U.S. patents available from 1976 to present.
U.S. patent applications available from 2005 to present.

Catalytic cracking unit with combined catalyst separator and stripper

Patent 5112576 Issued on May 12, 1992. Estimated Expiration Date: Icon_subject May 25, 2010. Estimated Expiration Date is calculated based on simple USPTO term provisions. It does not account for terminal disclaimers, term adjustments, failure to pay maintenance fees, or other factors which might affect the term of a patent.

Patent References

2422501

2903416

3353925

3785782

Method and means for separating gasiform materials from finely divided catalyst particles
Patent #: 4043899
Issued on: 08/23/1977
Inventor: Anderson, et al.

Fluidized catalytic cracking
Patent #: 4414100
Issued on: 11/08/1983
Inventor: Krug ,   et al.

Apparatus for the separation of fluid cracking catalyst particles from gaseous hydrocarbons
Patent #: 4692311
Issued on: 09/08/1987
Inventor: Parker ,   et al.

Process and apparatus for fluid bed catalytic cracking
Patent #: 4695370
Issued on: 09/22/1987
Inventor: Galtier ,   et al.

Separation of reacted hydrocarbons and catalyst in fluidized catalytic cracking
Patent #: 4721603
Issued on: 01/26/1988
Inventor: Krug ,   et al.

Heavy oil catalytic cracking process and apparatus
Patent #: 5000841
Issued on: 03/19/1991
Inventor: Owen

More ...

Inventor

Assignee

Application

No. 529191 filed on 05/25/1990

US Classes:

422/144, Including means to strip reaction mass from, or to regenerate, the particulate matter (including fluidized bed regenerators, per se)422/147, And means mechanically separating and removing particulate bed material from fluid effluent422/214Transfer line type reaction chamber

Examiners

Primary: Kratz, Peter

Attorney, Agent or Firm

International Class

B01J 008/18

Abstract

A catalytic cracking apparatus is provided for cost-effectively separating and stripping hydrocarbon from catalyst while limiting the occurrence of undesired catalytic overcracking and thermal cracking reactions. The apparatus includes a reactor, a combined gross separator and catalyst stripping vessel, and a disengaging vessel. The combined vessel is positioned to quickly separate catalyst from reactor products, reduce catalytic overcracking and strip volatile hydrocarbon from coked catalyst in one unitary vessel. The disengager is designed to dampen the flow of grossly separated hydrocarbon, substantially separate catalyst fines from the grossly separated hydrocarbon, and convey the catalyst fines to the combined gross separation and catalyst stripping vessel.

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