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Electrowinning of Iron from Spent Leaching Solutions Using Novel Anion Exchange Membranes

机译:使用新型阴离子交换膜对废浸出液中的铁进行电沉积

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摘要

In the Pyror process, electrowinning (EW) is used to recover acid and iron from spent leaching solutions (SLS), where a porous Terylene membrane acts as a separator between the cathode and anode. In this study, a novel anion exchange membrane (AEM)-based EW process is benchmarked against a process without and with a porous Terylene membrane by comparing the current efficiency, specific energy consumption (SEC), and sulfuric acid generation using an in-house constructed EW flow cell. Using an FAP-PK-130 commercial AEM, it was shown that the AEM-based process was more efficient than the traditional processes. Subsequently, 11 novel polybenzimidazole (PBI)-based blend AEMs were compared with the commercial AEM. The best performing novel AEM (BM-5), yielded a current efficiency of 95% at an SEC of 3.53 kWh/kg Fe, which is a 10% increase in current efficiency and a 0.72 kWh/kg Fe decrease in SEC when compared to the existing Pyror process. Furthermore, the use of the novel BM-5 AEM resulted in a 0.22 kWh/kg Fe lower SEC than that obtained with the commercial AEM, also showing mechanical stability in the EW flow cell. Finally, it was shown that below 5 g/L Fe, side reactions at the cathode resulted in a decrease in process efficiency, while 40 g/L yielded the highest efficiency and lowest SECs.
机译:在Pyror工艺中,电解沉积(EW)用于从废浸出溶液(SLS)中回收酸和铁,其中多孔的涤纶膜充当阴极和阳极之间的隔板。在这项研究中,通过比较电流效率,比能耗(SEC)和使用内部硫酸生成的方法,将基于新型阴离子交换膜(AEM)的EW工艺与不带有或带有多孔Terylene膜的工艺进行比较构造的EW流通池。使用FAP-PK-130商业AEM,表明基于AEM的过程比传统过程更有效。随后,将11种新型的基于聚苯并咪唑(PBI)的混合AEM与商业AEM进行了比较。性能最佳的新型AEM(BM-5)在SEC为3.53 kWh / kg Fe的情况下产生了95%的电流效率,与相比,SEC电流效率提高了10%,Fe降低了0.72 kWh / kg现有的Pyror流程。此外,新型BM-5 AEM的使用使SEC的SEC比商业AEM降低了0.22 kWh / kg Fe,这也显示了EW流通池的机械稳定性。最后,结果表明,Fe含量低于5 g / L时,阴极的副反应导致工艺效率降低,而40 g / L则产生最高的效率和最低的SEC。

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