Recycle of oily refinery wastes

• US 5,009,767 A
• Filed: 09/21/1989
• Issued: 04/23/1991
• Est. Priority Date: 02/02/1988
• Status: Expired due to Fees

• Current Assignee: Mobil Oil Corporation (Exxon Mobil Corporation)
• Original Assignee: Mobil Oil Corporation (Exxon Mobil Corporation)
• Inventors: Bartilucci, Mark P., Tracy, William J. III, Karsner, Grant G.
• Primary Examiner(s): MCFARLANE, ANTHONY R
• Application Number:
  US07/410,434
• Time in Patent Office: 579 Days
• Field of Search: 208/131, 208/48 Q, 208/46, 208/85, 208/13, 585/240, 201/2.5, 201/20, 201/25
• US Class Current: 208/85
• CPC Class Codes: C10B 39/06 in the oven
• 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

Petroleum refinery waste stream sludges are recycled by segregating the sludges according to their oil content. Sludges of high oil content are developed and then injected into a delayed coking unit during the coking phase so that they are converted to coke and liquid coking products. High water content sludges are used to quench the coke during the quench phase of the coking cycle, with minimal increases in coke volatile matter. The process increases the capacity of the delayed coking unit to process and recycle refinery waste sludges and produce a coke of lower volatile content.

Claims

1. A process for disposing of petroleum containing sludge comprising:

(i) segregating waste oil-containing sludges into a first sludge and a second sludge, the first sludge being of high oil content relative to the second sludge and the second sludge being of high water content relative to the first sludge;

(ii) dewatering the first, high oil content sludge;

(iii) introducing the dewatered sludge into a delayed coking drum under delayed coking conditions in the presence of a liquid coker hydrocarbon feedstock to form coke;

(iv) introducing the second, high water content sludge into a delayed coking drum to quench the coke formed in the coking drum.

2. A process according to claim 1 in which the high oil content sludge contains from 15 to 25 percent oil.

3. A process according to claim 2 in which the high water content sludge contains at least 80 percent water.

4. The process of claim 1 in which the dewatered sludge is slurried with oil prior to mixing with the coker feed for introduction into the delayed coker.

5. The process of claim 4 in which the dewatered sludge is slurried with oil to a solids content of from 10 to 20 weight percent prior to mixing with the coker feed for introduction into the delayed coker.

6. The process of claim 1, in which the first, high oil content sludge contains less than 70% by weight of water.

7. The process of claim 1, in which the first, high water content sludge contains at least 80% by weight of water.

8. The process of claim 1, in which the delayed coking conditions include a coking temperature of from about 850°

F. to about 950°

F.

9. The process of claim 1, in which the high oil content sludge comprises slop oil emulsion solids or API (American Petroleum Institute) separator skimmings.

10. The process of claim 1, in which the high water content sludge is a biosludge or DAF float (Dissolved Air Flotation) sludge or a mixture of these.

11. The process of claim 1, in which steam is introduced intermediate steps (iii) and (iv) to strip volatiles in the coker drum.

12. A process for disposing of petroleum refinery sludges in a delayed coker by introducing a hydrocarbon coker feedstock into a delayed coking drum under coking conditions to produce delayed coke in the drum and quench coke produced in the drum, in which a first, dewatered petroleum of high oil content relative to a second sludge is the coker feedstock introduced into the delayed coking drum and subjected to delayed coking in the coking drum to form coke, and quenching the coke in the coking drum with the second sludge of which is of higher water content relative to the first sludge.

13. The process according to claim 12 in which the dewatered high oil content sludge contains 15-25 weight percent oil.

14. A process according to claim 12 in which the second, high water content sludge contains at least 80 percent water.

15. A process for disposing of petroleum refinery sludges in a delayed coker by introducing a liquid hydrocarbon coker feedstock into a delayed coking drum under delayed coking conditions to produce delayed coker in the drum and quenching the coke produced in the drum, which comprises:

(i) dewatering a first, refinery sludge of high oil content relative to a second refinery sludge which is of high water content relative to the first sludge by filtering the sludge to remove water from it;

(ii) introducing the dewatered sludge into a delayed coker drum with coking feed;

(iii) subjecting the dewatered sludge and coking feed to coking conditions in the coking drum to form delayed coke;

(iv) quenching the coke in the drum with the second refinery sludge of higher water content relative to the first sludge.

16. A process according to claim 15 in which the first, refinery sludge of high oil content comprises API (American Petroleum Institute) separator skimmings, slop oil or slop oil emulsion solids.

17. A process according to claim 15 in which the sludge of high oil content is filtered on a continuous belt filter.

18. A process according to claim 15 in which the refinery sludge of higher water content comprises DAF (Dissolved Air Flotation) float or a biosludge.

19. A process according to claim 15 in which the dewatered sludge is slurried with an oil prior to injection into the coking drum.

20. A process for disposing of petroleum refinery sludge in a delayed coker unit while producing fuels grade coke and anode grade coke, which process comprises:

(i) introducing a liquid hydrocarbon coker feedstock into a delayed coking drum for anode grade coke production and coking the feed under delayed coking conditions and quenching the coke produced in the drum to produce delayed anode grade coke in the drum,

(ii) dewatering a first refinery sludge of high oil content relative to a second refinery sludge by filtering the sludge to remove water from it;

(iii) introducing the dewatered sludge into a delayed coker drum with coking feed;

(iv) subjecting the dewatered sludge and coking feed to coking conditions in the coking drum to form delayed fuels grade coke;

(v) quenching the fuels grade coke in the drum with the second refinery sludge of higher water content relative to the first sludge.

21. A process according to claim 20 in which the dewatered sludge is preheated to a temperature of from 200°

to 500°

F. prior to being mixed with the coker feed.

22. A process according to claim 20 in which the first, high oil content sludge is dewatered by filtration.

23. A process according to claim 20 in which the the dewatered sludge is slurried with oil to a solids content of 10 to 20 weight percent prior to being mixed with the coker feed.

24. A process according to claim 20 in which the first refinery sludge of high oil content comprises API (American Petroleum Institute) separator skimmings, slop oil or slop oil emulsion solids and the second sludge of relatively high water content comprises DAF (Dissolved Air Flotation) float or a biosludge.