2018
DOI: 10.1016/j.mcat.2018.10.006
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Three inter-linked active sites in the dehydrogenation of n-octane over magnesium molybdate based catalysts and their influences on coking and cracking side reactions

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Cited by 16 publications
(5 citation statements)
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“…The activation of n-octane at 450 °C, using the 0.04 mol alkaline earth metal modified Ga-NaY catalysts showed the previously reported ODH products of n-octane, which were octenes, aromatics, oxygenates, cracked products and carbon oxides [1][2][3][4]. Only GHSV was varied between the catalysts to achieve iso-conversion.…”
Section: Product Selectivity At Iso-conversionmentioning
confidence: 52%
See 1 more Smart Citation
“…The activation of n-octane at 450 °C, using the 0.04 mol alkaline earth metal modified Ga-NaY catalysts showed the previously reported ODH products of n-octane, which were octenes, aromatics, oxygenates, cracked products and carbon oxides [1][2][3][4]. Only GHSV was varied between the catalysts to achieve iso-conversion.…”
Section: Product Selectivity At Iso-conversionmentioning
confidence: 52%
“…Oxidation, cracking, dehydrogenation, dehydrocyclization, and oxidative dehydrogenation are possible reactions that can activate paraffins using heterogeneous catalysts. Dehydrogenation (DH) of n-octane is one of the important reactions industrially and can be carried out using a variety of catalysts, both mono-and bi-functional [1][2][3][4]. Paraffins are easily and cheaply obtained from natural gas and petroleum, and this, with their relative environmental friendliness, makes them interesting alternatives to olefinic and aromatic feedstocks.…”
Section: Introductionmentioning
confidence: 99%
“…The catalyst which was determined to have the lowest nickel occupation in both these sites (Sp-0.06 Nb) and less oxygen vacancies from XPS data showed the highest selectivity to carbon oxides. Fadalla et al [58] again reported the oxidative dehydrogenation of n-octane over molybdate-based catalysts. This study focused on the application of magnesium molybdate with different Mg:Mo ratios ranging from 1:0.87 to 1:1.25.…”
Section: Unsupported Metal Oxidesmentioning
confidence: 97%
“…It has been shown that the formation of active oxygen species during the re-oxidation of the catalysts influences the selectivity of products in the oxidative dehydrogenation of n-octane. Mechanistic investigations have revealed that the basicity and the redox capacity of the metal will influence the selectivity to olefins [55,58]. Metal oxides interact with the hydrogen atoms of alkanes and promote the dissociation of C-H bonds and the subsequent formation of hydrogen and olefins.…”
Section: Catalysts Usedmentioning
confidence: 99%
“…In addition, a large number of coking precursors formed in combustion also restrict the efficient utilization of a transport fuel. , Accurate prediction of the difference in coke precursor formation is of great help to evaluate the coking trend of isomer fuels. However, a comprehensive introduction to the coking mechanism difference of six isomers is rarely reported in the literature . Most of them only introduce the coking behavior of individual isomers, for example, Friedrich et al found that the addition of a metal (Mg) would promote the undesired coking reactions of n -octane. Therefore, an in-depth understanding of the coking mechanism difference of octane isomers is of significance to improve fuel quality and provide a reliable basis for selecting suitable fuel surrogates.…”
Section: Introductionmentioning
confidence: 99%