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L-Sorbose production in a continuous fermenter with and without cell recycle

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Abstract

The kinetics of continuous l-sorbose fermentation using Acetobacter suboxydans with and without cell recycle (100%) were investigated at dilution rates (D) of 0.05, 0.10, 0.15 and 0.3 h−1. The biomass and sorbose concentrations for continuous fermentation without recycle increased as the dilution rate was increased from 0.05 to 0.10 h−1. A maximum biomass concentration of 8.44 g l−1 and sorbose concentration of 176.90 g l−1 were obtained at D=0.10 h−1. The specific rate of sorbose production and volumetric sorbose productivity at this dilution rate were 2.09 g g−1 h−1 and 17.69 g l−1 h−1. However, on further increasing the dilution rate to 0.3 h−1, both biomass and sorbose concentrations decreased to 2.93 and 73.20 g l−1 respectively, mainly due to washout of the reactor contents. However, the specific rate of sorbose formation and volumetric sorbose productivity at this dilution rate increased to 7.49 g g−1 h−1 and 21.96 g l−1 h−1 respectively. Continuous fermentation with 100% cell recycle served to further enhance the concentration of biomass and sorbose to 28.27 and 184.32 g l−1 respectively (in the reactor at a dilution rate of 0.05 h−1). Even though, there was a decline in the biomass and sorbose concentrations to 6.8 and 83.40 g l−1 at a dilution rate of 0.3 h−1, the specific rates of sorbose formation and volumetric sorbose productivity increased to 3.67 g g−1h−1 and 25.02 g l−1 h−1.

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References

  • Beschkov, V. & Tepavicharova, I. 1984 On the kinetics of D-sorbitol to L-sorbose oxidation by Acetobacter suboxydans. Comptes Rendus de l' Academie Bulgare des Sciences 37, 73–76.

    Google Scholar 

  • Bonomi, A., Augusto, E.F.P., Barbosa, N.S., Mattos, M.N., Magossi, L.R. & Santos, A.L. 1993 Unstructured model proposal for the microbial oxidation of D-sorbitol to L-sorbose. Journal of Biotechnology 31, 39–59.

    Google Scholar 

  • Bosjnak, M., Pintar, P. & Gomercic, K. 1991 Gradient fed-batch culture as efficient microbial oxidation method. Mededelingen van de Faculteit Landbouwwetenschappen, Rijksuniversiteit Gent 56, 1723–1730.

    Google Scholar 

  • Bourdant, J. 1990 Microbial processes for ascorbic acid biosynthesis: a review. Enzyme and Microbial Technology 12, 322–329.

    Google Scholar 

  • Bull, D.N. 1981 Enhanced product formation in continuous fermentation with microbial cell recycle. Biotechnology and Bioengineering 23, 373–389.

    Google Scholar 

  • Cheryan, M. & Mehaia, M.A. 1984 Ethanol production in a membrane recycle bioreactor. Conversion of glucose using Saccharomyces cerevisiae. Process Biochemistry 19, 206–208.

    Google Scholar 

  • Cysewski, C.R. & Wilke, C.R. 1977 Rapid ethanol fermentation using vacuum and cell recycle. Biotechnology and Bioengineering 19, 1125–1143.

    Google Scholar 

  • Damodaran, M. & Subramanian, S.S. 1951 Bacterial oxidation of sorbitol to sorbose. Journal of Scientific and Industrial Research 5, 7–13.

    Google Scholar 

  • Elenkov, D., Beschkov, V. & Mitov, S. 1989 Influence of product addition on the oxidation of D-sorbitol to L-sorbose by the strain Acetobacter suboxydans. Biocatalysis 2, 283–292.

    Google Scholar 

  • Kim, W.K., Chun, V.H., Park, Y.M., Kim, C.H., Choi, E.S. & Rha, S.K. 1994 L-sorbose production from glucose and fructose using Zymomonas mobilis and Guconobacter suboxydans in a two-stage fed-batch reactor. Process Biochemistry 29, 277–283.

    Google Scholar 

  • Kulhanek, M. 1970 Fermentation processes employed in vitamin-C synthesis. Advances in Applied Microbiology 12, 11–30.

    Google Scholar 

  • Melzoch, K., Rychtera, M., Markcichov, N.S., Pospichaova, V., Basarova, G. & Mankov, M.N. 1991 Application of membrane recycle bioreactor for continuous ethanol production. Applied Microbiology and Biotechnology 34, 469–472.

    Google Scholar 

  • Miller, G.L. 1959 Use of Dinitrosalicylic reagent for determination of reducing sugar. Analytical Chemistry 31, 426–428.

    Google Scholar 

  • Mori, H., Kobayashi, T. & Shimizu, S. 1981 High density production of sorbose from sorbitol by fed-batch culture with DO-stat. Journal of Chemical Engineering Japan 14, 65–70.

    Google Scholar 

  • Srivastava, A.K. & Lasrado, P.R. 1998 Fed batch sorbitol to sorbose fermentation by Acetobacter suboxydans. Bioprocess Engineering 18, 457–461.

    Google Scholar 

  • Shinagawa, E., Matsushita, K., Adachi, O. & Ameyama, M. 1982 Purification and characterisation of D-sorbitol dehydrogenase from membrane of Gluconobacter suboxydans var. α. Agricultural and Biological Chemistry 46, 135–141.

    Google Scholar 

  • Yamada, S., Wada, M. & Chibata, I. 1978 Effect of high oxygen partial pressure on the conversion of sorbitol to sorbose by Acetobacter suboxydans. Journal of Fermentation Technology 56, 29–34.

    Google Scholar 

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Giridhar, R., Srivastava, A. L-Sorbose production in a continuous fermenter with and without cell recycle. World Journal of Microbiology and Biotechnology 17, 185–189 (2001). https://doi.org/10.1023/A:1016677211656

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  • DOI: https://doi.org/10.1023/A:1016677211656

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