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Leaching of Chalcopyrite Concentrate in Iodide-Sulfuric Acid Medium with Seawater

机译:用海水浸出黄铜矿浓缩碘硫酸介质的浸出

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The chalcopyrite leaching process has had poor success rates because this mineral shows a slow and incomplete oxidation due a strong passivation in acid solutions and formation of an impermeable layer which impedes the attack. However, the use of some strong oxidizing agents, such as iodine/iodide salts, can be used to increase the reaction rates and break this layer. Also, as an advantage, this compound oxides typical water soluble species than can be found oxidant that typical water-soluble species can be found in caliche mineral. The applications and use of iodide for copper extraction scarcely used however it dissolves successfully many sulfide minerals including chalcopyrite at an acceptable kinetic rate, due to high proton activity created by the acid forming a strong oxidizing agent. This oxidant (iodide) offered an alternative to the leaching process along or with other salts commons. In addition to the above-mentioned, due to the scarcity of fresh water resources in places like northern Chile, the use of seawater in mineral processing is becoming increasingly important. The direct use of seawater without desalination pre-treatment can be attractive in chalcopyrite leaching due to aggressive nature of chloride solutions and the formation of stable cuprous chloro-complexes. The leaching tests, were investigated at two temperatures (25 °C and 50 °C) using a chalcopyrite concentrate (61.5 wt.%) with a P80= -60 ?m. The leaching tests were conducted in instrumented reactors using double-jacketed glass with a 2000 cm3 volume capacity where each reactor contained 50 g of concentrate in 1000 cm3 of solution with a stirring speed of 400 rpm. The leaching tests continued for 66 and 216 hours where solutions samples were collected periodically and determined using AAS. As preliminary results showed that copper extraction increased with the increase of temperature and acid concentrations, obtaining values close to 80 % of copper recovery.
机译:黄铜矿浸出过程的成功率差,因为这种矿物在酸性溶液中强烈钝化并形成了阻碍攻击的不渗透层的慢性和不完全氧化。然而,使用一些强氧化剂,例如碘/碘化物盐,可用于增加反应速率并破坏该层。而且,作为一个优点,这种复合氧化物典型的水溶性物质可以被发现氧化剂可以在Caliche矿物中发现典型的水溶性物质。碘化物对铜萃取的应用和使用几乎不使用,然而它成功地溶解了许多硫化物矿物,其包括硫代铜矿的硫化物,由于由形成强氧化剂的酸产生的高质量活性,因此是由于酸的高质量活性。该氧化剂(碘化物)沿着或用其他盐分组提供浸出过程的替代方案。除了上述情况外,由于北北北部的淡水资源稀缺,矿物加工中的海水正在变得越来越重要。由于氯化物溶液的激进性质和稳定的亚铜络合物的形成,直接使用海水预处理的海水预处理可吸引黄铜矿浸出。使用P80 =-60μm的黄铜矿浓缩物(61.5重量%)在两个温度(25℃和50℃)下研究浸出试验。浸出试验在仪器反应器中使用双夹套玻璃进行,双夹套玻璃,其中2000cm 3体积容量,其中每个反应器在1000cm 3溶液中含有50g浓缩液,搅拌速度为400rpm。浸出试验持续66和216小时,定期收集溶液样品并使用AAS测定。作为初步结果表明,随着温度和酸浓度的增加而增加,铜提取增加,可获得铜回收率的80%的值。

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