JPS63254396A - Finned heat exchanger - Google Patents

Finned heat exchanger

Info

Publication number
JPS63254396A
JPS63254396A JP9028487A JP9028487A JPS63254396A JP S63254396 A JPS63254396 A JP S63254396A JP 9028487 A JP9028487 A JP 9028487A JP 9028487 A JP9028487 A JP 9028487A JP S63254396 A JPS63254396 A JP S63254396A
Authority
JP
Japan
Prior art keywords
cut
fin
fins
raised
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.)
Granted
Application number
JP9028487A
Other languages
Japanese (ja)
Other versions
JP2523618B2 (en
Inventor
Osao Kido
長生 木戸
Shinji Fujimoto
藤本 眞嗣
Hachiro Koma
小間 八郎
Shinichi Ide
井手 晋一
Hiroaki Kase
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

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 completely divide growth of a temperature boundary layer and to enable maintenance of a heat transfer rate between an air flow and a fin at a high value, by a method wherein a cut-rise surface extending in parallel to the direction of an air flow is formed in a fin surface, and the height of the cut rise is changed in a stepped manner to form a meandering pattern. CONSTITUTION:Fins 5 are fixed in a corrugated manner to a heat transfer pipe 4 at intervals of a fin pitch. Cut rise surfaces 6 formed on both surfaces of the fin 5 are formed so as to extend in parallel to the direction of an air flow B. The height of the cut-rise surface 6 from the fin 5 is set to values in two stages of the one being 1/5 of a fin pitch and the other being 2/5 of the fin pitch. The cut-rise surface 6 in a five-stage is changed by 1/5 of a fin pitch at each stage to form a meandering pattern. Since, during heat exchange, an air flow B flows a flow passage where increase and decrease in a distance between the fins are repeated, a pressure difference is produced between both surfaces of the fin 5, and by dividing growth of the temperature boundary layer of the air flow B generated on the cut-rise surface 6, a heat transfer rate can be maintained at a high value.

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。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a finned heat exchanger used in air conditioning equipment, refrigeration equipment, etc.

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。
BACKGROUND OF THE INVENTION In recent years, the performance of finned heat exchangers has improved markedly, and finned heat exchangers equipped with corrugated fins characterized by a large heat transfer area on the air side 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 mentioned above will be explained 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1直管部1′を
ほぼ平行に備えてし)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の表面に気流入方向と平行に設けられた切り
起こし面で、フィン2の両面から気流入方向で連続して
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−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 Figures 4 to 6,
Reference numeral 1 denotes a flat heat exchanger tube bent in a meandering manner, with straight tube portions 1' substantially parallel to each other. Fins 2 are provided between the opposing straight pipe portions 1' of the heat exchanger tube 1, and are fixed to the heat exchanger tube 1 in a wave shape with a fin pitch Pa at a constant interval. 3
is a cut-and-raised surface provided on the surface of the fin 2 parallel to the air inflow direction, which is cut and raised continuously from both sides of the fin 2 in the air inflow direction alternately up and down with a width Wa, and is provided on the surface of the fin 2 with a width Wa. They are all formed in the same direction with the same cut-and-raise pattern.

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4図から第7図を用いてその動作を説明する。
The operation of the finned heat exchanger constructed as 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が気流入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Ja
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 airflow A flowing between the fins of the fins 2 and the heat medium flowing inside the heat exchanger tube 1 via the fins 2 and the heat exchanger tube 1. At that time, a cut and raised surface 3 is provided on the surface of the fin 2, and the temperature boundary Ja of the airflow A generated on the surface of the fin 2 because the fin 2 is divided in the air inflow direction.
This suppresses the development of fins 2 and improves the heat transfer coefficient between the airflow A and the fins 2.

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。
Problems to be Solved by the Invention However, in the above configuration, as shown in FIG.
The temperature boundary layer a traces its tail to the cut-and-raised surface 3 on the downstream side and is not divided, and the temperature boundary layer a gradually develops as it goes downstream. The problem was that the heat transfer coefficient decreased.

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 addresses the above problems and maintains a high heat transfer coefficient with the airflow throughout the entire area from the upstream fins to the downstream fins,
The present invention provides a finned heat exchanger with 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t!:arり返したフ
ィン問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-mentioned problems, the finned heat exchanger of the present invention has a cut-and-raised surface parallel to the direction of the airflow passing between the fins, which is continuously cut from the fin surface in the direction of the airflow. The cut-and-raised height of the cut-and-raised surface from the fin surface is changed stepwise in multiple steps in the airflow direction to meander, and the distance between the fins is expanded/reduced in the airflow direction. : It is equipped with a configuration in which a reversible fin flow path is provided.

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 The present invention has the above-described configuration, and since the inter-fin flow path repeatedly expands and contracts, a pressure difference is generated on both sides of the fins when the airflow passes between the fins. A part of the airflow is condensed and flows into the gap between the surfaces, and this condensed flow completely disrupts the development of the temperature boundary layer of the airflow that occurs on the surface of the cut-up surface, and the gap between the airflow and the fins. This means that the heat transfer coefficient 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 Hereinafter, a finned heat exchanger according to an example of the present invention will be described 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。
FIG. 1 and FIG. 2 show the fin shape of a finned heat exchanger in an embodiment of the present invention.

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。
In FIGS. 1 and 2, reference numeral 4 denotes a heat transfer tube, which has the same structure as the conventional example, and includes a straight tube portion 4'.

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ルb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f!:流れる気IB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hl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。
Fins 5 are provided between the straight pipe portions 4' of the heat exchanger tube 4, and are fixed to the heat exchanger tube 4 in a wave shape at constant fin pitch b intervals. 6 is a cut-and-raised surface provided on both sides of the fins 5, and f! : It is cut and raised from the surface of the fin 5 with a width wb so as to be parallel to the flowing air IB direction, and the cut and raised heights hl and h2 of the cut and raised surface 6 from the fin 5 are respectively 5 of the fin pitch pb on both sides. The cut-and-raised surface 6 is formed in two steps of 1/5 and 2/5, and the 5-step cut-and-raised surface 6 including the remaining fins 5' without being cut and raised is 1/5 of the fin pitch pb.
A serpentine pattern shown by a polygonal line m is formed while changing the dimensions of .

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である。
In addition, the arrangement pattern of the cut and raised surfaces 6 is arranged to be symmetrical across the inter-fin center line n between the adjacent fins 5, and the distance between the fins with the adjacent fins repeats expansion and contraction. This forms a flow path.

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
The operation of the finned heat exchanger configured as above will be explained 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
度境界層す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!f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 of the fins 5 and the heat medium flowing within the heat exchanger tubes 4 via the fins 5 and the heat exchanger tubes 4. At this time, since the airflow B flows through the inter-fin flow path in which the distance between the fins has been repeatedly expanded and contracted, a pressure difference is generated on both sides of the fins 5, and this pressure difference causes the cut-and-raised surfaces 6 to be arranged in a step-like manner. A part of the airflow B flows into the gap S between them in a contracted flow, and this contracted flow completely interrupts the development of the temperature boundary layer of the airflow B generated on the surface of the cut and raised surface 6. , heat transfer between fin 5 and airflow B! f can be maintained 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。
In addition, since the gaps S between the cut and raised surfaces 6 are all formed to have the same size, and the flow paths between the fins are also symmetrical in the direction of the airflow B, the air condenses uniformly in every gap S. Which cut-and-raised surface 6
Almost uniform heat transfer coefficient can also be obtained.

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、上流か
ら下流に至るまでフィンと気流との間の熱伝達率を極め
て高く維持し、熱交換性能の優れたフィン付熱交換器を
得ることができる。
Effects of the Invention As described above, the present invention provides a cut-and-raised surface that is parallel to the direction of airflow passing between the fins and is continuously cut and raised from the fin surface in the airflow direction, and that the cut-and-raised surface is cut and raised from the fin surface. By creating an inter-fin flow path in which the height is changed stepwise in multiple steps in the airflow direction and the distance between the fins is repeatedly expanded and contracted in the airflow direction, the fins and airflow are connected from upstream to downstream. It is possible to obtain a finned heat exchanger with excellent heat exchange performance by maintaining an extremely high heat transfer coefficient between the fins.

【図面の簡単な説明】[Brief explanation 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8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。 5−−−フィン 第 2 図                  Δ−
−−切っ起;し面b 第3図 第4図 第5図 第 6 図
Fig. 1 is a perspective view of a main part showing the fin shape of a finned heat exchanger according to an embodiment of the present invention, Fig. 2 is a sectional view of a main part of Fig. 1, and Fig. 8 is a temperature of the air flow in Fig. 1. FIG. 4 is a sectional view of the main part showing the state of the boundary layer, FIG. 4 is a perspective view showing the schematic shape of the finned heat exchanger according to the present invention, and FIG. 5 is the main part showing the fin shape of the conventional finned heat exchanger. 6 is a sectional view of the main part of FIG. 5, and FIG. 7 is a sectional view of the main part showing the state of the temperature boundary layer of the air flow in FIG. 5. 4... Heat exchanger tube, 5... Fin, 6... Cut and raised surface. 5--Fin Fig. 2 Δ-
--Cut and raised surface b Fig. 3 Fig. 4 Fig. 5 Fig. 6

Claims (3)

【特許請求の範囲】[Claims] (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 exchanger tube and a fin fixed to the heat exchanger tube are provided, and a cut-and-raised surface parallel to the direction of airflow passing between the fins is continuously cut and raised from the surface of the fin in the direction of the airflow, and the The height of the cut and raised surface from the fin surface is changed in multiple steps in the airflow direction to create a meandering flow path between the fins, which repeatedly expands and contracts the distance between the fins in the airflow direction. Heat exchanger with fins.
(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) The cut-and-raised pattern of the cut-and-raised surface is provided line-symmetrically between adjacent fins across the center line between the fins,
2. The finned heat exchanger according to claim 1, wherein the fin-to-fin flow passages are symmetrical in the air flow direction.
(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
さを階段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 cut-and-raised height of the cut-and-raised surface from both sides of the fin is formed in two steps on each side, and the fin surface that is not cut-and-raised is also included to form a cut-and-raised surface of 5 steps on both sides, and the fin pitch is 3. The finned heat exchanger according to claim 1, wherein the cut-and-raised height is changed in steps of one-fifth of the dimension.
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 true JPS63254396A (en) 1988-10-21
JP2523618B2 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)

Cited By (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
CN103502765A (en) * 2011-10-19 2014-01-08 松下电器产业株式会社 Heat exchanger
CN104089517A (en) * 2014-07-18 2014-10-08 丹佛斯微通道换热器(嘉兴)有限公司 Fin used for heat exchanger and heat exchanger with same

Citations (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

Patent Citations (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

Cited By (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
CN103502765A (en) * 2011-10-19 2014-01-08 松下电器产业株式会社 Heat exchanger
CN104089517A (en) * 2014-07-18 2014-10-08 丹佛斯微通道换热器(嘉兴)有限公司 Fin used for heat exchanger and heat exchanger with same

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