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~; :_: <br />Item ~ ~ ~oLt per Tone of Ore <br /> <br />'' <br />O~t't :' ~ <br />C S 0.09 <br />:.t::~: <br />a S 0.04 <br />Electrlcair't S 0.02 <br />- NaOH"' S 0.16 <br />Operatof`t 5 0-Ot <br /> S 0.31 <br />1A Based on SO.Q4/Ib for 93% H=SO~. <br />m Based on 50.04/Ib CaO. <br />at Based on the current mine price of 50.04/kw-hr. <br />r't Based on 48% caustic solution at 50.18/Ib. <br />j6j 8ased on 535,000 per year. <br />The second mine Is a 3,500 ton/day operation exhibiting a slurry flow of 1,100 gpm and a wad cyanide level <br />of about 600 mg/I. The estimated capital and operating costs were 52,000,000 and 50.73/tone of ore <br />processed, respectively. A summary of the costs are present In Tables 15 and 16. Employing a cost of <br />50.70/Ib for NaCN and a 95% recovery, the recoverable value of cyanide was 52.83/ton of ore processed. <br />The net recovered value was 52.10/ton or 52,600,000/year. The corresponding costs for chemical treatment <br />were several dollars per ton of ore processed. <br />TABLE 15 <br />ESTIMATED CAPITAL COST FOR CYANIDE RECOVERY <br />Item Total Cost <br />Stripping Towers S 75,000 <br />. Absorber Towers .. .. _._ ., - 75,000 . <br />Tower Internals - - <br />Demisters •. 60,000 <br />- Distributers _ . ._ .. . ' 60,000 <br />Support Gratings • ~ 30,000 <br />Packing 100,000 <br />Reactors 35,000 <br />Mixers 50.000 <br />Fans 30,000 <br />H,SO, Feed System + Storage 25,000 <br />Lime Feed System + Storage 100,000 <br />NaOH Feed System + Storage 15.000 <br />Subtotal Equipment Costs S 655,000 <br />Installation Factor x 3.0 <br />TOTAL CAPITAL COST 51,965,000 <br />