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

被引:3
|
作者
Wang, Zhidong [1 ]
Su, Kuizu [1 ]
Shu, Tong [1 ]
Wang, Weihong [2 ]
机构
[1] Hefei Univ Technol, Dept Civil Engn, Hefei 230009, Anhui, Peoples R China
[2] Xinjiang Agr Univ, Coll Hydraul & Civil Engn, Urumqi 830091, Peoples R China
基金
中国国家自然科学基金;
关键词
computational fluid dynamics; membrane bioreactors; membrane fouling; particle packed structure; porosity; CROSS-FLOW FILTRATION; PACKING DENSITY; WATER TREATMENT; FLUID-FLOW; CAKE; MODEL; DEPOSITION; RESISTANCE; MICROFILTRATION; PERMEABILITY;
D O I
10.2166/wst.2017.426
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
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.
引用
收藏
页码:2503 / 2514
页数:12
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