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Effluent treatment using a bipolar electrochemical reactor with rotating cylinder electrodes of woven wire meshes

机译:使用带有旋转丝网电极的双极电化学反应器进行废水处理

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BACKGROUND: The behaviour of a bipolar electrochemical reactor consisting of one or more rotating cylinder electrodes ofwoven wire meshes is reported using copper and cadmium deposition from dilute solutions as test reactions. RESULTS: The best performance related to electrode number was determined for copper deposition and was achieved by anarrangement with two bipolar electrodes, for which the conversion in a single pass was approximately 47%. The specific energyconsumption was 3.27 kWh kg~(-1)with a normalised space velocity of 23.05 h-1. The copper powder obtained showed nodularand dendritic surface morphology. This reactor configuration was also analysed for cadmium deposition, in which hydrogenevolution takes place simultaneously as a side cathodic reaction, considering the effect of flow rate and total current. Themaximum conversion per pass for cadmium removal was 38.91%. In this case the reactor with two bipolar electrodes showed aperformance similar to that of a monopolar reactor operated at a rotation speed three times higher. CONCLUSION: A continuous electrochemical reactor with two rotating bipolar electrodes of woven wire meshes presents a goodperformance for copper or cadmium removal from dilute solutions.
机译:背景:报道了一种使用由稀溶液中的铜和镉沉积作为测试反应的,由一个或多个金属丝网旋转圆柱电极组成的双极电化学反应器的行为。结果:与电极数量有关的最佳性能已确定用于铜沉积,并通过与两个双极电极的排列实现,其单次转化率约为47%。比能耗为3.27 kWh kg〜(-1),归一化空速为23.05 h-1。得到的铜粉显示出结节状和树枝状的表面形态。还分析了该反应器配置的镉沉积情况,其中考虑了流速和总电流的影响,同时发生了氢演变,同时发生了副阴极反应。每次除镉的最大转化率为38.91%。在这种情况下,具有两个双极电极的反应堆的性能类似于以三倍高的转速运行的单极反应堆的性能。结论:具有两个旋转双极编织金属丝网电极的连续电化学反应器对于从稀溶液中去除铜或镉具有良好的性能。

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