Oxidative dehydrogenation of lower alkanes over metal incorporated MCM-41 catalysts

被引:8
|
作者
Ahmed, Shakeel [1 ,2 ]
Rahman, Faizur [1 ,2 ]
Al-Amer, Adnan M. J. [3 ]
Al-Mutairi, Eid M. [3 ]
Baduruthamal, Uwais [1 ,2 ]
Alam, Khurshid [1 ,2 ]
机构
[1] King Fahd Univ Petr & Minerals, Ctr Res Excellence Petr Refining & Petrochem, Dhahran 31261, Saudi Arabia
[2] King Fahd Univ Petr & Minerals, Res Inst, Ctr Refining & Petrochem, Dhahran 31261, Saudi Arabia
[3] King Fahd Univ Petr & Minerals, Dept Chem Engn, Dhahran 31261, Saudi Arabia
关键词
Oxidative dehydrogenation; Propane; Butane; MCM-4; Lower alkanes; SELECTIVE OXIDATION; PROPANE; ALUMINA; TEMPERATURE; ETHANE;
D O I
10.1007/s11144-011-0393-1
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
A series of metal incorporated M-MCM-41 (M = Ce, Mo, and/or V) mesoporous materials were synthesized by the hydrothermal method. The synthesized mesoporous materials were characterized by the XRD, BET, TPR and EPR techniques. The extent of mesoporous structural ordering was evident from the XRD pattern of M-MCM-41. The catalytic properties of the metal containing MCM-41 catalysts were evaluated for oxidative dehydrogenation of propane and n-butane in a fixed-bed micro-reactor. The results showed higher activity in case of V-MCM-41 catalyst as compared to that of Mo-MCM-41 catalysts over a temperature range of 500-600 degrees C at atmospheric pressure. Cerium containing MCM-41 catalyst showed high selectivity (78%) for butadiene at moderate conversion of about 4%. The major products include ethylene, propylene and butanes. Propane conversion of about 20% with corresponding propylene selectivity of around 30% was obtained at 575 degrees C over V-MCM-41 catalyst. A small amount of H-2 besides COx was also produced during catalytic runs under the conditions of catalyst performance evaluation.
引用
收藏
页码:483 / 493
页数:11
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