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Reagents <br />Lime <br />PAX <br />Water <br />Rate <br />Ore feed <br />Amount used (2) <br />Amount used (3) <br />12.51b /ton (1) <br />56,000 tons /yr <br />350 tons /yr <br />- <br />1.91b /ton <br />56,000 tons /yr <br />5.4 tons /yr <br />- <br />0.8st H <br />56,000 tons /yr <br />45,700st/y <br />Future Crushing Circuit <br />The planned additional crushing facility and storage silo, allows RoM ( -6 ") to be dumped <br />directly from the OTR trucks into a 1000 ton capacity coarse ore bin prior to feeding the crusher <br />circuit. Utilizing a similar grizzly, screening, primary and secondary crusher system, the <br />material flow will be in the range of 50% screened and sent to the silo and 50% sent to the <br />primary and secondary crushers, recombined with the screened material and sent to the silo. The <br />storage silo feeds an enclosed overhead belt, conveying the crushed material directly to the <br />grinding/flotation building fine ore bin, by- passing the existing crushing facility. <br />The future crushing circuit also has a truck scale, which allows the mill facility in -house <br />weighing capability. <br />Grinding Circuit <br />Material from the fine ore bin is transported to the grinding circuit via a belt feeder. Lime, <br />Ca(OH)2, is also added to this stream to bring the pH level to 10, as needed, to increase metal <br />recovery. This is a wet grinding circuit. This grinding circuit is comprised of one, 5 ft diameter <br />x 4 ft long Marcy ball mill. The ball mill, as it is configured at present, has a 40 hp motor. This <br />mill is capable of processing a maximum of 8 ton/hr. <br />The grinding system operates in closed circuit with a classifier to produce a final flotation feed. <br />The oversize reports back to the ball mill with a 180% circulating load for 8 tons/hr feed. The <br />underflow will be fed to the rougher flotation circuit. <br />Water is added at the ball mill discharge trough. Reagents are added at the ball mill and the <br />conditioning tank through reagent feeders. As shown in Table C -1, lime is added at the grinding <br />mill to control pH. Potassium amyl xanthate (PAX) is added as a promoter at the grinding mill <br />for increased reagent reaction time. The lime is added through a dry reagent feeder and the PAX <br />is a 1% solution, mixed on site from pellets. <br />Reagent usage added at the grinding circuit is presented in Table C -1. Emissions are generated <br />when the dry chemicals are added to the reagent mixers. Negative pressure ventilation collects <br />fugitive pm emissions from the reagent mixing area. The same dust collector in the crushing and <br />conveying circuit captures the emissions. <br />Table C -1: Chemical Usage, Ball Mill (56,000 ton /yr <br />"' Reagent rate based on dry ore feed tonnage <br />(2) Dry US tons of reagents — annual quantity <br />(3) Liquid US tons of reagents — annual quantity <br />Flotation Circuit <br />The comminution product reports to the rougher floatation circuit where it is mixed with water to <br />achieve a density of 35% solids by weight, which is carried through to the scavenger and cleaner <br />circuits. The rougher flotation cell bank consists of six, 25" x24" x29" (60.4ft tank cells. Tails <br />from rougher flotation will report to the scavenger flotation circuit which consists of six, 25" <br />x24" x29" (60.4ft tank cells. Tails from the scavenger flotation circuit report to the tails <br />thickener. <br />M1990 -057 September 27, 2011 <br />