Preparation of Mo/HZSM-5/Bentonite Catalyst for Methane Aromatization in a Fluidized Bed Reactor

被引:7
|
作者
Lasobras, J. [1 ]
Medrano, J. A. [1 ]
Soler, J. [1 ]
Herguido, J. [1 ]
Menendez, M. [1 ]
Jimenez, A. [2 ]
Da Silva, M. [2 ]
Franco, M. J. [2 ]
Barrio, I. [2 ]
Lazaro, J. [2 ]
机构
[1] Univ Zaragoza, Dept Chem & Environm Engn, Inst Engn Res I3A, Zaragoza, Spain
[2] Ctr Invest CEPSA, Alcala De Henares 28805, Spain
关键词
methane aromatization; zeolite; bentonite; molybdenum; fluidized bed reactor; NONOXIDATIVE CONDITIONS; DEHYDRO-AROMATIZATION; MO/HZSM-5; CATALYSTS; ZEOLITE; MO/ZSM-5; OXYGEN; DEHYDROGENATION; IDENTIFICATION; PERFORMANCE; CALCINATION;
D O I
10.1515/ijcre-2017-0081
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Methane aromatization is a promising technology for the transformation of natural gas to added-value products. The main objective of this work was to obtain a catalyst with suitable performance and good mechanical stability for methane aromatization reaction in fluidized bed reactors. The selected catalyst was Mo/H-ZSM5/bentonite mixture. Mo/ZSM-5 was chosen as the active material, since it provides good selectivity to aromatics but the particle size of the zeolite was too small for operation in a fluidized bed and a binder was needed. We prepared two series of catalysts with two different zeolites. We tested several heating velocities (1, 7 and 10 degrees C min(-1)) in the different stages of catalyst synthesis. Methane conversion and selectivity to aromatic products improved when using gentle thermal treatments, increasing 2% and 10%, respectively, for the best catalyst tested.
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页数:9
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