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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. 2.

Fig. 2

Fermentation kinetics of immobilized cultures. The experiments were conducted in anaerobic batch bioreactors containing 0.7 l semi-defined medium supplemented with sugars and with 0.35 l of beads. pH was controlled at 7. The immobilized cell concentration was 11.4 g-CDW/l-gel (see Materials and Methods). (A) Immobilized AFF01/pLOI297 with an initial concentration of 30 g/l glucose (graphic file with name nihms239285ig1.jpg), 30 g/l xylose (graphic file with name nihms239285ig2.jpg), and 20 g/l arabinose (graphic file with name nihms239285ig3.jpg) converted into ethanol (graphic file with name nihms239285ig4.jpg). (B) Immobilized CT1101/pLOI297 with an initial concentration of 30 g/l glucose, 20 g/l xylose and 20 g/l arabinose. (C) Relation of consumed sugars from a sugar mixture of glucose, xylose, and arabinose for immobilized cells of AFF01/pLOI297 (graphic file with name nihms239285ig5.jpg), CT1101/pLOI297 (graphic file with name nihms239285ig6.jpg) and wild-type MG1655/pLOI297 (graphic file with name nihms239285ig7.jpg).