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Fig. 4 | Biotechnology for Biofuels and Bioproducts

Fig. 4

From: An engineered non-oxidative glycolytic bypass based on Calvin-cycle enzymes enables anaerobic co-fermentation of glucose and sorbitol by Saccharomyces cerevisiae

Fig. 4

Sorbitol consumption by anaerobic chemostat cultures of S. cerevisiae strains IMX2506 (optimized PRK-RuBisCO bypass and gpd2∆ mutation, overexpression cassettes for HXT15 and SOR2) (A) and IMX1489 (optimized PRK-RuBisCO bypass and gpd2∆ mutation [26]) (B). Chemostat cultures were grown at a dilution rate of 0.025 h−1 on 10 g L−1 of glucose and 10 g L−1 of sorbitol. A Average residual sorbitol concentration ± standard deviation in four chemostat cultures of strain IMX2506. After 400 h, the CO2 content of the inlet gas was reduced to zero in two of the four cultures. The dotted line represents expected wash-in kinetics of sorbitol in the absence of sorbitol consumption: c(t) = cin-((cin-c400)*e(−D*t)) with c = residual sorbitol concentration, c400 = sorbitol concentration at 400 h, \( \hbox{c}_{{\rm in}}\) = sorbitol concentration in medium feed and D = dilution rate. B: Average sorbitol concentration ± standard deviation in two chemostats of strain IMX1489. CO2 supplementation was stopped at 700 h

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