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在生物电化学厌氧消化反应器中,批量溶液和生物电极上的食物垃圾产甲烷的贡献分析。

Contribution analysis of methane production from food waste in bulk solution and on bio-electrode in a bio-electrochemical anaerobic digestion reactor.

机构信息

Department of Environmental Engineering, Chungbuk National University, Republic of Korea.

Department of Environmental Engineering, Chungbuk National University, Republic of Korea.

出版信息

Sci Total Environ. 2019 Jun 20;670:741-751. doi: 10.1016/j.scitotenv.2019.02.112. Epub 2019 Feb 20.

Abstract

Quantitative evaluation of methane production either in bulk sludge or biofilm on electrodes was performed in a bio-electrochemical anaerobic digestion (BEAD) reactor with a lower electrode surface area/reactor working volume (A/V) ratio (7.0 m/m). Methane production by electrochemical reaction was also evaluated in the BEAD reactor with a biofilm-free electrode under the same conditions as in other experimental sets. The contributions of bulk sludge, biofilms on the electrodes, and electrochemical reactions in the BEAD reactor, on methane production, were 70.2%, 29.8%, and 0%, respectively. The principal methane-producing reactions occurred in the bulk sludge facilitated by H-dependent methylotrophic and hydrogenotrophic methanogens. Hydrogenotrophic methanogenesis was also the main methane-producing reaction in the biofilms attached to the bio-electrodes. Quantitative analysis of methane production (29.8%) in the biofilm revealed that bio-electrochemical processes involving H and direct bio-electrochemical methane production contributed 8.7% and less than 0.1%, respectively. Interestingly, biochemical processes (21.1%) contributed the most to the overall production of methane in the biofilm. Bulk sludge contributed more to methane production than the biofilm, but the methane production per unit mass of volatile solid on the electrodes was about 1.6-times higher than that of bulk sludge. Methane was not produced in the BEAD reactor with biofilm-free electrodes. Therefore, formation and maintenance of biofilms on the electrodes are essential for improved methane production in BEAD reactors.

摘要

采用低电极表面积/反应器工作体积(A/V)比(7.0 m/m)的生物电化学厌氧消化(BEAD)反应器,对絮体污泥或电极上生物膜中的甲烷生成进行了定量评估。在相同条件下,在无生物膜的电极的 BEAD 反应器中进行了电化学反应产生的甲烷的评估。BEAD 反应器中,絮体污泥、电极上的生物膜和电化学反应对甲烷生成的贡献分别为 70.2%、29.8%和 0%。主要的产甲烷反应发生在絮体污泥中,由 H 依赖性甲基营养型和氢营养型产甲烷菌促成。氢营养型产甲烷作用也是附着在生物电极上的生物膜中的主要产甲烷反应。对生物膜中甲烷生成(29.8%)的定量分析表明,涉及 H 和直接生物电化学甲烷生成的生物电化学过程分别贡献了 8.7%和不到 0.1%。有趣的是,生化过程(21.1%)对生物膜中甲烷的总生成贡献最大。絮体污泥对甲烷生成的贡献大于生物膜,但电极上挥发性固体单位质量的甲烷生成量约比絮体污泥高 1.6 倍。在无生物膜的电极的 BEAD 反应器中未产生甲烷。因此,在 BEAD 反应器中形成和维持电极上的生物膜对于提高甲烷生成是必要的。

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