期刊文献+

Study of decomposing carbonyl slag

Study of decomposing carbonyl slag
在线阅读 下载PDF
导出
摘要 A new technology was put forward to deal with the carbonyl slag at low acidity and low oxygen pressure in the kettle. With the orthogonal experiments for analyzing the sequence of four factors and some single factor experiments for the best conditions. The best conditions are used for extracting nickel, cobalt and copper and enriching precious metals: the cupric ion concentration is 5 g/L; and pH=6; the sulfur coefficient is 1.4; the oxygen pressure is 0.08 MPa; the time bubbling oxygen is 20 min; the ratio of liquid to solid is 8:1; the leaching time is 2 h; the heating time is 2.5 h. The leaching rates of nickel and cobalt are more than 98% and that of copper is above 97%. Nickel and cobalt can be separated efficiently from copper and precious metals from the carbonyl slag. Moreover, its leaching liquor has less copper. Nickel and cobalt can be reclaimed only once. During the whole process, the leaching rates of Au and Ag are more than 99.9%, while other precious metals are still in the residue without any loss. A new technology was put forward to deal with the carbonyl slag at low acidity and low oxygen pressure in the kettle. With the orthogonal experiments for analyzing the sequence of four factors and some single factor experiments for the best conditions. The best conditions are used for extracting nickel, cobalt and copper and enriching precious metals: the cupric ion concentration is 5 g/L; and pH=6; the sulfur coefficient is 1.4; the oxygen pressure is 0.08 MPa; the time bubbling oxygen is 20 rain; the ratio of liquid to solid is 8:1; the leaching time is 2 h; the heating time is 2.5 h. The leaching rates of nickel and cobalt are more than 98% and that of copper is above 97%. Nickel and cobalt can be separated efficiently from copper and precious metals from the carbonyl slag. Moreover, its leaching liquor has less copper. Nickel and cobalt can be reclaimed only once. During the whole process, the leaching rates of Au and Ag are more than 99.9%, while other precious metals are still in the residue without any loss.
出处 《中国有色金属学会会刊:英文版》 EI CSCD 2006年第2期477-482,共6页 Transactions of Nonferrous Metals Society of China
关键词 羰基矿渣 分解 浸出 有色金属 综合利用 carbonyl slag nickel cobalt copper low oxygen pressure leaching reclaiming efficiency leaching rates
  • 相关文献

参考文献2

二级参考文献14

  • 1傅崇说.有色冶金原理[M].冶金工业出版社,1990,10..
  • 2库巴谢夫斯基O 奥尔考克CB 邱竹贤 梁英教 李席孟 译.冶金热化学[M].北京: 冶金工业出版社,1985..
  • 3Tyroler PM.羰基镍文集(第一辑)(下册)[C].金川公司情报室译.1996.77-85.
  • 4武汉大学,吉林大学,等.无机化学(第三版)(上册)[M].北京:高等教育出版社,1995.
  • 5天津大学物理化学教研室.朱世谟,庄公惠,王正烈修正.物理化学(第三版)(上册)[M].北京:高等教育出版社,1997.
  • 6任鸿九,王立川.有色冶金提取手册(铜镍卷)[M].北京:冶金工业出版社,2000.
  • 7Akio Yamamoto. A reminiscence and a future prospect of transition metal-catalyzed cross-coupling processes [J]. Journal of Organometallic Chemistry, 2002,653:5 - 10.
  • 8Moskalyk R R, Alfantazi A M. Nickel laterite processing and electrowinning practice[J]. Minerals Engineering,2002, 15:593 - 606.
  • 9Cristina Femoni, Maria Carmela lapalucci, Giuliano Longoni. The new enneanuclear nickel carbonyl anion [ Ni9 (CO) 16 ] 2 - and its relationships with the [Ni12(CO)21 ]4- and [Ni6Rh3 (CO)17 ]3- clusters[J]. lnorganica Chimica Acta, 2002,53:111 - 117.
  • 10Akio Yamamoto. A reminiscence and a future prospect of transition metal-catalyzed cross-coupling processes [ J ]. Journal of Organometallic Chemistry, 2002,6(53) :5 - 10.

共引文献3

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部