WO2011135816A1 - Rotary compressor - Google Patents

Rotary compressor Download PDF

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Publication number
WO2011135816A1
WO2011135816A1 PCT/JP2011/002370 JP2011002370W WO2011135816A1 WO 2011135816 A1 WO2011135816 A1 WO 2011135816A1 JP 2011002370 W JP2011002370 W JP 2011002370W WO 2011135816 A1 WO2011135816 A1 WO 2011135816A1
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WO
WIPO (PCT)
Prior art keywords
refrigerant
rotary compressor
working refrigerant
discharge
working
Prior art date
Application number
PCT/JP2011/002370
Other languages
French (fr)
Japanese (ja)
Inventor
信吾 大八木
裕文 吉田
健 苅野
啓晶 中井
竜一 大野
飯田 登
Original Assignee
パナソニック株式会社
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 パナソニック株式会社 filed Critical パナソニック株式会社
Priority to JP2012512657A priority Critical patent/JP5828075B2/en
Priority to CN201180021069.7A priority patent/CN102859199B/en
Priority to EP11774604.0A priority patent/EP2565459B1/en
Publication of WO2011135816A1 publication Critical patent/WO2011135816A1/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
    • F04C29/00Component parts, details or accessories of pumps or pumping installations, not provided for in groups F04C18/00 - F04C28/00
    • F04C29/06Silencing
    • F04C29/065Noise dampening volumes, e.g. muffler chambers
    • 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
    • F04C29/06Silencing
    • F04C29/068Silencing the silencing means being arranged inside the pump housing
    • 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
    • F04C18/30Rotary-piston pumps specially adapted for elastic fluids having the characteristics covered by two or more of groups F04C18/02, F04C18/08, F04C18/22, F04C18/24, F04C18/48, or having the characteristics covered by one of these groups together with some other type of movement between co-operating members
    • F04C18/32Rotary-piston pumps specially adapted for elastic fluids having the characteristics covered by two or more of groups F04C18/02, F04C18/08, F04C18/22, F04C18/24, F04C18/48, or having the characteristics covered by one of these groups together with some other type of movement between co-operating members having both the movement defined in group F04C18/02 and relative reciprocation between the co-operating members
    • 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
    • F04C2210/00Fluid
    • F04C2210/26Refrigerants with particular properties, e.g. HFC-134a
    • 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
    • F04C2210/00Fluid
    • F04C2210/26Refrigerants with particular properties, e.g. HFC-134a
    • F04C2210/263HFO1234YF
    • 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

Definitions

  • the present invention relates to room air conditioners, refrigerators, other air conditioners, etc., which use as a working refrigerant a refrigerant mainly containing hydrofluoroolefins that do not contain chlorine atoms and have a low global warming potential and a double bond between carbons.
  • the present invention relates to a rotary compressor that can be incorporated into a refrigeration cycle.
  • a rotary compressor is used that sucks the working refrigerant evaporated by the evaporator, compresses it to a pressure necessary for condensation, and sends the high-temperature and high-pressure working refrigerant into the refrigerant circuit. Since most of the power of the refrigeration apparatus is used in the compressor, the performance of the compressor greatly affects the performance of the refrigeration apparatus. In order to improve the performance of a rotary compressor used in a conventional HFC-based refrigerant, an optimum shape is designed for using HFC410A, which is a typical working refrigerant.
  • a rotary compressor is known as one of such rotary compressors (see, for example, Patent Document 1).
  • the rotary compressor is one in which an electric motor 101 and a compression mechanism 102 are connected by a shaft 103 and accommodated in a sealed container 100, and the electric motor 101 is constituted by a rotor 104 and a stator 105.
  • a balance weight 106 is provided on the top and bottom of the rotor to reduce vibration and noise in the vertical direction.
  • the rotor 104 is coupled to the compression mechanism unit 102 by a shaft 103, and the compression mechanism is operated by electrically rotating the rotor 104.
  • the compression mechanism unit 102 is supported by a compression chamber 110 formed by a cylinder 107, an upper end plate 108 and a lower end plate 109 that block both end faces of the cylinder 107, and an upper end plate 108 and a lower end plate 109 in the compression chamber.
  • a roller 111 fitted to the eccentric portion of the shaft 103, and a vane 112 which contacts the outer periphery of the roller 111 and reciprocates following the eccentric rotation of the roller 111 to partition the compression chamber into a low pressure portion and a high pressure portion. ing.
  • the cylinder 107 is opened with a suction port 114 for sucking the working refrigerant toward the low pressure portion in the compression chamber, and the upper plate 108 discharges the working refrigerant from the high pressure portion formed by turning from the low pressure portion in the compression chamber.
  • a discharge port (not shown) is opened, and the roller 111 is accommodated in a compression chamber 110 formed by a cylinder closed from above and below by an upper end plate 108 and a lower end plate 109.
  • a discharge muffler 117 is provided so as to cover the upper surface of the discharge valve.
  • the sliding contact portion of the roller 111 passes through the suction port 114 on the low pressure portion side and gradually separates from the suction chamber, and the working refrigerant is supplied from the suction port 114 to the suction chamber. Inhale.
  • the sliding part of the roller 111 approaches the discharge port (not shown) while gradually reducing the compression chamber 110, and when it is compressed to a predetermined pressure or higher, the discharge valve (not shown). Opens and discharges the working refrigerant from a discharge port (not shown). The discharged working refrigerant is discharged into the sealed space via a space formed by the discharge muffler and the upper end plate.
  • the working refrigerant when a refrigerant mainly containing hydrofluoroolefin not containing chlorine atoms and having a low global warming potential and having a double bond between carbon is used as the working refrigerant, the working refrigerant
  • the suction working refrigerant density is lower than that of HFC410A, which is a typical working refrigerant of conventional HFC refrigerants.
  • HFC410A which is a typical working refrigerant of conventional HFC refrigerants.
  • the present invention has been made in view of such problems of the prior art, and provides a rotary compressor that reliably reduces pressure loss, and is highly efficient, reliable, and durable. It is an object.
  • the space volume of the discharge muffler is set by the suction working refrigerant density.
  • the rotary compressor according to the present invention by providing a discharge muffler corresponding to the suction working refrigerant density, even if a working refrigerant having a low global warming potential is used, a decrease in reliability and durability due to refrigerant decomposition is suppressed. In addition, since a proper discharge muffler space area can be ensured, pressure loss can be reliably reduced, so that a highly reliable and highly efficient rotary compressor can be provided.
  • FIG. 1 is a longitudinal sectional view of a rotary compressor according to Embodiment 1 of the present invention.
  • FIG. 2 is a cross-sectional view of the discharge muffler portion in the first embodiment.
  • FIG. 3 is a longitudinal sectional view of the discharge muffler portion in the first embodiment.
  • FIG. 4 is a graph comparing the refrigerant density sucked by various working refrigerants under the condition that the condensation and saturation temperature is equivalent to R410A in a certain operating range of the compressor.
  • FIG. 5 is a characteristic diagram showing the global warming potential (GWP) according to the mixing ratio of the refrigerant in which two components of tetrafluoropropene and difluoromethane are mixed.
  • GWP global warming potential
  • FIG. 6 is a longitudinal sectional view of the discharge muffler portion in the second embodiment of the present invention.
  • FIG. 7 is a cross-sectional view of the discharge muffler portion in the third embodiment of the present invention.
  • FIG. 8 is a longitudinal sectional view of a compression mechanism section according to Embodiment 4 of the present invention.
  • FIG. 9 is a longitudinal sectional view of a conventional rotary compressor
  • the first invention encloses and compresses a single refrigerant containing hydrofluoroolefin having a double bond between carbon and carbon, or a working refrigerant mixed with hydrofluorocarbon which always contains at least a double bond and does not have a double bond.
  • the mechanism portion includes a suction port that sucks the working refrigerant, a compression chamber that uses the working refrigerant sucked from the suction port as a high pressure, a discharge port that discharges the working refrigerant that is high pressure in the compression chamber, A rotary compressor having a discharge muffler covering the discharge port, wherein the volume of the discharge muffler is set according to the density of the working refrigerant, and a pressure loss associated with an increase in the working refrigerant flow rate is ensured. It is possible to provide a rotary compressor that reduces the discharge temperature and prevents an increase in the discharge temperature and suppresses the reduction in reliability and durability due to the decomposition of the working refrigerant.
  • the discharge muffler according to the first invention is provided so as to form a space at least above the discharge port, and the working refrigerant is in a state where the flow velocity is high immediately after being discharged from the discharge port.
  • a low-noise, low-loss rotary compressor can be provided.
  • the discharge muffler according to the first and second aspects of the invention has a shape in which the axial direction of the shaft is a long side, and the discharge muffler is arranged in the flow direction of the working refrigerant discharged from the discharge port. Can reduce the pressure loss and discharge the discharged working refrigerant to a space away from the compression chamber. High efficiency can be achieved.
  • the discharge muffler of the first to third aspects of the invention has a shape in which no space volume is provided around the suction port, and high-temperature working refrigerant does not stay around the suction port. Therefore, the heat reception to the suction working refrigerant can be efficiently reduced, and an excessive increase in the discharge temperature can be prevented. For this reason, since decomposition
  • coolant can be reduced, a further highly reliable rotary compressor can be provided.
  • the discharge muffler of the first to fourth aspects of the invention is provided on the opposite side of the electric motor via the compression portion, and the heat generating portion due to the rotation of the electric motor of the working refrigerant. Therefore, it is easy to secure a space in which a discharge muffler is provided, so that it is possible to provide a rotary compressor that is easy to design and highly reliable. Moreover, since the periphery of the discharge muffler is surrounded by oil, low noise can be realized.
  • the sixth aspect of the invention is particularly configured to provide a plurality of the discharge mufflers according to the first to fifth aspects of the invention, and even if the space volume of the discharge muffler cannot be secured at one place, it is distributed at a plurality of places.
  • the degree of freedom in design can be improved, and a small and highly reliable rotary compressor can be provided.
  • the space volume of the discharge muffler of the first to sixth inventions is increased by 1.01 to 1.7 times compared to the case where the working refrigerant uses R410A.
  • a highly reliable and highly efficient rotary compressor can be provided.
  • the hydrofluoroolefin is tetrafluoropropene or trifluoropropene, a single refrigerant, or the main component thereof, and the global warming potential is 5 or more. Therefore, it is possible to provide a rotary compressor that has a low environmental load and is highly reliable and highly efficient.
  • the ninth invention is particularly the working refrigerant of the first to eighth inventions
  • the hydrofluoroolefin is mainly composed of tetrafluoropropene or trifluoropropene, difluoromethane and pentafluoroethane, and a global warming potential of 5 or more.
  • 750 or less each of which is a mixture of two components or three components, has a low environmental load, suppresses the flow rate, and can lower the discharge temperature, effectively and highly reliable and highly efficient.
  • a rotary compressor can be provided.
  • the tenth invention is particularly set in the eighth or ninth invention such that the global warming potential is 350 or less.
  • the eleventh aspect of the invention relates to polyoxyalkylene glycols, polyvinyl ethers, poly (oxy) alkylene glycols or their monoether and polyvinyl ether copolymers, particularly as refrigeration oils used in the working refrigerants of the first to eighth aspects of the invention.
  • Synthetic oils based on oxygenated compounds such as polyol esters and polycarbonates, or synthetic oils based on alkylbenzenes and ⁇ -olefins as the main component, effectively rotating with high reliability and efficiency
  • a compressor can be provided.
  • the hydrofluoroolefin of the first to eleventh inventions is tetrafluoropropene (HFO1234yf), the hydrofluorocarbon is difluoromethane (HFC32), and the mixing ratio of the mixed refrigerant is tetrafluoropropene (HFO1234yf).
  • the working refrigerant composed of 80% hydrofluorocarbon and 20% difluoromethane (HFC32) is used, and the space volume of the discharge muffler is 1.01 to 1.4 times that of the case where the working refrigerant uses R410A.
  • the hydrofluoroolefin of the first to eleventh inventions is tetrafluoropropene (HFO1234yf), the hydrofluorocarbon is difluoromethane (HFC32), and the mixing ratio of the mixed refrigerant is tetrafluoropropene (HFO1234yf).
  • the working refrigerant composed of 60% hydrofluorocarbon and 40% difluoromethane (HFC32) is used, and the space volume of the discharge muffler is 1.01 to 1.2 times larger than the case where the working refrigerant uses R410A.
  • the year-round energy consumption efficiency as an air conditioner can ensure the same performance as HFC410A, and the environmental load can be kept small, effectively providing a highly reliable and highly efficient rotary compressor. Can do.
  • FIG. 1 is a longitudinal sectional view of a hermetic compressor according to Embodiment 1.
  • a rotary compressor is one in which an electric motor 2 and a compression mechanism 3 are connected by a shaft 31 and housed in a sealed container 1.
  • the compression mechanism 3 includes a cylinder 30 and both ends of the cylinder 30.
  • a compression chamber 39 formed by an upper end plate 34 and a lower end plate 35 that close the surface, and an eccentric portion 31a of the shaft 31 supported by the upper end plate 34 and the lower end plate 35 in the compression chamber 39 are fitted.
  • a roller 32 and a vane 33 that contacts the outer periphery of the roller 32 and reciprocates following the eccentric rotation of the roller 32 to partition the inside of the compression chamber 39 into a low pressure portion and a high pressure portion are provided.
  • the cylinder 30 is opened with a suction port 40 for sucking the working refrigerant toward the low pressure portion in the compression chamber 39, and the upper end plate 34 is operated from a high pressure portion formed by turning from the low pressure portion in the compression chamber 39.
  • a discharge port 38 for discharging the refrigerant is opened, and the roller 32 is accommodated in a compression chamber 39 formed by the cylinder 30 being closed from above and below by the upper end plate 34 and the lower end plate 35.
  • the discharge port 38 is formed as a hole penetrating the upper end plate 34, and a discharge valve 36 is provided on the upper surface of the discharge port 38 that is released when a pressure of a predetermined magnitude or more is applied.
  • a discharge muffler 37 is provided so as to cover the discharge valve 36.
  • the sliding contact part of the roller 32 passes through the suction port 40 and moves away while gradually expanding the suction chamber.
  • the working refrigerant is sucked into the suction chamber from the suction port 40.
  • the sliding portion of the roller 32 approaches the discharge port 38 while gradually reducing the compression chamber 39, and when the pressure is compressed to a predetermined pressure or higher, the discharge valve 36 opens and operates from the discharge port 38.
  • the refrigerant flows out and is discharged from the discharge muffler 37 into the sealed container 1, and passes through the notch 28 formed by the stator 22 and the inner wall of the sealed container 1, and the air gap 26 of the motor 2. It is sent out to the shell 5 space and discharged from the refrigerant discharge pipe 51 to the outside of the sealed container 1. Arrows indicate the refrigerant flow.
  • a single refrigerant of hydrofluoroolefin having a double bond between carbon and carbon or a mixed refrigerant mixed with a hydrofluorocarbon which always contains at least a double bond is not operated. Used as a refrigerant.
  • FIG. 2 is a transverse sectional view of the discharge muffler 37 as seen from the upper end plate 34 in the first embodiment
  • FIG. 3 is a longitudinal sectional view of the portion of the discharge muffler 37.
  • the space volume of the discharge muffler 37 is a hatched portion covered with the upper end plate 34 and the discharge muffler 37.
  • This space volume is set corresponding to the change in the density of the suction working refrigerant used in the present invention with respect to the density of the working refrigerant used in the compressor as a base.
  • the suction working refrigerant density used in the base compressor is A
  • the suction working refrigerant density used in the present invention is B.
  • the refrigerant used in the present invention has a flow rate of about A / B times that of the working refrigerant used in the base. For this reason, if the discharge muffler 37 is set to the same spatial volume as the conventional one, the refrigerant flow rate is too high, so that the working refrigerant discharged from the discharge port 38 cannot be allowed within the space volume of the discharge muffler 37. For this reason, the discharge from the discharge muffler 37 to the sealed container space is not smoothly performed and a loss occurs.
  • the space volume of the discharge muffler 37 of the rotary compressor designed for the conventional working refrigerant is set according to the suction working refrigerant density ratio. It has been changed. A specific example of setting the space area of the discharge muffler 37 will be described.
  • FIG. 4 is a diagram comparing the suction refrigerant density by various working refrigerants under the condition that the condensation and saturation temperature is equivalent to R410A in a certain operating range of the compressor in the first embodiment.
  • the dotted line shown in FIG. 4 is the suction refrigerant density when HFO1234yf and R32 are mixed at a mixing ratio of 5: 5. Even when a refrigerant in which HFO1234yf and R32 are mixed at various ratios, the suction refrigerant density based on the mixing ratio is calculated.
  • the discharge muffler 37 is not set larger than the space volume designed when the HFC 410A is used, the space volume is too small and pressure loss occurs.
  • the space volume is set larger than necessary, the sealed container 1 itself is enlarged, and a compact rotary compressor cannot be designed.
  • the spatial volume of the discharge muffler 37 is 1.01 to 1 compared to the case where the HFC 410A is used. It is formed to expand to about .7. Thereby, even when using HFO1234yf, a loss can be reduced, decomposition
  • coolant can be suppressed, and a compact highly efficient and highly reliable rotary compressor can be provided.
  • FIG. 5 is a characteristic diagram showing a global warming potential (GWP) according to a mixing ratio of a refrigerant in which two components of tetrafluoropropene and difluoromethane are mixed.
  • GWP global warming potential
  • the refrigerant in which a hydrofluoroolefin having a double bond between carbon and carbon is used as a basic component and a hydrofluorocarbon having no double bond is used, the refrigerant is refrigerated as compared with a single refrigerant of hydrofluoroolefin. It is possible to improve the predetermined characteristics such as capacity and make it easier to use as a refrigerant. Therefore, in the refrigerant to be sealed, the ratio of tetrafluoropropene including a single refrigerant is appropriately selected according to the purpose of the cooling cycle apparatus incorporating the compressor and the above-mentioned conditions such as the GWP restriction. That's fine.
  • difluoromethane in order to mix tetrafluoropropene and difluoromethane to make GWP150 or less, difluoromethane is 20 wt% or less, in order to make GWP300 or less, difluoromethane is 40 wt% or less, Will be mixed with.
  • the mixing ratio of HFO1234yf and R32 is 8: 2
  • GWP150 or less can be satisfied, and the ratio of the density of the suction gas at this time is HFO1234yf: HFC410A ⁇ 1: 1.4.
  • HFO1234yf and R32 are used as working refrigerants, a refrigerant having a flow rate approximately 1.4 times that of HFC410A flows. Therefore, when the HFO 1234yf is used based on the spatial volume of the discharge muffler 37 when the HFC 410A is used, the spatial volume of the discharge muffler 37 is 1.01 to 1 compared with the case where the HFC 410A is used. If the magnification is increased by about 4 times, the influence on the global environment is suppressed, the loss is reduced, and the decomposition of the refrigerant is suppressed, so that a highly efficient and highly reliable rotary compressor can be provided.
  • HFO1234yf and R32 are used as a mixed refrigerant of HFO1234yf and R32 when the ratio is 6: 4, in view of efficiency including pressure loss as a refrigeration cycle device, performance almost equivalent to conventional year-round energy consumption efficiency And GWP could be suppressed to the lowest level.
  • the ratio of the density of the suction gas at this time is HFO1234yf: HFC410A ⁇ 1: 1.2. For this reason, when HFO1234yf and R32 are used as working refrigerants, a refrigerant having a flow rate approximately 1.2 times that of HFC410A flows.
  • the spatial volume of the discharge muffler 37 is 1.01 to 1 compared with the case where the HFC 410A is used. If it is enlarged to about twice, it is possible to provide a highly efficient and highly reliable rotary compressor because the environmental load is reduced, the loss is reduced, and the decomposition of the refrigerant is suppressed.
  • the mixed refrigerant mixed at the above ratio can reduce the temperature difference in spite of the non-azeotropic mixed refrigerant and behaves more like a pseudo-azeotropic mixed refrigerant, improving the cooling performance and cooling performance coefficient (COP) of the refrigeration system. can do.
  • the discharge muffler 37 is shaped so as to provide a space at least above the discharge port 38, it is possible to prevent the working refrigerant from colliding with the discharge muffler 37 in a state where the flow velocity immediately after being discharged from the discharge port 38 is high. It is possible to provide a rotary compressor with low noise and low loss.
  • FIG. 6 is a longitudinal sectional view of the discharge muffler 37 portion in the second embodiment.
  • the second embodiment is different from the first embodiment in the following points, and is basically the same as the first embodiment in the other points. Only the part is explained. The same applies to each embodiment described below.
  • the discharge muffler 37 b has a space volume along the axial direction of the shaft 31.
  • the axial length L of the shaft 31 is longer than the horizontal length W of the shaft 31. Since the space volume of the discharge muffler 37b can be ensured while reducing the heat receiving area from the discharge muffler 37b to the compression chamber 39, over-compression and re-expansion can be prevented, and the rise in discharge temperature can be suppressed. Therefore, the decomposition of the refrigerant can be suppressed, and a highly efficient and highly reliable rotary compressor can be provided.
  • FIG. 7 is a cross-sectional view of the discharge muffler portion in the third embodiment.
  • the discharge muffler 37 c has a shape that avoids the periphery of the suction port 40.
  • heat received by the suction working refrigerant through the discharge muffler 37c can be efficiently reduced, an excessive increase in the discharge working refrigerant temperature can be prevented, and highly reliable rotary compression that suppresses decomposition of the working refrigerant. Machine can be provided.
  • FIG. 8 is a vertical cross-sectional view of the compression mechanism in the fourth embodiment.
  • the discharge muffler 37 d is provided on the side opposite to the electric motor 2 so as to cover the lower end plate 35 of the compression chamber 39.
  • the working refrigerant can reduce the heat received from the heat generation part due to the rotation of the electric motor 2, and there is no other part such as the electric motor 2 in the vicinity of the discharge muffler 37d, so that it is easy to secure a space for providing the discharge muffler 37d. It is possible to provide a rotary compressor that is easy to design and highly reliable.
  • the increase in flow rate is not limited to the discharge muffler 37, and it is desirable to set the volume of the pressure loss generation part according to the density of the working refrigerant in the total pressure loss generation part. Based on this design guideline, a rotary compressor that has been conventionally used can be used with a different working refrigerant by a simple design change.
  • a single refrigerant composed of a refrigerant based on a hydrofluoroolefin having a double bond between carbon and carbon or a mixed refrigerant containing the refrigerant is used as a working refrigerant.
  • a refrigerant mixed with a hydrofluoroolefin having a double bond between them as a base component and a hydrofluorocarbon having no double bond may be used as a working refrigerant.
  • a mixed refrigerant in which the hydrofluoroolefin is tetrafluoropropene (HFO1234yf or HFO1234ze) and the hydrofluorocarbon is difluoromethane may be used as a working refrigerant.
  • a mixed refrigerant in which the hydrofluoroolefin is tetrafluoropropene (HFO1234yf) and the hydrofluorocarbon is pentafluoroethane (HFC125) may be used as the working refrigerant.
  • a three-component mixed refrigerant in which the hydrofluoroolefin is tetrafluoropropene (HFO1234yf) and the hydrofluorocarbon is pentafluoroethane (HFC125) and difluoromethane (HFC32) may be used as the working refrigerant.
  • a mixture of two or three components is preferably used so that the global warming potential is 5 or more and 750 or less, preferably 350 or less.
  • the refrigerating machine oil used for the working refrigerant includes polyoxyalkylene glycols, polyvinyl ethers, poly (oxy) alkylene glycols or their monoether and polyvinyl ether copolymers, polyol esters, and oxygen-containing compounds of polycarbonates. Or a synthetic oil mainly composed of alkylbenzenes or ⁇ -olefins.
  • the rotary compressor has been described as an example. However, it is needless to say that a scroll compressor which is one of rotary compressors may be used.
  • the rotary compressor according to the present invention uses, as a working refrigerant, a single refrigerant composed of a refrigerant based on carbon or a hydrofluoroolefin having a double bond between carbons or a mixed refrigerant containing the refrigerant. Even in this case, high efficiency and high reliability can be achieved. Thereby, it can apply also to the use of rotary compressors, such as an air conditioner, a heat pump type water heater, a refrigerator-freezer, and a dehumidifier.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Applications Or Details Of Rotary Compressors (AREA)

Abstract

Disclosed is a rotary compressor provided with a compression chamber (39) wherein a single refrigerant of hydrofluoroolefin having double bonds between carbons, or a working refrigerant which at least essentially contains the hydrofluoroolefin mixed with hydrofluorocarbon having no double bonds, is enclosed, and a compression mechanism unit (3) increases the pressure of the working refrigerant; a discharge port (38) for discharging the working refrigerant compressed in the compression chamber; and a discharge muffler (37) which covers the discharge port. The volume of the inner space of the discharge muffler is set in accordance with the density of the working refrigerant. Thus, the pressure loss associated with the increase of the flow rate of the working refrigerant can be reliably reduced, the discharge temperature can be prevented from increasing, and the dissolution of the working refrigerant can be suppressed.

Description

回転式圧縮機Rotary compressor
 本発明は、塩素原子を含まず地球温暖化係数の低い炭素と炭素間に2重結合を有するハイドロフルオロオレフィンを主体とした冷媒を作動冷媒としたルームエアコン、冷蔵庫、その他の空気調和装置等の冷凍サイクルに組み込まれることが可能な回転式圧縮機に関するものである。 The present invention relates to room air conditioners, refrigerators, other air conditioners, etc., which use as a working refrigerant a refrigerant mainly containing hydrofluoroolefins that do not contain chlorine atoms and have a low global warming potential and a double bond between carbons. The present invention relates to a rotary compressor that can be incorporated into a refrigeration cycle.
 従来の冷凍装置では作動冷媒としてオゾン層破壊係数ゼロのHFC(ハイドロフルオロカーボン)系に移行してきているが、このHFC系冷媒は一方では地球温暖化係数が非常に高いため近年問題になってきている。そこで塩素原子を含まず地球温暖化係数の低い炭素と炭素間に2重結合を有するハイドロフルオロオレフィンを主体とした冷媒の冷凍装置が考えられてきている。 In conventional refrigeration equipment, the working refrigerant has shifted to HFC (hydrofluorocarbon) system with zero ozone depletion coefficient, but this HFC refrigerant has become a problem in recent years due to its extremely high global warming potential. . Therefore, a refrigerant refrigeration system mainly composed of carbon containing no chlorine atoms and a low global warming potential and a hydrofluoroolefin having a double bond between the carbons has been considered.
 ところで冷凍装置などにおいては、蒸発器で蒸発した作動冷媒を吸入し、凝縮するために必要な圧力まで圧縮して冷媒回路中に高温高圧の作動冷媒を送り出す回転式圧縮機が使用されている。冷凍装置の動力の大部分は圧縮機で使用されるため、圧縮機の性能が冷凍装置の性能を大きく左右する。従来のHFC系冷媒で使用される回転式圧縮機は性能向上のため、代表的な作動冷媒であるHFC410Aを使用するにあたり最適な形状の設計がされている。 By the way, in a refrigeration apparatus or the like, a rotary compressor is used that sucks the working refrigerant evaporated by the evaporator, compresses it to a pressure necessary for condensation, and sends the high-temperature and high-pressure working refrigerant into the refrigerant circuit. Since most of the power of the refrigeration apparatus is used in the compressor, the performance of the compressor greatly affects the performance of the refrigeration apparatus. In order to improve the performance of a rotary compressor used in a conventional HFC-based refrigerant, an optimum shape is designed for using HFC410A, which is a typical working refrigerant.
 このような回転式圧縮機の一つとして、ロータリ圧縮機が知られている(例えば、特許文献1参照)。ロータリ圧縮機は、例えば図9に示すように、電動機101と圧縮機構部102をシャフト103で連結して密閉容器100内に収納したものであって、電動機101は回転子104と固定子105によって形成されており、回転子上下には鉛直方向に振動、騒音低減を目的としたバランスウエイト106が設けられている。回転子104はシャフト103によって圧縮機構部102に連結されており、電気的に回転子104を回転させることによって圧縮機構を作動させる。 A rotary compressor is known as one of such rotary compressors (see, for example, Patent Document 1). For example, as shown in FIG. 9, the rotary compressor is one in which an electric motor 101 and a compression mechanism 102 are connected by a shaft 103 and accommodated in a sealed container 100, and the electric motor 101 is constituted by a rotor 104 and a stator 105. A balance weight 106 is provided on the top and bottom of the rotor to reduce vibration and noise in the vertical direction. The rotor 104 is coupled to the compression mechanism unit 102 by a shaft 103, and the compression mechanism is operated by electrically rotating the rotor 104.
 圧縮機構部102は、シリンダ107と、このシリンダ107の両端面を閉塞する上端板108と下端板109とで形成された圧縮室110と、この圧縮室内に上端板108および下端板109に支持されたシャフト103の偏心部に嵌合されたローラ111と、このローラ111の外周に当接しローラ111の偏心回転に追従して往復運動し圧縮室内を低圧部と高圧部とに仕切るベーン112を備えている。 The compression mechanism unit 102 is supported by a compression chamber 110 formed by a cylinder 107, an upper end plate 108 and a lower end plate 109 that block both end faces of the cylinder 107, and an upper end plate 108 and a lower end plate 109 in the compression chamber. A roller 111 fitted to the eccentric portion of the shaft 103, and a vane 112 which contacts the outer periphery of the roller 111 and reciprocates following the eccentric rotation of the roller 111 to partition the compression chamber into a low pressure portion and a high pressure portion. ing.
 シリンダ107には、圧縮室内の低圧部に向けて作動冷媒を吸入する吸入ポート114が開通され、上端板108には、圧縮室内の低圧部から転じて形成される高圧部から作動冷媒を吐出する吐出ポート(図示せず)が開通されており、ローラ111はシリンダが上端板108,下端板109に上下から閉塞されることによって形成される圧縮室110に収容されている。吐出ポート(図示せず)の上面には所定の大きさ以上の圧力を受けた場合に解放される吐出バルブ(図示せず)が設けられている。そして吐出バルブ上面を覆うように吐出マフラ117が設けられている。 The cylinder 107 is opened with a suction port 114 for sucking the working refrigerant toward the low pressure portion in the compression chamber, and the upper plate 108 discharges the working refrigerant from the high pressure portion formed by turning from the low pressure portion in the compression chamber. A discharge port (not shown) is opened, and the roller 111 is accommodated in a compression chamber 110 formed by a cylinder closed from above and below by an upper end plate 108 and a lower end plate 109. On the upper surface of the discharge port (not shown), there is provided a discharge valve (not shown) that is released when a pressure of a predetermined magnitude or more is applied. A discharge muffler 117 is provided so as to cover the upper surface of the discharge valve.
 上述した構成のロータリ圧縮機においては、低圧部側ではローラ111の摺接部が吸入ポート114を通過して吸入室を徐々に拡大しながら離れていき、吸入ポート114から吸入室内に作動冷媒を吸入する。一方、高圧部側ではローラ111の摺動部が吐出ポート(図示せず)へ圧縮室110を徐々に縮小しながら近づいていき、所定圧力以上に圧縮された時点で吐出バルブ(図示せず)が開いて吐出ポート(図示せず)から作動冷媒を吐出させる。この吐出された作動冷媒が吐出マフラと上端板によって形成される空間を経由して密閉空間に放出される。 In the rotary compressor having the above-described configuration, the sliding contact portion of the roller 111 passes through the suction port 114 on the low pressure portion side and gradually separates from the suction chamber, and the working refrigerant is supplied from the suction port 114 to the suction chamber. Inhale. On the other hand, on the high pressure part side, the sliding part of the roller 111 approaches the discharge port (not shown) while gradually reducing the compression chamber 110, and when it is compressed to a predetermined pressure or higher, the discharge valve (not shown). Opens and discharges the working refrigerant from a discharge port (not shown). The discharged working refrigerant is discharged into the sealed space via a space formed by the discharge muffler and the upper end plate.
特開2008-303887号公報JP 2008-303887 A
 しかしながら、上記構成の回転式圧縮機において、塩素原子を含まず地球温暖化係数の低い炭素と炭素間に2重結合を有するハイドロフルオロオレフィンを主体とした冷媒を作動冷媒とした場合、前記作動冷媒の吸入作動冷媒密度は、従来のHFC系冷媒の代表的な作動冷媒であるHFC410Aに比べ、低下する。この為、従来のHFC410Aを作動冷媒とした圧縮機を使用する場合、その作動冷媒を多くする必要があり、その結果流量の増加に伴い、従来の吐出マフラでは、容積が不足する。また、流量が多いため、冷媒の流れが悪いと圧力損失がおき、圧縮機の効率低下を引き起こす。また、吐出マフラ内で冷媒が滞留すると、過圧縮や再膨張、吸入作動冷媒の受熱を引き起こすことになり、吐出される作動冷媒温度の過上昇の要因となる。塩素原子を含まず炭素と炭素間に2重結合を有するハイドロフルオロオレフィンを主体とした冷媒は、高温で分解しやすい特性を有するため、過圧縮、再膨張による吐出温度の上昇は致命的な問題となる。 However, in the rotary compressor configured as described above, when a refrigerant mainly containing hydrofluoroolefin not containing chlorine atoms and having a low global warming potential and having a double bond between carbon is used as the working refrigerant, the working refrigerant The suction working refrigerant density is lower than that of HFC410A, which is a typical working refrigerant of conventional HFC refrigerants. For this reason, when using the compressor which used the conventional HFC410A as the working refrigerant, it is necessary to increase the working refrigerant. As a result, the volume of the conventional discharge muffler becomes insufficient as the flow rate increases. Further, since the flow rate is large, if the refrigerant flow is poor, a pressure loss occurs, causing a reduction in the efficiency of the compressor. Further, if the refrigerant stays in the discharge muffler, it causes over-compression, re-expansion, and heat reception of the suction working refrigerant, which causes an excessive rise in the discharged working refrigerant temperature. Refrigerants mainly composed of hydrofluoroolefins that do not contain chlorine atoms and have a double bond between carbon and carbon have the property of easily decomposing at high temperatures. It becomes.
 本発明は、従来技術の有するこのような問題点に鑑みてなされたものであり、圧力損失を確実に低減し、高効率で信頼性、耐久性に優れた、回転式圧縮機を提供することを目的としている。 The present invention has been made in view of such problems of the prior art, and provides a rotary compressor that reliably reduces pressure loss, and is highly efficient, reliable, and durable. It is an object.
 上記目的を達成するため、本発明に係る回転式圧縮機は、吐出マフラの空間容積を、吸入作動冷媒密度によって設定したものである。 In order to achieve the above object, in the rotary compressor according to the present invention, the space volume of the discharge muffler is set by the suction working refrigerant density.
 これによって、圧力損失を確実に低減し、信頼性、耐久性に優れた、高効率な回転式圧縮機を提供できる。 This makes it possible to provide a highly efficient rotary compressor that reliably reduces pressure loss and has excellent reliability and durability.
 本発明に係る回転式圧縮機は、吸入作動冷媒密度に応じた吐出マフラを設けることによって、地球温暖化係数の低い作動冷媒を使用していても冷媒分解による信頼性、耐久性の低下を抑制し、かつ、適正な吐出マフラ空間面積を確保できるため、圧力損失を確実に低減できることから、高信頼性で高効率な回転式圧縮機を提供することができる。 In the rotary compressor according to the present invention, by providing a discharge muffler corresponding to the suction working refrigerant density, even if a working refrigerant having a low global warming potential is used, a decrease in reliability and durability due to refrigerant decomposition is suppressed. In addition, since a proper discharge muffler space area can be ensured, pressure loss can be reliably reduced, so that a highly reliable and highly efficient rotary compressor can be provided.
図1は本発明の実施の形態1におけるロータリ圧縮機の縦断面図1 is a longitudinal sectional view of a rotary compressor according to Embodiment 1 of the present invention. 図2は実施の形態1における吐出マフラ部の横断面図FIG. 2 is a cross-sectional view of the discharge muffler portion in the first embodiment. 図3は実施の形態1における吐出マフラ部の縦断面図FIG. 3 is a longitudinal sectional view of the discharge muffler portion in the first embodiment. 図4は圧縮機のある運転範囲で凝縮、飽和温度をR410Aと同等とする条件での各種作動冷媒による吸入冷媒密度を比較したグラフFIG. 4 is a graph comparing the refrigerant density sucked by various working refrigerants under the condition that the condensation and saturation temperature is equivalent to R410A in a certain operating range of the compressor. 図5はテトラフルオロプロペンとジフルオロメタンの2成分を混合した冷媒の混合比率による地球温暖化係数(GWP)を示した特性図FIG. 5 is a characteristic diagram showing the global warming potential (GWP) according to the mixing ratio of the refrigerant in which two components of tetrafluoropropene and difluoromethane are mixed. 図6は本発明の実施の形態2における吐出マフラ部の縦断面図FIG. 6 is a longitudinal sectional view of the discharge muffler portion in the second embodiment of the present invention. 図7は本発明の実施の形態3における吐出マフラ部の横断面図FIG. 7 is a cross-sectional view of the discharge muffler portion in the third embodiment of the present invention. 図8は本発明の実施の形態4における圧縮機構部の縦断面図FIG. 8 is a longitudinal sectional view of a compression mechanism section according to Embodiment 4 of the present invention. 図9は従来のロータリ圧縮機の縦断面図FIG. 9 is a longitudinal sectional view of a conventional rotary compressor
 第1の発明は、炭素と炭素間に2重結合を有するハイドロフルオロオレフィンを単一冷媒、またはそれを少なくとも必ず含有し、2重結合を有しないハイドロフルオロカーボンと混合した作動冷媒を封入し、圧縮機構部は前記作動冷媒を吸入する吸入ポートと、前記吸入ポートから吸入された前記作動冷媒を高圧とする圧縮室と、前記圧縮室にて高圧となった前記作動冷媒を排出する吐出ポートと、前記吐出ポートを覆う吐出マフラとを備えた回転式圧縮機であって、前記吐出マフラの空間容積を、前記作動冷媒の密度によって設定したものであり、作動冷媒流量増加に伴う圧力損失を確実に低減し、かつ吐出温度の上昇を防止し、作動冷媒分解による、信頼性、耐久性の低減を抑制した、回転式圧縮機を提供することができる。 The first invention encloses and compresses a single refrigerant containing hydrofluoroolefin having a double bond between carbon and carbon, or a working refrigerant mixed with hydrofluorocarbon which always contains at least a double bond and does not have a double bond. The mechanism portion includes a suction port that sucks the working refrigerant, a compression chamber that uses the working refrigerant sucked from the suction port as a high pressure, a discharge port that discharges the working refrigerant that is high pressure in the compression chamber, A rotary compressor having a discharge muffler covering the discharge port, wherein the volume of the discharge muffler is set according to the density of the working refrigerant, and a pressure loss associated with an increase in the working refrigerant flow rate is ensured. It is possible to provide a rotary compressor that reduces the discharge temperature and prevents an increase in the discharge temperature and suppresses the reduction in reliability and durability due to the decomposition of the working refrigerant.
 第2の発明は、特に、第1の発明の前記吐出マフラは少なくとも前記吐出ポート上部に空間を形成するように設けたものであり、吐出ポートから吐出された直後の流速の速い状態で作動冷媒が、吐出マフラに衝突することを避けられるため、低騒音で損失の少ない回転式圧縮機を提供することができる。 In the second invention, in particular, the discharge muffler according to the first invention is provided so as to form a space at least above the discharge port, and the working refrigerant is in a state where the flow velocity is high immediately after being discharged from the discharge port. However, since it can avoid colliding with a discharge muffler, a low-noise, low-loss rotary compressor can be provided.
 第3の発明は、特に、第1~2の発明の前記吐出マフラは前記シャフトの軸方向が長辺となる形状としたものであり、吐出ポートから吐出された作動冷媒の流れ方向に吐出マフラの空間容積を確保できるため、圧力損失の低減ができ、かつ、圧縮室から離れた空間に吐出作動冷媒を排出するため、吸入作動冷媒への受熱を低減することにより、更なる高信頼性と高効率化を図ることができる。 According to a third aspect of the invention, in particular, the discharge muffler according to the first and second aspects of the invention has a shape in which the axial direction of the shaft is a long side, and the discharge muffler is arranged in the flow direction of the working refrigerant discharged from the discharge port. Can reduce the pressure loss and discharge the discharged working refrigerant to a space away from the compression chamber. High efficiency can be achieved.
 第4の発明は、特に、第1~3の発明の前記吐出マフラは前記吸入ポート周囲に空間容積を設けない形状としたものであり、吸入ポート周囲で高温の作動冷媒が滞留することがないので、吸入作動冷媒への受熱を効率的に低減することができ、吐出温度の過上昇を防ぐことができる。このため、作動冷媒の分解を低減することができるので、さらなる高信頼性な回転式圧縮機を提供することができる。 In the fourth aspect of the invention, in particular, the discharge muffler of the first to third aspects of the invention has a shape in which no space volume is provided around the suction port, and high-temperature working refrigerant does not stay around the suction port. Therefore, the heat reception to the suction working refrigerant can be efficiently reduced, and an excessive increase in the discharge temperature can be prevented. For this reason, since decomposition | disassembly of a working refrigerant | coolant can be reduced, a further highly reliable rotary compressor can be provided.
 第5の発明は、特に、第1~4の発明の前記吐出マフラは、前記圧縮部を介して、前記電動機とは反対側に設けたものであり、作動冷媒の電動機の回転による発熱部分からの受熱を低減でき、かつ、吐出マフラを設ける空間を確保しやすいので、設計が容易で高信頼性な回転式圧縮機を提供することができる。また吐出マフラ周囲がオイルに囲まれているため、低騒音も実現できる。 According to a fifth aspect of the invention, in particular, the discharge muffler of the first to fourth aspects of the invention is provided on the opposite side of the electric motor via the compression portion, and the heat generating portion due to the rotation of the electric motor of the working refrigerant. Therefore, it is easy to secure a space in which a discharge muffler is provided, so that it is possible to provide a rotary compressor that is easy to design and highly reliable. Moreover, since the periphery of the discharge muffler is surrounded by oil, low noise can be realized.
 第6の発明は、特に、第1~5の発明の前記吐出マフラを複数設ける構成としたものであり1箇所では吐出マフラの空間容積を確保できなくとも、複数の箇所に分散して設けることによって、設計自由度を向上させ、小型で、高信頼性な回転式圧縮機を提供することができる。 The sixth aspect of the invention is particularly configured to provide a plurality of the discharge mufflers according to the first to fifth aspects of the invention, and even if the space volume of the discharge muffler cannot be secured at one place, it is distributed at a plurality of places. Thus, the degree of freedom in design can be improved, and a small and highly reliable rotary compressor can be provided.
 第7の発明は、特に、第1~6の発明の吐出マフラの空間容積を、作動冷媒がR410Aを使用する場合に比べ、1.01~1.7倍に拡大したものであり、確実に、高信頼性で高効率な回転式圧縮機を提供することができる。 In the seventh invention, in particular, the space volume of the discharge muffler of the first to sixth inventions is increased by 1.01 to 1.7 times compared to the case where the working refrigerant uses R410A. A highly reliable and highly efficient rotary compressor can be provided.
 第8の発明は、特に、第1~7の発明における作動冷媒を、ハイドロフルオロオレフィンはテトラフルオロプロペンまたはトリフルオロプロペンとし、単一冷媒、またはそれらを主成分とし、地球温暖化係数が5以上、750以下となるように、それぞれ2成分混合もしくは3成分混合したもので、環境負荷が小さく、効果的に高信頼性で高効率な回転式圧縮機を提供することができる。 In the eighth invention, in particular, the working refrigerant in the first to seventh inventions, the hydrofluoroolefin is tetrafluoropropene or trifluoropropene, a single refrigerant, or the main component thereof, and the global warming potential is 5 or more. Therefore, it is possible to provide a rotary compressor that has a low environmental load and is highly reliable and highly efficient.
 第9の発明は、特に、第1~8の発明の作動冷媒を、ハイドロフルオロオレフィンはテトラフルオロプロペンまたはトリフルオロプロペンを主成分とし、ジフルオロメタンとペンタフルオロエタンを、地球温暖化係数が5以上、750以下となるように、それぞれ2成分混合もしくは3成分混合したものであり、環境負荷が小さく、流速を抑制し、吐出温度を下げることができるので、効果的に高信頼性で高効率な回転式圧縮機を提供することができる。 The ninth invention is particularly the working refrigerant of the first to eighth inventions, the hydrofluoroolefin is mainly composed of tetrafluoropropene or trifluoropropene, difluoromethane and pentafluoroethane, and a global warming potential of 5 or more. , 750 or less, each of which is a mixture of two components or three components, has a low environmental load, suppresses the flow rate, and can lower the discharge temperature, effectively and highly reliable and highly efficient. A rotary compressor can be provided.
 第10の発明は、特に、第8あるいは第9の発明において、地球温暖化係数が350以下となるように設定したものである。 The tenth invention is particularly set in the eighth or ninth invention such that the global warming potential is 350 or less.
 第11の発明は、特に、第1~8の発明の作動冷媒に用いる冷凍機油として、ポリオキシアルキレングリコール類、ポリビニルエーテル類、ポリ(オキシ)アルキレングリコールまたはそのモノエーテルとポリビニルエーテルの共重合体、ポリオールエステル類およびポリカーボネート類の含酸素化合物を主成分とする合成油か、アルキルベンゼン類やαオレフィン類を主成分とする合成油としたものであり、効果的に高信頼性で高効率な回転式圧縮機を提供することができる。  The eleventh aspect of the invention relates to polyoxyalkylene glycols, polyvinyl ethers, poly (oxy) alkylene glycols or their monoether and polyvinyl ether copolymers, particularly as refrigeration oils used in the working refrigerants of the first to eighth aspects of the invention. Synthetic oils based on oxygenated compounds such as polyol esters and polycarbonates, or synthetic oils based on alkylbenzenes and α-olefins as the main component, effectively rotating with high reliability and efficiency A compressor can be provided.
 第12の発明は、特に、第1~11の発明のハイドロフルオロオレフィンをテトラフルオロプロペン(HFO1234yf)とし、ハイドロフルオロカーボンをジフルオロメタン(HFC32)とし、混合冷媒の混合比をテトラフルオロプロペン(HFO1234yf)を80%、ハイドロフルオロカーボンをジフルオロメタン(HFC32)を20%で構成された作動冷媒とし、前記吐出マフラの空間容積を、作動冷媒がR410Aを使用する場合に比べ、1.01~1.4倍に拡大したことにより、GWP150以下を満足させ、環境負荷も小さく、効果的に高信頼性で高効率な回転式圧縮機を提供することができる。 In the twelfth invention, in particular, the hydrofluoroolefin of the first to eleventh inventions is tetrafluoropropene (HFO1234yf), the hydrofluorocarbon is difluoromethane (HFC32), and the mixing ratio of the mixed refrigerant is tetrafluoropropene (HFO1234yf). The working refrigerant composed of 80% hydrofluorocarbon and 20% difluoromethane (HFC32) is used, and the space volume of the discharge muffler is 1.01 to 1.4 times that of the case where the working refrigerant uses R410A. By enlarging, it is possible to provide a rotary compressor that satisfies GWP 150 or less, has a low environmental load, and is effectively highly reliable and highly efficient.
 第13の発明は、特に、第1~11の発明のハイドロフルオロオレフィンをテトラフルオロプロペン(HFO1234yf)とし、ハイドロフルオロカーボンをジフルオロメタン(HFC32)とし、混合冷媒の混合比をテトラフルオロプロペン(HFO1234yf)を60%、ハイドロフルオロカーボンをジフルオロメタン(HFC32)を40%で構成された作動冷媒とし、前記吐出マフラの空間容積を、作動冷媒がR410Aを使用する場合に比べ、1.01~1.2倍に拡大したことにより、空調機として通年エネルギー消費効率がHFC410Aと同等の性能を確保し、かつ環境負荷を小さく抑えることができ、効果的に高信頼性で高効率な回転式圧縮機を提供することができる。 In the thirteenth invention, in particular, the hydrofluoroolefin of the first to eleventh inventions is tetrafluoropropene (HFO1234yf), the hydrofluorocarbon is difluoromethane (HFC32), and the mixing ratio of the mixed refrigerant is tetrafluoropropene (HFO1234yf). The working refrigerant composed of 60% hydrofluorocarbon and 40% difluoromethane (HFC32) is used, and the space volume of the discharge muffler is 1.01 to 1.2 times larger than the case where the working refrigerant uses R410A. As a result of the expansion, the year-round energy consumption efficiency as an air conditioner can ensure the same performance as HFC410A, and the environmental load can be kept small, effectively providing a highly reliable and highly efficient rotary compressor. Can do.
 以下、本発明の実施の形態について、図面を参照しながら説明する。なお、この実施の形態によって本発明が限定されるものではない。 Hereinafter, embodiments of the present invention will be described with reference to the drawings. Note that the present invention is not limited to the embodiments.
 (実施の形態1)
 図1は実施の形態1における密閉型圧縮機の縦断面図である。図1において、ロータリ圧縮機は、電動機2と圧縮機構部3をシャフト31で連結して密閉容器1内に収納したものであって、圧縮機構部3は、シリンダ30と、このシリンダ30の両端面を閉塞する上端板34と下端板35とで形成された圧縮室39と、この圧縮室39内に上端板34および下端板35に支持されたシャフト31の偏芯部31aに嵌合されたローラ32と、このローラ32の外周に当接しローラ32の偏心回転に追従して往復運動し圧縮室39内を低圧部と高圧部とに仕切るベーン33を備えている。
(Embodiment 1)
1 is a longitudinal sectional view of a hermetic compressor according to Embodiment 1. FIG. In FIG. 1, a rotary compressor is one in which an electric motor 2 and a compression mechanism 3 are connected by a shaft 31 and housed in a sealed container 1. The compression mechanism 3 includes a cylinder 30 and both ends of the cylinder 30. A compression chamber 39 formed by an upper end plate 34 and a lower end plate 35 that close the surface, and an eccentric portion 31a of the shaft 31 supported by the upper end plate 34 and the lower end plate 35 in the compression chamber 39 are fitted. A roller 32 and a vane 33 that contacts the outer periphery of the roller 32 and reciprocates following the eccentric rotation of the roller 32 to partition the inside of the compression chamber 39 into a low pressure portion and a high pressure portion are provided.
 シリンダ30には、圧縮室39内の低圧部に向けて作動冷媒を吸入する吸入ポート40が開通され、上端板34には、圧縮室39内の低圧部から転じて形成される高圧部から作動冷媒を吐出する吐出ポート38が開通されており、ローラ32はシリンダ30が上端板34,下端板35に上下から閉塞されることによって形成される圧縮室39に収容されている。吐出ポート38は上端板34を貫通する孔として形成されており、吐出ポート38の上面には所定の大きさ以上の圧力を受けた場合に解放される吐出バルブ36が設けられている。そして、この吐出バルブ36を覆うように吐出マフラ37が設けられている。 The cylinder 30 is opened with a suction port 40 for sucking the working refrigerant toward the low pressure portion in the compression chamber 39, and the upper end plate 34 is operated from a high pressure portion formed by turning from the low pressure portion in the compression chamber 39. A discharge port 38 for discharging the refrigerant is opened, and the roller 32 is accommodated in a compression chamber 39 formed by the cylinder 30 being closed from above and below by the upper end plate 34 and the lower end plate 35. The discharge port 38 is formed as a hole penetrating the upper end plate 34, and a discharge valve 36 is provided on the upper surface of the discharge port 38 that is released when a pressure of a predetermined magnitude or more is applied. A discharge muffler 37 is provided so as to cover the discharge valve 36.
 以上のように構成された回転式圧縮機について、以下その動作、作用を説明すると、低圧部側ではローラ32の摺接部が吸入ポート40を通過して吸入室を徐々に拡大しながら離れていき、吸入ポート40から吸入室内に作動冷媒を吸入する。一方、高圧部側ではローラ32の摺動部が吐出ポート38へ圧縮室39を徐々に縮小しながら近づいていき、所定圧力以上に圧縮された時点で吐出バルブ36が開いて吐出ポート38から作動冷媒を流出し、吐出マフラ37より密閉容器1内に放出され、固定子22と密閉容器1内壁で形成された切欠部28と、電動機2のエアギャップ26を通って、電動機2の上部の上シェル5空間に送り出され、冷媒吐出管51から密閉容器1の外に吐出される。矢印は、冷媒の流れを示す。 The operation and action of the rotary compressor configured as described above will be described below. On the low pressure part side, the sliding contact part of the roller 32 passes through the suction port 40 and moves away while gradually expanding the suction chamber. The working refrigerant is sucked into the suction chamber from the suction port 40. On the other hand, on the high pressure side, the sliding portion of the roller 32 approaches the discharge port 38 while gradually reducing the compression chamber 39, and when the pressure is compressed to a predetermined pressure or higher, the discharge valve 36 opens and operates from the discharge port 38. The refrigerant flows out and is discharged from the discharge muffler 37 into the sealed container 1, and passes through the notch 28 formed by the stator 22 and the inner wall of the sealed container 1, and the air gap 26 of the motor 2. It is sent out to the shell 5 space and discharged from the refrigerant discharge pipe 51 to the outside of the sealed container 1. Arrows indicate the refrigerant flow.
 ここで、この回転式圧縮機では炭素と炭素間に2重結合を有するハイドロフルオロオレフィンを単一冷媒、またはそれを少なくとも必ず含有し、2重結合を有しないハイドロフルオロカーボンと混合した混合冷媒を作動冷媒として使用している。 Here, in this rotary compressor, a single refrigerant of hydrofluoroolefin having a double bond between carbon and carbon or a mixed refrigerant mixed with a hydrofluorocarbon which always contains at least a double bond is not operated. Used as a refrigerant.
 図2は本実施の形態1における上端板34からみた吐出マフラ37の横断面図、図3は同吐出マフラ37部の縦断面図である。 2 is a transverse sectional view of the discharge muffler 37 as seen from the upper end plate 34 in the first embodiment, and FIG. 3 is a longitudinal sectional view of the portion of the discharge muffler 37.
 図2、図3に示すように、吐出マフラ37の空間容積は上端板34と吐出マフラ37とで覆われた斜線部となる。この空間容積は、ベースとなる圧縮機で使用されている作動冷媒の密度に対して、本発明で使用する吸入作動冷媒の密度が変化することに対応して設定されている。 As shown in FIGS. 2 and 3, the space volume of the discharge muffler 37 is a hatched portion covered with the upper end plate 34 and the discharge muffler 37. This space volume is set corresponding to the change in the density of the suction working refrigerant used in the present invention with respect to the density of the working refrigerant used in the compressor as a base.
 すなわち、ベースとなる圧縮機で使用されている吸入作動冷媒密度をAとし、それに対して、本発明で使用する吸入作動冷媒密度をBとする。吸入作動冷媒密度がBはAよりも小さいと、ベースで使用されていた作動冷媒流量に比べ、本発明で使用する冷媒では約A/B倍の流量の冷媒が流れることとなる。このため、吐出マフラ37を従来と同じ空間容積に設定すると、冷媒流量が多すぎる為に、吐出マフラ37の空間容積以内で、吐出ポート38から吐出された作動冷媒を許容することができない。このため吐出マフラ37から密閉容器空間への放出もスムーズに行われなくなり損失がおきる。また、吐出ポート38への逆流も発生しやすくなるため、過圧縮、再膨張が発生しやすくなる。このため、冷媒の温度が上昇し、この種冷媒特有の課題である高温での分解が進行してしまう。 That is, the suction working refrigerant density used in the base compressor is A, and the suction working refrigerant density used in the present invention is B. When the suction working refrigerant density B is smaller than A, the refrigerant used in the present invention has a flow rate of about A / B times that of the working refrigerant used in the base. For this reason, if the discharge muffler 37 is set to the same spatial volume as the conventional one, the refrigerant flow rate is too high, so that the working refrigerant discharged from the discharge port 38 cannot be allowed within the space volume of the discharge muffler 37. For this reason, the discharge from the discharge muffler 37 to the sealed container space is not smoothly performed and a loss occurs. In addition, backflow to the discharge port 38 is likely to occur, and overcompression and reexpansion are likely to occur. For this reason, the temperature of a refrigerant | coolant rises and decomposition | disassembly at the high temperature which is a subject peculiar to this kind of refrigerant will advance.
 以上のことから、本発明で使用する作動冷媒を用いる場合には、従来の作動冷媒に対応して設計してある回転式圧縮機の吐出マフラ37の空間容積を、吸入作動冷媒密度比に応じて変更してある。この吐出マフラ37の空間面積設定の具体的な一例を説明する。 From the above, when using the working refrigerant used in the present invention, the space volume of the discharge muffler 37 of the rotary compressor designed for the conventional working refrigerant is set according to the suction working refrigerant density ratio. It has been changed. A specific example of setting the space area of the discharge muffler 37 will be described.
 図4は本実施の形態1における圧縮機のある運転範囲で凝縮、飽和温度をR410Aと同等とする条件での各種作動冷媒による吸入冷媒密度を比較した図である。図4に示す点線はHFO1234yfとR32を混合比、5:5で混合させたときの吸入冷媒密度である。HFO1234yfとR32を様々な比率で混合した冷媒としたときも、その混合比による吸入冷媒密度が算出される。 FIG. 4 is a diagram comparing the suction refrigerant density by various working refrigerants under the condition that the condensation and saturation temperature is equivalent to R410A in a certain operating range of the compressor in the first embodiment. The dotted line shown in FIG. 4 is the suction refrigerant density when HFO1234yf and R32 are mixed at a mixing ratio of 5: 5. Even when a refrigerant in which HFO1234yf and R32 are mixed at various ratios, the suction refrigerant density based on the mixing ratio is calculated.
 図4に示すように、従来使用している作動冷媒HFC410Aを使用した場合と、本発明で使用する作動冷媒をHFO1234yfを使用した場合、同一条件における吸入作動冷媒密度比は、HFO1234yf:HFC410A≒1:1.7である。このため、HFO1234yfを作動冷媒として、用いる場合、HFC410Aに比べ、おおよそ1.7倍の流量の冷媒が流れることとなる。 As shown in FIG. 4, when the conventionally used working refrigerant HFC410A is used and when the working refrigerant used in the present invention is HFO1234yf, the suction working refrigerant density ratio under the same conditions is HFO1234yf: HFC410A≈1. : 1.7. For this reason, when HFO1234yf is used as a working refrigerant, a refrigerant having a flow rate approximately 1.7 times that of HFC410A flows.
 このため、吐出マフラ37はHFC410Aを使用する場合に設計された空間容積よりも、大きく設定しなければ、空間容積が小さすぎ圧力損失が発生する。また、必要以上に空間容積を大きく設定すると、密閉容器1自体を大きくすることとなり、コンパクトな回転式圧縮機を設計できない。このため、HFC410Aを使用する際の吐出マフラ37の空間容積をベースとしたとき、HFO1234yfを使用する場合には、吐出マフラ37の空間容積を、HFC410Aを使用する場合に比べて1.01~1.7程度に拡大するように形成してある。これにより、HFO1234yfを使用する際でも、損失を低減し、冷媒の分解を抑制し、コンパクトな高効率で高信頼性の回転式圧縮機を提供することができる。 Therefore, if the discharge muffler 37 is not set larger than the space volume designed when the HFC 410A is used, the space volume is too small and pressure loss occurs. On the other hand, if the space volume is set larger than necessary, the sealed container 1 itself is enlarged, and a compact rotary compressor cannot be designed. For this reason, when the HFO 1234yf is used when the spatial volume of the discharge muffler 37 when using the HFC 410A is used as a base, the spatial volume of the discharge muffler 37 is 1.01 to 1 compared to the case where the HFC 410A is used. It is formed to expand to about .7. Thereby, even when using HFO1234yf, a loss can be reduced, decomposition | disassembly of a refrigerant | coolant can be suppressed, and a compact highly efficient and highly reliable rotary compressor can be provided.
 図5は、テトラフルオロプロペンとジフルオロメタンの2成分を混合した冷媒の混合比率による地球温暖化係数(GWP)を示した特性図である。冷媒をテトラフルオロプロペンの単一冷媒とした時にはGWP4となり極めて良好な値を示す。しかしながら、ハイドロフルオロカーボンと混合した冷媒に比べて比容積が大きいことなどから冷凍能力が低くなるため、より大きな冷却サイクル装置が必要になる。換言すれば、炭素と炭素間に2重結合を有するハイドロフルオロオレフィンを基本成分とし、2重結合を有しないハイドロフルオロカーボンを混合した冷媒を用いれば、ハイドロフルオロオレフィンの単一冷媒と比較して冷凍能力などの所定の特性を改善して冷媒として使用しやすくすることができる。従って、封入する冷媒において、単一冷媒を含めてテトラフルオロプロペンの割合をどれほどにするかは、圧縮機を組み込む冷却サイクル装置等の目的や上述したGWPの制限などの条件に応じて適宜選択すればよい。 FIG. 5 is a characteristic diagram showing a global warming potential (GWP) according to a mixing ratio of a refrigerant in which two components of tetrafluoropropene and difluoromethane are mixed. When the refrigerant is a single refrigerant of tetrafluoropropene, it becomes GWP4 and shows a very good value. However, since the refrigerating capacity is reduced due to the large specific volume as compared with the refrigerant mixed with hydrofluorocarbon, a larger cooling cycle device is required. In other words, if a refrigerant in which a hydrofluoroolefin having a double bond between carbon and carbon is used as a basic component and a hydrofluorocarbon having no double bond is used, the refrigerant is refrigerated as compared with a single refrigerant of hydrofluoroolefin. It is possible to improve the predetermined characteristics such as capacity and make it easier to use as a refrigerant. Therefore, in the refrigerant to be sealed, the ratio of tetrafluoropropene including a single refrigerant is appropriately selected according to the purpose of the cooling cycle apparatus incorporating the compressor and the above-mentioned conditions such as the GWP restriction. That's fine.
 具体的には図5に示すように、テトラフルオロプロペンとジフルオロメタンとを混合してGWP150以下とするためにはジフルオロメタンを20wt%以下、GWP300以下とするためにはジフルオロメタンを40wt%以下、と混合することになる。すなわちHFO1234yfとR32を混合比、8:2のときGWP150以下を満たすことができ、このときの吸入ガスの密度の比は、HFO1234yf:HFC410A≒1:1.4である。このため、HFO1234yfとR32を作動冷媒として用いる場合、HFC410Aに比べ、約1.4倍の流量の冷媒が流れることとなる。このことからHFC410Aを使用する際の吐出マフラ37の空間容積をベースとしたとき、HFO1234yfを使用する場合には、吐出マフラ37の空間容積を、HFC410Aを使用する場合に比べて1.01~1.4倍程度に拡大すれば、地球環境への影響を抑え、損失を低減し、冷媒の分解を抑制するため、高効率で高信頼性の回転式圧縮機を提供することができる。 Specifically, as shown in FIG. 5, in order to mix tetrafluoropropene and difluoromethane to make GWP150 or less, difluoromethane is 20 wt% or less, in order to make GWP300 or less, difluoromethane is 40 wt% or less, Will be mixed with. In other words, when the mixing ratio of HFO1234yf and R32 is 8: 2, GWP150 or less can be satisfied, and the ratio of the density of the suction gas at this time is HFO1234yf: HFC410A≈1: 1.4. For this reason, when HFO1234yf and R32 are used as working refrigerants, a refrigerant having a flow rate approximately 1.4 times that of HFC410A flows. Therefore, when the HFO 1234yf is used based on the spatial volume of the discharge muffler 37 when the HFC 410A is used, the spatial volume of the discharge muffler 37 is 1.01 to 1 compared with the case where the HFC 410A is used. If the magnification is increased by about 4 times, the influence on the global environment is suppressed, the loss is reduced, and the decomposition of the refrigerant is suppressed, so that a highly efficient and highly reliable rotary compressor can be provided.
 また、HFO1234yfとR32を混合比、6:4のときHFO1234yfとR32の混合冷媒として使用するとき、冷凍サイクル装置として圧損等を含めた効率を鑑みて、従来の通年エネルギー消費効率とほぼ同等の性能を維持しかつ、GWPをもっとも低く抑えることができた。このときの吸入ガスの密度の比は、HFO1234yf:HFC410A≒1:1.2である。このため、HFO1234yfとR32を作動冷媒として用いる場合、HFC410Aに比べ、約1.2倍の流量の冷媒が流れることとなる。このことからHFC410Aを使用する際の吐出マフラ37の空間容積をベースとしたとき、HFO1234yfを使用する場合には、吐出マフラ37の空間容積を、HFC410Aを使用する場合に比べて1.01~1.2倍程度に拡大すれば、環境負荷を抑えつつ、損失を低減し、冷媒の分解を抑制するため、高効率で高信頼性の回転式圧縮機を提供することができることができる。 In addition, when HFO1234yf and R32 are used as a mixed refrigerant of HFO1234yf and R32 when the ratio is 6: 4, in view of efficiency including pressure loss as a refrigeration cycle device, performance almost equivalent to conventional year-round energy consumption efficiency And GWP could be suppressed to the lowest level. The ratio of the density of the suction gas at this time is HFO1234yf: HFC410A≈1: 1.2. For this reason, when HFO1234yf and R32 are used as working refrigerants, a refrigerant having a flow rate approximately 1.2 times that of HFC410A flows. Therefore, when the HFO 1234yf is used based on the spatial volume of the discharge muffler 37 when the HFC 410A is used, the spatial volume of the discharge muffler 37 is 1.01 to 1 compared with the case where the HFC 410A is used. If it is enlarged to about twice, it is possible to provide a highly efficient and highly reliable rotary compressor because the environmental load is reduced, the loss is reduced, and the decomposition of the refrigerant is suppressed.
 これらによって回収されない冷媒が大気に放出されても地球温暖化に対しその影響を極少に保つことができる。また前記比率で混合された混合冷媒は、非共沸混合冷媒にも関わらず温度差を小さくでき擬似共沸混合冷媒に挙動が近づくため、冷凍装置の冷却性能や冷却性能係数(COP)を改善することができる。 Even if the refrigerant that is not recovered by these is released into the atmosphere, the influence on global warming can be kept to a minimum. In addition, the mixed refrigerant mixed at the above ratio can reduce the temperature difference in spite of the non-azeotropic mixed refrigerant and behaves more like a pseudo-azeotropic mixed refrigerant, improving the cooling performance and cooling performance coefficient (COP) of the refrigeration system. can do.
 また、上記吐出マフラ37は少なくとも吐出ポート38上部に空間を設けるような形状としてあるため、吐出ポート38から吐出された直後の流速の速い状態で作動冷媒が、吐出マフラ37に衝突することを避けれ、低騒音で損失の少ない回転式圧縮機を提供することができる。 Further, since the discharge muffler 37 is shaped so as to provide a space at least above the discharge port 38, it is possible to prevent the working refrigerant from colliding with the discharge muffler 37 in a state where the flow velocity immediately after being discharged from the discharge port 38 is high. It is possible to provide a rotary compressor with low noise and low loss.
 (実施の形態2)
 図6は実施の形態2における吐出マフラ37部の縦断面図である。この実施の形態2は、次に述べる点で実施の形態1と相違するものであり、その他の点については実施の形態1と基本的には同一であるので、重複する説明を省略し、異なる部分のみ説明する。以下、下記に説明する各実施の形態においても同様である。
(Embodiment 2)
FIG. 6 is a longitudinal sectional view of the discharge muffler 37 portion in the second embodiment. The second embodiment is different from the first embodiment in the following points, and is basically the same as the first embodiment in the other points. Only the part is explained. The same applies to each embodiment described below.
 図6に示すように吐出マフラ37bは、シャフト31の軸方向に沿って空間容積が形成されている。図6に示すように、シャフト31の軸方向長さLがシャフト31の水平方向長さWより長い構造である。吐出マフラ37bから圧縮室39への受熱面積を低減しつつ、吐出マフラ37bの空間容積を確保することができるので、過圧縮、再膨張を防止することができ、吐出温度の上昇を抑えることができるので、冷媒の分解を抑制でき、高効率で高信頼性の回転式圧縮機を提供することができる。 As shown in FIG. 6, the discharge muffler 37 b has a space volume along the axial direction of the shaft 31. As shown in FIG. 6, the axial length L of the shaft 31 is longer than the horizontal length W of the shaft 31. Since the space volume of the discharge muffler 37b can be ensured while reducing the heat receiving area from the discharge muffler 37b to the compression chamber 39, over-compression and re-expansion can be prevented, and the rise in discharge temperature can be suppressed. Therefore, the decomposition of the refrigerant can be suppressed, and a highly efficient and highly reliable rotary compressor can be provided.
 (実施の形態3)
 図7は実施の形態3における吐出マフラ部の横断面図である。図7に示すように、吐出マフラ37cはその形状を吸入ポート40の周囲を避けた形状としてある。これによって、吐出マフラ37cを通じての吸入作動冷媒への受熱を効率的に低減することができ、吐出作動冷媒温度の過上昇を防ぐことができ、作動冷媒の分解を抑える高信頼性の回転式圧縮機を提供することができる。
(Embodiment 3)
FIG. 7 is a cross-sectional view of the discharge muffler portion in the third embodiment. As shown in FIG. 7, the discharge muffler 37 c has a shape that avoids the periphery of the suction port 40. As a result, heat received by the suction working refrigerant through the discharge muffler 37c can be efficiently reduced, an excessive increase in the discharge working refrigerant temperature can be prevented, and highly reliable rotary compression that suppresses decomposition of the working refrigerant. Machine can be provided.
 (実施の形態4)
 図8は実施の形態4における圧縮機構部の縦断面図である。図8に示すように、吐出マフラ37dは圧縮室39の下端板35を覆うように電動機2とは反対側に設けてある。これにより、作動冷媒は電動機2の回転による発熱部分からの受熱を低減でき、かつ、吐出マフラ37d付近に電動機2のような他の部品がないため、吐出マフラ37dを設ける空間を確保しやすく、設計が容易で高信頼性な回転式圧縮機を提供することができる。
(Embodiment 4)
FIG. 8 is a vertical cross-sectional view of the compression mechanism in the fourth embodiment. As shown in FIG. 8, the discharge muffler 37 d is provided on the side opposite to the electric motor 2 so as to cover the lower end plate 35 of the compression chamber 39. Thereby, the working refrigerant can reduce the heat received from the heat generation part due to the rotation of the electric motor 2, and there is no other part such as the electric motor 2 in the vicinity of the discharge muffler 37d, so that it is easy to secure a space for providing the discharge muffler 37d. It is possible to provide a rotary compressor that is easy to design and highly reliable.
 また、吐出マフラ37dは下端板35周囲に貯留されたオイルに囲まれているため、低騒音の回転式圧縮機を提供することができる。 Further, since the discharge muffler 37d is surrounded by oil stored around the lower end plate 35, a low-noise rotary compressor can be provided.
 なお、流量の増加は吐出マフラ37に限定されたことでなく、全圧力損失発生部において、作動冷媒の密度によって圧力損失発生部の容積を設定することが望ましい。この設計指針に基づき、簡単な設計の変更で従来使用していた回転式圧縮機を異なる作動冷媒で使用することができる。 It should be noted that the increase in flow rate is not limited to the discharge muffler 37, and it is desirable to set the volume of the pressure loss generation part according to the density of the working refrigerant in the total pressure loss generation part. Based on this design guideline, a rotary compressor that has been conventionally used can be used with a different working refrigerant by a simple design change.
 上記実施の形態では、炭素と炭素間に2重結合を有するハイドロフルオロオレフィンをベース成分とした冷媒からなる単一冷媒または前記冷媒を含む混合冷媒を作動冷媒として使用しているが、炭素と炭素間に2重結合を有するハイドロフルオロオレフィンをベース成分とし、2重結合を有しないハイドロフルオロカーボンと混合した冷媒を作動冷媒として使用してもよい。 In the above embodiment, a single refrigerant composed of a refrigerant based on a hydrofluoroolefin having a double bond between carbon and carbon or a mixed refrigerant containing the refrigerant is used as a working refrigerant. A refrigerant mixed with a hydrofluoroolefin having a double bond between them as a base component and a hydrofluorocarbon having no double bond may be used as a working refrigerant.
 また、ハイドロフルオロオレフィンをテトラフルオロプロペン(HFO1234yfまたはHFO1234ze)とし、ハイドロフルオロカーボンをジフルオロメタン(HFC32)とした、混合冷媒を作動冷媒としてもよい。 Alternatively, a mixed refrigerant in which the hydrofluoroolefin is tetrafluoropropene (HFO1234yf or HFO1234ze) and the hydrofluorocarbon is difluoromethane (HFC32) may be used as a working refrigerant.
 また、ハイドロフルオロオレフィンをテトラフルオロプロペン(HFO1234yf)とし、ハイドロフルオロカーボンをペンタフルオロエタン(HFC125)とした、混合冷媒を作動冷媒としてもよい。 Also, a mixed refrigerant in which the hydrofluoroolefin is tetrafluoropropene (HFO1234yf) and the hydrofluorocarbon is pentafluoroethane (HFC125) may be used as the working refrigerant.
 また、ハイドロフルオロオレフィンをテトラフルオロプロペン(HFO1234yf)とし、ハイドロフルオロカーボンをペンタフルオロエタン(HFC125)、ジフルオロメタン(HFC32)とした、3成分からなる混合冷媒を作動冷媒としてもよい。 Also, a three-component mixed refrigerant in which the hydrofluoroolefin is tetrafluoropropene (HFO1234yf) and the hydrofluorocarbon is pentafluoroethane (HFC125) and difluoromethane (HFC32) may be used as the working refrigerant.
 そして、上記いずれの場合も地球温暖化係数が5以上、750以下となるように、望ましくは350以下となるようにそれぞれ2成分混合もしくは3成分混合したものが好ましい。 In any of the above cases, a mixture of two or three components is preferably used so that the global warming potential is 5 or more and 750 or less, preferably 350 or less.
 また、上記作動冷媒に用いる冷凍機油としては、ポリオキシアルキレングリコール類、ポリビニルエーテル類、ポリ(オキシ)アルキレングリコールまたはそのモノエーテルとポリビニルエーテルの共重合体、ポリオールエステル類およびポリカーボネート類の含酸素化合物を主成分とする合成油か、アルキルベンゼン類やαオレフィン類を主成分とする合成油が好ましい。 The refrigerating machine oil used for the working refrigerant includes polyoxyalkylene glycols, polyvinyl ethers, poly (oxy) alkylene glycols or their monoether and polyvinyl ether copolymers, polyol esters, and oxygen-containing compounds of polycarbonates. Or a synthetic oil mainly composed of alkylbenzenes or α-olefins.
 なお、上記各実施の形態ではロータリーコンプレッサーを例にして説明したが、回転式圧縮機のひとつであるスクロールコンプレッサーであってもよいのはもちろんである。 In each of the above embodiments, the rotary compressor has been described as an example. However, it is needless to say that a scroll compressor which is one of rotary compressors may be used.
 以上のように、本発明の回転式圧縮機は、炭素と炭素間に2重結合を有するハイドロフルオロオレフィンをベース成分とした冷媒からなる単一冷媒または前記冷媒を含む混合冷媒を作動冷媒として使用した場合でも、高効率化で高信頼性を図ることが可能となる。これにより、エアーコンディショナーやヒートポンプ式給湯機、冷凍冷蔵庫、除湿機など回転式圧縮機の用途にも適用できる。 As described above, the rotary compressor according to the present invention uses, as a working refrigerant, a single refrigerant composed of a refrigerant based on carbon or a hydrofluoroolefin having a double bond between carbons or a mixed refrigerant containing the refrigerant. Even in this case, high efficiency and high reliability can be achieved. Thereby, it can apply also to the use of rotary compressors, such as an air conditioner, a heat pump type water heater, a refrigerator-freezer, and a dehumidifier.
 1  密閉容器
 2  電動機
 26 エアギャップ
 28 切欠部
 3  圧縮機構部
 30 シリンダ
 31 シャフト
 31a 偏芯部
 32 ローラ
 33 ベ-ン
 34 上端板
 35 下端板
 36 吐出バルブ
 37、37b、37c、37d 吐出マフラ
 38 吐出ポート
 39 圧縮室
 40 吸入ポート
 51 冷媒吐出管
DESCRIPTION OF SYMBOLS 1 Airtight container 2 Electric motor 26 Air gap 28 Notch part 3 Compression mechanism part 30 Cylinder 31 Shaft 31a Eccentric part 32 Roller 33 Vane 34 Upper end plate 35 Lower end plate 36 Discharge valve 37, 37b, 37c, 37d Discharge muffler 38 Discharge port 39 Compression chamber 40 Suction port 51 Refrigerant discharge pipe

Claims (13)

  1. 炭素と炭素間に2重結合を有するハイドロフルオロオレフィンを単一冷媒、またはそれを少なくとも必ず含有し、2重結合を有しないハイドロフルオロカーボンと混合した作動冷媒を封入し、圧縮機構部は前記作動冷媒を吸入する吸入ポートと、前記吸入ポートから吸入された前記作動冷媒を高圧とする圧縮室と、前記圧縮室にて高圧となった前記作動冷媒を排出する吐出ポートと、前記吐出ポートを覆う吐出マフラとを備えた回転式圧縮機であって、前記吐出マフラの空間容積を、前記作動冷媒の密度によって設定したことを特徴とする回転式圧縮機。 A single refrigerant containing hydrofluoroolefin having a double bond between carbon and carbon, or at least a working refrigerant mixed with hydrofluorocarbon not containing a double bond is enclosed, and the compression mechanism section includes the working refrigerant. A suction port for sucking in, a compression chamber in which the working refrigerant sucked from the suction port has a high pressure, a discharge port for discharging the working refrigerant in a high pressure in the compression chamber, and a discharge covering the discharge port A rotary compressor including a muffler, wherein a spatial volume of the discharge muffler is set according to a density of the working refrigerant.
  2. 前記吐出マフラは少なくとも前記吐出ポート上部に空間を形成するように設けたことを特徴とする請求項1記載の回転式圧縮機。 The rotary compressor according to claim 1, wherein the discharge muffler is provided so as to form a space at least above the discharge port.
  3. 前記吐出マフラは前記シャフトの軸方向が長辺となる構成としたことを特徴とする請求項1または2記載の回転式圧縮機。 The rotary compressor according to claim 1 or 2, wherein the discharge muffler has a configuration in which an axial direction of the shaft is a long side.
  4. 前記吐出マフラは前記吸入ポート周囲に空間容積を設けない形状としたことを特徴とする請求項1~3のいずれか1項記載の回転式圧縮機。 The rotary compressor according to any one of claims 1 to 3, wherein the discharge muffler has a shape that does not provide a space volume around the suction port.
  5. 前記吐出マフラは、前記圧縮部を介して、前記電動機とは反対側に設けたことを特徴とする請求項1~4のいずれか1項記載の回転式圧縮機。 The rotary compressor according to any one of claims 1 to 4, wherein the discharge muffler is provided on the opposite side of the electric motor via the compressor.
  6. 前記吐出マフラを複数設けたことを特徴とする請求項1~5のいずれか1項記載の回転式圧縮機。 The rotary compressor according to any one of claims 1 to 5, wherein a plurality of the discharge mufflers are provided.
  7. 前記吐出マフラの空間容積を、作動冷媒がR410Aを使用する場合に比べ、1.01~1.70倍に拡大したことを特徴とする請求項1~6のいずれか1項記載の回転式圧縮機。 The rotary compression according to any one of claims 1 to 6, wherein a space volume of the discharge muffler is expanded by 1.01 to 1.70 times compared to a case where the working refrigerant uses R410A. Machine.
  8. ハイドロフルオロオレフィンはテトラフルオロプロペンまたはトリフルオロプロペンとし、単一冷媒、またはそれらを主成分とし、地球温暖化係数が5以上、750以下となるように、それぞれ2成分混合もしくは3成分混合した混合冷媒を作動冷媒としたことを特徴とする請求項1~7のいずれか1項記載の回転式圧縮機。 Hydrofluoroolefin is tetrafluoropropene or trifluoropropene and is a single refrigerant or a mixed refrigerant in which two or three components are mixed so that the main component thereof is a global warming potential of 5 or more and 750 or less. The rotary compressor according to any one of claims 1 to 7, wherein a working refrigerant is used.
  9. ハイドロフルオロオレフィンはテトラフルオロプロペンまたはトリフルオロプロペンを主成分とし、ジフルオロメタンとペンタフルオロエタンを、地球温暖化係数が5以上、750以下となるように、それぞれ2成分混合もしくは3成分混合した混合冷媒を作動冷媒としたことを特徴とする請求項1~8のいずれか1項記載の回転式圧縮機。 Hydrofluoroolefin is a mixed refrigerant in which tetrafluoropropene or trifluoropropene is the main component, and difluoromethane and pentafluoroethane are mixed in two or three components so that the global warming potential is 5 or more and 750 or less. The rotary compressor according to any one of claims 1 to 8, wherein a working refrigerant is used.
  10. 地球温暖化係数が350以下となるように設定した請求項8または9記載の回転式圧縮機。 The rotary compressor according to claim 8 or 9, wherein the global warming coefficient is set to be 350 or less.
  11. 冷凍機油として、ポリオキシアルキレングリコール類、ポリビニルエーテル類、ポリ(オキシ)アルキレングリコールまたはそのモノエーテルとポリビニルエーテルの共重合体、ポリオールエステル類およびポリカーボネート類の含酸素化合物を主成分とする合成油か、アルキルベンゼン類やαオレフィン類を主成分とする合成油としたことを特徴とする請求項1~8のいずれか1項記載の回転式圧縮機。 Is it a synthetic oil mainly composed of polyoxyalkylene glycols, polyvinyl ethers, poly (oxy) alkylene glycols or their monoether and polyvinyl ether copolymers, polyol esters, and oxygenates of polycarbonates as refrigeration oils? The rotary compressor according to any one of claims 1 to 8, which is a synthetic oil mainly composed of alkylbenzenes and α-olefins.
  12. ハイドロフルオロオレフィンをテトラフルオロプロペン(HFO1234yf)とし、ハイドロフルオロカーボンをジフルオロメタン(HFC32)とした、混合冷媒の混合比をテトラフルオロプロペン(HFO1234yf)を80%、ハイドロフルオロカーボンをジフルオロメタン(HFC32)を20%で構成された作動冷媒とし、前記吐出マフラの空間容積を、作動冷媒がR410Aを使用する場合に比べ、1.01~1.4倍に拡大したことを特徴とする請求項1~11のいずれか1項記載の回転式圧縮機。 The hydrofluoroolefin is tetrafluoropropene (HFO1234yf), the hydrofluorocarbon is difluoromethane (HFC32), the mixing ratio of the mixed refrigerant is 80% tetrafluoropropene (HFO1234yf), and the hydrofluorocarbon is 20% difluoromethane (HFC32). 12. The working refrigerant configured as described above, wherein a space volume of the discharge muffler is expanded 1.01 to 1.4 times compared to a case where the working refrigerant uses R410A. A rotary compressor according to claim 1.
  13. ハイドロフルオロオレフィンをテトラフルオロプロペン(HFO1234yf)とし、ハイドロフルオロカーボンをジフルオロメタン(HFC32)とした、混合冷媒の混合比をテトラフルオロプロペン(HFO1234yf)を60%、ハイドロフルオロカーボンをジフルオロメタン(HFC32)を40%で構成された作動冷媒とし、前記吐出マフラの空間容積を、作動冷媒がR410Aを使用する場合に比べ、1.01~1.2倍に拡大したことを特徴とする請求項1~11のいずれか1項記載の回転式圧縮機。 The hydrofluoroolefin is tetrafluoropropene (HFO1234yf), the hydrofluorocarbon is difluoromethane (HFC32), the mixing ratio of the mixed refrigerant is 60% tetrafluoropropene (HFO1234yf), and the hydrofluorocarbon is 40% difluoromethane (HFC32). 12. The working refrigerant configured as described above, wherein a space volume of the discharge muffler is expanded 1.01 to 1.2 times compared to a case where the working refrigerant uses R410A. A rotary compressor according to claim 1.
PCT/JP2011/002370 2010-04-28 2011-04-22 Rotary compressor WO2011135816A1 (en)

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