Typical Heterotrophic and Autotrophic Nitrogen Removal Process Coupled with Membrane Bioreactor: Comparison of Fouling Behavior and Characterization

厌氧氨氧化菌 化学 膜污染 胞外聚合物 膜生物反应器 结垢 异养 挥发性悬浮物 缺氧水域 色谱法 生物反应器 自养 活性污泥 环境化学 氮气 污水处理 反硝化 生物化学 细菌 环境工程 有机化学 生物 工程类 遗传学 反硝化细菌 生物膜
作者
Qiushan Liu,Tong Zhou,Yuru Liu,Wenjun Wu,Yufei Wang,Guohan Liu,Na Wei,Guangshuo Yin,Jin Guo
出处
期刊:Membranes [Multidisciplinary Digital Publishing Institute]
卷期号:14 (10): 214-214
标识
DOI:10.3390/membranes14100214
摘要

There is limited research on the relationship between membrane fouling and microbial metabolites in the nitrogen removal process coupled with membrane bioreactors (MBRs). In this study, we compared anoxic-oxic (AO) and partial nitritation–anammox (PNA), which were selected as representative heterotrophic and autotrophic biological nitrogen removal–coupled MBR processes for their fouling behavior. At the same nitrogen loading rate of 100 mg/L and mixed liquor suspended solids (MLSS) concentration of 4000 mg/L, PNA-MBR exhibited more severe membrane fouling compared to AO-MBR, as evidenced by monitoring changes in transmembrane pressure (TMP). In the autotrophic nitrogen removal process, without added organic carbon, the supernatant of PNA-MBR had higher concentrations of protein, polysaccharides, and low-molecular-weight humic substances, leading to a rapid flux decline. Extracellular polymeric substances (EPS) extracted from suspended sludge and cake sludge in PNA-MBR also contributed to more severe membrane fouling than in AO-MBR. The EPS subfractions of PNA-MBR exhibited looser secondary structures in protein and stronger surface hydrophobicity, particularly in the cake sludge, which contained higher contents of humic substances with lower molecular weights. The higher abundances of Candidatus Brocadia and Chloroflexi in PNA-MBR could lead to the production of more hydrophobic organics and humic substances. Hydrophobic metabolism products as well as anammox bacteria were deposited on the hydrophobic membrane surface and formed serious fouling. Therefore, hydrophilic membrane modification is more urgently needed to mitigate membrane fouling when running PNA–MBR than AO–MBR.
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