Cyanidation of mercury-rich tailings in artisanal and small-scale gold mining: identifying strategies to manage environmental risks in Southern Ecuador
Section snippets
Introduction and background
Mecury amalgamation is carried out by 15 million artisanal and small-scale gold miners (ASGM) in more than 70 countries. This gold recovery method, however, has serious environmental and health consequences for miners, associated populations, and the global community (Veiga and Hinton, 2002, Sousa and Veiga, 2009). Annually, approximately estimated 1000 tonnes of mercury is released into the environment by ASGM due to poor mining practices (Swain et al., 2007).
In Ecuador, ASGM has been the main
The cyanidation process
Generally speaking, Chilean-mill Centers also have cyanidation facilities. However, in Portovelo, there are facilities present that consist of only leaching tanks for the processing of tailings, ores or gravity concentrates. In fact, there are approximately 375 cyanidation tanks in Portovelo, their capacity ranging from 14 to 40 m3 and which employ two types of cyanidation circuits: 1) Merrill-Crowe process (representing ∼40%); and 2) Carbon-in-Pulp (CIP) process (representing ∼60%). Many
Methodology
With the participation of local miners and owners of processing plants, this study was conducted in the Portovelo-Zaruma region and is based on field observations, and analysis of mercury in solid and liquid samples. While assessing mercury, informal consultations were used to characterize the cyanidation process and to explore the miners’ perceptions about mercury use and its loss. The participation of the miners was important for planning, communicating, and identifying the weaknesses and
Results
The technical characteristics of the Merrill-Crowe and the CIP processing systems are depicted in Table 1. In the Merrill-Crowe process, about 6000–7000 kg of tailings with grain size below 0.2 mm are added to cement agitated tanks of 14 m3. The amount of water added ranges from 8000 to 11,000 L. Overall, the pH values in the agitated tanks in Portovelo at the beginning of the cyanidation process were highly alkaline, with an average of 11.2 ± 0.5. At the end of the process, the pH was slightly
Mercury in Merrill-Crowe and CIP process
Miners have developed devices to trap mercury before administering tailings into cyanidation circuits. For instance, in the CIP process, they wash tailings with water in a small tank before introducing the material into the leaching tank. Miners believe they remove half of mercury from the pulp by this way, but in fact less than 3% of mercury is trapped at the bottom of this tank. In the Merril-Crowe process, the amount of mercury that is trapped in the tank and can be eventually recovered
Conclusions
Since all amalgamated tailings contain residual gold, the owners of the processing centers and the miners in Southern Ecuador leach the remaining gold using cyanide through either the Merrill-Crowe or the CIP system. This study has investigated the behaviour of mercury in these two circuits in ASGM operations. Findings indicate that an estimated 50% of the mercury entering the cyanidation tanks is dissolved forming cyanide–mercury complexes in both the Merril-Crowe and CIP processes. An
Acknowledgements
The authors would like to thank to APROPLASMIN (Asociacion de propietarios de plantas de beneficio mineral), in particular to owners and workers who participated and contributed with this study. This research was supported by the Canadian International Development Agency (CIDA) through the project “Sustainable management of environmental health risks in Ecuador”, and the Global Mercury project funded by United Nations Industrial Development Organization.
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