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首页> 外文期刊>Electrochimica Acta >Electrooxidation as post treatment of ultrafiltration effluent in a landfill leachate MBR treatment plant: Effects of BDD, Pt and DSA anode types
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Electrooxidation as post treatment of ultrafiltration effluent in a landfill leachate MBR treatment plant: Effects of BDD, Pt and DSA anode types

机译:电氧化作为垃圾渗滤液中超滤流出物的后处理MBR处理厂:BDD,PT和DSA阳极类型的影响

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In this study, ultrafiltration (UF) effluent from a landfill leachate treatment plant (equipped with anoxicaerobic oxidation and UF) was treated by Electrooxidation (EO) process in a batch reactor using different dimensionally stable electrodes (DSA anodes: Ti/PtO2-IrO2, Ti/RuO2-TiO2, Ti/RuO2-IrO2, and Ti/IrO2-Ta2O5), boron doped diamond (BDD) and Pt as anode and stainless-steel electrode as cathode. The untreated UF effluent had COD and TOC concentrations of 888 mg/L and 398.6 mg/L, respectively. Overall, BDD anode performed better than the other DSA anodes under the tested conditions with removal efficiencies of 64.9-86.8% and 68.2-92.0% for TOC and COD, respectively. The calculated energy consumptions at maximum removal efficiencies were 111.2 kWh per m(3) (136.01 kWh/kg COD and 321.27 kWh/kg TOC) at 360 A/m(2) and 4 h of treatment time for BDD anode. However, TOC and COD removal efficiencies of 31.3-86.8% and 36.5-92.0%, respectively, were obtained for the other DSA anodes at current densities between 60 and 360 A/m(2) and 4 h of treatment time. Energy consumptions and anode efficiency for DSA anodes ranged from 7.3-111.2 kWh/m(3) (15.67-194.87 kWh/kg COD) and 4.40-34.24 g COD/Ah m(2) (or 1.77-14.62 g TOC/Ah m(2)). The general COD and TOC removal mechanism well fitted the pseudo first-order kinetic model with R-2 of 0.94 particularly for BDD electrode under all applied current densities. The chloride content in the leachate promoted indirect oxidation leading to higher COD and TOC removal efficiencies. Moreover, high performance size exclusion chromatography (HPSEC) was used to evaluate the variation of fractions in wastewater during EO. (C) 2018 Published by Elsevier Ltd.
机译:在本研究中,通过使用不同尺寸稳定的电极(DSA阳极:Ti / PTO2-IRO2),通过电氧化(EO)工艺处理来自垃圾填埋场渗滤液处理厂(配备亚氧基杂虫氧化和UF)的垃圾渗滤液处理厂的流出物(DSA阳极:Ti / PTO2-IRO2, Ti / Ruo2-TiO2,Ti / Ruo2-IRO2和TI / IRO2-TA2O5),硼掺杂金刚石(BDD)和PT作为阴极作为阳极和不锈钢电极。未处理的UF流出物分别具有888mg / L和398.6 mg / L的COD和TOC浓度。总体而言,BDD阳极比测试条件下的其他DSA阳极更好,分别除去效率为64.9-86.8%和68.2-92.0%,分别为TOC和COD。在最高去除效率下计算出的能量消耗为每M(3)(136.01千瓦时/千克COD和321.27千瓦时/ kg TOC),在360A / m(2)和4小时的BDD阳极的4小时。然而,对于在60至360A / m(2)和4小时的电流密度的其他DSA阳极,分别为31.3-86.8%和36.5-92.0%的TOC和COD去除效率。 DSA阳极的能量消耗和阳极效率范围为7.3-111.2千瓦时/ m(3)(15.67-194.87 kWh / kg COD)和4.40-34.24g COD / AH M(2)(或1.77-14.62 G TOC / AH M) (2))。一般COD和TOC去除机构井拟合伪第一阶动力学模型,其R-2> 0.94,特别是在所有施加电流密度下的BDD电极。渗滤液中的氯化物含量促进了间接氧化,导致较高的COD和TOC去除效率。此外,高性能尺寸排阻色谱(HPSEC)用于评价EO期间废水中级分的变化。 (c)2018年由elestvier有限公司发布

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