2007
DOI: 10.1007/s10562-007-9232-4
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Enhanced Stability of HZSM-5 Supported Ga2O3 Catalyst in Propane Dehydrogenation by Dealumination

Abstract: Gallium oxide catalysts supported on HZSM-5 with different Si/Al ratios were characterized by pyridine adsorption FT-IR, model reactions and XPS studies. As the Si/Al ratio of the support HZSM-5 zeolite rises, the acidity of the supported catalysts decreases accordingly, which comes from two aspects: the loss of acid sites present on HZSM-5 support and the loss of the acid sites present on gallium oxides. The latter was caused by the change in the interaction between Ga 2 O 3 and support. The initial activity … Show more

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Cited by 49 publications
(31 citation statements)
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“…The initial propane conversion decreases as the Si/Al ratio increases, due to the decrease of the acid sites on the catalysts, quite similar to the results over Ga 2 O 3 /HZSM-5 catalysts. 16 Meanwhile, the selectivity to propylene increases with the increase of Si/Al ratio. Thus, the initial propylene yield has the sequence of Figure 4B.…”
Section: Catalytic Activitymentioning
confidence: 99%
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“…The initial propane conversion decreases as the Si/Al ratio increases, due to the decrease of the acid sites on the catalysts, quite similar to the results over Ga 2 O 3 /HZSM-5 catalysts. 16 Meanwhile, the selectivity to propylene increases with the increase of Si/Al ratio. Thus, the initial propylene yield has the sequence of Figure 4B.…”
Section: Catalytic Activitymentioning
confidence: 99%
“…Similar results were observed before. 16,17 The catalytic activities of these supported gallium oxide catalysts toward cumene cracking, a typical strong acid catalyzed reaction, have been investigated. The results are given in Table 2.…”
Section: Acidity Measurementsmentioning
confidence: 99%
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