Proceedings of the Twenty-Fifth Symposium on Biotechnology for Fuels and Chemicals Held May 4–7, 2003, in Breckenridge, CO 2004
DOI: 10.1007/978-1-59259-837-3_72
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Continuous Production of Butanol by Clostridium acetobutylicum Immobilized in a Fibrous Bed Bioreactor

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Cited by 46 publications
(65 citation statements)
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“…In continuous ABE fermentation, as the solventogenic Clostridia cells continue to undergo shifts between acidogenesis and solventogenesis, the bioreactor houses a mixture of actively dividing cells (acidogenic), non-dividing cells (solventogenic), sporulated cells, and dead cells. The oscillatory behavior of the ABE concentration in the bioreactor and effluent during the continuous ABE fermentation by C. acetobutylicum indicates that there are periods of time when the non-dividing cells (solventogenic) concentration is comparatively high or low in the bioreactor resulting in high or low ABE production (Lai and Traxler, 1994;Mulchandani and Volesky, 1994;Huang et al, 2004).…”
Section: Two-stage Abe Fermentation With Integrated Liquid-liquid Extmentioning
confidence: 99%
“…In continuous ABE fermentation, as the solventogenic Clostridia cells continue to undergo shifts between acidogenesis and solventogenesis, the bioreactor houses a mixture of actively dividing cells (acidogenic), non-dividing cells (solventogenic), sporulated cells, and dead cells. The oscillatory behavior of the ABE concentration in the bioreactor and effluent during the continuous ABE fermentation by C. acetobutylicum indicates that there are periods of time when the non-dividing cells (solventogenic) concentration is comparatively high or low in the bioreactor resulting in high or low ABE production (Lai and Traxler, 1994;Mulchandani and Volesky, 1994;Huang et al, 2004).…”
Section: Two-stage Abe Fermentation With Integrated Liquid-liquid Extmentioning
confidence: 99%
“…At a dry cell mass concentration of 8 g/L and a dilution rate of D=0.64 h [108]. Huang and Ramey [109] determined the influence of dilution rate and pH in continuous cultures of Clostridium acetobutylicum in a fibrous bed bioreactor with high cell density and butyrate concentrations at pH 5.4 and 35°C. By feeding glucose and butyrate as cosubstrates, the fermentation was maintained in the solventogenesis phase, and the optimal butanol productivity of 4.6 g L were obtained at a dilution rate of 0.9 h -1 and pH 4.3.…”
Section: Continuous Fermentationmentioning
confidence: 99%
“…In immobilized cell fermentation, cells are stationary, which have the advantages of the long survival time of cells in solventogenic phase. In one study, immobilized cell fermentation using C. acetobutylicum produced 20% higher butanol yield than did free cell fermentation [90]. However, the scale up process using immobilized technology seems to have technical problems due to excessive cell growth in the packed beds and blockage [85].…”
Section: Process Configurationmentioning
confidence: 99%