Physical Properties
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[126.85; 153.51]
J/mol×K
[349.00; 534.17]
Cp,gas
126.85
J/mol×K
349.00
Joback Calculated Property
Cp,gas
132.66
J/mol×K
379.86
Joback Calculated Property
Cp,gas
137.87
J/mol×K
410.72
Joback Calculated Property
Cp,gas
142.53
J/mol×K
441.59
Joback Calculated Property
Cp,gas
146.66
J/mol×K
472.45
Joback Calculated Property
Cp,gas
150.31
J/mol×K
503.31
Joback Calculated Property
Cp,gas
153.51
J/mol×K
534.17
Joback Calculated Property
Cp,liquid
[167.00; 173.00]
J/mol×K
[290.00; 320.00]
Cp,liquid
167.00
J/mol×K
290.00
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid
168.60
J/mol×K
298.15
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid
169.00
J/mol×K
300.00
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid
171.00
J/mol×K
310.00
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid
173.00
J/mol×K
320.00
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Δvap H
30.50
kJ/mol
300.00
NIST
Pvap
101.30
kPa
319.15
Vapor Liquid Equilibrium for the 1,1,1-Trifluorotrichloroethane + Sulfuryl Chloride System at 101.3 kPa
Correlations
Property
Value
Unit
Temperature (K)
Source
Pvap
[1.33; 207.03]
kPa
[229.59; 341.35]
The Yaws Handbook of Vapor Pressure
Equation ln(Pvp) = A + B/(T + C) Coefficient A 1.48158e+01 Coefficient B -3.05174e+03 Coefficient C -1.95350e+01 Temperature range, min. 229.59
Temperature range, max. 341.35
Pvap
1.33
kPa
229.59
Calculated Property
Pvap
3.00
kPa
242.01
Calculated Property
Pvap
6.19
kPa
254.43
Calculated Property
Pvap
11.89
kPa
266.84
Calculated Property
Pvap
21.45
kPa
279.26
Calculated Property
Pvap
36.67
kPa
291.68
Calculated Property
Pvap
59.83
kPa
304.10
Calculated Property
Pvap
93.68
kPa
316.51
Calculated Property
Pvap
141.50
kPa
328.93
Calculated Property
Pvap
207.03
kPa
341.35
Calculated Property
Similar Compounds
Find more compounds similar to trichlorotrifluoroethane .
Mixtures
Sources
Cheméo Relay (1.0)
Crippen Method
Crippen Method
Vapor Liquid Equilibrium for the 1,1,1-Trifluorotrichloroethane + Sulfuryl Chloride System at 101.3 kPa
Solubility Differences of Halocarbon Isomers in Ionic Liquid [emim][Tf2N]
Joback Method
McGowan Method
NIST Webbook
The Yaws Handbook of Vapor Pressure
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
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