Selective Separation of Arsenic from High-Arsenic Dust in the NaOH-S System Based on Response Surface Methodology

被引:2
|
作者
Zhang, Lei [1 ,2 ]
Guo, Xue-yi [1 ,2 ]
Tian, Qing-hua [1 ,2 ]
Qin, Hong [1 ,2 ]
机构
[1] Cent South Univ, Sch Met & Environm, Changsha 410083, Peoples R China
[2] China Nonferrous Met Ind Assoc, Cleaner Met Engn Res Ctr, Changsha 410083, Peoples R China
基金
中国国家自然科学基金; 湖南省自然科学基金;
关键词
Arsenic separate; Arsenic dust; Alkaline leaching; Response surface methodology; SODIUM-HYDROXIDE; BEARING DUST; REMOVAL; ANTIMONY; COPPER; EXTRACTION; ACID; RICH; STABILIZATION; BEHAVIOR;
D O I
10.1007/s40831-021-00372-0
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The selective separation of arsenic in the NaOH-S system from arsenic dust containing Pb, Sb, and Zn was studied by central composite design response surface method in this investigation. The results indicated that the presence of elemental sulfur can prevent lead and antimony leaching from arsenic dust effectively. The optimal leaching conditions were established as follows: 3.0 mol/L sodium hydroxide, 10 g/L sulfur, leaching temperature 95 degrees C, leaching time 2.0 h, liquid to solid ratio 6, and stirring speed 400 r/min. The arsenic leaching efficiency can reach 99.37% under the optimized conditions, meanwhile 98.39% of Sb, 99.74% of Zn, and 99.91% of Pb remained in the leach residue with the arsenic content < 0.1%. Oxidation-cooling crystallization has been used to recover sodium arsenate from the leaching solution under the optimal reaction conditions: C(H2O2)/C(As) 0.45, oxidation temperature 50 degrees C, stirring speed 200 r/min, crystallization temperature 30 degrees C, and crystallization time 120 min. This work presents a novel route for selective separation of arsenic and potential recycling lead and antimony from the arsenic dust in the NaOH leaching system with adding elemental sulfur.
引用
收藏
页码:684 / 703
页数:20
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