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CFD simulation of gas-liquid-sludge three-phase flow in membrane bioreactor
Authors: LI HuiQiang, LIU Qiao, WANG Qing, XU Nong, DONG Qiang, DING AiQin, FAN Long
Units: 1 School of Energy, Materials and Chemical Engineering, Hefei University, 230601, Hefei 2Stage Key Laboratory of Biochemical Engineering, Institute of Process Engineering, Chinese Academy of Sciences, 100190, Beijing 3Nanjing Tech. University, State Key Laboratory of Materials-Oriented Chemical Engineering, 211816, Nanjing
KeyWords: gas-liquid-solid three-phase flow; computational fluid dynamics; membrane bioreactor; sludge sedimentation
ClassificationCode:TQ028.5, O359
year,volume(issue):pagination: 2023,43(2):138-149

Abstract:
  The gas-water-sludge three-phase flow in an aerated membrane bioreactor (MBR) is simulated using computational fluid dynamics software FLUENT. The activated sludge is treated as a single phase. Not only the flow and the distribution of gas in the reactor are obtained, but also the hydrodynamics and settling characteristic of sludge are presented. The possible area for sludge settling, i.e. the consequent membrane pollution area, is provided. Furthermore, the effects of aeration bubble diameter, aeration area, and aeration location on the flow and sludge sedimentation are investigated. Both the operation conditions and the reactor structure are optimized to minimize membrane pollution. In the simulated range, the potential to have membrane fouling is minimal when the distance between the aeration surface and the bottom of the membrane unit is 350 mm, the width of the simplified aeration surface is 2 mm, and the bubble diameter is between 4-6 mm. Since the data for gas-liquid-solid three-phase flow in MBR are scarce, the gas-liquid two-phase flow is simulated for the purpose of verification. The mixture of water and sludge is treated as one single liquid phase. The comparison of two-phase simulation with literature proved the reliability of the simulation method and results.

Funds:
安徽省重点研究和开发计划项目(2022a05020041);安徽省教育厅重点项目(KJ2021A1015,KJ2020A0669);中国科学院过程工程研究所生化国家重点实验室开放基金项目;南京工业大学材料化学工程国家重点实验室开放基金项目(KL21-04)。

AuthorIntro:
李会强(1996—),男,安徽霍邱人,硕士研究生,研究方向为计算流体力学。E-mail:lhqstu127@163.com

Reference:
 [1] Yusuf Z, Wahab N, Sahlan S. Fouling control strategy for submerged membrane bioreactor filtration processes using aeration airflow, backwash, and relaxation: a review[J]. Desalination and Water Treatment, 2016, 57(38):1-13.
[2] Chio C, Kim M, Yang E, et al. Effects of aeration on/off times and hydraulic retention times in an intermittently aerated membrane bioreactor[J]. Desalination and Water Treatment, 2016, 57(16):7574-7581.
[3] Wang Y, Pan X, Sheng G, et al. Development of an energy-saving anaerobic hybrid membrane bioreactors for 2-chlorophenol-contained wastewater treatment[J]. Chemosphere, 2015, 140:79-84.
[4] Qing Z, Rongle X, Xiang Z, et al. Simulation and optimization of airlift external circulation membrane bioreactor using computational fluid dynamics[J]. Water Science and Technology, 2014,69(9):1846-1852.
[5] Ndinisa N, Fane A, Wiley D, et al. Fouling Control in a Submerged Flat Sheet Membrane System: Part II—Two-Phase Flow Characterization and CFD Simulations[J]. Separation Science and Technology, 2006, 41(7):1411-1445.
[6] 林进, 沈浩, 景文珩. 气升式陶瓷膜过滤过程的气液两相流模拟[J]. 化工学报, 2016, 67(6):9.
[7] Brannock M, Wang Y, Leslie G. Mixing characterisation of full-scale membrane bioreactors: CFD modelling with experimental validation[J]. Water Research, 2010, 44(10): 3181-3191.
[8] Brannock M, Wever H, Wang Y, et al. Computational fluid dynamics simulations of MBRs: Inside submerged versus outside submerged membranes[J]. Desalination, 2009, 236(1/2/3): 244-251.
[9] Brannock M, Wang Y, Leslie G. Optimising mixing in full-scale MBRs: CFD modelling and validation[J].Water, 2008,35(2):114-115.
[10] Wu Q, Yan X, Xiao K, et al. Optimization of membrane unit location in a full-scale membrane bioreactor using computational fluid dynamics[J]. Bioresource Technology, 2018,249:402-409.
[11] Wang B, Zhang Y, Zhang G , et al. Innovation and optimization of aeration in free bubbling flat sheet MBRs[J]. Journal of Membrane Science, 2021,635: 119522.
[12] Cao Y , Gu B, Sonnenburg A , et al. CFD simulation of the aeration process and baffle influence in a full-scale commercial flat sheet module[J]. Water Science & Technology, 2020, 81(9): 2004-2010.
[13] 曹迎晨, Alexander S, Wilhelm U. MBR平板膜中气泡运动的水力特征的数值分析[J]. 环境工程学报, 2020, 14(2):9.
[14] Liu M, Yang M, Chen M,et al. Numerical optimization of membrane module design and operation for a full-scale submerged MBR by computational fluid dynamics.[J]. Bioresource Technology, 2018,269: 300-308.
[15] Bayat M, Mehrnia M R, Mostoufi N, et al. Investigating wastewater treatment in MBRs using computational fluid dynamics [J]. Journal of Environmental Studies, 2015, 41(1): 1-12.
[16] Kang C, Hua J, Lou J, et al, Bridging the gap between membrane bio-reactor (MBR) pilot and plant studies [J]. Journal of Membrane Science, 2008, 325: 861–871
[17] Amini E, Mehrnia M R, Mousavi S M, et al. Experimental study and computational fluid dynamics simulation of a full-scale membrane bioreactor for municipal wastewater treatment application [J]. Industrial & Engineering Chemistry Research, 2013, 52: 9930−9939
[18] 张鹏,吴志超,敖华军. 污泥的粘度与浓度,温度三者关系式的实验推导[J].环境污染治理技术与设备,2006, 7(3):72-74.
[19] Liu X, Wang Y, David W, et al. Numerical simulation of bubble induced shear in membrane bioreactors: Effects of mixed liquor rheology and membrane configuration[J]. Water Research,2015,75: 131-145.
[20] 严晓旭. 基于CFD的膜生物反应器膜池水力学特性及其优化研究[D].北京:清华大学,2018.
[21] Wang Y, Brannock M, Cox S, et al. CFD simulations of membrane filtration zone in a submerged hollow fibre membrane bioreactor using a porous media approach[J]. Journal of Membrane Science, 2010, 363(1/2):57-66.
[22] Ratkovich N, Chan C, Berube P, et al. Experimental study and CFD modelling of a two-phase slug flow for an airlift tubular membrane[J]. Chemical Engineering Science, 2009, 64(16):3576-3584.
[23] 张君,李秀芬,王新华,等.曝气强度对膜生物反应器运行特性的影响[J].环境化学,2012, 31(1):82-87.
[24] Jan G, Philippe S, Claire A, et al. A numerical approach to study the impact of packing density on fluid flow distribution in hollow fiber module[J]. Journal of Membrane Science,2010,348(1): 277-286.
[25] 王栋.曝气对平板式膜生物反应器膜污染控制及其机理研究[D].合肥:合肥工业大学,2014.
 

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