Effect of calcium dopant on catalysis of Ir/La2O3 for hydrogen production by oxidative steam reforming of glycerol

被引:29
作者
Yang, Guangxing [1 ]
Yu, Hao [1 ]
Huang, Xiaoya [1 ]
Peng, Feng [1 ]
Wang, Hongjuan [1 ]
机构
[1] S China Univ Technol, Sch Chem & Chem Engn, Guangzhou 510640, Guangdong, Peoples R China
基金
国家高技术研究发展计划(863计划);
关键词
Iridium; La2O2Co3; Reforming; Glycerol; Calcium; NICKEL-CATALYSTS; SYNTHESIS GAS; NI/AL2O3; CATALYSTS; FILAMENTOUS CARBON; RENEWABLE HYDROGEN; METHANE; ETHANOL; CONVERSION; REACTIVITY; STABILITY;
D O I
10.1016/j.apcatb.2012.08.003
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
The superfluous glycerol derived from biodiesel production can be a low-cost feedstock for hydrogen production via reforming technology. In this work, a La2O3 supported iridium catalyst was employed to catalyze the oxidative steam reforming of glycerol (OSRG) for hydrogen production, in the range of S/C ratio of 1-3,C/O ratio of 0.75-1 and 550-750 degrees C. The catalyst was modified with Na, Mg and Ca to optimize the catalytic performance in OSRG reaction. It was found that Ca is promising in promoting Ir/La2O3 catalyst for OSRG, offering excellent activity, hydrogen selectivity and stability. By combining multiple techniques, i.e. XRD, FTIR, Raman, XPS, H-2-TPR, CO2-TPD and HRTEM, the Ca modified Ir/La2O3 catalyst was characterized to understand the role of Ca promoter. Multi-functions of Ca were demonstrated, including inducing structural defects of La2O2CO3, endowing the catalyst strong basicity and tuning the metal-support interaction, which make the catalyst highly resistant to coking and sintering, therefore performing excellent long-term stability for 100 h. (C) 2012 Elsevier B.V. All rights reserved.
引用
收藏
页码:89 / 98
页数:10
相关论文
共 55 条
[1]   Conversion of glycerol to hydrogen via a steam reforming process over nickel catalysts [J].
Adhikari, Sushil ;
Fernando, Sandun D. ;
To, S. D. Filip ;
Bricka, R. Mark ;
Steele, Philip H. ;
Haryanto, Agus .
ENERGY & FUELS, 2008, 22 (02) :1220-1226
[2]   Hydrogen production from glycerin by steam reforming over nickel catalysts [J].
Adhikari, Sushil ;
Fernando, Sandun D. ;
Haryanto, Agus .
RENEWABLE ENERGY, 2008, 33 (05) :1097-1100
[3]   Hydrogen production from glycerol: An update [J].
Adhikari, Sushil ;
Fernando, Sandun D. ;
Haryanto, Agus .
ENERGY CONVERSION AND MANAGEMENT, 2009, 50 (10) :2600-2604
[4]   STRUCTURE DETERMINATIONS OF LA2O2CO3-II AND THE UNUSUAL DISORDERED PHASE LA2O2.52(CO3)0.74LI0.52 USING POWDER DIFFRACTION [J].
ATTFIELD, JP ;
FEREY, G .
JOURNAL OF SOLID STATE CHEMISTRY, 1989, 82 (01) :132-138
[5]  
Bando KK, 1998, APPL CATAL A-GEN, V175, P67
[6]   Physicochemical and catalytic properties in methane combustion of La1-xCaxMnO3±y (0≤X≤1; -0.04≤y≤0.24) [J].
Batis, NH ;
Delichere, P ;
Batis, H .
APPLIED CATALYSIS A-GENERAL, 2005, 282 (1-2) :173-180
[7]   Ethanol steam reforming over Co-based catalysts: Investigation of cobalt coordination environment under reaction conditions [J].
Bayram, Burcu ;
Soykal, I. Ilgaz ;
von Deak, Dieter ;
Miller, Jeffrey T. ;
Ozkan, Umit S. .
JOURNAL OF CATALYSIS, 2011, 284 (01) :77-89
[8]   Efficient hydrogen production from ethanol and glycerol by vapour-phase reforming processes with new cobalt-based catalysts [J].
Brum Pereira, Evandro ;
Ramirez de la Piscina, Pilar ;
Homs, Narcis .
BIORESOURCE TECHNOLOGY, 2011, 102 (03) :3419-3423
[9]   Nickel catalysts applied in steam reforming of glycerol for hydrogen production [J].
Buffoni, Ivana N. ;
Pompeo, Francisco ;
Santori, Gerardo F. ;
Nichio, Nora N. .
CATALYSIS COMMUNICATIONS, 2009, 10 (13) :1656-1660
[10]   Hydrogen production from glycerol by reforming in supercritical water over Ru/Al2O3 catalyst [J].
Byrd, Adam J. ;
Pant, K. K. ;
Gupta, Ram B. .
FUEL, 2008, 87 (13-14) :2956-2960