Strategic Water Infrastructure Laboratory, School of Civil, Mining and Environmental Engineering, University of Wollongong, Wollongong, NSW, 2522, Australia.
Strategic Water Infrastructure Laboratory, School of Chemistry and Molecular Bioscience, University of Wollongong, Wollongong, NSW, 2522, Australia.
J Environ Manage. 2021 Mar 1;281:111919. doi: 10.1016/j.jenvman.2020.111919. Epub 2021 Jan 5.
While cleaning wastewater, biological wastewater treatment processes such as membrane bioreactors (MBR) produce a significant amount of sludge that requires costly management. In the oxic-settling-anoxic (OSA) process, sludge is retained for a temporary period in side-stream reactors with low oxygen and substrate, and then it is recirculated to the main reactor. In this way, excess sludge production is reduced. We studied the influence of the rate of sludge exchange between MBR and side-stream anoxic reactors on sludge yield reduction within MBR. Two MBRs, namely, MBR and MBR, each coupled with separate external anoxic side-stream reactors, were run in parallel for 350 days. Unlike MBR, MBR had sludge exchange with the external reactors connected to it. During the investigation over a sludge interchange rate (SIR) range of 0-22%, an SIR of 11% achieved the highest sludge reduction (58%). Greater volatile solids destruction i.e., bacterial cell lysis and extracellular polymeric substance (EPS) destruction occurred at the SIR of 11%, which helped to achieve the highest sludge reduction. The enhanced volatile solids destruction was evident by the release of nutrients in the external anoxic reactors. It was confirmed that the sludge yield reduction was achieved without compromising the wastewater treatment quality, sludge settleability and hydraulic performance of the membrane in MBR.
在清洁废水时,生物废水处理工艺(如膜生物反应器(MBR))会产生大量需要昂贵管理的污泥。在好氧-沉淀-缺氧(OSA)工艺中,污泥在低氧和低底物的侧流反应器中保留一段时间,然后再循环到主反应器。这样可以减少剩余污泥的产生。我们研究了 MBR 和侧流缺氧反应器之间的污泥交换率对 MBR 中污泥产率降低的影响。两个 MBR,即 MBR 和 MBR,分别与单独的外部缺氧侧流反应器相连接,平行运行了 350 天。与 MBR 不同,MBR 与连接的外部反应器进行了污泥交换。在调查污泥交换率(SIR)范围为 0-22%的过程中,SIR 为 11%时达到了最高的污泥减少(58%)。在 SIR 为 11%时,挥发性固体的破坏(即细菌细胞裂解和细胞外聚合物物质(EPS)的破坏)更大,这有助于实现最高的污泥减少。通过外部缺氧反应器中营养物质的释放可以明显看出挥发性固体的破坏增强。可以确认,在不影响废水处理质量、污泥沉降性和 MBR 中膜的水力性能的情况下,实现了污泥产率的降低。