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苏彩丽, 张楠, 朱灵峰, 李海华. EGSB反应器处理产氢发酵液[J]. 环境工程学报, 2014, 8(1): 126-130.
引用本文: 苏彩丽, 张楠, 朱灵峰, 李海华. EGSB反应器处理产氢发酵液[J]. 环境工程学报, 2014, 8(1): 126-130.
shu
Su Caili, Zhang Nan, Zhu Lingfeng, Li Haihua. Start-up of EGSB reactor for treatment of biohydrogen fermentative liquid[J]. Chinese Journal of Environmental Engineering, 2014, 8(1): 126-130.
Citation: Su Caili, Zhang Nan, Zhu Lingfeng, Li Haihua. Start-up of EGSB reactor for treatment of biohydrogen fermentative liquid[J]. Chinese Journal of Environmental Engineering, 2014, 8(1): 126-130.
shu

EGSB反应器处理产氢发酵液

  • 1.

    华北水利水电大学环境与市政工程学院, 郑州 450011

  • 基金项目:

    河南省教育厅资助项目（12A610008）

    河南省科技厅科技攻关项目（112102310440）

  • 中图分类号: X703

Start-up of EGSB reactor for treatment of biohydrogen fermentative liquid

  • 1.

    College of Environment and Municipal Engineering, North China University of Water Resources and Electric Power, Zhengzhou 450011, China

  • Fund Project:

  • 摘要: 以厌氧颗粒污泥为接种污泥，对厌氧颗粒污泥膨胀床（EGSB）反应器处理产氢发酵液的启动性能进行了研究。结果表明，在温度为（35±1）℃，水力停留时间（HRT）为6 h的条件下，逐渐提高进水COD，经过40 d连续运行，EGSB反应器启动成功。容积负荷达到14 kg COD/（m3·d）时，COD去除率约为80%，产气量为26.84 L/d，甲烷含量为57.9%。
    Abstract: The start-up of the expanded granular sludge blanket (EGSB) reactor inoculated with anaerobic granular sludge for the treatment of biohydrogen fermentative liquid was investigated. The EGSB reactor can be successfully started up with 6 h of hydraulic retention time (HRT) in 40 days at (35±1)℃ by gradually increasing the influent COD concentration. The COD removal efficiency reached about 80%, biogas production was 26.84 L/d, and CH4 content was 57.9% when the volume load reached 14 kg COD/(m3·d).
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出版历程
  • 收稿日期:  2012-12-24
  • 刊出日期:  2014-01-03
苏彩丽, 张楠, 朱灵峰, 李海华. EGSB反应器处理产氢发酵液[J]. 环境工程学报, 2014, 8(1): 126-130.
引用本文: 苏彩丽, 张楠, 朱灵峰, 李海华. EGSB反应器处理产氢发酵液[J]. 环境工程学报, 2014, 8(1): 126-130.
shu
Su Caili, Zhang Nan, Zhu Lingfeng, Li Haihua. Start-up of EGSB reactor for treatment of biohydrogen fermentative liquid[J]. Chinese Journal of Environmental Engineering, 2014, 8(1): 126-130.
Citation: Su Caili, Zhang Nan, Zhu Lingfeng, Li Haihua. Start-up of EGSB reactor for treatment of biohydrogen fermentative liquid[J]. Chinese Journal of Environmental Engineering, 2014, 8(1): 126-130.
shu

EGSB反应器处理产氢发酵液

  • 1. 华北水利水电大学环境与市政工程学院, 郑州 450011
  • 收稿日期:  2012-12-24
基金项目:

河南省教育厅资助项目（12A610008）

河南省科技厅科技攻关项目（112102310440）

摘要: 以厌氧颗粒污泥为接种污泥，对厌氧颗粒污泥膨胀床（EGSB）反应器处理产氢发酵液的启动性能进行了研究。结果表明，在温度为（35±1）℃，水力停留时间（HRT）为6 h的条件下，逐渐提高进水COD，经过40 d连续运行，EGSB反应器启动成功。容积负荷达到14 kg COD/（m3·d）时，COD去除率约为80%，产气量为26.84 L/d，甲烷含量为57.9%。

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