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The Performance and Spatial Distribution of Membrane Fouling in a Sequencing Batch Ceramic Membrane Bioreactor: A Pilot Study for Swine Wastewater Treatment

机译:序批陶瓷膜生物反应器中膜污染的性能和空间分布:猪废水处理的中试研究

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摘要

The extensive application of ceramic membranes in wastewater treatment draws increasing attention due to their ultra-long service life. A cost-effective treatment for high-strength swine wastewater is an urgent and current need that is a worldwide challenge. A pilot-scale sequencing batch flat-sheet ceramic membrane bioreactor (ScMBR) coupled with a short-cut biological nitrogen removal (SBNR) process was developed to treat high-strength swine wastewater. The ScMBR achieved stable and excellent removal of COD (95.3%), NH4+-N (98.3%), and TN (92.7%), though temperature went down from 20 °C, to 15 °C, to 10 °C stepwise along three operational phases. The COD and NH4+-N concentrations in the effluent met with the discharge standards (GB18596-2001). Microbial community diversity was high, and the genera Pseudomonas and Comamonas were dominant in denitritation, and Nitrosomonas was dominant in nitritation. Ceramic membrane modules of this pilot-scale reactor were separated into six layers (A, B, C, D, E, F) from top to bottom. The total filtration resistance of both the top and bottom membrane modules was relatively low, and the resistance of the middle ones was high. These results indicate that the spatial distribution of the membrane fouling degree was different, related to different aeration scour intensities demonstrated by computational fluid dynamics (CFD). The results prove that the membrane fouling mechanism can be attributed to the cake layer formation of the middle modules and pore blocking of the top and bottom modules, which mainly consist of protein and carbohydrates. Therefore, different cleaning measures should be adopted for membrane modules in different positions. In this study, the efficient treatment of swine wastewater shows that the ScMBR system could be applied to high-strength wastewater. Furthermore, the spatial distribution characteristics of membrane fouling contribute to cleaning strategy formulation for further full-scale MBR applications.
机译:陶瓷膜因其超长的使用寿命而在废水处理中的广泛应用越来越受到关注。对高浓度猪废水进行经济高效的处理是一项紧迫且当前的需求,也是全球面临的挑战。开发了一种中试规模测序分批平板陶瓷膜生物反应器 (ScMBR) 与快速生物脱氮 (SBNR) 工艺相结合,用于处理高强度猪废水。ScMBR 实现了稳定和出色的 COD (95.3%)、NH4+-N (98.3%) 和 TN (92.7%) 去除,尽管温度在三个操作阶段从 20 °C 逐步下降到 15 °C,再到 10 °C。出水中的 COD 和 NH4+-N 浓度符合排放标准 (GB18596-2001)。微微生物群落多样性高,假单胞菌属 (Pseudomonas) 和 Comamonas 属在反硝化作用中占优势,亚硝化单胞菌属 (Nitrosomonas) 在硝化作用中占优势。该中试规模反应器的陶瓷膜组件从上到下分为六层(A、B、C、D、E、F)。顶部和底部膜组件的总过滤阻力相对较低,而中间膜组件的总过滤阻力较高。这些结果表明,膜污染程度的空间分布不同,这与计算流体动力学 (CFD) 所证明的不同曝气冲刷强度有关。研究结果表明,膜污染机制可归因于中间模块的饼层形成和顶部和底部模块的孔隙堵塞,主要由蛋白质和碳水化合物组成。因此,对于不同位置的膜组件,应采取不同的清洗措施。本研究对猪废水的高效处理表明,ScMBR 系统可应用于高浓度废水。此外,膜污染的空间分布特性有助于进一步全面 MBR 应用的清洁策略制定。

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