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Electroconductive moving bed membrane bioreactor (EcMB-MBR) for single-step decentralized wastewater treatment: Performance, mechanisms, and cost

机译:用于单步分散废水处理的导电运动床膜生物反应器(ECMB-MBR):性能,机制和成本

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Membrane bioreactor (MBR) is an advantageous technology for wastewater treatment. However, efficient nutrient removal and membrane fouling mitigation remain major challenges in its applications. In this study, an electroconductive moving bed membrane bioreactor (EcMB-MBR) was proposed for simultaneous removal of organics and nutrients from domestic wastewater. The EcMB-MBR was composed of a submerged MBR, filled with electrodes and free-floating conductive media. Conductive media were introduced to reduce energy consumption in an electrochemical MBR, to improve nitrogen removal, and to mitigate membrane fouling. The results showed that COD, total nitrogen, and total phosphorus removal was up to 97.1 +/- 1.4%, 88.8 +/- 4.2%, and 99.0 +/- 0.9%, respectively, in comparison with those of 93.4 +/- 1.5%, 65.2 +/- 5.3%, and 20.4 +/- 11.3% in a conventional submerged MBR. Meanwhile, a total membrane resistance reduction of 26.7% was obtained in the EcMB-MBR. The optimized operating condition was determined at an intermittent electricity exposure time of 10 min-ON/10 min-OFF, and a direct current density of 15 A/m(2). The interactions between electric current and conductive media were explored to understand the working mechanism in this proposed system. The conductive media reduced 21% of the electrical resistivity in the mixed liquor at a selected packing density of 0.20 (v/v). The combination of electrochemical process and conductive media specially enhanced the reduction of nitrate-nitrogen (NO3--N) through hybrid bio-electrochemical denitrification processes. These mechanisms involved with electrochemically assisted autotrophic denitrification by autotrophic denitrifying bacteria. As a result, 5.2% of NO3--N remained in the effluent of EcMB-MBR in comparison with that of 29.5% in the MBR. Membrane fouling was minimized via both mechanical scouring and electrochemical decomposition/precipitation of organic/particulate foulants. Furthermore, a preliminary cost analysis indicated that an additional operating cost of 0.081 USD/m(3), accounting for 10 - 30% increment of the operating cost of a conventional MBR, was needed to enhance the nitrogen and phosphorus removal correspondingly in the EcMB-MBR. (C) 2020 Elsevier Ltd. All rights reserved.
机译:膜生物反应器(MBR)是废水处理的有利技术。然而,有效的营养消除和膜结垢缓解在其应用中仍存在重大挑战。在该研究中,提出了一种导电运动床膜生物反应器(ECMB-MBR),用于同时从国内废水中去除有机物和营养素。 ECMB-MBR由浸没式MBR组成,填充有电极和自由浮动导电介质。引入导电介质以降低电化学MBR中的能量消耗,以改善氮气去除,并减轻膜污垢。结果表明,与93.4 +/- 1.5相比,COD,总氮和总磷除去可分别为97.1 +/- 1.4%,88.8 +/- 1.4%和99.0 +/- 0.9%常规浸没式MBR中%,65.2 +/- 5.3%和20.4 +/- 11.3%。同时,在ECMB-MBR中获得了总膜阻力26.7%。优化的操作条件是在10分钟的间歇电曝光时间为10分钟/ 10缩小的,并且直流密度为15a / m(2)。探索了电流和导电介质之间的相互作用以了解该提出的系统中的工作机制。导电介质以0.20(v / v)的选定填料密度降低了混合液中的电阻率的21%。电化学工艺和导电介质的组合通过杂化生物电化学反硝化过程特别提高了硝酸氮(NO3 - N)的还原。通过自营养的反硝化细菌来涉及电化学辅助的自养反硝化的机制。结果,与MBR中的29.5%相比,ECMB-MBR的流出物中残留在5.2%的NO 3 - N。通过机械擦洗和电化学分解/沉淀的有机/颗粒污垢污垢的电化学分解/沉淀最小化膜污垢。此外,初步成本分析表明,需要额外的0.081美元/ m(3)的运营成本,占常规MBR的运营成本的10-30%,以增强氮气和磷去除在ECMB中-MBR。 (c)2020 elestvier有限公司保留所有权利。

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