The use of sodium formate for the recovery of precious metals from acidic base metal effluents

被引:8
作者
Julsing, HG [1 ]
McCrindle, RI [1 ]
机构
[1] Technikon Pretoria, Dept Chem & Phys, ZA-0001 Pretoria, South Africa
关键词
platinum group metals; reduction; sodium formate;
D O I
10.1002/jctb.385
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
Zinc was used for the reduction of the platinum group metals (PGMs) in acidic effluents. Due to the increasing cost of zinc, sodium formate was investigated as an alternative reductant. In a base metal-containing acidic effluent, called diethylenetriamine barren, sodium formate was used to precipitate the PGMs. This effluent was the filtrate obtained after a precipitation procedure had been used to remove rhodium and iridium. It was found that pH 1.5 was the optimum starting pH for sodium formate reduction. The pH increased to approximately 4.5 after the addition of sodium formate. The optimum concentration of sodium formate was found to be 30g dm(-3) at a temperature of 100 degreesC where the process time was 6h. Platinum and palladium were the most effectively reduced PGMs, both exhibiting an average precipitation efficiency of greater than 99%. Difficulty was experienced with the precipitation of iridium (average precipitation efficiency of 76%). The precipitated PGMs readily dissolved in hydrochloric acid (6M) and sodium chlorate (2%). A reduction in costs resulted from the discontinuation of the use of zinc for reduction purposes. An additional advantage was that zinc was no longer introduced into the PGM refinery circuits. (C) 2001 Society of Chemical Industry
引用
收藏
页码:349 / 354
页数:6
相关论文
共 17 条
[1]  
ADAMS RW, 1986, MINING CHEM HDB, P118
[2]  
[Anonymous], 1972, BRIT POLYM J, DOI [10.1002/pi.4980040307, DOI 10.1002/PI.4980040307]
[3]  
DICINOSKI GM, 1994, RESINS SELECTIVE GOL, P73
[4]  
GRASSO JR, 1981, S REC RECL PREC MET, V13, P8
[5]  
HARRIS GB, 1993, 4 INT S HYDR, P795
[6]  
HASENPUSCH W, 1987, CHEM FUER LABOR BETR, V38, P459
[7]  
HAUNG HH, 1989, CAN METALL QUART, V28, P225
[8]  
HOKE CM, 1982, REFINING PRECIOUS ME, P92
[9]  
Julsing HG, 2000, S AFR J CHEM-S-AFR T, V53, P86
[10]  
JULSING HG, 1997, THESIS MAGISTER TECH, P99