WO2014153616A1 - Slurry pump impeller - Google Patents

Slurry pump impeller Download PDF

Info

Publication number
WO2014153616A1
WO2014153616A1 PCT/AU2014/000337 AU2014000337W WO2014153616A1 WO 2014153616 A1 WO2014153616 A1 WO 2014153616A1 AU 2014000337 W AU2014000337 W AU 2014000337W WO 2014153616 A1 WO2014153616 A1 WO 2014153616A1
Authority
WO
WIPO (PCT)
Prior art keywords
edge
face
pumping
pump impeller
back shroud
Prior art date
Application number
PCT/AU2014/000337
Other languages
French (fr)
Inventor
Craig Ian Walker
Original Assignee
Weir Minerals Australia Ltd
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
Priority claimed from AU2013901086A external-priority patent/AU2013901086A0/en
Priority to US14/780,700 priority Critical patent/US20160040682A1/en
Priority to EP14774127.6A priority patent/EP2978975B1/en
Priority to BR112015024718A priority patent/BR112015024718A2/en
Priority to ES14774127T priority patent/ES2709199T3/en
Priority to CN201480017925.5A priority patent/CN105074225B/en
Application filed by Weir Minerals Australia Ltd filed Critical Weir Minerals Australia Ltd
Priority to AP2015008763A priority patent/AP2015008763A0/en
Priority to CA2902759A priority patent/CA2902759A1/en
Priority to PL14774127T priority patent/PL2978975T3/en
Priority to MX2015013549A priority patent/MX365143B/en
Priority to EA201591520A priority patent/EA031306B1/en
Priority to AU2014245856A priority patent/AU2014245856B2/en
Publication of WO2014153616A1 publication Critical patent/WO2014153616A1/en
Priority to PH12015501912A priority patent/PH12015501912A1/en

Links

Classifications

    • 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
    • F04D29/18Rotors
    • F04D29/22Rotors specially for centrifugal pumps
    • F04D29/2261Rotors specially for centrifugal pumps with special measures
    • F04D29/2294Rotors specially for centrifugal pumps with special measures for protection, e.g. against abrasion
    • 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
    • F04D29/18Rotors
    • F04D29/22Rotors specially for centrifugal pumps
    • F04D29/24Vanes
    • 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
    • F04D29/18Rotors
    • F04D29/22Rotors specially for centrifugal pumps
    • F04D29/24Vanes
    • F04D29/242Geometry, shape
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D7/00Pumps adapted for handling specific fluids, e.g. by selection of specific materials for pumps or pump parts
    • F04D7/02Pumps adapted for handling specific fluids, e.g. by selection of specific materials for pumps or pump parts of centrifugal type
    • F04D7/04Pumps adapted for handling specific fluids, e.g. by selection of specific materials for pumps or pump parts of centrifugal type the fluids being viscous or non-homogenous

Definitions

  • This disclosure relates generally to impellers for centrifugal slurry pumps.
  • Slurries are usually a mixture of liquid and particulate solids, and are commonly found in the minerals processing, sand and gravel and/or dredging industry.
  • Centrifugal slurry pumps generally include a pump casing having a pumping chamber therein which may be of a volute configuration with an impeller mounted for rotation within the pumping chamber.
  • a drive shaft is operatively connected to the pump impeller for causing rotation thereof, the drive shaft entering the pump casing from one side.
  • the pump further includes a pump inlet which is typically coaxial with respect to the drive shaft and located on the opposite side of the pump casing to the drive shaft. There is also a discharge outlet typically located at a periphery of the pump casing.
  • the pump casing may be in the form of a liner which is encased within an outer pump housing.
  • the impeller typically includes a hub to which the drive shaft is operatively connected, and at least one shroud. Pumping vanes are provided on one side of the shroud with discharge passageways between adjacent pumping vanes.
  • the impeller may be of the closed type where two shrouds are provided with the pumping vanes being disposed therebetween.
  • the impeller may however be of the "open" face type which comprises one shroud only.
  • slurry pumps handling heterogeneous slurries (with settling particles of typical size 0.5mm) it is common for there to be solids concentration gradients throughout the flows in the inlet pipe and within the impeller and pump casing.
  • concentration gradients are caused by the various forces acting on the particle including: gravity, fluid drag and centrifugal forces.
  • the slurr enters the impeller it has to turn through a 90 degree angle of flow so as to be directed out of the pump, and with both inertial forces and Coriolis forces (exerted by the vane), the slurry particles are at their highest concentration at the root of the vane on the back shroud of the impeller, that is, in the region where a side edge of the vane contacts the shroud.
  • a pump impeller which includes:
  • each pumping vane including:
  • first side face at the leading edge is in a plane which is at an acute angle with respect to a plane of the inner main face of the back shroud
  • first side face at the trailing edge is in a plane which is at an obtuse angle with respect to the plane of the inner main face of the back shroud
  • the configuration of the vane is such that in use the Coriolis force generated by the vane disperses particles across that vane at its trailing edge thereby reducing wear near the region where the vane abuts against the face of the back shroud.
  • the first side face at the trailing edge is in a plane which is at an obtuse angle in a range of greater than about 90° to about 135".
  • the impeller further includes a front shroud having an inner main face the pumping vanes extending between the inner main faces of the front and back shrouds, although in some embodiments the impeller may not have a front shroud at all (in "open" face type impellers).
  • the inner main face of the back shroud is at right angles to the central axis, although in other embodiments there can be some alignment of these at other than right angles.
  • the angle of the first side face progressively changes when moving from the leading edge to the trailing edge of the vane. This may be in a continuous form of curvature when moving from the leading edge to the trailing edge, or in multiple straight sectors at different acute or obtuse angles to form the shape of the pumping vane.
  • the first side face is a leading face with respect to the direction of rotation, so that fluid being pumped is impacted against it.
  • each pumping vane includes a leading edge section terminating at the leading edge the leading edge section tapering inwardly towards the leading edge, and a trailing edge section terminating at the trailing edge the trailing edge section tapering inwardly towards the trailing edge, each pumping vane including a main section between the leading and trailing edge sections which has a width or thickness which is generally constant from one side edge thereof to an opposed side edge and along its length from the leading edge section to the trailing edge section.
  • the first side face is a pumping or pressure side face.
  • the first side face is configured such that the surface thereof, at any line between the leading and trailing edges which is at 90° from one side edge to the other, is flat or linear in the direction of that line.
  • the pumping vanes are curved in a lengthwise direction between the leading and trailing edges although in some other embodiments the impeller pumping vanes can be straight along their distal length.
  • the vanes are backwardly curved with respect to the direction of rotation of the impeller, although for some applications the direction of curv ature may be forwardly curved with respect to the direction of rotation of the impeller, depending on the nature of fluid.
  • a pump impeller which includes: - a back shroud having an inner main face with an outer peripheral edge and a central axis, the impeller in use being rotatable about the central axis in a direction of rotation,
  • each pumping vane including:
  • a line extending from one side edge to the other side edge of the pumping vane at the leading edge is at an acute angle with respect to a plane of the inner main face of the back shroud
  • a line extending from one side edge to the other side edge of the pumping vane at the trailing edge is at an obtuse angle with respect to the plane of the inner main face of the back shroud
  • Figure 1 illustrates an exemplary, schematic, partial cross-sectional side elevation of a pump incorporating an impeller and an impeller and liner combination, in accordance with one embodiment
  • Figure 2 illustrates an exemplary, schematic view of part of an impeller and a pumping vane in accordance with one embodiment
  • Figures 3 to 5 illustrate exemplary sectional views of an impeller shroud and an impeller pumping vane taken along the lines 1 , 2 and 3 in Figure 2;
  • Figures 6 and 7 are pictorial views of a portion of an impeller illustrating features of the pumping vanes according to one embodiment.
  • Figure 8 is a top, perspective view of an impeller illustrating features of the pumping vanes according to one embodiment.
  • Figure 9 is a bottom, perspective view of an impeller illustrating features of the pumping vanes according to one embodiment.
  • Figure 10 illustrates an exemplary schematic view of part of an impeller and a pumping vane in accordance with another embodiment.
  • FIG. 1 there is illustrated a typical example of a pump 10 which includes a pump casing or volute 12, a back liner 14, a front liner 30 and a pump outlet 18.
  • An internal chamber 20 is adapted to receive an impeller 40 for rotation about rotational axis X-X.
  • the front liner 30 includes a cylindrically-shaped delivery section 32 through which slurry enters the pump chamber 20.
  • the delivery section 32 has a passage 33 therein with a first, outermost end 34 operatively connectable to a feed pipe (not shown) and a second, innermost end 35 adjacent the chamber 20.
  • the front liner 30 further includes a side wall section 15 which mates in use with the pump casing 12 to form and enclose the chamber 20, the side wall section 15 having an inner face 37.
  • the second end 35 of the front liner 30 has a raised lip 38 thereat, which is arranged in a close facing relationship with the impeller 40.
  • the impeller 40 includes a hub 41 from which a plurality of circumferentially spaced pumping vanes 42 extend. An eye portion 47 extends forwardly from the hub towards the passage 33 in the front liner.
  • the impeller further includes a front shroud 50 and a back shroud 51, the vanes 42 being disposed therebetween.
  • the pumping vanes include a leading edge section 60 having a leading edge 43 and a trailing edge section 61 having a trailing edge 44.
  • the leading edge section 60 is tapered inwardly towards the leading edge 43 and the trailing edge section 61 is tapered inwardly towards the trailing edge 44.
  • the pumping vanes have a main section 63 between the leading edge section 60 and trailing edge section 61 which at any planar height above the back shroud 51 has a width or thickness 64 which is generally constant from one side edge 56 to the other side edge 57 and along its length from the leading edge section 60 to the trailing edge section 61.
  • FIG. 2 only one exemplary pumping vane 42 is shown which extends between opposing main inner faces 53, 54 of the shrouds 50, 51. Normally such an impeller has a plurality of such pumping vanes spaced evenly around the area between the shrouds 50, 51. Typically three, four or five pumping vanes are usual in slurry pumps. In this drawing only one pumping vane has been shown for convenience to illustrate the features.
  • the pumping vane 42 is generally arcuate in cross-section and includes an inner leading edge 43 and an outer trailing edge 44, opposed side edges 56, 57 and opposed first and second faces 45, 46 between the side edges 56, 57, the face 45 being a pumping or pressure side face.
  • the vanes of this type are normally referred to as backward-curving vanes when viewed with the direction of rotation.
  • the side edge 56, 57 are disposed against respective inner faces of the shrouds 50, 51.
  • the inner faces 53, 54 are generally at right angles to the central rotation axis X-X.
  • the face 45 which is a pumping or pressure side face of the pumping vane 42 is configured such that the surface thereof at any line between the leading and trailing edges 43, 44 which is at 90° from one side edge 56 to the other 57 is flat or linear in the direction of that line.
  • the face 45 may be likened to a face of a rectangular flat strip with the leading edge 43 and the trailing edge 44 forming the two shorter sides of the rectangular flat strip and the side edges 56, 57 each forming the two respective longer sides of the rectangular flat strip.
  • the rectangular flat strip is twisted about an axis that extends from the leading edge 43 to the trailing edge 44.
  • the rectangular flat strip is also curved between the leading edge 43 and the trailing edge 44 which provides that face 45 is backward-curved.
  • a face (that is face 45) of the rectangular flat strip that is twisted and curved in this way, is linear or flat in the direction of a line which is drawn from one longer side (that is side edge 56) to the other longer side (that is side edge 57) at any point between the two shorter sides (that is the leading edge 43 and the trailing edge 44) of the rectangular flat strip when the line meets each of the longer sides at an angle of 90°.
  • the first face 45 is flat or linear when viewed at any cross-section along its length from the leading edge 43 to the trailing edge 44, each cross- section being taken at rights angles to the side edges 56, 57 of the vane. Examples of such cross-sections are illustrated in Figures 3 to 5 showing cross-sections taken along the lines 1 , 2, and 3 in Figure 2. As is apparent from viewing these Figures, the first face 45 is flat or linear at these cross sections. Described in another way, it means that the first face 45 is not bowed or convex at any of the cross-sectional views in question. In the embodiment described, the second face 46 is also flat or linear when viewed at any cross section.
  • the angle of inclination Y of the side face 45 with respect to the main inner face 53 of the back shroud 51 progressively changes along the length of the vane 42 when moving from its leading edge 43 to its trailing edge 44. This change in angle is clearly shown in Figures 3 to 5.
  • the angle of inclination Y is also referred to as the leading angle of the vane with respect to the direction of rotation of the impeller in use.
  • the angle of inclination Y is an acute angle at the leading edge 43.
  • the angle is in a range from about 45° to less than 90°, more preferably the angle is in a range from about 70° to about 80°, and more preferably is about 75°.
  • the angle progressively changes and, at the position shown in Figure 4, it is at right angles (perpendicular).
  • the angle of inclination is obtuse.
  • the angle at the trailing edge is in a range from greater than 90° up to about 135°, more preferably the angle is in a range from about 100° to about 130°, and more preferably is about 1 10°.
  • the Coriolis force (Arrow B in Figure 2), which is generated as a result of the in use rotation of the impeller in the direction of arrow A in Figure 2, causes the particulates C in a slurry or fluid which is being conveyed by the pump impeller of the present embodiment, to disperse over the face of the vane as the particulates travel along the vane from the leading edge to the trailing edge.
  • the vane shape arrangement can assist to break up solid particle concentration gradients within the impeller where the slurry particles are at their highest concentration at the root of the vane on the back shroud of the impeller, that is, in the region where a side edge of the vane contacts the shroud. This can result in a reduction of the wear due to grooving of the impeller at that point.
  • Figures 6, 7, 8 and 9 illustrate an impeller according to one embodiment.
  • the same reference numerals as used to identify parts in Figures 1 , 2, 3, 4 and 5 are used to identify similar parts in the embodiment of Figures 6, 7, 8 and 9.
  • Figures 6 and 7 depict portions of an impeller 40 from different sides looking into the discharge passageways between the vanes 42, and Figures 8 and 9 each show an impeller 40 in its entirety.
  • the angle of inclination of the side face 45 with respect to the main inner face 53 of the back shroud 51 progressively changes along the length of the vanes 42 when moving from the leading edge (now shown) to its trailing edge 44.
  • Figure 10 illustrates a modified form of the arrangement shown in Figure 2.

Abstract

A pump impeller which includes: a back shroud having an inner main face with an outer peripheral edge and a central axis, the impeller in use being rotatable about the central axis in a direction of rotation, a plurality of pumping vanes extending from the inner main face of the back shroud, the pumping vanes being disposed in spaced apart relation, and each pumping vane including: opposed first and second side faces, a leading edge in the region of the central axis and a trailing edge in the region of the outer peripheral edge of the back shroud, and with a passageway between adjacent pumping vanes, wherein the first side face at the leading edge is in a plane which is at an acute angle with respect to a plane of the inner main face of the back shroud, and the first side face at the trailing edge is in a plane which is at an obtuse angle with respect to the plane of the inner main face of the back shroud.

Description

SLURRY PUMP IMPELLER Technical Field
[0001] This disclosure relates generally to impellers for centrifugal slurry pumps. Slurries are usually a mixture of liquid and particulate solids, and are commonly found in the minerals processing, sand and gravel and/or dredging industry.
Background Art
[0002] Centrifugal slurry pumps generally include a pump casing having a pumping chamber therein which may be of a volute configuration with an impeller mounted for rotation within the pumping chamber. A drive shaft is operatively connected to the pump impeller for causing rotation thereof, the drive shaft entering the pump casing from one side. The pump further includes a pump inlet which is typically coaxial with respect to the drive shaft and located on the opposite side of the pump casing to the drive shaft. There is also a discharge outlet typically located at a periphery of the pump casing. The pump casing may be in the form of a liner which is encased within an outer pump housing.
[0003] The impeller typically includes a hub to which the drive shaft is operatively connected, and at least one shroud. Pumping vanes are provided on one side of the shroud with discharge passageways between adjacent pumping vanes. The impeller may be of the closed type where two shrouds are provided with the pumping vanes being disposed therebetween. The impeller may however be of the "open" face type which comprises one shroud only.
[00041 In some applications conventional pumping vanes are laid over such that a section through the vane forms an acute angle to the shroud on a pressure surface of the vane and provides for a smooth transition from inlet to discharge along the vane length. [0005] Two examples of impellers having warped vanes are illustrated in US 2010/0284812 and US 6,082,000. US 2010/0284812 discloses a centrifugal water pump having an impeller which has aerofoil shaped vanes with a thick base (portion in contact with back shroud) tapering to a thin tip (portion closest to the fluid inlet). Although the vanes are twisted along their length, they would not be suitable for use in slurry pumps. In US 6,082,000, the vanes of D2 are typical of the mixed flow type, that is the vanes are of a double curvature type. The patent is concerned with a novel method to produce such a vane.
10006] For slurry pumps handling heterogeneous slurries (with settling particles of typical size 0.5mm) it is common for there to be solids concentration gradients throughout the flows in the inlet pipe and within the impeller and pump casing. The concentration gradients are caused by the various forces acting on the particle including: gravity, fluid drag and centrifugal forces. As the slurr enters the impeller it has to turn through a 90 degree angle of flow so as to be directed out of the pump, and with both inertial forces and Coriolis forces (exerted by the vane), the slurry particles are at their highest concentration at the root of the vane on the back shroud of the impeller, that is, in the region where a side edge of the vane contacts the shroud.
[0007] A consequence of this flow of concentrated particles along the root of the vane is high and uneven wear due to grooving of the impeller at that point, which can prematurely render the impeller ineffective.
Summary of the Disclosure
[0008] In a first aspect, embodiments are disclosed of a pump impeller which includes:
- a back shroud having an inner main face with an outer peripheral edge and a central axis, the impeller in use being rotatable about the central axis in a direction of rotation, - a plurality of pumping vanes extending from the inner main face of the back shroud, the pumping vanes being disposed in spaced apart relation, and each pumping vane including:
-opposed first and second side faces,
- a leading edge in the region of the central axis and
- a trailing edge in the region of the outer peripheral edge of the back shroud, and
- with a passageway between adjacent pumping vanes,
wherein the first side face at the leading edge is in a plane which is at an acute angle with respect to a plane of the inner main face of the back shroud, and the first side face at the trailing edge is in a plane which is at an obtuse angle with respect to the plane of the inner main face of the back shroud.
|0009] The configuration of the vane is such that in use the Coriolis force generated by the vane disperses particles across that vane at its trailing edge thereby reducing wear near the region where the vane abuts against the face of the back shroud.
[0010] In certain embodiments, the first side face at the trailing edge is in a plane which is at an obtuse angle in a range of greater than about 90° to about 135".
[0011] In certain embodiments, the impeller further includes a front shroud having an inner main face the pumping vanes extending between the inner main faces of the front and back shrouds, although in some embodiments the impeller may not have a front shroud at all (in "open" face type impellers).
[0012] In certain embodiments the inner main face of the back shroud is at right angles to the central axis, although in other embodiments there can be some alignment of these at other than right angles.
[0013] In certain embodiments, the angle of the first side face progressively changes when moving from the leading edge to the trailing edge of the vane. This may be in a continuous form of curvature when moving from the leading edge to the trailing edge, or in multiple straight sectors at different acute or obtuse angles to form the shape of the pumping vane.
[0014] In certain embodiments, the first side face is a leading face with respect to the direction of rotation, so that fluid being pumped is impacted against it.
[0015] In certain embodiments each pumping vane includes a leading edge section terminating at the leading edge the leading edge section tapering inwardly towards the leading edge, and a trailing edge section terminating at the trailing edge the trailing edge section tapering inwardly towards the trailing edge, each pumping vane including a main section between the leading and trailing edge sections which has a width or thickness which is generally constant from one side edge thereof to an opposed side edge and along its length from the leading edge section to the trailing edge section.
[0016] In certain embodiments the first side face is a pumping or pressure side face.
[0017[ In certain embodiments, the first side face is configured such that the surface thereof, at any line between the leading and trailing edges which is at 90° from one side edge to the other, is flat or linear in the direction of that line.
[0018] In certain embodiments the pumping vanes are curved in a lengthwise direction between the leading and trailing edges although in some other embodiments the impeller pumping vanes can be straight along their distal length.
[0019] In certain embodiments, the vanes are backwardly curved with respect to the direction of rotation of the impeller, although for some applications the direction of curv ature may be forwardly curved with respect to the direction of rotation of the impeller, depending on the nature of fluid.
[0020] In another aspect, embodiments are disclosed of a pump impeller which includes: - a back shroud having an inner main face with an outer peripheral edge and a central axis, the impeller in use being rotatable about the central axis in a direction of rotation,
- a plurality of pumping vanes extending from the inner main face of the back shroud, the pumping vanes being disposed in spaced apart relation, and each pumping vane including:
- opposed first and second side faces,
- opposed side edges one of which is located at the back shroud,
- a leading edge in the region of the central axis and
- a trailing edge in the region of the outer peripheral edge of the back shroud, and
- with a passageway between adjacent pumping vanes,
wherein a line extending from one side edge to the other side edge of the pumping vane at the leading edge is at an acute angle with respect to a plane of the inner main face of the back shroud, and a line extending from one side edge to the other side edge of the pumping vane at the trailing edge is at an obtuse angle with respect to the plane of the inner main face of the back shroud.
[0021] Other aspects, features, and advantages will become apparent from the following detailed description when taken in conjunction with the accompanying drawings, which are a part of this disclosure and which illustrate, by way of example, principles of inventions disclosed.
Brief Description of the Drawings
[0022| Notwithstanding any other forms which may fall within the scope of the method and apparatus as set forth in the Summary, specific embodiments of the method and apparatus will now be described, by way of example, and with reference to the accompanying drawings in which:
[0023] Figure 1 illustrates an exemplary, schematic, partial cross-sectional side elevation of a pump incorporating an impeller and an impeller and liner combination, in accordance with one embodiment;
[0024] Figure 2 illustrates an exemplary, schematic view of part of an impeller and a pumping vane in accordance with one embodiment;
[0025] Figures 3 to 5 illustrate exemplary sectional views of an impeller shroud and an impeller pumping vane taken along the lines 1 , 2 and 3 in Figure 2; and
|0026] Figures 6 and 7 are pictorial views of a portion of an impeller illustrating features of the pumping vanes according to one embodiment.
[0027] Figure 8 is a top, perspective view of an impeller illustrating features of the pumping vanes according to one embodiment.
[0028] Figure 9 is a bottom, perspective view of an impeller illustrating features of the pumping vanes according to one embodiment.
[0029] Figure 10 illustrates an exemplary schematic view of part of an impeller and a pumping vane in accordance with another embodiment.
Detailed Description of Specific Embodiments
[0030] Referring to Figure 1 , there is illustrated a typical example of a pump 10 which includes a pump casing or volute 12, a back liner 14, a front liner 30 and a pump outlet 18. An internal chamber 20 is adapted to receive an impeller 40 for rotation about rotational axis X-X.
[0031] The front liner 30 includes a cylindrically-shaped delivery section 32 through which slurry enters the pump chamber 20. The delivery section 32 has a passage 33 therein with a first, outermost end 34 operatively connectable to a feed pipe (not shown) and a second, innermost end 35 adjacent the chamber 20. The front liner 30 further includes a side wall section 15 which mates in use with the pump casing 12 to form and enclose the chamber 20, the side wall section 15 having an inner face 37. The second end 35 of the front liner 30 has a raised lip 38 thereat, which is arranged in a close facing relationship with the impeller 40.
[0032] The impeller 40 includes a hub 41 from which a plurality of circumferentially spaced pumping vanes 42 extend. An eye portion 47 extends forwardly from the hub towards the passage 33 in the front liner. The impeller further includes a front shroud 50 and a back shroud 51, the vanes 42 being disposed therebetween.
[0033] Referring now to Figure 2, this illustrates an impeller according to one embodiment. The same reference numerals as used to identify parts in Figure 1 are used to identify similar parts in the embodiment of Figure 2. The pumping vanes include a leading edge section 60 having a leading edge 43 and a trailing edge section 61 having a trailing edge 44. The leading edge section 60 is tapered inwardly towards the leading edge 43 and the trailing edge section 61 is tapered inwardly towards the trailing edge 44. The pumping vanes have a main section 63 between the leading edge section 60 and trailing edge section 61 which at any planar height above the back shroud 51 has a width or thickness 64 which is generally constant from one side edge 56 to the other side edge 57 and along its length from the leading edge section 60 to the trailing edge section 61.
|0034] In Figure 2 only one exemplary pumping vane 42 is shown which extends between opposing main inner faces 53, 54 of the shrouds 50, 51. Normally such an impeller has a plurality of such pumping vanes spaced evenly around the area between the shrouds 50, 51. Typically three, four or five pumping vanes are usual in slurry pumps. In this drawing only one pumping vane has been shown for convenience to illustrate the features. As shown in Figure 2, the pumping vane 42 is generally arcuate in cross-section and includes an inner leading edge 43 and an outer trailing edge 44, opposed side edges 56, 57 and opposed first and second faces 45, 46 between the side edges 56, 57, the face 45 being a pumping or pressure side face. The vanes of this type are normally referred to as backward-curving vanes when viewed with the direction of rotation. The side edge 56, 57 are disposed against respective inner faces of the shrouds 50, 51. The inner faces 53, 54 are generally at right angles to the central rotation axis X-X. The face 45 which is a pumping or pressure side face of the pumping vane 42 is configured such that the surface thereof at any line between the leading and trailing edges 43, 44 which is at 90° from one side edge 56 to the other 57 is flat or linear in the direction of that line.
[0035] Described in another way, the face 45 may be likened to a face of a rectangular flat strip with the leading edge 43 and the trailing edge 44 forming the two shorter sides of the rectangular flat strip and the side edges 56, 57 each forming the two respective longer sides of the rectangular flat strip. The rectangular flat strip is twisted about an axis that extends from the leading edge 43 to the trailing edge 44. In addition to being twisted, the rectangular flat strip is also curved between the leading edge 43 and the trailing edge 44 which provides that face 45 is backward-curved. A face (that is face 45) of the rectangular flat strip that is twisted and curved in this way, is linear or flat in the direction of a line which is drawn from one longer side (that is side edge 56) to the other longer side (that is side edge 57) at any point between the two shorter sides (that is the leading edge 43 and the trailing edge 44) of the rectangular flat strip when the line meets each of the longer sides at an angle of 90°.
[0036] In certain embodiments, the first face 45 is flat or linear when viewed at any cross-section along its length from the leading edge 43 to the trailing edge 44, each cross- section being taken at rights angles to the side edges 56, 57 of the vane. Examples of such cross-sections are illustrated in Figures 3 to 5 showing cross-sections taken along the lines 1 , 2, and 3 in Figure 2. As is apparent from viewing these Figures, the first face 45 is flat or linear at these cross sections. Described in another way, it means that the first face 45 is not bowed or convex at any of the cross-sectional views in question. In the embodiment described, the second face 46 is also flat or linear when viewed at any cross section.
[0037] As illustrated, the angle of inclination Y of the side face 45 with respect to the main inner face 53 of the back shroud 51 progressively changes along the length of the vane 42 when moving from its leading edge 43 to its trailing edge 44. This change in angle is clearly shown in Figures 3 to 5. The angle of inclination Y is also referred to as the leading angle of the vane with respect to the direction of rotation of the impeller in use. As shown in Figure 3 the angle of inclination Y is an acute angle at the leading edge 43. Preferably the angle is in a range from about 45° to less than 90°, more preferably the angle is in a range from about 70° to about 80°, and more preferably is about 75°. The angle progressively changes and, at the position shown in Figure 4, it is at right angles (perpendicular). In the position shown in Figure 5 at the trailing edge 44 of the vane, the angle of inclination is obtuse. Preferably the angle at the trailing edge is in a range from greater than 90° up to about 135°, more preferably the angle is in a range from about 100° to about 130°, and more preferably is about 1 10°.
[0038] In operation, the Coriolis force (Arrow B in Figure 2), which is generated as a result of the in use rotation of the impeller in the direction of arrow A in Figure 2, causes the particulates C in a slurry or fluid which is being conveyed by the pump impeller of the present embodiment, to disperse over the face of the vane as the particulates travel along the vane from the leading edge to the trailing edge. The vane shape arrangement can assist to break up solid particle concentration gradients within the impeller where the slurry particles are at their highest concentration at the root of the vane on the back shroud of the impeller, that is, in the region where a side edge of the vane contacts the shroud. This can result in a reduction of the wear due to grooving of the impeller at that point.
[0039] Figures 6, 7, 8 and 9 illustrate an impeller according to one embodiment. The same reference numerals as used to identify parts in Figures 1 , 2, 3, 4 and 5 are used to identify similar parts in the embodiment of Figures 6, 7, 8 and 9. Figures 6 and 7 depict portions of an impeller 40 from different sides looking into the discharge passageways between the vanes 42, and Figures 8 and 9 each show an impeller 40 in its entirety. As can be seen, the angle of inclination of the side face 45 with respect to the main inner face 53 of the back shroud 51 progressively changes along the length of the vanes 42 when moving from the leading edge (now shown) to its trailing edge 44. [0040] Figure 10 illustrates a modified form of the arrangement shown in Figure 2. The same reference numerals as used to identify parts in Figure 2 are used to identify similar parts in the modified form of Figure 10. The change in the angle of inclination Y along the length of the vane 42 as shown in Figure 10 is greater than the change in the angle of inclination Y along the length of the vane 42 as shown in Figure 2.
[0041] In the foregoing description of preferred embodiments, specific terminology has been resorted to for the sake of clarity. However, the invention is not intended to be limited to the specific terms so selected, and it is to be understood that each specific term includes all technical equivalents which operate in a similar manner to accomplish a similar technical purpose. Terms such as "front" and "rear", "inner" and "outer", "above", "below", "upper" and "lower" and the like are used as words of convenience to provide reference points and are not to be construed as limiting terms.
[0042] The reference in this specification to any prior publication (or information derived from it), or to any matter which is known, is not, and should not be taken as, an acknowledgement or admission or any form of suggestion that prior publication (or information derived from it) or known matter forms part of the common general knowledge in the field of endeavour to which this specification relates.
[00431 In this specification, the word "comprising" is to be understood in its "open" sense, that is, in the sense of "including", and thus not limited to its "closed" sense, that is the sense of "consisting only of. A corresponding meaning is to be attributed to the corresponding words "comprise", "comprised" and "comprises" where they appear.
[0044] In addition, the foregoing describes only some embodiments of the invention(s), and alterations, modifications, additions and/or changes can be made thereto without departing from the scope and spirit of the disclosed embodiments, the embodiments being illustrative and not restrictive.
[0045] Furthermore, invention(s) have been described in connection with what are presently considered to be the most practical and preferred embodiments, it is to be understood that the invention is not to be limited to the disclosed embodiments, but on the contrary, is intended to cover various modifications and equivalent arrangements included within the spirit and scope of the invention(s). Also, the various embodiments described above may be implemented in conjunction with other embodiments, e.g., aspects of one embodiment may be combined with aspects of another embodiment to realize yet other embodiments. Further, each independent feature or component of any given assembly may constitute an additional embodiment.
Table of Parts
Pump 10
Pump casing (volute) 12
Back liner 14
Front liner 30
Pump outlet 18
Internal chamber 20
Central or rotational axis X-X
Delivery section 32
Passage 33
Outer end 34
Inner end 35
Sidewall section 15
Inner face 37
Lip 38
Impeller 40
Hub 41
Pumping vanes 42
Eye portion 47
Leading edge section 60
Leading edge 43
Impeller inlet 48
Trailing edge section 61
Trailing edge 44
Main section 63
Width or thickness 64
Outlet 49
Front shroud 50
Back shroud 51
First face 45 Second face 46 Side edge 56 Side edge 57

Claims

CLAIMS:
1 A pump impeller which includes:
- a back shroud having an inner main face with an outer peripheral edge and a central axis, the impeller in use being rotatable about the central axis in a direction of rotation,
- a plurality of pumping vanes extending from the inner main face of the back shroud, the pumping vanes being disposed in spaced apart relation, and each pumping vane including:
- opposed first and second side faces,
- a leading edge in the region of the central axis and
- a trailing edge in the region of the outer peripheral edge of the back shroud, and
- with a passageway between adjacent pumping vanes,
wherein the first side face at the leading edge is in a plane which is at an acute angle with respect to a plane of the inner main face of the back shroud, and the first side face at the trailing edge is in a plane which is at an obtuse angle with respect to the plane of the inner main face of the back shroud.
2. A pump impeller according to claim 1. wherein the first side face at the leading edge is in a plane which is at an acute angle in a range of about 45° to less than about 90°.
3. A pump impeller according to claim 1 or claim 2 wherein the first side face at the trailing edge is in a plane which is at an obtuse angle in a range of greater than about 90° to about 135°.
4. A pump impeller according to any one of the preceding claims, wherein each pumping vane includes a leading edge section terminating at the leading edge, the leading edge section tapering inwardly towards the leading edge, and a trailing edge section terminating at the trailing edge, the trailing edge section tapering inwardly towards the trailing edge, each pumping vane including a main section between the leading and trailing edge sections which has a width or thickness which is generally constant from one side edge thereof to an opposed side edge thereof and along its length from the leading edge section to the trailing edge section.
5. A pump impeller according to any one of the preceding claims, further including a front shroud having an inner main face the pumping vanes extending between the inner main faces of the front and back shrouds.
6. A pump impeller according to any one of the preceding claims, wherein the angle of the first side face progressively changes when moving from the leading edge to the trailing edge.
7. A pump impeller according to any one of the preceding claims, wherein the first side face is a leading face with respect to the direction of rotation.
8. A pump impeller according to any one of the preceding claims, wherein the first side face is a pumping or pressure side face.
9. A pump impeller according to any one of the preceding claims, wherein the first side face is configured such that the surface thereof, at any line between the leading and trailing edges which is at 90° from one side edge to the other, is flat or linear in the direction of that line.
10. A pump impeller according to any one of the preceding claims, wherein the pumping vanes are curved in a lengthwise direction between the leading and trailing edges.
1 1. A pump impeller according to claim 10 wherein the vanes are backwardly curved with respect to the direction of rotation of the impeller.
12. A pump impeller which includes: - a back shroud having an inner main face with an outer peripheral edge and a central axis, the impeller in use being rotatable about the central axis in a direction of rotation,
- a plurality of pumping vanes extending from the inner main face of the back shroud, the pumping vanes being disposed in spaced apart relation, and each pumping vane including:
- opposed first and second side faces,
- opposed side edges one of which is located at the back shroud,
- a leading edge in the region of the central axis and
- a trailing edge in the region of the outer peripheral edge of the back shroud, and
- with a passageway between adjacent pumping vanes,
wherein a line extending from one side edge to the other side edge of the pumping vane at the leading edge is at an acute angle with respect to a plane of the inner main face of the back shroud, and a line extending from one side edge to the other side edge of the pumping vane at the trailing edge is at an obtuse angle with respect to the plane of the inner main face of the back shroud.
13. A pump impeller according to claim 12, further including a front shroud having an inner main face, the pumping vanes extending between the inner main faces of the front and back shrouds and joined to said shrouds at the said opposed side edges.
14. A pump impeller according to claim 12 or claim 13, otherwise as claimed in any one of claim 5, or claims 6 to 1 1.
PCT/AU2014/000337 2013-03-28 2014-03-28 Slurry pump impeller WO2014153616A1 (en)

Priority Applications (12)

Application Number Priority Date Filing Date Title
AU2014245856A AU2014245856B2 (en) 2013-03-28 2014-03-28 Slurry pump impeller
CA2902759A CA2902759A1 (en) 2013-03-28 2014-03-28 Slurry pump impeller
BR112015024718A BR112015024718A2 (en) 2013-03-28 2014-03-28 mud pump impeller
ES14774127T ES2709199T3 (en) 2013-03-28 2014-03-28 Sludge pump impeller
CN201480017925.5A CN105074225B (en) 2013-03-28 2014-03-28 Slurry pump impeller
US14/780,700 US20160040682A1 (en) 2013-03-28 2014-03-28 Slurry Pump Impeller
AP2015008763A AP2015008763A0 (en) 2013-03-28 2014-03-28 Slurry pump impeller
EP14774127.6A EP2978975B1 (en) 2013-03-28 2014-03-28 Slurry pump impeller
PL14774127T PL2978975T3 (en) 2013-03-28 2014-03-28 Slurry pump impeller
MX2015013549A MX365143B (en) 2013-03-28 2014-03-28 Slurry pump impeller.
EA201591520A EA031306B1 (en) 2013-03-28 2014-03-28 Slurry pump impeller
PH12015501912A PH12015501912A1 (en) 2013-03-28 2015-08-28 Slurry pump impeller

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
AU2013901086A AU2013901086A0 (en) 2013-03-28 Slurry pump impeller
AU2013901086 2013-03-28

Publications (1)

Publication Number Publication Date
WO2014153616A1 true WO2014153616A1 (en) 2014-10-02

Family

ID=51622284

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/AU2014/000337 WO2014153616A1 (en) 2013-03-28 2014-03-28 Slurry pump impeller

Country Status (17)

Country Link
US (1) US20160040682A1 (en)
EP (1) EP2978975B1 (en)
CN (1) CN105074225B (en)
AP (1) AP2015008763A0 (en)
AU (1) AU2014245856B2 (en)
BR (1) BR112015024718A2 (en)
CA (1) CA2902759A1 (en)
CL (1) CL2015002887A1 (en)
EA (1) EA031306B1 (en)
ES (1) ES2709199T3 (en)
MX (1) MX365143B (en)
PE (1) PE20151584A1 (en)
PH (1) PH12015501912A1 (en)
PL (1) PL2978975T3 (en)
PT (1) PT2978975T (en)
TR (1) TR201901181T4 (en)
WO (1) WO2014153616A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2542233A (en) * 2015-08-26 2017-03-15 Weir Minerals Europe Ltd Rotary parts for a slurry pump

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9599120B2 (en) * 2012-08-24 2017-03-21 Asmo Co., Ltd. Impeller for centrifugal pump and centrifugal pump of vehicle washer device
AU201614369S (en) 2016-08-12 2016-10-27 Weir Minerals Australia Ltd Impeller
USD810788S1 (en) 2016-08-25 2018-02-20 Weir Minerals Australia Ltd. Pump impeller
AU201614664S (en) 2016-08-25 2016-11-08 Weir Minerals Australia Ltd Pump impeller
USD810789S1 (en) 2016-08-25 2018-02-20 Weir Minerals Australia Ltd. Pump impeller
CN107299910B (en) * 2017-07-07 2019-10-18 安徽卧龙泵阀股份有限公司 A kind of chemical centrifugal pump impeller unit
USD847863S1 (en) * 2017-12-20 2019-05-07 Crane Pumps & Systems, Inc. Slicer blade and striker plate assembly for a centrifugal pump
CN108561330A (en) * 2018-06-29 2018-09-21 浙江南元泵业有限公司 Centrifugal pump impeller
EP3830420A4 (en) * 2018-08-01 2022-08-24 Weir Slurry Group, Inc. Inverted annular side gap arrangement for a centrifugal pump
CN213808111U (en) * 2020-08-27 2021-07-27 芜湖美的厨卫电器制造有限公司 Impeller, water pump and water heater

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6082000A (en) 1997-03-14 2000-07-04 Dab Pumps S.P.A. Method for producing an impeller for turbine pumps provided with vanes having an improved profile
US20100284812A1 (en) 2009-05-08 2010-11-11 Gm Global Technology Operations, Inc. Centrifugal Fluid Pump
EP2570674A1 (en) 2011-09-15 2013-03-20 Sandvik Intellectual Property AB Erosion resistant impeller vane made of metallic laminate

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2640328B1 (en) * 1988-12-09 1991-03-15 Schlumberger Cie Dowell BLADES ROTOR FOR CENTRIFUGAL PUMP, PUMP AND MIXER USING THE SAME
US5730582A (en) * 1997-01-15 1998-03-24 Essex Turbine Ltd. Impeller for radial flow devices
CN2412114Y (en) * 1999-03-11 2000-12-27 王庆武 Sand removing water pump vane
ITMI20012414A1 (en) * 2001-11-15 2003-05-15 Nuovo Pignone Spa BLADE FOR CENTRIFUGAL COMPRESSOR IMPELLER WITH MEDIUM-HIGH FLOW COEFFICIENT
US8037713B2 (en) * 2008-02-20 2011-10-18 Trane International, Inc. Centrifugal compressor assembly and method
CN201288694Y (en) * 2008-10-07 2009-08-12 石家庄工业水泵有限公司 Highly efficient slurry pump
CN101368574A (en) * 2008-10-15 2009-02-18 许洪元 Design method of two phase flow pump impeller
EP2497956A1 (en) * 2011-03-08 2012-09-12 Egger Pumps Technology AG Free flow pump
JP5879103B2 (en) * 2011-11-17 2016-03-08 株式会社日立製作所 Centrifugal fluid machine
DE102012209832B3 (en) * 2012-06-12 2013-09-12 E.G.O. Elektro-Gerätebau GmbH Pump and method of making an impeller for a pump

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6082000A (en) 1997-03-14 2000-07-04 Dab Pumps S.P.A. Method for producing an impeller for turbine pumps provided with vanes having an improved profile
US20100284812A1 (en) 2009-05-08 2010-11-11 Gm Global Technology Operations, Inc. Centrifugal Fluid Pump
EP2570674A1 (en) 2011-09-15 2013-03-20 Sandvik Intellectual Property AB Erosion resistant impeller vane made of metallic laminate

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP2978975A4

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2542233A (en) * 2015-08-26 2017-03-15 Weir Minerals Europe Ltd Rotary parts for a slurry pump
GB2542233B (en) * 2015-08-26 2018-02-07 Weir Minerals Europe Ltd Rotary parts for a slurry pump

Also Published As

Publication number Publication date
US20160040682A1 (en) 2016-02-11
EA201591520A1 (en) 2016-01-29
AU2014245856A1 (en) 2015-09-17
CL2015002887A1 (en) 2016-05-20
PE20151584A1 (en) 2015-11-18
TR201901181T4 (en) 2019-02-21
AU2014245856B2 (en) 2018-02-15
PL2978975T3 (en) 2019-06-28
EP2978975A4 (en) 2016-11-09
EA031306B1 (en) 2018-12-28
MX2015013549A (en) 2016-04-07
PH12015501912B1 (en) 2016-01-11
EP2978975A1 (en) 2016-02-03
BR112015024718A2 (en) 2017-07-18
CN105074225A (en) 2015-11-18
MX365143B (en) 2019-05-24
PH12015501912A1 (en) 2016-01-11
PT2978975T (en) 2019-02-08
EP2978975B1 (en) 2019-01-02
CA2902759A1 (en) 2014-10-02
CN105074225B (en) 2017-02-15
ES2709199T3 (en) 2019-04-15
AP2015008763A0 (en) 2015-09-30

Similar Documents

Publication Publication Date Title
AU2014245856B2 (en) Slurry pump impeller
CA2911924C (en) Improvements relating to centrifugal pump impellers
CA2961066C (en) Slurry pump impeller
AU2013202462B2 (en) Improvements relating to centrifugal pump impellers
CA2558869C (en) Improved velocity profile impeller vane
CA2839472C (en) Improvements to pumps and components therefor
US10883508B2 (en) Eddy pump

Legal Events

Date Code Title Description
WWE Wipo information: entry into national phase

Ref document number: 201480017925.5

Country of ref document: CN

121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 14774127

Country of ref document: EP

Kind code of ref document: A1

DPE1 Request for preliminary examination filed after expiration of 19th month from priority date (pct application filed from 20040101)
ENP Entry into the national phase

Ref document number: 2902759

Country of ref document: CA

WWE Wipo information: entry into national phase

Ref document number: 201591520

Country of ref document: EA

ENP Entry into the national phase

Ref document number: 2014245856

Country of ref document: AU

Date of ref document: 20140328

Kind code of ref document: A

WWE Wipo information: entry into national phase

Ref document number: MX/A/2015/013549

Country of ref document: MX

WWE Wipo information: entry into national phase

Ref document number: 002072-2015

Country of ref document: PE

NENP Non-entry into the national phase

Ref country code: DE

WWE Wipo information: entry into national phase

Ref document number: 14780700

Country of ref document: US

WWE Wipo information: entry into national phase

Ref document number: 2014774127

Country of ref document: EP

REG Reference to national code

Ref country code: BR

Ref legal event code: B01A

Ref document number: 112015024718

Country of ref document: BR

ENP Entry into the national phase

Ref document number: 112015024718

Country of ref document: BR

Kind code of ref document: A2

Effective date: 20150925