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燃料电池阴极氧还原过电位的起源

Origin of the Overpotential for Oxygen Reduction at a Fuel-Cell Cathode.

作者信息

Nørskov J K, Rossmeisl J, Logadottir A, Lindqvist L, Kitchin J R, Bligaard T, Jónsson H

机构信息

Center for Atomic-scale Materials Physics, Department of Physics, Technical University of Denmark, DK-2800 Lyngby, Denmark.

Department of Chemical Engineering, University of Delaware, Newark, Delaware 19716.

出版信息

J Phys Chem B. 2004 Nov 18;108(46):17886-17892. doi: 10.1021/jp047349j.

Abstract

We present a method for calculating the stability of reaction intermediates of electrochemical processes on the basis of electronic structure calculations. We used that method in combination with detailed density functional calculations to develop a detailed description of the free-energy landscape of the electrochemical oxygen reduction reaction over Pt(111) as a function of applied bias. This allowed us to identify the origin of the overpotential found for this reaction. Adsorbed oxygen and hydroxyl are found to be very stable intermediates at potentials close to equilibrium, and the calculated rate constant for the activated proton/electron transfer to adsorbed oxygen or hydroxyl can account quantitatively for the observed kinetics. On the basis of a database of calculated oxygen and hydroxyl adsorption energies, the trends in the oxygen reduction rate for a large number of different transition and noble metals can be accounted for. Alternative reaction mechanisms involving proton/electron transfer to adsorbed molecular oxygen were also considered, and this peroxide mechanism was found to dominate for the most noble metals. The model suggests ways to improve the electrocatalytic properties of fuel-cell cathodes.

摘要

我们提出了一种基于电子结构计算来计算电化学过程反应中间体稳定性的方法。我们将该方法与详细的密度泛函计算相结合,以详细描述在Pt(111)上电化学氧还原反应的自由能景观随外加偏压的变化。这使我们能够确定该反应过电位的来源。发现在接近平衡电位时,吸附的氧和羟基是非常稳定的中间体,并且计算得到的活化质子/电子转移到吸附的氧或羟基的速率常数能够定量地解释观察到的动力学。基于计算得到的氧和羟基吸附能数据库,可以解释大量不同过渡金属和贵金属的氧还原速率趋势。还考虑了涉及质子/电子转移到吸附的分子氧的替代反应机制,发现这种过氧化物机制在大多数贵金属中占主导地位。该模型提出了改善燃料电池阴极电催化性能的方法。

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