WO2018096824A1 - Scroll compressor - Google Patents

Scroll compressor Download PDF

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Publication number
WO2018096824A1
WO2018096824A1 PCT/JP2017/036937 JP2017036937W WO2018096824A1 WO 2018096824 A1 WO2018096824 A1 WO 2018096824A1 JP 2017036937 W JP2017036937 W JP 2017036937W WO 2018096824 A1 WO2018096824 A1 WO 2018096824A1
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WO
WIPO (PCT)
Prior art keywords
compression chamber
chamber
compression
refrigerant
injection port
Prior art date
Application number
PCT/JP2017/036937
Other languages
French (fr)
Japanese (ja)
Inventor
啓晶 中井
淳 作田
Original Assignee
パナソニックIpマネジメント株式会社
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by パナソニックIpマネジメント株式会社 filed Critical パナソニックIpマネジメント株式会社
Priority to JP2018552453A priority Critical patent/JP6928792B2/en
Priority to US16/463,276 priority patent/US20190309750A1/en
Priority to EP17873176.6A priority patent/EP3546753B1/en
Priority to CN201780071842.8A priority patent/CN109996961B/en
Publication of WO2018096824A1 publication Critical patent/WO2018096824A1/en

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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04CROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
    • F04C18/00Rotary-piston pumps specially adapted for elastic fluids
    • F04C18/02Rotary-piston pumps specially adapted for elastic fluids of arcuate-engagement type, i.e. with circular translatory movement of co-operating members, each member having the same number of teeth or tooth-equivalents
    • F04C18/0207Rotary-piston pumps specially adapted for elastic fluids of arcuate-engagement type, i.e. with circular translatory movement of co-operating members, each member having the same number of teeth or tooth-equivalents both members having co-operating elements in spiral form
    • F04C18/0215Rotary-piston pumps specially adapted for elastic fluids of arcuate-engagement type, i.e. with circular translatory movement of co-operating members, each member having the same number of teeth or tooth-equivalents both members having co-operating elements in spiral form where only one member is moving
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04CROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
    • F04C18/00Rotary-piston pumps specially adapted for elastic fluids
    • F04C18/02Rotary-piston pumps specially adapted for elastic fluids of arcuate-engagement type, i.e. with circular translatory movement of co-operating members, each member having the same number of teeth or tooth-equivalents
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04CROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
    • F04C18/00Rotary-piston pumps specially adapted for elastic fluids
    • F04C18/02Rotary-piston pumps specially adapted for elastic fluids of arcuate-engagement type, i.e. with circular translatory movement of co-operating members, each member having the same number of teeth or tooth-equivalents
    • F04C18/0207Rotary-piston pumps specially adapted for elastic fluids of arcuate-engagement type, i.e. with circular translatory movement of co-operating members, each member having the same number of teeth or tooth-equivalents both members having co-operating elements in spiral form
    • F04C18/0215Rotary-piston pumps specially adapted for elastic fluids of arcuate-engagement type, i.e. with circular translatory movement of co-operating members, each member having the same number of teeth or tooth-equivalents both members having co-operating elements in spiral form where only one member is moving
    • F04C18/0223Rotary-piston pumps specially adapted for elastic fluids of arcuate-engagement type, i.e. with circular translatory movement of co-operating members, each member having the same number of teeth or tooth-equivalents both members having co-operating elements in spiral form where only one member is moving with symmetrical double wraps
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04CROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
    • F04C18/00Rotary-piston pumps specially adapted for elastic fluids
    • F04C18/02Rotary-piston pumps specially adapted for elastic fluids of arcuate-engagement type, i.e. with circular translatory movement of co-operating members, each member having the same number of teeth or tooth-equivalents
    • F04C18/0207Rotary-piston pumps specially adapted for elastic fluids of arcuate-engagement type, i.e. with circular translatory movement of co-operating members, each member having the same number of teeth or tooth-equivalents both members having co-operating elements in spiral form
    • F04C18/0246Details concerning the involute wraps or their base, e.g. geometry
    • F04C18/0253Details concerning the base
    • F04C18/0261Details of the ports, e.g. location, number, geometry
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04CROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
    • F04C23/00Combinations of two or more pumps, each being of rotary-piston or oscillating-piston type, specially adapted for elastic fluids; Pumping installations specially adapted for elastic fluids; Multi-stage pumps specially adapted for elastic fluids
    • F04C23/008Hermetic pumps
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04CROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
    • F04C28/00Control of, monitoring of, or safety arrangements for, pumps or pumping installations specially adapted for elastic fluids
    • F04C28/24Control of, monitoring of, or safety arrangements for, pumps or pumping installations specially adapted for elastic fluids characterised by using valves controlling pressure or flow rate, e.g. discharge valves or unloading valves
    • F04C28/26Control of, monitoring of, or safety arrangements for, pumps or pumping installations specially adapted for elastic fluids characterised by using valves controlling pressure or flow rate, e.g. discharge valves or unloading valves using bypass channels
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04CROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
    • F04C28/00Control of, monitoring of, or safety arrangements for, pumps or pumping installations specially adapted for elastic fluids
    • F04C28/28Safety arrangements; Monitoring
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04CROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
    • F04C29/00Component parts, details or accessories of pumps or pumping installations, not provided for in groups F04C18/00 - F04C28/00
    • F04C29/0007Injection of a fluid in the working chamber for sealing, cooling and lubricating
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04CROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
    • F04C29/00Component parts, details or accessories of pumps or pumping installations, not provided for in groups F04C18/00 - F04C28/00
    • F04C29/02Lubrication; Lubricant separation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04CROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
    • F04C29/00Component parts, details or accessories of pumps or pumping installations, not provided for in groups F04C18/00 - F04C28/00
    • F04C29/04Heating; Cooling; Heat insulation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04CROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
    • F04C29/00Component parts, details or accessories of pumps or pumping installations, not provided for in groups F04C18/00 - F04C28/00
    • F04C29/12Arrangements for admission or discharge of the working fluid, e.g. constructional features of the inlet or outlet

Definitions

  • the present invention relates to a scroll compressor used in refrigerators such as an air conditioner, a water heater, and a refrigerator.
  • compression is performed by sucking the gas refrigerant evaporated in the evaporator, compressing the gas refrigerant to the pressure required for condensation in the condenser, and sending the high-temperature and high-pressure gas refrigerant into the refrigerant circuit
  • the machine is being used.
  • the scroll compressor is provided with two expansion valves between the condenser and the evaporator, and the intermediate pressure refrigerant flowing between the two expansion valves is injected into the compression chamber during the compression process, thereby providing a refrigeration cycle. To reduce power consumption and improve capacity.
  • the refrigerant circulating through the condenser increases by the amount of injected refrigerant, and if it is an air conditioner, the heating capacity is improved.
  • COP Coefficient Of Performance
  • the amount of refrigerant flowing through the condenser is equal to the sum of the amount of refrigerant flowing through the evaporator and the amount of refrigerant injected, and the ratio of the amount of injected refrigerant to the amount of refrigerant in the condenser is the injection rate.
  • the injection rate should be increased. And since a refrigerant
  • the refrigerant flowing into the compression chamber from the injection pipe is preferentially taken out and sent from the gas-liquid separator.
  • the gas refrigerant flows from the injection tube in a state where liquid refrigerant is mixed.
  • an appropriate amount of oil is fed into the compression chamber having many sliding parts and compressed together with the refrigerant.
  • the oil in the compression chamber is washed away by the liquid refrigerant.
  • the sliding state deteriorates, and component wear and seizure occur. Therefore, it is important that the liquid refrigerant flowing from the injection pipe is not sent into the compression chamber as much as possible, and only the gas refrigerant is guided to the injection port.
  • the intermediate pressure is controlled, and the internal pressure and the intermediate pressure of the compression chamber in the compressor to which the injection pipe is finally connected are controlled.
  • the injection refrigerant is sent into the compression chamber by the pressure difference. For this reason, if the intermediate pressure is adjusted high, the injection rate increases.
  • the gas phase component ratio in the refrigerant flowing from the condenser through the upstream expansion valve to the gas-liquid separator decreases as the intermediate pressure increases, the gas-liquid separator increases when the intermediate pressure is excessively increased.
  • the liquid refrigerant increases, and the liquid refrigerant flows into the injection pipe, resulting in a decrease in heating capacity and a decrease in the reliability of the compressor. Therefore, it is desirable for the compressor to be able to take in a large amount of injection refrigerant at the lowest possible intermediate pressure, and as the compression method, a scroll type with a moderate compression speed is suitable.
  • the symmetrical scroll compressor in which compression chambers with the same volume are formed at the same timing on the outer and inner sides of the orbiting scroll wrap, has features such as low vibration and excellent mechanical balance due to the symmetry of the compression chamber. It has been used in various fields including air conditioning applications.
  • the conventional scroll compressor discloses the opening range of the injection port and the bypass port (see, for example, Patent Document 1).
  • correspond with various performance modes including injection with sufficient performance is provided.
  • the compression start timings of the first compression chamber formed outside the orbiting scroll wrap and the second compression chamber formed inside the orbiting scroll wrap are equal, and a single injection port is used. It is difficult to always feed the same amount of injection refrigerant into the first compression chamber and the second compression chamber.
  • Patent Document 1 Although the relationship between the bypass port and the opening section of the injection port is disclosed, the relationship between the amount of injection into the first compression chamber and the second compression chamber and the bypass port is disclosed. Absent.
  • the present invention avoids over-compression operation due to the difference in injection amount that inevitably occurs in a symmetric scroll compressor, and maximizes the original effect of the injection cycle. Therefore, the present invention is highly efficient for operation at a higher injection rate. To provide a scroll compressor that can cope with the increase in capacity.
  • a scroll compressor includes a fixed scroll and a turning scroll in which a spiral wrap rises from an end plate.
  • a first compression chamber formed on the outer wall side of the orbiting scroll wrap and a second compression chamber formed on the inner wall side of the orbiting scroll wrap are formed, and the suction volume of the first compression chamber Is substantially equal to the suction volume of the second compression chamber.
  • a discharge port that discharges the refrigerant compressed in the compression chamber is provided at the center of the end plate of the fixed scroll, and a discharge bypass port that discharges the refrigerant compressed in the compression chamber is provided before the compression chamber communicates with the discharge port.
  • At least one injection port for injecting the intermediate pressure refrigerant into the first compression chamber and the second compression chamber is opened to the first compression chamber or the second compression chamber in the compression stroke after the suction refrigerant is closed.
  • the end plate of the fixed scroll is provided at a position where it is inserted.
  • one of the compression chambers that increases the amount of refrigerant injected from the injection port is a compression chamber that can discharge the refrigerant in the compression chamber to the other compression chamber.
  • the discharge bypass port is arranged so that the volume ratio, which is the ratio of the suction volume to the discharge volume, becomes small.
  • FIG. 1 is a refrigeration cycle diagram provided with a scroll compressor according to a first embodiment of the present invention.
  • FIG. 2 is a longitudinal sectional view of the scroll compressor according to the first embodiment of the present invention.
  • FIG. 3 is an enlarged view of a main part of FIG.
  • FIG. 4 is a view taken along line 4-4 in FIG.
  • FIG. 5 is a view taken in the direction of arrows 5-5 in FIG. 6 is a view taken along line 6-6 in FIG.
  • FIG. 7 is a graph showing the internal pressure of the compression chamber of the scroll compressor without the injection operation.
  • FIG. 8 is an explanatory diagram showing the positional relationship between the oil supply path and the seal member accompanying the turning motion of the scroll compressor according to the first embodiment of the present invention.
  • FIG. 8 is an explanatory diagram showing the positional relationship between the oil supply path and the seal member accompanying the turning motion of the scroll compressor according to the first embodiment of the present invention.
  • FIG. 9 is an explanatory view showing an opening state of an oil supply path and an injection port accompanying a turning motion of the scroll compressor according to the first embodiment of the present invention.
  • FIG. 10 is a longitudinal sectional view of a scroll compressor according to the second embodiment of the present invention.
  • FIG. 1 is a refrigeration cycle diagram provided with a scroll compressor according to this embodiment.
  • the refrigeration cycle apparatus provided with the scroll compressor includes a compressor 91 that is a scroll compressor, a condenser 92, an evaporator 93, expansion valves 94a and 94b, an injection pipe 95, And a gas-liquid separator 96.
  • the refrigerant that is the working fluid condensed in the condenser 92 is decompressed to an intermediate pressure by the upstream expansion valve 94a, and the gas-liquid separator 96 is connected to the gas phase component (gas refrigerant) and the liquid phase component (liquid refrigerant) of the intermediate pressure refrigerant. (Refrigerant).
  • the liquid refrigerant whose pressure has been reduced to the intermediate pressure further passes through the expansion valve 94b on the downstream side, and is led to the evaporator 93 as a low-pressure refrigerant.
  • the liquid refrigerant sent to the evaporator 93 evaporates by heat exchange and is discharged as a gas refrigerant mixed with a gas refrigerant or a part of the liquid refrigerant.
  • the refrigerant discharged from the evaporator 93 is taken into the compression chamber of the compressor 91.
  • the intermediate-pressure gas refrigerant separated by the gas-liquid separator 96 passes through the injection pipe 95 and is guided to the compression chamber in the compressor 91.
  • a configuration may be provided in which a blocking valve or an expansion valve is provided in the injection pipe 95 to adjust and stop the injection pressure.
  • the compressor 91 compresses the low-pressure refrigerant flowing in from the evaporator 93, and in the compression process, the intermediate-pressure refrigerant of the gas-liquid separator 96 is injected (injected) into the compression chamber for compression, and the high-temperature high-pressure refrigerant is condensed from the discharge pipe. To the container 92.
  • the ratio between the gas phase component and the liquid phase component separated by the gas-liquid separator 96 is such that the larger the pressure difference between the inlet side pressure and the outlet side pressure of the expansion valve 94a provided on the upstream side, the larger the gas phase component, The smaller the degree of supercooling of the refrigerant at the outlet of the condenser 92, or the greater the degree of thirst, the more gas phase components.
  • the amount of refrigerant sucked by the compressor 91 through the injection pipe 95 increases as the intermediate pressure increases, the amount of the refrigerant separated by the gas-liquid separator 96 exceeds the ratio of the gas phase components of the refrigerant from the injection pipe 95.
  • the gas refrigerant in the gas-liquid separator 96 is exhausted and the liquid refrigerant flows into the injection pipe 95.
  • it is desirable that the gas refrigerant separated in the gas-liquid separator 96 is sucked into the compressor 91 from the injection pipe 95 without leaving any excess.
  • the compressor 91 needs to be configured to maintain high reliability even in such a case.
  • FIG. 2 is a longitudinal sectional view of the scroll compressor according to this embodiment.
  • FIG. 3 is an enlarged view of a main part of FIG.
  • FIG. 4 is a view taken along line 4-4 of FIG.
  • FIG. 5 is a view taken along line 4-4 in FIG.
  • the compressor 91 includes a compression mechanism 2, a motor unit 3, and an oil storage unit 20 inside the sealed container 1.
  • the compression mechanism 2 includes a main bearing member 11 fixed to the sealed container 1 by welding or shrink fitting, a fixed scroll (compression chamber partition member) 12 bolted on the main bearing member 11, and a turning scroll 13 meshing with the fixed scroll 12. And have.
  • the shaft 4 is pivotally supported by the main bearing member 11.
  • a rotation restraint mechanism 14 such as an Oldham ring that guides the orbiting scroll 13 to rotate and prevent it from rotating.
  • the orbiting scroll 13 is eccentrically driven by the eccentric shaft portion 4 a at the upper end of the shaft 4, and moves in a circular orbit by the rotation restraint mechanism 14.
  • the compression chamber 15 is formed between the fixed scroll 12 and the orbiting scroll 13.
  • the suction pipe 16 communicates with the outside of the sealed container 1, and a suction port 17 is provided on the outer periphery of the fixed scroll 12.
  • the working fluid (refrigerant) sucked from the suction pipe 16 is guided from the suction port 17 to the compression chamber 15.
  • the compression chamber 15 moves while reducing its volume from the outer peripheral side toward the central portion, and the working fluid that has reached a predetermined pressure in the compression chamber 15 is discharged from the discharge port 18 provided in the central portion of the fixed scroll 12 to the discharge chamber 31.
  • the discharge port 18 is provided with a discharge reed valve 19.
  • the working fluid that has reached a predetermined pressure in the compression chamber 15 pushes the discharge reed valve 19 open and is discharged into the discharge chamber 31.
  • the working fluid discharged into the discharge chamber 31 is discharged out of the sealed container 1.
  • the intermediate-pressure working fluid led from the injection pipe 95 flows into the intermediate pressure chamber 41, opens the check valve 42 provided in the injection port 43, and is injected into the compression chamber 15 after being closed, and the suction port Together with the working fluid sucked from 17, it is discharged into the sealed container 1 from the discharge port 18.
  • a pump 25 is provided at the lower end of the shaft 4.
  • the pump 25 is arranged so that the suction port exists in the oil storage unit 20.
  • the pump 25 is driven by the shaft 4 and can reliably suck up the oil 6 in the oil storage section 20 provided at the bottom of the hermetic container 1 regardless of the pressure condition and the operation speed. It will be resolved.
  • the oil 6 sucked up by the pump 25 is supplied to the compression mechanism 2 through an oil supply hole 26 formed in the shaft 4. If foreign matter is removed from the oil 6 with an oil filter or the like before or after the oil 25 is sucked up by the pump 25, foreign matter can be prevented from entering the compression mechanism 2 and further reliability can be improved.
  • the pressure of the oil 6 guided to the compression mechanism 2 is substantially equal to the discharge pressure of the scroll compressor, and also serves as a back pressure source for the orbiting scroll 13. As a result, the orbiting scroll 13 does not move away from the fixed scroll 12 and does not come into contact with each other, and the predetermined compression function is stably exhibited.
  • a ring-shaped seal member 78 is disposed on the back surface 13 e of the end plate of the orbiting scroll 13.
  • the high pressure region 30 is formed inside the seal member 78, and the back pressure chamber 29 is formed outside the seal member 78.
  • the back pressure chamber 29 is set to a pressure between a high pressure and a low pressure.
  • the compression chamber 15 formed by the fixed scroll 12 and the orbiting scroll 13 is formed on the outer wall side of the wrap of the orbiting scroll 13.
  • connection path 55 from the high pressure region 30 to the back pressure chamber 29 includes a connecting path 55 from the high pressure region 30 to the back pressure chamber 29 and a supply path 56 from the back pressure chamber 29 to the second compression chamber 15b.
  • connection path 55 is formed on the back surface 13 e of the orbiting scroll 13, and travels between the inside and outside of the seal member 78, and the other second opening end 55 b always opens to the high-pressure region 30. Yes. Thereby, intermittent oil supply is realizable.
  • a part of the oil 6 enters the fitting portion between the eccentric shaft portion 4a and the orbiting scroll 13 and the bearing portion 66 between the shaft 4 and the main bearing member 11 so as to obtain a clearance by the supply pressure and the own weight. After lubricating each part, it falls and returns to the oil storage part 20.
  • the oil supply path to the compression chamber 15 is configured by a passage 13 a formed inside the orbiting scroll 13 and a recess 12 a formed on the lap surface side end plate of the fixed scroll 12. Yes.
  • the third opening end 56a of the passage 13a is formed at the lap tip 13c, and is periodically opened in the recess 12a according to the turning motion, and the fourth opening end 56b of the passage 13a is always opened in the back pressure chamber 29. . Thereby, the back pressure chamber 29 and the 2nd compression chamber 15b can be intermittently connected.
  • the injection port 43 for injecting the intermediate pressure refrigerant is provided through the end plate of the fixed scroll 12.
  • the injection port 43 opens sequentially to the first compression chamber 15a and the second compression chamber 15b.
  • the injection port 43 is provided at a position that is opened during the compression process after being closed in the first compression chamber 15a and the second compression chamber 15b.
  • the end plate of the fixed scroll 12 is provided with a discharge bypass port 21 that discharges the refrigerant compressed in the compression chamber 15 before communicating with the discharge port 18.
  • the compressor 91 As shown in FIGS. 3 to 4, the compressor 91 according to the present embodiment is provided with an intermediate pressure chamber 41 that is fed from the injection pipe 95 and guides the intermediate pressure working fluid before being injected into the compression chamber 15.
  • the intermediate pressure chamber 41 is formed by a fixed scroll 12 that is a compression chamber partition member, an intermediate pressure plate 44, and an intermediate pressure cover 45.
  • the intermediate pressure chamber 41 and the compression chamber 15 are opposed to each other with the fixed scroll 12 interposed therebetween.
  • the intermediate pressure chamber 41 is located at a position lower than the intermediate pressure chamber inlet 41a into which the intermediate pressure working fluid flows, the injection port inlet 43a of the injection port 43 that injects the intermediate pressure working fluid into the compression chamber 15, and the intermediate pressure chamber inlet 41a.
  • the liquid reservoir 41b is formed.
  • the liquid reservoir 41b is formed on the upper surface of the end plate of the fixed scroll 12.
  • the intermediate pressure plate 44 is provided with a check valve 42 for preventing a refrigerant backflow from the compression chamber 15 to the intermediate pressure chamber 41.
  • a check valve 42 for preventing a refrigerant backflow from the compression chamber 15 to the intermediate pressure chamber 41.
  • the check valve 42 is configured by a reed valve 42a that lifts to the compression chamber 15 side and communicates the compression chamber 15 and the intermediate pressure chamber 41, and the internal pressure of the compression chamber 15 is intermediate.
  • the intermediate pressure chamber 41 is communicated with the compression chamber 15 only when the pressure is lower than the pressure chamber 41.
  • the reed valve 42a By using the reed valve 42a, there are few sliding parts in a movable part, a sealing performance can be maintained for a long time, and it is easy to expand a flow path area as needed.
  • the check valve 42 is not provided or the check valve 42 is provided in the injection pipe 95, the refrigerant in the compression chamber 15 flows back to the injection pipe 95, and wasteful compression power is consumed.
  • the check valve 42 is provided on the intermediate pressure plate 44 close to the compression chamber 15 to suppress the backflow from the compression chamber 15.
  • the upper surface of the end plate of the fixed scroll 12 is at a position lower than the intermediate pressure chamber inlet 41a, and a liquid reservoir 41b in which a working fluid of a liquid phase component is provided on the upper surface of the end plate of the fixed scroll 12.
  • the injection port inlet 43a is provided at a position higher than the height of the intermediate pressure chamber inlet 41a. Therefore, among the intermediate pressure working fluid, the working fluid of the gas phase component is guided to the injection port 43, and the working fluid of the liquid phase component accumulated in the liquid reservoir 41b is vaporized on the surface of the fixed scroll 12 in a high temperature state. Therefore, it is difficult for the working fluid of the liquid phase component to flow into the compression chamber 15.
  • the intermediate pressure chamber 41 and the discharge chamber 31 are provided at positions adjacent to each other via the intermediate pressure plate 44, and promotes vaporization when the working fluid of the liquid phase component flows into the intermediate pressure chamber 41, and discharges. Since the temperature rise of the high-pressure refrigerant in the chamber 31 can also be suppressed, the operation can be performed up to a higher discharge pressure condition.
  • the intermediate pressure working fluid guided to the injection port 43 pushes and opens the reed valve 42 a due to a pressure difference between the injection port 43 and the compression chamber 15, and merges with the low pressure working fluid sucked from the suction port 17 in the compression chamber 15.
  • the intermediate pressure working fluid remaining in the injection port 43 between the check valve 42 and the compression chamber 15 repeats re-expansion and re-compression, which causes a reduction in the efficiency of the compressor 91. Therefore, the thickness of the valve stop 42b (see FIG. 5) that regulates the maximum displacement amount of the reed valve 42a is changed according to the lift restricting portion of the reed valve 42a, and the volume in the injection port 43 downstream from the reed valve 42a is reduced. is doing.
  • the reed valve 42a and the valve stop 42b shown in FIG. 5 are fixed to the intermediate pressure plate 44 by a fixing member 46 including a bolt. Since the fixing hole of the fixing member 46 including the screw provided in the valve stop 42b is opened only on the insertion side of the fixing member 46 without penetrating the valve stop 42b, the fixing member 46 becomes an intermediate pressure chamber as a result. 41 is configured to open only to 41. Thereby, it can suppress that a working fluid leaks between the intermediate
  • the intermediate pressure chamber 41 shown in FIG. 3 has a suction volume equal to or larger than the suction volume of the compression chamber 15 so that the injection amount into the compression chamber 15 can be sufficiently supplied.
  • the suction volume is the volume of the compression chamber 15 when the working fluid guided from the suction port 17 is closed in the compression chamber 15, that is, when the suction process is completed, and the first compression chamber 15a and the second compression chamber.
  • the intermediate pressure chamber 41 is provided so as to spread on the plane of the end plate of the fixed scroll 12 to increase the volume.
  • the volume of the intermediate pressure chamber 41 is preferably not less than the suction volume of the compression chamber 15 and not more than 1 ⁇ 2 of the oil volume of the sealed oil 6.
  • FIG. 6 is a view taken along line 6-6 in FIG.
  • FIG. 6 is a view of the orbiting scroll 13 engaged with the fixed scroll 12 and viewed from the back surface 13e side of the orbiting scroll 13.
  • FIG. 6 the number of turns of the spiral wrap of the fixed scroll 12 and the spiral wrap of the orbiting scroll 13 are equal in a state where the fixed scroll 12 and the orbiting scroll 13 are engaged with each other.
  • the compression chamber 15 formed by the fixed scroll 12 and the orbiting scroll 13 includes a first compression chamber 15a formed on the outer wall side of the wrap of the orbiting scroll 13 and a second compression chamber 15b formed on the inner wall side of the wrap. There is.
  • the timing for confining the working fluid in the first compression chamber 15a and the timing for confining the working fluid in the second compression chamber 15b are substantially equal, and the first compression chamber 15a and the second compression chamber 15b start compression simultaneously. Thereby, the pressure balance between the 1st compression chamber 15a and the 2nd compression chamber 15b is maintained, and the behavior of the turning scroll 13 is stabilized.
  • R is a pressure curve showing the internal pressure of the compression chamber of the scroll compressor without injection operation.
  • the pressure increasing speeds of the first compression chamber 15a and the second compression chamber 15b with respect to the crank rotation angle are equal.
  • the pressure increase speed varies depending on the amount of injection.
  • Fig. 7 shows the difference in compression speed due to the difference in injection amount.
  • the discharge pressure is reached in a short compression section from the start of compression.
  • the pressure increase rate of the first compression chamber 15a shown in the pressure curve P is the pressure increase rate of the second compression chamber 15b shown in the pressure curve Q. Will be faster.
  • the discharge bypass port 21 is provided in accordance with the internal pressure of the compression chamber with a small injection amount shown in the pressure curve Q
  • the internal pressure of the compression chamber with a large injection amount shown in the pressure curve P is the internal pressure shown in the pressure curve Q. Reach the discharge pressure faster.
  • the discharge bypass port 21 is provided at a position where the first compression chamber 15a having a large injection amount can be discharged at an earlier timing than the second compression chamber 15b.
  • the internal pressure of the compression chamber is increased by the injection refrigerant, and in the compression chamber in which the injection amount is small or not injected, the pressure increase is slower than the other.
  • the discharge bypass port 21 is provided at a position where the first compression chamber 15a having a large injection amount can be discharged at an earlier timing than the second compression chamber 15b.
  • the volume ratio defined by the ratio of the suction volume of the compression chamber to the volume of the compression chamber that allows the refrigerant to be discharged by communicating with the discharge port or the discharge bypass port 21 is the first compression with a large injection amount. It is made small in the chamber 15a.
  • the opening section of the injection port 43 to the second compression chamber 15b overlaps at least a part of the oil supply section from the back pressure chamber 29 to the second compression chamber 15b.
  • the overlapping section in which the fueling section overlaps with the opening section is a partial section in the latter half of the fueling section, and the injection port 43 opens in the latter half of the fueling section and the opening section starts.
  • the lap tip 13c of the orbiting scroll 13 is gradually increased in height from the winding start portion which is the central portion to the winding end portion which is the outer peripheral portion based on the measurement result of the temperature distribution during operation.
  • a slope shape is provided so as to be. This absorbs a dimensional change due to thermal expansion and facilitates preventing local sliding.
  • FIG. 8 is an explanatory diagram showing the positional relationship between the oil supply path and the seal member accompanying the turning motion of the scroll compressor according to the present embodiment.
  • FIG. 8 shows a state in which the orbiting scroll 13 is engaged with the fixed scroll 12 and viewed from the back surface 13e side of the orbiting scroll 13, and the phase is shifted by 90 degrees.
  • the first opening end 55 a of the connection path 55 is formed on the back surface 13 e of the orbiting scroll 13.
  • the back surface 13 e of the orbiting scroll 13 is partitioned by the seal member 78 into an inner high pressure region 30 and an outer back pressure chamber 29.
  • the first opening end 55a is open to the back pressure chamber 29 that is outside the seal member 78, so that the oil 6 is supplied.
  • FIGS. 8A, 8C, and 8D the first opening end 55a is opened inside the seal member 78, so that no oil is supplied.
  • the first opening end 55a of the connection path 55 travels between the high pressure region 30 and the back pressure chamber 29, but only when a pressure difference occurs between the first opening end 55a and the second opening end 55b of the connection path 55.
  • Oil 6 is supplied to the pressure chamber 29.
  • the passage diameter of the connection passage 55 is configured to be 10 times or more that of the oil filter. It becomes possible.
  • a scroll compressor that realizes performance can be provided.
  • the case where the second opening end 55b is always in the high pressure region 30 and the first opening end 55a travels between the high pressure region 30 and the back pressure chamber 29 has been described as an example. Even when the first opening end 55a is always in the back pressure chamber 29, the pressure difference occurs between the first opening end 55a and the second opening end 55b, so that intermittent lubrication is realized. The same effect can be obtained.
  • FIG. 9 is an explanatory diagram showing an oil supply path and an injection port opening state associated with the turning motion of the scroll compressor according to the present embodiment.
  • FIG. 9 shows a state where the orbiting scroll 13 is engaged with the fixed scroll 12, and the phase is shifted by 90 degrees.
  • intermittent communication is realized by periodically opening the third opening end 56 a of the passage 13 a formed in the wrap tip 13 c into the recess 12 a formed in the end plate of the fixed scroll 12. Yes.
  • the third opening end 56a opens into the recess 12a.
  • the oil 6 passes from the back pressure chamber 29 to the second compression chamber 15b through the supply path 56 and the passage 13a. Supplied.
  • the oil supply path is provided by the third opening end 56a at a position that opens to the second compression chamber 15b in the compression stroke after the intake refrigerant is closed.
  • FIGS. 9A, 9 ⁇ / b> B, and 9 ⁇ / b> C the third opening end 56 a is not opened in the recess 12 a, so that the oil 6 is not supplied from the back pressure chamber 29 to the second compression chamber 15 b. .
  • the oil 6 in the back pressure chamber 29 is intermittently guided to the second compression chamber 15b through the oil supply path, the pressure fluctuation in the back pressure chamber 29 can be suppressed, and the predetermined pressure can be maintained. It becomes possible to control.
  • the oil 6 supplied to the second compression chamber 15b plays a role of improving the sealing property and the lubricating property during compression.
  • the injection port 43 opens in the state shown in FIG.
  • the opening section of the injection port 43 is substantially equal as the section between the first compression chamber 15a and the second compression chamber 15b, but the first compression chamber 15a is performing injection into the compression chamber having a low pressure immediately after the start of compression.
  • more injection refrigerant is fed, and the pressure increase in the first compression chamber 15a is accelerated relative to the second compression chamber 15b.
  • the injection refrigerant can be compressed without flowing back to the suction port 17 in any of the compression chambers, it is easy to increase the amount of refrigerant circulation, and a highly efficient injection operation is possible.
  • the injection port 43 is provided at a position that sequentially opens into the first compression chamber 15a and the second compression chamber 15b. Further, as shown in FIGS. 9C and 9D, the injection port 43 is opened to the first compression chamber 15a during the compression stroke after the intake refrigerant is closed, or FIG. 9A. (B), the end plate of the fixed scroll 12 is provided so as to penetrate the second compression chamber 15b in the compression stroke after the suction refrigerant is closed.
  • the oil supply section starts from (C) to (D) in FIG. 9, and the injection port 43 opens to the second compression chamber 15 b between (A) and (B) in FIG.
  • the opening section of the injection port 43 has an overlapping section with the refueling section.
  • the oil supply section is equal to the opening of the third opening end 56a into the recess 12a.
  • the pressure in the back pressure chamber 29 depends on the internal pressure of the compression chamber 15 at the end of the oil supply section, and the injection refrigerant is fed into the compression chamber 15 from the middle of the oil supply section, so that the pressure in the back pressure chamber 29 is only during the injection operation. Can be suppressed, and instability of the behavior of the orbiting scroll 13 can be suppressed.
  • At least part of the oil supply section to the compression chamber 15 is configured to overlap with the opening section of the injection port 43.
  • the pressure applied from the back surface 13e to the orbiting scroll 13 increases with the internal pressure of the compression chamber 15 in the oil supply section as the intermediate pressure of the injection refrigerant increases. Therefore, the orbiting scroll 13 is more stably pressed against the fixed scroll 12, reducing leakage from the back pressure chamber 29 to the compression chamber 15 and performing stable operation. Thereby, the behavior of the orbiting scroll 13 can be realized more stably, the optimum performance can be realized, and the injection rate can be further improved.
  • a discharge port 18 that discharges the refrigerant compressed in the compression chamber 15 is provided at the center of the end plate of the fixed scroll 12, and a discharge bypass provided as a discharge bypass port 21 at a position communicating with the first compression chamber 15a.
  • a port 21a and a discharge bypass port 21b provided at a position communicating with the second compression chamber 15b are provided.
  • the first compression chamber 15a closes the intake refrigerant in the state of FIG. 9C, and the discharge bypass port 21a opens to the first compression chamber 15a in the state of FIG. 9D.
  • the second compression chamber 15b closes the suction refrigerant in the state of FIG. 9C, but the discharge bypass port 21b is still in the second compression chamber 15b in the states of FIG. 9D and FIG. Is not communicated, and is in the state of FIG. 9B and communicates with the second compression chamber 15b.
  • the 1st compression chamber 15a takes in more injection refrigerant
  • the provision of the discharge bypass port 21a that communicates with the first compression chamber 15a and the discharge bypass port 21b that communicates with the second compression chamber 15b also allows the refrigerant in the compression chamber 15 to be discharged.
  • the volume ratio that is the ratio of the suction volume to the discharge volume can be made smaller in the first compression chamber 15a than in the second compression chamber 15b. Therefore, an excessive pressure increase in the first compression chamber 15a can be suppressed even in the maximum injection state.
  • FIG. 10 is a longitudinal sectional view of a scroll compressor according to the second embodiment of the present invention.
  • a first injection port 48a that opens only to the first compression chamber 15a and a second injection port 48b that opens only to the second compression chamber 15b are provided.
  • a first check valve 47a is provided in the first injection port 48a, and a second check valve 47b is provided in the second injection port 48b. Since other configurations are the same as those in the above embodiment, the same reference numerals are given and description thereof is omitted.
  • the amount of refrigerant injected from the first injection port 48a into the first compression chamber 15a can be reduced from the second injection port 48b.
  • the amount of refrigerant injected into the second compression chamber 15b is larger.
  • the first compression chamber 15a and the second compression chamber 15b are provided. It becomes possible to individually adjust the injection amount. Further, it is possible to always inject the first compression chamber 15a and the second compression chamber 15b, or simultaneously inject the first compression chamber 15a and the second compression chamber 15b, and the pressure difference of the refrigeration cycle is large. It is effective to realize a high injection rate under certain conditions. Further, since the degree of freedom in setting the oil supply section from the back pressure chamber 29 is increased, the pressure adjustment function from the back pressure chamber 29 can be effectively utilized, and the pressure application from the back surface 13e of the orbiting scroll 13 can be stably performed. Can be controlled.
  • the case where the first injection port 48a has a larger port diameter than the second injection port 48b is shown.
  • the opening section where the first injection port 48a opens to the first compression chamber 15a is longer than the opening section where the second injection port 48b opens to the second compression chamber 15b. May be.
  • the pressure difference between the intermediate pressure in the first injection port 48a and the internal pressure in the first compression chamber 15a is the second compression chamber of the second injection port 48b.
  • the pressure difference between the intermediate pressure in the second injection port 48b and the internal pressure of the second compression chamber 15b at the time of opening to 15b can be made larger.
  • first injection port 48a and the second injection port 48b that open only to the first compression chamber 15a and the second compression chamber 15b have been described. However, only the injection ports opened in both the first compression chamber 15a and the second compression chamber 15b shown in the first embodiment, and the first compression chamber 15a and the second compression chamber 15b shown in the present embodiment, respectively.
  • the first injection port 48a and the second injection port 48b that are opened may be combined to increase the amount of injection into the first compression chamber 15a than the amount of injection into the second compression chamber 15b.
  • the scroll compressor according to the first disclosure includes the discharge port that discharges the refrigerant compressed in the compression chamber at the center of the end plate of the fixed scroll, and compresses the compression chamber before it communicates with the discharge port.
  • a discharge bypass port for discharging the refrigerant compressed in the chamber is provided.
  • at least one injection port for injecting the intermediate pressure refrigerant into the first compression chamber and the second compression chamber is opened to the first compression chamber or the second compression chamber in the compression stroke after the suction refrigerant is closed.
  • the end plate of the fixed scroll is provided at a position where it is inserted.
  • one compression chamber that increases the amount of refrigerant injected from the injection port is connected to the other compression chamber so that the refrigerant in the compression chamber can be discharged.
  • the discharge bypass port is arranged so that the volume ratio, which is the ratio of the suction volume to the discharge volume, becomes small.
  • the volume ratio of the first compression chamber and the second compression chamber is also equal,
  • the internal pressure of the compression chamber reaches the discharge pressure in a shorter compression section than the other compression chamber.
  • the dischargeable port and the compression chamber do not communicate with each other, excessive compression occurs, requiring not only excessive compression power, but also pulling the orbiting scroll away from the fixed scroll This generates force, leading to instability of the compression motion.
  • the injection port is provided with a check valve that allows a refrigerant flow to the compression chamber and inhibits the refrigerant flow from the compression chamber.
  • the check valve and the compression chamber close to each other, even if the internal pressure of the compression chamber rises above the intermediate pressure in the section where the injection port is open to the compression chamber, the compression of the injection pipe or the like Therefore, it is possible to minimize the refrigerant compression in the space that is ineffective, and to increase the injection rate up to the condition where the theoretical performance of the injection cycle can be maximized.
  • an oil storage part for storing oil is formed in a sealed container having a fixed scroll and a turning scroll therein, and a high pressure is provided on a rear surface of the turning scroll.
  • An area and a back pressure chamber are formed.
  • the oil supply path for supplying oil from the oil storage section to the compression chamber passes through the back pressure chamber, and the oil supply path in which the back pressure chamber communicates with the first compression chamber or the second compression chamber is the compression after the suction refrigerant is closed. It is provided at a position that opens to the first compression chamber or the second compression chamber during the stroke. Further, at least a part of the oil supply section in which the oil supply path communicates with the first compression chamber or the second compression chamber is overlapped with the opening section where the injection port opens into the first compression chamber or the second compression chamber.
  • the force that presses the orbiting scroll to the fixed scroll is linked to the pressure in the compression chamber that communicates with the oil supply path, so that the more intermediate pressure refrigerant is injected into the compression chamber, the more the orbiting scroll The force that pushes the fixed scroll to the fixed scroll is also increased, and the orbiting scroll can be stably operated without leaving the fixed scroll.
  • an overlapping section in which the fueling section overlaps with the opening section is defined as a part of the latter half of the fueling section.
  • the back pressure chamber pressure corresponding to the internal pressure in the compression chamber in a state where injection has been completed or more injected can be set.
  • the pressure in the back pressure chamber is high under conditions where the revolving force of the orbiting scroll due to injection is large, and stable orbiting is possible, while the pressure in the back pressure chamber is low under conditions where the amount of injection is small, It is possible to prevent excessive pressing force.
  • At least one injection port is provided at a position that sequentially opens into the first compression chamber and the second compression chamber.
  • the injection port can be shared when injecting into both the first compression chamber and the second compression chamber, not only can the size and the number of components be reduced, but also the injection rate can be increased. It is possible to maximize the injection cycle effect. Further, in the scroll compressor, since the compression start timing is generally 180 degrees different between the first compression chamber and the second compression chamber, a position where injection is performed immediately after the start of compression from any one injection port to any compression chamber. It is also possible to provide a high injection rate.
  • a sixth disclosure is a scroll compressor according to any one of the first to fourth disclosures, and as the injection port, a first injection port that opens only in the first compression chamber, and a second And a second injection port that opens only to the compression chamber. Further, any one of the following configurations (1) to (3) is added.
  • the first injection port has a larger port diameter than the second injection port.
  • the opening section where the first injection port opens into the first compression chamber is longer than the opening section where the second injection port opens into the second compression chamber.
  • the pressure difference between the intermediate pressure in the first injection port and the internal pressure in the first compression chamber when the first injection port opens into the first compression chamber is the opening of the second injection port into the second compression chamber.
  • the pressure difference between the intermediate pressure in the second injection port and the internal pressure in the second compression chamber at the time is larger.
  • the amount of injection into the first compression chamber having a large volume and a slow pressure increase rate can be surely increased, and an efficient injection refrigerant amount can be distributed.
  • the scroll compressor of the present invention is useful for a refrigeration cycle apparatus such as a hot water heater, an air conditioner, a water heater, or a refrigerator in which an evaporator is used in a low temperature environment.

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Abstract

Provided is a scroll compressor, wherein at least one injection port is provided, passing through a mirror plate of a fixed scroll (12), at a position open to a first compression chamber (15a) or a second compression chamber (15b), which is in a compression stroke performed after sealing a suctioned refrigerant. In addition, among the first compression chamber (15a) and the second compression chamber (15b), the first compression chamber (15a), which is a compression chamber on one side and has a greater amount of refrigerant injected from an injection port (43) than the second compression chamber (15b), is provided with a discharge bypass port (21) such that the volume ratio of the suctioned volume to discharged volume of the second compression chamber (15b) is reduced to allow the refrigerant in the first compression chamber (15a) to be discharged to the second compression chamber (15b), which is the compression chamber on the other side.

Description

スクロール圧縮機Scroll compressor
 本発明は、特に空気調和機、給湯器、冷蔵庫等の冷凍機に用いられる、スクロール圧縮機に関する。 The present invention relates to a scroll compressor used in refrigerators such as an air conditioner, a water heater, and a refrigerator.
 冷凍装置や空気調和装置には、蒸発器で蒸発したガス冷媒を吸入し、凝縮器にて凝縮させるために必要な圧力までガス冷媒を圧縮して冷媒回路中に高温高圧のガス冷媒を送り出す圧縮機が使用されている。そして、スクロール圧縮機は、凝縮器と蒸発器との間に2つの膨張弁を設け、2つの膨張弁の間を流れる中間圧の冷媒を圧縮工程中の圧縮室内にインジェクションすることで、冷凍サイクルの消費電力削減や能力向上を図っている。 For refrigeration equipment and air conditioning equipment, compression is performed by sucking the gas refrigerant evaporated in the evaporator, compressing the gas refrigerant to the pressure required for condensation in the condenser, and sending the high-temperature and high-pressure gas refrigerant into the refrigerant circuit The machine is being used. The scroll compressor is provided with two expansion valves between the condenser and the evaporator, and the intermediate pressure refrigerant flowing between the two expansion valves is injected into the compression chamber during the compression process, thereby providing a refrigeration cycle. To reduce power consumption and improve capacity.
 すなわち、凝縮器を循環する冷媒は、インジェクションされた冷媒量だけ増加し、空調機であれば暖房能力が向上する。また、インジェクションされる冷媒は、中間圧状態であり、圧縮に必要な動力は、中間圧から高圧までであるため、インジェクションを行わずに同じ能力を実現する場合に比べて、COP(Coefficient Of Performance)が向上し、消費電力も削減できる。 That is, the refrigerant circulating through the condenser increases by the amount of injected refrigerant, and if it is an air conditioner, the heating capacity is improved. In addition, since the refrigerant to be injected is in an intermediate pressure state and the power necessary for compression is from the intermediate pressure to the high pressure, COP (Coefficient Of Performance) is achieved compared to the case where the same capability is realized without performing injection. ) And power consumption can be reduced.
 凝縮器を流れる冷媒量は、蒸発器を流れる冷媒量とインジェクションされる冷媒量との和に等しく、凝縮器の冷媒量に対するインジェクション冷媒量の比がインジェクション率である。 The amount of refrigerant flowing through the condenser is equal to the sum of the amount of refrigerant flowing through the evaporator and the amount of refrigerant injected, and the ratio of the amount of injected refrigerant to the amount of refrigerant in the condenser is the injection rate.
 インジェクションの効果を大きくするには、インジェクション率を高くすればよい。そして、インジェクションされる冷媒圧と圧縮室の内圧との圧力差で冷媒がインジェクションされるため、インジェクション率を高くするには、インジェクションされる冷媒圧を高くする必要がある。 To increase the effect of injection, the injection rate should be increased. And since a refrigerant | coolant is injected by the pressure difference of the refrigerant | coolant pressure injected and the internal pressure of a compression chamber, in order to make an injection rate high, it is necessary to raise the refrigerant | coolant pressure injected.
 しかし、インジェクションされる冷媒圧を高くすると、液冷媒が圧縮室にインジェクションされてしまい、暖房能力の低下や圧縮機の信頼性低下を招いてしまう。 However, if the refrigerant pressure to be injected is increased, the liquid refrigerant is injected into the compression chamber, leading to a reduction in heating capacity and a reduction in the reliability of the compressor.
 インジェクション管から圧縮室に流入する冷媒は、気液分離器からガス冷媒を優先的に取り出して送り込まれるが、中間圧制御のバランスが崩れた場合や過渡的な条件変化の際には、ガス冷媒に液冷媒が混ざった状態でインジェクション管から流入する。摺動部分を多く有する圧縮室には、摺動状態を良好に保つために適量のオイルを送り込んで冷媒とともに圧縮しているが、液冷媒が混入すると圧縮室のオイルが液冷媒によって洗い流されることで、摺動状態が悪化し、部品磨耗や焼き付きが生じる。従って、インジェクション管から流入した液冷媒は、極力圧縮室には送り込まず、ガス冷媒だけをインジェクションポートに導くことが重要となる。 The refrigerant flowing into the compression chamber from the injection pipe is preferentially taken out and sent from the gas-liquid separator. However, when the balance of the intermediate pressure control is lost or transient conditions change, the gas refrigerant It flows from the injection tube in a state where liquid refrigerant is mixed. In order to maintain a good sliding state, an appropriate amount of oil is fed into the compression chamber having many sliding parts and compressed together with the refrigerant. When liquid refrigerant is mixed, the oil in the compression chamber is washed away by the liquid refrigerant. As a result, the sliding state deteriorates, and component wear and seizure occur. Therefore, it is important that the liquid refrigerant flowing from the injection pipe is not sent into the compression chamber as much as possible, and only the gas refrigerant is guided to the injection port.
 気液分離器の上流側および下流側にそれぞれ設けた膨張弁の開度を調整することで、中間圧を制御し、インジェクション管が最終的に繋がる圧縮機内の圧縮室の内圧と中間圧との圧力差でインジェクション冷媒を圧縮室に送り込む。このため、中間圧を高く調整すればインジェクション率は増加する。一方で、凝縮器から上流側の膨張弁を通って気液分離器に流入する冷媒中の気相成分比率は、中間圧が高いほど少なくなるため、過剰に中間圧を上げると気液分離器の液冷媒が増加し、液冷媒がインジェクション管に流れ込み、暖房能力の低下や圧縮機の信頼性低下を招く。よって、圧縮機としてはできるだけ低い中間圧で多くのインジェクション冷媒を取り込める構成が望ましく、圧縮方式としては圧縮速度が緩やかなスクロール型が適している。 By adjusting the opening degree of the expansion valve provided on the upstream side and downstream side of the gas-liquid separator, the intermediate pressure is controlled, and the internal pressure and the intermediate pressure of the compression chamber in the compressor to which the injection pipe is finally connected are controlled. The injection refrigerant is sent into the compression chamber by the pressure difference. For this reason, if the intermediate pressure is adjusted high, the injection rate increases. On the other hand, since the gas phase component ratio in the refrigerant flowing from the condenser through the upstream expansion valve to the gas-liquid separator decreases as the intermediate pressure increases, the gas-liquid separator increases when the intermediate pressure is excessively increased. The liquid refrigerant increases, and the liquid refrigerant flows into the injection pipe, resulting in a decrease in heating capacity and a decrease in the reliability of the compressor. Therefore, it is desirable for the compressor to be able to take in a large amount of injection refrigerant at the lowest possible intermediate pressure, and as the compression method, a scroll type with a moderate compression speed is suitable.
 中でも、旋回スクロールラップの外側と内側に同じタイミングで容積の等しい圧縮室が形成される対称型スクロール圧縮機は、圧縮室の対称性から低振動で力学的なバランスが優れているなどの特徴を有しており、空調用途をはじめ、様々な分野で用いられてきた。 Above all, the symmetrical scroll compressor, in which compression chambers with the same volume are formed at the same timing on the outer and inner sides of the orbiting scroll wrap, has features such as low vibration and excellent mechanical balance due to the symmetry of the compression chamber. It has been used in various fields including air conditioning applications.
 一方、インジェクションに関しては、従来のスクロール圧縮機では、インジェクションポートおよびバイパスポートの開口範囲について開示されている(例えば、特許文献1参照)。これにより、インジェクションを含めた多様な運転モードに性能よく対応できるスクロール圧縮機を提供している。 On the other hand, regarding the injection, the conventional scroll compressor discloses the opening range of the injection port and the bypass port (see, for example, Patent Document 1). Thereby, the scroll compressor which can respond | correspond with various performance modes including injection with sufficient performance is provided.
特許第3764261号公報Japanese Patent No. 3764261
 対称型スクロール圧縮機においては、旋回スクロールラップの外側に形成される第1圧縮室と、旋回スクロールラップの内側に形成される第2圧縮室の圧縮開始のタイミングが等しく、単一のインジェクションポートから第1圧縮室および第2圧縮室に対して常に同じ量のインジェクション冷媒を送り込むことは難しい。 In the symmetric scroll compressor, the compression start timings of the first compression chamber formed outside the orbiting scroll wrap and the second compression chamber formed inside the orbiting scroll wrap are equal, and a single injection port is used. It is difficult to always feed the same amount of injection refrigerant into the first compression chamber and the second compression chamber.
 また、特許文献1においては、バイパスポートとインジェクションポートの開口区間の関係については開示されているものの、第1圧縮室および第2圧縮室へのインジェクション量とバイパスポートとの関係については開示されていない。 Further, in Patent Document 1, although the relationship between the bypass port and the opening section of the injection port is disclosed, the relationship between the amount of injection into the first compression chamber and the second compression chamber and the bypass port is disclosed. Absent.
 本発明は、対称型スクロール圧縮機で必然的に生じるインジェクション量の違いによる過圧縮運転を回避し、インジェクションサイクル本来の効果を最大化し得るために、より高いインジェクション率での運転にも高効率に対応でき、能力向上量についても拡大できるスクロール圧縮機を提供する。 The present invention avoids over-compression operation due to the difference in injection amount that inevitably occurs in a symmetric scroll compressor, and maximizes the original effect of the injection cycle. Therefore, the present invention is highly efficient for operation at a higher injection rate. To provide a scroll compressor that can cope with the increase in capacity.
 本発明のスクロール圧縮機は、鏡板から渦巻き状のラップが立ち上がる固定スクロール及び旋回スクロールを備え、固定スクロールのラップと旋回スクロールのラップとを噛み合わせて、固定スクロールと旋回スクロールとの間に圧縮室を形成する。また、圧縮室として、旋回スクロールのラップの外壁側に形成される第1圧縮室と、旋回スクロールのラップの内壁側に形成される第2圧縮室とが形成され、第1圧縮室の吸入容積が第2圧縮室の吸入容積とほぼ等しい。また、固定スクロールの鏡板の中心部に、圧縮室で圧縮した冷媒を吐出する吐出ポートを備え、圧縮室が吐出ポートと連通する前に圧縮室で圧縮した冷媒を吐出する吐出バイパスポートを設ける。また、第1圧縮室及び第2圧縮室に中間圧の冷媒をインジェクションする、少なくとも1つのインジェクションポートを、吸入冷媒を閉じ込み後の圧縮行程中にある第1圧縮室又は第2圧縮室に開口する位置に、固定スクロールの鏡板を貫通して設ける。さらに、第1圧縮室及び第2圧縮室の内、インジェクションポートからインジェクションする冷媒量を多くする一方の圧縮室が、他方の圧縮室に対して、圧縮室の冷媒が吐出可能となる圧縮室の吐出容積に対する吸入容積の比である容積比が小さくなるように吐出バイパスポートを配置する。 A scroll compressor according to the present invention includes a fixed scroll and a turning scroll in which a spiral wrap rises from an end plate. Form. Also, as the compression chamber, a first compression chamber formed on the outer wall side of the orbiting scroll wrap and a second compression chamber formed on the inner wall side of the orbiting scroll wrap are formed, and the suction volume of the first compression chamber Is substantially equal to the suction volume of the second compression chamber. In addition, a discharge port that discharges the refrigerant compressed in the compression chamber is provided at the center of the end plate of the fixed scroll, and a discharge bypass port that discharges the refrigerant compressed in the compression chamber is provided before the compression chamber communicates with the discharge port. Further, at least one injection port for injecting the intermediate pressure refrigerant into the first compression chamber and the second compression chamber is opened to the first compression chamber or the second compression chamber in the compression stroke after the suction refrigerant is closed. The end plate of the fixed scroll is provided at a position where it is inserted. Furthermore, of the first compression chamber and the second compression chamber, one of the compression chambers that increases the amount of refrigerant injected from the injection port is a compression chamber that can discharge the refrigerant in the compression chamber to the other compression chamber. The discharge bypass port is arranged so that the volume ratio, which is the ratio of the suction volume to the discharge volume, becomes small.
 このように、容積比の小さい圧縮室に対して多くのインジェクションを行うことで、インジェクション率を高め、インジェクションサイクル効果を最大化して、従来以上の効率向上と能力拡大効果を得ることが可能となる。 In this way, by performing many injections on the compression chamber with a small volume ratio, it is possible to increase the injection rate and maximize the injection cycle effect, and to obtain the efficiency improvement and capacity expansion effects over the conventional ones. .
図1は、本発明の第1の実施の形態によるスクロール圧縮機を備えた冷凍サイクル図である。FIG. 1 is a refrigeration cycle diagram provided with a scroll compressor according to a first embodiment of the present invention. 図2は、本発明の第1の実施の形態によるスクロール圧縮機の縦断面図である。FIG. 2 is a longitudinal sectional view of the scroll compressor according to the first embodiment of the present invention. 図3は、図2の要部拡大図である。FIG. 3 is an enlarged view of a main part of FIG. 図4は、図3の4-4線矢視図である。FIG. 4 is a view taken along line 4-4 in FIG. 図5は、図4の5-5線矢視図である。FIG. 5 is a view taken in the direction of arrows 5-5 in FIG. 図6は、図3の6-6線矢視図である。6 is a view taken along line 6-6 in FIG. 図7は、インジェクション運転を伴わない場合のスクロール圧縮機の圧縮室の内圧を示すグラフである。FIG. 7 is a graph showing the internal pressure of the compression chamber of the scroll compressor without the injection operation. 図8は、本発明の第1の実施の形態によるスクロール圧縮機の旋回運動に伴う給油経路とシール部材との位置関係を示す説明図である。FIG. 8 is an explanatory diagram showing the positional relationship between the oil supply path and the seal member accompanying the turning motion of the scroll compressor according to the first embodiment of the present invention. 図9は、本発明の第1の実施の形態によるスクロール圧縮機の旋回運動に伴う給油経路およびインジェクションポートの開口状態を示す説明図である。FIG. 9 is an explanatory view showing an opening state of an oil supply path and an injection port accompanying a turning motion of the scroll compressor according to the first embodiment of the present invention. 図10は、本発明の第2の実施の形態によるスクロール圧縮機の縦断面図である。FIG. 10 is a longitudinal sectional view of a scroll compressor according to the second embodiment of the present invention.
 (第1の実施の形態)
 以下本発明の第1の実施の形態によるスクロール圧縮機について説明する。なお、以下の本実施の形態によって本発明が限定されるものではない。
(First embodiment)
The scroll compressor according to the first embodiment of the present invention will be described below. In addition, this invention is not limited by the following this Embodiment.
 図1は本実施の形態によるスクロール圧縮機を備えた冷凍サイクル図である。 FIG. 1 is a refrigeration cycle diagram provided with a scroll compressor according to this embodiment.
 図1に示すように、本実施の形態によるスクロール圧縮機を備えた冷凍サイクル装置は、スクロール圧縮機である圧縮機91、凝縮器92、蒸発器93、膨張弁94a、94b、インジェクション管95、および気液分離器96を備えている。 As shown in FIG. 1, the refrigeration cycle apparatus provided with the scroll compressor according to the present embodiment includes a compressor 91 that is a scroll compressor, a condenser 92, an evaporator 93, expansion valves 94a and 94b, an injection pipe 95, And a gas-liquid separator 96.
 凝縮器92で凝縮した作動流体である冷媒は上流側の膨張弁94aで中間圧まで減圧され、気液分離器96は、中間圧の冷媒の気相成分(ガス冷媒)と液相成分(液冷媒)を分離する。中間圧まで減圧された液冷媒は、更に下流側の膨張弁94bを通り、低圧冷媒となって蒸発器93に導かれる。 The refrigerant that is the working fluid condensed in the condenser 92 is decompressed to an intermediate pressure by the upstream expansion valve 94a, and the gas-liquid separator 96 is connected to the gas phase component (gas refrigerant) and the liquid phase component (liquid refrigerant) of the intermediate pressure refrigerant. (Refrigerant). The liquid refrigerant whose pressure has been reduced to the intermediate pressure further passes through the expansion valve 94b on the downstream side, and is led to the evaporator 93 as a low-pressure refrigerant.
 蒸発器93に送り込まれた液冷媒は、熱交換によって蒸発し、ガス冷媒又は一部液冷媒が混じったガス冷媒として排出される。蒸発器93から排出された冷媒は圧縮機91の圧縮室に取り込まれる。 The liquid refrigerant sent to the evaporator 93 evaporates by heat exchange and is discharged as a gas refrigerant mixed with a gas refrigerant or a part of the liquid refrigerant. The refrigerant discharged from the evaporator 93 is taken into the compression chamber of the compressor 91.
 一方、気液分離器96で分離された中間圧状態のガス冷媒は、インジェクション管95を通り、圧縮機91内の圧縮室に導かれる。なお、図示していないが、インジェクション管95に閉塞弁や膨張弁を設け、インジェクションする圧力を調整、停止する構成を設けても良い。 On the other hand, the intermediate-pressure gas refrigerant separated by the gas-liquid separator 96 passes through the injection pipe 95 and is guided to the compression chamber in the compressor 91. Although not shown, a configuration may be provided in which a blocking valve or an expansion valve is provided in the injection pipe 95 to adjust and stop the injection pressure.
 圧縮機91は蒸発器93から流入する低圧冷媒を圧縮し、圧縮過程において気液分離器96の中間圧の冷媒を圧縮室に噴射(インジェクション)させて圧縮し、高温高圧冷媒を吐出管から凝縮器92に送り出す。 The compressor 91 compresses the low-pressure refrigerant flowing in from the evaporator 93, and in the compression process, the intermediate-pressure refrigerant of the gas-liquid separator 96 is injected (injected) into the compression chamber for compression, and the high-temperature high-pressure refrigerant is condensed from the discharge pipe. To the container 92.
 気液分離器96で分離される気相成分と液相成分の比率は、上流側に設けた膨張弁94aの入口側圧力と出口側圧力との圧力差が大きいほど気相成分が多く、また凝縮器92出口の冷媒の過冷却度が小さい、もしくは渇き度が大きいほど気相成分が多くなる。 The ratio between the gas phase component and the liquid phase component separated by the gas-liquid separator 96 is such that the larger the pressure difference between the inlet side pressure and the outlet side pressure of the expansion valve 94a provided on the upstream side, the larger the gas phase component, The smaller the degree of supercooling of the refrigerant at the outlet of the condenser 92, or the greater the degree of thirst, the more gas phase components.
 一方、圧縮機91がインジェクション管95を介して吸入する冷媒の量は、中間圧が高いほど多くなるため、気液分離器96で分離される冷媒の気相成分比率よりも多くインジェクション管95から冷媒を吸い込むと、気液分離器96のガス冷媒が枯渇し、インジェクション管95に液冷媒が流入する。圧縮機91の能力を最大限に発揮するためには、気液分離器96において分離されるガス冷媒が余すことなくインジェクション管95から圧縮機91に吸い込まれることが望ましい。しかし、その均衡状態から外れてしまうとインジェクション管95から圧縮機91に液冷媒が流入するため、そのような場合においても圧縮機91が高い信頼性を維持できるよう構成する必要がある。 On the other hand, since the amount of refrigerant sucked by the compressor 91 through the injection pipe 95 increases as the intermediate pressure increases, the amount of the refrigerant separated by the gas-liquid separator 96 exceeds the ratio of the gas phase components of the refrigerant from the injection pipe 95. When the refrigerant is sucked, the gas refrigerant in the gas-liquid separator 96 is exhausted and the liquid refrigerant flows into the injection pipe 95. In order to maximize the performance of the compressor 91, it is desirable that the gas refrigerant separated in the gas-liquid separator 96 is sucked into the compressor 91 from the injection pipe 95 without leaving any excess. However, since the liquid refrigerant flows into the compressor 91 from the injection pipe 95 when the equilibrium state is deviated, the compressor 91 needs to be configured to maintain high reliability even in such a case.
 図2は、本実施の形態によるスクロール圧縮機の縦断面図である。図3は図2の要部拡大図である。図4は図3の4-4線矢視図である。図5は図4の4-4線矢視図である。 FIG. 2 is a longitudinal sectional view of the scroll compressor according to this embodiment. FIG. 3 is an enlarged view of a main part of FIG. FIG. 4 is a view taken along line 4-4 of FIG. FIG. 5 is a view taken along line 4-4 in FIG.
 図2に示すように、圧縮機91は、密閉容器1の内部に、圧縮機構2、モータ部3、貯油部20を備えている。 2, the compressor 91 includes a compression mechanism 2, a motor unit 3, and an oil storage unit 20 inside the sealed container 1.
 圧縮機構2は、密閉容器1に溶接や焼き嵌めによって固定した主軸受部材11と、主軸受部材11上にボルト止めした固定スクロール(圧縮室区画部材)12と、固定スクロール12と噛み合う旋回スクロール13とを有する。シャフト4は主軸受部材11で軸支されている。 The compression mechanism 2 includes a main bearing member 11 fixed to the sealed container 1 by welding or shrink fitting, a fixed scroll (compression chamber partition member) 12 bolted on the main bearing member 11, and a turning scroll 13 meshing with the fixed scroll 12. And have. The shaft 4 is pivotally supported by the main bearing member 11.
 旋回スクロール13と主軸受部材11との間には、旋回スクロール13の自転を防止して円軌道運動するように案内するオルダムリングなどによる自転拘束機構14を設けている。 Between the orbiting scroll 13 and the main bearing member 11, there is provided a rotation restraint mechanism 14 such as an Oldham ring that guides the orbiting scroll 13 to rotate and prevent it from rotating.
 旋回スクロール13は、シャフト4の上端にある偏心軸部4aにて偏心駆動し、自転拘束機構14によって円軌道運動する。 The orbiting scroll 13 is eccentrically driven by the eccentric shaft portion 4 a at the upper end of the shaft 4, and moves in a circular orbit by the rotation restraint mechanism 14.
 圧縮室15は、固定スクロール12と旋回スクロール13との間に形成される。 The compression chamber 15 is formed between the fixed scroll 12 and the orbiting scroll 13.
 吸入パイプ16は密閉容器1外に通じ、固定スクロール12の外周部には吸入ポート17を設けている。吸入パイプ16から吸入される作動流体(冷媒)は、吸入ポート17から圧縮室15に導かれる。圧縮室15は、外周側から中央部に向かって容積を縮めながら移動し、圧縮室15で所定の圧力に到達した作動流体は、固定スクロール12の中央部に設けた吐出ポート18から吐出室31に吐出される。吐出ポート18には吐出リード弁19を設けている。圧縮室15で所定の圧力に到達した作動流体は、吐出リード弁19を押し開いて吐出室31に吐出される。吐出室31に吐出された作動流体は、密閉容器1外に吐出される。 The suction pipe 16 communicates with the outside of the sealed container 1, and a suction port 17 is provided on the outer periphery of the fixed scroll 12. The working fluid (refrigerant) sucked from the suction pipe 16 is guided from the suction port 17 to the compression chamber 15. The compression chamber 15 moves while reducing its volume from the outer peripheral side toward the central portion, and the working fluid that has reached a predetermined pressure in the compression chamber 15 is discharged from the discharge port 18 provided in the central portion of the fixed scroll 12 to the discharge chamber 31. Discharged. The discharge port 18 is provided with a discharge reed valve 19. The working fluid that has reached a predetermined pressure in the compression chamber 15 pushes the discharge reed valve 19 open and is discharged into the discharge chamber 31. The working fluid discharged into the discharge chamber 31 is discharged out of the sealed container 1.
 一方、インジェクション管95から導かれた中間圧の作動流体は、中間圧室41に流入し、インジェクションポート43に設けた逆止弁42を開き、閉じ込み後の圧縮室15にインジェクションされ、吸入ポート17から吸い込んだ作動流体と共に吐出ポート18から密閉容器1内に吐出される。 On the other hand, the intermediate-pressure working fluid led from the injection pipe 95 flows into the intermediate pressure chamber 41, opens the check valve 42 provided in the injection port 43, and is injected into the compression chamber 15 after being closed, and the suction port Together with the working fluid sucked from 17, it is discharged into the sealed container 1 from the discharge port 18.
 シャフト4の下端にはポンプ25を設けている。ポンプ25は、その吸い込み口が貯油部20内に存在するように配置する。ポンプ25は、シャフト4によって駆動され、密閉容器1の底部に設けられた貯油部20にあるオイル6を、圧力条件や運転速度に関係なく、確実に吸い上げることができ、オイル6切れの心配も解消される。ポンプ25で吸い上げたオイル6は、シャフト4内に形成しているオイル供給穴26を通じて圧縮機構2に供給される。なお、オイル6をポンプ25で吸い上げる前もしくは吸い上げた後に、オイルフィルタ等でオイル6から異物を除去すると、圧縮機構2への異物混入が防止でき、更なる信頼性向上を図ることができる。 A pump 25 is provided at the lower end of the shaft 4. The pump 25 is arranged so that the suction port exists in the oil storage unit 20. The pump 25 is driven by the shaft 4 and can reliably suck up the oil 6 in the oil storage section 20 provided at the bottom of the hermetic container 1 regardless of the pressure condition and the operation speed. It will be resolved. The oil 6 sucked up by the pump 25 is supplied to the compression mechanism 2 through an oil supply hole 26 formed in the shaft 4. If foreign matter is removed from the oil 6 with an oil filter or the like before or after the oil 25 is sucked up by the pump 25, foreign matter can be prevented from entering the compression mechanism 2 and further reliability can be improved.
 圧縮機構2に導かれたオイル6の圧力は、スクロール圧縮機の吐出圧とほぼ同等であり、旋回スクロール13に対する背圧源ともなる。これにより、旋回スクロール13は固定スクロール12から離れたり片当たりしたりすることはなく、所定の圧縮機能を安定して発揮する。 The pressure of the oil 6 guided to the compression mechanism 2 is substantially equal to the discharge pressure of the scroll compressor, and also serves as a back pressure source for the orbiting scroll 13. As a result, the orbiting scroll 13 does not move away from the fixed scroll 12 and does not come into contact with each other, and the predetermined compression function is stably exhibited.
 図3に示すように、旋回スクロール13の鏡板の背面13eにはリング状のシール部材78を配置している。 As shown in FIG. 3, a ring-shaped seal member 78 is disposed on the back surface 13 e of the end plate of the orbiting scroll 13.
 シール部材78の内側には高圧領域30が形成され、シール部材78の外側には背圧室29が形成される。背圧室29は、高圧と低圧との間の圧力に設定されている。シール部材78を用いることにより、高圧領域30と背圧室29とを分離できるため、旋回スクロール13の背面13eからの圧力付加を安定的に制御できる。 The high pressure region 30 is formed inside the seal member 78, and the back pressure chamber 29 is formed outside the seal member 78. The back pressure chamber 29 is set to a pressure between a high pressure and a low pressure. By using the seal member 78, the high pressure region 30 and the back pressure chamber 29 can be separated, so that pressure application from the back surface 13e of the orbiting scroll 13 can be stably controlled.
 なお、図3の6-6線矢視図である図6に示すように、固定スクロール12と旋回スクロール13により形成される圧縮室15には、旋回スクロール13のラップの外壁側に形成される第1圧縮室15aと、ラップの内壁側に形成される第2圧縮室15bとがある。 As shown in FIG. 6 as viewed in the direction of arrows 6-6 in FIG. 3, the compression chamber 15 formed by the fixed scroll 12 and the orbiting scroll 13 is formed on the outer wall side of the wrap of the orbiting scroll 13. There are a first compression chamber 15a and a second compression chamber 15b formed on the inner wall side of the wrap.
 図3に示す貯油部20からの給油経路としては、高圧領域30から背圧室29への接続路55と、背圧室29から第2圧縮室15bへの供給路56とを有する。高圧領域30から背圧室29への接続路55を設けることで、自転拘束機構14の摺動部や、固定スクロール12と旋回スクロール13のスラスト摺動部にオイル6を供給することができる。 3 includes a connecting path 55 from the high pressure region 30 to the back pressure chamber 29 and a supply path 56 from the back pressure chamber 29 to the second compression chamber 15b. By providing the connection path 55 from the high pressure region 30 to the back pressure chamber 29, the oil 6 can be supplied to the sliding portion of the rotation restraint mechanism 14 and the thrust sliding portion of the fixed scroll 12 and the orbiting scroll 13.
 接続路55の一方の第1開口端55aは、旋回スクロール13の背面13eに形成し、シール部材78の内側と外側を往来し、他方の第2開口端55bは常に高圧領域30に開口している。これにより間欠給油が実現できる。 One first opening end 55 a of the connection path 55 is formed on the back surface 13 e of the orbiting scroll 13, and travels between the inside and outside of the seal member 78, and the other second opening end 55 b always opens to the high-pressure region 30. Yes. Thereby, intermittent oil supply is realizable.
 オイル6の一部は、供給圧や自重によって、逃げ場を求めるようにして偏心軸部4aと旋回スクロール13との嵌合部、シャフト4と主軸受部材11との間の軸受部66に進入してそれぞれの部分を潤滑した後落下し、貯油部20へ戻る。 A part of the oil 6 enters the fitting portion between the eccentric shaft portion 4a and the orbiting scroll 13 and the bearing portion 66 between the shaft 4 and the main bearing member 11 so as to obtain a clearance by the supply pressure and the own weight. After lubricating each part, it falls and returns to the oil storage part 20.
 本実施の形態によるスクロール圧縮機では、圧縮室15への給油経路が、旋回スクロール13の内部に形成された通路13aと、固定スクロール12のラップ面側鏡板に形成された凹部12aから構成されている。通路13aの第3開口端56aはラップ先端13cに形成し、旋回運動にあわせて周期的に凹部12aに開口させ、また通路13aの第4開口端56bは常に背圧室29に開口させている。これにより、背圧室29と第2圧縮室15bを間欠的に連通させることができる。 In the scroll compressor according to the present embodiment, the oil supply path to the compression chamber 15 is configured by a passage 13 a formed inside the orbiting scroll 13 and a recess 12 a formed on the lap surface side end plate of the fixed scroll 12. Yes. The third opening end 56a of the passage 13a is formed at the lap tip 13c, and is periodically opened in the recess 12a according to the turning motion, and the fourth opening end 56b of the passage 13a is always opened in the back pressure chamber 29. . Thereby, the back pressure chamber 29 and the 2nd compression chamber 15b can be intermittently connected.
 中間圧の冷媒をインジェクションするためのインジェクションポート43は、固定スクロール12の鏡板を貫通して設けている。インジェクションポート43は、第1圧縮室15a及び第2圧縮室15bに順次開口する。インジェクションポート43は、第1圧縮室15a及び第2圧縮室15bでの閉じ込み後の圧縮工程中に開口する位置に設けている。 The injection port 43 for injecting the intermediate pressure refrigerant is provided through the end plate of the fixed scroll 12. The injection port 43 opens sequentially to the first compression chamber 15a and the second compression chamber 15b. The injection port 43 is provided at a position that is opened during the compression process after being closed in the first compression chamber 15a and the second compression chamber 15b.
 固定スクロール12の鏡板には、吐出ポート18と連通する前に圧縮室15で圧縮した冷媒を吐出する吐出バイパスポート21を設けている。 The end plate of the fixed scroll 12 is provided with a discharge bypass port 21 that discharges the refrigerant compressed in the compression chamber 15 before communicating with the discharge port 18.
 図3から図4に示すように、本実施の形態による圧縮機91は、インジェクション管95から送り込まれ、圧縮室15にインジェクションする前の中間圧作動流体を導く中間圧室41を設けている。 As shown in FIGS. 3 to 4, the compressor 91 according to the present embodiment is provided with an intermediate pressure chamber 41 that is fed from the injection pipe 95 and guides the intermediate pressure working fluid before being injected into the compression chamber 15.
 中間圧室41は、圧縮室区画部材である固定スクロール12と、中間圧プレート44と、中間圧カバー45とで形成している。中間圧室41と圧縮室15とは、固定スクロール12を挟んで対向させている。中間圧室41は、中間圧作動流体が流入する中間圧室入口41aと、中間圧作動流体を圧縮室15にインジェクションするインジェクションポート43のインジェクションポート入口43aと、中間圧室入口41aより低い位置に形成した液溜め部41bとを有している。 The intermediate pressure chamber 41 is formed by a fixed scroll 12 that is a compression chamber partition member, an intermediate pressure plate 44, and an intermediate pressure cover 45. The intermediate pressure chamber 41 and the compression chamber 15 are opposed to each other with the fixed scroll 12 interposed therebetween. The intermediate pressure chamber 41 is located at a position lower than the intermediate pressure chamber inlet 41a into which the intermediate pressure working fluid flows, the injection port inlet 43a of the injection port 43 that injects the intermediate pressure working fluid into the compression chamber 15, and the intermediate pressure chamber inlet 41a. The liquid reservoir 41b is formed.
 液溜め部41bは固定スクロール12の鏡板の上面で形成している。 The liquid reservoir 41b is formed on the upper surface of the end plate of the fixed scroll 12.
 中間圧プレート44には、圧縮室15から中間圧室41への冷媒逆流を防止する逆止弁42が設けられている。インジェクションポート43が圧縮室15に開口している区間において、圧縮室15の内圧がインジェクションポート43の中間圧よりも高い場合には、圧縮室15から中間圧室41に向けて冷媒が逆流するため、逆止弁42を設けることにより冷媒の逆流を阻止できる。 The intermediate pressure plate 44 is provided with a check valve 42 for preventing a refrigerant backflow from the compression chamber 15 to the intermediate pressure chamber 41. In the section where the injection port 43 is open to the compression chamber 15, if the internal pressure of the compression chamber 15 is higher than the intermediate pressure of the injection port 43, the refrigerant flows backward from the compression chamber 15 toward the intermediate pressure chamber 41. The reverse flow of the refrigerant can be prevented by providing the check valve 42.
 本実施の形態による圧縮機91では、逆止弁42は圧縮室15側にリフトして圧縮室15と中間圧室41を連通させるリード弁42aで構成しており、圧縮室15の内圧が中間圧室41の圧力よりも低い時にのみ中間圧室41を圧縮室15に連通させる。リード弁42aを用いることで、可動部における摺動箇所が少なく、長期に亘りシール性を維持できるとともに、流路面積を必要に応じて拡大し易い。逆止弁42を設けなかったり、逆止弁42をインジェクション管95に設けたりした場合は、圧縮室15の冷媒がインジェクション管95まで逆流し、無駄な圧縮動力を消費することになる。本実施の形態では逆止弁42を圧縮室15に近い中間圧プレート44に設けることで圧縮室15からの逆流を抑制している。 In the compressor 91 according to the present embodiment, the check valve 42 is configured by a reed valve 42a that lifts to the compression chamber 15 side and communicates the compression chamber 15 and the intermediate pressure chamber 41, and the internal pressure of the compression chamber 15 is intermediate. The intermediate pressure chamber 41 is communicated with the compression chamber 15 only when the pressure is lower than the pressure chamber 41. By using the reed valve 42a, there are few sliding parts in a movable part, a sealing performance can be maintained for a long time, and it is easy to expand a flow path area as needed. When the check valve 42 is not provided or the check valve 42 is provided in the injection pipe 95, the refrigerant in the compression chamber 15 flows back to the injection pipe 95, and wasteful compression power is consumed. In the present embodiment, the check valve 42 is provided on the intermediate pressure plate 44 close to the compression chamber 15 to suppress the backflow from the compression chamber 15.
 固定スクロール12の鏡板の上面は、中間圧室入口41aよりも低い位置にあり、固定スクロール12の鏡板の上面に、液相成分の作動流体が溜まる液溜め部41bを設けている。また、インジェクションポート入口43aは、中間圧室入口41aの高さよりも高い位置に設けている。従って、中間圧作動流体の内、気相成分の作動流体はインジェクションポート43に導かれ、液溜め部41bに溜まった液相成分の作動流体は、高温状態にある固定スクロール12の表面で気化されるため、圧縮室15には液相成分の作動流体が流入しにくい。 The upper surface of the end plate of the fixed scroll 12 is at a position lower than the intermediate pressure chamber inlet 41a, and a liquid reservoir 41b in which a working fluid of a liquid phase component is provided on the upper surface of the end plate of the fixed scroll 12. Further, the injection port inlet 43a is provided at a position higher than the height of the intermediate pressure chamber inlet 41a. Therefore, among the intermediate pressure working fluid, the working fluid of the gas phase component is guided to the injection port 43, and the working fluid of the liquid phase component accumulated in the liquid reservoir 41b is vaporized on the surface of the fixed scroll 12 in a high temperature state. Therefore, it is difficult for the working fluid of the liquid phase component to flow into the compression chamber 15.
 さらに、中間圧室41と吐出室31とは中間圧プレート44を介して隣接する位置に設けており、中間圧室41に液相成分の作動流体が流入した際の気化を促進するとともに、吐出室31の高圧冷媒の温度上昇も抑制できるため、その分だけ高い吐出圧条件まで運転を行うことができる。 Further, the intermediate pressure chamber 41 and the discharge chamber 31 are provided at positions adjacent to each other via the intermediate pressure plate 44, and promotes vaporization when the working fluid of the liquid phase component flows into the intermediate pressure chamber 41, and discharges. Since the temperature rise of the high-pressure refrigerant in the chamber 31 can also be suppressed, the operation can be performed up to a higher discharge pressure condition.
 インジェクションポート43に導かれた中間圧作動流体は、インジェクションポート43と圧縮室15との圧力差によりリード弁42aを押し開き、吸入ポート17から吸い込んだ低圧作動流体と圧縮室15で合流する。しかし、逆止弁42から圧縮室15までの間のインジェクションポート43に残る中間圧作動流体は、再膨張と再圧縮を繰り返すため、圧縮機91の効率を低下させる要因となる。そこで、リード弁42aの最大変位量を規制するバルブストップ42b(図5参照)の厚みを、リード弁42aのリフト規制箇所に応じて変化させ、リード弁42aより下流のインジェクションポート43内体積を小さくしている。 The intermediate pressure working fluid guided to the injection port 43 pushes and opens the reed valve 42 a due to a pressure difference between the injection port 43 and the compression chamber 15, and merges with the low pressure working fluid sucked from the suction port 17 in the compression chamber 15. However, the intermediate pressure working fluid remaining in the injection port 43 between the check valve 42 and the compression chamber 15 repeats re-expansion and re-compression, which causes a reduction in the efficiency of the compressor 91. Therefore, the thickness of the valve stop 42b (see FIG. 5) that regulates the maximum displacement amount of the reed valve 42a is changed according to the lift restricting portion of the reed valve 42a, and the volume in the injection port 43 downstream from the reed valve 42a is reduced. is doing.
 また、リード弁42aおよび図5に示すバルブストップ42bはボルトを含む固定部材46により中間圧プレート44に固定されている。バルブストップ42bに設けたねじを含む固定部材46の固定用孔は、バルブストップ42bを貫通することなく固定部材46の挿入側にのみ開口しているため、結果として、固定部材46は中間圧室41にのみ開放するように構成している。これにより、固定部材46の隙間を介して中間圧室41と圧縮室15との間で作動流体が漏れるのを抑制でき、インジェクション率を向上させることができる。 Further, the reed valve 42a and the valve stop 42b shown in FIG. 5 are fixed to the intermediate pressure plate 44 by a fixing member 46 including a bolt. Since the fixing hole of the fixing member 46 including the screw provided in the valve stop 42b is opened only on the insertion side of the fixing member 46 without penetrating the valve stop 42b, the fixing member 46 becomes an intermediate pressure chamber as a result. 41 is configured to open only to 41. Thereby, it can suppress that a working fluid leaks between the intermediate | middle pressure chamber 41 and the compression chamber 15 via the clearance gap between the fixing members 46, and can improve an injection rate.
 図3に示す中間圧室41は、圧縮室15へのインジェクション量を十分に供給可能とするために圧縮室15の吸入容積以上とする。ここで吸入容積とは、吸入ポート17から導いた作動流体を圧縮室15に閉じ込んだ時点、すなわち吸入工程完了時点での圧縮室15の容積であり、第1圧縮室15aと第2圧縮室15bとの合計容積である。本実施例の圧縮機91では、中間圧室41を固定スクロール12の鏡板の平面上に広がるように設け、容積を拡大している。しかしながら、圧縮機91に封入されたオイル6の一部が吐出冷媒と共に圧縮機91から出ていき、気液分離器96からインジェクション管95を通って中間圧室41に戻った場合に、液溜め部41bに残るオイル6が多すぎると貯油部20のオイル6が不足してしまう問題を生じるため、中間圧室41の容積が大きすぎるのも適切でない。このことから、中間圧室41の容積は、圧縮室15の吸入容積以上で、封入されるオイル6のオイル容積の1/2以下とすることが好ましい。 The intermediate pressure chamber 41 shown in FIG. 3 has a suction volume equal to or larger than the suction volume of the compression chamber 15 so that the injection amount into the compression chamber 15 can be sufficiently supplied. Here, the suction volume is the volume of the compression chamber 15 when the working fluid guided from the suction port 17 is closed in the compression chamber 15, that is, when the suction process is completed, and the first compression chamber 15a and the second compression chamber. The total volume with 15b. In the compressor 91 of the present embodiment, the intermediate pressure chamber 41 is provided so as to spread on the plane of the end plate of the fixed scroll 12 to increase the volume. However, when a part of the oil 6 sealed in the compressor 91 comes out of the compressor 91 together with the discharged refrigerant and returns to the intermediate pressure chamber 41 from the gas-liquid separator 96 through the injection pipe 95, the liquid reservoir If too much oil 6 remains in the portion 41b, there will be a problem that the oil 6 in the oil storage portion 20 will be insufficient. Therefore, it is not appropriate that the volume of the intermediate pressure chamber 41 is too large. Therefore, the volume of the intermediate pressure chamber 41 is preferably not less than the suction volume of the compression chamber 15 and not more than ½ of the oil volume of the sealed oil 6.
 図6は図3の6-6線矢視図である。 FIG. 6 is a view taken along line 6-6 in FIG.
 図6は固定スクロール12に旋回スクロール13を噛み合わせ、旋回スクロール13の背面13e側から見た図である。図6に示すように固定スクロール12と旋回スクロール13を噛み合わせた状態で、固定スクロール12の渦巻きラップと旋回スクロール13の渦巻きラップとの巻き数は等しい。 FIG. 6 is a view of the orbiting scroll 13 engaged with the fixed scroll 12 and viewed from the back surface 13e side of the orbiting scroll 13. FIG. As shown in FIG. 6, the number of turns of the spiral wrap of the fixed scroll 12 and the spiral wrap of the orbiting scroll 13 are equal in a state where the fixed scroll 12 and the orbiting scroll 13 are engaged with each other.
 固定スクロール12と旋回スクロール13により形成される圧縮室15には、旋回スクロール13のラップの外壁側に形成される第1圧縮室15aと、ラップの内壁側に形成される第2圧縮室15bとがある。 The compression chamber 15 formed by the fixed scroll 12 and the orbiting scroll 13 includes a first compression chamber 15a formed on the outer wall side of the wrap of the orbiting scroll 13 and a second compression chamber 15b formed on the inner wall side of the wrap. There is.
 第1圧縮室15aの作動流体を閉じ込めるタイミングと第2圧縮室15bの作動流体を閉じ込めるタイミングとは略等しく、第1圧縮室15aと第2圧縮室15bとは同時に圧縮を開始する。これにより、第1圧縮室15aと第2圧縮室15b間の圧力バランスが保たれ、旋回スクロール13の挙動が安定する。 The timing for confining the working fluid in the first compression chamber 15a and the timing for confining the working fluid in the second compression chamber 15b are substantially equal, and the first compression chamber 15a and the second compression chamber 15b start compression simultaneously. Thereby, the pressure balance between the 1st compression chamber 15a and the 2nd compression chamber 15b is maintained, and the behavior of the turning scroll 13 is stabilized.
 図7において、Rはインジェクション運転を伴わない場合のスクロール圧縮機の圧縮室の内圧を示す圧力曲線。 In FIG. 7, R is a pressure curve showing the internal pressure of the compression chamber of the scroll compressor without injection operation.
 インジェクション運転を伴わない場合には、クランク回転角に対する第1圧縮室15aと第2圧縮室15bの圧力上昇速度は等しい。しかしながら、第1圧縮室15aおよび第2圧縮室15bへのインジェクション量が異なる場合、そのインジェクション量に応じて圧力上昇速度が異なる。 When the injection operation is not involved, the pressure increasing speeds of the first compression chamber 15a and the second compression chamber 15b with respect to the crank rotation angle are equal. However, when the amount of injection into the first compression chamber 15a and the second compression chamber 15b is different, the pressure increase speed varies depending on the amount of injection.
 図7ではインジェクション量の違いによる圧縮速度の違いを示している。インジェクション量の多い圧縮室では圧縮開始から短い圧縮区間で吐出圧力に到達する。本実施例では、第1圧縮室15aに対するインジェクション冷媒量を多くすることから、圧力曲線Pに示す第1圧縮室15aの圧力上昇速度は、圧力曲線Qに示す第2圧縮室15bの圧力上昇速度よりも速くなる。図7において、圧力曲線Qに示す少ないインジェクション量の圧縮室の内圧に合わせて吐出バイパスポート21を設けた場合、圧力曲線Pに示すインジェクション量の多い圧縮室の内圧は、圧力曲線Qに示す内圧よりも速く吐出圧力に到達する。しかし、吐出圧力到達後も逃げ場なく圧縮し続ける第1圧縮室15aにおいて過圧縮が生じ、吐出バイパスポート21に連通してから過圧縮が緩和されていく。つまり、図中Aの面積に相当する圧縮動力が余分に必要となる。そこで、本発明では、インジェクション量の多い第1圧縮室15aに対しては、第2圧縮室15bよりも更に早いタイミングで吐出可能とし得る位置に吐出バイパスポート21を設けている。 Fig. 7 shows the difference in compression speed due to the difference in injection amount. In the compression chamber with a large injection amount, the discharge pressure is reached in a short compression section from the start of compression. In the present embodiment, since the injection refrigerant amount to the first compression chamber 15a is increased, the pressure increase rate of the first compression chamber 15a shown in the pressure curve P is the pressure increase rate of the second compression chamber 15b shown in the pressure curve Q. Will be faster. In FIG. 7, when the discharge bypass port 21 is provided in accordance with the internal pressure of the compression chamber with a small injection amount shown in the pressure curve Q, the internal pressure of the compression chamber with a large injection amount shown in the pressure curve P is the internal pressure shown in the pressure curve Q. Reach the discharge pressure faster. However, overcompression occurs in the first compression chamber 15a that continues to compress without escape after reaching the discharge pressure, and the overcompression is alleviated after communicating with the discharge bypass port 21. That is, extra compression power corresponding to the area A in the figure is required. Therefore, in the present invention, the discharge bypass port 21 is provided at a position where the first compression chamber 15a having a large injection amount can be discharged at an earlier timing than the second compression chamber 15b.
 すなわち、インジェクション量が多い圧縮室はインジェクション冷媒によって圧縮室の内圧が高まり、インジェクション量が少ないか、インジェクションされない圧縮室は他方と比べて圧力上昇は遅くなる。これは言い換えれば、インジェクション量の多い圧縮室に対しては、他方の圧縮室よりも早いタイミングから吐出可能な状態にする必要があるが、インジェクション量が必然的に異なる対称型スクロール圧縮においては、その考慮がなされないままインジェクション運転されると効率が低下する。本実施の形態では、インジェクション量の多い第1圧縮室15aに対しては、第2圧縮室15bよりも更に早いタイミングで吐出可能とし得る位置に吐出バイパスポート21を設けている。このことで、圧縮室が吐出ポートや吐出バイパスポート21と連通して冷媒が吐出可能となる圧縮室の容積に対する圧縮室の吸入容積の比で定義する容積比を、インジェクション量が多い第1圧縮室15aで小さくしている。 That is, in the compression chamber having a large injection amount, the internal pressure of the compression chamber is increased by the injection refrigerant, and in the compression chamber in which the injection amount is small or not injected, the pressure increase is slower than the other. In other words, for the compression chamber with a large injection amount, it is necessary to make it possible to discharge from an earlier timing than the other compression chamber, but in the symmetrical scroll compression in which the injection amount is necessarily different, If the injection operation is performed without taking such consideration into consideration, the efficiency decreases. In the present embodiment, the discharge bypass port 21 is provided at a position where the first compression chamber 15a having a large injection amount can be discharged at an earlier timing than the second compression chamber 15b. Thus, the volume ratio defined by the ratio of the suction volume of the compression chamber to the volume of the compression chamber that allows the refrigerant to be discharged by communicating with the discharge port or the discharge bypass port 21 is the first compression with a large injection amount. It is made small in the chamber 15a.
 図7に示すように、第2圧縮室15bへのインジェクションポート43の開口区間と、背圧室29から第2圧縮室15bへの給油区間の少なくとも一部の区間とを重複させている。給油区間が開口区間と重複する重複区間は、給油区間の後半の一部の区間とし、給油区間の後半にインジェクションポート43が開口して開口区間が開始する。 As shown in FIG. 7, the opening section of the injection port 43 to the second compression chamber 15b overlaps at least a part of the oil supply section from the back pressure chamber 29 to the second compression chamber 15b. The overlapping section in which the fueling section overlaps with the opening section is a partial section in the latter half of the fueling section, and the injection port 43 opens in the latter half of the fueling section and the opening section starts.
 また、旋回スクロール13のラップ先端13cには、運転中の温度分布を測定した結果をもとに、中心部である巻き始め部から外周部である巻き終わり部にかけて、徐々にハネ高さが高くなるようにスロープ形状が設けられている。これにより熱膨張による寸法変化を吸収し、局所摺動を防止し易くなる。 Further, the lap tip 13c of the orbiting scroll 13 is gradually increased in height from the winding start portion which is the central portion to the winding end portion which is the outer peripheral portion based on the measurement result of the temperature distribution during operation. A slope shape is provided so as to be. This absorbs a dimensional change due to thermal expansion and facilitates preventing local sliding.
 図8は、本実施の形態によるスクロール圧縮機の旋回運動に伴う給油経路とシール部材との位置関係を示す説明図である。 FIG. 8 is an explanatory diagram showing the positional relationship between the oil supply path and the seal member accompanying the turning motion of the scroll compressor according to the present embodiment.
 図8は固定スクロール12に旋回スクロール13を噛み合わせ、旋回スクロール13の背面13e側から見た状態であり、位相を90度ずつずらした図である。 FIG. 8 shows a state in which the orbiting scroll 13 is engaged with the fixed scroll 12 and viewed from the back surface 13e side of the orbiting scroll 13, and the phase is shifted by 90 degrees.
 接続路55の第1開口端55aは旋回スクロール13の背面13eに形成している。 The first opening end 55 a of the connection path 55 is formed on the back surface 13 e of the orbiting scroll 13.
 図8に示すように、シール部材78で旋回スクロール13の背面13eは内側の高圧領域30と外側の背圧室29に仕切られている。 As shown in FIG. 8, the back surface 13 e of the orbiting scroll 13 is partitioned by the seal member 78 into an inner high pressure region 30 and an outer back pressure chamber 29.
 図8の(B)の状態では、第1開口端55aはシール部材78の外側である背圧室29に開口しているため、オイル6が供給される。 8 (B), the first opening end 55a is open to the back pressure chamber 29 that is outside the seal member 78, so that the oil 6 is supplied.
 これに対し図8の(A)、(C)、(D)では、第1開口端55aはシール部材78の内側に開口しているため、オイルが供給されることはない。 On the other hand, in FIGS. 8A, 8C, and 8D, the first opening end 55a is opened inside the seal member 78, so that no oil is supplied.
 すなわち接続路55の第1開口端55aは、高圧領域30と背圧室29とを往来するが、接続路55の第1開口端55a、第2開口端55bで圧力差が生じたときのみ背圧室29にオイル6が供給される。この構成にすると、給油量は第1開口端55aがシール部材78の内側と外側を往来する時間割合で調整できるため、接続路55の通路径をオイルフィルタに対し10倍以上の寸法で構成することが可能となる。これにより、通路13aに異物が噛み込んで閉塞する恐れがなくなるため、安定した背圧の印加と同時にスラスト摺動部及び自転拘束機構14の潤滑も良好な状態を維持でき、高効率かつ高信頼性を実現するスクロール圧縮機を提供することができる。なお本実施例では、第2開口端55bが常に高圧領域30にあり、第1開口端55aが高圧領域30と背圧室29を往来する場合を例として説明したが、第2開口端55bが高圧領域30と背圧室29を往来し、第1開口端55aが常に背圧室29にある場合でも、第1開口端55aおよび第2開口端55bで圧力差が生じるため、間欠給油が実現でき同様の効果が得られる。 That is, the first opening end 55a of the connection path 55 travels between the high pressure region 30 and the back pressure chamber 29, but only when a pressure difference occurs between the first opening end 55a and the second opening end 55b of the connection path 55. Oil 6 is supplied to the pressure chamber 29. With this configuration, the amount of oil supply can be adjusted by the time ratio at which the first opening end 55a travels between the inside and the outside of the seal member 78. Therefore, the passage diameter of the connection passage 55 is configured to be 10 times or more that of the oil filter. It becomes possible. As a result, there is no possibility of foreign matter getting caught in the passage 13a, so that the thrust sliding portion and the rotation restraint mechanism 14 can be kept in good lubrication simultaneously with the stable application of the back pressure, and highly efficient and highly reliable. A scroll compressor that realizes performance can be provided. In the present embodiment, the case where the second opening end 55b is always in the high pressure region 30 and the first opening end 55a travels between the high pressure region 30 and the back pressure chamber 29 has been described as an example. Even when the first opening end 55a is always in the back pressure chamber 29, the pressure difference occurs between the first opening end 55a and the second opening end 55b, so that intermittent lubrication is realized. The same effect can be obtained.
 図9は、本実施の形態によるスクロール圧縮機の旋回運動に伴う給油経路およびインジェクションポートの開口状態を示す説明図である。 FIG. 9 is an explanatory diagram showing an oil supply path and an injection port opening state associated with the turning motion of the scroll compressor according to the present embodiment.
 図9は、固定スクロール12に旋回スクロール13を噛み合わせた状態であり、位相を90度ずつずらした図である。 FIG. 9 shows a state where the orbiting scroll 13 is engaged with the fixed scroll 12, and the phase is shifted by 90 degrees.
 図9に示すように、ラップ先端13cに形成された通路13aの第3開口端56aを、固定スクロール12の鏡板に形成された凹部12aに周期的に開口させることで、間欠連通を実現させている。 As shown in FIG. 9, intermittent communication is realized by periodically opening the third opening end 56 a of the passage 13 a formed in the wrap tip 13 c into the recess 12 a formed in the end plate of the fixed scroll 12. Yes.
 図9の(D)の状態で第3開口端56aは凹部12aに開口しており、この状態では、供給路56及び通路13aを通って背圧室29から第2圧縮室15bにオイル6が供給される。このように、第3開口端56aによって給油経路は、吸入冷媒を閉じ込み後の圧縮行程中にある第2圧縮室15bに開口する位置に設けている。 In the state of FIG. 9D, the third opening end 56a opens into the recess 12a. In this state, the oil 6 passes from the back pressure chamber 29 to the second compression chamber 15b through the supply path 56 and the passage 13a. Supplied. Thus, the oil supply path is provided by the third opening end 56a at a position that opens to the second compression chamber 15b in the compression stroke after the intake refrigerant is closed.
 これに対し図9の(A)、(B)、(C)では、第3開口端56aは凹部12aに開口していないため、背圧室29から第2圧縮室15bにオイル6は供給されない。以上のことから、背圧室29のオイル6は、給油経路を通って第2圧縮室15bに間欠的に導かれるので、背圧室29の圧力変動を抑制することができ、所定の圧力に制御することが可能となる。また同時に、第2圧縮室15bに供給されたオイル6は圧縮時のシール性向上や潤滑性向上の役割を果たす。 On the other hand, in FIGS. 9A, 9 </ b> B, and 9 </ b> C, the third opening end 56 a is not opened in the recess 12 a, so that the oil 6 is not supplied from the back pressure chamber 29 to the second compression chamber 15 b. . From the above, since the oil 6 in the back pressure chamber 29 is intermittently guided to the second compression chamber 15b through the oil supply path, the pressure fluctuation in the back pressure chamber 29 can be suppressed, and the predetermined pressure can be maintained. It becomes possible to control. At the same time, the oil 6 supplied to the second compression chamber 15b plays a role of improving the sealing property and the lubricating property during compression.
 第1圧縮室15aの閉じ込み時点を示す図9の(C)では、インジェクションポート43は第1圧縮室15aに開口している。 In FIG. 9C showing the closing time of the first compression chamber 15a, the injection port 43 is open to the first compression chamber 15a.
 他方、第2圧縮室15bに対しては、圧縮が進んだ状態を示す図9の(A)の状態においてインジェクションポート43が開口する。これにより、インジェクションポート43の開口区間は第1圧縮室15aと第2圧縮室15bとで区間としては概ね等しくとも、圧縮開始直後の圧力が低い圧縮室へインジェクションを行っている第1圧縮室15aの方が、より多くのインジェクション冷媒が送り込まれ、第1圧縮室15aの圧力上昇は第2圧縮室15bに対して早まることとなる。また、いずれの圧縮室に対しても、インジェクション冷媒が吸入ポート17まで逆流することなく圧縮できるため、冷媒循環量を増加し易く、高効率なインジェクション運転が可能となる。 On the other hand, with respect to the second compression chamber 15b, the injection port 43 opens in the state shown in FIG. Thereby, the opening section of the injection port 43 is substantially equal as the section between the first compression chamber 15a and the second compression chamber 15b, but the first compression chamber 15a is performing injection into the compression chamber having a low pressure immediately after the start of compression. In this case, more injection refrigerant is fed, and the pressure increase in the first compression chamber 15a is accelerated relative to the second compression chamber 15b. Moreover, since the injection refrigerant can be compressed without flowing back to the suction port 17 in any of the compression chambers, it is easy to increase the amount of refrigerant circulation, and a highly efficient injection operation is possible.
 このように、インジェクションポート43は、第1圧縮室15aと第2圧縮室15bとに順次開口する位置に設けている。また、インジェクションポート43は、図9の(C)、(D)に示すように吸入冷媒を閉じ込み後の圧縮行程中にある第1圧縮室15aに開口する位置、又は図9の(A)、(B)に示すように吸入冷媒を閉じ込み後の圧縮行程中にある第2圧縮室15bに開口する位置に、固定スクロール12の鏡板を貫通して設けている。 Thus, the injection port 43 is provided at a position that sequentially opens into the first compression chamber 15a and the second compression chamber 15b. Further, as shown in FIGS. 9C and 9D, the injection port 43 is opened to the first compression chamber 15a during the compression stroke after the intake refrigerant is closed, or FIG. 9A. (B), the end plate of the fixed scroll 12 is provided so as to penetrate the second compression chamber 15b in the compression stroke after the suction refrigerant is closed.
 図9では、図9の(C)から(D)にかけて給油区間が開始し、インジェクションポート43はそれに遅れて図9の(A)から(B)の間に第2圧縮室15bに開口し、インジェクションポート43の開口区間は給油区間との間に重複区間を有する。本実施の形態では、給油区間は第3開口端56aの凹部12aへの開口に等しい。背圧室29の圧力は、この給油区間の終了時の圧縮室15の内圧に依存し、給油区間の途中からインジェクション冷媒を圧縮室15に送り込むことで、インジェクション運転時にのみ背圧室29の圧力を上昇させて、旋回スクロール13の挙動の不安定化を抑制することを可能としている。また、インジェクションポート43の開口開始を給油区間の前半まで早めない理由として、給油区間の早期からインジェクション冷媒により圧縮室15の内圧が上昇し過ぎると、背圧室29から圧縮室15へ十分に給油される前に圧縮室15の内圧と背圧室29の圧力が等しくなり、給油不足になって圧縮機の信頼性に課題を生じさせる可能性が高まる。 In FIG. 9, the oil supply section starts from (C) to (D) in FIG. 9, and the injection port 43 opens to the second compression chamber 15 b between (A) and (B) in FIG. The opening section of the injection port 43 has an overlapping section with the refueling section. In the present embodiment, the oil supply section is equal to the opening of the third opening end 56a into the recess 12a. The pressure in the back pressure chamber 29 depends on the internal pressure of the compression chamber 15 at the end of the oil supply section, and the injection refrigerant is fed into the compression chamber 15 from the middle of the oil supply section, so that the pressure in the back pressure chamber 29 is only during the injection operation. Can be suppressed, and instability of the behavior of the orbiting scroll 13 can be suppressed. Further, as a reason why the start of opening of the injection port 43 cannot be advanced to the first half of the oil supply section, if the internal pressure of the compression chamber 15 is excessively increased by the injection refrigerant from the early stage of the oil supply section, sufficient oil supply from the back pressure chamber 29 to the compression chamber 15 is performed. Before the operation is performed, the internal pressure of the compression chamber 15 and the pressure of the back pressure chamber 29 become equal, and there is a high possibility of causing a problem in the reliability of the compressor due to insufficient lubrication.
 圧縮室15への給油区間の少なくとも一部を、インジェクションポート43の開口区間と重複するよう構成する。この構成により、背面13eから旋回スクロール13への圧力付加は、インジェクション冷媒の中間圧が上昇するのに応じて、給油区間中の圧縮室15の内圧と共に大きくなる。そのため、旋回スクロール13は固定スクロール12に対してより安定的に押し付けられ、背圧室29から圧縮室15への漏れを低減するとともに、安定した運転を行うことができる。これにより、旋回スクロール13の挙動はより安定的に、最適性能を実現し、インジェクション率を更に向上させることができる。 少 な く と も At least part of the oil supply section to the compression chamber 15 is configured to overlap with the opening section of the injection port 43. With this configuration, the pressure applied from the back surface 13e to the orbiting scroll 13 increases with the internal pressure of the compression chamber 15 in the oil supply section as the intermediate pressure of the injection refrigerant increases. Therefore, the orbiting scroll 13 is more stably pressed against the fixed scroll 12, reducing leakage from the back pressure chamber 29 to the compression chamber 15 and performing stable operation. Thereby, the behavior of the orbiting scroll 13 can be realized more stably, the optimum performance can be realized, and the injection rate can be further improved.
 図9では、固定スクロール12の鏡板の中心部に、圧縮室15で圧縮した冷媒を吐出する吐出ポート18を備え、吐出バイパスポート21として、第1圧縮室15aに連通する位置に設けた吐出バイパスポート21aと、第2圧縮室15bに連通する位置に設けた吐出バイパスポート21bとを設けている。 In FIG. 9, a discharge port 18 that discharges the refrigerant compressed in the compression chamber 15 is provided at the center of the end plate of the fixed scroll 12, and a discharge bypass provided as a discharge bypass port 21 at a position communicating with the first compression chamber 15a. A port 21a and a discharge bypass port 21b provided at a position communicating with the second compression chamber 15b are provided.
 第1圧縮室15aは図9の(C)の状態で吸入冷媒を閉じ込み、吐出バイパスポート21aは図9の(D)の状態において第1圧縮室15aに開口している。 The first compression chamber 15a closes the intake refrigerant in the state of FIG. 9C, and the discharge bypass port 21a opens to the first compression chamber 15a in the state of FIG. 9D.
 他方、第2圧縮室15bは図9の(C)の状態で吸入冷媒を閉じ込むが、吐出バイパスポート21bは図9の(D)および(A)の状態においてはまだ第2圧縮室15bには連通せず、図9の(B)の状態になって第2圧縮室15bと連通する。これにより、第1圧縮室15aは第2圧縮室15bに対してより多くのインジェクション冷媒を取り込んでも過圧縮することなく、インジェクションサイクルの効果を発揮することができる。 On the other hand, the second compression chamber 15b closes the suction refrigerant in the state of FIG. 9C, but the discharge bypass port 21b is still in the second compression chamber 15b in the states of FIG. 9D and FIG. Is not communicated, and is in the state of FIG. 9B and communicates with the second compression chamber 15b. Thereby, even if the 1st compression chamber 15a takes in more injection refrigerant | coolants with respect to the 2nd compression chamber 15b, it can exhibit the effect of an injection cycle, without overcompressing.
 このように、第1圧縮室15aに連通する吐出バイパスポート21aと、第2圧縮室15bに連通する吐出バイパスポート21bとを設けることでも、圧縮室15の冷媒が吐出可能となる圧縮室15の吐出容積に対する吸入容積の比である容積比を、第2圧縮室15bよりも第1圧縮室15aを小さくすることができる。そのため、最大インジェクション状態においても第1圧縮室15aの過剰な圧力上昇を抑制することができる。 Thus, the provision of the discharge bypass port 21a that communicates with the first compression chamber 15a and the discharge bypass port 21b that communicates with the second compression chamber 15b also allows the refrigerant in the compression chamber 15 to be discharged. The volume ratio that is the ratio of the suction volume to the discharge volume can be made smaller in the first compression chamber 15a than in the second compression chamber 15b. Therefore, an excessive pressure increase in the first compression chamber 15a can be suppressed even in the maximum injection state.
 (第2の実施の形態)
 図10は、本発明の第2の実施の形態によるスクロール圧縮機の縦断面図である。
(Second Embodiment)
FIG. 10 is a longitudinal sectional view of a scroll compressor according to the second embodiment of the present invention.
 本実施例では、第1圧縮室15aのみに開口する第1インジェクションポート48aと第2圧縮室15bのみに開口する第2インジェクションポート48bとを備えている。第1インジェクションポート48aには第1逆止弁47aを設け、第2インジェクションポート48bには第2逆止弁47bを設けている。その他の構成は、上記実施例と同一であるため、同一符号を付して説明を省略する。 In the present embodiment, a first injection port 48a that opens only to the first compression chamber 15a and a second injection port 48b that opens only to the second compression chamber 15b are provided. A first check valve 47a is provided in the first injection port 48a, and a second check valve 47b is provided in the second injection port 48b. Since other configurations are the same as those in the above embodiment, the same reference numerals are given and description thereof is omitted.
 本実施例では、第1インジェクションポート48aのポート径を第2インジェクションポート48bよりも大きくすることで、第1インジェクションポート48aから第1圧縮室15aにインジェクションする冷媒量を、第2インジェクションポート48bから第2圧縮室15bにインジェクションする冷媒量よりも多くしている。 In the present embodiment, by making the port diameter of the first injection port 48a larger than that of the second injection port 48b, the amount of refrigerant injected from the first injection port 48a into the first compression chamber 15a can be reduced from the second injection port 48b. The amount of refrigerant injected into the second compression chamber 15b is larger.
 このように、第1圧縮室15aのみに開口する第1インジェクションポート48aと第2圧縮室15bのみに開口する第2インジェクションポート48bとを設けることで、第1圧縮室15aと第2圧縮室15bへのインジェクション量を個別に調整することが可能になる。さらに、第1圧縮室15aと第2圧縮室15bに対して常時インジェクションさせ、又は第1圧縮室15aと第2圧縮室15bに対して同時にインジェクションさせることも可能となり、冷凍サイクルの圧力差が大きい条件下において、高いインジェクション率を実現するのに有効となる。さらに、背圧室29からの給油区間の設定の自由度が高まるため、前述の背圧室29からの圧力調整機能を有効に活用でき、旋回スクロール13の背面13eからの圧力付加を安定的に制御できる。 Thus, by providing the first injection port 48a that opens only to the first compression chamber 15a and the second injection port 48b that opens only to the second compression chamber 15b, the first compression chamber 15a and the second compression chamber 15b are provided. It becomes possible to individually adjust the injection amount. Further, it is possible to always inject the first compression chamber 15a and the second compression chamber 15b, or simultaneously inject the first compression chamber 15a and the second compression chamber 15b, and the pressure difference of the refrigeration cycle is large. It is effective to realize a high injection rate under certain conditions. Further, since the degree of freedom in setting the oil supply section from the back pressure chamber 29 is increased, the pressure adjustment function from the back pressure chamber 29 can be effectively utilized, and the pressure application from the back surface 13e of the orbiting scroll 13 can be stably performed. Can be controlled.
 なお、本実施の形態では、第1インジェクションポート48aが、第2インジェクションポート48bよりもポート径が大きい場合を示した。しかし、この構成とともに、又はこの構成に代えて、第1インジェクションポート48aが第1圧縮室15aに開口する開口区間が、第2インジェクションポート48bが第2圧縮室15bに開口する開口区間より長くしてもよい。また、第1インジェクションポート48aの第1圧縮室15aへの開口時における第1インジェクションポート48a内の中間圧と第1圧縮室15a内圧との圧力差が、第2インジェクションポート48bの第2圧縮室15bへの開口時における第2インジェクションポート48b内の中間圧と第2圧縮室15b内圧との圧力差より大きくすることもできる。 In the present embodiment, the case where the first injection port 48a has a larger port diameter than the second injection port 48b is shown. However, together with this configuration or instead of this configuration, the opening section where the first injection port 48a opens to the first compression chamber 15a is longer than the opening section where the second injection port 48b opens to the second compression chamber 15b. May be. Further, when the first injection port 48a is opened to the first compression chamber 15a, the pressure difference between the intermediate pressure in the first injection port 48a and the internal pressure in the first compression chamber 15a is the second compression chamber of the second injection port 48b. The pressure difference between the intermediate pressure in the second injection port 48b and the internal pressure of the second compression chamber 15b at the time of opening to 15b can be made larger.
 また、本実施の形態では、第1圧縮室15aと第2圧縮室15bにのみそれぞれ開口する第1インジェクションポート48aと第2インジェクションポート48bについて説明した。しかし、第1の実施の形態で示した第1圧縮室15aと第2圧縮室15b双方に開口するインジェクションポートと、本実施の形態で示す第1圧縮室15aと第2圧縮室15bにのみそれぞれ開口する第1インジェクションポート48aと第2インジェクションポート48bとを組み合わせて、第1圧縮室15aへのインジェクション量を第2圧縮室15bへのインジェクション量よりも多くしてもよい。 In the present embodiment, the first injection port 48a and the second injection port 48b that open only to the first compression chamber 15a and the second compression chamber 15b have been described. However, only the injection ports opened in both the first compression chamber 15a and the second compression chamber 15b shown in the first embodiment, and the first compression chamber 15a and the second compression chamber 15b shown in the present embodiment, respectively. The first injection port 48a and the second injection port 48b that are opened may be combined to increase the amount of injection into the first compression chamber 15a than the amount of injection into the second compression chamber 15b.
 作動流体である冷媒として、吐出冷媒の温度が高温となり易いR32や二酸化炭素を用いた場合には、吐出冷媒温度の上昇を抑制できる効果が発揮され、モータ部3(図2参照)の絶縁材など樹脂材料の劣化を抑え、長期に亘って信頼性の高い圧縮機を提供することが可能となる。 When R32 or carbon dioxide, which is likely to have a high temperature of the discharged refrigerant, is used as the refrigerant that is the working fluid, the effect of suppressing an increase in the discharged refrigerant temperature is exhibited, and the insulating material of the motor unit 3 (see FIG. 2) It is possible to provide a highly reliable compressor over a long period of time by suppressing deterioration of the resin material.
 一方、炭素間に二重結合を有する冷媒、又はその冷媒を含むGWP500以下(GWP:Global Warming Potential(地球温暖化係数))の冷媒を用いた場合には、高温時に冷媒分解反応を生じ易いため、吐出冷媒温度の上昇を抑制する効果により、冷媒の長期安定性に効果を発揮する。 On the other hand, when a refrigerant having a double bond between carbons or a refrigerant of GWP500 or less (GWP: Global Warming Potential) containing the refrigerant is used, a refrigerant decomposition reaction easily occurs at a high temperature. The effect of suppressing the rise in the discharged refrigerant temperature is effective in the long-term stability of the refrigerant.
 以上説明したように、第1の開示によるスクロール圧縮機は、固定スクロールの鏡板の中心部に、圧縮室で圧縮した冷媒を吐出する吐出ポートを備え、圧縮室が吐出ポートと連通する前に圧縮室で圧縮した冷媒を吐出する吐出バイパスポートを設ける。また、第1圧縮室及び第2圧縮室に中間圧の冷媒をインジェクションする、少なくとも1つのインジェクションポートを、吸入冷媒を閉じ込み後の圧縮行程中にある第1圧縮室又は第2圧縮室に開口する位置に、固定スクロールの鏡板を貫通して設ける。また、第1圧縮室及び第2圧縮室の内、インジェクションポートからインジェクションする冷媒量を多くする一方の圧縮室を、他方の圧縮室に対して、圧縮室の冷媒が吐出可能となる圧縮室の吐出容積に対する吸入容積の比である容積比が小さくなるように吐出バイパスポートを配置する。 As described above, the scroll compressor according to the first disclosure includes the discharge port that discharges the refrigerant compressed in the compression chamber at the center of the end plate of the fixed scroll, and compresses the compression chamber before it communicates with the discharge port. A discharge bypass port for discharging the refrigerant compressed in the chamber is provided. Further, at least one injection port for injecting the intermediate pressure refrigerant into the first compression chamber and the second compression chamber is opened to the first compression chamber or the second compression chamber in the compression stroke after the suction refrigerant is closed. The end plate of the fixed scroll is provided at a position where it is inserted. Further, of the first compression chamber and the second compression chamber, one compression chamber that increases the amount of refrigerant injected from the injection port is connected to the other compression chamber so that the refrigerant in the compression chamber can be discharged. The discharge bypass port is arranged so that the volume ratio, which is the ratio of the suction volume to the discharge volume, becomes small.
 本開示により、第1圧縮室と第2圧縮室とで吐出容積と吸入容積が等しいスクロール圧縮機では、第1圧縮室と第2圧縮室の容積比も等しいが、一方の圧縮室に対してより多くのインジェクションを行うことで、他方の圧縮室よりも圧縮室の内圧が、より短い圧縮区間で吐出圧力に到達する。圧縮室の内圧が吐出圧力に到達しても吐出可能なポートと圧縮室が連通していなければ過剰な圧縮が生じ、余分な圧縮動力が必要となるだけでなく、旋回スクロールを固定スクロールから引き離す力を生じるため、圧縮運動の不安定化を招いてしまう。インジェクションする冷媒量を多くする一方の圧縮室を、他方の圧縮室に対して、容積比が小さくなるように吐出バイパスポートを配置することで、最大インジェクション状態においても過剰な圧力上昇を抑制することができる。つまり、本実施の形態によれば、インジェクション量の多い圧縮室に対して吐出バイパスポートを早期に連通させ、容積比を小さくすることで、高いインジェクション率の運転時にも過圧縮を防止し、インジェクションサイクル効果を最大化して、従来以上の効率向上と能力拡大効果を得ることが可能となる。 According to the present disclosure, in the scroll compressor in which the discharge volume and the suction volume are the same in the first compression chamber and the second compression chamber, the volume ratio of the first compression chamber and the second compression chamber is also equal, By performing more injections, the internal pressure of the compression chamber reaches the discharge pressure in a shorter compression section than the other compression chamber. Even if the internal pressure of the compression chamber reaches the discharge pressure, if the dischargeable port and the compression chamber do not communicate with each other, excessive compression occurs, requiring not only excessive compression power, but also pulling the orbiting scroll away from the fixed scroll This generates force, leading to instability of the compression motion. By disposing the discharge bypass port so that the volume ratio of one compression chamber that increases the amount of refrigerant to be injected is smaller than that of the other compression chamber, excessive pressure rise is suppressed even in the maximum injection state. Can do. In other words, according to the present embodiment, by connecting the discharge bypass port to the compression chamber with a large injection amount at an early stage and reducing the volume ratio, over-compression can be prevented even during operation at a high injection rate. By maximizing the cycle effect, it becomes possible to obtain an efficiency improvement and capacity expansion effect that are more than conventional.
 第2の開示は、第1の開示によるスクロール圧縮機において、インジェクションポートには、圧縮室への冷媒の流れを許容し、圧縮室からの冷媒の流れを抑止する逆止弁を設ける。 According to a second disclosure, in the scroll compressor according to the first disclosure, the injection port is provided with a check valve that allows a refrigerant flow to the compression chamber and inhibits the refrigerant flow from the compression chamber.
 本開示によれば、逆止弁と圧縮室を近づけて設けることで、インジェクションポートが圧縮室に開口している区間において圧縮室の内圧が中間圧以上に上昇しても、インジェクション管などの圧縮に無効な空間内の冷媒圧縮を最小限に抑制でき、インジェクションサイクルの理論性能を最大限に発揮可能な条件までインジェクション率を高めることができる。 According to the present disclosure, by providing the check valve and the compression chamber close to each other, even if the internal pressure of the compression chamber rises above the intermediate pressure in the section where the injection port is open to the compression chamber, the compression of the injection pipe or the like Therefore, it is possible to minimize the refrigerant compression in the space that is ineffective, and to increase the injection rate up to the condition where the theoretical performance of the injection cycle can be maximized.
 第3の開示は、第1の開示または第2の開示によるスクロール圧縮機において、固定スクロールと旋回スクロールを内部に備えた密閉容器にオイルを溜める貯油部を形成し、旋回スクロールの背面には高圧領域と背圧室とを形成する。また、貯油部から圧縮室にオイルを給油する給油経路は背圧室を経由し、背圧室が第1圧縮室又は第2圧縮室に連通する給油経路は、吸入冷媒を閉じ込み後の圧縮行程中にある第1圧縮室又は第2圧縮室に開口する位置に設ける。さらに、給油経路が第1圧縮室又は第2圧縮室に連通する給油区間の少なくとも一部の区間を、インジェクションポートが第1圧縮室又は第2圧縮室に開口する開口区間と重複させる。 According to a third disclosure, in the scroll compressor according to the first disclosure or the second disclosure, an oil storage part for storing oil is formed in a sealed container having a fixed scroll and a turning scroll therein, and a high pressure is provided on a rear surface of the turning scroll. An area and a back pressure chamber are formed. In addition, the oil supply path for supplying oil from the oil storage section to the compression chamber passes through the back pressure chamber, and the oil supply path in which the back pressure chamber communicates with the first compression chamber or the second compression chamber is the compression after the suction refrigerant is closed. It is provided at a position that opens to the first compression chamber or the second compression chamber during the stroke. Further, at least a part of the oil supply section in which the oil supply path communicates with the first compression chamber or the second compression chamber is overlapped with the opening section where the injection port opens into the first compression chamber or the second compression chamber.
 圧縮室に中間圧の冷媒をインジェクションした場合、インジェクションを行わなかった場合に比べて圧縮室の圧力上昇が早くなるため、旋回スクロールを固定スクロールから引き離そうとする力が従来以上に大きくなる。本開示によれば、旋回スクロールを固定スクロールへ押圧する力は給油経路が連通している圧縮室の圧力に連動するため、中間圧の冷媒が圧縮室にインジェクションされればされるほど、旋回スクロールを固定スクロールに押圧する力も大きくなり、旋回スクロールが固定スクロールから離れることなく安定した運転が可能となる。 When intermediate pressure refrigerant is injected into the compression chamber, the pressure in the compression chamber rises faster than when injection is not performed, so the force for pulling the orbiting scroll away from the fixed scroll is greater than before. According to the present disclosure, the force that presses the orbiting scroll to the fixed scroll is linked to the pressure in the compression chamber that communicates with the oil supply path, so that the more intermediate pressure refrigerant is injected into the compression chamber, the more the orbiting scroll The force that pushes the fixed scroll to the fixed scroll is also increased, and the orbiting scroll can be stably operated without leaving the fixed scroll.
 第4の開示は、第3の開示によるスクロール圧縮機において、給油区間が開口区間と重複する重複区間を、給油区間の後半の一部の区間とする。 In the fourth disclosure, in the scroll compressor according to the third disclosure, an overlapping section in which the fueling section overlaps with the opening section is defined as a part of the latter half of the fueling section.
 本開示によれば、背圧室の圧力は重複区間の後半の圧縮室の内圧と連動するため、インジェクションが完了した状態もしくはより多くインジェクションされた状態の圧縮室の内圧に応じた背圧室圧力の設定が可能となる。これにより、インジェクションによる旋回スクロールの引き離し力が大きい条件では背圧室の圧力は高く、安定した旋回運動が可能であり、一方、インジェクション量が少ない条件では背圧室の圧力は低く、固定スクロールへの過剰な押圧力を防止することができる。 According to the present disclosure, since the pressure in the back pressure chamber is linked to the internal pressure in the compression chamber in the latter half of the overlapping section, the back pressure chamber pressure corresponding to the internal pressure in the compression chamber in a state where injection has been completed or more injected Can be set. As a result, the pressure in the back pressure chamber is high under conditions where the revolving force of the orbiting scroll due to injection is large, and stable orbiting is possible, while the pressure in the back pressure chamber is low under conditions where the amount of injection is small, It is possible to prevent excessive pressing force.
 第5の開示は、第1の開示から第4の開示のいずれかによるスクロール圧縮機において、少なくとも1つのインジェクションポートを、第1圧縮室と第2圧縮室とに順次開口する位置に設ける。 According to a fifth disclosure, in the scroll compressor according to any one of the first disclosure to the fourth disclosure, at least one injection port is provided at a position that sequentially opens into the first compression chamber and the second compression chamber.
 本開示によれば、第1の圧縮室および第2の圧縮室の双方にインジェクションする際にインジェクションポートを共用化できため、小型化や部品点数の削減が図れるだけでなく、インジェクション率を高めてインジェクションサイクル効果を最大限に引き出すことが可能となる。さらに、スクロール圧縮機では一般的に第1圧縮室と第2圧縮室の圧縮開始のタイミングが180度異なるため、一つのインジェクションポートからいずれの圧縮室に対しても圧縮開始直後にインジェクションを行う位置に設けることも可能であり、高いインジェクション率の実現に適している。 According to the present disclosure, since the injection port can be shared when injecting into both the first compression chamber and the second compression chamber, not only can the size and the number of components be reduced, but also the injection rate can be increased. It is possible to maximize the injection cycle effect. Further, in the scroll compressor, since the compression start timing is generally 180 degrees different between the first compression chamber and the second compression chamber, a position where injection is performed immediately after the start of compression from any one injection port to any compression chamber. It is also possible to provide a high injection rate.
 第6の開示は、第1の開示から第4の開示のいずれかの実施の形態によるスクロール圧縮機であって、インジェクションポートとして、第1圧縮室のみに開口する第1インジェクションポートと、第2圧縮室のみに開口する第2インジェクションポートとを備える。また、下記(1)~(3)のいずれかの構成を加える。
(1)第1インジェクションポートが、第2インジェクションポートよりもポート径が大きい。
(2)第1インジェクションポートが第1圧縮室に開口する開口区間が、第2インジェクションポートが第2圧縮室に開口する開口区間より長い。
(3)第1インジェクションポートの第1圧縮室への開口時における第1インジェクションポート内の中間圧と第1圧縮室の内圧との圧力差が、第2インジェクションポートの第2圧縮室への開口時における第2インジェクションポート内の中間圧と第2圧縮室の内圧との圧力差より大きい。
A sixth disclosure is a scroll compressor according to any one of the first to fourth disclosures, and as the injection port, a first injection port that opens only in the first compression chamber, and a second And a second injection port that opens only to the compression chamber. Further, any one of the following configurations (1) to (3) is added.
(1) The first injection port has a larger port diameter than the second injection port.
(2) The opening section where the first injection port opens into the first compression chamber is longer than the opening section where the second injection port opens into the second compression chamber.
(3) The pressure difference between the intermediate pressure in the first injection port and the internal pressure in the first compression chamber when the first injection port opens into the first compression chamber is the opening of the second injection port into the second compression chamber. The pressure difference between the intermediate pressure in the second injection port and the internal pressure in the second compression chamber at the time is larger.
 本開示によれば、容積が大きく圧力上昇速度が緩やかな第1圧縮室へのインジェクション量を確実に多くすることができ、効率的なインジェクション冷媒量の分配が可能とる。 According to the present disclosure, the amount of injection into the first compression chamber having a large volume and a slow pressure increase rate can be surely increased, and an efficient injection refrigerant amount can be distributed.
 本発明のスクロール圧縮機は、蒸発器が低温環境下で使用される温水暖房装置、空気調和装置、給湯器、又は冷凍機などの冷凍サイクル装置に有用である。 The scroll compressor of the present invention is useful for a refrigeration cycle apparatus such as a hot water heater, an air conditioner, a water heater, or a refrigerator in which an evaporator is used in a low temperature environment.
 1 密閉容器
 2 圧縮機構
 3 モータ部
 4 シャフト
 4a 偏心軸部
 6 オイル
 11 主軸受部材
 12 固定スクロール
 12a 凹部
 13 旋回スクロール
 13c ラップ先端
 13e 背面
 14 自転拘束機構
 15 圧縮室
 15a 第1圧縮室
 15b 第2圧縮室
 16 吸入パイプ
 17 吸入ポート
 18 吐出ポート
 19 吐出リード弁
 20 貯油部
 21,21a,21b 吐出バイパスポート
 25 ポンプ
 26 オイル供給穴
 29 背圧室
 30 高圧領域
 31 吐出室
 41 中間圧室
 41a 中間圧室入口
 41b 液溜め部
 42 逆止弁
 42a リード弁
 42b バルブストップ
 43 インジェクションポート
 43a インジェクションポート入口
 44 中間圧プレート(中間圧室隔壁部材)
 45 中間圧カバー(中間圧室隔壁部材)
 46 固定部材
 47a 第1逆止弁
 47b 第2逆止弁
 48 インジェクションポート
 48a 第1インジェクションポート
 48b 第2インジェクションポート
 55 接続路
 55a 第1開口端
 55b 第2開口端
 56 供給路
 56a 第3開口端
 56b 第4開口端
 66 軸受部
 78 シール部材
 91 圧縮機
 92 凝縮器
 93 蒸発器
 94a,94b 膨張弁
 95 インジェクション管
 96 気液分離器
DESCRIPTION OF SYMBOLS 1 Airtight container 2 Compression mechanism 3 Motor part 4 Shaft 4a Eccentric shaft part 6 Oil 11 Main bearing member 12 Fixed scroll 12a Recessed part 13 Orbiting scroll 13c Lap tip 13e Back surface 14 Rotation restraint mechanism 15 Compression chamber 15a 1st compression chamber 15b 2nd compression Chamber 16 Suction pipe 17 Suction port 18 Discharge port 19 Discharge reed valve 20 Oil storage part 21, 21a, 21b Discharge bypass port 25 Pump 26 Oil supply hole 29 Back pressure chamber 30 High pressure region 31 Discharge chamber 41 Intermediate pressure chamber 41a Intermediate pressure chamber inlet 41b Liquid reservoir 42 Check valve 42a Reed valve 42b Valve stop 43 Injection port 43a Injection port inlet 44 Intermediate pressure plate (intermediate pressure chamber partition member)
45 Intermediate pressure cover (intermediate pressure chamber partition member)
46 fixing member 47a first check valve 47b second check valve 48 injection port 48a first injection port 48b second injection port 55 connection path 55a first opening end 55b second opening end 56 supply path 56a third opening end 56b 4th opening end 66 Bearing part 78 Seal member 91 Compressor 92 Condenser 93 Evaporator 94a, 94b Expansion valve 95 Injection pipe 96 Gas-liquid separator

Claims (8)

  1.  鏡板から渦巻き状のラップが立ち上がる固定スクロール及び旋回スクロールを備え、前記固定スクロールの前記ラップと前記旋回スクロールの前記ラップとを噛み合わせて、前記固定スクロールと前記旋回スクロールとの間に圧縮室を形成し、前記圧縮室として、前記旋回スクロールの前記ラップの外壁側に形成される第1圧縮室と、前記旋回スクロールの前記ラップの内壁側に形成される第2圧縮室とが形成され、前記第1圧縮室の吸入容積が前記第2圧縮室の吸入容積と等しいスクロール圧縮機において、
    前記固定スクロールの前記鏡板の中心部に、前記圧縮室で圧縮した冷媒を吐出する吐出ポートを備え、前記圧縮室が前記吐出ポートと連通する前に前記圧縮室で圧縮した前記冷媒を吐出する吐出バイパスポートを設け、前記第1圧縮室及び前記第2圧縮室に中間圧の冷媒をインジェクションする、少なくとも1つのインジェクションポートを、吸入冷媒を閉じ込み後の圧縮行程中にある前記第1圧縮室又は前記第2圧縮室に開口する位置に、前記固定スクロールの前記鏡板を貫通して設け、前記第1圧縮室及び前記第2圧縮室の内、前記インジェクションポートからインジェクションする冷媒量を多くする前記第1圧縮室および前記第2圧縮室のいずれか一方が、前記第1圧縮室および前記第2圧縮室の他方に対して、前記圧縮室の冷媒が吐出可能となる前記圧縮室の吐出容積に対する前記吸入容積の比である容積比が小さくなるように前記吐出バイパスポートを配置したことを特徴とするスクロール圧縮機。
    A fixed scroll and a orbiting scroll in which a spiral wrap rises from an end plate, and a compression chamber is formed between the fixed scroll and the orbiting scroll by meshing the wrap of the fixed scroll and the wrap of the orbiting scroll. The first compression chamber formed on the outer wall side of the wrap of the orbiting scroll and the second compression chamber formed on the inner wall side of the wrap of the orbiting scroll are formed as the compression chamber, In the scroll compressor, the suction volume of one compression chamber is equal to the suction volume of the second compression chamber,
    A discharge port that discharges the refrigerant compressed in the compression chamber is provided at the center of the end plate of the fixed scroll, and discharge that discharges the refrigerant compressed in the compression chamber before the compression chamber communicates with the discharge port. The first compression chamber or the first compression chamber that is in the compression stroke after the intake refrigerant is closed by providing a bypass port and injecting intermediate pressure refrigerant into the first compression chamber and the second compression chamber The first compression chamber and the second compression chamber are provided at positions that open to the second compression chamber so as to penetrate the end plate, and the first compression chamber and the second compression chamber increase the amount of refrigerant injected from the injection port. Either one of the first compression chamber and the second compression chamber discharges the refrigerant in the compression chamber from the other of the first compression chamber and the second compression chamber. Scroll compressor, wherein a volume ratio which is the ratio of the suction volume is arranged the discharge bypass port so as to be smaller for the discharge volume of the compression chamber becomes possible.
  2.  前記インジェクションポートには、前記圧縮室への前記冷媒の流れを許容し、前記圧縮室からの前記冷媒の流れを抑止する逆止弁を設けたことを特徴とする請求項1に記載のスクロール圧縮機。 2. The scroll compression according to claim 1, wherein the injection port is provided with a check valve that allows the flow of the refrigerant to the compression chamber and inhibits the flow of the refrigerant from the compression chamber. Machine.
  3.  前記固定スクロールと前記旋回スクロールを内部に備えた密閉容器には、オイルを溜める貯油部を形成し、前記旋回スクロールの背面には高圧領域と背圧室とを形成し、前記貯油部から前記圧縮室に前記オイルを給油する給油経路は前記背圧室を経由し、前記背圧室が前記第1圧縮室又は前記第2圧縮室に連通する前記給油経路は、前記吸入冷媒を閉じ込み後の前記圧縮行程中にある前記第1圧縮室又は前記第2圧縮室に開口する前記位置に設け、前記給油経路が前記第1圧縮室又は前記第2圧縮室に連通する給油区間の少なくとも一部の区間を、前記インジェクションポートが前記第1圧縮室又は前記第2圧縮室に開口する開口区間と重複させたことを特徴とする請求項1に記載のスクロール圧縮機。 The sealed container having the fixed scroll and the orbiting scroll is provided with an oil storage part for storing oil, and a high pressure region and a back pressure chamber are formed on the rear surface of the orbiting scroll, and the compression is performed from the oil storage part. An oil supply path for supplying the oil to the chamber passes through the back pressure chamber, and the oil supply path in which the back pressure chamber communicates with the first compression chamber or the second compression chamber is provided after the intake refrigerant is closed. Provided at the position that opens to the first compression chamber or the second compression chamber in the compression stroke, and the oil supply path is at least part of the oil supply section that communicates with the first compression chamber or the second compression chamber. The scroll compressor according to claim 1, wherein a section is overlapped with an opening section where the injection port opens into the first compression chamber or the second compression chamber.
  4.  前記固定スクロールと前記旋回スクロールを内部に備えた密閉容器には、オイルを溜める貯油部を形成し、前記旋回スクロールの背面には高圧領域と背圧室とを形成し、前記貯油部から前記圧縮室に前記オイルを給油する給油経路は前記背圧室を経由し、前記背圧室が前記第1圧縮室又は前記第2圧縮室に連通する前記給油経路は、前記吸入冷媒を閉じ込み後の前記圧縮行程中にある前記第1圧縮室又は前記第2圧縮室に開口する前記位置に設け、前記給油経路が前記第1圧縮室又は前記第2圧縮室に連通する給油区間の少なくとも一部の区間を、前記インジェクションポートが前記第1圧縮室又は前記第2圧縮室に開口する開口区間と重複させたことを特徴とする請求項2に記載のスクロール圧縮機。 The sealed container having the fixed scroll and the orbiting scroll is provided with an oil storage part for storing oil, and a high pressure region and a back pressure chamber are formed on the rear surface of the orbiting scroll, and the compression is performed from the oil storage part. An oil supply path for supplying the oil to the chamber passes through the back pressure chamber, and the oil supply path in which the back pressure chamber communicates with the first compression chamber or the second compression chamber is provided after the intake refrigerant is closed. Provided at the position that opens to the first compression chamber or the second compression chamber in the compression stroke, and the oil supply path is at least part of the oil supply section that communicates with the first compression chamber or the second compression chamber. The scroll compressor according to claim 2, wherein a section is overlapped with an opening section where the injection port opens into the first compression chamber or the second compression chamber.
  5.  前記給油区間が前記開口区間と重複する重複区間を、前記給油区間の後半の一部の区間としたことを特徴とする請求項3に記載のスクロール圧縮機。 The scroll compressor according to claim 3, wherein an overlapping section in which the refueling section overlaps with the opening section is a partial section in the latter half of the refueling section.
  6.  前記給油区間が前記開口区間と重複する重複区間を、前記給油区間の後半の一部の区間としたことを特徴とする請求項4に記載のスクロール圧縮機。 The scroll compressor according to claim 4, wherein an overlapping section in which the fueling section overlaps with the opening section is a part of the latter half of the fueling section.
  7.  少なくとも1つの前記インジェクションポートを、前記第1圧縮室と前記第2圧縮室とに順次開口する位置に設けたことを特徴とする請求項1から請求項6のいずれか1項に記載のスクロール圧縮機。 The scroll compression according to any one of claims 1 to 6, wherein at least one of the injection ports is provided at a position that sequentially opens into the first compression chamber and the second compression chamber. Machine.
  8.  前記インジェクションポートとして、前記第1圧縮室のみに開口する第1インジェクションポートと、前記第2圧縮室のみに開口する第2インジェクションポートとを備え、前記第1インジェクションポートが、前記第2インジェクションポートよりもポート径が大きいか、前記第1インジェクションポートが前記第1圧縮室に開口する開口区間が、前記第2インジェクションポートが前記第2圧縮室に開口する開口区間より長いか、又は前記第1インジェクションポートの前記第1圧縮室への開口時における前記第1インジェクションポート内の中間圧と前記第1圧縮室の内圧との圧力差が、前記第2インジェクションポートの前記第2圧縮室への開口時における前記第2インジェクションポート内の中間圧と前記第2圧縮室の内圧との圧力差より大きいことを特徴とする請求項1から請求項6のいずれか1項に記載のスクロール圧縮機。 The injection port includes a first injection port that opens only to the first compression chamber, and a second injection port that opens only to the second compression chamber, and the first injection port is more than the second injection port. Or the opening section where the first injection port opens into the first compression chamber is longer than the opening section where the second injection port opens into the second compression chamber, or the first injection. When the port opens to the first compression chamber, the pressure difference between the intermediate pressure in the first injection port and the internal pressure of the first compression chamber is the time when the second injection port opens to the second compression chamber. Between the intermediate pressure in the second injection port and the internal pressure of the second compression chamber Scroll compressor according to any one of claims 1 to 6, wherein greater than the force difference.
PCT/JP2017/036937 2016-11-24 2017-10-12 Scroll compressor WO2018096824A1 (en)

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JP2018552453A JP6928792B2 (en) 2016-11-24 2017-10-12 Scroll compressor
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EP17873176.6A EP3546753B1 (en) 2016-11-24 2017-10-12 Scroll compressor
CN201780071842.8A CN109996961B (en) 2016-11-24 2017-10-12 Scroll compressor having a discharge port

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JP2020139489A (en) * 2019-03-01 2020-09-03 サンデン・オートモーティブコンポーネント株式会社 Scroll compressor
JP2020139490A (en) * 2019-03-01 2020-09-03 サンデン・オートモーティブコンポーネント株式会社 Scroll compressor

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CN112567136A (en) * 2019-02-08 2021-03-26 松下知识产权经营株式会社 Scroll compressor having a discharge port
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JP2020139490A (en) * 2019-03-01 2020-09-03 サンデン・オートモーティブコンポーネント株式会社 Scroll compressor
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EP3546753A4 (en) 2019-11-27
EP3546753B1 (en) 2024-04-24
CN109996961B (en) 2020-12-18
EP3546753A1 (en) 2019-10-02
JPWO2018096824A1 (en) 2019-10-17
US20190309750A1 (en) 2019-10-10
CN109996961A (en) 2019-07-09

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