Modeling the partial oxidation of methane in a fixed bed with detailed chemistry

AIChE Journal ◽  
2004 ◽  
Vol 50 (6) ◽  
pp. 1289-1299 ◽  
Author(s):  
M. Bizzi ◽  
G. Saracco ◽  
R. Schwiedernoch ◽  
O. Deutschmann
2019 ◽  
Vol 98 (3) ◽  
pp. 757-766
Author(s):  
Yonghui Li ◽  
Chao Lu ◽  
Xingxing Cao ◽  
Zhongfeng Geng ◽  
Minhua Zhang

2007 ◽  
Vol 126 (1-2) ◽  
pp. 54-63 ◽  
Author(s):  
Stefan Hannemann ◽  
Jan-Dierk Grunwaldt ◽  
Niels van Vegten ◽  
Alfons Baiker ◽  
Pit Boye ◽  
...  

2009 ◽  
Vol 52 (10) ◽  
pp. 1360-1370 ◽  
Author(s):  
Stefan Hannemann ◽  
Jan-Dierk Grunwaldt ◽  
Bertram Kimmerle ◽  
Alfons Baiker ◽  
Pit Boye ◽  
...  

2007 ◽  
Vol 7 (1 & 2) ◽  
pp. 108
Author(s):  
Luis F. Razon ◽  
Carlito M. Salazar ◽  
Hiroo Niiyama ◽  
Long The Nam Doan

The effect of catalyst preparation methods, NiO/MgO molar ratio and reaction temperature on the performance of Ni-MgO catalysts supported on Al2O3 in the partial oxidation of methane to syngas were investigated in a fixed-bed flow reactor. Three catalyst preparation methods (all slight variants of the precipitation method) produced comparable results in CH4 conversion, CO and H2 selectivities. Energy Dispersive X-Ray (EDX) analysis and the color of the catalysts after reaction showed that catalysts produced by simultaneous dissolution of the nickel and magnesium salts may have better carbon deposition resistance. NiO/MgO molar ratio significantly affected the performance of the catalyst. When the NiO/MgO ratio decreased, activity decreased. At a NiO/MgO molar ratio of 1/2 and a reduction temperature of 850°C, CH4 conversion and CO selectivity increased when reaction temperature increased while H2 selectivity remained almost the same. The catalyst gave excellent activity and remained stable after 5h time-on-stream.


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