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在集成厌氧反应器中利用微生物电解独立阴极提高甲烷产量。

Methane production enhancement by an independent cathode in integrated anaerobic reactor with microbial electrolysis.

机构信息

State Key Laboratory of Urban Water Resource and Environment, Harbin Institute of Technology (SKLUWRE, HIT), Harbin 150090, China.

Technical University of Denmark, Department of Chemical and Biochemical Engineering, Lyngby, Denmark.

出版信息

Bioresour Technol. 2016 May;208:13-18. doi: 10.1016/j.biortech.2016.02.028. Epub 2016 Feb 10.

Abstract

Anaerobic digestion (AD) represents a potential way to achieve energy recovery from waste organics. In this study, a novel bioelectrochemically-assisted anaerobic reactor is assembled by two AD systems separated by anion exchange membrane, with the cathode placing in the inside cylinder (cathodic AD) and the anode on the outside cylinder (anodic AD). In cathodic AD, average methane production rate goes up to 0.070 mL CH4/mL reactor/day, which is 2.59 times higher than AD control reactor (0.027 m(3) CH4/m(3)/d). And COD removal is increased ∼15% over AD control. When changing to sludge fermentation liquid, methane production rate has been further increased to 0.247 mL CH4/mL reactor/day (increased by 51.53% comparing with AD control). Energy recovery efficiency presents profitable gains, and economic revenue from increased methane totally self-cover the cost of input electricity. The study indicates that cathodic AD could cost-effectively enhance methane production rate and degradation of glucose and fermentative liquid.

摘要

厌氧消化(AD)代表了从有机废物中回收能源的一种潜在方法。在这项研究中,通过阴离子交换膜将两个 AD 系统分离组装成一种新型的生物电化学辅助厌氧反应器,阴极置于内筒(阴极 AD),阳极置于外筒(阳极 AD)。在阴极 AD 中,平均甲烷产率达到 0.070 毫升 CH4/毫升反应器/天,比 AD 对照反应器(0.027 立方米 CH4/立方米/天)高 2.59 倍。COD 去除率比 AD 对照提高了约 15%。当改为污泥发酵液时,甲烷产率进一步提高到 0.247 毫升 CH4/毫升反应器/天(与 AD 对照相比增加了 51.53%)。能源回收效率呈现出盈利性增长,增加的甲烷产生的经济收入完全覆盖了输入电力的成本。该研究表明,阴极 AD 可以有效地提高甲烷产率和葡萄糖及发酵液的降解。

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