CN104285121B - Heat exchanger collector, possess the heat exchanger of this heat exchanger collector, freezing cycle device and air conditioner - Google Patents
Heat exchanger collector, possess the heat exchanger of this heat exchanger collector, freezing cycle device and air conditioner Download PDFInfo
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- CN104285121B CN104285121B CN201380025220.3A CN201380025220A CN104285121B CN 104285121 B CN104285121 B CN 104285121B CN 201380025220 A CN201380025220 A CN 201380025220A CN 104285121 B CN104285121 B CN 104285121B
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End 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
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End plates
- F28F9/026—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
- F28F9/0265—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits by using guiding means or impingement means inside the header box
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- 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
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/16—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End plates
- F28F9/026—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
- F28F9/0265—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits by using guiding means or impingement means inside the header box
- F28F9/0268—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits by using guiding means or impingement means inside the header box in the form of multiple deflectors for channeling the heat exchange medium
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- 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
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
- F28D2021/0068—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for refrigerant cycles
- F28D2021/0071—Evaporators
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End plates
- F28F2009/0285—Other particular headers or end plates
- F28F2009/0292—Other particular headers or end plates with fins
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- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Details Of Heat-Exchange And Heat-Transfer (AREA)
Abstract
The present invention provides a kind of simply constructed heat exchanger collector and possesses the heat exchanger of this heat exchanger collector, and the pressure loss can be suppressed low, will not cause the decline of the heat transfer property of heat exchanger by it, it is possible to assignment system cryogen equably.The heat exchanger collector (10) of the heat exchanger of flowing in making cold-producing medium concurrently at the multiple heat-transfer pipes (30) configured concurrently, (20) in, aforementioned collector is set up in parallel multiple through hole (12) on long side direction, the plurality of through hole connects one end of aforesaid plurality of heat-transfer pipe, form at least one chamber (10A) connecting with aforesaid plurality of through hole and becoming refrigerant flow path, each of aforesaid plurality of through hole is the entrance side through hole that is connected of the end of the refrigerant inlet side with aforesaid plurality of heat-transfer pipe or refrigerant outlet side or outlet side through hole, in aforementioned cavity with said inlet side through hole part in opposite directions, the short side direction orthogonal with aforementioned long side direction is formed multiple groove (14) extended on the long side direction of aforementioned collector.
Description
Technical field
The present invention relates to such as air conditioner etc. freezing cycle device heat exchanger heat exchanger collection
Manage, possess the heat exchanger of this heat exchanger collector, freezing cycle device and air conditioner.
Background technology
In the past, there is the heat exchanger being configured to following: left at left and right directions by a pair collector extended at above-below direction
Ground configuration, configures multiple flat tube the most concurrently, by the both ends of multiple heat-exchange tubes with a pair collector even
Logical.In this heat exchanger, in the case of using as vaporizer, owing to cold-producing medium flows into gas-liquid two-phase flow, so,
Liquid in the collector of entrance side on gravity direction accumulate, and gas accumulation in collector above.Accordingly, there are can not be equal
Etc. ground to each flat tube assignment system cryogen, the problem of the hydraulic performance decline of heat exchanger.
Therefore, in the case of being used as vaporizer by heat exchanger, the collector for entrance side requires to divide equably
The function of preparation cryogen.As possessing the collector of such function, there is following such collector: exist at collector Inner Constitution in the past
The annular flow path that above-below direction is turned back, makes the two-phase system cryogen stream flowed in collector inner loop and homogenize, to multiple biographies
Each distribution (for example, with reference to patent documentation 1) of heat pipe.
Citation
Patent documentation
Patent documentation 1: Japanese Unexamined Patent Publication 2011-85324 publication (summary, Fig. 1)
Summary of the invention
The problem that invention is to be solved
But, in the collector of patent documentation 1, owing to making cold-producing medium flow through in annular flow path, so, there is generation pressure
Power is lost, and the heat transfer property causing heat exchanger declines such problem.
It addition, in the collector of patent documentation 1, owing to needs form annular flow path inside collector separately, so, exist
Structure complexity, causes the such problem of cost increase.
The present invention is the invention made in view of such point, its objective is to provide one the pressure loss to be suppressed
Low, the decline of the heat transfer property of heat exchanger will not be caused, can assignment system cryogen equably, simply constructed heat exchanger collects
Manage, possess the heat exchanger of this heat exchanger collector, freezing cycle device and air conditioner.
For solving the means of problem
The heat exchanger collector of the present invention is the heat exchanger collector of a kind of heat exchanger, and this heat exchanger makes refrigeration
Agent is flowed in the multiple heat-transfer pipes configured concurrently concurrently, wherein,
Aforementioned collector utilizes capillary effect assignment system cryogen and is allowed to flow concurrently in aforesaid plurality of heat-transfer pipe
It is dynamic,
Being set up in parallel multiple through hole on long side direction, the plurality of through hole connects the one of aforesaid plurality of heat-transfer pipe
End,
At least form a chamber connected and become refrigerant flow path with aforesaid plurality of through hole,
Each of aforesaid plurality of through hole is the refrigerant inlet side with aforesaid plurality of heat-transfer pipe or refrigerant outlet side
The entrance side through hole that connects of end or outlet side through hole, in aforementioned cavity with said inlet side through hole in opposite directions
Part, the short side direction orthogonal with aforementioned long side direction is formed multiple on the long side direction of aforementioned collector extend
Groove.
Invention effect
Can the pressure loss be suppressed low in accordance with the invention it is possible to obtain one, the heat transfer of heat exchanger will not be caused
The decline of performance, can assignment system cryogen and simply constructed heat exchanger collector equably.
Accompanying drawing explanation
Fig. 1 is the use of the general principal view of the heat exchanger 1 of the heat exchanger collector of embodiments of the present invention 1.
Fig. 2 is the axonometric chart of the flat tube 30 representing Fig. 1.
Fig. 3 is the exploded perspective view of the inlet header 10 of Fig. 1.
Fig. 4 is the A-A sectional view of the inlet header section of Fig. 1.
Fig. 5 is the figure of the refrigerant loop of the freezing cycle device 50 of the heat exchanger 1 representing and applying Fig. 1.
Fig. 6 is the figure of the flowing representing the cold-producing medium in the case of being used by the heat exchanger 1 of Fig. 1 as vaporizer.
Fig. 7 is the figure representing the cold-producing medium flow regime in inlet header 10.
Fig. 8 is the B-B sectional view of Fig. 7.
Fig. 9 is to be denoted as comparative example, could be made without the cold-producing medium flowing arranging in the collector in the case of the collector of groove
The figure of state.
Figure 10 is the figure of the variation 1 of the groove 14 representing Fig. 3.
Figure 11 is the figure of the variation 2 of the groove 14 representing Fig. 3.
Figure 12 is the figure of the heat exchanger 1A representing embodiments of the present invention 2.
Figure 13 is the exploded perspective view of the collector 70 of Figure 12.
Figure 14 is the figure of the variation of the groove 14 representing Figure 13.
Figure 15 is the figure of the heat exchanger 1B representing embodiments of the present invention 3.
Detailed description of the invention
Embodiment 1.
Fig. 1 is the use of the general principal view of the heat exchanger of the heat exchanger collector of embodiments of the present invention 1.?
In Fig. 1 and figure described later, the parts being labelled with identical reference are identical or the most suitable parts, and this is in description
In Quan Wen general.Further, the mode of the element represented by description full text only illustrates, it is not limited to these notes
Carry.
Heat exchanger 1 is the heat exchanger of the concurrent flow making cold-producing medium flow concurrently, especially overall at heat exchanger 1
In, make cold-producing medium from the heat exchanger of the dynamic one direction stream type of direction the opposing party's effluent.Heat exchanger 1 possess mutually from
Turn up the soil configuration a pair collector 10,20；It is arranged in concurrently between a pair collector 10,20 and two ends and a pair collector 10,20
The multiple flat tubes (heat-transfer pipe) 30 connected；With multiple fins 40.A pair collector 10,20, flat tube 30 and fin 40 by
Aluminum or aluminum alloy is constituted.
Fin 40 is that the most empty standard width of a room in an old-style house is every the tabular wing being laminated between a pair collector 10,20, air passes through betwixt
Sheet, through for multiple flat tubes 30.It addition, fin 40 can also be not necessarily plate-shaped fins, as long as be configured to air at sky
The fin 40 that gas is passed through by direction.For example, it is also possible to above-below direction alternately laminated with flat tube 30 configure
The fin etc. of wave, as long as sum it up, be configured to the fin that air is passed through by direction at air.
Flat tube 30 is as in figure 2 it is shown, have multiple through hole 30a becoming refrigerant flow path.It addition, heat-transfer pipe not limits
In flat tube, pipe, other what kind of shape all can use.
System is connected at the inlet header 10 of the refrigerant inlet side becoming multiple flat tube 30 in a pair collector 10,20
Cryogen entrance pipe arrangement 10a, connects refrigerant outlet at the outlet header 20 of refrigerant outlet side becoming multiple flat tube 30
Pipe arrangement 20a.
The collector (hereinafter, referred to as inlet header 10) of the present invention especially entrance side in a pair collector 10,20 has
Feature, below, see Fig. 3, its structure is illustrated.
Fig. 3 is the exploded perspective view of the inlet header 10 of Fig. 1.Fig. 4 is the A-A sectional view of the inlet header section of Fig. 1.
Inlet header 10 has the header body 11 of the box like of an opening and the plate of the opening 11a of covering header body 11
The lid 13 of shape, is formed at least 1 chamber 10A of refrigerant flow path between.In header body 11, with open
Mouth 11a bottom surface 11b in opposite directions is set up in parallel the multiple through holes as entrance side through hole along the long side direction of header body 11
12.At the plurality of through hole 12, connect the end of the refrigerant inlet side of multiple flat tubes 30, chamber 10A connect.It addition,
Refrigerant inlet pipe arrangement 10a is connected at inlet header 10.
It addition, on lid 13, at least 1 chamber 10A with through hole 12 face 13a in opposite directions on throughout with long limit
The short side direction that direction is orthogonal be integrally formed multiple long side direction extend groove 14.Groove 14 is specifically highlighted by from lid 13
Multiple teats 15 gap each other formed.Groove 14 is arranged for by utilizing capillary effect, will flow into
Refrigerant liquid in inlet header 10 is incorporated into inside groove, thus carrys out to carry out equably cold-producing medium from inlet header 10 to respectively
The distribution in path.
When manufacturing the inlet header 10 so constituted, formed the header body 11 of box like by machining etc., at collection
Tube body 11 forms through hole 12.It addition, form lid 13 by machining etc..Lid 13 can be configured chimericly, in order to
Can temporal persistence in the opening 11a of header body 11, apply soldering material at telescoping part.
And, when manufacturing heat exchanger 1 and being overall, lid 13 is entrenched in the opening 11a of header body 11 and is allowed to temporary
Time stop, and when all assembling outlet header 20, flat tube 30 and fin 40, soldered joint is overall simultaneously.
Fig. 5 is the figure of the refrigerant loop of the freezing cycle device 50 of the heat exchanger 1 representing and applying Fig. 1.
Freezing cycle device 50 possess compressor 51, condenser 52, as the expansion valve 53 of decompressor and vaporizer 54.
At least one party at condenser 52 and vaporizer 54 uses heat exchanger 1.The gas refrigerant discharged from compressor 51 flows into
Condenser 52, carries out heat exchange with the air passed through at condenser 52, becomes high pressure liquid refrigerant and flow out.From condenser 52
The high pressure liquid refrigerant flowed out is reduced pressure by expansion valve 53, becomes the gas-liquid two-phase cold-producing medium of low pressure, flows into vaporizer 54.Flow into
The gas-liquid two-phase cold-producing medium of low pressure to vaporizer 54 carries out heat exchange with the air passed through at vaporizer 54, becomes low-pressure gas
Cold-producing medium, is again sucked into compressor 51.
Fig. 6 is the figure of the flowing representing the cold-producing medium in the case of being used by the heat exchanger 1 of Fig. 1 as vaporizer.
The gas-liquid two-phase cold-producing medium flowed out from expansion valve 53 flows in inlet header 10 from refrigerant inlet pipe arrangement 10a.Stream
The cold-producing medium entered in inlet header 10 is from constituting the one end of each flat tube 30 in each path of heat exchanger 1 to other end stream
Dynamic, collaborate at outlet header 20, flow out to outside from refrigerant outlet pipe arrangement 20a.
Then, the action within inlet header is illustrated.Fig. 7 is to represent the cold-producing medium flowing shape in inlet header 10
The figure of state.Fig. 8 is the B-B sectional view of Fig. 7, is to represent that, in inlet header 10, liquid refrigerant accumulates in the state between groove
Schematic diagram.Fig. 9 (a), (b) are to be denoted as comparative example to be not provided with cold-producing medium in the collector of groove 14, in collector flowing shape
The figure of state.
First, by Fig. 9, the cold-producing medium flow regime of comparative example is illustrated.When the system of circulation in refrigerant loop
In the case of cryogen amount is many, it is flowed into gas-liquid two-phase cold-producing medium such as Fig. 9 (a) of inlet header 10 from refrigerant inlet pipe arrangement 10a
Shown in, accumulate in the top of inlet header 10 because of momentum when flowing into.On the other hand, when the system of circulation in refrigerant loop
In the case of cryogen amount is few, it is flowed into the liquid system of the gas-liquid two-phase cold-producing medium of inlet header 10 from refrigerant inlet pipe arrangement 10a
Cryogen accumulates in the bottom of inlet header 10 because of the impact of gravity.At the knot not arranging groove 14 like this at inlet header 10
In the case of structure, liquid refrigerant concentrates on top or bottom, and the distribution to each path is unequal.
Then, by Fig. 7 and Fig. 8, the cold-producing medium flow regime in the inlet header 10 of present embodiment is said
Bright.The gas-liquid two-phase cold-producing medium being flowed in inlet header 10 from refrigerant inlet pipe arrangement 10a flows in inlet header 10, borrows
Helping capillary effect, liquid refrigerant is introduced in groove 14.Thus, liquid refrigerant in inlet header 10 by equably
Being held in long side direction, the liquid refrigerating dosage flowed into each flat tube 30 is homogenized.
As explained above, according to present embodiment 1, by arranging multiple groove 14 on lid 13, surface is made to open
Power plays a role, it is possible to suppression liquid refrigerant unbalance, it is possible to is distributed equably by cold-producing medium, is allowed to be flowed into multiple flat
Each of pipe 30.Thereby, it is possible to raising heat exchanger effectiveness, it is possible to play heat exchanger 1 to greatest extent as vaporizer
Ability in the case of use.
It addition, present embodiment 1 is owing to being to utilize the surface tension effects of liquid refrigerant to seek to prevent unequal system
The structure of refrigerant distribution, so, compared with conventional structure, it is possible to the suppression pressure loss, it is possible to suppress heat exchanger 1 as steaming
Send out the hydraulic performance decline in the case of device uses.
It addition, the inlet header 10 of present embodiment 1 is owing to being made up of header body 11 and the lid 13 with groove 14, structure
Make simple, so, easy to manufacture, it is possible to cost degradation.
It addition, the inlet header of the present invention is not limited to the structure shown in Fig. 3, at the model of the purport without departing from the present invention
In enclosing, such as, can carry out various deformation as following (1), (2) and implement.
(1) Figure 10 is the figure of variation 1 of the groove 14 representing Fig. 3.
In the structure of the groove 14 of the present embodiment shown in Fig. 5, the height of teat 15 is the most identical, but it is also possible to
As Figure 10, make the height making teat 15 at the short side direction (for above-below direction in Figure 10) of lid 13 and alternately uprise change
Low structure.In the case of so constituting, owing to the end face (inclined plane) of flat tube 30 side of groove 14 (uses chain-dotted line in Figure 10
14a represents) make highly consistent structure broaden than as shown in Figure 5, thus it is possible to expect to improve liquid refrigerant introducing
Effect.It addition, the height of teat 15 is not limited to the structure of the most alternately length, if making the short side direction made along lid 13
The structure that adjacent teat 15 height each other is interlaced, then can expect same effect.Short as make along lid 13
Other example of the structure that the height of the adjacent teat 15 of edge direction teat 15 each other is interlaced, it is also possible to make following change
Shape example 2.
(2) Figure 11 is the figure of variation 2 of the groove 14 representing Fig. 3.
Cold-producing medium in the groove 14 produced because of surface tension keeps the width acting on groove 14 (for above-below direction in Figure 11
Length) the narrowest, and the biggest when the height of groove 14 is the highest.It addition, be flowed into the liquid refrigerant of inlet header 10 with regard to lid
Its two ends are easily accumulated in for the short side direction of 13.Thus, in this variation 2, by the height of teat 15 along with from minor face
The two end portions whereabouts core in direction and formed higher, the height of adjustment tank 14 makes the retentivity of cold-producing medium along with whereabouts
The core of short side direction and become big.Accordingly, for short side direction, the unbalance of cold-producing medium is also inhibited, in long limit side
To with this two side of short side direction, it is possible to make the refrigerant amount homogenization in each groove 14.Its result is, it is possible to expect to each flat tube
Each of 30 can more equally among assignment system cryogen.It addition, here, the example of the height only changing groove 14 is illustrated, but,
The width making groove 14 can also be configured to narrow along with whereabouts core.
As explained above, it is a feature of the present invention that and multiple grooves 14 are arranged at this point of inlet header 10.And,
As applying the heat exchanger 1 of this feature, in present embodiment 1, illustrate in heat exchanger entirety cold-producing medium from one
The example of the heat exchanger of the one direction stream type of direction the opposing party flowing, on the way flows but it is also possible to be applied to one side
Turn back the heat exchanger of stream type of turning back of one side flowing in road.Below, by embodiments below 2, embodiment 3, right
Structure in the heat exchanger application present invention of stream type of turning back illustrates.
Embodiment 2.
Figure 12 is the figure of the heat exchanger 1A representing embodiments of the present invention 2.
Heat exchanger 1A is the heat exchanger of the concurrent flow making cold-producing medium flow concurrently, stream type of especially turning back
Heat exchanger.It addition, shown herein as the structure example making number of paths be 5.
Heat exchanger 1A possesses a pair collector 70,80 configured away from each other；Be arranged in concurrently a pair collector 70,
Many (being 20 here) flat tubes (heat-transfer pipe) 30 that between 80 and two ends are connected with a pair collector 70,80；With multiple fins
40.A pair collector 70,80, flat tube 30 and fin 40 are constituted by aluminum or aluminum alloy.Flat tube 30 and the knot of fin 40
Structure is identical with embodiment 1.
Figure 13 is the exploded perspective view of the collector 70 of Figure 12.
Collector 70 has the header body 71 of the box like of an opening.Header body 71 with the opening 71a end in opposite directions
On the 71b of face, the long side direction along header body 71 is set up in parallel the multiple through holes 72 connected for multiple flat tubes 30.It addition,
2 demarcation strips 73 are set in the inside of header body 71, are formed and connect with multiple through holes 72 and become the 3 of refrigerant flow path
Individual independent chamber A, B, C, closed by lid 74A, 74B, 74C respectively.
Flowing to the cold-producing medium in heat exchanger 1A will be set forth later, but on lid 74A, 74B, 74C, with flat
The end of the refrigerant inlet side of flat pipe 30 part in opposite directions forms multiple grooves 14 with the effect identical with embodiment 1.
Below, specifically illustrate.
Chamber A is the inflow chamber flowed into from outside cold-producing medium, due at the multiple through holes 72 connected with chamber A
Place connects the end of the refrigerant inlet side of flat tube 30, so, lid 74A is integrally formed groove 14.It addition, chamber B
It is the chamber of turning back becoming stream of turning back, owing to the top half in the multiple through holes 72 connected with chamber B is connected flat
The end of the refrigerant inlet side of pipe 30, connects the end of the refrigerant outlet side of flat tube 30 in the latter half, so, at lid
The top half of body 74B is provided with groove 14.It addition, the outflow chamber that cavity C is cold-producing medium to flow out to outside, due to cavity C
Multiple through holes 72 of connection connect the end of the refrigerant outlet side having flat tube 30, so, lid 74C is not provided with
Groove 14.It addition, have the through hole connected by the end of the refrigerant inlet side of flat tube 30 in multiple through holes 72 below
It is referred to as entrance side through hole, the end of the refrigerant outlet side of flat tube 30 through hole connected is referred to as outlet side through hole
Situation.
On the other hand, collector 80 is provided with 1 demarcation strip 83 as shown in figure 12, is internally divided into 2 chambers D, E.And,
As collector 70, each chamber D, E are closed by lid 84D, 84E respectively.And, on lid 84D, 84E the most as described above,
Multiple groove 14 is being formed with the part in opposite directions of the entrance side through hole in flat tube 30.Specifically, every at lid 84D, 84E
In one, it is formed with multiple groove 14 in top half.
When manufacturing the collector 70 so constituted, form header body 71 by machining etc., in header body 71 shape
Become through hole 72.It addition, form each lid 74A, 74B, 74C by machining etc..Each lid 74A, 74B, 74C can be fitted together to ground
It is configured, so as to temporal persistence, in the opening of each chamber A, B, C of header body 71, applies soldering material at telescoping part.
Collector 80 also is able to similarly manufacture.
And, when manufacturing heat exchanger 1B entirety, respectively lid 74A, 74B, 74C are embedded in each chamber of collector 70
The opening of A, B, C is also allowed to temporal persistence, and lid 84D, 84E are embedded in by collector 80 the most respectively each chamber D,
The opening of E is also allowed to temporal persistence.And, when all assembling flat tube 30 and fin 40, soldering simultaneously connects
Close entirety.
Below, see Figure 12, the flowing of cold-producing medium in heat exchanger 1A is described.Here, illustrate to make heat exchanger 1A
The flowing of the cold-producing medium in the case of using for vaporizer.In Figure 12, solid arrow represents the flowing of cold-producing medium.
The gas-liquid two-phase cold-producing medium flowed into from refrigerant inlet pipe arrangement 10a flows into chamber A, from flat with what chamber A was connected
Flowing towards the other end in one end of pipe group, flows into chamber D.The cold-producing medium being flowed into chamber D is here turned back, from chamber D even
Flowing to the other end in the one end of other the flat tube group connect, flows into chamber B.And, it is flowed into the cold-producing medium of chamber B here
Turn back, flow from the one end of other the flat tube group being connected with chamber B to the other end, flow into chamber E.And, it is flowed into chamber
The cold-producing medium of room E is here turned back, and flows from the one end of other the flat tube group being connected with chamber E to the other end.And, from
Each cold-producing medium that this other end flows out collaborates in cavity C, flows out to outside from refrigerant outlet pipe arrangement 20a.
In the flowing of superincumbent cold-producing medium, owing to arranging opposite to each other with the end of the refrigerant inlet side of each flat tube group
There is groove 14, so, as above-mentioned embodiment 1, by the bias current of the surface tension effects suppression cold-producing medium of liquid refrigerant,
From each chamber to each path assignment system cryogen substantially uniformly.
Ground as described above is such, according to present embodiment 2, even if in the heat exchanger turning back stream type, also can
Access the effect identical with embodiment 1.
It addition, in present embodiment 2, although make entrance side through hole group and outlet side in multiple teats 15 through
The structure that the position of the end of the boundary line side of hole group is the most consistent, above-mentioned multiple teats 15 are formed at the chamber becoming chamber of turning back
Lid 74B, 84D, 84E of room B, D, E, but it is also possible to as figure 14 below.
Figure 14 is the figure of the variation of the groove 14 representing Figure 13, is lid 74B, 84D, 84E in terms of the side, formation face of groove 14
Figure.
As shown in Figure 14 (a), it is also possible to make in multiple teats 15, entrance side through hole group and outlet side through hole group
The structure alternately interlocked at the short side direction of lid of the position of end of boundary line side.If so constituting, then due to groove 14
The end face of aforementioned boundary line side become inclined plane, the structure of the position consistency of end face end more such than Figure 13 broadens, thus it is possible to
Enough effects expecting that liquid refrigerant is introduced by raising.It addition, be not limited to the position of the end of teat 15 the most alternately
Staggered structure, if making the structure interlaced along the adjacent teat 15 of the short side direction of lid position each other, the most also can
Enough expect same effect.
It addition, Figure 14 (b) is to make the structure interlaced along the adjacent teat 15 of the short side direction of lid position each other
Other example, but it is also possible to like this along with whereabouts short side direction central part and by the long side direction of teat 15
Length is configured shorter, or goes out although not shown, but along with whereabouts short side direction central part and by the long side direction of teat 15
Length is configured longer.
It addition, for the variation that constitute certain applications identical with embodiment 1 for present embodiment 2 similarly
It is suitable for.Alternatively, it is also possible to make the variation illustrated in present embodiment 2 and the variation illustrated in embodiment 1
The structure of combination.These points in embodiment 3 described later too.
Embodiment 3.
Embodiment 3 is equivalent to pass through to set on direction at air by the heat exchanger of the stream type of turning back of embodiment 2
Put the structure of multiple row (being 2 row here).
Figure 15 is the figure of the heat exchanger representing embodiments of the present invention 3.Figure 15 (a) be from use dash-dot arrows table
The air shown sees the summary side elevation of heat exchanger by the direction that direction is orthogonal.Figure 15 (b) is to pass through direction relative to air
The general profile chart of upstream side heat exchange department 1Ba of upstream side.Figure 15 (c) is the downstream passing through direction relative to air
The general profile chart of downstream heat exchange department 1Bb.Figure 15 (d) is the top view of heat exchanger.Below, with embodiment 3 with real
Illustrate centered by executing the part that mode 2 is different.
Heat exchanger 1B possesses the heat exchanger 1A identical with embodiment 2 and is used as upstream side heat exchange department 1Ba, then
Have, by the downstream in direction, there is downstream heat exchange department 1Bb at air.And, upstream side heat exchange department 1Ba and downstream
Heat exchange department 1Bb is connected by across row pipe arrangement 90.
Being made up of 5 paths relative to upstream side heat exchange department 1Ba, downstream heat exchange department 1Bb is upper by number of paths ratio
10 many for trip side heat exchange department 1Ba paths are constituted.For like this at upstream side heat exchange department 1Ba and downstream heat exchange department
1Bb changes the reason of number of paths and will be set forth later.Downstream heat exchange department 1Bb is warm with upstream side except the structure of manifold portion
Outside exchange part 1Ba difference, identical with upstream side heat exchange department 1Ba.
In the heat exchange department 1Bb of downstream, connection is hot with upstream side across the quantity of the demarcation strip of the collector 700 of row pipe arrangement 90
Exchange part 1Ba is different, in collector 700, arranges 1 demarcation strip 703, is being internally formed 2 chambers F, G.It addition, at collector
It is not provided with demarcation strip in 800, makes the structure being integrally formed 1 chamber H.It addition, as embodiment 1,2,
In the collector 700,800 of downstream heat exchange department 1Bb, the also portion in opposite directions in the end with the refrigerant inlet side of each flat tube 30
Set up separately and be equipped with groove 14.
Below, see Figure 15, the flowing of cold-producing medium in heat exchanger 1B is described.Here, illustrate to make heat exchanger 1B
The flowing of the cold-producing medium in the case of using for vaporizer.In Figure 15, solid arrow represents the flowing of cold-producing medium.
The flowing of the cold-producing medium in heat exchanger 1B is for upstream side heat exchange department 1Ba, identical with embodiment 2.And
And, the cold-producing medium flowed out from the refrigerant outlet pipe arrangement 20a of upstream side heat exchange department 1Ba from refrigerant inlet pipe arrangement 100a through across
Row pipe arrangement 90 flows into the chamber F of downstream heat exchange department 1Bb.It is flowed into the cold-producing medium of chamber F from the flat tube connected with chamber F
Flowing towards the other end in one end of group, flows into chamber H.And, the cold-producing medium being flowed into chamber H is here turned back, from chamber H
Flow towards the other end in the one end of other the flat tube group connected.And, each cold-producing medium flowed out from this other end is at chamber G
Interflow, flows out to outside from refrigerant outlet pipe arrangement 200a.
In the flowing of superincumbent cold-producing medium, owing to arranging opposite to each other with the end of the refrigerant inlet side of each flat tube group
There is groove 14, so, as above-mentioned embodiment 1,2, the surface tension effects by liquid refrigerant suppresses the inclined of cold-producing medium
Stream, from each chamber to each path assignment system cryogen substantially uniformly.
Then, the reason changing number of paths at upstream side heat exchange department 1Ba and downstream heat exchange department 1Bb is carried out
Explanation.
In the case of heat exchanger 1B is used as vaporizer, owing to cold-producing medium flows into gas-liquid two-phase state,
Become gas refrigerant eventually and flow out, so, aridity becomes big along with the latter half of of whereabouts stream.In the situation that aridity is little
Under, due to little by crushing during stream, it is preferred, therefore, that make refrigerant flow rates accelerate, promote the coefficient of overall heat transmission.On the other hand, dry
In the case of dry degree is big, due to big by crushing during stream, it is preferred, therefore, that make refrigerant flow rates slow, more increase number of path
Amount refrigerant flow rates is the slowest.
In heat exchanger 1B, in the upstream side heat exchange department 1Ba being equivalent to stream first half, due to doing of cold-producing medium
Dry degree is little, so, make number of paths tail off, promote refrigerant flow rates, promote the coefficient of overall heat transmission.On the other hand, stream is being equivalent to
In latter half of downstream heat exchange department 1Bb, owing to aridity becomes big, so, make number of paths many, make under refrigerant flow rates
Fall, seeks to reduce the pressure loss.
As explained above, according to present embodiment 3, it is possible to obtain and the identical effect of embodiment 1,2, and
Owing to making many array structures, thus it is possible to improve heat-exchange capacity.It addition, because reduce little by the aridity of cold-producing medium
The air number of paths by direction upstream side, promotes refrigerant flow rates, promotes the coefficient of overall heat transmission, so, it also is able to scheme in this respect
Seek raising heat-exchange capacity.
It addition, in present embodiment 3, illustrate 2 array structures, but it is also possible to make the structure that 3 row are above.
It addition, in the respective embodiments described above, illustrate the example that outer shape is square shape of collector, but, not
It is limited to square shape, it is also possible to make cylindrical shape.It addition, in the case of multiple row as embodiment 3, from guaranteeing as collection
Size needed for pipe and seek from the viewpoint of row interfere with each other, to be preferably made to square shape.
Description of reference numerals
1: heat exchanger；1A: heat exchanger；1B: heat exchanger；1Ba: upstream side heat exchange department；1Bb: downstream heat is handed over
Change portion；10: collector (inlet header)；10A: chamber；10a: refrigerant inlet pipe arrangement；11: header body；11a: opening；11b:
Bottom surface；12: through hole；13: lid；13a: face；14: groove；15: teat；20: collector (outlet header)；20a: refrigerant outlet
Pipe arrangement；30: flat tube；30a: through hole；40: fin；50: freezing cycle device；51: compressor；52: condenser；53: expand
Valve；54: vaporizer；70: collector；71: header body；71a: opening；71b: bottom surface；72: through hole；73: demarcation strip；74A: lid
Body；74B: lid；74C: lid；80: collector；83: demarcation strip；84D: lid；84E: lid；90: across row pipe arrangement；100a: system
Cryogen entrance pipe arrangement；200a: refrigerant outlet pipe arrangement；700: collector；703: demarcation strip；800: collector；A～H: chamber.
Claims (14)
1. a heat exchanger collector for heat exchanger, this heat exchanger makes cold-producing medium in the multiple heat transfers configured concurrently
Pipe flows concurrently, it is characterised in that
Aforementioned collector utilizes capillary effect assignment system cryogen and is allowed to flow concurrently in aforesaid plurality of heat-transfer pipe,
Being set up in parallel multiple through hole on long side direction i.e. gravity direction, the plurality of through hole connects aforesaid plurality of heat-transfer pipe
One end,
The long side direction of aforementioned collector is separated and forms multiple and aforesaid plurality of through hole and connect and become cold-producing medium stream
The chamber on road,
Each of aforesaid plurality of through hole is the refrigerant inlet side with aforesaid plurality of heat-transfer pipe or the end of refrigerant outlet side
Portion connect entrance side through hole or outlet side through hole, in aforesaid plurality of chamber except for cold-producing medium from aforementioned collector to
Outside flow out flow out in each outside chamber, in aforementioned cavity with said inlet side through hole part in opposite directions,
The short side direction orthogonal with aforementioned long side direction is formed multiple groove extended on the long side direction of aforementioned collector.
2. heat exchanger collector as claimed in claim 1, it is characterised in that each of aforesaid plurality of chamber is classified as
Flow into chamber for flow into from outside cold-producing medium, become turn back chamber and aforementioned outflow chamber any of stream of turning back
One,
It is all entrance side through hole with the through hole of aforementioned inflow chamber, at part aforementioned forming aforementioned inflow chamber
Long side direction aforesaid plurality of groove is integrally formed,
Be divided into entrance side through hole group and outlet side through hole group with the through hole of aforementioned fold return chamber, with entrance side
Through hole group part in opposite directions forms aforesaid plurality of groove,
It is all outlet side through hole with the through hole of aforementioned outflow chamber, there is no shape in the part forming aforementioned outflow chamber
Become aforesaid plurality of groove.
3. heat exchanger collector as claimed in claim 2, it is characterised in that aforesaid plurality of groove by the multiple teats highlighted that
Gap between this is formed, in the aforesaid plurality of teat being formed at aforementioned fold return chamber, for said inlet side through hole group
For the position of the end of the boundary line side of said outlet side through hole group, along the adjacent aforementioned teat of aforementioned short side direction that
This is interlaced.
4. the heat exchanger collector as described in any one in claims 1 to 3, it is characterised in that aforesaid plurality of groove is by dashing forward
The multiple teats gone out gap each other is formed, and the height each other of the adjacent aforementioned teat in aforesaid plurality of teat is the most not
With.
5. heat exchanger collector as claimed in claim 4, it is characterised in that make the height of aforesaid plurality of teat aforementioned short
Step-down is alternately uprised on edge direction.
6. heat exchanger collector as claimed in claim 4, it is characterised in that the height of aforesaid plurality of teat is formed as with
The core of the aforementioned short side direction of whereabouts and uprise.
7. the heat exchanger collector as described in any one in claims 1 to 3, it is characterised in that aforementioned collector has: collection
Tube body, it is the box like of an opening, and is being formed with aforesaid plurality of through hole with aforementioned opening bottom surface in opposite directions；And covering
The lid being formed tabular of aforementioned opening.
8. heat exchanger collector as claimed in claim 7, it is characterised in that aforementioned grooves is formed on aforementioned lid.
9. a heat exchanger, it is characterised in that possess the heat exchanger collector described in any one in claims 1 to 3.
10. a heat exchanger, it is characterised in that by direction, at least there is 2 heat exchange departments, described heat exchange department at air
Possessing: the heat exchanger collector described in a pair claim 2 or claim 3, it is passing through direction relative to aforementioned air
Configure away from each other on orthogonal direction；Multiple heat-transfer pipes, it is arranged in aforementioned a pair heat exchanger collector concurrently
Between, and two ends are connected with the aforesaid plurality of through hole of a pair heat exchanger collector；With multiple fins, it is configured to air
Aforementioned air by side upwardly through, aforementioned heat exchange department is each other by connecting across row pipe arrangement and forming refrigerant flow path, at this
In refrigerant flow path, cold-producing medium is in the air aforesaid plurality of heat-transfer pipe by the aforementioned heat exchange department of direction upstream side, in the past
State inflow chamber to aforementioned outflow chamber and to turn back at aforementioned fold return chamber, then, be flowed into across row pipe arrangement through aforementioned
The air aforementioned heat exchange department by downstream, direction, equally, from the aforementioned inflow chamber of aforesaid heat exchangers collector to front
State outflow chamber and turn back at aforementioned fold return chamber,
In the case of heat exchanger uses as vaporizer, the refrigerant path number that the aforementioned heat exchange department at upstream side flows
Fewer than the refrigerant path number that the aforementioned heat exchange department in downstream flows.
11. heat exchangers as claimed in claim 9, it is characterised in that previous heat transfer pipe is to have multiple to become cold-producing medium stream
The flat tube of the through hole on road.
12. heat exchangers as claimed in claim 10, it is characterised in that previous heat transfer pipe is to have multiple to become cold-producing medium stream
The flat tube of the through hole on road.
13. 1 kinds of freezing cycle devices, it is characterised in that possess the heat exchanger described in any one in claim 9 to 12.
14. 1 kinds of air conditioners, it is characterised in that possess the freezing cycle device described in claim 13.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PCT/JP2012/002879 WO2013160956A1 (en) | 2012-04-26 | 2012-04-26 | Heat-exchanger header and heat exchanger provided therewith |
| JPPCT/JP2012/002879 | 2012-04-26 | ||
| PCT/JP2013/061858 WO2013161795A1 (en) | 2012-04-26 | 2013-04-23 | Heat-exchanger header and heat exchanger provided therewith |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104285121A CN104285121A (en) | 2015-01-14 |
| CN104285121B true CN104285121B (en) | 2016-10-12 |
Family
ID=49482333
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201380025220.3A Active CN104285121B (en) | 2012-04-26 | 2013-04-23 | Heat exchanger collector, possess the heat exchanger of this heat exchanger collector, freezing cycle device and air conditioner |
| CN201320216136.7U Expired - Lifetime CN203464829U (en) | 2012-04-26 | 2013-04-26 | Heat-exchanger header box and heat exchanger therewith |
Family Applications After (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320216136.7U Expired - Lifetime CN203464829U (en) | 2012-04-26 | 2013-04-26 | Heat-exchanger header box and heat exchanger therewith |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US20150053384A1 (en) |
| EP (1) | EP2865983B1 (en) |
| CN (2) | CN104285121B (en) |
| ES (1) | ES2883139T3 (en) |
| WO (2) | WO2013160956A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111433548A (en) * | 2017-12-11 | 2020-07-17 | 三菱电机株式会社 | Fin-less heat exchanger and refrigeration cycle device |
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| US10032693B2 (en) * | 2015-10-20 | 2018-07-24 | General Electric Company | Heat transfer chassis and method for forming the same |
| CN107367089A (en) * | 2016-05-13 | 2017-11-21 | 浙江盾安热工科技有限公司 | Micro-channel heat exchanger |
| US10883745B2 (en) | 2016-06-27 | 2021-01-05 | Mitsubishi Electric Corporation | Refrigeration cycle apparatus |
| EP3521747B1 (en) * | 2016-09-29 | 2021-06-23 | Daikin Industries, Ltd. | Heat exchanger and air conditioner |
| JP6772731B2 (en) * | 2016-09-30 | 2020-10-21 | ダイキン工業株式会社 | How to make a heat exchanger |
| CN107941054B (en) * | 2017-12-13 | 2020-04-17 | 深圳易信科技股份有限公司 | Gas-liquid heat exchanger |
| CN108592663B (en) | 2018-02-12 | 2020-02-21 | 深圳易信科技股份有限公司 | Gas-liquid heat exchange device |
| US11098966B2 (en) * | 2018-08-08 | 2021-08-24 | Denso International America, Inc. | Header tank for heat exchanger |
| US11402161B2 (en) * | 2019-04-22 | 2022-08-02 | Hitachi-Johnson Controls Air Conditioning, Inc. | Distributor, heat exchanger, indoor unit, outdoor unit, and air-conditioning device |
| JP6822525B2 (en) * | 2019-06-28 | 2021-01-27 | ダイキン工業株式会社 | Heat exchanger and heat pump equipment |
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| JPH11325785A (en) * | 1998-05-14 | 1999-11-26 | Zexel:Kk | Radiator with integrated oil cooler |
| JPH11337289A (en) * | 1998-05-27 | 1999-12-10 | Showa Alum Corp | Heat exchanger |
| US6308771B1 (en) * | 1998-10-29 | 2001-10-30 | Advanced Thermal Solutions, Inc. | High performance fan tail heat exchanger |
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| US7044194B2 (en) * | 1999-10-26 | 2006-05-16 | Duramax Marine, Llc | Heat exchanger with beveled header |
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2012
- 2012-04-26 WO PCT/JP2012/002879 patent/WO2013160956A1/en active Application Filing
-
2013
- 2013-04-23 WO PCT/JP2013/061858 patent/WO2013161795A1/en active Application Filing
- 2013-04-23 EP EP13780882.0A patent/EP2865983B1/en active Active
- 2013-04-23 ES ES13780882T patent/ES2883139T3/en active Active
- 2013-04-23 US US14/394,124 patent/US20150053384A1/en not_active Abandoned
- 2013-04-23 CN CN201380025220.3A patent/CN104285121B/en active Active
- 2013-04-26 CN CN201320216136.7U patent/CN203464829U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111433548A (en) * | 2017-12-11 | 2020-07-17 | 三菱电机株式会社 | Fin-less heat exchanger and refrigeration cycle device |
| CN111433548B (en) * | 2017-12-11 | 2022-04-26 | 三菱电机株式会社 | Fin-less heat exchanger and refrigeration cycle device |
Also Published As
| Publication number | Publication date |
|---|---|
| WO2013160956A1 (en) | 2013-10-31 |
| ES2883139T3 (en) | 2021-12-07 |
| EP2865983B1 (en) | 2021-07-14 |
| CN104285121A (en) | 2015-01-14 |
| US20150053384A1 (en) | 2015-02-26 |
| CN203464829U (en) | 2014-03-05 |
| EP2865983A1 (en) | 2015-04-29 |
| WO2013161795A1 (en) | 2013-10-31 |
| EP2865983A4 (en) | 2016-05-25 |
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