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2011-09-27_REVISION - M1990057 (10)
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2011-09-27_REVISION - M1990057 (10)
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Last modified
6/16/2021 6:12:53 PM
Creation date
9/29/2011 11:33:52 AM
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Template:
DRMS Permit Index
Permit No
M1990057
IBM Index Class Name
REVISION
Doc Date
9/27/2011
Doc Name
Revised TR-03, with Adequacy Responses Incorporated.
From
The Union Milling Company
To
DRMS
Type & Sequence
TR3
Email Name
MAC
Media Type
D
Archive
No
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Reagents <br />DAF -30 <br />Water <br />Rate <br />Concentrate feed <br />Amount used (2) <br />Amount reclaim (3) <br />0.0161b /ton (1) <br />6,150 ton/yr <br />0.05 ton/yr <br />- <br />1.5st H /ton <br />6,150 ton/yr <br />- <br />9,100 ton/yr <br />Reagents <br />Pine Oil <br />Water <br />Rate <br />Ore feed <br />Amount used (2) <br />Amount used (3) <br />0.O1gal/ton (1) <br />56,000 ton/yr <br />450ga1/yr <br />- <br />0.6st H /ton <br />56,000 tons /yr <br />- <br />31,800 tons /yr <br />The concentrate from the rougher and scavenger flotation cells report to the cleaner flotation <br />circuit, which consists of two, 25" x 24" x29" (20.1 ft tank cells. The tailings from the cleaner <br />flotation circuit report back to the scavenger flotation circuit for additional residence time. <br />The concentrate from the cleaner flotation circuit reports to the concentrate thickener. <br />Reagents are added at the conditioning tank through reagent feeders. As shown in Table C -2, <br />Pine Oil is added as a frother. Pine Oil is diluted from 100% Pine Oil liquid solution. <br />Table C -2: Chemical Usage, Conditioning Tank (56,000 ton/vr <br />Reagent rate based on dry ore feed tonnage <br />(2) US gallons of reagents — annual quantity <br />(3) Liquid US tons of reagents — annual quantity <br />(4) Water is added at rougher flotation cell <br />Concentrate Circuit <br />The concentrate from the 2nd flotation cleaner cell will report to a thickener to maximize the <br />recovery of process water. The thickened concentrate, 65% solids, will go to the concentrate <br />filter. The filter additionally recovers process water. The material is 65% solids entering the <br />filter and 90% solids exiting the filter. Overflow from the concentrate thickener will be returned <br />to the circuit as process water. The concentrate filter gravity discharges its concentrate cake onto <br />a conveyor which transports the concentrate into a 4 ton bin from where it is loaded into super <br />sacks for shipment. <br />The sacks are stored within the facility until shipped. The super sacks are loaded to highway <br />trucks for shipment. This is a 10% moisture product. <br />Dry reagents are added at the thickener through a reagent mixer, diluted with water and added <br />through a chemical feed pump. As shown in Table C -3, DAF -30 is added as a flocculant. <br />Approximately 0.3 lb. of reagent are used per day. <br />Table C -3: Chemical Usage, Concentrate Thickener (56,000 ton/vr <br />Reagent rate based on dry concentrate feed tonnage (11% mass pull to concentrate) <br />(2) Tons of reagents — annual quantity <br />(3) Liquid US tons of reagents — annual quantity <br />(4) Water is reclaimed at thickener and vacuum filter and recycled <br />Tailings Circuit <br />Tailings from scavenger flotation will be sent to a tailings thickener. Thickened underflow will <br />be sent to the tailing storage facility at 65% solids. Overflow from the tailings thickener will be <br />M1990 -057 September 27, 2011 <br />
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