Cu/ZnO and Cu/ZnO/ZrO2 catalysts used for methanol steam reforming

被引:53
作者
Sanches, S. G. [1 ]
Huertas Flores, J. [1 ]
Pais da Silva, M., I [1 ]
机构
[1] Pontificia Univ Catolica Rio de Janeiro, Dept Quim, Rua Marques de Sao Vicente 225, BR-22453900 Gavea, RJ, Brazil
关键词
Cu/Zn/Zr catalyst; Methanol steam reforming; XANES; EXAFS; Hydrogen production; GAS SHIFT REACTION; IN-SITU INVESTIGATIONS; ZINC-OXIDE; HOMOGENEOUS PRECIPITATION; CU-ZNO/ZRO2; CATALYSTS; HYDROGEN-PRODUCTION; CO2; HYDROGENATION; CU/ZRO2; ZNO CATALYSTS; PART I;
D O I
10.1016/j.mcat.2018.05.012
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Cu/ZnO and Cu/ZnO/ZrO2 catalysts were prepared by co-precipitation method and used in methanol steam reforming at 250 degrees C. The catalysts were characterized by N-2 adsorption, X-ray diffraction (XRD), temperature programmed reduction (TPR), H-2 temperature-programmed desorption (H-2-TPD), transmission electron microscopy (TEM), X-ray absorption near-edge structure (XANES) and extended X-ray absorption fine structure (EXAFS). ZrO2 affect the textural, structural and morphological properties of the CuO/ZnO catalyst. ZrO2 nanoclusters or amorphous material was found in Zr-based catalyst which role was to prevent the CuO and ZnO crystallite growth causing a microstrain in Cu and Zn oxides lattice. This effect facilitated the formation of exposed CuO species, which were easier to reduce and favored the catalytic performance of Zr-based catalyst. Monoclinic ZrO2 found in Zr-based catalyst decrease the CO formation deeply because of the higher capacity of monoclinical ZrO2 to adsorbed CO. The Cu2O active site found in CuO/ZnO catalyst was not more efficient than active sites in Zr-based catalyst. The results confirmed that the interactions between Cu and ZnO/ZrO2 were different from those between Cu and ZnO.
引用
收藏
页码:55 / 62
页数:8
相关论文
共 54 条
[1]   Production of hydrogen from methanol over binary Cu/ZnO catalysts -: Part I.: Catalyst preparation and characterisation [J].
Agrell, J ;
Boutonnet, M ;
Melián-Cabrera, I ;
Fierro, JLG .
APPLIED CATALYSIS A-GENERAL, 2003, 253 (01) :201-211
[2]   Production of hydrogen from methanol over Cu/ZnO catalysts promoted by ZrO2 and Al2O3 [J].
Agrell, J ;
Birgersson, H ;
Boutonnet, M ;
Melián-Cabrera, I ;
Navarro, RM ;
Fierro, JLG .
JOURNAL OF CATALYSIS, 2003, 219 (02) :389-403
[3]   Solid-state interactions, adsorption sites and functionality of Cu-ZnO/ZrO2 catalysts in the CO2 hydrogenation to CH3OH [J].
Arena, Francesco ;
Italiano, Giuseppe ;
Barbera, Katia ;
Bordiga, Silvia ;
Bonura, Giuseppe ;
Spadaro, Lorenzo ;
Frusteri, Francesco .
APPLIED CATALYSIS A-GENERAL, 2008, 350 (01) :16-23
[4]   Synthesis, characterization and activity pattern of Cu-ZnO/ZrO2 catalysts in the hydrogenation of carbon dioxide to methanol [J].
Arena, Francesco ;
Barbera, Katia ;
Italiano, Giuseppe ;
Bonura, Giuseppe ;
Spadaro, Lorenzo ;
Frusteri, Francesco .
JOURNAL OF CATALYSIS, 2007, 249 (02) :185-194
[5]  
Avila G., 2008, CATAL COMMUN, V9, P2550
[6]   Influences of preparation methods of ZrO2 support and treatment conditions of Cu/ZrO2 catalysts on synthesis of methanol via CO hydrogenation [J].
Bai, Yongge ;
He, Dehua ;
Ge, Shaohui ;
Liu, Huimin ;
Liu, Jinyao ;
Huang, Wei .
CATALYSIS TODAY, 2010, 149 (1-2) :111-116
[7]   Hybrid Cu-ZnO-ZrO2/H-ZSM5 system for the direct synthesis of DME by CO2 hydrogenation [J].
Bonura, G. ;
Cordaro, M. ;
Spadaro, L. ;
Cannilla, C. ;
Arena, F. ;
Frusteri, F. .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2013, 140 :16-24
[8]   THE ROLE OF COPPER AND ZINC-OXIDE IN METHANOL SYNTHESIS CATALYSTS [J].
BURCH, R ;
GOLUNSKI, SE ;
SPENCER, MS .
JOURNAL OF THE CHEMICAL SOCIETY-FARADAY TRANSACTIONS, 1990, 86 (15) :2683-2691
[9]   THE ACTIVITY AND STATE OF THE COPPER SURFACE IN METHANOL SYNTHESIS CATALYSTS [J].
CHINCHEN, GC ;
WAUGH, KC ;
WHAN, DA .
APPLIED CATALYSIS, 1986, 25 (1-2) :101-107
[10]   Study of the reducibility of copper in CuO-ZnO catalysts by temperature-programmed reduction [J].
Fierro, G ;
LoJacono, M ;
Inversi, M ;
Porta, P ;
Cioci, F ;
Lavecchia, R .
APPLIED CATALYSIS A-GENERAL, 1996, 137 (02) :327-348