title: Continuous hydrogen production during fermentation of alpha-cellulose by the thermophillic bacterium Clostridium thermocellum.
abstract: Continuous hydrogen (H2) production during fermentation of alpha-cellulose was established using the thermophillic, anaerobic bacterium Clostridium thermocellum ATCC 27405. The objectives of this work were to characterize growth of C. thermocellum, quantify H2 production and determine soluble end-product synthesis patterns during fermentation of a cellulosic substrate under continuous culture conditions. A 5 L working volume fermentor was established and growth experiments were maintained for over 3,000 h. Substrate concentrations were varied from 1 to 4 g/L and the feed was introduced with continuous nitrogen gas sparging to prevent clogging of the feed-line. The pH and temperature of the reactor were maintained at 7.0 and 600 degrees C, respectively, throughout the study. At concentrations above 4 g/L, the delivery of alpha-cellulose was impaired due to feed-line clogging and it became difficult to maintain a homogenous suspension. The highest total gas (H2 plus CO2) production rate, 56.6 mL L(-1) h(-1), was observed at a dilution rate of 0.042 h(-1) and substrate concentration of 4 g/L. Under these conditions, the H2 production rate was 5.06 mmol h(-1). Acetate and ethanol were the major soluble end-products, while lactate and formate were greatly reduced compared to production in batch cultures. Concentrations of all metabolites increased with increasing substrate concentration, with the exception of lactate. Despite a number of short-term electrical and mechanical failures during the testing period, the system recovered quickly, exhibiting substantial robustness. A carbon balance was completed to ensure that all end-products were accounted for, with final results indicating near 100% carbon recovery. This study shows that long-term, stable H2 production can be achieved during direct fermentation of an insoluble cellulosic substrate under continuous culture conditions.
authors.affiliation: Department of Biosystems Engineering, University of Manitoba, Winnipeg, MB, Canada R3T5V6.
authors.forename: Lauren
authors.initials: L
authors.lastname: Magnusson
authors.forename: Nazim
authors.initials: N
authors.lastname: Cicek
authors.forename: Richard
authors.initials: R
authors.lastname: Sparling
authors.forename: David
authors.initials: D
authors.lastname: Levin
mesh_terms: D000085:Acetates / Q000378:metabolism; D001674:Bioelectric Energy Sources; D019149:Bioreactors; D002245:Carbon Dioxide / Q000378:metabolism; D002482:Cellulose / Q000378:metabolism*; D048013:Acetivibrio thermocellus / Q000378:metabolism*; D004867:Equipment Design; D019544:Equipment Failure Analysis; D000431:Ethanol / Q000378:metabolism; D005285:Fermentation; D005561:Formates / Q000378:metabolism; D006859:Hydrogen / Q000378:metabolism*; D006863:Hydrogen-Ion Concentration; D019344:Lactic Acid / Q000378:metabolism; D012037:Refuse Disposal / Q000379:methods; D013696:Temperature
chemical_list: D000085:Acetates; D005561:Formates; C030544:formic acid; D002245:Carbon Dioxide; D019344:Lactic Acid; D000431:Ethanol; D006859:Hydrogen; D002482:Cellulose