| Summary and Recommendation | WNP Processing Plant Air Discharge Assessment | 4397169-66885702-113 | 16/06/2022 | 25 Sensitivity: General ore. Following crushing through a jaw crusher (3), the ore is fed into the semi autogenous grinding (SAG) mill along with water and steel balls. The grinding process reduces the rock to a slurry. The SAG mill is a large revolving cylinder. Rock is ground by the turning action of the mill, and impact from the hardened steel balls and the rock itself. In order to ensure that the rock is ground finely enough the SAG mill has a trommel screen (5), which acts like a large sieve. The oversize rock (SCATS) is caught by the trommel, along with the worn hardened steel balls. This material is fed past a magnet (12) to separate out the steel balls. The oversize rock passes through the SCATS cone crusher (13), prior to passing once again into the SAG mill (4) for further grinding. The slurry that is fine enough passes through the trommel to a sump and then to a primary hydrocyclone. This hydrocyclone classifies the ground rock particles according to size – using centrifugal and gravitational forces to split the fine particles from the coarse particles. The fine particles are pumped via a sump (8) to a secondary hydrocyclone, and the larger particles return to the SAG mill for further grinding. The secondary hydrocyclone further classifies the slurry, with the coarse particles being directed to the ball mill and fine particles reporting to the trash screen. The ball mill is very similar to the SAG mill, except it has a larger proportion of steel balls to assist in the grinding process. Following grinding in the ball mill, the material is returned via the sump to the secondary hydrocyclone for resizing. The trash screen removes wood from the old mine workings that may have found its way into the processing circuit. The slurry that remains after this process has a very fine particle size. Typically, 80% of the ore particles are less than 70 microns in size (about the same consistency as fine beach sand). Such a fine particle size is required for gold liberation – the size required for the cyanide to be able to ‘see’ the gold in the leaching process. The remaining slurry passes through a pre-leach thickener to remove some of the water. The recovered water is reused in the grinding circuit while the thickened slurry moves into the leaching circuit. Leaching and adsorption The slurry of ground ore and lime moves into a series of six leach tanks where a sodium cyanide solution is added. The tanks provide sufficient retention time to allow the gold and silver to be dissolved by the cyanide solution. Oxygen is added to assist in this process. The slurry then moves through a series of carbon adsorption tanks. While the leaching process continues in these tanks, the primary objective is to remove the gold and silver from the solution. To achieve this, carbon granules are fed through the tanks and the gold and silver adsorbs (attaches) to the granules. Carbon is heated to 600 degrees C and fed into the circuit in the opposite direction to the slurry flow, moving from the last adsorption tank to the first. This is because the gold and silver move towards the carbon via a diffusive process. It is necessary to have ‘fresh’ carbon at the end of the chain, to scalp the gold and silver that has not been removed in the previous tanks. By the time the slurry reaches the final adsorption tank, most of the precious metals have been removed. The barren slurry, now known as tailings, is pumped to the tailings storage facility. In contrast, by the time the carbon reaches the first adsorption tank it has recovered most of the gold and silver from solution. This ‘loaded’ carbon is then screened out and pumped to the elution circuit where the gold and silver is washed off with superheated water. The washed solution, called pregnant eluate, is passed to the electrowinning circuit. The remaining barren carbon is reactivated by acid washing and kilning and returned to the adsorption tanks.
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