WO2014106895A1 - ヒートポンプシステム - Google Patents
ヒートポンプシステム Download PDFInfo
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- WO2014106895A1 WO2014106895A1 PCT/JP2013/050023 JP2013050023W WO2014106895A1 WO 2014106895 A1 WO2014106895 A1 WO 2014106895A1 JP 2013050023 W JP2013050023 W JP 2013050023W WO 2014106895 A1 WO2014106895 A1 WO 2014106895A1
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- WIPO (PCT)
- Prior art keywords
- hot water
- water supply
- heating
- indoor
- heat exchanger
- Prior art date
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 381
- 238000004781 supercooling Methods 0.000 claims abstract description 19
- 238000010438 heat treatment Methods 0.000 claims description 150
- 230000007246 mechanism Effects 0.000 claims description 132
- 239000003507 refrigerant Substances 0.000 claims description 82
- 230000006837 decompression Effects 0.000 claims description 60
- 238000003860 storage Methods 0.000 claims description 32
- 230000008859 change Effects 0.000 claims description 20
- 230000009467 reduction Effects 0.000 claims description 11
- 238000005259 measurement Methods 0.000 claims description 8
- 230000005494 condensation Effects 0.000 claims description 7
- 238000009833 condensation Methods 0.000 claims description 7
- 238000005338 heat storage Methods 0.000 claims description 7
- 239000008236 heating water Substances 0.000 claims description 2
- 239000007788 liquid Substances 0.000 description 19
- 238000000034 method Methods 0.000 description 17
- 239000007789 gas Substances 0.000 description 14
- 238000009826 distribution Methods 0.000 description 13
- 238000009434 installation Methods 0.000 description 9
- 230000003247 decreasing effect Effects 0.000 description 8
- 230000007423 decrease Effects 0.000 description 7
- 238000010586 diagram Methods 0.000 description 7
- 238000004891 communication Methods 0.000 description 6
- 230000008569 process Effects 0.000 description 6
- 238000009835 boiling Methods 0.000 description 5
- 239000002826 coolant Substances 0.000 description 5
- 238000001816 cooling Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000005057 refrigeration Methods 0.000 description 3
- 230000004044 response Effects 0.000 description 3
- OHMHBGPWCHTMQE-UHFFFAOYSA-N 2,2-dichloro-1,1,1-trifluoroethane Chemical compound FC(F)(F)C(Cl)Cl OHMHBGPWCHTMQE-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 229920000092 linear low density polyethylene Polymers 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 230000000630 rising effect Effects 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 230000005856 abnormality Effects 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 230000001143 conditioned effect Effects 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000001307 helium Substances 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 238000005304 joining Methods 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000010079 rubber tapping Methods 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 230000001052 transient effect Effects 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
Images
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
- F24D17/00—Domestic hot-water supply systems
- F24D17/02—Domestic hot-water supply systems using heat pumps
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
- F24D19/00—Details
- F24D19/10—Arrangement or mounting of control or safety devices
- F24D19/1006—Arrangement or mounting of control or safety devices for water heating systems
- F24D19/1051—Arrangement or mounting of control or safety devices for water heating systems for domestic hot water
- F24D19/1054—Arrangement or mounting of control or safety devices for water heating systems for domestic hot water the system uses a heat pump
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
- F24D5/00—Hot-air central heating systems; Exhaust gas central heating systems
- F24D5/12—Hot-air central heating systems; Exhaust gas central heating systems using heat pumps
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H1/00—Water heaters, e.g. boilers, continuous-flow heaters or water-storage heaters
-
- 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
-
- 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
-
- 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
-
- 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
-
- 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
- F25B2313/021—Indoor unit or outdoor unit with auxiliary heat exchanger not forming part of the indoor or outdoor unit
- F25B2313/0214—Indoor unit or outdoor unit with auxiliary heat exchanger not forming part of the indoor or outdoor unit the auxiliary heat exchanger being used parallel to the indoor unit during heating operation
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2313/00—Compression machines, plants or systems with reversible cycle not otherwise provided for
- F25B2313/031—Sensor arrangements
- F25B2313/0314—Temperature sensors near the indoor heat exchanger
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2313/00—Compression machines, plants or systems with reversible cycle not otherwise provided for
- F25B2313/031—Sensor arrangements
- F25B2313/0315—Temperature sensors near the outdoor heat exchanger
-
- 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
- F25B2339/00—Details of evaporators; Details of condensers
- F25B2339/04—Details of condensers
- F25B2339/047—Water-cooled condensers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2700/00—Sensing or detecting of parameters; Sensors therefor
- F25B2700/19—Pressures
- F25B2700/193—Pressures of the compressor
- F25B2700/1931—Discharge pressures
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2700/00—Sensing or detecting of parameters; Sensors therefor
- F25B2700/21—Temperatures
- F25B2700/2115—Temperatures of a compressor or the drive means therefor
- F25B2700/21152—Temperatures of a compressor or the drive means therefor at the discharge side of the compressor
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/13—Hot air central heating systems using heat pumps
Definitions
- the present invention relates to a heat pump system capable of simultaneously performing a heating operation and a hot water supply operation, and more particularly to a heat pump system that simultaneously controls the heating capability of an indoor unit and the hot water supply capability of a hot water supply unit.
- JP 2010-196955 A pages 14-17, FIG. 5 etc.
- Japanese Patent Laying-Open No. 2006-105434 pages 10-11, FIG. 1, etc.
- the temperature difference Tx is calculated by subtracting the indoor air temperature Tr from the indoor target set temperature To. If the temperature difference Tx is equal to or greater than the predetermined value Ta, it is determined that the heating capacity is necessary, and the heating capacity is reduced by decreasing the opening degree of the hot water supply side pressure reducing mechanism (first use side flow rate adjustment valve 42a). Secure. On the other hand, when the temperature difference Tx is less than the predetermined value Ta, it is determined that the heating capacity is unnecessary, and the opening degree of the heating side pressure reducing mechanism (second use side flow rate adjustment valve 102a) is reduced to ensure the hot water supply capacity.
- the heating-side pressure reducing mechanism (heating-side flow rate adjustment valve 26) is set to a valve opening that is one step smaller than the initial valve opening. Control.
- the hot water supply-side pressure reducing mechanism (hot water storage-side flow rate adjustment valve 27) is controlled to a valve opening that is one step larger than the beginning of simultaneous operation.
- the valve opening degree of the decompression mechanism of a heating side and a hot water supply side is each adjusted according to the fluctuation
- the SC (subcool) on the heating side becomes excessively large, resulting in insufficient refrigerant. This caused a decrease in the low pressure and an increase in the discharge temperature, which also had to reduce the operating frequency of the compressor, resulting in a decrease in the capacity of the heat source unit and a decrease in the operating efficiency.
- boiling water is heated at the same time as controlling the room temperature, so we want to increase the heat source capacity as much as possible by increasing the heat source capacity, which is the output power of the heat source unit, in order to avoid running out of hot water.
- This is very important from the standpoint of hot water supply capability even when the heating load is large.
- it is very important that the operation state can be appropriately controlled even if the heating and hot water supply are simultaneously operated.
- the water temperature is often higher than the room temperature (for example, the room temperature is 20 ° C. and the water temperature is 55 ° C.).
- the conventional technology cannot maximize the heat source capacity, and it takes time to complete the hot water supply, or it becomes unwarmed and the indoor comfort is impaired.
- the present invention has been made to solve the above-described problems, and an object of the present invention is to provide a heat pump system that realizes maximization of heat source capacity and operation efficiency even in any load balance between heating capacity and hot water supply capacity. It is what.
- a heat pump system includes a compressor, an indoor heat exchanger, a hot water supply side heat exchanger, an indoor pressure reducing mechanism, a hot water supply pressure reducing mechanism, and a heat source side heat exchanger, A flow path in which the indoor heat exchanger and the indoor pressure reducing mechanism are connected in series and a flow path in which the hot water supply heat exchanger and the hot water pressure reducing mechanism are connected in series are connected in parallel.
- a refrigerant circuit together with the compressor and the heat source side heat exchanger, a heating load for heating air with the indoor side heat exchanger, and a hot water supply load for heating water with the hot water supply side heat exchanger Are requested at the same time, the heating priority mode in which the opening degree of the indoor side pressure reducing mechanism is larger than the opening degree of the hot water supply side pressure reducing mechanism, and the hot water supply in which the opening degree of the hot water supply side pressure reducing mechanism is larger than the opening degree of the indoor side pressure reducing mechanism
- the indoor Subcooling heat exchanger is adjusted, and in the hot water supply priority mode, in which either the discharge temperature of the supercooling degree or the compressor of the hot water supply-side heat exchanger is adjusted.
- the heat pump system has a heating priority mode or a hot water supply priority mode, controls the degree of supercooling of the indoor heat exchanger in the heating priority mode, and in the hot water priority mode. Since the degree of supercooling of the heat exchanger or the discharge temperature of the compressor is controlled, it is possible to achieve the maximum capacity and operating efficiency of the heat source unit with respect to any load balance between the heating capacity and the hot water supply capacity.
- FIG. 1 is a schematic diagram showing a refrigerant circuit configuration of a heat pump system 100 (hereinafter simply referred to as system 100) according to Embodiment 1 of the present invention.
- FIG. 2 is a block diagram showing an electrical configuration of the control device 101 of the system 100. Based on FIG.1 and FIG.2, the structure of the system 100 is demonstrated.
- the system 100 can simultaneously process a heating command (heating ON / OFF) by the indoor unit 302 and a hot water supply command (hot water ON / OFF) by the hot water supply unit 303 by performing a vapor compression refrigeration cycle operation. Is. That is, the system 100 can simultaneously control the heating capacity of the indoor unit 302 and the hot water supply capacity of the hot water supply unit 303.
- the system 100 includes a heat source unit 301, an indoor unit 302, and a hot water supply unit 303.
- the heat source unit 301 and the indoor unit 302 are connected by an indoor gas extension pipe 4 that is a refrigerant pipe and an indoor liquid extension pipe 7 that is a refrigerant pipe.
- the heat source unit 301 and the hot water supply unit 303 are connected by a water side gas extension pipe 9 that is a refrigerant pipe and a water side liquid extension pipe 11 that is a refrigerant pipe.
- coolant used for the system 100 is not specifically limited.
- HFC (hydrofluorocarbon) refrigerants such as R410A, R407C, R404A, and R32
- HCFC (hydrochlorofluorocarbon) refrigerants such as R22 and R134a
- natural refrigerants such as hydrocarbon, helium, carbon dioxide, etc. It can be used as a refrigerant.
- the heat source unit 301 includes the compressor 1, the discharge electromagnetic valves 2a and 2b, the four-way valve 3, the indoor side pressure reducing mechanism 8, the hot water supply side pressure reducing mechanism 12, the heat source side heat exchanger 13, and the heat source side blower 14. And accumulator 15.
- the compressor 1, the discharge solenoid valves 2a and 2b, the four-way valve 3, the indoor side pressure reducing mechanism 8, the hot water supply side pressure reducing mechanism 12, the heat source side heat exchanger 13, and the accumulator 15 are connected by pipes so that a part of the refrigerant circuit is connected. It is composed.
- the four-way valve 3, the heat source side blower 14, and the accumulator 15 are not essential.
- the compressor 1 is a type in which the number of revolutions is controlled by an inverter and capacity control is possible, and the refrigerant 1 is sucked and compressed to be in a high temperature and high pressure state.
- the discharge side pipe connected to the compressor 1 is branched in the middle, and one side is connected to the indoor side gas extension pipe 4 via the discharge electromagnetic valve 2a, and the other side is extended to the water side gas via the discharge electromagnetic valve 2b.
- Each is connected to a pipe 9.
- the discharge solenoid valves 2a and 2b control the flow of the refrigerant by opening and closing the refrigerant flow path.
- the discharge solenoid valve 2 a is installed on a pipe that is branched on the discharge side of the compressor 1 and connected to the indoor side gas extension pipe 4.
- the discharge electromagnetic valve 2 b is branched on the discharge side of the compressor 1 and installed in a pipe connected to the water side gas extension pipe 9.
- the four-way valve 3 controls the flow direction of the refrigerant.
- the four-way valve 3 is installed on the downstream side of the discharge electromagnetic valve 2a.
- the four-way valve 3 does not need to be installed.
- the heat source side heat exchanger 13 is, for example, a cross fin type fin-and-tube heat exchanger configured by heat transfer tubes and a large number of fins, and performs heat exchange between a heat medium such as outside air and a refrigerant. It is.
- the heat source side heat exchanger 13 functions as an evaporator during heating operation and as a condenser during cooling operation.
- the heat source side blower 14 is constituted by a centrifugal fan, a multiblade fan, or the like driven by a DC motor (not shown), and can adjust the amount of blown air.
- the heat source side blower 14 draws outdoor air into the heat source unit 301 and causes the heat source side heat exchanger 13 to exchange heat with the refrigerant, and then discharges the air to the outside.
- the heat source side blower 14 is preferably installed in the vicinity of the heat source side heat exchanger 13. If the heat source side heat exchanger 13 is not an air-refrigerant heat exchanger, the heat source side blower 14 need not be installed.
- the indoor side decompression mechanism 8 adjusts the refrigerant flow rate by decompressing and expanding the refrigerant.
- the indoor pressure reducing mechanism 8 may be constituted by a flow rate control means that can be variably controlled in opening degree, for example, a precise flow rate control means using an electronic expansion valve.
- the indoor-side decompression mechanism 8 is installed in the indoor-side liquid extension pipe 7 that connects the heat source-side heat exchanger 13 and the indoor-side heat exchanger 5.
- the hot water supply side decompression mechanism 12 decompresses and expands the refrigerant to adjust the refrigerant flow rate.
- the hot water supply side pressure reducing mechanism 12 may be constituted by a flow rate control means that can control the opening degree variably, for example, an electronic expansion valve.
- the hot water supply side pressure reducing mechanism 12 is installed in the water side liquid extension pipe 11 connecting the heat source side heat exchanger 13 and the water side heat exchanger 10.
- the accumulator 15 is provided on the suction side of the compressor 1, and stores liquid refrigerant to the compressor 1 when an abnormality occurs in the system 100 or during a transient response of an operation state associated with a change in operation control. Has a function to prevent liquid back.
- the accumulator 15 is not essential.
- the heat source unit 301 is provided with a pressure sensor 201, a temperature sensor 202, a temperature sensor 206, and a temperature sensor 207.
- the pressure sensor 201 is provided on the discharge side of the compressor 1 and measures the refrigerant pressure at the installation location.
- the temperature sensor 202 is provided on the discharge side of the compressor 1 and measures the refrigerant temperature at the installation location.
- the temperature sensor 206 is provided on the liquid side of the heat source side heat exchanger 13 and measures the refrigerant temperature at the installation location.
- the temperature sensor 207 is provided at the air suction port and measures the temperature of the outside air taken into the heat source side blower 14.
- the heat source unit 301 is provided with a control device 101, and information measured by each sensor provided in the heat source unit 301 is sent to the control device 101.
- the control device 101 will be described in detail later.
- the indoor unit 302 includes the indoor side heat exchanger 5 and the indoor side blower 6.
- the indoor heat exchanger 5 is a cross-fin type fin-and-tube heat exchanger configured by, for example, heat transfer tubes and a large number of fins, and performs heat exchange between indoor air and refrigerant.
- the indoor heat exchanger 5 functions as a condenser during heating operation and as an evaporator during cooling operation.
- the indoor blower 6 includes a centrifugal fan, a multiblade fan, and the like driven by a DC motor (not shown), and can adjust the amount of air blown.
- the indoor blower 6 sucks indoor air into the indoor unit 302 and exchanges heat with the refrigerant in the indoor heat exchanger 5, and then blows the air (conditioned air) into the room. .
- the indoor unit 302 is provided with a temperature sensor 203 and a temperature sensor 204.
- the temperature sensor 203 is provided on the liquid side of the indoor heat exchanger 5 and measures the refrigerant temperature at the installation location.
- the temperature sensor 204 is provided on the indoor air inlet side, and measures the temperature of the indoor air flowing into the indoor unit 302. Information measured by each sensor provided in the indoor unit 302 is sent to the control device 101.
- the hot water supply unit 303 includes a water side heat exchanger 10, a water pump 16, a coil heat exchanger 17, and a hot water storage tank 18. And the water pump 16, the water side heat exchanger 10, and the coil heat exchanger 17 are connected by piping, and the water circuit is comprised. In addition, by installing the coil heat exchanger 17 in the hot water storage tank 18, the water stored in the hot water storage tank 18 is boiled. Furthermore, in the water circuit, water that is a heat exchange medium circulates as intermediate water.
- the water-side heat exchanger 10 is configured by, for example, a plate-type water heat exchanger, and heats the intermediate water by exchanging heat between the intermediate water and the refrigerant.
- the water side heat exchanger 10 functions as a condenser during a hot water supply operation.
- the water pump 16 is configured, for example, with a constant rotation speed or variable with an inverter, and circulates intermediate water in the water side circuit.
- the coil heat exchanger 17 is installed in the hot water storage tank 18 and heat-exchanges between the hot water stored in the hot water storage tank 18 and the intermediate water circulating in the water circuit to generate hot water by heating the hot water. It is.
- the hot water storage tank 18 stores the heated hot water.
- the hot water storage tank 18 is of a full-water type, and hot water is discharged from the upper part of the tank in response to a hot water request, and city water that is as low as the amount of water discharged is supplied from the lower part of the tank (not shown).
- the operation state of the water side circuit will be described.
- the intermediate water fed by the water pump 16 in the hot water supply unit 303 is heated by the refrigerant in the water side heat exchanger 10 and becomes high temperature. Thereafter, the heated high-temperature water flows into the coil heat exchanger 17 in the hot water storage tank 18 and heats the hot water to lower the temperature. Thereafter, it flows out of the coil heat exchanger 17 of the hot water storage tank 18, flows into the water pump 16, is retransmitted, and becomes hot water in the water-side heat exchanger 10. In such a process, the hot water in the hot water storage tank 18 is boiled.
- the method of heating the water in the hot water storage tank 18 by the hot water supply unit 303 is not limited to the heat exchange method using the intermediate water as in the first embodiment. Alternatively, a heating method may be used in which heat is exchanged at 10 to obtain hot water and then returned to the hot water storage tank 18 again.
- the hot water supply unit 303 is provided with a temperature sensor 205 and a temperature sensor 208.
- the temperature sensor 205 is provided on the liquid side of the water-side heat exchanger 10 and measures the refrigerant temperature at the installation location.
- the temperature sensor 208 is installed on the side surface of the hot water storage tank 18 and measures the water temperature in the hot water storage tank 18 at the installation position height. Information measured by each sensor provided in the hot water supply unit 303 is sent to the control device 101.
- FIG. 2 shows a control device 101 for controlling the system 100, a remote controller 102 connected to the control device 101, sensors and actuators (compressor 1, four-way valve 3, discharge electromagnetic valves 2a and 2b, indoor side pressure reducing mechanism 8). , The hot water supply side pressure reducing mechanism 12, the heat source side blower 14, the indoor side blower 6, the water pump 16, and the like).
- the control device 101 includes a measurement unit 103, a control unit 104, a communication unit 105, and a storage unit 106.
- the control unit 104 includes the compressor 1, the discharge electromagnetic valves 2 a and 2 b, the four-way valve 3, the heat source side blower 14, the indoor side decompression mechanism 8, the hot water supply side decompression mechanism 12, and the indoor side
- the blower 6 and the water pump 16 are controlled.
- the communication unit 105 receives communication data information from a communication means such as a telephone line, a LAN line, and a radio, and inputs / outputs information to / from the remote controller 102.
- the storage unit 106 stores predetermined constants and setting values transmitted from the remote controller 102. The contents stored in the storage unit 106 can be referred to and rewritten as necessary.
- the measurement unit 103, the control unit 104, and the communication unit 105 are configured by a microcomputer, and the storage unit 106 is configured by a semiconductor memory or the like.
- the control device 101 is disposed in the heat source unit 301, but FIG. 1 merely shows an example of the installation location.
- the location where the control device 101 is arranged is not particularly limited.
- the control device 101 may be installed in the indoor unit 302 and the hot water supply unit 303, or may be installed in a place different from each unit.
- the system 100 includes a remote controller 102 that is a user interface device for inputting and outputting information between the system 100 and a user.
- the remote control 102 includes an input unit 107 and a display unit 108.
- the input unit 107 receives instructions from the user. For example, the input unit 107 receives selection of cooling ON / OFF, heating ON / OFF, and hot water supply ON / OFF, or receives input of indoor set temperature and boiling temperature. Can do. Further, when the temperature detected by the temperature sensor 208 installed on the wall side surface of the hot water storage tank 18 becomes a predetermined value or lower (for example, 45 ° C. or lower), the hot water supply ON and the input unit 107 are automatically input. It has become.
- the display unit 108 displays the current operation mode of the system 100 and the priority operation mode in the simultaneous heating and hot water supply operation.
- the system 100 can simultaneously process heating ON and hot water supply ON input via the remote controller 102, and can perform simultaneous heating and hot water supply operation. Below, the refrigerant
- the four-way valve 3 connects the discharge side of the compressor 1 to the gas side of the indoor heat exchanger 5 and connects the suction side to the gas side of the heat source side heat exchanger 13. Further, the discharge electromagnetic valve 2a is open and the discharge electromagnetic valve 2b is open.
- the high-temperature and high-pressure gas refrigerant discharged from the compressor 1 is distributed to the refrigerant flowing through the discharge electromagnetic valve 2a or the discharge electromagnetic valve 2b.
- the refrigerant flowing through the discharge electromagnetic valve 2 a flows through the indoor gas extension pipe 4 via the four-way valve 3 and flows into the indoor heat exchanger 5.
- the refrigerant that has flowed into the indoor heat exchanger 5 heats the indoor air supplied by the indoor fan 6 and flows out of the indoor heat exchanger 5. Thereafter, the pressure is reduced by the indoor pressure reducing mechanism 8 via the indoor liquid extension pipe 7 and merges with the refrigerant flowing through the discharge electromagnetic valve 2b.
- the refrigerant flowing through the discharge electromagnetic valve 2b flows into the water side heat exchanger 10 via the water side gas extension pipe 9.
- the refrigerant that has flowed into the water-side heat exchanger 10 heats the intermediate water supplied by the water pump 16.
- This refrigerant flows out of the water-side heat exchanger 10 is decompressed by the hot water supply-side decompression mechanism 12 via the water-side liquid extension pipe 11, and merges with the refrigerant that has flowed through the discharge electromagnetic valve 2a.
- the refrigerant flowing into the heat source side heat exchanger 13 exchanges heat with the outdoor air supplied by the heat source side blower 14, and becomes a low-pressure gas refrigerant.
- the operation frequency of the compressor 1 when the hot water supply is ON, the operation frequency of the compressor 1 is fixed at the maximum with priority on prevention of hot water shortage. Further, in the system 100, since a large amount of refrigerant flows into the heat source side heat exchanger 13 when the operating frequency of the compressor 1 is maximized, the rotational speed of the heat source side blower 14 is also fixed at the maximum rotational speed. Furthermore, in the system 100, the rotation speed of the indoor fan 6 is fixed to a command value input to the user's remote controller 102. Furthermore, in the system 100, the rotational speed of the water pump 16 is fixed to a predetermined rotational speed.
- the room temperature is a temperature detected by the temperature sensor 204.
- the heating / hot water supply opening ratio which is the opening ratio between the opening of the indoor-side decompression mechanism 8 and the opening of the hot-water supply-side decompression mechanism 12, is 5: 5, and the total decompression mechanism opening is 480p (480 pulses). An example is shown.
- the heating load can be predicted and reflected in the control by using the information on the indoor differential temperature and the indoor temperature change.
- the heat source capacity is not excessively biased toward the heating side or the hot water supply side, and appropriate distribution of the heating capacity and the hot water supply capacity according to the heating load can be realized.
- the distribution of heating capacity and hot water supply capacity can be controlled by the heating hot water supply opening ratio, but this alone does not control the refrigerant state. Therefore, there is a possibility that a high pressure rise or a low pressure drop may be caused, and the operation efficiency may be lowered. Therefore, in the system 100, the operation efficiency is maximized by controlling the total decompression mechanism opening, which is the sum of the opening of the indoor decompression mechanism 8 and the hot water supply decompression mechanism 12, according to the operating state of the refrigerant. I have to.
- the target operating state realized by controlling the total pressure reducing mechanism opening differs depending on which one of hot water supply capacity and heating capacity is desired to be increased. In addition, it depends on the driving conditions. The optimal control target and target state are selected and controlled from these two factors.
- the priority mode is determined and selected as to which of the hot water supply capacity and the heating capacity is to be increased.
- FIG. 3 is a flowchart showing a processing flow of the priority mode determination method during simultaneous heating and hot water supply operation of the system 100. Based on FIG. 3, the determination method of the priority mode at the time of the simultaneous heating / hot-water supply operation of the system 100 will be described. Note that the control subject in the flowchart shown in FIG.
- step S1 it is determined whether or not the operation mode is the heating and hot water supply simultaneous operation mode. If it is determined that the operation mode is the heating / hot water simultaneous operation mode, the opening Sji of the indoor decompression mechanism 8 and the opening Sjw of the hot water supply decompression mechanism are acquired in step S2. In step S3, it is determined whether or not the opening Sji of the indoor decompression mechanism 8 is equal to or greater than the opening Sjw of the hot water supply decompression mechanism. If it is determined that Sji is greater than or equal to Sjw, it is determined that the heating load is large and the heating capacity is desired to be greater than or equal to the hot water supply capacity, and the priority mode is determined to be the heating priority mode in step S4.
- the priority mode is determined to be the hot water supply priority mode in step S5.
- the priority mode is determined as described above. Therefore, the target operating state can be determined.
- FIG. 4 is a flowchart showing a process flow of the control method of the total decompression mechanism opening degree of the system 100.
- FIG. 5 is a schematic diagram illustrating an operation state of the system 100 in the heating priority mode.
- FIG. 6 is a schematic diagram illustrating an operation state at a low water temperature in the hot water supply priority mode of the system 100.
- FIG. 7 is a schematic diagram showing an operation state at the time of high water temperature in the hot water supply priority mode of the system 100.
- a method for controlling the total pressure reducing mechanism opening will be described with reference to FIGS. Note that the control subject in the flowchart shown in FIG. 5 to 7, the horizontal axis indicates the specific enthalpy [kJ / kg], and the vertical axis indicates the pressure [MPaG].
- step S11 it is determined whether or not the priority mode is the heating priority mode. If it is determined that the heating priority mode is set, it is determined in step S12 whether the indoor supercooling degree is equal to or greater than a predetermined value. When it is determined that the indoor supercooling degree is equal to or greater than the predetermined value, the total pressure reducing mechanism opening is increased in step S13. On the other hand, when it is determined that the indoor supercooling degree is less than the predetermined value, the total pressure reducing mechanism opening is decreased in step S14.
- the indoor supercooling degree is obtained by subtracting the detected temperature of the temperature sensor 203 from the saturation temperature of the detected pressure of the pressure sensor 201.
- the indoor side subcooling degree is set to a predetermined value (for example, 10) so that the performance of the indoor heat exchanger 5 is maximized. (Circle degree).
- step S11 when it is determined in step S11 that the priority mode is the hot water supply priority mode, it is determined in step S15 whether the hot water supply side subcooling degree is equal to or greater than a predetermined value.
- the total pressure reducing mechanism opening is increased in step S16 to reduce the hot water supply side subcooling degree.
- the hot water supply side subcooling degree is obtained by subtracting the detected temperature of the temperature sensor 205 from the saturation temperature of the detected pressure of the pressure sensor 201.
- the hot water supply side subcooling degree is set to a predetermined value (for example, 5) so that the performance of the water side heat exchanger 10 is maximized. (Circle degree).
- step S15 when it is determined in step S15 that the hot water supply side subcooling degree is less than the predetermined value, it is determined in step S17 whether or not the discharge temperature is equal to or higher than a reference value (reference discharge temperature).
- the discharge temperature is a temperature detected by the temperature sensor 202.
- the high pressure increases (the refrigerant temperature on the high pressure side increases), and the opening degree of the indoor pressure reducing mechanism 8 is smaller than the opening degree of the hot water supply pressure reducing mechanism 12, so The degree increases. Therefore, the surplus liquid refrigerant disappears from the accumulator 15, and the suction superheat degree of the compressor 1 increases. And the refrigerant
- the following operation is performed in order to determine whether or not there is a surplus liquid refrigerant. That is, the discharge temperature when the suction superheat degree of the compressor 1 is 5 ° C. is set as the reference discharge temperature, and it is determined whether or not the surplus liquid refrigerant exists in the accumulator 15 depending on whether the discharge temperature is equal to or higher than the reference discharge temperature.
- the reference discharge temperature TdB may be obtained from the data table.
- the high pressure Pc is a pressure detected by the pressure sensor 201
- the low pressure Pe is a pressure converted from the temperature detected by the temperature sensor 206.
- a data table is created at a reference discharge temperature of, for example, about 3 ° C. to 10 ° C. assuming that the degree of suction superheat is small. Moreover, since the change of the discharge temperature with respect to the operating frequency F of the compressor 1 is not so large, the data table may be created only with the representative operating frequency.
- the discharge temperature is equal to or higher than the reference discharge temperature, it is determined that the temperature is high (for example, the outlet water temperature is about 55 ° C.) and it is difficult to adjust the hot water supply side subcooling degree to a predetermined value.
- the mechanism opening is increased so that the discharge temperature does not exceed a predetermined value. By doing in this way, the increase in discharge temperature and the suction superheat degree of the compressor 1 can be suppressed. Therefore, the maximum amount of refrigerant discharged from the compressor 1 can be secured according to the amount of refrigerant sealed in the refrigerant circuit of the system 100, and the hot water supply capacity can be increased. Therefore, the boiling speed can be increased in a high water temperature and low heating load situation.
- the total pressure reducing mechanism opening is decreased in step S19.
- the opening degree of the indoor side decompression mechanism 8 is larger than the opening degree of the hot water supply side decompression mechanism 12, and therefore the indoor side subcooling degree is often smaller than the hot water supply side subcooling degree.
- the hot water supply priority mode since the opening degree of the hot water supply side pressure reducing mechanism 12 is larger than the opening degree of the indoor side pressure reducing mechanism 8, the hot water supply side subcooling degree is often smaller than the indoor side subcooling degree.
- the case where the degree of supercooling is controlled is a situation in which the smaller degree of subcooling is controlled between the indoor side supercooling degree and the hot water supply side subcooling degree.
- the opening When changing the total decompression mechanism opening, the opening is distributed so that the sum of the opening of the indoor decompression mechanism 8 and the opening of the hot water supply decompression mechanism 12 becomes the changed total decompression mechanism opening.
- the opening distribution method is implemented by heating / hot water opening ratio control.
- the opening before change of the total decompression mechanism opening is 480 p
- the opening after change is 500 p
- the opening degree of the indoor decompression mechanism 8 before the change is 336p (480 ⁇ 7/10)
- the opening degree of the hot water supply side decompression mechanism 12 before the change is 144p (480 ⁇ 3/10).
- the heating / hot water supply opening ratio is 7: 3, and the fully opened openings of the indoor-side decompression mechanism 8 and the hot-water supply decompression mechanism 12 are both 480p.
- the opening of the indoor decompression mechanism 8 is 480p
- the opening of the hot water supply decompression mechanism 12 is 206p
- the room assumee that the inner supercooling degree is equal to or greater than a predetermined value.
- the opening of the indoor decompression mechanism 8 cannot be increased even if it is desired to increase the total decompression mechanism opening. Therefore, the total pressure reducing mechanism opening cannot be distributed according to the heating hot water supply opening ratio.
- the controller 104 forcibly changes the heating / hot water supply opening ratio so that the total decompression mechanism opening can be realized.
- the heating hot water supply opening ratio which was 7: 3, is set to 6.9: 3.1
- the opening degree of the indoor pressure reducing mechanism 8 is set to 480 p
- the opening degree of the hot water supply side pressure reducing mechanism 12 is set to 220 p.
- the heating hot water supply opening degree ratio is changed by the same processing.
- the heating hot water supply opening ratio controls the ratio of the refrigerant flow rate flowing through the indoor heat exchanger 5 and the water heat exchanger 10, but the change in the refrigerant flow rate depends on the refrigerant operation state (degree of subcooling and discharge temperature). Faster than change. In the refrigerant operation state, the response is delayed because it takes time until the refrigerant distribution in the indoor heat exchanger 5 and the water heat exchanger 10 completely changes. Therefore, the control unit 104 may control the change interval of the total decompression mechanism opening so as to be longer than the change interval of the heating hot water supply opening ratio. By doing in this way, since a refrigerant
- the heating thermo is turned off, and the indoor side pressure reducing mechanism 8 is closed to prevent the room temperature from rising.
- the dropping operation is performed. If this operation is frequently performed, the operation state becomes unstable, resulting in a decrease in operation efficiency. Therefore, in the case of simultaneous heating / hot water supply operation in the control unit 104, the temperature difference between the room temperature and the room set temperature until the heating thermo is turned off is increased (for example, 2 ° C.). By doing in this way, since the frequency
- the completion time of boiling water is shorter than the temperature control in the heating room.
- the number of people taking a shower at night increases unexpectedly.
- the hot water supply capacity can be increased. It becomes possible to maintain the simultaneous operation of heating and hot water supply. Therefore, the time until the hot water supply is completed can be shortened.
- the heat source capacity and the operating efficiency can be maximized at a predetermined heating load under any room temperature and water temperature conditions. Avoiding non-warming and early completion of hot water supply operation. In particular, when the hot water supply capacity is increased under high water temperature conditions, the degree of indoor supercooling increases, and there is a case where excess liquid refrigerant disappears from the accumulator 15, but even in that case, an excessive discharge temperature can be avoided.
- the heat source capacity can be maximized according to the amount of refrigerant sealed in the.
- the heat source capacity is maximized by controlling the total decompression mechanism opening according to the size of the heating load and the operating state. And a predetermined heating capacity and hot water supply capacity can be acquired.
- an extreme change in high pressure or low pressure can be suppressed by appropriately selecting a target in any one of the above states according to the discharge temperature and realizing a target operation state, and with a predetermined hot water supply capacity.
- the hot water supply and heating simultaneous operation capable of ensuring the heating capacity can be performed.
- the case where the indoor unit 302 and the hot water supply unit 303 have the same capacity has been described as an example, but the present technology can be similarly applied to different cases.
- capacitance of the hot water supply side pressure reduction mechanism 12 were made the same, this technique is applicable even when this differs. Even if it is such an apparatus structure, since it can be controlled to predetermined hot-water supply capability and heating capability by heating hot-water supply opening ratio control, there is no problem.
- the heating side opening determined by the ratio of the total decompression mechanism opening and the heating hot water supply opening degree. May be divided for each capacity.
- the indoor unit 302 is a system having one 2HP and two 1HPs, and the heating / hot water supply opening ratio is 7: 3 with a total pressure reducing mechanism opening 480p.
- FIG. FIG. 8 is a schematic diagram showing a refrigerant circuit configuration of a heat pump system 200 (hereinafter simply referred to as system 200) according to Embodiment 2 of the present invention.
- system 200 a heat pump system 200
- the configuration and operation of the system 200 will be described with reference to FIG.
- the difference from the first embodiment described above will be mainly described, and parts having the same functions as those in the first embodiment will be denoted by the same reference numerals and description thereof will be omitted.
- the system 200 performs a vapor compression refrigeration cycle operation, thereby performing a heating command (heating ON / OFF) by the indoor unit 302 and a hot water supply command (hot water supply) by the hot water supply unit 303.
- a heating command heating ON / OFF
- a hot water supply command hot water supply
- ON / OFF can be processed simultaneously. That is, the system 200 can simultaneously control the heating capacity of the indoor unit 302 and the hot water supply capacity of the hot water supply unit 303.
- the circuit configuration and basic operation of the system 200 are the same as those of the system 100 according to the first embodiment, except that five temperature sensors (from the bottom 209a to 209e) are installed in the tank height direction of the hot water storage tank 18.
- the system 100 differs from the system 100 in that a temperature sensor 210 is installed at the outlet of the water-side heat exchanger 10 in the side circuit.
- the system 200 is configured so that the hot water supply ON time can be measured by the measuring unit 103.
- the system 200 is configured to be able to acquire the hot water supply load status in more detail than in the first embodiment, such as acquisition of water temperature and measurement of hot water supply time.
- the amount of heat stored in the tank can be calculated.
- the hot water storage tank 18 is divided in the height direction for each installation position of the temperature sensors 209a to 209e, and based on the measurement data of the upper and lower temperature sensors 209 in each divided section measured by the measuring unit 103, for each divided section. Calculate the average temperature. In the lowermost section, the temperature sensor 209a is the average temperature, and in the uppermost section, the temperature of the temperature sensor 209e is the average temperature.
- the divided section volume and the specific heat of water are multiplied by the value obtained by subtracting the city water temperature from the average temperature, and the amount of stored hot water in each divided section is estimated.
- the estimated amount of hot water stored in each divided section is integrated, and the integrated amount of heat is used as the amount of stored hot water in the hot water storage tank 18.
- the divided section volume is obtained by dividing the internal volume of the hot water storage tank 18 by the number of installed temperature sensors 211 + 1.
- the city water is fixed at 15 ° C., for example.
- the tank heat storage amount is lower than the target tank heat storage amount by a predetermined percentage (for example, 20% or less), the time until boiling is completed becomes longer, so the operation mode is forcibly set to the hot water supply priority mode. Specifically, the opening degree of the indoor side pressure reducing mechanism 8 is prohibited from being equal to or larger than the opening degree of the hot water supply side pressure reducing mechanism 12.
- the operation mode is forcibly set to the hot water supply priority mode. By doing in this way, it can avoid that the time until completion of hot water supply becomes extremely long, and the possibility of hot water running out decreases.
- the hot water supply priority mode an operation in which the hot water supply capacity becomes larger than the heating capacity by increasing the opening degree of the hot water supply side pressure reducing mechanism 12 to be larger than the opening degree of the indoor side pressure reducing mechanism 8 is aimed.
- the opening degree of the hot water supply side pressure reducing mechanism 12 is larger than the opening degree of the indoor side pressure reducing mechanism 8
- the condensation latent heat of the refrigerant is not used for heating the water unless the condensation temperature is equal to or higher than the water temperature. .
- the hot water supply capacity is small. Therefore, the condensation temperature is set to be equal to or higher than the temperature of the water flowing through the water-side heat exchanger 10.
- the temperature sensor is installed on the outlet side of the water-side heat exchanger 10.
- the temperature sensor is not limited to this, and may be installed on the inlet side of the water-side heat exchanger 10. Good.
- the system 200 is configured to monitor the hot water supply load status (temperature sensor 209, hot water supply time) and the operating water temperature information (temperature sensor 210), so that the hot water supply is completed in addition to the effects of the first embodiment. It is possible to avoid an extremely long time until the hot water runs out and to reduce the possibility of running out of hot water.
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Abstract
Description
このように、特許文献1のヒートポンプシステムでは、温度差Txに基づいて、給湯能力と暖房能力の配分を制御するため、給湯ユニットと室内ユニットの運転能力の総和が熱源ユニットの暖房定格容量を超過してしまう可能性を抑制できる。
このように、特許文献2のヒートポンプシステムでは、暖房側の負荷の変動に応じて、暖房側と給湯側の減圧機構の弁開度をそれぞれ調整する。こうすることによって、圧縮機の能力を能力余裕側から能力不足側へ移行させる配分調整が可能となり、暖房と給湯のそれぞれの状況に対応した能力配分を実行している。
図1は、本発明の実施の形態1に係るヒートポンプシステム100(以下、単にシステム100と称する)の冷媒回路構成を示す概略図である。図2は、システム100の制御装置101の電気的な構成を示すブロック図である。図1及び図2に基づいて、システム100の構成について説明する。
システム100は、熱源ユニット301と、室内ユニット302と、給湯ユニット303と、を有している。熱源ユニット301と室内ユニット302とは、冷媒配管である室内側ガス延長配管4と冷媒配管である室内側液延長配管7とで接続されている。熱源ユニット301と給湯ユニット303とは、冷媒配管である水側ガス延長配管9と冷媒配管である水側液延長配管11とで接続されている。
熱源ユニット301は、圧縮機1と、吐出電磁弁2a,2bと、四方弁3と、室内側減圧機構8と、給湯側減圧機構12と、熱源側熱交換器13と、熱源側送風機14と、アキュムレータ15と、を有している。そして、圧縮機1、吐出電磁弁2a,2b、四方弁3、室内側減圧機構8、給湯側減圧機構12、熱源側熱交換器13、アキュムレータ15が、配管接続されて冷媒回路の一部を構成している。ただし、四方弁3、熱源側送風機14、アキュムレータ15は、必須なものではない。
吐出電磁弁2a、2bは、冷媒流路を開閉することで冷媒の流れを制御するものである。吐出電磁弁2aは、圧縮機1の吐出側で分岐され、室内側ガス延長配管4に接続する配管に設置されている。吐出電磁弁2bは、圧縮機1の吐出側で分岐され、水側ガス延長配管9に接続する配管に設置されている。
熱源側熱交換器13は、たとえば伝熱管と多数のフィンとにより構成されたクロスフィン式のフィン・アンド・チューブ型熱交換器であり、外気等の熱媒体と冷媒との熱交換を行うものである。熱源側熱交換器13は、暖房運転時には蒸発器、冷房運転時には凝縮器として機能する。
給湯側減圧機構12は、冷媒を減圧して膨張させ、冷媒流量を調整するものである。この給湯側減圧機構12は、開度が可変に制御可能なもの、たとえば電子式膨張弁による緻密な流量制御手段で構成するとよい。給湯側減圧機構12は、熱源側熱交換器13と水側熱交換器10とを接続している水側液延長配管11に設置されている。
圧力センサ201は、圧縮機1の吐出側に設けられ、設置場所の冷媒圧力を計測するものである。
温度センサ202は、圧縮機1の吐出側に設けられ、設置場所の冷媒温度を計測するものである。
温度センサ206は、熱源側熱交換器13の液側に設けられ、設置場所の冷媒温度を計測するものである。
温度センサ207は、空気吸込口に設けられており、熱源側送風機14に取り込まれる外気の温度を計測するものである。
室内ユニット302は、室内側熱交換器5と、室内側送風機6と、を有している。
室内側熱交換器5は、たとえば伝熱管と多数のフィンとにより構成されたクロスフィン式のフィン・アンド・チューブ型熱交換器であり、室内空気と冷媒との熱交換を行うものである。室内側熱交換器5は、暖房運転時には凝縮器、冷房運転時には蒸発器として機能する。
室内側送風機6は、DCモータ(図示せず)によって駆動される遠心ファンや多翼ファン等から構成されており、送風量を調整することが可能なものである。室内側送風機6は、室内ユニット302内に室内空気を吸入して、室内側熱交換器5にて冷媒と熱交換させた後に、その空気(調和空気)を室内に吹出すようになっている。
温度センサ203は、室内側熱交換器5の液側に設けられ、設置場所の冷媒温度を計測するものである。
温度センサ204は、室内空気の吸入口側に設けられ、室内ユニット302内に流入する室内空気の温度を計測するものである。
室内ユニット302に設けられている各センサで計測された情報は、制御装置101に送られるようになっている。
給湯ユニット303は、水側熱交換器10と、水ポンプ16と、コイル熱交換器17と、貯湯タンク18と、を有している。そして、水ポンプ16、水側熱交換器10、コイル熱交換器17が配管接続されて水回路を構成している。また、コイル熱交換器17を貯湯タンク18に設置することで、貯湯タンク18に貯湯される水を沸き上げるようになっている。さらに、水回路には、熱交換媒体である水が中間水として循環する。
水ポンプ16は、たとえば回転数が一定速、もしくはインバータで可変にできるもので構成され、水側回路に中間水を循環させるものである。
コイル熱交換器17は、貯湯タンク18内に設置されており、貯湯タンク18の貯湯水と水回路を循環する中間水との間で熱交換させ、貯湯水を加熱して湯を生成するものである。
貯湯タンク18は、沸きあげられた湯を貯留するものである。貯湯タンク18は、満水式であり、出湯要求に応じてタンク上部より湯が出水し、出水した量だけ低温の市水がタンク下部より給水されるようになっている(図示せず)。
給湯ユニット303にて水ポンプ16により送水された中間水は、水側熱交換器10で冷媒により加熱され高温となる。その後、加熱された高温水は、貯湯タンク18内のコイル熱交換器17に流入し、貯湯水を加熱して温度が低下する。その後、貯湯タンク18のコイル熱交換器17を流出し、水ポンプ16に流れ、再送水されて水側熱交換器10にて温水となる。このようなプロセスにて貯湯タンク18の湯が沸き上げられる。
温度センサ205は、水側熱交換器10の液側に設けられ設置場所の冷媒温度を計測するものである。
温度センサ208は、貯湯タンク18の側面に設置され、設置位置高さの貯湯タンク18内の水温を計測するものである。
給湯ユニット303に設けられている各センサで計測された情報は、制御装置101に送られるようになっている。
図2には、システム100の制御を行う制御装置101、制御装置101に接続されるリモコン102、各センサ及びアクチュエータ(圧縮機1、四方弁3、吐出電磁弁2a,2b、室内側減圧機構8、給湯側減圧機構12、熱源側送風機14、室内側送風機6、水ポンプ16等)の接続状態を示している。また、制御装置101は、測定部103、制御部104、通信部105、記憶部106を内蔵している。
制御部104は、測定部103に入力された情報に基づき、圧縮機1、吐出電磁弁2a、2b、四方弁3、熱源側送風機14、室内側減圧機構8、給湯側減圧機構12、室内側送風機6、水ポンプ16を制御するようになっている。
通信部105は、電話回線、LAN回線、無線などの通信手段からの通信データ情報が入力されたり、リモコン102と情報の入出力を行ったりするようになっている。
記憶部106は、予め定められた定数やリモコン102から送信される設定値を記憶するようになっている。記憶部106に記憶されている記憶内容は、必要に応じて参照、書き換えることが可能になっている。
システム100は、システム100とユーザーとの間で情報の入出力を行うためのユーザーインターフェース装置であるリモコン102を有している。リモコン102には、入力部107、表示部108が内蔵されている。
表示部108は、現在のシステム100の運転モードや、暖房給湯同時運転での優先運転モードを表示するものである。
<暖房給湯同時運転モード>
システム100は、リモコン102を介して入力された暖房ON及び給湯ONを同時に処理することが可能なものであり、暖房給湯同時運転を実施することができる。以下に暖房給湯同時運転モード時の冷媒流れ状態及び各機器の制御について説明する。
次に、室内側減圧機構8及び給湯側減圧機構12の制御について説明する。システム100では、室内側減圧機構8及び給湯側減圧機構12の個別開度を暖房負荷によって制御することで、暖房負荷に応じた暖房能力と給湯能力の能力配分を実現している。具体的には以下のようにして制御する。
この場合、室内温度が室内設定温度以上かつ室内温度が上昇しているため、暖房給湯開度比を4:6として、室内側減圧機構8を480×4/10=192p、給湯側減圧機構12を480×6/10=288pとする。こうすることで、暖房能力を減少させて給湯能力を上昇させる。
(2)dTset≧0かつdtTa<0の場合
この場合、室内温度は室内設定温度以上だが室内温度が下降しているため、暖房給湯開度比は5:5のままとする。
この場合、室内温度は室内設定温度未満だが室内温度が上昇しているため、暖房給湯開度比は5:5のままとする。
この場合。室内温度は室内設定温度未満かつ室内温度も下降しているため、暖房給湯開度比を6:4として、室内側減圧機構8を288p、給湯側減圧機構12を192pとする。こうすることで、暖房能力を増加させて給湯能力を減少させる。
暖房給湯開度比によって暖房能力と給湯能力の配分は制御できるようになったが、これだけだと冷媒状態をコントロールしていない。そのため、高圧上昇や低圧低下をもたらすことがあり、運転効率が低下する可能性がある。そのため、システム100では、室内側減圧機構8の開度と給湯側減圧機構12の開度の合計であるトータル減圧機構開度を冷媒の運転状態により制御することで運転効率の最大化を図るようにしている。トータル減圧機構開度を制御することで実現する目標運転状態は、給湯能力と暖房能力のどちらを大きくしたいかにより異なる。加えて、運転状態により決める。この二つの要因から最適な制御目標と目標状態を選定し制御する。なお、給湯能力と暖房能力のどちらを大きくしたいかは優先モードを判定し、選択する。
つまり、圧縮機1の吸入過熱度が5℃の場合の吐出温度を基準吐出温度として、吐出温度が基準吐出温度以上であるかによってアキュムレータ15に余剰液冷媒が存在しているかを判定する。なお、基準吐出温度TdBと、圧縮機1の高圧圧力Pcと、低圧圧力Peと、圧縮機1の運転周波数Fにおいて、TdB=f(Pc,Pe,F)の関係を有するデータテーブルを記憶部106に記憶しておき、データテーブルより基準吐出温度TdBを求めるとよい。ここで、高圧圧力Pcは圧力センサ201の検出圧力であり、低圧圧力Peは温度センサ206の検出温度を換算した圧力である。
一方で給湯優先モードでは給湯側減圧機構12の開度が室内側減圧機構8の開度より大きいため、給湯側過冷却度が室内側過冷却度よりも小さくなっている場合が多い。
このように、過冷却度が制御されている場合というのは、おおよそ室内側過冷却度と給湯側過冷却度のうち小さい方の過冷却度が制御されている状況である。
図8は、本発明の実施の形態2に係るヒートポンプシステム200(以下、単にシステム200と称する)の冷媒回路構成を示す概略図である。図8に基づいて、システム200の構成及び動作について説明する。なお、この実施の形態2では上述した実施の形態1との相違点を中心に説明するものとし、実施の形態1と同一作用である部分には、同一符号を付して説明を省略するものとする。
Claims (12)
- 圧縮機と、室内側熱交換器と、給湯側熱交換器と、室内側減圧機構と、給湯側減圧機構と、熱源側熱交換器と、を有し、
前記室内側熱交換器と前記室内側減圧機構とが直列に接続された流路と、前記給湯側熱交換器と前記給湯側減圧機構とが直列に接続された流路と、が並列に接続されて、前記圧縮機及び前記熱源側熱交換器とともに冷媒回路を構成しており、
前記室内側熱交換器で空気を加熱する暖房負荷と、前記給湯側熱交換器で水を加熱する給湯負荷と、が同時に要求された際、
前記室内側減圧機構開度が前記給湯側減圧機構開度よりも大きい暖房優先モードと、
前記給湯側減圧機構開度が前記室内側減圧機構開度よりも大きい給湯優先モードと、を有し、
前記暖房優先モードでは、前記室内側熱交換器の過冷却度が調整され、
前記給湯優先モードでは、前記給湯側熱交換器の過冷却度又は前記圧縮機の吐出温度のどちらか一方が調整される
ことを特徴とするヒートポンプシステム。 - 前記室内側減圧機構の開度と前記給湯側減圧機構の開度のトータル減圧機構開度によって、
前記暖房優先モードにおける前記室内側熱交換器の過冷却度が制御され、
前記給湯優先モードにおける前記給湯側熱交換器の過冷却度又は前記圧縮機の吐出温度が制御される
ことを特徴とする請求項1に記載のヒートポンプシステム。 - 前記給湯優先モードにおいて、
前記給湯側熱交換器の過冷却度が予め設定されている所定値未満であって、前記圧縮機の吐出温度が基準値以上である場合は、前記圧縮機の吐出温度が制御される
ことを特徴とする請求項1又は2に記載のヒートポンプシステム。 - 暖房能力と給湯能力の割合は、
前記トータル減圧機構開度に対する前記室内側減圧機構開度と前記トータル減圧機構開度に対する前記給湯側減圧機構開度とで決まる暖房給湯開度比により制御され、
前記トータル減圧機構開度を変更する場合は、
前記暖房給湯開度比によって、前記室内側減圧機構開度の変更量と前記給湯側減圧機構開度の変更量が決定される
ことを特徴とする請求項1~3のいずれか一項に記載のヒートポンプシステム。 - 前記暖房給湯開度比は前記暖房負荷によって決定される
ことを特徴とする請求項4に記載のヒートポンプシステム。 - 前記トータル減圧機構開度を超えないように前記暖房給湯開度比が変更される
ことを特徴とする請求項4又は5に記載のヒートポンプシステム。 - 前記トータル減圧機構開度の変更間隔は、
前記暖房給湯開度比の変更間隔よりも長くされる
ことを特徴とする請求項4~6のいずれか一項に記載のヒートポンプシステム。 - 室内温度が室内設定温度よりも所定値以上となると暖房サーモOFFとなるものにおいて、
前記暖房サーモOFFとなるまでの前記室内温度と前記室内設定温度の温度差が大きくされる
ことを特徴とする請求項1~7のいずれか一項に記載のヒートポンプシステム。 - 前記暖房優先モード又は前記給湯優先モードを表示し、前記暖房優先モード又は前記給湯優先モードを選択的に入力できるリモコンを備えた
ことを特徴とする請求項1~8のいずれか一項に記載のヒートポンプシステム。 - 前記給湯側熱交換器で加熱された水を貯える貯湯タンクを備え、
給湯時間及び前記貯湯タンクの蓄熱量の少なくとも一方を測定し、
前記給湯時間が所定値以上、及び、給湯開始時に前記貯湯タンクの蓄熱量が所定値以下の少なくとも一方を満たす場合には、優先モードが前記給湯優先モードとされる
ことを特徴とする請求項1~9のいずれか一項に記載のヒートポンプシステム。 - 前記貯湯タンクの高さ方向に複数個の温度センサを備え、
前記温度センサでの計測情報に基づいて前記貯湯タンクの蓄熱量が測定される
ことを特徴とする請求項10に記載のヒートポンプシステム。 - 前記給湯優先モードでは、
凝縮温度が前記給湯側熱交換器を流れる水の水温以上とされる
ことを特徴とする請求項1~11のいずれか一項に記載のヒートポンプシステム。
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