US20170045273A1 - Cryogenic refrigeration system - Google Patents
Cryogenic refrigeration system Download PDFInfo
- Publication number
- US20170045273A1 US20170045273A1 US15/305,911 US201515305911A US2017045273A1 US 20170045273 A1 US20170045273 A1 US 20170045273A1 US 201515305911 A US201515305911 A US 201515305911A US 2017045273 A1 US2017045273 A1 US 2017045273A1
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- Prior art keywords
- refrigerant
- heat exchanger
- refrigeration system
- cryogenic
- disposed
- Prior art date
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- 238000005057 refrigeration Methods 0.000 title claims abstract description 39
- 239000003507 refrigerant Substances 0.000 claims abstract description 115
- 238000001816 cooling Methods 0.000 claims abstract description 34
- 230000017525 heat dissipation Effects 0.000 claims abstract description 28
- 238000010248 power generation Methods 0.000 claims description 24
- 238000006243 chemical reaction Methods 0.000 claims description 21
- 238000007906 compression Methods 0.000 claims description 19
- 230000006835 compression Effects 0.000 claims description 18
- 238000001514 detection method Methods 0.000 claims description 6
- 239000007789 gas Substances 0.000 description 42
- 238000010586 diagram Methods 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 239000002887 superconductor Substances 0.000 description 5
- 230000009977 dual effect Effects 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 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
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 230000020169 heat generation Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 238000005339 levitation Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
Images
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- 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
- F25B25/00—Machines, plants or systems, using a combination of modes of operation covered by two or more of the groups F25B1/00 - F25B23/00
-
- 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
- F25B49/00—Arrangement or mounting of control or safety devices
- F25B49/02—Arrangement or mounting of control or safety devices for compression type machines, plants or systems
-
- 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
- F25B2309/1428—Control of a Stirling refrigeration machine
-
- 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
- F25B2339/00—Details of evaporators; Details of condensers
- F25B2339/04—Details of condensers
- F25B2339/047—Water-cooled condensers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2600/00—Control issues
- F25B2600/25—Control of valves
- F25B2600/2501—Bypass valves
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2700/00—Sensing or detecting of parameters; Sensors therefor
- F25B2700/19—Pressures
- F25B2700/193—Pressures of the compressor
- F25B2700/1933—Suction pressures
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2700/00—Sensing or detecting of parameters; Sensors therefor
- F25B2700/21—Temperatures
- F25B2700/2115—Temperatures of a compressor or the drive means therefor
- F25B2700/21151—Temperatures of a compressor or the drive means therefor at the suction side of the compressor
Definitions
- the present invention disclosed herein relates to a cryogenic refrigeration system, and more particularly, to a cryogenic refrigeration system capable of improving a coefficient of performance thereof.
- a cryogenic refrigerator may be used to cool a superconductor or a small-sized electronic component.
- the cryogenic refrigerator may include a stifling refrigerator, a GM refrigerator, and a Joule-Thomson refrigerator.
- the above-described cryogenic refrigerator may generate refrigeration output through an expansion process of working fluid such as helium or hydrogen. The expansion process may accompany heat generation of a compression process.
- the cryogenic refrigerator may be cooled by a heat dissipater.
- the typical cryogenic refrigerator may be cooled by a dual heat dissipater.
- the dual heat dissipater may include a water-cooling type heat dissipater and a vapor compression refrigerator.
- the water-cooling type radiator may cool the cryogenic refrigerator.
- the water-cooling type heat dissipater may be cooled by the vapor compression refrigerator However, since the water-cooling type heat dissipater uses water that has a low cooling efficiency of performance, a coefficient of performance of the cryogenic refrigerator may be reduced. In addition, the water-cooling type heat dissipater and the vapor compression refrigerator may increase costs for operating the cryogenic refrigerator to reduce productivity.
- the present invention provides a cryogenic refrigeration system capable of increasing a radiant efficiency due to a coefficient of performance of refrigerant.
- the present invention also provides a cryogenic refrigeration system capable of minimizing costs for operating a cryogenic refrigerator.
- Embodiments of the present invention provide a cryogenic refrigeration system including: a cryogenic refrigerator; and a heat dissipation module configured to cool the cryogenic refrigerator.
- the heat dissipation module includes: a condenser spaced apart from the cryogenic refrigerator to condense a refrigerant that cools the cryogenic refrigerator; and a heat exchanger connected to the cryogenic refrigerator to circulate the refrigerant between the cryogenic refrigerator and the condenser, thereby cooling the cryogenic refrigerator.
- cryogenic refrigeration systems include: a cryogenic refrigerator comprising a power generation part, a power conversion part configured to convert power generated in the power generation part, and a gas cooling part configured to cool a gas by using the power converted in the power conversion part; and a heat dissipation module configured to circulate a refrigerant that cools the cryogenic refrigerator into the power generation part, the power conversion part, and the gas cooling part.
- the cryogenic refrigeration system may use refrigerant having a coefficient of performance and/or a heat absorption efficiency greater than that of the water to increase a radiant efficiency of the cryogenic refrigerator.
- the cryogenic refrigerator may be directly cooled by the heat dissipation module to minimize the operational costs.
- FIG. 1 is a diagram illustrating an example of a cryogenic refrigeration system according to the present invention.
- FIG. 2 is a diagram illustrating a cryogenic refrigerator in FIG. 1 .
- FIG. 3 is a diagram illustrating another example of the cryogenic refrigeration system in FIG. 1 .
- FIG. 4 is a diagram illustrating still another example of the cryogenic refrigeration system in FIG. 1 .
- FIG. 1 is a diagram illustrating an example of a cryogenic refrigeration system 10 according to the present invention.
- FIG. 2 is a diagram illustrating a cryogenic refrigerator 100 in FIG. 1 .
- the cryogenic refrigeration system 10 may include the cryogenic refrigerator 100 and a heat dissipation module 200 .
- the cryogenic refrigerator 100 may be cooled to a cryogenic temperature.
- the heat dissipation module 200 may dissipate heat from the cryogenic refrigerator 100 .
- the cryogenic refrigerator 100 may include a sterling cryogenic refrigerator. According to an embodiment, the cryogenic refrigerator 100 may include a power generation part 110 , a power conversion part 120 , and a gas cooling part 130 .
- the power generation part 110 may generate rotational power by external power.
- the power generation part 110 may include a motor.
- the power generation part 110 may be connected to the power conversion part 120 .
- the power generation part 110 may be heated to a temperature greater than a room temperature.
- the power generation part 110 may be heated to a temperature equal to or greater than about 30° C.
- the power conversion part 120 may convert the rotational power to reciprocating linear power.
- the power conversion part 120 may include a shaft 1 cam 125 , a plurality of connecting rods 126 , and a housing 128 .
- the shaft 122 may be connected to the power generation part 110 .
- the cam 124 may be connected between the shaft 122 and the connecting rods 126 .
- the connecting rods 126 may extend to the gas cooling part 130 .
- the housing 128 may surround the cam 124 .
- the housing 128 may be connected to the gas cooling part 130 .
- the housing 121 may be provided in the housing 128 . Oil 121 may be heated by operation of the shaft 122 , the cam 124 , and the connecting rods 126 .
- the gas cooling part 130 may be disposed on the power conversion part 120 .
- the gas cooling part 130 may cool gas 131 at the cryogenic temperature.
- the gas 131 may include helium gas.
- the gas cooling part 130 may include a cylinder 132 , a displacer 140 , and a piston 150 .
- the cylinder 132 may be connected onto the power conversion part 120 .
- the gas 131 may be provided into the cylinder 132 .
- the displacer 140 and the piston 150 may be connected to the connecting rods 126 to move up and down in the cylinder 132 .
- the displacer 140 may be disposed above the pistol 150 .
- One of the connecting rods 126 may pass through the piston 150 .
- the cylinder 132 may include a gas expansion region 134 , a gas compression region 136 , and a piston movement region 138 .
- the gas expansion region 134 may be disposed above the gas compression region 136 .
- the displacer 140 may be connected to one of the connecting rods 126 to move up and down in the gas expansion region 134 and the gas compression region 136 .
- the displacer 140 may expand and cool the gas 131 in the gas expansion region 134 .
- the gas expansion region 134 may be a cooling region.
- the gas compression region 136 may be connected to the rest of the connecting rods 126 and disposed between the gas expansion region 134 and the piston movement region 138 .
- the piston 150 may move up and down in the piston movement region 138 .
- the piston movement region 138 may be a region through which one of the connecting rods 126 passes.
- the displacer 140 and the piston 150 may compress the gas 131 in the gas compression region 136 .
- the compressed gas 131 may heat the cylinder 132 in the gas compression region 136 .
- the gas compression region 136 may be a heating region.
- the heat dissipation module 200 may circulate to supply refrigerant to the power generation part 110 , the power conversion part 120 , and the gas cooling part 130 to directly cool the cryogenic refrigerator 100 .
- the direct cooling method may have a size smaller than that of the typical dual heat dissipater and reduce maintenance costs. Accordingly, the cryogenic refrigeration system 10 according to the present invention may reduce the operational costs.
- the heat dissipation module 200 may include a condenser 210 , a compressor 220 , heat exchangers 230 , a refrigerant expander 240 , a refrigerant supply line 250 , and a refrigerant collecting line 260 .
- the condenser 210 may condense the refrigerant.
- the compressor 220 may be connected to the condenser 210 .
- the condenser 220 may compress the refrigerant.
- the refrigerant may include R22, R123, R134a, HFC-407C, HFC-407A, or R-123yf.
- the refrigerant may have a freezing point and an evaporation point, which are lower than those of water.
- the water may have a coefficient of performance (COP) of about 0.2625.
- the refrigerant of the R22 may have the coefficient of performance greater than that of the water.
- the R22 at a temperature of about ⁇ 30° C. is heat-exchanged to about ⁇ 15° C.
- the R22 may have the coefficient of performance of about 0.323.
- the heat exchangers 230 may be connected to the power generation part 110 , the power conversion part 120 , and the gas cooling part 130 .
- the refrigerant supply line 250 may be connected between the condenser 210 and the heat exchangers 230 .
- a radiant efficiency of the cryogenic refrigerator 100 may be increased.
- the refrigerant expander 240 may be connected to the refrigerant supply line 250 .
- the refrigerant collecting line 260 may be connected between the compressor 220 and the heat exchangers 230 .
- the condenser 210 may liquefy the refrigerant.
- the condenser 210 may include a water-cooling type condenser and an air-cooling type condenser.
- the refrigerant expander 240 may be disposed between the condenser 210 and the heat exchangers 230 .
- the refrigerant expander 240 may vaporize and cool the refrigerant.
- the cooled refrigerant may be supplied to the heat exchangers 230 through the refrigerant supply line 250 ,
- the refrigerant may be heated in the heat exchangers 230 .
- the compressor 220 may supply the heated refrigerant to the condenser 210 with a predetermined pressure.
- the refrigerant in a gas state may be supplied to the condenser 210 .
- the refrigerant may be circulated between the heat exchangers 230 and the condenser 210 .
- the heat exchangers 230 may cool the power generation part 110 , the power conversion part 120 , and the gas cooling part 130 .
- the heat exchangers 230 may include a gas heat exchanger 232 , an oil heat exchanger 234 , and a motor heat exchanger 236 .
- the gas heat exchanger 232 may be disposed in the compression region 136 .
- the gas heat exchanger 232 may cool the cylinder 132 in the compression region 136 .
- the heat exchange supply line 233 may connect the gas heat exchanger 232 to the oil heat exchanger 234 .
- the heat exchange collecting line 235 may connect the gas heat exchanger 232 to the motor heat exchanger 236 .
- the refrigerant may be sequentially supplied to the oil heat exchanger 234 , the gas heat exchanger 232 , and the motor heat exchanger 236 .
- a first protection cover 312 may be disposed to surround the gas heat exchanger 232 .
- the first protection cover 312 may protect the gas heat exchanger 232 .
- the first protection cover 312 may prevent dew formation caused by cooling of the gas heat exchanger 231 .
- the power generation part 234 may be disposed on the power conversion part 120 .
- the oil heat exchanger 234 may cool the oil in the power conversion part 120 .
- the oil heat exchanger 234 may be connected to the refrigerant supply tine 250 .
- a second protection cover 314 may be disposed to surround the heat exchanger 234 .
- the second protection cover 314 may protect the oil heat exchanger 234 .
- the motor heat exchanger 236 may be disposed on the power generation part 110 .
- the motor heat exchanger 236 may cool the power generation part 110 .
- the motor heat exchanger 236 may be connected to the refrigerant collecting line 260 .
- FIG. 3 is a diagram illustrating another example of the cryogenic refrigeration system 10 in FIG. 1 .
- the heat dissipation module 200 may include a first pressure transducer 272 , a first temperature sensor 274 , and a circulation flow rate controller 276 .
- the first pressure transducer 272 may be disposed in the refrigerant collecting line 260 between the heat exchangers 230 and the compressor 220 .
- the first pressure transducer 272 may detect a pressure of the refrigerant.
- the first temperature sensor 274 may be disposed in the refrigerant collecting line 260 disposed adjacent to the first pressure transducer 272 .
- the first temperature sensor 274 may detect a temperature of the refrigerant.
- the circulation flow rate controller 276 may be connected to the first pressure transducer 272 , the first temperature sensor 274 , and the refrigerant expander 240 . Also, the circulation flow rate controller 276 may receive a detection signal of the temperature and the pressure of the first pressure transducer 272 and the first temperature sensor 274 . The circulation flow rate of the refrigerant may be controlled on the basis of the temperature and the pressure. The refrigerant expander 240 may control the circulation flow rate of the refrigerant according to the control signal of the circulation flow rate controller 276 .
- the cryogenic refrigerator 100 and the condenser 210 , the compressor 220 , the heat exchangers 230 , the refrigerant expander 240 , the refrigerant supply line 250 , and the refrigerant collecting line 260 of the heat dissipation module 200 may be the same as those in FIGS. 1 and 2 .
- FIG. 4 is a diagram illustrating still another example of the cryogenic refrigeration system 10 in FIG. 1 .
- the heat dissipation module 200 may include a second temper sensor 282 , a second pressure transducer 284 , a bypass valve 286 , a bypass controller 288 , a bypass line 290 , and a sensitive heat tube 292 .
- the second temperature sensor 282 may be disposed in the refrigerant collecting line 260 .
- the second temperature sensor 282 may detect the temperature of the refrigerant.
- the second pressure transducer 284 may be disposed in the refrigerant collecting line 260 .
- the second pressure transducer 284 may detect the pressure of the refrigerant.
- the bypass valve 286 may be disposed in the refrigerant collecting line 260 between the condenser 210 and the compressor 220 .
- the bypass valve 286 may be connected to the bypass line 290 .
- the bypass valve 286 may include a three-way valve.
- the bypass controller 288 may control the bypass valve 286 .
- the bypass controller 288 may receive temperature and pressure signals of the second temperature sensor 282 and the second pressure transducer 284 .
- the bypass line 290 may detour the condenser 210 to connect the refrigerant collecting line 260 to the refrigerant supply line 250 .
- the bypass line 290 may be branched from the bypass valve 286 .
- the bypass line 290 may be connected to the refrigerant supply line 250 between the heat exchangers 230 and the refrigerant expander 240 .
- the bypass controller 288 may allow the refrigerant to detour from the refrigerant collecting line 260 to the refrigerant supply line 250 through the bypass line 290 .
- the bypass controller 288 may allow the refrigerant to detour from the refrigerant collecting line 260 to the refrigerant supply line 250
- the sensitive heat tube 292 may be disposed in the refrigerant collecting line 260 , The sensitive heat tube 292 may be connected to the refrigerant expander 240 .
- the sensitive heat tube 292 may detect the temperature of the refrigerant in the refrigerant collecting line 260 .
- the sensitive heat tube 292 regulates the refrigerant expander 240 on the basis of the temperature of the refrigerant.
- the sensitive heat tube 292 may output a turn-on signal and a turn-off signal of the refrigerant expander 240 . When the temperature of the refrigerant is high, the sensitive heat tube 292 may output the turn-on signal. When the temperature of the refrigerant is low, the sensitive heat tube 292 may output the turn-off signal.
- the cryogenic refrigerator 100 and the condenser 210 , the compressor 220 , the heat exchangers 230 , the refrigerant expander 240 , the refrigerant supply line 250 , and the refrigerant collecting line 260 of the heat dissipation module 200 may be the same as those in FIGS. 1 and 2 .
- the cryogenic refrigerator may increase the radiant efficiency thereof to minimize the operational costs.
- the cryogenic refrigerator may effectively cool the low temperature superconductor or high temperature superconductor.
- the superconductor may be used as a source material for a power plant, a substation, a magnetic resonance device, a magnetic levitation train, a superconductor research center.
- the cryogenic refrigerator may be widely used in the field of superconductor technology.
- the cryogenic refrigerator may be mounted on a tensile tester for cryogenic metal.
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- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Devices That Are Associated With Refrigeration Equipment (AREA)
- Containers, Films, And Cooling For Superconductive Devices (AREA)
Abstract
Provided is a cryogenic refrigeration system. The cryogenic refrigeration system includes a cryogenic refrigerator, and a heat dissipation module configured to cool the cryogenic refrigerator. Here, the heat dissipation module includes a condenser configured to condense a refrigerant that cools the cryogenic refrigerator, and a heat exchanger connected to the cryogenic refrigerator to circulate the refrigerant between the cryogenic refrigerator and the condenser, thereby cooling the cryogenic refrigerator.
Description
- This U.S. non-provisional patent application claims priority under 35 U.S.C. §119 of Korean Patent Application No. PCT/KR2015/004044, filed Apr. 23, 2015, the entire contents of which are hereby incorporated by reference.
- The present invention disclosed herein relates to a cryogenic refrigeration system, and more particularly, to a cryogenic refrigeration system capable of improving a coefficient of performance thereof.
- In general, a cryogenic refrigerator may be used to cool a superconductor or a small-sized electronic component. For example, the cryogenic refrigerator may include a stifling refrigerator, a GM refrigerator, and a Joule-Thomson refrigerator. The above-described cryogenic refrigerator may generate refrigeration output through an expansion process of working fluid such as helium or hydrogen. The expansion process may accompany heat generation of a compression process. Accordingly, the cryogenic refrigerator may be cooled by a heat dissipater. The typical cryogenic refrigerator may be cooled by a dual heat dissipater. The dual heat dissipater may include a water-cooling type heat dissipater and a vapor compression refrigerator. The water-cooling type radiator may cool the cryogenic refrigerator. The water-cooling type heat dissipater may be cooled by the vapor compression refrigerator However, since the water-cooling type heat dissipater uses water that has a low cooling efficiency of performance, a coefficient of performance of the cryogenic refrigerator may be reduced. In addition, the water-cooling type heat dissipater and the vapor compression refrigerator may increase costs for operating the cryogenic refrigerator to reduce productivity.
- The present invention provides a cryogenic refrigeration system capable of increasing a radiant efficiency due to a coefficient of performance of refrigerant.
- The present invention also provides a cryogenic refrigeration system capable of minimizing costs for operating a cryogenic refrigerator.
- Embodiments of the present invention provide a cryogenic refrigeration system including: a cryogenic refrigerator; and a heat dissipation module configured to cool the cryogenic refrigerator. Here, the heat dissipation module includes: a condenser spaced apart from the cryogenic refrigerator to condense a refrigerant that cools the cryogenic refrigerator; and a heat exchanger connected to the cryogenic refrigerator to circulate the refrigerant between the cryogenic refrigerator and the condenser, thereby cooling the cryogenic refrigerator.
- In other embodiments of the present invention, cryogenic refrigeration systems include: a cryogenic refrigerator comprising a power generation part, a power conversion part configured to convert power generated in the power generation part, and a gas cooling part configured to cool a gas by using the power converted in the power conversion part; and a heat dissipation module configured to circulate a refrigerant that cools the cryogenic refrigerator into the power generation part, the power conversion part, and the gas cooling part.
- As described above, the cryogenic refrigeration system according to the embodiments of the present invention may use refrigerant having a coefficient of performance and/or a heat absorption efficiency greater than that of the water to increase a radiant efficiency of the cryogenic refrigerator. The cryogenic refrigerator may be directly cooled by the heat dissipation module to minimize the operational costs.
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FIG. 1 is a diagram illustrating an example of a cryogenic refrigeration system according to the present invention. -
FIG. 2 is a diagram illustrating a cryogenic refrigerator inFIG. 1 . -
FIG. 3 is a diagram illustrating another example of the cryogenic refrigeration system inFIG. 1 . -
FIG. 4 is a diagram illustrating still another example of the cryogenic refrigeration system inFIG. 1 . - Exemplary embodiments of the present invention will be described in detail with reference to the accompanying drawings. Advantages and features of the present invention, and implementation methods thereof will be clarified through following embodiments described with reference to the accompanying drawings. The present invention may, however, be embodied in different forms and should not be construed as limited to the embodiments set forth herein. Rather, these embodiments are provided so that this invention will be thorough and complete, and will fully convey the scope of the present invention to those skilled in the art. Further, the present invention is only defined by scopes of claims. Like reference numerals refer to like elements throughout.
- In the specification, the technical terms are used only for explaining a specific exemplary embodiment while not limiting the present invention. In the specification, the terms of a singular form may include plural forms unless referred to the contrary. The meaning of ‘comprises’ and/or ‘comprising’ specifies a component, a step, an operation and/or an element does not exclude other components, steps, operations and/or elements. Also, it will be understood that the terms such as chambers, units, arms, links, blades, motors, pulleys, rotational shafts, and belts are used as general mechanical terms in the specification. Since preferred embodiments are provided below, the order of the reference numerals given in the description is not limited thereto.
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FIG. 1 is a diagram illustrating an example of acryogenic refrigeration system 10 according to the present invention.FIG. 2 is a diagram illustrating acryogenic refrigerator 100 inFIG. 1 . - Referring to
FIGS. 1 and 2 , thecryogenic refrigeration system 10 according to the present invention may include thecryogenic refrigerator 100 and aheat dissipation module 200. Thecryogenic refrigerator 100 may be cooled to a cryogenic temperature. Theheat dissipation module 200 may dissipate heat from thecryogenic refrigerator 100. - The
cryogenic refrigerator 100 may include a sterling cryogenic refrigerator. According to an embodiment, thecryogenic refrigerator 100 may include apower generation part 110, apower conversion part 120, and agas cooling part 130. - The
power generation part 110 may generate rotational power by external power. For example, thepower generation part 110 may include a motor. Thepower generation part 110 may be connected to thepower conversion part 120. Thepower generation part 110 may be heated to a temperature greater than a room temperature. Thepower generation part 110 may be heated to a temperature equal to or greater than about 30° C. - The
power conversion part 120 may convert the rotational power to reciprocating linear power. Thepower conversion part 120 may include a shaft 1 cam 125, a plurality of connectingrods 126, and ahousing 128. Theshaft 122 may be connected to thepower generation part 110. Thecam 124 may be connected between theshaft 122 and the connectingrods 126. The connectingrods 126 may extend to thegas cooling part 130. Thehousing 128 may surround thecam 124. Thehousing 128 may be connected to thegas cooling part 130. - The
housing 121 may be provided in thehousing 128.Oil 121 may be heated by operation of theshaft 122, thecam 124, and the connectingrods 126. - The
gas cooling part 130 may be disposed on thepower conversion part 120. Thegas cooling part 130 may coolgas 131 at the cryogenic temperature. Thegas 131 may include helium gas. According to an example, thegas cooling part 130 may include acylinder 132, adisplacer 140, and apiston 150. Thecylinder 132 may be connected onto thepower conversion part 120. Thegas 131 may be provided into thecylinder 132. Thedisplacer 140 and thepiston 150 may be connected to the connectingrods 126 to move up and down in thecylinder 132. Thedisplacer 140 may be disposed above thepistol 150. One of the connectingrods 126 may pass through thepiston 150. - The
cylinder 132 may include agas expansion region 134, agas compression region 136, and apiston movement region 138. Thegas expansion region 134 may be disposed above thegas compression region 136. Thedisplacer 140 may be connected to one of the connectingrods 126 to move up and down in thegas expansion region 134 and thegas compression region 136. Thedisplacer 140 may expand and cool thegas 131 in thegas expansion region 134. Accordingly, thegas expansion region 134 may be a cooling region. Thegas compression region 136 may be connected to the rest of the connectingrods 126 and disposed between thegas expansion region 134 and thepiston movement region 138. Thepiston 150 may move up and down in thepiston movement region 138. Alternatively, thepiston movement region 138 may be a region through which one of the connectingrods 126 passes. Thedisplacer 140 and thepiston 150 may compress thegas 131 in thegas compression region 136. Thecompressed gas 131 may heat thecylinder 132 in thegas compression region 136. Thus, thegas compression region 136 may be a heating region. - The
heat dissipation module 200 may circulate to supply refrigerant to thepower generation part 110, thepower conversion part 120, and thegas cooling part 130 to directly cool thecryogenic refrigerator 100. The direct cooling method may have a size smaller than that of the typical dual heat dissipater and reduce maintenance costs. Accordingly, thecryogenic refrigeration system 10 according to the present invention may reduce the operational costs. - According to an example, the
heat dissipation module 200 may include acondenser 210, acompressor 220,heat exchangers 230, arefrigerant expander 240, arefrigerant supply line 250, and arefrigerant collecting line 260. Thecondenser 210 may condense the refrigerant. Thecompressor 220 may be connected to thecondenser 210. Thecondenser 220 may compress the refrigerant. According to an example, the refrigerant may include R22, R123, R134a, HFC-407C, HFC-407A, or R-123yf. The refrigerant may have a freezing point and an evaporation point, which are lower than those of water. For example, when water at a temperature of about 15° C. is heat-exchanged to about 30° C. with respect to thecryogenic refrigerator 100 at a temperature of about 63K, the water may have a coefficient of performance (COP) of about 0.2625. Meanwhile, the refrigerant of the R22 may have the coefficient of performance greater than that of the water. When the R22 at a temperature of about −30° C. is heat-exchanged to about −15° C., the R22 may have the coefficient of performance of about 0.323. Theheat exchangers 230 may be connected to thepower generation part 110, thepower conversion part 120, and thegas cooling part 130. Therefrigerant supply line 250 may be connected between thecondenser 210 and theheat exchangers 230. A radiant efficiency of thecryogenic refrigerator 100 may be increased. Therefrigerant expander 240 may be connected to therefrigerant supply line 250. Therefrigerant collecting line 260 may be connected between thecompressor 220 and theheat exchangers 230. - The
condenser 210 may liquefy the refrigerant. Thecondenser 210 may include a water-cooling type condenser and an air-cooling type condenser. - The
refrigerant expander 240 may be disposed between thecondenser 210 and theheat exchangers 230. Therefrigerant expander 240 may vaporize and cool the refrigerant. The cooled refrigerant may be supplied to theheat exchangers 230 through therefrigerant supply line 250, The refrigerant may be heated in theheat exchangers 230. - The
compressor 220 may supply the heated refrigerant to thecondenser 210 with a predetermined pressure. The refrigerant in a gas state may be supplied to thecondenser 210. The refrigerant may be circulated between theheat exchangers 230 and thecondenser 210. - The
heat exchangers 230 may cool thepower generation part 110, thepower conversion part 120, and thegas cooling part 130. According to an example, theheat exchangers 230 may include agas heat exchanger 232, anoil heat exchanger 234, and amotor heat exchanger 236. - The
gas heat exchanger 232 may be disposed in thecompression region 136. Thegas heat exchanger 232 may cool thecylinder 132 in thecompression region 136. The heatexchange supply line 233 may connect thegas heat exchanger 232 to theoil heat exchanger 234. The heatexchange collecting line 235 may connect thegas heat exchanger 232 to themotor heat exchanger 236. The refrigerant may be sequentially supplied to theoil heat exchanger 234, thegas heat exchanger 232, and themotor heat exchanger 236. Afirst protection cover 312 may be disposed to surround thegas heat exchanger 232. Thefirst protection cover 312 may protect thegas heat exchanger 232. On the other hand, thefirst protection cover 312 may prevent dew formation caused by cooling of the gas heat exchanger 231. - The
power generation part 234 may be disposed on thepower conversion part 120. Theoil heat exchanger 234 may cool the oil in thepower conversion part 120. Theoil heat exchanger 234 may be connected to therefrigerant supply tine 250. Asecond protection cover 314 may be disposed to surround theheat exchanger 234. Thesecond protection cover 314 may protect theoil heat exchanger 234. - The
motor heat exchanger 236 may be disposed on thepower generation part 110. Themotor heat exchanger 236 may cool thepower generation part 110. Themotor heat exchanger 236 may be connected to therefrigerant collecting line 260. -
FIG. 3 is a diagram illustrating another example of thecryogenic refrigeration system 10 inFIG. 1 . - Referring to
FIG. 3 , theheat dissipation module 200 may include afirst pressure transducer 272, afirst temperature sensor 274, and a circulationflow rate controller 276. - The
first pressure transducer 272 may be disposed in therefrigerant collecting line 260 between theheat exchangers 230 and thecompressor 220. Thefirst pressure transducer 272 may detect a pressure of the refrigerant. - The
first temperature sensor 274 may be disposed in therefrigerant collecting line 260 disposed adjacent to thefirst pressure transducer 272. Thefirst temperature sensor 274 may detect a temperature of the refrigerant. - The circulation
flow rate controller 276 may be connected to thefirst pressure transducer 272, thefirst temperature sensor 274, and therefrigerant expander 240. Also, the circulationflow rate controller 276 may receive a detection signal of the temperature and the pressure of thefirst pressure transducer 272 and thefirst temperature sensor 274. The circulation flow rate of the refrigerant may be controlled on the basis of the temperature and the pressure. Therefrigerant expander 240 may control the circulation flow rate of the refrigerant according to the control signal of the circulationflow rate controller 276. - The
cryogenic refrigerator 100 and thecondenser 210, thecompressor 220, theheat exchangers 230, therefrigerant expander 240, therefrigerant supply line 250, and therefrigerant collecting line 260 of theheat dissipation module 200 may be the same as those inFIGS. 1 and 2 . -
FIG. 4 is a diagram illustrating still another example of thecryogenic refrigeration system 10 inFIG. 1 . - Referring to
FIG. 4 , theheat dissipation module 200 may include asecond temper sensor 282, asecond pressure transducer 284, abypass valve 286, abypass controller 288, abypass line 290, and asensitive heat tube 292. - The
second temperature sensor 282 may be disposed in therefrigerant collecting line 260. Thesecond temperature sensor 282 may detect the temperature of the refrigerant. - The
second pressure transducer 284 may be disposed in therefrigerant collecting line 260. Thesecond pressure transducer 284 may detect the pressure of the refrigerant. - The
bypass valve 286 may be disposed in therefrigerant collecting line 260 between thecondenser 210 and thecompressor 220. Thebypass valve 286 may be connected to thebypass line 290. Thebypass valve 286 may include a three-way valve. - The
bypass controller 288 may control thebypass valve 286. Thebypass controller 288 may receive temperature and pressure signals of thesecond temperature sensor 282 and thesecond pressure transducer 284. - The
bypass line 290 may detour thecondenser 210 to connect therefrigerant collecting line 260 to therefrigerant supply line 250. According to an example, thebypass line 290 may be branched from thebypass valve 286. Thebypass line 290 may be connected to therefrigerant supply line 250 between theheat exchangers 230 and therefrigerant expander 240. For example, when the temperature of the refrigerant of therefrigerant collecting line 260 is low, thebypass controller 288 may allow the refrigerant to detour from therefrigerant collecting line 260 to therefrigerant supply line 250 through thebypass line 290. Also, when the pressure of the refrigerant of therefrigerant collecting line 260 is high, thebypass controller 288 may allow the refrigerant to detour from therefrigerant collecting line 260 to therefrigerant supply line 250 - The
sensitive heat tube 292 may be disposed in therefrigerant collecting line 260, Thesensitive heat tube 292 may be connected to therefrigerant expander 240. Thesensitive heat tube 292 may detect the temperature of the refrigerant in therefrigerant collecting line 260. Thesensitive heat tube 292 regulates therefrigerant expander 240 on the basis of the temperature of the refrigerant. Thesensitive heat tube 292 may output a turn-on signal and a turn-off signal of therefrigerant expander 240. When the temperature of the refrigerant is high, thesensitive heat tube 292 may output the turn-on signal. When the temperature of the refrigerant is low, thesensitive heat tube 292 may output the turn-off signal. - The
cryogenic refrigerator 100 and thecondenser 210, thecompressor 220, theheat exchangers 230, therefrigerant expander 240, therefrigerant supply line 250, and therefrigerant collecting line 260 of theheat dissipation module 200 may be the same as those inFIGS. 1 and 2 . - Although the exemplary embodiments of the present invention have been described, it is understood that the present invention should not be limited to these exemplary embodiments but various changes and modifications can be made by one ordinary skilled in the art within the spirit and scope of the present invention as hereinafter claimed. Thus, the above-disclosed embodiments are to be considered illustrative and not restrictive.
- According to the embodiment of the present invention, the cryogenic refrigerator may increase the radiant efficiency thereof to minimize the operational costs. In addition, the cryogenic refrigerator may effectively cool the low temperature superconductor or high temperature superconductor. The superconductor may be used as a source material for a power plant, a substation, a magnetic resonance device, a magnetic levitation train, a superconductor research center. The cryogenic refrigerator may be widely used in the field of superconductor technology. Furthermore, the cryogenic refrigerator may be mounted on a tensile tester for cryogenic metal.
Claims (20)
1. A cryogenic refrigeration system comprising:
a cryogenic refrigerator; and
a heat dissipation module configured to cool the cryogenic refrigerator,
wherein the heat dissipation module comprises:
a condenser spaced apart from the cryogenic refrigerator to condense a refrigerant that cools the cryogenic refrigerator; and
a heat exchanger connected to the cryogenic refrigerator to circulate the refrigerant between the cryogenic refrigerator and the condenser, thereby cooling the cryogenic refrigerator.
2. The cryogenic refrigeration system of claim 1 , wherein the cryogenic refrigerator comprises a gas cooling part configured to expand a gas, thereby cooling the gas, and
the heat exchanger comprises a first heat exchanger configured to cool the gas cooling part.
3. The cryogenic refrigeration system of claim 2 , wherein the gas cooling part comprises:
a cylinder comprising an expansion region in which the gas is expanded and a compression region defined below the expansion region;
a displacer disposed in the cylinder to move between the expansion region and the compression region; and
a piston disposed below the displacer to move in the compression region,
wherein the first heat exchanger is disposed in the compression region.
4. The cryogenic refrigeration system of claim 3 , wherein the cryogenic refrigerator further comprises a power generation part configured to generate power provided to the displacer and the piston, and
the heat exchanger further comprises a second heat exchanger configured to cool the power generation part.
5. The cryogenic refrigeration system of claim 4 , wherein the cryogenic refrigerator further comprises a power conversion part disposed below the cylinder to convert the power generated in the power generation part, and
the heat exchanger further comprises a third heat exchanger configured to cool the power conversion part.
6. The cryogenic refrigeration system of claim 5 , wherein the heat dissipation module further comprises:
a heat exchange collecting line configured to connect the first heat exchanger to the second heat exchanger; and
a heat exchange supply line configured to connect the first heat exchanger to the third heat exchanger.
7. The cryogenic refrigeration system of claim 5 , wherein the heat dissipation module comprises:
a refrigerant collecting line connected between the second heat exchanger and the condenser to collect the refrigerant; and
a refrigerant supply line connected between the third heat exchanger and the condenser to supply the refrigerant.
8. The cryogenic refrigeration system of claim 7 , further comprising:
a compressor disposed in the refrigerant collecting line to compress the refrigerant; and
an expander disposed in the refrigerant supply line to expand the refrigerant.
9. The cryogenic refrigeration system of claim 8 , wherein the heat dissipation module further comprises:
a first pressure transducer disposed in the refrigerant collecting line between the condenser and the second heat exchanger to detect a pressure of the refrigerant;
a first temperature sensor disposed in the refrigerant collecting line disposed adjacent to the first pressure transducer to detect a temperature of the refrigerant; and
a circulation flow rate controller configured to receive a pressure detection signal and a temperature detection signal of the first pressure transducer and the first temperature sensor to control the expander.
10. The cryogenic refrigeration system of claim 8 , wherein the heat dissipation module further comprises:
a bypass valve disposed in the refrigerant collecting line between the condenser and the compressor, and
a bypass line branched from the bypass valve and connected to the refrigerant supply line between the expander and the third heat exchanger by bypassing the condenser.
11. The cryogenic refrigeration system of claim 10 , wherein the heat dissipation module further comprises:
a second pressure transducer disposed in the refrigerant collecting line between the compressor and the second heat exchanger to detect a pressure of the refrigerant;
a second temperature sensor disposed in the refrigerant collecting line disposed adjacent to the second pressure transducer to detect a temperature of the refrigerant; and
a bypass controller configured to receive a pressure detection signal and a temperature detection signal of the second pressure transducer and the second temperature sensor to control the bypass valve.
12. The cryogenic refrigeration system of claim 10 , wherein the heat dissipation module further comprises a sensitive heat tube disposed in the refrigerant collecting line between the compressor and the second heat exchanger to detect a temperature of the refrigerant, thereby outputting turn-on and turn-off signals of the expander.
13. A cryogenic refrigeration system comprising:
a cryogenic refrigerator comprising a power generation part, a power conversion part configured to convert power generated in the power generation part, and a gas cooling part configured to cool a gas by using the power converted in the power conversion part; and
a heat dissipation module configured to circulate a refrigerant that cools the cryogenic refrigerator into the power generation part, the power conversion part, and the gas cooling part.
14. The cryogenic refrigeration system of claim 13 , wherein the heat dissipation module comprises:
a condenser configured to condense the refrigerant; and
a heat exchanger configured to provide the refrigerant condensed in the condenser to the power generation part, the power conversion part, and the gas cooling part.
15. The cryogenic refrigeration system of claim 14 , wherein the heat dissipation module further comprises:
a refrigerant collecting line configured to collect the refrigerant between the condenser and the heat exchanger; and
a refrigerant supply line configured to supply the refrigerant between the condenser and the heat exchanger.
16. The cryogenic refrigeration system of claim 15 , wherein the heat exchanger comprises:
a first heat exchanger configured to cool the gas cooling part;
a second heat exchanger configured to cool the power generation part; and
a first heat exchanger configured to cool the power conversion part.
17. The cryogenic refrigeration system of claim 16 , wherein the heat dissipation module further comprises:
a heat exchange refrigerant collecting line configured to collect the refrigerant between the first heat exchanger and the second heat exchanger; and
a heat exchange refrigerant supply line configured to supply the refrigerant between the first heat exchanger and the third heat exchanger.
18. The cryogenic refrigeration system of claim 16 , wherein the gas cooling part comprises a cylinder having an expansion region in which the gas is expanded and a compression region in which the gas is compressed, and
the first heat exchanger is disposed in the compression region.
19. The cryogenic refrigeration system of claim 15 , wherein the heat dissipation module further comprises:
a compressor disposed in the refrigerant collecting line to compress the refrigerant;
a pressure transducer disposed between the compressor and the heat exchanger to detect a pressure of the refrigerant;
an expander disposed in the refrigerant supply line to expand the refrigerant; and
a circulation flow rate controller configured to receive a pressure detection signal of the pressure transducer to control the expander.
20. The cryogenic refrigeration system of claim 15 , wherein the heat dissipation module further comprises:
a bypass valve disposed in the refrigerant collecting line; and
a bypass line connected to the bypass valve and connected to the refrigerant supply line by bypassing the condenser.
Applications Claiming Priority (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR10-2014-0050248 | 2014-04-25 | ||
| KR20140050248 | 2014-04-25 | ||
| KR1020150052640A KR20150124390A (en) | 2014-04-25 | 2015-04-14 | cryogenic refrigeration system |
| KR10-2015-0052640 | 2015-04-14 | ||
| PCT/KR2015/004044 WO2015163703A1 (en) | 2014-04-25 | 2015-04-23 | Cryogenic refrigeration system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US20170045273A1 true US20170045273A1 (en) | 2017-02-16 |
Family
ID=54600605
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US15/305,911 Abandoned US20170045273A1 (en) | 2014-04-25 | 2015-04-23 | Cryogenic refrigeration system |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US20170045273A1 (en) |
| EP (1) | EP3136021A4 (en) |
| JP (1) | JP2017514101A (en) |
| KR (1) | KR20150124390A (en) |
| CN (1) | CN106461285A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP7611573B2 (en) * | 2021-05-14 | 2025-01-10 | 大学共同利用機関法人自然科学研究機構 | Cascade type cryogenic refrigerator |
| EP4265987A1 (en) * | 2022-04-21 | 2023-10-25 | Bluefors Oy | Cryostat, and method for cooling a cryostat |
| CN120653037B (en) * | 2025-06-17 | 2025-11-28 | 天津掌心医药科技有限公司 | A method and system for multi-zone temperature collaborative management of a high and low temperature integrated machine |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5963465A (en) * | 1982-10-05 | 1984-04-11 | 松下電器産業株式会社 | thermodynamic reciprocating refrigeration engine |
| KR20000052196A (en) * | 1999-01-30 | 2000-08-16 | 구자홍 | Cooling system for lubricationless pulse tube refrigerator |
| US20110100031A1 (en) * | 2009-11-04 | 2011-05-05 | Emidio Barsanti | Device and method for operating a refrigeration cycle with noncondensable gas addition. |
| US20140000235A1 (en) * | 2009-07-01 | 2014-01-02 | Deka Products Limited Partnership | Stirling cycle machine |
Family Cites Families (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2551000B2 (en) * | 1987-05-29 | 1996-11-06 | アイシン精機株式会社 | Cryogenic generator |
| JPH0733932B2 (en) * | 1989-04-28 | 1995-04-12 | ダイキン工業株式会社 | Helium compressor for cryocoolers |
| JPH06159838A (en) * | 1992-11-30 | 1994-06-07 | Sanden Corp | Stirling cycle refrigerating machine |
| JP3949135B2 (en) * | 2004-11-17 | 2007-07-25 | シャープ株式会社 | Piezoelectric pump and Stirling refrigerator |
| JP4718957B2 (en) * | 2005-09-29 | 2011-07-06 | 株式会社東芝 | Pulse tube refrigerator |
| JP2008249157A (en) * | 2007-03-29 | 2008-10-16 | Saginomiya Seisakusho Inc | Reversible temperature expansion valve |
| JP2009264688A (en) * | 2008-04-28 | 2009-11-12 | Hitachi Ltd | Air conditioner for railway vehicle |
| CN201909486U (en) * | 2010-12-13 | 2011-07-27 | 泰豪科技股份有限公司 | Air conditioner capable of performing low-load running of machine set by hot-gas bypass adjusting valve |
| JP2012202672A (en) * | 2011-03-28 | 2012-10-22 | Mitsubishi Heavy Ind Ltd | Expansion valve control device, heat source machine, and expansion valve control method |
| CN203501316U (en) * | 2013-05-08 | 2014-03-26 | 艾默生网络能源有限公司 | Air conditioning system |
-
2015
- 2015-04-14 KR KR1020150052640A patent/KR20150124390A/en not_active Withdrawn
- 2015-04-23 EP EP15783887.1A patent/EP3136021A4/en not_active Withdrawn
- 2015-04-23 US US15/305,911 patent/US20170045273A1/en not_active Abandoned
- 2015-04-23 CN CN201580022039.6A patent/CN106461285A/en active Pending
- 2015-04-23 JP JP2017507662A patent/JP2017514101A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5963465A (en) * | 1982-10-05 | 1984-04-11 | 松下電器産業株式会社 | thermodynamic reciprocating refrigeration engine |
| KR20000052196A (en) * | 1999-01-30 | 2000-08-16 | 구자홍 | Cooling system for lubricationless pulse tube refrigerator |
| US20140000235A1 (en) * | 2009-07-01 | 2014-01-02 | Deka Products Limited Partnership | Stirling cycle machine |
| US20110100031A1 (en) * | 2009-11-04 | 2011-05-05 | Emidio Barsanti | Device and method for operating a refrigeration cycle with noncondensable gas addition. |
Non-Patent Citations (1)
| Title |
|---|
| KR 196 the applicant 12/6/17 - * |
Also Published As
| Publication number | Publication date |
|---|---|
| EP3136021A1 (en) | 2017-03-01 |
| EP3136021A4 (en) | 2018-05-02 |
| CN106461285A (en) | 2017-02-22 |
| KR20150124390A (en) | 2015-11-05 |
| JP2017514101A (en) | 2017-06-01 |
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