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WO2013031618A1 - Closed- and gas circulation-type freezing apparatus and operation method thereof - Google Patents

Closed- and gas circulation-type freezing apparatus and operation method thereof Download PDF

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Publication number
WO2013031618A1
WO2013031618A1 PCT/JP2012/071259 JP2012071259W WO2013031618A1 WO 2013031618 A1 WO2013031618 A1 WO 2013031618A1 JP 2012071259 W JP2012071259 W JP 2012071259W WO 2013031618 A1 WO2013031618 A1 WO 2013031618A1
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Prior art keywords
refrigerant gas
pressure
refrigerant
compressor
air
Prior art date
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Ceased
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PCT/JP2012/071259
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French (fr)
Japanese (ja)
Inventor
伸哉 石塚
一寿 上田
進太郎 村岡
智久 高橋
曜一 平賀
津幡 行一
明登 町田
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Mayekawa Manufacturing Co
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Mayekawa Manufacturing Co
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Publication date
Application filed by Mayekawa Manufacturing Co filed Critical Mayekawa Manufacturing Co
Priority to EP12820846.9A priority Critical patent/EP2602572B1/en
Priority to ES12820846.9T priority patent/ES2548077T3/en
Publication of WO2013031618A1 publication Critical patent/WO2013031618A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B9/00Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point
    • F25B9/002Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the refrigerant
    • F25B9/004Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the refrigerant the refrigerant being air

Definitions

  • the present invention relates to a refrigeration apparatus such as an air refrigerant type refrigeration apparatus that cools by sensible heat of a gas circulating in a gas phase, and more specifically, the refrigerant gas pressure in a compressor suction side refrigerant gas path can be adjusted.
  • the present invention relates to a closed-type gas circulation refrigeration apparatus.
  • Air is used as the refrigerant
  • high-pressure high-temperature air is used in the compressor, and this is cooled by a cooler using cooling water or a cold-heat recovery heat exchanger, and then low-pressure by an expander driven by the same drive shaft as the compressor.
  • an air refrigerant refrigeration apparatus that uses low-temperature air and performs cooling with sensible heat of the low-temperature and low-pressure air. Since the air refrigerant refrigeration apparatus does not use refrigerants such as Freon and ammonia, there is an advantage that the environment is not harmed.
  • an open-type air refrigerant refrigeration apparatus in which a part of the refrigerant air circulation system is provided with an atmosphere open end and the refrigerant air circulation system are connected to the atmosphere.
  • a closed type air refrigerant refrigeration apparatus hereinafter referred to as a closed type apparatus
  • the open type device discharges low-temperature air at the outlet side of the expander in the freezer, cools the object to be cooled with this low-temperature air, and supplies the air after cooling to the compressor suction connected to the compressor suction port It is returned to the side refrigerant air path.
  • the refrigerant air pressure in the compressor suction side refrigerant air passage is always maintained at atmospheric pressure.
  • the closed-type air refrigerant refrigeration system exchanges heat between the low-temperature air on the outlet side of the expander and the brine, and cools the object to be cooled with the cooled brine. It has a heat exchange configuration with a brine to be cooled. For this reason, the compressor suction side refrigerant air pressure varies depending on the operating state and is not constant.
  • the open-type device and the closed-type device cannot be used with the same design specifications (such as pressure), and devices with different design specifications are required, resulting in high costs.
  • the compressor suction side refrigerant air pressure of the closed type device can be adjusted, the pressure on the compressor suction side can be adjusted to atmospheric pressure, the deterioration of the cooling function can be eliminated, and the pressure resistance of the closed type device can be reduced with one model.
  • the deterioration of the cooling function can be eliminated.
  • Patent Document 1 is disclosed as a technique that makes it possible to adjust the compressor suction side refrigerant air pressure.
  • the device of Patent Document 1 is an open-type device, but when the compressor suction pressure is abnormally reduced, when dry air is supplied to the refrigerant flow path and the compressor suction pressure becomes equal to or higher than atmospheric pressure, a part of the refrigerant air Is provided with a flow path blockage prevention and pressure adjusting means for releasing the air to the outside.
  • the device disclosed in Patent Document 1 is an open-type device that originally discharges low-temperature air at the outlet side of the expander in the freezer, and is not a closed-type device, but maintains the compressor suction pressure at around atmospheric pressure.
  • JP 2004-317081 A Japanese Patent Laid-Open No. 10-47829
  • Patent Document 2 introduces dry air having a dew point of about ⁇ 30 ° C. into the compressor suction path, and then fills the refrigerant gas circulation path to a predetermined pressure, for example, about 1 kg / cm 2 G.
  • a predetermined pressure for example, about 1 kg / cm 2 G.
  • an operation for cooling the regenerator material with the refrigerant gas, and the circulating refrigerant Is applied to a special refrigeration device that performs the operation of freezing the object to be frozen at the same time or at different times, and only discloses that dry air is introduced before starting the compressor, There is no description of adjusting the side pressure.
  • An object of the present invention is to realize a closed-type gas circulation type refrigeration apparatus that can adjust the compressor suction side pressure with a simple and low-cost apparatus configuration in view of the problems of the prior art. To do.
  • a closed-type gas circulation refrigeration apparatus of the present invention includes a compressor and an expander connected to a single output shaft of a drive device, a cooler that cools a compressor discharge side refrigerant gas, A brine cooler that cools a brine that cools an object to be cooled with a refrigerant gas composed of air or nitrogen gas, and a cold recovery heat exchanger that further cools the refrigerant gas cooled by the cooler with a return refrigerant gas from the brine cooler
  • a closed-system refrigerant gas supply / discharge device comprising a compressor suction-side connection path that connects a tank and a compressor suction-side refrigerant gas path, and a compressor discharge-side connection path that connects an expansion tank and a compressor discharge-side refrigerant gas path
  • the device of the present invention even in a closed type device provided with the above-described closed system refrigerant gas supply / exhaust device without an open port to the outside, replenishment of refrigerant gas from the expansion tank to the compressor suction side refrigerant gas path; In order to discharge the refrigerant gas from the refrigerant gas path on the compressor discharge side to the expansion tank, the replenishment and expansion of the refrigerant gas from the expansion tank is ensured by using the pressure difference between the compressor discharge side and the suction side.
  • the refrigerant gas can be discharged to the tank.
  • the refrigerant gas pressure in the compressor suction side refrigerant gas path is maintained while maintaining the closed circulation system without unnecessary refrigerant gas being released into the atmosphere. Can be adjusted.
  • the expansion tank can be kept below 0.2 MPa (gauge pressure), which is the pressure outside the high-pressure gas safety method. As a result, even a closed type device can be used as a device having the same design specifications (such as pressure) as that of an open type device, and the cost can be reduced.
  • the refrigerant gas is not released to the outside. Therefore, the wear of the refrigerant gas is eliminated, and the external air is not mixed into the refrigerant gas path, so that the moisture of the external air is not mixed into the refrigerant gas. Therefore, if the expansion tank is filled with dry air or nitrogen gas having a dew point lower than the operating temperature of the refrigeration system, it can always be operated at a temperature higher than the dew point temperature of the refrigerant gas, so a dehumidifier is not required and the refrigerant gas The problem of increased pressure loss in the refrigerant gas flow path due to freezing of the contained water does not occur. Furthermore, wear of the refrigerant gas can be suppressed by using the closed system refrigerant gas supply / discharge device.
  • the refrigerant gas pressure in the expansion tank is maintained at a pressure higher than the refrigerant gas pressure in the compressor suction side refrigerant gas path, and at a pressure lower than the refrigerant gas pressure in the compressor discharge side refrigerant gas path and not applicable to the high pressure gas safety method. If it is less than a certain 0.2 MPa (gauge pressure), even a closed type device having the same design specifications as the open type device is low-cost and refrigerant from the expansion tank to the compressor suction side refrigerant gas path The gas supply and the discharge of the refrigerant gas from the compressor discharge side refrigerant gas passage to the expansion tank can be performed smoothly.
  • the first on-off valve provided in the compressor suction side connection path, the second on-off valve provided in the compressor discharge side connection path, the detection signal of the pressure sensor is input, the first on-off valve, And a controller that operates the second on-off valve to maintain the refrigerant gas pressure in the suction side refrigerant gas passage within a set range.
  • the first on-off valve is opened, the refrigerant gas is supplied to the compressor suction side refrigerant gas passage, and the detected value of the pressure sensor is set. If it exceeds the range, the second on-off valve opens, and excess refrigerant gas is recovered from the refrigerant gas passage to the expansion tank. As a result, the refrigerant gas pressure in the refrigerant gas passage can be accurately maintained within the set range.
  • the expansion tank contains a hollow stretchable body in which gas is sealed inside a stretchable hollow hermetic membrane, and the hollow stretchable body is placed in accordance with the refrigerant gas pressure in the compressor suction side refrigerant gas path.
  • the refrigerant gas pressure in the compressor suction side refrigerant gas passage may be configured to be expanded and contracted to be maintained within a set range. As a result, when the refrigerant gas pressure in the compressor suction side refrigerant gas path falls below the set range, the hollow expandable body automatically expands and supplies the refrigerant gas to the compressor suction side refrigerant gas path.
  • the compressor suction side refrigerant gas pressure in the refrigerant gas passage is kept within a set range without requiring complicated control such as valve operation. Can be maintained.
  • the compressor suction side refrigerant gas pressure can be automatically set by predetermining the gas pressure of the hollow stretchable body in accordance with the size of the expansion tank.
  • the operation method of the present invention using the apparatus of the present invention includes a step of detecting a refrigerant gas pressure in the suction side refrigerant gas path with a pressure sensor, and a suction side refrigerant from the expansion tank when the refrigerant gas pressure falls below a set range. Supplying the refrigerant gas to the gas passage and returning the refrigerant gas pressure to the set range; and when the refrigerant gas pressure exceeds the set range, discharging the refrigerant gas from the discharge side refrigerant gas passage to the expansion tank, Returning the refrigerant gas pressure in the refrigerant gas path to the set range.
  • the refrigerant gas is supplied / discharged between the closed system refrigerant gas supply / discharge device and the closed type refrigerant gas passage via the expansion tank, so that the compressor suction side refrigerant gas pressure is adjusted. It becomes possible.
  • the expansion tank can be kept below 0.2 MPa (gauge pressure), which is the pressure outside the high-pressure gas safety method. Further, wear due to the release of the refrigerant gas to the atmosphere (external) is eliminated, and the external air is not mixed into the refrigerant gas path.
  • the moisture of the external air is not mixed in the refrigerant gas, so that the operation can always be performed at or above the outdoor temperature of the refrigerant gas. Therefore, no dehumidifier is required. Further, since the sealed refrigerant gas supply / discharge device is used, there is no wear of the refrigerant gas.
  • the feature is that the refrigerant gas pressure in the expansion tank is higher than the refrigerant gas pressure in the compressor suction side refrigerant gas passage and lower than the refrigerant gas pressure in the compressor discharge side refrigerant gas passage (0.2 MPa (gauge). Pressure))), the refrigerant gas pressure in the compressor suction-side refrigerant gas passage can be adjusted smoothly, and it is not necessary to install a dehumidifier. Supply and discharge can be performed smoothly. Moreover, even a closed-type device can be used as a device having the same design specifications (such as pressure) as an open-type device, and the expansion tank is kept below 0.2 MPa (gauge pressure), which is a pressure not applied to the high-pressure gas safety law. Can be low cost.
  • FIG. 1 is a system diagram of a closed air refrigerant refrigeration apparatus according to a first embodiment in which the present invention is applied to an air refrigerant refrigeration apparatus. It is a system diagram of a closed type air refrigerant refrigeration apparatus according to a second embodiment in which the present invention is applied to an air refrigerant refrigeration apparatus.
  • FIG. 1 A first embodiment in which the present invention is applied to an air refrigerant refrigeration apparatus will be described with reference to FIG.
  • refrigerant air passages 12a to 12f through which refrigerant air circulates are provided.
  • a type heat exchanger 16, a heat recovery heat exchanger 18, and a brine cooler 20 are provided.
  • the compression / expansion unit 14 includes a compressor 22, a motor 24, and an expander 26.
  • the compressor 22 and the expander 26 are coupled to a rotating shaft 24a of the motor 24 and rotate coaxially.
  • the compressor discharge side refrigerant air passage 12 b connected to the discharge port of the compressor 22 is connected to the inlet of the high temperature side passage of the water-cooled heat exchanger 16.
  • the outlet of the high temperature side passage is connected to the refrigerant air passage 12c, and the other end of the refrigerant air passage 12c is connected to the inlet of the high temperature side passage of the heat recovery heat exchanger 18.
  • the outlet of the high temperature side passage is connected to the refrigerant air passage 12d, and the other end of the refrigerant air passage 12d is connected to the inlet of the expander 26.
  • the outlet of the expander 26 is connected to the refrigerant air passage 12e, and the other end of the refrigerant air passage 12e is connected to the inlet of the brine cooler 20.
  • the refrigerant air passage 12 f is connected to the outlet of the brine cooler 20, and the other end of the refrigerant air passage 12 f is connected to the inlet of the low temperature side passage of the heat recovery heat exchanger 18.
  • the outlet of the low temperature side flow path is connected to the compressor suction side refrigerant air path 12 a, and the other end of the compressor suction side refrigerant air path 12 a is connected to the suction port of the compressor 22.
  • a cooling water circulation path 28 is connected to the inlet and outlet of the low temperature side channel of the water-cooled heat exchanger 16.
  • the cooling water circulation path 28 is provided with a cooling tower 30, a pump 32, and a flow rate adjusting valve 34.
  • the cooling water is cooled by the cooling tower 30 and circulated in the direction of the arrow by the pump 32.
  • the cooling water circulation path 28 is appropriately supplemented with makeup water c such as well water and industrial water.
  • a brine circulation path 36 is disposed inside the brine cooler 20.
  • the brine circulation path 36 is connected to a heat exchange pipe 38 disposed inside the freezer 40.
  • a sealed expansion tank 51 is provided that encloses refrigerant air at a pressure equal to or higher than atmospheric pressure and has no open port to the outside.
  • the expansion tank 51 and the compressor suction side refrigerant air passage 12a communicate with each other through a compressor suction side connection (replenishment) passage 52, and the expansion tank 51 and the compressor discharge side refrigerant air passage 12b connect to the compressor discharge side connection ( (Recovery) Communicating through a path 54.
  • the compressor suction side connection (replenishment) path 52 is provided with a pressure reducing valve 56 and an electromagnetic valve 58
  • the compressor discharge side connection (recovery) path 54 is provided with an electromagnetic valve 60.
  • the expansion tank 51 is filled with dry air or nitrogen gas having a dew point lower than the operating temperature condition of the refrigeration apparatus.
  • the pressure in the expansion tank 51 is set higher than the refrigerant air pressure in the compressor suction side refrigerant air passage 12a and lower than the refrigerant air pressure in the compressor discharge side refrigerant air passage 12b.
  • a pressure sensor 62 for detecting refrigerant air pressure is provided in the compressor suction side refrigerant air passage 12a.
  • the controller 64 inputs the detection signal of the pressure sensor 62 and controls the opening / closing operation of the electromagnetic valves 58 and 60.
  • the expansion tank 51, the compressor suction side connection path 52, the compressor discharge side connection path 54, and the devices equipped thereto constitute a closed system refrigerant air supply / discharge device 50.
  • the refrigerant air is compressed by the compressor 22 and discharged at a high temperature and a high pressure.
  • the refrigerant air that has become high temperature and pressure is primarily cooled by cooling water in the water-cooled heat exchanger 16.
  • the primary cooled refrigerant air is secondarily cooled by the refrigerant air returned from the brine cooler 20 in the heat recovery heat exchanger 18.
  • the secondary-cooled refrigerant air is expanded by the expander 26 and becomes cryogenic and low-pressure refrigerant air.
  • the low-temperature and low-pressure refrigerant air is supplied to the brine cooler 20 through the refrigerant gas passage 12e, and the brine cooler 20 exchanges heat with the brine circulating in the brine circulation passage 36, thereby cooling the brine.
  • the cooled brine is sent to the heat exchange pipe 38 in the freezer 40, and the atmosphere in the freezer 40 is cooled to, for example, ⁇ 50 ° C. to ⁇ 100 ° C.
  • the object to be cooled such as food stored in the freezer 40 is stored frozen.
  • the refrigerant air after being used for cooling the brine by the brine cooler 20 reaches the heat recovery heat exchanger 18 via the refrigerant air passage 12f.
  • the heat recovery heat exchanger 18 exchanges heat with the refrigerant air before being sent to the expander 26, cools the refrigerant air, and then passes through the compressor suction side refrigerant air passage 12a to the suction port of the compressor 22. Sent.
  • the refrigerant air in the refrigerant air passages 12d to 12f gradually cools, and at the same time, the volume of the refrigerant air decreases, and the density increases as the volume decreases. I will do it.
  • the refrigerant air pressure in the refrigerant air passages 12a, 12e, and 12f gradually decreases, becomes negative in the compressor suction side refrigerant air passage 12a, and falls below the set range. Therefore, this is detected by the pressure sensor 62 and the electromagnetic valve 58 is opened by the controller 64.
  • the refrigerant air sealed in the expansion tank 51 is supplied to the compressor suction side refrigerant air path 12a via the compressor suction side connection (replenishment) path 52, and the refrigerant air pressure in the compressor suction side refrigerant air path 12a is reduced. Return to the setting range.
  • the operation may not be started. Therefore, when the refrigerant air pressure exceeds the set range, this is detected by the pressure sensor 62 and the electromagnetic valve 60 is opened by the controller 64. As a result, the refrigerant air in the compressor discharge side refrigerant air passage 12b is returned to the expansion tank 51 via the compressor discharge side connection (collection) passage 54, and the refrigerant air pressure in the compressor suction side refrigerant air passage 12a is returned to the set range. .
  • the refrigerant air pressure of the compressor suction side refrigerant air passage 12a of the closed-type air refrigerant refrigeration apparatus 10A can be adjusted within a set range, so that switching to an open-type air refrigerant refrigeration apparatus is possible. become. Therefore, one air refrigerant type refrigeration device can be used as both a closed type and an open type air refrigerant type refrigeration device, and the expansion tank 51 is 0.2 MPa (gauge pressure), which is a pressure not applied to the high-pressure gas safety method. Since it can hold below, it becomes low-cost.
  • the refrigerant air is supplied and discharged between the closed-system refrigerant air supply / discharge device 50 and the compressor suction-side refrigerant air passage 12a, the refrigerant air is not worn and the external air is not mixed into the refrigerant gas. Since there is no moisture in the external air in the refrigerant gas, it can always be operated above the outdoor temperature of the refrigerant gas. Therefore, no dehumidifier is required. Furthermore, since the refrigerant air is not released to the outside, the refrigerant air is not worn.
  • the refrigerant air is supplied from the expansion tank 51 to the low-pressure compressor suction-side refrigerant air passage 12a, and the refrigerant air in the compressor discharge-side refrigerant gas passage 12b is connected to the compressor discharge-side connection from the compressor discharge-side refrigerant air passage 12b ( Since the refrigerant is discharged to the low-pressure expansion tank 51 via the recovery) passage 54, the refrigerant air can be smoothly supplied and discharged from these refrigerant air passages. Further, the refrigerant air pressure in the compressor suction side refrigerant air passage 12a is detected by the pressure sensor 62, and the electromagnetic valves 58 and 60 are opened and closed by the controller 64 so that the detected pressure value falls within the set range. The refrigerant air pressure in the refrigerant air passage 12a can be accurately maintained within the set range.
  • air is used as the refrigerant gas, but nitrogen gas may be used instead of air.
  • nitrogen gas is sealed in the expansion tank 51.
  • the controller 64 controls the opening degree of the flow rate adjusting valve 34 to adjust the flow rate of the cooling water flowing through the cooling water circulation path 28, thereby adjusting the cooling capacity of the water-cooled heat exchanger 16. .
  • a hollow elastic body 74 in which a gas g is enclosed in an expansion / contraction hollow sealed membrane inside an expansion tank 72 constituting the closed-system refrigerant air supply / exhaust device 70.
  • the sealing film may be made of, for example, rubber, and air or nitrogen gas can be used as the gas g enclosed in the hollow stretchable body 74.
  • the pressure reducing valve 56 and the electromagnetic valve 58 of the first embodiment are removed from the suction side connection path 52, and the controller 64 inputs a detection signal of the pressure sensor 62.
  • the electromagnetic valve 60 is opened and closed according to the detection signal.
  • Other configurations are the same as those of the first embodiment.
  • the hollow sealed membrane 72 automatically expands, and the compressor suction side refrigerant passes through the compressor suction side connection (replenishment) passage 52. Refrigerant air is supplied to the air passage 12a. Conversely, if the refrigerant air pressure in the compressor suction side refrigerant air passage 12a rises, the refrigerant air around the telescopic hollow body 74 presses the telescopic hollow body 74 from the outside, so the telescopic hollow body 74 automatically contracts. Then, the refrigerant air is recovered from the compressor suction side refrigerant air passage 12a.
  • the electromagnetic valve 60 When the refrigerant air pressure in the compressor suction side refrigerant air passage 12 a exceeds the set range even by the expansion and contraction of the hollow elastic body 74, the electromagnetic valve 60 is opened by the controller 64 and the compressor discharge side connection (collection) passage 54 is connected. It collect
  • a pressure reducing valve and an on-off valve are provided in the compressor suction side refrigerant air passage 12a. Need not be provided. Therefore, since complicated control for operation of these valves is not required, there is an advantage that the closed-system refrigerant air supply / exhaust device 70 can be reduced in cost. Further, by predetermining the gas pressure of the hollow stretchable body 74 according to the size of the expansion tank 72, the refrigerant air pressure of the compressor suction side refrigerant air passage 12a can be automatically set.
  • the refrigerant gas pressure in the expansion tank is less than 0.2 MPa (gauge pressure), which is higher than the refrigerant gas pressure in the compressor suction side refrigerant gas path and lower than the refrigerant gas pressure in the compressor discharge side refrigerant gas path.
  • MPa gauge pressure

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  • Physics & Mathematics (AREA)
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Abstract

A closed- and gas circulation-type freezing apparatus (10A) of the present invention first cools a high-temperature and high-pressure refrigerant air compressed by a compressor (22) with a water-cooled heat exchanger (16) and a heat recovery heat exchanger (18), and then expands the air at an expander (26) to turn the air into a low-pressure refrigerant air having an extremely low temperature. The low-temperature and low-pressure refrigerant air is supplied to a brine cooler (20). A closed system refrigerant air supply and discharge device (50) is installed, which comprises an expansion tank (51), a compressor inlet side connection (52), and a compressor outlet side connection (54). A pressure sensor (62) is used to detect a pressure of the refrigerant air of a compressor inlet side refrigerant air passage (12a). The refrigerant air is supplied and discharged between the expansion tank (51) and the compressor inlet side refrigerant air passage (12a) or a compressor outlet side refrigerant air passage (12b) so that the pressure of the refrigerant air remain in a predetermined range.

Description

閉鎖型ガス循環式冷凍装置及びその運転方法Closed gas circulation refrigeration system and operation method thereof

 本発明は、空気冷媒式冷凍装置に代表されるような、気相で循環するガスの顕熱によって冷却を行なう冷凍装置に関し、詳しくは、圧縮機吸入側冷媒ガス路の冷媒ガス圧を調整可能にした閉鎖型ガス循環式冷凍装置に関する。 The present invention relates to a refrigeration apparatus such as an air refrigerant type refrigeration apparatus that cools by sensible heat of a gas circulating in a gas phase, and more specifically, the refrigerant gas pressure in a compressor suction side refrigerant gas path can be adjusted. The present invention relates to a closed-type gas circulation refrigeration apparatus.

 冷媒として空気を用い、圧縮機で高圧高温の空気とし、これを冷却水を用いた冷却器や冷熱回収熱交換器で冷却した後、圧縮機と同一の駆動軸で駆動される膨張機で低圧低温の空気とし、この低温低圧空気の顕熱で冷却を行なう空気冷媒式冷凍装置が知られている。空気冷媒式冷凍装置は、フロンやアンモニア等の冷媒を用いないので、環境を害しない利点がある。 Air is used as the refrigerant, high-pressure high-temperature air is used in the compressor, and this is cooled by a cooler using cooling water or a cold-heat recovery heat exchanger, and then low-pressure by an expander driven by the same drive shaft as the compressor. There is known an air refrigerant refrigeration apparatus that uses low-temperature air and performs cooling with sensible heat of the low-temperature and low-pressure air. Since the air refrigerant refrigeration apparatus does not use refrigerants such as Freon and ammonia, there is an advantage that the environment is not harmed.

 このような空気冷媒式冷凍装置には、冷媒空気循環系の一部に大気開放端を具えた開放型空気冷媒式冷凍装置(以下開放型装置という)と前記冷媒空気循環系が大気に対して閉鎖されている閉鎖型空気冷媒式冷凍装置(以下閉鎖型装置という)とがある。開放型装置は、例えば膨張機出口側の低温空気を冷凍庫内で放出し、この低温空気で冷却対象物を冷却し、冷却に供した後の空気を圧縮機吸入口に接続された圧縮機吸入側冷媒空気路に戻している。そのため、圧縮機吸入側冷媒空気路の冷媒空気圧は、常に大気圧に保持されている。一方、閉鎖型空気冷媒式冷凍装置は、冷媒空気循環系が大気に対して閉鎖されている為に、膨張機出口側の低温空気とブラインとを熱交換させ、冷却したブラインで冷却対象物を冷却するブラインを介在した熱交換構成にしている。そのため、圧縮機吸入側冷媒空気圧は、運転状態によって異なり、一定とはならない。 In such an air refrigerant refrigeration apparatus, an open-type air refrigerant refrigeration apparatus (hereinafter referred to as an open-type apparatus) in which a part of the refrigerant air circulation system is provided with an atmosphere open end and the refrigerant air circulation system are connected to the atmosphere. There is a closed type air refrigerant refrigeration apparatus (hereinafter referred to as a closed type apparatus) that is closed. The open type device, for example, discharges low-temperature air at the outlet side of the expander in the freezer, cools the object to be cooled with this low-temperature air, and supplies the air after cooling to the compressor suction connected to the compressor suction port It is returned to the side refrigerant air path. Therefore, the refrigerant air pressure in the compressor suction side refrigerant air passage is always maintained at atmospheric pressure. On the other hand, since the refrigerant air circulation system is closed to the atmosphere, the closed-type air refrigerant refrigeration system exchanges heat between the low-temperature air on the outlet side of the expander and the brine, and cools the object to be cooled with the cooled brine. It has a heat exchange configuration with a brine to be cooled. For this reason, the compressor suction side refrigerant air pressure varies depending on the operating state and is not constant.

 閉鎖型空気冷媒式冷凍装置は、大気圧で運転を開始した場合、冷媒空気循環系内の冷媒空気が徐々に冷えていき、体積の減少によって、冷媒空気循環系内の空気圧は徐々に低下し、圧縮機吸入側では負圧になる。そのため、圧縮機の圧縮機能や膨張機の冷却機能が急激に低下し、あるいは故障の原因となる。従って、開放型装置と閉鎖型装置とで、同一な(圧力等)の設計仕様の装置を兼用できず、夫々別な設計仕様の装置が必要になり、高コストとなる。 When the closed-type air refrigerant refrigeration system starts operating at atmospheric pressure, the refrigerant air in the refrigerant air circulation system gradually cools, and the air pressure in the refrigerant air circulation system gradually decreases as the volume decreases. In the compressor suction side, negative pressure is applied. For this reason, the compression function of the compressor and the cooling function of the expander are abruptly reduced or cause a failure. Therefore, the open-type device and the closed-type device cannot be used with the same design specifications (such as pressure), and devices with different design specifications are required, resulting in high costs.

 閉鎖型装置の圧縮機吸入側冷媒空気圧を調整可能とすれば、圧縮機吸入側で大気圧となることが出来、前記冷却機能の低下を解消できるとともに、耐圧的に一機種で閉鎖型装置と開放型装置とを兼用できると共に、閉鎖型装置として用いられとき、冷却機能の低下を解消できる。 If the compressor suction side refrigerant air pressure of the closed type device can be adjusted, the pressure on the compressor suction side can be adjusted to atmospheric pressure, the deterioration of the cooling function can be eliminated, and the pressure resistance of the closed type device can be reduced with one model. In addition to being able to be used as an open type device, when used as a closed type device, the deterioration of the cooling function can be eliminated.

 かかる圧縮機吸入側冷媒空気圧を調整可能とする技術として、例えば特許文献1が開示されている。
 かかる特許文献1の装置は、開放型装置であるが、圧縮機吸込圧の異常低下時に、乾燥空気を冷媒流路に供給し、圧縮機吸込圧が大気圧以上になると、冷媒空気の一部を外部に放出する流路閉塞防止兼圧力調整手段を具えている。
 前記特許文献1に開示された装置は、元々膨張機出口側の低温空気を冷凍庫内で放出する開放型の装置であって、閉鎖型装置ではないが、圧縮機吸込圧を大気圧前後に維持する点において、耐圧的に一機種で閉鎖型装置と開放型装置とを兼用できる課題を解決出来る。
 しかしながら前記装置にあっては、圧力調整のために圧縮機吸入側に乾燥空気導入部と空気放出路を設けているために導入する空気圧と放出する空気圧が平衡し易く、円滑な圧力制御が困難になり易い。
 また、閉鎖型の冷凍装置において、例えば特許文献2において、冷媒ガス補給装置から導入経路を介して冷媒ガス循環経路を形成する圧縮機吸入経路に、露点約-30℃の乾燥空気を導入する技術が開示されている。
For example, Patent Document 1 is disclosed as a technique that makes it possible to adjust the compressor suction side refrigerant air pressure.
The device of Patent Document 1 is an open-type device, but when the compressor suction pressure is abnormally reduced, when dry air is supplied to the refrigerant flow path and the compressor suction pressure becomes equal to or higher than atmospheric pressure, a part of the refrigerant air Is provided with a flow path blockage prevention and pressure adjusting means for releasing the air to the outside.
The device disclosed in Patent Document 1 is an open-type device that originally discharges low-temperature air at the outlet side of the expander in the freezer, and is not a closed-type device, but maintains the compressor suction pressure at around atmospheric pressure. In view of this, it is possible to solve the problem that a closed type device and an open type device can be used in a single model in terms of pressure.
However, in the above apparatus, since the dry air introduction part and the air discharge path are provided on the suction side of the compressor for pressure adjustment, the air pressure to be introduced and the air pressure to be released are easily balanced, and smooth pressure control is difficult. It is easy to become.
Further, in a closed refrigeration apparatus, for example, in Patent Document 2, a technique for introducing dry air having a dew point of about −30 ° C. into a compressor suction path that forms a refrigerant gas circulation path from a refrigerant gas replenishment apparatus via an introduction path. Is disclosed.

特開2004-317081号公報JP 2004-317081 A 特開平10-47829号公報Japanese Patent Laid-Open No. 10-47829

 前記特許文献2に開示された装置は、圧縮機吸入経路に、露点約-30℃の乾燥空気を導入して、その後に冷媒ガス循環経路内が所定圧力、例えば約1kg/cm2 G程度に充圧された後、圧縮機を起動する閉塞型装置(段落[0019]参照)ではあるが、段落[0008]に開示のあるように、前記冷媒ガスにより蓄冷材を冷却する運転と、前記循環冷媒により被冷凍物を冷凍する運転とを、同時に又は異なる時間帯に行うという特殊な冷凍装置に適用するもので、圧縮機を起動する前に乾燥空気を導入する旨の開示しかなく、圧縮機吸入側圧を調整することの記載はない。 The apparatus disclosed in Patent Document 2 introduces dry air having a dew point of about −30 ° C. into the compressor suction path, and then fills the refrigerant gas circulation path to a predetermined pressure, for example, about 1 kg / cm 2 G. Although it is a closed type device that starts the compressor after being pressurized (see paragraph [0019]), as disclosed in paragraph [0008], an operation for cooling the regenerator material with the refrigerant gas, and the circulating refrigerant Is applied to a special refrigeration device that performs the operation of freezing the object to be frozen at the same time or at different times, and only discloses that dry air is introduced before starting the compressor, There is no description of adjusting the side pressure.

 本発明は、かかる従来技術の課題に鑑み、空気又は窒素ガス冷媒とし、簡易かつ低コストな装置構成で、圧縮機吸入側圧を調整可能な閉鎖型ガス循環式冷凍装置を実現することを目的とする。 An object of the present invention is to realize a closed-type gas circulation type refrigeration apparatus that can adjust the compressor suction side pressure with a simple and low-cost apparatus configuration in view of the problems of the prior art. To do.

 かかる目的を達成するため、本発明の閉鎖型ガス循環式冷凍装置は、駆動装置の単一出力軸に連結された圧縮機及び膨張機と、圧縮機吐出側冷媒ガスを冷却する冷却器と、空気または窒素ガスからなる冷媒ガスで冷却対象物を冷却するブラインを冷却するブライン冷却器と、冷却器で冷却された冷媒ガスをブライン冷却器からの戻り冷媒ガスでさらに冷却する冷熱回収熱交換器とを備えた閉鎖型ガス循環式冷凍装置において、大気圧以上の圧力を有し且つ高圧ガス保安法適用外圧力である0.2MPa(ゲージ圧)未満の冷媒ガスが封入された膨張タンク、膨張タンクと圧縮機吸入側冷媒ガス路とを接続する圧縮機吸入側接続路、及び膨張タンクと圧縮機吐出側冷媒ガス路とを接続する圧縮機吐出側接続路からなる密閉系冷媒ガス給排装置と、圧縮機吸入側冷媒ガス路を流れる冷媒ガスの圧力を検出する圧力センサと、を備え、圧力センサで圧縮機吸入側冷媒ガス路の冷媒ガス圧を検出しながら、膨張タンクから圧縮機吸入側冷媒ガス路への冷媒ガスの補給と、圧縮機吐出側冷媒ガス路から膨張タンクへの冷媒ガスの排出とを行い、圧縮機吸入側冷媒ガス路の冷媒ガス圧を設定範囲に保持するように構成したものである。 In order to achieve such an object, a closed-type gas circulation refrigeration apparatus of the present invention includes a compressor and an expander connected to a single output shaft of a drive device, a cooler that cools a compressor discharge side refrigerant gas, A brine cooler that cools a brine that cools an object to be cooled with a refrigerant gas composed of air or nitrogen gas, and a cold recovery heat exchanger that further cools the refrigerant gas cooled by the cooler with a return refrigerant gas from the brine cooler An expansion tank in which a refrigerant gas having a pressure higher than atmospheric pressure and less than 0.2 MPa (gauge pressure), which is a pressure outside the high-pressure gas safety method, is enclosed, A closed-system refrigerant gas supply / discharge device comprising a compressor suction-side connection path that connects a tank and a compressor suction-side refrigerant gas path, and a compressor discharge-side connection path that connects an expansion tank and a compressor discharge-side refrigerant gas path A pressure sensor for detecting the pressure of the refrigerant gas flowing through the compressor suction side refrigerant gas path, and detecting the refrigerant gas pressure in the compressor suction side refrigerant gas path from the expansion tank while detecting the refrigerant gas pressure in the compressor suction side refrigerant gas path Refrigerant gas supply to the refrigerant gas passage and discharge of refrigerant gas from the compressor discharge side refrigerant gas passage to the expansion tank, so that the refrigerant gas pressure in the compressor suction side refrigerant gas passage is maintained within a set range. It is composed.

 本発明装置では、外部への開放口のない前記密閉系冷媒ガス給排装置を設けている閉塞型装置であっても、膨張タンクから圧縮機吸入側冷媒ガス路への冷媒ガスの補給と、圧縮機吐出側の冷媒ガス路から膨張タンクへの冷媒ガスの排出とを行うために、圧縮機吐出側と吸入側の圧力差を利用して確実に、膨張タンクよりの冷媒ガスの補給と膨張タンクへの冷媒ガスの排出を行う事が出来る。
 また、冷媒ガスの補給と排出は膨張タンクを経由する閉鎖循環路であるために、冷媒ガスの無用な大気放出がなく閉鎖循環系を維持しながら、圧縮機吸入側冷媒ガス路の冷媒ガス圧を調整可能になる。これによって、膨張タンクを高圧ガス保安法適用外圧力である0.2MPa(ゲージ圧)未満に保持することができる。
この結果閉鎖型装置であっても開放型装置と同一な(圧力等)の設計仕様の装置として兼用でき低コスト化が可能となる。
In the device of the present invention, even in a closed type device provided with the above-described closed system refrigerant gas supply / exhaust device without an open port to the outside, replenishment of refrigerant gas from the expansion tank to the compressor suction side refrigerant gas path; In order to discharge the refrigerant gas from the refrigerant gas path on the compressor discharge side to the expansion tank, the replenishment and expansion of the refrigerant gas from the expansion tank is ensured by using the pressure difference between the compressor discharge side and the suction side. The refrigerant gas can be discharged to the tank.
In addition, since the supply and discharge of the refrigerant gas is a closed circulation path via the expansion tank, the refrigerant gas pressure in the compressor suction side refrigerant gas path is maintained while maintaining the closed circulation system without unnecessary refrigerant gas being released into the atmosphere. Can be adjusted. As a result, the expansion tank can be kept below 0.2 MPa (gauge pressure), which is the pressure outside the high-pressure gas safety method.
As a result, even a closed type device can be used as a device having the same design specifications (such as pressure) as that of an open type device, and the cost can be reduced.

 また、冷媒ガスの外部への放散が生じない。そのため、冷媒ガスの損耗がなくなると共に、外部空気が冷媒ガス路に混入しないので、冷媒ガス中に外部空気の湿分が混入しない。従って、膨張タンクに冷凍装置の運転温度より低い露点をもつ乾燥空気若しくは窒素ガスを封入しておけば、常に冷媒ガスの露点温度以上で運転できるので、除湿機を必要とせず、また、冷媒ガス含有水分の凍結による冷媒ガス流路の圧力損失増加の問題も起こらない。更に、密閉系冷媒ガス給排装置を用いることで、冷媒ガスの損耗を抑制できる。 Also, the refrigerant gas is not released to the outside. Therefore, the wear of the refrigerant gas is eliminated, and the external air is not mixed into the refrigerant gas path, so that the moisture of the external air is not mixed into the refrigerant gas. Therefore, if the expansion tank is filled with dry air or nitrogen gas having a dew point lower than the operating temperature of the refrigeration system, it can always be operated at a temperature higher than the dew point temperature of the refrigerant gas, so a dehumidifier is not required and the refrigerant gas The problem of increased pressure loss in the refrigerant gas flow path due to freezing of the contained water does not occur. Furthermore, wear of the refrigerant gas can be suppressed by using the closed system refrigerant gas supply / discharge device.

 また、膨張タンクの冷媒ガス圧を圧縮機吸入側冷媒ガス路の冷媒ガス圧より高圧に保持すると共に、圧縮機吐出側冷媒ガス路の冷媒ガス圧より低圧の且つ高圧ガス保安法適用外圧力である0.2MPa(ゲージ圧)未満にしておけば、開放型装置と同様な設計仕様の閉鎖型装置であっても、低コストであり、且つ膨張タンクから圧縮機吸入側冷媒ガス路への冷媒ガスの供給と、圧縮機吐出側冷媒ガス路から膨張タンクへの冷媒ガスの排出とを、スムーズに行なうことができる。 In addition, the refrigerant gas pressure in the expansion tank is maintained at a pressure higher than the refrigerant gas pressure in the compressor suction side refrigerant gas path, and at a pressure lower than the refrigerant gas pressure in the compressor discharge side refrigerant gas path and not applicable to the high pressure gas safety method. If it is less than a certain 0.2 MPa (gauge pressure), even a closed type device having the same design specifications as the open type device is low-cost and refrigerant from the expansion tank to the compressor suction side refrigerant gas path The gas supply and the discharge of the refrigerant gas from the compressor discharge side refrigerant gas passage to the expansion tank can be performed smoothly.

 本発明において、圧縮機吸入側接続路に設けられた第1開閉弁と、圧縮機吐出側接続路に設けられた第2開閉弁と、圧力センサの検出信号を入力し、第1開閉弁及び第2開閉弁を操作して吸入側冷媒ガス路の冷媒ガス圧を設定範囲に保持するコントローラと、を備えるようにするとよい。 In the present invention, the first on-off valve provided in the compressor suction side connection path, the second on-off valve provided in the compressor discharge side connection path, the detection signal of the pressure sensor is input, the first on-off valve, And a controller that operates the second on-off valve to maintain the refrigerant gas pressure in the suction side refrigerant gas passage within a set range.

 かかる構成において、装置の運転中、圧力センサの検出値が設定範囲を下回れば、第1開閉弁が開いて、圧縮機吸入側冷媒ガス路に冷媒ガスが供給され、圧力センサの検出値が設定範囲を上回れば第2開閉弁が開いて、過剰な冷媒ガスを冷媒ガス路から膨張タンクに回収するようにする。これによって、冷媒ガス路の冷媒ガス圧を精度良く設定範囲に維持できる。 In such a configuration, when the detected value of the pressure sensor falls below the set range during operation of the apparatus, the first on-off valve is opened, the refrigerant gas is supplied to the compressor suction side refrigerant gas passage, and the detected value of the pressure sensor is set. If it exceeds the range, the second on-off valve opens, and excess refrigerant gas is recovered from the refrigerant gas passage to the expansion tank. As a result, the refrigerant gas pressure in the refrigerant gas passage can be accurately maintained within the set range.

 本発明装置において、膨張タンクが、伸縮可能な中空密閉膜の内部にガスを封入してなる中空伸縮体を内蔵し、圧縮機吸入側冷媒ガス路の冷媒ガス圧に応じて該中空伸縮体を伸縮させ、圧縮機吸入側冷媒ガス路の冷媒ガス圧を設定範囲に保持するように構成するとよい。これによって、圧縮機吸入側冷媒ガス路の冷媒ガス圧が設定範囲より低下すれば、中空伸縮体が自動的に膨張し、圧縮機吸入側冷媒ガス路に冷媒ガスを供給する。逆に、圧縮機吸入側冷媒ガス圧が設定範囲より上昇すれば、中空伸縮体の周囲の冷媒ガスが中空伸縮体を圧迫するので、中空伸縮体が自動的に収縮し、圧縮機吸入側冷媒ガス路から冷媒ガスを回収する。 In the apparatus of the present invention, the expansion tank contains a hollow stretchable body in which gas is sealed inside a stretchable hollow hermetic membrane, and the hollow stretchable body is placed in accordance with the refrigerant gas pressure in the compressor suction side refrigerant gas path. The refrigerant gas pressure in the compressor suction side refrigerant gas passage may be configured to be expanded and contracted to be maintained within a set range. As a result, when the refrigerant gas pressure in the compressor suction side refrigerant gas path falls below the set range, the hollow expandable body automatically expands and supplies the refrigerant gas to the compressor suction side refrigerant gas path. Conversely, if the compressor suction side refrigerant gas pressure rises above the set range, the refrigerant gas around the hollow stretchable body compresses the hollow stretchable body, so that the hollow stretchable body automatically contracts and the compressor suction side refrigerant is compressed. Recover the refrigerant gas from the gas path.

 かかる構成とすれば、圧縮機吸入側冷媒ガス路に減圧弁や開閉弁を設ける必要がなくなると共に、弁操作等の複雑な制御を必要とせずに、冷媒ガス路の冷媒ガス圧を設定範囲に維持できる。また、中空伸縮体のガス圧を膨張タンクの大きさに応じて予め決めておくことにより、圧縮機吸入側冷媒ガス圧を自動的に設定できる。 With this configuration, it is not necessary to provide a pressure reducing valve or an on-off valve in the compressor suction side refrigerant gas passage, and the refrigerant gas pressure in the refrigerant gas passage is kept within a set range without requiring complicated control such as valve operation. Can be maintained. Moreover, the compressor suction side refrigerant gas pressure can be automatically set by predetermining the gas pressure of the hollow stretchable body in accordance with the size of the expansion tank.

 前記本発明装置を利用した本発明の運転方法は、圧力センサで吸入側冷媒ガス路の冷媒ガス圧を検出するステップと、該冷媒ガス圧が設定範囲を下回った時、膨張タンクから吸入側冷媒ガス路に冷媒ガスを供給し、該冷媒ガス圧を設定範囲に戻すステップと、該冷媒ガス圧が設定範囲を上回った時、吐出側冷媒ガス路から膨張タンクに冷媒ガスを排出し、吸入側冷媒ガス路の冷媒ガス圧を設定範囲に戻すステップと、からなるものである。 The operation method of the present invention using the apparatus of the present invention includes a step of detecting a refrigerant gas pressure in the suction side refrigerant gas path with a pressure sensor, and a suction side refrigerant from the expansion tank when the refrigerant gas pressure falls below a set range. Supplying the refrigerant gas to the gas passage and returning the refrigerant gas pressure to the set range; and when the refrigerant gas pressure exceeds the set range, discharging the refrigerant gas from the discharge side refrigerant gas passage to the expansion tank, Returning the refrigerant gas pressure in the refrigerant gas path to the set range.

 本発明方法では、密閉系冷媒ガス給排装置と膨張タンクを経由する閉鎖型の冷媒ガス路との間で冷媒ガスの給排を行なうようにしているので、圧縮機吸入側冷媒ガス圧を調整可能になる。これによって、膨張タンクを高圧ガス保安法適用外圧力である0.2MPa(ゲージ圧)未満に保持することができる。また、冷媒ガスの大気(外部)への放出による損耗がなくなると共に、外部空気が冷媒ガス路に混入しない。そのため、乾燥ガスを膨張タンクに封入しておけば、冷媒ガス中に外部空気の湿分が混入しないので、常に冷媒ガスの露天温度以上で運転できる。従って、除湿機を必要としない。また、密閉型冷媒ガス給排装置を用いるので、冷媒ガスの損耗がない。 In the method of the present invention, the refrigerant gas is supplied / discharged between the closed system refrigerant gas supply / discharge device and the closed type refrigerant gas passage via the expansion tank, so that the compressor suction side refrigerant gas pressure is adjusted. It becomes possible. As a result, the expansion tank can be kept below 0.2 MPa (gauge pressure), which is the pressure outside the high-pressure gas safety method. Further, wear due to the release of the refrigerant gas to the atmosphere (external) is eliminated, and the external air is not mixed into the refrigerant gas path. Therefore, if the dry gas is sealed in the expansion tank, the moisture of the external air is not mixed in the refrigerant gas, so that the operation can always be performed at or above the outdoor temperature of the refrigerant gas. Therefore, no dehumidifier is required. Further, since the sealed refrigerant gas supply / discharge device is used, there is no wear of the refrigerant gas.

 本発明によれば、特徴は 膨張タンクの冷媒ガス圧を圧縮機吸入側冷媒ガス路の冷媒ガス圧より高圧で且つ圧縮機吐出側冷媒ガス路の冷媒ガス圧より低圧(の0.2MPa(ゲージ圧)未満)に保持することにより、圧縮機吸入側冷媒ガス路の冷媒ガス圧の調整を円滑に行なうことができるとともに、除湿機の設置等を必要とせず、冷媒ガス路からの冷媒ガスの給排をスムーズに行なうことができる。 しかも閉鎖型装置であっても開放型装置と同一な(圧力等)の設計仕様の装置として兼用でき、膨張タンクを高圧ガス保安法適用外圧力である0.2MPa(ゲージ圧)未満に保持することができるので低コストとなる。 According to the present invention, the feature is that the refrigerant gas pressure in the expansion tank is higher than the refrigerant gas pressure in the compressor suction side refrigerant gas passage and lower than the refrigerant gas pressure in the compressor discharge side refrigerant gas passage (0.2 MPa (gauge). Pressure))), the refrigerant gas pressure in the compressor suction-side refrigerant gas passage can be adjusted smoothly, and it is not necessary to install a dehumidifier. Supply and discharge can be performed smoothly. Moreover, even a closed-type device can be used as a device having the same design specifications (such as pressure) as an open-type device, and the expansion tank is kept below 0.2 MPa (gauge pressure), which is a pressure not applied to the high-pressure gas safety law. Can be low cost.

本発明を空気冷媒式冷凍装置に適用した第1実施形態に係る閉鎖型空気冷媒式冷凍装置の系統図である。1 is a system diagram of a closed air refrigerant refrigeration apparatus according to a first embodiment in which the present invention is applied to an air refrigerant refrigeration apparatus. 本発明を空気冷媒式冷凍装置に適用した第2実施形態に係る閉鎖型空気冷媒式冷凍装置の系統図である。It is a system diagram of a closed type air refrigerant refrigeration apparatus according to a second embodiment in which the present invention is applied to an air refrigerant refrigeration apparatus.

 以下、本発明を図に示した実施形態を用いて詳細に説明する。但し、この実施形態に記載されている構成部品の寸法、材質、形状、その相対配置などは特に特定的な記載がない限り、この発明の範囲をそれのみに限定する趣旨ではない。 Hereinafter, the present invention will be described in detail using embodiments shown in the drawings. However, the dimensions, materials, shapes, relative arrangements, and the like of the component parts described in this embodiment are not intended to limit the scope of the present invention to that unless otherwise specified.

(実施形態1)
 本発明を空気冷媒式冷凍装置に適用した第1実施形態を図1に基づいて説明する。図1に示す本実施形態に係る閉鎖型空気冷媒式冷凍装置10Aにおいて、冷媒空気が循環する冷媒空気路12a~fが設けられ、該冷媒空気路12a~fに、圧縮膨張ユニット14と、水冷式熱交換器16と、熱回収熱交換器18と、ブラインクーラ20とが設けられている。圧縮膨張ユニット14は、圧縮機22と、モータ24と、膨張機26とからなり、圧縮機22と膨張機26とは、モータ24の回転軸24aに結合され、同軸に回転する。
(Embodiment 1)
A first embodiment in which the present invention is applied to an air refrigerant refrigeration apparatus will be described with reference to FIG. In the closed-type air refrigerant refrigeration apparatus 10A according to the present embodiment shown in FIG. 1, refrigerant air passages 12a to 12f through which refrigerant air circulates are provided. A type heat exchanger 16, a heat recovery heat exchanger 18, and a brine cooler 20 are provided. The compression / expansion unit 14 includes a compressor 22, a motor 24, and an expander 26. The compressor 22 and the expander 26 are coupled to a rotating shaft 24a of the motor 24 and rotate coaxially.

 圧縮機22の吐出口に接続された圧縮機吐出側冷媒空気路12bは、水冷式熱交換器16の高温側流路の入口に接続されている。該高温側流路の出口は冷媒空気路12cに接続され、冷媒空気路12cの他端は、熱回収熱交換器18の高温側流路の入口に接続されている。該高温側流路の出口は冷媒空気路12dに接続され、冷媒空気路12dの他端は、膨張機26の入口に接続されている。 The compressor discharge side refrigerant air passage 12 b connected to the discharge port of the compressor 22 is connected to the inlet of the high temperature side passage of the water-cooled heat exchanger 16. The outlet of the high temperature side passage is connected to the refrigerant air passage 12c, and the other end of the refrigerant air passage 12c is connected to the inlet of the high temperature side passage of the heat recovery heat exchanger 18. The outlet of the high temperature side passage is connected to the refrigerant air passage 12d, and the other end of the refrigerant air passage 12d is connected to the inlet of the expander 26.

 膨張機26の出口は冷媒空気路12eに接続され、冷媒空気路12eの他端は、ブラインクーラ20の入口に接続されている。ブラインクーラ20の出口には冷媒空気路12fが接続され、冷媒空気路12fの他端は、熱回収熱交換器18の低温側流路の入口に接続されている。該低温側流路の出口は、圧縮機吸入側冷媒空気路12aに接続され、圧縮機吸入側冷媒空気路12aの他端は、圧縮機22の吸入口に接続されている。 The outlet of the expander 26 is connected to the refrigerant air passage 12e, and the other end of the refrigerant air passage 12e is connected to the inlet of the brine cooler 20. The refrigerant air passage 12 f is connected to the outlet of the brine cooler 20, and the other end of the refrigerant air passage 12 f is connected to the inlet of the low temperature side passage of the heat recovery heat exchanger 18. The outlet of the low temperature side flow path is connected to the compressor suction side refrigerant air path 12 a, and the other end of the compressor suction side refrigerant air path 12 a is connected to the suction port of the compressor 22.

 水冷式熱交換器16の低温側流路の入口及び出口は、冷却水循環路28が接続されている。冷却水循環路28には冷却塔30、ポンプ32及び流量調整弁34が設けられている。冷却水は、冷却塔30によって冷却され、ポンプ32によって矢印方向に循環する。冷却水循環路28には、適宜井水、工業用水等の補給水cが補給される。
 ブラインクーラ20の内部には、ブライン循環路36が配設されている。ブライン循環路36は、冷凍庫40の内部に配設された熱交換管38と接続されている。
A cooling water circulation path 28 is connected to the inlet and outlet of the low temperature side channel of the water-cooled heat exchanger 16. The cooling water circulation path 28 is provided with a cooling tower 30, a pump 32, and a flow rate adjusting valve 34. The cooling water is cooled by the cooling tower 30 and circulated in the direction of the arrow by the pump 32. The cooling water circulation path 28 is appropriately supplemented with makeup water c such as well water and industrial water.
A brine circulation path 36 is disposed inside the brine cooler 20. The brine circulation path 36 is connected to a heat exchange pipe 38 disposed inside the freezer 40.

 また、大気圧以上の圧力で冷媒空気を封入し、外部への開放口のない密閉された膨張タンク51が設けられている。膨張タンク51と圧縮機吸入側冷媒空気路12aとは圧縮機吸入側接続(補給)路52で連通しており、膨張タンク51と圧縮機吐出側冷媒空気路12bとは圧縮機吐出側接続(回収)路54で連通している。圧縮機吸入側接続(補給)路52には減圧弁56、電磁弁58が設けられ、圧縮機吐出側接続(回収)路54には電磁弁60が設けられている。なお、膨張タンク51には、冷凍装置の運転温度条件より低い露点となる乾燥空気若しくは窒素ガスを封入する。また、膨張タンク51内の圧力を、圧縮機吸入側冷媒空気路12aの冷媒空気圧より高く、圧縮機吐出側冷媒空気路12bの冷媒空気圧より低くなるようにしておく。 In addition, a sealed expansion tank 51 is provided that encloses refrigerant air at a pressure equal to or higher than atmospheric pressure and has no open port to the outside. The expansion tank 51 and the compressor suction side refrigerant air passage 12a communicate with each other through a compressor suction side connection (replenishment) passage 52, and the expansion tank 51 and the compressor discharge side refrigerant air passage 12b connect to the compressor discharge side connection ( (Recovery) Communicating through a path 54. The compressor suction side connection (replenishment) path 52 is provided with a pressure reducing valve 56 and an electromagnetic valve 58, and the compressor discharge side connection (recovery) path 54 is provided with an electromagnetic valve 60. The expansion tank 51 is filled with dry air or nitrogen gas having a dew point lower than the operating temperature condition of the refrigeration apparatus. The pressure in the expansion tank 51 is set higher than the refrigerant air pressure in the compressor suction side refrigerant air passage 12a and lower than the refrigerant air pressure in the compressor discharge side refrigerant air passage 12b.

 また、圧縮機吸入側冷媒空気路12aには、冷媒空気圧を検出する圧力センサ62が設けられている。コントローラ64は、圧力センサ62の検出信号を入力し、電磁弁58及び60の開閉動作を制御する。膨張タンク51、圧縮機吸入側接続路52、圧縮機吐出側接続路54、及びこれらに装備された機器類で密閉系冷媒空気給排装置50を構成している。 Further, a pressure sensor 62 for detecting refrigerant air pressure is provided in the compressor suction side refrigerant air passage 12a. The controller 64 inputs the detection signal of the pressure sensor 62 and controls the opening / closing operation of the electromagnetic valves 58 and 60. The expansion tank 51, the compressor suction side connection path 52, the compressor discharge side connection path 54, and the devices equipped thereto constitute a closed system refrigerant air supply / discharge device 50.

 かかる構成において、冷媒空気は圧縮機22で圧縮され、高温高圧となって吐出される。高温高圧となった冷媒空気は、水冷式熱交換器16で冷却水によって一次冷却される。一次冷却された冷媒空気は、熱回収熱交換器18で、ブラインクーラ20から戻った冷媒空気によって二次冷却される。二次冷却された冷媒空気は、膨張機26で膨張して極低温で低圧の冷媒空気となる。 In such a configuration, the refrigerant air is compressed by the compressor 22 and discharged at a high temperature and a high pressure. The refrigerant air that has become high temperature and pressure is primarily cooled by cooling water in the water-cooled heat exchanger 16. The primary cooled refrigerant air is secondarily cooled by the refrigerant air returned from the brine cooler 20 in the heat recovery heat exchanger 18. The secondary-cooled refrigerant air is expanded by the expander 26 and becomes cryogenic and low-pressure refrigerant air.

 低温低圧となった冷媒空気は、冷媒ガス路12eを経てブラインクーラ20に供給され、ブラインクーラ20でブライン循環路36を循環するブラインと熱交換し、ブラインを冷却する。ここで冷却されたブラインは、冷凍庫40内の熱交換管38に送られ、冷凍庫40内の雰囲気を、例えば-50℃~-100℃に冷却する。これによって、冷凍庫40に保管された食品等の冷却対象物を冷凍保存する。ブラインクーラ20でブラインの冷却に供した後の冷媒空気は、冷媒空気路12fを経て、熱回収熱交換器18に達する。そして、熱回収熱交換器18で膨張機26に送られる前の冷媒空気と熱交換し、該冷媒空気を冷却した後、圧縮機吸入側冷媒空気路12aを経て、圧縮機22の吸入口に送られる。 The low-temperature and low-pressure refrigerant air is supplied to the brine cooler 20 through the refrigerant gas passage 12e, and the brine cooler 20 exchanges heat with the brine circulating in the brine circulation passage 36, thereby cooling the brine. The cooled brine is sent to the heat exchange pipe 38 in the freezer 40, and the atmosphere in the freezer 40 is cooled to, for example, −50 ° C. to −100 ° C. As a result, the object to be cooled such as food stored in the freezer 40 is stored frozen. The refrigerant air after being used for cooling the brine by the brine cooler 20 reaches the heat recovery heat exchanger 18 via the refrigerant air passage 12f. The heat recovery heat exchanger 18 exchanges heat with the refrigerant air before being sent to the expander 26, cools the refrigerant air, and then passes through the compressor suction side refrigerant air passage 12a to the suction port of the compressor 22. Sent.

 閉鎖型空気冷媒式冷凍装置10Aの運転を開始すると、冷媒空気路12d~f内の冷媒空気が徐々に冷えていき、それと共に冷媒空気の体積が減少し、体積の減少と共に、その密度が増加していく。そのため、冷媒空気路12a,12e,12fの冷媒空気圧は徐々に低下し、圧縮機吸入側冷媒空気路12aでは負圧になり、設定範囲を下回る。そこで、圧力センサ62でそれを検出し、コントローラ64で電磁弁58を開放する。これによって、膨張タンク51に封入された冷媒空気が圧縮機吸入側接続(補給)路52を介して圧縮機吸入側冷媒空気路12aに供給され、圧縮機吸入側冷媒空気路12aの冷媒空気圧を設定範囲に戻す。 When the operation of the closed-type air refrigerant refrigeration apparatus 10A is started, the refrigerant air in the refrigerant air passages 12d to 12f gradually cools, and at the same time, the volume of the refrigerant air decreases, and the density increases as the volume decreases. I will do it. For this reason, the refrigerant air pressure in the refrigerant air passages 12a, 12e, and 12f gradually decreases, becomes negative in the compressor suction side refrigerant air passage 12a, and falls below the set range. Therefore, this is detected by the pressure sensor 62 and the electromagnetic valve 58 is opened by the controller 64. As a result, the refrigerant air sealed in the expansion tank 51 is supplied to the compressor suction side refrigerant air path 12a via the compressor suction side connection (replenishment) path 52, and the refrigerant air pressure in the compressor suction side refrigerant air path 12a is reduced. Return to the setting range.

 また、冷凍装置の周囲温度の上昇等に起因して、圧縮機吸入側冷媒空気路12aの冷媒空気圧が上昇すると、運転開始不能となる場合がある。そこで、冷媒空気圧が設定範囲を上回った時、圧力センサ62でこれを検出し、コントローラ64で電磁弁60を開放する。これによって、圧縮機吐出側冷媒空気路12bの冷媒空気を圧縮機吐出側接続(回収)路54を介して膨張タンク51に戻し、圧縮機吸入側冷媒空気路12aの冷媒空気圧を設定範囲に戻す。 Also, if the refrigerant air pressure in the compressor suction side refrigerant air passage 12a rises due to an increase in the ambient temperature of the refrigeration system, the operation may not be started. Therefore, when the refrigerant air pressure exceeds the set range, this is detected by the pressure sensor 62 and the electromagnetic valve 60 is opened by the controller 64. As a result, the refrigerant air in the compressor discharge side refrigerant air passage 12b is returned to the expansion tank 51 via the compressor discharge side connection (collection) passage 54, and the refrigerant air pressure in the compressor suction side refrigerant air passage 12a is returned to the set range. .

 本実施形態によれば、閉鎖型空気冷媒式冷凍装置10Aの圧縮機吸入側冷媒空気路12aの冷媒空気圧を設定範囲に調整可能になるので、開放型空気冷媒式冷凍装置への切り替え使用が可能になる。そのため、1基の空気冷媒式冷凍装置で閉鎖型と開放型空気冷媒式冷凍装置との兼用が可能になり、しかも膨張タンク51を高圧ガス保安法適用外圧力である0.2MPa(ゲージ圧)未満に保持することができるので低コストとなる。 According to the present embodiment, the refrigerant air pressure of the compressor suction side refrigerant air passage 12a of the closed-type air refrigerant refrigeration apparatus 10A can be adjusted within a set range, so that switching to an open-type air refrigerant refrigeration apparatus is possible. become. Therefore, one air refrigerant type refrigeration device can be used as both a closed type and an open type air refrigerant type refrigeration device, and the expansion tank 51 is 0.2 MPa (gauge pressure), which is a pressure not applied to the high-pressure gas safety method. Since it can hold below, it becomes low-cost.

 また、密閉系冷媒空気給排装置50と圧縮機吸入側冷媒空気路12aとの間で冷媒空気の給排を行なうので、冷媒空気の損耗がなくなると共に、外部空気が冷媒ガスに混入しない。冷媒ガス中に外部空気の湿分の混入がないため、常に冷媒ガスの露天温度以上で運転できる。そのため、除湿機を必要としない。さらに、冷媒空気を外部に放出しないので、冷媒空気が損耗しない。 Further, since the refrigerant air is supplied and discharged between the closed-system refrigerant air supply / discharge device 50 and the compressor suction-side refrigerant air passage 12a, the refrigerant air is not worn and the external air is not mixed into the refrigerant gas. Since there is no moisture in the external air in the refrigerant gas, it can always be operated above the outdoor temperature of the refrigerant gas. Therefore, no dehumidifier is required. Furthermore, since the refrigerant air is not released to the outside, the refrigerant air is not worn.

 また、冷媒空気を膨張タンク51から低圧の圧縮機吸入側冷媒空気路12aに供給し、圧縮機吐出側冷媒ガス路12bの冷媒空気を圧縮機吐出側冷媒空気路12bより圧縮機吐出側接続(回収)路54を介して低圧の膨張タンク51に排出するようにしているので、これら冷媒空気路からの冷媒空気の給排をスムーズに行なうことができる。
 また、圧力センサ62で圧縮機吸入側冷媒空気路12aの冷媒空気圧を検出し、この圧力検出値が設定範囲となるように、コントローラ64で電磁弁58及び60を開閉するので、圧縮機吸入側冷媒空気路12aの冷媒空気圧を精度良く設定範囲に維持できる。
Further, the refrigerant air is supplied from the expansion tank 51 to the low-pressure compressor suction-side refrigerant air passage 12a, and the refrigerant air in the compressor discharge-side refrigerant gas passage 12b is connected to the compressor discharge-side connection from the compressor discharge-side refrigerant air passage 12b ( Since the refrigerant is discharged to the low-pressure expansion tank 51 via the recovery) passage 54, the refrigerant air can be smoothly supplied and discharged from these refrigerant air passages.
Further, the refrigerant air pressure in the compressor suction side refrigerant air passage 12a is detected by the pressure sensor 62, and the electromagnetic valves 58 and 60 are opened and closed by the controller 64 so that the detected pressure value falls within the set range. The refrigerant air pressure in the refrigerant air passage 12a can be accurately maintained within the set range.

 なお、本実施形態では、冷媒ガスとして、空気を用いているが、空気の代わりに窒素ガスを用いるようにしてもよい。この場合、膨張タンク51には窒素ガスを封入するようにする。
 また、コントローラ64で流量調整弁34の開度を制御し、冷却水循環路28を流れる冷却水の流量を調整し、これによって、水冷式熱交換器16の冷却能力を調整するようにしてもよい。
In this embodiment, air is used as the refrigerant gas, but nitrogen gas may be used instead of air. In this case, nitrogen gas is sealed in the expansion tank 51.
Further, the controller 64 controls the opening degree of the flow rate adjusting valve 34 to adjust the flow rate of the cooling water flowing through the cooling water circulation path 28, thereby adjusting the cooling capacity of the water-cooled heat exchanger 16. .

 (実施形態2)
 次に、本発明を空気冷媒式冷凍装置に適用した第2実施形態を図2に基づいて説明する。本実施形態の閉鎖型空気冷媒式冷凍装置10Bでは、密閉系冷媒空気給排装置70を構成する膨張タンク72の内部に、伸縮可能な中空密閉膜の内部にガスgを封入した中空伸縮体74を内蔵している。該密閉膜は例えばゴム製でもよく、中空伸縮体74の内部に封入されるガスgは、空気又は窒素ガスを用いることができる。
(Embodiment 2)
Next, a second embodiment in which the present invention is applied to an air refrigerant refrigeration apparatus will be described with reference to FIG. In the closed-type air refrigerant refrigeration apparatus 10B of the present embodiment, a hollow elastic body 74 in which a gas g is enclosed in an expansion / contraction hollow sealed membrane inside an expansion tank 72 constituting the closed-system refrigerant air supply / exhaust device 70. Built in. The sealing film may be made of, for example, rubber, and air or nitrogen gas can be used as the gas g enclosed in the hollow stretchable body 74.

 また、本実施形態の密閉系冷媒空気給排装置70では、前記第1実施形態の減圧弁56及び電磁弁58を吸入側接続路52から取り去り、コントローラ64は、圧力センサ62の検出信号を入力し、該検出信号に応じて電磁弁60を開閉するものである。その他の構成は第1実施形態と同一である。 Further, in the closed system refrigerant air supply / exhaust device 70 of the present embodiment, the pressure reducing valve 56 and the electromagnetic valve 58 of the first embodiment are removed from the suction side connection path 52, and the controller 64 inputs a detection signal of the pressure sensor 62. The electromagnetic valve 60 is opened and closed according to the detection signal. Other configurations are the same as those of the first embodiment.

 本実施形態では、圧縮機吸入側冷媒空気路12aの冷媒空気が低下すれば、中空密閉膜72が自動的に膨張し、圧縮機吸入側接続(補給)路52を介して圧縮機吸入側冷媒空気路12aに冷媒空気を供給する。逆に、圧縮機吸入側冷媒空気路12aの冷媒空気圧が上昇すれば、伸縮中空体74の周囲の冷媒空気が伸縮中空体74を外部から圧迫するので、伸縮中空体74が自動的に収縮し、圧縮機吸入側冷媒空気路12aから冷媒空気を回収する。 In the present embodiment, when the refrigerant air in the compressor suction side refrigerant air passage 12a decreases, the hollow sealed membrane 72 automatically expands, and the compressor suction side refrigerant passes through the compressor suction side connection (replenishment) passage 52. Refrigerant air is supplied to the air passage 12a. Conversely, if the refrigerant air pressure in the compressor suction side refrigerant air passage 12a rises, the refrigerant air around the telescopic hollow body 74 presses the telescopic hollow body 74 from the outside, so the telescopic hollow body 74 automatically contracts. Then, the refrigerant air is recovered from the compressor suction side refrigerant air passage 12a.

 なお、中空伸縮体74の伸縮によっても、圧縮機吸入側冷媒空気路12aの冷媒空気圧が設定範囲を上回る場合、コントローラ64によって電磁弁60を開放し、圧縮機吐出側接続(回収)路54より中空伸縮体74に回収し、圧縮機吸入側冷媒空気路12aの冷媒空気圧を設定範囲に戻すようにする。 When the refrigerant air pressure in the compressor suction side refrigerant air passage 12 a exceeds the set range even by the expansion and contraction of the hollow elastic body 74, the electromagnetic valve 60 is opened by the controller 64 and the compressor discharge side connection (collection) passage 54 is connected. It collect | recovers to the hollow expansion-contraction body 74, and returns the refrigerant | coolant air pressure of the compressor suction side refrigerant | coolant air path 12a to a setting range.

 かかる構成によれば、第1実施形態と同様に、圧縮機吸入側冷媒空気路12aの冷媒空気圧の調整が可能になることに加えて、圧縮機吸入側冷媒空気路12aに減圧弁や開閉弁を設ける必要がなくなる。そのため、これら弁の操作等のための複雑な制御を必要としないので、密閉系冷媒空気給排装置70を低コストにできる利点がある。また、中空伸縮体74のガス圧を膨張タンク72の大きさに応じて予め決めておくことにより、圧縮機吸入側冷媒空気路12aの冷媒空気圧を自動的に設定できる。 According to such a configuration, as in the first embodiment, in addition to being able to adjust the refrigerant air pressure of the compressor suction side refrigerant air passage 12a, a pressure reducing valve and an on-off valve are provided in the compressor suction side refrigerant air passage 12a. Need not be provided. Therefore, since complicated control for operation of these valves is not required, there is an advantage that the closed-system refrigerant air supply / exhaust device 70 can be reduced in cost. Further, by predetermining the gas pressure of the hollow stretchable body 74 according to the size of the expansion tank 72, the refrigerant air pressure of the compressor suction side refrigerant air passage 12a can be automatically set.

 本発明によれば、膨張タンクの冷媒ガス圧を圧縮機吸入側冷媒ガス路の冷媒ガス圧より高圧で且つ圧縮機吐出側冷媒ガス路の冷媒ガス圧より低圧の0.2MPa(ゲージ圧)未満に保持することにより、圧縮機吸入側冷媒ガス路の冷媒ガス圧を調整可能で、低コストな閉鎖型ガス循環式冷凍装置を実現できる。 According to the present invention, the refrigerant gas pressure in the expansion tank is less than 0.2 MPa (gauge pressure), which is higher than the refrigerant gas pressure in the compressor suction side refrigerant gas path and lower than the refrigerant gas pressure in the compressor discharge side refrigerant gas path. By holding the refrigerant gas in the low-cost closed-type gas circulation refrigeration apparatus, the refrigerant gas pressure in the compressor suction-side refrigerant gas passage can be adjusted.

Claims (4)

 駆動装置の単一出力軸に連結された圧縮機及び膨張機と、圧縮機吐出側冷媒ガスを冷却する冷却器と、空気または窒素ガスからなる冷媒ガスで冷却対象物を冷却するブラインを冷却するブライン冷却器と、前記冷却器で冷却された冷媒ガスをブライン冷却器からの戻り冷媒ガスでさらに冷却する冷熱回収熱交換器とを備えた閉鎖型ガス循環式冷凍装置において、
 大気圧以上の圧力を有し且つ高圧ガス保安法適用外圧力である0.2MPa(ゲージ圧)未満の冷媒ガスが封入された膨張タンク、該膨張タンクと圧縮機吸入側冷媒ガス路とを接続する圧縮機吸入側接続路、及び膨張タンクと圧縮機吐出側冷媒ガス路とを接続する圧縮機吐出側接続路からなる密閉系冷媒ガス給排装置と、圧縮機吸入側冷媒ガス路を流れる冷媒ガスの圧力を検出する圧力センサと、を備え、
 前記圧力センサで圧縮機吸入側冷媒ガス路の冷媒ガス圧を検出しながら、前記膨張タンクから圧縮機吸入側接続路を介して圧縮機吸入側冷媒ガス路への冷媒ガスの供給と、圧縮機吐出側冷媒ガス路から圧縮機吐出側接続路を介して膨張タンクへの冷媒ガスの排出とを行い、圧縮機吸入側冷媒ガス路の冷媒ガス圧を設定範囲に保持するように構成したことを特徴とする閉鎖型ガス循環式冷凍装置。
The compressor and the expander connected to the single output shaft of the driving device, the cooler for cooling the compressor discharge side refrigerant gas, and the brine for cooling the cooling object with the refrigerant gas composed of air or nitrogen gas are cooled. In a closed gas circulation refrigeration apparatus comprising a brine cooler and a cold recovery heat exchanger that further cools the refrigerant gas cooled by the cooler with a return refrigerant gas from the brine cooler,
An expansion tank filled with a refrigerant gas having a pressure higher than atmospheric pressure and less than 0.2 MPa (gauge pressure) that is not applicable to the High Pressure Gas Safety Law, and the expansion tank and the compressor suction side refrigerant gas passage are connected A closed-system refrigerant gas supply / discharge device comprising a compressor suction-side connection path, a compressor discharge-side connection path connecting the expansion tank and the compressor discharge-side refrigerant gas path, and a refrigerant flowing through the compressor suction-side refrigerant gas path A pressure sensor for detecting the pressure of the gas,
Supply of refrigerant gas from the expansion tank to the compressor suction side refrigerant gas path via the compressor suction side connection path, while detecting the refrigerant gas pressure of the compressor suction side refrigerant gas path with the pressure sensor; The refrigerant gas is discharged from the discharge side refrigerant gas path to the expansion tank via the compressor discharge side connection path, and the refrigerant gas pressure of the compressor suction side refrigerant gas path is maintained within a set range. A closed-type gas circulation refrigeration device.
 前記圧縮機吸入側接続路に設けられた第1開閉弁と、前記圧縮機吐出側接続路に設けられた第2開閉弁と、前記圧力センサの検出信号を入力し、第1開閉弁及び第2開閉弁を操作して圧縮機吸入側冷媒ガス路の冷媒ガス圧を設定範囲に保持するコントローラと、を備えていることを特徴とする請求項1に記載の閉鎖型ガス循環式冷凍装置。 The first on-off valve provided in the compressor suction side connection path, the second on-off valve provided in the compressor discharge side connection path, and the detection signal of the pressure sensor are input, and the first on-off valve and the first on-off valve 2. A closed-type gas circulation refrigeration apparatus according to claim 1, further comprising: a controller that operates the two on-off valves to maintain the refrigerant gas pressure in the compressor suction side refrigerant gas passage within a set range.  前記膨張タンクが、伸縮可能な中空密閉膜の内部にガスを封入してなる中空伸縮体を内蔵し、圧縮機吸入側冷媒ガス路の冷媒ガス圧に応じて該中空伸縮体を伸縮させ、圧縮機吸入側冷媒ガス路の冷媒ガス圧を設定範囲に保持するように構成したことを特徴とする請求項1に記載の閉鎖型ガス循環式冷凍装置。 The expansion tank incorporates a hollow stretchable body in which gas is sealed inside a stretchable hollow hermetic membrane, and the hollow stretchable body is stretched and compressed according to the refrigerant gas pressure in the refrigerant gas passage on the compressor suction side. 2. The closed-type gas circulation type refrigeration apparatus according to claim 1, wherein the refrigerant gas pressure of the machine suction side refrigerant gas passage is held within a set range.  請求項1に記載の閉鎖型ガス循環式冷凍装置の運転方法において、
 前記圧力センサで圧縮機吸入側冷媒ガス路の冷媒ガス圧を検出するステップと、
 該冷媒ガス圧が設定範囲を下回った時、前記膨張タンクから圧縮機吸入側接続路を介して圧縮機吸入側冷媒ガス路に冷媒ガスを供給し、該冷媒ガス圧を設定範囲に戻すステップと、
 該冷媒ガス圧が設定範囲を上回った時、圧縮機吐出側冷媒ガス路から圧縮機吐出側接続路を介して膨張タンクに冷媒ガスを排出し、圧縮機吸入側冷媒ガス路の冷媒ガス圧を設定範囲に戻すステップと、からなることを特徴とする閉鎖型ガス循環式冷凍装置の運転方法。
In the operation method of the closed-type gas circulation type refrigeration apparatus according to claim 1,
Detecting the refrigerant gas pressure in the compressor suction side refrigerant gas path with the pressure sensor;
When the refrigerant gas pressure falls below a set range, supplying refrigerant gas from the expansion tank to the compressor suction side refrigerant gas path via the compressor suction side connection path, and returning the refrigerant gas pressure to the set range; ,
When the refrigerant gas pressure exceeds the set range, the refrigerant gas is discharged from the compressor discharge side refrigerant gas passage to the expansion tank via the compressor discharge side connection passage, and the refrigerant gas pressure in the compressor suction side refrigerant gas passage is reduced. And a step of returning to a set range.
PCT/JP2012/071259 2011-08-26 2012-08-23 Closed- and gas circulation-type freezing apparatus and operation method thereof Ceased WO2013031618A1 (en)

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