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<br />t D.6 Tailings Disoosal <br />D.6.1 General <br />' The mill tailings will be drum-filtered or cycloned and <br /> screened to produce a moisture content of approximately 22 <br />' percent in the mill. The dewatered tailings will then be <br /> transported by truck to the south waste rockJtailings disposal <br />' area for disposal on the upstream face of the waste rock <br />t <br />i <br />b <br />d <br />d <br /> re <br />a <br />ning <br />erms, as <br />escribe <br />in Section D.3. The tailings will <br /> be deposited in a relatively thin layer on the face of the <br />' waste rock berm, which will then be covered by an end-dumped <br /> layer of waste rock. It is anticipated that the tailings and <br /> waste rack layering will continue in this manner and produce <br /> an estimated disposal ratio of approximately 1:1 in the <br />' combined disposal area. <br /> D.6.2 Material Characteristics <br /> <br /> Tailings material generated as part of small scale mill <br /> processing of San Luis ore at Battle Mountain Gold Company's <br /> Battle Mountain, Nevada laboratory were tested to determine <br /> <br />1 geotechnical and geochemical characteristics. The sample was <br /> processed as described in the following paragrapn. <br />' The sample was ground to 80 percent passing 250 microns <br />in the presence of 0.15 pounds of potassium amyl .~anthate per <br />' ton of ore. The ground sample was floated for approximately <br />five minutes using 0.05 pounds of glycol per ton of ore to <br />maintain a stable froth bed. The flotation tails were filtered. <br />The flotation concentrate was ground to 80 percent passing 75 <br />microns. The concentrate slurry was adjusted to pH 11 with Type <br />3 Portland cement. Sodium cyanide was added at the rate of <br />eight pounds per ton of concentrate. The concentrate was <br />leached for 48 hours at ambient temperature. The concentrate <br />slurry was filtered and the filtrate was re<:overed for <br />1 <br />D-35 (Revised 4/20/89) <br />