A review of copper cyanide recovery technologies for the cyanidation of copper containing gold ores

2012 ◽  
Vol 25 (1) ◽  
pp. 1-13 ◽  
Author(s):  
Xianwen Dai ◽  
Andrew Simons ◽  
Paul Breuer
Keyword(s):  
2017 ◽  
Vol 262 ◽  
pp. 131-134
Author(s):  
Anna A. Faiberg ◽  
Aleksandra N. Mikhailova ◽  
Vladimir E. Dementiev ◽  
Sergey S. Gudkov

An optimal approach to the problem of cupriferous gold ores hydrometallurgical processing is the recycling of process solutions after copper recovery and regeneration of cyanide bound in complexes. The study focuses on the copper-cyanide solutions processing technology using biogenic hydrogen sulfide for copper recovery in the form of сhalcocite, and cyanide regeneration. The strains of anaerobic sulfidogenic thermophilic microorganisms Desulfurella acetivorans and Desulfurella Kamchatkensis were used for producing hydrogen sulfide. The studies on copper precipitation and cyanide regeneration were conducted on copper-cyanide process solutions which were obtained during cyanidation of refractory cupriferous gold-bearing flotation concentrates from one of the deposits in the South Ural (Russia). Ten cycles of "Cyanidation-Regeneration" were carried out in total. The copper recovery was 86–96 %; the cyanide regeneration obtained 96 %. On an average 8.9 kg of sodium cyanide and 4.6 kg of copper sulfide were recovered from 1 m3 of solution. The sodium cyanide consumption decreased from 25.0 kg/t to 6.0 kg/t without reducing gold recovery during the CIL (carbon-in-leach) recycling process. The gold recovery was the same 63–68 %.


1992 ◽  
Vol 26 (9-11) ◽  
pp. 2357-2360
Author(s):  
J. Zagorc-Koncan ◽  
M. Dular

A laboratory river model for the study of self-purification inhibition in a stream containing toxic substances is presented. It enables an engineering - technological prediction of the impact of toxic substances or wastewaters on dissolved oxygen (DO) profile in an organically polluted river downstream from the point of entry of toxic effluent thus providing rapidly and inexpensively significant design information to an environmental scientist or engineer. The method was applied to the toxicity evaluation of wastewaters from electroplating industry. The effects of copper, cyanide (representing two significant constituents of this type of wastewaters) and wastewater from electroplating industry on the biodegradation of organic municipal pollution in receiving stream were evaluated experimentally.


2019 ◽  
Vol 1347 ◽  
pp. 012127
Author(s):  
Guodong Chen ◽  
Hongying Yang ◽  
Huiqun Niu ◽  
Linlin Tong ◽  
Shuiping Zhong ◽  
...  
Keyword(s):  

2014 ◽  
Vol 88 (s2) ◽  
pp. 252-253 ◽  
Author(s):  
E.V. BELOGUB ◽  
E.E. PALENOVA ◽  
A.V. CHUGAEV ◽  
O.Yu. PLOTINSKAYA
Keyword(s):  

2021 ◽  
Vol 170 ◽  
pp. 106990
Author(s):  
Clement Owusu ◽  
Selorm Mensah ◽  
Kenneth Ackah ◽  
Richard K. Amankwah
Keyword(s):  

1991 ◽  
Vol 30 (12) ◽  
pp. 2586-2588 ◽  
Author(s):  
Urs. Geiser ◽  
Hau H. Wang ◽  
K. Douglas. Carlson ◽  
Jack M. Williams ◽  
Henry A. Charlier ◽  
...  

2013 ◽  
Vol 825 ◽  
pp. 352-355 ◽  
Author(s):  
Zeng Ling Wu ◽  
Zhong Sheng Huang ◽  
Ren Man Ruan ◽  
Shui Ping Zhong ◽  
Brenda K.C. Chan

Low-grade, finely disseminated refractory sulfide gold ores associated with high arsenic are ubiquitous resources all over the world. Since heap bio-oxidation is an economic and promising biotechnology to recover gold, low grade, high organic carbon and arsenic bearing gold ores from Zhesang Mines in China were chosen for this purpose to study the key factors that would affect biooxidation. Pyrite and arsenopyrite (particle size 0.002-0.22 mm) were the main minerals from Mineral Liberation Analysis (MLA). Column biooxidation and cyanidation of mineral size < 10 mm were evaluated for its potential for gold extraction. Results showed that temperature was the main factor influencing sulfide oxidation. 58-67 % of sulfide was oxidized at 35-45°C after > 240 days of biooxidation with mixed mesophiles, while higher sulfide-S dissolution (77%) was obtained at 60°C. Sulfide-S fraction distribution revealed higher mineral decomposition, finer fractions and eventually higher sulfide oxidation at 60°C. Jarosite and scorodite were found from the residues at 60°C by SEM and EDX, which implies higher temperature accelerated arsenic precipitation. No elemental sulfur was detected during the biooxidation at 35-60°C. After bio-oxidation, column cyanidation was successfully demonstrated recovery of gold from the residues, with gold extraction rate reaching 66%.


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