Abstract
A potential industrial substrate (liquefied corn starch; LCS) has been employed for successful acetone butanol ethanol (ABE) production. Fermentation of LCS (60 g l(-1)) in a batch process resulted in the production of 18.4 g l(-1) ABE, comparable to glucose: yeast extract based medium (control experiment, 18.6 g l(-1) ABE). A batch fermentation of LCS integrated with product recovery resulted in 92% utilization of sugars present in the feed. When ABE was recovered by gas stripping (to relieve inhibition) from the fed-batch reactor fed with saccharified liquefied cornstarch (SLCS), 81.3 g l(-1) ABE was produced compared to 18.6 g l(-1) (control). In this integrated system, 225.8 g l(-1) SLCS sugar (487 % of control) was consumed. In the absence of product removal, it is not possible for C. beijerinckii BA101 to utilize more than 46 g l(-1) glucose. A combination of fermentation of this novel substrate (LCS) to butanol together with product recovery by gas stripping may economically benefit this fermentation.
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