Info

Greek letters

oc

Relative volatility

y

Activity coefficient

<J> Fugacity coefficient

<J> Fugacity coefficient

<|> Poynting pressure correction term

1.3.3 Subscripts

1,2 Component number. In a binary system, 1 signifies the more-volatile component, 2 the less-volatile component.

ij Components in mixture r Ratio

1.3.4 Superscripts

L Liquid V Vapor

1.4 References

2. Underwood, A. J. V., Trans. Inst. Ckem. Engrs. 13, 34, 1935.

3. Forbes, R. J., Short History of the Art of Distillation, E. J. Brill, Leiden, 1948.

4. Haselden, G. G., in P. N. Snowden, Practical Distillation—A Post Experience Course, University of Leeds, 1981.

5. Rush, F. E„ I. Ckem. E. Symp. Ser. 56, p. 4.1.1,1979.

6. Zuiderweg, F. J., Chem. Engr. Centenary Supplement, p. 44, Dec. 1988.

8. Ellis, S. R. M., and A. P. Boyes, Trans. Inst. Ckem. Engrs. (London), 52, 202,1974.

9. Prausnitz, J. M., C. A. Eckert, R. V. Opre, and J. P. O'CoimeLL, Computer Calculation for Multicomponent Vapor-Liquid Equilibrium, Prentice-Hall, Englewood Cliffs, N.J., 1967.

10. Prausnitz, J. M., T. Anderson, E. Grens, C. Eckert, R. Hsieh, and J. O'Connell, Computer Calculations for Multicomponent Vapor-Liquid and Liquid-Liquid Equilibria, Prentice-Hall, Englewood Cliffs, N.J., 1980.

11. Reid, R. C., J. M. Prausnitz, and T. K. Sherwood, The Properties of Gases and Liquids, 3d ed., McGraw-Hill, New York, 1977.

12. Edimister, W. C., Applied Hydrocarbon Thermodynamics, vol. 1, 2d ed., Gulf Publishing, Houston, Texas, 1984.

13. American Petroleum Institute, Technical Data Book—Petroleum Refining, 3d ed., API, Division of Refining, Washington, 1976.

14. GPA Engineering Data Book, 9th ed., Tulsa, 1981.

15. Null, H. R., Phase Equilibrium in Process Design, Wiley-Interstience, New York, 1970.

16. Hala, E., J. Pick, V. Fried, and O. Vilim, Vapor-Liquid Equilibrium, 2d ed., Perg&mon Press, London, 1968.

17. Hala, E., I. Wichterle, J. Polak, and T. Boublik, Vapor-Liquid Equilibrium Data at Normal Pressures, Pergamon Press, Oxford, 1968.

18. Wichterle, I., J. Linek, and E. Hala, Vapor-Liquid Equilibrium Data Bibliography, Elsevier, Amsterdam, 1973; Vapor-Liquid Equilibrium Data Bibliography—Supplement /, Elsevier, Amsterdam, 1976.

19. Gmehling, J., and U. Onken, Vapor-Liquid Equilibrium Data Collection, DECHEMA Chemistry Data Series, Frankfurt, 1977.

20. Hiza, M. J., A- J. Kidnay, and R. C. Miller, Equilibrium Properties of Fluid Mix-tures—A Bibliography of Data on Fluids of Cryogenic Interest, NSRDS Bibliography Series, Plenum, New York, 1975.

21. Hicks, C. P., "Bibliography of Thermodynamic Quantities for Binary Fluid Mixtures," in M. L. McGlashan fed.), Chemical Thermodynamics, vol. 2, Chem. Soc., London, 1978.

22. Hirata, M., S. Ohe, and K. Nagahama, Computer Aided Data Book of Vapor-Liquid Equilibria, Elsevier, Amsterdam, 1975,

23. Palmer, D. A., Handbook of Applied Thermodynamics, CRC Press, Boca Raton, Fla., 1987.

24. Fredenslund, A., J. Gmehling, and P. Rasmussen, Vapor-Liquid Equilibria Using UN IF AC, Elsevier, Amsterdam, 1977.

25. Roy, P., and G. K. Hobson, I. Chem. E, Symp. Ser. 104, p. A273, 1987.

26. Heidemann, R. A., and A. Fredenslund, I, Chem. E. Symp. Ser. 104, p. A291, 1987.

27. Mathur, G. P., and M. B. Powley in E. J. Henley (ed.), Stagewise and Mass Transfer Operations, vol. 1, A.I.Ch.E. Modular Instruction, 1980.

28. Doig, I. D„ Aust. Ckem. Eng., 12(7), 5, 1971.

29. Robinson, C. S., and E. R. Gilliland, Elements of Fractional Distillation, McGraw-Hill, New York, 1950.

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