氧化铝生产液中镓提取工艺及电工设备的改进

V. Skachkov, L. Pasechnik, I.S. Mediankina, S. Bibanaeva, N. Sabirzyanov
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引用次数: 0

摘要

通过电解初步纯化的氧化铝生产铝酸盐溶液,可制得不低于6N的高纯镓,控制杂质(除H、C、N、O外)浓度最高为0.00007,包括wt.%·10-8:Fe - 2、Cu - 5、Pb - 4、Mn - 1、In - 2和Sn - 2.5。改进了镓电萃取电解槽的设计,提高了电解槽的效率。提出了用纵向隔板将高效率电解槽的机匣分成两部分,每一部分又用横向隔板分成8段。这些截面的宽度比现有电解槽的宽度小三分之一。这些部分的尺寸和电极的排列减少了一半,从140毫米减少到70毫米——这是没食子酸盐和锌酸盐离子从电解质深度到阴极的距离,这减少了电解的持续时间。在计算密度为5.8 kА/m3时,提出最佳电流密度为7.5 kА/m3,可降低电能消耗。通过将阳极表面强化三倍,降低平均电流密度,降低了电解槽上电压的极化分量。从循环铝酸盐溶液中提取金属镓的七个连续操作的工艺顺序如下:1)用空气或蒸气-空气混合物净化电解液;2)石灰净化溶液;3)阴极的镀锌和阴极沉淀的溶解;4)净化电解;5)锌镓合金碱性电解沉淀;6)铝镓胶结镓;7)去除杂质。对没食子酸锌酸盐碱性溶液进行初步净化,使镓胶结过程中颗粒铝的消耗量降低到Al: Ga = 1:1的重量比
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Improvement of extraction technology and electrotechnological equipment for obtaining gallium from alumina production solutions
High-purity gallium, not worse than 6N, with the concentration of controlled impurities (except H, C, N, O) of maximum 0.00007, including, wt.%·10–8: Fe — 2, Cu — 5, Pb — 4, Mn — 1, In — 2, and Sn — 2.5 was produced by electrolysis of preliminarily purified aluminate solutions of alumina production. An improved design of electrolyzer with increased efficiency has been developed for gallium electroextraction. It was proposed to divide the casing of the advanced-efficiency electrolyzer by longitudinal partitions into two parts, each of which was divided by transverse partitions into 8 sections. The width of these sections was by one third smaller than that of available electrolyzers. The dimensions of the sections and the arrangement of elec- trodes in them were reduced by half, from 140 to 70 mm — a distance covered by gallate and zincate ions from electrolyte depth to cathodes, which decreased the duration of electrolysis. The optimal current density of 7.5 kА/m3 at the calculated density 5.8 kА/m3 was proposed, which allowed electrical energy consumption to be reduced. The polarization component of voltage on the electrolyzer was decreased by lowering the average current density achieved by three-fold enhancement of the anode surface. The technological order of seven sequential operations of metallic gallium extraction from cycling aluminate solutions is shown: 1) purification of electrolyte by an air or vapor-air mixture; 2) purification of solution by lime; 3) galvanization of cathodes and dissolution of cathode precipitate; 4) purifying electrolysis; 5) basic electrolysis with precipitation of zinc-gallium alloy; 6) cementation of gallium by aluminum gallam; 7) removal of impurities. Preliminary purification of gallate-zincate alkaline solution allows decreasing the granular aluminum consumption to the weight ratio Al : Ga = 1 : 1 during gallium cementation
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