98/03769 Mechanism of the partial oxidation of methane to synthesis gas over Pd
- Publisher
- Elsevier Science
- Year
- 1998
- Weight
- 215 KB
- Volume
- 39
- Category
- Article
- ISSN
- 0140-6701
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โฆ Synopsis
03 Gaseous fuels (derived gaseous fuels)
Ca(OH)z during the latter part of gasification. Fixed carbon conversion at 850ยฐC 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 the main product is Hz. Calcium increases Hz and COz, but it decreases CO, which leads to much higher Hz/ CO ratio in the presence of calcium. Thus, Ca(OH)s and CaCOs promote shift reaction of CO formed with steam and are suitable for the production of Hz-rich gas from petroleum coke.
๐ SIMILAR VOLUMES
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
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
A series of calcium-modified alumina-supported cobalt catalysts were prepared with a two-step impregnation method, and the effect of calcium on the catalytic performances of the catalysts for the partial oxidation of methane to syngas (CO and H 2 ) was investigated at 750 8C. Also, the catalysts wer
Ni catalysts supported on perovskite were in situ prepared from Cal \_ xSrxTil \_ yNiyO precursors and were tested in the oxidation of CH4 by increasing reaction temperature from room temperature to 800ยฐC. Nit originally separated from the perovskite structure under sol-gel preparation conditions wa