- InChI
- InChI=1S/C7H14O2/c1-3-5-6-7(8)9-4-2/h3-6H2,1-2H3
- InChI Key
- ICMAFTSLXCXHRK-UHFFFAOYSA-N
- Formula
- C7H14O2
- SMILES
- CCCCC(=O)OCC
- Molecular Weight1
- 130.18
- CAS
- 539-82-2
- Other Names
-
- ETHYL ESTER VALERIC ACID
- ETHYL N-VALERATE
- ETHYL PENTANOATE
- Ethyl valerate
- Pentyl propanoate
- Valeric acid, ethyl ester
- n-Valeric acid ethyl ester
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- 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).
- 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).
- Tboil : Boiling point at given 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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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | [-4202.40; -4201.60] | kJ/mol |
|
| ΔcH°liquid | -4201.60 ± 2.50 | kJ/mol | NIST |
| ΔcH°liquid | -4202.40 ± 2.50 | kJ/mol | NIST |
| ΔfG° | -225.86 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-507.70; -507.00] | kJ/mol |
|
| ΔfH°gas | -507.00 ± 2.00 | kJ/mol | NIST |
| ΔfH°gas | -507.70 | kJ/mol | NIST |
| ΔfH°gas | -507.00 ± 3.00 | kJ/mol | NIST |
| ΔfH°liquid | [-554.10; -553.10] | kJ/mol |
|
| ΔfH°liquid | -554.10 ± 0.80 | kJ/mol | NIST |
| ΔfH°liquid | -553.80 ± 2.50 | kJ/mol | NIST |
| ΔfH°liquid | -553.10 ± 8.40 | kJ/mol | NIST |
| ΔfusH° | 16.67 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [46.00; 47.10] | kJ/mol |
|
| ΔvapH° | 47.00 ± 1.00 | kJ/mol | NIST |
| ΔvapH° | 47.10 | kJ/mol | NIST |
| ΔvapH° | 47.01 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 46.00 ± 1.00 | kJ/mol | NIST |
| ΔvapH° | 46.10 | kJ/mol | NIST |
| log10WS | [-2.25; -1.75] |
|
|
| log10WS | -1.75 | Aq. Sol... | |
| log10WS | -2.25 | Estimat... | |
| logPoct/wat | 1.740 | Crippen Calculated Property | |
| McVol | 116.930 | ml/mol | McGowan Calculated Property |
| Pc | 2730.40 | kPa | Develop... |
| Inp | [871.00; 929.00] |
|
|
| Inp | 883.00 | NIST | |
| Inp | 896.00 | NIST | |
| Inp | 913.00 | NIST | |
| Inp | 882.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 879.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 887.00 | NIST | |
| Inp | 887.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 882.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 902.00 | NIST | |
| Inp | 898.00 | NIST | |
| Inp | 902.00 | NIST | |
| Inp | 904.00 | NIST | |
| Inp | Outlier 929.00 | NIST | |
| Inp | 901.00 | NIST | |
| Inp | 898.00 | NIST | |
| Inp | 901.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 893.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 904.00 | NIST | |
| Inp | 907.00 | NIST | |
| Inp | 903.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 898.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 901.00 | NIST | |
| Inp | 893.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 905.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 904.00 | NIST | |
| Inp | 898.00 | NIST | |
| Inp | 915.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 898.00 | NIST | |
| Inp | 905.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 908.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 882.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 898.00 | NIST | |
| Inp | 902.00 | NIST | |
| Inp | Outlier 919.00 | NIST | |
| Inp | 904.00 | NIST | |
| Inp | 901.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 887.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 902.00 | NIST | |
| Inp | 885.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 901.00 | NIST | |
| Inp | 902.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 893.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 904.00 | NIST | |
| Inp | 905.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 898.00 | NIST | |
| Inp | 880.00 | NIST | |
| I | [1113.00; 1170.00] |
|
|
| I | 1125.00 | NIST | |
| I | Outlier 1159.00 | NIST | |
| I | 1113.00 | NIST | |
| I | 1131.00 | NIST | |
| I | Outlier 1162.00 | NIST | |
| I | 1130.00 | NIST | |
| I | 1140.00 | NIST | |
| I | 1142.00 | NIST | |
| I | 1140.00 | NIST | |
| I | 1134.00 | NIST | |
| I | 1139.00 | NIST | |
| I | 1138.00 | NIST | |
| I | 1125.00 | NIST | |
| I | 1146.00 | NIST | |
| I | 1134.00 | NIST | |
| I | 1137.00 | NIST | |
| I | 1127.00 | NIST | |
| I | 1125.00 | NIST | |
| I | 1131.00 | NIST | |
| I | 1124.00 | NIST | |
| I | 1125.00 | NIST | |
| I | 1139.00 | NIST | |
| I | 1139.00 | NIST | |
| I | 1131.00 | NIST | |
| I | Outlier 1160.00 | NIST | |
| I | 1120.00 | NIST | |
| I | 1129.00 | NIST | |
| I | 1138.00 | NIST | |
| I | 1133.00 | NIST | |
| I | 1139.00 | NIST | |
| I | Outlier 1161.00 | NIST | |
| I | 1122.00 | NIST | |
| I | 1133.00 | NIST | |
| I | 1140.00 | NIST | |
| I | 1142.00 | NIST | |
| I | 1136.00 | NIST | |
| I | 1128.00 | NIST | |
| I | 1128.00 | NIST | |
| I | 1133.00 | NIST | |
| I | 1148.00 | NIST | |
| I | 1116.00 | NIST | |
| I | 1145.00 | NIST | |
| I | Outlier 1170.00 | NIST | |
| I | 1135.00 | NIST | |
| I | 1158.00 | NIST | |
| I | 1147.00 | NIST | |
| I | 1141.00 | NIST | |
| I | 1141.00 | NIST | |
| I | 1124.00 | NIST | |
| I | 1138.00 | NIST | |
| I | 1131.00 | NIST | |
| I | 1132.00 | NIST | |
| I | 1127.00 | NIST | |
| I | 1122.00 | NIST | |
| I | 1145.00 | NIST | |
| I | 1118.00 | NIST | |
| I | 1136.00 | NIST | |
| I | 1124.00 | NIST | |
| I | 1140.00 | NIST | |
| I | 1142.00 | NIST | |
| I | 1120.00 | NIST | |
| I | 1127.00 | NIST | |
| I | 1149.00 | NIST | |
| I | 1124.00 | NIST | |
| I | 1127.00 | NIST | |
| I | 1124.00 | NIST | |
| I | 1149.00 | NIST | |
| I | 1134.00 | NIST | |
| I | Outlier 1160.00 | NIST | |
| I | 1138.00 | NIST | |
| I | 1133.00 | NIST | |
| I | 1125.00 | NIST | |
| I | 1130.00 | NIST | |
| Tboil | [407.00; 419.30] | K |
|
| Tboil | 419.20 | K | KDB |
| Tboil | 419.30 | K | Ternary... |
| Tboil | 417.70 | K | NIST |
| Tboil | 417.20 ± 0.40 | K | NIST |
| Tboil | 418.60 ± 0.25 | K | NIST |
| Tboil | 408.15 ± 1.50 | K | NIST |
| Tboil | 417.70 ± 1.00 | K | NIST |
| Tboil | 417.00 ± 5.00 | K | NIST |
| Tboil | 417.90 ± 2.00 | K | NIST |
| Tboil | Outlier 407.00 ± 2.00 | K | NIST |
| Tc | [570.00; 593.30] | K |
|
| Tc | 570.00 | K | KDB |
| Tc | 593.30 ± 1.00 | K | NIST |
| Tc | 570.20 ± 20.00 | K | NIST |
| Tfus | [181.90; 182.05] | K |
|
| Tfus | 181.90 | K | KDB |
| Tfus | 182.05 | K | Aq. Sol... |
| 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] |
|
| 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 |
| η | [0.0002656; 0.0031909] | Pa×s | [240.81; 435.85] |
|
| 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 | 38.00 | kJ/mol | 293.00 | NIST |
| n0 | [1.39800; 1.39810] | [298.15; 298.15] |
|
|
| n0 | 1.39800 | 298.15 | Thermod... | |
| n0 | 1.39810 | 298.15 | Correla... | |
| ρl | [872.36; 877.15] | kg/m3 | [293.20; 298.20] |
|
| ρl | 877.15 | kg/m3 | 293.20 | Modelin... |
| ρl | 872.36 | kg/m3 | 298.20 | Modelin... |
| λ | [0.12; 0.15] | W/m×K | [249.21; 363.57] |
|
| λ | 0.15 | W/m×K | 249.21 | Measure... |
| λ | 0.15 | W/m×K | 263.90 | Measure... |
| λ | 0.14 | W/m×K | 273.50 | Measure... |
| λ | 0.14 | W/m×K | 283.80 | Measure... |
| λ | 0.14 | W/m×K | 288.74 | Measure... |
| λ | 0.14 | W/m×K | 289.42 | Measure... |
| λ | 0.14 | W/m×K | 293.69 | Measure... |
| λ | 0.14 | W/m×K | 298.79 | Measure... |
| λ | 0.13 | W/m×K | 303.69 | Measure... |
| λ | 0.13 | W/m×K | 308.61 | Measure... |
| λ | 0.13 | W/m×K | 313.74 | Measure... |
| λ | 0.13 | W/m×K | 318.49 | Measure... |
| λ | 0.13 | W/m×K | 323.74 | Measure... |
| λ | 0.13 | W/m×K | 328.62 | Measure... |
| λ | 0.13 | W/m×K | 333.51 | Measure... |
| λ | 0.12 | W/m×K | 338.47 | Measure... |
| λ | 0.12 | W/m×K | 343.55 | Measure... |
| λ | 0.12 | W/m×K | 348.55 | Measure... |
| λ | 0.12 | W/m×K | 353.49 | Measure... |
| λ | 0.12 | W/m×K | 358.46 | Measure... |
| λ | 0.12 | W/m×K | 363.57 | Measure... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboil | [345.40; 414.90] | K | [7.10; 91.70] |
|
| Tboil | 345.40 | K | 7.10 | Vapor-l... |
| Tboil | 350.70 | K | 8.90 | Vapor-l... |
| Tboil | 361.10 | K | 13.90 | Vapor-l... |
| Tboil | 374.90 | K | 24.10 | Vapor-l... |
| Tboil | 388.30 | K | 39.10 | Vapor-l... |
| Tboil | 395.70 | K | 52.70 | Vapor-l... |
| Tboil | 403.90 | K | 69.30 | Vapor-l... |
| Tboil | 414.90 | K | 91.70 | Vapor-l... |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 100.00 | 298.15 | 870.7 |
| 100.00 | 303.15 | 865.5 |
| 100.00 | 308.15 | 860.3 |
| 100.00 | 313.15 | 855.0 |
| 100.00 | 318.15 | 849.8 |
| 100.00 | 323.15 | 844.4 |
| 100.00 | 328.15 | 839.1 |
| 100.00 | 333.15 | 833.7 |
| 100.00 | 338.15 | 828.4 |
| 100.00 | 343.15 | 823.0 |
| 100.00 | 348.15 | 817.7 |
| 100.00 | 353.15 | 812.2 |
| 100.00 | 363.15 | 801.2 |
| 100.00 | 373.15 | 790.7 |
| 100.00 | 383.15 | 779.9 |
| 100.00 | 393.15 | 769.0 |
| 1000.00 | 298.15 | 871.5 |
| 1000.00 | 303.15 | 866.4 |
| 1000.00 | 308.15 | 861.2 |
| 1000.00 | 313.15 | 855.9 |
| 1000.00 | 318.15 | 850.6 |
| 1000.00 | 323.15 | 845.3 |
| 1000.00 | 328.15 | 840.0 |
| 1000.00 | 333.15 | 834.7 |
| 1000.00 | 338.15 | 829.5 |
| 1000.00 | 343.15 | 824.1 |
| 1000.00 | 348.15 | 818.7 |
| 1000.00 | 353.15 | 813.3 |
| 1000.00 | 363.15 | 802.5 |
| 1000.00 | 373.15 | 792.0 |
| 1000.00 | 383.15 | 781.3 |
| 1000.00 | 393.15 | 770.5 |
| 2000.00 | 298.15 | 872.4 |
| 2000.00 | 303.15 | 867.4 |
| 2000.00 | 308.15 | 862.1 |
| 2000.00 | 313.15 | 856.9 |
| 2000.00 | 318.15 | 851.7 |
| 2000.00 | 323.15 | 846.4 |
| 2000.00 | 328.15 | 841.1 |
| 2000.00 | 333.15 | 836.0 |
| 2000.00 | 338.15 | 830.7 |
| 2000.00 | 343.15 | 825.3 |
| 2000.00 | 348.15 | 820.0 |
| 2000.00 | 353.15 | 814.6 |
| 2000.00 | 363.15 | 803.9 |
| 2000.00 | 373.15 | 793.5 |
| 2000.00 | 383.15 | 783.0 |
| 2000.00 | 393.15 | 772.3 |
| 2780.00 | 298.15 | 873.0 |
| 2780.00 | 303.15 | 868.1 |
| 2780.00 | 308.15 | 862.9 |
| 2780.00 | 313.15 | 857.7 |
| 2780.00 | 318.15 | 852.4 |
| 2780.00 | 323.15 | 847.2 |
| 2780.00 | 328.15 | 842.0 |
| 2780.00 | 333.15 | 836.9 |
| 2780.00 | 338.15 | 831.5 |
| 2780.00 | 343.15 | 826.2 |
| 2780.00 | 348.15 | 821.0 |
| 2780.00 | 353.15 | 815.6 |
| 2780.00 | 363.15 | 805.0 |
| 2780.00 | 373.15 | 794.7 |
| 2780.00 | 383.15 | 784.2 |
| 2780.00 | 393.15 | 773.6 |
| 3000.00 | 298.15 | 873.2 |
| 3000.00 | 303.15 | 868.3 |
| 3000.00 | 308.15 | 863.1 |
| 3000.00 | 313.15 | 857.9 |
| 3000.00 | 318.15 | 852.7 |
| 3000.00 | 323.15 | 847.4 |
| 3000.00 | 328.15 | 842.3 |
| 3000.00 | 333.15 | 837.1 |
| 3000.00 | 338.15 | 831.8 |
| 3000.00 | 343.15 | 826.5 |
| 3000.00 | 348.15 | 821.3 |
| 3000.00 | 353.15 | 815.9 |
| 3000.00 | 363.15 | 805.5 |
| 3000.00 | 373.15 | 795.0 |
| 3000.00 | 383.15 | 784.5 |
| 3000.00 | 393.15 | 774.1 |
| 5000.00 | 298.15 | 875.1 |
| 5000.00 | 303.15 | 870.1 |
| 5000.00 | 308.15 | 865.0 |
| 5000.00 | 313.15 | 859.9 |
| 5000.00 | 318.15 | 854.6 |
| 5000.00 | 323.15 | 849.4 |
| 5000.00 | 328.15 | 844.4 |
| 5000.00 | 333.15 | 839.3 |
| 5000.00 | 338.15 | 834.0 |
| 5000.00 | 343.15 | 828.8 |
| 5000.00 | 348.15 | 823.7 |
| 5000.00 | 353.15 | 818.4 |
| 5000.00 | 363.15 | 808.1 |
| 5000.00 | 373.15 | 797.9 |
| 5000.00 | 383.15 | 787.6 |
| 5000.00 | 393.15 | 777.4 |
| 10000.00 | 298.15 | 879.4 |
| 10000.00 | 303.15 | 874.5 |
| 10000.00 | 308.15 | 869.5 |
| 10000.00 | 313.15 | 864.5 |
| 10000.00 | 318.15 | 859.4 |
| 10000.00 | 323.15 | 854.3 |
| 10000.00 | 328.15 | 849.4 |
| 10000.00 | 333.15 | 844.5 |
| 10000.00 | 338.15 | 839.4 |
| 10000.00 | 343.15 | 834.4 |
| 10000.00 | 348.15 | 829.4 |
| 10000.00 | 353.15 | 824.3 |
| 10000.00 | 363.15 | 814.6 |
| 10000.00 | 373.15 | 804.8 |
| 10000.00 | 383.15 | 795.0 |
| 10000.00 | 393.15 | 785.1 |
| 15000.00 | 298.15 | 883.4 |
| 15000.00 | 303.15 | 878.7 |
| 15000.00 | 308.15 | 873.8 |
| 15000.00 | 313.15 | 868.9 |
| 15000.00 | 318.15 | 863.9 |
| 15000.00 | 323.15 | 859.0 |
| 15000.00 | 328.15 | 854.2 |
| 15000.00 | 333.15 | 849.5 |
| 15000.00 | 338.15 | 844.5 |
| 15000.00 | 343.15 | 839.6 |
| 15000.00 | 348.15 | 834.8 |
| 15000.00 | 353.15 | 829.9 |
| 15000.00 | 363.15 | 820.5 |
| 15000.00 | 373.15 | 810.9 |
| 15000.00 | 383.15 | 801.5 |
| 15000.00 | 393.15 | 791.6 |
| 20000.00 | 298.15 | 887.3 |
| 20000.00 | 303.15 | 882.6 |
| 20000.00 | 308.15 | 877.8 |
| 20000.00 | 313.15 | 873.0 |
| 20000.00 | 318.15 | 868.2 |
| 20000.00 | 323.15 | 863.4 |
| 20000.00 | 328.15 | 858.7 |
| 20000.00 | 333.15 | 854.1 |
| 20000.00 | 338.15 | 849.3 |
| 20000.00 | 343.15 | 844.5 |
| 20000.00 | 348.15 | 839.9 |
| 20000.00 | 353.15 | 835.1 |
| 20000.00 | 363.15 | 826.0 |
| 20000.00 | 373.15 | 816.7 |
| 20000.00 | 383.15 | 807.6 |
| 20000.00 | 393.15 | 797.7 |
| 25000.00 | 298.15 | 891.0 |
| 25000.00 | 303.15 | 886.5 |
| 25000.00 | 308.15 | 881.8 |
| 25000.00 | 313.15 | 877.0 |
| 25000.00 | 318.15 | 872.3 |
| 25000.00 | 323.15 | 867.6 |
| 25000.00 | 328.15 | 863.0 |
| 25000.00 | 333.15 | 858.6 |
| 25000.00 | 338.15 | 853.9 |
| 25000.00 | 343.15 | 849.2 |
| 25000.00 | 348.15 | 844.7 |
| 25000.00 | 353.15 | 840.0 |
| 25000.00 | 363.15 | 831.2 |
| 25000.00 | 373.15 | 822.2 |
| 25000.00 | 383.15 | 813.4 |
| 25000.00 | 393.15 | 803.5 |
| 30000.00 | 298.15 | 894.6 |
| 30000.00 | 303.15 | 890.2 |
| 30000.00 | 308.15 | 885.6 |
| 30000.00 | 313.15 | 880.9 |
| 30000.00 | 318.15 | 876.3 |
| 30000.00 | 323.15 | 871.7 |
| 30000.00 | 328.15 | 867.1 |
| 30000.00 | 333.15 | 862.9 |
| 30000.00 | 338.15 | 858.2 |
| 30000.00 | 343.15 | 853.7 |
| 30000.00 | 348.15 | 849.3 |
| 30000.00 | 353.15 | 844.7 |
| 30000.00 | 363.15 | 836.0 |
| 30000.00 | 373.15 | 827.3 |
| 30000.00 | 383.15 | 818.9 |
| 30000.00 | 393.15 | 809.0 |
| 35000.00 | 298.15 | 898.1 |
| 35000.00 | 303.15 | 893.8 |
| 35000.00 | 308.15 | 889.2 |
| 35000.00 | 313.15 | 884.6 |
| 35000.00 | 318.15 | 880.1 |
| 35000.00 | 323.15 | 875.5 |
| 35000.00 | 328.15 | 871.1 |
| 35000.00 | 333.15 | 867.0 |
| 35000.00 | 338.15 | 862.4 |
| 35000.00 | 343.15 | 858.0 |
| 35000.00 | 348.15 | 853.6 |
| 35000.00 | 353.15 | 849.1 |
| 35000.00 | 363.15 | 840.8 |
| 35000.00 | 373.15 | 832.3 |
| 35000.00 | 383.15 | 824.0 |
| 35000.00 | 393.15 | 814.0 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [312.40; 439.62] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.53691e+01 | |||
| Coefficient B | -3.84124e+03 | |||
| Coefficient C | -5.77010e+01 | |||
| Temperature range, min. | 312.40 | |||
| Temperature range, max. | 439.62 | |||
| Pvap | 1.33 | kPa | 312.40 | Calculated Property |
| Pvap | 2.95 | kPa | 326.54 | Calculated Property |
| Pvap | 6.02 | kPa | 340.67 | Calculated Property |
| Pvap | 11.48 | kPa | 354.81 | Calculated Property |
| Pvap | 20.64 | kPa | 368.94 | Calculated Property |
| Pvap | 35.29 | kPa | 383.08 | Calculated Property |
| Pvap | 57.69 | kPa | 397.21 | Calculated Property |
| Pvap | 90.68 | kPa | 411.35 | Calculated Property |
| Pvap | 137.66 | kPa | 425.48 | Calculated Property |
| Pvap | 202.63 | kPa | 439.62 | Calculated Property |
| Pvap | [4.54; 179.54] | kPa | [328.15; 430.15] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 4.34447e+02 | |||
| Coefficient B | -2.34143e+04 | |||
| Coefficient C | -6.33502e+01 | |||
| Coefficient D | 5.04777e-05 | |||
| Temperature range, min. | 328.15 | |||
| Temperature range, max. | 430.15 | |||
| Pvap | 4.54 | kPa | 328.15 | Calculated Property |
| Pvap | 8.38 | kPa | 339.48 | Calculated Property |
| Pvap | 14.42 | kPa | 350.82 | Calculated Property |
| Pvap | 23.36 | kPa | 362.15 | Calculated Property |
| Pvap | 35.94 | kPa | 373.48 | Calculated Property |
| Pvap | 52.89 | kPa | 384.82 | Calculated Property |
| Pvap | 74.95 | kPa | 396.15 | Calculated Property |
| Pvap | 102.88 | kPa | 407.48 | Calculated Property |
| Pvap | 137.45 | kPa | 418.82 | Calculated Property |
| Pvap | 179.54 | kPa | 430.15 | Calculated Property |
Similar Compounds
Find more compounds similar to Pentanoic acid, ethyl ester.
Mixtures
- Pentanoic acid, ethyl ester + Butanoic acid + Water
- Pentanoic acid, ethyl ester + Formic acid + Water
- Pentanoic acid, ethyl ester + Ethanol
- Pentanoic acid, ethyl ester + Ethane, 1,2-dichloro-
- Pentanoic acid, ethyl ester + Propane, 1,3-dichloro-
- Pentanoic acid, ethyl ester + Butane, 1,4-dichloro-
- Pentanoic acid, ethyl ester + Pentane, 1,5-dichloro-
- Pentanoic acid, ethyl ester + Hexane, 1,6-dichloro-
- Pentanoic acid, ethyl ester + Ethane, 1,2-dibromo-
- Pentanoic acid, ethyl ester + Propane, 1,3-dibromo-
- Pentanoic acid, ethyl ester + Butane, 1,4-dibromo-
- Pentanoic acid, ethyl ester + Pentane, 1,5-dibromo-
- Pentanoic acid, ethyl ester + Hexane, 1,6-dibromo-
- Pentanoic acid, ethyl ester + Dodecane
- Pentanoic acid, ethyl ester + Ethyl Acetate
- Pentanoic acid, ethyl ester + Dodecane + Ethyl Acetate
- Pentanoic acid, ethyl ester + Carbon dioxide
- Pentanoic acid, ethyl ester + Carbon dioxide + Ethanol
- Pentanoic acid, ethyl ester + Ethanol + Water
- Pentanoic acid, ethyl ester + Pentanoic acid + Water
Find more mixtures with Pentanoic acid, ethyl ester.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Ternary phase diagrams for aqueous mixtures of butyric acid with several solvents: experimental and correlated data
- Modeling extraction equilibria of butyric acid distributed between water and tri-n-butyl amine/diluent or tri-n-butyl phosphate/diluent system: Extension of the LSER approach
- Modeling phase equilibria of ternary systems (water + formic acid + ester or alcohol) through UNIFAC-original, SERLAS, NRTL, NRTL-modified, and three-suffix Margules: Parameter estimation using genetic algorithm
- Vapor-liquid and liquid-liquid equilibrium modeling of systems involving ethanol, water, and ethyl valerate (valeric acid) using the PC-SAFT equation of state
- Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) I: HE and V E for 25 binary mixtures {xCu-1H2u-1CO2C2H5 + (1-x)a,x-ClCH2(CH2)v-2CH2Cl}, where u = 1 to 5, a = 1 and v = x = 2 to 6
- Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) II: HE m and V E m for 25 binary mixtures {xCu-1H2u-1CO2C2H5 + (1 - x)a,x-BrCH2(CH2)v-2CH2Br}, where u = 1 to 5, a = 1 and v = x = 2 to 6
- Correlation and prediction of mixing thermodynamic properties of ester-containing systems: Ester + alkane and ester + ester binary systems and the ternary dodecane + ethyl pentanoate + ethyl ethanoate
- Liquid-liquid equilibrium of ternary systems comprising ethyl valerate(1), water(2), ethanol(3) and valeric acid(4)
- Phase equilibrium measurements and thermodynamic modelling for the systems involving valeric acid, ethanol, ethyl valerate and water plus CO2
- Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
- Development of a Predictive Equation of State for CO2 + Ethyl Ester Mixtures Based on Critical Points Measurements
- PVT Property Measurements for Ethyl Propionate, Ethyl Butyrate, and Ethyl Pentanoate Esters from (298 to 393) K and up to 35 MPa
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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