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1989-10-10_REVISION - M1988112 (12)
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1989-10-10_REVISION - M1988112 (12)
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Last modified
6/19/2021 6:49:18 AM
Creation date
11/21/2007 2:38:50 PM
Metadata
Fields
Template:
DRMS Permit Index
Permit No
M1988112
IBM Index Class Name
Revision
Doc Date
10/10/1989
Doc Name
GENERAL OPERATION INFORMATION
Type & Sequence
AM1
Media Type
D
Archive
No
Tags
DRMS Re-OCR
Description:
Signifies Re-OCR Process Performed
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solution to remove calcium carbonate scale and other impurities. In <br />the second step the gold is removed from the carbon using the Zadra <br />elution procedure. Elution or desorption is accomplished by <br />contacting the carbon with a caustic/cyanide solution at elevated <br />temperatures. The vessel is operated under pressure to ensure the <br />desired temperatures. The desorption vessel is operated in closed- <br />circuit with the electrowinning cell. The final step in this process <br />is to reactivate or regenerate the carbon by passing the carbon <br />through a kiln. The regenerated carbon is returned to the adsorption <br />circuit. <br />The gold will be plated from the desorption solution or <br />electrolyte by electrowinning. Electrowinning is an electrolysis <br />procedure that utilizes an insoluble anode. Stainless steel anodes <br />and steel wool cathodes will be used. The gold is plated onto the <br />steel wool cathode. The steel wool cathodes are removed periodically <br />and smelted in a dore furnace. The iron and other impurities are <br />slagged off and a dore bar containing the precious metals is poured. <br />The slurry will be removed from the leach tanks for treatment. <br />Treatment will use sulfuric acid to lower solution pH levels to below <br />9.0 to promote precipitation of some of the salt and metal levels <br />and to allow liberation and volatilization of the cyanide. The <br />relationship between cyanide and pH is shown on the enclosed Figure <br />0.5-1. As shown on this figure, approximately 10X of the cyanide can <br />be volatilized by pH control. The reactions will be initiated in an <br />agitated vessel. The pH level will be measured during the treatment <br />process to ensure that the proposed pH levels are achieved prior to <br />disposal. Additional volatization will occur as a result of the <br />proposed thin layer disposal method and the exposure of the beach <br />area to ultraviolet light fora period of time until the next layer <br />is deposited. <br />The mill design will include an internal curbing and collection <br />system within the mill to ensure that in the event of a tank rupture <br />;~ or leak all solutions are collected and contained within the mill. <br />d=16 <br />
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