Abstract

Thiosulfate leaching is a promising alternative to cyanidation, and the main hindrances for its wide commercial application are the high thiosulfate consumption and the difficult recovery of dissolved gold. In this review, the four solutions to reduce the consumption of thiosulfate, including the control of reaction conditions, the use of additives, the generation of thiosulfate in situ, and the replacement of traditional cupric-ammonia catalysis, are introduced and evaluated after the presentation of background knowledge about thiosulfate consumption. The replacement of cupric-ammonia catalysis with other metals, such as nickel- and cobalt-based catalysts, is proposed. The reason is that it not only reduces thiosulfate consumption observably via decreasing the redox potential of leach solution significantly but also is beneficial to gold recovery mainly owing to eliminating the interference of cuprous thiosulfate [Cu(S2O3)3]5−. Based on the comparative analysis for five common recovery techniques of rare-noble metals from pregnant leach solution, ion-exchange resin adsorption is considered to be the most appropriate to recover aurothiosulfate [Au(S2O3)2]3− because the resin can be employed in the form of resin-in-leach/pulp and, furthermore, is able to be eluted and regenerated simultaneously at ambient temperature. At last, how to reduce the process cost of the resin adsorption technique is discussed. In order to simplify the complex two-stage elution process for loaded resins, the traditional catalysis is suggested to be replaced.

Highlights

  • Cyanidation has been the predominant gold leaching technique since it was first put forward byJohn Stewart MacArthur in the 1880s [1] because of its simple process and low cost

  • According to the literature [18,23], the thiosulfate consumptions in different studies are usually over 25 kg/t-ore during leaching and the dissolved gold cannot be effectively recovered by the simple techniques of active carbon adsorption and cementation that is used widely in cyanidation, both of which make the commercial competitiveness of thiosulfate leaching weak

  • The influence of cations, including calcium, sodium, and ammonium, on the leaching of a pyrite concentrate has been studied by Feng and Van Deventer [49], and the results showed that calcium thiosulfate and sodium thiosulfate have the best effect on gold leaching and thiosulfate consumption, respectively

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Summary

Introduction

Cyanidation has been the predominant gold leaching technique since it was first put forward by. The carbonaceous gold ore in Goldstrike deposit cannot be efficiently leached by cyanidation due to the “preg-robbing” phenomenon, this phenomenon does not occur during thiosulfate leaching owing to the very weak affinity of carbonaceous substance for gold thiosulfate complex [24] This leads to the problem that the dissolved gold in thiosulfate solution cannot be effectively recovered by active carbon adsorption which is the dominant technique used for pregnant cyanide solution. According to the literature [18,23], the thiosulfate consumptions in different studies are usually over 25 kg/t-ore during leaching and the dissolved gold cannot be effectively recovered by the simple techniques of active carbon adsorption and cementation that is used widely in cyanidation, both of which make the commercial competitiveness of thiosulfate leaching weak. The main intentions of this review are to propose an optimal approach for the reduction of thiosulfate consumption and a commercially-viable technique to recover dissolved gold from pregnant thiosulfate solution

Background
Electrochemical-Catalytic Mechanism of Thiosulfate Leaching
Route of Thiosulfate Decomposition
Effect of Associated Minerals
The Control of Reaction Conditions
Inorganic Additives
Organic Macromolecular Additives
The Generation of Thiosulfate In Situ
The Replacement of Traditional Cupric-Ammonia Catalysis
Gold Recovery from Pregnant Thiosulfate Leach Solution
Resin Adsorption
Findings
Conclusions
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