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2015,119(45):25145 [15]Ito H,Maeda T,Nakano A,et al.Properties of Nafion membranes under PEM water electrolysis conditions.IntJ drogen Energ,2011,36(17):10527 [16]Battino R,Clever HL.The solubility of gases in liquids.Chem Rev,1966,66:395 [17]Mann R F,Amphlett JC,Peppley BA,et al.Henry's Law and the solubilities of reactant gases in the modelling of PEM fuel cells.J Power Sources,2006,161(2):768 [18]Wise D L,Houghton G.The diffusion coefficients of ten slightly soluble gases in water at 10-60 C.Chem Eng Sci. 1966,21(11:999 [19]Sakai T,Takenaka H,Wakabayashi N,et al.Gas Permeation Properties of Solid Polymer Electrolyte(SPE)Membranes. J Electrochem Soc.1985.132(6):1328 [20]Yoshitake M,Tamura M,Yoshida N,et al.Studies of Perfluorinated Ion Exchange Membranes for Polymer Electrolyte Fuel Cells.Denki Kagaku,1996,64(6):727 [21]Kocha S S,Yang J D,Yi J S.Characterization of gas crossover and its implications in PEM fue cells.Aiche J,2006. 52(5):1916 [22]Broka K,Ekdunge PJ.Oxygen and hydrogen permeation properties and water uptake of Nafion 117 membrane and recast film for PEM fuel cell.J App/Electrochem,1997,27(2):117 [23]Barbir F.PEM electrolysis for production of hydrogen from renewable energy sources.Sol Energy,2005,78:661 [24]Sakai T,Takenaka H,Torikai E.Gas Diffusion in the Dried and Hydrated Nafions.JElectrochem Soc,198,133(1):88 [25]Chiou JS,Paul DR.Gas permeation in a dry Nafion membrane.VndEng Chem Res,1988,27(11):2161 [26]Mohamed H F M,Ito K,Kobayashi Y,et al.Free volume and permeabilities of O2 and H2 in Nafion membranes for polymer electrolyte fuel cells.Polymer,2008,49(13-14):3091 [27]Schalenbach M,Michael A H,JeffT G,et al.Gas Permeation through Nafion.Part2:Resistor Network Model./Phys Chem C.2015.119(45):25156 [28]Trinke P,Bensmann B,Reichstein S,et al.Hydrogen Permeation in PEM Electrolyzer Cells Operated at Asymmetric Pressure Conditions.J Electrochem Soc.2016.163(11):F3164 [29]Fales JL,Vanderborgh N E,Stroeve P.The influence of channel geometry on ionic transport /Proceedings of the Symposium on Diaphragms.Separators,and lon-Exchange Membranes,1986:13 [30]Sellin R C.Mozet K.Menage A.et al Measuring electro-osmotic drag coefficients in PFSA membranes without any diffusion assumption.IntJHydrogen Energ,2019,44(45)24905 [31]Wakita H,Kawabata N,Kani Measurement of water permeation through membranes from extremely high hydraulic pressure to atmospheric pfessure.IntJ Hydrogen Energ,2019,44(59):31257 [32]Shin H S,Oh B S.Water transport according to temperature and current in PEM water electrolyzer.IntJ Hydrogen Energ,2019,45(1)s6 [33]Trinke P Bensmann B,Hanke-Rauschenbach R.Current density effect on hydrogen permeation in PEM water electrolyzers.Im JHydrogen Energ,2017,42(21):14355 [34]Schalenbach M.Erratum:pressurized PEM water electrolysis:efficiency and gas crossover.Int J Hydrogen Energ, 2013,38(35):14921.IntJ Hydrogen Energ,2016,41(1)729 [35]Grigoriev SA,Millet P,Korobtsev S V,et al.Hydrogen safety aspects related to highpressure polymer electrolyte membrane water electrolysis.IntJ Hydrogen Energ,2009,34(14):5986 [36]Ito H,Miyazaki N,Ishida M,et al.Cross-permeation and consumption of hydrogen during proton exchange membrane electrolysis.Int J Hydrogen Energ,2016,41(45):20439 [37]Han B,Mo J K,Kang Z Y,et al.Effects of membrane electrode assembly properties on two-phase transport and performance in proton exchange membrane electrolyzer cells.Electrochimi Acta,2016,188:317 38]Bromberger K,Ghinaiya J,Lickert T,et al.Hydraulic ex situ through-plane characterization of porous transport layers2015, 119(45): 25145 [15] Ito H, Maeda T, Nakano A, et al. Properties of Nafion membranes under PEM water electrolysis conditions. Int J Hydrogen Energ, 2011, 36(17): 10527 [16] Battino R, Clever H L. The solubility of gases in liquids. Chem Rev, 1966, 66: 395 [17] Mann R F, Amphlett J C, Peppley B A, et al. Henry's Law and the solubilities of reactant gases in the modelling of PEM fuel cells. J Power Sources, 2006, 161(2): 768 [18] Wise D L, Houghton G. The diffusion coefficients of ten slightly soluble gases in water at 10-60 °C. Chem Eng Sci, 1966, 21(11): 999 [19] Sakai T, Takenaka H, Wakabayashi N, et al. Gas Permeation Properties of Solid Polymer Electrolyte (SPE) Membranes. J Electrochem Soc, 1985, 132(6): 1328 [20] Yoshitake M, Tamura M, Yoshida N, et al. Studies of Perfluorinated Ion Exchange Membranes for Polymer Electrolyte Fuel Cells. Denki Kagaku, 1996, 64(6): 727 [21] Kocha S S, Yang J D, Yi J S. Characterization of gas crossover and its implications in PEM fuel cells. Aiche J, 2006, 52(5): 1916 [22] Broka K, Ekdunge P J. Oxygen and hydrogen permeation properties and water uptake of Nafion 117 membrane and recast film for PEM fuel cell. J Appl Electrochem, 1997, 27(2): 117 [23] Barbir F. PEM electrolysis for production of hydrogen from renewable energy sources. Sol Energy, 2005, 78: 661 [24] Sakai T, Takenaka H, Torikai E. Gas Diffusion in the Dried and Hydrated Nafions. J Electrochem Soc, 1986, 133(1): 88 [25] Chiou J S, Paul D R. Gas permeation in a dry Nafion membrane. Ind Eng Chem Res, 1988, 27(11): 2161 [26] Mohamed H F M, Ito K, Kobayashi Y, et al. Free volume and permeabilities of O2 and H2 in Nafion membranes for polymer electrolyte fuel cells. Polymer, 2008, 49(13-14): 3091 [27] Schalenbach M, Michael A H, Jeff T G, et al. Gas Permeation through Nafion. Part2: Resistor Network Model. J Phys Chem C, 2015, 119(45): 25156 [28] Trinke P, Bensmann B, Reichstein S, et al. Hydrogen Permeation in PEM Electrolyzer Cells Operated at Asymmetric Pressure Conditions. J Electrochem Soc, 2016, 163(11): F3164 [29] Fales J L, Vanderborgh N E, Stroeve P. The influence of channel geometry on ionic transport // Proceedings of the Symposium on Diaphragms, Separators, and Ion-Exchange Membranes, 1986: 13 [30] Sellin R C ,Mozet K ,Ménage A, et al. Measuring electro-osmotic drag coefficients in PFSA membranes without any diffusion assumption. Int J Hydrogen Energ, 2019, 44(45): 24905 [31] Wakita H, Kawabata N, Kani Y. Measurement of water permeation through membranes from extremely high hydraulic pressure to atmospheric pressure. Int J Hydrogen Energ, 2019, 44(59): 31257 [32] Shin H S, Oh B S. Water transport according to temperature and current in PEM water electrolyzer. Int J Hydrogen Energ, 2019, 45(1): 56 [33] Trinke P, Bensmann B, Hanke-Rauschenbach R. Current density effect on hydrogen permeation in PEM water electrolyzers. Int J Hydrogen Energ, 2017, 42(21): 14355 [34] Schalenbach M. Erratum: pressurized PEM water electrolysis: efficiency and gas crossover. Int J Hydrogen Energ, 2013, 38(35): 14921. Int J Hydrogen Energ, 2016, 41(1): 729 [35] Grigoriev S A, Millet P, Korobtsev S V, et al. Hydrogen safety aspects related to highpressure polymer electrolyte membrane water electrolysis. Int J Hydrogen Energ, 2009, 34(14): 5986 [36] Ito H, Miyazaki N, Ishida M, et al. Cross-permeation and consumption of hydrogen during proton exchange membrane electrolysis. Int J Hydrogen Energ, 2016, 41(45): 20439 [37] Han B, Mo J K, Kang Z Y, et al. Effects of membrane electrode assembly properties on two-phase transport and performance in proton exchange membrane electrolyzer cells. Electrochimi Acta, 2016, 188: 317 [38] Bromberger K, Ghinaiya J, Lickert T, et al. Hydraulic ex situ through-plane characterization of porous transport layers 录用稿件,非最终出版稿
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