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Title: Scale-up and performance of an immobilized cell reactor separator for the production of ethanol from whey lactose

Conference ·
OSTI ID:6819948

An adsorbed microbial cell, trickle flow, reactor incorporating a circulating gas phase to simultaneously separate a volatile inhibitory product has shown high fermentation rates and effective product separation on a 1 in. diameter lab bench scale. Carbon dioxide generated by the fermentation is recirculated to strip the volatile fermentation product from the fermentation broth. Random and structured packings were evaluated and a parallel type structured packing was developed consisting of a plates of absorbant material to which cells are adsorbed and spaced to allow passage of the circulating gas stream. The substrate solution flows by gravity in a capillary flow fashion down through the plates in which the cells are immobilized. The theoretical reactor separation and fermentation performance as a function of plate thickness and gas channel spacing was evaluated. This reactor has been scaled up to a 6 in. ID reactor with a total reactor volume of about 50 liters using a spiral wound version of the parallel plates, and then to a 24 in. ID reactor with a reactor volume of about 1300 liters. 16 refs., 12 figs., 1 tab.

Research Organization:
Purdue Univ., Lafayette, IN (USA). Dept. of Agricultural Engineering
Sponsoring Organization:
DOE/CE
DOE Contract Number:
FG02-85CE40772
OSTI ID:
6819948
Report Number(s):
CONF-8808305-1; ON: DE90012543
Resource Relation:
Conference: Society of Industrial Engineers Meeting (SIM), Chicago, IL (USA), 8 Aug 1988
Country of Publication:
United States
Language:
English