期刊
ACS CATALYSIS
卷 11, 期 23, 页码 14489-14506出版社
AMER CHEMICAL SOC
DOI: 10.1021/acscatal.1c03641
关键词
Zn/H-MFI; zinc; zeolite; propane dehydrogenation; zinc chloride; solid-state ion exchange; catalyst characterization; kinetics
资金
- Chevron Energy Technology Co.
- DOE Office of Science [DE-AC02-06CH11357]
- Department of Energy
- NIH [S10-RR027172]
- MRCAT
The study prepared Zn/H-MFI with varying Zn/Al ratios via solid-state ion exchange (SSIE) and characterized it by various methods. It was found that Zn/H-MFI with higher Zn loadings contains Z(2)O(4)/ZnAl2O4,Cl-2 nanoclusters, which can be transformed into [ZnH](+) cations through postsynthetic treatment.
Light alkanes in shale gas are an attractive source of carbon for the production of alkenes and aromatics compared to petroleum-derived naphtha. Zinc-exchanged zeolite H-MFI (Zn/H-MFI) is active and selective for light alkane dehydrogenation and dehydroaromatization. In this study, Zn/H-MFI with varying Zn/Al ratios was prepared via solid-state ion exchange (SSIE) of ZnCl2 and characterized by various methods. As-prepared Zn/HMFI with Zn/Al <= 0.52 contains isolated [ZnCl]+ and [ZnCl-(HCl)](+) species; Zn/H-MFI with higher Zn loadings also contains Z(2)O(4)/ZnAl2O4,Cl-2, nanoclusters. Postsynthetic treatment in He and subsequently in 2.5% H-2 in He at 773 K removes Cl and adsorbed HCl, resulting in the formation of [ZnH](+) cations. Studies of C3H8 dehydrogenation and cracking suggest that in the absence of cofed H-2, [ZnH](+) cations are transformed to bridging Zn2+ cations, which exhibit higher C3H8 dehydrogenation activity and selectivity relative to [ZnH](+) cations. The kinetics of dehydrogenation and cracking over Zn/H-MFI were investigated as a function of Zn loading, C3H8 partial pressure, and temperature. The turnover frequency for propane dehydrogenation and cracking increases with Zn loading, which we propose is due to localization of Zn2+ cations either at increasingly distant pairs of Al atoms or at the beta-site in the MFI framework. The selectivity to dehydrogenation over cracking over Zn (2+) is independent of C3H8 partial pressure and temperature, consistent with dehydrogenation and cracking pathways that proceed via a common surface intermediate and have similar enthalpies of activation. The product distribution is thus determined by the entropy of activation for each pathway, which is less negative in the case of C3H8 dehydrogenation.
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