JP2523618B2 - Heat exchanger with fins - Google Patents

Heat exchanger with fins

Info

Publication number
JP2523618B2
JP2523618B2 JP62090284A JP9028487A JP2523618B2 JP 2523618 B2 JP2523618 B2 JP 2523618B2 JP 62090284 A JP62090284 A JP 62090284A JP 9028487 A JP9028487 A JP 9028487A JP 2523618 B2 JP2523618 B2 JP 2523618B2
Authority
JP
Japan
Prior art keywords
fins
cut
raised
fin
heat exchanger
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.)
Expired - Lifetime
Application number
JP62090284A
Other languages
Japanese (ja)
Other versions
JPS63254396A (en
Inventor
長生 木戸
眞嗣 藤本
八郎 小間
晋一 井手
広明 加瀬
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Refrigeration Co
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 Matsushita Refrigeration Co filed Critical Matsushita Refrigeration Co
Priority to JP62090284A priority Critical patent/JP2523618B2/en
Publication of JPS63254396A publication Critical patent/JPS63254396A/en
Application granted granted Critical
Publication of JP2523618B2 publication Critical patent/JP2523618B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • F28D1/053Heat-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 straight
    • F28D1/0535Heat-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 straight the conduits having a non-circular cross-section
    • F28D1/05366Assemblies of conduits connected to common headers, e.g. core type radiators
    • F28D1/05383Assemblies of conduits connected to common headers, e.g. core type radiators with multiple rows of conduits or with multi-channel conduits
    • 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

Description

【発明の詳細な説明】 産業上の利用分野 本発明は空調機器や冷凍機器等に用いられるフィン付
熱交換器に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat exchanger with fins used in air conditioners, refrigeration equipment and the like.

従来の技術 近年、フィン付熱交換器の性能向上は目覚ましいもの
があり、空気側伝熱面積が大きいことを特徴とする波形
状フィンを備えたフィン付熱交換器が既に実用化されて
いる。
2. Description of the Related Art In recent years, the performance of finned heat exchangers has been remarkably improved, and finned heat exchangers having corrugated fins having a large air-side heat transfer area have already been put into practical use.

以下、図面を参照しながら上述した従来のフィン付熱
交換器について説明を行う。
Hereinafter, the conventional finned heat exchanger will be described with reference to the drawings.

第4図は本発明に係わるフィン付熱交換器の概略形状
を示し、第5図、第6図は従来のフィン付熱交換器のフ
ィン形状を示すものである。第4図から第6図におい
て、1は蛇行状に屈曲した偏平状の伝熱管で、直管部
1′をほぼ平行に備えている。2は伝熱管1の向かい合
う直管部1′相互間に設けられたフィンで、波形状に一
定間隔のフィンピッチPaで伝熱管1に固定されている。
3はフィン2の表面に気流A方向と平行に設けられた切
り起こし面で、フィン2の両面から気流A方向で連続し
て上下互い違いに幅Waで切り起こして設けられ、かつ隣
接するフィン2′もすべて同一切り起こしパターンで同
一方向に形成されている。
FIG. 4 shows a schematic shape of a finned heat exchanger according to the present invention, and FIGS. 5 and 6 show fin shapes of a conventional finned heat exchanger. In FIGS. 4 to 6, reference numeral 1 is a flat heat transfer tube bent in a meandering shape and provided with straight pipe portions 1 ′ substantially in parallel. Reference numeral 2 denotes fins provided between the straight tube portions 1 ′ facing each other of the heat transfer tube 1, which are fixed to the heat transfer tube 1 at a fin pitch Pa having a wave shape at regular intervals.
Reference numeral 3 denotes a cut-and-raised surface provided on the surface of the fin 2 in parallel with the airflow A direction. ′ Are also formed in the same direction with the same cut and raised pattern.

以上のように構成されたフィンは付熱交換器につい
て、以下第4図から第7図を用いてその動作を説明す
る。
The operation of the heat exchanger with the fin configured as described above will be described below with reference to FIGS. 4 to 7.

フィン2のフィン間を流れる気流Aと伝熱管1の管内
を流れる熱媒体との間でフィン2及び伝熱管1を介して
熱交換が行われる。その際、フィン2の表面に切り起こ
し面3が設けられ、フィン2が気流A方向で分断されて
いるためにフィン2の表面に生じる気流Aの温度境界層
aの発達が抑えられ、気流Aとフィン2との熱伝達率の
向上が図られている。
Heat exchange is performed between the fins 2 and the heat transfer tubes 1 between the airflow A flowing between the fins 2 and the heat medium flowing in the heat transfer tubes 1. At that time, since the cut-and-raised surface 3 is provided on the surface of the fin 2 and the fin 2 is divided in the direction of the air flow A, the development of the temperature boundary layer a of the air flow A generated on the surface of the fin 2 is suppressed, and the air flow A The heat transfer coefficient between the fins 2 and the fins 2 is improved.

発明が解決しようとする問題点 しかしながら上記のような構成では、第7図に示すよ
うに、上流側の切り起こし面3によって形成された気流
Aの温度境界層aは下流側の切り起こし面3まで尾を引
いて分断されず、下流側へ行くほど前記温度境界層aは
徐々に発達し、下流側へ行くほどフィン2と気流Aとの
熱伝達率が低下するという問題点を有していた。
DISCLOSURE OF THE INVENTION Problems to be Solved by the Invention However, in the above-described configuration, as shown in FIG. 7, the temperature boundary layer a of the air flow A formed by the cut-and-raised surface 3 on the upstream side has the cut-and-raised surface 3 on the downstream side. The temperature boundary layer a gradually develops toward the downstream side, and the heat transfer coefficient between the fins 2 and the air flow A decreases toward the downstream side. It was

本発明は上記問題点に絡み、上流側フィンから下流側
フィンに至るまで全域で気流との熱伝達率を高く維持
し、熱交換性能の優れたフィン付熱交換器を提供するも
のである。
The present invention is concerned with the above problems, and provides a heat exchanger with fins, which maintains a high heat transfer coefficient with an airflow in the entire region from the upstream fins to the downstream fins and has excellent heat exchange performance.

問題点を解決するための手段 上記問題点を解決するために本発明のフィン付熱交換
器は、フィン間を通過する気流方向と平行な切り起こし
面をフィン表面から気流方向に連続して切り起こして設
け、前記切り起こし面のフィン方面からの切り起こし高
さを気流方向で多段階に階段状に変化させて蛇行させ、
気流方向でフィン間距離の拡大縮小を繰り返したフィン
間流路を設けるという構成を備えたものである。
Means for Solving the Problems In order to solve the above problems, the heat exchanger with fins of the present invention is configured such that a cut and raised surface parallel to the air flow direction passing between fins is continuously cut from the fin surface in the air flow direction. It is provided upright, and the cut and raised height from the fin direction of the cut and raised surface is made to meander by changing in a stepwise manner in multiple steps in the air flow direction,
It is provided with a configuration in which a flow path between fins is provided by repeatedly expanding and reducing the distance between fins in the air flow direction.

作用 本発明は上記した構成によって、フィン間流路が拡大
縮小を繰り返しているために、気流がフィン間を通過す
る際にフィンの両面で圧力差を生じるので、階段状に形
成された切り起こし面間の隙間に気流の一部が縮流され
て流れ込み、この縮流された流れによって切り起こし面
表面に生じる気流の温度境界層の発達が完全に分断さ
れ、気流とフィンとの間の熱伝達率を極めて高く維持で
きることとなる。
Effect According to the present invention, since the flow path between fins is repeatedly expanded and contracted by the above-described configuration, a pressure difference is generated on both sides of the fin when the airflow passes between the fins. A part of the airflow is contracted and flows into the gap between the surfaces, and the contracted flow completely cuts off the development of the temperature boundary layer of the airflow generated on the surface of the surface, and the heat between the airflow and the fins is cut off. The transmission rate can be maintained extremely high.

実施例 以下本発明の一実施例のフィン付熱交換器について図
面を参照しながら説明する。
Example A heat exchanger with fins according to an example of the present invention will be described below with reference to the drawings.

第1図、第2図は本発明の一実施例におけるフィン付
熱交換器のフィン形状を示すものである。第1図、第2
図において、4は伝熱管で従来例の構成と同じものであ
り、直管部4′を備えている。5は伝熱管4の直管部
4′相互間に設けられたフィンで、波形状に一定のフィ
ンピッチpb間隔で伝熱管4に固定されている。6はフィ
ン5の両面に設けられた切り起こし面で、フィン5間を
流れる気流B方向と平行となるようにフィン5表面から
幅wbで切り起こして設けられ、かつ切り起こし面6のフ
ィン5からの切り起こし高さh1及びh2は両面共にそれぞ
れフィンピッチPbの5分の1及び5分の2の2段階に形
成され、切起こさずに残ったフィン5′を含めた5段階
の切り起こし面6はフィンピッチPbの5分の1の寸法ず
つ変化しながら折れ線mで示した蛇行状パターンを形成
している。また、切り起こし面6の配列パターンは隣接
するフィン5とのフィン間中心線nを挟んで線対称とな
るように設けられてあり、隣接するフィンとのフィン間
距離が拡大縮小を繰り返すフィン間流路を形成してあ
る。
1 and 2 show the fin shape of the finned heat exchanger in one embodiment of the present invention. 1 and 2
In the figure, reference numeral 4 denotes a heat transfer tube having the same structure as that of the conventional example and provided with a straight tube portion 4 '. Reference numeral 5 is a fin provided between the straight pipe portions 4'of the heat transfer tube 4, and is fixed to the heat transfer tube 4 in a wave shape at a constant fin pitch pb interval. Reference numeral 6 is a cut-and-raised surface provided on both sides of the fin 5, and is provided by cutting and raised from the surface of the fin 5 with a width wb so as to be parallel to the air flow B direction flowing between the fins 5, and the fin 5 of the cut-and-raised surface 6 The cut-and-raised heights h1 and h2 are formed in two steps of 1/5 and 2/5 of the fin pitch Pb on both sides, respectively. The surface 6 forms a meandering pattern indicated by a polygonal line m while changing by a dimension of 1/5 of the fin pitch Pb. Further, the arrangement pattern of the cut-and-raised surfaces 6 is provided so as to be line-symmetrical with the center line n between the fins with the adjacent fins 5 interposed therebetween, and the distance between the fins with the adjacent fins is between the fins which repeats expansion and contraction. A flow path is formed.

以上のように構成されたフィン付熱交換器について、
以下第1図から第3図を用いてその動作について説明す
る。
Regarding the finned heat exchanger configured as described above,
The operation will be described below with reference to FIGS. 1 to 3.

フィン5のフィン間を流れる気流Bと伝熱管4の管内
を流れる熱媒体との間でフィン5及び伝熱管4を介して
熱交換が行われる。その際、フィン間距離の拡大縮小を
繰り返したフィン間流路を気流Bが流れるために、フィ
ン5の両面で圧力差を生じることとなり、この圧力差に
よって階段状に配列された切り起こし面6間の隙間sに
気流Bの一部が縮流されて流れ込むこととなり、この縮
流された流れが切り起こし面6の表面に生じる気流Bの
温度境界層bの発達を完全に分断することとなり、フィ
ン5と気流Bとの間の熱伝達率を極めて高く維持するこ
とができる。
Heat exchange is performed between the airflow B flowing between the fins 5 and the heat medium flowing in the heat transfer tubes 4 via the fins 5 and the heat transfer tubes 4. At that time, since the airflow B flows through the inter-fin flow path in which the inter-fin distance is repeatedly expanded and contracted, a pressure difference is generated on both sides of the fin 5, and the cut-raised surfaces 6 arranged in a stepwise manner due to this pressure difference. A part of the airflow B is contracted and flows into the gap s between them, and this contracted flow completely divides the development of the temperature boundary layer b of the airflow B generated on the surface of the cut and raised surface 6. The heat transfer coefficient between the fins 5 and the air flow B can be kept extremely high.

また前記切り起こし面6間の隙間sはすべて同一寸法
となるように形成され、かつフィン間流路も気流B方向
で左右対称形状となっているので、どの隙間sにも均一
に縮流された流れを得ることができ、どの切り起こし面
6にもほぼ均一な熱伝達率を得ることができる。
Further, all the gaps s between the cut-and-raised surfaces 6 are formed to have the same size, and the flow paths between the fins are also symmetrical in the direction of the air flow B, so that all the gaps s are uniformly contracted. A uniform flow can be obtained, and a substantially uniform heat transfer coefficient can be obtained on any of the cut and raised surfaces 6.

発明の効果 以上のように本発明は、フィン間を通過する気流方向
と平行な切り起こし面をフィン表面から気流方向に連続
して切り起こして設け、前記切り起こし面のフィン表面
からの切り起こし高さを気流方向で多段階に階段状に変
化させて蛇行させ、気流方向でフィン間距離の拡大縮小
を繰り返したフィン間流路を形成することにより、気流
がフィン間を通過する際にフィンの両面で圧力差を生じ
るので、階段状に形成された切り起こし面間の隙間に気
流の一部が縮流されて流れ込み、この縮流された流れに
よって切り起こし面表面に生じる気流の温度境界層の発
達が完全に分断され、気流とフィンとの間の熱伝達率を
極めて高く維持できる。
EFFECTS OF THE INVENTION As described above, according to the present invention, a cut-and-raised surface parallel to the airflow direction passing between fins is continuously cut and raised from the fin surface in the airflow direction, and the cut-and-raised surface is cut and raised from the fin surface. By changing the height in a stepwise manner in multiple steps in the airflow direction to meander and forming a fin-to-fin flow path that repeatedly expands and contracts the inter-fin distance in the airflow direction, fins are formed when the airflow passes between fins. Since a pressure difference is generated on both surfaces of the cut-and-raised surface, a part of the airflow is contracted and flows into the gap between the cut-and-raised surfaces formed in a stepwise manner, and the temperature boundary of the airflow generated on the cut-and-raised surface surface The layer development is completely decoupled and the heat transfer coefficient between the air flow and the fins can be kept very high.

【図面の簡単な説明】[Brief description of drawings]

第1図は本発明の一実施例におけるフィン付熱交換器の
フィン形状を示す要部斜視図、第2図は第1図の要部断
面図、第3図は第1図における気流の温度境界層の状態
を示す要部断面図、第4図は本発明に係わるフィン付熱
交換器の概略形状を示す斜視図、第5図は従来のフィン
付熱交換器のフィン形状を示す要部斜視図、第6図は第
5図の要部断面図、第7図は第5図における気流の温度
境界層の状態を示す要部断面図である。 4……伝熱管、5……フィン、6……切り起こし面。
FIG. 1 is a perspective view of a main part showing a fin shape of a heat exchanger with fins according to an embodiment of the present invention, FIG. 2 is a cross-sectional view of the main part of FIG. 1, and FIG. 3 is a temperature of an air flow in FIG. FIG. 4 is a perspective view showing a schematic shape of a finned heat exchanger according to the present invention, and FIG. 5 is a principal part showing a fin shape of a conventional finned heat exchanger. FIG. 6 is a perspective view, FIG. 6 is a cross-sectional view of an essential part of FIG. 5, and FIG. 4 ... Heat transfer tube, 5 ... Fin, 6 ... Cut and raised surface.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 井手 晋一 東大阪市高井田本通3丁目22番地 松下 冷機株式会社内 (72)発明者 加瀬 広明 東大阪市高井田本通3丁目22番地 松下 冷機株式会社内 (56)参考文献 実開 昭58−21788(JP,U) 実開 昭56−117289(JP,U) 実公 昭62−5582(JP,Y2) ─────────────────────────────────────────────────── ─── Continued Front Page (72) Inventor Shinichi Ide 3-22 Takaida Hondori, Higashi Osaka City Matsushita Refrigerator Co., Ltd. (72) Hiroaki Kase 3-22 Takaida Hondori, Higashi Osaka (56) References Actual Open Sho-58-21788 (JP, U) Actual Open Sho-56-117289 (JP, U) Actual Public Sho-62-5582 (JP, Y2)

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】伝熱管と、前記伝熱管に固定されたフィン
とを備え、前記フィン間を通過する気流方向と平行な切
り起こし面を前記フィン表面から気流方向に連続して切
り起こして設け、前記切り起こし面のフィン表面からの
切り起こし高さを気流方向で多段階に階段状に変化させ
て蛇行させ、気流方向でフィン間距離の拡大縮小を繰り
返したフィン間流路を形成したことを特徴とするフィン
付熱交換器。
1. A heat transfer tube and fins fixed to the heat transfer tube, wherein cut and raised surfaces parallel to the air flow direction passing between the fins are continuously cut and raised from the fin surfaces in the air flow direction. The inter-fin flow path is formed by changing the cut-and-raised height of the cut-and-raised surface from the fin surface in a stepwise manner in a multi-step manner in the airflow direction to meander to repeatedly expand and contract the inter-fin distance in the airflow direction. A heat exchanger with fins.
【請求項2】切り起こし面の切り起こしパターンを隣接
するフィンどうしでフィン間の中心線を挟んで線対称に
設け、気流方向で左右対称なフィン間流路を形成したこ
とを特徴とする特許請求の範囲第1項記載のフィン付熱
交換器。
2. A patent characterized in that a cut-and-raised pattern of a cut-and-raised surface is provided in line symmetry with adjacent fins sandwiching a center line between the fins to form bilaterally symmetrical fin flow paths in the air flow direction. The heat exchanger with fins according to claim 1.
【請求項3】切り起こし面のフィン両面からの切り起こ
し高さを各面で2段階に形成し、切り起こしていないフ
ィン面も合わせて両面で5段の切り起こし面を形成する
と共に、フィンピッチの5分の1の寸法ずつ前記切り起
こし高さを段階状に変化させたことを特徴とする特許請
求の範囲第1項又は第2項記載のフィン付熱交換器。
3. The fins of the cut-and-raised surface are formed in two steps on each surface, and the fin surfaces not cut and raised together form a five-step cut-and-raised surface on both sides, and the fins are formed. The heat exchanger with fins according to claim 1 or 2, wherein the cut-and-raised height is changed stepwise by a dimension of 1/5 of a pitch.
JP62090284A 1987-04-13 1987-04-13 Heat exchanger with fins Expired - Lifetime JP2523618B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62090284A JP2523618B2 (en) 1987-04-13 1987-04-13 Heat exchanger with fins

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62090284A JP2523618B2 (en) 1987-04-13 1987-04-13 Heat exchanger with fins

Publications (2)

Publication Number Publication Date
JPS63254396A JPS63254396A (en) 1988-10-21
JP2523618B2 true JP2523618B2 (en) 1996-08-14

Family

ID=13994218

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62090284A Expired - Lifetime JP2523618B2 (en) 1987-04-13 1987-04-13 Heat exchanger with fins

Country Status (1)

Country Link
JP (1) JP2523618B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102032831A (en) * 2009-09-28 2011-04-27 无锡市鑫盛换热器制造有限公司 Radiating fin
EP2770289A4 (en) * 2011-10-19 2015-03-04 Panasonic Corp Heat exchange apparatus
CN104089517B (en) * 2014-07-18 2016-08-17 丹佛斯微通道换热器(嘉兴)有限公司 Fin and the heat exchanger with this fin for heat exchanger

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56117289U (en) * 1980-02-05 1981-09-08
JPS5821788U (en) * 1981-07-31 1983-02-10 株式会社東芝 Heat exchanger
JPS625582U (en) * 1985-06-26 1987-01-13

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JPS63254396A (en) 1988-10-21

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