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Impact of recycling cyanide and its reaction products on upstream unit operations

机译:氰化物及其反应产物的回收对上游装置运行的影响

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A typical operations outcome to dealing with the environmental and economic issues associated with cyanide in gold plant tailings streams involves the recycle of cyanide and its associated reaction products. This recycle stream may take the form of return dam water or tailings thickener overflow to the mill, or a cyanide recovery stream to the leach from a SART (sulphidization-acidification-recycling-thickening) or AVR (acidification-volatilization-reneutralization) circuit. The chemical composition and cyanide speci-ation of these solutions may be relatively complex, containing various metal cyanide species, thiocyanate, cyanate and other breakdown products. Several of these species are reported to have a deleterious effect on upstream unit operations. For example, while cyanide is in common use as a depressant for pyrite in mineral flotation, ferrocyanide and thiocyanate ions have also been shown to exhibit a depressant action in some cases. Primary flotation recovery of gold can thus be compromised and may be responsible for significant lost revenue, particularly from high-grade refractory gold operations. Bioleaching plants tend to separate cyanide circuits to an independent water balance to ensure that no cyanide or thiocyanate returns to inflict dire consequences on the bacterial population. Tolerable levels of these ions are exceedingly low, creating a risk factor and constraining water balance flexibility. Milling-in-cyanide has been periodically mooted as a beneficial circuit modification, particularly in operations that have tailings thickening, SART or dolomitic ore from which significant levels of free and complexed cyanides and thiocyanates are present. Potential consequences include unwanted side reactions with freshly activated mineral surfaces within mills operating at elevated temperatures and significant cyanide losses under these conditions.
机译:处理金厂尾矿流中与氰化物有关的环境和经济问题的典型操作成果涉及氰化物及其相关反应产物的再循环。该循环物流可以采用回流坝水或尾渣增稠剂溢流到工厂的形式,也可以采用氰化物回收流从SART(硫化-酸化-循环-增稠)或AVR(酸化-挥发-再中和)回路到浸出的形式。这些溶液的化学组成和氰化物规格可能相对复杂,包含各种金属氰化物,硫氰酸盐,氰酸盐和其他分解产物。据报道,这些物种中的几种对上游单元的运行具有有害作用。例如,尽管氰化物通常用作矿物浮选中黄铁矿的抑制剂,但在某些情况下,亚铁氰化物和硫氰酸根离子也表现出抑制作用。因此,一次浮选金的回收可能会受到损害,并可能导致大量的收入损失,尤其是来自高等级耐火金业务的收入损失。生物浸出厂倾向于将氰化物回路分离成独立的水平衡,以确保没有氰化物或硫氰酸盐的返回对细菌种群造成可怕的后果。这些离子的可容忍水平极低,这是一个危险因素,并限制了水平衡的灵活性。氰化物铣削作为一种有益的电路改进方法已定期提出来,特别是在尾矿变稠,SART或白云石矿石的作业中,其中存在大量游离和络合的氰化物和硫氰酸盐。潜在的后果包括在高温下运行的工厂内与新鲜活化的矿物表面发生有害的副反应,以及在这些条件下氰化物的大量损失。

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