Mathematical Model for the Industrial SMTO Reactor with a SAPO-34 Catalyst
Author:
Affiliation:
1. Research Institute of Petroleum Processing, East China University of Science and Technology, Shanghai 200237, China
2. Petro-CyberWorks Information Technology Co., Ltd., Shanghai 200050, China
Publisher
American Chemical Society (ACS)
Subject
General Chemical Engineering,General Chemistry
Link
https://pubs.acs.org/doi/pdf/10.1021/acsomega.3c00304
Reference86 articles.
1. Comprehensive energy analysis and integration of coal-based MTO process
2. Kinetic Modeling of Catalytic Olefin Cracking and Methanol-to-Olefins (MTO) over Zeolites: A Review
3. Maximization of FCC light olefins by high severity operation and ZSM-5 addition
4. The oxidative dehydrogenation of ethane and propane as an alternative way for the production of light olefins
5. Highly effective P-modified HZSM-5 catalyst for the cracking of C4 alkanes to produce light olefins
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