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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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>−1</sup> g<sub>cat.</sub><sup>−1</sup>), high turnover frequency (0.180 s<sup>−1</sup>), high CO selectivity (>99%), and high stability (753 K, 45000 cm<sup>3</sup>h<sup>−1</sup>g<sub>cat.</sub><sup>−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>−1</sup> g<sub>cat.</sub><sup>−1</sup>), high turnover frequency (0.180 s<sup>−1</sup>), high CO selectivity (>99%), and high stability (753 K, 45000 cm<sup>3</sup>h<sup>−1</sup>g<sub>cat.</sub><sup>−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 |
work_keys_str_mv |
AT chenyuchou reversewatergasshiftironcatalystderivedfrommagnetite AT jasonaloiland reversewatergasshiftironcatalystderivedfrommagnetite AT raulflobo reversewatergasshiftironcatalystderivedfrommagnetite |
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1724998092250415104 |