EP3551947A1 - Regenerator für kryo-kühler mit helium als arbeitsgas, ein verfahren zum herstellen eines solchen regenerators sowie einen kryo-kühler mit einem solchen regenerator - Google Patents
Regenerator für kryo-kühler mit helium als arbeitsgas, ein verfahren zum herstellen eines solchen regenerators sowie einen kryo-kühler mit einem solchen regeneratorInfo
- Publication number
- EP3551947A1 EP3551947A1 EP17832047.9A EP17832047A EP3551947A1 EP 3551947 A1 EP3551947 A1 EP 3551947A1 EP 17832047 A EP17832047 A EP 17832047A EP 3551947 A1 EP3551947 A1 EP 3551947A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- regenerator
- helium
- cell
- working gas
- cells
- 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
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
- F25B9/14—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
- F25B9/14—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
- F25B9/145—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 pulse-tube 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
- F25B2309/00—Gas cycle refrigeration machines
- F25B2309/002—Gas cycle refrigeration machines with parallel working cold producing expansion devices in one circuit
-
- 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
- F25B2309/003—Gas cycle refrigeration machines characterised by construction or composition of the regenerator
-
- 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
- F25B2309/1408—Pulse-tube cycles with pulse tube having U-turn or L-turn type geometrical arrangements
-
- 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
- F25B2309/1415—Pulse-tube cycles characterised by regenerator details
Definitions
- Regenerator for cryocooler with helium as working gas a method for producing such a regenerator and a cryocooler with such a regenerator
- the invention relates to a regenerator for cryocoolers with helium as the working gas according to claim 1, a method for producing such a regenerator according to claim 16 and 17 and provided with such a regenerator cryocooler according to claim 18.
- Fig. 12 shows the typical structure of a two-stage pulse tube refrigerator with a first cold stage 20 to about 30K and a second cold stage 22 to about 2K.
- the first cold stage 220 includes a first pulse tube 224, a first regenerator 226.
- the second cold stage 222 includes a second pulse tube 228 and a second regenerator 230 according to the present invention.
- the first cold stage 220 are about 30K and with the second cold stage 222 are reached about 4K.
- the first pulse tube 224, the first regenerator 226 and the second pulse tube 228 terminate in a connection means 232 which separates the environment from the area to be cooled.
- Working gas lines 234 supply and discharge pulsating working gas from a pump (not shown).
- the working gas lines 234 open into the first regenerator 226 and via valves 236 there is a connection to the first pulse tube 224 and the second pulse tube 228 and Baiastvolumen 238.
- the second regenerator 230 in the second cold stage 222 consists of a first regenerator section 240 and from a cryogenic temperature Regenerator section 242.
- the first regenerator section 240 consists of stacked metal screens 244 - see FIG. 13.
- the cryogenic regenerator section 242 contains rare earth connections, e.g. B. ErNi, H0CU2 and the like.
- the construction of the second regenerator 230 is shown schematically in FIG. 11. Rare earth connections are relatively expensive. Furthermore, these materials are used in the form of beads 46 (100 to several 100 microns in diameter).
- a problem here is the fixation of the balls in the oscillating flow of the working gas, since any kind of movement leads to abrasion and thus dust, which drastically reduces the life of the cryocooler.
- ball beds according to FIG. 13 cause a considerable dead volume, which does not contribute to the heat exchange and also not to the cooling capacity.
- Helium is often used as a working gas in cryogenic coolers. Helium has a comparatively high heat capacity in the temperature range from 2K to 20K, equal to the heat capacity of rare earth compounds in this temperature range. Therefore, it has been proposed to use helium as a regenerator material. From US 2012/0304668 A1, DE 10319510 A1, DE 102005007627 A1, CN 104197591 A, DE 19924184 A1 and US 4359872 A, helium-filled closed hollow bodies made of glass or metal are known as regenerator structures. This basic idea has not led to a finished product yet. In addition, beads filled with helium again lead to abrasion, which reduces the service life of the cryocooler. The basic problem of this known closed hollow body with helium is the complicated filling of the hollow body with helium under pressure. Due to the overpressure, the wall thickness of the hollow body must be increased, which leads to a deterioration of the heat transfer resistances.
- the regenerator consists in the simplest case of a hollow cell with heat-conducting cell walls.
- the outside of the cell walls defines at least in part a flow channel for the working gas helium.
- the cavity is filled with helium as a heat storage material and is connected via a pressure equalization opening with the outside of the cell.
- the working gas helium flows around the can-shaped cell, whereby on the cell walls, a heat transfer between the working gas helium takes place outside the cavity and the helium within the cavity.
- the size of the cell (s) in relation to the size of the flow channel of the working gas is chosen so that set the desired pressure differences at the lowest possible dead volume between the high pressure side and the low pressure side of the regenerator.
- the cell walls of the cell have a very small wall thickness, so that the desired heat exchange can take place.
- the ratio of the volume of the cavities or opening area or outflow resistance of the pressure compensation opening is selected so that the pressure in the cavity or in the cavities in the operating frequency range of the cooler operation (about 1 to 60 Hz) barely or at least only slightly changes. This mode of operation is similar to a capacitor at high frequencies - this gets virtually nothing of the change in voltage when the capacity is high enough and the voltage change low. In the typical application, the pressure in the cell would always fluctuate around the mean pressure of the cooling system, typically about 16 bar.
- the stable pressure is important because otherwise the volume of the cavity (s) would be a major contributor to the "dead volume” if its pressure fluctuated between 8 and 24 bars at any period without contributing to cooling
- the opening area or the outflow resistance of the pressure compensation opening is selected such that helium enters the cavity or cavities before the startup of the regenerator and during the startup phase due to the prevailing pressure conditions Pressure fluctuations in the area of the regenerator with the working frequency of a radiator. In the start-up phase, the temperature of the working gas helium and also of helium in the regenerator cavities decreases. Consequently, the volume of helium decreases and helium continues to flow into the regenerator cavities via the pressure equalization port. Ie.
- the cell is penetrated by flow channels bounded by cell walls.
- the flow channels are preferably formed as slots.
- the slit flow passages for working gas are preferably straight and parallel to each other to minimize flow resistance and to make the tubular cavities uniform between them. Due to the straightness and the parallelism results in a simple way between two flow channels an equal distance.
- a single cell possibly with a plurality of tubular structures, may take the form of a disk. have. Alternatively, multiple cells may be assembled into a disc shape. - Claim 3.
- the successive arrangement according to claim 4 increases the heat storage capacity of the regenerator.
- thermal insulation between in the flow direction of the working gas sequentially arranged cells - claim 5 - prevents heat is exchanged between the cavities in the flow direction of the working gas.
- Such a heat exchange in the flow direction of the working gas would mean a short circuit of the regenerator; a heat exchange in the flow direction of the working gas does not contribute to the function of the regenerator.
- the thickness of the thermally insulating layer is preferably between 0.1 mm and 0.5 mm.
- alignment elements By aligning elements according to claim 6 to 8, the alignment of the flow channels of cells lying on each other is simplified.
- the alignment elements are z.
- the pressure compensation opening is preferably in the form of a capillary, d. H. the cross-sectional area of the opening is very small in comparison to the surface of the hollow body - claim 9.
- the pressure equalization port may also be provided by leaks that occur in the manufacture of the cells - claim 10.
- the size and thus the permeability of the pressure compensation opening are chosen so that during a working cycle of the regenerator, the pressure change in the cell is a maximum of 20% and preferably at most 10%. This is an optimization process.
- the surfaces of the hollow bodies are provided with swirling structures.
- the cross-sectional shapes of the rohrformigen cavities according to claim 13 allow the production of the regenerator by means of 3D printing (claim 16).
- the cuboid or rectangular shape of the cross sections of the cavities is optimal for heat exchange.
- Cells with rohrformigen cavities with at least one oblique cell wall or triangular cross-section can be easily produced by 3D printing.
- structures with vertical or oblique cell walls (bevels of 45 ° or more) can be produced easily. This is most easily ensured if the triangular cross-section of the cavities has a right angle.
- flow channels are arranged between the rohrformigen cavities - claim 14.
- the disk-shaped regenerator consists of one or more disk-shaped cells and each cell comprises two half-cells
- both half-cells can be produced by means of 3D printing.
- the proportion of the volume of the cavities - and thus of the helium in the cavities - increases in the total volume of the regenerator compared to regenerators, which have only one-piece cells. This increases the heat storage capacity of the regenerator or the regenerator can be made more compact with the same heat capacity.
- 3D printing processes cuboidal cavities or ellipsoidal cavities can be produced as a whole or in two steps from two components - claim 16 or 17. According to claim 17, first a first component with "open cavities" or cup-shaped depressions is produced Recesses are then covered by second components in a second step, and the first and second components are permanently bonded together, eg by gluing or welding.
- regenerators according to the present invention are particularly suitable for in particular for Stirling, Gifford-McMahon or pulse tube coolers - claim 8.
- the hollow bodies are made of metal and / or can be made very thin due to the pressure equalization over the prior art, whereby the heat transfer resistance between the helium inside the cavities and the working gas helium outside cavities decreases.
- the cell walls of the cavities preferably have a constant thickness at least along the flow channels and are in the range between 0.1 mm and 0.5 mm. Due to the constant wall thickness of the cell walls, a uniform heat transfer is achieved between the working gas helium in the flow channels and the helium in the cavities.
- the entire regenerator preferably has a thickness of 5 mm to 100 mm in the flow direction of the working gas.
- 1 is a sectional view of a first embodiment of the regenerator in a flow channel for working gas
- 2 is a sectional view of the first embodiment along II - II in Fig. 1
- FIG. 3a and 3b a schematic representation of a second embodiment
- FIG. 4 a schematic representation of a third embodiment
- FIG. 5 a schematic representation of a fourth embodiment
- FIG. 6 a schematic representation of a fifth embodiment
- FIG. 7 shows a sixth embodiment in the form of a three-dimensional matrix arrangement with two layers of cells with an annular outer diameter
- FIGS. 9 and 10 are schematic diagrams for producing the regenerator from a shell structure and a cover according to a seventh embodiment
- FIG. 11 shows an eighth embodiment of the invention, which consists of two structures produced by means of 3D printing
- FIG. 13 shows the typical structure of a cryocooler in the form of a pulse tube refrigerator with two cold stages, wherein the second cold stage has a cryogenic regenerator, and
- FIG. 14 shows the schematic structure of a low-temperature regenerator of the prior art with rare earth in the form of beads.
- Figures 1 and 2 show a first embodiment of the regenerator 1 according to the invention in its simplest form.
- the regenerator 1 consists of a cell 2 with cell walls 4, which enclose a cavity 6.
- the cell walls 4 have an outer side 4a and an inner side 4i.
- the cell walls 4 are penetrated by a pressure equalization opening in the form of a capillary 8.
- the regenerator 1 has an annular cross section and is arranged in a tubular flow channel 10 for working gas helium.
- the interior of the cavity 6 is filled with helium as a regenerator medium or as a heat-storing medium.
- the regenerator 1 or the cell 2 is dimensioned such that an annular gap 12 remains between the tubular flow channel 10 for working gas and the outside 4a of the cell wall 4.
- the working gas helium can flow around the regenerator 1 and exchange heat with the helium in the cavity 6 via the heat-conducting cell walls 4.
- FIG. 3a and 3b show a second embodiment of the invention with a disk-shaped cell 2.
- the cell 2 differs from the cell 2 of Figures 1 and 2 in that the cell 2 according to the second embodiment of a plurality of straight in a plane extending Slits 20 is interspersed as flow channels for working gas.
- the slot-shaped flow channels 20 are parallel to each other, but end in front of the edge of the cell 2, so that the cell 2 can not fall apart.
- rectangular areas between the slot-shaped flow channels 20 are tubular cavities 6 with a rectangular cross-section. All the cavities 6 open into a peripheral channel 24 provided on the edge of the disk-shaped cell 2, so that the cavities 6 and the peripheral channel 24 form a single cavity.
- Fig. 4 shows a third embodiment of the invention in which a plurality of cells 2-1, 2-2, 2-3 are stacked one above the other.
- the three disk-shaped cells 2-i with a circular cross-section have an identical structure.
- the cells 2-i are similar to the cell 2 of the second embodiment and differ from the cell of FIGS.
- the cells 2-i are interspersed by a plurality of slots 20 running in a straight line as working gas flow channels.
- the slot-shaped flow channels 20 run parallel to one another, but end before the edge of the cells 2-i, so that the cell 2 can not fall apart.
- tubular cavities 6-i which have a cross section in the form of an equilateral triangle at right angles. The apex of the triangle with the right angle points upwards, so that the two sides of the equilateral triangle extend at an angle of 45 ° upwards. Cavities 6-i with triangular cross-section can be easily produced by means of 3D printing.
- the cavities 6-i are connected to each other at the edge of the disk-shaped cells 2-i.
- a pressure equalization port 8 connects the cavities 6-i to the area outside the cells 2-i.
- the cells 2-i have a plurality of alignment pins 30 on their upper side and corresponding alignment recesses 32 are arranged on the opposite side.
- these alignment elements 30, 32 it is achieved that the slit-shaped flow channels 20 of the superimposed cells 6-i are aligned with one another, so that through the regenerator continuous flow channels result.
- a thermally insulating layer 34 is arranged, which is penetrated by the alignment pin 30, so that the alignment pins can engage in the overlying cht apertures 32.
- FIG. 5 shows schematically a fourth embodiment of the regenerator in the form of a disc-shaped cell 2, which differs from the cells 2-i of Fig. 4, characterized in that instead of a tubular cavity with triangular cross-section two tubular cavities 6a and 6b are provided.
- the cross section of the tubular cavities 6a and 6b also has the shape of an equilateral triangle at right angles. The right angle is applied to the inside of the partition 4, which limits the slot-shaped flow channels. This results in a partition wall 4 with a constant wall thickness between the flow channels 20 and the cavities 6-i. This leads to an improved heat transfer between the working gas in the flow channel 20 and the helium in the cavities 6a and 6b.
- the pressure equalization opening 8 connects the cavities 6a, 6b with the area outside the cell 2.
- Fig. 6 shows a fifth embodiment of the invention, which differs from the embodiment of Figure 4 only in that the tubular cavities 6a, 6b are arranged with triangular cross-section with the base of the right triangle to the flow channels 20. Since the base is the length of the side of the equilateral triangle, this improves the heat transfer.
- FIG. 7 shows a regenerator 101 having a plurality of cells 102 arranged in the form of a 3-dimensional matrix 103 with two layers of cells 102.
- the cells 102 are cube-shaped and fundamentally identical in construction. However, since the regenerator 101 fills a tube cross-section, the cells 102 forcibly have a different shape in the edge region.
- the individual cells 102 each comprise a cube-shaped cavity 106 with a heat-conducting sleeve 104 and a pressure compensation opening 108 in the form of a capillary. As can be seen from Fig. 8, the individual cells 102 are arranged one behind the other in the flow direction 1 12 of the working gas.
- the adjacent cells 102 are connected to each other by means of thermally conductive connecting elements 1 14.
- the in the flow direction 1 12 consecutive cells 102 are connected to each other with thermally insulating or poorly conductive connecting elements 1 16 and form a flow channel 120.
- the mechanically fixed matrix assembly 103 of cells 102 In Fig. 7 are only two layers shown by cells 102, while in Fig. 8, three layers of cells 102 are shown.
- the gas volume of the individual cavities 106 is about 1 mm 2
- the wall thickness of the shell 104 is about 0.2 mm.
- the distance between the individual cells 102 is about 0.2 mm.
- the total footprint of a cell 102 is about 8mm 3 .
- the regenerator 101 according to the invention is preferably used in the coldest cold stage of a cryocooler as a low-temperature regenerator section 242.
- Figures 9 and 10 show seventh embodiment of the invention, in which the cell 2 with slit-shaped flow channels 20 according to the embodiments of Figures 3 to 6.
- the difference from the embodiments of Figures 4 to 6 is in the form of the tubular cavities 6 '.
- the cavities 6 ' are rectangular as in the second embodiment of Fig. 3a and 3b in cross section.
- the production takes place - in contrast to the second embodiment in two steps with at least two components.
- a first component 40 with "open cavities” or with cup-shaped depressions 42 is produced, for example by means of 3D printing, 3D printed loose material is removed from the cup-shaped depressions in a second step in a third step covered by second components 44.
- the first and second components 40, 44 are permanently joined together, eg by gluing or welding.
- Fig. 1 shows an eighth embodiment of the invention in the form of a disc-shaped cell 2, which is composed of a first and a second half-cell 50, 52, so that a cell 2 results analogous to the embodiments of FIGS. 5 and 6 between the slot-shaped flow channels 20 has structures in cross-section cuboid structures.
- Both half-cells 50, 52 each have a plurality of first and second cavities 54 and 56 with a cross-section of an equilateral triangle.
- the two half-cells 50, 52 can be produced by means of 3D printing.
- the two half-cells each have a flat side 58 and an uneven side 60.
- the two uneven sides 60 have a complementary shape and when the two half-cells 50, 52 are assembled, the complementary uneven sides 60 of the two half-cells lie on each other.
- the regenerators with cells 2 which increases in each case two half-cells 50, 52 have the proportion of the void volume in the total volume of the regenerator. The regenerator thus becomes more efficient.
- the embodiments according to FIGS. 4 to 6 and 9 to 1 1 also have a circumferential channel 24.
- the pressure compensation opening 8 is not shown in FIGS. 2 to 6 and 9 to 11, but is present. Since the cavities 6-i; 6 ', 6a, 6b are interconnected, the pressure equalization opening 8 may be provided at any point of the cells 2.
- Figures 12a, 12b and 12c show possible further cross-sectional shapes of the cavities 6 in the disk-shaped regenerators of Figures 3 to 6 and 1 1, which can be easily produced by means of 3D printing.
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Compressors, Vaccum Pumps And Other Relevant Systems (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Separation By Low-Temperature Treatments (AREA)
Abstract
Description
Claims
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE202016106860.6U DE202016106860U1 (de) | 2016-12-08 | 2016-12-08 | Regenerator für Kryo-Kühler mit Helium als Arbeitsgas |
| DE102017203506.4A DE102017203506A1 (de) | 2016-12-08 | 2017-03-03 | Regenerator für Kryo-Kühler mit Helium als Arbeitsgas, ein Verfahren zum Herstellen eines solchen Regenerators sowie einen Kryo-Kühler mit einem solchen Regenerator |
| PCT/EP2017/081750 WO2018104410A1 (de) | 2016-12-08 | 2017-12-06 | Regenerator für kryo-kühler mit helium als arbeitsgas, ein verfahren zum herstellen eines solchen regenerators sowie einen kryo-kühler mit einem solchen regenerator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EP3551947A1 true EP3551947A1 (de) | 2019-10-16 |
| EP3551947B1 EP3551947B1 (de) | 2022-09-14 |
Family
ID=61765518
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP17832047.9A Active EP3551947B1 (de) | 2016-12-08 | 2017-12-06 | Regenerator für kryo-kühler mit helium als arbeitsgas, ein verfahren zum herstellen eines solchen regenerators sowie einen kryo-kühler mit einem solchen regenerator |
Country Status (6)
| Country | Link |
|---|---|
| US (1) | US11333406B2 (de) |
| EP (1) | EP3551947B1 (de) |
| JP (2) | JP2019536972A (de) |
| CN (1) | CN110050161B (de) |
| DE (2) | DE202016106860U1 (de) |
| WO (1) | WO2018104410A1 (de) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116358323A (zh) * | 2023-05-06 | 2023-06-30 | 中国科学院理化技术研究所 | 高压氦气换热系统、换热方法及回热式热机系统 |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10041747B2 (en) * | 2010-09-22 | 2018-08-07 | Raytheon Company | Heat exchanger with a glass body |
| FR3090840B1 (fr) * | 2018-12-20 | 2021-01-08 | Univ Franche Comte | Régénérateur et procédé de fabrication d’un tel régénérateur |
| DE202021100084U1 (de) | 2021-01-11 | 2022-04-12 | Pressure Wave Systems Gmbh | Regenerator für Kryo-Kühler mit Helium als Arbeitsgas und als Wärmespeichermaterial sowie einen Kryo-Kühler mit einem solchen Regenerator |
Family Cites Families (18)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4359872A (en) * | 1981-09-15 | 1982-11-23 | North American Philips Corporation | Low temperature regenerators for cryogenic coolers |
| JPS62233688A (ja) * | 1986-03-31 | 1987-10-14 | Aisin Seiki Co Ltd | 蓄熱器 |
| JP2558810B2 (ja) * | 1988-05-14 | 1996-11-27 | 住友電気工業株式会社 | 焼結中空部品の製造方法 |
| JP2697470B2 (ja) * | 1992-04-08 | 1998-01-14 | ダイキン工業株式会社 | 再生器及びその製造方法 |
| EP0637727A3 (de) * | 1993-08-05 | 1997-11-26 | Corning Incorporated | Kreuzstromwärmetauscher und Herstellungsverfahren |
| DE4401246A1 (de) * | 1994-01-18 | 1995-07-20 | Bosch Gmbh Robert | Regenerator |
| JPH07318181A (ja) * | 1994-05-20 | 1995-12-08 | Daikin Ind Ltd | 極低温冷凍機 |
| US6131644A (en) * | 1998-03-31 | 2000-10-17 | Advanced Mobile Telecommunication Technology Inc. | Heat exchanger and method of producing the same |
| DE19924184A1 (de) * | 1999-05-27 | 2000-11-30 | Christoph Heiden | Vorrichtung zur Nutzung der spezifischen Wärme von Helium-Gas in Regeneratoren von Tieftemperaturgaskältemaschinen |
| DE10318510A1 (de) * | 2003-04-24 | 2004-11-11 | Leybold Vakuum Gmbh | Wärmespeichermittel |
| DE10319510B4 (de) | 2003-04-30 | 2016-12-29 | Zumtobel Lighting Gmbh | Stromschienensystem für Leuchten und Verriegelungselement zur Verwendung in einem Stromschienensystem |
| DE102005007627A1 (de) * | 2004-02-19 | 2005-09-15 | Siemens Ag | Regenerator für einen kryogenen Refrigerator |
| JP5468424B2 (ja) * | 2010-03-12 | 2014-04-09 | 住友重機械工業株式会社 | 蓄冷器、蓄冷式冷凍機、クライオポンプ、および冷凍装置 |
| WO2011115200A1 (ja) * | 2010-03-19 | 2011-09-22 | 住友重機械工業株式会社 | 蓄冷器、gm冷凍機およびパルスチューブ冷凍機 |
| WO2012065245A1 (en) * | 2010-11-18 | 2012-05-24 | Etalim Inc. | Stirling cycle transducer apparatus |
| JP5790989B2 (ja) * | 2011-05-10 | 2015-10-07 | 独立行政法人国立高等専門学校機構 | 蓄冷器 |
| CN104197591B (zh) * | 2014-08-29 | 2016-11-30 | 浙江大学 | 采用氦气作为回热介质的深低温回热器及其脉管制冷机 |
| JP6185954B2 (ja) * | 2015-03-31 | 2017-08-23 | ミネベアミツミ株式会社 | 球面すべり軸受及びその製造方法 |
-
2016
- 2016-12-08 DE DE202016106860.6U patent/DE202016106860U1/de not_active Expired - Lifetime
-
2017
- 2017-03-03 DE DE102017203506.4A patent/DE102017203506A1/de active Pending
- 2017-12-06 JP JP2019526323A patent/JP2019536972A/ja active Pending
- 2017-12-06 CN CN201780074908.9A patent/CN110050161B/zh active Active
- 2017-12-06 WO PCT/EP2017/081750 patent/WO2018104410A1/de not_active Ceased
- 2017-12-06 EP EP17832047.9A patent/EP3551947B1/de active Active
-
2019
- 2019-06-08 US US16/435,477 patent/US11333406B2/en active Active
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2022
- 2022-03-31 JP JP2022057805A patent/JP2022084912A/ja active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116358323A (zh) * | 2023-05-06 | 2023-06-30 | 中国科学院理化技术研究所 | 高压氦气换热系统、换热方法及回热式热机系统 |
Also Published As
| Publication number | Publication date |
|---|---|
| CN110050161A (zh) | 2019-07-23 |
| JP2019536972A (ja) | 2019-12-19 |
| US20190323737A1 (en) | 2019-10-24 |
| DE202016106860U1 (de) | 2018-03-09 |
| US20220057114A9 (en) | 2022-02-24 |
| EP3551947B1 (de) | 2022-09-14 |
| DE102017203506A1 (de) | 2018-06-14 |
| US11333406B2 (en) | 2022-05-17 |
| CN110050161B (zh) | 2021-06-04 |
| JP2022084912A (ja) | 2022-06-07 |
| WO2018104410A1 (de) | 2018-06-14 |
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