Comparison of the iso-structural H-SAPO-37 and H-faujasite as catalysts for the isobutane/2-butene alkylation
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An exciting opportunity for zeolite adsorbent design in separation of C<inf>4</inf> olefins through adsorptive separation
2019, Separation and Purification TechnologyCitation Excerpt :The highest application of 2-butene is alkylate gasoline with about 70% of the total 2-butene production [16]. Alkylation reaction between 2-butene and isobutane was carried out using hexagonal faujasite H-EMT and H-FAU zeolites [81], dealuminated H-EMT and H-FAU zeolites [82], LaX and LaY zeolites [83,84], H-SAPO-37 and H-FAU zeolites [85], Cs+, NH4+, and K+ cations of 12-tungstophosphoric acid [86], mordenite, beta, LTL, and ZSM-12 zeolites [87] to increase high octane number of gasoline. Approximately, 24% of 2-butene is utilized to produce propene obtained over the cross metathesis between 2-butene and ethene [16] using tungsten based catalysts [73] and cationic nickel complexes [79] and 6% of the total 2-butene production is used to make methyl ethyl ketone (MEK) [16].
Chloride-free Cu-modified SAPO-37 catalyst for the oxidative carbonylation of methanol in the gas phase
2012, Applied Catalysis B: EnvironmentalCitation Excerpt :Introduction of Si into aluminophosphates during the synthesis to replace P in the crystalline framework would result in SAPO materials that possesses Brønsted acid sites, but of modified strength in comparison to zeolite Y [8,9]. The use of SAPO-37 in acid-catalyzed reactions is described, e.g. for o-xylene isomerisation [10], reaction of cyclohexene with H2O2 [11], isobutene/2-butene alkylation [12], cracking of n-heptane and 2,2,4-trimethylpentane [13] as well as the conversion of n-hexane, cyclohexane and gas oil [14]. Because of structural degradation of non-modified, Brønsted-acid SAPO-37 in the presence of water vapor traces, applications in oxidation reactions are rare.
Dimerization of 1-butene in liquid phase reaction: Influence of structure, pore size and acidity of Beta zeolite and MCM-41 mesoporous material
2012, Microporous and Mesoporous MaterialsCitation Excerpt :Over all catalysts the selectivity to cracking products increased with increasing conversion, although over H-Beta-11-96 h the selectivity increased very rapidly with increasing conversion. The cracking activity of the catalysts in olefin oligomerization has been correlated with the presence of strong acid sites [16]. The main 6 carbon atom containing hydrocarbons was 2,2-dimethylbutene over H-Beta-11-96 h catalyst, about 8 mol%, whereas much lower amounts of 2-methylpentane and 1-hexene were formed.
Theoretical studies of IM-12 zeolite for acidic catalysts
2008, Microporous and Mesoporous MaterialsIn situ flow MAS NMR spectroscopy: State of the art and applications in heterogeneous catalysis
2008, Progress in Nuclear Magnetic Resonance SpectroscopyComparison of zeolites LaX and LaY as catalysts for isobutane/2-butene alkylation
2008, Applied Catalysis A: General