop... | |
| n0 | 1.38724 | 348.15 | Thermop... | |
| n0 | 1.38501 | 353.15 | Thermop... | |
| n0 | 1.38276 | 358.15 | Thermop... | |
| ρl | 875.61 | kg/m3 | 298.15 | Densiti... |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 294.20 | 107.00 | 0.0011 |
| 294.13 | 4967.00 | 0.0012 |
| 293.85 | 9970.00 | 0.0012 |
| 293.58 | 14994.00 | 0.0013 |
| 292.87 | 19994.00 | 0.0014 |
| 292.56 | 25040.00 | 0.0014 |
| 292.04 | 30028.00 | 0.0015 |
| 303.15 | 102.00 | 0.0009 |
| 303.12 | 5011.00 | 0.0010 |
| 303.08 | 10026.00 | 0.0010 |
| 303.05 | 14993.00 | 0.0011 |
| 303.02 | 19985.00 | 0.0011 |
| 302.93 | 25017.00 | 0.0012 |
| 302.83 | 29961.00 | 0.0012 |
| 312.77 | 103.00 | 0.0008 |
| 312.78 | 5010.00 | 0.0009 |
| 312.65 | 10009.00 | 0.0009 |
| 312.66 | 15001.00 | 0.0010 |
| 312.62 | 20047.00 | 0.0010 |
| 312.57 | 25001.00 | 0.0010 |
| 312.49 | 29986.00 | 0.0011 |
| 322.33 | 96.00 | 0.0007 |
| 322.26 | 5004.00 | 0.0008 |
| 322.23 | 10018.00 | 0.0008 |
| 322.21 | 15004.00 | 0.0008 |
| 322.17 | 19955.00 | 0.0009 |
| 322.23 | 25027.00 | 0.0009 |
| 322.09 | 29925.00 | 0.0010 |
| 331.85 | 99.00 | 0.0006 |
| 331.78 | 5007.00 | 0.0007 |
| 331.78 | 9972.00 | 0.0007 |
| 331.74 | 15035.00 | 0.0008 |
| 331.67 | 19865.00 | 0.0008 |
| 331.68 | 25041.00 | 0.0008 |
| 331.56 | 30001.00 | 0.0009 |
| 341.67 | 96.00 | 0.0006 |
| 341.72 | 5062.00 | 0.0006 |
| 341.68 | 10141.00 | 0.0006 |
| 341.48 | 14961.00 | 0.0007 |
| 341.81 | 20048.00 | 0.0007 |
| 341.80 | 25032.00 | 0.0008 |
| 341.73 | 29980.00 | 0.0008 |
| 351.27 | 10077.00 | 0.0006 |
| 351.26 | 14966.00 | 0.0006 |
| 351.31 | 19977.00 | 0.0006 |
| 351.49 | 24997.00 | 0.0007 |
| 351.46 | 30010.00 | 0.0007 |
| 361.37 | 20002.00 | 0.0006 |
| 361.47 | 25022.00 | 0.0006 |
| 361.24 | 29993.00 | 0.0006 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 100.00 | 880.16 |
| 293.15 | 1000.00 | 880.29 |
| 293.15 | 3000.00 | 881.98 |
| 293.15 | 5000.00 | 883.19 |
| 293.15 | 10000.00 | 886.99 |
| 293.15 | 15000.00 | 890.49 |
| 293.15 | 20000.00 | 893.86 |
| 293.15 | 25000.00 | 897.18 |
| 293.15 | 30000.00 | 900.36 |
| 293.15 | 35000.00 | 903.34 |
| 293.15 | 40000.00 | 906.22 |
| 293.15 | 50000.00 | 912.14 |
| 293.15 | 60000.00 | 917.16 |
| 303.15 | 100.00 | 870.66 |
| 303.15 | 1000.00 | 871.46 |
| 303.15 | 3000.00 | 873.07 |
| 303.15 | 5000.00 | 874.66 |
| 303.15 | 10000.00 | 878.5 |
| 303.15 | 15000.00 | 882.18 |
| 303.15 | 20000.00 | 885.64 |
| 303.15 | 25000.00 | 889.08 |
| 303.15 | 30000.00 | 892.3 |
| 303.15 | 35000.00 | 895.46 |
| 303.15 | 40000.00 | 898.49 |
| 303.15 | 50000.00 | 904.43 |
| 303.15 | 60000.00 | 909.95 |
| 313.15 | 100.00 | 861.82 |
| 313.15 | 1000.00 | 862.16 |
| 313.15 | 3000.00 | 863.9 |
| 313.15 | 5000.00 | 865.62 |
| 313.15 | 10000.00 | 869.71 |
| 313.15 | 15000.00 | 873.55 |
| 313.15 | 20000.00 | 877.29 |
| 313.15 | 25000.00 | 880.89 |
| 313.15 | 30000.00 | 884.32 |
| 313.15 | 35000.00 | 887.66 |
| 313.15 | 40000.00 | 890.73 |
| 313.15 | 50000.00 | 896.98 |
| 313.15 | 60000.00 | 902.59 |
| 323.15 | 100.00 | 852.25 |
| 323.15 | 1000.00 | 853.12 |
| 323.15 | 3000.00 | 854.89 |
| 323.15 | 5000.00 | 856.64 |
| 323.15 | 10000.00 | 860.97 |
| 323.15 | 15000.00 | 865.07 |
| 323.15 | 20000.00 | 869.08 |
| 323.15 | 25000.00 | 872.69 |
| 323.15 | 30000.00 | 876.31 |
| 323.15 | 35000.00 | 879.74 |
| 323.15 | 40000.00 | 883.15 |
| 323.15 | 50000.00 | 889.53 |
| 323.15 | 60000.00 | 895.63 |
| 333.15 | 100.00 | 843.03 |
| 333.15 | 1000.00 | 843.81 |
| 333.15 | 3000.00 | 845.84 |
| 333.15 | 5000.00 | 847.68 |
| 333.15 | 10000.00 | 852.16 |
| 333.15 | 15000.00 | 856.43 |
| 333.15 | 20000.00 | 860.63 |
| 333.15 | 25000.00 | 864.64 |
| 333.15 | 30000.00 | 868.31 |
| 333.15 | 35000.00 | 871.91 |
| 333.15 | 40000.00 | 875.61 |
| 333.15 | 50000.00 | 882.2 |
| 333.15 | 60000.00 | 888.39 |
| 343.15 | 100.00 | 833.48 |
| 343.15 | 1000.00 | 834.64 |
| 343.15 | 3000.00 | 836.7 |
| 343.15 | 5000.00 | 838.79 |
| 343.15 | 10000.00 | 843.47 |
| 343.15 | 15000.00 | 848.02 |
| 343.15 | 20000.00 | 852.59 |
| 343.15 | 25000.00 | 856.55 |
| 343.15 | 30000.00 | 860.57 |
| 343.15 | 35000.00 | 864.43 |
| 343.15 | 40000.00 | 867.96 |
| 343.15 | 50000.00 | 875.0 |
| 343.15 | 60000.00 | 881.19 |
| 353.15 | 100.00 | 824.35 |
| 353.15 | 1000.00 | 825.27 |
| 353.15 | 3000.00 | 827.61 |
| 353.15 | 5000.00 | 829.66 |
| 353.15 | 10000.00 | 834.76 |
| 353.15 | 15000.00 | 839.63 |
| 353.15 | 20000.00 | 844.11 |
| 353.15 | 25000.00 | 848.48 |
| 353.15 | 30000.00 | 852.65 |
| 353.15 | 35000.00 | 856.65 |
| 353.15 | 40000.00 | 860.37 |
| 353.15 | 50000.00 | 867.57 |
| 353.15 | 60000.00 | 874.32 |
| 363.15 | 100.00 | 815.19 |
| 363.15 | 1000.00 | 816.36 |
| 363.15 | 3000.00 | 818.75 |
| 363.15 | 5000.00 | 821.0 |
| 363.15 | 10000.00 | 826.14 |
| 363.15 | 15000.00 | 831.57 |
| 363.15 | 20000.00 | 836.11 |
| 363.15 | 25000.00 | 840.56 |
| 363.15 | 30000.00 | 845.01 |
| 363.15 | 35000.00 | 849.23 |
| 363.15 | 40000.00 | 853.33 |
| 363.15 | 50000.00 | 860.82 |
| 363.15 | 60000.00 | 867.91 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [334.72; 471.89] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.51732e+01 | |||
| Coefficient B | -4.00813e+03 | |||
| Coefficient C | -6.54580e+01 | |||
| Temperature range, min. | 334.72 | |||
| Temperature range, max. | 471.89 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
| Pvap | 1.33 | kPa | 334.72 | Calculated Property |
| Pvap | 2.96 | kPa | 349.96 | Calculated Property |
| Pvap | 6.06 | kPa | 365.20 | Calculated Property |
| Pvap | 11.57 | kPa | 380.44 | Calculated Property |
| Pvap | 20.82 | kPa | 395.68 | Calculated Property |
| Pvap | 35.56 | kPa | 410.93 | Calculated Property |
| Pvap | 58.05 | kPa | 426.17 | Calculated Property |
| Pvap | 91.09 | kPa | 441.41 | Calculated Property |
| Pvap | 138.00 | kPa | 456.65 | Calculated Property |
| Pvap | 202.64 | kPa | 471.89 | Calculated Property |
Similar Compounds
Find more compounds similar to Heptanoic acid, methyl ester.
Mixtures
- Toluene + Heptanoic acid, methyl ester + Acetic acid, methyl ester
- Heptanoic acid, methyl ester + Water
- Heptanoic acid, methyl ester + 1-Hexanol
- Octane + Heptanoic acid, methyl ester + 1-Hexanol
- Benzene + Heptanoic acid, methyl ester
- Carbon dioxide + Heptanoic acid, methyl ester
Sources
- Crippen Method
- 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
- Densities, speeds of sound, and refractive indices of the ternary mixtures (toluene + methyl acetate + butyl acetate) and (toluene + methyl acetate + methyl heptanoate) at 298.15 K
- Densities and interfacial tensions for fatty acid methyl esters (from methyl formate to methyl heptanoate) + water demixed mixtures at atmospheric pressure conditions
- Solubilities of CO2 capture absorbents methyl benzoate, ethyl hexanoate and methyl heptanoate
- Below the room temperature measurements of solubilities in ester absorbents for CO2 capture
- 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
- A Study on Properties Derived from Densities and Viscosities for the Ternary Systems (Methyl Pentanoate or Methyl Heptanoate) + n-Octane + 1-Hexanol and their Binary Subsystems at Various Temperatures.
- 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
- Experimental Study of Thermodynamic Properties of Mixtures Containing Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate Using Gas-Liquid Chromatography and Transpiration Method
- Isobaric Vapor-Liquid Equilibria for the Binary Systems Benzene + Methyl Ethanoate, Benzene + Butyl Ethanoate, and Benzene + Methyl Heptanoate at 101.31kPa
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.