EP3098542B1 - Refrigeration cycle device - Google Patents
Refrigeration cycle device Download PDFInfo
- Publication number
- EP3098542B1 EP3098542B1 EP14877666.9A EP14877666A EP3098542B1 EP 3098542 B1 EP3098542 B1 EP 3098542B1 EP 14877666 A EP14877666 A EP 14877666A EP 3098542 B1 EP3098542 B1 EP 3098542B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- refrigerant
- expander
- expansion unit
- shell
- pipe
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- 238000005057 refrigeration Methods 0.000 title claims description 49
- 239000003507 refrigerant Substances 0.000 claims description 200
- 239000010721 machine oil Substances 0.000 claims description 89
- 239000003921 oil Substances 0.000 claims description 84
- 230000008878 coupling Effects 0.000 claims description 2
- 238000010168 coupling process Methods 0.000 claims description 2
- 238000005859 coupling reaction Methods 0.000 claims description 2
- 239000007788 liquid Substances 0.000 description 21
- 238000010586 diagram Methods 0.000 description 17
- 230000006835 compression Effects 0.000 description 14
- 238000007906 compression Methods 0.000 description 14
- 238000010438 heat treatment Methods 0.000 description 6
- 238000001816 cooling Methods 0.000 description 5
- 230000006837 decompression Effects 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 3
- 238000005461 lubrication Methods 0.000 description 3
- 230000002528 anti-freeze Effects 0.000 description 2
- 238000001514 detection method Methods 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 230000001419 dependent effect Effects 0.000 description 1
- 230000001052 transient effect Effects 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
- F25B11/00—Compression machines, plants or systems, using turbines, e.g. gas turbines
- F25B11/02—Compression machines, plants or systems, using turbines, e.g. gas turbines as expanders
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B13/00—Compression machines, plants or systems, with reversible cycle
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B31/00—Compressor arrangements
- F25B31/002—Lubrication
- F25B31/004—Lubrication oil recirculating 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
- F25B41/00—Fluid-circulation arrangements
- F25B41/30—Expansion means; Dispositions thereof
- F25B41/37—Capillary tubes
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B41/00—Fluid-circulation arrangements
- F25B41/30—Expansion means; Dispositions thereof
- F25B41/39—Dispositions with two or more expansion means arranged in series, i.e. multi-stage expansion, on a refrigerant line leading to the same evaporator
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2313/00—Compression machines, plants or systems with reversible cycle not otherwise provided for
- F25B2313/027—Compression machines, plants or systems with reversible cycle not otherwise provided for characterised by the reversing means
- F25B2313/02742—Compression machines, plants or systems with reversible cycle not otherwise provided for characterised by the reversing means using two four-way valves
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
- F25B2400/13—Economisers
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2600/00—Control issues
- F25B2600/25—Control of valves
- F25B2600/2519—On-off valves
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2700/00—Sensing or detecting of parameters; Sensors therefor
- F25B2700/03—Oil level
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2700/00—Sensing or detecting of parameters; Sensors therefor
- F25B2700/21—Temperatures
- F25B2700/2115—Temperatures of a compressor or the drive means therefor
-
- 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
- F25B2700/21155—Temperatures of a compressor or the drive means therefor of the oil
Definitions
- the present invention relates to a refrigeration cycle apparatus including an expander configured to recover expansion power of refrigerant as electric power.
- a conventional refrigeration cycle apparatus including a compressor and an expander arranged to a refrigerant circuit.
- a compressor casing and an expander casing communicate to each other through a communication pipe, and a discharge pipe and the expander casing communicate to each other through a branch outlet pipe to uniformly apply pressure to the inside of the two casings.
- An oil regulating valve is arranged to an oil flow pipe connecting an oil reservoir of the compressor to an oil reservoir of the expander.
- a conventional refrigeration cycle apparatus including a compressor and an expander arranged to a refrigerant circuit.
- refrigerant compressed by a compression mechanism is discharged to internal space of a compressor casing.
- refrigerating machine oil accumulated at the bottom of the compressor casing is supplied to the compression mechanism.
- the refrigerating machine oil accumulated at the bottom of the compressor casing is directly introduced to an expansion mechanism of the expander through an oil supply pipe (see, for example, Patent Literature 2).
- EP 2 123 996 A1 discloses a refrigerating cycle apparatus according to the preamble of claim 1.
- a refrigerant circuit in an air conditioner includes a compressor and an expander.
- refrigerant compressed by a compression mechanism is discharged into the internal space of a compressor casing.
- refrigeration oil which has accumulated in the bottom of the compressor casing is supplied to the compression mechanism.
- the refrigeration oil in the bottom of the compressor casing is directly introduced into an expansion mechanism of the expander through an oil supply pipe.
- a refrigerant circuit of an air conditioner includes a compressor and an expander.
- refrigerator oil is supplied from an oil reservoir to a compression mechanism.
- the expander the refrigerator oil is supplied from an oil reservoir to an expansion mechanism.
- the inner pressures of the compressor casing and the expander casing are the high pressure and the low pressure of the refrigeration cycle, respectively.
- An oil adjusting valve is provided in an oil pipe connecting the compressor casing and the expander casing. The oil amount adjusting valve is operated on the basis of an output signal of an oil level sensor. When the oil amount adjusting valve is opened, the refrigerator oil flows from the oil reservoir in the compressor casing toward the oil reservoir in the expander casing through the oil pipe.
- the compressor shell (compressor casing) and the expander shell (expander casing) are connected by a pipe. Part of gas refrigerant in the compressor shell is caused to flow into the expander shell so that part of the refrigerating machine oil in the compressor is caused to flow into the expander shell.
- Patent Literature 1 cannot be applied to a configuration in which the pressure in the compressor shell and the pressure in the expander shell are different from each other, for example, a configuration in which the pressure in the compressor shell is high and the pressure in the expander shell is low, or vice versa.
- the present invention has been made to solve the problems described above, and an object of the present invention is to provide a refrigeration cycle apparatus capable of storing refrigerating machine oil in an expander shell irrespective of the pressure in a compressor shell and suppressing depletion of the refrigerating machine oil in an expander.
- a refrigeration cycle apparatus including a refrigerant circuit, the refrigerant circuit comprising a compressor, a load-side heat exchanger, an expander, a heat source-side heat exchanger, a first four-way valve, and a second four-way valve, which are connected by pipes so that refrigerant is circulated through the refrigerant circuit
- the expander comprising: an expander shell defining an outer shell of the expander and storing refrigerant machine oil; an expansion unit arranged in the expander shell, the expansion unit being configured to expand the refrigerant flowing out from the load-side heat exchanger or the heat source-side heat exchanger that serves as a condenser to generate driving force, and configured for causing the expanded refrigerant to flow into the load-side heat exchanger or the heat source-side heat exchanger that serves as an evaporator, a power generator arranged in the expander shell, the power generator being configured to rotate by the driving force generated by the expansion unit; and
- the refrigerant flows from the inlet of the expander shell, the refrigerating machine oil contained in the refrigerant is stored in the expander shell, and the refrigerant flows from the outlet of the expander shell into the suction-side pipe of the compressor. Therefore, the refrigerating machine oil can be stored in the expander shell irrespective of the pressure in the compressor shell, and depletion of the refrigerating machine oil in the expander can be suppressed.
- Fig. 1 is a diagram for illustrating a configuration of a refrigeration cycle apparatus 100 according to Embodiment 1.
- Embodiment 1 is not an embodiment of the invention, but helpful to understand certain aspects thereof.
- the refrigeration cycle apparatus 100 includes a compressor 1, a load-side heat exchanger 2, an expander 3, a heat source-side heat exchanger 4, a first four-way valve 5, and a second four-way valve 6.
- the compressor 1, the load-side heat exchanger 2, the expander 3, and the heat source-side heat exchanger 4 are connected by pipes to form a refrigerant circuit through which refrigerant is circulated.
- the compressor 1 is, for example, a hermetically sealed compressor.
- An outer shell of the compressor 1 is defined by a compressor shell 15.
- An electric motor unit 17 and a compression unit 18 are accommodated in the compressor shell 15.
- refrigerating machine oil 50 is stored in the compressor shell 15.
- the refrigerating machine oil 50 is supplied to each of the electric motor unit 17 and the compression unit 18 to be used for lubrication.
- the compressor 1 sucks low-pressure refrigerant from a suction-side pipe 21 into the compressor shell 15.
- the compression unit 18 is driven by the electric motor unit 17.
- the low-pressure refrigerant sucked into the compressor shell 15 is compressed by the compression unit 18.
- the high-pressure refrigerant compressed by the compression unit 18 is discharged to a discharge-side pipe 10.
- the pressure in the compressor shell 15 is a low pressure.
- the compressor shell 15 is a so-called low-pressure shell.
- Embodiment 1 a case in which the pressure in the compressor shell 15 is a low pressure is described, but the present invention is not limited thereto.
- the compression unit 18 directly sucks the low-pressure refrigerant from the suction-side pipe 21.
- the high-pressure refrigerant compressed by the compression unit 18 is released into the compressor shell 15. Then, the refrigerant released into the compressor shell 15 is discharged to the discharge-side pipe 10.
- the configuration in which the pressure inside the compressor shell 15 is a high pressure may be employed.
- the compressor shell 15 may be a so-called high-pressure shell.
- An outer shell of the expander 3 is defined by an expander shell 34.
- An expansion unit 31 and a power generator 32 (motor) are accommodated in the expander shell 34.
- the expansion unit 31 and the power generator 32 are coupled to each other through a rotation shaft 33.
- the refrigerating machine oil 50 is stored in the expander shell 34.
- the refrigerating machine oil 50 is supplied to at least one of the expansion unit 31 and the power generator 32 to be used for lubrication.
- the expansion unit 31 includes an expansion unit inlet 43 configured for allowing the refrigerant to flow therein, and an expansion unit outlet 44 configured for allowing the refrigerant to flow out therefrom.
- the expansion unit inlet 43 is connected to an inlet pipe 35.
- the expansion unit outlet 44 is connected to an outlet pipe 36.
- the inlet pipe 35 is connected to a condenser (the load-side heat exchanger 2 or the heat source-side heat exchanger 4) through the second four-way valve 6.
- the outlet pipe 36 is connected to an evaporator (the load-side heat exchanger 2 or the heat source-side heat exchanger 4) through the second four-way valve 6.
- the expansion unit 31 expands the refrigerant flowing from the inlet pipe 35 into the expansion unit inlet 43, and causes the expanded refrigerant to flow from the expansion unit outlet 44 to the outlet pipe 36. Further, the expansion unit 31 rotationally drives the rotation shaft 33 by using expansion power generated when the refrigerant is expanded.
- the power generator 32 is coupled to the expansion unit 31 through the rotation shaft 33, and is rotated by the driving force generated by the expansion unit 31 to generate electric power. In this way, the expansion power of the expansion unit 31 is recovered as electric power.
- An inlet 41 configured for allowing the refrigerant to flow into the expander shell 34 and an outlet 42 configured for allowing the refrigerant to flow out from the expander shell 34 are formed in the expander shell 34 of the expander 3.
- the inlet 41 is connected to a low-pressure pipe 22.
- the low-pressure pipe 22 is connected to the evaporator (the load-side heat exchanger 2 or the heat source-side heat exchanger 4) through the first four-way valve 5.
- the low-temperature and low-pressure refrigerant discharged from the evaporator flows into the expander shell 34.
- the refrigerant flowing into the expander shell 34 is separated into gas refrigerant and the refrigerating machine oil 50. In this way, the refrigerating machine oil 50 contained in the refrigerant that is discharged from the evaporator is stored in the expander shell 34.
- the outlet 42 is connected to the suction-side pipe 21 of the compressor 1.
- the refrigerant flowing out from the expander shell 34 passes through the suction-side pipe 21 of the compressor 1, and is sucked into the compressor 1.
- the load-side heat exchanger 2 is, for example, a fin-and-tube heat exchanger.
- the load-side heat exchanger 2 exchanges heat between air as a load-side medium and the refrigerant.
- the load-side medium is not limited to air, and, for example, water or antifreeze may be used as a heat source.
- the heat source-side heat exchanger 4 is, for example, a fin-and-tube heat exchanger.
- the heat source-side heat exchanger 4 exchanges heat between outside air as a heat source-side medium and the refrigerant.
- the heat source-side medium is not limited to outside air (air), and, for example, water or antifreeze may be used as a heat source.
- the first four-way valve 5 and the second four-way valve 6 are used to switch the flow of the refrigerant circuit.
- the first four-way valve 5 connects the discharge-side pipe 10 of the compressor 1 to the heat source-side heat exchanger 4, and connects the load-side heat exchanger 2 to the low-pressure pipe 22.
- the second four-way valve 6 connects the load-side heat exchanger 2 to the inlet pipe 35, and connects the outlet pipe 36 to the heat source-side heat exchanger 4.
- the first four-way valve 5 connects the low-pressure pipe 22 to the load-side heat exchanger 2, and connects the heat source-side heat exchanger 4 to the discharge-side pipe 10 of the compressor 1.
- the second four-way valve 6 connects the heat source-side heat exchanger 4 to the inlet pipe 35, and connects the outlet pipe 36 to the load-side heat exchanger 2.
- a controller 200 includes, for example, a microcomputer, and has a CPU, a RAM, a ROM, and other components. A control program and the like are stored in the ROM. Detection values from various kinds of sensors configured to detect, for example, the pressure, the temperature, and other conditions of the refrigerant in the refrigerant circuit, or temperatures of the load-side medium and the heat source-side medium are input to the controller 200. The controller 200 controls each unit of the refrigeration cycle apparatus 100 based on the detection values from the sensors. Further, the controller 200 controls switching of the first four-way valve 5 and the second four-way valve 6.
- the first four-way valve 5 and the second four-way valve 6 are switched to states indicated by the dotted lines in Fig. 1 .
- the compressor 1 compresses the low-pressure refrigerant in the compressor shell 15, and discharges the high-temperature and high-pressure gas refrigerant to the discharge-side pipe 10.
- the gas refrigerant discharged from the compressor 1 contains the refrigerating machine oil 50 in the compressor shell 15.
- the high-temperature and high-pressure gas refrigerant discharged from the compressor 1 flows through the discharge-side pipe 10 of the compressor 1, passes through the first four-way valve 5, and is condensed by the load-side heat exchanger 2 that serves as a condenser (cooler in the case of supercritical refrigerant, e.g., CO 2 ) into liquid refrigerant.
- the liquid refrigerant flows out from the load-side heat exchanger 2. After that, the liquid refrigerant flowing out from the load-side heat exchanger 2 passes through the second four-way valve 6 and flows into the expansion unit inlet 43 in the expander 3 through the inlet pipe 35.
- the liquid refrigerant flowing into the expansion unit inlet 43 is expanded by the expansion unit 31 into low-pressure two-phase refrigerant, and flows out from the expansion unit outlet 44 into the outlet pipe 36.
- the power generator 32 coupled to the rotation shaft 33 is rotated by the driving force generated by the expansion unit 31.
- the low-pressure two-phase refrigerant flowing out from the expansion unit 31 passes through the second four-way valve 6, and flows into the heat source-side heat exchanger 4 that serves as an evaporator.
- the low-pressure two-phase refrigerant flowing into the heat source-side heat exchanger 4 exchanges heat with a heat source-side medium (outside air) and receives heat to be evaporated into low-pressure gas refrigerant.
- the low-pressure gas refrigerant flows out from the heat source-side heat exchanger 4.
- the low-pressure gas refrigerant flowing out from the heat source-side heat exchanger 4 passes through the first four-way valve 5 and further through the low-pressure pipe 22, and flows into the expander shell 34 from the inlet 41 of the expander 3.
- At least part of the refrigerating machine oil 50 contained in the gas refrigerant flowing into the expander shell 34 is separated in the expander shell 34, and the separated refrigerating machine oil 50 is stored in the expander shell 34.
- the gas refrigerant and the remaining refrigerating machine oil 50 contained in the gas refrigerant flow out from the outlet 42 toward the low pressure-side pipe 21 of the compressor 1.
- the gas refrigerant flowing out from the outlet 42 of the expander 3 is sucked into the compressor 1 through the low pressure-side pipe 21 of the compressor 1.
- the entire low-pressure gas refrigerant flowing out from the evaporator flows into the expander shell 34, and the refrigerating machine oil 50 contained in the gas refrigerant is separated in the expander shell 34 and is stored in the expander shell 34.
- the refrigerating machine oil 50 stored in the expander shell 34 is supplied to each of the electric motor unit 17 and the compression unit 18 via the rotation shaft 33 to be used for lubrication.
- the first four-way valve 5 and the second four-way valve 6 are switched to states indicated by the solid lines in Fig. 1 .
- the gas refrigerant discharged from the compressor 1 flows through the discharge-side pipe 10 of the compressor 1 and further through the first four-way valve 5, and is condensed by the heat source-side heat exchanger 4 that serves as a condenser (cooler in the case of supercritical refrigerant, e.g., CO 2 ) into liquid refrigerant.
- the liquid refrigerant flows out from the heat source-side heat exchanger 4. After that, the liquid refrigerant flowing out from the heat source-side heat exchanger 4 passes through the second four-way valve 6 and the inlet pipe 35, is expanded into low-pressure two-phase refrigerant by the expansion unit 31, and flows out therefrom.
- the low-pressure two-phase refrigerant flowing out from the expansion unit 31 passes through the second four-way valve 6, and flows into the load-side heat exchanger 2 that serves as an evaporator.
- the low-pressure two-phase refrigerant flowing into the load-side heat exchanger 2 exchanges heat with a load-side medium (air) and receives heat to be evaporated into low-pressure gas refrigerant.
- the low-pressure gas refrigerant flows out from the load-side heat exchanger 2.
- the low-pressure gas refrigerant flowing out from the load-side heat exchanger 2 passes through the first four-way valve 5 and further through the low-pressure pipe 22, and flows into the expander shell 34 from the inlet 41 of the expander 3.
- the gas refrigerant flowing out from the outlet 42 of the expander 3 is sucked into the compressor 1 through the low pressure-side pipe 21 of the compressor 1.
- an oil quantity of the refrigerating machine oil 50 contained in the gas refrigerant flowing out from the expander shell 34 is approximately the same as an oil quantity of the refrigerating machine oil 50 flowing into the expander shell 34.
- the refrigerating machine oil 50 stored in the expander shell 34 is consumed by being supplied to the expansion unit 31 and the power generator 32. For example, part of the refrigerating machine oil 50 supplied to the expansion unit 31 is mixed into the refrigerant in the expansion unit 31, and flows into the compressor 1 through the refrigerant passage. Therefore, an oil quantity of the refrigerating machine oil 50 stored in the expander shell 34 may be reduced.
- the expander 3 includes the expander shell 34 that defines the outer shell, the expansion unit 31 arranged in the expander shell 34 and configured to expand the refrigerant flowing out from the condenser to generate the driving force, and configured for causing the expanded refrigerant to flow into the evaporator, and the power generator 32 arranged in the expander shell 34 and configured to rotate by the driving force generated by the expansion unit 31.
- the inlet 41 configured for allowing the refrigerant to flow into the expander shell 34 and the outlet 42 configured for allowing the refrigerant flowing into the expander shell 34 from the inlet 41 to flow into the suction-side pipe 21 of the compressor 1 are formed in the expander shell 34.
- the refrigerating machine oil 50 contained in the refrigerant flowing into the expander shell 34 is stored in the expander shell 34, and the refrigerating machine oil 50 is supplied to at least one of the expansion unit and the power generator.
- the refrigerating machine oil 50 stored in the expander shell 34 can be supplied to the expansion unit 31 and the power generator 32, and depletion of the refrigerating machine oil 50 in the expander shell 34 can be suppressed.
- the low-temperature and low-pressure refrigerant flowing out from the evaporator flows into the expander shell 34, and thus, the power generator 32 can be cooled. Therefore, reduction in efficiency of the power generator 32 can be suppressed.
- temperature rise in the expander shell 34 can be suppressed, and thus, heat is less likely to be exchanged between the refrigerant in the expansion unit 31 and the gas refrigerant in the expander shell 34 so that increase in enthalpy of the refrigerant flowing from the expansion unit 31 into the evaporator can be suppressed to alleviate reduction in refrigeration capacity.
- an oil supply pipe as in the technique disclosed in Patent Literature 2 is not arranged, and thus, the refrigerant that dissolves in the refrigerating machine oil 50 does not form bubbles, thereby being capable of suppressing unsatisfactory lubricity. Further, even under a transitional state, e.g., at a startup of the compressor 1, the expansion unit 31 and the power generator 32 can be lubricated with the refrigerating machine oil 50 stored in the expander shell 34.
- the refrigerant flowing out from the expander shell 34 is caused to flow into the suction-side pipe 21 of the compressor 1, and thus, the refrigerating machine oil 50 can be stored in the expander shell 34 irrespective of the internal pressure of the compressor shell 15 (high-pressure shell or low-pressure shell).
- Embodiment 2 is not an embodiment of the invention, but helpful to understand certain aspects thereof. In Embodiment 2, differences from Embodiment 1 are mainly described. Like reference numerals are used to designate components that are the same as those in Embodiment 1, and description thereof is omitted.
- Figs. 2 are diagrams for illustrating configurations of an expander 3 of a refrigeration cycle apparatus 100 according to Embodiment 2.
- the outlet 42 of the expander shell 34 is formed by an opening port formed in a side surface of the expander shell 34.
- the outlet 42 is formed at a position (Lm) higher than an oil level (Ln) of a preset necessary quantity of the refrigerating machine oil 50 to be stored in the expander shell 34.
- the preset necessary quantity is a minimum necessary quantity of oil defined by, for example, specifications of the expander 3.
- a pipe that communicates the inside and the outside of the expander shell 34 may be arranged and the outlet 42 may be formed by an opening port at an end portion of the pipe. Also in this case, the outlet 42 is formed at a position (Lm) higher than the oil level (Ln) of the preset necessary quantity of the refrigerating machine oil 50 to be stored in the expander shell 34.
- the preset necessary quantity of the refrigerating machine oil 50 can be stored in the expander shell 34. Therefore, the minimum oil quantity necessary for the expander 3 can be secured.
- Embodiment 3 is not an embodiment of the invention, but helpful to understand certain aspects thereof. In Embodiment 3, differences from Embodiment 1 are mainly described. Like reference numerals are used to designate components that are the same as those in Embodiment 1, and description thereof is omitted.
- Fig. 3 is a diagram for illustrating a configuration of a refrigeration cycle apparatus 100 according to Embodiment 3.
- the refrigeration cycle apparatus 100 further includes, in addition to the configuration of Embodiment 1, an oil return pipe 52 configured for causing the refrigerating machine oil 50 in the expander shell 34 to flow into the suction-side pipe 21 of the compressor 1.
- the oil return pipe 52 connects an oil outlet 45 formed in a bottom portion of the expander shell 34 and the suction-side pipe 21 of the compressor 1. Further, an on-off valve 54 configured to open and close the passage is formed in the oil return pipe 52.
- the controller 200 controls opening and closing of the on-off valve 54.
- the controller 200 opens the on-off valve 54 and returns part of the refrigerating machine oil 50 in the expander shell 34 into the compressor shell 15.
- the oil quantity in the compressor shell 15 may be determined, for example, by providing an oil level indicator, or by measuring the shell temperature with a temperature sensor, e.g., a thermistor.
- a flow control valve with a variable opening degree may be arranged. Further, through omission of the on-off valve 54 and adjustment of the pipe diameter and the length of the oil return pipe 52, a small quantity of the refrigerating machine oil 50 may be returned all the time.
- the level of the outlet 42 of the expander shell 34 may be set depending on the minimum necessary quantity of oil in the compressor shell 15.
- the refrigerating machine oil 50 in the expander shell 34 can be returned to the compressor 1, and thus, when the quantity of the refrigerating machine oil 50 contained in the refrigerant that is discharged from the compressor 1 (quantity of the oil that is taken out) is large at, for example, a startup, depletion of the refrigerating machine oil 50 in the compressor shell 15 can be suppressed.
- the refrigerating machine oil 50 in the expander shell 34 is excessively stored, the refrigerating machine oil 50 can be returned into the compressor shell 15.
- the oil can be returned to the compressor 1 irrespective of the level of the outlet 42 of the expander shell 34.
- Embodiment 4 is not an embodiment of the invention, but helpful to understand certain aspects thereof.
- differences from Embodiment 1 are mainly described.
- Like reference numerals are used to designate components that are the same as those in Embodiment 1, and description thereof is omitted.
- Fig. 4 is a diagram for illustrating a configuration of a refrigeration cycle apparatus 100 according to Embodiment 4.
- the refrigeration cycle apparatus 100 further includes, in addition to the configuration of Embodiment 1 described above, a first bypass pipe 23 configured to branch off from the low-pressure pipe 22 to join the suction-side pipe 21 of the compressor 1.
- the first bypass pipe 23 branches off from the passage from the evaporator (the load-side heat exchanger 2 or the heat source-side heat exchanger 4) to the inlet 41 of the expander shell 34 to join the passage from the outlet 42 of the expander shell 34 to the compressor 1.
- the refrigerant liquefied by the condenser flows into the expansion unit 31 in the expander 3, and thus, the temperature of the refrigerant flowing through the expansion unit 31 is lower than the temperature of the refrigerant flowing into the expander shell 34. Therefore, the refrigerant in the expansion unit 31 and the refrigerant flowing into the expander shell 34 exchange heat therebetween.
- Embodiment 4 part of the refrigerant flowing out from the evaporator flows from the pipe 10 into the expander shell 34, and another part thereof flows from the first bypass pipe 23 into the suction-side pipe 21 of the compressor 1.
- the flow rate of the refrigerant flowing into the expander shell 34 is reduced compared with a case in which the entire refrigerant flowing out from the evaporator flows into the expander shell 34. Accordingly, the heat exchange quantity between the refrigerant in the expansion unit 31 and the refrigerant flowing into the expander shell 34 can be reduced.
- the size of the expander 3 is smaller than the size of the compressor 1, and thus, the quantity of the refrigerating machine oil 50 contained in the refrigerant flowing out from the expander shell 34 (quantity of oil that is taken out) is smaller than the quantity of the refrigerating machine oil 50 contained in the refrigerant that is discharged from the compressor 1. That is, it is sufficient that a quantity of the oil that is smaller than the quantity of the oil that is taken out of the compressor 1 is supplied to the expander 3.
- the length and the diameter of the low-pressure pipe 22 or the first bypass pipe 23 are selected so that the flow rate of the refrigerant that passes through the low-pressure pipe 22 may be lower than the flow rate of the refrigerant that passes through the first bypass pipe 23.
- the heat exchange quantity in the expansion unit 31 can be suppressed, and depletion of the refrigerating machine oil 50 in the expander shell 34 can be suppressed.
- a flow control valve or other components may be arranged to the low-pressure pipe 22 or the first bypass pipe 23 to control the flow rate of the refrigerant flowing into the expander shell 34.
- the controller 200 may increase the flow rate of the refrigerant flowing into the expander shell 34 to increase the oil quantity of the stored refrigerating machine oil 50 when the oil quantity of the refrigerating machine oil 50 in the expander shell 34 is smaller than the preset oil quantity.
- the oil quantity in the expander shell 34 may be determined, for example, by providing an oil level indicator, or by measuring the shell temperature with a temperature sensor, e.g., a thermistor.
- the configuration of Embodiment 1 may further additionally include the oil return pipe 52 configured for causing the refrigerating machine oil 50 in the expander shell 34 to flow into the suction-side pipe 21 of the compressor 1, and the first bypass pipe 23 configured to branch off from the passage from the evaporator to the inlet 41 of the expander shell 34 to join the passage from the outlet 42 of the expander shell 34 to the compressor 1.
- the oil return pipe 52 configured for causing the refrigerating machine oil 50 in the expander shell 34 to flow into the suction-side pipe 21 of the compressor 1
- the first bypass pipe 23 configured to branch off from the passage from the evaporator to the inlet 41 of the expander shell 34 to join the passage from the outlet 42 of the expander shell 34 to the compressor 1.
- Embodiment 5 of the present invention differences from Embodiment 1 are mainly described. Like reference numerals are used to designate components that are the same as those in Embodiment 1, and description thereof is omitted.
- Fig. 6 is a diagram for illustrating a configuration of a refrigeration cycle apparatus 100 according to Embodiment 5 of the present invention.
- the refrigeration cycle apparatus 100 includes, in addition to the configuration of Embodiment 1, a second bypass pipe 61 configured to branch off from the passage (inlet pipe 35) from the condenser to the expansion unit 31 for causing the refrigerant to flow into the inlet 41 of the expander shell 34.
- a decompression unit e.g., a capillary tube 63 configured to decompress the refrigerant flowing through the second bypass pipe 61
- a heat exchanger 60 configured to exchange heat between the refrigerant branched off to the second bypass pipe 61 to be decompressed and the refrigerant flowing through the inlet pipe 35 (refrigerant flowing from the condenser into the expansion unit) are arranged to the second bypass pipe 61.
- the outlet 42 of the expander shell 34 in Embodiment 5 joins the suction-side pipe 21 of the compressor 1 through an outlet pipe 20.
- a decompression unit e.g., a capillary tube 24, which is configured to decompress the refrigerant, is formed in the outlet pipe 20.
- the suction-side pipe 21 of the compressor 1 is connected to the evaporator (the load-side heat exchanger 2 or the heat source-side heat exchanger 4) through the first four-way valve 5.
- Embodiment 5 With regard to operation of Embodiment 5, differences from Embodiment 1 are mainly described.
- the refrigerant flowing out from the condenser passes through the second four-way valve 6, and flows into the inlet pipe 35. Part of the refrigerant flowing through the inlet pipe 35 flows into the second bypass pipe 61.
- the refrigerant flowing into the second bypass pipe 61 is decompressed by the capillary tube 63 and the temperature thereof falls.
- the heat exchanger 60 exchanges heat between the refrigerant that is decompressed by the capillary tube 63 to have the lowered temperature and the high-pressure refrigerant flowing from the inlet pipe 35 into the expansion unit 31 so that the refrigerant decompressed by the capillary tube 63 turns into gas refrigerant.
- the gas refrigerant flows into the inlet 41 of the expander shell 34. Then, after the refrigerating machine oil 50 contained in the refrigerant is separated, the refrigerant flows from the outlet 42 to the outlet pipe 20. Then, after the refrigerant is decompressed by the capillary tube 24, the refrigerant joins the suction-side pipe 21 of the compressor 1.
- a decompression device with a variable flow rate may be arranged. Arrangement of such a decompression device with a variable flow rate enables keeping appropriate temperature of the refrigerant flowing into the expander shell depending on the operation state, and the power generator 32 can be effectively cooled. Further, occurrence of transient liquid return (liquid backflow) into the expander shell 34 can be prevented to suppress lowering of oil concentration in the expander shell 34.
- the refrigerant flowing into the expander shell 34 can be brought into a gas state, and thus, even when, for example, liquid backflow in which the refrigerant in a liquid state flows out from the evaporator occurs, the refrigerant in the liquid state can be prevented from flowing into the expander shell 34. Therefore, the refrigerant in the liquid state can be prevented from being mixed into the refrigerating machine oil 50, and the oil concentration can be prevented from being lowered.
- the pressure and the temperature in the expander shell 34 can be set at desired values. Therefore, by lowering the temperature in the expander shell 34, temperature rise of the power generator 32 can be suppressed, and reduction in efficiency of the power generator 32 can be suppressed.
- Embodiment 5 may further additionally include the oil return pipe 52 configured for causing the refrigerating machine oil 50 in the expander shell 34 to flow into the suction-side pipe 21 of the compressor 1.
- the oil return pipe 52 configured for causing the refrigerating machine oil 50 in the expander shell 34 to flow into the suction-side pipe 21 of the compressor 1.
- the pressure in the expander shell 34 is higher than that of the refrigerant passing through the expansion unit 31, there can be attained oil supply using a pressure difference as a method of supplying the refrigerating machine oil 50 stored in the expander shell 34 to the expansion unit 31 and the power generator 32, and the reliability of the expander 3 is improved. Further, the pressure on the suction side of the compressor 1 is lower than the pressure in the expander shell 34, and thus, the refrigerating machine oil 50 in the expander shell 34 can be returned to the compressor 1 without fail by using the pressure difference.
- a third bypass pipe 65 configured to branch off from the passage from the evaporator to the compressor 1 (low-pressure pipe 22) to join the second bypass pipe 61 at a downstream side of the heat exchanger 60.
- Embodiment 6 is not an embodiment of the invention, but helpful to understand certain aspects thereof. With regard to Embodiment 6, differences from Embodiment 5 are mainly described. Like reference numerals are used to designate components that are the same as those in Embodiment 5, and description thereof is omitted.
- Fig. 9 is a diagram for illustrating a configuration of a refrigeration cycle apparatus 100 according to Embodiment 6.
- the refrigeration cycle apparatus 100 includes, in addition to the configuration of Embodiment 5, an oil separator 7 configured to separate the refrigerating machine oil 50 contained in the refrigerant that is discharged from the compressor 1, and a fourth bypass pipe 13 configured to join the refrigerating machine oil 50 separated by the oil separator 7 to the refrigerant decompressed by the second bypass pipe 61.
- the heat exchanger 60 is unnecessary.
- the discharge-side pipe 10 of the compressor 1 is connected to the oil separator 7. Further, the oil separator 7 and the first four-way valve 5 are connected through the gas pipe 11.
- the configuration in which the oil return pipe 52 configured to cause the refrigerating machine oil 50 in the expander shell 34 to flow into the suction-side pipe 21 of the compressor 1 is arranged may be employed.
- the high-temperature and high-pressure refrigerant discharged from the compressor 1 flows into the oil separator 7 through the pipe 10.
- the oil separator 7 at least part of the refrigerating machine oil 50 contained in the refrigerant is separated.
- the refrigerating machine oil 50 separated by the oil separator 7 joins the low-pressure liquid refrigerant flowing through the second bypass pipe 61 through the fourth bypass pipe 13.
- the low-pressure liquid refrigerant flowing through the second bypass pipe 61 joins the high-temperature refrigerating machine oil 50 to be heated and turned into refrigerant in a gas state.
- the gasified refrigerant and the refrigerating machine oil 50 flow from the inlet 41 into the expander shell 34.
- the gas refrigerant separated by the oil separator 7 passes through the gas pipe 11, and flows into the condenser (the load-side heat exchanger 2 or the heat source-side heat exchanger 4) through the first four-way valve 5.
- the refrigerant flowing into the expander shell 34 can be brought into a gas state, and thus, even when, for example, liquid backflow in which the refrigerant in a liquid state flows out from the evaporator occurs, the refrigerant in the liquid state can be prevented from flowing into the expander shell 34. Therefore, the refrigerant in the liquid state can be prevented from being mixed into the refrigerating machine oil 50, and the oil concentration can be prevented from being lowered.
- the pressure and the temperature in the expander shell 34 can be set at desired values. Therefore, by lowering the temperature in the expander shell 34, temperature rise of the power generator 32 can be suppressed, and reduction in efficiency of the power generator 32 can be suppressed.
- the low-temperature refrigerant flowing through the second bypass pipe 61 can cool the high-temperature refrigerating machine oil 50, and thus, temperature rise of the power generator 32 can be suppressed.
- the refrigerating machine oil 50 can be supplied from the oil separator 7, and thus, a sufficient quantity of the oil can be supplied into the expander shell 34.
- Embodiment 7 is not an embodiment of the invention, but helpful to understand certain aspects thereof. In Embodiment 7, differences from Embodiment 1 are mainly described. Like reference numerals are used to designate components that are the same as those in Embodiment 1, and description thereof is omitted.
- Fig. 10 is a diagram for illustrating a configuration of a refrigeration cycle apparatus 100 according to Embodiment 7.
- the refrigeration cycle apparatus 100 further includes, in addition to the configuration of Embodiment 1, a fifth bypass pipe 37 configured to branch off from the inlet pipe 35 to join the outlet pipe 36 and a second expansion valve 38 arranged to the fifth bypass pipe 37 and configured to expand the refrigerant.
- the fifth bypass pipe 37 branches off from the passage (inlet pipe 35) from the condenser to the expansion unit 31 to join the passage (outlet pipe 36) from the expansion unit 31 to the evaporator.
- the second expansion valve 38 is, for example, an electronically controlled expansion valve with a variable opening degree.
- the controller 200 controls the opening degree of the second expansion valve 38 in accordance with a preset condition.
- an on-off valve configured to open and close the passage of the fifth bypass pipe 37 is provided and the opening degree of the second expansion valve 38 is fixed.
- the controller 200 controls the on-off valve.
- the refrigerant decompressed by the second expansion valve 38 joins the outlet pipe 36, passes through the second four-way valve 6, and flows into the evaporator.
- the controller 200 opens the second expansion valve 38, causes the refrigerant to flow through the fifth bypass pipe 37, and stops the drive of the expansion unit 31.
- the preset condition in this case is, for example, at least one of the following conditions (1) to (3).
- the drive of the expansion unit 31 can be prevented until the discharge pressure of the compressor 1 is sufficiently increased, and liquid backflow into the compressor 1 and the like can be suppressed.
- the expansion unit 31 can be driven at the rotation speed falling within a desired range.
- Embodiment 7 can also be applied to any of Embodiments 1 to 6.
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Description
- The present invention relates to a refrigeration cycle apparatus including an expander configured to recover expansion power of refrigerant as electric power.
- There is a conventional refrigeration cycle apparatus including a compressor and an expander arranged to a refrigerant circuit. A compressor casing and an expander casing communicate to each other through a communication pipe, and a discharge pipe and the expander casing communicate to each other through a branch outlet pipe to uniformly apply pressure to the inside of the two casings. An oil regulating valve is arranged to an oil flow pipe connecting an oil reservoir of the compressor to an oil reservoir of the expander. In the proposed related art, when the oil regulating valve is opened, the oil reservoir in the compressor casing and the oil reservoir in the expander casing communicate to each other, and refrigerating machine oil flows through the oil flow pipe (see, for example, Patent Literature 1).
- Further, there is a conventional refrigeration cycle apparatus including a compressor and an expander arranged to a refrigerant circuit. In the compressor, refrigerant compressed by a compression mechanism is discharged to internal space of a compressor casing. In the compressor, refrigerating machine oil accumulated at the bottom of the compressor casing is supplied to the compression mechanism. In the proposed related art, the refrigerating machine oil accumulated at the bottom of the compressor casing is directly introduced to an expansion mechanism of the expander through an oil supply pipe (see, for example, Patent Literature 2).
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EP 2 123 996 A1claim 1. According to this document, a refrigerant circuit in an air conditioner includes a compressor and an expander. In the compressor, refrigerant compressed by a compression mechanism is discharged into the internal space of a compressor casing. In the compressor, refrigeration oil which has accumulated in the bottom of the compressor casing is supplied to the compression mechanism. The refrigeration oil in the bottom of the compressor casing is directly introduced into an expansion mechanism of the expander through an oil supply pipe. -
EP 2 009 368 A1claim 1. According to this document, a refrigerant circuit of an air conditioner includes a compressor and an expander. In the compressor, refrigerator oil is supplied from an oil reservoir to a compression mechanism. In the expander, the refrigerator oil is supplied from an oil reservoir to an expansion mechanism. The inner pressures of the compressor casing and the expander casing are the high pressure and the low pressure of the refrigeration cycle, respectively. An oil adjusting valve is provided in an oil pipe connecting the compressor casing and the expander casing. The oil amount adjusting valve is operated on the basis of an output signal of an oil level sensor. When the oil amount adjusting valve is opened, the refrigerator oil flows from the oil reservoir in the compressor casing toward the oil reservoir in the expander casing through the oil pipe. -
- Patent Literature 1: Japanese Unexamined Patent Application Publication No.
2007-285674 - Patent Literature 2: Japanese Unexamined Patent Application Publication No.
2008-224053 - In the technique disclosed in
Patent Literature 1, the compressor shell (compressor casing) and the expander shell (expander casing) are connected by a pipe. Part of gas refrigerant in the compressor shell is caused to flow into the expander shell so that part of the refrigerating machine oil in the compressor is caused to flow into the expander shell. - Therefore, the pressure in the compressor shell and the pressure in the expander shell are equal to each other. Thus, there is a problem in that the technique disclosed in
Patent Literature 1 cannot be applied to a configuration in which the pressure in the compressor shell and the pressure in the expander shell are different from each other, for example, a configuration in which the pressure in the compressor shell is high and the pressure in the expander shell is low, or vice versa. - Further, high-pressure and high-temperature refrigerant flows into the expander shell, and thus, there is a problem in that a power generator (motor) in the expander shell is difficult to cool.
- In the technique disclosed in
Patent Literature 2, the refrigerating machine oil accumulated at the bottom of the compressor shell (compressor casing) is directly introduced into an expansion unit (expansion mechanism) in the expander through the oil supply pipe. - Therefore, there is a problem in that, when the refrigerating machine oil in the compressor shell is depleted, the oil cannot be supplied into the expander.
- Further, when the refrigerating machine oil flows through the oil supply pipe, there is a problem in that the refrigerant that dissolves in the refrigerating machine oil is decompressed to form bubbles, and refrigerant gas is mixed into the refrigerating machine oil so that the lubricity thereof is lowered.
- The present invention has been made to solve the problems described above, and an object of the present invention is to provide a refrigeration cycle apparatus capable of storing refrigerating machine oil in an expander shell irrespective of the pressure in a compressor shell and suppressing depletion of the refrigerating machine oil in an expander.
- The object of the present invention is solved by
claim 1. Advantageous embodiments are described by the dependent claims. - According to an aspect of the present invention, there is provided a refrigeration cycle apparatus including a refrigerant circuit, the refrigerant circuit comprising a compressor, a load-side heat exchanger, an expander, a heat source-side heat exchanger, a first four-way valve, and a second four-way valve, which are connected by pipes so that refrigerant is circulated through the refrigerant circuit, the expander comprising: an expander shell defining an outer shell of the expander and storing refrigerant machine oil; an expansion unit arranged in the expander shell, the expansion unit being configured to expand the refrigerant flowing out from the load-side heat exchanger or the heat source-side heat exchanger that serves as a condenser to generate driving force, and configured for causing the expanded refrigerant to flow into the load-side heat exchanger or the heat source-side heat exchanger that serves as an evaporator, a power generator arranged in the expander shell, the power generator being configured to rotate by the driving force generated by the expansion unit; and a rotation shaft coupling the power generator to the expansion unit, the expander shell including: an inlet configured for allowing the refrigerant to flow into the expander shell; and an outlet configured for allowing the refrigerant that flowed into the expander shell from the inlet to flow out from the expander shell and to flow into a suction-side pipe of the compressor, the expander shell being configured such that the refrigerating machine oil contained in the refrigerant is stored therein, and is supplied to at least one of the expansion unit and the power generator, the expansion unit including: an expansion unit inlet configured for allowing the refrigerant to flow into the expansion unit from an inlet pipe; and an expansion unit outlet configured for allowing the refrigerant flow out from the expansion unit and to flow into an outlet pipe, the inlet pipe being connected to the condenser through the second four-way valve, the outlet pipe being connected to the evaporator through the second four-way valve, wherein the refrigeration cycle apparatus further comprises; a second bypass pipe configured to branch off from a passage from the condenser to the expansion unit, to decompress the refrigerant and to cause the refrigerant to flow into the inlet of the expander shell; and a heat exchanger configured to exchange heat between the refrigerant branched off and decompressed at the second bypass pipe and the refrigerant flowing from the condenser into the expansion unit.
- According to the aspect of the present invention, the refrigerant flows from the inlet of the expander shell, the refrigerating machine oil contained in the refrigerant is stored in the expander shell, and the refrigerant flows from the outlet of the expander shell into the suction-side pipe of the compressor. Therefore, the refrigerating machine oil can be stored in the expander shell irrespective of the pressure in the compressor shell, and depletion of the refrigerating machine oil in the expander can be suppressed.
-
- [
Fig. 1] Fig. 1 is a diagram for illustrating a configuration of arefrigeration cycle apparatus 100 according toEmbodiment 1,Embodiment 1 being not an embodiment of the claimed invention. - [
Figs. 2] Figs. 2 are diagrams for illustrating configurations of anexpander 3 of arefrigeration cycle apparatus 100 according toEmbodiment 2,Embodiment 2 being not an embodiment of the claimed invention. - [
Fig. 3] Fig. 3 is a diagram for illustrating a configuration of arefrigeration cycle apparatus 100 according toEmbodiment 3,Embodiment 3 being not an embodiment of the claimed invention. - [
Fig. 4] Fig. 4 is a diagram for illustrating a configuration of arefrigeration cycle apparatus 100 according toEmbodiment 4,Embodiment 4 being not an embodiment of the claimed invention. - [
Fig. 5] Fig. 5 is a diagram for illustrating another configuration of arefrigeration cycle apparatus 100 according toEmbodiment 4,Embodiment 4 being not an embodiment of the claimed invention. - [
Fig. 6] Fig. 6 is a diagram for illustrating a configuration of arefrigeration cycle apparatus 100 according toEmbodiment 5 of the present invention. - [
Fig. 7] Fig. 7 is a diagram for illustrating another configuration of arefrigeration cycle apparatus 100 according toEmbodiment 5 of the present invention. - [
Fig. 8] Fig. 8 is a diagram for illustrating another configuration of arefrigeration cycle apparatus 100 according toEmbodiment 5 of the present invention. - [
Fig. 9] Fig. 9 is a diagram for illustrating a configuration of arefrigeration cycle apparatus 100 according toEmbodiment 6,Embodiment 6 being not an embodiment of the claimed invention. - [
Fig. 10] Fig. 10 is a diagram for illustrating a configuration of arefrigeration cycle apparatus 100 according toEmbodiment 7,Embodiment 7 being not an embodiment of the claimed invention. -
Fig. 1 is a diagram for illustrating a configuration of arefrigeration cycle apparatus 100 according toEmbodiment 1.Embodiment 1 is not an embodiment of the invention, but helpful to understand certain aspects thereof. - As illustrated in
Fig. 1 , therefrigeration cycle apparatus 100 includes acompressor 1, a load-side heat exchanger 2, anexpander 3, a heat source-side heat exchanger 4, a first four-way valve 5, and a second four-way valve 6. Thecompressor 1, the load-side heat exchanger 2, theexpander 3, and the heat source-side heat exchanger 4 are connected by pipes to form a refrigerant circuit through which refrigerant is circulated. - The
compressor 1 is, for example, a hermetically sealed compressor. An outer shell of thecompressor 1 is defined by acompressor shell 15. Anelectric motor unit 17 and acompression unit 18 are accommodated in thecompressor shell 15. - Further, refrigerating
machine oil 50 is stored in thecompressor shell 15. The refrigeratingmachine oil 50 is supplied to each of theelectric motor unit 17 and thecompression unit 18 to be used for lubrication. - The
compressor 1 sucks low-pressure refrigerant from a suction-side pipe 21 into thecompressor shell 15. Thecompression unit 18 is driven by theelectric motor unit 17. The low-pressure refrigerant sucked into thecompressor shell 15 is compressed by thecompression unit 18. The high-pressure refrigerant compressed by thecompression unit 18 is discharged to a discharge-side pipe 10. - In this way, the pressure in the
compressor shell 15 is a low pressure. In other words, thecompressor shell 15 is a so-called low-pressure shell. - In
Embodiment 1, a case in which the pressure in thecompressor shell 15 is a low pressure is described, but the present invention is not limited thereto. - For example, the following configuration may be employed. The
compression unit 18 directly sucks the low-pressure refrigerant from the suction-side pipe 21. The high-pressure refrigerant compressed by thecompression unit 18 is released into thecompressor shell 15. Then, the refrigerant released into thecompressor shell 15 is discharged to the discharge-side pipe 10. - In this way, the configuration in which the pressure inside the
compressor shell 15 is a high pressure may be employed. In other words, thecompressor shell 15 may be a so-called high-pressure shell. - An outer shell of the
expander 3 is defined by anexpander shell 34. Anexpansion unit 31 and a power generator 32 (motor) are accommodated in theexpander shell 34. Theexpansion unit 31 and thepower generator 32 are coupled to each other through arotation shaft 33. - Further, the refrigerating
machine oil 50 is stored in theexpander shell 34. The refrigeratingmachine oil 50 is supplied to at least one of theexpansion unit 31 and thepower generator 32 to be used for lubrication. - The
expansion unit 31 includes anexpansion unit inlet 43 configured for allowing the refrigerant to flow therein, and anexpansion unit outlet 44 configured for allowing the refrigerant to flow out therefrom. Theexpansion unit inlet 43 is connected to aninlet pipe 35. Theexpansion unit outlet 44 is connected to anoutlet pipe 36. - The
inlet pipe 35 is connected to a condenser (the load-side heat exchanger 2 or the heat source-side heat exchanger 4) through the second four-way valve 6. - The
outlet pipe 36 is connected to an evaporator (the load-side heat exchanger 2 or the heat source-side heat exchanger 4) through the second four-way valve 6. - The
expansion unit 31 expands the refrigerant flowing from theinlet pipe 35 into theexpansion unit inlet 43, and causes the expanded refrigerant to flow from theexpansion unit outlet 44 to theoutlet pipe 36. Further, theexpansion unit 31 rotationally drives therotation shaft 33 by using expansion power generated when the refrigerant is expanded. - The
power generator 32 is coupled to theexpansion unit 31 through therotation shaft 33, and is rotated by the driving force generated by theexpansion unit 31 to generate electric power. In this way, the expansion power of theexpansion unit 31 is recovered as electric power. - An
inlet 41 configured for allowing the refrigerant to flow into theexpander shell 34 and anoutlet 42 configured for allowing the refrigerant to flow out from theexpander shell 34 are formed in theexpander shell 34 of theexpander 3. - The
inlet 41 is connected to a low-pressure pipe 22. The low-pressure pipe 22 is connected to the evaporator (the load-side heat exchanger 2 or the heat source-side heat exchanger 4) through the first four-way valve 5. The low-temperature and low-pressure refrigerant discharged from the evaporator flows into theexpander shell 34. The refrigerant flowing into theexpander shell 34 is separated into gas refrigerant and the refrigeratingmachine oil 50. In this way, the refrigeratingmachine oil 50 contained in the refrigerant that is discharged from the evaporator is stored in theexpander shell 34. - The
outlet 42 is connected to the suction-side pipe 21 of thecompressor 1. The refrigerant flowing out from theexpander shell 34 passes through the suction-side pipe 21 of thecompressor 1, and is sucked into thecompressor 1. - The load-
side heat exchanger 2 is, for example, a fin-and-tube heat exchanger. The load-side heat exchanger 2 exchanges heat between air as a load-side medium and the refrigerant. The load-side medium is not limited to air, and, for example, water or antifreeze may be used as a heat source. - The heat source-
side heat exchanger 4 is, for example, a fin-and-tube heat exchanger. The heat source-side heat exchanger 4 exchanges heat between outside air as a heat source-side medium and the refrigerant. The heat source-side medium is not limited to outside air (air), and, for example, water or antifreeze may be used as a heat source. - The first four-
way valve 5 and the second four-way valve 6 are used to switch the flow of the refrigerant circuit. - When the load-
side heat exchanger 2 is caused to function as a condenser (radiator) and the heat source-side heat exchanger 4 is caused to function as an evaporator (heating operation), the first four-way valve 5 connects the discharge-side pipe 10 of thecompressor 1 to the heat source-side heat exchanger 4, and connects the load-side heat exchanger 2 to the low-pressure pipe 22. Further, the second four-way valve 6 connects the load-side heat exchanger 2 to theinlet pipe 35, and connects theoutlet pipe 36 to the heat source-side heat exchanger 4. - On the other hand, when the load-
side heat exchanger 2 is caused to function as an evaporator and the heat source-side heat exchanger 4 is caused to function as a condenser (radiator) (cooling operation), the first four-way valve 5 connects the low-pressure pipe 22 to the load-side heat exchanger 2, and connects the heat source-side heat exchanger 4 to the discharge-side pipe 10 of thecompressor 1. Further, the second four-way valve 6 connects the heat source-side heat exchanger 4 to theinlet pipe 35, and connects theoutlet pipe 36 to the load-side heat exchanger 2. - When the heating operation and the cooling operation are not switched, there is no need to provide the first four-
way valve 5 and the second four-way valve 6. - A
controller 200 includes, for example, a microcomputer, and has a CPU, a RAM, a ROM, and other components. A control program and the like are stored in the ROM. Detection values from various kinds of sensors configured to detect, for example, the pressure, the temperature, and other conditions of the refrigerant in the refrigerant circuit, or temperatures of the load-side medium and the heat source-side medium are input to thecontroller 200. Thecontroller 200 controls each unit of therefrigeration cycle apparatus 100 based on the detection values from the sensors. Further, thecontroller 200 controls switching of the first four-way valve 5 and the second four-way valve 6. - Next, the heating operation and the cooling operation of the
refrigeration cycle apparatus 100 according to this embodiment are described. - During the heating operation, the first four-
way valve 5 and the second four-way valve 6 are switched to states indicated by the dotted lines inFig. 1 . - The
compressor 1 compresses the low-pressure refrigerant in thecompressor shell 15, and discharges the high-temperature and high-pressure gas refrigerant to the discharge-side pipe 10. The gas refrigerant discharged from thecompressor 1 contains the refrigeratingmachine oil 50 in thecompressor shell 15. - The high-temperature and high-pressure gas refrigerant discharged from the
compressor 1 flows through the discharge-side pipe 10 of thecompressor 1, passes through the first four-way valve 5, and is condensed by the load-side heat exchanger 2 that serves as a condenser (cooler in the case of supercritical refrigerant, e.g., CO2) into liquid refrigerant. The liquid refrigerant flows out from the load-side heat exchanger 2. After that, the liquid refrigerant flowing out from the load-side heat exchanger 2 passes through the second four-way valve 6 and flows into theexpansion unit inlet 43 in theexpander 3 through theinlet pipe 35. The liquid refrigerant flowing into theexpansion unit inlet 43 is expanded by theexpansion unit 31 into low-pressure two-phase refrigerant, and flows out from theexpansion unit outlet 44 into theoutlet pipe 36. At this time, thepower generator 32 coupled to therotation shaft 33 is rotated by the driving force generated by theexpansion unit 31. - The low-pressure two-phase refrigerant flowing out from the
expansion unit 31 passes through the second four-way valve 6, and flows into the heat source-side heat exchanger 4 that serves as an evaporator. The low-pressure two-phase refrigerant flowing into the heat source-side heat exchanger 4 exchanges heat with a heat source-side medium (outside air) and receives heat to be evaporated into low-pressure gas refrigerant. The low-pressure gas refrigerant flows out from the heat source-side heat exchanger 4. The low-pressure gas refrigerant flowing out from the heat source-side heat exchanger 4 passes through the first four-way valve 5 and further through the low-pressure pipe 22, and flows into theexpander shell 34 from theinlet 41 of theexpander 3. - At least part of the refrigerating
machine oil 50 contained in the gas refrigerant flowing into theexpander shell 34 is separated in theexpander shell 34, and the separated refrigeratingmachine oil 50 is stored in theexpander shell 34. The gas refrigerant and the remaining refrigeratingmachine oil 50 contained in the gas refrigerant flow out from theoutlet 42 toward the low pressure-side pipe 21 of thecompressor 1. The gas refrigerant flowing out from theoutlet 42 of theexpander 3 is sucked into thecompressor 1 through the low pressure-side pipe 21 of thecompressor 1. - In this way, the entire low-pressure gas refrigerant flowing out from the evaporator flows into the
expander shell 34, and the refrigeratingmachine oil 50 contained in the gas refrigerant is separated in theexpander shell 34 and is stored in theexpander shell 34. The refrigeratingmachine oil 50 stored in theexpander shell 34 is supplied to each of theelectric motor unit 17 and thecompression unit 18 via therotation shaft 33 to be used for lubrication. - Differences from the heating operation are mainly described.
- During the cooling operation, the first four-
way valve 5 and the second four-way valve 6 are switched to states indicated by the solid lines inFig. 1 . - The gas refrigerant discharged from the
compressor 1 flows through the discharge-side pipe 10 of thecompressor 1 and further through the first four-way valve 5, and is condensed by the heat source-side heat exchanger 4 that serves as a condenser (cooler in the case of supercritical refrigerant, e.g., CO2) into liquid refrigerant. The liquid refrigerant flows out from the heat source-side heat exchanger 4. After that, the liquid refrigerant flowing out from the heat source-side heat exchanger 4 passes through the second four-way valve 6 and theinlet pipe 35, is expanded into low-pressure two-phase refrigerant by theexpansion unit 31, and flows out therefrom. - The low-pressure two-phase refrigerant flowing out from the
expansion unit 31 passes through the second four-way valve 6, and flows into the load-side heat exchanger 2 that serves as an evaporator. The low-pressure two-phase refrigerant flowing into the load-side heat exchanger 2 exchanges heat with a load-side medium (air) and receives heat to be evaporated into low-pressure gas refrigerant. The low-pressure gas refrigerant flows out from the load-side heat exchanger 2. The low-pressure gas refrigerant flowing out from the load-side heat exchanger 2 passes through the first four-way valve 5 and further through the low-pressure pipe 22, and flows into theexpander shell 34 from theinlet 41 of theexpander 3. The gas refrigerant flowing out from theoutlet 42 of theexpander 3 is sucked into thecompressor 1 through the low pressure-side pipe 21 of thecompressor 1. - When the refrigerating
machine oil 50 stored in theexpander shell 34 is increased and the oil level of the refrigeratingmachine oil 50 reaches theoutlet 42 of theexpander shell 34, an oil quantity of the refrigeratingmachine oil 50 contained in the gas refrigerant flowing out from theexpander shell 34 is approximately the same as an oil quantity of the refrigeratingmachine oil 50 flowing into theexpander shell 34. - The refrigerating
machine oil 50 stored in theexpander shell 34 is consumed by being supplied to theexpansion unit 31 and thepower generator 32. For example, part of the refrigeratingmachine oil 50 supplied to theexpansion unit 31 is mixed into the refrigerant in theexpansion unit 31, and flows into thecompressor 1 through the refrigerant passage. Therefore, an oil quantity of the refrigeratingmachine oil 50 stored in theexpander shell 34 may be reduced. - As described above, in
Embodiment 1, theexpander 3 includes theexpander shell 34 that defines the outer shell, theexpansion unit 31 arranged in theexpander shell 34 and configured to expand the refrigerant flowing out from the condenser to generate the driving force, and configured for causing the expanded refrigerant to flow into the evaporator, and thepower generator 32 arranged in theexpander shell 34 and configured to rotate by the driving force generated by theexpansion unit 31. - Therefore, power generated when the refrigerant is expanded can be recovered as electric power.
- Further, in
Embodiment 1, theinlet 41 configured for allowing the refrigerant to flow into theexpander shell 34 and theoutlet 42 configured for allowing the refrigerant flowing into theexpander shell 34 from theinlet 41 to flow into the suction-side pipe 21 of thecompressor 1 are formed in theexpander shell 34. The refrigeratingmachine oil 50 contained in the refrigerant flowing into theexpander shell 34 is stored in theexpander shell 34, and the refrigeratingmachine oil 50 is supplied to at least one of the expansion unit and the power generator. - Therefore, the refrigerating
machine oil 50 stored in theexpander shell 34 can be supplied to theexpansion unit 31 and thepower generator 32, and depletion of the refrigeratingmachine oil 50 in theexpander shell 34 can be suppressed. - Further, the low-temperature and low-pressure refrigerant flowing out from the evaporator flows into the
expander shell 34, and thus, thepower generator 32 can be cooled. Therefore, reduction in efficiency of thepower generator 32 can be suppressed. - Further, temperature rise in the
expander shell 34 can be suppressed, and thus, heat is less likely to be exchanged between the refrigerant in theexpansion unit 31 and the gas refrigerant in theexpander shell 34 so that increase in enthalpy of the refrigerant flowing from theexpansion unit 31 into the evaporator can be suppressed to alleviate reduction in refrigeration capacity. - Further, an oil supply pipe as in the technique disclosed in
Patent Literature 2 is not arranged, and thus, the refrigerant that dissolves in the refrigeratingmachine oil 50 does not form bubbles, thereby being capable of suppressing unsatisfactory lubricity. Further, even under a transitional state, e.g., at a startup of thecompressor 1, theexpansion unit 31 and thepower generator 32 can be lubricated with the refrigeratingmachine oil 50 stored in theexpander shell 34. - Further, the refrigerant flowing out from the
expander shell 34 is caused to flow into the suction-side pipe 21 of thecompressor 1, and thus, the refrigeratingmachine oil 50 can be stored in theexpander shell 34 irrespective of the internal pressure of the compressor shell 15 (high-pressure shell or low-pressure shell). -
Embodiment 2 is not an embodiment of the invention, but helpful to understand certain aspects thereof. InEmbodiment 2, differences fromEmbodiment 1 are mainly described. Like reference numerals are used to designate components that are the same as those inEmbodiment 1, and description thereof is omitted. -
Figs. 2 are diagrams for illustrating configurations of anexpander 3 of arefrigeration cycle apparatus 100 according toEmbodiment 2. - As illustrated in
Fig. 2(a) , theoutlet 42 of theexpander shell 34 is formed by an opening port formed in a side surface of theexpander shell 34. Theoutlet 42 is formed at a position (Lm) higher than an oil level (Ln) of a preset necessary quantity of the refrigeratingmachine oil 50 to be stored in theexpander shell 34. In this case, the preset necessary quantity is a minimum necessary quantity of oil defined by, for example, specifications of theexpander 3. - As illustrated in
Fig. 2(b) , a pipe that communicates the inside and the outside of theexpander shell 34 may be arranged and theoutlet 42 may be formed by an opening port at an end portion of the pipe. Also in this case, theoutlet 42 is formed at a position (Lm) higher than the oil level (Ln) of the preset necessary quantity of the
refrigeratingmachine oil 50 to be stored in theexpander shell 34. - With the configuration described above, the preset necessary quantity of the refrigerating
machine oil 50 can be stored in theexpander shell 34. Therefore, the minimum oil quantity necessary for theexpander 3 can be secured. -
Embodiment 3 is not an embodiment of the invention, but helpful to understand certain aspects thereof. InEmbodiment 3, differences fromEmbodiment 1 are mainly described. Like reference numerals are used to designate components that are the same as those inEmbodiment 1, and description thereof is omitted. -
Fig. 3 is a diagram for illustrating a configuration of arefrigeration cycle apparatus 100 according toEmbodiment 3. - As illustrated in
Fig. 3 , therefrigeration cycle apparatus 100 according toEmbodiment 3 further includes, in addition to the configuration ofEmbodiment 1, anoil return pipe 52 configured for causing the refrigeratingmachine oil 50 in theexpander shell 34 to flow into the suction-side pipe 21 of thecompressor 1. - The
oil return pipe 52 connects anoil outlet 45 formed in a bottom portion of theexpander shell 34 and the suction-side pipe 21 of thecompressor 1. Further, an on-offvalve 54 configured to open and close the passage is formed in theoil return pipe 52. - The
controller 200 controls opening and closing of the on-offvalve 54. When, for example, the oil quantity of the refrigeratingmachine oil 50 in thecompressor shell 15 is smaller than the preset oil quantity, thecontroller 200 opens the on-offvalve 54 and returns part of the refrigeratingmachine oil 50 in theexpander shell 34 into thecompressor shell 15. - The oil quantity in the
compressor shell 15 may be determined, for example, by providing an oil level indicator, or by measuring the shell temperature with a temperature sensor, e.g., a thermistor. - Instead of the on-off
valve 54, a flow control valve with a variable opening degree may be arranged. Further, through omission of the on-offvalve 54 and adjustment of the pipe diameter and the length of theoil return pipe 52, a small quantity of the refrigeratingmachine oil 50 may be returned all the time. - Further, by lowering the level of the
outlet 42 of theexpander shell 34, the quantity of the refrigeratingmachine oil 50 stored in theexpander shell 34 is reduced and the quantity of the refrigeratingmachine oil 50 stored in thecompressor shell 15 is increased. Therefore, the level of theoutlet 42 of theexpander shell 34 may be set depending on the minimum necessary quantity of oil in thecompressor shell 15. - With the configuration described above, the refrigerating
machine oil 50 in theexpander shell 34 can be returned to thecompressor 1, and thus, when the quantity of the refrigeratingmachine oil 50 contained in the refrigerant that is discharged from the compressor 1 (quantity of the oil that is taken out) is large at, for example, a startup, depletion of the refrigeratingmachine oil 50 in thecompressor shell 15 can be suppressed. - Further, when the refrigerating
machine oil 50 in theexpander shell 34 is excessively stored, the refrigeratingmachine oil 50 can be returned into thecompressor shell 15. - Further, even when, for example, the configuration in the
expander 3 or other factors impose a limit and theoutlet 42 cannot be formed at a desired position, the oil can be returned to thecompressor 1 irrespective of the level of theoutlet 42 of theexpander shell 34. - The
embodiment 4 is not an embodiment of the invention, but helpful to understand certain aspects thereof. InEmbodiment 4, differences fromEmbodiment 1 are mainly described. Like reference numerals are used to designate components that are the same as those inEmbodiment 1, and description thereof is omitted. -
Fig. 4 is a diagram for illustrating a configuration of arefrigeration cycle apparatus 100 according toEmbodiment 4. - As illustrated in
Fig. 4 , therefrigeration cycle apparatus 100 according toEmbodiment 4 further includes, in addition to the configuration ofEmbodiment 1 described above, afirst bypass pipe 23 configured to branch off from the low-pressure pipe 22 to join the suction-side pipe 21 of thecompressor 1. Specifically, thefirst bypass pipe 23 branches off from the passage from the evaporator (the load-side heat exchanger 2 or the heat source-side heat exchanger 4) to theinlet 41 of theexpander shell 34 to join the passage from theoutlet 42 of theexpander shell 34 to thecompressor 1. - In this case, the refrigerant liquefied by the condenser (the load-
side heat exchanger 2 or the heat source-side heat exchanger 4) flows into theexpansion unit 31 in theexpander 3, and thus, the temperature of the refrigerant flowing through theexpansion unit 31 is lower than the temperature of the refrigerant flowing into theexpander shell 34. Therefore, the refrigerant in theexpansion unit 31 and the refrigerant flowing into theexpander shell 34 exchange heat therebetween. - In
Embodiment 4, part of the refrigerant flowing out from the evaporator flows from thepipe 10 into theexpander shell 34, and another part thereof flows from thefirst bypass pipe 23 into the suction-side pipe 21 of thecompressor 1. - Thus, the flow rate of the refrigerant flowing into the
expander shell 34 is reduced compared with a case in which the entire refrigerant flowing out from the evaporator flows into theexpander shell 34. Accordingly, the heat exchange quantity between the refrigerant in theexpansion unit 31 and the refrigerant flowing into theexpander shell 34 can be reduced. - Therefore, increase in enthalpy of the refrigerant flowing into the evaporator can be suppressed to alleviate reduction in refrigeration capacity.
- Further, excess supply of the refrigerating
machine oil 50 into theexpander shell 34 can be suppressed. Therefore, a situation in which the oil level of the refrigerating
machine oil 50 in theexpander shell 34 reaches thepower generator 32 can be suppressed. - In the configuration described above, the size of the
expander 3 is smaller than the size of thecompressor 1, and thus, the quantity of the refrigeratingmachine oil 50 contained in the refrigerant flowing out from the expander shell 34 (quantity of oil that is taken out) is smaller than the quantity of the refrigeratingmachine oil 50 contained in the refrigerant that is discharged from thecompressor 1. That is, it is sufficient that a quantity of the oil that is smaller than the quantity of the oil that is taken out of thecompressor 1 is supplied to theexpander 3. - Therefore, the length and the diameter of the low-
pressure pipe 22 or thefirst bypass pipe 23 are selected so that the flow rate of the refrigerant that passes through the low-pressure pipe 22 may be lower than the flow rate of the refrigerant that passes through thefirst bypass pipe 23. - As described above, by supplying the refrigerant and the oil at an appropriate refrigerant flow rate and an appropriate oil flow rate to the
expander 3, the heat exchange quantity in theexpansion unit 31 can be suppressed, and depletion of the refrigeratingmachine oil 50 in theexpander shell 34 can be suppressed. - A flow control valve or other components may be arranged to the low-
pressure pipe 22 or thefirst bypass pipe 23 to control the flow rate of the refrigerant flowing into theexpander shell 34. For example, thecontroller 200 may increase the flow rate of the refrigerant flowing into theexpander shell 34 to increase the oil quantity of the stored refrigeratingmachine oil 50 when the oil quantity of the refrigeratingmachine oil 50 in theexpander shell 34 is smaller than the preset oil quantity. - The oil quantity in the
expander shell 34 may be determined, for example, by providing an oil level indicator, or by measuring the shell temperature with a temperature sensor, e.g., a thermistor. - The configuration described above in
Embodiment 3 and the configuration described inEmbodiment 4 may be combined. - For example, as illustrated in
Fig. 5 , the configuration ofEmbodiment 1 may further additionally include theoil return pipe 52 configured for causing the refrigeratingmachine oil 50 in theexpander shell 34 to flow into the suction-side pipe 21 of thecompressor 1, and thefirst bypass pipe 23 configured to branch off from the passage from the evaporator to theinlet 41 of theexpander shell 34 to join the passage from theoutlet 42 of theexpander shell 34 to thecompressor 1. Such a configuration can achieve effects similar to those described above. - In
Embodiment 5 of the present invention, differences fromEmbodiment 1 are mainly described. Like reference numerals are used to designate components that are the same as those inEmbodiment 1, and description thereof is omitted. -
Fig. 6 is a diagram for illustrating a configuration of arefrigeration cycle apparatus 100 according toEmbodiment 5 of the present invention. - As illustrated in
Fig. 6 , therefrigeration cycle apparatus 100 according toEmbodiment 5 includes, in addition to the configuration ofEmbodiment 1, asecond bypass pipe 61 configured to branch off from the passage (inlet pipe 35) from the condenser to theexpansion unit 31 for causing the refrigerant to flow into theinlet 41 of theexpander shell 34. - Further, a decompression unit, e.g., a
capillary tube 63 configured to decompress the refrigerant flowing through thesecond bypass pipe 61, and aheat exchanger 60 configured to exchange heat between the refrigerant branched off to thesecond bypass pipe 61 to be decompressed and the refrigerant flowing through the inlet pipe 35 (refrigerant flowing from the condenser into the expansion unit) are arranged to thesecond bypass pipe 61. - The
outlet 42 of theexpander shell 34 inEmbodiment 5 joins the suction-side pipe 21 of thecompressor 1 through anoutlet pipe 20. A decompression unit, e.g., acapillary tube 24, which is configured to decompress the refrigerant, is formed in theoutlet pipe 20. - Further, in
Embodiment 5, the suction-side pipe 21 of thecompressor 1 is connected to the evaporator (the load-side heat exchanger 2 or the heat source-side heat exchanger 4) through the first four-way valve 5. - With regard to operation of
Embodiment 5, differences fromEmbodiment 1 are mainly described. - The refrigerant flowing out from the condenser passes through the second four-
way valve 6, and flows into theinlet pipe 35. Part of the refrigerant flowing through theinlet pipe 35 flows into thesecond bypass pipe 61. The refrigerant flowing into thesecond bypass pipe 61 is decompressed by thecapillary tube 63 and the temperature thereof falls. Theheat exchanger 60 exchanges heat between the refrigerant that is decompressed by thecapillary tube 63 to have the lowered temperature and the high-pressure refrigerant flowing from theinlet pipe 35 into theexpansion unit 31 so that the refrigerant decompressed by thecapillary tube 63 turns into gas refrigerant. - The gas refrigerant flows into the
inlet 41 of theexpander shell 34. Then, after the refrigeratingmachine oil 50 contained in the refrigerant is separated, the refrigerant flows from theoutlet 42 to theoutlet pipe 20. Then, after the refrigerant is decompressed by thecapillary tube 24, the refrigerant joins the suction-side pipe 21 of thecompressor 1. - There may be employed a configuration in which the refrigerant is decompressed through adjustment of the pipe diameters and the lengths of the
second bypass pipe 61 and theoutlet pipe 20 without arranging the decompression units, e.g., thecapillary tubes - Instead of the
capillary tube 63, a decompression device with a variable flow rate may be arranged. Arrangement of such a decompression device with a variable flow rate enables keeping appropriate temperature of the refrigerant flowing into the expander shell depending on the operation state, and thepower generator 32 can be effectively cooled. Further, occurrence of transient liquid return (liquid backflow) into theexpander shell 34 can be prevented to suppress lowering of oil concentration in theexpander shell 34. - With the configuration described above, the refrigerant flowing into the
expander shell 34 can be brought into a gas state, and thus, even when, for example, liquid backflow in which the refrigerant in a liquid state flows out from the evaporator occurs, the refrigerant in the liquid state can be prevented from flowing into theexpander shell 34. Therefore, the refrigerant in the liquid state can be prevented from being mixed into the refrigeratingmachine oil 50, and the oil concentration can be prevented from being lowered. - Further, by setting the pressure of the refrigerant flowing through the
second bypass pipe 61, the pressure and the temperature in theexpander shell 34 can be set at desired values. Therefore, by lowering the temperature in theexpander shell 34, temperature rise of thepower generator 32 can be suppressed, and reduction in efficiency of thepower generator 32 can be suppressed. - The configuration described above in
Embodiment 3 and the configuration described inEmbodiment 5 may be combined. - For example, as illustrated in
Fig. 7 , the configuration ofEmbodiment 5 may further additionally include theoil return pipe 52 configured for causing the refrigeratingmachine oil 50 in theexpander shell 34 to flow into the suction-side pipe 21 of thecompressor 1. Such a configuration can achieve effects similar to those described above. - Further, by setting the pressure in the
expander shell 34 to be higher than that of the refrigerant passing through theexpansion unit 31, there can be attained oil supply using a pressure difference as a method of supplying the refrigeratingmachine oil 50 stored in theexpander shell 34 to theexpansion unit 31 and thepower generator 32, and the reliability of theexpander 3 is improved. Further, the pressure on the suction side of thecompressor 1 is lower than the pressure in theexpander shell 34, and thus, the refrigeratingmachine oil 50 in theexpander shell 34 can be returned to thecompressor 1 without fail by using the pressure difference. - As illustrated in
Fig. 8 , in addition to the configuration described inEmbodiment 5, there may be further arranged athird bypass pipe 65 configured to branch off from the passage from the evaporator to the compressor 1 (low-pressure pipe 22) to join thesecond bypass pipe 61 at a downstream side of theheat exchanger 60. - With such a configuration, even when the refrigerant, which flows out from the evaporator and then passes through the low-
pressure pipe 22, is in a moist state, the refrigerant in the moist state and the refrigerant, which passes through thesecond bypass pipe 61 and is brought into the gas state by theheat exchanger 60, join together. Thus, the refrigerant in the moist state can be heated and liquid backflow to theexpander shell 34 can be suppressed. - The
embodiment 6 is not an embodiment of the invention, but helpful to understand certain aspects thereof. With regard toEmbodiment 6, differences fromEmbodiment 5 are mainly described. Like reference numerals are used to designate components that are the same as those inEmbodiment 5, and description thereof is omitted. -
Fig. 9 is a diagram for illustrating a configuration of arefrigeration cycle apparatus 100 according toEmbodiment 6. - As illustrated in
Fig. 9 , therefrigeration cycle apparatus 100 according toEmbodiment 6 includes, in addition to the configuration ofEmbodiment 5, anoil separator 7 configured to separate the refrigeratingmachine oil 50 contained in the refrigerant that is discharged from thecompressor 1, and afourth bypass pipe 13 configured to join the refrigeratingmachine oil 50 separated by theoil separator 7 to the refrigerant decompressed by thesecond bypass pipe 61. InEmbodiment 6, the heat
exchanger 60 is unnecessary. - Further, in
Embodiment 6, the discharge-side pipe 10 of thecompressor 1 is connected to theoil separator 7. Further, theoil separator 7 and the first four-way valve 5 are connected through thegas pipe 11. - As described in Modified Example 1 of
Embodiment 5, the configuration in which theoil return pipe 52 configured to cause the refrigeratingmachine oil 50 in theexpander shell 34 to flow into the suction-side pipe 21 of thecompressor 1 is arranged may be employed. - In the
refrigeration cycle apparatus 100 according toEmbodiment 6, the high-temperature and high-pressure refrigerant discharged from thecompressor 1 flows into theoil separator 7 through thepipe 10. In theoil separator 7, at least part of the refrigeratingmachine oil 50 contained in the refrigerant is separated. The refrigeratingmachine oil 50 separated by theoil separator 7 joins the low-pressure liquid refrigerant flowing through thesecond bypass pipe 61 through thefourth bypass pipe 13. The low-pressure liquid refrigerant flowing through thesecond bypass pipe 61 joins the high-temperaturerefrigerating machine oil 50 to be heated and turned into refrigerant in a gas state. The gasified refrigerant and the refrigeratingmachine oil 50 flow from theinlet 41 into theexpander shell 34. - On the other hand, the gas refrigerant separated by the
oil separator 7 passes through thegas pipe 11, and flows into the condenser (the load-side heat exchanger 2 or the heat source-side heat exchanger 4) through the first four-way valve 5. - With the configuration described above, the refrigerant flowing into the
expander shell 34 can be brought into a gas state, and thus, even when, for example, liquid backflow in which the refrigerant in a liquid state flows out from the evaporator occurs, the refrigerant in the liquid state can be prevented from flowing into theexpander shell 34. Therefore, the refrigerant in the liquid state can be prevented from being mixed into the refrigeratingmachine oil 50, and the oil concentration can be prevented from being lowered. - Further, by setting the pressure of the refrigerant flowing through the
second bypass pipe 61, the pressure and the temperature in theexpander shell 34 can be set at desired values. Therefore, by lowering the temperature in theexpander shell 34, temperature rise of thepower generator 32 can be suppressed, and reduction in efficiency of thepower generator 32 can be suppressed. - Further, the low-temperature refrigerant flowing through the
second bypass pipe 61 can cool the high-temperaturerefrigerating machine oil 50, and thus, temperature rise of thepower generator 32 can be suppressed. - Further, the refrigerating
machine oil 50 can be supplied from theoil separator 7, and thus, a sufficient quantity of the oil can be supplied into theexpander shell 34. - The
embodiment 7 is not an embodiment of the invention, but helpful to understand certain aspects thereof. InEmbodiment 7, differences fromEmbodiment 1 are mainly described. Like reference numerals are used to designate components that are the same as those inEmbodiment 1, and description thereof is omitted. -
Fig. 10 is a diagram for illustrating a configuration of arefrigeration cycle apparatus 100 according toEmbodiment 7. - As illustrated in
Fig. 10 , therefrigeration cycle apparatus 100 according toEmbodiment 7 further includes, in addition to the configuration ofEmbodiment 1, afifth bypass pipe 37 configured to branch off from theinlet pipe 35 to join theoutlet pipe 36 and asecond expansion valve 38 arranged to thefifth bypass pipe 37 and configured to expand the refrigerant. - The
fifth bypass pipe 37 branches off from the passage (inlet pipe 35) from the condenser to theexpansion unit 31 to join the passage (outlet pipe 36) from theexpansion unit 31 to the evaporator. - The
second expansion valve 38 is, for example, an electronically controlled expansion valve with a variable opening degree. Thecontroller 200 controls the opening degree of thesecond expansion valve 38 in accordance with a preset
condition. - There may be employed a configuration in which an on-off valve configured to open and close the passage of the
fifth bypass pipe 37 is provided and the opening degree of thesecond expansion valve 38 is fixed. In this case, thecontroller 200 controls the on-off valve. - When the opening degree of the
second expansion valve 38 is fully closed, the refrigerant flowing through theinlet pipe 35 does not flow through thefifth bypass pipe 37. In this case, the operation is similar to that inEmbodiment 1. - On the other hand, when the
second expansion valve 38 is opened, the refrigerant flowing through theinlet pipe 35 flows through thefifth bypass pipe 37. The refrigerant flowing through thefifth bypass pipe 37 is decompressed by thesecond expansion valve 38. At this time, the flow rate of the refrigerant flowing to theexpansion unit 31 is reduced, and thus, the drive of theexpansion unit 31 is stopped. An on-off valve or other components may be arranged to theinlet pipe 35 or theoutlet pipe 36 to completely stop the flow of the refrigerant into theexpansion unit 31. - The refrigerant decompressed by the
second expansion valve 38 joins theoutlet pipe 36, passes through the second four-way valve 6, and flows into the evaporator. - Next, control of the
second expansion valve 38 by thecontroller 200 is described. - When a preset condition is satisfied, the
controller 200 opens thesecond expansion valve 38, causes the refrigerant to flow through thefifth bypass pipe 37, and stops the drive of theexpansion unit 31. - The preset condition in this case is, for example, at least one of the following conditions (1) to (3).
- (1) The period of time elapsed since a startup of the
compressor 1 is equal to or shorter than a preset period of time. - (2) The quantity of the refrigerating
machine oil 50 in theexpander shell 34 is equal to or smaller than a preset quantity. - (3) The rotation speed of the
expansion unit 31 is equal to or higher than a preset upper limit, or equal to or lower than a preset lower limit. - With the configuration described above, when the preset condition is satisfied, the drive of the
expansion unit 31 can be stopped. - That is, by stopping the drive of the
expansion unit 31 when the period of time elapsed since a startup of thecompressor 1 is equal to or shorter than the preset period of time, the drive of theexpansion unit 31 can be prevented until the discharge pressure of thecompressor 1 is sufficiently increased, and liquid backflow into thecompressor 1 and the like can be suppressed. - Further, by stopping the drive of the
expansion unit 31 when the refrigeratingmachine oil 50 in theexpander shell 34 is reduced to the preset quantity or less, breakage of theexpander 3 can be prevented. - Further, by stopping the drive of the
expansion unit 31 when the rotation speed of theexpansion unit 31 is equal to or higher than the preset upper limit, or equal to or lower than the preset lower limit, theexpansion unit 31 can be driven at the rotation speed falling within a desired range. - The configuration of
Embodiment 7 can also be applied to any ofEmbodiments 1 to 6. -
- 1
compressor 2 load-side heat exchanger 3expander 4 heat source-side heat exchanger 5 first four-way valve 6 second four-way valve - 7
oil separator 10pipe 11gas pipe 13fourth bypass pipe 15compressor shell 17electric motor unit 18compression unit 20 outlet pipe - 21
pipe 22 low-pressure pipe 23first bypass pipe 24capillary tube 31expansion unit 32power generator 33rotation shaft 34expander shell 35inlet pipe 36outlet pipe 37fifth bypass pipe 38second expansion valve 41inlet 42outlet 43expansion unit inlet 44expansion unit outlet 45oil outlet 50 refrigeratingmachine oil 52oil return pipe 54 on-offvalve 60heat exchanger 61second bypass pipe 63capillary tube 65third bypass pipe 100refrigeration cycle apparatus 200 controller
Claims (8)
- A refrigeration cycle apparatus comprising a refrigerant circuit,
the refrigerant circuit comprising a compressor (1), a load-side heat exchanger (2), an expander (3), a heat source-side heat exchanger (4), a first four-way valve (5), and a second four-way valve (6), which are connected by pipes so that refrigerant is circulated through the refrigerant circuit,
the expander (3) comprising:an expander shell (34) defining an outer shell of the expander (3) and storing refrigerant machine oil (50);an expansion unit (31) arranged in the expander shell (34), the expansion unit (31) being configured to expand the refrigerant flowing out from the load-side heat exchanger (2) or the heat source-side heat exchanger (4) that serves as a condenser to generate driving force, and configured for causing the expanded refrigerant to flow into the load-side heat exchanger (2) or the heat source-side heat exchanger (4) that serves as an evaporator,a power generator (32) arranged in the expander shell (34), the power generator (32) being configured to rotate by the driving force generated by the expansion unit (31); anda rotation shaft (33) coupling the power generator (32) to the expansion unit (31),the expander shell (34) including:an inlet (41) configured for allowing the refrigerant to flow into the expander shell (34); andan outlet (42) configured for allowing the refrigerant that flowed into the expander shell (34) from the inlet (41) to flow out from the expander shell (34) and to flow into a suction-side pipe (21) of the compressor (1),the expander shell (34) being configured such that the refrigerating machine oil (50) contained in the refrigerant is stored therein, and is supplied to at least one of the expansion unit (31) and the power generator (32),
the expansion unit (31) including:an expansion unit inlet (43) configured for allowing the refrigerant to flow into the expansion unit (31) from an inlet pipe (35); andan expansion unit outlet (44) configured for allowing the refrigerant flow out from the expansion unit (31) and to flow into an outlet pipe (36),the inlet pipe (35) being connected to the condenser (2, 4) through the second four-way valve (6),
the outlet pipe (36) being connected to the evaporator (2, 4) through the second four-way valve (6),
characterized in that
the refrigeration cycle apparatus further comprises;a second bypass pipe (61) configured to branch off from a passage from the condenser (2, 4) to the expansion unit (31), to decompress the refrigerant and to cause the refrigerant to flow into the inlet (41) of the expander shell (34); anda heat exchanger (60) configured to exchange heat between the refrigerant branched off and decompressed at the second bypass pipe (61) and the refrigerant flowing from the condenser (2, 4) into the expansion unit (31). - The refrigeration cycle apparatus of claim 1, wherein the outlet (42) of the expander shell (34) is formed at a position higher than an oil level of a preset necessary quantity of the refrigerating machine oil (50) to be stored in the expander shell (34).
- The refrigeration cycle apparatus of claim 1 or 2, further comprising an oil return pipe (52) configured for causing the refrigerating machine oil (50) in the expander shell (34) to flow into the suction-side pipe (21) of the compressor (1).
- The refrigeration cycle apparatus of any one of claims 1 to 3, wherein a pressure of the refrigerant in the expander shell (34) is higher than a pressure of the refrigerant flowing out from the expansion unit (31).
- The refrigeration cycle apparatus of any one of claims 1 to 4, further comprising a third bypass pipe (65) configured to branch off from a passage from the evaporator (2, 4) to the compressor (1) and to join the second bypass pipe (61) at a downstream side of the heat exchanger (60).
- The refrigeration cycle apparatus of any one of claims 1 to 5, further comprising:an oil separator (7) configured to separate the refrigerating machine oil (50) contained in the refrigerant discharged from the compressor (1); anda fourth bypass pipe (13) configured to join the refrigerating machine oil (50) separated by the oil separator (7) to the refrigerant decompressed at the second bypass pipe (61).
- The refrigeration cycle apparatus of any one of claims 1 to 6, further comprising:a fifth bypass pipe (37) configured to branch off from a passage from the condenser (2, 4) to the expansion unit (31) and to join a passage from the expansion unit (31) to the evaporator (2, 4); anda second expansion valve (38) arranged to the fifth bypass pipe (37) and configured to expand the refrigerant,wherein, when a preset condition is satisfied, the refrigerant is caused to flow through the fifth bypass pipe (37).
- The refrigeration cycle apparatus of claim 7, wherein the preset condition comprises at least one of:a condition that a period of time elapsed since a startup of the compressor (1) is equal to or shorter than a preset period of time;a condition that a quantity of the refrigerating machine oil (50) in the expander shell (34) is equal to or smaller than a preset quantity; anda condition that a rotation speed of the expansion unit (31) is equal to or higher than a preset upper limit, or equal to or lower than a preset lower limit.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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PCT/JP2014/050257 WO2015104823A1 (en) | 2014-01-09 | 2014-01-09 | Refrigeration cycle device |
Publications (3)
Publication Number | Publication Date |
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EP3098542A1 EP3098542A1 (en) | 2016-11-30 |
EP3098542A4 EP3098542A4 (en) | 2017-10-25 |
EP3098542B1 true EP3098542B1 (en) | 2021-05-05 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP14877666.9A Active EP3098542B1 (en) | 2014-01-09 | 2014-01-09 | Refrigeration cycle device |
Country Status (3)
Country | Link |
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EP (1) | EP3098542B1 (en) |
JP (1) | JP6150907B2 (en) |
WO (1) | WO2015104823A1 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN115823759A (en) * | 2022-11-25 | 2023-03-21 | 珠海格力电器股份有限公司 | Compression refrigeration system and control method |
Family Cites Families (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4075429B2 (en) * | 2002-03-26 | 2008-04-16 | 三菱電機株式会社 | Refrigeration air conditioner |
EP1939547B1 (en) * | 2005-08-26 | 2013-05-01 | Mitsubishi Electric Corporation | Refrigerating air conditioner |
JP4591402B2 (en) * | 2006-04-20 | 2010-12-01 | ダイキン工業株式会社 | Refrigeration equipment |
JP4715615B2 (en) * | 2006-04-20 | 2011-07-06 | ダイキン工業株式会社 | Refrigeration equipment |
JP5103952B2 (en) | 2007-03-08 | 2012-12-19 | ダイキン工業株式会社 | Refrigeration equipment |
JP5036593B2 (en) * | 2008-02-27 | 2012-09-26 | パナソニック株式会社 | Refrigeration cycle equipment |
JP5521709B2 (en) * | 2010-03-31 | 2014-06-18 | ダイキン工業株式会社 | Refrigeration equipment |
JP2012042110A (en) * | 2010-08-18 | 2012-03-01 | Panasonic Corp | Refrigerating cycle device |
JPWO2012029203A1 (en) * | 2010-09-02 | 2013-10-28 | 三菱電機株式会社 | Expander and refrigeration cycle equipment |
JP2013139890A (en) * | 2011-12-28 | 2013-07-18 | Daikin Industries Ltd | Refrigeration apparatus |
-
2014
- 2014-01-09 EP EP14877666.9A patent/EP3098542B1/en active Active
- 2014-01-09 JP JP2015556681A patent/JP6150907B2/en not_active Expired - Fee Related
- 2014-01-09 WO PCT/JP2014/050257 patent/WO2015104823A1/en active Application Filing
Also Published As
Publication number | Publication date |
---|---|
EP3098542A1 (en) | 2016-11-30 |
JP6150907B2 (en) | 2017-06-21 |
EP3098542A4 (en) | 2017-10-25 |
JPWO2015104823A1 (en) | 2017-03-23 |
WO2015104823A1 (en) | 2015-07-16 |
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