Pilot-scale hydrogen fermentation system start-up performance

Chiu Yue Lin, Shu Yii Wu, Ping Jei Lin, Jo Shu Chang, Chun Hsiung Hung, Kuo Shing Lee, Feng Yuan Chang, Chen Yeon Chu, Chin Hung Cheng, Chyi How Lay, Alex C. Chang

研究成果: Article同行評審

49 引文 斯高帕斯(Scopus)

摘要

A high-rate hydrogen production process able to produce H2 at a maximum rate of 15 L/L/h was successfully developed by the Feng Chia University (FCU) biohydrogen research team. This highly efficient hydrogen fermentation system includes a 400 L pilot-scale system constructed for determining scale-up operation parameters for commercializing the bioH2 production technology. The pilot-scale system is composed of a feedstock tank, mixing system, fermentor, gas/liquid separator and automatic control system. The fermentor is fed with sucrose (20 g COD/L) and operated at 35 °C. A batch strategy is used for system start-up. The fermentor was first operated in a batch mode for two days and then switched to a continuous-feeding mode (HRT 12 h) for one month. During the continuous operation, pH notably affected H 2 production efficiency and bacterial community. For the first 14-day operation, the H2 production rate increased from 0.017 to 0.256 L/L/h with a pH variation from 5.0 to 7.0. The DGGE results indicate the presence of two Clostridium species (namely, Clostridium butyricum and Clostridium pasteurianum) in the fermenter. Stable hydrogen production rate was obtained at pH 5.5-6.0 when C. pasteurianum became dominant in the mixed culture.

原文English
頁(從 - 到)13452-13457
頁數6
期刊International Journal of Hydrogen Energy
35
發行號24
DOIs
出版狀態Published - 2010 12月

All Science Journal Classification (ASJC) codes

  • 可再生能源、永續發展與環境
  • 燃料技術
  • 凝聚態物理學
  • 能源工程與電力技術

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