- InChI
- InChI=1S/C2H3Cl/c1-2-3/h2H,1H2
- InChI Key
- BZHJMEDXRYGGRV-UHFFFAOYSA-N
- Formula
- C2H3Cl
- SMILES
- C=CCl
- Molecular Weight1
- 62.50
- CAS
- 75-01-4
- Other Names
-
- C2H3Cl
- CHLOROETHENE
- CHLOROETHYLENE
- Chlorethene
- Chlorethylene
- Chlorure de vinyle
- Cloruro di vinile
- Ethylene monochloride
- Ethylene, chloro-
- Monochloroethene
- Monochloroethylene
- Rcra waste number U043
- Trovidur
- UN 1086
- VC
- VCM
- Vinyl C monomer
- Vinyl chloride
- Vinyl chloride monomer
- Vinylchlorid
- Vinyle(chlorure de)
- Winylu chlorek
- ω : Acentric Factor.
- Tig : Autoignition Temperature (K).
- 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,cc : Flash Point (Closed Cup Method) (K).
- 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).
- ΔfusH : Enthalpy of fusion 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).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : 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).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.1220 | KDB | |
| Tig | 745.37 | K | KDB |
| μ | 1.45 | debye | KDB |
| LFL | 4.00 | % in Air | KDB |
| UFL | 26.00 | % in Air | KDB |
| Tflash,cc | 194.26 | K | KDB |
| ΔfG° | 51.54 | kJ/mol | KDB |
| ΔfH°gas | [21.00; 38.10] | kJ/mol |
|
| ΔfH°gas | 35.17 | kJ/mol | KDB |
| ΔfH°gas | 22.00 ± 3.00 | kJ/mol | NIST |
| ΔfH°gas | 29.00 | kJ/mol | NIST |
| ΔfH°gas | 21.00 | kJ/mol | NIST |
| ΔfH°gas | 35.30 ± 1.40 | kJ/mol | NIST |
| ΔfH°gas | 38.10 ± 0.84 | kJ/mol | NIST |
| ΔfH°liquid | 0.90 ± 3.20 | kJ/mol | NIST |
| ΔfusH° | 3.85 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 21.00 ± 1.00 | kJ/mol | NIST |
| IE | [9.98; 10.20] | eV |
|
| IE | 9.99 ± 0.02 | eV | NIST |
| IE | 9.98 ± 0.02 | eV | NIST |
| IE | 9.99 ± 0.02 | eV | NIST |
| IE | 10.01 | eV | NIST |
| IE | 10.00 | eV | NIST |
| IE | 10.00 ± 0.01 | eV | NIST |
| IE | 10.00 ± 0.01 | eV | NIST |
| IE | 10.00 ± 0.02 | eV | NIST |
| IE | 10.00 ± 0.01 | eV | NIST |
| IE | 9.99 | eV | NIST |
| IE | 10.00 ± 0.01 | eV | NIST |
| IE | Outlier 10.20 | eV | NIST |
| IE | Outlier 10.20 | eV | NIST |
| IE | 10.15 | eV | NIST |
| log10WS | [-1.75; -1.75] |
|
|
| log10WS | -1.75 | Aq. Solubility Prediction | |
| log10WS | -1.75 | Estimated Solubility | |
| logPoct/wat | 1.369 | Crippen Calculated Property | |
| McVol | 46.980 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 4 | KDB | |
| NFPA Health | 2 | KDB | |
| NFPA Safety | 2 | KDB | |
| Pc | 5155.00 | kPa | KDB |
| Inp | [353.00; 378.00] |
|
|
| Inp | 362.00 | NIST | |
| Inp | 363.00 | NIST | |
| Inp | 364.00 | NIST | |
| Inp | 366.00 | NIST | |
| Inp | 366.00 | NIST | |
| Inp | Outlier 378.00 | NIST | |
| Inp | 353.00 | NIST | |
| Inp | 366.00 | NIST | |
| I | [505.00; 603.00] |
|
|
| I | 603.00 | NIST | |
| I | 505.00 | NIST | |
| S°liquid | 118.00 | J/mol×K | NIST |
| Tboil | [259.05; 259.45] | K |
|
| Tboil | 259.35 | K | KDB |
| Tboil | 259.35 | K | NIST |
| Tboil | 259.45 ± 0.20 | K | NIST |
| Tboil | 259.05 ± 0.40 | K | NIST |
| Tboil | 259.30 ± 0.20 | K | NIST |
| Tc | 424.61 | K | KDB |
| Tfus | [94.43; 119.45] | K |
|
| Tfus | 119.40 | K | KDB |
| Tfus | 119.45 | K | Aq. Solubility Prediction |
| Tfus | 119.35 | K | NIST |
| Tfus | Outlier 94.43 ± 0.10 | K | NIST |
| Tfus | 119.36 ± 0.02 | K | NIST |
| Tfus | 113.50 ± 0.20 | K | NIST |
| Ttriple | 119.31 ± 0.02 | K | NIST |
| Vc | 0.167 | m3/kmol | Relay (1.0) Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [52.25; 70.09] | J/mol×K | [279.27; 453.15] |
|
| Cp,gas | 52.25 | J/mol×K | 279.27 | Joback Calculated Property |
| Cp,gas | 55.59 | J/mol×K | 308.25 | Joback Calculated Property |
| Cp,gas | 58.78 | J/mol×K | 337.23 | Joback Calculated Property |
| Cp,gas | 61.82 | J/mol×K | 366.21 | Joback Calculated Property |
| Cp,gas | 64.71 | J/mol×K | 395.19 | Joback Calculated Property |
| Cp,gas | 67.47 | J/mol×K | 424.17 | Joback Calculated Property |
| Cp,gas | 70.09 | J/mol×K | 453.15 | Joback Calculated Property |
| Cp,liquid | 89.45 | J/mol×K | 298.15 | NIST |
| η | [0.0002043; 0.0017378] | Pa×s | [140.46; 279.27] |
|
| η | 0.0017378 | Pa×s | 140.46 | Joback Calculated Property |
| η | 0.0009451 | Pa×s | 163.59 | Joback Calculated Property |
| η | 0.0005978 | Pa×s | 186.73 | Joback Calculated Property |
| η | 0.0004183 | Pa×s | 209.87 | Joback Calculated Property |
| η | 0.0003142 | Pa×s | 233.00 | Joback Calculated Property |
| η | 0.0002485 | Pa×s | 256.13 | Joback Calculated Property |
| η | 0.0002043 | Pa×s | 279.27 | Joback Calculated Property |
| ΔfusH | [4.92; 4.92] | kJ/mol | [119.30; 119.31] |
|
| ΔfusH | 4.92 | kJ/mol | 119.30 | NIST |
| ΔfusH | 4.92 | kJ/mol | 119.30 | NIST |
| ΔfusH | 4.92 | kJ/mol | 119.31 | NIST |
| ΔvapH | [22.26; 23.30] | kJ/mol | [234.50; 265.50] |
|
| ΔvapH | 23.30 | kJ/mol | 234.50 | NIST |
| ΔvapH | 22.90 | kJ/mol | 243.00 | NIST |
| ΔvapH | 22.26 | kJ/mol | 259.40 | KDB |
| ΔvapH | 22.70 | kJ/mol | 265.50 | NIST |
| Pvap | [172.00; 601.50] | kPa | [273.10; 313.15] |
|
| Pvap | 172.00 | kPa | 273.10 | Vapor-Liquid Equilibria on Seven Binary Systems: Ethylene Oxide + 2-Methylpropane; Acetophenone + Phenol; cis-1,3-Dichloropropene + 1,2-Dichloropropane; 1,5-Hexadiene + Allyl Chloride; Isopropyl Acetate + Acetonitrile; Vinyl Chloride + Methyl Chloride; and 1,4-Butanediol + c-Butyrolactone |
| Pvap | 601.50 | kPa | 313.15 | Vapor-Liquid Equilibria on Seven Binary Systems: Ethylene Oxide + 2-Methylpropane; Acetophenone + Phenol; cis-1,3-Dichloropropene + 1,2-Dichloropropane; 1,5-Hexadiene + Allyl Chloride; Isopropyl Acetate + Acetonitrile; Vinyl Chloride + Methyl Chloride; and 1,4-Butanediol + c-Butyrolactone |
| ρl | 969.00 | kg/m3 | 259.00 | KDB |
| ΔfusS | 41.20 | J/mol×K | 119.31 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.69] | kPa | [187.41; 277.61] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.38927e+01 | |||
| Coefficient B | -2.09601e+03 | |||
| Coefficient C | -3.33500e+01 | |||
| Temperature range, min. | 187.41 | |||
| Temperature range, max. | 277.61 | |||
| Pvap | 1.33 | kPa | 187.41 | Calculated Property |
| Pvap | 3.06 | kPa | 197.43 | Calculated Property |
| Pvap | 6.38 | kPa | 207.45 | Calculated Property |
| Pvap | 12.30 | kPa | 217.48 | Calculated Property |
| Pvap | 22.13 | kPa | 227.50 | Calculated Property |
| Pvap | 37.59 | kPa | 237.52 | Calculated Property |
| Pvap | 60.77 | kPa | 247.54 | Calculated Property |
| Pvap | 94.12 | kPa | 257.57 | Calculated Property |
| Pvap | 140.40 | kPa | 267.59 | Calculated Property |
| Pvap | 202.69 | kPa | 277.61 | Calculated Property |
| Pvap | [1.65e-05; 5873.76] | kPa | [119.36; 432.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 9.48913e+01 | |||
| Coefficient B | -5.42760e+03 | |||
| Coefficient C | -1.26907e+01 | |||
| Coefficient D | 1.80238e-05 | |||
| Temperature range, min. | 119.36 | |||
| Temperature range, max. | 432.00 | |||
| Pvap | 1.65e-05 | kPa | 119.36 | Calculated Property |
| Pvap | 0.02 | kPa | 154.10 | Calculated Property |
| Pvap | 1.32 | kPa | 188.84 | Calculated Property |
| Pvap | 17.50 | kPa | 223.57 | Calculated Property |
| Pvap | 99.05 | kPa | 258.31 | Calculated Property |
| Pvap | 340.45 | kPa | 293.05 | Calculated Property |
| Pvap | 862.76 | kPa | 327.79 | Calculated Property |
| Pvap | 1809.24 | kPa | 362.52 | Calculated Property |
| Pvap | 3375.42 | kPa | 397.26 | Calculated Property |
| Pvap | 5873.76 | kPa | 432.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Ethene, chloro-.
Mixtures
Sources
- KDB Vapor Pressure Data
- Cheméo Relay (1.0)
- Crippen Method
- Vapor-Liquid Equilibria on Seven Binary Systems: Ethylene Oxide + 2-Methylpropane; Acetophenone + Phenol; cis-1,3-Dichloropropene + 1,2-Dichloropropane; 1,5-Hexadiene + Allyl Chloride; Isopropyl Acetate + Acetonitrile; Vinyl Chloride + Methyl Chloride; and 1,4-Butanediol + c-Butyrolactone
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Low Pressure Solubilities of Vinyl Chloride in Ionic Liquids
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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