US20090321051A1 - Method and means for pumping in heat exchange applications - Google Patents

Method and means for pumping in heat exchange applications Download PDF

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Publication number
US20090321051A1
US20090321051A1 US12/296,203 US29620307A US2009321051A1 US 20090321051 A1 US20090321051 A1 US 20090321051A1 US 29620307 A US29620307 A US 29620307A US 2009321051 A1 US2009321051 A1 US 2009321051A1
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United States
Prior art keywords
heat exchanger
medium
pump
fan
periphery
Prior art date
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Abandoned
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US12/296,203
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English (en)
Inventor
Eva Gudmundsson
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Individual
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Individual
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Publication of US20090321051A1 publication Critical patent/US20090321051A1/en
Abandoned legal-status Critical Current

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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/06Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
    • F28F13/12Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media by creating turbulence, e.g. by stirring, by increasing the force of circulation
    • F28F13/125Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media by creating turbulence, e.g. by stirring, by increasing the force of circulation by stirring
    • 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
    • F04D29/58Cooling; Heating; Diminishing heat transfer
    • F04D29/582Cooling; Heating; Diminishing heat transfer specially adapted for elastic fluid pumps
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D11/00Heat-exchange apparatus employing moving conduits
    • F28D11/02Heat-exchange apparatus employing moving conduits the movement being rotary, e.g. performed by a drum or roller
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2250/00Arrangements for modifying the flow of the heat exchange media, e.g. flow guiding means; Particular flow patterns
    • F28F2250/08Fluid driving means, e.g. pumps, fans

Definitions

  • the present invention relates to ways and means to arrange pumping of medium, liquid or gases through a heat exchanger, which can have design to what is described in European patent 0586402 or another equipment, where powerful pumping of the media is acquired to the heat exchanger and also pumping from the heat exchanger.
  • the invention also relates to embodiment of the method, consisting of a rotating part comprising internal cavities that provides pumping and transport of gases or liquids.
  • One example of such applications where such pumps can be used are heat exchanger system in climate units for cooling of telecom stations or heat exchangers in heat recovery systems for real estates, cooling in climate units or other applications where pumping of two fluids, gases or liquids should be obtained in heat exchanger applications with high requirements of pressure performance.
  • heat exchanger can be arranged by embodiment with rotating disc surfaces and cavities between the disk surfaces such that heat exchange occurs between two or more medias, flowing in the cavities. Heat Exchange occurs, by heat transfer, from one medium to the other through the disc surfaces.
  • Primarily patent EU 0586402 embodiment or similar embodiments are characterized by cavities and rotating disc surfaces stacked at different axial levels along a rotating shaft. Heat-exchange basically occurs from one level along the rotating shaft to another level. The intention is that the media for each level with cavities can move along the disc surfaces basically in cavities.
  • said embodiment could be implemented in such a way that one media has a media-flow that, from the center channel inlet, enters a cavity between two rotating disc surfaces and, after passage of the cavity, exits the cavity in radial slots at the periphery, between two disc surfaces.
  • This flow is pumped out of the heat exchanger itself and for most cases does not need any further pump or fan device.
  • the other media flows, if the complicated rotating fluid mechanical movement is disregarded, mainly from periphery and radially inwards towards sector channels in centre, in cavities between disc surfaces.
  • This media or flow that passes from the periphery and towards the centre in the heat exchanger cavities has large pressure drop. It needs some highly efficient pump or fan device to overcome this pressure drop and make flow through heat exchanger possible.
  • a pump or fan wheel with the same diameter as the heat exchanger on the same shaft as the heat exchanger that has the same speed of rotation as the heat exchanger can not according to any known pumping technology achieve enough pumping pressure head to overcome the pressure drops for the passage in the heat exchanger cavities for commercially used flows in the heat exchanger.
  • a pumping wheel on the same shaft as the same heat exchanger must either have much higher speed of rotation, which is mechanically very complicated or be designed with much larger diameter, which require larger volume for the whole heat exchanger.
  • One third way is to arrange two pumping wheels which make pumping in series after each other or one pump before and one after passing the heat exchanger, which requires much bigger volume and makes the pumping system volume comparable with the heat exchanger as a whole. This reduces the advantages with heat exchanging according to patent EU 0586402.
  • the intention of the present invention is to eliminate the drawbacks listed above for pump or fan device in counter flow heat exchanger systems according to European patent EU 0586402 or similar, for the flow that passes heat exchange process in cavities between disc surfaces from periphery and radially inwards towards the center, with a method for pumping or as a pump or a fan device, that in one unit makes efficient pumping effect and pressure head for flow both before and also after passing the heat exchange process.
  • FIG. 1 illustrating an embodiment of the present invention with a rotating part, in combination with heat exchanger according to patent EU 0586402 or similar heat exchangers, the invention is illustrated in a side view parallel with the fan or pump embodiments rotation axis.
  • FIG. 2 illustrating a pump or fan embodiment according to it's mainly parts. The parts are seen in views from beneath the rotating part in FIG. 1 . At the top of the figure is the lid of the pump or fan embodiment. At the bottom is the pump or fan embodiment bottom. In between is a part with several cavities and barriers connecting lid and bottom. In this figure the two medium flows is also illustrated.
  • pumping embodiment or device means both fan and pump embodiment or device.
  • Medium means all types of fluids that can be gases or liquids where any of the gases can be air.
  • FIG. 1 an embodiment of a heat exchanger according to patent EU 0586402 or similar embodiments provided with the pump device according to the present invention is shown.
  • the heat exchanger comprises a rotating part 1 being symmetrical in rotation that can be revolved around an axis of rotation 2 by means of driving of an electrical engine or another driving arrangement.
  • the rotating part 1 consists of a package with several similar discs and stacked to each other axially along a shaft with cavities between discs.
  • the cavities in rotating part 1 communicate mutually such that they altogether are separated in two different volumes separated from each other.
  • One fluent medium in one volume cannot go into the other volume inside the heat exchanger package in rotating part 1 . Two different mediums can then be kept separated from each other in the rotating part 1 .
  • One of the flows enters in sector channels in centre of rotating part 1 and passes in each other cavity axially and leaves the heat exchanger at the periphery of rotating part 1 . This flow can be ignored for the innovation of the pump embodiment or device.
  • the other flow medium 3 that in the stack of heat exchanger enters the other cavities at the periphery passes the heat exchangers cavities mainly radially inwards towards the centre of the rotating part 1 and leaves the cavities in channels in the centre, which are connected to the special pump embodiment 16 , intended as the invention.
  • the medium 3 has, after heat exchange, thermodynamically changed its condition when it leaves the heat exchanger channels in the centre. It is then called medium 4 .
  • FIG. 2 shows the pump or wheel embodiment 16 earlier described with the different parts in views along rotational axis and from points beneath the rotating part 1 in FIG. 1 .
  • It consists of a lid 6 , middle part with barriers 8 , 9 and 19 and bottom part 10 .
  • the barriers 8 , 9 and 19 connect lid 6 and bottom 10 axially along rotational axis 2 .
  • Medium 3 is sucked into the pump or wheel 16 through sector holes 5 near the centre of the lid 6 .
  • the medium 3 is brought to rotate in cavities 7 by force from barriers 8 and 9 , which gives a pumping effect of medium 3 before it leaves pump and flows to openings 18 and enters into axial channels at the periphery of the heat exchangers stack in rotating part 1 .
  • the cavities 7 are enclosed between the pumping wheel lid 6 and radially formed or almost radially formed walls 8 , 9 and barrier 19 at the periphery and also pumping wheel bottom 10 , with exceptions of openings 5 and 18 .
  • a pipe system can also connect the sector formed holes 5 in the pumping wheel lid 6 and the axial channels 18 in pumping wheel bottom 10 with similar physical effect regarding fluid dynamics and pumping effect.
  • the turbine formed vanes for the walls 8 and 9 according to FIG. 2 can be replaced by a straight radial form or another curved form.
  • the conditions for fluid dynamics and speed of rotation will determine what curve form that is the most optimal for the special case.
  • FIG. 2 shows also how medium 4 , the medium that is heat exchanged in heat exchanger stack in rotating part 1 , enters pump or fan 16 from heat exchanger through sector formed openings 11 in the centre of bottom 10 . It is further guided in cavities 12 to be brought to rotation by force from barriers 8 and 9 once more and leaves the pumping wheel through pump or fan wheel openings 13 at the periphery. Medium 4 gets with this bringing to rotation, so called pressure head, which also contributes to the sucking capacity of medium 4 from the centre channels 11 . Barriers 8 , 9 and 19 between lid 6 and bottom 10 prevent that medium 4 is mixed with medium 3 .
  • the medium 4 gets its force to rotation from the sides of barrier 8 and 9 which is exposed to cavity 12 .
  • the medium 3 gets its force to rotation from the sides of barrier 8 and 9 which is exposed to cavity 7 .
  • the space 14 in FIG. 1 with medium 4 flowing from rotating part 1 is kept separate from the space 15 outside rotating part 1 by a sealing 17 between rotating part 1 and stator parts 20 outside rotating part 1 .
  • This sealing 17 is a barrier between the spaces 14 and 15 and connects with no gap, a small gap or very small gap between rotating part 1 and the stator parts 20 that are radially outside rotating part 1 .
  • FIG. 1 A similar sealing 21 FIG. 1 exists between inlet to the pumping wheel lid 6 and the stator 20 around the pumping wheel 16 and rotating part 1 .
  • the purpose of this sealing 21 is to separate medium 3 and medium 4 from each other, actually the same medium that has changed thermally condition.
  • the sealing 21 can be of the same type as 17 .
  • sealings for both 17 and 21 can be in the market existing common axial seals, radial seals, lip seals, labyrinth seals or another form that combines a rotating part with a stator part. It shall a accomplish separation between spaces for different mediums around rotating parts.
  • the two pump wheels with the same diameter as the disc stack in rotating part 1 should require more than 50% of the volume of the disc stack in the heat exchanger.
  • the properties of the invention makes it possible that pump or fan wheel embodiment 16 with its double functioning pump effect can make the intentional pumping effect that is required for this type of heat exchanger in only one pump or fan wheel 16 .
  • big advantages are achieved with design that is much more volume effective than with two pumping wheels.
  • the pumping wheel 16 has also less details and is also simpler to produce than two separate pumping wheels which also reduce cost for the total design.
  • the inflow of medium 3 goes to the centre hole in stator enclosure 20 .
  • the outflow of medium 4 goes also out in the lower part of stator enclosure 20 and can be separated from the environment and among that the medium which the heat is exchanged to. It is necessary for certain heat exchange applications, for example cooling of outdoor telecom stations where separation from outdoor environment is necessary for the air that is inside the station. With that arrangement complicated channel systems outside the heat exchanger system can be avoided.
  • the invention is not limited only for use connected with heat exchange according to patent EU 0586402 or similar embodiments.
  • the described invention can also be used where pumping to medium flows is needed in the same rotating unit.
  • the described embodiments with sealings 17 and 20 which are described between the rotating pumping wheel and the stator enclosure 20 is an essential to separate the two media flows and eventually other environmental medium of other kinds.
  • the various described and shown embodiments, but variations thereof are naturally possible within the scope of claim 1 .

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Structures Of Non-Positive Displacement Pumps (AREA)
US12/296,203 2006-04-07 2007-04-05 Method and means for pumping in heat exchange applications Abandoned US20090321051A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
SE0600785A SE0600785L (sv) 2006-04-07 2006-04-07 Sätt och anordning för två medier i en enhet
SE0600785-0 2006-04-07
PCT/SE2007/000328 WO2007117194A1 (en) 2006-04-07 2007-04-05 Method and means for pumping in heat exchange applications

Publications (1)

Publication Number Publication Date
US20090321051A1 true US20090321051A1 (en) 2009-12-31

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US12/296,203 Abandoned US20090321051A1 (en) 2006-04-07 2007-04-05 Method and means for pumping in heat exchange applications

Country Status (5)

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US (1) US20090321051A1 (sv)
EP (1) EP2005099A1 (sv)
CN (1) CN101416014A (sv)
SE (1) SE0600785L (sv)
WO (1) WO2007117194A1 (sv)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8491277B2 (en) * 2010-02-12 2013-07-23 Ebara Corporation Submersible motor pump, motor pump, and tandem mechanical seal
CN108444319B (zh) * 2018-05-03 2023-12-15 株洲智热技术有限公司 一种空间旋转设备水冷散热的换热方法及换热器
US11149994B2 (en) * 2019-01-08 2021-10-19 Haier Us Appliance Solutions, Inc. Uneven flow valve for a caloric regenerator

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2596622A (en) * 1944-09-25 1952-05-13 Vannerus Torbjorn Recuperative heat exchanger of the counterflow type for gaseous media
US3563710A (en) * 1968-02-16 1971-02-16 Monsanto Co Polymerization apparatus
US3844341A (en) * 1972-05-22 1974-10-29 Us Navy Rotatable finned heat transfer device
US5117655A (en) * 1991-08-12 1992-06-02 Anderson Raymond L Heat exchanger
US6290216B1 (en) * 1997-04-19 2001-09-18 Interotex Limited Rotary heat and/or mass transfer arrangements

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE875386C (de) * 1942-04-28 1953-05-04 Motala Verkst Ab Rekuperativer Waermeaustauscher fuer gasfoermige Mittel
JPS51137946A (en) * 1975-05-26 1976-11-29 Toyo Radiator Kk Multi-layor rotary heat exchanger
SE517219C2 (sv) * 1991-04-17 2002-05-07 Bjoern Gudmundsson Sätt och anordning för värme eller massöverföring

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2596622A (en) * 1944-09-25 1952-05-13 Vannerus Torbjorn Recuperative heat exchanger of the counterflow type for gaseous media
US3563710A (en) * 1968-02-16 1971-02-16 Monsanto Co Polymerization apparatus
US3844341A (en) * 1972-05-22 1974-10-29 Us Navy Rotatable finned heat transfer device
US5117655A (en) * 1991-08-12 1992-06-02 Anderson Raymond L Heat exchanger
US6290216B1 (en) * 1997-04-19 2001-09-18 Interotex Limited Rotary heat and/or mass transfer arrangements

Also Published As

Publication number Publication date
WO2007117194A1 (en) 2007-10-18
SE0600785L (sv) 2007-10-08
EP2005099A1 (en) 2008-12-24
CN101416014A (zh) 2009-04-22

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