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. Author manuscript; available in PMC: 2011 Oct 15.
Published in final edited form as: J Biotechnol. 2010 Aug 10;150(2):215–223. doi: 10.1016/j.jbiotec.2010.08.002

Fig. 4.

Fig. 4

Fermentation kinetics by immobilized mixed culture of AFF01/pLOI297 and CT1101/pLOI297. The experiments were performed in capped shake flasks containing 100 ml of semi-defined medium supplied with sugar mixtures and with 35 ml beads containing cell concentration of 10.2 g-CDW/l-gel. Optimal cell fraction fopt was determined from the kinetic model (see Equ. (14)). (A) Relation of consumed xylose with an initial concentration of 60 g/l and consumed glucose with an initial concentration of 20 g/l at the fraction of CT1101/pLOI297 cells used in the immobilization: f = 0.27 (graphic file with name nihms239285ig1.jpg), f = 0.34 (graphic file with name nihms239285ig8.jpg), f = 0 (graphic file with name nihms239285ig9.jpg). (B) Relation of consumed sugars in the mixture: glucose-xylose at cell fraction fopt = 0.41 (graphic file with name nihms239285ig10.jpg), glucose-arabinose at cell fraction fopt = 0.47 (graphic file with name nihms239285ig11.jpg), and arabinose-xylose at cell fraction fopt = 0.58 (graphic file with name nihms239285ig12.jpg). (C) Immobilized mixed culture at the optimal cell fraction in a sugar mixture of glucose (graphic file with name nihms239285ig1.jpg) and xylose (graphic file with name nihms239285ig2.jpg) converted into ethanol (graphic file with name nihms239285ig4.jpg). (D) Immobilized mixed cultures at the optimal cell fraction in a sugar mixture of glucose and arabinose (graphic file with name nihms239285ig3.jpg). (E) Immobilized mixed cultures at the optimal cell fraction in a sugar mixture of xylose and arabinose.