• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    Heat exchanger (1) between a first fluid flowing in a longitudinal direction (X) and a second fluid, said exchanger (1) comprising: - two parallel plates (6) spaced apart from each other; at least a first and a second row (8a, 8b) of fins (9) arranged perpendicularly between said plates (6), each fin (9) being delimited longitudinally by a first edge (10) and a second edge (11); ), said first edge (10) comprising at each of its ends a connecting zone with the corresponding plate (6); characterized in that said connecting regions of said first edge (10) are respectively inclined with respect to a normal to the plates (6) in a plane (P) perpendicular to said plates (6) and parallel to the direction (X), said first edge (10) and said second edge (11) of each of the fins (9) having an identical profile in said plane (P).
    公开号:FR3058510A1
    申请号:FR1660886
    申请日:2016-11-10
    公开日:2018-05-11
    发明作者:Ephraim Toubiana
    申请人:Safran SA；
    IPC主号:
    专利说明:

    (54) HEAT EXCHANGER.
    ©) Heat exchanger (1) between a first fluid SOCoulant in a longitudinal direction (X) and a second fluid, said exchanger (1) comprising:
    - two parallel plates (6) spaced from each other;
    - at least a first and a second row (8a, 8b) of fins (9) arranged perpendicularly between said plates (6), each fin (9) being delimited longitudinally by a first edge (10) and a second edge (11 ), said first edge (10) comprising at each of its ends a connection zone with the corresponding plate (6); characterized in that said connecting zones of said first edge (10) are respectively inclined with respect to a normal to the plates (6) in a plane (P) perpendicular to said plates (6) and parallel to the direction (X), said first edge (10) and said second edge (11) of each of the fins (9) having an identical profile in said plane (P).
    X
    2- ^.
    HEAT EXCHANGER
    TECHNICAL AREA
    The present invention relates to heat exchangers in particular for a turbomachine.
    STATE OF THE ART
    A turbomachine comprises a gas generator comprising, for example, from upstream to downstream in the direction of gas flow, one or more compressor stages, a combustion chamber, one or more turbine stages, and an ejection nozzle exhaust gases.
    A heat exchanger is installed in a turbomachine to allow transfer of thermal energy from one fluid to another.
    Such a heat exchanger is for example used for the transfer of thermal energy from the hot exhaust gases to a gas intended to be introduced upstream of the combustion chamber, for the benefit in particular of the fuel consumption of the turbomachine. This heat exchanger can also be used to cool the lubricant (for example oil) of the various means for guiding the rotors of the gas generator.
    Such an exchanger is for example obtained by additive manufacturing by selective melting on powder beds commonly designated by the English acronym SLM for "Selective Laser Melting". The principle of SLM additive manufacturing is based on the fusion of thin two-dimensional (2D) layers of powder (metallic, plastic, ceramic, etc.) using a high-power laser. SLM technology has the advantage of enabling the production of parts with complex geometric shapes and good mechanical characteristics.
    With equivalent aerothermal performance, finned heat exchangers are particularly used in turbomachinery due in particular to their low mass.
    Such a heat exchanger, between a first fluid (for example hot exhaust gases) flowing in a longitudinal direction X and a second fluid (for example air), comprises for example two distant parallel plates l ' one of the other so as to define a circulation passage for the first fluid and a plurality of rows of fins arranged perpendicularly between the plates.
    More specifically, the rows of fins extend longitudinally. Each fin is delimited longitudinally by a leading edge and a trailing edge perpendicular to the plates.
    Such an architecture has the particular disadvantage of causing a significant loss of mechanical energy of the first fluid partly due to the presence of a recirculation zone in the flow at each of the leading edges of the fins. This recirculation zone is all the more significant due to the variation in the cross-sections of the first fluid, which causes local accelerations.
    In addition, by SLM manufacturing, in a vertical orientation (plates and fins perpendicular to the construction support), such an architecture does not make it possible to meet the dimensional and geometric tolerances desired at the end of the manufacturing. Indeed, the fusion of an overhanging layer, the normal of which is parallel to the direction of addition of the layers, poses difficulties in achieving the fact in particular that only the non-fused powder serves as a support during the fusion of such a layer. overhanging.
    The objective of the present invention is thus to propose a heat exchanger, with equivalent mass, having improved aerothermal characteristics, and respecting the desired dimensional and geometric tolerances, when it is obtained by additive manufacturing by selective melting on beds of powder.
    STATEMENT OF THE INVENTION
    To this end, the invention proposes a heat exchanger between a first fluid flowing in a longitudinal direction X and a second fluid, said exchanger comprising:
    - two parallel plates spaced from one another so as to define a circulation passage for said first fluid;
    - At least a first and a second row of fins arranged perpendicularly between said plates, said first and second rows extending longitudinally, the fins of said first row being preferably staggered relative to the fins of said second row, each winglet being delimited longitudinally by a first edge and a second edge, said first edge comprising at each of its ends a zone of connection with the corresponding plate;
    characterized in that said connecting zones of said first edge are respectively inclined by an angle A and by an angle B with respect to a normal N to the plates in a plane P perpendicular to said plates and parallel to the direction X, said first edge and said second edge of each of the fins having an identical profile in said plane P.
    Such geometrical characteristics associated with the fins allow, at equivalent mass, not only to significantly improve the aerothermal performance of the exchanger but also to respect the desired dimensional and geometrical tolerances, when it is obtained by additive manufacturing by selective melting on beds. powder.
    On the one hand, such geometric characteristics make it possible to significantly reduce the recirculation zone in the flow at each of the leading edges (first edge or second edge depending on the direction of flow) of the fins , and therefore reduce mechanical energy losses. This reduction is all the more important since there is no variation in the cross sections of the first fluid. Compared to the heat exchangers of the prior art, it is estimated that the reduction in pressure losses is of the order of 15%.
    On the other hand, for SLM manufacturing, by positioning the hollow edge on the side of the construction support if necessary, the connection zones respectively constitute a first and a second primer for manufacturing the fin. Thus, during manufacture, there is no overhanging layer to be fused and in other words the non-fused powder is not used as a support, for the benefit of compliance with dimensional and geometric tolerances.
    The exchanger according to the invention may include one or more of the following characteristics, taken in isolation from one another or in combination with each other:
    - angle A is equal to angle B;
    - the angle A and / or the angle B is greater than 40 °, and preferably greater than or equal to 45 °;
    in the plane P, more than 90% of the length of the first edge is inclined relative to the normal N, and preferably more than 95%;
    - Said first edge comprises at least one rectilinear section inclined with respect to the normal N and / or at least one circular section and / or at least one elliptical section;
    - Said first edge comprises two rectilinear sections inclined with respect to the normal N and having concurrent directions;
    - the fins are spaced longitudinally at a constant pitch.
    The second object of the invention is a method of producing an exchanger as described above, in which it comprises a step of producing said exchanger by additive manufacturing by selective melting on powder beds along a manufacturing axis Z parallel to said direction longitudinal X.
    Alternatively, said fins each comprise a first hollow edge and a second projecting edge, the exchanger being produced on a construction support, said first hollow edge being oriented on the side of said support.
    The third object of the invention is a turbomachine comprising a heat exchanger as described above.
    DESCRIPTION OF THE FIGURES
    The invention will be better understood and other details, characteristics and advantages of the invention will appear more clearly on reading the following description given by way of non-limiting example and with reference to the accompanying drawings in which:
    - Figures 1 and 2 are perspective views of a heat exchanger (two stages) according to the invention, each stage comprising two plates and a plurality of rows of fins arranged between the plates, according to a first mode of production ;
    - Figure 3 is a detail view of a fin of the heat exchanger of Figures 1 and 2, in a plane P;
    - Figure 4 is a perspective view of a heat exchanger, according to a second embodiment;
    - Figure 5 is a detail view of a fin of the heat exchanger of Figure 4, in a plane P;
    - Figure 6 is a schematic view of a machine for producing a heat exchanger (or a heat exchanger stage) according to the invention, by additive manufacturing;
    - Figures 7 to 10 are detailed views, in a plane P, similar to those of Figures 3 and 5, and illustrate alternative embodiments of the fins according to the invention.
    DETAILED DESCRIPTION
    FIGS. 1 and 2 show a heat exchanger 1 between a first fluid (for example hot exhaust gases) flowing in a longitudinal direction X and a second fluid (for example air).
    More specifically, the exchanger 1 is stepped, namely a first and a second stage 2, 3 for circulation of the first fluid. A first path 4 for circulation of the second fluid is formed between the first and second stages 2, 3 (inter-stage circulation path). A second path 5 for circulation of the second fluid (not shown in FIG. 2) is provided on the free side of the second stage 3.
    The example illustrated is in no way limiting, depending on the needs, the exchanger 1 could have a number N of stages each defining a circulation passage for the first fluid, two adjacent stages being separated by a circulation path from the second fluid.
    Note that the flow of the first fluid in the longitudinal direction X can be upstream downstream (as illustrated in Figure 1) or downstream upstream.
    In heat exchanger 1, there is no mixture between the first and the second fluid.
    Each stage 2, 3 of the exchanger 1 comprises two parallel plates 6 distant from each other so as to define a passage 7 for circulation of the first fluid and a plurality of rows 8a, 8b (in this case ten) fins 9 conducting heat arranged perpendicularly between said plates 6.
    More specifically, the rows 8a, 8b extend longitudinally (in the direction X). The fins 9 of two adjacent rows 8a, 8b are staggered. Each fin 9 is delimited longitudinally by a first edge 10 and a second edge 11, the first edge 10 comprising at each of its ends a connecting zone 12a, 12b with the corresponding plate 6.
    The connecting zones 12a, 12b of the first edge 10 are respectively inclined by an angle A and by an angle B relative to a normal N to the plates 6, in a plane P perpendicular to the plates 6 and parallel to the direction X. The first edge 10 and the second edge 11 of each of the fins 9 have an identical profile, in the plane P.
    According to the embodiment illustrated in Figures 1 to 2 (respectively in the embodiment of Figure 4), the fins 9 are identical (that is to say that they have the same geometric and dimensional characteristics) and spaced longitudinally by a constant pitch (or spacing). On the same row 8a, 8b, two consecutive fins 9 are spaced by an interval equivalent to a fin 9 (and more precisely to the longitudinal dimension of a fin 9).
    By staggered arrangement is meant a repetitive arrangement, row to row, where every other row, the fins 9 are offset by half a step with respect to the adjacent rows.
    As a variant, the pitch could be variable or the exchanger 1 could be divided longitudinally into portions, each portion having its own pitch.
    As a variant, the fins 9 of two adjacent rows 8a, 8b could overlap partially, in the plane P.
    Within the meaning of the invention, in a plane P, when the connecting zone 12a is rectilinear, the angle A (respectively for the angle B) corresponds to the angle between the connecting zone 12a and the normal N.
    Within the meaning of the invention, in a plane P, when the connecting zone 12a (respectively connecting zone 12b) is curved, the angle A (respectively for the angle B) corresponds to the angle between the tangent T to the connection area 12a (at a point located near the corresponding plate 6) and the normal N.
    Advantageously, in a plane P, more than 90% of the length of the first edge 10 (respectively of the second edge 11) is inclined relative to the normal N, and preferably more than 95%.
    The angle A and / or the angle B is greater than 40 °, and cb preferably greater than or equal to 45 °.
    According to a first embodiment illustrated in FIGS. 1 to 3, for each fin 9, in a plane P, the first edge 10 (respectively the second edge 11) comprises two rectilinear sections 13 inclined with respect to the normal N and having concurrent directions.
    More precisely, the first edge 10 has a general shape of V. Each of the rectilinear sections 13 converges from the corresponding plate 6. The two rectilinear sections 13 are joined by a fillet 14 (concave shape). The angle A is equal to the angle B, and is equal to 45 °.
    According to a second embodiment illustrated in FIGS. 4 and 5, for each fin 9, in a plane P, the first edge 10 comprises a single rectilinear section 15 inclined relative to the normal N. Each fin 9 thus has a shape of parallelogram. The angle A is equal to the angle B, and is equal to 45 °.
    FIG. 6 shows a machine 100 for manufacturing a heat exchanger 1 or a stage 2, 3 of the exchanger 1 by additive manufacturing, and in particular by selective melting of powder layers 160 by high energy bundle 195 .
    The heat exchanger 1 (or the stage 2, 3 of the exchanger 1) is advantageously manufactured along a manufacturing axis Z parallel to the longitudinal direction X (plates 6 and fins 9 perpendicular to the construction support 180) (see Figures 3 and 5).
    The machine 100 comprises a supply tank 170 containing powder 160 (metallic in the present case), a roller 130 for transferring this powder 160 from the tank 170 and spreading a first layer 110 of this powder 160 on a construction support 180 movable in translation along the manufacturing axis Z (the support 180 may for example be a plate, part of another room or a grid).
    The machine 100 also includes a recycling bin 140 for recovering the excess powder 160 after spreading the powder layer by the roller 130 on the construction support 180.
    The machine 100 further comprises a laser beam generator 190 195, and a control system 150 capable of directing this beam 195 over the whole of the construction support 180 so as to merge the desired portions of powder 160. The shaping of the laser beam 195 and the variation of its diameter on the focal plane are done respectively by means of a beam dilator 152 and a focusing system 154, the assembly constituting the optical system.
    More specifically, the control system 150 comprises for example at least one orientable mirror 155 on which the laser beam 195 is reflected before reaching the powder layer 160. The angular position of this mirror 155 is controlled, for example, by a galvanometric head so that the laser beam 195 scans the desired portions of the first layer 110 of powder 160, according to a preset profile.
    The heat exchanger 1 (or stage 2, 3 of the exchanger 1) is manufactured along the manufacturing axis Z (parallel to the direction X) (plates 6 and fins 9 perpendicular to the construction support 180). As illustrated in FIG. 3, when the profile of the fins 9 comprises a hollow edge 10 and a projecting edge 11, the hollow edges 10 must be oriented towards the side of the construction plate in order to avoid any overhanging layer to merge.
    The manufacture of an exchanger 1 (or of a stage 2, 3 of exchanger 1) using the machine 100 comprises the following steps.
    A first layer 110 of powder 160 is deposited on the construction support 180 using the roller 130. At least a portion of this first layer 110 of powder 160 is brought to a temperature higher than the melting temperature of this powder 160 by means of the laser beam 195 so that the powder particles 160 of this portion of the first layer 110 are melted and form a first bead 115 in one piece, integral with the construction support 180.
    Then the support 180 is lowered by a height corresponding to the already defined thickness of the first layer 110. A second layer 120 of powder 160 is deposited on the first layer 110 and on this first bead 115, then at least a portion located partially or completely above this first bead 115 is heated by exposure to the laser beam 195 so that the powder particles 160 of this portion of the second layer 120 are melted, with at least part of the first element 115, and form a second cord 125. All of these two cords 115 and 125 form a unitary block.
    The process of building the part is then continued layer by layer, by adding additional layers of powder 160 to the assembly already formed. The scanning with the beam 195 makes it possible to construct each layer by giving it a shape in accordance with the geometry of the part to be produced.
    Exchanger 1 (or stage 2, 3 of exchanger 1) in three dimensions (3D) is therefore obtained by superimposing layers in two dimensions (2D), along the manufacturing axis Z.
    The powder 160 is advantageously made of a material having good thermal conductivity in order to maximize the heat transfers between the first fluid and the second fluid, and thus increase the efficiency of the heat exchanger 1.
    Advantageously, the powder 160 is metallic and preferably made of steel or a metallic alloy, for example based on nickel.
    Figures 7 to 10 illustrate different alternative embodiments of the invention.
    According to a first alternative embodiment shown in FIG. 7, for each fin 9, in a plane P, the first edge 10 comprises a single concave elliptical section 16. The elliptical section 16 corresponds to a section of an ellipse 17 of construction (shown in dotted lines) the center of which is located equidistant from the two plates 6, offset longitudinally with respect to the connecting zones 12a, 12b, the ellipse 17 of construction being tangent to the plates 6. The elliptical section 16 has an angle at the center slightly less than 180 °.
    According to a second alternative embodiment shown in the figure
    8, for each fin 9, in a plane P, the first edge 10 comprises two elliptical sections 18 convex.
    More precisely, each of the elliptical sections 18 converges from the corresponding plate 6. The two elliptical sections 18 are joined by a fillet 19 (concave shape) so as to form a first and a second inflection point I, J. The elliptical sections 18 each correspond to a section of an ellipse 20 of construction (shown dotted line) having an angle at the center substantially equal to 90 ° (ellipse quarter). These construction ellipses 20 are superimposed, aligned and have the same dimensional characteristics.
    According to a third alternative embodiment shown in the figure
    9, for each fin 9, in a plane P, the first edge 10 comprises a single concave elliptical section 21. The elliptical section 21 corresponds to an ellipse section having an angle at the center substantially equal to 90 ° (ellipse quarter) and is connected to one of the plates 6 via a fillet 22 (concave shape).
    According to a fourth alternative embodiment shown in the figure
    10, for each fin 9, in a plane P, the first edge 10 comprises a single circular section 23 convex. The circular section 23 corresponds to an arc of a circle having an angle at the center substantially equal to 90 ° (quarter of a circle) and is connected to the plates 6 via a fillet 24 (concave shape).
    To improve mechanical and aerothermal performance, the sharp edges can be replaced by fillets (concave shape) or rounded shapes (convex shape).
    The various illustrated embodiments of the fins 9 are not limiting. Indeed, within the meaning of the invention, the first edge 10 may contain one or more rectilinear sections and / or one or more curved sections, however, advantageously, more than 90% of the length of the first edge 10 (in a plane P ) (and respectively of the second edge 11) is inclined relative to the normal N, and preferably 95%.
    权利要求:
    Claims (10)
    [1" id="c-fr-0001]
    1. Heat exchanger (1) between a first fluid flowing in a longitudinal direction (X) and a second fluid, said exchanger (1) comprising:
    - two parallel plates (6) spaced from one another so as to define a passage (7) for circulation of said first fluid;
    - At least a first and a second row (8a, 8b) of fins (9) arranged perpendicularly between said plates (6), said first and second rows (8a, 8b) extending longitudinally, the fins (9) of said first row (8a) being preferably staggered relative to the fins (9) of said second row (8b), each fin (9) being delimited longitudinally by a first edge (10) and a second edge (11), said first edge (10) comprising at each of its ends a connection zone (12a, 12b) with the corresponding plate (6);
    characterized in that said zones (12a, 12b) of connection of said first edge (10) are respectively inclined by an angle (A) and an angle (B) relative to a normal (N) to the plates (6) in a plane (P) perpendicular to said plates (6) and parallel to the direction (X), said first edge (10) and said second edge (11) of each of the fins (9) having an identical profile in said plane (P ).
    [2" id="c-fr-0002]
    2. Exchanger according to claim 1, characterized in that the angle (A) is equal to the angle (B).
    [3" id="c-fr-0003]
    3. Exchanger according to one of the preceding claims, characterized in that the angle (A) and / or the angle (B) is greater than 40 °, and preferably greater than or equal to 45 °.
    [4" id="c-fr-0004]
    4. Exchanger according to one of the preceding claims, characterized in that, in the plane (P), more than 90% of the length of the first edge (10) is inclined relative to the normal (N), and preferably more than 95%.
    [5" id="c-fr-0005]
    5. Exchanger according to one of the preceding claims, characterized in that said first edge (10) comprises at least one rectilinear section (13, 15) inclined relative to the normal (N) and / or at least one circular section ( 23) and / or at least one elliptical section (16, 18, 21).
    [6" id="c-fr-0006]
    6. Exchanger according to one of claims 1 to 4, characterized in that said first edge (10) comprises two rectilinear sections (13) inclined relative to the normal (N) and having concurrent directions.
    [7" id="c-fr-0007]
    7. Exchanger according to one of the preceding claims, characterized in that the fins (9) are spaced longitudinally by a constant pitch.
    [8" id="c-fr-0008]
    8. Method for producing an exchanger (1) according to one of claims 1 to 7, in which it comprises a step for producing said exchanger (1) by additive manufacturing by selective melting on powder beds (160) according to a manufacturing axis (Z) parallel to said longitudinal direction (X).
    [9" id="c-fr-0009]
    9. Method according to claim 8, characterized in that said fins (9) each comprise a first hollow edge (10) and a second projecting edge (11), the exchanger (1) being produced on a construction support (180 ), said first hollow edge (10) being oriented on the side of said support (180).
    [10" id="c-fr-0010]
    10. Turbomachine comprising a heat exchanger (1) according to one of claims 1 to 7.
    3 ° 5δ5ΐο
    1/4
    8b <o σ> (q <o F 'Sl · 2
    X
    3/4
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    同族专利:
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    引用文献:
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    法律状态:
    2017-10-19| PLFP| Fee payment|Year of fee payment: 2 |
    2018-05-11| PLSC| Publication of the preliminary search report|Effective date: 20180511 |
    2018-10-24| PLFP| Fee payment|Year of fee payment: 3 |
    2019-10-22| PLFP| Fee payment|Year of fee payment: 4 |
    2020-10-21| PLFP| Fee payment|Year of fee payment: 5 |
    2021-10-20| PLFP| Fee payment|Year of fee payment: 6 |
    优先权:
    申请号 | 申请日 | 专利标题
    FR1660886A|FR3058510B1|2016-11-10|2016-11-10|HEAT EXCHANGER|
    FR1660886|2016-11-10|FR1660886A| FR3058510B1|2016-11-10|2016-11-10|HEAT EXCHANGER|
    PCT/FR2017/053059| WO2018087480A1|2016-11-10|2017-11-09|Heat exchanger|
    RU2019113787A| RU2742365C2|2016-11-10|2017-11-09|Heat exchanger|
    CN201780068618.3A| CN109952485B|2016-11-10|2017-11-09|Heat exchanger|
    EP17801087.2A| EP3538832B1|2016-11-10|2017-11-09|Heat exchanger|
    JP2019523591A| JP2019535990A|2016-11-10|2017-11-09|Heat exchanger|
    CA3042754A| CA3042754A1|2016-11-10|2017-11-09|Heat exchanger|
    US16/348,111| US20190277576A1|2016-11-10|2017-11-09|Heat exchanger|
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