EP2211124A1 - Tiefkühler und steuerverfahren dafür - Google Patents

Tiefkühler und steuerverfahren dafür Download PDF

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Publication number
EP2211124A1
EP2211124A1 EP08851240A EP08851240A EP2211124A1 EP 2211124 A1 EP2211124 A1 EP 2211124A1 EP 08851240 A EP08851240 A EP 08851240A EP 08851240 A EP08851240 A EP 08851240A EP 2211124 A1 EP2211124 A1 EP 2211124A1
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EP
European Patent Office
Prior art keywords
pressure
cryogenic
temperature
low
storage tank
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EP08851240A
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English (en)
French (fr)
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EP2211124A4 (de
Inventor
Nobuyoshi Saji
Toshio Takahashi
Seiichiro Yoshinaga
Hirohisa Wakisaka
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IHI Corp
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IHI Corp
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Publication of EP2211124A1 publication Critical patent/EP2211124A1/de
Publication of EP2211124A4 publication Critical patent/EP2211124A4/de
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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
    • F25B9/00—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point
    • F25B9/06—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point using expanders
    • 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
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/003—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production
    • F25J1/0047—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using an "external" refrigerant stream in a closed vapor compression cycle
    • F25J1/005—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using an "external" refrigerant stream in a closed vapor compression cycle by expansion of a gaseous refrigerant stream with extraction of work
    • 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
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/006—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the refrigerant fluid used
    • F25J1/0062—Light or noble gases, mixtures thereof
    • 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
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/006—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the refrigerant fluid used
    • F25J1/0062—Light or noble gases, mixtures thereof
    • F25J1/0065—Helium
    • 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
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
    • F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
    • F25J1/0244—Operation; Control and regulation; Instrumentation
    • F25J1/0245—Different modes, i.e. 'runs', of operation; Process control
    • F25J1/0248—Stopping of the process, e.g. defrosting or deriming, maintenance; Back-up mode 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
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
    • F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
    • F25J1/0257—Construction and layout of liquefaction equipments, e.g. valves, machines
    • F25J1/0275—Construction and layout of liquefaction equipments, e.g. valves, machines adapted for special use of the liquefaction unit, e.g. portable or transportable devices
    • F25J1/0276—Laboratory or other miniature devices
    • 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
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
    • F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
    • F25J1/0279—Compression of refrigerant or internal recycle fluid, e.g. kind of compressor, accumulator, suction drum etc.
    • F25J1/0285—Combination of different types of drivers mechanically coupled to the same refrigerant compressor, possibly split on multiple compressor casings
    • F25J1/0288—Combination of different types of drivers mechanically coupled to the same refrigerant compressor, possibly split on multiple compressor casings using work extraction by mechanical coupling of compression and expansion of the refrigerant, so-called companders
    • 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 
    • F25B2309/1401—Ericsson or Ericcson cycles
    • 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
    • F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
    • F25B2400/16—Receivers
    • 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
    • F25B2500/00—Problems to be solved
    • F25B2500/27—Problems to be solved characterised by the stop of the refrigeration 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
    • F25B2600/00—Control issues
    • F25B2600/25—Control of valves
    • F25B2600/2519—On-off 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
    • F25B45/00—Arrangements for charging or discharging refrigerant
    • 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
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2245/00—Processes or apparatus involving steps for recycling of process streams
    • F25J2245/02—Recycle of a stream in general, e.g. a by-pass stream
    • 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
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2270/00—Refrigeration techniques used
    • F25J2270/14—External refrigeration with work-producing gas expansion loop
    • F25J2270/16—External refrigeration with work-producing gas expansion loop with mutliple gas expansion loops of the same refrigerant
    • 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
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2270/00—Refrigeration techniques used
    • F25J2270/90—External refrigeration, e.g. conventional closed-loop mechanical refrigeration unit using Freon or NH3, unspecified external refrigeration
    • F25J2270/912—Liquefaction cycle of a low-boiling (feed) gas in a cryocooler, i.e. in a closed-loop refrigerator

Definitions

  • the present invention relates to a cryogenic refrigerator having a cooling capacity of cooling a cooled object up to cryogenic temperatures and a control method therefor.
  • a cryogenic refrigerator for example, a Brayton cycle refrigerator or an Ericsson cycle refrigerator
  • HTS high temperature superconducting
  • HTS high temperature superconducting
  • the lowest temperature is 65K, 40K, 30K, 20K, or the like, though it depends on the type and application of a superconducting wire.
  • cooling output is 1 to 10kW or so at each temperature, and helium (the boiling point is approx. 4K), neon (the boiling point is approx. 27K), or a mixture gas of helium and neon is used as a refrigerant gas.
  • This type of cryogenic refrigerator is disclosed in, for example, Patent Documents 1 and 2 and Non-patent Document 1.
  • the cascade-turbo helium refrigerating liquefier in Patent Document 1 includes a neon refrigeration cycle, which has a turbo type compressor 51, heat exchangers 52a to 52e, and a turbo type expander 53, and a helium refrigeration cycle, which has a turbo type compressor 54, heat exchangers 55a to 55c, an expansion turbine 56, and a Joule-Thomson valve 57. It is characterized that the neon refrigeration cycle previously cools helium.
  • the refrigerator disclosed in Patent Document 2 is intended to prevent a cooling medium from being solidified, to extend the maintenance period, to enable a large output, and to eliminate vibration.
  • the refrigerator 61 includes a centrifugal compressor 62 and a turbine 63 with a one-stage wing 64 of the compressor 62 and converts a gas 65, which is compressed by the compressor 62 and introduced to the turbine 63, to, for example, a gas mixture of helium and argon or of helium and nitrogen or the like.
  • Non-patent Document 1 discloses a cryogenic refrigerator for cooling liquid nitrogen (the boiling point is approx. 77K) up to 65K in order to cool a high temperature superconducting cable as shown in Fig. 3 .
  • cryogenic refrigerator using the expensive working gases is required to minimize a gas charging weight and to stabilize the internal pressure from the start of the refrigerator to the steady operation.
  • a low-pressure low-temperature portion of the running cryogenic refrigerator is cooled from, for example, a room temperature (for example, 300 K) to a cryogenic temperature (for example, 60 K) along with a decrease in temperature of the inside of the refrigerator, the gas volume of the low-pressure low-temperature portion is reduced to one fifth (1/5). Therefore, in order to maintain a predetermined pressure (for example, one half (1/2) of the pressure on start-up), the low-pressure low-temperature portion is required to be supplied with a working gas so that the working gas is five halves (5/2) of the working gas on start-up.
  • a predetermined pressure for example, one half (1/2) of the pressure on start-up
  • the pressure rises after the stop of the operation and therefore it is necessary to discharge the working gas to the outside or to bleed the working gas to a pressure vessel, which is provided separately.
  • discharging the working gas to the outside causes a great loss of the expensive working gas
  • bleeding the working gas to the pressure vessel causes excess pressure resistance of the pressure vessel.
  • the present invention has been devised in order to solve the above problems. Specifically, it is an object of the present invention to provide a cryogenic refrigerator and a control method therefor, the cryogenic refrigerator having a cooling capacity of cooling a cooled object up to a predetermined cryogenic temperature, capable of maintaining the pressure in a high-pressure portion at a substantially constant level from a room temperature in a stopped state to a cryogenic temperature in an operating state without using a pressure vessel whose pressure resistance exceeds a predetermined pressure (for example, 1 MPa) and without discharging or supplying a working gas, and capable of preventing a reverse rotation of a compressor even in the case of an emergency stop.
  • a predetermined pressure for example, 1 MPa
  • a cryogenic refrigerator which generates a cryogenic temperature by compressing a working gas in a closed loop and expanding the compressed working gas
  • the cryogenic refrigerator comprising: a bypass line which allows a high-pressure portion and a low-pressure portion in the closed loop to communicate with each other; a gas storage tank which is located midway in the bypass line and has pressure regulation valves on the high-pressure side and the low-pressure side, respectively; and a pressure control unit which controls the pressure regulation valves, wherein the pressure control unit controls the pressure regulation valves so that the pressure in the gas storage tank is equal to the pressure in the closed loop at room temperature and in a stopped state and controls the pressure regulation valves so that the pressure in the high-pressure portion is equal to a predetermined pressure in an operating state in which the cryogenic temperature is generated.
  • the capacity of the gas storage tank is set so as to enable the pressure in the gas storage tank to be maintained at a predetermined reference pressure or lower at room temperature and in the stopped state and so as to enable the pressure in the high-pressure portion to be maintained at a predetermined operating pressure in the operating state in which the cryogenic temperature is generated.
  • the pressure control unit maintains the pressure regulation valves to be fully opened in the stopped state of the cryogenic refrigerator and opens the pressure regulation valve connected to the high-pressure side in the case where the pressure in the high-pressure portion exceeds a predetermined maximum pressure and opens the pressure regulation valve connected to the low-pressure side in the case where the pressure in the high-pressure portion is equal to or lower than a predetermined minimum pressure.
  • the cryogenic refrigerator further comprises: a room-temperature compressor which is installed in a room temperature portion in the closed loop to compress the working gas from a predetermined low pressure to a predetermined high-pressure; a first intermediate heat exchanger which is located between a cryogenic temperature portion in the closed loop and the room temperature portion to perform a heat exchange between the working gases; and an expander which is installed on the cryogenic temperature portion side from the first intermediate heat exchanger to isentropically expand the working gas.
  • the room-temperature compressor includes a plurality of turbo compressors which compress the working gas in multiple stages from the predetermined low pressure to the high pressure;
  • the expander includes a plurality of expansion turbines which expand the working gas in multiple stages from the high pressure to the low pressure; and a plurality of intermediate heat exchangers which perform a heat exchange between working gases are disposed in the middle of the plurality of expansion turbines.
  • a control method for a cryogenic refrigerator which generates a cryogenic temperature by compressing a working gas in a closed loop and expanding the compressed working gas
  • the control method comprising: providing the cryogenic refrigerator with a bypass line which allows a high-pressure portion and a low-pressure portion in the closed loop to communicate with each other and a gas storage tank which is located midway in the bypass line and has pressure regulation valves on the high-pressure side and the low-pressure side, respectively; and controlling the pressure regulation valves so that the pressure in the gas storage tank is equal to the pressure in the closed loop at room temperature and in a stopped state and controlling the pressure regulation valves so that the pressure in the high-pressure portion is equal to a predetermined pressure in an operating state in which a cryogenic temperature is generated.
  • the capacity of the gas storage tank is set so as to enable the pressure in the gas storage tank to be maintained at a predetermined reference pressure or lower at room temperature in the stopped state and so as to enable the pressure in the high-pressure portion to be maintained at a predetermined operating pressure in the operating state in which the cryogenic temperature is generated.
  • the cryogenic refrigerator comprises a bypass line which allows a high-pressure portion and a low-pressure portion in the closed loop, which constitutes the cryogenic refrigerator, to communicate with each other and a gas storage tank which is located midway in the bypass line and has pressure regulation valves on the high-pressure side and the low-pressure side, respectively, and therefore it is possible to set the pressure of the entire system, which includes the closed loop, the bypass line, and the gas storage tank, to a predetermined reference pressure or lower by controlling the pressure regulation valves (for example, maintaining the pressure regulation valves to be fully opened in the stopped state) so that the pressure in the gas storage tank is equal to the pressure in the closed loop at room temperature and in a stopped state.
  • the pressure regulation valves for example, maintaining the pressure regulation valves to be fully opened in the stopped state
  • this enables the pressures on the inlet side and outlet side of the compressor to be equalized in the stopped state of the refrigerator, and therefore it is possible to prevent a reverse rotation of the compressor caused by a pressure difference between the inlet side and the outlet side of the compressor after the stop.
  • the low-pressure low-temperature portion of the cryogenic refrigerator in the operating state requires, for example, five halves of the working gas on start-up due to a decrease in temperature and in pressure
  • the capacity of the gas storage tank is set so that the pressure in the gas storage tank is able to be maintained at a predetermined reference pressure or lower level at room temperature in the stopped state and so that the pressure in the high-pressure portion is able to be maintained at a predetermined operating pressure level in the operating state in which the cryogenic temperature is generated, thereby enabling the cryogenic refrigerator to have a cooling capacity of cooling an cooled object up to a predetermined cryogenic temperature and to maintain the pressure in the high-pressure portion at a substantially constant level from the room temperature in the stopped state to the cryogenic temperature in the operating state without using a pressure vessel whose pressure resistance exceeds a predetermined pressure (for example, 1 MPa) and without discharging or supplying the working gas.
  • a predetermined pressure for example, 1 MPa
  • the cryogenic refrigerator 10 is a cryogenic refrigerator which generates a cryogenic temperature by compressing a working gas in a closed loop 11 and expanding the compressed working gas.
  • the expansion by an expansion turbine is preferably an isentropic expansion.
  • the cryogenic refrigerator 10 has the closed loop 11 in which a working gas circulates, and the closed loop 11 is provided with a cryogenic heat exchanger 12, a room-temperature compressor 14, a first intermediate heat exchanger 16, and an expander 18.
  • the working gas used to circulate in the closed loop 11 is helium (the boiling point is approx. 4K), neon (the boiling point is approx. 27K), or a mixture gas of helium and neon.
  • the cryogenic heat exchanger 12 is installed in a cryogenic temperature portion of the closed loop 11 and indirectly cools down a cooled object with the working gas.
  • the cooled object is high temperature superconducting (HTS) equipment (for example, a superconducting transmission cable, a superconducting transformer, a superconducting motor, a superconducting coil for storing superconducting power, a large accelerator, a nuclear fusion test facility, MHD power generation, a superconducting coil, or the like), and the outlet temperature of the cryogenic heat exchanger 12 in the cryogenic temperature portion is, for example, 65K.
  • HTS high temperature superconducting
  • the room-temperature compressor 14 is, for example, a turbo compressor, which is installed in a room temperature portion (for example, in a room at a temperature around 300 K) of the closed loop 11 to compress the working gas from a predetermined low pressure to a predetermined high pressure.
  • the predetermined low pressure is, for example, 0.5 to 0.6 MPa
  • the predetermined high pressure is, for example, 1.0 to 1.2 MPa
  • the compression ratio of the compressor is around 2.
  • a water-cooled gas cooler 15 is installed on the downstream side (high-pressure side) of the room-temperature compressor 14 to cool the working gas, which has increased in temperature as a result of the compression, preferably up to around 300 K by using cooling water supplied from an external cooling water circulation unit 9.
  • the first intermediate heat exchanger 16 is located between the cryogenic temperature portion and the room temperature portion to perform a heat exchange between the working gas in the high-pressure side and the working gas in the low pressure side.
  • the heat exchange cools the working gas on the high-pressure side preferably up to 65 to 70 K.
  • the expander 18 is, for example, an expansion turbine and is installed on the cryogenic temperature portion side from the first intermediate heat exchanger 16 to isentropically expand the working gas, which has been cooled by the first intermediate heat exchanger 16.
  • the expansion by the expansion turbine causes the working gas to generate a predetermined cryogenic temperature (for example, 56 K).
  • the expansion turbine is coaxial with the turbo compressor, and preferably the same electric motor drives the expansion turbine and the turbo compressor.
  • the working gas at the cryogenic temperature is supplied to the cryogenic heat exchanger 12 to cool the cooled object indirectly with the working gas, and cools the working gas on the high-pressure side indirectly in the first intermediate heat exchanger 16. Subsequently, the working gas is supplied to the room-temperature compressor 14 and is compressed again.
  • the foregoing structure allows the cooled object up to the predetermined cryogenic temperature by compressing the working gas in the closed loop 11 and expanding the compressed working gas using the expander 18 to generate a cryogenic temperature.
  • the cryogenic refrigerator 10 further includes a bypass line 22, a gas storage tank 24, and a pressure control unit 26.
  • the bypass line 22 allows a high-pressure portion and a low-pressure portion of the closed loop 11 to communicate with each other directly.
  • the above high-pressure portion is on the downstream side from the compressor 14 in this example, and more specifically, has the volume of the high-pressure side of the gas cooler 15 and the first intermediate heat exchanger 16, and a connecting pipe located from the outlet of the compressor 14 to the inlet of the expander 18.
  • the above low-pressure portion is on the upstream side from the room-temperature compressor 14 in this example, and more specifically, has the volume of the low-pressure side of the cryogenic heat exchanger 12 and the first intermediate heat exchanger 16, and a connecting pipe from the outlet of the expander 18 to the inlet of the room-temperature compressor 14.
  • the gas storage tank 24 is located midway in the bypass line 22, having pressure regulation valves 23a and 23b on the high-pressure side and the low-pressure side, respectively.
  • the capacity of the gas storage tank is set so that the pressure in the gas storage tank 24 is able to be maintained at a predetermined reference pressure (for example, 1 MPa) or lower level at room temperature in a stopped state and so that the pressure in the high-pressure portion is able to be maintained at a predetermined operating pressure level (for example, 1.0 to 1.2 MPa) in an operating state in which a cryogenic temperature is generated.
  • a predetermined reference pressure for example, 1 MPa
  • a predetermined operating pressure level for example, 1.0 to 1.2 MPa
  • the capacity of the gas storage tank 24 requires a volume of the gas storage tank, which satisfies the condition that a difference between the total mass of a gas exclusive of the gas storage tank 24 in the closed loop 11 calculated from the temperature and pressure in the operating state and the mass of a gas loaded at the pressure (for example, 1 MPa) in the high-pressure portion (on the downstream side from the gas cooler 15 in Fig.
  • the operating state for the volume of the closed loop 11 exclusive of the gas storage tank 24 in the stopped state and at room temperature is equal to a difference between the mass of a gas obtained in the case where the gas storage tank 24 is filled with the pressure in the high-pressure portion in the operating state and the mass of a gas obtained in the case where the gas storage tank 24 is filled with the pressure in the low-pressure portion (the upstream side from the room-temperature compressor 14 in Fig. 4 ) in the operating state.
  • the temperature of the gas storage tank is always constant.
  • the pressure in the gas storage tank is maximum when it is equal to the pressure on the high-pressure side in the operating state and is minimum when it is equal to the pressure on the low-pressure side in the operating state.
  • the capacity of the gas storage tank 24 is preferably set so as to be 3 or more times, preferably 4 or 5 times, the volume of the low-temperature low-pressure portion at cryogenic temperature and low pressure.
  • a pressure sensor 25 is installed in the high-pressure portion in the closed loop 11, and detected pressure data is input to the pressure control unit 26.
  • the pressure control unit 26 controls the pressure regulation valves 23a and 23b so that the pressure in the gas storage tank 24 is equal to the pressure in the closed loop 11 at room temperature and in a stopped state on the basis of the detected pressure data and controls the pressure regulation valves 23a and 23b so that the pressure in the gas storage tank 24 is between the pressures in the high-pressure portion and in the low-pressure portion and close to the pressure in the low-pressure portion (a pressure slightly higher than the pressure in the low-pressure portion) in the operating state in which the cryogenic temperature is generated.
  • the pressure control unit 26 performs the following controls by using the cryogenic refrigerator 10 having the above configuration:
  • the same controls are performed to stop the cryogenic refrigerator 10 from the steady operation which generates the cryogenic temperature. More specifically, the pressure on the high-pressure side rises up along with an increase in the temperature and pressure of the low-temperature low-pressure portion at cryogenic temperature and low pressure in the operating state, and therefore it is possible to collect excess working gas into the gas storage tank 24 by the above operation (C).
  • the operation (A) for maintaining the pressure regulation valves 23a and 23b to be fully opened enables the pressure on the inlet side of the compressor 14 to be equalized with the pressure on the outlet side of the compressor 14 in the stopped state of the refrigerator, and therefore it is possible to prevent a reverse rotation of the compressor caused by a pressure difference between the inlet side and outlet side of the compressor 14 after the stop of the refrigerator.
  • the cryogenic refrigerator 10 includes the gas storage tank 24, which is located midway in the bypass line 22 allowing the high-pressure portion and the low-pressure portion in the closed loop 11 to communicate with each other, and which has the pressure regulation valves 23a and 23b on the high-pressure side and the low-pressure side, respectively. Therefore, it is possible to set the pressure in the entire system, which includes the closed loop 11, the bypass line 22, and the gas storage tank 24, to a predetermined reference pressure (for example, 1 MPa) or lower by controlling the pressure regulation valves so that the pressure in the gas storage tank 24 is equal to the pressure in the closed loop 11 at room temperature and in the stopped state (for example, by maintaining the pressure regulation valves 23a and 23b to be fully opened in the stopped state).
  • a predetermined reference pressure for example, 1 MPa
  • this enables the pressure on the inlet side of the compressor 14 to be equalized with the pressure on the outlet side of the compressor 14 in the stopped state of the refrigerator, and therefore it is possible to prevent a reverse rotation of the compressor caused by pressure after the stop of the refrigerator.
  • the pressure regulation valves 23a and 23b are controlled so that the pressure in the gas storage tank 24 is between the pressures in the high-pressure portion and in the low-pressure portion and close to the pressure in the low-pressure portion in the operating state in which the cryogenic temperature is generated, and therefore it is possible to supply the corresponding working gas from the gas storage tank even if the pressure of the working gas in the closed loop drops along with a decrease in the temperature of the low-temperature portion in the refrigerator after the start of the operation.
  • the capacity of the gas storage tank 24 is set so as to be 3 or more times the volume V of the low-temperature low-pressure portion at cryogenic temperature and low pressure in the operating state, it is necessary to supply the low-temperature low-pressure portion with working gas so that the gas volume of the portion is five halves (2.5) of the gas volume on start-up in order to maintain the pressure (for example, one half of the pressure on start-up) in the low-temperature low-pressure portion due to a decrease in temperature (for example, 300 K to 60 K) and a decrease in pressure (for example, to one half). Therefore, even if the working gas corresponding to the shortfall of 1.5 V is supplied from the gas storage tank 24 to the low-temperature low-pressure portion, it is possible to maintain the pressure in the gas storage tank 24 at one half or more of the pressure in the stopped state.
  • the capacity of the gas storage tank 24 is set so that the pressure in the gas storage tank 24 is able to be maintained at the predetermined reference pressure (for example, 1 MPa) or lower level at room temperature in the stopped state and so that the pressure in the high-pressure portion is able to be maintained at the predetermined operating pressure level in an operating state in which the cryogenic temperature is generated, thereby enabling the cryogenic refrigerator to have a cooling capacity of cooling the cooled object up to the predetermined cryogenic temperature and to maintain the pressure in the high-pressure portion at a substantially constant level from the room temperature in the stopped state to the cryogenic temperature in the operating state without using a gas storage tank whose pressure resistance exceeds the predetermined pressure (for example, 1 MPa) and without discharging or supplying the working gas.
  • the predetermined reference pressure for example, 1 MPa
  • FIG. 5 there is shown a diagram illustrating a second embodiment of the cryogenic refrigerator according to the present invention.
  • the outlet temperature of the cryogenic temperature portion is 65 K and the cooling capacity thereof is 3 kW in this example, where P, T and G in this figure represent the pressure (bar), the temperature (K), and the mass flow rate (g/s), respectively.
  • the room-temperature compressor 14 includes a first stage compressor 14A, which compresses a working gas from a predetermined low pressure (5.57 bar) to a first intermediate pressure (8.03 bar) between the low pressure and the high pressure, and a second stage compressor 14B, which compresses the working gas from the first intermediate pressure to a high pressure (11.0 bar).
  • Water-cooled gas coolers 15 are installed on the downstream side (the high-pressure side) of the first stage compressor 14A and the second stage compressor 14B, respectively.
  • the expander 18 includes a first expander 18A, which expands the working gas from the high pressure (11.0 bar) to a second intermediate pressure (10.29 bar) between the low pressure and the high pressure, and a second expander 18B, which expands the working gas from the second intermediate pressure to the low pressure (5.57 bar).
  • a second intermediate heat exchanger 17 which exchanges heat between the low-pressure working gas and the high-pressure working gas, between the first expander 18A and the second expander 18B.
  • the first stage compressor 14A and the second stage compressor 14B are turbo compressors, and the first expander 18A and the second expander 18B are expansion turbines.
  • the first stage compressor 14A is coaxial with the second expander 18B, and the second stage compressor 14B is coaxial with the first expander 18A.
  • the same electric motor drives the turbo compressors and the expansion turbines.
  • Other parts of the configuration are the same as in Fig. 4 .
  • this configuration enables the generation of a cryogenic temperature of 56 K by compressing the working gas in the closed loop 11 and expanding the compressed working gas by using the first expander 18A and the second expander 18B, thereby enabling an absorption of 3 kW heat from the cooled object.
  • a room temperature portion is provided with the gas storage tank 24 and is connected via a pipe (the bypass line 22) having the pressure regulation valves 23a and 23b on the high-pressure side (the outlet side of the compressor) and the low-pressure side (the return side) of the refrigerator, respectively. While both of the reference pressures in the control of the pressure regulation valves 23a and 23b are high-pressure side pressures, the pressure regulation valve 23a with the pipe connected to the high-pressure side is "opened" when the pressure exceeds a specified pressure and the pressure regulation valve 23b with the pipe connected to the return side is "opened” when the high-pressure side pressure drops to a lower value than the specified pressure to increase the pressure in the system.
  • the volume of the gas storage tank 24 is set to a value as small as possible within a scope that the pressure is maintained at a slightly higher level than the return-side pressure in the operating state and the pressure does not exceed a design pressure even at room temperature in the system in the stopped state.
  • the expansion turbines (the first expander 18A and the second expander 18B) are adapted to be coaxial with the turbo compressors (the first stage compressor 14A and the second stage compressor 14B) and the same electric motor drives the expansion turbines and the turbo compressors, thereby enabling the collection of the power of the expansion turbines so as to reduce the electric motor power and enabling the rotational speed of the expansion turbines to be limited to that of the electric motor so as to essentially prevent the overspeed of the expansion turbines. Therefore, there is no need to use bypass valves for the expansion turbines or throttle valves in the inlet and the compressors are able to operate at a rated speed from the start-up.
  • both of the pressure regulation valves 23a and 23b are opened in the stopped state of the refrigerator to equalize the pressures on the inlet side and outlet side of the compressor, thereby preventing the reverse rotation of the compressors (the first stage compressor 14A and the second stage compressor 14B) caused by a pressure difference between the inlet side and the outlet side of the compressors after the stop of the refrigerator.
  • the room-temperature compressor 14 increases the pressure of the working gas
  • the gas cooler 15 decreases the increased temperature of the gas up to close to a room temperature
  • the working gas passes through the first intermediate heat exchanger 16 and the expander 18, thereby decreasing the temperature and decreasing the pressure.
  • a return gas which has removed heat from the cooled object which is a refrigeration load, increases in temperature up to close to a room temperature while cooling the working gas on the high-pressure side in the first intermediate heat exchanger 16 and then returns to the room-temperature compressor 14.
  • a pressure ratio between the high-pressure side and the low-pressure side is around 2.
  • the gas storage tank 24 is connected via the pipe (the bypass line 22) having the pressure regulation valves 23a and 23b on the high-pressure side of the refrigerator (the outlet side from the compressor) and the return side of the refrigerator (the inlet side from the compressor), respectively.
  • both of the reference pressures in the control of the pressure regulation valves 23a and 23b are high-pressure side pressures
  • the pressure regulation valve 23a with the pipe connected to the high-pressure side is "opened” when the pressure exceeds a specified pressure and the pressure regulation valve 23b with the pipe connected to the return side is “opened” when the high-pressure side pressure drops to a lower value than the specified pressure to increase the pressure in the system. Due to the functions of the two pressure regulation valves 23a and 23b, the pressure on the high-pressure side is maintained at a constant level in the operating state, on start-up, and in the stopped state.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • Clinical Laboratory Science (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
  • Separation By Low-Temperature Treatments (AREA)
EP08851240.5A 2007-11-19 2008-11-05 Tiefkühler und steuerverfahren dafür Withdrawn EP2211124A4 (de)

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EP2625474A1 (de) * 2010-10-08 2013-08-14 Sumitomo Cryogenics Of America Inc. Tiefsttemperaturkälteanlage mit schneller abwärmung
EP2729705A1 (de) * 2011-07-06 2014-05-14 Sumitomo (Shi) Cryogenics of America, Inc. Kaltwasserdampf-kryopumpe mit gasausgeglichenem brayton-kreislauf
EP2729705A4 (de) * 2011-07-06 2015-04-29 Sumitomo Shi Cryogenics Am Inc Kaltwasserdampf-kryopumpe mit gasausgeglichenem brayton-kreislauf
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EP2940406A4 (de) * 2013-05-31 2016-06-15 Maekawa Seisakusho Kk Brayton-kreislauf-kühlvorrichtung
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EP3339605A1 (de) * 2016-12-23 2018-06-27 Linde Aktiengesellschaft Verfahren zum verdichten gasmischung umfassend neon
FR3101404A1 (fr) * 2019-10-01 2021-04-02 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Dispositif de motorisation, véhicule volant et procédé de refroidissement d’un moteur
FR3119669A1 (fr) * 2021-02-10 2022-08-12 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Dispositif et procédé de liquéfaction d’un fluide tel que l’hydrogène et/ou de l’hélium
FR3119667A1 (fr) * 2021-02-10 2022-08-12 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Dispositif et procédé de liquéfaction d’un fluide tel que l’hydrogène et/ou de l’hélium
WO2022171392A1 (fr) * 2021-02-10 2022-08-18 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Dispositif et procédé de liquéfaction d'un fluide tel que l'hydrogène et/ou de l'hélium
WO2022171391A1 (fr) * 2021-02-10 2022-08-18 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Dispositif et procédé de liquéfaction d'un fluide tel que l'hydrogène et/ou de l'hélium
WO2022171485A1 (fr) * 2021-02-10 2022-08-18 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Dispositif et procédé de liquéfaction d'un fluide tel que l'hydrogène et/ou de l'hélium
WO2022171390A1 (fr) * 2021-02-10 2022-08-18 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Dispositif et procédé de liquéfaction d'un fluide tel que l'hydrogène et/ou de l'hélium

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EP2211124A4 (de) 2015-07-22
US20100275616A1 (en) 2010-11-04
JP2009121786A (ja) 2009-06-04
KR20100087135A (ko) 2010-08-03
CN101861500A (zh) 2010-10-13
CN101861500B (zh) 2012-07-18
KR101161339B1 (ko) 2012-06-29
WO2009066565A1 (ja) 2009-05-28

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