Closed reactor FCC system with provisions for surge capacity

• US 4,579,716 A
• Filed: 09/06/1983
• Issued: 04/01/1986
• Est. Priority Date: 09/06/1983
• Status: Expired due to Term

• Current Assignee: Mobil Oil Corporation (Exxon Mobil Corporation)
• Original Assignee: Mobil Oil Corporation (Exxon Mobil Corporation)
• Inventors: Krambeck, Frederick J., Schatz, Klaus W.
• Primary Examiner(s): NOT, DEFINED
• Assistant Examiner(s): Johnson, William R.
• Application Number:
  US06/529,824
• Time in Patent Office: 938 Days
• Field of Search: 422/112, 422/113, 422/144, 422/146, 422/145, 422/214, 208/113, 208/161, 208/164, 137/527, 137/545, 55/432
• US Class Current: 422/113
• CPC Class Codes: B01J 8/0055 using cyclones
• CPC Class Codes: C10G 11/18 according to the "fluidised-bed" technique

Abstract

A fluid catalytic cracking (FCC) apparatus and process comprising a reactor riser zone, a primary and a secondary cyclones, connected in series to the riser zone, and a stripping zone. The riser zone, the primary and the secondary cyclones, and the stripping zone, are placed within a single reactor vessel. The primary cyclone is connected to the reactor riser zone by an enclosed conduit which prevents random post-riser thermal cracking of the hydrocarbons after they exit the reactor riser zone. The conduit contains a trickle valve, or other means, to accommodate sudden increased surges of flow of the hydrocarbons and catalyst mixture.

Claims

1. An apparatus for the fluid catalytic cracking of a hydrocarbon feed in a closed cyclone system, said apparatus comprising:

a riser conversion zone defined by a vertically disposed elongated tubular conduit having an upstream end and a downstream end, wherein the downstream end terminates within a reactor vessel, said riser conversion zone having a suspension of hydrocarbon feed and a catalyst introduced into the upstream end thereof and a mixture of the catalyst and cracked hydrocarbon feed exiting from the downstream end thereof,

a primary cyclone connected to said downstream end by a first enclosed conduit, a secondary cyclone connected to said primary cyclone by a second enclosed conduit,

a first surge capacity means, located on said first enclosed conduit, for accommodating a sudden increased rate of flow of said mixture within said first enclosed conduit, said first surge capacity means being substantially closed during a normal rate of flow of said mixture within said first enclosed conduit, wherein said first surge capacity means comprises first means for preventing catalyst flow therethrough when said first surge capacity means is substantially closed and second means for allowing a first portion of stripping gas flow therethrough when said first surge capacity means is substantially closed, and

means defining a catalyst stripping zone for stripping hydrocarbons from catalyst received from said cyclones.

2. An apparatus of claim 1 wherein said stripping zone is located beneath said primary and secondary cyclones.

3. An apparatus of claim 2, wherein said first enclosed conduit further comprises means defining a port for passing a second portion of stripping gases from said catalyst stripping zone into said first enclosed conduit.

4. An apparatus of claim 3 wherein said apparatus further comprises a first and second dipleg connected to said primary and secondary cyclones, respectively, for returning separated catalyst to said catalyst stripping zone.

5. An apparatus of claim 4, wherein said primary cyclone is a stripper cyclone and wherein said catalyst is separated from said mixture by passage of said mixture from said riser conversion zone into a cyclonic separation zone of said stripper cyclone, wherein a first cyclonic separation is carried out between said catalyst and said cracked hydrocarbon feed, the thus-separated catalyst being passed substantially immediately into a lower separate portion of said stripper cyclone through an opening into an annular zone wherein it is contacted with a tangentially introduced stripping gas, said stripping gas and stripped products being separated from said catalyst in said annular zone upwardly through an open end restricted passageway concentric with said annular zone and in open communication with an upper withdrawal passageway for removing cracked hydrocarbon feed from the upper portion of said stripper cyclone into said second enclosed conduit;

said catalyst being conducted from said stripper cyclone into said stripping zone.

6. An apparatus of claim 1, wherein said first surge capacity means comprises means defining a first opening in said first enclosed conduit, and said first means for preventing catalyst flow therethrough comprises a trickle valve which covers said first opening.

7. An apparatus of claim 6, wherein said trickle valve further comprises means for pivoting a top portion of said trickle valve about a trickle valve axis which is substantially perpendicular to the longitudinal axis of said riser conversion zone.

8. An apparatus of claim 7, wherein said second means for allowing stripping gas therethrough comprises means for horizontally elevating the bottom portion of said trickle valve with respect to said first enclosed conduit when said trickle valve is in said closed position.

9. An apparatus of claim 8, wherein said apparatus comprises a means for maintaining a pressure in said reactor vessel higher than in the primary cyclone thereby facilitating operation of said first surge capacity means.

10. An apparatus of claim 8, wherein said means for elevating comprises a serrated edge attached to said first enclosed conduit.

11. An apparatus of claim 10, further comprising a second surge capacity means, located on said second enclosed conduit, for accommodating a sudden increased rate of flow of said material within said second enclosed conduit, said second surge capacity means being substantially closed during a normal rate of flow of said material within said second enclosed conduit, wherein said second surge capacity means comprises third means for preventing catalyst flow therethrough when said second surge capacity means is substantially closed and fourth means for allowing stripping gas flow therethrough when said second surge capacity means is substantially closed.

12. An apparatus of claim 10, wherein said trickle valve further comprises a bottom portion which contacts said serrated edge when said valve is in a closed position.

13. An apparatus of claim 12, wherein said first surge capacity means is sized to accommodate a two to twenty fold sudden increase of the steady state rate of flow of said mixture.

14. An apparatus for the fluid catalytic cracking of a hydrocarbon feed in a closed cyclone system, said apparatus comprising:

a riser conversion zone defined by a vertically disposed elongated tubular conduit having an upstream end and a downstream end, said downstream end terminating within a reactor vessel,

said riser conversion zone having a suspension of hydrocarbon feed and catalyst introduced into the upstream end thereof and a mixture of the catalyst and cracked hydrocarbon feed exiting from the downstream end thereof,

a primary cyclone connected to said downstream end by a first enclosed conduit,

a secondary cyclone connected to said primary cyclone by a second enclosed conduit, said first and said second conduits completely separating the material conducted therein from the atmosphere of said reactor vessel,

a surge capacity means located on said second enclosed conduit, for accommodating a sudden increased rate of flow of said material within said second enclosed conduit, said second surge capacity means being substantially closed during a normal rate of flow of said material within said second enclosed conduit, and comprising means for preventing catalyst flow therethrough when said surge means is substantially closed and means for allowing stripping gas flow therethrough when said surge means is substantially closed, and

means defining a catalyst stripping zone for stripping hydrocarbons from catalyst received from said cyclones.