Fluid treatment process

• US 7,964,101 B2
• Filed: 03/24/2009
• Issued: 06/21/2011
• Est. Priority Date: 01/25/2006
• Status: Active Grant

• Current Assignee: Q'Max Solutions, Inc.
• Original Assignee: Q'Max Solutions, Inc.
• Inventors: Slough, Kevin, Lupul, Troy
• Primary Examiner(s): Hruskoci; Peter A
• Application Number:
  US12/410,248
• Publication Number:
  US 20090178975A1
• Time in Patent Office: 819 Days
• Field of Search: 210/802
• US Class Current: 210/709
• CPC Class Codes: B01D 21/0045 Plurality of essentially parallel plates
• CPC Class Codes: B01D 21/06 with rotating scrapers
• CPC Class Codes: B01D 21/08 provided with flocculating compartments
• CPC Class Codes: B01D 21/2405 Feed mechanisms for settling tanks
• CPC Class Codes: B01D 21/2427 The feed or discharge opening located at a distant position from the side walls
• CPC Class Codes: B01D 21/32 Density control of clear liquid or sediment, e.g. optical control ; Control of physical properties
• 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
• CPC Class Codes: E21B 21/065 Separating solids from drilling fluids

Abstract

Processes for treating drilling fluid by passing the fluid through a separator including a clarifying zone and a thickening zone, the clarifying zone having inclined plates and the thickening zone having at least one wall with an angle of less than about 60°. The separator may optionally include an agglomeration zone and a removal zone.

Claims

1. A process of treating a primary fluid stream containing solids and liquids to produce a clarified liquid, comprising:

(a) introducing the primary fluid stream into a primary separator to separate first size solids and produce a solids fraction and a secondary fluid stream comprising liquids and second size solids;

(b) providing a secondary separator, the secondary separator comprising;

(i) an agglomeration zone;

(ii) a clarifying zone having a plurality of spaced apart clarifying plates;

(iii) a thickening zone having a lower end comprising at least one wall and a downwardly diminishing cross-sectional area, the agglomeration zone, clarifying zone and thickening zone being in fluid communication with each other; and

(iv) a diffuser having a plurality of ports disposed between the agglomeration zone and the clarifying zone;

(c) introducing the secondary fluid stream into the agglomeration zone and allowing the secondary fluid stream to mix with an agglomerate to produce agglomerated solids;

(d) allowing the secondary fluid stream and solids to flow through the ports of the diffuser to produce a substantially uniform flow in a substantially horizontal direction into the clarifying zone at or below a top edge of the clarifying plates; and

(e) allowing the solids to contact the clarifying plates and settle downwardly from the clarifying plates into the thickening zone to form settled solids in the lower end and clarified liquid in the clarifying zone.

2. The process of claim 1, further comprising providing in the thickening zone thickening pickets, the thickening pickets passing through the settled solids and releasing trapped clarified liquid.

3. The process of claim 1, further comprising removing the clarified liquid from the clarifying zone by means of a launder.

4. The process of claim 1, further comprising removing the settled solids from the thickening zone.

5. The process of claim 4, whereby the settled solids are removed by means of an auger having a first end inside the thickening zone and a second end outside the secondary separator, the auger rotatingly displacing the settled solids from the first end to the second end.

6. The process of claim 5, further comprising providing an auger motor for varying auger rotation speed.

7. The process of claim 6, further comprising providing a settled solids sensor operably coupled with the auger motor, the sensor sensing characteristics of the settled solids and inducing variation of the auger motor speed in response thereto.

8. The process of claim 4, whereby the settled solids are removed by means of a solids pump and a solids tank, the solids pump pumping the settled solids into the solids tank.

9. The process of claim 8, further comprising providing a settled solids sensor operably coupled with the solids pump, the sensor sensing characteristics of the settled solids and inducing variation of the solids pump speed in response thereto.

10. The process of claim 8, wherein the solids pump comprises a varying speed motor.

11. The process of claim 8, further comprising removing the solids fraction from the at least one primary separator into the solids tank.

12. The process of claim 1, wherein the clarifying plates are inclined.

13. The process of claim 1, further comprising introducing agglomerant into the secondary fluid stream prior to introducing the secondary fluid stream into the agglomeration zone.

14. The process of claim 1, wherein the agglomeration zone further comprises an intermixing sub-zone for rapid mixing of agglomerant with the secondary fluid stream.

15. The process of claim 1, wherein the at least one primary separator is a shale shaker.

16. The process of claim 1, wherein the at least one primary separator is a hydrocyclone.

17. The process of claim 1, wherein the at least one primary separator is a centrifuge.

18. The process of claim 1, further comprising the step of introducing the secondary fluid stream into a pump box prior to introducing the secondary fluid stream into the secondary separator.

19. The process of claim 1, wherein the lower end of the lower thickening zone comprises a frusto-conical configuration and a displacer is provided at the lower end selected from the group consisting of rotational scrapers, rotational sweepers, and rotational plows.

20. A process for treating drilling fluid containing solids and liquids to produce a clarified liquid, comprising:

(a) introducing a stream of drilling fluid into at least one primary separator to separate first size solids and produce a solids fraction and a secondary fluid stream comprising liquid and second size solids;

(b) providing a secondary separator, the secondary separator comprising an agglomeration zone having an inlet for receiving the secondary fluid stream and at least one fluid outlet, said agglomeration zone comprising an energy displacement sub-zone including a flow path obstacle disposed therein in substantially facing relation to the fluid inlet and having two ends, operative to turbulently mix agglomerant with the secondary fluid to agglomerate a portion of the second size solids therein while dissipating the energy of the second fluid, said at least one fluid outlet disposed proximately perpendicular to at least one of said ends, a clarifying zone having a plurality of spaced apart clarifying plates and a thickening zone having a lower end, said lower end having a downwardly diminishing cross-sectional area and comprising at least one angled wall, said agglomeration zone, clarifying zone and thickening zone being in fluid communication with one another;

(c) introducing the secondary fluid stream into the agglomeration zone and mixing an agglomerant with the secondary fluid stream in the agglomeration zone;

(d) introducing the secondary fluid stream from the agglomeration zone through said fluid outlet into the clarifying zone at a position at or below a top end of the clarifying plates and allowing the secondary fluid stream to flow among the clarifying plates; and

(e) allowing the second size solids to contact the clarifying plates and settle downwardly from the clarifying plates into the thickening zone to form settled solids in the lower end of the thickening zone and clarified liquid in the clarifying zone.

21. The process of claim 20, further comprising providing in the thickening zone thickening pickets, the thickening pickets passing through the settled solids and releasing trapped clarified liquid.

22. The process of claim 20, further comprising removing the clarified liquid from the clarifying zone by means of a launder.

23. The process of claim 20, further comprising removing the settled solids from the thickening zone by means of an auger having a first end inside the thickening zone and a second end outside the secondary separator, the auger rotatingly displacing the settled solids from the first end to the second end.

24. The process of claim 20, wherein the at least one primary separator is a shale shaker, a hydrocyclone, a centrifuge or a combination thereof.

25. The process of claim 20, further comprising the step of introducing the secondary fluid stream into a pump box prior to introducing the secondary fluid stream into the secondary separator.

26. The process of claim 20, wherein the lower end of the lower thickening zone comprises a frusto-conical configuration and a displacer is provided at the lower end selected from the group consisting of rotational scrapers, rotational sweepers, and rotational plows.