WO2014199788A1 - Air-conditioning device - Google Patents
Air-conditioning device Download PDFInfo
- Publication number
- WO2014199788A1 WO2014199788A1 PCT/JP2014/063289 JP2014063289W WO2014199788A1 WO 2014199788 A1 WO2014199788 A1 WO 2014199788A1 JP 2014063289 W JP2014063289 W JP 2014063289W WO 2014199788 A1 WO2014199788 A1 WO 2014199788A1
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- WO
- WIPO (PCT)
- Prior art keywords
- refrigerant
- expansion valve
- heat exchanger
- compressor
- pressure
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B13/00—Compression machines, plants or systems, with reversible cycle
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B41/00—Fluid-circulation arrangements
- F25B41/30—Expansion means; Dispositions thereof
- F25B41/39—Dispositions with two or more expansion means arranged in series, i.e. multi-stage expansion, on a refrigerant line leading to the same evaporator
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2313/00—Compression machines, plants or systems with reversible cycle not otherwise provided for
- F25B2313/027—Compression machines, plants or systems with reversible cycle not otherwise provided for characterised by the reversing means
- F25B2313/02741—Compression machines, plants or systems with reversible cycle not otherwise provided for characterised by the reversing means using one four-way valve
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2313/00—Compression machines, plants or systems with reversible cycle not otherwise provided for
- F25B2313/029—Control issues
- F25B2313/0294—Control issues related to the outdoor fan, e.g. controlling speed
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2313/00—Compression machines, plants or systems with reversible cycle not otherwise provided for
- F25B2313/031—Sensor arrangements
- F25B2313/0314—Temperature sensors near the indoor heat exchanger
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2313/00—Compression machines, plants or systems with reversible cycle not otherwise provided for
- F25B2313/031—Sensor arrangements
- F25B2313/0315—Temperature sensors near the outdoor heat exchanger
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2600/00—Control issues
- F25B2600/02—Compressor control
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2600/00—Control issues
- F25B2600/25—Control of valves
- F25B2600/2513—Expansion valves
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2700/00—Sensing or detecting of parameters; Sensors therefor
- F25B2700/21—Temperatures
- F25B2700/2106—Temperatures of fresh outdoor air
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2700/00—Sensing or detecting of parameters; Sensors therefor
- F25B2700/21—Temperatures
- F25B2700/2115—Temperatures of a compressor or the drive means therefor
- F25B2700/21151—Temperatures of a compressor or the drive means therefor at the suction side of the compressor
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2700/00—Sensing or detecting of parameters; Sensors therefor
- F25B2700/21—Temperatures
- F25B2700/2115—Temperatures of a compressor or the drive means therefor
- F25B2700/21152—Temperatures of a compressor or the drive means therefor at the discharge side of the compressor
Definitions
- the present invention relates to an air conditioner, and more particularly, an air conditioner that circulates a refrigerant while expanding a high-pressure refrigerant discharged from a compressor by an upstream expansion valve and a downstream expansion valve in two stages in the order of intermediate pressure and low pressure.
- an air conditioner that circulates a refrigerant while expanding a high-pressure refrigerant discharged from a compressor by an upstream expansion valve and a downstream expansion valve in two stages in the order of intermediate pressure and low pressure.
- Patent Document 1 Japanese Patent Laid-Open No. 10-132393
- high-pressure refrigerant discharged from a compressor by an upstream expansion valve and a downstream expansion valve is expanded in two stages in the order of intermediate pressure and low pressure.
- an air conditioner having a refrigerant circuit that circulates a refrigerant while allowing the refrigerant to circulate.
- the refrigerant circuit of the air conditioner is configured by connecting a compressor, an outdoor heat exchanger, two expansion valves, and an indoor heat exchanger.
- Patent Document 2 Japanese Patent Laid-Open No. 2003-106683
- an air conditioner that performs feedforward control in which the opening degree of the expansion valve is changed based on such a predicted value.
- An object of the present invention is to enable feed-forward control of two expansion valves without providing a sensor for detecting an intermediate pressure in an air conditioner having a refrigerant circuit with two-stage expansion. is there.
- An air conditioner is configured by connecting a compressor, an outdoor heat exchanger, an upstream expansion valve, a downstream expansion valve, and an indoor heat exchanger, and includes an upstream expansion valve and a downstream side.
- a refrigerant circuit that circulates the refrigerant while expanding the high-pressure refrigerant discharged from the compressor by an expansion valve in two steps in the order of intermediate pressure and low pressure, and outdoor air that serves as a cooling source or heating source is supplied to the outdoor heat exchanger It is an air conditioner having an outdoor fan.
- the operating capacity of the compressor and / or the outdoor under the prediction condition based on the correlation between the high pressure side pressure difference obtained by subtracting the intermediate pressure from the high pressure and the low pressure side pressure difference obtained by subtracting the low pressure from the intermediate pressure.
- Predicting changes in the amount of refrigerant circulating through the upstream and downstream expansion valves after changing the fan operating capacity change the operating capacity of the compressor and / or the outdoor fan.
- control is performed to change the opening degree of the upstream side expansion valve and the downstream side expansion valve in consideration of the predicted change in the refrigerant circulation amount.
- the operating capacity of the compressor or outdoor fan is changed under a prediction condition based on the correlation between the high pressure side pressure difference and the low pressure side pressure difference.
- the change of the refrigerant circulation amount passing through the upstream side expansion valve and the downstream side expansion valve after being made is predicted.
- the air conditioner according to the second aspect is the air conditioner according to the first aspect, wherein the correlation is before and after the operating capacity of the compressor and / or the operating capacity of the outdoor fan is changed.
- the relationship between the pressure difference and the low pressure side pressure difference is constant.
- the air conditioner according to the third aspect is the air conditioner according to the first aspect, wherein the correlation is before and after the operating capacity of the compressor and / or the operating capacity of the outdoor fan is changed.
- the relationship is that the pressure difference is constant.
- An air conditioner according to a fourth aspect is the air conditioner according to any one of the first to third aspects, wherein the upstream side expansion valve serves as a radiator radiator of the outdoor heat exchanger and the indoor heat exchanger.
- the opening degree is controlled so that the degree of subcooling of the refrigerant at the outlet of the functioning heat exchanger becomes a predetermined target degree of subcooling
- the downstream expansion valve is an evaporator of the refrigerant among the outdoor heat exchanger and the indoor heat exchanger.
- the degree of opening is controlled so that the degree of superheat of the refrigerant at the outlet of the heat exchanger that functions as a predetermined target superheat degree.
- the opening degree control of the upstream side expansion valve and the downstream side expansion valve feedback control based on the degree of supercooling and the degree of superheat is performed together with feedforward control. Therefore, here, when the operating capacities of the compressor and the outdoor fan change, the opening degree of the upstream expansion valve and the downstream expansion valve is adjusted by feedforward control after the operating capacities of the compressor and the outdoor fan change. Can be made to coincide with the optimum opening degree by feedback control after being brought close to the optimum opening degree in advance.
- the time required for feedback control of the upstream side expansion valve and the downstream side expansion valve can be effectively shortened. And when the operating capacity of a compressor or an outdoor fan changes, the control followability of the opening degree of an upstream side expansion valve and a downstream side expansion valve can be improved.
- FIG. 1 is a schematic configuration diagram of an air conditioner 1 according to an embodiment of the present invention.
- the air conditioner 1 is a device that can cool and heat a room such as a building by performing a vapor compression refrigeration cycle.
- the air conditioner 1 is mainly configured by connecting an outdoor unit 2 and an indoor unit 4.
- the outdoor unit 2 and the indoor unit 4 are connected via a liquid refrigerant communication tube 5 and a gas refrigerant communication tube 6.
- the vapor compression refrigerant circuit 10 of the air conditioner 1 is configured by connecting the outdoor unit 2 and the indoor unit 4 via the refrigerant communication pipes 5 and 6.
- Various refrigerants can be used as the refrigerant sealed in the refrigerant circuit 10, but here, R32, which is a kind of HFC refrigerant, is enclosed as the refrigerant.
- the indoor unit 4 is installed indoors and constitutes a part of the refrigerant circuit 10.
- the indoor unit 4 mainly has an indoor heat exchanger 41.
- the indoor heat exchanger 41 is a heat exchanger that functions as a refrigerant evaporator during cooling operation to cool room air, and functions as a refrigerant radiator during heating operation to heat indoor air.
- the liquid side of the indoor heat exchanger 41 is connected to the liquid refrigerant communication tube 5, and the gas side of the indoor heat exchanger 41 is connected to the gas refrigerant communication tube 6.
- the indoor unit 4 has an indoor fan 42 for sucking indoor air into the indoor unit 4 and exchanging heat with the refrigerant in the indoor heat exchanger 41 and supplying the indoor air as supply air.
- the indoor fan 42 is driven by an indoor fan motor 43.
- the indoor unit 4 is provided with various sensors. Specifically, the indoor heat exchanger 41 includes an indoor heat exchange liquid side temperature sensor 57 that detects the temperature Trrl of the refrigerant on the liquid side of the indoor heat exchanger 41, and the refrigerant in the intermediate portion of the indoor heat exchanger 41. An indoor heat exchanger intermediate temperature sensor 58 for detecting the temperature Trrm is provided. The indoor unit 4 is provided with an indoor temperature sensor 59 that detects the temperature Tra of the indoor air sucked into the indoor unit 4.
- the indoor unit 4 has an indoor side control unit 44 that controls the operation of each unit constituting the indoor unit 4.
- the indoor side control unit 44 includes a microcomputer, a memory, and the like provided for controlling the indoor unit 4, and exchanges control signals and the like with a remote controller (not shown). Control signals and the like can be exchanged with the outdoor unit 2 via the transmission line 8a.
- the outdoor unit 2 is installed outside and constitutes a part of the refrigerant circuit 10.
- the outdoor unit 2 mainly includes a compressor 21, a four-way switching valve 22, an outdoor heat exchanger 23, a first expansion valve 24, a receiver 25, a second expansion valve 26, and a liquid side closing valve 27. And a gas side closing valve 28.
- the compressor 21 is a device that compresses the low-pressure refrigerant in the refrigeration cycle until it reaches a high pressure.
- the compressor 21 has a hermetic structure in which a displacement type compression element (not shown) such as a rotary type or a scroll type is driven by a compressor motor 21a whose frequency is controlled by an inverter. Thereby, the compressor 21 is configured such that its operating capacity is variable.
- the compressor 21 has a suction pipe 31 connected to the suction side and a discharge pipe 32 connected to the discharge side.
- the suction pipe 31 is a refrigerant pipe that connects the suction side of the compressor 21 and the first port 22 a of the four-way switching valve 22.
- the suction pipe 31 is provided with an accumulator 29.
- the discharge pipe 32 is a refrigerant pipe that connects the discharge side of the compressor 21 and the second port 22 b of the four-way switching valve 22.
- the discharge pipe 32 is provided with a check valve 32a.
- the four-way switching valve 22 is a switching valve for switching the direction of refrigerant flow in the refrigerant circuit 10.
- the four-way switching valve 22 causes the outdoor heat exchanger 23 to function as a radiator for the refrigerant compressed in the compressor 21 and the indoor heat exchanger 41 for the refrigerant that has radiated heat in the outdoor heat exchanger 23.
- the discharge side of the compressor 21 (here, the discharge pipe 32) and the gas side of the outdoor heat exchanger 23 (here, the first gas refrigerant pipe 33) are connected (four-way switching valve in FIG. 1). (See 22 solid line).
- the suction side (here, the suction pipe 31) of the compressor 21 and the gas refrigerant communication pipe 6 side (here, the second gas refrigerant pipe 34) are connected (solid line of the four-way switching valve 22 in FIG. 1). See).
- the four-way switching valve 22 causes the outdoor heat exchanger 23 to function as an evaporator of the refrigerant that has radiated heat in the indoor heat exchanger 41 during the heating operation, and the indoor heat exchanger 41 is compressed in the compressor 21.
- the four-way switching valve 22 switches between the second port 22b and the fourth port 22d and the first port 22a and the third port 22c during the heating operation.
- the discharge side (here, the discharge pipe 32) of the compressor 21 and the gas refrigerant communication pipe 6 side (here, the second gas refrigerant pipe 34) are connected (of the four-way switching valve 22 in FIG. 1). (See dashed line).
- the suction side of the compressor 21 here, the suction pipe 31
- the gas side of the outdoor heat exchanger 23 here, the first gas refrigerant pipe 33
- the first gas refrigerant pipe 33 is a refrigerant pipe that connects the third port 22 c of the four-way switching valve 22 and the gas side of the outdoor heat exchanger 23.
- the second gas refrigerant pipe 33 is a refrigerant pipe connecting the fourth port 22d of the four-way switching valve 22 and the gas refrigerant communication pipe 6 side.
- the outdoor heat exchanger 23 is a heat exchanger that functions as a refrigerant radiator that uses outdoor air as a cooling source during cooling operation, and that functions as a refrigerant evaporator that uses outdoor air as a heating source during heating operation.
- the outdoor heat exchanger 23 has a liquid side connected to the liquid refrigerant pipe 35 and a gas side connected to the first gas refrigerant pipe 33.
- the liquid refrigerant pipe 35 is a refrigerant pipe that connects the liquid side of the outdoor heat exchanger 23 and the liquid refrigerant communication pipe 5 side.
- the first expansion valve 24 functions as an upstream expansion valve for expanding the refrigerant discharged from the compressor 21 in two stages during the cooling operation, and the high-pressure refrigerant in the refrigeration cycle radiating heat in the outdoor heat exchanger 23 is It is a valve that reduces the pressure to an intermediate pressure in the refrigeration cycle.
- the first expansion valve 24 functions as a downstream expansion valve for expanding the refrigerant discharged from the compressor 21 in two stages during the heating operation, and is an intermediate-pressure refrigerant in the refrigeration cycle stored in the receiver 25. Is a valve for reducing the pressure to a low pressure in the refrigeration cycle.
- the first expansion valve 24 is provided in a portion of the liquid refrigerant pipe 35 between the outdoor heat exchanger 23 and the receiver 25.
- the receiver 25 is provided between the first expansion valve 24 and the second expansion valve 26 (that is, between the upstream expansion valve and the downstream expansion valve).
- the receiver 25 is a container that can store an intermediate-pressure refrigerant in the refrigeration cycle during cooling operation and heating operation.
- the second expansion valve 26 functions as a downstream expansion valve for expanding the refrigerant discharged from the compressor 21 in two stages during the cooling operation, and refrigerates the intermediate-pressure refrigerant in the refrigeration cycle stored in the receiver 25.
- the second expansion valve 26 functions as an upstream expansion valve for expanding the refrigerant discharged from the compressor 21 in two stages during the heating operation, and has a high pressure in the refrigeration cycle that dissipates heat in the indoor heat exchanger 41. It is a valve that reduces the refrigerant to an intermediate pressure in the refrigeration cycle.
- the second expansion valve 26 is provided in a portion of the liquid refrigerant pipe 35 between the receiver 25 and the liquid side closing valve 27.
- the liquid side shut-off valve 27 and the gas side shut-off valve 28 are valves provided at connection ports with external devices and pipes (specifically, the liquid refrigerant communication pipe 5 and the gas refrigerant communication pipe 6).
- the liquid side closing valve 27 is provided at the end of the liquid refrigerant pipe 35.
- the gas side closing valve 28 is provided at the end of the second gas refrigerant pipe 34.
- the outdoor unit 2 has an outdoor fan 36 for sucking outdoor air into the outdoor unit 2, exchanging heat with the refrigerant in the outdoor heat exchanger 23, and then discharging the air to the outside.
- the outdoor fan 36 is driven by an outdoor fan motor 37 capable of controlling the rotation speed. As a result, the outdoor fan 36 has a variable operating capacity.
- the outdoor unit 2 is provided with various sensors. Specifically, the suction pipe 31 is provided with a suction temperature sensor 51 that detects the temperature Ts of the low-pressure refrigerant in the refrigeration cycle sucked into the compressor 21.
- the discharge pipe 32 is provided with a discharge temperature sensor 52 that detects the temperature Td of the high-pressure refrigerant in the refrigeration cycle discharged from the compressor 21.
- the outdoor heat exchanger 23 includes an outdoor heat exchange intermediate temperature sensor 53 that detects a refrigerant temperature Torm in an intermediate portion of the outdoor heat exchanger 23, and an outdoor that detects a refrigerant temperature Torl on the liquid side of the outdoor heat exchanger 23.
- a heat exchanger side temperature sensor 54 is provided.
- the outdoor unit 2 is provided with an outdoor temperature sensor 55 that detects the temperature Toa of the outdoor air sucked into the outdoor unit 2.
- the liquid refrigerant pipe 35 is provided with a liquid pipe temperature sensor 56 that detects a liquid pipe temperature Tlp of the refrigerant in a portion between the second expansion valve 26 and the liquid side closing valve 27.
- the outdoor unit 2 includes an outdoor control unit 38 that controls the operation of each unit constituting the outdoor unit 2.
- the outdoor control unit 38 includes a microcomputer and a memory provided for controlling the outdoor unit 2, and exchanges control signals and the like with the indoor unit 4 via the transmission line 8 a. Can be done.
- Refrigerant communication pipes 5 and 6 are refrigerant pipes constructed on site when the air conditioner 1 is installed at an installation location such as a building, and installation conditions such as the installation location and a combination of an outdoor unit and an indoor unit. Those having various lengths and tube diameters are used.
- the refrigerant circuit 10 of the air conditioner 1 is configured by connecting the outdoor unit 2, the indoor unit 4, and the refrigerant communication pipes 5 and 6.
- the refrigerant circuit 10 of the air conditioner 1 switches the four-way switching valve 22 to the cooling cycle state, so that the compressor 21, the outdoor heat exchanger 23, the first expansion valve 24 as the upstream expansion valve, and the downstream expansion valve.
- the second expansion valve 26 and the indoor heat exchanger 41 are connected, and the compressor 21 is connected by the first expansion valve 24 as the upstream side expansion valve and the second expansion valve 26 as the downstream side expansion valve.
- a cooling operation is performed in which the high-pressure refrigerant discharged from the refrigerant is circulated in two stages in the order of intermediate pressure and low pressure.
- the refrigerant circuit 10 of the air conditioning apparatus 1 switches the four-way switching valve 22 to the heating cycle state, so that the compressor 21, the indoor heat exchanger 41, the second expansion valve 26 as an upstream expansion valve, and the downstream side.
- a first expansion valve 24 as an expansion valve and an outdoor heat exchanger 23 are connected, and compression is performed by a second expansion valve 26 as an upstream expansion valve and a first expansion valve 24 as a downstream expansion valve.
- Heating operation is performed in which the high-pressure refrigerant discharged from the machine 21 is expanded in two stages in the order of intermediate pressure and low pressure, and the refrigerant is circulated.
- the air conditioner 1 also includes an outdoor fan 36 that supplies outdoor air to the outdoor heat exchanger 23 as a cooling source or a heating source.
- the air conditioner 1 can control each device of the outdoor unit 2 and the indoor unit 4 by the control unit 8 including the indoor side control unit 44 and the outdoor side control unit 38. That is, the control unit 8 that performs operation control of the entire air conditioner 1 including the cooling operation and the heating operation described above is configured by the transmission line 8a that connects between the indoor side control unit 44 and the outdoor side control unit 38.
- the control unit 8 is connected so as to receive detection signals from various sensors 51 to 59 and the like, and based on these detection signals and the like, various devices and valves 21a, 22 are connected. , 24, 26, 37, 43, etc. are connected so that they can be controlled.
- the air conditioner 1 can perform a cooling operation and a heating operation as basic operations.
- the low-pressure gas refrigerant in the refrigeration cycle is sucked into the compressor 21, compressed after being compressed to a high pressure in the refrigeration cycle, and then discharged.
- the high-pressure gas refrigerant discharged from the compressor 21 is sent to the indoor heat exchanger 41 through the four-way switching valve 22, the gas side closing valve 28 and the gas refrigerant communication pipe 6.
- the high-pressure gas refrigerant sent to the indoor heat exchanger 41 radiates heat by exchanging heat with indoor air supplied as a cooling source by the indoor fan 42 in the indoor heat exchanger 41 to become a high-pressure liquid refrigerant. . Thereby, indoor air is heated, and indoor heating is performed by being supplied indoors after that.
- the high-pressure liquid refrigerant radiated by the indoor heat exchanger 41 is sent to the second expansion valve 26 as the upstream side expansion valve through the liquid refrigerant communication pipe 5 and the liquid side closing valve 27.
- the high-pressure liquid refrigerant sent to the second expansion valve 26 is depressurized to the intermediate pressure in the refrigeration cycle by the second expansion valve 26, and becomes an intermediate-pressure gas-liquid two-phase refrigerant.
- the intermediate-pressure gas-liquid two-phase refrigerant decompressed by the second expansion valve 26 is temporarily stored in the receiver 25 and then sent to the first expansion valve 24 as a downstream expansion valve.
- the intermediate-pressure gas-liquid two-phase refrigerant sent to the first expansion valve 24 is depressurized by the first expansion valve 24 to a low pressure in the refrigeration cycle, and becomes a low-pressure gas-liquid two-phase refrigerant.
- the low-pressure gas-liquid two-phase refrigerant decompressed by the first expansion valve 24 is sent to the outdoor heat exchanger 23.
- the low-pressure gas-liquid two-phase refrigerant sent to the outdoor heat exchanger 23 evaporates in the outdoor heat exchanger 23 by exchanging heat with the outdoor air supplied as a heating source by the outdoor fan 36. Become a gas refrigerant.
- the low-pressure refrigerant evaporated in the outdoor heat exchanger 23 is again sucked into the compressor 21 through the four-way switching valve 22.
- control unit 8 controls the operating capacity of the compressor 21 and the outdoor fan 36 according to the required heating load of the indoor unit 4, and controls the opening of the expansion valves 24 and 26. Is also going. The control of the operating capacity of the compressor 21 and the outdoor fan 36 and the opening control of the expansion valves 24 and 26 will be described later.
- the low-pressure gas refrigerant in the refrigeration cycle is sucked into the compressor 21, compressed after being compressed to a high pressure in the refrigeration cycle, and then discharged.
- the high-pressure gas refrigerant discharged from the compressor 21 is sent to the outdoor heat exchanger 23 through the four-way switching valve 22.
- the high-pressure gas refrigerant sent to the outdoor heat exchanger 23 performs heat exchange with the outdoor air supplied as a cooling source by the outdoor fan 36 in the outdoor heat exchanger 23 to dissipate heat to become a high-pressure liquid refrigerant. .
- the high-pressure liquid refrigerant that has radiated heat in the outdoor heat exchanger 23 is sent to a first expansion valve 24 as an upstream expansion valve.
- the high-pressure liquid refrigerant sent to the first expansion valve 24 is depressurized to the intermediate pressure in the refrigeration cycle by the first expansion valve 24, and becomes an intermediate-pressure gas-liquid two-phase refrigerant.
- the intermediate-pressure gas-liquid two-phase refrigerant decompressed by the first expansion valve 24 is temporarily stored in the receiver 25 and then sent to the second expansion valve 26 as a downstream expansion valve.
- the intermediate-pressure gas-liquid two-phase refrigerant sent to the second expansion valve 26 is depressurized to a low pressure in the refrigeration cycle by the second expansion valve 26 to become a low-pressure gas-liquid two-phase refrigerant.
- the low-pressure gas-liquid two-phase refrigerant decompressed by the second expansion valve 26 is sent to the indoor heat exchanger 41 through the liquid side closing valve 27 and the liquid refrigerant communication pipe 5.
- the low-pressure gas-liquid two-phase refrigerant sent to the indoor heat exchanger 41 evaporates in the indoor heat exchanger 41 by exchanging heat with indoor air supplied as a heating source by the indoor fan 42. As a result, the room air is cooled and then supplied to the room to cool the room.
- the low-pressure gas refrigerant evaporated in the indoor heat exchanger 41 is again sucked into the compressor 21 through the gas refrigerant communication pipe 6, the gas side closing valve 28 and the four-way switching valve 22.
- control unit 8 controls the operation capacity of the compressor 21 and the outdoor fan 36 according to the required heating load of the indoor unit 4, and controls the opening degree of the expansion valves 24 and 26. Is also going. The control of the operating capacity of the compressor 21 and the outdoor fan 36 and the opening control of the two expansion valves 24 and 26 will be described later.
- Control of the operating capacity of the compressor 21 and / or the outdoor fan 36 is performed by a capacity controller 82 of the controller 8 as shown in FIG.
- the capacity control unit 82 controls the operating capacity of the compressor 21 and / or the outdoor fan 36 so that the low pressure or high pressure in the refrigeration cycle of the refrigerant circuit 10 becomes a target value.
- the target value of the low pressure or high pressure (or the evaporation temperature or the condensation temperature corresponding to the low pressure or high pressure) in the refrigeration cycle of the refrigerant circuit 10 is set by a target value determination unit 81 of the control unit 8 as shown in FIG. Is set.
- the control of the operation capacity of the compressor 21 and / or the outdoor fan 36 will be described separately for the cooling operation and the heating operation.
- the target value determination unit 81 sets the indoor set temperature Tt input from a remote controller (not shown) or the like, and the refrigerant temperature Trrm in the indoor heat exchanger 41 detected by the indoor heat exchanger intermediate temperature sensor 58. Based on (here, corresponding to the condensation temperature Tc corresponding to the high pressure in the refrigeration cycle of the refrigerant circuit 10), the target condensation temperature Tcs that is the target value of the condensation temperature Tc is set. For example, when the temperature difference obtained by subtracting the refrigerant temperature Trrm in the indoor heat exchanger 41 from the set temperature Tt is large, the heating capacity needs to be increased, so the target condensing temperature Tcs is set to be high. In addition, when the temperature difference obtained by subtracting the refrigerant temperature Trrm in the indoor heat exchanger 41 from the set temperature Tt is small, the heating capacity needs to be reduced, so the target condensation temperature Tcs is set to be low.
- the capacity control unit 82 changes the frequency of the compressor motor 21a so that the condensation temperature Tc corresponding to the high pressure in the refrigeration cycle of the refrigerant circuit 10 becomes the target condensation temperature Tcs set by the target value determination unit 81. By doing so, the operating capacity of the compressor 21 is controlled. For example, when the condensation temperature Tc is lower than the target condensation temperature Tcs, the operating capacity of the compressor 21 is changed to increase by increasing the frequency of the compressor motor 21a. In addition, when the condensation temperature Tc is higher than the target condensation temperature Tcs, the operating capacity of the compressor 21 is changed to be decreased by decreasing the frequency of the compressor motor 21a.
- the capacity control unit 82 controls the operating capacity of the outdoor fan 36 by changing the rotational speed of the outdoor fan motor 37 so that the condensation temperature Tc becomes the target condensation temperature Tcs. For example, when the condensation temperature Tc is lower than the target condensation temperature Tcs, the rotational speed of the outdoor fan motor 37 is increased to change the operating capacity of the outdoor fan 36. When the condensation temperature Tc is higher than the target condensation temperature Tcs, the rotational speed of the outdoor fan motor 37 is decreased to change the operating capacity of the outdoor fan 36.
- the capacity control unit 82 controls the operating capacities of the compressor 21 and the outdoor fan 36. However, only the operating capacities of the compressor 21 may be controlled, or the operating of the outdoor fan 36 may be controlled. Only the capacity may be controlled.
- the target value determining unit 81 sets the indoor set temperature Tt input from a remote controller (not shown) or the like, and the refrigerant temperature Trrm in the indoor heat exchanger 41 detected by the indoor heat exchanger intermediate temperature sensor 58. Based on (here, corresponding to the evaporation temperature Te corresponding to the low pressure in the refrigeration cycle of the refrigerant circuit 10), the target evaporation temperature Tes that is the target value of the evaporation temperature Te is set. For example, when the temperature difference obtained by subtracting the set temperature Tt from the refrigerant temperature Trrm in the indoor heat exchanger 41 is large, it is necessary to increase the cooling capacity, so that the target evaporation temperature Tes is set to be low. Further, when the temperature difference obtained by subtracting the set temperature Tt from the refrigerant temperature Trrm in the indoor heat exchanger 41 is small, it is necessary to reduce the cooling capacity, so that the target evaporation temperature Tes is set to be high.
- the capacity control unit 82 changes the frequency of the compressor motor 21a so that the evaporation temperature Te corresponding to the low pressure in the refrigeration cycle of the refrigerant circuit 10 becomes the target evaporation temperature Tes set by the target value determining unit 81. By doing so, the operating capacity of the compressor 21 is controlled. For example, when the evaporation temperature Te is higher than the target evaporation temperature Tes, the operating capacity of the compressor 21 is changed to increase by increasing the frequency of the compressor motor 21a. Further, when the evaporation temperature Te is lower than the target evaporation temperature Tes, the operating capacity of the compressor 21 is changed in a direction to decrease by decreasing the frequency of the compressor motor 21a.
- the capacity control unit 82 controls the operating capacity of the outdoor fan 36 by changing the rotational speed of the outdoor fan motor 37 so that the evaporation temperature Te becomes the target evaporation temperature Tes. For example, when the evaporation temperature Te is higher than the target evaporation temperature Tes, the rotational speed of the outdoor fan motor 37 is increased to change the operating capacity of the outdoor fan 36. Further, when the evaporation temperature Te is lower than the target evaporation temperature Tes, the operation speed of the outdoor fan 36 is changed by decreasing the rotational speed of the outdoor fan motor 37.
- the capacity control unit 82 controls the operating capacities of the compressor 21 and the outdoor fan 36. However, only the operating capacities of the compressor 21 may be controlled, or the operating of the outdoor fan 36 may be controlled. Only the capacity may be controlled.
- ⁇ Feedback control of expansion valve> As the opening control of the two expansion valves 24 and 26, feedback control based on the degree of supercooling and the degree of superheat is performed along with feedforward control described later.
- the feedback control of the expansion valves 24 and 26 is performed by a feedback control unit 84 of the control unit 8 as shown in FIG.
- the feedback control unit 84 expands the refrigerant so that the degree of subcooling of the refrigerant at the outlet of the heat exchanger functioning as a refrigerant radiator of the outdoor heat exchanger 23 and the indoor heat exchanger 41 becomes a predetermined target subcooling degree.
- the opening degree of the expansion valve that functions as the upstream side expansion valve is controlled.
- the feedback control unit 84 expands the refrigerant so that the superheat degree of the refrigerant at the outlet of the heat exchanger functioning as the refrigerant evaporator of the outdoor heat exchanger 23 and the indoor heat exchanger 41 becomes a predetermined target superheat degree.
- the opening degree of the expansion valve that functions as a downstream side expansion valve is controlled.
- feedback control of the expansion valves 24 and 26 will be described separately for the cooling operation and the heating operation.
- the feedback control unit 84 functions as an upstream expansion valve located on the upstream side of the receiver 25 so that the refrigerant subcooling degree SC at the outlet of the indoor heat exchanger 41 becomes the target subcooling degree SCs.
- the opening degree of the second expansion valve 26 is controlled. For example, when the supercooling degree SC is larger than the target supercooling degree SCs, the opening degree of the second expansion valve 26 is changed to be increased in order to increase the flow rate of the refrigerant passing through the indoor heat exchanger 41. To do.
- the opening degree of the second expansion valve 26 is changed to be smaller.
- the supercooling degree SC of the refrigerant at the outlet of the indoor heat exchanger 41 is the temperature of the refrigerant detected by the indoor heat exchanger side temperature sensor 57 from the refrigerant temperature Trrm detected by the indoor heat exchanger intermediate temperature sensor 58. It is obtained by subtracting Trrl.
- the feedback control 84 is a downstream expansion valve located on the downstream side of the receiver 25 so that the superheat degree SH of the refrigerant at the outlet of the outdoor heat exchanger 23 becomes a predetermined target superheat degree SHs.
- the opening degree of the first expansion valve 24 is controlled. For example, when the superheat degree SH is larger than the target superheat degree SHs, the opening degree of the first expansion valve 24 is changed to increase in order to increase the flow rate of the refrigerant passing through the outdoor heat exchanger 23. Further, when the superheat degree SH is smaller than the target superheat degree SHs, the opening degree of the first expansion valve 24 is changed to be smaller in order to reduce the flow rate of the refrigerant passing through the outdoor heat exchanger 23.
- the superheat degree SH of the refrigerant at the outlet of the outdoor heat exchanger 23 is obtained by subtracting the refrigerant temperature Tor detected by the outdoor heat exchanger intermediate temperature sensor 53 from the refrigerant temperature Ts detected by the suction temperature sensor 51. can get.
- the sensor for obtaining the degree of supercooling SC and the degree of superheating SH is not limited to the above, and when a pressure sensor for detecting high pressure and low pressure in the refrigeration cycle is provided and / or heat When other temperature sensors are provided in the exchanger and in the vicinity thereof, detection values of these sensors may be used.
- the feedback control unit 84 functions as an upstream expansion valve located on the upstream side of the receiver 25 so that the refrigerant subcooling degree SC at the outlet of the outdoor heat exchanger 23 becomes the target subcooling degree SCs.
- the opening degree of the first expansion valve 24 is controlled. For example, when the degree of supercooling SC is larger than the target degree of supercooling SCs, the opening degree of the first expansion valve 24 is changed to increase in order to increase the flow rate of the refrigerant passing through the outdoor heat exchanger 23. To do.
- the opening degree of the first expansion valve 24 is changed to be smaller.
- the supercooling degree SC of the refrigerant at the outlet of the outdoor heat exchanger 23 is the temperature of the refrigerant detected by the outdoor heat exchanger side temperature sensor 54 from the refrigerant temperature Tor detected by the outdoor heat exchanger intermediate temperature sensor 53. It is obtained by subtracting Tor.
- the feedback control 84 is a downstream expansion valve located on the downstream side of the receiver 25 so that the superheat degree SH of the refrigerant at the outlet of the indoor heat exchanger 41 becomes a predetermined target superheat degree SHs.
- the opening degree of the second expansion valve 26 is controlled. For example, when the superheat degree SH is larger than the target superheat degree SHs, the opening degree of the second expansion valve 26 is changed to increase in order to increase the flow rate of the refrigerant passing through the indoor heat exchanger 41. When the superheat degree SH is smaller than the target superheat degree SHs, in order to reduce the flow rate of the refrigerant passing through the indoor heat exchanger 41, the opening degree of the second expansion valve 26 is changed.
- the superheat degree SH of the refrigerant at the outlet of the indoor heat exchanger 41 is obtained by subtracting the refrigerant temperature Trrm detected by the indoor heat exchanger intermediate temperature sensor 58 from the refrigerant temperature Ts detected by the suction temperature sensor 51. can get.
- the sensor for obtaining the degree of supercooling SC and the degree of superheating SH is not limited to the above, and when a pressure sensor for detecting high pressure and low pressure in the refrigeration cycle is provided and / or heat When other temperature sensors are provided in the exchanger and in the vicinity thereof, detection values of these sensors may be used.
- Feed-forward control of expansion valve> As the opening control of the two expansion valves 24, 26, the refrigerant that passes through the expansion valves 24, 26 when the operation capacity of the compressor 21 and / or the operation capacity of the outdoor fan 36 is changed. Feed-forward control is performed in which a change in the circulation amount is predicted, and the opening degree of the two expansion valves 24 and 26 as the upstream expansion valve and the downstream expansion valve is changed in consideration of the predicted change in the refrigerant circulation amount. I am doing so.
- the feedforward control of the expansion valves 24 and 26 is performed by a feedforward control unit 83 of the control unit 8 as shown in FIG.
- the feedforward control unit 83 includes a prediction unit 83a and an opening change unit 83b.
- the predicting unit 83a includes a compressor under a prediction condition based on a correlation between a high pressure side pressure difference obtained by subtracting the intermediate pressure in the refrigeration cycle from a high pressure in the refrigeration cycle and a low pressure side pressure difference obtained by subtracting the low pressure in the refrigeration cycle from the intermediate pressure. 21 and / or a change in the refrigerant circulation amount passing through the two expansion valves 24 and 26 as the downstream expansion valve after changing the operation capacity of the outdoor fan 36 is predicted. .
- the predicting unit 83a takes into account the change in the refrigerant circulation amount predicted when the operating capacity of the compressor 21 and / or the operating capacity of the outdoor fan 36 is changed. The opening degree of the two expansion valves 24 and 26 as the expansion valves is calculated.
- the opening changing unit 83b performs control to change the opening of the two expansion valves 24 and 26 as the upstream expansion valve and the downstream expansion valve to the opening calculated by the prediction unit 83a.
- the feedforward control of the expansion valves 24 and 26 will be described separately for the cooling operation and the heating operation.
- the feedforward control unit 83 first determines whether or not the operation capacity of the compressor 21 and / or the operation capacity of the outdoor fan 36 changes as shown in FIG. 4 (step ST1). .
- the operating capacity of the compressor 21 and / or the outdoor fan 36 is changed by controlling the operating capacity of the compressor 21 and / or the outdoor fan 36 described above. For this reason, when it determines with the operation capacity of the compressor 21 and / or the outdoor fan 36 changing in step ST1, the control of the operation capacity of the above-mentioned compressor 21 and / or the outdoor fan 36 is performed. Means. If it is determined in step ST1 that the operating capacity of the compressor 21 and / or the outdoor fan 36 changes, the process proceeds to steps ST2 to ST7.
- step ST2 the prediction unit 83a of the feedforward control unit 83 performs two expansions immediately before the operation capacity of the compressor 21 and / or the outdoor fan 36 is controlled (that is, immediately before the operation capacity changes).
- a virtual combined opening EVFF before the change in operating capacity is calculated by adding the openings EVu and EVd of the valves 24 and 26.
- the virtual total opening degree EVFF before the operation capacity change is calculated by the following formula ⁇ 1>.
- EVu is the value of the upstream side expansion valve (here, the second expansion valve 26) immediately before the operation capacity of the compressor 21 and / or the outdoor fan 36 is controlled (that is, immediately before the operation capacity changes).
- the opening degree here, the opening degree normalized so that the maximum opening degree is 1).
- EVd indicates that the downstream expansion valve (here, the first expansion valve 24) is opened immediately before the operation capacity of the compressor 21 and / or the outdoor fan 36 is controlled (that is, immediately before the operation capacity changes).
- Degree here, the opening degree normalized so that the maximum opening degree is 1).
- step ST3 the prediction unit 83a passes through the two expansion valves 24 and 26 immediately before the operation capacity of the compressor 21 and / or the outdoor fan 36 is controlled (that is, immediately before the operation capacity changes).
- the refrigerant circulation amount Gr before the operating capacity change is calculated.
- the refrigerant circulation amount Gr before the operation capacity change can be expressed as a function of the virtual total opening EVFF before the operation capacity change calculated in step ST2, as in the following formula ⁇ 2>.
- step ST4 the prediction unit 83a sets the two expansion valves 24 and 26 immediately after the operation capacity of the compressor 21 and / or the outdoor fan 36 is controlled (that is, immediately after the operation capacity is changed).
- the refrigerant circulation amount Grc after the change in operating capacity to pass through is calculated.
- the refrigerant circulation amount Grc after the change in the operation capacity is the operation capacity ratio Fcc / Fc before and after the change in the operation capacity of the compressor 21 and the change in the operation capacity of the outdoor fan 36 before and after the change as shown in the following equation ⁇ 3>.
- Grc f (Fcc / Fc, Ffc / Ff, Tc, Te) ⁇ Gr (3)
- Fcc is the operating capacity of the compressor 21 immediately after the operating capacity of the compressor 21 is controlled (that is, immediately after the operating capacity changes)
- Fc is the control of the operating capacity of the compressor 21. Is the operating capacity of the compressor 21 immediately before the operation is performed (that is, immediately before the operating capacity is changed).
- the frequency ratio of the compressor motor 21a before and after the change in the operation capacity of the compressor 21 is used as the operation capacity ratio Fcc / Fc before and after the change in the operation capacity of the compressor 21.
- Ffc is the operating capacity of the outdoor fan 36 immediately after the operating capacity of the outdoor fan 36 is controlled (that is, immediately after the operating capacity is changed), and Ff is the operating capacity of the outdoor fan 36. This is the operating capacity of the outdoor fan 36 immediately before it is performed (that is, immediately before the operating capacity changes).
- the rotational speed ratio of the outdoor fan motor 37 before and after the change in the operating capacity of the outdoor fan 36 is used as the operating capacity ratio Ffc / Ff before and after the change in the operating capacity of the outdoor fan 36.
- the refrigerant temperature Trrm in the indoor heat exchanger 41 functioning as a refrigerant condenser is used, and the refrigeration cycle before the operation capacity change.
- the evaporation temperature Te the refrigerant temperature Tor in the indoor heat exchanger 23 functioning as the refrigerant evaporator is used (during cooling operation, the temperature Tor becomes the condensation temperature Tc, and the temperature Trrm is equal to the evaporation temperature Te. Become).
- step ST5 the prediction unit 83a determines whether the two expansion valves 24 and 26 immediately after the operation capacity of the compressor 21 and / or the outdoor fan 36 is controlled (that is, immediately after the operation capacity is changed).
- a virtual combined opening EVFFc after changing the operating capacity is calculated by adding the opening (that is, the opening EVuc of the upstream expansion valve after changing the operating capacity and the opening EVdc of the downstream expansion valve after changing the operating capacity). To do.
- the virtual combined opening EVFFc after the change in the operation capacity can be expressed as a function of the refrigerant circulation amount Grc after the change in the operation capacity calculated in step ST4 as in the following formula ⁇ 4>.
- step ST6 the prediction unit 83a uses the virtual total opening EVFFc after the change in operating capacity calculated in step ST5, and the openings EVuc and EVdc after the changes in operating capacity of the two expansion valves 24 and 26. Is calculated.
- the sensors 53 and 58 for detecting the condensation temperature Tc corresponding to the high pressure Ph and the evaporation temperature Te corresponding to the low pressure Pl are provided, but a sensor for detecting the intermediate pressure Pm is provided. Not.
- a prediction condition is set based on the correlation between the high pressure side pressure difference ⁇ Ph obtained by subtracting the intermediate pressure Pm from the high pressure Ph and the low pressure side pressure difference ⁇ P1 obtained by subtracting the low pressure Pl from the intermediate pressure Pm.
- the relationship between the high pressure side pressure difference ⁇ Ph and the low pressure side pressure difference ⁇ Pl is constant before and after the operating capacity of the compressor 21 and / or the outdoor fan 36 is changed. It is set.
- step ST7 the opening changing unit 83b of the feedforward control unit 83 performs control to change the opening of the two expansion valves 24 and 26 to the opening EVuc and EVdc calculated in step ST6.
- step ST1 the process returns to step ST1 again, and each time the operating capacity of the compressor 21 and / or the outdoor fan 36 is changed, the process of steps ST2 to ST7 is performed. In this way, feedforward control of the two expansion valves 24 and 26 is performed.
- the second expansion valve 26 functions as an upstream expansion valve
- the first expansion valve 24 functions as a downstream expansion valve
- the indoor heat exchanger 41 functions as a refrigerant condenser.
- the outdoor heat exchanger 23 functions as a refrigerant evaporator
- the first expansion valve 24 functions as an upstream expansion valve and the second expansion valve during cooling operation.
- 26 is functioning as a downstream expansion valve
- the outdoor heat exchanger 23 is functioning as a refrigerant condenser
- the indoor heat exchanger 41 is functioning as a refrigerant evaporator. Since it is the same as that at the time of heating operation except for a point, detailed description is abbreviate
- the air conditioner 1 of the present embodiment has the following features.
- the compressor 21 and / or a change in the amount of refrigerant circulating through the upstream expansion valve and the downstream expansion valve (in this case, the expansion valves 24 and 26) after changing the operation capacity of the outdoor fan 36 is predicted.
- the upstream expansion valve and the downstream expansion valve are opened in consideration of the predicted change in the refrigerant circulation amount. Control is performed to change the degree.
- the compressor 21 and the outdoor fan are used under the prediction condition based on the correlation between the high pressure side pressure difference ⁇ Ph and the low pressure side pressure difference ⁇ Pm.
- the change of the refrigerant circulation amount passing through the upstream side expansion valve and the downstream side expansion valve after changing the operation capacity of 36 is predicted.
- the ratio between the high pressure side pressure difference ⁇ Ph and the low pressure side pressure difference ⁇ Pl is constant before and after the operation capacity of the compressor 21 and / or the operation capacity of the outdoor fan 36 is changed. The relationship that there is.
- the upstream expansion valve here, one of the expansion valves 24 and 26
- the degree of opening of the refrigerant is controlled so that the refrigerant supercooling degree SC at the outlet of the evaporator becomes a predetermined target supercooling degree SCs
- the downstream expansion valve here, the other of the expansion valves 24 and 26
- the opening degree is controlled so that the superheat degree SH of the refrigerant at the outlet of the heat exchanger functioning as the refrigerant evaporator of the indoor heat exchanger 41 becomes a predetermined target superheat degree SHs.
- feedback control based on the degree of supercooling and the degree of superheat is performed together with the feedforward control described above as the opening degree control of the upstream side expansion valve and the downstream side expansion valve. Therefore, here, when the operating capacities of the compressor 21 and the outdoor fan 36 change, the opening degrees of the upstream side expansion valve and the downstream side expansion valve are controlled by feedforward control to operate the compressor 21 and the outdoor fan 36. After approaching the optimum opening after the change in capacity in advance, it can be made to coincide with the optimum opening by feedback control.
- the time required for feedback control of the upstream side expansion valve and the downstream side expansion valve can be effectively shortened. And when the operating capacity of the compressor 21 and the outdoor fan 36 changes, the control followability of the opening degree of the upstream side expansion valve and the downstream side expansion valve can be improved.
- a relationship in which the high-pressure side pressure difference ⁇ Ph is constant before and after the operation capacity of the compressor 21 and / or the operation capacity of the outdoor fan 36 is changed may be set.
- feedforward control of the expansion valves 24 and 26 adopting this correlation will be described.
- the content during the heating operation will be described, and the content during the cooling operation will be omitted.
- the feedforward control unit 83 firstly operates the capacity of the compressor 21 and / or the outdoor, similarly to step ST1 in the above-described feedforward control (see FIG. 4). It is determined whether or not the operating capacity of the fan 36 changes (step ST11). If it is determined in step ST11 that the operating capacity of the compressor 21 and / or the outdoor fan 36 changes, the process proceeds to steps ST12 to ST20.
- step ST12 the prediction unit 83a of the feedforward control unit 83 controls the operating capacity of the compressor 21 and / or the outdoor fan 36 in the same manner as in step ST2 in the above-described feedforward control (see FIG. 4).
- a virtual combined opening EVFF before the operation capacity change is calculated by adding the openings EVu and EVd of the two expansion valves 24 and 26 immediately before the operation capacity is changed (that is, immediately before the operation capacity is changed). For example, when an expansion valve having a characteristic in which the opening degree and the Cv value are proportional to each other is adopted as the expansion valves 24 and 26, the virtual total opening degree EVFF before the change in the operation capacity is the above feedforward control (FIG. 4). In the same manner as in step ST2 in the reference), it is calculated by the following formula ⁇ 11>.
- step ST13 the prediction unit 83a immediately before the control of the operating capacity of the compressor 21 and / or the outdoor fan 36 is performed as in step ST3 in the above-described feedforward control (see FIG. 4) (that is, The refrigerant circulation amount Gr before the change of the operation capacity passing through the two expansion valves 24 and 26 immediately before the change of the operation capacity is calculated.
- the refrigerant circulation amount Gr before the change in the operation capacity is the same as that in step ST3 in the above-described feedforward control (see FIG. 4), as shown in the following formula ⁇ 12>, before the change in the operation capacity. Can be expressed as a function of the virtual combined opening EVFF.
- step ST14 unlike step ST3 in the above feedforward control (see FIG. 4), immediately after the operation capacity of the compressor 21 and / or the outdoor fan 36 is controlled (that is, the operation capacity changes).
- the operation capacity of the compressor 21 and / or the outdoor fan 36 of the upstream side expansion valve (the second expansion valve 26 during the heating operation or the first expansion valve 24 during the cooling operation) is controlled.
- the refrigerant circulation amount Gruc that passes through the upstream expansion valve after the change in the operating capacity immediately after (that is, immediately after the operating capacity changes) is calculated.
- the refrigerant circulation amount Gruc that passes through the upstream side expansion valve after the change in the operation capacity is equal to the operation capacity ratio Fcc / Fc before and after the change in the operation capacity of the compressor 21, as shown in the following formula ⁇ 13>. It can be expressed as a function of the operation capacity ratio Ffc / Ff before and after the change of the operation capacity and the refrigerant circulation amount Gr before the operation capacity change.
- the refrigerant circulation amount Gruc passing through the upstream side expansion valve after the change of the operation capacity is the value after the change of the operation capacity calculated under the condition that the high pressure Ph, the intermediate pressure Pm, and the low pressure Pl are not changed before and after the change of the operation capacity. Refrigerant circulation amount.
- step ST15 the prediction unit 83a determines the opening degrees of the two expansion valves 24 and 26 after the change in the operation capacity under the condition that there is no change in the high pressure Ph, the intermediate pressure Pm, and the low pressure Pl before and after the change in the operation capacity.
- the virtual combined opening EVFFuc after the change of the combined operation capacity is calculated.
- the virtual total opening EVFFuc after the change in the operation capacity under the condition that there is no change in the high pressure Ph, the intermediate pressure Pm and the low pressure Pl before and after the change in the operation capacity is calculated in step ST14 as shown in the following formula ⁇ 14>. It can be expressed as a function of the refrigerant circulation amount Gruc after the change in the operation capacity under the condition that there is no change in the high pressure Ph, the intermediate pressure Pm and the low pressure Pl before and after the change in the operation capacity.
- step ST16 the prediction unit 83a determines the virtual total opening EVFFuc after the change in operating capacity under the condition that there is no change in the high pressure Ph, the intermediate pressure Pm, and the low pressure Pl before and after the change in operating capacity calculated in step ST15. Is used to calculate the opening degree EVuc after the operation capacity change of the upstream side expansion valve (the second expansion valve 26 during the heating operation or the first expansion valve 24 during the cooling operation).
- step S16 unlike step ST6 of the above-described feedforward control (see FIG. 4), the downstream side expansion valve (the first expansion valve 24 during the heating operation or the second expansion valve during the cooling operation).
- the opening degree EVdc after the change of the operation capacity in 26) is not calculated, but is calculated in steps ST17 to ST19.
- step ST17 the prediction unit 83a immediately after the operation capacity of the compressor 21 and / or the outdoor fan 36 is controlled (that is, similarly to step ST4 in the above-described feedforward control (see FIG. 4) (that is, The refrigerant circulation amount Grc after the change of the operation capacity passing through the two expansion valves 24 and 26 immediately after the operation capacity is changed is calculated.
- the refrigerant circulation amount Grc after the change in the operation capacity is the operation capacity ratio Fcc / Fc before and after the change in the operation capacity of the compressor 21 and the change in the operation capacity of the outdoor fan 36 before and after the change as shown in the following equation ⁇ 17>. It can be expressed as a function of the operating capacity ratio Ffc / Ff, the condensation temperature Tc in the refrigeration cycle before the operating capacity change, the evaporation temperature Te in the refrigeration cycle before the operating capacity change, and the refrigerant circulation amount Gr before the operating capacity change.
- step ST18 the prediction unit 83a sets the two expansion valves 24 and 26 immediately after the operation capacity of the compressor 21 and / or the outdoor fan 36 is controlled (that is, immediately after the operation capacity is changed).
- a virtual combined opening EVFFc after changing the operating capacity is calculated by adding the opening (that is, the opening EVuc of the upstream expansion valve after changing the operating capacity and the opening EVdc of the downstream expansion valve after changing the operating capacity).
- the virtual combined opening EVFFc after the change in the operation capacity can be expressed as a function of the refrigerant circulation amount Grc after the change in the operation capacity calculated in step ST17, as in the following formula ⁇ 18>.
- step ST19 the prediction unit 83a determines the virtual total opening degree EVFFc after the change in operating capacity calculated in step ST18 and the opening degree EVuc of the upstream side expansion valve after the change in operating capacity calculated in step ST16. Is used to calculate the opening degree EVdc after the operation capacity change of the downstream side expansion valve (the first expansion valve 24 during the heating operation or the second expansion valve 26 during the cooling operation).
- the opening degree EVdc calculated in step ST16 and the opening degree EVFFc calculated in step ST18 are substituted into the expression ⁇ 19> similar to the expression ⁇ 5> in the above-described feedforward control (see FIG. 4).
- the opening degree EVdc after the operation capacity change of the downstream side expansion valve is calculated.
- step ST20 the opening changing unit 83b of the feedforward control unit 83 changes the opening of the two expansion valves 24 and 26 to the opening EVuc and EVdc calculated in step ST16 and step ST19. I do.
- step ST11 each time the operating capacity of the compressor 21 and / or the outdoor fan 36 is changed, the process of steps ST12 to ST20 is performed. In this way, feedforward control of the two expansion valves 24 and 26 is performed.
- a sensor for detecting the intermediate pressure Pm In the feedforward control of the two expansion valves 24 and 26 according to the present modification, as in the feedforward control of the two expansion valves 24 and 26 (see FIG. 4), a sensor for detecting the intermediate pressure Pm. Without providing the above, it is possible to perform feedforward control of the upstream expansion valve and the downstream expansion valve by predicting a change in the refrigerant circulation amount passing through the upstream expansion valve and the downstream expansion valve. And when the operating capacity of the compressor 21 or the outdoor fan 36 changes, the control followability of the opening degree of the upstream side expansion valve and the downstream side expansion valve can be improved.
- the opening degree control of the upstream side expansion valve and the downstream side expansion valve the feedback control based on the degree of supercooling and the degree of superheat is performed together with the above-described feedforward control (see FIG. 5).
- the opening degree of the upstream side expansion valve and the downstream side expansion valve is brought close to the optimum opening degree after the change of the operating capacity of the compressor 21 and the outdoor fan 36 by feedforward control. After that, the optimum opening degree can be matched by feedback control.
- the present invention is widely applied to an air conditioner that circulates a refrigerant while expanding a high-pressure refrigerant discharged from a compressor by an upstream expansion valve and a downstream expansion valve in two stages in the order of intermediate pressure and low pressure. Is possible.
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Abstract
Description
本発明は、空気調和装置、特に、上流側膨張弁及び下流側膨張弁によって圧縮機から吐出された高圧の冷媒を中間圧、低圧の順に2段階で膨張させつつ冷媒の循環を行う空気調和装置に関する。 The present invention relates to an air conditioner, and more particularly, an air conditioner that circulates a refrigerant while expanding a high-pressure refrigerant discharged from a compressor by an upstream expansion valve and a downstream expansion valve in two stages in the order of intermediate pressure and low pressure. About.
従来より、特許文献1(特開平10-132393号公報)に示すように、上流側膨張弁及び下流側膨張弁によって圧縮機から吐出された高圧の冷媒を中間圧、低圧の順に2段階で膨張させつつ冷媒の循環を行う冷媒回路を有する空気調和装置がある。具体的には、空気調和装置の冷媒回路は、圧縮機、室外熱交換器、2つの膨張弁、室内熱交換器が接続されることによって構成されている。 Conventionally, as shown in Patent Document 1 (Japanese Patent Laid-Open No. 10-132393), high-pressure refrigerant discharged from a compressor by an upstream expansion valve and a downstream expansion valve is expanded in two stages in the order of intermediate pressure and low pressure. There is an air conditioner having a refrigerant circuit that circulates a refrigerant while allowing the refrigerant to circulate. Specifically, the refrigerant circuit of the air conditioner is configured by connecting a compressor, an outdoor heat exchanger, two expansion valves, and an indoor heat exchanger.
また、特許文献2(特開2003-106683号公報)に示すように、膨張弁の開度制御として、圧縮機の運転容量変化の前後の高圧及び低圧(膨張弁の入口及び出口における冷媒の圧力に対応)を予測して、このような予測値に基づいて膨張弁の開度を変化させるフィードフォワード制御を行う空気調和装置がある。 Further, as shown in Patent Document 2 (Japanese Patent Laid-Open No. 2003-106683), as control of the opening degree of the expansion valve, high pressure and low pressure before and after the change of the operating capacity of the compressor (pressure of the refrigerant at the inlet and outlet of the expansion valve) There is an air conditioner that performs feedforward control in which the opening degree of the expansion valve is changed based on such a predicted value.
ここで、特許文献1に示される2段膨張の冷媒回路を有する空気調和装置において、特許文献2のような膨張弁のフィードフォワード制御を適用することが考えられる。
Here, in the air conditioner having the two-stage expansion refrigerant circuit shown in Patent Document 1, it is conceivable to apply the feedforward control of the expansion valve as in
このとき、2段膨張の冷媒回路を構成する2つの膨張弁のそれぞれについてフィードフォワード制御を行うために、圧縮機の運転容量変化の前後の膨張弁の入口及び出口における冷媒の圧力を予測する必要がある。そして、このような予測においては、冷凍サイクルにおける高圧及び低圧だけでなく、2つの膨張弁の間の冷媒の圧力である冷凍サイクルにおける中間圧を知る必要がある。 At this time, in order to perform feedforward control for each of the two expansion valves constituting the refrigerant circuit of the two-stage expansion, it is necessary to predict the refrigerant pressure at the inlet and outlet of the expansion valve before and after the change in the operation capacity of the compressor There is. In such prediction, it is necessary to know not only the high pressure and low pressure in the refrigeration cycle, but also the intermediate pressure in the refrigeration cycle, which is the pressure of the refrigerant between the two expansion valves.
しかし、中間圧を検出するためのセンサを設けるとコストアップが発生することになるため、中間圧を検出するためのセンサを設けることなく、2つの膨張弁のフィードフォワード制御を行えるようにすることが望ましい。 However, if a sensor for detecting the intermediate pressure is provided, the cost increases. Therefore, it is possible to perform feed-forward control of the two expansion valves without providing a sensor for detecting the intermediate pressure. Is desirable.
本発明の課題は、2段膨張の冷媒回路を有する空気調和装置において、中間圧を検出するためのセンサを設けることなく、2つの膨張弁のフィードフォワード制御を行うことができるようにすることにある。 An object of the present invention is to enable feed-forward control of two expansion valves without providing a sensor for detecting an intermediate pressure in an air conditioner having a refrigerant circuit with two-stage expansion. is there.
第1の観点にかかる空気調和装置は、圧縮機、室外熱交換器、上流側膨張弁、下流側膨張弁、室内熱交換器が接続されることによって構成されており上流側膨張弁及び下流側膨張弁によって圧縮機から吐出された高圧の冷媒を中間圧、低圧の順に2段階で膨張させつつ冷媒の循環を行う冷媒回路と、室外熱交換器に冷却源又は加熱源となる室外空気を供給する室外ファンとを有する空気調和装置である。そして、ここでは、高圧から中間圧を差し引いた高圧側圧力差と中間圧から低圧を差し引いた低圧側圧力差との相関関係に基づく予測条件にて、圧縮機の運転容量、及び/又は、室外ファンの運転容量を変化させた後における上流側膨張弁及び下流側膨張弁を通過する冷媒循環量の変化を予測して、圧縮機の運転容量、及び/又は、室外ファンの運転容量を変化させた際に、予測された冷媒循環量の変化を加味して上流側膨張弁及び下流側膨張弁の開度を変化させる制御を行う。 An air conditioner according to a first aspect is configured by connecting a compressor, an outdoor heat exchanger, an upstream expansion valve, a downstream expansion valve, and an indoor heat exchanger, and includes an upstream expansion valve and a downstream side. A refrigerant circuit that circulates the refrigerant while expanding the high-pressure refrigerant discharged from the compressor by an expansion valve in two steps in the order of intermediate pressure and low pressure, and outdoor air that serves as a cooling source or heating source is supplied to the outdoor heat exchanger It is an air conditioner having an outdoor fan. And here, the operating capacity of the compressor and / or the outdoor under the prediction condition based on the correlation between the high pressure side pressure difference obtained by subtracting the intermediate pressure from the high pressure and the low pressure side pressure difference obtained by subtracting the low pressure from the intermediate pressure. Predicting changes in the amount of refrigerant circulating through the upstream and downstream expansion valves after changing the fan operating capacity, change the operating capacity of the compressor and / or the outdoor fan. In this case, control is performed to change the opening degree of the upstream side expansion valve and the downstream side expansion valve in consideration of the predicted change in the refrigerant circulation amount.
ここでは、上流側膨張弁及び下流側膨張弁のフィードフォワード制御を行うに当たり、高圧側圧力差と低圧側圧力差との相関関係に基づく予測条件にて、圧縮機や室外ファンの運転容量を変化させた後における上流側膨張弁及び下流側膨張弁を通過する冷媒循環量の変化を予測するようにしている。 Here, when performing feedforward control of the upstream side expansion valve and downstream side expansion valve, the operating capacity of the compressor or outdoor fan is changed under a prediction condition based on the correlation between the high pressure side pressure difference and the low pressure side pressure difference. The change of the refrigerant circulation amount passing through the upstream side expansion valve and the downstream side expansion valve after being made is predicted.
これにより、ここでは、中間圧を検出するためのセンサを設けることなく、上流側膨張弁及び下流側膨張弁を通過する冷媒循環量の変化を予測して、上流側膨張弁及び下流側膨張弁のフィードフォワード制御を行うことができる。そして、圧縮機や室外ファンの運転容量が変化する際に、上流側膨張弁及び下流側膨張弁の開度の制御追従性を向上させることができる。 Thereby, here, without providing a sensor for detecting the intermediate pressure, a change in the refrigerant circulation amount passing through the upstream expansion valve and the downstream expansion valve is predicted, and the upstream expansion valve and the downstream expansion valve are predicted. Feedforward control can be performed. And when the operating capacity of a compressor or an outdoor fan changes, the control followability of the opening degree of an upstream side expansion valve and a downstream side expansion valve can be improved.
第2の観点にかかる空気調和装置は、第1の観点にかかる空気調和装置において、相関関係が、圧縮機の運転容量、及び/又は、室外ファンの運転容量を変化させた前後において、高圧側圧力差と低圧側圧力差との比率が一定であるという関係である。 The air conditioner according to the second aspect is the air conditioner according to the first aspect, wherein the correlation is before and after the operating capacity of the compressor and / or the operating capacity of the outdoor fan is changed. The relationship between the pressure difference and the low pressure side pressure difference is constant.
第3の観点にかかる空気調和装置は、第1の観点にかかる空気調和装置において、相関関係が、圧縮機の運転容量、及び/又は、室外ファンの運転容量を変化させた前後において、高圧側圧力差が一定であるという関係である。 The air conditioner according to the third aspect is the air conditioner according to the first aspect, wherein the correlation is before and after the operating capacity of the compressor and / or the operating capacity of the outdoor fan is changed. The relationship is that the pressure difference is constant.
第4の観点にかかる空気調和装置は、第1~第3の観点のいずれかにかかる空気調和装置において、上流側膨張弁が、室外熱交換器及び室内熱交換器のうち冷媒の放熱器として機能する熱交換器の出口における冷媒の過冷却度が所定の目標過冷却度になるように開度制御され、下流側膨張弁が、室外熱交換器及び室内熱交換器のうち冷媒の蒸発器として機能する熱交換器の出口における冷媒の過熱度が所定の目標過熱度になるように開度制御される。 An air conditioner according to a fourth aspect is the air conditioner according to any one of the first to third aspects, wherein the upstream side expansion valve serves as a radiator radiator of the outdoor heat exchanger and the indoor heat exchanger. The opening degree is controlled so that the degree of subcooling of the refrigerant at the outlet of the functioning heat exchanger becomes a predetermined target degree of subcooling, and the downstream expansion valve is an evaporator of the refrigerant among the outdoor heat exchanger and the indoor heat exchanger. The degree of opening is controlled so that the degree of superheat of the refrigerant at the outlet of the heat exchanger that functions as a predetermined target superheat degree.
ここでは、上流側膨張弁及び下流側膨張弁の開度制御として、フィードフォワード制御とともに、過冷却度や過熱度に基づくフィードバック制御を行うようにしている。このため、ここでは、圧縮機や室外ファンの運転容量が変化する際に、上流側膨張弁及び下流側膨張弁の開度を、フィードフォワード制御によって、圧縮機や室外ファンの運転容量の変化後の最適な開度に予め近づけた後に、フィードバック制御によって、最適な開度に一致させることができる。 Here, as the opening degree control of the upstream side expansion valve and the downstream side expansion valve, feedback control based on the degree of supercooling and the degree of superheat is performed together with feedforward control. Therefore, here, when the operating capacities of the compressor and the outdoor fan change, the opening degree of the upstream expansion valve and the downstream expansion valve is adjusted by feedforward control after the operating capacities of the compressor and the outdoor fan change. Can be made to coincide with the optimum opening degree by feedback control after being brought close to the optimum opening degree in advance.
これにより、ここでは、上流側膨張弁及び下流側膨張弁のフィードバック制御に要する時間を効果的に短縮することができる。そして、圧縮機や室外ファンの運転容量が変化する際に、上流側膨張弁及び下流側膨張弁の開度の制御追従性を向上させることができる。 Thereby, here, the time required for feedback control of the upstream side expansion valve and the downstream side expansion valve can be effectively shortened. And when the operating capacity of a compressor or an outdoor fan changes, the control followability of the opening degree of an upstream side expansion valve and a downstream side expansion valve can be improved.
以下、本発明にかかる空気調和装置の実施形態及びその変形例について、図面に基づいて説明する。尚、本発明にかかる空気調和装置の具体的な構成は、下記の実施形態及びその変形例に限られるものではなく、発明の要旨を逸脱しない範囲で変更可能である。 Hereinafter, embodiments of the air-conditioning apparatus according to the present invention and modifications thereof will be described with reference to the drawings. In addition, the specific structure of the air conditioning apparatus concerning this invention is not restricted to the following embodiment and its modification, It can change in the range which does not deviate from the summary of invention.
(1)空気調和装置の構成
図1は、本発明の一実施形態にかかる空気調和装置1の概略構成図である。
(1) Configuration of Air Conditioner FIG. 1 is a schematic configuration diagram of an air conditioner 1 according to an embodiment of the present invention.
空気調和装置1は、蒸気圧縮式の冷凍サイクルを行うことによって、建物等の室内の冷房及び暖房を行うことが可能な装置である。空気調和装置1は、主として、室外ユニット2と、室内ユニット4とが接続されることによって構成されている。ここで、室外ユニット2と室内ユニット4とは、液冷媒連絡管5及びガス冷媒連絡管6を介して接続されている。すなわち、空気調和装置1の蒸気圧縮式の冷媒回路10は、室外ユニット2と、室内ユニット4とが冷媒連絡管5、6を介して接続されることによって構成されている。また、この冷媒回路10に封入される冷媒としては、種々のものが使用可能であるが、ここでは、冷媒として、HFC系冷媒の一種であるR32が封入されている。
The air conditioner 1 is a device that can cool and heat a room such as a building by performing a vapor compression refrigeration cycle. The air conditioner 1 is mainly configured by connecting an
<室内ユニット>
室内ユニット4は、室内に設置されており、冷媒回路10の一部を構成している。室内ユニット4は、主として、室内熱交換器41を有している。
<Indoor unit>
The
室内熱交換器41は、冷房運転時には冷媒の蒸発器として機能して室内空気を冷却し、暖房運転時には冷媒の放熱器として機能して室内空気を加熱する熱交換器である。室内熱交換器41の液側は液冷媒連絡管5に接続されており、室内熱交換器41のガス側はガス冷媒連絡管6に接続されている。
The indoor heat exchanger 41 is a heat exchanger that functions as a refrigerant evaporator during cooling operation to cool room air, and functions as a refrigerant radiator during heating operation to heat indoor air. The liquid side of the indoor heat exchanger 41 is connected to the liquid
室内ユニット4は、室内ユニット4内に室内空気を吸入して、室内熱交換器41において冷媒と熱交換させた後に、供給空気として室内に供給するための室内ファン42を有している。室内ファン42は、室内ファン用モータ43によって駆動される。
The
室内ユニット4には、各種のセンサが設けられている。具体的には、室内熱交換器41には、室内熱交換器41の液側における冷媒の温度Trrlを検出する室内熱交液側温度センサ57と、室内熱交換器41の中間部分における冷媒の温度Trrmを検出する室内熱交中間温度センサ58とが設けられている。室内ユニット4には、室内ユニット4内に吸入される室内空気の温度Traを検出する室内温度センサ59が設けられている。
The
室内ユニット4は、室内ユニット4を構成する各部の動作を制御する室内側制御部44を有している。そして、室内側制御部44は、室内ユニット4の制御を行うために設けられたマイクロコンピュータやメモリ等を有しており、リモコン(図示せず)との間で制御信号等のやりとりを行ったり、室外ユニット2との間で伝送線8aを介して制御信号等のやりとりを行うことができるようになっている。
The
<室外ユニット>
室外ユニット2は、室外に設置されており、冷媒回路10の一部を構成している。室外ユニット2は、主として、圧縮機21と、四路切換弁22と、室外熱交換器23と、第1膨張弁24と、レシーバ25と、第2膨張弁26と、液側閉鎖弁27と、ガス側閉鎖弁28とを有している。
<Outdoor unit>
The
圧縮機21は、冷凍サイクルにおける低圧の冷媒を高圧になるまで圧縮する機器である。圧縮機21は、ロータリ式やスクロール式等の容積式の圧縮要素(図示せず)をインバータにより周波数制御される圧縮機用モータ21aによって駆動する密閉式構造となっている。これにより、圧縮機21は、その運転容量が可変に構成されている。圧縮機21は、吸入側に吸入管31が接続されており、吐出側に吐出管32が接続されている。吸入管31は、圧縮機21の吸入側と四路切換弁22の第1ポート22aとを接続する冷媒管である。吸入管31には、アキュムレータ29が設けられている。吐出管32は、圧縮機21の吐出側と四路切換弁22の第2ポート22bとを接続する冷媒管である。吐出管32には、逆止弁32aが設けられている。
The
四路切換弁22は、冷媒回路10における冷媒の流れの方向を切り換えるための切換弁である。四路切換弁22は、冷房運転時には、室外熱交換器23を圧縮機21において圧縮された冷媒の放熱器として機能させ、かつ、室内熱交換器41を室外熱交換器23において放熱した冷媒の蒸発器として機能させる冷房サイクル状態への切り換えを行う。すなわち、四路切換弁22は、冷房運転時には、第2ポート22bと第3ポート22cとを連通させ、かつ、第1ポート22aと第4ポート22dとを連通させる切り換えを行う。これにより、圧縮機21の吐出側(ここでは、吐出管32)と室外熱交換器23のガス側(ここでは、第1ガス冷媒管33)とが接続される(図1の四路切換弁22の実線を参照)。しかも、圧縮機21の吸入側(ここでは、吸入管31)とガス冷媒連絡管6側(ここでは、第2ガス冷媒管34)とが接続される(図1の四路切換弁22の実線を参照)。また、四路切換弁22は、暖房運転時には、室外熱交換器23を室内熱交換器41において放熱した冷媒の蒸発器として機能させ、かつ、室内熱交換器41を圧縮機21において圧縮された冷媒の放熱器として機能させる暖房サイクル状態への切り換えを行う。すなわち、四路切換弁22は、暖房運転時には、第2ポート22bと第4ポート22dとを連通させ、かつ、第1ポート22aと第3ポート22cとを連通させる切り換えを行う。これにより、圧縮機21の吐出側(ここでは、吐出管32)とガス冷媒連絡管6側(ここでは、第2ガス冷媒管34)とが接続される(図1の四路切換弁22の破線を参照)。しかも、圧縮機21の吸入側(ここでは、吸入管31)と室外熱交換器23のガス側(ここでは、第1ガス冷媒管33)とが接続される(図1の四路切換弁22の破線を参照)。第1ガス冷媒管33は、四路切換弁22の第3ポート22cと室外熱交換器23のガス側とを接続する冷媒管である。第2ガス冷媒管33は、四路切換弁22の第4ポート22dとガス冷媒連絡管6側とを接続する冷媒管である。
The four-
室外熱交換器23は、冷房運転時には室外空気を冷却源とする冷媒の放熱器として機能し、暖房運転時には室外空気を加熱源とする冷媒の蒸発器として機能する熱交換器である。室外熱交換器23は、液側が液冷媒管35に接続されており、ガス側が第1ガス冷媒管33に接続されている。液冷媒管35は、室外熱交換器23の液側と液冷媒連絡管5側とを接続する冷媒管である。
The
第1膨張弁24は、冷房運転時には、圧縮機21から吐出された冷媒を2段階で膨張させるための上流側膨張弁として機能し、室外熱交換器23において放熱した冷凍サイクルにおける高圧の冷媒を冷凍サイクルにおける中間圧まで減圧する弁である。また、第1膨張弁24は、暖房運転時には、圧縮機21から吐出された冷媒を2段階で膨張させるための下流側膨張弁として機能し、レシーバ25に溜められた冷凍サイクルにおける中間圧の冷媒を冷凍サイクルにおける低圧まで減圧する弁である。第1膨張弁24は、液冷媒管35のうち室外熱交換器23とレシーバ25との間の部分に設けられている。
The
レシーバ25は、第1膨張弁24と第2膨張弁26との間(すなわち、上流側膨張弁と下流側膨張弁との間)に設けられている。レシーバ25は、冷房運転時及び暖房運転時には、冷凍サイクルにおける中間圧の冷媒を溜めることが可能な容器である。
The
第2膨張弁26は、冷房運転時には、圧縮機21から吐出された冷媒を2段階で膨張させるための下流側膨張弁として機能し、レシーバ25に溜められた冷凍サイクルにおける中間圧の冷媒を冷凍サイクルにおける低圧まで減圧する弁である。また、第2膨張弁26は、暖房運転時には、圧縮機21から吐出された冷媒を2段階で膨張させるための上流側膨張弁として機能し、室内熱交換器41において放熱した冷凍サイクルにおける高圧の冷媒を冷凍サイクルにおける中間圧まで減圧する弁である。第2膨張弁26は、液冷媒管35のうちレシーバ25と液側閉鎖弁27との間の部分に設けられている。
The
液側閉鎖弁27及びガス側閉鎖弁28は、外部の機器・配管(具体的には、液冷媒連絡管5及びガス冷媒連絡管6)との接続口に設けられた弁である。液側閉鎖弁27は、液冷媒管35の端部に設けられている。ガス側閉鎖弁28は、第2ガス冷媒管34の端部に設けられている。
The liquid side shut-off
室外ユニット2は、室外ユニット2内に室外空気を吸入して、室外熱交換器23において冷媒と熱交換させた後に、外部に排出するための室外ファン36を有している。室外ファン36は、回転数を制御することが可能な室外ファン用モータ37によって駆動される。これにより、室外ファン36は、その運転容量が可変に構成されている。
The
室外ユニット2には、各種のセンサが設けられている。具体的には、吸入管31には、圧縮機21に吸入される冷凍サイクルにおける低圧の冷媒の温度Tsを検出する吸入温度センサ51が設けられている。吐出管32には、圧縮機21から吐出される冷凍サイクルにおける高圧の冷媒の温度Tdを検出する吐出温度センサ52が設けられている。室外熱交換器23には、室外熱交換器23の中間部分における冷媒の温度Tormを検出する室外熱交中間温度センサ53と、室外熱交換器23の液側における冷媒の温度Torlを検出する室外熱交液側温度センサ54とが設けられている。室外ユニット2には、室外ユニット2内に吸入される室外空気の温度Toaを検出する室外温度センサ55が設けられている。液冷媒管35には、第2膨張弁26と液側閉鎖弁27との間の部分における冷媒の液管温度Tlpを検出する液管温度センサ56が設けられている。
The
室外ユニット2は、室外ユニット2を構成する各部の動作を制御する室外側制御部38を有している。そして、室外側制御部38は、室外ユニット2の制御を行うために設けられたマイクロコンピュータやメモリ等を有しており、室内ユニット4との間で伝送線8aを介して制御信号等のやりとりを行うことができるようになっている。
The
<冷媒連絡管>
冷媒連絡管5、6は、空気調和装置1を建物等の設置場所に設置する際に、現地にて施工される冷媒管であり、設置場所や室外ユニットと室内ユニットとの組み合わせ等の設置条件に応じて種々の長さや管径を有するものが使用される。
<Refrigerant communication pipe>
以上のように、室外ユニット2と、室内ユニット4と、冷媒連絡管5、6とが接続されることによって、空気調和装置1の冷媒回路10が構成されている。空気調和装置1の冷媒回路10は、四路切換弁22を冷房サイクル状態に切り換えることで、圧縮機21、室外熱交換器23、上流側膨張弁としての第1膨張弁24、下流側膨張弁としての第2膨張弁26、室内熱交換器41が接続されるようになっており、上流側膨張弁としての第1膨張弁24及び下流側膨張弁としての第2膨張弁26によって圧縮機21から吐出された高圧の冷媒を中間圧、低圧の順に2段階で膨張させつつ冷媒を循環させる冷房運転を行うようになっている。また、空気調和装置1の冷媒回路10は、四路切換弁22を暖房サイクル状態に切り換えることで、圧縮機21、室内熱交換器41、上流側膨張弁としての第2膨張弁26、下流側膨張弁としての第1膨張弁24、室外熱交換器23が接続されるようになっており、上流側膨張弁としての第2膨張弁26及び下流側膨張弁としての第1膨張弁24によって圧縮機21から吐出された高圧の冷媒を中間圧、低圧の順に2段階で膨張させつつ冷媒を循環させる暖房運転を行うようになっている。また、空気調和装置1は、室外熱交換器23に冷却源又は加熱源となる室外空気を供給する室外ファン36を有している。
As described above, the refrigerant circuit 10 of the air conditioner 1 is configured by connecting the
<制御部>
空気調和装置1は、室内側制御部44と室外側制御部38とから構成される制御部8によって、室外ユニット2及び室内ユニット4の各機器の制御を行うことができるようになっている。すなわち、室内側制御部44と室外側制御部38との間を接続する伝送線8aとによって、上記の冷房運転や暖房運転等を含む空気調和装置1全体の運転制御を行う制御部8が構成されている。そして、制御部8は、図2に示すように、各種センサ51~59等の検出信号を受けることができるように接続されるとともに、これらの検出信号等に基づいて各種機器及び弁21a、22、24、26、37、43等を制御することができるように接続されている。
<Control unit>
The air conditioner 1 can control each device of the
(2)空気調和装置の基本動作
次に、空気調和装置1の基本動作について、図1を用いて説明する。空気調和装置1は、基本動作として、冷房運転及び暖房運転を行うことが可能である。
(2) Basic operation | movement of an air conditioning apparatus Next, the basic operation | movement of the air conditioning apparatus 1 is demonstrated using FIG. The air conditioner 1 can perform a cooling operation and a heating operation as basic operations.
<暖房運転>
暖房運転時には、四路切換弁22が暖房サイクル状態(図1の破線で示される状態)に切り換えられる。
<Heating operation>
During the heating operation, the four-
冷媒回路10において、冷凍サイクルにおける低圧のガス冷媒は、圧縮機21に吸入され、冷凍サイクルにおける高圧になるまで圧縮された後に吐出される。
In the refrigerant circuit 10, the low-pressure gas refrigerant in the refrigeration cycle is sucked into the
圧縮機21から吐出された高圧のガス冷媒は、四路切換弁22、ガス側閉鎖弁28及びガス冷媒連絡管6を通じて、室内熱交換器41に送られる。
The high-pressure gas refrigerant discharged from the
室内熱交換器41に送られた高圧のガス冷媒は、室内熱交換器41において、室内ファン42によって冷却源として供給される室内空気と熱交換を行って放熱して、高圧の液冷媒になる。これにより、室内空気は加熱され、その後に、室内に供給されることで室内の暖房が行われる。
The high-pressure gas refrigerant sent to the indoor heat exchanger 41 radiates heat by exchanging heat with indoor air supplied as a cooling source by the
室内熱交換器41で放熱した高圧の液冷媒は、液冷媒連絡管5及び液側閉鎖弁27を通じて、上流側膨張弁としての第2膨張弁26に送られる。
The high-pressure liquid refrigerant radiated by the indoor heat exchanger 41 is sent to the
第2膨張弁26に送られた高圧の液冷媒は、第2膨張弁26によって冷凍サイクルにおける中間圧まで減圧されて、中間圧の気液二相状態の冷媒になる。
The high-pressure liquid refrigerant sent to the
第2膨張弁26で減圧された中間圧の気液二相状態の冷媒は、レシーバ25に一時的に溜められた後に、下流側膨張弁としての第1膨張弁24に送られる。
The intermediate-pressure gas-liquid two-phase refrigerant decompressed by the
第1膨張弁24に送られた中間圧の気液二相状態の冷媒は、第1膨張弁24によって冷凍サイクルにおける低圧まで減圧されて、低圧の気液二相状態の冷媒になる。
The intermediate-pressure gas-liquid two-phase refrigerant sent to the
第1膨張弁24で減圧された低圧の気液二相状態の冷媒は、室外熱交換器23に送られる。
The low-pressure gas-liquid two-phase refrigerant decompressed by the
室外熱交換器23に送られた低圧の気液二相状態の冷媒は、室外熱交換器23において、室外ファン36によって加熱源として供給される室外空気と熱交換を行って蒸発して、低圧のガス冷媒になる。
The low-pressure gas-liquid two-phase refrigerant sent to the
室外熱交換器23で蒸発した低圧の冷媒は、四路切換弁22を通じて、再び、圧縮機21に吸入される。
The low-pressure refrigerant evaporated in the
このような暖房運転時において、制御部8は、室内ユニット4の要求暖房負荷に応じて、圧縮機21や室外ファン36の運転容量の制御を行い、また、膨張弁24、26の開度制御も行っている。尚、圧縮機21や室外ファン36の運転容量の制御、及び、膨張弁24、26の開度制御については、後述するものとする。
During such heating operation, the
<冷房運転>
冷房運転時には、四路切換弁22が冷房サイクル状態(図1の実線で示される状態)に切り換えられる。
<Cooling operation>
During the cooling operation, the four-
冷媒回路10において、冷凍サイクルにおける低圧のガス冷媒は、圧縮機21に吸入され、冷凍サイクルにおける高圧になるまで圧縮された後に吐出される。
In the refrigerant circuit 10, the low-pressure gas refrigerant in the refrigeration cycle is sucked into the
圧縮機21から吐出された高圧のガス冷媒は、四路切換弁22を通じて、室外熱交換器23に送られる。
The high-pressure gas refrigerant discharged from the
室外熱交換器23に送られた高圧のガス冷媒は、室外熱交換器23において、室外ファン36によって冷却源として供給される室外空気と熱交換を行って放熱して、高圧の液冷媒になる。
The high-pressure gas refrigerant sent to the
室外熱交換器23において放熱した高圧の液冷媒は、上流側膨張弁としての第1膨張弁24に送られる。
The high-pressure liquid refrigerant that has radiated heat in the
第1膨張弁24に送られた高圧の液冷媒は、第1膨張弁24によって冷凍サイクルにおける中間圧まで減圧されて、中間圧の気液二相状態の冷媒になる。
The high-pressure liquid refrigerant sent to the
第1膨張弁24で減圧された中間圧の気液二相状態の冷媒は、レシーバ25に一時的に溜められた後に、下流側膨張弁としての第2膨張弁26に送られる。
The intermediate-pressure gas-liquid two-phase refrigerant decompressed by the
第2膨張弁26に送られた中間圧の気液二相状態の冷媒は、第2膨張弁26によって冷凍サイクルにおける低圧まで減圧されて、低圧の気液二相状態の冷媒になる。
The intermediate-pressure gas-liquid two-phase refrigerant sent to the
第2膨張弁26で減圧された低圧の気液二相状態の冷媒は、液側閉鎖弁27及び液冷媒連絡管5を通じて、室内熱交換器41に送られる。
The low-pressure gas-liquid two-phase refrigerant decompressed by the
室内熱交換器41に送られた低圧の気液二相状態の冷媒は、室内熱交換器41において、室内ファン42によって加熱源として供給される室内空気と熱交換を行って蒸発する。これにより、室内空気は冷却され、その後に、室内に供給されることで室内の冷房が行われる。
The low-pressure gas-liquid two-phase refrigerant sent to the indoor heat exchanger 41 evaporates in the indoor heat exchanger 41 by exchanging heat with indoor air supplied as a heating source by the
室内熱交換器41において蒸発した低圧のガス冷媒は、ガス冷媒連絡管6、ガス側閉鎖弁28及び四路切換弁22を通じて、再び、圧縮機21に吸入される。
The low-pressure gas refrigerant evaporated in the indoor heat exchanger 41 is again sucked into the
このような冷房運転時において、制御部8は、室内ユニット4の要求暖房負荷に応じて、圧縮機21や室外ファン36の運転容量の制御を行い、また、膨張弁24、26の開度制御も行っている。尚、圧縮機21や室外ファン36の運転容量の制御、及び、2つの膨張弁24、26の開度制御については、後述するものとする。
During such cooling operation, the
(3)圧縮機、室外ファン及び2つの膨張弁の制御
次に、圧縮機21、室外ファン36及び2つの膨張弁24、26の制御について、図1~図5を用いて説明する。
(3) Control of Compressor, Outdoor Fan, and Two Expansion Valves Next, control of the
<圧縮機、室外ファンの運転容量の制御>
圧縮機21及び/又は室外ファン36の運転容量の制御は、図3に示すように、制御部8の容量制御部82によって行われる。容量制御部82は、冷媒回路10の冷凍サイクルにおける低圧や高圧が目標値になるように、圧縮機21及び/又は室外ファン36の運転容量を制御する。ここで、冷媒回路10の冷凍サイクルにおける低圧や高圧(又は、低圧や高圧に相当する蒸発温度や凝縮温度)の目標値は、図3に示すように、制御部8の目標値決定部81によって設定される。以下、冷房運転時と暖房運転時とに分けて、圧縮機21及び/又は室外ファン36の運転容量の制御について説明する。
<Control of operating capacity of compressor and outdoor fan>
Control of the operating capacity of the
-暖房運転時-
暖房運転において、目標値決定部81は、リモコン(図示せず)等から入力される室内の設定温度Ttと、室内熱交中間温度センサ58によって検出される室内熱交換器41における冷媒の温度Trrm(ここでは、冷媒回路10の冷凍サイクルにおける高圧に相当する凝縮温度Tcに対応)とに基づいて、凝縮温度Tcの目標値である目標凝縮温度Tcsを設定する。例えば、設定温度Ttから室内熱交換器41における冷媒の温度Trrmを差し引いた温度差が大きい場合には、暖房能力を大きくする必要があるため、目標凝縮温度Tcsが高くなるように設定される。また、設定温度Ttから室内熱交換器41における冷媒の温度Trrmを差し引いた温度差が小さい場合には、暖房能力を小さくする必要があるため、目標凝縮温度Tcsが低くなるように設定される。
-During heating operation-
In the heating operation, the target
そして、容量制御部82は、冷媒回路10の冷凍サイクルにおける高圧に相当する凝縮温度Tcが目標値決定部81によって設定された目標凝縮温度Tcsになるように、圧縮機用モータ21aの周波数を変更することによって圧縮機21の運転容量を制御する。例えば、凝縮温度Tcが目標凝縮温度Tcsよりも低い場合には、圧縮機用モータ21aの周波数を大きくすることによって圧縮機21の運転容量を増加させる方向に変更する。また、凝縮温度Tcが目標凝縮温度Tcsよりも高い場合には、圧縮機用モータ21aの周波数を小さくすることによって圧縮機21の運転容量を減少させる方向に変更する。また、容量制御部82は、凝縮温度Tcが目標凝縮温度Tcsになるように、室外ファン用モータ37の回転数を変更することによって室外ファン36の運転容量を制御する。例えば、凝縮温度Tcが目標凝縮温度Tcsよりも低い場合には、室外ファン用モータ37の回転数を大きくすることによって室外ファン36の運転容量を増加させる方向に変更する。また、凝縮温度Tcが目標凝縮温度Tcsよりも高い場合には、室外ファン用モータ37の回転数を小さくすることによって室外ファン36の運転容量を減少させる方向に変更する。
The
尚、ここでは、容量制御部82が、圧縮機21及び室外ファン36の運転容量を制御しているが、圧縮機21の運転容量だけを制御してもよいし、又は、室外ファン36の運転容量だけを制御してもよい。
Here, the
-冷房運転時-
冷房運転において、目標値決定部81は、リモコン(図示せず)等から入力される室内の設定温度Ttと、室内熱交中間温度センサ58によって検出される室内熱交換器41における冷媒の温度Trrm(ここでは、冷媒回路10の冷凍サイクルにおける低圧に相当する蒸発温度Teに対応)とに基づいて、蒸発温度Teの目標値である目標蒸発温度Tesを設定する。例えば、室内熱交換器41における冷媒の温度Trrmから設定温度Ttを差し引いた温度差が大きい場合には、冷房能力を大きくする必要があるため、目標蒸発温度Tesが低くなるように設定される。また、室内熱交換器41における冷媒の温度Trrmから設定温度Ttを差し引いた温度差が小さい場合には、冷房能力を小さくする必要があるため、目標蒸発温度Tesが高くなるように設定される。
-During cooling operation-
In the cooling operation, the target
そして、容量制御部82は、冷媒回路10の冷凍サイクルにおける低圧に相当する蒸発温度Teが目標値決定部81によって設定された目標蒸発温度Tesになるように、圧縮機用モータ21aの周波数を変更することによって圧縮機21の運転容量を制御する。例えば、蒸発温度Teが目標蒸発温度Tesよりも高い場合には、圧縮機用モータ21aの周波数を大きくすることによって圧縮機21の運転容量を増加させる方向に変更する。また、蒸発温度Teが目標蒸発温度Tesよりも低い場合には、圧縮機用モータ21aの周波数を小さくすることによって圧縮機21の運転容量を減少させる方向に変更する。また、容量制御部82は、蒸発温度Teが目標蒸発温度Tesになるように、室外ファン用モータ37の回転数を変更することによって室外ファン36の運転容量を制御する。例えば、蒸発温度Teが目標蒸発温度Tesよりも高い場合には、室外ファン用モータ37の回転数を大きくすることによって室外ファン36の運転容量を増加させる方向に変更する。また、蒸発温度Teが目標蒸発温度Tesよりも低い場合には、室外ファン用モータ37の回転数を小さくすることによって室外ファン36の運転容量を減少させる方向に変更する。
Then, the
尚、ここでは、容量制御部82が、圧縮機21及び室外ファン36の運転容量を制御しているが、圧縮機21の運転容量だけを制御してもよいし、又は、室外ファン36の運転容量だけを制御してもよい。
Here, the
<膨張弁のフィードバック制御>
ここでは、2つの膨張弁24、26の開度制御として、後述のフィードフォワード制御とともに、過冷却度や過熱度に基づくフィードバック制御を行うようにしている。膨張弁24、26のフィードバック制御は、図3に示すように、制御部8のフィードバック制御部84によって行われる。フィードバック制御部84は、室外熱交換器23及び室内熱交換器41のうち冷媒の放熱器として機能する熱交換器の出口における冷媒の過冷却度が所定の目標過冷却度になるように、膨張弁24、26のうち上流側膨張弁として機能する膨張弁の開度を制御する。また、フィードバック制御部84は、室外熱交換器23及び室内熱交換器41のうち冷媒の蒸発器として機能する熱交換器の出口における冷媒の過熱度が所定の目標過熱度になるように、膨張弁24、26のうち下流側膨張弁として機能する膨張弁の開度を制御する。以下、冷房運転時と暖房運転時とに分けて、膨張弁24、26のフィードバック制御について説明する。
<Feedback control of expansion valve>
Here, as the opening control of the two
-暖房運転時-
暖房運転時において、フィードバック制御部84は、室内熱交換器41の出口における冷媒の過冷却度SCが目標過冷却度SCsになるように、レシーバ25の上流側に位置する上流側膨張弁としての第2膨張弁26の開度を制御する。例えば、過冷却度SCが目標過冷却度SCsよりも大きい場合には、室内熱交換器41を通過する冷媒の流量を増加させるために、第2膨張弁26の開度を大きくする方向に変更する。また、過冷却度SCが目標過冷却度SCsよりも小さい場合には、室内熱交換器41を通過する冷媒の流量を減少させるために、第2膨張弁26の開度を小さくする方向に変更する。ここで、室内熱交換器41の出口における冷媒の過冷却度SCは、室内熱交中間温度センサ58によって検出される冷媒の温度Trrmから室内熱交液側温度センサ57によって検出される冷媒の温度Trrlを差し引くことによって得られる。
-During heating operation-
During the heating operation, the
また、暖房運転時において、フィードバック制御84は、室外熱交換器23の出口における冷媒の過熱度SHが所定の目標過熱度SHsになるように、レシーバ25の下流側に位置する下流側膨張弁としての第1膨張弁24の開度を制御する。例えば、過熱度SHが目標過熱度SHsよりも大きい場合には、室外熱交換器23を通過する冷媒の流量を増加させるために、第1膨張弁24の開度を大きくする方向に変更する。また、過熱度SHが目標過熱度SHsよりも小さい場合には、室外熱交換器23を通過する冷媒の流量を減少させるために、第1膨張弁24の開度を小さくする方向に変更する。ここで、室外熱交換器23の出口における冷媒の過熱度SHは、吸入温度センサ51によって検出される冷媒の温度Tsから室外熱交中間温度センサ53によって検出される冷媒の温度Tormを差し引くことによって得られる。
Further, during the heating operation, the
尚、過冷却度SCや過熱度SHを得るためのセンサは、上記のものに限定されず、冷凍サイクルにおける高圧や低圧を検出するための圧力センサが設けられている場合、及び/又は、熱交換器及びその近傍に他の温度センサが設けられている場合には、これらのセンサの検出値を使用してもよい。 The sensor for obtaining the degree of supercooling SC and the degree of superheating SH is not limited to the above, and when a pressure sensor for detecting high pressure and low pressure in the refrigeration cycle is provided and / or heat When other temperature sensors are provided in the exchanger and in the vicinity thereof, detection values of these sensors may be used.
-冷房運転時-
冷房運転時において、フィードバック制御部84は、室外熱交換器23の出口における冷媒の過冷却度SCが目標過冷却度SCsになるように、レシーバ25の上流側に位置する上流側膨張弁としての第1膨張弁24の開度を制御する。例えば、過冷却度SCが目標過冷却度SCsよりも大きい場合には、室外熱交換器23を通過する冷媒の流量を増加させるために、第1膨張弁24の開度を大きくする方向に変更する。また、過冷却度SCが目標過冷却度SCsよりも小さい場合には、室外熱交換器23を通過する冷媒の流量を減少させるために、第1膨張弁24の開度を小さくする方向に変更する。ここで、室外熱交換器23の出口における冷媒の過冷却度SCは、室外熱交中間温度センサ53によって検出される冷媒の温度Tormから室外熱交液側温度センサ54によって検出される冷媒の温度Torlを差し引くことによって得られる。
-During cooling operation-
During the cooling operation, the
また、冷房運転時において、フィードバック制御84は、室内熱交換器41の出口における冷媒の過熱度SHが所定の目標過熱度SHsになるように、レシーバ25の下流側に位置する下流側膨張弁としての第2膨張弁26の開度を制御する。例えば、過熱度SHが目標過熱度SHsよりも大きい場合には、室内熱交換器41を通過する冷媒の流量を増加させるために、第2膨張弁26の開度を大きくする方向に変更する。また、過熱度SHが目標過熱度SHsよりも小さい場合には、室内熱交換器41を通過する冷媒の流量を減少させるために、第2膨張弁26の開度を小さくする方向に変更する。ここで、室内熱交換器41の出口における冷媒の過熱度SHは、吸入温度センサ51によって検出される冷媒の温度Tsから室内熱交中間温度センサ58によって検出される冷媒の温度Trrmを差し引くことによって得られる。
Further, during the cooling operation, the
尚、過冷却度SCや過熱度SHを得るためのセンサは、上記のものに限定されず、冷凍サイクルにおける高圧や低圧を検出するための圧力センサが設けられている場合、及び/又は、熱交換器及びその近傍に他の温度センサが設けられている場合には、これらのセンサの検出値を使用してもよい。 The sensor for obtaining the degree of supercooling SC and the degree of superheating SH is not limited to the above, and when a pressure sensor for detecting high pressure and low pressure in the refrigeration cycle is provided and / or heat When other temperature sensors are provided in the exchanger and in the vicinity thereof, detection values of these sensors may be used.
<膨張弁のフィードフォワード制御>
ここでは、2つの膨張弁24、26の開度制御として、圧縮機21の運転容量、及び/又は、室外ファン36の運転容量を変化させた際に、各膨張弁24、26を通過する冷媒循環量の変化を予測して、予測された冷媒循環量の変化を加味して上流側膨張弁及び下流側膨張弁としての2つの膨張弁24、26の開度を変化させるフィードフォワード制御を行うようにしている。膨張弁24、26のフィードフォワード制御は、図3に示すように、制御部8のフィードフォワード制御部83によって行われる。フィードフォワード制御部83は、予測部83aと開度変更部83bとを有している。予測部83aは、冷凍サイクルにおける高圧から冷凍サイクルにおける中間圧を差し引いた高圧側圧力差と中間圧から冷凍サイクルにおける低圧を差し引いた低圧側圧力差との相関関係に基づく予測条件にて、圧縮機21の運転容量、及び/又は、室外ファン36の運転容量を変化させた後における上流側膨張弁及び下流側膨張弁としての2つの膨張弁24、26を通過する冷媒循環量の変化を予測する。そして、予測部83aは、圧縮機21の運転容量、及び/又は、室外ファン36の運転容量を変化させた際に、予測された冷媒循環量の変化を加味して上流側膨張弁及び下流側膨張弁としての2つの膨張弁24、26の開度を算出する。そして、開度変更部83bは、上流側膨張弁及び下流側膨張弁としての2つの膨張弁24、26の開度を、予測部83aによって算出された開度に変更する制御を行う。以下、冷房運転時と暖房運転時とに分けて、膨張弁24、26のフィードフォワード制御について説明する。
<Feed-forward control of expansion valve>
Here, as the opening control of the two
-暖房運転時-
暖房運転時において、フィードフォワード制御部83は、図4に示すように、まず、圧縮機21の運転容量、及び/又は、室外ファン36の運転容量が変化するかどうかを判定する(ステップST1)。ここでは、圧縮機21及び/又は室外ファン36の運転容量は、上述の圧縮機21及び/又は室外ファン36の運転容量の制御によって変化する。このため、ステップST1において圧縮機21及び/又は室外ファン36の運転容量が変化するものと判定される場合とは、上述の圧縮機21及び/又は室外ファン36の運転容量の制御が行われることを意味する。そして、ステップST1において、圧縮機21及び/又は室外ファン36の運転容量が変化するものと判定された場合には、ステップST2~ST7の処理に移行する。
-During heating operation-
During the heating operation, the
次に、ステップST2において、フィードフォワード制御部83の予測部83aは、圧縮機21及び/又は室外ファン36の運転容量の制御が行われる直前(すなわち、運転容量が変化する直前)における2つの膨張弁24、26の開度EVu、EVdを合算した運転容量変化前の仮想合算開度EVFFを算出する。例えば、膨張弁24、26として開度とCv値とが比例する特性の膨張弁を採用する場合には、運転容量変化前の仮想合算開度EVFFは、次式<1>によって算出される。
Next, in step ST2, the
1/EVFF = 1/EVu +1/EVd ・・・<1>
ここで、EVuは、圧縮機21及び/又は室外ファン36の運転容量の制御が行われる直前(すなわち、運転容量が変化する直前)における上流側膨張弁(ここでは、第2膨張弁26)の開度(ここでは、最大開度が1となるように正規化した開度)である。また、EVdは、圧縮機21及び/又は室外ファン36の運転容量の制御が行われる直前(すなわち、運転容量が変化する直前)における下流側膨張弁(ここでは、第1膨張弁24)の開度(ここでは、最大開度が1となるように正規化した開度)である。
1 / EVFF = 1 / EVu + 1 / EVd (1)
Here, EVu is the value of the upstream side expansion valve (here, the second expansion valve 26) immediately before the operation capacity of the
次に、ステップST3において、予測部83aは、圧縮機21及び/又は室外ファン36の運転容量の制御が行われる直前(すなわち、運転容量が変化する直前)における2つの膨張弁24、26を通過する運転容量変化前の冷媒循環量Grを算出する。ここで、運転容量変化前の冷媒循環量Grは、次式<2>のように、ステップST2において算出された運転容量変化前の仮想合算開度EVFFの関数として表すことができる。
Next, in step ST3, the
Gr = f(EVFF) ・・・<2>
次に、ステップST4において、予測部83aは、圧縮機21及び/又は室外ファン36の運転容量の制御が行われた直後(すなわち、運転容量が変化した直後)における2つの膨張弁24、26を通過する運転容量変化後の冷媒循環量Grcを算出する。ここで、運転容量変化後の冷媒循環量Grcは、次式<3>のように、圧縮機21の運転容量の変化前後の運転容量比Fcc/Fc、室外ファン36の運転容量の変化前後の運転容量比Ffc/Ff、運転容量変化前の冷凍サイクルにおける凝縮温度Tc、運転容量変化前の冷凍サイクルにおける蒸発温度Te、及び、運転容量変化前の冷媒循環量Grの関数として表すことができる。
Gr = f (EVFF) (2)
Next, in step ST4, the
Grc = f(Fcc/Fc、Ffc/Ff、Tc、Te)×Gr ・・・<3>
ここで、Fccは、圧縮機21の運転容量の制御が行われた直後(すなわち、運転容量が変化した直後)における圧縮機21の運転容量であり、Fcは、圧縮機21の運転容量の制御が行われる直前(すなわち、運転容量が変化する直前)における圧縮機21の運転容量である。そして、ここでは、圧縮機21の運転容量の変化前後の運転容量比Fcc/Fcとして、圧縮機21の運転容量の変化前後の圧縮機用モータ21aの周波数比が使用されている。また、Ffcは、室外ファン36の運転容量の制御が行われた直後(すなわち、運転容量が変化した直後)における室外ファン36の運転容量であり、Ffは、室外ファン36の運転容量の制御が行われる直前(すなわち、運転容量が変化する直前)における室外ファン36の運転容量である。そして、ここでは、室外ファン36の運転容量の変化前後の運転容量比Ffc/Ffとして、室外ファン36の運転容量の変化前後の室外ファン用モータ37の回転数比が使用されている。また、運転容量変化前の冷凍サイクルにおける凝縮温度Tcとしては、暖房運転時においては、冷媒の凝縮器として機能する室内熱交換器41における冷媒の温度Trrmが使用され、運転容量変化前の冷凍サイクルにおける蒸発温度Teとしては、冷媒の蒸発器として機能する室内熱交換器23における冷媒の温度Tormが使用されている(冷房運転時は、温度Tormが凝縮温度Tcとなり、温度Trrmが蒸発温度Teとなる)。
Grc = f (Fcc / Fc, Ffc / Ff, Tc, Te) × Gr (3)
Here, Fcc is the operating capacity of the
次に、ステップST5において、予測部83aは、圧縮機21及び/又は室外ファン36の運転容量の制御が行われた直後(すなわち、運転容量が変化した直後)における2つの膨張弁24、26の開度(すなわち、運転容量変化後の上流側膨張弁の開度EVuc、及び、運転容量変化後の下流側膨張弁の開度EVdc)を合算した運転容量変化後の仮想合算開度EVFFcを算出する。ここで、運転容量変化後の仮想合算開度EVFFcは、次式<4>のように、ステップST4において算出された運転容量変化後の冷媒循環量Grcの関数として表すことができる。
Next, in step ST5, the
EVFFc = f(Grc) ・・・<4>
次に、ステップST6において、予測部83aは、ステップST5において算出された運転容量変化後の仮想合算開度EVFFcを用いて、2つの膨張弁24、26の運転容量変化後の開度EVuc、EVdcを算出する。
EVFFc = f (Grc) (4)
Next, in step ST6, the
ここで、2つの膨張弁24、26の運転容量変化後の開度EVuc、EVdcを算出するためには、第1膨張弁24の入口及び出口における冷媒の圧力、第2膨張弁26の入口及び出口における冷媒の圧力を予測する必要がある。このような予測においては、冷凍サイクルにおける高圧Ph及び低圧Plだけでなく、2つの膨張弁24、26の間の冷媒の圧力である冷凍サイクルにおける中間圧Pmを知る必要がある。
Here, in order to calculate the opening degree EVuc and EVdc after the operation capacity change of the two
しかし、ここでは、高圧Phに対応する凝縮温度Tc及び低圧Plに対応する蒸発温度Teを検出するためのセンサ53、58が設けられているが、中間圧Pmを検出するためのセンサが設けられていない。
However, here, the
そこで、ここでは、高圧Phから中間圧Pmを差し引いた高圧側圧力差ΔPhと中間圧Pmから低圧Plを差し引いた低圧側圧力差ΔPlとの相関関係に基づく予測条件を設定している。具体的には、この相関関係として、圧縮機21及び/又は室外ファン36の運転容量を変化させた前後において、高圧側圧力差ΔPhと低圧側圧力差ΔPlとの比率が一定であるという関係を設定している。
Therefore, here, a prediction condition is set based on the correlation between the high pressure side pressure difference ΔPh obtained by subtracting the intermediate pressure Pm from the high pressure Ph and the low pressure side pressure difference ΔP1 obtained by subtracting the low pressure Pl from the intermediate pressure Pm. Specifically, as this correlation, the relationship between the high pressure side pressure difference ΔPh and the low pressure side pressure difference ΔPl is constant before and after the operating capacity of the
すなわち、ここでは、次の2つの式<5>及び<6>と、ステップST5において算出された運転容量変化後の仮想合算開度EVFFcと、既知の運転容量変化前の開度EVu、EVdとを用いて、連立式を解くことで、2つの膨張弁24、26の運転容量変化後の開度EVuc、EVdcが算出されるようになっている。
That is, here, the following two formulas <5> and <6>, the virtual combined opening EVFFc after the operating capacity change calculated in step ST5, and the opening EVu and EVd before the known operating capacity change, Is used to calculate the opening degree EVuc and EVdc after the change of the operating capacity of the two
1/EVFFc = 1/EVuc +1/EVdc ・・・<5>
EVu:EVd = EVuc:EVdc ・・・<6>
次に、ステップST7において、フィードフォワード制御部83の開度変更部83bは、2つの膨張弁24、26の開度を、ステップST6において算出された開度EVuc、EVdcに変更する制御を行う。
1 / EVFFc = 1 / EVuc + 1 / EVdc... <5>
EVu: EVd = EVuc: EVdc ... <6>
Next, in step ST7, the
そして、再び、ステップST1の処理に戻り、圧縮機21及び/又は室外ファン36の運転容量を変化させる毎に、上記のステップST2~ST7の処理が行われる。このようにして、2つの膨張弁24、26のフィードフォワード制御が行われる。
Then, the process returns to step ST1 again, and each time the operating capacity of the
-冷房運転時-
冷房運転時においても、上述の暖房運転時と同様のフィードフォワード制御が行われる。尚、暖房運転時においては、第2膨張弁26が上流側膨張弁として機能し、かつ、第1膨張弁24が下流側膨張弁として機能し、また、室内熱交換器41が冷媒の凝縮器として機能し、かつ、室外熱交換器23が冷媒の蒸発器として機能するのに対して、冷房運転時においては、第1膨張弁24が上流側膨張弁として機能し、かつ、第2膨張弁26が下流側膨張弁として機能し、また、室外熱交換器23が冷媒の凝縮器として機能し、かつ、室内熱交換器41が冷媒の蒸発器として機能する点が異なっているが、これらの点を除いては、暖房運転時と同様であるため、ここでは詳細な説明を省略する。
-During cooling operation-
Even during the cooling operation, the same feedforward control as that during the heating operation described above is performed. During heating operation, the
(4)空気調和装置の特徴
本実施形態の空気調和装置1には、以下のような特徴がある。
(4) Features of the air conditioner The air conditioner 1 of the present embodiment has the following features.
ここでは、上述のように、高圧Phから中間圧Pmを差し引いた高圧側圧力差ΔPhと中間圧Pmから低圧Plを差し引いた低圧側圧力差ΔPlとの相関関係に基づく予測条件にて、圧縮機21の運転容量、及び/又は、室外ファン36の運転容量を変化させた後における上流側膨張弁及び下流側膨張弁(ここでは、膨張弁24、26)を通過する冷媒循環量の変化を予測して、圧縮機21の運転容量、及び/又は、室外ファン36の運転容量を変化させた際に、予測された冷媒循環量の変化を加味して上流側膨張弁及び下流側膨張弁の開度を変化させる制御を行うようにしている。
Here, as described above, under the prediction condition based on the correlation between the high pressure side pressure difference ΔPh obtained by subtracting the intermediate pressure Pm from the high pressure Ph and the low pressure side pressure difference ΔP1 obtained by subtracting the low pressure Pl from the intermediate pressure Pm, the
すなわち、ここでは、上流側膨張弁及び下流側膨張弁のフィードフォワード制御を行うに当たり、高圧側圧力差ΔPhと低圧側圧力差ΔPmとの相関関係に基づく予測条件にて、圧縮機21や室外ファン36の運転容量を変化させた後における上流側膨張弁及び下流側膨張弁を通過する冷媒循環量の変化を予測するようにしている。尚、ここでは、相関関係として、圧縮機21の運転容量、及び/又は、室外ファン36の運転容量を変化させた前後において、高圧側圧力差ΔPhと低圧側圧力差ΔPlとの比率が一定であるという関係を設定している。
That is, here, in performing feedforward control of the upstream side expansion valve and the downstream side expansion valve, the
これにより、ここでは、中間圧Pmを検出するためのセンサを設けることなく、上流側膨張弁及び下流側膨張弁を通過する冷媒循環量の変化を予測して、上流側膨張弁及び下流側膨張弁のフィードフォワード制御を行うことができる。そして、圧縮機21や室外ファン36の運転容量が変化する際に、上流側膨張弁及び下流側膨張弁の開度の制御追従性を向上させることができる。
Thereby, here, without providing a sensor for detecting the intermediate pressure Pm, a change in the refrigerant circulation amount passing through the upstream expansion valve and the downstream expansion valve is predicted, and the upstream expansion valve and the downstream expansion valve are predicted. Valve feedforward control can be performed. And when the operating capacity of the
また、ここでは、上述のように、上流側膨張弁(ここでは、膨張弁24、26の一方)が、室外熱交換器23及び室内熱交換器41のうち冷媒の放熱器として機能する熱交換器の出口における冷媒の過冷却度SCが所定の目標過冷却度SCsになるように開度制御し、下流側膨張弁(ここでは、膨張弁24、26の他方)が、室外熱交換器23及び室内熱交換器41のうち冷媒の蒸発器として機能する熱交換器の出口における冷媒の過熱度SHが所定の目標過熱度SHsになるように開度制御するようになっている。
Here, as described above, heat exchange in which the upstream expansion valve (here, one of the
ここでは、上流側膨張弁及び下流側膨張弁の開度制御として、上述のフィードフォワード制御とともに、過冷却度や過熱度に基づくフィードバック制御を行うようにしている。このため、ここでは、圧縮機21や室外ファン36の運転容量が変化する際に、上流側膨張弁及び下流側膨張弁の開度を、フィードフォワード制御によって、圧縮機21や室外ファン36の運転容量の変化後の最適な開度に予め近づけた後に、フィードバック制御によって、最適な開度に一致させることができる。
Here, feedback control based on the degree of supercooling and the degree of superheat is performed together with the feedforward control described above as the opening degree control of the upstream side expansion valve and the downstream side expansion valve. Therefore, here, when the operating capacities of the
これにより、ここでは、上流側膨張弁及び下流側膨張弁のフィードバック制御に要する時間を効果的に短縮することができる。そして、圧縮機21や室外ファン36の運転容量が変化する際に、上流側膨張弁及び下流側膨張弁の開度の制御追従性を向上させることができる。
Thereby, here, the time required for feedback control of the upstream side expansion valve and the downstream side expansion valve can be effectively shortened. And when the operating capacity of the
(5)変形例
上記の2つの膨張弁24、26のフィードフォワード制御(図4参照)では、上流側膨張弁及び下流側膨張弁のフィードフォワード制御を行うに当たり、高圧側圧力差ΔPhと低圧側圧力差ΔPmとの相関関係として、圧縮機21の運転容量、及び/又は、室外ファン36の運転容量を変化させた前後において、高圧側圧力差ΔPhと低圧側圧力差ΔPlとの比率が一定であるという関係を設定しているが、これに限定されるものではない。
(5) Modified Example In the feed forward control (see FIG. 4) of the two
例えば、相関関係として、圧縮機21の運転容量、及び/又は、室外ファン36の運転容量を変化させた前後において、高圧側圧力差ΔPhが一定であるという関係を設定するようにしてもよい。以下、この相関関係を採用した膨張弁24、26のフィードフォワード制御について説明する。尚、ここでも、上述のフィードフォワード制御と同様に、暖房運転時における内容だけを説明し、冷房運転時における内容を省略する。
For example, as a correlation, a relationship in which the high-pressure side pressure difference ΔPh is constant before and after the operation capacity of the
暖房運転時において、フィードフォワード制御部83は、図5に示すように、まず、上述のフィードフォワード制御(図4参照)におけるステップST1と同様に、圧縮機21の運転容量、及び/又は、室外ファン36の運転容量が変化するかどうかを判定する(ステップST11)。そして、ステップST11において、圧縮機21及び/又は室外ファン36の運転容量が変化するものと判定された場合には、ステップST12~ST20の処理に移行する。
During the heating operation, as shown in FIG. 5, the
次に、ステップST12において、フィードフォワード制御部83の予測部83aは、上述のフィードフォワード制御(図4参照)におけるステップST2と同様に、圧縮機21及び/又は室外ファン36の運転容量の制御が行われる直前(すなわち、運転容量が変化する直前)における2つの膨張弁24、26の開度EVu、EVdを合算した運転容量変化前の仮想合算開度EVFFを算出する。例えば、膨張弁24、26として開度とCv値とが比例する特性の膨張弁を採用する場合には、上述の運転容量変化前の仮想合算開度EVFFは、上述のフィードフォワード制御(図4参照)におけるステップST2と同様に、次式<11>によって算出される。
Next, in step ST12, the
1/EVFF = 1/EVu +1/EVd ・・・<11>
次に、ステップST13において、予測部83aは、上述のフィードフォワード制御(図4参照)におけるステップST3と同様に、圧縮機21及び/又は室外ファン36の運転容量の制御が行われる直前(すなわち、運転容量が変化する直前)における2つの膨張弁24、26を通過する運転容量変化前の冷媒循環量Grを算出する。ここで、運転容量変化前の冷媒循環量Grは、上述のフィードフォワード制御(図4参照)におけるステップST3と同様に、次式<12>のように、ステップST12において算出された運転容量変化前の仮想合算開度EVFFの関数として表すことができる。
1 / EVFF = 1 / EVu + 1 / EVd ... <11>
Next, in step ST13, the
Gr = f(EVFF) ・・・<12>
次に、ステップST14において、上述のフィードフォワード制御(図4参照)におけるステップST3とは異なり、圧縮機21及び/又は室外ファン36の運転容量の制御が行われた直後(すなわち、運転容量が変化した直後)における上流側膨張弁(暖房運転時における第2膨張弁26、又は、冷房運転時における第1膨張弁24)の圧縮機21及び/又は室外ファン36の運転容量の制御が行われた直後(すなわち、運転容量が変化した直後)における運転容量変化後の上流側膨張弁を通過する冷媒循環量Grucを算出する。ここで、運転容量変化後の上流側膨張弁を通過する冷媒循環量Grucは、次式<13>のように、圧縮機21の運転容量の変化前後の運転容量比Fcc/Fc、室外ファン36の運転容量の変化前後の運転容量比Ffc/Ff、及び、運転容量変化前の冷媒循環量Grの関数として表すことができる。
Gr = f (EVFF) ... <12>
Next, in step ST14, unlike step ST3 in the above feedforward control (see FIG. 4), immediately after the operation capacity of the
Gruc = f(Fcc/Fc、Ffc/Ff)×Gr ・・・<13>
ここで、上式<13>において、上述のフィードフォワード制御(図4参照)における式<3>とは異なり、運転容量変化前の冷凍サイクルにおける凝縮温度Tc、及び、運転容量変化前の冷凍サイクルにおける蒸発温度Teの関数にしていないのは、実質的には、運転容量の変化前後で冷凍サイクルにおける高圧Ph、中間圧Pm及び低圧Plの変化がないこと、すなわち、運転容量の変化前後で高圧側圧力差ΔPhが一定であるという相関関係を考慮したためである。すなわち、運転容量変化後の上流側膨張弁を通過する冷媒循環量Grucは、運転容量の変化前後で高圧Ph、中間圧Pm及び低圧Plの変化がないという条件で算出された運転容量変化後の冷媒循環量である。
Gruc = f (Fcc / Fc, Ffc / Ff) × Gr (13)
Here, in the above formula <13>, unlike the formula <3> in the above feedforward control (see FIG. 4), the condensation temperature Tc in the refrigeration cycle before the change in operating capacity and the refrigeration cycle before the change in operating capacity. What is not a function of the evaporation temperature Te is that there is substantially no change in the high pressure Ph, intermediate pressure Pm and low pressure Pl in the refrigeration cycle before and after the change in operating capacity, that is, high pressure before and after the change in operating capacity. This is because the correlation that the side pressure difference ΔPh is constant is taken into consideration. That is, the refrigerant circulation amount Gruc passing through the upstream side expansion valve after the change of the operation capacity is the value after the change of the operation capacity calculated under the condition that the high pressure Ph, the intermediate pressure Pm, and the low pressure Pl are not changed before and after the change of the operation capacity. Refrigerant circulation amount.
次に、ステップST15において、予測部83aは、運転容量の変化前後で高圧Ph、中間圧Pm及び低圧Plの変化がないという条件における運転容量変化後の2つの膨張弁24、26の開度を合算した運転容量変化後の仮想合算開度EVFFucを算出する。ここで、運転容量の変化前後で高圧Ph、中間圧Pm及び低圧Plの変化がないという条件における運転容量変化後の仮想合算開度EVFFucは、次式<14>のように、ステップST14において算出された運転容量の変化前後で高圧Ph、中間圧Pm及び低圧Plの変化がないという条件における運転容量変化後の冷媒循環量Grucの関数として表すことができる。
Next, in step ST15, the
EVFFuc = f(Gruc) ・・・<14>
次に、ステップST16において、予測部83aは、ステップST15において算出された運転容量の変化前後で高圧Ph、中間圧Pm及び低圧Plの変化がないという条件における運転容量変化後の仮想合算開度EVFFucを用いて、上流側膨張弁(暖房運転時における第2膨張弁26、又は、冷房運転時における第1膨張弁24)の運転容量変化後の開度EVucを算出する。
EVFFuc = f (Gruc) ... <14>
Next, in step ST16, the
ここでは、上述のフィードフォワード制御(図4参照)における式<5>及び<6>と同様の式<15>及び<16>の連立式を解くことで、上流側膨張弁の運転容量変化後の開度EVucを算出する。但し、このステップS16においては、上述のフィードフォワード制御(図4参照)のステップST6とは異なり、下流側膨張弁(暖房運転時における第1膨張弁24、又は、冷房運転時における第2膨張弁26)の運転容量変化後の開度EVdcは算出せず、ステップST17~ST19において算出する。
Here, by solving the simultaneous equations <15> and <16> similar to the equations <5> and <6> in the feedforward control described above (see FIG. 4), the operating capacity of the upstream side expansion valve is changed. The opening degree EVuc of is calculated. However, in step S16, unlike step ST6 of the above-described feedforward control (see FIG. 4), the downstream side expansion valve (the
1/EVFFuc = 1/EVuc +1/EVdc ・・・<15>
EVu:EVd = EVuc:EVdc ・・・<16>
次に、ステップST17において、予測部83aは、上述のフィードフォワード制御(図4参照)におけるステップST4と同様に、圧縮機21及び/又は室外ファン36の運転容量の制御が行われた直後(すなわち、運転容量が変化した直後)における2つの膨張弁24、26を通過する運転容量変化後の冷媒循環量Grcを算出する。ここで、運転容量変化後の冷媒循環量Grcは、次式<17>のように、圧縮機21の運転容量の変化前後の運転容量比Fcc/Fc、室外ファン36の運転容量の変化前後の運転容量比Ffc/Ff、運転容量変化前の冷凍サイクルにおける凝縮温度Tc、運転容量変化前の冷凍サイクルにおける蒸発温度Te、及び、運転容量変化前の冷媒循環量Grの関数として表すことができる。
1 / EVFFuc = 1 / EVuc + 1 / EVdc ... <15>
EVu: EVd = EVuc: EVdc ... <16>
Next, in step ST17, the
Grc = f(Fcc/Fc、Ffc/Ff、Tc、Te)×Gr ・・・<17>
次に、ステップST18において、予測部83aは、圧縮機21及び/又は室外ファン36の運転容量の制御が行われた直後(すなわち、運転容量が変化した直後)における2つの膨張弁24、26の開度(すなわち、運転容量変化後の上流側膨張弁の開度EVuc、及び、運転容量変化後の下流側膨張弁の開度EVdc)を合算した運転容量変化後の仮想合算開度EVFFcを算出する。ここで、運転容量変化後の仮想合算開度EVFFcは、次式<18>のように、ステップST17において算出された運転容量変化後の冷媒循環量Grcの関数として表すことができる。
Grc = f (Fcc / Fc, Ffc / Ff, Tc, Te) × Gr ... <17>
Next, in step ST18, the
EVFFc = f(Grc) ・・・<18>
次に、ステップST19において、予測部83aは、ステップST18において算出された運転容量変化後の仮想合算開度EVFFc、及び、ステップST16において算出された運転容量変化後の上流側膨張弁の開度EVucを用いて、下流側膨張弁(暖房運転時における第1膨張弁24、又は、冷房運転時における第2膨張弁26)の運転容量変化後の開度EVdcを算出する。
EVFFc = f (Grc) ... <18>
Next, in step ST19, the
ここでは、上述のフィードフォワード制御(図4参照)における式<5>と同様の式<19>に、ステップST16において算出された開度EVdc及びステップST18において算出された開度EVFFcを代入することによって、下流側膨張弁(暖房運転時における第1膨張弁24、又は、冷房運転時における第2膨張弁26)の運転容量変化後の開度EVdcが算出されるようになっている。
Here, the opening degree EVdc calculated in step ST16 and the opening degree EVFFc calculated in step ST18 are substituted into the expression <19> similar to the expression <5> in the above-described feedforward control (see FIG. 4). Thus, the opening degree EVdc after the operation capacity change of the downstream side expansion valve (the
1/EVFFc = 1/EVuc +1/EVdc ・・・<19>
次に、ステップST20において、フィードフォワード制御部83の開度変更部83bは、2つの膨張弁24、26の開度を、ステップST16及びステップST19において算出された開度EVuc、EVdcに変更する制御を行う。
1 / EVFFc = 1 / EVuc + 1 / EVdc ... <19>
Next, in step ST20, the
そして、再び、ステップST11の処理に戻り、圧縮機21及び/又は室外ファン36の運転容量を変化させる毎に、上記のステップST12~ST20の処理が行われる。このようにして、2つの膨張弁24、26のフィードフォワード制御が行われる。
Then, returning to the process of step ST11 again, each time the operating capacity of the
本変形例にかかる2つの膨張弁24、26のフィードフォワード制御においても、上述の2つの膨張弁24、26のフィードフォワード制御(図4参照)と同様に、中間圧Pmを検出するためのセンサを設けることなく、上流側膨張弁及び下流側膨張弁を通過する冷媒循環量の変化を予測して、上流側膨張弁及び下流側膨張弁のフィードフォワード制御を行うことができる。そして、圧縮機21や室外ファン36の運転容量が変化する際に、上流側膨張弁及び下流側膨張弁の開度の制御追従性を向上させることができる。
In the feedforward control of the two
また、上流側膨張弁及び下流側膨張弁の開度制御として、上述のフィードフォワード制御(図5参照)とともに、過冷却度や過熱度に基づくフィードバック制御を行うことで、圧縮機21や室外ファン36の運転容量が変化する際に、上流側膨張弁及び下流側膨張弁の開度を、フィードフォワード制御によって、圧縮機21や室外ファン36の運転容量の変化後の最適な開度に予め近づけた後に、フィードバック制御によって、最適な開度に一致させることができる。
Further, as the opening degree control of the upstream side expansion valve and the downstream side expansion valve, the feedback control based on the degree of supercooling and the degree of superheat is performed together with the above-described feedforward control (see FIG. 5). When the operating capacity of 36 changes, the opening degree of the upstream side expansion valve and the downstream side expansion valve is brought close to the optimum opening degree after the change of the operating capacity of the
本発明は、上流側膨張弁及び下流側膨張弁によって圧縮機から吐出された高圧の冷媒を中間圧、低圧の順に2段階で膨張させつつ冷媒の循環を行う空気調和装置に対して、広く適用可能である。 The present invention is widely applied to an air conditioner that circulates a refrigerant while expanding a high-pressure refrigerant discharged from a compressor by an upstream expansion valve and a downstream expansion valve in two stages in the order of intermediate pressure and low pressure. Is possible.
1 空気調和装置
10 冷媒回路
21 圧縮機
23 室外熱交換器
24 第1膨張弁(上流側膨張弁、下流側膨張弁)
26 第2膨張弁(下流側膨張弁、上流側膨張弁)
36 室外ファン
41 室内熱交換器
DESCRIPTION OF SYMBOLS 1 Air conditioning apparatus 10
26 Second expansion valve (downstream expansion valve, upstream expansion valve)
36 Outdoor fan 41 Indoor heat exchanger
Claims (4)
前記高圧から前記中間圧を差し引いた高圧側圧力差と前記中間圧から前記低圧を差し引いた低圧側圧力差との相関関係に基づく予測条件にて、前記圧縮機の運転容量、及び/又は、前記室外ファンの運転容量を変化させた後における前記上流側膨張弁及び前記下流側膨張弁を通過する冷媒循環量の変化を予測して、前記圧縮機の運転容量、及び/又は、前記室外ファンの運転容量を変化させた際に、前記予測された冷媒循環量の変化を加味して前記上流側膨張弁及び前記下流側膨張弁の開度を変化させる制御を行う、
空気調和装置(1)。 The compressor (21), the outdoor heat exchanger (23), the upstream side expansion valves (24, 26), the downstream side expansion valves (26, 24), and the indoor heat exchanger (41) are connected to each other. A refrigerant circuit (10) for circulating the refrigerant while expanding the high-pressure refrigerant discharged from the compressor by the upstream expansion valve and the downstream expansion valve in two stages in the order of intermediate pressure and low pressure; In an air conditioner having an outdoor fan (36) for supplying outdoor air serving as a cooling source or a heating source to a heat exchanger,
In the prediction condition based on the correlation between the high pressure side pressure difference obtained by subtracting the intermediate pressure from the high pressure and the low pressure side pressure difference obtained by subtracting the low pressure from the intermediate pressure, the operating capacity of the compressor and / or the Predicting a change in the amount of refrigerant circulating through the upstream expansion valve and the downstream expansion valve after changing the operating capacity of the outdoor fan, the operating capacity of the compressor and / or the outdoor fan When the operating capacity is changed, control is performed to change the opening degree of the upstream side expansion valve and the downstream side expansion valve in consideration of the predicted change in the refrigerant circulation amount.
Air conditioner (1).
請求項1に記載の空気調和装置(1)。 The correlation is such that the ratio between the high pressure side pressure difference and the low pressure side pressure difference before and after the operating capacity of the compressor (21) and / or the operating capacity of the outdoor fan (36) is changed. The relationship is constant,
The air conditioner (1) according to claim 1.
請求項1に記載の空気調和装置(1)。 The correlation is a relationship that the high-pressure side pressure difference is constant before and after the operating capacity of the compressor (21) and / or the operating capacity of the outdoor fan (36) is changed.
The air conditioner (1) according to claim 1.
前記下流側膨張弁(26、24)は、前記室外熱交換器及び前記室内熱交換器のうち冷媒の蒸発器として機能する熱交換器の出口における冷媒の過熱度が所定の目標過熱度になるように開度制御される、
請求項1~3のいずれか1項に記載の空気調和装置(1)。 The upstream expansion valves (24, 26) have a refrigerant subcooling degree at the outlet of a heat exchanger functioning as a refrigerant radiator of the outdoor heat exchanger (23) and the indoor heat exchanger (41). The opening degree is controlled so as to achieve a predetermined target supercooling degree,
In the downstream expansion valves (26, 24), the superheat degree of the refrigerant at the outlet of the heat exchanger functioning as the refrigerant evaporator of the outdoor heat exchanger and the indoor heat exchanger becomes a predetermined target superheat degree. So that the opening is controlled,
The air conditioner (1) according to any one of claims 1 to 3.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2013-122803 | 2013-06-11 | ||
| JP2013122803A JP5673738B2 (en) | 2013-06-11 | 2013-06-11 | Air conditioner |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2014199788A1 true WO2014199788A1 (en) | 2014-12-18 |
Family
ID=52022089
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/JP2014/063289 Ceased WO2014199788A1 (en) | 2013-06-11 | 2014-05-20 | Air-conditioning device |
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| Country | Link |
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| JP (1) | JP5673738B2 (en) |
| WO (1) | WO2014199788A1 (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108286512A (en) * | 2018-04-18 | 2018-07-17 | 格力电器(芜湖)有限公司 | Temperature adjusting system, air supplementing device of double-stage compressor of temperature adjusting system and control method of air supplementing device |
| JP2018204849A (en) * | 2017-06-02 | 2018-12-27 | ヤンマー株式会社 | Heat pump device |
| US10801767B2 (en) * | 2016-09-06 | 2020-10-13 | Mitsubishi Electric Corporation | Refrigeration cycle apparatus |
| US11243016B2 (en) * | 2017-09-12 | 2022-02-08 | Hill Phoenix, Inc. | Refrigeration system with combined superheat and subcooling control |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2017017767A1 (en) * | 2015-07-27 | 2017-02-02 | 三菱電機株式会社 | Air conditioning device |
| KR102488575B1 (en) | 2016-03-11 | 2023-01-16 | 한화파워시스템 주식회사 | Control system for compressor and method of controlling the compressor |
| US12467673B2 (en) | 2021-03-31 | 2025-11-11 | Mitsubishi Electric Corporation | Refrigeration cycle apparatus and refrigeration cycle method |
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| JPH0464851A (en) * | 1990-07-05 | 1992-02-28 | Matsushita Electric Ind Co Ltd | Control device for multi-room air conditioners |
| JPH11501114A (en) * | 1995-02-28 | 1999-01-26 | アメリカン・スタンダード・インコーポレイテッド | Feedforward control of expansion valve |
| JP2003106683A (en) * | 2001-09-28 | 2003-04-09 | Daikin Ind Ltd | Refrigeration equipment |
| JP2004003717A (en) * | 2002-05-31 | 2004-01-08 | Mitsubishi Electric Corp | Air conditioner |
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- 2013-06-11 JP JP2013122803A patent/JP5673738B2/en not_active Expired - Fee Related
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2014
- 2014-05-20 WO PCT/JP2014/063289 patent/WO2014199788A1/en not_active Ceased
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0464851A (en) * | 1990-07-05 | 1992-02-28 | Matsushita Electric Ind Co Ltd | Control device for multi-room air conditioners |
| JPH11501114A (en) * | 1995-02-28 | 1999-01-26 | アメリカン・スタンダード・インコーポレイテッド | Feedforward control of expansion valve |
| JP2003106683A (en) * | 2001-09-28 | 2003-04-09 | Daikin Ind Ltd | Refrigeration equipment |
| JP2004003717A (en) * | 2002-05-31 | 2004-01-08 | Mitsubishi Electric Corp | Air conditioner |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10801767B2 (en) * | 2016-09-06 | 2020-10-13 | Mitsubishi Electric Corporation | Refrigeration cycle apparatus |
| JP2018204849A (en) * | 2017-06-02 | 2018-12-27 | ヤンマー株式会社 | Heat pump device |
| US11243016B2 (en) * | 2017-09-12 | 2022-02-08 | Hill Phoenix, Inc. | Refrigeration system with combined superheat and subcooling control |
| US11732938B2 (en) | 2017-09-12 | 2023-08-22 | Hill Phoenix, Inc. | Refrigeration system with combined superheat and subcooling control |
| US20230358449A1 (en) * | 2017-09-12 | 2023-11-09 | Hill Phoenix, Inc. | Refrigeration System with Combined Superheat and Subcooling Control |
| US12055327B2 (en) | 2017-09-12 | 2024-08-06 | Hill Phoenix, Inc. | Refrigeration system with combined superheat and subcooling control |
| CN108286512A (en) * | 2018-04-18 | 2018-07-17 | 格力电器(芜湖)有限公司 | Temperature adjusting system, air supplementing device of double-stage compressor of temperature adjusting system and control method of air supplementing device |
| CN108286512B (en) * | 2018-04-18 | 2024-02-09 | 格力电器(芜湖)有限公司 | Temperature regulating system, and two-stage compressor air supplementing device and control method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2014240714A (en) | 2014-12-25 |
| JP5673738B2 (en) | 2015-02-18 |
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