Feickert Fenske Carolina, Kirzeder Franz, Strübing Dietmar, Koch Konrad
Chair of Urban Water Systems Engineering, Technical University of Munich, Am Coulombwall 3, 85748 Garching, Germany.
Chair of Urban Water Systems Engineering, Technical University of Munich, Am Coulombwall 3, 85748 Garching, Germany.
Bioresour Technol. 2023 May;376:128868. doi: 10.1016/j.biortech.2023.128868. Epub 2023 Mar 11.
The biological methanation of H and CO in trickle bed reactors is one promising energy conversion technology for energy storage, but experiences at pilot-scale under real application conditions are still rare. Therefore, a trickle bed reactor with a reaction volume of 0.8 m was constructed and installed in a wastewater treatment plant to upgrade raw biogas from the local digester. The biogas HS concentration of about200 ppm was reduced by half, but an artificial sulfur source was required to completely satisfy the sulfur demand of the methanogens. Increasing the ammonium concentration to > 400 mg/L was the most successful pH control strategy, enabling stable long-term biogas upgrading at a CH production of 6.1 m/(m·d) with synthetic natural gas quality (CH > 98%). The results of this study with a reactor operation period of nearly 450 days, including two shutdowns, represents an important step towards the necessary full-scale integration.
在滴流床反应器中对氢气和一氧化碳进行生物甲烷化是一种很有前景的用于能量存储的能量转换技术,但在实际应用条件下中试规模的经验仍然很少。因此,建造了一个反应体积为0.8立方米的滴流床反应器,并安装在一家废水处理厂中,以提纯来自当地沼气池的粗制沼气。沼气中约200 ppm的硫化氢浓度降低了一半,但需要人工硫源才能完全满足产甲烷菌的硫需求。将铵浓度提高到>400 mg/L是最成功的pH控制策略,能够在合成天然气质量(甲烷含量>98%)下以6.1立方米/(立方米·天)的甲烷产量实现稳定的长期沼气提纯。本研究中反应器运行近450天(包括两次停机)的结果代表了朝着必要的全面整合迈出的重要一步。