Modification of Nafion membrane using interfacial polymerization for vanadium redox flow battery applications

Abstract In order to reduce the permeation of vanadium ions across the ion exchange membrane during the operation of vanadium redox flow battery (VRB) based on Nafion membrane, the interfacial polymerization was applied to form a cationic charged layer on the surface of Nafion 117 membrane. The area resistance and the permeability of vanadium ions were measured. The results indicate that comparing with the unmodified Nafion membrane, the modification of Nafion membrane results in a dramatic reduction in crossover of vanadium ions across the membrane and a little higher area resistance of the membrane. As a result, the columbic efficiency for the VRB single cell based on the modified Nafion membrane(VRB-modified Nafion), which is related to the concentration of the incubation solution of polyethylenimine (PEI), was increased significantly. The value is 96.2–97.3%, which is higher than that obtained with the VRB single cell based on unmodified Nafion membrane(VRB-Nafion) (around 93.8%). Due to the little higher area resistance caused by the modification, the voltage efficiency of VRB-modified Nafion is lower than that of VRB-Nafion. Furthermore, the water transfer across the modified membrane was also reduced. The ion exchange capacity (IEC) of the modified Nafion membrane was also evaluated. The formation of the thin cationic charged layer on the membrane surface was confirmed by IR spectra analysis.

[1]  Maria Skyllas-Kazacos,et al.  Characteristics and performance of 1 kW UNSW vanadium redox battery , 1991 .

[2]  T. Hayashita,et al.  Transport of alkali metal cations through monoazacrown ether-modified NafionTM 117 membrane , 1996 .

[3]  Maria Skyllas-Kazacos,et al.  Investigation of the V(V)/V(IV) system for use in the positive half-cell of a redox battery , 1985 .

[4]  H. Ohya,et al.  Crosslinking of anion exchange membrane by accelerated electron radiation as a separator for the all-vanadium redox flow battery , 1997 .

[5]  Xinping Qiu,et al.  Influences of permeation of vanadium ions through PVDF-g-PSSA membranes on performances of vanadium redox flow batteries. , 2005, The journal of physical chemistry. B.

[6]  Maria Skyllas-Kazacos,et al.  Modification of membranes using polyelectrolytes to improve water transfer properties in the vanadium redox battery , 2003 .

[7]  T. Sata,et al.  Studies on cation-exchange membranes having permselectivity between cations in electrodialysis , 2002 .

[8]  D. Collins,et al.  Power Sources 3 , 1971 .

[9]  He-sun Zhu,et al.  Modification of a Nafion® ion exchange membrane by a plasma polymerization process , 2000 .

[10]  Stéphanie Roualdes,et al.  Separation of H+/Cu2+ cations by electrodialysis using modified proton conducting membranes , 2003 .

[11]  R. Lichtenthaler,et al.  Sorption isotherms of vanadium with H3O+ ions in cation exchange membranes , 1998 .

[12]  Haruhiko Ohya,et al.  Preparation of cation exchange membrane as a separator for the all-vanadium redox flow battery , 1996 .

[13]  P. Colomban,et al.  Nanostructure of Nafion® membranes at different states of hydration , 2001 .

[14]  Toraj Mohammadi,et al.  Water transport study across commercial ion exchange membranes in the vanadium redox flow battery , 1997 .

[15]  Toraj Mohammadi,et al.  Preparation of sulfonated composite membrane for vanadium redox flow battery applications , 1995 .