首页> 外文会议>The Brimacombe Memorial Symposium October 1-4, 2000, Vancouver, British Columbia, Canada >Cleaner smelting and alternative processes for copper concentrates
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Cleaner smelting and alternative processes for copper concentrates

机译:铜精矿的更清洁冶炼和替代工艺

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New copper smelting technologies such as flash smelting - flash converting are replacing conventional ones, nevertheless, some limitations intrinsic to smelting still remain. Process based on solid-gas reactions rather than based in reactions between molten phases and gases could be a valid altetnative. Three differents options are proposed: A combined pyro hydro- process for standard copper concentrates, that considers a dead roast followed by two-stages leaching in which in the first one is dissolved the copper oxide and in a second and more energetic one is dissolved the copper ferrite. In a close loop, the resulting solution is then thermally decomposed to copper sulphate and hematite to further dissolve the copper in the first leaching. The copper is obtained finally as cathodes from the leach solution. A process for high-arsenic copper concentrates that consists of two concentric fluidised bed reactors: in the inner one is fed the high-arsenic copper concentrate which operates at 660-700 deg C and heated by heat by transfered through its wal from an outer annular oxidising reactor. The dearsenified calcine generated in the inner reactor overflow continuously into the outer oxidising reactor which operates at 780-820 deg C, where the remaining sulphur of the calcine is removed as SO_2. Finally, the copper oxide is reduced to metal with carbon and CO in a molten bath of oxides, reducing the copper oxide and ferrite to copper metal while slagging the iron with silica. As an alternative to conventional Peirce-Smith converters it is proposed a process that consists of the dead roast of the grinded matte or white metal in a fluidised bed roaster which operates at 780-800 deg C. The calcines generated are leached with spent electrolyte form the EW cells and the pregnant electrolyte, with very low levels of impurities, is send to the EW step to recover the copper as cathodes. The residue, which contains the ferrite and the precious metals is cyanided to recover these metals and the resulting ferrite residue is returned to the smelting furnace to recover the copper contained.
机译:闪速熔炼-闪速转换等新的铜熔炼技术正在取代传统的熔炼技术,但仍存在一些固有的限制。基于固体气体反应而不是基于熔融相和气体之间反应的过程可能是有效的替代方法。提出了三种不同的选择:标准铜精矿的联合热解加氢工艺,其中考虑了一次焙烧,然后进行两步浸出,其中在第一步中溶解了氧化铜,在第二步中溶解了更多的高能铜。铜铁氧体。然后在闭环中,将所得溶液热分解为硫酸铜和赤铁矿,以在第一浸出中进一步溶解铜。最终从浸出溶液获得铜作为阴极。一种高砷铜精矿的工艺,该工艺由两个同心流化床反应器组成:在内部进料的高砷铜精矿在660-700摄氏度下运行,并通过沃尔玛从外圆环传递而被热量加热。氧化反应器。在内部反应器中产生的脱砷的煅烧炉连续溢流到外部氧化反应器中,该外部氧化反应器在780-820℃下运行,在那里,煅烧炉中的剩余硫以SO_2的形式被除去。最后,在氧化物的熔池中将铜氧化物与碳和CO还原为金属,将铜氧化物和铁氧体还原为铜金属,同时用二氧化硅将铁矿渣。作为常规Peirce-Smith转换器的替代方案,提出了一种方法,该方法包括在780-800℃下运行的流化床焙烧炉中,将磨砂或白金属进行死焙烧。含有极少量杂质的EW细胞和母液进入EW步骤以回收铜作为阴极。将含有铁氧体和贵金属的残留物氰化以回收这些金属,然后将所得的铁氧体残留物返回到熔炼炉以回收所含的铜。

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