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deposition/filling in the Tenmile and Mayflower Tailing Impoundments. The upgrades will also <br />assure compliance with current and projected effluent limitations associated with the Climax <br />Mine CPDES Permit and provide for improved dischazge water quality. Once this project is <br />completed, it is expected that the upgrades will serve water treatment system requirements for a <br />period in excess of 20 yeazs. <br />The principle driver for modification of the Climax Water Treatment System is limited low <br />density water treatment sludge settling capacity in Mayflower and Temnile Tailing Ponds. <br />Significant volumes of solids generated by water treatment activities over the past twenty yeazs <br />have been deposited in the ponds, reducing settling azea and storage volume in Mayflower <br />Tailing Pond. A secondary driver exists with the new statewide standazd for aluminum. <br />Climax identified water management changes and treatment alternatives that would address the <br />shrinking settling capacity in Mayflower Pond and the potential aluminum limitation and <br />concluded that the existing pond treatment system requires neaz term modiflcafion to maintain <br />sufficient residence time for metals precipitation in the treatment ponds. Moreover, <br />improvements aze needed to the two stage pH adjustment currently used to treat water at Climax <br />in order to effectively remove aluminum. <br />Figure 1 shows the general layout of the proposed upgrades. The strategy for addressing water <br />treatment needs calls for wllection and mixing of key impacted flows in a collection chamber <br />neaz the existing Lime Station, and treatment of these combined flows in a Sludge Densification <br />Plant (SDP). Treated water from the SDP will be routed through Tenmile Pond to a new second <br />stage neutralization mix pond at the base of No. 3 Dam, prior to entering Mayflower Pond. The <br />SDP and Tenmile Pond will be considered first stage treatment, while the No. 3 Dam mix pond <br />and Mayflower Pond will continue to be considered second stage treatment. Also included <br />within the process design aze necessary upgrades to the Lime Station and enhanced electronic <br />process control at key site locations. The SDP will treat most of the flows throughout the yeaz, <br />and during high flow periods, excess flows will be neutralized and handled in the existing pond <br />system. On average, 95.3% of the solids loading to first stage neutralization will be handled by <br />the SDP. <br />Upon implementation of the water treatment upgrades, sludge loading to Mayflower pond will be <br />reduced from the current estimated 25.6 million pounds to 6.4 million pounds per yeaz of dry <br />solids. The densification plant will produce a 20%+ solids sludge that can be stored and <br />disposed of in wnstructed cells on Tenmile tailing Pond. Two cells will be required to allow for <br />alternative cell use and sludge densification to projected 50% solids. <br />The Sludge Management Project is not in and of itself a water treatment system and therefore not <br />singulazly capable of meeting dischazge permit limits. The upgrades are intended to complement <br />and fortify the existing water treatment system at the Climax Mine. <br />An addendum to the Climax Mine Reclamation Permit, Exhibit G, water Information is attached <br />with feasibility level design considerations for the water treatment upgrades. Climax considers <br />components of the constructed system to be Environmental Protection Facilities under the <br />Climax Mine Environmental Protection Plan. <br />