Ethane, 1-chloro-1,1-difluoro-
- Formula: C2H3ClF2
- Molecular weight: 100.495
- IUPAC Standard InChIKey: BHNZEZWIUMJCGF-UHFFFAOYSA-N
- CAS Registry Number: 75-68-3
- Chemical structure:
This structure is also available as a 2d Mol file or as a computed 3d SD file
The 3d structure may be viewed using Java or Javascript. - Other names: α-Chloroethylidene fluoride; Freon 142; Freon 142b; FC 142b; Genetron 101; Genetron 142b; R 142b; 1-Chloro-1,1-Difluoroethane; 1,1-Difluoro-1-chloroethane; CH3CF2Cl; CFC 142b; Chloroethylidene fluoride; Fluorocarbon FC142b; Gentron 142B; Hydrochlorofluorocarbon 142b; UN 2517; Dymel 142; F 142b; HCFC 142b; Propellant 142b
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Condensed phase thermochemistry data
Go To: Top, Phase change data, Henry's Law data, Gas Chromatography, References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data compiled by: Eugene S. Domalski and Elizabeth D. Hearing
Constant pressure heat capacity of liquid
Cp,liquid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
132.15 | 300. | Nakagawa, Hori, et al., 1993 | T = 276 to 350 K. p = 0.358 MPa |
130.5 | 294.9 | Riedel, 1942 | T = -61 to 21°C. Value is unsmoothed experimental datum for saturated liquid. |
130.5 | 294.8 | Riedel, 1941 | T = -61 to 22°C. Value is unsmoothed experimental datum. |
130.5 | 291.6 | Perlick, 1937 | T = -180 to 18°C. Value is unsmoothed experimental datum for saturated liquid. |
130.5 | 291.6 | Perlick, 1937, 2 | T = -180 to 18°C. Value is unsmoothed experimental datum. |
Phase change data
Go To: Top, Condensed phase thermochemistry data, Henry's Law data, Gas Chromatography, References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data compiled as indicated in comments:
BS - Robert L. Brown and Stephen E. Stein
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
AC - William E. Acree, Jr., James S. Chickos
DH - Eugene S. Domalski and Elizabeth D. Hearing
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 263.2 | K | N/A | Aldrich Chemical Company Inc., 1990 | BS |
Tboil | 263.55 | K | N/A | Henne and Renoll, 1936 | Uncertainty assigned by TRC = 0.6 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 142.710 | K | N/A | Blanke and Weiss, 1991 | Uncertainty assigned by TRC = 0.01 K; on ITS-90; TRC |
Ttriple | 142.4 | K | N/A | Perlick, 1937, 3 | Uncertainty assigned by TRC = 0.2 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Ptriple | 0.00005 | bar | N/A | Blanke and Weiss, 1991 | Uncertainty assigned by TRC = 0.00002 bar; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 410.2 ± 0.5 | K | AVG | N/A | Average of 6 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 40.48 | bar | N/A | Sako, Sato, et al., 1996 | Uncertainty assigned by TRC = 0.06 bar; measurement made to check technique; TRC |
Pc | 40.53 | bar | N/A | Fukushima and Watanabe, 1992 | Uncertainty assigned by TRC = 0.05 bar; TRC |
Pc | 40.41 | bar | N/A | Yada, Kumagai, et al., 1991 | Uncertainty assigned by TRC = 0.03 bar; by extrapolating obs. vapor pressures to Tc = 410.29 K; TRC |
Pc | 43.3164 | bar | N/A | Cherneeva, 1958 | Uncertainty assigned by TRC = 0.25 bar; TRC |
Pc | 41.2305 | bar | N/A | Mears, Stahl, et al., 1955 | Uncertainty assigned by TRC = 1.0342 bar; from vapor pressure equation at Tc; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 4.42 | mol/l | N/A | Sako, Sato, et al., 1996 | Uncertainty assigned by TRC = 0.04 mol/l; measurement made to check techniaue; TRC |
ρc | 4.44 | mol/l | N/A | Fukushima and Watanabe, 1992 | Uncertainty assigned by TRC = 0.05 mol/l; TRC |
ρc | 4.44 | mol/l | N/A | Tanikawa, Tatoh, et al., 1992 | Uncertainty assigned by TRC = 0.05 mol/l; TRC |
ρc | 4.47 | mol/l | N/A | Chae, Schmidt, et al., 1990 | Uncertainty assigned by TRC = 0.11 mol/l; derived from obs L and G refractive index; TRC |
ρc | 4.236 | mol/l | N/A | Cherneeva, 1958 | Uncertainty assigned by TRC = 0.04 mol/l; TRC |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
24.2 | 240. | EB | Silva and Weber, 1993 | Based on data from 225. to 285. K.; AC |
22.7 | 263. | A | Stephenson and Malanowski, 1987 | Based on data from 248. to 390. K. See also Dykyj, 1970.; AC |
24.0 | 233. | BG | Mears, Stahl, et al., 1955, 2 | AC |
21.9 | 273. | BG | Mears, Stahl, et al., 1955, 2 | AC |
19.2 | 313. | BG | Mears, Stahl, et al., 1955, 2 | AC |
15.4 | 353. | BG | Mears, Stahl, et al., 1955, 2 | AC |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
2.686 | 142.4 | Perlick, 1937 | DH |
2.686 | 142.4 | Perlick, 1937, 2 | DH |
2.69 | 142.4 | Domalski and Hearing, 1996 | AC |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
18.86 | 142.4 | Perlick, 1937 | DH |
18.86 | 142.4 | Perlick, 1937, 2 | DH |
Henry's Law data
Go To: Top, Condensed phase thermochemistry data, Phase change data, Gas Chromatography, References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data compiled by: Rolf Sander
Henry's Law constant (water solution)
kH(T) = k°H exp(d(ln(kH))/d(1/T) ((1/T) - 1/(298.15 K)))
k°H = Henry's law constant for solubility in water at 298.15 K (mol/(kg*bar))
d(ln(kH))/d(1/T) = Temperature dependence constant (K)
k°H (mol/(kg*bar)) | d(ln(kH))/d(1/T) (K) | Method | Reference |
---|---|---|---|
0.014 | 2500. | C | N/A |
Gas Chromatography
Go To: Top, Condensed phase thermochemistry data, Phase change data, Henry's Law data, References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data compiled by: NIST Mass Spectrometry Data Center, William E. Wallace, director
Normal alkane RI, non-polar column, temperature ramp
Column type | Active phase | I | Reference | Comment |
---|---|---|---|---|
Capillary | OV-101 | 402. | Zenkevich, 2005 | 25. m/0.20 mm/0.10 μm, N2/He, 6. K/min; Tstart: 50. C; Tend: 250. C |
Normal alkane RI, non-polar column, custom temperature program
Column type | Active phase | I | Reference | Comment |
---|---|---|---|---|
Capillary | Methyl Silicone | 346. | Blunden, Aneja, et al., 2005 | 60. m/0.32 mm/1.0 μm, Helium; Program: -50 0C (2 min) 8 0C/min -> 200 0C (7.75 min) 25 0C -> 225 0C (8 min) |
References
Go To: Top, Condensed phase thermochemistry data, Phase change data, Henry's Law data, Gas Chromatography, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Nakagawa, Hori, et al., 1993
Nakagawa, S.; Hori, T.; Sato, H.,
and Watanabe K., Isobaric heat capacity for liquid 1-chloro-1,1-difluorethane and 1,1-difluoroethane,
J. Chem. Eng. Data, 1993, 38(1), 70-74. [all data]
Riedel, 1942
Riedel, L.,
Determination of the thermal and caloric properties of difluoromonochloroethane,
Bull. Int. Inst. Refrig. Annex 23, 1942, No.2, 1-5. [all data]
Riedel, 1941
Riedel, L.,
Bestimmung der thermischen und kalorischen Eigenschaften von Difluoromonochloräthan,
Z. ges. Kalte-Ind., 1941, 48, 105-107. [all data]
Perlick, 1937
Perlick, A.,
Calorimetric investigations on dichloromethane, difluoromonochloroethane and tetrafluorodichloroethane,
Bull. Int. Inst. Refrig., 1937, 18, 1-9. [all data]
Perlick, 1937, 2
Perlick, A.,
Kalorimetrische Messungen an Schwefeldioxyd, Methylenchlorid, Difluormonochloraethan und Tetrafluordichloraethan,
Z. ges. Kalt-Ind., 1937, 44, 201-206. [all data]
Aldrich Chemical Company Inc., 1990
Aldrich Chemical Company Inc.,
Catalog Handbook of Fine Chemicals, Aldrich Chemical Company, Inc., Milwaukee WI, 1990, 1. [all data]
Henne and Renoll, 1936
Henne, A.L.; Renoll, M.W.,
J. Am. Chem. Soc., 1936, 58, 889. [all data]
Blanke and Weiss, 1991
Blanke, W.; Weiss, R.,
Thermodynamic properties of refrigerants. Part I: the triple points of the refrigerants R11, R12, R22, R142b, and 152a,
PTB-Mitt., 1991, 101, 337-9. [all data]
Perlick, 1937, 3
Perlick, A.,
Calorimetric investigations on dichloromethane, difluoromonochloroethane and tetrafluorodichloroethane,
Bull. Inst. Int. Froid., 1937, 18, 4, A-1. [all data]
Sako, Sato, et al., 1996
Sako, T.; Sato, M.; Nakazawa, N.; Oowa, M.; Yasumoto, M.; Ito, H.; Yamashita, S.,
Critical Properties of Fluorinated Ethers,
J. Chem. Eng. Data, 1996, 41, 802-805. [all data]
Fukushima and Watanabe, 1992
Fukushima, M.; Watanabe, N.,
Thermodynamic properties of HCFC-142b (1-chloro-1,1-difluoroethane),
Nippon Reito Kyokai Ronbunshu, 1992, 9, 247-55. [all data]
Yada, Kumagai, et al., 1991
Yada, N.; Kumagai, K.; Tamatsu, T.; Sato, H.; Watanabe, K.,
Measurements of the Thermodynamic Properties of HCFC 142b,
J. Chem. Eng. Data, 1991, 36, 12-14. [all data]
Cherneeva, 1958
Cherneeva, L.I.,
Experimental Investigation into the Thermodynamic Properties of Freon-142,
Teploenergetika (Moscow), 1958, 5, 7, 38. [all data]
Mears, Stahl, et al., 1955
Mears, W.H.; Stahl, R.F.; Orfeo, S.R.; Shair, R.C.; Kells, L.F.; Thompson, W.; McCann, H.,
Thermodynamic Properties of Halogenated Ethanes and Ethylenes,
Ind. Eng. Chem., 1955, 47, 1449. [all data]
Tanikawa, Tatoh, et al., 1992
Tanikawa, S.; Tatoh, J.; Maezawa, Y.; Sato, H.; Watanabe, K.,
Vapor-liquid coexistence curve and the critical parameters of 1-chloro-1,1- difluoroethane (HCFC-142b),
J. Chem. Eng. Data, 1992, 37, 74-6. [all data]
Chae, Schmidt, et al., 1990
Chae, H.B.; Schmidt, J.W.; Moldover, M.R.,
Alternative refrigerants R123a, R134, R141b, R142b, and R152a: critical temperature, refractive index, surface tension, and estimates of liquid, vapor, and critical densities,
J. Phys. Chem., 1990, 94, 8840-5. [all data]
Silva and Weber, 1993
Silva, Alberto M.; Weber, Lloyd A.,
Ebulliometric measurement of the vapor pressure of 1-chloro-1,1-difluoroethane and 1,1-difluoroethane,
J. Chem. Eng. Data, 1993, 38, 4, 644-646, https://doi.org/10.1021/je00012a043
. [all data]
Stephenson and Malanowski, 1987
Stephenson, Richard M.; Malanowski, Stanislaw,
Handbook of the Thermodynamics of Organic Compounds, 1987, https://doi.org/10.1007/978-94-009-3173-2
. [all data]
Dykyj, 1970
Dykyj, J.,
Petrochemica, 1970, 10, 2, 51. [all data]
Mears, Stahl, et al., 1955, 2
Mears, Whitney H.; Stahl, Richard F.; Orfeo, S. Robert; Shair, Robert C.; Kells, Lyman F.; Thompson, Walter; McCann, Harold,
Thermodynamic Properties of Halogenated Ethanes and Ethylenes,
Ind. Eng. Chem., 1955, 47, 7, 1449-1454, https://doi.org/10.1021/ie50547a052
. [all data]
Domalski and Hearing, 1996
Domalski, Eugene S.; Hearing, Elizabeth D.,
Heat Capacities and Entropies of Organic Compounds in the Condensed Phase. Volume III,
J. Phys. Chem. Ref. Data, 1996, 25, 1, 1, https://doi.org/10.1063/1.555985
. [all data]
Zenkevich, 2005
Zenkevich, I.G.,
Experimentally measured retention indices., 2005. [all data]
Blunden, Aneja, et al., 2005
Blunden, J.; Aneja, V.P.; Lonneman, W.A.,
Characterization of non-methane volatile organic compounds at swine facilities in eastern North Carolina,
Atm. Environ., 2005, 39, 36, 6707-6718, https://doi.org/10.1016/j.atmosenv.2005.03.053
. [all data]
Notes
Go To: Top, Condensed phase thermochemistry data, Phase change data, Henry's Law data, Gas Chromatography, References
- Symbols used in this document:
Cp,liquid Constant pressure heat capacity of liquid Pc Critical pressure Ptriple Triple point pressure Tboil Boiling point Tc Critical temperature Ttriple Triple point temperature d(ln(kH))/d(1/T) Temperature dependence parameter for Henry's Law constant k°H Henry's Law constant at 298.15K ΔfusH Enthalpy of fusion ΔfusS Entropy of fusion ΔvapH Enthalpy of vaporization ρc Critical density - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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