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2012-02-28_REVISION - M1980244 (78)
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2012-02-28_REVISION - M1980244 (78)
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Last modified
8/24/2016 4:49:12 PM
Creation date
3/15/2012 2:18:08 PM
Metadata
Fields
Template:
DRMS Permit Index
Permit No
M1980244
IBM Index Class Name
REVISION
Doc Date
2/28/2012
Doc Name
VOL 6, Part 2: Facility & ADR Process Description & Design Basis
From
CC&V
To
DRMS
Type & Sequence
AM10
Email Name
TC1
Media Type
D
Archive
No
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SQUAW GULCH VALLEY LEACH <br />FACILITY AND ADR PROCESS <br />DESCRIPTION & DESIGN BASIS <br />1/25/2012 <br />Page 3 of 3 <br />containers. The container is positioned on a double contained unloading area and a basic water <br />solution is pumped through the containers to dissolve the briquettes. The dissolved solution is <br />stored in tanks (approximately 25,000 gallons each) in a secondary containment area for use in <br />the SGADR processes. <br />Caustic Solution System <br />Sodium Hydroxide is used in the SGADR to raise the pH of the barren solutions. This is required <br />to prevent the formation of hydrogen cyanide gas. The sodium hydroxide will be delivered by <br />tanker trucks and will be stored in a tank (approximately 20,000 gallons) within a double <br />contained area. <br />Hydrochloric Acid System <br />The pregnant solution at this site causes potential scaling to occur on the activated carbon. To <br />manage this scale, the carbon is occasionally washed with a dilute acid solution in the Carbon <br />Acid Wash System. Hydrochloric acid is used for this process. The acid is delivered by tanker <br />trucks to the SGADR. It is stored in a separate double containment area in an FRP storage tank <br />(approximately 10,000 gallons). The tank is equipped with an acid scrubber to remove any acid <br />vapor that would be released during filling or tank expansion due to high ambient <br />temperatures. <br />
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