- InChI
- InChI=1S/C2Cl3F3/c3-1(4,6)2(5,7)8
- InChI Key
- AJDIZQLSFPQPEY-UHFFFAOYSA-N
- Formula
- C2Cl3F3
- SMILES
- FC(F)(Cl)C(F)(Cl)Cl
- Molecular Weight1
- 187.38
- CAS
- 76-13-1
- Other Names
-
- 1,1,2-TRICHLORO-1,2,2-TRIFLUOROETHANE
- 1,1,2-Trichlorotrifluoroethane
- 1,1,2-Trifluoro-1,2,2-trichloroethane
- 1,1,2-Trifluorotrichloroethane
- 1,1,2-trichlorotrifluoroethane (Freon 113)
- 1,2,2-Trichlorotrifluoroethane
- 1,2,2-Trifluorotrichloroethane
- ARCTON 63
- Arklone
- Arklone P
- Asahifron 113
- CFC-113
- CFCl2CF2Cl
- Daiflon S 3
- Delifrene LS
- Distillex DS5
- F 113
- FC 113
- FC 133
- Fluorocarbon 113
- Forane 113
- Freon 113
- Freon 113 TR-T
- Freon F113
- Freon R 113
- Freon TF
- Freon TF (113)
- Frigen 113
- Frigen 113 TR
- Frigen 113 TR-T
- Frigen 113A
- Genesolv D
- Genetron 113
- Halocarbon 113
- Halon 113
- Isceon 113
- Kaiser chemicals 11
- Khladon 113
- LEDON 113
- R 113
- R 113(Halocarbon)
- R-113
- REFRIGERANT-113
- Refrigerant 113
- Refrigerant R 113
- Trichloro 1,2,2-trifluoroethane
- 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).
- 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).
- 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).
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρc : Critical 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).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | -641.60 ± 1.90 | kJ/mol | NIST |
| ΔfG° | -648.58 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -726.80 ± 4.30 | kJ/mol | NIST |
| ΔfH°liquid | -755.00 ± 4.30 | kJ/mol | NIST |
| ΔfusH° | 7.94 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [28.20; 28.70] | kJ/mol |
|
| ΔvapH° | 28.61 | kJ/mol | NIST |
| ΔvapH° | 28.20 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 28.40 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 28.20 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 28.70 | kJ/mol | NIST |
| IE | [11.99; 12.05] | eV |
|
| IE | 11.99 ± 0.02 | eV | NIST |
| IE | 12.05 | eV | NIST |
| log10WS | [-3.04; -3.04] |
|
|
| log10WS | -3.04 | Aq. Sol... | |
| log10WS | -3.04 | Estimat... | |
| logPoct/wat | 2.919 | Crippen Calculated Property | |
| McVol | 81.070 | ml/mol | McGowan Calculated Property |
| Pc | [3379.00; 3420.00] | kPa |
|
| Pc | 3420.00 | kPa | KDB |
| Pc | 3379.00 ± 5.00 | kPa | NIST |
| Pc | 3410.82 ± 6.89 | kPa | NIST |
| Pc | 3412.89 | kPa | NIST |
| ρc | [569.62; 575.24] | kg/m3 |
|
| ρc | 569.62 ± 5.70 | kg/m3 | NIST |
| ρc | 569.92 ± 9.61 | kg/m3 | NIST |
| ρc | 575.24 ± 1.87 | kg/m3 | NIST |
| Inp | [522.00; 555.00] |
|
|
| Inp | 528.00 | NIST | |
| Inp | 540.00 | NIST | |
| Inp | 524.00 | NIST | |
| Inp | 532.00 | NIST | |
| Inp | 526.00 | NIST | |
| Inp | 522.00 | NIST | |
| Inp | 522.00 | NIST | |
| Inp | 527.00 | NIST | |
| Inp | Outlier 555.00 | NIST | |
| Inp | 530.00 | NIST | |
| Inp | 530.00 | NIST | |
| I | [660.00; 660.00] |
|
|
| I | 660.00 | NIST | |
| I | 660.00 | NIST | |
| S°liquid | 289.50 | J/mol×K | NIST |
| Tboil | [320.42; 321.00] | K |
|
| Tboil | 320.80 | K | KDB |
| Tboil | 321.00 | K | NIST |
| Tboil | 320.42 ± 0.10 | K | NIST |
| Tboil | 320.90 | K | NIST |
| Tboil | 320.70 | K | NIST |
| Tboil | 320.70 | K | NIST |
| Tc | 487.30 | K | KDB |
| Tfus | [238.00; 238.15] | K |
|
| Tfus | 238.00 | K | KDB |
| Tfus | 238.15 | K | NIST |
| Ttriple | [236.55; 237.93] | K |
|
| Ttriple | 236.55 ± 0.10 | K | NIST |
| Ttriple | 237.93 ± 0.02 | K | NIST |
| Ttriple | 236.92 ± 0.02 | K | NIST |
| Vc | 0.325 | m3/kmol | KDB |
| Zc | 0.2743320 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [126.81; 153.48] | J/mol×K | [348.80; 533.87] |
|
| Cp,gas | 126.81 | J/mol×K | 348.80 | Joback Calculated Property |
| Cp,gas | 132.62 | J/mol×K | 379.64 | Joback Calculated Property |
| Cp,gas | 137.83 | J/mol×K | 410.49 | Joback Calculated Property |
| Cp,gas | 142.49 | J/mol×K | 441.33 | Joback Calculated Property |
| Cp,gas | 146.63 | J/mol×K | 472.18 | Joback Calculated Property |
| Cp,gas | 150.28 | J/mol×K | 503.02 | Joback Calculated Property |
| Cp,gas | 153.48 | J/mol×K | 533.87 | Joback Calculated Property |
| Cp,liquid | [172.50; 179.80] | J/mol×K | [298.15; 303.15] |
|
| Cp,liquid | 172.90 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 172.80 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 179.80 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 177.00 | J/mol×K | 298.20 | NIST |
| Cp,liquid | 177.00 | J/mol×K | 298.20 | NIST |
| Cp,liquid | 172.50 | J/mol×K | 303.15 | NIST |
| ΔfusH | [0.83; 2.47] | kJ/mol | [82.50; 273.93] |
|
| ΔfusH | 0.83 | kJ/mol | 82.50 | NIST |
| ΔfusH | 2.47 | kJ/mol | 236.90 | NIST |
| ΔfusH | 2.47 | kJ/mol | 236.90 | NIST |
| ΔfusH | 2.33 | kJ/mol | 273.93 | NIST |
| ΔsubH | 32.90 | kJ/mol | 219.00 | NIST |
| ΔvapH | [26.60; 30.90] | kJ/mol | [295.50; 416.50] |
|
| ΔvapH | 28.20 | kJ/mol | 295.50 | NIST |
| ΔvapH | 28.30 | kJ/mol | 296.00 | NIST |
| ΔvapH | 30.90 | kJ/mol | 301.00 | NIST |
| ΔvapH | 30.80 | kJ/mol | 302.00 | NIST |
| ΔvapH | 28.80 | kJ/mol | 307.00 | NIST |
| ΔvapH | 27.50 ± 0.10 | kJ/mol | 313.00 | NIST |
| ΔvapH | 27.04 | kJ/mol | 320.70 | NIST |
| ΔvapH | 26.60 ± 0.10 | kJ/mol | 328.00 | NIST |
| ΔvapH | 26.90 | kJ/mol | 416.50 | NIST |
| ΔfusS | [8.49; 10.42] | J/mol×K | [82.50; 273.93] |
|
| ΔfusS | 10.08 | J/mol×K | 82.50 | NIST |
| ΔfusS | 10.42 | J/mol×K | 236.90 | NIST |
| ΔfusS | 8.49 | J/mol×K | 273.93 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 3358.42] | kPa | [232.76; 487.21] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.40069e+01 | |||
| Coefficient B | -2.62436e+03 | |||
| Coefficient C | -4.14730e+01 | |||
| Temperature range, min. | 232.76 | |||
| Temperature range, max. | 487.21 | |||
| Pvap | 1.33 | kPa | 232.76 | Calculated Property |
| Pvap | 7.80 | kPa | 261.03 | Calculated Property |
| Pvap | 30.50 | kPa | 289.30 | Calculated Property |
| Pvap | 90.19 | kPa | 317.58 | Calculated Property |
| Pvap | 218.07 | kPa | 345.85 | Calculated Property |
| Pvap | 453.78 | kPa | 374.12 | Calculated Property |
| Pvap | 841.86 | kPa | 402.39 | Calculated Property |
| Pvap | 1427.71 | kPa | 430.67 | Calculated Property |
| Pvap | 2254.06 | kPa | 458.94 | Calculated Property |
| Pvap | 3358.42 | kPa | 487.21 | Calculated Property |
| Pvap | [1.95; 3548.42] | kPa | [238.15; 487.25] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.11463e+02 | |||
| Coefficient B | -7.08030e+03 | |||
| Coefficient C | -1.49859e+01 | |||
| Coefficient D | 1.67919e-05 | |||
| Temperature range, min. | 238.15 | |||
| Temperature range, max. | 487.25 | |||
| Pvap | 1.95 | kPa | 238.15 | Calculated Property |
| Pvap | 10.49 | kPa | 265.83 | Calculated Property |
| Pvap | 38.02 | kPa | 293.51 | Calculated Property |
| Pvap | 104.82 | kPa | 321.18 | Calculated Property |
| Pvap | 238.37 | kPa | 348.86 | Calculated Property |
| Pvap | 472.79 | kPa | 376.54 | Calculated Property |
| Pvap | 850.73 | kPa | 404.22 | Calculated Property |
| Pvap | 1428.93 | kPa | 431.89 | Calculated Property |
| Pvap | 2288.07 | kPa | 459.57 | Calculated Property |
| Pvap | 3548.42 | kPa | 487.25 | Calculated Property |
Similar Compounds
Find more compounds similar to Ethane, 1,1,2-trichloro-1,2,2-trifluoro-.
Mixtures
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Hydrogen substitution effect on the solubility of perhalogenated compounds in ionic liquid [bmim][PF6]
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Solubility Differences of Halocarbon Isomers in Ionic Liquid [emim][Tf2N]
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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