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中空纤维膜极化系数影响因素分析

耿雷铭 张瑞华 刘卫华

耿雷铭, 张瑞华, 刘卫华. 中空纤维膜极化系数影响因素分析[J]. 航空动力学报, 2025, 40(3):20220087 doi: 10.13224/j.cnki.jasp.20220087
引用本文: 耿雷铭, 张瑞华, 刘卫华. 中空纤维膜极化系数影响因素分析[J]. 航空动力学报, 2025, 40(3):20220087 doi: 10.13224/j.cnki.jasp.20220087
GENG Leiming, ZHANG Ruihua, LIU Weihua. Influencing factors of polarization coefficient of hollow fiber membrane[J]. Journal of Aerospace Power, 2025, 40(3):20220087 doi: 10.13224/j.cnki.jasp.20220087
Citation: GENG Leiming, ZHANG Ruihua, LIU Weihua. Influencing factors of polarization coefficient of hollow fiber membrane[J]. Journal of Aerospace Power, 2025, 40(3):20220087 doi: 10.13224/j.cnki.jasp.20220087

中空纤维膜极化系数影响因素分析

doi: 10.13224/j.cnki.jasp.20220087
基金项目: 国家自然科学基金民航联合基金(U1933121); 江苏省科研与实践创新计划(KYCX19_0198); 中央高校基本科研业务费专项资金(NC2020001); 江苏高校优势学科建设工程
详细信息
    作者简介:

    耿雷铭(1987-),男,高级工程师,博士生,主要从事运输类飞机适航技术研究。E-mail:fredgeng@163.com

    通讯作者:

    刘卫华(1965-),男,教授,博士,主要从事飞行器环境与生命保障工程、飞行器燃油系统研究。E-mail:liuwh@nuaa.edu.cn

  • 中图分类号: V217;TQ138

Influencing factors of polarization coefficient of hollow fiber membrane

  • 摘要:

    以氧氮分离为研究对象,通过建立中空纤维膜气体分离数学模型,分析丝内外压差、进气初始氧体积分数、进气流量、丝外侧背压等参数对极化系数的影响,以探究操作参数对浓差极化影响程度,并提出降低浓差极化技术方案。研究表明:在考虑丝内压降、浓差极化现象的情况下,所建立的中空纤维膜气体分离数学模型具有一定的可信度;丝内外压差、进气初始氧体积分数、进气流量、丝外侧背压等因素对极化系数有一定影响,其中极化系数与丝内外压差、进气初始氧体积分数、丝外侧背压呈正相关,与进气流量呈负相关;可采用渗透侧负压抽吸方式提高膜透过流量、降低浓差极化。

     

  • 图 1  中空纤维膜内部流型示意图

    Figure 1.  Schematic diagram of internal current models of hollow fiber membrane

    图 2  氧分压在膜组件截面轴向的分布

    Figure 2.  Axial distribution of oxygen partial pressure in the section of membrane module

    图 3  计算值与实测值对比结果

    Figure 3.  Comparison results of calculated values and measured values

    图 4  浓差极化系数随膜内外压差的变化规律

    Figure 4.  Variation of concentration polarization coefficient with the pressure difference inside and outside the filament

    图 5  浓差极化系数随组分1初始进气体体积分数的变化

    Figure 5.  Variation of concentration polarization coefficient with the initial intake concentration of component 1

    图 6  浓差极化系数随原料气流量的变化规律

    Figure 6.  Variation of concentration polarization coefficient with the feed gas flow rate

    图 7  浓差极化系数随丝外侧背压的变化规律

    Figure 7.  Variation of concentration polarization coefficient with the inlet pressure in filament

    表  1  实验数据与微分数学模型计算结果对比

    Table  1.   Comparison of experimental data with calculated results of differential mathematical model

    序号 操作条件 xl/%
    pi/105 Pa T/K ul/(kg/h) x0/% 实验值 计算值1 计算值2
    1 4 303.15 20 21 7.63 7.52 8.04
    2 4 323.15 20 21 6.78 6.75 7.21
    3 4 343.15 20 21 6.26 6.20 6.63
    4 4 363.15 20 21 6.05 6.01 6.42
    5 4 383.15 20 21 5.83 5.84 6.24
    6 6 303.15 20 21 5.34 5.31 5.74
    7 6 323.15 20 21 4.35 4.30 4.64
    8 6 343.15 20 21 4.00 3.95 4.25
    9 6 363.15 20 21 3.95 3.87 4.17
    10 6 383.15 20 21 4.16 4.12 4.45
    注:计算值1为考虑浓差极化的情况,计算值2为不考虑浓差极化的情况。
    下载: 导出CSV
  • [1] 罗鸣. 膜技术在气体分离中的应用[J]. 大众标准化,2020(24): 184-185. LUO Ming. Application of membrane technology in gas separation[J]. Popular Standardization,2020(24): 184-185. (in Chinese doi: 10.3969/j.issn.1007-1350.2020.24.090

    LUO Ming. Application of membrane technology in gas separation[J]. Popular Standardization, 2020(24): 184-185. (in Chinese) doi: 10.3969/j.issn.1007-1350.2020.24.090
    [2] 刘庆祥,张文水. 气体膜技术研究进展[J]. 湖北农机化,2020(18): 71-72. LIU Qingxiang,ZHANG Wenshui. Research progress of gas membrane technology[J]. Hubei Agricultural Mechanization,2020(18): 71-72. (in Chinese

    LIU Qingxiang, ZHANG Wenshui. Research progress of gas membrane technology[J]. Hubei Agricultural Mechanization, 2020(18): 71-72. (in Chinese)
    [3] 张玲玲. 基于原位EIS技术的离子交换膜界面污染与浓差极化研究[D]. 天津: 天津工业大学,2020. ZHANG Lingling. Study on interface pollution and concentration polarization of ion exchange membrane based on in-situ EIS technology[D]. Tianjin: Tianjin Polytechnic University,2020. (in Chinese

    ZHANG Lingling. Study on interface pollution and concentration polarization of ion exchange membrane based on in-situ EIS technology[D]. Tianjin: Tianjin Polytechnic University, 2020. (in Chinese)
    [4] BANIASADI J,ZARGHAMI S,KAMELIAN F S,et al. Fabrication of asymmetric cellulose acetate/pluronic F-127 forward osmosis membrane: minimization of internal concentration polarization via control thickness and porosity[J]. Polymer Bulletin,2022,79(1): 569-586. doi: 10.1007/s00289-020-03514-8
    [5] TOSTO E,MARTINEZ-DIAZ D,SANZ R,et al. Systematic experimental assessment of concentration polarization and inhibition in Pd-based membranes for hydrogen purification[J]. Fuel Processing Technology,2021,213: 106661. doi: 10.1016/j.fuproc.2020.106661
    [6] COKER D T,FREEMAN B D,FLEMING G K. Modeling multicomponent gas separation using hollow-fiber membrane contactors[J]. AIChE Journal,1998,44(6): 1289-1302. doi: 10.1002/aic.690440607
    [7] WANG R,LIU S L,LIN T T,et al. Characterization of hollow fiber membranes in a permeator using binary gas mixtures[J]. Chemical Engineering Science,2002,57(6): 967-976. doi: 10.1016/S0009-2509(01)00435-3
    [8] 郑辉东,赵素英,王良恩. 用正交配置法求解中空纤维气体膜分离过程的数学模型[J]. 计算机与应用化学,2005,22(1): 69-72. ZHENG Huidong,ZHAO Suying,WANG Liang’en. Solving mathematical model of gas separation in hollow fiber membrane by orthogonal collocation[J]. Computers and Applied Chemistry,2005,22(1): 69-72. (in Chinese doi: 10.3969/j.issn.1001-4160.2005.01.013

    ZHENG Huidong, ZHAO Suying, WANG Liang’en. Solving mathematical model of gas separation in hollow fiber membrane by orthogonal collocation[J]. Computers and Applied Chemistry, 2005, 22(1): 69-72. (in Chinese) doi: 10.3969/j.issn.1001-4160.2005.01.013
    [9] BUCK F,FELDHOFF A,CARO J,et al. Permeation improvement of LCCF hollow fiber membranes by spinning and sintering optimization[J]. Separation and Purification Technology,2021,259: 118023. doi: 10.1016/j.seppur.2020.118023
    [10] HAN Yu,HUANG Xiao,LU Yin,et al. Study of intrinsic oxygen mass transfer characteristic and model on polypropylene hollow fiber membrane contactor[J]. International Communications in Heat and Mass Transfer,2021,121: 105045. doi: 10.1016/j.icheatmasstransfer.2020.105045
    [11] 陈庚. 膜吸收过程传质行为的模型化研究[D]. 北京: 北京化工大学,2009. CHEN Geng. Modeling study on the mass transfer behavior in membrane absorption process[D]. Beijing: Beijing University of Chemical Technology,2009. (in Chinese

    CHEN Geng. Modeling study on the mass transfer behavior in membrane absorption process[D]. Beijing: Beijing University of Chemical Technology, 2009. (in Chinese)
    [12] 李振兴,陈博, 梁才航. 流致振动条件下中空纤维膜的传热传质特性[J]. 工程热物理, 2023, 44(9): 2496-2503. LI Zhenxing, CHEN Bo, LIANG Caihang. Heat and mass transfer characteristics of hollow fiber membrane under flow-inducted vibration[J]. Journal of engineering thermophysics, 2023, 44(9): 2496-2503. (in Chinese

    LI Zhenxing, CHEN Bo, LIANG Caihang. Heat and mass transfer characteristics of hollow fiber membrane under flow-inducted vibration[J]. Journal of engineering thermophysics, 2023, 44(9): 2496-2503. (in Chinese)
    [13] 穆思图,樊慧菊,韩秉均. 中空纤维膜的膜污染过程及数学模型研究进展[J]. 膜科学与技术,2018,28(1): 114-121. MU Situ,FAN Huiju,HAN Bingjun. Review of membrane fouling stages and mathematical models for hollow fiber membrane[J]. Membrane science and technology,2018,28(1): 114-121. (in Chinese

    MU Situ, FAN Huiju, HAN Bingjun. Review of membrane fouling stages and mathematical models for hollow fiber membrane[J]. Membrane science and technology, 2018, 28(1): 114-121. (in Chinese)
    [14] 张彤,林晓峰,姚懿娟,等. 浓差极化对正渗透膜通量影响研究[J]. 山东化工,2017,46(12): 7-11. ZHANG Tong,LIN Xiaofeng,YAO Yijuan,et al. Influence of concentrative and dilutive internal concentration polarization on flux behavior in forward osmosis[J]. Shandong Chemical Industry,2017,46(12): 7-11. (in Chinese doi: 10.3969/j.issn.1008-021X.2017.12.003

    ZHANG Tong, LIN Xiaofeng, YAO Yijuan, et al. Influence of concentrative and dilutive internal concentration polarization on flux behavior in forward osmosis[J]. Shandong Chemical Industry, 2017, 46(12): 7-11. (in Chinese) doi: 10.3969/j.issn.1008-021X.2017.12.003
    [15] BRYLL A,ŚLĘZAK A. The mathematical model of concentration polarization coefficient in membrane transport and volume flows[J]. Journal of Biological Physics,2017,43(1): 31-44. doi: 10.1007/s10867-016-9432-5
    [16] 侯京伟,彭述明,胡胜,等. 钯膜分离氢氦过程中浓差极化现象[J]. 强激光与粒子束,2015,27(1): 16015. HOU Jingwei,PENG Shuming,HU Sheng,et al. Concentration polarization in Pd-based membrane for the separation of H2/He[J]. High Power Laser and Particle Beams,2015,27(1): 16015. (in Chinese doi: 10.3788/HPLPB20152701.16015

    HOU Jingwei, PENG Shuming, HU Sheng, et al. Concentration polarization in Pd-based membrane for the separation of H2/He[J]. High Power Laser and Particle Beams, 2015, 27(1): 16015. (in Chinese) doi: 10.3788/HPLPB20152701.16015
    [17] 蔡琰,林贵平,曾宇,等. 中空纤维膜机载制氮装置的数学建模分析[J]. 航空动力学报,2015,30(9): 2100-2107. CAI Yan,LIN Guiping,ZENG Yu,et al. Mathematical modeling analysis of hollow fiber membrane onboard inert gas generation system[J]. Journal of Aerospace Power,2015,30(9): 2100-2107. (in Chinese

    CAI Yan, LIN Guiping, ZENG Yu, et al. Mathematical modeling analysis of hollow fiber membrane onboard inert gas generation system[J]. Journal of Aerospace Power, 2015, 30(9): 2100-2107. (in Chinese)
    [18] 贺高红,徐仁贤,朱葆琳. 中空纤维膜气体分离器的数学模型[J]. 化工学报,1994,45(2): 162-167. HE Gaohong,XU Renxian,ZHU Baolin. Mathematical model for hollow fiber membrane gas separator[J]. CIESC Journal,1994,45(2): 162-167. (in Chinese

    HE Gaohong, XU Renxian, ZHU Baolin. Mathematical model for hollow fiber membrane gas separator[J]. CIESC Journal, 1994, 45(2): 162-167. (in Chinese)
    [19] CARAVELLA A,BARBIERI G,DRIOLI E. Concentration polarization analysis in self-supported Pd-based membranes[J]. Separation and Purification Technology,2009,66(3): 613-624.
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  • 收稿日期:  2022-02-25
  • 网络出版日期:  2024-12-04

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