Nafion and modified-Nafion membranes for polymer fuel cells

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Nafion and modified-Nafion membranes for polymer fuel cells ( nafion-and-modified-nafion-membranes-polymer-fuel-cells )

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Nafion and modified-Nafion membranes for polymer electrolyte fuel cells 291 cell polarization data as a function of varying load cur- rent-density. Figure 7 compares the polarization curves for the Nafion–silica composite and commercial Nafion- 1135 membranes under fully-wet condition (≈ 100%RH) at 60°C under ambient pressure. In all the experiments, the flow rates for both the fuel and the oxidant are fixed so as to preclude any water retention in the cell. Nafion– silica composite membranes with varying silica content show better performance in relation to Nafion mem- branes. The peak power density of 720 mW/cm2 for the PEFC is achieved with Nafion–silica (10 wt.%) compo- site membrane as compared to 550 mW/cm2 for the PEFC with Nafion-1135 membrane under identical operational conditions. Proton conductivity in the Nafion–silica com- posite membrane is attributed to protons that are trans- ferred through hydrogen bonding with water-filled ion pores. However, an excess of silica phase in Nafion matrix reduces the PEFC performance due to electrode flooding in the PEFC. Accordingly, the peak power den- sity for the PEFC with Nafion–silica (15 wt.%) composite membrane is lower in relation to PEFC with Nafion– silica (10 wt.%) composite membrane. Polarization data for PEFCs with Nafion-1135 and Nafion-silica composite membranes under near-dry con- ditions (≤ 18% RH) are shown in figure 8. At these RH values, the humidification of hydrogen gas is inapt to ope- rate PEFCs with pure Nafion membranes as the PEFCs yield a peak power-density of only about 30 mW/cm2 at 100 mA/cm2 primarily due to the poor conductivity of the Nafion membrane. By contrast, under identical condi- tions, PEFCs employing Nafion-silica composite mem- branes perform much better in relation to those with pristine-Nafion membranes. The performance of PEFCs with Nafion–silica composite membranes increases gradu- ally with increasing silica content in the Nafion matrix. A peak power-density of 300 mW/cm2 is achieved at Figure 7. Performance of H2/O2 PEFC with Nafion-1135 and Nafion–silica composite membranes at 100% RH under atmos- pheric pressure operating at 60°C. 1200 mA/cm2 for the PEFC employing a Nafion–silica composite membrane with 15 wt.% silica while operating at 60°C under atmospheric pressure. It is, therefore, quite obvious that PEFC performance is purely related to water-management. In commercial Nafion membranes, the limited availability of water at the anode, electroos- motic drag of water from anode to cathode and insufficient water back-diffusion from cathode to anode cause the membrane to dehydrate. The membrane dehydration is manifested with an increase in ohmic resistance of the cell leading to decreased cell performance. By contrast, in the case of composite Nafion membranes, due to water reten- tion characteristics of the silica, such a problem is obviated. 3.3 Nafion–mesoporous zirconium phosphate composite membranes as electrolytes for PEFCs Synthesis of mesoporous zirconium phosphate (MZP) by co-assembly of a tri-block copolymer, viz. pluronic-F127, as a structure directing agent and a mixture of zirconium butoxide and phosphorous trichloride as inorganic pre- cursors has been recently reported (Sahu et al 2009). Nafion–MZP composite membrane is obtained by em- ploying MZP as surface-functionalized solid-super-acid- proton-conducting medium as well as inorganic filler with high affinity to absorb water and fast proton-transport across the electrolyte membrane even under low relative humidity conditions. The presence of large pores and high internal-surface-area ameliorates the hydrophilic character of the internal pore-surfaces and results in a solid super-acid exhibiting fast proton-conduction. MZP, thus synthesized, is impregnated with the Nafion ionomer to realize a proton-conducting composite membrane. Figure 9 shows the FTIR spectra for the calcined zirconium phosphate with a strong sharp band centred at Figure 8. Performance of H2/O2 PEFC with Nafion-1135 and Nafion–silica composite membranes at 18% RH under atmo- spheric pressure operating at 60°C.

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