EP1996888B1 - Échangeur thermique pour véhicule automobile - Google Patents

Échangeur thermique pour véhicule automobile Download PDF

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Publication number
EP1996888B1
EP1996888B1 EP07723149.6A EP07723149A EP1996888B1 EP 1996888 B1 EP1996888 B1 EP 1996888B1 EP 07723149 A EP07723149 A EP 07723149A EP 1996888 B1 EP1996888 B1 EP 1996888B1
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EP
European Patent Office
Prior art keywords
flow path
flow
heat exchanger
exchanger according
ducts
Prior art date
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Application number
EP07723149.6A
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German (de)
English (en)
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EP1996888A1 (fr
Inventor
Christian Domes
Peter Geskes
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Mahle Behr GmbH and Co KG
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Mahle Behr GmbH and Co KG
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Publication of EP1996888A1 publication Critical patent/EP1996888A1/fr
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Classifications

    • 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
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/16Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation
    • F28D7/1684Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation the conduits having a non-circular cross-section
    • F28D7/1692Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation the conduits having a non-circular cross-section with particular pattern of flow of the heat exchange media, e.g. change of flow direction
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02MSUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M26/00Engine-pertinent apparatus for adding exhaust gases to combustion-air, main fuel or fuel-air mixture, e.g. by exhaust gas recirculation [EGR] systems
    • F02M26/13Arrangement or layout of EGR passages, e.g. in relation to specific engine parts or for incorporation of accessories
    • F02M26/22Arrangement or layout of EGR passages, e.g. in relation to specific engine parts or for incorporation of accessories with coolers in the recirculation passage
    • F02M26/23Layout, e.g. schematics
    • F02M26/25Layout, e.g. schematics with coolers having bypasses
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02MSUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M26/00Engine-pertinent apparatus for adding exhaust gases to combustion-air, main fuel or fuel-air mixture, e.g. by exhaust gas recirculation [EGR] systems
    • F02M26/13Arrangement or layout of EGR passages, e.g. in relation to specific engine parts or for incorporation of accessories
    • F02M26/22Arrangement or layout of EGR passages, e.g. in relation to specific engine parts or for incorporation of accessories with coolers in the recirculation passage
    • F02M26/29Constructional details of the coolers, e.g. pipes, plates, ribs, insulation or materials
    • F02M26/32Liquid-cooled heat exchangers
    • 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
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/0066Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids
    • F28D7/0075Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids with particular circuits for the same heat exchange medium, e.g. with the same heat exchange medium flowing through sections having different heat exchange capacities or for heating or cooling the same heat exchange medium at different temperatures
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/02Tubular elements of cross-section which is non-circular
    • F28F1/022Tubular elements of cross-section which is non-circular with multiple channels
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/02Tubular elements of cross-section which is non-circular
    • F28F1/04Tubular elements of cross-section which is non-circular polygonal, e.g. rectangular
    • 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
    • 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
    • F28F13/14Arrangements for modifying heat-transfer, e.g. increasing, decreasing by endowing the walls of conduits with zones of different degrees of conduction of heat
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F27/00Control arrangements or safety devices specially adapted for heat-exchange or heat-transfer apparatus
    • F28F27/02Control arrangements or safety devices specially adapted for heat-exchange or heat-transfer apparatus for controlling the distribution of heat-exchange media between different channels
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/02Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
    • F28F3/04Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element
    • F28F3/042Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element in the form of local deformations of the element
    • F28F3/044Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element in the form of local deformations of the element the deformations being pontual, e.g. dimples
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02MSUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M26/00Engine-pertinent apparatus for adding exhaust gases to combustion-air, main fuel or fuel-air mixture, e.g. by exhaust gas recirculation [EGR] systems
    • F02M26/50Arrangements or methods for preventing or reducing deposits, corrosion or wear caused by impurities
    • 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
    • F28D21/00Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D21/0001Recuperative heat exchangers
    • F28D21/0003Recuperative heat exchangers the heat being recuperated from exhaust gases
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2215/00Fins
    • F28F2215/04Assemblies of fins having different features, e.g. with different fin densities
    • 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
    • F28F2250/06Derivation channels, e.g. bypass

Definitions

  • the present invention relates to a heat exchanger for a motor vehicle according to the preamble of claim 1.
  • the document JP2001027157 discloses in Figures 4 and 5 such a heat exchanger.
  • the fluid is the exhaust gas of an internal combustion engine of the motor vehicle.
  • a particularly large temperature difference of typically several 100 ° C is achieved in the fluid cooling, so that the adjustment of the flow resistance of the two downstream flow paths in the course of cooling of the exhaust gas is particularly effective.
  • the first flow path has a smaller flow resistance than the second flow path.
  • the region of the first flow path on average there is a higher temperature difference to the coolant than in the region of the second flow path.
  • a high cooling capacity is already given due to the temperature difference. Due to the temperature of at least gaseous fluids, high pressure losses are present anyway in this region, so that the flow resistance, in particular the generation of turbulence to improve the heat transfer, can be kept relatively small in the first flow path.
  • the fluid is already partially cooled, so that in the second flow path to obtain a sufficient heat transfer advantageously a greater flow resistance, in particular a larger proportion of turbulent flows, is present. In this way, an overall optimization of the heat exchanger performance is achieved taking into account the lowest possible total pressure drop across the heat exchanger.
  • turbulence-generating means are provided in at least one of the two flow paths, whereby the heat exchanger performance is improved.
  • the turbulence-generating means are formed as protruding into the flow path formations of walls of the flow path. These may be dimples or so-called " winglets" (V-shaped aligned embossed webs).
  • the turbulence-generating means may also be deposits defined in the flow path. Such inserts may be, for example, rib ribs or corrugated ribs or the like.
  • all turbulence-generating agents which are known from the prior art are suitable for the purposes of the present invention. What is essential is only the different design of the flow resistances in the first flow path and in the second flow path.
  • ribs are arranged to increase a contact area with the fluid, wherein the ribs in the first flow path and in the second flow path have a different density. Even in a case where, for example, are longitudinal ribs such as corrugated fins, in which predominantly laminar and less turbulent flows are formed, a different density of the ribs leads to different flow resistances.
  • the flow resistances of the flow paths can therefore be influenced in principle both by generating turbulences and by influencing laminar flow fractions.
  • first flow path and the second flow path may each comprise a plurality of separate, parallel flow channels.
  • the number of channels of the first flow path is different, in particular smaller, than the number of channels of the second flow path.
  • the channels of the first flow path can each have a different, in particular larger, cross-sectional area than the channels of the second flow path.
  • the channels of a flow path have different flow resistances among one another.
  • the flow resistance of an outer channel with respect to the deflection region is greater than the flow resistance of an inner channel of the same flow path.
  • the first flow path preferably has a different, in particular larger, free cross-sectional area than the second flow path.
  • free cross-sectional area is meant the geometric cross-sectional area for free flow of the fluid.
  • the flow paths are arranged in a housing through which the coolant flows.
  • the coolant is advantageously a liquid, in particular cooling liquid of a main cooling circuit of the motor vehicle. As a result, an overall effective cooling of the fluid is ensured.
  • the heat exchanger comprises a connection region with a first connection for supplying the fluid to the first flow path and a second connection for discharging the fluid from the second flow path, thereby enabling a compact and cost-saving design of the heat exchanger.
  • an adjusting element is provided in the connection region, by means of which a direct connection of the first connection and the second connection for bypassing the flow paths is selectably adjustable. This makes it possible to bypass the cooling of the fluid selectable, which is desired especially in internal combustion engines of motor vehicles under certain operating conditions such as the warm-up phase of the engine.
  • the flow paths and / or the flow channels are made of aluminum.
  • the flow paths and / or the flow channels are made of stainless steel.
  • the flow paths and / or the flow channels are made of aluminum and stainless steel.
  • the fluid is exhaust gas of an internal combustion engine of the motor vehicle.
  • turbulence-generating means are formed as defined in the flow path deposits.
  • the flow paths are arranged in a housing through which the coolant flows.
  • the flow paths in particular the flow channels made of aluminum and / or stainless steel are formed.
  • Fig. 1 shows a U-flow heat exchanger for cooling recirculated exhaust gas of a motor vehicle diesel engine, in which a first flow path 1 and a second flow path 2 are arranged in parallel and side by side within a housing 3.
  • the housing 3 is flowed through by means of two ports 4, 5 of a liquid coolant, which is branched off from a main cooling circuit of the diesel engine.
  • the flow paths 1, 2 each comprise a number of flow channels 6, 7, which in the present case are designed as flat tubes with a rectangular cross-section.
  • the cross section can in principle also have another, approximately round, shape.
  • the connection region 8 has a first connection 9 for supplying exhaust gas of a diesel engine of the motor vehicle and a second connection 10 for discharging the cooled exhaust gas.
  • a control element 11 designed as a pivotable flap is provided, which is adjustable via a rotary shaft 12.
  • the exhaust gas is passed from the first port 9 in the first flow path 1, where it first undergoes a first cooling. After flowing through the first flow path 1, the exhaust gas enters a deflecting region 13 arranged at the end of the housing 3.
  • the deflection region 13 here is a substantially semi-cylindrical, hollow housing part, in which the exhaust gas flow is deflected by 180 °, after which it enters the second flow path 2.
  • the second flow path 2 flows through the exhaust gas in the opposite direction to the first flow path 1, wherein it undergoes a further cooling.
  • When leaving the second Flow path 2 enters the exhaust gas again in the connection area 8, where it in the case of the first position of the actuating element 11 according to Fig. 1 is guided in the second terminal 10.
  • each of the flow paths 1, 2 comprises a bundle of nine flow channels 6, 7 each of rectangular cross-section.
  • the outer dimensions of the flow channels 6, 7 are each identical.
  • the flow channels 6 of the first flow path 1 and the flow channels 7 of the second flow path 2 turbulence generating means in the form of indentations 6a, 7a, which have a different size.
  • the impressions 6a of the first flow channels 6 protrude less deeply into the channel cross section than the impressions 7a of the second flow channels 7. In this way, the geometric free flow cross section of the second flow channels 7 becomes smaller compared to the geometric free cross section of the first flow channels 6.
  • more turbulence is introduced into the exhaust gas flow in the second flow channels 7 through the deeper protruding turbulence-generating means 7a than in the first flow channels 6.
  • the turbulence-generating means 6a, 7a can be dimples and / or winglets. Alternatively or in addition, it may also be in itself act known structured deposits, which are inserted into the flow channels 6, 7 and welded.
  • the second heat exchanger In the second heat exchanger according to Fig. 3 is the first flow path 1 as well as constructed in the first heat exchanger.
  • the second flow path 2 In contrast to the first heat exchanger, the second flow path 2 not only has different turbulence-generating means 7a, but also has a smaller number of flow channels 7 than the first flow path 1, which have a different outer dimension relative to the flow channels 6 of the first flow path 1.
  • the second flow path comprises fewer flow channels 7 with a larger external dimension, a greater flow resistance is generated for the second flow path 2 by the deeper projecting turbulence-generating means 7a than for the first flow path 1. Due to the changed number and outer geometry of the flow channels 7 the flow resistance of the second flow path in the second embodiment is slightly smaller than the flow resistance of the second flow path in the first heat exchanger.
  • each of the flow paths 1, 2 each have three parallel flat tubes 6, 7 as flow channels, each having identical outer dimensions.
  • the flow channels 6, 7 are provided with rib-like inserts 6b, 7b, whereby the contact area between the exhaust gas flow and heat-conducting metal is increased.
  • fewer fins are provided in the case of the flow channels 6 of the first flow path 1 than in the case of the flow channels 7 of the second flow path 2. Due to the greater fin density of the second flow path 2 with otherwise identical dimensions and numbers the flow channels 6, 7, the second flow path 2 has a greater flow resistance than the first flow path 1.
  • the embodiment illustrates that even with predominantly laminar flows by appropriate design of the flow channels 6, 7 different flow resistance can be generated.
  • the fluid to be cooled is in particular exhaust gas.
  • the fluid to be cooled charge air, oil, especially transmission oil, a water-containing cooling liquid, refrigerant of an air conditioner such as CO2.
  • the heat exchanger is at least one exhaust gas cooler.
  • the heat exchanger is at least one intercooler and / or an oil cooler and / or a coolant radiator and / or a condenser of an air conditioner and / or an evaporator of an air conditioner and / or a gas cooler of an air conditioner.
  • the heat exchanger is a combination of at least one exhaust gas cooler and at least one other of the aforementioned heat exchangers.
  • the heat exchanger has a flow resistance of the flow path 1, which is between 0.1% and 300%, in particular between 1% and 100%, in particular between 5% and 80%, between 10% and 70%, between 20 % and 60%, between 30% and 50% is above the flow resistance of the flow path 2, preferably only 10% above the flow resistance of the flow path. 2
  • the flow resistance of the first flow path 1 is below the flow resistance of the flow path 2.
  • Heat exchangers with a deflection region 13 are referred to as U-flow heat exchangers, since the fluid to be cooled flows in a first flow path as far as a deflection section and flows back in a first flow path in the first flow path after deflection in a second flow path substantially in the opposite direction.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Thermal Sciences (AREA)
  • Geometry (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Claims (14)

  1. Echangeur de chaleur pour un véhicule automobile, comprenant un carter, une première voie d'écoulement (1), une zone de retour de flux (13) disposée en aval de la première voie d'écoulement (1), et comprenant une seconde voie d'écoulement (2) disposée en aval de la zone de retour de flux (13), où le carter est traversé par un moyen de refroidissement, et les voies d'écoulement sont disposées dans le carter, où la première et la seconde voie d'écoulement (1, 2) sont traversées par un fluide à refroidir, et où la première et la seconde voie d'écoulement (1, 2) sont baignées par le moyen de refroidissement servant à la dissipation de la chaleur, où la seconde voie d'écoulement (2) présente une résistance d'écoulement différente de celle de la première voie d'écoulement (1), caractérisé en ce que des nervures (6b, 7b) sont disposées dans les voies d'écoulement (1, 2), lesdites nervures servant à augmenter une surface de contact avec le fluide, où les nervures (6b, 7b) présentent une densité différente dans la première voie d'écoulement (1) et dans la seconde voie d'écoulement (2).
  2. Echangeur de chaleur selon la revendication 1, caractérisé en ce que la première voie d'écoulement (1) présente une résistance d'écoulement plus faible que celle de la seconde voie d'écoulement (2).
  3. Echangeur de chaleur selon la revendication 1 ou 2, caractérisé en ce que la première voie d'écoulement (1) présente une résistance d'écoulement plus forte que celle de la seconde voie d'écoulement (2).
  4. Echangeur de chaleur selon l'une quelconque des revendications précédentes, caractérisé en ce que des moyens (6a, 7a) produisant des turbulences sont prévus dans au moins l'une des deux voies d'écoulement (1, 2).
  5. Echangeur de chaleur selon la revendication 4, caractérisé en ce que les moyens (6a, 7a) produisant des turbulences sont conçus comme des parties saillantes de parois de la voie d'écoulement, lesdites parties saillantes pénétrant dans le canal d'écoulement (6, 7).
  6. Echangeur de chaleur selon l'une quelconque des revendications précédentes, caractérisé en ce que la première voie d'écoulement (1) et la seconde voie d'écoulement (2) comprennent respectivement une pluralité de conduits d'écoulement (6, 7) parallèles et séparés.
  7. Echangeur de chaleur selon la revendication 6, caractérisé en ce que le nombre des conduits (6) de la première voie d'écoulement est différent, en particulier inférieur au nombre des conduits (7) de la seconde voie d'écoulement.
  8. Echangeur de chaleur selon l'une des revendications 6 ou 7, caractérisé en ce que les conduits (6) de la première voie d'écoulement présentent à chaque fois une surface de section transversale différente, en particulier plus grande que celle des conduits (7) de la seconde voie d'écoulement.
  9. Echangeur de chaleur selon l'une quelconque des revendications 6 à 8, caractérisé en ce que les conduits (6, 7) d'une voie d'écoulement présentent des résistances d'écoulement différentes les unes des autres.
  10. Echangeur de chaleur selon la revendication 9, caractérisé en ce que la résistance d'écoulement d'un conduit se trouvant à l'extérieur par rapport à la zone de retour de flux (13) est plus importante que la résistance d'écoulement d'un conduit de la même voie d'écoulement, ledit conduit se trouvant à l'intérieur.
  11. Echangeur de chaleur selon l'une quelconque des revendications précédentes, caractérisé en ce que la première voie d'écoulement (1) présente une surface de section transversale libre qui est différente, en particulier plus grande par rapport à celle de la seconde voie d'écoulement (2).
  12. Echangeur de chaleur selon l'une quelconque des revendications 1 à 11, caractérisé en ce que le moyen de refroidissement est un liquide, en particulier un liquide de refroidissement d'un circuit de refroidissement principal du véhicule automobile.
  13. Echangeur de chaleur selon l'une quelconque des revendications précédentes, comprenant en outre une zone de raccordement (8) comportant un premier raccord (9) destiné à la conduite d'alimentation du fluide fourni à la première voie d'écoulement (1) et un second raccord (10) servant à l'évacuation du fluide provenant de la seconde voie d'écoulement (2).
  14. Echangeur de chaleur selon la revendication 13, caractérisé en ce que la zone de raccordement (8) comprend un actionneur (11) au moyen duquel une connexion directe du premier raccord (9) et du second raccord (10) peut être réglée de manière sélective pour le contournement des voies d'écoulement (1, 2).
EP07723149.6A 2006-03-10 2007-03-09 Échangeur thermique pour véhicule automobile Active EP1996888B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102006011592 2006-03-10
PCT/EP2007/002084 WO2007104491A1 (fr) 2006-03-10 2007-03-09 Échangeur thermique pour véhicule automobile

Publications (2)

Publication Number Publication Date
EP1996888A1 EP1996888A1 (fr) 2008-12-03
EP1996888B1 true EP1996888B1 (fr) 2019-07-24

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Family Applications (1)

Application Number Title Priority Date Filing Date
EP07723149.6A Active EP1996888B1 (fr) 2006-03-10 2007-03-09 Échangeur thermique pour véhicule automobile

Country Status (5)

Country Link
US (1) US8573286B2 (fr)
EP (1) EP1996888B1 (fr)
CN (1) CN101400960B (fr)
DE (1) DE102007011953A1 (fr)
WO (1) WO2007104491A1 (fr)

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DE10333577A1 (de) * 2003-07-24 2005-02-24 Bayer Technology Services Gmbh Verfahren und Vorrichtung zur Entfernung von flüchtigen Substanzen aus hochviskosen Medien
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DE102008018594A1 (de) * 2007-04-11 2008-10-16 Behr Gmbh & Co. Kg Wärmetauscher
FR2923859B1 (fr) * 2007-11-15 2009-12-18 Valeo Systemes Thermiques Branche Thermique Habitacle Echangeur de chaleur pour circuit d'alimentation en air d'un moteur de vehicule automobile
US20110100342A1 (en) * 2009-11-02 2011-05-05 International Engine Intellectual Property Company Llc Forced convection egr cooling system
DE102011007748A1 (de) * 2011-04-20 2012-10-25 Behr Gmbh & Co. Kg Abgaskühler zum Kühlen von Verbrennungsabgas einer Verbrennungskraftmaschine, Wassersammeladapter, Abgaskühlsystem und Verfahren zum Herstellen eines Abgaskühlsystems
WO2013085771A1 (fr) * 2011-12-08 2013-06-13 Carrier Corporation Procédé et appareil de formation de tubes d'échangeur de chaleur
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DE102007011953A1 (de) 2007-11-15
US20090090495A1 (en) 2009-04-09
WO2007104491A1 (fr) 2007-09-20
US8573286B2 (en) 2013-11-05
EP1996888A1 (fr) 2008-12-03
CN101400960A (zh) 2009-04-01
CN101400960B (zh) 2010-12-29

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