EP2899487B1 - Échangeur thermique à empilement de disques - Google Patents

Échangeur thermique à empilement de disques Download PDF

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Publication number
EP2899487B1
EP2899487B1 EP14199018.4A EP14199018A EP2899487B1 EP 2899487 B1 EP2899487 B1 EP 2899487B1 EP 14199018 A EP14199018 A EP 14199018A EP 2899487 B1 EP2899487 B1 EP 2899487B1
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EP
European Patent Office
Prior art keywords
main
stacking direction
additional
heat exchanger
fluid
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.)
Active
Application number
EP14199018.4A
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German (de)
English (en)
Other versions
EP2899487A1 (fr
Inventor
Andreas Dränkow
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.)
Mahle Behr GmbH and Co KG
Original Assignee
Mahle Behr GmbH and Co KG
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.)
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Application filed by Mahle Behr GmbH and Co KG filed Critical Mahle Behr GmbH and Co KG
Publication of EP2899487A1 publication Critical patent/EP2899487A1/fr
Application granted granted Critical
Publication of EP2899487B1 publication Critical patent/EP2899487B1/fr
Active legal-status Critical Current
Anticipated expiration legal-status Critical

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D9/00—Heat-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
    • F28D9/0031—Heat-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
    • F28D9/0043—Heat-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
    • F28D9/005—Heat-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
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/06—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
    • F28F13/08—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media by varying the cross-section of the flow channels
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2250/00—Arrangements for modifying the flow of the heat exchange media, e.g. flow guiding means; Particular flow patterns
    • F28F2250/04—Communication passages between channels

Definitions

  • the present invention relates to a stacked disk heat exchanger for heat transfer between a first fluid and a second fluid, having the features of the preamble of claim 1.
  • Such a stacked disk heat exchanger is basically known. It has a plurality of main disks which are stacked in a stacking direction to form a stack.
  • the main disks each have two openings for the first fluid and two openings for the second fluid, wherein two of the openings are each enclosed by a dome.
  • the main disks are stacked in the stack so that in the stack for the first fluid a common, parallel to the stacking direction first inlet channel, a common, parallel to the stacking direction first outlet and a plurality of perpendicular to the stacking direction, the first inlet channel with the first outlet channel fluidly connecting first connecting channels and for the second fluid a common, parallel to the stacking direction extending second inlet channel, a common, parallel to the stacking direction extending second outlet and a plurality of perpendicular to the stacking direction, the second inlet channel to the second outlet channel fluidly connecting second connection channels are formed.
  • main disks as identical identical parts and to design them so that they can be stacked around a parallel to the stacking direction longitudinal central axis of the stack each rotated by 180 ° to each other to the two fluid paths for forming the first fluid and the second fluid within the stack. With identical main plates then arise identical flow paths for the first and second fluid.
  • the heat release capacity of one fluid may be significantly different than the heat capacity of the other fluid. This can be caused, for example, by different volume flows and / or different heat conduction coefficients within the two fluids. There is therefore a need to be able to adapt such a stacked plate heat exchanger to different fluid and skillsströmungssituationen to improve the efficiency of heat transfer.
  • the present invention is concerned with the problem of providing for a stacked plate heat exchanger of the type mentioned an improved or at least another embodiment, which is particularly characterized in that it is adaptable with a relatively low cost to different flow situations and / or fluid pairings.
  • the invention is based on the general idea of equipping the stacked disk heat exchanger with at least one additional disk, which is arranged in the stacking direction between two adjacent main disks.
  • the additional disk is designed so that in the stack, an additional connection channel (additional connection channel) is formed, which is fluidly connected only with one of its immediately adjacent in the stacking direction connecting channels (main connection channels).
  • additional connection channel additional connection channel
  • main connection channels main connection channels
  • any ratios of integers between first connection channels, that is to say the sum of main connection channels and auxiliary connection channels assigned to the first fluid path, and second connection channels can be realized, ie the sum of main connection channels and additional connection channels assigned to the second fluid path.
  • the respective additional disk has two openings for the first fluid and two openings for the second fluid in the stacking direction in alignment with the main disks, wherein two of the openings are each enclosed by a dome.
  • the dome of the respective additional disk in the stacking direction are higher than the dome of the main disks and / or arranged radially outwardly or inwardly offset relative to the domes of the main disks with respect to a longitudinal central axis of the respective inlet channel or outlet channel. Due to the proposed embodiment and / or positioning of the dome of the additional disc, the additional connecting channel formed in the stack with the aid of the additional disk is connected in parallel to the respective adjacent main connecting channel in terms of its throughflow.
  • the respective auxiliary connection channel in the stacking direction may be substantially the same height as the main connection channels.
  • the respective additional disc may be arranged in the stack that the one main disc, which limits the additional connecting channel in the stacking direction with the respective additional disc is arranged free-standing in the area of their not enclosed by the domes of this main disc openings, so that the additional connection channel through these openings are fluidly connected to the adjacent main connection channel. In this way, an internal bypass is created within the stack, through which the respective fluid in addition, so it can flow parallel to the associated main connection channel.
  • the domes of the respective additional disc may be sized and arranged to engage the domes of one of the adjacent main discs.
  • the domes of the respective additional disc are divided into the formation of the respective inlet channel and outlet channel. This simplifies stacking.
  • the dome of the respective additional disc can be substantially twice as high as the dome of the main discs. This ensures that in the respective additional connection channel the height measured parallel to the stacking direction is substantially the same as in the adjacent main connection channel.
  • the respective additional disc may be arranged in the stack so that it is arranged free-standing in the area of their not enclosed by their domes openings, so that the additional connection channel is fluidly connected through these openings with the adjacent main connection channel. Also in this construction, an internal bypass is realized within the stack, which allows the parallel flow through the additional connection channel and the adjacent main connection channel.
  • the dome of the respective additional disc can be dimensioned and arranged so that they contact the adjacent main disc with respect to the longitudinal central axis of the respective inlet channel or outlet channel radially outside the dome of the adjacent main disc. This design is more tolerant of deviations in the manufacturing process.
  • the dome of the respective additional disc in the stacking direction may be about the same height as the dome of the main discs. This ensures that when outside of the dome of the main disc contacting domes of the additional disc measured in the stacking direction height of the additional connection channel is about the same size as the adjacent main connection channel.
  • the main discs form identical parts, which reduces the unit cost due to higher quantities.
  • the identical main disks are expediently configured in such a way that they can be stacked on one another in such a way that adjacent main disks parallel to the stacking direction are rotated by 180 ° relative to one another in the stacking direction.
  • the stacked disk heat exchanger presented here can in principle make do with a single such additional disk. Likewise, however, several such additional disks can be used at the same time. If two or more auxiliary disks are used, they are configured identically according to an advantageous embodiment, ie also as identical parts. Again, the use of identical parts leads to increased quantities and reduced unit prices.
  • the main disks and the respective additional disk can each have a circulation, wherein the circuits of adjacent disks in the stacking direction, ie two main disks or a main disk and an additional disk, interlock and thereby the connection channels, so the main connection channels and the respective additional connection channel close tightly.
  • revolutions of the main discs and the circulation of the respective additional disc are identical in terms of height and inclination in order to simplify the meshing.
  • Fig. 1-5 comprises a stacked plate heat exchanger 1, which is suitable for heat transfer between a indicated in the figures each by a hollow arrow first fluid 2 and in the figures indicated by a solid arrow second fluid 3, a plurality of main disks 4.
  • the main disks 4 are in a stacking direction. 5 stacked together to form a stack 6.
  • the main disks 4 each have two openings 7, 8 for the first fluid 2 and two openings 9, 10 for the second fluid 3.
  • Two The openings 7, 8, 9, 10, here in each case an opening 8 assigned to the first fluid 2 and an opening 10 assigned to the second fluid 3, are respectively of a dome 11 for the opening 8 and of a dome 12 for the opening 10 edged.
  • the main disks 4 are stacked in the stack 6 so that in the stack 6 for the first fluid 2 a common, parallel to the stacking direction 5 extending first inlet channel 13 and a common, parallel to the stacking direction 5 extending first outlet channel are formed, wherein the first outlet channel in the Sectional views shown here is not visible.
  • a plurality of first main connection channels 14 are formed in the stack 6, which fluidly connect the first inlet channel 13 with said first outlet channel and which run perpendicular to the stacking direction 5.
  • the main disks 4 for the second fluid 3 form a common, parallel to the stacking direction 5 second inlet channel 15 and a common, parallel to the stacking direction 5 extending second outlet channel, which is not recognizable due to the selected sectional planes in the figures.
  • main disks 4 extend perpendicular to the stacking direction 5 extending second main connection channels 16 which fluidly connect the second inlet channel 15 with said second outlet channel.
  • second main connection channels 16 which fluidly connect the second inlet channel 15 with said second outlet channel.
  • the stacked disk heat exchanger 1 presented here is also characterized by at least one additional disk 17, which is arranged in the stacking direction 5 between two adjacent main disks 4.
  • the additional disc 17 has two openings 18, 19 for the first fluid 2 and two openings 20, 21 for the second fluid 3.
  • the four openings 18, 19, 20, 21 of the respective additional disc 17 in the stack 6 axially, ie in the stacking direction 5, arranged in alignment with the four openings 7, 8, 9, 10 of the main disks 4.
  • two of the openings 18, 19, 20, 21 of the respective additional disk 17 respectively provided by a dome 22 for the opening 19 and by a dome 23 for the opening 21, which encloses the respective opening 19 and 21, respectively.
  • the domes 23 of the respective additional disk 17 in the stacking direction 5 are higher, that is larger in size than the domes 11, 12 of the main disks 4 3 and 4
  • the domes 22 of the respective additional disk 17 are arranged offset radially outwards relative to the domes 11, 12 of the main disks 4 with respect to a longitudinal central axis 24 of the respective inlet channel 13 or 15 or the respective outlet channel, not shown here.
  • the respective intermediate disk 17 can be inserted between two adjacent main disks 4 in such a way that an additional connecting channel 25 is formed in the stack 6 and is fluidically connected to one of its main connecting channels 14 or 16 immediately adjacent in the stacking direction 5.
  • the respective additional connecting channel 25 is fluidically connected to a first main connecting channel.
  • the respective additional connecting channel 25 is fluidically connected to one of the second main connecting channels 16.
  • the Fig. 1 and 2 show an embodiment in which within the stack 6 only a single such additional disk 17 is used.
  • exactly two such additional disks 17 are provided in the stack 6 purely by way of example, which accordingly provide two additional connecting channels 25, which in the example of FIG 3 and 4 are each associated with the second fluid 3.
  • shows Fig. 5 purely by way of example an embodiment in which three such additional discs 17 are used, wherein in the example of the Fig. 5 associated with the second fluid 3.
  • the respective additional disc in the in Fig. 1 and 2 shown embodiment associated with the first fluid 2.
  • the respective additional disk 17 is likewise assigned to the second fluid 3.
  • the Fig. 5 embodiment shown corresponds in terms of their construction basically in the Fig. 1 and 2 shown embodiment, so that in terms of constructive details on the embodiments, for example Fig. 1 and 2 can be referenced.
  • the respective additional disk 17 is arranged in the stack 6 in such a way that the one main disk 4 which delimits the additional connecting channel 25 with the respective additional disk 17, that is, the one in the stack Fig. 1 and 2 immediately above the main disc 4, in the region of their not surrounded by the domes 11, 12 of this main disc 4 openings 7, 9 is arranged free-standing.
  • the resulting free-standing edge of the affected main disc 4 is in Fig. 2 denoted by 26.
  • the respective additional connection channel 25 can now communicate fluidically with the adjacent main connection channel 14 through this opening 7 enclosed by the edge 26.
  • an internal bypass is created within the stack 6.
  • the additional connection channel 25 and the fluidically connected main connection channel 14 are connected in fluidic parallel, so that these two connection channels 14, 25 are flowed through in parallel by the respective fluid, here by the first fluid 2.
  • the dome 23 of the respective washer 17 is dimensioned and arranged so that they engage in the dome 12 of one of the adjacent main disks 4.
  • This intervention area is in Fig. 2 surrounded by a circle and denoted by 27.
  • the dome 23 of the washer 17 axially into the dome 12 of the main disk 4, so parallel to the stacking direction 5 can engage, they are shaped accordingly complementary.
  • the measured parallel to the stacking direction 5 distances between adjacent main discs 4 and between the auxiliary disc 17 and the respective adjacent main disc 4 are about the same size
  • the respective dome 23 of the auxiliary disc 17 parallel to the stacking direction 5 is about twice as high as the associated dome 12 of respective main disk 4.
  • two such additional disks 17 are arranged in the stack 6.
  • the upper additional disk 17, which is also referred to below as additional disk 17 ', is arranged in the stack 6 so that it is arranged free-standing in the region of that opening 20 which is not surrounded by a dome 22 of the additional disk 17'.
  • a the respective opening 20 bordering edge of the additional disk 17 ' is in Fig. 3 denoted by 28.
  • the lower auxiliary disk 17, which is also referred to below with 17 ", is like the additional disk 17 in the Fig.
  • the dome 22 of the additional disc 17 are dimensioned and arranged so that they contact the adjacent main disc 4 with respect to the longitudinal central axis 24 of the respective inlet channel 13 and 15 radially outside the dome 11, 12 of the adjacent main disc 4.
  • Contact zones 29, in which the domes 22 of the respective additional disk 17 contact the respective adjacent main disk 4 offset radially outwards to contact zones 30 in which the domes 11 of an adjacent main disk 4 touch the respective additional disk 17 (here the upper auxiliary disk 17 '). , or another main disk 4 touch, here so at the lower auxiliary disk 17 ".
  • These contact areas of the upper and lower auxiliary disk 17 'and 17" are in Fig. 4 each marked by a circle and designated 31.
  • the dome 22 of the auxiliary disks 17 in the stacking direction 5 may be about the same height as the dome 11 and 12 of the main disks. 4
  • main disks 4 are designed identically, that is, that they are identical parts.
  • adjacent main disks 4 are rotated about a parallel to the stacking direction 5 extending longitudinal center axis of the stack 6 by 180 ° to each other, whereby the separate flow paths can form.
  • additional discs 17 are present, they are expediently identical, so designed as equal parts.
  • the main discs 4 as well as the respective additional disc 17 each equipped with a circulation 32.
  • the circulations 32 engage each other and can thereby the main connection channels 14 and 16 as well close the respective additional connection channel 25 tight.
  • the stacked plate heat exchanger 1 shown here comes without an additional housing, so that it is configured without housing.
  • Fig. 1 and 5 can take the stack 6 with respect to the stacking direction 5 end side at least one end plate 33 have to close the stack 6 at this end fluidly tight.
  • Supply and discharge connections for the first and second fluid 2, 3 are then expediently arranged at an end of the stack 6 opposite this end disk 33.
  • the main disks 4, the respective additional disk 17 and the optional end disk 33 are preferably formed sheet metal parts which have the respective circulation 32 and the domes 11, 12, 22 and 23 integrally.

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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)

Claims (12)

  1. Echangeur thermique à plaques empilées servant à transmettre de la chaleur entre un premier fluide (2) et un deuxième fluide (3),
    - comprenant plusieurs plaques principales (4), qui sont empilées les unes sur les autres dans une direction d'empilement (5) et qui forment une pile (6), et qui présentent respectivement deux ouvertures (7, 8) pour le premier fluide (2) et deux ouvertures (9, 10) pour le deuxième fluide (3),
    - dans lequel les plaques principales (4) sont empilées les unes sur les autres dans la pile (6) de telle sorte que sont réalisés, dans la pile (6), pour le premier fluide (2) un premier canal d'admission (13) commun s'étendant de manière parallèle par rapport à la direction d'empilement (5), un premier canal d'évacuation commun s'étendant de manière parallèle par rapport à la direction d'empilement (5) et plusieurs premiers canaux de liaison principaux (14) s'étendant de manière perpendiculaire par rapport à la direction d'empilement (5), reliant de manière fluidique le premier canal d'admission (13) au premier canal d'évacuation, et, pour le deuxième fluide (3), un deuxième canal d'admission (15) commun s'étendant de manière parallèle par rapport à la direction d'empilement (5), un deuxième canal d'évacuation commun s'étendant de manière parallèle par rapport à la direction d'empilement (5) et plusieurs deuxièmes canaux de liaison principaux (16) s'étendant de manière perpendiculaire par rapport à la direction d'empilement (5), reliant de manière fluidique le deuxième canal d'admission (15) au deuxième canal d'évacuation,
    caractérisé en ce
    qu'est prévue au moins une plaque supplémentaire (17), qui est disposée entre deux plaques principales (4) adjacentes de manière à former dans la pile (6) un canal de liaison supplémentaire (25), qui est relié de manière fluidique à un de ses canaux de liaison principaux (14, 16) directement adjacents dans la direction d'empilement (5).
  2. Echangeur de chaleur selon la revendication 1,
    caractérisé en ce
    - que pour la plaque principale (4) respective, deux des ouvertures (8, 10) sont respectivement encadrées par un dôme (11, 12),
    - que la plaque supplémentaire (17) respective présente, dans la direction d'empilement (5), au même niveau que les plaques principales (4), deux ouvertures (18, 19) pour le premier fluide (2) et deux ouvertures (20, 21) pour le deuxième fluide (3), dans lequel deux des ouvertures (19, 21) sont respectivement encadrées par un dôme (22, 23),
    - que les dômes (22, 23) de la plaque supplémentaire (17) respective sont plus hauts dans la direction d'empilement (5) que les dômes (11, 12) des plaques principales (4) et/ou sont disposés de manière décalée radialement par rapport à un axe central longitudinal (24) du canal d'admission (13, 15) respectif ou du canal d'évacuation par rapport aux dômes (11, 12) des plaques principales (4).
  3. Echangeur de chaleur selon la revendication 1,
    caractérisé en ce
    que le canal de liaison supplémentaire (25) respectif est à peu près aussi haut dans la direction d'empilement (5) que les canaux de liaison principaux (14, 16).
  4. Echangeur de chaleur selon la revendication 2 ou 3,
    caractérisé en ce
    qu'au moins une plaque supplémentaire (17) de ce type est disposée de telle sorte dans la pile (6) que la plaque principale (4), qui précisément délimite, avec la plaque supplémentaire (17) respective, le canal de liaison supplémentaire (25), dans la direction d'empilement (5), est disposée de manière isolée dans la zone de ses ouvertures (7, 9) qui ne sont pas encadrées par les dômes (11, 12) de ladite plaque principale (4) si bien que le canal de liaison supplémentaire (25) est relié de manière fluidique par lesdites ouvertures (7, 9) au canal de liaison principal (4) adjacent.
  5. Echangeur de chaleur selon l'une quelconque des revendications 1 à 4,
    caractérisé en ce
    que les dômes (23) de la plaque supplémentaire (17) respective présentent des dimensions telles et sont disposés de telle manière qu'ils viennent en prise avec les dômes (12) d'une des plaques principales (4) adjacentes.
  6. Echangeur de chaleur selon la revendication 5,
    caractérisé en ce
    que les dômes (23) de la plaque supplémentaire (17) respective présentent une hauteur sensiblement deux fois plus grande que les dômes (12) de la plaque principale (4) respective.
  7. Echangeur de chaleur selon l'une quelconque des revendications 1 à 6,
    caractérisé en ce
    qu'au moins une plaque supplémentaire (17) de ce type est disposée dans la pile (6) de telle manière qu'elle est disposée de manière isolée dans la zone de son ouverture (20) qui n'est pas encadrée par son dôme (22) si bien que le canal de liaison supplémentaire (25) est relié de manière fluidique par ladite ouverture (20) au canal de liaison principale (14, 16) adjacent.
  8. Echangeur de chaleur selon l'une quelconque des revendications 2, 3 et 7,
    caractérisé en ce
    que les dômes (22) de la plaque supplémentaire (17) respective présentent une dimension telle et sont disposés de telle manière qu'ils établissent un contact avec la plaque principale (4) adjacente par rapport à l'axe central longitudinal (24) du canal d'admission (13,15) respectif ou du canal d'évacuation de manière radiale à l'extérieur des dômes (11, 12) de la plaque principale (4) adjacente.
  9. Echangeur de chaleur selon la revendication 8,
    caractérisé en ce
    que les dômes (22) de la plaque supplémentaire (17) respective présente à peu près la même hauteur dans la direction d'empilement (5) que les dômes (11, 12) de la plaque principale (4).
  10. Echangeur de chaleur selon l'une quelconque des revendications 1 à 9,
    caractérisé en ce
    que toutes les plaques principales (4) sont configurées de manière identique, dans lequel des plaques principales (4) adjacentes dans la direction d'empilement (5) sont tournées les unes par rapport aux autres de 180° de manière parallèle par rapport à la direction d'empilement (5).
  11. Echangeur de chaleur selon l'une quelconque des revendications 1 à 10,
    caractérisé en ce
    que toutes les plaques supplémentaires (17) sont configurées de manière identique.
  12. Echangeur de chaleur selon l'une quelconque des revendications 1 à 11,
    caractérisé en ce
    que les plaques principales (4) et la plaque supplémentaire (17) respective possèdent respectivement une périphérie (32), dans lequel les périphéries (32) s'imbriquent les unes dans les autres et terminent de manière étanche les canaux de liaison principaux (14, 16) ainsi que le canal de liaison supplémentaire (25) respectif.
EP14199018.4A 2014-01-28 2014-12-18 Échangeur thermique à empilement de disques Active EP2899487B1 (fr)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE102014201456.5A DE102014201456A1 (de) 2014-01-28 2014-01-28 Stapelscheibenwärmeübertrager

Publications (2)

Publication Number Publication Date
EP2899487A1 EP2899487A1 (fr) 2015-07-29
EP2899487B1 true EP2899487B1 (fr) 2017-02-15

Family

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EP14199018.4A Active EP2899487B1 (fr) 2014-01-28 2014-12-18 Échangeur thermique à empilement de disques

Country Status (4)

Country Link
EP (1) EP2899487B1 (fr)
KR (1) KR20150089958A (fr)
CN (1) CN205014870U (fr)
DE (1) DE102014201456A1 (fr)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102020201131A1 (de) * 2020-01-30 2021-08-05 Mahle International Gmbh Wärmeübertrager-Platte für einen Wärmeübertrager, insbesondere für einen Stapelscheiben-Wärmeübertrager oder für einen Platten-Wärmeübertrager

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1084276A (fr) *
NL125884C (fr) * 1965-04-08
DE19757803A1 (de) * 1997-12-24 1999-07-01 Behr Gmbh & Co Wärmeübertrager
DE10152363A1 (de) 2001-10-24 2003-05-08 Modine Mfg Co Gehäuseloser Plattenwärmetauscher
JP2004293880A (ja) * 2003-03-26 2004-10-21 Calsonic Kansei Corp 積層型熱交換器
US7063047B2 (en) * 2003-09-16 2006-06-20 Modine Manufacturing Company Fuel vaporizer for a reformer type fuel cell system
DE10348803B4 (de) * 2003-10-21 2024-03-14 Modine Manufacturing Co. Gehäuseloser Plattenwärmetauscher
BRPI0418955A (pt) * 2004-07-16 2007-12-04 Matsushita Electric Ind Co Ltd trocador de calor
DE102005034305A1 (de) * 2005-07-22 2007-01-25 Behr Gmbh & Co. Kg Plattenelement für einen Plattenkühler
FR2967248B1 (fr) * 2010-11-10 2015-01-23 Valeo Systemes Thermiques Echangeur de chaleur fluide/fluide
DE102011090159A1 (de) * 2011-12-30 2013-07-04 Behr Gmbh & Co. Kg Wärmeübertrager
DE102012202276A1 (de) 2012-02-15 2013-08-22 Mahle International Gmbh Plattenwärmetauscher

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Publication number Publication date
DE102014201456A1 (de) 2015-07-30
KR20150089958A (ko) 2015-08-05
EP2899487A1 (fr) 2015-07-29
CN205014870U (zh) 2016-02-03

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