School of Environment and Energy Engineering, Beijing University of Civil Engineering and Architecture, Beijing, People's Republic of China.
Key Laboratory of Urban Stormwater System and Water Environment, Ministry of Education, Beijing University of Civil Engineering and Architecture, Beijing, People's Republic of China.
Environ Technol. 2024 Jan;45(4):612-623. doi: 10.1080/09593330.2022.2118083. Epub 2022 Sep 16.
Anaerobic co-digestion can effectively break the limitations of mono-digestion. However, there are still some problems such as long residence time, unsatisfactory methane yield, and unstable performance for co-digestion of sewage sludge (SS) and food waste (FW). Therefore, the SS in the reactor treating co-digestion of SS and FW is considered to be pretreated by thermal hydrolysis. In this work, the anaerobic co-digestion of SS of thermal hydrolysis pretreatment (THP) and FW significantly improved the stability, methane production of the digestive reactor, and dewaterability of the digested sludge. The R6 obtained the most cumulative methane production (315.76 mL/g VS). In addition, compared to R3, the cumulative methane production and maximum methane production rate of R5 increased by 9.93% and 14.56%, respectively. The dewaterability of R4, R5, and R6 was improved, while the dewatering performance of the R3 decreased to a greater extent. The results of the kinetic model fitting were consistent with the experimental results. Among them, the hydrolysis constants (K) of anaerobic co-digestion of THP-SS and FW were 0.121, 0.130, and 0.114 d, respectively, which were higher than those of other groups. And the estimated lag time (λ) of co-digestion was also lower than that of mono-digestion groups. Microbial community analysis indicated that the bacterial diversity and richness of anaerobic co-digested groups of THP-SS and FW were enhanced, while the methanogens with acetoclastic pathway became the main methanogenic microorganisms. This work provides essential information on anaerobic co-digestion containing different THP-SS contents.
厌氧共消化可以有效地突破单消化的限制。然而,对于污水污泥(SS)和食物废物(FW)的共消化仍然存在一些问题,如停留时间长、甲烷产量不理想、性能不稳定等。因此,被认为是在处理 SS 和 FW 共消化的反应器中对 SS 进行热水解预处理。在这项工作中,经过热水解预处理(THP)的 SS 和 FW 的厌氧共消化显著提高了消化反应器的稳定性、甲烷产量和消化污泥的脱水性能。R6 获得了最多的累积甲烷产量(315.76 mL/g VS)。此外,与 R3 相比,R5 的累积甲烷产量和最大甲烷产率分别提高了 9.93%和 14.56%。R4、R5 和 R6 的脱水性能得到了改善,而 R3 的脱水性能则下降得更为明显。动力学模型拟合的结果与实验结果一致。其中,THP-SS 和 FW 的厌氧共消化的水解常数(K)分别为 0.121、0.130 和 0.114 d,高于其他组。并且共消化的估计滞后时间(λ)也低于单消化组。微生物群落分析表明,THP-SS 和 FW 的厌氧共消化组的细菌多样性和丰富度得到了增强,而具有乙酰氧化途径的产甲烷菌成为主要的产甲烷微生物。这项工作为含有不同 THP-SS 含量的厌氧共消化提供了必要的信息。