Systems and methods for oil field solid waste processing for re-injection

• US 10,589,287 B2
• Filed: 07/10/2015
• Issued: 03/17/2020
• Est. Priority Date: 07/10/2015
• Status: Active Grant

• Current Assignee: Ngl Water Solutions Permian, LLC (NGL Energy Partners LP)
• Original Assignee: NGL Solids Solutions, LLC (NGL Energy Partners LP)
• Inventors: Harman, Robert, Bailey, Terry, White, Justin, Bailey, Dustin, Garrett, Luke
• Primary Examiner(s): Self, Shelley M
• Assistant Examiner(s): Bapthelus, Smith Oberto
• Application Number:
  US14/796,073
• Publication Number:
  US 20170009557A1
• Time in Patent Office: 1,712 Days
• Field of Search: 241 23, 241 21, 241 80, 241 97, 209 121
• CPC Class Codes: B02C 23/14 with more than one separator
• CPC Class Codes: B02C 23/20 after crushing or disintegrating
• CPC Class Codes: E21B 41/0057 Disposal of a fluid by injection into a subterranean formation
• CPC Class Codes: E21B 43/35 specially adapted for separating solids down-hole drilling fluid separation systems E21B21/002; separating solids from drilling fluids E21B21/065
• CPC Class Codes: E21B 43/40 Separation associated with re-injection of separated materials E21B43/385 takes precedence

Abstract

Systems and methods for processing solid wastes from oil field operations including removal of wastes from oil tanks by a washout and vacuum conveyance system to form a slurry containing solid particles, solid particle size reduction by one or more grinders and, optionally, high velocity transport through recirculation circuits and disposal by injection into a subterranean formation.

Claims

1. A method of processing oil field waste for re-injection, the method comprising:

(i) receiving waste from an oil field waste source, the waste including first solid particles and second solid particles;

(ii) separating the waste through a first particle size separator;

wherein the first solid particles having a particle size smaller than a particle size threshold, are transferred to a first slurry tank, combined with fluid to form a first slurry, and at least a portion of the first slurry is removed and re-circulated back into the first slurry tank at a velocity sufficient for reducing particle size upon impact of the first solid particles with the first slurry tank as the first slurry is re-circulated;

wherein the second solid particles having a size larger than the particle size threshold, are transferred to a particle size reduction apparatus, reduced in size, transferred to a second slurry tank, combined with fluid to form a second slurry, and at least a portion of the second slurry is removed and re-circulated back into the second slurry tank and, at a velocity sufficient for reducing particle size upon impact of the second solid particles with the second slurry tank as the second slurry is recirculated;

(iii) removing at least a portion of slurry from the first slurry tank to create first slurry tank removed slurry and transferring the first slurry tank removed slurry to a second particle size separator; and

(iv) separating the first slurry tank removed slurry into (a) waste solids having a particle size larger than the particle size threshold and into (b) a re-injection slurry comprising particles with a particle size smaller than the particle size threshold.

2. The method of claim 1, wherein a portion of the second slurry is re-circulated back to the first separator.

3. The method of claim 1, wherein the waste solids having a particle size larger than the particle size threshold are transferred to a transportable container.

4. The method of claim 1, wherein the fluid to form the first slurry is selected from the group consisting essentially of water and brine.

5. The method of claim 1, wherein the waste from the oil field waste source is transferred to the second particle size separator without being processed through the first particle size separator.

6. The method of claim 1, wherein the particle size threshold of the first particle size separator and the particle size threshold of the second particle size separator, are in the range of 200 to 500 μ

m.

7. The method of claim 1, wherein at least a portion of the re-injection slurry is transferred to a positive displacement injection pump capable of pumping the portion of the re-injection slurry into a subterranean injection zone.

8. The method of claim 7, wherein some or all of the re-injection slurry is transferred to a surge volume tank when capacity of the positive displacement injection pump is exceeded or wherein some or all of the oil field waste is transferred to a surge volume tank when capacity of the first separator is exceeded.

9. The method of claim 1, wherein dilution brine water is transferred to at least one of a group consisting essentially of the first separator, the second separator, and the second slurry tank.

10. The method of claim 1, wherein the oil field waste source is an oil field tanker truck or a frac tank.

11. The method of claim 10, wherein the oil field waste from the oil field tanker truck or frac tank is diluted with a washout fluid and removed from the oil field tanker truck or frac tank by negative pressure.

12. The method of claim 11, wherein the negative pressure is produced by a vacuum conveyance system comprising:

a vacuum vessel capable of receiving washout waste;

a vacuum pump operably connected to the vacuum vessel and capable of producing negative pressure within the vacuum vessel; and

a transfer pump operably connected to the vacuum vessel and capable of transferring washout waste out of the vacuum vessel through positive pressure.

13. The method of claim 1, wherein the particle size reduction apparatus is selected from the group consisting essentially of a grinder, rotary blade crusher, ball mill, and hammer mill.

14. The method of claim 1, wherein waste from the oil field waste source is transferred to the second particle size separator and/or a third particle size separator when waste volume exceeds the capacity of the first particle size separator.

15. The method of claim 14, wherein the second particle size separator and third particle size separator separate waste or slurry into (a) waste solids having a particle size larger than the particle size threshold of the second particle size separator and third particle size separator and into (b) a re-injection slurry comprising particles with a particle size smaller than the particle size threshold of the second particle size separator and third particle size separator.

16. The method of claim 15, wherein the waste solids having a particle size larger than the particle size threshold of the second particle size separator and third particle size separator are transferred to a transportable solids container in communication with the second particle size separator and the third particle size separator.

17. The method of claim 1, wherein slurry from the second slurry tank is transferred to the second particle size separator and/or a third particle size separator.

18. The method of claim 1, further comprising a third particle separator, wherein both the second particle separator and third particle separator are operably connected to the first slurry tank.

19. A system for processing oil field waste comprising:

the oil field waste contained in a tank and comprising solid waste, oil-based mud, water-based mud, drill cuttings, crude oil sludge, cement residue, contaminated soil, and production tank bottoms;

a vacuum vessel sized to hold several hundred barrels of liquid oil field waste, and a high volume vacuum pump connected to the tank said high volume vacuum pump is capable of producing negative pressure within the vacuum vessel; and

;

a first particle separator positioned downstream of the vacuum vessel and a second particle separator positioned downstream of the first particle separator;

a first slurry tank and a second slurry tank; and

a particle size reduction apparatus;

a first pump and a second pump;

a first recirculation circuit and a second recirculation circuit and a transfer conduit;

wherein;

the first particle separator is operably connected to the particle size reduction apparatus and the first slurry tank;

the particle size reduction apparatus is operably connected to the second slurry tank;

the first pump is connected with the first slurry tank and the second particle separator in a manner to provide for re-circulation of slurry back into the first slurry tank through the first recirculation circuit and to transfer slurry to the second particle separator from the first slurry tank through the transfer conduit;

the second pump is connected with the second slurry tank, the first particle separator, and the particle size reduction apparatus in a manner to provide for re-circulation of slurry back into at least one of the second slurry tank, the first particle separator, and the particle size reduction apparatus through the second recirculation circuit.

20. The system of claim 19, wherein the first and second separator each comprise at least one vibratory mesh screen.

21. The system of claim 19, further comprising a positive displacement injection pump, wherein the second separator is operably connected to the first slurry tank and the positive displacement injection pump is operably connected to the first slurry tank.

22. The system of claim 19, further comprising:

a transfer pump operably connected to the vacuum vessel and capable of transferring the oil field waste out of the vacuum vessel through positive pressure.

23. The system of claim 19, further comprising brine water and a brine water transfer conduit configured for transferring brine water to at least one of the first separator, second separator, and second tank.

24. The system of claim 19, wherein the system is contained on a vehicle.

25. A system for processing oil field waste for re-injection, comprising:

a first particle separator and a second particle separator;

a first slurry tank, a second slurry tank, and a third slurry tank;

a particle size reduction apparatus;

a first pump and a second pump;

a first recirculation circuit and a second recirculation circuit and a transfer conduit;

wherein;

the first particle separator is operably connected to the particle size reduction apparatus and the first slurry tank;

the particle size reduction apparatus is operably connected to the second slurry tank;

the second particle separator is operably connected to the third slurry tank;

the first pump is connected with the first slurry tank and the second particle separator in a manner to provide for re-circulation of slurry back into the first slurry tank through the first recirculation circuit and to transfer slurry to the second particle separator from the first slurry tank through the transfer conduit;

the second pump is connected with the second slurry tank, the first particle separator, and the particle size reduction apparatus in a manner to provide for re-circulation of slurry back into the second slurry tank, the first particle separator, or the particle size reduction apparatus through the second recirculation circuit;

wherein a portion of slurry from the first slurry tank is transferred to the second particle separator and is separated through the second particle separator based on the particle size threshold of the second particle separator, wherein solid particles having a size below the particle size threshold of the second separator are transferred to the third slurry tank, and solid particles having a size above the particle size threshold are transferred to a transportable container.

26. The system of claim 25, further comprising:

a washout fluid source, wherein washout fluid from the washout fluid source is pumped into the interior of a tank to produce a washout waste;

a vacuum vessel capable of receiving the washout waste;

a vacuum pump operably connected to the vacuum vessel and capable of producing negative pressure within the vacuum vessel;

a transfer pump operably connected to the vacuum vessel and capable of transferring the washout waste out of the vacuum vessel through positive pressure; and

wherein the washout waste is transferred from the vacuum vessel to a magnetic filter capable of removing ferrous materials through magnetic attraction.

27. The system of claim 25 wherein the first particle separator is a vibratory shaker having internal screens with predetermined mesh sizes.

28. The system of claim 25 further comprising a filter vessel that contains a magnetic filter grating assembly to remove ferrous materials.

29. The system of claim 25 wherein the particle size reduction apparatus is selected from the group consisting essentially of a grinder, rotary blade crusher, ball mill, and hammer mill.

30. The system of claim 25 further comprising a third particle separator and a fourth slurry tank, wherein the third particle size separator separate waste or slurry into (a) waste solids having a particle size larger than the particle size threshold of the second particle size separator and third particle size separator and into (b) a re-injection slurry comprising particles with a particle size smaller than the particle size threshold of the second particle size separator and third particle size separator.

31. The system of claim 30 wherein at least a portion of the re-injection slurry is transferred to a positive displacement injection pump capable of pumping the portion of the re-injection slurry into a subterranean injection zone.

32. The system of claim 25 further comprising a sensor for measuring one or more properties of the slurry, including density, weight, viscosity, and particle size.

33. The system of claim 32 further comprising a processor operably linked to a motor that may be controlled according to a set of computer executable instructions.