WO2023157580A1 - Heat pump system, and method for controlling heat pump system - Google Patents
Heat pump system, and method for controlling heat pump system Download PDFInfo
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- WO2023157580A1 WO2023157580A1 PCT/JP2023/002088 JP2023002088W WO2023157580A1 WO 2023157580 A1 WO2023157580 A1 WO 2023157580A1 JP 2023002088 W JP2023002088 W JP 2023002088W WO 2023157580 A1 WO2023157580 A1 WO 2023157580A1
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F11/00—Control or safety arrangements
- F24F11/70—Control systems characterised by their outputs; Constructional details thereof
- F24F11/80—Control systems characterised by their outputs; Constructional details thereof for controlling the temperature of the supplied air
- F24F11/86—Control systems characterised by their outputs; Constructional details thereof for controlling the temperature of the supplied air by controlling compressors within refrigeration or heat pump circuits
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60H—ARRANGEMENTS OF HEATING, COOLING, VENTILATING OR OTHER AIR-TREATING DEVICES SPECIALLY ADAPTED FOR PASSENGER OR GOODS SPACES OF VEHICLES
- B60H1/00—Heating, cooling or ventilating [HVAC] devices
- B60H1/00642—Control systems or circuits; Control members or indication devices for heating, cooling or ventilating devices
- B60H1/00814—Control systems or circuits characterised by their output, for controlling particular components of the heating, cooling or ventilating installation
- B60H1/00878—Control systems or circuits characterised by their output, for controlling particular components of the heating, cooling or ventilating installation the components being temperature regulating devices
- B60H1/00899—Controlling the flow of liquid in a heat pump system
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60H—ARRANGEMENTS OF HEATING, COOLING, VENTILATING OR OTHER AIR-TREATING DEVICES SPECIALLY ADAPTED FOR PASSENGER OR GOODS SPACES OF VEHICLES
- B60H1/00—Heating, cooling or ventilating [HVAC] devices
- B60H1/32—Cooling devices
- B60H1/3204—Cooling devices using compression
- B60H1/3225—Cooling devices using compression characterised by safety arrangements, e.g. compressor anti-seizure means or by signalling devices
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F11/00—Control or safety arrangements
- F24F11/30—Control or safety arrangements for purposes related to the operation of the system, e.g. for safety or monitoring
- F24F11/32—Responding to malfunctions or emergencies
- F24F11/38—Failure diagnosis
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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
- F25B49/00—Arrangement or mounting of control or safety devices
- F25B49/02—Arrangement or mounting of control or safety devices for compression type machines, plants or systems
- F25B49/022—Compressor control arrangements
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60H—ARRANGEMENTS OF HEATING, COOLING, VENTILATING OR OTHER AIR-TREATING DEVICES SPECIALLY ADAPTED FOR PASSENGER OR GOODS SPACES OF VEHICLES
- B60H1/00—Heating, cooling or ventilating [HVAC] devices
- B60H1/32—Cooling devices
- B60H2001/3236—Cooling devices information from a variable is obtained
- B60H2001/3248—Cooling devices information from a variable is obtained related to pressure
- B60H2001/325—Cooling devices information from a variable is obtained related to pressure of the refrigerant at a compressing unit
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60H—ARRANGEMENTS OF HEATING, COOLING, VENTILATING OR OTHER AIR-TREATING DEVICES SPECIALLY ADAPTED FOR PASSENGER OR GOODS SPACES OF VEHICLES
- B60H1/00—Heating, cooling or ventilating [HVAC] devices
- B60H1/32—Cooling devices
- B60H2001/3236—Cooling devices information from a variable is obtained
- B60H2001/3255—Cooling devices information from a variable is obtained related to temperature
- B60H2001/3261—Cooling devices information from a variable is obtained related to temperature of the air at an evaporating unit
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60H—ARRANGEMENTS OF HEATING, COOLING, VENTILATING OR OTHER AIR-TREATING DEVICES SPECIALLY ADAPTED FOR PASSENGER OR GOODS SPACES OF VEHICLES
- B60H1/00—Heating, cooling or ventilating [HVAC] devices
- B60H1/32—Cooling devices
- B60H2001/3269—Cooling devices output of a control signal
- B60H2001/327—Cooling devices output of a control signal related to a compressing unit
- B60H2001/3272—Cooling devices output of a control signal related to a compressing unit to control the revolving speed of a compressor
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F2140/00—Control inputs relating to system states
- F24F2140/10—Pressure
- F24F2140/12—Heat-exchange fluid pressure
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F2140/00—Control inputs relating to system states
- F24F2140/20—Heat-exchange fluid temperature
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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
- F25B25/00—Machines, plants or systems, using a combination of modes of operation covered by two or more of the groups F25B1/00 - F25B23/00
- F25B25/005—Machines, plants or systems, using a combination of modes of operation covered by two or more of the groups F25B1/00 - F25B23/00 using primary and secondary systems
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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
- F25B2600/025—Compressor control by controlling speed
- F25B2600/0253—Compressor control by controlling speed with variable 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
- F25B2700/00—Sensing or detecting of parameters; Sensors therefor
- F25B2700/19—Pressures
- F25B2700/193—Pressures of the compressor
- F25B2700/1933—Suction pressures
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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
- F25B41/00—Fluid-circulation arrangements
- F25B41/20—Disposition of valves, e.g. of on-off valves or flow control 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
- F25B5/00—Compression machines, plants or systems, with several evaporator circuits, e.g. for varying refrigerating capacity
- F25B5/02—Compression machines, plants or systems, with several evaporator circuits, e.g. for varying refrigerating capacity arranged in parallel
Definitions
- the present invention relates to a heat pump system and a heat pump system control method.
- heat pumps are known in which the refrigerant continuously radiates heat and absorbs heat by circulating in refrigerant pipes while repeatedly condensing and evaporating, thereby cooling and warming indoor air.
- a heat pump is used not only as a refrigerator or an air conditioner installed in a building, but also as a vehicle air conditioner that is mounted on a vehicle to cool and heat the interior of the vehicle.
- the heat pump is provided with a compressor for compressing the refrigerant.
- the compressor could be damaged.
- a method of controlling the driving of the compressor is adopted so that the pressure of the refrigerant sucked into the compressor, that is, the suctioned refrigerant pressure does not become a negative pressure.
- the suction refrigerant pressure is measured by a pressure sensor on the suction side, or the pressure state of the refrigerant is detected by estimating it from the measurement value of the pressure sensor on the discharge side, and the compressor is driven. Inhibitory control is described.
- the pressure sensor is required to measure and detect minute drops in refrigerant intake pressure (shift to negative pressure) with high accuracy relative to normal operation, so high measurement accuracy is required for the pressure sensor. be.
- the pressure sensor has a problem of basically poor responsiveness and accuracy at the time of measurement near the atmospheric pressure. In order to solve this problem, a pressure sensor capable of measuring with higher accuracy and higher response is required even in an environment near atmospheric pressure, which may lead to an increase in cost.
- the present invention provides a heat pump system and a control method for the heat pump system that can estimate the state of the sucked refrigerant with high accuracy while keeping costs down and protect the compressor.
- a heat pump system includes a compressor, a radiator, an expansion mechanism, and a heat absorber that are connected to each other by refrigerant pipes, and the compressor, the radiator, the expansion mechanism, and the heat absorber a refrigerant circuit in which refrigerant can circulate through the refrigerant pipe in the order of the vessel, a temperature sensor for measuring the temperature of the refrigerant, a pressure sensor for measuring the pressure of the refrigerant, and a pressure drop of the refrigerant sucked into the compressor and a drive suppression control device that suppresses and controls the compressor so as to suppress the driving of the compressor by determining the determining the pressure drop of the refrigerant sucked into the compressor from the measured value of the temperature sensor, suppressing and controlling the compressor, and satisfying a predetermined second condition different from the first condition;
- the pressure drop of the refrigerant sucked into the compressor is determined from the measured value of the pressure sensor, and suppression control is performed on the compressor.
- the first condition includes that the measured value of the temperature sensor is equal to or lower than a predetermined reference temperature
- the second condition is that the measured value of the temperature sensor is higher than the reference temperature.
- the heat pump system further includes an environmental temperature sensor that measures the temperature of the environment in which the heat absorber is installed, and the first condition is that the measured value of the environmental temperature sensor is equal to or lower than a predetermined reference environmental temperature. and the second condition may include that the measured value of the environmental temperature sensor is higher than the reference environmental temperature.
- the heat pump system is used as a vehicle air conditioner mounted on a vehicle. and an outdoor air heat absorption heating operation mode in which the refrigerant circulating in the refrigerant circuit functions as an outdoor heat exchanger that absorbs heat into the compressor through the vehicle heat recovery device without passing through the heat absorber.
- a mode switching control device capable of switching the circulation path of the refrigerant in the refrigerant circuit between the recovery heating operation mode and the mode switching control device, wherein the first condition is that the mode switching control device is in the outside air heat absorption heating operation mode. mode, wherein the second condition may include switching to the heat recovery heating operation mode by the mode switching control device.
- the first condition is that the actual pressure of the refrigerant immediately before being sucked into the compressor during steady operation (hereinafter referred to as the actual pressure immediately before suction) is equal to or lower than a predetermined reference pressure.
- the second condition may include that the actual pressure immediately before suction during steady operation is greater than the reference pressure.
- the pressure sensor measures the pressure of the refrigerant immediately before being sucked into the compressor, and the drive suppression control device detects the actual pressure immediately before the suction from the pressure sensor. It may be estimated from measurements.
- the drive suppression control device measures the degree of superheat of the refrigerant immediately before being sucked into the compressor by measuring the measured value of the temperature sensor and the pressure sensor. It may be calculated from the value, and the driving of the compressor may be controlled based on the degree of superheat.
- a control method for a heat pump system comprises a refrigerant circuit configured by a compressor, a radiator, an expansion mechanism, and a heat absorber, which are connected to each other by refrigerant pipes.
- a control method for a heat pump in which a refrigerant circulates in the order of an expansion mechanism and the heat absorber comprising: a temperature measurement step of measuring the temperature of the refrigerant; a pressure measurement step of measuring the pressure of the refrigerant; and a drive suppression control step of determining a pressure drop of the refrigerant and performing suppression control so as to suppress the driving of the compressor, wherein a predetermined first condition is satisfied in the drive suppression control step.
- the pressure drop of the refrigerant sucked into the compressor is determined from the measured value of the temperature sensor, the compressor is inhibited and controlled, and a predetermined second condition different from the first condition is satisfied.
- the condition is established, the pressure drop of the refrigerant sucked into the compressor is determined from the measured value of the pressure sensor, and the compressor is restrained and controlled.
- FIG. 4 It is a mimetic diagram showing a heat pump system concerning a first embodiment of the present invention.
- A is a block diagram showing a hardware configuration of an ECU of the heat pump system of the first embodiment
- B is a block diagram showing a functional configuration of the ECU.
- 4 is a saturation curve showing characteristics of refrigerant circulating in the refrigerant circuit of the heat pump system of the first embodiment; It is a figure which shows the flow of the control method of the heat pump system of said 1st embodiment.
- 4 is a ph diagram showing the state of refrigerant circulating in the refrigerant circuit of the heat pump system of the first embodiment;
- FIG. It is a schematic diagram which shows the modification of the heat pump system of said 1st embodiment.
- FIG. 1 It is a mimetic diagram showing a heat pump system concerning a second embodiment of the present invention.
- A is a block diagram showing the hardware configuration of an ECU of the heat pump system of the second embodiment
- B is a block diagram showing the functional configuration of the ECU.
- a heat pump system 100 cools or warms indoor air using a refrigerant.
- the place where the heat pump system 100 is installed is not particularly limited, but in the present embodiment, the heat pump system 100 is used in a vehicle air conditioner (air conditioner) that is mounted on a vehicle and performs cooling and heating of the vehicle interior. explain.
- vehicle air conditioner air conditioner
- the heat pump system 100 as a vehicle air conditioner may be installed in a vehicle powered only by an internal combustion engine. It is suitable for vehicles such as difficult HEV (Hybrid Electric Vehicle) and EV (Electric Vehicle) that cannot be heated by exhaust heat of the internal combustion engine.
- HEV Hybrid Electric Vehicle
- EV Electric Vehicle
- the heat pump system 100 includes a refrigerant circuit 1 in which refrigerant circulates, a temperature sensor 2 that measures the temperature of the refrigerant in the refrigerant circuit 1, a pressure sensor 3 that measures the pressure of the refrigerant in the refrigerant circuit 1, A drive suppression control device 4 that suppresses and controls the driving of the compressor 10 in the refrigerant circuit 1 based on the measured value of the temperature sensor 2 and the measured value of the pressure sensor 3 is provided.
- the refrigerant circuit 1 has a compressor 10, a first heat exchanger 11, an expansion mechanism 12, a second heat exchanger 13, and refrigerant pipes 14 connecting these to each other.
- the refrigerant circulates through the refrigerant pipes 14 through the compressor 10, the first heat exchanger 11, the expansion mechanism 12, and the second heat exchanger 13 in this order.
- the type of refrigerant is not particularly limited, and may be, for example, R-1234yf.
- the compressor 10 sucks and compresses the refrigerant from the upstream side of the refrigerant circuit 1 and discharges the refrigerant downstream as a high-temperature, high-pressure gas.
- the type of the compressor 10 is not particularly limited, for example, a piston-type or scroll-type electric compressor is adopted.
- An accumulator 15 that separates liquid from the refrigerant is provided upstream of the compressor 10 in the refrigerant circuit 1 .
- the first heat exchanger 11 functions as a radiator in this embodiment.
- the refrigerant which has been turned into a high-temperature, high-pressure gas by the compressor 10, is allowed to pass therethrough, and heat is released from the refrigerant, thereby cooling the refrigerant.
- the first heat exchanger 11 is arranged in a device called HVAC (Heating Ventilation and Air-Conditioning) 20 provided in the vehicle.
- HVAC Heating Ventilation and Air-Conditioning
- the air A taken into the air flow path 22 by the blower 21 is heated by exchanging heat with the refrigerant in the first heat exchanger 11, and is supplied into the passenger compartment. That is, in this embodiment, the heat pump system 100 is operated in the heating operation mode for heating the interior of the vehicle.
- the expansion mechanism 12 includes an expansion valve, a capillary tube, and the like, and decompresses and expands the high-pressure refrigerant that has passed through the first heat exchanger 11 to produce a low-pressure refrigerant.
- the second heat exchanger 13 functions as a heat absorber in this embodiment.
- the refrigerant whose pressure has been reduced by the expansion mechanism 12 is allowed to pass therethrough to absorb heat and heat the refrigerant.
- the second heat exchanger 13 is an outdoor heat exchanger that causes the refrigerant to absorb heat from outside air.
- the second heat exchanger 13 functions as a radiator and the first heat exchanger 11 functions as a heat absorber.
- An operation in the cooling operation mode is also possible, but illustration and detailed description are omitted.
- the temperature sensor 2 is provided in the refrigerant pipe 14 on the upstream side of the inlet of the compressor 10 (downstream side of the accumulator 15) so as to be able to measure the temperature of the refrigerant immediately before being drawn into the compressor 10.
- the pressure sensor 3 is provided in the refrigerant pipe 14 on the upstream side of the inlet of the compressor so as to be able to measure the pressure of the refrigerant immediately before being drawn into the compressor 10 .
- a pressure/temperature sensor in which the temperature sensor 2 and the pressure sensor 3 are integrated is provided as the temperature sensor 2 and the pressure sensor 3 .
- the temperature and pressure are simultaneously and always measured at least while the refrigerant is circulating in the refrigerant circuit.
- the drive suppression control device 4 is a control device that determines the pressure drop of the refrigerant sucked into the compressor 10 and suppresses the drive of the compressor 10 . Specifically, the actual pressure of the refrigerant immediately before being sucked into the compressor 10 (hereinafter referred to as the actual pressure immediately before suction Pf) does not fall below the allowable lower limit pressure of the compressor 10, which is “0 [MPaG] in gauge pressure”. Control (hereinafter referred to as suppression control) is performed to stop the drive of the compressor 10 or to drive it intermittently so as to prevent the compressor 10 from being overheated.
- the suppression determination threshold pressure Pb is set to a pressure slightly higher than the allowable lower limit pressure (for example, 0.05 [MPaG] in gauge pressure).
- the pressure of the refrigerant immediately before being sucked into the compressor 10 is calculated (estimated) from the measured value of the temperature sensor 2 and/or the measured value of the pressure sensor 3, and this calculated (estimated) pressure (hereinafter referred to as pre-suction estimation pressure) becomes smaller than the suppression determination threshold pressure Pb, suppression control is executed.
- the drive suppression control device 4 calculates the estimated pressure immediately before intake using the measured value of the temperature sensor 2, and determines the pressure drop of the estimated pressure immediately before intake. to suppress and control the driving of the compressor 10 .
- the drive suppression control device 4 uses the measured value of the pressure sensor 3 to estimate the pre-intake presumed pressure. Compressor 10 is suppressed and controlled by judging the decrease in pressure.
- the drive suppression control device 4 is realized by an ECU 400 for air conditioners.
- the ECU 400 includes a CPU (Central Processing Unit) 402, memory 404 such as ROM (Read Only Memory) and RAM (Random Access Memory), and non-volatile storage such as HDD (Hard Disk Drive) and SSD (Solid State Drive). 406 and communication control unit 408 .
- CPU 402 , memory 404 , storage unit 406 , and communication control unit 408 are communicably connected to each other via internal bus 410 .
- the communication control unit 408 is connected to the temperature sensor 2, the pressure sensor 3, and (the control driver of) the compressor 10 via a communication line, acquires temperature information and pressure information from the temperature sensor 2 and the pressure sensor 3, and controls the compressor. 10 can transmit a control signal.
- a drive suppression control program is stored in the storage unit 406 .
- the drive suppression control program is read out from the storage unit 406 and developed in the memory 404, and the drive suppression control program developed in the memory 404 is executed by the CPU 402, so that the drive suppression control device 4 shown in FIG. and performs drive suppression control processing.
- FIG. 2(B) shows the functional configuration of the drive suppression control device 4 realized by the ECU 400.
- the drive suppression control device 4 includes a drive suppression execution processing unit 502 , a pressure detection via temperature estimation processing unit 504 , a pressure detection via pressure estimation processing unit 506 , and a pressure estimation method switching processing unit 508 .
- the drive suppression execution processing unit 502 calculates the refrigerant pressure immediately before being sucked into the compressor 10 (hereinafter referred to as immediately before suction estimated pressure) is below the suppression judgment threshold pressure (0.05 [MPaG] in gauge pressure here). Inhibition control such as
- the temperature detection-mediated pressure estimation processing unit 504 uses the measured value of the temperature sensor 2 to calculate the estimated pressure immediately before inhalation (hereinafter referred to as the estimated pressure immediately before inhalation via temperature detection). Specifically, the temperature detection via pressure estimation processing unit 504 stores a comparison table (or calculation formula) indicating the temperature-pressure relationship of the refrigerant, and calculates the pressure information from the temperature information. This comparison table (or calculation formula) is preferably based on the saturation curve showing the relationship between the saturation temperature and the saturation pressure of the refrigerant shown in FIG. 3, for example.
- the pressure detection-mediated pressure estimation processing unit 506 uses the measured value of the pressure sensor 3 to calculate the estimated pressure immediately before inhalation (hereinafter referred to as the pre-inhalation estimated pressure via pressure detection).
- the pre-inhalation estimated pressure via pressure detection since the pressure sensor 3 measures the pressure of the refrigerant immediately before being sucked into the compressor 10, the measurement result is directly used as the pre-suction estimated pressure via pressure detection.
- the location (measuring location) of the pressure sensor 3 is far from just before the refrigerant is drawn into the compressor 10, the pressure Estimated pressure immediately before detection inhalation is calculated.
- the pressure estimation method switching processing unit 508 uses the estimated pressure immediately before suction via temperature detection calculated by the pressure estimation processing unit 504 via temperature detection, or performs pressure estimation processing via pressure detection. Switches between using the estimated pre-inhalation pressure via pressure detection calculated in the unit 506 . Specifically, it holds information about conditions for switching determination (here, first condition C1 and second condition C2). A pressure estimation method switching processing unit 508 executes these condition determinations, and switches between refrigerant pressure monitoring using the estimated pressure immediately before suction via temperature detection and refrigerant pressure monitoring using the estimated pressure immediately before suction via pressure detection.
- the first condition C1 which is a condition for monitoring the actual pressure Pf immediately before suction of the refrigerant by the measured value of the temperature sensor 2 and estimating (judging) the decrease thereof, is that "the measured value of the temperature sensor 2 is a predetermined monitoring switching criterion. be equal to or lower than the temperature Tr".
- This monitoring switching reference temperature Tr is preferably set within a range of, for example, -20 [°C] to 10 [°C], and preferably set within a range of -15 [°C] to 5 [°C]. Further, it is preferably set to 0[°C] or less, more preferably -5[°C] or less, and is set to -10[°C] here.
- the pressure estimation method switching processing unit 508 monitors the pre-inhalation estimated pressure via temperature detection calculated from the measured value of the temperature sensor 2 in the pressure estimation processing unit 504 via temperature detection.
- a command is sent to the drive suppression execution processing unit 502 .
- the drive suppression execution processing unit 502 refers to the estimated pressure immediately before intake via temperature detection over time, and the value of the estimated pressure immediately before intake via temperature detection becomes equal to or less than a predetermined suppression determination threshold pressure Pb. In this case, it is estimated that the actual pressure Pf immediately before suction of the refrigerant has approached the allowable lower limit pressure, and the drive of the compressor 10 is restrained and controlled.
- the suppression judgment threshold pressure Pb is 0.05 [MPaG] in gauge pressure, but the present invention is not limited to this, and for example, a value in the range of 0.01 [MPaG] in gauge pressure or more and, on the safer side, a value within the range of 0.1 [MPaG] or more and 1 [MPaG] or less is more preferable.
- the second condition C2 which is a condition for monitoring the actual pressure Pf immediately before suction of the refrigerant based on the measured value of the pressure sensor 3 and estimating (determining) the decrease thereof, is that "the measured value of the temperature sensor 2 is equal to the reference temperature Tr It includes "becoming greater than”.
- the pressure estimation method switching processing unit 508 monitors the pre-inhalation estimated pressure via pressure detection calculated from the measured value of the pressure sensor 3 in the pressure detection via pressure estimation processing unit 506. A command is sent to the drive suppression execution processing unit 502 .
- the drive suppression execution processing unit 502 Upon receiving this command, the drive suppression execution processing unit 502 refers to the estimated pressure immediately before inhalation via pressure detection over time, and the value of the estimated pressure immediately before inhalation via pressure detection becomes equal to or less than a predetermined suppression determination threshold pressure Pb. In this case, it is estimated that the actual pressure Pf immediately before suction of the refrigerant has approached the allowable lower limit value, and the drive of the compressor 10 is restrained and controlled.
- the temperature sensor 2 and the pressure sensor 3 measure the temperature of the refrigerant (hereinafter referred to as suction refrigerant temperature) and pressure (hereinafter referred to as suction refrigerant pressure) in step S1. to run.
- steady operation is a state in which the heat pump system 100 is operated in a non-abnormal state (for example, a state in which refrigerant is leaking from the refrigerant pipe 14, a state in which the refrigerant pipe 14 is blocked, etc.). indicates that
- step S2 of monitoring the pressure of the refrigerant is executed.
- step S3 is executed to determine whether or not the measured value of the temperature sensor 2 is equal to or lower than the monitoring switching reference temperature Tr.
- Step S4a of calculating is executed.
- the first condition C1 is not satisfied and the second condition C2 is satisfied (NO).
- Step S4b is executed in which the measured value is used as it is as the estimated pressure immediately before inhalation via pressure detection.
- step S5 is executed to determine whether or not the pre-inhalation estimated pressure is equal to or lower than the suppression determination threshold pressure Pb. If the estimated pressure immediately before suction is equal to or lower than the suppression determination threshold pressure Pb in step S5 (YES), it is estimated that the actual pressure Pf immediately before suction of the refrigerant has approached the allowable lower limit, and the drive of the compressor 10 is suppressed and controlled. S6 is executed. After that, the process returns to step S1.
- step S5 if the estimated pressure immediately before suction is greater than the suppression determination threshold pressure Pb in step S5 (NO), it is estimated that the actual pressure immediately before suction Pf of the refrigerant has moved away from the allowable lower limit value to the safe side, and suppression control is performed. It returns to step S1 without performing.
- the first condition C1 ie, the determination that "the measured value of the temperature sensor 2 is equal to or lower than the predetermined monitoring switching reference temperature Tr", tends to deteriorate the monitoring accuracy (pressure estimation accuracy) of the pressure sensor 3.
- the temperature sensor 2 can ensure sufficient monitoring accuracy (pressure estimation accuracy).
- the second condition C2, ⁇ the measured value of the temperature sensor 2 must be greater than the reference temperature Tr,'' can sufficiently ensure the monitoring accuracy (pressure estimation accuracy) of the pressure sensor 3.
- the temperature sensor 2 can satisfy a mode in which the monitoring accuracy (pressure estimation accuracy) is likely to deteriorate. In this way, by setting conditions in which each of the temperature sensor 2 and the pressure sensor 3 is good, for example, it is not necessary to use the pressure sensor 3, which can achieve high measurement accuracy under all conditions (measurement range).
- the temperature sensor 2 can be used instead of the pressure sensor 3 to monitor the state in which the actual pressure Pf immediately before the refrigerant intake becomes a negative pressure or a pressure close to the atmospheric pressure.
- the cost of the pressure sensor 3 can be suppressed by covering the measurement range that the pressure sensor 3 is not good at with the temperature sensor 2, and the state of the sucked refrigerant can be estimated with high accuracy while suppressing the cost of the heat pump system 100 as a whole. and the compressor 10 can be reliably protected.
- the first condition C1 includes that the measured value of the temperature sensor 2 is equal to or lower than the monitoring switching reference temperature Tr (-10[°C]).
- Tr monitoring switching reference temperature
- the refrigerant just before being sucked into the compressor 10 is in a saturated vapor state, it is positioned at a specific point E on the saturated vapor line L in the ph diagram shown in FIG. If the temperature of the refrigerant at this specific point E is measured by the temperature sensor 2, the pressure of the refrigerant can be correctly estimated from the saturation curve of FIG.
- the refrigerant immediately before being sucked into the compressor 10 is a superheated gas, the refrigerant is positioned at a specific point E1 in a region having a higher specific enthalpy than the saturated vapor line L shown in FIG.
- the isothermal line M1 passing through the specific point E1 of the refrigerant extends curvedly along the vertical axis (pressure axis) in FIG. If the refrigerant is further heated and the degree of superheating of the refrigerant increases immediately before suction while the pressure Px remains the same, the refrigerant shifts to the right, as shown at singular points E2 and E3. As indicated by the isothermal line M2 passing through the singular point E2 and the isothermal line M3 passing through the singular point E3, if the degree of superheating of the refrigerant changes, the temperature of the refrigerant rises even if the pressure Px remains the same. .
- the second condition C2 includes that the measured value of the temperature sensor 2 is higher than the monitoring switching reference temperature Tr (-10 [°C]).
- This condition can also be expressed as an operating condition in which the degree of superheat tends to increase.
- This condition is a state in which sufficient pressure measurement accuracy can be expected even with the pressure sensor 3, and at the same time, it can be said that the temperature sensor 2 is in a state where the pressure estimation accuracy is likely to deteriorate due to an overheated state.
- the suctioned refrigerant pressure measured by the pressure sensor 3 can be used for monitoring the compressor 10, and the compressor 10 can be reliably protected.
- the monitoring switching reference temperature Tr which is the threshold for separating the first condition C1 and the second condition C2, is higher.
- the monitoring switching reference temperature Tr can be converted to the monitoring switching reference pressure Pr.
- the pressure gauge pressure
- the temperature sensor 2 can cover a wider range that the pressure sensor 3 is not good at, and the compressor 10 can be protected more reliably.
- the first condition C1 is that the actual pressure immediately before suction of the refrigerant (including the estimated pressure immediately before suction estimated by some calculation) during steady operation is equal to or lower than the monitoring switching reference pressure Pr.
- the second condition C2 may include that the actual pressure immediately before intake during steady operation is higher than the monitoring switching reference pressure Pr. That is, when the actual pressure immediately before suction can be directly measured or estimated without using the temperature sensor 2, the threshold for separating the first condition C1 and the second condition C2 is not the monitoring switching reference temperature Tr. , the monitoring switching reference pressure Pr may be used.
- the drive suppression control device 4 may further include an overheating suppression execution processing unit 510 as shown in FIG.
- the overheat suppression execution processing unit 510 When the second condition C2 is satisfied, that is, when the degree of superheat is likely to increase, in addition to the suppression control by the drive suppression execution processing unit 502, the overheat suppression execution processing unit 510 outputs the measured value of the temperature sensor 2 and the The compressor 10 may be inhibited and controlled based on the degree of superheat of the refrigerant calculated from the measured value of the pressure sensor 3 . If the degree of superheat becomes abnormally high, for example, there is a possibility that the amount of refrigerant circulating in the path is insufficient.
- the compressor 10 will lock due to insufficient lubrication due to the lean refrigerant. Therefore, by operating the compressor 10 at a low capacity, the circulation amount of the refrigerant is increased to avoid insufficient lubrication and prevent failure of the compressor 10 .
- this control is referred to as "overheat suppression control”.
- the overheat suppression execution processing unit 510 of the drive suppression control device 4 stores a table (or calculation formula) indicating the state of the refrigerant, and based on this table (or calculation formula), the temperature sensor 2 measures From both the suctioned refrigerant temperature and the suctioned refrigerant pressure measured by the pressure sensor 3, the degree of superheat ⁇ T of the refrigerant immediately before being drawn into the compressor is calculated.
- the superheat suppression execution processing unit 510 monitors the degree of superheat ⁇ T, and when the degree of superheat ⁇ T is greater than a predetermined suppression judgment threshold superheat degree ⁇ Tb, it is estimated that, for example, the refrigerant is insufficient.
- the compressor 10 is stopped, or if the compressor 10 is of a variable displacement type, the compressor 10 is driven with a reduced displacement to ensure lubrication in the compressor 10 .
- the table (or calculation formula) for calculating the degree of superheat ⁇ T is based on the ph diagram shown in FIG. 4, for example.
- the temperature sensor 2 and the pressure sensor 3 constantly measure the temperature and pressure of the refrigerant drawn in, so the degree of superheat ⁇ T of the refrigerant immediately before being drawn into the compressor 10 is always calculated and grasped. You can do it. Therefore, the degree of superheat ⁇ T can be easily diverted to protect the compressor.
- the heat pump system 100 may further include an environment temperature sensor 30 that measures the temperature of the environment in which the second heat exchanger (heat absorber) 13 is installed. That is, the ambient temperature sensor 30 measures the outside air temperature.
- the first condition C1 includes that the measured value of the environmental temperature sensor 30 is equal to or lower than the predetermined monitoring switching reference environmental temperature Ts
- the second condition C2 is that the measured value of the environmental temperature sensor 30 It may include becoming higher than the monitoring switching reference environmental temperature Ts.
- the compressor 10 can be monitored using the temperature sensor 2, which can be expected to have high pressure estimation accuracy, and using the estimated pressure immediately before suction calculated from the measured value of the temperature sensor 2. It is possible to reliably protect the compressor 10 .
- the outside air temperature is relatively high, the actual intake refrigerant temperature is high, and the actual pressure immediately before intake is high. is also high.
- the refrigerant tends to become a superheated gas. Therefore, it is possible to monitor the compressor 10 by estimating the measured value of the pressure sensor 3 as the estimated pressure immediately before suction using the pressure sensor 3, which can be expected to have high measurement accuracy in a high pressure region, and to operate the compressor 10 more reliably. can be protected.
- the heating operation mode is selected, and the measured value of the environmental temperature sensor 30 is higher than the monitoring switching reference environmental temperature Ts.
- the refrigerant circulation path may be switched so that the cooling operation mode (a mode other than the heating operation mode) is selected when the temperature increases.
- the heat pump system 200 includes a vehicle heat recovery device 40 that absorbs heat generated in the vehicle by the refrigerant circulating in the refrigerant circuit 1, and switches the refrigerant circulation path in the refrigerant circuit 1. and a possible mode switching controller 41 .
- the vehicle heat recovery device 40 includes a bypass refrigerant pipe 50 that allows refrigerant to be sucked into the compressor 10 without passing through the second heat exchanger (heat absorber) 13, and a third heat exchanger provided in the middle of the bypass refrigerant pipe 50. It has a vessel 51.
- the bypass refrigerant pipe 50 is located at a first position P1 on the upstream side of the second heat exchanger (heat absorber) 13 in the refrigerant circuit 1 and a second position between the second heat exchanger (heat absorber) 13 and the accumulator 15. P2 and .
- the third heat exchanger 51 causes the refrigerant to absorb heat (exhaust heat) from the internal combustion engine, storage battery, motor, etc., which are the heat sources H of the vehicle, through a heat recovery heat medium (coolant).
- a heat recovery heat medium coolant
- an expansion mechanism 52 is provided between the first position P ⁇ b>1 where the bypass refrigerant pipe 50 branches from the refrigerant circuit 1 and the third heat exchanger 51 .
- the mode switching control device 41 is realized by an ECU 400 shown in FIG. 8(A).
- the hardware configuration of the ECU 400 is the same as that of the first embodiment.
- a mode switching control processing unit 520 is provided as a functional configuration of the ECU 400, in addition to the first embodiment, a mode switching control processing unit 520 is provided. Function.
- the mode switching control device 41 operates in an outside air heat absorption heating operation mode (corresponding to the heating operation mode in the first embodiment) in which the second heat exchanger (heat absorber) 13 functions as an outdoor unit, and an operation other than the outside air heat absorption heating operation mode. mode, the circulation path of the refrigerant in the refrigerant circuit 1 is switched.
- the refrigerant circulating in the refrigerant circuit 1 is sucked into the compressor 10 via the vehicle heat recovery device 40 without passing through the second heat exchanger (heat absorber) 13. It includes a heat recovery heating mode of operation that allows The operation modes other than the outdoor air heat absorption heating operation mode include the cooling operation mode described in the first embodiment, the defrosting operation mode that melts frost when the outdoor heat exchanger (second heat exchanger 13) is frosted, It also includes a battery heating mode for heating a storage battery by heating a heat recovery heat carrier (coolant).
- the mode switching control device 41 switches the operation mode from the outside air heat absorption heating operation mode to the heat recovery heating operation mode
- the second heat exchanger (heat absorber) 13 upstream of the refrigerant circuit 1
- the first switching valve 55 provided between the expansion mechanism 12 arranged on the side and the first position P1 where the bypass refrigerant pipe 50 branches from the refrigerant pipe 14 is closed, and the bypass refrigerant pipe 50 is provided with
- the second switching valve 56 By opening the second switching valve 56 , the refrigerant is allowed to flow into the bypass refrigerant pipe 50 , pass through the third heat exchanger 51 , and is led to the compressor 10 .
- the switching to the heat recovery heating operation mode is performed based on the state of heat generation in the heat source H, the temperature of the heat recovery heat medium (coolant), and the like.
- the mode switching control device 41 switches the operation mode from the heat recovery heating operation mode to the outside air heat absorption heating operation mode
- the first switching valve 55 is opened, the second switching valve 56 is closed, and the second switching valve 56 is closed.
- the refrigerant is led to the compressor 10 through a second heat exchanger (heat absorber) 13 .
- the mode switching control device 41 switches to the outside air heat absorption heating operation mode. including "switching".
- the second condition C2 which is a condition for monitoring the actual pressure Pf immediately before refrigerant suction based on the measured value of the pressure sensor 3 and estimating the decrease thereof, is that "the mode switching control device 41 is in a mode other than the outside air heat absorption heating operation mode. switching to the operation mode (heat recovery heating operation mode in this embodiment).
- the outside air heat absorption heating operation mode is an operation mode that is selected when the outside air temperature is low. is in a low state. Therefore, even in a low pressure region, the compressor 10 can be monitored using the temperature sensor 2, which can be expected to have high pressure estimation accuracy, and using the estimated pressure immediately before suction calculated from the measured value of the temperature sensor 2. Compressor 10 can be reliably protected.
- the actual intake refrigerant temperature is high and the actual pressure immediately before intake is also high. Therefore, it is possible to monitor the compressor 10 by using the pressure sensor 3, which can be expected to have high measurement accuracy in a high pressure region, and to use the measured value of the pressure sensor 3 as the estimated pressure immediately before suction, thereby protecting the compressor 10 more reliably. can be done.
- the compressor 10 can be protected, the cost of the pressure sensor 3 can be suppressed, and as a result, the cost of the heat pump system 200 as a whole can be suppressed. .
- the intake refrigerant temperature measured by the temperature sensor 2 and the pressure sensor 3 Based on the degree of superheat ⁇ T of the refrigerant calculated from the suctioned refrigerant pressure measured in (1), the driving of the compressor 10 may be suppressed and controlled during overheating.
- temperature sensor 2 and pressure sensor 3 do not have to be integrated, and temperature sensor 2 and pressure sensor 3 do not have to measure at the same time. That is, the temperature sensor 2 may be used for measurement only when the first condition C1 is satisfied, and the pressure sensor 3 may be used for measurement only when the second condition C2 is satisfied. Moreover, the temperature sensor 2 and the pressure sensor 3 do not necessarily have to perform measurements all the time, and the temperature sensor 2 and/or the pressure sensor 3 may perform measurements at necessary timings.
- the temperature sensor 2 and the pressure sensor 3 measure the discharge refrigerant temperature and the discharge refrigerant pressure on the discharge side (downstream side) of the compressor 10, and from the compression characteristics of the compressor 10, the actual intake refrigerant temperature and the actual pressure may be estimated.
- first conditions C1 second conditions C2
- second conditions C2 Various first conditions C1 (second conditions C2) described above may be combined as appropriate.
- the temperature sensor 2 The driving of the compressor 10 may be controlled based on the measured value of the pressure sensor 3).
- the heat pump system of the present invention it is possible to estimate the state of the sucked refrigerant with high accuracy while keeping costs down, and to protect the compressor.
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Abstract
Description
本発明は、ヒートポンプシステム、およびヒートポンプシステムの制御方法に関する。 The present invention relates to a heat pump system and a heat pump system control method.
従来、冷媒が凝縮と蒸発とを繰り返しながら冷媒管内を循環することによって、冷媒が連続的に放熱および吸熱を行い、室内の空気を冷やしたり暖めたりするヒートポンプが知られている。このようなヒートポンプは例えば冷凍機や建物に設置される空調装置だけでなく、車両に搭載されて車室内の冷暖房を行う車両用空調装置としても使用されている。 Conventionally, heat pumps are known in which the refrigerant continuously radiates heat and absorbs heat by circulating in refrigerant pipes while repeatedly condensing and evaporating, thereby cooling and warming indoor air. Such a heat pump is used not only as a refrigerator or an air conditioner installed in a building, but also as a vehicle air conditioner that is mounted on a vehicle to cool and heat the interior of the vehicle.
ところでヒートポンプには冷媒を圧縮するための圧縮機が設けられているが、圧縮機に吸入される冷媒の圧力が負圧、もしくは負圧に近い状態となったまま圧縮機の駆動を継続させると圧縮機が損傷してしまう可能性がある。このため例えば特許文献1に示されているように、圧縮機に吸入される冷媒の圧力、すなわち吸入冷媒圧力が負圧とならないように圧縮機の駆動を制御する手法が採用されている。具体的に特許文献1には、吸入冷媒圧力を吸入側の圧力センサによって測定し、または、吐出側の圧力センサの測定値から推定することによって冷媒の圧力状態を検知し、圧縮機の駆動を抑制制御することが記載されている。
By the way, the heat pump is provided with a compressor for compressing the refrigerant. The compressor could be damaged. For this reason, as disclosed in
しかしながら、圧縮機の運転態様によっては、圧力が大気圧よりも高い領域であるものの、大気圧に極めて近い条件で圧縮機を定常運転しなければならない場合がある。この場合、定常運転時を基準とした吸入冷媒圧力の微小な低下(負圧へのシフト)を、圧力センサで高精度に測定、検知しなければならないため、圧力センサに高い測定精度が要求される。しかし圧力センサは、この大気圧近辺の測定時の応答性や精度が基本的に悪いという問題があるため、特許文献1に記載の手法では十分な圧力測定精度が得られない。これを解決しようとすると、大気圧近辺の環境でも、より高精度・高応答で測定が可能な圧力センサが必要となりコストアップの要因となり得る。 However, depending on the operating mode of the compressor, there are cases where the compressor must be steadily operated under conditions that are extremely close to the atmospheric pressure, even though the pressure is in a region higher than the atmospheric pressure. In this case, the pressure sensor is required to measure and detect minute drops in refrigerant intake pressure (shift to negative pressure) with high accuracy relative to normal operation, so high measurement accuracy is required for the pressure sensor. be. However, the pressure sensor has a problem of basically poor responsiveness and accuracy at the time of measurement near the atmospheric pressure. In order to solve this problem, a pressure sensor capable of measuring with higher accuracy and higher response is required even in an environment near atmospheric pressure, which may lead to an increase in cost.
そこで本発明は、コストを抑えつつ吸入冷媒の状態を高精度で推定し、圧縮機を保護することが可能なヒートポンプシステム、およびヒートポンプシステムの制御方法を提供する。 Therefore, the present invention provides a heat pump system and a control method for the heat pump system that can estimate the state of the sucked refrigerant with high accuracy while keeping costs down and protect the compressor.
本発明の一態様に係るヒートポンプシステムは、冷媒管によって互いに接続された圧縮機、放熱器、膨張機構、および吸熱器によって構成されるとともに、前記圧縮機、前記放熱器、前記膨張機構、前記吸熱器の順に冷媒が前記冷媒管を循環可能な冷媒回路と、前記冷媒の温度を測定する温度センサと、前記冷媒の圧力を測定する圧力センサと、前記圧縮機に吸入される前記冷媒の圧力低下を判定して、前記圧縮機の駆動に抑制をかけるように該圧縮機を抑制制御する駆動抑制制御装置と、を備え、前記駆動抑制制御装置は、所定の第一の条件が成立する場合に、前記温度センサの測定値から、前記圧縮機に吸入される前記冷媒の前記圧力低下を判定して前記圧縮機を抑制制御し、前記第一の条件と異なる所定の第二の条件が成立する場合に、前記圧力センサの測定値から、前記圧縮機に吸入される前記冷媒の前記圧力低下を判定して、前記圧縮機を抑制制御する。 A heat pump system according to an aspect of the present invention includes a compressor, a radiator, an expansion mechanism, and a heat absorber that are connected to each other by refrigerant pipes, and the compressor, the radiator, the expansion mechanism, and the heat absorber a refrigerant circuit in which refrigerant can circulate through the refrigerant pipe in the order of the vessel, a temperature sensor for measuring the temperature of the refrigerant, a pressure sensor for measuring the pressure of the refrigerant, and a pressure drop of the refrigerant sucked into the compressor and a drive suppression control device that suppresses and controls the compressor so as to suppress the driving of the compressor by determining the determining the pressure drop of the refrigerant sucked into the compressor from the measured value of the temperature sensor, suppressing and controlling the compressor, and satisfying a predetermined second condition different from the first condition; In this case, the pressure drop of the refrigerant sucked into the compressor is determined from the measured value of the pressure sensor, and suppression control is performed on the compressor.
上記ヒートポンプシステムでは、前記第一の条件は、前記温度センサの測定値が、所定の基準温度以下となることを含み、前記第二の条件は、前記温度センサの測定値が、前記基準温度よりも大きくなることを含んでもよい。 In the above heat pump system, the first condition includes that the measured value of the temperature sensor is equal to or lower than a predetermined reference temperature, and the second condition is that the measured value of the temperature sensor is higher than the reference temperature. may also include increasing
上記ヒートポンプシステムは、前記吸熱器が設置された環境の温度を測定する環境温度センサをさらに備え、前記第一の条件は、前記環境温度センサの測定値が、所定の基準環境温度以下となることを含み、前記第二の条件は、前記環境温度センサの測定値が、前記基準環境温度よりも大きくなることを含んでもよい。 The heat pump system further includes an environmental temperature sensor that measures the temperature of the environment in which the heat absorber is installed, and the first condition is that the measured value of the environmental temperature sensor is equal to or lower than a predetermined reference environmental temperature. and the second condition may include that the measured value of the environmental temperature sensor is higher than the reference environmental temperature.
上記ヒートポンプシステムは車両に搭載される車両用空調装置として用いられ、前記車両において発生する熱を、前記冷媒回路を循環する前記冷媒に吸熱させる車両熱回収装置と、前記吸熱器を外気から前記冷媒に吸熱させる室外熱交換器として機能させる外気吸熱暖房運転モードと、前記冷媒回路を循環する前記冷媒を前記吸熱器を経由させずに前記車両熱回収装置を経由させて前記圧縮機に吸入させる熱回収暖房運転モードとの間で、前記冷媒回路における前記冷媒の循環経路を切り替え可能なモード切り替え制御装置と、をさらに備え、前記第一の条件は、前記モード切り替え制御装置が前記外気吸熱暖房運転モードに切り替えることを含み、前記第二の条件は、前記モード切り替え制御装置が前記熱回収暖房運転モードに切り替えることを含んでもよい。 The heat pump system is used as a vehicle air conditioner mounted on a vehicle. and an outdoor air heat absorption heating operation mode in which the refrigerant circulating in the refrigerant circuit functions as an outdoor heat exchanger that absorbs heat into the compressor through the vehicle heat recovery device without passing through the heat absorber. a mode switching control device capable of switching the circulation path of the refrigerant in the refrigerant circuit between the recovery heating operation mode and the mode switching control device, wherein the first condition is that the mode switching control device is in the outside air heat absorption heating operation mode. mode, wherein the second condition may include switching to the heat recovery heating operation mode by the mode switching control device.
上記ヒートポンプシステムでは、前記第一の条件は、定常運転時における前記圧縮機に吸入される直前の前記冷媒の実際の圧力(以下、吸入直前実圧力)が、所定の基準圧力以下となることを含み、前記第二の条件は、定常運転時における前記吸入直前実圧力が、前記基準圧力よりも大きくなることを含んでもよい。 In the heat pump system, the first condition is that the actual pressure of the refrigerant immediately before being sucked into the compressor during steady operation (hereinafter referred to as the actual pressure immediately before suction) is equal to or lower than a predetermined reference pressure. The second condition may include that the actual pressure immediately before suction during steady operation is greater than the reference pressure.
上記ヒートポンプシステムでは、前記圧力センサは、前記圧縮機に吸入される直前の前記冷媒の圧力を測定するようになっており、前記駆動抑制制御装置は、前記吸入直前実圧力を、前記圧力センサの測定値から推定してもよい。 In the above heat pump system, the pressure sensor measures the pressure of the refrigerant immediately before being sucked into the compressor, and the drive suppression control device detects the actual pressure immediately before the suction from the pressure sensor. It may be estimated from measurements.
上記ヒートポンプシステムでは、前記駆動抑制制御装置は、前記第二の条件が成立する場合に、前記圧縮機に吸入される直前の前記冷媒の過熱度を前記温度センサの測定値および前記圧力センサの測定値から算出し、該過熱度に基づいて前記圧縮機の駆動を制御してもよい。 In the above heat pump system, when the second condition is satisfied, the drive suppression control device measures the degree of superheat of the refrigerant immediately before being sucked into the compressor by measuring the measured value of the temperature sensor and the pressure sensor. It may be calculated from the value, and the driving of the compressor may be controlled based on the degree of superheat.
本発明の一態様に係るヒートポンプシステムの制御方法は、冷媒管によって互いに接続された圧縮機、放熱器、膨張機構、および吸熱器によって構成される冷媒回路を、前記圧縮機、前記放熱器、前記膨張機構、前記吸熱器の順に冷媒が循環するヒートポンプの制御方法であって、前記冷媒の温度を測定する温度測定ステップと、前記冷媒の圧力を測定する圧力測定ステップと、前記圧縮機に吸入される前記冷媒の圧力低下を判定して、前記圧縮機の駆動に抑制をかけるように抑制制御する駆動抑制制御ステップと、を含み、前記駆動抑制制御ステップでは、所定の第一の条件が成立する場合に、前記温度センサの測定値から、前記圧縮機に吸入される前記冷媒の前記圧力低下を判定して前記圧縮機を抑制制御し、前記第一の条件と異なる所定の第二の条件が成立する場合に、前記圧力センサの測定値から、前記圧縮機に吸入される前記冷媒の前記圧力低下を判定して、前記圧縮機を抑制制御する。 A control method for a heat pump system according to an aspect of the present invention comprises a refrigerant circuit configured by a compressor, a radiator, an expansion mechanism, and a heat absorber, which are connected to each other by refrigerant pipes. A control method for a heat pump in which a refrigerant circulates in the order of an expansion mechanism and the heat absorber, comprising: a temperature measurement step of measuring the temperature of the refrigerant; a pressure measurement step of measuring the pressure of the refrigerant; and a drive suppression control step of determining a pressure drop of the refrigerant and performing suppression control so as to suppress the driving of the compressor, wherein a predetermined first condition is satisfied in the drive suppression control step. the pressure drop of the refrigerant sucked into the compressor is determined from the measured value of the temperature sensor, the compressor is inhibited and controlled, and a predetermined second condition different from the first condition is satisfied. When the condition is established, the pressure drop of the refrigerant sucked into the compressor is determined from the measured value of the pressure sensor, and the compressor is restrained and controlled.
上記のヒートポンプシステム等によれば、コストを抑えつつ吸入冷媒の状態を高精度で推定し、圧縮機を保護することが可能となる。 According to the above heat pump system, etc., it is possible to estimate the state of the sucked refrigerant with high accuracy while keeping costs down, thereby protecting the compressor.
〔第一実施形態〕
以下、本発明の第一実施形態に係るヒートポンプシステム100について説明する。
ヒートポンプシステム100は、冷媒を用いて室内の空気を冷やしたり暖めたりするものである。ヒートポンプシステム100が設置される場所は特に限定されるものではないが、本実施形態では、車両に搭載されて車室内の冷暖房を行う車両用空調装置(エアコン)にヒートポンプシステム100が用いられる場合について説明する。
[First Embodiment]
A
The
車両用空調装置としてのヒートポンプシステム100は、内燃機関のみを動力とする車両に搭載されてもよいが、内燃機関のみを動力とする車両に比べて内燃機関の排熱のみでは十分な熱量確保が難しいHEV(Hybrid Electric Vehicle)や、内燃機関の排熱による暖房ができないEV(Electric Vehicle)等の車両に好適に用いられる。
The
(全体構成)
図1に示すようにヒートポンプシステム100は、冷媒が循環する冷媒回路1と、冷媒回路1において冷媒の温度を測定する温度センサ2と、冷媒回路1において冷媒の圧力を測定する圧力センサ3と、温度センサ2の測定値および圧力センサ3の測定値に基づいて冷媒回路1における圧縮機10の駆動を抑制制御する駆動抑制制御装置4とを備えている。
(overall structure)
As shown in FIG. 1, the
(冷媒回路)
冷媒回路1は、圧縮機10、第一熱交換器11、膨張機構12、および第二熱交換器13と、これらを互いに接続する冷媒管14とを有している。後述する暖房運転モードでは、冷媒回路1において冷媒が冷媒管14を通じて圧縮機10、第一熱交換器11、膨張機構12、第二熱交換器13の順に循環するようになっている。
ここで本実施形態では、冷媒に「R134a」を用いる場合について説明するが、冷媒の種類は特に限定されるものではなく、例えばR-1234yf等であってもよい。
(refrigerant circuit)
The
Here, in this embodiment, the case where "R134a" is used as the refrigerant will be described, but the type of refrigerant is not particularly limited, and may be, for example, R-1234yf.
(圧縮機)
圧縮機10は、冷媒回路1における上流側から冷媒を吸入して圧縮し、冷媒を高温高圧のガスとして下流側に向けて吐出する。圧縮機10の形式は特に限定されるものではないが、例えばピストン式やスクロール式の電動コンプレッサが採用される。冷媒回路1において圧縮機10の上流側には、冷媒からの液分離を行うアキュムレータ15が設けられている。
(compressor)
The
(第一熱交換器)
第一熱交換器11は、本実施形態では放熱器として機能する。放熱器としての第一熱交換器11では、圧縮機10によって高温高圧のガスとなった冷媒を通過させて冷媒から放熱させ、冷媒を冷却する。ここで第一熱交換器11は車両に設けられたHVAC(Heating Ventilation and Air-Conditioning)20と呼ばれる装置内に配置されている。HVAC20では、ブロア21によって空気流路22に取り込まれた空気Aが、第一熱交換器11において冷媒と熱交換することで暖められ、車室内に供給されるようになっている。すなわち本実施形態では車室内を暖房する暖房運転モードでヒートポンプシステム100が運転されている。
(first heat exchanger)
The
(膨張機構)
膨張機構12は、膨張弁やキャピラリチューブ等によって構成され、第一熱交換器11を通過した高圧の冷媒を減圧、膨張させて低圧の冷媒とする。
(Expansion mechanism)
The
(第二熱交換器)
第二熱交換器13は、本実施形態では吸熱器として機能する。吸熱器としての第二熱交換器13では、膨張機構12によって低圧となった冷媒を通過させて冷媒に吸熱させ、冷媒を加熱する。ここで第二熱交換器13は外気から冷媒に吸熱させる室外熱交換器となっている。
なおヒートポンプシステム100では、不図示の切替弁によって冷媒回路1における冷媒の循環経路を切り替えることで、第二熱交換器13を放熱器として機能させ、第一熱交換器11を吸熱器として機能させる冷房運転モードでの運転も可能となっているが、図示および詳細な説明は省略する。
(Second heat exchanger)
The
In the
(温度センサ)
温度センサ2は、圧縮機10に吸入される直前の冷媒の温度を測定可能となるように、圧縮機10の入口の上流側(アキュムレータ15の下流側)において冷媒管14に設けられている。
(temperature sensor)
The
(圧力センサ)
圧力センサ3は、圧縮機10に吸入される直前の冷媒の圧力を測定可能となるように、圧縮機の入口の上流側において冷媒管14に設けられている。本実施形態においては、温度センサ2および圧力センサ3として、温度センサ2と圧力センサ3とが一体となった圧力/温度センサが設けられている。そしてこの圧力/温度センサでは少なくとも冷媒が冷媒回路を循環している状態において、温度および圧力を同時に、常時測定するようになっている。
(pressure sensor)
The
(駆動抑制制御装置)
駆動抑制制御装置4は、圧縮機10に吸入される冷媒の圧力低下を判定して、圧縮機10の駆動に抑制をかける制御装置である。具体的には、圧縮機10に吸入される直前の冷媒の実際の圧力(以下、吸入直前実圧力Pf)が、圧縮機10の許容下限圧となる「ゲージ圧で0〔MPaG〕」を下回らないように、圧縮機10の駆動を停止させたり、間欠的に駆動させたりといった制御(以下、抑制制御)が行われる。駆動抑制制御装置4では、抑制判定閾圧力Pbを、上記許容下限圧よりも少しだけ高い圧力(例えば、ゲージ圧で0.05〔MPaG〕)に設定しておく。温度センサ2の測定値および/または圧力センサ3の測定値から圧縮機10に吸入される直前の冷媒の圧力を算出(推定)して、この算出(推定)された圧力(以下、吸入直前推定圧力)が、抑制判定閾圧力Pbよりも小さくなったら、抑制制御を実行することになる。
(Driving restraint control device)
The drive
そして駆動抑制制御装置4は、所定の第一の条件C1が成立する場合に、温度センサ2の測定値を利用して吸入直前推定圧力を算出し、この吸入直前推定圧力の圧力低下を判定して、圧縮機10の駆動を抑制制御する。一方で駆動抑制制御装置4は、第一の条件C1と異なる所定の第二の条件C2が成立する場合に、圧力センサ3の測定値を利用して吸入直前推定圧力を推定し、吸入直前推定圧力の低下を判定して圧縮機10を抑制制御する。
Then, when the predetermined first condition C1 is satisfied, the drive
図2(A)に示すように、駆動抑制制御装置4は、エアコン用のECU400で実現される。ECU400は、CPU(Central Processing Unit)402と、ROM(Read Only Memory)やRAM(Random Access Memory)などのメモリ404と、HDD(Hard Disk Drive)やSSD(Solid State Drive)などの不揮発性の記憶部406と、通信制御部408を含んでいる。CPU402、メモリ404、記憶部406、および通信制御部408は内部バス410を介して互いに通信可能に接続されている。通信制御部408は、温度センサ2、圧力センサ3、圧縮機10(の制御ドライバ)と通信回線で接続されており、温度センサ2や圧力センサ3から温度情報及び圧力情報を取得し、圧縮機10に対しては制御信号を送信できるようになっている。
As shown in FIG. 2(A), the drive
記憶部406には、駆動抑制制御プログラムが記憶されている。ECU400は、駆動抑制制御プログラムが記憶部406から読み出されてメモリ404に展開され、メモリ404に展開された駆動抑制制御プログラムがCPU402によって実行されることで、図1に示す駆動抑制制御装置4として機能し、駆動抑制制御処理を行う。
A drive suppression control program is stored in the storage unit 406 . The drive suppression control program is read out from the storage unit 406 and developed in the memory 404, and the drive suppression control program developed in the memory 404 is executed by the
図2(B)には、ECU400によって実現される駆動抑制制御装置4の機能構成を示す。具体的に駆動抑制制御装置4は、駆動抑制実行処理部502、温度検知経由圧力推定処理部504、圧力検知経由圧力推定処理部506、圧力推定方式切り替え処理部508を有する。
FIG. 2(B) shows the functional configuration of the drive
駆動抑制実行処理部502は、温度検知経由圧力推定処理部504又は圧力検知経由圧力推定処理部506のいずれか一方で算出された、圧縮機10に吸入される直前の冷媒圧力(以下、吸入直前推定圧力)が、抑制判定閾圧力(ここではゲージ圧で0.05〔MPaG〕)を下回るか否かを判定し、下回る場合は、圧縮機10の駆動を停止させたり、間欠的に駆動させたりといった抑制制御を実行する。 The drive suppression execution processing unit 502 calculates the refrigerant pressure immediately before being sucked into the compressor 10 (hereinafter referred to as immediately before suction estimated pressure) is below the suppression judgment threshold pressure (0.05 [MPaG] in gauge pressure here). Inhibition control such as
温度検知経由圧力推定処理部504は、温度センサ2の測定値を利用して吸入直前推定圧力(以下、温度検知経由吸入直前推定圧力)を算出する。具体的に温度検知経由圧力推定処理部504、冷媒の温度-圧力関係を示す対比テーブル(または計算式)を記憶しており、温度情報から圧力情報を算出する。この対比テーブル(または計算式)は、例えば図3に示す冷媒の飽和温度と飽和圧力との関係を示す飽和曲線に基づくものであることが好ましい。
The temperature detection-mediated pressure estimation processing unit 504 uses the measured value of the
圧力検知経由圧力推定処理部506は、圧力センサ3の測定値を利用して吸入直前推定圧力(以下、圧力検知経由吸入直前推定圧力)を算出する。なお、本実施形態では、圧力センサ3が、圧縮機10に吸入される直前の冷媒の圧力を測定していることから、この測定結果を、そのまま圧力検知経由吸入直前推定圧力とする。一方で、圧力センサ3の配置場所(測定場所)が、圧縮機10に吸入される直前から離れている場合は、冷媒経路内の圧力勾配を意味する対比テーブルや計算式を参照して、圧力検知吸入直前推定圧力を算出する。
The pressure detection-mediated pressure estimation processing unit 506 uses the measured value of the
圧力推定方式切り替え処理部508は、駆動抑制実行処理部502における圧力監視時に、温度検知経由圧力推定処理部504で算出される温度検知経由吸入直前推定圧力を利用するか、圧力検知経由圧力推定処理部506で算出される圧力検知経由吸入直前推定圧力を利用するか、を切り替える。具体的には、切り替え判定用の条件に関する情報(ここでは、第一の条件C1、第二の条件C2)を保持する。圧力推定方式切り替え処理部508、これらの条件判定を実行し、温度検知経由吸入直前推定圧力を利用した冷媒圧力監視と、圧力検知経由吸入直前推定圧力を利用した冷媒圧力監視とを切り替える。 When pressure is monitored by the drive suppression execution processing unit 502, the pressure estimation method switching processing unit 508 uses the estimated pressure immediately before suction via temperature detection calculated by the pressure estimation processing unit 504 via temperature detection, or performs pressure estimation processing via pressure detection. Switches between using the estimated pre-inhalation pressure via pressure detection calculated in the unit 506 . Specifically, it holds information about conditions for switching determination (here, first condition C1 and second condition C2). A pressure estimation method switching processing unit 508 executes these condition determinations, and switches between refrigerant pressure monitoring using the estimated pressure immediately before suction via temperature detection and refrigerant pressure monitoring using the estimated pressure immediately before suction via pressure detection.
(第一の条件)
温度センサ2の測定値によって冷媒の吸入直前実圧力Pfを監視し、その低下を推定(判定)する条件となる第一の条件C1は、「温度センサ2の測定値が、所定の監視切替基準温度Tr以下となること」を含んでいる。この監視切替基準温度Trは、例えば、-20〔℃〕以上10〔℃〕以下の範囲内に設定されることが好ましく、望ましくは-15〔℃〕以上5〔℃〕以下の範囲内に設定し、さらに望ましくは0〔℃〕以下に設定され、より望ましくは-5〔℃〕以下に設定され、ここでは-10〔℃〕に設定している。
(First condition)
The first condition C1, which is a condition for monitoring the actual pressure Pf immediately before suction of the refrigerant by the measured value of the
第一の条件C1が成立する場合には、圧力推定方式切り替え処理部508は、温度検知経由圧力推定処理部504において温度センサ2の測定値から算出される温度検知経由吸入直前推定圧力を監視する命令を駆動抑制実行処理部502に送信する。この命令を受けた駆動抑制実行処理部502は、温度検知経由吸入直前推定圧力を経時的に参照し、この温度検知経由吸入直前推定圧力の値が、所定の抑制判定閾圧力Pb以下となった場合に、冷媒の吸入直前実圧力Pfが許容下限圧に近づいたと推定して圧縮機10の駆動を抑制制御する。ここで抑制判定閾圧力Pbはここではゲージ圧で0.05〔MPaG〕を例示したが、本発明はこれに限定されず、例えばゲージ圧で0.01〔MPaG〕以上の範囲内にある値であることが好ましく、より安全側としては、0.1〔MPaG〕以上1〔MPaG〕以下の範囲内の値であることがより好ましい。
When the first condition C1 is satisfied, the pressure estimation method switching processing unit 508 monitors the pre-inhalation estimated pressure via temperature detection calculated from the measured value of the
(第二の条件)
圧力センサ3の測定値によって冷媒の吸入直前実圧力Pfを監視し、その低下を推定(判定)する条件となる第二の条件C2は、「温度センサ2の測定値が、上記の基準温度Trよりも大きくなること」を含んでいる。第二の条件C2が成立する場合には、圧力推定方式切り替え処理部508は、圧力検知経由圧力推定処理部506において圧力センサ3の測定値から算出される圧力検知経由吸入直前推定圧力を監視する命令を駆動抑制実行処理部502に送信する。この命令を受けた駆動抑制実行処理部502は、圧力検知経由吸入直前推定圧力を経時的に参照し、この圧力検知経由吸入直前推定圧力の値が、所定の抑制判定閾圧力Pb以下となった場合に、冷媒の吸入直前実圧力Pfが許容下限値に近づいたと推定して圧縮機10の駆動を抑制制御する。
(Second condition)
The second condition C2, which is a condition for monitoring the actual pressure Pf immediately before suction of the refrigerant based on the measured value of the
(ヒートポンプシステムの制御方法(制御プログラム))
次に図4を参照して、駆動抑制制御装置4による圧縮機10の抑制制御を行う手順について説明する。
まず、少なくとも冷媒が冷媒回路1を循環している定常運転時において、温度センサ2および圧力センサ3によって冷媒の温度(以下、吸入冷媒温度)および圧力(以下、吸入冷媒圧力)を測定するステップS1を実行する。ここで定常運転時とは、異常ではない状態(例えば冷媒管14から冷媒が漏れている状態や、冷媒管14が閉塞されているような状態等)でヒートポンプシステム100が運転されている時のことを示す。
(Heat pump system control method (control program))
Next, with reference to FIG. 4, a procedure for performing suppression control of the
First, at least during steady operation in which the refrigerant circulates in the
次に、異常時に圧縮機10の駆動に抑制をかけるために、冷媒の圧力を監視するステップS2を実行する。ステップS2では、まず温度センサ2の測定値が、監視切替基準温度Tr以下となっているか否かを判定するステップS3が実行される。
Next, in order to suppress the driving of the
そしてステップS3で温度センサ2の測定値が監視切替基準温度Tr以下となる場合、第一の条件C1が成立するとして(YES)、温度センサ2の測定値から、温度検知経由吸入直前推定圧力を算出するステップS4aを実行する。一方、ステップS3で温度センサ2の測定値が監視切替基準温度Trよりも大きくなる場合、第一の条件C1が成立せず、第二の条件C2が成立するとして(NO)、圧力センサ3の測定値をそのまま圧力検知経由吸入直前推定圧力とするステップS4bを実行する。
If the measured value of the
ステップS4aまたはステップS4bの実行後、吸入直前推定圧力が、抑制判定閾圧力Pb以下となっているか否かを判定するステップS5を実行する。ステップS5において吸入直前推定圧力が抑制判定閾圧力Pb以下となっている場合(YES)、冷媒の吸入直前実圧力Pfが許容下限値に近づいたと推定して圧縮機10の駆動を抑制制御するステップS6が実行される。その後、ステップS1に戻る。一方、ステップS5において吸入直前推定圧力が抑制判定閾圧力Pbよりも大きくなっている場合(NO)、冷媒の吸入直前実圧力Pfが許容下限値から安全側に離れたと推定して、抑制制御を行わずにステップS1に戻る。
After executing step S4a or step S4b, step S5 is executed to determine whether or not the pre-inhalation estimated pressure is equal to or lower than the suppression determination threshold pressure Pb. If the estimated pressure immediately before suction is equal to or lower than the suppression determination threshold pressure Pb in step S5 (YES), it is estimated that the actual pressure Pf immediately before suction of the refrigerant has approached the allowable lower limit, and the drive of the
(作用効果)
以上説明した本実施形態のヒートポンプシステム100によれば、第一の条件C1が成立する場合には、温度センサ2の測定値から吸入直前推定圧力を算出し、第二の条件C2が成立する場合には圧力センサ3の測定値を吸入直前推定圧力と推定して、この吸入冷媒圧力が、抑制判定閾圧力Pbよりも低下した場合に、圧縮機10を抑制制御するようになっている。
(Effect)
According to the
そして第一の条件C1である「温度センサ2の測定値が、所定の監視切替基準温度Tr以下となること」という判定により、圧力センサ3では監視精度(圧力推定精度)が悪化し易いが、温度センサ2では監視精度(圧力推定精度)を十分に確保できる。また、第二の条件C2である「温度センサ2の測定値が、上記の基準温度Trよりも大きくなること」という判定により、圧力センサ3では監視精度(圧力推定制度)を十分に確保できるが、温度センサ2では監視精度(圧力推定精度)が悪化し易い態様を満たすことができる。このように、温度センサ2と圧力センサ3の各々が得意とする条件を設定することによって、例えば、すべての条件(測定範囲)で高い測定精度を出すことができる圧力センサ3を用いなくて済むという利点が得られる。つまり、圧力センサ3では監視精度が悪化し易い、冷媒の吸入直前実圧力Pfが負圧、もしくは大気圧に近い圧力となった状態を圧力センサ3に代わって温度センサ2で監視できる。結果、圧力センサ3が苦手とする測定範囲を温度センサ2でカバーすることで圧力センサ3のコストを抑えることができ、ヒートポンプシステム100全体のコストを抑えつつ、吸入冷媒の状態を高精度で推定し、圧縮機10を確実に保護することが可能となる。
The first condition C1, ie, the determination that "the measured value of the
また本実施形態では、第一の条件C1が、温度センサ2の測定値が上記の監視切替基準温度Tr(-10〔℃〕)以下となることを含んでいる。図3に示すように、冷媒が-10〔℃〕になると、飽和時、即ち、圧縮機10の吸入直前時の冷媒圧力がゲージ圧で0.1〔MPaG〕になり、圧力センサ3による圧力測定精度が悪化し易い圧力領域に近づく。そこで、冷媒が-10〔℃〕以下の場合は、十分に温度測定精度が得られる温度センサ2を用い、温度センサ2の測定値から吸入直前推定圧力を算出して監視することで、圧縮機10を確実に保護することができる。
Also, in this embodiment, the first condition C1 includes that the measured value of the
ところで圧縮機10に吸入される直前の冷媒が、丁度、飽和蒸気状態の場合は、図5に示すp-h線図における飽和蒸気線L上の特定点Eに位置する。この特定点Eの冷媒の温度を温度センサ2で測定すれば、図3の飽和曲線から、冷媒の圧力を正しく推定できる。一方、圧縮機10に吸入される直前の冷媒が過熱ガスになっている場合には、冷媒は図5に示す飽和蒸気線Lよりも比エンタルピーの高い領域の特定点E1に位置する。
By the way, when the refrigerant just before being sucked into the
そして冷媒の特定点E1を通過する等温線M1は、図5の縦軸(圧力軸)に沿って湾曲するように延びる。仮に、冷媒にさらに熱が加えられて、同一圧力Pxのまま吸入直前の冷媒の過熱度が上昇すると、その冷媒は特異点E2、特異点E3のように右側にシフトする。特異点E2を通過する等温線M2や,特異点E3を通過する等温線M3に示されるように、冷媒の過熱度が変化すれば、圧力Pxが同じであっても、冷媒の温度は上昇する。換言すると、冷媒が過熱ガス状態の場合は、温度センサ2で冷媒温度を測定しても、図3の飽和曲線のみ(つまり、冷媒が図5の飽和蒸気線L上に位置するという仮定下)では、圧力推定に誤差が生じる。エアコンの運転では、冷媒の吸入直前温度が上昇するほど、過熱度が上昇する傾向となるため、温度センサ2による圧力算出精度が悪化し易い。
The isothermal line M1 passing through the specific point E1 of the refrigerant extends curvedly along the vertical axis (pressure axis) in FIG. If the refrigerant is further heated and the degree of superheating of the refrigerant increases immediately before suction while the pressure Px remains the same, the refrigerant shifts to the right, as shown at singular points E2 and E3. As indicated by the isothermal line M2 passing through the singular point E2 and the isothermal line M3 passing through the singular point E3, if the degree of superheating of the refrigerant changes, the temperature of the refrigerant rises even if the pressure Px remains the same. . In other words, when the refrigerant is in a superheated gas state, even if the refrigerant temperature is measured by the
この点、本実施形態では第二の条件C2が、温度センサ2の測定値が上記の監視切替基準温度Tr(-10〔℃〕)よりも大きくなることを含んでいる。この条件は、過熱度が上昇し易い運転条件と表現することもできる。この条件は、圧力センサ3でも、十分な圧力測定精度を期待できる状態であると同時に、温度センサ2にとっては過熱状態によって圧力推定精度が悪化し易い状態と言える。結果、圧力センサ3で測定した吸入冷媒圧力を圧縮機10の監視に用いることができ、圧縮機10を確実に保護することができる。
In this regard, in the present embodiment, the second condition C2 includes that the measured value of the
圧力センサ3にとっては、第一の条件C1と第二の条件C2とを分ける閾値となる監視切替基準温度Trが高いほうが望ましい。例えば、図3に示すように冷媒が飽和蒸気であると仮定した場合において、監視切替基準温度Trは、監視切替基準圧力Prに換算することもできる。監視切替基準圧力Prで考えると、その圧力(ゲージ圧)が、0.03〔MPaG〕以上0.31〔MPaG〕以下の範囲内に設定されることが好ましい。その結果、圧力センサ3が苦手とするより広い範囲を、温度センサ2によってカバーすることができ、より確実に圧縮機10を保護することができる。
For the
つまり本実施形態においては、第一の条件C1が、定常運転時における冷媒の吸入直前実圧力(何らかの計算によって推定される吸入直前推定圧力を含む)が、上記の監視切替基準圧力Pr以下となることを含み、第二の条件C2は、定常運転時における吸入直前実圧力が、上記の監視切替基準圧力Prよりも大きくなることを含んでいてもよい。すなわち温度センサ2によらずに吸入直前実圧力を直接的に測定または推定できる場合には、第一の条件C1と第二の条件C2とを分ける閾値として、上記の監視切替基準温度Trではなく、監視切替基準圧力Prを用いてもよい。
That is, in the present embodiment, the first condition C1 is that the actual pressure immediately before suction of the refrigerant (including the estimated pressure immediately before suction estimated by some calculation) during steady operation is equal to or lower than the monitoring switching reference pressure Pr. In addition, the second condition C2 may include that the actual pressure immediately before intake during steady operation is higher than the monitoring switching reference pressure Pr. That is, when the actual pressure immediately before suction can be directly measured or estimated without using the
ここで本実施形態においては、駆動抑制制御装置4はさらに、図2に示すように過熱時抑制実行処理部510を備えるようにしてもよい。第二の条件C2が成立する場合、即ち過熱度が高まり易い状態の場合に、駆動抑制実行処理部502による抑制制御に加えて、過熱時抑制実行処理部510が、温度センサ2の測定値および圧力センサ3の測定値から算出される冷媒の過熱度に基づいて、圧縮機10を抑制制御してもよい。過熱度が異常に高くなる場合は、例えば、経路内の冷媒の循環量が不足している可能性があり、そのまま運転を継続すると、希薄冷媒に基づく潤滑不足で圧縮機10がロックする。そこで、圧縮機10を低容量運転することで、冷媒の循環量を増大させて潤滑不足を回避し、圧縮機10の故障を予防する。なお本実施形態では、この制御を「過熱時抑制制御」と称する。
Here, in the present embodiment, the drive
この場合、駆動抑制制御装置4の過熱時抑制実行処理部510が、冷媒の状態を示すテーブル(または計算式)を記憶しており、このテーブル(または計算式)に基づき、温度センサ2で測定した吸入冷媒温度および圧力センサ3で測定した吸入冷媒圧力の双方から、圧縮機に吸入される直前の冷媒の過熱度ΔTを算出する。過熱時抑制実行処理部510は、この過熱度ΔTを監視しておくようにし、過熱度ΔTが所定の抑制判定閾過熱度ΔTbよりも大きい場合には、例えば冷媒が不足していると推定して、圧縮機10の駆動を停止させたり、圧縮機10が可変容量タイプである場合には容量を小さくして駆動させたりすることで圧縮機10内の潤滑を確保する。なお過熱度ΔTを算出するためのテーブル(または計算式)は、例えば図4に示すp-h線図に基づくものである。
In this case, the overheat suppression execution processing unit 510 of the drive
そして本実施形態では常時、温度センサ2および圧力センサ3で吸入冷媒温度および吸入冷媒圧力を測定しているため、常時、圧縮機10に吸入される直前の冷媒の過熱度ΔTを算出して把握することができるようになっている。よって、容易に過熱度ΔTを圧縮機の保護に転用することができる。
In this embodiment, the
〔変形例〕
また図6に示すように、本実施形態においてはヒートポンプシステム100が第二熱交換器(吸熱器)13の設置された環境の温度を測定する環境温度センサ30をさらに備えていてもよい。すなわち環境温度センサ30が外気温度を測定するようになっている。この場合、第一の条件C1は、環境温度センサ30の測定値が所定の監視切替基準環境温度Ts以下となることを含み、第二の条件C2は、環境温度センサ30の測定値が上記の監視切替基準環境温度Tsよりも大きくなることを含んでいてもよい。
[Modification]
Further, as shown in FIG. 6, in the present embodiment, the
このように環境温度センサ30の測定値が監視切替基準環境温度Ts(例えばTs=5〔℃〕)以下となる第一の条件C1においては、外気温度が低い状態であり、実際の吸入冷媒温度が低く、結果、吸入直前実圧力も低い状態となっている。したがって圧力が低い領域においても、高い圧力推定精度を期待できる温度センサ2を用い、温度センサ2の測定値から算出した吸入直前推定圧力を利用して、圧縮機10を監視することができ、より確実に圧縮機10を保護することが可能となる。
In the first condition C1 under which the measured value of the
一方で、環境温度センサ30の測定値が監視切替基準環境温度Tsよりも大きくなる第二の条件C2においては、外気温度がある程度高い状態であり、実際の吸入冷媒温度が高く、吸入直前実圧力も高い状態となっている。しかも圧縮機10の吸入直前において、冷媒が過熱ガスとなり易い。したがって圧力が高い領域において測定精度を期待できる圧力センサ3を用い、圧力センサ3の測定値を吸入直前推定圧力と推定して、圧縮機10を監視することができ、より確実に圧縮機10を保護することが可能となる。
On the other hand, under the second condition C2 in which the measured value of the
なお、環境温度センサ30の測定値が上記の監視切替基準環境温度Ts以下となった際には暖房運転モードが選択され、環境温度センサ30の測定値が上記の監視切替基準環境温度Tsよりも大きくなった際には、冷房運転モード(暖房運転モード以外のモード)が選択されるように、冷媒の循環経路が切り替えられてもよい。
When the measured value of the
〔第二実施形態〕
次に、本発明の第二実施形態に係るヒートポンプシステム200について説明する。
図7に示すように本実施形態に係るヒートポンプシステム200は、車両において発生する熱を、冷媒回路1を循環する冷媒に吸熱させる車両熱回収装置40と、冷媒回路1における冷媒の循環経路を切り替え可能なモード切り替え制御装置41とをさらに備えている。
[Second embodiment]
Next, a
As shown in FIG. 7, the
(熱回収装置)
車両熱回収装置40は、第二熱交換器(吸熱器)13を経由させずに圧縮機10に冷媒を吸入させるバイパス冷媒管50と、バイパス冷媒管50の途中に設けられた第三熱交換器51とを有している。
(Heat recovery device)
The vehicle
バイパス冷媒管50は、冷媒回路1における第二熱交換器(吸熱器)13の上流側の第一位置P1と、第二熱交換器(吸熱器)13とアキュムレータ15との間の第二位置P2と、を接続している。
The
第三熱交換器51は、熱回収用熱媒体(クーラント)を介して車両の熱源Hとなる内燃機関、蓄電池、モーター等からの熱(排熱)を冷媒に吸熱させる。バイパス冷媒管50において、当該バイパス冷媒管50が冷媒回路1から分岐する第一位置P1と、第三熱交換器51との間には膨張機構52が設けられている。
The
(モード切り替え制御装置)
モード切り替え制御装置41は、図8(A)に示すECU400で実現される。なお、ECU400のハード構成は、第一実施形態と同様である。図8(B)に示すように、ECU400の機能構成として、第一実施形態に加えて、モード切り替え制御処理部520を備えており、このモード切り替え制御処理部520が、モード切り替え制御装置41として機能する。モード切り替え制御装置41は、第二熱交換器(吸熱器)13を室外機として機能させる外気吸熱暖房運転モード(第一実施形態における暖房運転モードに相当)と、外気吸熱暖房運転モード以外の運転モードとの間で、冷媒回路1における冷媒の循環経路を切り替える。外気吸熱暖房運転モード以外の運転モードには、冷媒回路1を循環する冷媒を、第二熱交換器(吸熱器)13を経由させずに車両熱回収装置40を経由させて圧縮機10に吸入させる熱回収暖房運転モードが含まれる。なお外気吸熱暖房運転モード以外の運転モードには、第一実施形態で説明した冷房運転モードや、室外熱交換器(第二熱交換器13)の着霜時に霜を溶かす除霜運転モードや、熱回収用熱媒体(クーラント)を加熱して蓄電池を加温するバッテリ加熱モード等も含まれる。
(Mode switching control device)
The mode
より具体的には、モード切り替え制御装置41が、外気吸熱暖房運転モードから熱回収暖房運転モードへと運転モードを切り替える際には、冷媒回路1において第二熱交換器(吸熱器)13の上流側に配置された膨張機構12と、バイパス冷媒管50が冷媒管14から分岐する第一位置P1との間に設けられた第一切替弁55を閉塞するとともに、バイパス冷媒管50に設けられた第二切替弁56を開放し、冷媒をバイパス冷媒管50に流入させて第三熱交換器51を通過させ、圧縮機10に導くようになっている。なお、熱回収暖房運転モードへの切り替えは、熱源Hにおける発熱の状況や熱回収用熱媒体(クーラント)の温度等に基づいて実施される。
More specifically, when the mode
一方、モード切り替え制御装置41が、熱回収暖房運転モードから外気吸熱暖房運転モードへ運転モードを切り替える際には、上記の第一切替弁55を開放するとともに第二切替弁56を閉塞し、第二熱交換器(吸熱器)13を通じて冷媒を圧縮機10に導くようになっている。
On the other hand, when the mode
(第一の条件)
本実施形態において温度センサ2の測定値によって冷媒の吸入直前実圧力Pfを監視し、その低下を推定する条件となる第一の条件C1は、「モード切り替え制御装置41が外気吸熱暖房運転モードに切り替えること」を含んでいる。
(First condition)
In this embodiment, the actual pressure Pf immediately before refrigerant suction is monitored by the measured value of the
(第二の条件)
一方で、圧力センサ3の測定値によって冷媒の吸入直前実圧力Pfを監視し、その低下を推定する条件となる第二の条件C2は、「モード切り替え制御装置41が外気吸熱暖房運転モード以外の運転モード(本実施形態では熱回収暖房運転モード)に切り替えること」を含んでいる。
(Second condition)
On the other hand, the second condition C2, which is a condition for monitoring the actual pressure Pf immediately before refrigerant suction based on the measured value of the
(作用効果)
以上説明した本実施形態のヒートポンプシステム200によれば、外気吸熱暖房運転モードは外気温度が低い状態で選択される運転モードであるため、実際の吸入冷媒温度が低く、結果、吸入直前実圧力も低い状態となっている。したがって圧力が低い領域においても、高い圧力推定精度を期待できる温度センサ2を用い、温度センサ2の測定値から算出した吸入直前推定圧力を利用して、圧縮機10を監視することができ、より確実に圧縮機10を保護することができる。
(Effect)
According to the
一方で熱回収暖房運転モードは、実際の吸入冷媒温度が高く、吸入直前実圧力も高い状態となっている。したがって圧力が高い領域において測定精度を期待できる圧力センサ3を用い、圧力センサ3の測定値を吸入直前推定圧力として、圧縮機10を監視することができ、より確実に圧縮機10を保護することができる。
On the other hand, in the heat recovery heating operation mode, the actual intake refrigerant temperature is high and the actual pressure immediately before intake is also high. Therefore, it is possible to monitor the
したがって圧力センサ3の測定精度が高くなくとも、圧縮機10を保護することが可能となり、圧力センサ3のコストを抑えることができ、この結果、ヒートポンプシステム200全体のコストを抑えることが可能である。
Therefore, even if the measurement accuracy of the
本実施形態においても、第一実施形態と同様に第二の条件C2が成立する場合、すなわち熱回収暖房運転モードに切り替えられた場合に、温度センサ2で測定された吸入冷媒温度および圧力センサ3で測定された吸入冷媒圧力から算出される冷媒の過熱度ΔTに基づいて、圧縮機10の駆動を過熱時抑制制御してもよい。
In this embodiment, as in the first embodiment, when the second condition C2 is satisfied, that is, when the operation mode is switched to the heat recovery heating operation mode, the intake refrigerant temperature measured by the
ここで本発明は上述の実施の形態に限定されるものではなく、本発明の要旨を逸脱しない範囲内において種々変更を加え得ることは勿論である。
例えば、温度センサ2および圧力センサ3は一体型である必要はなく、また、温度センサ2および圧力センサ3が同時に測定を行わなくともよい。すなわち、第一の条件C1が成立する場合に限って温度センサ2での測定を行い、第二の条件C2が成立する場合に限って圧力センサ3で測定を行うようにしてもよい。また温度センサ2および圧力センサ3は必ずしも常時測定を行わなくともよく、必要なタイミングで温度センサ2による測定、および/または圧力センサ3による測定を行ってもよい。
Here, the present invention is not limited to the above-described embodiments, and it goes without saying that various modifications can be made without departing from the gist of the present invention.
For example,
また温度センサ2および圧力センサ3は、圧縮機10の吐出側(下流側)で吐出冷媒温度、吐出冷媒圧力を測定し、圧縮機10の圧縮特性から、実際の吸入冷媒温度、吸入直前実圧力を推定するようにしてもよい。
The
上述した様々な第一の条件C1(第二の条件C2)は適宜組み合わせてもよく、例えば上述したすべての第一の条件C1(第二の条件C2)を満足する場合に、温度センサ2(圧力センサ3)の測定値に基づき圧縮機10の駆動を制御してもよい。
Various first conditions C1 (second conditions C2) described above may be combined as appropriate. For example, when all the first conditions C1 (second conditions C2) described above are satisfied, the temperature sensor 2 ( The driving of the
本発明のヒートポンプシステムによれば、コストを抑えつつ吸入冷媒の状態を高精度で推定し、圧縮機を保護することが可能となる。 According to the heat pump system of the present invention, it is possible to estimate the state of the sucked refrigerant with high accuracy while keeping costs down, and to protect the compressor.
1 冷媒回路
2 温度センサ
3 圧力センサ
4 駆動抑制制御装置
10 圧縮機
11 第一熱交換器
12 膨張機構
13 第二熱交換器
14 冷媒管
30 環境温度センサ
40 車両熱回収装置
41 モード切り替え制御装置
100、200 ヒートポンプシステム
400 ECU
Pf 吸入直前実圧力
Pb 抑制判定閾圧力
Tr 監視切替基準温度
Ts 監視切替基準環境温度
ΔT 過熱度
ΔTb 抑制判定閾過熱度
1
Pf Actual pressure immediately before intake Pb Suppression judgment threshold pressure Tr Monitoring switching reference temperature Ts Monitoring switching reference environmental temperature ΔT Superheat degree ΔTb Suppression judgment threshold superheat degree
Claims (8)
前記冷媒の温度を測定する温度センサと、
前記冷媒の圧力を測定する圧力センサと、
前記圧縮機に吸入される前記冷媒の圧力低下を判定して、前記圧縮機の駆動に抑制をかけるように該圧縮機を抑制制御する駆動抑制制御装置と、
を備え、
前記駆動抑制制御装置は、
所定の第一の条件が成立する場合に、前記温度センサの測定値から、前記圧縮機に吸入される前記冷媒の前記圧力低下を判定して前記圧縮機を抑制制御し、
前記第一の条件と異なる所定の第二の条件が成立する場合に、前記圧力センサの測定値から、前記圧縮機に吸入される前記冷媒の前記圧力低下を判定して、前記圧縮機を抑制制御するヒートポンプシステム。 A compressor, a radiator, an expansion mechanism, and a heat absorber are connected to each other by refrigerant pipes, and the refrigerant can circulate through the refrigerant pipes in the order of the compressor, the radiator, the expansion mechanism, and the heat absorber. a refrigerant circuit,
a temperature sensor that measures the temperature of the refrigerant;
a pressure sensor that measures the pressure of the refrigerant;
a drive suppression control device that determines a pressure drop of the refrigerant sucked into the compressor and suppresses and controls the compressor so as to suppress the driving of the compressor;
with
The drive suppression control device includes:
when a predetermined first condition is established, the pressure drop of the refrigerant sucked into the compressor is determined from the measurement value of the temperature sensor, and suppression control is performed on the compressor;
When a predetermined second condition different from the first condition is established, the pressure drop of the refrigerant sucked into the compressor is determined from the measurement value of the pressure sensor, and the compressor is suppressed. Heat pump system to control.
前記第二の条件は、前記温度センサの測定値が、前記基準温度よりも大きくなることを含む請求項1に記載のヒートポンプシステム。 The first condition includes that the measured value of the temperature sensor is equal to or lower than a predetermined reference temperature,
2. The heat pump system according to claim 1, wherein said second condition includes that the measured value of said temperature sensor is higher than said reference temperature.
前記第一の条件は、前記環境温度センサの測定値が、所定の基準環境温度以下となることを含み、
前記第二の条件は、前記環境温度センサの測定値が、前記基準環境温度よりも大きくなることを含む請求項1または2に記載のヒートポンプシステム。 further comprising an environmental temperature sensor that measures the temperature of the environment in which the heat absorber is installed;
The first condition includes that the measured value of the environmental temperature sensor is equal to or lower than a predetermined reference environmental temperature,
3. The heat pump system according to claim 1, wherein said second condition includes that the measured value of said environmental temperature sensor is higher than said reference environmental temperature.
前記車両において発生する熱を、前記冷媒回路を循環する前記冷媒に吸熱させる車両熱回収装置と、
前記吸熱器を外気から前記冷媒に吸熱させる室外熱交換器として機能させる外気吸熱暖房運転モードと、前記冷媒回路を循環する前記冷媒を前記吸熱器を経由させずに前記車両熱回収装置を経由させて前記圧縮機に吸入させる熱回収暖房運転モードとの間で、前記冷媒回路における前記冷媒の循環経路を切り替え可能なモード切り替え制御装置と、
をさらに備え、
前記第一の条件は、前記モード切り替え制御装置が前記外気吸熱暖房運転モードに切り替えることを含み、
前記第二の条件は、前記モード切り替え制御装置が前記熱回収暖房運転モードに切り替えることを含むヒートポンプシステム。 The heat pump system according to any one of claims 1 to 3, which is used as a vehicle air conditioner mounted on a vehicle,
a vehicle heat recovery device that causes the refrigerant circulating in the refrigerant circuit to absorb heat generated in the vehicle;
An outside air heat absorption heating operation mode in which the heat absorber functions as an outdoor heat exchanger that absorbs heat from the outside air into the refrigerant, and an outside air heat absorption heating operation mode in which the refrigerant circulating in the refrigerant circuit is passed through the vehicle heat recovery device without passing through the heat absorber. a mode switching control device capable of switching the circulation path of the refrigerant in the refrigerant circuit between a heat recovery heating operation mode in which the refrigerant is sucked into the compressor by
further comprising
The first condition includes switching the mode switching control device to the outside air endothermic heating operation mode,
The heat pump system, wherein the second condition includes switching the mode switching control device to the heat recovery heating operation mode.
前記第二の条件は、定常運転時における前記吸入直前実圧力が、前記基準圧力よりも大きくなることを含む請求項1から4のいずれか一項に記載のヒートポンプシステム。 The first condition includes that the actual pressure of the refrigerant immediately before being sucked into the compressor during steady operation (hereinafter referred to as the actual pressure immediately before suction) is equal to or lower than a predetermined reference pressure,
5. The heat pump system according to any one of claims 1 to 4, wherein the second condition includes that the actual pressure immediately before suction during steady operation is higher than the reference pressure.
前記駆動抑制制御装置は、前記吸入直前実圧力を、前記圧力センサの測定値から推定する請求項5に記載のヒートポンプシステム。 The pressure sensor measures the pressure of the refrigerant immediately before being sucked into the compressor,
6. The heat pump system according to claim 5, wherein the drive suppression control device estimates the actual pressure immediately before suction from the measured value of the pressure sensor.
前記冷媒の温度を測定する温度測定ステップと、
前記冷媒の圧力を測定する圧力測定ステップと、
前記圧縮機に吸入される前記冷媒の圧力低下を判定して、前記圧縮機の駆動に抑制をかけるように抑制制御する駆動抑制制御ステップと、
を含み、
前記駆動抑制制御ステップでは、
所定の第一の条件が成立する場合に、前記温度センサの測定値から、前記圧縮機に吸入される前記冷媒の前記圧力低下を判定して前記圧縮機を抑制制御し、
前記第一の条件と異なる所定の第二の条件が成立する場合に、前記圧力センサの測定値から、前記圧縮機に吸入される前記冷媒の前記圧力低下を判定して、前記圧縮機を抑制制御するヒートポンプシステムの制御方法。 A heat pump in which a refrigerant circulates through a refrigerant circuit composed of a compressor, a radiator, an expansion mechanism, and a heat absorber, which are connected to each other by refrigerant pipes, in the order of the compressor, the radiator, the expansion mechanism, and the heat absorber. A control method comprising:
a temperature measurement step of measuring the temperature of the refrigerant;
a pressure measuring step of measuring the pressure of the refrigerant;
a drive suppression control step of determining a pressure drop of the refrigerant sucked into the compressor and performing suppression control so as to suppress the driving of the compressor;
including
In the drive suppression control step,
when a predetermined first condition is established, the pressure drop of the refrigerant sucked into the compressor is determined from the measurement value of the temperature sensor, and suppression control is performed on the compressor;
When a predetermined second condition different from the first condition is established, the pressure drop of the refrigerant sucked into the compressor is determined from the measurement value of the pressure sensor, and the compressor is suppressed. A control method for a controlled heat pump system.
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| CN202380020178.XA CN118647830A (en) | 2022-02-18 | 2023-01-24 | Heat pump system and control method of heat pump system |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61268958A (en) * | 1985-05-24 | 1986-11-28 | 松下電器産業株式会社 | Defrostation controller for air conditioner |
| JP2022010435A (en) * | 2020-06-29 | 2022-01-17 | パナソニックIpマネジメント株式会社 | Air conditioner |
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| JP4285060B2 (en) * | 2003-04-23 | 2009-06-24 | 株式会社デンソー | Vapor compression refrigerator |
| JP2010013017A (en) * | 2008-07-04 | 2010-01-21 | Denso Corp | Air conditioning device for vehicle |
| JP2011168071A (en) * | 2010-02-16 | 2011-09-01 | Calsonic Kansei Corp | Air conditioner for vehicle |
| JP2017180995A (en) * | 2016-03-31 | 2017-10-05 | 株式会社富士通ゼネラル | Air conditioner |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61268958A (en) * | 1985-05-24 | 1986-11-28 | 松下電器産業株式会社 | Defrostation controller for air conditioner |
| JP2022010435A (en) * | 2020-06-29 | 2022-01-17 | パナソニックIpマネジメント株式会社 | Air conditioner |
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