CROSS-REFERENCE TO RELATED APPLICATIONS
[0001] This U.S. non-provisional patent application claims priority under 35 U.S.C. § 119
of Korean Patent Application No.
PCT/KR2015/004044, filed April 23, 2015, the entire contents of which are hereby incorporated by reference.
TECHNICAL FIELD
[0002] 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
BACKGROUND ART
[0003] 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 stirling
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.
DISCLOSURE OF THE INVENTION
TECHNICAL PROBLEM
[0004] The present invention provides a cryogenic refrigeration system capable of increasing
a radiant efficiency due to a coefficient of performance of refrigerant.
[0005] The present invention also provides a cryogenic refrigeration system capable of minimizing
costs for operating a cryogenic refrigerator.
TECHNICAL SOLUTION
[0006] 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.
[0007] 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.
ADVANTAGEOUS EFFECTS
[0008] 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.
BRIEF DESCRIPTION OF THE DRAWINGS
[0009]
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.
BEST MODE FOR CARRYING OUT THE INVENTION
[0010] 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.
[0011] 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.
[0012] 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.
[0013] Referring to FIGS. 1 and 2, the cryogenic refrigeration system 10 according to the
present invention 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.
[0014] The cryogenic refrigerator 100 may include a stirling 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.
[0015] The power generation part 110 may generate rotational power by external power. For
example, 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.
[0016] The power conversion part 120 may convert the rotational power to reciprocating linear
power. The power conversion part 120 may include a shaft 122, a 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.
[0017] 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.
[0018] 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. According to an example, 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 piston
150. One of the connecting rods 126 may pass through the piston 150.
[0019] 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. Accordingly, 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.
Alternatively, 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. Thus, the gas compression region 136
may be a heating region.
[0020] 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.
[0021] According to an example, 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. 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 the cryogenic 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. 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.
[0022] The condenser 210 may liquefy the refrigerant. The condenser 210 may include a water-cooling
type condenser and an air-cooling type condenser.
[0023] 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.
[0024] 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.
[0025] The heat exchangers 230 may cool the power generation part 110, the power conversion
part 120, and the gas cooling part 130. According to an example, the heat exchangers
230 may include a gas heat exchanger 232, an oil heat exchanger 234, and a motor heat
exchanger 236.
[0026] 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. On the other
hand, the first protection cover 312 may prevent dew formation caused by cooling of
the gas heat exchanger 232.
[0027] 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 line 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.
[0028] 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.
MODE FOR CARRYING OUT THE INVENTION
[0029] FIG. 3 is a diagram illustrating another example of the cryogenic refrigeration system
10 in FIG. 1.
[0030] Referring to FIG. 3, the heat dissipation module 200 may include a first pressure
transducer 272, a first temperature sensor 274, and a circulation flow rate controller
276.
[0031] 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.
[0032] 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.
[0033] 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.
[0034] 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.
[0035] FIG. 4 is a diagram illustrating still another example of the cryogenic refrigeration
system 10 in FIG. 1.
[0036] Referring to FIG. 4, 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.
[0037] 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.
[0038] 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.
[0039] 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.
[0040] 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.
[0041] The bypass line 290 may detour the condenser 210 to connect the refrigerant collecting
line 260 to the refrigerant supply line 250. According to an example, 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. For example, when the temperature of the refrigerant of the refrigerant
collecting line 260 is low, 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. Also, when the pressure of the refrigerant of the refrigerant
collecting line 260 is high, the bypass controller 288 may allow the refrigerant to
detour from the refrigerant collecting line 260 to the refrigerant supply line 250
[0042] 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.
[0043] 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.
[0044] 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.
INDUSTRIAL APPLICABILITY
[0045] 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.
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.