US20120227418A1 - Cooling unit - Google Patents

Cooling unit Download PDF

Info

Publication number
US20120227418A1
US20120227418A1 US13/413,786 US201213413786A US2012227418A1 US 20120227418 A1 US20120227418 A1 US 20120227418A1 US 201213413786 A US201213413786 A US 201213413786A US 2012227418 A1 US2012227418 A1 US 2012227418A1
Authority
US
United States
Prior art keywords
refrigerant
cooling unit
cooling
load
cooled
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Abandoned
Application number
US13/413,786
Inventor
Lutz Decker
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Linde GmbH
Original Assignee
Linde GmbH
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Linde GmbH filed Critical Linde GmbH
Assigned to LINDE AKTIENGESELLSCHAFT reassignment LINDE AKTIENGESELLSCHAFT ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: DECKER, LUTZ
Publication of US20120227418A1 publication Critical patent/US20120227418A1/en
Abandoned legal-status Critical Current

Links

Images

Classifications

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

Abstract

The invention relates to a cooling unit for cooling a load having a refrigeration circuit, at least one compressor for compressing a refrigerant that circulates in the refrigeration circuit, several heat exchangers, in which the refrigerant is cooled against itself, and two expansion devices that operate at different temperature levels, in which, at least temporarily, at least one partial stream of the refrigerant is expanded to produce cold. At least one additional expansion device is provided. The latter is connected to the refrigeration circuit in such a way that the refrigerant that can be, at least temporarily, at least partially expanded in the additional expansion device to produce cold.

Description

    SUMMARY OF THE INVENTION
  • The invention relates to a cooling unit, comprising
      • a refrigeration circuit,
      • at least one compressor, which uses the compression of the refrigerant that circulates in the refrigeration circuit,
      • several heat exchangers, in which the refrigerant is cooled against itself, and
      • two expansion devices that operate at different temperature levels, in which, at least temporarily, at least one partial stream of the refrigerant is expanded to produce cold.
  • The invention also relates to a method for operating a cooling unit.
  • A general cooling unit as well as a general method for operating a cooling unit are known, for example, from the un-prepublished German Patent Application 102011009965.
  • General cooling units are usually used for cooling or heating cryogenic loads, such as, for example, superconducting magnets, wherein the so-called Claude process is used. The cooling is normally carried out at a temperature from ambient temperature to 5 K. The Claude process is designed for a defined cooling temperature. If cooling at another temperature level is now required, such as, for example, during the controlled cooling or heating of superconducting magnets, the flow cross-sections are largely specified within the cold-generating expansion stages. This has the result that the available compressor mass flow can be used only partially in these expansion stages. During such a time period, the installed power capacity is thus available for cold generation to only a limited extent.
  • To eliminate this problem, approaches were already implemented in which the non-usable compressor mass flow is cooled by means of an auxiliary refrigerant—usually liquid nitrogen—via additional heat exchangers and is tempered via a mixing section before it supports the cooling of the load. In this connection, however, it is disadvantageous that the use of the entire compressor mass flow is possible only by an additional consumption of auxiliary refrigerant.
  • An object of the invention is to provide a cooling unit, as well as a method for operating a cooling unit, wherein at essentially each temperature level it is possible to use the entire compressor mass flow, without having to provide an auxiliary refrigerant.
  • Upon further study of the specification and appended claims, other objects and advantages of the invention will become apparent.
  • To achieve these objects, a cooling unit is provided, which is characterized in that at least one additional expansion device is provided, whereby the latter is incorporated into the refrigeration circuit in such a way, after the load is cooled, that the refrigerant that circulates in the refrigeration circuit can be, at least temporarily, at least partially expanded in the additional expansion device to produce cold.
  • The method according to the invention for operating a cooling unit is characterized in that the compressor mass flow is divided and sent to three expansion devices during the cooling and/or heating procedure in such a way that essentially at any time, the entire compressor mass flow serves to cool the load that is to be cooled.
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • The invention is illustrated schematically with reference to an exemplary embodiment in the drawing and will be described extensively hereinafter with reference to the drawing. Various other features and attendant advantages of the present invention will be more fully appreciated as the same becomes better understood when considered in conjunction with the accompanying drawing wherein:
  • the FIGURE illustrates an exemplary embodiment of the invention.
  • The cooling unit according to the invention, the method according to the invention for operating a cooling unit, as well as other advantageous configurations of the same are explained in more detail below based on the embodiment depicted in the FIGURE.
  • The cooling unit depicted in the FIGURE has several heat exchangers HX1 to HX6, a separator D, several valves V1 to V9, as well as three expansion devices TU1 to TU3. Below, the cooling and heating procedures of a cryogenic load, which is to be cooled by means of the cooling unit according to the invention, are explained in more detail.
  • At the beginning of the cooling procedure, the temperature of the cryogenic load that is to be cooled is approximately 300 K. Via the line 1, the refrigerant, compressed to the desired circulation pressure by means of a compressor (not shown), is fed to the first heat exchanger HX1. With the regulating valve V7 opened, a partial stream of the refrigerant is fed via the line sections 1, 2 and 3 to the load that is to be cooled. The heated refrigerant is removed from the load that is to be cooled via the line 4 with the regulating valve C9 opened. After cooling in the heat exchanger HX2, the refrigerant is fed via the line sections 4′, 20 and 21 to the expansion device TU3 and expanded in the latter to produce cold.
  • Then, the expanded partial refrigerant stream flows through line sections 22, 6 and 7, passing through heat exchangers HX4 TO HX1, before being delivered to the compressor or the compressor unit of the cooling unit according to the invention.
  • A partial stream of the refrigerant that is fed to the load that is to be cooled is fed via line 13, with a regulating valve V2 opened, to the second expansion device TU2, expanded in the latter to produce cold, and then, via the line sections 14 and 15, combined with the refrigerant stream, removed from the load that is to be cooled, in line section 4′. The heat exchanger HX3 has a bypass line 12, in which a regulating valve V4 is arranged. By means of the two regulating valves V2 and V4, the inlet temperature of the expansion device TU2 can be regulated.
  • The refrigerant stream that is not fed to the expansion device TU3 is expanded to a low pressure via the line 5, in which a regulating valve V5 is arranged, and mixed into the refrigerant stream in the line 6. As return temperature (i.e., the temperature of the stream fed to the compressor) drops, the flow through the valve V5 continually decreases until it stops entirely.
  • At the same time, the first expansion device TU1 is turned on and is fed more power as return temperature drops. To this end, a portion of the compressed refrigerant stream is fed via line 10, in which a regulating valve V1 is arranged, to the expansion device TU1. After expansion in expansion device TU1, the refrigerant is combined, via line 11, with the refrigerant stream that is fed to the expansion device TU3.
  • During this cooling phase, quantitatively small partial refrigerant streams are permanently fed via the slightly opened valves V6 and V8 to the heat exchangers HX6 and HX5 in order to cool the latter simultaneously.
  • By means of the previously described procedure, the load that is to be cooled can be cooled to a temperature of approximately 100 K. In order to achieve additional cooling to a temperature of approximately 30 K, the regulating valves V7 and V9 are closed, while the regulating valves V6 and V8 are further opened.
  • The refrigerant that is to be fed to the load to be cooled is now divided into two partial streams. The first partial stream is delivered to the first expansion device TU1 and then fed, via the line sections 10, 11, 20, 15, and 40, to the load that is to be cooled. The second refrigerant stream is fed via the second expansion device TU2 and thus via the line sections 2, 13, 14 and 40 to the load that is to be cooled. During the cooling process, the mass stream that is fed to the third expansion device TU3 is successively reduced until the expansion device TU3 is fed exclusively from the expansion device TU1 that is placed upstream therefrom.
  • To implement the last stage of the cooling procedure—wherein, e.g., a cooling of the load to a temperature of approximately 5 K is performed—the third expansion device TU3 is throttled more and more as return temperature drops and is finally stopped. The compressor mass flow now flows to the load to be cooled exclusively via the two expansion devices TU1 and TU2, which now operate in parallel, but at different temperature levels. The refrigerant that flows back from the load that is to be cooled is expanded via V8 and sent to phase separator D. By the Joule-Thomson Effect that occurs at this temperature, it is cooled once more and partially liquefied. The liquefied refrigerant is guided over line section 32 through the heat exchanger HX6 and evaporated therein by countercurrent heat exchange. The vapor portion from phase separator D is delivered via line section 31 directly to the heat exchanger HX5.
  • During the heating procedure, the previously described course of the process is performed in reverse sequence.
  • As can be seen from the previously described process, the entire compressor mass flow is completely available for cooling in each phase of the cooling and heating procedure.
  • Relative to a general cooling unit, as it is described in, for example, the above-mentioned German Patent Application 102011009965, the cooling unit according to the invention has at least three additional process lines including related valves. As a result, a distribution of the remaining compressor mass flow is made possible, which makes it possible, at any point, to draw on the entire compressor mass flow for cooling the cryogenic load.
  • By means of the cooling unit according to the invention or the process of using the cooling unit, the entire compressor mass flow can now be used for cold generation. The cooling unit according to the invention thus reaches a maximum level of efficiency during the operation of the cooling and heating procedures of the cryogenic load. The previously required use of an additional auxiliary refrigerant thus becomes unnecessary.
  • The entire disclosure[s] of all applications, patents and publications, cited herein and of corresponding German Application No. DE 10 2011 013 345.3, filed Mar. 8, 2011 are incorporated by reference herein.
  • The preceding examples can be repeated with similar success by substituting the generically or specifically described reactants and/or operating conditions of this invention for those used in the preceding examples.

Claims (4)

1. A cooling unit for cooling a load, said cooling unit comprising a refrigeration circuit, which comprises:
at least one compressor which compresses the refrigerant that circulates in the refrigeration circuit,
a plurality of heat exchangers (HX1-HX6), wherein the refrigerant is cooled against itself, and
two expansion devices (TU1, TU2) that operate at different temperature levels, in which, at least temporarily, at least one partial stream of the refrigerant is expanded to produce cold, and
at least one additional expansion device (TU3) is connected to the refrigeration circuit in such a way that the refrigerant that circulates in the refrigeration circuit, after the load is cooled, can be, at least temporarily, at least partially expanded in the additional expansion device (TU3) to produce cold.
2. A method for operating a cooling unit according to claim 1, wherein, during the cooling and/or heating procedure, the compressor mass flow is divided into partial streams and sent to the three expansion devices (TU1, TU2, TU3) in such a way that essentially at any time, the entire compressor mass flow serves to cool the load that is to be cooled.
3. A method according to claim 2, wherein the cooling unit is used to cool a cryogenic load.
4. A method according to claim 3, wherein the cooling unit is used to cool a superconducting magnet.
US13/413,786 2011-03-08 2012-03-07 Cooling unit Abandoned US20120227418A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102011013345A DE102011013345A1 (en) 2011-03-08 2011-03-08 refrigeration plant
DE102011013345.3 2011-03-08

Publications (1)

Publication Number Publication Date
US20120227418A1 true US20120227418A1 (en) 2012-09-13

Family

ID=46705354

Family Applications (1)

Application Number Title Priority Date Filing Date
US13/413,786 Abandoned US20120227418A1 (en) 2011-03-08 2012-03-07 Cooling unit

Country Status (4)

Country Link
US (1) US20120227418A1 (en)
JP (1) JP6032905B2 (en)
DE (1) DE102011013345A1 (en)
FR (1) FR2972521A1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013057495A (en) * 2011-09-08 2013-03-28 Linde Ag Cold heat equipment
US20190162802A1 (en) * 2016-07-27 2019-05-30 Nippon Steel & Sumitomo Metal Corporation Bulk magnet structure and bulk magnet system for nmr

Citations (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3060699A (en) * 1959-10-01 1962-10-30 Alco Valve Co Condenser pressure regulating system
US3194025A (en) * 1963-01-14 1965-07-13 Phillips Petroleum Co Gas liquefactions by multiple expansion refrigeration
US3360955A (en) * 1965-08-23 1968-01-02 Carroll E. Witter Helium fluid refrigerator
US3371500A (en) * 1966-05-13 1968-03-05 Trane Co Refrigeration system starting
US3389565A (en) * 1964-04-29 1968-06-25 Sulzer Ag Process for liquefaction of helium by expansion
US3581511A (en) * 1969-07-15 1971-06-01 Inst Gas Technology Liquefaction of natural gas using separated pure components as refrigerants
US3611740A (en) * 1968-12-19 1971-10-12 Sulzer Ag Process for cooling a consumer consisting of a partly stabilized superconductive magnet
US3702063A (en) * 1968-11-04 1972-11-07 Linde Ag Refrigeration cycle for the aliquefaction of natural gas
US3818714A (en) * 1971-03-04 1974-06-25 Linde Ag Process for the liquefaction and subcooling of natural gas
US3878691A (en) * 1973-02-20 1975-04-22 Linde Ag Method and apparatus for the cooling of an object
US4267701A (en) * 1979-11-09 1981-05-19 Helix Technology Corporation Helium liquefaction plant
US4765813A (en) * 1987-01-07 1988-08-23 Air Products And Chemicals, Inc. Hydrogen liquefaction using a dense fluid expander and neon as a precoolant refrigerant
US5144806A (en) * 1990-05-31 1992-09-08 Linde Aktiengesellschaft Process for the liquefaction of gases
JPH0545050A (en) * 1991-08-09 1993-02-23 Nippon Sanso Kk Method for liquefying permanent gas using cryogenic cold of liquefied natural gas
US5347819A (en) * 1992-11-05 1994-09-20 Ishikawajima-Harima Heavy Industries, Co., Ltd. Method and apparatus for manufacturing superfluidity helium
US5430423A (en) * 1994-02-25 1995-07-04 General Electric Company Superconducting magnet having a retractable cryocooler sleeve assembly
US6170290B1 (en) * 1998-03-02 2001-01-09 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Refrigeration process and plant using a thermal cycle of a fluid having a low boiling point
US6748753B2 (en) * 2002-02-27 2004-06-15 Denso Corporation Air conditioner
US7409834B1 (en) * 2005-03-10 2008-08-12 Jefferson Science Associates Llc Helium process cycle
US7540171B2 (en) * 2004-11-15 2009-06-02 Mayekawa Mfg. Co., Ltd. Cryogenic liquefying/refrigerating method and system

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0686963B2 (en) * 1989-08-22 1994-11-02 超電導発電関連機器・材料技術研究組合 Device for removing hydrogen etc. in the helium freeze liquefaction system
JPH03247965A (en) * 1990-02-26 1991-11-06 Hitachi Ltd Helium refrigerating plant
JP2873388B2 (en) * 1990-05-15 1999-03-24 日本酸素株式会社 Refrigerator and method for adjusting refrigeration capacity
JPH04359760A (en) * 1991-06-04 1992-12-14 Hitachi Ltd Helium freezer
JPH06101919A (en) * 1992-09-18 1994-04-12 Hitachi Ltd Cryogenic freezing apparatus
DE102007005098A1 (en) * 2007-02-01 2008-08-07 Linde Ag Method for operating a refrigeration cycle
FR2924205B1 (en) * 2007-11-23 2013-08-16 Air Liquide CRYOGENIC REFRIGERATION DEVICE AND METHOD
JP5688784B2 (en) * 2008-07-31 2015-03-25 千代田化工建設株式会社 Heating module
DE102011009965A1 (en) 2011-02-01 2012-08-02 Linde Aktiengesellschaft Method for operating refrigeration circuit, involves temporarily varying flow rates of cooling medium so that partial streams of cooling medium are branched from main stream of cooling medium and are expanded

Patent Citations (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3060699A (en) * 1959-10-01 1962-10-30 Alco Valve Co Condenser pressure regulating system
US3194025A (en) * 1963-01-14 1965-07-13 Phillips Petroleum Co Gas liquefactions by multiple expansion refrigeration
US3389565A (en) * 1964-04-29 1968-06-25 Sulzer Ag Process for liquefaction of helium by expansion
US3360955A (en) * 1965-08-23 1968-01-02 Carroll E. Witter Helium fluid refrigerator
US3371500A (en) * 1966-05-13 1968-03-05 Trane Co Refrigeration system starting
US3702063A (en) * 1968-11-04 1972-11-07 Linde Ag Refrigeration cycle for the aliquefaction of natural gas
US3611740A (en) * 1968-12-19 1971-10-12 Sulzer Ag Process for cooling a consumer consisting of a partly stabilized superconductive magnet
US3581511A (en) * 1969-07-15 1971-06-01 Inst Gas Technology Liquefaction of natural gas using separated pure components as refrigerants
US3818714A (en) * 1971-03-04 1974-06-25 Linde Ag Process for the liquefaction and subcooling of natural gas
US3878691A (en) * 1973-02-20 1975-04-22 Linde Ag Method and apparatus for the cooling of an object
US4267701A (en) * 1979-11-09 1981-05-19 Helix Technology Corporation Helium liquefaction plant
US4765813A (en) * 1987-01-07 1988-08-23 Air Products And Chemicals, Inc. Hydrogen liquefaction using a dense fluid expander and neon as a precoolant refrigerant
US5144806A (en) * 1990-05-31 1992-09-08 Linde Aktiengesellschaft Process for the liquefaction of gases
JPH0545050A (en) * 1991-08-09 1993-02-23 Nippon Sanso Kk Method for liquefying permanent gas using cryogenic cold of liquefied natural gas
US5347819A (en) * 1992-11-05 1994-09-20 Ishikawajima-Harima Heavy Industries, Co., Ltd. Method and apparatus for manufacturing superfluidity helium
US5430423A (en) * 1994-02-25 1995-07-04 General Electric Company Superconducting magnet having a retractable cryocooler sleeve assembly
US6170290B1 (en) * 1998-03-02 2001-01-09 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Refrigeration process and plant using a thermal cycle of a fluid having a low boiling point
US6748753B2 (en) * 2002-02-27 2004-06-15 Denso Corporation Air conditioner
US7540171B2 (en) * 2004-11-15 2009-06-02 Mayekawa Mfg. Co., Ltd. Cryogenic liquefying/refrigerating method and system
US7409834B1 (en) * 2005-03-10 2008-08-12 Jefferson Science Associates Llc Helium process cycle

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013057495A (en) * 2011-09-08 2013-03-28 Linde Ag Cold heat equipment
US20190162802A1 (en) * 2016-07-27 2019-05-30 Nippon Steel & Sumitomo Metal Corporation Bulk magnet structure and bulk magnet system for nmr
US10712411B2 (en) * 2016-07-27 2020-07-14 Nippon Steel Corporation Bulk magnet structure and bulk magnet system for NMR

Also Published As

Publication number Publication date
JP2012189314A (en) 2012-10-04
DE102011013345A1 (en) 2012-09-13
JP6032905B2 (en) 2016-11-30
FR2972521A1 (en) 2012-09-14

Similar Documents

Publication Publication Date Title
US9156333B2 (en) System for the heating, ventilation, and/or air conditioning of a vehicle, comprising at least one heat exchanger through which a heat-transfer fluid flows
US11635233B2 (en) Cooling system
KR102124677B1 (en) Refrigeration and/or liquefaction device and corresponding method
EP2554411B1 (en) Refrigerating system for a vehicle and method of controlling a refrigerating system for a vehicle
CN108700349B (en) Refrigeration device comprising a plurality of storage compartments
KR101789031B1 (en) Tempering device
EP2751499B1 (en) Refrigeration system and refrigeration method providing heat recovery
EP2649387B1 (en) Refrigeration circuit
US10928107B2 (en) Method for operating a vapour compression system with heat recovery
US20120227418A1 (en) Cooling unit
CN113251681A (en) Refrigeration system with a plurality of heat absorption heat exchangers
US10895411B2 (en) Cooling system
CN114270109A (en) Cooling and/or liquefaction system and method
US11268746B2 (en) Cooling system with partly flooded low side heat exchanger
JPWO2018051409A1 (en) Refrigeration cycle device
US10767911B2 (en) Cooling system
KR101325586B1 (en) Natural gas liquefaction system
US20080184722A1 (en) Method and apparatus for a refrigeration circuit
US20180202712A1 (en) Method for cooling a process flow
JP6176905B2 (en) Refrigeration equipment
EP3564600A1 (en) Cooling system and operation method
US20190056151A1 (en) Superheat Control Scheme
WO2016096051A1 (en) Refrigeration and heating system

Legal Events

Date Code Title Description
AS Assignment

Owner name: LINDE AKTIENGESELLSCHAFT, GERMANY

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:DECKER, LUTZ;REEL/FRAME:027978/0812

Effective date: 20120323

STCB Information on status: application discontinuation

Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION