BACKGROUND: The metal–acid bifunctional catalysts are widely used in many industrially significant chemical processes, including hydroisomerization of n-hexane. Deactivation and regeneration of metal–acid bifunctional extrudates was investigated in continuous n-hexane hydroisomerization in a fixed-bed reactor. Four Pt/H-Beta-25 catalysts containing 30% Bindzil binder were prepared with the same composition and controlled metal deposition. RESULTS: Different preparation steps led to differences in the mechanical strength, Pt particle size, acidity and strength, metal-to-acid site (cPt/cAS) ratio and proximity between two types of active sites. A very slow deactivation and high selectivity to C6 isomers was obtained when Pt was deposited on H-Beta-25 zeolite. CONCLUSION: Initial selectivity to the desired products was correlated with the physicochemical properties of the catalysts. Location of the metal has a larger influence on catalyst deactivation of the bifunctional catalysts rather than the metal-to-acid site ratio or site proximity. Decline of n-hexane conversion and selectivity to C6 isomers were correlated with changes in the textural properties and acidity of the deactivated catalyst, respectively. © 2021 The Authors. Journal of Chemical Technology & Biotechnology published by John Wiley & Sons Ltd on behalf of Society of Chemical Industry.
CITATION STYLE
Vajglová, Z., Kumar, N., Peurla, M., Hupa, L., Semikin, K., Sladkovskiy, D. A., & Murzin, D. Y. (2021). Deactivation and regeneration of Pt-modified zeolite Beta–Bindzil extrudates in n-hexane hydroisomerization. Journal of Chemical Technology and Biotechnology, 96(6), 1645–1655. https://doi.org/10.1002/jctb.6685
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