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Studies on leaching of massive rich copper ore in acidic ferric sulfate solutions

机译:酸性硫酸铁溶液中浸出块状富铜矿的研究

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摘要

Representative samples of Kure (Turkey) massive rich copper ore were leached in acidic ferric sulfate solutions in order to recover copper and its associated metals (Zn, Co, Ni) present in the ore. The effects of leaching time, ferric ion concentration, acid concentration, solid/liquid ratio, temperature and silver sulfaste addition on metal leaching recoveries were investigated. Optimum leaching conditions and leaching kinetics were determined. Formation of elemental sulfur, which creates a diffusion barrier, was elucidated. In order to remove the retarding effect of elemental sulfur, silver ions were introduced to the leach medium and significant improvements were observed, especially in copper dissolution. Activation energies were found to be 36.7 kJ/mole for Cu and 43.3 kJ/mole for Zn dissolutions. The rate-controlling step was found as the diffusion of ferric ions into the solution filling the pores of sulfur layer formed on the surface of partially leached ore particles.
机译:为了回收矿石中存在的铜及其伴生金属(Zn,Co,Ni),在酸性硫酸铁溶液中浸提了代表性的Kure(土耳其)块状富铜矿样品。研究了浸出时间,三价铁离子浓度,酸浓度,固液比,温度和硫酸亚银添加量对金属浸出回收率的影响。确定了最佳浸出条件和浸出动力学。阐明了形成扩散阻挡层的元素硫的形成。为了消除元素硫的阻滞作用,将银离子引入浸出介质并观察到显着的改善,特别是在铜溶解方面。发现活化能对于Cu为36.7kJ /摩尔,对于Zn溶解为43.3kJ /摩尔。速率控制步骤被发现为铁离子扩散到溶液中,该溶液充满了部分浸出的矿石颗粒表面上形成的硫层孔隙。

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