焦炭
甲醇
化学
催化作用
化学工程
煤
吸附
选择性
扩散
多相催化
无机化学
有机化学
热力学
物理
工程类
作者
D. Chen,K. Moljord,Anders Holmen
标识
DOI:10.1016/j.micromeso.2012.06.046
摘要
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.
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