Acetic acid ethenyl ester

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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:
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
BS - Robert L. Brown and Stephen E. Stein
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
AC - William E. Acree, Jr., James S. Chickos

Quantity Value Units Method Reference Comment
Tboil345.7 ± 0.6KAVGN/AAverage of 9 values; Individual data points
Quantity Value Units Method Reference Comment
Tfus172.95KN/ADolliver, Gresham, et al., 1938Uncertainty assigned by TRC = 0.3 K; TRC
Quantity Value Units Method Reference Comment
Tc519.13KN/ADaubert, Jalowka, et al., 1987Uncertainty assigned by TRC = 0.4 K; TRC
Quantity Value Units Method Reference Comment
Pc41.85barN/ADaubert, Jalowka, et al., 1987Uncertainty assigned by TRC = 0.09 bar; TRC
Quantity Value Units Method Reference Comment
Δvap37.2 ± 0.84kJ/molVVilcu and Perisanu, 1980ALS

Enthalpy of vaporization

ΔvapH (kJ/mol) Temperature (K) Method Reference Comment
34.4309.AStephenson and Malanowski, 1987Based on data from 294. - 346. K. See also Dykyj, 1971, Capková and Fried, 1963, and Boublik, Fried, et al., 1984.; AC
31.4348.N/ASwamy and Van Winkle, 1965Based on data from 340. - 355. K.; AC

Antoine Equation Parameters

log10(P) = A − (B / (T + C))
    P = vapor pressure (bar)
    T = temperature (K)

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Temperature (K) A B C Reference Comment
340. - 355.5.228411807.3320.726Swamy and Van Winkle, 1965Coefficents calculated by NIST from author's data.
294.98 - 345.194.340321299.069-46.183Capková and Fried, 1963Coefficents calculated by NIST from author's data.

Enthalpy of fusion

ΔfusH (kJ/mol) Temperature (K) Reference Comment
8.46180.6Kulagina and Lebedev, 1997AC

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:


References

Go To: Top, Phase change data, Notes

Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.

Dolliver, Gresham, et al., 1938
Dolliver, M.A.; Gresham, T.L.; Kistiakowsky, G.B.; Smith, E.A.; Vaughan, W.E., Heats of Organic Reactions VI. Heats of Hydrogenation of Some Oxygen- Containing Compounds, J. Am. Chem. Soc., 1938, 60, 440. [all data]

Daubert, Jalowka, et al., 1987
Daubert, T.E.; Jalowka, J.W.; Goren, V., Vapor pressure of 22 pure industrial chemicals, AIChE Symp. Ser., 1987, 83, 256, 128-156. [all data]

Vilcu and Perisanu, 1980
Vilcu, R.; Perisanu, S., The ideal gas state enthalpies of formation of some monomers, Rev. Roum. Chim., 1980, 25, 619-624. [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, 1971
Dykyj, J., Petrochemia, 1971, 11, 2, 27. [all data]

Capková and Fried, 1963
Capková, A.; Fried, V., Gleichgewicht flüssigkeit-dampf XXX. System vinylacetat-essigsäure, Collect. Czech. Chem. Commun., 1963, 28, 8, 2235-2239, https://doi.org/10.1135/cccc19632235 . [all data]

Boublik, Fried, et al., 1984
Boublik, T.; Fried, V.; Hala, E., The Vapour Pressures of Pure Substances: Selected Values of the Temperature Dependence of the Vapour Pressures of Some Pure Substances in the Normal and Low Pressure Region, 2nd ed., Elsevier, New York, 1984, 972. [all data]

Swamy and Van Winkle, 1965
Swamy, P.A.; Van Winkle, Matthew, Vapor-Liquid Equilibria at 760 Mm. Mercury for the System Vinyl Acetate-2,4-Dimethyl Pentane., J. Chem. Eng. Data, 1965, 10, 3, 214-215, https://doi.org/10.1021/je60026a002 . [all data]

Kulagina and Lebedev, 1997
Kulagina, T.G.; Lebedev, B.V., Thermodynamic properties of vinyl acetate at 0-330 K, Zh. Fiz. Khim., 1997, 71, 4, 601. [all data]


Notes

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