CO2 Hydrogenation over Pt-Containing UiO-67 Zr-MOFsThe Base Case

CO2 hydrogenation was carried out over Pt-containing UiO-67 Zr-MOFs at T = 220–280 °C and ambient pressure, with H2/CO2 = 0.2–9 and contact times, τ = 0.004–0.01 gcat·min·mL–1. The catalysts were characterized by XRD, N2 adsorption, FESEM, TEM and HRTEM, Pt L3-edge XANES and EXAFS, dissolution-NMR,...

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Veröffentlicht in:Industrial & engineering chemistry research 2017-11, Vol.56 (45), p.13206-13218
Hauptverfasser: Gutterød, Emil Sebastian, Øien-Ødegaard, Sigurd, Bossers, Koen, Nieuwelink, Anne-Eva, Manzoli, Maela, Braglia, Luca, Lazzarini, Andrea, Borfecchia, Elisa, Ahmadigoltapeh, Sajjad, Bouchevreau, Boris, Lønstad-Bleken, Bjørn Tore, Henry, Reynald, Lamberti, Carlo, Bordiga, Silvia, Weckhuysen, Bert M, Lillerud, Karl Petter, Olsbye, Unni
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Sprache:eng
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Zusammenfassung:CO2 hydrogenation was carried out over Pt-containing UiO-67 Zr-MOFs at T = 220–280 °C and ambient pressure, with H2/CO2 = 0.2–9 and contact times, τ = 0.004–0.01 gcat·min·mL–1. The catalysts were characterized by XRD, N2 adsorption, FESEM, TEM and HRTEM, Pt L3-edge XANES and EXAFS, dissolution-NMR, CO chemisorption, IR spectroscopy, and TGA. A positive correlation was observed between the degree of Pt reduction and CO2 conversion. Contact time variation experiments showed that CO is a primary product of reaction, while CH4 is a secondary product. Testing of catalyst crystals with 0.15 and 2.0 μm crystal size, respectively, revealed no influence of diffusion on the reaction rate. Comparison to a conventional Pt/SiO2 catalyst showed very similar activation energy, with E app = 50 ± 3 kJ·mol–1. However, the turnover frequency over Pt/SiO2 was significantly lower, and Pt/SiO2 did not yield methane as a product. The Pt-containing UiO-67 Zr-MOF catalyst showed stable activity during 60 h of testing.
ISSN:0888-5885
1520-5045
DOI:10.1021/acs.iecr.7b01457