Sludge dewatering and destruction within a delayed coking process

• US 4,968,407 A
• Filed: 04/25/1988
• Issued: 11/06/1990
• Est. Priority Date: 04/25/1988
• Status: Expired due to Term

• Current Assignee: Foster Wheeler USA Corporation (John Wood Group PLC)
• Original Assignee: Foster Wheeler USA Corporation (John Wood Group PLC)
• Inventors: McGrath, Michael J., Godino, Rino L.
• Primary Examiner(s): Caldarola, Glenn
• Application Number:
  US07/185,617
• Time in Patent Office: 925 Days
• Field of Search: 208/131, 208/48 Q, 208/50, 201/10, 201/25, 202/135, 202/95
• US Class Current: 208/131
• CPC Class Codes: C10B 55/00 Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material cracking oils C10G
• CPC Class Codes: C10B 57/045 containing mineral oils, bitumen, tar or the like or mixtures thereof

Abstract

Wet refinery sludges are disposed of by feeding them into a delayed coking process. The sludge is fed to the blowdown drum of the delayed coking process and mixed with oil condensed from the coke drum overhead, and the resulting sludge-oil mixture is fed to the coke drum where it is converted into coke. In order to remove the water from the sludge, a portion of the sludge-oil mixture is heated and recirculated to the blowdown drum where it provides the heat for drying and heating the sludge. The recirculating sludge-oil mixture is heated by a low level heat source, such as one of the fluid streams taken off from the fractionator.

Claims

1. A method for disposing of refinery sludge in a delayed coking process employing a coker heater, at least one coke drum in which coke is formed, a fractionator and a blowdown drum, in which oil vapors from coke formed in the coke drum are sent to the blowdown drum where the oil vapors condense into oil, comprising:

feeding the sludge to the blowdown drum, where the sludge mixes with the oil to form a sludge-oil mixture; and

feeding the sludge-oil mixture to the coke drum during the formation of coke, whereby the sludge in the sludge-oil mixture is incorporated in the formed coke.

2. The method according to claim 1, wherein the blowdown drum includes a plurality of trays, and the step of feeding the sludge comprises feeding the sludge to the blowdown drum above the trays.

3. The method according to claim 1, wherein the refinery sludge is wet and the sludge-oil mixture contains water, the method further comprising, after feeding the sludge, removing the water from the sludge by heating the sludge to vaporize the water.

4. The method according to claim 3, wherein the water is removed from the sludge in the blowdown drum.

5. The method according to claim 4, wherein the delayed coking process further employs a condenser, a settling drum and a sour water line connected in series to the overhead of the blowdown drum, and the vaporized water is directed through the overhead, the condenser and the settling drum to the sour water line.

6. The method according to claim 4, wherein the sludge is heated in the blowdown drum.

7. The method according to claim 3, wherein the delayed coking process includes taking off at least one hot fluid product stream from the fractionator, and heat for heating the sludge is provided by the fluid product stream.

8. The method according to claim 6, wherein a portion of the sludge-oil mixture is heated and recirculated to the blowdown drum, and the heat for heating the sludge is provided by the sludge-oil mixture.

9. The method according to claim 8, wherein the delayed coking process includes taking off at least one hot fluid product stream from the fractionator, and the sludge-oil mixture is heated by passing at least a portion of the hot fluid product stream in heat transfer relationship with the sludge-oil mixture.

10. The method according to claim 9, wherein the hot fluid product stream is lean sponge oil, and the sludge-oil mixture is heated by passing at least a portion of the lean sponge oil in heat transfer relationship with the sludge-oil mixture.

11. The method according to claim 1, further comprising adding a diluent to the sludge-oil mixture.

12. The method according to claim 11, wherein the delayed coking process includes taking off at least one hot fluid product stream from the fractionator, and the step of adding a diluent comprises adding a portion of the fluid product stream to the sludge-oil mixture.

13. The method according to claim 12, wherein the hot fluid product stream is light coker gas oil, and the step of adding a diluent comprises adding a portion of the light coker gas oil to the sludge-oil mixture.

14. A combined delayed coking and refinery sludge disposal system comprising:

at least one coke drum;

a blowdown drum in fluid communication with said coke drum to receive oil removed from coke in said coke drum;

means for conducting wet refinery sludge to said blowdown drum;

means for mixing the oil and the sludge in said blowdown drum to form a mixture;

means for conducting the mixture to said coke drum; and

means for drying the sludge in said blowdown drum.

15. The system of claim 14, wherein said drying means comprises means for heating the sludge to drive off water vapor.

16. The system of claim 14, wherein said drying means comprises means for recirculating a portion of the mixture to said blowdown drum, and means for heating the portion of the mixture.

17. The system of claim 16, further comprising a fractionator for producing hot fluid products, and said heating means comprises a heat exchanger mounted in said recirculating means and means for passing one of the hot fluid products through said heat exchanger in heat exchange relationship with the mixture of sludge and oil.

18. The system of claim 15, further comprising a sour water line for removing sour water from said system and means for directing the water from the water vapor to the sour water line.

19. A combined delayed coking and refinery sludge disposal system comprising:

at least one coke drum;

a blowdown drum in fluid communication with said coke drum to receive oil removed from coke in said coke drum;

means for conducting wet refinery sludge to said blowdown drum;

means for mixing the oil and the sludge in said blowdown drum to form a mixture;

means for conducting the mixture to said coke drum; and

means for diluting the mixture.

20. The system of claim 19, further comprising a fractionator for producing hot fluid products, and said diluting means comprises means for conveying one of said hot fluid products to said means for conducting the mixture to the coke drum.