- 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.
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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] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 160 170 180 190 200 210 400 450 500 550 | ||||
| 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] |
|
|
T(K) Dynamic viscosity (Pa×s) 3.00e-4 3.50e-4 4.00e-4 4.50e-4 5.00e-4 300 320 340 | ||||
| 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] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 34 35 36 37 38 350 400 450 | ||||
| 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] |
|
|
T(K) Liquid thermal conductivity (W/m×K) 0.12 0.13 0.13 0.14 0.14 0.15 0.15 0.16 280 300 320 340 | ||||
| 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 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 | ||||
| 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 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 200 300 400 500 | ||||
| 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
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