Partial oxidation of methane to syngas in fluidized bed reactor
- Publisher
- Elsevier Science
- Year
- 2002
- Weight
- 183 KB
- Volume
- 43
- Category
- Article
- ISSN
- 0140-6701
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A fluidized bed reactor has been used to investigate the partial oxidation of methane to syngas over a NiO/NiAlzO, catalyst. The axial concentration profiles of the different species along the bed have been determined and related to the observed temperature profiles. The amount of carbon deposited o
for the reaction C(a)+ O(a) = CO(a) is the highest among all the elementary reactions, the rate-determining step of the partial oxidation of methane could possibly be the above mentioned reaction. Method and apparatus for control of pressure of carbonization chamber of coke oven
The partial oxidation of methane to synthesis gas over Ni/a-Al 2 O 3 catalysts (1 and 5 wt.-% Ni loading, 71Β±160 and 250Β±355 mm particle diameter) was investigated in different types of fluidized-bed reactors, i.e., the bubbling fluidized bed (FlB), the spout fluid bed (SFB) and the internally circu