a Department of Civil Engineering , VSB Engineering College , Karur , India.
b Department of Civil Engineering , Indian Institute of Technology , Roorkee , India.
Prep Biochem Biotechnol. 2019;49(7):704-717. doi: 10.1080/10826068.2019.1605525. Epub 2019 Apr 24.
Conventional completely mixed anaerobic treatment systems limit the chances of the different species of bacteria to spatially group together according to their mutual cooperation and as a result, show a lower efficiency and vulnerability towards shock situations. It is interesting to know about the stratification of the different bacterial species participating in the degradation process and the intermediates that they produce. In this study, we established and optimized a two-phase anaerobic packed bed biofilm reactor system (AnPBR) with porous PVA gel beads used as bio-carriers and ran the reactor system in a steady state to observe the VFAs produced along with the microbial diversity of the predominant species at different stages of the reactor system. We observed that acetate and butyrate were the predominant intermediate VFAs while concentrations of other VFAs such that propionic acid were low. and were found to be the most abundant bacterial species in acidogenic reactor while methanogenic reactor was highly enriched with and Apart from the above, syntrophic populations such as were also observed to be dominant in both the reactors - especially towards the end of acidogenic reactor and the initial part of the methanogenic reactor.
传统的完全混合厌氧处理系统限制了不同细菌物种根据相互合作在空间上聚集的机会,因此表现出较低的效率和对冲击情况的脆弱性。了解参与降解过程的不同细菌物种的分层以及它们产生的中间产物是很有趣的。在这项研究中,我们建立并优化了一个两相厌氧填充床生物膜反应器系统(AnPBR),使用多孔 PVA 水凝胶珠作为生物载体,并使反应器系统在稳定状态下运行,以观察在反应器系统的不同阶段产生的 VFAs 以及主要物种的微生物多样性。我们观察到乙酸和丁酸是主要的中间 VFA,而丙酸等其他 VFA 的浓度较低。在产酸反应器中, 和 是最丰富的细菌物种,而产甲烷反应器则高度富集了 和 。除此之外,还观察到共生种群,如 ,在两个反应器中都占主导地位 - 特别是在产酸反应器的末端和产甲烷反应器的初始部分。