Patent Grant
11892206
This application is a U.S. national stage application of International Patent Application No. PCT/JP2019/012903 filed on Mar. 26, 2019, the disclosure of which is incorporated herein by reference.
The present invention relates to a heat exchanger and a refrigeration cycle apparatus.
Japanese Patent Laying-Open No. 2018-059673 discloses a heat exchanger in which an inflow pipe and an outflow pipe connected to a distributor are each provided with flow rate control means. The flow rate control means controls a flow rate through each of the inflow pipe and the outflow pipe, to uniformly distribute gas-liquid two-phase refrigerant to heat transfer tubes disposed relatively above and heat transfer tubes disposed relatively below.
PTL 1: Japanese Patent Laying-Open No. 2018-059673
The heat exchanger described above, however, includes the flow rate control means in addition to the distributor, the heat transfer tubes, fins, and the like, and therefore has an increased size compared to a heat exchanger without the flow rate control means. The heat exchanger described above also requires a higher cost of manufacturing than a heat exchanger without the flow rate control means.
A main object of the present invention is to provide a heat exchanger and a refrigeration cycle apparatus, the heat exchanger being capable of uniformly distributing gas-liquid two-phase refrigerant to a heat transfer tube disposed relatively above and a heat transfer tube disposed relatively below, and having a reduced size compared to a conventional heat exchanger.
A refrigeration cycle apparatus according to the present invention includes a distributor, and a first heat transfer tube and a second heat transfer tube connected in parallel with each other with respect to the distributor. The first heat transfer tube is disposed above the second heat transfer tube. The first heat transfer tube has a first inner circumferential surface, and at least one first groove recessed relative to the first inner circumferential surface and arranged side by side in a circumferential direction of the heat transfer tube. The second heat transfer tube has a second inner circumferential surface, and at least one second groove recessed relative to the second inner circumferential surface and arranged side by side in a circumferential direction. An internal pressure loss of the first heat transfer tube is smaller than an internal pressure loss of the second heat transfer tube.
According to the present invention, a heat exchanger and a refrigeration cycle apparatus can be provided, the heat exchanger being capable of uniformly distributing gas-liquid two-phase refrigerant to a heat transfer tube disposed relatively above and a heat transfer tube disposed relatively below, and having a reduced size compared to a conventional heat exchanger.
Embodiments of the present invention will be described hereinafter in detail with reference to the drawings. The same or corresponding parts in the drawings are designated by the same characters and a description thereof will not be repeated in principle.
<Configuration of Refrigeration Cycle Apparatus>
As shown in
Compressor 101 has a discharge port through which to discharge the refrigerant, and a suction port through which to suck the refrigerant. Decompression unit 103 is an expansion valve, for example. Decompression unit 103 is connected to a third inflow/outflow portion 5 of first heat exchanger 1.
Four-way valve 102 has a first opening P1 connected to the discharge port of compressor 101 via a discharge pipe, a second opening P2 connected to the suction port of compressor 101 via a suction pipe, a third opening P3 connected to a first inflow/outflow portion 6a and a second inflow/outflow portion 6b of first heat exchanger 1, and a fourth opening P4 connected to second heat exchanger 11. Four-way valve 102 is provided to switch between a first state in which first heat exchanger 1 serves as a condenser and second heat exchanger 11 serves as an evaporator, and a second state in which second heat exchanger 11 serves as a condenser and first heat exchanger 1 serves as an evaporator. Note that solid line arrows shown in
<Configuration of First Heat Exchanger>
As shown in
As shown in
Each of the plurality of second heat transfer tubes 3b is disposed above each of the plurality of third heat transfer tubes 4, for example. Here, each of the plurality of second heat transfer tubes 3b being disposed above each of the plurality of third heat transfer tubes 4 means that, in the second state in which first heat exchanger 1 serves as an evaporator, the flow inlet through which the refrigerant flows into each second heat transfer tube 3b is disposed above a flow inlet through which the refrigerant flows into each third heat transfer tube 4.
As shown in
As shown in
As shown in
First heat transfer tubes 3a connected in series with one another via first connection portion 21a form a first refrigerant flow path. Second heat transfer tubes 3b connected in series with one another via second connection portion 21b form a second refrigerant flow path. The plurality of third heat transfer tubes 4 connected in series with one another via third connection portion 22 form a third refrigerant flow path. The first refrigerant flow path is disposed above the second refrigerant flow path. The second refrigerant flow path is disposed above the third refrigerant flow path, for example.
The first refrigerant flow path and the second refrigerant flow path form branched paths diverging from the third refrigerant flow path. The first refrigerant flow path and the second refrigerant flow path are connected in series with the third refrigerant flow path via distributor 10. First heat transfer tubes 3a and second heat transfer tubes 3b are connected in parallel with each other with respect to distributor 10. First heat transfer tubes 3a and second heat transfer tubes 3b are each connected in series with the plurality of third heat transfer tubes 4 via distributor 10.
The first refrigerant flow path has one end connected to first port P5 of distributor 10. The second refrigerant flow path has one end connected to second port P6 of distributor 10. The first refrigerant flow path has the other end connected to first inflow/outflow portion 6a. The second refrigerant flow path has the other end connected to second inflow/outflow portion 6b. The first refrigerant flow path has the other end connected to third opening P3 in four-way valve 102 via first inflow/outflow portion 6a. The second refrigerant flow path has the other end connected to third opening P3 in four-way valve 102 via second inflow/outflow portion 6b. The first refrigerant flow path connecting first port P5 of distributor 10 to first inflow/outflow portion 6a has a flow path length equal to that of the second refrigerant flow path connecting second port P6 of distributor 10 to second inflow/outflow portion 6b, for example. The third refrigerant flow path has one end connected to decompression unit 103 via third inflow/outflow portion 5. The third refrigerant flow path has the other end connected to respective one ends of the first refrigerant flow path and the second refrigerant flow path via distributor 10.
As shown in
Each first heat transfer tube 3a has an outer shape identical to that of each second heat transfer tube 3b, for example. Each first heat transfer tube 3a has an outer diameter equal to that of each second heat transfer tube 3b, for example. Each third heat transfer tube 4 has an outer shape identical to that of each first heat transfer tube 3a and each second heat transfer tube 3b, for example. Each third heat transfer tube 4 has an outer diameter equal to that of each first heat transfer tube 3a and each second heat transfer tube 3b, for example.
As shown in
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As shown in
The depth of each first groove 31a (described later in detail) is equal to the depth of each second groove 31b, for example. The lead angle of each first groove 31a (described later in detail) is equal to the lead angle of each second groove 31b, for example. The tube thickness of each first heat transfer tube 3a (described later in detail) is equal to the tube thickness of each second heat transfer tube 3b, for example.
As shown in
The number of third grooves 41 is defined as the number of third grooves 41 arranged side by side in the circumferential direction in a cross section perpendicular to the axial direction of third heat transfer tube 4. As described above, preferably, the internal pressure loss of the plurality of first heat transfer tubes 3a is greater than the internal pressure loss of the plurality of third heat transfer tubes 4. Preferably, the number of first grooves 31a is higher than the number of third grooves 41. Stated another way, preferably, the width of each third groove 41 in the circumferential direction is greater than the width of each first groove 31a in the circumferential direction.
<Flow of Refrigerant Through First Heat Exchanger 1>
When refrigeration cycle apparatus 100 is in the first state, first heat exchanger 1 serves as a condenser. In this case, first inflow/outflow portion 6a and second inflow/outflow portion 6b are connected in parallel with each other with respect to the discharge port of compressor 101. Thus, some of the refrigerant discharged from compressor 101 flows into the first refrigerant flow path through first inflow/outflow portion 6a, and the rest of the refrigerant flows into the second refrigerant flow path through second inflow/outflow portion 6b. The refrigerant that has flowed into the first refrigerant flow path exchanges heat with air and condenses while flowing through first heat transfer tubes 3a, to gradually decrease in its degree of dryness. The refrigerant that has flowed into the second refrigerant flow path exchanges heat with air and condenses while flowing through second heat transfer tubes 3b, to gradually decrease in its degree of dryness. The refrigerants that have flowed through the first refrigerant flow path and the second refrigerant flow path merge at distributor 10 and flow into the third refrigerant flow path. The refrigerant that has flowed into the third refrigerant flow path exchanges heat with air and condenses while flowing through third heat transfer tubes 4, to further decrease in its degree of dryness. The refrigerant that has flowed through the third refrigerant flow path flows out of first heat exchanger 1 through third inflow/outflow portion 5, and flows into decompression unit 103.
When refrigeration cycle apparatus 100 is in the second state, first heat exchanger 1 serves as an evaporator. In this case, all of the refrigerant decompressed in decompression unit 103 flows into the third refrigerant flow path through third inflow/outflow portion 5. The refrigerant that has flowed into the third refrigerant flow path exchanges heat with air and evaporates while flowing through third tube portions 3, to gradually increase in its degree of dryness. The gas-liquid two-phase refrigerant that has flowed through the third refrigerant flow path is branched at distributor 10 so that some of the refrigerant flows into the first refrigerant flow path, and the rest of the refrigerant flows into the second refrigerant flow path. The gas-liquid two-phase refrigerant that has flowed into the first refrigerant flow path exchanges heat with air and further evaporates while flowing through first heat transfer tubes 3a, to further increase in the degree of dryness. The gas-liquid two-phase refrigerant that has flowed into the second refrigerant flow path exchanges heat with air and further evaporates while flowing through second heat transfer tubes 3b, to further increase in the degree of dryness. The refrigerant that has flowed through each of the first refrigerant flow path and the second refrigerant flow path flows out of first heat exchanger 1 through first inflow/outflow portion 6a and second inflow/outflow portion 6b, and flows into the suction port of compressor 101.
<Performance of Distribution of Gas-Liquid Two-Phase Refrigerant in First Heat Exchanger 1>
In gas-liquid two-phase refrigerant, the specific gravity of gas-phase refrigerant is lower than the specific gravity of liquid-phase refrigerant. Therefore, if distributor 10 distributes gas-liquid two-phase refrigerant to the first refrigerant flow path disposed relatively above and the second refrigerant flow path disposed relatively below, and the internal pressure loss of the heat transfer tubes forming the first refrigerant flow path is equal to the internal pressure loss of the heat transfer tubes forming the second refrigerant flow path, the gas-phase refrigerant in the gas-liquid two-phase refrigerant flows in a greater amount through the second refrigerant flow path than through the first refrigerant flow path, and the liquid-phase refrigerant flows in a greater amount through the second refrigerant flow path than through the first refrigerant flow path. Accordingly, in the refrigerant flow path disposed above, the flow rate of the liquid-phase refrigerant becomes too low with respect to heat exchange capacity, resulting in an increased degree of overheating at the outlet. In the refrigerant flow path disposed below, on the other hand, the flow rate of the liquid-phase refrigerant becomes too high with respect to heat exchange capacity, resulting in the liquid-phase refrigerant flowing out without completely evaporating. As a result, such a heat exchanger has reduced performance.
In contrast, in first heat exchanger 1, the internal pressure loss of first heat transfer tubes 3a forming the first refrigerant flow path disposed above is smaller than the internal pressure loss of second heat transfer tubes 3b forming the second refrigerant flow path disposed below the first refrigerant flow path. In first heat exchanger 1, therefore, the difference in flow rate between the liquid-phase refrigerants flowing through first heat transfer tubes 3a and second heat transfer tubes 3b is reduced compared to that of the conventional heat exchanger described above. As a result, first heat exchanger 1 has improved heat exchange performance compared to that of the conventional heat exchanger described above.
Further, in first heat exchanger 1, because the number of first grooves 31a is less than the number of second grooves 31b, the internal pressure loss of first heat transfer tube 3a is set to be smaller than the internal pressure loss of second heat transfer tube 3b. In other words, the internal pressure loss of first heat transfer tube 3a is set to be smaller than the internal pressure loss of second heat transfer tube 3b, while first heat transfer tube 3a has an outer diameter equal to that of second heat transfer tube 3b, and each through hole in fin 2 through which each of first heat transfer tube 3a and second heat transfer tube 3b is inserted has a constant diameter. Thus, first heat exchanger 1 is readily assembled as compared to, for example, a heat exchanger in which the outer diameter and inner diameter of a heat transfer tube are varied with location in order to reduce pressure loss.
<Pressure Loss of Refrigerant in First Heat Exchanger 1>
Pressure loss of refrigerant increases with an increase in specific volume of the refrigerant, and with an increase in flow rate of the refrigerant. Further, pressure loss of refrigerant increases with an increase in flow path resistance of a heat transfer tube through which the refrigerant flows.
In the first state, the refrigerant that has been discharged from compressor 101 and having a high degree of dryness flows into first heat transfer tube 3a and second heat transfer tube 3b, and the refrigerant that has condensed in first heat transfer tube 3a and second heat transfer tube 3b and having a reduced degree of dryness flows into third heat transfer tube 4. Thus, the specific volume of the refrigerant flowing through each of first heat transfer tube 3a and second heat transfer tube 3b is higher than the specific volume of the refrigerant flowing through each third heat transfer tube 4. Further, because the number of each of first grooves 31a and second grooves 31b is higher than the number of third grooves 41, the flow path resistance of each of first heat transfer tube 3a and second heat transfer tube 3b is higher than the flow path resistance of third heat transfer tube 4. On the other hand, the flow rate of the refrigerant flowing through each of first heat transfer tube 3a and second heat transfer tube 3b is lower than, for example, about one-half of, the flow rate of the refrigerant flowing through each third heat transfer tube 4.
In other words, the specific volume of the refrigerant flowing through each of first heat transfer tube 3a and second heat transfer tube 3b and the flow path resistances of first heat transfer tube 3a and second heat transfer tube 3b caused by first grooves 31a and second grooves 31b are higher than the specific volume of the refrigerant flowing through each third heat transfer tube 4 and the flow path resistance of each third heat transfer tube 4 caused by third grooves 41. In contrast, the flow rate through each of first heat transfer tube 3a and second heat transfer tube 3b is lower than the flow rate through each third heat transfer tube 4. Thus, increase in pressure loss of the refrigerant in first heat transfer tube 3a and second heat transfer tube 3b is suppressed.
On the other hand, the flow rate through each third heat transfer tube 4 is higher than the flow rate through each of first heat transfer tube 3a and second heat transfer tube 3b. In contrast, the specific volume of the refrigerant flowing through each third heat transfer tube 4 and the flow path resistance of each third heat transfer tube 4 caused by third grooves 41 are lower than the specific volume of the refrigerant flowing through each of first heat transfer tube 3a and second heat transfer tube 3b and the flow path resistances of first heat transfer tube 3a and second heat transfer tube 3b caused by first grooves 31a and second grooves 31b. Thus, increase in pressure loss of the refrigerant in each third heat transfer tube 4 is suppressed.
In the second state, the refrigerant that has been decompressed in decompression unit 103 and having a low degree of dryness flows into third heat transfer tube 4. The refrigerant that has evaporated in third heat transfer tube 4 and having an increased degree of dryness is branched at distributor 10 into first heat transfer tube 3a and second heat transfer tube 3b. Thus, while the flow rate of the refrigerant through each third heat transfer tube 4 is higher than the flow rate of the refrigerant through each of first heat transfer tube 3a and second heat transfer tube 3b, the specific volume of the refrigerant flowing through each third heat transfer tube 4 is lower than the specific volume of the refrigerant flowing through each of first heat transfer tube 3a and second heat transfer tube 3b. Further, because the number of third grooves 41 is lower than the number of each of first grooves 31a and second grooves 31b, the flow path resistance of third heat transfer tube 4 is lower than the flow path resistance of each of first heat transfer tube 3a and second heat transfer tube 3b.
In other words, the flow rate through each third heat transfer tube 4 is lower than the flow rate through each of first heat transfer tube 3a and second heat transfer tube 3b. In contrast, the specific volume of the refrigerant flowing through each third heat transfer tube 4 and the flow path resistance of each third heat transfer tube 4 caused by third grooves 41 are lower than the specific volume of the refrigerant flowing through each of first heat transfer tube 3a and second heat transfer tube 3b and the flow path resistance of each of first heat transfer tube 3a and second heat transfer tube 3b caused by first grooves 31a and second grooves 31b. Thus, increase in pressure loss of the refrigerant in each third heat transfer tube 4 is suppressed.
On the other hand, the flow path resistance of each of first heat transfer tube 3a and second heat transfer tube 3b is higher than the flow path resistance of third heat transfer tube 4. In contrast, the flow rate through each of first heat transfer tribe 3a and second heat transfer tube 3b is lower than the flow rate through each third heat transfer tube 4. Thus, increase in pressure loss of the refrigerant in each of first heat transfer tube 3a and second heat transfer tube 3b is suppressed.
In this manner, in the first state and the second state, the pressure loss of the refrigerant in entire first heat exchanger 1 is kept relatively low. In particular, the pressure loss of the refrigerant in entire first heat exchanger 1 is kept lower than the pressure loss of the refrigerant in the entire heat exchanger in which the entire heat transfer tube is a grooved tube similar to second heat transfer tube 3b.
In other words, in first heat exchanger 1, reduction in heat exchange performance is suppressed in the entire heat exchanger, while pressure loss of the refrigerant is reduced in the entire heat exchanger, as compared to a conventional heat exchanger.
By including first heat exchanger 1 described above, refrigeration cycle apparatus 100 is more efficient than a conventional refrigeration cycle apparatus.
A refrigeration cycle apparatus and a first heat exchanger according to a second embodiment basically have similar configurations to refrigeration cycle apparatus 100 and first heat exchanger 1 according to the first embodiment, but are different in that the depth of each first groove 31a is less than the depth of each second groove 31b.
In the first heat exchanger according to the second embodiment, the number of first grooves 31a in the cross section perpendicular to the axial direction of first heat transfer tube 3a is equal to the number of second grooves 31b in the cross section perpendicular to the axial direction of second heat transfer tube 3b, for example.
As shown in
In the first heat exchanger according to the second embodiment, depth H1 of each first groove 31a is less than depth H2 of each second groove 31b. The area of the inner surfaces of first grooves 31a is less than the area of the inner surfaces of second grooves 31b. Thus, as in first heat exchanger 1 according to the first embodiment, also in the first heat exchanger according to the second embodiment, the internal pressure loss of first heat transfer tube 3a is smaller than the internal pressure loss of second heat transfer tube 3b, and the difference in flow rate between the liquid-phase refrigerants flowing through first heat transfer tube 3a and second heat transfer tube 3b is reduced compared to that of the conventional heat exchanger described above. As a result, the first heat exchanger according to the second embodiment also has improved heat exchange performance compared to that of the conventional heat exchanger described above.
The depth of each third groove is less than depth H1 of each first groove 31a. The flow path resistance of first heat transfer tube 3a is higher than the flow path resistance of third heat transfer tube 4. Thus, the pressure loss of the refrigerant in the entire first heat exchanger according to the second embodiment is kept lower than the pressure loss of the refrigerant in the entire heat exchanger in which the entire heat transfer tube is a grooved tube similar to second heat transfer tube 3b.
In this manner, the first heat exchanger according to the second embodiment can produce similar effects to those of first heat exchanger 1 according to the first embodiment.
As in first heat exchanger 1 according to the first embodiment, also in the first heat exchanger according to the second embodiment, the number of first grooves 31a in the cross section perpendicular to the axial direction of first heat transfer tube 3a may be less than the number of second grooves 31b in the cross section perpendicular to the axial direction of second heat transfer tube 3b, for example. In such a first heat exchanger, the difference in internal pressure loss between first heat transfer tube 3a and second heat transfer tube 3b that is required to reduce the difference in flow rate between the liquid-phase refrigerants flowing through first heat transfer tube 3a and second heat transfer tube 3b is designed by the difference in each of two parameters, which are the numbers and the depths of first grooves 31a and second grooves 31b. Therefore, even when it is difficult to design the difference in internal pressure loss only by the difference in one of the two parameters, for example, the difference in internal pressure loss is relatively readily achieved.
A refrigeration cycle apparatus and a first heat exchanger according to a third embodiment basically have similar configurations to refrigeration cycle apparatus 100 and first heat exchanger 1 according to the first embodiment, but are different in that the lead angle of each first groove 31a is less than the lead angle of each second groove 31b.
In the first heat exchanger according to the third embodiment, the number of first grooves 31a in the cross section perpendicular to the axial direction of first heat transfer tube 3a is equal to the number of second grooves 31b in the cross section perpendicular to the axial direction of second heat transfer tube 3b, for example. In addition, in the first heat exchanger according to the third embodiment, depth H1 of each first groove 31a is equal to depth H2 of each second groove 31b, for example.
As shown in
As shown in
In the first heat exchanger according to the third embodiment, lead angle θ1 of each first groove 31a is less than lead angle θ2 of each second groove 31b. The length of each such first groove 31a in the extension direction is less than the length of each second groove 31b in the extension direction. Thus, when the number and the depth of first grooves 31a are equal to or less than the number and the depth of second grooves 31b, the area of the inner surfaces of first grooves 31a is less than the area of the inner surfaces of second grooves 31b. Thus, as in first heat exchanger 1 according to the first embodiment, also in the first heat exchanger according to the third embodiment, the internal pressure loss of first heat transfer tube 3a is smaller than the internal pressure loss of second heat transfer tube 3b, and the difference in flow rate between the liquid-phase refrigerants flowing through first heat transfer tube 3a and second heat transfer tube 3b is reduced compared to that of the conventional heat exchanger described above. As a result, the first heat exchanger according to the third embodiment also has improved heat exchange performance compared to that of the conventional heat exchanger described above.
The lead angle of each third groove is less than lead angle θ1 of each first groove 31a. Thus, the flow path resistance of first heat transfer tube 3a is higher than the flow path resistance of third heat transfer tube 4. Thus, the pressure loss of the refrigerant in the entire first heat exchanger according to the third embodiment is kept lower than the pressure loss of the refrigerant in the entire heat exchanger in which the entire heat transfer tube is a grooved tube similar to second heat transfer tube 3b.
In this manner, the first heat exchanger according to the third embodiment can produce similar effects to those of first heat exchanger 1 according to the first embodiment.
As in first heat exchanger 1 according to the first embodiment, also in the first heat exchanger according to the third embodiment, the number of first grooves 31a in the cross section perpendicular to the axial direction of first heat transfer tube 3a may be less than the number of second grooves 31b in the cross section perpendicular to the axial direction of second heat transfer tube 3b, for example. In such a first heat exchanger, the difference in internal pressure loss between first heat transfer tube 3a and second heat transfer tube 3b that is required to reduce the difference in flow rate between the liquid-phase refrigerants flowing through first heat transfer tube 3a and second heat transfer tube 3b is designed by the difference in each of two parameters, which are the numbers and the lead angles of first grooves 31a and second grooves 31b. Therefore, even when it is difficult to design the difference in internal pressure loss only by the difference in one of the two parameters, for example, the difference in internal pressure loss is relatively readily achieved.
As in first heat exchanger 1 according to the second embodiment, also in the first heat exchanger according to the third embodiment, depth H1 of each first groove 31a may be less than depth H2 of each second groove 31b. In such a first heat exchanger, the difference in internal pressure loss between first heat transfer tube 3a and second heat transfer tube 3b that is required to reduce the difference in flow rate between the liquid-phase refrigerants flowing through first heat transfer tube 3a and second heat transfer tube 3b is designed by the difference in each of two parameters, which are the depths and the lead angles of first grooves 31a and second grooves 31b. Therefore, even when it is difficult to design the difference in internal pressure loss only by the difference in one of the two parameters, for example, the difference in internal pressure loss is relatively readily achieved.
A refrigeration cycle apparatus and a first heat exchanger according to a fourth embodiment basically have similar configurations to refrigeration cycle apparatus 100 and first heat exchanger 1 according to the first embodiment, but are different in that the tube thickness of each first heat transfer tube 3a is less than the tube thickness of each second heat transfer tube 3b.
First heat transfer tube 3a has an outer diameter equal to that of second heat transfer tube 3b. The number of first grooves 31a in the cross section perpendicular to the axial direction of first heat transfer tube 3a is equal to the number of second grooves 31b in the cross section perpendicular to the axial direction of second heat transfer tube 3b, for example. In the first heat exchanger according to the fourth embodiment, depth H1 of each first groove 31a is equal to depth H2 of each second groove 31b, for example. In the first heat exchanger according to the fourth embodiment, lead angle θ1 of each first groove 31a is equal to lead angle θ2 of each second groove 31b, for example.
As shown in
As shown in
In the first heat exchanger according to the fourth embodiment, tube thickness W1 of each first heat transfer tube 3a is smaller than tube thickness W2 of each second heat transfer tube 3b. Also in this case, because first heat transfer tube 3a has an outer diameter equal to that of second heat transfer tube 3b, an internal flow path cross-sectional area of first heat transfer tube 3a is less than an internal flow path cross-sectional area of second heat transfer tube 3b. Thus, as in first heat exchanger 1 according to the first embodiment, also in the first heat exchanger according to the fourth embodiment, the internal pressure loss of first heat transfer tube 3a is smaller than the internal pressure loss of second heat transfer tube 3b, and the difference in flow rate between the liquid-phase refrigerants flowing through first heat transfer tube 3a and second heat transfer tube 3b is reduced compared to that of the conventional heat exchanger described above. As a result, the first heat exchanger according to the fourth embodiment also has improved heat exchange performance compared to that of the conventional heat exchanger described above.
The tube thickness of third heat transfer tube 4 is less than tube thickness W1 of first heat transfer tube 3a. Third heat transfer tube 4 has an outer diameter equal to that of first heat transfer tube 3a. Thus, the internal pressure loss of first heat transfer tube 3a is higher than the internal pressure loss of third heat transfer tube 4. As a result, the pressure loss of the refrigerant in the entire first heat exchanger according to the fourth embodiment is kept lower than the pressure loss of the refrigerant in the entire heat exchanger in which the entire heat transfer tube is a grooved tube similar to second heat transfer tube 3b.
In this manner, the first heat exchanger according to the fourth embodiment can produce similar effects to those of first heat exchanger 1 according to the first embodiment.
As in first heat exchanger 1 according to the first embodiment, also in the first heat exchanger according to the fourth embodiment, the number of first grooves 31a in the cross section perpendicular to the axial direction of first heat transfer tube 3a may be less than the number of second grooves 31b in the cross section perpendicular to the axial direction of second heat transfer tube 3b, for example. In such a first heat exchanger, the difference in internal pressure loss between first heat transfer tube 3a and second heat transfer tube 3b that is required to reduce the difference in flow rate between the liquid-phase refrigerants flowing through first heat transfer tube 3a and second heat transfer tube 3b is designed by the difference in each of two parameters, which are the numbers of first grooves 31a and second grooves 31b, and the tube thicknesses of first heat transfer tube 3a and second heat transfer tube 3b. Therefore, even when it is difficult to design the difference in internal pressure loss only by the difference in one of the two parameters, for example, the difference in internal pressure loss is relatively readily achieved.
As in first heat exchanger 1 according to the second embodiment, also in the first heat exchanger according to the fourth embodiment, depth H1 of each first groove 31a may be less than depth H2 of each second groove 31b. In such a first heat exchanger, the difference in internal pressure loss between first heat transfer tube 3a and second heat transfer tube 3b that is required to reduce the difference in flow rate between the liquid-phase refrigerants flowing through first heat transfer tube 3a and second heat transfer tube 3b is designed by the difference in each of two parameters, which are the depths of first groove 31a and second groove 31b, and the tube thicknesses of first heat transfer tube 3a and second heat transfer tube 3b. Therefore, even when it is difficult to design the difference in internal pressure loss only by the difference in one of the two parameters, for example, the difference in internal pressure loss is relatively readily achieved.
As in first heat exchanger 1 according to the third embodiment, also in the first heat exchanger according to the fourth embodiment, lead angle θ1 of each first groove 31a may be less than lead angle θ2 of each second groove 31b. In such a first heat exchanger, the difference in internal pressure loss between first heat transfer tube 3a and second heat transfer tube 3b that is required to reduce the difference in flow rate between the liquid-phase refrigerants flowing through first heat transfer tube 3a and second heat transfer tube 3b is designed by the difference in each of two parameters, which are the lead angles of first groove 31a and second groove 31b, and the tube thicknesses of first heat transfer tube 3a and second heat transfer tube 3b. Therefore, even when it is difficult to design the difference in internal pressure loss only by the difference in one of the two parameters, for example, the difference in internal pressure loss is relatively readily achieved.
A refrigeration cycle apparatus and a first heat exchanger according to a fifth embodiment basically have similar configurations to refrigeration cycle apparatus 100 and first heat exchanger 1 according to the first embodiment, but are different in that the number of first grooves 31a is less than the number of second grooves 31b, that depth H1 of each first groove 31a is less than depth H2 of each second groove 31b, that lead angle θ1 of each first groove 31a is less than lead angle θ2 of each second groove 31b, and that tube thickness W1 of each first heat transfer tube 3a is less than tube thickness W2 of each second heat transfer tube 3b.
The first heat exchanger according to the fifth embodiment also basically has a similar configuration to the first heat exchangers according to the first to fourth embodiments described above, and can therefore produce similar effects to those of the first heat exchangers according to the first to fourth embodiments.
In addition, in the first heat exchanger according to the fifth embodiment, the difference in internal pressure loss between first heat transfer tube 3a and second heat transfer tube 3b that is required to reduce the difference in flow rate between the liquid-phase refrigerants flowing through first heat transfer tube 3a and second heat transfer tube 3b is designed by the difference in each of four parameters, which are the numbers, the depths, and the lead angles of first grooves 31a and second grooves 31b, and the tube thicknesses of first heat transfer tube 3a and second heat transfer tube 3b. Therefore, even when it is difficult to design the difference in internal pressure loss only by the differences in three of the four parameters, for example, the difference in internal pressure loss is relatively readily achieved.
As described above, in the first heat exchangers according to the first to fifth embodiments, at least one of the number, the depth, and the lead angle of the plurality of first grooves 31a, and the tube thickness of the plurality of first heat transfer tubes 3a is less than at least one of the number, the depth, and the lead angle of the plurality of second grooves 31b, and the tube thickness of the plurality of second heat transfer tubes 3b.
In addition, in the first heat exchangers according to the first to fifth embodiments, at least one of the number, the depth, and the lead angle of the plurality of first grooves 31a, and the tube thickness of the plurality of first heat transfer tubes 3a exceeds at least one of the number, the depth, and the lead angle of the plurality of third grooves 41, and the tube thickness of the plurality of third heat transfer tubes 4.
A refrigeration cycle apparatus and a first heat exchanger according to a sixth embodiment basically have similar configurations to refrigeration cycle apparatus 100 and first heat exchanger 1 according to the first embodiment, but are different in further including a plurality of fourth heat transfer tubes 3c and a plurality of fifth heat transfer tubes 3d connected in parallel with the plurality of first heat transfer tubes 3a and the plurality of second heat transfer tubes 3b.
Each of the plurality of fourth heat transfer tubes 3c is disposed above each of the plurality of third heat transfer tubes 4 and below each of the plurality of second heat transfer tubes 3b, for example. In other words, in the second state in which first heat exchanger 1 serves as an evaporator, a flow inlet through which the refrigerant flows into each fourth heat transfer tube 3c is disposed above the flow inlet through which the refrigerant flows into each third heat transfer tube 4 and below the flow inlet through which the refrigerant flows into each second heat transfer tube 3b.
Each of the plurality of fifth heat transfer tubes 3d is disposed above each of the plurality of third heat transfer tubes 4 and below each of the plurality of fourth heat transfer tubes 3c, for example. In other words, in the second state in which first heat exchanger 1 serves as an evaporator, a flow inlet through which the refrigerant flows into each fifth heat transfer tube 3d is disposed above the flow inlet through which the refrigerant flows into each third heat transfer tube 4 and below the flow inlet through which the refrigerant flows into each fourth heat transfer tube 3c.
As shown in
As shown in
As shown in
First port P5, second port P6, fourth port P8 and fifth port P9 are disposed above third port P7. Distributor 10 has the refrigerant flow path connecting first port P5 to third port P7, the refrigerant flow path connecting second port P6 to third port P7, a refrigerant flow path connecting fourth port P8 to third port P7, and a refrigerant flow path connecting fifth port P9 to third port P7. The pressure loss of each refrigerant flow path within distributor 10 is set to be equal to one another, for example.
Fourth heat transfer tubes 3c connected in series with one another via seventh connection portion 21c form a fourth refrigerant flow path. Fifth heat transfer tubes 3d connected in series with one another via eighth connection portion 21d form a fifth refrigerant flow path. The fourth refrigerant flow path is disposed above the fifth refrigerant flow path. The fifth refrigerant flow path is disposed above the third refrigerant flow path.
The first refrigerant flow path, the second refrigerant flow path, the fourth refrigerant flow path and the fifth refrigerant flow path form branched paths diverging from the third refrigerant flow path. The first refrigerant flow path, the second refrigerant flow path, the fourth refrigerant flow path and the fifth refrigerant flow path are connected in series with the third refrigerant flow path via distributor 10. First heat transfer tubes 3a, second heat transfer tubes 3b, fourth heat transfer tubes 3c, and fifth heat transfer tubes 3d are connected in parallel with one another with respect to distributor 10. First heat transfer tubes 3a, second heat transfer tubes 3b, fourth heat transfer tubes 3c, and fifth heat transfer tubes 3d are each connected in series with the plurality of third heat transfer tubes 4 via distributor 10.
The third refrigerant flow path has one end connected to decompression unit 103 via third inflow/outflow portion 5. The third refrigerant flow path has the other end connected to one end of the first refrigerant flow path, one end of the second refrigerant flow path, one end of the fourth refrigerant flow path, and one end of the fifth refrigerant flow path via distributor 10. The first refrigerant flow path has the other end connected to third opening P3 in four-way valve 102 via first inflow/outflow portion 6a. The second refrigerant flow path has the other end connected to third opening P3 in four-way valve 102 via second inflow/outflow portion 6b. The fourth refrigerant flow path has the other end connected to third opening P3 in four-way valve 102 via a fourth inflow/outflow portion 6c. The fifth refrigerant flow path has the other end connected to third opening P3 in four-way valve 102 via a fifth inflow/outflow portion 6d.
The plurality of first heat transfer tubes 3a, the plurality of second heat transfer tubes 3b, the plurality of third heat transfer tubes 4, the plurality of fourth heat transfer tubes 3c, and the plurality of fifth heat transfer tubes 3d are each configured as a circular tube.
An internal pressure loss of the plurality of fourth heat transfer tubes 3c is greater than the internal pressure loss of the plurality of second heat transfer tubes 3b, and is smaller than an internal pressure loss of the plurality of fifth heat transfer tubes 3d. The internal pressure loss of the plurality of fifth heat transfer tubes 3d is greater than the internal pressure loss of the plurality of third heat transfer tubes 4.
Each fourth heat transfer tube 3c has a fourth inner circumferential surface which is not shown, and a plurality of fourth grooves which are not shown. The fourth inner circumferential surface is a surface that makes contact with the refrigerant flowing through fourth heat transfer tube 3c. Each fourth groove is recessed relative to the fourth inner circumferential surface. Each of the plurality of fourth grooves has a similar configuration, for example. The fourth grooves are spaced from one another in the circumferential direction of fourth heat transfer tube 3c. Each fourth groove is provided in spiral form with respect to central axis O of fourth heat transfer tube 3c. Each fourth groove intersects the radial direction of fourth heat transfer tube 3c. Each fourth groove is provided such that its width in the circumferential direction decreases toward the outer circumference of fourth heat transfer tube 3c in the radial direction, for example.
Each fifth heat transfer tube 3d has a fifth inner circumferential surface which is not shown, and a plurality of fifth grooves which are not shown. The fifth inner circumferential surface is a surface that makes contact with the refrigerant flowing through fifth heat transfer tube 3d. Each fifth groove is recessed relative to the fifth inner circumferential surface. Each of the plurality of fifth grooves has a similar configuration, for example. The fifth grooves are spaced from one another in the circumferential direction of fifth heat transfer tube 3d. Each fifth groove is provided in spiral form with respect to central axis O of fifth heat transfer tube 3d. Each fifth groove intersects the radial direction of fifth heat transfer tube 3d. Each fifth groove is provided such that its width in the circumferential direction decreases toward the outer circumference of fifth heat transfer tube 3d in the radial direction, for example.
Second heat transfer tube 3b and fourth heat transfer tube 3c have a relationship with each other, and fourth heat transfer tube 3c and fifth heat transfer tube 3d have a relationship with each other, that are similar to the relationship between first heat transfer tube 3a and second heat transfer tube 3b. In other words, at least one of the number, the depth, and the lead angle of second grooves 31b, and the tube thickness of second heat transfer tube 3b is less than at least one of the number, the depth, and the lead angle of the fourth grooves, and the tube thickness of fourth heat transfer tube 3c. At least one of the number, the depth, and the lead angle of the fourth grooves, and the tube thickness of fourth heat transfer tube 3c is less than at least one of the number, the depth, and the lead angle of the fifth grooves, and the tube thickness of fifth heat transfer tube 3d. Note that the number, the depth, and the lead angle of each of the fourth grooves and the fifth grooves are defined similarly to the number, the depth, and the lead angle of each of first grooves 31a and second grooves 31b. The tube thickness of each of fourth heat transfer tube 3c and fifth heat transfer tube 3d is defined similarly to the tube thickness of each of first heat transfer tube 3a and second heat transfer tube 3b.
The number of second grooves 31b exceeds the number of first grooves 31a, and is less than the number of the fourth grooves, for example. That is, any one of the parameters including the number, the depth, the lead angle, and the tube thickness that satisfies the above-described relationship of magnitude between first heat transfer tube 3a and second heat transfer tube 3b is the same as a parameter that satisfies the above-described relationship of magnitude between second heat transfer tube 3b and fourth heat transfer tube 3c, for example. In other words, first heat transfer tube 3a, second heat transfer tube 3b, and fourth heat transfer tube 3c are provided such that any one of these parameters including the number, the depth, the lead angle, and the tube thickness satisfies the above-described two-stage relationship of magnitude, for example. The number of second grooves 31b may exceed the number of first grooves 31a, and the depth of second grooves 31b may be less than the depth of the plurality of fourth grooves, for example. That is, any one of the parameters including the number, the depth, the lead angle, and the tube thickness that satisfies the above-described relationship of magnitude between first heat transfer tube 3a and second heat transfer tube 3b may be different from a parameter that satisfies the above-described relationship of magnitude between second heat transfer tube 3b and fourth heat transfer tube 3c. In the above-described case, the number of second grooves 31b may be equal to the number of the fourth grooves. In other words, second heat transfer tube 3b and fourth heat transfer tube 3c may be provided to be equal in any one of the parameters including the number, the depth, the lead angle, and the tube thickness that satisfies the above-described relationship of magnitude between first heat transfer tube 3a and second heat transfer tube 3b.
The number of the fourth grooves exceeds the number of second grooves 31b, and is less than the number of the fifth grooves, for example. That is, any one of the parameters including the number, the depth, the lead angle, and the tube thickness that satisfies the above-described relationship of magnitude between second heat transfer tube 3b and fourth heat transfer tube 3c is the same as a parameter that satisfies the above-described relationship of magnitude between fourth heat transfer tube 3c and fifth heat transfer tube 3d, for example. In other words, first heat transfer tube 3a, second heat transfer tube 3b, fourth heat transfer tube 3c, and fifth heat transfer tube 3d are provided such that any one of these parameters including the number, the depth, the lead angle, and the tube thickness satisfies the above-described three-stage relationship of magnitude, for example. The number of the fourth grooves may exceed the number of second grooves 31b, and the depth of the fourth grooves may be less than the depth of the plurality of fifth grooves, for example. That is, any one of the parameters including the number, the depth, the lead angle, and the tube thickness that satisfies the above-described relationship of magnitude between second heat transfer tube 3b and fourth heat transfer tube 3c may be different from a parameter that satisfies the above-described relationship of magnitude between fourth heat transfer tube 3c and fifth heat transfer tube 3d. In the above-described case, the number of the fifth grooves may be equal to the number of the fourth grooves. In other words, fourth heat transfer tube 3c and fifth heat transfer tube 3d may be provided to be equal in any one of the parameters including the number, the depth, the lead angle, and the tube thickness that satisfies the above-described relationship of magnitude between second heat transfer tube 3b and fourth heat transfer tube 3c.
First heat exchanger 1 according to the sixth embodiment has a higher number of refrigerant flow paths connecting distributor 10 to third opening P3 in four-way valve 102, and therefore has a higher capacity than first heat exchanger 1 according to the first embodiment. First heat exchanger 1 according to the sixth embodiment, on the other hand, can produce similar effects to those of first heat exchanger 1 according to the first embodiment, because its first to fifth refrigerant flow paths connecting distributor 10 to third opening P3 in four-way valve 102 basically have a similar configuration to the first to third refrigerant flow paths in first heat exchanger 1 according to the first embodiment.
The refrigeration cycle apparatuses according to the first to sixth embodiments may include at least one first groove 31a and at least one second groove 31b. When the refrigeration cycle apparatuses according to the first to sixth embodiments include one second groove 31b, first groove 31a may be less than second groove 31b in at least one of the depth, the lead angle, and the tube thickness. Similarly, the refrigeration cycle apparatus according to the sixth embodiment may include at least one fourth groove. When the refrigeration cycle apparatus according to the sixth embodiment includes one fourth groove, second groove 31b may be less than the fourth groove in at least one of the depth and the lead angle.
A refrigeration cycle apparatus and a first heat exchanger according to a seventh embodiment basically have similar configurations to refrigeration cycle apparatus 100 and first heat exchanger 1 according to the first embodiment, but are different in that first heat transfer tube 3a, second heat transfer tube 3b, and third heat transfer tube 4 are each configured as a flat tube. The heat exchanger according to the seventh embodiment may have a similar configuration to any of the heat exchangers according to the second to fifth embodiments.
The internal pressure loss of the plurality of first heat transfer tubes 3a is smaller than the internal pressure loss of the plurality of second heat transfer tubes 3b. The internal pressure loss of the plurality of second heat transfer tubes 3b is smaller than the internal pressure loss of the plurality of fourth heat transfer tubes 3c. The internal pressure loss of the plurality of fourth heat transfer tubes 3c is smaller than the internal pressure loss of the plurality of fifth heat transfer tubes 3d. Preferably, the internal pressure loss of the plurality of first heat transfer tubes 3a is greater than the internal pressure loss of the plurality of third heat transfer tubes 4.
As shown in
As shown in
The internal pressure loss of the plurality of fourth heat transfer tubes 3c is greater than the internal pressure loss of the plurality of second heat transfer tubes 3b, and is smaller than the internal pressure loss of the plurality of fifth heat transfer tubes 3d. The internal pressure loss of the plurality of fifth heat transfer tubes 3d is greater than the internal pressure loss of the plurality of third heat transfer tubes 4.
Second heat transfer tube 3b and fourth heat transfer tube 3c have a relationship with each other, and fourth heat transfer tube 3c and fifth heat transfer tube 3d have a relationship with each other, that are similar to the relationship between first heat transfer tube 3a and second heat transfer tube 3b. In other words, at least one of the number of holes in second heat transfer tube 3b and the tube thickness of second heat transfer tube 3b is less than at least one of the number of holes in fourth heat transfer tube 3c and the tube thickness of fourth heat transfer tube 3c. At least one of the number of holes in second heat transfer tube 3b and the tube thickness of fourth heat transfer tube 3c is less than at least one of the number of holes in fifth heat transfer tube 3d and the tube thickness of fifth heat transfer tube 3d.
The number of holes in second heat transfer tube 3b exceeds the number of holes in first heat transfer tube 3a and is less than the number of holes in fourth heat transfer tube 3c, for example. That is, any one of the parameters including the number of holes and the tube thickness that satisfies the above-described relationship of magnitude between first heat transfer tube 3a and second heat transfer tube 3b is the same as a parameter that satisfies the above-described relationship of magnitude between second heat transfer tube 3b and fourth heat transfer tube 3c, for example. In other words, first heat transfer tube 3a, second heat transfer tube 3b, and fourth heat transfer tube 3c are provided such that any one of these parameters including the number of holes and the tube thickness satisfies the above-described two-stage relationship of magnitude, for example. The number of holes in second heat transfer tube 3b may exceed the number of holes in first heat transfer tube 3a, and the tube thickness of second heat transfer tube 3b may be less than the tube thickness of fourth heat transfer tube 3c, for example. That is, any one of the parameters including the number of holes and the tube thickness that satisfies the above-described relationship of magnitude between first heat transfer tube 3a and second heat transfer tube 3b may be different from a parameter that satisfies the above-described relationship of magnitude between second heat transfer tube 3b and fourth heat transfer tube 3c. In the above-described case, the number of holes in second heat transfer tube 3b may be equal to the number of holes in fourth heat transfer tube 3c. In other words, second heat transfer tube 3b and fourth heat transfer tube 3c may be provided to be equal in any one of the parameters including the number of holes and the tube thickness that satisfies the above-described relationship of magnitude between first heat transfer tube 3a and second heat transfer tube 3b.
The number of holes in fourth heat transfer tube 3c is less than the number of holes in fifth heat transfer tube 3d, for example. That is, any one of the parameters including the number of holes and the tube thickness that satisfies the above-described relationship of magnitude between second heat transfer tube 3b and fourth heat transfer tube 3c is the same as a parameter that satisfies the above-described relationship of magnitude between fourth heat transfer tube 3c and fifth heat transfer tube 3d, for example. In other words, first heat transfer tube 3a, second heat transfer tube 3b, fourth heat transfer tube 3c, and fifth heat transfer tube 3d are provided such that any one of these parameters including the number of holes and the tube thickness satisfies the above-described two-stage relationship of magnitude, for example. The number of holes in fourth heat transfer tube 3c may exceed the number of holes in second heat transfer tube 3b, and the tube thickness of fourth heat transfer tube 3c may be less than the tube thickness of fifth heat transfer tube 3d, for example. That is, any one of the parameters including the number of holes and the tube thickness that satisfies the above-described relationship of magnitude between second heat transfer tube 3b and fourth heat transfer tube 3c may be different from a parameter that satisfies the above-described relationship of magnitude between fourth heat transfer tube 3c and fifth heat transfer tube 3d. In the above-described case, the number of holes in fourth heat transfer tube 3c may be equal to the number of holes in fifth heat transfer tube 3d. In other words, fourth heat transfer tube 3c and fifth heat transfer tube 3d may be provided to be equal in any one of the parameters including the number of holes and the tube thickness that satisfies the above-described relationship of magnitude between second heat transfer tube 3b and fourth heat transfer tube 3c.
In this case, the first heat exchanger according to the seventh embodiment also basically has a similar configuration to the first heat exchanger according to the sixth embodiment described above, and can therefore produce similar effects to those of the first heat exchanger according to the sixth embodiment.
Although the internal pressure loss of first heat transfer tube 3a is reduced compared to the internal pressure loss of second heat transfer tube 3b by at least one of the numbers of holes in and the tube thicknesses of first heat transfer tube 3a and second heat transfer tube 3b in the refrigeration cycle apparatus according to the seventh embodiment, this is not restrictive. First heat transfer tube 3a and second heat transfer tube 3b have first grooves 31a and second groove 31b, as with first heat transfer tube 3a and second heat transfer tube 3b in any of the first to sixth embodiments, and the internal pressure loss of first heat transfer tube 3a may be reduced compared to the internal pressure loss of second heat transfer tube 3b by at least one of the numbers, the depths, and the lead angles of these grooves.
Although the first refrigerant flow path is provided to have a flow path length equal to that of the second refrigerant flow path in the refrigeration cycle apparatuses according to the first to seventh embodiments, this is not restrictive. The first refrigerant flow path may have a flow path length different from that of the second refrigerant flow path. The first refrigerant flow path may have a flow path length shorter than that of the second refrigerant flow path, for example.
Although first heat transfer tube 3a is provided to have an outer shape identical to that of second heat transfer tube 3b in the refrigeration cycle apparatuses according to the first to seventh embodiments, this is not restrictive. First heat transfer tube 3a may have an outer diameter exceeding that of second heat transfer tube 3b, for example. Third heat transfer tube 4 may have an outer diameter exceeding that of first heat transfer tube 3a, for example.
In the refrigeration cycle apparatuses according to the first to seventh embodiments, second heat exchanger 11 may also have a similar configuration to first heat exchanger 1. In this case, third inflow/outflow portion 5 of second heat exchanger 11 may be connected to decompression unit 103, and first inflow/outflow portion 6a and second inflow/outflow portion 6b may be connected to fourth opening P4 in four-way valve 102.
Although the embodiments of the present invention have been described as above, the embodiments described above can be modified in various manners. In addition, the scope of the present invention is not limited to the embodiments described above. The scope of the present invention is defined by the terms of the claims, and is intended to include any modifications within the meaning and scope equivalent to the terms of the claims.
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/JP2019/012903 | 3/26/2019 | WO |
| Publishing Document | Publishing Date | Country | Kind |
|---|---|---|---|
| WO2020/194517 | 10/1/2020 | WO | A |
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| 9568221 | Suhara | Feb 2017 | B2 |
| 20080041559 | Woong | Feb 2008 | A1 |
| 20160223265 | Jindou | Aug 2016 | A1 |
| Number | Date | Country |
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| H03-102193 | Apr 1991 | JP |
| H05-248785 | Sep 1993 | JP |
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| 2012147336 | Nov 2012 | WO |
| Entry |
|---|
| Office Action dated Jul. 26, 2022 issued in the counterpart Japanese Application No. 2021-508479 (and English translation). |
| International Search Report dated Jun. 25, 2019, issued in corresponding International Application No. PCT/JP2019/012903 (and English translation). |
| Office Action dated Jan. 5, 2023 issued in corresponding Chinese Patent Application No. 201980094118.6 (and English translation). |
| Number | Date | Country | |
|---|---|---|---|
| 20220113069 A1 | Apr 2022 | US |
