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1 1 2 3 4 1 5 6 <br /> OPTION 1 - 25OTPH <br /> Stream No. <br /> (PFD) 10-547-01 10447-02 10847-02-011G847-02-01 10647-04 1D-047-04 10-647-06 IG447-06 10b17-08 104547-02-01 10847-02-01 10-647-02-01 10-647-02 1041474F2 WA <br /> Description <br /> Concerumte Concentrate ROpgller Con Rolgllar Con <br /> Cyckwas Rougher Ch"' Cleaner Concentrate CIP Flker Rougher Con Cleaner Cbanx Flotation <br /> Osaka, T�. Column Con Column Tails Thickener Cake Fikrete Dilution Scanerger Tails St a ranger Con Concentrate Cells 182 Cells 3,485 FNrccr4wlt <br /> Strewn OFlow l7Flow <br /> Properties <br /> Solds tlawrate stph 250.OD 242.90 2.20 11.50 1 7.10 7.10 13.20 1 4.80 1 7.10 13.70 6.60 A <br /> A ..an fowrate st 548.20 628.30 S.OD 119.40 18.10 5.80 1.10 4.70 45.30 16, =3.20 <br /> 17 30 92.80 4d.60 0.13 !1 <br /> Total at- st h 796.20 871.20 7.20 130.80 18.10 12.90 8.10 4.70 45.30 160,60 24.40 10650 51.10 0.13 <br /> Total stream fowrate gpm 2573.30 2856.60 21.80 494.70 84.30 31.20 1220 19.00 181.30 689.70 77.10 390.10 187.40 0.50 <br /> %Solids % 31.30 27.90 31.00 8.80 55.OD 87.00 7.30 29.10 12go 12.90 0.25 <br /> Stream SG 120 1.20 1.30 1.10 1.00 1.70 270 1.00 1,00 1.00 1.30 1.10 1.10 1.00 <br /> Solids SG 260 2.80 1.80 2.70 3.50 3.50 2.60 3.50 2.90 2.80 <br /> OPTION 1 - 275TPH <br /> sream No. 'CJ <br /> (PFD) 10847-01 ,04)47-02 704347-02-01104)47-02-01 16647-04 tOW7-04 1PS47-06 10647-06 16647-08 10E4T-02-01 10fi47-02-01 10d47-02-01rR -n <br /> tOS47471 WA <br /> Description <br /> Concentrate Concentrate <br /> Cyclone Rougher Cleaner Cleaner Concentrate CIP Filter Rougher Con Geana Cleaner Flotation Rougher Con FkwcWant <br /> s€ Thickener Thireckener <br /> 3 Stream Oked w Tells Column Can Column Tells Cake Flttrate Dilution Scalerger Tails Soae W Con Concentrate Cells 3,485 <br /> C Floal U'FI- <br /> Sollos fo4.ate stph 275.00 287.20 2.50 12.80 7.80 7.80 0.00 14.50 5.30 7.80 7.20 <br /> * Solution tlowrate stph 803.00 891.10 =31.408.80 <br /> 17.50 6.40 1.20 5.20 49.80 184.10 13.40 18.00 102.00 49.00 0.13 <br /> a Total at- a 876.OD 858.30 17.50 14.20 9.01) 5.20 49.80 198.80 18.70 ZB.BD 117.10 56.30 U.13 <br /> Tdel stream to". gpm 28NO 317,4100 70.00 34.30 13.40 20.90 199.40 758.80 60.40 84ti) 429.10 206.10 0.50 <br /> a %Solid. % 31.30 27.90 55.00 87.00 7.30 28.40 2g.30 12.90 12.90Stream SG 1.20 1,20 100 1.70 2.70 1.00 1.0( 1.00 120 1.30 1.10 1.10Solids SG 2.80 2.80 3.50 1 3.50 2.60 3.20 3.50 2.90 1 2.90 <br /> B B <br /> OPTION 2 - 275TPH <br /> E ®Q Steam No. <br /> Y (PFD) 10647-01 10647-02 tG847-02-0110$47-02-01 10517-04 10847-04 106Q-08 1G&t7-08 10847� 10647-02-01 1G6/7-02-01 10847-02-0/ 10847Q! 10647-02 WA <br /> Descrip0on <br /> 9s <br /> 55€55€ Concentrate Concentrate <br /> 'S Cycbro Rougher Cleaner Cloonan Concentrate CIP Fitter Rougher Con Clsaw Cloonan Flotation Rougher Con Rougher Con <br /> Thickener Thinckener Flocculent <br /> Stream mow' Tars Column Con Column Tait OFlow U'Flow Cake Fikrele Dilutor ficelanpM Tait Seaeertper Can Concentrate Cells/82 Calls 3,485 <br /> $ Propeellos <br /> Solids llowrate Mph 275.00 266.40 3.60 18.w 8.80 8.80 13.60 5.00 8.60 22.30 <br /> Solution fowr4ta atph 603.00 689.40 7.50 193.80 18,70 7.10 1.30 5.80 49.50 182.10 12.60 20AO 150.70 0.13 <br /> € Total is s 878.00 95 M. 11.10 21210 18.70 ,5.70 9.90 5.80 49.50 195.80 1T.80 28.80 173.00 0.13 <br /> Total stream fowrate 2830.70 3188.30 33.10 803.10 71.80 38.30 15.20 23.10 t86.10 749.80 57.50 90.50 834.00 0.50 <br /> %Solids % 31.30 27.90 32.80 8.80 55.00 57.00 7.00 211 30.00 12.90 0.25 <br /> Stream SG ,.20 1.20 1.30 1.10 1.00 1.60 2.GO <br /> 1.00 1.00 1.00 1.20 1.30 1.10 1.00 <br /> Solids SG 2.W 2.60 4.70 2.70 3.10 3.40 2.80 2.90 3.40 290 <br /> 1 <br /> E OPTION 3(BYPASS) 275TPH <br /> �$y C <br /> Stream No. <br /> x § (PFD) 10617-01 10-647-02 1D647-04 10847-04 10464746 10647-M 10-647-02-01 WA <br /> � t®8 Description <br /> x3 <br /> ggg Concentrate Concentrate <br /> Cyclone Rougher Concentrate C5'F)ker, Rotation <br /> Tails Cake <br /> Thick-Thick- Thinckerer ClikeFiltrate Concentrate Flocculent <br /> Strewn v <br /> ¢¢ OFlow l7Flow <br /> F Properties <br /> Solids lowrate stph 275.00 253.80 21.20 21.20 21.20 <br /> Solution Acetate stptr BIXi.OD 611.80 136.40 17.30 4.70 ,2.70 141.20 1 D.40 <br /> R Total atream loweste gpm 2832.30 2436.80 545.90 99.80 4g�0 50.80 505.50 11.60 <br /> L %Sdmc % 3,.30 33.,0 55.00 82.00 13.10 0.30 REVISION <br /> Strom SG 120 1.3o t.oG 1.50 2.10 1.00 1.10 1.W PLEASE DESTROY <br /> Solid.6G 2.80 z.eo z.eo 2.80 2.80 ALL PREVIOUS COPIES <br /> 09/01/2017 <br /> REVISIONS REFERENCE DRAWINGS ISSUE RECORD ENGR RECORD D <br /> ing <br /> No DEscPopraN DATE 8Y cHK AM DwIwN1G NO TITLE DATE ISS REV TO MR BY DATE SE We Provide Solutions EngineerSolutions <br /> Dew PLCM 11 18 2011 8450 E.Crescent Parkway.Suit.200 Phone:303.714 4840 <br /> 0 0 ISSUED FOR DESIGN 09/01/2017 JRJ KA 10-647-01 7HRU 10-647-12 PROCESS FLOW Ol4GRAMS omo-D w m/iyuv Greenwood Village,CO 80111 Fax 303,714.4800 <br /> n 1 ISSUED FOR DESIGN 10/12/2D17 JP KA aom sk-We tl C IC CRIPPLE CREEK&VICTOR TITLE <br /> GOLD MINING COMPANY HIGH GRADE MILL <br /> CIP AND AGGLOMERATION AREA <br /> go AT V HIGH GRADE MILL CLEANER CIRCUIT AND CONCENTRATE LOADOUT <br /> MATERIAL BALANCE SHEET <br /> n FOR CC&V VICTOJRE- <br /> NONECo. <br /> o Y wrz DWG SIZE SCALE JOB NO DRAWING NO D 17168 10-647-24 <br /> aua <br /> CE22x34 Continued from project(s): <br />