WO2014054090A1 - Air conditioning device - Google Patents
Air conditioning device Download PDFInfo
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- WO2014054090A1 WO2014054090A1 PCT/JP2012/075309 JP2012075309W WO2014054090A1 WO 2014054090 A1 WO2014054090 A1 WO 2014054090A1 JP 2012075309 W JP2012075309 W JP 2012075309W WO 2014054090 A1 WO2014054090 A1 WO 2014054090A1
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- WIPO (PCT)
- Prior art keywords
- flow rate
- control device
- heat exchanger
- refrigerant
- side heat
- Prior art date
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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
- F25B29/00—Combined heating and refrigeration systems, e.g. operating alternately or simultaneously
- F25B29/003—Combined heating and refrigeration systems, e.g. operating alternately or simultaneously of the compression type system
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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
- F25B30/00—Heat pumps
- F25B30/02—Heat pumps of the compression type
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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
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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
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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
- F25B6/00—Compression machines, plants or systems, with several condenser circuits
- F25B6/02—Compression machines, plants or systems, with several condenser circuits arranged in parallel
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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
- F25B2313/023—Compression machines, plants or systems with reversible cycle not otherwise provided for using multiple indoor units
- F25B2313/0231—Compression machines, plants or systems with reversible cycle not otherwise provided for using multiple indoor units with simultaneous cooling and heating
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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
- F25B2313/023—Compression machines, plants or systems with reversible cycle not otherwise provided for using multiple indoor units
- F25B2313/0233—Compression machines, plants or systems with reversible cycle not otherwise provided for using multiple indoor units in parallel arrangements
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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
- F25B2313/0272—Compression machines, plants or systems with reversible cycle not otherwise provided for characterised by the reversing means using bridge circuits of one-way 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
- 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
- F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
- F25B2400/23—Separators
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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
- F25B2600/2509—Economiser valves
Definitions
- the present invention relates to an air conditioner.
- Some conventional air conditioners include a high-stage compressor and a low-stage compressor, and liquid refrigerant is allowed to flow from the injection pipe to the high-stage compressor (see, for example, Patent Document 1).
- the conventional air conditioner includes a flow control device between the heat source side heat exchanger and the pressure detection means, and controls the opening degree of the flow control device according to the detection value of the pressure detection means. (For example, see Patent Document 1).
- the conventional air conditioner (Patent Document 1)
- a plurality of compressors In order to continue the operation, the opening degree of the flow control device has to be controlled based on the pressure detection means. Therefore, when the outside air temperature decreases during the simultaneous cooling and heating operation, a high-cost air conditioner is required to continue the cooling operation while maintaining the heating capacity. For this reason, the conventional air conditioner (Patent Document 1) has a problem that, when the outside air temperature decreases during the cooling and heating simultaneous operation, the cooling operation cannot be continued while maintaining the heating capacity at low cost. there were.
- the present invention has been made to solve the above-described problems. Even when the outside air temperature decreases during the simultaneous cooling and heating operation, the cooling operation can be performed while maintaining the heating capacity at a low cost. It aims at providing the air conditioning apparatus which can be continued.
- the present invention performs heat exchange between one compressor that compresses and discharges the refrigerant, a heat source side heat exchanger that exchanges heat between the refrigerant and the surrounding heat source medium, and the refrigerant and the surrounding utilization medium.
- a heat source side heat exchanger that exchanges heat between the refrigerant and the surrounding heat source medium, and the refrigerant and the surrounding utilization medium.
- a relay that switches a part of the plurality of use side heat exchangers to the heating operation side, and according to a control command, any one of the cooling operation side and the heating operation side among the plurality of use side heat exchangers
- An air conditioner that performs simultaneous cooling and heating operations by switching each of the plurality of use side heat exchangers, provided between the relay unit and the heat source unit side heat exchanger, the heat source Bypass the refrigerant flowing into the machine side heat exchanger and supply it to the one compressor
- FIG. 1 It is a figure which shows the structural example of the air conditioning apparatus 1 in Embodiment 1 of this invention. It is the figure which modeled and showed the connection relation of the 2nd flow control device 122 in Embodiment 1 of the present invention, the 3rd flow control device 123, and the 3rd flow regulator 115 of relay machine B. It is a cooling-heating simultaneous operation in Embodiment 1 of this invention, Comprising: It is a figure which shows the structural example of the air conditioning apparatus 1 explaining the driving
- FIG. 1 is a diagram illustrating a configuration example of an air-conditioning apparatus 1 according to Embodiment 1 of the present invention.
- the air conditioner 1 uses an indoor unit C, an indoor unit D, a relay unit B, check valves 118 to 121, a four-way valve 102, and the like.
- a cycle and a heating refrigeration cycle are formed, and simultaneous cooling and heating operations are performed.
- the amount of refrigerant flowing to the compressor 101 is adjusted by the second flow control device and the amount of refrigerant flowing to the heat source unit side heat exchanger 103 is described later. Is adjusted by the third flow control device 123.
- the air conditioner 1 includes a heat source unit A, a relay unit B, an indoor unit C, an indoor unit D, and the like.
- the relay unit B is provided between the heat source unit A, the indoor unit C, and the indoor unit D.
- the heat source machine A and the relay machine B are connected by a first connection pipe 106 and a second connection pipe 107 having a pipe diameter smaller than that of the first connection pipe 106.
- the relay machine B and the indoor unit C are connected by the 1st connection piping 106c and the 2nd connection piping 107c.
- the relay machine B and the indoor unit D are connected by the 1st connection piping 106d and the 2nd connection piping 107d.
- the relay unit B relays the refrigerant flowing between the heat source unit A, the indoor unit C, and the indoor unit D.
- the present invention is not particularly limited thereto.
- the case where two or more indoor units are provided may be used.
- a plurality of heat source machines may be used.
- a plurality of relay machines B may be provided.
- the heat source machine A includes a compressor 101, a four-way valve 102, a heat source machine side heat exchanger 103, and an accumulator 104.
- the heat source machine A includes a check valve 118, a check valve 119, a check valve 120, and a check valve 121.
- the heat source machine A includes a second flow rate control device 122, a third flow rate control device 123, a fourth flow rate adjustment valve 124, and a control unit 141.
- the heat source device A includes an outside air temperature detecting unit 131 that measures the outside air temperature and supplies the measurement result to the control unit 141.
- the compressor 101 is provided between the four-way valve 102, the accumulator 104 and the second flow control device 122.
- the compressor 101 compresses and discharges the refrigerant.
- the discharge side is connected to the four-way valve 102 and the suction side is connected to the accumulator 104 and the second flow control device 122.
- the four-way valve 102 includes four ports. Each port includes a discharge side of the compressor 101, a heat source unit side heat exchanger 103, an accumulator 104, an outlet side of the check valve 119, and an inlet of the check valve 120. And the refrigerant flow path is switched.
- the heat source machine side heat exchanger 103 is provided between the four-way valve 102, the third flow rate control device 123, and the fourth flow rate adjustment valve 124.
- One of the heat source device side heat exchangers 103 is connected to the four-way valve 102 and the other is connected to a pipe connected to the third flow rate control device 123 and the fourth flow rate adjustment valve 124.
- the heat source device side heat exchanger 103 exchanges heat between the refrigerant flowing in the heat source device side heat exchanger 103 and the ambient air of the heat source device side heat exchanger 103.
- the accumulator 104 is connected between the four-way valve 102 and the suction side of the compressor 101, separates the liquid refrigerant, and supplies the gas refrigerant to the compressor 101.
- the compressor 101, the four-way valve 102, and the heat source device side heat exchanger 103 described above constitute a part of the refrigerant circuit.
- the check valve 118 includes an outlet side of the fourth flow rate adjustment valve 124 and the check valve 121 connected to the heat source apparatus side heat exchanger 103, and an outlet side of the second connection pipe 107 and the check valve 120. Between.
- the inlet side of the check valve 118 is connected to piping connected to the fourth flow rate adjustment valve 124 and the outlet side of the check valve 121.
- the outlet side of the check valve 118 is connected to the second connection pipe 107 and a pipe connected to the outlet side of the check valve 120.
- the check valve 118 allows the refrigerant to flow only from one direction to the second connection pipe 107 through the fourth flow rate adjustment valve 124 from the heat source apparatus side heat exchanger 103.
- the check valve 119 is provided between the inlet side of the four-way valve 102 and the check valve 120 and the inlet side of the first connection pipe 106 and the check valve 121.
- the inlet side of the check valve 119 is connected to a pipe connected to the first connection pipe 106 and the inlet side of the check valve 121.
- the outlet side of the check valve 119 is connected to a pipe connected to the four-way valve 102 and the inlet side of the check valve 120.
- the check valve 119 allows the refrigerant to flow only from one direction from the first connection pipe 106 to the four-way valve 102.
- the check valve 120 is provided between the outlet side of the four-way valve 102 and the check valve 119, the outlet side of the check valve 118, and the second connection pipe 107.
- the inlet side of the check valve 120 is connected to piping connected to the four-way valve 102 and the outlet side of the check valve 119.
- the outlet side of the check valve 120 is connected to a pipe connected to the outlet side of the check valve 118 and the second connection pipe 107.
- the check valve 120 allows the refrigerant to flow from the four-way valve 102 to the second connection pipe 107 only from one direction.
- the check valve 121 includes an inlet side of the check valve 119 and the first connection pipe 106, and a fourth flow rate adjustment valve 124 connected to the inlet side of the check valve 118 and the heat source unit side heat exchanger 103. Between.
- the inlet side of the check valve 121 is connected to a pipe connected to the inlet side of the check valve 119 and the first connection pipe 106.
- the outlet side of the check valve 121 is connected to a pipe connected to the inlet side of the check valve 118 and the fourth flow rate adjustment valve 124.
- the check valve 121 allows the refrigerant to flow only from one direction from the first connection pipe 106 to the heat source apparatus side heat exchanger 103 via the fourth flow rate adjustment valve 124.
- the check valve 118 to the check valve 121 described above constitute a flow path switching valve of the refrigerant circuit.
- the relay unit B which will be described in detail later, the indoor unit C, and the indoor unit D, in the refrigerant circuit, the refrigeration cycle of the cooling operation, and the heating operation A refrigeration cycle is formed.
- the second flow control device 122 has one end connected to the inlet side of the check valve 121 and the other end connected to the suction side of the compressor 101.
- the inlet side of the check valve 121 is connected to one end of the first connection pipe 106.
- the other end of the first connection pipe 106 is connected to the repeater B. Due to this connection configuration, the second flow control device 122 is connected in series with the relay machine B, and the refrigerant is supplied from the relay machine B.
- the second flow control device 122 is a flow control device having a variable opening. Therefore, the second flow control device 122 controls the refrigerant amount after gas-liquid separation flowing in from the relay B by adjusting the opening, and the refrigerant is controlled while the refrigerant amount is controlled. To supply.
- the second flow rate control device 122 corresponds to the compressor flow rate control device in the present invention.
- the third flow rate control device 123 is provided between the second flow rate control device 122 and the heat source unit side heat exchanger 103 and is connected in parallel with the second flow rate control device 122. Specifically, the third flow control device 123 is connected to the end of the second flow control device 122 on the side connected to the inlet side of the check valve 121 among the both ends of the second flow control device 122. Connected with the part. Due to this connection configuration, the third flow control device 123 is connected in series with the relay unit B, and the refrigerant is supplied from the relay unit B.
- the third flow control device 123 is a flow control device having a variable opening.
- the third flow control device 123 controls the amount of refrigerant flowing from the relay B by adjusting the opening, and supplies the refrigerant to the heat source device side heat exchanger 103 in a state where the amount of refrigerant is controlled.
- the third flow rate control device 123 corresponds to the heat source unit side heat exchanger flow rate control device in the present invention.
- the third flow rate control device 123 is connected in parallel with the second flow rate control device 122 and connected in series with the repeater B. Therefore, the refrigerant flowing from the relay B is the second flow control device 122 and the third flow rate according to the opening of the second flow control device 122 and the opening of the third flow control device 123. It is distributed and supplied to the control device 123.
- the fourth flow rate adjusting valve 124 is provided between the outlet side of the check valve 121 and the inlet side of the check valve 118 and the heat source unit side heat exchanger 103, and in parallel with the third flow rate control device 123. Connected. Specifically, one end of the fourth flow rate adjustment valve 124 is connected to a pipe connected to the outlet side of the check valve 121 and the inlet side of the check valve 118. The other end of the fourth flow rate adjustment valve 124 is connected to piping on the side connected to the heat source device side heat exchanger 103 in both ends of the third flow rate control device 123. Due to this connection configuration, the fourth flow rate adjustment valve 124 is connected in series via the relay B and the check valve 121, and the refrigerant is supplied from the relay B.
- the fourth flow rate adjustment valve 124 is a flow rate adjustment valve having a variable opening degree. Therefore, the fourth flow rate adjustment valve 124 controls the amount of refrigerant flowing from the relay B by adjusting the opening, and supplies the refrigerant to the heat source device side heat exchanger 103 in a state where the amount of refrigerant is controlled.
- the fourth flow rate adjustment valve 124 is connected in parallel to the second flow rate control device 122 and the third flow rate control device 123 via the check valve 121 and is connected in series with the relay B. Connected. Therefore, the refrigerant flowing from the relay machine B depends on the opening of the second flow control device 122, the opening of the third flow control device 123, and the opening of the fourth flow control valve 124.
- the second flow control device 122, the third flow control device 123, and the fourth flow control valve 124 are distributed and supplied.
- the control unit 141 is configured mainly by, for example, a microprocessor unit, and performs overall control of the entire heat source apparatus A, communication with an external device, for example, the relay machine B, and various calculations.
- the outside air temperature detection means 131 is formed by a thermistor, for example.
- the outside air temperature detection means 131 supplies the outside air temperature measurement result to the control unit 141.
- the outside air temperature detection means 131 may supply the measurement result to the control unit 141 as it is, or may supply the measurement result accumulated after accumulating the measurement result for a certain period to the control unit 141 at a predetermined cycle interval.
- the example in which the outside temperature detecting means 131 is a thermistor has been described.
- the present invention is not particularly limited to this.
- the relay B includes a first branching unit 110, a second branching unit 111, a gas-liquid separator 112, a second flow rate regulator 113, a third flow rate regulator 115, a first heat exchanger 116, a first 2 heat exchanger 117, temperature detection means 125, pressure detection means 127a, pressure detection means 127b, and control unit 151.
- the relay machine B is connected to the heat source machine A via the first connection pipe 106 and the second connection pipe 107.
- the relay machine B is connected to the indoor unit C via the first connection pipe 106c and the second connection pipe 107c.
- the relay machine B is connected to the indoor unit D through the first connection pipe 106d and the second connection pipe 107d.
- the first branching unit 110 includes an electromagnetic valve 108a and an electromagnetic valve 108b.
- the solenoid valve 108a and the solenoid valve 108b are connected to the indoor unit C through the first connection pipe 106c.
- the solenoid valve 108a and the solenoid valve 108b are connected to the indoor unit D through the first connection pipe 106d.
- the solenoid valve 108a is a valve that can be opened and closed, and has one end connected to the first connection pipe 106 and the other end connected to one terminal of the first connection pipe 106c, the first connection pipe 106d, and the solenoid valve 108b. It is connected.
- the electromagnetic valve 108b is a valve that can be opened and closed, and has one end connected to the second connection pipe 107 and the other end connected to one terminal of the first connection pipe 106c, the first connection pipe 106d, and the electromagnetic valve 108a. It is connected.
- the first branch 110 is connected to the indoor unit C via the first connection pipe 106c.
- the first branch 110 is connected to the indoor unit D via the first connection pipe 106d.
- the first branch part 110 is connected to the heat source machine A through the first connection pipe 106 and the second connection pipe 107.
- the first branching section 110 is connected to one of the first connection pipe 106 c, the first connection pipe 106, and the second connection pipe 107 using the electromagnetic valve 108 a and the electromagnetic valve 108 b.
- the first branch part 110 is connected to one of the first connection pipe 106d, the first connection pipe 106, and the second connection pipe 107 using the electromagnetic valve 108a and the electromagnetic valve 108b.
- the second branch portion 111 includes a check valve 137a and a check valve 137b.
- the check valve 137a and the check valve 137b are connected to each other in an antiparallel relationship.
- the input side of the check valve 137a and the output side of the check valve 137b are connected to the indoor unit C through the second connection pipe 107c, and are connected to the indoor unit D through the second connection pipe 107d.
- the output side of the check valve 137a is connected to the meeting part 137a_all.
- the input side of the check valve 137b is connected to the meeting part 137b_all.
- the second branch portion 111 is connected to the indoor unit C via the second connection pipe 107c.
- the second branch portion 111 is connected to the indoor unit D via the second connection pipe 107d.
- the second branch part 111 is connected to the second flow rate regulator 113 and the first heat exchanger 116 via the meeting part 137a_all.
- the second branch part 111 is connected to the third flow rate regulator 115 and the first heat exchanger 116 via the meeting part 137b_all.
- the gas-liquid separator 112 is provided in the middle of the second connection pipe 107, the gas phase portion is connected to the electromagnetic valve 108b of the first branching portion 110, and the liquid phase portion is the first heat exchange.
- the second branching unit 111 is connected to the second branching unit 111 through the second unit 116, the second flow rate regulator 113, the second heat exchanger 117, and the third flow rate regulator 115.
- the second flow rate regulator 113 has one end connected to the first heat exchanger 116 and the other end connected to one end of the second heat exchanger 117 and the meeting part 137a_all of the second branching part 111. .
- the piping connected between the first heat exchanger 116 and the second flow rate regulator 113 is provided with a pressure detection means 127a described later in detail.
- a pipe connected between the second flow rate regulator 113, the second heat exchanger 117, and the meeting portion 137a_all is provided with a pressure detection means 127b described later in detail.
- the second flow rate regulator 113 is a flow rate regulator whose opening degree can be adjusted so that the difference between the pressure value detected by the pressure detection means 127a and the pressure value detected by the pressure detection means 127b is constant. Adjust the opening.
- the third flow rate regulator 115 is a flow rate regulator whose opening degree can be adjusted, and is any one or a plurality of the outside air temperature detection means 131, the temperature detection means 125, the pressure detection means 127a, and the pressure detection means 127b. Adjust the opening by the combination.
- the bypass pipe 114 has one end connected to the first connection pipe 106 and the other end connected to the third flow rate regulator 115. Therefore, the amount of refrigerant supplied to the heat source unit A varies depending on the opening of the third flow rate regulator 115.
- the first heat exchanger 116 is provided between the gas-liquid separator 112, the second heat exchanger 117, and the second flow rate regulator 113, and includes a bypass pipe 114, the gas-liquid separator 112, and the first heat exchanger 116. Heat exchange is performed with a pipe provided between the two flow rate regulators 113.
- the second heat exchanger 117 is between the first heat exchanger 116 and the second flow rate regulator 113, and one end of the third flow rate regulator 115 and the other end of the third flow rate regulator 115. Is provided. In this case, the other end of the third flow rate regulator 115 is connected to the meeting part 137b_all.
- the second heat exchanger 117 performs heat exchange between the bypass pipe 114 and a pipe provided between the second flow rate regulator 113 and the third flow rate regulator 115.
- the temperature detection means 125 is formed by a thermistor, for example.
- the temperature detection means 125 measures the temperature of the refrigerant flowing in the pipe provided between the third flow rate regulator 115 and the second heat exchanger 117 and supplies the measurement result to the control unit 151.
- the temperature detection unit 125 may supply the measurement result to the control unit 151 as it is, or may supply the measurement result accumulated after a certain period of accumulation to the control unit 151 at a predetermined cycle interval.
- the temperature detection unit 125 is described as an example of a thermistor, but is not particularly limited thereto.
- the pressure detection unit 127 a measures the pressure of the refrigerant flowing in the pipe provided between the first heat exchanger 116 and the second flow rate regulator 113 and supplies the measurement result to the control unit 151.
- the pressure detection means 127b measures the pressure of the refrigerant flowing in the pipe provided between the second flow rate regulator 113, the second heat exchanger 117, and the second branch part 111, and the measurement result is obtained. It supplies to the control part 151.
- the pressure detection means 127a and the pressure detection means 127b are collectively referred to as a pressure detection means 127.
- the pressure detection unit 127 may supply the measurement result as it is to the control unit 151, or may supply the measurement result accumulated after a certain period of accumulation to the control unit 151 at a predetermined cycle interval.
- the control unit 151 is configured mainly by, for example, a microprocessor unit, and executes overall control of the entire relay unit B, communication with an external device, for example, the heat source unit A, and various calculations.
- the indoor unit C includes a use side heat exchanger 105c, a liquid pipe temperature detecting means 126c, a first flow rate regulator 109c, and the like.
- a plurality of use side heat exchangers 105c are provided. Between the use side heat exchanger 105c and the first flow rate regulator 109c, a liquid pipe temperature detecting means 126c for detecting the temperature of the pipe is provided.
- the utilization side heat exchanger 105c and the first flow rate regulator 109c described above constitute a part of the refrigerant circuit.
- the indoor unit D includes a use side heat exchanger 105d, a liquid pipe temperature detection means 126d, a first flow rate regulator 109d, and the like.
- a plurality of use side heat exchangers 105d are provided. Between the use side heat exchanger 105d and the first flow rate regulator 109d, a liquid pipe temperature detecting means 126d for detecting the temperature of the pipe is provided.
- the utilization side heat exchanger 105d and the first flow rate control device 109d described above constitute a part of the refrigerant circuit.
- FIG. 2 is a diagram showing a modeled connection relationship between the second flow rate control device 122, the third flow rate control device 123, and the third flow rate regulator 115 of the relay B in the first embodiment of the present invention. It is. As shown in FIG. 2, a second flow rate control device 122 is provided between the relay machine B and the compressor 101. In addition, a third flow rate control device 123 and a fourth flow rate adjustment valve 124 are provided between the relay unit B and the heat source unit side heat exchanger 103. The third flow control device 123 and the fourth flow control valve 124 are connected in parallel, and the third flow control device 123 and the second flow control device 122 are connected in parallel.
- the 2nd flow control device 122, the 3rd flow control device 123, and the 4th flow control valve 124 have a parallel relation mutually, and have a serial relation to relay machine B.
- the relay unit B includes the third flow rate regulator 115 and adjusts the amount of refrigerant to the heat source unit A side.
- the third flow rate regulator 115 determines the amount of refrigerant flowing through the second flow rate control device 122, the third flow rate control device 123, and the fourth flow rate adjustment valve 124.
- the control unit 141 adjusts the opening degrees of the second flow rate control device 122, the third flow rate control device 123, and the fourth flow rate adjustment valve 124.
- the control unit 151 adjusts the opening degree of the third flow rate regulator 115. And the control part 141 and the control part 151 supply mutual control content by transmitting / receiving various signals.
- FIG. 3 is a diagram illustrating a configuration example of the air-conditioning apparatus 1 for explaining an operation state in the cooling-heating simultaneous operation according to the first embodiment of the present invention and mainly in a cooling operation.
- a cooling operation is set for the indoor unit C and a heating operation is set for the indoor unit D, and the operation of the air conditioner 1 is performed mainly by the cooling.
- the indoor unit C side is opened, and the indoor unit D side is closed.
- the indoor unit C side is closed and the indoor unit D side is opened.
- the opening degree of the second flow rate regulator 113 is controlled so that the differential pressure between the pressure detection means 127a and the pressure detection means 127b becomes an appropriate value.
- the high-temperature and high-pressure gas refrigerant compressed and discharged by the compressor 101 flows into the heat source unit side heat exchanger 103 through the four-way valve 102.
- the heat source machine side heat exchanger 103 exchanges heat with a heat source medium such as air or water.
- the heat-exchanged high-temperature and high-pressure gas refrigerant becomes a gas-liquid two-phase high-temperature and high-pressure refrigerant.
- the gas-liquid two-phase high-temperature and high-pressure refrigerant passes through the second connection pipe 107 via the fourth flow rate adjustment valve 124 and the check valve 118 and is supplied to the gas-liquid separator 112 of the relay B.
- the gas-liquid separator 112 separates the gas-liquid two-phase high-temperature and high-pressure refrigerant into a gaseous refrigerant and a liquid refrigerant.
- the separated gaseous refrigerant flows into the first branch part 110.
- the gaseous refrigerant that has flowed into the first branch portion 110 is supplied to the indoor unit D in which the heating operation is set, through the electromagnetic valve 108b on the open side and the first connection pipe 106d.
- the use side heat exchanger 105d exchanges heat with a use medium such as air, and condenses and liquefies the supplied gaseous refrigerant.
- the usage-side heat exchanger 105d is controlled by the first flow rate regulator 109d based on the degree of supercooling at the outlet of the usage-side heat exchanger 105d.
- the first flow controller 109d depressurizes the liquid refrigerant condensed and liquefied by the use side heat exchanger 105d, and converts it into a gas-liquid two-phase refrigerant having an intermediate pressure that is an intermediate pressure between the high pressure and the low pressure.
- the gas-liquid two-phase refrigerant that has reached the intermediate pressure flows into the second branch portion 111.
- the gas refrigerant of the gas-liquid two-phase refrigerant that has flowed into the second branch portion 111 flows into the indoor unit D.
- the liquid refrigerant of the gas-liquid two-phase refrigerant that has flowed into the second branch part 111 exits from the second branch part 111, and then merges with the liquid refrigerant that has passed through the second flow rate regulator 113, so that the first heat After the heat exchange is performed by the exchanger 116 as described later, the flow returns to the second branch portion 111 again and flows into the indoor unit C and the indoor unit D.
- the first connection pipe 106 has a low pressure
- the second connection pipe 107 has a high pressure. Therefore, due to the pressure difference between them, the refrigerant flows to the check valve 118 and the check valve 119, while the refrigerant does not flow to the check valve 120 and the check valve 121.
- the liquid refrigerant separated by the gas-liquid separator 112 passes through the second flow rate regulator 113 that controls the pressure difference between the high pressure and the intermediate pressure to be constant, and flows into the second branch portion 111.
- the supplied liquid refrigerant passes through the check valve 108d connected to the indoor unit C and flows into the indoor unit C.
- the inflowing liquid refrigerant is decompressed to a low pressure by using the first flow rate regulator 109c controlled according to the degree of superheat at the outlet of the utilization side heat exchanger 105c of the indoor unit C. It is supplied to the heat exchanger 105c.
- the supplied liquid refrigerant is evaporated and gasified by exchanging heat with a use medium such as air.
- the refrigerant that has been gasified to become a gas refrigerant passes through the first connection pipe 106 c and flows into the first branch 110.
- the solenoid valve 108a on the side connected to the indoor unit C is open. Therefore, the gas refrigerant that has flowed in passes through the electromagnetic valve 108 a on the side connected to the indoor unit C, and flows into the first connection pipe 106.
- the gas refrigerant flows into the check valve 119 having a lower pressure than the check valve 121, and is sucked into the compressor 101 through the four-way valve 102 and the accumulator 104. With such an operation, a refrigeration cycle is formed and a cooling main operation is performed.
- the refrigerants that have been separated by the gas-liquid separator 112 and have flowed into the second branch portion 111 there are refrigerants that have not flowed into the indoor unit C.
- Such a liquid refrigerant flows into the second branch portion 111, but flows into the third flow rate regulator 115 through the first heat exchanger 116.
- the third flow rate regulator 115 depressurizes the inflowing liquid refrigerant to a low pressure to lower the refrigerant evaporation temperature.
- the liquid refrigerant whose evaporation temperature has decreased passes through the bypass pipe 114, and exchanges heat with the liquid refrigerant mainly supplied from the second flow rate regulator 113.
- the liquid refrigerant supplied from the gas-liquid separator 112 becomes a gas refrigerant and flows into the first connection pipe 106.
- FIG. 4 is a diagram showing a configuration example of the air-conditioning apparatus 1 for explaining an operation state in the case of heating and cooling simultaneous operation in Embodiment 1 of the present invention and mainly heating.
- a heating operation is set for the indoor unit C and a cooling operation is set for the indoor unit D, and the operation of the air conditioner 1 is performed mainly by heating.
- the indoor unit C side is closed and the indoor unit D side is opened.
- the indoor unit C side is opened, and the indoor unit D side is closed.
- the opening degree of the second flow rate regulator 113 is controlled so that the differential pressure between the pressure detection means 127a and the pressure detection means 127b becomes an appropriate value.
- the high-temperature and high-pressure gas refrigerant compressed and discharged by the compressor 101 passes through the four-way valve 102, the check valve 120, the second connection pipe 107, and the relay machine.
- B gas-liquid separator 112 is supplied.
- the gas-liquid separator 112 supplies a high-temperature and high-pressure gas refrigerant to the first branch part 110.
- the gas refrigerant supplied to the first branch part 110 is supplied to the indoor unit C in which the heating operation is set, through the open solenoid valve 108b and the first connection pipe 106c.
- the use side heat exchanger 105c exchanges heat with a use medium such as air, and the supplied gas refrigerant is condensed and liquefied.
- the use side heat exchanger 105c is controlled by the first flow rate regulator 109c based on the degree of supercooling at the outlet of the use side heat exchanger 105c.
- the first flow controller 109c depressurizes the liquid refrigerant condensed and liquefied by the use side heat exchanger 105c, and converts it into a gas-liquid two-phase refrigerant having an intermediate pressure that is an intermediate pressure between the high pressure and the low pressure.
- the gas-liquid two-phase refrigerant that has reached the intermediate pressure flows into the second branch portion 111.
- the gas-liquid two-phase refrigerant that has flowed into the second branch part 111 joins at the meeting part 137a_all.
- the gas-liquid two-phase refrigerant joined at the meeting part 137a_all passes through the first heat exchanger 116 to become a liquid refrigerant, reaches the meeting part 137b_all, passes through the check valve 137b connected to the indoor unit D, and passes through the second heat exchanger 116. It flows into the indoor unit D through the connecting pipe 107d.
- the inflowing liquid refrigerant is decompressed to a low pressure by using the first flow rate regulator 109d controlled according to the degree of superheat at the outlet of the utilization side heat exchanger 105d of the indoor unit D. It is supplied to the heat exchanger 105d.
- the supplied liquid refrigerant evaporates and gasifies by exchanging heat with a use medium such as air.
- the refrigerant that has been gasified to become a gas refrigerant passes through the first connection pipe 106d and flows into the first branch 110.
- the solenoid valve 108a by the side connected with the indoor unit D is opening. Therefore, the gas refrigerant that has flowed in passes through the electromagnetic valve 108 a on the side connected to the indoor unit D, and flows into the first connection pipe 106.
- the gas refrigerant flows into the check valve 121 side having a pressure lower than that of the check valve 119, and flows into the fourth flow rate adjustment valve 124 and the heat source unit side heat exchanger 103 to evaporate into a gas state.
- the air is sucked into the compressor 101 through the four-way valve 102 and the accumulator 104. With such an operation, a refrigeration cycle is formed, and a heating main operation is performed.
- the first connection pipe 106 has a low pressure
- the second connection pipe 107 has a high pressure. Therefore, due to the pressure difference between them, the refrigerant flows to the check valve 120 and the check valve 121, while the refrigerant does not flow to the check valve 118 and the check valve 119.
- the heat source apparatus side heat exchanger 103, the second flow control device 122, the third flow control device 123 are mutually influential. Specifically, as the outside air temperature decreases, the air conditioner 1 cannot maintain a high pressure at a high level, and the heating capacity decreases. Moreover, since the low-pressure pressure decreases, the indoor unit D that is performing the cooling operation cannot maintain the continuous operation, and a problem occurs in both the cooling operation and the heating operation.
- FIG. 5 is a diagram for explaining an example of the correlation between the outside air temperature and the heating capacity ratio according to the opening degree of the second flow control device 122 according to Embodiment 1 of the present invention.
- the reference temperature on the horizontal axis is ⁇ and the reference heating capacity ratio on the vertical axis is ⁇ .
- the heating capacity ratio is improved. In other words, in order to increase the heating capacity, the high pressure can be maintained high by increasing the opening of the second flow control device 122.
- the high-pressure pressure increases and the heating capacity can be increased.
- the heating capacity increases by about 8%.
- the opening degree of the third flow control device 123 is also examined.
- the third flow control device 123 is opened to a certain degree of opening or more, the second flow control device 122 and the third flow control device 123 are connected in parallel.
- the flow rate decreases.
- the liquid pipe temperature detecting means 126 of the indoor unit D becomes a certain value or less.
- the cooling operation cannot be maintained.
- priority is given to the injection amount to the compressor 101 at the same time as the liquid pipe temperature of the indoor unit D is raised by suppressing the opening of the third flow control device 123. With this operation, a comfortable operation can be performed regardless of whether it is a cooling operation or a heating operation.
- the opening degree of the second flow control device 122 and the opening degree of the third flow control device 123 will be described.
- FIG. 6 illustrates an example of the correlation between the outside air temperature and the flow rate ratio according to the opening degree of the second flow control device 122 and the opening degree of the third flow control device 123 in Embodiment 1 of the present invention.
- FIG. 6 it is assumed that the reference temperature on the horizontal axis is ⁇ and the reference flow ratio on the vertical axis is ⁇ .
- the flow rate of the third flow control device 123 is decreased and the flow rate of the second flow control device 122 is increased. With this operation, the heating capacity can be increased. At this time, since the low pressure is also lowered, there is no influence on the cooling capacity.
- FIG. 7 shows the outside air temperature according to the opening of the second flow control device 122, the opening of the third flow control device 123, and the opening of the third flow regulator 115 in Embodiment 1 of the present invention. It is a figure explaining an example of the correlation with a flow rate ratio.
- the third flow rate regulator 115 provided in the relay B that controls the differential pressure between the high pressure before and after the pressure detection means 127 a and 127 b and the intermediate pressure to be constant is the operation of the third flow control device 123.
- the opening of the third flow rate regulator 115 is reduced. With this operation, the pressure difference between the high pressure and the intermediate pressure is maintained constant, and at the same time, the liquid pipe temperature of the indoor unit D can be raised. As a result, the cooling operation can be maintained.
- FIG. 8 is a diagram illustrating an example of the correlation between the outside air temperature and the heating capacity ratio depending on whether or not there is proper control of the second flow control device 122 in Embodiment 1 of the present invention. . As shown in FIG. 8, when the outside air temperature exceeds a certain value, the influence on the cooling capacity can be reduced by adjusting the appropriate opening degree of the second flow control device 122, and the stable cooling capacity. Can be maintained.
- FIG. 9 is a diagram for explaining an example of the correlation between the outside air temperature and the heating capacity ratio depending on whether or not the fourth flow regulating valve 124 is appropriately controlled in Embodiment 1 of the present invention. .
- the opening degree of the fourth flow rate adjustment valve 124 by adjusting the opening degree of the fourth flow rate adjustment valve 124, the influence on the cooling capacity can be reduced, and the stable cooling capacity can be maintained.
- the opening degree of the fourth flow rate adjustment valve 124 is reduced, and when the outside air temperature is high compared to a certain value, the opening degree of the fourth flow rate adjustment valve 124.
- Increase With this operation the influence on the cooling capacity can be reduced, and a stable cooling capacity can be maintained.
- connection pipes of the heat source machine A, the relay machine B, the first connection pipe 106, and the second connection pipe 107 is two, the total of the connection pipes is three. Can achieve the same effect.
- FIG. 10 is a flowchart for explaining an operation example of the control unit 141 provided in the heat source machine A according to Embodiment 1 of the present invention.
- Step S11 The controller 141 of the heat source device A determines whether or not the cooling and heating simultaneous operation is being performed.
- the control unit 141 of the heat source device A determines that the cooling / heating simultaneous operation is being performed, the control unit 141 proceeds to step S12.
- it determines with the control part 141 of the heat source machine A not being in simultaneous cooling and heating operation it progresses to step S16.
- Step S12 The control unit 141 of the heat source device A acquires the outside air temperature. For example, the outside temperature data detected by the outside temperature detecting means 131 is acquired.
- Step S13 The control unit 141 of the heat source device A determines whether or not the outside air temperature corresponds to any of a plurality of predetermined threshold values. For example, when the outside air temperature is equal to or lower than the injection start threshold (WB ° C.), the control unit 141 of the heat source device A proceeds to step S14.
- the injection start threshold (WB ° C.) corresponds to ⁇ -5 (WB ° C.), which is a start temperature at which the opening degree of the second flow control device 122 gradually increases.
- ⁇ -5 (WB ° C.) for example, 0 ° C. is assumed. In the above description, an example in which ⁇ -5 (WB ° C.) is 0 ° C. has been described, but the present invention is not particularly limited to this.
- the specific value of ⁇ -5 (WB ° C.) may be varied flexibly according to the surrounding environment and the operating condition of the air conditioner 1.
- the control unit 141 of the heat source device A proceeds to step S15.
- the opening degree suppression threshold (WB ° C.) corresponds to ⁇ -20 (WB ° C.), which is a starting temperature at which the opening degree of the third flow control device 123 becomes small, as shown in FIG. 6, for example.
- ⁇ -20 (WB ° C.) for example, ⁇ 15 ° C. is assumed.
- control unit 141 of the heat source device A proceeds to step S16 when the outside air temperature is other than that (injection start threshold value or opening degree suppression threshold value).
- Step S14 The control part 141 of the heat source machine A increases the opening degree of the second flow rate control device 122 at a preset ratio. For example, as shown in FIG. 6, the ratio of the degree of opening that is gradually reduced is changed according to the outside air temperature.
- Step S15 The control unit 141 of the heat source device A suppresses the opening degree of the third flow control device 123. For example, as shown in FIG. 6, when the outside air temperature is from ⁇ to ⁇ -20, the opening degree of the third flow control device 123 is fully open, but when the outside air temperature is ⁇ -20 or less, the third flow control device 123 is open. The opening degree of the flow control device 123 is narrowed down.
- Step S16 The control unit 141 of the heat source machine A determines whether or not there is an end command.
- the control part 141 of the heat source machine A ends the process when there is an end command. On the other hand, if there is no termination command, the control unit 141 of the heat source machine A returns to step S12 and repeats the processing of steps S12 to S15.
- FIG. 11 is a flowchart for explaining an operation example of the control unit 151 included in the relay station B according to Embodiment 1 of the present invention.
- Step S51 The control unit 151 of the relay machine B sets the first ratio.
- the first ratio is the ratio of the degree of opening for narrowing the third flow rate regulator 115 while the outside air temperature is higher than ⁇ -20 and lower than ⁇ .
- Step S52 The control unit 151 of the relay B sets a second ratio that satisfies the condition that the second ratio> the first ratio.
- the second ratio is the ratio of the degree of opening that narrows down the third flow regulator 115 when the outside air temperature is ⁇ 20 or less.
- ⁇ -20 is assumed to be the outside air temperature at which the cooling operation cannot be continued, if the outside air temperature becomes ⁇ -20 or less, the cooling operation is not performed unless the liquid pipe temperature of the indoor unit during the cooling operation is increased. Can't continue. Therefore, the ratio to narrow down is set large.
- Step S53 The control unit 151 of the relay machine B determines whether or not the cooling and heating simultaneous operation is being performed. When the air conditioner simultaneous operation is being performed, the control unit 151 of the relay machine B proceeds to step S54. On the other hand, the control part 151 of the relay machine B complete
- Step S54 The control unit 151 of the relay machine B determines whether or not there is an end command.
- the control unit 151 of the relay machine B ends the process when there is an end command. On the other hand, if there is no termination command, the control unit 151 of the relay station B proceeds to step S55.
- Step S55 The control unit 151 of the relay machine B acquires the high pressure side pressure value.
- the control unit 151 of the relay machine B acquires the pressure value on the high pressure side among the pressure detection units 127a and 127b. Which is on the high voltage side may be determined by the control unit 151 of the relay B holding a correspondence table in which which corresponds to the high voltage side is registered in advance according to the operating state.
- Step S56 The control unit 151 of the relay machine B acquires the intermediate pressure side pressure value.
- the control unit 151 of the relay machine B acquires the pressure value on the intermediate pressure side among the pressure detection units 127a and 127b. Which is on the intermediate pressure side may be determined by the control unit 151 of the relay B holding a correspondence table in which which corresponds to the intermediate pressure side is registered in advance according to the operating state.
- Step S57 The control unit 151 of the relay machine B obtains a differential pressure between the high pressure side pressure value and the intermediate pressure side pressure value.
- Step S58 The control unit 151 of the relay B determines whether or not the differential pressure is constant. When the differential pressure is constant, the control unit 151 of the relay machine B proceeds to step S59. On the other hand, when the differential pressure is not constant, the control unit 151 of the relay station B proceeds to step S60.
- Step S59 The control unit 151 of the relay machine B acquires the outside air temperature.
- Step S60 The control unit 151 of the relay machine B makes the differential pressure constant by the third flow rate regulator 115.
- Step S61 The control unit 151 of the relay machine B determines whether or not the outside air temperature corresponds to any of a plurality of predetermined threshold values. For example, when the outside air temperature exceeds the second threshold value (WB ° C.) and is equal to or lower than the first threshold value (WB ° C.), the process proceeds to step S62. For example, when the outside air temperature is equal to or lower than the second threshold (WB ° C.), the process proceeds to step S63. For example, in other cases (when exceeding the first threshold (WB ° C.)), the process returns to step S54.
- Step S62 The control unit 151 of the relay machine B suppresses the opening degree of the third flow rate regulator 115 at the first rate, and returns to step S54.
- Step S63 The control unit 151 of the relay machine B suppresses the opening degree of the third flow rate regulator 115 at the second rate, and returns to step S54.
- the outside air temperature decreased during simultaneous cooling and heating operations by increasing the injection amount to one compressor and suppressing the refrigerant flow rate to the heat source side heat exchanger according to the outside air temperature. Even in this case, the cooling operation can be continued at a low cost while maintaining the heating capacity. Due to this configuration, highly efficient cooling and heating simultaneous operation can be performed.
- one compressor 101 that compresses and discharges the refrigerant, the heat source machine side heat exchanger 103 that exchanges heat between the refrigerant and the surrounding heat source medium, the refrigerant and the surrounding utilization medium, Are provided between the plurality of usage side heat exchangers 105, the heat source unit side heat exchanger 103, and the usage side heat exchanger 105, and a part of the plurality of usage side heat exchangers 105 is cooled.
- a relay unit B that switches a part of the plurality of use side heat exchangers 105 to the heating operation side, and among the plurality of use side heat exchangers 105, the cooling operation side and the heating are provided according to a control command.
- An air conditioner 1 that performs simultaneous cooling and heating operations by switching each of the plurality of use side heat exchangers 105 to any one of the operation side, between the relay unit B and the heat source unit side heat exchanger 103
- the refrigerant that is provided and flows into the heat source machine side heat exchanger 103
- An injection pipe 135 that is bypassed and supplied to one compressor 101;
- a second flow rate control device 122 that is provided in the injection pipe 135 and adjusts the flow rate of the refrigerant flowing into the one compressor 101;
- the third flow control device 123 which is connected in parallel to the flow control device 123 of the first flow control device and adjusts the flow rate of the refrigerant flowing into the heat source apparatus side heat exchanger 103, the second flow control device 122, and the third flow control device.
- the control unit 141 adjusts the opening degree of the second flow rate control device 122 and the opening degree of the third flow rate control device 123 according to the outside air temperature. Even when the outside air temperature decreases during the simultaneous operation, the cooling operation can be continued while maintaining the heating capacity at low cost. Due to this configuration, highly efficient cooling and heating simultaneous operation can be performed.
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Abstract
Description
したがって、冷暖房同時運転中に外気温度が低下した場合、暖房能力を維持しつつ、冷房運転を継続させるには、高コストの空気調和装置が必要だった。
このため、従来の空気調和装置(特許文献1)は、冷暖房同時運転中に外気温度が低下した場合、低コストで、暖房能力を維持しつつ、冷房運転を継続させることができないという問題点があった。 However, in the conventional air conditioner (Patent Document 1), when the outside air temperature decreases during the simultaneous cooling and heating operation, a plurality of compressors must be provided in order to maintain the heating capacity. In order to continue the operation, the opening degree of the flow control device has to be controlled based on the pressure detection means.
Therefore, when the outside air temperature decreases during the simultaneous cooling and heating operation, a high-cost air conditioner is required to continue the cooling operation while maintaining the heating capacity.
For this reason, the conventional air conditioner (Patent Document 1) has a problem that, when the outside air temperature decreases during the cooling and heating simultaneous operation, the cooling operation cannot be continued while maintaining the heating capacity at low cost. there were.
図1は、本発明の実施の形態1における空気調和装置1の構成例を示す図である。図1に示すように、空気調和装置1は、室内機C、室内機D、中継機B、逆止弁118~121、及び四方弁102等を用い、空気調和装置1内に、冷房用冷凍サイクルと、暖房用冷凍サイクルとを形成し、冷暖房同時運転を行う。冷暖房同時運転時に外気温度が低下した場合には、詳細については後述するように、圧縮機101へ流れる冷媒量を第2の流量制御装置で調整し、熱源機側熱交換器103へ流れる冷媒量を第3の流量制御装置123で調整する。この動作で、中継機Bから熱源機Aへ流れる冷媒量のうち、圧縮機101へ流れる冷媒量と、熱源機側熱交換器103へ流れる冷媒量とを分配する。この結果、冷暖房同時運転中に外気温度が低下した場合であっても、低コストで、暖房能力を維持しつつ、冷房運転を継続させ、高効率な冷暖房同時運転を実施する。
以下、上述した内容の詳細について順に説明する。
FIG. 1 is a diagram illustrating a configuration example of an air-
Hereinafter, details of the above-described contents will be described in order.
この接続構成で、中継機Bは、熱源機Aと、室内機C及び室内機Dとの間を流れる冷媒を中継する。
なお、熱源機が1台、室内機が2台の場合の一例について説明するが、特にこれに限定しない。例えば、室内機が2台以上の複数台の場合であってもよい。また、例えば、熱源機が複数台の場合であってもよい。また、例えば、中継機Bが複数台であってもよい。 The
With this connection configuration, the relay unit B relays the refrigerant flowing between the heat source unit A, the indoor unit C, and the indoor unit D.
In addition, although an example in case of one heat source unit and two indoor units will be described, the present invention is not particularly limited thereto. For example, the case where two or more indoor units are provided may be used. Further, for example, a plurality of heat source machines may be used. Further, for example, a plurality of relay machines B may be provided.
この接続構成のため、第2の流量制御装置122は、中継機Bと直列接続され、中継機Bから冷媒が供給される。また、第2の流量制御装置122は、開度が可変な流量制御装置である。
したがって、第2の流量制御装置122は、開度を調整することで中継機Bから流入する気液分離後の冷媒量を制御し、冷媒量を制御した状態で冷媒を圧縮機101の吸入側に供給する。
なお、第2の流量制御装置122は、本発明における圧縮機用流量制御装置に相当する。 The second flow control device 122 has one end connected to the inlet side of the check valve 121 and the other end connected to the suction side of the
Due to this connection configuration, the second flow control device 122 is connected in series with the relay machine B, and the refrigerant is supplied from the relay machine B. The second flow control device 122 is a flow control device having a variable opening.
Therefore, the second flow control device 122 controls the refrigerant amount after gas-liquid separation flowing in from the relay B by adjusting the opening, and the refrigerant is controlled while the refrigerant amount is controlled. To supply.
The second flow rate control device 122 corresponds to the compressor flow rate control device in the present invention.
この接続構成のため、第3の流量制御装置123は、中継機Bと直列接続され、中継機Bから冷媒が供給される。また、第3の流量制御装置123は、開度が可変な流量制御装置である。
したがって、第3の流量制御装置123は、開度を調整することで中継機Bから流入する冷媒量を制御し、冷媒量を制御した状態で冷媒を熱源機側熱交換器103に供給する。
なお、第3の流量制御装置123は、本発明における熱源機側熱交換器用流量制御装置に相当する。 The third flow rate control device 123 is provided between the second flow rate control device 122 and the heat source unit
Due to this connection configuration, the third flow control device 123 is connected in series with the relay unit B, and the refrigerant is supplied from the relay unit B. The third flow control device 123 is a flow control device having a variable opening.
Therefore, the third flow control device 123 controls the amount of refrigerant flowing from the relay B by adjusting the opening, and supplies the refrigerant to the heat source device
The third flow rate control device 123 corresponds to the heat source unit side heat exchanger flow rate control device in the present invention.
よって、中継機Bから流れる冷媒は、第2の流量制御装置122の開度と、第3の流量制御装置123の開度とに応じて、第2の流量制御装置122と、第3の流量制御装置123とに分配されて供給される。 Further, because of the connection configuration described above, the third flow rate control device 123 is connected in parallel with the second flow rate control device 122 and connected in series with the repeater B.
Therefore, the refrigerant flowing from the relay B is the second flow control device 122 and the third flow rate according to the opening of the second flow control device 122 and the opening of the third flow control device 123. It is distributed and supplied to the control device 123.
この接続構成のため、第4の流量調整弁124は、中継機Bと逆止弁121を介して直列接続され、中継機Bから冷媒が供給される。また、第4の流量調整弁124は、開度が可変な流量調整弁である。
したがって、第4の流量調整弁124は、開度を調整することで中継機Bから流入する冷媒量を制御し、冷媒量を制御した状態で冷媒を熱源機側熱交換器103に供給する。 The fourth flow rate adjusting valve 124 is provided between the outlet side of the check valve 121 and the inlet side of the check valve 118 and the heat source unit
Due to this connection configuration, the fourth flow rate adjustment valve 124 is connected in series via the relay B and the check valve 121, and the refrigerant is supplied from the relay B. The fourth flow rate adjustment valve 124 is a flow rate adjustment valve having a variable opening degree.
Therefore, the fourth flow rate adjustment valve 124 controls the amount of refrigerant flowing from the relay B by adjusting the opening, and supplies the refrigerant to the heat source device
したがって、中継機Bから流れる冷媒は、第2の流量制御装置122の開度と、第3の流量制御装置123の開度と、第4の流量調整弁124の開度とに応じて、第2の流量制御装置122と、第3の流量制御装置123と、第4の流量調整弁124とに分配されて供給される。 Due to such a connection configuration, the fourth flow rate adjustment valve 124 is connected in parallel to the second flow rate control device 122 and the third flow rate control device 123 via the check valve 121 and is connected in series with the relay B. Connected.
Therefore, the refrigerant flowing from the relay machine B depends on the opening of the second flow control device 122, the opening of the third flow control device 123, and the opening of the fourth flow control valve 124. The second flow control device 122, the third flow control device 123, and the fourth flow control valve 124 are distributed and supplied.
なお、上記の説明では、外気温度検出手段131は、サーミスタで形成される一例について説明したが、特にこれに限定しない。 The outside air temperature detection means 131 is formed by a thermistor, for example. The outside air temperature detection means 131 supplies the outside air temperature measurement result to the
In the above description, the example in which the outside temperature detecting means 131 is a thermistor has been described. However, the present invention is not particularly limited to this.
中継機Bは、第1の接続配管106及び第2の接続配管107を介して、熱源機Aと接続されている。中継機Bは、第1の接続配管106c及び第2の接続配管107cを介して、室内機Cと接続されている。中継機Bは、第1の接続配管106d及び第2の接続配管107dを介して、室内機Dと接続されている。 The relay B includes a first branching unit 110, a second branching unit 111, a gas-liquid separator 112, a second flow rate regulator 113, a third
The relay machine B is connected to the heat source machine A via the
電磁弁108aは、開閉可能な弁であり、一端が第1の接続配管106に接続され、他端が第1の接続配管106c、第1の接続配管106d、及び電磁弁108bの一方の端子と接続されている。電磁弁108bは、開閉可能な弁であり、一端が第2の接続配管107に接続され、他端が第1の接続配管106c、第1の接続配管106d、及び電磁弁108aの一方の端子と接続されている。 The first branching unit 110 includes an electromagnetic valve 108a and an electromagnetic valve 108b. The solenoid valve 108a and the solenoid valve 108b are connected to the indoor unit C through the first connection pipe 106c. The solenoid valve 108a and the solenoid valve 108b are connected to the indoor unit D through the first connection pipe 106d.
The solenoid valve 108a is a valve that can be opened and closed, and has one end connected to the
第2の流量調整器113は、開度が調整可能な流量調整器であり、圧力検出手段127aで検出した圧力値と、圧力検出手段127bで検出した圧力値との差が一定となるように開度を調整する。 The second flow rate regulator 113 has one end connected to the
The second flow rate regulator 113 is a flow rate regulator whose opening degree can be adjusted so that the difference between the pressure value detected by the pressure detection means 127a and the pressure value detected by the pressure detection means 127b is constant. Adjust the opening.
また、バイパス配管114は、一端が第1の接続配管106に接続され、他端が第3の流量調整器115に接続されている。
したがって、第3の流量調整器115の開度に応じて、熱源機Aへ供給する冷媒量は変動する。 One end of the third
The bypass pipe 114 has one end connected to the
Therefore, the amount of refrigerant supplied to the heat source unit A varies depending on the opening of the third
The
なお、上記の説明では、温度検出手段125は、サーミスタで形成される一例について説明したが、特にこれに限定しない。 The temperature detection means 125 is formed by a thermistor, for example. The temperature detection means 125 measures the temperature of the refrigerant flowing in the pipe provided between the third
In the above description, the temperature detection unit 125 is described as an example of a thermistor, but is not particularly limited thereto.
圧力検出手段127bは、第2の流量調整器113と、第2の熱交換器117及び第2の分岐部111との間に設けられた配管内を流れる冷媒の圧力を測定し、測定結果を制御部151に供給する。
なお、圧力検出手段127a及び圧力検出手段127bを総称して、圧力検出手段127と称する。圧力検出手段127は、測定結果をそのまま制御部151に供給してもよく、一定期間測定結果を蓄積後に蓄積した測定結果を所定の周期間隔で制御部151に供給してもよい。 The pressure detection unit 127 a measures the pressure of the refrigerant flowing in the pipe provided between the
The pressure detection means 127b measures the pressure of the refrigerant flowing in the pipe provided between the second flow rate regulator 113, the second heat exchanger 117, and the second branch part 111, and the measurement result is obtained. It supplies to the control part 151.
The pressure detection means 127a and the pressure detection means 127b are collectively referred to as a pressure detection means 127. The
上記で説明した利用側熱交換器105c及び第1の流量調整器109cで、冷媒回路の一部は構成される。 The indoor unit C includes a use side heat exchanger 105c, a liquid pipe temperature detecting means 126c, a first flow rate regulator 109c, and the like. A plurality of use side heat exchangers 105c are provided. Between the use side heat exchanger 105c and the first flow rate regulator 109c, a liquid pipe temperature detecting means 126c for detecting the temperature of the pipe is provided.
The utilization side heat exchanger 105c and the first flow rate regulator 109c described above constitute a part of the refrigerant circuit.
上記で説明した利用側熱交換器105d及び第1の流量制御装置109dで、冷媒回路の一部は構成される。 The indoor unit D includes a use side heat exchanger 105d, a liquid pipe temperature detection means 126d, a first flow rate regulator 109d, and the like. A plurality of use side heat exchangers 105d are provided. Between the use side heat exchanger 105d and the first flow rate regulator 109d, a liquid pipe temperature detecting means 126d for detecting the temperature of the pipe is provided.
The utilization side heat exchanger 105d and the first flow rate control device 109d described above constitute a part of the refrigerant circuit.
中継機Bは、上述したように、第3の流量調整器115を備え、熱源機A側への冷媒量の調整をする。 FIG. 2 is a diagram showing a modeled connection relationship between the second flow rate control device 122, the third flow rate control device 123, and the third
As described above, the relay unit B includes the third
なお、制御部141は、第2の流量制御装置122、第3の流量制御装置123、及び第4の流量調整弁124の開度を調整する。制御部151は、第3の流量調整器115の開度を調整する。そして、制御部141と、制御部151とは、各種信号を送受信することで、互いの制御内容を供給する。 Therefore, the third
Note that the
前提条件として、室内機Cには冷房運転、室内機Dには暖房運転がそれぞれ設定され、冷房主体で空気調和装置1の運転が行われると想定する。 FIG. 3 is a diagram illustrating a configuration example of the air-
As a precondition, it is assumed that a cooling operation is set for the indoor unit C and a heating operation is set for the indoor unit D, and the operation of the
第2の流量調整器113の開度は、圧力検出手段127aと圧力検出手段127bとの差圧が適度な値になるように制御される。 Of the electromagnetic valve 108a, the indoor unit C side is opened, and the indoor unit D side is closed. Of the electromagnetic valve 108b, the indoor unit C side is closed and the indoor unit D side is opened.
The opening degree of the second flow rate regulator 113 is controlled so that the differential pressure between the pressure detection means 127a and the pressure detection means 127b becomes an appropriate value.
熱源機側熱交換器103は、空気や水等の熱源媒体と熱交換する。熱交換した高温高圧のガス冷媒は、気液二相の高温高圧の冷媒となる。次に、気液二相の高温高圧の冷媒は、第4の流量調整弁124、逆止弁118を経て、第2の接続配管107を通過し、中継機Bの気液分離器112へ供給される。
気液分離器112は、気液二相の高温高圧の冷媒を、ガス状冷媒と、液状冷媒とに分離する。
分離されたガス状冷媒は、第1の分岐部110へ流入する。第1の分岐部110へ流入したガス状冷媒は、開口している側の電磁弁108b、第1の接続配管106dを経て、暖房運転が設定されている室内機Dへ供給される。 The flow of the refrigerant will be described. As indicated by a solid thick arrow, the high-temperature and high-pressure gas refrigerant compressed and discharged by the
The heat source machine
The gas-liquid separator 112 separates the gas-liquid two-phase high-temperature and high-pressure refrigerant into a gaseous refrigerant and a liquid refrigerant.
The separated gaseous refrigerant flows into the first branch part 110. The gaseous refrigerant that has flowed into the first branch portion 110 is supplied to the indoor unit D in which the heating operation is set, through the electromagnetic valve 108b on the open side and the first connection pipe 106d.
また、利用側熱交換器105dは、利用側熱交換器105dの出口の過冷却度に基づいて、第1の流量調整器109dで制御される。
第1の流量調整器109dは、利用側熱交換器105dで凝縮液化された液冷媒を減圧し、高圧と、低圧との中間の圧力である中間圧の気液二相冷媒にする。
中間圧となった気液二相冷媒は、第2の分岐部111に流入される。
第2の分岐部111に流入した気液二相冷媒のガス冷媒は、室内機Dへと流入する。第2の分岐部111に流入した気液二相冷媒の液冷媒は、第2の分岐部111から出た後、第2の流量調整器113を通った液冷媒と合流し、第1の熱交換器116で後述するように熱交換された後、再び第2の分岐部111へ戻り、室内機Cや室内機Dへ流入する。 In the indoor unit D, the use side heat exchanger 105d exchanges heat with a use medium such as air, and condenses and liquefies the supplied gaseous refrigerant.
In addition, the usage-side heat exchanger 105d is controlled by the first flow rate regulator 109d based on the degree of supercooling at the outlet of the usage-side heat exchanger 105d.
The first flow controller 109d depressurizes the liquid refrigerant condensed and liquefied by the use side heat exchanger 105d, and converts it into a gas-liquid two-phase refrigerant having an intermediate pressure that is an intermediate pressure between the high pressure and the low pressure.
The gas-liquid two-phase refrigerant that has reached the intermediate pressure flows into the second branch portion 111.
The gas refrigerant of the gas-liquid two-phase refrigerant that has flowed into the second branch portion 111 flows into the indoor unit D. The liquid refrigerant of the gas-liquid two-phase refrigerant that has flowed into the second branch part 111 exits from the second branch part 111, and then merges with the liquid refrigerant that has passed through the second flow rate regulator 113, so that the first heat After the heat exchange is performed by the
次に、第2の分岐部111では、供給された液状冷媒は、室内機C側に接続されている逆止弁108dを通過し、室内機Cへ流入する。
次に、流入した液状冷媒は、室内機Cの利用側熱交換器105cの出口の過熱度に応じて制御される第1の流量調整器109cを用いて低圧まで減圧された状態で、利用側熱交換器105cに供給される。
利用側熱交換器105cでは、供給された液状冷媒は、空気等の利用媒体と熱交換することで、蒸発してガス化する。
ガス化して、ガス冷媒となった冷媒は、第1の接続配管106cを通過し、第1の分岐部110へ流入する。第1の分岐部110では、室内機Cと接続された側の電磁弁108aが開口している。そこで、流入したガス冷媒は、室内機Cと接続された側の電磁弁108aを通過し、第1の接続配管106へ流入する。
次に、ガス冷媒は、逆止弁121よりも低圧の逆止弁119側へ流入し、四方弁102、アキュムレータ104を経て、圧縮機101へ吸入される。
このような動作で、冷凍サイクルが形成され、冷房主体運転が行われる。 On the other hand, the liquid refrigerant separated by the gas-liquid separator 112 passes through the second flow rate regulator 113 that controls the pressure difference between the high pressure and the intermediate pressure to be constant, and flows into the second branch portion 111. To do.
Next, in the second branch portion 111, the supplied liquid refrigerant passes through the check valve 108d connected to the indoor unit C and flows into the indoor unit C.
Next, the inflowing liquid refrigerant is decompressed to a low pressure by using the first flow rate regulator 109c controlled according to the degree of superheat at the outlet of the utilization side heat exchanger 105c of the indoor unit C. It is supplied to the heat exchanger 105c.
In the use-side heat exchanger 105c, the supplied liquid refrigerant is evaporated and gasified by exchanging heat with a use medium such as air.
The refrigerant that has been gasified to become a gas refrigerant passes through the first connection pipe 106 c and flows into the first branch 110. In the first branch part 110, the solenoid valve 108a on the side connected to the indoor unit C is open. Therefore, the gas refrigerant that has flowed in passes through the electromagnetic valve 108 a on the side connected to the indoor unit C, and flows into the
Next, the gas refrigerant flows into the
With such an operation, a refrigeration cycle is formed and a cooling main operation is performed.
前提条件として、室内機Cには暖房運転、室内機Dには冷房運転がそれぞれ設定され、暖房主体で空気調和装置1の運転が行われると想定する。 FIG. 4 is a diagram showing a configuration example of the air-
As a precondition, it is assumed that a heating operation is set for the indoor unit C and a cooling operation is set for the indoor unit D, and the operation of the
第2の流量調整器113の開度は、圧力検出手段127aと圧力検出手段127bとの差圧が適度な値になるように制御される。 Of the electromagnetic valve 108a, the indoor unit C side is closed and the indoor unit D side is opened. Of the electromagnetic valve 108b, the indoor unit C side is opened, and the indoor unit D side is closed.
The opening degree of the second flow rate regulator 113 is controlled so that the differential pressure between the pressure detection means 127a and the pressure detection means 127b becomes an appropriate value.
気液分離器112は、高温高圧のガス冷媒を、第1の分岐部110へ供給する。第1の分岐部110へ供給されたガス冷媒は、開口している側の電磁弁108b、第1の接続配管106cを経て、暖房運転が設定されている室内機Cへ供給される。 The flow of the refrigerant will be described. As indicated by a solid thick arrow, the high-temperature and high-pressure gas refrigerant compressed and discharged by the
The gas-liquid separator 112 supplies a high-temperature and high-pressure gas refrigerant to the first branch part 110. The gas refrigerant supplied to the first branch part 110 is supplied to the indoor unit C in which the heating operation is set, through the open solenoid valve 108b and the first connection pipe 106c.
また、利用側熱交換器105cは、利用側熱交換器105cの出口の過冷却度に基づいて、第1の流量調整器109cで制御される。
第1の流量調整器109cは、利用側熱交換器105cで凝縮液化された液冷媒を減圧し、高圧と、低圧との中間の圧力である中間圧の気液二相冷媒にする。
中間圧となった気液二相冷媒は、第2の分岐部111に流入される。 In the indoor unit C, the use side heat exchanger 105c exchanges heat with a use medium such as air, and the supplied gas refrigerant is condensed and liquefied.
The use side heat exchanger 105c is controlled by the first flow rate regulator 109c based on the degree of supercooling at the outlet of the use side heat exchanger 105c.
The first flow controller 109c depressurizes the liquid refrigerant condensed and liquefied by the use side heat exchanger 105c, and converts it into a gas-liquid two-phase refrigerant having an intermediate pressure that is an intermediate pressure between the high pressure and the low pressure.
The gas-liquid two-phase refrigerant that has reached the intermediate pressure flows into the second branch portion 111.
次に、流入した液状冷媒は、室内機Dの利用側熱交換器105dの出口の過熱度に応じて制御される第1の流量調整器109dを用いて低圧まで減圧された状態で、利用側熱交換器105dに供給される。
利用側熱交換器105dでは、供給された液状冷媒は、空気等の利用媒体と熱交換することで、蒸発してガス化する。 Next, the gas-liquid two-phase refrigerant that has flowed into the second branch part 111 joins at the meeting part 137a_all. The gas-liquid two-phase refrigerant joined at the meeting part 137a_all passes through the
Next, the inflowing liquid refrigerant is decompressed to a low pressure by using the first flow rate regulator 109d controlled according to the degree of superheat at the outlet of the utilization side heat exchanger 105d of the indoor unit D. It is supplied to the heat exchanger 105d.
In the use side heat exchanger 105d, the supplied liquid refrigerant evaporates and gasifies by exchanging heat with a use medium such as air.
次に、ガス冷媒は、逆止弁119よりも低圧の逆止弁121側へ流入し、第4の流量調整弁124、熱源機側熱交換器103に流入して蒸発してガス状態となる。次に、四方弁102、アキュムレータ104を経て、圧縮機101へ吸入される。
このような動作で、冷凍サイクルが形成され、暖房主体運転が行われる。 The refrigerant that has been gasified to become a gas refrigerant passes through the first connection pipe 106d and flows into the first branch 110. In the 1st branch part 110, the solenoid valve 108a by the side connected with the indoor unit D is opening. Therefore, the gas refrigerant that has flowed in passes through the electromagnetic valve 108 a on the side connected to the indoor unit D, and flows into the
Next, the gas refrigerant flows into the check valve 121 side having a pressure lower than that of the
With such an operation, a refrigeration cycle is formed, and a heating main operation is performed.
具体的には、空気調和装置1は、外気温度が低くなるにつれ、高圧圧力を高く維持できなくなり、暖房能力は低下してしまう。また、低圧圧力が低下することで、冷房運転している室内機Dは、継続した運転を維持できなくなってしまい、冷房運転と、暖房運転との両方において問題が生じる。 Here, when the cooling / heating simultaneous operation is being performed and the outside air temperature is low during the heating-main operation, the heat source apparatus
Specifically, as the outside air temperature decreases, the
図5では、横軸の基準温度がα、縦軸の基準暖房能力比がβであると想定する。
図5に示すように、外気温度がある値以下となった場合、第2の流量制御装置122の開度が小さければ、暖房能力比は低いが、第2の流量制御装置122の開度を大きくすると、暖房能力比は向上する。
換言すれば、暖房能力を上昇させるには、第2の流量制御装置122の開度を大きくとれば、高圧圧力を高く維持することができる。
具体的には、第2の流量制御装置122から圧縮機101へバイパスさせる流量、すなわち、インジェクション量を多くすることで、高圧圧力が上昇し、暖房能力を高くすることができる。例えば、外気温度がα-30℃において、インジェクション量を30~40%大きくすると、暖房能力は、約8%上昇する。 FIG. 5 is a diagram for explaining an example of the correlation between the outside air temperature and the heating capacity ratio according to the opening degree of the second flow control device 122 according to
In FIG. 5, it is assumed that the reference temperature on the horizontal axis is α and the reference heating capacity ratio on the vertical axis is β.
As shown in FIG. 5, when the outside air temperature falls below a certain value, if the opening of the second flow control device 122 is small, the heating capacity ratio is low, but the opening of the second flow control device 122 is reduced. If it is increased, the heating capacity ratio is improved.
In other words, in order to increase the heating capacity, the high pressure can be maintained high by increasing the opening of the second flow control device 122.
Specifically, by increasing the flow rate bypassed from the second flow control device 122 to the
上記で説明した点を考慮すると、冷暖房同時運転中であって、暖房主体運転時、外気温度がある値と比較して低下した場合、室内機Dの液管温度検出手段126がある値以下となり、冷房運転を維持できなくなる。この理由のため、第3の流量制御装置123の開度を抑制することで、室内機Dの液管温度を上げると同時に、圧縮機101へのインジェクション量を優先させる。
この動作で、冷房運転であっても、暖房運転であっても快適な運転を行うことができる。
このような相関特性を考慮し、第2の流量制御装置122の開度と、第3の流量制御装置123の開度について説明する。 Here, the opening degree of the third flow control device 123 is also examined. When the third flow control device 123 is opened to a certain degree of opening or more, the second flow control device 122 and the third flow control device 123 are connected in parallel. The flow rate decreases.
Considering the points described above, when the cooling / heating simultaneous operation is being performed and the outside air temperature is lower than a certain value during the heating main operation, the liquid pipe temperature detecting means 126 of the indoor unit D becomes a certain value or less. The cooling operation cannot be maintained. For this reason, priority is given to the injection amount to the
With this operation, a comfortable operation can be performed regardless of whether it is a cooling operation or a heating operation.
Considering such correlation characteristics, the opening degree of the second flow control device 122 and the opening degree of the third flow control device 123 will be described.
図6では、横軸の基準温度がα、縦軸の基準流量比がβである場合を想定する。
図6に示すように、外気温度がα-20℃のとき、第3の流量制御装置123の流量を低下させ、第2の流量制御装置122の流量を上昇させる。
この動作で、暖房能力を上昇させることができる。このときには、低圧圧力も低下しているため、冷房能力への影響は生じない。 FIG. 6 illustrates an example of the correlation between the outside air temperature and the flow rate ratio according to the opening degree of the second flow control device 122 and the opening degree of the third flow control device 123 in
In FIG. 6, it is assumed that the reference temperature on the horizontal axis is α and the reference flow ratio on the vertical axis is β.
As shown in FIG. 6, when the outside air temperature is α-20 ° C., the flow rate of the third flow control device 123 is decreased and the flow rate of the second flow control device 122 is increased.
With this operation, the heating capacity can be increased. At this time, since the low pressure is also lowered, there is no influence on the cooling capacity.
図7は、本発明の実施の形態1における第2の流量制御装置122の開度、第3の流量制御装置123の開度、及び第3の流量調整器115の開度に応じた外気温度と流量比との相関関係の一例を説明する図である。
図7では、圧力検出手段127a、127bの前後の高圧と中間圧との差圧を一定に制御する中継機Bが備える第3の流量調整器115は、第3の流量制御装置123の動作と同様に、外気温度が低下するにつれ、第3の流量調整器115の開度を小さくさせる。
この動作で、高圧と、中間圧との差圧が一定に維持されると同時に、室内機Dの液管温度を上昇させることができる。
この結果、冷房運転を維持させることができる。 Next, the correlation with the relay station B is also examined.
FIG. 7 shows the outside air temperature according to the opening of the second flow control device 122, the opening of the third flow control device 123, and the opening of the
In FIG. 7, the third
With this operation, the pressure difference between the high pressure and the intermediate pressure is maintained constant, and at the same time, the liquid pipe temperature of the indoor unit D can be raised.
As a result, the cooling operation can be maintained.
図8に示すように、外気温度がある値以上となった場合には、第2の流量制御装置122の適正開度を調整することで、冷房能力への影響を小さくでき、安定した冷房能力を維持できる。 FIG. 8 is a diagram illustrating an example of the correlation between the outside air temperature and the heating capacity ratio depending on whether or not there is proper control of the second flow control device 122 in
As shown in FIG. 8, when the outside air temperature exceeds a certain value, the influence on the cooling capacity can be reduced by adjusting the appropriate opening degree of the second flow control device 122, and the stable cooling capacity. Can be maintained.
図9に示すように、第4の流量調整弁124の開度を調整することで、冷房能力への影響を小さくでき、安定した冷房能力を維持できる。例えば、外気温度がある値と比較して低い場合、第4の流量調整弁124の開度を小さくし、外気温度がある値と比較して高い場合、第4の流量調整弁124の開度を大きくする。
この動作で、冷房能力への影響を小さくでき、安定した冷房能力を維持できる。 FIG. 9 is a diagram for explaining an example of the correlation between the outside air temperature and the heating capacity ratio depending on whether or not the fourth flow regulating valve 124 is appropriately controlled in
As shown in FIG. 9, by adjusting the opening degree of the fourth flow rate adjustment valve 124, the influence on the cooling capacity can be reduced, and the stable cooling capacity can be maintained. For example, when the outside air temperature is low compared to a certain value, the opening degree of the fourth flow rate adjustment valve 124 is reduced, and when the outside air temperature is high compared to a certain value, the opening degree of the fourth flow rate adjustment valve 124. Increase
With this operation, the influence on the cooling capacity can be reduced, and a stable cooling capacity can be maintained.
したがって、高効率な冷暖房同時運転を行うことができる。
なお、本実施の形態1では、冷房主体運転及び暖房主体運転について説明したが、特にこれに限定しない。例えば、暖房のみであってもよい。
また、熱源機Aの台数、中継機Bの台数、及び室内機の台数の何れにおいても上記実施の形態1と異なる台数であっても同様の効果を奏することができる。
また、熱源機側熱交換器103と直列又は並列に氷蓄熱槽や水蓄熱槽(湯を含む)が設置されても同様の効果を奏する。
さらに、熱源機A、中継機B、第1の接続配管106、第2の接続配管107の接続配管の合計が2本の構成について説明したが、接続配管の合計が3本の構成であっても同様の効果を奏することができる。 As described above, by appropriately controlling the opening degree of the second flow rate control device 122, the third flow rate control device 123, and the third
Therefore, highly efficient cooling and heating simultaneous operation can be performed.
In addition, in this
Moreover, even if the number of heat source units A, the number of relay units B, and the number of indoor units are different from those in the first embodiment, the same effect can be obtained.
Moreover, even if an ice heat storage tank or a water heat storage tank (including hot water) is installed in series or in parallel with the heat source device
Furthermore, although the total of the connection pipes of the heat source machine A, the relay machine B, the
図10は、本発明の実施の形態1における熱源機Aが備える制御部141の動作例を説明するフローチャートである。 Next, on the assumption of the above description, an operation example will be described with reference to the drawings.
FIG. 10 is a flowchart for explaining an operation example of the
熱源機Aの制御部141は、冷暖房同時運転中であるか否かを判定する。熱源機Aの制御部141は、冷暖房同時運転中であると判定した場合、ステップS12へ進む。一方、熱源機Aの制御部141は、冷暖房同時運転中でないと判定した場合、ステップS16へ進む。 (Step S11)
The
熱源機Aの制御部141は、外気温度を取得する。例えば、外気温度検出手段131で検出した外気温度データを取得する。 (Step S12)
The
熱源機Aの制御部141は、外気温度が予め定めた複数の閾値の何れかに該当するか否かを判定する。
例えば、熱源機Aの制御部141は、外気温度がインジェクション開始閾値(WB℃)以下である場合、ステップS14へ進む。インジェクション開始閾値(WB℃)は、例えば、図6で示すように、第2の流量制御装置122の開度が少しづつ大きくなる開始温度であるα-5(WB℃)に相当する。α-5(WB℃)は、例えば、0℃が想定される。
なお、上記の説明では、α-5(WB℃)が0℃である一例について説明したが、特にこれに限定しない。α-5(WB℃)の具体的な値は、周囲環境や空気調和装置1の稼働状況に応じて、臨機応変に可変されればよい。 (Step S13)
The
For example, when the outside air temperature is equal to or lower than the injection start threshold (WB ° C.), the
In the above description, an example in which α-5 (WB ° C.) is 0 ° C. has been described, but the present invention is not particularly limited to this. The specific value of α-5 (WB ° C.) may be varied flexibly according to the surrounding environment and the operating condition of the
具体的には、室内機C及び室内機Dの何れかが冷房運転中に、外気温度が-15℃に到達したとき、冷房中の室内機と、第2の分岐部111との間の配管の液管温度が低下し、冷房運転を継続することができない。そこで、外気温度が-15℃の場合、第3の流量制御装置123の開度を絞り込むことで、その配管の液管温度を上げ、冷房運転を継続させる。
なお、上記の説明では、α-20(WB℃)が-15℃である一例について説明したが、特にこれに限定しない。α-20(WB℃)の具体的な値は、周囲環境や空気調和装置1の稼働状況に応じて、臨機応変に可変されればよい。 For example, when the outside air temperature is equal to or lower than the opening degree suppression threshold (WB ° C.), the
Specifically, when either the indoor unit C or the indoor unit D is in the cooling operation and the outside air temperature reaches −15 ° C., the piping between the indoor unit being cooled and the second branching unit 111 The liquid pipe temperature of the tube drops, and the cooling operation cannot be continued. Therefore, when the outside air temperature is −15 ° C., the opening degree of the third flow control device 123 is narrowed to raise the liquid pipe temperature of the pipe and continue the cooling operation.
In the above description, an example in which α-20 (WB ° C.) is −15 ° C. has been described, but the present invention is not particularly limited to this. The specific value of α-20 (WB ° C.) may be varied in a flexible manner according to the surrounding environment and the operating status of the
熱源機Aの制御部141は、第2の流量制御装置122の開度を予め設定した割合で大きくする。例えば、図6に示すように、外気温度に応じて、段階的に絞り込む開度の割合を変更していく。 (Step S14)
The
熱源機Aの制御部141は、第3の流量制御装置123の開度を抑制する。例えば、図6に示すように、外気温度がαからα-20までは、第3の流量制御装置123の開度は全開にしていたが、外気温度がα-20以下の場合、第3の流量制御装置123の開度は絞り込まれていく。 (Step S15)
The
熱源機Aの制御部141は、終了指令が有るか否かを判定する。熱源機Aの制御部141は、終了指令が有る場合、処理を終了させる。一方、熱源機Aの制御部141は、終了指令が無い場合、ステップS12へ戻り、ステップS12~ステップS15の処理を繰り返す。 (Step S16)
The
中継機Bの制御部151は、第1の割合を設定する。第1の割合は、図7に示すように、外気温度がα-20を上回り、かつ、α以下である間に、第3の流量調整器115を絞り込む開度の割合である。 (Step S51)
The control unit 151 of the relay machine B sets the first ratio. As shown in FIG. 7, the first ratio is the ratio of the degree of opening for narrowing the third
中継機Bの制御部151は、第2の割合>第1の割合という条件を満たす第2の割合を設定する。第2の割合は、図7に示すように、外気温度がα-20以下の場合、第3の流量調整器115を絞り込む開度の割合である。上述したように、α-20を冷房運転が継続できなくなる外気温度と想定したとき、外気温度がα-20以下となったら、冷房運転中の室内機の液管温度を上げなければ冷房運転を継続できない。そこで、絞り込む割合を大きく設定する。 (Step S52)
The control unit 151 of the relay B sets a second ratio that satisfies the condition that the second ratio> the first ratio. As shown in FIG. 7, the second ratio is the ratio of the degree of opening that narrows down the
中継機Bの制御部151は、冷暖房同時運転中であるか否かを判定する。中継機Bの制御部151は、冷暖房同時運転中である場合、ステップS54へ進む。一方、中継機Bの制御部151は、冷暖房同時運転中でない場合、処理を終了する。 (Step S53)
The control unit 151 of the relay machine B determines whether or not the cooling and heating simultaneous operation is being performed. When the air conditioner simultaneous operation is being performed, the control unit 151 of the relay machine B proceeds to step S54. On the other hand, the control part 151 of the relay machine B complete | finishes a process, when it is not in the air conditioning simultaneous operation.
中継機Bの制御部151は、終了指令が有るか否かを判定する。中継機Bの制御部151は、終了指令が有る場合、処理を終了する。一方、中継機Bの制御部151は、終了指令が無い場合、ステップS55へ進む。 (Step S54)
The control unit 151 of the relay machine B determines whether or not there is an end command. The control unit 151 of the relay machine B ends the process when there is an end command. On the other hand, if there is no termination command, the control unit 151 of the relay station B proceeds to step S55.
中継機Bの制御部151は、高圧側圧力値を取得する。例えば、中継機Bの制御部151は、圧力検出手段127a、127bのうち、高圧側となっている圧力値を取得する。どちらが高圧側であるかは、中継機Bの制御部151が、予め運転状態に応じて、どちらが高圧側に該当するかが登録された対応テーブルを保持し、そこから判断してもよい。 (Step S55)
The control unit 151 of the relay machine B acquires the high pressure side pressure value. For example, the control unit 151 of the relay machine B acquires the pressure value on the high pressure side among the pressure detection units 127a and 127b. Which is on the high voltage side may be determined by the control unit 151 of the relay B holding a correspondence table in which which corresponds to the high voltage side is registered in advance according to the operating state.
中継機Bの制御部151は、中間圧側圧力値を取得する。例えば、中継機Bの制御部151は、圧力検出手段127a、127bのうち、中間圧側となっている圧力値を取得する。どちらが中間圧側であるかは、中継機Bの制御部151が、予め運転状態に応じて、どちらが中間圧側に該当するかが登録された対応テーブルを保持し、そこから判断してもよい。 (Step S56)
The control unit 151 of the relay machine B acquires the intermediate pressure side pressure value. For example, the control unit 151 of the relay machine B acquires the pressure value on the intermediate pressure side among the pressure detection units 127a and 127b. Which is on the intermediate pressure side may be determined by the control unit 151 of the relay B holding a correspondence table in which which corresponds to the intermediate pressure side is registered in advance according to the operating state.
中継機Bの制御部151は、高圧側圧力値と中間圧側圧力値との差圧を求める。 (Step S57)
The control unit 151 of the relay machine B obtains a differential pressure between the high pressure side pressure value and the intermediate pressure side pressure value.
中継機Bの制御部151は、差圧は一定であるか否かを判定する。中継機Bの制御部151は、差圧が一定である場合、ステップS59へ進む。一方、中継機Bの制御部151は、差圧が一定でない場合、ステップS60へ進む。 (Step S58)
The control unit 151 of the relay B determines whether or not the differential pressure is constant. When the differential pressure is constant, the control unit 151 of the relay machine B proceeds to step S59. On the other hand, when the differential pressure is not constant, the control unit 151 of the relay station B proceeds to step S60.
中継機Bの制御部151は、外気温度を取得する。 (Step S59)
The control unit 151 of the relay machine B acquires the outside air temperature.
中継機Bの制御部151は、第3の流量調整器115で差圧を一定にする。 (Step S60)
The control unit 151 of the relay machine B makes the differential pressure constant by the third
中継機Bの制御部151は、外気温度が予め定めた複数の閾値の何れかに該当するか否かを判定する。
例えば、外気温度が、第2閾値(WB℃)を上回り、かつ、第1閾値(WB℃)以下の場合、ステップS62へ進む。
また、例えば、外気温度が、第2閾値(WB℃)以下の場合、ステップS63へ進む。
また、例えば、それ以外の場合(第1閾値(WB℃)を上回る場合)、ステップS54へ戻る。 (Step S61)
The control unit 151 of the relay machine B determines whether or not the outside air temperature corresponds to any of a plurality of predetermined threshold values.
For example, when the outside air temperature exceeds the second threshold value (WB ° C.) and is equal to or lower than the first threshold value (WB ° C.), the process proceeds to step S62.
For example, when the outside air temperature is equal to or lower than the second threshold (WB ° C.), the process proceeds to step S63.
For example, in other cases (when exceeding the first threshold (WB ° C.)), the process returns to step S54.
中継機Bの制御部151は、第3の流量調整器115の開度を第1の割合で抑制し、ステップS54へ戻る。 (Step S62)
The control unit 151 of the relay machine B suppresses the opening degree of the third
中継機Bの制御部151は、第3の流量調整器115の開度を第2の割合で抑制し、ステップS54へ戻る。 (Step S63)
The control unit 151 of the relay machine B suppresses the opening degree of the third
Claims (6)
- 冷媒を圧縮して吐出する1台の圧縮機と、
前記冷媒と周囲の熱源媒体とで熱交換する熱源機側熱交換器と、
前記冷媒と周囲の利用媒体とで熱交換する複数の利用側熱交換器と、
前記熱源機側熱交換器と、前記利用側熱交換器との間に設けられ、前記複数の利用側熱交換器の一部を冷房運転側に切り換え、前記複数の利用側熱交換器の一部を暖房運転側に切り換える中継機と
を備え、
制御指令に応じて、前記複数の利用側熱交換器のうち、前記冷房運転側及び前記暖房運転側の何れかに前記複数の利用側熱交換器のそれぞれを切り換えることで、冷暖房同時運転を行う空気調和装置であって、
前記中継機と、前記熱源機側熱交換器との間に設けられ、該熱源機側熱交換器に流入する前記冷媒をバイパスして前記1台の圧縮機に供給するインジェクション配管と、
前記インジェクション配管に設けられ、前記1台の圧縮機に流入する前記冷媒の流量を調整する圧縮機用流量制御装置と、
前記圧縮機用流量制御装置と並列に接続され、前記熱源機側熱交換器に流入する前記冷媒の流量を調整する熱源機側熱交換器用流量制御装置と、
前記圧縮機用流量制御装置及び前記熱源機側熱交換器用流量制御装置を調整する制御部と
を備え、
前記制御部は、
外気温度に応じて、前記圧縮機用流量制御装置の開度及び前記熱源機側熱交換器用流量制御装置の開度を調整する
ことを特徴とする空気調和装置。 One compressor that compresses and discharges the refrigerant;
A heat source side heat exchanger that exchanges heat between the refrigerant and the surrounding heat source medium;
A plurality of use side heat exchangers for exchanging heat between the refrigerant and the surrounding use medium;
Provided between the heat source unit side heat exchanger and the use side heat exchanger, a part of the plurality of use side heat exchangers is switched to a cooling operation side, and one of the plurality of use side heat exchangers A relay unit for switching the part to the heating operation side,
According to a control command, among the plurality of use side heat exchangers, the cooling and heating simultaneous operation is performed by switching each of the plurality of use side heat exchangers to either the cooling operation side or the heating operation side. An air conditioner,
An injection pipe that is provided between the relay machine and the heat source machine side heat exchanger, bypasses the refrigerant flowing into the heat source machine side heat exchanger, and supplies the refrigerant to the one compressor;
A compressor flow controller for adjusting a flow rate of the refrigerant that is provided in the injection pipe and flows into the one compressor;
A flow control device for heat source side heat exchanger that is connected in parallel with the flow rate control device for compressor and adjusts the flow rate of the refrigerant flowing into the heat source side heat exchanger;
A controller for adjusting the flow rate control device for the compressor and the flow rate control device for the heat source unit side heat exchanger, and
The controller is
An air conditioner that adjusts an opening degree of the compressor flow rate control device and an opening degree of the heat source unit side heat exchanger flow control device according to an outside air temperature. - 前記制御部は、
前記インジェクション配管から前記冷媒の供給を開始するインジェクション開始閾値が設定され、
前記熱源機側熱交換器用流量制御装置を通過する前記冷媒の流量を小さくする開度抑制閾値が設定され、
前記外気温度が前記インジェクション開始閾値以下の場合、前記圧縮機用流量制御装置の開度を予め設定した割合で大きくし、
前記外気温度が前記開度抑制閾値以下の場合、前記熱源機側熱交換器用流量制御装置の開度を小さくする
ことを特徴とする請求項1に記載の空気調和装置。 The controller is
An injection start threshold for starting the supply of the refrigerant from the injection pipe is set,
An opening degree suppression threshold for reducing the flow rate of the refrigerant passing through the heat source unit side heat exchanger flow control device is set,
If the outside air temperature is less than or equal to the injection start threshold, increase the opening of the compressor flow control device at a preset rate,
2. The air conditioner according to claim 1, wherein when the outside air temperature is equal to or less than the opening degree suppression threshold, the opening degree of the heat source unit side heat exchanger flow control device is reduced. - 前記中継機は、
前記圧縮機用流量制御装置及び前記熱源機側熱交換器用流量制御装置と直列に接続され、該中継機を流れる前記冷媒の流量を調整する流量調整器を備え、
前記外気温度に応じて、前記流量調整器の開度を調整する
ことを特徴とする請求項2に記載の空気調和装置。 The repeater is
A flow rate regulator that is connected in series with the flow rate control device for the compressor and the flow rate control device for the heat source side heat exchanger, and that adjusts the flow rate of the refrigerant flowing through the relay,
The air conditioner according to claim 2, wherein an opening degree of the flow rate regulator is adjusted in accordance with the outside air temperature. - 前記中継機は、
第1の割合と、該第1の割合に対応する第1閾値が設定され、
前記第1の割合と比べて大きな値となる第2の割合と、該第2の割合に対応する第2閾値が設定され、
前記外気温度が前記第1閾値以下の場合、前記流量調整器の開度を前記第1の割合で小さくし、
前記外気温度が前記第2閾値以下の場合、前記流量調整器の開度を前記第2の割合で小さくする
ことを特徴とする請求項3に記載の空気調和装置。 The repeater is
A first ratio and a first threshold value corresponding to the first ratio are set;
A second ratio that is larger than the first ratio and a second threshold value corresponding to the second ratio are set;
When the outside air temperature is less than or equal to the first threshold, the opening of the flow rate regulator is reduced by the first rate,
4. The air conditioner according to claim 3, wherein when the outside air temperature is equal to or lower than the second threshold, the opening degree of the flow rate regulator is decreased by the second ratio. - 前記中継機と前記熱源機側熱交換器との間に設けられ、前記熱源機側熱交換器用流量制御装置と並列に接続され、前記冷媒の流量を調整する流量調整弁を備え、
前記制御部は、
前記外気温度に応じて、前記流量調整弁の開度を調整する
ことを特徴とする請求項4に記載の空気調和装置。 Provided between the relay machine and the heat source machine side heat exchanger, connected in parallel with the heat source machine side heat exchanger flow control device, comprising a flow rate adjustment valve for adjusting the flow rate of the refrigerant,
The controller is
The air conditioner according to claim 4, wherein an opening degree of the flow rate adjusting valve is adjusted according to the outside air temperature. - 前記制御部は、
前記外気温度が前記インジェクション開始閾値以下の場合、前記圧縮機用流量制御装置の開度の調整で、前記中継機から供給される冷媒量のうち、前記圧縮機へ流す冷媒量を増加させ、
前記外気温度が前記開度抑制閾値以下の場合、前記熱源機側熱交換器用流量制御装置の開度及び前記流量調整弁の開度の調整で、前記中継機から供給される冷媒量のうち、前記熱源機側熱交換器へ流す冷媒量を小さくさせる
ことを特徴とする請求項5に記載の空気調和装置。 The controller is
When the outside air temperature is equal to or lower than the injection start threshold, by adjusting the opening of the compressor flow control device, among the amount of refrigerant supplied from the relay, the amount of refrigerant flowing to the compressor is increased,
When the outside air temperature is equal to or less than the opening degree suppression threshold, among the amount of refrigerant supplied from the relay machine by adjusting the opening degree of the heat source unit side heat exchanger flow control device and the opening degree of the flow rate adjustment valve, The air conditioner according to claim 5, wherein the amount of refrigerant flowing to the heat source unit side heat exchanger is reduced.
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EP12886159.8A EP2905560A4 (en) | 2012-10-01 | 2012-10-01 | Air conditioning device |
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PCT/JP2012/075309 WO2014054090A1 (en) | 2012-10-01 | 2012-10-01 | Air conditioning device |
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US (1) | US20150219373A1 (en) |
EP (1) | EP2905560A4 (en) |
JP (1) | JPWO2014054090A1 (en) |
WO (1) | WO2014054090A1 (en) |
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CN103759455B (en) * | 2014-01-27 | 2015-08-19 | 青岛海信日立空调系统有限公司 | Reclamation frequency conversion thermal multiple heat pump and control method thereof |
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- 2012-10-01 US US14/420,761 patent/US20150219373A1/en not_active Abandoned
- 2012-10-01 WO PCT/JP2012/075309 patent/WO2014054090A1/en active Application Filing
- 2012-10-01 EP EP12886159.8A patent/EP2905560A4/en not_active Withdrawn
- 2012-10-01 JP JP2014539487A patent/JPWO2014054090A1/en not_active Ceased
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Also Published As
Publication number | Publication date |
---|---|
US20150219373A1 (en) | 2015-08-06 |
EP2905560A1 (en) | 2015-08-12 |
EP2905560A4 (en) | 2016-05-18 |
JPWO2014054090A1 (en) | 2016-08-25 |
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