Partial oxidation of methane to carbon monoxide and hydrogen in a fluidized bed reactor
✍ Scribed by A. Santos; M. Menéndez; J. Santaríana
- Publisher
- Elsevier Science
- Year
- 1994
- Tongue
- English
- Weight
- 524 KB
- Volume
- 21
- Category
- Article
- ISSN
- 0920-5861
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✦ Synopsis
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 on the catalyst under different operating conditions has also been determined. The results show that under suitable conditions, the bubbling fluidization regime gives a stable reactor performance with high conversion and selectivity, and a limited amount of carbon formation.
📜 SIMILAR VOLUMES
The partial oxidation of methane to synthesis gas over Ni/a-Al 2 O 3 catalysts (1 and 5 wt.-% Ni loading, 71±160 and 250±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
## Abstract In this project, the selective oxidation of benzene to maleic anhydride (MAN) was studied. Gas phase catalytic oxidation of benzene was carried out in a laboratory scale fluidized bed reactor on six different types of catalysts, which have different compositions. Effects of temperature,