EP3394544B1 - Wärmeaustauscher, insbesondere für ein kraftfahrzeug - Google Patents

Wärmeaustauscher, insbesondere für ein kraftfahrzeug Download PDF

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Publication number
EP3394544B1
EP3394544B1 EP16826391.1A EP16826391A EP3394544B1 EP 3394544 B1 EP3394544 B1 EP 3394544B1 EP 16826391 A EP16826391 A EP 16826391A EP 3394544 B1 EP3394544 B1 EP 3394544B1
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EP
European Patent Office
Prior art keywords
heat exchange
frames
fluid
heat exchanger
frame
Prior art date
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Application number
EP16826391.1A
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English (en)
French (fr)
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EP3394544A1 (de
Inventor
Carlos Martins
Anne-Sylvie Magnier-Cathenod
Jérôme MOUGNIER
Sébastien JACOPE
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Valeo Systemes Thermiques SAS
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Valeo Systemes Thermiques SAS
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Publication of EP3394544A1 publication Critical patent/EP3394544A1/de
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Classifications

    • 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
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/16Heat-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 being arranged in parallel spaced relation
    • F28D7/1684Heat-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 being arranged in parallel spaced relation the conduits having a non-circular cross-section
    • F28D7/1692Heat-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 being arranged in parallel spaced relation the conduits having a non-circular cross-section with particular pattern of flow of the heat exchange media, e.g. change of flow direction
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2275/00Fastening; Joining
    • F28F2275/04Fastening; Joining by brazing
    • F28F2275/045Fastening; Joining by brazing with particular processing steps, e.g. by allowing displacement of parts during brazing or by using a reservoir for storing brazing material
    • 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
    • F28F9/06Arrangements for sealing elements into header boxes or end plates by dismountable joints

Definitions

  • the invention relates to the field of heat exchangers according to the preamble of claim 1.
  • EP 1,870,658 discloses such an exchanger.
  • the invention relates more particularly to heat exchangers capable of being traversed by a refrigerant fluid having a relatively high operating pressure, as is the case of natural gases such as carbon dioxide designated by CO 2 , having a pressure of superior operation to the refrigerant gases used in state-of-the-art solutions.
  • Such heat exchangers find particular application in motor vehicles. They can in particular constitute a gas cooler in which the refrigerant fluid such as CO 2 is cooled by a second fluid, such as liquid. Conversely, the second fluid can be cooled by the first fluid, for example in gaseous form, the heat exchanger is then commonly designated by “Water chiller” in English.
  • Such heat exchangers can in particular be used in the thermal regulation of one or more batteries of an electric or hybrid vehicle.
  • the thermal regulation of the batteries is an important point because if the batteries are subjected to too cold temperatures, their autonomy can decrease strongly and if they are subjected to too high temperatures, there is a risk of thermal runaway which can go up to destruction of the battery, or even of the motor vehicle.
  • a heat transfer fluid in general cooling liquid comprising a mixture of glycol water, which circulates within a heat exchanger in contact with the battery or batteries.
  • the coolant can thus bring heat to the battery or batteries to heat them, this heat having been absorbed by the coolant for example during the heat exchange with the CO 2 circulating in the gas cooler.
  • the coolant can also, if necessary, absorb heat emitted by the battery or batteries in order to cool them and evacuate this heat at the level of one or more other heat exchangers.
  • Such heat exchangers can also be used like any other gas cooler in an air conditioning system.
  • Heat exchangers are known, for example, comprising a stack of plates allowing the circulation of the first fluid, such as the refrigerant or refrigerant gas, and of the second fluid such as the coolant.
  • the plate heat exchangers known from the prior art do not make it possible to withstand such high pressures.
  • heat exchangers are also known from the prior art comprising a stack of tubes connected together by at least one collector of the first fluid, in particular the coolant on each side of the tubes, and the second fluid, for example in liquid form, can circulate around the tubes in an envelope connected to a water box.
  • the heat exchangers can in particular be assembled by brazing.
  • a brazing material is generally provided on different elements of the heat exchanger.
  • the brazing material which melts can block the channels in which at least one fluid is intended to circulate, in particular the refrigerant.
  • the present invention aims to improve the solutions of the state of the art and to at least partially resolve the drawbacks exposed above by proposing a heat exchanger whose assembly by brazing is improved.
  • the spacers respectively have at least one tank capable of collecting the coating during the brazing of the heat exchanger, each tank being arranged on one end of a spacer and facing one end of a tube d heat exchange, so as to prevent the coating from clogging said at least one circulation channel of the heat exchange tube during brazing of the heat exchanger.
  • the coating present to ensure the junction between the elements of the heat exchanger during assembly does not run the risk of blocking, when it melts, the circulation channels of the first fluid.
  • the coating which migrates during brazing flows into the reservoirs opposite the ends of the heat exchange tubes instead of risking entering the circulation channels of the first fluid accessible at the ends of the heat exchange tubes.
  • the heat exchanger may further comprise one or more of the following characteristics taken alone or in combination.
  • the spacers respectively have at least one reservoir on each face opposite a heat exchange tube.
  • the heat exchanger thus comprises a stack of simple elements, namely frames and heat exchange tubes in which the first fluid circulates, such as the coolant, inserted in the first frames and between which the second fluid circulates. only coolant.
  • the superimposed frames allow the flow path of the first refrigerant to be created, when the frames are brazed together, and likewise, the superimposed frames create the coolant flow path, in particular on two opposite sides of the bundle d 'heat exchange.
  • the frames designate a part, or an assembly of parts, which can be rigid, delimiting a closed or not space. In this space can be positioned, in our example, heat exchange tubes.
  • the heat exchange bundle which comprises a plurality of heat exchange tubes, is distinct from the frames.
  • Such a heat exchanger has better mechanical strength compared to the solutions of the prior art and very good resistance to high pressures, in particular due to the circulation of CO 2 as refrigerant.
  • the reservoir is produced by reducing the material of an interlayer, or intermediate frame.
  • the reservoir is produced in the form of a groove extending substantially perpendicular to the direction of flow of the first fluid in the heat exchange tubes.
  • the reservoir extends opposite the entire end of a heat exchange tube, for example over the entire width of a heat exchange tube produced in the form of a flat tube.
  • the first receiving frames respectively have at least one recess at an interior corner receiving a corner of a heat exchange tube, for the flow of the coating during brazing of the heat exchanger, so as to prevent the coating from clogging the channels of the heat exchange tubes.
  • the width of the step is substantially equal to the width of the groove.
  • This arrangement corresponds to the arrangement of the elements in the mounted state in a motor vehicle in particular.
  • the invention relates to a heat exchanger 1 in particular for a motor vehicle, for a heat exchange between at least a first fluid and a second fluid.
  • the first fluid can enter the heat exchanger 1 in gaseous form and the second fluid in liquid form.
  • the heat exchanger 1 has at least partially, that is to say on at least certain elements or certain parts, a coating intended to melt to ensure the joining of elements of the heat exchanger during the 'assembly by brazing, as will be detailed later.
  • the heat exchanger 1 according to the invention is in particular suitable for the circulation of at least one fluid having a high operating pressure, in particular greater than 100 bars.
  • the first fluid is a refrigerant intended to circulate at high pressure such as CO 2 , also designated by R744 according to the industrial nomenclature.
  • the heat exchanger 1 can in particular be a gas cooler in which the refrigerant fluid such as CO 2 is cooled by a second fluid, for example in liquid form, such as coolant comprising a mixture of glycol water.
  • the second fluid such as the coolant can also be cooled by the first fluid such as CO 2 , such a heat exchanger is then commonly designated by "Water chiller" in English.
  • the heat exchanger 1 comprises a heat exchange bundle 3 allowing the heat exchange between the first fluid and the second fluid.
  • the heat exchange bundle 3 has a generally substantially parallelepiped shape.
  • the circulation of the first and second fluids is advantageously done against the current in the heat exchange bundle 3.
  • the introduction and evacuation of the first fluid in the heat exchange bundle 3 or out of the heat exchange bundle 3 is shown schematically by way of example by the arrows F1 I for the introduction and F1 O for the evacuation .
  • the heat exchanger 1, and more precisely the heat exchange bundle 3 can be configured for circulation in at least two passes of one of the two fluids, or even of the two fluids, as will be described in more detail below. detail later.
  • the heat exchange bundle 3 comprises a plurality of heat exchange tubes 5 (see figure 2 ) stacked so as to alternately define first circulation channels 7 for the first fluid in the heat exchange tubes 5 and second circulation channels 9 for the second fluid between the heat exchange tubes 5.
  • the heat exchange tubes 5 can be produced in the form of flat tubes, advantageous in terms of space.
  • the flat tubes 5 have a generally substantially rectangular shape, with a length for example of the order of 32mm and a thickness of the order of a millimeter.
  • the thickness, or no tube, is here considered in the direction of the height of the heat exchange bundle 3, we can also speak of the height of the heat exchange tubes 5.
  • Each heat exchange tube 5 defines a predetermined number of first circulation channels 7 for the first fluid, in particular micro-circulation channels 7 for the first fluid.
  • the first channels or micro-channels 7 here extend substantially longitudinally, in a substantially "I” or rectilinear shape.
  • the first circulation channels or micro-channels 7 for the first fluid allow the flow of the first fluid extend respectively in a direction parallel to the longitudinal direction of the heat exchange tubes 5.
  • the first fluid can follow a circulation in a pass called “I” circulation but also a circulation in two passes called “U” circulation as will be described later.
  • the second circulation channels 9 for the second fluid can be shaped to allow circulation in a so-called “I” circulation pass but also a circulation in two passes called “U” circulation as will be described later.
  • Turbulators 11 for the flow of the second fluid are advantageously arranged in the second circulation channels 9, thus improving the heat exchange between the two fluids.
  • the turbulators 11 can be carried by a separate element from the heat exchange tubes 5.
  • turbulators 11 can be formed on the heat exchange tubes 5, for example by deformations such as corrugations of the heat exchange tubes 5 which project into the second circulation channels 9 for the second fluid.
  • Interleaves are advantageously arranged between the heat exchange tubes 5, and define the pitch between the heat exchange tubes 5.
  • the heat exchange bundle 3 comprises an alternating stack of first frames 13 and second frames 15.
  • At least some second frames 15 form the spacers.
  • the stacking takes place here substantially vertically.
  • Each first frame 13 is capable of receiving at least one heat exchange tube 5 and this assembly forms a stage of the heat exchange bundle 3.
  • the first frames 13 can be designated by tube frames.
  • Each second frame 15 can receive turbulators 11 and this assembly forms another stage of the heat exchange bundle 3.
  • the first frames 13 and the second frames 15 are described in more detail below.
  • closure plates 17, 18 in particular at least one lower closing plate 17 and at least one upper closing plate 17, 18 can be arranged on either side of the stack of first frames 13 and second frames 15, so as to close the beam d heat exchange 3.
  • the heat exchanger 1 further comprises at least one manifold 19 of the first fluid arranged in fluid communication with the first circulation channels 7.
  • the manifold 19 is, according to the illustrated example, arranged on an upper closure plate 18 disposed at the top of the heat exchange bundle 3.
  • the heat exchanger 1 further comprises at least two fluid inlet and outlet pipes 21 allowing the introduction and the evacuation of the second fluid.
  • the two pipes 21 are arranged on the same upper closure plate 18 as the manifold 19 for the first fluid.
  • the manifold 19 can be arranged on one side of the heat exchange bundle 3 and the pipes 21 can be arranged on the other side of the heat exchange bundle 3, thus allowing counter-current circulation of the two fluids.
  • the manifold 19 is arranged on the left while the pipes 21 are arranged on the right.
  • First frames called tube frames
  • the first frames 13 can be at least partially made in aluminum.
  • the general direction of flow of the first fluid is understood to be the direction of circulation in “I” in the case of a one-pass circulation of the first fluid, or the direction of the branches of the “U” in the case of 'a circulation in two passes of the first fluid.
  • the first frames 13 are of generally substantially rectangular shape and have two longitudinal edges 13C, 13D, forming long sides, extending substantially parallel to the general direction of flow of the first fluid and two lateral edges. 13A, 13B, forming short sides, extending in the width direction, substantially perpendicular to the direction of flow of the first fluid.
  • the longitudinal axis of the first frames 13 and the heat exchange tubes 5 is here combined.
  • These first frames 13 have the same thickness as the heat exchange tubes 5 which they receive, in particular of the order of a few millimeters, for example of the order of 1mm.
  • the thickness is considered in the direction of the height of the heat exchange bundle 3, we can also speak of the height of the first frames 13.
  • the heat exchange tubes 5 can be held in the respective first frames 13 before the different frames 13, 15 are superposed.
  • each first frame 13 may be able to receive a single heat exchange tube 5 allowing circulation in one pass of the first fluid.
  • each first frame 13 has a housing 130 for receiving an associated heat exchange tube 5.
  • each first receiving frame 13 is able to receive two heat exchange tubes 5.
  • the heat exchange bundle 3 then has two rows of heat exchange tubes 5: first heat exchange tubes and second heat exchange tubes.
  • two adjacent tubes in a first frame 13 communicate with each other at one end so as to allow circulation in two passes of the first fluid.
  • the heat exchange bundle 3 therefore has at least one area for reversing the first fluid, that is to say allowing the first fluid having circulated in a heat exchange tube 5 to flow to another heat exchange tube 5, namely the adjacent heat exchange tube 5 received in the same first frame 13.
  • the first fluid having circulated in a heat exchange tube 5 to flow to another heat exchange tube 5, namely the adjacent heat exchange tube 5 received in the same first frame 13.
  • the placing in fluid communication at one end of two adjacent heat exchange tubes 5 received in a first frame 13 is advantageously ensured by a second frame 15 as will be described in more detail below.
  • the first frames 13 comprise means for placing in fluid communication 131 the first circulation channels 7 of the heat exchange tubes 5 with the manifold 19.
  • each first frame 13 are therefore arranged in fluid communication with the fluid communication means 131 of the other first frames 13 of the heat exchange bundle 3 and with the manifold 19.
  • the fluid communication means 131 define two rows respectively associated with a row of heat exchange tubes 5.
  • first communication means 131 ensure the fluid communication of the first heat exchange tubes 5 or in other words of a first row of first heat exchange tubes 5 with the manifold 19.
  • second communication means 131 ensure the fluid communication of the second heat exchange tubes 5 or in other words of the second row of second heat exchange tubes 5 with the manifold 19.
  • the first frames 13 respectively have a predefined number of recesses 131 forming the means of fluid communication, in which the ends, in particular the longitudinal ends, of the heat exchange tubes 5 open.
  • the number of recesses 131 is adapted as a function of the number of first circulation channels 7 of the heat exchange tubes 5.
  • These recesses 131 are here provided on two opposite edges 13A, 13B of the first frames 13 which are opposite the ends of the heat exchange tubes 5. These are the lateral edges of the first frames 13.
  • the first frames 13 are arranged so that their recesses 131 are in fluid communication with the recesses 131 of the other first frames 13.
  • the recesses 131 of the first frames 13 are aligned in the direction of the height of the heat exchange bundle 3. In addition, on one side of the first frames 13, the recesses 131 are aligned with the manifold 19.
  • At least one lateral edge 13A, 13B of a first receiving frame 13, arranged opposite one end of a heat exchange tube 5, is shaped according to a pattern defining a succession of arches.
  • the arches are advantageously arranged over the entire width of the lateral edge 13A, 13B which is opposite the ends of the heat exchange tubes 5 received in the same first frame 13.
  • the arches are provided over the entire width of the set of heat exchange tubes 5 that the first frame 13 can receive, here two heat exchange tubes 5.
  • arch means the assembly formed by an arch vault 132 connecting two arch feet 133.
  • two adjacent arch vaults 132 are connected by a common arch base 133.
  • a recess 131 is delimited by an arch, in other words each recess 131 is formed between two adjacent arch legs 133 and is delimited by these two arch legs 133 and the arch vault 132 connecting them .
  • the diameter of a through opening is of the order of 0.5 mm.
  • each first frame 13 advantageously comprises at least one stress absorption zone on at least one lateral edge 13A, 13B facing one end of a heat exchange tube 5.
  • Such a stress absorption zone is able to withstand mechanical stresses, in particular due to pressure.
  • the stress absorption zones can be produced by a predetermined number of stress absorption legs formed on at least one lateral edge 13A, 13B of a first frame 13 opposite one end of a heat exchange tube 5.
  • the arch feet 133 perform this function of stress absorption legs.
  • the arches are therefore dimensioned taking into account the mechanical strength of the first frame 13 and the flow of the first fluid through the recesses 131 defined by the arches.
  • the arch legs 133 also make it possible to define brazing zones with the second frames 15 as will be described below.
  • the first frames 13 also have guides 134 for the passage of the second fluid.
  • the first frames 13 are respectively shaped with at least one handle 134 which when a heat exchange tube 5 is arranged in the first frame 13 makes it possible to define a through passage opening allowing the flow of the second fluid.
  • the figures show various embodiments of the handles 134, in particular the figure 1 , illustrates a first embodiment of the handles 134 of substantially rounded shape, while the figures 2, 3 and 5 illustrate a second embodiment of the handles 134, the outline of which is more straight.
  • any other form of the handles 134 can be envisaged.
  • the handles 134 make it possible to define the guides for the passage of the second fluid.
  • this through opening has a diameter of around 2mm.
  • the ratio between the diameter of a passage opening for the second fluid and the diameter of a through opening 131 for placing in fluid communication allowing the flow of the first fluid is in this example of the order of 4.
  • each first frame 13 is arranged in alignment with the handles 134 of the other first frames 13 of the heat exchange bundle 3 so as to allow the second fluid to flow through the heat exchange bundle 3.
  • each first receiving frame 13 has, according to the embodiment illustrated in the figures 2 and 3 , at least one partition 135 which compartments the first receiving frame 13.
  • This partition 135 is here arranged in the extension of an arch foot 133.
  • each first receiving frame 13 has a partition 135, for example substantially central, which compartments the first receiving frame 13 into two housings 130 to each receive a heat exchange tube 5.
  • the partition 135 therefore finds itself arranged between two heat exchange tubes 5 when they are placed in the first frame 13.
  • the partition 135 in this example extends over the entire length of the heat exchange tubes 5 received in the first frame 13.
  • the partition 135 of a first frame 13 can be made in one piece with this first frame 13.
  • Such a first frame 13 can be produced by stamping cutting in a simple manner.
  • FIG. 4 An enlarged portion of a first frame 13 is illustrated on the figure 4 .
  • the heat exchanger 1 is in particular assembled by brazing.
  • the coating is commonly designated by "clad” in the field of brazing of metal parts, in particular aluminum.
  • the coating is added to the core of the parts, such as the first frames 13 and second frames 15, during manufacture, for example by cold rolling.
  • the percentage of the coating is for example of the order of 5% to 10% of the material of a frame 13, 15 for example.
  • the percentage of the coating is chosen small enough not to weaken the elements of the heat exchange bundle 3, in particular the first frames 13 and the second 15, after brazing.
  • the first frames 13 respectively have at least one step 139 at an inner corner receiving a corner of a heat exchange tube 5, that is to say on a corner of the inner edge of a first frame 13, which faces a heat exchange tube 5 when the latter is arranged in the first receiving frame 13.
  • Such a step 139 is provided to allow the coating to flow during the brazing of the heat exchanger 1, thus preventing the coating from clogging the first circulation channels or micro-channels 7 of the heat exchange tubes 5.
  • this detachment 139 takes account of a compromise so as not to weaken the first frame 13 while being able to collect a sufficient quantity of the coating which has migrated during brazing.
  • this recess 139 is substantially equal to the width of a groove 154 provided for a similar purpose on a second frame 15 as described below.
  • the first frames 13 respectively have four recesses 139 respectively arranged at each of the four interior corners of a first frame 13.
  • the recess (s) 139 are arranged near the fluid communication means 131.
  • At least one edge of a first frame 13 is shaped with a succession of arches
  • at least one step 139 is produced in the extension of an extreme arch, that is to say of the first or last arch of the succession of arches.
  • the second frames 15 can be at least partially made of aluminum.
  • the second frames 15 When the second frames 15 receive turbulators 11, the second frames 15 are called turbulator frames or turbulator-carrying frames.
  • the general direction of flow of the second fluid is understood to be the direction of circulation in “I” in the case of a one-pass circulation of the second fluid, or the direction of the branches of the “U” in the case of 'a circulation in two passes of the second fluid.
  • the second frames 15 are of general shape similar to the first frames 13, here substantially rectangular.
  • the second frames 15 have two longitudinal edges, forming long sides, extending substantially parallel to the longitudinal edges of the first frames 13 and to the general direction of flow of the second fluid, and two lateral edges, forming short sides, extending in the width direction, substantially perpendicular to the direction of flow of the second fluid parallel to the lateral edges of the first frames 13.
  • the second frames 15 extend over the same length and the same width as the first frames 13.
  • the outer contours of the first frames 13 and second frames 15 are practically identical so that the alternating stacking of the first frames 13 and second frames 15 forms a block.
  • each second frame 15 defines an internal width and an internal length.
  • internal width means the width defined between the internal walls of the opposite longitudinal edges.
  • internal length means the length defined between the inner walls of opposite side edges.
  • the side edges of the second frames 15 may be slightly larger than the side edges of the first frames 13, so that the ends of the heat exchange tubes 5 received in the first frames 13 stacked with the second frames 15, rest on the peripheral edge of the lateral edges of the second frames 15.
  • the second frames 15 therefore define an internal length L less than the internal length defined by the interior space of the first frames 13.
  • the second frames 15 have a thickness which is of the order of a few millimeters, for example of the order of 0.5mm to 4mm, preferably of the order of 2mm.
  • the thickness is here considered in the direction of the height of the heat exchange bundle 3, we can also speak of the height of the second frames 15. In other words, it is the thickness in the stacking direction of the frames 13, 15.
  • the second frames 15 can be produced by stamping cutting.
  • a plurality of second frames 15, called intermediate frames, are arranged between two first frames 13 for receiving the heat exchange tubes 5, thus defining the pitch between two stages of heat exchange tubes 5.
  • the heat exchange bundle 3 may further comprise a second end frame (not illustrated) optionally arranged between a first frame 13 and a closure plate 17, in particular the closure plate lower 17.
  • Such a second end frame can be put in place for reasons of mechanical strength.
  • Each second frame 15 can be shaped for one-pass circulation of the second fluid.
  • each second frame 15 defines a second circulation channel 9 for the second fluid.
  • the second circulation channel 9 here extends in a substantially "I" shape.
  • the second frames 15 allow a circulation in two passes of the second fluid.
  • the second frames 15 each comprise a bar 150 arranged inside the respective second frame 15 so as to separate two circulation passes for the second fluid.
  • the bar 150 makes it possible to conform the second circulation channel 9 substantially in a "U" shape.
  • the bar 150 extends longitudinally inside a second frame 15.
  • the bar 150 therefore extends in this example substantially parallel to the longitudinal edges of the second frame 15.
  • the bar 150 does not extend over the entire internal length of the second frame 15. In other words, the bar 150 extends from a lateral edge of a second frame 15 towards the opposite lateral edge but without reaching this opposite side edge.
  • the bar 150 is therefore secured to a lateral edge of a second frame 15 and projects with its free end towards the internal space of the second frame 15 in the direction of the opposite lateral edge, leaving a space.
  • the internal bar 150 therefore extends longitudinally from a lateral edge of a second frame 15 over a length l less than the internal length L of the second frame 15.
  • the internal bar 150 does not extend over the entire internal width of the second frame 15 either.
  • the internal bar 150 has a smaller width than the internal width of the second frame 15.
  • the bar 150 can also be described as a tongue.
  • the bar 150 is substantially the same thickness as the second frame 15.
  • the bar 150 is for example arranged substantially centrally. More specifically, the bar 150 is arranged substantially in the center of a second frame 15 in the width direction of the second frame 15.
  • the bar 150 divides the second frame 15 into two parts of the same size.
  • the internal bar 150 extends over a length l at least equal to half the internal length L of a second frame 15.
  • each second frame 15 may have an internal length L comprised in a range of the order of 30mm to 500mm.
  • the heat exchange tubes 5 or mono-tubes received in the first frames 13 can rest on the bars 150 of the second frames 15 facing each other.
  • the internal bars 150 of the second frames 15 are located opposite the partitions 135 of the first frames 13 produced according to the embodiment illustrated in the figures 2 and 3 .
  • the second frames 15, in particular the second intermediate frames 15, have guides 151 for the passage of the first fluid allowing its flow in the stack of the first receiving frames 13 and the second frames 15, in particular inserts.
  • the guides 151 are here produced in the form of through-passage orifices 151 arranged in alignment with the recesses 131 for placing the first receiving frames 13 in fluid communication, delimited here by the succession of arches.
  • the through passage orifices 151 are therefore arranged on at least one lateral edge of a second frame 15, here of a second intermediate frame 15.
  • the number of through passage openings 151 is adapted as a function of the number of recesses 131 and therefore of the number of first channels of circulation 7 of the heat exchange tubes 5.
  • the second end frame when present, is produced in a similar manner to a second intermediate frame, except that the second end frame does not have through passage openings 151 for the passage of the first fluid.
  • the second frames 15 respectively present means for placing in fluid communication 152 the second circulation channels 9 between them on the one hand and with the pipes 21 for the second fluid on the other hand.
  • the second frames 15 respectively have a predefined number of through openings 152 for fluid communication.
  • These through openings 152 are here arranged on the longitudinal edges of the second frames 15 and are aligned with each other in the height direction of the heat exchange bundle 3.
  • the through openings 152 lead respectively to the interior of a second frame 15.
  • the through openings 152 are arranged on the same side of a second frame 15 in the longitudinal direction, that is to say here on the right or on the left, in a complementary manner to the arrangement of the pipes 21 on the same side of the heat exchange bundle 3, here on the right with reference to the arrangement shown on the figure 1 .
  • the through openings 152 make it possible to define a fluid inlet 152 towards the interior space of the second frame 15 on a longitudinal edge, and a fluid outlet 152 out of the second frame 15 on the opposite longitudinal edge.
  • the second frames 15 have handles 153 which make it possible to delimit the through openings 152.
  • the handles 153 of the second frames 15 are produced in a similar manner to the handles 134 of the first frames 13 and are aligned with these handles 134 which allow the passage of the second fluid through the heat exchange bundle 3.
  • the figures show different embodiments of the handles 153, in particular the figure 1 , illustrates a first example of realization of handles 153 of substantially rounded shape, while the figure 5 , illustrates a second embodiment of the handles 153, the outline of which is more straight.
  • the handles 134 of the first frames 13 are produced according to the first embodiment
  • the handles 153 of the second frames 15 are produced in a similar manner according to the first embodiment.
  • the handles 134 of the first frames 13 are produced according to the second embodiment, the handles 153 of the second frames 15 are produced in a similar manner according to the second embodiment example.
  • any other form of the handles 153 can be envisaged.
  • the opening delimited by a first handle is arranged in fluid communication with a first tube 21 and the opening delimited by a second handle is arranged in fluid communication with a second tube 21.
  • the heat exchanger 1 is preferably assembled by brazing.
  • the second frames 15 are intended to be assembled by brazing to the first frames 13.
  • the longitudinal edges of the second frames 15 are intended to be assembled by brazing to the longitudinal edges of the first frames 13 and the lateral edges of the second frames 15 are intended to be assembled by brazing with the arch legs 133 provided on the edges side of the first frames 13.
  • the second frames 15 respectively have at least one reservoir 154, better visible on the figure 6 , suitable for collecting the coating or "clad" during brazing of the heat exchanger 1.
  • Each reservoir 154 is here arranged on a lateral edge of a second frame 15.
  • a reservoir 154 is advantageously provided on each lateral edge of a second frame 15.
  • Each reservoir 154 is then located opposite a lateral edge 13A, 13B of a first receiving frame 13 onto which opens one end 50, 52 of a heat exchange tube 5.
  • the coating disposed on the first frames 13 and the second frames 15 facing each other melts and migrates so as to block the clearances between the parts of the heat exchanger 1 and flows into the reservoirs 154, thus preventing the coating having melted and migrated from clogging the first circulation channels or micro-channels 7 of the heat exchange tubes 5.
  • the reservoir or reservoirs 154 are provided on each face of a second intermediate frame 15 arranged between two first frames 13.
  • the reservoir or reservoirs 154 may be arranged on one face of this second end frame, namely on the face opposite a heat exchange tube 5, and not on the opposite face of the second end frame, facing a closure plate 17.
  • Each reservoir 154 can be produced by local reduction of material from a second frame 15.
  • the depth p of a reservoir 154 must be chosen to be large enough to collect the coating, which is for example of the order of 5% to 10% of the material of the second frame 15, and small enough not to weaken the mechanical strength. second frame 15.
  • the reservoir 154 may have a depth p of the order of 0.5mm.
  • the reservoir 154 is produced in the form of a groove 154 extending substantially perpendicular to the direction of flow of the first fluid in the heat exchange tubes 5, here in the direction of the width of a second frame 15.
  • the reservoir 154 extends opposite the entire end of a heat exchange tube 5, in other words over the entire width of a tube or of each heat exchange tube 5.
  • the width of the groove 154 on a second frame 15 is substantially equal to the width of the recess 139 on a first frame 13.
  • the second frames 15, in particular the second intermediate frames 15, can also be shaped to put in fluid communication two heat exchange tubes 5 received in the same first frame 13 according to the embodiment of the first frames 13 illustrated in figures 2 and 3 .
  • each second frame 15, in particular an intermediate frame advantageously has at least one turning orifice 155 (see figure 5 ) which is in fluid communication with both a first and a second fluid communication means 131, here a first and a second recess 131, of the first frames 13 on either side of the second intermediate frame 15.
  • each reversal orifice 155 is arranged between two adjacent heat exchange tubes 5 received in a first frame 13 and in fluid communication with these two heat exchange tubes 5.
  • the first fluid which emerges from a first heat exchange tube 5 undergoes a reversal in the reversal orifice 155 then circulates to a second heat exchange tube 5.
  • the two rows of heat exchange tubes 5 arranged in the first frames 13 then communicate at one end via the reversal orifices 155 provided on the second frames 15, in particular spacers.
  • Each reversal orifice 155 is here formed between through passage orifices 151 on at least one lateral edge of each second frame 15, in particular in between.
  • Each reversal orifice 155 advantageously has a longitudinal shape extending substantially perpendicular to the general direction of flow of the first fluid in the two heat exchange tubes 5.
  • each reversal orifice 155 has a longitudinal shape extending perpendicular to the longitudinal edges of the second frame 15, in particular in between.
  • each reversal orifice 155 arranged opposite a first receiving frame 13, extends longitudinally on either side of the partition 135 of this first receiving frame 13.
  • the reversal orifice 155 has a substantially oblong shape.
  • the reversal orifice 155 is dimensioned so as to have a section for the reversal of the first fluid at least equal to the section of passage of a heat exchange tube 5.
  • a circulation in two passes known as a “U”
  • a circulation in two passes called "U” shape of the second fluid in a second frame 15 according to the second embodiment.
  • the heat exchanger 1 is then dual circulation in "U”.
  • the heat exchanger 1 comprises a stack of the heat exchange tubes 5 advantageously received in first frames 13 and second frames 15 advantageously receiving turbulators 11.
  • the reservoirs 154 provided on the end edges of the second frames 15 allow the coating which melts and migrates during brazing to flow into these reservoirs 154 thus avoiding blocking the first circulation channels or micro-channels 7 for the first fluid in the heat exchange tubes 5.

Landscapes

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

Claims (8)

  1. Wärmeaustauscher (1) für einen Wärmeaustausch zwischen wenigstens einem ersten Fluid und einem zweiten Fluid, insbesondere für ein Kraftfahrzeug:
    - wobei der Wärmeaustauscher (1) ein Wärmeaustauschbündel (3) umfasst, mit einem Stapel mit abwechselnder Anordnung:
    • von Wärmeaustauschrohren (5), die Zirkulationskanäle (7) für das erste Fluid aufweisen, und
    • von Zwischenstücken (15), und
    - wobei der Wärmeaustauscher (1) wenigstens teilweise eine Beschichtung aufweist, die in der Lage ist zu schmelzen, um so die Verbindung von Elementen des Wärmeaustauschers bei einem Zusammenbau durch Löten sicherzustellen,
    dadurch gekennzeichnet, dass:
    - die Zwischenstücke (15) jeweils wenigstens einen Behälter (154) aufweisen, der in der Lage ist, die Beschichtung beim Löten des Wärmeaustauschers (1) zu sammeln,
    - jeder Behälter (154) an einem Ende eines Zwischenstücks (15) und gegenüber einem Ende eines Wärmeaustauschrohres (5) angeordnet ist,
    um so zu verhindern, dass die Beschichtung den wenigstens einen Zirkulationskanal (7) des Wärmeaustauschrohres (5) beim Löten des Wärmeaustauschers (1) verstopft.
  2. Wärmeaustauscher (1) nach dem vorhergehenden Anspruch, wobei die Zwischenstücke (15) jeweils wenigstens einen Behälter (154) auf jeder Seite gegenüber einem Wärmeaustauschrohr (5) aufweisen.
  3. Wärmeaustauscher (1) nach einem der Ansprüche 1 oder 2, welcher einen Stapel umfasst mit abwechselnder Anordnung:
    - von ersten Rahmen (13) zur Aufnahme der Wärmeaustauschrohre, und
    - von zweiten Rahmen (15), wobei wenigstens einige zweite Rahmen die Zwischenstücke bilden, wobei die zweiten Rahmen (15) jeweils wenigstens einen Behälter (154) an wenigstens einem Rand des zweiten Rahmens (15) aufweisen, der sich im Wesentlichen senkrecht zur Fließrichtung des ersten Fluids in den Wärmeaustauschrohren (5) erstreckt.
  4. Wärmeaustauscher (1) nach einem der vorhergehenden Ansprüche, wobei der Behälter (154) durch Materialreduzierung eines Zwischenstücks (15) hergestellt ist.
  5. Wärmeaustauscher (1) nach einem der vorhergehenden Ansprüche, wobei der Behälter in Form einer Nut (154) hergestellt ist, die sich im Wesentlichen senkrecht zur Fließrichtung des ersten Fluids in den Wärmeaustauschrohren (5) erstreckt.
  6. Wärmeaustauscher (1) nach einem der vorhergehenden Ansprüche, wobei sich der Behälter (154) gegenüber jedem Ende eines Wärmeaustauschrohres (5) erstreckt, zum Beispiel auf der gesamten Länge eines Wärmeaustauschrohres (5), das in Form eines Flachrohres hergestellt ist.
  7. Wärmeaustauscher (1) nach Anspruch 3 in Kombination mit einem der vorhergehenden Ansprüche, wobei die ersten Rahmen (13) zur Aufnahme jeweils wenigstens einen Rücksprung (139) an einer inneren Ecke, die eine Ecke eines Wärmeaustauschrohres (5) aufnimmt, für das Fließen der Beschichtung beim Löten des Wärmeaustauschers (1) aufweisen, um so zu verhindern, dass die Beschichtung die Kanäle (7) der Wärmeaustauschrohre (5) verstopft.
  8. Wärmeaustauscher (1) nach Anspruch 5 in Kombination mit Anspruch 7, wobei die Breite des Rücksprungs (139) im Wesentlichen gleich der Breite der Nut (154) ist.
EP16826391.1A 2015-12-21 2016-12-16 Wärmeaustauscher, insbesondere für ein kraftfahrzeug Active EP3394544B1 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR1562888A FR3045800B1 (fr) 2015-12-21 2015-12-21 Echangeur thermique, notamment pour vehicule automobile
PCT/FR2016/053502 WO2017109354A1 (fr) 2015-12-21 2016-12-16 Échangeur thermique, notamment pour véhicule automobile

Publications (2)

Publication Number Publication Date
EP3394544A1 EP3394544A1 (de) 2018-10-31
EP3394544B1 true EP3394544B1 (de) 2020-01-08

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Family Applications (1)

Application Number Title Priority Date Filing Date
EP16826391.1A Active EP3394544B1 (de) 2015-12-21 2016-12-16 Wärmeaustauscher, insbesondere für ein kraftfahrzeug

Country Status (3)

Country Link
EP (1) EP3394544B1 (de)
FR (1) FR3045800B1 (de)
WO (1) WO2017109354A1 (de)

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1870658A1 (de) * 2006-06-20 2007-12-26 Delphi Technologies, Inc. Wärmetauscher und Verfahren zum Herstellen eines Wärmetauschers
DE102008019320A1 (de) * 2008-04-16 2009-10-22 Behr Gmbh & Co. Kg Wärmeübertrager, insbesondere Abgasverdampfer eines Kraftfahrzeuges
DE202008013351U1 (de) * 2008-10-08 2010-03-25 Autokühler GmbH & Co. KG Wärmeaustauschernetz und damit ausgerüsteter Wärmeaustauscher

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
None *

Also Published As

Publication number Publication date
EP3394544A1 (de) 2018-10-31
WO2017109354A1 (fr) 2017-06-29
FR3045800B1 (fr) 2017-12-29
FR3045800A1 (fr) 2017-06-23

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