## Abstract A 1βD stationary reactor model describes the catalytic conversion of a gaseous hydrocarbon fuel with air and steam to synthesis gas by autothermal reforming and catalytic partial oxidation. The model defines two subsequent sections in the reactor: an upstream oxidation section and a dow
β¦ LIBER β¦
Autothermal Reforming of Methane in a Reverse-Flow Reactor
β Scribed by T. Liu; H. Temur; G. Veser
- Publisher
- John Wiley and Sons
- Year
- 2009
- Tongue
- English
- Weight
- 624 KB
- Volume
- 32
- Category
- Article
- ISSN
- 0930-7516
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