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Recovery of valuable metals from a low-grade nickel ore using an ammonium sulfate roasting-leaching process

机译:使用硫酸铵焙烧浸出过程从低级镍矿石中回收贵金属

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Metal leaching from a low-grade nickel ore was investigated using an ammonium sulfate roasting-water leaching process. The nickel ore was mixed with ammonium sulfate, followed by roasting and finally leaching with water. During the process the effects of the amount of ammonium sulfate, roasting temperature, and roasting time on the leaching recovery of metal elements were analyzed. The optimum technological parameters were determined as follows: ammonium sulfate/ore ratio, 0.8 g/g; roasting temperature, 400 deg C; and roasting time, 2 h. Under the optimum condition the leaching recoveries of Ni, Cu, Fe, and Mg were 83.48%, 76.24%, 56.43%, and 62.15%, respectively. Furthermore, the dissolution kinetics of Ni and Mg from the nickel ore was studied. The apparent activation energies for the leaching reaction of Ni and Mg were 18.782 and 10.038 kJ-mol~(-1), which were consistent with the values of diffusion control reactions. Therefore, the results demonstrated that the leaching recoveries of Ni and Mg were controlled by diffusion.
机译:使用硫酸铵焙烧 - 水浸出方法研究了从低级镍矿石的金属浸出。将镍矿与硫酸铵混合,然后焙烧,最后用水浸出。在过程中,分析了硫酸铵,焙烧温度和焙烧时间对金属元素浸出回收的影响。最佳的技术参数如下确定:硫酸铵/矿石比,0.8g / g;烤温度,400℃;和烤的时间,2小时。在最佳条件下,Ni,Cu,Fe和Mg的浸出回收率分别为83.48%,76.24%,56.43%和62.15%。此外,研究了来自镍矿石的Ni和Mg的溶出动力学。 Ni和Mg的浸出反应的表观活化能量为18.782和10.038 kJ-mol〜(-1),其与扩散控制反应的值一致。因此,结果表明Ni和Mg的浸出回收是通过扩散控制的。

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