Abstract

Preferential oxidation of CO in H2 was studied by in situ ultraviolet–visible (UV–Vis) and mass spectrometry on flat model Cu and Cu/CeOx catalysts. The experimental findings were interpreted and compared with the results from density functional theory (DFT) calculations of the adsorption and activation energies for the essential reaction steps on Cu(1 1 1). It was found that oxidation of CO preferentially takes place on Cu(0) and that no significant H2 oxidation took place under any of the investigated conditions. The presence of CeOx accelerates Cu(0)-oxidation which leads to catalyst deactivation. In contrast, CeOx promotes the CO oxidation rate on catalysts that were already oxidized to CuOx. The coexistence of CO and H2 is important to sustain the stability of metallic Cu and thereby a high rate of CO2 formation. In pure CO/O2 gas, the metallic phase can only be maintained as long as full O2 conversion is reached. In pure H2/O2, Cu is always partly but never fully oxidized, suggesting that a passivating surface layer is formed. This is also the case for H2 rich gas mixtures with small amounts of CO and O2. The most active surface termination, Cu(0), can therefore not be maintained under the industrially most interesting reaction condition where full conversion of trace amounts of CO in H2 is required. DFT calculations predict that the dissociative H2 adsorption is a key limiting step for hydrogen oxidation on the Cu(1 1 1) surface, especially when the low sticking coefficient is taken into account.

Highlights

  • H2 is mainly produced from steam reforming of hydrocarbons

  • The first set of experiments aims at clarifying the behavior of Cu and Cu/CeOx catalysts for CO Preferential oxidation (PROX) in a H2 flow

  • This part of the work is focused on the reaction conditions where metallic Cu is stable, since Cu(0) has been shown to be the most active phase for CO oxidation [21,28]

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Summary

Introduction

H2 is mainly produced from steam reforming of hydrocarbons. This process is followed by a water–gas shift reaction to increase the amount of hydrogen and remove CO [1,2,3,4]. The produced H2 inevitably contains tiny amounts of CO. An additional CO removal step is needed if highly pure H2 is required, e.g. for use in fuel cells. Crucial requirements for a good catalyst are: (i) high reactivity towards CO oxidation, and (ii) low activity towards H2 oxidation, so that CO may be removed without significant H2 consumption and without excessive energy consumption

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