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生物电化学强化上流式厌氧污泥床(UASB)反应器处理高有机负荷率废水的厌氧甲烷化过程

Bioelectrochemical enhancement of anaerobic methanogenesis for high organic load rate wastewater treatment in a up-flow anaerobic sludge blanket (UASB) reactor.

作者信息

Zhao Zhiqiang, Zhang Yaobin, Chen Shuo, Quan Xie, Yu Qilin

机构信息

Key Laboratory of Industrial Ecology and Environmental Engineering (Dalian University of Technology), Ministry of Education, School of Environmental Science and Technology, Dalian University of Technology, Dalian 116024, China.

出版信息

Sci Rep. 2014 Oct 17;4:6658. doi: 10.1038/srep06658.

Abstract

A coupling process of anaerobic methanogenesis and electromethanogenesis was proposed to treat high organic load rate (OLR) wastewater. During the start-up stage, acetate removal efficiency of the electric-biological reactor (R1) reached the maximization about 19 percentage points higher than that of the control anaerobic reactor without electrodes (R2), and CH4 production rate of R1 also increased about 24.9% at the same time, while additional electric input was 1/1.17 of the extra obtained energy from methane. Coulombic efficiency and current recorded showed that anodic oxidation contributed a dominant part in degrading acetate when the metabolism of methanogens was low during the start-up stage. Along with prolonging operating time, aceticlastic methanogenesis gradually replaced anodic oxidation to become the main pathway of degrading acetate. When the methanogens were inhibited under the acidic conditions, anodic oxidation began to become the main pathway of acetate decomposition again, which ensured the reactor to maintain a stable performance. FISH analysis confirmed that the electric field imposed could enrich the H2/H(+)-utilizing methanogens around the cathode to help for reducing the acidity. This study demonstrated that an anaerobic digester with a pair of electrodes inserted to form a coupling system could enhance methanogenesis and reduce adverse impacts.

摘要

提出了一种厌氧产甲烷与电产甲烷耦合工艺来处理高有机负荷率(OLR)废水。在启动阶段,电生物反应器(R1)的乙酸盐去除效率达到最大值,比无电极的对照厌氧反应器(R2)高约19个百分点,同时R1的CH4产率也提高了约24.9%,而额外的电输入是从甲烷中额外获得能量的1/1.17。库仑效率和记录的电流表明,在启动阶段产甲烷菌代谢较低时,阳极氧化在降解乙酸盐中起主要作用。随着运行时间的延长,乙酸裂解产甲烷逐渐取代阳极氧化成为降解乙酸盐的主要途径。当产甲烷菌在酸性条件下受到抑制时,阳极氧化又开始成为乙酸盐分解的主要途径,这确保了反应器保持稳定的性能。荧光原位杂交(FISH)分析证实,施加的电场可使阴极周围利用H2/H(+)的产甲烷菌富集,有助于降低酸度。本研究表明,插入一对电极形成耦合系统的厌氧消化器可提高产甲烷能力并减少不利影响。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/4437/4200407/9fb326ac2025/srep06658-f1.jpg

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