WO2021219678A1 - Vertical turbine pump and vertical turbine pump arrangement - Google Patents

Vertical turbine pump and vertical turbine pump arrangement Download PDF

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Publication number
WO2021219678A1
WO2021219678A1 PCT/EP2021/061044 EP2021061044W WO2021219678A1 WO 2021219678 A1 WO2021219678 A1 WO 2021219678A1 EP 2021061044 W EP2021061044 W EP 2021061044W WO 2021219678 A1 WO2021219678 A1 WO 2021219678A1
Authority
WO
WIPO (PCT)
Prior art keywords
guide vane
hub
vertical turbine
vane
pump
Prior art date
Application number
PCT/EP2021/061044
Other languages
French (fr)
Inventor
Erik ANDRÉ
Original Assignee
Xylem Europe Gmbh
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Xylem Europe Gmbh filed Critical Xylem Europe Gmbh
Priority to CN202180031607.4A priority Critical patent/CN115461543A/en
Publication of WO2021219678A1 publication Critical patent/WO2021219678A1/en

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D13/00Pumping installations or systems
    • F04D13/02Units comprising pumps and their driving means
    • F04D13/06Units comprising pumps and their driving means the pump being electrically driven
    • F04D13/08Units comprising pumps and their driving means the pump being electrically driven for submerged use
    • F04D13/10Units comprising pumps and their driving means the pump being electrically driven for submerged use adapted for use in mining bore holes
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D1/00Radial-flow pumps, e.g. centrifugal pumps; Helico-centrifugal pumps
    • F04D1/06Multi-stage pumps
    • F04D1/063Multi-stage pumps of the vertically split casing type
    • F04D1/066Multi-stage pumps of the vertically split casing type the casing consisting of a plurality of annuli bolted together
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D29/00Details, component parts, or accessories
    • F04D29/40Casings; Connections of working fluid
    • F04D29/42Casings; Connections of working fluid for radial or helico-centrifugal pumps
    • F04D29/426Casings; Connections of working fluid for radial or helico-centrifugal pumps especially adapted for liquid pumps
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D29/00Details, component parts, or accessories
    • F04D29/40Casings; Connections of working fluid
    • F04D29/42Casings; Connections of working fluid for radial or helico-centrifugal pumps
    • F04D29/44Fluid-guiding means, e.g. diffusers
    • F04D29/445Fluid-guiding means, e.g. diffusers especially adapted for liquid pumps
    • F04D29/448Fluid-guiding means, e.g. diffusers especially adapted for liquid pumps bladed diffusers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F05INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
    • F05DINDEXING SCHEME FOR ASPECTS RELATING TO NON-POSITIVE-DISPLACEMENT MACHINES OR ENGINES, GAS-TURBINES OR JET-PROPULSION PLANTS
    • F05D2240/00Components
    • F05D2240/10Stators
    • F05D2240/12Fluid guiding means, e.g. vanes
    • F05D2240/123Fluid guiding means, e.g. vanes related to the pressure side of a stator vane
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F05INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
    • F05DINDEXING SCHEME FOR ASPECTS RELATING TO NON-POSITIVE-DISPLACEMENT MACHINES OR ENGINES, GAS-TURBINES OR JET-PROPULSION PLANTS
    • F05D2240/00Components
    • F05D2240/10Stators
    • F05D2240/12Fluid guiding means, e.g. vanes
    • F05D2240/124Fluid guiding means, e.g. vanes related to the suction side of a stator vane

Definitions

  • the present invention relates generally to the technical field of bowl pumps for pumping liquid, such as clean/drinking water, chemicals, etc.
  • Bowl pumps are also known under the term vertical turbine pumps or multistage pumps. More precisely the present invention relates specifically to the technical field of guide vanes of such bowl pumps/ vertical turbine pumps.
  • the present invention relates to a vertical turbine pump that comprises:
  • an outer pump housing having an inlet, an outlet and an axial centre axis extending from said inlet to said outlet,
  • hub arrangement comprises:
  • the pump housing having an inner surface and an imaginary inner surface and the hub having an outer surface and an imaginary outer surface, wherein the imaginary inner surface of the pump housing is offset radially inwards from said inner surface fifteen percent of the radial distance between the inner surface of the pump housing and outer surface of the hub, and wherein the imaginary outer surface of the hub is offset radially outwards from said outer surface fifteen percent of the radial distance between the inner surface of the pump housing and the outer surface of the hub.
  • the vertical turbine pump further comprises a set of guide vanes, each guide vane extending in the radial direction between the outer surface of the hub and the inner surface of the pump housing, and extending in the axial direction from a start position located adjacent the impeller to an end position located downstream said start position, wherein each guide vane has a pressure side surface and a suction side surface, wherein said start position is defined as the radial plane through the vertical turbine pump that is located closest to the inlet of the pump housing and that intersects the guide vane the full distance from the imaginary inner surface of the pump housing to the imaginary outer surface of the hub, wherein said end position is defined as the radial plane through the vertical turbine pump that is located closest to the outlet of the pump housing and that intersects the guide vane the full distance from the imaginary inner surface of the pump housing to the imaginary outer surface of the hub, wherein each guide vane has a relative axial position along the axial centre axis starting from zero at the start position and ending at one at the end position, and wherein each guide vane in each
  • the present invention relates to a vertical turbine pump arrangement
  • a drive unit having a motor and a drive shaft, a column, a discharge connection connected to an upper end of said column, and at least one vertical turbine pump connected to a lower end of said column.
  • Bowl pumps are designed to have the advantages of centrifugal pumps in terms of efficiency and pressure while allowing a discharge flow in the axial direction like axial/propeller pumps.
  • the pump is designed to guide the liquid in an outward spiral in a mixture of radial/axial direction from the impeller towards the pump housing in order to increase the pressure by centrifugal action and thereafter guide vanes are used to redirect the liquid flow from rotating to axial in order to recover static pressure and to try to improve the flow profile leaving the pump housing to the next bowl pump.
  • the inlet of the bowl pump and the outlet of the bowl pump are of the same dimension.
  • the flow is the same through each bowl pump when having a multistage/stacked bowl pump arrangement, and at the same time the pressure/head is expected to increase in each stage/bowl pump.
  • the guide vanes extending in the radial direction between the outer surface of the hub and the inner surface of the pump housing are shaped to have an essentially straight radial extension or a slightly negative lean angle, i.e. the guide vane is tilted towards the suction side of the guide vane, i.e. the suction side surface of the guide vane is facing the outer surface of the hub, at the beginning of the guide vane and/or at the crest of the hub.
  • the conventional shape of the guide vanes are the consequence of a simplified design principle based on stream surfaces where the exchange of momentum perpendicular to the stream surface is limited.
  • known casting methods limits the variation of the lean angle along the axial extension of the guide vane, identified by the inventors limits the maximum possible efficiency of the pump.
  • this conventional guide vane design entails low efficiency, flow separation downstream the crest of the hub and resulting in dynamic pressure losses, especially in a multistage/stacked bowl pump arrangement where insufficient control of the flow profile in the an upstream stage pump causes problems for the downstream stage pump.
  • the present invention aims at obviating the aforementioned disadvantages and failings of previously known bowl pumps, and at providing an improved bowl/vertical turbine pump.
  • a primary object of the present invention is to provide an improved vertical turbine pump of the initially defined type wherein the guide vanes have a more optimal design/shape entailing a higher efficiency and less dynamic flow losses. It is another object of the present invention to provide a vertical turbine pump, wherein the guide vanes guide the pumped liquid towards the hub in order to obtain higher efficiency and more optimal flow profile leaving the pump housing.
  • each guide vane has a mean radial span vane angle (d) determined as a mean value of:
  • suction side radial span vane angle (b) between the suction side radial span and a radial line extending from the axial centre axis through the intersection between the suction side surface of the guide vane and the imaginary outer surface of the hub, wherein the suction side radial span vane angle (b) is positive measured from said radial line and in the rotational direction from suction side to pressure side, wherein each guide vane has a mean radial span vane angle (d) that is equal to or more than 30 degrees from 0,1 to 0,2 relative axial position of the guide vane.
  • a vertical turbine pump arrangement comprising an above-mentioned bowl pump, wherein the impeller of the vertical turbine pump is connected to a drive shaft extending from said motor.
  • the present invention is based on the insight of shaping the guide vanes, before the crest and/or at the crest, to guide the liquid flow towards the hub instead of towards the pump housing of the bowl pump in order to obtain higher efficiency, less flow separation and more optimal flow profile leaving the pump housing.
  • the guide vane is provided with positive lean angle at least before and/or at the crest of the hub, i.e. that the guide vanes are tilted towards the pressure side of the guide vane.
  • the pressure side surface of the guide vane is facing the outer surface of the hub.
  • each guide vane has a mean radial span vane angle (d) that is equal to or more than 30 degrees up to 0,3 relative axial position of the guide vane, preferably up to 0,5 relative axial position and most preferably up to 0,7 relative axial position. This means that the efficiency of the bowl pump is further enhanced, and the flow profile is even more optimal.
  • each guide vane has a mean radial span vane angle (d) that is equal to or more than 35 degrees from 0,1 to 0,2 relative axial position. This means that the efficiency of the bowl pump is further enhanced, and the flow profile is even more optimal.
  • each guide vane has a mean radial span vane angle (d) that is equal to or more than 40 degrees from 0,2 to 0,3 relative axial position. This means that the efficiency of the bowl pump is further enhanced, and the flow profile is even more optimal.
  • the crest of the hub is located upstream 0,3 relative axial position and located downstream 0,05 relative axial position.
  • Fig. 1 is a schematic semi cross sectional side view of a vertical bowl pump arrangement
  • Fig. 2 is a schematic perspective view from above of an inventive bowl/vertical turbine pump
  • Fig. 3 is a schematic cross-sectional side view of the bowl pump of figure 2
  • Fig. 4 is a schematic cross-sectional view from above of a bowl pump highlighting the pressure side radial span vane angle (a) and the suction side radial span vane angle (b), and Fig. 5a-f are schematic cross-sectional views from above at different relative axial position of the guide vanes.
  • the present invention relates to a bowl/vertical turbine pump, generally designated 1, and a vertical turbine pump arrangement, generally designated 2.
  • a bowl/vertical turbine pump generally designated 1
  • a vertical turbine pump arrangement generally designated 2.
  • a vertical bowl pump arrangement 2 is used for pumping liquid, such as clean/drink water, chemicals, etc., at great flow and great geodetic head, for instance for lifting liquid from deep wells or the like reservoirs.
  • Vertical bowl pump arrangements 2 comprises a drive unit 3 having a motor 4 and a drive shaft 5 extending from the motor 4 and driven in rotation by the motor 4.
  • the vertical bowl pump arrangement 2 further comprises a column 6 and a discharge connection 7 connected to an upper end of the column 6.
  • the column 6 has the function of a discharge/outlet pipe and the discharge connection 7 has the function of connecting the column 6 to outgoing piping or a tank (not disclosed).
  • the discharge connection 7 redirects the liquid flow from vertical to horizontal.
  • At the lower end of the column 6 one or more bowl pumps 1 are connected in series, i.e. stacked or multistage vertical bowl pump arrangement.
  • the vertical bowl pump arrangement 2 further comprises an inlet screen 8 or filter unit connected to the lowest bowl pump 1.
  • the vertical bowl pump arrangement 2 also comprises a drive shaft sleeve 9 surrounding and protecting the drive shaft 5 and extending inside the column 6.
  • the motor 4 is arranged outside the column 6, i.e. above the discharge connection 7.
  • the motor 4 is arranged inside the column 6, i.e. below the discharge connection 7, or arranged inside the discharge connection 7.
  • the drive shaft sleeve 9 may be constituted by several segments, especially smaller segments located between the bowl pumps 1.
  • the column 6 may be constituted by several segments.
  • the bowl pump 1 comprises an outer pump housing 10 having an inlet 11 and an outlet 12.
  • the bowl pump 1 comprises a center axis A extending from the inlet 11 to the outlet 12 and which is common with the center axis of the drive shaft 5, i.e. the center axis of the vertical bowl pump arrangement 2.
  • the inlet 11 and the outlet 12 match each other in order to be stackable, i.e. several bowl pumps 1 connected in series.
  • the inlet 11 and the outlet 12 have corresponding dimensions.
  • the bowl pump 1 further comprises a hub arrangement 13 located inside the pump housing 10, wherein the hub arrangement 13 comprises a stationary hub 14 and an impeller 15.
  • the hub 14 is located entirely inside the pump housing 10.
  • the impeller 15 is suspended from the hub 14 and located adjacent the inlet 11 of the pump housing 10.
  • the impeller 15 is located partly inside the pump housing 10 and partly outside the pump housing 10, i.e. protruding from the inlet 11.
  • the impeller 15 is a socalled closed or channel type impeller having an axial inlet 16 and radial outlets 17.
  • the impeller 15 comprises an upper cover disc 18 (cone shaped), a lower cover disc 19 (funnel shaped) and several spirally extending blades 20 extending between the lower cover disc 19 and the upper cover disc 18.
  • the impeller 15 is connected to the drive shaft 5 and driven in rotation by the drive shaft 5.
  • the hub 14 is onion shaped and the crest of the hub 14 is the location having the largest diameter.
  • the pump housing 10 comprises an inner surface 21 and the hub 14
  • the bowl pump 1 further comprises a set of guide vanes 23, wherein each guide vane 23 extending in the radial direction between the outer surface 22 of the hub 14 and the inner surface 21 of the pump housing 10, and extending in the axial direction from a start position located adjacent the impeller 15 to an end position located downstream said start position.
  • Each guide vane 23 has a pressure side surface 24 and a suction side surface 25.
  • the pump housing 10 has an imaginary inner surface 21' and the hub 14 has an imaginary outer surface 22' , wherein the imaginary inner surface 21' of the pump housing 10 is offset radially inwards from said inner surface 21 fifteen percent of the radial distance between the inner surface 21 of the pump housing 10 and outer surface 22 of the hub 14), and wherein the imaginary outer surface 22' of the hub 14 is offset radially outwards from said outer surface 22 fifteen percent of the radial distance between the inner surface 21 of the pump housing and the outer surface 22 of the hub.
  • the imaginary outer surface 22' and the imaginary inner surface 21' are used in order not to be disturbed during measurement by possible extra material at the transitions from hub 14 to guide vane 23 and from guide vane 23 to pump housing 10.
  • Said start position of the guide vane 23 is defined as the radial plane through the bowl pump 1 that is located closest to the inlet 11 of the pump housing and that intersects the guide vane 23 the full distance from the imaginary inner surface 2 of the pump housing 10 to the imaginary outer surface 22' of the hub 14.
  • Said end position of the guide vane 23 is defined as the radial plane through the bowl pump 1 that is located closest to the outlet 12 of the pump housing 10 and that intersects the guide vane 23 the full distance from the imaginary inner surface 2 of the pump housing 10 to the imaginary outer surface 22' of the hub 14.
  • each guide vane 23 has a relative axial position along the axial centre axis A starting from zero at the start position and ending at one at the end position.
  • Each guide vane 23 in each radial plane through the bowl pump 1 between the start position and the end position has a pressure side radial span 26, that extends between the intersection between the pressure side surface 24 of the guide vane 23 and the imaginary outer surface 22' of the hub 14 and the intersection between the pressure side surface 24 of the guide vane and the imaginary inner surface 21' of the pump housing, and has a suction side radial span 27, that extends between the intersection between the suction side surface 25 of the guide vane and the imaginary outer surface 22' of the hub and the intersection between the suction side surface 25 of the guide vane and the imaginary inner surface 2 of the pump housing.
  • FIG. 5a is taken at the start position of the guide vane 23 (i.e. at 0,0 relative axial position)
  • figure 5b is taken at 0,2 relative axial position
  • figure 5c is taken at 0,3 relative axial position
  • figure 5d is taken at 0,5 relative axial position
  • figure 5e is taken at 0,8 relative axial position
  • figure 5f is taken at the end position of the guide vane 23 (i.e. at 1,0 relative axial position).
  • each guide vane 23 has a mean radial span vane angle (d) determined as a mean value of:
  • a pressure side radial span vane angle (a) between the pressure side radial span 26 and a radial line extending from the axial centre axis A through the intersection between the pressure side surface 24 of the guide vane and the imaginary outer surface 22' of the hub, wherein the pressure side radial span vane angle (a) is positive measured from said radial line and in the rotational direction from suction side to pressure side, and - a suction side radial span vane angle (b) between the suction side radial span 27 and a radial line extending from the axial centre axis through the intersection between the suction side surface 25 of the guide vane and the imaginary outer surface 22' of the hub, wherein the suction side radial span vane angle (b) is positive measured from said radial line and in the rotational direction from suction side to pressure side.
  • Each guide vane 23 has a mean radial span vane angle (d) that is equal to or more than 30 degrees from 0,1 to 0,2 relative axial position of the guide vane. Thus, in the stated range the guide vane has positive lean.
  • a positive mean radial span vane angle (d) disclose that the guide vane is tilted in a direction that is opposite the rotational direction of the impeller, i.e. clockwise in figure 4.
  • the described definition of the mean radial span vane angle is chosen in order to simplify measurement, i.e. in a 3D-model or a real bowl pump it is easy to provide a radial cross section through the bowl pump 1 and measure the defined angles.
  • the mean radial span vane angle (d) is equal to or more than 30 degrees up to 0,3 relative axial position of the guide vane, preferably up to 0,5 relative axial position and most preferably up to 0,7 relative axial position, in addition to the mentioned range.
  • the mean radial span vane angle (d) is preferably equal to or more than 30 degrees from 0,05 relative axial position, in addition to the mentioned range.
  • the upper and lower limit of the mentioned range may be adjusted independently from each other.
  • the lower limit of the range may be as low as strictly more than 0.
  • the mean radial span vane angle (d) is equal to or more than 35 degrees from 0,1 to 0,2 relative axial position, preferably up to 0,3 relative axial position, and most preferably up to 0,5 relative axial position.
  • the mean radial span vane angle (d) that is equal to or more than 40 degrees from 0,2 to 0,3 relative axial position, preferably up to 0,4 relative axial position.
  • the mean radial span vane angle (d) is equal to or more than 20 degrees from 0,1 to 1 relative axial position of the guide vane.
  • the crest of the hub 14 is located upstream 0,3 relative axial position, and located downstream 0,05 relative axial position.
  • most guiding of the liquid flow inwards towards the hub 14 is performed before and/or at the crest of the hub 14, in order to reduce or entirely eliminate flow separation of the liquid at the outer surface 22 of the hub 14 downstream the crest.
  • the main redirection of the liquid flow from rotating to axial flow is performed downstream the crest of the hub 14.
  • the guide vanes 23 provide a reaction force inward towards the hub 14 at or about the crest.
  • crest per definition is the ridge or top or apex of the hub, i.e. the point where the hub is the widest/thickest seen in the radial direction, in conformity with a thread of a screw or the like.
  • the liquid flow is redirected from inclining outwards to inclining inwards in relation to the axial centre axis.
  • the liquid flow profile at the outlet 12 of the pump housing 10 has a greater density at the center, i.e. adjacent the drive shaft sleeve 9, than prior art solutions.
  • the next/downstream bowl pump will be fed with a liquid flow having a more uniform flow profile and higher pressure at the center and thereby the next/downstream bowl pump will add more pressure to the liquid than prior art solutions and will thereto be starting at a higher pressure level thanks to the output from the first/upstream bowl pump 1, i.e. entailing a much higher efficiency than prior art bowl pump arrangements.
  • the pressure side surface 24 and the suction side surface 25 of the guide vane can be parallel, diverging and/or approaching each other seen from the hub outwards.
  • the shape of these surfaces may be curved or straight or combination thereof.
  • one and the same guide vane may have different shape along the axial direction.
  • the pressure side radial span vane angle (a) and the suction side radial span vane angle (b) can be equal to each other of different.
  • the pressure side radial span and the suction side radial span are defined in a way not to be limited by the shape of the pressure side surface and the suction side surface.
  • the invention is defined in a way to embrace all variants concerning shape and thickness of the guide vanes.
  • the present invention also protects a bowl pump having the impeller temporarily disconnected from the hub, or having the impeller not yet installed in the bowl pump.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Mining & Mineral Resources (AREA)
  • Structures Of Non-Positive Displacement Pumps (AREA)

Abstract

The invention relates to a bowl pump and a vertical bowl pump arrangement. The bowl pump (1) comprises a pump housing (10), a hub (14) and guide vanes (23) extending between the hub (14) and pump housing (10). The guide vanes (23) has a positive lean angle, i.e. a mean radial span vane angle determined as a mean value of a pressure side radial span (26) vane angle (α) and a suction side radial span (27) vane angle (β) is equal to or more than 30 degrees from 0,1 to 0,2 relative axial position of the guide vane (23).

Description

VERTICAL TURBINE PUMP AND VERTICAL TURBINE PUMP ARRANGEMENT
Technical field of the Invention
The present invention relates generally to the technical field of bowl pumps for pumping liquid, such as clean/drinking water, chemicals, etc. Bowl pumps are also known under the term vertical turbine pumps or multistage pumps. More precisely the present invention relates specifically to the technical field of guide vanes of such bowl pumps/ vertical turbine pumps.
According to a first aspect the present invention relates to a vertical turbine pump that comprises:
- an outer pump housing having an inlet, an outlet and an axial centre axis extending from said inlet to said outlet,
- a hub arrangement, wherein the hub arrangement comprises:
- a stationary hub located inside the pump housing, and
- an impeller that is suspended from the hub and located adjacent said inlet of the pump housing, the pump housing having an inner surface and an imaginary inner surface and the hub having an outer surface and an imaginary outer surface, wherein the imaginary inner surface of the pump housing is offset radially inwards from said inner surface fifteen percent of the radial distance between the inner surface of the pump housing and outer surface of the hub, and wherein the imaginary outer surface of the hub is offset radially outwards from said outer surface fifteen percent of the radial distance between the inner surface of the pump housing and the outer surface of the hub.
The vertical turbine pump further comprises a set of guide vanes, each guide vane extending in the radial direction between the outer surface of the hub and the inner surface of the pump housing, and extending in the axial direction from a start position located adjacent the impeller to an end position located downstream said start position, wherein each guide vane has a pressure side surface and a suction side surface, wherein said start position is defined as the radial plane through the vertical turbine pump that is located closest to the inlet of the pump housing and that intersects the guide vane the full distance from the imaginary inner surface of the pump housing to the imaginary outer surface of the hub, wherein said end position is defined as the radial plane through the vertical turbine pump that is located closest to the outlet of the pump housing and that intersects the guide vane the full distance from the imaginary inner surface of the pump housing to the imaginary outer surface of the hub, wherein each guide vane has a relative axial position along the axial centre axis starting from zero at the start position and ending at one at the end position, and wherein each guide vane in each radial plane through the vertical turbine pump between the start position and the end position has a pressure side radial span, that extends between the intersection between the pressure side surface of the guide vane and the imaginary outer surface of the hub and the intersection between the pressure side surface of the guide vane and the imaginary inner surface of the pump housing, and has a suction side radial span, that extends between the intersection between the suction side surface of the guide vane and the imaginary outer surface of the hub and the intersection between the suction side surface of the guide vane and the imaginary inner surface of the pump housing.
According to a second aspect the present invention relates to a vertical turbine pump arrangement comprising a drive unit having a motor and a drive shaft, a column, a discharge connection connected to an upper end of said column, and at least one vertical turbine pump connected to a lower end of said column.
Background of the Invention
Bowl pumps are designed to have the advantages of centrifugal pumps in terms of efficiency and pressure while allowing a discharge flow in the axial direction like axial/propeller pumps. Thus, the pump is designed to guide the liquid in an outward spiral in a mixture of radial/axial direction from the impeller towards the pump housing in order to increase the pressure by centrifugal action and thereafter guide vanes are used to redirect the liquid flow from rotating to axial in order to recover static pressure and to try to improve the flow profile leaving the pump housing to the next bowl pump. The inlet of the bowl pump and the outlet of the bowl pump are of the same dimension. Thus, the flow is the same through each bowl pump when having a multistage/stacked bowl pump arrangement, and at the same time the pressure/head is expected to increase in each stage/bowl pump.
In known bowl/vertical turbine pumps, the guide vanes extending in the radial direction between the outer surface of the hub and the inner surface of the pump housing are shaped to have an essentially straight radial extension or a slightly negative lean angle, i.e. the guide vane is tilted towards the suction side of the guide vane, i.e. the suction side surface of the guide vane is facing the outer surface of the hub, at the beginning of the guide vane and/or at the crest of the hub. The conventional shape of the guide vanes are the consequence of a simplified design principle based on stream surfaces where the exchange of momentum perpendicular to the stream surface is limited. Thereto known casting methods limits the variation of the lean angle along the axial extension of the guide vane, identified by the inventors limits the maximum possible efficiency of the pump.
However, the inventors have identified that this conventional guide vane design entails low efficiency, flow separation downstream the crest of the hub and resulting in dynamic pressure losses, especially in a multistage/stacked bowl pump arrangement where insufficient control of the flow profile in the an upstream stage pump causes problems for the downstream stage pump.
Object of the Invention
The present invention aims at obviating the aforementioned disadvantages and failings of previously known bowl pumps, and at providing an improved bowl/vertical turbine pump. A primary object of the present invention is to provide an improved vertical turbine pump of the initially defined type wherein the guide vanes have a more optimal design/shape entailing a higher efficiency and less dynamic flow losses. It is another object of the present invention to provide a vertical turbine pump, wherein the guide vanes guide the pumped liquid towards the hub in order to obtain higher efficiency and more optimal flow profile leaving the pump housing.
It is another object of the present invention to provide a vertical turbine pump, wherein the flow separation of the liquid at the hub after the crest is decreased or entirely eliminated.
Summary of the Invention
According to the invention at least the primary object is attained by means of the initially defined bowl/vertical turbine pump having the features defined in the independent claims. Preferred embodiments of the present invention are further defined in the dependent claims.
According to a first aspect of the present invention, there is provided a vertical turbine pump of the initially defined type, which is characterized in that each guide vane has a mean radial span vane angle (d) determined as a mean value of:
- a pressure side radial span vane angle (a) between the pressure side radial span and a radial line extending from the axial centre axis through the intersection between the pressure side surface of the guide vane and the imaginary outer surface of the hub, wherein the pressure side radial span vane angle (a) is positive measured from said radial line and in the rotational direction from suction side to pressure side, and
- a suction side radial span vane angle (b) between the suction side radial span and a radial line extending from the axial centre axis through the intersection between the suction side surface of the guide vane and the imaginary outer surface of the hub, wherein the suction side radial span vane angle (b) is positive measured from said radial line and in the rotational direction from suction side to pressure side, wherein each guide vane has a mean radial span vane angle (d) that is equal to or more than 30 degrees from 0,1 to 0,2 relative axial position of the guide vane.
According to a second aspect of the present invention, there is provided a vertical turbine pump arrangement comprising an above-mentioned bowl pump, wherein the impeller of the vertical turbine pump is connected to a drive shaft extending from said motor.
Thus, the present invention is based on the insight of shaping the guide vanes, before the crest and/or at the crest, to guide the liquid flow towards the hub instead of towards the pump housing of the bowl pump in order to obtain higher efficiency, less flow separation and more optimal flow profile leaving the pump housing. Thus, the guide vane is provided with positive lean angle at least before and/or at the crest of the hub, i.e. that the guide vanes are tilted towards the pressure side of the guide vane. Thus, the pressure side surface of the guide vane is facing the outer surface of the hub.
According to various embodiments of the present invention, each guide vane has a mean radial span vane angle (d) that is equal to or more than 30 degrees up to 0,3 relative axial position of the guide vane, preferably up to 0,5 relative axial position and most preferably up to 0,7 relative axial position. This means that the efficiency of the bowl pump is further enhanced, and the flow profile is even more optimal.
According to various embodiments, each guide vane has a mean radial span vane angle (d) that is equal to or more than 35 degrees from 0,1 to 0,2 relative axial position. This means that the efficiency of the bowl pump is further enhanced, and the flow profile is even more optimal.
According to various embodiments, each guide vane has a mean radial span vane angle (d) that is equal to or more than 40 degrees from 0,2 to 0,3 relative axial position. This means that the efficiency of the bowl pump is further enhanced, and the flow profile is even more optimal.
According to various embodiments, the crest of the hub is located upstream 0,3 relative axial position and located downstream 0,05 relative axial position.
Further advantages with and features of the invention will be apparent from the other dependent claims as well as from the following detailed description of preferred embodiments.
Brief description of the drawings
A more complete understanding of the abovementioned and other features and advantages of the present invention will be apparent from the following detailed description of preferred embodiments in conjunction with the appended drawings, wherein:
Fig. 1 is a schematic semi cross sectional side view of a vertical bowl pump arrangement,
Fig. 2 is a schematic perspective view from above of an inventive bowl/vertical turbine pump,
Fig. 3 is a schematic cross-sectional side view of the bowl pump of figure 2,
Fig. 4 is a schematic cross-sectional view from above of a bowl pump highlighting the pressure side radial span vane angle (a) and the suction side radial span vane angle (b), and Fig. 5a-f are schematic cross-sectional views from above at different relative axial position of the guide vanes.
Detailed description of preferred embodiments of the invention
The present invention relates to a bowl/vertical turbine pump, generally designated 1, and a vertical turbine pump arrangement, generally designated 2. Reference are initially made to figures 1-3.
A vertical bowl pump arrangement 2 is used for pumping liquid, such as clean/drink water, chemicals, etc., at great flow and great geodetic head, for instance for lifting liquid from deep wells or the like reservoirs. Vertical bowl pump arrangements 2 comprises a drive unit 3 having a motor 4 and a drive shaft 5 extending from the motor 4 and driven in rotation by the motor 4. The vertical bowl pump arrangement 2 further comprises a column 6 and a discharge connection 7 connected to an upper end of the column 6. The column 6 has the function of a discharge/outlet pipe and the discharge connection 7 has the function of connecting the column 6 to outgoing piping or a tank (not disclosed). In the disclosed embodiment the discharge connection 7 redirects the liquid flow from vertical to horizontal. At the lower end of the column 6 one or more bowl pumps 1 are connected in series, i.e. stacked or multistage vertical bowl pump arrangement.
In the disclosed embodiment the vertical bowl pump arrangement 2 further comprises an inlet screen 8 or filter unit connected to the lowest bowl pump 1. The vertical bowl pump arrangement 2 also comprises a drive shaft sleeve 9 surrounding and protecting the drive shaft 5 and extending inside the column 6. In the disclosed embodiment the motor 4 is arranged outside the column 6, i.e. above the discharge connection 7. According to various alternative embodiments the motor 4 is arranged inside the column 6, i.e. below the discharge connection 7, or arranged inside the discharge connection 7. The drive shaft sleeve 9 may be constituted by several segments, especially smaller segments located between the bowl pumps 1. The column 6 may be constituted by several segments.
The bowl pump 1 comprises an outer pump housing 10 having an inlet 11 and an outlet 12. The bowl pump 1 comprises a center axis A extending from the inlet 11 to the outlet 12 and which is common with the center axis of the drive shaft 5, i.e. the center axis of the vertical bowl pump arrangement 2. The inlet 11 and the outlet 12 match each other in order to be stackable, i.e. several bowl pumps 1 connected in series. Thus, the inlet 11 and the outlet 12 have corresponding dimensions.
The bowl pump 1 further comprises a hub arrangement 13 located inside the pump housing 10, wherein the hub arrangement 13 comprises a stationary hub 14 and an impeller 15. The hub 14 is located entirely inside the pump housing 10. The impeller 15 is suspended from the hub 14 and located adjacent the inlet 11 of the pump housing 10. In the disclosed embodiment, the impeller 15 is located partly inside the pump housing 10 and partly outside the pump housing 10, i.e. protruding from the inlet 11. The impeller 15 is a socalled closed or channel type impeller having an axial inlet 16 and radial outlets 17. The impeller 15 comprises an upper cover disc 18 (cone shaped), a lower cover disc 19 (funnel shaped) and several spirally extending blades 20 extending between the lower cover disc 19 and the upper cover disc 18. The impeller 15 is connected to the drive shaft 5 and driven in rotation by the drive shaft 5. The hub 14 is onion shaped and the crest of the hub 14 is the location having the largest diameter. The pump housing 10 comprises an inner surface 21 and the hub 14 comprises an outer surface 22.
The bowl pump 1 further comprises a set of guide vanes 23, wherein each guide vane 23 extending in the radial direction between the outer surface 22 of the hub 14 and the inner surface 21 of the pump housing 10, and extending in the axial direction from a start position located adjacent the impeller 15 to an end position located downstream said start position. Each guide vane 23 has a pressure side surface 24 and a suction side surface 25.
Reference is now also made to figure 4, schematic and not disclosing all guide vanes.
The pump housing 10 has an imaginary inner surface 21' and the hub 14 has an imaginary outer surface 22' , wherein the imaginary inner surface 21' of the pump housing 10 is offset radially inwards from said inner surface 21 fifteen percent of the radial distance between the inner surface 21 of the pump housing 10 and outer surface 22 of the hub 14), and wherein the imaginary outer surface 22' of the hub 14 is offset radially outwards from said outer surface 22 fifteen percent of the radial distance between the inner surface 21 of the pump housing and the outer surface 22 of the hub. The imaginary outer surface 22' and the imaginary inner surface 21' are used in order not to be disturbed during measurement by possible extra material at the transitions from hub 14 to guide vane 23 and from guide vane 23 to pump housing 10.
Said start position of the guide vane 23 is defined as the radial plane through the bowl pump 1 that is located closest to the inlet 11 of the pump housing and that intersects the guide vane 23 the full distance from the imaginary inner surface 2 of the pump housing 10 to the imaginary outer surface 22' of the hub 14. Said end position of the guide vane 23 is defined as the radial plane through the bowl pump 1 that is located closest to the outlet 12 of the pump housing 10 and that intersects the guide vane 23 the full distance from the imaginary inner surface 2 of the pump housing 10 to the imaginary outer surface 22' of the hub 14. Thereto, each guide vane 23 has a relative axial position along the axial centre axis A starting from zero at the start position and ending at one at the end position.
Each guide vane 23 in each radial plane through the bowl pump 1 between the start position and the end position has a pressure side radial span 26, that extends between the intersection between the pressure side surface 24 of the guide vane 23 and the imaginary outer surface 22' of the hub 14 and the intersection between the pressure side surface 24 of the guide vane and the imaginary inner surface 21' of the pump housing, and has a suction side radial span 27, that extends between the intersection between the suction side surface 25 of the guide vane and the imaginary outer surface 22' of the hub and the intersection between the suction side surface 25 of the guide vane and the imaginary inner surface 2 of the pump housing.
Reference is now also made to figures 5a - 5f, disclosing six different radial planes or cross sections of the bowl pump 1. Figure 5a is taken at the start position of the guide vane 23 (i.e. at 0,0 relative axial position), figure 5b is taken at 0,2 relative axial position, figure 5c is taken at 0,3 relative axial position, figure 5d is taken at 0,5 relative axial position, figure 5e is taken at 0,8 relative axial position, figure 5f is taken at the end position of the guide vane 23 (i.e. at 1,0 relative axial position).
According to the invention each guide vane 23 has a mean radial span vane angle (d) determined as a mean value of:
- a pressure side radial span vane angle (a) between the pressure side radial span 26 and a radial line extending from the axial centre axis A through the intersection between the pressure side surface 24 of the guide vane and the imaginary outer surface 22' of the hub, wherein the pressure side radial span vane angle (a) is positive measured from said radial line and in the rotational direction from suction side to pressure side, and - a suction side radial span vane angle (b) between the suction side radial span 27 and a radial line extending from the axial centre axis through the intersection between the suction side surface 25 of the guide vane and the imaginary outer surface 22' of the hub, wherein the suction side radial span vane angle (b) is positive measured from said radial line and in the rotational direction from suction side to pressure side.
Each guide vane 23 has a mean radial span vane angle (d) that is equal to or more than 30 degrees from 0,1 to 0,2 relative axial position of the guide vane. Thus, in the stated range the guide vane has positive lean.
Thus, a positive mean radial span vane angle (d) disclose that the guide vane is tilted in a direction that is opposite the rotational direction of the impeller, i.e. clockwise in figure 4.
The described definition of the mean radial span vane angle is chosen in order to simplify measurement, i.e. in a 3D-model or a real bowl pump it is easy to provide a radial cross section through the bowl pump 1 and measure the defined angles.
According to preferred embodiments the mean radial span vane angle (d) is equal to or more than 30 degrees up to 0,3 relative axial position of the guide vane, preferably up to 0,5 relative axial position and most preferably up to 0,7 relative axial position, in addition to the mentioned range. Thereto, the mean radial span vane angle (d) is preferably equal to or more than 30 degrees from 0,05 relative axial position, in addition to the mentioned range. Thus, the upper and lower limit of the mentioned range may be adjusted independently from each other.
The lower limit of the range may be as low as strictly more than 0.
According to preferred embodiments the mean radial span vane angle (d) is equal to or more than 35 degrees from 0,1 to 0,2 relative axial position, preferably up to 0,3 relative axial position, and most preferably up to 0,5 relative axial position.
According to preferred embodiments the mean radial span vane angle (d) that is equal to or more than 40 degrees from 0,2 to 0,3 relative axial position, preferably up to 0,4 relative axial position.
According to preferred embodiments the mean radial span vane angle (d) is equal to or more than 20 degrees from 0,1 to 1 relative axial position of the guide vane.
According to preferred embodiments the crest of the hub 14 is located upstream 0,3 relative axial position, and located downstream 0,05 relative axial position.
Thus, according to the invention and the preferred embodiments most guiding of the liquid flow inwards towards the hub 14 is performed before and/or at the crest of the hub 14, in order to reduce or entirely eliminate flow separation of the liquid at the outer surface 22 of the hub 14 downstream the crest. Thereto, the main redirection of the liquid flow from rotating to axial flow is performed downstream the crest of the hub 14. Thus, as little redirection as possible from rotating to axial at or about the crest of the hub, while the guide vanes 23 provide a reaction force inward towards the hub 14 at or about the crest. In order to reduce or entirely eliminate flow separation of the liquid at the outer surface 22 of the hub 14 downstream the crest. It shall be pointed out that the term "crest" per definition is the ridge or top or apex of the hub, i.e. the point where the hub is the widest/thickest seen in the radial direction, in conformity with a thread of a screw or the like. Thus, at the crest of the hub the liquid flow is redirected from inclining outwards to inclining inwards in relation to the axial centre axis.
Thanks to the inventive design of the guide vanes 23 the liquid flow profile at the outlet 12 of the pump housing 10 has a greater density at the center, i.e. adjacent the drive shaft sleeve 9, than prior art solutions. Thereby, the next/downstream bowl pump will be fed with a liquid flow having a more uniform flow profile and higher pressure at the center and thereby the next/downstream bowl pump will add more pressure to the liquid than prior art solutions and will thereto be starting at a higher pressure level thanks to the output from the first/upstream bowl pump 1, i.e. entailing a much higher efficiency than prior art bowl pump arrangements.
It shall be pointed out, as already covered by the claims and disclosed in the text and figures, that the pressure side surface 24 and the suction side surface 25 of the guide vane can be parallel, diverging and/or approaching each other seen from the hub outwards. Thereto the shape of these surfaces may be curved or straight or combination thereof. Thus, one and the same guide vane may have different shape along the axial direction. Thus, the pressure side radial span vane angle (a) and the suction side radial span vane angle (b) can be equal to each other of different. Thereto the pressure side radial span and the suction side radial span are defined in a way not to be limited by the shape of the pressure side surface and the suction side surface. Thus the invention is defined in a way to embrace all variants concerning shape and thickness of the guide vanes.
Feasible modifications of the Invention
The invention is not limited only to the embodiments described above and shown in the drawings, which primarily have an illustrative and exemplifying purpose. This patent application is intended to cover all adjustments and variants of the preferred embodiments described herein, thus the present invention is defined by the wording of the appended claims and the equivalents thereof. Thus, the equipment may be modified in all kinds of ways within the scope of the appended claims.
For instance, it shall be pointed out that the present invention also protects a bowl pump having the impeller temporarily disconnected from the hub, or having the impeller not yet installed in the bowl pump.
It shall also be pointed out that all information about/concerning terms such as above, under, upper, lower, etc., shall be interpreted/read having the equipment oriented according to the figures, having the drawings oriented such that the references can be properly read. Thus, such terms only indicate mutual relations in the shown embodiments, which relations may be changed if the inventive equipment is provided with another structure/design. It shall also be pointed out that even thus it is not explicitly stated that features from a specific embodiment may be combined with features from another embodiment, the combination shall be considered obvious, if the combination is possible.
Throughout this specification and the claims which follows, unless the context requires otherwise, the word "comprise", and variations such as "comprises" or "comprising", will be understood to imply the inclusion of a stated integer or steps or group of integers or steps but not the exclusion of any other integer or step or group of integers or steps.

Claims

Claims
1. Vertical turbine pump (1) for pumping liquid, comprising:
- an outer pump housing (10) having an inlet (11), an outlet (12) and an axial centre axis (A) extending from said inlet to said outlet,
- a hub arrangement (13), wherein the hub arrangement comprises:
- a stationary hub (14) located inside the pump housing (10), and
- an impeller (15) that is suspended from the hub (14) and located adjacent said inlet (11) of the pump housing, the pump housing (10) having an inner surface (21) and an imaginary inner surface (2 ) and the hub (14) having an outer surface (22) and an imaginary outer surface (22'), wherein the imaginary inner surface (2 ) of the pump housing is offset radially inwards from said inner surface (21) fifteen percent of the radial distance between the inner surface (21) of the pump housing (10) and outer surface (22) of the hub (14), and wherein the imaginary outer surface (22') of the hub is offset radially outwards from said outer surface (22) fifteen percent of the radial distance between the inner surface of the pump housing and the outer surface of the hub, the vertical turbine pump further comprising:
- a set of guide vanes (23), each guide vane (23) extending in the radial direction between the outer surface of the hub (14) and the inner surface of the pump housing (10), and extending in the axial direction from a start position located adjacent the impeller (15) to an end position located downstream said start position,
- wherein each guide vane (23) has a pressure side surface (24) and a suction side surface (25),
- wherein said start position is defined as the radial plane through the vertical turbine pump that is located closest to the inlet (11) of the pump housing and that intersects the guide vane (23) the full distance from the imaginary inner surface (2 ) of the pump housing (10) to the imaginary outer surface (22') of the hub (14),
- wherein said end position is defined as the radial plane through the vertical turbine pump that is located closest to the outlet (12) of the pump housing and that intersects the guide vane (23) the full distance from the imaginary inner surface (2 ) of the pump housing to the imaginary outer surface (22') of the hub,
- wherein each guide vane (23) has a relative axial position along the axial centre axis (A) starting from zero at the start position and ending at one at the end position,
- wherein each guide vane in each radial plane through the vertical turbine pump between the start position and the end position has a pressure side radial span (26), that extends between the intersection between the pressure side surface (24) of the guide vane and the imaginary outer surface (22') of the hub and the intersection between the pressure side surface (24) of the guide vane and the imaginary inner surface (2 ) of the pump housing, and has a suction side radial span (27), that extends between the intersection between the suction side surface (25) of the guide vane and the imaginary outer surface (22') of the hub and the intersection between the suction side surface (27) of the guide vane and the imaginary inner surface (2 ) of the pump housing, characterized in that each guide vane (23) has a mean radial span vane angle (d) determined as a mean value of:
- a pressure side radial span vane angle (a) between the pressure side radial span (26) and a radial line extending from the axial centre axis (A) through the intersection between the pressure side surface (24) of the guide vane and the imaginary outer surface (22') of the hub, wherein the pressure side radial span vane angle (a) is positive measured from said radial line and in the rotational direction from suction side to pressure side, and
- a suction side radial span vane angle (b) between the suction side radial span (27) and a radial line extending from the axial centre axis through the intersection between the suction side surface (25) of the guide vane and the imaginary outer surface (22') of the hub, wherein the suction side radial span vane angle (b) is positive measured from said radial line and in the rotational direction from suction side to pressure side, wherein each guide vane (23) has a mean radial span vane angle (d) that is equal to or more than 30 degrees from 0,1 to 0,2 relative axial position of the guide vane (23).
2. The vertical turbine pump (1) according to claim 1, wherein each guide vane (23) has a mean radial span vane angle (d) that is equal to or more than 30 degrees from 0,1 up to 0,3 relative axial position of the guide vane, preferably up to 0,5 relative axial position and most preferably up to 0,7 relative axial position.
3. The vertical turbine pump (1) according to claim 1 or 2, wherein each guide vane (23) has a mean radial span vane angle (d) that is equal to or more than 30 degrees from 0,05 up to 0,2 relative axial position, preferably up to 0,3 relative axial position.
4. The vertical turbine pump according to claim 1, wherein each guide vane (23) has a mean radial span vane angle (d) that is equal to or more than 35 degrees from 0,1 to 0,2 relative axial position.
5. The vertical turbine pump according to claim 4, wherein each guide vane (23) has a mean radial span vane angle (d) that is equal to or more than 35 degrees from 0,1 up to 0,3 relative axial position, preferably up to 0,5 relative axial position.
6. The vertical turbine pump according to claim 1, wherein each guide vane (23) has a mean radial span vane angle (d) that is equal to or more than 40 degrees from 0,2 to 0,3 relative axial position.
7. The vertical turbine pump according to claim 6, wherein each guide vane (23) has a mean radial span vane angle (d) that is equal to or more than 40 degrees from 0,2 up to 0,4 relative axial position.
8. The vertical turbine pump according to any preceding claim, wherein the crest of the hub (14) is located upstream 0,3 relative axial position.
9. The vertical turbine pump according to any preceding claim, wherein the crest of the hub (14) is located downstream 0,05 relative axial position.
10. The vertical turbine pump according to any preceding claim, wherein each guide vane (23) has a mean radial span vane angle (d) that is equal to or more than 20 degrees from 0,1 to 1 relative axial position of the guide vane.
11. A vertical turbine pump arrangement (2) for pumping liquid, comprising:
- a drive unit (3) having a motor (4) and a drive shaft (5),
- a column (6),
- a discharge connection (7) connected to an upper end of said column (6), and
- at least one vertical turbine pump (1) connected to a lower end of said column (6), characterized in that said at least one vertical turbine pump (1) is constituted by a vertical turbine pump (1) according to any of claims 1-10, wherein the impeller (15) of the vertical turbine pump (1) is connected to the drive shaft (5) extending from said motor (4).
PCT/EP2021/061044 2020-04-28 2021-04-28 Vertical turbine pump and vertical turbine pump arrangement WO2021219678A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202180031607.4A CN115461543A (en) 2020-04-28 2021-04-28 Vertical turbine pump and vertical turbine pump device

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP20171820.2 2020-04-28
EP20171820.2A EP3904695A1 (en) 2020-04-28 2020-04-28 Bowl pump and vertical bowl pump arrangement

Publications (1)

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WO2021219678A1 true WO2021219678A1 (en) 2021-11-04

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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1976200A (en) * 1931-04-14 1934-10-09 A D Cook Inc Deep-well turbine pump
GB581444A (en) * 1944-05-17 1946-10-14 James Herbert Wainwright Gill Improvements in or relating to pumps, fans and like machines for transmitting energy to fluids
US3776664A (en) * 1972-08-18 1973-12-04 A Kimmel Small diameter irrigation pump
US20090155064A1 (en) * 2007-12-13 2009-06-18 Baker Hughes Incorporated System, method and apparatus for two-phase homogenizing stage for centrifugal pump assembly
US20140178190A1 (en) * 2012-12-20 2014-06-26 Ge Oil & Gas Esp, Inc. Multiphase pumping system
US20170122333A1 (en) * 2015-10-30 2017-05-04 General Electric Company Oil and gas well pump components and method of coating such components

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1976200A (en) * 1931-04-14 1934-10-09 A D Cook Inc Deep-well turbine pump
GB581444A (en) * 1944-05-17 1946-10-14 James Herbert Wainwright Gill Improvements in or relating to pumps, fans and like machines for transmitting energy to fluids
US3776664A (en) * 1972-08-18 1973-12-04 A Kimmel Small diameter irrigation pump
US20090155064A1 (en) * 2007-12-13 2009-06-18 Baker Hughes Incorporated System, method and apparatus for two-phase homogenizing stage for centrifugal pump assembly
US20140178190A1 (en) * 2012-12-20 2014-06-26 Ge Oil & Gas Esp, Inc. Multiphase pumping system
US20170122333A1 (en) * 2015-10-30 2017-05-04 General Electric Company Oil and gas well pump components and method of coating such components

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