Delayed coking drum quench overflow systems and methods

• US 9,187,696 B2
• Filed: 03/14/2013
• Issued: 11/17/2015
• Est. Priority Date: 03/14/2013
• Status: Active Grant

• Current Assignee: Bechtel Energy Technologies & Solutions Incorporated
• Original Assignee: Bechtel Hydrocarbon Technology Solutions, Inc. (Bechtel Group Incorporated)
• Inventors: Ward, John D., Alexander, Scott
• Primary Examiner(s): Warden, Jill
• Assistant Examiner(s): Woodard, Joye L
• Application Number:
  US13/803,848
• Publication Number:
  US 20140262724A1
• Time in Patent Office: 978 Days
• Field of Search: 210/774, 208/106, 208/131, 208/48.R, 208/48.Q, 208/187, 201/39, 201/3
• US Class Current: 1/1
• CPC Class Codes: C10B 45/00 Other details
• 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

Delayed coking drum quench overflow systems and methods, which relate to removing hydrocarbon particulates from an overflow stream in a delayed coking drum quench operation. In one embodiment, an improved overflow system incorporates one or more filters to remove hydrocarbon particulates from the system before passing through a conventional closed blowdown system.

Claims

1. A method for removing hydrocarbon particulates from an overflow stream in a delayed coking quench overflow system, which comprises:

pumping an overflow stream comprising a fluid and hydrocarbon particulates from a coke drum through a filter system;

removing a portion of the hydrocarbon particulates from the overflow stream as the overflow stream is pumped though the filter system, wherein the filter system removes hydrocarbon particulates from the overflow stream that are as small as about 10-25 microns in size; and

pumping the overflow stream from the filter system through a closed blowdown system, which comprises at least one of a blowdown condenser and a settling drum.

2. The method of claim 1, wherein the filter system comprises a debris filter for removing hydrocarbon particulates from the overflow stream that are larger than about ⅜

inch in size.

3. The method of claim 2, wherein the filter system comprises another debris filter for removing hydrocarbon particulates from the overflow stream that are larger than about ⅜

inch in size.

4. The method of claim 1, wherein the filter system comprises a coke fines filter for removing the hydrocarbon particulates from the overflow stream that are as small as about 10-25 microns in size.

5. The method of claim 4, wherein the filter system comprises another coke fines filter for removing the hydrocarbon particulates from the overflow stream that are as small as about 10-25 microns in size.

6. The method of claim 1, further comprising controlling a flow of the overflow stream through the filter system with an overflow pump and a flow controller.

7. The method of claim 6, further comprising maintaining a predetermined static head pressure in the filter system using the flow controller, the overflow pump and a pump for pumping a fluid into the coke drum.

8. The method of claim 1, further comprising:

pumping the overflow stream around the blowdown condenser through the settling drum; and

mixing the overflow stream with a cooled fluid to reduce a temperature of the overflow stream before entering the settling drum.

9. A delayed coking quench overflow system, which comprises:

a coke drum;

a closed blowdown system, which comprises at least one of a blowdown condenser and a settling drum; and

a filter system connected to the coke drum at one end by a fluid passageway and connected to the closed blowdown system at another end by another fluid passageway, wherein the filter system removes hydrocarbon particulates from an overflow stream from the coke drum that are as small as about 10-25 microns in size.

10. The system of claim 9, wherein the filter system comprises a debris filter for removing hydrocarbon particulates from the overflow stream that are larger than about ⅜

inch in size.

11. The system of claim 10, wherein the filter system comprises another debris filter for removing hydrocarbon particulates from the overflow stream that are larger than about ⅜

inch in size.

12. The system of claim 11, wherein the debris filter and the another debris filter are connected in series or in parallel.

13. The system of claim 9, wherein the filter system comprises a coke fines filter for removing the hydrocarbon particulates from the overflow stream that are as small as about 10-25 microns in size.

14. The system of claim 13, wherein the filter system comprises another coke fines filter for removing the hydrocarbon particulates from the overflow stream that are as small as about 10-25 microns in size.

15. The system of claim 14, wherein the coke fines filter and another coke fines filter are connected in series or in parallel.

16. The system of claim 9, wherein the filter system comprises an overflow pump and a flow controller for controlling a flow of the overflow stream through the filter system.

17. The system of claim 16, wherein a capacity for the overflow pump is about equal to a capacity for a pump used to pump a fluid into the coke drum.