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牺牲铁电极电化学处理及运行成本分析纺织废水。

Electrochemical treatment and operating cost analysis of textile wastewater using sacrificial iron electrodes.

机构信息

Department of Environmental Engineering, Gebze Institute of Technology, Gebze 41400, Turkey.

出版信息

Water Sci Technol. 2009;60(9):2261-70. doi: 10.2166/wst.2009.672.

Abstract

Electrocoagulation (EC) method with iron electrode was used to treat the textile wastewater in a batch reactor. Iron electrode material was used as a sacrificial electrode in monopolar parallel mode in this study. The removal efficiencies of the wastewater by EC were affected by initial pH of the solution, current density, conductivity and time of electrolysis. Under the optimal experimental conditions (initial pH 6.9, current density of 10 mA/cm(2), conductivity of 3,990 microS/cm, and electrolysis time of 10 min), the treatment of textile wastewater by the EC process led to a removal capacity of 78% of chemical oxygen demand (COD) and 92% of turbidity. The energy and electrode consumptions at the optimum conditions were calculated to be 0.7 kWh/kg COD (1.7 kWh/m(3)) and 0.2 kgFe/kg COD (0.5 kgFe/m(3)), respectively. Moreover, the operating cost was calculated as 0.2 euro/kg removed COD or 0.5 euro/m(3) treated wastewater. Zeta potential measurement was used to determine the charge of particle formed during the EC which revealed that Fe(OH)(3) might be responsible for the EC process.

摘要

电化学凝聚(EC)法采用铁电极在批式反应器中处理纺织废水。在本研究中,铁电极材料以单极平行模式作为牺牲电极使用。EC 对废水的去除效率受溶液初始 pH 值、电流密度、电导率和电解时间的影响。在最佳实验条件(初始 pH 值 6.9、电流密度 10 mA/cm(2)、电导率 3,990 microS/cm 和电解时间 10 分钟)下,EC 工艺处理纺织废水可使化学需氧量(COD)去除率达到 78%,浊度去除率达到 92%。在最佳条件下,能量和电极消耗分别计算为 0.7 kWh/kg COD(1.7 kWh/m(3))和 0.2 kgFe/kg COD(0.5 kgFe/m(3))。此外,运行成本计算为 0.2 欧元/千克去除的 COD 或 0.5 欧元/m(3)处理的废水。Zeta 电位测量用于确定 EC 过程中形成的颗粒的电荷,结果表明 Fe(OH)(3)可能是 EC 过程的原因。

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