Abstract

Ca, Ni, Co, and Ge promoters were examined as potential candidates to substitute for the current toxic Cr in Cu-promoted Fe oxide-based catalysts for the HT-WGS reaction. The Ca and Ni promoters were found to improve catalyst performance relative to promotion with Cr. The HS-LEIS surface analysis data demonstrate that Ca and Ge tend to segregate on the surface, while Ni, Co, and Cr form solid solutions in the Fe3O4 bulk lattice. The corresponding number of catalytic active sites, redox, and WGS activity values of the catalysts were determined with CO-TPR, CO+H2O-TPSR, and SS-WGS studies, respectively. The poorer HT-WGS performances of the Ge and Co promoters are related to the presence of surface Ge and Co that inhibits catalyst redox ability, with the Co also not stabilizing the surface area of the Fe3O4 support. The Ni promoter uniformly disperses the Cu nanoparticles on the catalyst surface and increases the number of FeOx-Cu interfacial redox sites. The Ca promoter on the catalyst surface, however, enhances the activity of the FeOx-Cu interfacial redox sites. The CO+H2O TPSR results reveal that the redox ability of the active sites follows the SS-WGS performance of the catalysts and show the following trend: 3Cu8CaFe > 3Cu8NiFe ≥ 3Cu8CrFe > 3Cu8CoFe >> 3Cu8GeFe. Furthermore, all the catalysts followed a redox-type reaction mechanism for the HT-WGS reaction.

Highlights

  • The water-gas shift (WGS) reaction converts CO in the presence of H2 O into CO2 and H2, which aims at controlling H2 to CO ratio for the synthesis of NH3 and CH3 OH, production of synthetic fuels, etc. [1,2]

  • Industrial high-temperature water gas shift (HT-WGS) catalysts mostly contain (~80–90% by bulk weight) Fe oxide with Cu and Cr oxides added as promoters for improved activity [4]

  • A thorough understanding of the structures and roles of various metal oxides present in Cu/Cr–Fe oxide catalysts, is needed for the rational design of a Cr-free catalyst for the HT-WGS reaction

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Summary

Introduction

The water-gas shift (WGS) reaction converts CO in the presence of H2 O into CO2 and H2 , which aims at controlling H2 to CO ratio for the synthesis of NH3 and CH3 OH, production of synthetic fuels, etc. [1,2]. Due to reversible and exothermic nature of the WGS reaction (Equation (1)), industrially, the reaction is performed in several stages with different catalysts to attain greater CO equilibrium conversions [3,4]. The hexavalent Cr (VI) present in the catalyst is a significant carcinogen [5] and has been the topic of intense research over the past decades, especially to find Cr-free HT-WGS catalysts. A thorough understanding of the structures and roles of various metal oxides present in Cu/Cr–Fe oxide catalysts, is needed for the rational design of a Cr-free catalyst for the HT-WGS reaction. In this regard, detailed in situ and Catalysts 2020, 10, 305; doi:10.3390/catal10030305 www.mdpi.com/journal/catalysts

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