H2 production with anaerobic sludge using activated-carbon supported packed-bed bioreactors.
Packed-bed bioreactors containing activated carbon as support carrier were used to produce H2 anaerobically from a sucrose-limiting medium while acclimated sewage sludge was used as the H2 producer. The effects of bed porosity (epsilon(b)) and substrate loading rate on H2 fermentation were examined using packed beds with epsilon(b) of 70-90% being operated at hydraulic retention times (HRT) of 0.5-4 h. Higher epsilon(b) and lower HRT favored H2 production. With 20 g COD l(-1) of sucrose in the feed, the optimal H2 production rate (7.4 l h(-1) l(-1)) was obtained when the bed with epsilon(b) = 90% was operated at HRT = 0.5 h. Flocculation of cells enhanced the retention of sludge for stable operations of the bioreactor at low HRTs. The gas products resulting from fermentative H2 production consisted of 30-40% H2 and 60-70% CO2. Butyric acid was the primary soluble product, followed by propionic acid and valeric acid.
Lee
Kuo-Shing
KS
Department of Chemical Engineering, Feng Chia University, Taichung, Taiwan.
Lo
Yung-Sheng
YS
Lo
Yung-Chung
YC
Lin
Ping-Jei
PJ
Chang
Jo-Shu
JS
D001421:Bacteria, Anaerobic / Q000378:metabolism*; D019149:Bioreactors / Q000382:microbiology*; D018914:Cells, Immobilized / Q000378:metabolism; D002606:Charcoal / Q000378:metabolism*; D006859:Hydrogen / Q000378:metabolism*; D008567:Membranes, Artificial; D016062:Porosity; D012722:Sewage / Q000382:microbiology*; D013395:Sucrose / Q000378:metabolism
D008567:Membranes, Artificial; D012722:Sewage; D002606:Charcoal; D013395:Sucrose; D006859:Hydrogen