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A nonlinear integral equation relating distillation processes

  • E. R. Rang
Conference paper
Part of the Lecture Notes in Mathematics book series (LNM, volume 312)

Abstract

Examples of the calculation are shown in the figures for data from Reference 1 on samples of gasolines and oil mixtures. The differential distillation curves which we calculate do not completely match the ASTM results. Possibly this is because some reflux action occurs in the ASTM procedure.

Keywords

Nonlinear Integral Equation Distillation Process Extractive Distillation Equilibrium Ratio Distillation Curve 
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.
    R. L. Geddes, "Computation of Petroleum Fractionation," Ind. and Eng. Chem. Vol. 33, No. 6, June 1941, 795–801.CrossRefGoogle Scholar
  2. 2.
    W. C. Edmister and K. I. Okamoto, "Applied Hydrocarbon Thermodynamics, Part 12: Equilibrium Flash Vaporization Calculation for Petroleum Fractions," Petroleum Refiner, Vol. 38, No. 8, August 1959, 117–129.Google Scholar
  3. 3.
    W. C. Edmister, Applied Hydrocarbon Thermodynamics, Gulf Publishing Co., Houston, 1961.Google Scholar
  4. 4.
    M. Van Winkle, "Easy Way to Figure EFV and TBP," Hydrocarbon Processing and Petroleum Refiner, Vol. 43, No. 4, April 1964, 139–142.Google Scholar
  5. 5.
    M. Van Winkle, Distillation, McGraw-Hill, 1967.Google Scholar
  6. 6.
    W. L. Nelson, Petroleum Refining Engineering, Fourth Edition, McGraw-New York, 1958, 111–120.Google Scholar
  7. 7.
    E. J. Hoffman, "Relations between true boiling point and ASTM distillation curves," Chem. Eng. Sci., 1969, Vol. 24, 113–117.CrossRefGoogle Scholar
  8. 8.
    E. J. Hoffman, "Differential vaporization curves for complex mixtures," Chem. Eng. Sci., 1969, Vol. 24, 1736–38.CrossRefGoogle Scholar
  9. 9.
    E. J. Hoffman, Azeotropic and Extractive Distillation, Interscience Pub. 1964, 75–89.Google Scholar
  10. 10.
    S. S. Gandbhir and P. S. Virk, "Rapid interconversion between ASTM and TBP distillations," Oil and Gas J., January 11, 1971, 53–55.Google Scholar
  11. 11.
    J. B. Maxwell, Data Book on Hydrocarbons, D. van Nostrand, 1950, pp. 222–229.Google Scholar
  12. 12.
    D. L. Taylor and W. C. Edmister, "Solutions for Distillation Processes Treating Petroleum Fractions," AIChE Journal Vol. 17, No. 6, Nov. 1971, 1324–1329.CrossRefGoogle Scholar
  13. 13.
    O. H. Hariu and R. C. Sage, "Crude Split Figured by Computer," Hydrocarbon Proc., April 1969, 143–148.Google Scholar
  14. 14.
    J. D. Baker and E. R. Rang, "Modeling processes with integral operators: application to distillation correlation," Proceedings of the 1972 Summer Simulation Conference, June 13–16, San Diego, Calif.Google Scholar
  15. 15.
    J. B. Maxwell and L. S. Bonnell, Derivation and Precision of a New Vapor Pressure Correlation for Petroleum Hydrocarbons," Ind. Eng. Chem. Vol. 49, No. 7 (1959), 1187–1196.CrossRefGoogle Scholar
  16. 16.
    R. A. Williams and E. J. Henley, "A Comprehensive Vapor-Liquid Equilibrium Computer Program — KVALUE," Chem. Eng. J., Vol. 1, 1970, 145–151.CrossRefGoogle Scholar
  17. 17.
    F. O. Mixon, B. Gumowski and B. H. Carpenter, "Computation of Vapor-Liquid Equilibrium Data from Solution Vapor Pressure Measurements," Inc. and Eng. Chem. Fundamentals, Vol. 4, No. 4, Nov. 1965, 455–459.CrossRefGoogle Scholar

Copyright information

© Springer-Verlag 1973

Authors and Affiliations

  • E. R. Rang

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