Extraction and separation of gold (I) cyanide in polyethylene glycol-based aqueous biphasic systems

被引:49
作者
Zhang, TX
Li, WJ
Zhou, WJ
Gao, HC
Wu, JG [1 ]
Xu, GX
Chen, J
Liu, HZ
Chen, JY
机构
[1] Beijing Univ, Coll Chem & Mol Engn, State Key Lab Rare Earth Mat Chem & Applicat, Beijing 100871, Peoples R China
[2] Beijing Univ, Univ Hong Kong, Joint Lab Rare Earth Mat & Bioinorgan Chem, Beijing 100871, Peoples R China
[3] Inst Precious Met, Kunming 650221, Peoples R China
[4] Chinese Acad Sci, Inst Chem Met, Beijing 100080, Peoples R China
基金
中国国家自然科学基金;
关键词
extraction; gold (I) cyanide; aqueous biphasic system; polyethylene glycol; partition;
D O I
10.1016/S0304-386X(01)00179-7
中图分类号
TF [冶金工业];
学科分类号
0806 [冶金工程];
摘要
The extraction of gold (I) cyanide in polyethylene glycol-based aqueous biphasic systems has been investigated. Almost all of gold (I) cyanide (> 96%) was transferred from salt-rich phase into the polyethylene glycol (PEG)-rich phase without addition of any extractant. No significant influence of solution pH on gold (I) cyanide extraction was observed. The aqueous biphasic systems have high capability of extraction. The gold (I) cyanide in the PEG-rich phase can be easily reduced by addition of zinc. The PEG-rich phase could be reused for extraction of gold (I) cyanide without decrease of extraction capability. The PEG/salt aqueous biphasic systems may provide a potential new technique for gold separation from cyanide solutions because all components of systems are virtually nontoxic and nonflammable. (C) 2001 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:41 / 46
页数:6
相关论文
共 20 条
[1]
Affinity partitioning of metal ions in aqueous polyethylene glycol/salt two-phase systems with PEG-Modified chelators [J].
AguinagaDiaz, PA ;
Guzman, RZ .
SEPARATION SCIENCE AND TECHNOLOGY, 1996, 31 (10) :1483-1499
[2]
Albertsson P.A., 1986, PARTITION CELL PARTI
[3]
Solvent extraction of Au(CN)(2)(-) with mixtures of the amine Primene JMT and the phosphine oxide Cyanex 923 [J].
Alguacil, FJ ;
Caravaca, C ;
Mochon, J ;
Sastre, A .
HYDROMETALLURGY, 1997, 44 (03) :359-369
[4]
THE PHOSPHINE OXIDES CYANEX-923 AND CYANEX-925 AS EXTRACTANTS FOR GOLD(I) CYANIDE AQUEOUS-SOLUTIONS [J].
ALGUACIL, FJ ;
CARAVACA, C ;
MARTINEZ, S ;
COBO, A .
HYDROMETALLURGY, 1994, 36 (03) :369-383
[5]
Synergistic extraction of gold(I) cyanide with the primary amine Primene JMT and the phosphine oxide Cyanex 921 [J].
Alguacil, FJ ;
Caravaca, C .
HYDROMETALLURGY, 1996, 42 (02) :197-208
[6]
FISCHER D, 1994, GMELIN HDB INORGANIC, V62, P290
[7]
FTIR and EXAFS investigations of microstructures of gold solvent extraction:: hydrogen bonding between modifier and Au(CN)2- [J].
Ma, G ;
Yan, WF ;
Hu, TD ;
Chen, J ;
Yan, CH ;
Gao, HC ;
Wu, JG ;
Xu, GX .
PHYSICAL CHEMISTRY CHEMICAL PHYSICS, 1999, 1 (22) :5215-5221
[8]
2-PHASE AQUEOUS SYSTEMS BASED ON POLY(ETHYLENE GLYCOL) FOR EXTRACTION SEPARATION OF ACTINIDES IN VARIOUS MEDIA [J].
MOLOCHNIKOVA, NP ;
SHKINEV, VM ;
MYASOEDOV, BF .
SOLVENT EXTRACTION AND ION EXCHANGE, 1992, 10 (04) :697-712
[9]
THE CHEMISTRY OF GOLD SOLVENT-EXTRACTION FROM ALKALINE CYANIDE SOLUTION BY SOLVATING EXTRACTANTS [J].
MOOIMAN, MB ;
MILLER, JD .
HYDROMETALLURGY, 1991, 27 (01) :29-46
[10]
MOOIMAN MB, 1983, P INT SOLV EXTR C IS, P530