KR101693245B1 - Heat Exchanger - Google Patents

Heat Exchanger Download PDF

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Publication number
KR101693245B1
KR101693245B1 KR1020110036038A KR20110036038A KR101693245B1 KR 101693245 B1 KR101693245 B1 KR 101693245B1 KR 1020110036038 A KR1020110036038 A KR 1020110036038A KR 20110036038 A KR20110036038 A KR 20110036038A KR 101693245 B1 KR101693245 B1 KR 101693245B1
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KR
South Korea
Prior art keywords
bead
plate
communication hole
inlet pipe
outlet pipe
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KR1020110036038A
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Korean (ko)
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KR20120118590A (en
Inventor
전태수
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한온시스템 주식회사
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Priority to KR1020110036038A priority Critical patent/KR101693245B1/en
Publication of KR20120118590A publication Critical patent/KR20120118590A/en
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Publication of KR101693245B1 publication Critical patent/KR101693245B1/en

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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/02Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
    • F28F3/04Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element
    • F28F3/042Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element in the form of local deformations of the element
    • 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
    • F28D9/00Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D9/0031Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other
    • F28D9/0043Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the plates having openings therein for circulation of at least one heat-exchange medium from one conduit to another
    • F28D9/005Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the plates having openings therein for circulation of at least one heat-exchange medium from one conduit to another the plates having openings therein for both heat-exchange media

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

Abstract

The present invention relates to a plate type heat exchanger, and more particularly, to a plate type heat exchanger in which a protruding bead is formed on a plate to improve the fluidity of a heat exchange medium and ensure sufficient heat exchange performance and durability, .

Description

[0001] Heat Exchanger [0002]

The present invention relates to a plate type heat exchanger, and more particularly, to a plate type heat exchanger in which a protruding bead is formed on a plate to improve the fluidity of a heat exchange medium and ensure sufficient heat exchange performance and durability, .

In recent years, interest in the environment and energy has been increasing worldwide in the automobile industry, and studies for improving fuel efficiency have been made. Research and development for lightening, miniaturization and high performance are continuously carried out in order to satisfy the needs of various consumers.

Particularly, in a vehicle air conditioning system, it is difficult to secure a sufficient space in the engine room. Therefore, the structure of the heat exchanger constituting the automotive air conditioning system is required to be compact and capable of improving efficiency.

1 is a view showing a conventional plate heat exchanger. The plate heat exchanger shown in FIG. 1 includes a first inlet pipe 10 through which a first heat exchange medium flows and a first outlet pipe (not shown) through which the first heat exchange medium is introduced; A second inlet pipe 30 through which the second heat exchange medium is introduced and a second outlet pipe through which the second heat exchange medium is introduced (not shown); A plate (50) for forming a first fluid flow portion (51) and a second fluid flow portion (52) in which a plurality of fluids are stacked and the first heat exchange medium and the second heat exchange medium alternately flow; And an inner pin (60) interposed between the plate (50).

The inner fin is provided to increase the durability of the overall plate heat exchanger and to further improve the heat exchange performance of the first heat exchange medium and the second heat exchange medium.

However, there is a problem that the inner fin functions as a resistance which interferes with the flow of the first heat exchange medium and the second heat exchange medium, and thus the inner pin becomes difficult to flow and can act as an element that hinders the heat exchange performance.

On the other hand, when the inner fin is not provided to improve the flow path resistance of the first heat exchange medium and the second heat exchange medium, it is difficult to ensure sufficient durability.

Accordingly, there is a demand for development of a plate type heat exchanger capable of improving the heat exchange performance by smoothly flowing the flow while making the flow of the heat exchange medium turbulent while having sufficient durability.

SUMMARY OF THE INVENTION It is an object of the present invention to provide an apparatus and a method for manufacturing a heat exchanger in which a protrusion bead including first to sixth beads is formed on a plate, And a sufficient heat exchange performance and durability can be ensured.

More specifically, it is an object of the present invention to provide a method and a device for forming a first heat exchange medium, which comprises a first bead formed with a protruding bead along a first reference line, the first heat exchange medium flowing through a first inlet pipe, And the central first bead is formed to have a longer length than the auxiliary first bead, thereby stably supporting the central portion of the plate, thereby improving the durability.

The plate heat exchanger (1000) of the present invention comprises a first inlet pipe (100) through which a first heat exchange medium is introduced and a first outlet pipe (200) discharged therefrom; A second inlet pipe 300 through which the second heat exchange medium is introduced and a second outlet pipe 400 through which the second heat exchange medium is introduced; A first communication hole 510 and a second communication hole 520 which are respectively hollowed to be communicated with the first inlet pipe 100 and the first outlet pipe 200 and the second communication hole 520 and the second inlet pipe 300, A third communication hole (530) and a fourth communication hole (540) are formed to communicate with the pipe (400), respectively. The first communication hole and the second communication hole are formed by stacking a plurality of first and second heat exchange media A plate (500) forming the moving part (501) and the second moving part (502); Wherein the first inlet pipe 100 and the first outlet pipe 200 are positioned in a diagonal direction and the second inlet pipe 300 And the second outlet pipe 400 are positioned in a diagonal direction so that the plate 500 guides the flow of the first heat exchange medium inside the first flow portion 501. The first inlet pipe 100, A first bead 610 formed in an odd number along a first reference line L1 connecting the centers of the first outlet pipes 200 and a second bead 610 formed along a second reference line L2 perpendicular to the first reference line L1. A plurality of protruding beads 600 including a plurality of second beads 620 formed in parallel to the first beads 611 are formed.

The total length of the first bead 610 is 30 to 60% of the length of the first reference line L1.

The first bead 610 is composed of a central first bead 611 positioned at the center and the remaining auxiliary first bead 612. The center first bead 611 is connected to the remaining auxiliary first beads 612. [ 612).

The protruding bead 600 may be formed of a material that is adjacent to the first communication hole 510 and the second communication hole 520 and that connects the first inlet pipe 100 and the second inlet pipe 300 3 reference line L3, a fourth reference line L4 connecting the center of the first inlet pipe 100 and the second outlet pipe 400, a second reference line L4 connecting the first outlet pipe 200 and the second inlet pipe 300 And a third reference line L6 connecting the center of the first outlet pipe 200 and the center of the second outlet pipe 400. The third bead 630 ). ≪ / RTI >

The protruding bead 600 may further include a fourth bead 640 adjacent to the third communication hole 530 and the fourth communication hole 540.

The protruding beads 600 are formed in the inner space formed by the first bead 610, the second bead 620 and the third bead 630 when viewed from above in the stacking direction of the plate 500 The first heat exchange medium introduced through the first inlet pipe 100 is guided to the second bead 620 side and the first heat exchange medium having passed through the second bead 620 flows through the first outlet pipe 200, And a fifth bead 650 is formed to guide the bead 650 to be discharged.

The length of the second bead 620 to the fifth bead 650 is the same as the length of the auxiliary first bead 612 in the plate 500.

The protruding bead 600 is further formed with a sixth bead 660 having a circular cross section along a seventh reference line L7 connecting the centers of the second inlet pipe 300 and the second outlet pipe 400 .

At this time, the plate 500 is formed with the first bonding portions 550 and 550 'protruding upward or downward around the circumferences of the first communication hole 510 and the second communication hole 520, The second connecting portions 560 and 560 'are formed in the circumferences of the three communication holes 530 and the fourth communication holes 540 in the direction opposite to the protruding direction of the first bonding portions 550 and 550' A first plate 500a in which the first joint portion 550 is formed in a downward direction, the second joint portion 560 is formed in an upward direction, and the protruding bead 600 is formed in an upward direction; A second plate 500b having the second joining part 560 'formed in an upward direction, the second joining part 560' formed in a downward direction and the protruding bead 600 formed in a downward direction; May be alternately stacked.

The plate 500 includes a first connection part 550 formed in a lower side of the first communication hole 510 and the second communication hole 520 and a second connection part 550 formed in the third communication hole 530 and fourth A first plate 500a having a second joint portion 560 formed at an upper portion of a periphery of the communication hole 540; A first connection part 550 formed in the peripheral direction of the first communication hole 510 and the second communication hole 520 in the upward direction and a second connection part 550 formed in the peripheral part of the third communication hole 530 and the fourth communication hole 540 A second plate 500b having a second joint portion 560 formed in a lower direction; The first plate 500a or the second plate 500b forming the first fluid part 501 may be formed in the form of a plate having the protruding bead 600 formed thereon, And a third plate 500c having a first hollow portion 571 to a fourth hollow portion 574 formed therein so as to penetrate through the fourth communication hole 540 are joined to each other.

Accordingly, it is an object of the present invention to provide a plate-type heat exchanger in which the protrusion beads including the first to sixth beads are formed on the plate to improve the fluidity of the heat exchange medium, There is an advantage that durability can be ensured.

More specifically, the plate heat exchanger of the present invention includes a first bead formed with a protruding bead along a first reference line so that a first heat exchange medium introduced through a first inlet pipe flows along a first flow pipe, In particular, the central first bead is formed to have a longer length than the auxiliary first bead, so that the central portion of the plate can be stably supported and the durability can be improved.

BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a view showing a conventional plate heat exchanger. FIG.
2 is a perspective view showing a plate-type heat exchanger according to the present invention.
3 and 4 are an exploded perspective view and a flow schematic view showing a plate heat exchanger according to the present invention.
5 is another exploded perspective view showing a plate-type heat exchanger according to the present invention.
6 is a plan view of a plate of a plate heat exchanger according to the present invention.
7 is a graph showing the durability and the pressure drop amount according to the ratio of the first bead length to the first baseline length of the plate heat exchanger according to the present invention.
8 is a graph showing the water resistance of the plate heat exchanger according to the present invention.

Hereinafter, the plate heat exchanger 1000 of the present invention having the above-described characteristics will be described in detail with reference to the accompanying drawings.

The plate heat exchanger 1000 of the present invention includes a first inlet pipe 100, a first outlet pipe 200, a second inlet pipe 300, a second outlet pipe 400, and a plate 500 .

The first inlet pipe 100 is a portion through which the first heat exchange medium is introduced, and the first outlet pipe 200 is a portion through which the first heat exchange medium is discharged.

In addition, the second inlet pipe 300 is a portion through which the second heat exchange medium is introduced, and the second outlet pipe 400 is a portion through which the second heat exchange medium is discharged.

The plate 500 includes a first fluid flow unit 501 in which a plurality of first fluid flows through the first inlet pipe 100 and flows into the first outlet pipe 200, A second fluid exchange unit that receives the second heat exchange medium introduced through the second inlet pipe 300 and is discharged to the second outlet pipe 400 is alternately stacked.

The plate 500 includes the first inlet pipe 100, the first outlet pipe 200, the second inlet pipe 300, and the second inlet pipe 300 to form the first fluid portion 501 and the second fluid portion 502, And the first communication hole 510 to the fourth communication hole 540 are formed to communicate with the first outlet pipe 400 and the second outlet pipe 400, respectively.

In this case, the peripheries of the first communication hole 510 to the fourth communication hole 540 are protruded upward or downward. The same plate 500 has a first through- A first joint portion 550 or 550 'protruding upward or downward is formed at a periphery of the communication hole 510 and the second communication hole 520 communicating with the first outlet pipe 200, A third communication hole 530 communicating with the inlet pipe 300 and a fourth communication hole 540 communicating with the second outlet pipe 400 are formed in a circumferential direction opposite to the first junction 550 or 550 ' The second bonding portions 560 and 560 'are formed.

That is, when the first joint part 550 is formed downward in the same plate 500, the second joint part 560 is formed in an upward direction.

In addition, when the first bonding portion 550 'is hardened in the upward direction, the second bonding portion 560' is formed in a downward direction.

In the present invention, the plate 500 having the first joint part 550 formed at the lower side and the second joint part 560 formed at the upper side is defined as a first plate 500a, and the first joint part 550 ' Is formed in the upper direction and the second joint portion 560 'is formed in the lower direction is defined as the second plate 500b.

That is, the plate 500 of the present invention includes the first plate 500a and the second plate 500b, and the first plate 500a and the second plate 500b are alternately stacked, The first fluid unit 501 and the second fluid unit 502 are alternately formed.

At this time, a first fluid portion 501 through which the first heat exchange medium flows is formed on the upper side of the first plate 500a, and a second fluid portion 501 through which the second heat exchange medium flows is formed on the upper side of the second plate 500b. And a flow portion 502 is formed.

The first inlet pipe 100 and the first outlet pipe 200 are positioned in a diagonal direction and the second inlet pipe 300 and the second outlet pipe 400 are connected to each other Diagonal direction.

This means that when the plate heat exchanger 1000 is viewed from the upper side, when the center lines of the pipes are connected to each other, they are formed to be opposed to each other diagonally.

The plate heat exchanger 1000 of the present invention is characterized in that the first inlet pipe 100 and the first outlet pipe 200 are positioned in a diagonal direction and the second inlet pipe 300 and the second outlet pipe 400 The first heat exchanging medium and the second heat exchanging medium can be effectively brought into contact with each other and heat exchanged in the entire region.

2 to 5 show examples in which the first inlet pipe 100, the first outlet pipe 200, the second inlet pipe 300, and the second outlet pipe 400 are all located on the top, The present invention is not limited thereto.

In this case, the plate heat exchanger 1000 of the present invention includes a plurality of protruding beads 600 formed on the plate 500 to guide the flow of the first heat exchange medium into the first flow portion 501.

The protruding beads 600 may be joined to each other at the inner side of the first moving part 501 by the joining of the plate 500 and may be formed by a separate plate 500c.

The protruding bead 600 serves to guide the flow of the first heat exchange medium and to guide the flow of the first heat exchange medium, and further to improve the overall durability.

First, an example of forming the protruding bead 600 by joining the first plate 500a and the second plate 500b will be described (see FIG. 3)

The protrusion bead 600 protrudes upward from the first fluid part 501 of the first plate 500a and protrudes upward from the second fluid part 502 of the second plate 500b In the downward direction.

The protruding beads 600 are bonded to each other by alternate lamination of the first plate 500a and the second plate 500b.

Second, an example in which the third plate 500c is further formed to form the protruding bead 600 (see FIG. 5) is the same as that described above except that the protruding bead 600 is formed The first plate 500a and the second plate 500b of the first plate 500a and the second plate 500b of the first plate 500a are used. A third plate 500c in which hollow first to fourth hollow portions 571 to 574 are formed so that the first to fourth communication holes 510 to 540 are penetrated in the form of a plate in which the first to fourth communication holes 510 to 440 are formed, Respectively.

The first hollow portion 571 is connected to the first communication hole 510 while the second hollow portion 572 is connected to the second communication hole 510 and the third hollow portion 573 is connected to the third In the communication hole 530, the fourth hollow portion 574 is formed to correspond to the fourth communication hole 540.

More specifically, the plate type heat exchanger 1000 of the present invention includes a third plate 500c, which is formed by alternately stacking the first plate 500a and the second plate 500b and forms the protruding bead 600, May be formed on the first plate (500a) or the second plate (500b) forming the first fluid part (501).

5, a plate portion of the third plate 500c is joined to the first plate 500a, and a second plate 500b, which forms the first plate 500a and the first fluid portion 501, A protruding bead 600 protruding from the protruding bead 600 is formed.

At this time, the third plate 500c may adjust the height of the protruding bead 600 so that the end of the protruding bead 600 is bonded to the second plate 500b.

The protruding bead 600 may include a first bead 610 and a second bead 620 to a sixth bead 660.

The first bead 610 is formed along a first reference line L 1 connecting the first inlet pipe 100 and the first outlet pipe 200.

The first beads 610 are provided along the first reference line L1 and the total length of the first beads 610 is 30 to 100 times the length Lt of the first reference line L1. 60 (%).

In the drawing, the length of the center first bead 611 is Lb, the length of the auxiliary first bead 612 is La, and the length of the first reference line L1 is Lt.

The total length of the first beads 610 is a length including the thickness of the material when viewed from the upper side in the stacking direction of the plate 500. The length of the central first bead 611 and the length of the auxiliary first bead 611, And the length of the beads 612, and in the case of the embodiment shown in the drawing, Lb + La x 2.

7, the relationship between the first baseline length Lt connecting the first heat exchange medium inlet / outlet section (first inlet pipe 100 and first outlet pipe 200) to the first bead formation total length 610 And when the ratio of the first baseline length Lt to the total length 610 of the first bead 610 is less than 30%, it is insufficient in durability, and when the ratio is more than 60%, the pressure drop is increased more than the predetermined value Can be confirmed.

In the plate heat exchanger 1000 of the present invention, the first bead 610 is provided in an odd number, and the center first bead 611 positioned at the center is positioned at a distance of 1.5 to 3 times the length of the remaining auxiliary first bead 612 It is preferable that it is formed as a double.

In the plate heat exchanger 1000 of the present invention, the length of the central first bead 611 is set to be greater than the length of the auxiliary first bead 611. In this case, 1 bead 612 is 1.5 to 3 times longer than the length of one bead 612, thereby ensuring sufficient durability.

It is difficult to expect a durability enhancement effect by the central first bead 611 when the length of the central first bead 611 is less than 1.5 times the length of the auxiliary first bead 612, Since the plate heat exchanger 1000 of the present invention can prevent the flow of the first heat exchange medium when the length of the bead 611 is formed to be more than 3 times the length of the auxiliary first bead 612, The length of the bead 611 is preferably 1.5 to 3 times the length of the auxiliary first bead 612.

Although a total of three first beads 611 and two auxiliary first beads 612 are illustrated in the drawing, the present invention is not limited thereto, .

When the plate heat exchanger 1000 of the present invention is formed to be large in the longitudinal direction of the plate 500, the second bead 612 having the same length as the first bead 610 (auxiliary first bead 612) 620 may be further provided.

The second bead 620 is arranged along the second reference line L2 perpendicular to the first reference line L1 and parallel to the central first bead 611. The numerical value of the plate 500 .

The third bead 630 is formed adjacent to the first communication hole 510 and the second communication hole 520. The third bead 630 is a part of the first heat exchange medium 100 flowing through the first inlet pipe 100, The first outlet pipe 100 and the second outlet pipe 200. The first outlet pipe 200 and the first outlet pipe 200 are formed to be uniformly distributed.

The third bead 630 includes a third reference line L3 adjacent to the first communication hole 510 and connecting the first inlet pipe 100 and the second inlet pipe 300 to each other, And a fourth reference line L4 connecting the first inlet pipe 100 and the second outlet pipe 400 to each other.

The third bead 630 may include a fifth reference line L5 adjacent to the second communication hole 520 and connecting the first outlet pipe 200 and the second inlet pipe 300 to each other, And is formed along a sixth reference line L6 connecting the centers of the first outlet pipe 200 and the second outlet pipe 400, respectively.

The fourth bead 640 is adjacent to the third communication hole 530 and the fourth communication hole 540. The fourth bead 640 adjacent to the third communication hole 530 may be formed by The first heat exchange medium flowing through the first inlet pipe 100 is stably branched and moved along the third communication hole 530 and the fourth bead 640 adjacent to the fourth communication hole 540 The first heat exchange medium is diverged along the fourth communication hole 540, and then stagnated at the corner portion and stably merged again.

In the figure, the fourth bead 640 is formed at a half of an angle between the first reference line L1 and the fourth reference line L4, and the first reference line L1 and the fifth reference line L5). The medium is guided so that the first heat exchange medium is directed to the L1 and L4 central regions, and is positioned at the central portions of L1 and L4 to enhance the durability.

The fifth bead 650 may be formed in the inner space formed by the first bead 610, the second bead 620, and the third bead 630 when viewed from above in the stacking direction of the plate 500. [ The first heat exchange medium introduced through the first inlet pipe 100 is guided to the second bead 620 side and the first heat exchange medium having passed through the second bead 620 flows through the first outlet pipe 200, As shown in FIG.

The plate heat exchanger 1000 is formed in a long shape in the transverse direction of the plate 500 so that the distance between the first communication hole 510 and the second communication hole 520 and the distance between the second bead 620 The fifth bead 650 guides the flow of the first heat exchange medium through the second bead 620 or through the second bead 620. [

The second bead 620 to the fifth bead 650 may be formed to have the same shape and length as the auxiliary first bead 612 to facilitate the manufacture of the plate.

The sixth bead 660 is not provided with the first bead 610 and the fifth bead 650 of the plate 500 and is added for the purpose of enhancing durability. It is preferably formed in a circular cross-sectional shape so as to be minimized.

The sixth bead 660 is preferably positioned above a seventh reference line L7 connecting the centers of the second inlet pipe 300 and the second outlet pipe 400.

Referring to FIG. 4, the first heat exchange medium flowing through the first inlet pipe 100 flows through the first communication hole (not shown) 510 and is moved along the space of the first fluid part 501 formed on the upper side of the first plate 500a and moved upward along the second communication hole 520, 1 exit pipe 200 (indicated by a thick line in Fig. 4)

The second heat exchange medium flowing through the second inlet pipe 300 is moved downward along the third communication hole 530 and the second fluid exchange unit 502), moves upward along the fourth communication hole 540, and is discharged through the second outlet pipe 400 (indicated by a thin line in FIG. 4).

4, as the protruding bead 600 is formed, the plate-type heat exchanger 1000 of the present invention can guide the flow of the first heat exchange medium to minimize the amount of pressure drop, There is an advantage that sufficient durability can be secured even without an inner pin.

In fact, FIG. 8 is a graph showing the water resistance of the plate-type heat exchanger 1000 according to the present invention, and shows the relationship between the present invention of the embodiment shown in FIG. 3, The water resistance of Comparative Example 2, which does not exist, was compared.

As described in the conventional problem, in the case of Comparative Example 1 in which the fins exist, it can be confirmed that the flow resistance of the first heat exchange medium is not smooth as the flow resistance of the first heat exchange medium is increased.

On the contrary, the present invention is lower than the water flow resistance of Comparative Example 2 in which no fins are present, and even if the flow amount of the first heat exchange medium is increased, the rise width is not large, and the flow of the heat exchange medium is smooth.

That is, the plate-type heat exchanger 1000 of the present invention is advantageous in that it can secure sufficient durability while smoothly flowing the heat exchange medium.

Also, the protruding bead 600 can guide the first heat exchange medium to improve heat exchange efficiency.

It will be understood by those skilled in the art that various changes in form and details may be made therein without departing from the spirit and scope of the invention as defined by the appended claims.

1000: Plate Heat Exchanger
100: first inlet pipe 200: first outlet pipe
300: second inlet pipe 400: second outlet pipe
500: plate
500a: first plate 500b: second plate
500c: third plate
501: first flow section 502: second flow section
510: first communication hole 520: second communication hole
530: Third communication hole 540: Fourth communication hole
550, 550 ': first connection part 560, 560': second connection part
571: first hollow portion 572: second hollow portion
573: third hollow portion 574: fourth hollow portion
600: extruded bead
610: first bead 611: central first bead
612: auxiliary first bead
620: second bead 630: third bead
640: fourth bead 650: fifth bead
660: Sixth bead
L1: first reference line L2: second reference line
L3: third reference line L4: fourth reference line
L5: fifth reference line L6: sixth reference line
L7: Seventh baseline
Lt: length of the first reference line
La: Length of center first bead
Lb: length of auxiliary first bead

Claims (10)

A first inlet pipe 100 through which the first heat exchange medium is introduced and a first outlet pipe 200 through which the first heat exchange medium is introduced; A second inlet pipe 300 through which the second heat exchange medium is introduced and a second outlet pipe 400 through which the second heat exchange medium is introduced; A first communication hole 510 and a second communication hole 520 which are respectively hollowed to be communicated with the first inlet pipe 100 and the first outlet pipe 200 and the second communication hole 520 and the second inlet pipe 300, A third communication hole (530) and a fourth communication hole (540) are formed to communicate with the pipe (400), respectively. The first communication hole and the second communication hole are formed by stacking a plurality of first and second heat exchange media A plate (500) forming the moving part (501) and the second moving part (502); The heat exchanger (1000)
The plate-type heat exchanger (1000)
The first inlet pipe 100 and the first outlet pipe 200 are positioned in a diagonal direction and the second inlet pipe 300 and the second outlet pipe 400 are positioned diagonally,
The plate 500 is connected to the first inlet pipe 100 and the first outlet pipe 200 so as to guide the flow of the first heat exchange medium inside the first flow unit 501, A plurality of second beads 620 are formed along the central first bead 611 along a second reference line L2 perpendicular to the first reference line L1, Wherein a plurality of protruding beads (600) are formed.
The method according to claim 1,
Wherein a total length of the first bead (610) is 30 to 60% of a length of the first reference line (L1).
The method according to claim 1,
The first bead 610 includes a central first bead 611 located at the center and the remaining auxiliary first bead 612. The center first bead 611 is connected to the remaining auxiliary first bead 612, The length of the plate-like heat exchanger is 1.5 to 3 times the length of the plate-like heat exchanger.
The method of claim 3,
The protruding bead 600 is disposed adjacent to the first communication hole 510 and the second communication hole 520 and is connected to a third reference line connecting the center of the first inlet pipe 100 and the second inlet pipe 300, A fourth reference line L4 connecting the center of the first inlet pipe 100 and the center of the second outlet pipe 400 and a fourth reference line L4 connecting the center of the first outlet pipe 200 and the second inlet pipe 300, And a third bead 630 formed along a sixth reference line L6 connecting the first outlet pipe 200 and the second outlet pipe 400 to each other, Further comprising a plate-shaped heat exchanger.
5. The method of claim 4,
Wherein the protruding bead (600) further comprises a fourth bead (640) adjacent to the third communication hole (530) and the fourth communication hole (540).
6. The method of claim 5,
The protruding beads 600 are formed in the inner space formed by the first beads 610, the second beads 620 and the third beads 630 in the stacking direction of the plate 500, The first heat exchange medium introduced through the inlet pipe 100 is guided toward the second bead 620 and the first heat exchange medium having passed through the second bead 620 flows through the first outlet pipe 200 And a fifth bead (650) guiding the liquid to be discharged is further formed.
The method according to claim 6,
Wherein a length of each of the second to sixth beads (620) to (650) is equal to a length of the auxiliary first bead (612).
8. The method of claim 7,
The protruding bead 600 further includes a sixth bead 660 having a circular cross section along a seventh reference line L7 connecting the centers of the second inlet pipe 300 and the second outlet pipe 400 Features a plate-type heat exchanger.
The method according to claim 1,
The plate 500 is formed with first bonding portions 550 and 550 'that protrude upward or downward from the periphery of the first communication hole 510 and the second communication hole 520, The second connection portions 560 and 560 'are formed in the circumferential portions of the first connection portions 530 and the fourth communication holes 540 in the direction opposite to the protruding direction of the first connection portions 550 and 550'
A first plate 500a in which the first joint part 550 is formed in a downward direction and the second joint part 560 is formed in an upward direction and the protruding bead 600 is formed in an upward direction; A second plate 500b having the second joining part 560 'formed in an upward direction, the second joining part 560' formed in a downward direction and the protruding bead 600 formed in a downward direction; Are stacked alternately.
The method according to claim 1,
The plate (500)
The first and second communication holes 510 and 540 are formed in the lower portion of the first communication hole 530 and the fourth communication hole 540 in the circumferential direction of the first communication hole 510 and the second communication hole 520, A first plate 500a having a second joint portion 560 formed in an upper direction; A first connection part 550 formed in the peripheral direction of the first communication hole 510 and the second communication hole 520 in the upward direction and a second connection part 550 formed in the peripheral part of the third communication hole 530 and the fourth communication hole 540 A second plate 500b having a second joint portion 560 formed in a lower direction; Are stacked alternately,
The first and second communication holes 510 to 412 are formed in a plate shape in which the protrusion beads 600 are formed on the first plate 500a or the second plate 500b forming the first fluid passage 501, And a third plate (500c) in which hollow first to fourth hollow portions (571 to 574) are formed so that the first to fourth hollow portions (540) penetrate.
KR1020110036038A 2011-04-19 2011-04-19 Heat Exchanger KR101693245B1 (en)

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KR1020110036038A KR101693245B1 (en) 2011-04-19 2011-04-19 Heat Exchanger

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KR101650160B1 (en) * 2013-02-18 2016-08-23 한온시스템 주식회사 Heat Exchanger
KR101927119B1 (en) * 2013-09-25 2019-03-12 한온시스템 주식회사 Heat exchanger assembly
KR20150043745A (en) * 2013-10-15 2015-04-23 한라비스테온공조 주식회사 Heat Exchanger
CN108955319B (en) * 2018-09-25 2023-12-15 江苏远卓设备制造有限公司 Box type heat exchanger
IT202000026251A1 (en) * 2020-11-04 2022-05-04 Ibs Tech Spa HEAT EXCHANGER

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JP4122578B2 (en) * 1997-07-17 2008-07-23 株式会社デンソー Heat exchanger
JP3292128B2 (en) * 1998-02-27 2002-06-17 ダイキン工業株式会社 Plate heat exchanger

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