DC Field | Value | Language |
---|---|---|
dc.contributor.author | Kim, Hak-Sung | ko |
dc.contributor.author | Ruy, D.D.Y. | ko |
dc.date.accessioned | 2013-02-25T19:45:52Z | - |
dc.date.available | 2013-02-25T19:45:52Z | - |
dc.date.created | 2012-02-06 | - |
dc.date.created | 2012-02-06 | - |
dc.date.issued | 1982-10 | - |
dc.identifier.citation | BIOTECHNOLOGY AND BIOENGINEERING, v.24, no.10, pp.2167 - 2174 | - |
dc.identifier.issn | 0006-3592 | - |
dc.identifier.uri | http://hdl.handle.net/10203/64803 | - |
dc.description.abstract | For the purpose of saving energy and raw materials required in glutamate fermentation, an immobilized whole-cell system was prepared, and its performance in a continuous reactor system was evaluated. Corynebacterium glutamicum (a mutant strain of ATCC 13058) whole cell was immobilized in kappa -carrageenan matrix, and the gel structure was strengthened by treatment with a hardening agent. The effect of the dilution rate on glutamate production and operational stability were investigated. The performance of the continuous whole-cell reactor system was evaluated by measuring glutamate productivity for a period of 30 days; it was found to be far superior to the performance of conventional batch reactor systems using free cells. | - |
dc.language | English | - |
dc.publisher | Wiley-VCH Verlag | - |
dc.title | Continuous glutamate production using an immobilized whole-cell system | - |
dc.type | Article | - |
dc.identifier.scopusid | 2-s2.0-0020201555 | - |
dc.type.rims | ART | - |
dc.citation.volume | 24 | - |
dc.citation.issue | 10 | - |
dc.citation.beginningpage | 2167 | - |
dc.citation.endingpage | 2174 | - |
dc.citation.publicationname | BIOTECHNOLOGY AND BIOENGINEERING | - |
dc.contributor.localauthor | Kim, Hak-Sung | - |
dc.contributor.nonIdAuthor | Ruy, D.D.Y. | - |
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