Ethene, 1,1-dichloro-
- Formula: C2H2Cl2
- Molecular weight: 96.943
- IUPAC Standard InChIKey: LGXVIGDEPROXKC-UHFFFAOYSA-N
- CAS Registry Number: 75-35-4
- 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: Ethylene, 1,1-dichloro-; Vinylidene chloride; 1,1-Dichloroethene; 1,1-Dichloroethylene; CH2=CCl2; Chlorure de vinylidene; 1,1-DCE; NCI-C54262; Rcra waste number U078; VDC; Vinylidene dichloride; Vinylidine chloride; 1,1-dichloroethylene (vinylidine chloride); 1,1-dichloroethylene (vinylidene chloride)
- Permanent link for this species. Use this link for bookmarking this species for future reference.
- Information on this page:
- Other data available:
- Data at other public NIST sites:
- Options:
Data at NIST subscription sites:
NIST subscription sites provide data under the NIST Standard Reference Data Program, but require an annual fee to access. The purpose of the fee is to recover costs associated with the development of data collections included in such sites. Your institution may already be a subscriber. Follow the links above to find out more about the data in these sites and their terms of usage.
Gas phase thermochemistry data
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 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 | 2. ± 2. | kJ/mol | Review | Manion, 2002 | derived from recommended ΔfHliquid° and ΔvapH°; DRB |
ΔfH°gas | 2.2 ± 1.4 | kJ/mol | Ccr | Mansson, Ringner, et al., 1971 | ALS |
Condensed phase thermochemistry data
Go To: Top, Gas 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 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 | -24. ± 2. | kJ/mol | Review | Manion, 2002 | weighted average of several measurements; DRB |
ΔfH°liquid | -24.3 ± 1.4 | kJ/mol | Ccr | Mansson, Ringner, et al., 1971 | ALS |
ΔfH°liquid | -25. ± 1. | kJ/mol | Ccb | Sinke and Stull, 1958 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -1096.0 ± 1.4 | kJ/mol | Ccr | Mansson, Ringner, et al., 1971 | ALS |
ΔcH°liquid | -1095.9 | kJ/mol | Ccb | Sinke and Stull, 1958 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
S°liquid | 201.54 | J/mol*K | N/A | Hildenbrand, McDonald, et al., 1959 | DH |
Constant pressure heat capacity of liquid
Cp,liquid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
111.29 | 298.15 | Hildenbrand, McDonald, et al., 1959 | T = 13 to 290 K.; DH |
Phase change data
Go To: Top, Gas phase thermochemistry data, Condensed phase 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:
BS - Robert L. Brown and Stephen E. Stein
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
DRB - Donald R. Burgess, Jr.
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
DH - Eugene S. Domalski and Elizabeth D. Hearing
AC - William E. Acree, Jr., James S. Chickos
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 304.2 | K | N/A | Aldrich Chemical Company Inc., 1990 | BS |
Tboil | 304.55 | K | N/A | Kovac, Svoboda, et al., 1985 | Uncertainty assigned by TRC = 0.2 K; TRC |
Tboil | 304.7 | K | N/A | Majer and Svoboda, 1985 | |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 150.59 | K | N/A | Hildenbrand, McDonald, et al., 1959, 2 | Uncertainty assigned by TRC = 0.02 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 26.74 | kJ/mol | N/A | Majer and Svoboda, 1985 | |
ΔvapH° | 26.74 ± 0.09 | kJ/mol | Review | Manion, 2002 | derived from vapor pressure data of Hildebranld, Kramer, et al., 1959 plus a correction for non-ideality; DRB |
ΔvapH° | 26.48 ± 0.08 | kJ/mol | C | Mansson, Ringner, et al., 1971 | ALS |
ΔvapH° | 26.48 ± 0.084 | kJ/mol | V | Hildenbrand, McDonald, et al., 1959 | ALS |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
26.14 | 304.7 | N/A | Majer and Svoboda, 1985 | |
26.476 | 298.15 | N/A | Hildenbrand, McDonald, et al., 1959 | P = 80.03 kPa; DH |
28.4 | 260. | A | Stephenson and Malanowski, 1987 | Based on data from 245. to 305. K. See also Hildenbrand and McDonald, 1959 and Dykyj, 1970.; AC |
Entropy of vaporization
ΔvapS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
88.80 | 298.15 | Hildenbrand, McDonald, et al., 1959 | P; DH |
Antoine Equation Parameters
log10(P) = A − (B / (T + C))
P = vapor pressure (bar)
T = temperature (K)
View plot Requires a JavaScript / HTML 5 canvas capable browser.
Temperature (K) | A | B | C | Reference | Comment |
---|---|---|---|---|---|
244.79 to 305.7 | 4.1078 | 1104.726 | -35.403 | Hildenbrand, McDonald, et al., 1959 | Coefficents calculated by NIST from author's data. |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
6.514 | 150.59 | Hildenbrand, McDonald, et al., 1959 | DH |
6.51 | 150.9 | Domalski and Hearing, 1996 | AC |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
43.26 | 150.59 | Hildenbrand, McDonald, et al., 1959 | DH |
Henry's Law data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change 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: 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 |
---|---|---|---|---|
0.034 | 4000. | L | N/A | |
0.037 | 3100. | X | N/A | |
0.043 | Q | N/A | missing citation give several references for the Henry's law constants but don't assign them to specific species. | |
0.034 | 4500. | X | N/A | |
0.037 | 2900. | X | N/A | |
0.039 | 3700. | M | Gossett, 1987 | |
0.065 | 1200. | X | N/A | |
0.027 | 4600. | X | Leighton and Calo, 1981 | |
0.0076 | L | N/A | ||
0.014 | 6600. | X | N/A | |
0.0052 | V | N/A | ||
0.0061 | V | N/A | Value at T = 293. K. | |
0.0065 | 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, Phase change 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]
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]
Sinke and Stull, 1958
Sinke, G.C.; Stull, D.R.,
Heats of combustion of some organic compounds containing chlorine,
J. Phys. Chem., 1958, 62, 397-401. [all data]
Hildenbrand, McDonald, et al., 1959
Hildenbrand, d.L.; McDonald, R.A.; Kramer, W.R.; Stull, D.R.,
Thermodynamic and spectroscopic study of vinylidene chloride. I. Thermodynamic properties of the solid, liquid, and ideal gas,
J. Chem. Phys., 1959, 30, 930-934. [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]
Kovac, Svoboda, et al., 1985
Kovac, A.; Svoboda, J.; Ondrus, I.,
Vapor-liquid equilibrium of some binary systems containing 1,1-dichloroethylene,
Chem. Zvesti, 1985, 39, 6, 729. [all data]
Majer and Svoboda, 1985
Majer, V.; Svoboda, V.,
Enthalpies of Vaporization of Organic Compounds: A Critical Review and Data Compilation, Blackwell Scientific Publications, Oxford, 1985, 300. [all data]
Hildenbrand, McDonald, et al., 1959, 2
Hildenbrand, D.L.; McDonald, R.A.; Kramer, W.R.; Stull, D.R.,
Thermodyn. and spectroscopic study of vinylidene chloride. I. Thermodyn. properties of the solid, liquid, and ideal gas,
J. Chem. Phys., 1959, 30, 930-4. [all data]
Hildebranld, Kramer, et al., 1959
Hildebranld, D.L.; Kramer, W.K.; McDonald, R.A.; Stull, D.R.,
Thermodynamic and Spectroscopic Study of Vinylidene Chloride. I. Thermodynamic Properties of the Solid, Liquid, and Ideal Gas,
J. Chem. Phys., 1959, 30, 4, 930, https://doi.org/10.1063/1.1730128
. [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]
Hildenbrand and McDonald, 1959
Hildenbrand, D.L.; McDonald, R.A.,
The Heat of Vaporization and Vapor Pressure of Carbon Tetrachloride; The Entropy from Calorimetric Data.,
J. Phys. Chem., 1959, 63, 9, 1521-1522, https://doi.org/10.1021/j150579a053
. [all data]
Dykyj, 1970
Dykyj, J.,
Petrochemica, 1970, 10, 2, 51. [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]
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, Phase change data, Henry's Law data, References
- Symbols used in this document:
Cp,liquid Constant pressure heat capacity of liquid S°liquid Entropy of liquid at standard conditions Tboil Boiling point 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 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 ΔfusH Enthalpy of fusion ΔfusS Entropy of fusion ΔvapH Enthalpy of vaporization ΔvapH° Enthalpy of vaporization at standard conditions ΔvapS Entropy of vaporization - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
- The National Institute of Standards and Technology (NIST) uses its best efforts to deliver a high quality copy of the Database and to verify that the data contained therein have been selected on the basis of sound scientific judgment. However, NIST makes no warranties to that effect, and NIST shall not be liable for any damage that may result from errors or omissions in the Database.
- Customer support for NIST Standard Reference Data products.