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Sanitary landfill leachate treatment using combined solar photo-Fenton and biological oxidation processes at pre-industrial scale

机译:工业前规模的太阳能光芬顿法和生物氧化法相结合的卫生垃圾渗滤液处理

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This work proposes a new strategy for the treatment of leachates from sanitary landfills after lagooning pretreatment, using a solar photo-Fenton oxidation process to eliminate the most recalcitrant organic compounds, leading to a biodegradability enhancement of the leachate and promoting its subsequent oxidation in an activated sludge biological reactor. The integrated leachate treatment process was conducted in a pre-industrial plant, incorporating a photocatalytic system with 39.52 m~2 of compound parabolic collectors (CPCs) and an activated sludge biological reactor, with 3.5 m~3 capacity, operated under aerated and anoxic conditions. An extensive physico-chemical characterization of the leachate after lagooning was performed during one year, from June 2010 to May 2011, showing its high recalcitrant character mainly associated with the presence of humic substances. The efficiency of the combined treatment was evaluated concerning the leachate characteristics' variability after lagooning, availability of solar radiation during the year, and different operational process variables, such as the amount of hydrogen peroxide necessary to reach the required COD target value, biodegradability enhancement during the photo-oxidation process/iron reutilization in consecutive oxidation processes, removal of acidic sludge resulting from the acidification process and leachate temperature/average solar power. The elimination of the remaining organic carbon fraction and nitrogen compounds after the pre-oxidation step was also assessed in an activated sludge biological reactor, under aerobic and anoxic conditions, considering the composition variability of photo-treated leachate. Nitrification and denitrification rates were also evaluated.
机译:这项工作提出了一种新的策略,用于处理泻湖预处理后的卫生垃圾填埋场中的渗滤液,采用太阳能光芬顿氧化工艺消除了难降解的有机化合物,从而提高了渗滤液的生物降解能力,并促进了其在活性炭中的后续氧化作用。污泥生物反应器。渗滤液的综合处理过程是在工业前工厂中进行的,该过程包括具有39.52 m〜2的复合抛物线捕集器(CPC)的光催化系统和容量为3.5 m〜3的活性污泥生物反应器,可在充气和缺氧条件下运行。从2010年6月至2011年5月的一年内,对泻湖中的渗滤液进行了广泛的理化表征,显示其高难降解性主要与腐殖质的存在有关。评估了联合处理的效率,涉及到泻湖之后渗滤液特征的变化,一年中太阳辐射的可获得性以及不同的操作过程变量,例如达到所需的COD目标值所需的过氧化氢的量,在处理过程中生物降解能力的提高在连续的氧化过程中进行光氧化过程/铁的再利用,去除酸化过程中产生的酸性污泥以及沥滤液的温度/平均太阳能。考虑到光处理渗滤液的组成变化性,在有氧和缺氧条件下,在活性污泥生物反应器中还评估了预氧化步骤后残留有机碳组分和氮化合物的消除。还评估了硝化和反硝化率。

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