Water

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Antoine Equation Parameters

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

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

Temperature (K) A B C Reference Comment
379. - 573.3.55959643.748-198.043Liu and Lindsay, 1970Coefficents calculated by NIST from author's data.
273. - 303.5.402211838.675-31.737Bridgeman and Aldrich, 1964Coefficents calculated by NIST from author's data.
304. - 333.5.203891733.926-39.485Bridgeman and Aldrich, 1964Coefficents calculated by NIST from author's data.
334. - 363.5.07681659.793-45.854Bridgeman and Aldrich, 1964Coefficents calculated by NIST from author's data.
344. - 373.5.083541663.125-45.622Bridgeman and Aldrich, 1964Coefficents calculated by NIST from author's data.
293. - 343.6.209632354.7317.559Gubkov, Fermor, et al., 1964Coefficents calculated by NIST from author's data.
255.9 - 373.4.65431435.264-64.848Stull, 1947Coefficents calculated by NIST from author's data.

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References

Go To: Top, Antoine Equation Parameters, Notes

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

Liu and Lindsay, 1970
Liu, C.-T.; Lindsay, W.T., Jr., Vapor Pressure of D2O from 106 to 300 ºC, J. Chem. Eng. Data, 1970, 15, 4, 510-513, https://doi.org/10.1021/je60047a015 . [all data]

Bridgeman and Aldrich, 1964
Bridgeman, O.C.; Aldrich, E.W., Vapor Pressure Tables for Water, J. Heat Transfer, 1964, 86, 2, 279-286, https://doi.org/10.1115/1.3687121 . [all data]

Gubkov, Fermor, et al., 1964
Gubkov, A.N.; Fermor, N.A.; Smirnov, N.I., Vapor Pressure of Mono-Poly Systems, Zh. Prikl. Khim. (Leningrad), 1964, 37, 2204-2210. [all data]

Stull, 1947
Stull, Daniel R., Vapor Pressure of Pure Substances. Organic and Inorganic Compounds, Ind. Eng. Chem., 1947, 39, 4, 517-540, https://doi.org/10.1021/ie50448a022 . [all data]


Notes

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