Two one-dimensional zeolite catalysts with similar pore structures and 0.3 Å difference in pore sizes (5.6 Å × 6.0 Å for H-ZSM-12 and 4.6 Å × 5.7 Å for H-ZSM-22) were exploited to gauge the critical sizes of the key intermediate species formed during the methanol conversion to olefins. Both zeolite catalysts are characterized by powder X-ray diffraction, scanning electron microscopy, 27 Al solid-state NMR spectroscopy, NH 3 temperature-programmed desorption, and N 2 adsorption/desorption analysis. In the methanol-to-olefin (MTO) process, the hydrocarbon-pool mechanism worked on the H-ZSM-12 zeolite with the 6.0 Å pore size, while the catalytic cycle could not be completed inside the H-ZSM-22 zeolite with the smaller 5.7 Å pore size. This finding strongly confirms that the hydrocarbon-pool mechanism is a space-demanding process and suggests that the size of key reactive hydrocarbon-pool intermediates for the MTO process is between 5.7 and 6.0 Å. These results will provide a strong experimental base for both theoretical and experimental studies in the MTO process.
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Wang et al. (2011) studied this question.
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