首页> 外国专利> ELECTROLYSIS PROCEDURES FOR REGENDING AN EISEN-III CHLORIDE OR EISEN-III SULPHICLE SOLUTION, MORE SPECIFIC TO THE PROCESSING OF STEEL

ELECTROLYSIS PROCEDURES FOR REGENDING AN EISEN-III CHLORIDE OR EISEN-III SULPHICLE SOLUTION, MORE SPECIFIC TO THE PROCESSING OF STEEL

机译:再生EISEN-III氯化物或EISEN-III硫化物溶液的电解方法,尤其是在钢的加工过程中

摘要

An electrolysis process for regenerating a ferric chloride or sulphate solution (etchant), in particular for spray etching steel, is disclosed. The etchant to be regenerated continuously flows through the anode chamber (17) of an electrolytic cell (10) whose cathode chamber (14) is filled with a diluted conductive acid. Anode and cathode chambers (12 and 14) are separated by a cation exchange membrane (16) through which Fe(II) ions, excess Fe(III) and dissolved non-ferrous metals, in particular nickel and chromium ions, reach the cathode chamber (14), while Fe(II) ions are oxidised into FE(III) ions at the anode. The metals accumulated in the catholyte preferably precipitate as a powder in the cathode chamber (14) or are electrolytically precipitated in a subsequent electrolytic cell whose cathode and anode chambers are separated by an anion exchange membrane. This process allows the etchant to be continuously regenerated in a closed circuit, ensures the depletion of non-ferrous metals and excess iron, as well as the electrolytic precipitation of the depleted metal ions.
机译:公开了一种用于再生氯化铁或硫酸铁溶液(蚀刻剂)的电解方法,特别是用于钢的喷雾蚀刻。待再生的蚀刻剂连续流过电解池(10)的阳极室(17),该电解池的阴极室(14)充满了稀的导电酸。阳极室和阴极室(12和14)被阳离子交换膜(16)隔开,Fe(II)离子,过量的Fe(III)和溶解的有色金属(尤其是镍和铬离子)通过阳离子交换膜到达阴极室(14),而Fe(II)离子在阳极被氧化成FE(III)离子。积累在阴极电解液中的金属优选以粉末形式沉淀在阴极室(14)中,或者在随后的电解池中电解沉淀,该电解池的阴极室和阳极室被阴离子交换膜隔开。该工艺可使蚀刻剂在闭合回路中连续再生,确保消耗有色金属和过量的铁,以及电解沉积沉淀的金属离子。

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