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Recovery of Gallium from Corundum Flue Dust by Two-Stage Alkali Leaching, Carbonation, Acid Leaching and Solvent Extraction Process

机译:通过两阶段碱浸出,碳酸化,酸浸出和溶剂萃取过程从刚玉烟灰粉尘中恢复镓

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摘要

Flue dust generated during the process of manufacturing corundum is a carrier of critical metal gallium. In this study, a process of alkali leaching-carbonation-acid leaching-solvent extraction was developed to recover and enrich gallium from corundum flue dust. Over 93% of the gallium in corundum flue dust could be recovered through a two-stage alkali leaching process, which consists of 120 min of concentrated alkali leaching in NaOH solution and a subsequent 30-min dilute alkali leaching (after dilution), with an alkali-to-ore mass ratio of 1.2:1. Liquid to solid ratios in two alkali leaching stages were 1.5:1 and 8:1, respectively. The carbonation process was employed to remove high-level Si in alkali leachate. After carbonation and HCl leaching, over 96% of gallium in the NaOH leachate could be dissolved into acid solution. After extracting gallium from the HCl leachate using N235 as extracting agent, 1% NaOH solution was used to strip gallium from the organic phase. The extraction and stripping efficiency of gallium was over 99% and 97%, respectively.
机译:在制造刚玉的过程中产生的烟尘是临界金属镓的载体。在该研究中,开发了一种碱浸出 - 碳酸化酸浸出溶剂萃取的方法,以从刚玉烟尘中恢复和富镓。通过两阶段碱浸出方法可以回收刚玉烟灰粉中超过93%的镓,其由NaOH溶液中的120分钟浓缩碱浸出,随后的30分钟稀释碱浸出(稀释后),具有碱 - 矿石质量比为1.2:1。液体在两种碱浸出阶段中的固体比例分别为1.5:1和8:1。使用碳酸化方法以除去碱渗滤液中的高水平Si。在碳酸化和HCl浸出后,NaOH渗滤液中超过96%的镓可以溶解在酸溶液中。在使用N235作为萃取剂从HCl渗滤液中提取镓后,使用1%NaOH溶液从有机相带镓。镓的提取和汽提效率分别为99%和97%。

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