EP3279598B1 - Heat exchanger and air conditioner - Google Patents
Heat exchanger and air conditioner Download PDFInfo
- Publication number
- EP3279598B1 EP3279598B1 EP16772077.0A EP16772077A EP3279598B1 EP 3279598 B1 EP3279598 B1 EP 3279598B1 EP 16772077 A EP16772077 A EP 16772077A EP 3279598 B1 EP3279598 B1 EP 3279598B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- heat exchanger
- corrugated
- flat tubes
- lug portions
- fin
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 38
- 239000003507 refrigerant Substances 0.000 claims description 22
- 238000004378 air conditioning Methods 0.000 claims description 15
- 230000005494 condensation Effects 0.000 claims description 4
- 238000009833 condensation Methods 0.000 claims description 4
- 238000010257 thawing Methods 0.000 description 43
- 230000004048 modification Effects 0.000 description 24
- 238000012986 modification Methods 0.000 description 24
- 238000010438 heat treatment Methods 0.000 description 20
- 230000015556 catabolic process Effects 0.000 description 14
- 238000006731 degradation reaction Methods 0.000 description 14
- 230000015572 biosynthetic process Effects 0.000 description 13
- 230000000694 effects Effects 0.000 description 12
- 230000001965 increasing effect Effects 0.000 description 7
- 230000002035 prolonged effect Effects 0.000 description 6
- 230000002093 peripheral effect Effects 0.000 description 5
- 238000005057 refrigeration Methods 0.000 description 5
- 230000002708 enhancing effect Effects 0.000 description 4
- 230000001737 promoting effect Effects 0.000 description 4
- 238000009826 distribution Methods 0.000 description 3
- 230000005484 gravity Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000011295 pitch Substances 0.000 description 2
- 238000001816 cooling Methods 0.000 description 1
- 230000000593 degrading effect Effects 0.000 description 1
- 230000014509 gene expression Effects 0.000 description 1
- 238000005304 joining Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
Images
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F1/00—Room units for air-conditioning, e.g. separate or self-contained units or units receiving primary air from a central station
- F24F1/06—Separate outdoor units, e.g. outdoor unit to be linked to a separate room comprising a compressor and a heat exchanger
- F24F1/14—Heat exchangers specially adapted for separate outdoor units
- F24F1/18—Heat exchangers specially adapted for separate outdoor units characterised by their shape
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F17/00—Removing ice or water from heat-exchange apparatus
- F28F17/005—Means for draining condensates from heat exchangers, e.g. from evaporators
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B39/00—Evaporators; Condensers
- F25B39/02—Evaporators
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B39/00—Evaporators; Condensers
- F25B39/02—Evaporators
- F25B39/022—Evaporators with plate-like or laminated elements
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D1/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
- F28D1/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
- F28D1/04—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits
- F28D1/053—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being straight
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D1/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
- F28D1/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
- F28D1/04—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits
- F28D1/053—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being straight
- F28D1/0535—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being straight the conduits having a non-circular cross-section
- F28D1/05366—Assemblies of conduits connected to common headers, e.g. core type radiators
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
- F28F1/12—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
- F28F1/126—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element consisting of zig-zag shaped fins
- F28F1/128—Fins with openings, e.g. louvered fins
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
- F28F1/12—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
- F28F1/24—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely
- F28F1/30—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely the means being attachable to the element
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
- F28F1/12—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
- F28F1/24—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely
- F28F1/32—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely the means having portions engaging further tubular elements
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F19/00—Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
- F28D2021/0068—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for refrigerant cycles
- F28D2021/0071—Evaporators
Definitions
- the present invention relates to a heat exchanger that is to be used in air-conditioning apparatuses such as a room air-conditioning apparatus and a package air-conditioning apparatus, and to an air-conditioning apparatus including the heat exchanger.
- Patent Literature 1 Japanese Unexamined Patent Application Publication JP 6-147 785 A
- the present invention has been made to solve the above-mentioned problem and has an object to provide a heat exchanger and an air-conditioning apparatus that are capable of preventing degradation of defrosting performance while promoting heat transfer.
- the corrugated fin includes the protruding portion protruding to the front side with respect to the front-side end portion of each of the flat tubes.
- the protruding portion includes the (first) lug portion to promote heat transfer.
- the lug portion is oriented obliquely to the front-and-back direction that is the airflow direction.
- a heat transfer passage is less likely to be divided by the lug portion during a defrosting operation as compared to a case where the lug portion is formed in the airflow orthogonal direction.
- heat can sufficiently be transferred to the protruding portion and the lug portion of the corrugated fin, thereby being capable of preventing the degradation of the defrosting performance.
- FIG. 1 is a perspective view for illustrating a corrugated-fin heat exchanger 10 according to Embodiment 1 of the present invention.
- FIG. 2 is an enlarged front view of flat tubes 1 and corrugated fins 2 of the corrugated-fin heat exchanger 10 according to Embodiment 1 of the present invention.
- the arrow WF in FIG. 1 indicates a flow of air (airflow direction) generated by a fan 31 (see FIG. 4 and FIG. 5 described later) or other units, and the arrow RF indicates a flow of refrigerant.
- the same arrows are used in the drawings described later.
- the expressions “up”, “down”, “left”, “right”, “front”, and “back” used in Embodiment 1 indicate directions that are given when the corrugated-fin heat exchanger 10 is viewed from the front side unless otherwise noted.
- the corrugated-fin heat exchanger 10 includes the plurality of flat tubes 1 arranged in an airflow orthogonal direction (right-and-left direction) orthogonal to the airflow direction (front-and-back direction) indicated by the arrow WF, the meandering corrugated fins 2 each sandwiched by the adjacent flat tubes 1 and thermally connected to the flat tubes 1 at each apex 2a, an inlet header 3 connected to one end (lower end) of each flat tube 1, and an outlet header 4 connected to the other end (upper end) of each flat tube 1.
- the corrugated-fin heat exchanger 10 exchanges heat between refrigerant flowing through the flat tubes 1 and air flowing through spaces each surrounded by the adjacent flat tubes 1 and the corrugated fin 2 (hereinafter referred to as "heat-exchanger air passages").
- Each flat tube 1 extends along an up-and-down direction.
- the corrugated fins 2 are each a metal thin plate shaped to have peaks and troughs that are apexes 2a alternately as viewed from one side.
- the peaks of the corrugated fin 2 are joined to a surface of one flat tube 1 of the two flat tubes 1 adjacent in the airflow orthogonal direction (right-and-left direction), and the troughs of the corrugated fin 2 are joined to a surface of the other flat tube 1.
- the peaks and the troughs of the corrugated fin 2 have a shape extending in the airflow direction (front-and-back direction).
- joined portions between the corrugated fin 2 and the flat tube 1 each have a linear shape being continuous in the airflow direction (front-and-back direction).
- the joined portions each have a width enough for the joining.
- the joined portions between the corrugated fins 2 and the flat tubes 1 each have a wide linear shape.
- FIG. 3 is a sectional view of the corrugated-fin heat exchanger 10 according to Embodiment 1 of the present invention that is taken along the line A-A of FIG. 2 .
- FIGS. 6 are views for illustrating first lug portions 7 of the corrugated-fin heat exchanger 10 according to Embodiment 1 of the present invention.
- a part (a) is a perspective view of the first lug portions 7, and a part (b) is a sectional view taken along the line B-B of the part (a).
- each of the corrugated fins 2 there is formed a protruding portion 5 protruding to a windward side (front side) with respect to windward-side end portions (front-side end portions) 1a of the flat tubes 1. Further, a plurality of lug portions are formed in the corrugated fin 2 to promote heat transfer (promote heat transfer between fin and air).
- the first lug portions 7 are formed in the protruding portion 5 in a radial direction extending from the flat tubes 1 toward a center portion of a windward-side end portion (front-side end portion) of the protruding portion 5. Those first lug portions 7 formed to be inclined (oblique) to the airflow direction (front-and-back direction) are provided such that the two first lug portions 7 are arranged in a bilaterally symmetrical manner.
- the first lug portions 7 are each of a louver type in which two slits (cut lines) are formed in the surface of the protruding portion 5 (hereinafter referred to as "protruding surface") of the corrugated fin 2, and the first lug portions 7 are each lugged from the two slits in the protruding surface of the corrugated fin 2 in both the up and down directions.
- second lug portions 6 formed in the airflow orthogonal direction (right-and-left direction), and the five second lug portions 6 are formed to be arrayed in the airflow direction (front-and-back direction).
- FIG. 4 is a schematic view for illustrating an outdoor unit (side-flow type) of an air-conditioning apparatus according to Embodiment 1 of the present invention.
- FIG. 5 is a schematic view for illustrating an outdoor unit (top-flow type) of the air-conditioning apparatus according to Embodiment 1 of the present invention.
- FIG. 4 and FIG. 5 are also referred to in Embodiment 2 described later.
- the corrugated-fin heat exchanger 10 is mounted to the outdoor unit of the air-conditioning apparatus including the fan 31, thereby constructing a refrigeration cycle for circulating refrigerant between the outdoor unit and an indoor unit connected to the outdoor unit by pipes.
- FIG. 4 As the outdoor unit in which the corrugated-fin heat exchanger 10 is mounted, a side-flow type illustrated in FIG. 4 and a top-flow type illustrated in FIG. 5 are given.
- an air outlet 32a is provided in a side surface of an outdoor-unit main body 30a on a front surface side.
- a corrugated-fin heat exchanger 10a having an L-shape in plan view is mounted to the outdoor unit, and air inlets 33a are provided in side surfaces of the outdoor-unit main body 30a that are opposed to the corrugated-fin heat exchanger 10a.
- the air With a flow of air that is generated by the fan 31, the air is sucked into the outdoor-unit main body 30a through the air inlets 33a, and flows through the corrugated-fin heat exchanger 10a. At this time, heat is exchanged between the air and refrigerant sent from the indoor unit (not shown), compressed in a compressor 34, and then flowing through the flat tubes of the corrugated-fin heat exchanger 10a. Subsequently, the air is blown out through the air outlet 32a to the outside of the outdoor-unit main body 30a.
- an air outlet 32b is provided in an upper surface of an outdoor-unit main body 30b.
- a corrugated-fin heat exchanger 10b having a U-shape in plan view is mounted to the outdoor unit, and air inlets 33b are provided in side surfaces of the outdoor-unit main body 30b that are opposed to the corrugated-fin heat exchanger 10b.
- the air With a flow of air that is generated by the fan 31, the air is sucked into the outdoor-unit main body 30b through the air inlets 33b, and flows through the corrugated-fin heat exchanger 10b. At this time, heat is exchanged between the air and refrigerant sent from the indoor unit (not shown), compressed in the compressor 34, and then flowing through the flat tubes of the corrugated-fin heat exchanger 10b. Subsequently, the air is blown out through the air outlet 32b to the outside of the outdoor-unit main body 30b.
- the air flows into the corrugated-fin heat exchanger 10, exchanges heat with the refrigerant flowing through the flat tubes 1 when the air flows through the heat-exchanger air passages, and flows out from the corrugated-fin heat exchanger 10.
- refrigerant that is returned after exchanging heat with air in the indoor unit to transfer heat to be liquefied and then being decompressed into a low-temperature and low-pressure two-phase gas-liquid state flows into the corrugated-fin heat exchanger 10 serving as an evaporator, which is mounted to the outdoor unit, through the inlet header 3.
- the refrigerant flows through the flat tubes 1, exchanges heat with air flowing through the heat-exchanger air passages to receive heat to be evaporated, then flows out through the outlet header 4, and flows into the indoor unit again. In this manner, the refrigerant circulates in the refrigeration circuit.
- the heat of the air flowing through the heat-exchanger air passages is removed by the flat tubes 1 through the corrugated fins 2, and water vapor in the air is brought into a supersaturated state. Then, the supersaturated water vapor is condensed on surfaces of the flat tubes 1 and the corrugated fins 2 to turn into water.
- the first lug portions 7 are formed in the radial direction extending from the flat tubes 1 toward the center of the windward-side end portion (front-side end portion) of the protruding portion 5.
- FIG. 7 is a perspective view for illustrating drainage passages of the corrugated-fin heat exchanger 10 according to Embodiment 1 of the present invention.
- the arrows DFa and DFb in FIG. 7 indicate flows of water in a drainage process.
- the corrugated-fin heat exchanger 10 has two drainage passages.
- the first passage is a passage for water flowing through the slits, which are formed in the protruding surface of the corrugated fin 2 in the course of forming the first lug portions 7, as indicated by the arrows DFb.
- the second passage is a passage for water flowing from the protruding portion 5 through the vicinity of the apex 2a of the corrugated fin 2 along the flat tube 1, as indicated by the arrows DFa.
- the first lug portions 7 are formed in the radial direction extending from the flat tubes 1 toward the center of the windward-side end portion (front-side end portion) of the protruding portion 5.
- drainage of water flowing along the flat tubes 1 is promoted by the air guiding action of the first lug portions 7.
- the fan 31 is stopped and the refrigeration cycle is switched to a cooling operation, or other measures are taken so that high-temperature refrigerant is caused to flow into the corrugated-fin heat exchanger 10. In this manner, the frost adhering to each of the surfaces of the flat tubes 1 and the corrugated fins 2 is melted.
- the melted frost turns into water and flows along the surfaces of the flat tubes 1. Further, the water flows through the slits, which are formed in the protruding surface of the corrugated fin 2 in the course of forming the first lug portions 7, to thereby be drained to the lower part of the corrugated-fin heat exchanger 10. After the defrosting is completed, the heating operation is started again.
- the lug portions when the lug portions are formed in the corrugated fins 2, the lug portions, specifically, the slits formed in the course of forming the lug portions divide heat transfer passages from a leeward side (back side) that is a side at the position of the flat tube 1, through which the refrigerant flows, to the windward side (front side), with the result that the fin efficiency (thermal conductivity in the fins) is lowered.
- the first lug portions 7 are formed in the protruding portion 5 in the radial direction extending from the flat tubes 1 toward the center portion of the windward-side end portion (front-side end portion) of the protruding portion 5. Consequently, the heat transfer passages are less likely to be divided by the lug portions as compared to the case where the lug portions are formed in the airflow orthogonal direction (right-and-left direction).
- an interval is secured between the right and left first lug portions 7.
- FIG. 8 is a view for illustrating a modification example of the corrugated-fin heat exchanger 10 according to Embodiment 1 of the present invention.
- FIG. 8 is a sectional view taken along the line A-A of FIG. 2 similarly to FIG. 3 .
- the number of the first lug portions 7 is two. However, the number of the first lug portions 7 is not limited to two, and the number of the first lug portions 7 may be one. Further, as illustrated in FIG. 8 , three or more first lug portions 7 may be formed in the radial direction extending from the flat tubes 1 toward the center portion of the windward-side end portion (front-side end portion) of the protruding portion 5.
- the drainage performance is enhanced with the action of guiding air to the flat tubes 1 serving as the drainage passages during the heating operation. Further, the heat transfer is promoted during the normal operation by the effect of front edges of the lug portions without degrading the defrosting performance during the defrosting operation, thereby being capable of enhancing the heating performance.
- FIGS. 9 are views for illustrating a first modification example of the first lug portions 7 of the corrugated-fin heat exchanger 10 according to Embodiment 1 of the present invention.
- FIGS. 10 are views for illustrating a second modification example of the first lug portions 7 of the corrugated-fin heat exchanger 10 according to Embodiment 1 of the present invention.
- FIGS. 11 are views for illustrating a third modification example of the first lug portions 7 of the corrugated-fin heat exchanger 10 according to Embodiment 1 of the present invention.
- FIGS. 12 are views for illustrating a fourth modification example of the first lug portions 7 of the corrugated-fin heat exchanger 10 according to Embodiment 1 of the present invention.
- a part (a) is a perspective view of a modification example of the first lug portions 7, and a part (b) is a sectional view taken along the line B-B of the part (a).
- the first modification example of the first lug portions 7 according to Embodiment 1 is of a slit type of being lugged (raised) in one direction (upward direction) from the protruding surface of the corrugated fin 2.
- the heat transfer performance is degraded as compared to the louver type illustrated in FIGS. 6 .
- the second modification example of the first lug portions 7 according to Embodiment 1 is of a type of being simply folded back in in one direction (upward direction) from the protruding surface of the corrugated fin 2 and lugged into a rectangular shape in plan view.
- the heat transfer performance is degraded as compared to the louver type illustrated in FIGS. 6 and the slit type illustrated in FIGS. 9 .
- the slits can be formed relatively easily, thereby attaining simplification of manufacture.
- the third modification example of the first lug portions 7 according to Embodiment 1 is of a type of being folded back in the one direction (upward direction) from the protruding surface of the corrugated fin 2 and lugged into a triangular shape in plan view, in which the lugged portions are reduced in height toward the windward-side end portion (front-side end portion) of the protruding portion 5.
- the first lug portions 7c illustrated in FIGS. 11 are increased in area to promote heat transfer by the effect of the front edges of the lug portions, that is, the first lug portions. Consequently, in the third modification example, the effect of promoting the heat transfer by the lug portions can be obtained more than the second modification example.
- the fourth modification example of the first lug portions 7 according to Embodiment 1 is of a slit type in which one slit is formed in the protruding surface of the corrugated fin 2, and the protruding surface of the corrugated fin 2 is not raised with the slit or is raised with the slit to a small extent to form a cutout.
- the first lug portions 7d illustrated in FIGS. 12 are small lug portions, and hence the effect of the heat transfer promotion by the lug portions is small. However, intervals formed by the fin can be prevented from being small, thereby being capable of preventing the degradation of the heating performance due to closure of the heat-exchanger air passages caused by the frost formation.
- water generated during the defrosting operation can be drained to the lower part of the corrugated-fin heat exchanger 20 through the slits that are formed in the protruding surface of the corrugated fin 2 in the course of forming the first lug portions 7d. That is, drainage passages for water to be drained can be secured with the slits.
- the slits of the first lug portions 7d are small, and hence the heat transfer passages are less likely to be divided. As a result, heat can sufficiently be transferred to the windward-side end portion (front-side end portion) of the protruding portion 5 and the first lug portions 7d during the defrosting operation, thereby being capable of preventing the degradation of the defrosting performance. That is, the time period required for the defrosting can be prevented from being prolonged.
- FIG. 13 is a view for illustrating a fifth modification example of the first lug portions 7 of the corrugated-fin heat exchanger 10 according to Embodiment 1 of the present invention.
- FIGS. 14 are enlarged front views of the flat tubes 1 and the corrugated fins 2, for illustrating a modification example of the corrugated fins 2 of the corrugated-fin heat exchanger 10 according to Embodiment 1 of the present invention.
- FIG. 13 is a front view of the corrugated fin 2 and the first lug portions 7 of the corrugated-fin heat exchanger 10.
- the corrugated fins 2 are each sandwiched by the adjacent flat tubes 1 and thermally connected to the flat tubes 1 at each apex 2a.
- the fifth modification example of the first lug portions 7 according to Embodiment 1 corresponds to the two first lug portions 7e formed on the right and left sides of the center portion (of the protruding portion 5) of the corrugated fin 2 in the airflow orthogonal direction (right-and-left direction).
- the first lug portion 7e1 on the left side is lugged from the surface of the corrugated fin 2 in the downward direction
- the first lug portion 7e2 on the right side is lugged from the surface of the corrugated fin 2 in the upward direction. That is, the first lug portions 7e are lugged toward an outer peripheral side at the vicinity of each apex 2a of the corrugated fin 2.
- the intervals formed by the fin are smaller on the inner peripheral side at the vicinity of each apex 2a.
- the first lug portions 7e are lugged toward the outer peripheral side on which the intervals formed by the fin are larger, so that air flows satisfactorily at portions at which the first lug portions 7e are formed. That is, by forming the first lug portions 7e toward the outer peripheral side at the vicinity of each apex 2a of the corrugated fin 2, increase in airflow resistance can be prevented as compared to a case where the first lug portions 7e are formed toward the inner peripheral side, thereby being capable of preventing the degradation of the heating performance.
- an interval is secured between the right and left first lug portions 7e.
- the two first lug portions 7 are formed in the protruding portion 5 on the right and left sides to promote heat transfer. Further, the first lug portions 7 are formed in the radial direction extending from the flat tubes 1 toward the center portion of the windward-side end portion (front-side end portion) of the protruding portion 5.
- the first lug portions 7 are oriented obliquely to the airflow direction (front-and-back direction).
- the lug portions are formed in the airflow orthogonal direction (right-and-left direction)
- water is easily drained with the action of guiding air to the flat tubes 1 serving as the drainage passages, and further, the heat transfer passages are less likely to be divided by the lug portions.
- the drainage performance is enhanced during the heating operation.
- heat can sufficiently be transferred to the windward-side end portion (front-side end portion) of the protruding portion 5 and the first lug portions 7, thereby being capable of preventing the degradation of the defrosting performance. That is, the time period required for the defrosting can be prevented from being prolonged.
- an interval is secured between the right and left first lug portions 7.
- the flat tubes 1 serving as the drainage passages extending in the up-and-down direction and the meandering corrugated fins 2 each sandwiched by the adjacent flat tubes 1 and thermally joined to the flat tubes 1.
- the shape of each of the apexes of the corrugated fins 2 that are joined to the flat tubes 1 is an arc shape.
- the shape may be a flat shape, and in this case, the joined area is increased to promote thermal conduction.
- the corrugated fins 2 may each have a shape having surfaces perpendicular to the flat tubes 1, that is, a shape having the surfaces perpendicular to the flat tubes 1 and parallel to one another. With this shape, the pitches of the corrugated fins 2 (interval between the adjacent apexes 2a) can be reduced to increase the mounting area, thereby enhancing the heat exchange performance.
- Embodiment 2 of the present invention is described below. Description of the same components as those of Embodiment 1 is omitted or partly omitted. The parts same as or corresponding to those of Embodiment 1 are denoted by the same reference signs.
- FIG. 15 is a perspective view for illustrating a corrugated-fin heat exchanger 20 according to Embodiment 2 of the present invention.
- FIG. 16 is an enlarged front view of the flat tubes 1 and the corrugated fins 2 of the corrugated-fin heat exchanger 20 according to Embodiment 2 of the present invention.
- FIG. 17 is a sectional view taken along the line C-C of FIG. 16 .
- the plurality of flat tubes 1 that are arranged in the airflow orthogonal direction (right-and-left direction) orthogonal to the airflow direction (front-and-back direction) indicated by the arrow WF are provided in two rows in the airflow direction (front-and-back direction).
- Each flat tube 1 extends along the up-and-down direction.
- the meandering corrugated fins 2 each sandwiched by the adjacent flat tubes 1 in the airflow orthogonal direction (right-and-left direction) and thermally connected to the flat tubes 1 at each apex 2a.
- the inlet header 3 is connected to one end (lower end) of each flat tube 1 on the windward side (front side)
- the outlet header 4 is connected to one end (lower end) of each flat tube 1 on the leeward side (back side).
- An intermediate header 11 is connected to the other end (upper end) of each flat tube 1 on the windward side (front side) and the other end (upper end) of each flat tube 1 on the leeward side (back side). Heat is exchanged between refrigerant flowing through the flat tubes 1 and air flowing through the spaces in each of the fins of the corrugated fins 2.
- each of the corrugated fins 2 there is formed the protruding portion 5 protruding to the windward side (front side) with respect to the windward-side end portions (front-side end portions) 1a of the flat tubes 1. Further, the plurality of lug portions are formed in the corrugated fin 2 to promote heat transfer.
- the two first lug portions 7 that are formed to be inclined (oblique) to the airflow direction (front-and-back direction) are provided on the right and left sides.
- the first lug portions 7 are oriented obliquely in the same direction with respect to the airflow direction (front-and-back direction).
- the second lug portions 6 formed in the airflow orthogonal direction (right-and-left direction), and the five second lug portions 6 are formed to be arrayed in the airflow direction (front-and-back direction).
- the corrugated-fin heat exchanger 20 is mounted to the outdoor unit of the air-conditioning apparatus including the fan 31, thereby constructing a refrigeration cycle for circulating refrigerant between the outdoor unit and an indoor unit connected to the outdoor unit by pipes.
- the air flows into the corrugated-fin heat exchanger 20, exchanges heat with the refrigerant flowing through the flat tubes 1 when the air flows through the heat-exchanger air passages, and flows out from the corrugated-fin heat exchanger 20.
- refrigerant that is returned after exchanging heat with air in the indoor unit to transfer heat to be liquefied and then being decompressed into a low-temperature and low-pressure two-phase gas-liquid state flows into the corrugated-fin heat exchanger 20 serving as an evaporator, which is mounted to the outdoor unit, through the inlet header 3.
- the refrigerant flows through the flat tubes 1 on the windward side (front side), flows through the flat tubes 1 on the leeward side (back side) through the intermediate header 11, exchanges heat with air flowing through the heat-exchanger air passages to receive heat to be evaporated, then flows out through the outlet header 4, and flows into the indoor unit again. In this manner, the refrigerant circulates in the refrigeration circuit.
- FIG. 18 is a view for illustrating a state of frost formation on the flat tubes 1 and the corrugated fins 2 during the heating operation in the corrugated-fin heat exchanger 20 according to Embodiment 2 of the present invention.
- FIG. 19 is a view for illustrating a state of frost formation on the flat tubes 1 and the corrugated fins 2 during the defrosting operation in the corrugated-fin heat exchanger 20 according to Embodiment 2 of the present invention.
- FIG. 20 is a perspective view for illustrating drainage passages of the corrugated-fin heat exchanger 20 according to Embodiment 2 of the present invention.
- FIG. 18 and FIG. 19 are sectional views taken along the line C-C of FIG. 16 similarly to FIG. 17 .
- the arrows DFa, DFb, DFc, and DFd of FIG. 20 indicate the flows of water during the defrosting operation.
- the amount of formed frost is small at a portion on the corrugated fin 2 at which the airflow velocity is low in the airflow velocity distribution, and the amount of formed frost is large at a portion on the corrugated fin 2 at which the airflow velocity is high in the airflow velocity distribution.
- the airflow velocity distribution is formed in a direction to which an airflow direction is slightly bent toward the airflow orthogonal direction (right-and-left direction) with the air guiding action by the first lug portions 7.
- frost is formed to be dispersed in the front-and-back direction (airflow direction).
- the amount of formed frost is small.
- the first lug portions 7 are inclined to the airflow direction (front-and-back direction) and extend along with an inclination direction of each surface of the meandering corrugated fin 2, and the first lug portions 7 are alternately inclined to directions horizontally opposite to each other in the up-and-down direction. That is, a first lug portion 7 ⁇ that is inclined in the left direction from the windward side (front side) to the leeward side (back side) is formed in a surface of the corrugated fin 2 that is inclined from the right side to the left side. Further, a first lug portion 7 ⁇ that is inclined in the right direction from the windward side (front side) to the leeward side (back side) is formed in a surface of the corrugated fin 2 that is inclined from the left side to the right side.
- the frost on the frost formation portion 40 illustrated in FIG. 18 is melted into water during the defrosting operation. Consequently, to drain the water to the lower part of the corrugated-fin heat exchanger 10, the drainage passages are formed in the corrugated-fin heat exchanger 20 as illustrated in FIG. 20 .
- the two drainage passages are provided.
- the first passage is a passage for water flowing through the slits formed in the protruding surface of the corrugated fin 2 in the course of forming the first lug portions 7, as indicated by the arrow DFc and the arrow DFd.
- the second passage is a passage for water flowing from the protruding portion 5 to the vicinity of the apex 2a of the corrugated fin 2 and flowing through a part between the flat tube 1 on the windward side (front side) and the flat tube 1 on the leeward side (back side), as indicated by the arrow DFa and the arrow DFb.
- the first lug portions 7 are provided to be inclined to the airflow direction (front-and-back direction) and to extend along with the inclination direction of the meandering corrugated fin 2.
- the gravity water is easily guided to the part between the flat tube 1 on the windward side (front side) and the flat tube 1 on the leeward side (back side).
- the flat tubes 1 are provided in two rows in the airflow direction (front-and-back direction). Consequently, in addition to the passage for water flowing through the slits and the passage for water flowing along the flat tube 1, there is formed the passage for water flowing through the part between the flat tube 1 on the windward side (front side) and the flat tube 1 on the leeward side (back side).
- the drainage performance can further be enhanced with the above-mentioned air guiding action.
- the enhancement of the drainage performance with the air guiding action exerts the effect to promote drainage of water to the flat tubes 1 not only during the defrosting operation but also during the normal heating operation even in a case where dew condensation occurs on the surfaces of the flat tubes 1 or the corrugated fins 2.
- the amount of formed frost is relatively small, and hence the influence of the degradation of the defrosting performance is small. Further, the air guiding action is promoted as compared to Embodiment 1, and an effect of being capable of prolonging a time period until the defrosting operation is performed is more significant.
- FIG. 21 is a sectional view taken along the line D-D of FIG. 17 .
- the thickness of the center portion of the corrugated fin 2 in the airflow orthogonal direction is formed larger than those of other portions (both right and left end portions).
- the thickness of the corrugated fin 2 is varied only at the windward-side end portion (front-side end portion) of the protruding portion 5 as described above is most efficient.
- the thickness of the corrugated fin 2 may be entirely varied in the same manner in the airflow direction (front-and-back direction).
- frost is formed on a part of the corrugated fin 2 on the leeward side (back side)
- the defrosting performance can be enhanced.
- the two first lug portions 7 are formed in the protruding portion 5 on the right and left sides to promote heat transfer.
- the first lug portions 7 are oriented obliquely in the same direction with respect to the airflow direction (front-and-back direction).
- the air guiding action is promoted as compared to Embodiment 1, thereby being capable of prolonging the time period until the defrosting operation is performed.
- the flat tubes 1 are provided in two rows in the airflow direction (front-and-back direction).
- the passage for water flowing through the part between the flat tube 1 on the windward side (front side) and the flat tube 1 on the leeward side (back side) is formed.
- the thickness of the center portion of the corrugated fin 2 in the airflow orthogonal direction is formed larger than those of other portions (both right and left end portions), and hence, during the defrosting operation, the fin efficiency can be enhanced substantially equally to that in the case where the entire thickness of the fin is increased. Consequently, heat can sufficiently be transferred to the windward-side end portion (front-side end portion) of the protruding portion 5 and the first lug portions 7, thereby being capable of preventing the degradation of the defrosting performance. That is, the time period required for the defrosting can be prevented from being prolonged.
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Description
- The present invention relates to a heat exchanger that is to be used in air-conditioning apparatuses such as a room air-conditioning apparatus and a package air-conditioning apparatus, and to an air-conditioning apparatus including the heat exchanger.
- There has been the following problem in a related-art corrugated-fin heat exchanger mounted to an outdoor unit of an air-conditioning apparatus. During a heating operation, heat of air flowing through air passages is removed by flat tubes through corrugated fins, so that water vapor in the air is brought into a supersaturated state. When surface temperatures of the flat tubes and the corrugated fins are 0 °C or less, the supersaturated water vapor turns into ice, and frost is formed on surfaces of the flat tubes and the corrugated fins. When the frost formation proceeds, spaces formed by each fin are closed, with the result that airflow resistance increases to degrade heating performance.
- To solve this problem, there has been proposed a corrugated-fin heat exchanger in which the corrugated fins partially protrude to a windward side with respect to windward-side end portions of the flat tubes (see, for example, Patent Literature 1).
EP-A-0021651 discloses a similar heat exchanger. - In the corrugated-fin heat exchanger disclosed in
Patent Literature 1, the protruding portions of the corrugated fins, which protrude to the windward side with respect to the windward-side end portions of the flat tubes, have a large heat-transfer distance from the flat tubes. Consequently, the fin efficiency (thermal conductivity in the fins) is lowered, so that the surface temperature of the corrugated fins is less likely to be lowered. Thus, the amount of formed frost is reduced, thereby being capable of preventing the spaces formed by each fin from being closed. - Patent Literature 1: Japanese Unexamined Patent Application Publication
JP 6-147 785 A - In the related-art corrugated-fin heat exchanger as disclosed in
Patent Literature 1, when lug portions formed in an airflow orthogonal direction are provided on the protruding portions of the corrugated fins to promote heat transfer (promote heat transfer between the fins and air), the fin efficiency is further lowered, thereby preventing frost formation on the lug portions. - However, there has been a problem in that, in a case where frost is once formed on the protruding portions or the lug portions of the corrugated fins, when the frost is melted by refrigerant heat during a defrosting operation, heat is less likely to be transferred from the flat tubes to the frost through the corrugated fins, with the result that the defrosting performance is degraded.
- The present invention has been made to solve the above-mentioned problem and has an object to provide a heat exchanger and an air-conditioning apparatus that are capable of preventing degradation of defrosting performance while promoting heat transfer.
- According to one embodiment of the present invention, there is provided a heat exchanger according to
claim 1. Advantageous embodiments of the invention are defined in claims 2-8. - In the heat exchanger of one embodiment of the present invention, the corrugated fin includes the protruding portion protruding to the front side with respect to the front-side end portion of each of the flat tubes. The protruding portion includes the (first) lug portion to promote heat transfer. The lug portion is oriented obliquely to the front-and-back direction that is the airflow direction.
- Consequently, a heat transfer passage is less likely to be divided by the lug portion during a defrosting operation as compared to a case where the lug portion is formed in the airflow orthogonal direction. As a result, heat can sufficiently be transferred to the protruding portion and the lug portion of the corrugated fin, thereby being capable of preventing the degradation of the defrosting performance.
-
- FIG. 1
- is a perspective view for illustrating a corrugated-fin heat exchanger according to
Embodiment 1 of the present invention. - FIG. 2
- is an enlarged front view of flat tubes and corrugated fins of the corrugated-fin heat exchanger according to
Embodiment 1 of the present invention. - FIG. 3
- is a sectional view taken along the line A-A of
FIG. 2 . - FIG. 4
- is a schematic view for illustrating an outdoor unit (side-flow type) of an air-conditioning apparatus according to
Embodiment 1 of the present invention. - FIG. 5
- is a schematic view for illustrating an outdoor unit (top-flow type) of the air-conditioning apparatus according to
Embodiment 1 of the present invention. - FIGS. 6
- are views for illustrating first lug portions of the corrugated-fin heat exchanger according to
Embodiment 1 of the present invention. - FIG. 7
- is a perspective view for illustrating drainage passages of the corrugated-fin heat exchanger according to
Embodiment 1 of the present invention. - FIG. 8
- is a view for illustrating a modification example of the corrugatedfin heat exchanger according to
Embodiment 1 of the present invention. - FIGS. 9
- are views for illustrating a first modification example of the first lug portions of the corrugated-fin heat exchanger according to
Embodiment 1 of the present invention. - FIGS. 10
- are views for illustrating a second modification example of the first lug portions of the corrugated-fin heat exchanger according to
Embodiment 1 of the present invention. - FIGS. 11
- are views for illustrating a third modification example of the first lug portions of the corrugated-fin heat exchanger according to
Embodiment 1 of the present invention. - FIGS. 12
- are views for illustrating a fourth modification example of the first lug portions of the corrugated-fin heat exchanger according to
Embodiment 1 of the present invention. - FIG. 13
- is a view for illustrating a fifth modification example of the first lug portions of the corrugated-fin heat exchanger according to
Embodiment 1 of the present invention. - FIGS. 14
- are enlarged front views of the flat tubes and the corrugated fins, for illustrating a modification example of the corrugated fins of the corrugated-fin heat exchanger according to
Embodiment 1 of the present invention. - FIG. 15
- is a perspective view for illustrating a corrugated-fin heat exchanger according to
Embodiment 2 of the present invention. - FIG. 16
- is an enlarged front view of the flat tubes and the corrugated fins of the corrugated-fin heat exchanger according to
Embodiment 2 of the present invention. - FIG. 17
- is a sectional view taken along the line C-C of
FIG. 16 . - FIG. 18
- is a view for illustrating a state of frost formation on the flat tubes and the corrugated fins during a heating operation in the corrugatedfin heat exchanger according to
Embodiment 2 of the present invention. - FIG. 19
- is a view for illustrating a state of frost formation on the flat tubes and the corrugated fins during the defrosting operation in the corrugated-fin heat exchanger according to
Embodiment 2 of the present invention. - FIG. 20
- is a perspective view for illustrating drainage passages of the corrugated-fin heat exchanger according to
Embodiment 2 of the present invention. - FIG. 21
- is a sectional view taken along the line D-D of
FIG. 17 . - Embodiments of the present invention are described below with reference to the drawings. The present invention is not limited to Embodiments described below. Moreover, in the drawings referred to below, the size relationship of components may be different from the actual size relationship in some cases.
-
FIG. 1 is a perspective view for illustrating a corrugated-fin heat exchanger 10 according toEmbodiment 1 of the present invention. Further,FIG. 2 is an enlarged front view offlat tubes 1 andcorrugated fins 2 of the corrugated-fin heat exchanger 10 according toEmbodiment 1 of the present invention. The arrow WF inFIG. 1 indicates a flow of air (airflow direction) generated by a fan 31 (seeFIG. 4 andFIG. 5 described later) or other units, and the arrow RF indicates a flow of refrigerant. The same arrows are used in the drawings described later. Further, the expressions "up", "down", "left", "right", "front", and "back" used inEmbodiment 1 indicate directions that are given when the corrugated-fin heat exchanger 10 is viewed from the front side unless otherwise noted. - As illustrated in
FIG. 1 and FIG. 2 , the corrugated-fin heat exchanger 10 according toEmbodiment 1 includes the plurality offlat tubes 1 arranged in an airflow orthogonal direction (right-and-left direction) orthogonal to the airflow direction (front-and-back direction) indicated by the arrow WF, the meanderingcorrugated fins 2 each sandwiched by the adjacentflat tubes 1 and thermally connected to theflat tubes 1 at each apex 2a, aninlet header 3 connected to one end (lower end) of eachflat tube 1, and anoutlet header 4 connected to the other end (upper end) of eachflat tube 1. - The corrugated-
fin heat exchanger 10 exchanges heat between refrigerant flowing through theflat tubes 1 and air flowing through spaces each surrounded by the adjacentflat tubes 1 and the corrugated fin 2 (hereinafter referred to as "heat-exchanger air passages"). Eachflat tube 1 extends along an up-and-down direction. - The
corrugated fins 2 are each a metal thin plate shaped to have peaks and troughs that areapexes 2a alternately as viewed from one side. The peaks of thecorrugated fin 2 are joined to a surface of oneflat tube 1 of the twoflat tubes 1 adjacent in the airflow orthogonal direction (right-and-left direction), and the troughs of thecorrugated fin 2 are joined to a surface of the otherflat tube 1. The peaks and the troughs of thecorrugated fin 2 have a shape extending in the airflow direction (front-and-back direction). - Consequently, joined portions between the
corrugated fin 2 and theflat tube 1 each have a linear shape being continuous in the airflow direction (front-and-back direction). The joined portions each have a width enough for the joining. Further, when the peaks and the troughs have flat surfaces, and the flat surfaces are joined to theflat tubes 1, the joined portions between thecorrugated fins 2 and theflat tubes 1 each have a wide linear shape. -
FIG. 3 is a sectional view of the corrugated-fin heat exchanger 10 according toEmbodiment 1 of the present invention that is taken along the line A-A ofFIG. 2 . Further,FIGS. 6 are views for illustratingfirst lug portions 7 of the corrugated-fin heat exchanger 10 according toEmbodiment 1 of the present invention. InFIGS. 6 , a part (a) is a perspective view of thefirst lug portions 7, and a part (b) is a sectional view taken along the line B-B of the part (a). - As illustrated in
FIG. 3 , on a windward side (front side) of each of thecorrugated fins 2, there is formed a protrudingportion 5 protruding to a windward side (front side) with respect to windward-side end portions (front-side end portions) 1a of theflat tubes 1. Further, a plurality of lug portions are formed in thecorrugated fin 2 to promote heat transfer (promote heat transfer between fin and air). - The
first lug portions 7 are formed in the protrudingportion 5 in a radial direction extending from theflat tubes 1 toward a center portion of a windward-side end portion (front-side end portion) of the protrudingportion 5. Thosefirst lug portions 7 formed to be inclined (oblique) to the airflow direction (front-and-back direction) are provided such that the twofirst lug portions 7 are arranged in a bilaterally symmetrical manner. - As illustrated in
FIGS. 6 , thefirst lug portions 7 are each of a louver type in which two slits (cut lines) are formed in the surface of the protruding portion 5 (hereinafter referred to as "protruding surface") of thecorrugated fin 2, and thefirst lug portions 7 are each lugged from the two slits in the protruding surface of thecorrugated fin 2 in both the up and down directions. - Further, on a part of the
corrugated fin 2 other than the protrudingportion 5, that is, the part sandwiched by the adjacentflat tubes 1, there are providedsecond lug portions 6 formed in the airflow orthogonal direction (right-and-left direction), and the fivesecond lug portions 6 are formed to be arrayed in the airflow direction (front-and-back direction). -
FIG. 4 is a schematic view for illustrating an outdoor unit (side-flow type) of an air-conditioning apparatus according toEmbodiment 1 of the present invention. Further,FIG. 5 is a schematic view for illustrating an outdoor unit (top-flow type) of the air-conditioning apparatus according toEmbodiment 1 of the present invention.FIG. 4 andFIG. 5 are also referred to inEmbodiment 2 described later. - As illustrated in
FIG. 4 andFIG. 5 , the corrugated-fin heat exchanger 10 is mounted to the outdoor unit of the air-conditioning apparatus including thefan 31, thereby constructing a refrigeration cycle for circulating refrigerant between the outdoor unit and an indoor unit connected to the outdoor unit by pipes. - As the outdoor unit in which the corrugated-
fin heat exchanger 10 is mounted, a side-flow type illustrated inFIG. 4 and a top-flow type illustrated inFIG. 5 are given. - In the outdoor unit of the side-flow type, as illustrated in
FIG. 4 , anair outlet 32a is provided in a side surface of an outdoor-unitmain body 30a on a front surface side. Further, a corrugated-fin heat exchanger 10a having an L-shape in plan view is mounted to the outdoor unit, andair inlets 33a are provided in side surfaces of the outdoor-unitmain body 30a that are opposed to the corrugated-fin heat exchanger 10a. - With a flow of air that is generated by the
fan 31, the air is sucked into the outdoor-unitmain body 30a through theair inlets 33a, and flows through the corrugated-fin heat exchanger 10a. At this time, heat is exchanged between the air and refrigerant sent from the indoor unit (not shown), compressed in acompressor 34, and then flowing through the flat tubes of the corrugated-fin heat exchanger 10a. Subsequently, the air is blown out through theair outlet 32a to the outside of the outdoor-unitmain body 30a. - Further, in the outdoor unit of the top-flow type, as illustrated in
FIG. 5 , anair outlet 32b is provided in an upper surface of an outdoor-unitmain body 30b. Further, a corrugated-fin heat exchanger 10b having a U-shape in plan view is mounted to the outdoor unit, andair inlets 33b are provided in side surfaces of the outdoor-unitmain body 30b that are opposed to the corrugated-fin heat exchanger 10b. - With a flow of air that is generated by the
fan 31, the air is sucked into the outdoor-unitmain body 30b through theair inlets 33b, and flows through the corrugated-fin heat exchanger 10b. At this time, heat is exchanged between the air and refrigerant sent from the indoor unit (not shown), compressed in thecompressor 34, and then flowing through the flat tubes of the corrugated-fin heat exchanger 10b. Subsequently, the air is blown out through theair outlet 32b to the outside of the outdoor-unitmain body 30b. - Next, an operation of the corrugated-
fin heat exchanger 10 according toEmbodiment 1 is described. - As illustrated in
FIG. 1 , with the flow of air that is generated by thefan 31, the air flows into the corrugated-fin heat exchanger 10, exchanges heat with the refrigerant flowing through theflat tubes 1 when the air flows through the heat-exchanger air passages, and flows out from the corrugated-fin heat exchanger 10. - Next, the flow of the refrigerant is described.
- During a heating operation, refrigerant that is returned after exchanging heat with air in the indoor unit to transfer heat to be liquefied and then being decompressed into a low-temperature and low-pressure two-phase gas-liquid state flows into the corrugated-
fin heat exchanger 10 serving as an evaporator, which is mounted to the outdoor unit, through theinlet header 3. - Then, the refrigerant flows through the
flat tubes 1, exchanges heat with air flowing through the heat-exchanger air passages to receive heat to be evaporated, then flows out through theoutlet header 4, and flows into the indoor unit again. In this manner, the refrigerant circulates in the refrigeration circuit. - During the heating operation, the heat of the air flowing through the heat-exchanger air passages is removed by the
flat tubes 1 through thecorrugated fins 2, and water vapor in the air is brought into a supersaturated state. Then, the supersaturated water vapor is condensed on surfaces of theflat tubes 1 and thecorrugated fins 2 to turn into water. - Part of this water flows along the surfaces of the
flat tubes 1, and part of this water flows through the slits formed in the protruding surface of thecorrugated fin 2, to be drained to a lower part of the corrugated-fin heat exchanger 10. In this case, when the amount of condensed dew is large, or the drainage performance is poor, water stagnates in spaces formed by the fin of thecorrugated fin 2, so that the heat-exchanger air passages are closed. - As a result, the performance of the corrugated-
fin heat exchanger 10 is degraded, thereby leading to degradation of heating performance. To solve this problem, in the corrugated-fin heat exchanger 10 according toEmbodiment 1, thefirst lug portions 7 are formed in the radial direction extending from theflat tubes 1 toward the center of the windward-side end portion (front-side end portion) of the protrudingportion 5. -
FIG. 7 is a perspective view for illustrating drainage passages of the corrugated-fin heat exchanger 10 according toEmbodiment 1 of the present invention. The arrows DFa and DFb inFIG. 7 indicate flows of water in a drainage process. - As illustrated in
FIG. 7 , the corrugated-fin heat exchanger 10 has two drainage passages. The first passage is a passage for water flowing through the slits, which are formed in the protruding surface of thecorrugated fin 2 in the course of forming thefirst lug portions 7, as indicated by the arrows DFb. The second passage is a passage for water flowing from the protrudingportion 5 through the vicinity of the apex 2a of thecorrugated fin 2 along theflat tube 1, as indicated by the arrows DFa. - In the second passage, the
first lug portions 7 are formed in the radial direction extending from theflat tubes 1 toward the center of the windward-side end portion (front-side end portion) of the protrudingportion 5. Thus, drainage of water flowing along theflat tubes 1 is promoted by the air guiding action of thefirst lug portions 7. - Further, when the surface temperatures of the
flat tubes 1 and thecorrugated fins 2 are 0 °C or less, supersaturated water vapor turns into ice, so that frost is formed on the surfaces. In particular, the effect of promoting the heat transfer is significant at the lug portions, and hence the amount of formed frost is large at the lug portions. - Next, when the performance of the corrugated-
fin heat exchanger 10 is degraded due to closure of the heat-exchanger air passages caused by frost formation in the corrugated-fin heat exchanger 10 or due to other factors, and the heating performance is degraded, a defrosting operation is started. - During the defrosting operation, normally, the
fan 31 is stopped and the refrigeration cycle is switched to a cooling operation, or other measures are taken so that high-temperature refrigerant is caused to flow into the corrugated-fin heat exchanger 10. In this manner, the frost adhering to each of the surfaces of theflat tubes 1 and thecorrugated fins 2 is melted. - Then, the melted frost turns into water and flows along the surfaces of the
flat tubes 1. Further, the water flows through the slits, which are formed in the protruding surface of thecorrugated fin 2 in the course of forming thefirst lug portions 7, to thereby be drained to the lower part of the corrugated-fin heat exchanger 10. After the defrosting is completed, the heating operation is started again. - In this case, when the lug portions are formed in the
corrugated fins 2, the lug portions, specifically, the slits formed in the course of forming the lug portions divide heat transfer passages from a leeward side (back side) that is a side at the position of theflat tube 1, through which the refrigerant flows, to the windward side (front side), with the result that the fin efficiency (thermal conductivity in the fins) is lowered. - As a result, during the defrosting operation, heat from the refrigerant cannot sufficiently be transferred to the windward-side end portion (front-side end portion) of the protruding
portion 5 and the lug portions, with the result that a time period required for the defrosting is prolonged. Meanwhile, when the heat-exchanger air passages are closed due to the frost formation, the heating performance is degraded. - To solve this problem, in the corrugated-
fin heat exchanger 10 according toEmbodiment 1, thefirst lug portions 7 are formed in the protrudingportion 5 in the radial direction extending from theflat tubes 1 toward the center portion of the windward-side end portion (front-side end portion) of the protrudingportion 5. Consequently, the heat transfer passages are less likely to be divided by the lug portions as compared to the case where the lug portions are formed in the airflow orthogonal direction (right-and-left direction). - As a result, during the defrosting operation, heat can sufficiently be transferred to the windward-side end portion (front-side end portion) of the protruding
portion 5 and thefirst lug portions 7, thereby being capable of preventing the degradation of the defrosting performance. That is, the time period required for the defrosting can be prevented from being prolonged. - Further, an interval is secured between the right and left
first lug portions 7. Thus, even when frost is formed on thefirst lug portions 7 during the defrosting operation, the heat-exchanger air passages can be secured, thereby being capable of preventing the degradation of the heating performance. - In the corrugated-
fin heat exchanger 10 ofEmbodiment 1, it is unnecessary to take a measure of, for example, increasing pitches of the corrugated fins 2 (interval between theadjacent apexes 2a) by sacrificing the performance during the normal operation, to achieve the above-mentioned effect. -
FIG. 8 is a view for illustrating a modification example of the corrugated-fin heat exchanger 10 according toEmbodiment 1 of the present invention.FIG. 8 is a sectional view taken along the line A-A ofFIG. 2 similarly toFIG. 3 . - In
Embodiment 1, the number of thefirst lug portions 7 is two. However, the number of thefirst lug portions 7 is not limited to two, and the number of thefirst lug portions 7 may be one. Further, as illustrated inFIG. 8 , three or morefirst lug portions 7 may be formed in the radial direction extending from theflat tubes 1 toward the center portion of the windward-side end portion (front-side end portion) of the protrudingportion 5. - When a large number of
first lug portions 7 are formed in this manner, the drainage performance is enhanced with the action of guiding air to theflat tubes 1 serving as the drainage passages during the heating operation. Further, the heat transfer is promoted during the normal operation by the effect of front edges of the lug portions without degrading the defrosting performance during the defrosting operation, thereby being capable of enhancing the heating performance. -
FIGS. 9 are views for illustrating a first modification example of thefirst lug portions 7 of the corrugated-fin heat exchanger 10 according toEmbodiment 1 of the present invention. Further,FIGS. 10 are views for illustrating a second modification example of thefirst lug portions 7 of the corrugated-fin heat exchanger 10 according toEmbodiment 1 of the present invention. Further,FIGS. 11 are views for illustrating a third modification example of thefirst lug portions 7 of the corrugated-fin heat exchanger 10 according toEmbodiment 1 of the present invention. - Further,
FIGS. 12 are views for illustrating a fourth modification example of thefirst lug portions 7 of the corrugated-fin heat exchanger 10 according toEmbodiment 1 of the present invention. In each ofFIGS. 9 to FIGS. 12 , a part (a) is a perspective view of a modification example of thefirst lug portions 7, and a part (b) is a sectional view taken along the line B-B of the part (a). - As illustrated in
FIGS. 9 , the first modification example of thefirst lug portions 7 according to Embodiment 1 (first lug portions 7a) is of a slit type of being lugged (raised) in one direction (upward direction) from the protruding surface of thecorrugated fin 2. - In the first modification example, the heat transfer performance is degraded as compared to the louver type illustrated in
FIGS. 6 . However, there are obtained effects of increasing the area of the raised portions of the slits (heat transfer area for promoting heat transfer) and increasing the strength of the fins. - Further, as illustrated in
FIGS. 10 , the second modification example of thefirst lug portions 7 according to Embodiment 1 (first lug portions 7b) is of a type of being simply folded back in in one direction (upward direction) from the protruding surface of thecorrugated fin 2 and lugged into a rectangular shape in plan view. - In the second modification example, the heat transfer performance is degraded as compared to the louver type illustrated in
FIGS. 6 and the slit type illustrated inFIGS. 9 . However, the slits can be formed relatively easily, thereby attaining simplification of manufacture. - Further, as illustrated in
FIGS. 11 , the third modification example of thefirst lug portions 7 according to Embodiment 1 (first lug portions 7c) is of a type of being folded back in the one direction (upward direction) from the protruding surface of thecorrugated fin 2 and lugged into a triangular shape in plan view, in which the lugged portions are reduced in height toward the windward-side end portion (front-side end portion) of the protrudingportion 5. - As compared to the
first lug portions 7b illustrated inFIGS. 10 , thefirst lug portions 7c illustrated inFIGS. 11 are increased in area to promote heat transfer by the effect of the front edges of the lug portions, that is, the first lug portions. Consequently, in the third modification example, the effect of promoting the heat transfer by the lug portions can be obtained more than the second modification example. - Further, as illustrated in
FIGS. 12 , the fourth modification example of thefirst lug portions 7 according to Embodiment 1 (first lug portions 7d) is of a slit type in which one slit is formed in the protruding surface of thecorrugated fin 2, and the protruding surface of thecorrugated fin 2 is not raised with the slit or is raised with the slit to a small extent to form a cutout. - The
first lug portions 7d illustrated inFIGS. 12 are small lug portions, and hence the effect of the heat transfer promotion by the lug portions is small. However, intervals formed by the fin can be prevented from being small, thereby being capable of preventing the degradation of the heating performance due to closure of the heat-exchanger air passages caused by the frost formation. - Further, water generated during the defrosting operation can be drained to the lower part of the corrugated-
fin heat exchanger 20 through the slits that are formed in the protruding surface of thecorrugated fin 2 in the course of forming thefirst lug portions 7d. That is, drainage passages for water to be drained can be secured with the slits. - Further, the slits of the
first lug portions 7d are small, and hence the heat transfer passages are less likely to be divided. As a result, heat can sufficiently be transferred to the windward-side end portion (front-side end portion) of the protrudingportion 5 and thefirst lug portions 7d during the defrosting operation, thereby being capable of preventing the degradation of the defrosting performance. That is, the time period required for the defrosting can be prevented from being prolonged. -
FIG. 13 is a view for illustrating a fifth modification example of thefirst lug portions 7 of the corrugated-fin heat exchanger 10 according toEmbodiment 1 of the present invention. Further,FIGS. 14 are enlarged front views of theflat tubes 1 and thecorrugated fins 2, for illustrating a modification example of thecorrugated fins 2 of the corrugated-fin heat exchanger 10 according toEmbodiment 1 of the present invention.FIG. 13 is a front view of thecorrugated fin 2 and thefirst lug portions 7 of the corrugated-fin heat exchanger 10. - The
corrugated fins 2 are each sandwiched by the adjacentflat tubes 1 and thermally connected to theflat tubes 1 at each apex 2a. - As illustrated in
FIG. 13 , the fifth modification example of thefirst lug portions 7 according to Embodiment 1 (first lug portions 7e) corresponds to the twofirst lug portions 7e formed on the right and left sides of the center portion (of the protruding portion 5) of thecorrugated fin 2 in the airflow orthogonal direction (right-and-left direction). - The first lug portion 7e1 on the left side is lugged from the surface of the
corrugated fin 2 in the downward direction, and the first lug portion 7e2 on the right side is lugged from the surface of thecorrugated fin 2 in the upward direction. That is, thefirst lug portions 7e are lugged toward an outer peripheral side at the vicinity of each apex 2a of thecorrugated fin 2. - In the
corrugated fins 2, the intervals formed by the fin are smaller on the inner peripheral side at the vicinity of each apex 2a. However, as illustrated inFIG. 13 , thefirst lug portions 7e are lugged toward the outer peripheral side on which the intervals formed by the fin are larger, so that air flows satisfactorily at portions at which thefirst lug portions 7e are formed. That is, by forming thefirst lug portions 7e toward the outer peripheral side at the vicinity of each apex 2a of thecorrugated fin 2, increase in airflow resistance can be prevented as compared to a case where thefirst lug portions 7e are formed toward the inner peripheral side, thereby being capable of preventing the degradation of the heating performance. - Further, an interval is secured between the right and left
first lug portions 7e. Thus, even when frost is formed on thefirst lug portions 7e during the defrosting operation, the heat-exchanger air passages can be secured, thereby being capable of preventing the degradation of the heating performance. - As described above, in the corrugated-
fin heat exchanger 10 ofEmbodiment 1, the twofirst lug portions 7 are formed in the protrudingportion 5 on the right and left sides to promote heat transfer. Further, thefirst lug portions 7 are formed in the radial direction extending from theflat tubes 1 toward the center portion of the windward-side end portion (front-side end portion) of the protrudingportion 5. - That is, the
first lug portions 7 are oriented obliquely to the airflow direction (front-and-back direction). With this configuration, as compared to a case where the lug portions are formed in the airflow orthogonal direction (right-and-left direction), water is easily drained with the action of guiding air to theflat tubes 1 serving as the drainage passages, and further, the heat transfer passages are less likely to be divided by the lug portions. As a result, the drainage performance is enhanced during the heating operation. - Further, during the defrosting operation, heat can sufficiently be transferred to the windward-side end portion (front-side end portion) of the protruding
portion 5 and thefirst lug portions 7, thereby being capable of preventing the degradation of the defrosting performance. That is, the time period required for the defrosting can be prevented from being prolonged. - Further, an interval is secured between the right and left
first lug portions 7. Thus, even when dew condensation or frost formation occurs on thefirst lug portions 7 during the defrosting operation, the heat-exchanger air passages can be secured, thereby being capable of preventing the degradation of the heating performance. - As basic configurations of the
flat tubes 1 and thecorrugated fins 2 of the corrugated-fin heat exchanger 10 according toEmbodiment 1, there are provided theflat tubes 1 serving as the drainage passages extending in the up-and-down direction and the meanderingcorrugated fins 2 each sandwiched by the adjacentflat tubes 1 and thermally joined to theflat tubes 1. InFIG. 2 , the shape of each of the apexes of thecorrugated fins 2 that are joined to theflat tubes 1 is an arc shape. - However, as illustrated in
FIG. 14(a) , the shape may be a flat shape, and in this case, the joined area is increased to promote thermal conduction. Further, as illustrated inFIG. 14(b) , thecorrugated fins 2 may each have a shape having surfaces perpendicular to theflat tubes 1, that is, a shape having the surfaces perpendicular to theflat tubes 1 and parallel to one another. With this shape, the pitches of the corrugated fins 2 (interval between theadjacent apexes 2a) can be reduced to increase the mounting area, thereby enhancing the heat exchange performance. - Effects similar to those described above can be obtained also in an air-conditioning apparatus including the corrugated-
fin heat exchanger 10 according toEmbodiment 1. -
Embodiment 2 of the present invention is described below. Description of the same components as those ofEmbodiment 1 is omitted or partly omitted. The parts same as or corresponding to those ofEmbodiment 1 are denoted by the same reference signs. -
FIG. 15 is a perspective view for illustrating a corrugated-fin heat exchanger 20 according toEmbodiment 2 of the present invention. Further,FIG. 16 is an enlarged front view of theflat tubes 1 and thecorrugated fins 2 of the corrugated-fin heat exchanger 20 according toEmbodiment 2 of the present invention. Further,FIG. 17 is a sectional view taken along the line C-C ofFIG. 16 . - As illustrated in
FIG. 15 and FIG. 16 , in the corrugated-fin heat exchanger 10 according toEmbodiment 2, the plurality offlat tubes 1 that are arranged in the airflow orthogonal direction (right-and-left direction) orthogonal to the airflow direction (front-and-back direction) indicated by the arrow WF are provided in two rows in the airflow direction (front-and-back direction). Eachflat tube 1 extends along the up-and-down direction. Further, there are provided the meanderingcorrugated fins 2 each sandwiched by the adjacentflat tubes 1 in the airflow orthogonal direction (right-and-left direction) and thermally connected to theflat tubes 1 at each apex 2a. - Further, the
inlet header 3 is connected to one end (lower end) of eachflat tube 1 on the windward side (front side), and theoutlet header 4 is connected to one end (lower end) of eachflat tube 1 on the leeward side (back side). Anintermediate header 11 is connected to the other end (upper end) of eachflat tube 1 on the windward side (front side) and the other end (upper end) of eachflat tube 1 on the leeward side (back side). Heat is exchanged between refrigerant flowing through theflat tubes 1 and air flowing through the spaces in each of the fins of thecorrugated fins 2. - As illustrated in
FIG. 17 , on the windward side (front side) of each of thecorrugated fins 2, there is formed the protrudingportion 5 protruding to the windward side (front side) with respect to the windward-side end portions (front-side end portions) 1a of theflat tubes 1. Further, the plurality of lug portions are formed in thecorrugated fin 2 to promote heat transfer. - In the protruding
portion 5, the twofirst lug portions 7 that are formed to be inclined (oblique) to the airflow direction (front-and-back direction) are provided on the right and left sides. Thefirst lug portions 7 are oriented obliquely in the same direction with respect to the airflow direction (front-and-back direction). - Further, on the part of the
corrugated fin 2 other than the protrudingportion 5, that is, the part sandwiched by the adjacentflat tubes 1, there are provided thesecond lug portions 6 formed in the airflow orthogonal direction (right-and-left direction), and the fivesecond lug portions 6 are formed to be arrayed in the airflow direction (front-and-back direction). - As illustrated in
FIG. 4 andFIG. 5 , the corrugated-fin heat exchanger 20 is mounted to the outdoor unit of the air-conditioning apparatus including thefan 31, thereby constructing a refrigeration cycle for circulating refrigerant between the outdoor unit and an indoor unit connected to the outdoor unit by pipes. - Next, an operation of the corrugated-
fin heat exchanger 20 according toEmbodiment 2 is described. - As illustrated in
FIG. 15 , with the flow of air that is generated by thefan 31, the air flows into the corrugated-fin heat exchanger 20, exchanges heat with the refrigerant flowing through theflat tubes 1 when the air flows through the heat-exchanger air passages, and flows out from the corrugated-fin heat exchanger 20. - Next, the flow of the refrigerant is described.
- During the heating operation, refrigerant that is returned after exchanging heat with air in the indoor unit to transfer heat to be liquefied and then being decompressed into a low-temperature and low-pressure two-phase gas-liquid state flows into the corrugated-
fin heat exchanger 20 serving as an evaporator, which is mounted to the outdoor unit, through theinlet header 3. - Then, the refrigerant flows through the
flat tubes 1 on the windward side (front side), flows through theflat tubes 1 on the leeward side (back side) through theintermediate header 11, exchanges heat with air flowing through the heat-exchanger air passages to receive heat to be evaporated, then flows out through theoutlet header 4, and flows into the indoor unit again. In this manner, the refrigerant circulates in the refrigeration circuit. - Other operations are similar to those in
Embodiment 1, and hence description of the operations is omitted. -
FIG. 18 is a view for illustrating a state of frost formation on theflat tubes 1 and thecorrugated fins 2 during the heating operation in the corrugated-fin heat exchanger 20 according toEmbodiment 2 of the present invention. Further,FIG. 19 is a view for illustrating a state of frost formation on theflat tubes 1 and thecorrugated fins 2 during the defrosting operation in the corrugated-fin heat exchanger 20 according toEmbodiment 2 of the present invention. - Further,
FIG. 20 is a perspective view for illustrating drainage passages of the corrugated-fin heat exchanger 20 according toEmbodiment 2 of the present invention.FIG. 18 andFIG. 19 are sectional views taken along the line C-C ofFIG. 16 similarly toFIG. 17 . Further, the arrows DFa, DFb, DFc, and DFd ofFIG. 20 indicate the flows of water during the defrosting operation. - The amount of formed frost is small at a portion on the
corrugated fin 2 at which the airflow velocity is low in the airflow velocity distribution, and the amount of formed frost is large at a portion on thecorrugated fin 2 at which the airflow velocity is high in the airflow velocity distribution. As illustrated inFIG. 18 andFIG. 19 , inEmbodiment 2, the airflow velocity distribution is formed in a direction to which an airflow direction is slightly bent toward the airflow orthogonal direction (right-and-left direction) with the air guiding action by thefirst lug portions 7. - Then, as in a frost formation portion (portion at which frost is formed) 40 illustrated in
FIG. 18 , frost is formed to be dispersed in the front-and-back direction (airflow direction). Thus, as compared to a case where frost is formed to be concentrated at the windward-side end portion (front-side end portion) of the protrudingportion 5, the amount of formed frost is small. - Consequently, a portion at which the amount of formed frost is small, that is, a portion at which the airflow resistance is relatively small is secured easily, thereby being capable of obtaining a configuration in which the entire front surface side (windward side) of the corrugated-
fin heat exchanger 20 is less likely to be closed. - As illustrated in
FIG. 20 , thefirst lug portions 7 are inclined to the airflow direction (front-and-back direction) and extend along with an inclination direction of each surface of the meanderingcorrugated fin 2, and thefirst lug portions 7 are alternately inclined to directions horizontally opposite to each other in the up-and-down direction. That is, a first lug portion 7α that is inclined in the left direction from the windward side (front side) to the leeward side (back side) is formed in a surface of thecorrugated fin 2 that is inclined from the right side to the left side. Further, a first lug portion 7β that is inclined in the right direction from the windward side (front side) to the leeward side (back side) is formed in a surface of thecorrugated fin 2 that is inclined from the left side to the right side. - The frost on the
frost formation portion 40 illustrated inFIG. 18 is melted into water during the defrosting operation. Consequently, to drain the water to the lower part of the corrugated-fin heat exchanger 10, the drainage passages are formed in the corrugated-fin heat exchanger 20 as illustrated inFIG. 20 . The two drainage passages are provided. The first passage is a passage for water flowing through the slits formed in the protruding surface of thecorrugated fin 2 in the course of forming thefirst lug portions 7, as indicated by the arrow DFc and the arrow DFd. - The second passage is a passage for water flowing from the protruding
portion 5 to the vicinity of the apex 2a of thecorrugated fin 2 and flowing through a part between theflat tube 1 on the windward side (front side) and theflat tube 1 on the leeward side (back side), as indicated by the arrow DFa and the arrow DFb. - In the second passage, the
first lug portions 7 are provided to be inclined to the airflow direction (front-and-back direction) and to extend along with the inclination direction of the meanderingcorrugated fin 2. Thus, with use of the gravity, water is easily guided to the part between theflat tube 1 on the windward side (front side) and theflat tube 1 on the leeward side (back side). - As described above, in
Embodiment 2, theflat tubes 1 are provided in two rows in the airflow direction (front-and-back direction). Consequently, in addition to the passage for water flowing through the slits and the passage for water flowing along theflat tube 1, there is formed the passage for water flowing through the part between theflat tube 1 on the windward side (front side) and theflat tube 1 on the leeward side (back side). - Consequently, not only water flows along the
flat tube 1 to be drained due to the gravity when theflat tubes 1 are provided in only one row, but also the water is sucked by a capillary force of a gap formed between theflat tube 1 on the windward side (front side) and theflat tube 1 on the leeward side (back side), so that the water is easily drained to the lower part of the corrugated-fin heat exchanger 10, thereby enhancing the drainage performance. - Further, when air is caused to flow after the defrosting, the drainage performance can further be enhanced with the above-mentioned air guiding action. The enhancement of the drainage performance with the air guiding action exerts the effect to promote drainage of water to the
flat tubes 1 not only during the defrosting operation but also during the normal heating operation even in a case where dew condensation occurs on the surfaces of theflat tubes 1 or thecorrugated fins 2. - When the two
first lug portions 7 that are oriented obliquely in the same direction with respect to the airflow direction (front-and-back direction) are formed on the right and left sides on the protrudingportion 5 of thecorrugated fin 2, onefirst lug portion 7 is not formed at a position in the radial direction extending from theflat tubes 1, and hence the defrosting performance is degraded as compared toEmbodiment 1. - However, in the protruding
portion 5 of thecorrugated fin 2, in which thefirst lug portions 7 are formed, the amount of formed frost is relatively small, and hence the influence of the degradation of the defrosting performance is small. Further, the air guiding action is promoted as compared toEmbodiment 1, and an effect of being capable of prolonging a time period until the defrosting operation is performed is more significant. -
FIG. 21 is a sectional view taken along the line D-D ofFIG. 17 . - As illustrated in
FIG. 21 , the thickness of the center portion of thecorrugated fin 2 in the airflow orthogonal direction (right-and-left direction) is formed larger than those of other portions (both right and left end portions). With this configuration, when frost is formed on the windward-side end portion (front-side end portion) of the protrudingportion 5, during the defrosting operation, the fin efficiency can be enhanced substantially equally to that in a case where the entire thickness of the fin is increased. - Consequently, heat can sufficiently be transferred to the windward-side end portion (front-side end portion) of the protruding
portion 5 and thefirst lug portions 7, thereby being capable of preventing the degradation of the defrosting performance. That is, the time period required for the defrosting can be prevented from being prolonged. - The case where the thickness of the
corrugated fin 2 is varied only at the windward-side end portion (front-side end portion) of the protrudingportion 5 as described above is most efficient. However, the thickness of thecorrugated fin 2 may be entirely varied in the same manner in the airflow direction (front-and-back direction). In this case, also when frost is formed on a part of thecorrugated fin 2 on the leeward side (back side), the defrosting performance can be enhanced. - As described above, in the corrugated-
fin heat exchanger 20 ofEmbodiment 2, the twofirst lug portions 7 are formed in the protrudingportion 5 on the right and left sides to promote heat transfer. Thefirst lug portions 7 are oriented obliquely in the same direction with respect to the airflow direction (front-and-back direction). Thus, the air guiding action is promoted as compared toEmbodiment 1, thereby being capable of prolonging the time period until the defrosting operation is performed. - Further, the
flat tubes 1 are provided in two rows in the airflow direction (front-and-back direction). Thus, in addition to the passage for water flowing through the slits, the passage for water flowing through the part between theflat tube 1 on the windward side (front side) and theflat tube 1 on the leeward side (back side) is formed. - Consequently, as compared to the case where the
flat tubes 1 are provided in only one row, water is easily drained to the lower part of the corrugated-fin heat exchanger 10, thereby enhancing the drainage performance. Further, when air is caused to flow after the defrosting, the drainage performance can be further enhanced with the above-mentioned air guiding action. - Further, the thickness of the center portion of the
corrugated fin 2 in the airflow orthogonal direction (right-and-left direction) is formed larger than those of other portions (both right and left end portions), and hence, during the defrosting operation, the fin efficiency can be enhanced substantially equally to that in the case where the entire thickness of the fin is increased. Consequently, heat can sufficiently be transferred to the windward-side end portion (front-side end portion) of the protrudingportion 5 and thefirst lug portions 7, thereby being capable of preventing the degradation of the defrosting performance. That is, the time period required for the defrosting can be prevented from being prolonged. - Effects similar to those described above can be obtained also in an air-conditioning apparatus including the corrugated-
fin heat exchanger 20 according toEmbodiment 2. -
- 1
- flat tube
- 2
- corrugated fin
- 2a
- apex
- 3
- inlet header
- 4
- outlet header
- 5
- protruding portion
- 6
- second lug portion
- 7
- first lug portion
- 7a
- first lug portion
- 7b
- first lug portion
- 7c
- first lug portion
- 7d
- first lug portion
- 7e
- first lug portion
- 7e1
- first lug portion
- 7e2
- first lug portion
- 7α
- first lug portion
- 7β
- first lug portion
- 10
- corrugated-fin heat exchanger
- 10a
- corrugated-fin heat exchanger
- 10b
- corrugated-fin heat exchanger
- 11
- intermediate header
- 20
- corrugated-fin heat exchanger
- 30a
- outdoor-unit main body
- 30b
- outdoor-unit main body
- 31
- fan
- 32a
- air outlet
- 32b
- air outlet
- 33a
- air inlet
- 33b
- air inlet
- 34
- compressor
- 40
- frost formation portion
Claims (8)
- A heat exchanger (10, 20), comprising:- a plurality of flat tubes (1) arranged in a right-and-left direction orthogonal to a front-and-back direction, the front-and-back direction being an airflow direction of the heat exchanger;- a corrugated fin (2) sandwiched by adjacent ones of the plurality of flat tubes (1) and thermally connected to the adjacent ones of the plurality of flat tubes (1) at each of apexes of the corrugated fin (2);- an inlet header (3) connected to one end of each of the plurality of flat tubes (1); and- an outlet header (4) connected to an other end of each of the plurality of flat tubes (1),- the heat exchanger (10, 20) being configured to serve as an evaporator for refrigerant flowing through the plurality of flat tubes (1),- a surface of the corrugated fin (2) being to be adhered by at least one of dew condensation and frost, wherein- the plurality of flat tubes (1) extends along an up-and-down direction of the heat exchanger (10, 20),- the corrugated fin (2) includes a protruding portion (5) protruding to a front side with respect to a front-side end portion of each of the plurality of flat tubes (1),- the protruding portion (5) includes a plurality of first lug portions (7) oriented obliquely to the front-and-back direction, the plurality of first lug portions (7) being positioned on right and left sides of the protruding portion (5),- the corrugated fin (2) further includes a second lug portion (6) formed in the right-and-left direction at a part sandwiched by the adjacent ones of the plurality of flat tubes (1), whereinbetween the plurality of first lug portions (7) positioned on the right and left sides, an interval is secured,the plurality of first lug portions (7) each includes a slit formed in the protruding portion (5),one or more of the plurality of first lug portions (7) are formed in a radial direction extending from one of the plurality of flat tubes (1) toward a center portion of a front-side end portion of the protruding portion (5), and the heat exchanger (10, 20) includes passages for at least one of water which was the dew condensation and water which was the frost, the slit serving as one of the passages, surfaces of the plurality of flat tubes (1) serving as another of the passages.
- The heat exchanger (10) of claim 1,
wherein the plurality of first lug portions (7) are formed in the radial direction extending from each of the plurality of flat tubes (1) toward the center portion of the front-side end portion of the protruding portion (5), the plurality of first lug portions (7) being positioned on the right and left sides of the protruding portion (5). - The heat exchanger (20) of claim 1,
wherein all of the plurality of first lug portions (7) are oriented obliquely in the same direction with respect to the front-and-back direction. - The heat exchanger (20) of claim 3,
wherein the plurality of first lug portions (7) are formed to be inclined in an inclination direction of each of surfaces of the corrugated fin (2) from the front side to a back side. - The heat exchanger (20) of any one of claims 1 to 3,
wherein the plurality of flat tubes (1) are provided in two rows in the front-and-back direction. - The heat exchanger (20) of any one of claims 1 to 5,
wherein a thickness of a center portion of the corrugated fin (2) in the right-and-left direction is formed larger than thicknesses of other portions of the corrugated fin (2). - The heat exchanger (10) of any one of claims 1 to 6,
wherein each of the plurality of first lug portions (7) is formed by forming the one slit in the protruding portion (5). - An air-conditioning apparatus, comprising:- the heat exchanger (10, 20) of any one of claims 1 to 7; and- a fan (31) configured to send air to the heat exchanger (10, 20);- the heat exchanger (10, 20) including the protruding portion (5) arranged on a windward side of the heat exchanger (10, 20).
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JP2015069429 | 2015-03-30 | ||
PCT/JP2016/056675 WO2016158193A1 (en) | 2015-03-30 | 2016-03-03 | Heat exchanger and air conditioner |
Publications (3)
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EP3279598A1 EP3279598A1 (en) | 2018-02-07 |
EP3279598A4 EP3279598A4 (en) | 2019-01-02 |
EP3279598B1 true EP3279598B1 (en) | 2022-07-20 |
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US (1) | US20180100659A1 (en) |
EP (1) | EP3279598B1 (en) |
JP (1) | JP6165360B2 (en) |
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US10627175B2 (en) * | 2015-05-29 | 2020-04-21 | Mitsubishi Electric Corporation | Heat exchanger and refrigeration cycle apparatus |
CN107614998A (en) * | 2015-05-29 | 2018-01-19 | 三菱电机株式会社 | Heat exchanger |
KR20170015146A (en) * | 2015-07-31 | 2017-02-08 | 엘지전자 주식회사 | Heat exchanger |
JP6997722B2 (en) * | 2016-12-02 | 2022-01-18 | 三菱電機株式会社 | Heat exchanger and air conditioner |
JP6400257B1 (en) * | 2017-02-21 | 2018-10-03 | 三菱電機株式会社 | Heat exchanger and air conditioner |
WO2019008997A1 (en) * | 2017-07-05 | 2019-01-10 | 日立ジョンソンコントロールズ空調株式会社 | Outdoor heat exchanger for air conditioner, and air conditioner equipped with same |
WO2019026243A1 (en) * | 2017-08-03 | 2019-02-07 | 三菱電機株式会社 | Heat exchanger and refrigeration cycle device |
EP3734190B1 (en) * | 2017-12-25 | 2024-02-21 | Mitsubishi Electric Corporation | Heat exchanger and refrigeration cycle device |
US20190310031A1 (en) * | 2018-04-05 | 2019-10-10 | United Technologies Corporation | Secondarily applied cold side features for cast heat exchanger |
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-
2016
- 2016-03-03 EP EP16772077.0A patent/EP3279598B1/en active Active
- 2016-03-03 JP JP2016567268A patent/JP6165360B2/en active Active
- 2016-03-03 CN CN201680017676.9A patent/CN107407534A/en active Pending
- 2016-03-03 US US15/560,175 patent/US20180100659A1/en not_active Abandoned
- 2016-03-03 WO PCT/JP2016/056675 patent/WO2016158193A1/en active Application Filing
Also Published As
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WO2016158193A1 (en) | 2016-10-06 |
CN107407534A (en) | 2017-11-28 |
EP3279598A1 (en) | 2018-02-07 |
EP3279598A4 (en) | 2019-01-02 |
US20180100659A1 (en) | 2018-04-12 |
JP6165360B2 (en) | 2017-07-19 |
JPWO2016158193A1 (en) | 2017-04-27 |
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