Reverse Water-Gas Shift Iron Catalyst Derived from Magnetite

The catalytic properties of unsupported iron oxides, specifically magnetite (Fe<sub>3</sub>O<sub>4</sub>), were investigated for the reverse water-gas shift (RWGS) reaction at temperatures between 723 K and 773 K and atmospheric pressure. This catalyst exhibited a fast cataly...

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Main Authors: Chen-Yu Chou, Jason A. Loiland, Raul F. Lobo
Format: Article
Language:English
Published: MDPI AG 2019-09-01
Series:Catalysts
Subjects:
Online Access:https://www.mdpi.com/2073-4344/9/9/773
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spelling doaj-bf17674fd6d541fc974807d0d4b43cf22020-11-25T01:51:11ZengMDPI AGCatalysts2073-43442019-09-019977310.3390/catal9090773catal9090773Reverse Water-Gas Shift Iron Catalyst Derived from MagnetiteChen-Yu Chou0Jason A. Loiland1Raul F. Lobo2Center for Catalytic Science and Technology, Department of Chemical and Biomolecular Engineering, University of Delaware, Newark, DE 19716, USACenter for Catalytic Science and Technology, Department of Chemical and Biomolecular Engineering, University of Delaware, Newark, DE 19716, USACenter for Catalytic Science and Technology, Department of Chemical and Biomolecular Engineering, University of Delaware, Newark, DE 19716, USAThe catalytic properties of unsupported iron oxides, specifically magnetite (Fe<sub>3</sub>O<sub>4</sub>), were investigated for the reverse water-gas shift (RWGS) reaction at temperatures between 723 K and 773 K and atmospheric pressure. This catalyst exhibited a fast catalytic CO formation rate (35.1 mmol h<sup>&#8722;1</sup> g<sub>cat.</sub><sup>&#8722;1</sup>), high turnover frequency (0.180 s<sup>&#8722;1</sup>), high CO selectivity (&gt;99%), and high stability (753 K, 45000 cm<sup>3</sup>h<sup>&#8722;1</sup>g<sub>cat.</sub><sup>&#8722;1</sup>) under a 1:1 H<sub>2</sub> to CO<sub>2</sub> ratio. Reaction rates over the Fe<sub>3</sub>O<sub>4</sub> catalyst displayed a strong dependence on H<sub>2</sub> partial pressure (reaction order of ~0.8) and a weaker dependence on CO<sub>2</sub> partial pressure (reaction order of 0.33) under an equimolar flow of both reactants. X-ray powder diffraction patterns and XPS spectra reveal that the bulk composition and structure of the post-reaction catalyst was formed mostly of metallic Fe and Fe<sub>3</sub>C, while the surface contained Fe<sup>2+</sup>, Fe<sup>3+</sup>, metallic Fe and Fe<sub>3</sub>C. Catalyst tests on pure Fe<sub>3</sub>C (iron carbide) suggest that Fe<sub>3</sub>C is not an effective catalyst for this reaction at the conditions investigated. Gas-switching experiments (CO<sub>2</sub> or H<sub>2</sub>) indicated that a redox mechanism is the predominant reaction pathway.https://www.mdpi.com/2073-4344/9/9/773RWGSiron oxidesCO<sub>2</sub> conversiongas-switching
collection DOAJ
language English
format Article
sources DOAJ
author Chen-Yu Chou
Jason A. Loiland
Raul F. Lobo
spellingShingle Chen-Yu Chou
Jason A. Loiland
Raul F. Lobo
Reverse Water-Gas Shift Iron Catalyst Derived from Magnetite
Catalysts
RWGS
iron oxides
CO<sub>2</sub> conversion
gas-switching
author_facet Chen-Yu Chou
Jason A. Loiland
Raul F. Lobo
author_sort Chen-Yu Chou
title Reverse Water-Gas Shift Iron Catalyst Derived from Magnetite
title_short Reverse Water-Gas Shift Iron Catalyst Derived from Magnetite
title_full Reverse Water-Gas Shift Iron Catalyst Derived from Magnetite
title_fullStr Reverse Water-Gas Shift Iron Catalyst Derived from Magnetite
title_full_unstemmed Reverse Water-Gas Shift Iron Catalyst Derived from Magnetite
title_sort reverse water-gas shift iron catalyst derived from magnetite
publisher MDPI AG
series Catalysts
issn 2073-4344
publishDate 2019-09-01
description The catalytic properties of unsupported iron oxides, specifically magnetite (Fe<sub>3</sub>O<sub>4</sub>), were investigated for the reverse water-gas shift (RWGS) reaction at temperatures between 723 K and 773 K and atmospheric pressure. This catalyst exhibited a fast catalytic CO formation rate (35.1 mmol h<sup>&#8722;1</sup> g<sub>cat.</sub><sup>&#8722;1</sup>), high turnover frequency (0.180 s<sup>&#8722;1</sup>), high CO selectivity (&gt;99%), and high stability (753 K, 45000 cm<sup>3</sup>h<sup>&#8722;1</sup>g<sub>cat.</sub><sup>&#8722;1</sup>) under a 1:1 H<sub>2</sub> to CO<sub>2</sub> ratio. Reaction rates over the Fe<sub>3</sub>O<sub>4</sub> catalyst displayed a strong dependence on H<sub>2</sub> partial pressure (reaction order of ~0.8) and a weaker dependence on CO<sub>2</sub> partial pressure (reaction order of 0.33) under an equimolar flow of both reactants. X-ray powder diffraction patterns and XPS spectra reveal that the bulk composition and structure of the post-reaction catalyst was formed mostly of metallic Fe and Fe<sub>3</sub>C, while the surface contained Fe<sup>2+</sup>, Fe<sup>3+</sup>, metallic Fe and Fe<sub>3</sub>C. Catalyst tests on pure Fe<sub>3</sub>C (iron carbide) suggest that Fe<sub>3</sub>C is not an effective catalyst for this reaction at the conditions investigated. Gas-switching experiments (CO<sub>2</sub> or H<sub>2</sub>) indicated that a redox mechanism is the predominant reaction pathway.
topic RWGS
iron oxides
CO<sub>2</sub> conversion
gas-switching
url https://www.mdpi.com/2073-4344/9/9/773
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AT jasonaloiland reversewatergasshiftironcatalystderivedfrommagnetite
AT raulflobo reversewatergasshiftironcatalystderivedfrommagnetite
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