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Table 14 -2 Potentially Toxic Chemicals In Use at the VLFs, ADRs, and High Grade Mill <br />Chemical Name <br />Use at the Site <br />Location for <br />Use <br />Location for Storage <br />Typical Quantities Used and /or Stored on Site <br />Secondary Containment Provided <br />Fate of Chemical <br />Sodium Cyanide <br />Delivered to the site in dry <br />bulk and mixed adjacent <br />to ADRs and High Grade <br />Mill facilities. Used as a <br />dilute solution for <br />leaching and product <br />recovery. <br />VLFs, ADRs, <br />and High <br />Grade Mill <br />facilities <br />The sodium cyanide is or will <br />be delivered as briquettes to <br />the ADRs and the High Grade <br />Mill facilities. The tanker <br />containing the briquettes parks <br />within a containment surface, <br />and the briquettes are <br />dissolved in water and pumped <br />to holding tanks. <br />There are two holding tanks for sodium cyanide at the <br />AGADR, two holding tanks will be at the SGADR, and one <br />holding tank will be at the High Grade Mill facilities. <br />Each holding tank is 20,000 gallons in size. <br />At least one 7,500 gallon tanker is on site to be staged and <br />mixed at each facility <br />The dissolving of the briquettes <br />occurs within secondary containment <br />at the ADRs and High Grade Mill <br />facilities. The holding tanks are also <br />located within secondary containment <br />on concrete foundations with curbing. <br />The SGADR, AGADR, and High <br />Grade Mill facilities are underlain by <br />a geomembrane liner system for <br />tertiary containment. <br />Is consumed in the dilute sodium <br />cyanide solution leach circuit — see <br />next box for ultimate fate of sodium <br />cyanide process solutions. <br />Dilute Sodium <br />Cyanide Solution <br />Barren solution is piped <br />from storage locations to <br />the VLFs and pregnant <br />solution is piped from <br />VLFs to ADRs. Dilute <br />sodium cyanide solution is <br />used in the High Grade <br />Mill facilities to bring the <br />gold into solution from <br />both the ground product <br />and the carbon. <br />VLFs, ADRs <br />and High <br />Grade Mill <br />facilities <br />ADRs, cyanidation, and CIP <br />tanks in High Grade Mill and <br />in PSSAs within the VLFs. <br />At each of the ADRs: <br />- Internal barren tank of 20,000 gallons <br />- Strip pregnant tank of 20,000 gallons <br />- Strip barren tank of 20,000 gallons <br />- Two Strip intermediate tanks of 20,000 gallons each <br />- Two barren enrichment tanks of 80,000 gallons each at <br />AGVLF only <br />29,100 gpm being applied at AGVLF at a strength of less <br />than 250 mg/L sodium cyanide. <br />17,000 gpm to be applied at SGVLF at a strength of less <br />than 250 mg/L sodium cyanide. <br />Solutions are continuously re- circulated between the VLFs <br />and ADRs. <br />At the High Grade Mill facilities: <br />- 20,000 gallons mixing tank <br />211 gpm(77 tons of slurry per hour) being continuously <br />circulated within the High Grade Mill facilities at a strength <br />of 2,500 mg/L sodium cyanide <br />Dilute sodium cyanide solutions have <br />primary, secondary, and tertiary <br />containment at the VLFs, ADRs, and <br />High Grade Mill facilities. Piping is <br />within secondary containment or <br />double - walled when outside of <br />containment. See Sections 6.0, 7.0 <br />and 8.0 of Project Description for <br />complete details of the containment. <br />The VLFs will be rinsed as will any <br />tanks and lines that have contained <br />sodium cyanide process solutions. <br />Dilute sodium cyanide solutions are <br />expected to breakdown during <br />rinsing. Upon completion of <br />rinsing, the dilute solutions will be <br />treated with hydrogen peroxide or <br />circulation enhanced to allow <br />evaporation of water. <br />Sodium Hydroxide <br />Used for pH control <br />VLFs and <br />ADRs <br />Stored in liquid form at ADRs <br />20,000 gallon tanks at each ADR <br />Tanks are within concrete <br />containment and also located on the <br />lined area of the VLFs. Concrete <br />containment is equipped with a float - <br />activated pump that would return <br />fluid to the plant in the event of <br />release. Outside of concrete <br />containment releases would flow onto <br />VLF liner systems. <br />Is consumed in pH control for <br />process solutions. <br />Hydrochloric Acid <br />Used to acid wash carbon <br />in carbon columns in the <br />ADRs. <br />ADRs <br />Stored in mixing tanks at <br />ADRs. <br />Stored inside ADRs in holding <br />At each of the ADRs: <br />- 8,200 gallons stored in mixing tank <br />- 7,000 gallons in holding tank <br />Mixing tanks are double walled and <br />within concrete containment outside <br />of ADRs. <br />Acidic solutions that have become <br />neutralized through rinsing of the <br />carbon and are not longer useable, <br />Cripple Creek & Victor Gold Mining Company <br />Cresson Project Mine Life Extension 2 <br />14 -4 <br />