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Catalytic Oxidation of Ferrous Ion in Acid Medium with Active Aeration Using Activated Carbon Doped with Transition Metals

机译:使用过渡金属掺杂活性炭的活性通气催化氧化亚铁离子的亚铁离子

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In this study, the catalytic oxidation of Fe2+ to Fe3+ is carried out with active aeration using activatedcarbon doped with Au, Pt and Ru, as an alternative to traditional oxidative methods for itsapplication in the ferric acid leaching of copper sulfides. An impregnation of Au, Pt, Ru in bothgranular (2 mm) and powdered (38 μm) activated carbons (274 m2/g) was performed. Using standardsolutions (48 mg/L) of these metals in contact with 4 g/L of activated carbon, for 2 hours in a stirredbed. Then, 5.6 g/L of NaBH4 was added for 3 hours to reduce the metal. The solution was filtratedand analyzed valued by UV-Vis analysis, while the obtained solid was dried. The catalytic oxidationtests were carried out in a stirred bed with an air flow of 384 NL/h, with activated carbonconcentrations between 0.8 and 8 g/L, using FeSO4.7H2O (500 mg/L) at pH =1. In periodic solutionsamples, the total iron content and the dissolved transition metals were determined by atomicabsorption spectrophotometry, the Fe2+ content by permanganimetry and by UV-Vis withphenanthroline. The texture and dispersion of the metals in the carbons were determined by SEMEDS.Powdered activated carbon at 0.8 g/L achieves an oxidation of 13.4% of Fe2+ in 4 hours, whileactivated carbon with 0.8 % Au, Pt, Ru content reaches 18.1 %, 15.6 % and 16.9 %, respectively. At aconcentration of 8 g/L of activated carbon doped with Au, an oxidation of 90 % of Fe2+ is achieved.Granular activated carbon with 0.8 % Au (8 g/L) achieves an oxidation of 17.8 % Fe2+. The use ofcatalytic oxidation of Fe2+ with activated carbon doped with Au, Pt, Ru and air is a promisingalternative that could be applied industrially.
机译:在该研究中,使用掺杂有Au,Pt和Ru的活化碳的活性通气来进行Fe2 +至Fe 3 +的催化氧化,作为传统氧化方法的替代,用于硫化铜酸浸出的丙酸浸出。浸渍双格状(2mM)和粉末状(38μm)活性碳(274m 2 / g)中的Au,pt,ru。使用这些金属的标准(48mg / L)与4g / L的活性炭接触,搅拌2小时。然后,加入5.6g / l的NaBH 4 3小时以减少金属。通过UV-VIS分析进行过滤和分析的滤液,干燥所得固体。催化氧化剂在搅拌床中进行,其气流为384nl / h,在pH = 1的FeSO 4.7H 2 O(500mg / L),在0.8和8g / L之间具有0.8和8g / L的活性炭浓缩。在周期性溶液中,通过原子吸收分光光度法,通过胚animetry的Fe2 +含量和通过UV-Vis含量测定总铁含量和溶解的过渡金属。碳金属在碳中的质地和分散由半乳渣测定。在0.8g / L的待氧化碳的活性炭达到13.4%的Fe2 +的氧化,在4小时内,与0.8%Au,Pt,ru含量达到18.1%的碳含量。分别为15.6%和16.9%。在掺杂8g / L活性炭的Aconcenteration掺杂Au的情况下,实现了90%Fe2 +的氧化。具有0.8%Au(8g / L)的氧化碳,达到17.8%Fe2 +的氧化。用掺杂有Au,Pt,Ru和空气的活性炭催化催化Fe2 +的Fe2 +的催化是可以在工业上应用的有知替代性。

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