Department of Environmental Engineering, Korea Maritime and Ocean University, Busan 49112, South Korea.
Department of Environmental Engineering, Korea Maritime and Ocean University, Busan 49112, South Korea.
Bioresour Technol. 2017 Oct;241:171-180. doi: 10.1016/j.biortech.2017.05.073. Epub 2017 May 15.
Methane production in the upflow anaerobic bioelectrochemical reactor (UABE) treating acidic distillery wastewater was compared to the upflow anaerobic sludge blanket reactor (UASB), and the electron transfer pathways for methane production were also evaluated in the effluent recirculation. The methane productions from reactors were influenced by the low pH of influent wastewater. However, the methane production rate and yield of the UABE were 2.08L/L.d and 320mL/g COD, which were higher than the UASB. The effluent recirculation containing alkalinity neutralized the acidic influent and increased the upflow velocity in both reactors, and improved the direct interspecies electron transfer more in the UABE. When the effluent recirculation ratio was 3.0 in the UABE, the methane production rate and yield were reached up to 3.88L/L.d and 501.0mL/g COD, respectively. The UABE requires electrode installation and electrical energy for operation, but the benefits from increased methane production are much higher.
上流式厌氧生物电化学反应器(UABE)处理酸性酿酒废水的甲烷产量与上流式厌氧污泥床反应器(UASB)进行了比较,还评估了在回流出口中甲烷的产生途径。进水的低 pH 值会影响反应器中的甲烷产量。然而,UABE 的甲烷产率和产甲烷量分别为 2.08L/L.d 和 320mL/g COD,高于 UASB。含有碱度的回流废水可中和酸性进水并增加两个反应器中的上流速度,从而在 UABE 中更有效地促进直接种间电子转移。当 UABE 的回流比为 3.0 时,甲烷的产率和产甲烷量分别达到 3.88L/L.d 和 501.0mL/g COD。UABE 需要安装电极并提供电能才能运行,但从增加的甲烷产量中获得的收益要高得多。