cs0c01455_si_001.pdf (1.69 MB)
Structure–Activity–Selectivity Relationships in Propane Dehydrogenation over Rh/ZrO2 Catalysts
journal contribution
posted on 2020-05-21, 19:43 authored by Yaoyuan Zhang, Yun Zhao, Tatiana Otroshchenko, Anna Perechodjuk, Vita A. Kondratenko, Stephan Bartling, Uwe Rodemerck, David Linke, Haijun Jiao, Guiyuan Jiang, Evgenii V. KondratenkoA few
years ago, we introduced alternative-type bulk ZrO2-based
catalysts for nonoxidative propane dehydrogenation (PDH).
Currently, they belong to the state of the art catalysts owing to
their environmental compatibility, high activity, propene selectivity,
and durability. However, the structure–activity–selectivity
relationships are still not appropriately understood. To close such
gaps, we focused on elucidating the role of surface defects (coordinatively
unsaturated Zr (Zrcus) sites) and supported Rh nanoparticles
(NPs) in Rh/ZrO2 for activity and selectivity in the PDH
reaction. Relevant physicochemical properties were analyzed by complementary
experimental techniques, while details of catalyst functioning on
an elementary-step level were derived from density functional theory
calculations. Two types of Zrcus sites responsible for
propane dehydrogenation were suggested to exist on the surface of
ZrO2. Those located at Rh NPs reveal higher intrinsic activity
owing to the positive effect of the metal on hydrogen desorption,
which is the rate-limiting step in the PDH reaction over bare ZrO2. However, when the reduction degree of ZrO2 is
increased, propene strongly adsorbs on Rh, resulting in blockage of
sites for hydrogen recombination. Consequently, the accelerating effect
of the metal is hindered. Moreover, the strong propene adsorption
plays a negative role in propene selectivity due to favoring conversion
of the adsorbed propene into coke. The most active Rh/ZrO2 catalyst revealed higher activity in comparison with the state of
the art Ru/YZrOx and an analogue of commercial
K-CrOx/Al2O3. It
was also durable over 60 PDH/regeneration cycles at 550, 600, and
625 °C lasting 11 days in total.