JPS5935762A - Condenser - Google Patents

Condenser

Info

Publication number
JPS5935762A
JPS5935762A JP14711582A JP14711582A JPS5935762A JP S5935762 A JPS5935762 A JP S5935762A JP 14711582 A JP14711582 A JP 14711582A JP 14711582 A JP14711582 A JP 14711582A JP S5935762 A JPS5935762 A JP S5935762A
Authority
JP
Japan
Prior art keywords
heat transfer
annular
fluid conduit
liquid
refrigerant
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.)
Pending
Application number
JP14711582A
Other languages
Japanese (ja)
Inventor
山口 紘一郎
茂 岩永
児玉 達明
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 JP14711582A priority Critical patent/JPS5935762A/en
Publication of JPS5935762A publication Critical patent/JPS5935762A/en
Pending legal-status Critical Current

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  • 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】 産業上の利用分野 本発明はヒートポンプ給湯機等の様に冷媒凝縮器で水道
水を加熱給湯したり、あるいは食物を加熱保温する場合
に、凝縮器の破損時の冷媒と水道水あるいは食物等との
混入を防止する様にした凝縮器に関するものである。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention is useful for heating tap water using a refrigerant condenser, such as in a heat pump water heater, or for heating and keeping food warm. This invention relates to a condenser designed to prevent contamination with tap water, food, etc.

従来例の構成とその問題点 従来の水冷式凝縮器としては第4図の外観図および第6
図の断面図に示す様な2重管式熱交換器や、シェルアン
ドキー−ブ式熱交換器(図示せず)が主体であったが、
本発明の利用分野の様に給湯に利用するものにおいては
、冷媒および潤滑油と給湯水の混入を防止する上で、上
記2徂式熱交換器やシェルアンドキューブ式熱交換器は
信頼性の上で満足するものでないために、安全構成の熱
交換器としては、第6図の断面図に示す様な内管を2層
壁とした3重管式熱交換器や、第7図に示す並設2重壁
熱交換器が用いられていた。しかし、いずれの構成にお
いても管材を用いたものであるため、管材という基本構
成上の制約により伝熱面積を高密度にしたり、熱交換器
自体を小型軽M化して省資源化したものを得ることは困
難であった。
The structure of the conventional example and its problems The external view of the conventional water-cooled condenser is shown in Fig. 4 and Fig. 6.
The main types of heat exchangers were double-tube heat exchangers as shown in the cross-sectional view of the figure, and shell-and-keave heat exchangers (not shown).
In applications used for hot water supply, such as the field of application of the present invention, the above-mentioned two-layer heat exchanger and shell-and-cube heat exchanger are reliable in preventing the mixing of refrigerant and lubricating oil with hot water supply. Since the above is not satisfied, heat exchangers with a safe configuration include a triple-tube heat exchanger with a double-walled inner tube as shown in the cross-sectional view of Fig. A side-by-side double wall heat exchanger was used. However, in both configurations, tube materials are used, so due to the limitations of the basic structure of the tube materials, the heat transfer area can be increased in density, and the heat exchanger itself can be made smaller and lighter in size to save resources. That was difficult.

特に水側か強制循環でない場合、例えば、貯湯槽内に凝
縮器を埋設する様に構成においては、水側の熱伝達率の
低下を補うために伝熱面積の拡大を要することになり、
長尺の管制を用いることになり、それたけに軽量小型化
の要請が強いものであった。
In particular, if there is no forced circulation on the water side, for example, in a configuration where the condenser is buried in the hot water storage tank, it is necessary to expand the heat transfer area to compensate for the decrease in the heat transfer coefficient on the water side.
Since long air traffic control systems were to be used, there was a strong demand for lighter and more compact systems.

発明の目的 本発明はかかる従来の問題点を解消するもので、伝熱筒
を密に拡大すると共に、冷媒側の熱伝達率を向上させて
凝縮器の小型高性能化を目的とするものである。
Purpose of the Invention The present invention is intended to solve these conventional problems, and aims to make the condenser compact and high-performance by enlarging the heat transfer tube densely and improving the heat transfer coefficient on the refrigerant side. be.

発明の構成 この目的を達成するため、本発明は外表面に第1の環状
伝熱フィンを固着した外筒の内周に、内表面に第2の環
状伝熱フィンを固着した内筒の外周を接触させた2重壁
伝熱筒を成すと共に、前記第2の環状伝熱フィンの中心
軸側端に流体導管部を設け、該流体導管部の一端側に圧
縮機吐出冷媒ガスの流出管を接続し、該流出管先端近傍
に凝縮冷媒液の流出孔を設けて前記流体導管部を気液2
相状態とし、流体導管の他端側から前記第2の環状フィ
ン間流路′\流入させ、前記第1の曖状フィある。
Structure of the Invention In order to achieve this object, the present invention provides an outer cylinder having first annular heat transfer fins fixed to the outer surface thereof, and an outer cylinder having second annular heat transfer fins fixed to the inner surface thereof. A fluid conduit portion is provided at the central axis side end of the second annular heat transfer fin, and an outflow pipe for refrigerant gas discharged from the compressor is provided at one end side of the fluid conduit portion. A condensed refrigerant liquid outflow hole is provided near the tip of the outflow pipe, and the fluid conduit section is connected to the gas/liquid 2.
The fluid is brought into a phase state, and the fluid is caused to flow into the second annular inter-fin flow path from the other end side of the fluid conduit to form the first ambiguous flow path.

この構成によって、2重壁伝熱筒を構成する外筒、内筒
の両側に伝熱フィンを密に設けて伝熱面積の拡大が図れ
ると共に、凝縮器への冷媒ガスの流出吸引効果により凝
縮冷媒液を吸引し気液混合の2相状態を流体導管部で作
る作用をするので、熱伝達率の低いガス域を除去呟熱伝
達率の高い気液2相状態で伝熱筒を介した熱交換作用を
得るものであり、前記高密度伝熱面積の拡大効果と、高
熱伝達率の2相域熱交換域の拡大効果の相剰作用により
、高性能小型化凝縮器として作用を有するものである。
With this configuration, heat transfer fins are densely provided on both sides of the outer and inner cylinders that make up the double-walled heat transfer cylinder, increasing the heat transfer area, and the refrigerant gas flowing out to the condenser is condensed by the suction effect. It works by sucking the refrigerant liquid and creating a gas-liquid two-phase state in the fluid conduit section, so it removes the gas region with low heat transfer coefficient and transfers the gas-liquid two-phase state with high heat transfer coefficient through the heat transfer tube. A device that obtains a heat exchange effect, and has an effect as a high-performance compact condenser due to the mutual effect of the expansion effect of the high-density heat transfer area and the expansion effect of the two-phase heat exchange area with a high heat transfer coefficient. It is.

実施例の説明 以下、本発明の実施例を第1,2,3図を用いて説明す
る。第1図は本発明による凝縮器1を貯湯槽2の下部に
取付は用いた場合の実施例である。
DESCRIPTION OF EMBODIMENTS Hereinafter, embodiments of the present invention will be explained using FIGS. 1, 2, and 3. FIG. 1 shows an embodiment in which a condenser 1 according to the present invention is attached to the lower part of a hot water storage tank 2.

3は給水管、4は出湯管である。凝縮器1はヒートポン
プ(図示せず)の構成要素の1つであり、ヒートポンプ
給湯機の場合を示す。第2図が不発明による凝縮器1の
構成図である。第3図は同じく縦断面である。第2,3
図において同一部材には同一番号を付している。5は外
筒、6は外筒1の外表面に設けた第1の環状フィン、7
は内筒、8は内筒7の内表面に設けた第2の環状伝熱フ
ィンで、外筒5の内周に内筒7の外周を接J114!さ
せて2市壁の伝熱筒9を構成している。従って外筒5の
外表面に設けた第1の環状伝熱フィン60間を流扛る流
体と内筒7の内表面に設けた第2の環状伝熱フィン8間
を流れる冷媒との間で、2重壁の伝熱筒9を介して熱交
換し、冷媒は冷却されてU縮液化することになる。さら
に第2の環状伝熱フィン8の中心軸側端に流体導管部1
0を設けており、この流体導管部10の一端側には、圧
縮機(図示せず)からの吐出冷媒ガスの流出管11を持
続すると共に、この流出管11の先端近傍に凝縮冷媒液
の流出孔12を設けている。つまり、圧縮機から吐出冷
媒ガスが流出管11から流体導管部10に流出する時の
吸引効果により、内筒7に設けてなる第2の環状伝熱フ
ィン8の間を流れている凝縮冷媒液の一部を流出孔12
より吸引するために、流体導管部1o内は、ただちにガ
ス液の2相状態となる。この気液2相状態の冷媒は、流
体導管部1Qの他端側から、内筒7の第2の環状伝熱フ
ィン8の間へと流入することにより、伝熱筒9を介した
熱交換域では、ガス域の熱交換はなく気液2相状態と凝
縮液化後の液相域の熱交換が行なわれる。この様に熱交
換伝熱面において熱伝達率の低いガス域での熱交換域に
替えて、熱伝達率の高い気液2相域での熱交換伝熱面を
構成するものである。
3 is a water supply pipe, and 4 is a hot water outlet pipe. The condenser 1 is one of the components of a heat pump (not shown), and the case of a heat pump water heater is shown. FIG. 2 is a block diagram of the condenser 1 according to the invention. FIG. 3 is also a longitudinal section. 2nd, 3rd
In the figures, the same members are given the same numbers. 5 is an outer cylinder; 6 is a first annular fin provided on the outer surface of the outer cylinder 1; 7 is a first annular fin provided on the outer surface of the outer cylinder 1;
is an inner cylinder, 8 is a second annular heat transfer fin provided on the inner surface of the inner cylinder 7, and the outer periphery of the inner cylinder 7 is in contact with the inner periphery of the outer cylinder 5. The heat transfer tubes 9 of the two city walls are configured. Therefore, between the fluid flowing between the first annular heat transfer fins 60 provided on the outer surface of the outer cylinder 5 and the refrigerant flowing between the second annular heat transfer fins 8 provided on the inner surface of the inner cylinder 7. , heat is exchanged through the double-walled heat transfer tube 9, and the refrigerant is cooled and liquefied. Furthermore, a fluid conduit portion 1 is provided at the end of the second annular heat transfer fin 8 on the central axis side.
One end of this fluid conduit section 10 is provided with an outflow pipe 11 for the refrigerant gas discharged from the compressor (not shown), and a condensed refrigerant liquid is provided near the tip of this outflow pipe 11. An outflow hole 12 is provided. That is, due to the suction effect when the refrigerant gas discharged from the compressor flows out from the outflow pipe 11 to the fluid conduit section 10, the condensed refrigerant liquid flows between the second annular heat transfer fins 8 provided in the inner cylinder 7. A part of the outflow hole 12
In order to draw more suction, the inside of the fluid conduit portion 1o immediately enters a two-phase gas-liquid state. This gas-liquid two-phase refrigerant flows from the other end of the fluid conduit section 1Q into between the second annular heat transfer fins 8 of the inner cylinder 7, thereby exchanging heat through the heat transfer cylinder 9. In this region, there is no heat exchange in the gas region, but heat exchange between the gas-liquid two-phase state and the liquid phase region after condensation and liquefaction. In this way, in the heat exchange heat transfer surface, instead of a heat exchange region in a gas region with a low heat transfer coefficient, a heat exchange heat transfer surface is configured in a gas-liquid two-phase region with a high heat transfer coefficient.

なお、13は第2の環状伝熱フィン8に設けた冷媒流通
孔で、気ill 2相状態の冷媒はこの冷媒流通孔13
を流れて第2の環状伝熱フィン8の間を次々に流れて行
く間に、冷却されてa縮液化して行くことになり、冷媒
液−f114により凝縮器1かも出て行くものである。
Note that 13 is a refrigerant flow hole provided in the second annular heat transfer fin 8, and the refrigerant in the two-phase state is passed through this refrigerant flow hole 13.
While flowing between the second annular heat transfer fins 8 one after another, it is cooled and condensed into a liquefied liquid, and the refrigerant liquid -F114 also leaves the condenser 1. .

15は7ランジで、貯湯槽2への取付固定を行う。Reference numeral 15 is a 7-lunge for attaching and fixing to the hot water tank 2.

発明の効果 以上の様に本発明の凝縮器によれば次の様な効果が得ら
れる。
Effects of the Invention As described above, the condenser of the present invention provides the following effects.

(1)外表面に第1の環状伝熱フィンを固着した外筒の
内周に、内表面に第2の環状伝熱フィンを固着した内筒
の外周を接触させて重壁伝熱筒を構成しているので、1
fJ記内外筒の各々に、密に伝熱フィンを設けることに
より伝熱面積の拡大が図れることにより、高密度小型の
凝縮器をに流体導管部を設け、該流体導管部の一端側に
圧縮機吐出冷媒ガスの流出管を接続し、該流出管先端近
傍に凝縮冷媒液の流出孔を設けて前記流体導管部を気液
2相状態とし、流体導管部の他端側から前記第2の環状
伝熱フィン間流路へ流入させ、前記第1の環状伝熱フィ
ン間流体との間で熱交換するように構成しているので、
熱交換伝熱面においては熱伝達率の低いガス状での熱交
換域に替えて熱伝達率の高い気液2相状態域を成すこと
により、高性能熱交換を行う凝縮器を得ることが出来る
(1) A heavy-walled heat transfer tube is formed by bringing the outer circumference of the inner tube, which has the second annular heat transfer fins fixed to its inner surface, into contact with the inner circumference of the outer tube, which has the first annular heat transfer fins fixed to its outer surface. Since it is configured, 1
The heat transfer area can be expanded by densely providing heat transfer fins on each of the outer and outer cylinders, and a fluid conduit section is provided in the high-density, small condenser, and compression is carried out at one end of the fluid conduit section. An outflow pipe for the refrigerant gas discharged from the machine is connected, an outflow hole for the condensed refrigerant liquid is provided near the tip of the outflow pipe to bring the fluid conduit section into a gas-liquid two-phase state, and the second Since it is configured to flow into the annular heat transfer fin inter-fin flow path and exchange heat with the first annular heat transfer fin inter-fin fluid,
In terms of heat exchange and heat transfer, it is possible to obtain a condenser that performs high-performance heat exchange by creating a gas-liquid two-phase state region with a high heat transfer coefficient instead of a gaseous heat exchange region with a low heat transfer coefficient. I can do it.

の内外表面に高密度に設けた伝熱フィン効果とガス域を
除去した気液2相域での熱交換促進効果により、従来の
管材を基本構成したものに比へて小型軽量の凝縮器を得
ることが出来る。
The effect of heat transfer fins densely provided on the inner and outer surfaces of the tube and the effect of promoting heat exchange in the gas-liquid two-phase region by removing the gas region make it possible to create a smaller and lighter condenser compared to conventional tube materials. You can get it.

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

第1図は本発明による凝縮器を用いた一実施例の断面図
、第2図、第3図は本発明による凝縮器の構成図、第4
図、第5図、第6図、第7図は従来例を示すものである
。 5・・・・・・外筒、6・・・・・・第1の環状伝熱フ
ィン、7・・・・・・内筒、8・・・・・・第2の環状
伝熱フィン、9・・・・・・伝熱筒、10・・・・・・
流体導管部、11・・・・・・流出管、12・・・・・
流出孔、13・・・・・・流通孔、14・・・・・・冷
媒液管。 代理人の氏名 弁理士 中 尾 敏 男 ほか1名第1
図 第2図 第4図 第6図
FIG. 1 is a sectional view of an embodiment using a condenser according to the present invention, FIGS. 2 and 3 are block diagrams of a condenser according to the present invention, and FIG.
5, 6, and 7 show conventional examples. 5... Outer cylinder, 6... First annular heat transfer fin, 7... Inner cylinder, 8... Second annular heat transfer fin, 9...Heat transfer tube, 10...
Fluid conduit section, 11...Outflow pipe, 12...
Outflow hole, 13... Distribution hole, 14... Refrigerant liquid pipe. Name of agent: Patent attorney Toshio Nakao and 1 other person No. 1
Figure 2 Figure 4 Figure 6

Claims (1)

【特許請求の範囲】[Claims] 外表面に第1の環状伝熱フィンを固着した外筒の内周に
、内表面に第2の環状伝熱フィンを固着した内筒の外周
を接触させ2市壁伝熱筒を成すと共に、前記第2の環状
伝熱フィンの中心軸側端に流体導管部を設け、二の流体
導管部の一端側に圧縮機吐出冷媒ガスの流出管を接続し
、この流出管先端近傍にa縮冷媒液の流出孔を設けてn
ij記流体流体導管部液2相状、西とし、流体導管部の
他端側から前記第2の環状フィン間流路へ流入さげ、「
)IJ記第1の環状フィン間流体との間・で熱交換する
凝縮2g。
The outer periphery of the inner cylinder having the second annular heat transfer fins fixed to the inner surface is brought into contact with the inner periphery of the outer cylinder having the first annular heat transfer fins fixed to the outer surface to form a two-wall heat transfer cylinder, and A fluid conduit portion is provided at the end of the second annular heat transfer fin on the central axis side, an outflow pipe for the refrigerant gas discharged from the compressor is connected to one end side of the second fluid conduit portion, and a condensing refrigerant is connected near the tip of this outflow pipe. Provide a liquid outflow hole
The liquid in the fluid conduit section is in a two-phase state, and flows into the second annular inter-fin channel from the other end side of the fluid conduit section, and
) 2g of condensation exchanging heat with the fluid between the first annular fins in IJ.
JP14711582A 1982-08-24 1982-08-24 Condenser Pending JPS5935762A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14711582A JPS5935762A (en) 1982-08-24 1982-08-24 Condenser

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14711582A JPS5935762A (en) 1982-08-24 1982-08-24 Condenser

Publications (1)

Publication Number Publication Date
JPS5935762A true JPS5935762A (en) 1984-02-27

Family

ID=15422863

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14711582A Pending JPS5935762A (en) 1982-08-24 1982-08-24 Condenser

Country Status (1)

Country Link
JP (1) JPS5935762A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20200097242A (en) * 2017-12-22 2020-08-18 상하이 파워 이큅먼트 리서치 인스티튜트 컴퍼니 리미티드 Outer fin heat exchange tube and how to use the same

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20200097242A (en) * 2017-12-22 2020-08-18 상하이 파워 이큅먼트 리서치 인스티튜트 컴퍼니 리미티드 Outer fin heat exchange tube and how to use the same
JP2021502540A (en) * 2017-12-22 2021-01-28 シャンハイ パワー エクイプメント リサーチ インスティテュート カンパニー,リミテッド Heat Exchange Tube with Outer Fins and Its Usage This disclosure was submitted to the Japan Patent Office on December 22, 2017, with an application number of 201711410324.2 and the title of the invention is "heat exchange tube with outer fins and its use. The method claims the priority of the application, the entire contents of which are incorporated herein by reference.

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