Ethene, 1,1-dichloro-

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
Δfgas2. ± 2.kJ/molReviewManion, 2002derived from recommended ΔfHliquid° and ΔvapH°; DRB
Δfgas2.2 ± 1.4kJ/molCcrMansson, Ringner, et al., 1971ALS

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
Δfliquid-24. ± 2.kJ/molReviewManion, 2002weighted average of several measurements; DRB
Δfliquid-24.3 ± 1.4kJ/molCcrMansson, Ringner, et al., 1971ALS
Δfliquid-25. ± 1.kJ/molCcbSinke and Stull, 1958ALS
Quantity Value Units Method Reference Comment
Δcliquid-1096.0 ± 1.4kJ/molCcrMansson, Ringner, et al., 1971ALS
Δcliquid-1095.9kJ/molCcbSinke and Stull, 1958ALS
Quantity Value Units Method Reference Comment
liquid201.54J/mol*KN/AHildenbrand, McDonald, et al., 1959DH

Constant pressure heat capacity of liquid

Cp,liquid (J/mol*K) Temperature (K) Reference Comment
111.29298.15Hildenbrand, McDonald, et al., 1959T = 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
Tboil304.2KN/AAldrich Chemical Company Inc., 1990BS
Tboil304.55KN/AKovac, Svoboda, et al., 1985Uncertainty assigned by TRC = 0.2 K; TRC
Tboil304.7KN/AMajer and Svoboda, 1985 
Quantity Value Units Method Reference Comment
Ttriple150.59KN/AHildenbrand, McDonald, et al., 1959, 2Uncertainty assigned by TRC = 0.02 K; TRC
Quantity Value Units Method Reference Comment
Δvap26.74kJ/molN/AMajer and Svoboda, 1985 
Δvap26.74 ± 0.09kJ/molReviewManion, 2002derived from vapor pressure data of Hildebranld, Kramer, et al., 1959 plus a correction for non-ideality; DRB
Δvap26.48 ± 0.08kJ/molCMansson, Ringner, et al., 1971ALS
Δvap26.48 ± 0.084kJ/molVHildenbrand, McDonald, et al., 1959ALS

Enthalpy of vaporization

ΔvapH (kJ/mol) Temperature (K) Method Reference Comment
26.14304.7N/AMajer and Svoboda, 1985 
26.476298.15N/AHildenbrand, McDonald, et al., 1959P = 80.03 kPa; DH
28.4260.AStephenson and Malanowski, 1987Based 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
88.80298.15Hildenbrand, McDonald, et al., 1959P; 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 305.74.10781104.726-35.403Hildenbrand, McDonald, et al., 1959Coefficents calculated by NIST from author's data.

Enthalpy of fusion

ΔfusH (kJ/mol) Temperature (K) Reference Comment
6.514150.59Hildenbrand, McDonald, et al., 1959DH
6.51150.9Domalski and Hearing, 1996AC

Entropy of fusion

ΔfusS (J/mol*K) Temperature (K) Reference Comment
43.26150.59Hildenbrand, McDonald, et al., 1959DH

In addition to the Thermodynamics Research Center (TRC) data available from this site, much more physical and chemical property data is available from the following TRC products:


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) = H exp(d(ln(kH))/d(1/T) ((1/T) - 1/(298.15 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)

H (mol/(kg*bar)) d(ln(kH))/d(1/T) (K) Method Reference Comment
0.0344000.LN/A 
0.0373100.XN/A 
0.043 QN/A missing citation give several references for the Henry's law constants but don't assign them to specific species.
0.0344500.XN/A 
0.0372900.XN/A 
0.0393700.MGossett, 1987 
0.0651200.XN/A 
0.0274600.XLeighton and Calo, 1981 
0.0076 LN/A 
0.0146600.XN/A 
0.0052 VN/A 
0.0061 VN/AValue at T = 293. K.
0.0065 MPearson and McConnell, 1975The 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