JPH0320576A - Evaporator - Google Patents

Evaporator

Info

Publication number
JPH0320576A
JPH0320576A JP7422490A JP7422490A JPH0320576A JP H0320576 A JPH0320576 A JP H0320576A JP 7422490 A JP7422490 A JP 7422490A JP 7422490 A JP7422490 A JP 7422490A JP H0320576 A JPH0320576 A JP H0320576A
Authority
JP
Japan
Prior art keywords
louvers
evaporator
condensed water
pitch
corrugated fins
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.)
Granted
Application number
JP7422490A
Other languages
Japanese (ja)
Other versions
JP2887495B2 (en
Inventor
Katsuhisa Suzuki
勝久 鈴木
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Altemira Co Ltd
Original Assignee
Showa Aluminum Corp
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
Application filed by Showa Aluminum Corp filed Critical Showa Aluminum Corp
Priority to JP2074224A priority Critical patent/JP2887495B2/en
Publication of JPH0320576A publication Critical patent/JPH0320576A/en
Application granted granted Critical
Publication of JP2887495B2 publication Critical patent/JP2887495B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

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
    • 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
    • F28D17/00Regenerative heat-exchange apparatus in which a stationary intermediate heat-transfer medium or body is contacted successively by each heat-exchange medium, e.g. using granular particles
    • F28D17/005Regenerative heat-exchange apparatus in which a stationary intermediate heat-transfer medium or body is contacted successively by each heat-exchange medium, e.g. using granular particles using granular particles
    • 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

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

PURPOSE:To improve the cooling performance of an evaporator, suppress the pressure loss, and clear waterdrops with a good efficiency by forming on level parts of corrugated fins louvers extended breadthways and arranged in parallel at a specific ratio of the height of the louvers to the pitch of the level parts of the corrugated fins. CONSTITUTION:On corrugated fins, since condensed water flows down through a slit 24 from an upper level part 21 onto a lower level part 21, the smaller a pitch P is, the more easily condensed water flows down. Accordingly, given a constant value H as the height of louvers 23, the pitch P becomes smaller the smaller the gap G between louvers 23 is, hence the more easily the condensed water falls. In considering the efficiency of an evaporator, the pressure loss as well as the cooling performance is an important factor. In considering the effect of such factors together with the effect on the fall of condensed water, all such factors can be made satisfactory by setting the gap ratio H/P in the range of 0.75-0.90.

Description

【発明の詳細な説明】 産業上の利用分野 この発明は、カーエヤコン等に用いられるエバボレータ
に閣する。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application This invention relates to an evaporator used in car air conditioners and the like.

従来の技術 エバボレータでは、空気を冷却する際に、空気中の水分
が凝縮し、凝縮した水分は水滴となってフィンに付着す
る。フィンに付着した水滴は、その自重により落下し排
水されるが、排水性を向上させる手段として、フィンの
表面に化学的な親水性処理を施すことがあった。
In conventional technology evaporators, when air is cooled, moisture in the air condenses, and the condensed moisture forms water droplets that adhere to the fins. Water droplets adhering to the fins fall due to their own weight and are drained, but as a means to improve drainage, the surfaces of the fins have sometimes been chemically treated to make them hydrophilic.

ところで、フィンにはルーバが形戊されているが、ルー
バの形状は、エバボレータの冷却性能の向上を図ること
、圧力損失の上昇を抑制すること等を主眼として決めら
れており、水滴の排水性については考慮されていなかっ
た。
Incidentally, the fins are shaped with louvers, and the shape of the louvers was determined with the main objectives of improving the cooling performance of the evaporator and suppressing the increase in pressure loss, and the shape of the louvers was determined with the main objectives of improving the cooling performance of the evaporator and suppressing the increase in pressure loss. was not considered.

発明が解決しようとする課題 この発明の目的は、エバボレータの冷却性能の向上を図
ること、圧力損失の上昇を抑制することに加えて、水滴
の排水性の良好なエバポレータを提供することにある。
Problems to be Solved by the Invention An object of the present invention is to improve the cooling performance of the evaporator, to suppress an increase in pressure loss, and to provide an evaporator with good drainage of water droplets.

課題を解決するための手段 この発明によるエバボレータは、コルゲートフィンの各
平坦部に、これの巾方向にのびたルーバが並列状に形威
され、コルゲートフィンの平坦部のピッチをPとし、ル
ーバの高さをHとしたときに、H / P − 0.7
5〜0,90であることを特徴とするものである。
Means for Solving the Problems In the evaporator according to the present invention, louvers extending in the width direction of the corrugated fins are formed in parallel on each flat part of the corrugated fins, the pitch of the flat parts of the corrugated fins is P, and the height of the louvers is When S is H, H / P - 0.7
5 to 0.90.

実  施  例 この発明の実施例を、図面を参照して次に説明する。Example Embodiments of the invention will now be described with reference to the drawings.

エバポレータは、第3図に示すように、並列状冷媒通路
1lを有するアルミニウム押出型材製蛇行状偏平管l2
と、偏平管l2の隣り合う直管部同じの間に介在されて
いるアルミニウムブレージングシ一ト製ルーバ付コルゲ
ートフィンL3と、偏平管12の両端部にそれぞれ設け
られている入口ヘッダl4および出口ヘツダ15とを備
えている。
As shown in Fig. 3, the evaporator consists of a serpentine flat tube l2 made of extruded aluminum and having a parallel refrigerant passage l2.
, a louvered corrugated fin L3 made of an aluminum brazing sheet interposed between adjacent straight pipe parts of the flat pipe 12, and an inlet header l4 and an outlet header provided at both ends of the flat pipe 12, respectively. 15.

偏甲管12およびフィン13の表面には親水性皮膜処理
が施されている。
The surfaces of the canal 12 and the fins 13 are treated with a hydrophilic film.

コルゲートフィン13は、第4図に詳しく示すように、
並列状平坦部2lと、隣り合う平坦部2lの同じ側の端
部同しを連絡しているU字状屈曲部22とよりなる。各
平坦部21には、これの111方向の全長にわたっての
びたルーバ23が並列状に形成されている。隣り合うル
ーバ23同じの間には、ルーバ23の切起しにより生じ
たスリット24が形成されている。第5図に示すように
、各平坦部2lに形成されたルーバ23は4つの群81
〜S4に分けられ、各群S1〜S4のルーバ23の向き
は1つ置きに同じになっている。
As shown in detail in FIG. 4, the corrugated fin 13 is
It consists of parallel flat portions 2l and a U-shaped bent portion 22 connecting the ends of the adjacent flat portions 2l on the same side. Louvers 23 extending over the entire length in the 111 direction are formed in parallel on each flat portion 21. A slit 24 is formed between adjacent louvers 23 by cutting and raising the louvers 23. As shown in FIG. 5, the louvers 23 formed on each flat portion 2l are divided into four groups 81.
- S4, and the orientation of every other louver 23 in each group S1 to S4 is the same.

第1図に、フィン設計上の重要な因子が示されているが
、これはつぎのとおりである。
FIG. 1 shows important factors in fin design, which are as follows.

P:フィンの平坦部のピッチ 關 θ:ルーバの角度 d e g. W:ルーバの山  車 H:ルーバの高さ 關 G:ルーバ間のギャップ(P−H)  ■上記コルゲー
トフィンにおいて、凝縮水は、スリット24を通って上
側の平坦部2lから下側の平坦部2lに流れ落ちるため
、ピッチPが小さいほど凝縮水が流れ落ちやすい。した
がって、ルーバ23の高さHが一定である場合、ルーバ
23間のギャップGが小さいほどビッチPが小さく、凝
縮水が落下しやすいことになる。
P: Pitch of flat part of fin θ: Angle of louver d e g. W: Mountain of the louver Wheel H: Height of the louver G: Gap between the louvers (P-H) ■In the above corrugated fin, condensed water passes through the slit 24 from the upper flat part 2l to the lower flat part. Since the condensed water flows down to 2L, the smaller the pitch P, the easier the condensed water will flow down. Therefore, when the height H of the louvers 23 is constant, the smaller the gap G between the louvers 23, the smaller the pitch P, and the easier the condensed water will fall.

上記因子の好ましい具体的数値はつぎの通りである。す
なわち、P−1.8〜2.2、θ一28〜38、W−2
.3〜2,7であることが好ましい。また、ルーバの高
さはHmW−tan(θ)の式により算出される。
Preferred specific values of the above factors are as follows. That is, P-1.8 to 2.2, θ-28 to 38, W-2
.. It is preferable that it is 3-2.7. Further, the height of the louver is calculated by the formula HmW-tan(θ).

そこで、フィンの設計の目安となるもう1つの因子とし
て、ギャップ率一H/Pと定義すると、ギャップ率が大
きい程、凝縮水落下の効果が大きいことになる。
Therefore, if we define gap ratio - H/P as another factor that serves as a guideline for fin design, the larger the gap ratio, the greater the effect of condensed water falling.

上記各因子の具体的数値をまとめて整理すると、表1の
とおりとなる。
Table 1 shows the specific numerical values of each of the above factors.

(以下余白) 表1 以上、ギャップ率について、凝縮水落下の効果について
のみ検討したが、エバボレータの性能としては、冷却性
能および圧力損失もまた重要な要素である。これらの要
素を凝縮水落下の効果とともにギャップ率についてまと
めものが、第2図に示すグラフである。グラフ中のデー
タは、つぎの仕様のエバボレータについて実測したもの
である。すなわち、エバボレータの巾Aは32Clam
,高さBは23Cl+++s,奥行きCは90闘である
(第3図参照)。上記仕様は必要に応じて変更されるが
、そのうち、とくに奥行きCは65〜110+a璽であ
ることが好ましい。
(Margins below) Table 1 In the above, only the effect of condensed water falling has been considered regarding the gap ratio, but cooling performance and pressure loss are also important factors for the performance of the evaporator. The graph shown in FIG. 2 summarizes these factors regarding the effect of condensed water falling and the gap ratio. The data in the graph was actually measured for an evaporator with the following specifications. That is, the width A of the evaporator is 32 Clams.
, the height B is 23Cl+++s, and the depth C is 90cm (see Figure 3). Although the above specifications may be changed as necessary, it is particularly preferable that the depth C is 65 to 110+a.

第2図からあきらかなように、ギャップ率H/ P −
 0.75〜0.90の範囲であれば、全ての要素を満
足することが判る。
As is clear from Fig. 2, the gap ratio H/P −
It can be seen that a range of 0.75 to 0.90 satisfies all the elements.

以上、各因子を総合的にまとめると、ルーバ巾Wを大き
くとった場合はルーバ角度θを小さく設定し、ルーバ巾
Wを小さくとった場合はルーバ角度θを小さくとってピ
ッチPを詰めるか、あるいはルーバ角度θを大きくとっ
てピッチPを拡げるように設定すればよい。
To summarize each factor above, if the louver width W is set large, the louver angle θ should be set small, and if the louver width W is set small, the louver angle θ should be set small to reduce the pitch P. Alternatively, the pitch P may be set to be wider by increasing the louver angle θ.

第6図に、上記エバボレータとは別のタイプのエバボレ
ータが示されている。すなわち、このエバボレータは、
並列状偏平管3iと、隣り合う偏平管31同じの間に介
在されているコルゲートフィン32とを備えている。各
悶平管31は、略樋状にプレス成形した2枚のプレージ
ングシ一ト33を重ね合せて接合することにより、両シ
ート33間に冷媒通路を形成したものである。偏平管3
lの上部には、膨出部34が設けられており、隣り合う
膨出部34同しを連通状に接合することにより、ヘッダ
タンク部35が設けられている。
FIG. 6 shows an evaporator of a different type from the evaporator described above. In other words, this evaporator is
It includes parallel flat tubes 3i and corrugated fins 32 interposed between adjacent flat tubes 31. Each plating tube 31 is formed by overlapping and joining two plating sheets 33 press-molded into a generally gutter shape to form a refrigerant passage between the two sheets 33. Flat tube 3
A bulging portion 34 is provided at the upper part of the tank l, and a header tank portion 35 is provided by joining adjacent bulging portions 34 in a communicating manner.

ヘッダタンク部35には入口管36および出口管37が
接続されている。コルゲートフィン32は、上記第3図
のエバボレータのフィンエ3と同じものである。
An inlet pipe 36 and an outlet pipe 37 are connected to the header tank section 35 . The corrugated fins 32 are the same as the fins 3 of the evaporator shown in FIG. 3 above.

発明の効果 この発明によれば、エバボレータの冷却性能の向上を図
ること、圧力損失の上昇を抑制することに加えて、水滴
の排水性の良好なエバボレ−タが提供される。
Effects of the Invention According to the present invention, an evaporator is provided which not only improves the cooling performance of the evaporator and suppresses an increase in pressure loss, but also has good water droplet drainage performance.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図はこの発明によるエバボレータのフィンの説明図
、第2図はエバボレータの性能を示すグラフである。 第3図はエバボレータ全体の゛斜視図、第4図はフィン
の一部を拡大して示す正面図、第5図はフィンの一部の
縦断面図である。 第6図は他のエバボレータの全体の斜視図である。 l3・・・フィン、2l・・・フィン平坦部、23・・
・ルーバ、P・・・フィン平坦部のピッチ、H・・・ル
ーバの高さ。 以  上 第IvA く 1 ギャップ率% 7J2図
FIG. 1 is an explanatory diagram of the fins of the evaporator according to the present invention, and FIG. 2 is a graph showing the performance of the evaporator. FIG. 3 is a perspective view of the entire evaporator, FIG. 4 is an enlarged front view of a portion of the fin, and FIG. 5 is a longitudinal sectional view of a portion of the fin. FIG. 6 is an overall perspective view of another evaporator. l3...Fin, 2l...Fin flat part, 23...
- Louver, P...Pitch of fin flat part, H...Height of louver. Above Chapter IvA 1 Gap rate % Figure 7J2

Claims (1)

【特許請求の範囲】 コルゲートフィンの各平坦部に、これの巾方向にのびた
ルーバが並列状に形成され、コルゲートフィンの平坦部
のピッチをPとし、ルーバの高さをHとしたときに、 H/P=0.75〜0.90である ことを特徴とするエバポレータ。
[Claims] Louvers extending in the width direction of each flat part of the corrugated fin are formed in parallel, and when the pitch of the flat part of the corrugated fin is P and the height of the louver is H, An evaporator characterized in that H/P=0.75 to 0.90.
JP2074224A 1989-03-31 1990-03-22 Evaporator for car air conditioner Expired - Fee Related JP2887495B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2074224A JP2887495B2 (en) 1989-03-31 1990-03-22 Evaporator for car air conditioner

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP8274689 1989-03-31
JP1-82746 1989-03-31
JP2074224A JP2887495B2 (en) 1989-03-31 1990-03-22 Evaporator for car air conditioner

Publications (2)

Publication Number Publication Date
JPH0320576A true JPH0320576A (en) 1991-01-29
JP2887495B2 JP2887495B2 (en) 1999-04-26

Family

ID=26415347

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2074224A Expired - Fee Related JP2887495B2 (en) 1989-03-31 1990-03-22 Evaporator for car air conditioner

Country Status (1)

Country Link
JP (1) JP2887495B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05149649A (en) * 1991-11-29 1993-06-15 Showa Alum Corp Evaporator
US7597490B2 (en) 2000-04-24 2009-10-06 Ricoh Company, Ltd. Camera and a portable apparatus having a flat body
CN104142037A (en) * 2014-08-08 2014-11-12 鑫田集团有限公司 Parallel-flow micro-channel evaporator for automobile air-conditioning system

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05149649A (en) * 1991-11-29 1993-06-15 Showa Alum Corp Evaporator
US7597490B2 (en) 2000-04-24 2009-10-06 Ricoh Company, Ltd. Camera and a portable apparatus having a flat body
CN104142037A (en) * 2014-08-08 2014-11-12 鑫田集团有限公司 Parallel-flow micro-channel evaporator for automobile air-conditioning system

Also Published As

Publication number Publication date
JP2887495B2 (en) 1999-04-26

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