Patent Application
20200309135
This invention relates generally to the field of pumping systems, and more particularly, but not by way of limitation, to an improved horizontal pump design for use in low net positive suction head (NPSH) applications.
Horizontal pumping systems are used in various industries for a variety of purposes. Large split-casing pumps are often used to move fluids between surface-based storage facilities. For example, in the oil and gas industry horizontal pumping systems are used to pump fluids, such as water separated from oil, to a remote destination, such as a tank, retention pond or disposal well. Many split casing pumps used in this industry are designed to meet or exceed the standards set forth in API 610. Although generally effective, split casing pumps are expensive, difficult to manufacture and often create large lead times to delivery and installation.
As an alternative to split casing pumps, manufacturers have turned to multistage pumps designed for use in a downhole environment. These multistage pumps are placed on a skid-supported frame and used in a horizontal orientation. Typically these horizontal pumping systems include a pump, a motor, and a suction housing positioned between the pump and the motor. A thrust chamber is also included between the motor and the suction housing. The pump includes a discharge assembly that is connected to downstream piping.
Although widely adopted for use in submersible applications, conventional multistage centrifugal pumps have design requirements that frustrate use in many surface-based, horizontal applications. In downhole pumping applications, the pressure of the fluid at the pump inlet is created by the column of fluid in the wellbore above the pump. In surface-based pumping systems, however, the net positive suction head available (NPSHA) may be much lower. To match the NPSHA to the suction pressure required by the pump (NPSHR), designers have attempted to incorporate a separate “boost pump” that charges the fluid to a NPSHA that matches or exceeds the NPSHR required by the horizontal pump. The use of a separate boost pump is expensive and requires additional space that may not be available in certain applications.
In some applications, the pump may be positioned above the intake liquid level, thereby creating a suction lift configuration. Pumps that are positioned on berms above retaining ponds must accommodate suction lift conditions to move fluids out of the below-grade reservoir. In the past, single-stage centrifugal pumps have been paired with dry-prime assist mechanisms that evacuate air from the suction line so that only liquid is available at the pump. Although these systems work well for single-stage conventional pumps that are designed to operate in lower NPSHa conditions, there remains a need for specialized surface pumping systems that are capable of providing high flow rates in low NPSHa and suction lift conditions. It is to these and other deficiencies in the prior art that the present invention is directed.
In one aspect, the present invention includes a horizontal pumping system that has a motor, a pump driven by the motor and a priming module. The pump has a discharge on a first end of the pump, a suction end on a second end of the pump, and a plurality of stages between the suction end and the discharge. Each of the plurality of stages includes an impeller and a diffuser that encases the impeller. Each diffuser is an independent pressure vessel. The priming module may be a wet priming module or a dry priming module. The priming module permits the use of the horizontal pumping system in applications in which a suction lift configuration is present at the pump.
In another aspect, the present invention provides a horizontal pumping system that has a motor, a pump driven by the motor and a priming module. The pump includes a discharge on a first end of the pump and a suction end on a second end of the pump, where the discharge is between the suction end and the motor. The pump further includes a shaft seal module connected to the discharge and a plurality of stages between the suction end and the discharge. The priming module is configured to supply liquid to the suction end of the pump.
In yet another embodiment, the present invention includes a horizontal pumping system that has a motor, a pump driven by the motor and a priming module. The pump has a discharge on a first end of the pump, a suction end on a second end of the pump, and a plurality of stages between the suction end and the discharge. The discharge is between the suction end and the motor. Each of the plurality of stages includes a diffuser and an impeller, where each diffuser is an independent pressure vessel. The priming module is configured to supply liquid to the suction end of the pump.
In accordance with an exemplary embodiment,
Turning to
As used herein, the terms “upstream” and “downstream” provide relative positional references to components within the horizontal pumping system 100 based. Upstream components will be understood to be positioned closer to the suction end 112, while downstream components are positioned at a greater distance from the suction end 112 in the direction of fluid flow away from the suction end 112. Although the preferred embodiments are depicted in connection with a horizontal pumping system 100, it will be appreciated that the preferred embodiments may also find utility in other pumping systems, including surface-mounted vertical pumping systems.
The pump 106 includes one or more turbomachinery stages 110, a suction end 112 and a discharge 114. As depicted, the pump 106 is configured as an “end-suction” pump in which the suction end 112 is positioned on the opposite end of the pump 106 from the thrust chamber 104. The discharge 114 is positioned between the stages 110 and the thrust chamber 104. Generally, the motor 102 drives the pump 106 through one or more shafts (not visible) that extend through the thrust chamber 104 and discharge 114 to the stages 110. The motor 102 can be configured as a 4-pole motor that operates at half the rotational speed of a conventional 2-pole motor with an equivalent electrical input frequency. In one embodiment, the motor 102 is configured to rotate at no more than about 1,750 revolutions per minute (RPM). In other embodiments, the motor 102 is an internal combustion engine that produces torque to drive the pump 106. In certain embodiments, it may be desirable to deploy gearboxes, torque converters, clutches, or additional transmission components between the motor 102 and the pump 106. In yet other embodiments, the motor 102 is configured as a 2-pole electric motor.
The discharge 114 includes a shaft seal module 116 that supports and seals the shaft as it enters the discharge 114. The shaft seal module 116 includes one or more shaft seals (not shown) that prevent high pressure fluid from being released from the discharge 114 through the shaft seal module 116.
Pumped fluids are provided to the suction end 112 from the intake line 202 and pressurized by the pump stages 110. Each of the pump stages 110 includes a diffuser 118 and an impeller 120 contained within the diffuser 118. Unlike conventional multistage surface pumping systems, the diffusers 118 are not contained within a separate external housing. In this way, the diffusers 118 are each configured as an independent pressure vessel that can be sized without restriction to a common external housing found in conventional multistage pumps. This permits the diffuser 118 and the impeller 120 to be enlarged (e.g., a larger outer diameter) and configured for optimal operation under low net positive suction head (NPSH) conditions while also providing high flow rate operation. Additionally, this permits each stage 110 to be sized differently from the other stages 110 in the pump 106. For example, it may be desirable to use a larger diffuser 118 and impeller 120 on the stage 110 closest to the suction end 112 to manage lower NPSH at the suction end. In higher pressure applications, the pump 106 may optionally include an external housing (not depicted) that reinforces the various components of the pump 106 against elevated internal pressures. In some embodiments, the pump 106 includes a plurality of pump stages 110 and each diffuser 118 within the plurality of pump stages 110 is a different size than the other diffusers 118 within the pump 106.
In some embodiments, the stages 110 are configured as large, mixed flow stages. Suitable stages 110 are found in vertical turbine pump applications often used in steam-based power generation facilities. The impellers 120 are designed to provide an increase in the pressure of the pumped fluid while minimizing cavitation. In other embodiments, the stages 110 are configured as radial flow stages or axial flow stages. In yet other embodiments, the pump 106 includes a combination of mixed flow stages 110, radial flow stages 110 and axial flow stages 110. In these embodiments, the diffusers 118 and impellers 120 within the stages 110 may be different sizes, and in particular, may have outer diameters that are different sizes.
For example, a pump 106 might include a large radial flow “inducer” stage 110 adjacent the suction end 112, a small radial flow stage 110 downstream from the large radial flow stage 110, a large mixed flow stage 110 downstream from the small radial flow stage 110, and a small mixed flow stage 110 downstream from the large mixed flow stage 110. In a modification of this embodiment, the pump 106 may further include one or more axial flow stages 110 downstream from the mixed flow stages 110
In the embodiment depicted in
The check valve 128 may be a conventional flapper-style valve that closes the discharge 114 when fluid is not being pumped through the horizontal pumping system 100, or when sufficient suction is applied by the vacuum generator 124 through the horizontal pumping system 100. When the vacuum generator 124 is activated, air in the horizontal pumping system 100 and intake line 202 is evacuated and vented to the atmosphere or storage tank. Once a sufficient negative pressure has been applied through the horizontal pumping system 100, liquid is drawn from the liquid source 200 to the suction end 112 through the intake line 202. When the liquid reaches the priming valve 126, a buoyant float within the priming valve 126 is lifted by the rising liquid level. The priming valve 126 can be configured to automatically throttle or turn off the vacuum generator 124, or to power on the motor 102 of the horizontal pumping system 100 to initiate the pumping operation. In this way, the dry prime module 122 is well-suited to extend the operating range of the horizontal pumping system 100 to situations in which a suction lift condition is present at the suction end 112.
Referring to
In other embodiments, the wet prime module 130 may include an independent wet prime trash pump that feeds the suction end 112 of the horizontal pumping system directly from the liquid source 200.
Thus, the surface pumping system 100 is well suited to pump large volumes of fluid between surface facilities under negative suction lift conditions. Suitable applications include the movement of fluids between storage containers, retention ponds and naturally occurring bodies of water. Because the surface pumping system 100 is configured for high volume operation, the surface pumping system 100 can also be used to provide the fluid feed on hydraulic fracturing operations from a sub-grade liquid source 200. In these applications, the surface pumping system 100 can be used to transfer “frac” fluid from a storage facility to the high pressure triplex pumps commonly used in hydraulic fracturing operations.
It is to be understood that even though numerous characteristics and advantages of various embodiments of the present invention have been set forth in the foregoing description, together with details of the structure and functions of various embodiments of the invention, this disclosure is illustrative only, and changes may be made in detail, especially in matters of structure and arrangement of parts within the principles of the present invention to the full extent indicated by the broad general meaning of the terms in which the appended claims are expressed. It will be appreciated by those skilled in the art that the teachings of the present invention can be applied to other systems without departing from the scope and spirit of the present invention.
This application claims the benefit of U.S. Provisional Patent Application Ser. No. 62/824,782 entitled “High Flow and Low NPSHr Horizontal Pump with Priming Module” filed Mar. 27, 2019, the disclosure of which is herein incorporated by reference.
| Number | Date | Country | |
|---|---|---|---|
| 62824782 | Mar 2019 | US |
