Oil recovery process and apparatus for oil refinery waste

• US 4,994,169 A
• Filed: 11/23/1988
• Issued: 02/19/1991
• Est. Priority Date: 11/23/1988
• 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: Elliott, John D. Jr., Godino, Rino L.
• Primary Examiner(s): Davis, Curtis R.
• Application Number:
  US07/275,259
• Time in Patent Office: 818 Days
• Field of Search: 208/131, 208/50, 201/25, 201/2.5, 196/104, 196/105, 202/96
• US Class Current: 208/50
• 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: C10G 9/005 Coking (in order to produce liquid products mainly)

Abstract

A process and apparatus for the recovery of oil from aqueous oil refinery waste involves mixing the waste with a fluidizing oil and evaporating the water from the mixture in a plurality of stages. The dewatered mixture is fed to a delayed coking system in which a conventional coker feedstock is being used. The heavy hydrocarbon portion of the dewatered mixture changes to coke and light hydrocarbon material, the inert solids become trapped in the coke, and the fluidizing oil vaporizes. A stream of heavy coker gas oil is fed from a fractionator in the delayed coking system to a fluidizing tank where it is mixed with the sludge to define the fluidizing oil. Another hot stream of hydrocarbon material from the coker fractionator is sent to the evaporator section to provide the heat for evaporation.

Claims

1. A process for recovery of oil from oily waste having high water content, a heavy hydrocarbon portion and inert solids, comprising:

mixing the waste with fluidizing oil to form a mixture;

evaporating the water from the mixture to dewater the mixture; and

feeding the dewatered mixture to a delayed coking process, including directing the dewatered mixture into a coke drum containing conventional coke feedstock and subjecting the dewatered mixture in the coke drum to coking conditions,

whereby the heavy hydrocarbon portion changes to coke and light hydrocarbon material, the inert solids become trapped in the coke, and the fluidizing oil vaporizes.

2. The process of claim 1, further comprising taking the fluidizing oil from a fractionator in the delayed coking process.

3. The process of claim 1, wherein the dewatered mixture is fed into the coke drum at the top of the coke drum.

4. The process of claim 1, wherein the dewatered mixture is fed into the coke drum at the bottom of the coke drum.

5. The process of claim 1, wherein the dewatered mixture is fed through a coker heater in the delayed coking process and then to the coke drum.

6. The process of claim 1, wherein heat for the evaporating step is provided by a fluid stream taken from a coker fractionator in the delayed coking process.

7. The process of claim 1, wherein water evaporated from the mixture contains some fluidizing oil, the water being separated from the fluidizing oil in a coalescer.

8. The process of claim 7, wherein the fluidizing oil in the coalescer is included with the fluidizing oil mixed with the oil waste.

9. The process of claim 1, wherein the fluidizing oil for the mixing steps taken from a fractionator in the delayed coking process.

10. The process of claim 1, wherein the evaporating step is performed in a series of stages.

11. Apparatus for disposing of oily waste having high water content, a heavy hydrocarbon portion and inert solids, comprising:

means for mixing the waste with fluidizing oil to form a mixture;

means for evaporating the water form the mixture, said evaporating means producing vapors of water and fluidizing oil to leave a dewatered mixture of waste and fluidizing oil;

means for recovering fluidizing oil from the vapors of water and fluidizing oil;

means for producing coke by a delayed coking method, said coke producing means including a coke drum having an inlet at its bottom, a coker heater heaving an inlet, a coker fractionator, and means for conducting conventional coker feedstock through the coker heater to the coke drum; and

means for feeding the dewatered mixture of waste and fluidizing oil from said evaporating means to said coke producing means,

whereby the heavy hydrocarbon portion of the dewatered mixture changes to coke and light hydrocarbon material, the inert solids become trapped in the coke, and the fluidizing oil vaporizes.

12. The apparatus of claim 11, wherein said feeding means comprises conduit means for carrying the dewatered mixture to the top of the coke drum.

13. The apparatus of claim 11, wherein said feeding means comprises conduit means for carrying the dewatered mixture to the inlet of the coker heater.

14. The apparatus of claim 11, wherein said feeding means comprises conduit means for carrying the dewatered mixture to the inlet of the coke drum.

15. The apparatus of claim 11, wherein said feeding means comprises a first conduit extending from the evaporating means to the top of the coke drum, a second conduit extending from the evaporating means to the inlet of the coker heater, a third conduit extending iron the evaporating means to the inlet of the coke drum, and a control valve mounted in each of said conduits, whereby the dewatered mixture can be fed to any one of the top of the coke drum, the inlet of the coker heater, and the inlet of the coke drum, as well as to combinations of these locations.

16. The apparatus of claim 11, wherein said coker fractionator contains hot hydrocarbon fluids, the apparatus further comprising means for leading a stream of said hot hydrocarbon fluids to said heat exchanger to provide heat for evaporating water from the mixture of fluidizing oil and waste.

17. The apparatus of claim 16, wherein the evaporating means includes a heat exchanger, the mixture of waste and fluidizing oil flows through said first flow path, and said leading means extends from the coker fractionator to said second flow path, whereby the stream of hot hydrocarbon fluids flows to said heat exchanger to transfer heat to the mixture.

18. The apparatus of claim 11, wherein said coker fractionator contains hydrocarbon fluids, the apparatus further comprising means for guiding hydrocarbon fluid to said mixing means, said fluidizing oil comprising said hydrocarbon fluid.

19. The apparatus of claim 18, wherein said hydrocarbon fluid is heavy coker gas oil.

20. The apparatus of claim 11, further comprising means for separating the fluidizing oil from the water in the vapor.

21. The apparatus of claim 20, further comprising means for returning the separated fluidizing oil of the separating means to said mixing means.

22. The apparatus of claim 11, wherein said evaporating means comprises a plurality of evaporator tanks and means for feeding the mixture of waste and fluidizing oil serially through each of said evaporator tanks.

23. The apparatus of claim 11, wherein said coke producing means further includes means for sending light material form the coke drum to the coker fractionator.