4.7 Article

Enhancing reactant selectivity for Ni/Mg reforming catalysts using silicalite-1 shells: A modeling study

Journal

CHEMICAL ENGINEERING JOURNAL
Volume 437, Issue -, Pages -

Publisher

ELSEVIER SCIENCE SA
DOI: 10.1016/j.cej.2022.135353

Keywords

Zeolites; Diffusion (membrane); Mass transfer; Coreshell catalyst; Optimization; Steam reforming

Funding

  1. US Department of Energy (DOE) [DE-EE0008488]

Ask authors/readers for more resources

This study investigated the ability of a zeolite shell to enhance the selective conversion of hydrocarbons. The results showed that the thickness of the zeolite shell and the size of the molecules/pores had an impact on the catalytic performance. A reaction-diffusion model was used to verify the model and suggest an optimal shell thickness that balances diffusion rates.
The ability of a zeolite shell to enhance the selective conversion of hydrocarbons through diffusional limitations was investigated using a multi-scale model of a fixed-bed reactor. The impact of shell thickness and molecule/ pore size on the catalytic performance of silicalite-1 zeolite encapsulated nickel catalyst pellets for steam reforming of C1-C7 hydrocarbons is reported. A reaction-diffusion model using kinetic expressions established in literature was employed. The model was verified through comparison with reported experimental results for steam reforming data over a temperature range of 748 - 1113 K and pressure of 1 - 10 bar. Comparisons are also made against experimental data for steam reforming in the presence of a zeolite shell. Evaluation of the Weisz-Prater criterion for both the core and encapsulated catalyst confirmed mass transfer limitation induced by the utilization of a zeolite shell. The model was used to suggest an optimal thickness that balances diffusional limitations imposed by the zeolite layer on methane versus that of the heavier hydrocarbons. The optimum thickness varied as a function of hydrocarbon size and shape which determined the diffusion rates. For toluene and heptane, a 50 nm thick shell was sufficient to wholly prevent reaction. Hydrocarbons like propane and butane required a shell 7.5 and 5 mu m thick. Increasing the gas-hourly-space-velocity from 10,000 to 60,000 h(-1) caused a decrease in the optimum shell thickness. This approach can be modified for application to other mixed hydrocarbon systems to predict optimal catalyst design.

Authors

I am an author on this paper
Click your name to claim this paper and add it to your profile.

Reviews

Primary Rating

4.7
Not enough ratings

Secondary Ratings

Novelty
-
Significance
-
Scientific rigor
-
Rate this paper

Recommended

No Data Available
No Data Available