JPS6059516B2 - Air-cooled heat exchanger with means to prevent supercooling - Google Patents

Air-cooled heat exchanger with means to prevent supercooling

Info

Publication number
JPS6059516B2
JPS6059516B2 JP594179A JP594179A JPS6059516B2 JP S6059516 B2 JPS6059516 B2 JP S6059516B2 JP 594179 A JP594179 A JP 594179A JP 594179 A JP594179 A JP 594179A JP S6059516 B2 JPS6059516 B2 JP S6059516B2
Authority
JP
Japan
Prior art keywords
heat exchanger
tube
tubes
air
pipe
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
JP594179A
Other languages
Japanese (ja)
Other versions
JPS5599584A (en
Inventor
邦彦 南
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.)
Sasakura Engineering Co Ltd
Original Assignee
Sasakura Engineering 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 Sasakura Engineering Co Ltd filed Critical Sasakura Engineering Co Ltd
Priority to JP594179A priority Critical patent/JPS6059516B2/en
Publication of JPS5599584A publication Critical patent/JPS5599584A/en
Priority to US06/214,086 priority patent/US4417619A/en
Priority to US06/497,863 priority patent/US4537248A/en
Publication of JPS6059516B2 publication Critical patent/JPS6059516B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 空冷式熱交換器の管束は一般にフィン管が多層に設け
られており、この管束を横切る空気流によつて高温の管
内蒸気が冷却されるが、空気流の温度は空気流の上流側
ほど低温度を示し、よつて管内蒸気との温度差が入口部
において最大となつて冷却能力は最大値を示し、空気流
がフィン管を横切つて下流側に進むにつれて、空気流は
順次フィン管との熱交換によつて加熱され、管内蒸気と
の温度差は減少し、これによりフィン管の熱移動量が減
少する。
[Detailed Description of the Invention] The tube bundle of an air-cooled heat exchanger is generally provided with multiple layers of finned tubes, and the high-temperature steam inside the tubes is cooled by the air flow that crosses this tube bundle, but the temperature of the air flow is The temperature is lower on the upstream side of the airflow, so the temperature difference with the steam inside the pipe is maximum at the inlet, and the cooling capacity is at its maximum value.As the airflow moves downstream across the finned pipe, The air stream is heated in turn by heat exchange with the finned tube, and the temperature difference with the steam inside the tube is reduced, thereby reducing the amount of heat transfer through the finned tube.

これは直接凝縮蒸気量の減少を意味する。 この結果、
最低温度のフィン管では、管内蒸気の凝縮に伴つて蒸気
の流入量は増大するが、フイーン管の流動抵抗が大とな
つて出印こ近ずく程蒸気の流れは減少し、十分な伝熱面
積があるにもかかわらず蒸気量が少ないため、凝縮水は
著しく過冷却し遂には凍結する結果を招来する。
This means a reduction in the amount of directly condensed steam. As a result,
In the finned tube at the lowest temperature, the amount of steam flowing into the tube increases as the steam inside the tube condenses, but as the flow resistance of the finned tube increases and the closer it gets to the exit, the flow of steam decreases, ensuring sufficient heat transfer. Because the amount of steam is small despite the area, the condensed water becomes extremely supercooled and eventually freezes.

特に大気温度が極度に低下したり、冬期、或は惑冷地に
おいてこの傾向は甚しく、また凝固点の高い管内流体の
場合も同じ障害が発生する。 これらの障害を防止する
ため、フィンのピッチを変え、または一部フィンを取除
いて裸管を用いたり、またはフィンの巻数、高さを変え
るなどの工夫がなされているが、たとえ空気量を調整し
ても大気温度が変化する度に管内圧力のバランスが崩れ
、過冷の現象が生ずる危険があつた。
This tendency is particularly severe when the atmospheric temperature is extremely low, in winter, or in cold regions, and the same problem occurs when the fluid in the pipe has a high freezing point. In order to prevent these problems, efforts have been made to change the pitch of the fins, remove some fins and use bare tubes, or change the number of turns and height of the fins. Even with this adjustment, there was a risk that the pressure inside the pipes would become unbalanced every time the atmospheric temperature changed, resulting in overcooling.

このような過冷に対しては、管束を構成する各伝熱管を
各々独立して閉回路とし、各管ごとにドレンを抜き出し
て過冷を防止する方式や、蒸気入口ヘッダーに複数のU
字管を内外に並設することによつて各々の内圧の差を考
慮した方式もあるが、前者は構部が複雑となり、後者て
は管内で生成したドレンがU字管の長い距離を流れて一
方の出口より排出されることとなり、必要以上に冷却さ
れ易いなどの欠点がなお残されている。 上記の欠点を
改良して、熱交換によつて生ずる伝熱管層の被冷却流体
の蒸気圧を各伝熱管内で均一に保ち、併せて凝縮水を迅
速に抜き出して凍結の防止と伝熱効率の向上を企図して
、出願人は先に特願昭53−68186(特公昭59−
24783号)によつて伝熱管を中間部で交差させるこ
とを特徴とする熱交換器を提案したが、本発明はさらに
これに改良を加え、伝熱管を水平方向に維持する管束に
も適用でき、しかも凝縮水の滞留を防いて流出を容易と
なし、一層過冷却防止に役立つ空冷熱交換器を得ようと
するものである。
To prevent such overcooling, there are methods in which each heat exchanger tube that makes up the tube bundle is made into an independent closed circuit, and the drain is extracted from each tube to prevent overcooling, and multiple U in the steam inlet header are used.
There is also a method that considers the difference in internal pressure by arranging U-shaped pipes in parallel inside and outside, but the former requires a complicated structure, and the latter requires drain generated inside the pipe to flow over a long distance in the U-shaped pipe. Therefore, there still remain drawbacks such as the fact that it is likely to be cooled more than necessary. By improving the above drawbacks, the vapor pressure of the fluid to be cooled in the heat transfer tube layer caused by heat exchange is kept uniform in each heat transfer tube, and condensed water is quickly extracted to prevent freezing and improve heat transfer efficiency. In order to improve the results, the applicant first filed Japanese Patent Application No. 53-68186
No. 24783) proposed a heat exchanger characterized by having heat exchanger tubes intersecting in the middle, but the present invention further improves this and can be applied to a tube bundle in which the heat exchanger tubes are maintained in a horizontal direction. Furthermore, the present invention aims to provide an air-cooled heat exchanger that prevents condensed water from accumulating and facilitates its outflow, thereby further helping to prevent overcooling.

以下本発明をその実施例を示す添付の図面について説明
するが、本発明は図面および以下の説明によつて限定さ
れるものではなく、本発明の技術範囲は特許請求の範囲
の項に示したとおりである。
The present invention will be described below with reference to the accompanying drawings showing examples thereof, but the present invention is not limited by the drawings or the following description, and the technical scope of the present invention is defined in the claims. That's right.

第1図に示す空冷熱交換器1は、冷却空気送給用ファン
装置2の上方両側に対称的に水平面と傾斜角α0をもた
せて入口側ヘッダー6と出口側ヘッダー7とを配設し、
左右の各両ヘッダー6と7間にそれぞれ管束3と3″が
配設されており、ここに使用する伝熱管4は水平方向と
し、これに伝熱面を増大させるため第4図に示すように
フィン5が巻きつけられている。
The air-cooled heat exchanger 1 shown in FIG. 1 has an inlet header 6 and an outlet header 7 arranged symmetrically on both sides above the cooling air supply fan device 2 with an inclination angle α0 to the horizontal plane.
Tube bundles 3 and 3'' are disposed between the left and right headers 6 and 7, respectively, and the heat transfer tubes 4 used here are oriented horizontally, as shown in Fig. 4 to increase the heat transfer surface. The fin 5 is wrapped around the fin 5.

第2図において、入口側ヘッダー6の管板8には下層管
孔A,A″,A″・・・および上層管孔B,B″,B″
・・・が穿設され、一方、出口側ヘッダー7の管板9に
も上層管孔A,a″,a″・・・および下層管孔B,b
″,b″・・・が穿設され、したがつて一流路当り上下
2層の伝熱管が設けられている。
In FIG. 2, the tube plate 8 of the inlet header 6 has lower tube holes A, A'', A''... and upper layer tube holes B, B'', B''.
... are bored in the tube plate 9 of the outlet header 7, and upper pipe holes A, a'', a''... and lower pipe holes B, b
'', b''... are bored, so that two layers of upper and lower heat transfer tubes are provided per channel.

この例においては、入口側ヘッダー6の管板8には第2
図及び第4図に明示したように管孔A.l!1.Bとを
水平方向に、管孔BとA″とを垂直方向に、管孔A″と
B″とを水平方向に設け、一方、第2図に示すように、
出口側ヘッダー7の管板9には管孔a<15bとを垂直
方向に、管孔B.(5a″を水平方向に、管孔a″とb
゛とを垂直方向に設けており、両ヘッダー6,7はいず
れも水平面に対する傾斜を45ッとしている。したがつ
て、管板8においては、管孔A,A゛,A″″が下層列
、管孔B,B″,B″が上層列をなし、管板9において
は、管孔A,a″,a″が上層列、管孔B,b″,b″
″が下層列をなしている。一端を管板8の下層管孔,A
,A″,A″に挿入した各伝熱管Pは、他端が管板9の
上層管孔A,a″,a″″に挿入され、中央部に水平方
向の折曲部10が形成されており、一方、一端を管板8
の上層管孔B,B″,B″″に挿入した各伝熱管Qは、
他端が管板9の下層管孔B,b″,b″に挿入され中央
部に鉛直方向の折曲部11が形成されている。斯くして
、入口側ては、各伝熱管Pが下層になり、各伝熱管Qが
上層になるが、出口側ではこれが逆配置となり、そして
各伝熱管PとQには管内流体の流れ方向にして立ち上り
箇所がないように構成されている。なお、第4図に示す
ように伝熱面積を増大するためフィン5を捲装した伝熱
管を用いる場合においては、上下両層の伝熱管のフィン
5が矢印で示した空気流の方向において部分的に重なり
合うようになつている。上記の構成を有する空冷熱交換
器において、入口側ヘッダー6に導入された蒸気は、そ
の一部が下層列の管孔A,A″,A″・・・から下層伝
熱管Pに入り、他の一部は上層列の管孔B,B″,B″
・・・に導入されるが、中間の折曲部10,11を通過
したのち、その流れの層が上下逆転する。
In this example, the tube plate 8 of the inlet header 6 has a second
As clearly shown in FIG. l! 1. B is provided horizontally, tube holes B and A'' are provided vertically, and tube holes A'' and B'' are provided horizontally, while as shown in FIG.
The tube plate 9 of the outlet side header 7 has tube holes a<15b in the vertical direction and tube holes B. (5a'' in the horizontal direction, pipe holes a'' and b
The headers 6 and 7 are both provided at an inclination of 45 degrees with respect to the horizontal plane. Therefore, in the tube sheet 8, the tube holes A, A'', A'''' form the lower row, and the tube holes B, B'', B'' form the upper layer row, and in the tube sheet 9, the tube holes A, a ″, a″ are upper rows, tube holes B, b″, b″
" form the lower row. One end is connected to the lower pipe hole of the tube plate 8, A
, A'', A'', the other end of each heat exchanger tube P is inserted into the upper tube hole A, a'', a'''' of the tube plate 9, and a horizontal bent portion 10 is formed in the center. and on the other hand, one end is connected to the tube plate 8.
Each heat exchanger tube Q inserted into the upper layer pipe hole B, B″, B″″ is
The other end is inserted into the lower tube holes B, b'', b'' of the tube plate 9, and a vertically bent portion 11 is formed in the center. Thus, on the inlet side, each heat exchanger tube P is in the lower layer and each heat exchanger tube Q is in the upper layer, but on the outlet side, this arrangement is reversed, and each heat exchanger tube P and Q has a flow direction of the fluid in the tube. The structure is such that there are no rising points. In addition, when using a heat exchanger tube wrapped with fins 5 to increase the heat transfer area as shown in FIG. They are starting to overlap. In the air-cooled heat exchanger having the above configuration, a part of the steam introduced into the inlet side header 6 enters the lower heat exchanger tubes P through the tube holes A, A″, A″, etc. in the lower row, and other parts A part of the upper row of pipe holes B, B″, B″
..., but after passing through the intermediate bends 10 and 11, the layers of the flow are turned upside down.

すなわ”ち、入口側ヘッダー6の上層の管孔A,A″,
A″・・・に連通した各伝熱管Pは、前半では下層とな
つているので、ファン装置2に最も近く、したがつて低
温空気流で強く冷却され、また、上層管孔B,B″,B
″・・・に連通した各伝熱管内Qは、前半では上層とな
つているので、上記下層の伝熱管Pを冷却して温度の上
昇した空気流によつて冷却されるが、管内流体との温度
差が小であつて、熱移動量が少なく、ひいては凝縮蒸気
量が減少する。しかしながら、上記伝熱管PとQとは、
その中間の折曲部10,11を通過したのち、層の上下
が逆になるので、後半における冷却効果も前半と逆の関
係になり、したがつて全体としての空気流による冷却は
均一化され、管内の残存蒸気及び不凝縮性ガスの蒸気圧
も上下両層て均一となり、一部の伝熱管のみが過冷され
ることはない。なお、上記の実施では、両ヘッダー6,
7の水平面に対する傾斜角を45ヘとし、二層の伝熱管
P.Qのうち、一方の伝熱管Pの中間折曲部10を水平
方向に、他方の伝熱管Qの中間折曲部11を鉛直方向に
形成しているが、管内に蒸気が滞留せず、また管相互が
接触しない程度に両ヘッダーおよび両折曲部を適宜傾斜
してもよく、そして出口側ヘッダー7に凝縮水取出管お
よびベント管を通常のとおりに設けることはいうまでも
ない。なおまた、上記実施例ては、2層の伝熱管にファ
ン装置よりの冷却空気を直接接触させる場合を示したが
、両ヘッダー間に通常配置されるように主凝縮管束を設
置し、その上方に設ける折流副凝縮管に本発明の技術手
段を採用することもてきる。以上要するに本発明は、水
平面に対し傾斜して配設した入口側ヘッダー及び出口側
ヘッダーと、上下2層に配列し上記両ヘッダーを連通せ
しめた水平伝熱管と、管内流体冷却用ファン装置とを有
する空冷熱交換器において、上下両層の水平伝熱管を、
管内流体の流れ方向に対して立ち上り部がないように中
間部でそれぞれ横方向と下方向に折曲せしめ、入口側と
出口側における両水平伝熱管の層を逆配置に変換したこ
とを特徴とする過冷却防止手段を施した空冷熱交換器を
要旨とし、これによれば、入口側の下層管内で強く冷却
れた管内流体は、出口側ては上層となつて下層伝熱管で
加温された空気流によつてゆるく冷却され、一方、入口
側の上層管内の流体は、その下層管内の流体と熱交換し
て温度上昇した空気流によつてゆるく冷却され、中間折
曲部を通過したのち、下層側に変換し、ここで低温空気
流によつて強く冷却されることになるので、結局、上下
両層の管内流体は全体として均一に冷却され、大気温度
が変化しても上下両層の伝熱管内の圧力のバンスが崩れ
ることはなく、従来のような最下層の伝熱管のみが過冷
却されて管内の凝縮液が凍結する欠点を回避することが
でき、また水平伝熱管、の中間部に設けた折曲部が、入
口側で下層をなす伝熱管では水平方向を採り、入口側で
上昇をなす伝熱管では下方向を採るように形成されてい
るので、全体を通じて管内流体の流れ方向について立ち
上がり箇所がなく、したがつて、凝縮液の流出が容易と
なつて、これが管内の滞留せず、出口側ヘッダーより迅
速に排出できて、過冷却の防止、ひいては凍結防止の効
果をさらに助長することができる。
In other words, the pipe holes A, A″ in the upper layer of the inlet header 6,
Each heat exchanger tube P connected to A''... is in the lower layer in the first half, so it is closest to the fan device 2 and is therefore strongly cooled by the low-temperature air flow. ,B
Since the inside of each heat exchanger tube Q connected to the `` The temperature difference is small, the amount of heat transfer is small, and the amount of condensed steam is reduced.However, the heat exchanger tubes P and Q are
After passing through the bends 10 and 11 in the middle, the layers are turned upside down, so the cooling effect in the second half is also the opposite of the first half, so the cooling by the air flow as a whole is made uniform. , the vapor pressure of the residual steam and non-condensable gas in the tubes becomes uniform in both the upper and lower layers, and only a part of the heat exchanger tubes is not overcooled. In addition, in the above implementation, both headers 6,
The inclination angle of P.7 with respect to the horizontal plane is set to 45 degrees, and the two-layer heat exchanger tube P. Among the heat exchanger tubes Q, the intermediate bent portion 10 of one heat exchanger tube P is formed in the horizontal direction, and the intermediate bent portion 11 of the other heat exchanger tube Q is formed in the vertical direction, but steam does not accumulate in the tube, and Both headers and both bent portions may be appropriately inclined to such an extent that the pipes do not contact each other, and it goes without saying that the outlet side header 7 is provided with a condensed water takeoff pipe and a vent pipe as usual. Furthermore, although the above embodiment shows a case in which the cooling air from the fan device is brought into direct contact with the two-layer heat transfer tubes, the main condensing tube bundle is installed so that it is normally placed between both headers, and the The technical means of the present invention can also be applied to the folded flow sub-condensing pipe provided in the sub-condenser pipe. In summary, the present invention comprises an inlet header and an outlet header arranged at an angle with respect to a horizontal plane, horizontal heat transfer tubes arranged in upper and lower layers to communicate with both headers, and a fan device for cooling fluid in the tubes. In an air-cooled heat exchanger with horizontal heat exchanger tubes in both upper and lower layers,
The pipe is characterized by bending it horizontally and downwardly at the middle part so that there is no rising part in the flow direction of the fluid inside the pipe, and converting the layers of both horizontal heat transfer tubes on the inlet side and the outlet side to reverse positions. The gist of the air-cooled heat exchanger is an air-cooled heat exchanger equipped with supercooling prevention means.According to this, the fluid in the tubes that is strongly cooled in the lower layer tubes on the inlet side becomes the upper layer on the outlet side and is heated in the lower layer heat exchanger tubes. On the other hand, the fluid in the upper pipe on the inlet side was gently cooled by the air flow, whose temperature increased by exchanging heat with the fluid in the lower pipe, and passed through the intermediate bend. It is then transferred to the lower layer, where it is strongly cooled by the low-temperature air flow, so that the fluid in both the upper and lower layers is cooled uniformly as a whole, and even if the atmospheric temperature changes, the fluid in both the upper and lower layers remains cool. The pressure balance in the heat exchanger tubes of the layers does not collapse, and it is possible to avoid the conventional disadvantage that only the lowest heat exchanger tube is supercooled and the condensate inside the tube freezes. The bending part provided in the middle of the tube is formed so that the lower heat transfer tube on the inlet side takes the horizontal direction, and the heat transfer tube that rises on the inlet side takes the downward direction. There are no rising points in the flow direction, and therefore, the condensate flows out easily, does not accumulate in the pipe, and can be quickly discharged from the outlet header, preventing overcooling and, ultimately, preventing freezing. can be further encouraged.

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

図面は本発明の一実施例を示すもので、第1図は概略配
置図、第2図は要部の斜面図、第3図はその拡大平面図
、第4図は第2図の管板の側面図、第5図は第2図の■
−V線断面図である。 1・・・・・・空冷熱交換器、2・・・・・・ファン装
置、3,3″・・・・・・管束、4・・・・・・各伝熱
管、5・・・・・フィン、6・・・・・・入口側ヘッダ
ー、7・・・・・・出口側ヘッダー、8・・・・・・入
口側管板、9・・・・・・出口側管板、A,A″,A″
・・・・・・入口側下層管孔、B,B″,B″・・・・
・・入口側上層管孔、A,a″,a″・・・・・・出口
側上層管孔、B,b″,b″″・・・・・・出口側下層
管孔、P・・・・・・入口側上層伝熱管、Q・・・・・
・入口側上層伝熱管、10・・・・・・伝゛熱管Pの接
曲部、11・・・・・・伝熱管Qの折曲部、α・・・ヘ
ッダーの傾斜角。
The drawings show one embodiment of the present invention, and Fig. 1 is a schematic layout diagram, Fig. 2 is a perspective view of the main parts, Fig. 3 is an enlarged plan view thereof, and Fig. 4 is a tube plate of Fig. 2. The side view of Figure 5 is the side view of Figure 2.
-V line sectional view. 1... Air-cooled heat exchanger, 2... Fan device, 3,3''... Tube bundle, 4... Each heat transfer tube, 5...・Fin, 6... Inlet side header, 7... Outlet side header, 8... Inlet side tube plate, 9... Outlet side tube plate, A ,A″,A″
...Inlet side lower pipe hole, B, B'', B''...
・・Inlet side upper layer pipe hole, A, a″, a″・・・・Outlet side upper layer pipe hole, B, b″, b″″・・・・・Outlet side lower layer pipe hole, P・・...Inlet side upper heat exchanger tube, Q...
- Upper layer heat exchanger tube on the inlet side, 10...Bending portion of heat transfer tube P, 11...Bending portion of heat transfer tube Q, α...Inclination angle of header.

Claims (1)

【特許請求の範囲】[Claims] 1 平面に対し傾斜して配設した入口側ヘッダー及び入
口側ヘッダーと、上下2層に配列し上記両ヘッダーを連
通せしめた水平伝熱管と、管内流体冷却用ファン装置と
を有する空冷熱交換器において、上下両層の水平伝熱管
を、管内流体の流れ方向に対して立ち上り部がないよう
に中間部でそれぞれ横方向と下方向に折曲せしめ、入口
側出口側における両水平伝熱管の層を逆配置に変換した
ことを特徴とする過冷却防止手段を施した空冷熱交換器
1. An air-cooled heat exchanger having an inlet header and an inlet header arranged at an angle with respect to a plane, horizontal heat transfer tubes arranged in upper and lower layers and communicating with both headers, and a fan device for cooling fluid in the tubes. In this method, horizontal heat exchanger tubes in both upper and lower layers are bent laterally and downwardly at the middle part so that there is no rising part in the flow direction of the fluid inside the tubes, and the layers of horizontal heat exchanger tubes on the inlet side and the outlet side are An air-cooled heat exchanger equipped with a means for preventing supercooling, which is characterized by converting the arrangement to reverse.
JP594179A 1978-06-05 1979-01-20 Air-cooled heat exchanger with means to prevent supercooling Expired JPS6059516B2 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP594179A JPS6059516B2 (en) 1979-01-20 1979-01-20 Air-cooled heat exchanger with means to prevent supercooling
US06/214,086 US4417619A (en) 1978-06-05 1980-12-08 Air-cooled heat exchanger
US06/497,863 US4537248A (en) 1978-06-05 1983-05-25 Air-cooled heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP594179A JPS6059516B2 (en) 1979-01-20 1979-01-20 Air-cooled heat exchanger with means to prevent supercooling

Publications (2)

Publication Number Publication Date
JPS5599584A JPS5599584A (en) 1980-07-29
JPS6059516B2 true JPS6059516B2 (en) 1985-12-25

Family

ID=11624919

Family Applications (1)

Application Number Title Priority Date Filing Date
JP594179A Expired JPS6059516B2 (en) 1978-06-05 1979-01-20 Air-cooled heat exchanger with means to prevent supercooling

Country Status (1)

Country Link
JP (1) JPS6059516B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4417619A (en) * 1978-06-05 1983-11-29 Sasakura Engineering Co., Ltd. Air-cooled heat exchanger
US4537248A (en) * 1978-06-05 1985-08-27 Sasakura Engineering Co., Ltd. Air-cooled heat exchanger

Also Published As

Publication number Publication date
JPS5599584A (en) 1980-07-29

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