膜科学与技术

位置：首页 >> 期刊内容阅读

基于受力分析调控微观流场优化平板膜组件抗污染性能

作者：刘正球，张立卿，杨镇豪，胡吉玉，张超

单位：济南大学土木建筑学院，济南，250022

关键词：受力分析，平板膜组件，微观流场，抗污染性能

DOI号：

分类号： TQ028.3，TQ028.3+8

出版年,卷(期):页码： 2022,42(2):110-116

摘要：

基于微观颗粒受力分析，结合“浅池沉淀理论”反向思维，建立了平板膜组件尺寸优化模型。通过计算流体力学（CFD）技术模拟膜组件微观流场，对平板膜组件进行了尺寸优选。并以城市污水典型污染物腐殖酸（HA）、海藻酸钠（SA）、牛血清蛋白（BSA）为研究对象，对膜组件的抗污染性能进行了试验研究。研究结果表明：当膜组件长宽高比例为40:30:1时，优化膜组件对HA、SA、BSA的比通量衰减率在2h内比原组件分别减小了14％、9.3％、7.9％，且污染膜阻力均小于原组件，采用受力分析优化膜组件可以在流场及污染控制中取得良好效果。

Based on the force analysis of micro-particles，the size optimization model of flat crossflow membrane module was established by combining the reverse idea of shallow tank sedimentation theory, and the size of flat membrane module was confirmed by using computational fluid dynamics (CFD) technology to simulate the micro-flow field. Humic acid (HA), sodium alginate (SA), and bovine serum albumin (BSA) were chosen as model foulants of effluent organic matter (EfOM) to investigate the antifouling performance of the membrane module experimentally. The results showed that when the ratio of length, width and height of the membrane module was 40:30:1, the flux decline rate of the optimized membrane module for HA, SA and BSA decreased by 14%, 9.3% and 7.9% respectively in two hours compared with the original module. The membrane fouling resistance was lower than that of the original module, indicating that the optimized membrane module using force analysis had a good effect on flow field and membrane fouling control.

基金项目：

国家自然科学基金项目(51408260)和绿色建筑西部国家重点实验室开放项目(LSKF201807）资助.

作者简介：

刘正球（1997年11月4日），男，江苏宿迁人，土木建筑学院研究生，主要从事膜分离相关工作，研究方向：纳滤膜抗污染相关研究

参考文献：

[1] Wu C-R, Xiao T-L. Biomimetic temperature-gated 2D cationic nanochannels for controllable osmotic power harvesting[J].Nano Energy,2020,76: 105113.
[2] Li R-J, Lou Y. Effects of surface morphology on alginate adhesion: Molecular insights into membrane fouling based on XDLVO and DFT analysis[J].Chemosphere,2019,233: 373-380.
[3] Zhang B, Tang H-L. Effect of pH on anionic polyacrylamide adhesion: New insights into membrane fouling based on XDLVO analysis[J].Journal of Molecular Liquids,2020,320: 114463.
[4] Gomez-Flores A, Solongo S K. Bubble−particle interactions with hydrodynamics, XDLVO theory, and surface roughness for flotation in an agitated tank using CFD simulations[J].Minerals Engineering,2020,152: 106368.
[5] Zhu Y-Y, Lu Y-Q. Super-hydrophobic F-TiO2@PP membranes with nano-scale “coral”-like synapses for waste oil recovery[J].Separation and Purification Technology,2021,267: 118579.
[6] Xu M-Y, Feng X-Q. MOF laminates functionalized polyamide self-cleaning membrane for advanced loose nanofiltration[J].Separation and Purification Technology,2021,275: 119150.
[7] Abdi S, Nasiri M. Fabrication of PES-based super-hydrophilic ultrafiltration membranes by combining hydrous ferric oxide particles and UV irradiation[J].Separation and Purification Technology,2021,259: 118132.
[8] Tang M, Christie K. Fabrication of a novel underwater-superoleophobic/hydrophobic composite membrane for robust anti-oil-fouling membrane distillation by the facile breath figures templating method[J].Journal of Membrane Science,2021,617: 118666.
[9] Harandi H B, Asadi A. Combined macroscopic and pore scale modeling of direct contact membrane distillation with micro-porous hydrophobic membranes[J].Desalination,2021,514: 115171.
[10] Shi Y-D, Hu Y. Optimized microporous structure of ePTFE membranes by controlling the particle size of PTFE fine powders for achieving high oil-water separation performances[J].Journal of Membrane Science,2021,629: 119294.
[11] Golubenko D. V., Yaroslavtsev A. B. Effect of current density, concentration of ternary electrolyte and type of cations on the monovalent selectivity of surface-sulfonated graft anion-exchange membranes: modelling and experiment[J].Journal of Membrane Science,2021,635: 119466.
[12] Qi J, Zhai Y-F. Effect of contaminant mixtures in air on proton exchange membrane fuel cell performance[J].Journal of Power Sources,2019,413: 86-97.
[13] Li K, Su Q. Aging of PVDF and PES ultrafiltration membranes by sodium hypochlorite: Effect of solution pH[J].Journal of Environmental Sciences,2021,104: 444-455.
[14] Zhao P-B, Yao B-W. Studies on the fouling behavior and cleaning method of pervaporation desalination membranes for reclamation of reverse osmosis concentrated water[J].Separation and Purification Technology,2021,274: 119034.
[15 ]Mehmood C. Tahir, Waheed H, et al. Photocatalytic quorum quenching: A new antifouling and in-situ membrane cleaning strategy for an external membrane bioreactor coupled to UASB[J].Journal of Environmental Chemical Engineering,2021,9(4): 105470.
[16] Menon S, Bansode K. Impact of cleaning agents on properties of tubular polyvinylidene fluoride (PVDF) membrane[J].Materials Today: Proceedings,2021,
[17] Darvishzadeh T, Bhattarai B. The critical pressure for microfiltration of oil-in-water emulsions using slotted-pore membranes[J].Journal of Membrane Science,2018,563: 610-616.
[18] Wu K, Sun W-C. Study of shear behavior of granular materials by 3D DEM simulation of the triaxial test in the membrane boundary condition[J].Advanced Powder Technology,2021,32(4): 1145-1156.
[19] Wang J-M, Jin Q-Q. Reducing the membrane fouling in cross-flow filtration using a facile fluidic oscillator[J].Separation and Purification Technology,2021,272: 118854.
[20] Nguyen T, Adha R S. Quantifying the influence of divalent cations mass transport on critical flux and organic fouling mechanism of forward osmosis membrane[J].Desalination,2021,512: 115146.
[21] Jing X-J, Yuan J-S. Concentrating and recycling of high-concentration printing and dyeing wastewater by a disc tube reverse osmosis-Fenton oxidation/low temperature crystallization process[J].Separation and Purification Technology,2021,266: 118583.
[22] Wu C-W, Li Q-B. Characteristics of organic matter removed from highly saline mature landfill leachate by an emergency disk tube-reverse osmosis treatment system[J].Chemosphere,2021,263: 128347.
[23] Zhang Z-W, Wu Y-H. Application of disk tube reverse osmosis in wastewater treatment: A review[J].Science of The Total Environment,2021,792: 148291.
[24] BAUDET K, KALE V, MIRZAKHANI M. Neutral heteroleptic lanthanide complexes for unravelling host-guest assemblies in organic solvents: The law of mass action revisited[J]. Inorg Chem, 2020,59(1): 62-75.
[25] ANDREW E. CHUBYKALO A E B P. The origin of the energy-momentum energy-momentum conservation law[J]. Annals of Physics, 2017,38: 384-389.
[26] 吴梓坚,余华荣,梁恒.应用前表面三维荧光表征有机膜污染物质的方法[J].哈尔滨工业大学学报,2019,51(2):22-26.
[27] 尚文涛. 纳滤过程浓差极化行为特征与LIF-PIV可视化表征研究[D]. 哈尔滨工业大学, 2016.
[28] Sreedhar I, Nahar T, Venugopal A, et al. Carbon capture by absorption-path covered and ahead[J]. Renewable and Sustainable Energy Reviews, 2017, 76: 1080-1107.
[29] Zhong M. Functional surface modification of PVDF membrane for chemical pulse cleaning[J].Journal of Membrane Science, 2017, 524 : 389-399.

服务与反馈：

【文章下载】【加入收藏】

《膜科学与技术》编辑部地址：北京市朝阳区北三环东路19号蓝星大厦邮政编码：100029 电话：010-64426130/64433466 传真：010-80485372邮箱：mkxyjs@163.com