Motor and pump parts

Abstract

A separator for reducing or eliminating the amount of suspending solids from a reservoir fluid of a downhole motor having a rotating seal. The cleaned fluid circulated past the seal and outermost bearing, the separator having a vortex, rotating cyclone or centrifuge, at least one inlet at least one outlet for cleaned fluid, at least one outlet for solid material, water, particulates or similar material separated from the cleaned fluid. The outlet for the clean fluid may include a porous filter.

Claims

1. A separator for reducing or eliminating the amount of suspending solids from a reservoir fluid of a downhole motor, having a rotating seal, cleaned fluid circulated past the seal and a bearing, the separator comprising a vortex comprising a rotating outer wall having a funnel shape and an inner surface having a constant diameter, at least one inlet located adjacent the base of the funnel shape where the distance between the funnel shape and an inner surface is a minimum, the rotation of the outer wall being sufficient to cause a vortex effect, at least one outlet for cleaned fluid located at the top of the inner surface, and at least one outlet located at the top of the funnel shape where the distance between the funnel shape and an inner surface is a maximum for solid material, water, particulates or similar material separated from the cleaned fluid.

2. The separator according to claim 1, wherein the outlet for the clean fluid includes a porous filter housed in an annulus between the central shaft and the inner surface.

3. The separator according to claim 2, including multiple bearings at different positions along a pump shaft, with different fluid pressures at each bearing.

4. The separator according to claim 3, wherein lee choke valves are used to choke the fluid pressure at each bearing.

5. The separator according to claim 4, wherein the lee choke valves have a different choke value to match the external pressure around the bearing at its location in the pump, the internal pressure inside the central shaft being sufficient to flush the bearing at the pump outlet which will be the greatest differential pressure.

6. The separator according to claim 1, further including a fluid path through the central shaft, and including a pump in communication with a gallery beneath the porous filter, the pump urging the cleaned fluid up through the central shaft.

7. The separator according to claim 6, wherein the cleaned fluid is energised by a screw pump.

8. The separator according to claim 1, wherein a rotating shaft drives the separator.

9. The separator according to claim 1, further including a fluid path through multiple bearings.

10. The separator according to claim 1, wherein there the cleaned fluid lubricates and flushes the bearings.

11. The separator according to claim 1, wherein a porous filter is used as a secondary filter.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) FIG. 1 is a section side view of the vortex separator and screw bearing lubrication boost pump.

(2) FIG. 2 is a section side view through a multi stage centrifugal pump.

(3) FIG. 3 is a section side view through a screw type pump.

(4) FIG. 4 is a graph illustration the external pressure at each pump bearing and the discharge pressure of the screw pump shown is FIG. 1.

(5) Referring to FIG. 1 there is shown a housing 1 with a flange 2 which connects to the output of a motor, typically via a protector (not shown). The assembly has a shaft 3 passing through its centre, which is mounted in bearings 4, 5. The outer housing 6 extends to an upper flange 7. Inlet ports 8 allow wellbore fluids to be drawn into the chamber 9 which is the inlet to the vortex separator 10. The vortex separator rotates with the shaft 1. The vortex separator has an outer wall 15 that has a funnel-shaped portion with a relatively wide diameter at its top 12 and tapers towards a relatively narrow diameter 11. An inner surface 28 has a constant diameter, so that the area 14 at the top of the funnel-shape then diminishes towards a more constricted area towards the base of the funnel-shape. With the turning of the vortex separator 10, as fluid and suspension mixture is introduced into the vortex separator from the chamber 9, the separator draws and separates the solids and water to flow along the wall 15 and through the outlet 43 while the lower density oil will flow to the upper edge 16 of the inner surface 28 and drawn into the filter 17. The oil passes downwards through the filter 17 into gallery 18, and then into the screw pump inlet 19. The screw pump consists of a main central screw 20, which is part of the main shaft 3 passing through the assembly, and two idle screw gears shafts 21 and 22 which are driven by the main screw 20. The oil is drawn downwards through the screws and is discharged at the high pressure end into the ID 24 of the shaft 3 via a passage 23. A rotating high pressure seal 25 provides a barrier at the interface of shaft 3 and housing 1. The pressure of the discharge of the screw pump is at least equal to the discharge pressure of the production fluid pump. At each bearing the pressurised oil passes through a Lee Viscojet miniature hydraulic choke 27 which controls the flow of oil into the bearing 5.

(6) Other forms of pump may be used, provided they are capable of developing a high pressure sufficient to overcome the discharge pressure of the production fluid pump.

(7) Since solids are separated by the action of the vortex, it may be found that the filter 17 is unnecessary, and the fluid directed to the centre of the separator has been sufficiently cleaned to be used without further filtering.

(8) If a filter is used, the direction of the fluid flow could periodically be reversed in order to flush the filter and release any build up of particulate matter which could clog the filter.

(9) Referring to FIG. 2 there is shown a multi stage centrifugal pump assembly 30, the shaft 3 transmitting the power through the vortex separator, drives the pump shaft 31 via a coupling 32. At each end of the coupling are 0 rings 33, 34 which seal respective surfaces 35, 36. The pressurized oil from the screw pump in passage 24 is also supplied into the ID 37 of the pump shaft 31, to feed the bearings 40, 41 via ports 38, 39. At each bearing the pressurised oil passes through a Lee Viscojet miniature hydraulic choke in the port 38 and 39 which controls the flow of oil into the bearing 40, 41. The excess oil passing through the bearing comingles with the production fluid 42.

(10) Referring to FIG. 3 there is shown a screw type pump, fully disclosed in US patent number 2013/0136639A1. This particularly lends itself to this application, in that it has a larger diameter drive shaft 50, and generates a greater pressure lift per stage, so requires fewer stages and hence fewer bearings 51, 52. It also has the advantage of having ports 53 through which clean fluid is fed, so continually flushing the moving outer surface of the screw pump with clean liquid and displacing any particulates such as formation sand away. The flushing fluid has to pass through a Lee Viscojet 54 to ensure the clean liquid flows at a controlled rate and the pressure inside the gallery 55 is maintained at the final discharge pressure. This is shown more clearly in FIG. 4. For a pump with 6 stages, there would be 7 bearings, for each new stage added, the discharge pressure at the end of that stage would be incrementally greater. At the end of the last stage added would be the maximum pump discharge pressure. The pressure inside the shaft would have to be equal to the maximum pump discharge pressure so that it can flush the final bearing 7. However, at each of the bearings 5, 4, the pressure required to flush the bearing is incrementally less. Hence, by adding a Lee Viscojet at each of these discharge points the amount of liquid that will exit and flush any one bearing is regulated, therefore uniform leakage along the entire shaft flow exit points is achieved. The screw pump can be sized to have a small flow rate to just flush the bearings, or it can be sized to have a higher flow rate so that it can flush both the bearings and the pump outer surfaces, preventing formation fines and solids from eroding the pump.