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Enhanced 2,3-butanediol production by Klebsiella oxytoca using a two-stage agitation speed control strategy
- Source :
-
Bioresource Technology . Jul2009, Vol. 100 Issue 13, p3410-3414. 5p. - Publication Year :
- 2009
-
Abstract
- Batch fermentative production of 2,3-butanediol by Klebsiella oxytoca was investigated using various oxygen supply methods though varying agitation speed. Based on the analysis of three kinetic parameters including specific cell growth rate (μ), specific glucose consumption rate (qs ) and specific 2,3-butanediol formation rate (qp ), a two-stage agitation speed control strategy, aimed at achieving high concentration, high yield and high productivity of 2,3-butanediol, was proposed. At the first 15h, agitation speed was controlled at 300rpm to obtain high μ for cell growth, subsequently agitation speed was controlled at 200rpm to maintain high qp for high 2,3-butanediol accumulation. Finally, the maximum concentration of 2,3-butanediol reached 95.5gl−1 with the yield of 0.478gg−1 and the productivity of 1.71gl−1 h−1, which were 6.23%, 6.22% and 22.14% over the best results controlled by constant agitation speeds. [Copyright &y& Elsevier]
- Subjects :
- *BUTANE
*DIACETYL
*ORGANIC compounds
*FERMENTATION
*BATCH processing
*KLEBSIELLA
Subjects
Details
- Language :
- English
- ISSN :
- 09608524
- Volume :
- 100
- Issue :
- 13
- Database :
- Academic Search Index
- Journal :
- Bioresource Technology
- Publication Type :
- Academic Journal
- Accession number :
- 37347458
- Full Text :
- https://doi.org/10.1016/j.biortech.2009.02.031