期刊
MICROPOROUS AND MESOPOROUS MATERIALS
卷 164, 期 -, 页码 239-250出版社
ELSEVIER
DOI: 10.1016/j.micromeso.2012.06.046
关键词
MTO; SAPO-34; Coke formation; Deactivation
The catalytic conversion of methanol to lower olefins (MTO) is a promising way of converting natural gas and coal to chemicals and fuels with methanol as an intermediate. Coke formation is a major cause of deactivation in the MTO processes and the present contribution deals with the progress on the study of adsorption, diffusion and reaction including deactivation due to coke formation during MTO. Design of SAPO-34 to achieve high activity and selectivity is discussed in terms of the two most important parameters, namely crystal size and operating temperatures. (C) 2012 Elsevier Inc. All rights reserved.
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