US3794110A - Heat exchanger and method of manufacturing the same - Google Patents
Heat exchanger and method of manufacturing the same Download PDFInfo
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- US3794110A US3794110A US00253360A US3794110DA US3794110A US 3794110 A US3794110 A US 3794110A US 00253360 A US00253360 A US 00253360A US 3794110D A US3794110D A US 3794110DA US 3794110 A US3794110 A US 3794110A
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- mass
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- block
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F7/00—Elements not covered by group F28F1/00, F28F3/00 or F28F5/00
- F28F7/02—Blocks traversed by passages for heat-exchange media
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
- F28F1/40—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only inside the tubular element
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
- F28F13/003—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by using permeable mass, perforated or porous materials
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2255/00—Heat exchanger elements made of materials having special features or resulting from particular manufacturing processes
- F28F2255/18—Heat exchanger elements made of materials having special features or resulting from particular manufacturing processes sintered
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S165/00—Heat exchange
- Y10S165/355—Heat exchange having separate flow passage for two distinct fluids
- Y10S165/395—Monolithic core having flow passages for two different fluids, e.g. one- piece ceramic
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T29/00—Metal working
- Y10T29/49—Method of mechanical manufacture
- Y10T29/4935—Heat exchanger or boiler making
Definitions
- R her, the mass consisting of particles of readily heat- 62/6, 138/38 conducting material sintered together with a layer of a [5 i I readily heat conducting material provided on an Outer [58] Fleld of Search-M 165N641 179; circumferential surface of the mass, and a soldered 29/1573; 62/6; 138/38 joint provided between the layer and the inner wall of the chamber in at least one zone extending throughout References Clted the circumference of the filling mass.
- the invention relates to a heat exchanger which is particularly suitable for use in the temperature range below 2 K and comprises a readily heat-conducting block of material having at least one chamber containing at least one gas-permeable filler of particles ofa likewise readily heat-conducting material which are sintered together, preferably the same material as that of the block, each of the chambers comprising at their oppositely located ends, connections with which they can be incorporated in ducts through which flows of helium can be conducted which exchange heat with each other.
- Heat exchangers of the type described are known. They are used, for example, in cooling devices in which He or a mixture of He and He circulates as a working medium between a cooled place (cooler) and a place to be cooled. Such cooling devices are described in Dutch Pat. application No. 6,807,902 and in U.S. Pat. No. 3,376,712. In these cooling devices the temperature of the place to be cooled lies below 1 K. In these devices it is desirable to cool the flow of medium flowing to the place to be cooled in the counter-current heat exchange with medium flowing away from the place to be cooled. For this purpose heat exchangers are used having a construction as described above, in which the filling mass is formed by sintered copper balls having a diameter of approximately 40 am and the surrounding block of material alsoconsists of copper.
- the very fine copper balls give a very large heatexchangingjsurface area with the circulating helium so that a good heat transfer is ensured between helium and the filling mass.
- cracks nearly always occur in the filling mass after sintering in the chamber, and furthermore the resistance to flow increases which disturbsthe satisfactory operation.
- the heatexcha'nger according to the invention is characterized in that the filling mass comprises at its circumferential surface a layer of a readily heat-conducting material provided thereon, preferably the same material as that of the'fillin'g mass and the block of material, andis incorporated so as to fit in the relative chamber, a soldered jointbein'g'provided between the layer of material and the wall of the relative chamber in at least one zone extending throughout the circumference of the filling mass.
- all the components of the heat exchanger are preferably manufactured from the same material.
- the advantage of this is that the thermal expansion and the shrinkage, respectively, is the same for all the components so that few thermal stresses occur.
- Copper is a very suitable material for this purpose.
- the layer of material is provided on the filling mass electrolytically.
- the invention furthermore relates to a method of manufacturing the above-described heat exchanger. It is characterized in that a rod of sintered material is turned down to a diameter which is smaller by approximately 1 mm than that of a chamber in a block of a readily heat-conducting material, after which the rod is provided electrolytically with a layer of readily conducting material, the ends of the rod being then liberated from the deposited layer of material, the rod being then rinsed to remote acid and salt, the rod being turned down to such a diameter that the filling mass sawn at the desirable length fits in the chamber, at least one annular groove being provided in the wall of the chamber prior to placing the filling mass, a soldering ring being provided in said groove the assembly being heated to above the melting temperature of the solder after placing the filling mass, the open side of the chamber being then sealed by soldering a cover.
- This heat exchanger comprises a copper block 1 in which two chambers 2 and 3 are recessed. In each of these chambers, filling masses 4 and 5, respectively, of sintered copper balls are accommodated, said filling masses comprising at their circumferential surface electrolytically grown layers 6 and 7, respectively, of copper.
- the layers 6 and 7, respectively, are soldered to the copper block 1, at the points 8,9 and 10,11, respectively.
- Pipes l2 and 13 soldered in an aperture in the block 1, communicate with the lower side of the chambers 2, 3 while the upper side of the chambers 2 and 3 is sealed by soldered covers 14 and 15, respectively, in each of which a pipe 16 and 17, respectively is soldered.
- pipes 12 and 16 (and also pipes 13 and 17) each constitute a pair of inlet-outlet means with a flow path defined between them.
- This heat exchanger is manufactured as follows:
- a rod of sintered copper balls is first turned down to a diameter which is smaller by approximately 1 mm than that of the chambers 2 and 3.
- a layer of copper, slightly more than 0.5 mm thick, is deposited electrolytically on said rod.
- the deposited layer is removed and the rod is then rinsed with alkali so as to remove the acid residues.
- it is rinsed with warm water so as to remove the formed salts, after which it is fired in a vacuum.
- Pieces which correspond to the dimensions of the filling masses 4 and 5 are then cut from said rod. Said filling masses are turned down to such a diameter as to fit in the chambers 2 and 3.
- annular grooves are provided in the wall of the chambers 2 and 3, in which grooves, rings of soldering material are laid, these rings as shown having thickness, t, substantially less than the length, L, of the filling mass in the direction of the flow path between the inlet and outlet pipes.
- the filling masses 4 and 5 are then placed in the chambers. Heating to above the melting temperature of the solder is then carried out so that the soldered joints are obtained at the points 8, 9 and 10, 11 respectively. Simultaneously with this soldering operation the pipes 12 and 13 can be soldered in the block 1.
- the covers 14 and 15 with the pipes 16 and 17 are then soldered on the block 1.
- a heat exchanger for use in a temperature range below 2 K comprising, a block of readily-heatconducting material, the block having at least one internal chamber defining inner walls, the chamber further having inlet and outlet means thus defining a flow path through said chamber, a gas-permeable filling mass having an outer surface and formed of sintered particles of a readily-heat-conducting material, a layer of readily-heat-conducting material deposited on said outer surface of the filling mass, said mass disposed within said flow path and constituting a partition of predetermined length between the inlet and the outlet, with said layer on said mass being in direct heat exchange contact with said inner walls of the chamber, and a soldered junction between said chamber walls and said layer on said filling mass, the junction defining a circumferential zone of smaller thickness in the flow path direction than said length of the mass, sealing said mass to said chamber walls such that the inlet and outlet can communicate only through said mass.
- a heat exchanger comprising a copper block having at least one internal chamber defining inner walls, and spaced apart inlet and outlet ducts thus defining a flow path through the chamber, a gas-permeable filling mass defining an outer surface, the mass formed of sintered copper particles, a layer of electrolytically deposited copper on said outer surface of said filling mass, said mass disposed within said flow path and constituting a partition between the inlet and the outlet with said layer on said mass being in direct heat exchange contact with said inner walls of the chamber, and a copper solder junction between said chamber walls and said layer on said filling mass the junction defining a circumferential annular zone sealing said mass to said chamber walls such that the inlet and outlet can communicate only through said mass.
- solder junction defines an annular ring defining a plane generally transverse to said flow path.
Abstract
A heat exchanger comprising a readily heat-conducting block of material having at least one chamber, a gas-permeable filling mass in said chamber, the mass consisting of particles of readily heat-conducting material sintered together with a layer of a readily heat-conducting material provided on an outer circumferential surface of the mass, and a soldered joint provided between the layer and the inner wall of the chamber in at least one zone extending throughout the circumference of the filling mass.
Description
nited States Patent 9 Severijns Feb. 26, 1974 [54] HEAT EXCHANGER AND METHOD OF 3,195,621 7/1965 Van Geuns et a1. 165/10 MANUFACTURING THE SAME 3,237,421 3/1966 Gifford t 165/10 X 3,306,353 2/1967 Bume 165/165 x [75] Inventor: Adrlanus Petrus Severuns, 3,407,615 10/1968 Klipping l65/l54 x Emmasingel, Eindhoven, 3,433,299 3/1969 Fleming 165/154 x Netherlands [73] Assignee: U.S. Philips Corporation, New a w Davis,
York Attorney, Agent, or FirmFrank R. Trifari [22] Filed: May 15, 1972 [21] Appl. No.: 253,360
[57] ABSTRACT Related US. Application Data [63] Continuation of Ser. No. 14,555, Feb 26, 1970, A heat exchanger comprising a readily heataballdonedconducting block of material having at least one chamber, a gas-permeable filling mass in said cham- U.S. R, her, the mass consisting of particles of readily heat- 62/6, 138/38 conducting material sintered together with a layer of a [5 i I readily heat conducting material provided on an Outer [58] Fleld of Search-M 165N641 179; circumferential surface of the mass, and a soldered 29/1573; 62/6; 138/38 joint provided between the layer and the inner wall of the chamber in at least one zone extending throughout References Clted the circumference of the filling mass.
UNITED STATES PATENTS 2,893,702 7/1959 Richardson 165/165 X 6 Claims, 1 Drawing Figure Pmmemwe w 3194,, 1 10 r INVENTOR. ADRIANUS P. SEVERIJNS AGENT HEAT EXCHANGER AND METHOD OF MANUFACTURING THE SAME This is a continuation of application Ser. No. 14,555, filed Feb. 26, 1970, now abandoned.
The invention relates to a heat exchanger which is particularly suitable for use in the temperature range below 2 K and comprises a readily heat-conducting block of material having at least one chamber containing at least one gas-permeable filler of particles ofa likewise readily heat-conducting material which are sintered together, preferably the same material as that of the block, each of the chambers comprising at their oppositely located ends, connections with which they can be incorporated in ducts through which flows of helium can be conducted which exchange heat with each other.
Heat exchangers of the type described are known. They are used, for example, in cooling devices in which He or a mixture of He and He circulates as a working medium between a cooled place (cooler) and a place to be cooled. Such cooling devices are described in Dutch Pat. application No. 6,807,902 and in U.S. Pat. No. 3,376,712. In these cooling devices the temperature of the place to be cooled lies below 1 K. In these devices it is desirable to cool the flow of medium flowing to the place to be cooled in the counter-current heat exchange with medium flowing away from the place to be cooled. For this purpose heat exchangers are used having a construction as described above, in which the filling mass is formed by sintered copper balls having a diameter of approximately 40 am and the surrounding block of material alsoconsists of copper.
The very fine copper balls give a very large heatexchangingjsurface area with the circulating helium so that a good heat transfer is ensured between helium and the filling mass. For a satisfactory operation of the heat exchanger it is furthermore necessary that a good heat transfer is ensured from the filling mass to the block of material. In order to achieve this it is known to sinter-the pre-sintered filling mass, after placing in the chamber, to the block under a compression pressure. In this case large difficulties occur. First of all, as a result of the sintering together of the copper b'alls, cracks nearly always occur in the filling mass after sintering in the chamber, and furthermore the resistance to flow increases which disturbsthe satisfactory operation. Secondly, as a resultof the compression the end face of the filling mass is more or less-squeezed so that the resistance to flow of the filling mass increases considerably. Since a low resistance to flowof the heat exchangers is essentialfor a satisfactory operation of the cooling device, it will be obvious that increase of the resistance to flow is not acceptable.
It is the objectof the invention to provide aheat exchanger of the above described type in whichthe said drawbacks are fully obviated.
For that purpose, the heatexcha'nger according to the invention is characterized in that the filling mass comprises at its circumferential surface a layer of a readily heat-conducting material provided thereon, preferably the same material as that of the'fillin'g mass and the block of material, andis incorporated so as to fit in the relative chamber, a soldered jointbein'g'provided between the layer of material and the wall of the relative chamber in at least one zone extending throughout the circumference of the filling mass.
Due to the atomic contact between the provided layer of material and the filling mass, a good heat contact is ensured. As a result of the soldered joint between the layer of material and the block of material, a good heat contact is obtained in this case also.
Since the filling mass, after placing in the chamber, is no longer sintered, cracking of the filling mass does not occur either, and the helium can nevertheless not flow between the block and the filling mass, since this is prevented on the one hand by the soldered joint and on the other hand by the layer of material. So this layer has both a heat transmitting function and a sealing function. The end faces of the filling masses remain readily open (no increase of the resistance to flow) since this is no longer sintered in the chamber.
According to the invention, all the components of the heat exchanger are preferably manufactured from the same material. The advantage of this is that the thermal expansion and the shrinkage, respectively, is the same for all the components so that few thermal stresses occur. Copper is a very suitable material for this purpose. In a further favorable embodiment the layer of material is provided on the filling mass electrolytically.
The invention furthermore relates to a method of manufacturing the above-described heat exchanger. It is characterized in that a rod of sintered material is turned down to a diameter which is smaller by approximately 1 mm than that of a chamber in a block of a readily heat-conducting material, after which the rod is provided electrolytically with a layer of readily conducting material, the ends of the rod being then liberated from the deposited layer of material, the rod being then rinsed to remote acid and salt, the rod being turned down to such a diameter that the filling mass sawn at the desirable length fits in the chamber, at least one annular groove being provided in the wall of the chamber prior to placing the filling mass, a soldering ring being provided in said groove the assembly being heated to above the melting temperature of the solder after placing the filling mass, the open side of the chamber being then sealed by soldering a cover.
In order that the invention may be readily carried into effect, one embodiment of a heat exchanger will now be described in greater detail, by way of example, with reference to the accompanying drawing which is diagrammatic and not drawn to scale.
This heat exchanger comprises a copper block 1 in which two chambers 2 and 3 are recessed. In each of these chambers, filling masses 4 and 5, respectively, of sintered copper balls are accommodated, said filling masses comprising at their circumferential surface electrolytically grown layers 6 and 7, respectively, of copper. The layers 6 and 7, respectively, are soldered to the copper block 1, at the points 8,9 and 10,11, respectively. Pipes l2 and 13 soldered in an aperture in the block 1, communicate with the lower side of the chambers 2, 3 while the upper side of the chambers 2 and 3 is sealed by soldered covers 14 and 15, respectively, in each of which a pipe 16 and 17, respectively is soldered. Thus pipes 12 and 16 (and also pipes 13 and 17) each constitute a pair of inlet-outlet means with a flow path defined between them.
This heat exchanger is manufactured as follows:
A rod of sintered copper balls is first turned down to a diameter which is smaller by approximately 1 mm than that of the chambers 2 and 3. A layer of copper, slightly more than 0.5 mm thick, is deposited electrolytically on said rod. At the ends of the rod, the deposited layer is removed and the rod is then rinsed with alkali so as to remove the acid residues. Then it is rinsed with warm water so as to remove the formed salts, after which it is fired in a vacuum. Pieces which correspond to the dimensions of the filling masses 4 and 5 are then cut from said rod. Said filling masses are turned down to such a diameter as to fit in the chambers 2 and 3. At the points 8,9 and 10,11, respectively, annular grooves are provided in the wall of the chambers 2 and 3, in which grooves, rings of soldering material are laid, these rings as shown having thickness, t, substantially less than the length, L, of the filling mass in the direction of the flow path between the inlet and outlet pipes. The filling masses 4 and 5 are then placed in the chambers. Heating to above the melting temperature of the solder is then carried out so that the soldered joints are obtained at the points 8, 9 and 10, 11 respectively. Simultaneously with this soldering operation the pipes 12 and 13 can be soldered in the block 1. The covers 14 and 15 with the pipes 16 and 17 are then soldered on the block 1.
in this manner a heat exchanger is obtained having a good thermal contact between the filling mass 4, 5 and the layer 6,7; as well as a good thermal contact between the layer 6,7 and the block 1. Leakage between the filling mass and the block is not possible. The filling masses 4 and 5 have a low resistance to flow, since no sintering takes place after the arrangement of the filling masses in their chambers.
What is claimed is:
l. A heat exchanger for use in a temperature range below 2 K, comprising, a block of readily-heatconducting material, the block having at least one internal chamber defining inner walls, the chamber further having inlet and outlet means thus defining a flow path through said chamber, a gas-permeable filling mass having an outer surface and formed of sintered particles of a readily-heat-conducting material, a layer of readily-heat-conducting material deposited on said outer surface of the filling mass, said mass disposed within said flow path and constituting a partition of predetermined length between the inlet and the outlet, with said layer on said mass being in direct heat exchange contact with said inner walls of the chamber, and a soldered junction between said chamber walls and said layer on said filling mass, the junction defining a circumferential zone of smaller thickness in the flow path direction than said length of the mass, sealing said mass to said chamber walls such that the inlet and outlet can communicate only through said mass.
2. A heat exchanger comprising a copper block having at least one internal chamber defining inner walls, and spaced apart inlet and outlet ducts thus defining a flow path through the chamber, a gas-permeable filling mass defining an outer surface, the mass formed of sintered copper particles, a layer of electrolytically deposited copper on said outer surface of said filling mass, said mass disposed within said flow path and constituting a partition between the inlet and the outlet with said layer on said mass being in direct heat exchange contact with said inner walls of the chamber, and a copper solder junction between said chamber walls and said layer on said filling mass the junction defining a circumferential annular zone sealing said mass to said chamber walls such that the inlet and outlet can communicate only through said mass.
3. Apparatus according to claim 1 wherein said block has a second chamber spaced from and similar to the first chamber.
4. Apparatus according to claim 1 wherein said layer is an electrolytically deposited layer.
5. Apparatus according to claim 1 wherein said block, the filling mass, and said layer are all copper.
6. Apparatus according to claim 1 wherein said solder junction defines an annular ring defining a plane generally transverse to said flow path.
Claims (6)
1. A heat exchanger for use in a temperature range below 2* K, comprising, a block of readily-heat-conducting material, the block having at least one internal chamber defining inner walls, the chamber further having inlet and outlet means thus defining a flow path through said chamber, a gas-permeable filling mass having an outer surface and formed of sintered particles of a readily-heat-conducting material, a layer of readily-heatconducting material deposited on said outer surface of the filling mass, said mass disposed within said flow path and constituting a partition of predetermined length between the inlet and the outlet, with said layer on said mass being in direct heat exchange contact with said inner walls of the chamber, and a soldered junction between said chamber walls and said layer on said filling mass, the junction defining a circumferential zone of smaller thickness in the flow path direction than said length of the mass, sealing said mass to said chamber walls such that the inlet and outlet can communicate only through said mass.
2. A heat exchanger comprising a copper block having at least one internal chamber defining inner walls, and spaced apart inlet and outlet ducts thus defining a flow path through the chamber, a gas-permeable filling mass defining an outer surface, the mass formed of sintered copper particles, a layer of electrolytically deposited copper on said outer surface of said filling mass, said mass disposed within said flow path and constituting a partition between the inlet and the outlet with said layer on said mass being in direct heat exchange contact with said inner walls of the chamber, and a copper solder junction between said chamber walls and said layer on said filling mass the junction defining a circumferential annular zone sealing said mass to said chamber walls such that the inlet and outlet can communicate only through said mass.
3. Apparatus according to claim 1 wherein said block has a second chamber spaced from and similar to the first chamber.
4. Apparatus according to claim 1 wherein said lAyer is an electrolytically deposited layer.
5. Apparatus according to claim 1 wherein said block, the filling mass, and said layer are all copper.
6. Apparatus according to claim 1 wherein said solder junction defines an annular ring defining a plane generally transverse to said flow path.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US25336072A | 1972-05-15 | 1972-05-15 |
Publications (1)
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US3794110A true US3794110A (en) | 1974-02-26 |
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US00253360A Expired - Lifetime US3794110A (en) | 1972-05-15 | 1972-05-15 | Heat exchanger and method of manufacturing the same |
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Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4366676A (en) * | 1980-12-22 | 1983-01-04 | The Regents Of The University Of California | Cryogenic cooler apparatus |
US4397156A (en) * | 1980-11-26 | 1983-08-09 | Leybold Heraeus Gmbh | Displacer for low-temperature refrigerating machines |
US4404808A (en) * | 1981-08-10 | 1983-09-20 | Helix Technology Corporation | Cryogenic refrigerator with non-metallic regenerative heat exchanger |
US4478276A (en) * | 1980-11-12 | 1984-10-23 | Rosenbaum Ralph L | Heat-exchanger particularly useful for low temperature applications, and method and apparatus for making same |
US5012650A (en) * | 1989-10-11 | 1991-05-07 | Apd Cryogenics, Inc. | Cryogen thermal storage matrix |
EP0666129A2 (en) * | 1994-02-08 | 1995-08-09 | Alfa Laval Flow Gmbh | Process for preparing sintered porous components and their use |
US5469709A (en) * | 1993-06-18 | 1995-11-28 | Samsung Electronics Co., Ltd. | Regenerator for Vuilleumier heat pump |
US6065295A (en) * | 1995-12-15 | 2000-05-23 | Leybold Vakuum Gmbh | Low-temperature refrigerator with cold head and a process for optimizing said cold head for a desired temperature range |
US6263958B1 (en) | 1998-02-23 | 2001-07-24 | William H. Fleishman | Heat exchangers that contain and utilize fluidized small solid particles |
US20170146273A1 (en) * | 2015-11-23 | 2017-05-25 | L-3 Communications Corporation | Evaporator Assembly |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2893702A (en) * | 1947-12-12 | 1959-07-07 | Richardson Edward Adams | Heat exchange apparatus |
US3195621A (en) * | 1961-09-19 | 1965-07-20 | Philips Corp | Heat exchanger |
US3237421A (en) * | 1965-02-25 | 1966-03-01 | William E Gifford | Pulse tube method of refrigeration and apparatus therefor |
US3306353A (en) * | 1964-12-23 | 1967-02-28 | Olin Mathieson | Heat exchanger with sintered metal matrix around tubes |
US3407615A (en) * | 1965-09-14 | 1968-10-29 | Max Planck Gesellschaft | Low temperature heat exchanger |
US3433299A (en) * | 1967-02-16 | 1969-03-18 | Gen Electric | Heat exchanger of porous metal |
-
1972
- 1972-05-15 US US00253360A patent/US3794110A/en not_active Expired - Lifetime
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2893702A (en) * | 1947-12-12 | 1959-07-07 | Richardson Edward Adams | Heat exchange apparatus |
US3195621A (en) * | 1961-09-19 | 1965-07-20 | Philips Corp | Heat exchanger |
US3306353A (en) * | 1964-12-23 | 1967-02-28 | Olin Mathieson | Heat exchanger with sintered metal matrix around tubes |
US3237421A (en) * | 1965-02-25 | 1966-03-01 | William E Gifford | Pulse tube method of refrigeration and apparatus therefor |
US3407615A (en) * | 1965-09-14 | 1968-10-29 | Max Planck Gesellschaft | Low temperature heat exchanger |
US3433299A (en) * | 1967-02-16 | 1969-03-18 | Gen Electric | Heat exchanger of porous metal |
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4478276A (en) * | 1980-11-12 | 1984-10-23 | Rosenbaum Ralph L | Heat-exchanger particularly useful for low temperature applications, and method and apparatus for making same |
US4397156A (en) * | 1980-11-26 | 1983-08-09 | Leybold Heraeus Gmbh | Displacer for low-temperature refrigerating machines |
US4366676A (en) * | 1980-12-22 | 1983-01-04 | The Regents Of The University Of California | Cryogenic cooler apparatus |
US4404808A (en) * | 1981-08-10 | 1983-09-20 | Helix Technology Corporation | Cryogenic refrigerator with non-metallic regenerative heat exchanger |
US5012650A (en) * | 1989-10-11 | 1991-05-07 | Apd Cryogenics, Inc. | Cryogen thermal storage matrix |
US5469709A (en) * | 1993-06-18 | 1995-11-28 | Samsung Electronics Co., Ltd. | Regenerator for Vuilleumier heat pump |
EP0666129A2 (en) * | 1994-02-08 | 1995-08-09 | Alfa Laval Flow Gmbh | Process for preparing sintered porous components and their use |
EP0666129A3 (en) * | 1994-02-08 | 1996-05-15 | Alfa Laval Flow Gmbh | Process for preparing sintered porous components and their use. |
US6065295A (en) * | 1995-12-15 | 2000-05-23 | Leybold Vakuum Gmbh | Low-temperature refrigerator with cold head and a process for optimizing said cold head for a desired temperature range |
US6263958B1 (en) | 1998-02-23 | 2001-07-24 | William H. Fleishman | Heat exchangers that contain and utilize fluidized small solid particles |
US20170146273A1 (en) * | 2015-11-23 | 2017-05-25 | L-3 Communications Corporation | Evaporator Assembly |
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