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U.S. Department of Energy
Office of Scientific and Technical Information

Catalytic cracking process

Patent ·
OSTI ID:5328429

A process is described which comprises recracking a cracked naphtha feed containing up to about 60%, suitably from about 20 to about 40% olefins, over a crystalline aluminosilicate zeolite catalyst to further crack the naphtha and saturate at least about 50% of the olefins, preferably from about 90 to about 100% of the olefins, based on the weight of the cracked naphtha feed. In a preferred combination a gas oil is catalytically cracked in a first stage to produce a cat cracked naphtha product of high olefin content, and an intermediate boiling component thereof is recracked as a feed in a second stage over a zeolite catalyst to saturate the olefins, and hydrodenitrogenate and hydrodesulfurize the cat cracked naphtha. The recracked cat cracked naphtha is then hydrotreated at low to mild severities and then catalytically reformed (hydroformed) to produce high octane gasoline.

Assignee:
Exxon Research and Engineering Co.
Patent Number(s):
US 4176049
OSTI ID:
5328429
Country of Publication:
United States
Language:
English