Hydrogen production through oxidative steam reforming of ethanol over Ni-based catalysts derived from La1-xCexNiO3 perovskite-type oxides

被引:99
作者
de Lima, Sania M. [1 ,2 ]
da Silva, Adriana M. [1 ]
da Costa, Lidia O. O. [1 ]
Assaf, Jose M. [3 ]
Mattos, Lisiane V. [4 ]
Sarkari, Reema [5 ]
Venugopal, A. [5 ]
Noronha, Fabio B. [1 ]
机构
[1] Inst Nacl Tecnol INT, BR-20081312 Rio De Janeiro, Brazil
[2] Univ Fed Sao Paulo UNIFESP, Dept Ciencias Exatas & Terra, Setor Engn Quim, BR-09972270 Diadema, Brazil
[3] Univ Fed Sao Carlos UFSCar, Lab Catalise, BR-13565905 Sao Carlos, SP, Brazil
[4] Univ Fed Fluminense, BR-24210240 Niteroi, RJ, Brazil
[5] Indian Inst Chem Technol, Inorgan & Phys Chem Div, Hyderabad 500607, Andhra Pradesh, India
关键词
Perovskite-type oxides; Hydrogen production; Ethanol oxidative steam reforming; Deactivation mechanism; Nickel catalyst; NOBLE-METAL CATALYSTS; BIO-ETHANOL; NICKEL-CATALYSTS; REACTION-MECHANISM; MIXED OXIDES; FUEL-CELLS; METHANE; PERFORMANCE; SUPPORT; DEACTIVATION;
D O I
10.1016/j.apcatb.2012.03.017
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
This paper investigates the effect of lanthanum substitution by cerium oxide on the performance of La1-xCexNiO3 (x = 0, 0.05, 0.1, 0.4, 0.7 and 1.0) perovskite-type oxide precursor for the oxidative steam reforming of ethanol. All catalysts are active and selective to hydrogen but carbon deposition occurs except for La0.90Ce0.10NiO3. Increasing the Ce content decreases the amount of carbon deposited, which passes through a minimum at around 10 wt% of Ce and then increases. The higher resistance to carbon formation on La0.90Ce0.10NiO3 catalyst is due to the smaller Ni crystallite size. Furthermore, the support also plays an important role on catalyst stability during ethanol conversion reaction. The reduced La0.9Ce0.1NiO3 sample exhibits the highest amount of oxygen vacancies, which decreases as ceria content increases. This highly mobile oxygen reacts with carbon species as soon as it forms, and thus keeps the metal surface free of carbon, inhibiting deactivation. (c) 2012 Elsevier B.V. All rights reserved.
引用
收藏
页码:1 / 9
页数:9
相关论文
共 43 条
[1]   Bio-ethanol catalytic steam reforming over supported metal catalysts [J].
Auprêtre, F ;
Descorme, C ;
Duprez, D .
CATALYSIS COMMUNICATIONS, 2002, 3 (06) :263-267
[2]   Hydrogen production from ethanol over Ir/CeO2 catalysts:: A comparative study of steam reforming, partial oxidation and oxidative steam reforming [J].
Cai, Weijie ;
Wang, Fagen ;
Zhan, Ensheng ;
Van Veen, A. C. ;
Mirodatos, Claude ;
Shen, Wenjie .
JOURNAL OF CATALYSIS, 2008, 257 (01) :96-107
[3]   Hydrogen produced from ethanol for internal reforming molten carbonate fuel cell [J].
Cavallaro, S ;
Mondello, N ;
Freni, S .
JOURNAL OF POWER SOURCES, 2001, 102 (1-2) :198-204
[4]   Autothermal reforming of ethanol for hydrogen production over perovskite LaNiO3 [J].
Chen, Hongqing ;
Yu, Hao ;
Peng, Feng ;
Yang, Guangxing ;
Wang, Hongjuan ;
Yang, Jian ;
Tang, Yong .
CHEMICAL ENGINEERING JOURNAL, 2010, 160 (01) :333-339
[5]   Regenerable and durable catalyst for hydrogen production from ethanol steam reforming [J].
Chen, S. Q. ;
Li, Y. D. ;
Liu, Y. ;
Bai, X. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2011, 36 (10) :5849-5856
[6]   Oxidative steam reforming of ethanol over carbon nanofiber supported Co catalysts [J].
da Silva, Andre L. M. ;
Mattos, Lisiane V. ;
den Breejen, Johan P. ;
Bitter, Johannes H. ;
de Jong, Krijn P. ;
Noronha, Fabio B. .
CATALYSIS TODAY, 2011, 164 (01) :262-267
[7]   Evaluation of the performance of Ni/La2O3 catalyst prepared from LaNiO3 perovskite-type oxides for the production of hydrogen through steam reforming and oxidative steam reforming of ethanol [J].
de Lima, Sania M. ;
da Silva, Adriana M. ;
da Costa, Lidia O. O. ;
Assaf, Jose M. ;
Jacobs, Gary ;
Davis, Burtron H. ;
Mattos, Lisiane V. ;
Noronha, Fabio B. .
APPLIED CATALYSIS A-GENERAL, 2010, 377 (1-2) :181-190
[8]   Study of catalyst deactivation and reaction mechanism of steam reforming, partial oxidation, and oxidative steam reforming of ethanol over Co/CeO2 catalyst [J].
de Lima, Sania M. ;
da Silva, Adriana M. ;
da Costa, Lidia O. O. ;
Graham, Uschi M. ;
Jacobs, Gary ;
Davis, Burtron H. ;
Mattos, Lisiane V. ;
Noronha, Fabio B. .
JOURNAL OF CATALYSIS, 2009, 268 (02) :268-281
[9]   Ethanol decomposition and steam reforming of ethanol over CeZrO2 and Pt/CeZrO2 catalyst: Reaction mechanism and deactivation [J].
de Lima, Sania M. ;
Silva, Adriana M. ;
Graham, Uschi M. ;
Jacobs, Gary ;
Davis, Burtron H. ;
Mattos, Lisiane V. ;
Noronha, Fabio B. .
APPLIED CATALYSIS A-GENERAL, 2009, 352 (1-2) :95-113
[10]   Adsorption and reactions of ethanol and ethanol-water mixture on alumina-supported Pt catalysts [J].
Domok, M. ;
Toth, M. ;
Rasko, J. ;
Erdohelyi, A. .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2007, 69 (3-4) :262-272