CN209672489U - Fin-tube type heat exchanger, air-conditioner outdoor unit and air conditioner - Google Patents
Fin-tube type heat exchanger, air-conditioner outdoor unit and air conditioner Download PDFInfo
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- CN209672489U CN209672489U CN201920334400.4U CN201920334400U CN209672489U CN 209672489 U CN209672489 U CN 209672489U CN 201920334400 U CN201920334400 U CN 201920334400U CN 209672489 U CN209672489 U CN 209672489U
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- heat exchanger
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- 239000003507 refrigerant Substances 0.000 claims abstract description 45
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 8
- 229910052802 copper Inorganic materials 0.000 claims description 8
- 239000010949 copper Substances 0.000 claims description 8
- 238000002474 experimental method Methods 0.000 description 17
- 230000015572 biosynthetic process Effects 0.000 description 16
- 238000003786 synthesis reaction Methods 0.000 description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 230000000694 effects Effects 0.000 description 4
- 230000002708 enhancing effect Effects 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000005452 bending Methods 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- VNFVKWMKVDOSKT-LREBCSMRSA-N (2r,3r)-2,3-dihydroxybutanedioic acid;piperazine Chemical compound C1CNCCN1.OC(=O)[C@H](O)[C@@H](O)C(O)=O VNFVKWMKVDOSKT-LREBCSMRSA-N 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000011888 foil Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000011056 performance test Methods 0.000 description 1
- BULVZWIRKLYCBC-UHFFFAOYSA-N phorate Chemical class CCOP(=S)(OCC)SCSCC BULVZWIRKLYCBC-UHFFFAOYSA-N 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 230000010148 water-pollination Effects 0.000 description 1
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
It includes the air-conditioner outdoor unit that the utility model, which discloses a kind of fin-tube type heat exchanger, air-conditioner outdoor unit and air conditioner, the air conditioner,.The air-conditioner outdoor unit includes fin-tube type heat exchanger.The fin-tube type heat exchanger includes multiple fins and the more refrigerant pipes through multiple fins, in which: the caliber D of the refrigerant pipe meets 2.5mm≤D≤4mm;Tube spacing P in the short transverse of the fin-tube type heat exchanger, between two adjacent refrigerant pipestMeet 10mm≤Pt≤13mm;The width P of the finrMeet 9mm≤Pr≤13.9mm.The fin-tube type heat exchanger of the utility model can be improved the heat exchange efficiency of fin-tube type heat exchanger.
Description
Technical field
The utility model relates to technical field of heat exchangers, in particular to a kind of fin-tube type heat exchanger, air-conditioner outdoor unit and sky
Adjust device.
Background technique
The caliber of the refrigerant pipe of usual heat exchanger is larger (usually 7mm or more), heat exchange effect of the refrigerant inside refrigerant pipe
Rate is lower, causes the heat transfer effect of heat exchanger poor.Research finds the caliber of reduction refrigerant pipe, can improve the heat exchange of heat exchanger
Effect.But if directly using heat exchanger instead caliber lesser refrigerant pipe, it is easy more in the fin surface condensation of heat exchanger
Frost and block fin, and then the heat exchange efficiency of heat exchanger is caused to decline.
Utility model content
The main purpose of the utility model is to propose a kind of fin-tube type heat exchanger, it is intended to improve the heat exchange of fin-tube type heat exchanger
Efficiency.
To achieve the above object, the utility model proposes a kind of fin-tube type heat exchanger, the fin-tube type heat exchanger includes more
A fin and more refrigerant pipes through multiple fins, in which: the caliber D of the refrigerant pipe meets 2.5mm≤D≤4mm;
Tube spacing P in the short transverse of the fin-tube type heat exchanger, between two adjacent refrigerant pipestMeet 10mm≤Pt
≤13mm;The width P of the finrMeet 9mm≤Pr≤13.9mm。
In one embodiment, the tube spacing PtMeet 10.4mm≤Pt≤ 12.6mm, the width P of the finrMeet
10mm≤Pr≤12mm。
In one embodiment, the fin is bridge chip-type fin, and the surface of the bridge chip-type fin is provided with multiple along it
The bridge piece unit of length direction arrangement.
In one embodiment, the bridge piece unit includes that multiple width directions along the bridge chip-type fin are intervally arranged
Bridge piece, the quantity of the bridge piece are 2~6.
In one embodiment, the quantity of the bridge piece is 3~5.
In one embodiment, the fin is corrugated fin or fenestration fin.
In one embodiment, the surface of the fin is provided with hydrophilic layer.
In one embodiment, the refrigerant pipe is inner screw thread copper pipe or smooth copper.
The utility model also provides a kind of air-conditioner outdoor unit and air conditioner, and the air conditioner includes air conditioner indoor unit and described
Air-conditioner outdoor unit, the air-conditioner outdoor unit and the air conditioner indoor unit are connected by refrigerant pipe.The air-conditioner outdoor unit includes shell
Body and fin-tube type heat exchanger, the fin-tube type heat exchanger are mounted in shell.The fin-tube type heat exchanger include multiple fins and
Through more refrigerant pipes of multiple fins, in which: the caliber D of the refrigerant pipe meets 2.5mm≤D≤4mm;In the pipe
Tube spacing P in the short transverse of fin heat exchanger, between two adjacent refrigerant pipestMeet 10mm≤Pt≤13mm;Institute
State the width P of finrMeet 9mm≤Pr≤13.9mm。
The technical solution of the utility model, by designing the caliber D of the refrigerant pipe of fin-tube type heat exchanger in 2.5mm≤D
≤ 4mm range, while requiring the tube spacing PtMeet 10mm≤Pt≤ 13mm, the width P of the finrMeet 9mm≤Pr≤
13.9mm makes the fin-tube type heat exchanger when using small diameter tube refrigerant pipe, by rationally controlling tube spacing P with thistAnd choosing
With arrow gauge (the lesser fin of width), to improve the synthesis heat exchange property of the fin-tube type heat exchanger, preferable heat exchange is made it have
Efficiency.Further, since the refrigerant pipe caliber of the fin-tube type heat exchanger and the width of fin are smaller, to can not only reduce into
This, can also reduce the overall volume of the fin-tube type heat exchanger, reduce occupied space, and then may make that air-conditioner outdoor unit is small-sized
Change.
Detailed description of the invention
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Or attached drawing needed to be used in the description of the prior art is briefly described, it should be apparent that, the accompanying drawings in the following description is only
It is some embodiments of the utility model, for those of ordinary skill in the art, in the premise not made the creative labor
Under, the structure that can also be shown according to these attached drawings obtains other attached drawings.
Fig. 1 is the top view of one embodiment of the utility model fin-tube type heat exchanger;
Fig. 2 is the partial structural diagram of the fin of single fin-tube type heat exchanger;
Fig. 3 is the partial structural diagram of the fin of double fin-tube type heat exchanger;
Fig. 4 is the curve graph of the synthesis heat exchange property A of the utility model fin-tube type heat exchanger;
Fig. 5 is the curve graph of the synthesis heat exchange property B of the utility model fin-tube type heat exchanger;
Fig. 6 be the utility model fin-tube type heat exchanger use different fins when refrigeration performance change rate column diagram;
Fig. 7 is bridge piece unit jackshaft piece quantity on the fin of the utility model fin-tube type heat exchanger to comprehensive heat exchange property shadow
Loud curve graph.
Drawing reference numeral explanation:
Label | Title | Label | Title |
100 | Fin-tube type heat exchanger | 20 | Refrigerant pipe |
10 | Fin |
The utility model aim is realized, the embodiments will be further described with reference to the accompanying drawings for functional characteristics and advantage.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describing, it is clear that described embodiment is only a part of the embodiment of the utility model, rather than all
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are not making creative work premise
Under every other embodiment obtained, fall within the protection scope of the utility model.
It is to be appreciated that if related in the utility model embodiment directionality instruction (such as upper and lower, left and right, it is preceding,
Afterwards ...), then directionality instruction is only used for explaining opposite between each component under a certain particular pose (as shown in the picture)
Positional relationship, motion conditions etc., if the particular pose changes, directionality instruction is also correspondingly changed correspondingly.
In addition, if relating to the description of " first ", " second " etc. in the utility model embodiment, " first ", " the
Two " etc. description is used for description purposes only, and is not understood to indicate or imply its relative importance or is implicitly indicated meaning
The quantity of the technical characteristic shown." first " is defined as a result, the feature of " second " can explicitly or implicitly include at least one
A this feature.It in addition, the technical solution between each embodiment can be combined with each other, but must be with ordinary skill
Based on personnel can be realized, this technical side will be understood that when the combination of technical solution appearance is conflicting or cannot achieve
The combination of case is not present, also not within the protection scope of the requires of the utility model.
The utility model discloses a kind of fin-tube type heat exchanger 100 and air-conditioner outdoor unit.The air-conditioner outdoor unit includes described
Fin-tube type heat exchanger 100.The air-conditioner outdoor unit includes shell, is mounted on the intracorporal wind wheel component of the shell and fin-tube type
Heat exchanger 100.Such as, but not limited to, the wind wheel component includes axial-flow windwheel.The fin-tube type heat exchanger 100 can be directly
The in line fin-tube type heat exchanger of row pattern setting is also possible to the bending fin-tube type heat exchanger of substantially L-shaped bending setting.
Fig. 1 and Fig. 2 are please referred to, the fin-tube type heat exchanger 100 of the utility model including multiple fins 10 and runs through multiple institutes
State more refrigerant pipes 20 of fin 10.Usual heat exchanger generallys use the refrigerant pipe that caliber is 7mm or more, but this with big
The usual heat exchanger of caliber refrigerant pipe, heat exchange efficiency are not satisfactory.And in the present invention, in order to improve tube fin type heat exchange
The heat exchange efficiency of its refrigerant pipe 20 of device 100 studies the refrigerant pipe 20 of the fin-tube type heat exchanger 100.
It has been investigated that when the caliber D of the refrigerant pipe 20 meets for 2.5mm≤D≤4mm, the heat exchange effect of refrigerant pipe 20
Rate is effectively improved.Such as, but not limited to: D=2.5mm, 2.8mm, 3.0mm, 3.4mm, 3.8mm, 4.0mm.And by institute
The caliber for stating refrigerant pipe 20 reduces, and the width equidimension of the fin 10 of the fin-tube type heat exchanger 100 is also required to accordingly reduce.But it is aobvious
So, the width of fin 10 is also impossible to infinitely reduce, and otherwise cannot ensure the synthesis heat exchange property of fin-tube type heat exchanger 100.
For this purpose, meet within the scope of 2.5mm~4mm in the caliber D of refrigerant pipe (such as 2.5mm, 3.0mm, 3.5mm,
4.0mm), P is controlledrIn the case where certain, the spacing of fin P is testedtTo the synthesis heat exchange property A's of the fin-tube type heat exchanger
It influences, obtains test data such as following table 1-1:
The tables of data of the synthesis heat exchange property A of the table 1-1. fin-tube type heat exchanger
Experimental group | Pr(mm) | Pt(mm) | A (%) |
Experiment 1 | 11 | 9.5 | 5.045 |
Experiment 2 | 11 | 10.0 | 5.385 |
Experiment 3 | 11 | 10.6 | 5.693 |
Experiment 4 | 11 | 11.7 | 5.945 |
Experiment 5 | 11 | 12.5 | 5.906 |
Experiment 6 | 11 | 13.2 | 5.756 |
Experiment 7 | 11 | 13.8 | 5.558 |
By seven groups of data in table 1-1, the spacing P of adjacent refrigerant pipe 12 has been fittedtWith the fin-tube type heat exchanger
The relation curve (referring to Fig. 4) of comprehensive heat exchange property A:
A=0.0015Pt4-0.061Pt3+0.7654Pt2- 2.4054Pt-1.0985, R2=0.9989.
As shown in figure 3, within the scope of caliber range 2.5mm~4mm of refrigerant pipe 20, the fin-tube type heat exchanger 100
Synthesis heat exchange property A with adjacent refrigerant pipe 12 tube spacing PtIncrease, first increase and then arrive reach to peak value (P at this timet≈
11.7mm), it is being gradually reduced.
Further, in caliber range 2.5mm~4mm of refrigerant pipe 12, the tube spacing P is testedtWith the fin
Width PrRatio, the influence with the comprehensive heat exchange property B of the fin-tube type, data measured such as following table 1-2:
The tables of data of the synthesis heat exchange property B of the table 1-2. fin-tube type heat exchanger
Experimental group | Pr(mm) | Pt(mm) | k(Pt/Pr) | B (%) |
Experiment 1 | 8.2 | 11.5 | 1.402 | 2.093 |
Experiment 2 | 8.9 | 11.5 | 1.292 | 2.998 |
Experiment 3 | 10.5 | 11.5 | 1.095 | 4.857 |
Experiment 4 | 11.4 | 11.5 | 1.009 | 5.058 |
Experiment 5 | 12.2 | 11.5 | 0.943 | 4.805 |
Experiment 6 | 13.2 | 11.5 | 0.871 | 4.084 |
Experiment 7 | 14.0 | 11.5 | 0.821 | 3.316 |
Experiment 8 | 14.7 | 11.5 | 0.782 | 2.571 |
By 8 groups of data in table 1-2, the tube spacing P has been fittedtWith the width P of the finrRatio k, with
The relation curve (referring to Fig. 5) of the synthesis heat exchange property B of the fin-tube type heat exchanger:
B=65.404k4-239.48k 3+283.86k 2- 109.11k+4.3699, R2=0.9988.
In conjunction with Fig. 4 and Fig. 5 analysis it is found that for the fin-tube type heat exchanger 100, in the situation that other parameters determine
Under, the spacing of fin PtWith the width P of the finrBoth this should be kept in a certain range, just can ensure that the fin-tube type changes
Device has preferably comprehensive heat exchange property.
Please refer to Fig. 4 and Fig. 5, in the present embodiment, Amax≈ 5.93, Bmax≈5.06.(0.93A can be chosenmax) to Amax
(Bmax- 1) to BmaxFor the more excellent section of performance, to can determine that the tube spacing PtIt can be chosen for Pt∈ [10mm, 13mm],
PrIt can be chosen for Pr∈ [9mm, 13.9mm].At this point, having while the fin-tube type heat exchanger 100 has preferably appearance frost volume
Preferable heat exchange amount.Such as, but not limited to: Pt=10mm, 11.5mm, 12mm, 12.5mm, 13mm;Pr=9mm, 10.5mm,
11mm、12.5mm、13mm、13.5mm、13.9mm。
In another embodiment, (0.95A is chosenmax) to Amax(0.95Bmax) to BmaxFor the more excellent section of performance, then may be used
Determine the tube spacing PtWith the width P of the finrIt needs to meet: Pt∈ [10.4mm, 12.6mm], Pr∈ [10mm,
12mm]。
The technical solution of the utility model, by the way that the caliber D design of the refrigerant pipe 20 of fin-tube type heat exchanger 100 exists
2.5mm≤D≤4mm range, while requiring the tube spacing PtMeet 10mm≤Pt≤ 13mm, the width P of the fin 10rSymbol
Close 9mm≤Pr≤ 13.9mm makes the fin-tube type heat exchanger 100 when using small diameter tube refrigerant pipe 20, by reasonable with this
Control tube spacing PtWith select arrow gauge (the lesser fin of width), to improve the synthesis heat exchange property of the fin-tube type heat exchanger 100,
Make it have preferable heat exchange efficiency.Further, since the width of refrigerant pipe 20 caliber and fin 10 of the fin-tube type heat exchanger 100
Degree is smaller, to not only can reduce cost, can also reduce the overall volume of the fin-tube type heat exchanger 100, reduce and occupy
Space, and then air-conditioner outdoor unit may make to minimize.
Based on the above embodiment, for the slot opening form of the fin 10 then there are many, such as: the fin 10 is chosen as
Corrugated fin perhaps bridge chip-type fin or louvered fin.But for the width P of the fin 10rMeet 9mm
≤PrFor≤13.9mm, which belongs to arrow gauge.The slot opening form of arrow gauge has the fin-tube type heat exchanger 100 different
It influences.Here, being carried out to study influence of the type of arrow gauge to the synthesis heat exchange property of the fin-tube type heat exchanger 100
Following experiment, it is as follows that experiment obtains performance test data:
The synthesis heat exchange property enhancing rate of 2. different type arrow gauge of table
Fin type | Compared to the enhancing rate of sheet type fin |
Sheet type fin | 0 |
Corrugated fin | 2.5 |
Bridge chip-type fin | 3.6 |
Louvered fin | 3.2 |
It is drawn to obtain the cylindricality of the synthesis heat exchange property enhancing rate of the arrow gauge of different slot opening forms according to the data of above-mentioned table 2
Scheme (such as Fig. 6).Referring to Fig. 6, being compared by the experimental result as it can be seen that the fin of the fin-tube type heat exchanger 100 is using bridge piece formula
When fin, synthesis heat exchange property is opposite to be able to ascend 3.6%, is higher than other types fin.Therefore, in the present embodiment, institute
The fin 10 for stating fin-tube type heat exchanger 100 is chosen as bridge chip-type fin.
Based on the above embodiment, the fin of the fin-tube type heat exchanger 100 is bridge chip-type fin.The bridge chip-type fin
Surface is provided with multiple bridge piece units (not shown) arranged along its length.The bridge piece unit includes multiple along the bridge
The bridge piece that the width direction of chip-type fin is intervally arranged.As for the quantity of the bridge piece, limited there is no specific.For example, described
The quantity of bridge piece is chosen as 2~6.But, it is contemplated that the quantity of bridge piece exchanges heat to the comprehensive of the fin-tube type heat exchanger 100
Performance also has an impact.Therefore, experimental study has also been carried out to the quantity of bridge piece, has measured that the experimental data are shown in the following table 3:
The synthesis heat exchange property change rate of the different bridge piece quantity of table 3.
Ripple quantity | Comprehensive heat exchange property change rate |
2 | 2.4% |
3 | 3.8% |
4 | 4.8% |
5 | 3.8% |
6 | 2.6% |
The change curve (such as Fig. 7) that fitting obtains comprehensive heat exchange property change rate is drawn according to above-mentioned table 3.
As seen from Figure 7, the change rate of the synthesis heat exchange property of the fin-tube type heat exchanger 100, on the fin 10
The increase of bridge piece quantity first gradually rises, and then arrives reach to peak value (bridge piece quantity is about 4 at this time), then gradually decrease.Thus
As it can be seen that it is not The more the better for being formed by bridge piece quantity on the fin 10, but need to be maintained at a preferable range
It is interior.Theoretically, the bridge piece quantity of the fin 10 is chosen as 2~6, such as 2,3,4,5,6.
Referring to Fig. 5, in the present embodiment, theoretically, the bridge piece quantity of the fin 10 is chosen as 2~6, such as
2,3,4,5,6.But being 2 or 6 in view of bridge piece quantity is that its heat exchange property change rate is lower.Therefore,
In a further preferred embodiment, choosing comprehensive heat exchange property change rate is 3.8%~4.8% for more excellent section, and correspondence can determine
The bridge piece quantity optimized scope of the fin 10 is 3~5 out, such as, but not limited to 3,4,5.Optimal bridge piece number
Amount is chosen as 4.
Based on above-mentioned any one embodiment, it is contemplated that when between the two adjacent fins 10 of the fin-tube type heat exchanger 100
Spacing is smaller, the droplet when the height of condensation droplet is more than to cool down the spacing between two adjacent fins 10, between fin 10
It will connect, form firm " water bridge ".Obviously, " water bridge " meeting occupied space, increases windage, is unfavorable for air stream and moves
Heat.Therefore, it is the generation of reduction " water bridge ", optionally, hydrophilic layer is set on the surface of the fin 10.The hydrophilic layer can be with
It is hydrophilic aluminum foil coating.The hydrophilic layer has stronger affinity to water, the hydrophily of fin 10 is improved, so that condensed water exists
It is spread on fin 10 very fast, it is not easy to be formed " water bridge ", and then reduce windage, be convenient for air fluid interchange.
In the present embodiment, the refrigerant pipe 20 is chosen as inner screw thread copper pipe or smooth copper.Wherein, the refrigerant
When pipe 20 is inner screw thread copper pipe, wherein internal screw thread is conducive to enhancing heat exchange, so can help to improve heat exchange efficiency.Therefore, institute
Stating refrigerant pipe 20 is preferably inner screw thread copper pipe
The utility model also provides a kind of air conditioner, and the air conditioner includes air conditioner indoor unit and air-conditioner outdoor unit, described
Air-conditioner outdoor unit is connected with the air conditioner indoor unit by refrigerant pipe.The specific structure of the air-conditioner outdoor unit is referring to above-mentioned implementation
Example, since this air conditioner uses whole technical solutions of above-mentioned all embodiments, the same skill with above-described embodiment
All beneficial effects brought by art scheme, this is no longer going to repeat them.
The above is only the preferred embodiment of the present invention, and therefore it does not limit the scope of the patent of the utility model,
It is all under the inventive concept of the utility model, equivalent structure made based on the specification and figures of the utility model becomes
It changes, or directly/be used in other related technical areas indirectly and be included in the scope of patent protection of the utility model.
Claims (10)
1. a kind of fin-tube type heat exchanger, which is characterized in that the fin-tube type heat exchanger includes multiple fins and runs through multiple described
More refrigerant pipes of fin, in which:
The caliber D of the refrigerant pipe meets 2.5mm≤D≤4mm;
Tube spacing P in the short transverse of the fin-tube type heat exchanger, between two adjacent refrigerant pipestMeet 10mm
≤Pt≤13mm;
The width P of the finrMeet 9mm≤Pr≤13.9mm。
2. fin-tube type heat exchanger as described in claim 1, which is characterized in that the tube spacing PtMeet 10.4mm≤Pt≤
12.6mm, the width P of the finrMeet 10mm≤Pr≤12mm。
3. fin-tube type heat exchanger as described in claim 1, which is characterized in that the fin is bridge chip-type fin, the bridge piece
The surface of formula fin is provided with multiple bridge piece units arranged along its length.
4. fin-tube type heat exchanger as claimed in claim 3, which is characterized in that the bridge piece unit includes multiple along the bridge piece
The bridge piece that the width direction of formula fin is intervally arranged, the quantity of the bridge piece are 2~6.
5. fin-tube type heat exchanger as claimed in claim 4, which is characterized in that the quantity of the bridge piece is 3~5.
6. fin-tube type heat exchanger as described in claim 1, which is characterized in that the fin is corrugated fin or windowing
Formula fin.
7. the fin-tube type heat exchanger as described in claim 1 to 6 any one, which is characterized in that the surface of the fin is arranged
There is hydrophilic layer.
8. the fin-tube type heat exchanger as described in claim 1 to 6 any one, which is characterized in that the refrigerant pipe is internal screw thread
Copper pipe or smooth copper.
9. a kind of air-conditioner outdoor unit, which is characterized in that the air-conditioner outdoor unit includes shell, and as claim 1 to 8 is any
Fin-tube type heat exchanger described in one, the fin-tube type heat exchanger are mounted in the shell.
10. a kind of air conditioner, which is characterized in that the air conditioner includes air conditioner indoor unit, and as claimed in claim 9 empty
Outdoor unit is adjusted, the air-conditioner outdoor unit is connect with the air conditioner indoor unit by refrigerant pipe.
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Cited By (1)
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CN112762520A (en) * | 2021-01-15 | 2021-05-07 | 青岛海信日立空调系统有限公司 | Indoor unit of air conditioner |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN112762520A (en) * | 2021-01-15 | 2021-05-07 | 青岛海信日立空调系统有限公司 | Indoor unit of air conditioner |
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