JPH03294033A - Manufacture of heat exchanger - Google Patents

Manufacture of heat exchanger

Info

Publication number
JPH03294033A
JPH03294033A JP9576790A JP9576790A JPH03294033A JP H03294033 A JPH03294033 A JP H03294033A JP 9576790 A JP9576790 A JP 9576790A JP 9576790 A JP9576790 A JP 9576790A JP H03294033 A JPH03294033 A JP H03294033A
Authority
JP
Japan
Prior art keywords
heat exchanger
tube
exchanger tube
heat transfer
heat
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
JP9576790A
Other languages
Japanese (ja)
Inventor
Nobuo Shimomura
下村 信雄
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 Refrigeration Co
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 Refrigeration Co filed Critical Matsushita Refrigeration Co
Priority to JP9576790A priority Critical patent/JPH03294033A/en
Publication of JPH03294033A publication Critical patent/JPH03294033A/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
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/40Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only inside the tubular element

Landscapes

  • Physics & Mathematics (AREA)
  • Engineering & Computer Science (AREA)
  • Geometry (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)

Abstract

PURPOSE:To improve the heat exchange capacity by expanding a heat exchanger tube in a state that grooves of a rugged shape are eliminated temporarily by a temperature variation and the inside surface of the heat exchanger tube is almost flattened, and allowing a heat exchanger fin and the heat exchanger tube to adhere closely to each other. CONSTITUTION:Heat exchanger fins are arranged in parallel at a prescribed interval, and gas is allowed to flow between them. A heat exchanger tube 11 is inserted vertically into this heat exchanger fin. The heat exchanger tube 11 is constituted of a shape memory alloy or a shape memory resin 15 which is subjected to reversible transformation in accordance with a temperature variation. Also, grooves 12, 13 of a rugged shape are formed in the heat exchanger tube 11. Subsequently, in a state that the grooves 12, 13 of a rugged shape are eliminated temporarily by a temperature variation and the inside surface of the heat exchanger tube 11 is almost flatted, the heat exchanger tube 11 is expanded, and the heat exchanger fin and the heat exchanger tube 11 are allowed to adhere closely to each other. In such a way, a heat transfer coefft. of the inside of the tube being equal to a single tube can be secured.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、冷凍冷蔵機器及び空調機器に広く用いられて
いる、冷媒と空気等の流体間で熱の授受を行う熱交換器
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 that transfers heat between a refrigerant and a fluid such as air, which is widely used in refrigeration equipment and air conditioning equipment.

従来の技術 近年、機器の高効率化が求められているなか、冷凍冷蔵
機器や空気熱源ヒートポンプ空調機に用いられる熱交換
器の効率向上が急務である。
BACKGROUND OF THE INVENTION In recent years, there has been a demand for higher efficiency in equipment, and there is an urgent need to improve the efficiency of heat exchangers used in refrigeration equipment and air-source heat pump air conditioners.

以下、図面を参照しながら従来の熱交換器の製造方法の
一例について説明する。
An example of a conventional method for manufacturing a heat exchanger will be described below with reference to the drawings.

第4図は従来の熱交換器の斜視図で、3oは熱交換器、
31は一定間隔で平行に並べられた伝熱フィン、32は
この伝熱フィン31に直角に挿入され、内面に螺旋溝が
加工された伝熱管であシ、空気の流れを矢印で示しであ
る。第5図は前記伝熱管32の単管時の側面図、33は
伝熱管32に加工された略螺旋状の溝、34は溝33の
略三角形状の山である。第6図は伝熱フィン31と伝熱
管32が密着される拡管工程を示すもので、35はマン
ドレル治具であシ、矢印でその挿入方向を示す。第7図
は拡管後の伝熱管32の側面図で、36は拡管で変形し
た山である。第8図は伝熱管32単体と熱交換器での冷
媒蒸発時の管内側熱伝達率と蒸発性能を比較したもので
ある。
Figure 4 is a perspective view of a conventional heat exchanger, where 3o is a heat exchanger;
31 is a heat transfer fin arranged in parallel at regular intervals; 32 is a heat transfer tube inserted into the heat transfer fin 31 at right angles and has a spiral groove formed on its inner surface; the air flow is indicated by an arrow. . FIG. 5 is a side view of the heat transfer tube 32 when it is a single tube, 33 is a substantially spiral groove machined into the heat transfer tube 32, and 34 is a substantially triangular peak of the groove 33. FIG. 6 shows a tube expansion process in which the heat transfer fins 31 and the heat transfer tubes 32 are brought into close contact with each other, and 35 is a mandrel jig, and the arrow indicates its insertion direction. FIG. 7 is a side view of the heat exchanger tube 32 after expansion, and 36 is a mountain deformed by expansion. FIG. 8 compares the tube inside heat transfer coefficient and evaporation performance during refrigerant evaporation between the heat transfer tube 32 alone and the heat exchanger.

以下、第4図のように構成された従来の熱交換器の動作
について説明すると、空気は伝熱フィン31の間を矢印
のように流れ、冷媒は伝熱管32内を流れることによっ
て熱交換する。この時、冷媒は伝熱管32の溝33と略
三角形状の山34によって沸騰あるいは、凝mが促進さ
れ、管内側熱伝達率が向上し、熱交換性能の向上が図ら
れている。
The operation of the conventional heat exchanger configured as shown in FIG. 4 will be explained below. Air flows between heat transfer fins 31 as shown by the arrow, and refrigerant flows through heat transfer tubes 32 to exchange heat. . At this time, boiling or condensation of the refrigerant is promoted by the grooves 33 and the substantially triangular peaks 34 of the heat transfer tube 32, improving the heat transfer coefficient inside the tube and improving the heat exchange performance.

発明が解決しようとする課題 しかしながら上記のような熱交換器の製造方法では、第
6図で示された伝熱管32の略三角形状の山34が、第
6図に示す拡管工程でマントシル治具36によって押し
広げられ、第7図の変形した山36になる。その結果第
8図に示すように冷媒蒸発時で比較すると、伝熱管32
単体より熱交換器30での方が管内側熱伝達率が減少し
、伝熱管単体性能からの理論計算よシも蒸発性能が減少
するという課題を有していた。なお、第8図において、
Aは単管でのデータ、Bは単管データよシの計算能力、
C,Dは熱交換器でのデータを示す。
Problem to be Solved by the Invention However, in the heat exchanger manufacturing method as described above, the approximately triangular peaks 34 of the heat exchanger tubes 32 shown in FIG. 36 and becomes the deformed mountain 36 shown in FIG. As a result, as shown in Fig. 8, when compared during refrigerant evaporation, the heat exchanger tube 32
The heat transfer coefficient inside the tube is lower in the heat exchanger 30 than in the heat exchanger 30 alone, and theoretical calculations based on the performance of the heat exchanger tube alone also have the problem of decreasing evaporation performance. In addition, in Fig. 8,
A is the data for a single tube, B is the calculation ability for the single tube data,
C and D show data for the heat exchanger.

また、冷媒凝縮時で比較しても同様に、伝熱管32単体
よシ熱交換器3oでの方が管内側熱伝達率が減少し、理
論計算よりも凝縮性能が減少するという課題を有してい
た。
Also, when comparing the refrigerant condensation, there is a problem that the heat transfer coefficient inside the tube is lower in the heat exchanger 3o than in the heat exchanger tube 32 alone, and the condensation performance is lower than in the theoretical calculation. was.

そこで本発明は、上記課題に鑑み、単管時と同等の伝熱
性能を発揮する熱交換器を提供するものである。
In view of the above problems, the present invention provides a heat exchanger that exhibits heat transfer performance equivalent to that of a single tube.

課題を解決するための手段 上記課題を解決するために本発明の熱交換器の製造方法
は、一定間隔で平行に並べられ、その間を気体が流動す
る伝熱フィンと、この伝熱フィンに直角に挿入され、内
面に、温度変化に応じて可逆変態する形状記憶合金もし
くは形状記憶樹脂から成る凹凸形状の溝を備えた伝熱管
とから構成され、前記凹凸形状の溝を温度変化にょシー
時的に無くし伝熱管内面を略平坦にした状態で伝熱管を
拡管し、前記伝熱フィンと伝熱管とを密着させるもので
ある。
Means for Solving the Problems In order to solve the above problems, the method for manufacturing a heat exchanger of the present invention includes heat transfer fins that are arranged in parallel at regular intervals and through which gas flows, and a heat exchanger that is perpendicular to the heat transfer fins. The heat exchanger tube is inserted into the tube and has an uneven groove on the inner surface made of a shape memory alloy or shape memory resin that undergoes reversible transformation in response to temperature changes. The heat transfer tube is expanded with the inner surface of the heat transfer tube made substantially flat, and the heat transfer fins and the heat transfer tube are brought into close contact with each other.

作   用 本発明は上記の製造方法によって、単管時と同等の管内
側熱伝達率を確保し、熱交換性能を向上する。
Function The present invention uses the above-described manufacturing method to ensure a tube inside heat transfer coefficient equivalent to that of a single tube and improve heat exchange performance.

実施例 以下本発明の一実施例の熱交換器の製造方法について図
面を参照しながら説明する。
EXAMPLE Hereinafter, a method for manufacturing a heat exchanger according to an example of the present invention will be described with reference to the drawings.

熱交換器は従来のように、一定間隔で平行に並べられた
伝熱フィン(図示せず)とこの伝熱フィンに直角に挿入
され、内面に温度変化に応じて可逆変態する形状記憶合
金もしくは形状記憶樹脂からなる凹凸形状の溝を備えた
伝熱管11で構成される。
Conventionally, a heat exchanger consists of heat transfer fins (not shown) arranged in parallel at regular intervals, inserted at right angles to the heat transfer fins, and made of a shape memory alloy or a shape memory alloy that undergoes reversible transformation in response to temperature changes on the inner surface. It is composed of a heat exchanger tube 11 made of shape memory resin and provided with uneven grooves.

第1図は本発明の熱交換器に使用される伝熱管11の側
面図で、12は凹形状、13は凸形状で、14は前記凹
凸形状よ構成る溝であシ、16は前記14の溝を形成す
る形状記憶合金もしくは形状記憶樹脂である。第2図は
伝熱フィンと伝熱管を密着する拡管時の伝熱管11の側
面図で22は前記凹部12の変形で、23は前記凸部が
変形した部分である。24は略平坦になった前記溝14
である。第3図は伝熱管11単体と熱交換器での蒸発時
の管内側熱伝達率と蒸発性能を比較したものである。
FIG. 1 is a side view of a heat exchanger tube 11 used in the heat exchanger of the present invention, in which 12 is a concave shape, 13 is a convex shape, 14 is a groove formed by the above-mentioned uneven shape, and 16 is a groove formed by the above-mentioned 14 Shape memory alloy or shape memory resin that forms the grooves. FIG. 2 is a side view of the heat exchanger tube 11 at the time of tube expansion in which the heat exchanger fins and the heat exchanger tube are brought into close contact with each other, and 22 is the deformation of the recess 12, and 23 is the deformation of the convex portion. 24 is the substantially flat groove 14;
It is. FIG. 3 compares the tube inside heat transfer coefficient and evaporation performance during evaporation between the heat transfer tube 11 alone and the heat exchanger.

以下本発明の熱交換器の製造方法について説明する。第
1図は拡管前後の伝熱管の側面図であシ、第6図で示す
拡管工程は第2図に示すように伝熱管の内面溝が温度変
化によシ略平坦になった状態で、行なわれる。拡管後は
温度変化によシ第1図の溝を再形成し、拡管の前後で同
一の溝形状を保つ。
The method for manufacturing the heat exchanger of the present invention will be explained below. FIG. 1 is a side view of the heat exchanger tube before and after expansion, and the tube expansion process shown in FIG. It is done. After pipe expansion, the grooves shown in Figure 1 are re-formed due to temperature changes, maintaining the same groove shape before and after pipe expansion.

その結果、蒸発時では第3図に示すように、伝熱管11
単体時と同等の熱交換器での管内側熱伝達率を実現し、
従来よシも熱交換器の性能が向上する。
As a result, during evaporation, as shown in FIG.
Achieves the same heat transfer coefficient inside the tube as a single heat exchanger,
The performance of the conventional heat exchanger is improved.

なお、第30において、Aは本発明に使用される単管の
データ、Bは単管よシの計算能力、Σ。
Note that in No. 30, A is the data of the single tube used in the present invention, B is the calculation ability of the single tube, and Σ.

Fは本発明の熱交換器でのデータを示す。F shows data for the heat exchanger of the present invention.

以上のように、内面に温度変化に応じて可逆変態する形
状記憶合金もしくは形状記憶樹脂からなる凹凸状の溝を
備えることによシ、従来品よシ優れた熱交換性能を発揮
する熱交換器を提供することができる製造方法である。
As described above, by providing the inner surface with uneven grooves made of shape memory alloy or shape memory resin that undergoes reversible transformation in response to temperature changes, the heat exchanger exhibits superior heat exchange performance compared to conventional products. This is a manufacturing method that can provide the following.

発明の効果 以上のように本発明は、一定間隔で平行に並べられ、そ
の間を気体が流動する伝熱フィンと、この伝熱フィンに
直角に挿入され、内面に、温度変化に応じて可逆変態す
る形状記憶合金もしくは形状記憶樹脂から成る凹凸形状
の溝を備えた伝熱管とから構成され、前記凹凸形状の溝
を温度変化によシー時的に無くし伝熱管内面を略平坦に
した状態で伝熱管を拡管し、前記伝熱フィンと伝熱管を
密着させる熱交換器の製造方法によシ単管時と同等の管
内側熱伝達率を確保し、従来より熱交換能力が向上する
Effects of the Invention As described above, the present invention consists of heat transfer fins that are arranged in parallel at regular intervals and through which gas flows, and that are inserted perpendicularly to the heat transfer fins and that have a structure that undergoes reversible transformation in response to temperature changes on the inner surface. The heat exchanger tube is made of a shape memory alloy or shape memory resin and has grooves in an uneven shape. By expanding the heat tube and bringing the heat transfer fins into close contact with the heat exchanger tube, a heat transfer coefficient inside the tube equivalent to that of a single tube is secured, and the heat exchange capacity is improved compared to the conventional method.

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

第1図は本発明の一英施例における熱交換器に使用され
る伝熱管が伝熱フィンと密着される拡管前後の形状を示
す側面図、第2図は第1図の伝熱管が伝熱フィンと密着
される拡管時の形状を示す側面図、第3図は同伝熱管と
熱交換器の性能を比較した特性図、第4図は従来の熱交
換器の斜視図、第6図は従来の熱交換器に使用される伝
熱管の拡管前の側面図、第6図は第5図の伝熱管が伝熱
フィンと密着される拡管工程を示す断面図、第7図は第
6図の拡管後の伝熱管の側面図、第8図は従来の製造方
法による熱交換器における伝熱管と熱交換器の性能を比
較した特性図である。 11・・・・・・伝熱管、14・・・・・・略螺旋状溝
、15・・・・・・形状記憶合金もしくは形状記憶樹脂
、31・・・・・・伝熱フィン。
FIG. 1 is a side view showing the shape of a heat transfer tube used in a heat exchanger according to an embodiment of the present invention before and after expansion when the heat transfer tube is brought into close contact with heat transfer fins, and FIG. 2 is a side view showing the shape of the heat transfer tube of FIG. Figure 3 is a characteristic diagram comparing the performance of the heat exchanger with the heat exchanger tube; Figure 4 is a perspective view of a conventional heat exchanger; Figure 6 6 is a side view of a heat transfer tube used in a conventional heat exchanger before expansion, FIG. 6 is a cross-sectional view showing the tube expansion process in which the heat transfer tube of FIG. FIG. 8 is a side view of the heat exchanger tube after tube expansion, and FIG. 8 is a characteristic diagram comparing the performance of the heat exchanger tube and the heat exchanger in a heat exchanger manufactured by a conventional manufacturing method. 11...Heat transfer tube, 14...Substantially spiral groove, 15...Shape memory alloy or shape memory resin, 31...Heat transfer fin.

Claims (1)

【特許請求の範囲】[Claims] 一定間隔で平行に並べられ、その間を気体が流動する伝
熱フィンと、この伝熱フィンに直角に挿入され、内面に
、温度変化に応じて可逆変態する形状記憶合金もしくは
形状記憶樹脂から成る凹凸形状の溝を備えた伝熱管とか
ら構成され、前記凹凸形状の溝を温度変化により一時的
に無くし伝熱管内面を略平坦にした状態で伝熱管を拡管
し、前記伝熱フィンと伝熱管とを密着させる熱交換器の
製造方法。
Heat transfer fins arranged in parallel at regular intervals, through which gas flows, and projections and depressions inserted perpendicularly into the heat transfer fins and made of a shape memory alloy or shape memory resin that reversibly transforms in response to temperature changes on the inner surface. The uneven grooves are temporarily removed due to a temperature change, and the heat exchanger tube is expanded with the inner surface of the heat exchanger tube made substantially flat, and the heat exchanger fins and the heat exchanger tube are expanded. A method of manufacturing a heat exchanger that brings the
JP9576790A 1990-04-10 1990-04-10 Manufacture of heat exchanger Pending JPH03294033A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9576790A JPH03294033A (en) 1990-04-10 1990-04-10 Manufacture of heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9576790A JPH03294033A (en) 1990-04-10 1990-04-10 Manufacture of heat exchanger

Publications (1)

Publication Number Publication Date
JPH03294033A true JPH03294033A (en) 1991-12-25

Family

ID=14146639

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9576790A Pending JPH03294033A (en) 1990-04-10 1990-04-10 Manufacture of heat exchanger

Country Status (1)

Country Link
JP (1) JPH03294033A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11300371B2 (en) * 2015-01-16 2022-04-12 Hamilton Sundstrand Corporation Self-regulating heat exchanger

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11300371B2 (en) * 2015-01-16 2022-04-12 Hamilton Sundstrand Corporation Self-regulating heat exchanger

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