Many forms of pumps require a specific amount of net positive suction head (NPSH) to operate correctly and prevent cavitation. In any operation, fluid flows from areas of high pressure to areas of low pressure. Pumps in the same fashion operate by creating a low pressure condition at the inlet of the pumps which allows fluid to be pushed into the pump by atmospheric pressure or head pressure.
In a topside air environment, increasing the pressure to the pump inlet is done by raising the level of the supply fluid above the pump to create sufficient NPSH for the pump. However, in a subsea environment this practice cannot be replicated as the ambient fluid seawater is of similar density to the process fluid and therefore does not allow for differences in height to produce sufficient increase in pressure. Additionally, most subsea reservoirs are made from flexible material which cannot maintain pressure differences between the fluid outside and inside the tank. Internal pressure boosting is also difficult as the flexible membrane between the process fluid and the ambient fluid may not be able to handle a large pressure differential.
Further complicating the issue is that specific types of pumps in a subsea environment worsen this condition. Many pumps are protected from hydrostatic pressure by either utilizing an extremely thick and heavy housing to withstand external hydrostatic pressure or utilizing a compensator. Compensators apply ambient hydrostatic pressure to the interior of an assembly, say, a hydraulic reservoir of a pump via a small bladder and a spring which is external to pump. In many instances this concept further raises the required NPSH of pump as the internal pressure of the pump and inlet is now higher than the ambient pressure.
In general, some types of subsea pumps may require high inlet pressure as they are not able to pull a vacuum. In this scenario, a charge pump can be utilized to increase the suction line pressure to get the pump to operate correctly subsea.
Various figures are included herein which illustrate aspects of embodiments of the disclosed inventions.
It is noted that a majority of process fluids used subsea typically have a pressure in and around the specific gravity of seawater. A few cases, such as methanol, deviate from this.
In a first embodiment, referring generally to
In typical embodiments, each subsea fluid reservoir 10 comprises housing 11 and bladder 12 which comprises fluid typically at ambient pressure.
In typical embodiments, charge pump 30, which has an ability to pull a vacuum and provide an output pressure of around 15 to around 30 psi (1-2 bar above the ambient seawater pressure), may comprise a gear pump, a positive displacement pump, a solenoid operated pump, a centrifugal pump, a diaphragm pump, or the like. Typically, charge pump 30 comprises motor 34 which is configured to drive charge pump 30 where charge pump 30 is mechanically or magnetically coupled to motor 34. Motor 34 may comprise a brushless DC motor, a hydraulic motor, a single phase AC motor, a multiphase AC motor, or the like. In certain embodiments, motor 34 comprises a motor housed in a dielectric fluid filled housing and/or motor housed in a one atmosphere (1 atm) housing.
In typical embodiments, feedback loop 102, which acts as a recirculation loop in the event of over pressurization, comprises first feedback fluid conduit 101 which is in fluid communication with charge pump fluid inlet 31 and with first fluid conduit 100; second feedback fluid conduit 103 which is in fluid communication with charge pump fluid outlet 32 and second fluid conduit 104; and first valve 33 which is in fluid communication with first feedback fluid conduit 101 and second feedback fluid conduit 103. Typically as well, first valve 33, which acts as a feedback loop check or relief valve, is disposed intermediate first feedback fluid conduit 101 and second feedback fluid conduit 103. It is noted that fluid in first fluid conduit 100 and first feedback fluid conduit 101 are typically at or around ambient pressure and the fluid in second feedback fluid conduit 103 is typically at or around charging pressure which can be around ten to twenty five psid.
Each controller 80 typically comprises housing 81, power source 83 operatively in communication with charge pump 30; and controls 82 which are disposed within housing 81 and operatively in communication with the charge pump 30. Controller 80 may be used to provide speed control to dial in flowrates as needed or as charge pump 30 loses efficiency over time. Controls 82 are typically disposed in a compensated oil filled or one atmosphere housing 81.
Fluid in first fluid conduit 100 may be at ambient pressure but fluid in second fluid conduit 104 is at a charged pressure which is greater than pressure in first fluid conduit, e.g. greater than ambient pressure such as having a fluid pressure of around 15 to 30 psi (1-2 bar above the ambient seawater).
In certain embodiments, one or more subsea pumps 70 may be present and disposed downstream from, and in fluid communication with, charge pump 30 via charge pump fluid outlet 32. Typically, each subsea pump 70 comprises subsea pump fluid inlet 71 and subsea pump fluid outlet 72 which is in fluid communication with third fluid conduit 106. Fluid in third fluid conduit 106 is typically at a fluid pressure greater than the charged pressure of fluid in second fluid conduit 104.
In alternative embodiments where subsea pump 70 is part of the configuration, one or more accumulators 40 may be present and disposed downstream of charge pump 30 intermediate subsea pump 70 and charge pump 30 where accumulator 70 is in fluid communication with charge pump fluid outlet 32. In such embodiments, one or more pressure transducers 50 may be present and operatively in communication with an associated accumulator 40 and controller 80. Each pressure transducer 50 is generally operative to provide a signal to controller 80 as to when controller 80 should turn on charge pump 30 to recharge accumulator 40 upon depletion of pressure within accumulator 40 to a predetermined pressure.
If subsea pump 70 is present, control valve 60 may be disposed intermediate subsea pump 70 and charge pump 30 where control valve 60 is operative to open or close fluid delivery to subsea pump 70 from charge pump 30 such as via charged pressure fluid conduit 105. Control valve 60 may be a remotely operated vehicle valve, an electrically actuated valve, or the like.
In certain currently contemplated embodiments, stepout 90 may be disposed intermediate, and in fluid communication with, charge pump outlet 32 and subsea pump 70. Stepout 90 may comprise a hose, a hydraulic flying lead with mechanical connections being made with a hotstab or coupler arrangement, or the like, or a combination thereof, such as charged pressure fluid conduit 105.
In the operation of exemplary embodiments, fluid charging system 1, which is as described above, may be used to provide adequate suction pressure for a pump inlet for a variety of flow rates and pressures. Fluid in bladder 12 is provided from a fluid source (not shown in the figures) and fluid charging system 1 used to provide protection for subsea fluid reservoir 10 and inlet conditions of subsea pump 30. First valve 33 protects its associated subsea fluid reservoir 10 from pressure leaking back.
Feedback loop 102 is used to protect inlet conditions of subsea pump 30 by setting first valve 33 to open near a maximum inlet condition. First valve 33 may be used to provide pressure protection in case first valve 33 is closed and charge pump 30 is run.
Charge pump 30 may comprise a charge pump configured to overcome a large pressure drop due to a long distance between subsea fluid reservoir 10 and charge pump fluid inlet 31 or a large set of restrictions or elbows and turns.
Charge pump 30 may also be used to directly charge accumulator 40 to minimize charge pump runtime.
With the circuit fully open, higher inlet pressures are delivered to subsea pump 70. Each charge pump 30 can be configured to deliver a variety of flowrates and pressure to subsea pump 70 depending on the application requirements. In general, these rates will consist of very low (less than around 0.1 GPM) to very high volumes (around 90 GPM).
The foregoing disclosure and description of the inventions are illustrative and explanatory. Various changes in the size, shape, and materials, as well as in the details of the illustrative construction and/or an illustrative method may be made without departing from the spirit of the invention.
This application claims priority through U.S. Provisional Application 62/636,528 filed on 28 Feb. 2018.
Number | Date | Country | |
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62636528 | Feb 2018 | US |