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Bioresources and Bioprocessing
Fig. 4 | Bioresources and Bioprocessing

Fig. 4

From: Efficient 1,3-dihydroxyacetone biosynthesis in Gluconobacter oxydans using metabolic engineering and a fed-batch strategy

Fig. 4

Time courses showing DHA accumulation using different initial glycerol concentrations. Fermentation of engineered strain G. oxydans WSH-003–4 was conducted in 5 L bioreactor. A Initial glycerol concentration = 100 g L−1. B Initial glycerol concentration = 120 g L−1. C Initial glycerol concentration = 140 g L−1. Black triangles; glycerol, blue squares; DHA, red circles; OD600

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