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Enhancing simultaneous electricity production and reduction of sewage sludge in two-chamber MFC by aerobic sludge digestion and sludge pretreatments

机译:通过好氧污泥消化和污泥预处理提高两室MFC的同时发电量和减少污泥

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摘要

Batch tests were conducted to enhancing simultaneous electricity production and reduction of sewage sludge in two-chamber MFC by aerobic sludge digestion in cathode chamber and sludge pretreatments (sterilization and base pretreatment) prior to sludge addition to anode chamber, respectively. During the stable stage, The voltage outputs and power densities of MFC increased from 0.28-0.31 V to 17.3-21.2mW/m~2 to 0.41-0.43V and 36.8-40.1 mW/m~2, respectively, when aerobic sludge digestion occurred in the cathode chamber. When the sludge added to the anode chamber was sterilized or base pretreated, the voltage outputs and power densities of MFC increased from 0.30-0.32 V and 19.9-22.6 mW/m2 (raw sludge) to 0.34-0.36 V and 25.5-28.6 mW/m~2 (sterilized sludge), 0.41-0.43 V and 37.1 -40.8 mW/m~2 (base pretreated sludge), respectively. At the end of the test, the total suspended solids (TSS) and volatile suspended solids (VSS) reduction of sludge in the anode chambers increased from 33.9% and 36.8% to 34.5% and 38.7% with aerobic sludge digestion in the cathode chamber, respectively;while, those (TSS and VSS reduction) with sludge pretreatments prior to the sludge addition to the anode chambers increased from 25.1% and 22.8% (raw sludge) to 32.8% and 34.6% (sterilized sludge), and 25.5% and 26.7% (base pretreated sludge), respectively. The experimental results illuminated both aerobic sludge digestion in the cathode chamber and sludge pretreatments (sterilization and base pretreatment) prior to sludge addition to the anode chamber could enhance simultaneous electricity production from sludge and sludge reduction.
机译:通过在阴极腔室中进行好氧污泥消化和在将污泥添加到阳极室之前进行污泥预处理(灭菌和基础预处理),分别进行了分批测试以提高两室MFC的同时发电量和减少污泥。在稳定阶段,发生好氧污泥消化时,MFC的电压输出和功率密度分别从0.28-0.31 V增加到17.3-21.2mW / m〜2到0.41-0.43V和36.8-40.1 mW / m〜2在阴极室中。当对添加到阳极室的污泥进行灭菌或碱预处理时,MFC的电压输出和功率密度从0.30-0.32 V和19.9-22.6 mW / m2(原始污泥)增加到0.34-0.36 V和25.5-28.6 mW / m〜2(灭菌污泥),0.41-0.43 V和37.1 -40.8 mW / m〜2(基础预处理污泥)。在测试结束时,阳极室中的好氧污泥消化后,阳极室中的污泥的总悬浮固体(TSS)和挥发性悬浮固体(VSS)的减少从33.9%和36.8%分别增加到34.5%和38.7%,同时,在将污泥添加到阳极室之前进行污泥预处理的那些(TSS和VSS减少)分别从25.1%和22.8%(原始污泥)增加到32.8%和34.6%(灭菌污泥)以及25.5%和26.7 %(碱预处理污泥)分别。实验结果表明,在阴极室中进行好氧污泥消化和在将污泥添加到阳极室之前进行污泥预处理(灭菌和基础预处理)都可以提高污泥的同时发电量和减少污泥。

著录项

  • 来源
    《Journal of Hazardous Materials》 |2011年第2期|p.444-449|共6页
  • 作者单位

    Research Center for Eco-Environmental Sciences, Chinese Academy of Sciences, Beijing 100085, PR China;

    Research Center for Eco-Environmental Sciences, Chinese Academy of Sciences, Beijing 100085, PR China;

    Research Center for Eco-Environmental Sciences, Chinese Academy of Sciences, Beijing 100085, PR China;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);美国《化学文摘》(CA);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    aerobic sludge digestion; electricity production; microbial fuel cell; sludge pretreatment; sludge reduction;

    机译:好氧污泥消化;电力生产;微生物燃料电池污泥预处理;减少污泥;

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