15900 HVAC Instrumentation and Controls

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16. H. Takayanagi, J. Fukuda, and E. Miyata, "Non-ionic Adsorbents in Separation Processes," in Downstream Processing of Natural Products, A Practical Handbook, M. , J. Wiley andSons, Chichester, 159-178 (1996). 17. F. X. Pollio and R. Runin, "The Use of Macroreticular Ion Exchange Resins of the Fractionation and Purification of Enzymes and Related Proteins," Chem. Eng. Symp. , 67(108), 66-74 (1971). 18. P. C. Sedek, P. W. Carr, R. M. Doherty, M. J. Kamlet, R. W. Tat~, and M. H. Abraham, "Study of Retention Processes in Reversed-Phase High-Performance Liquid Chromatography by the Use of the Solvatochromic Comparison Method," Anal.

33 (1998) 707-722. 4. N. Nagata, K. J. Herouvis, D. M. Dziewulski, and G. Belfort, Biotechnol. , 34 (1989) 447-466. 5. H. Kroner, W. Hummel, J. -R. Kula, pp. 223-232, in E. Dorioli and M. ), Membranes and Membrane Processes, Plenum Press, New York, 1986. 6. T. Tanaka, R. Kamimura, K. Itoh, K. Nakanishi, and R. Matsuno, Biotechnol. , 41 (1993)617-624. 7. T. Tanaka, S. Tsuneyoshi, W. Kitazawa, and K. Nakanishi, Sep. Sci. , 32 (1997) 1885-1898. 8. A. Kotera, K. Furusawa, and Y. Takeda, Kolloid-Zeitschrift und Zeitschrift Polymere, 230 (1970) 677-681.

It enhances the separation performance compared with the conventional RAC operation. 3. MATHEMATICAL MODEL The mathematical model is constructed by modifying the model reported in our previous work[6] on a binary separation of glutamic acid and valine using cation exchange resin packing. Figure 3 shows the schematic diagram of the states in liquid and resin phases. Mass balance in liquid phase is expressed as equation(l) by considering axial and circumferential disTemion, convection, rotation and ion exchange between the liquid and resin phases.

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