Improving the dehydrogenation function and stability of Zn-modified ZSM-5 catalyst in methanol-to-aromatics reaction by Ca addition

Journal Article (2024)
Author(s)

Héctor Vicente (University of the Basque Country)

C. Liu (TU Delft - ChemE/Inorganic Systems Engineering)

Ana G. Gayubo (University of the Basque Country)

Pedro Castaño (University of the Basque Country, King Abdullah University of Science and Technology)

Evgeny A. Pidko (TU Delft - ChemE/Inorganic Systems Engineering)

Research Group
ChemE/Inorganic Systems Engineering
DOI related publication
https://doi.org/10.1016/j.apcata.2024.119854
More Info
expand_more
Publication Year
2024
Language
English
Research Group
ChemE/Inorganic Systems Engineering
Volume number
683
Reuse Rights

Other than for strictly personal use, it is not permitted to download, forward or distribute the text or part of it, without the consent of the author(s) and/or copyright holder(s), unless the work is under an open content license such as Creative Commons.

Abstract

Adding Zn to the ZSM-5 zeolite effectively increases the aromatic selectivity in the methanol-to-aromatics (MTA) process. The formation of metal-derived Lewis acid sites promotes the dehydrogenation but at the cost of a rapid deactivation of the catalyst by coke, due to the increased aromatic formation. In this work, we impregnated a Zn-modified catalyst (2 wt%) with variable contents of Ca (0.02 and 0.5 wt%) and evaluated their kinetic behavior in the MTA and ethane dehydrogenation reactions. The results proved the superior performance of the Zn(2)Ca(0.02) catalyst due to a synergistic effect between the two metals. The Ca ions limit coke formation from excessive aromatization, increasing catalyst stability and removing Zn clusters, resulting in a recovery of Brønsted acid sites (BAS) active for the formation of light aromatics. Combining these effects results in a more efficient and viable catalyst for aromatic production from methanol.