Position:Home >> Abstract

Fluid dynamics of tubular membrane filtration process based on CFD
Authors: DU Yuhong1,FENG Qiyin1,LIU Enhua2,GENG Donghan1
Units: Tianjin Polytechnic University 1 School of Mechanical Engineering, Tianjin Key Laboratory of Advanced Electromechanical Equipment Technology; 2 School of Material Science and Engineering, State Key Laboratory of Hollow Fiber Membrane Materials and Processes; TianJin,300387,China
KeyWords: tubular membrane ; Fluid dynamics ; CFD
ClassificationCode:TQ028.8
year,volume(issue):pagination: 2016,36(1):72-80

Abstract:
 Using the method of CFD numberical calculation,tubular membrane fluid dynamics analysis was carried out under 80kpa constant pressure different flow rates by darcy’s law and k-ω SST model, reveals its internal flow rule, after experimental verification, simulation results are in good agreement with the experimental value. The analysis shows that, when flow rate increases,the wash on membrane wall surface is stronger, vortex disturbance is more intense, seepage flow is greater, transmembrane pressure difference is bigger.In the membrane tube the pressure decreases linearly with the increase of the axial distance, the slope of the linear decrease k decreases with the increase of Q (L/H), conform to the relationship of  k=-0.0125Q.

Funds:
国家高技术研究发展计划(863计划)项目(2012AA03A602);国家自然科学青年基金项目(51205288);天津市科委面上基金项目(13jcybjc15900)

AuthorIntro:
作者简介:杜玉红(1974—),女,副教授,黑龙江人,主要从事CFD数值模拟方面的研究。E-mail:duyuhong@tjpu.Edu.cn

Reference:
[1] Polyakov Y S.. Deadend outside-in hollow fiber membrane filter: Mathematical model[J]. Journal of Membrane Science,2006,279(1):615-624. 
[2] Vargas A. Controlled backwashing in a membrane sequencing batch reactor used for toxic wastewater treatment[J]. Journal of Membrane Science,2008,320(1):185-190.
[3] Clech P L,Chen V, Fane T A G. Fouling in membrane bioreactors used in wastewater treatment[J]. Journal of Membrane Science,2006,284(1):17-53.
[4]Ghidossi R , Veyret D , Moulin P.computational fluid dynamics applied to membranes: State of the art and opportunities[J].Chemical Engineering and Processing,2006,45(6):437-454.
[5]Saber Ahmed,M. Taif Seraji,Jonaid Jahedi,et al. CFD simulation of turbulence promoters in a tubular membrane channel[J]. Desalination,2011,276(1):191-198.
[6]Saber Ahmed,M. Taif Seraji,Jonaid Jahedi,et al. Application of CFD for simulation of a baffled tubular membrane[J]. Chemical Engineering Research and Design,2012,90(5):600-608.
[7]Liu yuanfa,He gaohong,Liu xudong,et al. CFD simulations of turbulent flow in baffle-filled membrane tubes[J]. Separation and Purification Technology,2009,67(1):14-20.
[8]Pak A , Mohammadi T , Hosseinalipour S M, et al. CFD modeling of porous membranes[J]. Desalination,2006,222(1):482-488.
[9]黄维菊,陈文梅,魏星,徐俊光,沈亮. 旋转横向流膜器环隙压力测试系统的研究[J]. 机械工程学报,2003,04:116-119.
[10] Rahimi M, Madaeni S S , Abbasi K. CFD modeling of permeate flux in cross-flow microfiltration membrane[J]. Journal of Membrane Science,2005,255(1):23-31. 
[11]陶文亮,艾浩,韩敏,路勇.无机膜管气体除尘流场分布的数值模拟[J]. 膜科学与技术,2008,06:102-105.
[12]彭文博,漆虹,李卫星,邢卫红,徐南平. 陶瓷膜通道相互作用的实验分析及CFD优化[J]. 化工学报,2008,03:602-606.
[13]彭文博,漆虹,陈纲领,邹琳玲,邢卫红,徐南平. 19通道多孔陶瓷膜渗透过程的CFD模拟[J]. 化工学报,2007,08:2021-2026.
[14]刘恩华,杨丽. 管式膜过滤过程中的流体力学研究[J]. 天津工业大学学报,2013,06:1-8. 
[15]朱旭东. 湍流模型的比较、改进和应用[D].南京航空航天大学,2005:12-15.
[16]Menter F R. Two-equation eddy-viscosity turbulence models
for engineering applications[J]. AIAA Journal,1994,32( 8): 1598-1605.
[17]Menter F R,Kuntz M,Langtry R. Ten years of industrial experience with the SST turbulence model[J]. Turbulence,Heat and Mass Transfer,2003(4):625-632.
 

Service:
Download】【Collect

《膜科学与技术》编辑部 Address: Bluestar building, 19 east beisanhuan road, chaoyang district, Beijing; 100029 Postal code; Telephone:010-80492417/010-80485372; Fax:010-80485372 ; Email:mkxyjs@163.com

京公网安备11011302000819号