The partial oxidation of methane to synthesis gas over Ni/a-Al 2 O 3 catalysts (1 and 5 wt.-% Ni loading, 71ยฑ160 and 250ยฑ355 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
โฆ LIBER โฆ
Experimental investigations of catalytic partial oxidation of methane to synthesis gas in various types of fluidized-bed reactors
- Publisher
- Elsevier Science
- Year
- 2002
- Weight
- 185 KB
- Volume
- 43
- Category
- Article
- ISSN
- 0140-6701
No coin nor oath required. For personal study only.
๐ SIMILAR VOLUMES
Experimental Investigations of Catalytic
โ
K.-J. Marschall; L. Mleczko
๐
Article
๐
2000
๐
John Wiley and Sons
๐
English
โ 169 KB
๐ 2 views
Partial oxidation of methane to syngas i
๐
Article
๐
2002
๐
Elsevier Science
โ 183 KB
Catalytic partial oxidation of methane t
โ
K. Heitnes; S. Lindberg; O.A. Rokstad; A. Holmen
๐
Article
๐
1994
๐
Elsevier Science
๐
English
โ 575 KB
Monolithic reactors for experimental stu
โ
Hofstad, K. Heitnes ;Rokstad, O. A. ;Holmen, A.
๐
Article
๐
1997
๐
Springer
๐
English
โ 268 KB
A fluidised-bed membrane reactor for the
โ
L. Mleczko; T. Ostrowski; T. Wurzel
๐
Article
๐
1996
๐
Elsevier Science
๐
English
โ 509 KB
A fluidised-bed membrane reactor was proposed as reaction engineering meam for performing the catalytic partial oxidation of methane to synthesm gas (syngas) in a safe and stable nuumer, and to achieve high syng~ yields at elevated pressures and low temperatures. In ocder to analyse the potential of
Catalytic partial oxidation of methane t
โ
K. Heitnes; S. Lindberg; O.A. Rokstad; A. Holmen
๐
Article
๐
1995
๐
Elsevier Science
๐
English
โ 351 KB
The partial oxidation of methane to synthesis gas has been studied using several different catalytic systems: Fixed-bed, a monolithic type catalyst, and a Pt gauze. The monoliths were impregnated with Ni and Pd (5 wt.% metal) whereas 5% Ni/ AI203 was used in the fixed-bed reactor. The experiments we