2022
DOI: 10.1039/d2cy00074a
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Atomic-scale changes of silica-supported catalysts with nanocrystalline or amorphous gallia phases: implications of hydrogen pretreatment on their selectivity for propane dehydrogenation

Abstract: We explore how H2 pretreatment changes the structure of two gallia-based propane dehydrogenation catalysts, viz. crystalline γ/β-Ga2O3 and amorphous Ga2O3 supported on silica, and how it affects their activity, selectivity and stability on stream.

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Cited by 15 publications
(17 citation statements)
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“…XPS experiments were performed to further investigate the state of Zn under (i) reducing conditions, (ii) a CO 2 /H 2 atmosphere, and (iii) methanol vapor. The measurements were performed by treating the passivated catalysts in a reaction chamber connected to the XPS instrument, which allows to study activated materials without their exposure to the ambient air . The Zn 2p 3/2 XPS region of Cu–Zn(5)/SiO 2 after pretreatment in H 2 (300 mbar) at 200 °C (1 h) features a broad peak, indicating the presence of both Zn 0 and Zn 2+ states (Figure b).…”
Section: Resultsmentioning
confidence: 99%
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“…XPS experiments were performed to further investigate the state of Zn under (i) reducing conditions, (ii) a CO 2 /H 2 atmosphere, and (iii) methanol vapor. The measurements were performed by treating the passivated catalysts in a reaction chamber connected to the XPS instrument, which allows to study activated materials without their exposure to the ambient air . The Zn 2p 3/2 XPS region of Cu–Zn(5)/SiO 2 after pretreatment in H 2 (300 mbar) at 200 °C (1 h) features a broad peak, indicating the presence of both Zn 0 and Zn 2+ states (Figure b).…”
Section: Resultsmentioning
confidence: 99%
“…The measurements were performed by treating the passivated catalysts in a reaction chamber connected to the XPS instrument, which allows to study activated materials without their exposure to the ambient air. 49 The Zn 2p 3/2 XPS region of Cu−Zn(5)/SiO 2 after pretreatment in H 2 (300 mbar) at 200 °C (1 h) features a broad peak, indicating the presence of both Zn 0 and Zn 2+ states (Figure 3b). Peak deconvolution yields a Zn 0 /Zn 2+ ratio of 0.45, which is higher than that of Zn(5)/SiO 2 pretreated under identical conditions (Zn 0 /Zn 2+ = 0.36, Figure S43).…”
Section: Co 2 Hydrogenation Testsmentioning
confidence: 99%
“…In contrast, the more active sites in unsupported nanoparticle catalysts such as β-Ga 2 O 3 or mixed oxide (Ga,Al) 2 O 3 are weak Lewis acid sites (LAS), yet a higher relative amount of mild LAS in those catalysts also leads to increased amounts of coking. [22][23][24][25] Here, we report that ALD-made [4] Ga (Si/Ga) and [5] Ga (Si/Ga) sites on dehydroxylated silica transform, upon contact with ambient air, to [4] Ga (Ga) and [6] Ga (Ga) sites that are contained in ca. sub-nanometer Ga x O y (OH) z clusters that feature no diffraction peaks and are not-discernable by highresolution TEM.…”
Section: Introductionmentioning
confidence: 86%
“…In contrast, the more active sites in unsupported nanoparticle catalysts such as β-Ga 2 O 3 or mixed oxide (Ga,Al) 2 O 3 are weak Lewis acid sites (LAS), yet a higher relative amount of mild LAS in those catalysts also leads to increased amounts of coking. 22–25…”
Section: Introductionmentioning
confidence: 99%
“…Developing alternative environmentally friendly and cost-effective PDH catalysts is significant to enhance propene production. It is reported in the literature that metal (Pd, Ru ) and metal oxide (GaO x , , ZnO x , , CoO x , VO x , , ZrO x ) based materials are two main PDH catalysts and have been extensively studied. Most of the above active components have to be loaded on a specific matrix to realize a higher dispersion for obtaining a satisfying catalytic performance.…”
Section: Introductionmentioning
confidence: 99%