Gallium and Arsenic Recovery from Waste Gallium Arsenide by Wet Refined Methods

被引:6
作者
Chen, Wei-Ting [1 ]
Chu, Yung-Chuan [1 ]
Wei, Jian-Ming [2 ]
Tsai, Lung-Chang [3 ]
Tsai, Fang-Chang [4 ]
Lin, Chun-Ping [5 ]
Shu, Chi-Min [3 ]
机构
[1] NYUST, Grad Sch Engn Sci & Technol, Doctoral Program, 123 Univ Rd,Sec 3, Touliu 64002, Yunlin, Taiwan
[2] HungKuang Univ, Environm Engn, Dept Safety Hlth, Taichung 43302, Taiwan
[3] Natl Yunlin Univ Sci & Technol, Environm Engn, Dept Safety Hlth, Disaster Prevent,Proc Safety, Touliu 64002, Yunlin, Taiwan
[4] Hubei Univ, Fac Mat Sci & Engn, Key Lab Green Preparat, Minist Educ,Funt Mat, Wuhan 430062, Peoples R China
[5] Asia Univ, Coll Hlth Sci, Dept Hlth & Nutrit Biotechnol, Taichung 41354, Taiwan
来源
ADVANCED ENGINEERING MATERIALS, PTS 1-3 | 2011年 / 194-196卷
关键词
Gallium Arsenide; Wet Refined Method; Di(2-Ethylhexyl) Phosphoric Acid; Electrolysis; Platinum-Stainless Steel;
D O I
10.4028/www.scientific.net/AMR.194-196.2115
中图分类号
T [工业技术];
学科分类号
08 ;
摘要
This study was focused on the recovery of gallium arsenide (GaAs) from semiconductor fabrication sludge. Wet refined methods were applied to recover gallium (Ga) including acid leaching, purified isolation, electrolysis, and coagulation. The result showed that leaching Ga with nitric acid (HNO3) was more efficient than with sulfuric acid (H2SO4). GaAs could be leached with 4 N HNO3 to obtain 100% Ga+ and arsenic (As-). The pH was adjusted with sodium hydroxide (NaOH). Then, the solution was extracted by di(2-ethylhexyl) phosphoric acid (D(2)EHPA) and was back extracted by H2SO4. In this way, Ga extraction efficiency was 80%. At the end of the process, electrolysis was applied to recover Ga. The resulting electrolysis efficiency with nickel-copper was only 56% and its purity was 92%. To further increase the recovery of Ga, the leaching solution was adjusted to alkaline solution and was then electrolyzed with platinum-stainless steel. In this way, recovery and purity could be as high as 90% and 94%, respectively. The removal of arsenic was 86% when the leaching solution was added with ferrous sulfate heptahydrate (Fe-2(SO4)(3) center dot xH(2)O) to form iron arsenate (AsFeO4).
引用
收藏
页码:2115 / +
页数:2
相关论文
共 7 条
[1]   Recovery of gallium and vanadium from gasification fly ash [J].
Font, Oriol ;
Querol, Xavier ;
Juan, Roberto ;
Casado, Raquel ;
Ruiz, Carmen R. ;
Lopez-Soler, Angel ;
Coca, Pilar ;
Garcia Pena, Francisco .
JOURNAL OF HAZARDOUS MATERIALS, 2007, 139 (03) :413-423
[2]   Extraction and recovery of Ga(III) from waste material using Cyanex 923 [J].
Gupta, Bina ;
Mudhar, Niti ;
Begum, Zareena ;
Singh, Indu .
HYDROMETALLURGY, 2007, 87 (1-2) :18-26
[3]  
Lee H.Y., 1994, PROCESS RECOVERY GAL
[4]   A study on the extraction of gallium from gallium arsenide scrap [J].
Lee, HS ;
Nam, CW .
HYDROMETALLURGY, 1998, 49 (1-2) :125-133
[5]   Effects of silicate, sulfate, and carbonate on arsenic removal by ferric chloride [J].
Meng, XG ;
Bang, S ;
Korfiatis, GP .
WATER RESEARCH, 2000, 34 (04) :1255-1261
[6]   Gallium: the backbone of the electronics industry [J].
Moskalyk, RR .
MINERALS ENGINEERING, 2003, 16 (10) :921-929
[7]  
Son S.H., 1993, J KOREAN INST MET MA, V31, P123