JPS6042873B2 - Cylindrical heat pipe heat exchanger - Google Patents

Cylindrical heat pipe heat exchanger

Info

Publication number
JPS6042873B2
JPS6042873B2 JP9833577A JP9833577A JPS6042873B2 JP S6042873 B2 JPS6042873 B2 JP S6042873B2 JP 9833577 A JP9833577 A JP 9833577A JP 9833577 A JP9833577 A JP 9833577A JP S6042873 B2 JPS6042873 B2 JP S6042873B2
Authority
JP
Japan
Prior art keywords
heat
cylindrical
heat exchange
heat exchanger
exchange section
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
Application number
JP9833577A
Other languages
Japanese (ja)
Other versions
JPS5432858A (en
Inventor
達也 小泉
修一 古谷
厚二 松本
健介 唐沢
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.)
Furukawa Electric Co Ltd
Original Assignee
Furukawa Electric Co Ltd
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 Furukawa Electric Co Ltd filed Critical Furukawa Electric Co Ltd
Priority to JP9833577A priority Critical patent/JPS6042873B2/en
Priority to SE7801115A priority patent/SE440274B/en
Priority to GB3811/78A priority patent/GB1596666A/en
Priority to DE2804106A priority patent/DE2804106C2/en
Priority to US05/875,092 priority patent/US4206807A/en
Publication of JPS5432858A publication Critical patent/JPS5432858A/en
Priority to US06/091,949 priority patent/US4327801A/en
Publication of JPS6042873B2 publication Critical patent/JPS6042873B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は熱交換効率を向上せしめた筒型ヒートパイプ
熱交換器に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a cylindrical heat pipe heat exchanger with improved heat exchange efficiency.

従来廃ガスの熱を回収して低温ガスを加熱するヒート
パイプ式のガス−ガス熱交換器としては直方体状のケー
シング内に仕切板を設けて内部を隔離し、この仕切板に
複数本のヒートパイプを貫挿して熱交換部を形成し、こ
の上部を低温ガスが流通する放熱部とし、下部を高温ガ
スが流通する吸熱部としたものがある。
Conventionally, a heat pipe type gas-to-gas heat exchanger that recovers heat from waste gas to heat low-temperature gas has a rectangular parallelepiped-shaped casing with a partition plate to isolate the inside, and a plurality of heat There is one in which a heat exchange part is formed by inserting a pipe, the upper part of which is a heat radiating part through which low-temperature gas flows, and the lower part is a heat absorbing part through which high-temperature gas flows.

しカルながら、このような熱交換器ではガスの流通抵
抗が大きくなるため厚さ方向には限界があり、従つて大
きな熱交換量を得るために幅軸方向に拡大させなければ
ならず、この結実装置が平板状になつてガスの供給が均
一にできなくなる欠点があつた。
However, in such a heat exchanger, there is a limit in the thickness direction due to the large gas flow resistance.Therefore, in order to obtain a large amount of heat exchange, it must be expanded in the width direction. There was a drawback that the fruiting device was shaped like a flat plate, making it impossible to supply gas uniformly.

このため本発明者らは周壁面が渦巻状をなし、且つ渦
の端面を開口した中空円筒体の、前記周壁面の内側に環
状の仕切板を水平に設けて上下にダクトを形成したケー
シング内に、多角形状または円板状の仕切板の上下方向
に複数本のヒートパイプを環状に貫挿した筒型の熱交換
部を装着して、この上部を加熱すべき低温ガスが流通す
る放熱部とし、下部を高温ガスが流通する吸熱部とした
筒型ヒートバイブ熱交換器を開発し、先に提案した。
For this reason, the inventors of the present invention constructed a casing in which an annular partition plate was provided horizontally inside the peripheral wall surface of a hollow cylindrical body with a spiral peripheral wall surface and an open end surface of the vortex to form ducts above and below. A cylindrical heat exchange section in which multiple heat pipes are inserted in an annular manner in the vertical direction of a polygonal or disk-shaped partition plate is installed, and a heat dissipation section through which the low-temperature gas to be heated flows through the upper part. We developed and previously proposed a cylindrical heat-vib heat exchanger with the lower part serving as a heat-absorbing section through which high-temperature gas flows.

しかるにこの熱交換器は小型化することができる反面、
この筒型の熱交換部が渦巻型のケーシング内に装着され
ているため、放熱部側において熱交換部の中央部から熱
交換を終えて外側に向うガスが、ダクト内を回転するガ
スとほぼ直角にぶつかるためダクト内で乱流を生じ圧力
損力が大きくなつて熱交換効率が低下する問題があつた
However, while this heat exchanger can be made smaller,
Since this cylindrical heat exchanger is installed inside a spiral casing, the gas that flows outward after completing heat exchange from the center of the heat exchanger on the heat radiation side is almost the same as the gas rotating inside the duct. Because they collide at right angles, turbulence occurs within the duct, increasing pressure loss and reducing heat exchange efficiency.

本発明はかかる点に鑑み種々研究を行なつた結果、本発
明者らが先に提案した渦巻状のケーシング内に筒型の熱
交換部を装着した筒型ヒートバイブ熱交換器において、
前記筒型熱交換部の放熱部側外周面に、渦の開口端方向
に沿つて傾斜した複数枚の風向ガイド板を設けて、乱流
の発生を抑制するようにした筒型ヒートバイブ熱交換器
を開発したものである。以下本発明を図面に示す実施例
を参照して説明する。
The present invention has been made based on various studies in view of the above points, and as a result, the present inventors have previously proposed a cylindrical heat-vib heat exchanger in which a cylindrical heat exchange section is installed in a spiral casing.
A cylindrical heat-vib heat exchanger in which a plurality of wind direction guide plates are provided on the outer circumferential surface of the cylindrical heat exchanger on the side of the heat radiation part to suppress generation of turbulence by providing a plurality of wind direction guide plates inclined along the opening end direction of the vortex. The device was developed. The present invention will be described below with reference to embodiments shown in the drawings.

第1図乃至第3図は本発明の一実施例を示すものである
1 to 3 show one embodiment of the present invention.

図において1は多角筒状に形成された熱交換部、2はこ
の熱交換部1を収納するケーシング、3は加熱すべき低
温ガスが流通する放熱部、4はこの放熱部3の下方に設
けられた高温ガスが流通する吸熱部を夫々示す。前記熱
交換部1は30度の角度をもつて断面三角形状のスペー
サー5・・・を介して12個の熱交換部ユニット61,
62,・・・61。
In the figure, 1 is a heat exchange part formed in a polygonal cylinder shape, 2 is a casing that houses this heat exchange part 1, 3 is a heat radiation part through which low-temperature gas to be heated flows, and 4 is provided below this heat radiation part 3. The heat absorbing portions through which the high-temperature gas flows are shown. The heat exchange section 1 has 12 heat exchange section units 61,
62,...61.

を環状に配して、複数のブロックに区分された多角筒状
に形成されている。この熱交換部ユニット6は第3図に
示す如く夫々矩形状をなす側板7,7、上板8、底板9
、および仕切板10で前後が開口した枠状に組立て、前
記仕切板10にフィン11を設けた複数本のヒートバイ
ブ12・・・を等間隔に貫挿して角筒状のバイブ群13
を構成し、放熱部3側となる上板8と仕切板10との間
に、これと垂直に且つ側板7に対して傾斜するように複
数枚の風向ガイド板14・・・を設けたものである。こ
の熱交換部ユニット61,62・・・612を第1図に
示す如く多角形状をなす仕切板15の周辺部にスペーサ
ー5を介して風向ガイド板14が渦の開口端方向に沿つ
て傾斜するように配置し、前記側板7を放射状に配置し
た隔壁16として、この隔壁16により区分された各ブ
ロックに夫々角柱状のバイブ群13・・・を構成して多
角筒状とした熱交換部1を形成したものである。
It is formed into a polygonal tube shape divided into a plurality of blocks arranged in an annular manner. As shown in FIG. 3, this heat exchanger unit 6 includes rectangular side plates 7, 7, a top plate 8, and a bottom plate 9.
, and is assembled into a frame shape with openings at the front and back by a partition plate 10, and a plurality of heat vibrators 12 having fins 11 provided in the partition plate 10 are inserted at equal intervals to form a rectangular tube-shaped vibe group 13.
, and a plurality of wind direction guide plates 14 are provided between the upper plate 8 and the partition plate 10 on the side of the heat dissipation part 3 so as to be perpendicular thereto and inclined with respect to the side plate 7. It is. As shown in FIG. 1, the heat exchanger units 61, 62, . The side plate 7 is arranged as a partition wall 16 arranged radially, and each block divided by the partition wall 16 has a prismatic vibrator group 13... to form a polygonal cylindrical heat exchange section 1. was formed.

また前記熱交換部1を収納するケーシング2は周壁面が
渦巻状をなし、且つ渦の端面を開口した中空円筒体2a
の、前記周壁面の内側路中央部に環状の仕切板2bを水
平に設けて上下にダクト17,17を形成したものであ
る。
The casing 2 that houses the heat exchanger 1 is a hollow cylindrical body 2a with a spiral peripheral wall surface and an open end surface of the vortex.
An annular partition plate 2b is provided horizontally at the center of the inner path of the peripheral wall surface, and ducts 17, 17 are formed above and below.

またこの渦巻型をなすケーシング2の渦の開口した端面
は仕切板2bで隔離した上部を空気などの低温ガスが加
熱されて排出される排気口2cとし、またこの下部を廃
ガスなどの高温ガスを取入れる吸気口2dとしている。
更にケーシング2の上面には熱交換部1の中空部1aに
通じる低温ガス取入用の吸気口2eが、また下面には渦
の端面に設けた前記吸気口2dから取入れた高温ガスが
熱交換を行つた後、中空部1bを通つて外部に排出され
る排気口2fが夫々形成されている。しかして、上記構
成の筒型ヒートバイブ熱交換器においてその作用を説明
すると、ケーシング2の上面に形成した吸気口2eから
低温ガスを放熱部3内に取入れると共に、ケーシング2
の端面下部に形成した吸気口2dから高温ガスを吸熱部
4内に取入れる。
Furthermore, the end surface of the spiral-shaped casing 2 where the vortex is open is separated by a partition plate 2b, and the upper part serves as an exhaust port 2c through which low-temperature gas such as air is heated and discharged, and the lower part serves as an exhaust port 2c for high-temperature gas such as waste gas. The intake port 2d takes in the air.
Further, on the upper surface of the casing 2, there is an intake port 2e for taking in low-temperature gas that communicates with the hollow part 1a of the heat exchange section 1, and on the lower surface, the high-temperature gas taken in from the intake port 2d provided at the end surface of the vortex is used for heat exchange. After performing this, an exhaust port 2f is formed for exhausting the gas to the outside through the hollow portion 1b. To explain the operation of the cylindrical heat-vib heat exchanger having the above configuration, low-temperature gas is taken into the heat radiating part 3 from the intake port 2e formed on the upper surface of the casing 2, and the casing 2
High-temperature gas is introduced into the heat absorbing section 4 through an intake port 2d formed at the lower end face of the heat absorbing section 4.

このとき吹込まれた高温ガスはダクト17内を周壁面に
沿つて渦巻状に回転しながら進行し、隔壁16で仕切ら
れた各部分から角柱状に配列されたヒートバイブ群13
を通り、ここで熱交換を行なつて冷却された後、熱交換
部1の”中央部に至り、しかる後ケーシング2の下面に
設けた排気口2fから外部に排出される。一方ヒートバ
イブ12は減圧密閉した金属管内に作動液を封入したも
ので高温ガスとの熱交換により吸熱した熱は放熱部3側
に急速に伝達され、.ここで吸気口2eから取入れた低
温ガスと熱交換を行なつてこれを加熱する。
The high-temperature gas blown in at this time travels inside the duct 17 while rotating in a spiral along the peripheral wall surface, and from each part partitioned by the partition wall 16 a group of heat vibrators 13 arranged in a prismatic shape are formed.
After being cooled by heat exchange, it reaches the center of the heat exchange section 1, and is then discharged to the outside from the exhaust port 2f provided on the lower surface of the casing 2.On the other hand, the heat vibrator 12 The working fluid is sealed in a metal tube sealed under reduced pressure, and the heat absorbed through heat exchange with high-temperature gas is rapidly transferred to the heat radiating section 3.Here, it exchanges heat with the low-temperature gas taken in from the intake port 2e. and heat it up.

この場合、ケーシング2の上面に設けた吸気口2eから
熱交換部1の中央部に流入した低温ガスは吸熱部4と同
様に放射状に設けた隔壁16により区分された各プロツ
lクに均一に流入して熱交換を行なう。この熱交換を行
なつて加熱されたガスは風向ガイド板14によつて渦の
開口端側に向つてダクト17内に吹出される。このよう
に風向ガイド板14によつて斜めに吹出されたガスは、
ダクト17内を渦の開口端側に向つて回転するガスと同
一方向であるため乱流の発生が抑制され、乱流による圧
力損失を低減せしめて熱交換効率を向上させることがで
きる。また第3図に示す如く熱交換ユニット6を予め形
成しておき、これを多角筒状に組合せたプレフアブ式の
熱交換器1は組立てが極めて容易である上、特に熱交換
量が大きい場合に装置の小型化を図ることができる。
In this case, the low-temperature gas flowing into the center of the heat exchange section 1 from the intake port 2e provided on the upper surface of the casing 2 is distributed uniformly to each block partitioned by partition walls 16 provided radially, similar to the heat absorption section 4. flows in and performs heat exchange. The gas heated through this heat exchange is blown out into the duct 17 by the wind guide plate 14 toward the open end of the vortex. The gas blown out obliquely by the wind direction guide plate 14 in this way is
Since it is in the same direction as the gas rotating in the duct 17 toward the open end of the vortex, generation of turbulent flow is suppressed, pressure loss due to turbulent flow is reduced, and heat exchange efficiency can be improved. Furthermore, as shown in FIG. 3, a prefabricated heat exchanger 1 in which a heat exchange unit 6 is formed in advance and assembled into a polygonal cylinder shape is extremely easy to assemble, and is particularly useful when the amount of heat exchange is large. The device can be made smaller.

なおこの場合、熱交換部1はP角形状に限らず任意に選
択することができる。
In this case, the heat exchange section 1 is not limited to the P-gon shape, and can be arbitrarily selected.

また熱交換部ユニット6はスペーサー5を介して配置し
たものについて示したが、このようなスペーサー5を設
けず連結具を介して接続したものでも良い。また風向ガ
イド板14は固定式のものに限らず第4図に示す如く熱
交換部ユニット61,・・・に軸18を介して回動自在
に取付け、且つこれら風向ガイド板14・・・を互に連
結杆19で接続して傾斜角度を調整できるようにしたも
のでも良い。また第5図は隔壁16を設けていない本発
明の他の実施例を示すもので、円板状の仕切板15に複
数本のヒートバイブ12・・・を環状に貫挿して円筒状
の熱交換部1を形成し、且つこの熱交換部1の低温ガス
が流通する放熱部3の周面に、渦の開口端方向に沿つて
傾斜した複数枚の風向ガイド板14・・・を設けた筒型
ヒートバイブ熱交換器である。
Further, although the heat exchanger unit 6 is shown as being arranged through the spacer 5, it may be connected through a connector without providing the spacer 5. Moreover, the wind direction guide plate 14 is not limited to a fixed type, but can be rotatably attached to the heat exchange unit 61, . . . via a shaft 18, as shown in FIG. They may be connected to each other by a connecting rod 19 so that the inclination angle can be adjusted. FIG. 5 shows another embodiment of the present invention in which the partition wall 16 is not provided, in which a plurality of heat vibrators 12 are inserted annularly through the disk-shaped partition plate 15 to generate cylindrical heat. A plurality of wind direction guide plates 14, which are inclined along the opening end direction of the vortex, are provided on the circumferential surface of the heat radiation part 3 that forms the exchange part 1 and through which the low-temperature gas of the heat exchange part 1 flows. This is a cylindrical heat-vibe heat exchanger.

次に本発明の具体的な実施例について説明する。Next, specific examples of the present invention will be described.

内管として銅を用い、外管として炭素鋼を用いた外径2
5.4?φ、全長380『の二重管の外側に炭素鋼から
なる外径52.4Tr0nφのフィン11をフィンピッ
チ3.5順で取付け、内部にジフェニル系熱媒体オイル
を作動液として封入したヒートバイブ12を製造した。
Outer diameter 2 using copper as the inner tube and carbon steel as the outer tube
5.4? A heat vibrator 12 in which fins 11 made of carbon steel and having an outer diameter of 52.4Tr0nφ are attached to the outside of a double tube with a diameter of 380mm and a total length of 380mm, with a fin pitch of 3.5, and diphenyl-based heat transfer oil is sealed inside as a working fluid. was manufactured.

このヒートバイブ12を第3図に示す如く仕切板10に
24段×12列で288本貫挿して熱交換部ユニット6
を組立て、この上部(放熱部側)に厚さ2.5Tf$L
1幅150Tf$L1長さ140『の風向ガイド板14
・・・を40度傾斜させて4枚取付けた。このようにし
て組立てた12個の熱交換部ユニット61,6。
As shown in FIG. 3, 288 heat vibrators 12 are inserted into the partition plate 10 in 24 stages x 12 rows, and the heat exchanger unit 6
Assemble this and attach a thickness of 2.5Tf$L to the upper part (heat radiation part side).
1Width 150Tf$L1Length 140'' Wind direction guide plate 14
... was installed at a 40 degree angle. Twelve heat exchange unit units 61, 6 were assembled in this manner.

・・・Rl。を第1図の如く1諭形状の仕切板15の周
辺に配置して外径69607mの1論筒状の熱交換部1
を形成し、これを渦巻型ケーシング内2に装着して筒型
ヒートバイブ熱交換器を組立てた。上記の如く組立てた
熱交換器を下記第1表に示す条件で高温ガスと低温ガス
の熱交換を行なつたところ交換熱量は9.6×1σKc
al/hであつた。
...Rl. As shown in FIG.
A cylindrical heat vibrator heat exchanger was assembled by mounting this inside the spiral casing 2. When the heat exchanger assembled as above was used to exchange heat between high temperature gas and low temperature gas under the conditions shown in Table 1 below, the amount of heat exchanged was 9.6 x 1σKc.
It was al/h.

また本発明と比較するために、風向ガイド板14・・・
を設けていない筒型ヒートバイブ熱交換器についても同
様にその熱交換量を測定したところ5.65×1σKc
al/hであり、本発明では約70%も向上し、また圧
力損失も約30%低下していることが認められた。以上
説明した如く本発明に係る筒型ヒートバイブ熱交換器に
よれば、放熱部側のダクト内に発生する乱流を最小限に
抑制することにより圧力損失を小さくして、この結果熱
交換効率を向上させることができると共に、プロアー(
送風器)やダクトを小型化することができ得るなど顕著
な効果を有するものである。
In addition, for comparison with the present invention, the wind direction guide plate 14...
The heat exchange amount of the cylindrical heat vib heat exchanger without the
al/h, which was improved by about 70% in the present invention, and the pressure loss was also reduced by about 30%. As explained above, according to the cylindrical heat-vib heat exchanger according to the present invention, the pressure loss is reduced by minimizing the turbulent flow generated in the duct on the heat radiation part side, and as a result, the heat exchange efficiency is reduced. In addition to being able to improve
This has remarkable effects such as making it possible to downsize air blowers and ducts.

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

第1図は本発明の筒型ヒートバイブ熱交換器を一部切欠
して示す平面図、第2図は第1図の■一■線に沿う断面
図、第3図は第1図に示す熱交換部を構成する熱交換部
ユニットの斜視図、第4図は風向ガイド板を回動自在に
取付けた熱交換部の要部を示す平面図、第5図は隔壁を
設けていない熱交換部を装着した筒型ヒートバイブ熱交
換器の一部切欠した平面図である。 1・・・・・・熱交換部、2・・・・・・ケーシング、
2a・・中空円筒体、2b・・・・・・仕切板、2c・
・・・・・排気口、2d・・・・・・吸気口、2e・・
・・・・吸気口、2f・・・・・・排気口、3・・・・
・・放熱部、4・・・・・・吸熱部、5・・・・・・ス
ペーサー、6,61,62・・・612・・・・・熱交
換部ユニット、10・・・・・・仕切板、12・・・・
・・ヒートバイブ、13・・・・・・バイブ群、14・
・・・・・風向ガイド板、15・・・・・仕切板、16
・・・・・・隔壁、17・・・・・・ダクト、19・・
・・・・連結杆。
Fig. 1 is a partially cutaway plan view of the cylindrical heat-vib heat exchanger of the present invention, Fig. 2 is a cross-sectional view taken along line 1 and 2 of Fig. 1, and Fig. 3 is shown in Fig. 1. A perspective view of the heat exchange section unit that constitutes the heat exchange section, Fig. 4 is a plan view showing the main parts of the heat exchange section with a wind direction guide plate rotatably attached, and Fig. 5 is a heat exchange unit without partition walls. FIG. 2 is a partially cutaway plan view of a cylindrical heat vib heat exchanger with a heat exchanger attached thereto. 1... Heat exchange section, 2... Casing,
2a...Hollow cylindrical body, 2b...Partition plate, 2c...
...Exhaust port, 2d...Intake port, 2e...
...Intake port, 2f...Exhaust port, 3...
... Heat radiation part, 4 ... Heat absorption part, 5 ... Spacer, 6, 61, 62 ... 612 ... Heat exchange unit, 10 ... Partition plate, 12...
・・Heat vibe, 13・・・・Vibe group, 14・
... Wind direction guide plate, 15 ... Partition plate, 16
...Bulkhead, 17...Duct, 19...
...Connecting rod.

Claims (1)

【特許請求の範囲】 1 周壁面が渦巻状をなし、且つ渦の端面を開口した中
空円筒体の、前記周壁面の内側に環状の仕切板を水平に
設けて上下にダクトを形成したケーシング内に、多角形
状または円形状の仕切板の上下方向に複数本のヒートパ
イプを環状に貫挿した筒型の熱交換部を装着して、この
上部を加熱すべき低温ガスが流通する放熱部とし、下部
に高温ガスが流通する吸熱部とした筒型ヒートパイプ熱
交換器において、前記筒型熱交換部の放熱部側外周面に
、渦の開口端方向に沿つて傾斜した複数枚の風向ガイド
板を設けて、乱流の発生を抑制するようにしてなる筒型
ヒートパイプ熱交換器。 2 熱交換部を構成する仕切板の周辺部の上下両面に、
これと垂直に夫々複数枚の隔壁を放射状に設けて、前記
熱交換部を複数のブロックに区分してなる特許請求の範
囲第1項記載の筒型ヒートパイプ熱交換器。 3 複数のブロックに区分した熱交換部の各ブロックを
ユニット化してプレフアブ式に構成してなる特許請求の
範囲第2項記載の筒型ヒートパイプ熱交換器。
[Scope of Claims] 1. Inside a casing of a hollow cylindrical body whose peripheral wall surface has a spiral shape and whose vortex end surface is open, and in which an annular partition plate is provided horizontally inside the peripheral wall surface to form a duct above and below. A cylindrical heat exchange section in which multiple heat pipes are inserted annularly in the vertical direction of a polygonal or circular partition plate is installed, and the upper part serves as a heat dissipation section through which the low-temperature gas to be heated flows. , in a cylindrical heat pipe heat exchanger having a heat absorption section in which high-temperature gas flows at the bottom thereof, a plurality of wind direction guides are provided on the outer circumferential surface of the cylindrical heat exchange section on the side of the heat dissipation section and are inclined along the opening end direction of the vortex. A cylindrical heat pipe heat exchanger that is equipped with a plate to suppress the occurrence of turbulence. 2. On both the upper and lower sides of the peripheral part of the partition plate that constitutes the heat exchange section,
2. The cylindrical heat pipe heat exchanger according to claim 1, wherein a plurality of partition walls are provided radially perpendicularly thereto to divide the heat exchange section into a plurality of blocks. 3. The cylindrical heat pipe heat exchanger according to claim 2, wherein each block of the heat exchange section divided into a plurality of blocks is unitized to form a prefabricated structure.
JP9833577A 1977-01-31 1977-08-17 Cylindrical heat pipe heat exchanger Expired JPS6042873B2 (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
JP9833577A JPS6042873B2 (en) 1977-08-17 1977-08-17 Cylindrical heat pipe heat exchanger
SE7801115A SE440274B (en) 1977-01-31 1978-01-30 CYLINDRICAL REFLECTOR
GB3811/78A GB1596666A (en) 1977-01-31 1978-01-31 Cylindrical heat exchanger using heat pipes
DE2804106A DE2804106C2 (en) 1977-01-31 1978-01-31 Heat exchanger
US05/875,092 US4206807A (en) 1977-01-31 1978-02-03 Cylindrical heat exchanger using heat pipes
US06/091,949 US4327801A (en) 1977-01-31 1979-11-07 Cylindrical heat exchanger using heat pipes

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9833577A JPS6042873B2 (en) 1977-08-17 1977-08-17 Cylindrical heat pipe heat exchanger

Publications (2)

Publication Number Publication Date
JPS5432858A JPS5432858A (en) 1979-03-10
JPS6042873B2 true JPS6042873B2 (en) 1985-09-25

Family

ID=14217023

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9833577A Expired JPS6042873B2 (en) 1977-01-31 1977-08-17 Cylindrical heat pipe heat exchanger

Country Status (1)

Country Link
JP (1) JPS6042873B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2381203A1 (en) * 2010-04-22 2011-10-26 Paul Wurth S.A. Modular heat pipe heat exchanger

Also Published As

Publication number Publication date
JPS5432858A (en) 1979-03-10

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