- InChI
- InChI=1S/C2H2Cl2/c3-1-2-4/h1-2H/b2-1+
- InChI Key
- KFUSEUYYWQURPO-OWOJBTEDSA-N
- Formula
- C2H2Cl2
- SMILES
- ClC=CCl
- Molecular Weight1
- 96.94
- CAS
- 156-60-5
- Other Names
-
- (E)-1,2-DICHLOROETHYLENE
- (E)-1,2-Dichloroethene
- (E)-CHCl=CHCl
- 1,2-trans-Dichloroethene
- 1,2-trans-Dichloroethylene
- 1,trans-2-Dichloroethene
- Dichloroethylene, trans-
- Ethene, 1,2-dichloro-, (1E)-
- Ethene, 1,2-dichloro-, (E)-
- Ethylene, 1,2-dichloro-, trans-
- HCC 1130t
- NSC 60512
- R 1130t
- Rcra waste number U079
- TRANS-1,2-DICHLOROETHENE
- TRANS-1,2-DICHLOROETHYLENE
- TRANS-ACETYLENE DICHLORIDE
- ethene, 1,2-dichloro-, trans-
- trans-Di-1,2-Chloroethylene
- trans-Dichloroethylene
- 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.
- NFPA Health : NFPA Health Rating.
- NFPA Safety : NFPA Safety Rating.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 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 | 0.2320 | KDB | |
| ΔcH°liquid | -1095.80 ± 8.40 | kJ/mol | NIST |
| μ | 0.00 | debye | KDB |
| ΔfG° | 26.60 | kJ/mol | KDB |
| ΔfH°gas | [-1.00; 4.19] | kJ/mol |
|
| ΔfH°gas | 4.19 | kJ/mol | KDB |
| ΔfH°gas | -1.00 ± 2.00 | kJ/mol | NIST |
| ΔfH°gas | 1.70 | kJ/mol | NIST |
| ΔfH°liquid | [-30.00; -14.34] | kJ/mol |
|
| ΔfH°liquid | -30.00 ± 2.20 | kJ/mol | NIST |
| ΔfH°liquid | -14.34 | kJ/mol | NIST |
| ΔfusH° | 9.53 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [29.47; 30.00] | kJ/mol |
|
| ΔvapH° | 30.00 ± 1.00 | kJ/mol | NIST |
| ΔvapH° | 29.47 | kJ/mol | NIST |
| IE | [9.60; 11.92] | eV |
|
| IE | 9.64 ± 0.02 | eV | NIST |
| IE | 9.64 | eV | NIST |
| IE | 9.69 | eV | NIST |
| IE | 9.60 | eV | NIST |
| IE | 9.66 ± 0.03 | eV | NIST |
| IE | 9.64 ± 0.02 | eV | NIST |
| IE | 9.63 | eV | NIST |
| IE | 9.80 | eV | NIST |
| IE | 9.80 | eV | NIST |
| IE | Outlier 11.92 | eV | NIST |
| IE | 9.72 | eV | NIST |
| log10WS | -1.81 | Crippen Calculated Property | |
| logPoct/wat | 1.935 | Crippen Calculated Property | |
| McVol | 59.220 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 2 | KDB | |
| NFPA Safety | 2 | KDB | |
| Pc | 5510.00 | kPa | KDB |
| Inp | [528.00; 596.00] |
|
|
| Inp | 558.00 | NIST | |
| Inp | 559.00 | NIST | |
| Inp | 557.00 | NIST | |
| Inp | 555.00 | NIST | |
| Inp | 559.00 | NIST | |
| Inp | Outlier 528.00 | NIST | |
| Inp | 551.00 | NIST | |
| Inp | 551.00 | NIST | |
| Inp | Outlier 596.00 | NIST | |
| Inp | 567.00 | NIST | |
| Inp | 558.00 | NIST | |
| Inp | 551.00 | NIST | |
| I | [863.21; 870.00] |
|
|
| I | 867.61 | NIST | |
| I | 866.47 | NIST | |
| I | 863.21 | NIST | |
| I | 870.00 | NIST | |
| I | 870.00 | NIST | |
| Tboil | [320.45; 322.70] | K |
|
| Tboil | 321.88 | K | KDB |
| Tboil | 320.70 | K | NIST |
| Tboil | 320.45 ± 0.25 | K | NIST |
| Tboil | 320.50 ± 0.40 | K | NIST |
| Tboil | 321.40 ± 0.60 | K | NIST |
| Tboil | 321.40 ± 0.70 | K | NIST |
| Tboil | 322.70 ± 2.00 | K | NIST |
| Tc | 516.50 | K | KDB |
| Tfus | [223.00; 223.30] | K |
|
| Tfus | 223.30 | K | KDB |
| Tfus | 223.00 ± 0.10 | K | NIST |
| Vc | 0.226 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [67.02; 84.99] | J/mol×K | [324.18; 517.06] |
|
| Cp,gas | 67.02 | J/mol×K | 324.18 | Joback Calculated Property |
| Cp,gas | 70.61 | J/mol×K | 356.33 | Joback Calculated Property |
| Cp,gas | 73.95 | J/mol×K | 388.47 | Joback Calculated Property |
| Cp,gas | 77.04 | J/mol×K | 420.62 | Joback Calculated Property |
| Cp,gas | 79.90 | J/mol×K | 452.76 | Joback Calculated Property |
| Cp,gas | 82.55 | J/mol×K | 484.91 | Joback Calculated Property |
| Cp,gas | 84.99 | J/mol×K | 517.06 | Joback Calculated Property |
| Cp,liquid | [112.08; 115.07] | J/mol×K | [268.30; 309.14] |
|
| Cp,liquid | 113.08 | J/mol×K | 268.30 | Heat ca... |
| Cp,liquid | 112.74 | J/mol×K | 268.30 | Heat ca... |
| Cp,liquid | 112.41 | J/mol×K | 268.30 | Heat ca... |
| Cp,liquid | 112.08 | J/mol×K | 268.30 | Heat ca... |
| Cp,liquid | 112.99 | J/mol×K | 278.51 | Heat ca... |
| Cp,liquid | 112.83 | J/mol×K | 278.51 | Heat ca... |
| Cp,liquid | 112.41 | J/mol×K | 278.51 | Heat ca... |
| Cp,liquid | 112.08 | J/mol×K | 278.51 | Heat ca... |
| Cp,liquid | 113.00 | J/mol×K | 288.00 | NIST |
| Cp,liquid | 113.41 | J/mol×K | 288.72 | Heat ca... |
| Cp,liquid | 113.49 | J/mol×K | 288.72 | Heat ca... |
| Cp,liquid | 112.58 | J/mol×K | 288.72 | Heat ca... |
| Cp,liquid | 112.91 | J/mol×K | 288.72 | Heat ca... |
| Cp,liquid | 114.24 | J/mol×K | 298.93 | Heat ca... |
| Cp,liquid | 113.99 | J/mol×K | 298.93 | Heat ca... |
| Cp,liquid | 113.41 | J/mol×K | 298.93 | Heat ca... |
| Cp,liquid | 113.82 | J/mol×K | 298.93 | Heat ca... |
| Cp,liquid | 115.07 | J/mol×K | 309.14 | Heat ca... |
| Cp,liquid | 114.49 | J/mol×K | 309.14 | Heat ca... |
| Cp,liquid | 114.16 | J/mol×K | 309.14 | Heat ca... |
| Cp,liquid | 113.66 | J/mol×K | 309.14 | Heat ca... |
| η | [0.0002698; 0.0028927] | Pa×s | [167.06; 324.18] |
|
| η | 0.0028927 | Pa×s | 167.06 | Joback Calculated Property |
| η | 0.0014903 | Pa×s | 193.25 | Joback Calculated Property |
| η | 0.0008995 | Pa×s | 219.43 | Joback Calculated Property |
| η | 0.0006046 | Pa×s | 245.62 | Joback Calculated Property |
| η | 0.0004387 | Pa×s | 271.81 | Joback Calculated Property |
| η | 0.0003368 | Pa×s | 297.99 | Joback Calculated Property |
| η | 0.0002698 | Pa×s | 324.18 | Joback Calculated Property |
| ΔvapH | [29.00; 31.40] | kJ/mol | [293.00; 397.00] |
|
| ΔvapH | 30.40 | kJ/mol | 293.00 | NIST |
| ΔvapH | 30.10 | kJ/mol | 296.00 | NIST |
| ΔvapH | 31.40 | kJ/mol | 296.50 | NIST |
| ΔvapH | 30.30 | kJ/mol | 321.50 | KDB |
| ΔvapH | 29.00 | kJ/mol | 397.00 | NIST |
| Pvap | [53.33; 269.90] | kPa | [303.15; 353.15] |
|
| Pvap | 53.33 | kPa | 303.15 | Phase E... |
| Pvap | 269.90 | kPa | 353.15 | Phase E... |
| ρl | 1255.00 | kg/m3 | 293.00 | KDB |
| γ | 0.02 | N/m | 293.20 | KDB |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.52; 6698.23] | kPa | [223.35; 516.50] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.50408e+01 | |||
| Coefficient B | -3.02933e+03 | |||
| Coefficient C | -3.03460e+01 | |||
| Temperature range, min. | 223.35 | |||
| Temperature range, max. | 516.50 | |||
| Pvap | 0.52 | kPa | 223.35 | Calculated Property |
| Pvap | 5.01 | kPa | 255.92 | Calculated Property |
| Pvap | 27.28 | kPa | 288.49 | Calculated Property |
| Pvap | 101.57 | kPa | 321.07 | Calculated Property |
| Pvap | 290.20 | kPa | 353.64 | Calculated Property |
| Pvap | 684.19 | kPa | 386.21 | Calculated Property |
| Pvap | 1396.96 | kPa | 418.78 | Calculated Property |
| Pvap | 2554.01 | kPa | 451.36 | Calculated Property |
| Pvap | 4281.80 | kPa | 483.93 | Calculated Property |
| Pvap | 6698.23 | kPa | 516.50 | Calculated Property |
| Pvap | [0.62; 5421.34] | kPa | [223.35; 513.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 8.76830e+01 | |||
| Coefficient B | -6.29447e+03 | |||
| Coefficient C | -1.11957e+01 | |||
| Coefficient D | 1.15854e-05 | |||
| Temperature range, min. | 223.35 | |||
| Temperature range, max. | 513.00 | |||
| Pvap | 0.62 | kPa | 223.35 | Calculated Property |
| Pvap | 5.73 | kPa | 255.53 | Calculated Property |
| Pvap | 29.23 | kPa | 287.72 | Calculated Property |
| Pvap | 101.06 | kPa | 319.90 | Calculated Property |
| Pvap | 268.16 | kPa | 352.08 | Calculated Property |
| Pvap | 592.41 | kPa | 384.27 | Calculated Property |
| Pvap | 1150.75 | kPa | 416.45 | Calculated Property |
| Pvap | 2041.81 | kPa | 448.63 | Calculated Property |
| Pvap | 3400.32 | kPa | 480.82 | Calculated Property |
| Pvap | 5421.34 | kPa | 513.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Ethylene, 1,2-dichloro-, (E)-.
Mixtures
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Heat capacities of selected chlorohydrocarbons
- Phase Equilibria on Four Binary Systems: 1,2-Dichloroethane + trans-1,2-Dichloroethylene, 1-Octene + 2-Methyl Thiophene, 2-Ethyl Thiophene + 2,2,4-Trimethylpentane, and Cyclopropanecarbonitrile + Water
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Joback Method
- KDB
- 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.