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Ammonia recovery from concentrated solution by designing novel stacked FCDI cell

机译:通过设计新颖的堆叠FCDI细胞从浓缩溶液中恢复氨

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摘要

Ammonia recovery from wastewater gained increasing attention worldwide with the growing world population. However, subsequent treatment of the recovered ammonia was still complex and challenging. Therefore, a proof of concept approach by designing a novel stacked flow electrode capacitive deionization (FCDI) cell was presented in this study, to achieve ammonia recovery and generation of value-added products. Ammonium sulfate was generated successfully in the product chamber with K2SO4 worked as an additive. To avoid the influence of the co-existing ions, the effect of a monovalent cation-selective exchange membrane (M-CEM) was emphasized in the stacked FCDI cell. Compared with the standard cation exchange membrane (S-CEM), the product purity increased from around 50% to 85%, while the ratio of NH4+ towards co-existing cations increased almost 2 times by using M-CEM. To illustrate the reasons for the enhanced ion selectivity, the characterizations of both membranes were conducted by Electrochemical impedance spectroscopy (EIS), scanning electron microscopy (SEM), Fourier transform infrared spectrometry (FTIR) and X-ray diffractometry (XRD). Therefore, this study indicated that the novel design and efficient operation of the stacked FCDI reactor is an alternative way for ammonia recovery and generation as value-added products, as well as a possible approach to scaling up.
机译:随着世界人口不断增长,废水中的氨恢复越来越受到全世界的关注。然而,随后治疗回收的氨仍然是复杂的并且挑战性。因此,本研究提出了通过设计新颖的堆叠流动电极电容去离子(FCDI)细胞来实现概念方法的证据,以实现氨恢复和增值产品的产生。在产品室中成功产生硫酸铵,用K 2 SO 4作为添加剂。为避免共存离子的影响,在堆叠的FCDI细胞中强调了一价阳离子选择性交换膜(M-CEM)的效果。与标准阳离子交换膜(S-CEM)相比,产物纯度从约50%增加到85%,而NH4 +对共存阳离子的比例通过使用M-CEM而增加了2次。为了说明增强离子选择性的原因,通过电化学阻抗光谱(EIS),扫描电子显微镜(SEM),傅里叶变换红外光谱(FTIR)和X射线衍射法(XRD)进行两种膜的表征。因此,本研究表明,堆叠的FCDI反应堆的新颖设计和有效操作是氨恢复和发电作为增值产品的替代方法,以及缩放的可能方法。

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