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Fluidized catalytic cracking process utilizing a high temperature reactor

Patent ·
OSTI ID:6163403
A process is described for the fluid catalytic cracking of hydrocarbons, said process comprising: (a) passing regenerated catalyst particles into the upstream portion of a riser conversion zone and accelerating said catalyst particles by contact with a lift gas to a gas velocity of at least 1.2 meters per second; (b) injecting a hydrocarbon feed into said riser at a point downstream from the point of lift gas addition in an amount sufficient to maintain an average temperature of at least 550 C (1,025 F) in said riser and contacting said feed and catalyst in said riser for 0.2 to 5 seconds to convert at least a portion of said feed to a conversion stream comprising conversion products; (c) directing said conversion stream and catalyst out of said riser and directly into a cyclone separator without substantial cooling of said catalyst particles and substantially separating said conversion products from said catalyst particles; (d) passing catalyst particles having absorbed hydrocarbons from said separator into a catalyst stripping zone and maintaining a temperature in said stripping zone of at least 525 C (975 F); (e) returning hydrocarbons from said stripping zone to said cyclone separator; (f) transferring conversion products directly from said cyclone separator into contact with a quench medium and reducing the temperature of said conversion products to a temperature of less than 500 C (930 F); (g) separating the said conversion products and quench liquid to recover at least one FCC product stream; and (h) removing spent catalyst from said stripping zone for regeneration.
Assignee:
UOP, Des Plaines, IL (United States)
Patent Number(s):
A; US 5234578
Application Number:
PPN: US 7-766498
OSTI ID:
6163403
Country of Publication:
United States
Language:
English