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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
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 /> F The WTP building will house the HDS processes and clarifier and will be approximately 105 feet wide <br /> and 150 feet long; <br /> Final treated water will gravity flow from the WTP to the discharge point at the Williams Fork Pump <br /> Station (Outfall 007) through the existing Williams Fork Pipeline; <br /> Feed water to the WTP will be supplied from the mill process water circuit; <br /> The plant will be equipped to divert and re-process water that does not meet discharge specifications; <br /> An emergency generator will be installed that will keep key process equipment operating during power <br /> outages; and <br /> The general site layout has been designed so that surface flow surrounding the site will be maintained <br /> within the process water system by routing flow to the TSF through the Bear Paw pipeline. <br /> Current design drawings for the WTP are presented in Appendix A and referenced throughout the following <br /> subsections. <br /> 2.1 Plant Location and Site Layout <br /> The proposed WTP will be constructed at approximate coordinates 39°50'52.17"N, 106' 4'39.32"W, northeast of <br /> the mill building in a previously disturbed area within the Mill Complex and current Affected Land Boundary. The <br /> WTP Project Area within the overall context of Henderson Mill facility is presented on Figure 1. The detailed site <br /> layout drawing for the area immediately around the proposed WTP are provided in drawings 530-DD10-PLN-601 <br /> and 530-DD10-PLN-602 in Appendix A. Drawings in Appendix A have been developed by Wood, the design <br /> engineer for the project, and generally represent an "Issue for Construction" level of design. Certain details <br /> depicted on the drawings, such as internal piping layouts, are subject to change as the project continues into <br /> construction, however, very little is anticipated to change relative to major equipment, overall layout, and building <br /> configurations. <br /> The detailed general arrangement drawing and section for the interior of the WTP are provided as drawings 530- <br /> DE10-GAD-101,530-DE10-GAD-102 and 530-DD30-PLN-401 in Appendix A. <br /> The WTP will be a pre-engineered steel building with concrete floor and foundation approximately 105 ft by 150 ft <br /> in size with an eve height of approximately 45 ft. Exterior to the steel building the lime silo and CO2 storage tank <br /> will be located on the south side of the WTP and the emergency generator and the transformer will be located on <br /> the west side of the WTP. The interior of the WTP comprises a large central area where the HDS reactor tanks, <br /> clarifier, gravity filters, lime slurry tank, spent backwash tank, effluent tank, sludge storage tank, flocculant and <br /> polymer system, and associated pumps and equipment will be located. Located on the outer perimeter wall of the <br /> WTP will be the break room,control room, restrooms, lab,and maintenance shop area(on the east wall),flocculant <br /> storage area (on the north wall), and electrical room, and communication room, with a small extension for <br /> compressors (on the west wall). The WTP has been designed with sumps to catch overflows and spills. These <br /> sumps will return captured water to the treatment process. Water for industrial uses and potable treatment supply <br /> will be provided by the raw water pipeline,which ties into the mill.A small reverse osmosis potable water treatment <br /> system capable of treating 2.8 gallons per minute on average and will be equipped with a 1,000-gallon storage <br /> tank. <br /> The area immediately surrounding the WTP will be asphalt paved, with a designated parking area located on the <br /> east side of the WTP building. The improved area will be graded to route stormwater flow to perimeter stormwater <br /> collection swales. These stormwater drainage swales direct drainage to existing drainage swales which route <br /> stormwater flow to the Bear Paw Drainage Pipeline inlet which drains to the TSF, maintaining stormwater within <br /> the process water system. Drainage from the roof of the building will also be captured in a gutter system and <br /> directed to the Bear Paw Drainage Pipeline Inlet in a buried pipeline. The existing Bear Paw pipeline captures <br /> runoff from other areas of the mill complex as well and conveys these flows to the TSF where it is managed as <br /> part of the process water system. Stormwater will flow to the TSF and be recirculated through the mill process <br /> water system. <br /> April 2022 <br />
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