Diana: Can You See The Real Me? by Matthew Delooze

By Matthew Delooze

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Au Tenth Mill Operators’ Conference Preliminary engineering was undertaken in parallel with ongoing exploration drilling and project development and as such resulted in changes to the initial design plant throughput during 2006. This paper describes the process selection and engineering of a process plant with the emphasis on treating high sulfide silver ores by utilising direct electrowinning. Electrometals Technology Limited provided the direct electrowinning technology via the use of their EMEW powder cells.

These tests reduced the WAD cyanide level to 126 mg/L and as such did not achieve the target level of 50 mg/L. It was noted during the tests that the viscosity of the slurry increased dramatically during testing. It is believed that this had a significant impact on the effectiveness of the detoxification process. It was also felt that a lower slurry pH would aid the process. Subsequent to the first phase of testing, cyanide optimisation test work had been carried out on the flotation concentrate sample.

Min for the first six hours and then slowly reduces over the next 18 hours. min. A summary of results for the oxygen uptake test work is given in Table 8. Merrill Crowe test work was performed on high-grade flotation concentrate leach liquors as an alternative process route to direct electrowinning. The test work indicated high silver and gold precipitation rates from the solution, although some minor redissolution was seen over one hour. 15:1. Final tailings samples following cyanide detoxification were sent to the consulting geotechnical laboratories for testing.

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