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2022-04-05_REVISION - M1977342
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2022-04-05_REVISION - M1977342
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Last modified
4/5/2022 4:30:02 PM
Creation date
4/5/2022 4:15:13 PM
Metadata
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Template:
DRMS Permit Index
Permit No
M1977342
IBM Index Class Name
Revision
Doc Date
4/5/2022
Doc Name
Adequacy Review Response
From
Climax Molybdenum
To
DRMS
Type & Sequence
TR35
Email Name
PSH
JLE
Media Type
D
Archive
No
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Climax Molybdenum Company <br /> Permit No.1977-342 Technical Revision JR-35) <br /> The WTP building pad will be built up slightly above the existing ground surface and will slope down to tie into <br /> existing grade at a 3H:1 V slope, with a small area on the east side of the WTP sloping down at 2.5H:1 V due to <br /> space constraints in that area related to the proximity of the North Mill Access Road. The septic tank and leach <br /> field will be located to the east and north of the WTP, respectively. The leach field area lies at an elevation <br /> approximately 10 ft below the proposed elevation of the WTP. <br /> 2.2 WTP Primary Treatment Processes <br /> The WTP relies on a single-stage, lime-based HDS process to remove constituents of concern, primarily metals, <br /> from the influent water. A simplified process diagram is included below to visually represent this process. <br /> LIME is added to the A FLOCCULANT is <br /> reaction to raise the pH to AIR is introduced to introduced to bond pH in the final effluent is <br /> oxidize metals for lowered using carbon <br /> favorable conditions far molecules and promote <br /> metals precipitation precipitation precipitation dioxide(CO2) <br /> LIME HDS CLARIFIER <br /> SLURRY REACTOR GRAVITY r <br /> LIME TANKS FILTER WATER! <br /> SLUDGE <br /> mix <br /> • : IN WASTE <br /> SLUDGE RECYCLE <br /> Diagram 1. Water Treatment Plant Process Diagram <br /> Detailed process flow diagrams are included as drawings 530-DC00-PFD-101 and 530-DC00-PFD-102 in <br /> Appendix A. <br /> Feedwater from the mill will be conveyed to the WTP through the influent pipeline. <br /> The major process components of the WTP include the following: <br /> Lime/Sludge Mix Tank— lime is mixed with recycled solids (sludge) from the clarifier <br /> HDS Reactors—two reactors are constructed to treat the water in series. In these reactors,the slurry <br /> from the lime/sludge mix tanks is mixed with the influent water, air is introduced, and elevated pH and <br /> the presence of oxygen causes targeted constituents to oxidize and precipitate. Following reaction, <br /> polymer is added to promote flocculation prior to flowing into the clarifier. <br /> Clarifier— flocculated particles in the reacted water settle and the clarified overflow is routed to the <br /> gravity filter while the heavy underflow of flocculated particles is recycled or pumped to the TSF for <br /> disposal. <br /> Gravity Filtration — remaining solids are removed in multi-media filters and filtrate is routed to the <br /> effluent tank for neutralization. <br /> Effluent tank& Neutralization—CO2 is dissolved in the water to neutralize the pH prior to discharge. <br /> The HDS process utilized by the plant re-circulates sludge to increase the neutralization potential of the added <br /> lime and improve coagulation and settling. Lime will be combined with recycled sludge from the clarifier in the <br /> lime/sludge mix tank. Influent water from the mill and lime/sludge slurry will flow into Reactor Tank#1 and then <br /> April 2022 <br />
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