WO2003001127A1 - Cold storage type freezing machine - Google Patents
Cold storage type freezing machine Download PDFInfo
- Publication number
- WO2003001127A1 WO2003001127A1 PCT/JP2002/006192 JP0206192W WO03001127A1 WO 2003001127 A1 WO2003001127 A1 WO 2003001127A1 JP 0206192 W JP0206192 W JP 0206192W WO 03001127 A1 WO03001127 A1 WO 03001127A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- temperature end
- refrigerator
- low
- pulse tube
- cooled
- Prior art date
Links
- 238000007710 freezing Methods 0.000 title abstract description 5
- 230000008014 freezing Effects 0.000 title abstract description 5
- 230000006835 compression Effects 0.000 claims abstract description 14
- 238000007906 compression Methods 0.000 claims abstract description 14
- 230000001172 regenerating effect Effects 0.000 claims description 27
- 238000005057 refrigeration Methods 0.000 claims description 10
- 238000001816 cooling Methods 0.000 abstract description 29
- 238000010438 heat treatment Methods 0.000 abstract description 11
- 239000004065 semiconductor Substances 0.000 abstract description 5
- 239000007789 gas Substances 0.000 description 48
- 238000010586 diagram Methods 0.000 description 14
- 238000011069 regeneration method Methods 0.000 description 10
- 230000008929 regeneration Effects 0.000 description 9
- 238000000034 method Methods 0.000 description 7
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 5
- 229910052802 copper Inorganic materials 0.000 description 5
- 239000010949 copper Substances 0.000 description 5
- 230000007704 transition Effects 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 4
- 239000003507 refrigerant Substances 0.000 description 4
- 230000033001 locomotion Effects 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 229910001220 stainless steel Inorganic materials 0.000 description 3
- 239000010935 stainless steel Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 230000002411 adverse Effects 0.000 description 2
- 235000020965 cold beverage Nutrition 0.000 description 2
- 229910001873 dinitrogen Inorganic materials 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000001307 helium Substances 0.000 description 2
- 229910052734 helium Inorganic materials 0.000 description 2
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 241001634822 Biston Species 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- FFGPTBGBLSHEPO-UHFFFAOYSA-N carbamazepine Chemical compound C1=CC2=CC=CC=C2N(C(=O)N)C2=CC=CC=C21 FFGPTBGBLSHEPO-UHFFFAOYSA-N 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 239000011232 storage material Substances 0.000 description 1
- 230000001360 synchronised effect Effects 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D20/00—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B9/00—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point
- F25B9/14—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the cycle used, e.g. Stirling cycle
- F25B9/145—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the cycle used, e.g. Stirling cycle pulse-tube cycle
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B9/00—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point
- F25B9/14—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the cycle used, e.g. Stirling cycle
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2309/00—Gas cycle refrigeration machines
- F25B2309/002—Gas cycle refrigeration machines with parallel working cold producing expansion devices in one circuit
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2309/00—Gas cycle refrigeration machines
- F25B2309/14—Compression machines, plants or systems characterised by the cycle used
- F25B2309/1408—Pulse-tube cycles with pulse tube having U-turn or L-turn type geometrical arrangements
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2309/00—Gas cycle refrigeration machines
- F25B2309/14—Compression machines, plants or systems characterised by the cycle used
- F25B2309/1412—Pulse-tube cycles characterised by heat exchanger details
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2309/00—Gas cycle refrigeration machines
- F25B2309/14—Compression machines, plants or systems characterised by the cycle used
- F25B2309/1418—Pulse-tube cycles with valves in gas supply and return lines
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2309/00—Gas cycle refrigeration machines
- F25B2309/14—Compression machines, plants or systems characterised by the cycle used
- F25B2309/1424—Pulse tubes with basic schematic including an orifice and a reservoir
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25D—REFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
- F25D19/00—Arrangement or mounting of refrigeration units with respect to devices or objects to be refrigerated, e.g. infrared detectors
- F25D19/006—Thermal coupling structure or interface
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/14—Thermal energy storage
Definitions
- the present invention relates to a regenerative refrigerator for a GM refrigerator, a pulse tube refrigerator, and the like, and more particularly, to a regenerative refrigerator capable of efficiently performing cooling and heating / regeneration of an object to be cooled. Things. Background art
- the pulse tube refrigerator has a simple structure with no moving parts in the low-temperature section, as shown in Fig. 2 described below, so that there is almost no vibration in the cold section and even during long-time operation. , High reliability. Furthermore, maintenance-free operation can be expected when operating the refrigerator, and it plays an important role as a type of sensor and cooling means for semiconductor devices.
- FIG. 1 is a schematic diagram illustrating the basic configuration and operating principle of a GM refrigerator.
- the expansion / compression unit 1 is provided with a displacer lc as an expansion biston. During operation, the displacer lc is configured to reciprocate by a stepping motor.
- the room temperature end la is located at the upper end of the expansion / compression section 1, and the cold end lb is located at the opposite lower end.
- the cold storage unit 2 is configured as a cylindrical tube having a room temperature end 2a at the upper end and a low temperature end 2b at the lower end, and a cold storage material such as a stainless steel mesh is laminated inside. Is filled. Further, between the low-temperature end lb of the expansion and compression section 1 and the low-temperature end 2b of the cold storage section 2, a connecting pipe 3 for connecting them is provided.
- the pressure control means 4 comprises a compressor 4a and a high-pressure switching valve 4b and a low-pressure switching valve 4c.
- the high-pressure switching valve 4b and the low-pressure switching valve 4c are synchronized with the movement of the display lc.
- the high-pressure switching valve 4b is opened, and high-pressure working gas enters the upper space of the displacer lc.
- the displacer lc rises to the room temperature end la, the high-pressure gas in the upper space moves to the lower space while being cooled through the regenerator 2.
- the gas contracts, and high-pressure working gas is supplied from the high-pressure switching valve 4b.
- the high-pressure switching valve 4b is closed and the low-pressure switching valve 4c is opened to discharge the high-pressure gas in the low-temperature space.
- the gas is adiabatically expanded, and cooling is obtained in the space below the cold end lb.
- the displacer lc descends to the lower end while the low-pressure switching valve 4c is open, the low-temperature gas in the low-temperature space absorbs the refrigeration load, moves to the upper space while being heated through the regenerator 2, and the remaining gas remains. The gas returns to the pressure control means 4 and is sucked.
- the high pressure switching valve 4b opens to allow the high pressure working gas to enter the headspace of the displacer lc.
- the cold obtained at the low-temperature end lb of the expansion / compression unit 1 passes through the cold head (cooling unit) 6 that covers the low-temperature end 2b of the regenerator 2 and the low-temperature end lb of the expansion / compression unit 1. Heat is transferred to the cooling object 7.
- the GM refrigerator since the GM refrigerator has a structure in which reciprocating motion is performed by the stepping motor, vibration is easily generated in the expansion / compression unit 1, and the vibration is transmitted to the object 7 to be cooled using the cold head 6 as a medium. Sometimes.
- FIG. 2 is a schematic diagram illustrating the basic configuration and operating principle of a pulse tube refrigerator.
- the working gas is replaced by the phase difference by removing the displacer of the GM refrigerator and providing a single tube. I am trying to do it. For this reason, the number of parts of the refrigeration system is small and the structure is simple.
- the pulse tube refrigerator has a pulse tube 1 with a room temperature end la at the upper end and a cold end lb at the lower end, and similarly, a room temperature end 2a at the upper end and a cold end at the lower end.
- the regenerator 2 provided with 2b is configured as a cylindrical tube, and the interior thereof is filled with a regenerator material such as a stainless steel mesh.
- the pressure control means 4 which communicates with the room temperature end 2a of the regenerator 2 and vibrates the pressure of the working gas, includes a compressor 4a and a high-pressure switching valve 4b and a low-pressure switching valve 4c.
- the phase control means 5 which communicates with the room temperature end la of the pulse tube 1 and adjusts the phase difference between the pressure fluctuation and the position fluctuation of the working gas in the refrigerator system is usually provided with a buffer tank. During operation of the refrigerator, the working gas in the machine and the working gas in the buffer tank flow back and forth, but due to a constant flow resistance, a phase difference occurs between the pressure fluctuation and the position fluctuation of the working gas. By controlling, the working gas is adiabatically expanded near the low temperature end lb of the pulse tube 1 to generate cold.
- the low temperature end 2b of the regenerator 2 and the low temperature end lb of the pulse tube 1 are connected by a connecting tube 3.
- Cold generated near the low-temperature end lb of the pulse tube 1 is, as in the case of the GM refrigerator, cold head 6 covering the low-temperature end 2b of the regenerator 2 and the low-temperature end lb of the pulse tube 1.
- the heat is transferred to the object to be cooled 7 via the.
- conventional GM refrigerators and pulse tube refrigerators use a structure in which a cold head that covers the cold generation part is provided, and the cold head is brought into contact with the object to be cooled to transfer the cold. It is. For this reason, a cold head integrally formed of copper with high thermal conductivity is used to increase the efficiency of heat transfer. Disclosure of the invention
- Cold storage using a cryopump Trap processing, cold processing of gas liquefaction equipment, and cryogenic freezing of superconducting elements and sensors For example, in a process using a cryopump, it is possible to reach a high vacuum while achieving a cold trap by adsorbing gas molecules on an adsorption panel attached to a cold head of a refrigerator. For this purpose, it is necessary to efficiently transfer the cold generated by the refrigerator to a predetermined cooling target site, with a small loss. On the other hand, in the cryopump process described above, if a certain amount or more of gas molecules are adsorbed on the adsorption panel and the gas molecule layer becomes thicker, the performance deteriorates. Need to be released.
- the vibration generated by the refrigerator is transmitted to the object to be cooled via the cold head, and cooling the sensors affects the instrument accuracy.
- a position shift occurs in a gap 18 during processing or transportation.
- the present invention has been made in view of such circumstances, and has a regenerative refrigerating system.
- cooling and heating and regeneration of the object to be cooled can be accelerated, efficient heat transfer can be achieved, and even when a GM refrigerator is used, vibration generated by the refrigerator is affected.
- the purpose is to provide a regenerative refrigerator that does not transmit to the cooling target.
- the present inventors have conducted various studies to solve the above-described problems, and as a result, in heat utilization in a regenerative refrigerator, heat transfer is performed by extending a flow path of a working gas to a target to be cooled. By doing so, it was found that cooling or heating regeneration could be accelerated and heat transfer efficiency could be improved.
- the heat transfer from the cold generating part of the refrigerator to the object to be cooled is replaced by solid-state heat transfer using a cold head, and the flow path for the low-temperature working gas to the object to be cooled or its vicinity. It is intended to efficiently transfer heat energy by directly flowing the working gas.
- the present invention has been completed on the basis of the above findings, and includes a regenerative refrigerator of the following (1) and a pulse tube refrigerator of the regenerative refrigerator of (2).
- a pressure control means comprising a compressor, a high pressure switching valve and a low pressure switching valve, an expansion / compression section having a room temperature end and a low temperature end at both ends, and a cold storage having a room temperature end and a low temperature end at both ends.
- a regenerative refrigerator having a heat transfer portion that transfers heat to the object to be cooled, the low temperature end of the expansion / compression portion being connected to the low temperature end of the cool storage portion, and the operation extending to the object to be cooled.
- a regenerative refrigerator equipped with a gas flow path.
- the object to be cooled includes an object to be cooled, a space to be cooled, and the like, as shown in FIGS. 3 and 4 described later.
- FIG. 1 is a schematic diagram illustrating the basic configuration and operating principle of a GM refrigerator.
- FIG. 2 is a schematic diagram illustrating the basic configuration and operating principle of a pulse tube refrigerator.
- FIG. 3 is a diagram showing a configuration example of a pulse tube refrigerator for a cooled object in the regenerative refrigerator of the present invention.
- FIG. 4 is a diagram showing a configuration example of a pulse tube refrigerator intended for a cooled space in the regenerative refrigerator of the present invention, and further, a schematic configuration of a cold trap process employed in the present invention example of the embodiment.
- FIG. 4 is a diagram showing a configuration example of a pulse tube refrigerator intended for a cooled space in the regenerative refrigerator of the present invention, and further, a schematic configuration of a cold trap process employed in the present invention example of the embodiment.
- Fig. 5 is a diagram showing the schematic configuration of the cold trap process adopted in the comparative example.
- Fig. 6 is a diagram comparing transitions of cooling temperature and time during cooling of a pipe type refrigerator and a panel type refrigerator.
- Fig. 7 is a diagram comparing the transition of heating temperature and time during regeneration with heating of a pipe-type refrigerator and a panel-type refrigerator.
- the regenerative refrigerator of the present invention is characterized in that the low-temperature end of the expansion / compression unit and the low-temperature end of the regenerative unit are connected, and a flow path of the working gas extending to the object to be cooled is provided.
- This allows the cold generated by the refrigerator to flow directly to the object to be cooled, instead of the conventional heat transfer using a cold head integrally formed of copper. Transfer Movement becomes possible. That is, the cooling and the temperature-raising regeneration can be performed at a high speed, and as a result, the operation rate of the regenerative refrigerator is improved.
- FIGS. 3 and 4 are diagrams showing a configuration example of a pulse tube refrigerator of the regenerative refrigerator of the present invention.
- FIG. 3 shows a case where the object to be cooled is an object to be cooled
- a pulse tube 1 with a room temperature end la at the upper end and a low temperature end lb at the lower end, a room temperature end 2a at the upper end and a low temperature end 2b at the lower end, and a regenerator material laminated inside
- the pressure control means 4 that oscillates the pressure of the working gas by communicating with the regenerator 2, the room temperature end 2 a of the regenerator 2, and the working gas in the refrigerator system by communicating with the room temperature end la of the pulse tube 1.
- the phase control means 5 for adjusting the phase difference between the pressure fluctuation and the position fluctuation is the same as a conventional pulse tube refrigerator.
- a low-temperature end lb of the pulse tube 1 is connected to the low-temperature end 2b of the regenerator 2 and a pipe 8 is provided as a flow path of a working gas extending to the object 7 to be cooled. ing.
- the working gas flow pipe 8 extended to the object to be cooled 7 as described above the working gas having cold flows directly to the object to be cooled and is transmitted to the object to be cooled 7, so that cooling is performed. Can be speeded up.
- FIGS. 3 and 4 the configuration example of the pulse tube refrigerator among the regenerative refrigerators is shown, but the present invention can be applied to a Suzuichi ring refrigerator or a GM refrigerator.
- a Stirling refrigerator or a GM refrigerator is applied, there is an advantage that vibrations generated in the refrigerator are not easily transmitted to the object to be cooled.
- the flow path of the working gas used in the present invention is not limited to a pipe having a tubular shape, but a circular, oval, rectangular, or other cross-sectional shape capable of flowing the working gas. Should be fine.
- comb-shaped or radial fins may be provided on the inner and outer surfaces of the pipe. Aluminum, copper, stainless steel, etc. can be used as the material of the pipes, fins, and the like. If the piping is exposed to the atmosphere, it is necessary to cover the relevant location with a heat insulating material.
- helium gas or nitrogen gas which is usually used for regenerative refrigerators can be used.
- the regenerative refrigerator of the present invention it is desirable to employ a pulse tube refrigerator.
- the structure of the device is simple and maintenance-free. Also, since no micro-vibration occurs, it does not adversely affect a class of sensors or semiconductor manufacturing equipment.
- a cold trap process was performed.
- a pulse tube refrigerator using a pipe hereinafter, referred to as a “cryo coil” in a flow path of a working gas
- a cold head type pulse tube refrigerator is used to cool and ascend.
- the transition of cooling time and heating time during thermal regeneration was compared. Assuming a vacuum pump that collects moisture during vacuum evacuation and enhances evacuation performance, the cooling area for adsorbing moisture is the same for both.
- FIG. 4 is a diagram showing a schematic configuration of the cold trap processing employed in the example of the present invention.
- the refrigerator used was a pulse tube with an inner diameter of 50 mm and a length of 300 mm, a regenerator with an inner diameter of 56.6 mm and a length of 100 mm.An active buffer was installed as a phase control device. Gas was supplied and exhausted. Helium gas was used as a refrigerant gas. below In the embodiment, the pulse tube refrigerator used as an example of the present invention is referred to as a “pipe type refrigerator”.
- FIG. 5 is a diagram showing a schematic configuration of a cold trap process employed in the comparative example.
- the refrigerator used had a pulse tube inner diameter of 38 mm, a length of 200 mm, a regenerator inner diameter of 54.8 mm and a length of 93 mm, and an active buffer was installed as a phase control device. Nitrogen gas was used as the refrigerant gas, and supply and exhaust of the refrigerant gas were performed by opening and closing the compressor and the valve.
- a pulse tube refrigerator used as a comparative example is referred to as a “panel refrigerator”. In this panel-type refrigerator, as shown in Fig.
- heat is transferred to the object to be cooled 7 (vacuum container) by a cold drink 9 consisting of a heat transfer block made of copper and a cold panel 10 serving as a cooling surface. It is composed of Furthermore, the refrigeration characteristics of the heater are confirmed to have a refrigeration capacity of 130 W at 133 ° C (140), which indicates that the performance is slightly superior to that of the above-mentioned pipe-type refrigerator.
- Fig. 6 is a diagram comparing transitions of cooling temperature and time during cooling of a pipe type refrigerator and a panel type refrigerator.
- the temperature shown in the figure is the surface temperature of the cryocoil for the pipe-type refrigerator and the tip temperature of the cold panel for the panel refrigerator. However, almost no temperature difference occurred at each point of the cryocoil.
- Fig. 7 is a diagram comparing the transition of heating temperature and time during regeneration with heating of a pipe-type refrigerator and a panel-type refrigerator.
- the temperature shown in the figure is the same as in the case of FIG. It takes about 4 minutes to heat from -163 ° C (110 K) to 20 ° C (293 K) in a pipe refrigerator, whereas it rises only about 20 ° C in 4 minutes in a panel refrigerator Stayed at. Although not shown in FIG. 7, it is -163 for the panel refrigerator. It took about 240 minutes to heat from C (110 K) to 20 ° C (293 K).
- the weight of the cryocoil of the pipe-type refrigerator used in this example was 2 kg, and the weight of the cold panel and the cold drink of the panel refrigerator was 3 kg.
- the delay time in cooling and heating of the panel refrigerator is acceptable up to 1.27 times.
- the delay time confirmed in FIGS. 6 and 7 exceeds that, and it can be seen that the effect of the pipe-type refrigerator of the example of the present invention is remarkable.
- the cooling areas of the pipe-type refrigerator and the panel-type refrigerator are equal, but in the pipe-type refrigerator, the cross-sectional area of the heat transfer member is increased to reduce the heat transfer resistance. It is not necessary, and as a result, it is a characteristic of the pipe-type refrigerator of the present invention that it can respond to the panel-type refrigerator at a weight ratio of 2/3.
- the heat transfer resistance is reduced and the weight of the member to be cooled can be reduced by utilizing the flow of the coolant gas for the heat transfer of the object to be cooled.
- heat transfer characteristics can be significantly improved.
- the regenerative refrigerator of the present invention when utilizing the heat, the cooling of the object to be cooled and the temperature rise regeneration can be accelerated, and efficient heat transfer can be achieved. As a result, the operating rate of the refrigerator can be significantly improved. Moreover, when the expansion piston (displacer) that slides during operation in the GM refrigerator among the regenerative refrigerators of the present invention, vibration generated in the refrigerator is not transmitted to the object to be cooled. . For this reason, sensors and semiconductor manufacturing equipment Since it does not adversely affect the application, it can be widely applied to these uses.
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- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Compressors, Vaccum Pumps And Other Relevant Systems (AREA)
- Devices That Are Associated With Refrigeration Equipment (AREA)
Description
Claims
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2003507481A JPWO2003001127A1 (ja) | 2001-06-21 | 2002-06-20 | 蓄冷型冷凍機 |
US10/480,212 US7047749B2 (en) | 2001-06-21 | 2002-06-20 | Regenerative refrigerating apparatus |
EP02743677A EP1408293A4 (en) | 2001-06-21 | 2002-06-20 | COLD STORAGE FACILITY FREEZER |
KR1020037016472A KR100629215B1 (ko) | 2001-06-21 | 2002-06-20 | 축냉형 냉동기 및 펄스관 냉동기 |
HK05100202A HK1067174A1 (en) | 2001-06-21 | 2005-01-11 | Cold storage type freezing machine |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001-188109 | 2001-06-21 | ||
JP2001188109 | 2001-06-21 |
Publications (1)
Publication Number | Publication Date |
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WO2003001127A1 true WO2003001127A1 (en) | 2003-01-03 |
Family
ID=19027279
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP2002/006192 WO2003001127A1 (en) | 2001-06-21 | 2002-06-20 | Cold storage type freezing machine |
Country Status (8)
Country | Link |
---|---|
US (1) | US7047749B2 (ja) |
EP (1) | EP1408293A4 (ja) |
JP (1) | JPWO2003001127A1 (ja) |
KR (1) | KR100629215B1 (ja) |
CN (1) | CN1244786C (ja) |
HK (1) | HK1067174A1 (ja) |
TW (1) | TW550366B (ja) |
WO (1) | WO2003001127A1 (ja) |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7062922B1 (en) * | 2004-01-22 | 2006-06-20 | Raytheon Company | Cryocooler with ambient temperature surge volume |
US7174721B2 (en) * | 2004-03-26 | 2007-02-13 | Mitchell Matthew P | Cooling load enclosed in pulse tube cooler |
WO2006075982A1 (en) * | 2005-01-13 | 2006-07-20 | Sumitomo Heavy Industries, Ltd. | Reduced input power cryogenic refrigerator |
JP2006284061A (ja) * | 2005-03-31 | 2006-10-19 | Sumitomo Heavy Ind Ltd | パルス管冷凍機 |
CN104763873B (zh) * | 2014-01-07 | 2016-08-17 | 同济大学 | 一种低温液体储罐盖子系统及低温液体储罐 |
US9551513B2 (en) * | 2014-06-12 | 2017-01-24 | Raytheon Company | Frequency-matched cryocooler scaling for low-cost, minimal disturbance space cooling |
US10422329B2 (en) | 2017-08-14 | 2019-09-24 | Raytheon Company | Push-pull compressor having ultra-high efficiency for cryocoolers or other systems |
CN115420034A (zh) * | 2022-08-30 | 2022-12-02 | 江苏捷思新能源科技有限公司 | 一种超导磁体极低温制冷机及其控制方法 |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
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JPH01139959A (ja) * | 1987-11-27 | 1989-06-01 | Sumitomo Heavy Ind Ltd | 蓄冷式He冷凍機 |
JPH03236551A (ja) * | 1990-02-14 | 1991-10-22 | Arubatsuku Kuraio Kk | 寒冷輸送方法 |
JPH08313084A (ja) * | 1995-05-19 | 1996-11-29 | Sanyo Electric Co Ltd | 極低温冷凍機の冷却部構造 |
US5927081A (en) | 1997-02-18 | 1999-07-27 | Sumitomo Heavy Industries, Ltd. | Pulse tube refrigerator and its running method |
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US4679401A (en) * | 1985-07-03 | 1987-07-14 | Helix Technology Corporation | Temperature control of cryogenic systems |
JP2707839B2 (ja) | 1990-12-25 | 1998-02-04 | 住友金属工業株式会社 | マルテンサイト系継目無鋼管とその製造方法 |
US5335505A (en) * | 1992-05-25 | 1994-08-09 | Kabushiki Kaisha Toshiba | Pulse tube refrigerator |
JP3566751B2 (ja) * | 1994-06-16 | 2004-09-15 | エア・ウォーター株式会社 | 大型パルスチューブ冷凍機 |
US5519999A (en) * | 1994-08-05 | 1996-05-28 | Trw Inc. | Flow turning cryogenic heat exchanger |
US6332925B1 (en) * | 1996-05-23 | 2001-12-25 | Ebara Corporation | Evacuation system |
DE19704485C2 (de) * | 1997-02-07 | 1998-11-19 | Siemens Ag | Stromzuführungsvorrichtung für eine gekühlte elektrische Einrichtung |
JP2000205960A (ja) * | 1998-12-23 | 2000-07-28 | Csp Cryogenic Spectrometers Gmbh | 検出器装置 |
WO2001001048A1 (de) * | 1999-06-24 | 2001-01-04 | Csp Cryogenic Spectrometers Gmbh | Kühlvorrichtung |
JP3577661B2 (ja) * | 1999-09-29 | 2004-10-13 | 住友重機械工業株式会社 | パルス管冷凍機 |
US6205812B1 (en) * | 1999-12-03 | 2001-03-27 | Praxair Technology, Inc. | Cryogenic ultra cold hybrid liquefier |
-
2002
- 2002-06-20 KR KR1020037016472A patent/KR100629215B1/ko not_active IP Right Cessation
- 2002-06-20 JP JP2003507481A patent/JPWO2003001127A1/ja active Pending
- 2002-06-20 CN CNB028120906A patent/CN1244786C/zh not_active Expired - Fee Related
- 2002-06-20 TW TW091113515A patent/TW550366B/zh not_active IP Right Cessation
- 2002-06-20 WO PCT/JP2002/006192 patent/WO2003001127A1/ja active Application Filing
- 2002-06-20 US US10/480,212 patent/US7047749B2/en not_active Expired - Fee Related
- 2002-06-20 EP EP02743677A patent/EP1408293A4/en not_active Withdrawn
-
2005
- 2005-01-11 HK HK05100202A patent/HK1067174A1/xx not_active IP Right Cessation
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01139959A (ja) * | 1987-11-27 | 1989-06-01 | Sumitomo Heavy Ind Ltd | 蓄冷式He冷凍機 |
JPH03236551A (ja) * | 1990-02-14 | 1991-10-22 | Arubatsuku Kuraio Kk | 寒冷輸送方法 |
JPH08313084A (ja) * | 1995-05-19 | 1996-11-29 | Sanyo Electric Co Ltd | 極低温冷凍機の冷却部構造 |
US5927081A (en) | 1997-02-18 | 1999-07-27 | Sumitomo Heavy Industries, Ltd. | Pulse tube refrigerator and its running method |
Non-Patent Citations (1)
Title |
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See also references of EP1408293A4 * |
Also Published As
Publication number | Publication date |
---|---|
KR20040016886A (ko) | 2004-02-25 |
JPWO2003001127A1 (ja) | 2004-10-14 |
CN1516798A (zh) | 2004-07-28 |
US20040168445A1 (en) | 2004-09-02 |
CN1244786C (zh) | 2006-03-08 |
EP1408293A4 (en) | 2006-06-21 |
HK1067174A1 (en) | 2005-04-01 |
US7047749B2 (en) | 2006-05-23 |
TW550366B (en) | 2003-09-01 |
EP1408293A1 (en) | 2004-04-14 |
KR100629215B1 (ko) | 2006-09-27 |
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