US20230061591A1 - Dimple chiller with secondary dimples - Google Patents

Dimple chiller with secondary dimples Download PDF

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Publication number
US20230061591A1
US20230061591A1 US17/756,781 US202117756781A US2023061591A1 US 20230061591 A1 US20230061591 A1 US 20230061591A1 US 202117756781 A US202117756781 A US 202117756781A US 2023061591 A1 US2023061591 A1 US 2023061591A1
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United States
Prior art keywords
dimples
main
heat exchanger
plate
exchanger according
Prior art date
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Pending
Application number
US17/756,781
Inventor
Gero Lapp
Julian Neukirchen
Felix Girmscheid
Jihoon Choi
Florian Bieregger
Matthias Herpers
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Hanon Systems Corp
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Hanon Systems Corp
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Assigned to HANON SYSTEMS reassignment HANON SYSTEMS ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: Neukirchen, Julian, Herpers, Matthias, CHOI, JIHOON, BIEREGGER, FLORIAN, GIRMSCHEID, FELIX
Assigned to HANON SYSTEMS reassignment HANON SYSTEMS ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: Lapp, Gero
Publication of US20230061591A1 publication Critical patent/US20230061591A1/en
Pending 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
    • 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
    • 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
    • F28D9/00Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D9/0031Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other
    • F28D9/0037Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the conduits for the other heat-exchange medium also being formed by paired plates touching each other
    • 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
    • F28D9/00Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D9/0031Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other
    • F28D9/0043Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the plates having openings therein for circulation of at least one heat-exchange medium from one conduit to another
    • F28D9/005Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the plates having openings therein for circulation of at least one heat-exchange medium from one conduit to another the plates having openings therein for both heat-exchange media
    • 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
    • F28F3/08Elements constructed for building-up into stacks, e.g. capable of being taken apart for cleaning
    • F28F3/086Elements constructed for building-up into stacks, e.g. capable of being taken apart for cleaning having one or more openings therein forming tubular heat-exchange passages

Definitions

  • Dimple plates in heat exchanger (HEX) applications often suffer from low specific heat exchange rates due to low velocities of the heat-exchanging fluids.
  • the invention can be regarded as being a plate of a heat exchanger or a heat exchanger having at least one plate which is preferably rectangular and comprises main dimples, between which secondary dimples are formed that are flatter and/or smaller with respect to their dimensions as seen in a plan view.
  • the plate thus has main dimples, depressions, bumps and/or protrusions or bulges which are preferably arranged in rows preferably extending obliquely to the edges of the preferably rectangular plate.
  • secondary dimples are formed between the main dimples, which can alternatively be designated as the main dimples as above.
  • the rows are thereby seen in those directions in which the dimples are lined up one behind the other with minimal spacing. These rows can extend at any angle to the edges, as well as perpendicular to the one edges and therefore parallel to the other edges.
  • the present invention leads to increased heat exchange rates in a dimple heat exchanger, in particular a cooler plate, while the active surface for heat exchange is not reduced.
  • the surface of heat exchange is increased without changing the use of material.
  • the velocities of the fluids around the secondary dimples are increased, which results in an increased heat exchange.
  • the invention further leads to a change in flow directions not only in the horizontal plane, but also perpendicular thereto, thus leading to a mixing of temperature layers in the channels between the dimple heat exchanger plates.
  • the depth of the secondary dimples is set to a maximum of 0.5 times the channel height and/or 0.5 times the depth of the main dimples.
  • the depth of the main dimples can be set to a maximum corresponding to the channel height.
  • the distance between the main and secondary dimples in an x direction can be varied between 1.9 and 2.5 mm and in they direction (a second diagonal direction) between 1.9 and 2.5 mm.
  • one secondary dimple can be formed between two main dimples.
  • at least one, preferably precisely one, secondary dimple is formed in each case on the entire plate between two main dimples, or several, preferably four, and preferably spaced apart by 90 degrees, secondary dimples are formed in the vicinity of each main dimple.
  • At least some, preferably all, of the secondary dimples can be arranged on the lines or rows that are described by the main dimples.
  • the main dimples are preferably arranged in rows which preferably extend obliquely to the edges of the preferably rectangular plate.
  • the rows are designated above as diagonals; however, they do not have to correspond to the diagonals of the rectangular plate, but can extend at an angle thereto.
  • the rows can be formed in two directions extending at an angle to each other, wherein the angle can be equal or not equal to 90 degrees. For all of the above-mentioned embodiments, favorable properties could be determined in initial tests and simulations.
  • the sheet thickness of the plate can thereby be less in the area of the main and/or secondary dimples than between the dimples.
  • the main and/or secondary dimples can be circular, elliptical, or oval in plan view.
  • the main axes of elliptical or oval main dimples can extend parallel to a plate edge, in particular parallel to the longer edge of a rectangular plate.
  • the main axes of elliptical or oval secondary dimples can extend at an angle to the plate edges of a rectangular plate.
  • the main axes of several elliptical or oval secondary dimples can extend parallel to each other and at an angle to the main axes of several other secondary dimples.
  • FIG. 1 shows a plan view of a plate of a conventional heat exchanger with dimples.
  • FIG. 2 shows a plate similar to that of FIG. 1 , which additionally comprises the secondary dimples according to the invention.
  • FIG. 3 is a graph showing the increase in performance of a heat exchanger with the plates of FIG. 2 compared to the heat exchanger with the plates of FIG. 1 .
  • FIGS. 4 and 5 show plates similar to those of FIGS. 1 , 2 , 4 and 5 including their dimensions.
  • FIG. 6 shows the plate of FIG. 8 including one detail and preferred sizes of the dimples.
  • FIG. 7 shows further experimental results indicating an increase in performance of the new type of plate by between 6.2 and 10.2%, without changing neither the size of the plate nor the amount of material used, although the secondary dimples are formed.
  • a plate 100 of a heat exchanger comprises numerous dimples which in this case, in plan view, are oval dimples 102 that are arranged on lines extending obliquely to the plate edges, which do not quite correspond to the diagonals of the rectangle forming the plate shape.
  • two groups of rows can be seen, one extending from bottom left to top right and the other from bottom right to top left, and which in the case shown intersect at an angle smaller than 90 degrees.
  • the arrangement of the main dimples 12 substantially corresponds to that of the (only present) dimples 102 as shown in FIG. 1 .
  • one secondary dimple 14 is formed in each case between every two main dimples 12 , which in this case in plan view is both smaller and, not visible in plan view, flatter.
  • precisely one secondary dimple 14 is formed in each case between two main dimples 12 , and therefore four secondary dimples are formed in the vicinity of every main dimple.
  • the secondary dimples are located on those lines or rows that are described by the main dimples.
  • the main dimples 12 are oval when viewed from the top, with their longer axis extending parallel to the longer edge of the rectangular plate 10 , and the secondary dimples are circular when viewed from the top.
  • FIG. 3 which shows a performance comparison of the plates from FIGS. 1 and 2 in a two-sided heated wall, there appears an increase in performance from 2.0 to nearly 5% depending on the coolant flow.
  • FIG. 4 shows a further plate 100 comprising only a single type of dimple 102 .
  • a plate 10 according to the invention according to FIG. 5 is provided with both main dimples 12 and secondary dimples 14 .
  • the main dimples 12 and the secondary dimples 14 are also arranged in intersecting rows in this embodiment, which also in this case do not correspond to the diagonals of the rectangular plate. However, they are arranged at an angle of 90 degrees to each other in this embodiment.
  • both the main dimples 12 and the secondary dimples 14 are circular in plan view.
  • the plates of FIGS. 4 and 5 can typically be between 60 mm and 100 mm wide and between 80 mm and 140 mm long. According to an exemplary embodiment, they are each 64 mm wide and 102 mm long.
  • the shape and alignment of the main dimples 12 and the secondary dimples 14 can be seen more clearly in the detailed view of FIG. 6 .
  • four secondary dimples 14 are arranged here around one main dimple 12 at a constant spacing of 90 degrees.
  • the main dimples of the plate of FIG. 6 can have a diameter of 4.1 mm and a depth of 1.2 mm. 67 dimples of this type can be present on the plate shown in FIG. 6 .
  • the secondary dimples can have a diameter of 1.9 mm and a depth of 0.6 mm, and 140 dimples of this type can be formed on the plate shown in FIG. 9 .

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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)

Abstract

A heat exchanger with at least one plate includes main dimples between which secondary dimples are formed which are flatter and/or smaller with respect to their dimensions as seen in a plan view. A depth of the secondary dimples may be at most 0.5 times a channel height and/or at most 0.5 times the depth of the main dimples.

Description

    CROSS-REFERENCE TO RELATED PATENT APPLICATIONS
  • This patent application is a United States nation phase patent application based on PCT/KR2021/001305 filed on Feb. 1, 2021, which claims the benefit of German Patent Application No. DE 10 2020 201 344.6 filed on Feb. 4, 2020 and German Patent Application No. DE 10 2020 212 900.2 filed on Oct. 13, 2020, the entire disclosures of which are hereby incorporated herein by reference.
  • TECHNICAL FIELD
  • Dimple plates in heat exchanger (HEX) applications often suffer from low specific heat exchange rates due to low velocities of the heat-exchanging fluids.
  • PRIOR ART
  • One known solution is the increase of dimple size to increase local velocities and change the flow directions in the fluid.
  • However, an increase of dimple size directly leads to a reduced surface for the heat exchange and to an increase of pressure drop in the channel. Therefore, a solution must be found to increase heat exchange rates with a minimal increase in pressure drop in the fluid at an accelerated rate and taking away from the surface of heat exchange.
  • DESCRIPTION OF THE INVENTION
  • The above problem is solved by the subject matter as shown and described herein.
  • The invention can be regarded as being a plate of a heat exchanger or a heat exchanger having at least one plate which is preferably rectangular and comprises main dimples, between which secondary dimples are formed that are flatter and/or smaller with respect to their dimensions as seen in a plan view.
  • The plate thus has main dimples, depressions, bumps and/or protrusions or bulges which are preferably arranged in rows preferably extending obliquely to the edges of the preferably rectangular plate. According to the invention, secondary dimples are formed between the main dimples, which can alternatively be designated as the main dimples as above. The rows are thereby seen in those directions in which the dimples are lined up one behind the other with minimal spacing. These rows can extend at any angle to the edges, as well as perpendicular to the one edges and therefore parallel to the other edges.
  • As a result of the secondary dimples, the present invention leads to increased heat exchange rates in a dimple heat exchanger, in particular a cooler plate, while the active surface for heat exchange is not reduced. In fact, the surface of heat exchange is increased without changing the use of material. In addition, the velocities of the fluids around the secondary dimples are increased, which results in an increased heat exchange. The invention further leads to a change in flow directions not only in the horizontal plane, but also perpendicular thereto, thus leading to a mixing of temperature layers in the channels between the dimple heat exchanger plates.
  • Preferred further developments are described herein.
  • The depth of the secondary dimples is set to a maximum of 0.5 times the channel height and/or 0.5 times the depth of the main dimples. The depth of the main dimples can be set to a maximum corresponding to the channel height.
  • The distance between the main and secondary dimples in an x direction (a first diagonal direction) can be varied between 1.9 and 2.5 mm and in they direction (a second diagonal direction) between 1.9 and 2.5 mm.
  • In each case one secondary dimple can be formed between two main dimples. Preferably at least one, preferably precisely one, secondary dimple is formed in each case on the entire plate between two main dimples, or several, preferably four, and preferably spaced apart by 90 degrees, secondary dimples are formed in the vicinity of each main dimple.
  • At least some, preferably all, of the secondary dimples can be arranged on the lines or rows that are described by the main dimples.
  • The main dimples are preferably arranged in rows which preferably extend obliquely to the edges of the preferably rectangular plate. The rows are designated above as diagonals; however, they do not have to correspond to the diagonals of the rectangular plate, but can extend at an angle thereto. The rows can be formed in two directions extending at an angle to each other, wherein the angle can be equal or not equal to 90 degrees. For all of the above-mentioned embodiments, favorable properties could be determined in initial tests and simulations.
  • The sheet thickness of the plate can thereby be less in the area of the main and/or secondary dimples than between the dimples.
  • The main and/or secondary dimples can be circular, elliptical, or oval in plan view. The main axes of elliptical or oval main dimples can extend parallel to a plate edge, in particular parallel to the longer edge of a rectangular plate. The main axes of elliptical or oval secondary dimples can extend at an angle to the plate edges of a rectangular plate. The main axes of several elliptical or oval secondary dimples can extend parallel to each other and at an angle to the main axes of several other secondary dimples.
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • Further details of the invention can be seen from the drawings.
  • FIG. 1 shows a plan view of a plate of a conventional heat exchanger with dimples.
  • FIG. 2 shows a plate similar to that of FIG. 1 , which additionally comprises the secondary dimples according to the invention.
  • FIG. 3 is a graph showing the increase in performance of a heat exchanger with the plates of FIG. 2 compared to the heat exchanger with the plates of FIG. 1 .
  • FIGS. 4 and 5 show plates similar to those of FIGS. 1, 2, 4 and 5 including their dimensions.
  • FIG. 6 shows the plate of FIG. 8 including one detail and preferred sizes of the dimples.
  • FIG. 7 shows further experimental results indicating an increase in performance of the new type of plate by between 6.2 and 10.2%, without changing neither the size of the plate nor the amount of material used, although the secondary dimples are formed.
  • DETAILED DESCRIPTION OF PREFERRED EMBODIMENTS OF THE INVENTION
  • As can be seen in FIG. 1 , a plate 100 of a heat exchanger comprises numerous dimples which in this case, in plan view, are oval dimples 102 that are arranged on lines extending obliquely to the plate edges, which do not quite correspond to the diagonals of the rectangle forming the plate shape. In particular, two groups of rows can be seen, one extending from bottom left to top right and the other from bottom right to top left, and which in the case shown intersect at an angle smaller than 90 degrees.
  • In the plate 10 of a heat exchanger according to the invention according to FIG. 2 , the arrangement of the main dimples 12 substantially corresponds to that of the (only present) dimples 102 as shown in FIG. 1 .
  • According to the invention, one secondary dimple 14 is formed in each case between every two main dimples 12, which in this case in plan view is both smaller and, not visible in plan view, flatter. In particular, precisely one secondary dimple 14 is formed in each case between two main dimples 12, and therefore four secondary dimples are formed in the vicinity of every main dimple. As is also preferred, the secondary dimples are located on those lines or rows that are described by the main dimples. In the case shown, the main dimples 12 are oval when viewed from the top, with their longer axis extending parallel to the longer edge of the rectangular plate 10, and the secondary dimples are circular when viewed from the top.
  • As is revealed in FIG. 3 , which shows a performance comparison of the plates from FIGS. 1 and 2 in a two-sided heated wall, there appears an increase in performance from 2.0 to nearly 5% depending on the coolant flow.
  • FIG. 4 shows a further plate 100 comprising only a single type of dimple 102.
  • In contrast, a plate 10 according to the invention according to FIG. 5 is provided with both main dimples 12 and secondary dimples 14. Unlike the plates of FIGS. 1, 2, and 4 , the main dimples 12 and the secondary dimples 14 are also arranged in intersecting rows in this embodiment, which also in this case do not correspond to the diagonals of the rectangular plate. However, they are arranged at an angle of 90 degrees to each other in this embodiment. Moreover, in this case, both the main dimples 12 and the secondary dimples 14 are circular in plan view. The plates of FIGS. 4 and 5 can typically be between 60 mm and 100 mm wide and between 80 mm and 140 mm long. According to an exemplary embodiment, they are each 64 mm wide and 102 mm long.
  • The shape and alignment of the main dimples 12 and the secondary dimples 14 can be seen more clearly in the detailed view of FIG. 6 . In particular, four secondary dimples 14 are arranged here around one main dimple 12 at a constant spacing of 90 degrees. The main dimples of the plate of FIG. 6 can have a diameter of 4.1 mm and a depth of 1.2 mm. 67 dimples of this type can be present on the plate shown in FIG. 6 . The secondary dimples can have a diameter of 1.9 mm and a depth of 0.6 mm, and 140 dimples of this type can be formed on the plate shown in FIG. 9 .
  • As is apparent from FIG. 7 , there is an increase in performance, depending on the coolant flow, between 6.2 and 10.2%.

Claims (11)

1.-10. (canceled)
11. A heat exchanger with at least one plate having main dimples, between which secondary dimples are formed which are flatter and/or smaller with respect to their dimensions as seen in a plan view.
12. The heat exchanger according to claim 11, wherein a depth of the secondary dimples is at most 0.5 times a channel height and/or at most 0.5 times a depth of the main dimples.
13. The heat exchanger according to claim 11, wherein a distance between the main dimples and the secondary dimples in at least one direction is 1.9 to 2.5 mm.
14. The heat exchanger according to claim 11, wherein one of the secondary dimples is formed in each case between two of the main dimples.
15. The heat exchanger according to claim 11, wherein the main dimples are arranged in rows, and the secondary dimples are arranged on the rows of main dimples.
16. The heat exchanger according to claim 15, wherein the rows of the main dimples are formed obliquely to at least one edge of the at least one plate.
17. The heat exchanger according to claim 11, wherein a sheet thickness of the at least one plate in an area of the main dimples and/or the secondary dimples is less than between the dimples.
18. The heat exchanger according to claim 11, wherein the main dimples and/or the secondary dimples have a circular, an elliptical, or an oval shape in plan view.
19. The heat exchanger according to claim 18, wherein a main axis of the main dimples having the elliptical or the oval shape are parallel to an edge of the at least one plate, in particular a longer edge of a rectangular plate.
20. The heat exchanger according to claim 18, wherein a main axis of the secondary dimples having the elliptical or the oval shape extend at an angle with respect to edges of a rectangular plate.
US17/756,781 2020-02-04 2021-02-01 Dimple chiller with secondary dimples Pending US20230061591A1 (en)

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
DE102020201344.6 2020-02-04
DE102020201344 2020-02-04
DE102020212900.2A DE102020212900A1 (en) 2020-02-04 2020-10-13 Dimple cooler with additional dimples
DE102020212900.2 2020-10-13
PCT/KR2021/001305 WO2021157980A1 (en) 2020-02-04 2021-02-01 Dimple chiller with secondary dimples

Publications (1)

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US20230061591A1 true US20230061591A1 (en) 2023-03-02

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US17/756,781 Pending US20230061591A1 (en) 2020-02-04 2021-02-01 Dimple chiller with secondary dimples

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US (1) US20230061591A1 (en)
JP (1) JP2023512552A (en)
KR (1) KR20220082916A (en)
CN (1) CN114599929A (en)
DE (1) DE102020212900A1 (en)
WO (1) WO2021157980A1 (en)

Citations (5)

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US20050047932A1 (en) * 2003-08-14 2005-03-03 Tomoyoshi Nakae Heat exchanging wall, gas turbine using the same, and flying body with gas turbine engine
US20140046248A1 (en) * 2011-06-09 2014-02-13 Sis-Ter S.P.A. Heat exchange device
US9033030B2 (en) * 2009-08-26 2015-05-19 Munters Corporation Apparatus and method for equalizing hot fluid exit plane plate temperatures in heat exchangers
US10352566B2 (en) * 2013-06-14 2019-07-16 United Technologies Corporation Gas turbine engine combustor liner panel
US10830448B2 (en) * 2016-10-26 2020-11-10 Raytheon Technologies Corporation Combustor liner panel with a multiple of heat transfer augmentors for a gas turbine engine combustor

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JPH0654198B2 (en) * 1985-10-14 1994-07-20 日本電装株式会社 Stacked heat exchanger
KR20000010016U (en) * 1998-11-14 2000-06-15 신영주 Heat exchanger tube
FR2788123B1 (en) * 1998-12-30 2001-05-18 Valeo Climatisation EVAPORATOR, HEATING AND/OR AIR CONDITIONING DEVICE AND VEHICLE COMPRISING SUCH EVAPORATOR
KR100350946B1 (en) * 1999-12-21 2002-08-28 한라공조주식회사 Laminate type heat exchanger for vehicle
KR100819010B1 (en) * 2001-08-29 2008-04-02 한라공조주식회사 Heat exchanger
US20080078538A1 (en) * 2006-09-28 2008-04-03 Ali Jalilevand Heat exchanger plate having integrated turbulation feature
JP2011007412A (en) * 2009-06-25 2011-01-13 Mahle Filter Systems Japan Corp Oil cooler
RU2502932C2 (en) * 2010-11-19 2013-12-27 Данфосс А/С Heat exchanger
JP2014016144A (en) * 2012-07-05 2014-01-30 Airec Ab Plate for heat exchanger, heat exchanger, and air cooler comprising heat exchanger
CN104654889A (en) * 2013-11-25 2015-05-27 李鹏 Heat transfer plate of plate heat exchanger

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20050047932A1 (en) * 2003-08-14 2005-03-03 Tomoyoshi Nakae Heat exchanging wall, gas turbine using the same, and flying body with gas turbine engine
US9033030B2 (en) * 2009-08-26 2015-05-19 Munters Corporation Apparatus and method for equalizing hot fluid exit plane plate temperatures in heat exchangers
US20140046248A1 (en) * 2011-06-09 2014-02-13 Sis-Ter S.P.A. Heat exchange device
US10352566B2 (en) * 2013-06-14 2019-07-16 United Technologies Corporation Gas turbine engine combustor liner panel
US10830448B2 (en) * 2016-10-26 2020-11-10 Raytheon Technologies Corporation Combustor liner panel with a multiple of heat transfer augmentors for a gas turbine engine combustor

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JP2023512552A (en) 2023-03-27
DE102020212900A1 (en) 2021-08-05
CN114599929A (en) 2022-06-07
WO2021157980A1 (en) 2021-08-12
KR20220082916A (en) 2022-06-17

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Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:NEUKIRCHEN, JULIAN;GIRMSCHEID, FELIX;CHOI, JIHOON;AND OTHERS;SIGNING DATES FROM 20220411 TO 20220916;REEL/FRAME:061304/0956

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