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Fig. 7 | Biotechnology for Biofuels and Bioproducts

Fig. 7

From: Immobilization techniques improve volumetric hydrogen productivity of Caldicellulosiruptor species in a modified continuous stirred tank reactor

Fig. 7

Yield coefficients, carbon balance (C.b.) and redox balance (R.b.) of all continuous cultures performed at a D of 0.3 h−1. A Case A (C. kronotskyensis without carriers, dotted bar, black); Case B (C. kronotskyensis with acrylic fibres, brick bar, black); Case C (C. kronotskyensis with acrylic fibres and chitosan, bar with vertical line, black); and Case D (C. kronotskyensis with chitosan, bar with diagonal line, black). B Case F (C. owensensis with acrylic fibres, brick bar, blue); Case G (C. owensensis with acrylic fibres and chitosan, bar with vertical line, blue); and Case H (C. owensensis with chitosan, bar with diagonal line, blue). C Case I (co-culture without carriers, dotted bar, green); Case J (co-culture with acrylic fibres, brick bar, green); Case K (co-culture with acrylic fibres and chitosan bar with vertical line, green); and Case L (co-culture with chitosan bar with diagonal line, green). YH2, YAc, YLac, and YSX represent molar yields of H2, acetate, lactate, and biomass per mole of substrate consumed, respectively. C.b. and R.b. represent carbon balance and redox balance, respectively

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