- InChI
- InChI=1S/C2Cl4/c3-1(4)2(5)6
- InChI Key
- CYTYCFOTNPOANT-UHFFFAOYSA-N
- Formula
- C2Cl4
- SMILES
- ClC(Cl)=C(Cl)Cl
- Molecular Weight1
- 165.83
- CAS
- 127-18-4
- Other Names
-
- 1,1,2,2-Tetrachloroethene
- 1,1,2,2-Tetrachloroethylene
- Ankilostin
- Antisal 1
- Antisol 1
- C2Cl4
- Carbon bichloride
- Carbon dichloride
- Czterochloroetylen
- Didakene
- Dilatin PT
- Dow-per
- ENT 1,860
- ETHYLENE TETRACHLORIDE
- Ethene, tetrachloro-
- Ethylene, tetrachloro-
- F 1110
- Fedal-Un
- Freon 1110
- NCI-C04580
- Nema
- Nema, veterinary
- PERC
- PERK
- PerSec
- Perawin
- Perchloorethyleen, per
- Perchlor
- Perchloraethylen, per
- Perchlorethylene
- Perchlorethylene, per
- Perchloroethene
- Perchloroethylene
- Perclene
- Perclene D
- Perclene TG
- Percloroetilene
- Percosolve
- Perklone
- RCRA Waste Number U210
- TETLEN
- TETRACHLOROETHENE
- Tetracap
- Tetrachlooretheen
- Tetrachloraethen
- Tetrachlorethylene
- Tetracloroetene
- Tetraguer
- Tetraleno
- Tetralex
- Tetravec
- Tetroguer
- Tetropil
- UN 1897
- 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).
- EA : Electron affinity (eV).
- 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).
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- 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).
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- 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 | 0.2272 | Relay (1.0) Calculated Property | |
| ΔcH°liquid | -830.00 ± 10.00 | kJ/mol | NIST |
| μ | 0.00 | debye | KDB |
| η | [0.0008474; 0.0008900] | Pa×s |
|
| η | 0.0008474 | Pa×s | Densities and Viscosities of Binary Liquid Mixtures of Trichloroethylene and Tetrachloroethylene with Some Polar and Nonpolar Solvents |
| η | 0.0008900 | Pa×s | Studies on Transport and Thermodynamic Properties of Binary Mixtures of Hexan-1-ol with Halogenated Compounds at 293.15 K |
| EA | [0.50; 0.64] | eV |
|
| EA | 0.64 ± 0.03 | eV | NIST |
| EA | 0.50 | eV | NIST |
| ΔfG° | 22.61 | kJ/mol | KDB |
| ΔfH°gas | [-24.00; -12.14] | kJ/mol |
|
| ΔfH°gas | -12.14 | kJ/mol | KDB |
| ΔfH°gas | -24.00 ± 4.00 | kJ/mol | NIST |
| ΔfH°gas | -15.00 | kJ/mol | NIST |
| ΔfH°liquid | [-64.00; -54.40] | kJ/mol |
|
| ΔfH°liquid | -64.00 ± 4.00 | kJ/mol | NIST |
| ΔfH°liquid | -54.40 | kJ/mol | NIST |
| ΔfusH° | 15.31 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [39.70; 39.72] | kJ/mol |
|
| ΔvapH° | 39.72 | kJ/mol | NIST |
| ΔvapH° | 39.72 ± 0.05 | kJ/mol | NIST |
| ΔvapH° | 39.70 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 39.70 ± 0.84 | kJ/mol | NIST |
| IE | [9.32; 9.51] | eV |
|
| IE | 9.33 ± 0.00 | eV | NIST |
| IE | 9.33 ± 0.00 | eV | NIST |
| IE | 9.51 | eV | NIST |
| IE | 9.34 | eV | NIST |
| IE | 9.32 ± 0.01 | eV | NIST |
| IE | 9.32 | eV | NIST |
| IE | 9.50 | eV | NIST |
| log10WS | [-2.60; -2.54] |
|
|
| log10WS | -2.60 | Aq. Solubility Prediction | |
| log10WS | -2.54 | Estimated Solubility | |
| logPoct/wat | 3.068 | Crippen Calculated Property | |
| McVol | 83.700 | ml/mol | McGowan Calculated Property |
| Pc | 4760.00 | kPa | KDB |
| Inp | [785.00; 832.30] |
|
|
| Inp | 825.59 | NIST | |
| Inp | Outlier 832.30 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 799.00 | NIST | |
| Inp | 801.00 | NIST | |
| Inp | 809.00 | NIST | |
| Inp | 814.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 825.00 | NIST | |
| Inp | 814.00 | NIST | |
| Inp | 801.00 | NIST | |
| Inp | 815.45 | NIST | |
| Inp | 817.10 | NIST | |
| Inp | 815.90 | NIST | |
| Inp | 794.80 | NIST | |
| Inp | 809.30 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 815.00 | NIST | |
| Inp | 796.00 | NIST | |
| Inp | 801.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 814.00 | NIST | |
| Inp | 807.00 | NIST | |
| Inp | 796.52 | NIST | |
| Inp | 819.00 | NIST | |
| Inp | 823.00 | NIST | |
| Inp | 794.00 | NIST | |
| Inp | 808.00 | NIST | |
| Inp | 814.00 | NIST | |
| Inp | 808.00 | NIST | |
| Inp | 815.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 794.51 | NIST | |
| Inp | 794.00 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 811.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 793.00 | NIST | |
| Inp | 793.00 | NIST | |
| Inp | 811.00 | NIST | |
| Inp | 797.00 | NIST | |
| Inp | 816.00 | NIST | |
| Inp | 785.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 797.00 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 796.00 | NIST | |
| Inp | 814.00 | NIST | |
| Inp | 794.00 | NIST | |
| Inp | 793.00 | NIST | |
| Inp | 785.00 | NIST | |
| Inp | 796.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 823.00 | NIST | |
| I | [1012.00; 1059.96] |
|
|
| I | 1044.00 | NIST | |
| I | 1038.00 | NIST | |
| I | 1050.23 | NIST | |
| I | Outlier 1059.96 | NIST | |
| I | 1036.20 | NIST | |
| I | 1030.00 | NIST | |
| I | 1024.00 | NIST | |
| I | 1022.00 | NIST | |
| I | 1022.00 | NIST | |
| I | 1021.00 | NIST | |
| I | 1026.00 | NIST | |
| I | 1045.00 | NIST | |
| I | 1012.00 | NIST | |
| I | 1012.00 | NIST | |
| I | 1018.00 | NIST | |
| I | 1021.00 | NIST | |
| I | 1024.00 | NIST | |
| I | 1044.00 | NIST | |
| I | 1030.00 | NIST | |
| S°liquid | 240.60 | J/mol×K | NIST |
| Tboil | [394.15; 394.45] | K |
|
| Tboil | 394.40 | K | KDB |
| Tboil | 394.45 | K | Excess volumes and speeds of sound of mixtures of 1,2-dibromoethane with chlorinated ethanes and ethenes at 303.15 K |
| Tboil | 394.15 | K | Excess molar enthalpies of dimethylsulfoxide with chloroethanes and chloroethenes at 298.15K |
| Tboil | 394.15 | K | Vapor-Liquid Equilibria and Excess Molar Enthalpies for N-Methyl-2-pyrrolidone with Chloroethanes and Chloroethenes |
| Tboil | 394.15 | K | Isobaric Vapor Liquid Equilibrium for Dimethylsulfoxide with Chloroethanes and Chloroethenes |
| Tc | [620.00; 620.20] | K |
|
| Tc | 620.20 | K | KDB |
| Tc | 620.00 | K | NIST |
| Tfus | [250.60; 251.00] | K |
|
| Tfus | 250.80 | K | KDB |
| Tfus | 251.00 | K | Aq. Solubility Prediction |
| Tfus | 250.97 ± 0.05 | K | NIST |
| Tfus | 250.60 ± 0.60 | K | NIST |
| Ttriple | 250.81 ± 0.02 | K | NIST |
| Vc | 0.298 | m3/kmol | Relay (1.0) Calculated Property |
Temperature Dependent Properties
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 308.15 | 101.00 | 0.0007 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 203.96] | kPa | [286.48; 421.37] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.42797e+01 | |||
| Coefficient B | -3.36251e+03 | |||
| Coefficient C | -4.61640e+01 | |||
| Temperature range, min. | 286.48 | |||
| Temperature range, max. | 421.37 | |||
| Pvap | 1.33 | kPa | 286.48 | Calculated Property |
| Pvap | 3.03 | kPa | 301.47 | Calculated Property |
| Pvap | 6.29 | kPa | 316.46 | Calculated Property |
| Pvap | 12.10 | kPa | 331.44 | Calculated Property |
| Pvap | 21.79 | kPa | 346.43 | Calculated Property |
| Pvap | 37.10 | kPa | 361.42 | Calculated Property |
| Pvap | 60.21 | kPa | 376.41 | Calculated Property |
| Pvap | 93.67 | kPa | 391.39 | Calculated Property |
| Pvap | 140.48 | kPa | 406.38 | Calculated Property |
| Pvap | 203.96 | kPa | 421.37 | Calculated Property |
| Pvap | [0.11; 4603.17] | kPa | [250.80; 620.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 6.04740e+01 | |||
| Coefficient B | -6.53097e+03 | |||
| Coefficient C | -6.66587e+00 | |||
| Coefficient D | 3.52238e-06 | |||
| Temperature range, min. | 250.80 | |||
| Temperature range, max. | 620.00 | |||
| Pvap | 0.11 | kPa | 250.80 | Calculated Property |
| Pvap | 1.75 | kPa | 291.82 | Calculated Property |
| Pvap | 12.55 | kPa | 332.84 | Calculated Property |
| Pvap | 55.13 | kPa | 373.87 | Calculated Property |
| Pvap | 173.62 | kPa | 414.89 | Calculated Property |
| Pvap | 432.94 | kPa | 455.91 | Calculated Property |
| Pvap | 912.80 | kPa | 496.93 | Calculated Property |
| Pvap | 1701.91 | kPa | 537.96 | Calculated Property |
| Pvap | 2896.38 | kPa | 578.98 | Calculated Property |
| Pvap | 4603.17 | kPa | 620.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Tetrachloroethylene.
Mixtures
- Tetrachloroethylene + 1-Hexanol
- Benzene + Tetrachloroethylene
- Tetrachloroethylene + Carbon Tetrachloride
- Phenol, 2-methyl- + Tetrachloroethylene
- Tetrachloroethylene + Formamide, N,N-dimethyl-
- Tetrachloroethylene + Ethane, 1,2-dibromo-
- Tetrachloroethylene + Tetrahydrofuran
- Tetrachloroethylene + Ethylbenzene
- Tetrachloroethylene + Acetamide, N-methyl-
- Tetrachloroethylene + Cyclohexane, methyl-
- p-Cresol + Tetrachloroethylene
- Tetrachloroethylene + 1-Decanol
- Tetrachloroethylene + Dimethyl Sulfoxide
- Tetrachloroethylene + 2-Pyrrolidinone, 1-methyl-
- Tetrachloroethylene + Heptane
- Benzene, nitro- + Tetrachloroethylene
- Tetrachloroethylene + Benzene, chloro-
- Tetrachloroethylene + Tributylamine
- Tetrachloroethylene + Methyl Alcohol
- Tetrachloroethylene + Ethanol
Find more mixtures with Tetrachloroethylene.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Cheméo Relay (1.0)
- Crippen Method
- Densities, Excess Molar Volumes, Ultrasonic Speeds, and Isentropic Compressibilities of Hexan-1-ol with 1,2-Dichloroethane, 1,2-Dibromoethane, and 1,1,2,2-Tetrachloroethene at (293.15 and 298.15) K
- Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachlorethane or tetrachloroethene with benzene at nine temperatures
- Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachloroethane or tetrachloroethene with tetrachloromethane at nine temperatures
- Bubble points of some binary mixtures formed by o-cresol at 95.75 kPa
- Excess Gibbs energies of selected binary mixtures formed by N,N-dimethyl formamide at 95.5 kPa
- Excess volumes and speeds of sound of mixtures of 1,2-dibromoethane with chlorinated ethanes and ethenes at 303.15 K
- Isothermal (vapour + liquid) equilibrium for binary mixtures of (tetrahydrofuran + 1,1,2,2-tetrachloroethane or tetrachloroethene) at nine temperatures
- Bubble points of the binary mixtures formed by ethylbenzene with some chloroaliphatics and substituted benzenes at p = 94.7 kPa
- Densities and viscosities of binary liquid mixtures of N-methylacetamide with some chloroethanes and chloroethenes at T = 308.15 K
- Excess molar volumes, viscosities, and speeds of sound of the ternary mixture {1-heptanol (1) + trichloroethylene (2) + methylcyclohexane (3)} at T = 298.15 K
- Activity coefficients and excess Gibbs free energy of some binary mixtures formed by p-cresol at 95.23 kPa
- Thermophysical and sonochemical behaviour of binary mixtures of decan-1-ol with halohydrocarbons at (T = 293.15 and 313.15) K
- Relation between characteristic molecular volume and hydrophobicity of nonpolar molecules
- Excess molar enthalpies of dimethylsulfoxide with chloroethanes and chloroethenes at 298.15K
- Vapor-Liquid Equilibria and Excess Molar Enthalpies for N-Methyl-2-pyrrolidone with Chloroethanes and Chloroethenes
- Bubble Temperature Measurements on the Binary Mixtures of n-Heptane or Nitrobenzene or Chlorobenzene with Some Chloroethanes and Chloroethylenes at (94.6 to 95.8) kPa
- Bubble-Temperature Measurements on Some Binary Mixtures Formed by Tetrahydrofuran or Amyl Alcohol with Hydrocarbons, Chlorohydrocarbons, or Butanols at (94.6 or 95.8) kPa
- Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of Tri-n-butylamine + Triethylamine, + Tetrahydrofuran, + Tetradecane, + Tetrachloroethylene, + Pyridine, or + Trichloroethylene at (298.15, 303.15, and 308.15) K
- Densities and Viscosities of Binary Liquid Mixtures of Trichloroethylene and Tetrachloroethylene with Some Polar and Nonpolar Solvents
- Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of Anisole with 2-Chloroethanol, 1,4-Dioxane, Tetrachloroethylene, Tetrachloroethane, DMF, DMSO, and Diethyl Oxalate at (298.15, 303.15, and 308.15) K
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Isobaric Vapor Liquid Equilibrium for Dimethylsulfoxide with Chloroethanes and Chloroethenes
- Vapor-Liquid Equilibria of Binary Mixtures Formed by Hexan-1-ol with Chloroethanes and Chloroethenes at 95.6 kPa
- Studies on Transport and Thermodynamic Properties of Binary Mixtures of Hexan-1-ol with Halogenated Compounds at 293.15 K
- Excess Molar Volumes and Sound Speed in (Phenylacetonitrile + 1,2-Dichloroethane), (Phenylacetonitrile + 1,1,2-Trichloroethane), (Phenylacetonitrile + 1,1,2,2-Tetrachloroethane), (Phenylacetonitrile + Trichloroethene), and (Phenylacetonitrile + Tetrachloroethene) at Temperatures of (303.15, 308.15, and 313.15) K
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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