Catalytic performance of manganese doped CuO-CeO2 catalysts for selective oxidation of CO in hydrogen-rich gas

被引:115
作者
Guo, Xiaolin [1 ]
Li, Jing [1 ]
Zhou, Renxian [1 ]
机构
[1] Zhejiang Univ, Inst Catalysis, Hangzhou 310028, Zhejiang, Peoples R China
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.
引用
收藏
页码:56 / 64
页数:9
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