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Abstract The optimization of membrane bioreactor (MBR) systems is a critical challenge in mitigating membrane fouling. To overcome this issue, a two-phase experimental–computational approach was applied to evaluate the effect of the distance between the aeration pipe and the membrane module on antifouling performance. In the first phase, flat-sheet membranes were fabricated by the NIPS (Non-solvent Induced Phase Separation) method and characterized by field emission scanning electron microscopy (FESEM), pure water flux (PWF), and contact angle measurements. Among the prepared membranes, M2 membrane exhibited the highest PWF of 134 L·m⁻ ²·h⁻ ¹, the lowest contact angle of 80.0°, and a more favourable pore size distribution. In the second phase, a computational fluid dynamics (CFD) model was developed to simulate the hydrodynamic conditions around the selected membranes (M2). Increasing the distance improved the uniformity of shear stress distribution across the membrane surfaces. D2 = 60 mm was identified as optimal, as it allowed the system to utilize its full filtration potential while experiencing lower surface friction, thereby reducing fouling. D2 = 60 mm results in the lowest average shear stress (~0.30 Pa), provides the most balanced stress regime, minimizing localized abrasion while maintaining sufficient shear for antifouling, and thereby supporting longer membrane lifespan. Key words: Membrane, CFD, MBR, Fouling.
References [1] P. Krzeminski, L. Leverette, S. Malamis and E. Katsou, “Membrane bioreactors – a review on recent developments in [2] F. Meng, S. Zhang, Y. Oh, Z. Zhou, H. S. Shin and S. R. Chae, “Fouling in membrane bioreactors: an updated review”, [3] M. Wu, Y. Chen, H. Lin, L. Zhao, L. Shen, R. Li, Y. Xu, H. Hong and Y. He, “Membrane fouling caused by biological [4] M. Wu, M. Zhang, L. Shen, X. Wang, D. Ying, H. Lin, R. Li, Y. Xu and H. Hong, “High propensity of membrane fouling [5] M. Yang, D. Yu, M. Liu, L. Zheng, X. Zheng, Y. Wei, F. Wang and Y. Fan, “Optimization of MBR hydrodynamics for [6] T. J. Rector, J. L. Garland and S. O. Starr, “Dispersion characteristics of a rotating hollow fiber membrane bioreactor: [7] K. Xiao, S. Liang, X. Wang, C. Chen and X. Huang, “Current state and challenges of full-scale membrane bioreactor [8] R. W. Samstag, J. J. Ducoste, A. Griborio, I. Nopens, D. J. Batstone, J. D. Wicks, S. Saunders, E. A. Wicklein, G. Kenny and J. Laurent, “CFD for wastewater treatment: an overview”, Water Science Technology (2016). Vol. 74, pp. 549-563. [9] X. Guo, Y. Wang, H. Zhang, P. Li and C. Ma, “Numerical and experimental investigation for cleaning process of [10] Y. Shi, Z. Wang, X. Du, B. Gong, V. Jegatheesan and I. U. Haq, “Recent advances in the prediction of fouling in [11] S. J. Poormohamadian, H. Koolivand, M. Koolivand-Salooki and M. Esfandyari, “Numerical modeling of wastewater [12] M. Bulgarini, A. Della Torre and A. Baricci, “Computational Fluid Dynamic Investigation of Local Flow-Field Conditions in Lab Polymer Electrolyte Membrane Fuel Cells to Identify Degradation Stressors and Performance [13] M. Yang, Y. Wei, X. Zheng, F. Wang, X. Yuan, J. Liu, N. Luo, R. Xu, D. Yu and Y. Fan, “Hydraulic optimization of [14] N. V. Ndinisa, A. G. Fane, D. E. Wiley, D. F. Fletcher, “Fouling Control in a Submerged Flat Sheet Membrane System: Part II—TwoPhase Flow Characterization and CFD Simulations”, Separation Science and Technology (2006). Vol. 41, pp. 1411-1445. [15] M. Brannock, Y. Wang and G. Leslie, “Mixing characterisation of full-scale membrane bioreactors: CFD modelling with experimental validation”, Water Research (2010). Vol. 44, pp. 3181-3191. [16] M. Brannock, G. Leslie, Y. Wang and S. Buetehorn, “Optimising mixing and nutrient removal in membrane bioreactors: CFD modelling and experimental validation”, Desalination (2010). Vol. 250, pp. 815-818. [17] S. M. Mohan, S. Nagalakshmi, “A review on aerobic selfforming dynamic membrane bioreactor: formation, performance, fouling and cleaning”, Journal of Water Process Engineering (2020). Vol. 37, 101541. [18] S. Zhang, K. Yang, W. Liu, Y. Xu, S. Hei, J. Zhang, C. Chen, X. Zhu, P. Liang, X. Zhang, X. Huang, “Understanding the mechanism of membrane fouling suppression in electroanaerobic membrane bioreactor”, Chemical Engineering Journal (2021). Vol. 418, 129384. [19] B. Wang, K. S. Zhang and R. W. Field, “Novel aeration of a large-scale flat sheet MBR: a CFD and experimental [20] B. Wang, Y. Zhang, Y. Fang, K. Zhang and R. W. Field, “Aeration pipe design for free bubbling hydrodynamic [21] Q. Wu, X. Yan, K. Xiao, J. Guan, T. Li, P. Liang and X. Huang, “Optimization of membrane unit location in a full-scale [22] F. Cortés-Juan, B. Balannec and T. Renouard, “CFDassisted design improvement of a bench-scale nanofiltration [23] S. Khakpour, Y. Jafarzadeh and R. Yegani, “Incorporation of graphene oxide/nanodiamond nanocomposite into PVC ultrafiltration membranes”, Chemical Engineering Research and Design (2019). Vol. 150, pp. 60-70. [24] M. Sayadi, S. Khakpour, Y. Jafarzadeh, “Effects of PMMAPEG Copolymer on the Structure and Performance of PVC Membranes for Oily Wastewater Treatment”, International Journal of Chemical Engineering (2025). 8183253. |
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