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2010-07-30_REVISION - M1977342
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2010-07-30_REVISION - M1977342
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Entry Properties
Last modified
6/16/2021 6:19:00 PM
Creation date
8/20/2010 7:25:16 AM
Metadata
Fields
Template:
DRMS Permit Index
Permit No
M1977342
IBM Index Class Name
REVISION
Doc Date
7/30/2010
Doc Name
Lime Slaker Construction Request
From
Climax Molybdenum
To
DRMS
Type & Sequence
TR4
Email Name
ACS
Media Type
D
Archive
No
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-,Climax <br />F-r- <br />Molybdenum <br />A Freeport-McMoRan Company <br />i/July 30, 2010 <br />Via Email and UPS Tracking #: 1Z 804 847 03 6594 5402 <br />Mr. Allen C. Sorenson <br />Division of Reclamation Mining and Safety <br />1313 Sherman St., Rm. 215 <br />Denver, CO 80203 <br />Re: Permit M-197742, TR-04, Lime Slaker Construction Request <br />Dear Mr. Sorenson: <br />COLORADO OPERATIONS <br />Henderson Mill <br />P.O. Box 68 <br />Empire, CO 80438 <br />Phone (303) 569-3221 <br />Fax (303) 569-2830 <br />Climax Molybdenum Company (CMC) is currently planning a project to construct a lime slaker at the <br />Henderson Mil in order to neutralize the tailing slurry. The slaker will be located on southwest side of the <br />Mill building and slaked lime will be gravity fed directly into the existing tailing discharge line. <br />When Henderson operations began in 1976, slaked lime was used as a control agent in the flotation <br />process. Eventually soda ash replaced the lime, but still as a process control agent. Over the years as <br />the flotation process evolved, it was determined these reagents were no longer required. In 2005, their <br />use was discontinued. The original detention type lime slaker, prone to continuous maintenance issues, <br />was partially dismantled. <br />A benefit of using these agents to control pH in the flotation process was that they also controlled pH of <br />the entire process water system. Discontinuing use of these agents has led to acidification of the mill <br />process water over the last couple of years, which results in corrosion to metal piping in the mill process <br />components. <br />The proposed lime slaker includes a complete system to receive, store and prepare lime slurry. The <br />design process rate is 4,000 lb/hr of dry quicklime with a minimum of 90% CaO content. Quicklime is <br />pneumatically conveyed from differential pressure bulk trucks to the lime storage silo with a capacity of <br />approximately 125 tons. The unloading area is sloped to a drain that flows to the tailing discharge line. <br />Quick Lime will be discharged from the storage silo via a bin activator and rotary valve. The rotary valve <br />will feed a volumetric feeder which meters lime into a slurry slaker. The slaker building is constructed with <br />a 2 foot high foundation wall and drains that will direct any overflow to the tailing discharge line. <br />The slurry will flow from the slaker by gravity discharge into an inclined chute/pipe for delivery to the <br />tailing discharge line. Controls and instrumentation will monitor and control the system. <br />The proposed lime slaker will constitute a new Environmental Protection Facility (EPF) per Mineral Rules <br />and Regulations of the Colorado Mined Land Reclamation Board for Hard Rock, Metal and Designated <br />Mining Operations (Rules), and will be managed in accordance with the Henderson Mine and Mill <br />Environmental Protection Plan submitted as Technical Revision #4 (TR-04) to Permit M-1977-342.
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