Abstract
This work demonstrates a continuous-flow biohydrogen producing system able to produce H 2 from starch at a high volumetric rate of over 4 L h -1 L -1 . Using phosphate-buffered medium containing cassava starch (15 g/L) as the feed, sludge granulation occurred within 15 days after start-up while operating at a hydraulic retention time (HRT) of 2.2 h, enabling efficient biomass retention in the bioreactor. Operation at a progressively decreasing HRT of 5.3-0.5 h gave rise to a H 2 content of nearly 50% (i.e., a CO 2 /H 2 ratio of 1.0) and a H 2 yield of 0.97-1.43 mol of H 2 /mol of hexose, which is 26-37% from the theoretical value. Operation at 0.5 h of HRT gave the highest H 2 production rate of 4.12 L h -1 L -1 , respectively, while further shortening of the HRT resulted in a washout of cells. The H 2 production rate obtained from this work appears to be much higher than those indicated in comparable studies using starch to produce H 2 via dark fermentation. The soluble metabolites were dominated by butyric acid (54-72% of total soluble products), followed by ethanol and acetic acid. The results indicate the feasibility of using starch as an inexpensive carbon substrate for high-rate and low-cost production of bio-H 2 via a granular-sludge-based continuous-flow bioreactor.
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