EP0183007A1 - Port bushings for internally manifolded stacked, finned-plate heat exchanger - Google Patents

Port bushings for internally manifolded stacked, finned-plate heat exchanger Download PDF

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Publication number
EP0183007A1
EP0183007A1 EP85112297A EP85112297A EP0183007A1 EP 0183007 A1 EP0183007 A1 EP 0183007A1 EP 85112297 A EP85112297 A EP 85112297A EP 85112297 A EP85112297 A EP 85112297A EP 0183007 A1 EP0183007 A1 EP 0183007A1
Authority
EP
European Patent Office
Prior art keywords
plate
ports
peripheral wall
fins
bushings
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.)
Withdrawn
Application number
EP85112297A
Other languages
German (de)
French (fr)
Inventor
Irwin E. Rosman
William Richard Wagner
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.)
Boeing North American Inc
Original Assignee
Rockwell International Corp
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 Rockwell International Corp filed Critical Rockwell International Corp
Publication of EP0183007A1 publication Critical patent/EP0183007A1/en
Withdrawn legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/02Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
    • F28F3/04Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element
    • F28F3/048Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element in the form of ribs integral with the element or local variations in thickness of the element, e.g. grooves, microchannels
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D9/00Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D9/0031Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other
    • F28D9/0043Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the plates having openings therein for circulation of at least one heat-exchange medium from one conduit to another
    • F28D9/005Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the plates having openings therein for circulation of at least one heat-exchange medium from one conduit to another the plates having openings therein for both heat-exchange media
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/08Elements constructed for building-up into stacks, e.g. capable of being taken apart for cleaning
    • F28F3/10Arrangements for sealing the margins

Definitions

  • This invention relates to plate-stack heat exchangers and especially to plate-stack heat exchangers with internal manifolding.
  • Finned-plate heat exchangers are mainly of the channel and rib-type construction. Countercurrent flow can be achieved; however, manifolding a plate stack which must separate the fluids at entry and exit becomes extremely complex. Since the manifolding of the crosscurrent heat exchangers is comparatively simple, this heat exchanger system is more widely used although it is less efficient than the countercurrent system and it induces serious thermal and mechanical stresses.
  • Campbell et al U.S. Patent No. 3,305,010.
  • Campbell et al teach a heat exchanger having superposed stacked plate and fin elements and complex manifolding means for introducing fluids of different temperatures into opposite ends of the assembly.
  • Campbell et al do not teach a plate which serves as both the plate and the fin, nor does Campbell et al teach means for internally manifolding the plate within the plate's plane.
  • One of the problems in the stacked plate type of heat exchanger is the blocking of a selected internal port at any stack level to prevent fluid flow from the selected port through the channels on that level and, thus, to force the fluid through the port to the next level where it is permitted to flow through the channels.
  • An object of the present invention is to provide a finned plate for an internally manifolded plate-stack heat exchanger.
  • Another object is to provide a simple means for blocking the flow from a fluid-inlet port at a given plate level in a plate-stack heat exchanger and for passing that fluid through to a fluid-inlet port in the next higher plate.
  • the invention comprises an internally manifolded, countercurrent, finned-plate- stack heat exchanger, each interior plate having manifold areas at opposite ends thereof.
  • Flow, or fluid entry, ports are excised through the plates, at least two at each manifold area.
  • the ports and the fins are formed so that the plates can be rotated 180° without the relative overall appearance being changed, i.e., the ports of the rotated plate will still be in mating position with the ports of an unrotated plate when the two plates are stacked.
  • Bushings of compressible, fluid-impervious material are inserted into two diagonally opposite ports in each plate and a gasket is inserted in a groove in the upper surface of the peripheral wall around the plate so that fluid does not flow between the contacting surfaces of the gasket and bushing with the bottom surface of the plate immediately above.
  • Fig. 1 shows a schematic view of two interior, adjacent, finned-channel plates 10 and 12 for a heat exchanger 50 (Figure 3) in accordance with the present Invention.
  • the lower and upper plates 10 and 12 are preferably rectangular and are formed with parallel, longitudinal, upstanding fins 16 which define longitudinal channels 18 between them.
  • the plates may be formed of metal by an extrusion process and areas 20 and 21 (see Fig. 2) can be formed later where the fins 16 are milled off at each end.
  • a pair of spaced fluid-entry ports 22 and 24 are drilled at one end toward the corners of the plates, and another pair of ports 26 and 28 are drilled similarly at the other end.
  • a frame 30 is placed upon and bonded to the periphery of the upper surface of each finned plate, thus forming a wall 31 around the plate and a well or manifold 32, 33 at each end where the fins 16 were milled off.
  • Two diagonally opposite ports on each plate are fitted with a bushing insert 34 which extends upwards as far as the top of the wall 31 of the frame 30 and the tops of the fins 16, the top surfaces of these members forming a flat plane.
  • the bushings 34 are preferably formed from a compressible material, such as a heat-resistant elastomer, in which case they may extend slightly above the aforementioned flat plane, or may be formed from a metal with a groove in the upper surface in which a circular gasket 36, or 0-ring, can be inserted.
  • the frame 30 is also preferably formed with a groove in its upper surface in which a gasket 38 is inserted.
  • the bottom surface of the interior plates 10 and 12, as well as that of the top plate 14, must be flat surfaces so that they make good contact with the gaskets 38 and 36 on the frames 30 and bushings 34 of the plates underneath the surfaces.
  • the gaskets 36 and 38 prevent the passage of fluids.
  • the bottom plate 10' (see Fig. 3) in the stack of plates is formed somewhat differently from the interior plates 10, 12, etc.
  • the bottom plate 10' is formed with only two ports 24' and 28', each in a different manifold area and each on the same longitudinal side of the plate.
  • One port 24' is the entry port for one fluid (B), e.g., cool air
  • the other port 28' is the entry port for a second fluid (A), e.g., hot oil which is to be cooled.
  • a bushing 34 is inserted through the entry port 24' for the fluid which is not to be circulated through the channels 18 in the bottom plate 10' thereby transforming this port into a non-dispersive port, i.e., a port through which the fluid flows only to the next plate 12 above the bottom plate 10'.
  • pressurized fluid A enters the bottom plate 10' through inlet port 28', fills the manifold 33 and a portion proceeds through the channels 18 between the fins 16 and up through the inlet port 22 in the second plate 12.
  • a second portion proceeds directly through the non-dispersive port 28 in the second plate 12 through the inlet port 28 in the third plate 10 where it provides the source of fluid flow to the left as in the first plate.
  • Pressurized fluid B enters the bottom plate 10' through non-dispersive port 24' and is prevented from flowing in the bottom plate 10' by the bushing 34. Fluid B goes through the inlet port 24 in the second plate 12 and fills the manifold 32 on the left side. A portion of the manifold fluid flows to the right through the channels 18 and then up through non-dispersive port 26 in plate 10 and port 26 in plate 11. It leaves the plate stack through the outlet duct 42 1n the top plate 14 which is formed with two outlet ducts, 42 for fluid B and 40 for fluid A. Fluid B always flows to the right in alternate plates, e.g., plates 12 and 11. For fluid B, the ports 24' and 24 1n each plate are inlet ports and the ports 26 diagonally opposite are outlet ports. For fluid A, the ports 28' and 28 are inlet ports and the ports 22 are outlet ports. The flows in the channels 18 for fluid A and B are counterflows.
  • Fig. 4 there is shown a unitary form of construction for a gasket 62 which may be inserted in a groove along the top of the peripheral wall and the circular gaskets 60 which may be put on the top of the bushings 34.

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Cooling Or The Like Of Semiconductors Or Solid State Devices (AREA)
  • Moulds For Moulding Plastics Or The Like (AREA)
  • Table Devices Or Equipment (AREA)

Abstract

Internal plates 10, 11, 12 for a finned-plate, plate stack heat exchanger 50 are formed with manifold areas 32, 33 one at each opposite end. Ports 22, 24, 26, 28 are excised through each plate in the manifold areas, two ports at each end. A pair of compressible, fluid-impervious bushings 34 are inserted in two diagonally opposed ports, e.g. 22, 28 or 24, 26, in each plate and extend upwards to make fluid-impervious contact with the bottom surface of the plate immediately above. Thus, fluid can flow through the bushings between a first and a third plate without leaking onto the second plate which is located between the first and third plates. The interior plates 10, 11 and 12 of the exchanger 50 are rotatable 180° without altering the mating orientation of the ports of any two adjacent interior plates, e.g.. 10 and 12.

Description

    Background of the Invention 1. Field of the Invention
  • This invention relates to plate-stack heat exchangers and especially to plate-stack heat exchangers with internal manifolding.
  • 2. Description of the Prior Art
  • Finned-plate heat exchangers are mainly of the channel and rib-type construction. Countercurrent flow can be achieved; however, manifolding a plate stack which must separate the fluids at entry and exit becomes extremely complex. Since the manifolding of the crosscurrent heat exchangers is comparatively simple, this heat exchanger system is more widely used although it is less efficient than the countercurrent system and it induces serious thermal and mechanical stresses.
  • One crosscurrent system which has attempted to solve the manifolding problem of the countercurrent heat exchanger is taught by Campbell et al, U.S. Patent No. 3,305,010. Campbell et al teach a heat exchanger having superposed stacked plate and fin elements and complex manifolding means for introducing fluids of different temperatures into opposite ends of the assembly. However. Campbell et al do not teach a plate which serves as both the plate and the fin, nor does Campbell et al teach means for internally manifolding the plate within the plate's plane.
  • One of the problems in the stacked plate type of heat exchanger is the blocking of a selected internal port at any stack level to prevent fluid flow from the selected port through the channels on that level and, thus, to force the fluid through the port to the next level where it is permitted to flow through the channels.
  • Obiects of the Invention
  • An object of the present invention is to provide a finned plate for an internally manifolded plate-stack heat exchanger.
  • Another object is to provide a simple means for blocking the flow from a fluid-inlet port at a given plate level in a plate-stack heat exchanger and for passing that fluid through to a fluid-inlet port in the next higher plate.
  • Other objects, advantages and novel features of the present invention will become apparent from the following detailed description of the invention when considered 1n conjunction with the accompanying drawing.
  • Summary of the Invention
  • The invention comprises an internally manifolded, countercurrent, finned-plate- stack heat exchanger, each interior plate having manifold areas at opposite ends thereof. Flow, or fluid entry, ports are excised through the plates, at least two at each manifold area. The ports and the fins are formed so that the plates can be rotated 180° without the relative overall appearance being changed, i.e., the ports of the rotated plate will still be in mating position with the ports of an unrotated plate when the two plates are stacked. Bushings of compressible, fluid-impervious material are inserted into two diagonally opposite ports in each plate and a gasket is inserted in a groove in the upper surface of the peripheral wall around the plate so that fluid does not flow between the contacting surfaces of the gasket and bushing with the bottom surface of the plate immediately above.
  • Brief Description of the Figures
    • Fig. 1 is a schematic diagram illustrating the structure of two adjacent interior plates according to the present invention.
    • Fig. 2 is a schematic diagram illustrating a frame which can be employed to form a peripheral wall around a plate.
    • Fig. 3 is a schematic diagram illustrating an embodiment of the plates of a plate stack heat exchanger in accordance with the present Invention.
    • Fig. 4 is a schematic diagram illustrating a unitary form of construction for the wall and bushing gaskets.
  • The same elements or parts throughout the figures of the drawing are designated by the same reference characters, while equivalent elements bear a prime designation.
  • Detailed Description of the Invention
  • Fig. 1 shows a schematic view of two interior, adjacent, finned- channel plates 10 and 12 for a heat exchanger 50 (Figure 3) in accordance with the present Invention. The lower and upper plates 10 and 12 are preferably rectangular and are formed with parallel, longitudinal, upstanding fins 16 which define longitudinal channels 18 between them. The plates may be formed of metal by an extrusion process and areas 20 and 21 (see Fig. 2) can be formed later where the fins 16 are milled off at each end. A pair of spaced fluid- entry ports 22 and 24 are drilled at one end toward the corners of the plates, and another pair of ports 26 and 28 are drilled similarly at the other end.
  • A frame 30 is placed upon and bonded to the periphery of the upper surface of each finned plate, thus forming a wall 31 around the plate and a well or manifold 32, 33 at each end where the fins 16 were milled off. Two diagonally opposite ports on each plate are fitted with a bushing insert 34 which extends upwards as far as the top of the wall 31 of the frame 30 and the tops of the fins 16, the top surfaces of these members forming a flat plane. The bushings 34 are preferably formed from a compressible material, such as a heat-resistant elastomer, in which case they may extend slightly above the aforementioned flat plane, or may be formed from a metal with a groove in the upper surface in which a circular gasket 36, or 0-ring, can be inserted. The frame 30 is also preferably formed with a groove in its upper surface in which a gasket 38 is inserted. The bottom surface of the interior plates 10 and 12, as well as that of the top plate 14, must be flat surfaces so that they make good contact with the gaskets 38 and 36 on the frames 30 and bushings 34 of the plates underneath the surfaces. The gaskets 36 and 38, of course, prevent the passage of fluids.
  • The bottom plate 10' (see Fig. 3) in the stack of plates is formed somewhat differently from the interior plates 10, 12, etc. The bottom plate 10' is formed with only two ports 24' and 28', each in a different manifold area and each on the same longitudinal side of the plate. One port 24' is the entry port for one fluid (B), e.g., cool air, and the other port 28' is the entry port for a second fluid (A), e.g., hot oil which is to be cooled. A bushing 34 is inserted through the entry port 24' for the fluid which is not to be circulated through the channels 18 in the bottom plate 10' thereby transforming this port into a non-dispersive port, i.e., a port through which the fluid flows only to the next plate 12 above the bottom plate 10'.
  • The arrows indicate the direction of the fluid flows. Thus, pressurized fluid A enters the bottom plate 10' through inlet port 28', fills the manifold 33 and a portion proceeds through the channels 18 between the fins 16 and up through the inlet port 22 in the second plate 12. A second portion proceeds directly through the non-dispersive port 28 in the second plate 12 through the inlet port 28 in the third plate 10 where it provides the source of fluid flow to the left as in the first plate.
  • Pressurized fluid B enters the bottom plate 10' through non-dispersive port 24' and is prevented from flowing in the bottom plate 10' by the bushing 34. Fluid B goes through the inlet port 24 in the second plate 12 and fills the manifold 32 on the left side. A portion of the manifold fluid flows to the right through the channels 18 and then up through non-dispersive port 26 in plate 10 and port 26 in plate 11. It leaves the plate stack through the outlet duct 42 1n the top plate 14 which is formed with two outlet ducts, 42 for fluid B and 40 for fluid A. Fluid B always flows to the right in alternate plates, e.g., plates 12 and 11. For fluid B, the ports 24' and 24 1n each plate are inlet ports and the ports 26 diagonally opposite are outlet ports. For fluid A, the ports 28' and 28 are inlet ports and the ports 22 are outlet ports. The flows in the channels 18 for fluid A and B are counterflows.
  • It should be noted that many more interior plates are present even though omitted 1n the drawing. All interior plates 10, 11, 12 have the same construction although any two adjacent plates are rotated by 180° from each other. (Plate 10 may differ only in the omission of a port 26.)
  • In Fig. 4, there is shown a unitary form of construction for a gasket 62 which may be inserted in a groove along the top of the peripheral wall and the circular gaskets 60 which may be put on the top of the bushings 34.
  • Obviously, many modifications and variations of the present invention are possible in light of the above teachings. It is therefore to be understood that, within the scope of the appended claims, the invention may be practiced otherwise than as specifically described.
  • What is claimed and desired to be secured by Letters Patent of the United States is:

Claims (10)

1. An internal plate for a plate-stack heat exchanger comprising:
a plate having an upper surface and a flat lower surface, the upper surface having flat ends on opposite sides thereof, the upper surface bearing a peripheral wall upstanding therefrom, a plurality of upstanding, spaced fins being centrally located upon said upper surface and extending between said flat ends, the spaces between said fins defining a plurality of spaced channels, the ends of said fins and the upstanding peripheral wall defining a pair of manifolds, one at each end of said upper surface,
the plate being formed with a set of two spaced ports therethrough in each manifold area at such locations that the plate may be rotated 180° from another such plate and the ports in both plates will still occupy mating locations, the upper surfaces of the fins and the peripheral wall being coplanar; and
a pair of bushings which fit into and are located in two diagonally opposite ports, the bushings extending upward at least to the plane formed by the peripheral wall and fins.
2. A plate as in claim 1, where:
said plate is rectangular.
3. A plate as in claim 1, wherein:
said bushings are formed from a compressible, fluid-impervious material so that, when they are in contact with the flat bottom part of another plate, fluids cannot flow past the contacting surfaces.
4. A plate as in claim 1, where:
said upstanding peripheral wall comprises a frame which is affixed to the upper surface of the plate at its periphery.
5. A plate as in claim 1, in which:
the plate is formed with a groove along the upper surface of the peripheral wall; and
the plate further includes a gasket which is fitted into the groove in the peripheral wall and extends upward at least to the plane formed by the peripheral wall and the fins.
6. A plate as in claim 5, wherein:
said gasket and bushings are formed from a compressible, fluid-impervious material so that, when they are in contact with the flat bottom part of another plate, fluids cannot flow past the contacting surfaces.
7. A plate stack heat exchanger comprising:
a plurality of interior plates stacked one upon another, each plate having an upper surface and a flat lower surface, the upper surface having flat ends on opposite sides thereof, the upper surface bearing a peripheral wall upstanding therefrom, a plurality of upstanding, spaced fins being centrally located upon said upper surface and extending between said flat ends, the spaces between said fins defining a plurality of spaced channels, the ends of said fins and the upstanding peripheral wall defining a pair of manifolds, one at each end of said upper surface,
each plate being rotated 180° with respect to the next lower plate;
a pair of bushings which fit into and are located in two diagonally opposite ports, the bushings extending upward at least to the plane formed by the peripheral wall and fins;
a bottom plate similar to said interior plates except that it is formed with only three ports, two in one manifold area and one in the other manifold area, the two diagonally opposed ports having bushings inserted therein; and
a top plate having a flat lower surface and having two ports formed therein, one above each of two non-diagonally opposed ports located at opposite manifold areas of the interior plate immediately below the top plate.
8. A plate stack heat exchanger as in claim 7. wherein:
all said plates are rectangular.
9. A plate stack heat exchanger as in claim 7, wherein:
said bushings are formed from a compressible, fluid-impervious material so that, when they are in contact with the flat bottom surface of another plate, fluids cannot flow past the contacting surfaces.
10. A plate stack heat exchanger as in claim 7, wherein:
the upstanding peripheral walls of each of the interior and bottom plates comprise a frame which is affixed to the upper surface of the plate at its periphery.
EP85112297A 1984-10-31 1985-09-27 Port bushings for internally manifolded stacked, finned-plate heat exchanger Withdrawn EP0183007A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US66693784A 1984-10-31 1984-10-31
US666937 1984-10-31

Publications (1)

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EP0183007A1 true EP0183007A1 (en) 1986-06-04

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EP85112297A Withdrawn EP0183007A1 (en) 1984-10-31 1985-09-27 Port bushings for internally manifolded stacked, finned-plate heat exchanger

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EP (1) EP0183007A1 (en)
JP (1) JPS61110880A (en)
DK (1) DK500785A (en)
NO (1) NO854327L (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE10021481A1 (en) * 2000-05-03 2001-11-08 Modine Mfg Co Plate heat exchanger
WO2016051608A1 (en) * 2014-10-01 2016-04-07 Mitsubishi Heavy Industries Compressor Corporation Plate laminated type heat exchanger
WO2021007093A1 (en) * 2019-07-09 2021-01-14 Board Of Trustees Of Michigan State University Heat exchanger and method of making same

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB520610A (en) * 1937-11-15 1940-04-29 Martin Larsen Improvements in or relating to plate heat exchanging apparatus
GB798535A (en) * 1957-02-19 1958-07-23 Rosenblads Patenter Ab Improvements in or relating to heat exchangers of the plate-pile type
FR2032206A5 (en) * 1968-06-28 1970-11-20 Hisaka Works Ltd
DE2030397A1 (en) * 1969-06-19 1971-01-07 Parkson Industrial Equipment Company Ltd , Dartford, Kent (Großbritannien) Process for cleaning plate heat exchangers
GB1344895A (en) * 1970-10-23 1974-01-23 Schmidt W K F Plate heat exchanger
FR2373025A1 (en) * 1976-12-04 1978-06-30 Hoechst Ag PLATES FOR HEAT EXCHANGER
FR2463377A1 (en) * 1979-08-08 1981-02-20 Apv Co Ltd PLATE HEAT EXCHANGER
US4347896A (en) * 1979-10-01 1982-09-07 Rockwell International Corporation Internally manifolded unibody plate for a plate/fin-type heat exchanger
GB2126703A (en) * 1982-09-07 1984-03-28 Apv Int Ltd Plate heat exchanger

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB520610A (en) * 1937-11-15 1940-04-29 Martin Larsen Improvements in or relating to plate heat exchanging apparatus
GB798535A (en) * 1957-02-19 1958-07-23 Rosenblads Patenter Ab Improvements in or relating to heat exchangers of the plate-pile type
FR2032206A5 (en) * 1968-06-28 1970-11-20 Hisaka Works Ltd
DE2030397A1 (en) * 1969-06-19 1971-01-07 Parkson Industrial Equipment Company Ltd , Dartford, Kent (Großbritannien) Process for cleaning plate heat exchangers
GB1344895A (en) * 1970-10-23 1974-01-23 Schmidt W K F Plate heat exchanger
FR2373025A1 (en) * 1976-12-04 1978-06-30 Hoechst Ag PLATES FOR HEAT EXCHANGER
FR2463377A1 (en) * 1979-08-08 1981-02-20 Apv Co Ltd PLATE HEAT EXCHANGER
US4347896A (en) * 1979-10-01 1982-09-07 Rockwell International Corporation Internally manifolded unibody plate for a plate/fin-type heat exchanger
GB2126703A (en) * 1982-09-07 1984-03-28 Apv Int Ltd Plate heat exchanger

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE10021481A1 (en) * 2000-05-03 2001-11-08 Modine Mfg Co Plate heat exchanger
US6530425B2 (en) 2000-05-03 2003-03-11 Modine Manufacturing Company Plate heat exchanger
WO2016051608A1 (en) * 2014-10-01 2016-04-07 Mitsubishi Heavy Industries Compressor Corporation Plate laminated type heat exchanger
US10281219B2 (en) 2014-10-01 2019-05-07 Mitsubishi Heavy Industries Compressor Corporation Plate laminated type heat exchanger
WO2021007093A1 (en) * 2019-07-09 2021-01-14 Board Of Trustees Of Michigan State University Heat exchanger and method of making same

Also Published As

Publication number Publication date
DK500785A (en) 1986-05-01
NO854327L (en) 1986-05-02
JPS61110880A (en) 1986-05-29
DK500785D0 (en) 1985-10-31

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