This U.S. National stage application claims priority under 35 U.S.C. §119(a) to Japanese Patent Application Nos. 2006-246155 and 2007-053351, filed in Japan on Sep. 11, 2006, Mar. 2, 2007, respectively, the entire contents of which are hereby incorporated herein by reference.
The present invention relates to a refrigeration device, and particularly relates to a refrigeration device in which the refrigerant attains a supercritical state during the refrigeration cycle.
Conventional refrigeration devices are widely known that are provided with a refrigerant circuit in which a compressor; a radiator configured to release heat from the refrigerant discharged from the compressor; a first expansion valve configured to reduce the pressure of the refrigerant that flows out from the radiator; a liquid receiver configured to store a portion of the refrigerant that flows out from the first expansion valve; a second expansion valve configured to reduce the pressure of the refrigerant that flows out from the liquid receiver; an evaporator configured to evaporate the refrigerant that flow out from the second expansion valve; and an internal heat exchanger for exchanging heat between the refrigerant that flows in a refrigerant pipe for connecting the exit side of the radiator and the refrigerant inflow side of the first expansion valve, and the refrigerant that flows in a refrigerant pipe for connecting the exit side of the evaporator and the refrigerant intake side of the compressor, are connected in sequence (see Japanese Laid-open Patent Application No. 2002-228282 (FIG. 10), for example).
However, when an internal heat exchanger is merely provided to the refrigerant inflow side of the first expansion valve in the manner described above, not only is it difficult to impart an adequate degree of subcooling to the refrigerant that has passed through the first expansion valve, but there is also a risk of the refrigerant sucked into the compressor becoming overly superheated.
An object of the present invention is to make it possible to impart an adequate degree of subcooling to the refrigerant that has passed through the first expansion mechanism, and to maintain the proper degree of superheating of the refrigerant sucked into the compressor in a refrigeration device such as the one described above.
A refrigeration device according to a first aspect of the present invention comprises a compression mechanism, a radiator, a first expansion mechanism, a second expansion mechanism, an evaporator, a first internal heat exchanger, a branch pipe, a third expansion mechanism, and a second internal heat exchanger. The compression mechanism configured to compress a refrigerant. The radiator is connected to a refrigerant discharge side of the compression mechanism. The first expansion mechanism is connected to an exit side of the radiator. The second expansion mechanism is connected to a refrigerant outflow side of the first expansion mechanism. The evaporator is connected to a refrigerant outflow side of the second expansion mechanism, and to a refrigerant intake side the compression mechanism. The first internal heat exchanger causes heat to be exchanged between refrigerant that flows in a first refrigerant pipe for connecting the exit side of the radiator and an inflow side of the first expansion mechanism, and refrigerant that flows in a second refrigerant pipe for connecting the exit side of the evaporator and the refrigerant inflow side of the compression mechanism. The branch pipe branches from a third refrigerant pipe for connecting the exit side of the radiator and the refrigerant inflow side of the second expansion mechanism, and merges with the second refrigerant pipe. The third expansion mechanism is provided to the branch pipe. The second internal heat exchanger causes heat to be exchanged between refrigerant that flows out from the first expansion mechanism and refrigerant that flows out from the third expansion mechanism.
In this refrigeration device, the branch pipe that branches from a third refrigerant pipe for connecting the exit side of the radiator and the refrigerant inflow side of the second expansion mechanism merges with the second refrigerant pipe for connecting the exit side of the evaporator and the refrigerant inflow side of the compression mechanism, and the third expansion mechanism is provided to the branch pipe. The proper degree of superheating of the refrigerant sucked into the compression mechanism can therefore be maintained in this refrigeration device. In the second internal heat exchanger in this refrigeration device, heat is exchanged between the refrigerant that flows out from the first expansion mechanism and the refrigerant that flows out from the third expansion mechanism. It is therefore possible in this refrigeration device to impart an adequate degree of subcooling to the refrigerant that has passed through the first expansion mechanism.
A refrigeration device according to a second aspect of the present invention is the refrigeration device according to the first aspect of the present invention, wherein the branch pipe branches from a fourth refrigerant pipe for connecting the refrigerant outflow side of the first expansion mechanism and the refrigerant inflow side of the second expansion mechanism and merging with the second refrigerant pipe.
In this refrigeration device, the branch pipe that branches from the fourth refrigerant pipe for connecting the refrigerant outflow side of the first expansion mechanism and the refrigerant inflow side of the second expansion mechanism merges with the second refrigerant pipe for connecting the exit side of the evaporator and the refrigerant intake side of the compression mechanism, and the third expansion mechanism is provided to the branch pipe. A more adequate degree of subcooling can therefore be imparted to the refrigerant that has passed through the first expansion mechanism in this refrigeration device.
A refrigeration device according to a third aspect of the present invention is the refrigeration device according to the first or second aspect of the present invention, wherein the branch pipe merges with the second refrigerant pipe so that refrigerant that flows out from the third expansion mechanism and undergoes heat exchange in the second internal heat exchanger merges with refrigerant that flows through the second refrigerant pipe before the refrigerant flows into the first internal heat exchanger.
In this refrigeration device, the branch pipe merges with the second refrigerant pipe so that refrigerant that flows out from the third expansion mechanism and undergoes heat exchange in the second internal heat exchanger merges with refrigerant that flows through the second refrigerant pipe before the refrigerant flows into the first internal heat exchanger. The capability of the first internal heat exchanger can therefore be adjusted in this refrigeration device.
A refrigeration device according to a fourth aspect of the present invention is the refrigeration device according to the first or second aspect of the present invention, wherein the branch pipe merges with the second refrigerant pipe so that refrigerant that flows out from the third expansion mechanism and undergoes heat exchange in the second internal heat exchanger merges with refrigerant that flows through the second refrigerant pipe after the refrigerant has passed through the first internal heat exchanger.
In this refrigeration device, the branch pipe merges with the second refrigerant pipe so that refrigerant that flows out from the third expansion mechanism and undergoes heat exchange in the second internal heat exchanger merges with refrigerant that flows through the second refrigerant pipe after the refrigerant has passed through the first internal heat exchanger. The proper degree of superheating of the refrigerant sucked into the compression mechanism can therefore be maintained in this refrigeration device by merging the refrigerant placed in a damp state by the third expansion mechanism with the refrigerant sucked into the compression mechanism in a case in which the degree of superheating of the refrigerant sucked into the compression mechanism is extremely high, for example.
A refrigeration device according to a fifth aspect of the present invention is the refrigeration device according to the first or second aspects of the present invention, wherein the branch pipe merges with the second refrigerant pipe connected to an entry side of the first internal heat exchanger.
In this refrigeration device, the branch pipe merges with the second refrigerant pipe connected to the entry side of the first internal heat exchanger. The capability of the first internal heat exchanger can therefore be adjusted in this refrigeration device.
A refrigeration device according to a sixth aspect of the present invention is the refrigeration device according to the first or second aspects of the present invention, wherein the branch pipe merges with the second refrigerant pipe connected to an exit side of the first internal heat exchanger.
In this refrigeration device, the branch pipe merges with the second refrigerant pipe connected to the exit side of the first internal heat exchanger. The proper degree of superheating of the refrigerant sucked into the compression mechanism can therefore be maintained in this refrigeration device by merging the refrigerant placed in a damp state by the third expansion mechanism with the refrigerant sucked into the compression mechanism in a case in which the degree of superheating of the refrigerant sucked into the compression mechanism is extremely high, for example.
A refrigeration device according to a seventh aspect of the present invention is the refrigeration device according to any of the first through sixth aspects of the present invention, further comprising a first control unit. The first control unit controls the third expansion mechanism so that the degree of superheating of the refrigerant that flows to the refrigerant intake side of the compression mechanism from a merging point of the branch pipe and the second refrigerant pipe is within a predetermined range.
In this refrigeration device, the first control unit controls the third expansion mechanism so that the degree of superheating of the refrigerant that flows to the refrigerant intake side of the compression mechanism from a merging point of the branch pipe and the second refrigerant pipe is within a predetermined range. The proper degree of superheating of the refrigerant sucked into the compression mechanism can therefore be maintained in this refrigeration device.
A refrigeration device according to an eighth aspect of the present invention is the refrigeration device according to any of the first through seventh aspects of the present invention, further comprising a liquid receiver and a second control unit. The liquid receiver is provided between the refrigerant outflow side of the first expansion mechanism and an inflow port for refrigerant that flows through the first refrigerant pipe of the second internal heat exchanger. The second control unit performs refrigerant cooling control for cooling the refrigerant that flows through the first refrigerant pipe by the first internal heat exchanger so that the refrigerant that has flowed out from the first expansion mechanism does not reach a state near the critical point.
When the refrigerant is expanded by the first expansion mechanism to a state near the saturation line in a case in which the liquid receiver is thus provided between the refrigerant outflow side of the first expansion mechanism and an inflow port for refrigerant that flows through the first refrigerant pipe of the second internal heat exchanger, the refrigerant sometimes reaches a state near the critical point, depending on the installation environment (e.g., a case such as overload during summer). When the refrigerant reaches a state near the critical point in this manner, not only is there a risk of cavitation and adverse effects on the constituent parts of the refrigerant circuit, but the fluid level of the refrigerant in the liquid receiver becomes difficult to control, and it can become impossible to maintain an appropriate amount of refrigerant in the refrigerant circuit.
However, in this refrigeration device, the second control unit performs refrigerant cooling control for cooling the refrigerant that flows through the first refrigerant pipe by the first internal heat exchanger so that the refrigerant that has flowed out from the first expansion mechanism does not reach a state near the critical point. The refrigerant can therefore be prevented from reaching a state near the critical point when the refrigerant is expanded by the first expansion mechanism to a state near the saturation line in this refrigeration device.
A refrigeration device according to a ninth aspect of the present invention is the refrigeration device according to the eighth aspect of the present invention, wherein the first expansion mechanism and the second expansion mechanism are controlled in the refrigerant cooling control so that the refrigerant that has flowed out from the first expansion mechanism does not reach a state near the critical point.
In this refrigeration device, the first expansion mechanism and the second expansion mechanism are controlled in the refrigerant cooling control so that the refrigerant that has flowed out from the first expansion mechanism does not reach a state near the critical point. The refrigerant can therefore be prevented from reaching a state near the critical point when the refrigerant is expanded by the first expansion mechanism to a state near the saturation line in this refrigeration device.
A refrigeration device according to a tenth aspect of the present invention is the refrigeration device according to the eighth or ninth aspect of the present invention, wherein the refrigerant that flows through the first refrigerant pipe is cooled by the first internal heat exchanger in the refrigerant cooling control so that the pressure of the refrigerant that has flowed out from the first expansion mechanism is equal to or lower than the pressure of {critical pressure (MPa)−0.3 MPa}.
In this refrigeration device, the refrigerant that flows through the first refrigerant pipe is cooled by the first internal heat exchanger in the refrigerant cooling control so that the pressure of the refrigerant that has flowed out from the first expansion mechanism is equal to or lower than the pressure of {critical pressure (MPa)−0.3 MPa}. The refrigerant can therefore be prevented from reaching a state near the critical point when the refrigerant is expanded by the first expansion mechanism to a state near the saturation line in this refrigeration device.
A refrigeration device according to an eleventh aspect of the present invention is the refrigeration device according to the tenth aspect of the present invention, further comprising a temperature detector. The temperature detector is provided in the vicinity of an exit of the radiator or in the vicinity of a refrigerant inflow port of the first expansion mechanism. The refrigerant that flows through the first refrigerant pipe is cooled by the first internal heat exchanger in the refrigerant cooling control so that the pressure of the refrigerant that has flowed out from the first expansion mechanism is equal to or lower than the pressure of {critical pressure (MPa)−0.3 MPa} when the temperature detected by the temperature detector is equal to or above a predetermined temperature.
In this refrigeration device, the refrigerant that flows through the first refrigerant pipe is cooled by the first internal heat exchanger in the refrigerant cooling control so that the pressure of the refrigerant that has flowed out from the first expansion mechanism is equal to or lower than the pressure of {critical pressure (MPa)−0.3 MPa} when the temperature detected by the temperature detector is equal to or above a predetermined temperature. It is therefore possible in this refrigeration device to prevent the refrigerant from reaching a state near the critical point when the refrigerant is expanded by the first expansion mechanism to a state near the saturation line and there is a risk of the refrigerant reaching a state near the critical point.
A refrigeration device according to a twelfth aspect of the present invention is the refrigeration device according to any of the eighth through eleventh aspects of the present invention, wherein the second control unit has control switching section (means). The control switching means switches between normal control and the refrigerant cooling control. The term “normal control” refers to control that gives priority to COP, for example, and other control. The control switching means switches between the refrigerant cooling control and the normal control.
In this refrigeration device, the control switching means switches between the refrigerant cooling control and the normal control. It is therefore possible to execute control that takes COP into account in the refrigeration device.
In the refrigeration device according to the first aspect, the proper degree of superheating of the refrigerant sucked into the compression mechanism can be maintained, and it is possible to impart an adequate degree of subcooling to the refrigerant that has passed through the first expansion mechanism.
In the refrigeration device according to the second aspect, a more adequate degree of subcooling can be imparted to the refrigerant that has passed through the first expansion mechanism.
In the refrigeration device according to the third aspect, the capability of the first internal heat exchanger can be adjusted.
In the refrigeration device according to the fourth aspect, the proper degree of superheating of the refrigerant sucked into the compression mechanism can be maintained by merging the refrigerant placed in a damp state by the third expansion mechanism with the refrigerant sucked into the compression mechanism in a case in which the degree of superheating of the refrigerant sucked into the compression mechanism is extremely high, for example.
In the refrigeration device according to the fifth aspect, the capability of the first internal heat exchanger can be adjusted.
In the refrigeration device according to the sixth aspect, the proper degree of superheating of the refrigerant sucked into the compression mechanism can be maintained by merging the refrigerant placed in a damp state by the third expansion mechanism with the refrigerant sucked into the compression mechanism in a case in which the degree of superheating of the refrigerant sucked into the compression mechanism is extremely high, for example.
In the refrigeration device according to the seventh aspect, the proper degree of superheating of the refrigerant sucked into the compression mechanism can be maintained in this refrigeration device.
In the refrigeration device according to the eighth aspect, the refrigerant can be prevented from reaching a state near the critical point when the refrigerant is expanded by the first expansion mechanism to a state near the saturation line.
In the refrigeration device according to the ninth aspect, the refrigerant can be prevented from reaching a state near the critical point when the refrigerant is expanded by the first expansion mechanism to a state near the saturation line.
In the refrigeration device according to the tenth aspect, the refrigerant can be prevented from reaching a state near the critical point when the refrigerant is expanded by the first expansion mechanism to a state near the saturation line.
In the refrigeration device according to the eleventh aspect, the refrigerant can be prevented from reaching a state near the critical point when the refrigerant is expanded by the first expansion mechanism to a state near the saturation line and there is a risk of the refrigerant reaching a state near the critical point.
In the refrigeration device according to the twelfth aspect, it is possible to execute control that takes COP into account.
<Structure of Air Conditioning Device>
This air conditioning device 1 is an air conditioning device that is capable of cooling operation and heating operation using carbon dioxide as the refrigerant, and is primarily composed of a refrigerant circuit 2, blower fans 23, 32, a control device 27, a high-pressure sensor 24, an intermediate-pressure sensor 26, a first temperature sensor 25, a second temperature sensor 29, and other components.
The refrigerant circuit 2 is composed primarily of a main refrigerant circuit 3, a first bypass line 4, a gas outlet line 5, an oil return line 6, and a second bypass line 7. Each circuit will be described in detail below.
(1) Main Refrigerant Circuit
The main refrigerant circuit 3 is equipped primarily with a compressor 11, an oil separator 12, a four-way switch valve 13, an outdoor heat exchanger 14, a first internal heat exchanger 15, a first electric expansion valve 16, a liquid receiver 17, a second internal heat exchanger 18, a second electric expansion valve 20, and an indoor heat exchanger 31, and the devices are connected via a refrigerant pipe as shown in
(2) Bypass Lines
As shown in
(3) Gas Outlet Line
The gas outlet line 5 is a line that extends from the upper part of the liquid receiver 17 and merges with a refrigerant pipe (hereinafter referred to as the thirteenth refrigerant pipe) for connecting the first internal heat exchanger 15 and the intake side of the compressor 11. An opening and closing valve 51 is provided to the gas outlet line 5. The opening and closing valve 51 is an electromagnetic valve or the like, for example, and the opening and closing thereof is controlled by the control device 27 described hereinafter.
(4) Oil Return Line
The oil return line 6 is a line that extends from the oil separator 12 and merges with an intake tube of the compressor 11. A capillary 28 is provided to the oil return line 6.
(5) Second Bypass Line
The second bypass line 7 is a line that branches from a refrigerant pipe for connecting the oil separator 12 and the four-way switch valve 13 and merges with a portion of the thirteenth refrigerant pipe that is between the first internal heat exchanger 15 and the merge point of the gas outlet line 5. An opening and closing valve 52 is provided to the second bypass line 7. The opening and closing valve 52 is an electromagnetic valve or the like, for example, and the opening and closing thereof is controlled by the control device 27 described hereinafter. This opening and closing valve is used for superheating the refrigerant flowing through the intake side of the compressor, and injecting high-pressure refrigerant gas to protect the low-pressure side when the pressure of the low-pressure side is too low at startup of the compressor.
In the present embodiment, the air conditioning device 1 is a separate-type air conditioning device, and can also be described as comprising an indoor unit 30, an outdoor unit 10, a first connecting pipe 41 for connecting the pipe for refrigerant fluid and the like of the indoor unit 30 and the pipe for refrigerant fluid and the like of the outdoor unit 10, and a second connecting pipe 42 for connecting the pipe for refrigerant gas and the like of the indoor unit 30 and the pipe for refrigerant gas and the like of the outdoor unit 10. The first connecting pipe 41 and the pipe for refrigerant fluid and the like of the outdoor unit 10 are connected via a first close valve 21 of the outdoor unit 10, and the second connecting pipe 42 and the pipe for refrigerant gas and the like of the outdoor unit 10 are connected via a second close valve 22 of the outdoor unit 10. The indoor unit 30 is mainly provided with the indoor heat exchanger 31 and the indoor fan 32 in the present embodiment. The outdoor unit 10 is primarily provided with the compressor 11, the oil separator 12, the four-way switch valve 13, the outdoor heat exchanger 14, the first internal heat exchanger 15, the first electric expansion valve 16, the liquid receiver 17, the second internal heat exchanger 18, the second electric expansion valve 20, the third electric expansion valve 19, the opening and closing valves 51, 52, the capillary 28, the high-pressure sensor 24, the intermediate-pressure sensor 26, the first temperature sensor 25, the second temperature sensor 29, the control device 27, and an outdoor fan 23.
(1) Indoor Unit
The indoor unit 30 primarily has the indoor heat exchanger 31, the indoor fan 32, and other components.
The indoor heat exchanger 31 is a heat exchanger for exchanging heat between the refrigerant and the indoor air, which is the air inside the room to be air-conditioned.
The indoor fan 32 is a fan for taking the air inside the air-conditioned room into the unit 30 and blowing conditioned air, which is the air after heat exchange with the refrigerant via the indoor heat exchanger 31, back into the air-conditioned room.
Employing such a configuration makes it possible for the indoor unit 30 to cause heat to be exchanged between the indoor air taken in by the indoor fan 32 and the liquid refrigerant that flows through the indoor heat exchanger 31, and generate conditioned air (cool air) during cooling operation, as well as to cause heat to be exchanged between the indoor air taken in by the indoor fan 32 and supercritical refrigerant that flows through the indoor heat exchanger 31, and generate conditioned air (warm air) during heating operation.
(2) Outdoor Unit
The outdoor unit 10 primarily has the compressor 11, the oil separator 12, the four-way switch valve 13, the outdoor heat exchanger 14, the outdoor fan 23, the first internal heat exchanger 15, the first electric expansion valve 16, the liquid receiver 17, the second internal heat exchanger 18, the second electric expansion valve 20, the third electric expansion valve 19, the opening and closing valves 51, 52, the capillary 28, the high-pressure sensor 24, the intermediate-pressure sensor 26, the first temperature sensor 25, the second temperature sensor 29, the control device 27, and other components.
The compressor 11 is a device for sucking in low-pressure refrigerant gas flowing through an intake pipe and compressing the refrigerant gas to a supercritical state, and then discharging the refrigerant to a discharge pipe.
The oil separator 12 is a device for separating freezer oil that is mixed in with the refrigerant discharged from the compressor 11.
The four-way switch valve 13 is a valve for switching the flow direction of the refrigerant in accordance with each operation mode, and is capable of connecting the discharge side of the compressor 11 and the high-temperature side of the outdoor heat exchanger 14, and connecting the intake side of the compressor 11 and the gas side of the indoor heat exchanger 31 via the first internal heat exchanger 15 during cooling operation; as well as connecting the discharge side of the compressor 11 and the second close valve 22, and connecting the intake side of the compressor 11 and the gas side of the outdoor heat exchanger 14 during heating operation.
The outdoor heat exchanger 14 is capable of cooling the high-pressure supercritical refrigerant discharged from the compressor 11 using the air outside the air-conditioned room as a heat source during cooling operation, and evaporating the liquid refrigerant returning from the indoor heat exchanger 31 during heating operation.
The outdoor fan 23 is a fan for drawing outside air into the unit 10 and discharging the air after heat exchange with the refrigerant via the outdoor heat exchanger 14.
The first internal heat exchanger 15 is a heat exchanger formed by placing close to each other the refrigerant pipe (hereinafter referred to as the fourteenth refrigerant pipe) for connecting the first electric expansion valve 16 and the low-temperature side (or liquid side) of the outdoor heat exchanger 14, and the refrigerant pipe (hereinafter referred to as the fifteenth refrigerant pipe) for connecting the four-way switch valve 13 and the intake side of the compressor 11. In the internal heat exchanger 15, heat is exchanged between the high-temperature high-pressure supercritical refrigerant flowing through the fourteenth refrigerant pipe, and the low-temperature low-pressure refrigerant gas flowing through the fifteenth refrigerant pipe during cooling operation.
The first electric expansion valve 16 reduces the pressure of the supercritical refrigerant (during cooling operation) that flows out from the low-temperature side of the outdoor heat exchanger 14, or the liquid refrigerant (during heating operation) that flows in through the liquid receiver 17.
The liquid receiver 17 stores refrigerant that occurs as excess depending on the operating mode or the air conditioning load.
The second internal heat exchanger 18 is a heat exchanger formed by placing close to each other the refrigerant pipe (hereinafter referred to as the sixteenth refrigerant pipe) for connecting the liquid receiver 17 and the second electric expansion valve 20, and the first bypass line 4 (portion between the third electric expansion valve 19 and the merge point with the twelfth refrigerant pipe). In the second internal heat exchanger 18, heat is exchanged between the refrigerant in a saturated state flowing in the sixteenth refrigerant pipe, and the refrigerant flowing in the first bypass line 4.
The second electric expansion valve 20 reduces the pressure of the liquid refrigerant (during cooling operation) that flows out from the liquid receiver 17 and through the second internal heat exchanger 18, or the supercritical refrigerant (during heating operation) that flows out from the low-temperature side of the indoor heat exchanger 31.
The third electric expansion valve 19 reduces the pressure of the liquid refrigerant (during cooling operation) that flows out from the liquid receiver 17 and passes through the second internal heat exchanger 18.
The opening and closing of the opening and closing valves 51, 52 are controlled by the control device 27 as described above.
The capillary 28 reduces the pressure of oil-rich refrigerant that flows out from the oil separator 12 and evaporates the oil-rich refrigerant.
The high-pressure sensor 24 is provided to the discharge side of the compressor 11.
The intermediate-pressure sensor 26 is provided between the first electric expansion valve 16 and the liquid receiver 17.
The first temperature sensor 25 is provided in the vicinity of the low-temperature side (or liquid side) of the outdoor heat exchanger 14.
The second temperature sensor 29 is provided to the intake side of the compressor 11.
The control device 27 has a communication connection with the high-pressure sensor 24, the intermediate-pressure sensor 26, the first temperature sensor 25, the second temperature sensor 29, the first electric expansion valve 16, the second electric expansion valve 20, the third electric expansion valve 19, and other components, and controls the degree of opening of the first electric expansion valve 16 and the second electric expansion valve 20 on the basis of temperature information transmitted from the first temperature sensor 25, high-pressure information transmitted from the high-pressure sensor 24, and intermediate-pressure information transmitted from the intermediate-pressure sensor 26. The control device 27 also controls the degree of opening of the third electric expansion valve 19 so that the temperature information transmitted from the second temperature sensor 29 is within a predetermined range. The control device 27 is also provided with control switching functionality (i.e., control switching section or means) for switching between normal control and refrigerant cooling control on the basis of high-pressure information and the temperature information of the first temperature sensor 25 during cooling operation. In normal control, the degree of opening of the first electric expansion valve 16, the second electric expansion valve 20, and the third electric expansion valve 19 is controlled so that COP or the like is enhanced. In refrigerant cooling control, the degree of opening of the first electric expansion valve 16 and the second electric expansion valve 20 is controlled so that the state of the refrigerant that has flowed out from the first electric expansion valve 16 is on the saturation line and not near the critical point to maintain the state of the refrigerant in the liquid receiver 17 at saturation. The refrigerant cooling control will be described in detail using a Mollier diagram.
In the present embodiment, normal control is automatically performed when there is no need for refrigerant cooling control.
<Operation of the Air Conditioning Device>
The operation of the air conditioning device 1 will be described using
(1) Cooling Operation
During cooling operation, the four-way switch valve 13 is in the state indicated by the solid line in
When the compressor 11 is activated in this state of the refrigerant circuit 2, the refrigerant gas is sucked into the compressor 11 and compressed to a supercritical state, and then sent through the oil separator 12 and the four-way switch valve 13 to the outdoor heat exchanger 14 and cooled in the outdoor heat exchanger 14. At this time, freezer oil that is mixed in with the refrigerant is separated by the oil separator 12. The separated freezer oil is then taken back into the compressor 11 through the oil return line 6.
The cooled supercritical refrigerant is sent to the first electric expansion valve 16 through the first internal heat exchanger 15. At this time, the supercritical refrigerant is cooled by the low-temperature refrigerant gas that flows in the fifteenth refrigerant pipe of the first internal heat exchanger 15. The supercritical refrigerant sent to the first electric expansion valve 16 is depressurized to a saturated state, and then sent to the third electric expansion valve 19 as well as to the second electric expansion valve 20 via the liquid receiver 17 and the second internal heat exchanger 18. At this time, the refrigerant in a saturated state sent to the second electric expansion valve 20 is cooled by the refrigerant depressurized by the third electric expansion valve 19 and flowing into the first bypass line 4. The refrigerant in a saturated state sent to the second electric expansion valve 20 is depressurized to liquid refrigerant, and then fed to the indoor heat exchanger 31 via the first close valve 21, and the liquid refrigerant cools the indoor air and evaporates into refrigerant gas.
The refrigerant gas passes through the second close valve 22 and the four-way switch valve 13, merges with the refrigerant that has then been depressurized by the third electric expansion valve 19 and that has flowed into the first bypass line 4, and flows into the first internal heat exchanger 15. This merged refrigerant is then heated by the high-temperature high-pressure supercritical refrigerant that flows to the fourteenth refrigerant pipe of the first internal heat exchanger 15, and is then sucked back into the compressor 11.
Cooling operation is performed in this manner. The control device 27 at this time appropriately switches between normal control and refrigerant cooling control on the basis of temperature information and high-pressure information in the manner described above.
(2) Heating Operation
During heating operation, the four-way switch valve 13 is in the state indicated by the dashed line in
When the compressor 11 is activated in this state of the refrigerant circuit 2, the refrigerant gas is sucked into the compressor 11 and compressed to a supercritical state, and then is fed to the indoor heat exchanger 31 via the oil separator 12, the four-way switch valve 13, and the second close valve 22. At this time, freezer oil that is mixed in with the refrigerant is separated by the oil separator 12. The separated freezer oil is then taken back into the compressor 11 through the oil return line 6.
The supercritical refrigerant heats the indoor air, and is cooled in the indoor heat exchanger 31. The cooled supercritical refrigerant is sent through the first close valve 21 to the second electric expansion valve 20. Since the third electric expansion valve 19 is closed at this time, the supercritical refrigerant does not flow into the first bypass line 4. The supercritical refrigerant sent to the second electric expansion valve 20 is depressurized to a saturated state, and then sent to the first electric expansion valve 16 via the liquid receiver 17. The refrigerant in a saturated state sent to the first electric expansion valve 16 is depressurized to liquid refrigerant, and then sent to the outdoor heat exchanger 14 and evaporated to refrigerant gas in the outdoor heat exchanger 14. This refrigerant gas is again sucked into the compressor 11 via the four-way switch valve 13.
Heating operation is performed in this manner.
<Characteristics of the Air Conditioning Device>
(1)
During cooling operation in the air conditioning device 1 according to the present embodiment, heat is exchanged in the second internal heat exchanger 18 between the refrigerant that flows out from the first electric expansion valve 16, and the refrigerant that flows out from the third electric expansion valve 19. An adequate degree of subcooling can therefore be imparted to the refrigerant that has passed through the first electric expansion valve 16 in this air conditioning device 1.
(2)
In the air conditioning device 1 according to the present embodiment, the first bypass line 4 that branches from the eleventh refrigerant pipe and merges with the twelfth refrigerant pipe passes through the second internal heat exchanger 18. In this first bypass line 4, the third electric expansion valve 19 is provided in the portion that extends from the branch point with the eleventh refrigerant pipe to the second internal heat exchanger 18. The capability of the first internal heat exchanger 15 can therefore be adjusted to maintain the proper degree of superheating in the refrigerant sucked into the compressor 11 in the air conditioning device 1.
(3)
In the air conditioning device 1 according to the present embodiment, the first electric expansion valve 16 and the second electric expansion valve 20 are controlled so that the state of the refrigerant that has flowed out from the first electric expansion valve 16 is on the saturation line, and so that the pressure of the refrigerant at this time is equal to or lower than the pressure of {critical pressure (MPa)−0.3 (MPa)}. It is therefore possible to prevent the refrigerant from reaching a state near the critical point when the refrigerant is expanded to a state near the saturation line by the first electric expansion valve 16 in the air conditioning device 1.
(4)
In the air conditioning device 1 according to the present embodiment, the control device 27 is provided with functionality for switching between refrigerant cooling control and normal control. It is therefore possible to execute control that takes COP into account in the air conditioning device 1.
<Modifications>
(A)
In the embodiment described above, the invention of the present application is applied to a separate-type air conditioning device 1 in which one indoor unit 30 is provided for one outdoor unit 10, but the invention of the present application may also be applied to a multi-type air conditioning device 101 in which a plurality of indoor units is provided for one outdoor unit, such as shown in
(B)
A first internal heat exchanger 15 in which the fourteenth refrigerant pipe and the fifteenth refrigerant pipe are placed close to each other is used in the air conditioning device 1 according to the embodiment described above, but a dual-pipe heat exchanger may also be used as the first internal heat exchanger.
(C)
A second internal heat exchanger 18 in which the sixteenth refrigerant pipe and the first bypass line 4 are placed close to each other is used in the air conditioning device 1 according to the embodiment described above, but a dual-pipe heat exchanger may also be used as the second internal heat exchanger.
(D)
In the air conditioning device 1 according to the embodiment described above, the first bypass line 4 merges with the twelfth refrigerant pipe, but a configuration may instead be adopted in which the first bypass line 4 merges with a refrigerant pipe for connecting the first internal heat exchanger 15 and the intake side of the compressor 11, as shown in
In
(E)
The high-pressure sensor 24 is provided to the discharge side of the compressor 11 in the air conditioning device 1 according to the embodiment described above, but the high-pressure sensor 24 may also be omitted. In this case, the degree of opening of the first electric expansion valve 16, the second electric expansion valve 20, and the third electric expansion valve 19 may be controlled so that the state of the refrigerant that has flowed out from the first electric expansion valve 16 is on the saturation line, and so that the pressure of the refrigerant is then equal to or lower than the pressure of {critical pressure (MPa)−0.3 (MPa)} when the temperature obtained from the first temperature sensor 25 positioned on the low-temperature side (or liquid side) of the outdoor heat exchanger 14 is equal to or above a predetermined temperature.
(F)
In the air conditioning device 1 according to the embodiment described above, the first internal heat exchanger 15, the second internal heat exchanger 18, the first electric expansion valve 16, the liquid receiver 17, the second electric expansion valve 20, and other components are disposed in the outdoor unit 10, but the positioning of these components is not particularly limited. For example, the second electric expansion valve 20 may be disposed in the indoor unit 30.
(G)
An electric expansion valve is used as the means for reducing the pressure of the refrigerant in the air conditioning device 1 according to the embodiment described above, but an expansion device 116 or the like such as shown in
(H)
The temperature sensor 25 is provided in the vicinity of the port on the low-temperature side (or liquid side) of the outdoor heat exchanger 14 in the air conditioning device 1 according to the embodiment described above, but the temperature sensor 25 may alternatively be provided in the vicinity of the port on the first internal heat exchanger side of the first electric expansion valve 16.
(I)
In the air conditioning device 1 according to the embodiment described above, the first bypass line 4 branches from a refrigerant pipe for connecting the second internal heat exchanger 18 and the second electric expansion valve 20, but the first bypass line may alternatively branch from a refrigerant pipe for connecting the outdoor heat exchanger 14 and the first internal heat exchanger 15, as shown in
(J)
In the air conditioning device 1 according to the embodiment described above, the first bypass line 4 branches from a refrigerant pipe for connecting the second internal heat exchanger 18 and the second electric expansion valve 20, but the first bypass line may alternatively branch from a refrigerant pipe for connecting the first internal heat exchanger 15 and the first electric expansion valve 16, as shown in
(K)
In the air conditioning device 1 according to the embodiment described above, the first bypass line 4 branches from a refrigerant pipe for connecting the second internal heat exchanger 18 and the second electric expansion valve 20, but the first bypass line may alternatively branch from a refrigerant pipe for connecting the first electric expansion valve 16 and the second internal heat exchanger 18 (not shown). In this case, the branch point may be positioned in front of or behind the liquid receiver 17.
The refrigeration device of the present invention has the characteristic of making it possible to impart an adequate degree of subcooling to the refrigerant that has passed through the first expansion mechanism, and the present invention is particularly useful in a refrigeration device in which carbon dioxide or the like is used as the refrigerant.
Number | Date | Country | Kind |
---|---|---|---|
2006-246155 | Sep 2006 | JP | national |
2007-053351 | Mar 2007 | JP | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
---|---|---|---|---|
PCT/JP2007/067470 | 9/7/2007 | WO | 00 | 3/5/2009 |
Publishing Document | Publishing Date | Country | Kind |
---|---|---|---|
WO2008/032645 | 3/20/2008 | WO | A |
Number | Name | Date | Kind |
---|---|---|---|
20060080989 | Aoki et al. | Apr 2006 | A1 |
20090013700 | Unezaki et al. | Jan 2009 | A1 |
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Number | Date | Country | |
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20100180612 A1 | Jul 2010 | US |