CN203869375U - Heat exchanger structure - Google Patents
Heat exchanger structure Download PDFInfo
- Publication number
- CN203869375U CN203869375U CN201420250533.0U CN201420250533U CN203869375U CN 203869375 U CN203869375 U CN 203869375U CN 201420250533 U CN201420250533 U CN 201420250533U CN 203869375 U CN203869375 U CN 203869375U
- Authority
- CN
- China
- Prior art keywords
- heat exchanger
- fin
- pipeline
- heat exchange
- exchanger fin
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 230000005494 condensation Effects 0.000 claims description 21
- 238000009833 condensation Methods 0.000 claims description 21
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 18
- 229910052802 copper Inorganic materials 0.000 claims description 18
- 239000010949 copper Substances 0.000 claims description 18
- 229910000831 Steel Inorganic materials 0.000 claims description 11
- 239000010959 steel Substances 0.000 claims description 11
- 229910052751 metal Inorganic materials 0.000 claims description 8
- 239000002184 metal Substances 0.000 claims description 8
- 238000004378 air conditioning Methods 0.000 claims description 4
- 238000005187 foaming Methods 0.000 claims description 4
- 241001466460 Alveolata Species 0.000 claims description 3
- 239000006260 foam Substances 0.000 abstract 1
- 239000007788 liquid Substances 0.000 description 6
- 239000000463 material Substances 0.000 description 6
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 3
- 229910052782 aluminium Inorganic materials 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000007547 defect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000003507 refrigerant Substances 0.000 description 1
Abstract
The utility model discloses a heat exchanger structure which comprises a heat exchanger fin and a heat exchanger pipeline, wherein the heat exchanger pipeline is arranged in the heat exchanger fin which adopts a foam fin provided with through holes. Compared with the prior art, the provided heat exchanger structure can effectively increase the heat exchange area of the heat exchanger fin and improve the disturbance of air passing the fin, so that the heat exchange efficiency of the heat exchanger is improved.
Description
Technical field
The utility model relates to air-conditioner field, exactly refers to a kind of heat exchanger structure.
Background technology
At present, the fin configuration that heat exchanger of air conditioner is used is generally plain film, ripple or the figurate aluminium flake of windowing.In order to improve heat exchange efficiency, must improve the heat exchange area of fin and the disturbance that air flows through fin, thereby improve heat exchanger heat exchange efficiency, therefore, heat exchanger fin can improve to improve heat exchange efficiency towards this direction.
Utility model content
For above-mentioned defect, the technical problem that the utility model solves is to provide a kind of heat exchanger structure, can effectively improve heat exchanger fin heat exchange area and improve the disturbance that air flows through fin, thereby improve heat exchanger heat exchange efficiency.
In order to solve above technical problem, the heat exchanger structure that the utility model provides, comprises heat exchanger fin and heat exchange manifold, and described heat exchange manifold is arranged in described heat exchanger fin, and described heat exchanger fin is the foam-like fin with through hole.
Preferably, described heat exchanger fin is that aluminum material is made.
Preferably, described heat exchanger fin is alveolate texture.
Preferably, the direct foaming on heat exchange manifold of described heat exchanger fin.
Preferably, described heat exchanger fin is fixing on air-conditioning by left end metal plate and right-hand member metal plate.
Preferably, described heat exchange manifold is inner screw thread copper pipe.
Preferably, described heat exchange manifold comprises condensation segment pipeline and super cooled sect pipeline, and described condensation segment pipeline is inner screw thread copper pipe, and described super cooled sect pipeline is copper pipe or steel pipe.
Preferably, the caliber of the caliber of described super cooled sect pipeline and described condensation segment pipeline is identical or different.
The heat exchanger structure that the utility model provides, comprises heat exchanger fin and heat exchange manifold, and heat exchange manifold is arranged in heat exchanger fin, and heat exchanger fin is the foam-like fin with through hole.Compared with prior art, the heat exchanger structure that the utility model provides, heat exchanger fin uses the foam-like fin with through hole to substitute plain film, ripple or the figurate fin of windowing using at present, can effectively improve heat exchanger fin heat exchange area and improve the disturbance that air flows through fin, thereby improve heat exchanger heat exchange efficiency.
Especially, the heat exchanger structure that the utility model provides, heat exchanger fin is foaming on heat exchange manifold directly, compare with the prior art of heat exchange manifold being combined with heat exchanger fin by tube mode, can be more firm, the thermal resistance of generation can be less, and heat exchange efficiency can more be increased.
Further, the heat exchanger structure that the utility model provides, condensation segment pipeline is inner screw thread copper pipe, super cooled sect pipeline is copper pipe or steel pipe, in super cooled sect pipeline, be condensed into liquid cold-producing medium in cooling stage again, no longer need to discharge a large amount of condenser heats, play the effect of storage simultaneously, super cooled sect pipeline adopts copper pipe or steel pipe, and because the market price of copper pipe or Steel material is than the low price of inner screw thread copper pipe, especially steel pipe is more cheap, therefore can guarantee under the prerequisite of the abundant heat exchange of cold-producing medium under different condensing states and storage, reduce materials'use cost simultaneously, strengthen the competitiveness of product in market.
Accompanying drawing explanation
Fig. 1 is the structural representation of heat exchanger structure in the utility model embodiment, the flow direction that in figure, the direction of arrow is cold-producing medium.
The specific embodiment
For those skilled in the art can understand technical scheme provided by the utility model better, below in conjunction with specific embodiment, set forth.
Refer to Fig. 1, this figure is the structural representation of heat exchanger structure in the utility model embodiment, the flow direction that in figure, the direction of arrow is cold-producing medium.
The heat exchanger structure that the utility model embodiment provides, comprise heat exchanger fin 1 and heat exchange manifold 2, heat exchanger fin 1 is fixing on air-conditioning by left end metal plate 4 and right-hand member metal plate 3, and heat exchange manifold 2 is arranged in heat exchanger fin 1, and heat exchanger fin 1 is the foam-like fin with through hole.The alveolate texture that heat exchanger fin 1 is made for aluminum material.
Heat exchanger fin 1 is foaming on heat exchange manifold 2 directly, compares with the prior art of heat exchange manifold being combined with heat exchanger fin by tube mode, and such structure can be more firm, and the thermal resistance of generation can be less, and heat exchange efficiency can more be increased.
Compared with prior art, the heat exchanger structure that the present embodiment provides, heat exchanger fin 1 use substitutes with the foam-like fin of through hole plain film, ripple or the figurate fin of windowing using at present, can effectively improve heat exchanger fin 1 heat exchange area and improve the disturbance that air flows through fin, thereby improve heat exchanger heat exchange efficiency.
As heat exchange manifold 2 is all used as condensation segment pipeline, 2 employings of heat exchange manifold are with the inner screw thread copper pipe of caliber; If pipeline is divided into two sections of condensation segment pipeline and super cooled sect pipelines, condensation segment adopts inner screw thread copper pipe, and super cooled sect pipeline adopts copper pipe or steel pipe.The caliber of super cooled sect pipeline is identical with the caliber of condensation segment pipeline, or differs from the caliber (not shown) of condensation segment pipeline.In super cooled sect pipeline, be condensed into liquid cold-producing medium in cooling stage again, no longer need to discharge a large amount of condenser heats, play the effect of storage simultaneously, this section of employing copper pipe or steel pipe, as adopt copper pipe or steel pipe, because the market price of copper pipe or Steel material is than the low price of inner screw thread copper pipe, especially steel pipe is more cheap, therefore can guarantee under the prerequisite of the abundant heat exchange of cold-producing medium under different condensing states and storage, reduce materials'use cost simultaneously, strengthen the competitiveness of product in market.
In order to adapt to different air-conditioners, the caliber of the caliber of super cooled sect pipeline and condensation segment pipeline is identical or different, and the caliber of super cooled sect pipeline can be greater than or less than the caliber of condensation segment pipeline.
The workflow of the heat exchanger of the air-conditioner that the utility model embodiment provides is as follows:
Heat exchanger fin 1 is fixing on air-conditioning by right-hand member metal plate 3 and left end metal plate 4, the gas refrigerant of HTHP enters heat exchanging pipe 2 condensation segments from heat exchanger air inlet, by condensation segment pipeline and heat exchanger fin 1 and cold air forced heat-exchanging, discharge a large amount of condensation heat, be condensed into liquid, enter super cooled sect pipeline, in super cooled sect pipeline pipe, stream send, by super cooled sect pipeline and heat exchanger fin 1 and cold air forced heat-exchanging, continue to reduce fluid temperature, become subcooled liquid, store this part subcooled liquid simultaneously, final by super cooled sect pipeline outlet outflow, complete heat exchange.
If heat exchanger heat-exchanging tube 2 is all used as condensation segment,, by condensation segment pipeline and heat exchanger fin 1 and cold air forced heat-exchanging, discharge a large amount of condensation heat, the liquid being condensed into directly flows out by the outlet of condensation segment pipeline, completes heat exchange.
Above-mentioned explanation to the disclosed embodiments, makes professional and technical personnel in the field can realize or use the utility model.To the multiple modification of these embodiment, will be apparent for those skilled in the art, General Principle as defined herein can, in the situation that not departing from spirit or scope of the present utility model, realize in other embodiments.Therefore, the utility model will can not be restricted to these embodiment shown in this article, but will meet the widest scope consistent with principle disclosed herein and features of novelty.
Claims (7)
1. a heat exchanger structure, is characterized in that, comprises heat exchanger fin and heat exchange manifold, and described heat exchange manifold is arranged in described heat exchanger fin, and described heat exchanger fin is the foam-like fin with through hole.
2. heat exchanger structure according to claim 1, is characterized in that, described heat exchanger fin is alveolate texture.
3. heat exchanger structure according to claim 1, is characterized in that, described heat exchanger fin is foaming on heat exchange manifold directly.
4. heat exchanger structure according to claim 1, is characterized in that, described heat exchanger fin is fixing on air-conditioning by left end metal plate and right-hand member metal plate.
5. heat exchanger structure according to claim 1, is characterized in that, described heat exchange manifold is inner screw thread copper pipe.
6. heat exchanger structure according to claim 1, is characterized in that, described heat exchange manifold comprises condensation segment pipeline and super cooled sect pipeline, and described condensation segment pipeline is inner screw thread copper pipe, and described super cooled sect pipeline is copper pipe or steel pipe.
7. heat exchanger structure according to claim 6, is characterized in that, the caliber of the caliber of described super cooled sect pipeline and described condensation segment pipeline is identical or different.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420250533.0U CN203869375U (en) | 2014-05-15 | 2014-05-15 | Heat exchanger structure |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420250533.0U CN203869375U (en) | 2014-05-15 | 2014-05-15 | Heat exchanger structure |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203869375U true CN203869375U (en) | 2014-10-08 |
Family
ID=51650319
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420250533.0U Active CN203869375U (en) | 2014-05-15 | 2014-05-15 | Heat exchanger structure |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203869375U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103954080A (en) * | 2014-05-15 | 2014-07-30 | 广东志高空调有限公司 | Heat exchanger structure |
-
2014
- 2014-05-15 CN CN201420250533.0U patent/CN203869375U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103954080A (en) * | 2014-05-15 | 2014-07-30 | 广东志高空调有限公司 | Heat exchanger structure |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204063687U (en) | Heat exchanger and freezing cycle device | |
| CN102692101A (en) | Heat exchanger and air conditioner equipment | |
| CN102121768A (en) | Heat exchange apparatus with heat pipe soaking device for refrigeration air conditioning system | |
| CN105066519A (en) | Dry-type evaporator and refrigeration system provided with dry-type evaporator | |
| CN104534722A (en) | Air conditioning refrigeration equipment | |
| CN105333642A (en) | Cold and heat type heat pump system | |
| JP2010216692A5 (en) | ||
| CN203869375U (en) | Heat exchanger structure | |
| CN201909495U (en) | Multi-tube coaxial type sleeve heat exchanger | |
| CN207280261U (en) | A kind of high-performance heat exchanger flow passage structure and air conditioner | |
| CN104006575B (en) | A kind of wind-water double-source heat pump water chiller-heater unit and control method thereof | |
| CN103954080A (en) | Heat exchanger structure | |
| CN203797945U (en) | Air conditioner water heating system | |
| CN2901185Y (en) | Variable diameter type sleeve evaporator | |
| CN203349414U (en) | Air conditioner system | |
| CN203731729U (en) | Water refrigerating unit | |
| CN203011009U (en) | Novel heat exchanger structure for air conditioner | |
| CN203011017U (en) | Heat exchanger structure for air conditioner | |
| CN204285906U (en) | Operation of air conditioning systems | |
| CN201974081U (en) | Heat-exchanging device with heat-pipe thermal spreader for refrigerative air-conditioning system | |
| CN202792723U (en) | Parallel flow condenser for freezer | |
| CN204535174U (en) | Multi-functional air conditioner unit | |
| CN212179271U (en) | Double-source heat pump unit | |
| CN201440014U (en) | Microchannel evaporator for domestic air conditioner | |
| CN203837339U (en) | Finned coil with efficient heat exchange design for heat pump |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| PP01 | Preservation of patent right |
Effective date of registration: 20240326 Granted publication date: 20141008 |
|
| PP01 | Preservation of patent right |