Fujian Provincial Engineering Research Center of Rural Waste Recycling Technology, College of Environment and Safety Engineering, Fuzhou University, Fujian 350116, China.
Fujian Provincial Engineering Research Center of Rural Waste Recycling Technology, College of Environment and Safety Engineering, Fuzhou University, Fujian 350116, China.
Water Res. 2022 Jul 15;220:118665. doi: 10.1016/j.watres.2022.118665. Epub 2022 May 25.
Integrating anammox with denitrifying anaerobic methane oxidation (DAMO) in the membrane biofilm reactor (MBfR) is a promising technology capable of achieving complete nitrogen removal from wastewater. However, it remains unknown whether reactor configurations featuring longitudinal gradients parallel to the membrane surface would affect the performance of the CH-driven MBfR. To this end, this work aims to study the impacts of longitudinal heterogeneity potentially present in the gas and liquid phases on a representative CH-driven MBfR performing anammox/DAMO by applying the reported modified compartmental modeling approach. Through comparing the modeling results of different reactor configurations, this work not only offered important guidance for better design, operation and monitoring of the CH-driven MBfR, but also revealed important implications for prospective related modeling research. The total nitrogen removal efficiency of the MBfR at non-excessive CH supply (e.g., surface loading of ≤0.064 g-COD m d in this work) was found to be insensitive to both longitudinal gradients in the liquid and gas phases. Comparatively, the longitudinal gradient in the liquid phase led to distinct longitudinal biomass stratification and therefore played an influential role in the effective CH utilization efficiency, which was also related to the extent of reactor compartmentation considered in modeling. When supplied with non-excessive CH, the MBfR is recommended to be designed/operated with both the biofilm reactor and the membrane lumen as plug flow reactors (PFRs) with co-current flow of wastewater and CH, which could mitigate dissolved CH discharge in the effluent. For the reactor configurations with the biofilm reactor designed/operated as a PFR, multi-spot sampling in the longitudinal direction is needed to obtain a correct representation of the microbial composition of the MBfR.
将厌氧氨氧化与反硝化厌氧甲烷氧化(DAMO)集成到膜生物膜反应器(MBfR)中是一项很有前途的技术,能够实现废水中的完全脱氮。然而,目前尚不清楚平行于膜表面的纵向梯度的反应器构型是否会影响 CH 驱动的 MBfR 的性能。为此,本工作旨在通过应用报告的改进分区建模方法,研究气相和液相中可能存在的纵向非均质性对代表性 CH 驱动的 MBfR 进行厌氧氨氧化/DAMO 的影响。通过比较不同反应器构型的建模结果,本工作不仅为更好地设计、操作和监测 CH 驱动的 MBfR 提供了重要指导,而且对未来相关建模研究也具有重要意义。在 CH 供应不过量的情况下(例如,在本工作中,表面负荷≤0.064 g-COD m d),MBfR 的总氮去除效率对液相和气相中的纵向梯度均不敏感。相比之下,液相中的纵向梯度导致明显的纵向生物量分层,因此对有效 CH 利用效率有影响,这也与建模中考虑的反应器分区程度有关。在供应不过量的 CH 时,建议将 MBfR 设计/操作成生物膜反应器和膜内腔均为废水和 CH 同向流动的推流反应器(PFR),这可以减轻出水中溶解 CH 的排放。对于生物膜反应器设计/操作成 PFR 的反应器构型,需要进行纵向多点采样,以正确表示 MBfR 的微生物组成。