| Brazilian Archives of Biology and Technology | |
| Production of 2,3-Butanediol from Sucrose by Klebsiella pneumoniae NRRL B199 in Batch and Fed-Batch Reactors | |
| Mauricio M. Silveira2  M. Berbert-molina1  A. M. R. Prata1  W. Schmidell1  | |
| [1] ,Universidade de Caxias do Sul Depto. de Eng. Química Instituto de BiotecnologiaCaxias do Sul RS ,Brazil | |
| 关键词: Klebsiella pneumoniae; 2; 3-butanediol; fed-batch process; | |
| DOI : 10.1590/S1516-89131998000300009 | |
| 来源: SciELO | |
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【 摘 要 】
In batch mode, Klebsiella pneumoniae growth and 2,3-butanediol/acetoin formation are increasingly inhibited by initial sucrose concentrations (S0) over 60 g/L. At non inhibitory conditions, a maximum sucrose consumption rate of 1,5 g/L/h was measured. With S0=204 g/L however, this rate decreased to 0.15 g/L/h. K. pneumoniae fermented 204 g/L sucrose to produce 84.3 g/L of a mixture 2,3-butanediol/acetoin with a yield of 0.41 g/g and a productivity of 1.06 g/L/h. Higher oxygen transfer rates improved the overall process rate but the product yield was reduced. Avoiding substrate inhibition, by performing the fermentation in fed-batch mode, a final 2,3-butanediol/acetoin concentration of 80.0 g/L was achieved. In this case, a productivity of 2.63 g/L/h and a product yield of 0.37 g/g were calculated.
【 授权许可】
CC BY-NC
All the contents of this journal, except where otherwise noted, is licensed under a Creative Commons Attribution License
【 预 览 】
| Files | Size | Format | View |
|---|---|---|---|
| RO202005130164710ZK.pdf | 36KB |
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