2018
DOI: 10.1039/c8cy01420e
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Direct dehydrogenation of isobutane to isobutene over Zn-doped ZrO2 metal oxide heterogeneous catalysts

Abstract: A series of unconventional nano-sized Zn-doped ZnZrO-x catalysts are applied for the first time to the direct dehydrogenation of isobutane to isobutene.

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Cited by 45 publications
(35 citation statements)
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“…Considering the EPR results (Figure ) and according to Silva‐Calpa et al., McFarland & Metiu and Liu et al., it can be suggested that Zn +2 substitutes Zr +4 in the t ‐ZrO 2 lattice generating oxygen vacancies and coordinatively unsaturated Zr 4+ ions (cus). The oxygen vacancies can be associated with strong basic sites whereas the cus species with Lewis acid sites.…”
Section: Resultsmentioning
confidence: 75%
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“…Considering the EPR results (Figure ) and according to Silva‐Calpa et al., McFarland & Metiu and Liu et al., it can be suggested that Zn +2 substitutes Zr +4 in the t ‐ZrO 2 lattice generating oxygen vacancies and coordinatively unsaturated Zr 4+ ions (cus). The oxygen vacancies can be associated with strong basic sites whereas the cus species with Lewis acid sites.…”
Section: Resultsmentioning
confidence: 75%
“…Indeed, replacing Zr +4 with Zn +2 makes the ZrO 2 surface more electrophilic. As oxygen is also electrophilic, it is easily displaced from the oxide surface generating vacancies . Silva‐Calpa et al .…”
Section: Resultsmentioning
confidence: 99%
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“…Alternatively, the O vacancies are associated with CO dissociation or formate decomposition to methoxy species, both suggested as the rate-limiting step of the methanation reaction. The CO 2 methanation mechanisms employing vacancy–cus pairs 12 are described in detail in the Results and discussion section.…”
Section: Introductionmentioning
confidence: 99%
“…The support materials, Al 2 O 3 [11], SiO 2 [6], ZrO 2 [12,13] and zeolite [3,14], can also affect catalytic performance on account of the significant differences in textural properties. Especially, the Mg(Al)O (c) by-product selectivity (reduction conditions: T = 600 °C, t = 2.5 h; reaction conditions: T = 600 °C, weight hourly space velocity (WSHV) = 3 h −1 , atmospheric pressure in the gas mixture of C3H8:H2:N2 molar ratio = 8:7:35; reaction time: 30 h for H2/N2 and 14 vol % H2/N2 reduced catalyst, 26 h for C3H8/H2/N2-reduced catalyst, 17 h for C3H8 and CO-reduced catalyst).…”
Section: Introductionmentioning
confidence: 99%