Ethane, 1,1,1-trifluoro-
- Formula: C2H3F3
- Molecular weight: 84.0404
- IUPAC Standard InChIKey: UJPMYEOUBPIPHQ-UHFFFAOYSA-N
- CAS Registry Number: 420-46-2
- 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: Methylfluoroform; 1,1,1-Trifluoroethane; CH3CF3; Freon 143a; FC 143a; Fluorocarbon FC143a; R 143a; 1,1,1-Trifluoroform
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Gas phase thermochemistry data
Go To: Top, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry 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: Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°gas | -178.94 ± 0.76 | kcal/mol | Eqk | Wu and Rodgers, 1974 | Reanalyzed by Kolesov and Papina, 1983, Original value = -178.2 ± 0.4 kcal/mol; Heat of formation Unpublished results by B.J. Zwolinski |
ΔfH°gas | -178.9 ± 0.4 | kcal/mol | Ccb | Kolesov, Martynov, et al., 1965 | Corrected for CODATA value of ΔfH; Authors hf298_gas[kcal/mol]=-174.1±0.4 |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°gas | -241.0 ± 0.4 | kcal/mol | Ccb | Kolesov, Martynov, et al., 1965 | Corrected for CODATA value of ΔfH; Authors hf298_gas[kcal/mol]=-174.1±0.4 |
Condensed phase thermochemistry data
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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
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
S°liquid | 53.561 | cal/mol*K | N/A | Russell, Golding, et al., 1944 |
Constant pressure heat capacity of liquid
Cp,liquid (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
26.209 | 220. | Russell, Golding, et al., 1944 | T = 15 to 226 K. |
Phase change data
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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
DH - Eugene S. Domalski and Elizabeth D. Hearing
AC - William E. Acree, Jr., James S. Chickos
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 226. | K | N/A | PCR Inc., 1990 | BS |
Tboil | 226.45 | K | N/A | Henne and Renoll, 1936 | Uncertainty assigned by TRC = 0.1 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 161.82 | K | N/A | Russell, Golding, et al., 1944, 2 | Crystal phase 1 phase; Uncertainty assigned by TRC = 0.02 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 345.860 | K | N/A | Fujiwara, Nakamura, et al., 1998 | Uncertainty assigned by TRC = 0.05 K; For ITS-90 scale. Includes review of and comparison with previous literature; TRC |
Tc | 345.860 | K | N/A | Aoyama, Kishizawa, et al., 1996 | Uncertainty assigned by TRC = 0.02 K; For ITS-90, at temperture corres. to DC, includes review of and comparison with previous literture; TRC |
Tc | 345.97 | K | N/A | Fukushima, 1993 | Uncertainty assigned by TRC = 0.2 K; TRC |
Tc | 346.25 | K | N/A | Mears, Stahl, et al., 1955 | Uncertainty assigned by TRC = 0.7 K; by sealed tube method; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 37.147 | atm | N/A | Fujiwara, Nakamura, et al., 1998 | Uncertainty assigned by TRC = 0.05 atm; includes review of and comparison with previous literature; TRC |
Pc | 33.670 | atm | N/A | Zhang, Sato, et al., 1995 | Uncertainty assigned by TRC = 0.05 atm; by extrapolation of vapor pressure to Tc from previous publ.; TRC |
Pc | 37.20 | atm | N/A | Fukushima, 1993 | Uncertainty assigned by TRC = 0.05 atm; TRC |
Pc | 37.0849 | atm | N/A | Mears, Stahl, et al., 1955 | Uncertainty assigned by TRC = 1.0207 atm; from vapor pressure equation at Tc; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 5.16 | mol/l | N/A | Fujiwara, Nakamura, et al., 1998 | Uncertainty assigned by TRC = 0.04 mol/l; includes review of and comparison with previous literature; TRC |
ρc | 5.16 | mol/l | N/A | Aoyama, Kishizawa, et al., 1996 | Uncertainty assigned by TRC = 0.02 mol/l; at critical opalesence, includes review of and comparison with previous literature; TRC |
ρc | 5.10 | mol/l | N/A | Fukushima, 1993 | Uncertainty assigned by TRC = 0.04 mol/l; TRC |
ρc | 5.16 | mol/l | N/A | Mears, Stahl, et al., 1955 | Uncertainty assigned by TRC = 0.18 mol/l; rectilinear diameters; TRC |
Enthalpy of vaporization
ΔvapH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
4.5829 | 224.40 | N/A | Russell, Golding, et al., 1944 | P - 94.54 kPa; DH |
4.33 | 240. | EB | Weber and Defibaugh, 1996 | Based on data from 236. to 280. K.; AC |
4.18 | 250. | EB | Weber and Defibaugh, 1996 | Based on data from 236. to 280. K.; AC |
3.99 | 260. | EB | Weber and Defibaugh, 1996 | Based on data from 236. to 280. K.; AC |
3.80 | 270. | EB | Weber and Defibaugh, 1996 | Based on data from 236. to 280. K.; AC |
4.52 | 233. | BG | Mears, Stahl, et al., 1955, 2 | AC |
3.92 | 273. | BG | Mears, Stahl, et al., 1955, 2 | AC |
3.30 | 303. | BG | Mears, Stahl, et al., 1955, 2 | AC |
2.1 | 333. | BG | Mears, Stahl, et al., 1955, 2 | AC |
4.90 | 211. | N/A | Russell, Golding, et al., 1944 | Based on data from 174. to 226. K.; AC |
4.59 ± 0.02 | 224. | C | Russell, Golding, et al., 1944 | AC |
Entropy of vaporization
ΔvapS (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
20.42 | 224.40 | Russell, Golding, et al., 1944 | P; DH |
Antoine Equation Parameters
log10(P) = A − (B / (T + C))
P = vapor pressure (atm)
T = temperature (K)
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Temperature (K) | A | B | C | Reference | Comment |
---|---|---|---|---|---|
173.60 to 225.78 | 4.01852 | 786.645 | -30.093 | Russell, Golding, et al., 1944 | Coefficents calculated by NIST from author's data. |
Enthalpy of fusion
ΔfusH (kcal/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
1.48 | 161.9 | Acree, 1991 | AC |
Enthalpy of phase transition
ΔHtrs (kcal/mol) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
0.0710 | 156.35 | crystaline, II | crystaline, I | Russell, Golding, et al., 1944 | DH |
1.480 | 161.82 | crystaline, I | liquid | Russell, Golding, et al., 1944 | DH |
Entropy of phase transition
ΔStrs (cal/mol*K) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
0.454 | 156.35 | crystaline, II | crystaline, I | Russell, Golding, et al., 1944 | DH |
9.144 | 161.82 | crystaline, I | liquid | Russell, Golding, et al., 1944 | DH |
Reaction thermochemistry data
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Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data compiled by: Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
Note: Please consider using the reaction search for this species. This page allows searching of all reactions involving this species. A general reaction search form is also available. Future versions of this site may rely on reaction search pages in place of the enumerated reaction displays seen below.
Individual Reactions
By formula: C2H3F3 + I2 = HI + C2H2F3I
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -15.3 ± 0.5 | kcal/mol | Eqk | Wu and Rodgers, 1974 | gas phase; Heat of formation Unpublished results by B.J. Zwolinski |
Gas Chromatography
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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 | 268. | Zenkevich, 2005 | 25. m/0.20 mm/0.10 μm, N2/He, 6. K/min; Tstart: 50. C; Tend: 250. C |
References
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Gas Chromatography, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Wu and Rodgers, 1974
Wu, E.; Rodgers, A.S.,
Thermochemistry of gas-phase equilibrium CF3CH3 + I2 = CF3CH2I + HI. The carbon-hydrogen bond dissociation energy in 1,1,1-trifluoroethane and the heat of formation of the 2,2,2-trifluoroethyl radical,
J. Phys. Chem., 1974, 78, 2315-2317. [all data]
Kolesov and Papina, 1983
Kolesov, V.P.; Papina, T.S.,
Thermochemistry of Haloethanes,
Russ. Chem. Rev., 1983, 52, 425. [all data]
Kolesov, Martynov, et al., 1965
Kolesov, V.P.; Martynov, A.M.; Skuratov, S.M.,
Standard enthalpy of formation of 1,1,1-trifluoroethane,
Russ. J. Phys. Chem. (Engl. Transl.), 1965, 39, 223-225. [all data]
Russell, Golding, et al., 1944
Russell, H., Jr.; Golding, D.R.V.; Yost, D.M.,
The heat capacity, heats of transition, fusion and vaporization, vapor pressure and entropy of 1,1,1-trifluoroethane,
J. Am. Chem. Soc., 1944, 66, 16-20. [all data]
PCR Inc., 1990
PCR Inc.,
Research Chemicals Catalog 1990-1991, PCR Inc., Gainesville, FL, 1990, 1. [all data]
Henne and Renoll, 1936
Henne, A.L.; Renoll, M.W.,
J. Am. Chem. Soc., 1936, 58, 889. [all data]
Russell, Golding, et al., 1944, 2
Russell, H.K.; Golding, D.R.; Yost, D.M.,
The heat capacity, heat of transition, fusion & vaporization, Vapor press. and entropy of 1,1,1-trifluoroethane,
J. Am. Chem. Soc., 1944, 66, 16. [all data]
Fujiwara, Nakamura, et al., 1998
Fujiwara, K.; Nakamura, S.; Noguchi, M.,
Critical Parameters and Vapor Pressure Measurements for 1,1,1-Trifluoroethane (R-143a),
J. Chem. Eng. Data, 1998, 43, 55-9. [all data]
Aoyama, Kishizawa, et al., 1996
Aoyama, H.; Kishizawa, G.; Sato, H.; Watanabe, K.,
Vapor-Liquid Coexistence Curves in the Critical Region and the Critical Temperatures and Densities of 1,1,1,2-Tetrafluoroethane (R-134a), 1,1,1- Trifluoroethane (R-143a), and 1,1,1,2,3,3- Hexafluorop,
J. Chem. Eng. Data, 1996, 41, 1046-1051. [all data]
Fukushima, 1993
Fukushima, M.,
Measurements of vapor pressure , vapor-liquid coexistence curve and critical parameters of HFC-143a,
Nippon Reito Kyokai Ronbunshu, 1993, 10, 87-93. [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]
Zhang, Sato, et al., 1995
Zhang, H.-L.; Sato, H.; Watanabe, K.,
Vapor Pressures, Gas-Phase PVT Properties, and Second Virial Coefficients for 1,1,1-Trifluoroethane,
J. Chem. Eng. Data, 1995, 40, 887-90. [all data]
Weber and Defibaugh, 1996
Weber, L.A.; Defibaugh, D.R.,
Vapor Pressures and PVT Properties of the Gas Phase of 1,1,1-Trifluoroethane,
J. Chem. Eng. Data, 1996, 41, 6, 1477-1480, https://doi.org/10.1021/je9602071
. [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]
Acree, 1991
Acree, William E.,
Thermodynamic properties of organic compounds: enthalpy of fusion and melting point temperature compilation,
Thermochimica Acta, 1991, 189, 1, 37-56, https://doi.org/10.1016/0040-6031(91)87098-H
. [all data]
Zenkevich, 2005
Zenkevich, I.G.,
Experimentally measured retention indices., 2005. [all data]
Notes
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Gas Chromatography, References
- Symbols used in this document:
Cp,liquid Constant pressure heat capacity of liquid Pc Critical pressure S°liquid Entropy of liquid at standard conditions Tboil Boiling point Tc Critical temperature Ttriple Triple point temperature ΔHtrs Enthalpy of phase transition ΔStrs Entropy of phase transition ΔcH°gas Enthalpy of combustion of gas at standard conditions ΔfH°gas Enthalpy of formation of gas at standard conditions ΔfusH Enthalpy of fusion ΔrH° Enthalpy of reaction at standard conditions ΔvapH Enthalpy of vaporization ΔvapS Entropy of vaporization ρc Critical density - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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