Research Center for Eco-Environmental Sciences, Chinese Academy of Sciences, Beijing 100085, PR China.
J Hazard Mater. 2011 May 15;189(1-2):444-9. doi: 10.1016/j.jhazmat.2011.02.058. Epub 2011 Feb 24.
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 17.3-21.2 mW/m(2) to 0.41-0.43 V 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/m(2) (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.
进行了批量测试,通过在阴极室中进行好氧污泥消化以及在将污泥添加到阳极室之前进行污泥预处理(灭菌和碱预处理),来增强两室 MFC 中的同步发电和减少污水污泥。在稳定阶段,当阴极室中发生好氧污泥消化时,MFC 的电压输出和功率密度从 0.28-0.31 V 增加到 17.3-21.2 mW/m(2),到 0.41-0.43 V 和 36.8-40.1 mW/m(2)。当添加到阳极室的污泥被灭菌或碱预处理时,MFC 的电压输出和功率密度从 0.30-0.32 V 和 19.9-22.6 mW/m(2)(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)(碱预处理污泥)。测试结束时,阳极室中污泥的总悬浮固体(TSS)和挥发性悬浮固体(VSS)去除率从 33.9%和 36.8%分别增加到 34.5%和 38.7%,在阴极室中进行好氧污泥消化;而在将污泥添加到阳极室之前进行污泥预处理(灭菌和碱预处理)时,阳极室中污泥的 TSS 和 VSS 去除率从 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)。实验结果表明,阴极室中的好氧污泥消化以及在将污泥添加到阳极室之前进行污泥预处理(灭菌和碱预处理)均可以增强从污泥中同步发电和污泥减少。