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Optimization of material and energy consumption for removal of Acid Red 14 by simultaneous electrocoagulation and electroflotation

机译:通过同时电凝和电浮选去除酸性红14的材料和能耗的优化

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Decolorization of wastewater of industries which consume dye is an environmental priority. Electrocoagulation and electroflotation methods are appropriate for treatment of these wastewaters. This study investigates the effect of four parameters, electrical conductivity, current density, initial dye concentration, and initial pH, on the performance of a simultaneous electrocoagulation/electroflotation system for removal of Acid Red 14. The optimum values of these parameters were determined based on the amount of electrical energy and aluminum consumption and the best performance of coagulation and bubble generation. The optimum condition was revealed to be electrical conductivity = 1,600 mu S/cm, current density = 60 mA/cm(2), initial dye concentration = 185 mg/L and initial pH = 7. After less than 180 min of electrolysis, 90% dye removal was achieved with a specific energy consumption = 102 kWh/kg dyeremoved, anode dissolution = 2.09 kg Al/kg dyeremoved and sludge total suspended solids = 15,050 mg/L. Liquid chromatography-UV-mass spectroscopy analyses were conducted on samples of raw and treated wastewater. Results showed that intermediate compounds formed from the breaking of the dye molecules. The advantages of this method are a low material and energy consumption. The amount of produced sludge was low; consequently sludge disposal and management costs would be reduced. This method should be used cautiously for treatment of textile wastewater due to the formation of intermediate compounds.
机译:消耗染料的工业废水的脱色是环境优先事项。电凝和电浮法适合处理这些废水。这项研究调查了电导率,电流密度,初始染料浓度和初始pH值这四个参数对同时电凝/电浮系统去除酸性红14的性能的影响。确定了这些参数的最佳值是基于电能和铝的消耗量以及最佳的凝结和气泡生成性能。最佳条件显示为电导率= 1,600μS / cm,电流密度= 60 mA / cm(2),初始染料浓度= 185 mg / L,初始pH =7。在不到180分钟的电解时间后,90去除特定染料的能耗= 102 kWh / kg染料,去除阳极溶解度= 2.09 kg Al / kg染料,污泥总悬浮固体= 15,050 mg / L,可实现%的染料去除率。液相色谱-紫外-质谱分析是对原废水和处理过的废水进行的。结果表明,中间体化合物是由染料分子的断裂形成的。该方法的优点是材料和能量消耗低。产生的污泥量低;因此,污泥处置和管理成本将减少。由于形成中间化合物,因此应谨慎使用该方法处理纺织废水。

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