EP2265824B1 - Unterwasserförderaggregat - Google Patents

Unterwasserförderaggregat Download PDF

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Publication number
EP2265824B1
EP2265824B1 EP20090730124 EP09730124A EP2265824B1 EP 2265824 B1 EP2265824 B1 EP 2265824B1 EP 20090730124 EP20090730124 EP 20090730124 EP 09730124 A EP09730124 A EP 09730124A EP 2265824 B1 EP2265824 B1 EP 2265824B1
Authority
EP
European Patent Office
Prior art keywords
housing
pump
pressure
module housing
delivery unit
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.)
Not-in-force
Application number
EP20090730124
Other languages
German (de)
English (en)
French (fr)
Other versions
EP2265824A2 (de
Inventor
Axel JÄSCHKE
Jörg LEWERENZ
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.)
ITT Bornemann GmbH
Original Assignee
Joh Heinr Bornemann GmbH
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Joh Heinr Bornemann GmbH filed Critical Joh Heinr Bornemann GmbH
Publication of EP2265824A2 publication Critical patent/EP2265824A2/de
Application granted granted Critical
Publication of EP2265824B1 publication Critical patent/EP2265824B1/de
Not-in-force legal-status Critical Current
Anticipated expiration legal-status Critical

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04C—ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
    • F04C13/00—Adaptations of machines or pumps for special use, e.g. for extremely high pressures
    • F04C13/008—Pumps for submersible use, i.e. down-hole pumping
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04C—ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
    • F04C11/00—Combinations of two or more machines or pumps, each being of rotary-piston or oscillating-piston type; Pumping installations
    • F04C11/008—Enclosed motor pump units
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04D—NON-POSITIVE-DISPLACEMENT PUMPS
    • F04D13/00—Pumping installations or systems
    • F04D13/02—Units comprising pumps and their driving means
    • F04D13/06—Units comprising pumps and their driving means the pump being electrically driven
    • F04D13/08—Units comprising pumps and their driving means the pump being electrically driven for submerged use
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04D—NON-POSITIVE-DISPLACEMENT PUMPS
    • F04D13/00—Pumping installations or systems
    • F04D13/02—Units comprising pumps and their driving means
    • F04D13/06—Units comprising pumps and their driving means the pump being electrically driven
    • F04D13/08—Units comprising pumps and their driving means the pump being electrically driven for submerged use
    • F04D13/086—Units comprising pumps and their driving means the pump being electrically driven for submerged use the pump and drive motor are both submerged
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04D—NON-POSITIVE-DISPLACEMENT PUMPS
    • F04D25/00—Pumping installations or systems
    • F04D25/02—Units comprising pumps and their driving means
    • F04D25/06—Units comprising pumps and their driving means the pump being electrically driven
    • F04D25/0686—Units comprising pumps and their driving means the pump being electrically driven specially adapted for submerged use
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04D—NON-POSITIVE-DISPLACEMENT PUMPS
    • F04D29/00—Details, component parts, or accessories
    • F04D29/08—Sealings
    • F04D29/10—Shaft sealings
    • F04D29/102—Shaft sealings especially adapted for elastic fluid pumps
    • F04D29/104—Shaft sealings especially adapted for elastic fluid pumps the sealing fluid being other than the working fluid or being the working fluid treated
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04D—NON-POSITIVE-DISPLACEMENT PUMPS
    • F04D29/00—Details, component parts, or accessories
    • F04D29/08—Sealings
    • F04D29/10—Shaft sealings
    • F04D29/106—Shaft sealings especially adapted for liquid pumps
    • F04D29/108—Shaft sealings especially adapted for liquid pumps the sealing fluid being other than the working liquid or being the working liquid treated
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04C—ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
    • F04C13/00—Adaptations of machines or pumps for special use, e.g. for extremely high pressures
    • F04C13/007—Venting; Gas and vapour separation during pumping
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04C—ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
    • F04C2210/00—Fluid
    • F04C2210/24—Fluid mixed, e.g. two-phase fluid
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04C—ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
    • F04C2240/00—Components
    • F04C2240/30—Casings or housings

Definitions

  • the invention relates to an underwater conveyor with a pump and a drive device, wherein the drive device is sealed against the surrounding water and against a process medium.
  • the invention is particularly suitable and intended to promote multiphase mixtures.
  • the DE 37 21 398 A1 describes a delivery unit of a pump with a drive device, wherein the pump is surrounded on all sides by a pump housing having a suction chamber with a suction port and a pressure chamber with an outlet port.
  • the pump housing is waterproof and connected to a likewise waterproof trained, the drive device receiving motor housing which encloses an encapsulated drive unit surrounding the engine compartment, which is divided liquid-tight with respect to the suction chamber.
  • the engine compartment is filled with a barrier medium, in this case with oil, which serves to lubricate the bearings, any gears or the like and acts on the seals and releases the heat through the motor housing to its surroundings.
  • a barrier medium in this case with oil, which serves to lubricate the bearings, any gears or the like and acts on the seals and releases the heat through the motor housing to its surroundings.
  • Such underwater conveyors are used to transport hydrocarbons in the sea.
  • the temperatures of the surrounding water and those of the conveying or process medium are different, while the water temperature is between 1 and 4 ° C, the process medium will be warm to over 100 ° C, so that correspondingly high thermal loads occur. All components that are integrated in a conveyor system must be able to withstand at least the loads listed above.
  • Pump systems for the production of hydrocarbons in the deep sea are usually carried out so that the pump and the drive means such as motor and clutch are installed in a common housing.
  • the two areas are separated by shaft seal; the area of engine, bearing and clutch space not filled with the process medium is filled with a barrier medium, usually with water or oil.
  • a disadvantage of this concept is a close link between the pressure-bearing housing and the necessary for the operation of tight tolerances for rotating elements and sealing components. Deformations due to the occurring pressures of + 350 to -500 bar and temperature fluctuations of 1 ° C to over 100 ° C must be at several sensitive to shape and position changes points, such. As bearings, shaft seals and engine gap, can be added. These are accompanied by large viscosity fluctuations in the barrier medium, if this as Oil is running. If no delivery phase is present, the motor and the pump cool down to the ambient temperature at standstill; During operation, they heat up to 60 ° C to 80 ° C due to the temperature of the process medium and friction.
  • the resulting barrier oil viscosities of about 100 cSt in a cold system and less than 2 cSt in a hot system require special measures in the barrier oil system.
  • the lubricity and carrying capacity of the barrier oil must be maintained both in the cold and in the warm state. In the cold state also high hydraulic friction losses z. B. be overcome in the engine.
  • sealing points to the environment should be minimized as far as possible in an underwater pumping unit, since sealing points pose a potential source of error and prone to leaks and the detection of a small leakage is very difficult, but for environmental reasons, any leakage should be avoided.
  • the joint extraction of oil and gas means that liquids and gases are transported side by side.
  • a so-called multiphase mixture is promoted, which has a high probability of the temporary presence of only one phase, so that for considerable periods only liquids or only gaseous components are promoted.
  • the composition of the multi-phase mixture varies over a wide range and over long periods of time, so that special requirements are placed on the pump technology.
  • the DE 100 81 956 T1 describes a vibration pump having a frame group and a drive solenoid housed in the frame group.
  • a transmission group with an axially oscillating to the frame group Element is provided, wherein the vibrating element is attached with one end to the drive solenoid.
  • the pump is designed as a submersible pump with a front end arranged at the bottom inlet. Via an auxiliary pumping chamber and outgoing pump outlets, the medium to be conveyed is conveyed through an annular passage to the pump outlet.
  • Such a pump is preferably provided as a shaft pump.
  • WO 92/06299 relates to a pressure pump for water with a housing having water chambers and an upper pressure outlet.
  • a suction device is formed by a bell-shaped housing part which receives the pump in and has an upper opening. Together with the outer surface of the pump, the bell-shaped housing forms an annular Hilfssaughunt. From the pump, the sucked medium is pumped through holes in a wall in the annular space and from there through the outlet.
  • the EP 719 940 A1 relates to a side-flow pump having an outer cylinder and a motor accommodated therein, comprising a stator disposed on a motor frame and a rotor mounted on a main shaft.
  • the outer cylinder defines an annular space defined about the engine frame, the outer cylinder having a suction port for introducing the fluid into the annular space.
  • An outlet is formed in the outer cylinder to pump away the fluid.
  • a pump unit with an impeller is disposed at one end of the main shaft.
  • An ejection housing is mounted on an outer peripheral surface of the outer cylinder and provided with a discharge port for ejecting the pumped fluid.
  • the EP 634 827 A1 describes a sealed motor for use in a pump with a stator on a frame housing and a rotatable in the Stator arranged shaft on which a rotor is arranged.
  • a cylinder of sheet metal is formed around the frame housing with an annulus therebetween, the cylinder having a pair of flanges.
  • a plurality of pumping units each having at least one impeller is provided.
  • the WO 98/00643 describes a pump having a housing with an inlet and an outlet, a motor and an impeller for conveying the liquid which is forced through the outlet.
  • the engine is advantageously cooled by the fluid being pumped while at the same time sealed against the fluid being pumped.
  • the DE 22 14 653 B1 describes a pumping and separating device, which is connected via a suction line with the arranged in the ground storage tank.
  • the pumping and separating device consists of a pump which is connected to the suction line and which has a uniform power.
  • the pump is provided with an air separation device and is particularly suitable for gasoline pumps. It has a suction pump, an air separator and a pump return valve, which is arranged below the air separator. About such a pump and Heilabscheidevoriques prevents subsidized air in the quantity measurement is taken into account.
  • the object of the present invention is therefore to provide an underwater pumping unit for hydrocarbons, which operates reliably and reduces the risk of environmental damage due to leaks, without the functionality and reliability is impaired.
  • the underwater pumping unit according to the invention with a pump and a drive device, in which the drive device is sealed against the surrounding water and against a process medium, provides that the pump and the drive device are combined into a module in a module housing and arranged in a pressure housing, wherein the Pressure housing is filled with the process fluid during operation and surrounds the module housing.
  • the module housing responsible for the change in shape experiences constant pressure forces and is decoupled from the external pressure, which rests on the pressure housing.
  • the process medium prevents direct contact of the module housing with the ambient water, which leads to a homogenization of the operating temperature and a lower temperature gradient, so that the pump and the drive are exposed to lower thermal loads.
  • the module housing be designed to substantially constant forces out, which means a reduction in design complexity and at the same time has a higher efficiency of the pump at the same time less probability of failure result.
  • separation means for separating a liquid phase and a gas phase of a multi-phase mixture are arranged, for example in the form of diverters or calming zones or targeted flow cross-section increases, to reduce the flow rates and cause a gravitational separation of liquid phase and gas phase.
  • the separate liquid phase can then be passed either within the module housing or from the pressure housing back into the suction chamber of the pump to effect a recirculation of the separated liquid phase, if necessary, for example, if for a longer time exclusively gas phase is promoted.
  • the recirculation serves to maintain the gap seal and the cooling of the conveying elements.
  • a recirculation is provided from the pressure chamber of the pump to the suction chamber of the pump in order to meter a separated liquid phase to the suction chamber.
  • the separation and the storage capacity of the separated liquid phase can be carried out independently of the orientation of the pressure housing or the pump and the drive device, so that a separation of liquid phase and gas phase can take place both in a horizontal and vertical installation.
  • a development of the invention provides that the module housing is mounted to form an annular space in the pressure housing, so that the module housing can be completely surrounded by the process medium, with exception of the necessary storage locations of the module housing within the pressure housing.
  • the annular space serves at the same time as a separation device, via which a liquid phase can be separated from a gas phase.
  • the annulus may act as a retention space for a liquid phase can be used, provided that it is arranged on the suction side to supply separated liquid phase to the suction of the pump to supply the usually executed as a screw pump pump with a sufficient amount of liquid phase, on the one hand a gap sealing the movement column of parallel screw spindles ensure and on the other hand to cause lubrication and cooling.
  • the annular space is arranged on the pressure side, it can serve as a separation space and make it possible to recirculate a previously conveyed liquid phase via a short-circuit line into the suction space of the pump.
  • the module housing is slidably mounted at least at a bearing point in the pressure housing, so that the necessary decoupling of the module or the module housing is ensured by thermal or hydrostatic deformation of the pressure housing by a floating bearing in the axial direction.
  • the module housing is cylindrical in order to ensure a high pressure stability, wherein the pressure housing is preferably arranged concentrically around the module housing.
  • the module housing is preferably mounted within the pressure housing at a point in a fixed bearing, wherein the fixed bearing is preferably provided with passages through the pressure housing, for example, to lead electrical or hydraulic supply lines to the module housing and the drive means.
  • the bushings can be statically sealed easily and safely.
  • the suction side Retention chamber for the liquid phase can on the suction side Retention chamber for the liquid phase be provided to have a sufficient supply for gas phase delivery periods.
  • the inlet side and the outlet side of the underwater pumping unit can be interconnected by at least one check valve, which allows a free passage of the process medium in one direction and locks in the other direction, so that a free passage of the process medium is ensured even when not activated pump and a free exchange can be ensured.
  • the floating bearing can also be used as inlet nozzle for the process medium, so that promoted by the floating bearing in the pressure housing, the process medium into the suction chamber of the pump and from there into the annulus of the pressure housing becomes. From the pressure chamber, the process medium is transported away via a corresponding pipeline.
  • the design of the module of pump and drive means in a common module housing has the advantage that the mechanically active element can be completely prefabricated and tested and only has to be inserted into an enclosing pressure housing. No mechanically moving parts have to be sealed off from the environment, but leaks can also occur inside the pump be harmless, since leaks are absorbed in the fully closed pressure housing. Only the efficiency can be reduced thereby.
  • the mechanically simple design of the pressure housing with the minimization of the interfaces and positive or non-positive bearings between the module housing and the pressure housing allow a very free choice in terms of material, the manufacturing process and the pressure stage of the pressure housing.
  • the number of seals to environments is minimized and limited to non-rotating seals.
  • the installation space for the seals is largely freely selectable.
  • module housing All mechanical functions of the underwater pumping unit are contained in the module housing. To test the function, only the module housing is needed. Since the module housing no longer has to absorb the pressure forces of the water column and the absolute process pressure, the dimensions and the weight can be reduced and the accessibility of components can be simplified. This also makes a complete functional test of the module with reduced effort possible.
  • the design of the pressure housing is independent of design conditions of the pump only in terms of maximum external and internal pressure, as well as the process and ambient temperature and the chemical composition of the process medium, whereas the module housing sufficient dimensional stability for the mechanical loads as well as a constant overpressure sufficient pressure balanced and the temperature fluctuations sufficiently resistant housing must form, which is largely decoupled from the deformations of the pressure housing and the external loads.
  • the module housing may be mounted in the pressure housing via vibration-damping bearings, such as rubber-metal bearings to transmit any noise emissions from the module housing to the pressure housing or to prevent transmission as possible.
  • vibration-damping bearings such as rubber-metal bearings to transmit any noise emissions from the module housing to the pressure housing or to prevent transmission as possible.
  • the figure shows a schematic sectional view of a delivery unit.
  • an underwater conveyor unit 1 with an outer pressure housing 2, which consists of two housing parts 21, 22, and a module housing 3 is arranged therein, wherein the module housing 3 receives a pump 31 and a drive means 32 with a coupling 33.
  • the drive device 32 and the coupling 33 are sealed by a barrier medium against penetration of a process medium.
  • the module housing 3 is mounted at its right end in a fixed bearing 24 of the second pressure housing part 22 and provided with bushings for electrical and hydraulic supply lines 5.
  • the pressure housing 31 is axially displaceably mounted in an inlet pipe 25, so that the left end of the module housing 3 is designed as a floating bearing.
  • two flanges 23, 26 are arranged, via which a connection to piping system can be made.
  • the module housing 3 is arranged in the pressure housing 2 such that an annular space 6 is formed around the module housing 3, which is filled with process medium.
  • the process medium is conveyed into the suction chamber 311 of the pump 31 and pumped from there through the pressure chamber 312 into the annular space 6, as indicated by the arrows. From the annular space 6, the process medium is then removed by the outlet port 26.
  • the pressure of the barrier medium is set specifically to the operating conditions.
  • a low constant overpressure usually between 1 and 25 bar from the barrier medium to the process medium in the pressure housing 2 is desired.
  • a constant pressure compensation of the entire module compared to the surrounding process pressure and a complete decoupling of the ambient pressure, ie the pressure of the water column is achieved.
  • the mechanical design of the module housing 3 can thereby be aligned to low, above all, to constant forces.
  • separation means such as diverters, labyrinths, or targeted cross-sectional enlargements may be provided to provide improved separation efficiency.
  • a short-circuit line can be led to the suction chamber 311 of the pump 31 in order to allow a recirculation of a separated liquid phase.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Structures Of Non-Positive Displacement Pumps (AREA)
  • Details Of Reciprocating Pumps (AREA)
  • Drilling And Exploitation, And Mining Machines And Methods (AREA)
EP20090730124 2008-04-10 2009-04-06 Unterwasserförderaggregat Not-in-force EP2265824B1 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE200810018407 DE102008018407B4 (de) 2008-04-10 2008-04-10 Unterwasserförderaggregat
PCT/DE2009/000470 WO2009124536A2 (de) 2008-04-10 2009-04-06 Unterwasserförderaggregat

Publications (2)

Publication Number Publication Date
EP2265824A2 EP2265824A2 (de) 2010-12-29
EP2265824B1 true EP2265824B1 (de) 2013-08-21

Family

ID=41060577

Family Applications (1)

Application Number Title Priority Date Filing Date
EP20090730124 Not-in-force EP2265824B1 (de) 2008-04-10 2009-04-06 Unterwasserförderaggregat

Country Status (9)

Country Link
US (1) US9103342B2 (da)
EP (1) EP2265824B1 (da)
CN (1) CN102037244B (da)
BR (1) BRPI0911323A2 (da)
CA (1) CA2721015C (da)
DE (1) DE102008018407B4 (da)
DK (1) DK2265824T3 (da)
RU (1) RU2498113C2 (da)
WO (1) WO2009124536A2 (da)

Cited By (1)

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CN111749905A (zh) * 2020-06-28 2020-10-09 金可友 一种护罩防损的潜水泵

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DE102010026239B4 (de) 2010-06-29 2012-05-31 Joh. Heinr. Bornemann Gmbh Unterwasserförderaggregat mit einer Pumpe und einer Antriebseinrichtung
DE102012015064B4 (de) 2012-07-31 2018-08-02 Joh. Heinr. Bornemann Gmbh Verfahren zum Betreiben einer Multiphasenpumpe und Vorrichtung dazu
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EP3134648B1 (en) 2014-04-22 2023-06-14 Project Phoenix, LLC Fluid delivery system with a shaft having a through-passage
EP3149343B1 (en) 2014-06-02 2020-06-17 Project Phoenix LLC Linear actuator assembly and system
WO2015187681A1 (en) 2014-06-02 2015-12-10 Afshari Thomas Hydrostatic transmission assembly and system
SG11201700472XA (en) 2014-07-22 2017-02-27 Project Phoenix Llc External gear pump integrated with two independently driven prime movers
US10072676B2 (en) 2014-09-23 2018-09-11 Project Phoenix, LLC System to pump fluid and control thereof
EP3204647B1 (en) 2014-10-06 2021-05-26 Project Phoenix LLC Linear actuator assembly and system
WO2016064569A1 (en) 2014-10-20 2016-04-28 Afshari Thomas Hydrostatic transmission assembly and system
DE102014017075B4 (de) * 2014-11-20 2017-11-02 Itt Bornemann Gmbh Vorrichtung zum Fördern eines Mediums
DE102014017072A1 (de) 2014-11-20 2016-05-25 Itt Bornemann Gmbh Vorrichtung zum Fördern eines Mediums
EP3344853B1 (en) 2015-09-02 2020-11-04 Project Phoenix LLC System to pump fluid and control thereof
EP3344874B1 (en) 2015-09-02 2021-01-20 Project Phoenix LLC System to pump fluid and control thereof
CN106082053B (zh) * 2016-08-25 2019-04-30 江苏科技大学 一种多单元水下垂直运输系统

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US6012909A (en) * 1997-09-24 2000-01-11 Ingersoll-Dresser Pump Co. Centrifugal pump with an axial-field integral motor cooled by working fluid
RU2208710C2 (ru) * 1997-10-13 2003-07-20 Маринокс Помпе ди Анголи Маргерита Насос с накопительным резервуаром
US6200108B1 (en) * 1998-03-11 2001-03-13 Aqua-Flo, Incorporated Heat exchanging means for a pump motor using a bypass tube within a recirculating water system
BR9903092C1 (pt) * 1999-06-22 2004-10-19 Anauger Motores Ind Ltd Aperfeiçoamento em bomba vibratória
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RU81471U1 (ru) 2008-12-01 2009-03-20 Федеральное Государственное образовательное учреждение высшего профессионального образования "Саратовский военный институт биологической и химической безопасности Министерства обороны Российской Федерации" (ФГОУ СВИБХБ МО РФ) Дистанционный беспилотный летательный аппарат для отбора проб жидкости

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111749905A (zh) * 2020-06-28 2020-10-09 金可友 一种护罩防损的潜水泵
CN111749905B (zh) * 2020-06-28 2021-09-28 金可友 一种护罩防损的潜水泵

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CA2721015A1 (en) 2009-10-15
RU2498113C2 (ru) 2013-11-10
WO2009124536A3 (de) 2010-04-29
BRPI0911323A2 (pt) 2015-09-29
DE102008018407A1 (de) 2009-10-15
RU2010145528A (ru) 2012-05-20
WO2009124536A2 (de) 2009-10-15
CA2721015C (en) 2016-03-29
CN102037244A (zh) 2011-04-27
DK2265824T3 (da) 2013-11-25
EP2265824A2 (de) 2010-12-29
US9103342B2 (en) 2015-08-11
CN102037244B (zh) 2014-04-30
US20110064592A1 (en) 2011-03-17
DE102008018407B4 (de) 2012-03-22

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