CN106225327A - A kind of fin heat exchanger pipeline structure - Google Patents
A kind of fin heat exchanger pipeline structure Download PDFInfo
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- CN106225327A CN106225327A CN201610763657.2A CN201610763657A CN106225327A CN 106225327 A CN106225327 A CN 106225327A CN 201610763657 A CN201610763657 A CN 201610763657A CN 106225327 A CN106225327 A CN 106225327A
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- Prior art keywords
- pipe
- pipeline
- straight
- line cell
- end port
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B39/00—Evaporators; Condensers
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B39/00—Evaporators; Condensers
- F25B39/02—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
- F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
- F28F13/06—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
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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
- F28F9/26—Arrangements for connecting different sections of heat-exchange elements, e.g. of radiators
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2339/00—Details of evaporators; Details of condensers
- F25B2339/02—Details of evaporators
- F25B2339/023—Evaporators consisting of one or several sheets on one face of which is fixed a refrigerant carrying coil
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2500/00—Problems to be solved
- F25B2500/09—Improving heat transfers
Abstract
The invention discloses a kind of fin heat exchanger pipeline structure, described heat exchanger pipeline includes that several are the most each other in the pipe-line cell of setting arranged in parallel；In the Y direction, several pipe-line cell described are arranged in Heterogeneous Permutation alternatively up and down；Described pipe-line cell includes that some are in same vertical plane and along the straight pipeline of Z-direction spaced set；Straight pipeline in same pipe-line cell is connected by bend pipe, constitutes coil line structure；Connected by reverse bend pipe between adjacent two pipe-line cell.The flow direction that present invention achieves cold-producing medium flow direction and wind is completely contrary, and i.e. cold-producing medium and wind flow direction are reverse flow, thus improve the heat exchanger effectiveness of heat exchanger pipeline.
Description
Technical field
The present invention relates to a kind of pipeline structure, particularly to a kind of fin heat exchanger pipeline structure.
Background technology
Refrigeration for refrigerator industry development is rapid at present, and wind cooling refrigerator share commercially is more and more higher, as wind cooling refrigerator
Refrigeration part heat exchanger development important in refrigeration system is the rapidest, and finned type heat exchanger is that existing market is applied
Many one, but it is as the development of refrigerator industry, refrigeration performance and cost requirement to refrigerator are more and more higher, and heat exchanger will
Directly affects the rate of heat exchange of refrigerator refrigeration system, the raising of existing finned type heat exchanger performance mainly increases fin number
Amount, increases length of pipe etc. and increases heat exchange area, and said structure can improve heat exchanger effectiveness, but increases heat-exchange surface
Long-pending meeting causes the increase of production cost, and the reduction to production industry and refrigerator cost brings great difficulty, increases heat-exchange surface
The long-pending volume that also can directly increase heat exchanger so that the volume that in refrigerator, heat exchanger occupies increases the effective profit reducing refrigerator
Use space.
Fin arrangement on existing heat exchanger is which floor composition of superposition, and refrigerant flow direction is to be layered to flow back and forth, one
Layer is identical with the direction of wind flow, and next layer is in opposite direction with wind flow, as it is shown in figure 1, when air-cooled fin heat exchanger
When wind flow direction on 1 ' is to flow from top to bottom, cold-producing medium flows into through heat exchanger 1 ' pipeline from outlet 3 ' stream from import 2 '
Going out, when cold-producing medium flows into import 2 ', cold-producing medium flows along pipeline direction along S type path, as in Fig. 2, the direction of arrow represents system
The flow direction of cryogen, after cold-producing medium flow direction a to BOP, flows along pipeline according to b direction, with tailing edge pipeline approach axis
C flows, then after the d bottom horizontal flow sheet of direction, is flowed downward by a Serpentis curved tailing edge pipeline direction e, after through outlet 3 '
Flow out, cold-producing medium in whole heat exchanger flow process, cold-producing medium flowing side c and wind flow is in opposite direction can form convection current,
Heat exchange is abundant, and heat exchanger effectiveness is high, but cold-producing medium flow direction a and direction e is then identical with wind flow direction and adjacent
Flow direction c is in opposite direction, therefore cold-producing medium is contrary at the flow direction of adjacent two layers, and the temperature height of heat exchanger adjacent layer becomes
Changing contrary, thus cause whole heat exchanger heat exchange to be in a kind of cold and hot admixture, conducting heat mutually, so causing heat exchange
Rate is low.
Summary of the invention
The technical problem to be solved in the present invention is to provide a kind of fin heat exchanger pipeline structure, by provided by the present invention
Fin heat exchanger pipeline structure to be capable of the flow direction of cold-producing medium flow direction and wind completely contrary, i.e. cold-producing medium and
Wind flow direction is reverse flow, thus improves the heat exchanger effectiveness of heat exchanger pipeline.
For solving above-mentioned technical problem, the present invention uses following technical proposals:
A kind of fin heat exchanger pipeline structure, described heat exchanger pipeline include several the most each other in
The pipe-line cell of setting arranged in parallel；Several pipe-line cell described are arranged in Heterogeneous Permutation alternatively up and down in the Y direction；
Described pipe-line cell includes that some are in same vertical plane and along the straight pipe of Z-direction spaced set
Road；
Straight pipeline in same pipe-line cell is connected by bend pipe, constitutes coil line structure；
Connected by reverse bend pipe between adjacent two pipe-line cell.
By using the pipeline structure of the present invention to arrange, after cold-producing medium inflow heat exchanger, in same pipe-line cell
Cold-producing medium flows along S type (i.e. in the vertical plane in Z-direction) in same vertical plane back and forth along straight pipeline；In level
On direction, (i.e. in X-direction), cold-producing medium flow direction only keeps flowing from a direction to another one direction, i.e. cold-producing medium exists
Heat exchanger pipeline the most back and forth flows, so makes the overall flow direction of cold-producing medium from heat exchanger one end to other one
End flowing, does not occur that rightabout flowing, this heat exchanger pipeline arrangement mode make cold-producing medium flow direction single,
Reverse flow does not occur.The heat exchanger using this tubes rows cloth to design can be directly realized by the flow direction and the air of cold-producing medium
The flow direction completely contrary, heat exchange in a heat exchanger realizes convection current, and according to heat exchange principle, convective heat exchange process heat is handed over
Change efficiency and can reach the highest.
Further, along described X-direction, the pipe-line cell of odd column is in the first same plane, the pipe of even column
Road unit is in the second same plane.
The present invention design pipeline arrangement make the pipe-line cell of odd column and even column not in same level,
So advantage of arrangement is that adjacent two pipe-line cell are the most interlaced, and more straight pipeline can be made directly to expose
Not stopping mutually, when heat exchange occurs, air can stop the most mutually, it is possible to pole with more pipeline contact
Big raising heat exchanging efficiency.
Further, described heat exchanger pipeline is for bend composition continuously by a pipeline.
Further, the pipe-line cell of adjacent two odd columns is relative to the idol between the pipe-line cell of these adjacent two odd columns
Ordered series of numbers pipe-line cell is that mirror image is to becoming to arrange.
Further, strange relative between the pipe-line cell of these adjacent two even columns of the pipe-line cell of adjacent two even columns
Ordered series of numbers pipe-line cell is that mirror image is to becoming to arrange.
Further, described heat exchanger pipeline includes in X direction in the first pipe misplaced alternatively up and down and be arranged side by side
Road unit and the second pipe-line cell；
Described first pipe-line cell includes that being in interior and along Z-direction spaced set the first upper strata of same vertical plane puts down
The straight pipeline in straight tube road and the first lower floor；
Described second pipe-line cell includes that being in interior and along Z-direction spaced set the second upper strata of same vertical plane puts down
The straight pipeline in straight tube road and the second lower floor；
One end port of the described first straight pipeline in upper strata is by one end port of the straight pipeline of bend pipe and the first lower floor even
Connecing, the other end port of the first straight pipeline of lower floor is connected by one end port of the straight pipeline of reverse bend pipe and the second lower floor,
The other end port of the second straight pipeline of lower floor is connected by one end port of the straight pipeline of bend pipe and the second upper strata.
Further, described heat exchanger pipeline includes in X direction in the first pipe misplaced alternatively up and down and be arranged side by side
Road unit and the second pipe-line cell；
Described first pipe-line cell includes that being in interior and along Z-direction spaced set the first upper strata of same vertical plane puts down
Straight tube road, the first straight pipeline of the straight pipeline in middle level and the first lower floor；
Described second pipe-line cell includes that being in interior and along Z-direction spaced set the second upper strata of same vertical plane puts down
Straight tube road, the second straight pipeline of the straight pipeline in middle level and the second lower floor；
One end port of the described first straight pipeline in upper strata is by one end port of the straight pipeline of bend pipe and the first middle level even
Connecing, the other end port of the first straight pipeline in middle level is connected by one end port of the straight pipeline of bend pipe and the first lower floor, and first
One end port connection by the straight pipeline of reverse bend pipe and the second lower floor of the other end port of lower floor is straight pipeline；
The other end port of the second straight pipeline of lower floor is connected by one end port of the straight pipeline of bend pipe and the second middle level,
The other end port of the second straight pipeline in middle level is connected by one end port of the straight pipeline of bend pipe and the second upper strata.
Further, described heat exchanger pipeline includes in X direction in the first pipe misplaced alternatively up and down and be arranged side by side
Road unit, the second pipe-line cell and the 3rd pipe-line cell；
Described first pipe-line cell includes that being in interior and along Z-direction spaced set the first upper strata of same vertical plane puts down
The straight pipeline in straight tube road and the first lower floor；
Described second pipe-line cell includes that being in interior and along Z-direction spaced set the second upper strata of same vertical plane puts down
The straight pipeline in straight tube road and the second lower floor；
Described 3rd pipe-line cell includes that being in interior and along Z-direction spaced set the 3rd upper strata of same vertical plane puts down
Straight tube road and the 3rd straight pipeline of lower floor；
One end port of the described first straight pipeline in upper strata is by one end port of the straight pipeline of bend pipe and the first lower floor even
Connecing, the other end port of the first straight pipeline of lower floor is connected by one end port of the straight pipeline of reverse bend pipe and the second lower floor,
The other end port of the second straight pipeline of lower floor is connected by one end port of the straight pipeline of bend pipe and the second upper strata, the second upper strata
The other end port of straight pipeline is connected by one end port of reverse bend pipe and the 3rd straight pipeline in upper strata, and the 3rd upper strata is straight
The other end port of pipeline is connected by one end port of bend pipe and the 3rd straight pipeline of lower floor.
The present invention compared with prior art, has the advantages that
1, heat exchanger pipeline structure provided by the present invention is capable of channel interior cold-producing medium and air-flow direction shape
Become adverse current, and disclosure satisfy that the counterflow heat exchanger demand to pipeline by this pipeline arrangement, real by this pipeline structure
Existing counterflow heat exchanger can promote overall thermal exchange efficiency 20%-30%.
2, the convection type that heat exchanger pipeline structure provided by the present invention is formed by above-mentioned cold-producing medium and air, makes
Obtain internal heat exchanger cold-producing medium and realize sufficient heat exchange with surroundings space temperature, make heat exchanger effectiveness reach
Height, this being designed under not increasing any cost, material and heat exchange volume improves rate of heat exchange.
Accompanying drawing explanation
Fig. 1 is the structural representation of prior art.
Fig. 2 is that the cold-producing medium of Fig. 1 is at tube runs direction schematic diagram.
Fig. 3 is the cold-producing medium in present heat exchanger pipeline and wind direction reverse flow principle schematic.
Fig. 4 is the structural front view of Fig. 3.
Fig. 5 is the perspective view of heat exchanger pipeline in first embodiment of the invention.
Fig. 6 is the structural front view of heat exchanger pipeline in first embodiment of the invention.
Fig. 7 is the perspective view of heat exchanger pipeline in second embodiment of the invention.
Fig. 8 is the structural front view of heat exchanger pipeline in second embodiment of the invention.
Fig. 9 is the perspective view of heat exchanger pipeline in third embodiment of the invention.
Figure 10 is the structural front view of heat exchanger pipeline in third embodiment of the invention.
Detailed description of the invention
The detailed description of the invention of the present invention is described below in conjunction with the accompanying drawings.
As shown in Figure 3,4, the present invention provides a kind of fin heat exchanger pipeline structure, if described heat exchanger pipeline includes
Dry pipe-line cell 1 in setting arranged in parallel the most each other；Several pipe-line cell 1 described are presented in the Y direction
Replace down Heterogeneous Permutation to arrange；Along described X-direction, the pipe-line cell 1 of odd column is in the first same plane 100, even number
The pipe-line cell 1 of row is in the second same plane 200.The pipe-line cell 1 of adjacent two odd columns is adjacent two strange relative to this
One-tenth is arranged by the even column pipe-line cell 1 between the pipe-line cell 1 of ordered series of numbers in mirror image；Pipe-line cell 1 phase of adjacent two even columns
For the odd column pipe-line cell 1 between the pipe-line cell 1 of these adjacent two even columns in mirror image to becoming to arrange.
Described pipe-line cell 1 includes that some are in same vertical plane and along the straight pipe of Z-direction spaced set
Road 2；Straight pipeline 2 in same pipe-line cell 1 is connected by bend pipe 3, constitutes coil line structure；Adjacent two pipe-line cell
Connected by reverse bend pipe 4 between 1.Described heat exchanger pipeline also includes being connected with the straight pipeline 2 in head end pipe-line cell 1
The cold-producing medium input pipe 5 connect, and the cold-producing medium outlet tube 6 being connected with the straight pipeline 2 in tail end pipe-line cell 1.
Further, described heat exchanger pipeline is for bend composition continuously by a pipeline.
The operation principle of the present invention is: when after cold-producing medium inflow heat exchanger, on same pipe-line cell 1 inner refrigerant edge
Straight pipeline 2 to flow back and forth along S type (i.e. in the vertical plane in Z-direction) in same vertical plane；In the horizontal direction
(i.e. in X-direction) cold-producing medium flow direction only keeps flowing from a direction to another one direction, and i.e. cold-producing medium is in heat exchange
Device pipeline the most back and forth flows, so makes the overall flow direction of cold-producing medium from heat exchanger one end to other end stream
Dynamic, do not occur that rightabout flowing, this heat exchanger pipeline arrangement mode make cold-producing medium flow direction single, do not have
Reverse flow occurs.The heat exchanger using this tubes rows cloth to design can be directly realized by the flow direction of cold-producing medium and the stream of air
To the most contrary, heat exchange in a heat exchanger realizes convection current, and according to heat exchange principle, convective heat exchange process heat exchange is imitated
Rate can reach the highest.
Embodiment 1:
As shown in Figure 5,6, in the present embodiment, described heat exchanger pipeline include in X direction in alternatively up and down dislocation and also
The first pipe-line cell 10 and the second pipe-line cell 20 that row is arranged；First pipe-line cell 10 is in the first plane 100, the second pipe
Road unit 20 is in the second plane 200.
In described first pipe-line cell 10 includes being in same vertical plane and along the first upper strata of Z-direction spaced set
Straight pipeline 101 and the straight pipeline of the first lower floor 102；
In described second pipe-line cell 20 includes being in same vertical plane and along the second upper strata of Z-direction spaced set
Straight pipeline 201 and the straight pipeline of the second lower floor 202；
One end port of the described first straight pipeline in upper strata 101 one end by the straight pipeline of bend pipe 3 and the first lower floor 102
Port connects, and the other end port of the first straight pipeline of lower floor 102 is by reverse bend pipe 4 and the straight pipeline of the second lower floor 202
One end port connects, and the other end port of the second straight pipeline of lower floor 202 is by the straight pipeline of bend pipe 3 and the second upper strata 201
One end port connects.
The other end port of the described first straight pipeline in upper strata 101 connects cold-producing medium input pipe 5, the second straight pipe in upper strata
The other end port on road 201 connects cold-producing medium outlet tube 6.
Embodiment 2:
As shown in Figure 7,8, in the present embodiment, described heat exchanger pipeline include in X direction in alternatively up and down dislocation and also
The first pipe-line cell 30 and the second pipe-line cell 40 that row is arranged；First pipe-line cell 30 is in the first plane 100, the second pipe
Road unit 40 is in the second plane 200.
In described first pipe-line cell 30 includes being in same vertical plane and along the first upper strata of Z-direction spaced set
The straight pipeline in straight pipeline the 301, first middle level 302 and the straight pipeline of the first lower floor 303；
In described second pipe-line cell 40 includes being in same vertical plane and along the second upper strata of Z-direction spaced set
The straight pipeline in straight pipeline the 401, second middle level 402 and the straight pipeline of the second lower floor 403；
One end port of the described first straight pipeline in upper strata 301 one end by the straight pipeline of bend pipe 3 and the first middle level 302
Port connects, the other end port of the first straight pipeline in middle level 302 one end by the straight pipeline of bend pipe 3 and the first lower floor 303
Port connects, and the other end port of the first straight pipeline of lower floor 303 is by reverse bend pipe 4 and the straight pipeline of the second lower floor 403
One end port connects；
The other end port of the second straight pipeline of lower floor 403 one end end by the straight pipeline of bend pipe 3 and the second middle level 402
Mouth connects, the other end port of the second straight pipeline in middle level 402 one end end by the straight pipeline of bend pipe 3 and the second upper strata 401
Mouth connects.
The other end port of the described first straight pipeline in upper strata 301 connects cold-producing medium input pipe 5, the second straight pipe in upper strata
The other end port on road 401 connects cold-producing medium outlet tube 6.
Embodiment 3:
Such as Fig. 9, shown in 10, in the present embodiment, described heat exchanger pipeline includes in X direction in dislocation alternatively up and down and also
The first pipe-line cell the 50, second pipe-line cell 60 and the 3rd pipe-line cell 70 that row is arranged；In the present embodiment, the first of odd column
Pipe-line cell 50 and the 3rd pipe-line cell 70 are in the first plane 100, and it is flat that the second pipe-line cell 60 of even column is in second
On face 200, and between the pipe-line cell 50,70 of adjacent two odd columns is relative to the pipe-line cell 50,70 of these adjacent two odd columns
Even column pipe-line cell 60 in mirror image to become arrange.
In described first pipe-line cell 50 includes being in same vertical plane and along the first upper strata of Z-direction spaced set
Straight pipeline 501 and the straight pipeline of the first lower floor 502；
In described second pipe-line cell 60 includes being in same vertical plane and along the second upper strata of Z-direction spaced set
Straight pipeline 601 and the straight pipeline of the second lower floor 602；
In described 3rd pipe-line cell 70 includes being in same vertical plane and along the 3rd upper strata of Z-direction spaced set
Straight pipeline 701 and the 3rd straight pipeline of lower floor 702；
One end port of the described first straight pipeline in upper strata 501 one end by the straight pipeline of bend pipe 3 and the first lower floor 502
Port connects, and the other end port of the first straight pipeline of lower floor 502 is by reverse bend pipe 4 and the straight pipeline of the second lower floor 602
One end port connects, and the other end port of the second straight pipeline of lower floor 602 is by the straight pipeline of bend pipe 3 and the second upper strata 601
One end port connects, and the other end port of the second straight pipeline in upper strata 601 passes through reverse bend pipe 4 and the 3rd straight pipeline in upper strata
One end port of 701 connects, and the other end port of the 3rd straight pipeline in upper strata 701 passes through bend pipe 3 and the 3rd straight pipeline of lower floor
One end port of 702 connects.
The other end port of the described first straight pipeline in upper strata 501 connects cold-producing medium input pipe 5, the 3rd straight pipe of lower floor
The other end port on road 702 connects cold-producing medium outlet tube 6.
The word in the description orientation employed in Ben Wen " on ", D score, "left", "right" etc. be for explanation facilitate base
In accompanying drawing for the orientation shown in drawing, in actual device these orientation be likely to be due to device disposing way and
Different.
In sum, embodiment of the present invention only provides a kind of optimal embodiment, in the technology of the present invention
Hold and technical characterstic has revealed that as above, but one skilled in the art scholar is still potentially based on disclosed content and makees
The various replacements without departing substantially from creation spirit of the present invention and modification；Therefore, protection scope of the present invention is not limited to disclosed in embodiment
Technology contents, therefore all shapes under this invention, structure and principle done equivalence change, be encompassed by the protection model of the present invention
In enclosing.
Claims (8)
1. a fin heat exchanger pipeline structure, it is characterised in that: described heat exchanger pipeline includes several phases in X direction
In the pipe-line cell of setting arranged in parallel between Hu；In the Y direction, several pipe-line cell described are in Heterogeneous Permutation alternatively up and down
Arrange；
Described pipe-line cell includes that some are in same vertical plane and along the straight pipeline of Z-direction spaced set；
Straight pipeline in same pipe-line cell is connected by bend pipe, constitutes coil line structure；
Connected by reverse bend pipe between adjacent two pipe-line cell.
A kind of fin heat exchanger pipeline structure the most according to claim 1, it is characterised in that: preferably, along described X side
To, the pipe-line cell of odd column is in the first same plane, and the pipe-line cell of even column is in the second same plane.
A kind of fin heat exchanger pipeline structure the most according to claim 1, it is characterised in that: described heat exchanger pipeline
For bending composition continuously by a pipeline.
A kind of fin heat exchanger pipeline structure the most according to claim 1, it is characterised in that: the pipe of adjacent two odd columns
Road unit is that mirror image is to becoming to arrange relative to the even column pipe-line cell between the pipe-line cell of these adjacent two odd columns.
A kind of fin heat exchanger pipeline structure the most according to claim 1, it is characterised in that: the pipe of adjacent two even columns
Road unit is that mirror image is to becoming to arrange relative to the odd column pipe-line cell between the pipe-line cell of these adjacent two even columns.
A kind of fin heat exchanger pipeline structure the most according to claim 1, it is characterised in that: described heat exchanger pipeline
Including in X direction in the first pipe-line cell misplaced alternatively up and down and be arranged side by side and the second pipe-line cell；
In described first pipe-line cell includes being in same vertical plane and along the first straight pipe in upper strata of Z-direction spaced set
The straight pipeline in road and the first lower floor；
In described second pipe-line cell includes being in same vertical plane and along the second straight pipe in upper strata of Z-direction spaced set
The straight pipeline in road and the second lower floor；
One end port of the described first straight pipeline in upper strata is connected by one end port of the straight pipeline of bend pipe and the first lower floor, the
The other end port of the one straight pipeline of lower floor is connected by one end port of the straight pipeline of reverse bend pipe and the second lower floor, second time
The other end port of the straight pipeline of layer is connected by one end port of the straight pipeline of bend pipe and the second upper strata.
A kind of fin heat exchanger pipeline structure the most according to claim 1, it is characterised in that: described heat exchanger pipeline
Including in X direction in the first pipe-line cell misplaced alternatively up and down and be arranged side by side and the second pipe-line cell；
In described first pipe-line cell includes being in same vertical plane and along the first straight pipe in upper strata of Z-direction spaced set
Road, the first straight pipeline of the straight pipeline in middle level and the first lower floor；
In described second pipe-line cell includes being in same vertical plane and along the second straight pipe in upper strata of Z-direction spaced set
Road, the second straight pipeline of the straight pipeline in middle level and the second lower floor；
One end port of the described first straight pipeline in upper strata is connected by one end port of the straight pipeline of bend pipe and the first middle level, the
The other end port of the one straight pipeline in middle level is connected by one end port of the straight pipeline of bend pipe and the first lower floor, and the first lower floor puts down
The other end port on straight tube road is connected by one end port of the straight pipeline of reverse bend pipe and the second lower floor；
The other end port of the second straight pipeline of lower floor is connected by one end port of the straight pipeline of bend pipe and the second middle level, and second
One end port connection by the straight pipeline of bend pipe and the second upper strata of the other end port of middle level is straight pipeline.
A kind of fin heat exchanger pipeline structure the most according to claim 1, it is characterised in that: described heat exchanger pipeline
Including in X direction in the first pipe-line cell misplacing alternatively up and down and being arranged side by side, the second pipe-line cell and the 3rd pipe-line cell；
In described first pipe-line cell includes being in same vertical plane and along the first straight pipe in upper strata of Z-direction spaced set
The straight pipeline in road and the first lower floor；
In described second pipe-line cell includes being in same vertical plane and along the second straight pipe in upper strata of Z-direction spaced set
The straight pipeline in road and the second lower floor；
In described 3rd pipe-line cell includes being in same vertical plane and along the 3rd straight pipe in upper strata of Z-direction spaced set
Road and the 3rd straight pipeline of lower floor；
One end port of the described first straight pipeline in upper strata is connected by one end port of the straight pipeline of bend pipe and the first lower floor, the
The other end port of the one straight pipeline of lower floor is connected by one end port of the straight pipeline of reverse bend pipe and the second lower floor, second time
The other end port of the straight pipeline of layer is connected by one end port of the straight pipeline of bend pipe and the second upper strata, the second straight pipe in upper strata
The other end port on road is connected by one end port of reverse bend pipe and the 3rd straight pipeline in upper strata, the 3rd straight pipeline in upper strata
Other end port is connected by one end port of bend pipe and the 3rd straight pipeline of lower floor.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610052211.9A CN105509374A (en) | 2016-01-27 | 2016-01-27 | Reverse-flow heat exchanger |
| CN2016100522119 | 2016-01-27 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106225327A true CN106225327A (en) | 2016-12-14 |
| CN106225327B CN106225327B (en) | 2018-09-25 |
Family
ID=55717542
Family Applications (4)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610052211.9A Pending CN105509374A (en) | 2016-01-27 | 2016-01-27 | Reverse-flow heat exchanger |
| CN201621016106.1U Active CN206037805U (en) | 2016-01-27 | 2016-08-30 | Fin structure of heat exchanger |
| CN201621016142.8U Withdrawn - After Issue CN206037485U (en) | 2016-01-27 | 2016-08-30 | Fin heat exchanger pipeline structure |
| CN201610763657.2A Active CN106225327B (en) | 2016-01-27 | 2016-08-30 | A kind of fin heat exchanger pipeline structure |
Family Applications Before (3)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610052211.9A Pending CN105509374A (en) | 2016-01-27 | 2016-01-27 | Reverse-flow heat exchanger |
| CN201621016106.1U Active CN206037805U (en) | 2016-01-27 | 2016-08-30 | Fin structure of heat exchanger |
| CN201621016142.8U Withdrawn - After Issue CN206037485U (en) | 2016-01-27 | 2016-08-30 | Fin heat exchanger pipeline structure |
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| CN (4) | CN105509374A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105509374A (en) * | 2016-01-27 | 2016-04-20 | 河南新科隆电器有限公司 | Reverse-flow heat exchanger |
| CN107477940A (en) * | 2017-07-10 | 2017-12-15 | 青岛海尔特种电器有限公司 | A kind of medical refrigerator |
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| CN101118107A (en) * | 2006-08-01 | 2008-02-06 | 海尔集团公司 | Condensator and heat exchange method thereof |
| CN101634506A (en) * | 2008-07-21 | 2010-01-27 | Tcl集团股份有限公司 | Heat exchanger structure of air conditioner and realizing method thereof |
| JP2010230304A (en) * | 2009-03-04 | 2010-10-14 | Sumitomo Light Metal Ind Ltd | Fin and tube type heat exchanger for air conditioner |
| CN201945096U (en) * | 2011-03-03 | 2011-08-24 | Tcl空调器(中山)有限公司 | Evaporator structure |
| CN204987565U (en) * | 2015-08-27 | 2016-01-20 | 南京国睿博拉贝尔环境能源有限公司 | Air source heat pump idle call fin type heat exchanger connection structure |
| CN206037485U (en) * | 2016-01-27 | 2017-03-22 | 河南新科隆电器有限公司 | Fin heat exchanger pipeline structure |
-
2016
- 2016-01-27 CN CN201610052211.9A patent/CN105509374A/en active Pending
- 2016-08-30 CN CN201621016106.1U patent/CN206037805U/en active Active
- 2016-08-30 CN CN201621016142.8U patent/CN206037485U/en not_active Withdrawn - After Issue
- 2016-08-30 CN CN201610763657.2A patent/CN106225327B/en active Active
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|---|---|---|---|---|
| CN101118107A (en) * | 2006-08-01 | 2008-02-06 | 海尔集团公司 | Condensator and heat exchange method thereof |
| CN101634506A (en) * | 2008-07-21 | 2010-01-27 | Tcl集团股份有限公司 | Heat exchanger structure of air conditioner and realizing method thereof |
| JP2010230304A (en) * | 2009-03-04 | 2010-10-14 | Sumitomo Light Metal Ind Ltd | Fin and tube type heat exchanger for air conditioner |
| CN201945096U (en) * | 2011-03-03 | 2011-08-24 | Tcl空调器(中山)有限公司 | Evaporator structure |
| CN204987565U (en) * | 2015-08-27 | 2016-01-20 | 南京国睿博拉贝尔环境能源有限公司 | Air source heat pump idle call fin type heat exchanger connection structure |
| CN206037485U (en) * | 2016-01-27 | 2017-03-22 | 河南新科隆电器有限公司 | Fin heat exchanger pipeline structure |
Also Published As
| Publication number | Publication date |
|---|---|
| CN206037485U (en) | 2017-03-22 |
| CN106225327B (en) | 2018-09-25 |
| CN105509374A (en) | 2016-04-20 |
| CN206037805U (en) | 2017-03-22 |
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