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Chromium ions (Cr~(6+) & Cr~(3+)) removal from synthetic wastewater by electrocoagulation using vertical expanded Fe anode

机译:垂直膨胀铁阳极电凝去除合成废水中的铬离子(Cr〜(6+)和Cr〜(3+))

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摘要

The performance of an innovative batch cell design in removing chromium ions (Cr~(6+) & Cr~(3+)) from synthetic wastewater solutions by electrocoagulation has been investigated. The cell consists of two concentric vertical cylindrical Fe-electrodes; the outer electrode is a cylindrical solid Fe-cathode which is supported in the vessel wall, whereas the inner electrode is an expanded cylindrical Fe-anode. The distance between the two electrodes is 0.5 cm apart. The performance of the present cell has been expressed in terms of % removal of (Cr~(6+) & Cr~(3+)). The effect of key parameters such as electrolysis time, current density, pH, initial (Cr~(6+) & Cr~(3+)) ions concentration, NaCl concentration and electrode connection on the % removal (Cr~(6+) & Cr~(3+)) has been investigated. The study revealed that as current density increases, % Cr~(3+) removal slightly increases, whereas % Cr~(6+) removal slightly decreases. As NaCl concentration increases, % Cr~(6+) removal increases gradually, while % Cr~(3+) removal increases up to 1 g/l and decreases beyond this value. Maximum % Cr~(6+) removal occurs at pH 4.5, whereas maximum % Cr~(3+) removal occurs at pH 8. As the initial concentration of Cr ions increases, % Cr removal decreases. Monopolar parallel electrode connection is the optimum electrode connection. Power consumption evaluation of the present cell design reveals that power consumption increases as current density increases, while it decreases as NaCl concentration increases. Power consumption calculations show that at optimum conditions of Cr~(3+) removal by Electrocoagulation (EC) a 10.98 kW h/kg (1.09 kW h/m~3) is required whereas at optimum conditions of Cr~(6+) removal by Electrocoagulation (EC) a 16.14 kW h/kg (2.299 kW h/m~3) is required.
机译:研究了一种创新的间歇式电解池设计在通过电凝去除合成废水中的铬离子(Cr〜(6+)和Cr〜(3+))中的性能。电解池由两个同心的垂直圆柱状铁电极组成。外电极是支撑在容器壁上的圆柱形固态铁阴极,而内电极是膨胀的圆柱形铁阳极。两个电极之间的距离为0.5厘米。本电池的性能以(Cr〜(6+)和Cr〜(3+))的去除%表示。诸如电解时间,电流密度,pH,初始(Cr〜(6+)和Cr〜(3+))离子浓度,NaCl浓度以及电极连接等关键参数对%去除率(Cr〜(6+) &Cr〜(3+))已被研究。研究表明,随着电流密度的增加,Cr〜(3+)去除率略有增加,而Cr〜(6+)去除率略有下降。随着NaCl浓度的增加,Cr〜(6+)的去除率逐渐增加,而Cr〜(3+)的去除率增加到1 g / l,并​​降低到该值以下。最大的Cr〜(6+)去除百分比在pH值为4.5时发生,而最大的Cr〜(3+)去除百分比在pH值为8时出现。随着Cr离子初始浓度的增加,Cr去除的百分比降低。单极并联电极连接是最佳的电极连接。本电池设计的功耗评估表明,功耗随着电流密度的增加而增加,而随着NaCl浓度的增加而降低。功耗计算表明,在通过电凝(EC)去除Cr〜(3+)的最佳条件下,需要10.98 kW h / kg(1.09 kW h / m〜3),而在去除Cr〜(6+)的最佳条件下通过电凝(EC),需要16.14 kW h / kg(2.299 kW h / m〜3)。

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