Autor: |
G. McElhiney, D.A. Harding, S. Cartlidge, S.W. Addison |
Rok vydání: |
1988 |
Předmět: |
|
Zdroj: |
Applied Catalysis. 45:307-323 |
ISSN: |
0166-9834 |
DOI: |
10.1016/s0166-9834(00)83036-5 |
Popis: |
Catalytic cracking catalysts containing hydrothermally stabilized, acid treated (USE) Y zeolites were prepared and tested for the conversion of West Texas Heavy Gas Oil. The cracking catalyst zeolite contents were equivalent; however, the amounts of zeolite non-framework aluminium were decreased from catalyst to catalyst. Steam deactivated cracking catalyst activity was highest when catalyst zeolite non-framework aluminium content was highest, as was the selectivity to gasoline. Zeolites which have low amounts of non-framework aluminium also have maximum free mesopore volumes. Cracking catalysts prepared from such low-aluminium zeolites are not active for heavy oil cracking and high boiling hydrocarbons plug the mesopores causing high coke yields. |
Databáze: |
OpenAIRE |
Externí odkaz: |
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