CN109210971A - Multiplate heat exchanger - Google Patents
Multiplate heat exchanger Download PDFInfo
- Publication number
- CN109210971A CN109210971A CN201810996311.6A CN201810996311A CN109210971A CN 109210971 A CN109210971 A CN 109210971A CN 201810996311 A CN201810996311 A CN 201810996311A CN 109210971 A CN109210971 A CN 109210971A
- Authority
- CN
- China
- Prior art keywords
- heat exchanger
- fin
- bushing
- pipeline
- multiplate
- 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.)
- Pending
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
- F28F1/12—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
- F28F1/24—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely
- F28F1/26—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely the means being integral with the element
- F28F1/28—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely the means being integral with the element the element being built-up from finned sections
-
- 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
- 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
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2270/00—Thermal insulation; Thermal decoupling
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Geometry (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The present invention relates to especially for the Multiplate heat exchanger (1) of vehicle application, with multiple fins (2) being stacked on stacking direction (5), it forms fin storehouse, wherein, each fin (2) is respectively formed the multiple openings (4) surrounded by bushing (3), and the bushing (3) of adjacent fins (2) is connected to each other, to form each pipeline (6) for the pipe-line system (7) of first flow path (8) for being used for first fluid in the region of the bushing (3) of connection, and the second flow path (9) of second fluid is formed between adjacent fins (2), described device also has end plate (10) in the end of fin storehouse, it is located remotely from each other on stacking direction (5), wherein, the pipeline (6) mutually fluidly connects in end plate (10).Such finned heat-exchange device (1) is particularly capable of making it possible that low cost is produced with simple, and can be assembled as pipe free construction.
Description
Technical field
The present invention relates to especially for the Multiplate heat exchanger of vehicle application.
Background technique
Heat-transfer arrangement is used to thermal energy being transferred to one other fluid from a kind of fluid.In heat transfer process, heat is special
Not not therefore, exchanged, i.e. the temperature of fluid becomes balanced.Therefore, the first hot fluid is by heat-transfer arrangement by colder the
Two fluids and cool down, wherein second fluid be heated or first fluid be colder fluid and by the second hot fluid by
Heating, wherein second fluid is cooled.Therefore heat-transfer arrangement is applied in much applications.Such as in the car, as
Charger-air cooler, they will be supplied to the pressurized air of internal combustion engine for cooling, or as exhaust gas heat-transfer arrangement
Or as the heat generated by internal combustion engine to be discharged in case his heat-transfer arrangement.
Summary of the invention
Therefore, the problem to be solved by the invention is to provide the improvement of the heat-transfer arrangement for the type being mentioned at the beginning that or
Person is at least interchangeable embodiment, and feature is particularly to simplify production.
The present general inventive concept heat-transfer arrangement finned based on formation.For this purpose, the finned heat transmitting dress
It sets comprising multiple fins being stacked in the stacking direction, forms fin storehouse.Herein, each fin all has by axis
Serve as a contrast surrounded opening, wherein the bushing of adjacent fins is connected to each other, to will form use in the region of the connection bushing
In each pipeline of the pipe-line system of the first flow path of first fluid.Fin is stacked, thus the bushing forms pipe-line system
These pipelines, opening and corresponding bushing through respective fin.In addition, the second flow path of second fluid passes through fin
It stacks and is formed between adjacent fin.Second flow path is generated from there through the fin for being spaced apart from each other stacking.Finned heat passes
Delivery device also includes end plate in the end of fin storehouse, is located remotely from each other in the stacking direction.End plate therefrom relative to
Stacking direction is arranged on the opposite end of Multiplate heat exchanger.End plate is also formed or is equipped in this way, to make
The pipeline fluid obtained in end plate mutually fluidly connects.The feature of such heat-transfer arrangement is particularly between respective pipeline
The deflection of first fluid carries out in Multiplate heat exchanger, and the Multiplate heat exchanger is built as in it
Portion is no pipe.
In a kind of advantageous embodiment, the edge of respective fin is formed in at least side of Multiplate heat exchanger
On, i.e., the described edge is on the direction perpendicular to stacking direction, and in this way, they form the closure of fin storehouse in the side
Side wall.For this purpose, the respective edges of fin have the shape with fin plane in drift angle, wherein the neighboring edge phase mutual connection of fin
Touching.The edge of side wall is formed thus with identical angle and in a same direction with corresponding fin in drift angle.Herein,
The two sides of Multiplate heat exchanger are positioned opposite to each other, in a preferred embodiment, each pass through fin respective edges
Formation and form closure side wall.
Other embodiments be also it is contemplated that, wherein pass through being correspondingly formed for the edge of each corresponding fin, wing
The adjacent side of chip heat-transfer arrangement will form the closure side wall of fin storehouse, wherein in this case, adjacent wall
Common angle optionally allows to be recycled to and the respective shapes at corresponding fin or edge in the area from a side wall adjacent
Side wall.It is particularly advantageous by the side wall that the formation of fin edges as described here generates, i.e., other components
Using or assembly can be omitted.
Alternatively, in contrast, in a preferred embodiment, Multiplate heat exchanger is relative to stacking direction
Shell in the transverse direction of transversal orientation by relative positioning two side walls and in the stacking direction pass through second flow path
End plate and limit, and the latter is thus surrounded to pipe-like in a circumferential direction, while in their longitudinal direction, by second
Road penetrates and includes two unlatching longitudinal ends, so that a longitudinal end forms the entrance of second fluid, while another
A longitudinal end forms the outlet of second fluid.
In practice, pipeline is arranged in second flow path, and the pipeline passes through second fluid on all sides as a result,
Circulation causes between the fluid of two flow paths through the especially intensive heat exchange of the wall and fin of pipeline.In another kind
It in preferred embodiment, may be provided that, pipeline passes through second transverse to the longitudinal direction of Multiplate heat exchanger
Road and extend, and be to be set parallel to each other in the longitudinal direction of Multiplate heat exchanger and transverse direction.It is based on
This, may be implemented compact configuration.
In another advantageous embodiment, individual fin can stack in this way, i.e., the axis accordingly connected
Lining adjoins each other.Direct neighbor and the bushing of connection in particular contact with each other as a result,.In this case, it adjoins each other
The connection of corresponding bushing realized optionally by junction, such as welding junction and solder joint.
The bushing of corresponding fin can be formed as arbitrary shape and size.However, it is advantageous that bushing is formed as justifying
Tapered form.These particularly result in corresponding fin and simply stack, to simply connect adjacent bushing or phase
The opening answered, and extraly ensure the space between independent fin.As other examples of bushing shape, that mentions herein has
Cylindrical, ellipse, hyperboloid and paraboloid bushing.It is also contemplated that such embodiment, wherein bushing quilt of different shapes
It uses.It herein, is not all bushings orientation all having the same of Multiplate heat exchanger.It particularly, is not wing
Thus all bushings of piece are protruded from corresponding fin in a same direction.Particularly, bushing can also be with such side
Formula forms, i.e., they are on the flow direction of first fluid or on the direction opposite with the flow direction or along fin
Stacking direction or the direction opposite with the stacking direction on from fin protrude.For this purpose, forming the adjacent channel of pipe-line system
The adjacent bushing of fin for example formed in an opposite direction.Such molding of bushing is particularly used for weakening or enhance
Such as the purpose of the braking of the flowing generated by bushing edge.Accordingly, for the certain of the first fluid flow velocity for flowing through pipeline
Influence be it is possible, in this way, the heat exchanger time in Multiplate heat exchanger is transformable.
It should be pointed out that individual bushing and the single opening without that must include corresponding fin.Simultaneously comprising multiple
The bushing of the opening of corresponding fin is also feasible.
In another embodiment, each end plate has one or more openings, each of these is used to the
One or second fluid supply to Multiplate heat exchanger or discharge it.The supply of such first fluid or discharge for example by
It is arranged in the region of respective end plates, wherein two pipelines of pipe-line system mutually fluidly connect.Herein, it supplies preferably
It is arranged in an end plate, and is discharged and is arranged in another end plate on the other side.In other embodiments, supply and discharge
Occur in identical end plate, however, the embodiment of the end plate comprising multiple supplies and/or discharge is also feasible.
According to another embodiment, the end plate of Multiplate heat exchanger is formed in this way, i.e., they distinguish
In the fin of the outer contacting direct neighbor of the opening or bushing of these fins.Herein, these contacts are line or face, and
And optionally for the fin by end plate connection to respective direct neighbor.Herein, which for example passes through connection method reality
It is existing.Contact between end plate and adjacent fins can establish between tubes now to be fluidly connected, and ensures the first and second fluids
Two flow paths between isolation.For this purpose, the end plate is for example comprising plate hollow space, wherein individual plate hollow space exists
Their own end contact, and thus adjacent fin is contacted in the open outer side region of these fins.End plate it is hollow
Space preferably has well-regulated, particularly periodic setting in this case.
In an advantageous embodiment, the plate hollow space of at least one end plate is formed in this way, i.e., they are every
One is connected the outlet end of single pipeline with the arrival end of single other pipelines.Connecting tube is consequently formed in plate hollow space
The corresponding pipeline of first fluid is connected with each other by road.In this case the corresponding outlet end of pipeline or arrival end relative to
The first flow path of first fluid and define, also by the connecting pipe of end plate and thus, plate hollow space is determined.It can replace
Change ground, plate hollow space formed in this way, i.e., each of which by the outlet end of multiple pipelines with it is a number of other
The arrival end of pipeline is connected.Connecting cavity is consequently formed in plate hollow space, influences flow path and thus influences mentioned outlet
End and arrival end.In addition, other embodiments are also feasible, wherein end plate include one or more connecting pipes and
Any combination of one or more connecting cavities and connecting pipe and connecting cavity.
In another advantageous embodiment, the bushing or opening of independent fin are formed in this way, i.e. pipeline
The pipeline of system extends parallel to each other.For this purpose, the fin bushing of Multiplate heat exchanger for example towards identical direction or
The opposite direction of person.Additionally or alternatively, pipeline extends along the route successively transverse to second fluid flowing direction.
Herein, these routes, which can have, is arranged in parallel.However, the setting of such route is also feasible, wherein in second
The route mutually followed on the flow direction of body is mutually aligned or is arranged with deviating transverse to the flow direction of second fluid.
According to another advantageous embodiment, at least one bushing extends through at least one pipe formed by bushing
Road.The bushing specifically now is used for such purpose, and independent fin is made for example to become possible by the connection of welding.This
Outside, the bushing particularly strengthens the stability of Multiplate heat exchanger by support function.
The fin and end plate of Multiplate heat exchanger preferably by during Multiplate heat exchanger is run due to hot item
Part and transmitted with appropriate heat and the heat proof material with desired capacity of heat transmission manufactures.Especially metal and metal close
Gold, such as aluminium, sheet metal and nickel-base alloy and aluminium alloy.Single fin and Multiplate heat exchanger and corresponding
The extremely simple and thus inexpensive production of bushing and opening in this case particularly by punching press or interior high pressure at
Type (hydro-forming) and be possibly realized.Such production method continuous material, particularly metal or metal alloy for being made of
Independent fin is particularly preferred.However, the opening of other forms, such as oval or oval and pointed is also feasible
's.
In addition it should be pointed out that Multiplate heat exchanger allows simple assembling and is easy the size changed.By
This only changes the number of fins of Multiplate heat exchanger to change the size of Multiplate heat exchanger.Thus may be used
It omits and prepares other components, such as various sizes of pipe.Therefore, Multiplate heat exchanger can be used for much on the way.Its
Possible example is exhaust gas heat-transfer arrangement, evaporator, waste gas circulation cooler, charger-air cooler, condenser, heat biography
Delivery device, conditioner and waste heat utilization device.
The other important feature and advantage of the present invention are by dependent claims, attached drawing and with reference to the accompanying drawings the attached drawing that is done is said
It is bright and obtain.
It should be understood that the mentioned above and feature that still will be described below and not only with the corresponding combination use,
But also be applied to other combinations or be used alone, it does not depart from the scope of the present invention.
Currently preferred illustrative embodiments are shown in the accompanying drawings and more detailed explanation in following discussion,
Wherein, identical appended drawing reference indicates the identical component of identical or similar or function.
It schematically shows in each case,
The detailed side view of Fig. 1 Multiplate heat exchanger,
The cross section of Fig. 2 Multiplate heat exchanger,
The perspective view of the Multiplate heat exchanger of Fig. 3 and 4 different embodiments,
The cross section of the details of the Multiplate heat exchanger of Figures 5 and 6 different embodiments.
According to Fig. 1 to 6, Multiplate heat exchanger 1 includes fin 2, is stacked on stacking direction 5, therein
Each includes the opening 4 surrounded by bushing 3.Herein, the fin 2 of the fin 2 Yu direct neighbor of stacking is separately.This
Outside, the bushing 3 of adjacent fins 2 is connected with each other on stacking direction 5.It is connected by these, the adjacent bushing on stacking direction 5
3 are respectively formed the pipeline 6 of pipe-line system 7.The pipeline 6 of pipe-line system 7 also forms the first flow path 8 of first fluid.In addition, especially
Ground passes through the space of adjacent fins 2 and bushing 3, and the second flow path 9 of second fluid generates between adjacent fin 2.In addition,
As shown in Fig. 2 to 4, Multiplate heat exchanger 1 also includes two end plates 10, wherein the stream of the pipeline 6 of first fluid
Body is connected in these end plates 10 and establishes.
In the embodiment shown in figure 1, the bushing 3 of each fin 2 is shaped to the shape of cone.In addition, all
The bushing 3 of fin 2 all has identical size and is orientated in a same direction, i.e., all bushings 3 are on stacking direction 5
It is protruded by corresponding fin 2.Two edges 11 of each fin 2 relatively position between each other, with the phase on stacking direction 5
Answer fin 2 in drift angle.The mutual face contact in edge 11 of direct neighbor fin 2 adjacent on stacking direction 5 as a result, wherein side
The angle of edge 11 has determined the space between each fin 2 and adjacent fins 2.Pass through the identical size and shape at all edges 11
Shape, and the identical angle at all edges 11 adjacent on 5 in the stacking direction in the corresponding side of fin 2, thus every
Identical space is obtained between the fin 2 of direct neighbor in kind situation.By the space, conical bushing 3 can fall into
In opening 4 or in bushing 3, the direct neighbor on the stacking direction 5 of the fin 2 of direct neighbor.It will form pipeline system as a result,
The parallelpiped 6 of system 7 is parallel to the extension of stacking direction 5.The edge 11 of each fin 2 of direct neighbor in the stacking direction
Face contact the closure side wall 12 of fin storehouse is formed also in corresponding side.Herein, the edge 11 of mutual face contact is logical
It crosses junction 14 and is connected with each other in corresponding contact area 13.
In Multiplate heat exchanger 1 shown in Fig. 2, the bushing 3 of fin 2 has tapered form.Fin 2 is with this
The mode of sample stacks, i.e., each connected bushing 3 mutually abuts and by junction 14 through resulting contact zone
Domain 13 and be connected with each other.The end plate 10 of this Multiplate heat exchanger 1 include hollow space 15, be of the same size and
Shape, and be isolated each by isolated part 16, each isolated part 16 is also of the same size and shape.It is stacking
An end plate 10 on direction 5 is arranged on the top of Multiplate heat exchanger 1, is connected to perpendicular to stacking direction 5
Direction 17 on pipeline 6, by 15 direct neighbor of hollow space, and one connected by hollow space 15 is isolated
A pipeline 6 and connection by isolated part 16 on direction 17 between another pipeline 6 of direct neighbor.End plate 10 it is hollow
Space 15 is consequently formed as connecting pipe.Between two pipelines 6 above-mentioned being isolated by the isolated part 16 of upper head plate 10
Connection realized by hollow space 15 relative to another bottom plate 10 of stacking direction 5, bottom plate 10 and upper head plate
10 hollow spaces 15 and isolated part 16 with same shape and size.For this purpose, the hollow space 15 of bottom plate 10 relative to
Upper head plate 10 deviates the half of 15 width of hollow space on direction 17.Each end plate also passes through their isolated part 16
Contact respective straight connects adjacent fin 2 in the flat site of these fins 2 except bushing 3 and opening 4.Herein, end plate
10 form in this way, i.e., the space between the isolated part 16 of two direct neighbors of each end plate 10 is corresponded in side
The space of two pipelines 6 of direct neighbor is double on to 17.In addition, 16 face contact of isolated part that end plate 10 passes through them
Each adjacent fin 2.In the face contact region, end plate 10 is connected to adjacent fin 2 by junction 14.
Multiplate heat exchanger 1 shown in figure 3 and 4 is on the upper head plate 10 on stacking direction 5 also comprising opening
18, by pipe 19 make it possible first fluid to pipe-line system 8 supply or discharge.Herein, end plate 10 is opened
Mouth 18 is arranged on the hollow space 15 of end plate 10, is made in the finned heat on the direction of stacking direction 5 20
The pipeline column 22 of transfer device be the outermost of Multiplate heat exchanger 1 on the direction of stacking direction 5 21
Pipeline column 22 are connected with each other.The hollow space 15 is designed to connecting cavity therefrom.Finned heat shown in figure 3 and 4 passes
The upper head plate 10 with different hollow spaces is also shown in the embodiment of delivery device 1.
The upper head plate 10 of Multiplate heat exchanger 1 shown in fig. 3 includes hollow space 15, each makes in side
The pipeline 6 of direct neighbor is connected with each other on to 21.Between these hollow spaces 15, end plate 10 has isolated part 16, simultaneously
Any connection between adjacent pipeline 6 on direction 20 is not allowed.These hollow spaces 15 are consequently formed as connecting pipe.
The hollow space 15 of the upper head plate 10 of embodiment shown in Fig. 4 has corresponding to heat-transfer arrangement 1 on direction 20
The length of length, and the width corresponding to the space of two pipelines 6 of direct neighbor on direction 21.These are hollow as a result,
Each of space 15 is connected to the pipeline column 22 of the direct neighbor on direction 21, and extends on direction 20.In these
It is consequently formed as connecting cavity for absolutely empty 15.
According to Fig. 3 and 4, the shell 25 of Multiplate heat exchanger 1 is orientated transverse to stacking direction 5 in a circumferential direction
Transverse direction 20 on limited by the two side walls 12 that are located opposite to each other and by two end plates 10 on stacking direction 5
Second flow path 9.Shell 25 is also penetrated in its radial direction 21 by second flow path 9, and includes second in its longitudinal end
The entrance 26 of fluid and outlet 27.
Multiplate heat exchanger 1 is also constructed so that pipeline 6 is arranged in shell 25 and in second flow path 9.This
Outside, provided pipeline 6 transverse to the longitudinal direction 21 of Multiplate heat exchanger 1 or shell 25 by second flow path 9 and
Extend on the longitudinal direction 21 and transverse direction 20 of Multiplate heat exchanger 1 or shell 25, is successively arranged in parallel.
Although in figures 3 and 4, pipeline 6 has been simplified description, they can also be comprising bushing 3 and similar to Fig. 1
The construction of the respective embodiment of statement and Figures 5 and 6 with 2.
Lining in the details of the fin storehouse of Multiplate heat exchanger 1 shown in Fig. 4, in each shown pipeline 6
Set 23 is coaxially arranged and contacts with these pipelines 6.Each bushing 23 is also connected to accordingly by contact position
Pipeline 6.Thus bushing 23 is particularly used for connection fin 2 and further stable Multiplate heat exchanger 1.However, not having
The embodiment of such bushing 23 is preferred.
Fig. 6 shows the stacking fin 2 of Multiplate heat exchanger 1.Herein, all bushings 3 are shaped to cone
Shape.In addition, two bushings 3 of the independent fin 2 of direct neighbor have opposite orientation on direction 17.Bushing 3 is therefrom
It forms in this way, i.e., it, and should on direction 17 in bushing 3 during being protruded on stacking direction 5 by corresponding fin 2
The bushing 3 of 3 direct neighbor of bushing is protruded with on the opposite direction of stacking direction 5 by corresponding fin 2.In addition, fin heap
The bushing 3 of stack forms in this way, i.e., the bushing 3 of each same pipeline 6 is in a same direction by corresponding fin 2
Protrusion, i.e., it is all on stacking direction 5 or all equal and stacking directions 5 are opposite.As a result, especially by bushing 3
Edge 24, and by the appropriate selection of the flow direction of pipeline 6 perhaps flow path 8 can influence first fluid flow velocity or
Flow resistance and heat transmitting.
Claims (15)
1. a kind of Multiplate heat exchanger (1) for vehicle application,
Have multiple fins (2), stacked spaced reciprocally on stacking direction (5), forms fin storehouse,
Wherein, each fin (2) includes multiple openings (4) surrounded by bushing (3),
Wherein, the bushing (3) of adjacent fins (2) is connected to each other, to be formed in the region of connection bushing (3) for the
Each pipeline (6) of the pipe-line system (7) of the first flow path (8) of one fluid,
Wherein, between adjacent fins (2), the second flow path (9) of second fluid is formed,
There is upper and lower two end plates (10), mutually isolated on stacking direction (5), end plate (10) in the end of fin storehouse
Comprising hollow space (15), the hollow space (15) is of the same size and shape, and each by isolated part
(16) it is isolated, each isolated part (16) is also of the same size and shape, and wherein bottom plate has identical with upper head plate
The hollow space (15) and isolated part (16) of shape and size, the hollow space of bottom plate is relative to upper head plate in direction thus
(17) deviate the half of hollow space (15) width on, each end plate in bushing (3) and is opened by isolated part (16)
Contact respective straight connects adjacent fin (2) in the flat site of fin (2) except mouth (4),
Wherein, in end plate (10), pipeline (6) is fluidly connected between each other,
Wherein, the deflection of the first fluid between respective pipeline carries out in Multiplate heat exchanger, and described finned
Heat-transfer arrangement is built as being no pipe inside it.
2. Multiplate heat exchanger according to claim 1, it is characterised in that the edge (11) of fin (2) is in this way
It is formed on at least side of Multiplate heat exchanger (1), i.e. its closure side wall (12) for forming fin storehouse.
3. Multiplate heat exchanger according to claim 2, it is characterised in that Multiplate heat exchanger (1) its transverse to
Shell (25) in the transverse direction (20) of stacking direction (5) orientation passes through two relative positionings relative to each other in a circumferential direction
Side wall (12) and second flow path (9) are surrounded by end plate (10) on stacking direction (5), while in its longitudinal direction
(21) it on, is penetrated by second flow path (9) and in entrance (26) of its longitudinal end comprising second fluid and outlet (27).
4. Multiplate heat exchanger according to claim 1, it is characterised in that pipeline (6) is arranged in second flow path (9).
5. Multiplate heat exchanger according to claim 4, it is characterised in that pipeline (6) is transverse to Multiplate heat exchanger
(1) longitudinal direction (21) is extended through second flow path (9), and the longitudinal direction in Multiplate heat exchanger (1)
(21) and in transverse direction (20) it is set in parallel to each other.
6. Multiplate heat exchanger according to claim 1, it is characterised in that the bushing (3) of fin (2) is the shape of cone
Shape.
7. Multiplate heat exchanger according to claim 1, it is characterised in that the bushing (3) of fin (2) is in first fluid
It flow direction on flow direction or with first fluid is protruded on opposite direction by respective fin (2).
8. Multiplate heat exchanger according to claim 1, it is characterised in that each end plate (10) is opened comprising at least one
Mouth (18) is used to supply first fluid to pipe-line system (7) or by its discharge.
9. Multiplate heat exchanger according to claim 1, it is characterised in that
Each end plate (10) in opening (4) or the fin (2) of the outer side contacts direct neighbor of bushing (3), and
It is contacted by these, forms fluidly connecting between pipeline (6), and
By the contact, the interval between two flow paths (8,9) of the first and second fluids is kept.
10. Multiplate heat exchanger according to claim 9, it is characterised in that
Contact between end plate (10) and respectively adjacent fin (2) is line or face, and/or
By the contact, end plate (10) is secured to the fin (2) of direct neighbor.
11. Multiplate heat exchanger according to claim 1, which is characterized in that each end plate (10) is comprising absolutely empty in plate
Between (15), by it, corresponding pipeline (6) is mutually fluidly connected in the end plate (10).
12. Multiplate heat exchanger according to claim 1, which is characterized in that
The plate hollow space (15) of at least one end plate (10) forms connecting pipe, each of these is all connected with single pipeline
(6) arrival end of outlet end and single other pipelines (6), or
The plate hollow space (15) of at least one end plate (10) forms connecting cavity, each of these is all connected with multiple pipelines
(16) arrival end of outlet end and a number of other pipelines (6).
13. Multiplate heat exchanger according to claim 1, it is characterised in that
Pipeline (6) extends parallel to each other, and/or
Pipeline (6) is in turn arranged in the route of second fluid, extends transverse to the flow direction (9) of second fluid,
Wherein, pipeline (6) be mutually aligned along the route on the flow direction (9) of second fluid or transverse to second fluid flowing
Deviate ground setting in direction (9).
14. Multiplate heat exchanger according to claim 1, which is characterized in that the bushing (3) connected adjoin each other and/
Or it is connected with each other by junction (14).
15. Multiplate heat exchanger according to claim 1, which is characterized in that at least one bushing (23) extend through by
At least one pipeline (6) that bushing (3) is formed, and the bushing that insulate (3).
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE102011076172.1 | 2011-05-20 | ||
| DE102011076172A DE102011076172A1 (en) | 2011-05-20 | 2011-05-20 | Finned heat exchangers |
| CN201280024443.3A CN103733012A (en) | 2011-05-20 | 2012-05-16 | Multiplate heat exchanger |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201280024443.3A Division CN103733012A (en) | 2011-05-20 | 2012-05-16 | Multiplate heat exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109210971A true CN109210971A (en) | 2019-01-15 |
Family
ID=46124360
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810996311.6A Pending CN109210971A (en) | 2011-05-20 | 2012-05-16 | Multiplate heat exchanger |
| CN201280024443.3A Pending CN103733012A (en) | 2011-05-20 | 2012-05-16 | Multiplate heat exchanger |
Family Applications After (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201280024443.3A Pending CN103733012A (en) | 2011-05-20 | 2012-05-16 | Multiplate heat exchanger |
Country Status (6)
| Country | Link |
|---|---|
| US (1) | US20140305621A1 (en) |
| EP (1) | EP2710318A1 (en) |
| JP (1) | JP5864731B2 (en) |
| CN (2) | CN109210971A (en) |
| DE (1) | DE102011076172A1 (en) |
| WO (1) | WO2012159958A1 (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| PT2730878T (en) * | 2012-11-07 | 2019-05-30 | Alfa Laval Corp Ab | Plate package and method of making a plate package |
| WO2015088369A1 (en) * | 2013-12-11 | 2015-06-18 | Владимир Германович МАЗЕИН | Template for radiator section of finned-tube radiator, radiator section made from said template, and radiator made of said section |
| JP2015159254A (en) * | 2014-02-25 | 2015-09-03 | 三桜工業株式会社 | Cooling device and manufacturing method of the same |
| DE112016000793T5 (en) * | 2015-02-18 | 2017-11-09 | Dana Canada Corporation | Flexible design of heat exchangers for heating and / or cooling liquids |
| CN110345801B (en) * | 2018-04-08 | 2021-06-15 | 神讯电脑(昆山)有限公司 | Enhanced heat dissipation module, heat dissipation fin structure and stamping method thereof |
| US11280559B2 (en) * | 2020-05-12 | 2022-03-22 | Hanon Systems | Dumbbell shaped plate fin |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2788195A (en) * | 1952-08-29 | 1957-04-09 | Karmazin John | Condenser and method of making same |
| FR2728668B1 (en) * | 1994-12-22 | 1997-02-07 |
Family Cites Families (25)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1761395A (en) * | 1923-05-28 | 1930-06-03 | Karmazin John | Radiator |
| US1960941A (en) * | 1930-06-20 | 1934-05-29 | Karmazin Engineering Company | Radiator |
| US1902350A (en) * | 1931-01-31 | 1933-03-21 | S R Dresser Mfg Co | Heat exchanger |
| US1960955A (en) * | 1931-07-17 | 1934-05-29 | Chase Companies Inc | Radiator-unit and method of producing the same |
| US2028455A (en) * | 1933-11-14 | 1936-01-21 | Karmazin Engineering Company | Header construction |
| US2028445A (en) * | 1935-04-22 | 1936-01-21 | Gelbman Louis | Brake for foot steered vehicles |
| US2028457A (en) * | 1935-05-07 | 1936-01-21 | Karmazin Engineering Company | Refrigerating apparatus |
| US2064036A (en) * | 1935-08-12 | 1936-12-15 | Oakes Prod Corp | Method of making a condenser |
| US3027142A (en) * | 1956-05-28 | 1962-03-27 | Reynolds Metals Co | Heat exchanger |
| US3443634A (en) * | 1967-04-06 | 1969-05-13 | Peerless Of America | Heat exchangers |
| US3430692A (en) * | 1967-06-16 | 1969-03-04 | John Karmazin | Return bend construction for heat exchangers |
| US3724537A (en) * | 1971-09-28 | 1973-04-03 | H Johnson | Heat exchanger with backed thin tubes |
| GB1448294A (en) * | 1973-03-09 | 1976-09-02 | Gould Contardo Spa | Heat exchanger |
| JPS51110751A (en) * | 1975-03-25 | 1976-09-30 | Taiyo Dennetsu Kk | DANTSUKISURIIPUOSONAETAHONETSUFUINTO KONOHONETSUFUINOSONAETANETSUPAIPU |
| IT1093291B (en) * | 1978-02-10 | 1985-07-19 | Gould Contardo Spa | PROCEDURE FOR THE MANUFACTURE OF RADIATORS, PARTICULARLY FOR MOTOR VEHICLES, AND PRODUCT OBTAINED WITH THE MODESIMAL PROCEDURE |
| US4428418A (en) * | 1982-05-17 | 1984-01-31 | Chromalloy American Corporation | Heat exchanger fin element with folded over side edges |
| FR2693545B1 (en) * | 1992-07-08 | 1994-09-30 | Valeo Thermique Moteur Sa | Heat exchanger with several rows of tubes, in particular for motor vehicles. |
| JP2001194083A (en) * | 2000-01-07 | 2001-07-17 | Inoue Heater Kk | Heat exchanger and its manufacturing method |
| DE10247264A1 (en) * | 2002-10-10 | 2004-04-29 | Behr Gmbh & Co. | Plate heat exchanger in stack construction |
| JP2006284165A (en) * | 2005-03-07 | 2006-10-19 | Denso Corp | Exhaust gas heat exchanger |
| ATE524700T1 (en) * | 2005-07-19 | 2011-09-15 | Behr Gmbh & Co Kg | HEAT EXCHANGER |
| TW200538696A (en) * | 2005-08-17 | 2005-12-01 | Cooler Master Co Ltd | Heat dissipation fins, heat sink formed of fins, and method for producing the same |
| WO2008099434A1 (en) * | 2007-02-15 | 2008-08-21 | Raffaele Giannoni | Tubeless heat exchanger and method for the manufacture thereof |
| EP2131131A1 (en) * | 2008-06-06 | 2009-12-09 | Scambia Industrial Developments AG | Heat exchanger |
| JP5617220B2 (en) * | 2009-11-10 | 2014-11-05 | パナソニック株式会社 | Heat exchanger and cooling system and refrigerator using the same |
-
2011
- 2011-05-20 DE DE102011076172A patent/DE102011076172A1/en active Pending
-
2012
- 2012-05-16 CN CN201810996311.6A patent/CN109210971A/en active Pending
- 2012-05-16 US US14/118,915 patent/US20140305621A1/en not_active Abandoned
- 2012-05-16 CN CN201280024443.3A patent/CN103733012A/en active Pending
- 2012-05-16 EP EP12721847.7A patent/EP2710318A1/en not_active Ceased
- 2012-05-16 JP JP2014510799A patent/JP5864731B2/en active Active
- 2012-05-16 WO PCT/EP2012/059144 patent/WO2012159958A1/en active Application Filing
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2788195A (en) * | 1952-08-29 | 1957-04-09 | Karmazin John | Condenser and method of making same |
| FR2728668B1 (en) * | 1994-12-22 | 1997-02-07 |
Also Published As
| Publication number | Publication date |
|---|---|
| WO2012159958A1 (en) | 2012-11-29 |
| EP2710318A1 (en) | 2014-03-26 |
| JP5864731B2 (en) | 2016-02-17 |
| US20140305621A1 (en) | 2014-10-16 |
| DE102011076172A1 (en) | 2012-11-22 |
| CN103733012A (en) | 2014-04-16 |
| JP2014513788A (en) | 2014-06-05 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN109210971A (en) | Multiplate heat exchanger | |
| CN100582627C (en) | Multifluid heat exchanger | |
| JP5509466B2 (en) | Finned cylindrical heat exchanger | |
| US20150300745A1 (en) | Counterflow helical heat exchanger | |
| EP2896923B1 (en) | Heat exchanger | |
| US20070000652A1 (en) | Heat exchanger with dimpled tube surfaces | |
| KR20140114770A (en) | Heat exchanger | |
| CN103925826A (en) | Tube for a heat exchanger | |
| US11421946B2 (en) | Heat exchanger and water heating apparatus including the same | |
| JP6341099B2 (en) | Refrigerant evaporator | |
| CN104735988B (en) | Hot-blast baker | |
| EP2351979B1 (en) | Heat Exchanger comprising three concentric tubes | |
| CN101788235A (en) | Heat exchanger | |
| CN106091759A (en) | A kind of type separating heat-pipe evaporator of rotating flow heating | |
| CN100362303C (en) | Flat pipe comprising a return bend section and a heat exchanger constructed therewith | |
| US20130146264A1 (en) | Heat exchanger for vehicle | |
| CN101776411A (en) | Flat pipe assembly and heat exchanger having same | |
| JP4328425B2 (en) | Stacked heat exchanger | |
| US20130146247A1 (en) | Heat Exchanger for Vehicle | |
| CN108627035A (en) | Heat-exchanging component and heat-exchange system | |
| US11143458B2 (en) | Tube-fin heat exchanger | |
| KR200428709Y1 (en) | Heat exchanger for air conditioning | |
| JP4247462B2 (en) | Heat exchanger for exhaust heat recovery | |
| WO2001023823A1 (en) | Heat exchanger | |
| CN209588793U (en) | Heat exchanger |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20190115 |