An Ir0.7Ru0.3Ox nanosized anode electrocatalyst was coupled to an Aquivion short-side chain perfluoro-sulfonic acid membrane (120 mm; EW: 870 g/eq) for operation in a PEM electrolyser. A conventional carbon supported Pt catalyst was used as cathode. An excellent performance, of 4 A cm2 at 1.9 V at 90 C, was achieved for this electrolyser configuration in the presence of a moderate noble metal loading (1.5 mg cm2 Ir þ Ru; 0.5 mg cm2 Pt). The interface of IrRuOx with Aquivion provided a 10% enhancement in performance compared to an equivalent interface with a Nafion membrane of similar thickness but characterized by a larger equivalent weight (EW: 1100 g/eq). The enhanced performance essentially derived from a decrease of polarization resistance. This appeared to be due to better interface characteristics between the electrodes and Aquivion® ionomer giving rise to an increased catalyst utilization. Whereas, no significant change in Tafel slope and activation energy was recorded indicating a similar reaction mechanism.

Performance of a PEM water electrolyser combining an IrRu-oxide anode electrocatalyst and a shortside chain Aquivion membrane

Siracusano S;Baglio V;
2015

Abstract

An Ir0.7Ru0.3Ox nanosized anode electrocatalyst was coupled to an Aquivion short-side chain perfluoro-sulfonic acid membrane (120 mm; EW: 870 g/eq) for operation in a PEM electrolyser. A conventional carbon supported Pt catalyst was used as cathode. An excellent performance, of 4 A cm2 at 1.9 V at 90 C, was achieved for this electrolyser configuration in the presence of a moderate noble metal loading (1.5 mg cm2 Ir þ Ru; 0.5 mg cm2 Pt). The interface of IrRuOx with Aquivion provided a 10% enhancement in performance compared to an equivalent interface with a Nafion membrane of similar thickness but characterized by a larger equivalent weight (EW: 1100 g/eq). The enhanced performance essentially derived from a decrease of polarization resistance. This appeared to be due to better interface characteristics between the electrodes and Aquivion® ionomer giving rise to an increased catalyst utilization. Whereas, no significant change in Tafel slope and activation energy was recorded indicating a similar reaction mechanism.
2015
Istituto di Tecnologie Avanzate per l'Energia - ITAE
Water electrolysis
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/20.500.14243/306590
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