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AUG- 9-95 WED 16:G3 CROWN TECHNOLOG`! FAX N0, 3179459096 P. 03 <br /> INTRODUCTION <br /> The environmental impacts of heap leach ore dumps and tailings ponds generated <br /> by the cyanide processing of precious metals are the subject of Increased public and <br /> regulatory attention. Avian mortalities and groundwater ccntaminatlon are problems of con- <br /> cern to the precious metals mining industry. <br /> Cyanide destruction or complexing is one method of mitigating these problems. <br /> Chlorine, hydrogen peroxide or sulfur dioxide have been used to destroy cyanide. The use <br /> of ferrous sulfate to complex cyanide present in precious metals milling solutions provides <br /> the mining industry with a more cost effective method of treatment. <br /> In one western state, mines may be required to maintain tailings ponds at cyanide <br /> concentrations lower than 60 ppm sodium cyanide. This level would be required to pre- <br /> vent bird mortalities. Ferrous sulfate can be used effectively and cheaply to control cyanide <br /> in tailings ponds at concentrations less than 50 ppm. <br /> This publication provides the mine operator with Information concerning the applica- <br /> tion and use of ferrous sulfate for the complexing of cyanide in precious metals mill soutlons. <br /> CHEMISTRY <br /> The complexing of cyanide by ferrous sulfate into ferrocyanide has been known since <br /> the early twentieth century. The conversion of sodium cyanide to ferrocyanide takes place <br /> according to the reaction: <br /> FeSO4 + 6NaCN -- Na4Fe(CN)6 + Na2SO4 <br /> The ferrocyanides are also known as Prussian or Turnbulls blue and are among the <br /> most stable cyanide complexes in aqueous solutions. Ferrocyanide is virtually nontoxic, <br /> it also being the product of the oral antidote for cyanide ingestion. <br /> Work conducted by Schiller (1) indicates the reaction to be pH dependent (Chart 1), <br /> the lowest concentration of Free cyanide in solution being obtained at a pH of about 8S. <br /> However, in general the pH of tailings solutions do not need to be adjusted. Schiller's work, <br /> treating pure potassium cyanide solutions, also showed that use of ferrous sulfate alone <br /> would not produce cyanide concentrations in solution lower than 3.8 to 5.6 ppm sodium <br /> cyanide. Reduction of cyanide in solution to lower levels requires the addition of other <br /> chemicals - sodium bisulfite or quaternary ammonium compounds. <br /> — 1 -- <br />