The thermodynamics and kinetics of the diethylbenzene-benzene transalkylation have been studied in liquid phase over faujasite Y in a batch reactor. The reactions were conducted at several temperatures between 423 and 513 K. The main product of the reaction was ethylbenzene. When the molar ratio of
97/01749 Fischer-Tropsch catalysts. Attrition of carbided iron catalyst in the slurry phase
- Publisher
- Elsevier Science
- Year
- 1997
- Weight
- 184 KB
- Volume
- 38
- Category
- Article
- ISSN
- 0140-6701
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β¦ Synopsis
Liquid fuels (transport, refining, quality, storage) segregation during loading of the chamber had been changed so that the large-sized pieces of the shale entering into the cylinder central grid were not hituminized during heating.
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