Catalytic transformation of methyl benzenes over zeolite catalysts

• Published in: Applied catalysis. A, General General, 2011-02, Vol.394 (1), p.176-190
• Main Authors: Al-Khattaf, S., Akhtar, M.N., Odedairo, T., Aitani, A., Tukur, N.M., Kubů, M., Musilová-Pavlačková, Z., Čejka, J.
• Format: Article
• Language: English
• Subjects: 1,2,4-Trimethylbenzene; Catalysis; Catalysts; Channels; Chemistry; Colloidal state and disperse state; Disproportionation; Exact sciences and technology; General and physical chemistry; Ion-exchange; Isomerization; m-Xylene; Mordenite; Porosity; Porous materials; SSZ-33; Surface physical chemistry; Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry; Three dimensional; TNU-9; Toluene; Transformations; Zeolites; Zeolites: preparations and properties; ZSM-5
• ISSN: 0926-860X; 1873-3875
• DOI: 10.1016/j.apcata.2010.12.031

[Display omitted] ▶ The effect of structure architecture of novel zeolites SSZ-33 and TNU-9 is reported for toluene, m-xylene and 1,2,3-trimethylbenzene reactions. ▶ We report on the kinetic data of a riser simulator. ▶ The experimental data of catalytic studies are contrasted to the kinetic model for all reactants and catalysts tested. Catalytic transformation of three methyl benzenes (toluene, m-xylene, and 1,2,4-trimethyl benzene) has been investigated over ZSM-5, TNU-9, mordenite and SSZ-33 catalysts in a novel riser simulator at different operating conditions. Catalytic experiments were carried out in the temperature range of 300–400 °C to understand the transformation of these alkyl benzenes over large pore (mordenite and SSZ-33) in contrast to medium-pore (ZSM-5 and TNU-9) zeolite-based catalysts. The effect of reaction conditions on the isomerization to disproportionation product ratio, distribution of trimethylbenzene (TMB) isomers, and p-xylene/ o-xylene ratios are reported. The sequence of reactivity of the three alkyl benzenes depends upon the pore structure of zeolites. The zeolite structure controls primarily the diffusion of reactants and products while the acidity of these zeolites is of a secondary importance. In the case of medium pore zeolites, the order of conversion was m-xylene > 1,2,4-TMB > toluene. Over large pore zeolites the order of reactivity was 1,2,4-TMB > m-xylene > toluene for SSZ-33 catalyst, and m-xylene ∼ 1,2,4-TMB > toluene over mordenite. Significant effect of pore size between ZSM-5 and TNU-9 was observed; although TNU-9 is also 3D 10-ring channel system, its slightly larger pores compared with ZSM-5 provide sufficient reaction space to behave like large-pore zeolites in transformation of aromatic hydrocarbons. We have also carried out kinetic studies for these reactions and activation energies for all three reactants over all zeolite catalysts under study have been calculated.