通过双极膜电渗析中的 pH 极化提高氨回收率

IF 3.5 Q3 ENGINEERING, ENVIRONMENTAL
Sandali Panagoda, Pengyi Yuan, Vladimir Pavlovic, John Barber and Younggy Kim
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引用次数: 0

摘要

在废水处理和管理中,从食物垃圾(包括其液态消化物)中回收氨气受到高度重视。在各种膜分离技术中,不含阴离子交换膜的双极膜电渗析(BMED)是一种具有吸引力的选择性氨分离候选技术,可减少结垢问题。在这项研究中,使用 5 对阳离子交换膜(CEM)和双极膜(BPM)构建了一个台式规模的双极膜电渗析堆。使用实验室规模的 BMED 叠层处理模拟食品液体消化物,以检查 3 种不同膜间距(0.82、1.64、2.46 毫米)的氨分离情况。膜间距为 1.64 毫米时,电流和氨气分离度最高,而带有 3 个间隔垫片(2.46 毫米)的 BMED 堆仍显示出相当的分离性能,电流或氨气回收率没有显著下降。就地清洗(CIP)溶液中残留的 Ca2+ 和 Mg2+ 表明,BMED 运行中没有严重的结垢问题。最后,即使在碱池中氨浓度高度累积(11,000 mg-N/L)的情况下,碱池和进料池之间的 pH 极化也能最大限度地减少氨的反向扩散。由于能耗要求相对较低(1.24-6.78 kWh/kg-N),缺乏 AEMs 的 BMED 被证实是一种可持续的从高氨废水中回收氨的方法。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Enhancing ammonia recovery through pH polarization in bipolar membrane electrodialysis†

Enhancing ammonia recovery through pH polarization in bipolar membrane electrodialysis†

Ammonia recovery from food waste (including its liquid digestate) is highly emphasized in wastewater treatment and management. Among various membrane-based separation technologies, bipolar membrane electrodialysis (BMED) without anion exchange membranes (AEMs) is an attractive candidate for selective ammonia separation with reduced scaling problems. In this study, a bench-scale BMED stack was built using 5 pairs of cation exchange membranes (CEMs) and bipolar membranes (BPMs). A simulated food liquid digestate was treated using a lab-scale BMED stack to examine the ammonia separation with 3 different intermembrane distances (0.82, 1.64, and 2.46 mm). The highest electric current and ammonia separation were obtained for the intermembrane distance of 1.64 mm, while the BMED stack with 3 spacer gaskets (2.46 mm) still showed comparable separation performance without significant decreases in electric current or ammonia recovery. The residual Ca2+ and Mg2+ in the cleaning-in-place (CIP) solutions indicated that there were no noticeable scaling problems during the BMED operation. Finally, the pH polarization between the base and feed cells was found to minimize the ammonia back-diffusion even with the highly accumulated ammonia concentration (>11 000 mgN L−1) in the base cell. With the relatively low energy requirement (1.24–6.78 kW h kgN−1), BMED lacking AEMs with wide intermembrane distances was confirmed to be a sustainable candidate for ammonia recovery from wastewater with high levels of ammonia.

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