- InChI
- InChI=1S/C2H4/c1-2/h1-2H2
- InChI Key
- VGGSQFUCUMXWEO-UHFFFAOYSA-N
- Formula
- C2H4
- SMILES
- C=C
- Molecular Weight1
- 28.05
- CAS
- 74-85-1
- Other Names
-
- Acetene
- Athylen
- Bicarburretted hydrogen
- C2H4
- Elayl
- Ethene
- Liquid ethyene
- Olefiant gas
- UN 1038
- UN 1962
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- Tig : Autoignition Temperature (K).
- BasG : Gas basicity (kJ/mol).
- ΔcH°gas : Standard gas 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).
- LFL : Lower Flammability Limit (% in Air).
- UFL : Upper Flammability Limit (% in Air).
- Tflash,oc : Flash Point (Open Cup Method) (K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- Rg : Radius of Gyration.
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°(+) ion : Enthalpy of formation of positive ion at standard conditions (kJ/mol).
- ΔfH(+) ion,0K : Enthalpy of formation of positive ion at 0K (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔsubH : Enthalpy of sublimation at a given temperature (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.
- NFPA Health : NFPA Health Rating.
- NFPA Safety : NFPA Safety Rating.
- Pc : Critical Pressure (kPa).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- γ : Surface Tension (N/m).
- ΔvapS : Entropy of vaporization at a given temperature (J/mol×K).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λ : Gas thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 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 | 0.0890 | KDB | |
| PAff | 680.50 | kJ/mol | NIST |
| Tig | 723.15 | K | KDB |
| BasG | 651.50 | kJ/mol | NIST |
| ΔcH°gas | -1411.20 ± 0.30 | kJ/mol | NIST |
| μ | 0.00 | debye | KDB |
| LFL | 2.70 | % in Air | KDB |
| UFL | 28.60 | % in Air | KDB |
| Tflash,oc | 137.04 | K | KDB |
| ΔfG° | 68.16 | kJ/mol | KDB |
| Rg | 1.5380 | KDB | |
| ΔfH°gas | [52.34; 52.40] | kJ/mol |
|
| ΔfH°gas | 52.34 | kJ/mol | KDB |
| ΔfH°gas | 52.40 ± 0.50 | kJ/mol | NIST |
| ΔfH°(+) ion | 1067.00 ± 0.80 | kJ/mol | NIST |
| ΔfH(+) ion,0K | 1080.00 | kJ/mol | NIST |
| ΔfusH° | -1.83 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 18.75 | kJ/mol | Joback Calculated Property |
| IE | [10.50; 10.80] | eV |
|
| IE | 10.51 ± 0.00 | eV | NIST |
| IE | 10.51 | eV | NIST |
| IE | 10.51 ± 0.00 | eV | NIST |
| IE | 10.51 ± 0.01 | eV | NIST |
| IE | 10.51 ± 0.01 | eV | NIST |
| IE | 10.51 | eV | NIST |
| IE | 10.50 ± 0.02 | eV | NIST |
| IE | 10.51 ± 0.01 | eV | NIST |
| IE | 10.51 | eV | NIST |
| IE | 10.51 ± 0.02 | eV | NIST |
| IE | 10.50 | eV | NIST |
| IE | 10.52 ± 0.00 | eV | NIST |
| IE | 10.52 ± 0.00 | eV | NIST |
| IE | 10.51 | eV | NIST |
| IE | 10.50 | eV | NIST |
| IE | 10.51 ± 0.00 | eV | NIST |
| IE | 10.51 ± 0.01 | eV | NIST |
| IE | 10.52 ± 0.00 | eV | NIST |
| IE | 10.51 | eV | NIST |
| IE | 10.51 | eV | NIST |
| IE | 10.51 | eV | NIST |
| IE | 10.56 | eV | NIST |
| IE | 10.51 ± 0.02 | eV | NIST |
| IE | 10.51 ± 0.05 | eV | NIST |
| IE | 10.50 ± 0.05 | eV | NIST |
| IE | 10.51 | eV | NIST |
| IE | 10.51 ± 0.01 | eV | NIST |
| IE | 10.50 ± 0.01 | eV | NIST |
| IE | 10.51 ± 0.00 | eV | NIST |
| IE | 10.50 ± 0.02 | eV | NIST |
| IE | 10.52 ± 0.01 | eV | NIST |
| IE | 10.51 ± 0.03 | eV | NIST |
| IE | Outlier 10.80 ± 0.05 | eV | NIST |
| IE | Outlier 10.68 | eV | NIST |
| IE | 10.50 ± 0.01 | eV | NIST |
| IE | 10.50 | eV | NIST |
| IE | 10.50 | eV | NIST |
| log10WS | [-0.40; -0.40] |
|
|
| log10WS | -0.40 | Estimat... | |
| log10WS | -0.40 | Aq. Sol... | |
| logPoct/wat | 0.802 | Crippen Calculated Property | |
| McVol | 34.740 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 4 | KDB | |
| NFPA Health | 1 | KDB | |
| NFPA Safety | 2 | KDB | |
| Pc | [5020.00; 5119.95] | kPa |
|
| Pc | 5041.00 | kPa | KDB |
| Pc | 5020.00 | kPa | Gas-Liq... |
| Pc | 5041.00 ± 4.00 | kPa | NIST |
| Pc | 5055.00 ± 5.04 | kPa | NIST |
| Pc | 5040.10 ± 5.00 | kPa | NIST |
| Pc | 5055.00 ± 5.00 | kPa | NIST |
| Pc | 5040.30 ± 0.20 | kPa | NIST |
| Pc | 5040.30 ± 0.20 | kPa | NIST |
| Pc | 5042.00 ± 4.00 | kPa | NIST |
| Pc | 5076.00 ± 2.00 | kPa | NIST |
| Pc | Outlier 5119.95 ± 20.26 | kPa | NIST |
| Pc | 5061.00 ± 101.32 | kPa | NIST |
| Ptriple | [0.12; 0.12] | kPa |
|
| Ptriple | 0.12 ± 0.01 | kPa | NIST |
| Ptriple | 0.12 | kPa | NIST |
| ρc | [214.05; 530.04] | kg/m3 |
|
| ρc | 214.05 ± 0.11 | kg/m3 | NIST |
| ρc | 214.14 ± 0.11 | kg/m3 | NIST |
| ρc | 214.16 ± 0.02 | kg/m3 | NIST |
| ρc | 530.04 ± 0.20 | kg/m3 | NIST |
| ρc | 215.97 ± 0.56 | kg/m3 | NIST |
| Inp | [158.00; 188.00] |
|
|
| Inp | 166.00 | NIST | |
| Inp | 175.00 | NIST | |
| Inp | 177.00 | NIST | |
| Inp | 177.00 | NIST | |
| Inp | 178.00 | NIST | |
| Inp | 178.00 | NIST | |
| Inp | 178.10 | NIST | |
| Inp | 164.00 | NIST | |
| Inp | 183.00 | NIST | |
| Inp | 158.00 | NIST | |
| Inp | 166.00 | NIST | |
| Inp | 165.00 | NIST | |
| Inp | 178.00 | NIST | |
| Inp | 180.00 | NIST | |
| Inp | 166.00 | NIST | |
| Inp | 165.00 | NIST | |
| Inp | 165.00 | NIST | |
| Inp | 165.00 | NIST | |
| Inp | 165.00 | NIST | |
| Inp | 188.00 | NIST | |
| Inp | 180.00 | NIST | |
| Inp | 166.00 | NIST | |
| Inp | 178.00 | NIST | |
| Inp | 183.00 | NIST | |
| Inp | 158.00 | NIST | |
| S°liquid | 117.80 | J/mol×K | NIST |
| Tboil | [168.08; 170.45] | K |
|
| Tboil | 169.38 | K | KDB |
| Tboil | 169.35 ± 0.02 | K | NIST |
| Tboil | 169.30 ± 0.20 | K | NIST |
| Tboil | Outlier 168.08 ± 2.00 | K | NIST |
| Tboil | 169.25 ± 0.50 | K | NIST |
| Tboil | 169.00 ± 0.30 | K | NIST |
| Tboil | 169.25 ± 0.50 | K | NIST |
| Tboil | 169.43 ± 0.50 | K | NIST |
| Tboil | 169.30 ± 0.50 | K | NIST |
| Tboil | Outlier 170.45 ± 0.70 | K | NIST |
| Tc | [282.33; 283.10] | K |
|
| Tc | 282.34 | K | KDB |
| Tc | 282.34 ± 0.02 | K | NIST |
| Tc | 282.33 ± 0.02 | K | NIST |
| Tc | 282.35 ± 0.02 | K | NIST |
| Tc | 282.33 ± 0.10 | K | NIST |
| Tc | 282.34 ± 0.00 | K | NIST |
| Tc | 282.34 ± 0.00 | K | NIST |
| Tc | 282.35 ± 0.03 | K | NIST |
| Tc | 282.65 ± 0.25 | K | NIST |
| Tc | 282.69 ± 0.30 | K | NIST |
| Tc | Outlier 283.10 ± 0.60 | K | NIST |
| Tfus | [103.70; 104.01] | K |
|
| Tfus | 104.00 | K | KDB |
| Tfus | 104.01 | K | Aq. Sol... |
| Tfus | 103.80 ± 0.20 | K | NIST |
| Tfus | 103.70 ± 0.50 | K | NIST |
| Tfus | 103.70 ± 1.00 | K | NIST |
| Ttriple | [103.80; 104.10] | K |
|
| Ttriple | 103.99 ± 0.05 | K | NIST |
| Ttriple | 103.98 ± 0.01 | K | NIST |
| Ttriple | 103.97 ± 0.02 | K | NIST |
| Ttriple | 103.97 ± 0.03 | K | NIST |
| Ttriple | 104.10 ± 0.50 | K | NIST |
| Ttriple | 103.97 ± 0.02 | K | NIST |
| Ttriple | 103.97 ± 0.15 | K | NIST |
| Ttriple | 103.95 ± 0.10 | K | NIST |
| Ttriple | Outlier 103.80 ± 0.30 | K | NIST |
| Vc | [0.129; 0.131] | m3/kmol |
|
| Vc | 0.131 | m3/kmol | KDB |
| Vc | 0.131 | m3/kmol | NIST |
| Vc | 0.131 ± 0.000 | m3/kmol | NIST |
| Vc | 0.131 ± 0.000 | m3/kmol | NIST |
| Vc | 0.129 ± 0.000 | m3/kmol | NIST |
| Zc | 0.2815210 | KDB | |
| Zra | 0.28 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [34.66; 59.25] | J/mol×K | [178.15; 463.60] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 35 40 45 50 55 60 200 300 400 | ||||
| Cp,gas | 34.66 ± 0.26 | J/mol×K | 178.15 | NIST |
| Cp,gas | 35.30 ± 0.26 | J/mol×K | 192.35 | NIST |
| Cp,gas | 36.29 ± 0.27 | J/mol×K | 210.40 | NIST |
| Cp,gas | 37.55 ± 0.28 | J/mol×K | 230.90 | NIST |
| Cp,gas | 39.02 ± 0.29 | J/mol×K | 250.60 | NIST |
| Cp,gas | 40.75 ± 0.02 | J/mol×K | 270.70 | NIST |
| Cp,gas | 41.02 ± 0.31 | J/mol×K | 271.80 | NIST |
| Cp,gas | 42.84 ± 0.32 | J/mol×K | 293.45 | NIST |
| Cp,gas | 43.47 ± 0.17 | J/mol×K | 300.00 | NIST |
| Cp,gas | 45.98 ± 0.04 | J/mol×K | 320.70 | NIST |
| Cp,gas | 49.74 ± 0.37 | J/mol×K | 367.70 | NIST |
| Cp,gas | 59.25 ± 0.44 | J/mol×K | 463.60 | NIST |
| Cp,liquid | [67.24; 67.40] | J/mol×K | [170.00; 170.00] |
|
| Cp,liquid | 67.40 | J/mol×K | 170.00 | NIST |
| Cp,liquid | 67.24 | J/mol×K | 170.00 | NIST |
| η | [0.0000940; 0.0005524] | Pa×s | [113.86; 234.36] |
|
|
T(K) Dynamic viscosity (Pa×s) 1.00e-4 2.00e-4 3.00e-4 4.00e-4 5.00e-4 150 200 | ||||
| η | 0.0005524 | Pa×s | 113.86 | Joback Calculated Property |
| η | 0.0003296 | Pa×s | 133.94 | Joback Calculated Property |
| η | 0.0002250 | Pa×s | 154.03 | Joback Calculated Property |
| η | 0.0001677 | Pa×s | 174.11 | Joback Calculated Property |
| η | 0.0001329 | Pa×s | 194.19 | Joback Calculated Property |
| η | 0.0001099 | Pa×s | 214.28 | Joback Calculated Property |
| η | 0.0000940 | Pa×s | 234.36 | Joback Calculated Property |
| ΔfusH | [3.35; 3.35] | kJ/mol | [103.95; 104.00] |
|
| ΔfusH | 3.35 | kJ/mol | 103.95 | NIST |
| ΔfusH | 3.35 | kJ/mol | 103.97 | NIST |
| ΔfusH | 3.35 | kJ/mol | 104.00 | NIST |
| ΔfusH | 3.35 | kJ/mol | 104.00 | NIST |
| ΔsubH | [15.00; 18.40] | kJ/mol | [90.00; 91.50] |
|
| ΔsubH | 15.00 | kJ/mol | 90.00 | NIST |
| ΔsubH | 18.40 | kJ/mol | 91.50 | NIST |
| ΔvapH | [13.54; 14.40] | kJ/mol | [145.00; 267.00] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 13.6 13.8 14 14.2 14.4 150 200 250 | ||||
| ΔvapH | 14.40 | kJ/mol | 145.00 | NIST |
| ΔvapH | 14.40 | kJ/mol | 147.50 | NIST |
| ΔvapH | 14.10 | kJ/mol | 151.00 | NIST |
| ΔvapH | 14.30 | kJ/mol | 161.00 | NIST |
| ΔvapH | 13.54 | kJ/mol | 169.40 | KDB |
| ΔvapH | 13.54 | kJ/mol | 169.40 | NIST |
| ΔvapH | 14.00 | kJ/mol | 170.00 | NIST |
| ΔvapH | 13.70 | kJ/mol | 190.00 | NIST |
| ΔvapH | 13.70 | kJ/mol | 221.50 | NIST |
| ΔvapH | 13.60 | kJ/mol | 231.50 | NIST |
| ΔvapH | 14.00 | kJ/mol | 267.00 | NIST |
| Pvap | [1476.00; 4891.00] | kPa | [233.73; 280.98] |
|
|
T(K) Vapor pressure (kPa) 1500 2000 2500 3000 3500 4000 4500 5000 240 260 280 | ||||
| Pvap | 1476.00 | kPa | 233.73 | Vapor-L... |
| Pvap | 1932.30 | kPa | 243.08 | Vapor-L... |
| Pvap | 2534.80 | kPa | 253.22 | Vapor-L... |
| Pvap | 2732.00 | kPa | 256.22 | Isother... |
| Pvap | 2903.00 | kPa | 258.59 | Isother... |
| Pvap | 3083.00 | kPa | 261.02 | Isother... |
| Pvap | 3247.50 | kPa | 263.22 | Vapor-L... |
| Pvap | 3272.00 | kPa | 263.48 | Isother... |
| Pvap | 3470.00 | kPa | 265.94 | Isother... |
| Pvap | 3648.50 | kPa | 268.13 | Vapor-l... |
| Pvap | 3671.00 | kPa | 268.37 | Isother... |
| Pvap | 3891.00 | kPa | 270.85 | Isother... |
| Pvap | 4094.00 | kPa | 273.15 | Phase e... |
| Pvap | 4102.00 | kPa | 273.18 | Vapor-L... |
| Pvap | 4113.00 | kPa | 273.29 | Isother... |
| Pvap | 4339.00 | kPa | 275.68 | Isother... |
| Pvap | 4588.00 | kPa | 278.16 | Isother... |
| Pvap | 4611.20 | kPa | 278.36 | Vapor-l... |
| Pvap | 4891.00 | kPa | 280.98 | Isother... |
| ρl | 577.00 | kg/m3 | 163.00 | KDB |
| ΔfusS | [32.23; 32.23] | J/mol×K | [103.95; 103.97] |
|
| ΔfusS | 32.23 | J/mol×K | 103.95 | NIST |
| ΔfusS | 32.23 | J/mol×K | 103.97 | NIST |
| γ | 0.02 | N/m | 133.20 | KDB |
| ΔvapS | 79.95 | J/mol×K | 169.40 | NIST |
| λ | [0.02; 0.04] | W/m×K | [283.47; 425.62] |
|
|
T(K) Gas thermal conductivity (W/m×K) 0.02 0.03 0.03 0.04 0.04 300 350 400 | ||||
| λ | 0.02 | W/m×K | 283.47 | Measure... |
| λ | 0.02 | W/m×K | 283.96 | Measure... |
| λ | 0.02 | W/m×K | 284.89 | Measure... |
| λ | 0.02 | W/m×K | 302.21 | Measure... |
| λ | 0.02 | W/m×K | 303.10 | Measure... |
| λ | 0.04 | W/m×K | 425.00 | Measure... |
| λ | 0.04 | W/m×K | 425.62 | Measure... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.14; 5057.85] | kPa | [104.00; 282.35] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.40310e+01 | |||
| Coefficient B | -1.49623e+03 | |||
| Coefficient C | -1.04200e+01 | |||
| Temperature range, min. | 104.00 | |||
| Temperature range, max. | 282.35 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 100 150 200 250 | ||||
| Pvap | 0.14 | kPa | 104.00 | Calculated Property |
| Pvap | 2.31 | kPa | 123.82 | Calculated Property |
| Pvap | 16.43 | kPa | 143.63 | Calculated Property |
| Pvap | 70.36 | kPa | 163.45 | Calculated Property |
| Pvap | 215.84 | kPa | 183.27 | Calculated Property |
| Pvap | 525.80 | kPa | 203.08 | Calculated Property |
| Pvap | 1084.87 | kPa | 222.90 | Calculated Property |
| Pvap | 1978.17 | kPa | 242.72 | Calculated Property |
| Pvap | 3282.00 | kPa | 262.53 | Calculated Property |
| Pvap | 5057.85 | kPa | 282.35 | Calculated Property |
| Pvap | [0.13; 5023.31] | kPa | [104.01; 282.36] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 4.31991e+01 | |||
| Coefficient B | -2.35577e+03 | |||
| Coefficient C | -4.89843e+00 | |||
| Coefficient D | 1.64142e-05 | |||
| Temperature range, min. | 104.01 | |||
| Temperature range, max. | 282.36 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 100 150 200 250 | ||||
| Pvap | 0.13 | kPa | 104.01 | Calculated Property |
| Pvap | 2.27 | kPa | 123.83 | Calculated Property |
| Pvap | 16.54 | kPa | 143.64 | Calculated Property |
| Pvap | 70.85 | kPa | 163.46 | Calculated Property |
| Pvap | 215.10 | kPa | 183.28 | Calculated Property |
| Pvap | 517.00 | kPa | 203.09 | Calculated Property |
| Pvap | 1055.47 | kPa | 222.91 | Calculated Property |
| Pvap | 1917.59 | kPa | 242.73 | Calculated Property |
| Pvap | 3201.28 | kPa | 262.54 | Calculated Property |
| Pvap | 5023.31 | kPa | 282.36 | Calculated Property |
Similar Compounds
Find more compounds similar to Ethylene.
Mixtures
- Butane, decafluoro- + Ethylene
- Propene, hexafluoro- + Ethylene
- Perfluorooctane + Ethylene
- Heptane, hexadecafluoro- + Ethylene
- Ethylene + nonane, eicosafluoro-
- Ethylene + Difluorochloromethane
- Carbon monoxide + Ethylene
- 1-Propanol, 2-methyl- + Ethylene
- Hydrogen + Ethylene
- Toluene + Ethylene
- Eicosane + Ethylene
- 1-Butanol + Ethylene
- Ethanol, 2,2,2-trifluoro- + Ethylene + Water
- Toluene + 2-Norbornene + Ethylene
- 2-Norbornene + Ethylene
- Methyl propionate + Ethylene
- Ethylene + Hexafluoropropylene oxide
- Methane + Ethylene + Ethanol, 2,2'-oxybis-
- Methane + Ethylene + Water
- Ethylene + Methyl Alcohol
Find more mixtures with Ethylene.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- The experiments and correlations of the solubility of ethylene in toluene solvent
- Phase behaviour in the vicinity of the three-phase solid liquid vapour line in asymmetric nonpolar systems at high pressures
- High-pressure phase equilibrium for ethylene + 1-butanol at 283.65 K and 290.80 K
- Solubilities of several non-polar gases in mixtures water + 2,2,2-trifluoroethanol at 298.15 K and 101.33 kPa
- Phase behavior of vinyl fluoride in room-temperature ionic liquids [emim][Tf2N], [bmim][N(CN)2], [bmpy][BF4], [bmim][HFPS] and [omim][TFES]
- Vapor-liquid equilibria of ethylene (C2H4) + decafluorobutane (C4F10) at 268 to 298 K from experiment, molecular simulation and the Peng-Robinson equation of state
- Solubility of ethylene in toluene, norbornene, and toluene + norbornene mixture
- Isothermal vapor-liquid equilibrium data for the ethylene + 1,1,2,3,3,3-hexafluoro-1-propene binary system between 258 and 308 K at pressures up to 4.56 MPa
- Solubility of ethylene in methyl propionate
- Isothermal vapor liquid equilibrium data for the ethene + 2,2,3- trifluoro-3-(trifluoromethyl)oxirane binary system between 258 and 308 K at pressures up to 4.5MPa
- High-pressure phase equilibria data for mixtures involving ethene and perfluoro-n-octane from 293 to 353 K
- Separation of methane/ethylene gas mixtures efficiently by using ZIF- 67/water-ethylene glycol slurry
- Binary vapour-liquid equilibrium data for C7 and C9 straight-chain perfluorocarbons with ethylene
- Measurement and prediction of phase equilibria of ethylene + vinyl acetate + methanol + poly(ethylene-co-vinyl acetate) systems
- Phase behavior and densities of propylene + toluene and ethylene + toluene systems to 580 K and 70 MPa
- Phase equilibrium and critical point data for ethylene and chlorodifluoromethane binary mixtures using a new static-analytic apparatus
- Measurements of the thermal conductivity of ethene in the supercritical region
- Measurement and prediction of phase equilibria of ethylene + methyl acrylate + poly(ethylene-co-methyl acrylate) systems
- Mixture densities and viscosities of toluene with ethylene or propylene at temperatures to 530 K and pressures to 70 MPa
- Solubility of gases in fluoroorganic alcohols. Part III. Solubilities of several non-polar gases in water + 1,1,1,3,3,3-hexafluoropropan-2-ol at 298.15 K and 101.33 kPa
- Solubilities of gases in cycloethers. The solubility of 13 nonpolar gases in 2,5-dimethyltetrahydrofuran at 273.15 to 303.15 K and 101.32 kPa
- Solubility of Ethene in n-Hexane and n-Heptane as Common Slurry-Phase Polymerization Solvents: Experimental Measurement and Modeling
- Influence of a-Olefin Concentration and Length on the High-Pressure Phase Behavior of (a-Olefin + n-Hexane + LLDPE) Systems
- Solubilities of Nonpolar Gases in Triethylene Glycol Dimethyl Ether, Tetraethylene Glycol Dimethyl Ether, Dimethyl Carbonate, and Diethyl Carbonate at 298.15 K and 101.33 kPa Partial Pressure of Gas
- High-Pressure Phase Equilibrium for Ethylene + Ethanol at 283.65 K
- Vapor-Liquid Equilibrium Data for the Ethylene + Hexane System
- High-Pressure Phase Equilibrium for Ethylene + 2-Propanol at 283.65 K
- High-Pressure Phase Equilibrium for Ethylene + Methanol at 278.15 K and 283.65 K
- Solubility of Ethylene in 2,2,4-Trimethylpentane at Various Temperatures and Pressures
- High-Pressure Multiphase Behavior of the Ternary Systems (Ethene + Water + Acetone) and (Ethane + Water + Acetone)
- Vapor-Liquid Equilibrium (PTxy) Measurements and Modeling for the CO-C2H4 Binary System
- Solubilities of the Gaseous and Liquid Solutes and Their Thermodynamics of Solubilization in the Novel Room-Temperature Ionic Liquids at Infinite Dilution by Gas Chromatography
- High-Pressure Vapor-Liquid Equilibrium for Ethylene + 2-Methyl-1-propanol
- Gas-Liquid Critical Properties of Ethylene + Hydrogen and Propylene + Hydrogen Binary Mixtures
- 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.