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闪锌矿氧压氨浸过程动力学研究
引用本文:刘春霞,尹周澜,丁治英,黄雅玲. 闪锌矿氧压氨浸过程动力学研究[J]. 矿冶工程, 2017, 37(4): 77-81. DOI: 10.3969/j.issn.0253-6099.2017.04.021
作者姓名:刘春霞  尹周澜  丁治英  黄雅玲
作者单位:中南大学 化学化工学院, 湖南 长沙 410083
基金项目:国家重点基础研究发展计划(973计划)(2014CB643401);国家自然科学基金(51404299)
摘    要:在NH3-(NH4)2SO4体系中, 采用氧压氨浸工艺, 研究了闪锌矿的浸出行为。研究表明, 在浸出温度110 ℃、总氨浓度4 mol/L、NH3与NH4+浓度比为5∶3、总压0.5 MPa、搅拌速度500 r/min、液固比25、矿物粒度-0.063 mm条件下浸出5 h, 锌浸出率可达97%。采用液固反应的收缩核模型进行模拟, 得到了闪锌矿氧压氨浸的浸出动力学方程式, 其表观活化能为47.26 kJ/mol。

关 键 词:闪锌矿  氧压氨浸  NH3-(NH4)2SO4体系  动力学  
收稿时间:2017-02-26

Kinetics of Sphalerite in Oxygen-pressure Ammonia-leaching Process
LIU Chun-xia,YIN Zhou-lan,DING Zhi-ying,HUANG Ya-ling. Kinetics of Sphalerite in Oxygen-pressure Ammonia-leaching Process[J]. Mining and Metallurgical Engineering, 2017, 37(4): 77-81. DOI: 10.3969/j.issn.0253-6099.2017.04.021
Authors:LIU Chun-xia  YIN Zhou-lan  DING Zhi-ying  HUANG Ya-ling
Affiliation:School of Chemistry and Chemical Engineering, Central South University, Changsha 410083, Hunan, China
Abstract:The leaching behavior of sphalerite concentrate in NH3-(NH4)2SO4 solution by oxygen-pressure ammonia-leaching process was investigated. The leaching rate of zinc could be up to 97% after 5h-leaching process under the following optimum conditions, including a leaching temperature of 110 ℃ with pressure of 0.5 MPa, a particle size of -0.063 mm, 2.5 mol/L NH3, 0.75 mol/L (NH4)2SO4, with total ammonia concentration at 4 mol/L, agitation speed at 500 r/min, liquid/solid ratio at 25. The shrinking core model for liquid-solid reaction was adopted for simulation to obtain the kinetic equation of sphalerite in the oxygen-pressure ammonia-leaching process. Then, the apparent activation energy was determined to be 47.26 kJ/mol.
Keywords:sphalerite  oxygen-pressure ammonia-leaching  NH3-(NH4)2SO4 solution  kinetics  
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