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Nuclear Production of Hydrogen, Fourth Information Exchange ...

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DEVELOPMENT OF CuCl-HCl ELECTROLYSIS FOR HYDROGEN PRODUCTION VIA Cu-Cl THERMOCHEMICAL CYCLE<br />

Figure 1: Schematic diagram <strong>of</strong> the CuCl(aq)/HCl(aq) electrolytic system<br />

Membranes<br />

Ion exchange membrane (IEM) is a key component <strong>of</strong> the CuCl-HCl electrolytic system and is used to<br />

separate the anodic and cathodic compartments as well as to provide ionic conductivity. For high<br />

performance, the IEM needs to have high counter ion conductivity and selectivity as well as good<br />

mechanical properties to withstand the aggressive concentrated HCl(aq) environment. To select the<br />

best membrane for the CuCl-HCl electrolyser, a variety <strong>of</strong> commercial membranes were evaluated,<br />

including anion exchange membranes (AEM) produced by Tokuyama Soda (AHA, AMX, ACS, ACM,<br />

AM-3) and Asahi Glass (AHT), as well as Nafion, a proton exchange membrane produced by E.I. du Pont<br />

de Nemours & Co., Inc. The membranes were characterised for swelling, ion exchange capacity (IEC),<br />

and conductivity.<br />

The membrane conductivity was measured in a specially designed “clip”-type conductivity cell<br />

(Figure 2). The cell consists <strong>of</strong> two compartments with a membrane fixed in between. Two titanium<br />

disk electrodes are applied to both sides <strong>of</strong> the membrane. Both compartments could be filled with<br />

various solutions <strong>of</strong> a desired concentration.<br />

Figure 2: Schematic <strong>of</strong> the conductivity cell<br />

NUCLEAR PRODUCTION OF HYDROGEN – © OECD/NEA 2010 253

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