JPS59112189A - Heat exchanger - Google Patents

Heat exchanger

Info

Publication number
JPS59112189A
JPS59112189A JP22213782A JP22213782A JPS59112189A JP S59112189 A JPS59112189 A JP S59112189A JP 22213782 A JP22213782 A JP 22213782A JP 22213782 A JP22213782 A JP 22213782A JP S59112189 A JPS59112189 A JP S59112189A
Authority
JP
Japan
Prior art keywords
heat
water
cylinder
heat transfer
fins
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
JP22213782A
Other languages
Japanese (ja)
Inventor
Koichiro Yamaguchi
山口 紘一郎
Shigeru Iwanaga
茂 岩永
Tatsuaki Kodama
児玉 達明
Masaaki Adachi
安立 正明
Mitsuhiro Ikoma
生駒 光博
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 JP22213782A priority Critical patent/JPS59112189A/en
Publication of JPS59112189A publication Critical patent/JPS59112189A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/003Arrangements for modifying heat-transfer, e.g. increasing, decreasing by using permeable mass, perforated or porous materials

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Dispersion Chemistry (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

PURPOSE:To enhance coefficient of heat transfer and contrive to reduce the size and enhance the performance of a heat exchanger, by a method wherein the interior of a double cylinder consisting of an inner cylinder and an outer cylinder is made to be a passage for a heat-exchanging medium, and heat-transmitting fins provided with a plurality of passing holes locally distributed in proximity to the inside and outside surfaces of the inner cylinder are provided. CONSTITUTION:A high-temperature refrigerant gas fed through a refrigerant inflow port 8 flows through the passing holes 12 of outside heat-transmitting fins 5 provided in the outer cylinder 2, while water fed through a water inflow port 7 flows through passing holes 10 of inside heat-transmitting fins provided in the inner cylinder 1 while exchanging heat with the fins 4, 5 and wall surfaces of the cylinder 1 as heat-transmitting surfaces, the refrigerant is condensed into a liquid, and water is heated to be hot water. In this case, since the passing holes 10, 12 are locally distributed in proximity to the inside and ouside surfaces the inner cylinder 1, stagnation of the refrigerant and adhesion of a lubricating oil in proximity to contact parts 13 of the fins 5 are prevented on the refrigerant passage side, while stagnation of water in proximity to contact parts 11 of the fins 4 is eliminated and water is stirred to form turbulent flows on the water passage side, and the coefficient of heat transfer is enhanced.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、冷凍機の蒸発器や凝縮器等の冷媒と水との間
での熱交換器に関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a heat exchanger between a refrigerant and water, such as an evaporator or a condenser of a refrigerator.

(従来例の構成とその問題点) 従来、この種の熱交換器としては第4図、第5図に示す
二重管式熱交換器や、第6図に示す水管と冷媒管との並
設二重壁熱交換器さらにシェルアンドチューブ式熱交換
器(図示せず)がある。さらに熱交換した水を冷水およ
び給湯に利用するものにおいては、冷媒や潤滑油と湯水
との混入を防止する上で、第6図に示す並設二重壁熱交
換器の他に第7図に示すような内管を二層壁とした二重
管式熱交換器を改良したものがある。しかし、この種の
従来熱交換器の構成は管材を部材として用いたものであ
るために、管材の形状構成上で伝熱面積を高密度にした
シ、熱交換器自体を小型軽量化して省資源化したものを
得ることは困難であった。
(Conventional structure and its problems) Conventionally, this type of heat exchanger has been a double pipe heat exchanger as shown in Figs. 4 and 5, and a double pipe heat exchanger as shown in Fig. 6. There is a double wall heat exchanger as well as a shell and tube heat exchanger (not shown). Furthermore, in systems where heat-exchanged water is used for cold water and hot water supply, in addition to the side-by-side double wall heat exchanger shown in Fig. 6, in addition to the parallel double-wall heat exchanger shown in Fig. 7, in order to prevent the mixing of refrigerant and lubricating oil with hot water, There is an improved double-tube heat exchanger with a double-walled inner tube, as shown in the figure below. However, since the structure of this type of conventional heat exchanger uses pipe materials as a component, it is necessary to make the heat transfer area high density in the shape of the pipe material, and to reduce the size and weight of the heat exchanger itself. It was difficult to obtain recycled materials.

(発明の目的) 本発明は、以上のような従来の欠点を除去するものて、
伝熱面を広く密に構成すると共に熱伝達率を向上させて
熱交換器の小型高性能化を図ることを目的にするもので
ある。
(Object of the invention) The present invention eliminates the above-mentioned conventional drawbacks, and
The purpose is to make the heat exchanger compact and high-performance by configuring the heat transfer surface widely and densely and improving the heat transfer coefficient.

(発明の構成) この目的を達成するために本発明の熱交換器は、内筒と
外筒の二重筒から構成し、該筒内を熱交換媒体釜々の流
路とし、前記内筒の内外表面に多数の流通孔を配した伝
、熱フィンを設けると共に、前記流通孔を内外側伝熱フ
ィン共に内筒の内外表面近くに偏在分布させて設けたも
のである。
(Structure of the Invention) In order to achieve this object, the heat exchanger of the present invention is composed of a double cylinder including an inner cylinder and an outer cylinder, the inside of the cylinder is used as a flow path for the heat exchange medium pots, and the inner cylinder Heat transfer fins having a large number of communication holes are provided on the inner and outer surfaces of the inner cylinder, and the communication holes are unevenly distributed near the inner and outer surfaces of both the inner and outer heat transfer fins.

この構成によって、熱交換媒体流路の各々において、従
来の管材による熱交換器と異なシ伝熱面を広く密に構成
できると共に、伝熱フィンに配した多数の流通孔を内筒
の内外表面近くに偏在分布させ、伝熱フィン取付は近傍
の流体のよどみを防止し攪拌乱流効果を促進させて熱伝
達率の向上を図る作用を得るので、小型高性能化を達成
することができるのである。
With this configuration, in each of the heat exchange medium flow paths, the heat transfer surface can be configured widely and densely, unlike in conventional heat exchangers using tube materials. By unevenly distributing the heat transfer fins in the vicinity, the heat transfer fins prevent the stagnation of the nearby fluid, promote the stirring turbulent flow effect, and improve the heat transfer coefficient, making it possible to achieve smaller size and higher performance. be.

(実施例の説明) 以下、本発明の一実施例を第1図、第2図、第3図を用
いて説明する。第1図は全体構成断面図、第2図は内側
伝熱フィン、第3図は外側伝熱フィンを示している。な
お、同一部材には同一番号を付している。図において1
は内筒、2は外筒、3は流路案内管、4は内筒1の内表
面に設けた内側伝熱フィン、5は内筒1の外衣面に設け
た外側伝熱フィン、6は内筒1への水流入口、7は同じ
く流出口、8は外筒2への冷媒流入口、9は同じく冷媒
流出口である。又、第2図の内側伝熱フィン4において
、10は多数の水流通孔、11は内筒1の内表面への取
付接触部で、第3図の外側伝熱フィン5においで、12
は多数の冷媒流通孔、13は内筒1の外表面への取付接
触部である。以上の構成において本発明の特徴とすると
ころは、内筒1と外筒2の二重筒から構成し、該筒内を
各々冷媒と水の流路とし、前記内筒1の内外表面に多数
の流通孔10,12を配した伝熱フィ/4゜5を設ける
と共に、前記流通孔10.12を内外側の伝熱フィン4
,5共に内筒1の内外表面近くに偏り分布させて構成し
たことにある。
(Description of Embodiment) An embodiment of the present invention will be described below with reference to FIGS. 1, 2, and 3. FIG. 1 is a sectional view of the overall configuration, FIG. 2 is an inner heat transfer fin, and FIG. 3 is an outer heat transfer fin. Note that the same members are given the same numbers. In the figure 1
is an inner cylinder, 2 is an outer cylinder, 3 is a flow path guide tube, 4 is an inner heat transfer fin provided on the inner surface of the inner cylinder 1, 5 is an outer heat transfer fin provided on the outer surface of the inner cylinder 1, and 6 is an outer heat transfer fin provided on the outer surface of the inner cylinder 1. 7 is a water inlet into the inner cylinder 1, 7 is also an outlet, 8 is a refrigerant inlet into the outer cylinder 2, and 9 is a refrigerant outlet. In the inner heat transfer fin 4 in FIG. 2, 10 is a large number of water flow holes, 11 is an attachment contact portion to the inner surface of the inner cylinder 1, and in the outer heat transfer fin 5 in FIG.
1 is a large number of refrigerant flow holes, and 13 is an attachment contact portion to the outer surface of the inner cylinder 1. The feature of the present invention in the above structure is that it is composed of a double cylinder of an inner cylinder 1 and an outer cylinder 2, and the inside of the cylinder is used as a flow path for refrigerant and water, respectively, and a large number of A heat transfer fin 4/4°5 having communication holes 10 and 12 is provided, and the communication holes 10 and 12 are connected to the inner and outer heat transfer fins 4.
, 5 are constructed with a biased distribution near the inner and outer surfaces of the inner cylinder 1.

以下、本発明による熱交換器の動作を冷凍機の凝縮器と
して使用した場合で説明する。冷媒流入口8からの高温
冷媒ガスは外筒2内の外側伝熱フィン5に配された多数
の流通孔12を流れ、他方水流人口6からの水は内筒1
内の内側伝熱フィン4に配された多数の流通孔10を流
れながら、内外伝熱フィン4,5と内筒1の壁面を伝熱
面として熱交換し、冷媒は凝縮液化し、水は加熱され温
湯になる。この時、水および冷媒の流路には内外伝熱フ
ィン4,5が密に取付けられているので伝熱面が高密度
且つ広く構成されることによって熱交換の促進が図られ
る。
Hereinafter, the operation of the heat exchanger according to the present invention will be explained in the case where it is used as a condenser of a refrigerator. High-temperature refrigerant gas from the refrigerant inlet 8 flows through a large number of flow holes 12 arranged on the outer heat transfer fins 5 in the outer cylinder 2, while water from the water flow port 6 flows through the inner cylinder 1.
While flowing through a large number of circulation holes 10 arranged in the inner heat transfer fins 4, the refrigerant exchanges heat with the inner and outer heat transfer fins 4 and 5 and the wall surface of the inner cylinder 1 as a heat transfer surface, and the refrigerant is condensed and liquefied. It is heated and becomes hot water. At this time, since the inner and outer heat transfer fins 4 and 5 are closely attached to the water and refrigerant flow paths, the heat transfer surface is configured to be dense and wide, thereby promoting heat exchange.

さらに、内外伝熱フイ/4,5の流通孔10゜12共に
、内筒1の内外表面へのフィン取付接触部11..13
の近くに偏在分布させているので、冷媒流路側において
は、外側伝熱フィ15の取付接触部13近傍の冷媒のよ
どみと潤滑油の付着を防止して熱伝達率を向上させると
共に、水流路側においては、内側伝熱フィン4の取付接
触部11近傍の水のよどみを除去し、乱流攪拌作用で同
じく熱伝達率の向上を得て熱交換性能を高める効果を有
している。
Further, both the communication holes 10° 12 of the inner and outer heat transfer fins 4 and 5 are connected to the inner and outer surfaces of the inner cylinder 1 at the fin attachment contact portions 11. .. 13
Since it is unevenly distributed near the refrigerant flow path side, it prevents refrigerant stagnation and lubricating oil adhesion near the attachment contact portion 13 of the outer heat transfer fiber 15 to improve the heat transfer coefficient, and also improves the heat transfer coefficient near the water flow path side. This has the effect of removing stagnation of water in the vicinity of the attachment contact portion 11 of the inner heat transfer fin 4, and similarly improving the heat transfer coefficient due to the turbulent agitation action, thereby enhancing the heat exchange performance.

(発明の効果) 以上のような本発明の熱交換器によれば次の効果が得ら
れる。
(Effects of the Invention) According to the heat exchanger of the present invention as described above, the following effects can be obtained.

■ 内筒と外筒の二重筒から構成し、該筒内を熱交換媒
体各々の流路とし、前記内筒の内外表面に多数の流通孔
を配した伝熱フィンを障けると共に、前記流通孔を内外
側伝熱フィン共に内筒の内外表面近くに偏在分布させて
いるので、伝熱面積の拡大効果と各々の熱媒体流路側で
の流体のよどみの防止と乱流攪拌作用による熱伝達率の
向上効果で、熱交換が促進され高性能化が図れる。
(2) It is composed of a double cylinder consisting of an inner cylinder and an outer cylinder, and the inside of the cylinder is used as a flow path for each heat exchange medium, and the heat transfer fins having a large number of circulation holes arranged on the inner and outer surfaces of the inner cylinder are blocked, and the The circulation holes are unevenly distributed near the inner and outer surfaces of the inner cylinder for both the inner and outer heat transfer fins, which increases the heat transfer area, prevents fluid stagnation on each heat medium flow path side, and reduces heat due to turbulent agitation. The effect of improving the transfer rate promotes heat exchange and improves performance.

■ 筒材と伝熱フィンは金属板材から成る熱交換器の構
成なので、伝熱面を高密度に形作ることにより、軽量小
型化して省資材熱交換器を得ることが出来る。
■ Since the tube material and heat transfer fins are the structure of the heat exchanger made of metal plates, by shaping the heat transfer surface with high density, it is possible to obtain a light and compact heat exchanger that saves materials.

■ さらに本発明の熱交換器は、従来管材によるものと
異なシ軽量小型化できるので機器への組込み取付けが容
易となる付加効果も有している。
(2) Moreover, the heat exchanger of the present invention has the additional effect that it can be made lighter and more compact than conventional tube materials, making it easier to incorporate it into equipment.

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

第1図は本発明、による熱交換器の断面全体構成図、第
2図は内側伝熱フィンの構成図、第3図は外側伝熱フィ
ンの構成図、第4図、第5図、第6図、第7図は従来の
熱交換器を示す図である。 1・・・内筒、2・・・外筒、4・・内側伝熱フィン、
5・・・外側伝熱フィン、10・・・内側伝熱フィンの
流通孔、11・・・外側伝熱フィンの流通孔。 第1図 第2図 第3図 第4図 第 519 第6し 第7図
FIG. 1 is a cross-sectional overall configuration diagram of a heat exchanger according to the present invention, FIG. 2 is a configuration diagram of inner heat transfer fins, FIG. 3 is a configuration diagram of outer heat transfer fins, and FIGS. 6 and 7 are diagrams showing conventional heat exchangers. 1... Inner cylinder, 2... Outer cylinder, 4... Inner heat transfer fin,
5... Outer heat transfer fin, 10... Communication hole of inner heat transfer fin, 11... Communication hole of outer heat transfer fin. Figure 1 Figure 2 Figure 3 Figure 4 Figure 519 Figure 6 and Figure 7

Claims (1)

【特許請求の範囲】[Claims] 内筒と外筒の二重筒から構成し、該筒内を熱交換媒体釜
々の流路とし、前記内筒の内外表面に多数の流通孔を配
した伝熱フィンを設け、前記流通孔を内筒の内外表面近
くに偏在分布させたことを特徴とする熱交換器。
It is composed of a double cylinder consisting of an inner cylinder and an outer cylinder, the inside of the cylinder is used as a flow path for the heat exchange medium pots, heat transfer fins with a large number of circulation holes are provided on the inner and outer surfaces of the inner cylinder, and the circulation holes are A heat exchanger characterized in that the heat exchanger is unevenly distributed near the inner and outer surfaces of the inner cylinder.
JP22213782A 1982-12-20 1982-12-20 Heat exchanger Pending JPS59112189A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22213782A JPS59112189A (en) 1982-12-20 1982-12-20 Heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22213782A JPS59112189A (en) 1982-12-20 1982-12-20 Heat exchanger

Publications (1)

Publication Number Publication Date
JPS59112189A true JPS59112189A (en) 1984-06-28

Family

ID=16777748

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22213782A Pending JPS59112189A (en) 1982-12-20 1982-12-20 Heat exchanger

Country Status (1)

Country Link
JP (1) JPS59112189A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5251603A (en) * 1991-05-29 1993-10-12 Sanoh Kogyo Kabushiki Kaisha Fuel cooling system for motorvehicles
JPWO2017006389A1 (en) * 2015-07-03 2017-09-14 三菱電機株式会社 Heat pump equipment
CN109668454A (en) * 2018-12-04 2019-04-23 广西平果博导铝镁线缆有限公司 The heat-exchange system of oil and water

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5373653A (en) * 1976-10-28 1978-06-30 Gen Electric Heat transfer means

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5373653A (en) * 1976-10-28 1978-06-30 Gen Electric Heat transfer means

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5251603A (en) * 1991-05-29 1993-10-12 Sanoh Kogyo Kabushiki Kaisha Fuel cooling system for motorvehicles
JPWO2017006389A1 (en) * 2015-07-03 2017-09-14 三菱電機株式会社 Heat pump equipment
US10508842B2 (en) 2015-07-03 2019-12-17 Mitsubishi Electric Corporation Heat pump device with separately spaced components
CN109668454A (en) * 2018-12-04 2019-04-23 广西平果博导铝镁线缆有限公司 The heat-exchange system of oil and water

Similar Documents

Publication Publication Date Title
US20060207757A1 (en) Heat exchanger exhaust gas recirculation cooler
EP1122505A1 (en) Plate type heat exchanger
CN110779373B (en) Water-cooled tube plate heat exchanger
EP2282140B1 (en) Heat exchanger and hot-water supply device using same
JP2019015200A (en) Intercooler
KR20130065173A (en) Heat exchanger for vehicle
JPS59112189A (en) Heat exchanger
KR20130065174A (en) Heat exchanger for vehicle
CN110779371B (en) Water-cooling tube-plate heat exchanger with optimally distributed fluid inlet and outlet
CN110793370B (en) Design method of water-cooled tube plate heat exchanger
JPH0614782U (en) Heat exchanger
JPH05340686A (en) Heat-exchanger
JPH09229579A (en) Heat transfer pipe and multitubular heat exchanger with the heat transfer pipe
CN114440675B (en) Gravity heat pipe with multiple heat release ends communicated
CN110779372B (en) Water-cooled tube plate heat exchanger with variable cylindrical fin spacing
CN217817563U (en) Micro-channel condenser for kitchen air conditioning system
JPH0449494Y2 (en)
CN213021123U (en) Full-sliding oil-moving inner-core type heat exchanger
JP2004077024A (en) Exhaust heat exchanger device
CN210051198U (en) Corrugated tube heat exchanger for enhancing heat exchange
JPS59115983A (en) Heat exchanger
JPS6222774Y2 (en)
JPS59125391A (en) Heat exchanger
JPS5997490A (en) Heat exchanger
JPH04108191U (en) Heat exchanger inlet header