Biological in-situ biogas upgrading is a promising approach for sustainable energy-powered technologies. This method increases the CH content in biogas via hydrogenotrophic methanogenesis with an external H supply. In this study, an anaerobic membrane bioreactor (AnMBR) was employed for in-situ biogas upgrading. The AnMBR was operated in semi-batch mode using waste activated sludge as the substrate. Pulsed H addition into the reactor and biogas recirculation effectively increased the CH content in the biogas. The addition of 4 equivalents of H relative to CO did not lead to appreciable biogas upgrading, although the acetate concentration increased significantly. When 11 equivalents of H were introduced, the biogas was successfully upgraded, and the CH content increased to 92%. The CH yield and CH production rate were 0.31 L/g-VS and 0.086 L/L/d, respectively. In this phase of the process, H addition increased the acetate concentration and the pH because of CO depletion. Compared with a continuously-stirred tank reactor, the AnMBR system attained higher CH content, even without the addition of H. The longer solid retention time (100 d) in the AnMBR led to greater degradation of volatile solids. Severe membrane fouling was not observed, and the transmembrane pressure remained stable under 10 kPa for 117 d of continuous filtration without cleaning of the membrane. The AnMBR could be a promising reactor configuration to achieve in-situ biogas upgrading during sludge digestion.
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http://dx.doi.org/10.1016/j.scitotenv.2022.154573 | DOI Listing |
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