Hydrocarbon upgrading process
AssigneeMobil Oil Corporation
InventorsDavid L. Fletcher, Michael S. Sarli, Stuart S. Shih, Stephen J. McGovern, Douglas S. Diez, Mohsen N. Harandi, Timothy L. Hilbert
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AssigneeMobil Oil Corporation
InventorsDavid L. Fletcher, Michael S. Sarli, Stuart S. Shih, Stephen J. McGovern, Douglas S. Diez, Mohsen N. Harandi, Timothy L. Hilbert
Estimating the term…
Low sulfur gasoline of relatively high octane number is produced from a catalytically cracked, sulfur-containing naphtha by hydrodesulfurization followed by treatment over an acidic catalyst under endothermic conditions in a second reaction zone. Heat is added to the endothermic reaction zone to initiate and maintain octane restoring reactions. The preferred acidic catalyst is an intermediate pore size zeolite such as ZSM-5. The treatment over the acidic catalyst in the second step restores the octane loss which takes place as a result of the hydrogenative treatment and results in a low sulfur gasoline product with an octane number comparable to that of the feed naphtha. The addition of heat at the second zone prolongs hydrodesulfurization catalyst life by allowing a lower hydrodesulfurization reactor temperature. The addition of heat also maximizes octane increase in the second zone.
A process of upgrading a sulfur-containing catalytically cracked fraction having a 95% point of at least about 325.degree. F. and boiling in the gasoline boiling range which comprises:
A process of upgrading a sulfur-containing feed fraction boiling in the gasoline boiling range which comprises:
A process of upgrading a sulfur-containing feed fraction boiling in the gasoline boiling range which comprises:
A process of upgrading a sulfur-containing feed fraction boiling in the gasoline boiling range which comprises:
Dependencies are inferred from the claim text.