Repeated biotransformation of glycerol to 1,3-dihydroxyacetone by immobilized cells of Gluconobacter oxydans with glycerol- and urea-feeding strategy in a bubble column bioreactor

•Achievement of near colorless DHA solution with few impurities.•Repeated production by continuous-feeding of glycerol and urea.•High DHA productivity and conversion rate of glycerol to DHA.•Immobilized cells on porous ceramics in a home-made bubble column bioreactor. Some inorganic nitrogen sources...

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Published inBioresource technology Vol. 233; pp. 144 - 149
Main Authors Hu, Zhong-Ce, Tian, Sheng-Ying, Ruan, Li-Juan, Zheng, Yu-Guo
Format Journal Article
LanguageEnglish
Published England Elsevier Ltd 01.06.2017
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Summary:•Achievement of near colorless DHA solution with few impurities.•Repeated production by continuous-feeding of glycerol and urea.•High DHA productivity and conversion rate of glycerol to DHA.•Immobilized cells on porous ceramics in a home-made bubble column bioreactor. Some inorganic nitrogen sources and amino acids instead of yeast extract, which resulted in trouble of product purification, were introduced for 1,3-dihydroxyacetone (DHA) production by biotransformation with Gluconobacter oxydans. The results showed that urea is an optimal nitrogen source. Furthermore, the effects of glycerol- and urea-feeding strategies for DHA production by immobilized cells in a home-made bubble column bioreactor were optimized. Cells immobilization was prepared by cultivation in the bioreactor packed with porous ceramics, and then the broth was removed. Then, repeated biotransformation by continuous-feeding of glycerol and urea was developed. Up to 96.4±4.1g/L of average DHA concentration with 94.8±2.2% of average conversion rate of glycerol to DHA was achieved after 12 cycles of run. Near colorless DHA solution with few impurities was obtained and the production cost could be decreased.
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content type line 23
ISSN:0960-8524
1873-2976
DOI:10.1016/j.biortech.2017.02.096