Fluid catalytic cracking process, and gasoline and liquefied petroleum gas obtained by the process

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United States of America Patent

PATENT NO 9567531
APP PUB NO 20100089795A1
SERIAL NO

12575503

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Abstract

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The fluid catalytic cracking process according to the present invention includes a first step of feeding a feedstock to a first fluid catalytic cracker, and catalytically cracking the feedstock in the first fluid catalytic cracker, so as to produce a fraction (LCO) having a boiling range of 221 to 343° C. and having a total aromatic content of 40 to 80 volume %; and a second step of feeding an oil to be processed containing the fraction to a second fluid catalytic cracker having a reaction zone, a separation zone, a stripping zone, and a regeneration zone, and catalytically cracking the oil in the reaction zone of the second fluid catalytic cracker, in the presence of a cracking catalyst, at an outlet temperature of the reaction zone of 550 to 750° C., a contact time between the oil and the catalyst of 0.1 to 1 second, and a catalyst/oil ratio of 20 to 40 wt/wt.

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Patent Owner(s)

Patent OwnerAddress
NIPPON OIL CORPORATIONTOKYO

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Inventor(s)

Inventor Name Address # of filed Patents Total Citations
Fujiyama, Yuichiro Yokohama, JP 23 329
Okuhara, Toshiaki Yokohama, JP 9 237

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