EP2192372A2 - Echangeur thermique à courants croisés - Google Patents

Echangeur thermique à courants croisés Download PDF

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Publication number
EP2192372A2
EP2192372A2 EP09176897A EP09176897A EP2192372A2 EP 2192372 A2 EP2192372 A2 EP 2192372A2 EP 09176897 A EP09176897 A EP 09176897A EP 09176897 A EP09176897 A EP 09176897A EP 2192372 A2 EP2192372 A2 EP 2192372A2
Authority
EP
European Patent Office
Prior art keywords
heat exchanger
cross
tubes
flow heat
exchanger according
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP09176897A
Other languages
German (de)
English (en)
Other versions
EP2192372A3 (fr
EP2192372B1 (fr
Inventor
Hans-Georg Herrmann
Fan Jin
Thomas Himmer
Eberhard Zwittig
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.)
Mahle Behr GmbH and Co KG
Original Assignee
Behr GmbH and Co KG
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 Behr GmbH and Co KG filed Critical Behr GmbH and Co KG
Publication of EP2192372A2 publication Critical patent/EP2192372A2/fr
Publication of EP2192372A3 publication Critical patent/EP2192372A3/fr
Application granted granted Critical
Publication of EP2192372B1 publication Critical patent/EP2192372B1/fr
Not-in-force legal-status Critical Current
Anticipated expiration legal-status Critical

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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
    • F28F21/00Constructions of heat-exchange apparatus characterised by the selection of particular materials
    • F28F21/06Constructions of heat-exchange apparatus characterised by the selection of particular materials of plastics material
    • F28F21/062Constructions of heat-exchange apparatus characterised by the selection of particular materials of plastics material the heat-exchange apparatus employing tubular conduits
    • 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
    • F28D1/053Heat-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 the conduits being straight
    • F28D1/0535Heat-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 the conduits being straight the conduits having a non-circular cross-section
    • F28D1/05366Assemblies of conduits connected to common headers, e.g. core type radiators
    • F28D1/05383Assemblies of conduits connected to common headers, e.g. core type radiators with multiple rows of conduits or with multi-channel conduits
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/12Tubular 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
    • F28F1/126Tubular 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 consisting of zig-zag shaped fins
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/12Tubular 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
    • F28F1/126Tubular 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 consisting of zig-zag shaped fins
    • F28F1/128Fins with openings, e.g. louvered fins
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F21/00Constructions of heat-exchange apparatus characterised by the selection of particular materials
    • F28F21/06Constructions of heat-exchange apparatus characterised by the selection of particular materials of plastics material
    • F28F21/067Details
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F21/00Constructions of heat-exchange apparatus characterised by the selection of particular materials
    • F28F21/08Constructions of heat-exchange apparatus characterised by the selection of particular materials of metal
    • 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
    • F28F9/04Arrangements for sealing elements into header boxes or end plates
    • F28F9/16Arrangements for sealing elements into header boxes or end plates by permanent joints, e.g. by rolling
    • F28F9/18Arrangements for sealing elements into header boxes or end plates by permanent joints, e.g. by rolling by welding
    • F28F9/182Arrangements for sealing elements into header boxes or end plates by permanent joints, e.g. by rolling by welding the heat-exchange conduits having ends with a particular shape, e.g. deformed; the heat-exchange conduits or end plates having supplementary joining means, e.g. abutments

Definitions

  • the invention relates to a cross-flow heat exchanger for a motor vehicle, with tubes which are flowed through by a medium and flowed around by another medium, with at least one collecting box into which the pipes open, and with guide elements which are arranged between the tubes.
  • Cross-flow heat exchangers can be made entirely of metal, for example aluminum, or of plastic. There are also heat exchangers in which the plastic collecting tank and the heat exchanger block are formed with the pipes and the corrugated fins made of metal. From the German disclosure documents DE 37 33 866 A1 and DE 42 44 017 A1 Heat exchangers are known with plastic water tanks, metal pipes and laminations. From the German patent application DE 100 20 798 A1 is a heat exchanger with a tube bundle is known, which is formed solely of flexible plastic tubes. The tubes are made by extruding a polyamide. Spacers hold the tubes at a selected distance.
  • German patent DE 44 11 745 C1 is a heat exchanger with a variety of heat exchanger tubes known from polytetrafluoroethylene, which are used in the end in tube sheets of polyfluoroalkyl.
  • German patent application DE 10 2005 050 293 A1 is a mat-shaped heat exchanger known by flowing through a heating or cooling medium flexible plastic pipes.
  • the mat-shaped heat exchanger is usually attached to a ceiling, a wall or on a floor and then covered by a thin plaster or screed layer.
  • the use of a contact with the plastic pipes in contact aluminum foil allows a greater distance between the plastic pipes.
  • Other heat exchangers with parts made of plastic are from the German patents DE 42 29 393 A1 .
  • DE 43 38 959 A1 and DE 195 43 740 A1 known.
  • the object of the invention is to provide a heat exchanger according to the preamble of claim 1, which is inexpensive to produce and has a relatively high efficiency.
  • the object is in a cross-flow heat exchanger for a motor vehicle, with tubes which are flowed through by a medium and are circulated by another medium, with at least one collecting box into which the tubes open, and with guide elements which are arranged between the tubes, achieved in that the collecting tank and the pipes made of plastic and the guide elements are formed of metal.
  • the collecting box can be designed, for example, essentially in the shape of a cuboid or a circular cylinder jacket, that is to say as a collecting tube.
  • the collection box can also have a different shape and is therefore referred to its function as a collector.
  • the tubes, which together with the guide elements, in particular corrugated fins, form the heat exchanger block extend between two substantially identical or similar collection boxes.
  • pipes made of plastic with guide elements, in the heat exchanger block, in particular corrugated fins, combined of metal are easier and less expensive to produce compared to an aluminum heat exchanger.
  • the heat exchanger according to the invention requires about the same space and has similar air and coolant side pressure drops.
  • the guide elements, in particular corrugated fins, made of metal, in particular aluminum undesirably high performance losses compared to aluminum heat exchangers can be prevented.
  • a preferred embodiment of the cross-flow heat exchanger is characterized in that the pipes made of plastic are welded to the collecting box made of plastic.
  • the pipe ends are preferably welded to a bottom of the header tank.
  • the collecting box can be made in one piece and in several parts.
  • the individual parts of the collecting tank are preferably welded together and to the ground. As a result, a high density can be achieved.
  • a further preferred embodiment of the cross-flow heat exchanger is characterized in that the tubes and / or the collecting box are formed from at least one plastic of the following group: chlorinated polyethylene (PE), polypropylene (PP), polyvinylidene fluoride (PVDF), polyphenylene oxides (PPO ), Polyetherimides (PI), tetrafluoroethylene / hexafluoropropylene copolymer (FEP), polyphenylene sulfide (PPS), self-reinforcing polymer (SRF), polyaryletherketone (PEEK), polytetrafluoroethylene (PTFE), silane-modified and / or cross-linked polypropylene (PP) , Silane-modified and / or cross-linked high density polyethylene (PE-HD), perfluoroalkoxy copolymer (PFA), polyphthalamide (PPA), polyamide (PA XXX), polysulfun (PSF), polyimide (PI).
  • PE
  • the tubes and the collecting box are formed from the same material.
  • the production and / or welding of the individual parts are facilitated with each other.
  • the pipes and the collection box can also be formed of different materials. It is also possible to form individual tubes or tube groups from different materials when the individual tubes or tube groups come into contact with different materials or are exposed to different temperatures.
  • the tubes are formed from a plastic which is filled with heat-conducting fillers.
  • heat-conducting fillers for example, metal powders, graphite or ceramics have proven advantageous as fillers.
  • the thermal conductivity can be significantly increased.
  • a further preferred embodiment of the cross-flow heat exchanger is characterized in that the collecting box comprises a bottom with through-holes whose peripheral edge forms a stop for the tubes.
  • the bottom of the header represents the interface to the tubes.
  • the bottom may be integrally connected to the header.
  • the floor is designed as a separate part, which is materially connected to the collection box.
  • the through holes are preferably adapted to the shape of the pipe ends. That is, the through holes preferably have the same cross section as the pipe ends inside.
  • the peripheral edge forms a stop during assembly of the tubes.
  • Another preferred embodiment of the cross-flow heat exchanger is characterized in that the peripheral edge is bordered by a circumferential collar, in which the tubes are inserted with their ends.
  • the collar increases the contact area between the pipe ends and the floor.
  • Another preferred embodiment of the cross-flow heat exchanger is characterized in that the collars are welded to the pipe ends. As a result, a tight connection between the pipe ends and the bottom or the collecting box is produced in a simple manner.
  • the tubes are designed as flat tubes.
  • the flat tubes preferably have the shape of a slot in cross-section.
  • the tubes may also have a round or angled cross-section.
  • the tubes are extruded.
  • the tubes can be provided inside and / or outside with a cross-sectional profile.
  • the tubes each have at least one inner web.
  • the tubes are divided in cross section into several channels.
  • the webs serve to significantly increase the rigidity of the tubes.
  • Another preferred embodiment of the cross-flow heat exchanger is characterized in that the tubes are positively connected to the guide elements and / or partially surrounded by the plastic material of the tubes. This creates a stable connection between the vanes and the tubes. This connection is achieved, for example, by using the pipes, for example with the help of of heating plates and heating elements, are heated prior to assembly with the guide elements. After heating, the heat exchanger block is pressed together with the preheated tubes and vanes.
  • the guide elements are designed as corrugated ribs with bending or bending points.
  • the corrugated fins are preferably folded in a known manner substantially zigzag and formed of aluminum or an aluminum alloy.
  • cross-flow heat exchanger is characterized in that in the region of the bending or bending points in each case at least one tab is bent out of the corrugated rib, which, at least partially, is arranged in the associated pipe.
  • cross-flow heat exchanger is characterized in that in the region of the bending or bending points in each case at least one opening is provided, which is penetrated by the pipe material.
  • the opening can, at least partially, be enclosed by a ring.
  • the preferably heated plastic material presses through the opening during compression of the heat exchanger block, so that an undercut is created.
  • the heat exchanger 1 comprises two header tanks 2 and 3, which have an approximately semicircular cross-section, and are therefore also referred to as manifolds. These collecting tanks 2, 3 can also have a different shape and serve in a known manner to collect a medium to be cooled or to be heated. Therefore, the headers 2, 3 are also referred to as collectors.
  • the collecting box 2 For feeding and discharging the medium, the collecting box 2 has two connecting pieces 4, 5, which are preferably connected in one piece with the collecting box 2.
  • a heat exchanger block 8 with tubes 10, 11, 12, which are designed as flat tubes. Between two tubes in each case a guide element 13, 14 is arranged in the form of a corrugated fin in a known manner.
  • the heat exchanger 1 may in a known manner also have only one collection box into which the tubes open at one end when the tubes are provided at their other ends with a likewise known deflection.
  • arrows 15, 16, 17 are in FIG. 1 the expansion directions of the heat exchanger 1 in the depth 15, in the width 16 and the height 17 indicated.
  • the expansion the heat exchanger 1 in the width 16 corresponds to the longitudinal extent or longitudinal direction of the collecting tanks 2, 3rd
  • the in the Figures 1 and 2 shown heat exchanger 1 is also referred to as a heat exchanger and is designed as Kreuzströmer.
  • a coolant is collected and passed through the tubes 10 to 12.
  • the guide elements 13, 14 between the tubes 10 to 12 flows in cross-flow to the coolant, for example, air.
  • the air is either cooled or heated.
  • the heat exchanger 1 is preferably used as a coolant radiator, radiator, oil and ⁇ hlenk Anlagenkühler, evaporator or condenser in the automotive field.
  • the medium, such as refrigerant or coolant in the collecting box 2 can be deflected by a partition 20. The medium can be deflected into the collecting tanks 2, 3 both in the depth 15 and in the width 16 of the heat exchanger 1.
  • the tubes 10 to 12 and the collecting tanks 2, 3 are made of plastic.
  • the guide elements 13, 14 are not made of plastic but of metal, preferably of aluminum or of an aluminum alloy.
  • the plastic parts of the heat exchanger 1 are produced for example by injection molding or gas injection molding and / or extrusion.
  • the plastic parts are then joined by a suitable welding method in a simple manner cohesively or connected to each other.
  • Various measures are provided by the present invention as to how the metal baffles 13, 14 can be interconnected with the header boxes 2, 3 and the plastic pipes 10 through 12 in a suitable manner. These measures concern in particular the shape of the joining partners and a special joining method.
  • the collecting boxes 2, 3 and / or the tubes 10 to 12 are preferably formed from a plastic which is resistant to a water-glycol mixture.
  • the plastic used preferably has a very high aging, hydrolysis and permeation resistance in the coolant.
  • the plastic used can withstand pressures of up to 6 bar and temperatures of up to 135 degrees Celsius.
  • a thermoplastic is preferably used as the plastic.
  • the plastic used with heat-conducting fillers, such as metal powder, graphite or ceramic.
  • fillers with the abbreviations BN, SiC, Beo, AlN and Al-oxides are mentioned.
  • the thermal conductivity of about 0.25 watts / (meter Kelvin) can be increased to about 2 to 30 watts / (meters Kelvin).
  • the collection box 2 is shown in different views.
  • the collecting box 2 may be formed from two half shells, for example by injection molding or gas injection injection molding, in several parts, in particular in two parts. The two half-shells are then welded.
  • the interior of the collecting tank 2 is in FIG. 4 designated 22.
  • the collection box interior 22 is delimited by a first collection box wall 23 and a second collection box wall 24.
  • the two Sammelkastenwandungen 23, 24 may also be referred to as half shells.
  • the collection box wall 23 is integral with the Bottom of the header 2 connected.
  • the bottom of the header tank 2 has a plurality of parallel slots or through holes 25.
  • the through hole 25 is bounded by a peripheral edge 26 which forms a stop when inserting the tube 10.
  • the peripheral edge 26, which delimits the through hole 25, is in turn enclosed by a collar 28 which projects at right angles from the collecting box wall 23.
  • the tube 10 comprises a tube wall 31, which has the shape of a slot in cross-section and rests flush against the peripheral edge 26 of the through hole 25.
  • the thickness of the pipe wall 31 corresponds to the extent of the peripheral edge 26 of the collar 28 inwardly.
  • the tube height of the tube 10 is in FIG. 4 denoted by 34.
  • the through hole 25 has an elongated cross section which corresponds to the cross section of the pipe wall 31 inside. Therefore, the through hole 26 is also referred to as a slot. Through the through hole 26, a connection between the collection box interior 22 and the tube interior 32 is provided.
  • the longitudinal axis of the through holes or slots 25 corresponds to the depth direction 15 of the heat exchanger 1.
  • the collar 28 grips the tubes 10 at their ends after they have been inserted into the collar 28 at the stop peripheral edge 26.
  • the collar 28 is welded after insertion with the associated pipe end, for example by Schuformemia, laser welding or transmission laser welding or vibration welding.
  • the components to be welded are simultaneously pressed together or pinched.
  • the collar 28 may be provided with an insertion ramp for the tube ends to facilitate the insertion of the tubes.
  • a tube 40 is shown, which is designed as a flat tube with a tube wall 41, which has the shape of a slot in cross-section.
  • the pipe wall 41 has the shape of a rectangle in cross section, whose short sides are designed as semicircles.
  • the channel height is indicated in the tube 40.
  • three webs 43, 44, 45 extend perpendicular to the longitudinal sides of the flat tube and divide this into four channels 46, 47, 48, 49, which have approximately the same cross-section.
  • the tube 40 with the webs 43 to 45 is preferably produced by extrusion.
  • the webs 43 to 45 provide during assembly of the heat exchanger and during operation for a sufficient rigidity of the flat tube 40 and the heat exchanger block with such flat tubes.
  • the webs 43 to 45 prevent unwanted collapse of the tube 40 on the long sides of the rectangular cross-section.
  • the heat transfer on the inside of the tube 40 is improved by the webs 43 to 45 to a small extent.
  • round tubes instead of the flat tubes, 40 round tubes can be used which have a round or oval cross-section.
  • the round tubes can also be provided with webs. In the depth direction 15 of the heat exchanger 1 and a plurality of round tubes can be arranged.
  • a flat tube 50 is shown in perspective, the flat tube 40 from FIG. 5 similar.
  • the flat tube 50 laterally elevations 51, 52 or thickenings, which serve to fix guide elements in a heat exchanger block.
  • the flat tubes 40; 50 are also provided with a roughness or ribbing, which extends in the depth direction 15 of the heat exchanger 1. The roughness or ribbing in the depth direction is preferred by extrusion during manufacture of the flat tubes 40; 50 generated.
  • the guide elements 13, 14 serve to increase the heat transfer surface on the outside of the tubes 10 to 12, whereby the performance of the heat exchanger 1 can be significantly increased.
  • the guide elements 13, 14 can, like conventional corrugated fins, be rolled longitudinally with rolling rolls.
  • the corrugated ribs are preferably formed from a multi-folded or shirred thin sheet metal material.
  • FIG. 7 is a guide element in the form of a corrugated fin 55 shown in perspective.
  • the corrugated fin 55 is bent in a known manner from a band-like sheet material 56 in a zigzag shape. By a double arrow 57, a bending or bending point is indicated.
  • the corrugated fin 55 comprises at each kink or bending point an opening 58 which is penetrated during assembly of the corrugated fin of the abutting plastic material of the respective tube. For this purpose, the plastic material from which the tubes are formed is heated prior to or during assembly of the corrugated fins.
  • the opening 58 is formed at the bending or bending point of the corrugated fin 50 by two lugs or tabs 59, 60 are bent out of the sheet material 56 at the kink or bending point.
  • the tabs or tabs 59, 60 are preferably bent out towards the tube, so that they at least partially penetrate during assembly of the corrugated fin in the plastic material from which the tubes are formed.
  • FIG. 9 a corrugated fin 80 is shown, which is provided with an additional ribbing 81 to 83.
  • the additional ribs 81, 82, 83, which are bent out of the sheet metal material, are also referred to as gills.
  • FIG. 8 a section of a heat exchanger according to another embodiment with tubes 71, 72 and corrugated fins 74, 75 is shown.
  • the corrugated fins 74, 75 are modified such that portions or regions 77 of the corrugated fin 74 are bent upwards or downwards in the front and / or rear direction in the depth direction 15 of the heat exchanger at the bending or bending points, after the corrugated fins 74, 75 in FIG these areas were slotted.
  • this embodiment can be based on the pre FIG. 7 described tabs or tabs 59, 60 are omitted.
  • corrugated fin 100 is shown in various views.
  • the corrugated fin 100 comprises, viewed in cross-section, two long legs 101, 102, which are arranged at one end relatively close to each other. The two other ends are connected by a short leg 104.
  • the long leg 102 merges at its end remote from the short leg 104 into a further short leg 105.
  • a double arrow 108 the extension of the corrugated fin 100 in the depth direction 15 of the heat exchanger 1 is indicated.
  • the corrugated fin 100 includes in the region of the short legs 104, 105, a plurality of uniformly spaced openings 110 or through holes, which allow the passage of plastic material when the corrugated fin 100 is pressed during assembly against a preferably heated plastic tube.
  • the openings 100 are preferably bordered by a rim 112, which may be continuous.
  • the collar 112 is divided into a plurality of rim segments 114, 115.
  • the rings 112 preferably extend outwards, that is, toward the respective pipe.
  • the wreaths can also be directed inwards.
  • the rings 112 may advantageously be inclined to the corrugated fin 100 such that the collar 112 and the corrugated fin 100 are at an angle of about 45 degrees to 135 degrees to each other.
  • FIG. 12 a heat exchanger 121 is shown according to a further embodiment, which corresponds to the in FIG. 1 illustrated embodiment is similar. To designate the same parts, the same reference numerals are used. To avoid repetition, the preceding description of the FIG. 1 directed. In the following, the differences between the individual embodiments will be discussed.
  • the in FIG. 12 illustrated heat exchanger 121 includes a heat exchanger 128 with tubes 131, 132, which are designed as flat tubes. Between two of the tubes 131, 132, of which in FIG. 12 only two are provided with a reference numeral, a guide element 134, 135 is arranged in each case.
  • the guide element 135 is shown in different views.
  • the guide element 135 is designed as a sheet metal strip 140 with a plurality of slots 141, 142, 143. Through the slots 141 to 143, the guide member 135 is similar to a comb.
  • the slots 141 to 143 serve to receive one of the flat tubes 131, 132.
  • the border of the slots can be bent out to form indentations 145 which come to rest on the respective tubes.
  • insertion slopes 156 can be provided in the region of the slots, which facilitate the insertion of the tubes into the slots.
  • the shape of the slots 141 to 143 is preferably adapted to the shape of the tubes 131, 132.
  • the metal strips 140 are a total of about as wide and as deep as the heat exchanger. 1
  • FIG. 14 is indicated at points 151, 152, that the indentations 145 and insertion bevels 146 in an advantageous manner after joining with the tube can be folded so that a subsequent release of the metal strip 140 is prevented from the pipe.
  • the metal strips 140 may moreover have surface-enlarging and / or heat transfer-increasing profilings, such as knobs or ribs / gills, which can also serve as spacers of the metal strips 140 to each other.
  • the assembly of the heat exchanger 1; 121 is preferably carried out as follows: First, the tubes, in particular flat tubes, 10 to 12; 40; 50; 71, 72; 131, 132 cassetted. Subsequently, the headers 2, 3 are arranged in the immediate vicinity of the flat tubes in the correct position. Then the guide devices or guide elements 13, 14; 134, 135 introduced. If the guide elements as corrugated ribs 55; 74, 75; 80; 100 are executed, then these corrugated fins are placed between the tubes. Previously, the tubes can be heated by means of hot plates.
  • the heat exchanger block thus formed is compressed in the width direction 16.
  • the corrugated ribs are connected to the pipes.
  • the flaps 59, 60 or rings 112 formed on the corrugated ribs penetrate into the pipe wall, which, in addition to improving the fixation, also leads to an improvement in the thermal conductivity.
  • the through holes 110 in the corrugated fins 100 also provide the advantage that the heated plastic material penetrates the corrugated fin 100 and trailing behind. This allows a hooking or a positive connection between the corrugated fin 100 and the associated pipe.
  • the up / down bent portions or portions 77 provide the necessary support between corrugated fin 74, 75 and tube 71, 72. It is also possible, conventional Corrugated ribs to be used, which are glued to the plastic pipes and / or hot pressed in the width direction 16 of the heat exchanger.
  • connection between the plastic pipes 10 to 12; 40; 50; 71, 72; 131, 132 with the collecting boxes 2, 3 is preferably initiated by heating the partners to be joined.
  • the heating takes place for example via Schuformmaschine.
  • the joining partners can be crimped or crimped together at the joint in the warm state in the height and / or width and / or depth direction 17, 15, 16 of the heat exchanger. Welding of the joining partners, for example by means of transmission laser welding, or gluing is also possible.
  • Plastics and processes for the production of, in particular, cross-flow heat exchangers are advantageous, for example silane-modified and crosslinked high-density polyethylene (HDPE) or polypropylene (PP) being advantageous.
  • low viscose matrix polymers are advantageous, such as liquid crystalline polymers (LCP), ETPE, HDPE / GF compound, PP / GF coumpound.
  • LCP liquid crystalline polymers
  • ETPE liquid crystalline polymers
  • HDPE / GF compound PP / GF coumpound
  • the HDPE or PP can be crosslinked by silane crosslinking technology. This allows the Continuous use temperature of the crosslinked polymer matrix can be increased to about 160 ° C.
  • the crosslinking of HDPE or PP leads to a significant improvement of the material properties and in particular of the mechanical properties, which significantly expands the application possibilities of these cost-effective polyolefin materials.
  • the cross-linked materials are characterized by an increased impact strength, improved heat distortion resistance, increased chemical resistance and high fillability.
  • HDPE and PP generation are practiced in a two-stage process.
  • Suitable fillers are inorganic fillers, such as. SiC: BeO; BN; Al 2 O 3 , ZnO; B 4 O 3 ; Glass; SiO 2 , BP, MgO, AlN, carbon black, etc.
  • Surface treatment of the inorganic filler particle and the glass fiber is carried out by means of the coupling reagents, e.g. For example, titanic acid or alkyl silane.
  • silane-crosslinked thermoplastics takes place in the development phase in the form of a two-stage process.
  • the grafting of the organosilane is carried out on the polymer, in the second step then the dynamic compounding of the thermoplastics and Grestoffipappel.
  • VTMOS condensable vinyltrimethoxysilane
  • VTEOS vinyltriethoxysilane
  • HDPE / PP 100phr Silane VTMOS or VTEOS: 0.5 ⁇ 6 phr; preferably 2.3- 3.0 phr DCUP * (DHBP **): 0.05 -0.5 phr; preferably 0.1-0.2 phr Master Bach: Thermostabilizer (Iganox 1010) 0.1 phr + DBTL (dibutyltin dilaurate (0.1-5 phr, preferably 0.2-0.3 phr) *: Dicumyl peroxide **: 2, 5-Dmethyl-2,5-di (tert-butylperoxy) hexane
  • the gel content of the silane-crosslinked polymer is between 60-85%, for higher operating conditions between 85-98%.

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  • 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)
EP09176897.8A 2008-12-01 2009-11-24 Echangeur thermique à courants croisés Not-in-force EP2192372B1 (fr)

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US20120312029A1 (en) * 2009-12-16 2012-12-13 Brehm Holger Thermoelectric heat exchanger
DE202012003241U1 (de) * 2012-03-30 2013-07-01 EWKtec GmbH Sammelrohr und Sammelrohrsystem eines Flächenheizsystems und Flächenheizsystem
CN112682500A (zh) * 2020-12-31 2021-04-20 南宁市安和机械设备有限公司 一种采用错位打点油冷器管制成的油冷器
US20220042749A1 (en) * 2020-08-04 2022-02-10 Evapco, Inc. Polymer tube dry cooling tower

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DE102010049637A1 (de) * 2010-10-28 2012-05-03 Benteler Automobiltechnik Gmbh Wärmetauscher mit Wärmetauscherrohr
DE102013215358A1 (de) * 2013-08-05 2015-02-19 Behr Gmbh & Co. Kg Wärmetauscher für eine Kühlung einer Fahrzeugbatterie, insbesondere für Hybrid- oder Elektrofahrzeuge
DE102016205044A1 (de) * 2016-03-24 2017-09-28 Mahle International Gmbh Kühleinrichtung, insbesondere für eine Brennkraftmaschine
DE102017216519A1 (de) * 2017-09-19 2019-03-21 Thyssenkrupp Ag Wärmeübertragungselement, Temperiervorrichtung und Batteriegehäuse mit mindestens einem Wärmeübertragungselement
DE102019102850A1 (de) * 2019-02-05 2020-08-06 Zehnder Group International Ag Kühlrohrregister und Luftentfeuchter
DE102019212361A1 (de) * 2019-08-19 2021-02-25 Hanon Systems Kühler aus Kunststoff sowie Batterie mit einem derartigen Kühler
DE102020211603A1 (de) * 2020-09-16 2022-03-17 Fränkische Industrial Pipes GmbH & Co. KG Vorrichtung zum temperieren eines bauteils und herstellungsverfahren der vorrichtung

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DE4229393A1 (de) 1992-09-03 1994-03-10 Rudolf Goerlich Wärmetauscher mit einer Steckverbindung
DE4238742A1 (de) 1992-11-17 1994-05-19 Rudolf Goerlich Rohrverbindung an Wärmetauschern
DE4244017A1 (de) 1992-12-24 1994-06-30 Behr Gmbh & Co Wärmetauscher, insbesondere für Kraftfahrzeuge
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US20120312029A1 (en) * 2009-12-16 2012-12-13 Brehm Holger Thermoelectric heat exchanger
US9291375B2 (en) * 2009-12-16 2016-03-22 Mahle International Gmbh Thermoelectric heat exchanger
DE202012003241U1 (de) * 2012-03-30 2013-07-01 EWKtec GmbH Sammelrohr und Sammelrohrsystem eines Flächenheizsystems und Flächenheizsystem
US20220042749A1 (en) * 2020-08-04 2022-02-10 Evapco, Inc. Polymer tube dry cooling tower
CN112682500A (zh) * 2020-12-31 2021-04-20 南宁市安和机械设备有限公司 一种采用错位打点油冷器管制成的油冷器
CN112682500B (zh) * 2020-12-31 2023-05-26 南宁市安和机械设备有限公司 一种采用错位打点油冷器管制成的油冷器

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EP2192372B1 (fr) 2019-07-31
DE102008059737A1 (de) 2010-06-02

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