Coker feed method and apparatus

• US 7,736,470 B2
• Filed: 03/12/2007
• Issued: 06/15/2010
• Est. Priority Date: 01/25/2007
• Status: Expired due to Fees

• Current Assignee: ExxonMobil Research & Engineering Company (Exxon Mobil Corporation)
• Original Assignee: ExxonMobil Research & Engineering Company (Exxon Mobil Corporation)
• Inventors: Mosley, Robert W., Massenzio, Scott F., Eppig, Christopher P., Chen, Te-Hung, Healy, Timothy M., Patel, Rutton D.
• Primary Examiner(s): BHAT, NINA NMN
• Application Number:
  US11/716,634
• Publication Number:
  US 20080179165A1
• Time in Patent Office: 1,191 Days
• Field of Search: 201/25, 201/28, 202/239, 208/131, 196/155
• US Class Current: 201/25
• CPC Class Codes: C10B 1/04 Vertical retorts
• CPC Class Codes: C10B 31/12 for liquid materials
• CPC Class Codes: C10B 55/00 Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material cracking oils C10G

Abstract

Described herein are methods and mechanisms for laterally dispensing fluid to a coke drum in a predictable and maintainable manner that alleviates thermal stress. In one embodiment, the methods and mechanisms utilize a split piping system to dispense fluid through two or more inlets into a spool that is connected to a coke drum and a coke drum bottom deheader valve. A combination of block valves and clean out ports provides a more effective means to clean the lines and allows fluid to be laterally dispensed in a controllable and predictable manner. The fluid is preferably introduced to the spool in opposing directions toward a central vertical axis of the spool at equal but opposing angles ranging from minus thirty (−30) to thirty (30) degrees relative to a horizontal line laterally bisecting the spool. Alternatively, however, fluid can be introduced to the spool tangentially.

Claims

1. A fluid dispensing apparatus for use with a delayed coke drum comprising the following components:

(a) a spool that has a wall that encloses an interior space, where the top of the spool is coupled to the bottom of a delayed coke drum and the bottom of the spool is coupled to the top of a coke drum bottom deheader valve;

(b) a main pipe for supplying a primary fluid stream; and

(c) a split piping system that comprises an intersection where the primary fluid stream is split into two secondary fluid streams that flow in separate directions along separate legs of branch piping, where each leg of the branch piping (i) includes one or more block valves and (ii) terminates with an equal number of ports;

(d) entry pipes each connected to a port of each leg of the branch piping and to a spool inlet that allows fluid to flow into the interior space enclosed by the spool, each entry pipe being (i) being disposed to direct the fluid to flow into and towards the center of the spool and (ii) angled to dispense fluid into the interior space of the spool at an upward angle not greater than 30 degrees above the horizontal and equal to the upward angle(s) of the other entry pipes(s).

2. The apparatus of claim 1 where each leg of the branch piping is sized so that the secondary fluid streams are substantially equal in flow mass and vapor/liquid proportion.

3. The apparatus of claim 1 where the two legs of branch piping are symmetrical to one another relative to at least one axis.

4. The apparatus of claim 1 where there is one spool inlet per leg of branch piping and the two spool inlets are located approximately 180 degrees apart along an inside surface of the spool wall.

5. The apparatus of claim 1 where there the secondary fluid streams are substantially equal in flow mass and vapor/liquid proportion, where the two legs of branch piping are symmetrical to one another relative to at least one axis, and where there is one spool inlet per leg of branch piping and the two spool inlets are located approximately 180 degrees apart along an inside surface of the spool wall.

6. The apparatus of claim 1 where the split piping system comprises the following components:

(i) two symmetrical branch pipes, each located downstream from the main pipe, each having an inlet port and an outlet port, each equal in diameter to one another but smaller in diameter to the main pipe, and each having a block valve therein,

(ii) a main pipe fitting that comprises at least four ports where a first port is an inlet port connected to an outlet port of the main pipe, a second port is an outlet port connected to the inlet port of one branch pipe, a third port is an outlet port connected to the inlet port of the other branch pipe a fourth port is a cleaning port that is removably covered and aligned opposite the first port,

(iii) two entry pipes, each located downstream on a different branch pipe and each having an inlet port arid an outlet port, wherein the outlet port of each entry pipe is connected to a spool inlet and

(iv) two branch pipe fittings each comprising at least four connection ports where a first port is an inlet port connected to the outlet port of a branch pipe, a second port is an outlet port connected to the inlet port of an entry pipe, a third port is a cleaning port that is removably covered and aligned opposite the first port; and

the fourth port is a cleaning port that is removably covered and aligned opposite the second port.

7. The apparatus of claim 1 where each leg of branch piping, or a portion thereof, is angled so that the secondary fluid streams dispense into the interior space of the spool at an angle that is five to twenty degrees above the horizontal.

8. The apparatus of claim 1 including a protective structure which extends above or around each spool inlet and penetrates into the spool interior a distance that, when measured horizontally, is no greater than five percent (5%) of the spool diameter at the same level.

9. The apparatus of claim 1 where the spool additionally contains thermocouples, positioned at various locations around the outside surface of the spool, which feed information to one or more controllers that control the rate at which quench water is added during a coked drum cool down step.

10. A delayed coking unit which comprises a coker furnace for heating coker feed, two or three delayed coke drums, a transfer line for heated effluent from the furnace, a switch valve to direct the heated feed from the transfer line to a particular coker drum, each coke drum having a fluid dispensing device as claimed in claim 1 located at the bottom of the coke drum with the top of the spool of the dispensing device coupled to the bottom of the respective coke drum and the bottom of the spool coupled to the top of a coke drum bottom deheader valve.

11. A fluid dispensing method for delayed coking comprising the following steps:

(a) supplying a spool that has a wall that encloses an interior space at the bottom of a delayed coke drum and where the bottom of the spool is coupled to the top of a coke drum bottom deheader valve;

(b) supplying a primary fluid stream for the delayed coke drum through a main pipe;

(c) routing the primary fluid stream through a split piping system that comprises an intersection where the primary fluid stream is split into two secondary fluid streams that flow in separate directions along separate legs of branch piping, where and where each leg of branch piping terminates with an equal number of ports that are each connected to an entry pipe which is also connected a spool inlet that allows fluid to flow into the interior space enclosed by the spool, each entry pipe being (i) being disposed to direct the fluid to flow into and towards the center of the spool and (ii) angled to dispense fluid into the interior space of the spool at an upward angle not greater than 30 degrees above the horizontal and equal to the upward angle(s) of the other entry pipes(s), and

(d) dispensing the secondary fluid streams into the interior space of the spool through the spool inlets.

12. The method of claim 11 where the secondary fluid streams are substantially equal in flow mass and vapor/liquid proportion.

13. The method of claim 11 where there the secondary fluid streams are substantially equal in flow mass and vapor/liquid proportion, where the two legs of branch piping are symmetrical to one another relative to at least one axis, and where there is one spool inlet per each of the two legs of branch piping and the two spool inlets are located approximately 180 degrees apart along an inside surface of the spool wall.

14. The method of claim 11 where, after the coke drum is tilled with coke, each leg of branch piping is purged by opening a cleaning port in a first leg of branch piping while the block valve in the leg is also open, closing the block valves in the other leg of branch piping, purging the first branch leg with water and/or steam and then reopening the closed block valves.

15. The method of claim 11 where the fluid, during a decoking stage of the delayed coking cycle, is steam introduced to control the flow rate of a coke and water mixture exiting the coke drum.

16. The method of claim 11 where each branch leg of branch piping, or a portion thereof, is angled so that the secondary fluid streams dispense into the interior space of the spool at an angle that is five to twenty degrees relative to horizontal.