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Study on treatment of coking wastewater by three-dimensional fluid bed electrode reactor combined with Fenton process

机译:三维流化床电极反应器结合Fenton工艺处理焦化废水的研究

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Experiments were conducted to investigate the behavior of the integrated process with a three-dimensional electrode reactor combined with Fenton process for coking wastewater treatment.Effects of initial pH value,reaction time,H2O2 dosage,Fe2+ dosage on Total organic carbon (TOC) removal rate were investigated.The kinetics of degradation of TOC from coking wastewater by three-dimensional fluid bed electrode reactor combined with Fenton process was also studied.Experimental results shows that three-dimensional fluid bed electrode reactor combined with Fenton process had better synergic effect,average 17.4% TOC removal rate was improved within an hour.It was found that TOC degradation in coking wastewater followed a pseudo-first-order reaction kinetic model.The optimum degradation efficiencies of TOC were up to 60% as pH3.4,3.5 mM of Fe2+ and1.2~1.8ml/L H2O2 in 90min reaction period.Furthermore,the integrated process showed a rapid reaction performance at a low temperature within a short reaction time and remained high efficiencies for TOC removal.Overall,the integrated process was proved feasible for coking wastewater treatment in practical applications.
机译:实验研究了三维电极反应器与Fenton工艺联合处理焦化废水的综合过程的行为。初始pH值,反应时间,H2O2用量,Fe2 +用量对总有机碳(TOC)去除率的影响三维流化床电极反应器结合Fenton工艺对焦化废水中总有机碳的降解动力学进行了研究。实验结果表明,三维流化床电极反应器与Fenton工艺相结合具有较好的协同作用,平均17.4。在一小时内提高了TOC的去除率。发现焦化废水中的TOC降解遵循拟一级反应动力学模型。当pH3.4、3.5 mM Fe2 +时,TOC的最佳降解效率高达60%。在90min的反应时间和1.2〜1.8ml / L H2O2的作用下。总的来说,该综合工艺在实际应用中被证明可用于焦化废水的处理。

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