Product shape selectivity of MFI-type, MEL-type, and BEA-type zeolites in the catalytic hydroconversion of heptane

Product shape selectivity of MFI-type, MEL-type, and BEA-type zeolites in the catalytic hydroconversion of heptane

Poursaeidesfahani, A. (TU Delft Engineering Thermodynamics)
de Lange, M.F. (TU Delft Engineering Thermodynamics)
Khodadadian, F. (TU Delft Intensified Reaction and Separation Systems)
Dubbeldam, D. (Universiteit van Amsterdam)
Rigutto, Marcello (Shell)
Nair, Nitish (Shell)
Vlugt, T.J.H. (TU Delft Engineering Thermodynamics)

2017

The influence of product shape selectivity on the bifunctional conversion of n-C₇ by zeolite catalysts is investigated. Three different zeolite catalysts with different pore sizes (MFI-type, MEL-type, and BEA-type zeolites) have been investigated experimentally. For all three catalysts, n-C₇ is isomerized to monobranched isomers which are further isomerized into dibranched isomers, and these dibranched molecules are converted into cracking products. More dibranched isomers and less cracking products are produced by BEA-type zeolite compared to MFI-type and MEL-type zeolites and clear differences are observed in the distribution of dibranched isomers produced by different catalysts. Molecular simulation is used to compute the adsorption isotherms and free energy barriers for diffusion of dibranched isomers in MFI-type, MEL-type, and BEA-type zeolites. Combining simulation results and experimental observations, it is shown that product shape selectivity can explain the distribution of dibranched molecules while transition state shape selectivity fails to do so. For the medium-pore zeolites (MFI-type and MEL-type zeolites), free energy barriers for diffusion of dibranched molecules are significant. For MFI-type and MEL-type zeolites, the dibranched molecule that has to overcome lower diffusion barrier is produced with a higher yield and the distribution of dimethylpentane molecules is determined by their diffusion rate. It is shown that there is almost no free energy barrier for the diffusion of any of these molecules in BEA-type zeolite. As BEA-type zeolite imposes no free energy barrier for diffusion of any of dibranched isomers, the distribution of dibranched isomers is very close to the equilibrium distribution in the gas phase. Due to the limited mobility of dimethylpentanes within the pores of MFI-type and MEL-type zeolites, most of the dimethylpentane molecules are trapped inside the zeolite and undergo consecutive cracking. Dimethylpentane molecules diffuse sufficiently fast in the large pores of BEA-type zeolite and transfer to the gas phase, before consecutive reaction converts these molecules into cracking products. Moreover, the effect of the MFI-type crystal size on the production of dibranched isomers is investigated. The yield of dibranched isomers reduces by increasing the size of the crystal and larger part of dibranched isomers are cracked as the crystal size of MFI-type is increased.

Experiments
Hydrocracking
Molecular simulation
Product distribution
Shape selectivity
Zeolites

http://resolver.tudelft.nl/uuid:794fb6ff-2422-47eb-bd04-d996a8e64848

https://doi.org/10.1016/j.jcat.2017.07.005

0021-9517

Journal of Catalysis, 353, 54-62

Institutional Repository

journal article

© 2017 A. Poursaeidesfahani, M.F. de Lange, F. Khodadadian, D. Dubbeldam, Marcello Rigutto, Nitish Nair, T.J.H. Vlugt