EP0327457A1 - Verfahren und Einrichtung zur Tiefsttemperaturerzeugung - Google Patents
Verfahren und Einrichtung zur Tiefsttemperaturerzeugung Download PDFInfo
- Publication number
- EP0327457A1 EP0327457A1 EP89400289A EP89400289A EP0327457A1 EP 0327457 A1 EP0327457 A1 EP 0327457A1 EP 89400289 A EP89400289 A EP 89400289A EP 89400289 A EP89400289 A EP 89400289A EP 0327457 A1 EP0327457 A1 EP 0327457A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- mixing box
- solution
- liquid
- isotope
- phase
- 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.)
- Granted
Links
Images
Classifications
-
- 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
- F25B9/12—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point using 3He-4He dilution
Definitions
- the present invention relates to a process and an apparatus for obtaining very low temperatures.
- the mixing box is associated with a column filled with equilibrium solution, and at the top of which is placed an evaporator which makes it possible to extract 3He from the solution.
- a concentration gradient is created in the column, and 3He migrates from the mixing box to the evaporator, which leads to the dissolution of pure 3He and the cooling of the mixing box.
- a cryostat could be operated in an analogous manner in which the mixing box contains a solution phase and a pure 4He phase.
- the object of the invention is to make it possible to overcome these constraints by producing a cryostat comprising neither a distiller nor a low pressure pumping line.
- the invention provides a process for obtaining very low temperatures by which, in a mixing box placed in a vacuum enclosure cooled to a temperature of the order of 2 ° K or lower, a two-phase system comprising a 3He solution phase in 4He liquid, and a liquid phase formed from the pure 3He isotope, this isotope is passed into the solution phase, the dissolving energy being borrowed from the can mixture to cool it, 3He is extracted from the mixing box in the form of a solution and a quantity of said 3He in the form of pure liquid is introduced into the mixing box equal to the amount of this isotope which leaves the box.
- this process having the particularity that the two-phase system is created by continuously feeding the mixing box with 4He and 3He liquids introduced separately, in that the solution phase is extracted under conditions of speed suchthat the 3He it contains cannot diffuse against the current in the solution sufficiently to significantly increase the 3He content of the liquid 4He introduced and reduce the dissolution, in this 4He, of the liquid 3He introduced simultaneously.
- the process of the invention has notable differences from the prior art. In both cases, it is sought to have a 4He with a low content of 3He, and in which the liquid 3He introduced can dissolve easily with production of cold.
- the 3He content is lowered by diffusing it through the solution towards an evaporator.
- the solution is extracted at a speed such that 3He cannot go back to raise the 3He content of 4He and therefore make it less capable of dissolving the liquid 3He.
- the discharge pipe of a cryostat according to the present invention will preferably be narrow, and the circulation speed relatively high.
- a heat exchanger 5 is constituted by three capillaries 2A, 3A, 4A made of CuNi of 0.1 mm inside diameter and 0.5 mm outside diameter, welded together over their entire length with tin and connected with a part to capillaries 2 to 4, and secondly to the mixing box.
- thermometer 7 consisting of a germanium resistor, is screwed to the outside of this box.
- the first consists of a conventional cryostat which by pumping a 4He bath allows a temperature close to 1.8 ° K to be obtained.
- a vacuum chamber 1 containing the cold part of the cryostat previously described.
- the two pure helium isotopes are injected in the form of gas into the cryostat at a flow rate controlled by two flow regulators. These gases are liquefied using exchangers in the main helium bath before being sent to cold chamber 1.
- the second device is a rotating cryostat operating by continuous circulation of 4He from a fixed tank.
- the rotation is obtained using a horizontal rotary connector on the 4He liquid supply line.
- This cryostat makes it possible to cool an exchanger to a temperature close to 1.6 ° K by pumping the 4He and using a cold expansion valve.
- On this exchanger is fixed the enclosure 1 containing the mixing chamber.
- the two helium isotopes are injected in gaseous form then cooled and liquefied in the helium vapors of the main circulation.
- cryostat is insensitive to gravity (no liquid-gas phase separation surface)
- the only connections with the outside are made by three capillaries less than a millimeter in diameter.
- such a system can be mounted on a support that can be oriented in all directions.
- 3He it is necessary to use in this case an auxiliary distillation unit as described above.
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Separation By Low-Temperature Treatments (AREA)
- Chemical Vapour Deposition (AREA)
- Mixers With Rotating Receptacles And Mixers With Vibration Mechanisms (AREA)
- Thermotherapy And Cooling Therapy Devices (AREA)
- Crystals, And After-Treatments Of Crystals (AREA)
- Diaphragms For Electromechanical Transducers (AREA)
- General Induction Heating (AREA)
- Investigating Or Analyzing Materials Using Thermal Means (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT89400289T ATE73920T1 (de) | 1988-02-03 | 1989-02-02 | Verfahren und einrichtung zur tiefsttemperaturerzeugung. |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR8801232 | 1988-02-02 | ||
FR8801232A FR2626658B1 (fr) | 1988-02-03 | 1988-02-03 | Procede et appareillage pour l'obtention de tres basses temperatures |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0327457A1 true EP0327457A1 (de) | 1989-08-09 |
EP0327457B1 EP0327457B1 (de) | 1992-03-18 |
Family
ID=9362892
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP89400289A Expired - Lifetime EP0327457B1 (de) | 1988-02-03 | 1989-02-02 | Verfahren und Einrichtung zur Tiefsttemperaturerzeugung |
Country Status (8)
Country | Link |
---|---|
US (1) | US4991401A (de) |
EP (1) | EP0327457B1 (de) |
AT (1) | ATE73920T1 (de) |
DE (1) | DE68900992D1 (de) |
ES (1) | ES2031366T3 (de) |
FR (1) | FR2626658B1 (de) |
GR (1) | GR3004121T3 (de) |
WO (1) | WO1993014357A1 (de) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2707375A1 (fr) * | 1993-07-05 | 1995-01-13 | Centre Nat Etd Spatiales | Procédé d'obtention de très basses températures. |
WO2010012939A1 (fr) * | 2008-07-31 | 2010-02-04 | L'air Liquide Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Réfrigérateur et procédé de production de froid à très basse température |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3195322A (en) * | 1961-09-22 | 1965-07-20 | Atomic Energy Authority Uk | Refrigerator employing helium |
FR2010177A1 (de) * | 1968-06-05 | 1970-02-13 | Philips Nv | |
FR2176809A1 (de) * | 1972-03-18 | 1973-11-02 | Philips Nv | |
EP0089391A1 (de) * | 1982-03-23 | 1983-09-28 | International Business Machines Corporation | Verfahren und Verdünnungskältemaschine zum Kühlen bei Temperaturen unter 1 K |
EP0188976A1 (de) * | 1984-12-17 | 1986-07-30 | Centre National De La Recherche Scientifique (Cnrs) | Mischkryostat |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2262267B1 (de) * | 1974-02-22 | 1976-12-03 | Commissariat Energie Atomique | |
NL7504835A (nl) * | 1975-04-24 | 1976-10-26 | Philips Nv | 3he-4he verdunnings koelmachine. |
NL7902014A (nl) * | 1979-03-14 | 1980-09-16 | Philips Nv | 3he-4he verdunningskoelmachine. |
NL7902438A (nl) * | 1979-03-29 | 1980-10-01 | Philips Nv | 3he-4he koelmachine. |
US4770006A (en) * | 1987-05-01 | 1988-09-13 | Arch Development Corp. | Helium dilution refrigeration system |
-
1988
- 1988-02-03 FR FR8801232A patent/FR2626658B1/fr not_active Expired - Lifetime
-
1989
- 1989-02-02 AT AT89400289T patent/ATE73920T1/de not_active IP Right Cessation
- 1989-02-02 WO PCT/FR1989/000034 patent/WO1993014357A1/fr unknown
- 1989-02-02 US US07/423,441 patent/US4991401A/en not_active Expired - Lifetime
- 1989-02-02 EP EP89400289A patent/EP0327457B1/de not_active Expired - Lifetime
- 1989-02-02 DE DE8989400289T patent/DE68900992D1/de not_active Expired - Lifetime
- 1989-02-02 ES ES198989400289T patent/ES2031366T3/es not_active Expired - Lifetime
-
1992
- 1992-03-23 GR GR910402241T patent/GR3004121T3/el unknown
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3195322A (en) * | 1961-09-22 | 1965-07-20 | Atomic Energy Authority Uk | Refrigerator employing helium |
FR2010177A1 (de) * | 1968-06-05 | 1970-02-13 | Philips Nv | |
FR2176809A1 (de) * | 1972-03-18 | 1973-11-02 | Philips Nv | |
EP0089391A1 (de) * | 1982-03-23 | 1983-09-28 | International Business Machines Corporation | Verfahren und Verdünnungskältemaschine zum Kühlen bei Temperaturen unter 1 K |
EP0188976A1 (de) * | 1984-12-17 | 1986-07-30 | Centre National De La Recherche Scientifique (Cnrs) | Mischkryostat |
Non-Patent Citations (3)
Title |
---|
CRYOGENICS, vol. 20, no. 3, mars 1980, pages 115-121, IPC Business Press; A.P. SEVERIJNS: "A novel He3 - He4 dilution refrigerator with superfluid He4 circulation" * |
CRYOGENICS, vol. 20, no. 3, mars 1980, pages 153-157, IPC Business Press; W. VAN HAERINGEN: "On the choice of tube lenghts and diameters in a He3 - He4 dilution refrigeration system" * |
PHYSICS LETTERS, vol. 53A, no. 4, 30 juin 1975, pages 327-328; F.A. STAAS et al.: "A dilution refrigerator with superfluid injection" * |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2707375A1 (fr) * | 1993-07-05 | 1995-01-13 | Centre Nat Etd Spatiales | Procédé d'obtention de très basses températures. |
WO1995002158A1 (fr) * | 1993-07-05 | 1995-01-19 | Centre National D'etudes Spatiales | Procede d'obtention de tres basses temperatures |
WO2010012939A1 (fr) * | 2008-07-31 | 2010-02-04 | L'air Liquide Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Réfrigérateur et procédé de production de froid à très basse température |
FR2934674A1 (fr) * | 2008-07-31 | 2010-02-05 | Air Liquide | Refrigerateur et procede de production de froid a tres basse temperature |
Also Published As
Publication number | Publication date |
---|---|
FR2626658B1 (fr) | 1990-07-20 |
DE68900992D1 (de) | 1992-04-23 |
EP0327457B1 (de) | 1992-03-18 |
ES2031366T3 (es) | 1992-12-01 |
GR3004121T3 (de) | 1993-03-31 |
US4991401A (en) | 1991-02-12 |
WO1993014357A1 (fr) | 1993-07-22 |
ATE73920T1 (de) | 1992-04-15 |
FR2626658A1 (fr) | 1989-08-04 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0628778B1 (de) | Verfahren und Hochdruckgasversorgungseinheit für eine ein Luftbestandteil verbrauchende Anlage | |
EP0605262B1 (de) | Druckgassauerstoffherstellungsverfahren und Apparat | |
EP0940624A1 (de) | Station und Verfahren zur Verteilung von Gas | |
FR2807504A1 (fr) | Colonne pour separation cryogenique de melanges gazeux et procede de separation cryogenique d'un melange contenant de l'hydrogene et du co utilisant cette colonne | |
EP0188976B1 (de) | Mischkryostat | |
EP0968387B1 (de) | Verfahren und vorrichtung zum füllen eines druckbehälters | |
EP0327457B1 (de) | Verfahren und Einrichtung zur Tiefsttemperaturerzeugung | |
EP2307823B1 (de) | Kältevorrichtung und verfahren zur erzeugung von kälte mit sehr niedrigen temperaturen | |
FR2673707A1 (fr) | Appareil de production d'hydrogene incluant de l'hydrogene solide et de l'hydrogene liquide coexistant l'un avec l'autre. | |
EP1078212B1 (de) | Luftzerlegungsanlage und deren kühlbox | |
FR2489843A1 (fr) | Procede et appareil pour fabriquer un verre modifie amorphe | |
FR2981442A1 (fr) | Dispositif d'alimentation en gaz froids et installation rmn comprenant un tel dispositif | |
EP0732556B1 (de) | Verfahren und Vorrichtung zur Verdampfung eines Flüssigkeitstromes | |
EP0706632B1 (de) | Verfahren zur tiefsttemperaturerzeugung | |
EP0592323B1 (de) | Verfahren und Einrichtung zur Herstellung von extrem reinem Stickstoff unter Druck | |
EP0699884A1 (de) | Sauerstoffherstellungsverfahren und Einrichtung durch kryogene Destillation | |
FR2558735A1 (fr) | Cryopiege | |
FR2719039A1 (fr) | Nouveau procédé de déshydratation d'alcool par adsorption/regénération sur tamis moléculaire, et installation pour sa mise en Óoeuvre. | |
EP0015626B1 (de) | Verfahren und Vorrichtung zur Herstellung von Natriumbikarbonatkristallen | |
FR2853723A1 (fr) | Procede et installation de traitement d'un bain de liquide riche en oxygene recueilli en pied d'une colonne de distillation cryogenique | |
FR2751060A1 (fr) | Procede et installation de distillation cryogenique d'un melange gazeux | |
CA2168944A1 (fr) | Echangeur de chaleur diphasique a temperature controlee | |
FR3147620A1 (fr) | Procédé et installation de vaporisation du CO2 liquide et de fourniture de CO2 gazeux à un poste utilisateur | |
BE431074A (de) | ||
BE366521A (de) |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AT BE CH DE ES FR GB GR IT LI LU NL SE |
|
17P | Request for examination filed |
Effective date: 19891031 |
|
17Q | First examination report despatched |
Effective date: 19900711 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AT BE CH DE ES FR GB GR IT LI LU NL SE |
|
REF | Corresponds to: |
Ref document number: 73920 Country of ref document: AT Date of ref document: 19920415 Kind code of ref document: T |
|
REF | Corresponds to: |
Ref document number: 68900992 Country of ref document: DE Date of ref document: 19920423 |
|
ITF | It: translation for a ep patent filed | ||
GBT | Gb: translation of ep patent filed (gb section 77(6)(a)/1977) | ||
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FG2A Ref document number: 2031366 Country of ref document: ES Kind code of ref document: T3 |
|
REG | Reference to a national code |
Ref country code: GR Ref legal event code: FG4A Free format text: 3004121 |
|
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
26N | No opposition filed | ||
EPTA | Lu: last paid annual fee | ||
EAL | Se: european patent in force in sweden |
Ref document number: 89400289.8 |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: IF02 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: LU Payment date: 20030116 Year of fee payment: 15 Ref country code: AT Payment date: 20030116 Year of fee payment: 15 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: NL Payment date: 20030117 Year of fee payment: 15 Ref country code: SE Payment date: 20030117 Year of fee payment: 15 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GB Payment date: 20030128 Year of fee payment: 15 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: ES Payment date: 20030217 Year of fee payment: 15 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: CH Payment date: 20030224 Year of fee payment: 15 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 20030227 Year of fee payment: 15 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GR Payment date: 20030228 Year of fee payment: 15 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: BE Payment date: 20030305 Year of fee payment: 15 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: AT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20040202 Ref country code: GB Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20040202 Ref country code: LU Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20040202 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: ES Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20040203 Ref country code: SE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20040203 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: BE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20040228 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LI Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20040229 Ref country code: CH Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20040229 |
|
BERE | Be: lapsed |
Owner name: CENTRE NATIONAL D'ETUDES *SPATIALES Effective date: 20040228 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20040901 Ref country code: NL Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20040901 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GR Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20040903 |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee |
Effective date: 20040202 |
|
EUG | Se: european patent has lapsed | ||
REG | Reference to a national code |
Ref country code: CH Ref legal event code: PL |
|
NLV4 | Nl: lapsed or anulled due to non-payment of the annual fee |
Effective date: 20040901 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES;WARNING: LAPSES OF ITALIAN PATENTS WITH EFFECTIVE DATE BEFORE 2007 MAY HAVE OCCURRED AT ANY TIME BEFORE 2007. THE CORRECT EFFECTIVE DATE MAY BE DIFFERENT FROM THE ONE RECORDED. Effective date: 20050202 |
|
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FD2A Effective date: 20040203 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: FR Payment date: 20080229 Year of fee payment: 20 |