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
98/03781 Studies of catalytic partial oxidation of methane to synthesis gas
- Publisher
- Elsevier Science
- Year
- 1998
- Weight
- 199 KB
- Volume
- 39
- Category
- Article
- ISSN
- 0140-6701
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β¦ Synopsis
and for a period of 10-3-10-2 s. The cycle is then repeated at a frequency of >350/min. The method may use as the raw material methane, ethane, or other gaseous hydrocarbons mainly produced during the separation of the large fraction of light hydrocarbons from petroleum gas. The method has a yield 2.5 times superior to that of conventional methods. 9Bi03777 Pyrolysis gas from biomass and pulverized biomass as reburn fuels in staged coal combustion
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The modeling and simulation of reactors for the catalytic partial oxidation of natural gas to synthesis gas is complex and requires detailed kinetics if it is to be representative and reliable. Adiabatic fixed bed reactors with a catalytic combustion zone fed with methane/oxygen or methane/air mixtu
## 03 Gaseous fuels (derived gaseous fuels) Ca(OH)z during the latter part of gasification. Fixed carbon conversion at 850Β°C without calcium is 65% after 2 h, whereas the catalysts achieve complete gasification within 1 h. The apparent activation energy is almost unchanged by calcium addition and t