Delayed coking process and apparatus

• US 7,828,959 B2
• Filed: 11/19/2007
• Issued: 11/09/2010
• Est. Priority Date: 11/19/2007
• Status: Active Grant

• Current Assignee: Kazem Ganji
• Original Assignee: Kazem Ganji
• Inventors: Ganji, Kazem
• Primary Examiner(s): Griffin; Walter D
• Assistant Examiner(s): ROBINSON, RENEE E
• Application Number:
  US11/942,564
• Publication Number:
  US 20090127090A1
• Time in Patent Office: 1,086 Days
• Field of Search: 208/50, 208/125, 208/131
• US Class Current: 208/50
• CPC Class Codes: C10B 33/00 Discharging devices; Coke guides
• 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

A delayed coking process and apparatus which greatly shorten the required duration of the alternating drum fill and decoking cycles and eliminate the need to perform drum quenching, draining, unheading, hydraulic decoking, reheading, pressure testing, and warming procedures in the decoking cycle. In the inventive system, the decoking cycle preferably comprises simply a steamout stage and a coke product draining procedure. The coke product produced in the coking drums is a hot, solid, flowable material from which heat can be recovered for preheating the coker feed and/or producing steam.

Claims

1. A process for producing a solid petroleum coke product in a delayed coking system, said delayed coking system including a plurality of coking drums with said process comprising:

each of said coking drums operating in alternating delayed coking cycles including a fill cycle followed by a second cycle,

wherein during said fill cycle a drum feed material is delivered into said coking drum to form said solid petroleum coke product therein and produce a vapor product which is delivered to a product fractionator,

wherein said drum feed material is not delivered into said coking drum when said coking drum is operating in said second cycle,

said solid petroleum coke product is not removed from said coking drum when said coking drum is operating in said fill cycle, and

said process further comprising the step in said second cycle of removing from said coking drum said solid petroleum coke product which has been formed in said coking drum without quenching said solid petroleum coke product with water or other quenching liquid in said coking drum and without cutting said solid petroleum coke product in said coking drum such that, when removed from said coking drum in said step of removing, said solid petroleum coke product is a flowable material which flows out of said coking drum in solid form.

2. The process of claim 1 wherein each of said fill cycle and said second cycle has a duration of not more than 10 hours.

3. The process of claim 1 wherein each of said fill cycle and said second cycle has a duration in a range of from about 4 to about 8 hours.

4. The process of claim 1 wherein said drum feed material is at a temperature exceeding 980°

F. when delivered into said coking drum in said fill cycle.

5. The process of claim 1 further comprising the step in said second cycle, prior to said step of removing, of delivering steam through said solid petroleum coke product while said solid petroleum coke product remains in said coking drum, wherein said steam then flows to said fractionator.

6. The process of claim 1 wherein, in said step of removing, said solid petroleum coke product being removed from said coking drum has a mean particle size in a range of from about 50 to about 400 μ

m.

7. The process of claim 1 further comprising the step, after a stream of said solid petroleum coke product has been removed from said coking drum, of heating a coker feed stream by indirect heat exchange with said stream of said solid petroleum coke product, wherein said indirect heat exchange occurs in a heat exchanger such that said stream of said solid petroleum coke product and said coker feed stream each flow through said heat exchanger without said stream of said solid petroleum coke product coming into direct contact with said coker feed stream.

8. The process of claim 7 wherein said stream of said solid petroleum coke product is cooled by said coker feed stream as said stream of said solid petroleum coke product flows through said heat exchanger such that said stream of said solid petroleum coke product enters said heat exchanger at a temperature of at least 920°

F. and exits said heat exchanger at a temperature of not more than 700°

F.

9. The process of claim 8 further comprising the step, after said step of heating said coker feed stream, of flowing said stream of said solid petroleum coke product through a steam generator to produce steam by indirect heat exchange with water, wherein said stream of said solid petroleum coke product is cooled as it flows through said steam generator such that said stream of said solid petroleum coker product exits said steam generator at a temperature of not more than 250°

F.

10. The process of claim 1 further comprising the step, after a stream of said solid petroleum coke product has been removed from said coking drum, of producing steam by flowing said stream of said solid petroleum coke product through a steam generator.

11. The process of claim 1 further comprising the step of delivering a coker feed stream to said fractionator and wherein said drum feed material is a bottom liquid product from said fractionator.

12. The process of claim 1 further comprising the step of delivering a coker feed stream to a feed flash vessel and wherein said drum feed material is a liquid product from said feed flash vessel.

13. The process of claim 12 wherein said coker feed stream is a raw crude stream.

14. The process of claim 13 further comprising the step of heating said raw crude stream to a temperature in a range of from about 600 to about 850°

F. for delivery to said feed flash vessel and wherein said feed flash vessel operates at a pressure in a range of from about 10 to about 30 psig.

15. The process of claim 12 further comprising the step of delivering a vapor product from said feed flash vessel to a second fractionator different from said coker fractionator and wherein said vapor product is separated in said second fractionator to produce at least a naphtha product, a kerosene product and a diesel product.