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

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中國有色金屬學(xué)報(bào)

ZHONGGUO YOUSEJINSHU XUEBAO

第27卷    第2期    總第215期    2017年2月

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文章編號(hào):1004-0609(2017)-02-0356-07
砷濾餅的銅砷分離
沈 忱1,閔小波1, 2, 3,史美清2,周波生1,趙宗文1,李轅成1,張 純1

(1. 中南大學(xué) 冶金與環(huán)境學(xué)院,長沙 410083;
2. 中南大學(xué) 國家重金屬污染防治工程技術(shù)研究中心,長沙 410083;
3. 中南大學(xué) 湖南省戰(zhàn)略金屬礦產(chǎn)資源清潔高效利用協(xié)同創(chuàng)新中心,長沙 410083
)

摘 要: 采用浸出方法使砷濾餅中的銅砷元素進(jìn)行分離,銅以硫化銅的形式沉淀,砷以砷酸根離子進(jìn)入溶液中。考察NaCl濃度、Na2S添加量、液固比、時(shí)間及溫度等因素對砷濾餅中砷、銅浸出率的影響。得出最優(yōu)的工藝條件如下:NaCl溶液濃度為20g/L、液固比7:1、Na2S與砷濾餅質(zhì)量比3:4、浸出時(shí)間4 h、溫度80 ℃、H2O2 20 mL。在此最優(yōu)工藝條件下,砷浸出率高達(dá)95.56%,銅浸出率低于0.5%,浸出渣銅含量富集至33.6%。浸出液采用硫酸亞鐵沉砷方法,沉砷率可以達(dá)到98%,生成的砷酸鐵晶體含砷量為32.15%,濾液含砷量為0.23g/L,濾液可以返回浸出過程,實(shí)現(xiàn)循環(huán)利用。

 

關(guān)鍵字: 砷濾餅;銅;砷;分離;浸出;脫砷

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

主管:中國科學(xué)技術(shù)協(xié)會(huì) 主辦:中國有色金屬學(xué)會(huì) 承辦:中南大學(xué)
湘ICP備09001153號(hào) 版權(quán)所有:《中國有色金屬學(xué)報(bào)》編輯部
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