Abstract

Hβ molecular sieves with different SiO2/Al2O3 ratios (Hβ(x))and Hβ(x) loading Pd(0.5 wt%) bifunctional catalysts(Pd/Hβ(x)) were prepared by hydrothermal synthesis and incipient wetness impregnation, respectively. The structure, morphology, pore and acid properties of Hβ(x) and Pd dispersion of Pd/Hβ (x) were characterized using XRD, SEM, N2 physical adsorption, NH3-TPD and H2 chemical absorption. Hβ (x) samples were highly crystalline microporous materials. With the increase of SiO2/Al2O3 ratios, BET surface area, micro-pore surface area and volume of Hβ (x) gradually decreased, and the external surface area and mesoporous volume gradually increased, and the number and acid strength of weak acid sites for Hβ(x) and Pd dispersion for Pd/Hβ(x) decreased. It was known from hydroisomerization perforamce of n-C16H34 that Pd/Hβ(40) catalysts showed the highest conversion of of 96.9% at 230°C. The select ivity of iso-C16H34 reached the highest value at the n-C16H34 conversion of 45~50%. Pd/Hβ(40) cata lysts exhib ited the highest iso-C16H34 selectivity of 84.4%, much more multi-branched iso-C16H34 and C4+C5 cracking components. The decrease of SiO2/Al2O3 molar ratios can increase the number of acid sites and dispersion of Pd/Hβ(x) bifunctional catalysts, thus not only aggravating the secondary heterogeneous reaction, but also accelerating the serious secondary cracking reaction.

Full Text
Paper version not known

Talk to us

Join us for a 30 min session where you can share your feedback and ask us any queries you have

Schedule a call

Disclaimer: All third-party content on this website/platform is and will remain the property of their respective owners and is provided on "as is" basis without any warranties, express or implied. Use of third-party content does not indicate any affiliation, sponsorship with or endorsement by them. Any references to third-party content is to identify the corresponding services and shall be considered fair use under The CopyrightLaw.