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Environmentally friendly way of complex extraction of nonferrous, rare and precious metals from ores and materials

机译:从矿石和材料中复杂提取有色,稀有和贵金属的环保方法

摘要

1. Environmentally friendly way to complex extraction ferrous, rare and precious metals from ores and materials, ores comprising leaching in two stages: the first stage of ore processing first circulating leach solution with the introduction of sulfuric acid, ferric salts and ferrous obtain productive solutions and / or rare metals, the second stage processing a second ore circulating leach solution with the introduction of sulfuric acid, salts of thiocyanates (thiocyanate) and ferric and productive yield sol Hur precious and / or rare metals, a separate solution processing each phase chemical deposition, sorption and / or by electrolysis and returns circulating fluids at appropriate stages, characterized in that in a first step the introduction of sulfuric acid and ferric iron in the leach solution is maintained in an amount providing at the end of the leaching solution in the productive molar concentration ratio of trivalent and bivalent iron ions is not less than 1: 1, and in a second step the introduction of sulfuric sour you salts thiocyanates and ferric iron in the leach solution is maintained in an amount to provide a productive solution the molar concentration ratio of thiocyanate ions and ferric not higher than 2: 1 and not less than 0.5: 1, and the molar concentration ratio of trivalent and bivalent iron ions and not less than 1: 1.2. A method according to claim 1, characterized in that, if necessary in the first stage to maintain the end of the leach the molar concentration ratio of trivalent and bivalent iron ions in a productive stretch
机译:1.以环保的方式从矿石和材料中复杂地提取铁,稀有和贵金属,矿石包括两个阶段的浸出:第一阶段是矿石加工,首先通过引入硫酸,铁盐和黑色金属的第一循环浸出溶液来获得生产解决方案和/或稀有金属,第二阶段通过引入硫酸,硫氰酸盐(硫氰酸盐)以及三价铁和生产性的贵金属和/或稀有金属的溶液来处理第二种矿石循环浸出溶液,分别处理各相化学物质沉积,吸附和/或通过电解并在适当的阶段返回循环流体,其特征在于,在第一步中,将硫酸和三价铁的引入量保持在浸出溶液末期提供的量。三价铁离子和二价铁离子的生产摩尔浓度比不小于1:1第二步,在浸出溶液中引入硫酸盐硫氰酸盐和三价铁的量要保持在一定的量,以提供一种生产性溶液,使硫氰酸盐离子与三价铁的摩尔浓度比不高于2:1且不低于0.5:1三价和二价铁离子的摩尔浓度比不小于1:1.2。 2.根据权利要求1所述的方法,其特征在于,如果需要在第一阶段中保持浸出结束,则在生产拉伸过程中三价和二价铁离子的摩尔浓度比

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