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材料研究学报  2014, Vol. 28 Issue (5): 353-361    DOI: 10.11901/1005.3093.2013.725
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聚全氟乙丙烯中空纤维膜制备及其膜蒸馏过程*
吴艳杰,肖长发(),黄庆林,陈凯凯
天津工业大学中空纤维膜材料与膜过程省部共建国家重点实验室培育基地 天津工业大学材料科学与工程学院 天津 300387
FEP Hollow Fiber Membrane and Its Membrane Distillation Process
Yanjie WU,Changfa XIAO(),Qinglin HUANG,Kaikai CHEN
Department of Materials Science and Engineering, Tianjin Polytechnic University, State Key Laboratory of Hollow Fiber Membrane Materials and Processes, Tianjin Polytechnic University, Tianjin 300387
引用本文:

吴艳杰,肖长发,黄庆林,陈凯凯. 聚全氟乙丙烯中空纤维膜制备及其膜蒸馏过程*[J]. 材料研究学报, 2014, 28(5): 353-361.
Yanjie WU, Changfa XIAO, Qinglin HUANG, Kaikai CHEN. FEP Hollow Fiber Membrane and Its Membrane Distillation Process[J]. Chinese Journal of Materials Research, 2014, 28(5): 353-361.

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摘要: 

以聚全氟乙丙烯(FEP)为成膜聚合物, 采用熔融纺丝-拉伸法制备FEP中空纤维膜, 研究了后拉伸倍数对FEP中空纤维膜结构与性能的影响。结果表明, 初生FEP中空纤维膜结构较为致密, 拉伸后出现微孔结构。随着拉伸倍数的提高膜的孔隙率和氮气通量明显增大, 而液体渗透压(LEP)有所降低。将所得FEP中空纤维膜用于减压膜蒸馏(VMD)研究, 并将其与常规熔融纺丝-拉伸法聚丙烯(PP)中空纤维膜比较。结果表明, 所得FEP中空纤维膜的疏水性能、液体渗透压力和力学强度均优于PP中空纤维膜。较强的疏水性能使其稳定运行而不被液体渗透, 脱盐率稳定在99%以上。同时, FEP中空纤维膜具有较大的内径(0.74 mm), 在保证较高脱盐率前提下可采用内压式减压膜蒸馏, 且真空膜蒸馏通量随着进料温度的升高显著增高。

关键词 有机高分子材料聚全氟乙丙烯(FEP)中空纤维膜聚丙烯(PP)膜蒸馏脱盐率    
Abstract

The influence of draw ratio on the structure and properties of poly(tetrafluoroethylene-co-hexafluoropropylene) (FEP) hollow fiber membrane which was fabricated by melt-spinning stretching (M-S) method was investigated in this article. The primary FEP hollow fiber membrane structure was compact while the porous structure occurs after stretching. Furthermore, the increase of membrane draw ratios induced the obvious increase of membrane porosity and the N2 flux while the decrease of the liquid entrance pressure (LEP). Meanwhile, the FEP hollow fiber membrane was applied to the vacuum membrane distillation (VMD) process to compared with M-S PP hollow fiber membrane which was the commercial product. The results show that the hydrophobic properties, LEP and mechanical strength of FEP hollow fiber membrane was better than PP hollow fiber membrane. The strong and stable of hydrophobic properties enabled the FEP membrane unpenetrated, which kept the desalination rate maintain up to 99%. The larger inner diameter (about 0.74 mm) of FEP hollow fiber membrane induced the use of internal pressure VMD type which brought about the higher VMD flux when the feed temperature increased.

Key wordsorganic polymer materials    poly(tetrafluoroethylene-co-hexafluoropropylene) (FEP)    hollow fiber membrane    polypropylene (PP)    membrane distillation    desalination rate
收稿日期: 2013-09-30     
基金资助:* 国家重点基础研究发展计划项目2012CB722706,国家自然科学基金20874073 和天津市应用基础与前沿技术研究计划重点项目12JCZDJC26600资助。
图1  FEP中空纤维膜纺丝流程图
Membrane FEP PP
Inner diameter/mm 0.74 0.23
Outer diameter/mm 1.31 0.45
The number of membrane 100 200
Effective length of components/m 0.18 0.24
Effective area of component/m2 0.042 0.068
表1  中空纤维膜结构参数
图2  中空纤维膜N2通量测试仪
图3  中空纤维膜液体渗透压测试流程图
图4  VMD装置流程图
LEP/MPa
First time Second time Third time Average value
50℃, 3 times stretch of FEP 0.40 0.39 0.37 0.39±0.015
70℃, 3 times stretch of FEP 0.35 0.37 0.35 0.36±0.012
90℃, 3 times stretch of FEP 0.33 0.35 0.33 0.34±0.012
90℃, 2 times stretch of FEP 0.35 0.35 0.36 0.36±0.006
90℃, 4 times stretch of FEP 0.32 0.33 0.33 0.33±0.006
表2  不同拉伸条件FEP膜的液体渗透压力
Membrane FEP PP
PWF/Lm-2h-1 6.78 82.30
The gas flux/m3m-2h-1 0.83 2.54
LEP/MPa 0.41 0.13
表3  PP和FEP中空纤维膜透过性能参数
Porosity/% Water Ethanol n-Butanol
FEP/Raw hollow fiber 12.74 14.68 36.18
FEP/Stretched 1.5 times 32.26 34.83 48.75
FEP/Stretched 1.9 times 16.16 34.48 38.20
PP 18.54 36.73 50.92
表4  FEP和PP中空纤维膜的孔隙率
图5  PP和FEP中空纤维膜静态接触角照片
图6  PP中空纤维膜的微观形貌
图7  FEP中空纤维膜的微观形貌
图8  不同拉伸倍数FEP中空纤维膜的表面形貌
图9  FEP中空纤维膜的应力-应变曲线
图10  PP中空纤维膜的应力-应变曲线
图11  水通量随时间的变化
图12  脱盐率随时间的变化
图13  温度对FEP中空纤维膜蒸馏通量的影响. 1-90℃, 2-80℃, 3-70℃, 4-60℃
图14  FEP组件在不同温度条件下的平均通量变化
图15  温度对FEP组件脱盐效果的影响
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