## Abstract The use of an internal circulating fluidized bed (ICFB) is proposed for the oxidative dehydrogenation of butane. The reactor consists of two adjacent zones, separated by a wall. In the oxidizing zone the catalyst is oxidized and in the reducing zone the butane is dehydrogenated by react
Development of fluidized-bed catalyst for partial oxidation of n-butane
β Scribed by Xu Wen; Gong Yang
- Publisher
- American Institute of Chemical Engineers
- Year
- 2003
- Tongue
- English
- Weight
- 120 KB
- Volume
- 49
- Category
- Article
- ISSN
- 0001-1541
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π SIMILAR VOLUMES
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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
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