Continous production of free gluconic acid by Gluconobacter suboxydans IFO 3290 immobilized by adsorption on ceramic honeycomb monolith: effect of reactor configuration on further oxidation of gluconic acid to keto-gluconic acid

Fumihide Shiraishi; Koei Kawakami; Akihiko Tamura; Satoshi Tsuruda; Koichiro Kusunoki

doi:10.1007/BF00270773

Continous production of free gluconic acid by Gluconobacter suboxydans IFO 3290 immobilized by adsorption on ceramic honeycomb monolith: effect of reactor configuration on further oxidation of gluconic acid to keto-gluconic acid

Fumihide Shiraishi, Koei Kawakami, Akihiko Tamura, Satoshi Tsuruda, Koichiro Kusunoki

Systems Biology

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Abstract

Gluconobacter suboxydans IFO 3290 was immobilized by adsorption on ceramic honeycomb monolith, and continuous production of free gluconic acid from 100 g/l glucose was carried out in one- and three-stage monolith reactors. Further oxidation of gluconic acid to keto-gluconic acid by the immobilized cells has been found to be more suppressed in the three-stage monolith reactor. This finding can be explained by the fact that, with the three-stage reactor, the opportunity to oxidize gluconic acid further was decreased because the residence time of the reaction mixture at glucose conversion above the threshold value was shorter.

Original language	English
Pages (from-to)	445-447
Number of pages	3
Journal	Applied Microbiology and Biotechnology
Volume	31
Issue number	5-6
DOIs	https://doi.org/10.1007/BF00270773
Publication status	Published - Oct 1 1989

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Biotechnology
Applied Microbiology and Biotechnology

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Shiraishi, F., Kawakami, K., Tamura, A., Tsuruda, S., & Kusunoki, K. (1989). Continous production of free gluconic acid by Gluconobacter suboxydans IFO 3290 immobilized by adsorption on ceramic honeycomb monolith: effect of reactor configuration on further oxidation of gluconic acid to keto-gluconic acid. Applied Microbiology and Biotechnology, 31(5-6), 445-447. https://doi.org/10.1007/BF00270773

Continous production of free gluconic acid by Gluconobacter suboxydans IFO 3290 immobilized by adsorption on ceramic honeycomb monolith: effect of reactor configuration on further oxidation of gluconic acid to keto-gluconic acid. / Shiraishi, Fumihide; Kawakami, Koei; Tamura, Akihiko et al.
In: Applied Microbiology and Biotechnology, Vol. 31, No. 5-6, 01.10.1989, p. 445-447.

Research output: Contribution to journal › Article › peer-review

Shiraishi, F, Kawakami, K, Tamura, A, Tsuruda, S & Kusunoki, K 1989, 'Continous production of free gluconic acid by Gluconobacter suboxydans IFO 3290 immobilized by adsorption on ceramic honeycomb monolith: effect of reactor configuration on further oxidation of gluconic acid to keto-gluconic acid', Applied Microbiology and Biotechnology, vol. 31, no. 5-6, pp. 445-447. https://doi.org/10.1007/BF00270773

Shiraishi F, Kawakami K, Tamura A, Tsuruda S, Kusunoki K. Continous production of free gluconic acid by Gluconobacter suboxydans IFO 3290 immobilized by adsorption on ceramic honeycomb monolith: effect of reactor configuration on further oxidation of gluconic acid to keto-gluconic acid. Applied Microbiology and Biotechnology. 1989 Oct 1;31(5-6):445-447. doi: 10.1007/BF00270773

Shiraishi, Fumihide ; Kawakami, Koei ; Tamura, Akihiko et al. / Continous production of free gluconic acid by Gluconobacter suboxydans IFO 3290 immobilized by adsorption on ceramic honeycomb monolith : effect of reactor configuration on further oxidation of gluconic acid to keto-gluconic acid. In: Applied Microbiology and Biotechnology. 1989 ; Vol. 31, No. 5-6. pp. 445-447.

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abstract = "Gluconobacter suboxydans IFO 3290 was immobilized by adsorption on ceramic honeycomb monolith, and continuous production of free gluconic acid from 100 g/l glucose was carried out in one- and three-stage monolith reactors. Further oxidation of gluconic acid to keto-gluconic acid by the immobilized cells has been found to be more suppressed in the three-stage monolith reactor. This finding can be explained by the fact that, with the three-stage reactor, the opportunity to oxidize gluconic acid further was decreased because the residence time of the reaction mixture at glucose conversion above the threshold value was shorter.",

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AB - Gluconobacter suboxydans IFO 3290 was immobilized by adsorption on ceramic honeycomb monolith, and continuous production of free gluconic acid from 100 g/l glucose was carried out in one- and three-stage monolith reactors. Further oxidation of gluconic acid to keto-gluconic acid by the immobilized cells has been found to be more suppressed in the three-stage monolith reactor. This finding can be explained by the fact that, with the three-stage reactor, the opportunity to oxidize gluconic acid further was decreased because the residence time of the reaction mixture at glucose conversion above the threshold value was shorter.

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Continous production of free gluconic acid by Gluconobacter suboxydans IFO 3290 immobilized by adsorption on ceramic honeycomb monolith: effect of reactor configuration on further oxidation of gluconic acid to keto-gluconic acid

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