4.8 Article

Weakening the Metal-Support Interactions of M/CeO2 (M = Co, Fe, Ni) Using a NH3-Treated CeO2 Support for an Enhanced Water-Gas Shift Reaction

期刊

ACS CATALYSIS
卷 12, 期 19, 页码 11942-11954

出版社

AMER CHEMICAL SOC
DOI: 10.1021/acscatal.2c0366411942

关键词

Co; CeO2 catalyst; water-gas shift reaction; NH3 treatment process; weakened metal-support interaction; oxygen vacancies

资金

  1. National Natural Science Foundation of China
  2. National Key R&D Program of China
  3. Beijing National Laboratory for Molecular Sciences
  4. [21832001]
  5. [2021YFA1501100]
  6. [BNLMS- CXXM-202104]

向作者/读者索取更多资源

The metal-support interface plays a crucial role in heterogeneous catalysis by influencing catalytic efficiency. This study presents a strategy to optimize the interfacial activity of Co/ CeO2 catalysts for the water-gas shift reaction (WGSR) through a simple NH3 treatment process. The NH3 treatment weakens the metal-support interaction and induces oxygen vacancy generation, resulting in improved CO adsorption and activation ability. This combination of effects enhances the catalytic efficiency for the WGSR via the carboxyl pathway at low temperatures.
The metal-support interface plays a crucial role in heterogeneous catalysis. The modulation of the metal-support interaction (MSI) affords the possibility of promoting the catalytic efficiency per active site. Here, we report a strategy to modulate the interfacial interaction and then optimize the interfacial activity of Co/ CeO2 catalysts for the water-gas shift reaction (WGSR) by a facile NH3 treatment process for the CeO2 support. The sample of Co/800N-CeO2 treated at 800 degrees C exhibited the highest reaction rate of 260 mu molCO/(gCo s), which was 23.8 times higher than the rate of the untreated Co/CeO2 sample. A combination of ex situ and in situ characterizations suggested that addition of the NH3 treatment process did not only weaken the metal-support interaction between the Co species and CeO2 support to strengthen CO adsorption and CO activation ability but also induced oxygen vacancy generation under reaction conditions to accelerate H2O activation. Both worked together in promoting the catalytic efficiency for the WGSR via the carboxyl pathway at a low temperature. It was worth mentioning that the N species of the CeO2 support introduced by the NH3 treatment was removed after changing the catalyst structure under reaction conditions. The interfacial structure was robust in a 60 h test at 400 degrees C due to the coexistence mechanism of carboxyl and formate pathways avoiding the poisoning effect of formate species on the active sites. The construction of active interfaces could be extended to Fe/CeO2 and Ni/CeO2 catalysts and could bring great promise in the design of the interfacial structure of supported catalysts in wide applications including chemical transformation reactions and industrial catalysis.

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