CN203163348U - Heat exchanger and air conditioning device - Google Patents

Heat exchanger and air conditioning device Download PDF

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Publication number
CN203163348U
CN203163348U CN 201320150404 CN201320150404U CN203163348U CN 203163348 U CN203163348 U CN 203163348U CN 201320150404 CN201320150404 CN 201320150404 CN 201320150404 U CN201320150404 U CN 201320150404U CN 203163348 U CN203163348 U CN 203163348U
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CN
China
Prior art keywords
header
heat exchanger
demarcation strip
tube
reversing tube
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Withdrawn - After Issue
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CN 201320150404
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Chinese (zh)
Inventor
佐藤宪一郎
程志明
徐龙贵
孙西辉
华龙
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Midea Group Co Ltd
GD Midea Air Conditioning Equipment Co Ltd
Original Assignee
Guangdong Midea Refrigeration Equipment Co Ltd
Guangdong Midea Electric Appliances Co Ltd
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Priority to CN 201320150404 priority Critical patent/CN203163348U/en
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Publication of CN203163348U publication Critical patent/CN203163348U/en
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Abstract

The utility model provides a heat exchanger and an air conditioning device. The heat exchanger can be used as a condenser or an evaporator. Separating plates are arranged in a flow collecting pipe to form a plurality of distribution cavities in the flow collecting pipe. The distribution cavities are matched with a plurality of inlet pipes and outlet pipes, so that coolants are distributed, when a hot house is used, the coolants in the distribution cavities form vortexes which are sprayed upwards from spraying holes in the upper faces of the distribution cavities to form spraying flows, the coolants are micronized and evenly enter a flat pipe to form annular flows of good heat transfer effects, heat exchanging among portions are evenly carried out, and performance of the heat exchanger is improved. When a cooling room is used, gas coolants release heat to the outside continuously through a pipeline to form condensed liquid or gas-liquid two-phase liquid. The condensed liquid or the gas-liquid two-phase liquid enters the distribution cavities from spraying holes in the lower portions of the distribution cavities inside a first flow collecting pipe, and are discharged from the outlet pipes integrally. In addition, the diameters of coolant particles become smaller, so that impact of the coolant particles on the inner wall of pipes and collisions between particles are restrained, and therefore noises of flowing of the coolants can be reduced.

Description

Heat exchanger and conditioner
Technical field
The utility model belongs to the air-conditioning production technical field, more particularly, relates to a kind of heat exchanger and conditioner.
Background technology
Existing parallel-flow heat exchanger for guaranteeing drainage, has the flat tube horizontal direction to extend, the method that the header vertical direction arranges.This mode is during at first as evaporimeter, below just becomes the necessary functional conditions of coolant distribution, that is: (1) makes a plurality of flat tubes that are assigned to of refrigerant equalization in the header; (2) each space is owing to gravitate in the header, and liquid refrigerants is difficult to be detained.But traditional heat exchanger also can't be had (1), (2) two functional conditions simultaneously.The scheme that satisfies (1) can be referring to document-1: Japan Patent JP1996-00957; Document-2: Japan Patent JP2012-002475; The scheme that satisfies (2) can be referring to document-3: Japan Patent JP2001-304720.
On the other hand as the necessary functional conditions of condenser: generate the liquid refrigerants of stablizing liquid level near the outlet of (3) outlet side header; (4) refrigerant that is mixed with machine oil can flow to the outside of refrigerator oil heat exchanger smoothly.About (3), (4) these two functional conditions, the technical scheme that possesses respectively exists, and sees also document-3: Japan Patent JP2001-304720; Document-4: Japan Patent JP2012-163313; Document-5:WO2012098917A1.But both as evaporimeter, during again as condenser, the scheme that satisfies (1)~(a 4) functional conditions does not simultaneously also have.
The utility model content
The purpose of this utility model is to provide a kind of heat exchanger, when being intended to make it not only as evaporimeter but also as condenser, can satisfy (1)~(4) functional conditions in the above-mentioned background technology simultaneously.
For solving the problems of the technologies described above, the technical solution adopted in the utility model is: a kind of heat exchanger is provided, comprise first header, second header, a plurality of flat tube, a plurality of fin and at least two inlet tubes and at least two outlets, described first header and described second header are erect setting at interval, described a plurality of flat tube horizontal parallel arranges, and an end of each described flat tube is communicated with described first header, the other end is communicated with described second header, and described a plurality of fins are the heat conduction with described a plurality of flat tubes and are connected;
Be provided with at least two first demarcation strip and second demarcation strips of forming arranging in described first header, be provided with at least one the 3rd demarcation strip in described second header, described second demarcation strip is provided with spray-hole, described second demarcation strip is positioned at the top of described first demarcation strip, and both and described first header surround and form a dispensed chambers, the top of each described second partition is formed with an ejection chamber respectively, described the 3rd demarcation strip is separated at least two compartments with described second header, each described inlet tube is communicated with a described dispensed chambers respectively, and each described outlet is communicated with a described compartment respectively.
Particularly, described first header, the second header side direction offer the dividing plate installation position, and each described first demarcation strip, second demarcation strip, the 3rd demarcation strip are located at respectively in the described dividing plate installation position.
Particularly, described fin is wavy texture, and each described fin is located between the two adjacent described flat tubes.
Perhaps, particularly, described fin is platy structure, and each described fin is provided with a plurality of be used to first notch part that installs described flat tube, and described flat tube is installed in described first notch part.
Particularly, the opposition side that connects a side of described flat tube on described first header is provided with at least two and is connected entrance with described dispensed chambers communicates, and each described inlet tube is inserted in respectively in each described connection entrance.
Especially, the described flat tube that one end is connected with described dispensed chambers, the upper and lower of the other end that this described flat tube is connected with described second header respectively is provided with one the 3rd demarcation strip, and the body of this two described the 3rd demarcation strip and described second header forms the parting seal chamber.
Perhaps, more specifically, this heat exchanger also comprises the reversing tube that equates with the quantity of described dispensed chambers, connecting described flat tube one side on described first header is provided with respectively with described dispensed chambers communicates and is connected entrance, one end of each described reversing tube is inserted in respectively in each described connection entrance, and the other end and described second header are fixed.
More specifically, each described fin is provided with second notch part for the described reversing tube of fixed installation, and each described reversing tube is fixedlyed connected with described second header.
More specifically, fixed form one as described reversing tube and described second header, described the 3rd demarcation strip arranges in described second header in pairs, body on described second header between every pair of described the 3rd demarcation strip is provided with two relative being used in position, and described reversing tube passes and fixing through hole, and described reversing tube is arranged in the described through hole.
Perhaps, more specifically, fixed form two as described reversing tube and described second header, described the 3rd demarcation strip arranges in described second header in pairs, body side direction on described second header between every pair of described the 3rd demarcation strip offers the groove position for fixing described reversing tube, and described reversing tube is fixed in the described groove position.
Perhaps, more specifically, as the fixed form three of described reversing tube and described second header, each described reversing tube is fixedly installed in the body outside of described second header by fixture.
Preferably, as the connected mode of reversing tube and dispensed chambers, each described reversing tube is connected with the inner cylindrical sidewall of each described dispensed chambers is tangent respectively.
Particularly, as a kind of decision design of reversing tube, the madial wall of described reversing tube is a plurality of groove surfaces formations along the length direction of described reversing tube.
Further optimally, the outer surface of described reversing tube is provided with the integrated fin of outwards digging for increasing heat transfer area.
The heat exchanger that the utility model provides had not only moved as evaporimeter but also as condenser; when greenhouse turns round; the utility model heat exchanger sprays upward at the spray-hole of whirlpool above dispensed chambers that dispensed chambers forms; form injection stream; enter flat tube equably, because the refrigerant of whirlpool injection stream is micronized refrigerant, in the microchannel of flat tube, be easy to form heat transfer effect annular flow preferably; make the impartial heat exchange of each several part of heat exchanger, further improved the performance of heat exchanger.In addition, the refrigerant particle diameter diminishes, and has suppressed the impact of refrigerant particle to inside pipe wall, and the collision between the particle, can reduce the noise that refrigerant flows with this.On the other hand, when cold-room turns round, gas coolant is along with passing through pipeline constantly to outside heat release, form condensed fluid or gas-liquid two-phase flow, the spray-hole of the bottom of the ejection chamber in first header enters into dispensed chambers, concentrates and discharges from inlet tube, at this moment, the liquid refrigerants of condensation and refrigerator oil are assembled in the first header bottom, but are not detained, but flow to dirty decompressor.
Another purpose of the present utility model is to provide a kind of conditioner, this conditioner comprises the coolant circulating system that is connected to form by pipeline by compressor, cross valve, off-premises station and indoor set, and described indoor set and described off-premises station adopt above-mentioned heat exchanger.
The beneficial effect of the conditioner that the utility model provides is: owing to adopted above-mentioned heat exchanger, the utility model conditioner heat exchange equalization, efficient height.
Description of drawings
The right view of the heat exchanger that Fig. 1 provides for the utility model embodiment one;
The fin that Fig. 2 provides for the utility model embodiment one is the perspective view one of wavy heat exchanger;
Fig. 3 be along A-A among Fig. 1 to sectional structure chart;
The fin that Fig. 4 provides for the utility model embodiment one is the perspective view of tabular heat exchanger;
The heat exchanger that Fig. 5 provides for the utility model embodiment one during as evaporimeter in first header refrigerant flow to schematic diagram;
The fin that Fig. 6 provides for the utility model embodiment one is the perspective view two of wavy heat exchanger;
Fig. 7 is the blast structural representation of Fig. 6;
The right view of the heat exchanger that Fig. 8 provides for the utility model embodiment two;
The fin that Fig. 9 provides for the utility model embodiment two is the front view of wavy heat exchanger;
Figure 10 be along B-B among Fig. 8 to sectional structure chart (wherein, fin is wavy);
The fin that Figure 11 provides for the utility model embodiment two is the stereogram of wavy heat exchanger;
Figure 12 is the blast structural representation (wherein, fin is wavy) of Figure 11;
The fin that Figure 13 provides for the utility model embodiment two is the front view of tabular heat exchanger;
Figure 14 be along B-B among Fig. 8 to cross-sectional view (wherein, fin is tabular);
The right view of the heat exchanger that Figure 15 provides for the utility model embodiment three;
The fin that Figure 16 provides for the utility model embodiment three is the front view of tabular heat exchanger;
The left view of the heat exchanger that Figure 17 provides for the utility model embodiment three;
Figure 18 be along C-C among Figure 15 to cross-sectional view (wherein, fin is tabular);
The three-dimensional structure diagram (wherein, fin is tabular, unassembled inlet tube) of the heat exchanger that Figure 19 provides for the utility model embodiment three;
The three-dimensional structure diagram (wherein, fin is tabular, has assembled inlet tube) of the heat exchanger that Figure 20 provides for the utility model embodiment three;
Figure 21 is the main TV structure figure of Figure 20;
Figure 22 is the blast structure chart one of heat exchanger shown in Figure 20;
The plate-shaped fins that Figure 23 adopts for the utility model embodiment three and the structure chart of reversing tube;
Figure 24 is the blast structure chart two of heat exchanger shown in Figure 20;
Figure 25 is the assembly structure generalized section between reversing tube and second header among Figure 20;
Figure 26 is second kind of assembly structure schematic diagram between reversing tube and second header among the utility model embodiment three;
Figure 27 is the assembly structure generalized section between reversing tube and second header among Figure 26;
Figure 28 is the third assembly structure schematic diagram between reversing tube and second header among the utility model embodiment three;
Figure 29 is the assembly structure generalized section between reversing tube and second header among Figure 28;
The structural representation of the reversing tube of the employing of the heat exchanger that Figure 30 provides for the utility model embodiment four;
The front view of heat exchanger after the outer surface of reversing tube is provided with integrated fin that Figure 31 provides for the utility model embodiment three;
The operation logic figure of the refrigerant of the heat exchanger that Figure 32 the utility model embodiment three provides as condenser or evaporimeter the time;
The theory structure schematic diagram of the conditioner that Figure 33 provides for the utility model embodiment.
The specific embodiment
In order to make technical problem to be solved in the utility model, technical scheme and beneficial effect clearer, below in conjunction with drawings and Examples, the heat exchanger that the utility model is provided is further elaborated.Should be appreciated that specific embodiment described herein only in order to explaining the utility model, and be not used in restriction the utility model.
See also Fig. 1 to Figure 14, one embodiment of the heat exchanger that provides as the utility model, this heat exchanger comprises first header 11, second header 12, a plurality of flat tubes 2, a plurality of fins and at least two inlet tubes 41 and at least two outlets 42, first header 11 and second header 12 are erect and are arranged, has certain interval between the two, a plurality of flat tube 2 horizontal parallel settings, and an end of each flat tube 2 is communicated with first header 11, the other end is communicated with second header 12, a plurality of fins are the heat conduction with a plurality of flat tubes 2 and are connected, above-mentioned each parts are aluminium alloy and make, and can assemble connection by modes such as solderings each other; Be provided with at least two first demarcation strip 51 and second demarcation strips of forming arranging 52 in first header 11, be provided with at least one the 3rd demarcation strip 53 in second header 12, second demarcation strip 52 is provided with spray-hole 520, second demarcation strip 52 is positioned at the top of first demarcation strip 51, and both and first header 11 surround and form a dispensed chambers 111, the top of each second partition is formed with an ejection chamber 112 respectively, the 3rd demarcation strip 53 is separated at least two compartments 121 with second header 12, each inlet tube 41 is communicated with a dispensed chambers 111 respectively, and each outlet 42 is communicated with a compartment 121 respectively.
In the present embodiment, inlet tube 41 and outlet 41 all are made as three, and be by the refrigerant of three shuntings, consistent with the quantity of the ejection chamber 112 of being cut apart formation by dividing plate, inlet tube 41, outlet 42; Yet as long as shunting is more than two and two.
See also Figure 32, the heat exchanger that the utility model provides, when greenhouse turns round, the utility model heat exchanger sprays upward at the spray-hole 520 of whirlpool above dispensed chambers 111 that dispensed chambers 111 forms, and forms injection stream, enters flat tube 2 equably, along with it flows to second header 12, the heat that absorbs extraneous air owing to fin makes its evaporation, forms gaseous coolant in second header 12, and is discharged from from outlet 42.Because the refrigerant of whirlpool injection stream is micronized refrigerant, in the microchannel of flat tube 2, be easy to form heat transfer effect annular flow preferably, make the impartial heat exchange of each several part of heat exchanger, further improved the heat exchange property of heat exchanger.Simultaneously, the refrigerant particle diameter diminishes, and has suppressed the refrigerant particle to the impact of inside pipe wall and the collision between the particle, can reduce the noise that refrigerant flows with this.On the other hand, when cold-room turns round, gas coolant is along with passing through pipeline constantly to outside heat release, form condensed fluid or gas-liquid two-phase flow, the spray-hole 520 of the bottom of the ejection chamber 112 in first header 11 enters into dispensed chambers 111, concentrates from inlet tube 41 and discharges, at this moment, the liquid refrigerants of condensation and refrigerator oil are assembled in first header, 11 bottoms, but are not detained, but flow to dirty decompressor.
See also Fig. 7 and Figure 12, specifically, can offer dividing plate installation position 110 in first header, 11 side direction, second header, 12 side direction offer dividing plate installation position 120, each first demarcation strip 51, second demarcation strip 52 are located at respectively in the dividing plate installation position 110, and each the 3rd demarcation strip 53 is located at respectively in the dividing plate installation position 120; Because it is one-body molded that this separation structure is not easy to, adopt the mode of assembling and welding after this moulding respectively can reduce difficulty and cost, be convenient to the manufacturing of heat exchanger.
See also Fig. 2, Fig. 3, Fig. 6, Fig. 7, Fig. 9 to Figure 12, as a kind of embodiment of fin, fin is corrugated fin 31, and each fin is located between the two adjacent flat tubes 2.
Referring to Fig. 4, Figure 13, Figure 14 and Figure 23, as the another kind of embodiment of fin, fin also can be plate-shaped fins 32, and each fin is provided with a plurality of be used to first notch part 321 that installs flat tube 2, flat tube 2 is installed in first notch part 321, can fix by soldering each other.
In order to make topology layout more reasonable, radiating effect is more optimized, and each plate-shaped fins 32 parallels with first header 11 and second header 12, and leaves the gap between adjacent two fins 32, is beneficial to improve exchange heat efficient.
As preferred embodiment, each outlet 42 preferably is connected to the middle position of corresponding with it compartment 121 above-below directions, do not influence flowing of refrigerant so that refrigerant has certain gathering in compartment 121, be convenient to balanced heat exchange, promote heat exchange property.
See also Fig. 7, in above-mentioned each embodiment, if radiator is subjected under the little situation of the restriction of installing space, the opposition side (i.e. the outside of first header 12) that connects a side of flat tube 2 on first header 11 is provided with at least two and is connected entrance 141 with dispensed chambers 111 communicates, each inlet tube 41 is inserted in respectively and respectively connects in the entrance 141, relatively simple for structure, be beneficial to and save material and reduce production process.
Referring to Fig. 2 to Fig. 4, if there is the part flat tube 2 that is communicated with dispensed chambers 111, for not flowed into directly, refrigerant flow in second header 12 by this flat tube 2, can in second header 12, it be shut.If i.e.: the flat tube 2 that has an end to be connected with dispensed chambers 111, the upper and lower of the other end that this flat tube 2 is connected with second header 12 respectively is provided with the 3rd demarcation strip 53, and the body of these two the 3rd demarcation strips 53 and second header 12 forms parting seal chamber 530.And at the upper and lower opening end of first header 11 and second header 12, can it be sealed by end cap 13.
See also Figure 15 to Figure 24, in order to reduce the left and right sides width of entire radiator, reduce the restriction that radiator is subjected to installing space, then this heat exchanger also adopts the reversing tube 43 that equates with the quantity of dispensed chambers 111 will change the direction that arranges of inlet tube 41, a side that connects flat tubes 43 at first header 11 arranges respectively with dispensed chambers 111 communicates and is connected entrance 143, one end of each institute's reversing tube 43 is inserted in respectively and respectively connects in the entrance 143, the other end and second header 12 fix, and each inlet tube 41 just can be communicated with a reversing tube 43 respectively like this.Thus, during the greenhouse running, with refrigerant inlet tube 41 and outlet 42 the same the same sides of second header 12 early that arrange, the space of air regulator pipe arrangement can be dwindled like this, pipe distribution operation can be simplified.In addition, cold-room when running, add the heat exchange field that the flat tube 2 except each path constitutes, each reversing tube 43 has also played the effect of auxiliary heat exchange, the refrigerant that circulation is clipped in the reversing tube 43 between the fin carries out heat release again, can promote supercooling and liquefaction, has improved refrigerating capacity.
Under the situation of above-mentioned employing reversing tube, the fin 32 of each platy structure is provided with second notch part 322 for fixed installation reversing tube 43, and each reversing tube 43 fixedlys connected with second header 12, can select soldering together.
See also Figure 16 to Figure 22, fixed form one as reversing tube 43 and second header 12, the 3rd demarcation strip 53 arranges in second header 12 in pairs, and the body between every pair of the 3rd demarcation strip 53 is provided with the through hole 123 that passes and fix for reversing tube 43 on second header 12, reversing tube 43 is arranged in the through hole 123, in this programme, all welded at the upper and lower sides of reversing tube 43 and to have divided the 3rd dividing plate 53, purpose is in order to prevent that refrigerant from leaking outside from through hole 123.
See also Figure 26 and Figure 27, as fixing a kind of alternate embodiments between reversing tube 43 and second header 12, in order to prevent that refrigerant from leaking outside, the 3rd demarcation strip 53 arranges in second header 12 in pairs, and on second header 12 on the body between every pair of the 3rd demarcation strip 53 side direction offer for the fixing groove position 124 of reversing tube 43, reversing tube 43 is fixed in the groove position 124, can realize fixing by modes such as solderings.
See also Figure 28 and Figure 29, as another kind of alternate embodiments fixing between reversing tube 43 and second header 12, each reversing tube 43 also can be fixedly installed in the body outside of second header 12 by fixture 125, fixture 125 herein can be the metal fixed block that is welded on second header 12, also can be other parts that can play a supporting role.
In the above-mentioned scheme that is provided with reversing tube 43, as the preferred embodiment that be connected of reversing tube with dispensed chambers, each reversing tube 43 is connected with the inner cylindrical sidewall of each dispensed chambers 111 is tangent respectively.That is to say that each reversing tube 43 preferably is connected to the tangential direction of each dispensed chambers 111, enter dispensed chambers 111 back formation vortex shapes in order to form refrigerant, be beneficial to ejection from the spray-hole 520 of top.
See also Figure 30, as a kind of optimization embodiment, the madial wall of reversing tube 43 is a plurality of groove surfaces 430 formations along the length direction of reversing tube 43, the inwall of reversing tube 43 and the heat exchange area of refrigerant have so just been increased, improved the heat exchange amount, and refrigerating capacity, it is particularly remarkable particularly to increase overcooled effect when greenhouse turns round.
See also Figure 31, can also be provided with the integrated fin of outwards digging 431 on the outer surface of reversing tube 43, for increasing heat transfer area, improve heat exchange efficiency; Certainly, integrated fin 431 herein also can be other structure member that can increase heat exchange area.
Referring to Fig. 5, the diameter of the spray-hole 520 on second demarcation strip 52 be second demarcation strip 52 external diameter 1/4th to 1/3rd.In the practice, can adjust best size according to the size of the kind of the kind of refrigerant, air-conditioning, air-conditioning, refrigerant circulation etc.In addition, because micronized degree also can further adjust, adjusting range and being of wide application.Just, can make man-hour that shunting design, ability improve, and new spec mould development number etc. obtain maximum reasonableization.
The utility model also provides a kind of conditioner.See also Figure 32 and Figure 33, conditioner comprises the coolant circulating system that is connected to form by pipeline by compressor 200, cross valve 300, off-premises station 401 and indoor set 402, and indoor set 402 adopts above-mentioned heat exchanger.Indoor set 402, off-premises station 401 are provided with indoor heat exchanger 4020, outdoor heat exchanger 4010 respectively, are connected with gas pipe arrangement 502 with liquid pipe arrangement 501, have formed the refrigerant loop of heat pump.Compressor 200, four-way change-over valve 300, choke valve 600(or decompression capillary are arranged in the refrigerant loop), pressure fan 4021 and pressure fan 4011 and corresponding with indoor heat exchanger 4020, outdoor heat exchanger 4010 respectively are set respectively in indoor set 402, off-premises station 401.
The cold-room running, refrigerant flows along the dotted line direction as the four-way change-over valve 300 among Figure 33, the high temperature and high pressure gas that comes out from compressor 200 liquefies through outdoor heat exchanger 4010, evaporate at indoor heat exchanger 4020 places by choke valve 600 backs again, form overheated cold media gas again and get back to compressor 200, finish a circulation.
On the other hand, during the greenhouse running, refrigerant flows along the solid line direction as the four-way change-over valve 300 among Figure 33, the high temperature and high pressure gas that comes out from compressor 200 liquefies through indoor heat exchanger 4020, evaporate at outdoor heat exchanger 4010 places by choke valve 600 backs again, cold media gas is got back to compressor 200 again, finishes the refrigerant circulation.
The conditioner that the utility model provides is owing to adopted above-mentioned heat exchanger, the utility model conditioner heat exchange equalization, efficient height.
The above only is preferred embodiment of the present utility model; not in order to limit the utility model; all any modifications of within spirit of the present utility model and principle, doing, be equal to and replace and improvement etc., all should be included within the protection domain of the present utility model.

Claims (15)

1. heat exchanger, comprise first header, second header, a plurality of flat tube, a plurality of fin and at least two inlet tubes and at least two outlets, described first header and described second header are erect setting at interval, described a plurality of flat tube horizontal parallel arranges, and an end of each described flat tube is communicated with described first header, the other end is communicated with described second header, and described a plurality of fins are the heat conduction with described a plurality of flat tubes and are connected; It is characterized in that:
Be provided with at least two first demarcation strip and second demarcation strips of forming arranging in described first header, be provided with at least one the 3rd demarcation strip in described second header, described second demarcation strip is provided with spray-hole, described second demarcation strip is positioned at the top of described first demarcation strip, and both and described first header surround and form a dispensed chambers, the top of each described second partition is formed with an ejection chamber respectively, described the 3rd demarcation strip is separated at least two compartments with described second header, each described inlet tube is communicated with a described dispensed chambers respectively, and each described outlet is communicated with a described compartment respectively.
2. heat exchanger as claimed in claim 1, it is characterized in that: described first header, the second header side direction offer the dividing plate installation position, and each described first demarcation strip, second demarcation strip, the 3rd demarcation strip are located at respectively in the described dividing plate installation position.
3. heat exchanger as claimed in claim 2, it is characterized in that: described fin is wavy texture, each described fin is located between the two adjacent described flat tubes.
4. heat exchanger as claimed in claim 2, it is characterized in that: described fin is platy structure, and each described fin is provided with a plurality of be used to first notch part that installs described flat tube, and described flat tube is installed in described first notch part.
5. as each described heat exchanger of claim 1 to 4, it is characterized in that: the opposition side that connects a side of described flat tube on described first header is provided with at least two and is connected entrance with described dispensed chambers communicates, and each described inlet tube is inserted in respectively in each described connection entrance.
6. heat exchanger as claimed in claim 5, it is characterized in that: the described flat tube that an end is connected with described dispensed chambers, the upper and lower of the other end that this described flat tube is connected with described second header respectively is provided with one the 3rd demarcation strip, and the body of this two described the 3rd demarcation strip and described second header forms the parting seal chamber.
7. as each described heat exchanger of claim 1 to 4, it is characterized in that: also comprise the reversing tube that equates with the quantity of described dispensed chambers, connecting described flat tube one side on described first header is provided with respectively with described dispensed chambers communicates and is connected entrance, one end of each described reversing tube is inserted in respectively in each described connection entrance, and the other end and described second header are fixed.
8. heat exchanger as claimed in claim 7 is characterized in that: each described fin is provided with second notch part for the described reversing tube of fixed installation, and each described reversing tube is fixedlyed connected with described second header.
9. heat exchanger as claimed in claim 8, it is characterized in that: described the 3rd demarcation strip arranges in described second header in pairs, body on described second header between every pair of described the 3rd demarcation strip is provided with two relative being used in position, and described reversing tube passes and fixing through hole, and described reversing tube is arranged in the described through hole.
10. heat exchanger as claimed in claim 8, it is characterized in that: described the 3rd demarcation strip arranges in described second header in pairs, body side direction on described second header between every pair of described the 3rd demarcation strip offers the groove position for fixing described reversing tube, and described reversing tube is fixed in the described groove position.
11. heat exchanger as claimed in claim 8 is characterized in that: each described reversing tube is fixedly installed in the body outside of described second header by fixture.
12. heat exchanger as claimed in claim 7 is characterized in that: each described reversing tube is connected with the inner cylindrical sidewall of each described dispensed chambers is tangent respectively.
13. heat exchanger as claimed in claim 7 is characterized in that: the madial wall of described reversing tube is a plurality of groove surfaces formations along the length direction of described reversing tube.
14. heat exchanger as claimed in claim 7 is characterized in that: the outer surface of described reversing tube is provided with the integrated fin of outwards digging for increasing heat transfer area.
15. a conditioner, comprise by compressor, cross valve, off-premises station and indoor set it is characterized in that by the coolant circulating system that pipeline is connected to form: described indoor set and described off-premises station adopt each described heat exchanger of claim 1 to 14.
CN 201320150404 2013-03-28 2013-03-28 Heat exchanger and air conditioning device Withdrawn - After Issue CN203163348U (en)

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Application Number Priority Date Filing Date Title
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103256757A (en) * 2013-03-28 2013-08-21 广东美的电器股份有限公司 Heat exchanger and air conditioner
CN105804853A (en) * 2014-12-30 2016-07-27 泰安鼎鑫冷却器有限公司 Multiunit combined heat radiator
CN111699351A (en) * 2018-03-27 2020-09-22 东芝开利株式会社 Heat exchanger, heat exchange module, and refrigeration cycle device

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103256757A (en) * 2013-03-28 2013-08-21 广东美的电器股份有限公司 Heat exchanger and air conditioner
CN103256757B (en) * 2013-03-28 2015-07-15 广东美的制冷设备有限公司 Heat exchanger and air conditioner
CN105804853A (en) * 2014-12-30 2016-07-27 泰安鼎鑫冷却器有限公司 Multiunit combined heat radiator
CN111699351A (en) * 2018-03-27 2020-09-22 东芝开利株式会社 Heat exchanger, heat exchange module, and refrigeration cycle device

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