A novel enzyme reactor using gluten membrane entrapping cell-associated enzyme
Article first published online: 12 NOV 2001
DOI: 10.1002/bit.10100
Copyright © 2001 John Wiley & Sons, Inc.
Additional Information
How to Cite
Lee, W.-C. and Guo, S.-H. (2001), A novel enzyme reactor using gluten membrane entrapping cell-associated enzyme. Biotechnol. Bioeng., 76: 311–317. doi: 10.1002/bit.10100
Publication History
- Issue published online: 12 NOV 2001
- Article first published online: 12 NOV 2001
- Manuscript Accepted: 16 AUG 2001
- Manuscript Received: 4 MAY 2001
Funded by
- National Science Council of Republic of China. Grant Number: NSC 88-2216-E-194-001
- Abstract
- References
- Cited By
Keywords:
- membrane enzyme reactor;
- gluten;
- immobilized biocatalyst;
- penicillin G acylase;
- cell-associated enzyme
Abstract
A membrane enzyme reactor consisting of variable pieces of replaceable cell-immobilized membranes was proposed for the continuous production of bioproducts. To demonstrate the characteristics of the reactor, cell-immobilized membranes were prepared by the entrapment of permeabilized recombinant Escherichia coli cells containing penicillin G acylase within the gluten matrices. A stainless-steel net that was created with a mesh frame was used to support each gluten membrane so that the membranes could be filled into the rectangular-shaped reactor. The reactor equipped with either six or 12 pieces of cell-immobilized gluten membranes containing a biomass concentration of 5%, w/w was effective in catalyzing the production of 6-aminopenicillanic acid from penicillin G. In comparison with intact cells, the cell-immobilized preparation was more stable and the half-life time of the immobilized cell-associate enzyme in gluten membrane was estimated to be 36 days by a long-term operation. As the substrate solution was forced to flow through the reactor equipped with six membranes and in the direction perpendicular to the membranes, the pressure drop was determined to be less than 50 cm H2O with a flow-rate up to 50 mL/min. This low pressure due to the porous structure of gluten membrane would lead to a lower operational cost. Increasing either the number of membranes or the area of each cell-immobilized membrane can easily do scaling-up of this membrane reactor. © 2001 John Wiley & Sons, Inc. Biotechnol Bioeng 76: 311–317, 2001.

1097-0290/asset/BIT_left.gif?v=1&s=5f6054ce9ff7b0421e44e8e4e33966356f37b71c)
1097-0290/asset/cover.gif?v=1&s=169bf64713ffd27abfe496301dbedc7070f98e92)