- InChI
- InChI=1S/C6H12O2/c1-3-5-6(7)8-4-2/h3-5H2,1-2H3
- InChI Key
- OBNCKNCVKJNDBV-UHFFFAOYSA-N
- Formula
- C6H12O2
- SMILES
- CCCC(=O)OCC
- Molecular Weight1
- 116.16
- CAS
- 105-54-4
- Other Names
-
- BUTYRIC ESTER
- Butyric acid, ethyl ester
- ETHYL BUTANOATE
- ETHYL BUTYRATE
- ETHYL N-BUTYRATE
- Ethyl ester of butanoic acid
- Ethyl n-butanoate
- NSC 8857
- UN 1180
- ethyl 1-butyrate
- ethyl butanoate (ethyl butyrate)
- n-Butyric acid ethyl ester
- ω : Acentric Factor.
- 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).
- μ : Dipole Moment (debye).
- 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).
- NFPA Fire : NFPA Fire Rating.
- 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).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.4610 | KDB | |
| ΔcH°liquid | [-3545.00; -3539.00] | kJ/mol |
|
| ΔcH°liquid | -3545.00 | kJ/mol | NIST |
| ΔcH°liquid | -3539.00 | kJ/mol | NIST |
| μ | 1.80 | debye | KDB |
| ΔfG° | -234.28 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -485.00 ± 1.00 | kJ/mol | NIST |
| ΔfH°liquid | -528.40 ± 0.79 | kJ/mol | NIST |
| ΔfusH° | 14.08 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [36.90; 44.00] | kJ/mol |
|
| ΔvapH° | 42.71 | kJ/mol | NIST |
| ΔvapH° | 44.00 ± 1.00 | kJ/mol | NIST |
| ΔvapH° | 43.40 | kJ/mol | NIST |
| ΔvapH° | 43.70 ± 1.30 | kJ/mol | NIST |
| ΔvapH° | 42.68 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 42.00 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 42.00 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | Outlier 36.90 ± 0.04 | kJ/mol | NIST |
| log10WS | -1.28 | Aq. Sol... | |
| logPoct/wat | 1.350 | Crippen Calculated Property | |
| McVol | 102.840 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| Pc | [3060.00; 3064.00] | kPa |
|
| Pc | 3060.00 | kPa | KDB |
| Pc | 3064.00 ± 151.99 | kPa | NIST |
| ρc | 276.46 ± 9.99 | kg/m3 | NIST |
| Inp | [760.00; 818.00] |
|
|
| Inp | 784.00 | NIST | |
| Inp | 780.20 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 783.00 | NIST | |
| Inp | 792.00 | NIST | |
| Inp | 796.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 782.00 | NIST | |
| Inp | 781.00 | NIST | |
| Inp | Outlier 760.00 | NIST | |
| Inp | 782.00 | NIST | |
| Inp | 778.00 | NIST | |
| Inp | 782.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 784.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 775.00 | NIST | |
| Inp | 785.00 | NIST | |
| Inp | 793.00 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 791.00 | NIST | |
| Inp | 792.00 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 790.00 | NIST | |
| Inp | 793.00 | NIST | |
| Inp | 790.00 | NIST | |
| Inp | Outlier 764.00 | NIST | |
| Inp | 799.00 | NIST | |
| Inp | 798.00 | NIST | |
| Inp | Outlier 764.00 | NIST | |
| Inp | 790.00 | NIST | |
| Inp | 791.00 | NIST | |
| Inp | 778.00 | NIST | |
| Inp | 779.00 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 801.00 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 778.00 | NIST | |
| Inp | 776.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 798.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 808.00 | NIST | |
| Inp | 808.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 805.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 794.00 | NIST | |
| Inp | 805.00 | NIST | |
| Inp | 801.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 797.00 | NIST | |
| Inp | 781.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 781.00 | NIST | |
| Inp | 781.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 805.00 | NIST | |
| Inp | 785.00 | NIST | |
| Inp | 781.00 | NIST | |
| Inp | 781.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 802.20 | NIST | |
| Inp | 790.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 774.00 | NIST | |
| Inp | 791.00 | NIST | |
| Inp | 782.00 | NIST | |
| Inp | 779.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 785.00 | NIST | |
| Inp | 787.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 778.00 | NIST | |
| Inp | 778.00 | NIST | |
| Inp | 778.00 | NIST | |
| Inp | 778.00 | NIST | |
| Inp | Outlier 818.00 | NIST | |
| Inp | 801.00 | NIST | |
| Inp | 805.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 807.00 | NIST | |
| Inp | 798.00 | NIST | |
| Inp | 770.00 | NIST | |
| Inp | 798.00 | NIST | |
| Inp | 805.00 | NIST | |
| Inp | 805.00 | NIST | |
| Inp | 805.00 | NIST | |
| Inp | 801.00 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 798.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 801.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 792.00 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 784.00 | NIST | |
| Inp | 801.00 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 774.00 | NIST | |
| Inp | 807.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 783.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 778.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 798.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 797.00 | NIST | |
| Inp | 799.00 | NIST | |
| Inp | 783.00 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 780.00 | NIST | |
| Inp | 812.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 780.00 | NIST | |
| Inp | 785.00 | NIST | |
| Inp | 790.00 | NIST | |
| Inp | 799.00 | NIST | |
| Inp | 784.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 799.00 | NIST | |
| Inp | 782.00 | NIST | |
| Inp | 791.00 | NIST | |
| Inp | 780.00 | NIST | |
| Inp | 784.00 | NIST | |
| Inp | 785.00 | NIST | |
| Inp | 781.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 785.00 | NIST | |
| Inp | 785.00 | NIST | |
| Inp | 782.00 | NIST | |
| Inp | 794.00 | NIST | |
| Inp | 796.00 | NIST | |
| Inp | 787.00 | NIST | |
| Inp | 774.00 | NIST | |
| Inp | 770.00 | NIST | |
| Inp | 807.00 | NIST | |
| Inp | 801.00 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 798.00 | NIST | |
| Inp | 801.00 | NIST | |
| Inp | 770.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 770.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 796.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 778.00 | NIST | |
| Inp | 799.00 | NIST | |
| Inp | 778.00 | NIST | |
| Inp | 770.00 | NIST | |
| Inp | 770.00 | NIST | |
| Inp | 774.00 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 774.00 | NIST | |
| Inp | 774.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 792.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 787.00 | NIST | |
| Inp | 787.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 798.00 | NIST | |
| Inp | 784.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 771.00 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 771.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 774.00 | NIST | |
| Inp | 771.00 | NIST | |
| Inp | 781.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 785.00 | NIST | |
| Inp | 774.00 | NIST | |
| Inp | 793.00 | NIST | |
| Inp | 796.00 | NIST | |
| Inp | 784.00 | NIST | |
| Inp | 784.00 | NIST | |
| Inp | 780.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 801.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 805.00 | NIST | |
| Inp | 780.00 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 780.00 | NIST | |
| Inp | 783.00 | NIST | |
| Inp | 784.00 | NIST | |
| Inp | 784.00 | NIST | |
| Inp | 787.00 | NIST | |
| Inp | 774.00 | NIST | |
| Inp | 798.00 | NIST | |
| Inp | 770.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 778.00 | NIST | |
| Inp | 792.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 785.00 | NIST | |
| Inp | 784.00 | NIST | |
| Inp | 801.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 787.00 | NIST | |
| Inp | 799.00 | NIST | |
| Inp | 796.00 | NIST | |
| Inp | 782.00 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | Outlier 764.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 805.00 | NIST | |
| I | [990.00; 1081.00] |
|
|
| I | 1025.00 | NIST | |
| I | 1051.00 | NIST | |
| I | 1054.00 | NIST | |
| I | Outlier 1008.00 | NIST | |
| I | 1032.00 | NIST | |
| I | 1045.00 | NIST | |
| I | 1032.00 | NIST | |
| I | 1058.00 | NIST | |
| I | 1057.00 | NIST | |
| I | 1010.00 | NIST | |
| I | 1044.00 | NIST | |
| I | 1044.00 | NIST | |
| I | 1040.00 | NIST | |
| I | 1026.00 | NIST | |
| I | 1042.00 | NIST | |
| I | 1043.00 | NIST | |
| I | 1045.00 | NIST | |
| I | Outlier 1005.00 | NIST | |
| I | 1028.00 | NIST | |
| I | 1036.00 | NIST | |
| I | 1048.00 | NIST | |
| I | 1035.00 | NIST | |
| I | 1035.00 | NIST | |
| I | 1041.00 | NIST | |
| I | 1049.00 | NIST | |
| I | 1061.00 | NIST | |
| I | 1041.00 | NIST | |
| I | 1033.00 | NIST | |
| I | 1039.00 | NIST | |
| I | 1027.00 | NIST | |
| I | 1052.00 | NIST | |
| I | 1048.00 | NIST | |
| I | 1048.00 | NIST | |
| I | Outlier 1067.00 | NIST | |
| I | Outlier 1073.00 | NIST | |
| I | Outlier 1069.00 | NIST | |
| I | Outlier 1000.00 | NIST | |
| I | 1037.00 | NIST | |
| I | 1029.00 | NIST | |
| I | 1052.00 | NIST | |
| I | 1022.00 | NIST | |
| I | 1022.00 | NIST | |
| I | Outlier 1001.00 | NIST | |
| I | 1023.00 | NIST | |
| I | 1041.00 | NIST | |
| I | 1023.00 | NIST | |
| I | 1030.00 | NIST | |
| I | 1021.00 | NIST | |
| I | 1036.00 | NIST | |
| I | 1037.00 | NIST | |
| I | 1021.00 | NIST | |
| I | 1041.00 | NIST | |
| I | 1057.00 | NIST | |
| I | 1025.00 | NIST | |
| I | 1020.00 | NIST | |
| I | 1024.00 | NIST | |
| I | 1025.00 | NIST | |
| I | 1040.40 | NIST | |
| I | 1039.00 | NIST | |
| I | 1039.00 | NIST | |
| I | 1021.00 | NIST | |
| I | 1023.00 | NIST | |
| I | 1044.00 | NIST | |
| I | 1037.00 | NIST | |
| I | 1040.00 | NIST | |
| I | 1032.00 | NIST | |
| I | 1025.00 | NIST | |
| I | 1031.00 | NIST | |
| I | 1057.00 | NIST | |
| I | 1025.00 | NIST | |
| I | 1032.00 | NIST | |
| I | 1040.00 | NIST | |
| I | 1040.00 | NIST | |
| I | 1046.00 | NIST | |
| I | 1040.00 | NIST | |
| I | 1055.00 | NIST | |
| I | 1034.00 | NIST | |
| I | 1034.00 | NIST | |
| I | 1032.00 | NIST | |
| I | 1044.00 | NIST | |
| I | 1028.00 | NIST | |
| I | 1028.00 | NIST | |
| I | 1056.00 | NIST | |
| I | 1021.00 | NIST | |
| I | 1034.00 | NIST | |
| I | 1042.00 | NIST | |
| I | 1056.00 | NIST | |
| I | 1022.00 | NIST | |
| I | 1047.00 | NIST | |
| I | 1037.00 | NIST | |
| I | 1038.00 | NIST | |
| I | 1041.00 | NIST | |
| I | 1041.00 | NIST | |
| I | 1025.00 | NIST | |
| I | 1043.00 | NIST | |
| I | 1044.00 | NIST | |
| I | 1041.00 | NIST | |
| I | 1037.00 | NIST | |
| I | 1035.00 | NIST | |
| I | 1028.00 | NIST | |
| I | 1048.00 | NIST | |
| I | 1038.00 | NIST | |
| I | 1021.00 | NIST | |
| I | 1033.00 | NIST | |
| I | 1038.00 | NIST | |
| I | 1026.00 | NIST | |
| I | 1040.00 | NIST | |
| I | 1032.00 | NIST | |
| I | 1028.00 | NIST | |
| I | 1029.00 | NIST | |
| I | 1037.00 | NIST | |
| I | 1014.00 | NIST | |
| I | 1042.00 | NIST | |
| I | 1042.00 | NIST | |
| I | 1036.00 | NIST | |
| I | 1054.00 | NIST | |
| I | 1015.00 | NIST | |
| I | 1035.00 | NIST | |
| I | 1046.00 | NIST | |
| I | 1031.00 | NIST | |
| I | 1031.00 | NIST | |
| I | 1038.00 | NIST | |
| I | 1050.00 | NIST | |
| I | 1013.00 | NIST | |
| I | Outlier 1066.00 | NIST | |
| I | 1030.00 | NIST | |
| I | 1025.00 | NIST | |
| I | 1047.00 | NIST | |
| I | 1035.00 | NIST | |
| I | 1057.00 | NIST | |
| I | 1028.00 | NIST | |
| I | 1044.00 | NIST | |
| I | 1038.00 | NIST | |
| I | 1032.00 | NIST | |
| I | 1050.00 | NIST | |
| I | 1036.00 | NIST | |
| I | 1022.00 | NIST | |
| I | 1036.00 | NIST | |
| I | 1040.00 | NIST | |
| I | 1036.00 | NIST | |
| I | 1031.00 | NIST | |
| I | 1025.00 | NIST | |
| I | 1043.00 | NIST | |
| I | 1048.00 | NIST | |
| I | 1030.00 | NIST | |
| I | 1023.00 | NIST | |
| I | 1025.00 | NIST | |
| I | 1031.00 | NIST | |
| I | 1035.00 | NIST | |
| I | 1043.00 | NIST | |
| I | 1033.00 | NIST | |
| I | 1025.00 | NIST | |
| I | 1043.00 | NIST | |
| I | 1033.00 | NIST | |
| I | 1052.00 | NIST | |
| I | 1043.00 | NIST | |
| I | 1043.00 | NIST | |
| I | 1029.00 | NIST | |
| I | 1009.00 | NIST | |
| I | 1025.00 | NIST | |
| I | 1010.00 | NIST | |
| I | 1018.00 | NIST | |
| I | 1025.00 | NIST | |
| I | 1030.90 | NIST | |
| I | 1025.00 | NIST | |
| I | 1060.00 | NIST | |
| I | 1028.00 | NIST | |
| I | 1035.00 | NIST | |
| I | 1035.00 | NIST | |
| I | 1035.00 | NIST | |
| I | 1037.00 | NIST | |
| I | 1035.00 | NIST | |
| I | 1037.00 | NIST | |
| I | 1035.00 | NIST | |
| I | 1037.00 | NIST | |
| I | 1035.00 | NIST | |
| I | 1037.00 | NIST | |
| I | 1028.00 | NIST | |
| I | 1030.00 | NIST | |
| I | 1039.00 | NIST | |
| I | 1036.00 | NIST | |
| I | Outlier 1075.00 | NIST | |
| I | 1060.00 | NIST | |
| I | 1032.00 | NIST | |
| I | 1039.00 | NIST | |
| I | 1033.00 | NIST | |
| I | 1033.00 | NIST | |
| I | Outlier 1002.00 | NIST | |
| I | 1023.00 | NIST | |
| I | 1023.00 | NIST | |
| I | 1050.00 | NIST | |
| I | 1026.00 | NIST | |
| I | Outlier 1076.00 | NIST | |
| I | Outlier 1078.00 | NIST | |
| I | Outlier 1079.00 | NIST | |
| I | 1035.00 | NIST | |
| I | 1040.00 | NIST | |
| I | 1046.00 | NIST | |
| I | 1031.00 | NIST | |
| I | 1022.00 | NIST | |
| I | 1043.00 | NIST | |
| I | 1026.00 | NIST | |
| I | 1043.00 | NIST | |
| I | 1029.00 | NIST | |
| I | 1022.00 | NIST | |
| I | 1037.00 | NIST | |
| I | 1037.00 | NIST | |
| I | 1044.00 | NIST | |
| I | 1028.00 | NIST | |
| I | Outlier 990.00 | NIST | |
| I | Outlier 1081.00 | NIST | |
| I | 1043.00 | NIST | |
| I | 1030.00 | NIST | |
| I | 1040.00 | NIST | |
| I | 1028.00 | NIST | |
| I | 1045.00 | NIST | |
| I | 1037.00 | NIST | |
| I | 1042.00 | NIST | |
| I | 1028.00 | NIST | |
| I | 1043.00 | NIST | |
| I | 1032.00 | NIST | |
| I | 1046.00 | NIST | |
| I | 1024.00 | NIST | |
| I | 1043.00 | NIST | |
| I | 1042.00 | NIST | |
| I | 1033.00 | NIST | |
| I | 1022.00 | NIST | |
| I | Outlier 1071.00 | NIST | |
| I | 1056.00 | NIST | |
| I | 1028.00 | NIST | |
| I | 1025.00 | NIST | |
| I | 1047.00 | NIST | |
| I | 1025.00 | NIST | |
| I | 1031.00 | NIST | |
| I | 1047.00 | NIST | |
| I | 1047.00 | NIST | |
| I | 1023.00 | NIST | |
| I | 1044.00 | NIST | |
| I | 1023.00 | NIST | |
| I | 1023.00 | NIST | |
| I | 1046.00 | NIST | |
| I | 1028.00 | NIST | |
| I | 1025.00 | NIST | |
| I | 1028.00 | NIST | |
| I | 1041.00 | NIST | |
| I | 1039.00 | NIST | |
| I | Outlier 1067.00 | NIST | |
| I | 1029.00 | NIST | |
| I | 1023.00 | NIST | |
| I | 1036.00 | NIST | |
| I | 1025.00 | NIST | |
| I | 1037.00 | NIST | |
| I | 1057.00 | NIST | |
| Tboil | [387.95; 394.90] | K |
|
| Tboil | 394.60 | K | KDB |
| Tboil | 394.55 | K | Ternary... |
| Tboil | 393.78 | K | Vapor L... |
| Tboil | 394.17 | K | Isobari... |
| Tboil | 394.13 | K | Solvent... |
| Tboil | 394.18 ± 0.40 | K | NIST |
| Tboil | 393.20 | K | NIST |
| Tboil | 393.00 | K | NIST |
| Tboil | 394.60 | K | NIST |
| Tboil | 393.95 ± 0.50 | K | NIST |
| Tboil | 392.15 ± 1.00 | K | NIST |
| Tboil | Outlier 388.65 ± 5.00 | K | NIST |
| Tboil | 393.15 ± 1.00 | K | NIST |
| Tboil | 394.55 ± 1.00 | K | NIST |
| Tboil | 393.15 ± 1.00 | K | NIST |
| Tboil | 393.00 ± 1.00 | K | NIST |
| Tboil | 394.70 ± 0.50 | K | NIST |
| Tboil | 394.15 ± 1.00 | K | NIST |
| Tboil | 394.50 ± 2.00 | K | NIST |
| Tboil | 393.10 ± 1.00 | K | NIST |
| Tboil | 394.70 ± 0.50 | K | NIST |
| Tboil | 394.35 ± 0.40 | K | NIST |
| Tboil | 393.40 ± 0.50 | K | NIST |
| Tboil | 393.30 ± 0.50 | K | NIST |
| Tboil | 393.20 ± 0.50 | K | NIST |
| Tboil | 393.35 ± 0.50 | K | NIST |
| Tboil | 393.45 ± 1.00 | K | NIST |
| Tboil | 391.65 ± 1.00 | K | NIST |
| Tboil | 392.15 ± 2.00 | K | NIST |
| Tboil | 394.90 ± 0.30 | K | NIST |
| Tboil | 393.15 ± 1.00 | K | NIST |
| Tboil | 393.40 ± 1.00 | K | NIST |
| Tboil | 394.65 ± 1.00 | K | NIST |
| Tboil | 394.40 ± 1.50 | K | NIST |
| Tboil | 391.90 ± 1.00 | K | NIST |
| Tboil | 393.15 ± 1.00 | K | NIST |
| Tboil | 392.15 ± 1.00 | K | NIST |
| Tboil | 393.75 ± 1.00 | K | NIST |
| Tboil | 393.80 ± 0.50 | K | NIST |
| Tboil | 394.10 ± 1.50 | K | NIST |
| Tboil | 394.40 ± 1.00 | K | NIST |
| Tboil | 394.25 ± 1.00 | K | NIST |
| Tboil | 392.15 ± 1.00 | K | NIST |
| Tboil | Outlier 387.95 ± 1.00 | K | NIST |
| Tboil | Outlier 387.95 ± 1.00 | K | NIST |
| Tc | [558.70; 577.50] | K |
|
| Tc | 566.00 | K | KDB |
| Tc | 569.98 | K | Develop... |
| Tc | 568.80 ± 0.60 | K | NIST |
| Tc | 558.70 ± 10.00 | K | NIST |
| Tc | 566.00 ± 2.00 | K | NIST |
| Tc | 577.50 ± 6.00 | K | NIST |
| Tfus | [170.65; 178.90] | K |
|
| Tfus | 175.00 | K | KDB |
| Tfus | 178.90 | K | Aq. Sol... |
| Tfus | 175.30 ± 0.30 | K | NIST |
| Tfus | 170.65 ± 0.70 | K | NIST |
| Vc | 0.421 | m3/kmol | KDB |
| Zc | 0.2737480 | KDB |
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 | [220.10; 229.70] | J/mol×K | [290.00; 298.15] |
|
| Cp,liquid | 229.70 | J/mol×K | 290.00 | NIST |
| Cp,liquid | 220.10 | J/mol×K | 297.20 | NIST |
| Cp,liquid | 220.10 | J/mol×K | 297.20 | NIST |
| Cp,liquid | 228.00 | J/mol×K | 298.15 | NIST |
| η | [0.0003820; 0.0006620] | Pa×s | [293.15; 343.15] |
|
| η | 0.0006620 | Pa×s | 293.15 | Density... |
| η | 0.0006200 | Pa×s | 298.15 | Density... |
| η | 0.0005830 | Pa×s | 303.15 | Density... |
| η | 0.0005490 | Pa×s | 308.15 | Density... |
| η | 0.0005190 | Pa×s | 313.15 | Density... |
| η | 0.0004910 | Pa×s | 318.15 | Density... |
| η | 0.0004650 | Pa×s | 323.15 | Density... |
| η | 0.0004420 | Pa×s | 328.15 | Density... |
| η | 0.0004200 | Pa×s | 333.15 | Density... |
| η | 0.0004000 | Pa×s | 338.15 | Density... |
| η | 0.0003820 | Pa×s | 343.15 | Density... |
| ΔvapH | [35.47; 48.30] | kJ/mol | [323.00; 394.60] |
|
| ΔvapH | 42.10 ± 0.10 | kJ/mol | 323.00 | NIST |
| ΔvapH | 41.80 | kJ/mol | 324.00 | NIST |
| ΔvapH | 48.30 | kJ/mol | 333.50 | NIST |
| ΔvapH | 40.20 | kJ/mol | 362.50 | NIST |
| ΔvapH | 39.40 | kJ/mol | 382.50 | NIST |
| ΔvapH | 35.47 | kJ/mol | 394.60 | NIST |
| Pvap | [22.50; 101.31] | kPa | [348.97; 394.13] |
|
| Pvap | 22.50 | kPa | 348.97 | Solvent... |
| Pvap | 25.00 | kPa | 351.83 | Solvent... |
| Pvap | 27.50 | kPa | 354.39 | Solvent... |
| Pvap | 30.03 | kPa | 356.76 | Solvent... |
| Pvap | 32.51 | kPa | 359.00 | Solvent... |
| Pvap | 35.02 | kPa | 361.08 | Solvent... |
| Pvap | 35.41 | kPa | 361.56 | Vapor L... |
| Pvap | 37.52 | kPa | 363.04 | Solvent... |
| Pvap | 40.04 | kPa | 364.86 | Solvent... |
| Pvap | 40.41 | kPa | 365.24 | Vapor L... |
| Pvap | 42.51 | kPa | 366.66 | Solvent... |
| Pvap | 45.03 | kPa | 368.24 | Solvent... |
| Pvap | 47.51 | kPa | 369.87 | Solvent... |
| Pvap | 50.00 | kPa | 371.33 | Vapor L... |
| Pvap | 50.01 | kPa | 371.44 | Solvent... |
| Pvap | 52.51 | kPa | 372.86 | Solvent... |
| Pvap | 54.40 | kPa | 373.83 | Vapor L... |
| Pvap | 55.03 | kPa | 374.31 | Solvent... |
| Pvap | 57.52 | kPa | 375.67 | Solvent... |
| Pvap | 58.98 | kPa | 376.28 | Vapor L... |
| Pvap | 60.00 | kPa | 376.95 | Solvent... |
| Pvap | 60.00 | kPa | 377.21 | Vapor L... |
| Pvap | 60.00 | kPa | 377.23 | Vapor L... |
| Pvap | 65.03 | kPa | 379.48 | Solvent... |
| Pvap | 65.75 | kPa | 379.65 | Vapor L... |
| Pvap | 67.53 | kPa | 380.68 | Solvent... |
| Pvap | 70.00 | kPa | 381.82 | Solvent... |
| Pvap | 72.52 | kPa | 382.96 | Solvent... |
| Pvap | 75.01 | kPa | 384.07 | Solvent... |
| Pvap | 77.20 | kPa | 384.82 | Vapor L... |
| Pvap | 77.51 | kPa | 385.13 | Solvent... |
| Pvap | 79.99 | kPa | 386.19 | Solvent... |
| Pvap | 82.52 | kPa | 387.22 | Solvent... |
| Pvap | 84.14 | kPa | 387.65 | Vapor L... |
| Pvap | 85.02 | kPa | 388.21 | Solvent... |
| Pvap | 87.54 | kPa | 389.17 | Solvent... |
| Pvap | 89.98 | kPa | 390.12 | Solvent... |
| Pvap | 90.84 | kPa | 390.23 | Vapor L... |
| Pvap | 92.53 | kPa | 391.06 | Solvent... |
| Pvap | 94.92 | kPa | 391.95 | Solvent... |
| Pvap | 97.45 | kPa | 392.83 | Solvent... |
| Pvap | 100.40 | kPa | 393.63 | Vapor L... |
| Pvap | 100.01 | kPa | 393.71 | Solvent... |
| Pvap | 101.30 | kPa | 393.78 | Vapor L... |
| Pvap | 101.31 | kPa | 394.13 | Solvent... |
| n0 | [1.38950; 1.38990] | [293.15; 298.15] |
|
|
| n0 | 1.38990 | 293.15 | Vapor l... | |
| n0 | 1.38950 | 298.15 | Thermod... | |
| n0 | 1.38980 | 298.15 | Measure... | |
| ρl | [847.00; 884.16] | kg/m3 | [288.15; 323.15] |
|
| ρl | 884.16 | kg/m3 | 288.15 | Volumet... |
| ρl | 879.00 | kg/m3 | 293.00 | KDB |
| ρl | 878.90 | kg/m3 | 293.15 | Volumet... |
| ρl | 879.18 | kg/m3 | 293.20 | Modelin... |
| ρl | 874.31 | kg/m3 | 298.15 | Acousti... |
| ρl | 873.62 | kg/m3 | 298.15 | Volumet... |
| ρl | 868.85 | kg/m3 | 303.15 | Acousti... |
| ρl | 868.33 | kg/m3 | 303.15 | Volumet... |
| ρl | 868.21 | kg/m3 | 303.15 | Densiti... |
| ρl | 863.40 | kg/m3 | 308.15 | Acousti... |
| ρl | 863.02 | kg/m3 | 308.15 | Volumet... |
| ρl | 857.94 | kg/m3 | 313.15 | Acousti... |
| ρl | 857.70 | kg/m3 | 313.15 | Volumet... |
| ρl | 852.36 | kg/m3 | 318.15 | Volumet... |
| ρl | 852.49 | kg/m3 | 318.15 | Acousti... |
| ρl | 847.03 | kg/m3 | 323.15 | Acousti... |
| ρl | 847.00 | kg/m3 | 323.15 | Volumet... |
| λ | [0.12; 0.15] | W/m×K | [268.57; 363.52] |
|
| λ | 0.15 | W/m×K | 268.57 | Measure... |
| λ | 0.14 | W/m×K | 273.61 | Measure... |
| λ | 0.14 | W/m×K | 278.63 | Measure... |
| λ | 0.14 | W/m×K | 283.58 | Measure... |
| λ | 0.14 | W/m×K | 288.65 | Measure... |
| λ | 0.14 | W/m×K | 293.58 | Measure... |
| λ | 0.14 | W/m×K | 298.53 | Measure... |
| λ | 0.13 | W/m×K | 303.56 | Measure... |
| λ | 0.13 | W/m×K | 308.67 | Measure... |
| λ | 0.13 | W/m×K | 313.49 | Measure... |
| λ | 0.13 | W/m×K | 318.61 | Measure... |
| λ | 0.13 | W/m×K | 323.42 | Measure... |
| λ | 0.13 | W/m×K | 328.48 | Measure... |
| λ | 0.12 | W/m×K | 333.46 | Measure... |
| λ | 0.12 | W/m×K | 338.50 | Measure... |
| λ | 0.12 | W/m×K | 343.51 | Measure... |
| λ | 0.12 | W/m×K | 348.54 | Measure... |
| λ | 0.12 | W/m×K | 353.36 | Measure... |
| λ | 0.12 | W/m×K | 358.57 | Measure... |
| λ | 0.12 | W/m×K | 363.52 | Measure... |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 100.00 | 298.15 | 873.3 |
| 100.00 | 303.15 | 868.1 |
| 100.00 | 308.15 | 862.6 |
| 100.00 | 313.15 | 857.3 |
| 100.00 | 318.15 | 851.9 |
| 100.00 | 323.15 | 846.7 |
| 100.00 | 328.15 | 841.4 |
| 100.00 | 333.15 | 835.8 |
| 100.00 | 338.15 | 830.3 |
| 100.00 | 343.15 | 824.8 |
| 100.00 | 348.15 | 819.1 |
| 100.00 | 353.15 | 813.5 |
| 100.00 | 363.15 | 799.9 |
| 100.00 | 373.15 | 788.5 |
| 100.00 | 383.15 | 776.9 |
| 100.00 | 393.15 | 765.1 |
| 1000.00 | 298.15 | 874.1 |
| 1000.00 | 303.15 | 868.9 |
| 1000.00 | 308.15 | 863.5 |
| 1000.00 | 313.15 | 858.2 |
| 1000.00 | 318.15 | 852.8 |
| 1000.00 | 323.15 | 847.4 |
| 1000.00 | 328.15 | 842.0 |
| 1000.00 | 333.15 | 837.0 |
| 1000.00 | 338.15 | 831.5 |
| 1000.00 | 343.15 | 825.9 |
| 1000.00 | 348.15 | 820.3 |
| 1000.00 | 353.15 | 814.7 |
| 1000.00 | 363.15 | 801.4 |
| 1000.00 | 373.15 | 790.1 |
| 1000.00 | 383.15 | 778.6 |
| 1000.00 | 393.15 | 766.9 |
| 2000.00 | 298.15 | 875.0 |
| 2000.00 | 303.15 | 869.8 |
| 2000.00 | 308.15 | 864.4 |
| 2000.00 | 313.15 | 859.1 |
| 2000.00 | 318.15 | 853.8 |
| 2000.00 | 323.15 | 848.4 |
| 2000.00 | 328.15 | 843.3 |
| 2000.00 | 333.15 | 838.1 |
| 2000.00 | 338.15 | 832.6 |
| 2000.00 | 343.15 | 827.1 |
| 2000.00 | 348.15 | 821.6 |
| 2000.00 | 353.15 | 816.1 |
| 2000.00 | 363.15 | 803.0 |
| 2000.00 | 373.15 | 791.7 |
| 2000.00 | 383.15 | 780.4 |
| 2000.00 | 393.15 | 768.8 |
| 3000.00 | 298.15 | 875.9 |
| 3000.00 | 303.15 | 870.7 |
| 3000.00 | 308.15 | 865.3 |
| 3000.00 | 313.15 | 860.1 |
| 3000.00 | 318.15 | 854.8 |
| 3000.00 | 323.15 | 849.5 |
| 3000.00 | 328.15 | 844.5 |
| 3000.00 | 333.15 | 839.2 |
| 3000.00 | 338.15 | 833.8 |
| 3000.00 | 343.15 | 828.3 |
| 3000.00 | 348.15 | 822.9 |
| 3000.00 | 353.15 | 817.4 |
| 3000.00 | 363.15 | 804.5 |
| 3000.00 | 373.15 | 793.4 |
| 3000.00 | 383.15 | 782.2 |
| 3000.00 | 393.15 | 770.8 |
| 3100.00 | 298.15 | 876.0 |
| 3100.00 | 303.15 | 870.7 |
| 3100.00 | 308.15 | 865.4 |
| 3100.00 | 313.15 | 860.2 |
| 3100.00 | 318.15 | 854.9 |
| 3100.00 | 323.15 | 849.6 |
| 3100.00 | 328.15 | 844.6 |
| 3100.00 | 333.15 | 839.3 |
| 3100.00 | 338.15 | 833.9 |
| 3100.00 | 343.15 | 828.4 |
| 3100.00 | 348.15 | 823.0 |
| 3100.00 | 353.15 | 817.5 |
| 3100.00 | 363.15 | 804.7 |
| 3100.00 | 373.15 | 793.6 |
| 3100.00 | 383.15 | 782.4 |
| 3100.00 | 393.15 | 771.0 |
| 5000.00 | 298.15 | 877.5 |
| 5000.00 | 303.15 | 872.4 |
| 5000.00 | 308.15 | 867.1 |
| 5000.00 | 313.15 | 861.9 |
| 5000.00 | 318.15 | 856.7 |
| 5000.00 | 323.15 | 851.7 |
| 5000.00 | 328.15 | 846.6 |
| 5000.00 | 333.15 | 841.2 |
| 5000.00 | 338.15 | 835.9 |
| 5000.00 | 343.15 | 830.7 |
| 5000.00 | 348.15 | 825.1 |
| 5000.00 | 353.15 | 819.8 |
| 5000.00 | 363.15 | 807.9 |
| 5000.00 | 373.15 | 796.8 |
| 5000.00 | 383.15 | 785.5 |
| 5000.00 | 393.15 | 774.5 |
| 10000.00 | 298.15 | 881.5 |
| 10000.00 | 303.15 | 876.5 |
| 10000.00 | 308.15 | 871.4 |
| 10000.00 | 313.15 | 866.3 |
| 10000.00 | 318.15 | 861.3 |
| 10000.00 | 323.15 | 856.7 |
| 10000.00 | 328.15 | 851.5 |
| 10000.00 | 333.15 | 846.3 |
| 10000.00 | 338.15 | 841.2 |
| 10000.00 | 343.15 | 836.2 |
| 10000.00 | 348.15 | 830.9 |
| 10000.00 | 353.15 | 825.7 |
| 10000.00 | 363.15 | 814.4 |
| 10000.00 | 373.15 | 804.0 |
| 10000.00 | 383.15 | 793.5 |
| 10000.00 | 393.15 | 783.1 |
| 15000.00 | 298.15 | 885.3 |
| 15000.00 | 303.15 | 880.4 |
| 15000.00 | 308.15 | 875.5 |
| 15000.00 | 313.15 | 870.5 |
| 15000.00 | 318.15 | 865.8 |
| 15000.00 | 323.15 | 861.1 |
| 15000.00 | 328.15 | 856.2 |
| 15000.00 | 333.15 | 851.1 |
| 15000.00 | 338.15 | 846.2 |
| 15000.00 | 343.15 | 841.4 |
| 15000.00 | 348.15 | 836.2 |
| 15000.00 | 353.15 | 831.2 |
| 15000.00 | 363.15 | 820.7 |
| 15000.00 | 373.15 | 810.8 |
| 15000.00 | 383.15 | 800.8 |
| 15000.00 | 393.15 | 790.9 |
| 20000.00 | 298.15 | 889.0 |
| 20000.00 | 303.15 | 884.1 |
| 20000.00 | 308.15 | 879.4 |
| 20000.00 | 313.15 | 874.5 |
| 20000.00 | 318.15 | 869.9 |
| 20000.00 | 323.15 | 865.4 |
| 20000.00 | 328.15 | 860.5 |
| 20000.00 | 333.15 | 855.6 |
| 20000.00 | 338.15 | 850.8 |
| 20000.00 | 343.15 | 846.1 |
| 20000.00 | 348.15 | 841.1 |
| 20000.00 | 353.15 | 836.3 |
| 20000.00 | 363.15 | 826.7 |
| 20000.00 | 373.15 | 817.2 |
| 20000.00 | 383.15 | 807.5 |
| 20000.00 | 393.15 | 798.0 |
| 25000.00 | 298.15 | 892.5 |
| 25000.00 | 303.15 | 887.8 |
| 25000.00 | 308.15 | 883.1 |
| 25000.00 | 313.15 | 878.4 |
| 25000.00 | 318.15 | 874.1 |
| 25000.00 | 323.15 | 869.4 |
| 25000.00 | 328.15 | 864.8 |
| 25000.00 | 333.15 | 860.1 |
| 25000.00 | 338.15 | 855.5 |
| 25000.00 | 343.15 | 850.1 |
| 25000.00 | 348.15 | 846.0 |
| 25000.00 | 353.15 | 841.4 |
| 25000.00 | 363.15 | 832.4 |
| 25000.00 | 373.15 | 823.1 |
| 25000.00 | 383.15 | 813.8 |
| 25000.00 | 393.15 | 804.6 |
| 30000.00 | 298.15 | 896.9 |
| 30000.00 | 303.15 | 892.3 |
| 30000.00 | 308.15 | 887.8 |
| 30000.00 | 313.15 | 883.2 |
| 30000.00 | 318.15 | 879.0 |
| 30000.00 | 323.15 | 874.5 |
| 30000.00 | 328.15 | 870.0 |
| 30000.00 | 333.15 | 865.4 |
| 30000.00 | 338.15 | 861.0 |
| 30000.00 | 343.15 | 855.7 |
| 30000.00 | 348.15 | 851.8 |
| 30000.00 | 353.15 | 847.4 |
| 30000.00 | 363.15 | 837.7 |
| 30000.00 | 373.15 | 828.7 |
| 30000.00 | 383.15 | 819.6 |
| 30000.00 | 393.15 | 810.7 |
| 35000.00 | 298.15 | 901.4 |
| 35000.00 | 303.15 | 896.9 |
| 35000.00 | 308.15 | 892.5 |
| 35000.00 | 313.15 | 888.1 |
| 35000.00 | 318.15 | 884.1 |
| 35000.00 | 323.15 | 879.7 |
| 35000.00 | 328.15 | 875.3 |
| 35000.00 | 333.15 | 870.8 |
| 35000.00 | 338.15 | 866.5 |
| 35000.00 | 343.15 | 861.8 |
| 35000.00 | 348.15 | 857.7 |
| 35000.00 | 353.15 | 853.4 |
| 35000.00 | 363.15 | 842.7 |
| 35000.00 | 373.15 | 834.0 |
| 35000.00 | 383.15 | 825.2 |
| 35000.00 | 393.15 | 816.6 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [292.72; 418.65] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.49602e+01 | |||
| Coefficient B | -3.54866e+03 | |||
| Coefficient C | -5.08630e+01 | |||
| Temperature range, min. | 292.72 | |||
| Temperature range, max. | 418.65 | |||
| Pvap | 1.33 | kPa | 292.72 | Calculated Property |
| Pvap | 2.97 | kPa | 306.71 | Calculated Property |
| Pvap | 6.11 | kPa | 320.70 | Calculated Property |
| Pvap | 11.68 | kPa | 334.70 | Calculated Property |
| Pvap | 21.01 | kPa | 348.69 | Calculated Property |
| Pvap | 35.86 | kPa | 362.68 | Calculated Property |
| Pvap | 58.46 | kPa | 376.67 | Calculated Property |
| Pvap | 91.55 | kPa | 390.67 | Calculated Property |
| Pvap | 138.36 | kPa | 404.66 | Calculated Property |
| Pvap | 202.65 | kPa | 418.65 | Calculated Property |
| Pvap | [8.60e-06; 3099.82] | kPa | [175.15; 571.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 6.66105e+01 | |||
| Coefficient B | -6.89506e+03 | |||
| Coefficient C | -7.55898e+00 | |||
| Coefficient D | 4.55093e-06 | |||
| Temperature range, min. | 175.15 | |||
| Temperature range, max. | 571.00 | |||
| Pvap | 8.60e-06 | kPa | 175.15 | Calculated Property |
| Pvap | 4.62e-03 | kPa | 219.13 | Calculated Property |
| Pvap | 0.25 | kPa | 263.12 | Calculated Property |
| Pvap | 3.65 | kPa | 307.10 | Calculated Property |
| Pvap | 25.25 | kPa | 351.08 | Calculated Property |
| Pvap | 106.95 | kPa | 395.07 | Calculated Property |
| Pvap | 326.95 | kPa | 439.05 | Calculated Property |
| Pvap | 798.47 | kPa | 483.03 | Calculated Property |
| Pvap | 1664.77 | kPa | 527.02 | Calculated Property |
| Pvap | 3099.82 | kPa | 571.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Butanoic acid, ethyl ester.
Mixtures
- Carbon dioxide + Butanoic acid, ethyl ester
- Butanoic acid + Butanoic acid, ethyl ester + Water
- Butanoic acid, ethyl ester + Ethane, 1,2-dichloro-
- Butane, 1,4-dichloro- + Butanoic acid, ethyl ester
- Butanoic acid, ethyl ester + Propane, 1,3-dichloro-
- Pentane, 1,5-dichloro- + Butanoic acid, ethyl ester
- Butanoic acid, ethyl ester + Hexane, 1,6-dichloro-
- Hexane, 1,6-dibromo- + Butanoic acid, ethyl ester
- Pentane, 1,5-dibromo- + Butanoic acid, ethyl ester
- Butanoic acid, ethyl ester + Butane, 1,4-dibromo-
- Propane, 1,3-dibromo- + Butanoic acid, ethyl ester
- Ethane, 1,2-dibromo- + Butanoic acid, ethyl ester
- 1,4-Butanediol + Butanoic acid, ethyl ester
- Octane + Butanoic acid, ethyl ester
- 2-Propanol, 2-methyl- + Butanoic acid, ethyl ester
- Butanoic acid, ethyl ester + Methyl Alcohol
- Butanoic acid, ethyl ester + Water
- Butanoic acid, ethyl ester + Methyl Alcohol + Water
- Butanoic acid, ethyl ester + Heptane
- Butanoic acid, ethyl ester + Nonane
Find more mixtures with Butanoic acid, ethyl ester.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Vapor liquid equilibria of carbon dioxide with isopropyl acetate, diethyl carbonate and ethyl butyrate at elevated pressures
- Ternary phase diagrams for aqueous mixtures of butyric acid with several solvents: experimental and correlated data
- Temperature dependence of limiting activity coefficients, Henry's law constants, and related infinite dilution properties of C4-C6 isomeric n-alkyl ethanoates/ethyl n-alkanoates in water. Measurement, critical compilation, correlation, and recommended 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
- 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
- Acoustic and volumetric study of renewable oxygenated fuel additives at (298.15-323.15) K: Isomeric butanediols with ethylbutyrate
- Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
- Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
- Density, Viscosity, and Refractive Index Data for a Ternary System of Wine Congeners (Ethyl Butyrate + Diethyl Succinate + Isobutanol) in the Temperature Range from 288.15 to 323.15 K and at Atmospheric Pressure
- Isobaric Vapor-Liquid Equilibria and Excess Quantities for Binary Mixtures of an Ethyl Ester + tert-Butanol and a New Approach to VLE Data Processing
- Densities, Viscosities, and Surface and Interfacial Tensions of the Ternary Mixture Water + Ethyl Butyrate + Methanol at 303.15 K.
- Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
- Vapor-Liquid Equilibrium Data of the Carbon Dioxide + Ethyl Butyrate and Carbon Dioxide + Propylene Carbonate Systems at Pressures from (1.00 to 13.00) MPa and Temperatures from (313.0 to 373.0) K
- Measurements and Correlations of the Isobaric Vapor Liquid Equilibria of Binary Mixtures and Excess Properties for Mixtures Containing an Alkyl (Methyl, Ethyl) Butanoate with an Alkane (Heptane, Nonane) at 101.3 kPa
- Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
- Development of a Predictive Equation of State for CO2 + Ethyl Ester Mixtures Based on Critical Points Measurements
- Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
- Fast Determination of Binary Vapor Liquid Equilibrium of CO2-Based Mixtures at Elevated Pressures
- 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
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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