Film formation and hydrogen production performance of photosynthetic bacteria in simulating microchannels photo-bioreactor
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Film formation and hydrogen production performance of photosynthetic bacteria in simulating microchannels photo-bioreactor
CIESC JournalIssue 11, (2010)
作者机构:
重庆大学工程热物理研究所
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基金信息:
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Online First:05 November 2010,
Published:05 November 2010
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朱恂. Film formation and hydrogen production performance of photosynthetic bacteria in simulating microchannels photo-bioreactor[J]. CIESC Journal, 2010, (11).
DOI:
朱恂. Film formation and hydrogen production performance of photosynthetic bacteria in simulating microchannels photo-bioreactor[J]. CIESC Journal, 2010, (11).DOI:
Film formation and hydrogen production performance of photosynthetic bacteria in simulating microchannels photo-bioreactor
摘要
Abstract
In order to understand the micro-behavior and mass transfer of photosynthetic bacteria (PSB)in an immobilized granule
a visualized microchannels photo-bioreactor was designed to observe the adsorption and film forming of PSB named as Rhodopseudomonas palustris CQK 01. And the effects of substrate concentration and flow rate on hydrogen production and substrate degradation of microchannels photo-bioreactor were investigated. The results showed that the PSB behavior in the microchannels can be divided into four stages: initial diffusion and adsorption
diffusion-adsorption and initial splitting and reproducing of bacteria
dividing-increasing and morphological transformation
and gathering and biofilm forming. With the increase of substrate concentration and flow rate
the rate and yield of hydrogen producing rised first and then fell down
but the substrate conversion monotonically went up with its rate slowed down. The substrate degradation efficiency increased first and then decreased with increase of substrate concentration
and reduced with increase of solution flow rate. At higher substrate concentration and flow rate
substrate inhibition and the loss of biofilm were the main reasons for lower rate and yield of hydrogen production. In the range of present experiments
the optimum substrate concentration and flow rate were 50mmol·L-1 and 2.1ml·h -1 respectively
the maximum rate and yield of hydrogen production were 2.4mmol·(g cell dry mass)-1 ·h -1 and 0.78 mol H2·(mol sub)-1 respectively.