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Gaseous CO and toluene co-oxidation over monolithic core-shell CoO-based hetero-structured catalysts
The inhibiting effects of using platinum group metal (PGM) catalysts are universal problems for the co-oxidation of CO and hydrocarbons (HCs), resulting in a higher temperature to handle CO and HCs pollutants. Herein, this work focuses on designing a series of Co 3 O 4 -based catalysts whose catalyt...
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Published in: | Journal of materials chemistry. A, Materials for energy and sustainability Materials for energy and sustainability, 2019-07, Vol.7 (27), p.16197-1621 |
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Main Authors: | , , , , , , , , , |
Format: | Article |
Language: | |
Online Access: | Get full text |
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Summary: | The inhibiting effects of using platinum group metal (PGM) catalysts are universal problems for the co-oxidation of CO and hydrocarbons (HCs), resulting in a higher temperature to handle CO and HCs pollutants. Herein, this work focuses on designing a series of Co
3
O
4
-based catalysts whose catalytic activities in the individual oxidation and co-oxidation of CO and toluene are comparable to Pt-based catalysts. The catalytic behaviors of CO and toluene oxidation over Pt/Al
2
O
3
are mutually inhibited in the presence of CO and toluene, in which CO oxidation could improve catalytic toluene degradation over Co
3
O
4
-based catalysts, as its CO oxidation is negatively affected by toluene oxidation. In addition, under the coexistence of CO and toluene, the light-off temperature of toluene oxidation on both Co
3
O
4
-based and Pt-based catalysts consistently followed that of CO oxidation. Among all monolithic core-shell Co
3
O
4
-based catalysts, these catalysts introduced to different elements (Co, Mn and Cu) showed the distinct promotion of CO and toluene oxidation, and the Co
3
O
4
@Co
3
O
4
catalyst exhibited the most outstanding catalytic performances for the individual oxidation and co-oxidation of CO and toluene. In addition, the physicochemical properties of core-shell hetero-structured catalysts are further characterized in detail by XRD, BET, SEM, TEM, H
2
-TPR, XPS, O
2
-TPD and Raman spectrometry. It was confirmed that the excellent performance of the Co
3
O
4
@Co
3
O
4
catalyst is mainly associated with the surface area, surface oxygen vacancies and low-temperature reducibility, whose prominent oxygen vacancy and low-temperature reducibility are induced by the synergistic effect of different Co
3
O
4
structures.
In situ
DRIFT spectroscopy confirmed that bidentate carbonate species and benzoate species were considered as a reaction intermediate species in CO and toluene oxidation, respectively. Moreover, there is a competitive adsorption-reaction on the active sites of Co
3
O
4
-based catalysts for CO and toluene, but the reaction mechanism of CO/toluene oxidation may be mutually independent under the coexistence of CO and toluene.
Gaseous CO co-existence could improve catalytic toluene oxidation over Co
3
O
4
-based catalysts, and the reaction mechanism on the CO/toluene oxidation may be mutually independent in the presence of both CO and toluene. |
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ISSN: | 2050-7488 2050-7496 |
DOI: | 10.1039/c9ta03750k |