Ceria-stabilized meso-Al2O3: synthesis, characterization and desorption kinetics

被引:18
作者
Adamu, Sagir [1 ]
Khan, Muhammad Y. [1 ]
Razzak, Shaikh A. [1 ,2 ]
Hossain, Mohammad M. [1 ,2 ]
机构
[1] King Fahd Univ Petr & Minerals, Dept Chem Engn, Dhahran, Saudi Arabia
[2] King Fahd Univ Petr & Minerals, KACST TIC CCS, Dhahran, Saudi Arabia
关键词
Ceria-doped alumina; Mesoporous; Deconvolution; Desorption kinetics; Stability; Gasification; MESOPOROUS GAMMA-ALUMINA; CATALYTIC CRACKING TCC; HYDROTHERMAL STABILITY; OXYGEN CARRIER; HYDROGEN-PRODUCTION; THERMAL-STABILITY; SILICA-ALUMINA; YTTRIUM-OXIDE; SUPPORT; GAMMA-AL2O3;
D O I
10.1007/s10934-017-0376-3
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
A highly stable mesoporous ceria-doped alumina for steam gasification of biomass was synthesized using a template free method. Aluminum nitrate nonahydrate and cerium nitrate hexahydrate were used as the precursors to synthesize the ceria-doped alumina support by hydrolyzing it with ammonium carbonate. The thermogravimetric analysis indicates that the ceria-doped alumina support was stable up to 750 A degrees C. By varying the amount of Ceria from 0.5 to 1.5 wt%, the structural and physico-chemical properties of the mesoporous support could be tuned. X-ray diffraction patterns showed that the newly prepared stabilized supports (calcined at 750 A degrees C), exhibit gamma-phase, while the textural characterization confirmed that all the catalyst supports are indeed mesoporous. The sample containing 1.0 wt% ceria on alumina has the highest post calcination (to 750 A degrees C) surface area of 152 m(2)/g, pore volume of 0.43 mL/g, total acidity of 6.87 cm(3)/g, indicating its suitable application in biomass gasification. NH3-desorption kinetics studies revealed that 1.0 wt % Ce containing Ce/Al2O3 sample has higher activation energy for NH3 desorption than bare Al2O3, implying a moderate Ce/Al2O3 matrix interaction and that ceria incorporation will not impair active site availability of the alumina support. Finally, the high oxygen carrying capacity of ceria coupled with the synthesis method, which ensured a high dispersion of ceria in alumina matrix are responsible for the observed thermal stability. The favorable properties of these new alumina supports, can serve them as potential candidates for steam gasification of biomass among other applications, when loaded with the appropriate metal, metal oxide, or an organic functional group.
引用
收藏
页码:1343 / 1352
页数:10
相关论文
共 52 条
[1]   VOx/c-Al2O3 catalyst for oxidative dehydrogenation of ethane to ethylene: Desorption kinetics and catalytic activity [J].
Al-Ghamdi, S. ;
Volpe, M. ;
Hossain, M. M. ;
de Lasa, H. .
APPLIED CATALYSIS A-GENERAL, 2013, 450 :120-130
[2]   Thermal stability of alumina aerogel doped with yttrium oxide, used as a catalyst support for the thermocatalytic cracking (TCC) process: An investigation of its textural and structural properties [J].
Al-Yassir, N. ;
Van Mao, R. Le .
APPLIED CATALYSIS A-GENERAL, 2007, 317 (02) :275-283
[3]   Cerium promoted and silica-alumina supported molybdenum oxide in the zeolite-containing hybrid catalyst for the selective deep catalytic cracking of petroleum naphthas [J].
Al-Yassir, N ;
Le Van Mao, R ;
Heng, F .
CATALYSIS LETTERS, 2005, 100 (1-2) :1-6
[4]   Evaluating and understanding the hydrothermal stability of alumina aerogel doped with yttrium oxide and used as a catalyst support for the thermo-catalytic cracking (TCC) process [J].
Al-Yassir, Nabil ;
Van Mao, Raymond Le .
CANADIAN JOURNAL OF CHEMISTRY, 2008, 86 (02) :146-160
[5]   Physico-chemical properties of mixed molybdenum and cerium oxides supported on silica-alumina and their use as catalysts in the thermal-catalytic cracking (TCC) of n-hexane [J].
Al-Yassir, Nabil ;
Le Van Mao, Raymond .
APPLIED CATALYSIS A-GENERAL, 2006, 305 (02) :130-139
[6]  
Alberton L., 2007, CATAL TODAY, V123
[7]   Thermal stabilization of alumina modified by lanthanum [J].
Alphonse, Pierre ;
Faure, Benjamin .
MICROPOROUS AND MESOPOROUS MATERIALS, 2014, 196 :191-198
[8]   Activity study of NiO-based oxygen carriers in chemical looping steam methane reforming [J].
Antzara, Andy ;
Heracleous, Eleni ;
Silvester, Lishil ;
Bukur, Dragomir B. ;
Lemonidou, Angeliki A. .
CATALYSIS TODAY, 2016, 272 :32-41
[9]  
Ayandiran A.A., 2016, Catal. Sci. Technol
[10]   Fluidized bed ODH of ethane to ethylene over VOx-MoOx/γ-Al2O3 catalyst: Desorption kinetics and catalytic activity [J].
Bakare, Idris A. ;
Mohamed, Shamseldin A. ;
Al-Ghamdi, Sameer ;
Razzak, Shaikh A. ;
Hossain, Mohammad M. ;
de Lasa, Hugo I. .
CHEMICAL ENGINEERING JOURNAL, 2015, 278 :207-216