2024
DOI: 10.1016/j.cej.2024.149366
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Elucidating the promoting advantages and fundamentals for their creation in Sn-modified commercial CrOx/Al2O3 catalyst for propane dehydrogenation

Lei Zhang,
Kezhen Chen,
Huarong Chen
et al.
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Cited by 4 publications
(1 citation statement)
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“…For example, taking advantage of the large surface area and ordered pore structure of ZSM-5, with the pore size of 0.56 × 0.51 nm being larger than the molecule dynamics diameter (0.47 nm) of propane molecules, Wang et al [18] investigated propane dehydrogenation over Cr loaded ZSM-5 (Cr-ZSM-5) zeolite, the Brönsted acid sites of which have also been reported to be favorable for the adsorption and reaction of propane. Igonina et al [19] impregnated 5 wt.% Cr on MCM-41 using the first impregnation method, which resulted in 20% conversion of C 3 H 8 and 76% selectivity of C 3 H 6 at 650 • C. Singh et al [20] used ZrO 2 as a support loaded with 2.5 wt.% Cr and achieved 16% conversion of C 3 H 8 and 86.6% selectivity of C 3 H 6 at 550 • C. Zhang et al [21] introduced 5 wt.% Sn into an Al 2 O 3 catalyst loaded with 3 wt.% Cr in order to improve the stability of the catalyst. The initial conversion of C 3 H 8 in the catalyst was 40%, and after 10 h of reaction, the conversion of C 3 H 8 was stable at 32%.…”
Section: Introductionmentioning
confidence: 99%
“…For example, taking advantage of the large surface area and ordered pore structure of ZSM-5, with the pore size of 0.56 × 0.51 nm being larger than the molecule dynamics diameter (0.47 nm) of propane molecules, Wang et al [18] investigated propane dehydrogenation over Cr loaded ZSM-5 (Cr-ZSM-5) zeolite, the Brönsted acid sites of which have also been reported to be favorable for the adsorption and reaction of propane. Igonina et al [19] impregnated 5 wt.% Cr on MCM-41 using the first impregnation method, which resulted in 20% conversion of C 3 H 8 and 76% selectivity of C 3 H 6 at 650 • C. Singh et al [20] used ZrO 2 as a support loaded with 2.5 wt.% Cr and achieved 16% conversion of C 3 H 8 and 86.6% selectivity of C 3 H 6 at 550 • C. Zhang et al [21] introduced 5 wt.% Sn into an Al 2 O 3 catalyst loaded with 3 wt.% Cr in order to improve the stability of the catalyst. The initial conversion of C 3 H 8 in the catalyst was 40%, and after 10 h of reaction, the conversion of C 3 H 8 was stable at 32%.…”
Section: Introductionmentioning
confidence: 99%