WO2017097133A1 - 一种换热器 - Google Patents

一种换热器 Download PDF

Info

Publication number
WO2017097133A1
WO2017097133A1 PCT/CN2016/107483 CN2016107483W WO2017097133A1 WO 2017097133 A1 WO2017097133 A1 WO 2017097133A1 CN 2016107483 W CN2016107483 W CN 2016107483W WO 2017097133 A1 WO2017097133 A1 WO 2017097133A1
Authority
WO
WIPO (PCT)
Prior art keywords
communication
cavity
bent portion
heat exchange
interface
Prior art date
Application number
PCT/CN2016/107483
Other languages
English (en)
French (fr)
Inventor
刘波
邹江
尹芳芳
吕刚
张荣荣
殷玉婷
Original Assignee
浙江三花汽车零部件有限公司
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
Priority claimed from CN201510906370.6A external-priority patent/CN106855328B/zh
Priority claimed from CN201510905980.4A external-priority patent/CN106855369B/zh
Priority claimed from CN201510906354.7A external-priority patent/CN106855327B/zh
Priority claimed from CN201610196745.9A external-priority patent/CN107289674B/zh
Priority claimed from CN201610196914.9A external-priority patent/CN107289675B/zh
Priority claimed from CN201610201002.6A external-priority patent/CN107289676B/zh
Priority claimed from CN201610201884.6A external-priority patent/CN107289677B/zh
Priority claimed from CN201610634384.1A external-priority patent/CN107687787B/zh
Priority claimed from CN201610629325.5A external-priority patent/CN107687726B/zh
Priority to EP16872324.5A priority Critical patent/EP3388770B1/en
Priority to US16/060,017 priority patent/US10520258B2/en
Application filed by 浙江三花汽车零部件有限公司 filed Critical 浙江三花汽车零部件有限公司
Publication of WO2017097133A1 publication Critical patent/WO2017097133A1/zh

Links

Images

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
    • F28D7/08Heat-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 otherwise bent, e.g. in a serpentine or zig-zag
    • F28D7/082Heat-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 otherwise bent, e.g. in a serpentine or zig-zag with serpentine or zig-zag configuration
    • 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
    • F28F1/02Tubular elements of cross-section which is non-circular
    • F28F1/025Tubular elements of cross-section which is non-circular with variable shape, e.g. with modified tube ends, with different geometrical features
    • 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
    • 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
    • F28F1/24Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely
    • F28F1/32Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely the means having portions engaging further tubular elements
    • F28F1/325Fins with openings
    • 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
    • F28F9/001Casings in the form of plate-like arrangements; Frames enclosing a heat exchange core
    • 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
    • F28F9/0219Arrangements for sealing end plates into casing or header box; Header box sub-elements
    • F28F9/0221Header boxes or end plates formed by stacked elements
    • 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
    • F28F9/0243Header boxes having a circular cross-section
    • 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
    • F28F9/0246Arrangements for connecting header boxes with flow lines
    • F28F9/0251Massive connectors, e.g. blocks; Plate-like connectors
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02Header boxes; End plates
    • F28F9/026Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
    • F28F9/0278Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits in the form of stacked distribution plates or perforated plates arranged over end plates
    • 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
    • F28D1/047Heat-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 bent, e.g. in a serpentine or zig-zag
    • F28D1/0477Heat-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 bent, e.g. in a serpentine or zig-zag the conduits being bent in a serpentine or zig-zag
    • F28D1/0478Heat-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 bent, e.g. in a serpentine or zig-zag the conduits being bent in a serpentine or zig-zag the conduits having a non-circular cross-section
    • 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
    • F28D21/00Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D2021/0019Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
    • F28D2021/0068Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for refrigerant cycles
    • 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
    • F28F1/02Tubular elements of cross-section which is non-circular
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2230/00Sealing means

Definitions

  • the invention relates to the field of heat exchange technology, such as to a vehicle heat exchange technology.
  • CO 2 is a new type of environmentally friendly refrigerant that can reduce the global greenhouse effect and fundamentally solve the problem of compound pollution to the environment. It has good economy and practicability. Compressed refrigeration cycle systems with CO 2 as the working fluid can be used in most refrigeration/heating fields.
  • CO 2 heat exchangers mainly include tube fin type, micro channel, plate type, shell and tube type, plate fin type and sleeve type. Among them, the plate type and the plate-fin type manufacturing process are complicated, and the tube-and-tube type, the tube type and the tube-and-tube type wall thickness need to be thick and waste materials.
  • the traditional CO 2 microchannel heat exchanger is heat exchanged by means of refrigerant and air forced convection, and the efficiency is low. Although the difference between liquid and air properties is large, liquid-gas heat exchange has high heat exchange efficiency, but the liquid-gas heat exchanger in the prior art has a thick wall thickness and poor heat transfer performance. .
  • the present invention provides a heat exchanger capable of effectively solving the above technical problems.
  • the present invention provides a heat exchanger comprising a tank body and a heat exchange core body accommodated in the tank body, a first fluid passage is formed in the tank body, and a second fluid passage is formed in the heat exchange core body.
  • the heat exchange core is external to the first fluid passage, the first fluid passage and the second fluid passage are isolated from each other, the heat exchange core includes one or more flat tubes, and the second fluid The channel is located in the flat tube, and the flat tube includes a plurality of first bending portions, a plurality of second bending portions and a plurality of straight portions, wherein the first bending portion and the second bending portion are respectively located at the The opposite sides of the heat exchange core body, two adjacent straight portions are substantially parallel and maintain a distance of 0.5 mm to 6 mm;
  • the box body is provided with a first hole and a second hole communicating with the outside, and the first bent portion and/or the flat portion is adjacent to the first bent portion to correspond to the first hole a projection of an inner wall direction of the case and a projection of an inner wall direction of the first hole or the first hole corresponding to the first hole at least partially, the second bent portion And/or a projection of the straight portion near the second bent portion toward the inner wall of the case corresponding to the second hole and the second hole or the second hole toward the first
  • the projection of the inner wall direction of the casing corresponding to the two holes is at least partially heavy.
  • the heat exchanger of the above technical solution can make the heat exchange fluid contact with most of the outer wall of the flat tube, can improve the effective heat exchange area of the heat exchanger, and the flow direction of the heat exchange fluid is substantially the same as the flow direction of the refrigerant or On the contrary, and the flow directions at the positions of the relatively straight portions are substantially parallel or anti-parallel, the heat exchange performance between the refrigerant and the heat exchange fluid can be improved, and the heat exchange performance of the heat exchanger can be effectively improved.
  • Figure 1 is a perspective view of an embodiment of a heat exchanger according to the present invention.
  • FIG 2 is a schematic exploded view of the heat exchanger shown in Figure 1;
  • Figure 3 is a cross-sectional view of the heat exchanger of Figure 1 taken along the line B-B;
  • Figure 4 is a cross-sectional view showing the A-A of the flat tube and fin assembly of the heat exchanger shown in Figure 1;
  • Figure 5 is a partial enlarged view of Figure 4.
  • Figure 6 is a partial structural view of the flat tube shown in Figure 4 at a bend
  • Figure 7 is a schematic view showing the structure of a flat tube in which adjacent bending portions are dislocated
  • Figure 8 is a schematic structural view of a distribution plate of the heat exchanger shown in Figure 1;
  • Figure 9 is a schematic structural view of the first cover of the heat exchanger shown in Figure 1;
  • FIG. 10 is a perspective view showing another embodiment of the heat exchanger of the present invention.
  • Figure 11 is a schematic exploded view of the first cover plate and the distribution plate of the embodiment shown in Figure 10;
  • Figure 12 is a schematic view showing still another structure of the distribution plate of the heat exchanger.
  • Figure 13 is a schematic view showing the structure of a plurality of heat exchange cores of a heat exchanger in which a plurality of flat tubes are arranged side by side;
  • Figure 14 is a schematic exploded view of a heat exchanger according to still another embodiment of the present invention.
  • Figure 15 is a schematic view of a distribution plate of the heat exchanger shown in Figure 14;
  • Figure 16 is a schematic view of another distribution plate of the heat exchanger shown in Figure 14;
  • FIG 17 is a schematic view of still another distribution plate of the heat exchanger shown in Figure 14;
  • FIG. 18 is a schematic view of the flat tube and the fin inside the box body of the heat exchanger shown in FIG. 14; wherein the dotted line generally depicts the example area, and the shape thereof is not limited;
  • Figure 19 is a bottom plan view showing an embodiment of the cover of the heat exchanger shown in Figure 14;
  • Figure 20 is a schematic exploded view of an embodiment of the heat exchanger of the present invention.
  • Figure 21 is a schematic structural view of a second connecting block of the heat exchanger shown in Figure 20;
  • Figure 22 is a schematic structural view of a mounting plate of the heat exchanger shown in Figure 20;
  • Figure 23 is a perspective view showing the first mounting plate and the second mounting plate of the heat exchanger shown in Figure 20 in combination;
  • Figure 24 is a cross-sectional view taken along line A-A of Figure 23;
  • Figure 25 is a cross-sectional view showing the housing of the heat exchanger shown in Figure 20;
  • Figure 26 is a cross-sectional view of the heat exchanger of Figure 20 at a third interface and a fourth interface portion;
  • Figure 27 is a cross-sectional view of the heat exchanger of Figure 20 in a first chamber and a second chamber;
  • Figure 28 is a schematic exploded view of a further embodiment of the heat exchanger of the present invention.
  • Figure 29 is a cross-sectional view of the heat exchanger shown in Figure 28.
  • FIG. 1 is a perspective view of an embodiment of a heat exchanger according to the present invention
  • FIG. 2 is a schematic exploded view of the heat exchanger of FIG. 1.
  • the heat exchanger includes a casing 1 and accommodates In the heat exchange core body in the casing 1, a first fluid passage is formed in the tank body, and a second fluid passage is formed in the heat exchange core body, the heat exchange core body is a part of the first fluid passage, and the first fluid passage is The second fluid passages are isolated from each other, and the first joints 5 and the second joints 4 communicating with the first fluid passages are fixedly disposed with the tank 1.
  • the space outside the heat exchange core includes a space between the flat tube and the flat tube, a space between the flat tube and the fin, and a space in the fin.
  • the box body 1 includes a box body 14, a first cover plate 12, a distribution plate 13 and a second cover plate 15.
  • the box body 14 is an approximately rectangular parallelepiped or a square body having open ends on two sides, and the two open ends of the box body 14 are located The two sides are disposed adjacent to each other, and the box body 14 is sealed with the second cover plate 15 by welding or the like to fix an open end, and at the other open end, the distribution plate 13 and the first cover plate are sequentially disposed from the inside of the box body from the inside to the outside. 12.
  • the distribution plate 13 includes a flat portion 138 and a first recess 133 and a second recess 134 recessed downward from the flat portion 138, so that the other side of the distribution plate 13 is formed with two projections.
  • the first groove 133 has an inner wall and an outer wall
  • the second groove 134 also has an inner wall and an outer wall.
  • the first groove 133 and the second groove 134 are spaced apart from each other and disposed adjacent to each other, and the flat portion 138 includes a partition portion 139 and the surrounding fitting portion 1380, the portion of the partition portion 139 between the first recess 133 and the second recess 134 facing the first cover 12 is flush with the portion of the mating portion 1380 facing the first cover 12, and the flat portion
  • the flatness of 138 is less than 0.1 mm
  • the partition 139 may further have a recess, such that the partition separated between the first recess 133 and the second recess 134 is divided into two parts which are flush with the flat portion. Make the separation between the two more reliable.
  • the open end edges of the first recess 133 and the second recess 134 are spaced apart from the edge of the distribution plate 133 such that the circumference of the planar portion 138 of the distribution plate 13 has a certain width to form the mating portion 1380, respectively, and The width of the surrounding fitting portion 1380 is greater than the wall thickness of the box body 14.
  • the inner wall of the first groove 133 may have a certain inclination such that the area at the opening of the first groove 133 is larger than the area of the bottom surface, and the cross-sectional area of the first groove 133 gradually becomes smaller from the opening toward the bottom surface.
  • the inner wall of the second groove 134 may also have a certain inclination such that the area of the opening of the second groove 134 is larger than the area of the bottom surface, and the cross-sectional area of the second groove 134 gradually decreases from the opening to the bottom surface. .
  • One or more distribution holes 131 may be defined in the bottom of the first recess 133, and a first communication hole 135 may be defined in the sidewall of the first recess 133, and the first communication hole 135 is disposed adjacent to the distribution hole 131, and is distributed.
  • the hole 131 can serve as the first hole.
  • the bottom of the second recess 134 is provided with one or more bus holes 132, and a second communication hole 136 is defined in the sidewall of the second recess 134, and the second communication hole 136 is disposed adjacent to the bus hole 132.
  • the flat tube is one.
  • the flat tube includes a plurality of straight portions 165 located opposite to the middle portion, a plurality of first bent portions 161 located opposite to one side, and a plurality of second bends on the other side.
  • the first bent portion 161 is relatively close to the distribution hole 131
  • the second bent portion 166 is relatively close to the collecting hole 132.
  • the distribution hole and the collecting hole are matched or distributed corresponding to the bent portion of the flat tube.
  • the hole and the bus hole correspond to the bent portion of the bent portion and/or the bent portion of the flat tube, or the first bent portion of the flat tube and/or the finless area near the first bent portion
  • the projection in the direction of the distribution plate overlaps at least partially with the distribution hole, and the projection and confluence of the second bent portion of the flat tube on the other side of the heat exchange core and the fin-free region near the second bent portion toward the distribution plate
  • the holes are at least partially overlapped; the plurality of distribution holes 131 are provided to improve the uniform distribution of the fluid, thereby improving the heat exchange performance of the heat exchanger.
  • the first surface and the second surface of the planar portion 138 of the distribution plate 13 are respectively located on a plane, where a plane means that the flatness of the surface is within 0.1 mm.
  • the distribution plate 13 is fixed to the second end of the box main body and the open end of the box main body 14 by welding, screwing or the like, as shown in the present embodiment.
  • the top surface of the box main body 14 facing the distribution plate is provided with an opening, and the fitting portion of the flat portion 138 toward the circumference of the second surface of the box main body abuts against the side wall of the box main body 14 and can pass through
  • the welding or the like is sealed and fixed, and the outer wall of the first recess 133 is kept at a certain distance from the inner wall of the tank main body 14.
  • the heat exchange core body also has fluid flow near the side wall of the tank 1, which can improve the effective heat exchange area of the heat exchanger, thereby improving the performance of the heat exchanger.
  • the width H of the flat tube is equal to or slightly smaller than the distance between the bottom 137 of the two grooves of the distribution plate to the bottom wall of the inside of the case, the distance between the bottom 137 of the groove and the bottom wall of the inside of the case and the flat tube
  • the difference in width H is less than 3 mm.
  • the spacing S1 between the two adjacent distribution holes is smaller than the distance d2 between the two adjacent straight portions, and the length L0 of the distribution plate setting distribution hole area is greater than or equal to the two distances farthest apart.
  • the straight distance L1 is reduced by twice the thickness of the flat tube h: L0 ⁇ L1-2h; further, the length L0 of the distribution plate setting distribution hole area is larger than the distance L1 of the two flat tubes farthest apart, so that the flat tube Any one of the bent portion and the straight portion can directly exchange heat with the fluid, so that the liquid distribution is relatively uniform, and the heat exchange area is also large; in addition, in consideration of assembly and other problems, the distribution plate can be provided with a distribution hole.
  • the length L0 of the region is less than or equal to the distance L1 of the two flat tubes which are farthest apart, and the thickness h of the flat tube is four times: L0 ⁇ L1 + 4h.
  • the length of the distribution plate to set the distribution hole area is the length L0 of the distribution hole, and the length L0 of the distribution hole is greater than or equal to the distance between the two flat tubes which are farthest apart from the flat tube group minus
  • the double flat tube thickness h, or the length of the dispensing hole enables the dispensing hole to cover the inside of the bend of any flat tube or the middle of any adjacent straight portion, plus the arrangement of the first communication hole
  • the outermost space of the flat tube is communicated through the first communication hole, so that any group of adjacent flat tubes can directly communicate with at least one distribution hole, so that the distribution of the fluid meets the needs of the system; Connecting the holes, and setting the length L0 of the distribution plate to the distribution hole area to be greater than the distance L1 of the two flat tubes farthest from each other plus the thickness h of the four times flat tube, so that the space in which the distribution holes communicate can include the flat tube
  • the space inside or outside of any of the bends or that allows the distribution holes to communicate can
  • the dispensing aperture is positioned relatively close to the side of the distribution plate, The position corresponds to the first bent portion of the flat tube and the portion of the first bent portion where the fin is not disposed. Accordingly, the position of the first communication hole is also corresponding to the first bent portion of the flat tube and/or The portion of the first bent portion where the fin is not provided, or the portion of the bent portion of the flat tube and the portion of the bent portion that is not provided with the fin, is at least partially coincident with the distribution hole in the direction of the distribution plate, and The position of the first communication hole is also relatively close to the distribution hole to improve distribution uniformity and heat exchange effect.
  • the first cover 12 is matched with the distribution plate 13, and the first cover 12 partially covers the distribution plate 13.
  • the first surface of the distribution plate 13 facing the first cover 12 is substantially attached to the first cover 12 and fixed by welding.
  • the first groove 133 and the second groove 134 are respectively formed into two first chambers and a second chamber which are isolated from each other.
  • the first cover 12 is provided with a first through hole 121 and a second through hole 122, wherein the first through hole 121 corresponds to the first groove 133, and the second through hole 122 corresponds to the second groove 134.
  • the projection of the first through hole 121 on the bottom surface of the first groove 133 is kept at a certain distance from the distribution hole 131, so that fluid can be prevented from rushing toward the distribution hole 131 when flowing from the first through hole 121 into the first groove 133, thereby causing fluid.
  • the projection of the second through hole 122 on the bottom surface of the second groove 134 is also kept at a certain distance from the bus hole 132.
  • the first through hole 121 cooperates with the first connecting tube 5 and is sealed and fixed.
  • the second through hole 122 is matched with the second connecting tube 4 and is sealed and fixed.
  • the hole of the first connecting tube serves as the first hole
  • the hole of the second connecting tube serves as the first hole.
  • the first cover 12 is further provided with a first slot 123 and a second slot 124 for limiting, and the shape of the slot may be semicircular or substantially U-shaped or the like.
  • the bottom areas of the first groove 133 and the second groove 134 are relatively large, the distribution hole 131 is disposed on the side of the bottom surface of the first groove 133 away from the second groove 134, and the other portions of the bottom surface are not disposed.
  • the bus hole 132 is disposed on a side of the bottom surface of the first groove 133 away from the first groove 133, and no other portion of the bottom surface is provided with a bus hole; the distribution hole 131 and the bus hole 132 are at a position opposite to the distribution plate 13.
  • the fluid has a larger flow path in the heat exchange core, which can ensure a more sufficient heat exchange of the fluid in the heat exchange core.
  • the distribution plate 13 and the first cover 12 are fitted together.
  • the first through hole 121 and the second through hole 122 of the first cover 12 can be disposed in a larger area, and the first through hole can be disposed.
  • the area of the second through hole is larger, and the positions of the first through hole 121 and the second through hole 122 and the distance between the first through hole 121 and the second through hole 122 can be set according to the needs of the system.
  • the heat exchange core is disposed between the distribution plate 13 of the casing 1 and the bottom of the tank main body 14.
  • the heat exchange core body comprises a flat tube 16 and a fin 17 having a substantially serpentine cross section.
  • the flat tube 16 is not limited to one, and may be juxtaposed to each other as shown in FIG. Set the way. If the flat tube 16 is one such that the width of the flat tube 16 is large, the width of the flat tube 16 is substantially equal to or slightly smaller than the distance between the distribution plate 13 and the bottom of the tank main body 14 in order to improve the heat exchange performance of the heat exchanger.
  • the inner passage of the flat tube 16 may be provided as a plurality of mutually parallel passages which form a second fluid passage.
  • the flat tube 16 is bent to form a plurality of straight portions 165 and a plurality of first bent portions 161 and a plurality of second bent portions 166, and the first bent portion 161 and the second bent portion 166 are respectively located in the heat exchange
  • the plurality of straight portions 165 are substantially parallel to each other, and a distance d2 is maintained between the two adjacent straight portions 165, and the value of d2 ranges from 0.5 mm to 6 mm, and most of the fins 17 are located.
  • the fins 17 may be zigzag fins or other forms of fins such as dimple plates, twisted strips, perforated fins, spiral coils, flat fins, and the like.
  • one end of the fin 17 adjacent to the first bent portion 161 may maintain a certain distance d1 from the first bent portion 161, and the value of d1 ranges from 5 mm to 30 mm, so that A portion of one end of the portion 165 near the first bent portion 161 is not provided with fins, and the flow resistance of the fluid in this portion is small, and the fluid may first be along the first bent portion and the flat portion 165 of the portion where the fin is not provided.
  • Flow in the width direction such that fluid in the space between any set of adjacent straight portions can be substantially evenly distributed within the space or along the width of the flat tube, and the fluid is then along the flat portion 165 between adjacent flat tubes.
  • the flow in the longitudinal direction can prevent the problem of large fluid flow near the distribution plate side, improve the uniformity of the distribution of the fluid in the width direction of the flat tube, and thereby improve the heat exchange performance of the heat exchanger.
  • the fins 17 are provided with a composite layer, and the fins 17 and the flat tubes 16 can be fixed together by brazing or the like. Further, the fins 17 and the distribution plate 13 may be fixed by welding, and the fins 17 and the inner wall of the box main body 14 facing the distribution plate 13 may be fixed by welding. In this way, the heat exchange core can be fixed in the casing 1 to improve the stability of the heat exchanger.
  • the first bent portion 161 includes a plurality of circularly connected arcs, and the first bent portion 161 includes a main bent portion 162, a first secondary bent portion 163, and a second secondary bent portion. a portion 164, wherein one end of the first sub-bend portion 163 and the second sub-bend portion 164 on the same side are respectively connected to two adjacent flat portions 165, and the first sub-bend portion 163 and the second sub-bend portion 164 are respectively
  • the main bent portion 162 is located between the first sub-bend portion 163 and the second sub-bend portion 164.
  • the radius of the arc of the main bending portion 162 is R1
  • the radius of the arc of the first sub-bending portion 163 is R2
  • the radius of the arc of the second sub-bending portion 164 is R3, and the value of R2 can be equal to R3, R1 ⁇ d2 ⁇ 2R1.
  • the arc diameter d0 of the main bending portion 162 is larger than the distance d2 between the two adjacent straight portions 165, so that the distance between the two adjacent straight portions 165 can be made small on the one hand, and the flat tube bending can be ensured.
  • the reliability of the processing so that the fins having a small fin height can be used to improve the heat exchange efficiency of the heat exchanger, and on the other hand, the distance d3 between the two adjacent first bent portions 161 can be kept small.
  • the fluid can be smoothly flowed in the region between the two adjacent first bent portions 161, preventing the two adjacent first bent portions 161 from abutting together to block the flow of the fluid, thereby improving the heat exchanger replacement.
  • Thermal performance For the structure of the second bent portion 166, reference may be made to the first bent portion 161.
  • the second bent portion or the first bent portion may also be other structures.
  • the second bent portion includes a plurality of circular arcs connected in a circular manner.
  • the two-folded portion includes a main bending portion and a secondary bending portion, and two ends of the auxiliary bending portion are respectively connected to the main bending portion and the straight portion, and the two ends of the main bending portion are respectively connected with the auxiliary bending portion and the straight portion, respectively.
  • One end of the bent portion connected to the straight portion is tangent to the straight portion, and the arc diameter of the main bent portion is larger than the distance between the two adjacent straight portions.
  • the two adjacent straight portions 165 are formed as fluid flow passages, and the fins disposed between the two adjacent straight portions 165 can increase the spoiler performance of the fluid, thereby improving the heat exchanger. Heat transfer performance.
  • the arc diameter d0 of the main bending portion 162 is greater than the distance d2 between the two adjacent straight portions 165, so that the fluid can be in contact with most of the flat tube or even the entire outer surface, and the fluid in the flat tube 16
  • the fluid outside the flat tube 16 can not only exchange heat through the flat portion 165, but also heat exchange through the bent portion, thereby improving the effective heat exchange area of the flat tube 16, thereby improving the heat exchange performance of the heat exchanger.
  • the heat exchanger further includes a first header 8 and a second header 9 that are in communication with the flow passages in the flat tubes 16, respectively.
  • One end of the flat tube 16 extends through the first fitting hole 152 of the second cover plate 15 into the first header 8, and the flat tube 16 and the first header 8 are sealed and fixed; the other end of the flat tube 16 passes through the first
  • the second fitting hole 151 of the second cover plate 15 extends into the second header 9 and is sealed and fixed between the flat tube 16 and the second header 9.
  • the first mating hole 152 and the flat tube 16 are matched, and the two can be fixed by welding; the second mating hole 151 and the flat tube 16 are matched, and the two can be fixed by welding.
  • the first header 8 and the second header 9 are respectively engaged with the first card slot 123 and the second card slot 124 for limiting, and are also respectively fixed by welding with the first header 8 and the second header 9 respectively.
  • the adapter is fixed and the adapter can be fixed by welding with the first cover.
  • the first header 8 and the second header 9 are welded and fixed to the adapter, and the stability of the heat exchanger can be improved by welding.
  • one end of the first header 8 is sealed by the first end cap 10, and the other end is An adapter 6 is connected, the first adapter 6 is connected and communicated with the third connector 2, and the third connector 2 can communicate with the interior of the first header 8 through the first adapter 6.
  • one end of the second header 9 is sealed by the second end cover 11, the other end is connected to the second adapter 7, the second adapter 7 is connected and communicated with the fourth connector 3, and the fourth connector 3 can pass.
  • the second adapter 7 is in communication with the interior of the second header 9.
  • the refrigerant flows from the third nozzle 2 into the first header 8, and then the refrigerant flows into the flat tube 16 that extends into the first header.
  • the flat tube 16 includes a refrigerant flow path or a plurality of substantially parallel refrigerant flow paths, and the refrigeration The agent flows through the flow path of the flat tube 16 and exchanges heat with the heat exchange fluid in the tank 1, and the heat-exchanged refrigerant flows into the second header 9 and flows out of the heat exchanger through the fourth nozzle 3.
  • the heat exchange fluid flows from the first nozzle 5 into the first groove 133, and the fluid flowing into the first groove 133 flows into the tank 1 through the distribution hole 131 or flows into the tank 1 through the distribution hole 131 and the first communication hole 135, due to the tank At least part of the portion corresponding to the distribution hole and the first communication hole in the body is not provided with fins, so that the fluid can be substantially evenly distributed at the end of the box body, and the first bent portion and the flat tube finless region near the first bent portion are disposed.
  • the portion of the heat exchange fluid first flows along the width direction of the first bent portion and the flat tube near the first bent portion, and then flows along the length of the straight portion 165.
  • the heat exchange fluid can In contact with the outer wall of most of the flat tubes 16, the heat exchange fluid exchanges heat with the refrigerant in the flat tubes 16, and the heat exchange fluid exchanged through the heat exchange fluid flows into the second recesses 134 through the manifold holes 132 or through the manifold holes 132 and The two flow holes 136 flow into the second groove 134, after which the fluid flows out of the heat exchanger through the second header 4.
  • the heat exchange core body is relatively tightly placed in the tank body, and the heat exchange fluid outside the flat tube of the heat exchange core body can effectively utilize most of the flat tubes, thereby improving the heat exchanger.
  • the effective heat exchange area improves the heat transfer performance of the heat exchanger.
  • the heat exchange fluid may flow through the fins 17 along the length direction of the straight portion 165, the flow direction of the heat exchange fluid is the same as or opposite to the flow direction of the refrigerant, and any of the two opposite sides of the flat portion 165
  • the flow direction at the position is parallel or anti-parallel. This arrangement can improve the heat exchange performance between the refrigerant and the heat exchange fluid, and can improve the heat transfer performance of the heat exchanger.
  • the two adjacent bent portions may be dislocated.
  • the adjacent two bent portions are not aligned, Instead, the bends are staggered so that the spacing of adjacent flat tubes can be appropriately reduced.
  • the minimum distance between two adjacent bent portions is greater than the minimum distance between the two adjacent bent portions and the straight portion.
  • the distribution holes are arranged such that there is a distribution hole between the inside of the bent portion of any flat tube or the adjacent straight portion near the bent portion, that is, at least one distribution hole is seen from a plan view.
  • the portion is located between the opposite inner side of the bent portion or the flat portion of the fin-free portion of the flat tube adjacent to the bent portion, and at least one of the distribution holes is located in or near any of the bent portions of the opposite outer side.
  • the distribution holes are arranged to allow the distribution holes between any of the adjacent flat tubes to be connected, that is, at least one of the distribution holes is viewed from a plan view.
  • the outer side of the bent portion outside the inner side or the outer side of the flat portion of the fin-free portion of the bent portion and the outer side of the bent portion on the outer side or the outer side of the flat portion of the fin-free portion of the bent portion.
  • the dashed box in the figure illustrates an embodiment in which the distribution apertures are connected in a substantially wide range.
  • the distribution plate 13 is not provided with a first groove and a second groove, the distribution plate 13 is a flat plate, and the distribution plate 13 is provided with a plate. Or a plurality of distribution holes and one or more manifold holes.
  • the first cover 12 is provided with a first cavity 125 and a second cavity 126 which are open at one end. The open end of the first cavity 125 corresponds to the distribution hole 131, and the open end of the second cavity 126 corresponds to the flow hole. .
  • the first chamber 125 is in communication with the first nozzle 5 and the second chamber 126 is in communication with the second nozzle 4.
  • a side wall of the first cavity 125 is provided with a first interface 127 for connection with the first connector 5, and the opening of the first interface 127 is oriented in the same direction as the juxtaposed arrangement of the respective distribution holes 131.
  • the flow area of the distribution holes near the first interface 127 may be smaller than the flow area away from the distribution holes at the first interface 127, or the flow area of each of the distribution holes may gradually increase in a direction away from the first interface 127. In this way, when the fluid flows from the first interface 127 into the first chamber 125, the flow rate of the region away from the first interface 127 is substantially the same as the flow rate of the region close to the first interface 127, and the heat exchange fluid can be made by providing the distribution holes having different flow areas.
  • the spacing S1 between the two adjacent distribution holes is smaller than the distance d2 between the two adjacent flat tubes, so that both the inside and the outside of any bent portion of the flat tube can directly and at least one
  • the distribution holes are connected to make the distribution of the fluid relatively uniform, and the length L0 of the distribution plate setting distribution hole area is larger than The distance L1 of the two flat tubes which are furthest away from each other plus twice the thickness h of the flat tube, the length of the distribution hole is set such that the distribution hole communicates with the inside of the bent portion of any flat tube and communicates with the outside of the bent portion;
  • the length of the distribution holes is larger than the distance L1 between the two flat tubes which are farthest apart from the flat tube group plus twice the thickness h of the flat tubes, so that the length of the distribution holes enables the distribution holes to Connecting the inside of the bent portion of any flat tube and communicating with the outside of the bent portion or connecting the sides of any flat tube, so that the
  • the length L0 of the distribution plate to set the distribution hole area or the length L0 of the bus hole area is larger than the distance L1 of the two flat tubes farthest from each other minus the thickness of the flat tube h. Further, the length L0 of the distribution plate setting distribution hole or the bus hole area is less than or equal to the distance L1 of the two flat tubes which are farthest apart, and the thickness h of the flat tube is four times: L0 ⁇ L1 + 4h, so that any one can be ensured Fluid flows through both sides of the flat tube for better heat exchange.
  • a sidewall of the second cavity 126 may also be provided with a second interface 128 communicating with the second connector 4, and the first interface 127 is corresponding to the opening of the second interface 128, so that the first interface is convenient for the first interface.
  • FIG. 12 is a schematic view showing still another structure of the distribution plate of the heat exchanger.
  • the dispensing orifices are of the same size so that the fluid can be distributed substantially evenly between adjacent flat tubes. Since the refrigerant flows in from the one end of the flat tube and flows out from the other end, the heat of the flat tube near the inlet end needs to be relatively heat exchanged, and the flat tube near the outlet side needs heat exchange.
  • the distribution hole 131a has a structure in which one end is large and the other end is relatively small, so that the width of the distribution hole relatively close to the inlet side is larger than the width of the distribution hole on the other side, and the distribution hole is wider.
  • One side is placed close to the corresponding side of the refrigerant inlet, which makes the heat exchanger relatively more efficient. It is of course also possible to make the area of the distribution hole relatively close to the inlet side of the flat tube larger than when a plurality of distribution holes are provided. The area of the distribution hole on the other side, and the side where the area of the distribution hole is larger is disposed near the corresponding side of the refrigerant inlet.
  • first cavity and the second cavity are not necessarily located on the same side of the case, or may be located on opposite sides of the case.
  • the bus hole and the second groove are respectively separated from the distribution hole and the first groove. Located on opposite sides of the casing, but the specific structure of the manifold, the second groove, the distribution hole and the first groove, and the relationship with the heat exchange core are the same as or similar to the above embodiment, and are no longer A narrative.
  • the heat exchanger 100' includes a casing and at least a portion thereof is housed in the casing. a heat exchange core body, the heat exchanger is formed with a first fluid passage in the tank body, and a second fluid passage is formed in the heat exchange core body, the first fluid passage is located outside a part of the heat exchange core body, the first fluid passage and the second The fluid channels are isolated from one another.
  • the first fluid in the first fluid passage is, for example, a coolant
  • the second fluid in the second fluid passage is, for example, a refrigerant. At least a portion of the first fluid flows in a direction along the length of the flat tube opposite the flow direction of the other portion of the first fluid along the length of the flat tube.
  • the case includes the case main body 101", the case main body 101" includes the side portion 1011', and the heat exchanger does not require the second cover.
  • the distribution plate 108" may include one or two or more first communication portions 1085", one or two or more second communication portions 1086" and one or two or more third communication portions 1087", first The communication portion 1085", the second communication portion 1086" and the first bending portion are located on a side of the box opposite to the first bending portion, and the third communication portion 1087' and the second bending portion are located at a relatively distant distance from the first body One side of the bent portion; at least three chambers are formed between the cover plate 102" and the distribution plate 108", and the chambers are isolated from each other, and the chamber includes a first chamber 10a", a second chamber 10b" and a The three chambers 10c", the first chamber 10a” is in communication with the first communication portion 1085", the second chamber 10b" is in communication with the second communication portion 1086", and the third chamber 10c" is in communication with the third communication portion 1087'.
  • the first communication portion 1085', the second communication portion 1086', and the third communication portion 1087' can communicate the chamber between the cover plate 102' and the distribution plate 108' with the chamber formed in the box body 101'. Fluid flows between these chambers.
  • the first communication portion 1085' communicates with a portion of the third communication portion 1087' through a portion of the first fluid passage, and the first fluid passage between the further portion of the third communication portion 1087' and the second communication portion 1086' Another part of the connection.
  • the first fluid enters the outer region of the flat tube inside the box through the first communication portion, enters the third chamber 10c' through a portion of the third communication portion, and then enters the other flat inside the box through another portion of the third communication portion 1087'.
  • the outer region of the tube enters the second chamber from the second communication portion, so that the flow path of the first fluid inside the tank body can be lengthened, which helps to improve the heat exchange effect.
  • the first interface 1021' on the cover 102' is located at a corresponding position of the first cavity 10a' and is in communication with the first cavity.
  • the second interface 1022' is located at a corresponding position of the second cavity 10b' and is in communication with the second cavity 10b'.
  • the projection of the first interface 1021' on the distribution plate 108' does not coincide with the first communication portion 1085', and the distance between the projection of the first interface 1021' on the distribution plate 108' and the first communication portion 1085' is not less than 1/8 of the length L' of the first communication portion 1085' in the width direction of the heat exchange core or the distance between the projection of the first interface on the distribution plate and the first communication portion is not less than two or more first communication portions
  • the sum of the lengths of the heat exchange cores in the width direction L' is 1/8; the projection of the second interface 1022' on the distribution plate 108' does not coincide with the second communication portion 1086', and the second interface 1022' is on the distribution plate 108
  • the distance between the upper projection and the second communicating portion 1086' is not less than 1/8 of the length L" of the second communicating portion 1086' along the width direction of the heat exchange core or the projection of the second interface on the distribution plate
  • the distance between the two communicating portions is not less than the length of the two or more
  • the distribution plate 108' includes a flat portion 1081' and a first recess 1082', a second recess 1083', and a third recess 1084' recessed downward from the flat portion 1081', thus enabling distribution
  • the other side of the plate 108' is formed with three projections, or the side of the distribution plate 108' adjacent to the case main body includes a step portion 10813' which is located inside the case main body and is fixed to the inner wall of the case main body.
  • the grooves are spaced apart from each other and disposed adjacent to each other, the first groove 1082', the second groove 1083' are located on one side of the distribution plate 108', and the third groove 1084' is located on the opposite side of the distribution plate 108', the plane
  • the portion 1081' includes a partition portion 10811' and a peripheral edge portion 10812'.
  • the portion of the partition portion 10811' facing the cover plate 102' is flush with the portion of the edge portion 10812' facing the cover plate, and the flatness of the flat portion 1081' is 0.1 mm.
  • the partition 10811' includes a first partition 10811a' and a second partition 10811b'.
  • the first partition 10811a' is located between the first recess 1082' and the second recess 1083', and the second partition 10811b is located at the first partition 10811'.
  • the width of the first partition portion 10811a' is not excessively large and relatively smaller than the width of the second partition portion 10811b', and the first partition portion is along the width direction of the heat exchange core
  • the width may be smaller than the distance d1 between the adjacent flat portions 1093' of the flat tube to prevent the fluid from being blocked by the first partition, resulting in waste of the heat exchange area.
  • the open end edge of the first recess 1082', the second recess 1083', the third recess 1084' is maintained at a distance from the edge of the distribution plate 108' such that the distribution plate 108'
  • the periphery of the flat portion 1081' has a certain width to form an edge portion 10812'.
  • the edge portion 10812' includes a front side and a back side. The front side is fixed to the cover plate, and the reverse side is fixed to the wall portion of the box body 101'.
  • the step portion 10813' projects outwardly a distance greater than the wall thickness of the box body 101'.
  • the edge portion 10812' faces the cover plate 102', and the portion of the partition portion 10811' facing the cover plate 102' is sealed and fixed to the cover plate 102' by welding, and the edge portion 10812' faces away from the cover plate 102' and the box
  • the wall portion of the main body 101' is hermetically fixed by welding.
  • the first communication portion 1085' is located at the first recess 1082' (eg, at the bottom of the first recess 1082'), and the first recess 1082' is formed with the cover as the first cavity 10a'
  • the second communication portion 1086 ′ is located at the second recess 1083 ′ (for example, at the bottom of the second recess 1083 ′), and the second recess 1083 ′ and the cover plate are formed as a second cavity 10 b ′
  • the third communication portion 1087' is located in the third recess 1084' (eg, at the bottom of the third recess 1084'), and the third recess 1084' is formed with the cover plate as a third cavity 10c'.
  • the first communication portion 1085' is substantially aligned with the position of the second communication portion 1086' and is adjacent to one side of the edge portion 10812' of the distribution plate 108', and the third communication portion 1087' is adjacent to the edge portion 10812' of the distribution plate 108'.
  • the distance between the side of the first communicating portion 1085', the adjacent side of the edge portion 10812' of the second communicating portion 1086' and the side of the third communicating portion 1087' adjacent the edge portion 10812' is substantially equal to the flat side
  • the length of the tube 109' is such that the flow path of the fluid in the first fluid passage is large, ensuring a sufficient heat exchange between the fluid in the first fluid passage and the fluid in the second fluid passage.
  • the length L' of the first communication portion 1085' along the width direction of the heat exchange core or the sum L' of the lengths of the two or more first communication portions along the width direction of the heat exchange core is less than or equal to the heat exchange between the second communication portion 1086'
  • the length L" in the width direction of the core or the sum L" of the lengths of the two or more second communicating portions in the width direction of the heat exchange core, the length L"' or both of the third communicating portion 1087' along the width direction of the heat exchange core The sum L"' of the lengths of the plurality of third communicating portions along the width direction of the heat exchange core is larger than the length L" of the second communicating portion 1086' along the width direction of the heat exchange core or the two or more second communicating portions 1086'
  • the second fluid enters from the second header 104' and exits from the first header 103'.
  • the first fluid enters the chamber cavity from the first interface 1021' via the first communication portion 1085' and exits from the second communication portion 1086'. In the inner cavity of the box, as shown in FIG.
  • the first communication portion 1085' is one, and the width of the first communication portion 1085' along the length direction of the flat tube is gradually reduced from the second cavity toward the first cavity, or the first communication portion 1085' is closer to the width of the end portion 1085a' of the second communication portion 1086' than the first communication portion 1085' is relatively far from the end portion 1085b' of the second communication portion 1086'; and/or the third communication portion 1087' is a And the width of the third communication portion 1087' is gradually reduced from the second cavity 10b' toward the first cavity 10a', or the width of both ends of the third communication portion 1087' is different, and the third communication portion 1087' is connected to the second The width of the end portion 1087a' corresponding to the portion 1086' is greater than the width of the end portion 1087b' corresponding to the third communication portion 1087' and the first communication portion 1085'.
  • the direction in which the first fluid moves from the tank main body side to the other side in the width direction of the heat exchange core body and the second fluid in the flat tube from the tank main body side to the other in the width direction of the heat exchange core body The side moves in opposite directions to allow for better heat exchange between the two fluids.
  • the difference in the width of the first communicating portion 1085' allows more of the first fluid to exchange heat with the fluid relatively close to the second fluid inlet side, which is advantageous for improving the heat exchange effect.
  • two or more first communication portions 1085' may be disposed at the first recess 1082' (for example, the bottom), and the projection of each of the first communication portions toward the flat tube is located adjacent to the flat tube.
  • the length of each of the first communication portions 1085' in the width direction of the heat exchange core is substantially equal to the distance d1 between the adjacent straight portions of the flat tubes.
  • the fluid in the first chamber 10a' can be better distributed between the adjacent flat portions to make the fluid distribution more uniform and contribute to the improvement of the heat exchange effect.
  • the projection of each of the first communicating portions toward the flat tube direction only needs to partially fall between the adjacent straight portions.
  • the distribution plate 108' and the cover plate 102' form three chambers, and the first fluid flows in from the first chamber 10a' into the interior of the tank body, and the fluid is reversed after passing through the third chamber 10c', from the second chamber. 10b' flows out and the second fluid channel is two processes.
  • the second fluid passage may also be a three-flow or a four-flow.
  • the distribution plate 108' includes a first communication portion 1085', a second communication portion 1086', and a third communication portion.
  • the distribution plate 108' and the cover plate 102' form four chambers, and the chamber includes a first cavity 10a', a second cavity 10b', a third cavity 10c' and a fourth cavity 10d ', the first cavity 10a' is in communication with the first communication portion 1085', the second cavity 10b' is in communication with the second communication portion 1086', the third cavity 10c' is in communication with the third communication portion 1087', and the fourth cavity 10d' is The fourth communication portion 1089' is in communication with the first communication portion 1085' and The second communication portion 1086' is located on one side of the distribution plate 108', the third communication portion 1087' and the fourth communication portion 1089' are located on the other side of the distribution plate 108', and the first interface 1021' on the cover plate 102' is located The corresponding position of the first cavity 10a', the second interface 1022' on the cover 102' is located at a corresponding position of the fourth cavity 10d'.
  • the first communication portion 1085', the second communication portion 1086' and the first bending portion 1091' are located on one side of the box body, and the third communication portion 1087', the fourth communication portion 1089' and the second bending portion 1092' are located.
  • the side of the box body is relatively away from the first bent portion 1091 ′: the first interface 1021 ′ and the first communication portion 1085 ′ are communicated through the first cavity 10 a ′, and the first communication portion 1085 ′ and the third communication portion 1087 ′′ A portion of the first fluid passage communicates with each other, and a portion of the third communication portion 1087' communicates with a further portion of the third communication portion 1087' through the third chamber 10c', and another portion of the third communication portion 1087' A portion of the second communication portion 1086' communicates with a further portion of the first fluid passage, and a portion of the second communication portion 1086' communicates with a further portion of the second communication portion 1086' through the second chamber 10b'.
  • a further portion of the two communication portions 1086' communicates with the fourth communication portion 1089' through a further portion of the first fluid passage, the fourth communication portion 1089' communicates with the fourth chamber 10d', and the second interface 1022' and the fourth chamber 10d' connectivity.
  • the first communication portion, the second communication portion, the third communication portion, and the fourth communication portion are located at the bottom of the distribution plate 108', and the distribution plate 108' includes a first groove 1082' and a second groove 1083' a third recess 1084' and a seventh recess 1088', the first recess 1082' and the second recess 1083' are located on one side of the distribution plate 108', the third recess 1084' and the seventh recess 1088' Located on the opposite side of the distribution plate 108'.
  • the length of the first communication portion along the width direction of the heat exchange core or the length of the length of the two or more first communication portions along the width direction of the heat exchange core is less than or equal to the length of the second communication portion along the width direction of the heat exchange core or two The sum of the lengths of the plurality of second communicating portions along the width direction of the heat exchange core, the length of the third communicating portion along the width direction of the heat exchange core or the sum of the lengths of the two or more third communicating portions along the width direction of the heat exchange core It is larger than a length of the fourth communication portion in the width direction of the heat exchange core or a length of two or more fourth communication portions along the width direction of the heat exchange core.
  • the second communication portion and the third communication portion have an overlapping portion in the width direction of the heat exchange core
  • the first communication portion and the third communication portion have an overlapping portion in the width direction of the heat exchange core
  • the second communication portion and the The four communicating portions have overlapping portions in the width direction of the heat exchange core.
  • Another portion of the portion enters the interior of the tank body, the fluid reversingly flows through the fin region between the straight portions of the flat tube, and then passes through a portion of the second communication portion into the second chamber 10b', and the fluid in the second chamber 10b' passes through Second communication
  • the other part enters the inside of the box body, and the fluid is again reversed to flow through the fin area between the straight portions of the flat tube, and enters the fourth chamber 10d' from the fourth communication portion, so that the first fluid passage can be called a three-flow process,
  • the first fluid can better exchange heat with the second fluid in the flat tube, and the heat exchange efficiency is improved in the case where the outer shape of the box is small.
  • the distribution plate has a plurality of grooves that cooperate with the cover plate to form a plurality of chambers.
  • the cover plate can also have a plurality of grooves, and the plurality of grooves on the cover plate and the distribution plate form a plurality of chambers.
  • the cover plate 102' includes a second planar portion 1025' and a fourth recess 1026', a fifth recess 1027', and a sixth recess 1028' recessed from the second planar portion 1025'.
  • the fourth groove 1026' forms a first chamber 10a' with the bottom of the distribution plate 108'
  • the fifth groove 1027' forms a second chamber 10b' with the bottom of the distribution plate
  • the sixth groove 1028' forms a bottom portion with the distribution plate.
  • the third chamber 10c'; the second flat portion 1025' and one side of the distribution plate are sealed and fixed as by welding.
  • the space between adjacent flat portions 1093' of the flat tube includes the first communication portion a first region 111' corresponding to the 1085' position, a second region 112' corresponding to the position of the second communication portion 1086', and a third region 113' corresponding to the position of the third communication portion 1087', the first region 111'
  • the end of the fin 110' adjacent to the first region 111' may maintain a certain distance d3 from the first bent portion 1091', and the value of d3 ranges from 5 mm to 30 mm, and the fin 110' is adjacent to the first portion.
  • the distance d3 between the end of the first region 111' and the first bent portion 1091' is greater than the width d4 of the first communicating portion 1085' along the longitudinal direction of the flat tube, and the width d4 is only an example, along the first communicating portion 1085' When the width of the flat tube in the longitudinal direction is different, d4 represents the maximum value.
  • the flat portion 1093' is disposed near the end of the first bent portion 1091' without fins, the flow resistance of the fluid in this portion is small, so the fluid can first follow the first bent portion and the portion.
  • the flat portion 1093' in which the fins are not provided flows in the width direction, so that the fluid in the space between any one of the adjacent flat portions 1093' can be substantially evenly distributed in the space or in the width direction of the flat tube, and then the fluid Flowing from the first bent portion 1091' toward the second bent portion 1092' or the first end portion 1094' or the second end portion 1095' to prevent fluid flow under the distribution plate 108' near the distribution plate 108' side
  • the larger problem is to increase the uniformity of the distribution of the fluid in the width direction of the flat tube, thereby improving the heat transfer performance of the heat exchanger.
  • the portion 113a corresponding to the second region 112' in the longitudinal direction of the flat tube is a finless region, and the end of the fin 110' adjacent to the portion 113a can be combined with the second bent portion.
  • 1092' maintains a certain distance d2, and the value of d2 ranges from 5 mm to 30 mm, so that a part of the third communication portion 1087' enters the third region.
  • the fluid of the portion 113a' flows smoothly in the width direction of the flat tube, so that the fluid enters the space between the straight portions more uniformly, and the uniformity of distribution of the fluid in the width direction of the flat tube is improved, thereby improving the heat transfer performance of the heat exchanger. .
  • the second fluid passage is located in the flat tube and is applicable to a high pressure refrigerant system having a relatively high working pressure.
  • the heat exchanger of the present embodiment can be used for a thermal management system of a vehicle or an air conditioning system of a vehicle.
  • the vehicle includes an electric vehicle or a fuel vehicle or a hybrid vehicle.
  • the fluid in the first fluid passage is a coolant
  • the fluid in the second fluid passage is a fluid.
  • High pressure refrigerants include, but are not limited to, supercritical carbon dioxide, subcritical carbon dioxide, and the like.
  • the heat exchanger includes a housing 7", a first connecting block 2", and a second connection that are open on one side.
  • Block 3 mounting plate 4" and a heat exchange core partially or completely housed in the housing 7"
  • the mounting plate 4" is fixedly mounted to the open side of the housing 7" and covers the opening of the housing, the heat exchange core A first fluid passage is formed.
  • the heat exchange core comprises at least one flat tube 5", the heat exchanger being further provided with a first interface 21" and a second interface 22", the first interface 21" and the second interface 22" being located at the first connection block 2". Both ends of the flat tube 5" are in communication with the first interface 21" and the second interface 22", respectively, such that the first fluid passage communicates with the first interface 21" and the second interface 22", respectively.
  • the housing 7" is also provided with a third interface 71" and a fourth interface 72", a chamber is formed in the housing, the heat exchange core is partially or completely accommodated in the chamber, the third interface and the fourth interface are in communication with the chamber, and the first fluid passage is The chamber is isolated.
  • the second connecting block 3" is provided with a first passage 31" and a second passage 32", and the first passage 31" and the second passage 32" are recessed in the first connection of the second connecting block 3"
  • the block 2" is opposite to the side.
  • the first passage 31" includes a first straight passage 311", a second straight passage 312", and a bend between the first straight passage 311" and the second straight passage 312"
  • the portion 313" and the bubble end 314" located at one end of the second straight channel 312" away from the bent portion 313".
  • the second passage 32" also includes a first straight passage 321", a second straight passage 322", a bent portion 323" between the first straight passage 321” and the second straight passage 322", and
  • the second straight channel 322" is away from the bubble end 324" at one end of the bent portion 323.
  • the second connecting block 3" is further provided with a first receiving socket 33" of the first passage corresponding to the first straight passage 311" of the first passage 31", and a first straight direction with the second passage 32"
  • the flat tube 5" With the clearance fit between the first receiving socket 33", one end of the flat tube 5" can pass through the first receiving socket 33" of the second passage 32", and the other end can pass through the first bearing of the first passage 31"
  • the jack 33", the flat tube 5" and the first receiving socket 33" can be fixedly mounted by welding or the like. At least a portion of the end of the first tube receiving the flat tube into the first passage extends into the first straight passage of the first passage or communicates with the first straight passage of the first passage, and the flat tube extends into the second passage At least a portion of one end of the first socket extends into the first straight passage of the second passage or communicates with the first straight passage of the second passage.
  • the depth of the first receiving socket is greater than or equal to 2 mm. It should be noted here that the gap between the flat tube 5" and the first socket 15" is filled with the solder material which can be melted by welding, thereby sealing between the flat tube 5" and the first socket 33". installation.
  • the inner diameter or equivalent inner diameter of the bubble ends 314", 324 is greater than the width of the second straight passages 312", 322, and the bubble end 314" of the first passage 31" is opposite the first interface 21", the first passage
  • the inner diameter or equivalent inner diameter of the bubble end 314" of 31" is substantially greater than or equal to the inner diameter or equivalent inner diameter of the portion of the bubble end 314" of the first interface 21" adjacent the first passage 31", the bubble of the second passage 32"
  • the end portion 324" is opposite the second interface 22", and the inner diameter or equivalent inner diameter of the bubble end 324" of the second passage 32" is substantially greater than or equal to the bubble end of the second interface 22" adjacent the second passage 32"
  • the inner diameter or equivalent inner diameter of the portion 324" which can effectively reduce the flow of fluid from the first interface 21" to the second straight passage 312" of the first passage 31" and from the second straight direction of the second passage 32"
  • the local sag resistance generated by the passage 322" to the second interface 22" effectively reduces the fluid pressure drop
  • the fluid first flows through the bent portion 323" and the first receiving socket 33" to the second interface 22", so that the flow resistance when the fluid flows from the respective small fluid passages of the flat tube 5" to the second passage 32" is substantially the same.
  • the problem of uneven distribution of fluid in the various small fluid passages of the flat tube 5" is reduced, thereby improving the heat exchange performance of the heat exchanger.
  • first interface 21" is disposed opposite to the bubble end 314" of the first channel 31
  • second interface 22 is disposed opposite to the bubble end 324" of the second channel 32" so that the flexible interface can be flexibly
  • the position of an interface 21" and the second interface 22" sets the first channel 31" and the second channel 32", thereby enabling the heat exchanger to be adapted to more complex installation environments.
  • the mounting plate 4" is provided with a second receiving socket 42" penetrating the mounting plate 4", and a clearance fit between the flat tube 5" and the second receiving socket 42", the flat tube 5"
  • the end portion can pass through the second receiving socket 42", and the flat tube 5" and the second receiving socket 42" can be fixedly mounted by welding, etc.
  • the mounting plate 4" and the second connecting block 3" can be welded or the like.
  • the first receiving socket 33" is opposite to the second receiving socket 42", and the flat tube 5" sequentially passes through the second receiving socket 42" and the first receiving socket 33".
  • the depth of the second socket 42" is greater than or equal to 2 mm.
  • the mounting plate 4" covers the open side of the housing 7", and in order to improve the sealing performance, a sealing member 8" is provided between the mounting plate 4" and the housing 7", in the case of the mounting plate 4" and the housing 7"
  • the contact portion is provided with a seal recess 41" and a screw hole 46" for mounting the seal, and the mounting plate 4" can be fixedly mounted to the housing 7" by screws.
  • the mounting plate 4" is also provided with a mounting for mounting the heat exchanger. Hole 47".
  • the connecting block also has the function of a mounting plate, in which case the connecting block is also provided with a seal groove and a screw hole, and in this embodiment, it is not necessary to provide a second receiving socket.
  • the mounting plate can also be disposed at other positions of the housing or fixed to other parts of the housing to serve the purpose of fixing the heat exchanger.
  • the first interface 21" and the second interface 22" of the first connection block 2" penetrate the first connection block 2", and the first interface 21" and the second interface 22" are stepped holes. It includes a small diameter portion near the side of the second connecting block 3" and a large diameter portion away from the side of the second connecting block 3".
  • the first interface 21" includes a large diameter portion 211" and a small diameter portion 212", wherein the small diameter portion 212" is opposite to the bubble end portion 314" of the first passage 31", and the inner diameter of the small diameter portion 212"
  • the equivalent inner diameter is substantially the same as or the same as the inner diameter or the equivalent inner diameter of the bubble end 314" of the first passage 31".
  • first passage 31" and the second passage 32" may also be disposed at the first connecting block 2 One side of the contact with the second connecting block 3", in the present embodiment, by the combination of the first connecting block 2", the second connecting block 3" and the mounting plate 4", on the one hand each part
  • the processing steps are relatively small, the processing is easy, and on the other hand, the material can be reduced (for example, the thickness of the mounting plate can be relatively relatively Small), thereby reducing costs.
  • both ends pass through the first receiving socket 33" and the second receiving socket 42" and then extend into the first passage 31" and the second passage 32", thereby making the first interface 21 "Connected to the second interface 22" through the first fluid passage.
  • the housing 7" includes an outer casing 701" and a partition 702", wherein the outer casing 701" and the partition 702" may both be integrally molded or integrally cast, according to the first fluid passage.
  • the fluid property and the application environment are selected to be integrally processed.
  • the partition member 702" is disposed in the outer casing 701", and the first cavity 73" is formed in the casing 7", The two chambers 74" and the third chambers 75", wherein the first chamber 73" is in communication with the third port 71", and the second chamber 74" is in communication with the fourth port 72".
  • the partition 702" includes a first partition wall 77 a first wall portion 732" and a second wall portion 742", wherein the first partition wall 77" is disposed between the first cavity 73" and the second cavity 74", the first cavity 73" and the second cavity 74 There is no direct connection between the two. Also, one end of the second chamber 74" is open, and one end of the third chamber 75" is open, and the opening of the second chamber 74" is oriented toward the opening of the third chamber 75".
  • the first wall portion 732" is disposed between the first cavity 73" and the third cavity 75", and the second wall portion 742" is disposed between the second cavity 74" and the third cavity 75".
  • the first wall portion 732" opposite to the third interface 71" is provided with a first communication hole 731", and the first cavity 73" communicates with the third cavity 75" through the first communication hole 731", with the fourth interface
  • the 72" opposing second wall portion 742" is provided with a second communication hole 741", and the second cavity 74" communicates with the third cavity 75" through the second communication hole 741".
  • the projection of the third interface 71" at the first wall portion 732" does not interfere with the first communication hole 731
  • the projection of the fourth interface 72" at the second wall portion 742” does not interfere with the second communication hole 741".
  • the projection of the first fin-free region 511" at the first wall portion 732" partially overlaps or completely coincides with the first communication hole 731
  • the projection of the fin 6" at the first wall portion 732" and the first communication hole 731" are not coincide.
  • the projection of the second fin-free region 512" at the second wall portion 742" partially overlaps or completely coincides with the second communication hole 741
  • the projection of the fin 6" at the second wall portion 742" and the second communication hole 741" are not coincide.
  • the first communication hole 731 includes a plurality of small communication holes having a small diameter, and each of the small communication holes is opposite to the at least one first flow area 513", that is, each of the first flow areas 513" is in the first wall portion.
  • the projection of 732" is located in a small communication hole.
  • the second communication hole 741" may also be provided with a plurality of small communication holes having a small diameter.
  • An extension portion 76" is provided on the opening side of the housing 7", and the extension portion 76" is provided with a plurality of screw holes 761", and the screw holes 761" of the extension portion cooperate with the screw holes 46" of the mounting holes, and the housing 7
  • the "and mounting plate 6" is fixedly mounted by screws 9" and is sealed by the seal 8".
  • FIGS. 28 and 29 it can also be arranged as shown in FIGS. 28 and 29, so that the flow direction of at least a portion of the first fluid along the length of the flat tube is opposite to the flow direction of the other portion of the first fluid along the length of the flat tube.
  • FIGS. 28 and 29 it can also be arranged as shown in FIGS. 28 and 29, so that the flow direction of at least a portion of the first fluid along the length of the flat tube is opposite to the flow direction of the other portion of the first fluid along the length of the flat tube.

Landscapes

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

Abstract

一种换热器,包括箱体(1)和换热芯体,箱体(1)内形成有第一流体通道,换热芯体内形成有第二流体通道,换热芯体包括扁管(16),第二流体通道位于扁管(16)内,扁管(16)包括多个折弯部(161、166)和多个平直部(165),两相邻平直部(165)之间保持一定距离;箱体(16)开设有与第一接管(5)连通的第一孔和与第二接管(4)连通的第二孔,第一孔与扁管(16)一侧的折弯部(161、166)或者靠近折弯部(161、166)的平直部(165)部分相对应,第二孔与扁管(16)另一侧的折弯部(161、166)或者靠近折弯部(161、166)的平直部(165)部分相对应。

Description

一种换热器
本申请要求下列发明专利申请的优先权,其全部内容通过引用结合在本申请中:
(1)2015年12月09日提交中国专利局、申请号为201510905980.4、发明名称为“一种换热器”的发明专利申请。
(2)2015年12月09日提交中国专利局、申请号为201510906370.6、发明名称为“一种换热器”的发明专利申请。
(3)2015年12月09日提交中国专利局、申请号为201510906354.7、发明名称为“一种换热器”的发明专利申请。
(4)2016年03月31日提交中国专利局、申请号为201610196914.9、发明名称为“换热器及车辆热管理系统”的发明专利申请。
(5)2016年03月31日提交中国专利局、申请号为201610201002.6、发明名称为“换热器及车辆空调系统”的发明专利申请。
(6)2016年03月31日提交中国专利局、申请号为201610201884.6、发明名称为“换热器及CO2冷却系统”的发明专利申请。
(7)2016年03月31日提交中国专利局、申请号为201610196745.9、发明名称为“换热器及车辆热管理系统”的发明专利申请。
(8)2016年08月03日提交中国专利局、申请号为201610634384.1、发明名称为“热交换装置”的发明专利申请。
(9)2016年08月03日提交中国专利局、申请号为201610629325.5、发明名称为“热交换装置”的发明专利申请。
技术领域
本发明涉及热交换技术领域,如涉及一种车辆热交换技术。
背景技术
CO2是一种新型的环保型制冷工质,可以减少全球温室效应,从根本上解决化合物对环境的污染问题,具有良好的经济性和实用性。以CO2为工质的压缩式制冷循环系统可以运用于大多数的制冷/制热领域。
但CO2制冷系统工作压力高,在设计CO2换热器时需充分考虑该类系统的这一特点,其部件设计仍不成熟导致该类系统并未大量应用。一般来说CO2换热器主要有管翅式、微通道、板式、管壳式、板翅式和套管式等。其中板式和板翅式制造工艺复杂,管翅式、套管式和管壳式管子壁厚需要较厚,浪费材料。
而传统的CO2微通道换热器是采用制冷剂和空气强制对流的方式换热,效率较低。虽然液体和空气物性差异较大,液-气方式换热具有较高的换热效率,但现有技术中的液-气换热器存在壁厚较厚,而且换热性能也较差的问题。
因此,如何提供一种适用于相对高压的制冷剂系统、且具有较好的换热性能的换热器是目前急需解决的技术问题。
发明内容
为了解决现有技术中存在的上述技术问题,本发明提供了一种换热器,能够有效的解决上述技术问题。
本发明提供一种换热器,包括箱体以及容纳于所述箱体内的换热芯体,所述箱体内形成有第一流体通道,所述换热芯体内形成有第二流体通道,所述换热芯体外部为所述第一流体通道的一部分,所述第一流体通道与第二流体通道相互隔离,所述换热芯体包括一个或者二个以上扁管,所述第二流体通道位于所述扁管内,所述扁管包括多个第一折弯部、多个第二折弯部和多个平直部,所述第一折弯部和第二折弯部分别位于所述换热芯体相对两侧,两相邻所述平直部大致平行且保持0.5mm~6mm的距离且;
所述箱体开设有与外部连通的第一孔和第二孔,所述第一折弯部和/或平直部靠近所述第一折弯部部分向与所述第一孔相对应的所述箱体的内壁方向的投影与所述第一孔或所述第一孔向所述第一孔相对应的所述箱体的内壁方向的投影至少部分重,所述第二折弯部和/或平直部靠近所述第二折弯部部分向与所述第二孔相对应的所述箱体的内壁方向的投影与所述第二孔或所述第二孔向所述第二孔相对应的所述箱体的内壁方向的投影至少部分重。
上述技术方案的换热器,可以使换热流体与绝大部分的扁管外壁接触,能够提高换热器的有效换热面积,并且换热流体的流动方向与制冷剂的流动方向大致相同或者相反,并且两者相对平直部位置处的流动方向大致平行或反向平行,能够提高制冷剂与换热流体之间的换热性能,能够有效提高换热器的换热性能。
附图说明
图1是本发明换热器的一实施例的立体示意图;
图2是图1所示换热器的爆炸示意图;
图3是图1所示换热器的B-B剖面示意图;
图4是图1所示换热器的扁管与翅片组合体的A-A剖面示意图;
图5是图4的局部放大示意图;
图6是图4所示扁管在折弯处的局部结构示意图;
图7是相邻折弯部错位设置的扁管结构示意图;
图8是图1所示换热器的分配板的结构示意图;
图9是图1所示换热器的第一盖板的结构示意图;
图10是本发明换热器的另一实施例的立体示意图;
图11是图10所示实施例的第一盖板和分配板的爆炸示意图;
图12是换热器的分配板的又一结构示意图;
图13是换热器的多个并排设置扁管的换热芯体结构示意图;
图14是本发明又一实施例的换热器的爆炸示意图;
图15是图14所示换热器的一种分配板的示意图;
图16是图14所示换热器的另一种分配板的示意图;
图17是图14所示换热器的又一种分配板的示意图;
图18图14所示换热器的箱主体内部扁管与翅片的示意图;其中,虚线大致描绘了例示区,并不对其形状有所限制;
图19是图14所示换热器的盖板的一种实施方式的仰视示意图;
图20是本发明换热器的一种实施方式的爆炸结构示意图;
图21是图20所示换热器的第二连接块的结构示意图;
图22是图20所示换热器的安装板的结构示意图;
图23是图20所示换热器的第一安装板和第二安装板结合时的透视示意图;
图24是图23的A-A剖视示意图;
图25是图20所示换热器的壳体的剖视示意图;
图26是图20所示换热器的在第三接口和第四接口部位的剖视示意图;
图27是图20所示换热器在第一腔和第二腔部位的剖视示意图;
图28是本发明换热器的又一实施方式的爆炸结构示意图;
图29是图28所示换热器的剖视示意图。
具体实施方式
下面结合附图对本发明的具体实施方式进行说明。
图1是本发明换热器的一实施例的立体示意图,图2是图1所示换热器的爆炸示意图,如图所示,在本实施例中,换热器包括箱体1以及容纳于箱体1内的换热芯体,箱体内形成有第一流体通道,换热芯体内形成有第二流体通道,换热芯体外部为第一流体通道的一部分,且第一流体通道与第二流体通道相互隔离,与第一流体通道连通的第一接管5和第二接管4与箱体1固定设置。这里应当指出,本领域技术人员可以理解,换热芯体外部的空间包括扁管与扁管之间的空间、扁管与翅片之间的空间、以及翅片中的空间等空间。
箱体1包括箱主体14、第一盖板12、分配板13和第二盖板15,箱主体14为一具有两个面开设有开口端的近似长方体或者正方体,箱主体14的两开口端所在的两个面相邻设置,箱主体14通过焊接等方式与第二盖板15密封固定一开口端,在另一开口端从箱主体由内到外依次设置有分配板13和第一盖板12。
如图8所示,分配板13包括平面部138和从平面部138向下凹进的第一凹槽133和第二凹槽134,可以使分配板13的另一侧形成有两凸起,从而使第一凹槽133具有内壁和外壁,第二凹槽134也具有内壁和外壁。第一凹槽133和第二凹槽134相互隔离且相邻设置,平面部138包括隔离部 139和四周的配合部1380,第一凹槽133和第二凹槽134之间的隔离部139朝向第一盖板12的部位与配合部1380朝向第一盖板12的部位齐平,平面部138的平面度在0.1mm以内,另外隔离部139还可以具有一个凹部,这样第一凹槽133和第二凹槽134之间分隔的隔离部就分成两部分与平面部齐平的隔离区域,使两者之间分隔更加可靠。第一凹槽133和第二凹槽134的开口端边缘与分配板133的边缘之间保持一定的距离,从而使分配板13的平面部138的四周分别具有一定的宽度形成配合部1380,并且四周的配合部1380的宽度大于箱主体14的壁厚。第一凹槽133的内壁可以具有一定的斜度,从而使第一凹槽133的开口处的面积大于底面的面积,并且第一凹槽133的横截面积从开口处向底面逐渐变小。第二凹槽134的内壁也可以具有一定的斜度,从而使第二凹槽134的开口处的面积大于底面的面积,并且第二凹槽134的横截面积从开口处向底面逐渐变小。
第一凹槽133的底部可以开设有一个或者多个分配孔131,还可以在第一凹槽133的侧壁开设有第一连通孔135,并且第一连通孔135靠近分配孔131设置,分配孔131可以作为第一孔。第二凹槽134的底部设置有一个或者多个汇流孔132,还可以在第二凹槽134的侧壁开设有第二连通孔136,并且第二连通孔136靠近汇流孔132设置,汇流孔可以作为第二孔。本实施例中扁管为一根,扁管包括相对位于中部的多个平直部165、相对位于一侧的多个第一折弯部161、及位于另一侧的多个第二折弯部166,第一折弯部161相对靠近分配孔131,第二折弯部166相对靠近汇流孔132;在换热器上,分配孔和汇流孔与扁管的折弯部相对应配合或者分配孔和汇流孔与靠近折弯部的无翅片区相对应配合和/或扁管的折弯部,或者说扁管的第一折弯部和/或靠近第一折弯部的无翅片区向分配板方向的投影与分配孔至少有部分重合,换热芯体的另一侧的扁管的第二折弯部及靠近该第二折弯部的无翅片区向分配板方向的投影与汇流孔至少有部分重合;设置多个分配孔131可以提高流体的均匀分布,从而提高换热器的换热性能。
分配板13的平面部138的第一面、第二面分别位于一平面,这里一平面是指表面的平面度在0.1mm以内。分配板13朝向箱主体的第二面与箱主体14的该开口端通过焊接、螺钉等方式密封固定,如图所示,在本实施 例中,箱主体14的朝向分配板的如图示的顶面呈开口设置,平面部138朝向箱主体的第二面的四周的配合部部分与箱主体14的侧壁相靠接并可以通过焊接等方式密封固定,并且第一凹槽133的外壁与箱主体14的内壁之间保持一定的距离。由于第一凹槽133的内壁具有一定的斜度,所以一部分流体可以较为顺畅的从第一凹槽133内穿过第一连通孔135流入箱主体14内。同样的,第二凹槽134的外壁与箱主体14的内壁之间保持一定的距离。由于第二凹槽134的内壁具有一定的斜度,所以一部分流体可以较为顺畅的从箱主体14内穿过第二连通孔136流入第二凹槽134内。这样可以使换热芯体靠近箱体1的侧壁处也具有流体流动,可以提高换热器的有效换热面积,从而提高换热器性能。
扁管的宽度H等于或略小于分配板的两个凹槽的底部137到箱体内部的底壁之间的距离,凹槽的底部137到箱体内部的底壁之间的距离与扁管的宽度H之差小于3mm。在分配孔为多个的情况下,两相邻分配孔之间的间距S1小于两相邻平直部之间间距d2,且分配板设置分配孔区域的长度L0大于等于相距最远的两平直部的距离L1减去两倍的扁管厚度h:L0≥L1-2h;进一步,分配板设置分配孔区域的长度L0大于相距最远的两个扁管的的距离L1,这样在扁管的任一折弯部和平直部的内部及外部均能直接流体进行热交换,使液体的分配相对均匀,换热面积也较大;另外,考虑到装配等问题,可以使分配板设置分配孔区域的长度L0小于等于相距最远的两个扁管的的距离L1再加上四倍扁管的厚度h:L0≤L1+4h。在分配孔为一个的情况下,分配板设置分配孔区域的长度即为分配孔的长度L0,分配孔的长度L0大于等于扁管组的相隔最远的两个扁管之间的距离减去两倍的扁管厚度h,或者说分配孔的长度使分配孔能够覆盖任一扁管的折弯部内部或者说任一相邻平直部的中间,再加上第一连通孔的设置使扁管最外端的空间通过第一连通孔连通,这样使任一组相邻扁管之间均能直接与至少一分配孔连通,使流体的分配满足系统的需要;另外也可以不设置第一连通孔,并使分配板设置分配孔区域的长度L0大于相距最远的两个扁管的的距离L1再加上四倍扁管的厚度h,这样使分配孔连通的空间能够包括扁管的任一折弯部内部及外部或者说使分配孔连通的空间能够包括任一组相邻平直部之间。相应地,分配孔设置的位置相对靠近分配板的一侧, 其位置对应于扁管的第一折弯部及靠近第一折弯部的没有设置翅片的部位,相应地,第一连通孔设置的位置也对应于扁管的第一折弯部和或靠近第一折弯部的没有设置翅片的部位,或者说,扁管的折弯部和或靠近折弯部的没有设置翅片的部位向分配板方向的投影与分配孔至少部分重合,而第一连通孔设置的位置也相对靠近分配孔,以提高分配均匀性及换热效果。
第一盖板12与分配板13相配合,第一盖板12部分覆盖分配板13,分配板13朝向第一盖板12的第一面与第一盖板12基本贴合并通过焊接相固定,使第一凹槽133与第二凹槽134分别形成两相互隔离的第一腔和第二腔。第一盖板12设有第一通孔121和第二通孔122,其中第一通孔121与第一凹槽133相对应,第二通孔122与第二凹槽134相对应。并且第一通孔121在第一凹槽133的底面上的投影与分配孔131保持一定距离,这样可以防止流体从第一通孔121流入第一凹槽133内时冲向分配孔131导致流体分配不均的问题。第二通孔122在第二凹槽134的底面上的投影也与汇流孔132保持一定距离。第一通孔121与第一接管5相配合且密封固定,第二通孔122与第二接管4相配合且密封固定,这里第一接管的孔作为第一孔,第二接管的孔作为第二孔。第一盖板12还设置有用于限位的第一卡槽123和第二卡槽124,卡槽的形状可以是半圆形或大致U形等。
而且,第一凹槽133和第二凹槽134的底面积相对较大,分配孔131设置于第一凹槽133的底面远离第二凹槽134的一侧,底面的其它部分则没有设置分配孔;同样,汇流孔132设置于第一凹槽133的底面远离第一凹槽133的一侧,底面的其它部分也没有设置汇流孔;分配孔131与汇流孔132在分配板13的相对位置较远,使流体在换热芯体中流动路径较大,可以保证流体在换热芯体中的较为充分的换热。而且,分配板13和第一盖板12配合安装,由于存在上述结构特征,第一盖板12的第一通孔121和第二通孔122可以设置的区域较大,可以设置第一通孔和第二通孔的区域较大,可以根据系统的需要来设定第一通孔121和第二通孔122的位置和第一通孔121和第二通孔122之间的距离。
如图2至图6所示,换热芯体设置在箱体1的分配板13与箱主体14底部之间部位。换热芯体包括一截面大致呈蛇状的扁管16和翅片17,这里应当指出,扁管16不限于一根,也可以是如图13所示多根相互并列设 置的方式。如果扁管16是一根,这样扁管16的宽度较大,为了提高换热器的换热性能,扁管16的宽度大致等于或者略小于分配板13与箱主体14底部之间的距离。扁管16内通道可以设置为多个相互平行的通道,该通道即形成第二流体通道。
扁管16经过折弯形成有多个平直部165和多个第一折弯部161及多个第二折弯部166,第一折弯部161和第二折弯部166分别位于换热芯体的相对两侧,多个平直部165大致相互平行,且两相邻平直部165之间保持一定距离d2,d2的取值范围为0.5mm~6mm,翅片17的大部分位于两相邻平直部165之间的空间。翅片17可以为锯齿形翅片,也可以是其他形式的翅片,例如酒窝(dimple)板、扭带、打孔翅片、螺旋线圈、平直翅片等。在与分配孔131相对应部分,翅片17靠近第一折弯部161的一端可以与第一折弯部161保持一定的距离d1,d1的取值范围为5mm~30mm,这样,由于平直部165靠近第一折弯部161的一端的一部分没有设置翅片,流体在这一部分的流动阻力小,流体可以先沿着第一折弯部及该部分未设置翅片的平直部165的宽度方向流动,使任一组相邻平直部之间的空间的流体在该空间内或沿扁管的宽度方向可以大致均匀分布,流体再沿着相邻扁管之间的平直部165的长度方向流动,可以防止出现靠近分配板侧流体流量较大的问题,提高流体在扁管宽度方向的分配均匀度,从而提高换热器的换热性能。
翅片17上设置有复合层,翅片17和扁管16可以通过钎焊等方式固定在一起。并且翅片17与分配板13之间也可以通过焊接固定,翅片17与箱主体14的与分配板13相对的内壁也可以通过焊接固定。这样,可以使换热芯体固定于箱体1内,提高换热器的稳定性。
如图所示,从俯视方向看,第一折弯部161包括多段圆滑连接的圆弧,第一折弯部161包括主折弯部162、第一副折弯部163和第二副折弯部164,其中第一副折弯部163和第二副折弯部164位于同一侧的一端分别连接两相邻平直部165,第一副折弯部163和第二副折弯部164分别与主折弯部162的两端连接,主折弯部162位于第一副折弯部163和第二副折弯部164之间。主折弯部162的圆弧半径为R1,第一副折弯部163的圆弧半径为R2,第二副折弯部164的圆弧半径为R3,R2的值可以等于R3,R1<d2<2R1。 主折弯部162的圆弧直径d0大于两相邻平直部165之间的距离d2,这样,一方面可以使两相邻平直部165之间的距离较小又能够保证扁管折弯加工的可靠性,从而可以采用翅片高度较小的翅片,提高换热器的换热效率,另一方面,也可以使两相邻第一折弯部161之间的距离d3保持较小,可以使流体能够在两相邻第一折弯部161之间的区域较为顺畅的流动,防止两相邻第一折弯部161抵靠在一起阻塞流体的流动,从而提高换热器的换热性能。第二折弯部166的结构可参照第一折弯部161,当然第二折弯部或者第一折弯部也可以是其它结构,例如第二折弯部包括多段圆滑连接的圆弧,第二折弯部包括主折弯部和副折弯部,副折弯部的两端分别连接主折弯部和平直部,主折弯部的两端分别连接副折弯部和平直部,主折弯部与平直部相连的一端与平直部相切,主折弯部的圆弧直径大于两相邻平直部之间的距离。
这样,在换热器中,两相邻平直部165之间形成为流体流动通道,两相邻平直部165之间设置的翅片可以增加流体的扰流性能,从而提高换热器的换热性能。并且主折弯部162的圆弧直径d0大于两相邻平直部165之间的距离d2,可以使流体能够与扁管的绝大部分区域甚至接近全部外表面接触,扁管16内的流体与扁管16外的流体不仅可以通过平直部165进行热交换,还可以通过折弯部进行热交换,提高了扁管16的有效换热面积,从而提高了换热器的换热性能。
如图所示,换热器还包括分别与扁管16内的流道相连通的第一集管8和第二集管9。扁管16的一端穿过第二盖板15的第一配合孔152伸入第一集管8内,扁管16与第一集管8之间密封固定;扁管16的另一端穿过第二盖板15的第二配合孔151伸入第二集管9内,扁管16与第二集管9之间密封固定。第一配合孔152和扁管16相配合,两者可以通过焊接密封固定;第二配合孔151和扁管16相配合,两者可以通过焊接密封固定。第一集管8和第二集管9分别卡设于第一卡槽123和第二卡槽124来进行限位,另外也通过与第一集管8和第二集管9分别焊接固定的转接座而固定,转接座可以通过与第一盖板焊接固定,第一集管8和第二集管9通过与转接座焊接固定,通过焊接固定可以提高换热器的稳定性。
在本实施例中,第一集管8的一端通过第一端盖10密封,另一端与第 一转接座6连接,第一转接座6与第三接管2连接并连通,第三接管2可以通过第一转接座6与第一集管8的内腔连通。同样的,第二集管9的一端通过第二端盖11密封,另一端与第二转接座7连接,第二转接座7与第四接管3连接并连通,第四接管3可以通过第二转接座7与第二集管9的内腔连通。通过设置转接座,可以方便设置不同规格、内径、外径的接管,使换热器与系统的配合方便。
下面示出本实施例的换热器的工作方式。
制冷剂从第三接管2流入第一集管8,之后制冷剂流入伸入第一集管的扁管16,扁管16包括一条制冷剂流道或多条大致平行的制冷剂流道,制冷剂通过扁管16的流道流动并与箱体1内的换热流体进行热交换,经过热交换的制冷剂再流入第二集管9,并通过第四接管3流出换热器。
换热流体从第一接管5流入第一凹槽133,流入第一凹槽133的流体通过分配孔131流入箱体1或通过分配孔131和第一连通孔135流入箱体1,由于在箱体内对应分配孔与第一连通孔的部位至少有部分没有设置翅片,这样流体可以基本均匀地分布于箱体这端设置第一折弯部及靠近第一折弯部的扁管无翅片区的部位,大部分换热流体先沿着第一折弯部及靠近第一折弯部的扁管的宽度方向流动,再沿着平直部165的长度方向流动,此时,换热流体可以与大部分的扁管16的外壁接触,换热流体与扁管16内的制冷剂进行热交换,经过热交换的换热流体通过汇流孔132流入第二凹槽134或通过汇流孔132和第二流通孔136流入第二凹槽134,之后流体通过第二集管4流出换热器。在本实施例中,换热芯体被相对密闭地置于箱体内,换热芯体的扁管外为换热流体,可以较为有效的利用绝大部分的扁管,从而提高换热器的有效换热面积,提高换热器的换热性能。并且,换热流体可以沿着平直部165的长度方向穿过翅片17流动,换热流体的流动方向与制冷剂的流动方向相同或者相反,且两者相对平直部165的任一相对位置处的流动方向平行或反向平行,这种设置方式可以提高制冷剂与换热流体之间的换热性能,可以提高换热器的换热性能。
为了进一步的减小两相邻扁管的平直部之间的距离,同时又保证两相邻折弯部之间不发生干涉,如图7所示,还可以使两相邻折弯部错位设置,其中扁管的位于箱体一侧的多个折弯部中,相邻的两个折弯部没有对齐, 而是使折弯部错开,这样可以使相邻扁管的间距适当减小。且两相邻折弯部之间的最小距离大于两相邻折弯部与平直部之间的最小距离。相应地,分配孔的设置是使任一扁管的折弯部内部或靠近折弯部的相邻的平直部之间有分配孔能够直接连通,即从俯视方向看,至少有一分配孔的局部是位于相对内侧的折弯部内或靠近该折弯部的扁管的无翅片区的平直部之间,至少有一分配孔的局部是位于相对外侧的任一折弯部内或靠近该折弯部的扁管的无翅片区的平直部之间;分配孔的设置是使任一组相邻扁管之间均有分配孔能够连通,即从俯视方向看,至少有一分配孔的局部是位于相对内侧的折弯部外侧或靠近该折弯部的无翅片区的平直部的外侧及相对外侧的折弯部外侧或靠近该折弯部的无翅片区的平直部外侧。图中的虚线框示意出了分配孔连通大致范围的一种实施方式。
图10和图11示出了本发明的另一实施例,在本实施例中,分配板13没有设置第一凹槽和第二凹槽,分配板13为一平板,分配板13设置有一个或者多个分配孔和一个或者多个汇流孔。相对应的,第一盖板12设置有一端开口的第一腔125和第二腔126,第一腔125的开口端与分配孔131相对应,第二腔126的开口端与汇流孔相对应。第一腔125与第一接管5连通,第二腔126与第二接管4连通。在本实施例中,第一腔125的一侧壁设有用于与第一接管5连接的第一接口127,第一接口127的开口朝向与各分配孔131的并列排列方向相同。并且,靠近第一接口127处分配孔的流通面积可小于远离第一接口127处分配孔的流通面积,或者,在远离第一接口127的方向上,各分配孔的流通面积逐渐增大。这样,流体从第一接口127流入第一腔125时,使远离第一接口127的区域流量与靠近第一接口127的区域流量大致相同,通过设置流通面积不同的分配孔,可以使换热流体较为均匀的流入箱体一侧,并进而相对均匀地流经换热芯体,从而提高换热器的换热性能;而且这种方式可以防止产生流体直接冲击分配孔导致的流体分配不均的问题。另外,也可以使分配孔大小相同,但使分配流量相对较大的一侧靠近扁管的进口侧设置,这样换热效果相对较好。在分配孔为多个的情况下,两相邻分配孔之间的间距S1小于两相邻的扁管的间距d2,这样在扁管的任一折弯部内部及外部均能直接与至少一分配孔连通,使流体的分配相对均匀,且分配板设置分配孔区域的长度L0大于 相距最远的两个扁管的的间距L1再加上两倍扁管的厚度h,设置分配孔的长度能使分配孔连通任一扁管的折弯部内部并连通折弯部外部;在分配孔为一个的情况下,分配孔的长度大于扁管组的相隔最远的两个扁管之间的间距L1再加上两倍扁管的厚度h,使分配孔的长度使分配孔能够连通任一扁管的折弯部内部并连通折弯部外部或者说连通任一扁管两侧,这样使扁管的任一折弯部内部及外部均能直接与至少一分配孔连通,使流体的分配适应系统需要;同样地,汇流孔的设置也是类似,汇流孔可以是一个,汇流孔的长度大于扁管组的相隔最远的两个扁管之间的间距L1再加上两倍扁管的厚度h,其长度使其能连通任一扁管的折弯部内部并连通折弯部外部;汇流孔也可以是多个。在分配板设置有第一连通孔的情况下,分配板设置分配孔区域的长度L0或汇流孔区域的长度L0大于相距最远的两个扁管的的间距L1减去两倍扁管的厚度h。进一步,分配板设置分配孔或汇流孔区域的长度L0小于等于相距最远的两个扁管的的间距L1再加上四倍扁管的厚度h:L0≤L1+4h,这样可以确保任一扁管两侧均有流体流过从而可以进行较好地热交换。
在本实施例中,第二腔126的一侧壁也可以开设有与第二接管4连通的第二接口128,并且第一接口127与第二接口128的开口朝向相对应,这样便于第一接管和第二接管的安装。
这里应当指出,在本实施例中也可以不设置分配板,而是在第一腔的对向箱体的壁部设置分配孔及汇流孔即可。本实施例的其它结构和工作方式与上述实施例相同或者相近似,这里不再一一赘述。图12是换热器的分配板的又一结构示意图。上面的实施例中分配孔大小相同,使流体大致可以均匀分配到各相邻扁管之间。而由于制冷剂是从扁管的一端流进,并从另一端流出,这样靠近进口一端的扁管需要进行热交换的热量会相对比较多,而靠近出口一侧的扁管需要进行热交换的热量会相对比较少,因此使换热流体也按需要进行分配,这样换热效果相对会较好。如图所示,使分配孔131a呈一端较大、而另一端相对较小的结构,使相对靠近进口侧的分配孔的宽度大于另一侧的分配孔的宽度,并使分配孔较宽的一侧靠近制冷剂进口对应的一侧设置,这样可以使换热器效率相对更好。当然也可以在设置有多个分配孔的情况下,使相对靠近扁管进口侧的分配孔的面积大于 另一侧的分配孔的面积,并使分配孔面积较大的一侧靠近制冷剂进口对应的一侧设置。
这里应当指出,第一腔和第二腔不一定位于箱体的同一侧面,也可以是位于箱体的两相对侧面,此时,汇流孔和第二凹槽与分配孔和第一凹槽分别位于箱体两相对的侧面,但汇流孔、第二凹槽、分配孔和第一凹槽的具体结构以及与换热芯体之间的关系与上述实施例相同或者相近似,这里不再一一赘述。
图14至图19示出了本发明换热器的又一实施例,如图14和图15所示,在本实施方式中,换热器100’包括箱体以及至少一部分收容于箱体内的换热芯体,换热器在箱体内形成有第一流体通道,换热芯体内形成有第二流体通道,第一流体通道位于换热芯体的一部分的外部,第一流体通道和第二流体通道相互隔离。第一流体通道内第一流体例如为冷却液,第二流体通道内第二流体例如为制冷剂。至少一部分第一流体沿扁管长度方向的流动方向与其它部分第一流体沿扁管长度方向的流动方向相反。
区别于上述实施例,箱体包括箱主体101”,箱主体101”包括侧部1011’,换热器无需第二盖板。
如图16所示,分配板108”可以包括一个或两个以上第一连通部1085”、一个或两个以上第二连通部1086”和一个或两个以上第三连通部1087”,第一连通部1085”、第二连通部1086”和第一折弯部位于箱体相对邻近第一折弯部的一侧,第三连通部1087’和第二折弯部位于箱体相对远离第一折弯部的一侧;盖板102”与分配板108”之间形成有至少三个腔室,各腔室之间相互隔离,腔室包括第一腔10a”、第二腔10b”和第三腔10c”,第一腔10a”与第一连通部1085”连通,第二腔10b”与第二连通部1086”连通,第三腔10c”与第三连通部1087’连通。第一连通部1085’、第二连通部1086’、第三连通部1087’可以使盖板102’与分配板108’之间的腔室与形成于箱主体101’内的腔室相通,供流体在这些腔室间流动。第一连通部1085’与第三连通部1087’的一部分之间通过第一流体通道的一部分相连通,第三连通部1087’的又一部分与第二连通部1086’之间通过第一流体通道的又一部分连通。第一流体经第一连通部进入箱体内部的扁管外部区域,再经第三连通部的一部分进入第三腔10c’,然后通过第三连通部1087’的另一部分进入箱体内部其他扁 管的外部区域,再从第二连通部进入第二腔,如此第一流体在箱主体内部的流动路径可加长,有助于提高换热效果。
盖板102’上的第一接口1021’位于第一腔10a’对应位置,且与第一腔连通,第二接口1022’位于第二腔10b’对应位置,且与第二腔10b’连通,第一接口1021’在分配板108’上的投影与第一连通部1085’不重合,且第一接口1021’在分配板108’上的投影与第一连通部1085’之间的距离不小于第一连通部1085’沿换热芯体宽度方向的长度L’的1/8或第一接口在分配板上的投影与第一连通部之间的距离不小于两个以上第一连通部沿换热芯体宽度方向的长度之和L’的1/8;第二接口1022’在分配板108’上的投影与第二连通部1086’不重合,且第二接口1022’在分配板108’上的投影与第二连通部1086’之间的距离不小于第二连通部1086’沿换热芯体宽度方向的长度L”的1/8或第二接口在分配板上的投影与第二连通部之间的距离不小于两个以上第二连通部沿换热芯体宽度方向的长度之和L’的1/8。如此,自第一接口1021’进入的第一流体可相对较好的分配至第一连通部1085’,防止流体集中在少数通道中流动,影响换热性能。
在本实施例中,分配板108’包括平面部1081’和从平面部1081’向下凹进的第一凹槽1082’、第二凹槽1083’和第三凹槽1084’,如此使分配板108’的另一侧形成有三个凸起,或者说分配板108’邻近箱主体的一侧包括有台阶部10813’,台阶部10813’位于箱主体内部并与箱主体内壁固定。各凹槽相互隔离且相邻设置,第一凹槽1082’、第二凹槽1083’位于分配板108’的一侧,第三凹槽1084’位于分配板108’的相对另一侧,平面部1081’包括隔离部10811’和四周的边缘部10812’,隔离部10811’朝向盖板102’的部位与边缘部10812’朝向盖板的部位齐平,平面部1081’的平面度在0.1mm以内。隔离部10811’包括第一隔离部10811a’和第二隔离部10811b’,第一隔离部10811a’位于第一凹槽1082’与第二凹槽1083’之间,第二隔离部10811b’位于第三凹槽与第一凹槽、第二凹槽之间,第一隔离部10811a’的宽度不要过大且相对小于第二隔离部10811b’的宽度,第一隔离部沿换热芯体宽度方向的宽度可以小于扁管相邻平直部1093’之间的距离d1,避免流体受第一隔离部阻挡,造成换热面积的浪费。第一凹槽1082’、第二凹槽1083’、第三凹槽1084’的开口端边缘与分配板108’的边缘之间保持一定的距离,从而使分配板108’ 的平面部1081’的四周具有一定的宽度形成边缘部10812’,边缘部10812’包括正面侧和反面侧,正面侧与盖板固定,反面侧与箱主体101’壁部固定,且反面侧自台阶部10813’向外伸出的距离大于箱主体101’的壁厚。边缘部10812’面向盖板102’的部位,隔离部10811’面向盖板102’的部位均与盖板102’如通过焊接方式密封固定,边缘部10812’背向盖板102’的部位与箱主体101’的壁部如通过焊接方式密封固定。
如图15所示,第一连通部1085’位于第一凹槽1082’(例如位于第一凹槽1082’的底部),第一凹槽1082’与盖板之间形成为第一腔10a’,第二连通部1086’位于第二凹槽1083’(例如位于第二凹槽1083’的底部),第二凹槽1083’与盖板之间形成为第二腔10b’,第三连通部1087’位于第三凹槽1084’(例如位于第三凹槽1084’的底部),第三凹槽1084’与盖板之间形成为第三腔10c’。第一连通部1085’与第二连通部1086’的位置大致相对齐,且靠近分配板108’的边缘部10812’的一侧,第三连通部1087’靠近分配板108’的边缘部10812’的相对另一侧,第一连通部1085’、第二连通部1086’的邻近边缘部10812’的一侧与第三连通部1087’邻近边缘部10812’的一侧之间的距离大致等于扁管109’的长度,如此可使第一流体通道内流体的流动路径较大,保证第一流体通道内流体与第二流体通道内流体的较充分的换热。第一连通部1085’沿换热芯体宽度方向的长度L’或两个以上第一连通部沿换热芯体宽度方向的长度之和L’小于或等于第二连通部1086’沿换热芯体宽度方向的长度L”或两个以上第二连通部沿换热芯体宽度方向的长度之和L”,第三连通部1087’沿换热芯体宽度方向的长度L”’或两个以上第三连通部沿换热芯体宽度方向的长度之和L”’大于第二连通部1086’沿换热芯体宽度方向的长度L”或两个以上第二连通部1086’沿换热芯体宽度方向的长度L”之和,第三连通部1087’沿换热芯体宽度方向的长度L”’或两个以上第三连通部沿换热芯体宽度方向的长度之和L”’大于第一连通部1085’沿换热芯体宽度方向的长度L’或两个以上第一连通部1085’沿换热芯体宽度方向的长度L’之和,并且第三连通部1087’沿换热芯体宽度方向的长度L”’或两个以上第三连通部沿换热芯体宽度方向的长度之和L”’可以等于或略小于相距最远的翅片之间的距离L3,如此,可使刚进入换热器的第一流体经第一连通部1085’分配至更多的扁管的平直部之间,相邻扁管的平直部间的流体流速增大, 使第一流体与第二流体的换热更充分,更有利于提高换热效果。
第二流体从第二集管104’进,从第一集管103’出,第一流体从第一接口1021’经第一连通部1085’进入箱体内腔,从第二连通部1086’离开箱体内腔,如图3所示第一连通部1085’为一个,且第一连通部1085’沿扁管长度方向的宽度自第二腔向着第一腔的方向逐渐缩小,或者第一连通部1085’靠近第二连通部1086’的端部1085a’的宽度大于第一连通部1085’相对远离第二连通部1086’的端部1085b’的宽度;和/或第三连通部1087’为一个,且第三连通部1087’的宽度自第二腔10b’向着第一腔10a’的方向逐渐缩小,或者第三连通部1087’的两端宽度不同,第三连通部1087’与第二连通部1086’对应的端部1087a’的宽度大于第三连通部1087’与第一连通部1085’对应的端部1087b’的宽度。如此,在箱主体内部,第一流体沿换热芯体宽度方向自箱主体一侧向另一侧移动的方向与扁管内第二流体沿换热芯体宽度方向自箱主体一侧向另一侧移动的方向相反,以使两种流体更好地进行热交换。而第一连通部1085’宽度设置的不同可使更多的第一流体与相对靠近第二流体进入侧的流体进行换热,有利于提高换热效果。
如图16所示,也可以设置成两个以上第一连通部1085’位于第一凹槽1082’(例如底部),各第一连通部朝着扁管方向的投影位于扁管相邻的平直部之间,各第一连通部1085’沿换热芯体宽度方向的长度大致等于扁管的相邻平直部之间的距离d1。如此第一腔10a’内流体可较好地分配入相邻平直部之间,使流体分配更为均匀,有助于换热效果的提高。当然,各第一连通部朝着扁管方向的投影只需部分落于相邻的平直部之间即可。
上述实施方式中分配板108’与盖板102’形成三个腔室,第一流体从第一腔10a’流入,进入箱主体内部,经第三腔10c’后流体换向,自第二腔10b’流出,第二流体通道为两流程。
除此以外,第二流体通道还可为三流程或四流程,举个例子,如图17所示,分配板108’包括第一连通部1085’、第二连通部1086’、第三连通部1087’和第四连通部1089’,分配板108’与盖板102’形成四个腔室,腔室包括第一腔10a’、第二腔10b’、第三腔10c’和第四腔10d’,第一腔10a’与第一连通部1085’连通,第二腔10b’与第二连通部1086’连通,第三腔10c’与第三连通部1087’连通,第四腔10d’与第四连通部1089’连通,第一连通部1085’和 第二连通部1086’位于分配板108’的一侧,第三连通部1087’和第四连通部1089’位于分配板108’的另一侧,盖板102’上的第一接口1021’位于第一腔10a’的对应位置,盖板102’上的第二接口1022’位于第四腔10d’的对应位置。第一连通部1085’、第二连通部1086’与第一折弯部1091’位于箱主体的一侧,第三连通部1087’、第四连通部1089’与第二折弯部1092’位于箱主体相对远离第一折弯部1091’的一侧:第一接口1021’与第一连通部1085’之间通过第一腔10a’连通,第一连通部1085’与第三连通部1087’的一部分之间通过第一流体通道的一部分连通,第三连通部1087’的一部分与第三连通部1087’的又一部分之间通过第三腔10c’连通,第三连通部1087’的又一部分与第二连通部1086’的一部分之间通过第一流体通道的又一部分连通,第二连通部1086’的一部分与第二连通部1086’的又一部分之间通过第二腔10b’连通,第二连通部1086’的又一部分与第四连通部1089’之间通过第一流体通道的再一部分连通,第四连通部1089’与第四腔10d’连通,第二接口1022’与第四腔10d’连通。
更为具体的,第一连通部、第二连通部、第三连通部、第四连通部位于分配板108’的底部,分配板108’包括第一凹槽1082’、第二凹槽1083’、第三凹槽1084’和第七凹槽1088’,第一凹槽1082’和第二凹槽1083’位于分配板108’的一侧,第三凹槽1084’和第七凹槽1088’位于分配板108’的相对另一侧。第一连通部沿换热芯体宽度方向的长度或两个以上第一连通部沿换热芯体宽度方向的长度之和小于或等于第二连通部沿换热芯体宽度方向的长度或两个以上第二连通部沿换热芯体宽度方向的长度之和,第三连通部沿换热芯体宽度方向的长度或两个以上第三连通部沿换热芯体宽度方向的长度之和大于第四连通部沿换热芯体宽度方向的长度或两个以上第四连通部沿换热芯体宽度方向的长度之和。第二连通部和第三连通部在换热芯体宽度方向上有交叠部,第一连通部和第三连通部在换热芯体宽度方向上有交叠部,第二连通部和第四连通部在换热芯体宽度方向上有交叠部。如此,第一腔的第一流体经第一连通部进入箱主体内部,沿着扁管的平直部之间的翅片区,从第三连通部的一部分进入第三腔,再从第三连通部的另一部分进入箱主体内部,流体换向流过扁管的平直部之间的翅片区,再经第二连通部的一部分进入第二腔10b’,第二腔10b’中流体再通过第二连通部的 另一部分进入箱主体内部,流体再次换向流过扁管的平直部之间的翅片区,从第四连通部进入第四腔10d’,如此第一流体通道可以称之为三流程,这样第一流体可以更好地与扁管内的第二流体进行热交换,在箱体外形结构较小的情况下,提高换热效率。
以上实施方式示出分配板具有多个凹槽,多个凹槽与盖板配合形成多个腔室。当然,盖板也可具有多个凹槽,盖板上的多个凹槽与分配板形成多个腔室。例如,如图19所示,盖板102’包括第二平面部1025’和自第二平面部1025’凹进的第四凹槽1026’、第五凹槽1027’、第六凹槽1028’,第四凹槽1026’与分配板108’底部形成第一腔室10a’,第五凹槽1027’与分配板底部形成第二腔室10b’,第六凹槽1028’与分配板底部形成第三腔室10c’;第二平面部1025’和分配板的一侧如通过焊接方式密封固定。
为了使第一流体从分配板与盖板之间的腔室能更好地分配至扁管表面,参照图18,扁管的相邻平直部1093’之间的空间包括与第一连通部1085’位置相对应的第一区111’,与第二连通部1086’位置相对应的第二区112’以及与第三连通部1087’位置对应的第三区113’,第一区111’为无翅片区,翅片110’邻近第一区111’的端部可以与第一折弯部1091’保持一定的距离d3,d3的取值范围为5mm~30mm,且翅片110’邻近第一区111’的端部与第一折弯部1091’之间的距离d3大于第一连通部1085’沿扁管长度方向的宽度d4,宽度d4仅为例示,在第一连通部1085’沿扁管长度方向的宽度不同时,d4代表最大值。这样,由于平直部1093’靠近第一折弯部1091’的一端的这部分无翅片布置,流体在这一部分的流动阻力较小,因此流体可以先沿着第一折弯部及该部分未设置翅片的平直部1093’的宽度方向流动,使任一组相邻平直部1093’之间的空间的流体在该空间内或沿扁管的宽度方向可以大致均匀分布,接着流体再自第一折弯部1091’向着第二折弯部1092’或第一端部1094’或第二端部1095’的方向流动,以防止分配板108’下方靠近分配板108’侧流体流量较大的问题,提高流体在扁管宽度方向的分配均匀度,从而提高换热器的换热性能。同理,在第三区113’位置,在扁管长度方向与第二区112’相对应的部分113a为无翅片区,翅片110’邻近该部分113a的端部可以与第二折弯部1092’保持一定的距离d2,d2的取值范围为5mm~30mm,以使自第三连通部1087’的一部分进入第三区的该部 分113a’的流体顺畅地在扁管宽度方向流动,使流体更均匀地进入各平直部之间的空间,提高流体在扁管宽度方向的分配均匀度,从而提高换热器的换热性能。
本实施例中,第二流体通道位于扁管内,可适用于工作压力相对较高的高压制冷剂系统。本实施例的换热器可用于车辆的热管理系统或车辆的空调系统,车辆包括电动车或燃油汽车或混合动力汽车,例如,第一流体通道内流体为冷却液,第二流体通道内流体为高压制冷剂,包括(但不限于)超临界二氧化碳、亚临界二氧化碳等。
本实施例的其它结构和特征与上述实施例相同或者相近似,这里不再一一赘述。
图20至图29示出了本发明的又一实施例,如图所示,在本实施例中,换热器包括一侧开口的壳体7”、第一连接块2”、第二连接块3”、安装板4”以及部分或者全部容纳于壳体7”内的换热芯体,安装板4”与壳体7”的开口侧固定安装且覆盖壳体的开口,换热芯体内形成有第一流体通道。
换热芯体包括至少一个扁管5”,换热器还设置有第一接口21”和第二接口22”,第一接口21”和第二接口22”位于第一连接块2”。扁管5”的两端分别与第一接口21”和第二接口22”连通,从而使第一流体通道分别与第一接口21”和第二接口22”连通。壳体7”还设置有第三接口71”和第四接口72”,壳体内形成有腔室,换热芯体部分或者全部容纳于腔室,第三接口和第四接口与腔室连通,且第一流体通道与所述腔室隔离。
如图21所示,第二连接块3”设置有第一通道31”和第二通道32”,第一通道31”和第二通道32”凹陷于第二连接块3”的与第一连接块2”相对一侧面。第一通道31”包括第一直向通道311”、第二直向通道312”、位于第一直向通道311”和第二直向通道312”之间的弯折部313”、以及位于第二直向通道312”远离弯折部313”一端的泡状端部314”。第二通道32”也包括第一直向通道321”、第二直向通道322”、位于第一直向通道321”和第二直向通道322”之间的弯折部323”、以及位于第二直向通道322”远离折弯部323的一端的泡状端部324”。第二连接块3”还设置有与第一通道31”的第一直向通道311”相对应的第一通道的第一承插孔33”、以及与第二通道32”的第一直向通道321”相对应的第二通道的第一承插孔33”。扁管5” 与第一承插孔33”之间间隙配合,扁管5”的一端可穿过第二通道32”的第一承插孔33”,另一端可穿过第一通道31”的第一承插孔33”,扁管5”与第一承插孔33”之间可以通过焊接等方式固定安装。扁管伸入第一通道的第一承插孔的一端至少一部分伸入第一通道的第一直向通道或者与第一通道的第一直向通道相连通,扁管伸入第二通道的第一承插孔的一端至少一部分伸入第二通道的第一直向通道或者与第二通道的第一直向通道相连通。为了保证扁管5”与第一承插孔33”之间的安装稳定性,第一承插孔的深度大于等于2mm。这里应当说明,扁管5”与第一承插孔33”之间的间隙在通过焊接时可以被溶化的焊接材料所填充,从而使扁管5”与第一承插孔33”之间密封安装。
泡状端部314”、324的内径或者当量内径大于第二直向通道312”、322的宽度,并且第一通道31”的泡状端部314”与第一接口21”相对,第一通道31”的泡状端部314”的内径或者当量内径大致大于或等于第一接口21”靠近第一通道31”的泡状端部314”部分的内径或者当量内径,第二通道32”的泡状端部324”与第二接口22”相对,第二通道32”的泡状端部324”的内径或者当量内径大致大于或等于第二接口22”靠近第二通道32”的泡状端部324”部分的内径或者当量内径,这样可以有效的减小流体从第一接口21”流向第一通道31”的第二直向通道312”时、以及从第二通道32”的第二直向通道322”流向第二接口22”时产生的局部突缩阻力,有效的减小流体压降损失。
通过在第一通道31设置设置第二直向通道312”和弯折部313”,并且使第一通道31”的弯折部313”与第一通道31”的第一承插孔33”保持距离,这样流体从第一接口21”流入后依次经过第二直向通道312”和弯折部313”流入扁管5”内的细小流体通道内,使流体从第一接口21”流入时不直接冲向扁管5”,能够减小流体在扁管5”的各细小流体通道内分配不均的问题,从而提高换热器的换热性能。
同样,通过在第二通道32”设置第二直向通道322”和弯折部32,并且使第二通道32”的弯折部323”与第二通道32”的第一承插孔33”保持距离。这样流体先通过弯折部323”和第一承插孔33”再流向第二接口22”,使流体从扁管5”的各细小流体通道流向第二通道32”时的流阻大致相同,能够 减小流体在扁管5”的各细小流体通道内分配不均的问题,从而提高换热器的换热性能。
并且,第一接口21”与第一通道31”的泡状端部314”相对设置,第二接口22”与第二通道32”的泡状端部324”相对设置,这样能够灵活的根据第一接口21”和第二接口22”的位置来设置第一通道31”和第二通道32”,从而使换热器能够适用更多复杂的安装环境。
如图20和图22所示,安装板4”设置有贯穿安装板4”的第二承插孔42”,扁管5”与第二承插孔42”之间间隙配合,扁管5”的端部可以穿过第二承插孔42”,扁管5”与第二承插孔42”可以通过焊接等方式固定安装。安装板4”与第二连接块3”可以通过焊接等方式密封固定。第一承插孔33”与第二承插孔42”相对,扁管5”依次穿过第二承插孔42”和第一承插孔33”。同样的,第二承插孔42”的深度大于等于2mm。
安装板4”覆盖壳体7”的开口侧,为了提高密封性能,在安装板4”和壳体7”之间还设置有密封件8”,在安装板4”的与壳体7”相接触部分设置有用于安装密封件的密封件凹槽41”和螺钉孔46”,安装板4”可以通过螺钉与壳体7”固定安装。安装板4”还设置有用于安装换热器的安装孔47”。
即连接块还具有安装板的功能,此时连接块也设置有密封件凹槽和螺钉孔,在这实施例中,无需设置第二承插孔。当然,安装板还可以设置于壳体的其它位置或者安装固定于壳体的其它部位,以起到固定换热器的目的。
如图23和图24所示,第一连接块2”的第一接口21”和第二接口22”贯穿第一连接块2”,并且第一接口21”和第二接口22”为阶梯孔,包括靠近第二连接块3”侧的小径部和远离第二连接块3”侧的大径部。如图24所示,第一接口21”包括大径部211”和小径部212”,其中小径部212”与第一通道31”的泡状端部314”相对,且小径部212”的内径或者当量内径与第一通道31”的泡状端部314”的内径或者当量内径大致相同或者相同。这里应当指出,第一通道31”和第二通道32”也可以设置在第一连接块2”的与第二连接块3”相接触的一侧部,在本实施例中,通过第一连接块2”、第二连接块3”和安装板4”的组合方式,一方面每个零件上的加工工序相对较少,加工容易,另一方面也能够减少材料(如安装板的厚度可以相对较 小),从而减省成本。
本实施例中,通过在第一连接块和/或第二连接块中设置密封的通道,不仅通道的耐压性能高,在高压下不易变形,而且结构简单,加工方便,成本较低。
扁管经过若干次折弯后,两端部穿过第一承插孔33”和第二承插孔42”后伸入第一通道31”和第二通道32”,从而使第一接口21”通过第一流体通道与第二接口22”连通。
在本实施例中,壳体7”包括外壳体701”和分隔件702”,其中外壳体701”和分隔件702”都可以为整体注塑件或者整体铸造件,可以根据第一流体通道中的流体性质以及应用环境来选择何种材料一体加工而成。如图25至图27所示,分隔件702”设置于外壳体701”内,壳体7”内形成有第一腔73”、第二腔74”和第三腔75”,其中第一腔73”与第三接口71”相连通,第二腔74”与第四接口72”相连通。分隔件702”包括第一分隔壁77”、第一壁部732”和第二壁部742”,其中,第一分隔壁77”设置于第一腔73”和第二腔74”之间,第一腔73”和第二腔74”之间不直接连通。并且,第二腔74”的一端开口设置,第三腔75”的一端开口设置,第二腔74”的开口朝向与第三腔75”的开口朝向相同。
第一壁部732”设置于第一腔73”和第三腔75”之间,第二壁部742”设置于第二腔74”和第三腔75”之间。在与第三接口71”相对的第一壁部732”设置有第一连通孔731”,第一腔73”通过第一连通孔731”与第三腔75”相连通,在与第四接口72”相对的第二壁部742”设置有第二连通孔741”,第二腔74”通过第二连通孔741”与第三腔75”相连通。
第三接口71”在第一壁部732”的投影与第一连通孔731”相互不干涉,第四接口72”在第二壁部742”的投影与第二连通孔741”相互不干涉。第一无翅片区511”在第一壁部732”的投影与第一连通孔731”部分重合或者完全重合,翅片6”在第一壁部732”的投影与第一连通孔731”不重合。第二无翅片区512”在第二壁部742”的投影与第二连通孔741”部分重合或者完全重合,翅片6”在第二壁部742”的投影与第二连通孔741”不重合。
并且,第一连通孔731包括包括若干通径较小的小连通孔,且各小连通孔与至少一个第一通流区513”相对,即各第一通流区513”在第一壁部 732”的投影位于一小连通孔。这样,如图27的箭头所示,当第三接口71”作为第一流体的进口时,第一流体从第三接口71”流入第一腔73”后,经过各小连通孔能够较为均匀的流入各第一通流区513”,穿过翅片6”和第二通流区514”后流入第二腔74”,并通过第四接口72”流出换热器,这种设置方式有利于提高换热器的换热性能。
当然,第二连通孔741”也可以设置有若干通径较小的小连通孔。
在壳体7”的开口侧开设置有外延部76”,外延部76”设置有多个螺钉孔761”,外延部的螺钉孔761”与安装孔的螺钉孔46”相配合,壳体7”和安装板6”通过螺钉9”固定安装,并通过密封件8”实现密封固定。
当然,也可以如图28和图29所示那样设置,从而实现至少一部分第一流体沿扁管长度方向的流动方向与其它部分第一流体沿扁管长度方向的流动方向相反。具体可以参见图14至图19所示实施例,这里不再一一赘述。
以上所述,仅是本发明的具体实施例而已,并非对本发明作任何形式上的限制。虽然本发明已以较佳实施例揭露如上,然而并非用以限定本发明。任何熟悉本领域的技术人员,在不脱离本发明技术方案范围情况下,都可利用上述揭示技术内容对本发明技术方案做出许多可能的变动和修饰,或修改为等同变化的等效实施例。因此,凡是未脱离本发明技术方案的内容,依据本发明的技术实质对以上实施例所做的任何简单修改、等同变化及修饰,均仍属于本发明技术方案保护的范围内。

Claims (14)

  1. 一种换热器,包括箱体以及容纳于所述箱体内的换热芯体,所述箱体内形成有第一流体通道,所述换热芯体内形成有第二流体通道,所述第一流体通道与第二流体通道相互隔离,所述换热芯体包括一个或者二个以上扁管,所述第二流体通道位于所述扁管内,所述扁管包括至少一个第一折弯部、至少一个第二折弯部和多个平直部,所述第一折弯部和第二折弯部分别位于所述换热芯体相对两侧,两相邻所述平直部大致平行且保持0.5mm~6mm的距离且;
    所述箱体开设有与所述第一折弯部附近的空间连通的开口,所述第一折弯部和/或平直部靠近所述第一折弯部部分向与所述箱体开设的与所述第一折弯部附近的空间连通的开口相对应的所述箱体的内壁方向的投影与所述箱体与所述第一折弯部连通的开口至少部分重合,所述箱体开设有与所述第二折弯部连通的开口,所述第二折弯部和/或平直部靠近所述第二折弯部部分向与所述箱体开设的与所述第二折弯部连通的开口相对应的所述箱体的内壁方向的投影与所述箱体与所述第二折弯部连通的开口至少部分重合。
  2. 根据权利要求1所述的换热器,其特征在于,所述箱体开设有与外部连通的第一孔和第二孔,所述第一孔为所述箱体开设的与所述第一折弯部附近的空间连通的开口,所述第一折弯部和/或平直部靠近所述第一折弯部部分向与所述第一孔相对应的所述箱体的内壁方向的投影与所述第一孔或所述第一孔在所述箱体的开口至少部分重合,所述第二孔为所述箱体开设的与所述第二折弯部附近的空间连通的开口,所述第二折弯部和/或平直部靠近所述第二折弯部部分向与所述第二孔相对应的所述箱体的内壁方向的投影与所述第二孔或所述第二孔在所述箱体的开口至少部分重合。
  3. 根据权利要求2所述的换热器,其特征在于,两相邻第一折弯部或者两相邻第二折弯部之间的最小距离大于零;所述第一折弯部包括多段圆滑连接的圆弧,所述第一折弯部包括主折弯部、第一副折弯部和第二副折弯部,所述第一副折弯部和第二副折弯部位于同一侧的一端分别连接两相邻平直部,所述第一副折弯部和第二副折弯部分别与所述主折弯部连接,所述主折弯部位于所述第一副折弯部和第二副折弯部之间,并且所述主折 弯部的圆弧半径R1和两相邻平直部之间的距离d2满足:R1<d2<2R1。
  4. 根据权利要求2所述的换热器,其特征在于,所述第一折弯部包括主折弯部和副折弯部,所述副折弯部的两端分别连接所述主折弯部和平直部,所述主折弯部的两端分别连接所述第一副折弯部和平直部,所述主折弯部与所述平直部相连的一端与所述平直部相切,所述主折弯部的圆弧直径大于两相邻平直部之间的距离。
  5. 根据权利要求1至4任一项所述的换热器,其特征在于,所述扁管的两相邻所述平直部之间设置有翅片,所述翅片和扁管固定,所述翅片的与所述箱体内壁接触部分与所述箱体内壁固定,所述翅片靠近所述第一折弯部的一端与所述第一折弯部保持5mm至30mm的距离,所述平直部靠近所述第一折弯部的一端的至少一部分没有设置所述翅片,所述平直部没有设置翅片部分向与所述第一孔相对应的所述箱体的内壁方向的投影与所述第一孔至少部分重合。
  6. 根据权利要求5所述的换热器,其特征在于,所述箱体包括箱主体、第一盖板、第一分配板和第二盖板,所述箱主体的两面开设有开口端,所述箱主体两开口端所在的两面相邻设置,所述箱主体与所述第二盖板密封固定,在另一开口端从所述箱主体由内到外依次设置有所述分配板和第一盖板,所述分配板设置有至少一个分配孔、以及至少一个汇流孔,所述分配孔为所述第一孔,所述汇流孔为所述第二孔;
    所述分配板与所述第一盖板相配合,所述分配板朝向所述第一盖板的第一面与所述第一盖板的四周部分基本贴合且密封固定,所述分配板与所述第一盖板之间形成有第一腔和第二腔,所述第一腔与第二腔之间相互隔离,所述第一腔与所述分配孔连通,所述第二腔与所述汇流孔连通。
  7. 一种换热器,包括箱体以及容纳于所述箱体内的换热芯体,所述箱体内形成有第一流体通道,所述换热芯体内形成有第二流体通道,所述第一流体通道与第二流体通道相互隔离,所述换热芯体包括一个或者二个以上扁管,所述第二流体通道位于所述扁管内,所述扁管包括至少两个第一折弯部、至少一个第二折弯部和多个平直部,所述第一折弯部和第二折弯部分别位于所述换热芯体相对两侧,两相邻所述平直部大致平行且保持0.5mm~6mm的距离;
    所述箱体包括箱主体、第一盖板和分配板,所述箱主体的一面开设有开口端,在所述开口端从所述箱主体由内到外依次固定有所述分配板和第一盖板,所述分配板设置有至少一个分配孔、以及至少一个汇流孔,所述第一折弯部和/或所述平直部靠近所述第一折弯部部分向与所述分配板方向的投影与所述分配孔至少部分重合,所述第二折弯部和/或平直部靠近所述第二折弯部部分向与所述分配板方向的投影与所述汇流孔至少部分重合;
    所述分配板与所述第一盖板相配合,所述分配板朝向所述第一盖板的第一面与所述第一盖板的四周部分基本贴合且密封固定,所述分配板与所述第一盖板之间形成有第一腔和第二腔,所述第一腔与第二腔之间相互隔离,所述第一腔与所述分配孔连通,所述第二腔与所述汇流孔连通。
  8. 一种换热器,包括箱体以及容纳于所述箱体内的换热芯体,所述箱体内形成有第一流体通道,所述换热芯体内形成有第二流体通道,所述第一流体通道与第二流体通道相互隔离,所述换热芯体包括一个或者二个以上扁管,所述第二流体通道位于所述扁管内,所述扁管包括至少两个第一折弯部、至少一个第二折弯部和多个平直部,所述第一折弯部和第二折弯部分别位于所述换热芯体相对两侧,两相邻所述平直部大致平行且保持0.5mm~6mm的距离,且两相邻第一折弯部或者两相邻第二折弯部之间的最小距离大于零,两相邻第一折弯部错位设置,两相邻第二折弯部错位设置,且两相邻第一折弯部之间的最小距离大于相邻第一折弯部与平直部之间的最小距离,两相邻第二折弯部之间的最小距离大于相邻第二折弯部与平直部之间的最小距离。
  9. 一种换热器,包括箱体和换热芯体,所述换热芯体的至少一部分收容于所述箱体内部,所述箱体内形成第一流体通道,所述换热芯体包括一个或两个以上扁管,所述扁管内部形成第二流体通道,所述第一流体通道与所述第二流体通道相互隔离;
    所述扁管包括至少两个第一折弯部、多个平直部和至少一个第二折弯部,所述第一折弯部位于所述箱体内部的一侧,所述第二折弯部位于所述箱体内部的另一侧,相邻平直部大致平行设置;
    所述箱体包括箱主体、分配板和盖板,所述箱主体的一侧设有开口部, 所述分配板与所述箱主体的开口部固定设置,所述分配板与所述盖板固定设置;
    所述盖板包括第一接口和第二接口,所述第一接口和第二接口与所述第一流体通道相连通;所述分配板包括一个或两个以上第一连通部、一个或两个以上第二连通部和一个或两个以上第三连通部,所述第一连通部、所述第二连通部相对靠近所述第一折弯部且与所述第一折弯部附近的空间连通,所述第三连通部相对靠近所述第二折弯部位且与所述第二折弯部附近的空间连通;所述盖板与所述分配板之间形成有至少三个腔室,所述腔室之间相互隔离,所述腔室包括第一腔、第二腔和第三腔,所述第一腔与所述第一连通部连通,所述第二腔与所述第二连通部连通,所述第三腔与所述第三连通部连通,所述第一接口与所述第一腔连通,所述第二接口与所述第二腔连通。
  10. 一种换热器,包括箱体和换热芯体,所述换热芯体的至少一部分收容于所述箱体内部,所述换热器在所述箱体内形成第一流体通道,所述换热芯体包括一个或两个以上扁管,所述扁管内部形成第二流体通道,所述第一流体通道与所述第二流体通道相互隔离;
    所述箱体包括盖体部和主体部,所述盖体部包括第一腔、第二腔和第三腔,所述第一腔、第二腔和第三腔相互隔离,所述盖体部的第一侧包括第一接口和第二接口,所述盖体部的第二侧包括一个或两个以上第一连通部、一个或两个以上第二连通部和一个或两个以上第三连通部,所述第一接口与所述第一腔连通,所述一个或两个以上第一连通部与所述第一腔相连通,所述第二接口与所述第二腔相连通,所述一个或两个以上第二连通部与所述第二腔相连通;所述盖体部的第二侧与所述主体部固定,所述第三连通部与所述第三腔连通;
    所述扁管包括至少两个第一折弯部、多个平直部和至少一个第二折弯部,所述第一折弯部位于所述箱体的主体部内部的一侧,所述第二折弯部位于所述箱体的主体部内部的另一侧,相邻平直部大致平行设置;所述箱体的主体部包括至少两个换热区,所述换热区包括第一换热区和第二换热区,所述第一换热区的一侧与所述第一连通部相连通,所述第一换热区的另一侧与所述第三连通部的一部分相连通,所述第二换热区的一侧与所述 第二连通部相连通,所述第二换热区的另一侧与所述第三连通部的另一部分相连通,所述第三连通部的一部分与所述第三腔连通,所述第三连通部的另一部分与所述第三腔相连通。
  11. 一种换热器,包括箱体和换热芯体,所述换热芯体的至少一部分收容于所述箱体内部,所述换热器在所述箱体内形成第一流体通道,所述换热芯体包括一个或两个以上扁管,所述扁管内部形成第二流体通道,所述第一流体通道与所述第二流体通道不连通;
    所述扁管包括至少两个第一折弯部、多个平直部和至少一个第二折弯部,所述第一折弯部位于所述箱体内部的一侧,所述第二折弯部位于所述箱体内部的另一侧,相邻平直部大致平行设置;所述扁管包括第一端部和第二端部,所述第一端部、第二端部与所述第二折弯部位于所述箱体相对远离所述第一折弯部的一侧;
    所述箱体包括箱主体和盖体,所述盖体包括第一接口、第二接口、至少两个腔室以及至少两个连通部,所述腔室包括第一腔和第二腔,所述各腔室相互隔离,所述连通部包括第一连通部和第二连通部,所述第一接口与所述第一腔连通,所述第一连通部与所述第一腔连通,所述第二接口与所述第二腔连通,所述第二连通部与所述第二腔连通,所述第一连通部、第二连通部与所述第一流体通道相连通;所述箱主体开设有开口端,所述盖体与所述箱主体的开口端固定设置;所述箱主体的一侧部开设有槽,所述扁管的一部分穿过所述槽,所述第一折弯部与所述第一端部或第二端部之间的距离L1小于或等于所述箱体内壁之间的距离L0。
  12. 一种换热器,包括箱体和换热芯体,所述换热芯体的至少一部分收容于所述箱体内部,所述换热器在所述箱体内形成第一流体通道,所述换热芯体包括两个或两个以上扁管,所述扁管内部形成第二流体通道,所述第一流体通道与所述第二流体通道相互隔离;
    所述箱体包括主体部、分隔部、第一盖体和第二盖体,所述主体部与所述第一盖体固定设置,所述主体部与所述第二盖体固定设置;所述第一盖体位于所述分隔部的一侧,所述第二盖体位于所述分隔部的另一侧;所述第一盖体、第二盖体和所述主体部之间形成所述第一流体通道;所述第一盖体包括第一接口、一个或两个以上第一连通部以及第一腔,所述第一 接口与所述第一腔连通,所述第一连通部与所述第一腔连通,所述第二盖体包括第二接口、一个或两个以上第二连通部以及第二腔,所述第二接口与所述第二腔连通,所述第二连通部与所述第二腔连通;
    所述扁管包括至少一个第一折弯部、多个平直部和至少一个第二折弯部,所述第一折弯部位于所述主体部内部的一侧,所述第二折弯部位于所述主体部内部的另一侧,相邻平直部大致平行设置;
    所述扁管包括第一扁管和第二扁管,所述第一扁管和第二扁管分设于所述分隔部两侧,在所述分隔部与第一盖体之间形成第一流通区,在所述分隔部与第二盖体之间形成第二流通区,所述第一流通区、第二流通区为所述第一流体通道的一部分;所述第一流通区与所述第一连通部连通,所述第二流通区与所述第二连通部连通;所述换热器还包括连通所述第一流通区和第二流通区的连通口。
  13. 一种换热器,包括壳体以及换热芯体,所述壳体内形成有腔室,所述换热芯体部分或者全部容纳于所述腔室,所述壳体还设置有第三接口和第四接口,所述第三接口和第四接口与所述腔室连通,所述换热芯体内形成有第一流体通道,所述第一流体通道与所述腔室隔离,其特征在于,所述换热器还包括连接块,所述连接块设置有第一通道、第二通道、与第一通道连通的第一接口、以及与第二通道连通的第二接口;
    所述连接块还设置有与第一通道相对应的第一通道的第一承插孔、以及与第二通道相对应的第二通道的第一承插孔,所述换热芯体包括至少一个扁平管,至少一部分所述第一流体通道位于所述扁平管内,所述扁平管的一端至少一部分伸入所述第一通道的第一承插孔且与所述第一通道的第一承插孔密封安装,所述第一通道与所述扁平管的第一流体通道连通,所述扁平管的另一端至少一部分伸入所述第二通道的第一承插孔且与所述第二通道的第一承插孔密封安装,所述第二通道与所述扁平管的第一流体通道连通。
  14. 一种换热器,包括壳体以及部分或者全部容纳于壳体内的换热芯体,所述壳体内形成有腔室,所述换热芯体部分或者全部容纳于所述腔室,所述壳体还设置有第三接口和第四接口,所述第三接口和第四接口与所述腔室连通,所述换热芯体内形成有第一流体通道,所述第一流体通道与所 述腔室的换热芯体外的空间相互隔离,其特征在于,所述换热器还包括连接块,所述连接块设置有第一通道、第二通道、与第一通道连通的第一接口、以及与第二通道连通的第二接口,所述第一接口和第二接口与所述第一流体通道连通;
    所述壳体包括外壳体和分隔件,所述分隔件设置于外壳体内,使所述壳体形成有第一腔、第二腔和第三腔,所述分隔件包括第一分隔壁、第一壁部和第二壁部,所述第一壁部位于所述第一腔和第三腔之间,所述第二壁部位于所述第二腔和第三腔之间,所述第一分隔壁位于所述第一腔和第二腔之间,所述第一壁部设置有第一连通孔,所述第一腔通过所述第一连通孔与所述第三腔相连通,所述第二壁部设置有第二连通孔,所述第二腔通过所述第二连通孔与第三腔相连通。
PCT/CN2016/107483 2015-12-09 2016-11-28 一种换热器 WO2017097133A1 (zh)

Priority Applications (2)

Application Number Priority Date Filing Date Title
US16/060,017 US10520258B2 (en) 2015-12-09 2016-11-28 Heat exchanger
EP16872324.5A EP3388770B1 (en) 2015-12-09 2016-11-28 Heat exchanger

Applications Claiming Priority (18)

Application Number Priority Date Filing Date Title
CN201510906370.6 2015-12-09
CN201510906370.6A CN106855328B (zh) 2015-12-09 2015-12-09 一种换热器
CN201510906354.7A CN106855327B (zh) 2015-12-09 2015-12-09 一种换热器
CN201510905980.4 2015-12-09
CN201510906354.7 2015-12-09
CN201510905980.4A CN106855369B (zh) 2015-12-09 2015-12-09 一种换热器
CN201610201002.6 2016-03-31
CN201610196914.9A CN107289675B (zh) 2016-03-31 2016-03-31 换热器及车辆热管理系统
CN201610201002.6A CN107289676B (zh) 2016-03-31 2016-03-31 换热器及车辆空调系统
CN201610196745.9 2016-03-31
CN201610201884.6 2016-03-31
CN201610196914.9 2016-03-31
CN201610196745.9A CN107289674B (zh) 2016-03-31 2016-03-31 换热器及车辆热管理系统
CN201610201884.6A CN107289677B (zh) 2016-03-31 2016-03-31 换热器及co2冷却系统
CN201610629325.5 2016-08-03
CN201610634384.1 2016-08-03
CN201610634384.1A CN107687787B (zh) 2016-08-03 2016-08-03 热交换装置
CN201610629325.5A CN107687726B (zh) 2016-08-03 2016-08-03 热交换装置

Publications (1)

Publication Number Publication Date
WO2017097133A1 true WO2017097133A1 (zh) 2017-06-15

Family

ID=59012680

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2016/107483 WO2017097133A1 (zh) 2015-12-09 2016-11-28 一种换热器

Country Status (3)

Country Link
US (1) US10520258B2 (zh)
EP (1) EP3388770B1 (zh)
WO (1) WO2017097133A1 (zh)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110411247A (zh) * 2018-04-27 2019-11-05 浙江三花汽车零部件有限公司 流体换热装置及热管理系统
EP3768534A4 (en) * 2018-03-23 2022-01-26 Modine Manufacturing Company LIQUID-REFRIGERANT HEAT EXCHANGER SUITABLE FOR HIGH PRESSURE
WO2022048251A1 (zh) * 2020-09-01 2022-03-10 浙江盾安人工环境股份有限公司 组合式换热器

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102491602B1 (ko) * 2015-10-23 2023-01-25 삼성전자주식회사 공기조화기
WO2020108513A1 (zh) * 2018-11-30 2020-06-04 浙江三花汽车零部件有限公司 一种换热装置
US20220146210A1 (en) * 2019-03-15 2022-05-12 Phase Change Energy Solutions, Inc. Thermal energy storage systems
EP3757503A1 (en) * 2019-06-26 2020-12-30 Valeo Autosystemy SP. Z.O.O. Heat exchanger with a connector
CN111664731A (zh) * 2020-05-21 2020-09-15 江苏远卓设备制造有限公司 一种长流程板式换热器

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5528476A (en) * 1978-08-22 1980-02-29 Nippon Denso Co Ltd Heat exchanger
KR20040038328A (ko) * 2002-10-31 2004-05-08 엘지전자 주식회사 열교환기의 연결 장치
CN201652995U (zh) * 2010-05-20 2010-11-24 三花丹佛斯(杭州)微通道换热器有限公司 微通道换热器
CN201706938U (zh) * 2010-06-24 2011-01-12 宁波连通设备制造有限公司 应用在余热锅炉中的螺旋扁管
CN103256757A (zh) * 2013-03-28 2013-08-21 广东美的电器股份有限公司 换热器及空气调节装置
CN203980722U (zh) * 2014-07-17 2014-12-03 广东美的制冷设备有限公司 平行流换热器和具有该平行流换热器的空调器
CN104949394A (zh) * 2014-03-26 2015-09-30 杭州三花研究院有限公司 一种换热器

Family Cites Families (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58106394A (ja) * 1981-12-18 1983-06-24 Hitachi Ltd 熱交換器
JPH09189463A (ja) 1996-02-29 1997-07-22 Mitsubishi Electric Corp 熱交換器の分配装置及びその製造方法
CN1285500A (zh) 1999-08-20 2001-02-28 瓦莱奥空调技术有限公司 汽车用的有加翅片扁管的换热器
JP4574535B2 (ja) * 2005-12-16 2010-11-04 リンナイ株式会社 潜熱回収型熱交換器の製造方法。
WO2009110664A1 (en) * 2008-03-07 2009-09-11 Lg Electronics Inc. Heat exchanger
DE102008043920A1 (de) * 2008-11-20 2010-05-27 BSH Bosch und Siemens Hausgeräte GmbH Kondensationstrockner mit einer Wärmepumpe sowie Verfahren zu seinem Betrieb
FR2963091B1 (fr) 2010-07-20 2012-08-17 Univ Savoie Module de circulation de fluides
KR101266917B1 (ko) * 2011-12-13 2013-05-27 주식회사 코렌스 웨이브핀을 이용한 과열증기발생장치
KR20130085864A (ko) * 2012-01-20 2013-07-30 한밭대학교 산학협력단 열교환기
DE102012211350A1 (de) 2012-06-29 2014-01-02 Behr Gmbh & Co. Kg Flachrohr und Wärmeübertrager mit einem solchen Flachrohr
KR101373130B1 (ko) 2012-06-29 2014-03-11 린나이코리아 주식회사 유로 파이프가 장착된 보일러의 열교환기
DE102012106782A1 (de) 2012-07-26 2014-01-30 Halla Visteon Climate Control Corporation Wärmeübertrager zur Abgaskühlung in Kraftfahrzeugen
CN104296422B (zh) 2013-07-19 2018-04-20 浙江三花汽车零部件有限公司 换热器集成组件
CN103868380B (zh) 2012-12-11 2016-08-24 杭州三花研究院有限公司 一种板式热交换器
CN203100483U (zh) 2013-01-07 2013-07-31 广东美的电器股份有限公司 换热器
CN203274364U (zh) 2013-03-21 2013-11-06 杭州三花微通道换热器有限公司 折弯式换热器
CN104121800B (zh) 2013-04-27 2017-09-26 杭州三花微通道换热器有限公司 流通管接头及具有该流通管接头的换热器
JP6202391B2 (ja) 2013-12-25 2017-09-27 株式会社ノーリツ 熱交換器およびその製造方法
CN103968698A (zh) 2014-04-30 2014-08-06 杭州三花微通道换热器有限公司 一种换热器及其翅片,以及换热器的加工方法
CN204188033U (zh) 2014-09-29 2015-03-04 杭州三花微通道换热器有限公司 一种换热器
CN204329704U (zh) 2014-12-12 2015-05-13 重庆超力高科技股份有限公司 一种换热器的边板
CN204730525U (zh) 2015-06-02 2015-10-28 浙江同星制冷有限公司 一种采用铝针片换热管的冰箱及空调用换热器

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5528476A (en) * 1978-08-22 1980-02-29 Nippon Denso Co Ltd Heat exchanger
KR20040038328A (ko) * 2002-10-31 2004-05-08 엘지전자 주식회사 열교환기의 연결 장치
CN201652995U (zh) * 2010-05-20 2010-11-24 三花丹佛斯(杭州)微通道换热器有限公司 微通道换热器
CN201706938U (zh) * 2010-06-24 2011-01-12 宁波连通设备制造有限公司 应用在余热锅炉中的螺旋扁管
CN103256757A (zh) * 2013-03-28 2013-08-21 广东美的电器股份有限公司 换热器及空气调节装置
CN104949394A (zh) * 2014-03-26 2015-09-30 杭州三花研究院有限公司 一种换热器
CN203980722U (zh) * 2014-07-17 2014-12-03 广东美的制冷设备有限公司 平行流换热器和具有该平行流换热器的空调器

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP3388770A4 *

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3768534A4 (en) * 2018-03-23 2022-01-26 Modine Manufacturing Company LIQUID-REFRIGERANT HEAT EXCHANGER SUITABLE FOR HIGH PRESSURE
US11609047B2 (en) 2018-03-23 2023-03-21 Modine Manufacturing Company High pressure capable liquid to refrigerant heat exchanger
CN110411247A (zh) * 2018-04-27 2019-11-05 浙江三花汽车零部件有限公司 流体换热装置及热管理系统
CN110411247B (zh) * 2018-04-27 2021-12-24 浙江三花汽车零部件有限公司 流体换热装置及热管理系统
WO2022048251A1 (zh) * 2020-09-01 2022-03-10 浙江盾安人工环境股份有限公司 组合式换热器

Also Published As

Publication number Publication date
US20180363988A1 (en) 2018-12-20
EP3388770B1 (en) 2023-05-24
EP3388770A1 (en) 2018-10-17
EP3388770A4 (en) 2019-07-10
US10520258B2 (en) 2019-12-31

Similar Documents

Publication Publication Date Title
WO2017097133A1 (zh) 一种换热器
US20120031598A1 (en) Plate heat exchanger
CN107289677B (zh) 换热器及co2冷却系统
CN107687787B (zh) 热交换装置
EP2792988B1 (en) Integrated heat exchanger for a vehicle
CN111256389B (zh) 一种换热器
WO2020238781A1 (zh) 板式换热器
CN211552541U (zh) 换热器
CN106855327B (zh) 一种换热器
CN112880436A (zh) 换热器
EP3495761B1 (en) Heat exchange device
CN107289675B (zh) 换热器及车辆热管理系统
CN112146475B (zh) 集流管及换热器
CN106855369B (zh) 一种换热器
CN210741194U (zh) 一种板式换热器
CN106855328A (zh) 一种换热器
CN110567311B (zh) 集管箱及换热器
CN107687726B (zh) 热交换装置
CN107289676B (zh) 换热器及车辆空调系统
CN211425152U (zh) 换热器
CN111256391B (zh) 换热装置
CN111256390B (zh) 换热装置
CN216159701U (zh) 换热器
CN111559218B (zh) 一种热交换器
CN111561795A (zh) 一种热交换器

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 16872324

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

WWE Wipo information: entry into national phase

Ref document number: 2016872324

Country of ref document: EP