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2012-02-28_REVISION - M1980244 (77)
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2012-02-28_REVISION - M1980244 (77)
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Last modified
8/24/2016 4:49:12 PM
Creation date
3/15/2012 2:08:49 PM
Metadata
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Template:
DRMS Permit Index
Permit No
M1980244
IBM Index Class Name
REVISION
Doc Date
2/28/2012
Doc Name
VOL 6, Part 1: Design Summary & Drawings - Mill Facilities
From
CC&V
To
DRMS
Type & Sequence
AM10
Email Name
TC1
Media Type
D
Archive
No
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41 03SmIoTH <br />1 <br />from approximately 65 %. From the pH Adjustment Tank slurry will be directed by gravity to <br />the first of six leach tanks (approximately 173,000 gallons in size each) in a single train via a <br />distribution tank. Leach tanks outlets will be stepped for gravity flow at a rate of approximately <br />200 gallons per minute. Each tank will be fitted with an agitator to ensure the ore makes <br />contact with the lime and cyanide solution. Air will be introduced to each tank through top <br />entry sparging lines which discharge below the agitator blades. The discharge from the last <br />leach tank will flow into the CIP Circuit Feed Tank. The leach circuit discharge slurry will be <br />pumped to the CIP circuit at a rate of approximately 211 tons per hour. <br />2.6.CIP Circuit <br />Design Summary <br />Squaw Gulch High Grade Mill Facilities <br />2.7. Processed Ore Thickeners and Process Water Tanks <br />1/24/2012 <br />Page 4 of 6 <br />The CIP circuit consists of eight tanks (approximately 12,000 gallons in size each) where <br />activated carbon is introduced from the slurry from the Leach Circuit at 1.5 tons twice per day. <br />The activated carbon in the CIP tanks allow the adsorption of the gold in solution onto the <br />carbon particles. <br />Each of the five CIP tanks will be charged with activated carbon (approximately 1.5 tons in each <br />one), Each tank will be equipped with Pump Cells that allow the transfer of slurry from tank to <br />tank without transporting the activated carbon. The slurry moves through all of the tanks and is <br />transferred from the last tank to the CIP Processed Ore Sump. From the CIP Processed Ore <br />Sump, the slurry is pumped to the High pH Thickener for water recovery. <br />On a regular timed basis, the contents of each CIP tank containing the activated carbon and <br />associated ore slurry will be pumped to a Preg Carbon Wash Screen to remove the loaded (gold <br />containing) carbon from the pumped slurry. The carbon is washed and loaded into a tank truck <br />(approximately 5 tons at a time) and then transferred for further processing and gold recovery <br />at the existing AGADR facility. The screen underflow slurry, now without carbon, is pumped <br />back into the CIP Circuit. <br />The thickeners are used to capture as much water as possible for reuse in the High Grade Mill <br />facilities. The processed ore thickeners will consist of the Processed Ore Thickener that de- <br />waters the Flotation System processed ore and the High pH Thickener that dewaters the CIP <br />processed ore. The clear overflow solutions from these thickeners are kept separate in the <br />High Grade Mill facilities to keep any residual cyanide separate from the grinding, flotation, and <br />regrind circuits. Water that does not contain any residual cyanide is stored in the Process <br />Water Tank, which is approximately 417,000 gallons in size. Water that may have traces of <br />Cyanide will be stored in the High pH Process Water Tank (which is approximately 28,000 <br />
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