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A novel electrochemical process for the recovery and recycling of ferric chloride from precipitation sludge

机译:从沉淀污泥中回收和回收氯化铁的新型电化学方法

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摘要

During wastewater treatment and drinking water production, significant amounts of ferric sludge (comprising ferric oxy-hydroxides and FePO4) are generated that require disposal. This practice has a major impact on the overall treatment cost as a result of both chemical addition and the disposal of the generated chemical sludge. Iron sulfide (FeS) precipitation via sulfide addition to ferric phosphate (FePO4) sludge has been proven as an effective process for phosphate recovery. In turn, iron and sulfide could potentially be recovered from the FeS sludge, and recycled back to the process. In this work, a novel process was investigated at lab scale for the recovery of soluble iron and sulfide from FeS sludge. Soluble iron is regenerated electrochemically at a graphite anode, while sulfide is recovered at the cathode of the same electrochemical cell. Up to 60±18% soluble Fe and 46±11% sulfide were recovered on graphite granules for up-stream reuse. Peak current densities of 9.5±4.2Am-2 and minimum power requirements of 2.4±0.5kWhkgFe-1 were reached with real full strength FeS suspensions. Multiple consecutive runs of the electrochemical process were performed, leading to the successful demonstration of an integrated process, comprising FeS formation/separation and ferric/sulfide electrochemical regeneration.
机译:在废水处理和饮用水生产过程中,会产生大量需要处理的三价铁污泥(包括羟基氧化铁和FePO4)。由于化学添加和产生的化学污泥的处置,这种做法对总体处理成本有重大影响。事实证明,通过将硫化物加到磷酸铁(FePO4)污泥中来沉淀硫化铁(FeS)是回收磷酸盐的有效方法。反过来,铁和硫化物可能会从FeS污泥中回收,并循环回工艺中。在这项工作中,在实验室规模下研究了一种从FeS污泥中回收可溶性铁和硫化物的新方法。可溶性铁在石墨阳极进行电化学再生,而硫化物在同一电化学电池的阴极进行回收。在石墨颗粒上回收了高达60±18%的可溶性Fe和46±11%的硫化物,用于上游再利用。使用真正的全强度FeS悬浮液可达到9.5±4.2Am-2的峰值电流密度和2.4±0.5kWhkgFe-1的最低功率要求。进行了多次连续的电化学过程,成功地证明了集成过程,包括FeS的形成/分离和三价铁/硫化物的电化学再生。

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