JPS6086389A - Heat exchanger - Google Patents
Heat exchangerInfo
- Publication number
- JPS6086389A JPS6086389A JP19556083A JP19556083A JPS6086389A JP S6086389 A JPS6086389 A JP S6086389A JP 19556083 A JP19556083 A JP 19556083A JP 19556083 A JP19556083 A JP 19556083A JP S6086389 A JPS6086389 A JP S6086389A
- Authority
- JP
- Japan
- Prior art keywords
- heat transfer
- fins
- fluid
- flow
- force
- 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
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
- F28F3/02—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
- F28F3/04—Elements 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
Landscapes
- 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
Description
【発明の詳細な説明】
(イ)産業上の利用分野
本発明は、冷凍機その他の機械に用いる熱交換器のよう
に、機械の運転条件によって熱交換する流体(以下、伝
熱流体という)の流量を変化させる熱交換器の改良に関
する。Detailed Description of the Invention (a) Industrial Application Field The present invention is directed to a fluid that exchanges heat depending on the operating conditions of the machine (hereinafter referred to as a heat transfer fluid), such as a heat exchanger used in a refrigerator or other machine. This invention relates to an improvement in a heat exchanger that changes the flow rate of a heat exchanger.
(ロ)従来技術
従来、熱交換器においては、その伝熱面にフィンを固設
することにより、伝熱面積を増やすと共に固設されたフ
ィンで伝熱流体の流れを乱して熱伝達率を高め、熱交換
器の性能を向上させる手段が知られている。(B) Conventional technology Conventionally, in a heat exchanger, by fixing fins on the heat transfer surface, the heat transfer area is increased, and the fixed fins disturb the flow of the heat transfer fluid to increase the heat transfer rate. Means are known for increasing the heat exchanger performance.
しかし、このような従来の手段においては、フィンが固
設されているために、伝熱流体の流量な増大させると圧
力損失が大きくなり、逆に流量を ゛減少させると流れ
を乱す効果が減少して伝熱性能が低下する欠点を有して
いた。However, in such conventional means, since the fins are fixed, increasing the flow rate of the heat transfer fluid increases the pressure loss, and conversely, decreasing the flow rate reduces the effect of disturbing the flow. This has the disadvantage that heat transfer performance deteriorates.
(ハ)発明の目的
本発明は、伝熱流体の流量が増大した場合の圧力損失を
軽減することができ、また、伝熱流体の流量が減少した
場合の伝熱性能の低下を軽減することのできる熱交換器
の提供を目的としたものである。(C) Purpose of the Invention The present invention is capable of reducing pressure loss when the flow rate of heat transfer fluid increases, and also reduces deterioration in heat transfer performance when the flow rate of heat transfer fluid decreases. The purpose is to provide a heat exchanger that can.
に)発明の構成
不発明は、熱交換器の構成部材である伝熱管や伝熱板な
どの表面(伝熱面)にフィンを形成し、かつ、このフィ
ンが伝熱流体の流動方向の力に応じて撓むように構成し
たものである。B) Structure of the invention The non-invention is that fins are formed on the surface (heat transfer surface) of heat transfer tubes, heat transfer plates, etc. that are the constituent members of a heat exchanger, and that the fins absorb the force in the flow direction of the heat transfer fluid. It is configured to flex according to the
本発明の熱交換器においては、伝熱流体の流量が増やさ
れて流動方向の力が強くなるとフィンが流動方向に太き
(撓んで流れの抵抗が小さくなるので、フィンの固設さ
れている従来の熱交換器にくらべ、伝熱流体の圧力損失
が軽減され、伝熱流体を熱交換器内に流すための動力を
軽減できる利点がある。また、逆に、伝熱流体の流量が
減らされて流動方向の力が弱くなると流動方向へのフィ
ンの撓みが小さくなって流れの乱れが促進されるので、
従来の熱交換器にくらべ、伝熱性能の低下を小さくする
ことができる。In the heat exchanger of the present invention, when the flow rate of the heat transfer fluid is increased and the force in the flow direction becomes stronger, the fins become thicker in the flow direction (bending and the flow resistance decreases, so the fins are fixed). Compared to conventional heat exchangers, it has the advantage of reducing the pressure loss of the heat transfer fluid and reducing the power required to flow the heat transfer fluid into the heat exchanger.Conversely, it also reduces the flow rate of the heat transfer fluid. When the force in the flow direction becomes weaker, the deflection of the fins in the flow direction becomes smaller and the turbulence of the flow is promoted.
Compared to conventional heat exchangers, the reduction in heat transfer performance can be reduced.
(ホ)実施例
第1図は本発明熱交換器の一実施例を示し、熱交換器の
伝熱壁の一部を拡大した概略構成図である。第1図にお
いて、(1)は熱交換器の伝熱壁で、この伝熱壁の上側
表面には切削加工によりフィン(21、(2)・・・が
形成されている。これらフィン(2L (2)・・・は
、その肉厚が基端(3)から先端(4)へと次第に薄く
なるように加工され、矢印方向に流れる伝熱流体の力に
よって弾性変形するようになっている。(E) Embodiment FIG. 1 shows an embodiment of the heat exchanger of the present invention, and is a schematic configuration diagram in which a part of the heat transfer wall of the heat exchanger is enlarged. In Fig. 1, (1) is a heat transfer wall of a heat exchanger, and fins (21, (2)...) are formed by cutting on the upper surface of this heat transfer wall.These fins (2L (2) ... is processed so that its wall thickness gradually becomes thinner from the base end (3) to the tip (4), and is elastically deformed by the force of the heat transfer fluid flowing in the direction of the arrow. .
なお、(5)、(5)・・・は切削により形成された伝
熱壁(1)面の窪みである。Note that (5), (5), . . . are depressions formed on the surface of the heat transfer wall (1) by cutting.
このように構成された熱交換器においては、伝熱流体の
流量を増大させると、流体の矢印方向の力が強くなり、
その力に応じてフィン(2)、(2)・・・が伝熱壁(
1)面側へなびくように撓むので、フィン(2)、(2
)・・・による矢印方向の流れの抵抗が小さくなって流
体の圧力損失が軽減される。その結果、フィンが固定さ
れている従来の熱交換器にくらべ、伝熱流体を熱交換器
内に流すためのポンプや送風機などの動力を軽減でき、
能力の小さいポンプや送風機の使用が可能となる。そし
て、逆に流量を減少させると、流体の矢印方向の力が弱
くなり、その弱くなった力とフィン(2)、(2)・・
・の弾性による力とが釣合うまで伝熱壁(1)面側から
立上るようにフィン(2)、(2)・・・が撓んで流れ
の抵抗が大きくなるので、伝熱流体の乱れの度合が従来
の熱交換器程には低下せず、従来の熱交換器にくらべて
伝熱性能の低下を軽減することができる。なお、第1図
に示した撓み角aは伝熱流体の流量が標準値にある場合
を表わしたもので、このaの具体的数値は伝熱流体の種
類や熱交換器を用いる機縁の種類あるいは仕様などによ
って適宜選定される。また、伝熱流体を流さない場合の
aの具体的数値a。も同様に適宜選定される。例えば、
伝熱流体に水を用い、冷房負荷O〜100%までの運転
条件を有する冷凍機に熱交換器を用いた例では、ao
の値を90゜にするのが好ましい。In a heat exchanger configured in this way, when the flow rate of the heat transfer fluid is increased, the force of the fluid in the direction of the arrow becomes stronger.
Depending on the force, the fins (2), (2)...
1) Since the fins (2) and (2
)... reduces the resistance to flow in the direction of the arrow, reducing fluid pressure loss. As a result, compared to conventional heat exchangers with fixed fins, the power required for pumps and blowers to flow the heat transfer fluid into the heat exchanger can be reduced.
It becomes possible to use a pump or blower with a small capacity. Conversely, when the flow rate is decreased, the force of the fluid in the direction of the arrow becomes weaker, and this weakened force and fins (2), (2)...
The fins (2), (2), etc. are bent to rise from the heat transfer wall (1) side until the elastic force of ・ is balanced, and the flow resistance increases, causing turbulence in the heat transfer fluid. The degree of heat transfer does not decrease as much as in conventional heat exchangers, and the decrease in heat transfer performance can be reduced compared to conventional heat exchangers. Note that the deflection angle a shown in Figure 1 represents the case where the flow rate of the heat transfer fluid is at a standard value, and the specific value of this a depends on the type of heat transfer fluid and the type of equipment using the heat exchanger. Alternatively, it is selected as appropriate depending on the specifications. Also, the specific value a of a when the heat transfer fluid is not flowing. are similarly selected as appropriate. for example,
In an example in which water is used as the heat transfer fluid and a heat exchanger is used in a refrigerator that has an operating condition of cooling load O to 100%, ao
It is preferable to set the value of 90°.
第2図は、本発明熱交換器の他の実施例を示したもので
、第1図と同様の構成機器には同一の図番を付している
。この実施例においては、伝熱壁(1)の上側表面に多
数の舌状のフィン(2)、(2)・・・を有(する基体
(3)を溶接や接着などで固着したもので、この基体お
よびフィン(2)、(2)・・・はバネ鋼その他の弾性
材で製作されている。FIG. 2 shows another embodiment of the heat exchanger of the present invention, in which the same components as in FIG. 1 are given the same figure numbers. In this embodiment, a base (3) having a large number of tongue-shaped fins (2), (2), etc. is fixed to the upper surface of a heat transfer wall (1) by welding or adhesive. , the base body and the fins (2), (2)... are made of spring steel or other elastic material.
また、第3図は本発明熱交換器の構成機器である伝熱管
およびその一部を切欠した概略構成説明図である。第3
図の実施例は、伝熱管(6)内の矢印方向に流量の変化
する伝熱流体を流し、伝熱管(6)の内壁面に伝熱流体
の流動方向の力に応じて撓み量が変化するフィン(2)
、(2)・・・を形成したものである。Moreover, FIG. 3 is a schematic structural explanatory diagram of a heat exchanger tube, which is a component of the heat exchanger of the present invention, and a portion thereof is cut away. Third
In the example shown in the figure, a heat transfer fluid whose flow rate changes in the direction of the arrow is flowed inside the heat transfer tube (6), and the amount of deflection changes depending on the force in the flow direction of the heat transfer fluid on the inner wall surface of the heat transfer tube (6). Fin (2)
, (2)... are formed.
(へ)発明の効果
以上のように、本発明熱交換器は、伝熱流体の流動方向
の力に応じて撓み量が変化するフィンを伝熱面に形成し
たものであるから、フィンの固設されている従来の熱交
換器にくらべ、伝熱流体の流量変化に伴なう圧力損失や
流れの乱れの変化を小さくでき、熱交換器へ伝熱流体を
送るための動力の軽減や熱交換器の伝熱性能の悪化の防
止などが可能となり、実用的価値の高いものである。(f) Effects of the Invention As described above, the heat exchanger of the present invention has fins formed on the heat transfer surface whose deflection amount changes depending on the force in the flow direction of the heat transfer fluid, so that the fins are not rigid. Compared to conventional heat exchangers installed in the heat exchanger, changes in pressure loss and flow turbulence due to changes in the flow rate of the heat transfer fluid can be reduced, reducing the power required to send the heat transfer fluid to the heat exchanger and reducing heat transfer. This makes it possible to prevent deterioration of the heat transfer performance of the exchanger, and has high practical value.
第1図ないし第3図は本発明熱交換器の実施例を示す図
で、第1図および第2図は本発明熱交換器の要部を拡大
した概略構成図であり、第3図は本発明熱交換器の伝熱
管の一部を切欠した概略構成図である。
(1)・・・伝熱壁、 (2)、(2)・・・フィン、
(6)・・・伝MIF。1 to 3 are diagrams showing embodiments of the heat exchanger of the present invention, FIGS. 1 and 2 are enlarged schematic configuration diagrams of the main parts of the heat exchanger of the present invention, and FIG. FIG. 2 is a schematic configuration diagram with a part of the heat exchanger tube of the heat exchanger of the present invention cut away. (1)...Heat transfer wall, (2), (2)...Fin,
(6)...den MIF.
Claims (1)
応じて撓み量が変化するフィンを形成したことを特徴と
する熱交換器。(1) A heat exchanger characterized in that fins are formed on the surface of a heat exchanger tube, a heat exchanger plate, etc., the amount of deflection of which changes depending on the force in the flow direction of the fluid.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19556083A JPS6086389A (en) | 1983-10-18 | 1983-10-18 | Heat exchanger |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19556083A JPS6086389A (en) | 1983-10-18 | 1983-10-18 | Heat exchanger |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6086389A true JPS6086389A (en) | 1985-05-15 |
Family
ID=16343142
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP19556083A Pending JPS6086389A (en) | 1983-10-18 | 1983-10-18 | Heat exchanger |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6086389A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5361828A (en) * | 1993-02-17 | 1994-11-08 | General Electric Company | Scaled heat transfer surface with protruding ramp surface turbulators |
US20090223648A1 (en) * | 2008-03-07 | 2009-09-10 | James Scott Martin | Heat exchanger with variable heat transfer properties |
US9957030B2 (en) | 2013-03-14 | 2018-05-01 | Duramax Marine, Llc | Turbulence enhancer for keel cooler |
US9982915B2 (en) | 2016-02-23 | 2018-05-29 | Gilles Savard | Air heating unit using solar energy |
-
1983
- 1983-10-18 JP JP19556083A patent/JPS6086389A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5361828A (en) * | 1993-02-17 | 1994-11-08 | General Electric Company | Scaled heat transfer surface with protruding ramp surface turbulators |
US20090223648A1 (en) * | 2008-03-07 | 2009-09-10 | James Scott Martin | Heat exchanger with variable heat transfer properties |
US9957030B2 (en) | 2013-03-14 | 2018-05-01 | Duramax Marine, Llc | Turbulence enhancer for keel cooler |
US10179637B2 (en) | 2013-03-14 | 2019-01-15 | Duramax Marine, Llc | Turbulence enhancer for keel cooler |
US9982915B2 (en) | 2016-02-23 | 2018-05-29 | Gilles Savard | Air heating unit using solar energy |
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