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GENERAL47956
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Last modified
8/24/2016 8:23:30 PM
Creation date
11/23/2007 3:58:14 PM
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Template:
DRMS Permit Index
Permit No
M1988112
IBM Index Class Name
General Documents
Doc Name
THE RECOVERY OF CYANIDE FROM SLURRIES
Media Type
D
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.. <br />~- <br />,., <br />Pags is ' ~- <br />Fourth, the capital costs of cyanide recovery systems are less than for either chemical or bidogkal <br />treatment facliftles. Incorporation of s cyanide recovery system Into the metallurgical clrcut reduces <br />downstream cyanide and metals levels, and thereby further reduces the capital and operating costs of <br />treatment by reducing the size d the treatment facOtry and the pedod of time treatment is requred fdlowing <br />mine dosure. The economic advantages are in addHlon to the environmental advantages discussed {n the <br />previous section.. <br />Examination of the proposed Golden Cross cyanide recovery system provides an excellent example of the <br />economics of the process (it). The anticipated capital cost for the G~ranisorb Process Is about S(NZ) <br />2,200,000. There are several direct caphal cost benefits due to incorporation of cyanide rec ovary. First, <br />there Ls no need for the backfill wash plant which would have cost about S(NZ) 600,000. Second, there are <br />substantial reductions In downstream treatment requirements associated with the hydrogen peroxde <br />treatment fac~ity. <br />The excess process water accumulating in the decant pond will be treated and discharged to a local river. <br />By Incorporating cyanide recovery, there Is a slgnHlcant decrease In untreated cyanide concentrations, <br />thereby decreasing chemical costs. The reduction In cyankfe minimizes the ammonia tormtd via natu2l <br />attenuation and chemical treatment to such an extent that nitrHication is not required. These modifications <br />in treatment capacity reduce the original capital cost estimate for cyanide, metals, and ammonia treatment <br />from about S(NZ) 6,300,000 to 5(NZ) 3,700,000. The overall capital cost savings Is S(NZ) 3,200,000 <br />compared to the S(NZ) 2,200,000 cost of the cyanide recovery system. <br />Based on the pilot plant results, estimates of the cost of cyanide recovery have been prepa~ed on a per <br />tonne basis. The cost per day to operate the cyanide recovery process including sulfuric acd, power for <br />the air supply, caustic, and lime Is S(NZ) 1.10/tonne. The cost assumes a power requirement of 150 kw at <br />a cost of S(NZ) 0.08/kw-hr, and chemical costs 3 to 5 times higher than In the United States. <br />In terms of operating cost credits, there Is a return for recovered cyanide and caustic contained In the <br />scrubber sdution. Assuming a 90 percent recovery from a 200 mg/I WAD cyanide slurry, the operating cost <br />credit is S(NZ) 2.17/tonne. The calculations assumed a sodium cyanide Cost of S(NZ) 3.30/kg. The cyanide <br />usage rate Is low and assuming a more realistic cyanide concentration of 300 mg/I and a 90 percent <br />recovery, the operating cost credit Increases to S(NZ) 3.23/tonne of ore processed. <br />introduction of the cyanide recovery system reduces the downstream WAD cyanide concentrat on requiring <br />treatment from about 45.0 mg/I to 4.0 mg/I. On the basis of hydrogen peroxide consumption alone, there <br />is a decrease In operating chemical costs of S(NZJ 1.08/tonne, assuming a peroxide cost of S(NZ) 1.56/kg . . <br />for 50 percent sdution, and a 250 percent theoretical excess of peroxide. <br />;.. _... The net operating Cost benefit for the cyanide recovery process Is S(NZ) 2.15/tonne of ore li.e. 52.17 + <br />51.08 - 51.10) or 5(NZ) 1,550,000 (or a 720,000-ton-per-year operation. The net operating r:ost savings <br />amounts to over 5(NZ) 12,000,000 during the eight-year life of the mine. <br />There are additional cost savings due to decreases In operating staff and other chemicals utilized (f.e. <br />copper sulfate) In the hydrogen peroxide treatment facility. Furthermore, there Is no need to line the <br />impoundment as would be case In many Installations In the U.S. Uning of an Impoundment cieslgned for <br />the Goden Cross Mine would require a several million ddlar expenditure, and would be very diNicult to <br />Install due to the terrain. The anticipated capital operating cost savings are significant In an a{~plicatlon of <br />low cyanide containing slurries and high chemical and power costs, with greater benefits realised fn more <br />typical mining installations. <br />The operating costs associated with Golconda C.R.P. Including chemicals, power, and labor were S(AUS) <br />1.07/tonne, with a cost recovery of 5(AUS) 2.13/tonne of sdution treated. Nearly 70 percent of the cost <br />
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