- InChI
- InChI=1S/C5H10O2/c1-3-5(6)7-4-2/h3-4H2,1-2H3
- InChI Key
- FKRCODPIKNYEAC-UHFFFAOYSA-N
- Formula
- C5H10O2
- SMILES
- CCOC(=O)CC
- Molecular Weight1
- 102.13
- CAS
- 105-37-3
- Other Names
-
- C2H5COOC2H5
- ETHYL ESTER PROPIONIC ACID
- Ethyl ester of propanoic acid
- Ethyl n-propionate
- Ethyl propanoate
- Ethyl propionate
- Ethylester kyseliny propionove
- NSC 8848
- Propionate d'ethyle
- Propionic acid, ethyl ester
- Propionic ester
- Propionic ether
- UN 1195
- n-Ethyl propanoate
- 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).
- 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).
- 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.
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3910 | KDB | |
| ΔcH°liquid | [-2912.10; -2888.00] | kJ/mol |
|
| ΔcH°liquid | -2894.00 ± 0.65 | kJ/mol | NIST |
| ΔcH°liquid | -2888.00 | kJ/mol | NIST |
| ΔcH°liquid | -2912.10 ± 2.00 | kJ/mol | NIST |
| μ | 1.80 | debye | KDB |
| ΔfG° | -323.70 | kJ/mol | KDB |
| ΔfH°gas | [-470.20; -463.60] | kJ/mol |
|
| ΔfH°gas | -470.20 | kJ/mol | KDB |
| ΔfH°gas | -466.50 ± 0.40 | kJ/mol | NIST |
| ΔfH°gas | -463.60 ± 0.70 | kJ/mol | NIST |
| ΔfH°liquid | [-505.59; -502.70] | kJ/mol |
|
| ΔfH°liquid | -505.59 ± 0.50 | kJ/mol | NIST |
| ΔfH°liquid | -502.70 ± 0.70 | kJ/mol | NIST |
| ΔfusH° | 11.49 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 35.88 | kJ/mol | Joback Calculated Property |
| IE | 10.00 ± 0.02 | eV | NIST |
| log10WS | [-0.66; -0.66] |
|
|
| log10WS | -0.66 | Aq. Sol... | |
| log10WS | -0.66 | Estimat... | |
| logPoct/wat | 0.959 | Crippen Calculated Property | |
| McVol | 88.750 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| Pc | [3359.70; 3510.00] | kPa |
|
| Pc | 3362.00 | kPa | KDB |
| Pc | 3385.60 | kPa | Develop... |
| Pc | 3362.00 ± 81.06 | kPa | NIST |
| Pc | 3359.70 ± 40.00 | kPa | NIST |
| Pc | 3510.00 ± 202.65 | kPa | NIST |
| Pc | 3510.00 ± 202.65 | kPa | NIST |
| ρc | [285.97; 296.90] | kg/m3 |
|
| ρc | 296.49 ± 10.01 | kg/m3 | NIST |
| ρc | 296.90 ± 4.09 | kg/m3 | NIST |
| ρc | 285.97 ± 10.01 | kg/m3 | NIST |
| ρc | 285.97 ± 10.01 | kg/m3 | NIST |
| Inp | [651.00; 733.00] |
|
|
| Inp | 694.20 | NIST | |
| Inp | 678.95 | NIST | |
| Inp | 700.00 | NIST | |
| Inp | 678.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 695.00 | NIST | |
| Inp | 707.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 694.00 | NIST | |
| Inp | 691.00 | NIST | |
| Inp | 694.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 704.00 | NIST | |
| Inp | 695.00 | NIST | |
| Inp | 679.00 | NIST | |
| Inp | Outlier 668.00 | NIST | |
| Inp | 693.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 693.00 | NIST | |
| Inp | 694.00 | NIST | |
| Inp | 699.00 | NIST | |
| Inp | 700.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 706.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 709.00 | NIST | |
| Inp | 706.00 | NIST | |
| Inp | 704.00 | NIST | |
| Inp | 714.00 | NIST | |
| Inp | 709.00 | NIST | |
| Inp | 711.00 | NIST | |
| Inp | 705.00 | NIST | |
| Inp | 680.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 714.00 | NIST | |
| Inp | 696.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 711.00 | NIST | |
| Inp | 691.00 | NIST | |
| Inp | 712.00 | NIST | |
| Inp | 700.00 | NIST | |
| Inp | 708.00 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | 712.00 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | 725.00 | NIST | |
| Inp | 698.00 | NIST | |
| Inp | 708.00 | NIST | |
| Inp | 714.00 | NIST | |
| Inp | 714.00 | NIST | |
| Inp | 710.00 | NIST | |
| Inp | 714.00 | NIST | |
| Inp | 702.00 | NIST | |
| Inp | Outlier 651.00 | NIST | |
| Inp | 714.00 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | Outlier 729.00 | NIST | |
| Inp | 705.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 705.00 | NIST | |
| Inp | 714.00 | NIST | |
| Inp | 705.00 | NIST | |
| Inp | 717.20 | NIST | |
| Inp | 712.00 | NIST | |
| Inp | 695.00 | NIST | |
| Inp | 703.00 | NIST | |
| Inp | 703.00 | NIST | |
| Inp | 705.00 | NIST | |
| Inp | 691.00 | NIST | |
| Inp | 709.00 | NIST | |
| Inp | 691.00 | NIST | |
| Inp | 691.00 | NIST | |
| Inp | 695.00 | NIST | |
| Inp | Outlier 657.00 | NIST | |
| Inp | 700.00 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | Outlier 733.00 | NIST | |
| Inp | 699.00 | NIST | |
| Inp | 714.00 | NIST | |
| Inp | 714.00 | NIST | |
| Inp | 710.00 | NIST | |
| Inp | 712.00 | NIST | |
| Inp | 711.00 | NIST | |
| Inp | 709.00 | NIST | |
| Inp | 708.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 707.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 708.00 | NIST | |
| Inp | 708.00 | NIST | |
| Inp | 703.00 | NIST | |
| Inp | 705.00 | NIST | |
| Inp | 714.00 | NIST | |
| Inp | 691.00 | NIST | |
| Inp | 709.00 | NIST | |
| Inp | 705.00 | NIST | |
| Inp | 709.00 | NIST | |
| Inp | 709.00 | NIST | |
| Inp | 709.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | Outlier 663.00 | NIST | |
| Inp | 694.00 | NIST | |
| Inp | 693.00 | NIST | |
| Inp | 695.00 | NIST | |
| Inp | 714.00 | NIST | |
| Inp | 715.00 | NIST | |
| Inp | 695.00 | NIST | |
| Inp | 679.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 693.00 | NIST | |
| Inp | 691.00 | NIST | |
| Inp | 691.00 | NIST | |
| Inp | 691.00 | NIST | |
| Inp | 679.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 708.00 | NIST | |
| Inp | 698.00 | NIST | |
| Inp | 714.00 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | 710.00 | NIST | |
| Inp | 703.00 | NIST | |
| Inp | 705.00 | NIST | |
| Inp | Outlier 663.00 | NIST | |
| Inp | 715.00 | NIST | |
| Inp | 691.00 | NIST | |
| Inp | 694.20 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 694.00 | NIST | |
| Inp | 695.00 | NIST | |
| Inp | 702.00 | NIST | |
| I | [910.00; 977.00] |
|
|
| I | 977.00 | NIST | |
| I | 957.00 | NIST | |
| I | 954.00 | NIST | |
| I | Outlier 910.00 | NIST | |
| I | 949.00 | NIST | |
| I | 970.00 | NIST | |
| I | 936.00 | NIST | |
| I | 977.00 | NIST | |
| I | 955.00 | NIST | |
| I | 966.00 | NIST | |
| I | 966.00 | NIST | |
| I | 951.00 | NIST | |
| I | 946.00 | NIST | |
| I | 953.00 | NIST | |
| I | 955.00 | NIST | |
| I | 976.00 | NIST | |
| I | 957.00 | NIST | |
| I | 939.00 | NIST | |
| I | 947.00 | NIST | |
| I | 922.00 | NIST | |
| I | 925.00 | NIST | |
| I | 928.00 | NIST | |
| I | 925.00 | NIST | |
| I | 961.00 | NIST | |
| I | 964.00 | NIST | |
| I | 953.00 | NIST | |
| I | 970.00 | NIST | |
| I | 951.00 | NIST | |
| I | 940.00 | NIST | |
| I | 960.00 | NIST | |
| I | 959.00 | NIST | |
| I | 960.00 | NIST | |
| I | 957.00 | NIST | |
| I | 965.00 | NIST | |
| I | 955.00 | NIST | |
| I | Outlier 915.00 | NIST | |
| I | 924.00 | NIST | |
| I | 951.00 | NIST | |
| I | 945.00 | NIST | |
| I | 960.00 | NIST | |
| I | 952.00 | NIST | |
| I | 949.00 | NIST | |
| I | 971.00 | NIST | |
| I | 956.00 | NIST | |
| I | 953.00 | NIST | |
| I | 953.00 | NIST | |
| I | 946.00 | NIST | |
| I | 931.00 | NIST | |
| I | 950.00 | NIST | |
| I | 950.00 | NIST | |
| I | 952.00 | NIST | |
| I | 952.00 | NIST | |
| I | 955.00 | NIST | |
| I | 955.00 | NIST | |
| I | 949.00 | NIST | |
| I | 945.00 | NIST | |
| I | 961.00 | NIST | |
| I | 967.00 | NIST | |
| I | 944.00 | NIST | |
| I | 940.00 | NIST | |
| I | 944.00 | NIST | |
| I | 952.00 | NIST | |
| I | 957.00 | NIST | |
| I | 939.00 | NIST | |
| I | 956.00 | NIST | |
| I | 957.00 | NIST | |
| I | 974.00 | NIST | |
| I | 964.00 | NIST | |
| I | 961.00 | NIST | |
| I | 957.00 | NIST | |
| I | 959.00 | NIST | |
| I | Outlier 916.00 | NIST | |
| I | 944.00 | NIST | |
| I | 950.00 | NIST | |
| I | 938.00 | NIST | |
| I | 925.00 | NIST | |
| I | 925.00 | NIST | |
| I | 925.00 | NIST | |
| I | 966.00 | NIST | |
| I | 944.00 | NIST | |
| I | 940.00 | NIST | |
| I | 948.00 | NIST | |
| I | 977.00 | NIST | |
| I | 970.00 | NIST | |
| I | 960.00 | NIST | |
| I | 955.00 | NIST | |
| I | 952.00 | NIST | |
| Tboil | [371.91; 372.25] | K |
|
| Tboil | 372.20 | K | KDB |
| Tboil | 372.20 | K | (Liquid... |
| Tboil | 372.25 | K | Isobari... |
| Tboil | 372.25 | K | Solubil... |
| Tboil | 371.91 | K | Isobari... |
| Tc | [545.60; 553.80] | K |
|
| Tc | 546.00 | K | KDB |
| Tc | 546.00 | K | NIST |
| Tc | 546.10 ± 1.00 | K | NIST |
| Tc | 546.00 ± 1.00 | K | NIST |
| Tc | 545.60 ± 1.00 | K | NIST |
| Tc | 552.70 ± 5.00 | K | NIST |
| Tc | 545.60 ± 2.00 | K | NIST |
| Tc | 553.80 ± 5.00 | K | NIST |
| Tfus | [199.20; 200.24] | K |
|
| Tfus | 199.85 | K | Aq. Sol... |
| Tfus | 199.20 | K | KDB |
| Tfus | 199.71 | K | Efficie... |
| Tfus | 199.25 ± 0.40 | K | NIST |
| Tfus | 200.24 ± 0.20 | K | NIST |
| Vc | 0.345 | m3/kmol | KDB |
| Zc | 0.2554980 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [163.46; 210.46] | J/mol×K | [390.09; 568.66] |
|
| Cp,gas | 163.46 | J/mol×K | 390.09 | Joback Calculated Property |
| Cp,gas | 171.91 | J/mol×K | 419.85 | Joback Calculated Property |
| Cp,gas | 180.12 | J/mol×K | 449.61 | Joback Calculated Property |
| Cp,gas | 188.08 | J/mol×K | 479.38 | Joback Calculated Property |
| Cp,gas | 195.80 | J/mol×K | 509.14 | Joback Calculated Property |
| Cp,gas | 203.26 | J/mol×K | 538.90 | Joback Calculated Property |
| Cp,gas | 210.46 | J/mol×K | 568.66 | Joback Calculated Property |
| Cp,liquid | [199.58; 200.90] | J/mol×K | [298.15; 298.33] |
|
| Cp,liquid | 200.90 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 199.58 | J/mol×K | 298.33 | NIST |
| η | [0.0003150; 0.0005230] | Pa×s | [293.15; 343.15] |
|
| η | 0.0005230 | Pa×s | 293.15 | Density... |
| η | 0.0004920 | Pa×s | 298.15 | Density... |
| η | 0.0004640 | Pa×s | 303.15 | Density... |
| η | 0.0004410 | Pa×s | 308.15 | Density... |
| η | 0.0004180 | Pa×s | 313.15 | Density... |
| η | 0.0003980 | Pa×s | 318.15 | Density... |
| η | 0.0003780 | Pa×s | 323.15 | Density... |
| η | 0.0003600 | Pa×s | 328.15 | Density... |
| η | 0.0003440 | Pa×s | 333.15 | Density... |
| η | 0.0003290 | Pa×s | 338.15 | Density... |
| η | 0.0003150 | Pa×s | 343.15 | Density... |
| ΔvapH | [33.88; 38.20] | kJ/mol | [313.00; 455.00] |
|
| ΔvapH | 38.20 ± 0.10 | kJ/mol | 313.00 | NIST |
| ΔvapH | 36.60 ± 0.10 | kJ/mol | 336.00 | NIST |
| ΔvapH | 38.20 | kJ/mol | 339.00 | NIST |
| ΔvapH | 36.00 ± 0.10 | kJ/mol | 344.00 | NIST |
| ΔvapH | 35.50 ± 0.10 | kJ/mol | 351.00 | NIST |
| ΔvapH | 34.50 ± 0.10 | kJ/mol | 363.00 | NIST |
| ΔvapH | 36.70 | kJ/mol | 367.50 | NIST |
| ΔvapH | 33.88 | kJ/mol | 372.20 | NIST |
| ΔvapH | 34.40 | kJ/mol | 455.00 | NIST |
| Pvap | [10.60; 101.30] | kPa | [313.15; 372.25] |
|
| Pvap | 10.60 | kPa | 313.15 | Total V... |
| Pvap | 101.30 | kPa | 372.25 | Isobari... |
| n0 | [1.37110; 1.38150] | [298.15; 318.15] |
|
|
| n0 | 1.38150 | 298.15 | Thermod... | |
| n0 | 1.38110 | 298.15 | Improve... | |
| n0 | 1.37110 | 318.15 | Thermod... | |
| ρl | 895.00 | kg/m3 | 289.00 | KDB |
| λ | [0.12; 0.15] | W/m×K | [263.55; 356.28] |
|
| λ | 0.15 | W/m×K | 263.55 | Measure... |
| λ | 0.15 | W/m×K | 268.41 | Measure... |
| λ | 0.15 | W/m×K | 270.94 | Measure... |
| λ | 0.15 | W/m×K | 278.51 | Measure... |
| λ | 0.14 | W/m×K | 283.51 | Measure... |
| λ | 0.14 | W/m×K | 288.56 | Measure... |
| λ | 0.14 | W/m×K | 293.54 | Measure... |
| λ | 0.14 | W/m×K | 296.36 | Measure... |
| λ | 0.14 | W/m×K | 301.40 | Measure... |
| λ | 0.14 | W/m×K | 306.51 | Measure... |
| λ | 0.13 | W/m×K | 311.34 | Measure... |
| λ | 0.13 | W/m×K | 316.45 | Measure... |
| λ | 0.13 | W/m×K | 321.47 | Measure... |
| λ | 0.13 | W/m×K | 326.44 | Measure... |
| λ | 0.13 | W/m×K | 331.53 | Measure... |
| λ | 0.13 | W/m×K | 336.40 | Measure... |
| λ | 0.12 | W/m×K | 341.36 | Measure... |
| λ | 0.12 | W/m×K | 346.42 | Measure... |
| λ | 0.12 | W/m×K | 351.35 | Measure... |
| λ | 0.12 | W/m×K | 356.28 | Measure... |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 100.00 | 298.15 | 884.3 |
| 100.00 | 303.15 | 878.5 |
| 100.00 | 308.15 | 872.7 |
| 100.00 | 313.15 | 866.8 |
| 100.00 | 318.15 | 860.9 |
| 100.00 | 323.15 | 854.9 |
| 100.00 | 328.15 | 849.2 |
| 100.00 | 333.15 | 843.1 |
| 100.00 | 338.15 | 836.9 |
| 100.00 | 343.15 | 831.1 |
| 100.00 | 348.15 | 824.9 |
| 100.00 | 353.15 | 818.7 |
| 100.00 | 363.15 | 803.5 |
| 100.00 | 373.15 | 790.9 |
| 1000.00 | 298.15 | 884.8 |
| 1000.00 | 303.15 | 879.0 |
| 1000.00 | 308.15 | 873.2 |
| 1000.00 | 313.15 | 867.4 |
| 1000.00 | 318.15 | 861.5 |
| 1000.00 | 323.15 | 856.0 |
| 1000.00 | 328.15 | 850.2 |
| 1000.00 | 333.15 | 844.2 |
| 1000.00 | 338.15 | 838.2 |
| 1000.00 | 343.15 | 832.2 |
| 1000.00 | 348.15 | 826.0 |
| 1000.00 | 353.15 | 819.9 |
| 1000.00 | 363.15 | 805.1 |
| 1000.00 | 373.15 | 792.6 |
| 1000.00 | 383.15 | 780.0 |
| 1000.00 | 393.15 | 766.4 |
| 2000.00 | 298.15 | 885.7 |
| 2000.00 | 303.15 | 880.0 |
| 2000.00 | 308.15 | 874.2 |
| 2000.00 | 313.15 | 868.4 |
| 2000.00 | 318.15 | 862.6 |
| 2000.00 | 323.15 | 857.1 |
| 2000.00 | 328.15 | 851.3 |
| 2000.00 | 333.15 | 845.4 |
| 2000.00 | 338.15 | 839.5 |
| 2000.00 | 343.15 | 833.5 |
| 2000.00 | 348.15 | 827.4 |
| 2000.00 | 353.15 | 821.3 |
| 2000.00 | 363.15 | 806.9 |
| 2000.00 | 373.15 | 794.5 |
| 2000.00 | 383.15 | 782.1 |
| 2000.00 | 393.15 | 768.7 |
| 3000.00 | 298.15 | 886.6 |
| 3000.00 | 303.15 | 880.9 |
| 3000.00 | 308.15 | 875.2 |
| 3000.00 | 313.15 | 869.4 |
| 3000.00 | 318.15 | 863.7 |
| 3000.00 | 323.15 | 858.1 |
| 3000.00 | 328.15 | 852.5 |
| 3000.00 | 333.15 | 846.6 |
| 3000.00 | 338.15 | 840.7 |
| 3000.00 | 343.15 | 834.8 |
| 3000.00 | 348.15 | 828.8 |
| 3000.00 | 353.15 | 822.7 |
| 3000.00 | 363.15 | 808.7 |
| 3000.00 | 373.15 | 796.4 |
| 3000.00 | 383.15 | 784.1 |
| 3000.00 | 393.15 | 770.8 |
| 3340.00 | 298.15 | 886.9 |
| 3340.00 | 303.15 | 881.2 |
| 3340.00 | 308.15 | 875.5 |
| 3340.00 | 313.15 | 869.8 |
| 3340.00 | 318.15 | 864.1 |
| 3340.00 | 323.15 | 858.4 |
| 3340.00 | 328.15 | 852.9 |
| 3340.00 | 333.15 | 847.0 |
| 3340.00 | 338.15 | 841.1 |
| 3340.00 | 343.15 | 835.2 |
| 3340.00 | 348.15 | 829.3 |
| 3340.00 | 353.15 | 823.2 |
| 3340.00 | 363.15 | 809.3 |
| 3340.00 | 373.15 | 797.1 |
| 3340.00 | 383.15 | 784.8 |
| 3340.00 | 393.15 | 771.5 |
| 5000.00 | 298.15 | 888.7 |
| 5000.00 | 303.15 | 883.0 |
| 5000.00 | 308.15 | 877.4 |
| 5000.00 | 313.15 | 871.7 |
| 5000.00 | 318.15 | 866.1 |
| 5000.00 | 323.15 | 860.3 |
| 5000.00 | 328.15 | 854.7 |
| 5000.00 | 333.15 | 849.0 |
| 5000.00 | 338.15 | 843.1 |
| 5000.00 | 343.15 | 837.4 |
| 5000.00 | 348.15 | 831.5 |
| 5000.00 | 353.15 | 825.6 |
| 5000.00 | 363.15 | 812.0 |
| 5000.00 | 373.15 | 800.0 |
| 5000.00 | 383.15 | 787.9 |
| 5000.00 | 393.15 | 775.0 |
| 10000.00 | 298.15 | 892.9 |
| 10000.00 | 303.15 | 887.4 |
| 10000.00 | 308.15 | 882.0 |
| 10000.00 | 313.15 | 876.5 |
| 10000.00 | 318.15 | 871.0 |
| 10000.00 | 323.15 | 865.4 |
| 10000.00 | 328.15 | 860.0 |
| 10000.00 | 333.15 | 854.6 |
| 10000.00 | 338.15 | 848.8 |
| 10000.00 | 343.15 | 843.4 |
| 10000.00 | 348.15 | 837.7 |
| 10000.00 | 353.15 | 832.1 |
| 10000.00 | 363.15 | 819.6 |
| 10000.00 | 373.15 | 808.2 |
| 10000.00 | 383.15 | 796.6 |
| 10000.00 | 393.15 | 784.5 |
| 15000.00 | 298.15 | 896.9 |
| 15000.00 | 303.15 | 891.6 |
| 15000.00 | 308.15 | 886.3 |
| 15000.00 | 313.15 | 880.9 |
| 15000.00 | 318.15 | 875.6 |
| 15000.00 | 323.15 | 870.2 |
| 15000.00 | 328.15 | 865.0 |
| 15000.00 | 333.15 | 859.7 |
| 15000.00 | 338.15 | 854.4 |
| 15000.00 | 343.15 | 848.9 |
| 15000.00 | 348.15 | 843.4 |
| 15000.00 | 353.15 | 838.0 |
| 15000.00 | 363.15 | 826.5 |
| 15000.00 | 373.15 | 815.6 |
| 15000.00 | 383.15 | 804.6 |
| 15000.00 | 393.15 | 793.1 |
| 20000.00 | 298.15 | 900.7 |
| 20000.00 | 303.15 | 895.6 |
| 20000.00 | 308.15 | 890.4 |
| 20000.00 | 313.15 | 885.1 |
| 20000.00 | 318.15 | 880.0 |
| 20000.00 | 323.15 | 874.7 |
| 20000.00 | 328.15 | 869.6 |
| 20000.00 | 333.15 | 864.5 |
| 20000.00 | 338.15 | 859.4 |
| 20000.00 | 343.15 | 854.0 |
| 20000.00 | 348.15 | 848.8 |
| 20000.00 | 353.15 | 843.5 |
| 20000.00 | 363.15 | 833.0 |
| 20000.00 | 373.15 | 822.5 |
| 20000.00 | 383.15 | 811.9 |
| 20000.00 | 393.15 | 800.8 |
| 25000.00 | 298.15 | 904.4 |
| 25000.00 | 303.15 | 899.4 |
| 25000.00 | 308.15 | 894.3 |
| 25000.00 | 313.15 | 889.3 |
| 25000.00 | 318.15 | 884.1 |
| 25000.00 | 323.15 | 879.1 |
| 25000.00 | 328.15 | 874.0 |
| 25000.00 | 333.15 | 869.2 |
| 25000.00 | 338.15 | 863.6 |
| 25000.00 | 343.15 | 859.1 |
| 25000.00 | 348.15 | 854.0 |
| 25000.00 | 353.15 | 848.9 |
| 25000.00 | 363.15 | 839.1 |
| 25000.00 | 373.15 | 829.0 |
| 25000.00 | 383.15 | 818.7 |
| 25000.00 | 393.15 | 808.0 |
| 30000.00 | 298.15 | 908.9 |
| 30000.00 | 303.15 | 904.0 |
| 30000.00 | 308.15 | 899.2 |
| 30000.00 | 313.15 | 894.4 |
| 30000.00 | 318.15 | 889.1 |
| 30000.00 | 323.15 | 884.3 |
| 30000.00 | 328.15 | 879.4 |
| 30000.00 | 333.15 | 874.8 |
| 30000.00 | 338.15 | 869.9 |
| 30000.00 | 343.15 | 865.0 |
| 30000.00 | 348.15 | 860.1 |
| 30000.00 | 353.15 | 855.3 |
| 30000.00 | 363.15 | 844.8 |
| 30000.00 | 373.15 | 834.9 |
| 30000.00 | 383.15 | 825.0 |
| 30000.00 | 393.15 | 814.7 |
| 35000.00 | 298.15 | 913.6 |
| 35000.00 | 303.15 | 908.9 |
| 35000.00 | 308.15 | 904.2 |
| 35000.00 | 313.15 | 899.5 |
| 35000.00 | 318.15 | 894.3 |
| 35000.00 | 323.15 | 889.7 |
| 35000.00 | 328.15 | 884.9 |
| 35000.00 | 333.15 | 880.6 |
| 35000.00 | 338.15 | 875.8 |
| 35000.00 | 343.15 | 871.0 |
| 35000.00 | 348.15 | 866.3 |
| 35000.00 | 353.15 | 861.6 |
| 35000.00 | 363.15 | 850.2 |
| 35000.00 | 373.15 | 840.6 |
| 35000.00 | 383.15 | 830.9 |
| 35000.00 | 393.15 | 820.9 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.62] | kPa | [275.40; 396.11] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.45526e+01 | |||
| Coefficient B | -3.16736e+03 | |||
| Coefficient C | -5.33670e+01 | |||
| Temperature range, min. | 275.40 | |||
| Temperature range, max. | 396.11 | |||
| Pvap | 1.33 | kPa | 275.40 | Calculated Property |
| Pvap | 3.00 | kPa | 288.81 | Calculated Property |
| Pvap | 6.20 | kPa | 302.22 | Calculated Property |
| Pvap | 11.89 | kPa | 315.64 | Calculated Property |
| Pvap | 21.40 | kPa | 329.05 | Calculated Property |
| Pvap | 36.47 | kPa | 342.46 | Calculated Property |
| Pvap | 59.27 | kPa | 355.87 | Calculated Property |
| Pvap | 92.45 | kPa | 369.29 | Calculated Property |
| Pvap | 139.07 | kPa | 382.70 | Calculated Property |
| Pvap | 202.62 | kPa | 396.11 | Calculated Property |
| Pvap | [7.72e-04; 3311.89] | kPa | [199.25; 546.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.01207e+02 | |||
| Coefficient B | -8.10148e+03 | |||
| Coefficient C | -1.28594e+01 | |||
| Coefficient D | 9.33835e-06 | |||
| Temperature range, min. | 199.25 | |||
| Temperature range, max. | 546.00 | |||
| Pvap | 7.72e-04 | kPa | 199.25 | Calculated Property |
| Pvap | 0.07 | kPa | 237.78 | Calculated Property |
| Pvap | 1.36 | kPa | 276.31 | Calculated Property |
| Pvap | 11.39 | kPa | 314.83 | Calculated Property |
| Pvap | 54.26 | kPa | 353.36 | Calculated Property |
| Pvap | 178.61 | kPa | 391.89 | Calculated Property |
| Pvap | 457.44 | kPa | 430.42 | Calculated Property |
| Pvap | 985.54 | kPa | 468.94 | Calculated Property |
| Pvap | 1883.25 | kPa | 507.47 | Calculated Property |
| Pvap | 3311.89 | kPa | 546.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Propanoic acid, ethyl ester.
Mixtures
- Propanoic acid, ethyl ester + Heptane
- Propanoic acid, ethyl ester + Nonane
- Propanoic acid, ethyl ester + Undecane
- Propanoic acid, ethyl ester + Tridecane
- Propanoic acid, ethyl ester + Pentadecane
- Propanoic acid, ethyl ester + Heptadecane
- Propanoic acid, ethyl ester + Ethane, 1,2-dichloro-
- Propanoic acid, ethyl ester + Propane, 1,3-dichloro-
- Propanoic acid, ethyl ester + Butane, 1,4-dichloro-
- Propanoic acid, ethyl ester + Pentane, 1,5-dichloro-
- Propanoic acid, ethyl ester + Hexane, 1,6-dichloro-
- Propanoic acid, ethyl ester + Ethane, 1,2-dibromo-
- Propanoic acid, ethyl ester + Propane, 1,3-dibromo-
- Propanoic acid, ethyl ester + Butane, 1,4-dibromo-
- Propanoic acid, ethyl ester + Pentane, 1,5-dibromo-
- Propanoic acid, ethyl ester + Hexane, 1,6-dibromo-
- Propanoic acid, ethyl ester + Butanoic acid + Water
- Propanoic acid, ethyl ester + Water
- Propanoic acid, ethyl ester + Ethane, iodo-
- Propanoic acid, ethyl ester + Propanoic acid + Water
Find more mixtures with Propanoic acid, ethyl ester.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Experimental determination and calculation of the critical curves for the binary systems of CO2 containing ketone, alkane, ester and alcohol, respectively
- 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
- Vapor-liquid equilibrium in the binary and ternary systems containing ethyl propionate, ethanol and alkane at 101.3 kPa
- Thermodynamic properties of (an ester + and alkane). XVII. Experimental He and Ve values for (an alkyl propanoate + an alkane) at 318.15K
- 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
- (Liquid + liquid) equilibria of (water + butyric acid + esters) ternary systems
- Efficient determination of crystallisation and melting points at low cooling and heating rates with novel computer controlled equipment
- Isothermal (vapour + liquid) equilibria for the binary systems of (carbon monoxide + methyl propionate) and (carbon monoxide + ethyl propionate)
- Liquid-liquid equilibrium of alcohol-ester systems with deep eutectic solvent on the base of choline chloride
- Isobaric vapour-liquid equilibrium for binary systems of ethyl iodide with ethanol, propionic acid and ethyl propionate at 101.3 kPa
- Solubility and critical surface in the system propionic acid-ethanol-ethyl propionate-water at 293.15, 303.15 and 313.15 K
- Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
- Isobaric Vapor-Liquid Equilibria and Excess Quantities for Binary Mixtures of an Ethyl Ester + tert-Butanol and a New Approach to VLE Data Processing
- Total Vapor Pressure Measurements for 2-Ethoxyethanol with Methyl Acetate, Ethyl Acetate, Propyl Acetate, and Ethyl Propionate at 313.15 K and for 2-Ethoxyethanol with Methyl Formate at 308.15 K
- Vapor-Liquid Equilibria of the Carbon Dioxide + Ethyl Propanoate and Carbon Dioxide + Ethyl Acetate Systems at Pressure from 2.96 MPa to 11.79 MPa and Temperature from 313 K to 393 K
- Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
- Improvements in the Experimentation and the Representation of Thermodynamic Properties (iso-p VLE and yE) of Alkyl Propanoate + Alkane Binaries
- 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
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.