Leaching and kinetic modelling of low-grade calcareous sphalerite in acidic ferric chloride solution

被引:47
作者
Dehghan, R. [1 ]
Noaparast, M. [1 ]
Kolahdoozan, M. [1 ]
机构
[1] Univ Tehran, Univ Coll Engn, Sch Min Engn, Tehran, Iran
关键词
Leaching kinetics; Modeling; Ferric chloride; Calcareous sphalerite; Statistical design; DISSOLUTION KINETICS; ZINC-SULFIDE; CONCENTRATE; OPTIMIZATION; COPPER; LEAD;
D O I
10.1016/j.hydromet.2008.11.002
中图分类号
TF [冶金工业];
学科分类号
0806 ;
摘要
The leaching kinetics of a low grade-calcareous sphalerite concentrate containing 38% ankerite and assaying 32% Zn, 7% Pb and 2.2% Fe was studied in HCI-FeCl3 solution. An L-16 (five factors in four levels) standard orthogonal array was employed to evaluate the effect of Fe(III) and HCl concentration, reaction temperature, solid-to-liquid ratio and particle size on the reaction rate of sphalerite. Statistical techniques were used to determine that pulp density and Fe(III) concentration were the most significant factors affecting the leaching kinetics and to determine the optimum conditions for dissolution. The kinetic data were analyzed with the shrinking particle and shrinking core models. A new variant of the shrinking core model (SCM) best fitted the kinetic data in which both the interfacial transfer and diffusion across the product layer affect the reaction rate. The orders of reaction with respect to (CFe3+), (C-HCl), and (S/L) were 0.86. 0.21 and - 1.54, respectively. The activation energy for the dissolution was found to be 49.2 kJ/mol and a semi-empirical rate equation was derived to describe the process. Similar kinetic behavior was observed during sphalerite dissolution in acidic ferric sulphate and ferric chloride solutions, but the reaction rate constants obtained by leaching in chloride Solutions were about tenfold higher than those in sulphate solutions. (C) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:275 / 282
页数:8
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