首页> 外文会议>International Solvent Extraction Conference, Jul, 1999, Catalunya (Spain) >A SEPARATION AND RECOVERY PROCESS OF GALLIUM AND INDIUM FROM ZINC REFINERY RESIDUE
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A SEPARATION AND RECOVERY PROCESS OF GALLIUM AND INDIUM FROM ZINC REFINERY RESIDUE

机译:锌精炼渣中镓和铟的分离和回收工艺

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The separation and recovery process of Ga and In from zinc refinery residue by liquid-liquid extraction with organophosphorus compounds, such as bis(2-ethylhexyl)phosphoric acid (D2EHPA), 2-ethylhexyl phosphonic acid mono-2-ethylhexyl ester (EHPNA) and bis(2-ethylhexyl)phosphinic acid (PIA-226), was investigated. The extraction equilibrium formulations for Ga, In and Zn were established up to high loadings of the extractant. D2EHPA is the most suitable extractants for separation of Ga/In. The simulation for the separation and recovery process of Ga and In from zinc refinery residue was carried out based on the equilibrium studies, and showed that effective separation and recovery of Ga and In was carried out with high purity.
机译:用双(2-乙基己基)磷酸(D2EHPA),2-乙基己基膦酸单-2-乙基己酯(EHPNA)等有机磷化合物液-液萃取从锌精炼渣中分离和回收Ga和In的过程研究了双(2-乙基己基)次膦酸(PIA-226)。建立了Ga,In和Zn的萃取平衡配方,直至萃取剂的高负载量为止。 D2EHPA是最适合分离Ga / In的萃取剂。在平衡研究的基础上,对锌精矿渣中Ga和In的分离和回收过程进行了模拟,结果表明,Ga和In的有效分离和回收率很高。

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