Development of a post-synthetic method for tuning the Al content of OSDA-free Beta as a catalyst for conversion of methanol to olefins
Author(s) -
Ryoichi Otomo,
Ulrich Müller,
Mathias Feyen,
Bilge Yilmaz,
Xiangju Meng,
FengShou Xiao,
Hermann Gies,
Xinhe Bao,
Weiping Zhang,
Dirk De Vos,
Toshiyuki Yokoi
Publication year - 2015
Publication title -
catalysis science and technology
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 1.635
H-Index - 115
eISSN - 2044-4761
pISSN - 2044-4753
DOI - 10.1039/c5cy00944h
Subject(s) - catalysis , methanol , beta (programming language) , materials science , chemical engineering , chemistry , organic chemistry , computer science , engineering , programming language
Zeolites synthesized without any organic structure-directing agent (OSDA) have several advantages over conventional zeolites synthesized with OSDAs. Their Al-rich compositions, however, are sometimes not suitable for applications as catalysts. In the present study, post-synthetic modification was performed using an Al-rich Beta zeolite synthesized without any OSDAs (designated as “Beta(OF)”) to obtain high-silica Beta zeolites. We have successfully developed a facile post-synthetic method for tuning the Al content of Beta(OF) with the *BEA-type structure retained by calcination at u003e750 °C followed by acid treatment. Solid-state 29Si and 27Al MAS NMR analyses revealed that during calcination, framework Al atoms were isomorphously substituted with Si atoms to form high-silica frameworks and concomitant extra-framework Al species. The stability of the obtained frameworks against acid treatment was evaluated in terms of the framework Al content, finding that the framework with the Si/Al ratio higher than 12 is well stabilized enough for acid treatment. Thus, dealuminated Beta(OF) zeolites with high-silica compositions were found to be effective catalysts for the methanol-to-olefin (MTO) reaction; particularly, the Beta zeolite with the Si/Al ratio of 112 maintained the conversion of methanol over 90% with selectivity to C2–C4 olefins over 70% even at 40 hours on stream at WHSV = 3.2 h−1.
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