Achievement of hydrogen production from autothermal steam reforming of methanol over Cu-loaded mesoporous CeO2 and Cu-loaded mesoporous CeO2-ZrO2 catalysts

被引:51
作者
Jampa, Sureerat [1 ]
Jamieson, Alexander M. [2 ]
Chaisuwan, Thanyalalz [1 ]
Luengnaruemitchai, Apanee [1 ]
Wongkasemjit, Sujitra [1 ]
机构
[1] Chulalongkorn Univ, Petr & Petrochem Coll, Bangkok 10330, Thailand
[2] Case Western Reserve Univ, Dept Macromol Sci & Engn, Cleveland, OH 44106 USA
关键词
H-2; production; Autothermal steam reforming of methanol; Mesoporous CeO2; Mesoporous CeO2-ZrO2; Cu-CeO2; Cu-CeO2-ZrO2; FUEL-CELLS; SELECTIVE PRODUCTION; CUO-CEO2; CATALYSTS; PARTIAL OXIDATION; CUZNAL(ZR)-OXIDE CATALYSTS; COMBUSTION METHOD; SOLID-SOLUTIONS; CARBON-DIOXIDE; ETHANOL; OXIDE;
D O I
10.1016/j.ijhydene.2017.05.022
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
Hydrogen production by oxidative steam reforming of methanol (OSRM) or autothermal steam reforming of methanol (ASRM) was investigated over Cu-loaded mesoporous CeO2 and Cu-loaded mesoporous CeO2-ZrO2 catalysts, synthesized via a nanocasting process using MCM-48 as a hard template, followed by a deposition-precipitation technique. Various Cu contents were loaded on the mesoporous CeO2 and CeO2-ZrO2 supports. The fresh and spent catalysts were characterized by N-2 adsorption-desorption, X-ray diffraction, temperature-programmed oxidation, and X-ray photoelectron spectroscopy. The ASRM results showed that 9 wt% Cu loading onto mesoporous CeO2 and CeO2-ZrO2 provided the best catalytic performance with 100% methanol conversion and 60% H-2 yield at 350 degrees and 300 degrees C, respectively. Furthermore, the time-on-stream stability testing of the 9 wt % Cu loading catalyst was at 168 h, and the CO selectivity of these two catalysts indicated that the addition of ZrO2 into the catalyst reduced the CO selectivity during the ASRM process. (C) 2017 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:15073 / 15084
页数:12
相关论文
共 53 条
[1]   Production of hydrogen from methanol over binary Cu/ZnO catalysts - Part II. Catalytic activity and reaction pathways [J].
Agrell, J ;
Boutonnet, M ;
Fierro, JLG .
APPLIED CATALYSIS A-GENERAL, 2003, 253 (01) :213-223
[2]   Partial oxidation of methanol to produce hydrogen over Cu-Zn-based catalysts [J].
Alejo, L ;
Lago, R ;
Pena, MA ;
Fierro, JLG .
APPLIED CATALYSIS A-GENERAL, 1997, 162 (1-2) :281-297
[3]   Effect of synthesis parameters on catalytic properties of CuO-CeO2 [J].
Avgouropoulos, George ;
Ioannides, Theophilos .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2006, 67 (1-2) :1-11
[4]   Oxidative steam reforming of ethanol over Ni/CeO2-ZrO2 catalyst [J].
Biswas, Prakash ;
Kunzru, Deepak .
CHEMICAL ENGINEERING JOURNAL, 2008, 136 (01) :41-49
[5]   Methanol reforming for fuel-cell applications: development of zirconia-containing Cu-Zn-Al catalysts [J].
Breen, JP ;
Ross, JRH .
CATALYSIS TODAY, 1999, 51 (3-4) :521-533
[6]  
Brown LF, 2001, INT J HYDROGEN ENERG, V26, P381, DOI 10.1016/S0360-3199(00)00092-6
[7]   Technology up date and new strategies on fuel cells [J].
Cacciola, G ;
Antonucci, V ;
Freni, S .
JOURNAL OF POWER SOURCES, 2001, 100 (1-2) :67-79
[8]   Ce and La modification of mesoporous Cu-Ni/SBA-15 catalysts for hydrogen production through ethanol steam reforming [J].
Calles, J. A. ;
Carrero, A. ;
Vizcaino, A. J. .
MICROPOROUS AND MESOPOROUS MATERIALS, 2009, 119 (1-3) :200-207
[9]   Organized mesoporous alumina: synthesis, structure and potential in catalysis [J].
Cejka, J .
APPLIED CATALYSIS A-GENERAL, 2003, 254 (02) :327-338
[10]   PEM fuel cells for transportation and stationary power generation applications [J].
Cleghorn, SJC ;
Ren, X ;
Springer, TE ;
Wilson, MS ;
Zawodzinski, C ;
Zawodzinski, TA ;
Gottesfeld, S .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 1997, 22 (12) :1137-1144