Catalytic partial oxidation of methane to synthesis gas in a ceramic membrane reactor
✍ Scribed by A. Santos; J. Coronas; M. Menéndez; J. Santamaría
- Book ID
- 112414019
- Publisher
- Springer US
- Year
- 1995
- Tongue
- English
- Weight
- 669 KB
- Volume
- 30
- Category
- Article
- ISSN
- 1011-372X
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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
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