IP Library › Granted Patent US 7,353,875
Granted Patent B2
US 7,353,875 · App. 11/302,649 · Granted Apr 8, 2008

Centrifugal blending system

Assignee: Halliburton Energy Services, Inc.
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Quick Facts
Patent No.
US 7,353,875
App. No.
11/302,649
Granted
Apr 8, 2008
Kind
B2
Abstract

The present invention relates generally to well servicing operations, and, more particularly, to devices, systems and methods useful in stimulation blending for fluids, mixtures, and/or slurries used in well servicing operations. A device, system and/or method is provided comprising a suction centrifugal pump capable of receiving an inlet fluid and providing a suction pressure arranged to substantially minimize a geyser effect in a proppant inlet and a mixer capable of receiving the inlet fluid provided by the suction centrifugal pump and mixing the inlet fluid with a proppant received from the proppant inlet, the mixer arranged to be substantially optimized for mixing. The device, system and/or method also comprises a discharge centrifugal pump capable of receiving the inlet fluid mixed with the proppant from the mixer and discharging the inlet fluid mixed with the proppant from the mixer downhole, the discharge centrifugal pump arranged to be substantially optimized for pumping. The system also comprises at least one downhole pump capable of receiving the inlet fluid mixed with the proppant from the mixer discharged downhole by the discharge centrifugal pump.

Claims (116)

1. A device comprising:

a suction centrifugal pump capable of receiving an inlet fluid and providing a suction pressure in a range of from about 1 pound per square inch to about 5 pounds per square inch and arranged to substantially minimize a geyser effect in a proppant inlet;

a mixer capable of receiving the inlet fluid provided by the suction centrifugal pump and mixing the inlet fluid with a proppant received from the proppant inlet, the mixer arranged to be substantially optimized for mixing; and

a discharge centrifugal pump capable of receiving the inlet fluid mixed with the proppant from the mixer and discharging the inlet fluid mixed with the proppant from the mixer downhole, the discharge centrifugal pump arranged to be substantially optimized for pumping.

2. The device of claim 1 , further comprising:

a speed sensor capable of sensing an impeller speed of the mixer;

a pressure sensor capable of sensing a mixer exit pressure;

a speed/pressure controller capable of receiving the impeller speed information sensed by the speed sensor and the mixer exit pressure information sensed by the pressure sensor;

a mixer hydraulic control head capable of being controlled by the speed/pressure controller;

a mixer hydraulic pump capable of being controlled by the hydraulic control head; and

a mixer hydraulic motor capable of cooperating with the mixer hydraulic pump to drive at least one impeller of the mixer.

3. The device of claim 1 , further comprising:

a suction pressure sensor capable of sensing the suction pressure of the inlet fluid provided by the suction centrifugal pump;

a suction pressure controller capable of receiving the suction pressure information sensed by the suction pressure sensor;

a suction hydraulic control head capable of being controlled by the suction pressure controller;

a suction hydraulic pump capable of being controlled by the suction hydraulic control head; and

a suction hydraulic motor capable of cooperating with the suction hydraulic pump to drive at least one impeller of the suction centrifugal pump.

4. The device of claim 1 , further comprising:

a discharge pressure sensor capable of sensing a discharge pressure of the inlet fluid mixed with the proppant from the mixer provided by the discharge centrifugal pump;

a discharge pressure controller capable of receiving the discharge pressure information sensed by the discharge pressure sensor;

a discharge hydraulic control head capable of being controlled by the discharge pressure controller;

a discharge hydraulic pump capable of being controlled by the discharge hydraulic control head; and

a discharge hydraulic motor capable of cooperating with the discharge hydraulic pump to drive at least one impeller of the discharge centrifugal pump.

5. The device of claim 1 , wherein the mixer arranged to be substantially optimized for mixing is capable of providing an additional pressure in a range of about 1 pound per square inch to about 10 pounds per square inch above the suction pressure provided by the suction centrifugal pump.

6. The device of claim 1 , wherein the mixer arranged to be substantially optimized for mixing is arranged to substantially minimize a wear rate in the mixer.

7. The device of claim 1 , wherein the mixer arranged to be substantially optimized for mixing is arranged to substantially minimize vapor released from volatile liquids due to lower differential pressures.

8. The device of claim 1 , wherein the mixer arranged to be substantially optimized for mixing is arranged to substantially minimize power required due to being substantially optimized for mixing.

9. The device of claim 2 , further comprising:

a suction pressure sensor capable of sensing the suction pressure of the inlet fluid provided by the suction centrifugal pump;

a suction pressure controller capable of receiving the suction pressure information sensed by the suction pressure sensor;

a suction hydraulic control head capable of being controlled by the suction pressure controller;

a suction hydraulic pump capable of being controlled by the suction hydraulic control head;

a suction hydraulic motor capable of cooperating with the suction hydraulic pump to drive at least one impeller of the suction centrifugal pump;

a discharge pressure sensor capable of sensing a discharge pressure of the inlet fluid mixed with the proppant from the mixer provided by the discharge centrifugal pump;

a discharge pressure controller capable of receiving the discharge pressure information sensed by the discharge pressure sensor;

a discharge hydraulic control head capable of being controlled by the discharge pressure controller;

a discharge hydraulic pump capable of being controlled by the discharge hydraulic control head; and

a discharge hydraulic motor capable of cooperating with the discharge hydraulic pump to drive at least one impeller of the discharge centrifugal pump, wherein the mixer arranged to be substantially optimized for mixing is arranged to substantially minimize a wear rate in the mixer, to substantially minimize vapor released from volatile liquids due to lower differential pressures, and to substantially minimize power required due to being substantially optimized for mixing.

10. A method comprising:

providing a suction pressure in a range of from about 1 pound per square inch to about 5 pounds per square inch and arranged to substantially minimize a geyser effect in a proppant inlet using a suction centrifugal pump receiving an inlet fluid;

receiving the inlet fluid provided by the suction centrifugal pump and mixing the inlet fluid with a proppant received from the proppant inlet using a mixer arranged to be substantially optimized for mixing; and

receiving the inlet fluid mixed with the proppant from the mixer and discharging the inlet fluid mixed with the proppant from the mixer downhole using a discharge centrifugal pump arranged to be substantially optimized for pumping.

11. The method of claim 10 , further comprising:

sensing an impeller speed of the mixer using a speed sensor;

sensing a mixer exit pressure using a pressure sensor;

receiving the impeller speed information sensed by the speed sensor and the mixer exit pressure information sensed by the pressure sensor using a speech/pressure controller;

controlling a mixer hydraulic control head using the speed/pressure controller;

controlling a mixer hydraulic pump using the hydraulic control head; and

driving at least one impeller of the mixer using a mixer hydraulic motor cooperating with the mixer hydraulic pump.

12. The method of claim 10 , further comprising:

sensing the suction pressure of the inlet fluid provided by the suction centrifugal pump using a suction pressure sensor;

receiving the suction pressure information sensed by the suction pressure sensor using a suction pressure controller;

controlling a suction hydraulic control head using the suction pressure controller;

controlling a suction hydraulic pump using the suction hydraulic control head; and

driving at least one impeller of the suction centrifugal pump using a suction hydraulic motor cooperating with the suction hydraulic pump.

13. The method of claim 10 , further comprising:

sensing a discharge pressure of the inlet fluid mixed with the proppant from the mixer provided by the discharge centrifugal pump using a discharge pressure sensor;

receiving the discharge pressure information sensed by the discharge pressure sensor using a discharge pressure controller;

controlling a discharge hydraulic control head using the discharge pressure controller;

controlling a discharge hydraulic pump using the discharge hydraulic control head; and

driving at least one impeller of the discharge centrifugal pump using a discharge hydraulic motor cooperating with the discharge hydraulic pump.

14. The method of claim 10 , wherein receiving the inlet fluid provided by the suction centrifugal pump and mixing the inlet fluid with the proppant received from the proppant inlet using the mixer arranged to be substantially optimized for mixing further comprises using the mixer to provide an additional pressure in a range of about 1 pound per square inch to about 10 pounds per square inch above the suction pressure provided by the suction centrifugal pump.

15. The method of claim 10 , wherein the mixer arranged to be substantially optimized for mixing is arranged to substantially minimize a wear rate in the mixer.

16. The method of claim 10 , wherein the mixer arranged to be substantially optimized for mixing is arranged to substantially minimize vapor released from volatile liquids due to lower differential pressures.

17. The method of claim 10 , wherein the mixer arranged to be substantially optimized for mixing is arranged to substantially minimize power required due to being substantially optimized for mixing.

18. The method of claim 11 , further comprising:

sensing the suction pressure of the inlet fluid provided by the suction centrifugal pump using a suction pressure sensor;

receiving the suction pressure information sensed by the suction pressure sensor using a suction pressure controller;

controlling a suction hydraulic control head using the suction pressure controller;

controlling a suction hydraulic pump using the suction hydraulic control head;

driving at least one impeller of the suction centrifugal pump using a suction hydraulic motor cooperating with the suction hydraulic pump;

sensing a discharge pressure of the inlet fluid mixed with the proppant from the mixer provided by the discharge centrifugal pump using a discharge pressure sensor;

receiving the discharge pressure information sensed by the discharge pressure sensor using a discharge pressure controller;

controlling a discharge hydraulic control head using the discharge pressure controller;

controlling a discharge hydraulic pump using the discharge hydraulic control head; and

driving at least one impeller of the discharge centrifugal pump using a discharge hydraulic motor cooperating with the discharge hydraulic pump, wherein the mixer arranged to be substantially optimized for mixing is arranged to substantially minimize a wear rate in the mixer, to substantially minimize vapor released from volatile liquids due to lower differential pressures, and to substantially minimize power required due to being substantially optimized for mixing.

19. A system useful in stimulation blending for at least one of fluids, mixtures, and slurries used in well servicing operations, the system comprising:

a suction centrifugal pump capable of receiving an inlet fluid and providing a suction pressure arranged to substantially minimize a geyser effect in a proppant inlet;

a mixer capable of receiving the inlet fluid provided by the suction centrifugal pump and mixing the inlet fluid with a proppant received from the proppant inlet, the mixer arranged to be substantially optimized for mixing;

a discharge centrifugal pump capable of receiving the inlet fluid mixed with the proppant from the mixer and discharging the inlet fluid mixed with the proppant from the mixer downhole, the discharge centrifugal pump arranged to be substantially optimized for pumping; and

at least one downhole pump capable of receiving the inlet fluid mixed with the proppant from the mixer discharged downhole by the discharge centrifugal pump.

20. The system of claim 19 , further comprising:

a speed sensor capable of sensing an impeller speed of the mixer;

a pressure sensor capable of sensing a mixer exit pressure;

a speed/pressure controller capable of receiving the impeller speed information sensed by the speed sensor and the mixer exit pressure information sensed by the pressure sensor;

a mixer hydraulic control head capable of being controlled by the speed/pressure controller;

a mixer hydraulic pump capable of being controlled by the hydraulic control head; and

a mixer hydraulic motor capable of cooperating with the mixer hydraulic pump to drive at least one impeller of the mixer.

21. The system of claim 19 , further comprising:

a suction pressure sensor capable of sensing the suction pressure of the inlet fluid provided by the suction centrifugal pump;

a suction pressure controller capable of receiving the suction pressure information sensed by the suction pressure sensor;

a suction hydraulic control head capable of being controlled by the suction pressure controller;

a suction hydraulic pump capable of being controlled by the suction hydraulic control head; and

a suction hydraulic motor capable of cooperating with the suction hydraulic pump to drive at least one impeller of the suction centrifugal pump.

22. The system of claim 19 , further comprising:

a discharge pressure sensor capable of sensing a discharge pressure of the inlet fluid mixed with the proppant from the mixer provided by the discharge centrifugal pump;

a discharge pressure controller capable of receiving the discharge pressure information sensed by the discharge pressure sensor;

a discharge hydraulic control head capable of being controlled by the discharge pressure controller;

a discharge hydraulic pump capable of being controlled by the discharge hydraulic control head; and

a discharge hydraulic motor capable of cooperating with the discharge hydraulic pump to drive at least one impeller of the discharge centrifugal pump.

23. The system of claim 19 , wherein the suction centrifugal pump capable of receiving the inlet fluid and providing the suction pressure arranged to substantially minimize the geyser effect in the proppant inlet is capable of providing the suction pressure in a range of from about 1 pound per square inch to about 5 pounds per square inch.

24. The system of claim 19 , wherein the mixer arranged to be substantially optimized for mixing is capable of providing an additional pressure in a range of about 1 pound per square inch to about 10 pounds per square inch above the suction pressure provided by the suction centrifugal pump.

25. The system of claim 19 , wherein the mixer arranged to be substantially optimized for mixing is arranged to substantially minimize a wear rate in the mixer.

26. The system of claim 19 , wherein the mixer arranged to be substantially optimized for mixing is arranged to substantially minimize vapor released from volatile liquids due to lower differential pressures.

27. The system of claim 19 , wherein the mixer arranged to be substantially optimized for mixing is arranged to substantially minimize power required due to being substantially optimized for mixing.

28. The system of claim 20 , further comprising:

a suction pressure sensor capable of sensing the suction pressure of the inlet fluid provided by the suction centrifugal pump;

a suction pressure controller capable of receiving the suction pressure information sensed by the suction pressure sensor;

a suction hydraulic control head capable of being controlled by the suction pressure controller;

a suction hydraulic pump capable of being controlled by the suction hydraulic control head;

a suction hydraulic motor capable of cooperating with the suction hydraulic pump to drive at least one impeller of the suction centrifugal pump;

a discharge pressure sensor capable of sensing a discharge pressure of the inlet fluid mixed with the proppant from the mixer provided by the discharge centrifugal pump;

a discharge pressure controller capable of receiving the discharge pressure information sensed by the discharge pressure sensor;

a discharge hydraulic control head capable of being controlled by the discharge pressure controller;

a discharge hydraulic pump capable of being controlled by the discharge hydraulic control head; and

a discharge hydraulic motor capable of cooperating with the discharge hydraulic pump to drive at least one impeller of the discharge centrifugal pump, wherein the mixer arranged to be substantially optimized for mixing is arranged to substantially minimize a wear rate in the mixer, to substantially minimize vapor released from volatile liquids due to lower differential pressures, and to substantially minimize power required due to being substantially optimized for mixing.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 15, 2005
From: STEPHENSON, STAN; HORINEK, HERBERT; PHILLIPPI, MAX L.
To: HALLIBURTON ENERGY SERVICES, INC.
Reel/Frame 017368/0824 →
Continuity (1)
Related Publication 20070137862A1 · Jun 21, 2007