Ethane, 1,1,1-trichloro-
- Formula: C2H3Cl3
- Molecular weight: 133.404
- IUPAC Standard InChIKey: UOCLXMDMGBRAIB-UHFFFAOYSA-N
- CAS Registry Number: 71-55-6
- 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. - Species with the same structure:
- Other names: α-Trichloroethane; Aerothene TT; Chlorotene; Chlorothane NU; Chlorothene; Chlorothene NU; Chlorothene VG; Chlorten; Inhibisol; Methylchloroform; Methyltrichloromethane; Trichloroethane; 1,1,1-Trichloroethane; CH3CCl3; α-T; Chloroethene NU; Chloroform, methyl-; NCI-C04626; Solvent 111; Trichloro-1,1,1-ethane; 1,1,1-Trichloraethan; 1,1,1-Tricloroetano; CF 2; Chloroetene; Chloroethene; Chlorothene SM; Ethana NU; ICI-CF 2; Rcra waste number U226; Tafclean; 1,1,1-TCE; Trichloromethylmethane; Tri-ethane; UN 2831; 1,1,1-Trichlorethane; Distillex DS1; Ethana; Solvethane; Cleanite; F 140a; Genklene LB; HCC 140a; Three One A; Three One S
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Gas phase thermochemistry data
Go To: Top, Condensed phase thermochemistry data, Reaction thermochemistry 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 as indicated in comments:
DRB - Donald R. Burgess, Jr.
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°gas | -145. ± 2. | kJ/mol | Review | Manion, 2002 | derived from recommended ΔfHliquid° and ΔvapH°; DRB |
ΔfH°gas | -144.4 ± 1.6 | kJ/mol | Ccb | Hu, Sinke, et al., 1972 | Reanalyzed by Cox and Pilcher, 1970, Original value = -146.0 ± 0.84 kJ/mol; see Hu and Sinke, 1969; ALS |
ΔfH°gas | -142.3 ± 1.4 | kJ/mol | Ccr | Mansson, Ringner, et al., 1971 | ALS |
Condensed phase thermochemistry data
Go To: Top, Gas phase thermochemistry data, Reaction thermochemistry 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 as indicated in comments:
DRB - Donald R. Burgess, Jr.
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
DH - Eugene S. Domalski and Elizabeth D. Hearing
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°liquid | -177. ± 2. | kJ/mol | Review | Manion, 2002 | weighted average of several measurements; DRB |
ΔfH°liquid | -174. | kJ/mol | Eqk | Levanova, Treger, et al., 1975 | Flow reactor at 50°C; ALS |
ΔfH°liquid | -178.6 ± 0.84 | kJ/mol | Ccb | Hu, Sinke, et al., 1972 | Reanalyzed by Cox and Pilcher, 1970, Original value = -176. ± 0.79 kJ/mol; see Hu and Sinke, 1969; ALS |
ΔfH°liquid | -174.8 ± 1.4 | kJ/mol | Ccr | Mansson, Ringner, et al., 1971 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -1108.0 ± 0.79 | kJ/mol | Ccb | Hu, Sinke, et al., 1972 | see Hu and Sinke, 1969; ALS |
ΔcH°liquid | -1112.1 ± 1.3 | kJ/mol | Ccr | Mansson, Ringner, et al., 1971 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
S°liquid | 226.7 | J/mol*K | N/A | Andon, Counsell, et al., 1973 | DH |
S°liquid | 227.48 | J/mol*K | N/A | Rubin, Levedahl, et al., 1944 | DH |
Constant pressure heat capacity of liquid
Cp,liquid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
144.4 | 298.15 | Andon, Counsell, et al., 1973 | T = 10 to 310 K.; DH |
138.9 | 257.29 | Crowe and Smyth, 1950 | T = 117 to 260 K. Value is unsmoothed experimental datum.; DH |
144.31 | 299.59 | Rubin, Levedahl, et al., 1944 | T = 12 to 300 K. Value is unsmoothed experimental datum.; DH |
Constant pressure heat capacity of solid
Cp,solid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
123. | 225. | Martin and Monti, 1988 | T = 10 to 225 K. Data given graphically and estimated from graph.; 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: C2H3Cl3 = C2H2Cl2 + HCl
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 56.9 | kJ/mol | Eqk | Levanova, Bushneva, et al., 1979 | liquid phase |
ΔrH° | 49.0 | kJ/mol | Eqk | Levanova, Bushneva, et al., 1979 | gas phase |
ΔrH° | 56.9 ± 2.1 | kJ/mol | Eqk | Levanova, Treger, et al., 1975 | liquid phase; solvent: Nitrobenzene; Flow reactor at 50°C |
By formula: C2H2Cl2 + HCl = C2H3Cl3
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -54.64 ± 0.84 | kJ/mol | Eqk | Hu, Sinke, et al., 1972 | gas phase; Heat of halogenation at 348-399 K |
By formula: C2H3Cl3 = C2H3Cl3
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 8.4 | kJ/mol | Ciso | Levanova, Treger, et al., 1975, 2 | gas phase |
Henry's Law 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: 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 | Comment |
---|---|---|---|---|
0.058 | 3900. | L | N/A | |
0.068 | 3800. | M | N/A | |
0.060 | 3100. | M | N/A | |
0.071 | 4700. | C | N/A | |
0.059 | 3200. | X | N/A | |
0.053 | M | N/A | ||
0.057 | 3200. | M | N/A | |
0.087 | X | N/A | Value given here as cited in missing citation. | |
0.063 | 3700. | X | N/A | |
0.061 | 3500. | M | N/A | |
0.058 | 3400. | X | N/A | |
0.051 | 5200. | X | N/A | |
0.057 | 3400. | X | N/A | |
0.058 | 4000. | X | Barr and Newsham, 1987 | |
0.059 | 4100. | M | Gossett, 1987 | |
0.059 | 4100. | X | N/A | |
0.058 | 4200. | X | N/A | |
0.059 | 4300. | X | N/A | |
0.059 | 4300. | M | N/A | |
0.077 | 3200. | M | N/A | |
0.22 | 1700. | X | N/A | |
0.050 | 4400. | X | Leighton and Calo, 1981 | |
0.036 | L | N/A | ||
0.027 | 7000. | X | N/A | |
0.11 | 4600. | X | N/A | |
0.034 | V | N/A | ||
0.040 | V | N/A | Value at T = 293. K. | |
0.11 | V | N/A | Value at T = 275. K. | |
0.062 | V | N/A | ||
0.029 | M | Pearson and McConnell, 1975 | The same data was also published in missing citation. Value at T = 293. K. |
References
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Reaction thermochemistry data, Henry's Law data, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Manion, 2002
Manion, J.A.,
Evaluated Enthalpies of Formation of the Stable Closed Shell C1 and C2 Chlorinated Hydrocarbons,
J. Phys. Chem. Ref. Data, 2002, 31, 1, 123-172, https://doi.org/10.1063/1.1420703
. [all data]
Hu, Sinke, et al., 1972
Hu, A.T.; Sinke, G.C.; Mintz, M.J.,
The enthalpy of formation of 1,1,1-trichloroethane from enthalpy of combustion and equilibrium studies,
J. Chem. Thermodyn., 1972, 4, 239-245. [all data]
Cox and Pilcher, 1970
Cox, J.D.; Pilcher, G.,
Thermochemistry of Organic and Organometallic Compounds, Academic Press, New York, 1970, 1-636. [all data]
Hu and Sinke, 1969
Hu, A.T.; Sinke, G.C.,
Combustion calorimetry of some chlorinated organic compounds,
J. Chem. Thermodyn., 1969, 1, 507-513. [all data]
Mansson, Ringner, et al., 1971
Mansson, M.; Ringner, B.; Sunner, S.,
The enthalpies of combustion and formation of some simple chloroalkanes and chloralkenes 1,1,1-trichloroethane and 1,1-dichloroethene,
J. Chem. Thermodyn., 1971, 3, 547-551. [all data]
Levanova, Treger, et al., 1975
Levanova, S.V.; Treger, Yu.A.; Velichko, S.M.; Rozhnov, A.M.; Bshneva, L.I.; Talanov, A.I.,
Equilibrium of the vinylidene chloride-methylchloroform system,
Zh. Prikl. Khim. (Leningrad), 1975, 42, 480-481. [all data]
Andon, Counsell, et al., 1973
Andon, R.J.L.; Counsell, J.F.; Lee, D.A.; Martin, J.F.,
Thermodynamic properties of aliphatic halogen compounds. Part 2. Heat capacity of 1,1,1-trichloroethane,
J. Chem. Soc. Faraday Trans., 1973, I 69, 1721-1726. [all data]
Rubin, Levedahl, et al., 1944
Rubin, T.R.; Levedahl, B.H.; Yost, D.M.,
The heat capacity, heat of transition, vaporization, vapor pressure and entropy of 1,1,1-trichloroethane,
J. Am. Chem. Soc., 1944, 66, 279-282. [all data]
Crowe and Smyth, 1950
Crowe, R.W.; Smyth, C.P.,
Heat capacities, dielectric constants and molecular rotational freedom in solid trichloroethanes and disubstituted propanes,
J. Am. Chem. Soc., 1950, 72, 4009-4015. [all data]
Martin and Monti, 1988
Martin, C.A.; Monti, G.A.,
Specific heat analysis in 1,1,1-trichloroethane,
Thermochim. Acta, 1988, 134, 27-34. [all data]
Levanova, Bushneva, et al., 1979
Levanova, s.V.; Bushneva, I.I.; Rodova, R.M.; Rozhnov, A.M.; Treger, Yu.A.; Aprelkin, A.S.,
Thermodynamic stability of chloroethanes in dehydrochlorination reactions,
J. Appl. Chem. USSR, 1979, 52, 1439-1442. [all data]
Levanova, Treger, et al., 1975, 2
Levanova, S.V.; Treger, Yu.A.; Velichko, S.M.; Rozhnov, A.M.; Khlestkov, A.I.; Pisarev, V.V.,
Liquid-phase hydrochlorination of symmetrical dichloroethylenes,
J. Appl. Chem. USSR, 1975, 48, 1628-1631, In original 1574. [all data]
Barr and Newsham, 1987
Barr, R.S.; Newsham, D.M.T.,
Phase Equilibrtia in Very Dilute Mixtures of Water and Chlorinated Hydrocarbons. Part I - Experimental Results,
Fluid Phase Equilibria, 1987, 35, 189-205. [all data]
Gossett, 1987
Gossett, J.M.,
Measurement of Henry's Law Constants for C1 and C2 Chlorinated Hydrocarbons,
Environ. Sci. Technol., 1987, 21, 202-208. [all data]
Leighton and Calo, 1981
Leighton, D.T.; Calo, J.M.,
Distribution Coefficients of Chlorinated Hydrocarbons in Dilute Air-Water Systems for Groundwater Contamination Applications,
J. Chem. Eng. Data, 1981, 26, 382-385. [all data]
Pearson and McConnell, 1975
Pearson, C.R.; McConnell, G.,
Chlorinated C1 and C2 Hydrocarbons in the Marine Environment,
Proc. R. Soc. London, B, 1975, 189, 305-332. [all data]
Notes
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Reaction thermochemistry data, Henry's Law data, References
- Symbols used in this document:
Cp,liquid Constant pressure heat capacity of liquid Cp,solid Constant pressure heat capacity of solid S°liquid Entropy of liquid at standard conditions d(ln(kH))/d(1/T) Temperature dependence parameter for Henry's Law constant k°H Henry's Law constant at 298.15K ΔcH°liquid Enthalpy of combustion of liquid at standard conditions ΔfH°gas Enthalpy of formation of gas at standard conditions ΔfH°liquid Enthalpy of formation of liquid at standard conditions ΔrH° Enthalpy of reaction at standard conditions - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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