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High Pressure Ternary Equilibrium in Aqueous — Hydrocarbon Systems

  • C. A. Irani
  • D. J. McHugh

Abstract

The possibility of using water as a solvent for aromatics extraction was first demonstrated by Arnold and Coghlan [1] in 1948 when they successfully extracted a nitration grade toluene from reformed naphtha. Experimental and theoretical work performed since then has led to a better understanding of the phase behavior of these systems. It is now possible to predict at least qualitatively and in a few instances quantitatively their binary equilibrium.

Keywords

Binodal Curve Sand Bath Batch Extractor Hydrocarbon Phase Back Pressure Regulator 
These keywords were added by machine and not by the authors. This process is experimental and the keywords may be updated as the learning algorithm improves.

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References

  1. 1.
    G. B. Arnold and C. A. Coghlan, Ind. Eng. Chem. 42, 177 (1950).CrossRefGoogle Scholar
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    J. S. Rowlinson, Liquids and Liquid Mixtures, Butterworths, London (1969).Google Scholar
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    C. J. Rebert and W. B. Kay, AIChEJ 5, 285 (1959).Google Scholar
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    G. Schneider, Chem. Eng. Prog. Sym. Series 64 (88), 9 (1968).Google Scholar
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    T. M. Grady, J. Chem. Eng. Data 12, 9 (1967).CrossRefGoogle Scholar
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    J. M. Prausnitz and P. L. Chueh, Computer Calculations for High Pressure Vapor-Liquid Equilibrium, Prentice-Hall, New Jersey (1968).Google Scholar

Copyright information

© Springer Science+Business Media New York 1979

Authors and Affiliations

  • C. A. Irani
    • 1
  • D. J. McHugh
    • 1
  1. 1.Exxon Research and Engineering CompanyLindenUSA

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