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厌氧渗透膜生物反应器中的微生物电化学营养物回收。

Microbial electrochemical nutrient recovery in anaerobic osmotic membrane bioreactors.

机构信息

Department of Civil, Environmental, and Architectural Engineering, University of Colorado Boulder, Boulder, CO, USA.

State Key Joint Laboratory of Environment Simulation and Pollution Control, School of Environment, Tsinghua University, Beijing, China.

出版信息

Water Res. 2017 May 1;114:181-188. doi: 10.1016/j.watres.2017.02.034. Epub 2017 Feb 20.

Abstract

This study demonstrates that by incorporating a microbial electrochemical unit into an anaerobic osmotic membrane bioreactor (AnOMBR), the system addressed several challenges faced by traditional anaerobic membrane bioreactors and recovered biogas, nitrogen, and phosphorus while maintaining high effluent quality with low dissolved methane. The microbial recovery cell (MRC)-AnOMBR system showed excellent organic (>93%) and phosphorus removal (>99%) and maintained effluent COD below 20 mg/L. Furthermore, the reactor effectively recovered up to 65% PO and 45% NH from the influent, which can be further improved if membranes with higher selectivity are used. Nutrients removal from bulk solution mitigated NH penetration to the draw solution and reduced scaling potential caused by PO. The maximum methane yield was 0.19 L CH/g COD, and low methane (<2.5 mL CH/L) was detected in the effluent. Further improvement can be made by increasing charge efficiency for better nutrient and energy recovery.

摘要

本研究表明,通过将微生物电化学单元纳入厌氧渗透膜生物反应器(AnOMBR)中,该系统解决了传统厌氧膜生物反应器面临的多个挑战,并在保持低溶解甲烷的情况下,回收沼气、氮和磷,同时保持高出水质量。微生物回收单元(MRC)-AnOMBR 系统表现出优异的有机物(>93%)和磷去除率(>99%),并将出水 COD 维持在 20mg/L 以下。此外,该反应器有效地从进水回收了高达 65%的 PO 和 45%的 NH, 如果使用选择性更高的膜,这一比例还可以进一步提高。从主体溶液中去除营养物质可以减轻 NH 向汲取液的渗透,并降低由 PO 引起的结垢潜力。最大甲烷产率为 0.19 L CH/g COD,且在出水中检测到低浓度甲烷(<2.5mL CH/L)。通过提高电荷效率以更好地回收营养物质和能量,可以进一步提高效率。

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