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Hydrometallurgical process for the leaching of Copper Oxide Minerals without the use of Sulphuric Acid

机译:不使用硫酸浸出氧化铜矿物的湿法冶金工艺

摘要

Claim 1: mineral hydrometallurgical process for the leaching of Copper Oxide to produce Copper Cathodes, sheets or Precipitate, which uses a non polluting Organic leaching Agent, characterized in that it comprises the following steps: a) Mineral leaching Copper Oxide, in which, once transferred the ore from the mine,It is the primary, secondary and tertiary crushing of the Ore for classification, after which it is transported to a phase of Agglomeration to be impregnated with a lixiviant which consists of an aqueous solution comprising acid tricarboxylic acid (C6H8O7) in combination with Water (H2O), in such a mixture in which the acidity varies between pH 1.0 and 50; ore already impregnated is moved and collected in Leach, which are irrigated with the lixiviant previously specified through a systematic Management that consists in dividing or segregate Heap Leach into sectors, which are consumed sequentially with the lixivi Before,Obtaining a Concentrated Copper Citrate; (b) electro deposition of Copper Citrate obtained which is driven and controlled by a Flow casting, electro Deposition, VATS containing anodes and cathodes, FED by a Voltage that varies between 0.1 and 7,0 Volts, a current Density that varies between 5 and 3000 amperes per square meter; (c) recovery of Leach by a Second grinding ore already exhausted the Leach pads, which consists in a Wet Milling in which employs the lixiviant previously identified, applying a Mechanical agitation for a Residence time controlled, determined according to the leaching Kinetics of each mineral.Which generates a Leach Pulp that allows the core of this mineral, which, once filtered, produces additional Copper Liquor that allows to recover the noble Metals (Gold, Silver and Platinum), as also the Copper sulphides which might still be content.
机译:权利要求1:使用无污染的有机浸出剂的矿物湿法冶金学,用于氧化铜的浸出以生产阴极铜,片材或沉淀物,其特征在于它包括以下步骤:a)矿物浸出氧化铜,其中一次从矿石中转移矿石,将矿石进行初次,二次和三次破碎以进行分类,然后将其运输到团聚阶段,并用浸滤剂浸渍,浸滤剂由含酸性三羧酸(C6H8O7的水溶液)组成)与水(H2O)混合,混合后酸度在pH 1.0到50之间变化;将已浸渍的矿石转移并收集到Leach中,并通过系统管理将以前浸出的浸出液通过系统管理进行灌溉,该管理包括将Heap Leach分为多个部分或与Lixivi进行顺序消耗,然后再获得浓缩柠檬酸铜; (b)通过流铸,电沉积,包含阳极和阴极的VATS进行驱动和控制所获得的柠檬酸铜的电沉积,电压在0.1伏特至7.0伏特之间变化的FED,电流密度在5伏特至7伏特之间变化每平方米3000安培; (c)用已经用尽的浸出垫的第二个磨矿回收浸出物,该浸出物是在湿磨中采用先前确定的浸滤剂,根据每种矿物的浸出动力学确定机械搅拌时间,以控制停留时间这将产生一种浸出浆,使该矿物的核得以吸收,一旦过滤,它就会产生额外的铜液,该铜液可以回收贵金属(金,银和铂)以及可能仍含有的硫化铜。

著录项

  • 公开/公告号AR083984A1

    专利类型

  • 公开/公告日2013-04-10

    原文格式PDF

  • 申请/专利权人 AGHEMIO RODRIGUEZ LUIS ALBERTO;

    申请/专利号AR2011P104385

  • 发明设计人

    申请日2011-11-24

  • 分类号C22B3/04;

  • 国家 AR

  • 入库时间 2022-08-21 16:42:29

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