WO2014091782A1 - 扁平管熱交換器、及びそれを備えた空気調和機の室外機 - Google Patents
扁平管熱交換器、及びそれを備えた空気調和機の室外機 Download PDFInfo
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- WO2014091782A1 WO2014091782A1 PCT/JP2013/067049 JP2013067049W WO2014091782A1 WO 2014091782 A1 WO2014091782 A1 WO 2014091782A1 JP 2013067049 W JP2013067049 W JP 2013067049W WO 2014091782 A1 WO2014091782 A1 WO 2014091782A1
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- flat tube
- heat exchanger
- tube heat
- fin
- row
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Classifications
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- 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
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/0066—Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids
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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
-
- 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
- F28D1/0408—Multi-circuit heat exchangers, e.g. integrating different heat exchange sections in the same unit or heat exchangers for more than two fluids
- F28D1/0426—Multi-circuit heat exchangers, e.g. integrating different heat exchange sections in the same unit or heat exchangers for more than two fluids with units having particular arrangement relative to the large body of fluid, e.g. with interleaved units or with adjacent heat exchange units in common air flow or with units extending at an angle to each other or with units arranged around a central element
- F28D1/0435—Combination of units extending one behind the other
-
- 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
- F28D1/047—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 bent, e.g. in a serpentine or zig-zag
- F28D1/0477—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 bent, e.g. in a serpentine or zig-zag the conduits being bent in a serpentine or zig-zag
- F28D1/0478—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 bent, e.g. in a serpentine or zig-zag the conduits being bent in a serpentine or zig-zag the conduits having a non-circular cross-section
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- 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
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2215/00—Fins
- F28F2215/12—Fins with U-shaped slots for laterally inserting conduits
Definitions
- the present invention relates to a finned tube heat exchanger used as a heat exchanger for an air conditioner, a refrigerator, a water heater, or the like, and an outdoor unit of an air conditioner including the same, and in particular, a flat heat transfer tube.
- the present invention relates to flat tube heat exchangers arranged in a staggered manner, and an outdoor unit of an air conditioner including the flat tube heat exchanger.
- a circular tube having a circular cross-sectional shape and a flat tube having a rectangular cross-sectional shape with a rectangular aspect ratio are generally known.
- a heat exchanger using a circular tube is referred to as a “circular tube heat exchanger”
- a heat exchanger using a flat tube is referred to as a “flat tube heat exchanger”.
- the heat transfer tubes are arranged in a staggered manner with respect to the fins (hereinafter referred to as “staggered arrangement”).
- staggered arrangement In the case of a circular tube heat exchanger, the circular tubes can be easily arranged in a staggered arrangement because the circular tubes are manufactured in one row.
- the flat tube is inserted into the fin or the fin slit is inserted into the outer periphery of the flat tube, but a method of inserting one row at a time is easy to manufacture. Therefore, in the case of a flat tube heat exchanger, for example, as shown in Patent Document 1, a structure in which a plurality of heat exchangers in which flat tubes are arranged one by one is arranged in a staggered arrangement is adopted. Yes.
- the present invention has been made to solve the above-described problems. Even when a plurality of rows of flat tube heat exchangers having the same shape are arranged, a staggered arrangement can be obtained, and fin ends can be arranged.
- An object of the present invention is to obtain a flat tube heat exchanger in which the positions of the parts are not uniform and an outdoor unit of an air conditioner equipped with the flat tube heat exchanger.
- the outdoor unit of an air conditioner according to the present invention is a shape in which a cross-sectional shape is a rectangle with a large aspect ratio cut off, a flat tube through which a heat exchange medium flows, and a flat tube that is bent into a U shape And a flat tube heat exchanger in which a plurality of plate-like fins having a plurality of plate-like fins joined to the flat tube in a right angle direction by brazing are coupled in a plurality of rows.
- An outdoor unit of an air conditioner in which a flat tube heat exchanger has flat tubes arranged at a constant pitch in a step direction perpendicular to the row direction of fins, and the pitch in the step direction of the flat tube is a coefficient of Dp and Dp Is k and 0 ⁇ k ⁇ 0.5 or 0.5 ⁇ k ⁇ 1, the distance between the fin end on one side in the step direction of the fin and the center in the thickness direction of the flat tube is k ⁇ Dp
- the distance between the fin end on the other side in the step direction of the fin and the center in the thickness direction of the flat tube is (1- k) ⁇ Dp
- the odd-numbered single-row flat tube heat exchangers and the even-numbered single-row flat tube heat exchangers are arranged opposite to each other in the step direction in the wind flow direction.
- the heights of the upper and lower ends of the row flat tube heat exchanger and the even-row single row flat tube heat exchanger are aligned.
- the outdoor unit of the air conditioner according to the present invention has 0 ⁇ k ⁇ 0.5 or 0.5 ⁇ k, where Dp is the pitch in the step direction of the flat tube and k is the coefficient of Dp. ⁇ 1, and the distance between the fin end on one side in the step direction of the fin and the flat tube is k ⁇ Dp, and the distance between the fin end on the other side in the step direction of the fin and the flat tube is (1 ⁇ k) ⁇ Dp. Since the first and second rows of the flat tubes are arranged opposite to each other in the step direction, it is possible to align the positions of the fin ends of the odd-numbered rows and even-numbered rows of the flat tube heat exchanger composed of a plurality of rows.
- the flat tubes can be brought close to a staggered arrangement, and the heat transfer performance can be improved. Therefore, according to the present invention, even if a plurality of rows of flat tube heat exchangers of the same shape are arranged in a plurality of rows, the air conditioner can be arranged in a staggered manner and the positions of fin ends are not uneven. An outdoor unit can be obtained.
- FIG. 1 drawings including FIG. 1 are schematically shown, and the relationship between the sizes of the constituent members may be different from the actual one.
- a single-row (single-row) flat tube heat exchanger 10 constituting the flat tube heat exchanger of this embodiment includes a flat tube 1 that is a heat transfer tube and a plate-like fin 2.
- the flat tube 1 has a shape obtained by rounding a rectangle having a large aspect ratio in cross section, and at least one (in the illustrated example, 10) flow paths 3 through which a heat exchange medium flows are formed.
- a fluid such as water, a refrigerant, or brine is used as the heat exchange medium.
- the flat tube 1 is made of a hollow metal tube having good thermal conductivity such as aluminum, and a plurality of partition plates 13 are provided inside. This is to improve the pressure resistance of the flat tube 1 because the gauge pressure of the refrigerant flowing through the flat tube 1 becomes as high as the order of MPa. Then, as shown in FIG. 1, the flat tubes 1 are arranged in multiple rows (in this example, 6 steps) in the step direction of the plate-like fins 2 (vertical direction in FIG. 1, ie, the longitudinal direction of the fins 2). Has been placed.
- the flat tube heat exchanger 10 when used as an outdoor unit of an air conditioner capable of cooling and heating operation, is a condenser during cooling operation and an evaporator during heating operation.
- the temperature of the flat tube heat exchanger 10 is lower than the outside air temperature, water vapor in the outside air is condensed, and water droplets adhere to the flat tube 1 and the fins 2. In order to remove this water droplet, the fin 2 needs a drainage channel.
- the left end of the flat tube 1 is located on the right side of the left end of the fin 2, but water droplets adhering to the flat tube 1 and the fin 2 are placed on the fin between the left end of the flat tube 1 and the left end of the fin 2.
- the left end of the flat tube 1 is positioned on the right side of the left end of the fin 2, or the right end of the flat tube 1 is positioned on the left side of the right end of the fin 2.
- the width of the fin 2 may be longer than the width of the flat tube 1 on both the left and right sides.
- a flat tube heat exchanger 10 is referred to as a fin-and-tube flat tube heat exchanger.
- Dp represents the pitch between the flat tubes 1 arranged in a plurality of stages
- k represents a coefficient.
- the plate-like fins 2 are arranged in a plurality of rows at a predetermined pitch (fin pitch) perpendicular to the tube axis direction of the flat tube 1.
- the fin 2 is made of a metal plate having good thermal conductivity such as aluminum or copper.
- the fin 2 is formed in the rectangular shape which consists of the long sides 2a and 2b and the short sides 2c and 2d.
- the flat tube 1 is inserted into the slit 4 formed by opening the edge of one long side 2b of the fin 2.
- a plurality of slits 4 are formed in the fin 2 at equal intervals. As shown in FIG.
- the flat tube 1 is bent into a hairpin shape to form the hairpin bent portion 5, and the flat tube 1 is inserted into each slit 4 of the fin 2, and the flat tube 1 is finned to each flat tube 1.
- the portion facing the slit 4 is brazed and joined to the fin 2 integrally.
- a U-bend 6, which is a merged pipe in which a single flow path is formed, is connected to the end of the flat tube 1, and a plurality of flat tubes 1 are connected.
- the flat tube 1 and the U bend 6 are joined by brazing or the like. For example, as shown in FIG.
- one row (single row) of flat tube heat exchangers 10 is formed so as to pass from the flat tube 1 on the refrigerant inlet 7 side to the flat tube 1 on the refrigerant outlet 8 side.
- the refrigerant inlet 7 and the refrigerant outlet 8 are connected to a header or a distributor.
- FIG. 2 (a) three flat tubes 1 having one hairpin bending portion 5 are prepared, and the three flat tubes 1 are connected using two U-bends 6 to form a single row of flat tubes.
- the example which comprised the heat exchanger 10 was demonstrated, it is not limited to it.
- a flat tube 1 having one hairpin bending portion 5 and a flat tube 1 having two or more hairpin bending portions 5 are connected using a U-bend 6 to form a single row.
- the flat tube heat exchanger 10 may be configured.
- the heat exchange medium flows through the flow path 3 of the flat tube 1, and a gap between the fins 2 is formed in a direction perpendicular to the tube axis direction of the flat tube 1.
- Heat exchange is performed by passing a heat exchange medium (for example, a fluid such as air or water).
- the pitch (step pitch) in the step direction of the flat tubes 1 orthogonal to the row direction of the fins 2 is Dp
- the coefficient of Dp is k
- the distance between the fin end (fin upper end in FIG. 1) 2c in the step direction of the fin 2 and the center in the thickness direction of the flat tube 1 is k ⁇ Dp
- the distance between the fin end (fin lower end in FIG. 1) 2d in the step direction of the fin 2 and the center of the flat tube 1 in the thickness direction is (1 ⁇ k) ⁇ Dp. Therefore, the flat tube heat exchanger 10 is formed so that the flat tubes 1 are vertically asymmetric with respect to the arrangement in the step direction.
- FIG. 4 is a front view of a flat tube heat exchanger (comparative example) in which the flat tube heat exchanger 10 is connected in a plurality of rows in the same direction.
- the flat tube heat exchangers 10 having the same shape are arranged in two rows in the same direction, the upper and lower ends of the fins 2 are aligned, but the flat tubes 1 are arranged in a grid pattern, which is a staggered arrangement. Compared to heat transfer performance.
- FIG. 5 is a front view of a two-row flat tube heat exchanger according to an embodiment of the present invention.
- the flat tube heat exchanger according to the embodiment of the present invention has good heat transfer performance by arranging one flat tube heat exchanger 10 of the two rows of flat tube heat exchangers 10 to be combined upside down. Staggered arrangement.
- the flat side heat exchanger 10 on the windward side is arranged with the short side 2d corresponding to the fin lower end facing upward and the short side 2c corresponding to the fin upper end facing downward. That is, the first and second rows of the flat tube heat exchanger 10 in which the distance between the short side 2c corresponding to the fin upper end and the flat tube 1 and the distance between the short side 2d corresponding to the fin lower end and the flat tube 1 are different.
- the eyes are arranged oppositely in the step direction of the flat tube 1.
- FIG. 6 is a diagram illustrating the relationship between the external heat transfer coefficient and the coefficient k of the flat tube heat exchanger 10 according to the embodiment of the present invention.
- the horizontal axis represents k
- the vertical axis represents the external heat transfer coefficient.
- the complete staggered arrangement is adjacent to the height position just at the center of the flat tubes 1 vertically adjacent to each other in the flat tubes 1 of the single-row flat tube heat exchanger 10 shown in FIG. That is, the flat tube 1 of the other single row flat tube heat exchanger 10 is arranged.
- FIG. 7 shows a side-blow type outdoor unit used for a room air conditioner or the like.
- the exterior of the outdoor unit 100 includes a top plate 200 that forms the top surface of the outdoor unit 100, a part of the front surface of the outdoor unit 100, a front panel 201 that forms the left side, and a part of the right side and back of the outdoor unit 100.
- a fan grill 203 which is a lattice-like member made up of vertical and horizontal beams, and the bottom surface of the outdoor unit 100.
- the outdoor unit 100 includes a partition plate 206 that divides the space in the outdoor unit 100 into a left side and a right side, a compressor 207 that compresses and discharges the refrigerant, and a propeller fan that supplies outside air to the flat tube heat exchanger 10. 208, an electric motor 209 that rotates the propeller fan 208, a motor support 210 that holds the electric motor 209, and a four-way valve 211 that is used to switch the refrigerant flow path.
- Fig. 8 shows a top-blow type outdoor unit used for a commercial air conditioner installed on the roof of a building.
- the outdoor unit 101 includes a front panel 250 that forms a front shell of the outdoor unit 101, a fan guard 251 provided on the top of the outdoor unit 101, a side panel 252 that forms a side shell of the outdoor unit 101, and a flat shape. And a base panel 253 that supports the tube heat exchanger 10 and the like.
- the outdoor unit 101 is provided with an air suction port 254 for taking in air into the side and back of the outer shell, and an air outlet 255 for exhausting air to the outside at the upper part of the outdoor unit 101.
- the outdoor unit 101 is formed in the side panel 252 and is formed in the air inlet 254 and the fan guard 251 that are used to take air into the outdoor unit 101, and the air in the outdoor unit 101 is transferred to the outdoor unit 101.
- an air outlet 255 which is used to discharge to the outside.
- the outdoor unit 101 is equipped with a compressor 256 that compresses and discharges the refrigerant, and a four-way valve 257 that is used to switch the refrigerant flow path.
- the flat tube heat exchanger 10 functions as a condenser (heat radiator) during the cooling operation to condense and liquefy the refrigerant, and functions as an evaporator during the heating operation. Evaporate.
- the flat tube heat exchanger 10 of FIG. 8 has been described as being three-tiered in the vertical direction, the present invention is not limited to this and may be in an unsuperposed manner.
- the flat tube heat exchanger 10 is arranged to stand vertically with respect to the base panel 204 and the base panel 253.
- FIG. 9 is an explanatory diagram of a method for manufacturing a circular tube heat exchanger.
- the manufacturing method of the heat exchanger in a circular pipe is demonstrated.
- a circular tube a plurality of fins 2 arranged in parallel are fixed, and the circular tube is inserted from the front side of the paper to the back side from the mounting side of the U bend 6.
- the circular tube insertion hole 15 of the fin 2 is larger than the outer diameter of the circular tube.
- the circular tube is inserted into the fin 2 because the circular tube insertion hole 15 of the fin 2 is larger than the outer diameter of the circular tube, so that variation in positional accuracy of the circular tube and the fin 2 can be allowed. Is easy to insert.
- the expanded ball is inserted into the inside of the circular tube in a direction perpendicular to the surface of the fin, and the outer diameter of the circular tube is increased.
- the circular tube and the fin collar provided on the fin 2 are brought into close contact with each other, and the contact thermal resistance between the circular tube and the fin is reduced.
- the circular tube and the expanded ball can be inserted at the same time.
- the flat tube 1 it is difficult to increase the outer diameter of the flat tube 1 after inserting the expanded ball into the flat tube 1 in a direction perpendicular to the surface of the fin 2. This is because the flat tube 1 is provided with nine partition plates 13 in the example shown in FIG. 1 in order to increase the pressure resistance inside the flat tube 1. For this reason, in the case of the flat tube 1, the flat tube 1 and the fin 2 are generally brazed to reduce the contact thermal resistance between the flat tube 1 and the fin 2.
- the circular tube insertion hole 15 of the fin 2 is larger than the outer diameter of the circular tube, so that the circular tube can be easily inserted into the fin 2.
- the flat tube 1 as the slit 4 of the fin 2 is made larger than the outer diameter of the flat tube 1, the gap between the fin collar provided on the fin 2 and the flat tube 1 during brazing is increased. The contact thermal resistance is likely to increase, making it difficult to fill. Because of such circumstances, the size of the outer diameter of the slit 4 formed in the fin 2 is limited, and it is more difficult to insert the flat tube 1 into the slit 4 of the fin 2 at the time of manufacture than in the circular tube. is there.
- FIG. 5 is an upside-down view of only the first row of FIG. 4, but when only one of the first row and the second row is turned upside down, the hairpin bending portion 5 and the U bend of FIG.
- the direction of 6 is also reversed.
- a staggered arrangement can be manufactured. The positions of the hairpin bending portion 5 of the flat tube heat exchanger 10 and the hairpin bending portion 5 of the other single-row flat tube heat exchanger 10 are reversed.
- the first method will be described with reference to FIGS. 10 (a) and 10 (b). This is a method of fixing the flat tube 1 and inserting the fins 2 into the flat tube 1.
- the distance between the upper end of the fin 2 and the flat tube 1 is (1-k) ⁇ Dp, and the distance between the lower end of the fin 2 and the flat tube 1 is k ⁇ Dp.
- the fins 2 are inserted into the flat tube 1 in order from the hairpin bending portion 5 side.
- the one shown in FIG. 10A is used as the odd-numbered single-row flat tube heat exchanger 10.
- the distance between the upper end of the fin 2 and the flat tube 1 is k ⁇ Dp
- the distance between the lower end of the fin 2 and the flat tube 1 is (1 ⁇ k).
- the second method will be described with reference to FIGS. 10 (a) and 10 (c).
- the second method is a method using the single-row flat tube heat exchanger 10 of FIG. 10A and the single-row flat tube heat exchanger 10 of FIG.
- the distance between the upper end of the fin 2 and the flat tube 1 is k ⁇ Dp
- the distance between the lower end of the fin 2 and the flat tube 1 is (1 ⁇ k) ⁇ Dp.
- the fins 2 are inserted into the flat tube 1 in order from the hairpin bending portion 5 side.
- FIG. 10A and FIG. 10C the positional relationship of the fins 2 is upside down. While maintaining the left and right sides of the single row flat tube heat exchanger 10 shown in FIG.
- the upper and lower sides are also superposed on the single row flat tube heat exchanger 10 shown in FIG. 10 (a).
- (1) The heights of the upper and lower ends are aligned, (2) the positions of the hairpin bending portion 5 and the U bend 6 are aligned, and (3) a plurality of rows of flat tube heat exchangers in which the flat tubes 1 are arranged in a staggered arrangement. 10 can be manufactured.
- the flat tube heat exchanger 10 shown in FIG. 5 and the flat tube heat exchanger 10 as shown in FIG. 16 described later can be manufactured.
- FIG. 11 is an explanatory view of a third manufacturing method of the flat tube heat exchanger 10 according to the embodiment and different from the manufacturing method shown in FIG. A third method will be described with reference to FIG.
- the flat tube 1 is fixed and the fin 2 is inserted into the flat tube 1, but in the method of FIG. 11, the fin 2 is fixed.
- the flat tube 1 is inserted into the slit 4 of the fin 2.
- the left end of the fin 2 is k ⁇ Dp
- the right end is (1 ⁇ k) ⁇ Dp
- the flat tube 1 is inserted from above, which is used in the odd-numbered rows.
- FIG. 12 is an explanatory diagram of a fourth manufacturing method of the flat tube heat exchanger 10 according to the embodiment, which is different from the manufacturing method shown in FIGS. 10 and 11.
- a fourth method will be described with reference to FIG.
- the method of FIG. 12 is a method of fixing the fin 2 and inserting the flat tube 1 into the fin 2 as in the method of FIG.
- the left end of the fin 2 is k ⁇ Dp
- the right end is (1 ⁇ k) ⁇ Dp
- the flat tube 1 extends from the front to the back of the page
- the U bend 6 is attached to the slit 4 of the fin 2. Insert and use this in the odd-numbered columns.
- the insertion direction of the flat tube 1 is reversed only from the back to the front of the page, or as shown in FIG.
- the left end is set to (1-k) ⁇ Dp
- the right end is set to k ⁇ Dp
- the flat tube 1 is inserted in the depth direction from the front of the page.
- a plurality of rows of flat tube heat exchangers 10 in which the flat tubes 1 are in a staggered arrangement can be manufactured.
- a single row of flat tube heat exchangers 10 can be manufactured in a plurality of rows at the same time. .
- a complicated fixing jig may be required, or the speed at which the flat tube 1 is inserted into the fin 2 may have to be reduced. In such a case, the manufacturing method described in FIGS. 10 and 11 may be employed.
- FIG. 14 is an explanatory diagram of a heat exchange promotion unit formed in an odd-numbered row and a heat exchange promotion unit formed in an even-numbered row among the plurality of rows of flat tube heat exchangers 10 according to the embodiment. is there.
- the fin 2 may be formed with a heat exchange accelerating portion that functions as a heat receiving portion or a heat radiating portion.
- this heat exchange promoting portion for example, the cut and raised portion 16 formed by cutting and raising the surface of the fin 2 (see the side view of FIG. 13 (a1) and the front view of FIG. 13 (a2)), A waffle portion 17 (see a side view of FIG. 13 (b1) and a front view of FIG. 13 (b2)) formed with an uneven shape on the surface may be employed.
- the flat tube heat exchanger 10 manufactured by combining the above-described one shown in FIG. 10 (a) and the one shown in FIG. 10 (b) includes the fin 2 in FIG. 10 (a) and FIG. 10 (b).
- the fins 2 may be made of a mold having the same shape.
- FIG. 14 the positions of the raised portions 16 and the waffle portions 17 in the odd and even rows are reversed on the left and right sides, and the external heat transfer coefficient of the flat tube heat exchanger 10 is improved by several percent. .
- the heat exchange is biased toward the side where the cut and raised portions 16 and the waffle portion 17 are located.
- FIG. 15 shows a first modification of the flat tube heat exchanger shown in FIG.
- two flat tube heat exchangers 10 in one row are combined with the side where the slit 4 of the fin 2 is open facing the side where the slit 4 is not opened.
- two rows of flat tube heat exchangers 10 in a single row are coupled with the sides of the fins 2 where the slits 4 are not opened facing each other.
- the fin 2 is formed with a plurality of slits 4 into which the flat tube 1 is inserted at one end thereof, but the odd-numbered single-row flat tube heat exchanger 10 and the even-numbered single-row
- the flat tube heat exchanger 10 is the other end side of the fins 2 of the odd-numbered single row flat tube heat exchanger 10 and the other end side of the fins 2 of the even-numbered single row flat tube heat exchanger 10. Are connected to face each other. Even in the case of FIG. 15, the same result as in FIG. 5 is obtained. That is, the heat transfer performance can be improved by arranging the flat tubes 1 in a staggered arrangement.
- the flat tube heat exchanger 10 as shown in FIG. 15 for example, two single row flat tube heat exchangers 10 shown in FIG. 10A are prepared, and one of the single row flat tube heat exchangers 10 is prepared. Can be manufactured by reversing the top and bottom while maintaining the left and right.
- the third and subsequent rows are in units of two rows as shown in FIG. 5 or FIG.
- the flat tubes 1 can be arranged in a staggered arrangement. In the case of (2n + 1) columns, it is preferable to arrange (2n + 2) columns in units of two columns and delete the (2n + 2) columns as described above.
- the step pitch of the flat tubes 1 is Dp, and the coefficient of Dp is k.
- the distance between the short side 2c corresponding to the fin upper end and the flat tube 1 is k ⁇ Dp, and the short side 2d corresponding to the fin lower end is Since the distance from the flat tube 1 is (1 ⁇ k) ⁇ Dp and the first and second rows of the flat tube 1 are arranged opposite to each other in the step direction, a staggered arrangement can be obtained. The transmission rate can be improved.
- the mounting space for the flat tube heat exchanger is not increased, and the mounting device for the flat tube heat exchanger can be downsized. Furthermore, since the flat tube heat exchanger 10 to be combined has the same shape, the mold of the fin 2 becomes one type, which contributes to the reduction of the manufacturing cost.
- FIG. 16 shows a second modification of the flat tube heat exchanger 10 shown in FIG.
- FIG. 17 is a diagram illustrating the relationship between the external heat transfer coefficient and the coefficient k of the flat tube heat exchanger 10 illustrated in FIG.
- a zigzag arrangement may be realized by setting 0 ⁇ m ⁇ 1 and fin ends at m ⁇ Dp and (1.5 ⁇ m) ⁇ Dp.
- 5, 15, and 16 show examples in which the single row of flat tube heat exchangers 10 are arranged in two rows, but the present invention is not limited to this, and the single row of flat tube heat exchangers 10 is not limited thereto. It is good also as two or more rows.
Abstract
Description
したがって、本発明によれば、同一形状の1列の扁平管熱交換器を複数列配置しても、千鳥配列にすることができ、かつ、フィン端部の位置が不揃いとならない空気調和機の室外機を得ることができる。
したがって、この扁平管熱交換器10は、扁平管1が段方向に配列に関し、上下非対称に形成されている。
図6示すように、k=0、0.5、1のとき、管外熱伝達率が最小となる。これは扁平管1が碁盤目配列となるためである。
また、k=0.25またはk=0.75のとき、管外熱伝達率が最大となる。これは扁平管1が完全な千鳥配列となるためである。ここで、完全な千鳥配列とは、図5に示すいずれか一方の単列の扁平管熱交換器10の扁平管1のうち上下に隣接する扁平管1のちょうど中央の高さ位置に、隣接する他方の単列の扁平管熱交換器10の扁平管1が配置されるということである。
また、室外機100は、室外機100内の空間を左側と右側に区画する仕切板206と、冷媒を圧縮して吐出する圧縮機207と、扁平管熱交換器10に外気を供給するプロペラファン208と、プロペラファン208を回転させる電動機209と、電動機209を保持するモーターサポート210と、冷媒流路を切り替えるのに利用される四方弁211とを有している。
これは、高さが揃わないと、その分、扁平管熱交換器10の高さが高くなり、室外機100及び室外機101の高さが必要以上に高くなってしまい、その分大型化してしまうからである。また、室外機100及び室外機101の高さが高くなると、室外機100及び室外機101の輸送及び搬入などがしにくくなってしまう。さらに、地震時などが発生して扁平管熱交換器10に振動が加わる場合に扁平管熱交換器10の下端に加わる局所荷重が増大してしまう。このような不具合を抑制するために、扁平管熱交換器10の端部の高さを揃えるようにしている。
上述で説明した第1の方法及び第2の方法では、図5に示す扁平管熱交換器10及び後述する図16に示すような扁平管熱交換器10を製造することができる。
図11(a)ではフィン2の左端をk・Dp、右端を(1-k)・Dpとし、扁平管1を上方から挿入し、これを奇数列目に用いる。偶数列目は、奇数列目の扁平管1の挿入時においてヘアピン曲げ部5とUベンド6の向きのみを逆にする、若しくは図11(b)に示したように、フィン2の左端を(1-k)・Dp、右端をk・Dpとし、扁平管1を上方から挿入する。このように製造した、奇数列目用、偶数列目用の扁平管熱交換器10を組み合わせることで、(1)上下端の高さが揃い、(2)ヘアピン曲げ部5及びUベンド6の位置が揃い、(3)扁平管1が千鳥配列となっている複数列の扁平管熱交換器10を製造することができる。
ただし、この図11の製造方法では扁平管熱交換器10を1列ずつ製造する必要があり、複数列同時に製造することはできない。
図12(a)ではフィン2の左端をk・Dp、右端を(1-k)・Dpとし、扁平管1を紙面手前から奥方向に、Uベンド6の取り付け側からフィン2のスリット4に挿入し、これを奇数列目に用いる。偶数列目は、奇数列目の扁平管1の挿入時において扁平管1の挿入方向を紙面奥から手前方向のみを逆にするか、若しくは図12(b)に示したように、フィン2の左端を(1-k)・Dp、右端をk・Dpとし、扁平管1を紙面手前から奥方向に挿入する。このように製造した、奇数列目用、偶数列目用の扁平管熱交換器10を組み合わせることで、(1)上下端の高さが揃い、(2)ヘアピン曲げ部5及びUベンド6の位置が揃い、(3)扁平管1が千鳥配列となっている複数列の扁平管熱交換器10を製造することができる。
図12の製造方法では、単列の扁平管熱交換器10を複数列同時に製造することができるが、複数のフィン2の配置位置の精度、扁平管1の挿入位置の精度などが必要となる。このため、これらの精度を確保するため、複雑な固定冶具が必要となったり、扁平管1をフィン2に挿入する速度を低下させなければならなかったりすることがある。このような場合には、図10及び図11で説明した製造方法を採用すればよい。
フィン2には、スリット4以外に、受熱部、又は放熱部として機能する熱交換促進部が形成されていてもよい。この熱交換促進部としては、たとえば、フィン2の表面が切り起こされて形成された切り起こし部16(図13(a1)の側面図及び図13(a2)の正面図参照)、フィン2の表面に凹凸形状を設けて形成されたワッフル部17(図13(b1)の側面図及び図13(b2)の正面図参照)などを採用するとよい。
なお、図10(a)に示すものと図10(c)に示すものとを組み合わせて扁平管熱交換器10を製造する場合には、フィン2を形成する金型は異なる。
さらに、組み合わされる扁平管熱交換器10は同一形状であるので、フィン2の金型が1種類になり、製造コストの削減に寄与する。
Claims (7)
- 断面形状がアスペクト比の大きい長方形を角取りした形状で、内部を熱交換媒体が流れる扁平管と、
前記扁平管がU字状にヘアピン曲げされた状態で挿入され、該扁平管に対し、ろう付けにより直角方向に接合される複数の板状のフィンと、
を有した単列扁平管熱交換器を複数列結合した扁平管熱交換器を備えた空気調和機の室外機であって、
前記扁平管熱交換器は、
前記扁平管が前記フィンの列方向と直交する段方向に一定のピッチで配置され、
前記扁平管の前記段方向のピッチをDp、Dpの係数をkとし、0<k<0.5、または0.5<k<1としたとき、
前記フィンの前記段方向の一方側のフィン端と前記扁平管の厚さ方向の中心との距離がk・Dp、前記フィンの前記段方向の他方側のフィン端と前記扁平管の厚さ方向の中心との距離が(1-k)・Dpとされ、
風の流れ方向に奇数列目の前記単列扁平管熱交換器と偶数列目の前記単列扁平管熱交換器とが前記段方向に反対に配置され、奇数列目の前記単列扁平管熱交換器と偶数列目の前記単列扁平管熱交換器の上下端の高さを揃えたものである
ことを特徴とする空気調和機の室外機。 - k=0.25、またはk=0.75とする
ことを特徴とする請求項1に記載の空気調和機の室外機。 - 前記扁平管熱交換器の前記フィンは、
その表面に熱交換促進部が複数形成され、
奇数列目の前記単列扁平管熱交換器と偶数列目の前記単列扁平管熱交換器とは、
奇数列目の前記単列扁平管熱交換器の前記熱交換促進部の形成されている側と、偶数列目の前記単列扁平管熱交換器の前記熱交換促進部の形成されている側とが逆となるように配置されている
ことを特徴とする請求項1又は2に記載の空気調和機の室外機。 - 前記扁平管熱交換器の前記熱交換促進部は、
前記フィンの表面が切り起こされて形成された切り起こし部、又は、前記フィンの表面に凹凸を設けて形成されたワッフル部である
ことを特徴とする請求項3に記載の空気調和機の室外機。 - 前記扁平管が前記フィンの一辺側から切り欠かれたスリットに挿入されており、単列の前記扁平管熱交換器の2つを、前記フィンの前記スリットが開口していない辺同士を対向させて結合したものである
ことを特徴とする請求項1~4のいずれか1項に記載の空気調和機の室外機。 - 断面形状がアスペクト比の大きい長方形を角取りした形状で、内部を熱交換媒体が流れる扁平管と、
前記扁平管がU字状にヘアピン曲げされた状態で挿入され、該扁平管に対し、ろう付けにより直角方向に接合される複数の板状のフィンと、
を有した単列扁平管熱交換器を複数列結合した扁平管熱交換器であって、
前記扁平管が前記フィンの列方向と直交する段方向に一定のピッチで配置され、
前記扁平管の前記段方向のピッチをDp、Dpの係数をkとし、0<k<0.5、または0.5<k<1としたとき、
前記フィンの前記段方向の一方側のフィン端と前記扁平管の厚さ方向の中心との距離がk・Dp、前記フィンの前記段方向の他方側のフィン端と前記扁平管の厚さ方向の中心との距離が(1-k)・Dpとされ、
風の流れ方向に奇数列目の前記単列扁平管熱交換器と偶数列目の前記単列扁平管熱交換器とが前記段方向に反対に配置され、奇数列目の前記単列扁平管熱交換器と偶数列目の前記単列扁平管熱交換器の上下端の高さを揃えたものである
ことを特徴とする扁平管熱交換器。 - k=0.25、またはk=0.75とする
ことを特徴とする請求項6に記載の扁平管熱交換器。
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