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2022-04-05_REVISION - M1977342
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2022-04-05_REVISION - M1977342
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Entry Properties
Last modified
4/5/2022 4:30:02 PM
Creation date
4/5/2022 4:15:13 PM
Metadata
Fields
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 (TR-35) <br /> 2. PROJECT DESCRIPTION <br /> The project scope includes the construction and operation of a 600 gpm WTP at the Henderson Mill.The proposed <br /> WTP will be located northeast of the mill building in a previously disturbed area within the Mill Complex and current <br /> Affected Land Boundary. Figure 1 presents an overall site plan for the Henderson Mill facility, with an inset <br /> showing the proposed location for the WTP, and the location of the outfall at the Williams Fork River. The WTP <br /> will treat surplus process water from the mill for discharge to the WFR. The main objectives for the WTP are to <br /> facilitate flexible site-wide water management under varying climatic conditions, maintain operational flexibility of <br /> the mill, increase the efficient use and re-use of water and achieve and maintain compliance with the effluent limits <br /> to be established underthe Colorado Discharge Permit System(CDPS)administered by the Water Quality Control <br /> Division (WQCD). <br /> The mill recirculates, stores, recycles and reuses process water between the TSF, EBR, and the mill. Process <br /> water from the mill is conveyed to the TSF with the tailing slurry for storage. Process water is then recycled from <br /> the TSF to the mill by pumping water from the TSF decant pond into the EBR and subsequently to the mill for use. <br /> Although water treatment has always been part of the long-term life-of-mine plan, the mill facility has operated as <br /> a zero-discharge facility since Henderson began operations in 1976; meaning that all water within the system has <br /> been recirculated for use within the milling circuit. <br /> The WTP treatment process will consist of a lime-based, single-stage high-density sludge (HDS) process capable <br /> of treating surplus water at a design flow rate of 600 gpm, which is 1.3 cfs or 0.86 MGD, year-round. The HDS <br /> process recirculates sludge to increase the neutralization potential of the added lime, improve coagulation and <br /> settling, and reduce reagent use. As the pH is raised to alkaline conditions, metals are precipitated. The resulting <br /> precipitate, or sludge, is thickened and removed from the HDS effluent using a clarifier. Ultimately, waste sludge <br /> will be conveyed to the TSF for disposal using existing pipelines. Clarifier overflow, or effluent, is filtered and <br /> undergoes pH neutralization using carbon dioxide. Finally, an existing pipeline will convey treated water from the <br /> WTP to the discharge location on the WFR at the existing Williams Fork pump station. <br /> The Henderson Mill holds an active CDPS permit which allows for the discharge of process water under certain <br /> conditions, although, as stated above, the Henderson Mill has operated as a zero-discharge facility. This current <br /> permit was issued in 2007 and has been administratively extended. A CDPS permit renewal application for the <br /> Henderson Mill was submitted to the WQCD on April 14, 2020,with modifications to encompass the WTP project. <br /> The WQCD will process the application and issue a permit establishing discharge limits, based on the applicable <br /> water quality standards in the receiving stream to protect its classified uses. <br /> The construction of the WTP is the subject of this Technical Revision. Key project elements are summarized <br /> below, and additional detail is provided in subsequent sections: <br /> The WTP will be located northeast of the mill building in a previously disturbed area within the Mill <br /> Complex; <br /> Plant capacity is rated at 600 gpm; <br /> The plant is designed as a High Density Sludge (HDS) process and includes polymer-enhanced <br /> flocculation, clarification, and gravity filtration; <br /> Sludge will be re-circulated to increase the neutralization potential of the added lime and improve <br /> coagulation and settling; <br /> Carbon dioxide will be dissolved in the water to neutralize the pH prior to discharge; <br /> Chemicals to be used for water treatment will include hydrated lime, flocculent polymer, and carbon <br /> dioxide; <br /> The WTP has been designed with sumps to catch overflows and spills. These sumps will return <br /> captured water to treatment; <br /> The WTP building will be a pre-engineered steel building with concrete floor and foundation; <br /> April 2022 <br />
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