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 in | Bioresource technology Vol. 233; pp. 144 - 149 |
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Main Authors | , , , |
Format | Journal Article |
Language | English |
Published |
England
Elsevier Ltd
01.06.2017
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Subjects | |
Online Access | Get full text |
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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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Bibliography: | ObjectType-Article-1 SourceType-Scholarly Journals-1 ObjectType-Feature-2 content type line 23 |
ISSN: | 0960-8524 1873-2976 |
DOI: | 10.1016/j.biortech.2017.02.096 |