99/02520 Mechanistic study of carbon dioxide reforming with methane over supported nickel catalysts
- Publisher
- Elsevier Science
- Year
- 1999
- Weight
- 205 KB
- Volume
- 40
- Category
- Article
- ISSN
- 0140-6701
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โฆ Synopsis
03 Gaseous fuels (derived gaseous fuels) two superimposed tiers. In almost 8000 h of plant operation up to September 1995, the filter operated well. A permanent clean gas dust content of <3 mg/m"(STP) was obtained, compared with the design value of 5 mg/m'(STP). Using dry gas cleaning at increased temperatures resulted in a simplified, more cost-efficient plant technology and improved efficiency in advanced power plant processes, such as integrated gasification combinedcycle power plants. This was considerably more effective than conventional wet gas clean-up processes. There are also advantages in servicing and maintenance. The two-tier filter was converted to a three-tier type, ensuring that this design principle can be transferred to very large-scale units.
๐ SIMILAR VOLUMES
Carbon dioxide reforming of methane to synthesis gas has been investigated over supported Ni catalysts in the temperature range of 5004350ยฐC. Addition of CaO ( 10 mol%) promoter to the Nil y-A1203 resulted in an increase of reaction rate and an improvement of catalyst stability, which may be related
## Adsorption equilibria and rate parameters for nitrogen and methane
The manufacture of mixed gases containing carbon monoxide and hydrogen comprises the decomposition of liquid-phase MeOH in the presence of copper-and chromium-containing solid catalysts. The catalyst may contain manganese compounds and/or alkaline earth compounds.