[go: up one dir, main page]

US3525390A - Header construction for a plate-fin heat exchanger - Google Patents

Header construction for a plate-fin heat exchanger Download PDF

Info

Publication number
US3525390A
US3525390A US751961A US3525390DA US3525390A US 3525390 A US3525390 A US 3525390A US 751961 A US751961 A US 751961A US 3525390D A US3525390D A US 3525390DA US 3525390 A US3525390 A US 3525390A
Authority
US
United States
Prior art keywords
core
heat exchanger
plate
fin
flow
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.)
Expired - Lifetime
Application number
US751961A
Inventor
Edward A Rothman
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.)
RTX Corp
Original Assignee
United Aircraft 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 United Aircraft Corp filed Critical United Aircraft Corp
Application granted granted Critical
Publication of US3525390A publication Critical patent/US3525390A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02Header boxes; End plates
    • F28F9/026Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
    • F28F9/0263Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits by varying the geometry or cross-section of header box
    • 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
    • F28D1/00Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
    • F28D1/02Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
    • F28D1/04Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits
    • F28D1/0408Multi-circuit heat exchangers, e.g. integrating different heat exchange sections in the same unit or heat exchangers for more than two fluids
    • F28D1/0426Multi-circuit heat exchangers, e.g. integrating different heat exchange sections in the same unit or heat exchangers for more than two fluids with units having particular arrangement relative to the large body of fluid, e.g. with interleaved units or with adjacent heat exchange units in common air flow or with units extending at an angle to each other or with units arranged around a central element
    • 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
    • F28D9/0062Heat-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 spaced plates with inserted elements
    • F28D9/0068Heat-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 spaced plates with inserted elements with means for changing flow direction of one heat exchange medium, e.g. using deflecting zones
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02Header boxes; End plates
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S165/00Heat exchange
    • Y10S165/355Heat exchange having separate flow passage for two distinct fluids
    • Y10S165/356Plural plates forming a stack providing flow passages therein
    • Y10S165/387Plural plates forming a stack providing flow passages therein including side-edge seal or edge spacer bar
    • Y10S165/391Plural plates forming a stack providing flow passages therein including side-edge seal or edge spacer bar including intermediate corrugated element

Definitions

  • the headering of a plate-fin heat exchanger is constructed to contain a series of stacked triangular-shaped plates attached to and coplanar with the parting sheets of the core and are supported by support means within the header.
  • the triangular plates can be made integral with the normal parting plates.
  • This invention relates to heat exchangers and particularly to the headering construction of a plate-fin pure counterflow heat exchanger.
  • plate-fin counterflow heat exchangers of the two pass type include in the thermodynamic core section means to divert the flow admitted at right angles relative to each other permitting a portion of the flow in the heat exchanger to pass in counterflow relationship.
  • the core generally comprises parting sheets mounted in spaced stacked relationship defining alternate layers of open-ended channels where fluid in alternate layers passes parallel to, but sealed from, the fluid in the adjacent layer. Fins between the parting sheet, in the heretofore known counterflow heat exchanger, are disposed at angles to change the direction of the flow so that at least a portion of the fluid will pass in counterflow relationship which in certain heat exchangers is undesirable and results in a loss in heat transfer effectiveness when compared with the eflectiveness possible with pure counterflow. Thus, a larger heat exchanger is necessary to handle the heat transfer load.
  • triangular-shaped distribution chambers in the header for distribution of the fluid through the thermodynamic core such that it passes in pure counterflow heat exchange relationship.
  • the triangular chambers are outside of the thermodynamic core and hence, are not supported by the fins. Instead they are supported by any suitable means dictated by structure precluding the possibility of having cross-flow sections within the thermodynamic core while allowing all the heat transfer to occur in pure counterflow which is sufliciently more efficient to compensate for the triangular chambers and support structure resulting in an overall lighter weight heat exchanger manifested by the increased heat transfer effectiveness.
  • a primary object of this invention is to provide an improved headering for a conterflow, plate-fin heat exchanger.
  • a series of stacked triangular-shaped plates mounted adjacent to and complementary with the parting sheets or formed integral therewith are disposed in the header for changing direction and distributing flow into the pure counterflow thermodynamic core section of the heat exchanger.
  • a pair of back-to-back triangular sections of the ice headers mounted adjacent the core of the seat exchanger are ararnged so as to accommodate two dilferent fluids placed in indirect heat exchange relationship with a third fluid passing in pure counterflow heat exchange relationship.
  • a further object of this invention is to provide headering for a heat exchanger to assure that the fluids in indirect heat exchange relationship in the core are in pure counterflow relationship and being characterized by the fact that the overall heat exchanger is lighter in weight for the same heat transfer effectiveness that was heretofore realized.
  • FIG. 1 is a perspective view of the heat exchanger with the headering of one of the passes removed.
  • FIG. 2 is a sectional view taken along line '22 of FIG. 1.
  • FIG. 3 is a detailed view in elevation showing one pass.
  • FIG. 4 is a view in elevation showing an adjacent pass to the pass shown in FIG. 3.
  • FIG. 5 is a sectional view showing another embodiment of this invention.
  • FIGS. 1 through 4 show a dual heat exchanger consisting of two counterflow cores of plate and fin construction.
  • the cores are housed in a rectangularshaped box 10 having top and bottom walls 12 (only one wall being shown) and side walls 14 (only one wall being shown).
  • the back and front faces carry flanges which are adapted to receiver headers for conducting the primary flow through the stacked open-ended channels 16.
  • Each core channel comprises a fin section 18 sandwiched between parting sheets 20 and 22 and closure bars 24 and 25 attached at either end.
  • the closure bars 24 and 25 serve to seal oif the edges of the fin sections and afiford structural support to the parting sheets.
  • Typical secondary flow channels are shown in FIGS. 2 and 3, noting that they are representative of the other channels in the cores. Since all stacked channels are identical, only one will be described for the sake of simplicity.
  • the core section for one of the secondary flow channels comprises a parting sheet 20 which is generally a flat sheet of metal to which is attached a plurality of parallel spaced corrugated fins 18.
  • the spaces between the fins define openended channels for permitting fluid to flow through the core section.
  • a second parting sheet 21 similar to and coextensive with parting sheet 20 overlies the fins for defining therewith one of the layers in the core.
  • Closure bars 28 and 30 extend the length of the core and are mounted adjacent the edge of the fins and serve to seal off the sides of the open-ended channels. It will be noted that the closure bars are the same height as the fins so as to be joined to the two adjacent parting sheets.
  • Closure bar 32 is mounted between the fins and between closure bars 28 and 30 and attached to closure bars 46 and 44 to separate the core into two sections for accommodating different fluids.
  • distributing chambers are mounted adjacent to the core for passing fluid in the core in counterflow relation with the fluid in the adjacent layer.
  • Each distributing chamber includes triangular-shaped parting sheets 34 mounted adjacent to and extending from parting sheets 20 and 21.
  • the structural support shown here as straight fins 36 serve to distribute fluid admitted from manifold 38 (see FIG. 2) to the core and support the structural loads on sheet 34. These sections may be integral with the parting sheets.
  • a similar triangular-shaped parting sheet 40 similarly supported is mounted on the opposite end of the core for receiving the fluid discharging from the core and admitting it to manifold 42 for discharging the fluid out of the heat exchanger. Closure bars 44 and 46 seal off the edges of the distributing header sections. The opposite section of the core is made in a similar manner.
  • FIG. 4 shows the next adjacent pass (primary flow) comprising the core section 48 formed in the same manner as the core section of the secondary fluid.
  • This section carries triangular-shaped parting sheets or plates 50 and 52 extending from and mounted adjacent to the parting sheet 22 of the core section.
  • the structural support shown here as straight fin 36 are arranged parallel to the flow path in the thermodynamic fin 18.
  • Closure bars 24 and 25 mounted on the top and bottom edges serve to seal the fluid. It being noted that this channel of the core is coextensive with the next adjacent channel as shown in FIG, 1.
  • FIG. shows another embodiment of this invention wherein the secondary pass is constructed as a single section to accommodate one fluid rather than two as shown in FIGS. 1 through 4.
  • the core section 60 is constructed identical to the core section described above.
  • the triangular-shaped distributing sections 62 and 64 are substantially the same as described above but one is reversed so as to pass the flow into and out of the heat.
  • each closure bar in the embodiments shown in FIGS. 1 through 4 and for FIG. 5 may be constructed such that the portion sealing off the edge of the core and the portion sealing Off the edge of the distributing section are made from one piece. Also the parting sheets of the core and distributing section may be integral.
  • Header construction for a plate fin heat exchanger in combination with a counterflow core section said core section including a series of stacked coplanar plates, fins coextensively sandwiched in between said plates defining counterflow passes, the fins in adjacent passes being oriented in the same direction
  • said header comprising a triangular shaped header chamber formed from a series of stacked triangularly shaped flat plates, closure bars mounted alternately on the end of and between two adjacent flat plates and extending from the apex to the base of said triangle, support members mounted between said flat plates, and said triangular shaped header chambers being in register with said fins to distribute heat exchanger fluid to alternate passes.
  • a heat exchanger having plate and fin core section, first means for directing flow through alternate layers of said plate and fin section, second means for conducting flow through intervening layers of said plate and fin core section so as to direct the flow in adjacent layers in counterflow relation, said second means comprising stacked parallely spaced triangularly shaped plate members having one side mounted adjacent the core, closure bars mounted between said triangularly shaped plate members extending at one end from the apex to the base thereof for defining a passage therewith for conducting flow to said core section 3.
  • a heat exchanger comprising a core section having parallely stacked rectangularly shaped parting sheets forming layers of passages, fins sandwiched between said parting sheets defining a plurality of open ended channels, disposed in counterflow relation, closure bars mounted between said parting sheets adjacent the opposite sides of said fins, first pair of headers mounted on opposite faces of said core adapter to conduct fluid through alternate layers of said open ended channels, header means on another side of said core and having complementary layers of parallely stacked triangularly shaped flat plates mounted adjacent said parting sheets, closure bars mounted on the outer side of alternate layers between said triangularly shaped flat plates blocking off the flow from said first pair of headers and defining a distributing chamber for conducting fluid through intervening layers of said core.
  • a heat exchanger having plate and fin core section, means for directing flow through alternate layers of said plate and fin core section, means including a distributing chamber for leading flow to intervening layers of said plate and fin core section so as to direct the flow in adjacent layers in counterflow relation, said distributing chamber comprising a first series of stacked parallely spaced triangularly shaped plate members having one side mounted adjacent the core section, closure bars mounted between said triangularly shaped plate members extending at one end from the apex to the base thereof for defining a passage for conducting fiow to said core section, said apex being located at one end of said core section, and a receiving chamber having a second series of stacked parallely spaced triangular shaped plate members having I one side mounted adjacent the opposite side of said core section, closure bars mounted between said triangularly shaped plate members extending at one end from the apex to the base thereof for defining a passage therewith for receiving flow discharging from said core section.

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Geometry (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Description

Aug. 25', 1-970 E. A. ROTHMAN HEADER CONSTRUCTION FOR A PLATE-FIN HEAT EXCHANGER Filed Aug. 12, 1968 HmmmgwwwgwwwwwwmW INVENTOR EDWARD A. ROTHMAN ATTORNEY United States Patent 3,525,390 HEADER CONSTRUCTION FOR A PLATE-FIN HEAT EXCHANGER Edward A. Rothmau, South Glastonbury, Conn., assignor to United Aircraft Corporation, East Hartford, Conn.,
a corporation of Delaware Filed Aug. 12, 1968, Ser. No. 751,961 Int. Cl. F28f 3/08 US. Cl. 165-166 4 Claims ABSTRACT OF THE DISCLOSURE The headering of a plate-fin heat exchanger is constructed to contain a series of stacked triangular-shaped plates attached to and coplanar with the parting sheets of the core and are supported by support means within the header. The triangular plates can be made integral with the normal parting plates.
BACKGROUND OF THE INVENTION This invention relates to heat exchangers and particularly to the headering construction of a plate-fin pure counterflow heat exchanger.
As is well known in the art, plate-fin counterflow heat exchangers of the two pass type include in the thermodynamic core section means to divert the flow admitted at right angles relative to each other permitting a portion of the flow in the heat exchanger to pass in counterflow relationship. The core generally comprises parting sheets mounted in spaced stacked relationship defining alternate layers of open-ended channels where fluid in alternate layers passes parallel to, but sealed from, the fluid in the adjacent layer. Fins between the parting sheet, in the heretofore known counterflow heat exchanger, are disposed at angles to change the direction of the flow so that at least a portion of the fluid will pass in counterflow relationship which in certain heat exchangers is undesirable and results in a loss in heat transfer effectiveness when compared with the eflectiveness possible with pure counterflow. Thus, a larger heat exchanger is necessary to handle the heat transfer load.
I have found that the problem noted above can be obviated by using triangular-shaped distribution chambers in the header for distribution of the fluid through the thermodynamic core such that it passes in pure counterflow heat exchange relationship. The triangular chambers are outside of the thermodynamic core and hence, are not supported by the fins. Instead they are supported by any suitable means dictated by structure precluding the possibility of having cross-flow sections within the thermodynamic core while allowing all the heat transfer to occur in pure counterflow which is sufliciently more efficient to compensate for the triangular chambers and support structure resulting in an overall lighter weight heat exchanger manifested by the increased heat transfer effectiveness.
SUMMARY OF THE INVENTION A primary object of this invention is to provide an improved headering for a conterflow, plate-fin heat exchanger.
In accordance with the present invention a series of stacked triangular-shaped plates mounted adjacent to and complementary with the parting sheets or formed integral therewith are disposed in the header for changing direction and distributing flow into the pure counterflow thermodynamic core section of the heat exchanger.
In accordance with the further aspect of the present invention a pair of back-to-back triangular sections of the ice headers mounted adjacent the core of the seat exchanger are ararnged so as to accommodate two dilferent fluids placed in indirect heat exchange relationship with a third fluid passing in pure counterflow heat exchange relationship.
A further object of this invention is to provide headering for a heat exchanger to assure that the fluids in indirect heat exchange relationship in the core are in pure counterflow relationship and being characterized by the fact that the overall heat exchanger is lighter in weight for the same heat transfer effectiveness that was heretofore realized.
Other features and advantages will be apparent from the specification and claims and from the accompanying drawings which illustrate an embodiment of the invention.
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a perspective view of the heat exchanger with the headering of one of the passes removed.
FIG. 2 is a sectional view taken along line '22 of FIG. 1.
FIG. 3 is a detailed view in elevation showing one pass.
FIG. 4 is a view in elevation showing an adjacent pass to the pass shown in FIG. 3.
FIG. 5 is a sectional view showing another embodiment of this invention.
DESCRIPTION OF THE PREFERRED EMBODIMENT An understanding of this invention can best be had by referring to FIGS. 1 through 4 which show a dual heat exchanger consisting of two counterflow cores of plate and fin construction. The cores are housed in a rectangularshaped box 10 having top and bottom walls 12 (only one wall being shown) and side walls 14 (only one wall being shown). The back and front faces carry flanges which are adapted to receiver headers for conducting the primary flow through the stacked open-ended channels 16. Each core channel comprises a fin section 18 sandwiched between parting sheets 20 and 22 and closure bars 24 and 25 attached at either end. The closure bars 24 and 25 serve to seal oif the edges of the fin sections and afiford structural support to the parting sheets. Typical secondary flow channels are shown in FIGS. 2 and 3, noting that they are representative of the other channels in the cores. Since all stacked channels are identical, only one will be described for the sake of simplicity.
Referring to FIG. 3 it will be noted that the core section for one of the secondary flow channels comprises a parting sheet 20 which is generally a flat sheet of metal to which is attached a plurality of parallel spaced corrugated fins 18. The spaces between the fins define openended channels for permitting fluid to flow through the core section. A second parting sheet 21 (see FIG. 1) similar to and coextensive with parting sheet 20 overlies the fins for defining therewith one of the layers in the core. Closure bars 28 and 30 extend the length of the core and are mounted adjacent the edge of the fins and serve to seal off the sides of the open-ended channels. It will be noted that the closure bars are the same height as the fins so as to be joined to the two adjacent parting sheets. Closure bar 32 is mounted between the fins and between closure bars 28 and 30 and attached to closure bars 46 and 44 to separate the core into two sections for accommodating different fluids.
In accordance with this invention distributing chambers are mounted adjacent to the core for passing fluid in the core in counterflow relation with the fluid in the adjacent layer. Each distributing chamber includes triangular-shaped parting sheets 34 mounted adjacent to and extending from parting sheets 20 and 21. The structural support shown here as straight fins 36 serve to distribute fluid admitted from manifold 38 (see FIG. 2) to the core and support the structural loads on sheet 34. These sections may be integral with the parting sheets. A similar triangular-shaped parting sheet 40 similarly supported is mounted on the opposite end of the core for receiving the fluid discharging from the core and admitting it to manifold 42 for discharging the fluid out of the heat exchanger. Closure bars 44 and 46 seal off the edges of the distributing header sections. The opposite section of the core is made in a similar manner.
FIG. 4 shows the next adjacent pass (primary flow) comprising the core section 48 formed in the same manner as the core section of the secondary fluid. This section carries triangular-shaped parting sheets or plates 50 and 52 extending from and mounted adjacent to the parting sheet 22 of the core section. The structural support shown here as straight fin 36 are arranged parallel to the flow path in the thermodynamic fin 18. Closure bars 24 and 25 mounted on the top and bottom edges serve to seal the fluid. It being noted that this channel of the core is coextensive with the next adjacent channel as shown in FIG, 1.
FIG. shows another embodiment of this invention wherein the secondary pass is constructed as a single section to accommodate one fluid rather than two as shown in FIGS. 1 through 4. The core section 60 is constructed identical to the core section described above. The triangular-shaped distributing sections 62 and 64 are substantially the same as described above but one is reversed so as to pass the flow into and out of the heat.
exchanger in Z route fashion.
It will be noted that each closure bar in the embodiments shown in FIGS. 1 through 4 and for FIG. 5 may be constructed such that the portion sealing off the edge of the core and the portion sealing Off the edge of the distributing section are made from one piece. Also the parting sheets of the core and distributing section may be integral.
It should be understood that the invention is not limited to the particular embodiments shown and described herein, but that various changes and modifications may be made without departing from the spirit or scope of this novel concept as defined by the following claims.
I claim:
1. Header construction for a plate fin heat exchanger in combination with a counterflow core section, said core section including a series of stacked coplanar plates, fins coextensively sandwiched in between said plates defining counterflow passes, the fins in adjacent passes being oriented in the same direction, said header comprising a triangular shaped header chamber formed from a series of stacked triangularly shaped flat plates, closure bars mounted alternately on the end of and between two adjacent flat plates and extending from the apex to the base of said triangle, support members mounted between said flat plates, and said triangular shaped header chambers being in register with said fins to distribute heat exchanger fluid to alternate passes.
2. A heat exchanger having plate and fin core section, first means for directing flow through alternate layers of said plate and fin section, second means for conducting flow through intervening layers of said plate and fin core section so as to direct the flow in adjacent layers in counterflow relation, said second means comprising stacked parallely spaced triangularly shaped plate members having one side mounted adjacent the core, closure bars mounted between said triangularly shaped plate members extending at one end from the apex to the base thereof for defining a passage therewith for conducting flow to said core section 3. A heat exchanger comprising a core section having parallely stacked rectangularly shaped parting sheets forming layers of passages, fins sandwiched between said parting sheets defining a plurality of open ended channels, disposed in counterflow relation, closure bars mounted between said parting sheets adjacent the opposite sides of said fins, first pair of headers mounted on opposite faces of said core adapter to conduct fluid through alternate layers of said open ended channels, header means on another side of said core and having complementary layers of parallely stacked triangularly shaped flat plates mounted adjacent said parting sheets, closure bars mounted on the outer side of alternate layers between said triangularly shaped flat plates blocking off the flow from said first pair of headers and defining a distributing chamber for conducting fluid through intervening layers of said core.
4. A heat exchanger having plate and fin core section, means for directing flow through alternate layers of said plate and fin core section, means including a distributing chamber for leading flow to intervening layers of said plate and fin core section so as to direct the flow in adjacent layers in counterflow relation, said distributing chamber comprising a first series of stacked parallely spaced triangularly shaped plate members having one side mounted adjacent the core section, closure bars mounted between said triangularly shaped plate members extending at one end from the apex to the base thereof for defining a passage for conducting fiow to said core section, said apex being located at one end of said core section, and a receiving chamber having a second series of stacked parallely spaced triangular shaped plate members having I one side mounted adjacent the opposite side of said core section, closure bars mounted between said triangularly shaped plate members extending at one end from the apex to the base thereof for defining a passage therewith for receiving flow discharging from said core section.
References Cited UNITED STATES PATENTS 1,409,520 3/1922 Bird 166 X 3,166,122 1/1965 Hryniszak 165166 X 3,198,248 8/1965 Stack 165166 3,322,189 5/1967 Topouzian 165134 X ROBERT A. OLEARY, Primary Examiner T. W. STREULE, Assistant Examiner
US751961A 1968-08-12 1968-08-12 Header construction for a plate-fin heat exchanger Expired - Lifetime US3525390A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US75196168A 1968-08-12 1968-08-12

Publications (1)

Publication Number Publication Date
US3525390A true US3525390A (en) 1970-08-25

Family

ID=25024253

Family Applications (1)

Application Number Title Priority Date Filing Date
US751961A Expired - Lifetime US3525390A (en) 1968-08-12 1968-08-12 Header construction for a plate-fin heat exchanger

Country Status (3)

Country Link
US (1) US3525390A (en)
FR (1) FR2015498B1 (en)
GB (1) GB1267839A (en)

Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3759323A (en) * 1971-11-18 1973-09-18 Caterpillar Tractor Co C-flow stacked plate heat exchanger
US3877519A (en) * 1973-07-30 1975-04-15 Gen Electric Pressurized strongback regenerator
US4042018A (en) * 1975-09-29 1977-08-16 Des Champs Laboratories Incorporated Packaging for heat exchangers
US4081025A (en) * 1974-05-24 1978-03-28 Borg-Warner Corporation Multiple fluid stacked plate heat exchanger
US4187090A (en) * 1978-09-29 1980-02-05 United Technologies Corporation Heat exchanger water collection system
US5121792A (en) * 1987-12-10 1992-06-16 Sita Maschinenbau- Und Forschungs Gmbh Countercurrent heat-exchanger
US20030116311A1 (en) * 2001-12-20 2003-06-26 Fitzpatrick Michael D. High temperature primary surface recuperator air cell
US20030213242A1 (en) * 2000-10-04 2003-11-20 Volvo Teknisk Utveckling Ab Thermal energy recovery device
US6705392B2 (en) * 2001-03-05 2004-03-16 Nissan Motor Co., Ltd. Heat exchanger
US20070074858A1 (en) * 2001-09-28 2007-04-05 Honeywell International Heat exchanger
US20070261836A1 (en) * 2004-06-15 2007-11-15 Behr Gmbh & Co.. Kg Heat Exchanger with an All-Metal Construction, in Particular an All-Aluminium Construction
US20080196871A1 (en) * 2005-06-29 2008-08-21 Alfa Laval Vicarb Condenser-Type Welded-Plate Heat Exchanger
US20120186282A1 (en) * 2011-01-20 2012-07-26 Hamilton Sundstrand Corporation Recirculation heat exchanger outlet header
US20170115026A1 (en) * 2014-04-02 2017-04-27 Level Holding B.V. Recuperator, the Heat-Exchanging Channels of which Extend Transversely of the Main Flow Direction
US11035626B2 (en) * 2018-09-10 2021-06-15 Hamilton Sunstrand Corporation Heat exchanger with enhanced end sheet heat transfer
US11162737B2 (en) * 2019-04-29 2021-11-02 Hamilton Sundstrand Corporation Offset/slanted cross counter flow heat exchanger
US11686530B2 (en) * 2018-03-16 2023-06-27 Hamilton Sundstrand Corporation Plate fin heat exchanger flexible manifold
US12013194B2 (en) 2019-04-29 2024-06-18 Hamilton Sundstrand Corporation Asymmetric cross counter flow heat exchanger

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1409520A (en) * 1920-05-08 1922-03-14 Bird John Cooling, heating, and ventilating apparatus
US3166122A (en) * 1962-03-30 1965-01-19 Parsons C A & Co Ltd Plate type heat exchangers with pairs of spaced plates and corrugated inserts
US3198248A (en) * 1963-04-10 1965-08-03 Minnesota Mining & Mfg Corrugated heat transfer exchangers
US3322189A (en) * 1965-12-21 1967-05-30 Ford Motor Co Heat exchange assembly

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB694890A (en) * 1950-03-30 1953-07-29 Air Preheater Mounting sinusoidal fin elements in heat exchange envelope
FR1396037A (en) * 1963-04-29 1965-04-16 Cie Europ Des Materiels Thermi heat exchanger
FR1496793A (en) * 1966-08-12 1967-10-06 Improvements to parallel channel heat exchangers separated by plates

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1409520A (en) * 1920-05-08 1922-03-14 Bird John Cooling, heating, and ventilating apparatus
US3166122A (en) * 1962-03-30 1965-01-19 Parsons C A & Co Ltd Plate type heat exchangers with pairs of spaced plates and corrugated inserts
US3198248A (en) * 1963-04-10 1965-08-03 Minnesota Mining & Mfg Corrugated heat transfer exchangers
US3322189A (en) * 1965-12-21 1967-05-30 Ford Motor Co Heat exchange assembly

Cited By (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3759323A (en) * 1971-11-18 1973-09-18 Caterpillar Tractor Co C-flow stacked plate heat exchanger
US3877519A (en) * 1973-07-30 1975-04-15 Gen Electric Pressurized strongback regenerator
US4081025A (en) * 1974-05-24 1978-03-28 Borg-Warner Corporation Multiple fluid stacked plate heat exchanger
US4042018A (en) * 1975-09-29 1977-08-16 Des Champs Laboratories Incorporated Packaging for heat exchangers
US4187090A (en) * 1978-09-29 1980-02-05 United Technologies Corporation Heat exchanger water collection system
US5121792A (en) * 1987-12-10 1992-06-16 Sita Maschinenbau- Und Forschungs Gmbh Countercurrent heat-exchanger
US7152407B2 (en) * 2000-10-04 2006-12-26 Volvo Technology Corporation Thermal energy recovery device
US20030213242A1 (en) * 2000-10-04 2003-11-20 Volvo Teknisk Utveckling Ab Thermal energy recovery device
US6705392B2 (en) * 2001-03-05 2004-03-16 Nissan Motor Co., Ltd. Heat exchanger
US20070074858A1 (en) * 2001-09-28 2007-04-05 Honeywell International Heat exchanger
US7493942B2 (en) * 2001-09-28 2009-02-24 Honeywell International, Inc. Heat exchanger
US20030116311A1 (en) * 2001-12-20 2003-06-26 Fitzpatrick Michael D. High temperature primary surface recuperator air cell
US20070261836A1 (en) * 2004-06-15 2007-11-15 Behr Gmbh & Co.. Kg Heat Exchanger with an All-Metal Construction, in Particular an All-Aluminium Construction
US8443869B2 (en) * 2005-06-29 2013-05-21 Alfa Laval Vicarb Condenser-type welded-plate heat exchanger
US20080196871A1 (en) * 2005-06-29 2008-08-21 Alfa Laval Vicarb Condenser-Type Welded-Plate Heat Exchanger
US8601826B2 (en) * 2011-01-20 2013-12-10 Hamilton Sundstrand Corporation Recirculation heat exchanger outlet header
US20120186282A1 (en) * 2011-01-20 2012-07-26 Hamilton Sundstrand Corporation Recirculation heat exchanger outlet header
US20170115026A1 (en) * 2014-04-02 2017-04-27 Level Holding B.V. Recuperator, the Heat-Exchanging Channels of which Extend Transversely of the Main Flow Direction
US11686530B2 (en) * 2018-03-16 2023-06-27 Hamilton Sundstrand Corporation Plate fin heat exchanger flexible manifold
US11035626B2 (en) * 2018-09-10 2021-06-15 Hamilton Sunstrand Corporation Heat exchanger with enhanced end sheet heat transfer
US11656038B2 (en) 2018-09-10 2023-05-23 Hamilton Sundstrand Corporation Heat exchanger with enhanced end sheet heat transfer
US11162737B2 (en) * 2019-04-29 2021-11-02 Hamilton Sundstrand Corporation Offset/slanted cross counter flow heat exchanger
US12013194B2 (en) 2019-04-29 2024-06-18 Hamilton Sundstrand Corporation Asymmetric cross counter flow heat exchanger

Also Published As

Publication number Publication date
GB1267839A (en) 1972-03-22
FR2015498B1 (en) 1974-03-15
FR2015498A1 (en) 1970-04-30

Similar Documents

Publication Publication Date Title
US3525390A (en) Header construction for a plate-fin heat exchanger
US4328861A (en) Louvred fins for heat exchangers
US2875986A (en) Heat exchanger
US4804041A (en) Heat-exchanger of plate fin type
US4401155A (en) Heat exchanger with extruded flow channels
US2656159A (en) Laminated heat exchanger
US3161234A (en) Multipass evaporator
US3627039A (en) Heat exchanger especially for nonstationary gas turbines
US3262496A (en) Heat exchanger construction
US2439208A (en) Heat exchanger
US6536512B2 (en) Heat exchanger block
US6892803B2 (en) High pressure heat exchanger
US2812165A (en) Header units for plate type heat exchanger
US3265129A (en) Heat exchanger construction
US3310105A (en) Heat exchanger with combined closing member and fluid distributor
GB1216306A (en) Plate-type heat exchangers
US2539870A (en) Crossflow heat exchanger
US4141412A (en) Air-to-air heat recuperating unit
US3153446A (en) Heat exchanger
US5099915A (en) Helical jet impingement evaporator
US4458750A (en) Inlet header flow distribution
US2963277A (en) Finned construction for heat exchangers
US3266568A (en) Connecting means for heat exchanger cores
US2620169A (en) Plate type heat exchanger
US2813701A (en) Cross-flow heat exchanger