WO2015140877A1 - 絞り装置及び冷凍サイクル装置 - Google Patents
絞り装置及び冷凍サイクル装置 Download PDFInfo
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- WO2015140877A1 WO2015140877A1 PCT/JP2014/057036 JP2014057036W WO2015140877A1 WO 2015140877 A1 WO2015140877 A1 WO 2015140877A1 JP 2014057036 W JP2014057036 W JP 2014057036W WO 2015140877 A1 WO2015140877 A1 WO 2015140877A1
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- WIPO (PCT)
- Prior art keywords
- refrigerant
- heat exchanger
- valve body
- refrigeration cycle
- flows
- Prior art date
Links
- 238000005057 refrigeration Methods 0.000 title claims description 54
- 239000003507 refrigerant Substances 0.000 claims abstract description 283
- 238000007323 disproportionation reaction Methods 0.000 claims abstract description 31
- 239000000126 substance Substances 0.000 claims description 37
- 239000007788 liquid Substances 0.000 claims description 29
- 230000008859 change Effects 0.000 claims description 12
- MIZLGWKEZAPEFJ-UHFFFAOYSA-N 1,1,2-trifluoroethene Chemical group FC=C(F)F MIZLGWKEZAPEFJ-UHFFFAOYSA-N 0.000 claims description 7
- 238000004378 air conditioning Methods 0.000 claims description 6
- 239000000463 material Substances 0.000 abstract description 4
- 238000001816 cooling Methods 0.000 description 48
- 238000010438 heat treatment Methods 0.000 description 48
- 239000003570 air Substances 0.000 description 30
- 239000007789 gas Substances 0.000 description 24
- 238000001514 detection method Methods 0.000 description 12
- 238000010586 diagram Methods 0.000 description 11
- 230000000694 effects Effects 0.000 description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 6
- 230000006870 function Effects 0.000 description 6
- 239000002826 coolant Substances 0.000 description 5
- 230000002528 anti-freeze Effects 0.000 description 4
- RWRIWBAIICGTTQ-UHFFFAOYSA-N difluoromethane Chemical compound FCF RWRIWBAIICGTTQ-UHFFFAOYSA-N 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- 239000012267 brine Substances 0.000 description 3
- 238000009833 condensation Methods 0.000 description 3
- 230000005494 condensation Effects 0.000 description 3
- 238000001704 evaporation Methods 0.000 description 3
- 230000008020 evaporation Effects 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 3
- FXRLMCRCYDHQFW-UHFFFAOYSA-N 2,3,3,3-tetrafluoropropene Chemical compound FC(=C)C(F)(F)F FXRLMCRCYDHQFW-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 238000013459 approach Methods 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000004891 communication Methods 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000001294 propane Substances 0.000 description 2
- 230000005855 radiation Effects 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- CDOOAUSHHFGWSA-OWOJBTEDSA-N (e)-1,3,3,3-tetrafluoroprop-1-ene Chemical compound F\C=C\C(F)(F)F CDOOAUSHHFGWSA-OWOJBTEDSA-N 0.000 description 1
- CDOOAUSHHFGWSA-UHFFFAOYSA-N 1,3,3,3-tetrafluoropropene Chemical compound FC=CC(F)(F)F CDOOAUSHHFGWSA-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 description 1
- 239000012080 ambient air Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 description 1
- XUCNUKMRBVNAPB-UHFFFAOYSA-N fluoroethene Chemical group FC=C XUCNUKMRBVNAPB-UHFFFAOYSA-N 0.000 description 1
- 230000020169 heat generation Effects 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- -1 propane Chemical compound 0.000 description 1
- 238000004781 supercooling Methods 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
Images
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B13/00—Compression machines, plants or systems, with reversible cycle
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B41/00—Fluid-circulation arrangements
- F25B41/30—Expansion means; Dispositions thereof
- F25B41/31—Expansion valves
- F25B41/34—Expansion valves with the valve member being actuated by electric means, e.g. by piezoelectric actuators
- F25B41/35—Expansion valves with the valve member being actuated by electric means, e.g. by piezoelectric actuators by rotary motors, e.g. by stepping motors
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B41/00—Fluid-circulation arrangements
- F25B41/30—Expansion means; Dispositions thereof
- F25B41/38—Expansion means; Dispositions thereof specially adapted for reversible cycles, e.g. bidirectional expansion restrictors
-
- 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
- F25B43/00—Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat
-
- 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
- F25B2313/003—Indoor unit with water as a heat sink or heat source
-
- 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
-
- 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
-
- 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
- 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
- F25B2700/19—Pressures
- F25B2700/193—Pressures of the compressor
- F25B2700/1933—Suction pressures
-
- 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]
- Y02B30/70—Efficient control or regulation technologies, e.g. for control of refrigerant flow, motor or heating
Definitions
- the present invention relates to a throttle device or the like used for a refrigeration cycle device such as an air conditioner applied to, for example, a building multi-air conditioner.
- a refrigeration cycle apparatus that forms a refrigerant circuit that circulates refrigerant and performs air conditioning, such as a multi air conditioner for buildings, generally R410A that is nonflammable, R32 that has weak flammability, strong flammability
- Disproportionation is the property that substances of the same type react to change to another substance. For example, when some strong energy is applied to the refrigerant in a state where the distance between adjacent substances such as a liquid state is very close, this energy causes a disproportionation reaction, and the adjacent substances react with each other, It changes to another substance. When the disproportionation reaction occurs, heat is generated and a rapid temperature rise occurs, so that the pressure may rise rapidly.
- a substance that causes a disproportionation reaction is used as a refrigerant in a refrigeration cycle device and is enclosed in a pipe such as copper, the pipe cannot withstand the pressure rise of the internal refrigerant, and the pipe will burst. Accidents may occur.
- substances having such a disproportionation reaction for example, 1,1,2-trifluoroethylene (HFO-1123), acetylene and the like are known.
- thermal cycle system refrigeration cycle apparatus
- HFO-1123 1,1,2-trifluoroethylene
- 1,1,2-trifluoroethylene (HFO-1123) is used as a thermal cycle working medium.
- 1,1,2-trifluoroethylene (HFO-1123) is a substance having a disproportionation reaction.
- the adjacent substances react with each other and change to another substance by some energy.
- accidents such as pipe rupture may occur due to a sudden rise in pressure.
- the present invention has been made in order to solve the above-described problems, and provides a throttling device having a structure in which the energy received by the refrigerant from the outside is reduced.
- a throttling device is a throttling device that constitutes a refrigerant circuit using a refrigerant containing a substance that causes a disproportionation reaction, and has a cylindrical valve body and a valve seat, and the valve body is a valve.
- a throttle portion that moves in the axial direction and changes the opening area by being inserted into the valve seat, and the tip of the valve body that is inserted into the throttle portion is moved from 0 in a direction perpendicular to the axial direction of the valve body. It has a structure that is formed with a large angle, which can reduce the collision energy when refrigerant flows into the throttle device, and can safely use substances that cause disproportionation as a refrigerant. is there.
- the shape or direction of the outlet of the inflow pipe is devised to reduce the collision energy when the refrigerant collides with the inner wall surface of the container.
- Substances that cause a disproportionation reaction such as fluoroethylene (HFO-1123) cannot be used as a refrigerant due to a disproportionation reaction, prevent accidents such as pipe rupture, and can be used safely as a refrigerant.
- a diaphragm device that can be obtained can be obtained.
- FIG. 1 and the following drawings the same reference numerals denote the same or corresponding parts, and are common to the whole text of the embodiments described below.
- the form of the component represented by the whole specification is an illustration to the last, Comprising: It does not limit to the form described in the specification.
- the combination of the components is not limited to the combination in each embodiment, and the components described in the other embodiments can be applied to another embodiment.
- the subscripts may be omitted.
- the upper side in the figure will be described as “upper side” and the lower side will be described as “lower side”.
- the size relationship of each component may be different from the actual one.
- the level of temperature, pressure, etc. is not particularly determined in relation to absolute values, but is relatively determined in the state, operation, etc. of the system, apparatus, and the like.
- FIG. Embodiment 1 of the present invention will be described with reference to the drawings.
- FIG. 1 is a schematic diagram illustrating an installation example of a refrigeration cycle apparatus according to Embodiment 1 of the present invention.
- the refrigeration cycle apparatus shown in FIG. 1 can select either a cooling mode or a heating mode as an operation mode by configuring a refrigerant circuit that circulates refrigerant and using a refrigerant refrigeration cycle.
- the refrigeration cycle apparatus of the present embodiment will be described by taking an air conditioning apparatus that performs air conditioning of the air-conditioning target space (indoor space 7) as an example.
- the refrigeration cycle apparatus has one outdoor unit 1 that is a heat source unit and a plurality of indoor units 2.
- the outdoor unit 1 and the indoor unit 2 are connected by an extension pipe (refrigerant pipe) 4 that conducts the refrigerant, and the cold or warm heat generated by the outdoor unit 1 is delivered to the indoor unit 2.
- extension pipe refrigerant pipe
- the outdoor unit 1 is usually arranged in an outdoor space 6 that is a space outside a building 9 such as a building (for example, a rooftop), and supplies cold or hot heat to the indoor unit 2.
- the indoor unit 2 is disposed at a position where air whose temperature is adjusted can be supplied to the indoor space 7 which is a space inside the building 9 (for example, a living room). Supply air.
- an outdoor unit 1 and each indoor unit 2 are connected to each other using two extension pipes 4.
- the indoor unit 2 is a ceiling cassette type
- Any type may be used as long as heating air or cooling air can be blown directly into the indoor space 7 by a duct or the like, such as a ceiling-embedded type or a ceiling-suspended type.
- FIG. 1 shows an example in which the outdoor unit 1 is installed in the outdoor space 6, but the present invention is not limited to this.
- the outdoor unit 1 may be installed in an enclosed space such as a machine room with a ventilation opening. Further, if the waste heat can be exhausted outside the building 9 by the exhaust duct, it may be installed inside the building 9. Furthermore, you may make it install in the inside of the building 9 using the water-cooled outdoor unit 1.
- the number of connected outdoor units 1 and indoor units 2 is not limited to the number shown in FIG. 1, but the number of units can be determined according to the building 9 in which the refrigeration cycle apparatus according to the present embodiment is installed. That's fine.
- FIG. 2 is a circuit configuration diagram showing an example of a circuit configuration of the refrigeration cycle apparatus (hereinafter referred to as the refrigeration cycle apparatus 100) according to the first embodiment. Based on FIG. 2, the detailed structure of the refrigerating-cycle apparatus 100 is demonstrated. As shown in FIG. 2, the outdoor unit 1 and the indoor unit 2 are connected by an extension pipe (refrigerant pipe) 4 through which a refrigerant flows.
- extension pipe refrigerant pipe
- Outdoor unit 1 The outdoor unit 1 is mounted with a compressor 10, a first refrigerant flow switching device 11 such as a four-way valve, a heat source side heat exchanger 12, and an accumulator 19 connected in series by a refrigerant pipe.
- the compressor 10 sucks refrigerant and compresses the refrigerant to a high temperature and high pressure state.
- the compressor 10 may be composed of an inverter compressor capable of capacity control.
- the first refrigerant flow switching device 11 switches the refrigerant flow during the heating operation and the refrigerant flow during the cooling operation.
- the heat source side heat exchanger 12 functions as an evaporator during heating operation, and functions as a condenser (or radiator) during cooling operation.
- the heat source side heat exchanger 12 serving as the first heat exchanger performs heat exchange between air supplied from a blower (not shown) and the refrigerant, and evaporates or condenses the refrigerant. is there.
- the heat source side heat exchanger 12 acts as a condenser in the operation of cooling the indoor space 7. Moreover, in the case of the driving
- the accumulator 19 is provided on the suction side of the compressor 10 and stores excess refrigerant in the refrigerant circuit due to an operation mode change or the like.
- the outdoor unit 1 includes a compressor 10, a first refrigerant flow switching device 11, a heat source side heat exchanger 12, an accumulator 19, a high pressure detection device 37, a low pressure detection device 38, and a control device 60.
- the compressor 10 has, for example, a low-pressure shell structure that has a compression chamber in a sealed container, the inside of the sealed container has a low-pressure refrigerant pressure atmosphere, and sucks and compresses the low-pressure refrigerant in the sealed container.
- a high-pressure shell structure is used in which the inside of the sealed container becomes a high-pressure refrigerant pressure atmosphere and the high-pressure refrigerant compressed in the compression chamber is discharged into the sealed container.
- the outdoor unit 1 includes a control device 60, and controls devices based on detection information from various detection devices, instructions from a remote controller, and the like. For example, the driving frequency of the compressor 10, the rotation speed of the blower (including ON / OFF), the switching of the first refrigerant flow switching device 11 and the like are controlled, and each operation mode described later is executed.
- the control device 60 of the present embodiment is configured by a microcomputer or the like having control arithmetic processing means such as a CPU (Central Processing Unit). Moreover, it has a memory
- control arithmetic processing means executes processing based on the program data to realize control.
- the indoor unit 2 is equipped with a load-side heat exchanger 15 serving as a second heat exchanger.
- the load side heat exchanger 15 is connected to the outdoor unit 1 by the extension pipe 4.
- the load-side heat exchanger 15 exchanges heat between air supplied from a blower (not shown) and a refrigerant, and generates heating air or cooling air to be supplied to the indoor space 7. .
- the load side heat exchanger 15 acts as a condenser in the case of an operation for heating the indoor space 7. Moreover, in the case of the driving
- FIG. 2 shows an example in which four indoor units 2 are connected, and are illustrated as an indoor unit 2a, an indoor unit 2b, an indoor unit 2c, and an indoor unit 2d from the bottom of the page.
- the load side heat exchanger 15 is also loaded from the lower side of the page with the load side heat exchanger 15a, the load side heat exchanger 15b, the load side heat exchanger 15c, and the load side heat exchange. It is shown as a container 15d.
- the number of connected indoor units 2 is not limited to four as shown in FIG.
- the refrigeration cycle apparatus 100 determines the operation mode of the outdoor unit 1 to be either the cooling operation mode or the heating operation mode based on an instruction from each indoor unit 2. That is, the refrigeration cycle apparatus 100 can perform the same operation (cooling operation or heating operation) for all of the indoor units 2 and adjusts the indoor temperature. Note that each indoor unit 2 can be freely operated / stopped in both the cooling operation mode and the heating operation mode.
- the operation mode executed by the refrigeration cycle apparatus 100 includes a cooling operation mode in which all the driven indoor units 2 perform a cooling operation (including a stop), and all of the driven indoor units 2 are in a heating operation. There is a heating operation mode for executing (including stopping). Below, each operation mode is demonstrated with the flow of a refrigerant
- FIG. 3 is a refrigerant circuit diagram illustrating the refrigerant flow in the cooling operation mode when the discharge temperature of the refrigeration cycle apparatus 100 is low.
- the cooling operation mode will be described by taking as an example a case where a cooling load is generated in all the load-side heat exchangers 15.
- a pipe indicated by a thick line indicates a pipe through which the refrigerant flows, and a flow direction of the refrigerant is indicated by a solid line arrow.
- the first refrigerant flow switching device 11 is switched so that the refrigerant discharged from the compressor 10 flows into the heat source side heat exchanger 12.
- the low-temperature and low-pressure refrigerant is compressed by the compressor 10 and discharged as a high-temperature and high-pressure gas refrigerant.
- the high-temperature and high-pressure gas refrigerant discharged from the compressor 10 flows into the heat source side heat exchanger 12 via the first refrigerant flow switching device 11. Then, the heat source side heat exchanger 12 condenses and liquefies while radiating heat to the outdoor air, becomes a high-pressure liquid refrigerant, and flows out of the outdoor unit 1.
- the high-pressure liquid refrigerant that has flowed out of the outdoor unit 1 passes through the extension pipe 4 and flows into each of the indoor units 2 (2a to 2d).
- the high-pressure liquid refrigerant that has flowed into the indoor unit 2 (2a to 2d) flows into the expansion device 16 (16a to 16d), and is throttled and decompressed by the expansion device 16 (16a to 16d). It becomes a phase refrigerant. Further, it flows into each of the load side heat exchangers 15 (15a to 15d) acting as an evaporator, absorbs heat from the air flowing around the load side heat exchanger 15, and becomes a low-temperature and low-pressure gas refrigerant.
- the low-temperature and low-pressure gas refrigerant flows out of the indoor unit 2 (2a to 2d), flows into the outdoor unit 1 again through the extension pipe 4, passes through the first refrigerant flow switching device 11, and passes through the accumulator 19. Then, it is sucked into the compressor 10 again.
- the opening degree (opening area) of the expansion devices 16a to 16d is determined based on the detected temperature of the load-side heat exchanger gas refrigerant temperature detection device 28 and the control device 60 of each outdoor unit 2 from the control device 60 of the outdoor unit 1 (FIG. It is controlled so that the temperature difference (superheat degree) between the evaporation temperature transmitted by communication to the target value (not shown) approaches the target value.
- the cooling operation mode when executed, the operation is stopped because there is no need to flow the refrigerant to the load-side heat exchanger 15 (including the thermo-off) without the heat load.
- the expansion device 16 corresponding to the stopped indoor unit 2 is fully closed or set to a small opening at which the refrigerant does not flow.
- FIG. 4 is a refrigerant circuit diagram illustrating a refrigerant flow when the refrigeration cycle apparatus 100 is in the heating operation mode.
- the heating operation mode will be described by taking as an example a case where a thermal load is generated in all the load side heat exchangers 15.
- a pipe indicated by a thick line indicates a pipe through which the refrigerant flows, and a flow direction of the refrigerant is indicated by a solid line arrow.
- the first refrigerant flow switching device 11 passes the refrigerant discharged from the compressor 10 to the indoor unit 2 without passing through the heat source side heat exchanger 12. Switch to allow inflow.
- the low-temperature and low-pressure refrigerant is compressed by the compressor 10 and discharged as a high-temperature and high-pressure gas refrigerant, passes through the first refrigerant flow switching device 11, and flows out of the outdoor unit 1.
- the high-temperature and high-pressure gas refrigerant that has flowed out of the outdoor unit 1 flows into each of the indoor units 2 (2a to 2d) through the extension pipe 4.
- the high-temperature and high-pressure liquid refrigerant that has flowed out of the load-side heat exchanger 15 (15a to 15d) flows into the expansion device 16 (16a to 16d), is throttled and decompressed by the expansion device 16 (16a to 16d), It becomes a low-pressure two-phase refrigerant and flows out of the indoor unit 2 (2a to 2d).
- the low-temperature and low-pressure two-phase refrigerant that has flowed out of the indoor unit 2 flows into the outdoor unit 1 again through the extension pipe 4.
- the opening degree (opening area) of the expansion devices 16a to 16d is determined based on the condensation temperature transmitted from the control device 60 of the outdoor unit 1 to the control device (not shown) of each indoor unit 2 through communication and the load side heat. Control is performed so that the temperature difference (degree of supercooling) from the detected temperature of the exchanger liquid refrigerant temperature detecting device 27 approaches the target value.
- the low-temperature and low-pressure two-phase refrigerant that has flowed into the outdoor unit 1 flows into the heat source side heat exchanger 12, absorbs heat from the air flowing around the heat source side heat exchanger 12, and evaporates to form a low-temperature and low-pressure gas refrigerant or low-temperature and low-pressure. It becomes a two-phase refrigerant with a large dryness.
- the low-temperature and low-pressure gas refrigerant or two-phase refrigerant is again sucked into the compressor 10 via the first refrigerant flow switching device 11 and the accumulator 19.
- the heating operation mode When the heating operation mode is executed, it is not necessary to flow the refrigerant to the load-side heat exchanger 15 (including the thermo-off) that has no heat load.
- the load-side heat exchanger 15 that is not in operation is set inside.
- the opening degree (opening area) of the expansion device 16 corresponding to the load-side heat exchanger 15 having no heat load is set to a large opening degree such as full opening to prevent accumulation of refrigerant.
- the first refrigerant flow switching device 11 generally uses a four-way valve. However, the first refrigerant flow switching device 11 is not limited to this and uses a plurality of two-way flow switching valves and a plurality of three-way flow switching valves. You may comprise so that a refrigerant
- coolant may flow into this.
- the accumulator 19 for storing the excess refrigerant is provided in the refrigerant circuit.
- the excess refrigerant is used when the extension pipe 4 is short, the number of the indoor units 2 is one, or the like. When there is little, the accumulator 19 does not need to be provided.
- high-pressure liquid refrigerant flows into the expansion device 16 (16a to 16d), and low-temperature and low-pressure two-phase refrigerant flows out.
- the refrigerant flowing out of the condenser may be in a two-phase state.
- the extension pipe 4 is often long. In this case, the refrigerant is two-phased due to pressure loss in the extension pipe 4 in the cooling operation. In some cases, you may have. In such a case, a two-phase refrigerant that is a mixed state of gas and liquid flows into the expansion device 16.
- the refrigerant is not a refrigerant such as 1,1,2-trifluoroethylene (HFO-1123) represented by C 2 H 1 F 3 and having one double bond in the molecular structure.
- HFO-1123 1,1,2-trifluoroethylene
- a substance that causes a leveling reaction or a mixed refrigerant in which a substance that causes a disproportionation reaction and another substance are mixed is used.
- HC-290 (propane) or the like may be mixed, and any substance having thermal performance that can be used as a refrigerant in a refrigeration cycle apparatus may be used. Any mixing ratio may be used.
- a substance that causes a disproportionation reaction is a state in which adjacent substances are brought into contact with each other when strong energy is applied in a state where the distance between adjacent substances is very close, such as a liquid state or a two-phase state. May react to change to another substance. For this reason, if a substance that causes a disproportionation reaction without using any countermeasure in the refrigerant circuit is used as a refrigerant, it will not function as a refrigerant as a separate substance, but also due to a sudden pressure increase due to heat generation. Accidents such as pipe rupture may occur.
- the disproportionation reaction is caused in a refrigerant circuit in a place where the refrigerant circuit is in a liquid state or a two-phase state where a gas and a liquid are mixed. It is necessary to devise something that does not exist. Here, the energy when the refrigerant collides with the structure is also a factor causing the material to disproportionate. In view of this, by disposing the components of the refrigerant circuit so as to reduce the collision energy applied to the refrigerant, the disproportionation reaction is less likely to occur.
- FIG. 5 is a schematic diagram of a configuration of the diaphragm device 16 (16a to 16d) according to the first embodiment of the present invention.
- the throttle device 16 includes a first connection pipe 41, a second connection pipe 42, a throttle portion 43, a valve body 44, and a motor 45.
- the solid line arrow indicates the direction in which the refrigerant flows during the heating operation
- the broken line arrow indicates the direction in which the refrigerant flows during the cooling operation.
- the first connection pipe 41 is connected to the pipe on the extension pipe 4 side.
- the heat source side heat exchanger 12 acts as an evaporator and the load side heat exchanger 15 acts as a condenser, it becomes a refrigerant inflow side pipe.
- the heat source side heat exchanger 12 acts as a condenser and the load side heat exchanger 15 acts as an evaporator, it becomes piping on the refrigerant outflow side.
- the second connection pipe 42 is connected to piping on the load side heat exchanger 15 side.
- the heat source side heat exchanger 12 acts as an evaporator and the load side heat exchanger 15 acts as a condenser, it becomes a refrigerant outflow side pipe.
- the heat source side heat exchanger 12 acts as a condenser and the load side heat exchanger 15 acts as an evaporator, it becomes a pipe on the refrigerant inflow side.
- the first connecting pipe 41 and the second connecting pipe 42 are arranged in a direction orthogonal to each other with the throttle 43 interposed therebetween.
- the throttle portion 43 having a valve seat is disposed between the first connection pipe 41 and the second connection pipe 42, and adjusts the flow of refrigerant passing therethrough depending on the degree of insertion of the valve body 44 into the opening portion of the valve seat. And depressurize the refrigerant.
- the valve body 44 is movable, and controls the flow rate of refrigerant and the refrigerant pressure (throttle amount) passing through the throttle device 16 together with the throttle unit 43.
- the valve body 44 moves and the distance (positional relationship) between the valve body 44 and the throttle portion 43 is changed, whereby the area (opening area) of the gap between the throttle portion 43 and the valve body 44 is controlled. Is controlled by changing the refrigerant flow rate and the refrigerant pressure.
- the motor 45 moves the valve body 44 based on an instruction from the control device 60 to adjust the distance between the throttle portion 43 and the valve body 44.
- the motor 45 is composed of, for example, a stepping motor.
- the high-pressure liquid refrigerant that flows out of the outdoor unit 1 and flows into the indoor unit 2 flows in from the second connection pipe 42.
- the pressure is reduced by the valve body 44, the refrigerant becomes low-temperature and low-pressure two-phase refrigerant, flows out of the first connection pipe 41, and flows into the load-side heat exchanger 15 (15 a to 15 d).
- the position of the valve body 44 (position in the vertical direction in FIG. 5) is controlled by the motor 45, and the opening area through which the refrigerant passes between the throttle portion 43 and the valve body 44 is changed. Is controlled.
- the valve body 44 has a cylindrical (columnar) shape, for example. If it is cylindrical, the cross-sectional area does not change even if it moves in the axial direction of the valve body 44 while rotating, so it is easy to use as the valve body 44 of the expansion device 16.
- the flow direction of the refrigerant flowing in from the first connection pipe 41 and the flow direction of the refrigerant flowing out of the second connection pipe 42 are substantially perpendicular to each other.
- the refrigerant flowing from the second connection pipe 42 collides with the cylindrical valve body 44 in the vertical direction (valve axis direction).
- the refrigerant collides with a circular portion at the shaft end.
- the high-pressure liquid refrigerant that has flowed out of the load-side heat exchanger 15 flows from the first connection pipe 41.
- the pressure is reduced by the valve body 44, becomes a low-temperature and low-pressure two-phase refrigerant, flows out from the throttle device 16 through the second connection pipe 42, and flows out from the indoor unit 2.
- the flow direction of the refrigerant flowing in from the first connection pipe 41 and the flow direction of the refrigerant flowing out of the second connection pipe 42 are substantially orthogonal to each other.
- the refrigerant collides sideways (circumferential direction) with respect to the cylindrical valve body 44. It is well known that when a refrigerant flows laterally (circumferentially) in a cylindrical structure, the refrigerant does not generate much turbulence, and can cause a disproportionation reaction of the refrigerant. Absent.
- the tip portion of the valve body 44 (the bottom surface portion of the cylinder on the flow path side in the valve body 44) flows in the flow direction of refrigerant flowing from the second connection pipe 42 (vertical (vertical ) Direction, axial direction) and a structure (for example, a conical structure) having an inclination of an angle ⁇ larger than 0 (zero) with respect to a direction (lateral (left / right) direction, circumferential direction in FIG. 5) orthogonal to To do.
- the valve body 44 has such a structure, the valve body 44 has an inclination of an angle ⁇ larger than 0 (zero) with respect to the flow direction of the refrigerant. Energy is reduced and disproportionation reaction is less likely to occur.
- the collision energy between the valve body 44 and the refrigerant is obtained by the equation (1).
- the change in the speed of the refrigerant depends on the angle ⁇ at the tip of the valve body 44 and is expressed by the equation (2).
- the collision energy between the refrigerant and the valve body 44 is proportional to the equation (2), and the reduction rate of the collision energy is based on the difference from 1 which is the calculation result of the equation (2) when ⁇ is 0 (zero). can get. Therefore, if the valve body 44 has a structure in which the angle ⁇ with respect to the direction orthogonal to the axial direction (circumferential direction) has a value larger than 0 (zero), the collision energy with the refrigerant becomes small, so the disproportionation reaction Is difficult to get up. Also, the amount of collision energy required to reduce the disproportionation reaction of the refrigerant depends on the state of the refrigerant (pressure and temperature), the speed of the refrigerant, etc.
- the collision energy can be reduced by 5% or more, the effect is great.
- the 5% impact energy reduction effect is obtained when the calculation result of Equation (2) is 0.95.
- ⁇ is about 18 degrees. Accordingly, if the angle ⁇ with respect to the direction orthogonal to the axial direction of the valve body 44 (circumferential direction) is 18 degrees or more, that is, the opening angle of the cone is 144 degrees or less, the impact energy can be reduced. Becomes larger.
- the upper limit of the angle ⁇ is not particularly defined as long as an opening angle of the cone that can effectively change the opening area of the refrigerant can be secured with the throttle portion 43 (if the angle ⁇ is too large). The function as a diaphragm device cannot be performed).
- FIG. 6 is a schematic diagram of another example of the configuration of the diaphragm device 16 (16a to 16d) according to Embodiment 1 of the present invention.
- the structure of the tip of the valve body 44 of the expansion device 16 (16a to 16d) is not limited to a conical shape, and may be a polyhedral structure.
- the tip of the valve body 44 is inclined at an angle ⁇ greater than 0 (zero) with respect to a direction (circumferential direction) orthogonal to the flow direction of the refrigerant flowing in from the second connection pipe 42 in many parts.
- Any structure that has As shown in FIG. 6, a part of the portion may have a disk shape (conical frustum) orthogonal to the flow.
- a portion having a structure having an inclination of an angle ⁇ larger than 0 (zero) with respect to a direction (circumferential direction) orthogonal to the flow direction of the refrigerant flowing in from the second connection pipe 42 is a valve body. It suffices to occupy 50% or more with respect to 44 circumferential cross-sectional areas.
- a stepping motor or the like is used as the motor 45 of the aperture device 16, but it is not limited thereto.
- the valve body 44 moves up and down while rotating to change the opening area.
- the structure of the shaft end of the valve body 44 is conical, there is no shape change associated with rotation, and the opening area can be easily controlled.
- a direct-acting throttle device that directly drives the valve body 44 by the motor 45 and a gear-type throttle device in which a gear is interposed between the motor 45 and the valve body 44. However, it can be applied and has the same effect.
- the refrigerant flows in from the first connection pipe 41 of the expansion device 16 and flows out of the second connection pipe 42 during the heating operation, and flows in from the second connection tube 42 of the expansion device 16 during the cooling operation.
- the case of flowing out from the one connecting pipe 41 has been described.
- the refrigerant flows in the cooling operation and the heating operation in opposite directions, the function as the expansion device 16 is not impaired, and the flow may be made in either direction.
- the refrigerant can be used in either the cooling operation or the heating operation. Flows into the expansion device 16 from the second connection pipe 42, and the same effect is produced.
- the two-phase refrigerant is a refrigerant in which a gaseous and liquid refrigerant are mixed. is there. Since it is necessary to prevent the disproportionation reaction from occurring in the liquid refrigerant in the two-phase refrigerant, the same structure is effective.
- the 1st connection pipe 41 and the 2nd connection pipe 42 are the directions which cross at right angles, and demonstrated as an example the case where the flow direction reverses by cooling operation and heating operation, it does not restrict to this. .
- the refrigerant flow path may be configured in a direction that is not perpendicular to the axial direction of the valve body 44.
- the flow path of the refrigerant is once directed in a direction orthogonal to the axial direction of the valve body 44, and then the flow path is further changed so that the first connection pipe 41 is The direction may be parallel to the second connecting pipe 42.
- the refrigeration cycle apparatus 100 has several operation modes. In these operation modes, the refrigerant flows through the extension pipe 4 that connects the outdoor unit 1 and the indoor unit 2.
- the high pressure detection device 37 and the low pressure detection device 38 are installed to control the refrigeration cycle high pressure and low pressure to target values, but may be a temperature detection device that detects a saturation temperature.
- coolant flow path switching device 11 was shown as if it were a four-way valve, it is not restricted to this, It uses the two-way flow path switching valve and the three-way flow path switching valve similarly, You may comprise so that a refrigerant
- the heat source side heat exchanger 12 and the load side heat exchangers 15a to 15d are provided with a blower, and in many cases, condensation or evaporation is promoted by blowing, but this is not restrictive.
- a blower for example, as the load side heat exchangers 15a to 15d, a panel heater using radiation can be used, and as the heat source side heat exchanger 12, a water-cooled type that moves heat by water or antifreeze. Things can also be used. Any heat exchanger having a structure capable of radiating or absorbing heat can be used.
- the indoor unit 2 can arbitrarily select one of a cooling operation and a heating operation, and the entire system can perform a mixed operation of the indoor unit 2 that performs the cooling operation and the indoor unit 2 that performs the heating operation.
- the present invention can also be applied to a refrigeration cycle apparatus and has the same effect.
- FIG. 7 is a circuit diagram of the refrigeration cycle apparatus according to the embodiment of the present invention.
- the outdoor unit 1 and the heat medium converter 3 are supplied with refrigerant through the load side heat exchanger 15 a and the load side heat exchanger 15 b provided in the heat medium converter 3. They are connected by an extension pipe 4 that flows inside.
- the heat medium converter 3 and the indoor unit 2 are also connected by a pipe 5 through which a heat medium such as water or brine flows through the load side heat exchanger 15a and the load side heat exchanger 15b.
- the operation mode executed by the refrigeration cycle apparatus 100 includes a cooling only operation mode in which all the driven indoor units 2 execute a cooling operation and a heating operation in which all the driven indoor units 2 execute a heating operation. There is an operation mode. Further, there are a cooling main operation mode executed when the cooling load is larger and a heating main operation mode executed when the heating load is larger.
- the high-temperature and high-pressure gas refrigerant discharged from the compressor 10 flows into the heat source side heat exchanger 12 via the first refrigerant flow switching device 11 and dissipates heat to the surrounding air. It condenses and becomes high-pressure liquid refrigerant and flows out of the outdoor unit 1 through the check valve 13a. Then, it flows into the heat medium relay unit 3 through the extension pipe 4. The refrigerant flowing into the heat medium relay unit 3 passes through the opening / closing device 17a, expands in the expansion device 16a and the expansion device 16b, and becomes a low-temperature and low-pressure two-phase refrigerant.
- the two-phase refrigerant flows into each of the load side heat exchanger 15a and the load side heat exchanger 15b acting as an evaporator, absorbs heat from the heat medium circulating in the heat medium circuit B, and becomes a low-temperature and low-pressure gas refrigerant. .
- the gas refrigerant flows out of the heat medium relay unit 3 via the second refrigerant flow switching device 18a and the second refrigerant flow switching device 18b. Then, it flows into the outdoor unit 1 again through the extension pipe 4.
- the refrigerant flowing into the outdoor unit 1 passes through the check valve 13d and is sucked into the compressor 10 again via the first refrigerant flow switching device 11 and the accumulator 19.
- the heat medium is cooled by the refrigerant in both the load side heat exchanger 15a and the load side heat exchanger 15b.
- the cooled heat medium flows through the pipe 5 by the pump 21a and the pump 21b.
- the heat medium flowing into the use side heat exchangers 26a to 26d through the second heat medium flow switching devices 23a to 23d absorbs heat from the indoor air.
- the indoor air is cooled to cool the indoor space 7.
- the refrigerant that has flowed out of the use side heat exchangers 26a to 26d flows into the heat medium flow control devices 25a to 25d, passes through the first heat medium flow switching devices 22a to 22d, and passes through the load side heat exchanger 15a and the load side.
- the heat medium flow control devices 25a to 25d corresponding to the use side heat exchangers 26a to 26d without heat load are fully closed. Further, the heat medium flow control devices 25a to 25d corresponding to the use side heat exchangers 26a to 26d having the heat load adjust the opening degree to adjust the heat load in the use side heat exchangers 26a to 26d.
- the high-temperature and high-pressure gas refrigerant discharged from the compressor 10 flows out of the outdoor unit 1 through the first refrigerant flow switching device 11 and the first connection pipe 4a and the check valve 13b. To do. Then, it flows into the heat medium relay unit 3 through the extension pipe 4.
- the refrigerant that has flowed into the heat medium relay unit 3 flows into the load-side heat exchanger 15a and the load-side heat exchanger 15b through the second refrigerant flow switching device 18a and the second refrigerant flow switching device 18b, respectively.
- the heat is radiated to the heat medium circulating in the heat medium circuit B, and becomes a high-pressure liquid refrigerant.
- the high-pressure liquid refrigerant expands in the expansion device 16a and the expansion device 16b to become a low-temperature and low-pressure two-phase refrigerant, and flows out of the heat medium converter 3 through the opening / closing device 17b. Then, it flows into the outdoor unit 1 again through the extension pipe 4.
- the refrigerant flowing into the outdoor unit 1 passes through the second connection pipe 4b and the check valve 13c, flows into the heat source side heat exchanger 12 acting as an evaporator, absorbs heat from the surrounding air, and is a low-temperature and low-pressure gas refrigerant. It becomes.
- the gas refrigerant is again sucked into the compressor 10 via the first refrigerant flow switching device 11 and the accumulator 19.
- the operation of the heat medium in the heat medium circuit B is the same as in the cooling only operation mode.
- the heat medium is heated by the refrigerant in the load-side heat exchanger 15a and the load-side heat exchanger 15b, and is radiated to the indoor air in the use-side heat exchanger 26a and the use-side heat exchanger 26b.
- the indoor space 7 is heated.
- the high-temperature and high-pressure gas refrigerant discharged from the compressor 10 flows into the heat source side heat exchanger 12 via the first refrigerant flow switching device 11 and radiates and condenses to the surrounding air. Then, it becomes a two-phase refrigerant and flows out of the outdoor unit 1 through the check valve 13a. Then, it flows into the heat medium relay unit 3 through the extension pipe 4. The refrigerant flowing into the heat medium relay unit 3 flows into the load-side heat exchanger 15b acting as a condenser through the second refrigerant flow switching device 18b, and dissipates heat to the heat medium circulating in the heat medium circuit B. And high pressure liquid refrigerant.
- the high-pressure liquid refrigerant expands in the expansion device 16b and becomes a low-temperature and low-pressure two-phase refrigerant.
- the two-phase refrigerant flows into the load-side heat exchanger 15a acting as an evaporator through the expansion device 16a, absorbs heat from the heat medium circulating in the heat medium circuit B, and becomes a low-pressure gas refrigerant. It flows out of the heat medium relay unit 3 through the path switching device 18a. Then, it flows into the outdoor unit 1 again through the extension pipe 4.
- the refrigerant flowing into the outdoor unit 1 passes through the check valve 13d and is sucked into the compressor 10 again via the first refrigerant flow switching device 11 and the accumulator 19.
- the heat of the refrigerant is transmitted to the heat medium by the load side heat exchanger 15b.
- the heated heat medium flows in the pipe 5 by the pump 21b.
- the heat medium that has flowed into the use side heat exchangers 26a to 26d for which heating is requested by operating the first heat medium flow switching devices 22a to 22d and the second heat medium flow switching devices 23a to 23d radiates heat to the indoor air.
- the indoor air is heated to heat the indoor space 7.
- the cold heat of the refrigerant is transmitted to the heat medium in the load side heat exchanger 15a.
- the cooled heat medium flows through the pipe 5 by the pump 21a.
- the heat medium that has flowed into the use side heat exchangers 26a to 26d for which cooling is requested by operating the first heat medium flow switching devices 22a to 22d and the second heat medium flow switching devices 23a to 23d absorbs heat from the indoor air. To do.
- the indoor air is cooled to cool the indoor space 7.
- the heat medium flow control devices 25a to 25d corresponding to the use side heat exchangers 26a to 26d without heat load are fully closed.
- the heat medium flow control devices 25a to 25d corresponding to the use side heat exchangers 26a to 26d having the heat load adjust the opening degree to adjust the heat load in the use side heat exchangers 26a to 26d.
- Heating main operation mode In the heating main operation mode, the high-temperature and high-pressure gas refrigerant discharged from the compressor 10 passes through the first refrigerant flow switching device 11, passes through the first connection pipe 4 a and the check valve 13 b, and then the outdoor unit 1. Spill from. Then, it flows into the heat medium relay unit 3 through the extension pipe 4. The refrigerant flowing into the heat medium relay unit 3 flows into the load-side heat exchanger 15b acting as a condenser through the second refrigerant flow switching device 18b, and dissipates heat to the heat medium circulating in the heat medium circuit B. And high pressure liquid refrigerant.
- the high-pressure liquid refrigerant expands in the expansion device 16b and becomes a low-temperature and low-pressure two-phase refrigerant.
- the two-phase refrigerant flows into the load-side heat exchanger 15a acting as an evaporator via the expansion device 16a, absorbs heat from the heat medium circulating in the heat medium circuit B, and passes through the second refrigerant flow switching device 18a. And flows out of the heat medium relay unit 3. Then, it flows into the outdoor unit 1 again through the extension pipe 4.
- the refrigerant flowing into the outdoor unit 1 flows into the heat source side heat exchanger 12 acting as an evaporator through the second connection pipe 4b and the check valve 13c, absorbs heat from the surrounding air, and is a low-temperature and low-pressure gas.
- the gas refrigerant is again sucked into the compressor 10 via the first refrigerant flow switching device 11 and the accumulator 19.
- the operation of the heat medium in the heat medium circuit B, the first heat medium flow switching devices 22a to 22d, the second heat medium flow switching devices 23a to 23d, the heat medium flow control devices 25a to 25d, and the use side The operations of the heat exchangers 26a to 26d are the same as those in the cooling main operation mode.
- refrigerant type and throttle device 16 (16a, 16b) The type of refrigerant and the expansion device 16 (16a, 16b) can be configured by applying the same configurations as those described in the first embodiment. And the same effect is show
- the first heat medium flow switching device 22 corresponding to the use side heat exchanger 26 performing the heating operation and The second heat medium flow switching device 23 is switched to a flow path connected to the load side heat exchanger 15b for heating. Further, the first heat medium flow switching device 22 and the second heat medium flow switching device 23 corresponding to the use side heat exchanger 26 performing the cooling operation are connected to the cooling load side heat exchanger 15a. Switch to the flow path. For this reason, in each indoor unit 2, heating operation and cooling operation can be performed freely.
- the first heat medium flow switching device 22 and the second heat medium flow switching device 23 are those that can switch a three-way flow path such as a three-way valve, and those that open and close a two-way flow path such as an on-off valve. What is necessary is just to switch a flow path, such as combining two.
- the first heat medium can be obtained by combining two things, such as a stepping motor driven mixing valve, which can change the flow rate of the three-way flow path, and two things, such as an electronic expansion valve, which can change the flow rate of the two-way flow path.
- the flow path switching device 22 and the second heat medium flow path switching device 23 may be used.
- the heat medium flow control device 25 may be installed as a control valve having a three-way flow path with a bypass pipe that bypasses the use-side heat exchanger 26 other than the two-way valve. Further, the heat medium flow control device 25 may be a stepping motor drive type that can control the flow rate flowing through the flow path, and may be a two-way valve or a device in which one end of the three-way valve is closed. Further, as the heat medium flow control device 25, a device that opens and closes a two-way flow path such as an open / close valve may be used, and the average flow rate may be controlled by repeating ON / OFF.
- first refrigerant flow switching device 11 and the second refrigerant flow switching device 18 are shown as if they were four-way valves.
- the present invention is not limited to this, and a two-way flow switching valve or a three-way flow switching is possible. A plurality of valves may be used so that the refrigerant flows in the same manner.
- the heat medium flow control device 25 is built in the heat medium converter 3 has been described as an example.
- the heat medium flow control device 25 is not limited thereto, and may be built in the indoor unit 2. 3 and the indoor unit 2 may be configured separately.
- the heat medium for example, brine (antifreeze), water, a mixture of brine and water, a mixture of water and an additive having a high anticorrosive effect, or the like can be used. Therefore, in the refrigeration cycle apparatus 100, even if the heat medium leaks into the indoor space 7 through the indoor unit 2, a highly safe heat medium is used, which contributes to an improvement in safety. Become.
- the heat source side heat exchanger 12 and the use side heat exchangers 26a to 26d are provided with a blower, and in many cases, condensation or evaporation is promoted by blowing, but this is not restrictive.
- a blower for example, as the use side heat exchangers 26a to 26d, a panel heater using radiation can be used.
- a water-cooled type that moves heat by water or antifreeze can also be used. Any structure that can dissipate or absorb heat can be used.
- the number of pumps 21a and 21b is not limited to one, and a plurality of small capacity pumps may be arranged in parallel.
- the compressor 10, the four-way valve (first refrigerant flow switching device) 11, and the heat source side heat exchanger 12 are accommodated in the outdoor unit 1, and the use side heat exchanger is configured to exchange heat between the air in the air-conditioning target space and the refrigerant.
- 26 is accommodated in the indoor unit 2
- the load-side heat exchanger 15 and the expansion device 16 are accommodated in the heat medium converter 3
- the outdoor unit 1 and the heat medium converter 3 are connected by the extension pipe 4 to form a refrigerant. Is circulated, and the heat medium is circulated by connecting the indoor unit 2 and the heat medium converter 3 with a set of two pipes 5 each, and the load-side heat exchanger 15 exchanges heat between the refrigerant and the heat medium.
- the system to be performed has been described by way of an example of a system that can perform a mixed operation of the indoor unit 2 that performs the cooling operation and the indoor unit 2 that performs the heating operation, but is not limited thereto.
- the outdoor unit 1 and the heat medium relay unit 3 described in the first embodiment can be combined and applied to a system that performs only a cooling operation or a heating operation in the indoor unit 2 and has the same effect.
- Embodiment 3 FIG.
- the collision energy of the refrigerant containing the substance having the property of causing the disproportionation reaction is suppressed for the expansion device 16 that constitutes the main refrigerant circuit and through which a large amount of refrigerant passes.
- the apparatus configuration for doing so has been described.
- the described device configuration is not limited to the expansion device 16 on the main refrigerant circuit.
- the present invention can be applied to a throttle device installed on a bypass circuit included in the refrigeration cycle apparatus.
- Heat source unit (outdoor unit), 2a, 2b, 2c, 2d indoor unit, 3 heat medium converter, 4 extension pipe (refrigerant pipe), 4a first connection pipe, 4b second connection pipe, 5 pipe (heat medium pipe) ), 6 outdoor space, 7 indoor space, 8 outdoor space such as the back of the ceiling and indoor space, 9 buildings, etc., 10 compressor, 11 first refrigerant flow switching device (four-way valve), 12 Heat source side heat exchanger, 13a, 13b, 13c, 13d check valve, 15, 15a, 15b, 15c, 15d Load side heat exchanger, 16a, 16b, 16c, 16d throttle device, 17a, 17b switchgear, 18, 18a, 18b second refrigerant flow switching device, 19 accumulator, 21a, 21b pump, 22, 22a, 22b, 22c, 22d first heat medium flow switching device, 23, 23a, 23b 23c, 23d, second heat medium flow switching device, 25, 25a, 25b, 25c, 25d, heat medium flow control device
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Abstract
Description
本発明の実施の形態1について、図面に基づいて説明する。図1は、本発明の実施の形態1に係る冷凍サイクル装置の設置例を示す概略図である。図1に示す冷凍サイクル装置は、冷媒を循環させる冷媒回路を構成して冷媒による冷凍サイクルを利用することで、運転モードとして冷房モードあるいは暖房モードのいずれかを選択できるものである。ここで、本実施の形態の冷凍サイクル装置は、空調対象空間(室内空間7)の空気調和を行う空気調和装置を例として説明する。
室外機1には、圧縮機10と、四方弁等の第1冷媒流路切替装置11と、熱源側熱交換器12と、アキュムレータ19とが冷媒配管で直列に接続されて搭載されている。
室内機2には、それぞれ第二の熱交換器となる負荷側熱交換器15が搭載されている。この負荷側熱交換器15は、延長配管4によって室外機1に接続するようになっている。この負荷側熱交換器15は、図示省略の送風機から供給される空気と冷媒との間で熱交換を行い、室内空間7に供給するための暖房用空気あるいは冷房用空気を生成するものである。負荷側熱交換器15は、室内空間7を暖房する運転の場合には凝縮器として作用する。また、室内空間7を冷房する運転の場合には蒸発器として作用する。
図3は、冷凍サイクル装置100の吐出温度が低い場合の冷房運転モード時における冷媒の流れを示す冷媒回路図である。この図3では、全部の負荷側熱交換器15において冷熱負荷が発生している場合を例に冷房運転モードについて説明する。なお、図3では、太線で表された配管が冷媒の流れる配管を示しており、冷媒の流れ方向を実線矢印で示している。
図4は、冷凍サイクル装置100の暖房運転モード時における冷媒の流れを示す冷媒回路図である。この図4では、全部の負荷側熱交換器15において温熱負荷が発生している場合を例に暖房運転モードについて説明する。なお、図4では、太線で表された配管が冷媒の流れる配管を示しており、冷媒の流れ方向を実線矢印で示している。
冷凍サイクル装置100で使用する冷媒として、R32、R410A等のように、通常、冷媒として使用されている物質を使用する場合は、冷媒回路内での冷媒の安定性を改善するための工夫を施すことなく、このまま普通に使用すればよい。しかし、本実施の形態では、冷媒として、C2H1F3で表され分子構造中に二重結合を1つ有する1,1,2-トリフルオロエチレン(HFO-1123)等のような不均化反応を起こす性質の物質、または、不均化反応を起こす性質の物質と別の物質とを混合した混合冷媒を用いるものとする。混合冷媒を生成させるために、不均化反応を起こす性質の物質に混合させる物質としては、たとえば、C3H2F4で表されるテトラフルオロプロペン(CF3CF=CH2で表される2,3,3,3-テトラフルオロプロペンであるHFO-1234yf、CF3CH=CHFで表される1,3,3,3-テトラフルオロ-1-プロペンであるHFO-1234ze等)や化学式がCH2F2で表されるジフルオロメタン(HFC-32)等が用いられる。ただ、これらに限るものではなく、HC-290(プロパン)等を混合させてもよく、冷凍サイクル装置の冷媒として使用できる熱性能を有する物質であれば、どのようなものを用いてもよく、どのような混合比としてもよい。
図5は、本発明の実施の形態1に係る絞り装置16(16a~16d)の構成の概略図である。図5において、絞り装置16は、第1接続管41、第2接続管42、絞り部43、弁体44、及び、モーター45から構成されている。図5において、実線矢印は暖房運転時に冷媒が流れる向きを示しており、破線矢印は冷房運転時に冷媒が流れる向きを示している。
以上説明したように、本実施の形態に係る冷凍サイクル装置100は、幾つかの運転モードを具備している。これらの運転モードにおいては、室外機1と室内機2とを接続する延長配管4には冷媒が流れている。
本発明の実施の形態2について、図面に基づいて説明する。図7は、本発明の実施の形態に係る冷凍サイクル装置の回路図である。図7に示す冷凍サイクル装置100は、室外機1と熱媒体変換機3とが、熱媒体変換機3に備えられている負荷側熱交換器15a及び負荷側熱交換器15bを介して冷媒が内部を流れる延長配管4で接続されている。また、熱媒体変換機3と室内機2とも、負荷側熱交換器15a及び負荷側熱交換器15bを介して水やブライン等の熱媒体が内部を流れる配管5で接続されている。
全冷房運転モードの場合、圧縮機10から吐出された高温高圧のガス冷媒は、第1冷媒流路切替装置11を介して、熱源側熱交換器12へ流入し、周囲の空気に放熱して凝縮液化し、高圧液冷媒となり、逆止弁13aを通って室外機1から流出する。そして、延長配管4を通って熱媒体変換機3に流入する。熱媒体変換機3に流入した冷媒は、開閉装置17aを通り、絞り装置16a及び絞り装置16bで膨張して低温低圧の二相冷媒となる。二相冷媒は、蒸発器として作用する負荷側熱交換器15a及び負荷側熱交換器15bのそれぞれに流入し、熱媒体循環回路Bを循環する熱媒体から吸熱し、低温低圧のガス冷媒となる。ガス冷媒は、第2冷媒流路切替装置18a及び第2冷媒流路切替装置18bを介して熱媒体変換機3から流出する。そして、延長配管4を通って再び室外機1へ流入する。室外機1へ流入した冷媒は、逆止弁13dを通って、第1冷媒流路切替装置11及びアキュムレータ19を介して、圧縮機10へ再度吸入される。
全暖房運転モードの場合、圧縮機10から吐出された高温高圧のガス冷媒は、第1冷媒流路切替装置11を介して第1接続配管4a、逆止弁13bを通り、室外機1から流出する。そして、延長配管4を通って熱媒体変換機3に流入する。熱媒体変換機3に流入した冷媒は、第2冷媒流路切替装置18a及び第2冷媒流路切替装置18bを通って、負荷側熱交換器15a及び負荷側熱交換器15bのそれぞれに流入し、熱媒体循環回路Bを循環する熱媒体に放熱し、高圧の液冷媒となる。高圧の液冷媒は、絞り装置16a及び絞り装置16bで膨張して低温低圧の二相冷媒となり、開閉装置17bを通って、熱媒体変換機3から流出する。そして、延長配管4を通って再び室外機1へ流入する。室外機1へ流入した冷媒は、第2接続配管4b及び逆止弁13cを通り、蒸発器として作用する熱源側熱交換器12に流入し、周囲の空気から吸熱して、低温低圧のガス冷媒となる。ガス冷媒は、第1冷媒流路切替装置11及びアキュムレータ19を介して圧縮機10へ再度吸入される。なお、熱媒体循環回路Bにおける熱媒体の動作は、全冷房運転モードの場合と同じである。全暖房運転モードでは、負荷側熱交換器15a及び負荷側熱交換器15bにおいて、熱媒体が冷媒によって加熱され、利用側熱交換器26a及び利用側熱交換器26bで室内空気に放熱して、室内空間7の暖房を行う。
冷房主体運転モードの場合、圧縮機10から吐出された高温高圧のガス冷媒は、第1冷媒流路切替装置11を介して熱源側熱交換器12に流入し、周囲の空気に放熱して凝縮し、二相冷媒となり、逆止弁13aを通って、室外機1から流出する。そして、延長配管4を通って熱媒体変換機3に流入する。熱媒体変換機3に流入した冷媒は、第2冷媒流路切替装置18bを通って凝縮器として作用する負荷側熱交換器15bに流入し、熱媒体循環回路Bを循環する熱媒体に放熱して高圧の液冷媒となる。高圧の液冷媒は、絞り装置16bで膨張して低温低圧の二相冷媒となる。二相冷媒は、絞り装置16aを介して蒸発器として作用する負荷側熱交換器15aに流入し、熱媒体循環回路Bを循環する熱媒体から吸熱して低圧のガス冷媒となり、第2冷媒流路切替装置18aを介して熱媒体変換機3から流出する。そして、延長配管4を通って再び室外機1へ流入する。室外機1へ流入した冷媒は、逆止弁13dを通って、第1冷媒流路切替装置11及びアキュムレータ19を介して、圧縮機10へ再度吸入される。
暖房主体運転モードの場合、圧縮機10から吐出された高温高圧のガス冷媒は、第1冷媒流路切替装置11を介して、第1接続配管4a及び逆止弁13bを通って、室外機1から流出する。そして、延長配管4を通って熱媒体変換機3に流入する。熱媒体変換機3に流入した冷媒は、第2冷媒流路切替装置18bを通って凝縮器として作用する負荷側熱交換器15bに流入し、熱媒体循環回路Bを循環する熱媒体に放熱して高圧の液冷媒となる。高圧の液冷媒は、絞り装置16bで膨張して低温低圧の二相冷媒となる。二相冷媒は、絞り装置16aを介して蒸発器として作用する負荷側熱交換器15aに流入し、熱媒体循環回路Bを循環する熱媒体から吸熱し、第2冷媒流路切替装置18aを介して熱媒体変換機3から流出する。そして、延長配管4を通って再び室外機1へ流入する。室外機1へ流入した冷媒は、第2接続配管4b及び逆止弁13cを通って、蒸発器として作用する熱源側熱交換器12に流入し、周囲の空気から吸熱して、低温低圧のガス冷媒となる。ガス冷媒は、第1冷媒流路切替装置11及びアキュムレータ19を介して圧縮機10へ再度吸入される。なお、熱媒体循環回路Bにおける熱媒体の動作、第1熱媒体流路切替装置22a~22d、第2熱媒体流路切替装置23a~23d、熱媒体流量調整装置25a~25d、及び、利用側熱交換器26a~26d、の動作は冷房主体運転モードと同一である。
冷媒の種類及び絞り装置16(16a、16b)に関しては、実施の形態1で説明した構成と同様のものを適用して構成することができる。そして、本実施の形態の冷凍サイクル装置100においても同様の効果を奏する。
本実施の形態における各運転モードにおいては、室外機1と熱媒体変換機3とを接続する延長配管4には冷媒が流れ、熱媒体変換機3と室内機2を接続する配管5には水や不凍液等の熱媒体が流れている。
前述した実施の形態1及び実施の形態2では、主となる冷媒回路を構成し、多量の冷媒が通過する絞り装置16について、不均化反応を起こす性質の物質を含む冷媒の衝突エネルギーを抑制するための装置構成について説明した。しかしながら、説明した装置構成は、主冷媒回路上の絞り装置16だけでない。たとえば、冷凍サイクル装置が有するバイパス回路上に設置された絞り装置にも適用することができる。
Claims (14)
- 不均化反応を起こす性質の物質を含む冷媒を用いる冷媒回路を構成する絞り装置であって、
円筒形状の弁体と、
弁座を有し、前記弁体が弁軸方向に移動して、前記弁座に挿入することにより開口面積を変化させる絞り部とを有し、
前記絞り部に挿入する前記弁体の先端部分を、前記弁体の軸方向と直交する方向から0より大きい角度をつけて形成する構造とする絞り装置。 - 前記弁体の前記先端部分が、円錐状または多面体形状である請求項1に記載の絞り装置。
- 前記弁体が回転しながら移動し、前記開口面積を変化させる請求項1または請求項2に記載の絞り装置。
- 前記角度は18度以上である請求項1~請求項3のいずれか一項に記載の絞り装置。
- 前記角度をθとすると、cos(θ)が0.95以下を満たす角度である請求項1~請求項3のいずれか一項に記載の絞り装置。
- 前記冷媒として、1,1,2-トリフルオロエチレンまたは1,1,2-トリフルオロエチレンを含む混合冷媒を使用する請求項1~請求項5のいずれか一項に記載の絞り装置。
- 圧縮機、第一の熱交換器、請求項1~請求項6のいずれか一項に記載の絞り装置及び第二の熱交換器を冷媒配管で接続して冷媒回路を構成する冷凍サイクル装置。
- 前記絞り装置に、液状態の冷媒または二相状態の冷媒を流入させる請求項7に記載の冷凍サイクル装置。
- 前記第二の熱交換器が凝縮器として作用する場合と蒸発器として作用する場合とで、前記絞り装置を通過する冷媒の流れる方向が反転するように前記冷媒回路を構成する請求項7または請求項8に記載の冷凍サイクル装置。
- 前記絞り装置は、冷媒が流入する方向と流出する方向とがほぼ直交する構造であり、前記第二の熱交換器が凝縮器として作用する場合と蒸発器として作用する場合のいずれかにおいて、前記冷媒を前記弁体の軸方向から流入させる請求項9に記載の冷凍サイクル装置。
- 前記絞り装置は、冷媒が流入する方向と流出する方向とがほぼ直交する構造であり、前記第二の熱交換器を蒸発器として作用させる場合には前記弁体の軸方向に沿って前記冷媒を流入させ、前記第二の熱交換器を凝縮器として作用させる場合には前記弁体の軸方向と直交する方向に沿って前記冷媒を流入させる請求項9に記載の冷凍サイクル装置。
- 対象空間の空気調和を行う複数台の室内機と、
1台または複数台の熱源側ユニットとを備える請求項7~請求項11のいずれか一項に記載の冷凍サイクル装置。 - 前記絞り装置と前記第二の熱交換器とを室内機に収容し、前記第二の熱交換器を凝縮器として作用させる場合には前記冷媒を前記弁体の軸方向と直交する方向から流入させる請求項7~請求項12のいずれか一項に記載の冷凍サイクル装置。
- 前記絞り装置と前記第二の熱交換器とを、室外機と室内機とは別体で離れた位置に設置可能な中継器に収容する請求項7~請求項12のいずれか一項に記載の冷凍サイクル装置。
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