CN109996994A - Air conditioner - Google Patents

Air conditioner Download PDF

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Publication number
CN109996994A
CN109996994A CN201780071215.4A CN201780071215A CN109996994A CN 109996994 A CN109996994 A CN 109996994A CN 201780071215 A CN201780071215 A CN 201780071215A CN 109996994 A CN109996994 A CN 109996994A
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CN
China
Prior art keywords
heat exchanger
protrusion
plate fin
ora terminalis
air conditioner
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.)
Granted
Application number
CN201780071215.4A
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Chinese (zh)
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CN109996994B (en
Inventor
丸本一彦
名越健二
山本宪昭
大城崇裕
奥村拓也
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Panasonic Intellectual Property Management Co Ltd
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Panasonic Intellectual Property Management Co Ltd
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Publication of CN109996994A publication Critical patent/CN109996994A/en
Application granted granted Critical
Publication of CN109996994B publication Critical patent/CN109996994B/en
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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F1/00Room units for air-conditioning, e.g. separate or self-contained units or units receiving primary air from a central station
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F13/00Details common to, or for air-conditioning, air-humidification, ventilation or use of air currents for screening
    • F24F13/22Means for preventing condensation or evacuating condensate
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/02Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
    • F28F3/04Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/08Elements constructed for building-up into stacks, e.g. capable of being taken apart for cleaning

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Air Filters, Heat-Exchange Apparatuses, And Housings Of Air-Conditioning Units (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Devices For Blowing Cold Air, Devices For Blowing Warm Air, And Means For Preventing Water Condensation In Air Conditioning Units (AREA)

Abstract

Air conditioner of the invention includes: plywood fin and the heat exchanger that constitutes;To the blower of above-mentioned heat exchanger air-supply;Be configured at above-mentioned heat exchanger vertical below drip tray.Using the protrusion being made of multiple protrusions for being configured at above-mentioned plate fin, gap is formed between adjacent plate fin.Above-mentioned heat exchanger is obliquely arranged.Above-mentioned protrusion has the downside ora terminalis multiple lower projections in the inner part being configured at than above-mentioned plate fin.

Description

Air conditioner
Technical field
The present invention relates to a kind of air conditioners, are especially able to suppress using generation when plate fin laminated type heat exchanger Condensed water drip tray enlargement and equipment entirety reduced performance air conditioner.
Background technique
In general, making by the refrigerant of compressor compresses in air conditioner in heat exchangers such as condenser, evaporators Middle circulation simultaneously makes it carry out heat exchange with air to carry out cooling supply or heating.Herein, heat exchanger is obliquely set to main body Interior wind path, the drip tray of the condensed water generated when being provided with for receiving cooling supply etc. in heat exchanger is (for example, referring to patent text It offers 1).
Figure 12 indicates air conditioner described in Patent Document 1.The existing air conditioner is set in the top of main body 100 There is blow-off outlet 101, is equipped with suction inlet 102 in lower surface.The wind path 103 divulged information from bottom to top is formed in main body 100.In wind It is provided with to the upper angled on road 103 heat exchanger 104, and is configured with air supply device 105.Moreover, being obliquely set to The lower section of heat exchanger 104 in wind path 103 is provided with the condensation for carrying out automatic heat-exchanger for receiving equal generations while cooling The drip tray 106 of water.
Performance, the energy saving of such existing air conditioner are largely imitated by the heat exchange of heat exchanger 104 Rate or so.Therefore, it is efficient to be strongly required heat exchanger 104.
In order to make the high efficiency of heat exchanger 104, a kind of heat conducting pipe that will run through fins set is proposed in the prior art The technology of thinning.
But there are limits for the downsizing of above-mentioned heat-transfer pipe, so the raising and miniaturization of heat exchanger effectiveness are increasingly By near limit.
Existing technical literature
Patent document
Patent document 1: Japanese Unexamined Patent Publication 2016-95038 bulletin
Summary of the invention
The present inventor is by using the heat exchanger that multiple plate fins are laminated and constitute, i.e., so-called plate fin laminated type Heat exchanger, it is intended to promote the high efficiency of heat exchanger.
In the plate fin laminated type heat exchanger, the refrigerant for the flow path being formed in plate fin be laminated Plate fin between carry out heat exchange between the air that flows.It is in plate fin that concave groove is stamping and form refrigerant flow path, Therefore the sectional area of the flow path can be made also smaller than the heat conducting pipe of fin-and-tube type, heat exchanger effectiveness improves.
In above-mentioned plate fin laminated type heat exchanger, between considering that column are set between multiple each plate fins for being used to form stacking A part of the protrusion of gap, multiple protrusions is arranged along the ora terminalis of the long side of plate fin.
In this case, there are following possibilities: condensing in heat exchanger when using the plate fin laminated type heat exchanger Ora terminalis (hereinafter referred to as on the downside of ora terminalis) of the water droplet along the downside as the heat exchanger being obliquely arranged when flowing down, water droplet touches It is tangled to the protrusion connect with the downside ora terminalis of plate fin column, is dripped downwards from the protrusion in this way because of gravity.
Therefore, when plate fin laminated type heat exchanger to be obliquely arranged, the drip tray below heat exchanger is set Need the size with the magnitude of inclination of heat exchanger (size when heat exchanger projects to below vertical) equal extent.As a result, Drip tray can be enlarged, as a result, there is performance deterioration caused by the enlargement for causing equipment, the increase of wind path resistance etc. A possibility that such technical problem.
The present invention is to solve the invention of such technical problem, and its purpose is to provide Chinese medicines to have high heat exchanger effectiveness simultaneously And compact, high performance air conditioner.
Air conditioner of the invention includes: plywood fin and the heat exchanger that constitutes;It blows to above-mentioned heat exchanger Blower;Be configured at above-mentioned heat exchanger vertical below drip tray.Using be configured at above-mentioned plate fin by multiple prominent The protrusion constituted is acted, is formed with gap between adjacent plate fin.Above-mentioned heat exchanger is obliquely set to above-mentioned air tune The intracorporal wind path of the shell of section machine.Above-mentioned protrusion has the downside ora terminalis multiple downsides in the inner part being configured at than above-mentioned plate fin Protrusion.
The heat exchanger improves heat exchanger effectiveness by the way that flow path to be thinned as a result,.Moreover, can prevent from being set to Downside ora terminalis protrusion in the inner part than the plate fin being obliquely arranged drips condensed water.It is solidifying thereby, it is possible to be used to receive The drip tray miniaturization born water inhibits the enlargement of equipment, wind path resistance to increase caused performance deterioration etc..
According to above structure, the present invention provides a kind of with high heat exchanger effectiveness and compact, high performance air conditioning Machine.
Detailed description of the invention
Fig. 1 is to indicate that the air conditioner of embodiments of the present invention 1 has the figure in the outline section of heat exchanger.
Fig. 2 is the perspective view for indicating the heat exchanger of the air conditioner.
Fig. 3 is the perspective view for discretely indicating the heat exchanger.
Fig. 4 is the perspective view cut off a part for the plate fin laminated body for constituting the heat exchanger to indicate.
Fig. 5 is the top view for constituting the plate fin of the plate fin laminated body.
Fig. 6 is the enlarged plan view of the plate fin.
Fig. 7 is the exploded perspective view for enlargedly indicating a part of the plate fin.
Fig. 8 is the amplification stereogram for indicating to be set to the protrusion of the plate fin.
Fig. 9 is the approximate stereogram for illustrating the effect of the heat exchanger.
Figure 10 is the figure for indicating the outline section for illustrating the effect of the heat exchanger.
Figure 11 is that the amplification of the plate fin for the heat exchanger that the air conditioner of composition embodiments of the present invention 2 has is vertical Body figure.
Figure 12 is the schematic structural diagram for indicating existing air conditioner.
Specific embodiment
The air conditioner of 1st mode air conditioner of the invention includes: plywood fin and the heat exchanger that constitutes; To the blower of above-mentioned heat exchanger air-supply;Be configured at above-mentioned heat exchanger vertical below drip tray.On being configured at The protrusion being made of multiple protrusions for stating plate fin is formed with gap between adjacent plate fin.Above-mentioned heat exchanger inclination Ground is set to the intracorporal wind path of shell of above-mentioned air conditioner.Above-mentioned protrusion, which has, is configured at the lower side than above-mentioned plate fin The multiple lower projections of edge in the inner part.
The heat exchanger improves heat exchanger effectiveness by the way that flow path to be thinned as a result,.Further, it is possible to prevent condensed water from The downside ora terminalis protrusion in the inner part being set to than the plate fin being obliquely arranged drips.Thereby, it is possible to inhibit to be used to connect Receive enlarged and performance deterioration etc. caused by the increase of wind path resistance of the drip tray miniaturization of condensed water and equipment.
In 2nd mode, above-mentioned multiple lower projections include: than the size in above-mentioned gap from above-mentioned lower side genesis by above-mentioned Multiple 1st protrusions of inside setting;With the 2nd protrusion for leaning on the setting of above-mentioned lower side edge side than above-mentioned multiple 1st protrusions.
As a result, the gap in condensed water between the fin plate lamination of the downside ora terminalis of plate fin and in the case where flow down, Also it can prevent the water to drip from encountering protrusion.When the water to drip as a result, is partially flowed down downwards by such impetus, Neng Goufang Only it hangs over protrusion and drips from the protrusion.Thereby, it is possible to be more reliably prevented to drip.
In 3rd mode, above-mentioned multiple respective tops of protrusion are dome shape.Herein, " dome shape " includes substantially dome shape.
Even if the feelings that a part for the condensed water that the downside ora terminalis for appearing in plate fin as a result, flows down and protrusion are encountered Condition, since the top of protrusion is dome shape, condensed water is also easy to leave from the top, can be in this way under plate fin Side edge flows down.Therefore, condensed water can be more reliably prevented to drip using protrusion as starting point.
In 4th mode, above-mentioned multiple 1st protrusions, which are set to below the vertical of above-mentioned downside ora terminalis, is not present above-mentioned water receiving The region of disk.
There are the protrusions of the downside ora terminalis of the plate fin of the part of drip tray below vertical as a result, are arranged extremely close The intensity of the weaker fin ora terminalis of intensity is improved at the ora terminalis of downside, thus, it is possible to improve its rigidity.Moreover, extremely close to ora terminalis Place is provided with the protrusion, and thus the heat exchange effective area positioned at the inside of protrusion increases, and heat exchanger effectiveness improves corresponding amount. That is, the rigidity of plate fin and the raising of heat exchanger effectiveness can be taken into account.
In 5th mode, above-mentioned protrusion has the multiple upper pleurapophysis being configured near the upside ora terminalis of above-mentioned plate fin It rises.
The rigidity raising and the heat exchange due to increase of heat exchange effective area of the upside end edge portion of plate fin point as a result, Efficiency improves, and can more effectively realize the rigidity of plate fin and the raising of heat exchanger effectiveness.
In 6th mode, above-mentioned heat exchanger configures in such a way that above-mentioned lower side edge is located at the upstream side of above-mentioned wind path.
Thereby, it is possible to inhibit the air stream due to flowing in wind path and the condensed water under the downside ora terminalis stream of plate fin Gravity caused by the effect of falling.As a result, condensed water is made more to flow down and then drip to the section below of plate fin. Therefore, drip tray can be made more compact, and the number of projection near the downside ora terminalis of plate fin is set and becomes more, into one Step improves the improvement effect of rigidity and heat exchanger effectiveness.
Hereinafter, being described in detail with reference to the accompanying drawings to embodiments of the present invention.Wherein, in implementation described below Mode is an example, and the present invention is not limited to the embodiments.
(embodiment 1)
Fig. 1 is the figure for indicating the outline section of the air conditioner of embodiments of the present invention 1.
In the air conditioner of present embodiment, although it is not shown, refrigerant is according to compressor, four-way valve, heat source side Heat exchanger, expansion valve are recycled using the sequence of side heat exchanger, four-way valve, compressor, and heat source side heat exchanger is as condensation Device plays a role, and plays a role using side heat exchanger as evaporator, thus carries out for blowdown firing.In addition, passing through switching four Port valve, in the air conditioner, refrigerant according to compressor, four-way valve, utilize side heat exchanger, expansion valve, heat source side heat The sequence circulation of exchanger, four-way valve, compressor, is played a role using side heat exchanger as condenser, heat source side heat exchange Device plays a role as evaporator, thus carries out warming operation.
Moreover, the air conditioner is by indoor unit and outdoor unit by being piped the Split type air tune to link together Section machine is accommodated with indoors using side heat exchanger etc. in unit, compressor, four-way valve, expansion is accommodated in outdoor unit Valve, heat source side heat exchanger etc..
The main body 1 of indoor unit as the air conditioner constituted as described above, as shown in Figure 1, in this embodiment party It is equipped with suction inlet 2 in lower surface in formula, blow-off outlet 3 is equipped in front surface, is formed with L between the suction inlet 2 and blow-off outlet 3 The wind path 4 of font (including generally L-shaped).Moreover, being provided in wind path 4 as 5 He of heat exchanger using side heat exchanger Blower 6.
Heat exchanger 5 is obliquely configured relative to vertical line, is provided with reception by heat exchanger in the lower end of heat exchanger 5 The drip tray 7 of the condensed water of 5 condensations.
Then, using Fig. 2~Figure 10, illustrate the structure of heat exchanger 5.
Fig. 2 is the perspective view for indicating the heat exchanger of air conditioner.Fig. 3 is the solid for discretely indicating the heat exchanger Figure.Fig. 4 is the perspective view for indicating a part cutting of the plate fin laminated body for the main body for constituting the heat exchanger.Fig. 5 is Constitute the top view of the plate fin of the plate fin laminated body.Fig. 6 is the enlarged plan view of the plate fin.Fig. 7 is enlargedly to indicate The exploded perspective view of a part of the plate fin.Fig. 8 is the amplification stereogram for indicating to be set to the protrusion of the plate fin.Fig. 9 is Illustrate the approximate stereogram of the effect of the heat exchanger.Figure 10 is the outline section for the effect for indicating to illustrate the heat exchanger Figure.
The heat exchanger 5 of present embodiment is as shown in Figure 2 and Figure 3, by multiple plate fins 11 stacking of rectangular plate It constitutes, when the two sides (left and right side in Fig. 2, Fig. 3) of its stacking direction are equipped with and overlook and plate fin 11 has same shape End plate 12a, the 12b of (including roughly the same shape).End plate 12a, 12b are formed by the plate with rigidity, such as pass through grinding The metal material of aluminium, aluminium alloy, stainless steel etc. is formed to carry out intermetallic composite coating.
In addition, above-mentioned end plate 12a, 12b, multiple plate fins 11 are closed with the state pricker soldered joint of stacking and make their one Change, constitutes the plate fin laminated body 13 for forming the main body of heat exchanger.
In addition, plate fin 11 have it is multiple side by side can flow the refrigerant of refrigerant as the 1st fluid in inside Flow path group.The refrigerant flow path group is formed as U-shaped (including substantially U-shaped).The 1st collector stream being connected with refrigerant flow path group Road 14, the 2nd collector flow path 15 are set to the one end of the end plate 12a of the side (being left side in Fig. 1) of plate fin laminated body 13 Side.
Specifically, as shown in Fig. 5~Fig. 7, plate fin 11 with multiple refrigerant flow paths 16 side by side be formed with and make A pair of plate-shaped component 17a, 17b (referring to Fig. 7) phase of the 1st connected collector flow path 14 of refrigerant line 16 and the 2nd collector flow path 15 It is constituted to the mode of ground soldered joint.Multiple refrigerant flow paths 16 are formed as U-shaped (including substantially U-shaped), with refrigerant stream The 1st connected collector flow path 14 of road 16 and the 2nd collector flow path 15 are configured in a manner of the one end side for concentrating on plate fin 11.
Moreover, multiple, composition Fig. 2, plate fin shown in Fig. 3 stacking is laminated in the plate fin 11 of above structure as shown in Figure 4 Body 13.Each plate fin 11 to each other, utilize column be set to plate fin 11 long side both ends and refrigerant flow path 16 between protrusion Portion 18 is formed with the gap 19 of air flow (referring to Fig. 4).Protrusion 18 is made of multiple protrusions.As described above, heat is handed over Parallel operation 5 enables the 2nd fluid to fold interflow in each plate fin of the plate fin laminated body with the 1st flowable flow path of fluid It is dynamic, heat exchange is able to carry out between the 1st fluid and the 2nd fluid.
Adjacent plate fin 11 is engaged with each other by protrusion 18, it may have the function of link plate fin 11.
In addition, refrigerant flow path 16 is formed as concave groove in plate-shaped member 17a, 17b, and it is easy thinning.
In addition, in refrigerant flow path 16, be connected to the 1st collector flow path 14 go trackside refrigerant flow path 16a with connect Between the return road side refrigerant flow path 16b of the 2nd collector flow path 15, the mobile slit of the heat being formed between preventing the two 20。
The heat exchanger 5 constituted as described above can be tilted by air in such a way that the gap 19 between plate fin 11 is flowed Ground setting.Herein, as shown in Figure 9, Figure 10, especially as shown in Figure 10, in the lower face side for the plate fin 11 being obliquely arranged, The downside ora terminalis 11a of upstream side as wind path 4 arranges the lower projection 18a set, is located at its all or part than downside The mode of ora terminalis 11a in the inner part is arranged.Moreover, in the present embodiment, positioned at the of the inclination section below of downside ora terminalis 11a 2 protrusion 18ab, in the close downside ora terminalis compared with the 1st protrusion 18aa of the inclination upper section positioned at downside ora terminalis 11a The mode of the position of the side 11a is arranged.
In other words, drip tray 7 is not present to be located at below the vertical for the heat exchanger 5 being obliquely arranged in heat exchanger 5 Opening part, that is, drip tray 7 opening drop shadow spread outside the 1st protrusion 18aa, positioned at the downside ora terminalis than plate fin 11 Mode of the 11a at the distance as defined in the inside is arranged.Moreover, being located at the 2nd protrusion in the opening drop shadow spread of drip tray 7 18ab is set on the downside of the fin of plate fin 11 near ora terminalis 11a.In addition it is also possible to for the 2nd protrusion 18ab with downside ora terminalis 11a is arranged in conplane mode.
Moreover, in the present embodiment, the 1st protrusion 18aa is from the ora terminalis 11a of downside to be located at than the sky between plate fin 11 The mode of the position of the size in the gap 19 of flow of air in the inner part is arranged.
In addition, the upper lateral process 18b that column are set to the upside ora terminalis 11b of plate fin 11 spreads the entire long side of plate fin 11, It is same as the 2nd protrusion 18ab, it is set on the upside of the position in the inner part than upside ora terminalis 11b, such as fin near ora terminalis 11b.
The positional relationship of protrusion 18 (18a, 18aa, 18ab, 18b) (figure as the enlarged plan view of Fig. 6 is expressed The lower section of plate fin 11 is downside ora terminalis 11a in 6, and top is upside ora terminalis 11b).
In addition, the whole of protrusion 18 (18a, 18aa, 18ab, 18b) or being at least set to the lower side of plate fin 11 The top of the lower projection 18a (18aa, 18ab) of edge 11a is dome shape (having substantially dome shape).
In addition, the tilt angle of heat exchanger 5 is different according to the structure of wind path 4, suitably set, if considering condensation The relationship for flowing down (stream) and dripping of water can be then opposite vertical line into 20 degree~50 degree, preferably at 30 degree~40 degree.
In the air conditioner constituted as described above, in case where when coagulating for blowdown firing, to it Function and effect are illustrated.
Firstly, illustrating the flowing and heat exchange action of refrigerant.Refrigerant is from the inflow side as plate fin laminated body 13 The 1st collector flow path 14 flow into 16 groups of refrigerant flow path.It is flowed into 16 groups of refrigerant flow path of refrigerant of each plate fin 11, from As refrigerant flow path 16 remove trackside go trackside refrigerant flow path 16a to the return road side refrigerant flow path as return road side 16b turns back, and the refrigerant circuit of refrigeration system is then flowed to from the 2nd collector flow path 15 as outlet side.
Then, when refrigerant is when refrigerant flow path 16 flows, with the plate fin lamination for passing through plate fin laminated body 13 Between gap 19 air carry out heat exchange.
At this point, being formed in the refrigerant of plate fin 11 by reducing about the flowable refrigerant flow path 16 of refrigerant The sectional area of the concave groove of flow path can be realized the thinning of flow path.As a result, compared with the heat conducting pipe mode the case where, energy It is enough that miniaturization is promoted while improving heat exchanger effectiveness.
In addition, heat exchanger 5 carries out heat exchange to the air in the gap 19 passing through plate fin lamination, become the air Cold air or heating.When making cold air to air progress heat exchange, the hydrogenesis in air is handed in heat sometimes The surface of parallel operation 5.Since heat exchanger 5 is obliquely arranged, condensed water is as shown in Figure 9 along the plate wing for constituting heat exchanger 5 The downside ora terminalis 11a of piece 11 is flowed down downwards.
Herein, heat exchanger 5 is plate fin laminated type heat exchanger, therefore as shown in Figure 10, in the ora terminalis of plate fin 11 The column such as part are equipped with the protrusion 18 (18a (18aa, 18ab), 18b) for forming the gap of plate fin to each other.Condensed water can The inclination upper section of the downside ora terminalis 11a of the plate fin 11 of flowing arranges the multiple 1st protrusion 18aa set, is located at than downside ora terminalis 11a inwardly (inboard) at defined distance, therefore condensed water will not meet the 1st protrusion 18aa and by tangling along plate wing The downside ora terminalis 11a of piece 11 is flowed down downwards.Moreover, in the present embodiment, the 2nd protrusion 18ab of the lowest part of plate fin 11 It is set on the downside of fin near ora terminalis 11a, therefore, the condensed water flowed down is met the 2nd protrusion 18ab and tangled, from the 2nd protrusion 18ab drips downwards.
Therefore, it can narrow to the 2nd protrusion 18ab's for receiving the drip tray 7 of the condensed water to drip from heat exchanger 5 Size M, and inclination size (size when heat exchanger projects below vertical) L (Figure 10 ginseng of not inclined heat exchanger 5 According to), it being capable of densification.In addition, 7 densification of drip tray can be made, therefore a part that can reduce drip tray 7 enters wind path 4 Or the limitation for having to make wind path 4 to narrow etc., performance deterioration etc. caused by being able to suppress because of above-mentioned reason.
In addition, in the present embodiment, according to above-mentioned explanation it is found that being set to the downside ora terminalis 11a's of plate fin 11 In lower projection 18a, the 1st protrusion 18aa of part not opposite with drip tray 7 is located at least in than the 2nd protrusion 18ab backup plate fin 11 inside setting, it is attached that the 2nd protrusion 18ab positioned at the part opposite with drip tray 7 is configured to be set to ora terminalis on the downside of fin Closely.
Therefore, in heat exchanger 5, the 2nd protrusion 18ab is located at the downside of the plate fin 11 of the part opposite with drip tray 7 Near ora terminalis 11a, the intensity of the smaller fin ora terminalis of intensity is improved to provide its rigidity.Moreover, the 2nd protrusion 18ab is arranged Near the ora terminalis 11a of downside, thus increase than the heat exchange effective area of the 2nd protrusion 18ab in the inner part, heat exchanger effectiveness improves Corresponding amount.
Specifically, as shown in fig. 6, when protrusion 18 being arranged near the downside ora terminalis 11a in plate fin 11, than setting The 2nd protrusion 18ab near the ora terminalis 11a of downside is the higher heat of heat exchanger effectiveness at refrigerant flow path 16 in the inner part Effective area X is exchanged, is greater than the 1st protrusion 18aa's being arranged in a manner of being located at (inboard) in the inner part than downside ora terminalis 11a The heat exchange effective area Y of inside.Therefore, heat exchanger effectiveness improves corresponding amount.
In addition, lower projection 18a (18aa, 18ab) does not contribute its own heat exchange effectively.Therefore, when under reduction It can increase when lateral process 18a (18aa, 18ab) itself to the contributive heat exchange area of the heat exchange of plate fin 11, Neng Goujin One step improves heat exchanger effectiveness.It is therefore preferable that lower projection 18a (18aa, 18ab) and upper lateral process 18b are contracted to required Minimal size.
It is arranged as described above, working as a protrusion in the protrusion column for be arranged in the downside ora terminalis 11a of plate fin 11 in lower side When near edge 11a, the rigidity that can take into account plate fin 11 improves and the raising of heat exchanger effectiveness.
In addition, being configured to be greater than plate wing from the size Z (referring to Fig. 6) that the downside ora terminalis 11a of the 1st protrusion 18aa is gone inwardly The size in the gap in the gap 19 (referring to Fig. 4) of piece 11 to each other.Therefore, even if condensed water spreads the downside ora terminalis of plate fin 11 Gap 19 between the fin plate 11 of 11a and flow down, can also make that it does not encounter with the 1st protrusion 18aa and part is flowed downwards as former state Under.Therefore, can prevent, which becomes condensed water, hangs over the 1st protrusion for being set to inclination upper section not opposite with drip tray 7 The case where state of 18aa is dripped using the 1st protrusion 18aa as starting point to condensed water, can be more reliably prevented from and drip.
In addition, protrusion 18 (18a, 18aa, 18ab, 18b) makes its top become dome shape (including substantially as shown in Figure 8 Dome shape).A part and the 1st protrusion 18aa of the condensed water under the downside ora terminalis 11a stream of plate fin 11 are become as a result, Encounter such situation, since the top of the 1st protrusion 18aa is dome shape (including substantially dome shape), condensed water is also difficult to Hang over the top.Therefore, condensed water can be more reliably prevented from condensed water as former state along ora terminalis 11a on the downside of fin with the 1st protrusion 18aa drips for starting point.
In addition, being equipped with upper lateral process in the downside ora terminalis 11a of plate fin 11 and the upside side ora terminalis 11b column in heat exchanger 5 18b, the upper lateral process 18b of the upside side ora terminalis 11b are configured to be set near the ora terminalis 11b of upside.Therefore, it can be improved plate fin The rigidity of the 11 upside part ora terminalis 11b, and heat exchanger effectiveness improves due to the increase of heat exchange effective area.Therefore, energy Enough rigidity for more effectively taking into account plate fin 11 improve and the raising of heat exchanger effectiveness.
In addition, in this embodiment, heat exchanger 5 is located at wind path 4 with the part downside ora terminalis 11a of its plate fin 11 The mode of upstream side configures.Thereby, it is possible to caused by the gravity of the condensed water under inhibiting the downside ora terminalis 11a in plate fin 11 to flow Whereabouts effect, condensed water can partially drip on the lower from than plate fin 11.Therefore, drip tray 7 can be made more compact.And And increase the quantity for the 2nd protrusion 18ab being set near the downside ora terminalis 11a of plate fin 11, rigidity can be further increased And heat exchanger effectiveness.
(embodiment 2)
Figure 11 indicates the protrusion of the plate fin of embodiment 2.In the present embodiment, it is set to the protrusion 18 of plate fin 11 (18a, 18aa, 18ab, 18b) cuts forming in the form of along refrigerant flow path 16 as shown in figure 11 and is formed, the incision configured ends Edge E is configured to opposite with the flow direction W of air of folded interflow in plate fin 11.
As a result, in protrusion 18 (18a, 18aa, 18ab, 18b), centainly same can be spaced between making plate fin lamination When, keep the dead water region for being easy to generate in the downstream side of protrusion 18 (18a, 18aa, 18ab, 18b) minimum and is being cut into Shape ora terminalis E plays leading edge effect in part.And it is opposite with the flow direction W of air due to cutting the part forming ora terminalis E, it is right The flow resistance of air becomes smaller.Therefore, the flow path resistance for being able to suppress the flow passage region of plate fin laminated body 13 increases, and further increases Heat exchanger effectiveness.
In addition, the incision of protrusion 18 (18a, 18aa, 18ab, 18b) is shaped along the refrigerant of plate fin laminated body 13 The mode of flow path 16 is formed.It therefore, there is no need to from the concave plane between the refrigerant flow path in the direction that refrigerant flow path 16 intersects 21 settings are used to form the thinning portion of wall thickness for cutting forming.Therefore, it is with protrusion 18 (18a, 18aa, 18ab, 18b) protuberance is made Mode that is cylindric and being formed is compared, and the concave plane size of refrigerant flow path to each other can be made to narrow and do not need setting wall thickness change The amount in thin portion, capable of correspondingly making plate fin 11, in other words heat exchanger minimizes.
The function and effect of other structures are identical as embodiment 1, omit the description.
More than, to air conditioner of the invention, it is illustrated using above embodiment, but the present invention is not limited to This.That is, all aspects of embodiments of the present invention are to illustrate, it is not considered that being limited, the scope of the present invention is not by upper The explanation stated provides, and is provided by the scope of the claims, mean equivalent comprising the scope of the claims and therewith content and All changes in range.
Utilization possibility in industry
According to the explanation of above embodiment it is found that the present invention be capable of providing a kind of heat exchanger effectiveness with higher and Compact, high performance air conditioner.Therefore, home-use air conditioner can not only be used as, can be also widely used as Industrial air conditioner.
Description of symbols
1 main body
2 suction inlets
3 blow-off outlets
4 wind paths
5 heat exchangers
6 blowers
7 drip trays
11 plate fins
Ora terminalis on the downside of 11a
Ora terminalis on the upside of 11b
12a, 12b end plate
13 plate fin laminated bodies
14 the 1st collector flow paths
15 the 2nd collector flow paths
16 refrigerant flow paths
16a removes trackside refrigerant flow path
The return road 16b side refrigerant flow path
17a, 17b plate-shaped member
18 protrusions
18a lower projection
The 1st protrusion of 18aa
The 2nd protrusion of 18ab
The upper lateral process of 18b
19 gaps
20 slits
21 concave planes.

Claims (6)

1. a kind of air conditioner characterized by comprising
Plywood fin and the heat exchanger constituted;
To the blower of heat exchanger air-supply;With
The drip tray being configured at below the vertical of the heat exchanger,
Using the protrusion being made of multiple protrusions for being configured at the plate fin, it is formed with gap between adjacent plate fin,
The heat exchanger is obliquely set to the intracorporal wind path of shell of the air conditioner,
The protrusion has the downside ora terminalis multiple lower projections in the inner part being configured at than the plate fin.
2. air conditioner as described in claim 1, it is characterised in that:
The multiple lower projection includes: than the size in the gap from the lower side genesis by the multiple of inside setting 1st protrusion;With the 2nd protrusion for leaning on the setting of downside ora terminalis side than the multiple 1st protrusion.
3. air conditioner as claimed in claim 1 or 2, it is characterised in that:
The multiple respective top of protrusion is dome shape.
4. air conditioner according to any one of claims 1 to 3, it is characterised in that:
The multiple 1st protrusion is set to the region that the drip tray is not present below the vertical of the downside ora terminalis.
5. air conditioner as described in any one of claims 1 to 4, it is characterised in that:
The protrusion has the multiple upper lateral process being configured near the upside ora terminalis of the plate fin.
6. such as air conditioner according to any one of claims 1 to 5, it is characterised in that:
The heat exchanger configures in such a way that the downside ora terminalis is located at the upstream side of the wind path.
CN201780071215.4A 2016-12-15 2017-11-15 Air conditioner Active CN109996994B (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP2016-242813 2016-12-15
JP2016242813A JP6739001B2 (en) 2016-12-15 2016-12-15 Air conditioner
PCT/JP2017/041016 WO2018110186A1 (en) 2016-12-15 2017-11-15 Air conditioner

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CN109996994A true CN109996994A (en) 2019-07-09
CN109996994B CN109996994B (en) 2021-05-14

Family

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Country Status (4)

Country Link
JP (1) JP6739001B2 (en)
CN (1) CN109996994B (en)
MY (1) MY195659A (en)
WO (1) WO2018110186A1 (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1433521A (en) * 1972-03-01 1976-04-28 Marlo Spa Induction air conditioning apparatus
CN1474101A (en) * 2002-05-28 2004-02-11 松下电器产业株式会社 Air conditioner
KR101371889B1 (en) * 2007-12-26 2014-03-07 (주)귀뚜라미 Apparatus for preventing leakage of condensate in air conditioner
JP2016151392A (en) * 2015-02-18 2016-08-22 有限会社和氣製作所 Heat exchanger

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007078280A (en) * 2005-09-15 2007-03-29 Denso Corp Heat exchanger for cooling
JP2008209073A (en) * 2007-02-27 2008-09-11 Xenesys Inc Heat exchanger manufacturing method and heat exchange plate
JP4947077B2 (en) * 2009-03-25 2012-06-06 ダイキン工業株式会社 Indoor unit of heat exchanger and air conditioner equipped with the same
JP5631452B2 (en) * 2013-07-02 2014-11-26 三菱電機株式会社 Finned tube heat exchanger and refrigeration cycle apparatus using the same

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1433521A (en) * 1972-03-01 1976-04-28 Marlo Spa Induction air conditioning apparatus
CN1474101A (en) * 2002-05-28 2004-02-11 松下电器产业株式会社 Air conditioner
KR101371889B1 (en) * 2007-12-26 2014-03-07 (주)귀뚜라미 Apparatus for preventing leakage of condensate in air conditioner
JP2016151392A (en) * 2015-02-18 2016-08-22 有限会社和氣製作所 Heat exchanger

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WO2018110186A1 (en) 2018-06-21
MY195659A (en) 2023-02-03
CN109996994B (en) 2021-05-14
JP2018096635A (en) 2018-06-21
JP6739001B2 (en) 2020-08-12

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