- 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 [R124]
- 1-chloro-1,2,2,2-tetrafluoroethane
- 2-chloro-1,1,1,2-tetrafluoroethane
- CF3CHFCl
- CFC 124
- Freon 124
- R 124
- R-124
- ω : Acentric Factor.
- 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).
- 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).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [594.00; 1045.00] | kPa | [313.15; 333.15] | 
|
| Pvap | 594.00 | kPa | 313.15 | 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 |
| Pvap | 776.00 | kPa | 323.15 | 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 |
| Pvap | 1045.00 | kPa | 333.15 | 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 |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [92.33; 161.07] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 1.21700e+01 | |||
| Coefficient B | 3.79500e-01 | |||
| Coefficient C | -3.46000e-04 | |||
| Coefficient D | 1.15400e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 92.33 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 108.23 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 121.22 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 131.65 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 139.89 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 146.31 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 151.27 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 155.14 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 158.29 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 161.07 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 3141.04] | kPa | [190.23; 395.43] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| 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-
- Ethane, 2-chloro-1,1,1,2-tetrafluoro- + Ethane, 1-chloro-1,1-difluoro- + Methane, chlorodifluoro-
Sources
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 ChEDL chemicals 1.5.2, from Marsh, K. N.; Abramson, A.; Ambrose, D.; Morton, D. W.; Nikitin, E.; Tsonopoulos, C.; Young, C. L. Vapor-Liquid Critical Properties of Elements and Compounds. 10. Organic Compounds Containing Halogens. J. Chem. Eng. Data 2007, 52, 1509-1538.
- PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
- Cheméo Relay (1.0)
- 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]
- Relative Permittivity and Dipole Moments of Replacement Refrigerant Mixtures (R408A and R409A) in the Liquid State
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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