US2845028A - Shallow well expanded output pump - Google Patents
Shallow well expanded output pump Download PDFInfo
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- US2845028A US2845028A US464430A US46443054A US2845028A US 2845028 A US2845028 A US 2845028A US 464430 A US464430 A US 464430A US 46443054 A US46443054 A US 46443054A US 2845028 A US2845028 A US 2845028A
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- pump
- stage
- output
- injector
- pump assembly
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D9/00—Priming; Preventing vapour lock
- F04D9/04—Priming; Preventing vapour lock using priming pumps; using booster pumps to prevent vapour-lock
- F04D9/06—Priming; Preventing vapour lock using priming pumps; using booster pumps to prevent vapour-lock of jet type
Definitions
- T provide a novel and improved pump assembly having the ability to pump larger volumes than comparable prior art pumps under similar conditions
- Figure 1 is a view in section through a pump assembly embodying the present invention
- Figure 2 is a view in section taken in the plane 22 of Figure 1;
- Figure 3 is a view, depicting by means of performance curves, the improved results attributable to the present invention.
- a base 1 having a suction line opening therein in the form of a threaded hole 3 for securing thereto the suction line 5 of apump system, whenthe pump assembly is installed in such a system.
- a bearing 7 Centrally supported in the base unit, which may be a casting, is a bearing 7 for rotatably supporting the lower end of the shaft 8 which carries the rotatable elements of the pump assembly.
- an impeller stage 9 Disposed adjacent the base unit is an impeller stage 9 which constitutes the first stage of the assembly, such stage involving an impeller 11 mounted on' the 'shaft and supported within a housing or spider 13 having peripheral United States Patent Ofice ports 15 about the periphery thereof to pass thedischarge a from the impeller.
- Such housing includes a generally circular outer wall 25, and ceiling 27, and a substahtially right angle parti-. tion 29 bounding a floorsection 31 which is provided with an opening for the pump shaft and its bearing'as. sembly, in line with a corresponding opening 35 in the ceilingofthe housing adapted to 'rotatablyreceivethe intake. end of the impeller 37 of animpeller'stage 39 K following the injector-unit. r
- That portion 41 of the injector housing lyingoutside the partition, is open to the preceding stage-for admission of water discharged from-such stage. j v t Through the wall and partitionpf the injector, housing, 21
- nozzle 43 and a Venturi 45 are aligned openings for the installation of an injector '2 unit involving a nozzle 43 and a Venturi 45.
- the nozzle is mounted in the outer wall opening, which is threaded for the purpose.
- the Venturi is removably sealed in the partition opening, by an O-ring seal 47, with the input end of the Venturi preferably threadedly secured about the nozzle.
- the Venturi In the region of the nozzle discharge, the Venturi is provided with an intake opening or openings 49 for admission of the flow from the preceding stage.
- the output of the injector unit is passed through the impeller stage 39, which in turn may be followed by one or more additional impeller stages 51 mounted on the same shaft, the discharge end of the final or last stage of the pump assembly, communicating with a spout or discharge coupling 53 integrally formed therewith.
- each stage includes a casing section formed with a wall passage communicating with each other, to form a flow passage 55 from the discharge of the final stage back to the nozzle of the injector unit, whereby a portion of the output of the pump will be supplied to the nozzle to run the injector stage.
- the pump unit may be of conventional design, including the motor bracket 57 and the drive motor 59.
- the significant factor in the pump unit assembly of the present invention is the disposal of an injector unit in the assembly with its suction end in communication with the discharge of a preceding stage in the assembly, to relieve the injector unit of the burden of working against a negative suction head, as when forced to lift the water from the well to the impeller stages of the pump assembly, this burden being placed upon the preceding impeller stage in the preferred embodiment of the invention.
- the injectorunit can then be designed to a different characteristic curve and operated at a favorable point on such curve where increased output would be available.
- Such curves represent the output capacities of the pump assemblies involved, measured in gallons per minute, plotted against thedischarge head in terms of pounds per square inch discharge pressure for maximum-suction lift conditions of 0, 10 and 20 feet respectively.
- the dash line curves are those of the reference pump unit wherein the injector unit constitutes the first element of the pump assembly. This might be deemed to represent the prior art.
- the solid line curves represent performance characteristics of a pump assembly embodyingthe present invention wherein the injector unit follows a previous stage such as an impeller stage and consequently functions on a more favorable portion of its characteristic curve.
- the prior art pump assembly developed a maximum output of 14 gallons per minute at which output the pressure was 30 pounds per square inch, whereas the pump assembly embodying the teachings of the present invention at the same pressure, had an output capacity of 16.3 gallons per minute. This means an etficiency of 116.4% or an increase in etficiency of 16.4%.
- the output of the first pump is 11 gallons per minute.
- the pump of the present invention is capable of producing a maximum output of 17.6 gallons per minute.
- the improved pump shows a gain in output over the first pump of close to 63%, as distinguished from the gain in output of 40% at zero suction lift, it being further noted that such increased output being within a pressure range suitable for household and farm installations.
- the curve 61 is that for a system in which the injector unit is installed in accordance with prior practice, e. g., in the base of the pump, While the curve 63 relates to system performance with the injector unit installed beyond the first impeller stage.
- the capacity of the system is limited to a maximum of 14 gallons per minute, but inasmuch as the water level in a well isnt apt to be at or even close to ground level, the likelihood ofsuch system ever approaching such maximum output capacity becomes but a remote possibility in practice.
- the system curve 63 covering this system establishes the realization of surprisingly increased output over the old system for corresponding values of suction lift, with its maximum capacity reaching 19.6 gallons per minute at the zero suction lift value.
- the injector unit While the new system, like the old, is operating at negative pressures in raising the water from a Well, the injector unit, unlike the corresponding unit in the old system, is not functioning under the same conditions, but is now operating under positive pressures, or in other words, in a region above the zero axis on the graph of Figure 3, and may well be represented as the phantom extension 67 of the curve 61.
- the pump of the present invention is adapted to a field of use not limited to shallow well systems, for such pump is capable of pumping hot or volatile liquids which normally present conditions simulating high suction lifts.
- Prior injector type pumps were incapable of coping satisfactorily with situations of this character.
- any number of such impeller stages may be employed before the jet unit, the only essential requirement of the present invention being that at least one such impeller stage shall precede the injector unit to avoid exposure of the injector unit to the negative pressures of suction lift conditions, while at the same time creating a more favorable condition under which the injector unit may function.
- a shallow well type pump assembly having means for coupling a suction line thereto, an injector involving a nozzle and a Venturi, an impeller stage having its suction end in flow connection with the entire output from said injector, means for directing a portion only of the output of said pump assembly to said nozzle, and pump means for continuously feeding liquid from such suction line to said Venturi at positive pressure.
- a shallow well type pump assembly involving a base having means for coupling a suction line thereto, an in jector involving a nozzle and Venturi, an impeller stage having its suction end in flow connection with the entire output from said injector, means for directing a portion only of the output of said pump assembly to said nozzle, and pump means in said base for continuously feeding liquid from such suction line to said Venturi at positive pressure.
- a shallow well type pump assembly involving a base having means for coupling a suction line thereto, at least one impeller stage at the intake end of said pump assembly with its suction end exposed to the suction line coupling means of said base, an injector involving a nozzle and Venturi, means coupling said Venturi in flow connection with the output of said impeller stage, another impeller stage, means for feeding the entire output of said injector stage to said last mentioned impeller stage, and means for directing a portion only of the output of said last mentioned stage to said nozzle.
- a shallow well type pump assembly involving a base having means for coupling a suction line thereto, at least one impeller stage at the intake end of said pump assembly with its suction end exposed to the suction line coupling means of said base, an injector involving a nozzle and Venturi, means coupling said Venturi in flow connection with the output of said impeller stage, another impeller stage, means coupling only the intake end of said other impeller stage in flow connection with the output from said injector, and means for continuously directing a portion only of the output of said other stage to said nozzle.
- a shallow well type pump assembly involving a base having means for coupling a suction line thereto, at least one impeller stage at the intake end of said pump assembly with its suction end exposed to the suction line coupling means of said base, an injector having a nozzle and Venturi, with said Venturi in flow connection with the output of said impeller stage, another impeller stage having its suction end in flow connection with the output from said injector, said other impeller stage having a continuous output, and means for directing a portion only of the continuous output of said other stage to said nozzle, and means directing the remainder of the output of said other stage to the discharge of said pump assembly.
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- Structures Of Non-Positive Displacement Pumps (AREA)
Description
July 29, 1958 F. M. NASH EI'AL I 2, SHALLOW WELL EXPANDED OUTPUT PUMP 1 Filed 001:. 25, 1954 3 Sheets-Sheet 1 IN VEN TOR.
FLOYD M. NASH y ALBERT H. CR/I/E'LL/ H/S ATTORNEYS y 1958 F. M. NASH ETAL 2,845,028
SHALLOW WELL EXPANDED OUTPUT PUMP Filed Oct. 25, 1954 v3 Sheets-Sheet 2 INVENTOR.
FLOYD M. NASH BYALBER 7' A. CR/VELL/ fi/zwa 9 WW H/S ATTORNEYS 2,845,028 Patented July 29, 1958 SHALLOW WELL EXPANDED OUTPUT PUMP Floyd M. Nash, Kensington, and Albert A. Crivelli, El Cerrito, Calif., assignors to Jacuzzi Bros., Incorporated, a corporation of California Application October 25, 1954, Serial No. 464,430
5 Claims. (Cl. 103-5) Our invention relates to shallow well pump systems and more particularly to a pump assembly therefor of the type involving an injector unit.
Among the objects of our invention are:
(1) To provide a novel and improved pump assembly for a pump system;
(2) T provide a novel and improved pump assembly having the ability to pump larger volumes than comparable prior art pumps under similar conditions;
(3) To provide a novel and improved pump assembly employing to maximum advantage, a combination of centrifugal and injector pump components.
Additional objects of our invention will be brought out in the following description of a preferred embodiment of the same, taken in conjunction with the accompanying drawings, wherein:
Figure 1 is a view in section through a pump assembly embodying the present invention;
Figure 2 is a view in section taken in the plane 22 of Figure 1;
Figure 3 is a view, depicting by means of performance curves, the improved results attributable to the present invention.
Referring to the drawings for details of our invention in its preferred form, the same involves a base 1 having a suction line opening therein in the form of a threaded hole 3 for securing thereto the suction line 5 of apump system, whenthe pump assembly is installed in such a system. Centrally supported in the base unit, which may be a casting, is a bearing 7 for rotatably supporting the lower end of the shaft 8 which carries the rotatable elements of the pump assembly.
Disposed adjacent the base unit is an impeller stage 9 which constitutes the first stage of the assembly, such stage involving an impeller 11 mounted on' the 'shaft and supported within a housing or spider 13 having peripheral United States Patent Ofice ports 15 about the periphery thereof to pass thedischarge a from the impeller.
Assembled over the impeller housing and defining therewith a flow passage 17 for the output of the impeller stage, is a section 19 of the pump casing, which extends above the impeller stage and forms a housing 21 for an injector unit 23, which in the instant embodiment of the invention, constitutes in effect the second stage of the pump assembly. I T Such housing includes a generally circular outer wall 25, and ceiling 27, and a substahtially right angle parti-. tion 29 bounding a floorsection 31 which is provided with an opening for the pump shaft and its bearing'as. sembly, in line with a corresponding opening 35 in the ceilingofthe housing adapted to 'rotatablyreceivethe intake. end of the impeller 37 of animpeller'stage 39 K following the injector-unit. r
. That portion 41 of the injector housing lyingoutside the partition,is open to the preceding stage-for admission of water discharged from-such stage. j v t Through the wall and partitionpf the injector, housing, 21
are aligned openings for the installation of an injector '2 unit involving a nozzle 43 and a Venturi 45. The nozzle is mounted in the outer wall opening, which is threaded for the purpose. The Venturi is removably sealed in the partition opening, by an O-ring seal 47, with the input end of the Venturi preferably threadedly secured about the nozzle.
In the region of the nozzle discharge, the Venturi is provided with an intake opening or openings 49 for admission of the flow from the preceding stage.
The output of the injector unit is passed through the impeller stage 39, which in turn may be followed by one or more additional impeller stages 51 mounted on the same shaft, the discharge end of the final or last stage of the pump assembly, communicating with a spout or discharge coupling 53 integrally formed therewith.
Beginning withthe injector unit, each stage includes a casing section formed with a wall passage communicating with each other, to form a flow passage 55 from the discharge of the final stage back to the nozzle of the injector unit, whereby a portion of the output of the pump will be supplied to the nozzle to run the injector stage.
Beyond the injector stage, the pump unit may be of conventional design, including the motor bracket 57 and the drive motor 59.
The significant factor in the pump unit assembly of the present invention is the disposal of an injector unit in the assembly with its suction end in communication with the discharge of a preceding stage in the assembly, to relieve the injector unit of the burden of working against a negative suction head, as when forced to lift the water from the well to the impeller stages of the pump assembly, this burden being placed upon the preceding impeller stage in the preferred embodiment of the invention. The injectorunit can then be designed to a different characteristic curve and operated at a favorable point on such curve where increased output would be available.
We have discovered that by relating such stages in the manner described, not only is the efl'iciency of the pump unit assembly enhanced, but the output capacity of a pump assembly could be expanded far beyond expectations, the magnitude of such increase in capacity running on the order of 40% to or more, with the same pump, the variations depending on the suction lift involvecl. This remarkable accomplishment may better be illustrated by reference to and analysis of the performance curves of Figure 3 ofthedrawings, the values depicted therein being the results of comparative tests, involving a pump assembly of .the present invention, and as a reference for comparison, ,a pump assembly having similar stages but arranged with the injector unit as the initial stage. The straight line curves represent the summation of the performance characteristics of both the im peller stages and injector unit, the slope and cut-01f being determined primarily by the injector unit.
' Such curves represent the output capacities of the pump assemblies involved, measured in gallons per minute, plotted against thedischarge head in terms of pounds per square inch discharge pressure for maximum-suction lift conditions of 0, 10 and 20 feet respectively. The dash line curves are those of the reference pump unit wherein the injector unit constitutes the first element of the pump assembly. This might be deemed to represent the prior art. The solid line curves, on the other hand; represent performance characteristics of a pump assembly embodyingthe present invention wherein the injector unit follows a previous stage such as an impeller stage and consequently functions on a more favorable portion of its characteristic curve.
For a condition of zero lift, the prior art pump assembly developed a maximum output of 14 gallons per minute at which output the pressure was 30 pounds per square inch, whereas the pump assembly embodying the teachings of the present invention at the same pressure, had an output capacity of 16.3 gallons per minute. This means an etficiency of 116.4% or an increase in etficiency of 16.4%.
Of probably greater importance than this, from a practical standpoint, is the fact that the output capacity of the pump has been expanded far beyond that of the prior pump, it being noted that under the zero lift condition, the new pump assembly is capable of delivering a maximum output of 19.6 gallons, which represents an increase in capacity over the old pump of the order of 40%.
Conversely, these curves will show that for the same output from both pump units, that from the pump unit of the present invention will be delivered at higher pressure.
With increase in suction lift, the increased efficiency is retained at about the same value, while at the same time, the output capacity of the pump increased at a substantial rate over that of the prior art pump assembly.
Taking a condition of a foot maximum suction lift, it is noted that the output of the first pump is 11 gallons per minute. By comparison, the pump of the present invention is capable of producing a maximum output of 17.6 gallons per minute. Under the condition of 10 foot maximum suction lift, therefore, the improved pump shows a gain in output over the first pump of close to 63%, as distinguished from the gain in output of 40% at zero suction lift, it being further noted that such increased output being within a pressure range suitable for household and farm installations.
Making a similar comparison of the two pumps for a condition of foot maximum suction lift, the results become even more remarkable. It is noted that the prior art pump develops under such condition, a maximum capacity of 8 gallons per minute, whereas the improved pump of the present invention under the same suction lift conditions is capable of developing a maximum output capacity of 15.5 gallons per minute. This represents a percentage gain of the order of 93% over that of the earlier pump.
The remarkable increase, both in efficiency and maximum output capacity, characteristic of the pump of the present invention is believed attributable to the fact that by installing the injector unit beyond an initial stage, conditions for operation which are more conducive to greater output at increased pressure can thereby be created, and the injector unit operated accordingly.
This might be explained to a degree byan analysis of the two curves 61 and 63, which represent jet system performance in terms of output in gallons per minute for various values of maximum suction lift. The curve 61 is that for a system in which the injector unit is installed in accordance with prior practice, e. g., in the base of the pump, While the curve 63 relates to system performance with the injector unit installed beyond the first impeller stage.
Analyzing the first curve, it is noted that inasmuch as the injector unit is in the base of the pump assembly and is directly exposed to the negative pressures involved, for example, in lifting water from a well, this curve also represents injector unit performance as well'as injectorsystem performance. From a practical viewpoint, therefore, the injector unit in a system of thistype, will practically always be operating at negative pressures, and ac cordingly, operation of the injector'unit will never occur above the zero axis. Therefore, the capacity of the system is limited to a maximum of 14 gallons per minute, but inasmuch as the water level in a well isnt apt to be at or even close to ground level, the likelihood ofsuch system ever approaching such maximum output capacity becomes but a remote possibility in practice. 1
Now, considering the improved pump assembly of the present invention, the system curve 63 covering this system, establishes the realization of surprisingly increased output over the old system for corresponding values of suction lift, with its maximum capacity reaching 19.6 gallons per minute at the zero suction lift value.
While the new system, like the old, is operating at negative pressures in raising the water from a Well, the injector unit, unlike the corresponding unit in the old system, is not functioning under the same conditions, but is now operating under positive pressures, or in other words, in a region above the zero axis on the graph of Figure 3, and may well be represented as the phantom extension 67 of the curve 61. The significance of all this lies in the fact that while the basic structural difference of the new and improved pump assembly over the old, might appear to reside in a mere raising of the injector unit from a position comparable to a first stage, to a position comparable to a second stage, from an operational viewpoint this does not hold, for the net effect of such change is to functionally submerge the injector unit a substantial distance below the level of the water in the well.
By reason of characteristics above described, the pump of the present invention is adapted to a field of use not limited to shallow well systems, for such pump is capable of pumping hot or volatile liquids which normally present conditions simulating high suction lifts. Prior injector type pumps were incapable of coping satisfactorily with situations of this character.
While the pump assembly illustrated and described above, utilized but one impeller stage before the jet unit, any number of such impeller stages may be employed before the jet unit, the only essential requirement of the present invention being that at least one such impeller stage shall precede the injector unit to avoid exposure of the injector unit to the negative pressures of suction lift conditions, while at the same time creating a more favorable condition under which the injector unit may function.
. invention in its preferred form, it is apparent that the same is subject to alteration and modification without departing from the underlying principles involved, and we accordingly do not desire to be limited in our protection to the specific details illustrated and described in the preferred embodiment, except as may be necessitated by the appended claims.
We claim:
1. A shallow well type pump assembly having means for coupling a suction line thereto, an injector involving a nozzle and a Venturi, an impeller stage having its suction end in flow connection with the entire output from said injector, means for directing a portion only of the output of said pump assembly to said nozzle, and pump means for continuously feeding liquid from such suction line to said Venturi at positive pressure.
2. A shallow well type pump assembly involving a base having means for coupling a suction line thereto, an in jector involving a nozzle and Venturi, an impeller stage having its suction end in flow connection with the entire output from said injector, means for directing a portion only of the output of said pump assembly to said nozzle, and pump means in said base for continuously feeding liquid from such suction line to said Venturi at positive pressure.
3. A shallow well type pump assembly involving a base having means for coupling a suction line thereto, at least one impeller stage at the intake end of said pump assembly with its suction end exposed to the suction line coupling means of said base, an injector involving a nozzle and Venturi, means coupling said Venturi in flow connection with the output of said impeller stage, another impeller stage, means for feeding the entire output of said injector stage to said last mentioned impeller stage, and means for directing a portion only of the output of said last mentioned stage to said nozzle.
4. A shallow well type pump assembly involving a base having means for coupling a suction line thereto, at least one impeller stage at the intake end of said pump assembly with its suction end exposed to the suction line coupling means of said base, an injector involving a nozzle and Venturi, means coupling said Venturi in flow connection with the output of said impeller stage, another impeller stage, means coupling only the intake end of said other impeller stage in flow connection with the output from said injector, and means for continuously directing a portion only of the output of said other stage to said nozzle.
5. A shallow well type pump assembly involving a base having means for coupling a suction line thereto, at least one impeller stage at the intake end of said pump assembly with its suction end exposed to the suction line coupling means of said base, an injector having a nozzle and Venturi, with said Venturi in flow connection with the output of said impeller stage, another impeller stage having its suction end in flow connection with the output from said injector, said other impeller stage having a continuous output, and means for directing a portion only of the continuous output of said other stage to said nozzle, and means directing the remainder of the output of said other stage to the discharge of said pump assembly.
References Cited in the file of this patent UNITED STATES PATENTS 1,319,797 Rogers Oct. 28, 1919 2,660,953 Tinker et a1. Dec. 1, 1953 2,677,389 Jisha et al May 4, 1954 FOREIGN PATENTS 219,697 Germany of 1909 220,237 Germany Mar. 19, 1910
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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US464430A US2845028A (en) | 1954-10-25 | 1954-10-25 | Shallow well expanded output pump |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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US464430A US2845028A (en) | 1954-10-25 | 1954-10-25 | Shallow well expanded output pump |
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US2845028A true US2845028A (en) | 1958-07-29 |
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US464430A Expired - Lifetime US2845028A (en) | 1954-10-25 | 1954-10-25 | Shallow well expanded output pump |
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3894813A (en) * | 1974-01-30 | 1975-07-15 | Trw Inc | Aircraft fuel supply system having a dual stream tow-phase fluid pump |
FR2414645A1 (en) * | 1978-01-13 | 1979-08-10 | Dunlop Ltd | Multistage rotary pump with injectors - connects rotary stage outlet to injector pump on another stage inlet |
US4294573A (en) * | 1979-05-17 | 1981-10-13 | Kobe, Inc. | Submersible electrically powered centrifugal and jet pump assembly |
US4381175A (en) * | 1980-09-11 | 1983-04-26 | Kobe, Inc. | Jet electric pump |
DE3409463A1 (en) * | 1984-03-15 | 1985-09-26 | Grundfos A/S, Bjerringbro | ROTATING FLOW PUMP WITH A FEED PUMP UNIT |
US20100108307A1 (en) * | 2008-10-30 | 2010-05-06 | Baker Hughes Incorporated | System, method and apparatus for gas extraction device for down hole oilfield applications |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE219697C (en) * | ||||
DE220237C (en) * | ||||
US1319797A (en) * | 1919-10-28 | rogers | ||
US2660953A (en) * | 1949-08-06 | 1953-12-01 | Fairbanks Morse & Co | Fluid pump assembly |
US2677389A (en) * | 1950-02-07 | 1954-05-04 | Mission Mfg Co | Pumping system for washing machines |
-
1954
- 1954-10-25 US US464430A patent/US2845028A/en not_active Expired - Lifetime
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE219697C (en) * | ||||
DE220237C (en) * | ||||
US1319797A (en) * | 1919-10-28 | rogers | ||
US2660953A (en) * | 1949-08-06 | 1953-12-01 | Fairbanks Morse & Co | Fluid pump assembly |
US2677389A (en) * | 1950-02-07 | 1954-05-04 | Mission Mfg Co | Pumping system for washing machines |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3894813A (en) * | 1974-01-30 | 1975-07-15 | Trw Inc | Aircraft fuel supply system having a dual stream tow-phase fluid pump |
FR2414645A1 (en) * | 1978-01-13 | 1979-08-10 | Dunlop Ltd | Multistage rotary pump with injectors - connects rotary stage outlet to injector pump on another stage inlet |
US4294573A (en) * | 1979-05-17 | 1981-10-13 | Kobe, Inc. | Submersible electrically powered centrifugal and jet pump assembly |
US4381175A (en) * | 1980-09-11 | 1983-04-26 | Kobe, Inc. | Jet electric pump |
DE3409463A1 (en) * | 1984-03-15 | 1985-09-26 | Grundfos A/S, Bjerringbro | ROTATING FLOW PUMP WITH A FEED PUMP UNIT |
US4627792A (en) * | 1984-03-15 | 1986-12-09 | Grundfos A/S | Rotating flow pump with a feed pump unit formed as an ejector |
US20100108307A1 (en) * | 2008-10-30 | 2010-05-06 | Baker Hughes Incorporated | System, method and apparatus for gas extraction device for down hole oilfield applications |
US7984766B2 (en) | 2008-10-30 | 2011-07-26 | Baker Hughes Incorporated | System, method and apparatus for gas extraction device for down hole oilfield applications |
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