Application and Upgrade of Ge Recovery Process Using B Reagent at Zhuzhou Smelter AITranslate
Abstract AITranslate
Application and upgrade of Ge recovery process using Breagent are presented. Practice shows that discontinuous addition of YW-100, instead of continuous, can lowered the YW-100 consumption to1/6-1/4 and reduced the emulsion during solvent extraction The use ofback extractant (B reagent) concentration of 0.5-1 .0 mol/L, instead offormer 2.0-2 .3 mol/L, can eliminated the two-stage cake scrubbing andevaporization operations, thus the environmental problem arising fromthe need for regular discharge of the excessive circulating solution hasbeen solved, Ge recovery is improved and consumption of B reagent isreduced.
KeyWords AITranslate
1肖华利.用“H”试剂从氧化锌酸浸液中回收锗的试验研究[J].稀有金属与硬质合金,1998,26(2):19-22. 被引量：1
2肖华利,夏永生.溶剂萃取锗过程中的乳化与消除[J].稀有金属与硬质合金,1999,27(3):52-54. 被引量：1
1刘志宏,张登凯,李玉虎,李启厚,艾侃.海绵铁中提取镓的研究[J].有色金属：冶炼部分,2005(3):33-35. 被引量：1
2周智华,莫红兵.稀散金属锗富集回收技术的研究进展[J].中国矿业,2006,15(2):64-67. 被引量：10
1谢访友,王纪,刘恒玉,牛玉清,赵瑞卿,舒毓璋,何贻柏,车文婷.从株洲冶铁厂氧化锌浸出液中萃取分离锗[J].有色金属：冶炼部分,1997(3):33-36. 被引量：4
2潘秀兰,王艳红,梁慧智,冯士超.国内外超低碳IF钢炼钢工艺分析[J].鞍钢技术,2009(1):6-9. 被引量：18
3张元福,陈家蓉.贵州含锗氧化铅锌矿资源的开发状况及前景[J].有色冶炼,1997(3):17-20. 被引量：9
4尹涛.新型碳氧枪在80t电炉的应用及改进[J].浙江冶金,2005(1):34-35.
5连铸[J].重钢技术,2005,48(2):57-57.
6徐郁,季煜.吃废工厂 吞下电镀废液 吐出稀贵金属[J].表面工程资讯,2008,8(5):25-25.
7赫冀成,张兴和.底吹钢包精炼装置内循环液的特性[J].鞍钢自动化,1993(4):32-40.
8邓志敢,魏昶,李兴彬,徐红胜,李旻廷,李存兄,樊刚.钒钛磁铁矿提钒尾渣浸取钒[J].中国有色金属学报,2012,22(6):1770-1777. 被引量：20
9杨庄.澳斯麦特熔炼技术在金昌冶炼厂的应用及改进[J].有色冶炼,2004,33(1):14-16. 被引量：3
10袁方,聂长果,陶飞.低耗稳定型炮泥在马钢2号高炉的应用[J].炼铁,2006,25(5):47-50. 被引量：2
Basic Information:
DOI：
Chinese Library Classification Number:TF843.052[冶金工程—有色金属冶金]
Citation Information:
Application and upgrade of Ge recovery process using Breagent are presented. Practice shows that discontinuous addition of YW-100, instead of continuous, can lowered the YW-100 consumption to1/6-1/4 and reduced the emulsion during solvent extraction The use ofback extractant (B reagent) concentration of 0.5-1 .0 mol/L, instead offormer 2.0-2 .3 mol/L, can eliminated the two-stage cake scrubbing andevaporization operations, thus the environmental problem arising fromthe need for regular discharge of the excessive circulating solution hasbeen solved, Ge recovery is improved and consumption of B reagent isreduced.
quote
| GB/T 7714-2015 | [1] XIAO Hua-li. Application and Upgrade of Ge Recovery Process Using B Reagent at Zhuzhou Smelter[J]. Rare Metals and Cemented Carbides, 1996(1): 11-14. |
| MLA | [1] XIAO Hua-li. "Application and Upgrade of Ge Recovery Process Using B Reagent at Zhuzhou Smelter." Rare Metals and Cemented Carbides, no. 1, 1996, pp. 11-14. |
| APA | [1] XIAO Hua-li. (1996). Application and Upgrade of Ge Recovery Process Using B Reagent at Zhuzhou Smelter. Rare Metals and Cemented Carbides(1), 11-14. |
| IEEE | [1] XIAO Hua-li, "Application and Upgrade of Ge Recovery Process Using B Reagent at Zhuzhou Smelter," Rare Metals and Cemented Carbides, no. 1, pp. 11-14, 1996. keywords: {B reagent (back extractant of Ge), Ge recovery process,upgrade} |