- InChI
- InChI=1S/C6H12O2/c1-3-4-5-6(7)8-2/h3-5H2,1-2H3
- InChI Key
- HNBDRPTVWVGKBR-UHFFFAOYSA-N
- Formula
- C6H12O2
- SMILES
- CCCCC(=O)OC
- Molecular Weight1
- 116.16
- CAS
- 624-24-8
- Other Names
-
- CH3(CH2)3COOCH3
- Methyl ester of pentanoic acid
- Methyl n-valerate
- Methyl pentanoate
- Methyl valerianate
- Pentanoic acid, methyl ester
- Propyl propanoate
- Valeric acid, methyl ester
- n-Valeric acid methyl ester
- valeric 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).
- IE : Ionization energy (eV).
- 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.
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (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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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | [-3561.70; -3548.00] | kJ/mol |
|
| ΔcH°liquid | -3561.70 ± 0.60 | kJ/mol | NIST |
| ΔcH°liquid | -3548.00 | kJ/mol | NIST |
| ΔfG° | -234.28 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-485.00; -472.00] | kJ/mol |
|
| ΔfH°gas | -472.00 ± 2.00 | kJ/mol | NIST |
| ΔfH°gas | -485.00 ± 2.00 | kJ/mol | NIST |
| ΔfH°liquid | [-527.00; -514.20] | kJ/mol |
|
| ΔfH°liquid | -514.20 ± 7.10 | kJ/mol | NIST |
| ΔfH°liquid | -527.00 | kJ/mol | NIST |
| ΔfusH° | 14.08 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 38.11 | kJ/mol | Joback Calculated Property |
| IE | 10.40 ± 0.20 | eV | NIST |
| log10WS | [-1.36; -1.34] |
|
|
| log10WS | -1.36 | Aq. Sol... | |
| log10WS | -1.34 | Estimat... | |
| logPoct/wat | 1.350 | Crippen Calculated Property | |
| McVol | 102.840 | ml/mol | McGowan Calculated Property |
| Pc | 3190.00 ± 202.65 | kPa | NIST |
| ρc | 278.78 ± 19.75 | kg/m3 | NIST |
| Inp | [784.00; 852.00] |
|
|
| Inp | 822.80 | NIST | |
| Inp | 821.90 | NIST | |
| Inp | 821.20 | NIST | |
| Inp | 794.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 816.00 | NIST | |
| Inp | 807.00 | NIST | |
| Inp | 812.00 | NIST | |
| Inp | 814.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 810.00 | NIST | |
| Inp | 807.00 | NIST | |
| Inp | 823.00 | NIST | |
| Inp | 823.00 | NIST | |
| Inp | 823.00 | NIST | |
| Inp | 825.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 808.80 | NIST | |
| Inp | 807.00 | NIST | |
| Inp | Outlier 852.00 | NIST | |
| Inp | 808.00 | NIST | |
| Inp | 821.00 | NIST | |
| Inp | 825.00 | NIST | |
| Inp | 808.00 | NIST | |
| Inp | 823.00 | NIST | |
| Inp | 809.00 | NIST | |
| Inp | 821.00 | NIST | |
| Inp | 829.10 | NIST | |
| Inp | 823.00 | NIST | |
| Inp | 823.00 | NIST | |
| Inp | 811.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 810.00 | NIST | |
| Inp | 810.00 | NIST | |
| Inp | 807.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | Outlier 784.00 | NIST | |
| Inp | 830.00 | NIST | |
| Inp | 807.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 808.00 | NIST | |
| Inp | 823.00 | NIST | |
| Inp | 808.80 | NIST | |
| Inp | 821.00 | NIST | |
| Inp | 822.80 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 830.00 | NIST | |
| I | [1075.00; 1123.00] |
|
|
| I | 1083.00 | NIST | |
| I | Outlier 1123.00 | NIST | |
| I | 1081.00 | NIST | |
| I | 1085.00 | NIST | |
| I | 1089.00 | NIST | |
| I | 1075.00 | NIST | |
| I | 1086.00 | NIST | |
| I | 1096.00 | NIST | |
| I | 1090.00 | NIST | |
| I | 1084.00 | NIST | |
| I | 1090.00 | NIST | |
| I | 1095.00 | NIST | |
| I | 1082.00 | NIST | |
| I | 1087.00 | NIST | |
| I | 1086.00 | NIST | |
| I | 1081.00 | NIST | |
| I | 1085.00 | NIST | |
| I | 1076.00 | NIST | |
| I | 1082.00 | NIST | |
| I | 1083.00 | NIST | |
| I | 1076.00 | NIST | |
| I | Outlier 1109.00 | NIST | |
| I | 1083.00 | NIST | |
| Tboil | 400.48 | K | Vapor L... |
| Tc | [556.70; 566.90] | K |
|
| Tc | 556.70 ± 20.00 | K | NIST |
| Tc | 566.90 ± 20.00 | K | NIST |
| Tfus | 182.50 ± 0.05 | K | NIST |
| Vc | 0.396 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [199.87; 254.27] | J/mol×K | [412.97; 590.55] |
|
| Cp,gas | 199.87 | J/mol×K | 412.97 | Joback Calculated Property |
| Cp,gas | 209.71 | J/mol×K | 442.57 | Joback Calculated Property |
| Cp,gas | 219.25 | J/mol×K | 472.16 | Joback Calculated Property |
| Cp,gas | 228.47 | J/mol×K | 501.76 | Joback Calculated Property |
| Cp,gas | 237.38 | J/mol×K | 531.36 | Joback Calculated Property |
| Cp,gas | 245.98 | J/mol×K | 560.96 | Joback Calculated Property |
| Cp,gas | 254.27 | J/mol×K | 590.55 | Joback Calculated Property |
| Cp,liquid | [226.11; 229.30] | J/mol×K | [298.15; 298.15] |
|
| Cp,liquid | 226.11 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 229.30 | J/mol×K | 298.15 | NIST |
| η | [0.0005510; 0.0008160] | Pa×s | [283.15; 313.15] |
|
| η | 0.0008160 | Pa×s | 283.15 | A Study... |
| η | 0.0007120 | Pa×s | 293.15 | A Study... |
| η | 0.0006610 | Pa×s | 298.15 | A Study... |
| η | 0.0006230 | Pa×s | 303.15 | A Study... |
| η | 0.0005510 | Pa×s | 313.15 | A Study... |
| ΔvapH | [39.20; 44.40] | kJ/mol | [350.00; 414.00] |
|
| ΔvapH | 41.30 | kJ/mol | 350.00 | NIST |
| ΔvapH | 42.50 | kJ/mol | 354.00 | NIST |
| ΔvapH | 44.10 ± 0.10 | kJ/mol | 382.50 | NIST |
| ΔvapH | 39.20 | kJ/mol | 390.50 | NIST |
| ΔvapH | 44.40 | kJ/mol | 414.00 | NIST |
| Pvap | [0.34; 101.30] | kPa | [274.90; 400.48] |
|
| Pvap | 0.34 | kPa | 274.90 | Transpi... |
| Pvap | 0.34 | kPa | 275.20 | Transpi... |
| Pvap | 0.42 | kPa | 278.20 | Transpi... |
| Pvap | 0.46 | kPa | 279.40 | Transpi... |
| Pvap | 0.52 | kPa | 281.20 | Transpi... |
| Pvap | 0.56 | kPa | 282.60 | Transpi... |
| Pvap | 0.64 | kPa | 284.20 | Transpi... |
| Pvap | 0.60 | kPa | 284.30 | Transpi... |
| Pvap | 0.62 | kPa | 284.50 | Transpi... |
| Pvap | 0.69 | kPa | 285.50 | Transpi... |
| Pvap | 0.75 | kPa | 287.40 | Transpi... |
| Pvap | 0.78 | kPa | 288.40 | Transpi... |
| Pvap | 0.79 | kPa | 288.40 | Transpi... |
| Pvap | 0.82 | kPa | 288.50 | Transpi... |
| Pvap | 0.83 | kPa | 288.70 | Transpi... |
| Pvap | 0.87 | kPa | 289.20 | Transpi... |
| Pvap | 0.93 | kPa | 290.30 | Transpi... |
| Pvap | 1.03 | kPa | 292.40 | Transpi... |
| Pvap | 1.09 | kPa | 293.30 | Transpi... |
| Pvap | 1.13 | kPa | 293.40 | Transpi... |
| Pvap | 1.23 | kPa | 294.50 | Transpi... |
| Pvap | 1.33 | kPa | 296.20 | Transpi... |
| Pvap | 1.51 | kPa | 297.50 | Transpi... |
| Pvap | 1.52 | kPa | 298.30 | Transpi... |
| Pvap | 1.61 | kPa | 299.20 | Transpi... |
| Pvap | 1.58 | kPa | 299.20 | Transpi... |
| Pvap | 1.97 | kPa | 302.20 | Transpi... |
| Pvap | 1.94 | kPa | 302.20 | Transpi... |
| Pvap | 2.27 | kPa | 305.20 | Transpi... |
| Pvap | 2.65 | kPa | 308.20 | Transpi... |
| Pvap | 3.11 | kPa | 311.20 | Transpi... |
| Pvap | 29.41 | kPa | 361.82 | Vapor L... |
| Pvap | 35.06 | kPa | 366.70 | Vapor L... |
| Pvap | 40.47 | kPa | 370.86 | Vapor L... |
| Pvap | 45.81 | kPa | 374.53 | Vapor L... |
| Pvap | 52.83 | kPa | 378.84 | Vapor L... |
| Pvap | 59.35 | kPa | 382.55 | Vapor L... |
| Pvap | 60.00 | kPa | 383.29 | Vapor L... |
| Pvap | 69.02 | kPa | 387.18 | Vapor L... |
| Pvap | 77.71 | kPa | 391.14 | Vapor L... |
| Pvap | 88.17 | kPa | 395.42 | Vapor L... |
| Pvap | 95.08 | kPa | 398.03 | Vapor L... |
| Pvap | 100.40 | kPa | 400.07 | Vapor L... |
| Pvap | 101.30 | kPa | 400.48 | Vapor L... |
| n0 | [1.39470; 1.39710] | [298.15; 298.15] |
|
|
| n0 | 1.39500 | 298.15 | Thermod... | |
| n0 | 1.39520 | 298.15 | Mixing ... | |
| n0 | 1.39680 | 298.15 | A Study... | |
| n0 | 1.39470 | 298.15 | Isobari... | |
| n0 | 1.39710 | 298.15 | Vapor-L... | |
| n0 | 1.39710 | 298.15 | Vapor-L... | |
| ρl | 885.66 | kg/m3 | 298.15 | Densiti... |
| λ | [0.12; 0.14] | W/m×K | [285.55; 362.16] |
|
| λ | 0.14 | W/m×K | 285.55 | Experim... |
| λ | 0.14 | W/m×K | 290.39 | Experim... |
| λ | 0.14 | W/m×K | 295.51 | Experim... |
| λ | 0.14 | W/m×K | 298.99 | Experim... |
| λ | 0.14 | W/m×K | 305.50 | Experim... |
| λ | 0.13 | W/m×K | 312.35 | Experim... |
| λ | 0.13 | W/m×K | 320.42 | Experim... |
| λ | 0.13 | W/m×K | 327.35 | Experim... |
| λ | 0.13 | W/m×K | 333.50 | Experim... |
| λ | 0.12 | W/m×K | 340.41 | Experim... |
| λ | 0.12 | W/m×K | 348.36 | Experim... |
| λ | 0.12 | W/m×K | 355.39 | Experim... |
| λ | 0.12 | W/m×K | 362.16 | Experim... |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 100.00 | 890.18 |
| 293.15 | 1000.00 | 890.39 |
| 293.15 | 3000.00 | 892.23 |
| 293.15 | 5000.00 | 893.59 |
| 293.15 | 10000.00 | 897.77 |
| 293.15 | 15000.00 | 901.59 |
| 293.15 | 20000.00 | 905.28 |
| 293.15 | 25000.00 | 908.91 |
| 293.15 | 30000.00 | 912.4 |
| 293.15 | 35000.00 | 915.63 |
| 293.15 | 40000.00 | 918.78 |
| 293.15 | 50000.00 | 925.12 |
| 293.15 | 60000.00 | 930.63 |
| 303.15 | 100.00 | 879.57 |
| 303.15 | 1000.00 | 880.52 |
| 303.15 | 3000.00 | 882.29 |
| 303.15 | 5000.00 | 884.05 |
| 303.15 | 10000.00 | 888.3 |
| 303.15 | 15000.00 | 892.37 |
| 303.15 | 20000.00 | 896.14 |
| 303.15 | 25000.00 | 899.89 |
| 303.15 | 30000.00 | 903.55 |
| 303.15 | 35000.00 | 906.97 |
| 303.15 | 40000.00 | 910.27 |
| 303.15 | 50000.00 | 916.73 |
| 303.15 | 60000.00 | 922.74 |
| 313.15 | 100.00 | 869.49 |
| 313.15 | 1000.00 | 869.89 |
| 313.15 | 3000.00 | 871.87 |
| 313.15 | 5000.00 | 873.76 |
| 313.15 | 10000.00 | 878.33 |
| 313.15 | 15000.00 | 882.44 |
| 313.15 | 20000.00 | 886.62 |
| 313.15 | 25000.00 | 890.61 |
| 313.15 | 30000.00 | 894.38 |
| 313.15 | 35000.00 | 898.09 |
| 313.15 | 40000.00 | 901.45 |
| 313.15 | 50000.00 | 908.24 |
| 313.15 | 60000.00 | 914.32 |
| 323.15 | 100.00 | 858.83 |
| 323.15 | 1000.00 | 859.81 |
| 323.15 | 3000.00 | 861.81 |
| 323.15 | 5000.00 | 863.85 |
| 323.15 | 10000.00 | 868.67 |
| 323.15 | 15000.00 | 873.18 |
| 323.15 | 20000.00 | 877.67 |
| 323.15 | 25000.00 | 881.64 |
| 323.15 | 30000.00 | 885.65 |
| 323.15 | 35000.00 | 889.44 |
| 323.15 | 40000.00 | 893.13 |
| 323.15 | 50000.00 | 900.12 |
| 323.15 | 60000.00 | 906.77 |
| 333.15 | 100.00 | 848.52 |
| 333.15 | 1000.00 | 849.45 |
| 333.15 | 3000.00 | 851.71 |
| 333.15 | 5000.00 | 853.79 |
| 333.15 | 10000.00 | 858.86 |
| 333.15 | 15000.00 | 863.66 |
| 333.15 | 20000.00 | 868.26 |
| 333.15 | 25000.00 | 872.72 |
| 333.15 | 30000.00 | 876.79 |
| 333.15 | 35000.00 | 880.79 |
| 333.15 | 40000.00 | 884.78 |
| 333.15 | 50000.00 | 892.02 |
| 333.15 | 60000.00 | 898.8 |
| 343.15 | 100.00 | 837.8 |
| 343.15 | 1000.00 | 839.04 |
| 343.15 | 3000.00 | 841.41 |
| 343.15 | 5000.00 | 843.76 |
| 343.15 | 10000.00 | 849.05 |
| 343.15 | 15000.00 | 854.23 |
| 343.15 | 20000.00 | 859.25 |
| 343.15 | 25000.00 | 863.69 |
| 343.15 | 30000.00 | 868.17 |
| 343.15 | 35000.00 | 872.41 |
| 343.15 | 40000.00 | 876.28 |
| 343.15 | 50000.00 | 884.03 |
| 343.15 | 60000.00 | 890.84 |
| 353.15 | 100.00 | 827.35 |
| 353.15 | 1000.00 | 828.43 |
| 353.15 | 3000.00 | 831.13 |
| 353.15 | 5000.00 | 833.48 |
| 353.15 | 10000.00 | 839.27 |
| 353.15 | 15000.00 | 844.84 |
| 353.15 | 20000.00 | 849.86 |
| 353.15 | 25000.00 | 854.79 |
| 353.15 | 30000.00 | 859.45 |
| 353.15 | 35000.00 | 863.9 |
| 353.15 | 40000.00 | 868.0 |
| 353.15 | 50000.00 | 875.94 |
| 353.15 | 60000.00 | 883.37 |
| 363.15 | 100.00 | 816.63 |
| 363.15 | 1000.00 | 817.89 |
| 363.15 | 3000.00 | 820.7 |
| 363.15 | 5000.00 | 823.32 |
| 363.15 | 10000.00 | 829.23 |
| 363.15 | 15000.00 | 835.46 |
| 363.15 | 20000.00 | 840.59 |
| 363.15 | 25000.00 | 845.61 |
| 363.15 | 30000.00 | 850.57 |
| 363.15 | 35000.00 | 855.31 |
| 363.15 | 40000.00 | 859.8 |
| 363.15 | 50000.00 | 868.09 |
| 363.15 | 60000.00 | 875.9 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [297.44; 438.38] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.40423e+01 | |||
| Coefficient B | -3.36903e+03 | |||
| Coefficient C | -5.25030e+01 | |||
| Temperature range, min. | 297.44 | |||
| Temperature range, max. | 438.38 | |||
| Pvap | 1.33 | kPa | 297.44 | Calculated Property |
| Pvap | 3.05 | kPa | 313.10 | Calculated Property |
| Pvap | 6.34 | kPa | 328.76 | Calculated Property |
| Pvap | 12.20 | kPa | 344.42 | Calculated Property |
| Pvap | 21.95 | kPa | 360.08 | Calculated Property |
| Pvap | 37.32 | kPa | 375.74 | Calculated Property |
| Pvap | 60.41 | kPa | 391.40 | Calculated Property |
| Pvap | 93.71 | kPa | 407.06 | Calculated Property |
| Pvap | 140.07 | kPa | 422.72 | Calculated Property |
| Pvap | 202.64 | kPa | 438.38 | Calculated Property |
| Pvap | [6.52; 2812.70] | kPa | [318.15; 575.15] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.06981e+02 | |||
| Coefficient B | -8.88364e+03 | |||
| Coefficient C | -1.35161e+01 | |||
| Coefficient D | 6.94116e-06 | |||
| Temperature range, min. | 318.15 | |||
| Temperature range, max. | 575.15 | |||
| Pvap | 6.52 | kPa | 318.15 | Calculated Property |
| Pvap | 23.20 | kPa | 346.71 | Calculated Property |
| Pvap | 64.54 | kPa | 375.26 | Calculated Property |
| Pvap | 149.08 | kPa | 403.82 | Calculated Property |
| Pvap | 298.76 | kPa | 432.37 | Calculated Property |
| Pvap | 536.55 | kPa | 460.93 | Calculated Property |
| Pvap | 884.91 | kPa | 489.48 | Calculated Property |
| Pvap | 1365.45 | kPa | 518.04 | Calculated Property |
| Pvap | 2000.03 | kPa | 546.59 | Calculated Property |
| Pvap | 2812.70 | kPa | 575.15 | Calculated Property |
Similar Compounds
Find more compounds similar to Methyl valerate.
Mixtures
- Ethane, 1,2-dibromo- + Methyl valerate
- Propane, 1,3-dibromo- + Methyl valerate
- Methyl valerate + Butane, 1,4-dibromo-
- Pentane, 1,5-dibromo- + Methyl valerate
- Hexane, 1,6-dibromo- + Methyl valerate
- Methyl formate + Methyl valerate
- Methyl valerate + Methyl Alcohol
- Methyl formate + Methyl valerate + Methyl Alcohol
- Methyl valerate + Water
- Octane + Methyl valerate
- Methyl valerate + Pentane, 2,2,4-trimethyl-
- Methyl valerate + Acetic acid, methyl ester
- Octane + Methyl valerate + Acetic acid, methyl ester
- Methyl valerate + Pentane, 2,2,4-trimethyl- + Acetic acid, methyl ester
- Methyl valerate + Heptane
- Methyl valerate + 1-Hexanol
- Octane + Methyl valerate + 1-Hexanol
- Acetonitrile + Methyl valerate
- Propanenitrile + Methyl valerate
Sources
- KDB Vapor Pressure Data
- 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
- Thermodynamic study of (alkyl esters + alpha,omega-alkyl dihalides) IV: Hex and Vex for 25 binary mixtures {xC(u-1)H(2u-1)CO2CH3 + (1-x)alpha,omega-BrCH2(CH2)(v-2)CH2Br}, where u = 1 to 5, alpha = 1 and v = omega = 2 to 6
- Mixing thermodynamic properties of ester-containing solutions: A study on the ternary (methyl alkanoate (pentanoate and methanoate) + methanol) and the corresponding binaries. New contributions to the (ester + ester) interactions
- 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
- A Study on Alkane + Ester + Ester Systems. Physicochemical Behavior of Binaries and Ternaries of Octane or Iso-octane with Methyl Esters (Ethanoate, Butanoate, Pentanoate)
- Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
- Isobaric Vapor-Liquid Equilibria and Excess Properties for the Binary Systems of Methyl Esters + Heptane
- 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
- 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
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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