The effect of solution parameters on the thiosulfate leaching of Zarshouran refractory gold ore

2014 ◽  
Vol 131 ◽  
pp. 43-50 ◽  
Author(s):  
M. Aazami ◽  
G.T. Lapidus ◽  
Amir Azadeh
Minerals ◽  
2021 ◽  
Vol 11 (9) ◽  
pp. 1021
Author(s):  
Sugyeong Lee ◽  
Charlotte E. Gibson ◽  
Ahmad Ghahreman

The use of alkaline pressure oxidation to pretreat refractory gold ore often results in insufficient gold recovery (<60%) in downstream thiosulfate leaching. To improve gold recovery, flotation was considered for the separation of carbonaceous matter (C-matter). In this study, the effect of MIBC on C-matter flotation was investigated to understand the role of the frother in bubble and froth formation and on flotation kinetics. MIBC dosages between 30 and 150 g/t were used in combination with 500 g/t of kerosene as a collector. The results showed that the recovery and selectivity of C-matter were improved with increasing MIBC dosages. Improved selectivity at higher MIBC dosages was attributed to faster C-matter recovery as bubble size decreased to the critical coalescence concentration (CCC) and to changes to the foam structure. Analysis of flotation kinetics showed that the flotation rate increased as the MIBC dosage increased due to the decreasing bubble size and the reduced induction time caused by the interaction between the collector and the frother. The results of this study explain the role of MIBC in C-matter flotation and can be used as a design basis for scavenger-cleaner flotation testing. Overall, the results show the potential for flotation as a means to improve gold recovery in thiosulfate leaching through the removal of C-matter.


2012 ◽  
Vol 548 ◽  
pp. 309-314
Author(s):  
Fu Ting Zi ◽  
Xian Zhi Hu ◽  
Wen Bin Zhang ◽  
Su Qiong He

In order to decrease the consumption of lixiviant, study on dissolution of pure gold and middle-refractory gold ore using a novel thiosulfate leaching system with ferricyanide as oxidant was carried out. The results showed that the advantage of the novel system is that the thiosulfate consumption is negligible though the potential of ferricyanide is much higher than that of traditional cupric ammine complex. And compared to the ferric oxalate system, novel system could be used at relatively high pH condition which benefit to the stability of thiosulfate because ferricyanide can’t transfer to iron hydroxide in base solution. It is unlikely that very high dissolution rate of gold can be obtained using an air saturated thiosulfate- ferricyanide system without thiourea catalyst. However gold dissolution rate was increased with the increasing of concentration of ferricyanid in 5 mmol/L to 30mmol/L. When 0.1mmol/L thiourea was presented, the dissolution of gold approximately 1.5 times faster than that of in the absence of thiourea. Leaching of middle-refractory gold ore show that both of the consumption of thiosulfate and leaching rate was decreased compare to the traditional copper–ammonia thiosulfate system. Thiourea is not stable in base solution, but it was found that gold dissolution rates can be increased with a little thiourea ,the mechanism is still unclear.


2021 ◽  
Vol 20 ◽  
pp. 100236
Author(s):  
Michail Samouhos ◽  
Antoniοs Peppas ◽  
Georgios Bartzas ◽  
Maria Taxiarchou ◽  
Petros E. Tsakiridis

2021 ◽  
Vol 164 ◽  
pp. 106822
Author(s):  
Hong Qin ◽  
Xueyi Guo ◽  
Qinghua Tian ◽  
Dawei Yu ◽  
Lei Zhang

1997 ◽  
Vol 10 (6) ◽  
pp. 577-583 ◽  
Author(s):  
Y. Wei ◽  
K. Zhong ◽  
E.V. Adamov ◽  
R.W. Smith
Keyword(s):  
Gold Ore ◽  

2017 ◽  
Vol 164 ◽  
pp. 6-10 ◽  
Author(s):  
Esmaeil Mohammadi ◽  
Mehdi Pourabdoli ◽  
Mehdi Ghobeiti-Hasab ◽  
Akbar Heidarpour

2019 ◽  
Vol 136 ◽  
pp. 89-98 ◽  
Author(s):  
Qiang Wang ◽  
Xianzhi Hu ◽  
Futing Zi ◽  
Xuecong Qin ◽  
Yanhe Nie ◽  
...  

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