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Heat exchanger and method of producing the same

A technology for heat exchangers and manufacturing methods, applied in the direction of heat exchanger types, indirect heat exchangers, lighting and heating equipment, etc., can solve the problems of insufficient reliability of fluid leakage, expensive heat exchangers, and accompanying difficulties, etc. Easy to manufacture, cheap to provide, and the effect of simplifying the process

Inactive Publication Date: 2009-04-08
PANASONIC CORP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, a precision machining device must be prepared in order to manufacture thin round tubes. Therefore, not only does the heat exchanger become expensive, but also the inlet box 31 and the outlet box 32 must be provided with the tubes 33 at a predetermined fine pitch. fine round holes, so that it is difficult to insert the pipe 33 into the inlet box 31 and the outlet box 32 for connection.
Therefore, even though the heat exchange performance of such a heat exchanger is high, its extremely high price and the fact that there is not sufficient reliability against fluid leakage during use have become existing problems.

Method used

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  • Heat exchanger and method of producing the same
  • Heat exchanger and method of producing the same
  • Heat exchanger and method of producing the same

Examples

Experimental program
Comparison scheme
Effect test

Embodiment approach 1

[0064] figure 1 is a front view of the heat exchanger according to Embodiment 1 of the present invention, figure 2 is a sectional view showing the heat exchanger in a direction perpendicular to the tube axis of the heat exchange section, image 3 is a sectional view showing the heat exchanger in the tube axis direction of the heat exchange portion.

[0065] exist Figure 1 to Figure 3 Among them, the heat exchanger is composed of a heat exchange unit 1 and headers 2 at both ends of the heat exchange unit 1 . The heat exchange unit 1 has tubes 3 , tube inner flow paths 4 , and tube outer flow paths 5 arranged in a grid pattern. The header part 2 has a branch flow path 6 , an inflow pipe 7 , and an outflow pipe 8 inside, and the in-pipe flow path 4 is connected to the branch flow path 6 . The cross-sectional shape of the pipe 3 is approximately square, and is composed of a strip-shaped long plate 9 and a long plate 10 with a U-shaped cross-sectional shape. The branch chan...

Embodiment approach 2

[0080] Figure 11 It is a perspective view of the heat exchange part in Embodiment 2 of this invention.

[0081] Figure 12 is a front view of the first substrate of Embodiment 2, Figure 13 is a front view of the second substrate. The heat exchange unit is constituted by alternately laminating first substrates 26 and second substrates 28 . A plurality of first slits 30 and a plurality of second slits 40 are alternately arranged substantially parallel to each other on the first substrate 26 . On the second substrate 28 , a third slit 50 having the same shape as the first slit 30 is provided at substantially the same position as the projection of the first slit 30 .

[0082] Accordingly, since the first slit 30 and the third slit 50 overlap each other on the projected plane, they are communicated with each other to form the tube-outside flow path 60 . In addition, the dimension in the longitudinal direction of the third slit 50 arranged on the second substrate 28 is shorte...

Embodiment approach 3

[0095] figure 1 9 is a perspective view of the heat exchange unit in Embodiment 3 of the present invention. The heat exchange unit is formed by stacking the first substrate 126 between the second substrate 128 . As in the second embodiment, the tube-outside flow path 160 is formed by the first slit 130 and the third slit 150 . In addition, an in-pipe flow path 170 is formed by the second slit 140 and the second substrate 128 . Here, on the inflow side of the external fluid, three first substrates 126 are laminated between the second substrates 128, followed by two, and one is laminated on the outlet end of the external fluid, whereby the in-pipe flow path 170 It becomes larger toward the inflow side of the external fluid in the substrate lamination direction.

[0096] In Embodiment 3, although three rows are arranged in the flow direction of the external fluid, not three rows but multiple rows may be used. In addition, the number of first substrates 126 to be laminated c...

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Abstract

A heat exchanger which, while having excellent heat exchanging performance, has a structure easy to produce, is of low cost, and has high quality and reliability. The heat exchanger has first base plates (26), in each of which first slits (30) and second slits (40) are provided in substantially parallel to each other, and has second base plates (28), in each of which third slits (50) with substantially the same shape as a first slit (30) are provided. The length in the longitudinal direction of a second base plate (28) is set to be less than the length of a second slit (40). The first base plates (26) and the second base plates (28) are layered over each other such that the first slits (30) provided in the first base plates (26) and the third slits (50) provided in the second base plates (28) are communicated. Flow paths (60) outside tubes are constructed by the first slits (30) provided in the first base plates (26) and the third base plates (50) provided in the second base plates (28). Flow paths (70) inside the tubes are constructed by the second slits (40) provided in the first base plates (26) and the second base plates (28). Since a heat exchanging section formed only by tubes can be constructed by the base plates with the slits, the heat exchanger can be easily produced. Further, the heat exchanger can be provided at low cost.

Description

technical field [0001] The present invention relates to heat exchangers for cooling systems, cooling systems and heating systems, and more particularly to liquid and gas heat exchangers used in systems requiring compactness such as information equipment. Background technique [0002] In the prior art, such heat exchangers generally consist of tubes and fins. In recent years, in order to achieve this compactness, there is a tendency to reduce the tube diameter and tube pitch, and to increase the density of tubes. For example, there are cases where the heat exchange part is constituted by a very small tube having a tube outer diameter of 0.5 mm. [0003] Figure 27 It is a front view of a conventional heat exchanger disclosed in JP-A-2001-116481. like Figure 27 As shown, in the conventional heat exchanger, the inlet box 31 and the outlet box 32 are arranged facing each other with a predetermined interval therebetween. Between the inlet box 31 and the outlet box 32 , a plur...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): F28D1/053
Inventor 谷口光德木户长生豆本寿章
Owner PANASONIC CORP
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