The influence of reduction temperature on the performance of ZrOx/Ni-MnOx/SiO2 catalyst for low-temperature CO2 reforming of methane

被引:47
作者
Yao, Lu [1 ]
Wang, Ye [2 ]
Shi, Jia [1 ]
Xu, Hualong [3 ]
Shen, Wei [3 ]
Hu, Changwei [1 ,2 ]
机构
[1] Sichuan Univ, Coll Chem, Minist Educ, Key Lab Green Chem & Technol, Chengdu 610064, Sichuan, Peoples R China
[2] Sichuan Univ, Coll Chem Engn, Chengdu 610065, Sichuan, Peoples R China
[3] Fudan Univ, Adv Mat Lab, Key Lab Mol Catalysis & Innovat Mat, Shanghai 200433, Peoples R China
基金
中国国家自然科学基金;
关键词
Methane; Carbon dioxide; Dry reforming; ZrOx/Ni-MnOx/SiO2; catalyst; Low temperature; Reduction temperature; CARBON-DIOXIDE; NI CATALYSTS; BIMETALLIC CATALYSTS; SUPPORT INTERACTION; CO/AL2O3; CATALYSTS; NI/SIO2; CATALYST; STABILITY; RESISTANCE; COKE; ADSORPTION;
D O I
10.1016/j.cattod.2016.05.031
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
ZrOx/Ni-MnOx/SiO2 catalyst for CO2 reforming of methane was prepared using impregnation method, and characterized by in situ DRIFTS, XRD, TEM, XPS and TG. Low-temperature activation of both methane and carbon dioxide was achieved over ZrOx/Ni-MnOx/SiO2 catalyst, and the catalytic activity was found to be dependent on the reduction temperature. It was found that after being reduced at 550 degrees C, the ZrOx/Ni-MnOx/SiO2 catalyst showed relative high content of surface Ni species and small particles of Ni species with a rather narrow particle size distribution. The ZrOx/Ni-MnOx/SiO2 catalyst reduced at 550 degrees C showed the highest catalytic activity, with 17.9% and 23.1% initial conversions of CH4 and CO2 at the reaction temperature of 500 degrees C, and the yield of H-2 and CO also reached the maximum value of 9.2% and 14.5%, respectively. In addition to the high catalytic activity, the ZrOx/Ni-MnOx/SiO2 catalyst also showed a quiet good stability at 500 degrees C. The initial and stable yields of H-2 and CO were 1.4% and 2.3% at the reaction temperature of 400 degrees C with the conversion of CH4 and CO2 being 2.2% and 4.9%, respectively. (C) 2016 Elsevier B.V. All rights reserved.
引用
收藏
页码:259 / 267
页数:9
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