EP3430341A1 - Wärmetauscher und zugehöriges herstellungsverfahren - Google Patents

Wärmetauscher und zugehöriges herstellungsverfahren

Info

Publication number
EP3430341A1
EP3430341A1 EP17716946.3A EP17716946A EP3430341A1 EP 3430341 A1 EP3430341 A1 EP 3430341A1 EP 17716946 A EP17716946 A EP 17716946A EP 3430341 A1 EP3430341 A1 EP 3430341A1
Authority
EP
European Patent Office
Prior art keywords
heat exchanger
tubes
separating wall
flow
cover
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.)
Withdrawn
Application number
EP17716946.3A
Other languages
English (en)
French (fr)
Inventor
Kamel Azzouz
Benjamin Ferlay
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.)
Valeo Systemes Thermiques SAS
Original Assignee
Valeo Systemes Thermiques SAS
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 Valeo Systemes Thermiques SAS filed Critical Valeo Systemes Thermiques SAS
Publication of EP3430341A1 publication Critical patent/EP3430341A1/de
Withdrawn legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02Header boxes; End plates
    • F28F9/026Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
    • F28F9/028Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits by using inserts for modifying the pattern of flow inside the header box, e.g. by using flow restrictors or permeable bodies or blocks with channels
    • 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
    • F28D1/00Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
    • F28D1/02Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
    • F28D1/04Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits
    • F28D1/053Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being straight
    • F28D1/05316Assemblies of conduits connected to common headers, e.g. core type radiators
    • F28D1/05325Assemblies of conduits connected to common headers, e.g. core type radiators with particular pattern of flow, e.g. change of flow direction
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02Header boxes; End plates
    • F28F9/026Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
    • F28F9/0263Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits by varying the geometry or cross-section of header box
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02Header boxes; End plates
    • F28F9/026Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
    • F28F9/0265Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits by using guiding means or impingement means inside the header box
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02Header boxes; End plates
    • F28F9/026Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
    • F28F9/0282Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits by varying the geometry of conduit ends, e.g. by using inserts or attachments for modifying the pattern of flow at the conduit inlet or outlet
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2270/00Thermal insulation; Thermal decoupling
    • F28F2270/02Thermal insulation; Thermal decoupling by using blind conduits

Definitions

  • the invention relates to a heat exchanger, in particular for a motor vehicle, and its method of manufacture.
  • the heat exchanger comprises a manifold for distributing and / or receiving the fluid circulating within the tubes.
  • a manifold or even both manifolds have a divider wall that defines two compartments. This is particularly the case for heat exchangers having a U-shaped fluid circulation where a first manifold comprises a separating wall, a first compartment for the arrival of fluid and a second compartment for the evacuation of the fluid, the second collector being closed and only redirect the fluid from the first compartment to the second compartment.
  • This is also the case for dual circulation heat exchangers, where two different fluids or different fluids circulate in different compartments.
  • each manifold has a separating wall and comprises two compartments in which separate fluids circulate.
  • the present invention therefore relates to a heat exchanger comprising: a bundle of tubes,
  • a manifold having a manifold plate comprising holes in which are inserted the ends of the tubes, and a cover covering said collecting plate, and
  • a partition wall disposed in at least one manifold, said partition wall defining two compartments within said manifold, said cover having at least one flow restrictor from position at least partially above the end of at least one of tubes located at the direct periphery of the separating wall.
  • the lid comprises two flow restrictors disposed on either side of the separating wall.
  • the tube or tubes located at the direct periphery of the separating wall have a fluid flow rate between 0 and 20, preferably between 1 and 10, of their theoretical flow.
  • the flow restrictor comes from material with the lid.
  • the dividing wall comes from material with the lid.
  • the lid comprises a recess directed towards the header plate, said recess forming the flow reducer (s) and the separating wall.
  • the flow restrictor comprises a lateral projection of the separating wall.
  • the flow restrictor has a length such that it is positioned only above the tube located at the direct periphery of the separating wall.
  • the flow restrictor has a length such that it is positioned above at least the first two tubes located at the direct periphery of the separating wall.
  • the distance between the end of a tube above which the flow restrictor is positioned and said restrictor increases as said tube is moved away from the separating wall.
  • FIG. 1 is a schematic sectional representation of a heat exchanger according to a first embodiment
  • FIG. 2 is a diagrammatic representation in section of the zone of the collector comprising the separating wall according to a particular embodiment
  • FIG. 3 is a diagrammatic representation in section of the zone of the collector comprising the separating wall according to another particular embodiment
  • FIG. 4 is a diagrammatic sectional representation of a heat exchanger according to a second embodiment
  • FIG. 5 is a diagrammatic sectional representation of a heat exchanger according to a third embodiment
  • FIG. 6 is a schematic representation in section of a variant of the heat exchanger of FIG. 5.
  • the heat exchanger 1 shown in FIGS. 1 to 6 comprises a bundle 2 formed of a multiplicity of tubes 20 within which a first fluid can circulate.
  • the tubes 20 are arranged parallel to each other. Between the tubes 20, interleaves 21 are arranged which act as a disrupter and increase the heat exchange surface with a second fluid passing between said tubes 20.
  • the tubes 20 and the spacers 21 are preferably made of metal materials and are brazed between them in order to form the beam 2. Having a brazed beam 2 improves the thermal performance, ie the heat exchange between the two heat transfer fluids, compared to a mechanically assembled beam.
  • the tubes 20 preferably have, in cross section, an oblong and relatively flat shape or a substantially rectangular shape with rounded corners.
  • the heat exchanger 1 also comprises two collectors 3, or water boxes, disposed at each end of the bundle 2.
  • These collectors 3 comprise a header plate 31 and a cover 32, 32 'coming to cover said header plate 31 and close the collector 3.
  • the seal between the cover 32, 32 'and the collector plate 31 can in particular be made by a seal 4.
  • These collectors 3 allow the collection and / or distribution of the first fluid so that it circulates in the tubes 20.
  • the collecting plate 31 makes the connection sealingly between the collector 3 and the bundle 2.
  • Said collector plate 31 comprises a core, which may be of generally rectangular shape, delimiting a multiplicity of holes of section corresponding to the shape of the section of the tubes. 20 and adapted to receive the ends of said tubes 20. As illustrated in FIGS.
  • the heat exchanger 1 comprises two collectors 3, at least one of them has a separating wall 33 defining two compartments 37a and / or 37b within said collector 3.
  • Each compartment 37a has an inlet 30a and each compartment 37b has a fluid outlet 30b.
  • the separating wall 33 connects the cover 32 and the collector plate 31 and bears against the collector plate 31 between two ends of tubes 20.
  • the seal of this support can be provided by a seal 4 '.
  • Said separating wall 33 may in particular be integral with the cover 32.
  • the cover 32 of the manifold 3 comprising the separating wall 33 also comprises at least one flow restrictor 34 which is positioned at least partially above the end of the at least one of the tubes 20 located at the direct periphery of the separating wall 33, so as to reduce the flow rate of fluid flowing in said tubes 20.
  • This reduction in the flow rate of the fluid at this level makes it possible to reduce the temperature difference between the tubes 20 located on either side of the partition wall 33 in its direct periphery.
  • the thermal shock at this level is therefore less important and the heat exchanger 1 is therefore less likely to deteriorate at the separating wall 33.
  • the fact of integrating the flow restrictor or 34 to the lid 32 allows in particular to facilitate the mounting of the heat exchanger 1. Indeed the said flow restrictor or 34 are installed by the introduction of the cover 32 and do not require a dedicated implementation step.
  • the cover 32 may comprise two flow restrictors 34 disposed on either side of the separating wall 33.
  • the fact of having a flow restrictor 34 on each side of the separating wall 33 allows a better reduction of the flow of the fluid within the tubes 20 located on either side of the separator plate 33 and above which is positioned a flow reducer 34.
  • a cover 32 having only one flow restrictor 34 located on only one side of the collecting wall 33 as shown in Figures 5 and 6.
  • the Flow reducers 34 may also be integral with the cover 32, as well as the separating wall 33.
  • the cover 32, the separating wall 31 and the flow restrictor (s) 34 may be formed in one go, by example by molding.
  • the or the flow restrictors 34 are made of material with only the cover 32, the partition wall 33 being an insert and installed during assembly to separate the compartments 37a and / or 37b.
  • the cover 32 may comprise a recess 35 directed towards the collecting plate 31.
  • This recess 35 allows the wall of the cover 32 to approach the collecting plate 31 so as to form the reduction gearbox. flow 34. Said recess 35 is extended until it bears on the collector plate 31 so as to also form the separating wall 33, as illustrated in FIGS. 1, 2 and 4.
  • the flow reducer 34 may comprise a lateral projection of the separating wall 33 as illustrated in FIGS. 3, 5 and 6.
  • the flow restrictor 34 extends a length L from the partition wall 33.
  • This length L may be such that at least the first two tubes 20 located at the direct periphery of the partition wall 33 have a flow restrictor 34 is positioned above them, as shown in Figure 2.
  • the length L may instead be such that only the first tube 20 located at the direct periphery of the partition wall 33 has a flow restrictor 34 positioned above him, as shown in Figure 3.
  • the tube or tubes 20 having a flow restrictor 34 positioned above them, more particularly the tubes 20 situated at the direct periphery of the separating wall 33, may have a fluid flow rate of between 0 and 20, preferably between 1 and 10, their theoretical flow.
  • a first flow control means is to play on the distance D between the end of a tube 20 having a flow restrictor 34 positioned above it and said flow reducer 34. The smaller this distance D is, the smaller the the flow will be weak too. In the particular case where the flow rate is 0, the flow restrictor 34 blocks the tube 20, the distance D will then be 0, and prevents any fluid flow within it.
  • Another way of controlling the flow rate is to vary the length L of the flow restrictor 34.
  • a flow reducer 34 when a flow reducer 34 is positioned partially above a tube 20, said tube 20 will have a larger fluid flow rate than a tube 20 where a flow reducer 34 is positioned above any the tube end 20.
  • a flow restrictor 34 whose distance D with the end of at least one tube 20 increases as said tube 20 is moved away from the separating wall 33.
  • a flow restrictor 34 is positioned above two tubes 20 simultaneously.
  • the tube 20 closest to the separating wall 33 has a distance D with the flow restrictor 34 smaller than the tube 20 farthest from the separating wall 33.
  • These two tubes 20 then both have a reduced but different flow rate. one of the other.
  • the heat exchanger 1 can be a heat exchanger 1 having a U-shaped fluid circulation.
  • one of the two collectors 3 has a separating wall 33, the other collector 32 'comprising for its part a single compartment 37c closed which allows the circulation of the fluid between the tubes 20.
  • This heat exchanger 1 may for example be a heat exchanger 1 of the air / air type.
  • the heat exchanger 1 may be a heat exchanger 1 having a double circulation of fluid.
  • each manifold 3 has a partition wall 33 defining two compartments 37a and / or 37b within said manifold 3.
  • Each manifold 3 thus comprises a compartment 37a having an inlet 30a and / or a compartment 37b having an outlet 30b of fluid.
  • two fluids each arrive at a different fluid inlet 30a, circulate in the tubes 20 and each spring at a different fluid outlet 30b located on the collector 3 opposite the one carrying the fluid inlet 30a.
  • the circulation of the fluid is in the opposite direction, that is to say that the manifolds 3 both comprise a compartment 37a comprising a fluid inlet 30a and another compartment 37b comprising an outlet fluid 30b.
  • the heat exchanger 1 allows a more economical assembly because possibly requiring mounting steps while allowing a decrease in fluid flow within the tubes 20 located on either side of the dividing wall 33, which decreases the intensity of the thermal shocks at this location and therefore increases the durability of the heat exchanger.

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Geometry (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Details Of Heat-Exchange And Heat-Transfer (AREA)
EP17716946.3A 2016-03-18 2017-03-16 Wärmetauscher und zugehöriges herstellungsverfahren Withdrawn EP3430341A1 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR1652313A FR3049051B1 (fr) 2016-03-18 2016-03-18 Echangeur de chaleur et procede de fabrication associe
PCT/FR2017/050605 WO2017158300A1 (fr) 2016-03-18 2017-03-16 Échangeur de chaleur et procédé de fabrication associé

Publications (1)

Publication Number Publication Date
EP3430341A1 true EP3430341A1 (de) 2019-01-23

Family

ID=56069104

Family Applications (1)

Application Number Title Priority Date Filing Date
EP17716946.3A Withdrawn EP3430341A1 (de) 2016-03-18 2017-03-16 Wärmetauscher und zugehöriges herstellungsverfahren

Country Status (4)

Country Link
EP (1) EP3430341A1 (de)
CN (1) CN109154480B (de)
FR (1) FR3049051B1 (de)
WO (1) WO2017158300A1 (de)

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5186249A (en) * 1992-06-08 1993-02-16 General Motors Corporation Heater core
US20080314076A1 (en) * 2004-06-15 2008-12-25 Showa Denko K.K. Heat Exchanger
FR2912209B1 (fr) * 2007-02-06 2013-08-23 Valeo Systemes Thermiques Echangeur multi circuits
FR2947331B1 (fr) * 2009-06-29 2011-07-29 Valeo Systemes Thermiques Echangeur de chaleur comprenant un faisceau de tubes avec au moins un tube inactif
BR102013014855B1 (pt) * 2013-06-13 2020-12-01 Valeo Sistemas Automotivos Ltda trocador de calor para veículo

Also Published As

Publication number Publication date
WO2017158300A1 (fr) 2017-09-21
CN109154480A (zh) 2019-01-04
CN109154480B (zh) 2021-03-02
FR3049051A1 (fr) 2017-09-22
FR3049051B1 (fr) 2019-04-19

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