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Electrochemical advanced oxidation processes for sanitary landfill leachate remediation: Evaluation of operational variables

机译:用于卫生垃圾渗滤液修复的电化学高级氧化工艺:操作变量评估

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The effect of various parameters on the performance of electrochemical advanced oxidation processes (EAOPs) like electro-Fenton (EF), photoelectro-Fenton (PEF) and solar PEF (SPEF) was assessed for the treatment of a sanitary landfill leachate previously subjected to biological and coagulation processes. The tested operational variables included: (i) anode material (boron-doped diamond (BDD) and Pt), (ii) initial total dissolved iron concentration (20-80 mg L-1), (iii) pH (2.8-4.0), (iv) initial addition of 1:3 Fe(III)-to-oxalate molar ratio at various pH values (2.8-5.0), (v) temperature (15-40 degrees C) and (vi) radiation source (UVA, UVA-Vis and UVC lamps and natural sunlight). The BDD anode showed high superiority over the Pt one for EF, PEF with UVA light (PEF-UVA) and SPEF processes, thereby advising an important role of the physisorbed hydroxyl radicals ((OH)-O-center dot) at the anode surface on landfill leachate oxidation even under the potent solar radiation. An initial total dissolved iron content of 60 mg L-1 was chosen as the best dose for the PEF-UVA process with the BDD anode (PEF-BDD-UVA). While PEF-BDD-UVA without external addition of oxalic acid yielded the best results at pH 2.8, the initial addition of 1:3 Fe(III)-to-oxalate molar ratio allowed operating at pH 3.5 with even higher efficiency and at pH 4.0 with only slightly lower efficiency. Effluent temperatures from 20 to 40 degrees C led to similar mineralization rates for the PEF-BDD-UVA technique. The use of UVA and UVC lamps and natural sunlight as radiation sources in PEF-BDD and SPEF-BDD systems led to similar mineralization profiles as a function of time. The UVA-Vis lamp induced lower effluent mineralization mainly for longer reaction times. (C) 2015 Elsevier B.V. All rights reserved.
机译:评估了各种参数对电化学高级氧化工艺(EAOP)的性能的影响,如电Fenton(EF),光电Fenton(PEF)和太阳能PEF(SPEF),用于处理以前经过生物垃圾处理的卫生垃圾渗滤液和凝血过程。测试的操作变量包括:(i)阳极材料(掺硼金刚石(BDD)和铂),(ii)初始总溶解铁浓度(20-80 mg L-1),(iii)pH(2.8-4.0) (iv)在各种pH值(2.8-5.0),(v)温度(15-40摄氏度)和(vi)辐射源(UVA, UVA-Vis和UVC灯以及自然阳光)。 BDD阳极在EF,使用UVA光的PEF(PEF-UVA)和SPEF工艺方面显示出比Pt阳极更高的优势,从而建议了阳极表面物理吸附的羟基自由基((OH)-O-中心点)的重要作用即使在强烈的太阳辐射下,也会对垃圾渗滤液产生氧化作用。选择最初的总溶解铁含量为60 mg L-1作为使用BDD阳极(PEF-BDD-UVA)进行PEF-UVA工艺的最佳剂量。尽管没有外部添加草酸的PEF-BDD-UVA在pH 2.8时效果最佳,但最初添加1:3的Fe(III)/草酸酯摩尔比使pH 3.5时的操作效率更高,pH值为4.0效率略低。 20至40摄氏度的出水温度导致PEF-BDD-UVA技术的相似矿化速率。在PEF-BDD和SPEF-BDD系统中使用UVA和UVC灯以及自然阳光作为辐射源会导致相似的矿化剖面随时间变化。 UVA-Vis灯诱导的废水矿化程度较低,主要是为了延长反应时间。 (C)2015 Elsevier B.V.保留所有权利。

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