欢迎登录材料期刊网

材料期刊网

高级检索

简述了全氟磺酸离子交换膜(PFSIEM)的分子结构和微观结构模型,特别是全氟磺酸离子交换树脂(PFSIER)的三相结构、"三明治"模型及"离子簇网络结构"模型等;重点论述了PFSIEM在氯碱电解、燃料电池、渗透汽化、气体分离及光催化等领域中的应用和研究进展;提出了PFSIEM应用与研究开发的方向.

参考文献

[1] Conolly D J;Longwood;Gresham W F et al.Fluorocarbon vinyl ether polymers[P].US 3282875,1966-11-01.
[2] Carla H W .Recent advances in perfluorinated ionmomer membranes:structure,properties and applications[J].Journal of Membrane Science,1996,120:1-33.
[3] Haubold H G;Vad T;Jungbluth H et al.Nano structure of NAFION:A SAXS study[J].Electrochimica Acta,2001,46:1559-1563.
[4] Gierke T D;Munn G E;Wilson F C et al.The morphology in Nafion perfluorinate membrane product,as determined by wide-and small-angle X-ray studies[J].Journal of Polymer Science Part A:Polymer Chemistry,1981,19:1687-1704.
[5] Lee E M;Thomas R K;Burgess A et al.Local and long-range structure of water in a perfluorinated ionomer membrane[J].Macromolecules,1992,25(12):3106-3109.
[6] Gebel G.;Lambard J. .SMALL-ANGLE SCATTERING STUDY OF WATER-SWOLLEN PERFLUORINATED IONOMER MEMBRANES[J].Macromolecules,1997(25):7914-7920.
[7] Veroni Barbi;Sergio S. Funari;Rainer Gehrke;Nico Scharnagl;Norbert Stribeck .Nanostructure of Nafion membrane material as a function of mechanical load studied by SAXS[J].Polymer: The International Journal for the Science and Technology of Polymers,2003(17):4853-4861.
[8] 王国柱 .离子膜的性能及使用寿命[J].氯碱化工,1994,2:8-10.
[9] 时均;袁权;高从堦.膜技术手册[M].北京:化学工业出版社,2001
[10] 方度;杨维驿.全氟离子交换膜--制法、性能及应用[M].北京:化学工业出版社,1993:114-119.
[11] 王伟红,邢家悟.离子交换膜技术在氯碱行业的应用与发展[J].膜科学与技术,2002(06):54-57,64.
[12] Smit M A;Ocampo A L;Espinosa-Medina M A et al.A modified Nafion membrane with in situ polymerizedpolypyrrole for the DMFC[J].Journal of Power Sources,2003,124:59-64.
[13] Z.Q. Ma;P. Cheng;T.S. Zhao .A palladium-alloy deposited Nafion membrane for direct methanol fuel cells[J].Journal of Membrane Science,2003(1/2):327-336.
[14] Shao Z G;Wang X .Composite Nafion/PVA membranes for the direct methanol fuel cell[J].Journal of Membrane Science,2002,210:147-153.
[15] Yang C;Costamagna P;Srinicasan S et al.Approaches and technical challenges to high temperature operation of proton exchange membrane fuel cell[J].Journal of Power Sources,2001,103:1-9.
[16] P. Costamagna;C. Yang;A. B. Bocarsly;S. Srinivasan .Nafion 115/zirconium phosphate composite membranes for operation of PEMFCs above 100 ℃[J].Electrochimica Acta,2002(7):1023-1033.
[17] Yang C;Srinicasan S;Arico A S et al.Composite nafion/zirconium phosphate membranes for direct methanol fuel cell operation at high temperature[J].Electrochemical and Solid-State Letters,2001,4(04):A31.
[18] Scott Sportsman K;Dovglas Way J;Chen Wen-Jang et al.The dehydration of nitric acid using pervaporation and a nafion perfluorosulfonate/perfluorocaboxylate bilayer membrane[J].Journal of Membrane Science,2002,203:155-166.
[19] Ray SK.;Joshi JB.;Pangarkar VG.;Sawant SB. .Dehydration of acetic acid by pervaporation[J].Journal of Membrane Science,1998(1):1-17.
[20] Samuel P;Kusumocahyo;Masao Sudoh .Dehydration of acetic acid by pervaporation with charged membrane[J].Journal of Membrane Science,1999,161:77-83.
[21] Jiang JS.;Fried JR.;Greenberg DB. .PERVAPORATION OF METHANOL FROM A TRIGLYME SOLUTION USING A NAFION MEMBRANE .1. TRANSPORT STUDIES[J].Journal of Membrane Science,1997(2):255-262.
[22] Jiang JS.;Fried JR.;Greenberg DB. .PERVAPORATION OF METHANOL FROM A TRIGLYME SOLUTION USING A NAFION MEMBRANE .2. CONCENTRATION POLARIZATION[J].Journal of Membrane Science,1997(2):263-271.
[23] Sumin Tanya Kao;Fengjan Joshua Wang;Shingjiang Jessie Lue .Sorption, diffusion, and pervaporation of benzene/cyclohexane mixtures on silver-Nafion membranes[J].Desalination: The International Journal on the Science and Technology of Desalting and Water Purification,2002(1/3):35-40.
[24] Sunget A;Way J D;Thoen P M et al.Reactive polymer membrane for ethylene/ethane separation[J].Journal of Membrane Science,1997,36:111-120.
[25] Takeo Yamaguchi;Chelsey Baertsch;Carl A. Koval;Richard D. Noble;Christopher N. Bowman .Olefin separation using silver impregnated ion-exchange membranes and silver salt/polymer blend membranes[J].Journal of Membrane Science,1996(1/2):151-161.
[26] Tricoli V.;Cussler EL. .AMMONIA SELECTIVE HOLLOW FIBERS[J].Journal of Membrane Science,1995(1/2):19-26.
[27] Yamaguchi T.;Noble RD.;Bowman CN.;Koval CA. .TRANSPORT MECHANISM OF CARBON DIOXIDE THROUGH PERFLUOROSULFONATE IONOMER MEMBRANES CONTAINING AN AMINE CARRIER[J].Chemical Engineering Science,1996(21):4781-4789.
[28] Way J D;Noble R D .Competitive facilitated transport of acid gases in perfluorosulfonic acid membrane[J].Journal of Membrane Science,1989,46:309-324.
[29] 韩世同,习海玲,史瑞雪,付贤智,王绪绪.半导体光催化研究进展与展望[J].化学物理学报,2003(05):339-349.
[30] Lund E A;Blatt E;Furlong D et al.The selective photocatalytic oxidation of m-phenoxytoluene on titanium dioxide particals supported in Nafion membranes[J].Austral J Den,1989,42(08):1367-1373.
[31] Miyoshi H;Tanaka K;Uchida H et al.Photoelectrochemical properties of iron oxide(Fe2O3) microcrystallites prepared in Nafion[J].Journal of Electroanalytical Chemistry and Interfacial Electrochemistry,1990,295(1-2):1-78.
[32] Fernandez J;Bandara J;Lopez A et al.Photoassisted Fenton degradation of nonbiodegradable azo dye (Orange Ⅱ) in Fe-free solutions mediated by cation transfer membranes[J].Langmuir,1999,15(01):185-192.
[33] Mugnthu R D;John K;Peter A et al.Photo-assisted immobilized fenton degradation up to pH8 of azo dye orange Ⅱ mediated by Fe3+/nafion/glass fibers[J].Helvetica Chimica Acta,2001,84:3433-3445.
[34] Premknmar J;Ramaraj R .Photocatalytic reduction of carbon dioxide to formic acid at porphyrin and phthalocyanine adsorbed Nafion membranes[J].Journal of Photochemistry and Photobiology A:Chemistry,1997,110:53-58.
[35] Premknmar J;Ramaraj R .Photocatalytic reduction of dioxygen to hydrogen peroxide at porphyrin and phthalocyanine adsorbed Nafion membranes[J].Journal of Molecular Catalysis A:Chemical,1999,142:153-162.
[36] 刘平,SUN Ya-ping,付贤智,王绪绪,李旦振.Nafion薄膜中单分散TiO2纳米晶体的合成[J].无机化学学报,2003(04):350-354.
上一张 下一张
上一张 下一张
计量
  • 下载量()
  • 访问量()
文章评分
  • 您的评分:
  • 1
    0%
  • 2
    0%
  • 3
    0%
  • 4
    0%
  • 5
    0%