JPS58187786A - Condenser - Google Patents

Condenser

Info

Publication number
JPS58187786A
JPS58187786A JP6909582A JP6909582A JPS58187786A JP S58187786 A JPS58187786 A JP S58187786A JP 6909582 A JP6909582 A JP 6909582A JP 6909582 A JP6909582 A JP 6909582A JP S58187786 A JPS58187786 A JP S58187786A
Authority
JP
Japan
Prior art keywords
fluid
condensed
gas
heat transfer
cylinder
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
JP6909582A
Other languages
Japanese (ja)
Other versions
JPS625274B2 (en
Inventor
Koichiro Yamaguchi
山口 紘一郎
Shigeru Iwanaga
茂 岩永
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 Electric Industrial 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP6909582A priority Critical patent/JPS58187786A/en
Publication of JPS58187786A publication Critical patent/JPS58187786A/en
Publication of JPS625274B2 publication Critical patent/JPS625274B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28BSTEAM OR VAPOUR CONDENSERS
    • F28B1/00Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser
    • F28B1/02Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser using water or other liquid as the cooling medium
    • 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
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/0008Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one medium being in heat conductive contact with the conduits for the other medium

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Details Of Heat-Exchange And Heat-Transfer (AREA)

Abstract

PURPOSE:To prevent the mixture of flows between two fluids by densely and widely providing fluid passages and heat transfer surfaces, effectively forming the contacting surfaces between the two fluid passages to improve the heat transfer, thereby reducing the size of a stereoscopic structure. CONSTITUTION:Condensed fluid is flowed in gas state from an inflow tube 7 to the internal space of a cylinder 1. Since the internal space has a guide plate 2 which forms a passage of the condensed fluid, the gas is moved downwardly in a zigzag along the plate 2. At this time the fluid is thermally exchanged with the fluid flowed in a zigzag downwardly through a fluid conduit 6 which is secured to a holder 3 provided from the outer wall surface of the cylinder 1, and becomes the state of gas-liquid phases. Since the heat transfer rates of the gas and the liquid are different, the pitch is varied in response to the variation in the state of the condensed fluid so that the pitch of the plate 2 which is used also as the heat transfer surface is optimized. The condensed fluid is increased in the condensed amount along the plate 2, completely condensed and then fed from the cylinder 1 at the low flowout tube 8.

Description

【発明の詳細な説明】 本発明は2つの流体間で熱父侯させるとともに流体通路
の破損が生じても流体が相互に異光しないようにした給
湯用熱交換器に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a heat exchanger for hot water supply that maintains thermal conditions between two fluids and prevents the fluids from emitting different light from each other even if a fluid passage is damaged.

従来この桶の熱交換器としては各々の流体が流れる管を
偏平して併設接触させたものや三重管構成にして最内管
と最外管にそれぞnの流体を流し最内管を二重壁管とし
て管壁の間に漏洩逃し4乞構成したり漏洩検湘装置を設
けたものがあった。
Conventionally, heat exchangers for this type of tub have been constructed by connecting flat tubes through which each fluid flows, or by having a triple tube configuration in which n fluids are flowed through the innermost tube and the outermost tube, respectively, and two tubes are connected to the innermost tube. Some heavy-walled pipes were constructed with four leakage vents between the pipe walls or were equipped with a leakage detection device.

以上のような従来構成の熱交換器は管材による伝熱面接
触構成であり、熱交換器全体の形状も菅の曲げ加工によ
り、規制されるために小型化および立体構造化には適し
ていない。また管材間の接触を密にかつ接触面を広くす
ることは加工上困難であるとともに管内を流れる流体の
伝熱面積の拡大にも制限があるために必要な熱伝達のた
めには管径および管長を大きくして熱交換器全構成する
必要があった。
The heat exchanger with the above conventional configuration has a heat transfer surface contact configuration using tube materials, and the shape of the entire heat exchanger is also restricted by the bending process of the tubes, so it is not suitable for miniaturization and three-dimensional structure. . In addition, it is difficult to make close contact between tube materials and widen the contact surface, and there is also a limit to the expansion of the heat transfer area of the fluid flowing inside the tube, so the tube diameter and It was necessary to increase the pipe length and configure the entire heat exchanger.

本発明は以上のような従来の欠点を除去するもので、流
体通路と伝熱面を密にかつ広く取るとともに2流体通路
間の接触面を確実にして熱伝達を同上させて立体構造小
型化を図り、2流体間の混流も防止することを目的にす
るものである。
The present invention eliminates the above-mentioned drawbacks of the conventional technology, and makes the fluid passage and the heat transfer surface dense and wide, and also ensures the contact surface between the two fluid passages to improve heat transfer and reduce the size of the three-dimensional structure. The purpose is to prevent mixed flow between two fluids.

この目的を達成するために本発明は、流入管と匠出管を
有する筒体の内部空間に凝縮流体の通路全構成する案内
板のピッチをガス域、気液2相域。
To achieve this objective, the present invention has an inlet pipe and an outlet pipe in the inner space of the cylinder, and the pitch of the guide plate that constitutes the entire condensed fluid passage into the gas region and the gas-liquid two-phase region.

液域の状態に応じて変えて内壁面から設け、保持部を外
壁面から設けた筒体を熱伝導性材料で一体成形し、前記
筒体の両端面を密閉するとともに前記保持部に他の液状
流体導管を固着して凝縮器を構成しているので、凝縮液
体の通路となる内部空間はその通路を構成する案内板を
流体の相変化に応じて最も効率よく熱伝達するようなピ
ッチで設けることにより、立体構造小型化を図り得るも
のである。
A cylindrical body is provided from the inner wall surface and a holding portion is provided from the outer wall surface depending on the state of the liquid region, and a cylindrical body is integrally molded with a thermally conductive material, both end surfaces of the cylindrical body are sealed, and other Since the condenser is constructed by fixing the liquid fluid conduit, the internal space that serves as the passage for the condensed liquid is designed so that the guide plates that make up the passage are arranged at a pitch that will most efficiently transfer heat according to the phase change of the fluid. By providing this, the three-dimensional structure can be made smaller.

また凝縮流体は面体上部から蛇行して内部空間を下部へ
流n1他の液状流体は下部から蛇行して前記筒体の保持
部の導管内を上部の流扛る構成にすることにより、熱伝
導性材料で一体成形された保持部に固着さ扛た導管を流
れる流体に熱が伝わりやすく、さらに対向流方式である
ことから効率よい凝縮器が得ら扛ることとなる。
In addition, the condensed fluid snakes from the upper part of the facepiece and flows through the inner space to the lower part.The other liquid fluid meanderes from the lower part and flows through the conduit of the holding part of the cylinder at the upper part, thereby improving heat conduction. Heat is easily transferred to the fluid flowing through the conduit that is fixed to the holding part integrally molded with a flexible material, and furthermore, since it is a counter-flow type, an efficient condenser can be obtained.

以下、本発明の一実施例を図面を用いて説明する。An embodiment of the present invention will be described below with reference to the drawings.

1は筒体、2は前記筒体1の内壁面から設けた案内板、
3は前記筒体1の外壁面から設けた保持部で、これらは
熱伝導性材料で一体成形しである。
1 is a cylindrical body; 2 is a guide plate provided from the inner wall surface of the cylindrical body 1;
Reference numeral 3 denotes a holding portion provided from the outer wall surface of the cylindrical body 1, and these are integrally molded from a thermally conductive material.

4.5はそnぞれ筒体1の両端面の密閉板、6は保持部
、3に固着した流体導管、7は前記筒体1に管である。
4.5 are sealing plates on both end faces of the cylinder 1, 6 is a holding portion, a fluid conduit fixed to 3, and 7 is a pipe connected to the cylinder 1.

以上のような構成において、凝縮流体はガス状で流入管
7から筒体1の内部空間に流入する。内部空間は凝縮流
体の通路を構成する案内板2があるのでこの案内板2に
沿ってガスは蛇行して下方へ流扛る。このとき、筒体1
の外壁面から設けた保持部3に固着された流体導管6を
下方から蛇行して流nてくる流体と熱交換し、気液2相
の状態になる。ガス状と気液2相状の熱伝達率は異なる
ので、熱伝達面を兼用する案内板2のピッチを最適化す
るように凝縮流体の状態変化に応じてピッチが変化して
いる。この変化している案内板2に沿って凝縮流体は凝
縮量を増し、完全液化した後に下部の流出管8から筒体
1を出るものである。
In the above configuration, the condensed fluid flows into the internal space of the cylindrical body 1 from the inflow pipe 7 in a gaseous state. In the internal space, there is a guide plate 2 that constitutes a passage for the condensed fluid, and the gas flows downward in a meandering manner along this guide plate 2. At this time, cylinder 1
Heat is exchanged with the fluid flowing in a meandering manner from below through a fluid conduit 6 fixed to a holding portion 3 provided from the outer wall surface of the fluid, resulting in a gas-liquid two-phase state. Since the heat transfer coefficients of the gaseous state and the gas-liquid two-phase state are different, the pitch of the guide plate 2, which also serves as a heat transfer surface, is changed in accordance with changes in the state of the condensed fluid so as to optimize the pitch. The amount of condensed fluid increases along this changing guide plate 2, and after being completely liquefied, it exits the cylinder 1 from the lower outlet pipe 8.

以上のような本発明の凝縮器において、凝縮液体の通路
は筒体1の内部空間に設・け、流路は熱伝達面と兼用し
た案内板2によシ構成さnている。
In the condenser of the present invention as described above, the passage for the condensed liquid is provided in the internal space of the cylindrical body 1, and the flow passage is constituted by the guide plate 2 which also serves as a heat transfer surface.

凝縮流体の熱交換においては、凝縮流体の相変化に伴な
い熱伝達率が異なるので、熱交換する対象である流体側
との相関において、凝縮流体側の熱伝達面の最適化構造
を取るように案内板2のピッチが、ガス域−9気液2相
域、液域の状態変化に応じて変えである。したがって本
発明の凝縮器においては外壁面から設けた保持部3に固
着した流体連室6を流詐る流体との間で、凝縮液体側の
全域にわたり最も効率よい熱交換を行なうように悄成さ
Cている。
In heat exchange of condensed fluid, since the heat transfer coefficient differs due to the phase change of the condensed fluid, it is necessary to optimize the structure of the heat transfer surface on the condensed fluid side in relation to the fluid side that is the target of heat exchange. The pitch of the guide plate 2 is changed according to changes in the state of the gas region-9, the gas-liquid two-phase region, and the liquid region. Therefore, the condenser of the present invention is designed to perform the most efficient heat exchange over the entire area on the condensed liquid side between the fluid flowing through the fluid communication chamber 6 fixed to the holding part 3 provided from the outer wall surface. There is a C.

また凝縮流体と、この凝縮流体と熱交換する流体とは対
向流の′型を取り、凝縮液体は上方から蛇行して下方へ
、熱交換対象流体は下方から蛇行して上方へ流すことに
より、熱交換対象流体が凝縮液体のガス域の扁温部の熱
と有効に熱交換することにより凝縮温度以上の熱交換流
体温度を得るようになっている。
In addition, the condensed fluid and the fluid that exchanges heat with the condensed fluid form counterflows, with the condensed fluid meandering downward from above and the fluid to be heat exchanged meandering upward from below. The fluid to be heat exchanged effectively exchanges heat with the heat of the cold part of the gas region of the condensed liquid, thereby obtaining a heat exchange fluid temperature higher than the condensation temperature.

以上のように熱伝導性材料で一体成形した筒体1の内部
空間の凝縮液体側熱伝達面を構成する案内板2の高密度
最適化と対向流方式の凝縮器構成により、立体小型化が
得られる。
As described above, three-dimensional miniaturization is achieved by optimizing the density of the guide plate 2 that constitutes the heat transfer surface on the condensed liquid side of the internal space of the cylinder 1 integrally molded with a thermally conductive material and by configuring the condenser using a counterflow method. can get.

さらに、凝縮液体とこれと熱交換する流体との間は二重
壁構造でかつ大気開放状態なので、どちらかの通路壁面
が破損しても他の流体側へ流n混入することもないので
ある。
Furthermore, since there is a double wall structure between the condensed liquid and the fluid that exchanges heat with it, and it is open to the atmosphere, even if one of the passage walls is damaged, there will be no flow into the other fluid side. .

以上のように本発明の凝#i器は流入管と流出管を有す
る筒体の内部空間に凝縮流体の通路金伺成する案内板の
ピッチをガス域、気液2相域、液域の状態に応じて変え
て内壁面から設け、保持部を外壁面から設けた筒体を熱
伝導性材料で一体成形し、前記筒体の両端面を密閉する
とともに前記保持部に他の液状流体導管全固着している
ので、面体の内部空間部に凝縮流体側の熱伝達[fik
状悪変化に応じて゛最適化構成にすることにより、立体
小型の凝縮器を得るとともに熱交換する流木間は二重壁
構造なので、1つの壁面が破損しても流体同志が混流す
ることを防止できる菱れた効果を奏するものである。
As described above, in the condenser of the present invention, the pitch of the guide plate forming the condensed fluid passageway in the internal space of the cylinder having the inflow pipe and the outflow pipe is adjusted to the gas region, gas-liquid two-phase region, and liquid region. A cylindrical body is provided from the inner wall surface depending on the situation, and a holder is provided from the outer wall surface. A cylindrical body is integrally molded with a thermally conductive material, both end surfaces of the cylindrical body are sealed, and another liquid fluid conduit is connected to the holder part. Since it is completely fixed, heat transfer from the condensed fluid side to the inner space of the facepiece [fik
By optimizing the configuration according to changes in the condition, a three-dimensional compact condenser can be obtained, and since the driftwood space that exchanges heat has a double wall structure, even if one wall is damaged, fluids will not mix with each other. It has a remarkable effect.

【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よる凝縮器の外観図、第2
図は一部縦断面図、第3図は横方向の一部縦断面図であ
る。 1・・・・・罰俸、2・・・・・案内板、3・・・・・
保持部、4.6・・・・・密閉板、6・・・・・流体導
管。 代理人の氏名 弁理士 中 尾 敏 男 ほか1名第3
FIG. 1 is an external view of a condenser according to an embodiment of the present invention, and FIG.
The figure is a partial vertical cross-sectional view, and FIG. 3 is a partial vertical cross-sectional view in the horizontal direction. 1...Punishment, 2...Information board, 3...
Holding part, 4.6...Sealing plate, 6...Fluid conduit. Name of agent: Patent attorney Toshio Nakao and 1 other person No. 3
figure

Claims (1)

【特許請求の範囲】[Claims] 流入管と流出管を有する筒体の内部空間に凝縮流体の通
路を構成する案内板のピッチをガス域気液2相域、液域
の状態に応じて変えて内壁面から設け、保持部を外壁面
から設けた筒体を熱伝導性材料で一体成形し、前記筒体
の両端面を密閉するとともに前記保持部に他の液状流体
導管を固着した凝縮器。
The pitch of the guide plate constituting the condensed fluid passage in the internal space of the cylinder having an inflow pipe and an outflow pipe is changed depending on the state of the gas region, gas-liquid two-phase region, and liquid region, and the holding part is installed from the inner wall surface. A condenser in which a cylindrical body provided from an outer wall surface is integrally molded with a thermally conductive material, both end surfaces of the cylindrical body are sealed, and another liquid fluid conduit is fixed to the holding part.
JP6909582A 1982-04-23 1982-04-23 Condenser Granted JPS58187786A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6909582A JPS58187786A (en) 1982-04-23 1982-04-23 Condenser

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6909582A JPS58187786A (en) 1982-04-23 1982-04-23 Condenser

Publications (2)

Publication Number Publication Date
JPS58187786A true JPS58187786A (en) 1983-11-02
JPS625274B2 JPS625274B2 (en) 1987-02-04

Family

ID=13392700

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6909582A Granted JPS58187786A (en) 1982-04-23 1982-04-23 Condenser

Country Status (1)

Country Link
JP (1) JPS58187786A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9227758B2 (en) 2010-11-12 2016-01-05 @Vance B.V. Auxiliary transport unit and method for use thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9227758B2 (en) 2010-11-12 2016-01-05 @Vance B.V. Auxiliary transport unit and method for use thereof

Also Published As

Publication number Publication date
JPS625274B2 (en) 1987-02-04

Similar Documents

Publication Publication Date Title
US4434112A (en) Heat transfer surface with increased liquid to air evaporative heat exchange
TW434395B (en) Heat exchanger
ITMI951001A1 (en) HEAT EXCHANGER
TWI672471B (en) Heat exchanger
JPS6142194B2 (en)
JPS58187786A (en) Condenser
US2452391A (en) Heat exchanger
JPH05340686A (en) Heat-exchanger
CN111692896A (en) Hot melt type gas-liquid two-phase heat exchange core structure
SU1657919A1 (en) Heat exchanger
JPS6334489A (en) Heat exchanger
JPS6034938Y2 (en) Heat pipe heat exchanger
JPS59109778A (en) Heat exchanger of condenser type
JPS59115983A (en) Heat exchanger
JPS6222774Y2 (en)
CN108458609A (en) A kind of plate-type heat-exchange unit
KR200349474Y1 (en) Thermosiphon Heat Pipe Type Heat Exchanger
CN212870851U (en) Novel heat exchanger
JPS59112189A (en) Heat exchanger
JPS58219374A (en) Heat exchanger for heating water
JPS6229592U (en)
JP3411792B2 (en) Vertical heat exchanger
JP2694894B2 (en) Heat exchanger
JPS5956088A (en) Heat exchanger
JPH0320700Y2 (en)