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Leaching Kinetics of Sulfides from Refractory Gold Concentrates by Nitric Acid

机译:硝酸对难处理金精矿中硫化物的浸出动力学

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The processing of refractory gold-containing concentrates by hydrometallurgical methods is becoming increasingly important due to the depletion of rich and easily extracted mineral resources, as well as due to the need to reduce harmful emissions from metallurgy, especially given the high content of arsenic in the ores. This paper describes the investigation of the kinetics of HNO 3 leaching of sulfide gold-containing concentrates of the Yenisei ridge (Yakutia, Russia). The effect of temperature (70–85 °C), the initial concentration of HNO 3 (10–40%) and the content of sulfur in the concentrate (8.22–22.44%) on the iron recovery into the solution was studied. It has been shown that increasing the content of S in the concentrate from 8.22 to 22.44% leads to an average of 45% increase in the iron recovery across the entire range temperatures and concentrations of HNO 3 per one hour of leaching. The leaching kinetics of the studied types of concentrates correlates well with the new shrinking core model, which indicates that the reaction is regulated by interfacial diffusion and diffusion through the product layer. Elemental S is found on the surface of the solid leach residue, as confirmed by XRD and SEM/EDS analysis. The apparent activation energy is 60.276 kJ/mol. The semi-empirical expression describing the reaction rate under the studied conditions can be written as follows: 1/3ln(1 ? X ) + [(1 ? X ) ?1/3 ? 1] = 87.811(HNO 3 ) 0.837 (S) 2.948 e ?60276/ RT · t .
机译:由于耗尽了丰富且易于提取的矿产资源,以及由于需要减少冶金方面的有害排放,特别是考虑到矿中砷的含量高,通过湿法冶金方法处理难熔含金精矿变得越来越重要。矿石。本文描述了叶尼塞山(俄罗斯雅库特)含硫化物金精矿中HNO 3浸出动力学的研究。研究了温度(70–85°C),HNO 3的初始浓度(10–40%)和精矿中硫的含量(8.22–22.44%)对铁在溶液中的回收率的影响。已经表明,将精矿中的S含量从8.22%增加到22.44%会导致整个浸提温度和每1个小时HNO 3浓度的铁回收率平均增加45%。研究类型的精矿的浸出动力学与新的收缩核模型有很好的相关性,这表明反应受界面扩散和通过产物层扩散的调控。通过XRD和SEM / EDS分析证实,元素S存在于固体浸出残渣的表面。表观活化能为60.276 kJ / mol。描述研究条件下反应速率的半经验表达式可以写为:1 / 3ln(1?X)+ [(1?X)?1/3? 1] = 87.811(HNO 3)0.837(S)2.948e≤60276/ RT·t。

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