- InChI
- InChI=1S/C2H2Cl4/c3-1-2(4,5)6/h1H2
- InChI Key
- QVLAWKAXOMEXPM-UHFFFAOYSA-N
- Formula
- C2H2Cl4
- SMILES
- ClCC(Cl)(Cl)Cl
- Molecular Weight1
- 167.85
- CAS
- 630-20-6
- Other Names
-
- 1,1,1,2-Tetrachloroethane
- CH2ClCCl3
- NCI-C52459
- R-130a
- REFRIGERANT-130A
- Rcra waste number U208
- freon 130a
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- 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).
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- 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.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | -973.90 ± 1.30 | kJ/mol | NIST |
| ΔfG° | -78.92 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-152.30; -135.60] | kJ/mol |
|
| ΔfH°gas | -152.30 ± 2.40 | kJ/mol | NIST |
| ΔfH°gas | -135.60 | kJ/mol | NIST |
| ΔfH°liquid | [-193.50; -178.00] | kJ/mol |
|
| ΔfH°liquid | -193.40 ± 2.30 | kJ/mol | NIST |
| ΔfH°liquid | -193.50 ± 1.40 | kJ/mol | NIST |
| ΔfH°liquid | -178.00 | kJ/mol | NIST |
| ΔfusH° | 10.31 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [41.10; 45.70] | kJ/mol |
|
| ΔvapH° | 41.10 ± 0.50 | kJ/mol | NIST |
| ΔvapH° | 45.70 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 42.17 | kJ/mol | NIST |
| IE | [11.10; 11.45] | eV |
|
| IE | 11.10 | eV | NIST |
| IE | 11.45 | eV | NIST |
| log10WS | [-2.18; -2.18] |
|
|
| log10WS | -2.18 | Aq. Sol... | |
| log10WS | -2.18 | Estimat... | |
| logPoct/wat | 2.595 | Crippen Calculated Property | |
| McVol | 88.000 | ml/mol | McGowan Calculated Property |
| Pc | 4222.04 | kPa | Joback Calculated Property |
| Inp | [821.50; 870.00] |
|
|
| Inp | 840.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 833.00 | NIST | |
| Inp | 821.50 | NIST | |
| Inp | 825.00 | NIST | |
| Inp | 827.20 | NIST | |
| Inp | 837.00 | NIST | |
| Inp | 835.00 | NIST | |
| Inp | 837.00 | NIST | |
| Inp | 843.00 | NIST | |
| Inp | Outlier 869.00 | NIST | |
| Inp | 843.00 | NIST | |
| Inp | Outlier 870.00 | NIST | |
| Inp | 833.00 | NIST | |
| Inp | 837.00 | NIST | |
| Inp | 843.00 | NIST | |
| I | [1255.00; 1283.29] |
|
|
| I | 1276.65 | NIST | |
| I | 1283.29 | NIST | |
| I | 1267.53 | NIST | |
| I | 1261.00 | NIST | |
| I | 1255.00 | NIST | |
| I | 1255.00 | NIST | |
| I | 1261.00 | NIST | |
| Tboil | [402.95; 411.20] | K |
|
| Tboil | 411.20 | K | NIST |
| Tboil | 403.70 | K | NIST |
| Tboil | 402.95 ± 0.20 | K | NIST |
| Tc | 607.53 | K | Joback Calculated Property |
| Tfus | 203.08 | K | Aq. Sol... |
| Vc | 0.333 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [119.32; 140.97] | J/mol×K | [391.65; 607.53] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 120 125 130 135 140 400 500 600 | ||||
| Cp,gas | 119.32 | J/mol×K | 391.65 | Joback Calculated Property |
| Cp,gas | 124.00 | J/mol×K | 427.63 | Joback Calculated Property |
| Cp,gas | 128.21 | J/mol×K | 463.61 | Joback Calculated Property |
| Cp,gas | 131.98 | J/mol×K | 499.59 | Joback Calculated Property |
| Cp,gas | 135.34 | J/mol×K | 535.57 | Joback Calculated Property |
| Cp,gas | 138.33 | J/mol×K | 571.55 | Joback Calculated Property |
| Cp,gas | 140.97 | J/mol×K | 607.53 | Joback Calculated Property |
| η | [0.0005057; 0.0058031] | Pa×s | [234.40; 391.65] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 1.00e-3 2.00e-3 3.00e-3 4.00e-3 5.00e-3 6.00e-3 250 300 350 | ||||
| η | 0.0058031 | Pa×s | 234.40 | Joback Calculated Property |
| η | 0.0031493 | Pa×s | 260.61 | Joback Calculated Property |
| η | 0.0019111 | Pa×s | 286.82 | Joback Calculated Property |
| η | 0.0012609 | Pa×s | 313.02 | Joback Calculated Property |
| η | 0.0008871 | Pa×s | 339.23 | Joback Calculated Property |
| η | 0.0006564 | Pa×s | 365.44 | Joback Calculated Property |
| η | 0.0005057 | Pa×s | 391.65 | Joback Calculated Property |
| ΔvapH | [39.20; 40.10] | kJ/mol | [367.50; 381.50] |
|
| ΔvapH | 39.20 | kJ/mol | 367.50 | NIST |
| ΔvapH | 40.10 | kJ/mol | 381.50 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [293.76; 441.42] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.35773e+01 | |||
| Coefficient B | -3.22872e+03 | |||
| Coefficient C | -5.08100e+01 | |||
| Temperature range, min. | 293.76 | |||
| Temperature range, max. | 441.42 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
| Pvap | 1.33 | kPa | 293.76 | Calculated Property |
| Pvap | 3.09 | kPa | 310.17 | Calculated Property |
| Pvap | 6.48 | kPa | 326.57 | Calculated Property |
| Pvap | 12.51 | kPa | 342.98 | Calculated Property |
| Pvap | 22.51 | kPa | 359.39 | Calculated Property |
| Pvap | 38.18 | kPa | 375.79 | Calculated Property |
| Pvap | 61.54 | kPa | 392.20 | Calculated Property |
| Pvap | 94.96 | kPa | 408.61 | Calculated Property |
| Pvap | 141.04 | kPa | 425.01 | Calculated Property |
| Pvap | 202.65 | kPa | 441.42 | Calculated Property |
| Pvap | [3.21e-04; 3886.10] | kPa | [202.94; 624.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 8.06625e+01 | |||
| Coefficient B | -7.62320e+03 | |||
| Coefficient C | -9.66669e+00 | |||
| Coefficient D | 5.22775e-06 | |||
| Temperature range, min. | 202.94 | |||
| Temperature range, max. | 624.00 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 200 400 600 | ||||
| Pvap | 3.21e-04 | kPa | 202.94 | Calculated Property |
| Pvap | 0.05 | kPa | 249.72 | Calculated Property |
| Pvap | 1.48 | kPa | 296.51 | Calculated Property |
| Pvap | 13.91 | kPa | 343.29 | Calculated Property |
| Pvap | 69.44 | kPa | 390.08 | Calculated Property |
| Pvap | 230.57 | kPa | 436.86 | Calculated Property |
| Pvap | 584.19 | kPa | 483.65 | Calculated Property |
| Pvap | 1231.37 | kPa | 530.43 | Calculated Property |
| Pvap | 2285.99 | kPa | 577.22 | Calculated Property |
| Pvap | 3886.10 | kPa | 624.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Ethane, 1,1,1,2-tetrachloro-.
Mixtures
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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