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Numerical simulation of filtration performance in submerged membrane bioreactors: effect of particle packed structure

机译:淹没膜生物反应器中过滤性能的数值模拟:颗粒填充结构的影响

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It is widely known that the accumulation of solid matter forming a cake layer on the membrane surface is one of the major limitations of the filtration performance in submerged membrane bioreactors (SMBR). This study is focused on the influence of the cake porosity of different particle microscopic packed structures on the filtration performance of hollow fiber systems. An integrated model based on the finite element method to simulate numerically the flow in an SMBR is presented. The model coupled the Navier-Stokes and Darcy Brinkman equations to simulate a complete filtration run. The cake growth took into consideration not only the deposition with local filtration velocity but also the effect of aeration scouring. A novel solution of mesh deformation was adopted to investigate transient cake growth along the fiber. Comparisons between simulations and experiments are in good agreement. The results show that a higher porosity particle packed structure causes non-uniform filtration and cake thickness but also higher permeate flux. Meanwhile, the proportion of cake resistance to total resistance increases with the decrease of porosity.
机译:众所周知,在膜表面上形成滤饼层的固体物质的积累是浸没膜生物反应器中过滤性能的主要限制之一(SMBR)。该研究专注于不同颗粒微观填充结构的蛋白质孔隙率对中空纤维系统过滤性能的影响。提出了一种基于有限元方法来模拟SMBR中的流量的集成模型。该模型耦合了Navier-Stokes和Darcy Brinkman方程来模拟完整的过滤运行。不仅考虑了局部过滤速度的沉积而且考虑了滤饼的增长,而且考虑了曝气液的影响。采用新型网眼变形溶液来研究沿纤维的瞬时滤饼生长。模拟与实验之间的比较很好。结果表明,较高的孔隙粒子填充结构导致非均匀的过滤和蛋糕厚度,但也具有更高的渗透助焊剂。同时,随着孔隙率的降低,滤饼对总阻力的比例增加。

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