Nickel-based ceria, zirconia, and ceria-zirconia catalytic systems for low-temperature carbon dioxide reforming of methane

被引:136
作者
Kumar, Prashant
Sun, Yanping
Idem, Raphael O. [1 ]
机构
[1] Univ Regina, Fac Engn, Hydogen Prod Res Grp, Proc Syst Engn, Regina, SK S4S 0A2, Canada
[2] HTC Pure Energy, Regina, SK S4P 0S7, Canada
关键词
D O I
10.1021/ef7002409
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Carbon dioxide reforming of methane (CDRM) was studied over a variety of ZrO2-, ceria-doped ZrO2-, and CeO2-ZrO2-supported Ni catalysts. Different techniques were used to prepare supports material having different physicochemical properties, and a correlation was established to show the importance of a robust support material. Various characterization of the catalyst further established that the coking behavior of the catalyst depends on the support preparation techniques. Compared to zirconia and ceria-doped zirconia, the use of ceria-zirconia (CexZr1-xO2) solid solution as a support prepared by using a surfactant was found to be the most stable for low-temperature CDRM. It seems the inhibition of reactions leading to carbon deposition is prominent in system having ZrO2. Temperature-programmed oxidation (TPO) experiments indicated excellent resistance toward carbon formation for Ni supported on CexZr1-xO2 compared with other catalysts studied. H-2-TPR (temperature-programmed reduction) analyses also showed that the stability of Ce-x,Zr1-xO2 solid solution is a function of its enhanced reducibility at lower temperatures as compared to either pure ceria or ceria-doped ZrO2. Based on all the catalysts studied, 5% Ni Ce0.6Zr0.4O2 was found to be the best catalyst as activity was stable for up to 100 It at 650 and 700 degrees C, while at 800 degrees C the catalyst activity remained stable for more than 200 h.
引用
收藏
页码:3113 / 3123
页数:11
相关论文
共 36 条
[21]   Methane reforming with CO2 over Ni/ZrO2-CeO2 catalysts prepared by sol-gel [J].
Montoya, JA ;
Romero-Pascual, E ;
Gimon, C ;
Del Angel, P ;
Monzón, A .
CATALYSIS TODAY, 2000, 63 (01) :71-85
[22]   Kinetic study of the catalytic carbon dioxide reforming of methane to synthesis gas over Ni-K/CeO2-Al2O3 catalyst [J].
Nandini, A. ;
Pant, K. K. ;
Dhingra, S. C. .
APPLIED CATALYSIS A-GENERAL, 2006, 308 (119-127) :119-127
[23]   Direct partial oxidation of methane to synthesis gas by cerium oxide [J].
Otsuka, K ;
Wang, Y ;
Sunada, E ;
Yamanaka, I .
JOURNAL OF CATALYSIS, 1998, 175 (02) :152-160
[24]   Catalytic oxidation of methane over CeO2-ZrO2 mixed oxide solid solution catalysts prepared via urea hydrolysis [J].
Pengpanich, S ;
Meeyoo, V ;
Rirksomboon, T ;
Bunyakiat, K .
APPLIED CATALYSIS A-GENERAL, 2002, 234 (1-2) :221-233
[25]   Study of Ni and Pt catalysts supported on α-Al2O3 and ZrO2 applied in methane reforming with CO2 [J].
Pompeo, Francisco ;
Nichio, Nora N. ;
Souza, Mariana M. V. M. ;
Cesar, Deborah V. ;
Ferretti, Osmar A. ;
Schmal, Martin .
APPLIED CATALYSIS A-GENERAL, 2007, 316 (02) :175-183
[26]   Carbon dioxide reforming of methane over co-precipitated Ni-Ce-ZrO2 catalysts [J].
Potdar, HS ;
Roh, HS ;
Jun, KW ;
Ji, M ;
Liu, ZW .
CATALYSIS LETTERS, 2002, 84 (1-2) :95-100
[27]   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
[28]   Carbon dioxide reforming of methane over Ni incorporated into Ce-ZrO2 catalysts [J].
Roh, HS ;
Potdar, HS ;
Jun, KW ;
Kim, JW ;
Oh, YS .
APPLIED CATALYSIS A-GENERAL, 2004, 276 (1-2) :231-239
[29]   A highly active and stable catalyst for carbon dioxide reforming of methane:: Ni/Ce-ZrO2/θ-Al2O3 [J].
Roh, HS ;
Jun, KW ;
Baek, SC ;
Park, SE .
CATALYSIS LETTERS, 2002, 81 (3-4) :147-151
[30]   Fuels and energy for the future: The role of catalysis [J].
Rostrup-Nielsen, JR ;
Nielsen, R .
CATALYSIS REVIEWS-SCIENCE AND ENGINEERING, 2004, 46 (3-4) :247-270