Effect of steam and carbon dioxide pretreatments on methane decomposition and carbon gasification over doped-ceria supported nickel catalyst

被引:54
作者
Huang, TJ [1 ]
Yu, TC [1 ]
机构
[1] Natl Tsing Hua Univ, Dept Chem Engn, Hsinchu 300, Taiwan
关键词
steam; carbon dioxide; pretreatment; methane decomposition; carbon gasification; doped ceria; nickel catalyst;
D O I
10.1007/s10562-005-5852-8
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
Effects of steam (H2O) and carbon dioxide (CO2) pretreatments on methane (CH4) decomposition and carbon gasification over doped-ceria supported nickel catalysts have been studied from 400 to 500 degrees C. The doped ceria employed were gadolinia-doped ceria and samaria-doped ceria. Results indicate that a drastic increase of both H2O and CO2 dissociation activities occurs as the temperature increases from 450 to 500 degrees C. The formation of the surface hydroxyl species during H2O treatment inhibits the followed CH4 decomposition. CO but no CO2 was formed during CH4 reaction after H2O treatment. Carbon deposition during CH4 decomposition is quite large but can be removed via gasification with afterward CO2 treatment. However, some of the deposited carbon species is in a form which can not be removed with CO2 treatment but can be removed with O-2 treatment. And, higher values of the oxygen-ion conductivity and the density of the surface oxygen vacancies lead to higher activities for all dissociation and decomposition reactions.
引用
收藏
页码:175 / 181
页数:7
相关论文
共 18 条
[11]   Steam reforming of methane over nickel catalysts at low reaction temperature [J].
Matsumura, Y ;
Nakamori, T .
APPLIED CATALYSIS A-GENERAL, 2004, 258 (01) :107-114
[12]   A highly active catalyst, Ni/Ce-ZrO2/θ-Al2O3, for on-site H2 generation by steam methane reforming:: pretreatment effect [J].
Oh, YS ;
Roh, HS ;
Jun, KW ;
Baek, YS .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2003, 28 (12) :1387-1392
[13]   Catalytic steam reforming of methane over Ce0.9Gd0.1O2-x [J].
Ramírez-Cabrera, E ;
Atkinson, A ;
Chadwick, D .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2004, 47 (02) :127-131
[14]   Highly active and stable Ni/Ce-ZrO2 catalyst for H2 production from methane [J].
Roh, HS ;
Jun, KW ;
Dong, WS ;
Chang, JS ;
Park, SE ;
Joe, YI .
JOURNAL OF MOLECULAR CATALYSIS A-CHEMICAL, 2002, 181 (1-2) :137-142
[15]   Evidence for oxidation of ceria by CO2 [J].
Sharma, S ;
Hilaire, S ;
Vohs, JM ;
Gorte, RJ ;
Jen, HW .
JOURNAL OF CATALYSIS, 2000, 190 (01) :199-204
[16]   Effects of carbon deposition and de-coking treatments on the activation of CH4 and CO2 in CO2 reforming of CH4 over Ni/yttria-doped ceria catalysts [J].
Wang, JB ;
Wu, YS ;
Huang, TJ .
APPLIED CATALYSIS A-GENERAL, 2004, 272 (1-2) :289-298
[17]   Study of carbon dioxide reforming of methane over Ni/yttria-doped ceria and effect of thermal treatments of support on the activity behaviors [J].
Wang, JB ;
Hsiao, SZ ;
Huang, TJ .
APPLIED CATALYSIS A-GENERAL, 2003, 246 (02) :197-211
[18]   Study of ceria-supported nickel catalyst and effect of yttria doping on carbon dioxide reforming of methane [J].
Wang, JSB ;
Tai, YL ;
Dow, WP ;
Huang, TJ .
APPLIED CATALYSIS A-GENERAL, 2001, 218 (1-2) :69-79