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Stream Niunhcr <br />NIa,s I kw SoliLI,. stph <br />310 <br />312 <br />314 <br />315 <br />316 <br />317 <br />318 <br />319 <br />320 <br />321 <br />322 <br />323 <br />324 <br />325 <br />333 <br />334 <br />335 <br />336 <br />337 <br />340 <br />341 <br />342 <br />343 <br />1.0 <br />1.5 <br />0.34 <br />0.6 <br />0.04 <br />(16 <br />0.031 <br />0.6 <br />0.41 <br />0 3 <br />1.27 <br />0.2 <br />0.04 <br />1.33 <br />1).0) <br />0 3 <br />0.2 <br />Ma„ 1 love 1 iywd, stph <br />6.1 <br />9.6 <br />2.11 <br />4 4 <br />0,26 <br />4.6 <br />0.24 <br />4.8 <br />2.61 <br />1.7 <br />5 11 <br />0 5 <br />1.25 <br />9.17 <br />0.4 <br />0 4 <br />0.4 <br />0.2 <br />0.0 <br />1) 0 <br />1 25 <br />0.6 <br />0 5 <br />\1a„ 1 I , 11Th <br />7 1 <br />11.2 <br />2.44 <br />5.1 <br />(1.30 <br />5 2 <br />0.'7 <br />5.4 <br />3.1)2 <br />2.0 <br />9.39 <br />0.7 <br />1.29 <br />10.65 <br />(1.4 <br />0 4 <br />(1.4 <br />0.2 <br />0,1) <br />0.(1 <br />129 <br />0.i) <br />0.7 <br />", Solids <br />13.8 <br />13.8 <br />13.5 <br />12.6 <br />12.6 <br />11.6 <br />11.6 <br />10.6 <br />13.5 <br />13.5 <br />13.5 <br />31.0 <br />3.0 <br />12.4 <br />3.0 <br />3 I.O <br />31.0 <br />S(i Solid, <br />4 00 <br />4.0 <br />2,70 <br />4.01) <br />2.7(1 <br />4 (Al <br />2.71) <br />4 00 <br />2 70 <br />4,01) <br />4.()() <br />4 01) <br />4 00 <br />4.1) <br />4.00 <br />4 0(1 <br />4.0)) <br />S(i 1 k1uid <br />1.00 <br />1.0 <br />1.0(1 <br />1.(1(1 <br />1.00 <br />1.00 <br />1.0(1 <br />1.011 <br />1.00 <br />1.011 <br />1 00 <br />1.00 <br />1.00 <br />1.0 <br />1,01) <br />1 -(1(1 <br />1,00 <br />1.011 <br />1.00 <br />1 00 <br />1.110 <br />1.00 <br />1.00 <br />S(i Foul <br />1.12 <br />1.1 <br />1.09 <br />1.10 <br />1.09 <br />1.10 <br />1.08 <br />1.09 <br />1.09 <br />1.12 <br />1.11 <br />1.30 <br />1.02 <br />1.1 <br />1.00 <br />1.00 <br />1.00 <br />1.00 <br />1.00 <br />1,00 <br />1.02 <br />1.30 <br />31.0 <br />} loTti{T <br />. ' m <br />25 <br />411. {) <br />9 <br />IN <br />1 <br />19 <br />1 <br />21 <br />11 <br />7 <br />34 <br />5 <br />78.7 <br />2 <br />1 <br />O <br />0 <br />5 <br />3 <br />2 <br />D <br />C <br />B <br />A <br />REV <br />PROCESS WATER <br />800 -D -811 <br />Zn CLEANER FLOTATION <br />FEED PUMP <br />300 -D -8038 <br />Pb CLEANER FLOTATION <br />FEED PUMP <br />11/12/12 <br />10/17/12 <br />09/18/12 <br />08/17/12 <br />DATE <br />> <br />J <br />300- 0-803A > <br />HECE fli � <br />NOV 292012 <br />DURANGO FIELD OFFICE <br />DIVISION OF RECLAMATION, <br />MINING AND SAFETY <br />J <br />ISSUED FOR DESIGN <br />GENERAL REVISIONS <br />ISSUED FOR CLIENT APPROVAL <br />ISSUED FOR REVIEW AND COMMENT <br />DESCRIPTION <br />300 - FCC -03NB <br />Pb CLEANER FLOTATION <br />CELLS - BANK 1 <br />zz <br />Z2 <br />ZZ <br />ZZ <br />CHKD <br />RE <br />RE <br />RE <br />RE <br />DRWN <br />APVD <br /><315> <br />300- FCC -04NB <br />Pb CLEANER FLOTATION <br />CELLS - BANK 2 <br />< 3 > <br />❑ <br />- 7 <br />I <br /><317> <br />300 - FCC -05NB <br />Pb CLEANER FLOTATION <br />CELLS - BANK <br />300 - PPB -06 <br />Pb CLEANER <br />CONCENTRATE <br />PUMP <br />318 <br />STAR MINE <br />OPERATIONS <br />300- PPB -07 <br />Pb CLEANER <br />TAILS PUMP <br />300- FCC -06A/8 <br />Zn CLEANER FLOTATION <br />CELLS - BANK <br />CH2MH I LL® <br />300 - FCC -07A/8 <br />Zn CLEANER FLOTATION <br />CELLS - BANK 2 <br />336 <br />300- PPB-08 <br />Zn CLEANER <br />CONCENTRATE <br />PUMP <br />SHEET TITLE <br />300 TPD CONCENTRATOR <br />PROCESS FLOW DIAGRAM <br />CLEANER FLOTATION <br />300- PPB -09 <br />Zn CLEANER <br />TAILS PUMP <br />EQUIP NO <br />300- FCC -03A /B <br />300- FCC -04A /B <br />300-FCC-OS/VS <br />300 - FCC -06A /B <br />300-FCC-OMB <br />300- FCC -08A /B <br />300 - PPB -06 <br />300 -PPB -07 <br />300 - PPB -08 <br />300 -PPB -09 <br />323 <br /><319) <br />PROJECT TITLE <br />REVENUE VIRGINIUS MINE <br />OURAY, COLORADO <br />SILVER STAR RESOURCES, LLC. <br />DENVER, COLORADO <br />NAME <br />Pb CLEANER FLOTATION CELLS <br />- BANK 1 <br />Pb CLEANER FLOTATION CELLS <br />- BANK 2 <br />Pb CLEANER FLOTATION CELLS <br />- BANK 3 <br />Zn CLEANER FLOTATION CELLS <br />- BANK 1 <br />Zn CLEANER FLOTATION CELLS 5 <br />- BANK 2 <br />Zn CLEANER FLOTATION CELLS 0 <br />-BANKS <br />Pb CLEANER CONCENTRATE <br />PUMP <br />Pb CLEANER TAILS PUMP <br />Zn CLEANER CONCENTRATE <br />PUMP <br />Zn CLEANER TAILS PUMP <br />LEGEND <br />Zn CONDITIONING TANK <br />300.0 -8038 > <br />Zn CONCENTRATE <br />FILTER FEED TANK <br />400 - 0 - 806 > <br />Pb CONDITIONING TANK <br />300- D -803A <br />Pb CONCENTRATE <br />FILTER FEED TANK <br />300 - 0 - 806 <br />STREAM NUMBER <br />EXISTING EQUIPMENT <br />MAJOR PROCESS FLOW <br />HP <br />30 <br />30 <br />30 <br />30 <br />10 <br />SCALE NONE <br />DRAWN R ELSTUN <br />DATE 08/07/12 <br />PRJ MGR W WRIGHT <br />PRJ NUM 437502 <br />DWG NUM 300 -0-804 <br />SHEET IREV D <br />B <br />C <br />D <br />A <br />1 <br />2 <br />4 <br />5 <br />6 <br />2 = <br />UJ N 2 <br />U <br />>0 <br />CC <br />Z <br />NO <br />�F- <br />zR <br />w O_ <br />W <br />La <br />F-0 <br />. 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