首页> 外国专利> Electrochemical treatment of aluminum-containing solution, e.g. spent aluminum surface treatment or rinsing solution, comprises electrolysis and electrodialysis in a divided cell containing a precious metal, oxide and/or mixed oxide anode

Electrochemical treatment of aluminum-containing solution, e.g. spent aluminum surface treatment or rinsing solution, comprises electrolysis and electrodialysis in a divided cell containing a precious metal, oxide and/or mixed oxide anode

机译:含铝溶液的电化学处理,例如废铝表面处理或冲洗溶液,包括在包含贵金属,氧化物和/或混合氧化物阳极的分隔式电池中进行电解和电渗析

摘要

Electrochemical treatment of aluminum-containing solutions involves electrolysis and electrodialysis in a divided electrolysis cell (3) containing a precious metal, oxide and/or mixed oxide anode (6). Independent claims are given for a process and a cell are claimed for electrochemical treatment of aluminum-containing solutions. The process includes pumping or periodically filling the solution as electrolyte (4) into a chamber (2) of a divided electrolysis cell (3) so that electrochemical reaction of (preferably chromium-containing) solution components occurs at the electrode (6). Other solution components (preferably aluminum and other impurity metal ions) migrate into another electrode chamber (2a) containing an agitated or moving electrolyte and form less soluble metal, hydroxide and/or similar compounds or deposits at a deposition electrode well spaced from the cell separator (5). The current density is 0.1-10 (preferably 2.5-7) A/dm2, the electrolyte in the other electrode chamber (2a) is preferably a mineral acid solution with a minimum conductivity of 0.25 S/m, the cathode preferably consists of a metal, a carbonaceous material or metallized plastic and the anode consists of a precious metal and/or an electrochemically active anode layer of oxide and/or mixed oxide structure preferably of one or more oxides of Ti, Ir, Ta, Ru, Pt, Mn, Pb, Cr, Ag, Sb, Ni and Sn.
机译:含铝溶液的电化学处理包括在包含贵金属,氧化物和/或混合氧化物阳极(6)的分隔式电解槽(3)中进行电解和电渗析。给出了一种方法的独立权利要求,并且要求保护一种用于电化学处理含铝溶液的电池。该方法包括将作为电解质(4)的溶液泵送或周期性地填充到分开的电解池(3)的腔室(2)中,使得(优选含铬的)溶液组分的电化学反应在电极(6)处发生。其他溶液成分(最好是铝和其他杂质金属离子)迁移到另一个包含搅动或移动电解质的电极腔室(2a)中,并在与电池分隔器相距一定距离的沉积电极上形成难溶的金属,氢氧化物和/或类似化合物或沉积物(5)。电流密度为0.1-10(优选2.5-7)A / dm 2,另一个电极室(2a)中的电解质优选为最小电导率为0.25S / m的无机酸溶液,阴极优选由金属,碳质材料或金属化塑料制成,阳极由贵金属和/或氧化物和/或混合氧化物结构的电化学活性阳极层组成,最好由一种或多种Ti,Ir,Ta,Ru,Pt氧化物组成,Mn,Pb,Cr,Ag,Sb,Ni和Sn。

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