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Production of Butyric Acid from Glucose and Xylose with Immobilized Cells of Clostridium tyrobutyricum in a Fibrous-bed Bioreactor

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Abstract

Butyric acid has many applications in chemical, food, and pharmaceutical industries. In the present study, Clostridium tyrobutyricum ATCC 25755 was immobilized in a fibrous-bed bioreactor to evaluate the performance of butyrate production from glucose and xylose. The results showed that the final concentration and yield of butyric acid were 13.70 and 0.46 g g−1, respectively, in batch fermentation when 30 g L−1 glucose was introduced into the bioreactor. Furthermore, high concentration 10.10 g L−1 and yield 0.40 g g−1 of butyric acid were obtained with 25 g L−1 xylose as the carbon source. The immobilized cells of C. tyrobutyricum ensured similar productivity and yield from repeated batch fermentation. In the fed-batch fermentation, the final concentration of butyric acid was further improved to 24.88 g L−1 with one suitable glucose feeding in the fibrous-bed bioreactor. C. tyrobutyricum immobilized in the fibrous-bed bioreactor would provide an economically viable fermentation process to convert the reducing sugars derived from plant biomass into the final bulk chemical (butyric acid).

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Acknowledgements

This work was supported by a grant from the Ministry of Science and Technology of China (National Basic Research Program of China, 2007CB707805).

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Correspondence to Jufang Wang or Zhinan Xu.

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Jiang, L., Wang, J., Liang, S. et al. Production of Butyric Acid from Glucose and Xylose with Immobilized Cells of Clostridium tyrobutyricum in a Fibrous-bed Bioreactor. Appl Biochem Biotechnol 160, 350–359 (2010). https://doi.org/10.1007/s12010-008-8305-1

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