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Catalytic performance of manganese doped CuO-CeO2 catalysts for selective oxidation of CO in hydrogen-rich gas
被引:114
作者:
Guo, Xiaolin
[1
]
Li, Jing
[1
]
Zhou, Renxian
[1
]
机构:
[1] Zhejiang Univ, Inst Catalysis, Hangzhou 310028, Zhejiang, Peoples R China
来源:
关键词:
Hydrogen purification;
CO selective oxidation;
CuO-MnOx-CeO2;
catalysts;
Mn doping;
Calcination temperature;
MIXED-OXIDE CATALYSTS;
IN-SITU DRIFTS;
PREFERENTIAL OXIDATION;
EXCESS HYDROGEN;
CALCINATION TEMPERATURE;
CARBON-MONOXIDE;
METAL;
CUO/CEO2;
MN;
CU;
D O I:
10.1016/j.fuel.2015.09.043
中图分类号:
TE [石油、天然气工业];
TK [能源与动力工程];
学科分类号:
0807 ;
0820 ;
摘要:
Manganese doped CuO-CeO2 catalysts (CuO-MnOx-CeO2) with Mn/Cu molar ratio of 1: 5 and variable calcination temperatures were prepared by a hydrothermal method and used for selective oxidation of CO in hydrogen-rich gas, characterized by various techniques. An appropriate calcination temperature shows an essential stimulative effect on CuO-MnOx-CeO2 catalysts for the CO-PROX. The catalyst calcined at 500 degrees C displays the highest low-temperature catalytic activity (T-50% = 74 degrees C) and the broadest operating temperature "window" (CO conversion > 99.0%, 110-140 degrees C). XRD and UV-Raman results reveal that an appropriate calcination temperature can promote the formation of Cu-Mn-Ce-O ternary oxide solid solution, adjust the degree of crystallinity of CeO2 and enhance the formation of oxygen vacancies. H-2-TPR and XPS demonstrate that calcining at 500 degrees C improves the active reducing species in both bulk and surface of the catalyst. In situ DRIFTS suggests that Cu+ species which possess strong interaction with ceria also can be facilitated with a suitable calcination temperature. (C) 2015 Elsevier Ltd. All rights reserved.
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页码:56 / 64
页数:9
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