Heat Exchanger Including Refrigerant Branch Distribution Device, and Refrigeration Cycle Apparatus
20190113244 ยท 2019-04-18
Inventors
Cpc classification
F25B39/028
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F25B2500/01
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F25B41/42
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F25B2313/0233
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F25B39/02
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F25B2313/02742
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F25B2313/0253
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F25B13/00
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F24F1/26
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F25B41/45
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
International classification
F24F1/26
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F25B41/00
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
Abstract
A refrigeration cycle apparatus is provided with a branch distribution portion configured to divide refrigerant in a two-phase state of liquid refrigerant and gas refrigerant into refrigerants having different liquid ratios. The branch distribution portion includes a pipe including a bent pipe, a branch pipe, a pipe, and a pipe. The refrigerant flowing through the pipe flows through the bent pipe and the branch pipe, thereby being divided into refrigerant having a high liquid ratio and refrigerant having a low liquid ratio. The refrigerant having a high liquid ratio is fed through a pipe to a heat exchanger having a large volume of air. The refrigerant having a low liquid ratio is fed through a pipe to a heat exchanger having a small volume of air.
Claims
1. A heat exchanger comprising a refrigerant branch distribution device, the refrigerant branch distribution device comprising: a first flow path, a second flow path and a third flow path; a branch portion connected to the first flow path and connected to the second flow path and the third flow path, the branch portion being configured to divide refrigerant so as to flow into the second flow path and the third flow path, the refrigerant including liquid refrigerant and gas refrigerant and flowing from the first flow path, when a ratio of the liquid refrigerant in a weight ratio between the liquid refrigerant and the gas refrigerant is defined as a liquid ratio, a first liquid ratio of first refrigerant flowing into the second flow path being higher than a second liquid ratio of second refrigerant flowing into the third flow path; a first distribution device provided in the second flow path and configured to further divide the first refrigerant flowing into the second flow path; a second distribution device provided in the third flow path and configured to further divide the second refrigerant flowing into the third flow path; a first heat exchanger connected to the second flow path and configured to perform heat exchange between the first refrigerant divided by the first distribution device and a first fluid; and a second heat exchanger connected to the third flow path and configured to perform heat exchange between the second refrigerant divided by the second distribution device and a second fluid, an amount of the first fluid being larger than an amount of the second fluid.
2. The heat exchanger according to claim 1, wherein the first flow path comprises a curved first bent portion, the second flow path is connected to a first position of the branch portion corresponding to an outer circumferential side of the first bent portion, and the third flow path is connected to a second position of the branch portion corresponding to an inner circumferential side of the first bent portion.
3. The heat exchanger according to claim 2, wherein the first flow path comprises a straight portion between the first bent portion and the branch portion, and a length L of the straight portion is set at L<10D, where D represents an inner diameter of the first flow path.
4. The heat exchanger according to claim 1, wherein the branch portion comprises: a first extending portion extending from a portion of the branch portion to which the first flow path is connected, in a first direction in which the first flow path extends; and a second extending portion branching off and extending from the first extending portion in a second direction intersecting with the first direction, the second flow path is connected to the first extending portion, and the third flow path is connected to the second extending portion.
5. The heat exchanger according to claim 4, wherein the second flow path comprises a second bent portion.
6. The heat exchanger according to claim 4, wherein an orifice is arranged in the first flow path.
7. The heat exchanger according to claim 1, wherein the branch portion comprises at least: a third extending portion branching off and extending from a portion of the branch portion to which the first flow path is connected, in a third direction intersecting with a first direction in which the first flow path extends; and a fourth extending portion branching off and extending from the portion of the branch portion to which the first flow path is connected, in a fourth direction intersecting with the first direction and the third direction, the branch portion is arranged, with the third extending portion located on an upper side and the fourth extending portion located on a lower side, the second flow path is connected to the fourth extending portion, and the third flow path is connected to the third extending portion.
8. The heat exchanger according to claim 7, wherein the second flow path comprises a third bent portion.
9. The heat exchanger according to claim 7, wherein an orifice is arranged in the first flow path.
10. The heat exchanger according to claim 1, wherein the branch portion comprises at least: a third extending portion branching off and extending from a portion of the branch portion to which the first flow path is connected, in a third direction intersecting with a first direction in which the first flow path extends; and a fourth extending portion branching off and extending from the portion of the branch portion to which the first flow path is connected, in a fourth direction opposite to the third direction, the second flow path is connected to the third extending portion, and the third flow path is connected to the fourth extending portion.
11. The heat exchanger according to claim 10, wherein the second flow path comprises a fourth bent portion.
12. The heat exchanger according to claim 10, wherein an orifice is arranged in the first flow path.
13. The heat exchanger according to claim 1, wherein the branch portion comprises a tubular body, the tubular body comprises an upper surface portion, a lower surface portion and a side surface portion, the first flow path is connected to the side surface portion, the second flow path is connected to the lower surface portion, and the third flow path is connected to the upper surface portion.
14. The heat exchanger according to claim 13, wherein the second flow path comprises a fifth bent portion.
15. (canceled)
16. A refrigeration cycle apparatus comprising the heat exchanger as recited in claim 1.
Description
BRIEF DESCRIPTION OF DRAWINGS
[0017]
[0018]
[0019]
[0020]
[0021]
[0022]
[0023]
[0024]
[0025]
[0026]
[0027]
[0028]
[0029]
[0030]
[0031]
[0032]
[0033]
[0034]
[0035]
[0036]
[0037]
[0038]
[0039]
[0040]
[0041]
[0042]
[0043]
[0044]
[0045]
[0046]
[0047]
[0048]
[0049]
[0050]
[0051]
[0052]
[0053]
[0054]
[0055]
[0056]
[0057]
[0058]
[0059]
[0060]
[0061]
[0062]
[0063]
[0064]
DETAILED DESCRIPTION
First Embodiment
[0065] A refrigeration cycle apparatus including a refrigerant distribution device according to a first embodiment will be described. First, a configuration of the refrigeration cycle apparatus will be described. A multi air conditioner for buildings will be described as an example of the refrigeration cycle apparatus.
[0066] As shown in
[0067] Furthermore, in refrigeration cycle apparatus 1, a branch distribution portion 11 is provided between refrigerant distribution devices 21a and 21b and expansion valve 13. Branch distribution portion 11 will be described below. Expansion valves 9a and 9b provided between branch distribution portion 11 and refrigerant distribution devices 21a and 21b are not essential and are provided as needed.
[0068] Next, as the operation of the multi air conditioner for buildings, heating operation will be described. By driving compressor 3, high-temperature and high-pressure gaseous refrigerant is discharged from compressor 3. The discharged high-temperature and high-pressure gas refrigerant (single phase) flows through four-way valves 5a and 5b into each of the plurality of indoor heat exchangers 15a, 15b, 15c, and 15d.
[0069] Air is introduced into indoor heat exchangers 15a to 15d by indoor fans 19a, 19b, 19c, and 19d, respectively. In each of indoor heat exchangers 15a to 15d, heat exchange is performed between the introduced air and the gas refrigerant flowing into each of indoor heat exchangers 15a to 15d, and the high-temperature and high-pressure gas refrigerant condenses to high-pressure liquid refrigerant (single phase). As a result of this heat exchange, each of the rooms where indoor heat exchangers 15a to 15d are arranged is heated.
[0070] Next, the high-pressure liquid refrigerant discharged from indoor heat exchangers 15a to 15d passes through expansion valves 13a, 13b, 13c, and 13d, to thereby become refrigerant in a two-phase state of low-pressure gas refrigerant and liquid refrigerant.
[0071] The refrigerant in a two-phase state flows into an outdoor unit 25. The refrigerant in a two-phase state flowing into outdoor unit 25 is divided into two in branch distribution portion 11. One refrigerant (refrigerant A), of the refrigerant divided into two, flows through expansion valve 9a, refrigerant distribution device 21a and pipes 47 into outdoor heat exchanger 7a. The other refrigerant (refrigerant B), of the refrigerant divided into two, flows through expansion valve 9b, refrigerant distribution device 21b and pipes 48 into outdoor heat exchanger 7b.
[0072] In outdoor heat exchangers 7a and 7b, heat exchange is performed between air introduced by outdoor fan 17 and the refrigerant (refrigerant A and refrigerant B) flowing into outdoor heat exchangers 7a and 7b, and the liquid refrigerant of the refrigerant in a two-phase state evaporates to low-pressure gas refrigerant (single phase). The low-pressure gas refrigerant discharged from outdoor unit 25 flows through four-way valves 5a and 5b and accumulator 23 into compressor 3. The low-pressure gas refrigerant flowing into compressor 3 is compressed to high-temperature and high-pressure gas refrigerant, which is again discharged from compressor 3. Thereafter, this cycle is repeated.
[0073] Next, cooling operation will be described. The high-temperature and high-pressure gas refrigerant compressed by compressor 3 flows through four-way valves 5a and 5b into outdoor heat exchangers 7a and 7b. In outdoor heat exchangers 7a and 7b, heat exchange is performed between the air introduced by outdoor fan 17 and the gas refrigerant flowing into outdoor heat exchangers 7a and 7b, and the high-temperature and high-pressure gas refrigerant condenses to low-temperature and high-pressure liquid refrigerant (single phase).
[0074] The low-temperature and high-pressure liquid refrigerant passes through expansion valves 13a to 13d and the like, to thereby become low-temperature and low-pressure liquid refrigerant. The low-temperature and low-pressure liquid refrigerant flows into each of the plurality of indoor heat exchangers 15a to 15d. In indoor heat exchangers 15a to 15d, heat exchange is performed between the air introduced by indoor fans 19a to 19d and the liquid refrigerant flowing into indoor heat exchangers 15a to 15d, and the low-temperature and low-pressure liquid refrigerant evaporates to low-pressure gas refrigerant (single phase). As a result of this heat exchange, each of the rooms where indoor heat exchangers 15a to 15d are arranged is cooled.
[0075] The low-pressure gas refrigerant discharged from indoor heat exchangers 15a to 15d flows through four-way valves 5a and 5b and accumulator 23 into compressor 3. The low-pressure gas refrigerant flowing into the compressor is compressed to high-temperature and high-pressure gas refrigerant, which is again discharged from the compressor. Thereafter, this cycle is repeated.
[0076] In refrigeration cycle apparatus 1 described above, outdoor heat exchanger 7 of outdoor unit 25 functions as an evaporator during heating operation, and functions as a condenser during cooling operation. One example of the outdoor unit of the multi air conditioner for buildings is an outdoor unit including a top flow-type fan. As shown in
[0077] Air inlets 27 through which the air is taken in are provided in three side surface portions (three sides) of four side surface portions of the housing. As shown in
[0078] In outdoor unit 25 described above, outdoor fan 17 is attached to the upper surface portion of housing 26. Therefore, in outdoor heat exchanger 7, a pressure loss of the air becomes lower as a distance from outdoor fan 17 becomes shorter, and the pressure loss of the air becomes higher as the distance from outdoor fan 17 becomes longer. That is, the pressure loss becomes higher gradually from an upper part toward a lower part of outdoor heat exchanger 7, and thus, a volume of air passing through outdoor heat exchanger 7a is relatively large and a volume of air passing through outdoor heat exchanger 7b is relatively small (see arrows in
[0079]
[0080] One refrigerant path extends from the heat transfer tube of the first row of outdoor heat exchanger 7aa through the heat transfer tube of the second row of outdoor heat exchanger 7ab and the heat transfer tube of the third row of outdoor heat exchanger 7ac to a refrigerant distribution device 29. As shown in
[0081] When outdoor heat exchanger 7 functions as an evaporator, it is required to allow the liquid refrigerant of the refrigerant in a two-phase state to flow into outdoor heat exchanger 7a having a larger volume of air, such that the liquid refrigerant efficiently evaporates to gas refrigerant. For this purpose, outdoor unit 25 is provided with branch distribution portion 11 as shown in
[0082] In branch distribution portion 11, the refrigerant in a two-phase state flowing from indoor heat exchanger 15 is divided into two lines of refrigerant (refrigerant A and refrigerant B) during heating operation. A ratio of the liquid refrigerant in a weight ratio between the liquid refrigerant and the gas refrigerant is defined as a liquid ratio. Refrigerant A is refrigerant having a high liquid ratio. Refrigerant B is refrigerant having a low liquid ratio. In branch distribution portion 11, the refrigerant is macroscopically divided into refrigerant A having a high liquid ratio and refrigerant B having a low liquid ratio. Refrigerant A is further divided microscopically by refrigerant distribution device 21a and fed to outdoor heat exchanger 7a having a large volume of air. Refrigerant B is further divided microscopically by refrigerant distribution device 21b and fed to outdoor heat exchanger 7b having a small volume of air.
[0083] A first example of a specific structure of branch distribution portion 11 will be described. As shown in
[0084] As a result, in pipe 41 immediately after the refrigerant flows through bent pipe 33, the refrigerant (refrigerant A) having a high liquid ratio flows through a region corresponding to the outer circumferential side of bent pipe 33, and the refrigerant (refrigerant B) having a low liquid ratio flows through a region corresponding to the inner circumferential side of bent pipe 33. The refrigerant flowing through pipe 41 in this state is divided into refrigerant A and refrigerant B by branch pipe 31. Divided refrigerant A flows through pipe 43, refrigerant distribution device 21a and pipes 47 into outdoor heat exchanger 7a. On the other hand, refrigerant B flows through pipe 44, refrigerant distribution device 21b and pipes 48 into outdoor heat exchanger 7b.
[0085] In this way, in outdoor unit 25, refrigerant A having a high liquid ratio flows into outdoor heat exchanger 7a having a larger volume of air, and refrigerant B having a low liquid ratio flows into outdoor heat exchanger 7b having a smaller volume of air. As a result, heat exchange between the refrigerant in a two-phase state and the air can be performed efficiently.
[0086] As a method for allowing the refrigerant having a high liquid ratio to flow into outdoor heat exchanger 7a having a larger volume of air, there has conventionally been a method for adjusting a pressure loss by changing a length of the pipes, an inner diameter of the pipes or the like connected to outdoor heat exchangers 7a and 7b. That is, there has been a method for dividing the refrigerant microscopically. However, according to this method, when the number of pipes increases, it becomes difficult to adjust the length of the pipes. In addition, a region for routing the pipes is also required. Furthermore, routing of the pipes is also complicated.
[0087] In contrast to such a method, the above-described method using branch distribution portion 11 can allow the refrigerant having a high liquid ratio to flow into outdoor heat exchanger 7a having a larger volume of air, with a simple structure of bent pipe 33 and branch pipe 31.
[0088] A length L of a straight portion of pipe 41 extending from bent pipe 33 to branch pipe 31 needs to be set at such a length that the liquid refrigerant in pipe 41 flows into branch pipe 31 with non-uniform and uneven distribution (see
[0089] As shown in
Second Embodiment
[0090] A second example of the branch distribution portion forming the refrigerant branch distribution device will now be described. As shown in
[0091] Pipe 43 (second flow path) including bent pipe 33 is connected to pipe portion A. Refrigerant distribution device 21a is connected to pipe 43, and further, a plurality of pipes 47 are connected to refrigerant distribution device 21a. On the other hand, pipe 44 (third flow path) is connected to pipe portion B. Refrigerant distribution device 21b is connected to pipe 44, and further, a plurality of pipes 48 are connected to refrigerant distribution device 21b. The plurality of pipes 47 are connected to outdoor heat exchanger 7a, and the plurality of pipes 48 are connected to outdoor heat exchanger 7b (see
[0092] Since the remaining configuration of the outdoor unit and the remaining configuration of the refrigeration cycle apparatus are similar to the configurations shown in
[0093] In branch distribution portion 11 described above, when the refrigerant in a two-phase state flowing through pipe 41 (first flow path) flows into T-shaped branch pipe 35a, a larger amount of liquid refrigerant flows through pipe portion A extending in one direction, due to the inertia. As a result, as shown in
[0094] On the other hand, a larger amount of gas refrigerant flows through pipe portion B branching off from pipe portion A. As a result, as shown in
[0095] The refrigerant (refrigerant A) in a two-phase state having a high liquid ratio and flowing through pipe 43 flows through bent pipe 33. At this time, non-uniformity occurs in the distribution of the liquid refrigerant included in refrigerant A. That is, as described above, due to the centrifugal force, an amount of the liquid refrigerant flowing along an inner wall surface on the outer circumferential side of bent pipe 33 becomes larger than an amount of the liquid refrigerant flowing along an inner wall surface on the inner circumferential side of bent pipe 33.
[0096] As a result, as shown in
[0097] The refrigerant (refrigerant AA and refrigerant AB) flowing through pipe 43 flows into refrigerant distribution device 21a in this state. In refrigerant distribution device 21a, the refrigerant flowing into refrigerant distribution device 21a is divided so as to flow into the plurality of pipes 47. At this time, as shown in
[0098] Divided refrigerant AA and refrigerant AB flow through pipes 47 into outdoor heat exchanger 7a. On the other hand, refrigerant B flows through pipes 48 into outdoor heat exchanger 7b. In this way, in outdoor unit 25, refrigerant A (refrigerant AA and refrigerant AB) having a high liquid ratio flows into outdoor heat exchanger 7a having a larger volume of air, and refrigerant B having a low liquid ratio flows into outdoor heat exchanger 7b having a smaller volume of air.
[0099] Particularly, in outdoor heat exchanger 7a, refrigerant AA having a high liquid ratio flows through an upper path of outdoor heat exchanger 7a having a relatively large volume of air, and refrigerant AB having a low liquid ratio flows through a lower path of outdoor heat exchanger 7a having a relatively small volume of air (see
Modification
[0100] A modification of the T-shaped branch pipe will now be described. As shown in
[0101] The remaining configuration of T-shaped branch pipe 35b and the like is similar to the configuration shown in
[0102] In branch distribution portion 11 described above, when the refrigerant in a two-phase state flowing through pipe 41 (first flow path) flows into T-shaped branch pipe 35b, liquid refrigerant 51 is more likely to flow through pipe 43 (second flow path) connected to pipe portion A by the inertia as described above, and thus, the refrigerant (refrigerant A) having a high liquid ratio flows into pipe 43.
[0103] On the other hand, the liquid refrigerant is less likely to flow through pipe portion B and pipe portion C branching off from pipe portion A, and thus, the refrigerant (refrigerant B) having a low liquid ratio flows through pipe portion B and pipe portion C. When pipe portion B is compared with pipe portion C, the gas refrigerant is likely to flow into pipe portion C located on the upstream side of the refrigerant flow, and thus, the refrigerant having a low liquid ratio flows into pipe portion C. The refrigerant having a high liquid ratio flows into pipe portion B located on the downstream side of the refrigerant flow.
[0104] As a result, as shown in
[0105] The refrigerant (refrigerant BB) flowing through pipe 45 flows into refrigerant distribution device 21c. In refrigerant distribution device 21c, the refrigerant flowing into refrigerant distribution device 21c is divided so as to flow into the plurality of pipes 49. The refrigerant (refrigerant BA) flowing through pipe 44 flows into refrigerant distribution device 21b. In refrigerant distribution device 21b, the refrigerant flowing into refrigerant distribution device 21b is divided so as to flow into the plurality of pipes 48.
[0106] As described above, refrigerant A flowing through pipe 43 is divided so as to flow into the plurality of pipes 47 by refrigerant distribution device 21a. As shown in
[0107] In addition, as shown in
[0108] On the other hand, divided refrigerant B (refrigerant BB and refrigerant BA) flows through pipes 48 and 49 into outdoor heat exchanger 7b. In this way, in outdoor unit 25, refrigerant A having a high liquid ratio flows into outdoor heat exchanger 7a having a larger volume of air, and refrigerant B (refrigerant BB and refrigerant BA) having a low liquid ratio flows into outdoor heat exchanger 7b having a smaller volume of air.
[0109] Particularly, in outdoor heat exchanger 7b, refrigerant BA having a high liquid ratio flows through an upper path of outdoor heat exchanger 7b having a relatively large volume of air, and refrigerant BB having a low liquid ratio flows through a lower path of outdoor heat exchanger 7b having a relatively small volume of air (see
Third Embodiment
[0110] A third example of the branch distribution portion forming the refrigerant branch distribution device will now be described. As shown in
[0111]
[0112]
[0113] The remaining configuration of T-shaped branch pipe 35a and the like is similar to the configuration shown in
[0114] In branch distribution portion 11 described above, the liquid refrigerant of the refrigerant in a two-phase state flowing through pipe 41 is taken off from an inner wall of pipe 41 by blocking portion 39a of orifice 39, before the refrigerant in a two-phase state flows into T-shaped branch pipe 35a. In addition, the refrigerant passes through opening 39b having a small flow path cross-sectional area, which results in an increase in flow velocity of the refrigerant. Thus, a larger amount of liquid refrigerant is likely to flow through pipe portion A of T-shaped branch pipe 35a extending in one direction. Particularly when a flow rate of the refrigerant in a two-phase state is low, an amount of the liquid refrigerant flowing into pipe portion A can be increased.
[0115] On the other hand, since the liquid refrigerant is taken off from the inner wall of pipe 41 before pipe portion B, the liquid refrigerant is less likely to flow into pipe portion B branching off from pipe portion A, as compared with the case of not having the orifice, and a larger amount of gas refrigerant is likely to flow into pipe portion B correspondingly. As a result, as shown in
[0116] Particularly, blocking portion 39a of orifice 39 shown in
[0117] As described above, the refrigerant having a high liquid ratio and flowing into pipe 43 flows through bent pipe 33, and thus, is divided into the refrigerant (refrigerant AA) having a high liquid ratio and the refrigerant (refrigerant AB) having a low liquid ratio as shown in
Fourth Embodiment
[0118] A fourth example of the branch distribution portion forming the refrigerant branch distribution device will now be described. As shown in
[0119] Since the remaining configuration of the outdoor unit and the remaining configuration of the refrigeration cycle apparatus are similar to the configurations shown in
[0120] In branch distribution portion 11 described above, the refrigerant in a two-phase state (see
[0121] The refrigerant flowing through pipe 43 flows through bent pipe 33 and is further divided by refrigerant distribution device 21a. The divided refrigerant flows through pipes 47 into outdoor heat exchanger 7a. On the other hand, the refrigerant flowing through pipe 44 flows through bent pipe 33 and is further divided by refrigerant distribution device 21b. The divided refrigerant flows through pipes 48 into outdoor heat exchanger 7b.
[0122]
[0123] As shown in
[0124] In this way, in outdoor unit 25, refrigerant A having a high liquid ratio flows into outdoor heat exchanger 7a having a larger volume of air, and refrigerant B having a low liquid ratio flows into outdoor heat exchanger 7b having a smaller volume of air. As a result, heat exchange between the refrigerant and the air can be performed more efficiently.
Modification
[0125] A modification of the Y-shaped branch pipe will now be described. As shown in
[0126] Structurally, Y-shaped branch pipe 37b includes a portion (pipe portion A) extending in one direction in which the refrigerant flows, a portion (pipe portion B) extending in another direction intersecting with the one direction, and a portion (pipe portion C) extending in a direction opposite to the other direction.
[0127] In branch distribution portion 11 described above, the refrigerant in a two-phase state (see
[0128] The refrigerant flowing through pipe 43 flows through bent pipe 33 and is further divided by refrigerant distribution device 21a. The divided refrigerant flows through pipes 47 into outdoor heat exchanger 7a. On the other hand, the refrigerant flowing through pipe 44 flows through bent pipe 33 and is further divided by refrigerant distribution device 21b. The divided refrigerant flows through pipes 48 into outdoor heat exchanger 7b.
[0129]
[0130] Particularly, Y-shaped branch pipe 37b has the portion (pipe portion A) configured to cause the refrigerant to branch so as to have the direction component (X direction component) of the direction (X direction) of the refrigerant flow. Therefore, even when a flow rate of the refrigerant is low, the liquid refrigerant is likely to flow by the inertial force, and thus, the refrigerant having a high liquid ratio can flow from pipe portion A to pipe 43.
[0131] Thus, in outdoor unit 25, refrigerant A having a high liquid ratio flows into outdoor heat exchanger 7a having a larger volume of air, and refrigerant B having a low liquid ratio flows into outdoor heat exchanger 7b having a smaller volume of air. As a result, heat exchange between the refrigerant and the air can be performed more efficiently.
Fifth Embodiment
[0132] A fifth example of the branch distribution portion forming the refrigerant branch distribution device will now be described. As shown in
[0133] Since the remaining configuration of the outdoor unit and the remaining configuration of the refrigeration cycle apparatus are similar to the configurations shown in
[0134] In branch distribution portion 11 described above, the refrigerant in a two-phase state (see
[0135] The refrigerant including a large amount of liquid refrigerant and accumulating in the lower part in tubular body 36 flows through pipe 43 including bent pipe 33 and is further divided by refrigerant distribution device 21a. The divided refrigerant flows through pipes 47 into outdoor heat exchanger 7a. On the other hand, the refrigerant including a large amount of gas refrigerant and accumulating in the upper part in tubular body 36 flows through pipe 44 including bent pipe 33 and is further divided by refrigerant distribution device 21b. The divided refrigerant flows through pipes 48 into outdoor heat exchanger 7b.
[0136]
[0137] As shown in
[0138] In this way, in outdoor unit 25, refrigerant A having a high liquid ratio flows into outdoor heat exchanger 7a having a larger volume of air, and refrigerant B having a low liquid ratio flows into outdoor heat exchanger 7b having a smaller volume of air. As a result, heat exchange between the refrigerant and the air can be performed more efficiently.
[0139] The branch distribution portions described in the embodiments can be variously combined as needed. For example, the orifice described in the third embodiment may be applied to the branch distribution portions in the other embodiments. Furthermore, the multi air conditioner for buildings has been described as an example of the refrigeration cycle apparatus. In addition to this, the present invention is also applicable to a refrigeration cycle apparatus such as, for example, a heat pump apparatus or a car air conditioner.
[0140] The embodiments disclosed herein are illustrative and non-restrictive. The present invention is defined by the terms of the claims, rather than the description above, and is intended to include any modifications within the scope and meaning equivalent to the terms of the claims.
INDUSTRIAL APPLICABILITY
[0141] The present invention is effectively utilized in a refrigeration cycle apparatus including a heat exchanger.