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The gas diffusion layer must be a highly conductive material for both fuel cell and<br />

electrolysis applications. It must have a porous structure to bring the reactants to the PEM<br />

for fuel cell and to expel the products for the electrolysis. In the conventional fuel <strong>cells</strong>, the<br />

gas diffusion layers are usually porous carbon matrix, such as carbon cloth or carbon paper.<br />

However, this structure is not suitable for <strong>water</strong> electrolysis due to the oxidation of carbon<br />

with active oxygen species, such as oxygen atom or hydroxyl free radicals, at high positive<br />

potentials of anode (Song et al. 2006, Petersson et al. 2006).<br />

Gas diffusion layer of an anode electrode should not be a hydrophobic material.<br />

Thus, PTFE loading generally decreases the efficiency of the cell similar to the PTFE<br />

loading effect on the catalyst layer (Ioroi et al. 2003). Woven metal cloths, expanded metal<br />

sheets, perforated metal sheets or metal foams which are made up of corrosive resistive<br />

metals, such as titanium, zirconium, hafnium, niobium and tantalum, are used as the<br />

electrolyzer gas diffusion plates (Petersson et al. 2006).<br />

Another approach for making electrolysis gas diffusion layer is to promote the<br />

traditional carbon matrix used in the fuel <strong>cells</strong> with a suitable metal(s). This approach aims<br />

to form an oxygen molecule rapidly before the atoms starts to diffuse the gas diffusion<br />

layer (Song et al. 2006) proposed it as a new cathode for electrolysis cell which had a <strong>water</strong><br />

reservoir placed inside the cell contacting with the membrane, and with the Toray carbon<br />

paper used as the gas diffusion layer. After the electrolysis operation, no corrosion of the<br />

oxygen electrode occurred because the <strong>water</strong> did not come in direct contact with the<br />

electrode and the active oxygen species were combined before reaching the gas diffusion<br />

layer. However, their cell structure was complicated and the gap between anode and<br />

cathode was wide which caused less voltage efficient electrolysis operation (Song et al<br />

2006).<br />

2.2.1.4. Bipolar Plates<br />

All the fuel <strong>cells</strong> and electrolyzers (with the exception of laboratory bench scale<br />

ones) are constructed with many <strong>cells</strong> connected in series. Similar to the serially connected<br />

battery systems, the serially connected fuel cell systems could generate electricity at high<br />

24

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