Different anode catalyst for high temperature polybenzimidazole-based direct ethanol fuel cells Jose ´ J. Linares 1 , Thairo A. Rocha, Sabrina Zignani, Valdecir A. Paganin, Ernesto R. Gonzalez* Instituto de Quı´mica de Sa ˜o Carlos, Universidade de Sa ˜o Paulo, Av. Trabalhador Sa ˜o-Carlense, 400 CP 780, CEP 13560-970 Sa ˜o Carlos, SP, Brazil article info Article history: Received 28 February 2012 Received in revised form 21 June 2012 Accepted 29 June 2012 Available online 25 July 2012 Keywords: DEFC Bimetallic catalysts PBI Cell performance Product distribution abstract Five different bimetallic catalyst formulations (PtRu/C, PtSn/C, PtW/C, PtRh/C and PtOs/C) were prepared by reduction with sodium borohydride, and physico-chemically charac- terized by X-Ray Diffraction, Transmission Electron Microscopy, Temperature Programmed Reduction and X-Ray Photoelectron Spectroscopy. It was observed that in the case of the PtRu/C and PtRh/C a large fraction of the second metal enters the platinum lattice struc- ture. The remaining metal, and in those catalysts in which no alloy was formed, its deposition was in a mixed metallic (Os) and/or oxide form, as TPR and XPS results dis- played. Crystal sizes were in the range 3e5 nm, except for the case of the PtW/C in which there was a large agglomeration of platinum particles, as the TEM images confirmed. Electrochemical half-cell tests demonstrated the better performance of these bimetallic catalysts in terms of ethanol oxidation, with lower onset potential and larger current densities, particularly in the case of the PtOs/C, PtRu/C and PtRh/C materials, and to a lower extent in the case of the PtSn/C. Actual fuel cell tests at high temperature (150 and 200 C) confirmed the beneficial effects of increasing the temperature in terms of cell performance, with an increase in the performance, particularly in the cases of PtOs/C and PtRu/C. Finally, the product distribution was also assessed, observing a large conversion to CO 2 by oper- ating at high temperatures, particularly for PtRh/C at low current density, and for Pt/C at high current density (up to 35%), although acetaldehyde remained as the main oxidation product for all the catalysts. Copyright ª 2012, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved. 1. Introduction Direct ethanol fuel cells (DEFCs) are an interesting alternative to traditional H 2 -based Polymer Electrolyte Membrane Fuel Cells (PEMFCs) [1]. This interest stems from the intrinsic advantages of ethanol as fuel: (i) non-toxicity, (ii) natural availability (from biomass), (iii) renewability, (iv) high power density (8 kWh kg 1 ), and (v) small green-house contribution to the atmosphere [2,3]. The much higher volumetric energy density (22.11 MJ m 3 vs. 2.531 MJ m 3 for compressed H 2 at 250 bar) defined an ideal scenario, further supported by other advantages such as the safer and easier handling, trans- portation and storage [4]. However, there are severe limita- tions in the development of the DEFC technology when * Corresponding author. Tel.: þ55 1633739899; fax: þ55 1633739903. E-mail address: Ernesto@iqsc.usp.br (E.R. Gonzalez). 1 Current address: Instituto de Quı ´mica, Universidade de Brası ´lia, Campus Darcy Ribeiro CP 04478, CEP 70910-000, Brazil. Available online at www.sciencedirect.com journal homepage: www.elsevier.com/locate/he international journal of hydrogen energy 38 (2013) 620 e630 0360-3199/$ e see front matter Copyright ª 2012, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved. http://dx.doi.org/10.1016/j.ijhydene.2012.06.113