The Role of Reducibility of PtGaO <i> <sub>x</sub> </i> ‐Based Catalysts for Efficient and Durable Propane Dehydrogenation

K Kai Wu (BNLMS, College of Chemistry and Molecular Engineering) V Vita A. Kondratenko M Mingxia Zhou D Dmitry E. Doronkin (Institute for Chemical Technology and Polymer Chemistry, and Institute of Catalysis Research and Technology Karlsruhe Institute of Technology Kaiserstr. 12 D‐76131 Karlsruhe Germany) S Stephan Bartling Q Qiyang Zhang S Shanlei Han (State Key Laboratory of Heavy Oil Processing China University of Petroleum Beijing 102249 China) X Xin Jia (School of Chemistry, Engineering Research Center of Energy Storage Materials and Devices of Ministry of Education, National Innovation Platform (Center) for Industry-Education Integration of Energy Storage Technology) Q Qi Liu D Dong Xiong (State Key Laboratory of Heavy Oil Processing China University of Petroleum Beijing 102249 China) C Chunming Xu (State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Chang Ping, Beijing 102249, China) G Guiyuan Jiang D Dan Zhao U Uwe Rodemerck (Department: Advanced Methods for Applied Catalysis Leibniz‐Institut für Katalyse e. V Albert‐Einstein‐Str. 29a 18059 Rostock Germany) D David Linke (Department: Advanced Methods for Applied Catalysis Leibniz‐Institut für Katalyse e. V Albert‐Einstein‐Str. 29a 18059 Rostock Germany) E Evgenii V. Kondratenko (Advanced Methods for Applied Catalysis, Leibniz-Institut für Katalyse, Albert Einstein-Str. 29a, 18059 Rostock, Germany)

Abstract

Abstract Although PtGaO x ‐containing catalysts are active and selective in the non‐oxidative dehydrogenation of propane (PDH) to propylene, they suffer from rapid deactivation and, especially, inability to recover their initial performance in a series of PDH/oxidative regeneration cycles, characteristics that are highly relevant to commercialization. Herein, we identified reducibility of GaO x as the key descriptor affecting the above catalyst features. Oxidized GaO x species are more active than reduced GaO x in the recombination of two H species formed from propane, which is the rate‐limiting step in the PDH reaction. This process is further accelerated by Pt. The reduction of GaO x with time on propane stream leads to catalyst deactivation. Easily reducible GaO x also tend to form PtGaO x under PDH conditions, from which Pt atoms present in fresh catalysts cannot be completely recovered during oxidative regeneration, which is detrimental to catalyst durability. Regardless of the reaction atmosphere, Pt single atoms exist on the surface of PtGaO x ‐containing catalysts with hardly reducible GaO x . Based on the knowledge derived, we developed a catalyst with 500 ppm Pt on the surface of mixed GaAlO x , which outperforms almost all previous PtGaO x ‐containing catalysts in terms of space‐time yield of propylene formation and shows durable operation under industrially relevant conditions.

Article Details

Volume / Issue Vol. 64, Issue 31
Published July 28, 2025
ISSN 1433-7851
Publisher Wiley

Journal Info

Angewandte Chemie International Edition

Wiley

ISSN: 1433-7851 Physical Sciences

Authors (16)

K

Kai Wu

BNLMS, College of Chemistry and Molecular Engineering

V

Vita A. Kondratenko

M

Mingxia Zhou

D

Dmitry E. Doronkin

Institute for Chemical Technology and Polymer Chemistry, and Institute of Catalysis Research and Technology Karlsruhe Institute of Technology Kaiserstr. 12 D‐76131 Karlsruhe Germany

S

Stephan Bartling

Q

Qiyang Zhang

S

Shanlei Han

State Key Laboratory of Heavy Oil Processing China University of Petroleum Beijing 102249 China

X

Xin Jia

School of Chemistry, Engineering Research Center of Energy Storage Materials and Devices of Ministry of Education, National Innovation Platform (Center) for Industry-Education Integration of Energy Storage Technology

Q

Qi Liu

D

Dong Xiong

State Key Laboratory of Heavy Oil Processing China University of Petroleum Beijing 102249 China

C

Chunming Xu

State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Chang Ping, Beijing 102249, China

G

Guiyuan Jiang

D

Dan Zhao

U

Uwe Rodemerck

Department: Advanced Methods for Applied Catalysis Leibniz‐Institut für Katalyse e. V Albert‐Einstein‐Str. 29a 18059 Rostock Germany

D

David Linke

Department: Advanced Methods for Applied Catalysis Leibniz‐Institut für Katalyse e. V Albert‐Einstein‐Str. 29a 18059 Rostock Germany

E

Evgenii V. Kondratenko

Advanced Methods for Applied Catalysis, Leibniz-Institut für Katalyse, Albert Einstein-Str. 29a, 18059 Rostock, Germany