Patent Application
20140137592
The present invention relates to an outdoor heat exchanger used in heat pump-type vehicle air conditioners and to a vehicle air conditioner using the outdoor heat exchanger.
Conventionally, for example, in an automobile equipped with a gasoline engine, a heat pump is used for cooling, while engine waste heat is used for heating. In recent years, hybrid automobiles in which the amount of engine waste heat is small, and electric automobiles in which engine waste heat cannot be used, have become increasingly widespread. Accordingly, vehicle air conditioners using a heat pump not only for cooling but also for heating have been developed.
For example, Patent Literature 1 discloses an outdoor heat exchanger that is used in a heat pump-type vehicle air conditioner and that functions as an evaporator during the heating operation. In this outdoor heat exchanger, as shown in
The corrugated fin 120 includes a plurality of plate portions 121 arranged in a direction in which the flat tubes 110 extend, and a plurality of folded portions 122 joined to the flat tubes 110. Each plate portion 121 projects windward from the flat tubes 110. Each plate portion 121 has a plurality of louvers 130 formed by cutting and raising in a region lying between the flat tubes 110.
During the heating operation, frost is likely to be deposited on the windward end of the plate portion 121. When the plate portion 121 projects windward from the flat tubes 110 as shown in
In the outdoor heat exchanger of Patent Literature 1, however, heat actively transfers from the windward end of the plate portion 121 to the flat tubes 110. Therefore, there remains a possibility that frost is deposited concentratedly on the windward end of the plate portion 121.
In view of such circumstances, the present invention aims to reduce the deposition of frost during the heating operation in an outdoor heat exchanger used in heat pump-type vehicle air conditioners. The present invention also aims to provide a vehicle air conditioner using the outdoor heat exchanger.
That is, the present disclosure provides an outdoor heat exchanger that is used in a heat pump-type vehicle air conditioner switchable between cooling operation and heating operation and that exchanges heat between a refrigerant and outdoor air, the outdoor air heat exchanger including: flat tubes in which the refrigerant flows, the flat tubes having a cross-sectional shape extended in a first direction, the flat tubes being arranged in a second direction orthogonal to the first direction so as to face each other, wherein the outdoor air is caused to flow between the flat tubes from one side to the other in the first direction; and a corrugated fin disposed between the flat tubes adjacent to each other, the corrugated fin including: a plurality of plate portions arranged in a third direction orthogonal to the first direction and the second direction; and a plurality of folded portions joined alternately to the flat tubes adjacent to each other. Each of the plurality of plate portions has a plurality of louvers formed by cutting and raising, the plurality of louvers being inclined with respect to the first direction and being substantially continuous with each other in the first direction. Each of the plurality of plate portions has an extension portion projecting windward in the first direction from a joining region where the plurality of folded portions are joined to the flat tubes. A foremost louver that is located on the most windward side among the plurality of louvers is disposed entirely within the extension portion. Each of the plurality of plate portions has a front flat portion as a part of the extension portion, the front flat portion being located windward of the foremost louver. The front flat portion has an area larger than half of that of the extension portion.
In addition, the present disclosure provides a vehicle air conditioner including: a refrigeration circuit including a compressor that compresses a refrigerant, an indoor heat exchanger that exchanges heat between the refrigerant and air to be fed into a vehicle interior, an expansion mechanism that expands the refrigerant, and the above outdoor heat exchanger; and a switching means that switches a flow direction of the refrigerant flowing in the refrigeration circuit upon switching between heating operation and cooling operation.
According to the above configuration, a louver is disposed entirely within the extension portion of the plate portion that projects from the joining region. Therefore, heat transfer from the windward end of the plate portion to the joining region can be adequately reduced. Furthermore, since the front flat portion is formed to be longer than the foremost louver, heat exchange in the front flat portion can be restricted. Therefore, deposition of frost on the windward end of the plate portion can be reduced during the heating operation.
A first aspect of the present disclosure provides an outdoor heat exchanger that is used in a heat pump-type vehicle air conditioner switchable between cooling operation and heating operation and that exchanges heat between a refrigerant and outdoor air, the outdoor air heat exchanger including: flat tubes in which the refrigerant flows, the flat tubes having a cross-sectional shape extended in a first direction, the flat tubes being arranged in a second direction orthogonal to the first direction so as to face each other, wherein the outdoor air is caused to flow between the flat tubes from one side to the other in the first direction; and a corrugated fin disposed between the flat tubes adjacent to each other, the corrugated fin including: a plurality of plate portions arranged in a third direction orthogonal to the first direction and the second direction; and a plurality of folded portions joined alternately to the flat tubes adjacent to each other. Each of the plurality of plate portions has a plurality of louvers formed by cutting and raising, the plurality of louvers being inclined with respect to the first direction and being substantially continuous with each other in the first direction. Each of the plurality of plate portions has an extension portion projecting windward in the first direction from a joining region where the plurality of folded portions are joined to the flat tubes. A foremost louver that is located on the most windward side among the plurality of louvers is disposed entirely within the extension portion. Each of the plurality of plate portions has a front flat portion as a part of the extension portion, the front flat portion being located windward of the foremost louver. The front flat portion has an area larger than half of that of the extension portion.
A second aspect provides the outdoor heat exchanger as set forth in the first aspect, wherein the foremost louver is continuous with the front flat portion so as to form a ridge line between the front flat portion and the foremost louver. According to such a structure, no opening is formed between the windward end of the foremost louver and the front flat portion. Therefore, there is no possibility that such an opening is blocked by frost formation.
A third aspect provides the outdoor heat exchanger as set forth in the first aspect, wherein the plurality of louvers are inclined at an angle of 15 degrees or more and 25 degrees or less. According to such a structure, it is possible to improve the heat exchange efficiency during the cooling operation while decreasing the outdoor air pressure loss which gives an indication of frost formation.
A fourth aspect provides the outdoor heat exchanger as set forth in the first aspect, wherein each of the plurality of folded portions is formed in a shape having a flat central portion so as to be in surface contact with the flat tube. According to such a structure, it is possible to reduce the retention of water inside the folded portion during defrosting.
A fifth aspect provides the outdoor heat exchanger as set forth in any one of the first to fourth aspects, wherein each of the plurality of plate portions has a rear flat portion located leeward of a rearmost louver that is located on the most leeward side among the plurality of louvers, and the rear flat portion has a length greater than that of the front flat portion in the first direction. According to such a structure, improvement in terms of the remaining water ratio can be achieved by virtue of the greater length of the rear flat portion.
A sixth aspect provides the outdoor heat exchanger as set forth in any one of the first to fifth aspects, wherein the plurality of louvers form a windward louver group constituted by parallel louvers including the foremost louver and a leeward louver group constituted by louvers inclined in an opposite direction to inclination of the foremost louver with respect to the first direction, and the windward louver group and the leeward louver group are axisymmetric when viewed in the second direction. According to such a structure, the windward louver group and the leeward louver group can be arranged in a balanced manner.
A seventh aspect provides the outdoor heat exchanger as set forth in any one of the first to sixth aspects, further including a pair of headers that extend in the second direction and to which both ends of the flat tubes are connected, wherein the first direction and the second direction are horizontal directions, and the third direction is a vertical direction. According to such a structure, the outdoor heat exchanger can have a simplified structure, and water discharge after defrosting is easy.
An eighth aspect provides the outdoor heat exchanger as set forth in the seventh aspect, wherein one or more partition plates are provided inside each of the pair of headers so as to divide the flat tubes into a plurality of tube groups between which a flow direction of the refrigerant is alternately reversed, and the corrugated fin is disposed at least between the flat tubes that constitute an evaporation-upstream tube group in which the refrigerant flows first in the heating operation among the plurality of tube groups. According to such a structure, the evaporation-upstream tube group has the lowest temperature in the heating operation. Therefore, the aforementioned effects can be obtained also when the corrugated fin having the feature described in the first aspect is disposed only between the flat tubes that constitute the evaporation-upstream tube group.
Ninth aspect provides the outdoor heat exchanger as set forth in any one of the first to eighth aspects, wherein the entire foremost louver is disposed leeward of a center of the extension portion in the first direction. According to such a structure, an appropriate distance from the joining region to the windward end of the plate portion is ensured. Therefore, heat transfer from the windward end of the plate portion to the joining region can be adequately reduced.
A tenth aspect provides the outdoor heat exchanger as set forth in any one of the first to ninth aspects, wherein a part of the louver that is adjacent to the foremost louver is disposed at a position of a rear end of the extension portion in the first direction. According to such a structure, the entire foremost louver can be disposed within the extension portion with certainty.
An eleventh aspect provides the outdoor heat exchanger as set forth in any one of the first to tenth aspects, wherein the plurality of louvers have the same length in the second direction. According to such a structure, formation of the louvers is easy.
A twelfth aspect provides the outdoor heat exchanger as set forth in any one of the first to eleventh aspects, wherein the extension portion has a length of 1.5 mm or more and 3.5 mm or less in the first direction.
In the case of conventional configurations, frost is likely to be deposited on the windward end of the plate portion 121 during the heating operation. When the plate portion 121 projects windward from the flat tubes 110 as shown in
In view of such circumstances, the twelfth aspect aims to make it possible to achieve both reduction in frost deposition during the heating operation and good heat exchange efficiency during the cooling operation in an outdoor heat exchanger used in heat pump-type vehicle air conditioners.
Patent Literature 1 states that the length of the projection of the plate portion from the flat tube is about 2 to 5 mm. However, both ends of the flat tube are rounded, and the rounded portions make no contribution to heat transfer from the flat tube to the corrugated fin. That is, the plate portion is required to project from a region where the folded portion and the flat tube are in contact, but does not necessarily have to project from the flat tube. The twelfth aspect has been made from such a standpoint.
According to the twelfth aspect, the extension portion of the plate portion that projects from the joining region has a reduced length. Therefore, good heat exchange efficiency can be obtained during the cooling operation. In addition, since a louver is disposed within the extension portion, the amount of heat transferred from the joining region to the windward end of the plate portion can be decreased, and deposition of frost on the windward end can be reduced during the heating operation.
A thirteenth aspect provides a vehicle air conditioner including: a refrigeration circuit including a compressor that compresses a refrigerant, an indoor heat exchanger that exchanges heat between the refrigerant and air to be fed into a vehicle interior, an expansion mechanism that expands the refrigerant, and the outdoor heat exchanger according to any one of the first to twelfth aspects; and a switching means that switches a flow direction of the refrigerant flowing in the refrigeration circuit upon switching between heating operation and cooling operation.
Hereinafter, embodiments of the present invention will be described with reference to the drawings. The following description relates to illustrative examples of the present invention, and the present invention is not limited by these examples.
An outdoor heat exchanger 13 according to an embodiment of the present invention is shown in
<Vehicle Air Conditioner>
The vehicle air conditioner 10 is switchable between cooling operation and heating operation, and includes a refrigeration circuit 2 in which a refrigerant is circulated. As the refrigerant, R134a, R410A, HFO-1234yf, HFO-1234ze, CO2, or the like can be used. In addition, other HFC refrigerants, other HC refrigerants, and the like, can also be used.
The refrigeration circuit 2 includes a compressor 11, a four-way valve 12, the outdoor heat exchanger 13, an expansion valve 14, and an indoor heat exchanger 15. These devices 11 to 15 are connected by first to sixth flow paths 21 to 26. Specifically, a suction port 11a of the compressor 11 and a discharge port 11b of the compressor 11 are respectively connected to two ports of the four-way valve 12 via the sixth flow path 26 and the first flow path 21. The other two ports of the four-way valve 12 are respectively connected to the outdoor heat exchanger 13 and the indoor heat exchanger 15 via the second flow path 22 and the fifth flow path 25. The outdoor heat exchanger 13 and the indoor heat exchanger 15 are connected to the expansion valve 14 via the third flow path 23 and the fourth flow path 24, respectively. An accumulator may be provided on the sixth flow path 26.
The four-way valve 12 corresponds to the switching means of the present invention. In the cooling operation, the four-way valve 12 switches the flow direction of the refrigerant flowing in the refrigeration circuit 2 to a first direction indicated by a dashed arrow C, while in the heating operation, the four-way valve 12 switches the flow direction to a second direction indicated by a solid arrow H. The first direction is a direction in which the refrigerant discharged from the compressor 11 passes through the outdoor heat exchanger 13, the expansion valve 14, and the indoor heat exchanger 15 in this order to return to the compressor 11. The second direction is a direction in which the refrigerant discharged from the compressor 11 passes through the indoor heat exchanger 15, the expansion valve 14, and the outdoor heat exchanger 13 in this order to return to the compressor 11.
The compressor 11 is driven by an electric motor which is not shown, compresses the refrigerant drawn through the suction port 11a, and discharges the refrigerant through the discharge port 11b. The electric motor may be disposed inside the compressor 11 or may be disposed outside the compressor 11.
The outdoor heat exchanger 13 is disposed, for example, in a front portion of an automobile, and exchanges heat between the refrigerant and outdoor air supplied by travel of the vehicle and by a fan 17. The outdoor heat exchanger 13 functions as a condenser during the cooling operation, and functions as an evaporator during the heating operation.
The expansion valve 14 is an example of the expansion mechanism that expands the refrigerant. For example, a positive-displacement expander that recovers power from the refrigerant being expanded can be employed as the expansion mechanism.
The indoor heat exchanger 15 is disposed in a duct 32, and exchanges heat between the refrigerant and air to be fed into the vehicle interior by a blower 31. The air taken into the duct 32 by the blower 31 may be either outdoor air or indoor air or may include both outdoor air and indoor air. The indoor heat exchanger 15 functions as an evaporator during the cooling operation, and functions as a condenser during the heating operation.
<Outdoor Heat Exchanger>
As shown in
In the present embodiment, the X direction and the Y direction are horizontal directions, and the Z direction is a vertical direction. In other words, the pair of headers 4A and 4B extend in the horizontal direction, and the flat tubes 5 disposed between the headers extend in the vertical direction. The flat tubes 5 do not necessarily have to extend in the vertical direction, and may extend in an oblique direction or the horizontal direction. The pair of headers 4A and 4B do not necessarily have to extend in the horizontal direction, and my extend in the vertical direction.
Outdoor air is caused to flow between the flat tubes 5 from one side to the other in the X direction. In addition, a plurality of partition walls 50 (see
A corrugated fin 6 is disposed between the flat tubes 5 adjacent to each other. In the present embodiment, corrugated fins 6 of the same shape are disposed between all of the flat tubes 5. The corrugated fin 6 may be disposed between the outermost flat tube 5 and a side wall (not shown) facing the outermost flat tube 5.
The pair of headers 4A and 4B are provided with a first flow port 41 to which the second flow path 22 is connected and a second flow port 42 to which the third flow path 23 is connected. That is, during the cooling operation in which the outdoor heat exchanger 13 functions as a condenser, the first flow port 41 serves as an inflow port, and the second flow port 42 serves as an outflow port. During the heating operation in which the outdoor heat exchanger 13 functions as an evaporator, the second flow port 42 serves as an inflow port, and the first flow port 41 serves as an outflow port. In the present embodiment, the first flow port 41 is provided in the header 4A located on the upper side, and the second flow port 42 is provided in the header 4B located on the lower side.
One or more partition plates 45 are provided inside each of the pair of headers 4A and 4B, and thus the flat tubes 5 are divided into a plurality of tube groups 51 to 53 between which the flow direction of the refrigerant is alternately reversed. In
The plurality of tube groups 51 to 53 includes the evaporation-upstream tube group 51 closest to the second flow port 42, the evaporation-downstream tube group 52 closest to the first flow port 41, and one or more intermediate tube groups 53 located between the tube groups 51 and 52. The number of the tube groups 51 to 53 is, for example, 3 or more and 6 or less.
In the present embodiment, the first flow port 41 and the second flow port 42 are provided in the different headers. One partition plate 45 is provided inside each of the pair of headers 4A and 4B, and the number of the tube groups 51 to 53 is three which is an odd number. However, the number of the tube groups 51 to 53 may be an even number, and the first flow port 41 and the second flow port 42 may be provided in the same header.
The number of the flat tubes 5 constituting each of the tube groups 51 to 53 preferably increases from the evaporation-upstream tube group 51 to the evaporation-downstream tube group 52 in a stepwise fashion. For example, in the case where the number of the tube groups 51 to 53 is three as in the present embodiment, the evaporation-upstream tube group 51 may be constituted by nineteen flat tubes 5, the intermediate tube group 53 may be constituted by twenty one flat tubes 5, and the evaporation-downstream group 51 may be constituted by twenty two flat tubes 5.
Next, the corrugated fin 6 will be described in detail with reference to
The corrugated fin 6 includes a plurality of plate portions 6A arranged in the Z direction and a plurality of folded portions 6B joined alternately to the flat tubes 5 adjacent to each other. The plate portions 6A are in the shape of a rectangle extending in the X direction, and the folded portions 6B connect together the end portions of the plate portions 6A in the width direction. That is, one wave is formed by one plate portion 6A, halves of two plate portions 6A located on both sides of the one plate portion 6A, and two folded portions 6B between the plate portions 6A.
Such corrugated fins 6 are formed successively by a roller gear system. In the roller gear system, a material supplying device 91, a fin forming device 92, a fin pitch adjusting device 93, and a fin cutting device 94 are used in this order as shown in
In the present embodiment, each folded portion 6B is formed in a shape having a flat central portion so as to be in surface contact with the flat tube 5. However, the folded portion 6B may be curved overall so as to be in line contact with the flat tube 5.
Each plate portion 6A has an extension portion 60 that projects windward in the X direction from a joining region 8 where the folded portions 6B are joined to the flat tubes 5. In the present embodiment, the plate portion 6A projects also leeward from the joining region 8, and the leeward end of the plate portion 6A is located at the same position as the leeward end of the flat tube 5 in the X direction.
The extension portion 60 preferably has a length of 1.5 mm or more and 3.5 mm or less so that the windward end of the plate portion 6A is as close to the joining region 8 as possible in the X direction.
In addition, each plate portion 6A has a plurality of louvers 7 formed by cutting and raising, the louvers 7 being inclined with respect to the X direction and being substantially continuous with each other in the X direction. Here, “substantially continuous” is a concept that includes not only a situation where all the louvers are completely continuous with each other but also a situation where a flat portion having a length which is twice or less the distance between cuts for raising lies between certain louvers. In the present embodiment, all the louvers 7 are completely continuous with each other.
The louvers 7 form a windward louver group 71 and a leeward louver group 72. The windward louver group 71 is constituted by parallel louvers 7 including a foremost louver 7a that is located on the most windward side among the louvers 7. The leeward louver group 72 is constituted by louvers 7 inclined in an opposite direction to the inclination of the foremost louver 7a with respect to the X direction, and includes a rearmost louver 7b that is located on the most leeward side among the louvers 7. In the present embodiment, the windward louver group 71 and the leeward louver group 72 are axisymmetric when viewed in the Y direction. In addition, the windward louver group 71 and the leeward louver group 72 have the same length in the Y direction.
The louvers 7 of the windward louver group 71 other than the louvers located at both ends of the windward louver group 71, and the louvers 7 of the leeward louver group 72 other than the louvers located at both ends of the leeward louver group 72, are each a two-protrusion louver protruding from the plate portion 6A on both sides in the Z direction. By contrast, the foremost louver 7a, the rearmost louver 7b, the louver 7 at the rear end of the windward louver group 71, and the louver 7 at the front end of the leeward louver group 72, are each a one-protrusion louver protruding from the plate portion 6A only on one side in the Z direction. The two-protrusion louver is formed by pushing a region between a pair of cuts in such a manner that the region is rotated about a center line of the region. Therefore, the length of the two-protrusion louver in the inclination direction is equal to the cut-to-cut distance. The one-protrusion louver is formed by pushing a region between a base line (line spaced from a cut by a distance that is half of the cut-to-cut distance) and a cut in such a manner that the region is rotated about the base line. Therefore, the length of the one-protrusion louver in the inclination direction is equal to half of the cut-to-cut distance. Since such a formation method is employed, both ends of each louver 7 in the Y direction are continuous with the plate portion 6A via Z-direction drawn portions.
When the inclination angle of the louvers 7 is too small, the pressure loss of outdoor air, which gives an indication of frost formation, can be indeed decreased, but the heat exchange efficiency during the cooling operation is deteriorated. On the other hand, when the inclination angle of the louvers 7 is too large, the heat exchange efficiency can be indeed improved during the cooling operation, but the pressure loss of outdoor air is increased. From such standpoints, the inclination angle of the louvers 7 is preferably 15 degrees or more and 25 degrees or less.
Furthermore, in the present embodiment, the foremost louver 7a is disposed within the extension portion 60 of the plate portion 6A. The entire foremost louver 7a is located leeward of the center of the extension portion 60 in the X direction. Specifically, in the X direction, the leeward end of the foremost louver 7a coincides with the end of the joining region 8 or is located windward of the end of the joining region 8, so that the entire foremost louver 7a lies within in the extension portion 60. The louver 7 that is adjacent to the foremost louver 7a is disposed in such a manner that the position corresponding to ⅓ of the louver 7 from its windward end coincides with the position of the rear end of the extension portion 60 in the X direction.
In addition, each plate portion 6A has a front flat portion 61 as a part of the extension portion 60, the front flat portion 61 being located windward of the foremost louver 7a. Also, the plate portion 6A has a rear flat portion 62 located leeward of the rearmost louver 7b. The front flat portion 61 has an area larger than half of that of the extension portion 60. That is, the front flat portion 61 is formed to have a greater length than the foremost louver 7a in the X direction. Specifically, the length of the front flat portion 61 in the X direction is about twice the length of the foremost louver 7a in the X direction. From the standpoint of workability in the cutting and raising, the front flat portion 61 and the rear flat portion 62 preferably have a length of 1 mm or more. From the standpoint of water discharge performance during defrosting, a length L2 of the rear flat portion 62 is preferably greater than a length L1 of the front flat portion 61 in the X direction. More preferably, the length L2 of the rear flat portion 62 is 1.5 or more times the length L1 of the front flat portion 61. Even more preferably, the length L2 of the rear flat portion 62 is 2.0 or more times the length L1 of the front flat portion 61.
The foremost louver 7a is formed as a one-protrusion louver as mentioned above, and is thus continuous with the front flat portion 61 so as to form a ridge line between the front flat portion 61 and the foremost louver 7a. Similarly, the rearmost louver 7b is also continuous with the rear flat portion 62 so as to form a ridge line between the rear flat portion 62 and the rearmost louver 7b.
As described above, in the outdoor heat exchanger 13 of the present embodiment, the extension portion 60 of the plate portion 6A that projects from the joining region 8 has a reduced length. Therefore, good heat exchange efficiency can be obtained during the cooling operation. In addition, since the louver 7 is disposed entirely within the extension portion 60 of the plate portion 6A that projects from the joining region 8, heat transfer from the windward end of the plate portion 6A to the joining region 8 can be adequately reduced. Furthermore, since the front flat portion 61 is formed to be longer than the foremost louver 7a, heat exchange in the front flat portion 61 can be restricted. Therefore, deposition of frost on the windward end of the plate portion 6A can be reduced during the heating operation.
In addition, in the present embodiment, each folded portion 6B is formed in a shape having a flat central portion so as to be in surface contact with the flat tube 5. Therefore, it is possible to reduce the retention of water inside the folded portion 6B during defrosting.
(Simulation)
Hereinafter, simulations performed to confirm the effect of the present embodiment will be described.
First, two conditions employing R134a as a refrigerant were set as analysis conditions. The first condition was a frost formation condition for evaluation of frost formation during the heating operation, and was that the temperature of the refrigerant was set to −5° C., the dry-bulb temperature of outdoor air was set to 2° C., and the wet-bulb temperature of outdoor air was set to 1° C. The second condition was set for evaluation of performance during the cooling operation, on the assumption of non-occurrence of frost formation in the heating operation. That is, the second condition was a dry condition set by excluding the setting of the wet-bulb temperature from the frost formation condition. The reason why the performance during the cooling operation can be evaluated using the dry condition is as described below.
The heat transfer coefficient for the refrigerant differs between the above dry condition and the cooling operation because of the difference depending on whether the refrigerant is evaporated or condensed. However, there is no difference in the heat transfer coefficient for outdoor air since the heat transfer coefficient for outdoor air depends on the fin shape and the air velocity. The heat transmission coefficient used for calculating the amount of heat exchanged in the outdoor heat exchanger is determined as an inverse number of the sum of the refrigerant-side thermal resistance derived from the heat transfer coefficient for the refrigerant and the air-side thermal resistance derived from the heat transfer coefficient for the outdoor air. However, since the refrigerant-side thermal resistance is very much smaller than the air-side thermal resistance, the heat transmission coefficient can be considered the same between the dry condition and the cooling operation. Therefore, the amount of heat exchanged during the cooling operation can be estimated from the amount of heat exchanged under the dry condition.
Similarly, although the absolute value of the outdoor air pressure loss in the outdoor heat exchanger varies by about several percent between the dry condition and the cooling operation because of the difference in density depending on the temperature of incoming outdoor air, the pressure loss during the cooling operation can be estimated by comparative observation of the pressure loss under the dry condition.
Next, five models 1 to 5 having a basic configuration as shown in
Model 1: 4.3 mm/1.5 mm
Model 2: 3.3 mm/2.5 mm
Model 3: 2.9 mm/2.9 mm
Model 4: 2.3 mm/3.5 mm
Model 5: 1.8 mm/4.0 mm
Common dimensions were set as follows: the width (the long axis of the cross-sectional shape) of the flat tube 5 was 17.8 mm; the thickness (the short axis of the cross-sectional shape) of the flat tube 5 was 2.2 mm; the thickness of the corrugated fin 6 was 0.08 mm; the length of the corrugated fin 6 in the X direction was 19.8 mm; the width of the corrugated fin 6 in the Y direction was 8.9 mm; and the pitch between the plate portions 6A was 1.8 mm (i.e., the wavelength was 3.6 mm). Furthermore, the radius of the corner portion of the flat tube 5 was set to 0.9 mm, and the leeward end of the corrugated fin 6 was caused to coincide with the end of the flat tube 5 in the X direction. Therefore, the length of the extension portion 60 was 2.9 mm, and the length of the joining region 8 was 16.0 mm.
For the louvers 7, the cut-to-cut distance was set to 1.4 mm, the angle with respect to the X direction was set to 20 degrees. Thus, configurations as shown in
The velocity of outdoor air supplied to the outdoor heat exchanger was changed among 2.0 m/s, 4.0 m/s, and 6.0 m/s, and the amount of heat exchanged per unit air path cross-sectional area in the plate portion 6A and the outdoor air pressure loss were determined under the dry condition for each velocity. Among the results, those for the models 1, 3, and 5 are shown in
In order to provide verification from another standpoint,
It can be understood from
Next, the models 1, 4, and 5 were analyzed as to how the air path blockage ratio and the outdoor air pressure loss change over time due to frost formation under the frost formation condition at an outdoor air velocity of 2.5 m/s. The results are shown in
In addition, the models 3 and 5 were analyzed as to how the remaining water ratio changes over time in the case where defrosting of deposited frost is performed and then outdoor air is supplied to the outdoor heat exchanger at a velocity of 2.5 m/s. The results are shown in
Furthermore, five models 6 to 10 were prepared by modifications of the model 5; specifically, the pitch between the plate portions 6A was changed to 1.5 mm, and the inclination angle of the louvers 7 was varied. Specific values of the inclination angle were as follows.
Model 6: 30 degrees
Model 7: 25 degrees
Model 8: 20 degrees
Model 9: 15 degrees
Model 10: 10 degrees
For the models 6 to 10, the velocity of outdoor air supplied to the outdoor heat exchanger was changed among 2.0 m/s, 4.0 m/s, and 6.0 m/s, and the outdoor air pressure loss and the amount of heat exchanged per unit air path cross-sectional area were determined under the dry condition for each velocity.
Next, the models 6 to 10 were analyzed as to how the air path blockage ratio and the outdoor air pressure loss change over time due to frost formation under the frost formation condition at an outdoor air velocity of 2.5 m/s. The results are shown in
Furthermore, five models 11 to 15 were prepared by modifications of the model 5; specifically, the pitch between the plate portions 6A was changed to 1.5 mm, and the length of the extension portion 60 was varied with the positions of the louvers 7 being fixed relative to the flat tube 5. In other words, the length L1 of the front flat portion 61 was varied among the five models 11 to 15. The length of the extension portion 60/the length L1 of the front flat portion 61 in each of the models 11 to 15 was as follows.
Model 11: 1.5 mm/0.4 mm
Model 12: 1.9 mm/0.8 mm
Model 13: 2.9 mm/1.8 mm (same as in the model 5)
Model 14: 3.5 mm/2.4 mm
Model 15: 4.9 mm/3.8 mm
Next, for the models 11 to 15, the amount of heat exchanged per unit air path cross-sectional area and the outdoor air pressure loss were determined under the dry condition at an outdoor air velocity of 2.5 m/s.
It can be understood from
In addition, the models 11 to 15 were analyzed as to how the air path blockage ratio and the outdoor air pressure loss change over time due to frost formation under the frost formation condition at an outdoor air velocity of 2.5 m/s. The results are shown in
(Modification)
In the embodiment described above, the corrugated fins 6 having the foremost louver 7a disposed within the extension portion 60 are disposed between all of the flat tubes 5. However, since during the heating operation the evaporation-upstream tube group 51 in which the refrigerant flows first has the lowest temperature among the tube groups 51 to 53, it is sufficient that the corrugated fins 6 having the foremost louver 7a disposed within the extension portion 60 be disposed at least between the flat tubes 5 that constitute the evaporation-upstream tube group 51. For example, the corrugated fins 6 having the foremost louver 7a disposed within the extension portion 60 may be employed for only the evaporation-upstream tube group 51, and corrugated fins in which the foremost louver 7a is not disposed within the extension portion 60 may be employed for the other tube groups 52 and 53.
In addition, the foremost louver 7a does not necessarily have to be continuous with the front flat portion 61. For example, as shown in
In addition, for example, a central flat portion 63 located in the same plane as the front flat portion 61 and the rear flat portion 62 and having a length that is twice or less the cut-to-cut distance may be provided between the windward louver group 71 and the leeward louver group 72, as shown in
In addition, the configuration of the vehicle air conditioner 10 is not limited to that shown in
In the configuration shown in
In the configuration shown in
As the switching means that switches the flow direction of the refrigerant flowing in the refrigeration circuit 2, for example, a combination of two three-way valves, a so-called bridge circuit, or the like, can be used as well as the four-way valve 12.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2011-155580 | Jul 2011 | JP | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/JP2012/004492 | 7/11/2012 | WO | 00 | 1/10/2014 |
