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TREATMENT OF NICKEL-CONTAINING WASTE WATER ON PHOSPHATING

机译:磷处理含镍废水的处理

摘要

Production of a nickel-containing solution consisting of a phosphating bath overflow and/or rinsing water comprises phosphating using an acidic phosphatizing solution containing 3-50 g/l phosphate ions, 0.2-3 g/l zinc ions, 0.01-2.5 g/l nickel ions and optionally further metal ions and an accelerator. The bath overflow and/or the rinsing water is passed over a weakly acidic ion exchanger after phosphating. The acid groups of the ion exchanger are neutralized to not more than 15 % with alkali metal ions. The nickel-containing aqueous solution has a pH of 2.5-6.0 on charging to the ion exchanger. Preferred Features: The bath overflow and/or the rinsing water is subjected to membrane filtration in the form of ultrafiltration, nanofiltration, reverse osmosis or other filtering process, and the aqueous solution is fed over the ion exchanger after filtering. The weakly acidic ion exchanger binds nickel ions stronger than zinc ions. The ion exchanger supports chelate-forming iminodiacetic acid groups.
机译:由磷化浴溢流和/或冲洗水组成的含镍溶液的生产包括使用含有3-50 g / l磷酸根离子,0.2-3 g / l锌离子,0.01-2.5 g / l的酸性磷化溶液进行磷化镍离子以及其他金属离子和促进剂。磷化后,镀液溢流和/或冲洗水通过弱酸性离子交换剂。离子交换剂的酸基团被碱金属离子中和至不超过15%。含镍水溶液在加入离子交换剂时的pH值为2.5-6.0。优选特征:将浴溢流和/或冲洗水以超滤,纳滤,反渗透或其他过滤过程的形式进行膜过滤,并且在过滤之后将水溶液进料到离子交换剂上。弱酸性离子交换剂与镍离子的结合力比锌离子强。离子交换剂支持形成螯合物的亚氨基二乙酸基团。

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