Mining Mirror September 2018 | Page 42

Mining in focus The Kansanshi copper mine in Zambia is one of the biggest copper mines in Africa. The plant also proved to be profitable to an extent that the copper industry became aware and interested in copper L/SX/EW. Improvement in L/SX/EW technology was inevitable. In Kordasky’s paper, he writes that “the first improvement in copper SX reagents came when LIX 64N was added as makeup to the Ranchers plant in late 1968”. LIX 64N had several advantages with greater extractive strength, faster kinetics, faster phase separation, and lower entrainment, among others. Kordosky explained that the benefits of LIX 64N resulted in reagent properties that broadened the range of copper leach liquors that could be successfully treated by solvent extraction. This had a knock-on effect on the SX plant, as capital costs were reduced. Decreased organic losses and tankhouse bleeds lowered overall operating costs. Adding LIX 860-1 to plants that were already using LIX 64N enabled the plants to upgrade plant performance and flexibility quickly and conveniently. Various companies with other improvements to L/SX/EW technology [40] MINING MIRROR SEPTEMBER 2018 were introduced to the market over time, each with their unique benefits. Among them was the reagent SME 529, which was an alternative to LIX 64N. Unfortunately, “the poor properties of the side products from the manufacture of this reagent overrode the very good properties of the extractant molecule widely used” — resulting in limited use of the reagent in the market. LIX 65N, SME 529, P-1, and LIX 84-1 were other technologies introduced to the market. From a leaching perspective, copper producers felt that this method was an important source of copper, especially after seeing the cost-effectiveness of purifying and concentrating copper from leach liquors. The Thin Layer (TL) acid cure leaching process was one of the copper leaching processes and in his paper, Kordosky explains that Sociedad Minera Pudahuel (SM) was the first plant to practice the TL leaching for copper in 1978. Through this process, the plant was able to achieve “high copper recovery from both the oxide and sulphuric portions of their ore low soluble silica in the pregnant leach liquor, and an overall water/acid balance to give a zero-discharge plant”. By leaching the tails from their TL operation for an additional 45 days, SMP was able to prove that total copper recovery from the chalcocite/bornite portion of their mixed oxide sulphide ore could reach 85%. From then, the significance of bacteria leaching metal sulphides was recognised. Kordosky mentions that in 1968, Ranchers installed flotation cells to remove entrained organic from the pregnant electrolyte, resulting in improved copper quality — which fell into the category of electrowinning (EW ). Seven years later, there was a breakthrough in EW with the registration of Baghdad cathode on the Comex, followed by the registration of Anamax cathode on the London Metal Exchange several years later. One of the methods of implementing cathode through EW was a cathode press to straighten two-day cathodes grown on copper starter sheets. The results of this process were higher current efficiencies and improved copper quality.