Improving biohydrogen production in a carrier-induced granular sludge bed by altering physical configuration and agitation pattern of the bioreactor

International Journal of Hydrogen Energy

Volumn 31, Issue 12, 2006, Pages 1648-1657

  Lee, Kuo Shing ^a   Lo, Yung Chung ^b   Lin, Ping Jei ^c   Chang, Jo Shu ^b  

^a CENTRAL TAIWAN UNIVERSITY OF SCIENCE AND TECHNOLOGY   (Taiwan)

^b NATIONAL CHENG KUNG UNIVERSITY   (Taiwan)

^c FENG CHIA UNIVERSITY   (Taiwan)

Author keywords

Agitation pattern; Biohydrogen production; Carrier induced granular sludge bed (CIGSB); Height to diameter (H D) ratio; Liquid upflow velocity

Indexed keywords

BIOMASS; BIOREACTORS; MASS TRANSFER; METABOLISM; METABOLITES; ORGANIC ACIDS; SEWAGE SLUDGE; VELOCITY;

AGITATION PATTERN; BIOHYDROGEN PRODUCTION; CARRIER-INDUCED GRANULAR SLUDGE BED (CIGSB); HEIGHT TO DIAMETER (H/D) RATIO; LIQUID UPFLOW VELOCITY;

HYDROGEN FUELS;

EID: 33747165790     PISSN: 03603199     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.ijhydene.2005.12.020     Document Type: Article

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