WO2021074299A1 - A heat exchanger - Google Patents

A heat exchanger Download PDF

Info

Publication number
WO2021074299A1
WO2021074299A1 PCT/EP2020/079052 EP2020079052W WO2021074299A1 WO 2021074299 A1 WO2021074299 A1 WO 2021074299A1 EP 2020079052 W EP2020079052 W EP 2020079052W WO 2021074299 A1 WO2021074299 A1 WO 2021074299A1
Authority
WO
WIPO (PCT)
Prior art keywords
cross
section
heat exchanger
tubes
tube
Prior art date
Application number
PCT/EP2020/079052
Other languages
French (fr)
Inventor
Lukasz BARUS
Lukasz DULIBAN
Dawid Szostek
Lukasz WIDZYK
Artur DOMITER
Original Assignee
Valeo Autosystemy Sp. Z O.O.
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 Autosystemy Sp. Z O.O. filed Critical Valeo Autosystemy Sp. Z O.O.
Publication of WO2021074299A1 publication Critical patent/WO2021074299A1/en

Links

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
    • 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
    • F28D1/0535Heat-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 the conduits having a non-circular cross-section
    • F28D1/05366Assemblies of conduits connected to common headers, e.g. core type radiators
    • 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
    • F28D1/03Heat-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 plate-like or laminated conduits
    • F28D1/0391Heat-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 plate-like or laminated conduits a single plate being bent to form one or more conduits
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2210/00Heat exchange conduits
    • F28F2210/06Heat exchange conduits having walls comprising obliquely extending corrugations, e.g. in the form of threads
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2210/00Heat exchange conduits
    • F28F2210/08Assemblies of conduits having different features

Definitions

  • the invention relates to a heat exchanger, in particular to the heat exchanger for a motor vehicle.
  • Automobile radiators are constructed of a pair of metal or plastic header tanks, linked by a core with many narrow passageways, giving a high surface area relative to volume.
  • This core is usually made of stacked layers of metal sheet, pressed to form channels and soldered or brazed together.
  • radiators were made from brass or copper cores soldered to brass headers. Modern radiators have aluminum cores, and often save money and weight by using plastic tanks with rubber gaskets.
  • This construction is more prone to failure and less easily repaired than traditional materials, yet it benefits from better heat transfer properties and lightweight construction.
  • the object of the invention is, among others, a heat exchanger, in particular for a motor vehicle, comprising a first manifold and a second manifold connected by a plurality of primary tubes with a first cross-section (A-A) and at least one secondary tube with a second cross-section, characterised in that the second cross-section (B-B) is different than the first cross-section (A-A), wherein the outer diameter of the secondary tube is constantly the same as the outer diameter of the primary tubes.
  • At least one secondary tube is deployed on one of the peripheral ends of the manifolds.
  • At least one primary tube is deployed between at least two secondary tubes.
  • the first cross section (A-A) has bigger hydraulic diameter than the second cross section (B-B).
  • the second cross section comprises corrugations on the inner side of the secondary tube.
  • the second cross section comprises surplus material on the inner side of the secondary tube compared to the first cross section.
  • the primary tubes and the secondary tubes are made from the folded sheet of metal.
  • the primary tubes and the secondary tubes are extruded.
  • Fig. 1 shows a schematic view of a heat exchanger comprising two different types of tubes.
  • Fig. 2 shows a cross section of the primary tube.
  • Fig. 3 shows a cross section of the secondary tube.
  • Fig. 4 shows an exemplary deployment of the primary and secondary tubes in one of the examples.
  • the invention relates to heat exchangers, in particular radiators used in automobiles.
  • the heat exchanger is configured to convey a cooling medium, such as a coolant through its sub-components so that the temperature of the cooling medium flowing out of the heat exchanger would be lower than the temperature of the cooling medium flowing into the heat exchanger thanks to heat exchange with a second medium, e.g. air.
  • the cooling medium is usually delivered into the heat exchanger by an inlet and collected by an outlet.
  • the inlet and the outlet are usually deployed either on the opposite sides of the heat exchanger, or on the same side thereof.
  • the inlet and the outlet have usually circular cross-section protruding from inlet and/or outlet of the tanks respectively.
  • Fig.1 presents a heat exchanger 1 , in particular for a motor vehicle, comprising a first manifold 2 and a second manifold 3 connected by a plurality of primary tubes 10 and at least one secondary tube 20.
  • the manifolds 2, 3 are usually associated with an assembly of the header and the tank, wherein the header may be configured to receive the primary tubes 10 or secondary tubes 20 and the tank may provide a coolant fluid distribution and fluidal communication with the rest of the system.
  • the first manifold 2 may comprise the inlet to the heat exchanger, whereas the outlet may be located on the second manifold.
  • the configuration of the inlet and the outlet may be different from the aforementioned one, i.e. the inlet could be located on the second manifold 3, whereas the outlet could be located on the first manifold 2.
  • both inlet and the outlet may be located on the same manifold 2, 3. Multiple inlets and outlets are also envisaged.
  • the primary tubes 10 and the secondary tubes 20 are usually made of a single sheet of metal which is folded inwardly, so that the terminal ends of metal sheet create an inner wall that can be attached (e.g. by brazing) to the flat, portion of the tube.
  • the inner wall may be deployed between the two opposite walls of the tube.
  • the tubes 10, 20 can be made in the process of extrusion. It is also possible for the tubes 10, 20 to not comprise any inner walls 5.
  • the primary tubes 10 and the secondary tubes 20 comprise two open ends, and they are usually deployed in parallel to each other between the first manifold 2 and the second manifold 3, wherein the open ends of the tubes 10, 20 are received in a slots of the headers.
  • the manifolds 2, 3 and the tubes 10, 20 may be brazed together.
  • Fig. 2 presents a cross-section (A-A) of the single primary tube 10.
  • the primary tube 10 comprises three dimensions characterising its outer periphery, i.e. a tube height a-i, a tube width bi and a tube length (not shown), wherein the length is perpendicular to the cross-section (A-A) presented in the Fig.2.
  • the primary tube 10 comprises also three dimensions characterising its inner dimensions, i.e. a channel height ci, a channel width d-i, and a channel length (not shown) which is essentially the same as the tube length.
  • the inner dimensions of the primary tube 10 presented in Fig. 2 are indicated for a single channel as in one of the embodiments the aforementioned inner wall 5 may be omitted.
  • Fig. 3 presents a cross-section (B-B) of the single secondary tube 20.
  • the secondary tube 20 comprises three dimensions characterising its outer dimensions, i.e. a tube height a ⁇ , a tube width b2 and a tube length (not shown), wherein the length is perpendicular to the cross-section (B-B) presented in the Fig.3.
  • the primary tube 10 comprises also three dimensions characterising its inner dimensions, i.e. a channel height C2, a channel width d2, and a channel length (not shown) which is essentially the same as the tube length.
  • the inner dimensions of the secondary tube 20 presented in Fig. 3 are indicated for a single channel as in one of the embodiments the aforementioned inner wall 5 may be omitted.
  • the outer dimensions may be used to determine, for example, the approximate outer diameter of the primary tubes 10 and the secondary tubes 20, as well as the inner dimensions may be used to determine, for example, the approximate inner diameter of the primary tubes 10 and the secondary tubes 20.
  • the second cross-section (B-B) is different than the first cross-section (A-A), wherein the outer diameter of the secondary tube 20 is constantly the same as the outer diameter of the primary tubes 10. Consequently, the first cross section (A-A) has different hydraulic diameter than the second cross section (B-B).
  • the second cross-section (B-B) may be for example bigger that the first cross-section (A-A), so that the primary tubes comprise a bigger hydraulic diameter than the secondary tubes 20.
  • Using the different cross-section (B-B) of the secondary tubes 20 may significantly improve the heat exchanger’s performance by increasing the coolant fluid velocity at the certain sections of the heat exchanger 1 , depending on the deployment of the secondary tubes 20 in the stack.
  • the secondary tubes 20 may comprise a smaller hydraulic diameter in comparison with the primary tubes 10.
  • the smaller internal dimensions of the secondary tubes 20 forces grater velocity of the coolant fluid thanks to increased local hydraulic pressure.
  • Fig. 3 presents an example, wherein at least one secondary tube 20 is deployed on one of the peripheral ends of the manifolds 2,3.
  • the heat exchanger 1 comprises two secondary tubes 20 deployed on the bottom of the stack to increase the coolant fluid in that area.
  • the heat exchanger 1 could comprise at least one secondary tube 20 deployed on the top of the stack to increase the coolant fluid in that area.
  • the heat exchanger 1 could comprise at least one primary tube 10 deployed between at least two secondary tubes 20.
  • Such configuration is covered, for example by Fig.1 , however other deployments are also envisaged.
  • the section of secondary tubes 20 stacked, for example on the top of the stack, could be separated by at least one primary tube 10 to ensure a precise coolant fluid flow in that area.
  • the secondary tubes 20 may be in fact manufactured using several different methods.
  • One of the methods may comprise using a metal sheets of different thickness for the primary tubes 10 and the secondary tubes 20.
  • the sheet of metal used for manufacturing the primary tubes 10 could be thinner than the sheet of metal used for manufacturing the secondary tubes 20.
  • Another method for increasing the cross section (B-B) of the secondary tubes 20 could comprise corrugations on the inner surface of the channel, so as to decrease its inner dimensions. The corrugations could increase the fluid velocity in the secondary tubes 20, analogically to aforementioned method, however the costs of manufacturing a secondary tube 20 of the corrugated sheet of metal would be significantly higher compared to the thicker sheet of metal.
  • Another method for increasing the cross section (B-B) of the secondary tubes 20 could comprise surplus material on the inner side of the secondary tube 20. The surplus material could have different physical properties than the secondary tube 20, yet it would be desired so that is remains unreactive to coolant fluid i.e. the surplus material should keep its form, so it is not, for example, washed out from the inner

Landscapes

  • 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)

Abstract

The invention comprises a heat exchanger (1), in particular for a motor vehicle, comprising a first manifold (2) and a second manifold (3) connected by a plurality of primary tubes (10) with a first cross-section (A-A) and at least one secondary tube (20) with a second cross-section (B-B), characterised in that the second cross-section (B-B) is different than the first cross-section (A-A), wherein the outer diameter of the secondary tube (20) is constantly the same as the outer diameter of the primary tubes (10).

Description

A HEAT EXCHANGER FIELD OF THE INVENTION
The invention relates to a heat exchanger, in particular to the heat exchanger for a motor vehicle.
BACKGROUND OF THE INVENTION Automobile radiators are constructed of a pair of metal or plastic header tanks, linked by a core with many narrow passageways, giving a high surface area relative to volume. This core is usually made of stacked layers of metal sheet, pressed to form channels and soldered or brazed together. For many years radiators were made from brass or copper cores soldered to brass headers. Modern radiators have aluminum cores, and often save money and weight by using plastic tanks with rubber gaskets.
This construction is more prone to failure and less easily repaired than traditional materials, yet it benefits from better heat transfer properties and lightweight construction.
However, the ongoing interest in continuous weight and size reduction of vehicle’s sub- components may lead to undesired decrease in efficiency of the whole heat exchange system. This may be caused by, for example, uneven thermal expansion between heat exchanger’s sub-components and also within the particular component, such as the core. The thermal expansion of the heat exchanger depends, for example, on the coolant fluid velocity in different sections of the heat exchanger. Another factor that may handicap the flow of the coolant fluid is the deployment of the inlet and the outlet on the header tanks. In industry, the deployment of the inlet and the outlet is usually predefined by the vehicle’s manufacturer requests which are not necessarily feasible in terms of even flow of the coolant fluid. Infeasible deployment of the inlet and outlet in the heat exchanger may lead to undesired flow disruption that can impact its performance and longevity.
It would be desired to provide the means of promoting the flow of the coolant fluid in the neglected parts of the heat exchanger core.
SUMMARY OF THE INVENTION
The object of the invention is, among others, a heat exchanger, in particular for a motor vehicle, comprising a first manifold and a second manifold connected by a plurality of primary tubes with a first cross-section (A-A) and at least one secondary tube with a second cross-section, characterised in that the second cross-section (B-B) is different than the first cross-section (A-A), wherein the outer diameter of the secondary tube is constantly the same as the outer diameter of the primary tubes.
Preferably, at least one secondary tube is deployed on one of the peripheral ends of the manifolds.
Preferably, at least one primary tube is deployed between at least two secondary tubes.
Preferably, the first cross section (A-A) has bigger hydraulic diameter than the second cross section (B-B).
Preferably, the second cross section comprises corrugations on the inner side of the secondary tube.
Preferably, the second cross section comprises surplus material on the inner side of the secondary tube compared to the first cross section.
Preferably, the primary tubes and the secondary tubes are made from the folded sheet of metal.
Preferably, the primary tubes and the secondary tubes are extruded. BRIEF DESCRIPTION OF DRAWINGS
Examples of the invention will be apparent from and described in detail with reference to the accompanying drawings, in which:
Fig. 1 shows a schematic view of a heat exchanger comprising two different types of tubes.
Fig. 2 shows a cross section of the primary tube.
Fig. 3 shows a cross section of the secondary tube. Fig. 4 shows an exemplary deployment of the primary and secondary tubes in one of the examples.
DETAILED DESCRIPTION OF EMBODIMENTS
The invention relates to heat exchangers, in particular radiators used in automobiles. The heat exchanger is configured to convey a cooling medium, such as a coolant through its sub-components so that the temperature of the cooling medium flowing out of the heat exchanger would be lower than the temperature of the cooling medium flowing into the heat exchanger thanks to heat exchange with a second medium, e.g. air. The cooling medium is usually delivered into the heat exchanger by an inlet and collected by an outlet. Depending on the architecture, i.e. the number of passes, desired heat exchanger deployment in the engine bay, etc., the inlet and the outlet are usually deployed either on the opposite sides of the heat exchanger, or on the same side thereof. The inlet and the outlet have usually circular cross-section protruding from inlet and/or outlet of the tanks respectively.
Fig.1 presents a heat exchanger 1 , in particular for a motor vehicle, comprising a first manifold 2 and a second manifold 3 connected by a plurality of primary tubes 10 and at least one secondary tube 20. The manifolds 2, 3 are usually associated with an assembly of the header and the tank, wherein the header may be configured to receive the primary tubes 10 or secondary tubes 20 and the tank may provide a coolant fluid distribution and fluidal communication with the rest of the system. The first manifold 2 may comprise the inlet to the heat exchanger, whereas the outlet may be located on the second manifold. Alternatively, the configuration of the inlet and the outlet may be different from the aforementioned one, i.e. the inlet could be located on the second manifold 3, whereas the outlet could be located on the first manifold 2. Alternatively, both inlet and the outlet may be located on the same manifold 2, 3. Multiple inlets and outlets are also envisaged.
The primary tubes 10 and the secondary tubes 20 are usually made of a single sheet of metal which is folded inwardly, so that the terminal ends of metal sheet create an inner wall that can be attached (e.g. by brazing) to the flat, portion of the tube. The inner wall may be deployed between the two opposite walls of the tube. Alternatively, the tubes 10, 20 can be made in the process of extrusion. It is also possible for the tubes 10, 20 to not comprise any inner walls 5.
The primary tubes 10 and the secondary tubes 20 comprise two open ends, and they are usually deployed in parallel to each other between the first manifold 2 and the second manifold 3, wherein the open ends of the tubes 10, 20 are received in a slots of the headers. To provide a tight connection, the manifolds 2, 3 and the tubes 10, 20 may be brazed together.
Fig. 2 presents a cross-section (A-A) of the single primary tube 10. The primary tube 10 comprises three dimensions characterising its outer periphery, i.e. a tube height a-i, a tube width bi and a tube length (not shown), wherein the length is perpendicular to the cross-section (A-A) presented in the Fig.2. The primary tube 10 comprises also three dimensions characterising its inner dimensions, i.e. a channel height ci, a channel width d-i, and a channel length (not shown) which is essentially the same as the tube length. The inner dimensions of the primary tube 10 presented in Fig. 2 are indicated for a single channel as in one of the embodiments the aforementioned inner wall 5 may be omitted.
Fig. 3 presents a cross-section (B-B) of the single secondary tube 20. The secondary tube 20 comprises three dimensions characterising its outer dimensions, i.e. a tube height aå, a tube width b2 and a tube length (not shown), wherein the length is perpendicular to the cross-section (B-B) presented in the Fig.3. The primary tube 10 comprises also three dimensions characterising its inner dimensions, i.e. a channel height C2, a channel width d2, and a channel length (not shown) which is essentially the same as the tube length. The inner dimensions of the secondary tube 20 presented in Fig. 3 are indicated for a single channel as in one of the embodiments the aforementioned inner wall 5 may be omitted.
The outer dimensions may be used to determine, for example, the approximate outer diameter of the primary tubes 10 and the secondary tubes 20, as well as the inner dimensions may be used to determine, for example, the approximate inner diameter of the primary tubes 10 and the secondary tubes 20.
According to Figs. 2 and 3 the second cross-section (B-B) is different than the first cross-section (A-A), wherein the outer diameter of the secondary tube 20 is constantly the same as the outer diameter of the primary tubes 10. Consequently, the first cross section (A-A) has different hydraulic diameter than the second cross section (B-B). The second cross-section (B-B) may be for example bigger that the first cross-section (A-A), so that the primary tubes comprise a bigger hydraulic diameter than the secondary tubes 20.
Using the different cross-section (B-B) of the secondary tubes 20 may significantly improve the heat exchanger’s performance by increasing the coolant fluid velocity at the certain sections of the heat exchanger 1 , depending on the deployment of the secondary tubes 20 in the stack.
The secondary tubes 20 may comprise a smaller hydraulic diameter in comparison with the primary tubes 10. The smaller internal dimensions of the secondary tubes 20 forces grater velocity of the coolant fluid thanks to increased local hydraulic pressure.
For example, Fig. 3 presents an example, wherein at least one secondary tube 20 is deployed on one of the peripheral ends of the manifolds 2,3. In this particular example, the heat exchanger 1 comprises two secondary tubes 20 deployed on the bottom of the stack to increase the coolant fluid in that area.
Analogically, the heat exchanger 1 could comprise at least one secondary tube 20 deployed on the top of the stack to increase the coolant fluid in that area. Alternatively, the heat exchanger 1 could comprise at least one primary tube 10 deployed between at least two secondary tubes 20. Such configuration is covered, for example by Fig.1 , however other deployments are also envisaged. For example, the section of secondary tubes 20 stacked, for example on the top of the stack, could be separated by at least one primary tube 10 to ensure a precise coolant fluid flow in that area.
The secondary tubes 20 may be in fact manufactured using several different methods. One of the methods may comprise using a metal sheets of different thickness for the primary tubes 10 and the secondary tubes 20. For example, the sheet of metal used for manufacturing the primary tubes 10 could be thinner than the sheet of metal used for manufacturing the secondary tubes 20. Another method for increasing the cross section (B-B) of the secondary tubes 20 could comprise corrugations on the inner surface of the channel, so as to decrease its inner dimensions. The corrugations could increase the fluid velocity in the secondary tubes 20, analogically to aforementioned method, however the costs of manufacturing a secondary tube 20 of the corrugated sheet of metal would be significantly higher compared to the thicker sheet of metal. Another method for increasing the cross section (B-B) of the secondary tubes 20 could comprise surplus material on the inner side of the secondary tube 20. The surplus material could have different physical properties than the secondary tube 20, yet it would be desired so that is remains unreactive to coolant fluid i.e. the surplus material should keep its form, so it is not, for example, washed out from the inner side of the secondary channel.
Other variations to the disclosed embodiments can be understood and effected by those skilled in the art in practicing the claimed invention, from a study of drawings, the disclosure, and the appended claims. The mere fact that certain measures are recited in mutually different dependent claims does not indicate that a combination of these measures cannot be used to the advantage.

Claims

Claims
1. A heat exchanger (1 ), in particular for a motor vehicle, comprising a first manifold (2) and a second manifold (3) connected by a plurality of primary tubes (10) with a first cross-section (A-A) and at least one secondary tube (20) with a second cross-section (B-B), characterised in that the second cross-section (B-B) is different than the first cross-section (A-A), wherein the outer diameter of the secondary tube (20) is constantly the same as the outer diameter of the primary tubes (10).
2. The heat exchanger (1) according to claim 1 , wherein at least one secondary tube (20) is deployed on one of the peripheral ends of the manifolds (2,3).
3. The heat exchanger (1) according to any of the preceding claims, wherein at least one primary tube (10) is deployed between at least two secondary tubes (20).
4. The heat exchanger (1) according to any of the preceding claims, wherein the first cross section (A-A) has bigger hydraulic diameter than the second cross section (B- B).
5. The heat exchanger (1) according to any of the preceding claims, wherein the second cross section comprises corrugations on the inner side of the secondary tube (20).
6. The heat exchanger (1) according to any of the preceding claims, wherein the second cross section comprises surplus material on the inner side of the secondary tube (20) compared to the first cross section.
7. The heat exchanger (1) according to any of the preceding claims, wherein the primary tubes (10) and the secondary tubes (20) are made from the folded sheet of metal.
8. The heat exchanger (1) according to any of the preceding claims, wherein the primary tubes (10) and the secondary tubes (20) are extruded.
PCT/EP2020/079052 2019-10-18 2020-10-15 A heat exchanger WO2021074299A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP19461590.2A EP3809081A1 (en) 2019-10-18 2019-10-18 A heat exchanger
EP19461590.2 2019-10-18

Publications (1)

Publication Number Publication Date
WO2021074299A1 true WO2021074299A1 (en) 2021-04-22

Family

ID=68296441

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/EP2020/079052 WO2021074299A1 (en) 2019-10-18 2020-10-15 A heat exchanger

Country Status (2)

Country Link
EP (1) EP3809081A1 (en)
WO (1) WO2021074299A1 (en)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5765393A (en) * 1997-05-28 1998-06-16 White Consolidated Industries, Inc. Capillary tube incorporated into last pass of condenser
US6394176B1 (en) * 1998-11-20 2002-05-28 Valeo Thermique Moteur Combined heat exchanger, particularly for a motor vehicle
WO2008019117A2 (en) * 2006-08-05 2008-02-14 Modine Manufacturing Company Heat exchanger and method
US20120000634A1 (en) * 2010-03-31 2012-01-05 Rod Janusz Heat Exchanger
EP3134695A1 (en) * 2014-04-22 2017-03-01 TitanX Engine Cooling Holding AB Heat exchanger comprising a core of tubes

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5765393A (en) * 1997-05-28 1998-06-16 White Consolidated Industries, Inc. Capillary tube incorporated into last pass of condenser
US6394176B1 (en) * 1998-11-20 2002-05-28 Valeo Thermique Moteur Combined heat exchanger, particularly for a motor vehicle
WO2008019117A2 (en) * 2006-08-05 2008-02-14 Modine Manufacturing Company Heat exchanger and method
US20120000634A1 (en) * 2010-03-31 2012-01-05 Rod Janusz Heat Exchanger
EP3134695A1 (en) * 2014-04-22 2017-03-01 TitanX Engine Cooling Holding AB Heat exchanger comprising a core of tubes

Also Published As

Publication number Publication date
EP3809081A1 (en) 2021-04-21

Similar Documents

Publication Publication Date Title
US11815318B2 (en) Flattened tube finned heat exchanger and fabrication method
US7073570B2 (en) Automotive heat exchanger
EP2810010B1 (en) Multiple tube bank heat exchanger assembly and fabrication method
US20090151918A1 (en) Heat Exchanger for Automobile and Fabricating Method Thereof
US9593889B2 (en) Heat exchanger construction
EP2810014B1 (en) Method for fabricating flattened tube finned heat exchanger
US7201216B2 (en) Heat exchanger, in particular oil cooler for a motor vehicle
US20160054075A1 (en) Folded tube multiple bank heat exchange unit
CN103238038A (en) Microchannel heat exchanger fin
US20050217839A1 (en) Integral primary and secondary heat exchanger
KR20140110968A (en) Heat exchanger utilizing tubular structures having internal flow altering members and external chamber assemblies
CN103502761A (en) A method of producing a heat exchanger and a heat exchanger
CN211855020U (en) Heat exchange tube and heat exchanger with same
US6543530B2 (en) Heat exchanger having an improved pipe connecting structure
EP3809081A1 (en) A heat exchanger
KR20130065174A (en) Heat exchanger for vehicle
CN212058426U (en) Heat exchanger
CN110595248B (en) Flat pipe, heat exchange pipe, heat exchanger and manufacturing method of heat exchange pipe
JP2512471Y2 (en) Vehicle heat exchanger
JPH10141875A (en) Heat exchanger
JP4164145B2 (en) Heat exchanger and car air conditioner using the same
JP5947158B2 (en) Outdoor heat exchanger for heat pump
EP3819579A1 (en) A heat exchanger
JP3772150B2 (en) Heat exchanger
JPH0259395B2 (en)

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 20799626

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 20799626

Country of ref document: EP

Kind code of ref document: A1