GB2054748A - Pump impeller - Google Patents

Pump impeller Download PDF

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Publication number
GB2054748A
GB2054748A GB8013566A GB8013566A GB2054748A GB 2054748 A GB2054748 A GB 2054748A GB 8013566 A GB8013566 A GB 8013566A GB 8013566 A GB8013566 A GB 8013566A GB 2054748 A GB2054748 A GB 2054748A
Authority
GB
United Kingdom
Prior art keywords
vane
impeller
pump
impellers
outlet
Prior art date
Legal status (The legal status 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 status listed.)
Granted
Application number
GB8013566A
Other versions
GB2054748B (en
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
TDK Micronas GmbH
ITT Inc
Original Assignee
Deutsche ITT Industries GmbH
ITT Industries Inc
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 Deutsche ITT Industries GmbH, ITT Industries Inc filed Critical Deutsche ITT Industries GmbH
Publication of GB2054748A publication Critical patent/GB2054748A/en
Application granted granted Critical
Publication of GB2054748B publication Critical patent/GB2054748B/en
Expired legal-status Critical Current

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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
    • F04D29/00Details, component parts, or accessories
    • F04D29/18Rotors
    • F04D29/22Rotors specially for centrifugal pumps
    • F04D29/2238Special flow patterns
    • F04D29/225Channel wheels, e.g. one blade or one flow channel

Abstract

In order to diminish the risk of clogging during pumping of, for instance, sewage, the vane (1) is formed with a varying thickness along its length. The speed reduction in the flow channel between the vane inlet and the vane outlet is then limited, since the channel only increases in cross-section by a predetermined limited amount towards the outlet and pressure decreases within the channel are minimised. The vane (1) can be made hollow to decrease balancing problems. <IMAGE>

Description

SPECIFICATION Pump Impeller The invention relates to an impeller for centrifugal and axial pumps, and in particular to an impeller of the so-called single vane type, which means that the impeller is provided with one single vane which goes helically around the impeller a part of one or several turns. The channel which is formed by the vane axially limited by cover discs which are parts of the impeller or the surrounding pump housing.
Pump impellers of the type referred to are above all used for pumping of liquids containing solid bodies, for instance sewage water. The advantage is that the risk for clogging decreases il one instead of several vanes are used. Sometimes a certain minimum size of through passage in a pump impeller for sewage pumps is prescribed by Authorities. This can only be fulfilled by single vane impellers if resonable dimensions should be kept.
In previously known impellers of the single vane type, the vane is formed with a constant thickness from the leading edge by the pump inlet to the trailing edge by the pump outlet. One such impeller is shown in the Swedish published patent application 7806198-3.
Such impellers have however certain disadvantages. As the vane thickness is constant, the channel which is formed by the vane has an essentially increasing cross-section towards the pump outlet. This increase, which is most significant shortly after the inlet, means a reduction of flow speed and a local pressure decreases (diffusion) which creates undesirable turbulence and sometimes cavitation. Besides, the risks increase that solid bodies will stick to the vane, especially on its leading edge, and thus decrease the free through passage which means risks for clogging and decreasing efficiency. With clogging of the impeller the load on the driving unit increases, thus sometimes releasing the overload protection and generating expensive stoppages and service work.
An object of the present invention is to provide an impeller of the single-vane type in which the speed reduction of the flow is reduced as much as possible.
According to the present invention there is provided a single vane impeller for use in centrifugal and axial pumps, wherein the thickness of the vane varies such that a channel defined by the vane and cover discs of the impeller or a surrounding pump housing has cross-section which increases towards the outlet by a predetermined limited amount whereby diffusion of the pumped medium within the impeller is prohibited.
An embodiment of the invention will now be described with reference to the accompanying drawings, in which: Fig. 1 shows an axial section through an embodiment of impeller according to the present invention; Fig. 2 shows a radial section taken along line Il-Il of Fig. 1, and Fig. 3 shows a perspective view of the impeller of Figs. 1 and 2 when inverted.
In the drawings, an impeller vane 1 has a leading edge (inlet edge) 2 and a trailing edge (outlet edge) 3. A channel 4 is formed by the vane 1 and cover discs 5. There is a hole 6 for an impeller shaft (not shown).
Unlike known impellers of the single vane type, the impeller according to the present invention has a vane 1 with varying thickness in the flow direction. This means that the channel 4, which is formed by the vane 1 and the cover discs 5, has a cross-section which only increases towards the outlet by a limited amount thus diminishing the risks of clogging.
Known impellers of the single vane type often accumulate a layer of particles near the leading edge 2. This layer often gives the vane a new profile which is somewhat like the vane profile according to the present invention. The disadvantages, except for the clogging tendency, are that the risks for overloading increase considerably and that a strong unbalance occurs in the impeller which brings about increasing strain on the bearings etc., causing a shorter length of life. According to the present invention, the right profile is formed from the beginning and the impeller is balanced accordingly.
In a preferred embodiment the vane is hollow in order to diminish its weight and thus the need for balancing material.
The vane 1 may be formed differently according to the needs. Different optimal conditions are valid for different types of pumped medium, impeller speed, volume flow and head.
Depending on these criteria the impeller is formed with a more or less expressed bulb form and with single or double bent sides. The vane may have a single bent outside and a double bent inside, or single bent in- and outsides, or double bent in and outsides. A common feature for all embodiments is the varying thickness of the vane. The bulb form may be such that the greatest thickness of the vane is between 200 and 400 from the leading edge 2.
The impellers of the present invention involve radically diminished clogging risk, an increased liquid flow through the impeller with a resultant improved efficiency and an improved balancing of the impeller without abandoning the minimum free through passage dimensions.
Claims
1. A single vane impeller for use in centrifugal and axial pumps, wherein the thickness of the vane varies such that a channel defined by the vane and cover discs of the impeller or a surrounding pump housing has cross-section which increases towards the outlet by a predetermined limited amount whereby diffusion of the pumped medium within the impeller is prohibited.
**WARNING** end of DESC field may overlap start of CLMS **.

Claims (9)

**WARNING** start of CLMS field may overlap end of DESC **. SPECIFICATION Pump Impeller The invention relates to an impeller for centrifugal and axial pumps, and in particular to an impeller of the so-called single vane type, which means that the impeller is provided with one single vane which goes helically around the impeller a part of one or several turns. The channel which is formed by the vane axially limited by cover discs which are parts of the impeller or the surrounding pump housing. Pump impellers of the type referred to are above all used for pumping of liquids containing solid bodies, for instance sewage water. The advantage is that the risk for clogging decreases il one instead of several vanes are used. Sometimes a certain minimum size of through passage in a pump impeller for sewage pumps is prescribed by Authorities. This can only be fulfilled by single vane impellers if resonable dimensions should be kept. In previously known impellers of the single vane type, the vane is formed with a constant thickness from the leading edge by the pump inlet to the trailing edge by the pump outlet. One such impeller is shown in the Swedish published patent application 7806198-3. Such impellers have however certain disadvantages. As the vane thickness is constant, the channel which is formed by the vane has an essentially increasing cross-section towards the pump outlet. This increase, which is most significant shortly after the inlet, means a reduction of flow speed and a local pressure decreases (diffusion) which creates undesirable turbulence and sometimes cavitation. Besides, the risks increase that solid bodies will stick to the vane, especially on its leading edge, and thus decrease the free through passage which means risks for clogging and decreasing efficiency. With clogging of the impeller the load on the driving unit increases, thus sometimes releasing the overload protection and generating expensive stoppages and service work. An object of the present invention is to provide an impeller of the single-vane type in which the speed reduction of the flow is reduced as much as possible. According to the present invention there is provided a single vane impeller for use in centrifugal and axial pumps, wherein the thickness of the vane varies such that a channel defined by the vane and cover discs of the impeller or a surrounding pump housing has cross-section which increases towards the outlet by a predetermined limited amount whereby diffusion of the pumped medium within the impeller is prohibited. An embodiment of the invention will now be described with reference to the accompanying drawings, in which: Fig. 1 shows an axial section through an embodiment of impeller according to the present invention; Fig. 2 shows a radial section taken along line Il-Il of Fig. 1, and Fig. 3 shows a perspective view of the impeller of Figs. 1 and 2 when inverted. In the drawings, an impeller vane 1 has a leading edge (inlet edge) 2 and a trailing edge (outlet edge) 3. A channel 4 is formed by the vane 1 and cover discs 5. There is a hole 6 for an impeller shaft (not shown). Unlike known impellers of the single vane type, the impeller according to the present invention has a vane 1 with varying thickness in the flow direction. This means that the channel 4, which is formed by the vane 1 and the cover discs 5, has a cross-section which only increases towards the outlet by a limited amount thus diminishing the risks of clogging. Known impellers of the single vane type often accumulate a layer of particles near the leading edge 2. This layer often gives the vane a new profile which is somewhat like the vane profile according to the present invention. The disadvantages, except for the clogging tendency, are that the risks for overloading increase considerably and that a strong unbalance occurs in the impeller which brings about increasing strain on the bearings etc., causing a shorter length of life. According to the present invention, the right profile is formed from the beginning and the impeller is balanced accordingly. In a preferred embodiment the vane is hollow in order to diminish its weight and thus the need for balancing material. The vane 1 may be formed differently according to the needs. Different optimal conditions are valid for different types of pumped medium, impeller speed, volume flow and head. Depending on these criteria the impeller is formed with a more or less expressed bulb form and with single or double bent sides. The vane may have a single bent outside and a double bent inside, or single bent in- and outsides, or double bent in and outsides. A common feature for all embodiments is the varying thickness of the vane. The bulb form may be such that the greatest thickness of the vane is between 200 and 400 from the leading edge 2. The impellers of the present invention involve radically diminished clogging risk, an increased liquid flow through the impeller with a resultant improved efficiency and an improved balancing of the impeller without abandoning the minimum free through passage dimensions. Claims
1. A single vane impeller for use in centrifugal and axial pumps, wherein the thickness of the vane varies such that a channel defined by the vane and cover discs of the impeller or a surrounding pump housing has cross-section which increases towards the outlet by a predetermined limited amount whereby diffusion of the pumped medium within the impeller is prohibited.
2. An impeller as claimed in claim 1, wherein the vane has a bulb form with its greatest thickness 20---40" from the leading edge of the vane.
3. An impeller as claimed in claim 1 or claim 2, wherein the vane is hollow.
4. An impeller as claimed in claim 1 or claim 2, wherein the vane is solid.
5. An impeller as claimed in claim 1, wherein the vane has a single bent outside and double bent inside.
6. An impeller as claimed in claim 1, wherein the vane has single bent in- and outsides.
7. An impeller as claimed in claim 1, wherein the vane has double bent in- and outsides.
8. A single vane impeller for use in centrifugal and axial pumps substantially as herein described with reference to and as illustrated in the accompanying drawings.
9. A pump including a single vane impeller as claimed in any one of the preceding claims.
GB8013566A 1979-04-27 1980-04-24 Pump impeller Expired GB2054748B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SE7903729A SE426976B (en) 1979-04-27 1979-04-27 PADDLE WHEEL

Publications (2)

Publication Number Publication Date
GB2054748A true GB2054748A (en) 1981-02-18
GB2054748B GB2054748B (en) 1983-03-23

Family

ID=20337920

Family Applications (1)

Application Number Title Priority Date Filing Date
GB8013566A Expired GB2054748B (en) 1979-04-27 1980-04-24 Pump impeller

Country Status (9)

Country Link
JP (1) JPS55160195A (en)
CA (1) CA1146809A (en)
DE (1) DE3015188A1 (en)
FI (1) FI800864A (en)
FR (1) FR2455197A1 (en)
GB (1) GB2054748B (en)
IT (1) IT1193387B (en)
NL (1) NL8002322A (en)
SE (1) SE426976B (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SE444970B (en) * 1982-10-11 1986-05-20 Flygt Ab CENTRIFUGAL PUMP WHEEL FOR PROMOTION OF PUMPING OF LIQUID MEDIA CONTAINING POLLUTANTS
FI73501C (en) * 1984-06-06 1987-10-09 Sarlin Ab Oy E Impeller at a pump.
JPH0641757B2 (en) * 1985-05-01 1994-06-01 株式会社鷺宮製作所 Drainage pump
DE3615686A1 (en) * 1986-05-09 1987-11-12 Klein Schanzlin & Becker Ag CHANNEL WHEEL FOR CENTRIFUGAL PUMPS
SE461996B (en) * 1988-09-14 1990-04-23 Flygt Ab CLOSED LOAD WHEEL FOR PUMPS, COMPRESSORS, FLATS ETC OF CENTRIFUGAL OR HALFAXIAL TYPE
JPH07117076B2 (en) * 1989-05-26 1995-12-18 太平洋機工株式会社 Impeller for turbo pump for water jet propulsion machine and turbo pump having the impeller
US6837684B2 (en) 2002-10-25 2005-01-04 Grundfos Management A/S Pump impeller
US10544693B2 (en) 2016-06-15 2020-01-28 Honeywell International Inc. Service routing configuration for a gas turbine engine diffuser system

Family Cites Families (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR525666A (en) * 1919-10-20 1921-09-26 John Stanley Hazell Improvements to centrifugal pumps
US1470607A (en) * 1922-11-03 1923-10-16 Unchokeable Pump Ltd Impeller for centrifugal pumps
DE457204C (en) * 1923-05-28 1928-03-10 Bucher Guyer Fa Centrifugal pump with a hollow wing similar to a pipe elbow for pumping liquids containing solid substances, in particular manure
US1754992A (en) * 1926-12-06 1930-04-15 American Well Works Centrifugal pump
GB377370A (en) * 1931-06-05 1932-07-28 Harland Engineering Co Ltd Improvements relating to centrifugal sewage pumps
CH189936A (en) * 1936-01-18 1937-03-31 Bucher Guyer Ag Masch Centrifugal pump for pumping liquid manure, sludge water and the like.
US2272469A (en) * 1939-12-23 1942-02-10 Chicago Pump Co Centrifugal pump
US2655868A (en) * 1947-09-08 1953-10-20 Fairbanks Morse & Co Bladeless pump impeller
US2741992A (en) * 1950-04-10 1956-04-17 Fairbanks Morse & Co Bladeless impeller balance means
DE1126250B (en) * 1954-03-25 1962-03-22 Emil Julius Ask Centrifugal pump with an impeller, the blade channels of which decrease in their clear width towards the circumference
US2853019A (en) * 1954-09-01 1958-09-23 New York Air Brake Co Balanced single passage impeller pump
US3082695A (en) * 1959-06-15 1963-03-26 Klein Schanzlin & Becker Ag Impellers, especially single vane impellers for rotary pumps
FR1274289A (en) * 1960-11-29 1961-10-20 Centrifugal pump with single duct rotor
US3234887A (en) * 1963-01-05 1966-02-15 Flygts Pumpar Ab Impeller, particularly with one or more channels
US3732032A (en) * 1971-02-16 1973-05-08 Baggers Ltd Centrifugal pumps

Also Published As

Publication number Publication date
GB2054748B (en) 1983-03-23
IT8021666A0 (en) 1980-04-24
FR2455197B1 (en) 1984-04-13
SE426976B (en) 1983-02-21
IT1193387B (en) 1988-06-15
FI800864A (en) 1980-10-28
NL8002322A (en) 1980-10-29
FR2455197A1 (en) 1980-11-21
JPS55160195A (en) 1980-12-12
SE7903729L (en) 1980-10-28
JPH0128234B2 (en) 1989-06-01
DE3015188A1 (en) 1980-10-30
CA1146809A (en) 1983-05-24

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Date Code Title Description
PE20 Patent expired after termination of 20 years

Effective date: 20000423