JPH01147294A - Heat exchanger - Google Patents
Heat exchangerInfo
- Publication number
- JPH01147294A JPH01147294A JP30646887A JP30646887A JPH01147294A JP H01147294 A JPH01147294 A JP H01147294A JP 30646887 A JP30646887 A JP 30646887A JP 30646887 A JP30646887 A JP 30646887A JP H01147294 A JPH01147294 A JP H01147294A
- Authority
- JP
- Japan
- Prior art keywords
- metallic
- foam
- flat
- pipe
- metallic pipe
- Prior art date
- Legal status (The legal status 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 status listed.)
- Pending
Links
- 239000006262 metallic foam Substances 0.000 claims abstract description 35
- 239000012530 fluid Substances 0.000 claims abstract description 10
- 229910052751 metal Inorganic materials 0.000 claims description 22
- 239000002184 metal Substances 0.000 claims description 22
- 239000003507 refrigerant Substances 0.000 abstract description 14
- 239000007769 metal material Substances 0.000 abstract description 6
- 238000005187 foaming Methods 0.000 abstract description 5
- 239000000463 material Substances 0.000 abstract description 5
- 229910052782 aluminium Inorganic materials 0.000 abstract description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 abstract description 3
- 238000005476 soldering Methods 0.000 abstract 2
- 239000006260 foam Substances 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 6
- 238000005219 brazing Methods 0.000 description 3
- WYTGDNHDOZPMIW-RCBQFDQVSA-N alstonine Natural products C1=CC2=C3C=CC=CC3=NC2=C2N1C[C@H]1[C@H](C)OC=C(C(=O)OC)[C@H]1C2 WYTGDNHDOZPMIW-RCBQFDQVSA-N 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D1/00—Heat-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
- F28D1/02—Heat-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
- F28D1/04—Heat-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
- F28D1/047—Heat-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
- F28D1/0477—Heat-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
- F28D1/0478—Heat-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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
- F28F13/003—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by using permeable mass, perforated or porous materials
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Dispersion Chemistry (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、車両用ニアコンディショナ等のエバポレータ
その他の各種の熱交換器の改良に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to improvements in evaporators and other various heat exchangers such as vehicle near conditioners.
従来、この種の熱交換器においては、例えば実公昭56
−32772号公報に示されているように、積層型エバ
ポレータにおいて偏平なチューブエレメント内に拡散板
を設けて、同チューブエレメント内の冷媒の流れを拡散
させるようにしたものがある。Conventionally, in this type of heat exchanger, for example,
As shown in Japanese Patent No. 32772, there is a stacked evaporator in which a diffusion plate is provided within a flat tube element to diffuse the flow of refrigerant within the tube element.
ところで、このような構成においては、拡散板が、プレ
ス加工により切起しを施した薄金属板でもって構成され
て、表面積の大きい網目状の冷媒通路をチューブエレメ
ント内に形成するようにしであるものの、プレス加工の
みによっては、薄金属板の切起しの細かさに限界が生じ
る。このため、チューブエレメント内における冷媒の流
れの均一化、冷媒の乱流効果の向上、伝熱表面積の拡大
等に自ら制限が生じる。その結果、エバポレータ全体に
おける均一な熱交換機能を確保し得ないという不具合を
招く。By the way, in such a configuration, the diffusion plate is made of a thin metal plate that has been cut and beveled by pressing, so that a mesh-like refrigerant passage with a large surface area is formed in the tube element. However, there is a limit to how finely the thin metal plate can be cut and raised by press working alone. For this reason, limitations arise in making the flow of the refrigerant uniform within the tube element, improving the turbulent flow effect of the refrigerant, expanding the heat transfer surface area, and the like. As a result, a problem arises in that a uniform heat exchange function cannot be ensured throughout the evaporator.
そこで、本発明は、このようなことに対処すべく、金属
発泡体の機能を有効に活用した熱交換器を提供しようと
するものである。Therefore, the present invention aims to provide a heat exchanger that effectively utilizes the functions of metal foam in order to cope with such problems.
かかる問題の解決にあたり、本発明の構成は、熱交換可
能な流体を通す偏平状金属管と、この金属管内に嵌装さ
れて前記流体の流れを均一化する金属発泡体とを設ける
ようにしたことにある。In order to solve this problem, the present invention includes a flat metal tube through which a heat exchangeable fluid passes, and a metal foam that is fitted into the metal tube to uniformize the flow of the fluid. There is a particular thing.
このように本発明を構成したことにより、前記流体が前
記金属管内に流入すると、同流体が前記金属発泡体を通
過することとなる。かかる場合、前記金属発泡体がその
全体に亘り一様な発泡作用を有するため、同金属発泡体
に流入した流体は、金属発泡体全体に亘り一様な乱流を
生じ同金属発泡体全体に亘り一様な分布状態となって通
過する。By configuring the present invention in this manner, when the fluid flows into the metal tube, the fluid passes through the metal foam. In such a case, since the metal foam has a uniform foaming effect throughout the metal foam, the fluid flowing into the metal foam causes a uniform turbulent flow throughout the metal foam. It passes in a uniformly distributed state.
このため、熱交換器の全表面に亘り一様な熱交換作用が
適正に発揮されてこの種熱交換器の熱交換能力の大幅な
改善に役立つ。また、この効果は、流体の金属発泡体内
部との接触面積増大に伴う熱伝達能力の向上により、よ
り一層促進され得る。Therefore, a uniform heat exchange effect is properly exerted over the entire surface of the heat exchanger, which helps greatly improve the heat exchange ability of this type of heat exchanger. Moreover, this effect can be further promoted by the improvement in heat transfer ability due to the increase in the contact area of the fluid with the inside of the metal foam.
以下、本発明の一実施例を図面により説明すると、第1
図は、本発明に係るサーペンタイン式エバポレータの一
部を示している。このエバポレータは、第1図にて図示
形状に曲折した帯状の偏平金属管10を備えており、こ
の偏平金属管10の各並行管部11〜11間には、各フ
ィン20が、第1図及び第2図に示すごとく、ロー付け
によりそれぞれ嵌着されている。Hereinafter, one embodiment of the present invention will be described with reference to the drawings.
The figure shows a part of a serpentine evaporator according to the invention. This evaporator is equipped with a band-shaped flat metal tube 10 bent into the shape shown in FIG. As shown in FIG. 2, they are fitted together by brazing.
偏平金属管10内には、ブロック状の金属発泡体30が
、第1図及び第2図に示すごとく、偏平金属管10の長
手方向に嵌装されており、この金属発泡体30の外表面
は偏平金属管10の内表面にロー付けにより一様に固着
されている。かかる場合、金属発泡体30は、発泡金属
材料からブロック状に加工した複数のブロック部として
偏平金属管10内に順次嵌装されている。本実施例にお
いて、上述の発泡金属材料としては、例えば、中央電気
工業(株)製のものを採用するのが好ましい。当該発泡
金属材料は、軽量で熱伝達良好なアルミニウム材料によ
り発泡率60%〜90%(連続発泡による)をもつよう
に形成されており、この発泡金属材料の骨格は、海綿の
ように三次元の−様な網目状となっている。このため、
金属発泡体30を冷媒が通るとき、この冷媒が金属発泡
体30の多数の網目により金属発泡体30の全体に亘り
一様に乱流を生しる。As shown in FIGS. 1 and 2, a block-shaped metal foam 30 is fitted into the flat metal tube 10 in the longitudinal direction of the flat metal tube 10. are uniformly fixed to the inner surface of the flat metal tube 10 by brazing. In such a case, the metal foam 30 is sequentially fitted into the flat metal tube 10 as a plurality of block parts processed into blocks from a foamed metal material. In this embodiment, it is preferable to use, for example, a foamed metal material manufactured by Chuo Electric Industry Co., Ltd. as the above-mentioned foamed metal material. The foamed metal material is made of lightweight aluminum material with good heat transfer and has a foaming rate of 60% to 90% (due to continuous foaming), and the skeleton of this foamed metal material is three-dimensional like a sponge. It has a mesh-like shape. For this reason,
When the refrigerant passes through the metal foam 30, the refrigerant generates a turbulent flow uniformly throughout the metal foam 30 due to the large number of meshes of the metal foam 30.
ところで、このようなエバポレータの製造にあたっては
、上述した金属発泡材料が柔軟性を有するため、偏平金
属管10内に金属発泡体30をブロック状にて順次嵌挿
ロー付けし、然る後、第1図に示すように曲折させるか
、金属発泡体30をブロック状にて順次嵌装し偏平金属
管を曲折して一体ロー付けすればよい。なお、第1図に
て、符号10aは、偏平金属管10の冷媒流入口を示す
。By the way, in manufacturing such an evaporator, since the above-mentioned metal foam material has flexibility, the metal foam 30 is sequentially fitted and brazed into the flat metal tube 10 in the form of blocks, and then The flat metal tube may be bent as shown in FIG. 1, or the metal foam 30 may be sequentially fitted in blocks, and the flat metal tube may be bent and brazed together. In FIG. 1, reference numeral 10a indicates a refrigerant inlet of the flat metal tube 10.
以上のように構成した本実施例において、エバポレータ
の偏平金属管10内にその冷媒流入口から冷媒が流入す
ると、同冷媒が金属発泡体30を通過する。かかる場合
、金属発泡体30が上述のような固有の特性を有するた
め、金属発泡体30内に流入した冷媒は、同金属発泡体
30の無数の網目状の発泡作用のもとに、金属発泡体3
0の全体に亘り一様に乱流を生じこの金属発泡体全体に
亘り一様に分布した状態にて通過する。換言すれば、金
属発泡体30による冷媒分布の均一化、及び金属発泡体
30の網目状の骨格に基く冷媒の金属発泡体30との接
触面積の著しい増大に起因して、偏平金属管10及び各
フィン20の各表面に接触する空気流との熱交換作用が
エバポレータ全表面に亘り一様に行なわれ得る。その結
果、エバポレータ全体に亘る−様な冷却能力を大幅に改
善できる。また、金属発泡体30がアルミニウム材料か
らなるため、エバポレータの軽量化にも役立つ。In this embodiment configured as described above, when the refrigerant flows into the flat metal tube 10 of the evaporator from the refrigerant inlet, the refrigerant passes through the metal foam 30. In such a case, since the metal foam 30 has the above-mentioned unique characteristics, the refrigerant that has flowed into the metal foam 30 will react to the metal foam under the foaming action of the countless meshes of the metal foam 30. body 3
A turbulent flow is generated uniformly over the whole of the metal foam and passes through the metal foam in a uniformly distributed state. In other words, the flat metal tube 10 and The heat exchange action with the air flow contacting each surface of each fin 20 can be performed uniformly over the entire surface of the evaporator. As a result, the cooling capacity throughout the evaporator can be significantly improved. Moreover, since the metal foam 30 is made of aluminum material, it also helps to reduce the weight of the evaporator.
なお、前記実施例においては、サーペンタイン式エバポ
レークに本発明が適用された例について説明したが、こ
れに代えて、ドロンカップ式エバポレータに本発明を適
用して実施しても、前記実施例と同様の作用効果を達成
し得る。かかる場合、冷媒通路を形成する各一対の金属
板40.50 (第3図にては一対のみを示す)間に
各金属発泡体60 (第3図にては、−枚のみを示す)
をロー付は挾持するように構成すればよい。なお、各金
属発泡体60は前記実施例における金属発泡体30と同
様の材料からなる。In the above embodiments, an example in which the present invention was applied to a serpentine evaporator was explained. However, even if the present invention is applied to a doron cup type evaporator instead, the same results as in the above embodiments will be obtained. can achieve the following effects. In such a case, each metal foam body 60 (only one plate is shown in FIG. 3) is placed between each pair of metal plates 40, 50 (only one pair is shown in FIG. 3) forming a refrigerant passage.
Brazing may be configured so that it is clamped. Note that each metal foam 60 is made of the same material as the metal foam 30 in the above embodiment.
また、本発明の実施にあたっては、エバポレータに限る
ことなく、ヒータコア、コンデンサ等の各種の熱交換器
に本発明を適用して実施してもよい。Further, in carrying out the present invention, the present invention is not limited to the evaporator, and may be applied to various heat exchangers such as heater cores and condensers.
第1図は本発明の一実施例を示す部分破断斜視図、第2
図は第1図における偏平金属管及び金属発泡体の部分断
面図、並びに第3図は前記実施例の変形例を示す要部分
解斜視図である。
符号の説明
10・・・偏平金属管、30.60・・・金属発泡体、
40.50・・・金属板。FIG. 1 is a partially cutaway perspective view showing one embodiment of the present invention, and FIG.
The figure is a partial sectional view of the flat metal tube and metal foam in FIG. 1, and FIG. 3 is an exploded perspective view of essential parts showing a modification of the embodiment. Explanation of symbols 10...Flat metal tube, 30.60...Metal foam,
40.50...Metal plate.
Claims (1)
に介装されて前記流体の流れを均一化する金属発泡体と
を備えた熱交換器。A heat exchanger comprising a flat metal tube through which a heat-exchangeable fluid passes, and a metal foam inserted within the metal tube to equalize the flow of the fluid.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP30646887A JPH01147294A (en) | 1987-12-03 | 1987-12-03 | Heat exchanger |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP30646887A JPH01147294A (en) | 1987-12-03 | 1987-12-03 | Heat exchanger |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH01147294A true JPH01147294A (en) | 1989-06-08 |
Family
ID=17957377
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP30646887A Pending JPH01147294A (en) | 1987-12-03 | 1987-12-03 | Heat exchanger |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01147294A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002540556A (en) * | 1999-03-22 | 2002-11-26 | インターナショナル フュエル セルズ,エルエルシー | Compact selective oxidizer for fuel cell power installations |
DE10324190A1 (en) * | 2003-05-28 | 2005-01-05 | M.Pore Gmbh | Metal foam heat exchanger, especially for electronic components, has a metal film on at least one of its outer surfaces with which a contact or connection is formed or made with the component that is to be cooled |
US7069975B1 (en) | 1999-09-16 | 2006-07-04 | Raytheon Company | Method and apparatus for cooling with a phase change material and heat pipes |
KR100717952B1 (en) * | 2005-12-16 | 2007-05-11 | 김경일 | Heat exchanger pipe and manufacturing method thereof |
-
1987
- 1987-12-03 JP JP30646887A patent/JPH01147294A/en active Pending
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002540556A (en) * | 1999-03-22 | 2002-11-26 | インターナショナル フュエル セルズ,エルエルシー | Compact selective oxidizer for fuel cell power installations |
US7069975B1 (en) | 1999-09-16 | 2006-07-04 | Raytheon Company | Method and apparatus for cooling with a phase change material and heat pipes |
US7416017B2 (en) | 1999-09-16 | 2008-08-26 | Raytheon Company | Method and apparatus for cooling with a phase change material and heat pipes |
DE10324190A1 (en) * | 2003-05-28 | 2005-01-05 | M.Pore Gmbh | Metal foam heat exchanger, especially for electronic components, has a metal film on at least one of its outer surfaces with which a contact or connection is formed or made with the component that is to be cooled |
DE10324190B4 (en) * | 2003-05-28 | 2009-07-23 | M.Pore Gmbh | heat exchangers |
KR100717952B1 (en) * | 2005-12-16 | 2007-05-11 | 김경일 | Heat exchanger pipe and manufacturing method thereof |
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