WO1993017290A1 - Systeme d'echangeur thermique - Google Patents

Systeme d'echangeur thermique Download PDF

Info

Publication number
WO1993017290A1
WO1993017290A1 PCT/AU1993/000085 AU9300085W WO9317290A1 WO 1993017290 A1 WO1993017290 A1 WO 1993017290A1 AU 9300085 W AU9300085 W AU 9300085W WO 9317290 A1 WO9317290 A1 WO 9317290A1
Authority
WO
WIPO (PCT)
Prior art keywords
heat exchanger
fluid
fins
core
exchanger assembly
Prior art date
Application number
PCT/AU1993/000085
Other languages
English (en)
Inventor
Milne Jurisich
Original Assignee
Melanesia International Trust Company Limited
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 Melanesia International Trust Company Limited filed Critical Melanesia International Trust Company Limited
Priority to EP93905101A priority Critical patent/EP0627065B1/fr
Priority to AU36226/93A priority patent/AU663168B2/en
Priority to JP5514401A priority patent/JPH07504264A/ja
Priority to US08/295,642 priority patent/US20010040025A1/en
Publication of WO1993017290A1 publication Critical patent/WO1993017290A1/fr
Priority to KR1019940703032A priority patent/KR950700529A/ko

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F42—AMMUNITION; BLASTING
    • F42B—EXPLOSIVE CHARGES, e.g. FOR BLASTING, FIREWORKS, AMMUNITION
    • F42B12/00—Projectiles, missiles or mines characterised by the warhead, the intended effect, or the material
    • F42B12/72—Projectiles, missiles or mines characterised by the warhead, the intended effect, or the material characterised by the material
    • F42B12/74—Projectiles, missiles or mines characterised by the warhead, the intended effect, or the material characterised by the material of the core or solid body
    • 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
    • F28F1/12—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
    • F28F1/14—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending longitudinally
    • F28F1/16—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending longitudinally the means being integral with the element, e.g. formed by extrusion
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D1/00—Heat-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
    • F28D1/02—Heat-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
    • F28D1/0246—Heat-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 heat-exchange elements having several adjacent conduits forming a whole, e.g. blocks
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/0008—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one medium being in heat conductive contact with the conduits for the other medium
    • F28D7/0025—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one medium being in heat conductive contact with the conduits for the other medium the conduits for one medium or the conduits for both media being flat tubes or arrays of tubes
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/0066—Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids
    • F28D7/0083—Multi-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 a supplementary heat exchange medium, e.g. with interleaved units or with adjacent units arranged in common flow of supplementary heat exchange medium
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/02—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
    • F28F3/04—Elements 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
    • F28F3/048—Elements 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
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
    • F28D2021/008—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for vehicles
    • F28D2021/0084—Condensers
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
    • F28D2021/008—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for vehicles
    • F28D2021/0089—Oil coolers
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
    • F28D2021/008—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for vehicles
    • F28D2021/0091—Radiators
    • F28D2021/0094—Radiators for recooling the engine coolant
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
    • F28D2021/008—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for vehicles
    • F28D2021/0091—Radiators
    • F28D2021/0096—Radiators for space heating

Definitions

  • This invention relates to improved heat exchanger cores and in particular heat exchanger cores which incorporates a plurality of heat exchanger elements or modules which may be utilised in applications where heat energy is to be transferred from one fluid to another.
  • heat exchangers There are many types of heat exchangers known. These can be generally divided into two main groups, the first being shell-and-tube heat exchangers and the second being plate heat exchangers.
  • One example of a shell and tube heat exchanger comprises an array or bundle of tubes and a surrounding for external shell.
  • Plate heat exchangers may have plate-fin arrangements such as described in U.S.A. Patent 4,282,927 or a series of rectangular stacked plates creating flow channels from two or more fluids when the plates are sealingly stacked upon one another as described for example in U.S. Patent 4,823,867.
  • each of the two groups in order to manufacture the heat exchanger, a number of parts are usually fabricated and joined together.
  • shell and tube heat exchangers for example, a number of tubes are assembled into a bundle, and prior to having the ends of each tube sealed into corresponding apertures of a pair of tube sheets, baffles are installed along the length of the bundle.
  • the bundle of tubes, baffles and tube sheets are then placed inside a pressure vessel which seals a pair of end zones around the tube sheets so that there are two fluid flow paths defined, the first being around the outside of the tubes and between the tube sheets, and the second being inside the tubes and in end chambers of the pressure vessel.
  • the shell and tube configuration and the plate type heat exchanger there is a large amount of material dedicated to defining and sealing fluid flow paths, and since the flow paths are defined by joining fabricated parts, there is always the danger of one fluid leaking into another.
  • fabricated heat exchangers suffer from inefficiency brought about by a plurality of boundaries constituted by welds, joins or parts interconnecting adjacent components of the heat exchangers, the boundaries providing zones of resistance to the conduction of heat to heat transmission surfaces of the exchanger.
  • An integral part of heat exchangers formed by processes such as extrusion or casting are known as “primary structure” and must be differentiated from components welded or otherwise attached to the primary structure wherein such components including the boundaries are termed “secondary” structure.
  • surface(s) of primary structure are known as “primary” surface(s) and surface(s) of "secondary” structure known as “secondary" surface(s).
  • U.S. Patents 3,743,252; 4,352,008; 3,566,959, 4,567,074; 3,137,785 show that formation of one piece extrusions are not new and thus U.S. Patent 3,137,785 shows a one piece extrusion for use as a component in an electric heater comprising a body with longitudinally extending fins on each side of the body. Within the body are a plurality of extruded passages. However these internal passages are for receiving and containing tubular heating elements or thermally sensitive control elements and are not fluid passages.
  • U.S. Patent 3,566,959 concerns an aluminium extrusion for use as a heat sink in semi conductor rectifiers.
  • U.S. Patent 4,657,074 refers to a one piece aluminium extrusion tubular heat exchanger element which has a tubular body and a number of interior and exterior fins projecting integrally radially from the tubular body. However this reference is not considered relevant to this invention.
  • U.K. Patent 2 142 129 which describes a radiator formed from a rectangular elongate hollow body which is provided on each of two opposite sides with a plurality of spaced heat radiating fins to thus form a plurality of air channels located intermediate mutually adjacent fins.
  • a cover plate extends across outer edges of each set of fins to form with said fins a plurality of open ended channels through which can flow air which is heated by a transfer of heat from a hot fluid flowing through the elongate hollow bod .
  • U.S. Patent 4,401,155 relates to a heat exchanger constructed from a plurality of stacked modules wherein each module has closed channels for high pressure flow and fins extending vertically up and/or down from the channels which form open channels suitable for low pressure flow when the modules are stacked parallel to each other along their length. It is specified that each fin be of uniform thickness and have an identical dimension perpendicular to the channels. Each module is generally formed from an aluminium extrusion.
  • the heat exchanger of U.S. Patent 4,401,155 is particularly directed at high pressure applications and especially where one heat exchange stream is at high pressure and another is at lows pressure. This has particular reference to cryogenic processes.
  • U.S. Patent 4,401,155 it is noted in regard to a first embodiment (i.e. FIGS 1, 3 and 4) that there are provided as many channels as there are fins while in another second embodiment (i.e. in FIGS 2, 6, 7 and 8) there are provided two channels for every fin.
  • the heat exchanger assembly would not be efficient in relation to effective heat transfer because of the fact that the channel surface area is substantially the same as the fin surface area and in this regard it has been ascertained as described in more detail hereinafter that for efficient heat transfer to take place the surface area of the fins should be substantially greater than the surface area of the channels.
  • This is important in a situation wherein the density of one fluid which may pass through the fins (e.g. air) is significantly different to the density of the fluid passing through the channels (eg water) . In this situation air has a density much less than water and this means that air will have a much less effective heat storage capacity than water.
  • heat exchangers formed as one piece extrusions having a plurality of fins generally will also be subject to the same disadvantages as described and thus references such as U.S. Patent 3,202,212, Australian Patent 85777/75, U.S. Patents 4,565,244; 3,743,252; 4,352,008; 3,566,959; 4,567,074; 3,137,785 and 3,467,180 will also be subject to these disadvantages.
  • thermoelectric cooler wherein semiconductor materials with dissimilar characteristics are connected electrically in series and thermally in parallel so that two junctions are created.
  • the semiconductor materials are N and P-type.
  • thermoelectrical cooler In a typical thermoelectrical cooler (TEC), alternative columns of these N-type and P- type semiconductor materials have their ends connected in a serpentine fashion by electrical conductors. These electrical conductors typically are metallisations formed on insulating or ceramic plates. With the application of direct current to the TEC, heat is absorbed on the cold side ceramic, passes through the semiconductor material and is dissipated at the hot side ceramic. A heat sink must be attached to the hot side ceramic for dissipating the heat from the TEC to the surrounding environment. Without a heat sink the TEC would overheat and fail within seconds.
  • a heat sink is a device that is generally associated with machines or apparatus which generates substantial amounts of heat such as a TEC, or a computer so that the heat may be rapidly dissipated. Therefore a heat sink is more effective when it may dissipate heat at greater rates.
  • U.S. Patent 5,042,257 therefore describes a heat sink for a TEC which includes a pair of opposed plates which have a plurality of fins on each of opposed faces wherein one array of fins on one face may be accommodated or interleaved between another array of fins on the other face whereby one array of fins may be retained in desired position by suitable retaining means such as a pair of relatively short fins which constitute thermal surface area contacts for sufficient exchange of heat.
  • the heat exchanger assembly of the invention is formed from primary structure comprises a core comprising a multiplicity of primary fluid sections and a plurality of secondary fluid sections wherein a respective primary fluid section is located adjacent to a respective secondary fluid section wherein each primary fluid section is substantially parallel to each secondary fluid section characterised in that each primary fluid section is bounded by a peripheral wall and that each secondary fluid section include a first array of fins extending away from the peripheral wall of one adjoining primary fluid section and a second array of fins extending away from the peripheral wall of another adjoining fluid section wherein an individual first fin may extend between each adjacent second fin in interleaved relationship wherein the surface area of each secondary fluid section is substantially greater than the surface area of each primary fluid section.
  • the primary fluid sections are provided with a plurality of webs wherein each web extends from opposed faces of the peripheral wall to thereby provide a number of parallel primary fluid passages.
  • the webs are useful for strengthening and reinforcement purposes to maintain the structural integrity of the core.
  • the tips of the first array of fins abut or are attached to an adjacent surface of the peripheral wall of said another adjoining fluid section.
  • the tips of the first array of fins are spaced from the adjacent surface.
  • the tips of the second array of fins may abut or be attached to an adjacent surface of the said one adjoining fluid section but more preferably are spaced therefrom.
  • each secondary fluid section may correspond to a single flow passage for secondary fluid.
  • a heat exchanger core which may be formed in one piece such as an extrusion formed from aluminium or other suitable metal.
  • the core be formed from a plurality of separate modules.
  • a particular module may include the peripheral wall which bounds the flow passages for primary fluid and both the first and second array of fins which extend away from external or outer surfaces of opposed parts of the peripheral wall respectively.
  • the peripheral wall and the elongate fins of each module are each formed simultaneously in formation of the one piece extrusion or casting so that the heat exchanger module is formed from primary structure.
  • the primary fluid passages and the secondary fluid passages are substantially parallel to each other -to form a parallel flow heat exchanger core which has advantages over cross flow heat exchangers of the type described previously. These advantages include the following - (i) with the secondary fluid comprising a cooling medium such as air, the parallel flow arrangement facilitates ducting of air both to and from the heat exchanger core. A fan may then be used to draw the air through and the hot air away from the heat exchanger core.
  • the heat exchange core of the invention does not have to rely upon ambient air passing through when used for example as a radiator in a motor vehicle. Therefore the heat exchanger core of the invention need not be located in front of the vehicle. (ii) when used as a radiator, the heat exchanger core of the invention need not have a large flat surface as is the case with a conventional radiator. Therefore it can be designed in a far more compact configuration. This means that the shape of the vehicle may be changed to permit reduced wind resistance in the case of a truck or increased usage of the interior in the case of a coach or bus.
  • the ducting of the hot air away from the heat exchanger core of the invention also facilitates the use of the hot air for other purposes such as for the supply of heat or as a power source, (iv) because the fluid passages are parallel
  • the heat exchanger element of the invention may be manufactured as a one piece extrusion. An extrusion could not be satisfactorily produced in the case of a crossflow arrangement.
  • the fins form an integral part of the heat exchanger core of the invention rather than being crimped, welded or soldered to the part. This avoidance of secondary structure maximises conductivity of the heat from the fluid to be cooled to the other fluid.
  • the one piece extrusion may be cut to any desired length and may be designed to be releasably attached to other heat exchanger elements or modules to produce a core of the invention. Not only length but height and width are all flexible and may be varied to suit the particular application desired, (vi) the heat exchanger core of the invention when compared to the prior art is far more efficient and also lighter. It also requires less power from the main power sources (e.g. an engine or motor) for operational purposes.
  • the core of the heat exchanger apparatus may take any form consistent with the function of providing definition for flow of both primary and secondary fluids.
  • the core may comprise a continuous cross section of indefinite length with the flow passages being disposed in the direction of the indefinite length.
  • each module is substantially rectangular having a pair of opposed substantially horizontal parts in use which are joined by a pair of opposed vertical parts.
  • the abovementioned webs of the primary fluid section formed by the peripheral wall are preferably substantially parallel to the vertical parts.
  • peripheral wall may have any other suitable shape such as being circular in cross section or triangular in cross section or polygonal in cross section.
  • the primary flow passages of the primary fluid section may have any suitable shape or configuration and thus may be round, rectangular or polygonal in cross section.
  • each fin may have any suitable shape.
  • each fin is of constant height and width although this is not absolutely essential.
  • each elongate fin is of constant height and width although this is not absolutely essential.
  • each elongate fin may taper in width from one end to the other if required if the heat exchange element of the invention is produced as a casting.
  • the elongate fins may also have projections or ribs on an outer surface to increase their surface area if required. It is also within the scope of the invention to have internal fins located in the flow passages of the body part if such is considered appropriate.
  • the heat exchanger cores of the invention may be provided with manifolding means adapted to supply the primary and secondary fluids to their respective flow sections and such manifolding means may take any appropriate form.
  • manifolding means may take any appropriate form.
  • an inlet manifold and an outlet manifold may be provided which enable primary fluid to communicate with the primary fluid section and secondary fluid to communicate with the secondary fluid section.
  • separate primary fluid and secondary fluid manifolds may be provided at inlet and outlet.
  • the flow of primary fluid and secondary fluid through their respective manifolds may also be normal to each other although this is not essential and the respective manifolds may be constructed so that the primary and/or the secondary fluid may flow at an acute angle to their respective core entry and core exit flow directions.
  • the primary fluid is suitably an "operating fluid” i.e. a fluid which is being processed by the heat exchanger and which is to be recirculated through a suitable flow system to which the heat exchanger of the invention is being applied.
  • an "operating fluid” i.e. a fluid which is being processed by the heat exchanger and which is to be recirculated through a suitable flow system to which the heat exchanger of the invention is being applied.
  • a fluid is suitably water.
  • the secondary fluid is preferably "an active fluid" which functions as a coolant for the operating fluid and which absorbs heat from the operating fluid after passage through the heat exchanger core.
  • an active fluid for vehicle radiators for example may comprise air.
  • the above is not essential and the "active fluid” in accordance with this invention may become the "operating fluid” if necessary.
  • the heat exchange modules for use in the invention may be adapted for vertical stacking or horizontal stacking as may- be required.
  • each module may be provided with connection means for this purpose.
  • the connection means may be such that interconnection of the adjacent modules defines a suitable flow passage for secondary fluid.
  • each module has integrally extruded therewith connection means to enable adjacent modules of the invention to be assembled together.
  • the connection means may be of any suitable type and thus comprise for example male members or projections engageable with female members or sockets in snap fit or interference fit relationship.
  • each module includes a top connection member and bottom connection member which may engage with corresponding top and bottom connection members of an adjacent module.
  • the top or bottom connection member may comprise a panel rib or flange which may engage with a corresponding ratchet rib or flange of a mating top or bottom connection member of an adjacent module.
  • Heat exchanger cores in accordance with the present invention may be used in gas/gas, liquid/gas or liquid/liquid application and are particularly suited to gas/air and liquid/air applications using impelled ambient air as the heat transfer fluid.
  • the cores can be placed in an enclosure suitable for natural or draft convection of air.
  • heat transfer fluids other than air may be employed, such as water, ethylene glycol, ammonia, fluorocarbon compounds, silicone compounds, mineral oils and the like.
  • co-current flow may be utilised.
  • the heat exchanger cores of the present invention may be of any suitable material, the suitability of a material being generally determined with reference to the application to which it is to be put. For example, use in extreme high temperature applications may dictate that a ceramic material be used for its high temperature properties, whereas for lower temperature applications it has been found that aluminium or its alloys or other metals are suitable for their relatively high thermal conductivities, permitting thicker wall sections per unit efficiency and thus increasing mechanical strength.
  • FIG 1 is an end view of a stack of four modules in regard to providing a heat exchanger core constructed in accordance with the invention
  • FIG 2 is a similar view of the core as shown in FIG 1 with external fins removed;
  • FIG 3 is a perspective view of a heat exchanger module constructed in accordance with the invention.
  • FIG 4 shows heat exchanger apparatus constructed in accordance with the invention with appropriate manifolds and using the core of FIG 2;
  • FIG 5 is a view of the heat exchanger assembly of the invention when used in vehicle engines.
  • FIG 6 is a detailed view of a fin of the module of FIG 3 showing the temperature distribution in use of not only the fin but also the spaces between adjacent fins.
  • BEST METHOD FOR CARRYING OUT THE INVENTION In FIG 1 there is shown heat exchanger core 10 in accordance with the invention including a vertical stack of modules 11.
  • Each module 11 includes a peripheral wall 12 of shallow rectangular configuration having opposed horizontal parts 13 and opposed vertical parts 14.
  • the peripheral wall 12 which is of a continuous nature defines a primary fluid section 15.
  • Webs 16 are included to define separate primary flow passages 17.
  • first array of fins 18 extending away from one horizontal part 13 and a second array of fins 19 extending away from the opposed horizontal part 13 of peripheral wall 12.
  • a section 20 for passage of secondary fluid is therefore defined by fins 18 extending between adjacent fins 19 and terminating short of an adjacent horizontal section 13 of wall 12 to define a space 21 and fins 19 extending between adjacent ribs 18 and terminating short of an adjacent horizontal section 13 of wall 12 to define a space 21.
  • Each adjacent module 11 is attached by ribs 23 of one module engaging with the ends 24 of vertical extensions 25A of terminal vertical parts 14 of each peripheral wall 12.
  • heat exchanger core 10 are primary fluid section(s) 15 and secondary fluid section(s) 17. Therefore ducts or manifolds communicating with sections 15 and 17 do so in the area between dotted lines AA and BB.
  • This means that the external fins 18A and 19A have no function in regard to heat exchanger apparatus of the invention 10 and may be omitted or cut off.
  • outer extensions 25A This will mean that the effective core of the heat exchanger apparatus of the invention is as shown in FIG 2. Ribs 23A may also be omitted.
  • FIG 2 therefore defines a core 1 OA which has been constructed in accordance with the invention. This of course does not mean that core 10 cannot be utilised. It is just more convenient to use core 10A because of the saving in space or storage capacity within a heat exchanger system which also incorporates appropriate inlet and outlet manifolds.
  • FIG 3 shows a perspective view of an individual module for use in the core 10 and 1 OA shown in FIGS 1-2.
  • Each of fins 18 and 19 may be provided with peripheral ribs 18B and 19B of relatively thin cross section.
  • heat exchanger apparatus 26 in accordance with the invention which includes a gas or air inlet duct or manifold 27 having inlet 28, core 1 OA constructed of five modules 11 , assembled as shown in FIGS 1-2, an air or gas outlet duct or manifold 28 with outlet 29, gas or air sections 20 including fins 18 and 19, liquid sections 15, welded areas 32 of liquid sections 15 which function as a plug or cover to prevent air or gas gaining access to sections 20, and liquid inlet manifold 33 with inlet conduits 34, 35, 36 and 37 and liquid outlet manifold 38 with associated outlet conduits 39, 40, 41 and 42.
  • the inlet manifold 33 has respective compartments 34A, 35A, 36A and 37A which register with inlet slots 34B (i.e.
  • outlet manifold 38 has outlet compartments 39A, 40A, 41A and 42A which register with outlet slots 39B (i.e. there are two of these slots), 40B, 41B and 42B respectively.
  • one manifold 27 may be utilised adjacent the inlet end of core 10A whereby forced air (e.g. by use of an air blower or air compressor) may be forced through core 10A or alternatively only one manifold 27 may be utilised adjacent the outlet end of core 10A whereby air may be forced through core 1OA by use of an exhaust fan.
  • forced air e.g. by use of an air blower or air compressor
  • the heat exchanger apparatus 26 is used for gas and liquid heat transfer.
  • gas inlet and outlet manifolds are located at opposed ends of the core and liquid inlet and outlet manifolds are located on the same side or on different sides if appropriateor even on top and/or bottom of the core if appropriate.
  • the gas therefore may make one pass through the core and the liquid may also make a single pass through the core.
  • Each of the liquid manifolds may have a single inlet and single outlet if the same fluid is being processed or different inlets and outlets as shown in FIG 4 if different liquids are being processed by core 10A.
  • conduit 34 may be used for engine cooling water
  • conduit 35 used for engine oil
  • conduit 36 used for transmission oil
  • conduit 37 used for condensing liquid for air conditioning.
  • Conduits 39, 40, 41 and 42 have the same functions as an outlet conduit.
  • FIG 5 reference is shown to truck or vehicle 63 wherein fuel from engine 64 is passed through line 65 to a heat exchanger assembly 66 constructed in accordance with the invention.
  • the fuel tank 67 may also be utilised which then passes the fuel back to the engine 64 through line 68.
  • a heat exchanger core constructed in accordance with the invention will overcome the disadvantages of the prior art discussed in detail above because a uniform heat distribution will be obtained throughout the core by the location of fins 18 and 19 as illustrated whereby the tips of the fins 18 and 19 which are normally the coolest part of a conventional heat exchanger core are placed in close proximity to the hottest part of a conventional heat exchanger core which is the peripheral wall 12. It therefore follows that the temperature of the core at the tips of the fins 18 and 19 will be substantially the same or slightly less than the temperature of the peripheral wall 12. This will mean that a uniform heat distribution or temperature distribution will be obtained in each of the liquid sections 20 and this will bring about substantially improved heat exchanger efficiency. Heat exchanger efficiency will also be improved by the manufacture of core 10 or 1 OA as a single piece aluminium extrusion or alternatively being comprised of a stack of modular aluminium extrusions 10 or 10A.
  • FIG 6 shows the temperature distribution through an individual fin 18 or 19 and adjacent spaces 22A in relation to a conventional heat exchanger.
  • the heat exchanger apparatus of the invention will be most useful in regard to function as a vehicle radiator but this does not preclude its use as a heat exchanger in relation to processing of gas to gas or liquid to liquid applications as discussed above.
  • the thickness of peripheral wall 12 and also of vertical extensions 25 is substantially the same and is of relatively narrow thickness e.g., about 3 mm or less and more suitably 2 mm or less and of the order of 1.5 mm or 1.0 mm or less.
  • the surface area of the secondary flow sections 20 is at least twice the surface area and more preferably is at least 7 times the area of primary fluid sections 15.
  • spaces 21 should be substantially uniform and this also applies to the spaces 22 between adjacent fins 18 or 19. Naturally each fluid channel 17 should also be substantially of the same volume.

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Geometry (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Separation By Low-Temperature Treatments (AREA)

Abstract

Un échangeur termique a un noyau constitué de modules (11) fait d'une seule pièce. Chaque module entoure des canaux (17) séparés par des nervures de renforcement (16) et ses faces larges externes portent des agencements de nervures de refroidissement respectives (18, 19). En empilant les modules avec les agencements de nervures en regard venant s'imbriquer ensemble, on forme d'autres canaux (20). La surface élevée des canaux (20) par comparaison avec celle des canaux (15) (le rapport des surfaces et de préférence supérieur à 7:1) fait que l'empilement de modules convient pour un échange thermique entre deux fluides de capacité calorifique différente circulant parallèlement et à contre-courant. L'appareil préféré comporte une circulation d'air forcée assurée par un ventilateur alimentant les canaux (20) par l'intermédiaire de distributeurs droits. Les nervures imbriquées servent à régulariser la température de l'air et sa vitesse dans le sens de la largeur des canaux. Les extrémités des canaux (17) sont fermées et un liquide (ou des liquides) entrent et sortent des canaux (17) à angles droits par rapport à ceux-ci, bien qu'une fois dans les canaux (17) le liquide s'écoule parallèlement et à contre-courant par rapport au flux d'air.
PCT/AU1993/000085 1992-02-28 1993-03-01 Systeme d'echangeur thermique WO1993017290A1 (fr)

Priority Applications (5)

Application Number Priority Date Filing Date Title
EP93905101A EP0627065B1 (fr) 1992-02-28 1993-03-01 Systeme d'echangeur thermique
AU36226/93A AU663168B2 (en) 1992-02-28 1993-03-01 Heat exchanger assembly
JP5514401A JPH07504264A (ja) 1992-02-28 1993-03-01 熱交換器アセンブリ
US08/295,642 US20010040025A1 (en) 1992-02-28 1993-03-01 Heat exchanger element
KR1019940703032A KR950700529A (ko) 1992-02-28 1994-08-29 열교환기 어셈블리

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
AUPL1129 1992-02-28
AUPL112992 1992-02-28

Publications (1)

Publication Number Publication Date
WO1993017290A1 true WO1993017290A1 (fr) 1993-09-02

Family

ID=3776012

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/AU1993/000085 WO1993017290A1 (fr) 1992-02-28 1993-03-01 Systeme d'echangeur thermique

Country Status (8)

Country Link
US (1) US20010040025A1 (fr)
EP (1) EP0627065B1 (fr)
JP (1) JPH07504264A (fr)
KR (1) KR950700529A (fr)
AU (1) AU663168B2 (fr)
CA (1) CA2117566A1 (fr)
ES (1) ES2133389T3 (fr)
WO (1) WO1993017290A1 (fr)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0693171A1 (fr) * 1993-03-29 1996-01-24 Melanesia International Trust Company Limited Ensemble echangeur de chaleur
EP0907061A2 (fr) * 1997-10-01 1999-04-07 Behr GmbH & Co. Echangeur de chaleur pour une installation de climatisation d'un véhicule automobile
DE102007022807A1 (de) * 2007-05-15 2008-11-20 Volkswagen Ag Wärmetauscher
NL2002567C2 (en) * 2009-02-26 2010-08-30 Hld Dejatech B V Heat exchanger and method for manufacturing such.
ITMN20100007A1 (it) * 2010-03-26 2011-09-27 Daniele Bresti Scambiatore di calore.
CN104101229A (zh) * 2014-07-11 2014-10-15 江苏五晟机械制造有限公司 一种冷凝器
WO2011117907A3 (fr) * 2010-03-26 2014-10-30 Cubo D S.R.L. Échangeur de chaleur
CN105486125A (zh) * 2016-01-11 2016-04-13 芜湖美的厨卫电器制造有限公司 换热器和热水器
US9903249B2 (en) 2014-07-28 2018-02-27 Eberspächer Climate Control Systems GmbH & Co. KG Heat exchanger arrangement, especially for a vehicle heater

Families Citing this family (27)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6969506B2 (en) * 1999-08-17 2005-11-29 Battelle Memorial Institute Methods of conducting simultaneous exothermic and endothermic reactions
EP1438537A4 (fr) * 2001-09-21 2005-04-13 Collins & Aikman Automotive Co Ventilateur soufflant non mecanique
FR2843448B1 (fr) * 2002-08-08 2005-04-29 Valeo Thermique Moteur Sa Echangeur de chaleur plan, en particulier pour vehicule automobile, et procede pour sa fabrication
DE10304077A1 (de) * 2003-01-31 2004-08-12 Heinz Schilling Kg Luft-/Wasser-Wärmetauscher mit Teilwasserwegen
US7044211B2 (en) * 2003-06-27 2006-05-16 Norsk Hydro A.S. Method of forming heat exchanger tubing and tubing formed thereby
US7648686B2 (en) * 2004-04-05 2010-01-19 Modine Manufacturing Company Actively cooled exothermic reactor
GB2424265A (en) * 2005-02-16 2006-09-20 Timothy Frank Brise Heat Exchanger including Heat Exchange Tubes with Integral Fins
BE1016886A3 (nl) * 2005-12-09 2007-09-04 Atlas Copco Airpower Nv Verbeterde warmtewisselaar.
US8192832B1 (en) * 2006-12-20 2012-06-05 Lang Ko C Structured packing with interleaved heat-transfer surfaces
DE102007043992B4 (de) * 2007-09-14 2009-08-27 Pierburg Gmbh Ladeluftmodul für eine Verbrennungskraftmaschine
CN103206875A (zh) * 2013-03-28 2013-07-17 尚小女 改进的热交换器
CN103206874A (zh) * 2013-03-28 2013-07-17 尚小女 汽车废气热交换器
CN103206877A (zh) * 2013-03-28 2013-07-17 尚小女 热交换器
US9404691B2 (en) * 2013-07-24 2016-08-02 Cale Patrick Collins Kaupp Condensing heat recovery unit for a portable fluid heater
JP6405914B2 (ja) * 2014-11-11 2018-10-17 株式会社デンソー 熱交換装置及び熱交換装置の製造方法
CN104654433B (zh) * 2014-12-31 2018-05-01 宁波先锋电器制造有限公司 带有曲折散热部的散热片及使用该散热片的电热油汀
JP6533070B2 (ja) * 2015-02-26 2019-06-19 株式会社ティラド 偏平チューブおよび熱交換器
DE102016102893A1 (de) * 2016-02-18 2017-08-24 Webasto SE Wärmetauschersystem
US11879691B2 (en) * 2017-06-12 2024-01-23 General Electric Company Counter-flow heat exchanger
US11808529B2 (en) * 2018-03-23 2023-11-07 Rtx Corporation Cast plate heat exchanger and method of making using directional solidification
CN210242511U (zh) 2018-07-26 2020-04-03 达纳加拿大公司 具有平行流动特征以增强热传导的热交换器
US11454450B2 (en) * 2018-12-19 2022-09-27 Honeywell International Inc. Three-way heat exchanger system for auxiliary power unit
EP3686535B1 (fr) * 2019-01-22 2024-03-06 Hitachi Energy Ltd Condensateur
CN110006174B (zh) * 2019-03-21 2023-12-19 西安交通大学 一种模块化挤压铝冷凝换热器及冷凝式锅炉
US11686537B2 (en) * 2021-04-06 2023-06-27 General Electric Company Heat exchangers and methods of manufacturing the same
US11940232B2 (en) * 2021-04-06 2024-03-26 General Electric Company Heat exchangers including partial height fins having at least partially free terminal edges
CN115143831A (zh) * 2022-07-01 2022-10-04 四川九洲电器集团有限责任公司 一种双错位型高散热性能板翅式换热器

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1021553B (de) * 1951-02-13 1957-12-27 S I R T A Soc It Radiatori Tir Heizkoerper aus nebeneinander angeordneten, senkrechten Gliedern
US4089302A (en) * 1975-05-16 1978-05-16 Remeha Fabrieken Br - The Netherlands Cast metal heat exchanger, as well as mould therefor
AU4511279A (en) * 1978-03-15 1979-09-20 Sulzer Brothers Limited Tubular heat exchanger with increased heat transfer area
DE3011011A1 (de) * 1979-03-22 1980-09-25 Hitachi Ltd Plattenwaermetauscher
US4401155A (en) * 1981-02-13 1983-08-30 Union Carbide Corporation Heat exchanger with extruded flow channels
FR2553503A1 (fr) * 1983-10-17 1985-04-19 Dietrich Sa Element de corps de chauffe a picots
EP0183211A2 (fr) * 1984-11-23 1986-06-04 Norsk Hydro A/S Modules d'échange de chaleur et méthode pour leur fabrication
EP0461781A1 (fr) * 1990-05-31 1991-12-18 Servotomic Limited Echangeur de chaleur

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0461791B1 (fr) * 1990-06-11 1997-01-02 Hector D. Barone Greffe d'aorte et appareil pour la réparation d'un anévrisme de l'aorte abdominale

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1021553B (de) * 1951-02-13 1957-12-27 S I R T A Soc It Radiatori Tir Heizkoerper aus nebeneinander angeordneten, senkrechten Gliedern
US4089302A (en) * 1975-05-16 1978-05-16 Remeha Fabrieken Br - The Netherlands Cast metal heat exchanger, as well as mould therefor
AU4511279A (en) * 1978-03-15 1979-09-20 Sulzer Brothers Limited Tubular heat exchanger with increased heat transfer area
DE3011011A1 (de) * 1979-03-22 1980-09-25 Hitachi Ltd Plattenwaermetauscher
US4401155A (en) * 1981-02-13 1983-08-30 Union Carbide Corporation Heat exchanger with extruded flow channels
FR2553503A1 (fr) * 1983-10-17 1985-04-19 Dietrich Sa Element de corps de chauffe a picots
EP0183211A2 (fr) * 1984-11-23 1986-06-04 Norsk Hydro A/S Modules d'échange de chaleur et méthode pour leur fabrication
EP0461781A1 (fr) * 1990-05-31 1991-12-18 Servotomic Limited Echangeur de chaleur

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP0627065A4 *

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0693171A1 (fr) * 1993-03-29 1996-01-24 Melanesia International Trust Company Limited Ensemble echangeur de chaleur
EP0693171A4 (fr) * 1993-03-29 1997-03-19 Melanesia Int Trust Ensemble echangeur de chaleur
EP0907061A2 (fr) * 1997-10-01 1999-04-07 Behr GmbH & Co. Echangeur de chaleur pour une installation de climatisation d'un véhicule automobile
EP0907061A3 (fr) * 1997-10-01 2000-05-03 Behr GmbH & Co. Echangeur de chaleur pour une installation de climatisation d'un véhicule automobile
DE102007022807A1 (de) * 2007-05-15 2008-11-20 Volkswagen Ag Wärmetauscher
WO2010098666A2 (fr) * 2009-02-26 2010-09-02 Hld Dejatech B.V. Échangeur de chaleur et son procédé de fabrication
NL2002567C2 (en) * 2009-02-26 2010-08-30 Hld Dejatech B V Heat exchanger and method for manufacturing such.
WO2010098666A3 (fr) * 2009-02-26 2011-04-28 Hld Dejatech B.V. Échangeur de chaleur et son procédé de fabrication
CN102439390A (zh) * 2009-02-26 2012-05-02 德扬技术全球能源方案有限公司 一种换热器及制造该换热器的方法
CN102439390B (zh) * 2009-02-26 2016-05-18 德扬技术控股有限公司 一种换热器及制造该换热器的方法
ITMN20100007A1 (it) * 2010-03-26 2011-09-27 Daniele Bresti Scambiatore di calore.
WO2011117907A3 (fr) * 2010-03-26 2014-10-30 Cubo D S.R.L. Échangeur de chaleur
CN104101229A (zh) * 2014-07-11 2014-10-15 江苏五晟机械制造有限公司 一种冷凝器
US9903249B2 (en) 2014-07-28 2018-02-27 Eberspächer Climate Control Systems GmbH & Co. KG Heat exchanger arrangement, especially for a vehicle heater
CN105486125A (zh) * 2016-01-11 2016-04-13 芜湖美的厨卫电器制造有限公司 换热器和热水器

Also Published As

Publication number Publication date
EP0627065B1 (fr) 1999-05-26
JPH07504264A (ja) 1995-05-11
US20010040025A1 (en) 2001-11-15
EP0627065A4 (fr) 1995-06-28
CA2117566A1 (fr) 1993-09-02
AU3622693A (en) 1993-09-13
AU663168B2 (en) 1995-09-28
EP0627065A1 (fr) 1994-12-07
KR950700529A (ko) 1995-01-16
ES2133389T3 (es) 1999-09-16

Similar Documents

Publication Publication Date Title
EP0627065B1 (fr) Systeme d'echangeur thermique
US4940085A (en) Fluid heat exchanger for an electronic component
US6619044B2 (en) Heat exchanger for an electronic heat pump
US6446442B1 (en) Heat exchanger for an electronic heat pump
JP5895301B2 (ja) 熱交換器
US7946339B2 (en) Multifluid heat exchanger
EP0693171B1 (fr) Ensemble echangeur de chaleur
US11223081B2 (en) Serpentine counter flow cold plate for a vehicle battery module
JP4101174B2 (ja) 熱交換器
US20040068991A1 (en) Heat exchanger for an electronic heat pump
GB2305721A (en) Multi-fluid heat exchanger with stacked plate structure
WO2019210413A1 (fr) Échangeur de chaleur doté d'une surface de transfert de chaleur multizone
US9698332B2 (en) Hybrid device comprising a thermoelectric module, notably intended to generate an electric current in a motor vehicle and a heat exchanger
US11085699B2 (en) Heat exchanger with crossover passages for cold fluid distribution
JP2019086183A (ja) 伝熱装置
CN105190922A (zh) 热电模块和包括这样的模块的热交换器
CN212340032U (zh) 动力电池组件及其换热器
US8689858B2 (en) Cooler block, especially for a change air cooler/coolant cooler
US11740028B2 (en) Two-pass heat exchanger with calibrated bypass
AU676297B2 (en) Heat exchanger assembly
CN117704682A (zh) 一种紧凑型适用于自循环蒸发冷却系统的高效板式冷凝器
JPH01193589A (ja) 積層型熱交換器
JP2001168254A (ja) 熱交換器
AU7891200A (en) A heat exchanger

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): AT AU BB BG BR CA CH CZ DE DK ES FI GB HU JP KP KR LK LU MG MN MW NL NO NZ PL PT RO RU SD SE SK UA US

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): AT BE CH DE DK ES FR GB GR IE IT LU MC NL PT SE BF BJ CF CG CI CM GA GN ML MR SN TD TG

DFPE Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101)
WWE Wipo information: entry into national phase

Ref document number: 2117566

Country of ref document: CA

Ref document number: 08295642

Country of ref document: US

WWE Wipo information: entry into national phase

Ref document number: 1993905101

Country of ref document: EP

WWP Wipo information: published in national office

Ref document number: 1993905101

Country of ref document: EP

REG Reference to national code

Ref country code: DE

Ref legal event code: 8642

WWG Wipo information: grant in national office

Ref document number: 1993905101

Country of ref document: EP