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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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ji3 SmiuTH <br />gallons in size). <br />Processed Ore Thickener: <br />Processed High Grade Ore slurry from the Flotation System is pumped to the Processed Ore <br />Thickener. The clear overflow from the thickener is sent to the Neutral pH Process Water Tank <br />for reuse in the High Grade Mill facilities. The thickened underflow from this thickener is <br />pumped to the Flotation Filter Feed Tank, which is approximately 33,000 gallons in size. <br />High pH Thickener: <br />2.8. Filtration and Agglomeration <br />Design Summary <br />Squaw Gulch High Grade Mill Facilities <br />1/24/2012 <br />Page 5 of 6 <br />CIP processed High Grade Ore from the CIP System is pumped to the High pH Thickener. The <br />clear overflow from the thickener is sent to the High pH Process Water Tank for reuse in the <br />High Grade Mill facilities. The thickened underflow from this thickener is pumped to the CIP <br />Filter Feed Tank. <br />In order for the processed ore to be handled effectively and to ensure all recoverable water is <br />recycled in the High Grade Mill facilities, additional water removal may be necessary. This is <br />done in the Flotation Processed Ore Filters and the CIP Processed Ore Filters. After filtration, <br />the processed ore will be agglomerated with cement and go through an agglomeration process <br />at a rate of approximately 250 tons per hour where the material is agglomerated to a size of <br />approximately 1 to 2 inches. The agglomeration process allow the processed ore to be handled <br />in a non - dusting form and to enhance the leachability of the processed ore for further gold <br />recovery once placed on either of the existing VLFs at the Cresson Project. <br />From the Processed Ore Thickener, the thickener underflow slurry is pumped to the Flotation <br />Filter Feed Tank. In the Flotation Filter Feed Tank, the slurry density is adjusted for optimal <br />filtration performance and is pumped into two Flotation Processed Ore Filters. The Processed <br />Ore Filter is a recessed plate pressure filter that will produce a filter cake of approximately 18% <br />moisture. <br />In like manner, the CIP Filter Feed Tank is fed thickened slurry from the High pH Thickener, the <br />slurry density adjusted, and the resultant slurry fed to two CIP Processed Ore Filters. The filter <br />cake from these filters will also be approximately 18% moisture. <br />The filter cake from both filter systems are collected on belt feeders and conveyed to the <br />Processed Ore Mixer which will mix the combined ore with cement. From the mixer, the <br />ore /cement mixture is introduced into the Processed Ore Agglomerator. In the Agglomerator, <br />
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