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Fig. 4 | Microbial Cell Factories

Fig. 4

From: Highly efficient fermentation of 5-keto-d-fructose with Gluconobacter oxydans at different scales

Fig. 4

Extended-batch-cultivation of G. oxydans 621H ΔhsdR pBBR1p264-fdhSCL-ST in a 2 L fermenter (Sartorius) with constant feeding of fructose (1180 g/L) between 18 and 44 h. Depicted is A the oxygen transfer rate (OTR, light blue), carbon dioxide transfer rate (CTR, orange) and respiratory quotient (RQ, dark red), B pH (pink), aeration rate (green) and filling volume (grey), C the dissolved oxygen tension (DOT, dark blue) and agitation rate (light green), D the optical density OD600 (purple) and osmolality (black), E fructose (light blue) and 5-ketofructose concentration (red). A. Cultivation was performed in complex medium (concentrated 1.6×) with 150 g/L initial fructose at 30 °C, initial pH value 6, pH control at 5 from 18 h with 3 M KOH, VL,start = 1 L in a 2 L fermenter. DOT was kept ≥ 30% by variation of agitation speed (500–1500 rpm), absolute aeration rate Qg = 1—2.5 SL/min. Feeding solution: 1180 \(\pm\) 2 gfructose/L, heat pretreatment: 100 °C, 10 min. Feed rate: 27.3 gfructose/h. Fructose feeding solution and peripheral feeding system were heated to ~ 55 °C. RQ-values are only shown, when OTR-values are above 5 mmol/L/h. Sampling for further experiments Fig. 5) are indicated by time stamps t1–t4 in A. A drift in the oxygen sensor was corrected by linear regression. For original data please refer to Additional file 1: Fig. S3

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