CN103528419A - Plate for heat exchanger, heat exchanger and air cooler comprising a heat exchanger - Google Patents
Plate for heat exchanger, heat exchanger and air cooler comprising a heat exchanger Download PDFInfo
- Publication number
- CN103528419A CN103528419A CN201310280264.2A CN201310280264A CN103528419A CN 103528419 A CN103528419 A CN 103528419A CN 201310280264 A CN201310280264 A CN 201310280264A CN 103528419 A CN103528419 A CN 103528419A
- Authority
- CN
- China
- Prior art keywords
- heat
- plate
- medium
- elevated portion
- recess
- 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.)
- Granted
Links
Images
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
-
- 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
-
- 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
- F28D9/0056—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 with U-flow or serpentine-flow inside conduits; with centrally arranged openings on the plates
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
- F28F3/02—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
- F28F3/04—Elements 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
- F28F3/042—Elements 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
- F28F3/02—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
- F28F3/04—Elements 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
- F28F3/042—Elements 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
- F28F3/044—Elements 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
- F28F3/12—Elements constructed in the shape of a hollow panel, e.g. with 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
- F28F2240/00—Spacing means
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 present invention relates to a plate (1) for a heat exchanger for heat exchange between a first and a second medium, wherein the plate has a first side (A) and an opposing second side (B), wherein said first side (A) is configured with at least one heat transferring elevation (2) and with at least one heat transfer surface (4) surrounding said elevation, wherein dimples (5, 7) are provided at either or both of the heat transferring elevation (2) and the heat transfer surface (4) to permit provision of a through-flow duct (X) for the first medium, and wherein said second side (B) is configured with at least one heat transferring depression (3) corresponding to said elevation, said depression being configured to define a part of a through-flow duct (Y) for the second medium, and with at least one bonding surface (6) corresponding to said heat transfer surface and surrounding said depression. The present invention also relates to a heat exchanger comprising a stack of the above-mentioned plates and to an air cooler comprising such a heat exchanger.
Description
Technical field
The present invention relates to a kind of for carry out the plate of the heat exchanger of heat exchange between the first and second media.This plate has the first side and the second opposing side.The first side configuration of described plate has at least one heat transmission elevated portion and is configured to allow to provide through-flow channel to first medium.The second side configuration of described plate has with the heat in the first side transmits at least one heat transmission depressed part corresponding to elevated portion, to be defined for a part for the through-flow channel of second medium.
The invention still further relates to a kind of heat exchanger, wherein heat exchanger comprises the heap of above-mentioned plate.Plate is arranged so that the first side adjacency and assembling of the first side and the adjacent panel in sheetpile of each plate, limits thus the through-flow channel of the first medium between described the first side in described plate.Therefore, plate is also arranged so that the second side adjacency and assembling of the second side and the adjacent panel in sheetpile of each plate, limits thus at least one through-flow channel of the second medium between described the second side in described plate.
The invention still further relates to the aerial cooler that comprises above-mentioned heat exchanger.
Background technology
Heat exchanger for example, for many different field, in Food processing industry, in using the building of heating and cooling system, in gas turbine, boiler etc.The heat exchange performance that attempt to improve heat exchanger is interesting all the time, even and very little improvement also obtain the appreciation of height.
Summary of the invention
One object of the present invention is to provide a kind of plate for heat exchanger and heat exchanger, for improvement of elementary and secondary heat exchange.
Above and other object is realized by such plate, the first side of wherein said plate not only configures has at least one heat transmission elevated portion, also configuration has at least one around the heat transfer surface of described elevated portion, and wherein on transmitting the arbitrary of elevated portion or both, heat transfer surface and heat is provided with recess, to allow to be provided for the through-flow channel of first medium, and wherein the second side of plate not only configures and has at least one heat and transmit depressed part, also configuration has corresponding to described heat transfer surface and around at least one mating surface of described depressed part.
Thereby, heat in the first side of plate is transmitted elevated portion and is defined for the primary heat transfer region of first medium with around the heat transfer surface of described elevated portion and for the secondary heat transfer area of first medium, and be positioned at heat in the second side of plate, transmit depressed part and defines the primary heat transfer region for second medium.Thus, provide the plate for heat exchanger, by means of it, defined the larger heat transfer area for described first medium, described first medium is the medium with minimum thermal carry-over factor, for example, the air for water, it should flow with the velocity/pressure compared with little.
By configuring, heat is transmitted elevated portion and corresponding heat is transmitted depressed part, make its width be greater than height/depth several times and make them there is the extension with two or more straight, parallel or substantially parallel parts, having expanded the primary heat transfer region that is respectively used to the first and second media.
Also by heat exchanger, realize above and other object, the first side that wherein said plate is not only arranged so that each plate is in abutting connection with the first side of adjacent panel in sheetpile, also make described plate thus by means of in heat transfer surface and in sheetpile the heat in the first side of two adjacent panel transmit arbitrary in elevated portion or recess on both and be provided for the through-flow channel of the first medium between described first side of described plate, and the second side that described plate is not only arranged so that each plate is in abutting connection with the second side of the adjacent panel in sheetpile, also make described plate by means of heat in the second side of two adjacent panel in sheetpile, transmit depressed part thus and be defined at least one through-flow channel of the second medium between described second side of described plate.
Thereby, because the relative recess in the heat transfer surface by means of being arranged in the first side of two adjacent panel of sheetpile is provided for the through-flow channel of first medium, and owing to transmitting depressed part and define the through-flow channel for second medium by being arranged in relative heat in the second side of two adjacent panel of sheetpile, a kind of heat exchanger is provided, by means of it, has defined the larger volume for the through-flow channel of described first medium.
Due to by width, be many times of the degree of depth, be the heat transfer surface of through-flow channel with respect to its volume and Yan Geng great and extension have two relatively hot transmission depressed parts straight, parallel or substantially parallel part defines the through-flow channel for second medium, improved the primary heat transfer performance of heat exchanger.
As limited, a kind of heat exchanger is provided, its total heat exchange performance is improved and its manufacturing cost reduces.
As limited, heat exchanger can be for providing for example improved aerial cooler, and a kind of medium is air, and another kind is liquid.
Accompanying drawing explanation
Below with reference to annexed drawings, further describe the present invention, wherein
Fig. 1 is according to the perspective schematic view of plate of the present invention embodiment;
Fig. 2 is another perspective view of the plate of Fig. 1;
Fig. 3 is according to the schematic plan view of a side of the embodiment of the plate of Fig. 1 and Fig. 2;
Fig. 4 is the schematic plan view of opposite side of the plate of Fig. 3;
Fig. 5 is a part of schematic side elevation of the plate of Fig. 1-4;
Fig. 6 is the perspective schematic view of having assembled according to the two boards of Fig. 1-4;
Fig. 7 is the schematic side elevation after the two boards of Fig. 6 is assembled;
Fig. 8 be assembling after according to the schematic diagram of four of Fig. 1-4 plates;
Fig. 9 a is the perspective schematic view according to heat exchanger of the present invention, and it comprises the sheetpile of the plate as shown in Fig. 1-8;
The heat exchanger that Fig. 9 b schematically shows Fig. 9 a how to be arranged in refrigerator display case and how the first and second media flow through heat exchanger;
Figure 10 is according to the perspective schematic view of the second embodiment of plate of the present invention, and
Figure 11 is according to the perspective schematic view of a part of the 3rd embodiment of plate of the present invention.The specific embodiment
Just as has been stated, the present invention relates to a kind of for carry out the plate of the heat exchanger of heat exchange between the first and second media.
The first and second media for heat exchange can be identical, for example gas/gas (such as air) or liquid/liquid (such as water).The first and second related media can be also two kinds of different media, for example gas/liquid or two kinds of different gas or liquid.
Especially as shown in Fig. 1-6, plate 1 has the first side A and the second side B.The first side A configuration of plate 1 has at least one heat and transmits elevated portion 2.
The first side A of plate 1 is also configured to allow the through-flow channel X(that is provided for first medium referring to Fig. 8).The second side B of plate 1 is configured to have at least one heat of the elevated portion 2 corresponding essentially on the first side A and transmits depressed part 3, be that depressed part defines the elevated portion 2 in described first side of plate, and there is substantially the same length and width, and its degree of depth equals the height of described elevated portion.Heat is transmitted through-flow channel Y(that depressed part 3 is configured to be defined for second medium referring to Fig. 7 and 8) a part.By making plate 1 stand for example punching press or perforation processing, make heat transmit elevated portion 2 and correspond to each other with heat transmission depressed part 3.If needed, can be respectively on the first side A of plate 1 and the second side B, a plurality of elevated portion 2 and corresponding depressed part 3 be set.
As particularly evident from Fig. 1,3 and 6, the first side A of plate 1 also configures has at least one heat transfer surface 4, and it transmits elevated portion 2 around heat.This heat transfer surface 4 disposes recess 5, and it allows to be provided for the through-flow channel X of first medium.Elevated portion 2 on the first side A of plate 1 defines the primary heat transfer region for first medium, and defines the secondary heat transfer area for first medium around the heat transfer surface 4 of described elevated portion.These primary and secondary heat transfer area, for example the region of described elevated portion 2 and the region sum of described heat transfer surface 4 are substantially equal to the overall area of the first side A of plate 1.Correspondingly, as being apparent that from Fig. 2,4 and 6, the second side B of plate 1 also configures has at least one mating surface 6, its corresponding to, there is identical extension with the heat transfer surface 4 on the first side A, and it correspondingly transmits depressed part 3 around heat.Depressed part 3 defines the primary heat transfer region for second medium.This primary heat transfer region, be the region that region that the region of depressed part 3 is substantially equal to described second side of plate deducts mating surface 6.According to above-mentioned, clearly, for the combination heat transfer area of first medium, be greater than the heat transfer area of second medium.When first medium has less heat transfer coefficient, such as the air with respect to water, and should be to flow than the less velocity/pressure of second medium so that when best heat transfer is provided, this feature is favourable.The heat exchanger that comprises the plate as above building will have the heat exchange performance of improvement.
Thereby, by the surface directly contacting on a kind of parts of plate of medium, provide primary heat transfer region as defined above, and the opposing surface of wherein said parts directly contacts another medium, and provide secondary heat transfer area by the surface directly contacting on a kind of parts of plate of medium, and the apparent surface of wherein said parts does not directly contact another medium.
In order to allow to be provided for the through-flow channel X of first medium, heat on the first side A of plate 1 is transmitted elevated portion 2 configurations and is had the first height h1, and recess 5 in heat transfer surface in described the first side has the second height h2, wherein h2 is greater than described the first height (especially referring to Fig. 5).Thus, recess 5 projects upwards higher than elevated portion 2.The heat corresponding to elevated portion 2 on plate 1 second side B is transmitted depressed part 3 so is configured to its degree of depth and is substantially equal to described the first height h1.Heat on plate 1 first side A is transmitted elevated portion 2 and in the illustrated embodiment of plate, is equipped with additional recess 7, to allow to be provided for the through-flow channel X of first medium.For this purpose, these additional recesses 7 are greater than described the first height with (first) height h1 sum of elevated portion 2.In the embodiment shown, the height h1 of the height of recess 7 and elevated portion 2 is substantially equal to the second height h2, the height of the recess 5 in instant heating transfer surface 4.Thereby the height of recess 7 is that h2 deducts h1.According in the described embodiment of the plate of Fig. 1-8, heat transmission elevated portion 2 on the first side A of plate has the first height h1 of the about 0.5-1 millimeter of the hot transfer surface 4 of distance, and corresponding heat transmission depressed part 3 on the second side B of plate has the degree of depth that is substantially equal to described the first height apart from mating surface 6, and recess 5 in the hot transfer surface of side A has the second height h2 of the about 2-2.5 millimeter of the described hot transfer surface of distance.Yet these highly can and will use the size of the heat exchanger of plate to change according to the application of expection therein.Can prepare in any suitable manner the recess 5 and 7 on the first side A of plate 1, punching press and the puncture of for example by being similar to heat, transmitting elevated portion 2/ depressed part 3 are processed, thereby on the second side B of plate, in mating surface 6 and depressed part, form respectively corresponding depressed part, and there is described elevated portion/depressed part simultaneously.The pattern of size, shape and the quantity of recess 5,7 and their settings also can change according to the size of desired application and heat exchanger.Plate 1 is larger, provides distance and the strong point to allow to be provided for the recess more than 5,7 of the through-flow channel X of first medium needs.Yet, it should be emphasized that, according to the present invention, can also be only by means of the recess 5 in heat transfer surface 4 or only transmit by means of heat the through-flow channel X that recess 7 in elevated portion 2 can allow to be provided for first medium.In an illustrated embodiment, recess 5,7 is circular substantially.
Shape, size, quantity and position that the heat transmission depressed part 3 of a part of the upper through-flow channel Y for second medium of the second side B of limiting plate and the corresponding heat on the first side A of plate are transmitted elevated portion 2 can change.Therefore, depressed part 3 and corresponding elevated portion 2 can be for example U-shapeds, comprise two straight, parallel or substantially parallel parts.Yet, in order to extend the heat exchanger time between the first and second media, depressed part 3 and corresponding elevated portion 2 can alternately have sinusoidal shape substantially, it has three or more straight, parallel or substantially parallel part, i.e. straight, the parallel or substantially parallel part of odd number (referring to Figure 10) or (referring to Fig. 1-8) even number.In order to maximize the heat exchange between the first and second media, advantageously, if the heat transfer area of depressed part 3 and corresponding elevated portion 2 is large as far as possible with respect to the volume of the through-flow channel Y for second medium.Therefore, the width w of depressed part 3 and corresponding elevated portion 2 is greater than the degree of depth of described depressed part and the corresponding height of elevated portion in the embodiment shown substantially, and for example large 5 times, and preferably in the embodiment shown, approximately 50-70 is doubly.Therefore, to have the first height h1 be about 0.5-1mm, heat transmits elevated portion 2 and have the corresponding heat that the degree of depth equals described the first height transmits in the illustrated embodiment of depressed part 3, the width w of elevated portion and respective recesses portion will be at least about 2.5mm, and preferred about 25-70mm.The width w of depressed part 3 and corresponding elevated portion 2 can be constant, or can change along its length, especially as shown in Fig. 1-4,6 and 10.In Fig. 1-4,6 and 10, first the width w that shows straight parallel portion reduces, and increases back its original width subsequently.Thereby if the first height h1 and respective depth are about 0.5mm, the width w that heat is transmitted elevated portion 2 and corresponding heat transmission compression unit 3 can be reduced to about 25mm from about 35mm, and is increased to about 35mm subsequently again.At depressed part 3, is connected the part place of its straight parallel portion with corresponding elevated portion 2, width w is far smaller than described straight portion office, is greater than in the embodiment shown the first h1 and corresponding to its approximately 20 times of the degree of depth highly.Similarly, in having the illustrated embodiment of rectangular slab 1, depressed part 3 and corresponding elevated portion 2 can be equipped with straight parallel portion, and it is advanced along the horizontal direction that longitudinally or substantially becomes that is transverse to plate.If needed, described straight parallel portion can plate 1 longitudinally on or in other required directions, alternately advance arbitrarily.
In order to prevent from compressing the through-flow channel Y of second medium, the heat on plate 1 second side B is transmitted depressed part 3 and is disposed resistance to compression recess 8.These resistance to compression recesses 8 are highly substantially equal to described the first height h1 in the embodiment shown, instant heating transmits the height of elevated portion 2, therefore and equal the degree of depth that heat is transmitted depressed part, thereby these recesses 8 finish in the outstanding same level of depressed part substantially.The horizontal plane identical by the mating surface 6 on the second side B with plate 1 finishes, described recess 8 can mesh the corresponding recess in another plate second side, to prevent from compressing the through-flow channel Y of second medium, and can contribute to safe by described recess is bonded to each other in the mode of matching and effectively the second side of described the second side and described other plates be assembled.By form turbulent flow in described flowing, recess 8 also promotes second medium to flow through through-flow channel Y, thereby has improved heat exchange effect.Yet if needed, the height of recess 8 can be less than described the first height h1.In an illustrated embodiment, recess 8 has circle and elongated shape.Some elongated recesses or bending.Recess 8 can also be set to the pattern of any appropriate, for optimization heat exchange effect.
In an embodiment who schematically shows at Figure 11, resistance to compression recess 8 is elongated, and transmit depressed part 3 extension that tilts in heat, preferably parallel to each other, and when the second side B of two boards 1 is together time, tilt by the through-flow channel Y of second medium, the preferred whole width of logical heat transfer depressed part/through-flow channel, and described elongated recess described heat transmit depressed part/through-flow channel longitudinally on be spaced apart from each other.Heat is transmitted some required some bifurcated that elevated portion 2/ depressed part 3 can be between elongated recess 8, and gang more at once subsequently, so that to the recess 5 extending from heat transfer surface 4 but not transmit from heat the recess 7 that elevated portion 2 extends space is provided, thereby, on the first side A of plate 1, only there is having the recess of the second height h2.Elongated recess 8 preferably has leg-of-mutton cross section substantially, but also can have other required cross sections arbitrarily, the example cross section of conical butt substantially as shown in figure 11.Recess 8 is arranged so that when the second side B of two boards 1 is adjacent to each other together, and described recess intersects advances, preferably rectangular each other, and a plurality of points for meshing are provided, and described recess can be assembled each other.
On the relative first side A of plate 1, thereby heat is transmitted elevated portion 2 by the elongated recess 8 in the heat transmission depressed part 3 on the second side B of plate and interrupts, described recess transmits in heat " groove " 8a that limits corresponding configuration in elevated portion thus, and it forms a part of the through-flow channel X of first medium.Therefore, these " grooves " 8a transmits elevated portion 2 updips in heat and tiltedly extends, and preferably from a side to opposite side, and is spaced apart from each other, and defines betwixt " rib-like " part 2a that heat is transmitted elevated portion.As described above, some such " rib-like " part 2a interrupt, and preferably in the central authorities of its longitudinal extension part, think that recess 5,6 provides space.As from Figure 11 clearly, the impression that this embodiment provides is, more appropriate is thinks that the heat of the first side A of plate 1 transmits elevated portion and comprise that a plurality of independently heat elongated, parallel and that tilt to extend transmits elevated portion, and what advance therebetween is the part (8a limits by " groove ") of heat transfer surface 4.
Above-mentioned and provide the strong through-flow channel Y that is used in particular for second medium as the embodiment being schematically shown in Figure 11, but according to above clearly, if needed, elongated recess 8 also can relative to each other extend with non-parallel direction, and the recess 7 that transmits " rib-like " part 2a extension of elevated portion 2 from heat can be provided.
In order to promote that by strengthening through-flow channel first medium flows through through-flow channel X and prevents that it from subsiding, the heat transfer surface 4 on the first side A of plate 1 is equipped with in a similar manner strengthens recess 9.These are strengthened recesses 9 and are highly substantially equal in the embodiment shown described the first height h1, and instant heating transmits the height of elevated portion 2, thus recess substantially with elevated portion 2 in same horizontal plane.Yet what need is that the height of recess 9 is less than described the first height h1, and preferably as far as possible little, so that minimize the mobile pressure drop of first medium in through-flow channel X, and still maintain the strengthening performance of recess.The height of recess 9 can also be greater than described the first height, as long as it does not exceed (second) height h2 of recess 5.In the embodiment shown, recess 9 has elongated shape.Recess 9 can also be set to the pattern of any appropriate, for optimization heat exchanger effectiveness.
Transmit elevated portion 2/ depressed part 3 with the heat that allows to provide the through-flow channel X of first medium and above-mentioned recess 5,7 the same, for example can by punching press or puncture process or with other suitable modes arbitrarily, and described elevated portion/depressed part and described above-mentioned recess 5,7 side by side form recess 8 and 9.It is upper that corresponding depressed part is formed on each opposite side A, the B of plate 1 thus, in the elevated portion on side A 2 respectively with the mating surface 6 of side B in.
As mentioned above, plate 1 can be rectangle, has two short side 1c and 1d that relative long side 1a is relative with 1b and two, and has the first and second apertures 10 and 11 that approach one or two long side and/or approach the first medium of one or two short side.The shape of plate 1 is depended in the position in aperture 10,11, and the heat on plate is transmitted shape and the position of elevated portion 2 and corresponding heat transmission depressed part 3.There is elevated portion 2 and comprising in the illustrated embodiment of rectangular slab 1 straight parallel portion, respective recesses portion 3 of even number, one of in the long side 1a that each 10,11 location, aperture is close identical and short side 1c, 1d, be arranged in the bight that described long side and each short side (referring to Fig. 1-4) limit.Use elevated portion 2 and the respective recesses portion 3 that comprises the straight parallel portion of Odd number, each aperture 10,11 for example locate near one of in long side 1a, 1b with short side 1c, 1d in one of, in the bight that each long side and each short side limit, i.e. on plate 1 (referring to Figure 10) relatively diagonally each other.Described in each, aperture 10,11 is positioned on described the first side A that configures respectively the plate with edge 10a and 11a, and it is around described aperture.Each edge 10a, 11a form a part for elevated portion 2, and height is corresponding to the second height h2 in the embodiment shown, corresponding to height and the elevated portion 2(h1 of recess 5) and recess 7(h2-h1) combined altitudes, and can there is identical function with described recess, allow to be provided for the through-flow channel X of first medium, and prevent that second medium from leaking the through-flow channel X that enters first medium.Plate 1 can be used as selectively as square, has four isometric limits, or other suitable quadrangles, triangle, polygon, circle, rhombus, ellipse or for other shapes with its application or purposes arbitrarily.
According in the illustrated embodiment of Fig. 1-8 at least, wherein the desired use of plate 1 is at the heat exchanger for refrigerator display case, and the length of plate 1 can be about 270 millimeters, and width is about 150 millimeters.Yet plate 1 can have for its optimized other sizes arbitrarily of expection application institute.Therefore, the length of plate 1 can for example surpass 1 meter, and its width can be over 0.5 meter.Based on plate for example how in heat exchanger and/or through-flow channel X, the Y of the first and second media how directed, the size of plate 1 can also be less than the plate in illustrated embodiment, and the width of plate can be greater than its length.
As mentioned above, the invention still further relates to for carry out the heat exchanger of heat exchange between the first and second media, wherein said heat exchanger comprises the heap of the plate 1 with said structure.The heap of this plate 1 can be positioned in the more or less open type framework 12 as shown in Fig. 9 a thus, it has relative panel element 13 and 14, wherein in relative panel element, one of at least (in Fig. 9 a, being panel element 13) is equipped with and has the pipe jointer 15 and 16 for second medium, and top board 17 and local unlimited base plate 18.The heap of the plate 1 of framework 12 shown in can being arranged in can comprise 360 blocks of plates, if the total height of every block of plate is about 2.5 millimeters, so total height is approximately 900 millimeters.Yet according to its expection application or purposes, in sheetpile, the quantity of plate 1 can change, and thereby the size of heat exchanger also can change.
If heat exchanger is in the refrigerator display case as shown in Fig. 9 b, the base plate 18 of its middle frame 12 down, the top board 17 of framework upward, and the relative panel element 13,14 of framework is towards side, plate in sheetpile 1 will in turn extend in substantially parallel perpendicular so, and first medium (for example,, by cooling air) will essentially horizontally flow into and flow through heat exchanger.Thereby, first medium can be for example from its left side inflow heat exchanger, and essentially horizontally pass through subsequently heat exchanger to the right, and leave heat exchanger on its right side, or as shown in Fig. 9 b, from the right side of heat exchanger, flow into, then essentially horizontally direction is passed through heat exchanger left (as shown in the arrow D2 in Fig. 9 b), and leaves heat exchanger in its left side.The second medium water of cooling-air (for example for) is by by providing one of the pipe jointer 15,16 of panel element 13 therein and inflow heat exchanger, along sinuous path substantially and flatly pass through heat exchanger, 16, its straight parallel or substantially parallel part (in Fig. 9 b by shown in arrow D1) in substantially vertical direction is advanced, and the described pipeline by described panel element connects, and in 15, another leaves heat exchanger.According in the illustrated embodiment of Fig. 9 b, second medium is inflow heat exchanger by the left side tube connector 15 of panel element 13, and leaves heat exchanger by right side tube connector 16.Thereby, according to Fig. 9 b, first medium is at substantially horizontal direction upper reaches over-heat-exchanger, and second medium with contrary horizontal direction along substantially vertically and substantially sinuous path pass through heat exchanger, thereby when two media has maximum temperature, cooling first medium is run into for cooling second medium with heat transmission or heat exchange method, thereby and described first medium cooling by progressively colder second medium.Realized multistep adverse current, wherein made to repeat cooling first medium contact for cooling second medium, described second medium passes through heat exchanger along substantially vertical with substantially sinusoidal path flow in contrary horizontal direction.Come the condensate of self cooled first medium by the base plate 18 by partly open leaves heat exchanger in bottom.Can provide in the bottom of heat exchanger drainage tube (not shown), for collecting condensate.Thereby the framework 12 of heat exchanger contributes to discharge condensate from heat exchanger.Similarly, by shown in framework 12 contribute to heat exchanger as shown in the figure check, clean and safeguard.
As above point out, the first side A that plate 1 in interchanger in sheetpile is arranged so that every block of plate is in abutting connection with the first side A of adjacent panel in sheetpile, transmits the recess 7 in elevated portion 2 and the through-flow channel X for first medium between described first side of described plate is provided thus by means of the recess 5 in heat transfer surface 4 and/or by means of the heat in the first side of adjacent two boards in sheetpile.And, the second side B that plate 1 is arranged so that every block of plate, in abutting connection with the second side B of adjacent panel in sheetpile, transmits depressed part 3 and limits at least one the through-flow channel Y for second medium between described second side of described plate by means of the heat in the second side of adjacent two boards in sheetpile thus.
By for example configuring every block of plate 1, make the second height h2 of the recess 5 on the first side A of plate be greater than the degree of depth (equaling the first height h1 that heat is transmitted elevated portion) that heat on the second side B of plate is transmitted depressed part 3, and the area that the heat in described first side of plate is transmitted elevated portion 2 and heat transfer surface 4 is greater than the area that heat in the second side of plate is transmitted depressed part, as mentioned above, when making respectively the first side A of adjacent two boards 1 and the second side B of adjacent two boards be adjacent to each other, can be so that the volume of the through-flow channel X of first medium be greater than the volume of the through-flow channel Y of second medium.Similarly, also can be so that recess and elevated portion/depressed part depart from.As shown in Fig. 7 and 8, when the relative recess 7 in the elevated portion 2 when the relative recess 5 by means of in heat transfer surface 4 and/or in by means of sheetpile on the first side A of adjacent two boards is provided for the through-flow channel of first medium, and when the relative depressed part 3 in sheetpile on the second side B of adjacent two boards is defined for the through-flow channel of second medium, the volume of the through-flow channel X of described first medium, with respect to the volume of the through-flow channel Y of described second medium, further increases.
For the sheetpile of the plate 1 of safety durable is provided, departing from or the 5 places assembling of unswerving recess in sheetpile in the heat transfer surface 4 of the first side A of adjacent two boards in described the first side, and the mating surface 6 places assembling of the second side B of adjacent two boards in described the second side in sheetpile.If there is recess 7 on heat is transmitted elevated portion 2, so in sheetpile the first side A of adjacent two boards also can or as alternatively in this recess place assembling.Thereby because the combination heat transfer area on the first side A of plate 1 is greater than the heat transfer area on plate the second side B, the total bond area in described first side of plate is less than the calmodulin binding domain CaM in described second side of plate.Adjacent panel 1 can be assembled by means of for example brazed process or by means of another suitable assemble method.At least in sheetpile, on opposite edges 10a, the 11a in the aperture 10,11 of the first side A of adjacent two boards, need leakproof assembling on the relative mating surface of the second side B of adjacent two boards 1 and in sheetpile.
According to clearly above-mentioned, the differing heights that recess 5 and heat are transmitted elevated portion 2/ depressed part 3 will provide configuration to have the alternately through-flow channel X for first medium of height, that is, when described first medium from the left flow direction right side or Fig. 8 from right flow to left with as Fig. 9 b from a right flow direction left side.Should the velocity/pressure of first medium during flowing through described through-flow channel X will be changed by height alternately.Thereby, according in the embodiment shown in Fig. 1-8 at least, for the through-flow channel X of first medium, be configured in heat on the first side A of adjacent two boards 1 and transmit between elevated portion 2 and there is third high degree h3, and in described first side of described adjacent two boards around thering is the 4th height h4 that is greater than described third high degree between the heat transfer surface of described elevated portion.The 4th height h4 is substantially equal to the twice of (second) height h2 of the recess 5 in the heat transfer surface 4 on the first side A of every block of plate 1 thus, and third high degree h3 is substantially equal to the described the 4th twice that highly deducts (first) height h1 of the elevated portion 2 in the first side of every block of plate.
According in the illustrated embodiment of Fig. 1-8 at least, through-flow channel Y configuration for second medium has the 5th height h5, and it is substantially equal to the twice (especially referring to Fig. 7) that heat on the second side B of every block of plate 1 is transmitted the degree of depth (transmitting (first) height h1 of elevated portion 2 corresponding to heat) of depressed part 3.
The sheetpile of the plate 1 in heat exchanger can comprise the plate of a type.Heat on every plate the first side A is for example transmitted elevated portion 2 and the heat on every block of plate the second side B and is transmitted depressed part 3 when having the sinusoidal shape substantially of straight, parallel or substantially parallel part of equal amount, is exactly this situation (as according in the embodiment of the plate of Fig. 1-8).Alternatively, the sheetpile of plate 1 can comprise the plate of two types.Heat on the first side A of for example every block of plate is transmitted heat on the second side B of elevated portion 2 and every block of plate and is transmitted depressed part 3 when having the sinusoidal shape substantially of straight, parallel or substantially parallel part of Odd number, is exactly this situation (as according in the embodiment of the plate of Figure 10).And if different if the recess 5 for example on adjacent two boards and/or heat are transmitted the height of described elevated portion on the first side A that elevated portion 2/ depressed part 3 relative to each other departs from a plate and/or the described elevated portion on the height of described recess and the first side A of another piece plate and/or described recess, so by the plate 1 that also needs two types.The height of recess 5 and/or elevated portion 2/ depressed part 3 can change widely, but it is naturally important that in thering is described the latter embodiment of two kind templates, the total height of recess is greater than the total height of relative elevated portion at least relatively, for the through-flow channel X for first medium between the first side A in two adjacent panel is provided.
According to heat exchanger of the present invention, it can be cross flow one type, wherein being defined for heat on the second side B of two adjacent panel 1 of through-flow channel Y of second medium transmits straight, the substantially parallel part of depressed part 3 and extends on the first direction D1 of plate, and wherein provide at the through-flow channel X for first medium between the first side A of adjacent two boards and extend on the second direction D2 at plate, wherein second direction is substantially perpendicular to described first direction.As mentioned above, above-mentioned heat exchanger is mainly the heat exchanger of the type.It is selectively the another type different from described cross flow one type that heat exchanger according to the present invention can be used as.
The heat exchanger being defined as above by use, comprising the sheetpile of the plate being defined as above, in fact, when for example using water cooling from the air of refrigerator display case, may reduce cooling energy consumption approximately 20%.The main cause of this positive result is, the temperature of cooling water needn't reduce with prior art structure in like that mainly with the effective cooling that air is provided.This is the result of the more directly extensive and mediate contact of air and water prolongation.
To be apparent that to those skilled in the art, according to can, in the scope of claim of enclosing, plate according to the present invention and heat exchanger being modified and be changed, and do not depart from concept of the present invention and object.Thereby, although being preferably aluminium, makes plate 1, it also can be made by any other suitable materials.The sheetpile of the plate in heat exchanger can be arranged in more unlimited framework, and as according to shown in the embodiment shown in Fig. 9 a, and framework also can be made by the material of any appropriate.And clearly, heat exchanger can be positioned at the position of any appropriate in the application of its expection, if as shown in embodiment level or need or wish, can be for vertically or tilt.The heat exchanger being defined as above is applicable to aerial cooler, because first medium, can be air by cooling medium.
Claims (15)
1. for carry out a plate for the heat exchanger of heat exchange between the first and second media,
Wherein plate (1) has the first side (A) and opposing the second side (B), first side (A) of wherein said plate (1) is configured to have that at least one heat is transmitted elevated portion (2) and around at least one heat transfer surface (4) of described elevated portion, wherein heat transmit elevated portion (2) and heat transfer surface (4) one of or both on recess (5 is set, 7) to allow to be provided for the through-flow channel (X) of first medium
At least one heat that second side (B) of wherein said plate (1) is configured to have corresponding to described elevated portion (2) is transmitted depressed part (3), described depressed part is configured to be defined for a part for the through-flow channel (Y) of second medium, and the second side has corresponding to described heat transfer surface (4) and around at least one mating surface (6) of described depressed part
The first height (h1) that wherein heat in first side (A) of plate (1) is transmitted elevated portion (2) equals the degree of depth that heat in second side (B) of plate is transmitted depressed part (3), and width (w) equals the width that heat is transmitted depressed part (3),
Wherein the heat in second side (B) of plate (1) is transmitted depressed part (3) and is provided with resistance to compression recess (8), and the height of described resistance to compression recess equals heat and transmits described first height (h1) of elevated portion (2) and the degree of depth that corresponding heat is transmitted depressed part.
2. plate according to claim 1, the recess (5) being wherein arranged in the heat transfer surface (4) in first side (A) of plate (1) has the second height (h2) that is greater than described the first height (h1), and/or is wherein arranged on heat in first side (A) of plate (1) and transmits the height (h2-h1) of the recess (7) in elevated portion (2) and height (h1) sum that heat is transmitted elevated portion and be greater than described first highly (h1).
3. plate according to claim 1 and 2, wherein to transmit the width (w) that elevated portion (2) and corresponding heat transmits depressed part (3) be at least 5 times that described heat is transmitted described first height (h1) of elevated portion and the degree of depth of corresponding heat transmission depressed part to heat.
4. according to the plate described in any one in claim 1-3, wherein the corresponding heat in second side (B) of the transmission elevated portion (2) of the heat in first side (A) of plate (1) and plate is transmitted depressed part (3) and is configured to have two or more straight, parallel or substantially parallel parts.
5. according to the plate described in any one in claim 1-4, wherein resistance to compression recess (8) is elongated and is arranged to transmit depressed part (3) updip in heat and tiltedly extends, and described heat transmit depressed part longitudinally on be spaced apart from each other.
6. according to the plate described in any one in claim 1-5, wherein the heat transfer surface (4) in first side (A) of plate (1) is configured to have reinforcement recess (9).
7. according to the plate described in any one in claim 2-6, wherein plate (1) is configured to have the first and second apertures (10 for second medium, 11), the first and second apertures (10 described in each, 11) described the first side (A) that is positioned at plate (1) goes up and is configured to have the edge (10a around described aperture, 11a), described edge forms described heat and transmits the part of elevated portion (2) and its described the second height (h2) that highly equals recess (5) and/or equal to be arranged on heat and transmit the height (h2-h1) of the recess (7) in elevated portion (2) and height (h1) sum that described heat is transmitted elevated portion.
8. for carry out a heat exchanger for heat exchange between first medium and second medium, wherein said heat exchanger comprises by the sheetpile forming according to the plate (1) described in any one in claim 1-6,
Wherein said plate (1) is arranged so that the first side (A) butt of every block of plate first side (A) of the adjacent panel (1) in sheetpile, by means of the heat transfer surface (4) in first side (A) of the adjacent two boards in sheetpile or heat, one of transmit in elevated portion (2) thus or the recess (5 on both, 7), the through-flow channel for first medium between described first side of described adjacent two boards (X) is provided, and
The second side (B) that makes every block of plate (1), in connection with second side (B) of the adjacent panel (1) in sheetpile, is transmitted depressed part (3) by means of the heat in second side (B) of the adjacent two boards in sheetpile thus and is defined at least one through-flow channel (Y) for second medium between described second side of described adjacent two boards.
9. heat exchanger according to claim 8, wherein the heat transfer surface (4) of first side (A) of the adjacent two boards (1) in sheetpile in described the first side and heat one of are transmitted in elevated portion (2) or the relative recess (5 on both, 7) locate assembling, and by locating leakproof and combine and assemble at described opposite edges place around the opposite edges (10a, 11a) in described first side of the aperture for second medium (10,11) in described plate.
10. heat exchanger according to claim 8 or claim 9, wherein the heat in second side (B) of the adjacent two boards (1) in sheetpile is transmitted resistance to compression recess (8) in depressed part (3) and is disposed for when second side (B) of the adjacent two boards (1) in sheetpile is against each other engaging one another.
11. heat exchangers according to claim 10, wherein second side (B) of the adjacent two boards (1) in sheetpile by by relative mating surface (6) leakproof in described the second side be bonded to each other and assemble, and the relative recess (8) that the heat in described the second side is transmitted depressed part (3) is located assembling.
Heat exchanger in 12. according to Claim 8-11 described in any one, the heat being wherein defined in second side (B) of adjacent two boards (1) of through-flow channel (Y) of second medium is transmitted straight, the parallel or substantially parallel part of depressed part (3) upper extension of first direction (D1) of plate, and be wherein arranged on the through-flow channel for first medium (X) between first side (A) of adjacent two boards (1) upper extension of second direction (D2) of plate, wherein second direction is substantially perpendicular to described first direction (D1).
Heat exchanger in 13. according to Claim 8-12 described in any one, wherein the plate of heat exchanger (1) heap is positioned in the framework (12) with relative panel element (13,14).
14. heat exchangers according to claim 13, wherein at least one relative panel element (13,14) is equipped with and has the pipe jointer (15,16) for second medium.
15. 1 kinds of aerial coolers, comprise the heat exchanger described in any one according to Claim 8-14, and wherein first medium is air, and second medium is liquid.
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP12175135.8 | 2012-07-05 | ||
| US13/541,788 US20140008046A1 (en) | 2012-07-05 | 2012-07-05 | Plate for heat exchanger, heat exchanger and air cooler comprising a heat exchanger |
| EP12175135.8A EP2682702B1 (en) | 2012-07-05 | 2012-07-05 | Plate for heat exchanger, heat exchanger and air cooler comprising a heat exchanger. |
| US13/541,788 | 2012-07-05 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103528419A true CN103528419A (en) | 2014-01-22 |
| CN103528419B CN103528419B (en) | 2017-03-01 |
Family
ID=48699687
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310280264.2A Expired - Fee Related CN103528419B (en) | 2012-07-05 | 2013-07-05 | For the plate of heat exchanger, heat exchanger and the air cooler including heat exchanger |
Country Status (4)
| Country | Link |
|---|---|
| EP (1) | EP2682703B1 (en) |
| JP (1) | JP2014016144A (en) |
| KR (1) | KR20140005795A (en) |
| CN (1) | CN103528419B (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2018066532A (en) * | 2016-10-21 | 2018-04-26 | パナソニックＩｐマネジメント株式会社 | Heat exchanger and refrigeration system using the same |
| CN109328291A (en) * | 2016-10-21 | 2019-02-12 | 松下知识产权经营株式会社 | Heat exchanger and the refrigerating plant for using it |
| CN110044200A (en) * | 2019-04-19 | 2019-07-23 | 富奥汽车零部件股份有限公司 | A kind of heat exchanger plates and the plate heat exchanger using the heat exchanger plates |
| CN114599929A (en) * | 2020-02-04 | 2022-06-07 | 翰昂汽车零部件有限公司 | Dimple cooler with dimples |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6531325B2 (en) * | 2015-02-18 | 2019-06-19 | 有限会社和氣製作所 | Heat exchanger |
| KR101717093B1 (en) * | 2015-07-23 | 2017-03-27 | 주식회사 경동나비엔 | Heat exchanger |
| PT3171115T (en) | 2015-11-18 | 2019-09-09 | Alfa Laval Corp Ab | Plate for heat exchange arrangement and heat exchange arrangement |
| SE542079C2 (en) | 2017-05-11 | 2020-02-18 | Alfa Laval Corp Ab | Plate for heat exchange arrangement and heat exchange arrangement |
| EP3447427B1 (en) * | 2017-08-22 | 2020-03-18 | InnoHeat Sweden AB | Heat exchanger |
| DE102018002201B4 (en) | 2018-03-19 | 2021-03-18 | EAW Energieanlagenbau GmbH Westenfeld | Water-lithium bromide absorption refrigeration system |
| CN111735070B (en) * | 2020-06-29 | 2022-07-15 | 浙江澄源环保科技有限公司 | Catalytic combustion equipment and catalytic combustion method for VOC gas |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6321495A (en) * | 1986-07-14 | 1988-01-29 | Nippon Denso Co Ltd | Lamination type heat exchanger |
| CN1151207A (en) * | 1994-06-20 | 1997-06-04 | 平板公司 | Three-circuit stacked plate heat exchanger |
| US6648062B2 (en) * | 2000-07-31 | 2003-11-18 | Honda Giken Kogyo Kabushiki Kaisha | Heat sink-type cooling device |
| CN1875240A (en) * | 2003-10-28 | 2006-12-06 | 贝洱两合公司 | Flow channel for a heat exchanger and heat exchanger with the same |
| WO2009080564A2 (en) * | 2007-12-21 | 2009-07-02 | Alfa Laval Corporate Ab | Heat exchanger |
| EP2267391A2 (en) * | 2009-06-26 | 2010-12-29 | SWEP International AB | Asymmetric heat exchanger |
| CN201867114U (en) * | 2010-11-26 | 2011-06-15 | 辽宁远东换热设备制造有限公司 | Heat exchange plate of plate heat exchanger |
| CN102466420A (en) * | 2010-11-15 | 2012-05-23 | 丰田自动车株式会社 | Vehicle heat exchanger |
Family Cites Families (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3207216A (en) * | 1963-02-27 | 1965-09-21 | Borg Warner | Heat exchanger |
| US3845814A (en) * | 1972-07-10 | 1974-11-05 | Union Carbide Corp | Finned primary surface heat exchanger |
| US4043388A (en) * | 1975-04-14 | 1977-08-23 | Deschamps Laboratories, Inc. | Thermal transfer care |
| US4470455A (en) * | 1978-06-19 | 1984-09-11 | General Motors Corporation | Plate type heat exchanger tube pass |
| JPH03140795A (en) * | 1989-10-25 | 1991-06-14 | Hitachi Ltd | Lamination type heat exchanger |
| JPH07151486A (en) * | 1993-09-30 | 1995-06-16 | Sanden Corp | Heat exchanger |
| KR100353020B1 (en) * | 1993-12-28 | 2003-01-10 | 쇼와 덴코 가부시키가이샤 | Multilayer Heat Exchanger |
| JP3612826B2 (en) * | 1995-11-29 | 2005-01-19 | 三菱電機株式会社 | Heat exchange element |
| JP3965901B2 (en) * | 2000-10-27 | 2007-08-29 | 株式会社デンソー | Evaporator |
| JP2004011936A (en) * | 2002-06-03 | 2004-01-15 | Nissan Motor Co Ltd | Heat exchanger |
| CA2389119A1 (en) * | 2002-06-04 | 2003-12-04 | Christopher R. Shore | Lateral plate finned heat exchanger |
| US7264045B2 (en) * | 2005-08-23 | 2007-09-04 | Delphi Technologies, Inc. | Plate-type evaporator to suppress noise and maintain thermal performance |
| US20080041556A1 (en) * | 2006-08-18 | 2008-02-21 | Modine Manufacutring Company | Stacked/bar plate charge air cooler including inlet and outlet tanks |
| SE536042C2 (en) * | 2010-06-16 | 2013-04-09 | Titanx Engine Cooling Holding Ab | Heat exchanger with extended heat transfer surface around attachment points |
-
2013
- 2013-07-04 JP JP2013141166A patent/JP2014016144A/en active Pending
- 2013-07-04 KR KR1020130078221A patent/KR20140005795A/en not_active Application Discontinuation
- 2013-07-04 EP EP13175040.8A patent/EP2682703B1/en not_active Not-in-force
- 2013-07-05 CN CN201310280264.2A patent/CN103528419B/en not_active Expired - Fee Related
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6321495A (en) * | 1986-07-14 | 1988-01-29 | Nippon Denso Co Ltd | Lamination type heat exchanger |
| CN1151207A (en) * | 1994-06-20 | 1997-06-04 | 平板公司 | Three-circuit stacked plate heat exchanger |
| US6648062B2 (en) * | 2000-07-31 | 2003-11-18 | Honda Giken Kogyo Kabushiki Kaisha | Heat sink-type cooling device |
| CN1875240A (en) * | 2003-10-28 | 2006-12-06 | 贝洱两合公司 | Flow channel for a heat exchanger and heat exchanger with the same |
| WO2009080564A2 (en) * | 2007-12-21 | 2009-07-02 | Alfa Laval Corporate Ab | Heat exchanger |
| EP2267391A2 (en) * | 2009-06-26 | 2010-12-29 | SWEP International AB | Asymmetric heat exchanger |
| CN102466420A (en) * | 2010-11-15 | 2012-05-23 | 丰田自动车株式会社 | Vehicle heat exchanger |
| CN201867114U (en) * | 2010-11-26 | 2011-06-15 | 辽宁远东换热设备制造有限公司 | Heat exchange plate of plate heat exchanger |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2018066532A (en) * | 2016-10-21 | 2018-04-26 | パナソニックＩｐマネジメント株式会社 | Heat exchanger and refrigeration system using the same |
| CN109328291A (en) * | 2016-10-21 | 2019-02-12 | 松下知识产权经营株式会社 | Heat exchanger and the refrigerating plant for using it |
| CN109416229A (en) * | 2016-10-21 | 2019-03-01 | 松下知识产权经营株式会社 | Heat exchanger and the refrigerating plant for using it |
| CN109416229B (en) * | 2016-10-21 | 2020-06-02 | 松下知识产权经营株式会社 | Heat exchanger and refrigerating apparatus using the same |
| CN110044200A (en) * | 2019-04-19 | 2019-07-23 | 富奥汽车零部件股份有限公司 | A kind of heat exchanger plates and the plate heat exchanger using the heat exchanger plates |
| CN114599929A (en) * | 2020-02-04 | 2022-06-07 | 翰昂汽车零部件有限公司 | Dimple cooler with dimples |
Also Published As
| Publication number | Publication date |
|---|---|
| EP2682703B1 (en) | 2018-03-28 |
| KR20140005795A (en) | 2014-01-15 |
| JP2014016144A (en) | 2014-01-30 |
| CN103528419B (en) | 2017-03-01 |
| EP2682703A1 (en) | 2014-01-08 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103528419A (en) | Plate for heat exchanger, heat exchanger and air cooler comprising a heat exchanger | |
| US20140158328A1 (en) | Plate for heat exchanger, heat exchanger and air cooler comprising a heat exchanger | |
| KR102291431B1 (en) | Heat exchanging board and board-type heat exchanger provided with heat exchanging board | |
| DK2585783T3 (en) | Exchanger plate and plate heat exchange | |
| JP6357480B2 (en) | Fin-tube heat exchanger | |
| US20120012291A1 (en) | Plate heat exchanger and refrigeration air conditioner | |
| JP5872859B2 (en) | Heat exchanger | |
| KR102231142B1 (en) | Heat exchanger plate and heat exchanger | |
| KR20150143682A (en) | Laminated header, heat exchanger, and air conditioner | |
| EP2682702B1 (en) | Plate for heat exchanger, heat exchanger and air cooler comprising a heat exchanger. | |
| CN203940771U (en) | Cascade type collector, heat exchanger and aircondition | |
| CN105371684B (en) | A kind of heat exchanger plate chip architecture | |
| EP3077753A1 (en) | Heat exchanging plate with varying pitch | |
| US20140008046A1 (en) | Plate for heat exchanger, heat exchanger and air cooler comprising a heat exchanger | |
| CN105387741B (en) | A kind of heat exchanger plate group of Novel asymmetric channel design | |
| EP3336469A1 (en) | Profiled joint for heat exchanger | |
| JP5414502B2 (en) | Plate heat exchanger and heat pump device | |
| CN104919266A (en) | Heat exchanger for air-conditioning device | |
| JP4874365B2 (en) | Plate heat exchanger and refrigeration cycle apparatus using the heat exchanger | |
| CN106802099A (en) | A kind of heat exchanger | |
| CN205300358U (en) | Heat exchanger sheet structure | |
| CN103837032B (en) | The fin of heat exchanger and heat exchanger | |
| EP3551954B1 (en) | Recuperator | |
| JP6422585B2 (en) | Plate heat exchanger | |
| JP2009079779A (en) | Plate-type heat exchanger and air conditioning device using the same |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| REG | Reference to a national code |
Ref country code: HK Ref legal event code: DE Ref document number: 1192001 Country of ref document: HK |
|
| EXSB | Decision made by sipo to initiate substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| REG | Reference to a national code |
Ref country code: HK Ref legal event code: WD Ref document number: 1192001 Country of ref document: HK |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170301 |