Process for controlling sulfur oxides using an alumina-impregnat

Mineral oils: processes and products – Chemical conversion of hydrocarbons – Cracking

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208124, 423244, 423563, 252417, 252466R, 252455R, B01J 2906, C01G 1104, C01B 1700

Patent

active

043326722

ABSTRACT:
Sulfur oxides are removed from flue gas in a catalyst regenerator in a fluid catalyst cracking system while liquid-hydrocarbon product yield from the system is maintained at a high level by heating a nonzeolitic, silica-containing catalyst to 800.degree.-1500.degree. F.; impregnating 0.1 to 25 weight percent aluminum onto the catalyst particles; and cycling the resulting particles through the cracking reactor and catalyst regenerator in the cracking system, the impregnated catalyst being particularly adaptable for cracking heavy, metals-containing feeds such as residua.

REFERENCES:
patent: 3158565 (1964-11-01), Sanford
patent: 3776854 (1973-12-01), Dautzenberg et al.
patent: 4071436 (1978-01-01), Blanton, Jr. et al.
patent: 4115249 (1978-09-01), Blanton, Jr. et al.

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