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PROCESS FOR THE PRODUCTION OF ELECTROLYTIC ZINC OR HIGH PURITY ZINC SALTS FROM SECONDARY ZINC RAW- MATERIALS

机译:用二次锌原料生产电解锌或高纯锌盐的过程

摘要

ABSTRACTThe present invention relates to a process forthe production of either electrolytic zinc or high purityzinc salts from secondary zinc raw materials, comprising:leaching the raw material in a slightly acid aqueoussolution at controlled pH; separating the reaction mixtureinto a leaching liquor containing the leached zinc and asolid residue, which after suitable washing is discarded;directing the zinc-bearing liquor to a solvent extractionfacility where it is brought into contact with an organicsolution containing organic acids as cationic extractionreagents, by means of which, an ion exchange of zinc byhydrogen ions is achieved, resulting in a zinc loaded organicsolution and in an aqueous solution containing the stoichio-metric acidity to the extracted zinc; recycling the acidaqueous raffinate to the previous leaching step where it isused as the slightly acid aqueous solution to carry-out thezinc leaching from the raw material; sending the zinc organicextract to a stripping facility where it is brought intocontact with a strong acid solution of zinc sulphate, bymeans of which an ion exchange of zinc by hydrogen ions takesplace, thus producing a concentrated solution of zincsulphate and an organic solution free of zinc, containingthe stoichiometric acidity to the stripped zinc, which isrecycled back to the previous step to perform the zincextraction; directing the concentrated zinc sulphate aqueoussolution either to an electrowinning facility to produceelectrolytic zinc, or to a crystallization plant forthe production of pure zinc sulphate; recycling back tothe previous step of zinc stripping either the spentelectrolyte from the electrowinning facility or the motherliquors from the crystallization plant to form, aftersuitable sulphuric acid make-up, the strong acid solutionof zinc sulphate, by means of which zinc stripping fromthe organic extract is achieved.
机译:抽象本发明涉及一种用于电解锌或高纯度产品的生产来自次级锌原料的锌盐,包括:将原料浸入弱酸性水溶液中在控制pH下的溶液;分离反应混合物到含有浸出的锌和固体残留物,经适当洗涤后被丢弃;将含锌液体引导至溶剂萃取与有机物接触的设施含有机酸的溶液作为阳离子萃取试剂,通过这些试剂,锌离子通过实现氢离子,从而产生载有锌的有机物溶液和含有化学计量的水溶液提取锌的酸度;回收酸提余液到上一个浸出步骤用作弱酸性水溶液进行从原材料中浸出锌;传送有机锌提取到提炼设施中与硫酸锌的强酸溶液接触通过氢离子进行锌离子交换的方法产生锌的浓缩液硫酸盐和不含锌的有机溶液,包含汽提锌的化学计量酸度为回收到上一步执行锌萃取;引导浓硫酸锌水溶液解决方案到电子取款设备进行生产电解锌,或送到结晶厂进行纯硫酸锌的生产;回收回锌提纯的前一步骤来自电子取水设备或母亲的电解质结晶厂中形成的酒适用硫酸配方,强酸溶液硫酸锌,从中汽提锌实现了有机提取物。

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