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Feasibility Study and Technical Report - Pretivm

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Table 13.34MaterialFlotationConcentrateFlotationTailingsFlotationTailingsRecommended Thickening Design ParameterspHFlocculantDose(g/t)ThickenerFeedSolids(%)UnderflowDensity(%)Unit Area forConventionalThickenerSizing(m 2 /t/d)10.78 35 to 45 20 68 to 72 0.190 to0.22510.38 35 to 45 10 61 to 65 0.430 to0.4758.34 90 to 100 10 61 to 65 0.430 to0.475HydraulicRate forHigh RateThickenerSizing(m 3 /m 2 /h)Thickener TypeRecommended5.2 to 6.0 High-Rate orHigh Density5.0 to 5.9 High-Rate orHigh Density4.2 to 5.0 High-Rate orHigh DensityThe production rates indicates that vacuum filtration would likely be an uneconomicaloption for concentrate <strong>and</strong> tailings dewatering. A horizontal recess plate filter isrecommended; the plate filter cake moisture content (Table 13.35) may be decreased bychoosing a membrane-type filter press to get a high-pressure cake.Table 13.35Filtration Test Results <strong>and</strong> Sizing SummaryFilterTypeMaterialFilter FeedSolids(%)Bulk CakeDensity(kg/m 3 )Filter SizingBasis(m 3 /t)Filter CakeMoisture(%)Filter CycleTime (min)HorizontalRecessPlateFlotationConcentrate *FlotationTailings68.3 2155.9 0.580 12.6 18.158.0 824.7 1.516 17.6 19.4FilterTypeMaterialFilter FeedSolids(%)Bulk CakeDensity(kg/m 3 )FilterProduction Rate(kg/m 2 /h)Filter CakeMoisture(%)FilterAid (g/t)HorizontalBeltVacuumNote:FlotationConcentrateFlotationConcentrateFlotationTailingsFlotationTailings*With blowing <strong>and</strong> membrane squeezing.59.5 1723.3 116.8 29.3 200 (HychemAF304)2047.8 49.7 24.0 None59.0 1460.0 546.2 29.8 320 (HychemAF340)1757.9 124.0 24.4 NonePretium Resources Inc. 13-52 1291990200-REP-R0012-02<strong>Feasibility</strong> <strong>Study</strong> <strong>and</strong> <strong>Technical</strong> <strong>Report</strong> on the BrucejackProject, Stewart, BC

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