Prior Art
Brown U.S. Pat. No. 3,781,134
McArthur et al U.S. Pat. No. 3,653,786
Coberly U.S. Pat. No. 2,812,723
Coberly U.S. Pat. No. 2,682,225
Jeffery U.S. Pat. No. 2,191,717
Burt U.S. Pat. No. 2,187,486
McMahon U.S. Pat. No. 2,114,905
McMahon U.S. Pat. No. 2,080,623
Wolff U.S. Pat. No. 2,041,803
McMahon U.S. Pat. No. 1,992,436
Martin U.S. Pat. No. 1,845,675
Overstreet U.S. Pat. No. 1,782,310
McMahon U.S. Pat. No. 1,642,121
Ehrhart U.S. Pat. No. 1,548,029
Lang U.S. Pat. No. 1,372,150
Lang U.S. Pat. No. 1,372,149
Kimble U.S. Pat. No. 1,258,418
Germany U.S. Pat. No. 1,160,602
Morison U.S. Pat. No. 1,055,210
Boetcher U.S. Pat. No. 801,641
Great Britain U.S. Pat. No. 735,866
Labadie U.S. Pat. No. 676,239
Guethler U.S. Pat. No. 636,333
Jamison U.S. Pat. No. 121,376
Background of the Invention
This invention relates to downhole jet pumps having provisions by which high velocity power fluid is forced through a nozzle into a throat area which creates a suction in its wake. This invention provides an advantage over the present known jet pumps by the employment of a variable throat design having a deflector device which utilizes the normally wasted fluid motion located in the center of the jet stream.
The deflector device deflects the total fluid in the jet stream radially outwardly against the variable throat area in proportion to the pressure exerted by the surface power unit used to supply the power fluid to the jet nozzle. The greater the pressure exerted on the jet stream exiting the nozzle, the further up the deflector the suction action will occur. As the suction area in the variable throat is increased, the wake suction action also is increased.
The use of this type throat design allows employment of a larger diameter throat opening than was previously possible, while retaining a high efficient pumping action, all of which is a great advantage over other jet type pumps.
Another advantage of the deflector is to put the wasted fluid motion to work. As the deflector is moved back towards the nozzle, the fluid is deflected into a cone shaped mist, and it is this cone shaped mist action which is used to create the suction in the variable throat.
Since this throat does not employ any straight internal surface area in its bore, it is unlike any known jet pump which uses a deflector of any type.
The deflector throat relation of 10.degree.-15.degree. mentioned herein is merely a suggested figure and may vary according to the size of the pump and the volumes demanded. These angles may be changed according to the particular pump design and operational perimeters.
Summary of the Invention
This invention teaches improvements in jet pumps, and in particular a jet pump having a concentrically arranged suction chamber, nozzle, venturi, and deflector. The suction chamber is formed about the nozzle and venturi inlet, and is connected to a formation fluid source so that when power fluid is forced to flow through the nozzle and into the venturi, the resulting stream of fluid entrains the formation fluid located within the suction chamber, so that mixed fluid flow occurs into the throat of the venturi.
The deflector is tapered in a direction towards the nozzle, and a marginal free end thereof is mounted within the discharge opening of the throat thereby leaving an annular area between the outer wall surface of the deflector and the circumferentially extending inner wall surface of the venturi throat; this annular area increases in a downstream direction, depending upon the relative angle of divergence of the venturi and deflector. Produced fluid and spent power fluid therefore flow from the discharge opening into a produced fluid outlet of the pump, where the comingled spent power fluid and the produced fluid are then forced to flow to the surface of the earth. Hence, the deflector cooperates with the discharge opening of the throat and with the nozzle in a manner to significantly increase the efficiency of operation of a jet pump apparatus.
Accordingly, a primary object of the present invention is the provision of improvements in downhole jet-type pumps.
Another object of the present invention is the provision of apparatus in conjunction with a jet-type pump which eliminates axial flow through the discharge opening of a venturi throat associated therewith.
A further object of this invention is to disclose and provide a jet-type pump having apparatus associated therewith which provides for flow of power fluid through the nozzle and into the throat entrance whereupon the flow is then forced into an annular configuration thereby eliminating axial flow through the discharge nozzle throat.
A still further object of this invention is the provision of improvements in downhole jet-type pumps for producing oil wells.
These and various other objects and advantages of the invention will become readily apparent to those skilled in the art upon reading the following detailed description and claims and by referring to the accompanying drawings.
The above objects are attained in accordance with the present invention by the provision of a combination of elements which are fabricated in a manner substantially as described in the above abstract and summary.
Brief Description of the Drawings
FIG. 1 is a broken, longitudinal, cross-sectional representation of the present invention operatively disclosed in conjunction with a hydrocarbon producing wellbore;
FIG. 2 is an enlarged, detailed, longitudinal, cross-sectional representation of part of the downhole jet pump of FIG. 1;
FIG. 3 is a diagrammatical, cross-sectional representation of a view taken along lines AA, BB, CC, and DD of FIG. 2;
FIG. 4 is an end view of FIG. 2; and,
FIG. 5 is a table of data related to FIGS. 2 and 3.
Detailed Description of the Preferred Embodiment
FIG. 1 illustrates one embodiment of a jet pump 10 made in accordance with the present invention. The pump includes a power fluid inlet 12 at the upper end thereof and a formation fluid inlet 48 located at the opposed end 14 thereof. Produced and spent power fluids are discharged through outlet port 15. Seating shoe 16 supportingly receives the lower end of the pump body in the same manner of a conventional downhole hydraulic pump, and provides a formation fluid inlet passageway thereinto.
Power oil tubing 18 conducts flow of fluid through the interior 20 thereof, and is supported from a wellhead (not shown). A supply of power fluid flows from a surface pump (not shown), downhole into the interior 20 of the tubing. Well casing 24 is concentrically arranged respective to the tubing and forms annulus 26 therebetween through which produced fluid and spent power fluid can flow up the borehole and out of the usual Christmas Tree located above the ground (not shown).
A packer nose assembly 30 separates annulus 32 from tubing interior 20, while seal ring 34 cooperates with the main body of the pump to separate annulus 36 from annulus 32. Ports 35 communicate the tubing annulus and casing annulus, 36 and 26, with one another. Packer device 38 anchors the lower end of the tubing string to the casing string and prevents the occurrence of fluid flow between annulus 26 and lower casing interior 40. Perforation 42 communicate a pay zone or production formation with the casing interior 40, thereby providing a source of formation fluid at production inlet 48.
As may be appreciated by those skilled in the art, the power fluid inlet 12 may be directly connected to the string of tubing for use with the present invention as a fixed type downhole pump; or, alternatively, the pump of this invention can be of the free type, such as disclosed in FIG. 1.
Upper sub 44 forms part of the main pump body and is connected to a barrel 45 which in turn is connected to an outlet sub 46, so as to enable the various components of the pump to be serviced. The details of this construction is considered within the comprehension of those skilled in the art.
Flow passageway 49 of the pump of FIG. 1 is connected to a suction chamber 51. Nozzle 52 is affixed to upper sub 44 and has a very hard metal alloy jet formed at the free end 54 thereof. The end 66 of the nozzle freely extends into the suction chamber and is spaced from venturi entrance 64 of the venturi assembly 55 and from the interior wall of the barrel. Venturi throat 58 is concentrically arranged respective to the nozzle and barrel and extends axially away from the entrance in a downstream direction as the throat diverges radially outwardly commencing at AA and terminating at lower end 59.
Discharge chamber 60 has a deflector 61 concentrically mounted therewithin, with the lower enlarged end of the deflector being affixed to the interior wall 62 of the venturi assembly, thereby leaving a free tapered end 72 of the deflector which extends axially uphole into proximity of the venturi entrance 64, as seen at 70. The venturi and deflector therefore jointly cooperate together in the illustrated manner of FIGS. 1-4 to form an annulus therebetween which is of varying cross-section.
The passageway 74, formed at the lower marginal end between the venturi throat and the deflector, continues at 76 into the annular chamber 60 which is connected to the before mentioned port 15 to form a produced fluid outlet for the pump.
As seen in FIGS. 2 and 3, the venturi has a throat which includes a circumferentially extending wall surface 58 in the form of a cone which is spaced from the tapered wall surface 72 of the deflector, thereby leaving an annular area therebetween. The conicity of wall surface 58 and the taper of the deflector are of slightly different angles so that the annulus formed therebetween increases in area, even with equal angles. As seen illustrated in FIGS. 2 and 3, the deflector is a cone of 10.degree. taper while the walls of the venturi throat is arranged with a 15.degree. taper. The arrows at A--A, B--B, C--C, and D--D coincide with areas a, b, c, d of FIG. 3 and illustrates the progressive enlargement of the annulus between the venturi throat and deflector.
The venturi entrance 64 is spaced from the nozzle outlet 68 so that formation fluid is sucked from the suction chamber 51 due to the velocity of the mass flow at 68 and 58.
Numerals 74 and 76 indicate the entrained fluid flow brought about by the suction of the high velocity stream at 68. Numeral 70 indicates the outermost free reduced end portion of the deflector which causes the power fluid, spent power fluid, and produced fluid to assume a toroidal or annular flow path. At numeral 74 most all of the power has been extracted from the power fluid, and the comingled spent power fluid and formation fluid exit the venturi at constant diameter part 76 and enter the discharge chamber 60.
In operation, as the power fluid moves into the entrance of the venturi, it commences to mix with the production fluid at 64, thereby sucking the production fluid from the suction chamber 51 into the throat 58. The power fluid which remains adjacent to the axial centerline of the throat ordinarily would be wasted energy in the absence of the deflector 61 because it cannot otherwise entrain any appreciable amount of the production fluid as noted in FIG. 3.
In order to move the power fluid from the relative inefficient central location into more intimate contact with the produced fluid, the deflector is employed in the illustrated manner of FIGS. 1-3. This new combination of elements increases the friction drag of the power fluid against the production fluid, thereby further increasing the suction which draws additional production into the venturi.
Progressively increasing the area of the annulus commencing at the apex 70 of the deflector and continuing through the venturi into the constant diameter chamber 76 places the power fluid in more intimate contact with the produced fluid, thereby significantly increasing the efficiency of the jet pump. This enables a greater production volume to be achieved at a lower operating pressure.