Pipeline integration oil recovery

Patent metadata

Field	Value
Publication number	US-11292972-B2
Application number	US-201916954110-A
Country	US
Kind code	B2
Filing date	Jul 11, 2019
Priority date	Jul 11, 2019
Publication date	Apr 5, 2022
Grant date	Apr 5, 2022

Abstract

A method may include: heating a hydrocarbon contaminated waste in a first heating unit, vaporizing at least a portion of water and hydrocarbons in the hydrocarbon contaminated waste and generating: a first vaporized stream and a first bottoms stream, heating the first bottoms stream in a second heating unit; vaporizing at least a portion of hydrocarbons in the first bottoms stream and generating: a second vaporized stream and a second bottoms stream, condensing the first vaporized stream to form a first condensed stream; and condensing the second vaporized stream to form a second condensed stream.

First claim

What is claimed is:

1. A method comprising:
heating a hydrocarbon contaminated waste in a first heating unit, wherein the hydrocarbon contaminated waste comprises hydrocarbons, particulates, and water;
vaporizing at least a portion of the water and the hydrocarbons in the hydrocarbon contaminated waste at a pressure less than 101.325 kPa to generate:
a first vaporized stream comprising vaporized water and vaporized hydrocarbons from the hydrocarbon contaminated waste; and
a first bottoms stream comprising at least a portion of the particulates and a portion of hydrocarbons not vaporized;

heating the first bottoms stream in a second heating unit;
vaporizing at least a portion of the hydrocarbons in the first bottoms stream at a pressure less than 101.325 kPa to generate:
a second vaporized stream comprising the at least the portion of the vaporized hydrocarbons from the first bottoms stream; and
a second bottoms stream comprising the particulates and portion of hydrocarbons not vaporized from the first bottoms stream;

condensing the first vaporized stream to form a first condensed stream; and
condensing the second vaporized stream to form a second condensed stream.

2. The method of claim 1 wherein the step of vaporizing at least a portion of the water and the hydrocarbons in the hydrocarbon contaminated waste is performed at a temperature of about 100° C. to about 250° C.

3. The method of claim 1 wherein the step of vaporizing at least a portion of the water and the hydrocarbons in the hydrocarbon contaminated waste is performed at a pressure of about 1 kPa to about 94 kPa.

4. The method of claim 1 wherein the step of vaporizing at least a portion of the hydrocarbons in the first bottoms stream is performed at a temperature of about 100° C. to about 250° C.

5. The method of claim 1 wherein the step of vaporizing at least a portion of the hydrocarbons in the first bottoms stream is performed at a pressure of about 1 kPa to about 94 kPa.

6. The method of claim 1 further comprising:
pumping a first motive fluid into a first eductor and generating a pressure drop within the first eductor thereby causing the first vaporized stream to be drawn into the first eductor; and
contacting the first motive fluid with the first vaporized stream in the first eductor, thereby causing at least a portion of the first vaporized stream to condense to form the first condensed stream.

7. The method of claim 6 wherein the first motive fluid comprises at least one fluid selected from the group consisting of air, steam, water, and combinations thereof.

8. The method of claim 1 further comprising:
pumping a crude oil into a second eductor and generating a pressure drop within the second eductor thereby causing the second vaporized stream to be drawn into the second eductor; and
contacting the crude oil with the second vaporized stream in the second eductor, thereby causing at least a portion of the second vaporized stream to condense to form the second condensed stream.

9. The method of claim 1 further comprising:
separating a hydrocarbon stream and an aqueous stream from the first condensed stream.

10. The method of claim 9 further comprising:
combining the second condensed stream and the hydrocarbon stream to form a reclaimed oil stream; and
introducing the reclaimed oil stream into a pipeline.

11. A method comprising:
heating a hydrocarbon contaminated waste in a first heating unit;
vaporizing at least a portion of the hydrocarbon contaminated waste to generate:
a first vaporized stream; and
a first bottoms stream;

heating the first bottoms stream in a second heating unit;
vaporizing at least a portion of the first bottoms stream to generate:
a second vaporized stream; and
a second bottoms stream;

condensing the first vaporized stream to form a first condensed stream; and
condensing the second vaporized stream to form a second condensed stream.

12. The method of claim 11 further comprising pumping a motive fluid into an eductor and generating a pressure drop within the eductor thereby causing the first vaporized stream to be drawn into the eductor; and
contacting the motive fluid with the first vaporized stream in the eductor, thereby causing at least a portion of the first vaporized stream to condense to form the first condensed stream.

13. The method of claim 11 further comprising pumping a motive fluid into an eductor and generating a pressure drop within the eductor thereby causing the second vaporized stream to be drawn into the eductor; and
contacting the motive fluid with the second vaporized stream in the eductor, thereby causing at least a portion of the second vaporized stream to condense to form the second condensed stream.

14. The method of claim 13 further comprising introducing the second vaporized stream into at least one cyclone prior to the step of introducing contacting the motive fluid with the second vaporized stream in the eductor.

15. The method of claim 11 further comprising introducing the first condensed stream into an oil-water separator and generating an output stream from the oil-water separator.

16. The method of claim 14 further comprising combining the output stream from the oil-water separator with the second condensed stream.

17. A system comprising:
a first heating unit comprising:
a first vessel;
at least one heater in thermal communication with the first vessel; and
a conveyance disposed within the first vessel;

a first eductor fluidically coupled to a vapor outlet of the first heating unit and a first motive fluid stream;
a second heating unit comprising:
a second vessel;
at least one heater in thermal communication with the second vessel; and
a conveyance disposed within the second vessel;

wherein an inlet of the second heating unit is fluidically coupled to a bottoms stream of the first heating unit; and
a second eductor fluidically coupled to an outlet of the second heating unit and a crude oil stream.

18. The system of claim 17 further comprising an oil-water separator fluidically coupled to an outlet of the first eductor.

19. The system of claim 17 further comprising at least one cyclone disposed between the outlet of the second heating unit and the second eductor, the at least one cyclone being fluidically coupled to the outlet of the second heating unit and an inlet of the second eductor.

20. The system of claim 17 further comprising a tank fluidically coupled to an outlet of the first eductor and an outlet of the second eductor.

Assignees

• Halliburton Energy Services Inc

Inventors

• Kapila Rajesh C

Classifications

• C10G31/06

  by heating, cooling, or pressure treatment · CPC title

• C10G2300/1003

  Waste materials · CPC title

• B01D45/16

  generated by the winding course of the gas stream {, the centrifugal forces being generated solely or partly by mechanical means, e.g. fixed swirl vanes} · CPC title

• C10G7/04 Primary

  Dewatering · CPC title

• B01D5/006

  with evaporation or distillation · CPC title