Transactions of Nonferrous Metals Society of China The Chinese Journal of Nonferrous Metals

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中国有色金属学报

ZHONGGUO YOUSEJINSHU XUEBAO

第27卷    第2期    总第215期    2017年2月

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文章编号:1004-0609(2017)-02-0356-07
砷滤饼的铜砷分离
沈 忱1,闵小波1, 2, 3,史美清2,周波生1,赵宗文1,李辕成1,张 纯1

(1. 中南大学 冶金与环境学院,长沙 410083;
2. 中南大学 国家重金属污染防治工程技术研究中心,长沙 410083;
3. 中南大学 湖南省战略金属矿产资源清洁高效利用协同创新中心,长沙 410083
)

摘 要: 采用浸出方法使砷滤饼中的铜砷元素进行分离,铜以硫化铜的形式沉淀,砷以砷酸根离子进入溶液中。考察NaCl浓度、Na2S添加量、液固比、时间及温度等因素对砷滤饼中砷、铜浸出率的影响。得出最优的工艺条件如下:NaCl溶液浓度为20g/L、液固比7:1、Na2S与砷滤饼质量比3:4、浸出时间4 h、温度80 ℃、H2O2 20 mL。在此最优工艺条件下,砷浸出率高达95.56%,铜浸出率低于0.5%,浸出渣铜含量富集至33.6%。浸出液采用硫酸亚铁沉砷方法,沉砷率可以达到98%,生成的砷酸铁晶体含砷量为32.15%,滤液含砷量为0.23g/L,滤液可以返回浸出过程,实现循环利用。

 

关键字: 砷滤饼;铜;砷;分离;浸出;脱砷

Separation of copper and arsenic in arsenic filtration cake
SHEN Chen1, MIN Xiao-bo1, 2, 3, SHI Mei-qing2, ZHOU Bo-sheng1, ZHAO Zong-wen1, LI Yuan-cheng1, ZHANG Chun1

1. School of Metallurgy and Environment, Central South University, Changsha 410083, China;
2. Chinese National Engineering Research Center for Control and Treatment of Heavy Metal Pollution, Central South University, Changsha 410083, China;
3. Co-Innovation Center for Clean and Efficient Utilization of Strategic Metal Mineral Resources, Central South University, Changsha 410083, China

Abstract:Leaching method was used to separate copper and arsenic in the arsenic filtration cake, which was achieved by the formation of CuS in the residue and AsO43- in the solution during the leaching process. The effects of various parameters, such as concentrations of NaCl, mass ratio of Na2S to arsenic filtration cake, liquid-solid ratio, leaching time and temperature, on leaching rate of As and Cu were investigated. On this basis, the optimal conditions are obtained through single factor experiment as follows, 20 g/L NaCl, liquid-solid ratio 7:1, mass ratio of Na2S to arsenic filtration cake 3:4, leaching at 80 ℃ for 4h, with 20 mL H2O2. Under this optimal condition, the leaching rate of As reaches 95.56%, and leaching rate of Cu is less than 0.5%. The copper content in leaching residue is as high as 33.6% (mass fraction). In addition, arsenic-containing leachate can be treated with FeSO4 and removal rate of As in leachate exceeds 98%. Arsenic content in the generated crystal is 32.15% (mass fraction), and arsenic concentration in the effluent is 0.23 g/L which can be returned to the leaching process.

 

Key words: arsenic filtration cake; copper; arsenic; separation; leaching; arsenic removal

ISSN 1004-0609
CN 43-1238/TG
CODEN: ZYJXFK

ISSN 1003-6326
CN 43-1239/TG
CODEN: TNMCEW

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