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A CLEAN METHOD APPLYING ANION-EXCHANGE SEPARATION AND MEMBRANE-ELECTROLYSIS TO REGENERATE Fe-Zn-HCl SPENT PICKLING LIQUORS

机译:一种清洁方法,将阴离子交换分离和膜电解用于再生Fe-Zn-HCl废酸洗液

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We have developed a novel method - at the laboratory scale - comprising an ion-exchange separation and a membrane-electrolysis step for the purpose of zero-waste regeneration of spent HCl pickling liquors originating from hot-dip galvanizing of common steels. It is aimed at the parallel regeneration of HCl and iron. Experiments revealed that iron can be electrodeposited at high current efficiencies by maintaining the following conditions: 0.04-0.08 M HCl, 500-1000 A/m{sup}2, 20°C and stationary electrolyte in a conventional cell. Zinc in the solution did not disturb the deposition of iron, however it contaminated the product and it poisons the anion-exchange membrane required to tackle acidity during electrolysis. For a preliminary separation, anion-exchange tests were carried out to produce pure iron solutions. Beyond the equilibrium studies, column experiments were carried out showing that low flow rates of the loading solution and the ~1.5 M HCl eluent are essential for separation.
机译:我们开发了一种新的方法 - 在实验室规模 - 包括离子交换分离和膜电解步骤,用于源自普通钢的热浸镀锌的废酸酸盐液的零废物再生。它的目标是HCl和铁的平行再生。实验表明,通过在常规细胞中维持以下条件:0.04-0.08M HCl,500-1000A / m {sup} 2,20°C和固定电解质,可以在高电流效率下电沉积铁。溶液中的锌并未扰乱铁的沉积,但它污染了产品,并且它毒物在电解过程中处理酸度所需的阴离子交换膜。为了进行初步分离,进行阴离子交换测试以产生纯铁溶液。除了平衡研究之外,进行了柱实验,表明载荷溶液的低流速和〜1.5M HCl洗脱液对于分离是必不可少的。

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