- InChI
- InChI=1S/C2HClF4/c3-1(4)2(5,6)7/h1H
- InChI Key
- BOUGCJDAQLKBQH-UHFFFAOYSA-N
- Formula
- C2HClF4
- SMILES
- FC(Cl)C(F)(F)F
- Molecular Weight1
- 136.48
- CAS
- 2837-89-0
- Other Names
-
- 1,1,1,2-tetrafluoro-2-chloroethane
- 1-chloro-1,2,2,2-tetrafluoroethane
- 2-Chloro-1,1,1,2-tetrafluoroethane
- CF3CHFCl
- CFC 124
- Freon 124
- R 124
- R-124
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : 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).
- 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).
- 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 |
|---|---|---|---|
| ΔfG° | -824.81 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -898.82 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 6.52 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 19.48 | kJ/mol | Joback Calculated Property |
| log10WS | -1.94 | Crippen Calculated Property | |
| logPoct/wat | 2.083 | Crippen Calculated Property | |
| McVol | 58.360 | ml/mol | McGowan Calculated Property |
| Pc | 3615.00 ± 5.00 | kPa | NIST |
| ρc | 566.38 ± 5.46 | kg/m3 | NIST |
| Tboil | 262.00 | K | NIST |
| Tc | 395.35 ± 0.20 | K | NIST |
| Tfus | 132.00 | K | Joback Calculated Property |
| Vc | 0.252 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [92.98; 119.46] | J/mol×K | [276.00; 422.54] | 
|
| Cp,gas | 92.98 | J/mol×K | 276.00 | Joback Calculated Property |
| Cp,gas | 98.08 | J/mol×K | 300.42 | Joback Calculated Property |
| Cp,gas | 102.89 | J/mol×K | 324.85 | Joback Calculated Property |
| Cp,gas | 107.43 | J/mol×K | 349.27 | Joback Calculated Property |
| Cp,gas | 111.69 | J/mol×K | 373.70 | Joback Calculated Property |
| Cp,gas | 115.70 | J/mol×K | 398.12 | Joback Calculated Property |
| Cp,gas | 119.46 | J/mol×K | 422.54 | Joback Calculated Property |
| Pvap | [594.00; 1045.00] | kPa | [313.15; 333.15] |
|
| Pvap | 594.00 | kPa | 313.15 | Vapor l... |
| Pvap | 776.00 | kPa | 323.15 | Vapor l... |
| Pvap | 1045.00 | kPa | 333.15 | Vapor l... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 3141.04] | kPa | [190.23; 395.43] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.36550e+01 | |||
| Coefficient B | -1.97920e+03 | |||
| Coefficient C | -4.21720e+01 | |||
| Temperature range, min. | 190.23 | |||
| Temperature range, max. | 395.43 | |||
| Pvap | 1.33 | kPa | 190.23 | Calculated Property |
| Pvap | 7.93 | kPa | 213.03 | Calculated Property |
| Pvap | 31.03 | kPa | 235.83 | Calculated Property |
| Pvap | 91.05 | kPa | 258.63 | Calculated Property |
| Pvap | 217.63 | kPa | 281.43 | Calculated Property |
| Pvap | 446.97 | kPa | 304.23 | Calculated Property |
| Pvap | 818.10 | kPa | 327.03 | Calculated Property |
| Pvap | 1369.08 | kPa | 349.83 | Calculated Property |
| Pvap | 2133.99 | kPa | 372.63 | Calculated Property |
| Pvap | 3141.04 | kPa | 395.43 | Calculated Property |
Similar Compounds
Find more compounds similar to Ethane, 2-chloro-1,1,1,2-tetrafluoro-.
Mixtures
- Ethane, 2-chloro-1,1,1,2-tetrafluoro- + Carbon dioxide
- Ethane, 2-chloro-1,1,1,2-tetrafluoro- + 2-Pyrrolidinone, 1-methyl-
- Ethane, 2-chloro-1,1,1,2-tetrafluoro- + Formamide, N,N-dimethyl-
Sources
- Crippen Method
- Crippen Method
- Vapor liquid equilibria of the carbon dioxide (CO2) + 2,2-dichloro-1,1,1-trifluoroethane (R123) system and carbon dioxide (CO2) + 1-chloro-1,2,2,2-tetrafluoroethane (R124) system
- Measurement and Correlation of Vapor-Liquid Equilibrium for R124 (1-Chloro-1,2,2,2-Tetrafluoroethane)-NMP (N-Methyl-2-Pyrrolidone) and R124-DMF (N,N-Dimethylformamide) Mixtures
- Solubility Differences of Halocarbon Isomers in Ionic Liquid [emim][Tf2N]
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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