Many mechanical devices which utilize a lubricated rotating shaft as a component require seals on those shafts to either contain a pressurized fluid, e.g., for a shaft driving a pump, or to isolate one component from contamination, or both.
In the case of downhole rotating equipment, such as an electrical submersible pump (ESP), or a geared centrifugal pump (GCP), the rotating shafts require seals, principally to protect the fluids inside sensitive components, such as the electric motor (ESP) or the transmission (GCP), from contamination such as from production fluids.
The seals in these two applications are not called upon to withstand significant a pressure differential, as they are typically equipped with pressure compensators that keep both sides of the seal at near equal pressures. This is important in downhole equipment applications, as the devices are designed to operate essentially maintenance and service free, while at full power, and for years, so leakage across the seals must be kept to a minimum. If, as and when maintenance or repair is called for, the entire string must be pulled adding an inordinate loss of time and consequent expense.
The shaft seal types used most commonly in these downhole applications are end face mechanical seals such as that shown in
In electric submersible pump applications, only one set of seals is required to protect the electric motor. Such an arrangement is illustrated in
In the geared centrifugal pump application, there is a set of seals above and below the transmission (
The present invention addresses the excessive differential pressure in one set of seals, having as its objective, the balancing of fluid pressures, including ambient pressure, for all seals, both upper and lower, thereby minimizing the differential pressure between all seals and transmission they protect. An objective related to the foregoing is the extension of times related to maintenance and repair of existing components which might otherwise occur due to contamination and leakage of fugitive fluids.
Those skilled in the art will, upon reading of the forthcoming Detailed Description of a Preferred Embodiment, see additional objectives to be accomplished by the present invention, when read in concert with the drawings, wherein:
Referring now to the drawings, and initially to
The flow of production fluid along this path between the pump 33 and the receiver 39 results in a frictional pressure drop that can exceed 5 psi for large flow rates (˜5000 bfpd). This pressure drop is shown graphically on
Since the transmission pressure compensator 26 is located in the upper seal section 20, the pressure inside the transmission section is maintained at the same level as the average pressure in the upper seal section, PUS. The upper seal section shaft seals 21 and 22 are exposed to the ambient pressure, PUS, and seal against a transmission pressure that is essentially the same, due to the pressure compensation, hence, having essentially nil differential pressure across them.
The shaft seals 23 and 24, in the lower seal section 25, on the other hand, are exposed to an ambient pressure equal to PLS (lower section), which can be several psi greater than PUS (upper section), e.g., ΔP as shown in
The present invention, the objectives of which include remedying the problem of excessive pressure differential across the lower seals, is shown in
In keeping with the objectives of the invention, a somewhat modified structure is detailed in
In order to achieve the pressure balance required to avoid damage to the seals and maintain optimum performance for extended periods while the system is down hole, the upper seal section 30 communicates with the various elements in the section by means of a pressure compensation line or tube 53. The tube 53 extends from the lower seal section 32 (
In the
Line 53 is also connected to inter-seal pressure compensator 70, which maintains the pressure in inter-seal chambers 71 and 72 at PLS. Line 53 also connects to a chamber 68, between the first and second shaft seals 45 and 46, respectively, and maintains a pressure in chamber 68 equal to PLS. Seal 46 is open only to chamber 68 at its upper end, and to the transmission fluid in the chamber between seals 46 and 47 below, which is kept at PLS by inter-seal pressure compensator 70 so both sides of the seal 46 “see” PLS, hence there is nil pressure differential across the seal. The pressures on both sides of shaft seals 47 and 48 are also equal to PLS due to the inter-seal pressure compensator 70 and the main transmission pressure compensator 51 pressure. The inter-seal pressure compensator 70 is also required to provide pressure relief for chambers 71 and 73 in the event of sudden pump stoppage due to power interruption or shut-in. This compensator also provides enough additional communicating volume to compensate for thermal expansion or contraction of the liquid in chambers 47 and 48 due to changes in operating temperature. Only seal 45 experiences a differential pressure equal to ΔP. Since the pressure in chamber 68 is greater than the upper seal section produced fluid flow path (external) pressure PUS, the leakage through seal 45 is into the upper flow path, and this leakage is made up by flow from the lower seal section via tube 53. Seal 45 would be designed for longevity, not sealing ability, such as a labyrinth seal, as all it must do is allow the chamber to remain at PLS so that seals 46, 47 and 48 continue to have essentially a nil differential pressure. Even a “loose” seal, like a labyrinth seal, leaks at a very low rate compared to what line 53 can provide for make up, so chamber 68 will be easily maintained at PLS.
In the lower seal section 32, the lowest most shaft seal 85 is a labyrinth seal similar to 45 in the upper seal section. The chamber 83 between seal 85 and the next seal 74 is connected to line 53 and is in flow and pressure communication with the external lower seal section volume and, hence, is maintained at pressure PLS. Shaft seal 74, in the series that protects the transmission section, experiences an external pressure equal to PLS. In addition, line 53 communicates with the lower seal pressure compensator 86, which, in turn, communicates with the inter-seal chambers 80 and 81, so the pressure on both sides of the seals 74, 75 and 76 are equal to PLS. Since the internal pressure in the transmission section is maintained at PLS by the pressure compensator 51, as described above, the shaft seals in the lower seal section experience a nil, or near nil, pressure differential. The inter-seal pressure compensator 86 is required to provide pressure relief for chambers 80 and 81 in the event of sudden pump stoppage due to power interruption or shut down, as well as enough additional communicating volume to compensate for thermal expansion or contraction of the liquid in chambers 49 and 50 due to changes in operating temperature. Note near the intake 93 of line 53 is situated a bleed valve assembly 87. This bleed valve assembly 87 allows the free flow of produced fluid from inside lower seal section 32 to enter line 53, but restricts the rate of outflow of fluid from line 53 in the event of a sudden shutting-in of the system. This prevents the rapid loss of pressure in the external chambers of lower inter-seal pressure compensator 86, as well as main compensator 51 and upper inter-seal pressure compensator 70 when pump 34 suddenly stops, from damaging the aforementioned shaft seals.
The
While, those skilled in the art may perceive minor variations in specific structures, it will be understood that such minor variations are within the contemplation of the invention as described in the following claims:
Applicant claims the benefits of provisional application Ser. No. 61/888,131, filed Oct. 9, 2013. The present invention relates, in a general sense, to pressure compensation apparatus, with particular emphasis on minimization of pressure differentials across shaft seals in downhole elements.
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Number | Date | Country | |
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61888131 | Oct 2013 | US |