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2011-08-09_REVISION - M1981185 (68)
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2011-08-09_REVISION - M1981185 (68)
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Last modified
6/15/2021 5:58:16 PM
Creation date
8/10/2011 8:53:04 AM
Metadata
Fields
Template:
DRMS Permit Index
Permit No
M1981185
IBM Index Class Name
REVISION
Doc Date
8/9/2011
Doc Name
CN-01 112d permit application Exhibit A thru F
From
Wildcat Mining Corporation
To
DRMS
Type & Sequence
CN1
Email Name
WHE
Media Type
D
Archive
No
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Process <br />Chemical <br />Proposed Application <br />Rate (lbs chemical /ton <br />ore) <br />Rod Mill <br />Sodium Carbonate <br />3.0 <br />Sodium Silicate <br />0.25 <br />Flotation <br />Biodegradable Surfactant <br />1.0 <br />Potassium amyl xanthate <br />15 <br />Sodium alkyl <br />dithiophosphate <br />0.05 <br />Copper sulfate <br />0.05 <br />Frother <br />Polyglycol ethers <br />0.10 <br />Mining Plan <br />Exhibit D <br />The proposed milling process (Figure D -2 and Figure D -3) is as follows: <br />• Two initial stages of crushing will be used: a jaw crusher as primary crusher and a <br />cone crusher as a secondary crusher; <br />• A vibrating screen in a closed circuit will complete the initial crushing circuit; <br />• The slurry from the ball mill will go into a slurry tank and then sent to a classifier; <br />• Following classification, heavier material will be returned to the mill and the <br />lighter material will be sent to the conditioner and flotation tanks; <br />• Concentrate will be collected and shipped offsite for further processing; and, <br />• Tailings will be transferred to the filter press and ultimately to the underground <br />workings for disposal. <br />During the mill optimization phase, the following processes will be evaluated: <br />• Recovery Optimization: The rate of chemical addition during milling will be <br />evaluated to maximize gold - silver concentrate recovery. The proposed chemicals <br />and application rates are presented below. On -site management of the chemicals <br />is presented in the EPP. (Exhibit U). <br />• Water and Chemical Recovery: A description of project water requirements and <br />sources is provided in Exhibit G. Preliminary design provides for at least 75% <br />water recovery from the tailings prior to disposal. The mill design will be verified <br />during the optimization phase. Additionally, the effectiveness of water recycling <br />and water quality will be evaluated with respect to recycling optimization and <br />potential disposal requirements, as discussed in the EPP. (Exhibit U). <br />• Tailings Disposal: Preliminary evaluation of the mine rock (Exhibit U) indicates <br />that it is suitable for disposal within the May Day No. 1 stope of the underground <br />workings. Further testing of the tailings will be performed as detailed in the EPP. <br />(Exhibit U). Up to 5,000 tons of tailings will be produced during this phase and <br />Wildcat Mining Corporation <br />May Day Idaho Mine Complex — 112d Permit Application <br />Revised August, 2011 <br />Exhibit D — Rule 6.4.4 <br />Page 6 of 10 <br />
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