Recirculating bioreactor-separator system for simultaneous biotransformation and recovery of product: Immobilized L-aspartate beta-decarboxylase reactor system.
A new combined bioreactor-separator system was designed and its operational feasibility demonstrated in order to develop a bioprocess that enables us to handle simultaneous biotransformation and recovery of product by crystallization. Enzymatic conversion of L-aspartate to L-alanine by L-aspartate beta-decarboxylase from Pseudomonas dacunhae (ATCC 21192) was used as a model system for this study to demonstrate the principles involved in the bioprocess design. Immobilized cells of P. dacunhae containing the enzyme were fluidized in a tapered column type of bioreactor and a filter-crystallizer combination was used as a separator unit in our experimental system.It was found that almost a theoretical yield was achieved, and the process control for both the bioreactor operation and separation was relatively easy. The Production systems, namely, the recirculating bioreactor separator combination system and the conventional batch reactor system, were analyzed and compared based on the results obtained form this study, and it was found that a significant cost reduction, by about 20%, can be achieved when the recirculating bioreactor-separator combination system was employed. Based on these findings, it is anticipated that the conceptual design of the bioreactor-separator combination system evaluated in this study has some potential for industrial application.
Takamatsu
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Department of Chemical Engineering, University of California, Davis, California 95616.
Ryu
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