Updated model of the batch acetone-butanol fermentation
β Scribed by A. K. Srivastava; B. Volesky
- Publisher
- Springer Netherlands
- Year
- 1990
- Tongue
- English
- Weight
- 504 KB
- Volume
- 12
- Category
- Article
- ISSN
- 0141-5492
No coin nor oath required. For personal study only.
π SIMILAR VOLUMES
Clostridium acetobutylicum was grown in fed-batch cultures at different feeding rates of glucose. The sugar converted to butanol and acetone increased with increasing the glucose flow, on the contrary the conversion to butyric acid was highest st slow glucose feeding rate. The acetic acid concentrat
C. acetobutylicum B18 produced a large amount of butanol over a wide range of pH (4.5-6.0). At pH 6.0 fermentation and cell growth were most active at pH 6.0, and the highest values of glucose consumption rate (4.37 g/L-h), butanol productivity (1.0 g/L-h), butyric acid recycle rate (0.31 g/L-h), an
The productivity of the acetone-butanol fermentation was increased by continuously removing acetone and butanol from the fermentation broth during fed-batch culture. Whole broth containing viable cells of Clostridium acetobutylicum was cycled to a Karr reciprocating plate extraction column in which