Patent Grant
10976085
The present invention relates to an air-conditioning apparatus.
Distribution of the wind speed (air quantity) of the air passing through a heat exchanger is generally not uniform but is distributed. For example, in the case of an air-conditioning apparatus in which the air, taken into the casing of an outdoor unit by an outdoor fan, exchanges heat in an outdoor heat exchanger and then the air is discharged from an upper portion of the casing, the wind speed in the outdoor heat exchanger is distributed in such a manner that the wind speed of the upper side increases and the wind speed in the lower side decreases. When the distribution of refrigerant supplied to the heat exchanger and the distribution of the wind speed (air quantity) do not match, the performance of the heat exchanger may not be drawn out. For example, in the case where the heat exchanger is an evaporator, the refrigerant cannot be evaporated completely at a portion of a heat transfer tube where air quantity passing through is small, so that the performance of the heat exchanger cannot be drawn out. To solve such a problem, as a conventional air-conditioning apparatus in which the air, taken into the casing of an outdoor unit by an outdoor fan, exchanges heat with an outdoor heat exchanger and then the air is discharged from an upper portion of the casing, one in which an outdoor heat exchanger is divided into a plurality of divided regions in an up and down direction, and for each divided region, two-phase refrigerant of the amount corresponding to the air quantity is supplied using a distributor, has been proposed (for example, see Patent Literature 1).
Patent Literature 1: Japanese Unexamined Patent Application Publication No. 2010-127601
In the air-conditioning apparatus described in Patent Literature 1, two-phase refrigerant, having flowed out of the expansion valve, is distributed to each divided region of the outdoor heat exchanger by a distributor. As such, in the divided region, as the refrigerant is equally distributed to the respective heat transfer tubes, there is a problem that the refrigerant cannot be distributed corresponding to the distribution of the wind speed in the divided region, so that the performance of the outdoor heat exchanger cannot be improved sufficiently.
The present invention has been made to solve such a problem. An object of the present invention is to achieve an air-conditioning apparatus that enables allocation of two-phase refrigerant according to the distribution of the wind speed in a divided region of an outdoor heat exchanger, and enables improvement of performance of the outdoor heat exchanger.
An air-conditioning apparatus, according to the present invention, includes a refrigeration cycle including an outdoor heat exchanger functioning as a compressor, a condenser, an expansion valve, or an evaporator, and a liquid header connected to a position that is a refrigerant inflow side of the outdoor heat exchanger when the outdoor heat exchanger functions as the evaporator; and an outdoor fan configured to supply air to the outdoor heat exchanger. The outdoor heat exchanger is provided to a casing of an outdoor unit such that heat transfer tubes are arranged in parallel in an up and down direction, and the air, sucked into the casing of the outdoor unit by the outdoor fan, is discharged from an upper portion of the casing after exchanging heat with the outdoor heat exchanger. The liquid header is divided into a plurality of liquid header portions in an up and down direction, and each of the liquid header portions is configured to be connected with each of the heat transfer tubes of the divided regions formed by dividing the outdoor heat exchanger in the up and down direction. The air-conditioning apparatus further includes a first gas-liquid separator configured to separate two-phase refrigerant, flowing out of the expansion valve, into gas refrigerant and liquid refrigerant; a bypass connecting the first gas-liquid separator and the suction side of the compressor, the bypass being configured to adjust an amount of the gas refrigerant, separated by the first gas-liquid separator, to be returned to the suction side of the compressor; and a shunt connecting the first gas-liquid separator and each of the liquid header portions, and supplying the two-phase refrigerant, in which quality is adjusted by the first gas-liquid separator, to each of the liquid header portions. The shunt is configured to supply, to each of the liquid header portions, the two-phase refrigerant of an amount corresponding to the air quantity of the divided region connected with each of the liquid header portions.
In the air-conditioning apparatus of the present invention, two-phase refrigerant in which the quality is adjusted by the first gas-liquid separator is supplied to the shunt. As such, in the air-conditioning apparatus of the present invention, the speed of gas refrigerant flowing in each liquid header portion can be adjusted. Further, in the air-conditioning apparatus of the present invention, the shunt supplies, to each liquid header portion, the two-phase refrigerant of the amount corresponding to the divided region of the outdoor heat exchanger to which each liquid header portion is connected. As such, in the air-conditioning apparatus of the present invention, the amount of liquid refrigerant lifted upward by the gas refrigerant in the liquid header portion can be adjusted according to the wind speed distribution, and the refrigerant can be supplied to the divided region along the wind speed distribution, whereby it is possible to improve the performance of the outdoor heat exchanger sufficiently.
Hereinafter, embodiments of an air-conditioning apparatus according to the present invention will be described based on the drawings. It should be noted that the present invention is not limited to the embodiments described below.
An air-conditioning apparatus 300 of Embodiment 1 includes a compressor 1, a four-way valve 2, an indoor heat exchanger 3, an expansion valve 4, and an outdoor heat exchanger 8. This means that at the time of heating operation, the refrigeration cycle of the air-conditioning apparatus 300 is configured such that the compressor 1, the four-way valve 2, the indoor heat exchanger 3, the expansion valve 4, and the outdoor heat exchanger 8 are connected in this order. Further, at the time of cooling operation, the refrigeration cycle of the air-conditioning apparatus 300 is configured such that the compressor 1, the four-way valve 2, the outdoor heat exchanger 8, the expansion valve 4, and the indoor heat exchanger 3 are connected in this order. As such, the indoor heat exchanger 3 functions as a condenser at the time of heating operation, and functions as an evaporator at the time of cooling operation. The outdoor heat exchanger 8 functions as an evaporator at the time of heating operation, and functions as a condenser at the time of cooling operation.
It should be noted that in the case where the air-conditioning apparatus 300 only performs either heating operation or cooling operation, the four-way valve 2 is not particularly required.
Further, the outdoor heat exchanger 8 is configured of a plurality of fins 16 and a plurality of heat transfer tubes 15, as described below. One end portion (end portion of a refrigerant inflow side at the time of heating operation) of each heat transfer tube 15 is connected with a liquid header 7, and the other end portion (end portion of a refrigerant outflow side at the time of heating operation) of each heat transfer tube 15 is connected with a gas header 9.
It should be noted that in Embodiment 1, the liquid header 7 is divided into two liquid header portions 7a and 7b in an up and down direction.
Further, the air-conditioning apparatus 300 of Embodiment 1 includes a first gas-liquid separator 5 for separating two-phase refrigerant, having flowed out of the expansion valve 4, into gas refrigerant and liquid refrigerant at the time of heating operation, and a bypass 10 that connects the first gas-liquid separator 5 and the suction side of the compressor 1 and adjusts the quantity of the gas refrigerant, separated by the first gas-liquid separator 5, to be returned to the suction side of the compressor 1. The bypass 10 connects the first gas-liquid separator 5 and the suction side of the compressor 1, and is configured of a first bypass pipe 10a for returning gas refrigerant, separated by the first gas-liquid separator 5, to the suction side of the compressor 1, and a flow rate control mechanism 11 (flow rate control valve, for example) that adjust the flow rate of the gas refrigerant flowing in the first bypass pipe 10a.
The air-conditioning apparatus 300 of Embodiment 1 further includes a shunt 6 that connects the first gas-liquid separator 5 and lower portions, for example, of the respective liquid header portions 7a and 7b, and supplies the two-phase refrigerant, in which the quality is adjusted by the first gas-liquid separator 5, to the liquid header portions 7a and 7b, respectively.
The above-described constituent elements, constituting the air-conditioning apparatus 300, are stored in an outdoor unit 100 and an indoor unit 200.
In more detail, in the outdoor unit 100, the compressor 1, the four-way valve 2, the expansion valve 4, the first gas-liquid separator 5, the shunt 6, the liquid header 7, the outdoor heat exchanger 8, the gas header 9, and the bypass 10 (first bypass pipe 10a, flow rate control mechanism 11) are stored. Further, in the indoor unit 200, the indoor heat exchanger 3 is stored. It should be noted that the outdoor unit 100 is also provided with a fan 12 that supplies air (outdoor air), to which heat exchange is applied, to the outdoor heat exchanger 8. The configuration of storing the fan 12 in the outdoor unit 100 will be described below.
The air-conditioning apparatus 300 of Embodiment 1 also includes a controller 20 configured of a microcomputer, for example. The controller 20 controls the rotation speed of the compressor 1, the flow channel of the four-way valve 2, the opening degree of the expansion valve 4, the opening degree of the flow rate control mechanism 11, the rotation speed (air quantity) of the fan 12, and the like.
Next, the details of the outdoor unit 100 will be described.
The outdoor unit 100 according to Embodiment 1 includes an approximately rectangular parallelepiped casing 13. At least one side face of the casing 13 has an air inlet, and the outdoor heat exchanger 8 is provided to face the air inlet. It should be noted that in Embodiment 1, air inlets are formed in three side faces of the casing 13. As such, as shown in
In more detail, the outdoor heat exchanger 8 is configured of a plurality of fins 16 and a plurality of heat transfer tubes 15. The fins 16 are in a substantially rectangular shape extended in the up and down direction, and the respective fins 16 are arranged in parallel in a horizontal direction at predetermined intervals. The heat transfer tubes 15 are formed in a U shape in a plan view, and the respective heat transfer tubes 15 are arranged in parallel at predetermined intervals in the up and down direction so as to penetrate the fins 16. It should be noted that the heat transfer tube 15 of Embodiment 1 is formed in a U shape, and at an end portion of one side of the U shape, it is folded to be in a U shape again. As such, both an end portion of the liquid header 7 (liquid header portions 7a and 7b) side and an end portion of the gas header 9 side of the heat transfer tube 15 are arranged at an end portion of one side of the U shape. It should be noted that the arrangement method may not be limited to an end portion of one side. For example, by allowing the refrigerant to flow in the heat transfer tubes 15 in parallel rather than folding back the heat transfer tube 15, the end portions of the liquid header 7 (liquid header portions 7a and 7b) side and the gas header 9 side may be arranged at end portions on both sides of the U shape.
Further, the outdoor unit 100 of Embodiment 1 has an air outlet formed in an upper portion of the casing 13, and the fan 12 equivalent to an outdoor fan of the present invention is provided below the air outlet. This means that the outdoor unit 100 of Embodiment 1 is configured such that the air sucked into the casing 13 by the fan 12 exchanges heat with the outdoor heat exchanger 8 and then discharged from the upper portion of the casing 13. As such, as shown in
Accordingly, in Embodiment 1, the liquid header 7 has a pipe structure that is divided into two liquid header portions 7a and 7b in an up and down direction so as to extend upward and downward. As such, it is configured that the heat transfer tubes 15 arranged in an upper portion of the outdoor heat exchanger 8 are connected with the liquid header portion 7a, and the heat transfer tubes 15 arranged in the lower portion of the outdoor heat exchanger 8 are connected with the liquid header portion 7b. In other words, the outdoor heat exchanger 8 is divided into a plurality of divided regions in the up and down direction, and different liquid header portions are connected with the respective different regions. Then, in Embodiment 1, the shunt 6 supplies two-phase refrigerant of the amount corresponding to the air quantity of the divided regions connected with the liquid header portion 7a and 7b, with respect to the respective liquid header portion 7a and 7b. Specifically, the shunt 6 supplies the two-phase refrigerant to the respective liquid header portions 7a and 7b such that an average refrigerant flow rate of the heat transfer tubes 15 connected with the liquid header portion 7a (flow rate of two-phase refrigerant supplied to the liquid header portion 7a/the number of heat transfer tubes 15 connected with the liquid header portion 7a) becomes larger than an average refrigerant flow rate of the heat transfer tubes 15 connected with the liquid header portion 7b (flow rate of two-phase refrigerant supplied to the liquid header portion 7b/the number of heat transfer tubes 15 connected with the liquid header portion 7b). It should be noted that as shown in
To enable allocation of refrigerant to the liquid header portions 7a and 7b in this way, the shunt 6 of Embodiment 1 is formed such that the inner diameter of the flow channels connected with the liquid header portions 7a and 7b differs according to each liquid header portion. Thereby, the amount of two-phase refrigerant supplied to each of the liquid header portions 7a and 7b can be changed.
The shunt 6 includes a main body 6a and connection pipes 6b of the same number as the number of liquid header portions. The main body 6a has a flow channel in which one end is connected with the first gas-liquid separator 5, and the other end is branched to be in the same number as the number of the liquid header portions. The connection pipe 6b is configured such that one end thereof is connected with another end (each branched portion) of the flow channel formed in the main body 6a, and the other end is connected with each of the liquid header portions 7a and 7b. In this case, as shown in
Further, although not shown, the length of the connection pipe unit 6b connected with the liquid header portion 7a may be formed to be longer than the length of the connection pipe unit 6b connected with the liquid header portion 7b. Even such a configuration, a larger amount of refrigerant can be supplied to the liquid header portion 7a side connected with a divided region of a large air quantity.
It should be noted that the flow dividing ratio of the refrigerant supplied to the liquid header portion 7a and the liquid header portion 7b may be fixed according to the air quantity distribution in an operating state where the air quantity distribution is biased most. Further, as shown in
Next, operation of the air-conditioning apparatus 300 according to Embodiment 1 will be described.
When the air-conditioning apparatus 300 performs heating operation, gas refrigerant, compressed to be high temperature and high pressure by the compressor 1, flows into the indoor heat exchanger 3 along with the solid line of the four-way valve 2, and exchanges heat with the indoor air and discharges heat to the indoor by an air sending means such as a fan not shown, whereby the gas refrigerant is condensed to be high-temperature and high-pressure liquid refrigerant. The high-temperature and high-pressure liquid refrigerant is decompressed by the expansion valve 4 to be two-phase refrigerant, and flows into the first gas-liquid separator 5. In the first gas-liquid separator 5, the two-phase refrigerant is separated into gas refrigerant and liquid refrigerant. Regarding the gas refrigerant, the flow rate thereof is controlled by the flow rate control mechanism 11, and the gas refrigerant is returned to the suction side of the compressor 1 through the bypass 10. The two-phase refrigerant, in which the quality is controlled by bypassing the gas refrigerant in the first gas-liquid separator 5, flows into the shunt 6. This means that the two-phase refrigerant, in which the amount of gas refrigerant is adjusted, flows into the shunt 6. The two-phase refrigerant having flowed in the shunt 6 is supplied to the liquid header portion 7a and the liquid header portion 7b that are divided into two. Then, the two-phase refrigerant supplied to the liquid header portion 7a is allocated to the respective heat transfer tubes 15 connected with the liquid header portion 7a (respective heat transfer tubes 15 arranged in the upper divided region in the outdoor heat exchanger 8). Further, the two-phase refrigerant supplied to the liquid header portion 7b is allocated to the respective heat transfer tubes 15 connected with the liquid header portion 7b (respective heat transfer tubes 15 arranged in the lower divided region in the outdoor heat exchanger 8).
Here, in the air-conditioning apparatus 300 according to Embodiment 1, refrigerant is allocated to the respective heat transfer tubes 15 as shown in
As described above, the shunt 6 supplies, to the respective liquid header portions 7a and 7b, two-phase refrigerant of the amount corresponding to the air quantities of the divided regions connected with the liquid header portions 7a and 7b. As such, as shown in
Further, in Embodiment 1, two-phase refrigerant, in which the amount of gas refrigerant is adjusted, flows into the liquid header portions 7a and 7b. This means that the refrigerant, in which the gas refrigerant speed is adjusted, flows into the liquid header portions 7a and 7b. As such, the liquid refrigerant in the liquid header portions 7a and 7b is lifted upward accompanied by the gas refrigerant. Accordingly, with respect to the heat transfer tube 15 of a divided region, refrigerant can be supplied along with the wind speed distribution (air quantity distribution) of the divided region. As such, the performance of the outdoor heat exchanger 8 can be further improved.
It should be noted that when the wind speed distribution of the outdoor heat exchanger 8 is changed such as a case where the air quantity of the fan 12 is changed according to variation of the air conditioning load, for example, it is only necessary to adjust the amount of gas refrigerant (that is, gas refrigerant speed) supplied to the liquid header portions 7a and 7b by controlling the opening degree of the flow rate control mechanism 11. For example, when the air quantity of the fan 12 is increased so that the wind speed distribution in the divided region is largely biased, the opening degree of the flow rate control mechanism 11 may be decreased to increase the amount of gas refrigerant flowing into the liquid header portions 7a and 7b to increase the gas refrigerant speed in the liquid header portions 7a and 7b. Thereby, the amount of liquid refrigerant lifted upward is increased, which enables the refrigerant to be allocated according to the wind speed distribution in the divided region. Meanwhile, when the air quantity of the fan 12 is reduced so that the bias of the wind speed distribution in the divided region is decreased, the opening degree of the flow rate control mechanism 11 may be increased to decrease the amount of gas refrigerant flowing into the liquid header portions 7a and 7b to decrease the gas refrigerant speed in the liquid header portions 7a and 7b. Thereby, the amount of liquid refrigerant lifted upward is decreased, which enables the refrigerant to be allocated according to the wind speed distribution in the divided region.
As described above, the two-phase refrigerant, flowing into the respective heat transfer tubes 15 of the outdoor heat exchanger 8 as described above, exchanges heat with the outdoor air and absorbs heat from the outdoor and evaporates to be low-pressure gas refrigerant, passes through the four-way valve 2 and returns to the suction side of the compressor 1.
When the air-conditioning apparatus 300 performs the cooling operation, the gas refrigerant compressed to be high temperature and high pressure by the compressor 1 flows into the outdoor heat exchanger 8 along with the broken line of the four-way valve 2. As the refrigerant is single-phase gas, it is allocated and supplied almost equally to the refrigerant heat transfer tubes of the outdoor heat exchanger 8 by the gas header 9. The gas refrigerant, having flowed therein, exchanges heat with the outdoor air by the fan 12 and discharges heat to the outdoor, and is condensed to high-temperature and high-pressure liquid refrigerant. The high-temperature and high-pressure liquid refrigerant passes through the first gas-liquid separator 5 and decompressed by the expansion valve 4 to be two-phase refrigerant, and flows into the indoor heat exchanger 3. Here, the flow rate control mechanism 11 is closed to prevent the refrigerant from returning from the first gas-liquid separator 5 to the suction side of the compressor 1. In the indoor heat exchanger 3, the refrigerant exchanges heat with the indoor air and absorbs heat from the inside of the room to evaporate to become low-pressure gas refrigerant that passes through the four-way valve 2 to return to the suction side of the compressor 1.
As described above, in the air-conditioning apparatus 300 configured as Embodiment 1, two-phase refrigerant, in which the quality is adjusted by the first gas-liquid separator 5, is supplied to the shunt 6. As such, the air-conditioning apparatus 300 of Embodiment 1 is able to adjust the gas refrigerant speed flowing in the respective liquid header portions 7a and 7b. Further, in the air-conditioning apparatus 300 according to Embodiment 1, the shunt 6 supplies, to the respective liquid header portions 7a and 7b, two-phase refrigerant of the amount corresponding to the divided regions of the outdoor heat exchanger 8 connected with the respective liquid header portions 7a and 7b. As such, as the air-conditioning apparatus 300 of Embodiment 1 is able to adjust the amount of liquid refrigerant lifted upward in the liquid header portion by the gas refrigerant according to the wind speed distribution, the performance of the outdoor heat exchanger 8 can be improved sufficiently.
In Embodiment 1, the liquid header portions 7a and 7b are formed to be in the same shape. However, the shapes of the liquid header portion 7a and the liquid header portion 7b may be different. For example, the inner diameters of the liquid header portion 7a and the liquid header portion 7b may be different. It should be noted that the configurations not described in Embodiment 2 are the same as those of Embodiment 1, and the configurations that are the same as those of Embodiment 1 are denoted by the same reference numerals.
As shown in
As such, in Embodiment 2, an inner diameter D7a of the liquid header portion 7a, arranged at a position close to the fan 12, is formed to be smaller than an inner diameter D7b of the liquid header portion 7b. By forming the inner diameter of the liquid header portion 7a to be smaller, the speed of gas refrigerant flowing in the liquid header portion 7a can be faster. As the flow velocity of the gas refrigerant in the liquid header portion 7a is faster, the liquid refrigerant in the liquid header portion 7a is lifted upward accompanied by the gas refrigerant. As such, even in the case where the distribution of the wind speed in a divided region is largely biased, the refrigerant can be supplied to the heat transfer tubes 15 of the divided region along the distribution of the wind speed (distribution of air quantity) of the divided region.
It should be noted that while the liquid header portions 7a and 7b of Embodiment 2 are in the same height (Ha=Hb) as in the case of Embodiment 1, the present invention is not limited to this. For example, when Ha<Hb, the capacity of a portion of the outdoor heat exchanger 8 connected with the liquid header portion 7b arranged at a position far from the fan 12, of the entire capacity of the outdoor heat exchanger 8, is larger, compared with the case of Ha=Hb. On the other hand, the capacity of a portion of the outdoor heat exchanger 8 connected with the liquid header portion 7a arranged at a position close to the fan 12 is smaller. In that case, a refrigerant flow rate G7a flowing in the liquid header portion 7a arranged at a position closer to the fan 12 is less than a refrigerant flow rate G7b flowing in the liquid header portion 7b. For example, Ha:Hb=G7a:G7b is satisfied, in proportion to the heights of the liquid header portions 7a and 7b. A refrigerant mass flux G7a′, flowing in the liquid header portion 7a arranged at a position close to the fan 12 in that case, is defined by the following Expression (1), for example:
G7a′=G7a/{(D7a/2)2×π} (1)
Similarly, a refrigerant mass flux G7b′, flowing in the liquid header portion 7b arranged at a position far from the fan 12, is defined by the following Expression (2), for example:
G7b′=G7b/{(D7b/2)2×π} (2)
At this time, when the inner diameter D7a of the liquid header portion 7a of Expression (1) is replaced with D7a′, there is D7a′ in which the refrigerant mass flux flowing to the liquid header portion 7a and the refrigerant mass flux flowing to the liquid header portion 7b become equal. This means that there is D7a′ satisfying G7a′=G7b′. D7a′ satisfies D7a′<D7b. As such, in the case of determining the inner diameters of the liquid header portions 7a and 7b to satisfy G7a′=G7b′, the inner diameter of the liquid header portion 7a at a position close to the fan 12 is D7a′, which is smaller than the inner diameter D7b of the liquid header portion 7b at a position far from the fan 12. However, the argument point in Embodiment 2 is not simply the size of the inner diameters of the liquid header portions 7a and 7b, but setting the inner diameter D7a of the liquid header portion 7a at a position close to the fan 12 to satisfy D7a<D7a′, considering a diameter equivalent to the refrigerant mass flux. This also applies to the case of Ha>Hb.
Here, the liquid header portion 7a corresponds to a first liquid header portion of the present invention. The liquid header portion 7b corresponds to a second liquid header portion of the present invention. D7a′ corresponds to D1 of the present invention, and D7a corresponds to D of the present invention.
As described above, by forming the inner diameter of the liquid header portion 7a arranged at a position close to the fan 12 (connected with a divided region where distribution of the wind speed is more biased) to be smaller than the inner diameter of the liquid header portion 7b arranged at a position away from the fan 12 (connected with a divided region where distribution of the wind speed is less biased) as in Embodiment 2, it is possible to realize refrigerant allocation along the distribution of the wind speed more, and to further improve the capability of the outdoor heat exchanger 8.
In the case of forming the liquid header portion 7a and the liquid header portion 7b to have different shapes, the heights of the liquid header portion 7a and the liquid header portion 7b may be different. It should be noted that the configurations not described in Embodiment 3 are the same as those of Embodiment 1 or Embodiment 2, and the configurations that are same as those of the above-described embodiments are denoted by the same reference numerals.
As shown in
As described above, when the width in the up and down direction of the upper divided region, where the distribution of the wind speed is more biased, is larger, by forming the height Ha of the liquid header portion 7a connected with the divided region to be higher, it is possible to supply more refrigerant to such a divided region, which enables refrigerant allocation along the distribution of the wind speed. Accordingly, the performance of the outdoor heat exchanger 8 can be further improved.
In Embodiments 1 to 3, the liquid header 7 is divided into two liquid header portions 7a and 7b. However, the number of divisions of the liquid header 7 is not limited to two. It is obvious that the liquid header 7 may be divided into three or more as in the case of Embodiment 4. It should be noted that the configurations not described in Embodiment 4 are the same as those in any of Embodiments 1 to 3, and the configurations that are same as those of the above-described embodiments are denoted by the same reference numerals.
In Embodiment 4, the liquid header 7 is divided into three, namely a liquid header portion 7a arranged in an upper portion, a liquid header portion 7b arranged in an intermediate portion, and a liquid header portion 7c arranged in a lower portion. Then, the inner diameter of the liquid header portion 7a connected with the upper divided region, where the distribution of the wind speed is most biased, is formed to be the smallest, the inner diameter of the liquid header portion 7b connected with the intermediate divided region, where the distribution of the wind speed is secondly biased, is formed to be the second smallest, and the inner diameter of the liquid header portion 7c connected with the lower divided region, where the distribution of the wind speed is least biased (constant), is formed to be the largest.
In the case where the distribution of the wind speed in the up and down direction of the outdoor heat exchanger 8 is suddenly increased near the fan 12, by dividing the liquid header 7 into three and forming the inner diameters of the liquid header 7 to be smaller in the order of the liquid header portion 7c, the liquid header portion 7b, and the liquid header portion 7a, as in the case of Embodiment 4, it is possible to supply a larger amount of refrigerant to the divided region of a larger air quantity, along the distribution of the air quantity. Accordingly, the performance of the outdoor heat exchanger 8 can be further improved.
In Embodiments 2 to 4, as the distribution of the wind speed is most biased in the upper divided region of the outdoor heat exchanger 8, the inner diameter of the liquid header portion 7a arranged in an upper portion (that is, arranged at a position closest to the fan 12) is formed to be the smallest. However, depending on the specification of the outdoor heat exchanger 8, there is a case where the distribution of the wind speed is most biased at a position other than the upper portion of the outdoor heat exchanger 8. In that case, the liquid header 7 may be configured as described below. It should be noted that the configurations not described in Embodiment 5 are the same as those in any of Embodiments 1 to 4, and the configurations that are the same as those of the above-described embodiments are denoted by the same reference numerals.
For example, as shown in
As such, in Embodiment 5, the liquid header 7 is divided into three, namely the liquid header portion 7a arranged in the upper portion, the liquid header portion 7b arranged in the intermediate portion, and the liquid header portion 7c arranged in the lower portion. Then, the inner diameter of the liquid header portion 7b connected with the central divided region, where distribution of the wind speed is more biased, is formed to be smaller, and the inner diameters of the liquid header portions 7a and 7c connected with the upper and lower divided regions, where distribution of the wind speed is less biased (constant), are formed to be larger. By forming the inner diameter of the liquid header portion 7b to be smaller than the inner diameters of the liquid header portions 7a and 7c, it is possible to supply refrigerant that is uniform in the height direction of the outdoor heat exchanger 8 to a portion where distribution of the air quantity is constant, and to supply refrigerant to a portion where distribution of the wind speed is increased along the distribution of the wind speed of the outdoor heat exchanger 8. As such, performance of the outdoor heat exchanger 8 can be improved sufficiently.
It should be noted that while
The present invention is also applicable to a multi-split type air-conditioning apparatus in which a plurality of indoor units are connected with a heat source unit (outdoor unit), and cooling or heating can be performed selectively by each indoor unit in such a manner that cooling can be performed in one indoor unit while heating can be performed in another indoor unit simultaneously. It should be noted that the configurations not described in Embodiment 6 are the same as those in any of Embodiments 1 to 5, and the configurations that are same as those of the above-described embodiments are denoted by the same reference numerals.
An air-conditioning apparatus (multi-split type air-conditioning apparatus) according to Embodiment 6 includes the outdoor unit having at least the compressor, a four-way valve, the liquid header divided into the liquid header portions in the up and down direction, the shunt, the outdoor heat exchanger, and the outdoor fan; a relay unit connected with the outdoor unit by a first connection pipe and a second connection pipe; and a plurality of indoor units each having at least an indoor heat exchanger and connected with the relay unit in parallel with each other. The outdoor unit includes a first path for guiding refrigerant, discharged from the compressor, to the second connection pipe through the four-way valve, the liquid header, and the outdoor heat exchanger; and a second path for guiding the refrigerant to the second connection pipe through the four-way valve while bypassing the liquid header and the outdoor heat exchanger, according respective operation modes of cooling, heating, cooling main, and heating main. The relay unit includes a second gas-liquid separator connected to the middle of the second connection pipe; a switching unit that selectively connects each of the indoor units and either the first connection pipe or the second connection pipe; a second bypass pipe connecting the second gas-liquid separator and each of other indoor units; a third bypass pipe connecting the first connection pipe and the second bypass pipe; and a bypass pipe flow rate control device interposed in the third bypass pipe and functioning as the expansion valve. The air conditioning apparatus further includes a third gas-liquid separator connected with the first connection pipe and functioning as the first gas-liquid separator in the heating operation mode and the heating main operation mode; a gas side outlet pipe and a flow rate control mechanism connecting the third gas-liquid separator and the suction side of the compressor, and functioning as the bypass in the heating operation mode and the heating main operation mode; and a third path for supplying two-phase refrigerant, in which quality is adjusted by the third gas-liquid separator, to the shunt, in the heating operation mode and the heating main operation mode.
Further, in the air-conditioning apparatus of Embodiment 6, the indoor unit includes an indoor heat exchanger functioning as the condenser when the indoor unit performs heating, and a first flow rate control device functioning as the expansion valve.
The multi-split type air-conditioning apparatus 10000 according to Embodiment 6 includes an outdoor unit (also referred to as a heat source unit) 101, a relay unit 102, and a plurality of indoor units 103 (103a, 103b, and 103c). It should be noted that while description is given on the case where one outdoor unit is connected with one relay unit and three indoor units in this embodiment, the case of connecting two or more outdoor units, two or more relay units, and two or more indoor units is the same.
Hereinafter, configuration of each device will be described in more detail.
(Configuration of Outdoor Unit 101)
The outdoor unit 101 includes therein a compressor 1 that compresses and discharges refrigerant, a four-way valve 2 that is a switching valve for switching the refrigerant flow direction in the outdoor unit 101, a gas header 9, an outdoor heat exchanger 8, a liquid header 7 (liquid header portions 7a and 7b), a shunt 6, an accumulator 44, and a third gas-liquid separator 140. The inlet of the third gas-liquid separator 140 is connected with a first connection pipe 21 provided inside a relay unit 102 described below. A liquid side outlet pipe 25 for discharging liquid refrigerant in which gas and liquid are separated by the third gas-liquid separator 140, or two-phase refrigerant in which the quality is adjusted, is connected with the four-way valve via a check valve 160. The check valve 160 allows liquid refrigerant to flow only from the third gas-liquid separator 140 to the four-way valve 2. Further, a gas side outlet pipe 26 for discharging gas refrigerant in which gas and liquid are separated by the third gas-liquid separator 140, is connected with the inlet or the inside of the accumulator 44 via a gas side bypass flow channel resistance 150 functioning as a flow rate control mechanism. In this way, it is configured that the refrigerant in the third gas-liquid separator 140 flows in one direction to the suction side of the compressor 1.
The compressor 1, the four-way valve 2, the gas header 9, the outdoor heat exchanger 8, (the liquid header portions 7a and 7b), and the shunt 6 are connected in this order by the discharge pipe 31. Further, the outdoor heat exchanger 8 is connected with the relay unit 102 via the second connection pipe 22 narrower than the first connection pipe 21, by the refrigerant pipe 32 in which the check valve 190 is provided. The check valve 190 has a function of allowing refrigerant to flow only from the outdoor heat exchanger 8 to the second connection pipe 22. The liquid side outlet pipe 25 and the refrigerant pipe 32 are connected with each other by a short-circuit pipe 33 having a check valve 170 and a short-circuit pipe 34 having a check valve 180. Both the check valve 170 and the check valve 180 allow refrigerant to flow only from the liquid side outlet pipe 25 to the refrigerant pipe 32. The circuits having the check valves 160, 170, 180, and 190 constitute a flow channel switching circuit 35 on the outdoor unit side.
The outlet of the accumulator 44 and the suction port of the compressor 1 are connected with each other by a suction pipe 36, and the four-way valve 2 and the accumulator 44 are connected with each other by a refrigerant pipe 37.
The outdoor unit 101 is provided with a fan 12 (not shown in
(Configuration of Relay Unit 102)
The outdoor unit 101 and the relay unit 102, configured as described above, are connected with each other by the first connection pipe 21 that is a wide pipe, and the second connection pipe 22 that is a pipe narrower than the first connection pipe 21.
The relay unit 102 includes a second gas-liquid separation device (intra-relay unit gas-liquid separation device) 50 connected to the middle of the second connection pipe 22. A gas phase portion of the second gas-liquid separator 50 is connected with branch pipes 21a, 21b, and 21c of the indoor units 103a, 103b, and 103c connected parallel to each other, via solenoid valves 120a, 120b, and 120c, respectively. The branch pipes 21a, 21b, and 21c are connected with indoor heat exchangers 1000a, 1000b, and 1000c of the indoor units 103a, 103b, and 103c. Further, the branch pipes 21a, 21b, and 21c are provided with the solenoid valves 130a, 130b, and 130c. Here, a circuit configured of the solenoid valves 120a, 120b, 120c and solenoid valves 130a, 130b, and 130c is called a switching unit 104. Further, the liquid phase portion of the second gas-liquid separator 50 is connected with a second bypass pipe 23, and the second bypass pipe 23 is connected with the indoor units 103a, 103b, and 103c via branch pipes 22a, 22b, and 22c, respectively. The branch pipes 22a, 22b, and 22c are provided with first flow rate control devices 110a, 110b, and 110c.
Further, a third bypass pipe 24 branching from the first connection pipe 21 is provided, and the other end of the third bypass pipe 24 is connected with the second bypass pipe 23. Between the second bypass pipe 23 and the third bypass pipe 24, a first heat exchanger 60 and a second heat exchanger 70, for exchanging heat between refrigerant flowing in the second bypass pipe 23 and refrigerant flowing in the third bypass pipe 24, are provided. Further, the second bypass pipe 23, located between the first heat exchanger 60 and second heat exchanger 70, is provided with an openable/closable third flow rate control device 85. Further, between the second heat exchanger 70 and the other end connecting portion of the third bypass pipe 24 (connecting portion with the second bypass pipe 23), an openable/closable second flow rate control device 90 (bypass pipe flow rate control device) is provided.
(Configuration of Indoor Unit 103)
The indoor units 103a, 103b, and 103c are connected with each other to allow refrigerant to circulate through the branch pipes 21a, 21b, and 21c branching from the first connection pipe 21 of the relay unit 102 and the branch pipes 22a, 22b, and 22c branching from the second bypass pipe 23. The respective indoor units 103a, 103b, and 103c include indoor heat exchangers 1000a, 1000b, and 1000c, and the openable/closable first flow rate control devices 110a, 110b, and 110c, respectively. The first flow rate control devices 110a, 110b, and 110c are connected in the vicinity of the indoor heat exchangers 1000a, 1000b, and 1000c, and at the time of cooling, they are controlled according to the degree of superheat of the outlet side of the indoor heat exchangers 1000a, 1000b, and 1000c, and at the time of heating, they are controlled according to the degree of subcooling.
Operational actions at the time of various types of operation performed by the multi-split type air-conditioning apparatus 10000 will be described. Operational actions by the multi-split type air-conditioning apparatus 10000 include four operation modes, namely cooling, heating, cooling main, and heating main.
In this embodiment, a cooling operation mode is an operation mode in which all operating indoor units perform cooling, and a heating operation mode is an operation mode in which all operating indoor units perform heating. A cooling main operation mode is an operation mode in which an indoor unit performing cooling operation and an indoor unit performing heating operation are mixed, and the cooling load is larger than the heating load. A heating main operation mode is an operation mode in which an indoor unit performing cooling operation and an indoor unit performing heating operation are mixed, and the heating load is larger than the cooling load.
In the cooling main operation mode, the outdoor heat exchanger 8 is connected to the discharge side of the compressor 1, and acts as a condenser (radiator). In the heating main operation mode, the outdoor heat exchanger 8 is connected to the suction side of the compressor 1, and acts as an evaporator. Hereinafter, the flow of refrigerant in each operation mode will be described.
(Heating Operation Mode)
In the case of performing heating operation, the four-way valve 2 is switched such that the refrigerant discharged from the compressor 1 passes through the second connection pipe 22 to flow into the switching unit 104 configured of the solenoid valves 120a, 120b, and 120c and the solenoid valves 130a, 130b, and 130c, without bypassing through the outdoor heat exchanger 8 and the liquid header 7. Further, in the switching unit 104, the solenoid valves 130a, 130b, and 130c provided to the branch pipes 21a, 21b, and 21c are controlled to be in a closed state, and the solenoid valves 120a, 120b, and 120c provided to the pipes connected from the second connection pipe 22 to the indoor units 103a, 103b, and 103c are controlled to be in an open state. It should be noted that in
The high-temperature and high-pressure gas refrigerant, discharged from the compressor 1, passes through the four-way valve 2, the short-circuit pipe 34, and the check valve 180, and flows into the switching unit 104 via the second connection pipe 22 and the second gas-liquid separator 50. The high-temperature and high-pressure gas refrigerant, flowing in the switching unit 104, branches by the switching unit 104, and the respective portions of the refrigerant flow into the indoor heat exchangers 1000a, 1000b, and 1000c through the solenoid valves 120a, 120b, and 120c. Then, the refrigerant is cooled, while heating the indoor air, to be medium-temperature and high-pressure liquid refrigerant.
The respective portions of medium-temperature and high-pressure liquid refrigerant, having flowed out of the indoor heat exchangers 1000a, 1000b, and 1000c, flow into the first flow rate control devices 110a, 110b, and 110c, and join at a second branch portion 105 configured of the branch pipes 22a, 22b, and 22c, and the refrigerant further flows into the second flow rate control device 90. Then, the high-pressure liquid refrigerant is throttled by the second flow rate control device 90 to be expanded and decompressed to be in a low-temperature and low-pressure two-phase gas-liquid state.
The refrigerant in the low-temperature and low-pressure two-phase gas-liquid state, having flowed out of the second flow rate control device 90, flows into the third gas-liquid separator 140 in the outdoor unit 101 via the third bypass pipe 24 and the first connection pipe 21. The gas refrigerant, in which gas and liquid are separated by the third gas-liquid separator 140, flows into the inlet or the inside of the accumulator 44 via the gas side outlet pipe 26 and the gas side bypass flow channel resistance 150. Further, the two-phase refrigerant, in which gas and liquid are separated and the quality is controlled by the third gas-liquid separator 140, flows from the liquid side outlet pipe 25 through the short circuit pipe 33 and the check valve 170, and then flows into the shunt 6. The two-phase refrigerant, flowing in the shunt 6, is supplied to the liquid header portion 7a and the liquid header portion 7b that are divided into two. Then, the two-phase refrigerant, supplied to the liquid header portion 7a, is allocated to the respective heat transfer tubes 15 connected with the liquid header portion 7a (respective heat transfer tubes 15 arranged in the upper divided region of the outdoor heat exchanger 8). Further, the two-phase refrigerant, supplied to the liquid header portion 7b, is allocated to the respective heat transfer tubes 15 connected with the liquid header portion 7b (respective heat transfer tubes 15 arranged in the lower divided portion of the outdoor heat exchanger 8). The refrigerant flowing in the outdoor heat exchanger 8 is heated, while cooling the outdoor air, to be low-temperature and low-pressure gas refrigerant.
The low-temperature and low-pressure gas refrigerant, having flowed out of the outdoor heat exchanger 8, passes through the four-way valve 2 via the gas header 9, and joins the gas refrigerant, in which gas and liquid are separated by the third gas-liquid separator 140, at the inlet or the inside of the accumulator 44, and flows into the compressor 1 and is compressed. Afterwards, the refrigerant circulates the same path as described above.
(Cooling Operation Mode)
In the case of performing cooling, the four-way valve 2 is switched such that the refrigerant, discharged from the compressor 1, flows into the outdoor heat exchanger 8. Further, in the switching unit 104, the solenoid valves 130a, 130b, and 130c connected with the indoor units 103a, 103b, and 103c are controlled to be in an open state, and the solenoid valves 120a, 120b, and 120c are controlled to be in a closed state. It should be noted that in
The high-temperature and high-pressure gas refrigerant, discharged from the compressor 1, flows into the outdoor heat exchanger 8 via the four-way valve 2. At this time, the refrigerant is cooled, while heating the outdoor air, to be medium-temperature and high-pressure liquid refrigerant.
The medium-temperature and high-pressure liquid refrigerant, having flowed out of the outdoor heat exchanger 8, passes through the second connection pipe 22, the second gas-liquid separator 50 and the second bypass pipe 23, and the third flow rate control device 85, via the check valve 190, and in the first heat exchanger 60 and the second heat exchanger 70, exchanges heat with the refrigerant flowing in the third bypass pipe 24 to be cooled.
The liquid refrigerant cooled by the first heat exchanger 60 and the second heat exchanger 70 flows into the second branch portion 105 configured of the branch pipes 22a, 22b, and 22c, while allowing a part of the refrigerant to bypass to flow into the third bypass pipe 24. The high-pressure liquid refrigerant flowing in the second branch portion 105 branches at the second branch portion 105 and the respective portions of the refrigerant flow into the first flow rate control devices 110a, 110b, and 110c. Then, the high-pressure liquid refrigerant is throttled by the first flow rate control devices 110a, 110b, and 110c to be expanded and compressed to be in a low-temperature and low-pressure two-phase gas-liquid state.
The respective portions of the refrigerant in the low-temperature and low-pressure two-phase gas-liquid state, having flowed out of the first flow rate control device 110a, 110b, and 110c, flow into the indoor heat exchangers 1000a, 1000b, and 1000c. Then, the refrigerant is heated, while cooling the indoor air, to be low-temperature and low-pressure gas refrigerant.
The respective portions of the low-temperature and low-pressure gas refrigerant, having flowed out of the indoor heat exchangers 1000a, 1000b, and 1000c, pass through the solenoid valves 130a, 130b, and 130c, respectively, join the low-temperature and low-pressure gas refrigerant heated by the first heat exchanger 60 and the second heat exchanger 70 of the third bypass pipe 24, and the refrigerant flows into the first connection pipe 21. At this time, in the refrigerant circuit of the present embodiment, as the flow of the refrigerant at the inlet of the second gas-liquid separator 50 is in one direction, the gas refrigerant passing through the first connection pipe 21 flows into the third gas-liquid separator 140, and flows out while branching to the two paths, namely the gas side outlet pipe 26 and the liquid side outlet pipe 25. The gas refrigerant, flowing to the gas side outlet pipe 26, passes through the gas side bypass flow channel resistance 150 and flows into the inlet or the inside of the accumulator 44. The gas refrigerant, flowing to the liquid side outlet pipe 25, passes through the check valve 160 and flows into the accumulator 44 via the four-way valve 2.
The respective portions of gas refrigerant, branched by the third gas-liquid separator 140, join at the inlet or the inside of the accumulator 44, and the refrigerant flows into the compressor 1 and is compressed. At this time, as the gas refrigerant, having flowed in through the first connection pipe 21, is branched by the third gas-liquid separator 140, the sectional area of the flow channel in the path from the third gas-liquid separator 140 to the accumulator 44 is increased, whereby it is possible to reduce the pressure loss in the path. As such, the compressor suction temperature is maintained at a high level, so that the performance of the compressor 1 is improved.
(Heating Main Operation Mode)
The high-temperature and high-pressure gas refrigerant, discharged from the compressor 1, passes through the four-way valve 2, the short-circuit pipe 34, and the check valve 180, and flows into the switching unit 104 via the second connection pipe 22 and the second gas-liquid separator 50. The high-temperature and high-pressure gas refrigerant, flowing in the switching unit 104, is branched by the switching unit 104, and the respective portions of the refrigerant pass through the solenoid valves 120a, and 120b, and flow into the indoor heat exchangers 1000a and 1000b that perform heating. Then, the refrigerant is cooled, while heating the indoor air, to be medium-temperature and high-pressure liquid refrigerant.
The respective portions of the medium-temperature and high-pressure liquid refrigerant, having flowed out of the indoor heat exchangers 1000a and 1000b, flow into the first flow rate control devices 110a and 110b, and join at the second branch portion 105 configured of the branch pipes 22a, 22b, and 22c. A portion of the high-pressure liquid refrigerant, joined at the second branch portion 105, flows into the first flow rate control device 110c connected with the indoor unit 103c that performs cooling. Then, the high-pressure liquid refrigerant is throttled by the first flow rate control device 110c and expanded to be in a low-temperature and low-pressure two-phase gas-liquid state. The refrigerant in the low-temperature and low-pressure two-phase gas-liquid state, having flowed out of the first flow rate control device 110c, flows into the indoor heat exchanger 1000c. Then, the refrigerant is heated, while cooling the indoor air, to be low-temperature and low-pressure gas refrigerant. The low-temperature and low-pressure gas refrigerant, having flowed out of the indoor heat exchanger 1000c, passes through the solenoid valve 130c and flows into the first connection pipe 21.
On the other hand, the residual of the high-pressure liquid refrigerant flowing from the indoor heat exchangers 1000a and 1000b, performing heating, to the second branch portion 105 flows into the second flow rate control device 90. Then, the high-pressure liquid refrigerant is throttled by the second flow rate control device 90 to be expanded (decompressed) to be in a low-temperature and low-pressure two-phase gas-liquid. The refrigerant in the low-temperature and low-pressure two-phase gas-liquid state, having flowed out of the second flow rate control device 90, passes through the third bypass pipe 24 and flows into the first connection pipe 21, and joins the refrigerant in a low-temperature and low-pressure vapor state having flowing from the indoor heat exchanger 1000c that performs cooling.
The refrigerant in the low-temperature and low-pressure two-phase gas-liquid state, joined at the first connection pipe 21, flows into the third gas-liquid separator 140 in the outdoor unit 101. The gas refrigerant, in which gas and liquid are separated by the third gas-liquid separator 140, flows into the inlet or the inside of the accumulator 44, via the gas side outlet pipe 26 and the gas side bypass flow channel resistance 150. The two-phase refrigerant, in which gas and liquid are separated and the quality is controlled by the third gas-liquid separator 140, flows from the liquid side outlet pipe 25 through the short circuit pipe 33 and the check valve 170, into the shunt 6. The two-phase refrigerant flowing in the shunt 6 is supplied to the liquid header portion 7a and the liquid header portion 7b that are divided into two. Then, the two-phase liquid refrigerant, supplied to the liquid header portion 7a, is allocated to the respective heat transfer tubes 15 connected with the liquid header portion 7a (respective heat transfer tubes 15 arranged in the upper divided region of the outdoor heat exchanger 8). Further, the two-phase refrigerant, supplied to the liquid header portion 7b, is allocated to the respective heat transfer tubes 15 connected with the liquid header portion 7b (respective heat transfer tubes 15 arranged in the lower divided portion of the outdoor heat exchanger 8). The refrigerant having flowed into the outdoor heat exchanger 8 absorbs heat from the outdoor air and is heated, while cooling the outdoor air, to be low-temperature and low-pressure gas refrigerant. The low-temperature and low-pressure gas refrigerant, having flowed out of the outdoor heat exchanger 8, passes through the four-way valve 2, joins the gas refrigerant, in which gas and liquid are separated by the third gas-liquid separator 140, at the inlet or the inside of the accumulator 44, and the refrigerant flows into the compressor 1 and is compressed. At this time, by allowing a part of gas refrigerant to bypass by the third gas-liquid separator 140, it is possible to reduce a pressure loss of the outdoor heat exchanger 8.
It should be noted that a configuration without the accumulator 44 may be possible. In that case, the gas side outlet pipe 26 is connected to the suction side of the compressor 1.
(Cooling Main Operation Mode)
The high-temperature and high-pressure gas refrigerant discharged from the compressor 1 flows into the outdoor heat exchanger 8 via the four-way valve 2. At this time, in the outdoor heat exchanger 8, the refrigerant is cooled while heating the outdoor air, remaining the amount of heat required for heating, to be in a medium-temperature and high-pressure two-phase gas-liquid state.
The medium-temperature and high-pressure two-phase gas-liquid refrigerant, having flowed out of the outdoor heat exchanger 8, passes through the second connection pipe 22 via the check valve 190 and flows into the second gas-liquid separator 50. Then, in the second gas-liquid separator 50, it is separated into gas refrigerant and liquid refrigerant.
The gas refrigerant, separated by the second gas-liquid separator 50, flows into the indoor heat exchanger 1000a that performs heating, via the solenoid valve 120a. Then, the refrigerant is cooled, while heating the indoor air, to be medium-temperature and high-pressure gas refrigerant.
On the other hand, the liquid refrigerant, separated by the second gas-liquid separator 50, flows into the first heat exchanger 60, and exchanges heat with the low-pressure refrigerant flowing in the third bypass pipe 24 to be cooled.
The refrigerant having flowed out of the indoor heat exchanger 1000a that performs heating and the refrigerant having flowed out of the first heat exchanger 60 pass through the first flow rate control device 110a and the third flow rate control device 85, and the second heat exchanger 70, respectively, and join.
The joined liquid refrigerant branches at the second branch portion 105 configured of the branch pipes 22a, 22b, and 22c, while allowing a portion of the refrigerant to bypass to flow into the third bypass pipe 24, and the respective portions of the refrigerant flow into the first flow rate control devices 110b and 110c of the indoor units 103b and 103c that perform cooling. Then, the high-pressure liquid refrigerant is throttled by the first flow rate control devices 110b and 110c and expanded and decompressed to be in a low-temperature and low-pressure two-phase gas-liquid state. Changes in the state of the respective portions of the refrigerant by the first flow rate control devices 110b and 110c are performed under a condition that enthalpy is constant.
The respective portions of the refrigerant in the low-temperature and low-pressure two-phase gas-liquid state, having flowed out of the first flow rate control devices 110b and 110c, flow into the indoor heat exchangers 1000b and 1000c that perform cooling. Then, the refrigerant is heated, while cooling the indoor air, to be low-temperature and low-pressure gas refrigerant.
The respective portions of the low-temperature and low-pressure gas refrigerant, having flowed out of the indoor heat exchanger 1000b and 1000c, pass through the solenoid valves 130b and 130c respectively and join, and the refrigerant passes through the first connection pipe 21. Then, the low-temperature and low-pressure gas refrigerant flowing in the first connection pipe 21 in a joined state, further joins the low-temperature and low-pressure gas refrigerant heated by the first heat exchanger 60 and the second heat exchanger 70 in the third bypass pipe 24, and flows into the first connection pipe 21.
The gas refrigerant, passing through the first connection pipe 21, flows into the third gas-liquid separator 140 in the outdoor unit 101, and flows out while branching to two paths namely the gas side outlet pipe 26 and the liquid side outlet pipe 25. The gas refrigerant, having flowed out to the gas side outlet pipe 26, passes through the gas side bypass flow channel resistance 150 and flows into the inlet or the inside of the accumulator 44. The gas refrigerant, having flowed out of the liquid side outlet pipe 25, passes through the check valve 160 and flows into the accumulator 44 via the four-way valve 2. The gas refrigerant, branched by the third gas-liquid separator 140, joins at the inlet or the inside of the accumulator 44, and the refrigerant flows into the compressor 1 and is compressed. At this time, as the gas refrigerant having flowed in through the first connection pipe 21 is branched by the third gas-liquid separator 140, the sectional area of the flow channel from the third gas-liquid separator 140 to the accumulator 44 is increased, whereby it is possible to reduce a pressure loss in the path. As such, the compressor suction temperature is maintained at a high level, and the performance of the compressor 1 is improved.
As described above, even in the multi-split type air-conditioning apparatus 10000 configured as Embodiment 6, in the heating operation mode and the heating main operation mode, two-phase refrigerant in which quality is adjusted by the third gas-liquid separator 140 is supplied to the shunt 6. As such, even in the multi-split type air-conditioning apparatus 10000 of Embodiment 6, the speed of the gas refrigerant flowing through the respective liquid header portions 7a and 7b can be adjusted. Further, even in the multi-split type air-conditioning apparatus 10000 according to Embodiment 6, the shunt 6 supplies, to the respective liquid header portions 7a and 7b, two-phase refrigerant of the amount corresponding to the divided regions of the outdoor heat exchanger 8 to which the respective liquid header portions 7a and 7b are connected. As such, even in the multi-split type air-conditioning apparatus 10000 of Embodiment 6, the amount of liquid refrigerant lifted upward by the gas refrigerant in the liquid header portion can be adjusted according to the distribution of the wind speed, and the refrigerant can be supplied to the divided region along the distribution of the wind speed. As such, performance of the outdoor heat exchanger 8 can be improved sufficiently.
It should be noted that while Embodiment 6 describes an example using the outdoor heat exchanger 8 and the liquid header 7 shown in Embodiment 1, the outdoor heat exchanger 8 and the liquid header 7 described in Embodiments 2 to 5 may be used. The effects described in Embodiments 2 to 5 can be achieved.
Further, the first heat exchanger 60, the second heat exchanger 70, and the third flow rate control device 85, provided to the second bypass pipe 23, are used for increasing the degree of subcooling of the liquid refrigerant flowing out of the second gas-liquid separator 50. As such, the first heat exchanger 60, the second heat exchanger 70, and the third flow rate control device 85 are not indispensable configurations in the present invention.
The multi-split type air-conditioning apparatus 10000, in which the present invention can be implemented, is not limited to the multi-split type air-conditioning apparatus 10000 described in Embodiment 6. It may be configured as described below. It should be noted that the configurations not described in Embodiment 7 are the same as those in any of Embodiments 1 to 6, and the configurations that are the same as those of the above-described embodiments are denoted by the same reference numerals.
In an air-conditioning apparatus (multi-split type air-conditioning apparatus) according to Embodiment 7, the relay unit includes a plurality of intermediate heat exchangers functioning as the condensers when the indoor units perform heating, and a plurality of first flow rate control devices connected with the respective intermediate heat exchangers and functioning as the expansion valves.
The indoor unit includes an indoor heat exchanger connected with the intermediate heat exchanger. To allow the refrigerant to flow in the outdoor unit and the intermediate heat exchanger of the relay unit, a closed first refrigerant circuit is configured, and to allow refrigerant other than the above-described refrigerant to flow in the indoor unit and the intermediate heat exchanger of the relay unit, a closed second refrigerant circuit is configured.
At the time of heating operation, the four-way valve 2 is switched such that the refrigerant flows from the compressor 1 to the indoor unit 103, and the solenoid valves 120a, 120b, and 120c in the relay unit 102 are controlled to be in an open state, and the solenoid valves 130a, 130b, and 130c are controlled to be in a closed state.
At the time of cooling main operation, when the indoor unit 103c performs heating operation and the indoor units 103a and 103b perform cooling operation, for example, the four-way valve 2 is switched such that the refrigerant flows from the compressor 1 to the outdoor heat exchanger 8, the solenoid valves 130a, 130b, and 120c in the relay unit 102 are controlled to be in an open state, and the solenoid valves 120a, 120b, and 130c are controlled to be in a closed state.
In the heating main operation, when the indoor unit 103c performs cooling operation and the indoor units 103a and 103b perform heating operation, for example, the four-way valve 2 is switched such that the refrigerant flows from the compressor 1 to the indoor unit 103, the solenoid valves 120a, 120b, and 130c in the relay unit 102 are controlled to be in an open state, and the solenoid valves 130a, 130b, and 120c are controlled to be in a closed state.
Further, in Embodiment 7, a relay unit side refrigerant circuit 41 (41a, 41b, and 41c) and an indoor unit side refrigerant circuit 42 (42a, 42b, and 42c), in which different kinds of refrigerants circulate as described below, are configured, and an intermediate heat exchanger 40 (40a, 40b, and 40c) is interposed between the two refrigerant circuits 41 and 42. This means that the branch pipes 22a, 22b, and 22c and the branch pipes 21a, 21b, and 21c are connected with each other such that the refrigerant circulates the outdoor unit 101 and the intermediate heat exchanger 40 (40a, 40b, and 40c) of the relay unit 102 connected with the outdoor unit 101 by the first connection pipe 21 and the second connection pipe 22, to form the closed refrigerant circuits 41a, 41b, and 41c. Then, the refrigerant circuits 41a, 41b, and 41c are provided with first flow rate control devices 110a, 110b, and 110c, respectively.
Meanwhile, the refrigerant circuits 42a, 42b, and 42c are configured to be closed such that refrigerant (water or antifreeze, for example) other than the above-described refrigerant circulates the indoor heat exchangers 1000a, 1000b, and 1000c of the indoor units 103a, 103b, and 103c and the intermediate heat exchangers 40 (40a, 40b, and 40c) of the relay unit 102. The refrigerant circuits 42a, 42b, and 42c are provided with pumps 43a, 43b, and 43c, and the intermediate heat exchangers 40a, 40b, and 40c are interposed between the relay unit side refrigerant circuits 41a, 41b, and 41c and the indoor unit side refrigerant circuits 42a, 42b, and 42c, to allow the refrigerant flowing in the refrigerant circuit 41 and the refrigerant flowing in the refrigerant circuit 42 to exchange heat with each other by the intermediate heat exchanger 40. The other functions and configurations are the same as those of Embodiment 6.
As described above, even when different kinds of refrigerants flow in the relay unit side refrigerant circuit 41 and the indoor unit side refrigerant circuit 42, the same effect as that of Embodiment 6 can be achieved.
In Embodiment 6 and Embodiment 7, the third gas-liquid separator 140 is provided to the outdoor unit 101. However, the third gas-liquid separator 140 may be provided to the relay unit 102. In the below description, an example in which the installment position of the third gas-liquid separator 140 is changed in the multi-split type air-conditioning apparatus 10000 shown in Embodiment 6 will be given.
In Embodiment 8, the third gas-liquid separator 140 is connected to the middle of the first connection pipe 21, and the third gas-liquid separator 140 is installed in the relay unit 102. By installing the third gas-liquid separator 140 in the relay unit 102 in this way, as gas refrigerant or liquid refrigerant, in which gas and liquid are separated, flows in the first connection pipe 21, it is possible to significantly reduce a pressure loss caused by the extension pipe between the outdoor unit 101 and the relay unit 102. The other functions and configurations are the same as those of Embodiment 6 and Embodiment 7.
(Zeotropic Refrigerant Mixture)
Regarding the refrigerant flowing in the outdoor units 100 and 101 described above, in the case of using zeotropic refrigerant mixture (for example, R404A, R407C, or the like) rather than single refrigerant (for example, R22 or the like) or azeotropic refrigerant mixture (for example, R502, R507A, or the like), gas refrigerant in which gas and liquid are separated, having a lower boiling point in the zeotropic refrigerant mixture, is allowed to bypass as gas refrigerant by the third gas-liquid separator 140, and liquid refrigerant, in which gas and liquid are separated, flows out as a zeotropic refrigerant mixture in which composition ratio is biased to refrigerant having a high boiling point with the inlet of the third gas-liquid separator 140. As such, in addition to the effect of reducing a pressure loss in the outdoor heat exchanger 8, there is an effect of mitigating temperature gradient (temperature glide) in a two-phase state that causes deterioration of performance of the zeotropic refrigerant mixture. The other functions and configurations are the same as Embodiments 1 to 8.
In Embodiments 1 to 9, details of a connection configuration between the liquid header portion and the outdoor heat exchanger 8 (in more detail, heat transfer tube 15) are not described particularly. By connecting the liquid header portion and the outdoor heat exchanger 8 as described below, it is possible to allow refrigerant to flow in a larger amount to the liquid header portion connected with a divided region of the outdoor heat exchanger 8 in which distribution of the wind speed is largely biased. It should be noted that the configurations not described in Embodiment 10 are the same as those in any of Embodiments 1 to 9, and the configurations that are the same as those of the above-described embodiments are denoted by the same reference numerals.
In Embodiment 10, respective liquid header portions 7a and 7b and the heat transfer tubes 15 of the outdoor heat exchanger 8 are connected by a plurality of branch pipes 45. In detail, the liquid header portion 7a arranged in an upper portion (connected with the heat transfer tubes 15 of a divided region having larger distribution of wind speed) is connected with the heat transfer tubes 15 of the outdoor heat exchanger 8 by the branch pipes 45a. Further, the liquid header portion 7b arranged in a lower portion (connected with the heat transfer tubes 15 of a divided region having a smaller distribution of wind speed) is connected with the heat transfer tubes 15 of the outdoor heat exchanger 8 by the branch pipes 45b. Compared with the liquid header portion 7b arranged in the lower portion, the liquid header portion 7a arranged in the upper portion has a configuration in which a larger number of branch pipes 45 are connected to a region of the same area. In other words, considering the number of each of the branch pipes 45a and 45b connected to a region of the same size, the number of the branch pipes 45a is larger than the number of the branch pipes 45b.
It should be noted that in Embodiment 10, when the outdoor heat exchanger 8 functions as an evaporator, the gas header 9 connected to a position which is a refrigerant outflow side of the outdoor heat exchanger 8 is divided into a plurality of gas header portions in the up and down direction. In
As described above, in Embodiment 10, compared with the liquid header portion 7b arranged in the lower portion, the liquid header portion 7a arranged in the upper portion has a configuration in which a larger number of branch pipes 45 are connected to a region of the same area. As such, the flow resistance of the refrigerant, flowing into the heat transfer tube 15 of a divided region having larger distribution of the wind speed, is smaller. Accordingly, a larger amount of refrigerant can be supplied to a divided region having larger wind speed distribution. As such, by connecting the liquid header portions 7a and 7b and the outdoor heat exchanger 8 as Embodiment 10, largely biased wind speed distribution can be managed.
In the configurations of Embodiments 1 to 10, by configuring the gas header 9 as described below, it is possible to supply a larger amount of refrigerant to a divided region having larger wind speed distribution. It should be noted that the configurations not described in Embodiment 11 are the same as those in any of Embodiments 1 to 10, and the configurations that are the same as those of the above-described embodiments are denoted by the same reference numerals.
In Embodiment 11, the gas header 9 is divided into a plurality of gas header portions in the up and down direction. In
In the configurations of Embodiments 1 to 11, even by configuring the gas header 9 as described below, it is possible to supply a larger amount of refrigerant to a divided region having larger wind speed distribution. It should be noted that the configurations not described in Embodiment 12 are the same as those in any of Embodiments 1 to 11, and the configurations that are the same as those of the above-described embodiments are denoted by the same reference numerals.
In Embodiment 12, the gas header 9 is divided into a plurality of gas header portions in the up and down direction. In
1 compressor 2 four-way valve 3 indoor heat exchanger 4 expansion valve 5 first gas-liquid separator 6 shunt 6a main body unit
6
b connection pipe 7 liquid header 7a to 7c liquid header portion 8 outdoor heat exchanger 8a outdoor heat exchanger 9 gas header 9a,9b gas header portion 10 bypass 10a first bypass pipe 11 flow rate control mechanism 12 fan 13 casing 14 orifice 15 heat transfer tube 16 fin
20 controller 21 first connection pipe 21a to 21c branch pipe 22 second connection pipe 22a to 22c branch pipe 23 second bypass pipe 24 third bypass pipe 25 liquid side outlet pipe 26 gas side outlet pipe 31 discharge pipe 32 refrigerant pipe 33,34 short circuit pipe 35 flow channel switching circuit 36 suction pipe 37 refrigerant pipe 40 (40a to 40c) intermediate heat exchanger 41 (41a to 41c) relay unit side refrigerant circuit 42 (42a to 42c) indoor unit side refrigerant circuit 43a to 43c pump 44 accumulator 45 (45a,45b) branch pipe 46 (46a,46b) refrigerant outlet pipe 50 second gas-liquid separator 60 first heat exchanger 70 second heat exchanger 85 third flow rate control device 90 second flow rate control device 100 outdoor unit 101 outdoor unit 102 relay unit 103 (103a to 103c) indoor unit 104 switching unit 105 second branch portion
110
a to 110c first flow rate control device 120a to 120c solenoid valve
130
a to 130c solenoid valve 140 third gas-liquid separator 150 gas side bypass resistance 160 to 190 check valve 200 indoor unit 300 air-conditioning apparatus 1000a to 1000c indoor heat exchanger 10000 multi-split type air-conditioning apparatus.
| Number | Date | Country | Kind |
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| JP2014-102954 | May 2014 | JP | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/JP2015/059095 | 3/25/2015 | WO | 00 |
| Publishing Document | Publishing Date | Country | Kind |
|---|---|---|---|
| WO2015/178097 | 11/26/2015 | WO | A |
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