Abstract

The extent of reduction of unsupported iron-based high-temperature water-gas shift catalysts with small (<5 wt %) lanthana contents was studied using UV-visible spectroscopy. Temperature- programmed reduction measurements showed that lanthana content higher than 0.5 wt % increased the extent of reduction to metallic Fe, while 0.5 wt % of lanthana facilitated the reduction to Fe3O4. In situ measurements on the iron oxide catalysts using mass and UV-visible spectroscopies permitted the quantification of the extent of reduction under temperature-programmed reduction and high-temperature water-gas shift conditions. The oxidation states were successfully calibrated against normalized absorbance spectra of visible light using the Kubelka-Munk theory. The normalized absorbance relative to the fully oxidized Fe2O3 increased as the extent of reduction increased. XANES suggested that the average bulk iron oxidation state during the water-gas shift reaction was Fe+2.57 for the catalyst with no lanthana and Fe+2.54 for the catalysts with 1 wt % lanthana. However, the UV-vis spectra suggest that the surface oxidation state of iron would be Fe+2.31 for the catalyst with 1 wt % lanthana if the oxidation state of iron in the catalyst with 0 wt % lanthana were Fe+2.57. The findings of this paper emphasize the importance of surface sensitive UV-visible spectroscopy for determining the extent of catalyst reduction during operation. The paper highlights the potential to use bench-scale UV-visible spectroscopy to study the surface chemistry of catalysts instead of less-available synchrotron X-ray radiation facilities.

Highlights

  • The water-gas shift (WGS) reaction is a critical industrial process for hydrogen production and for controlling carbon monoxide to hydrogen ratio in multiple chemical processes [1,2]

  • Inspection the position positionofofthe thepre-edge pre-edgefeature feature and Inspectionofofthe thespectral spectralfeatures, features, in in particular, particular, the and thethe position of the main edgeedge suggest that that oxidation state state of iron the in samples is closeistoclose that of position of the main suggest oxidation of in iron the samples to magnetite that of magnetite

  • A thorough study on the extent of reduction of iron-based high-temperature water-gas shift catalysts using different characterization techniques has been presented in this paper

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Summary

Introduction

The water-gas shift (WGS) reaction is a critical industrial process for hydrogen production and for controlling carbon monoxide to hydrogen ratio in multiple chemical processes [1,2]. The exothemicity and reversibility of the WGS reaction lead it to be performed in 2 steps in industrial reactors: (1) high-temperature (HT) at ~400 ◦ C and (2) low-temperature (LT) at ~220 ◦ C, Catalysts 2018, 8, 63; doi:10.3390/catal8020063 www.mdpi.com/journal/catalysts. Catalysts 2018, 7, x FOR PEER REVIEW in order to minimize the CO concentration in the effluent gas stream. Industrial high-temperature (HT) WGS catalysts are typically 92 wt % Fe3 O4order /8 wtto%minimize. Cr2 O3 that serve as active and stable catalysts the CO concentration in the effluent gas stream. At reaction temperatures close to 400 C [2].

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