Furnace systems and methods for cracking hydrocarbons

Patent metadata

Field	Value
Publication number	US-12024684-B2
Application number	US-202017624634-A
Country	US
Kind code	B2
Filing date	Jul 22, 2020
Priority date	Jul 24, 2019
Publication date	Jul 2, 2024
Grant date	Jul 2, 2024

Abstract

Furnace systems and methods for steam cracking hydrocarbons to produce ethylene and other light olefins are provided herein. A furnace system for cracking hydrocarbons includes a radiant firebox containing a plurality of burners and an injection nozzle, a primary transfer line exchanger fluidly coupled to and downstream of the radiant firebox, and a flow restrictor fluidly coupled to and downstream of the primary transfer line exchanger. The furnace system also includes a decoke vessel containing an effluent inlet, a fluid outlet, and a coke outlet, where the effluent inlet is fluidly coupled to and downstream of the flow restrictor and the fluid outlet is fluidly coupled to and upstream of the injection nozzle of the radiant firebox, and a coke collection bin is coupled to the coke outlet of the decoke vessel.

First claim

The invention claimed is:

1. A furnace system for cracking hydrocarbons, comprising:
a radiant firebox comprising a plurality of burners and an injection nozzle;
a primary transfer line exchanger fluidly coupled to and downstream of the radiant firebox;
a flow restrictor fluidly coupled to and downstream of the primary transfer line exchanger;
a decoke vessel comprising an effluent inlet, a fluid outlet, and a coke outlet, wherein the effluent inlet is fluidly coupled to and downstream of the flow restrictor and the fluid outlet is fluidly coupled to and upstream of the injection nozzle of the radiant firebox; and
at least one of (a) a moveable coke collection bin that is coupled to the coke outlet of the decoke vessel and (b) a fixed coke collection bin that is coupled to the coke outlet of the decoke vessel and is adapted to convey coke away from the furnace system.

2. The furnace system of claim 1 , further comprising a valve disposed between the primary transfer line exchanger and the flow restrictor.

3. The furnace system of claim 1 , further comprising a secondary transfer line exchanger fluidly coupled to and downstream of the primary transfer line exchanger and to the flow restrictor.

4. The furnace system of claim 3 , further comprising a valve disposed between the primary transfer line exchanger and the secondary transfer line exchanger.

5. The furnace system of claim 3 , wherein the secondary transfer line exchanger comprises an inlet and an outlet, wherein the inlet of the secondary transfer line exchanger is fluidly coupled to the outlet of the primary transfer line exchanger and the outlet of the secondary transfer line exchanger is fluidly coupled to a recovery system.

6. The furnace system of claim 1 , wherein the decoke vessel comprises a cyclone separator.

7. The furnace system of claim 6 , wherein the cyclone separator is configured to:
receive decoke effluent via the effluent inlet,
separate the decoke effluent into coke particles and a decoke fluid, and
transfer the coke particles to the coke collection bin via the coke outlet and the decoke fluid to the injection nozzle via the fluid outlet.

8. The furnace system of claim 7 , wherein the coke collection bin is configured to store the coke particles at ambient pressure.

9. The furnace system of claim 1 , wherein at least a portion of the plurality of burners is located on a bottom surface of the radiant firebox.

10. The furnace system of claim 1 , wherein the injection nozzle is located adjacent to at least a portion of the plurality of burners.

11. The furnace system of claim 1 , wherein the radiant firebox further comprises one or more coils disposed therein, wherein the coils comprise radiant coils, convection coils, or any combination thereof.

12. The furnace system of claim 1 , wherein the flow restrictor comprises one or more flow restriction orifices configured to restrict flow.

13. A furnace system for cracking hydrocarbons, comprising:
a radiant firebox comprising a plurality of burners and an injection nozzle;
a primary transfer line exchanger fluidly coupled to and downstream of the radiant firebox;
a secondary transfer line exchanger fluidly coupled to and downstream of the primary transfer line exchanger;
a first valve disposed between the primary transfer line exchanger and the secondary transfer line exchanger;
a decoke effluent line fluidly coupled to and downstream of the primary transfer line exchanger and fluidly coupled to and upstream of the first valve;
a second valve fluidly coupled to the decoke effluent line downstream of the primary transfer line exchanger;
a flow restrictor fluidly coupled to the decoke effluent line downstream of the second valve;
a decoke vessel fluidly coupled to the decoke effluent line and comprising an effluent inlet, a fluid outlet, and a coke outlet, wherein the effluent inlet is fluidly coupled to and downstream of the flow restrictor and the fluid outlet is fluidly coupled to and upstream of the injection nozzle of the radiant firebox; and
at least one of (a) a moveable coke collection bin that is coupled to the coke outlet of the decoke vessel and (b) a fixed coke collection bin that is coupled to the coke outlet of the decoke vessel and is adapted to convey coke away from the furnace system.

14. The furnace system of claim 13 , wherein the decoke vessel comprises a cyclone separator.

15. The furnace system of claim 14 , wherein the cyclone separator is configured to:
receive decoke effluent via the effluent inlet,
separate the decoke effluent into coke particles and a decoke fluid, and
transfer the coke particles to the coke collection bin via the coke outlet and the decoke fluid to the injection nozzle via the fluid outlet.

16. The furnace system of claim 14 , wherein the coke collection bin is configured to store the coke particles at ambient pressure.

17. The furnace system of claim 13 , wherein the radiant firebox further comprises one or more coils disposed therein, and wherein the coils comprise radiant coils, convection coils, or any combination thereof.

18. A furnace system for cracking hydrocarbons, comprising:
a radiant firebox comprising a plurality of burners, an injection nozzle, and one or more coils, wherein the coils comprise radiant coils, convection coils, or any combination thereof,
a primary transfer line exchanger fluidly coupled to and downstream of the radiant firebox;
a secondary transfer line exchanger fluidly coupled to and downstream of the primary transfer line exchanger;
a first valve disposed between the primary transfer line exchanger and the secondary transfer line exchanger;
a decoke effluent line fluidly coupled to and downstream of the primary transfer line exchanger and fluidly coupled to and upstream of the first valve;
a second valve fluidly coupled to the decoke effluent line downstream of the primary transfer line exchanger;
a flow restrictor fluidly coupled to the decoke effluent line downstream of the second valve;
a decoke vessel fluidly coupled to the decoke effluent line and comprising an effluent inlet, a fluid outlet, and a coke outlet, wherein the effluent inlet is fluidly coupled to and downstream of the flow restrictor and the fluid outlet is fluidly coupled to and upstream of the injection nozzle of the radiant firebox, wherein the decoke vessel comprises a cyclone separator and is configured to:
receive decoke effluent via the effluent inlet,
separate the decoke effluent into coke particles and a decoke fluid, and
transfer the decoke fluid to the injection nozzle via the fluid outlet; and

at least one of (a) a moveable coke collection bin that is coupled to the coke outlet of the decoke vessel and (b) a fixed coke collection bin that is coupled to the coke outlet of the decoke vessel and is adapted to convey coke away from the furnace system; wherein at least one of the moveable coke collection bin and fixed coke collection bin bine has an interior volume containing coke particles at ambient pressure.

19. A method of cracking hydrocarbons in a cracking furnace, comprising:
during decoking mode flowing a decoke effluent from a radiant firebox through a primary transfer line exchanger;
flowing the decoke effluent from the primary transfer line exchanger through a flow restrictor;
flowing the decoke effluent from the flow restrictor to a decoke vessel;
separating the decoke effluent into coke particles and a decoke fluid within the decoke vessel;
transferring the decoke fluid from the decoke vessel to the radiant fi

Assignees

• Exxonmobil Chemical Patents Inc

Inventors

• Aslaner William A
• Hirst Thomas T
• Spicer David
• Stephens George

Classifications

• C10G2400/20

  C2-C4 olefins · CPC title

• C10G9/36 Primary

  with heated gases or vapours · CPC title

• C10G9/20 Primary

  Tube furnaces · CPC title

• B04C5/185

  Dust collectors · CPC title

• B01D45/16

  generated by the winding course of the gas stream {, the centrifugal forces being generated solely or partly by mechanical means, e.g. fixed swirl vanes} · CPC title