Kinetics and reactor modeling of the conversion of n-pentane using HZSM-5 catalysts with different Si/Al ratio

T. Cordero-Lanzac, A. Aguayo, P. Castaño, J. Bilbao
Kinetics and reactor modeling of the conversion of n-pentane using HZSM-5 catalysts with different Si/Al ratio, (2019)

Kinetics and reactor modeling of the conversion of n-pentane using HZSM-5 catalysts with different Si/Al ratio

Keywords

Olefins

Abstract

​The production of olefins and aromatics from n-pentane has been modeled using the experimental results collected in an isothermal packed bed reactor with HZSM-5 zeolite catalysts with different Si/Al ratios (15 and 140) in the temperature range of 400–550 ºC. In a first stage, a lump-based kinetic model has been established, evaluating the role of the Si/Al ratio in the kinetic parameters and therefore, in the conversion, product distribution and deactivation by coke. The effect of the catalyst acidity and the reaction conditions has been explained by analyzing the used catalysts by means of N2 and tert-butylamine adsorption-desorption, temperature-programmed oxidation and confocal fluorescence microscopy. In a second stage, the kinetic parameters extracted for both catalysts have been used in simulations of an isothermal packed bed reactor in order to study the evolution of the reaction with the space time and time on stream. It has been found certain suitable conditions (550 ºC and 3.5 gcat h molC-1) for maximizing the yield and selectivity of olefins (31 and 51 %, respectively, using the zeolite with Si/Al = 140) and aromatics (yield and selectivity of 53 %, using the one with Si/Al = 15) in the simulated range.

Code

DOI: 10.1039/C9RE00222G

Sources

Website PDF

See all publications 2019