Apparatus and methods of separation of materials in an under-balanced drilling operation

• US 6,328,118 B1
• Filed: 03/08/1999
• Issued: 12/11/2001
• Est. Priority Date: 03/08/1999
• Status: Expired due to Term

• Current Assignee: Halliburton Energy Services Incorporated (Halliburton Company)
• Original Assignee: Halliburton Energy Services Incorporated (Halliburton Company)
• Inventors: Burris, Wesley Jay II, Karigan, Joseph Michael
• Primary Examiner(s): NEUDER, WILLIAM P
• Application Number:
  US09/265,553
• Time in Patent Office: 1,009 Days
• Field of Search: 175/66, 175/206, 210/744, 210/788, 210/801, 210/803, 210/804, 210/747, 210/170, 210/188, 210/512.1, 210/519, 210/523, 210/526
• US Class Current: 175/66
• CPC Class Codes: B01D 21/10 Settling tanks with multiple outlets for the separated liquids
• CPC Class Codes: B01D 21/2411 having a tangential inlet
• CPC Class Codes: B01D 21/245 Discharge mechanisms for the sediments
• CPC Class Codes: B01D 21/2472 Means for fluidising the sediments, e.g. by jets or mechanical agitators
• CPC Class Codes: B01D 21/2494 provided with means for the removal of gas, e.g. noxious gas, air
• CPC Class Codes: B01D 21/26 Separation of sediment aided by centrifugal force or centripetal forcecentrifuges B04B; cyclones B04C
• CPC Class Codes: B01D 21/34 Controlling the feed distribution; Controlling the liquid level ; Control of process parameters
• CPC Class Codes: B01D 2221/04 Separation devices for treating liquids from earth drilling, mining separation of well effluents E21B43/34, flotation in general B03D1/00
• CPC Class Codes: E21B 21/063 by separating components
• CPC Class Codes: E21B 21/065 Separating solids from drilling fluids

Abstract

Disclosed are improved apparatus and methods of separation and control of drilling fluids in under-balanced drilling. Separation is conducted at reduced pressures to improve gas separation efficiencies. Preferably, separation is performed in multiple steps of pressure drops to eliminate foaming and to enhance gas removal. Solids are removed from the shaped bottom of a separation pressure chamber by creating a slurry and fluidizing and agitating the slurry to enhance solids removal.

Claims

1. A method of separating fluids present in a hydrocarbon well in an under-balanced drilling operation wherein operating fluid circulating through the well during drilling is mixed with well materials flowing into the wall from a surrounding well formation and is mixed with solids from the drilling operation and wherein a returning stream of mixed fluids and solids flowing out of the well is at an elevated pressure, comprising the steps of:

supplying the returning stream flowing out of the well to a vertically extending separation chamber with a substantially conical bottom head with a solids outlet therein;

separating the liquid, gas, and solids of the returning stream in the chamber;

collecting the solids in the bottom of the chamber by gravity; and

removing the solids from the chamber by forming a moving slurry in the bottom of the chamber to agitate the solids and move them out through the solids inlet.

2. A method as in claim 1 wherein the moving slurry in the bottom of the chamber to agitate the solids and move them out through the solids outlet is formed by at least one sparging ring.

3. A method as in claim 1 wherein the moving slurry in the bottom of the chamber to agitate the solids and move them out through the solids outlet is formed by at least one sparging ling.

4. A method as in claim 2 wherein the moving slurry in the bottom of the chamber to agitate the solids and move them out through the solids outlet is formed by at least one vortex generator.

5. A method of drilling a hydrocarbon well as in claim 1 further comprising an inlet diverter for diverting the returning stream in the chamber into a vortex to separate the gas from the solids and liquids.

6. A method as in claim 5 wherein the inlet diverter comprises multiple parallel diverter units.

7. A method as in claim 5 wherein the inlet diverter comprises a hydrocyclone.

8. A method as in claim 5 wherein the inlet diverter comprises a tangential diverter.

9. A method as in claim 1 further comprising removing mist droplets from the gas after the gas is separated from the liquids and solids.

10. A method as in claim 1 wherein the chamber comprises at least one fluid outlet.

11. A method as in claim 10 wherein the chamber comprises a heavy fluids outlet and a light fluids outlet spaced vertically apart.

12. A method as in claim 11 further comprising controlling the level of the liquids in the chamber.

13. A method as in claim 1 wherein the moving slurry is removed from the chamber at least in part by a slurry pump operably attached to the solids outlet.

14. An vertically extending separation apparatus for separating materials from a returning stream from a hydrocarbon well in an under-balanced condition wherein operating fluid circulating through the well during drilling is mixed with well materials flowing into the well from a surrounding well formation and is mixed with solids from the drilling operation and wherein a returning stream of mixed liquid, gas and solids flowing out of the well is at an elevated pressure, comprising;

a pressure chamber having an interior wall, the chamber for separating the liquid, gas and solids of the returning stream;

a substantially conical bottom head in the chamber with a solids outlet therein, the bottom head of the chamber for collecting the solids by gravity to form a solids slurry; and

an agitation means in the bottom head of the chamber for agitating the solids slurry to thereby move the solids out through the solids outlet.

15. An apparatus as in claim 14 wherein the agitation means comprises at least one sparging ring.

16. An apparatus as in claim 14 wherein the agitation means comprises at least one sparging line.

17. An apparatus as in claim 14 wherein the agitation means comprises at least one vortex generator.

18. An apparatus as in claim 14 further comprising an inlet diverter for diverting the returning stream in the chamber into a vortex to separate the gas from the solids and liquids.

19. An apparatus as in claim 18 wherein the inlet diverter comprises multiple parallel diverter units.

20. An apparatus as in claim 18 wherein the inlet diverter comprises a hydrocyclone.

21. An apparatus as in claim 18 wherein the inlet diverter comprises a tangential diverter such that the returning stream is diverted to vortex along the interior wall of the chamber.

22. An apparatus as in claim 14 further comprising a mist removal device for removing mist droplets from the gas that is separated from the liquids and solids.

23. An apparatus as in claim 14 further comprising at least one fluid outlet in the interior wall of the chamber.

24. An apparatus as in claim 23 wherein the at least one fluid outlet comprises a heavy fluids outlet and a light fluids outlet spaced vertically apart and extending through the interior wall of the chamber.

25. An apparatus as in claim 24 further comprising a level controller for controlling the level of the liquids in the chamber.

26. An apparatus as in claim 14 further comprising a slurry pump operably attached to the solids outlet for removing the solids slurry from the chamber.