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Removal of iron from industrial grade aluminum sulfate by primary amine extraction system

机译:通过伯胺萃取系统去除工业级硫酸铝中的铁

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The removal of iron from industrial aluminum sulfate by the primary amine extraction system composed of primary amine N-1923 as the extractant, n-octanol as the modifier and kerosene as the diluent was studied. The mechanism of removing iron by primary amine system was determined through slope analysis method and IR spectra. Also investigated were effects such as pH in aqueous phase, phase ratios O/A (organic/ aqueous), the volume fractions of extractant and modifier in organic phase, and the contact time of extraction. At the same time, the research was conducted on stripping of iron using sodium chloride solution or sulfuric acid as stripping agents from the iron-loaded organic phase. The results showed 99.99% extraction of iron from industrial aluminum sulfate with the extraction system composed of 25 vol.% N-1923, 25 vol.% n-octanol and 50 vol.% kerosene when the phase ratio O/A was 1:2, pH valueN1.2 and contact time was 6 min. The difficulties in separating aqueous phase and organic phase were effectively overcome by n-octanol. The strip recovery of iron using 4.0mol L~(-1) sulfuric acid as the stripping agent was 96.5% which was slightly higher than that using 2.0 mol L~(-1) sodium chloride.
机译:以伯胺N-1923为萃取剂,正辛醇为改性剂,煤油为稀释剂组成的伯胺萃取体系,研究了工业硫酸铝中铁的去除。通过斜率分析法和红外光谱确定了伯胺体系除铁的机理。还研究了诸如水相中的pH,O / A(有机/水)相比,有机相中萃取剂和改性剂的体积分数以及萃取的接触时间等影响。同时,进行了以氯化钠溶液或硫酸作为脱铁剂从载铁有机相中汽提铁的研究。结果表明,当相比O / A为1:2时,由25%(体积)的N-1923、25%(体积)的正辛醇和50%(体积)的煤油组成的萃取体系可从工业硫酸铝中萃取99.99%的铁。 ,pH值为N1.2,接触时间为6分钟。正辛醇有效地克服了分离水相和有机相的困难。用4.0mol L〜(-1)硫酸作为汽提剂的铁的汽提回收率为96.5%,略高于使用2.0mol L〜(-1)氯化钠的铁的汽提率。

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