Abstract
Informed through synthesis and characterization of NH 3 TPD, BET techniques, the current study investigated the right contribution of silicon and water content on a 9 sample SAPO-34 catalyst with different molar ratios. The final prepared SAPO-34 catalytic performed reaction for the Methanol to olefin process was processed and reported at 410 0 C a reactor of fixed-bed. It was shown that catalysts with different SiO2 /Al2O3 and H2O/Al 2 O 3 ratios demonstrated high ethylene and propylene selectivity, due to their intensified crystallinity and size of crystals (1.3 to 1.7 μm). The highest degrees of ethylene and propylene selectivity for 3 samples were 50.25, 21.20, and 48.44, 19.16 respectively. Samples with ratios of different that possess high density and acute acidic sites to deactivate rapidly. The high density of acute acidic sites promoted the ultimate response to saturated hydrocarbons and aromatics based on olefins’ hydrogen transfer to and resulted in the coke generation on the top layer of the catalyst.
Keywords: Methanol to olefin, BET, Ethylene, Propylene
Acknowledgements
Department of Chemical Engineering, Arak Branch, Islamic Azad University, Arak, Iran.
Young Researchers and Elite Club, Gachsaran Branch, Islamic Azad University, Gachsaran, Iran.
Nomenclature
- MTO
Methanol to olefin
- NH3-TPD
NH3 Temperature-Programmed Desorption
- WHSV
weigh hourly space velocity
- OCT
Olefins Conversion Technology
- SAPO
silica-alumina-phosphates
Author Contributions
Not applicable.
Data Availability
Not applicable.
Declarations
Ethics Approval
Not applicable
Consent to Participate
Not applicable
Consent for Publication
Not applicable
Conflict of Interest
The authors declare that they have no conflicts of interest.
Research Involving Human Participants and/or Animals
Not applicable
Footnotes
Publisher’s Note
Springer Nature remains neutral with regard to jurisdictional claims in published maps and institutional affiliations.
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