JPS629184A - Heat exchanger - Google Patents
Heat exchangerInfo
- Publication number
- JPS629184A JPS629184A JP14716685A JP14716685A JPS629184A JP S629184 A JPS629184 A JP S629184A JP 14716685 A JP14716685 A JP 14716685A JP 14716685 A JP14716685 A JP 14716685A JP S629184 A JPS629184 A JP S629184A
- Authority
- JP
- Japan
- Prior art keywords
- heat exchanger
- heat transfer
- tube
- exchanger tube
- core material
- 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
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
- F28F13/06—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/10—Heat-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 being arranged one within the other, e.g. concentrically
- F28D7/12—Heat-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 being arranged one within the other, e.g. concentrically the surrounding tube being closed at one end, e.g. return type
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
〔発明の技術分野〕
本発明は、熱交換器に係り、たとえばスターリングエン
ジンのヒータに組込むの和好適する熱交換器に関する。DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to a heat exchanger, and more particularly, to a heat exchanger suitable for being incorporated into a heater of a Stirling engine, for example.
最近、省エネルギ化の一環として、スターリングエンジ
ンが見直され、熱心な研究が行われている。スターリン
グエンジンには種々の形態のものがあるが、たとえば、
2ピストン方式のものを例にとると、それぞれパワーピ
ストンを内蔵したパワーシリンダ間に再生熱交換器を閉
流路構成に接続するとともに再生熱交換器の一端と一方
のパワーシリンダとの間の流路をヒータで加熱し、再生
熱交換器の他端と他方のパワーシリンダとの間の流路を
ターラで冷却するように構成されている。Recently, as part of efforts to save energy, the Stirling engine has been reviewed and intensive research is being conducted. There are various types of Stirling engines, for example,
Taking a two-piston type as an example, a regenerative heat exchanger is connected in a closed flow path configuration between power cylinders each containing a built-in power piston, and the flow between one end of the regenerative heat exchanger and one power cylinder is The passage is heated by a heater, and the passage between the other end of the regenerative heat exchanger and the other power cylinder is cooled by a roller.
この機関は、理論的熱効率が高く、あらゆる熱源を使用
できると言う特徴を有している。This engine is characterized by its high theoretical thermal efficiency and the ability to use any heat source.
ところで、スターリングエンジンの出力は、シリンダー
内のピストン移動による最大空間容積。By the way, the output of a Stirling engine is determined by the maximum space volume created by the movement of the piston inside the cylinder.
温度比9機械効率等によっても左右されるが、ヒータ等
における死空間容積(デッドスペース)によっても左右
され、デッドスペースが小さい程。Temperature ratio 9 It depends on mechanical efficiency, etc., but it also depends on dead space in heaters, etc., and the smaller the dead space, the smaller the dead space.
出力を増加させることができる。このため、このエンジ
ンのヒータに組込まれる熱交換器としては。Output can be increased. Therefore, as a heat exchanger incorporated in the heater of this engine.
デッドスペースとなり得る空間が可能な限り小さいもの
が望まれる。しかし、他方においては、ヒータでの加熱
温度が高い程効率を向上させることができるので、この
エンジンのヒータに組込まれる熱交換器は十分に広い伝
熱面積を有していることも必要条件となる。It is desired that the space that can become dead space be as small as possible. However, on the other hand, the higher the heating temperature in the heater, the higher the efficiency, so it is also a necessary condition that the heat exchanger built into the engine heater has a sufficiently large heat transfer area. Become.
このようなことから、従来、スターリングエンジンのヒ
ータに組込まれる熱交換器として、内径1〜4INR程
度の細い伝熱管を多数使用して熱交換器を構成する提案
がなされている。しかしながら。For this reason, it has been proposed to use a large number of thin heat transfer tubes with an inner diameter of about 1 to 4 INR to construct a heat exchanger to be incorporated into a Stirling engine heater. however.
このような構成の熱交換器では、多数の細い伝熱管をシ
リンダのヘッドに接続する必要があるため。This is because a heat exchanger with this configuration requires a large number of thin heat transfer tubes to be connected to the cylinder head.
溶接箇所が多く、溶接作業が非常に面倒化するばかりか
、溶接箇所が多いことが原因して作動流体が漏れ易く、
装置としての信頼性に欠けると言う問題があった。There are many welding points, which not only makes welding work extremely troublesome, but also causes the working fluid to leak easily due to the large number of welding points.
There was a problem that the device lacked reliability.
そこで、このような問題を解消するために、特開昭58
−167863号公報に示されているように、大径の伝
熱管を使用することによって伝熱面積の増大化を図り、
また、大径の伝熱管を使用したことによって起こるデッ
ドスペースの増加を抑えるために伝熱管内に芯材を挿設
して熱が伝わる方向と同方向の流路幅(あるいは厚み)
を小さくするようにした熱交換器の提案もなされている
。Therefore, in order to solve this problem,
As shown in Publication No. 167863, the heat transfer area is increased by using large diameter heat transfer tubes,
In addition, in order to suppress the increase in dead space caused by the use of large diameter heat transfer tubes, a core material is inserted into the heat transfer tubes to increase the channel width (or thickness) in the same direction as the heat transfer direction.
There have also been proposals for heat exchangers that have a smaller size.
このような構成の熱交換器では、細い伝熱管を用いたも
のとは違って、溶接箇所を大幅に減少させることができ
る。しかし、伝熱面積をざらに増加させようとすると、
さらに大径の伝熱管を使用するか、伝熱管の数を増加さ
せる必要があり、限られたスペース内で伝熱面積を増大
させるのには限界があった。A heat exchanger with such a configuration can significantly reduce the number of welding points, unlike a heat exchanger using thin heat exchanger tubes. However, if you try to roughly increase the heat transfer area,
Furthermore, it is necessary to use heat exchanger tubes with a larger diameter or increase the number of heat exchanger tubes, and there is a limit to increasing the heat transfer area within a limited space.
さらに、上述した2種類の熱交換器に共通に言えること
は、シリンダとピストンとの間の隙間を通して作動空間
内に侵入した潤滑油に起因する伝熱管の腐蝕を如何にし
て防止するかと言う点である。すなわち、スターリング
エンジンのヒータに組込まれる熱交換器の伝熱管は9通
常数100℃にも加熱される。作動空間に侵入した潤滑
油が上記温度に加熱されると分解し、この分解成分によ
って伝熱管の腐蝕が促進される。したがって、この腐蝕
に対する対策も解決する必要があった。Furthermore, what is common to the two types of heat exchangers mentioned above is how to prevent corrosion of the heat transfer tubes caused by lubricating oil that has entered the working space through the gap between the cylinder and piston. It is. That is, the heat exchanger tubes of the heat exchanger incorporated in the heater of the Stirling engine are usually heated to several 100 degrees Celsius. When the lubricating oil that has entered the working space is heated to the above temperature, it decomposes, and the decomposed components accelerate corrosion of the heat exchanger tubes. Therefore, it was necessary to find a countermeasure against this corrosion.
本発明は、このような事情に鑑みてなされたもので、そ
の目的とするところは、溶接作業の簡素化および作動流
体の漏れ防止化を図れるとともに限られたスペース内に
おいて伝熱面積の増大化を図れ、しかも耐腐蝕性に冨ん
だ熱交換器を提供することにある。The present invention was made in view of the above circumstances, and its purpose is to simplify welding work, prevent leakage of working fluid, and increase heat transfer area within a limited space. It is an object of the present invention to provide a heat exchanger which is capable of achieving high corrosion resistance and is highly corrosion resistant.
(発明の概要〕
本発明によれば、一端側が閉じられた外側伝熱管と、こ
の外側伝熱管内に挿設された伝熱芯材と。(Summary of the Invention) According to the present invention, there is provided an outer heat transfer tube with one end closed, and a heat transfer core inserted into the outer heat transfer tube.
この伝熱芯材と前記外側伝熱管との間に挿設され上記外
側伝熱管と上記伝熱芯材との間に上記外側伝熱管の他端
側から前記一端側へ向けて延びた後。After being inserted between the heat transfer core material and the outer heat transfer tube and extending between the outer heat transfer tube and the heat transfer core material from the other end side of the outer heat transfer tube toward the one end side.
上記一端側で折返して上記他端側へ向けて延びる折返し
流体通路を形成する内側伝熱管と、この内側伝熱管の外
面に一体的に、かつ前記外側伝熱管の内面に密接する高
さに形成され前記折返し流体通路の上記内側伝熱管と前
記外側伝熱管との間に位置する部分を周方向に複数に区
画する複数の第1の突条と、前記内側伝熱管の内面また
は前記伝熱芯材の外面の何れか一方に一体的に、かつ他
方に密接する高さに設けられ前記折返し流体通路の上記
内側伝熱管と上記伝熱芯材との間に位置する部分を周方
向に複数に区画する複数の第2の突条と、前記外側伝熱
管の内面、前記内側伝熱管の内外面および前記伝熱芯材
の外面にそれぞれ設けられたメッキ層とを備えた熱交換
器が提供される。an inner heat exchanger tube that is folded back at the one end side to form a folded fluid passage extending toward the other end side; and an inner heat exchanger tube formed integrally with the outer surface of the inner heat exchanger tube and at a height close to the inner surface of the outer heat exchanger tube. a plurality of first protrusions dividing a portion of the folded fluid passage located between the inner heat transfer tube and the outer heat transfer tube into a plurality of sections in the circumferential direction; and an inner surface of the inner heat transfer tube or the heat transfer core. A plurality of portions in the circumferential direction are provided integrally on one of the outer surfaces of the material and at a height close to the other and located between the inner heat transfer tube and the heat transfer core material of the folded fluid passage. A heat exchanger is provided, comprising a plurality of partitioning second protrusions, and plating layers provided on the inner surface of the outer heat transfer tube, the inner and outer surfaces of the inner heat transfer tube, and the outer surface of the heat transfer core material. Ru.
本発明によれば、外側伝熱管の外面を高温流体に接触さ
せ、前述した折返し流体通路に低温流体を通流させると
、高温流体の熱は、外側伝熱管の外面〜外側伝熱管〜外
側伝熱管の内面〜低温流体からなる第1の経路と、外側
伝熱管の外面〜外側伝熱管〜外側伝熱管の内面〜第1の
突条〜内側伝熱管〜内側伝熱管の内・外面〜低温流体か
らなる第2の経路と、外側伝熱管の外面〜外側伝熱管〜
外側伝熱管の内面〜第1の突条〜内側伝熱管〜第2の突
条〜伝熱芯材〜伝熱芯材の外面〜低温流体からなる第3
の経路との3つの経路で低温流体に伝わることになる。According to the present invention, when the outer surface of the outer heat exchanger tube is brought into contact with the high temperature fluid and the low temperature fluid is caused to flow through the above-mentioned folded fluid passage, the heat of the high temperature fluid is transferred from the outer surface of the outer heat exchanger tube to the outer heat exchanger tube and the outer side. The first path consisting of the inner surface of the heat exchanger tube - the low temperature fluid, and the outer surface of the outer heat exchanger tube - the outer heat exchanger tube - the inner surface of the outer heat exchanger tube - the first protrusion - the inner heat exchanger tube - the inner and outer surfaces of the inner heat exchanger tube - the low temperature fluid. and the outer surface of the outer heat exchanger tube ~ the outer heat exchanger tube ~
Inner surface of the outer heat transfer tube - first protrusion - inner heat transfer tube - second protrusion - heat transfer core material - outer surface of the heat transfer core material - third layer made of low-temperature fluid
It is transmitted to the low-temperature fluid through three routes:
したがって、外側伝熱管の内径を等しいとして比較する
と、芯材を挿設して伝熱管内に単に折返し流路を形成し
たものに較べて伝熱面積を倍以上に拡大させることがで
きる。このため、全体の小形化を図った状態で、なおか
つ熱交換効率を向上させることができる。また、第1お
よび第2の突条の高さの選択で、伝熱面積をそれ程減少
させることなく折返し流体通路における熱の伝わる方向
と同方向の幅(あるいは厚み)を十分小さくできる。し
たがって、デッドスペースとなり得る空間の小さい構造
とすることができる。さらに、外側伝熱管の内面、内側
伝熱管の内外面、および伝熱芯材の外面にメッキ層を設
けているので、このメッキ層の材質を選択することによ
って折返し流体通路内に腐蝕成分が侵入した場合であっ
ても、これによって構成部材が腐蝕されるのを防止でき
る。このように、伝熱面積を十分広く取れるとともにデ
ッドスペースとなり得る空間を狭くでき、しかも耐腐蝕
性を向上させることができるので、スターリングエンジ
ンのヒータ等に組込むのに適した熱交換器を得ることが
できる。Therefore, when compared assuming that the inner diameters of the outer heat exchanger tubes are the same, the heat transfer area can be more than doubled compared to a case in which a core material is inserted to simply form a folded passage in the heat exchanger tube. Therefore, it is possible to improve the heat exchange efficiency while reducing the overall size. Further, by selecting the heights of the first and second protrusions, the width (or thickness) in the same direction as the heat transfer direction in the folded fluid passage can be made sufficiently small without reducing the heat transfer area so much. Therefore, it is possible to create a structure with a small space that can become a dead space. Furthermore, since plating layers are provided on the inner surface of the outer heat transfer tube, the inner and outer surfaces of the inner heat transfer tube, and the outer surface of the heat transfer core material, corrosive components can enter the folded fluid passage by selecting the material for this plating layer. Even in such a case, it is possible to prevent the structural members from being corroded. In this way, it is possible to obtain a heat exchanger that is suitable for being incorporated into a heater of a Stirling engine, etc., since a sufficiently large heat transfer area can be obtained, a space that can become a dead space can be narrowed, and corrosion resistance can be improved. I can do it.
以下1本発明の実施例を図面を参照しながら説明する。 An embodiment of the present invention will be described below with reference to the drawings.
第1図は1本発明の一実施例に係る熱交換器をヒータに
組込んでなる2ピストン方式のスターリングエンジンの
縦断面図を示している。FIG. 1 shows a longitudinal sectional view of a two-piston Stirling engine in which a heat exchanger according to an embodiment of the present invention is incorporated into a heater.
すなわち、このスターリングエンジンは、大きく別けて
1作動流体の膨張用に供されるパワーシリンダ1(以後
、膨張シリンダと称す。)と、この膨張シリンダ1内に
摺動自在に装着されたパワーピストン2(以後、膨張ピ
ストンと称す。)と。That is, this Stirling engine is broadly divided into a power cylinder 1 (hereinafter referred to as an expansion cylinder) used for expanding one working fluid, and a power piston 2 slidably mounted within the expansion cylinder 1. (Hereafter referred to as the expansion piston.)
作動流体の圧縮用に供されるパワーシリンダ3(以後、
圧縮シリンダと称す。)と、この圧縮シリンダ3内に囲
動自在に装着されたパワーピストン4(以俊、圧縮ピス
トンと称す。)と、膨張シリンダ1と圧縮シリンダ3と
の間に設けられたヒータ5.再生熱交換器6およびクー
ラ7と、膨張ピストン2および圧縮ピストン4にそれぞ
れコンロッド8,9.クランク軸10.11を介して連
結された出力軸12とで構成されている。Power cylinder 3 (hereinafter referred to as
It is called a compression cylinder. ), a power piston 4 (referred to as a compression piston by Ishitoshi) mounted movably within the compression cylinder 3, and a heater 5 provided between the expansion cylinder 1 and the compression cylinder 3. Connecting rods 8, 9 . It consists of an output shaft 12 connected via a crankshaft 10.11.
前記ヒータ5は、膨張シリンダ1のヘッド13を取り囲
むように断熱材14を配置して形成された燃焼室15と
、この燃焼室15内に配置された複数の熱交換器16と
、燃焼v15に臨むように配置されたバーナ17と、燃
焼に必要な空気を燃焼ガスで予熱する予熱器18とで構
成されている。The heater 5 includes a combustion chamber 15 formed by arranging a heat insulating material 14 so as to surround the head 13 of the expansion cylinder 1, a plurality of heat exchangers 16 arranged within the combustion chamber 15, and a combustion v15. It is comprised of a burner 17 placed so as to face the engine, and a preheater 18 that preheats the air necessary for combustion with combustion gas.
前記各熱交換器16は、それぞれ外形が棒状に形成され
おり、各流体通路の一端側を膨張シリンダ1内の頂部に
通じさせ、他端側をヘッド13内に形成されたマニホル
ド19に通じさせて、全体で漏斗を形成する如く配置さ
れている。そして。Each of the heat exchangers 16 has a rod-like outer shape, and one end of each fluid passage communicates with the top of the expansion cylinder 1, and the other end communicates with a manifold 19 formed within the head 13. They are arranged so as to form a funnel as a whole. and.
各熱交換器16は、具体的には第2図および第3図に示
すように構成されている。すなわち、この熱交換器16
は、大きく分けて、一端側が閉じられ、他端側が解放さ
れた外側伝熱管21と、この外側伝熱管21内に同心的
に挿設された両端解放の内側伝熱管22と、この内側伝
熱管22内に同心的に、挿設された伝熱芯材23とで構
成されている。外側伝熱管21は、熱伝導率が良く、シ
かも耐熱性および対圧性に富んだ材料で形成されたもの
で、その内面にはニッケルメッキが施してあり。Each heat exchanger 16 is specifically constructed as shown in FIGS. 2 and 3. That is, this heat exchanger 16
Broadly divided, the outer heat exchanger tube 21 is closed at one end and open at the other end, the inner heat exchanger tube 22 is inserted concentrically into the outer heat exchanger tube 21 and both ends are open, and the inner heat exchanger tube 21 is open at both ends. 22 and a heat transfer core material 23 inserted concentrically therein. The outer heat exchanger tube 21 is made of a material with good thermal conductivity, heat resistance, and pressure resistance, and its inner surface is nickel plated.
また、その外周面の先端側、つまり閉じられている側に
はフィン24が複数突設されている。内側伝熱管22は
、外側伝熱管21より熱伝導率のよい、たとえば銅で外
側伝熱管21より所定だけ長めに形成されており、一方
の端部25が外側伝熱管21の閉塞壁から所定距離だけ
離れるとともに他方の端部26が外側伝熱管21より突
出する状態に外側伝熱管21内に挿設されている。そし
て。Further, a plurality of fins 24 are provided protruding from the tip side of the outer circumferential surface, that is, the closed side. The inner heat exchanger tube 22 is made of a material having better thermal conductivity than the outer heat exchanger tube 21 , for example, copper, and is formed to be longer than the outer heat exchanger tube 21 by a predetermined length, and one end 25 is a predetermined distance from the closed wall of the outer heat exchanger tube 21 . It is inserted into the outer heat exchanger tube 21 such that the other end 26 protrudes from the outer heat exchanger tube 21 while being separated by the same amount. and.
この内側伝熱管22の外面には、第3図にも示すように
周方向の4箇所に亙ってそれぞれ軸方向に延びる突条2
7が一体的に形成されている。この突条27は、内側伝
熱管22を外側伝熱管21内に第2図5示すように挿設
したとき外側伝熱管21の内面に密接する高さに形成さ
れている。また、内側伝熱管22の内・外面にはニッケ
ルメッキが施されている。伝熱芯材23は、同じく銅な
どで内側伝熱管22より若干長めに形成されている。こ
の伝熱芯材23は、その一方の端部28が外側伝熱管2
1の閉塞壁より所定距離だけ離れるとともに内側伝熱管
22の端部25より所定距離だけ突出し、他方の端部2
9が内側伝熱管22の端部26と面一となり、しかも後
述する突条30が前記突条27の設けられている位置と
重合する状態に内側伝熱管22内に挿設されている。伝
熱芯材23の外面には第3図にも示すように周方向の4
箇所に亙ってそれぞれ軸方向に延びる突条30が一体的
に形成さ6れている。この突条30は。On the outer surface of the inner heat exchanger tube 22, as shown in FIG.
7 is integrally formed. The protrusions 27 are formed at such a height that they come into close contact with the inner surface of the outer heat exchanger tube 21 when the inner heat exchanger tube 22 is inserted into the outer heat exchanger tube 21 as shown in FIG. 5. Further, the inner and outer surfaces of the inner heat exchanger tube 22 are nickel plated. The heat transfer core material 23 is also made of copper or the like and is formed to be slightly longer than the inner heat transfer tube 22. This heat transfer core material 23 has one end 28 connected to the outer heat transfer tube 2.
1, and protrudes from the end 25 of the inner heat exchanger tube 22 by a predetermined distance, and the other end 2
9 is inserted into the inner heat exchanger tube 22 so that it is flush with the end 26 of the inner heat exchanger tube 22, and a protrusion 30, which will be described later, overlaps the position where the protrusion 27 is provided. As shown in FIG. 3, the outer surface of the heat transfer core material 23 has four
Projections 30 extending in the axial direction are integrally formed 6 over the locations. This protrusion 30 is.
伝熱芯材23を内側伝熱管22内に第2図に示すように
挿設したとき内側伝熱管22の内面に密接する高さに形
成されている。また、伝熱芯材23の外面にはニッケル
メッキが施されている。When the heat transfer core material 23 is inserted into the inner heat transfer tube 22 as shown in FIG. 2, it is formed at such a height that it comes into close contact with the inner surface of the inner heat transfer tube 22. Further, the outer surface of the heat transfer core material 23 is plated with nickel.
上記のように構成された各熱交換器16は、第1図に示
すように内側伝熱管22の端部26が膨張シリンダ1内
の頂部に通じる関係にヘッド13に溶接接続され、また
外側伝熱管21の解放端31がマニホルド19に通じる
関係にヘッド13に溶接接続されている。Each heat exchanger 16 configured as described above is welded to the head 13 such that the end 26 of the inner heat exchanger tube 22 communicates with the top in the expansion cylinder 1, as shown in FIG. The open end 31 of the heat tube 21 is welded to the head 13 in communication with the manifold 19 .
しかして、マニホルド19は、接続管32を介して再生
熱交換器6に接続され、この再生熱交換器6は熱交換器
によって構成されたクーラ7を介して圧縮シリンダ3内
の頂部に接続されている。Thus, the manifold 19 is connected to the regenerative heat exchanger 6 via the connecting pipe 32, and the regenerative heat exchanger 6 is connected to the top inside the compression cylinder 3 via the cooler 7 constituted by the heat exchanger. ing.
そして、膨張シリンダ1と膨張ピストン2とで囲まれた
空間、各熱交換器16.マニホルド19゜接続管32.
再生熱交換器6.クーラ7、圧縮シリンダ3と圧縮ピス
トン4とで囲まれた空間からなる閉じられた空間には作
動流体としての)−1eが封入されている。A space surrounded by the expansion cylinder 1 and the expansion piston 2, each heat exchanger 16. Manifold 19° connection pipe 32.
Regenerative heat exchanger6. -1e as a working fluid is sealed in a closed space surrounded by the cooler 7, the compression cylinder 3, and the compression piston 4.
なお、第1図中、33は潤滑油が所定レベルまで収容さ
れたクランク室を示し、34.35はリニアベアリング
を示し、36はクーラ7の冷媒を案内する配管を示して
いる。In FIG. 1, numeral 33 indicates a crank chamber containing lubricating oil up to a predetermined level, numerals 34 and 35 indicate linear bearings, and numeral 36 indicates piping for guiding the refrigerant of the cooler 7.
このような構成であると、バーナ17に点火するととも
に配管36に冷媒を通流させている状態で、外部動力源
によって出力軸12を一時的に回転させると、この出力
軸12にクランク軸10゜11、コンロッド8.9を介
して連結されている膨張ピストン2および圧縮ピストン
4がある位相差を以て往復動する。この往復動によって
膨張ピストン2が圧縮行程に移ると、膨張シリンダ1内
のHeが各熱交換器16.マニホルド19.接続管32
.再生熱交換器6.クーラ7を介して圧縮シリンダ3内
に流れ込み、膨張ピストン2が上死点に達した時点でH
eのほとんどが圧縮シリンダ3内に流れ込む。このとき
、Heは再生熱交換器6を通過する間に、その保有して
いる熱を再生熱交換器6に奪われ、またクーラ7を通過
する間にさらに冷却される。出力軸12の回転に伴って
圧縮ピストン4が下死点から上死点に向けて移動を開始
すると、圧縮シリンダ3内の低温のHeが圧縮され、い
ままでとは逆の経路で膨張シリンダ1内へ流れ込む。こ
のとき、Heは再生熱交換器6を通過する間に吸熱して
高温に加熱され9次に各熱交換器16を通過する間にさ
らに加熱される。With such a configuration, when the output shaft 12 is temporarily rotated by an external power source while the burner 17 is ignited and the refrigerant is flowing through the pipe 36, the output shaft 12 is connected to the crankshaft 10. 11, the expansion piston 2 and the compression piston 4, which are connected via the connecting rod 8.9, reciprocate with a certain phase difference. When the expansion piston 2 moves to the compression stroke due to this reciprocating movement, He in the expansion cylinder 1 is transferred to each heat exchanger 16. Manifold 19. Connecting pipe 32
.. Regenerative heat exchanger6. It flows into the compression cylinder 3 via the cooler 7, and when the expansion piston 2 reaches the top dead center, H
Most of e flows into the compression cylinder 3. At this time, while the He passes through the regenerative heat exchanger 6, its retained heat is taken away by the regenerative heat exchanger 6, and while it passes through the cooler 7, it is further cooled. When the compression piston 4 begins to move from the bottom dead center toward the top dead center as the output shaft 12 rotates, the low-temperature He in the compression cylinder 3 is compressed, and is moved to the expansion cylinder 1 in the opposite path. Flow inward. At this time, He absorbs heat while passing through the regenerative heat exchanger 6 and is heated to a high temperature, and is further heated while passing through each heat exchanger 16.
膨張シリンダ1内に流れ込んだ高温のHeは、膨張して
膨張ピストン2を押し下げる。以後、上述した動作が繰
り返され、外部動力源を断った状態でも出力軸12が回
転を継続し、スターリングエンジンとしての機能を発揮
する。The high temperature He that has flowed into the expansion cylinder 1 expands and pushes down the expansion piston 2. Thereafter, the above-described operations are repeated, and even when the external power source is cut off, the output shaft 12 continues to rotate, and functions as a Stirling engine.
ところで、Heは上記のように膨張シリンダ1と圧縮シ
リンダ3との間を移動するのであるが。By the way, He moves between the expansion cylinder 1 and the compression cylinder 3 as described above.
このHeが各熱交換器16を通過するときには次のよう
な経路を通る。すなわち、今、Heがマニホルド19か
ら膨張シリンダ1に向けて流れる場合を例にとると、各
熱交換器16の外側伝熱管21の解放端31がマニホル
ド19に通じ、内側伝熱管22の端部26が膨張シリン
ダ1内の頂部に通じていることからして、Heは第2図
中に実線矢印で示すように、外側伝熱管21と内側伝熱
管22との間に、突条27の存在によって周方向に4つ
に区画形成された通路41を軸心線に沿って外側伝熱管
21の閉塞壁側へと流れ2.閉塞壁近傍で折返し、続い
て内側伝熱管22と伝熱芯材23との間に、突条30の
存在によって周方向に4つに区画形成された通路42を
軸心線に沿って流れた後、膨張シリンダ1へと流れる。When this He passes through each heat exchanger 16, it passes through the following route. That is, taking as an example the case where He flows from the manifold 19 toward the expansion cylinder 1, the open end 31 of the outer heat exchanger tube 21 of each heat exchanger 16 communicates with the manifold 19, and the end of the inner heat exchanger tube 22 communicates with the manifold 19. 26 communicates with the top inside the expansion cylinder 1, He indicates the existence of the protrusion 27 between the outer heat exchanger tube 21 and the inner heat exchanger tube 22, as shown by the solid arrow in FIG. Flows along the axis of the passage 41, which is divided into four sections in the circumferential direction, toward the closed wall of the outer heat exchanger tube 21.2. It turned around near the closing wall, and then flowed along the axis through a passage 42 that was divided into four sections in the circumferential direction by the presence of the protrusions 30 between the inner heat transfer tube 22 and the heat transfer core material 23. After that, it flows to the expansion cylinder 1.
各熱交換器16は燃焼室15内に位置している。したが
って、上記経路で熱交換器16内をHeが通流すると、
このHeは加熱されるが、この場合、各熱交換器16を
上記のように構成しているので効率よく加熱することが
できる。すなわち、燃焼室15で発生した熱は、外側伝
熱管21〜外側伝熱管21の内面〜Heからなる第1の
経路と、外側伝熱管21〜外側伝熱管21の内面〜突条
27〜内側伝熱管22の内・外面〜Heからなる第2の
経路と、外側伝熱管21〜外側伝熱管21の内面〜突条
27〜内側伝熱管22〜内側伝熱管22の内面〜突条3
0〜伝熱芯材23〜伝熱芯材23の外面〜Heからなる
第3の経路との3つの経路で1−1eに伝わる。したが
って、外側伝熱管21の内径と等しい伝熱管を使用し、
この伝熱管内に芯材を挿設して単なる折返し通路を形成
したものに較べて伝熱面積を数倍に拡大できる。このた
め、熱交換器16の交換効率の向上化および全体の小形
化を図ることができる。また、突条27.30の高さ低
く設定するだけで伝熱面積をほとんど減少させることな
しに各通路41.42の伝熱方向と同方向の厚みYを薄
くすることができ、この結果。Each heat exchanger 16 is located within the combustion chamber 15. Therefore, when He flows through the heat exchanger 16 through the above path,
This He is heated, and in this case, since each heat exchanger 16 is configured as described above, it can be heated efficiently. That is, the heat generated in the combustion chamber 15 is transmitted through a first path consisting of the outer heat exchanger tube 21, the inner surface of the outer heat exchanger tube 21, and He, and the outer heat exchanger tube 21, the inner surface of the outer heat exchanger tube 21, the protrusion 27, and the inner surface. A second path consisting of the inner and outer surfaces of the heat exchanger tube 22 - He, and the outer heat exchanger tube 21 - the inner surface of the outer heat exchanger tube 21 - the protrusion 27 - the inner heat exchanger tube 22 - the inner surface of the inner heat exchanger tube 22 - the protrusion 3
It is transmitted to 1-1e through three routes: 0 to the heat transfer core material 23, the outer surface of the heat transfer core material 23, and a third path consisting of He. Therefore, using a heat exchanger tube that has the same inner diameter as the outer heat exchanger tube 21,
The heat transfer area can be expanded several times compared to a case where a core material is inserted into the heat transfer tube to form a simple folded passage. Therefore, it is possible to improve the exchange efficiency of the heat exchanger 16 and to downsize the entire heat exchanger 16. Furthermore, by simply setting the height of the protrusions 27.30 low, the thickness Y of each passage 41.42 in the same direction as the heat transfer direction can be reduced without substantially reducing the heat transfer area.
スターリングエンジンにとって最も好ましい熱交換器、
つまりデッドスペースとなり得る空間の小さい熱交換器
を実現できる。また、外側伝熱管21の内面、内側伝熱
管22の内・外面および伝熱芯材23の外面にニッケル
メッキを施すようにしているので、運転中に、たとえi
m滑油が侵入した場合であっても上記メッキ層の存在で
熱交換器構成材料が腐蝕されるのを防止でき、結局、前
述した効果を発運させることができる。The most preferred heat exchanger for Stirling engines,
In other words, it is possible to realize a heat exchanger with a small space that can become a dead space. In addition, since nickel plating is applied to the inner surface of the outer heat transfer tube 21, the inner and outer surfaces of the inner heat transfer tube 22, and the outer surface of the heat transfer core material 23, even if the
Even if lubricating oil enters the heat exchanger, the presence of the plating layer prevents the heat exchanger constituent materials from being corroded, and as a result, the above-mentioned effects can be achieved.
なお2本発明は上述した実施例に限定されるものではな
く種々変形することができる。すなわち。Note that the present invention is not limited to the embodiments described above, and can be modified in various ways. Namely.
上記実施例では突条30を伝熱芯材23に設けているが
、これは内側伝熱管22の内面に一体的に設けてもよい
。また、メッキ層は、ニッケルメッキ層に限られるもの
ではなく、使用する潤滑油との関係において選択すれば
よい。また1本発明に係る熱交換器はスターリングエン
ジンだけにその使用を限定されるものではなく各種流体
間の熱交換に使用できることは勿論である。その他2本
発明の要旨を逸脱しない範囲で種々変形することができ
る。In the above embodiment, the protrusions 30 are provided on the heat transfer core material 23, but they may be provided integrally on the inner surface of the inner heat transfer tube 22. Furthermore, the plating layer is not limited to the nickel plating layer, and may be selected depending on the lubricating oil used. Further, the use of the heat exchanger according to the present invention is not limited to Stirling engines, but can of course be used for heat exchange between various fluids. Other 2 Various modifications can be made without departing from the gist of the present invention.
第1vIは本発明の一実施例に係る熱交換器を組込んで
なるスターリングエンジンの縦断面図、第2図は同エン
ジンのヒータに組込まれた熱交換器の縦断面図、第3図
は同熱交換器を第2図におけるX−X線に沿って切断し
矢印方向に見た図である。
1・・・膨張シリンダ、2・・・膨張ピストン、31°
圧縮シリンダ、4・・・圧縮ピストン、5・・・ヒータ
、6・・・再生熱交換器、7・・・クーラ、16・・・
熱交換器。
21・・・外側伝熱管、22・・・内側伝熱管、23・
・・伝熱芯材、24・・・フィン、27.30・・・突
条、41゜42・・・折返し流体通路を構成する通路。1vI is a longitudinal sectional view of a Stirling engine incorporating a heat exchanger according to an embodiment of the present invention, FIG. 2 is a longitudinal sectional view of a heat exchanger incorporated in a heater of the engine, and FIG. FIG. 3 is a view of the heat exchanger cut along the line XX in FIG. 2 and viewed in the direction of the arrow. 1... Expansion cylinder, 2... Expansion piston, 31°
Compression cylinder, 4... Compression piston, 5... Heater, 6... Regeneration heat exchanger, 7... Cooler, 16...
Heat exchanger. 21...Outer heat exchanger tube, 22...Inner heat exchanger tube, 23.
... Heat transfer core material, 24 ... Fin, 27.30 ... Projection, 41° 42 ... Passage constituting the folded fluid passage.
Claims (3)
熱管内に挿設された伝熱芯材と、この伝熱芯材と前記外
側伝熱管との間に挿設され上記外側伝熱管と上記伝熱芯
材との間に上記外側伝熱管の他端側から前記一端側へ向
けて延びた後、上記一端側で折返して上記他端側へ向け
て延びる折返し流体通路を形成する内側伝熱管と、この
内側伝熱管の外面に一体的に、かつ前記外側伝熱管の内
面に密接する高さに形成され前記折返し流体通路の上記
内側伝熱管と前記外側伝熱管との間に位置する部分を周
方向に複数に区画する複数の第1の突条と、前記内側伝
熱管の内面または前記伝熱芯材の外面の何れか一方に一
体的に、かつ他方に密接する高さに設けられ前記折返し
流体通路の上記内側伝熱管と上記伝熱芯材との間に位置
する部分を周方向に複数に区画する複数の第2の突条と
、前記外側伝熱管の内面、前記内側伝熱管の内外面およ
び前記伝熱芯材の外面にそれぞれ設けられたメッキ層と
を具備してなることを特徴とする熱交換器。(1) An outer heat transfer tube with one end closed, a heat transfer core inserted into the outer heat transfer tube, and an outer heat transfer tube inserted between the heat transfer core and the outer heat transfer tube. and the heat transfer core material to form a folded fluid passage that extends from the other end of the outer heat transfer tube toward the one end, is folded back at the one end, and extends toward the other end. a heat exchanger tube, and is formed integrally with the outer surface of the inner heat exchanger tube and at a height close to the inner surface of the outer heat exchanger tube, and is located between the inner heat exchanger tube and the outer heat exchanger tube of the folded fluid passage. A plurality of first protrusions dividing the portion into a plurality of parts in the circumferential direction, and provided integrally with either the inner surface of the inner heat transfer tube or the outer surface of the heat transfer core material and at a height close to the other. a plurality of second protrusions dividing a portion of the folded fluid passage located between the inner heat transfer tube and the heat transfer core material into a plurality of sections in the circumferential direction; A heat exchanger comprising plating layers provided on the inner and outer surfaces of a heat tube and the outer surface of the heat transfer core material.
熱管より熱伝導率の高い材料で形成されてなることを特
徴とする特許請求の範囲第1項記載の熱交換器。(2) The heat exchanger according to claim 1, wherein the inner heat transfer tube and the heat transfer core material are formed of a material having higher thermal conductivity than the outer heat transfer tube.
を特徴とする特許請求の範囲第1項記載の熱交換器。(3) The heat exchanger according to claim 1, wherein the plating layer is a nickel plating layer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14716685A JPH0631692B2 (en) | 1985-07-04 | 1985-07-04 | Heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14716685A JPH0631692B2 (en) | 1985-07-04 | 1985-07-04 | Heat exchanger |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS629184A true JPS629184A (en) | 1987-01-17 |
| JPH0631692B2 JPH0631692B2 (en) | 1994-04-27 |
Family
ID=15424078
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP14716685A Expired - Fee Related JPH0631692B2 (en) | 1985-07-04 | 1985-07-04 | Heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0631692B2 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01249953A (en) * | 1988-03-31 | 1989-10-05 | Toshiba Corp | Heater of stirling engine |
| WO2006111315A1 (en) * | 2005-04-18 | 2006-10-26 | Unical Ag S.P.A. | Protected carbon steel pipe for fire tube heat exchange devices, particularly boilers |
| CN111720236A (en) * | 2019-03-20 | 2020-09-29 | 内蒙古工业大学 | Heaters and Stirling Engines in Stirling Engines |
-
1985
- 1985-07-04 JP JP14716685A patent/JPH0631692B2/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01249953A (en) * | 1988-03-31 | 1989-10-05 | Toshiba Corp | Heater of stirling engine |
| WO2006111315A1 (en) * | 2005-04-18 | 2006-10-26 | Unical Ag S.P.A. | Protected carbon steel pipe for fire tube heat exchange devices, particularly boilers |
| EA011432B1 (en) * | 2005-04-18 | 2009-02-27 | Уникал Аг С.П.А. | Protected carbon steel pipe for fire tube heat exchange device, particularly boilers |
| CN111720236A (en) * | 2019-03-20 | 2020-09-29 | 内蒙古工业大学 | Heaters and Stirling Engines in Stirling Engines |
| CN111720236B (en) * | 2019-03-20 | 2023-07-28 | 内蒙古工业大学 | Heater in Stirling engine and Stirling engine |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0631692B2 (en) | 1994-04-27 |
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