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首页> 外文期刊>Chemical Engineering Research & Design: Transactions of the Institution of Chemical Engineers >Copper recovery and simultaneous COD removal from copper phthalocyanine dye effluent using bipolar disc reactor
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Copper recovery and simultaneous COD removal from copper phthalocyanine dye effluent using bipolar disc reactor

机译:使用双极盘式反应器从铜酞菁染料废水中回收铜并同时去​​除COD

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摘要

Electrochemical treatment of real acidic effluent of copper phthalocyanine dye manufacturing plant with a view to explore the feasibility of the simultaneous removal of copper and phthalocyanine using a bipolar disc electrochemical reactor has been investigated. Experiments were conducted in a bipolar capillary gap disc stack electrochemical reactor under batch recirculation mode. Electrodes were RuO2 and IrO2 coated on titanium as anode and titanium as cathode. Effects of current density, electrolysis time and effluent flow rate on copper recovery and simultaneous COD removal and energy consumption were critically examined. The current density of 2.5Adm~(-2) and flow rate of 20 L h~(-1) achieved 91.1% COD removal and 90.1% copper recovery with the energy consumption of 50.86 kWh kg~(-1) for COD removal and simultaneous recovery of copper in a bipolar disc stack reactor.
机译:为了研究使用双极盘电化学反应器同时去除铜和酞菁的可行性,对铜酞菁染料制造厂的实际酸性废水进行了电化学处理。在分批再循环模式下在双极毛细管间隙盘堆叠电化学反应器中进行实验。电极上涂有RuO2和IrO2,涂在钛上作阳极,钛作阴极。严格检查了电流密度,电解时间和废水流速对铜回收率以及同时去除COD和能耗的影响。 2.5Adm〜(-2)的电流密度和20 L h〜(-1)的流量实现了91.1%的COD去除率和90.1%的铜回收率,去除COD的能耗为50.86 kWh kg〜(-1)。在双极盘式堆反应器中同时回收铜。

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