FCC reactor and riser design for short contact-time catalytic cracking of hydrocarbons

Patent metadata

Field	Value
Publication number	US-9358516-B2
Application number	US-201213685866-A
Country	US
Kind code	B2
Filing date	Nov 27, 2012
Priority date	May 14, 2008
Publication date	Jun 7, 2016
Grant date	Jun 7, 2016

Abstract

The present invention is an improved design and operation of a short contact time Fluid Catalytic Cracking (FCC) Reactor wherein the upper internal riser and a lower internal riser are in fluid connection with one another and provide an improved disengaging zone for entraining the vapors from the dilute phase area of the FCC reactor. Detailed preferred embodiments include improvements over the prior art to the internal central riser, riser termination apparatus, cyclone separators, and a coke mitigation baffle system, as well as associated improved fluid catalytic cracking processes utilizing the novel reactor design.

First claim

What is claimed is:

1. A fluid catalytic cracking reactor vessel, comprising:
a) a lower internal reactor riser, wherein a portion of the lower internal reactor riser is located within the fluid catalytic cracking reactor vessel, and wherein the lower end of the lower internal reactor riser is attached to the shell of the fluid catalytic cracking reactor vessel; and
b) an upper internal reactor riser located within the fluid catalytic cracking reactor vessel, wherein the lower end of the upper internal reactor riser terminates in a conical section which is connected to a cylindrical sleeve; wherein the upper section of the upper internal reactor riser is not in fluid connection with the dilute phase section of the reactor vessel, and at least two riser outlet ports are mechanically connected to the upper section of the upper internal reactor riser;
wherein the upper end of the lower internal reactor riser is in fluid connection with the upper internal reactor riser and the dilute phase section of the reactor vessel; the lower internal reactor riser is not mechanically connected to the upper internal reactor riser; the largest diameter of the conical section of the upper internal reactor riser is larger than the diameter of the upper end of the lower internal reactor riser; the cylindrical sleeve of the upper internal reactor riser has a diameter larger than the diameter of the upper end of the lower internal reactor riser; at least a portion of the cylindrical sleeve of the upper internal reactor riser overlaps with at least a portion of the upper end of the lower internal reactor riser; and there is no mechanical means located in the region of the overlapping portion of the cylindrical sleeve of the upper internal reactor riser and the upper end of the lower internal reactor riser for restricting the eccentricity between the cylindrical sleeve and the upper end of the lower internal reactor riser; and wherein the eccentricity between the cylindrical sleeve of the upper internal reactor riser and the upper end of the lower internal reactor riser is greater than 10% in an operating condition.

2. The fluid catalytic cracking reactor vessel of claim 1 , wherein the riser outlet ports are each physically connected by a first conduit to a primary mechanical cyclone inlet port which primary mechanical cyclone is designed for centrifugally separating catalyst particles from hydrocarbon vapors, and wherein there are no openings in the first conduits except for the riser outlet port on the first end of the first conduits and the primary mechanical cyclone inlet port on the second end of the first conduits.

3. The fluid catalytic cracking reactor vessel of claim 2 , wherein at least one primary mechanical cyclone has a vapor outlet port which is physically connected by a second conduit to a secondary mechanical cyclone inlet port which secondary mechanical cyclone is designed for centrifugally separating catalyst particles from hydrocarbon vapors, and wherein there are no openings in the second conduit except for the primary mechanical cyclone outlet port on the first end of the second conduit and the secondary mechanical cyclone inlet port on the second end of the second conduit.

4. The fluid catalytic cracking reactor vessel of claim 1 , wherein the length of the overlapping portion of the cylindrical sleeve of the upper internal reactor riser and the upper end of the lower internal reactor riser is from about 6 to about 36 inches when the fluid catalytic cracking reactor vessel is in the operating (hot) condition.

5. The fluid catalytic cracking reactor vessel of claim 4 , wherein the length of the overlapping portion of the cylindrical sleeve of the upper internal reactor riser and the upper end of the lower internal reactor riser is from about 9 to about 24 inches when the fluid catalytic cracking reactor vessel is in the operating (hot) condition.

6. The fluid catalytic cracking reactor vessel of claim 1 , wherein the acute angle between the conical section of the upper internal reactor riser and the axis of the upper internal reactor riser is from about 5° to about 25°.

7. The fluid catalytic cracking reactor vessel of claim 6 , wherein the acute angle between the conical section of the upper internal reactor riser and the axis of the upper internal reactor riser is from about 5° to about 20°.

8. The fluid catalytic cracking reactor vessel of claim 4 , wherein the acute angle between the conical section of the upper internal reactor riser and the axis of the upper internal reactor riser is from about 5° to about 25°.

9. The fluid catalytic cracking reactor vessel of claim 1 , wherein a transition length as measured from the top of the lower internal reactor riser to the bottom of the conical section is from about 6 to about 36 inches when the fluid catalytic cracking reactor vessel is in the operating (hot) condition.

10. The fluid catalytic cracking reactor vessel of claim 4 , wherein a transition length as measured from the top of the lower internal riser to the bottom of the conical section is from about 6 to about 36 inches when the fluid catalytic cracking reactor vessel is in the operating (hot) condition.

11. The fluid catalytic cracking reactor vessel of claim 8 , wherein a transition length as measured from the top of the lower internal riser to the bottom of the conical section is from about 6 to about 36 inches when the fluid catalytic cracking reactor vessel is in the operating (hot) condition.

12. The fluid catalytic cracking reactor vessel of claim 1 , wherein there is an annular gap between the lower internal reactor riser and the cylindrical sleeve of the upper internal reactor riser of from about 1 to about 4 inches.

13. The fluid catalytic cracking reactor vessel of claim 11 , wherein there is an annular gap between the lower internal reactor riser and the cylindrical sleeve of the upper internal reactor riser of from about 1 to about 4 inches.

14. The fluid catalytic cracking reactor vessel of claim 1 , further comprising a substantially horizontally displaced anti-coking baffle plate which substantially segregates an upper section of the fluid catalytic cracking reactor vessel from a lower section of the fluid catalytic cracking reactor vessel, wherein the anti-coking baffle is located in the fluid catalytic cracking reactor vessel at an elevation below the primary mechanical cyclone inlet port; the anti-coking baffle is mechanically connected to the upper internal reactor riser section, at least one primary cyclone, at least one secondary cyclone, or a combination thereof; and wherein the anti-coking baffle plate is free to move relative to the internal wall of the reactor vessel.

15. The fluid catalytic cracking reactor vessel of claim 14 , wherein the anti-coking baffle plate is comprised of a plurality of vapor transfer holes and/or open pipes, which penetrate through the anti-coking baffle plate wherein the vapor transfer holes and/or open pipes are located substantially adjacent to the upper internal reactor riser.

16. The fluid catalytic cracking reactor vessel of claim 1 , wherein the eccentricity between the cylindrical sleeve of the upper internal reactor riser and the upper end of the lower internal reactor riser is greater than 20% in the operating condition.

17. The fluid catalytic cracking reactor vessel of claim 1 , wherein at least a portion of the inner diameter of the upper internal reactor riser above the conical section is greater than at least a portion of the inner diameter of the lower internal reactor riser.

18. The fluid catalytic cracki

Assignees

• Exxonmobil Res & Eng Co

Inventors

• Tammera Robert F
• Jones Edward Nicholas
• Smalley Christopher G
• Deis Phillip A
• Chen Alvin U
• Gurciullo Christopher S

Classifications

• C10G11/18 Primary

  according to the "fluidised-bed" technique · CPC title

• B01J8/388

  externally, i.e. the particles leaving the vessel and subsequently re-entering it · CPC title

• F27B15/00 Primary

  Fluidised-bed furnaces; Other furnaces using or treating finely-divided materials in dispersion · CPC title

• B01J8/20 Primary

  with liquid as a fluidising medium · CPC title