Abstract
AbstractThe exploitation of methane to produce aromates is already seen for a long time as very attractive. Although investigated intensively, methane dehydro‐aromatization (MDA) is far from being applied industrially. MDA under non‐oxidative conditions is severely limited by thermodynamics and rapid catalyst deactivation. Mo/MCM‐22 was reported as a promising catalyst. Thus, kinetic experiments were performed to parametrize rate expressions and to identify trends regarding the selectivity‐conversion behavior including catalyst deactivation. Finally, mass transfer was described mathematically to evaluate the potential of hydrogen‐selective membranes within a membrane reactor of the extractor type. Such a removal would be beneficial to overcome the thermodynamic limitations.
Sign-in/Register to access full text options 
Talk to us
Join us for a 30 min session where you can share your feedback and ask us any queries you have
Schedule a callDisclaimer: All third-party content on this website/platform is and will remain the property of their respective owners and is provided on "as is" basis without any warranties, express or implied. Use of third-party content does not indicate any affiliation, sponsorship with or endorsement by them. Any references to third-party content is to identify the corresponding services and shall be considered fair use under The CopyrightLaw.
