JP7734960B2 - Double-pipe heat exchanger manufacturing method - Google Patents
Double-pipe heat exchanger manufacturing methodInfo
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Description
本発明は、外管と内管とを備えた二重管式熱交換器の製造方法に関する。 The present invention relates to a method for manufacturing a double-pipe heat exchanger having an outer pipe and an inner pipe.
カーエアコンには、冷凍サイクルを構成するコンデンサからの高温の液体冷媒と、同じく冷凍サイクルを構成するエバポレータからの低温の気体冷媒とを熱交換させて、エバポレータの冷房効率を向上させる内部熱交換器が用いられている場合がある。この内部熱交換器は、外管と、該外管内に配置された内管とからなり、外管と内管との間にコンデンサからの高温の液体冷媒の流路が形成され、内管の内部にエバポレータからの低温の気体冷媒の流路が形成された二重管式熱交換器である。 Car air conditioners sometimes use an internal heat exchanger that improves the cooling efficiency of the evaporator by exchanging heat between the high-temperature liquid refrigerant from the condenser, which is part of the refrigeration cycle, and the low-temperature gaseous refrigerant from the evaporator, which is also part of the refrigeration cycle. This internal heat exchanger is a double-pipe heat exchanger consisting of an outer tube and an inner tube placed inside the outer tube, with a flow path for the high-temperature liquid refrigerant from the condenser formed between the outer and inner tubes, and a flow path for the low-temperature gaseous refrigerant from the evaporator formed inside the inner tube.
二重管式熱交換器では、外管と内管との間に隙間があると、外力が作用したときに、外管の変形に内管が追従できず、内管が異常な変形や割れを起こすおそれがあるので、外管と内管とを接触させて固定することが行われている。 In double-pipe heat exchangers, if there is a gap between the outer and inner pipes, the inner pipe will not be able to follow the deformation of the outer pipe when an external force is applied, which could result in abnormal deformation or cracking of the inner pipe. Therefore, the outer and inner pipes are usually fixed in place so that they are in contact with each other.
例えば、特許文献1には、外管と内管とを備え、内管に溝部が形成された二重管において、直管部では、内管が外管に接触していないか、径方向の一方向だけで接触し、曲げ部では、内管が外管の径方向の複数方向に接触している二重管が記載されている。 For example, Patent Document 1 describes a double pipe comprising an outer pipe and an inner pipe, with a groove formed in the inner pipe, in which, in the straight pipe section, the inner pipe is not in contact with the outer pipe or is in contact only in one radial direction, and in the bent section, the inner pipe is in contact with the outer pipe in multiple radial directions.
特許文献1では、外管の内部に内管を位置させたまま、外管と内管とを曲げることにより、外管と内管とを接触させているので、外管と内管とを曲げる際に、内管が割れるおそれがあるうえ、外管と内管とが接触しない箇所も生じていた。また、外管と内管とが接触しないと、外管と内管との間の流路の断面積が大きく、冷媒量が増大する。 In Patent Document 1, the outer and inner pipes are bent while the inner pipe remains positioned inside the outer pipe, thereby bringing the two into contact. This raises the risk of the inner pipe cracking when bending the outer and inner pipes, and also creates areas where the outer and inner pipes do not come into contact. Furthermore, if the outer and inner pipes do not come into contact, the cross-sectional area of the flow path between the outer and inner pipes becomes large, increasing the amount of refrigerant.
特許文献2には、内管に伝熱面積を増大させて熱交換効率を増大させるための凹状の溝を形成した二重管式熱交換器と、内管に溝付け工具を押し付けたまま、内管を移動させて内管に凹状の溝を成形する製造方法とが記載されている。 Patent Document 2 describes a double-pipe heat exchanger in which concave grooves are formed in the inner pipe to increase the heat transfer area and improve heat exchange efficiency, and a manufacturing method in which the inner pipe is moved while a groove-forming tool is pressed against the inner pipe to form the concave grooves in the inner pipe.
特許文献2では、溝付け工具を用いる転造により内管の凹状の溝が形成されるため、製造装置が高価で、加工に長時間を要する問題があった。 In Patent Document 2, the concave grooves in the inner tube are formed by rolling using a groove-forming tool, which poses problems such as expensive manufacturing equipment and a long processing time.
本願出願人は、特許文献3において、内管に波型形状部を短時間で形成することができる二重管式熱交換器の製造方法を提案している。 In Patent Document 3, the applicant proposes a method for manufacturing a double-pipe heat exchanger that allows for the formation of a corrugated portion on the inner pipe in a short period of time.
本発明は、従来の問題点に鑑みてなされたもので、二重管を曲げる際に内管が変形したり割れるおそれが無く、外管と内管との間の流路断面積を縮小して冷媒量を減少することができ、外管の縮径加工が容易に行える二重管式熱交換器の製造方法を提供することを課題とする。 The present invention has been made in consideration of the problems of the conventional art, and aims to provide a method for manufacturing a double-pipe heat exchanger in which the inner pipe is not deformed or cracked when bending the double pipe, the cross-sectional area of the flow path between the outer pipe and the inner pipe can be reduced to reduce the amount of refrigerant, and the outer pipe can be easily reduced in diameter.
前記課題を解決するための手段として、
(1)本発明に係る二重管式熱交換器は、
外管と、前記外管の内部に挿入された内管とを備える二重管式熱交換器において、
前記内管の外面に複数の底部と頂部とが形成され、
前記外管は縮径されて、前記外管の内面の複数箇所が前記内管の頂部に接触していることを特徴とする。
ここで、「縮径」とは、外管の外面の一部を径方向内方に変形させること、外管の外面の全周を径方向内方に変形させることを含む。
As a means for solving the above problem,
(1) The double-pipe heat exchanger according to the present invention is
A double-pipe heat exchanger including an outer pipe and an inner pipe inserted inside the outer pipe,
a plurality of bottoms and tops are formed on the outer surface of the inner tube;
The outer tube is characterized in that its diameter is reduced so that a plurality of points on the inner surface of the outer tube are in contact with the top of the inner tube.
Here, "diameter reduction" includes deforming a part of the outer surface of the outer tube inward in the radial direction, and deforming the entire periphery of the outer surface of the outer tube inward in the radial direction.
(2)前記外管は、前記外管の外面に軸方向に延びる凹部を形成することによって縮径されていることが好ましい。 (2) It is preferable that the outer tube has a reduced diameter by forming a recess extending in the axial direction on the outer surface of the outer tube.
(3)前記外管は、前記外管の外面に軸方向に延びる凹溝を形成することによって縮径されていることが好ましい。 (3) It is preferable that the outer tube has a reduced diameter by forming a recessed groove extending in the axial direction on the outer surface of the outer tube.
(4)前記外管は、前記外管の外面に軸方向に延びる螺旋状の凹溝を形成することによって縮径されていることが好ましい。 (4) It is preferable that the outer tube has a reduced diameter by forming a spiral groove extending in the axial direction on the outer surface of the outer tube.
(5)本発明に係る二重管式熱交換器の製造方法は、
外管と、前記外管の内部に挿入された内管とを備える二重管式熱交換器の製造方法において、
外面に複数の底部と頂部とが形成された内管に対して、前記外管を径方向内方に押圧して軸方向の所定範囲を縮径し、前記外管の内面の複数箇所を前記内管の頂部に接触させることを特徴とする。
(5) A method for manufacturing a double-pipe heat exchanger according to the present invention includes the steps of:
A method for manufacturing a double-pipe heat exchanger including an outer pipe and an inner pipe inserted into the outer pipe,
The method is characterized in that the outer tube is pressed radially inward against an inner tube having a plurality of bottoms and tops formed on its outer surface, thereby reducing the diameter within a predetermined range in the axial direction and bringing multiple points on the inner surface of the outer tube into contact with the tops of the inner tube.
(6)前記外管の回りに等間隔に配置された複数の可動片を前記外管に径方向内方に押し付けて縮径した後、前記外管と前記内管とを軸方向に移動させ、これを複数回繰り返すことで、前記外管の外面に軸方向に延びる凹部を形成することにより、縮径することが好ましい。 (6) It is preferable that the diameter of the outer tube is reduced by pressing multiple movable pieces arranged at equal intervals around the outer tube radially inward against the outer tube, and then moving the outer tube and the inner tube axially. This is repeated multiple times to form recesses extending axially on the outer surface of the outer tube, thereby reducing the diameter.
(7)前記外管の中心軸と直交する平面上に回転軸を有する複数のローラを前記外管に押し付けたまま、前記外管と前記内管とを軸方向に移動させて、前記ローラにより、前記外管の外面に軸方向に延びる凹部を形成することにより、縮径することが好ましい。 (7) It is preferable to reduce the diameter by moving the outer tube and the inner tube in the axial direction while pressing a plurality of rollers having rotation axes on a plane perpendicular to the central axis of the outer tube against the outer tube, and forming recesses extending in the axial direction on the outer surface of the outer tube with the rollers.
(8)前記外管の中心軸と直交する平面上に回転軸を有する複数のローラを前記外管に押し付けたまま、前記外管と前記内管とを軸方向に移動させて、前記ローラにより、前記外管の外面に軸方向に延びる凹溝を形成することにより、縮径することが好ましい。 (8) It is preferable to reduce the diameter by moving the outer tube and the inner tube in the axial direction while pressing multiple rollers having rotation axes on a plane perpendicular to the central axis of the outer tube against the outer tube, and forming axially extending grooves on the outer surface of the outer tube with the rollers.
(9)前記外管の中心軸と平行な回転軸を有する複数のローラを前記外管に押し付けたまま、前記ローラを前記外管の回りに旋回させるとともに、前記外管と前記内管とを軸方向に移動させて、前記ローラにより、前記外管の外面に軸方向に延びる螺旋状の凹溝を形成することにより、縮径することが好ましい。 (9) It is preferable to reduce the diameter by rotating a plurality of rollers, each having a rotation axis parallel to the central axis of the outer tube, against the outer tube while rotating the rollers around the outer tube and moving the outer tube and inner tube in the axial direction, and forming a spiral groove extending in the axial direction on the outer surface of the outer tube with the rollers.
本発明によれば、外管の内面の複数箇所が内管の頂部に接触して、内管が外管に支持されているので、二重管を曲げる際に内管が変形したり割れるおそれが無い。また、外管が縮径されて、外管と内管との間の流路断面積が縮小されているので、冷媒量を減少することができる。 According to the present invention , the inner surface of the outer pipe is in contact with the top of the inner pipe at multiple points, and the inner pipe is supported by the outer pipe, so there is no risk of the inner pipe being deformed or cracked when the double pipe is bent. Furthermore, the outer pipe is reduced in diameter, reducing the cross-sectional area of the flow path between the outer pipe and the inner pipe, allowing for a reduction in the amount of refrigerant.
本発明によれば、径方向に移動可能な複数の絞り工具を用いて、複数の絞り工具により外管を径方向内方に押圧するだけで、外管の縮径加工が容易に行える。 According to the present invention , the outer tube can be easily reduced in diameter by simply pressing the outer tube radially inward using a plurality of radially movable drawing tools.
以下、本発明の実施形態を添付図面に従って説明する。 Embodiments of the present invention will be described below with reference to the accompanying drawings.
図1は、本発明の第1実施形態に係る二重管式熱交換器1を示す。この二重管式熱交換器1は、外管2と、外管2の内部に挿入された内管3とからなる。本実施形態では、二重管式熱交換器1は、カーエアコン用の内部熱交換器であり、外管2と内管3との間の第1流路4には高温高圧の液体の冷媒が流れ、内管3内の第2流路5には低温低圧の気体の冷媒が流れ、両冷媒は対向流であるとして説明するが、逆に、第1流路4には低温低圧の気体の冷媒が流れ、第2流路5には高温高圧の冷媒が流れてもよく、また、両者は並行流であってもよい。 Figure 1 shows a double-pipe heat exchanger 1 according to a first embodiment of the present invention. This double-pipe heat exchanger 1 comprises an outer pipe 2 and an inner pipe 3 inserted inside the outer pipe 2. In this embodiment, the double-pipe heat exchanger 1 is an internal heat exchanger for a car air conditioner. A high-temperature, high-pressure liquid refrigerant flows through a first flow path 4 between the outer pipe 2 and the inner pipe 3, and a low-temperature, low-pressure gas refrigerant flows through a second flow path 5 within the inner pipe 3. The two refrigerants are described as flowing in countercurrent fashion. However, the opposite is also true: a low-temperature, low-pressure gas refrigerant may flow through the first flow path 4 and a high-temperature, high-pressure refrigerant may flow through the second flow path 5, or the two may flow in parallel.
図2に示すように、外管2は、横断面円形のアルミニウム押出形材からなり、軸方向の所定範囲に後述する方法によって縮径された縮径部6を有している。外管2の縮径部6の内面7は、複数箇所Pにおいて、後述する内管3の波型形成部10の頂部10bに接触している。図1に示すように、外管2の両端は、内管3の外面に接合されて閉じられている。外管2には、高温高圧の液体冷媒が流入する外管流入口8と、内管3の気体冷媒と熱交換を終えた液体冷媒が流出する外管流出口9とが形成されている。 As shown in Figure 2, the outer pipe 2 is made of an aluminum extrusion with a circular cross section and has a reduced diameter section 6 within a predetermined axial range, which has been reduced in diameter by a method described below. The inner surface 7 of the reduced diameter section 6 of the outer pipe 2 contacts the crests 10b of the corrugated sections 10 of the inner pipe 3, which will be described later, at multiple locations P. As shown in Figure 1, both ends of the outer pipe 2 are joined to the outer surface of the inner pipe 3 and closed. The outer pipe 2 is formed with an outer pipe inlet 8 through which high-temperature, high-pressure liquid refrigerant flows in, and an outer pipe outlet 9 through which the liquid refrigerant flows out after heat exchange with the gas refrigerant in the inner pipe 3.
図2に示すように、内管3は、横断面円形のアルミニウム押出形材からなり、外管2の内面より小さい外径を有している。内管3には、外側から見て、軸方向に延びる複数の底部10aと頂部10bとが、周方向に交互に繰り返す8つの波型形状部10が形成されている。波型形状部10は、プレス、転造等により公知の方法で形成されている。波型形状部10は、軸方向に螺旋状に延びるものであってもよい。図1に示すように、内管3は、一端に低温低圧の気体冷媒が流入する内管流入口11を有し、他端に外管2と内管3との間の液体冷媒との熱交換を終えた気体冷媒が流出する内管流出口12を有している。 As shown in FIG. 2, the inner pipe 3 is made of an aluminum extrusion with a circular cross section and has an outer diameter smaller than the inner surface of the outer pipe 2. When viewed from the outside, the inner pipe 3 has eight corrugated portions 10, each of which has a plurality of axially extending bottom portions 10a and top portions 10b that alternate in the circumferential direction. The corrugated portions 10 are formed by known methods such as pressing or rolling. The corrugated portions 10 may also extend spirally in the axial direction. As shown in FIG. 1, the inner pipe 3 has an inner pipe inlet 11 at one end through which a low-temperature, low-pressure gas refrigerant flows in, and an inner pipe outlet 12 at the other end through which the gas refrigerant flows out after heat exchange with the liquid refrigerant between the outer pipe 2 and inner pipe 3.
続いて、二重管式熱交換器1の作用を説明する。 Next, we will explain the operation of the double-pipe heat exchanger 1.
図1において、外管2と内管3との間の第1流路4に流れる高温高圧の液体冷媒が保有する熱は、内管3の管壁外面への熱伝達と、内管3の管壁内の熱伝導と、内管3の管壁内面からの熱伝達とにより、内管3の第2流路5を流れる低温低圧の気体冷媒に伝わる。 In Figure 1, the heat held by the high-temperature, high-pressure liquid refrigerant flowing in the first flow path 4 between the outer tube 2 and the inner tube 3 is transferred to the low-temperature, low-pressure gas refrigerant flowing in the second flow path 5 of the inner tube 3 through heat transfer to the outer surface of the wall of the inner tube 3, heat conduction within the wall of the inner tube 3, and heat transfer from the inner surface of the wall of the inner tube 3.
これにより、外管2と内管3との間の第1流路4を流れる高温高圧の液体冷媒と、内管3内の第2流路5を流れる低温低圧の気体冷媒との間で熱交換が行なわれ、外管2と内管3との間の第1流路4の高温高圧の液体冷媒は冷却され、内管3内の第2流路5の低温低圧の気体冷媒は加熱される。特に、内管3は、波型形状部10を有する中央部の伝熱面積が、波型形状部10を有さない場合に比べて大きいので、熱交換効率がよい。 This allows heat exchange to occur between the high-temperature, high-pressure liquid refrigerant flowing through the first flow path 4 between the outer tube 2 and the inner tube 3 and the low-temperature, low-pressure gas refrigerant flowing through the second flow path 5 within the inner tube 3. The high-temperature, high-pressure liquid refrigerant in the first flow path 4 between the outer tube 2 and the inner tube 3 is cooled, and the low-temperature, low-pressure gas refrigerant in the second flow path 5 within the inner tube 3 is heated. In particular, the inner tube 3 has a larger heat transfer area in the central portion having the corrugated portion 10 than when it does not have the corrugated portion 10, resulting in good heat exchange efficiency.
前記実施形態の二重管式熱交換器1によれば、図2に示すように、外管2の内面の複数箇所が内管3の波型形状部10の頂部10bに接触して、内管3が外管2に支持されているので、図3に示すように、二重管を曲げる際に内管3が変形したり割れるおそれが無い。また、外管2が縮径されて、外管2と内管3との間の高圧の液体冷媒の流路断面積が縮小されているので、二重管式熱交換器1が設けられる冷凍サイクルに注入する冷媒量を減少することができる。 In the double-pipe heat exchanger 1 of the above embodiment, as shown in FIG. 2, multiple points on the inner surface of the outer pipe 2 contact the apex 10b of the corrugated portion 10 of the inner pipe 3, and the inner pipe 3 is supported by the outer pipe 2. Therefore, as shown in FIG. 3, there is no risk of the inner pipe 3 deforming or cracking when the double pipe is bent. Furthermore, because the outer pipe 2 is reduced in diameter, the cross-sectional area of the flow path for high-pressure liquid refrigerant between the outer pipe 2 and the inner pipe 3 is reduced, so the amount of refrigerant injected into the refrigeration cycle in which the double-pipe heat exchanger 1 is installed can be reduced.
次に、二重管式熱交換器1の製造方法、特に、外管2を内管3に接触させる方法の実施形態を説明する。 Next, we will explain an embodiment of a method for manufacturing the double-pipe heat exchanger 1, particularly a method for contacting the outer pipe 2 with the inner pipe 3.
<第1実施形態>
図4は、外管2を内管3に接触させる第1実施形態の複数の可動片21を示す。複数の可動片21は、外管2の回りに等間隔に8つ配置されている。各可動片21は、径方向の断面が扇形で、径方向内側の内面は、外管2の外周面より少し小さい半径の曲面からなり、軸方向に所定長さを有している。各可動片21は、外管2の径方向に移動可能で、外管2を同時に押し付けることができる。
First Embodiment
4 shows the multiple movable pieces 21 of the first embodiment that bring the outer tube 2 into contact with the inner tube 3. Eight movable pieces 21 are arranged at equal intervals around the outer tube 2. Each movable piece 21 has a sector-shaped cross section in the radial direction, and the inner surface on the radially inner side is a curved surface with a radius slightly smaller than the outer peripheral surface of the outer tube 2, and has a predetermined length in the axial direction. Each movable piece 21 is movable in the radial direction of the outer tube 2 and can simultaneously press against the outer tube 2.
外管2の内側に内管3を挿入し、外管2の両端から内管3の両端部が突出するように配置した状態で、外管2を縮径する所定範囲Lの一端に複数の可動片21を位置させる。ここで、複数の可動片21は、内管3の波型形状部10の頂部10bと対向するようにすることが好ましい。複数の可動片21を径方向内方に移動し、外管2を押圧すると、図6に示すように、外管2の可動片21に押圧された部分が径方向内方に内管3に向かって移動して、内管3の波型形状部10の頂部10bに接触した状態で塑性変形し、外管2の外面に凹部6aを形成する。この凹部6aが周方向に複数形成されて、縮径部6となる。 The inner tube 3 is inserted inside the outer tube 2, with both ends of the inner tube 3 protruding from both ends of the outer tube 2. Multiple movable pieces 21 are positioned at one end of the predetermined range L for reducing the diameter of the outer tube 2. Preferably, the multiple movable pieces 21 face the crests 10b of the corrugated portion 10 of the inner tube 3. When the multiple movable pieces 21 are moved radially inward and the outer tube 2 is pressed, as shown in Figure 6, the portions of the outer tube 2 pressed by the movable pieces 21 move radially inward toward the inner tube 3 and plastically deform while in contact with the crests 10b of the corrugated portion 10 of the inner tube 3, forming recesses 6a on the outer surface of the outer tube 2. Multiple recesses 6a are formed circumferentially, forming the reduced diameter portion 6.
図5(a)に示すように、複数の可動片21により1回目の凹部6aを形成した後、図5(b)に示すように、外管2の軸方向に移動させて、2回目の凹部6aを形成し、これを複数回繰り返す。複数の可動片21により先に形成された凹部6aの軸方向長さsと、次に形成される凹部6aの軸方向長さsとは、所定寸法ΔLだけ、一部重なるようにする。複数回の長さsの凹部6aの形成を繰り返すことにより、図5(c)に示すように、所定範囲Lに凹部6aが形成される。なお、長さsの凹部6aは、軸方向に間隔を空けて、重ならないようにしてもよいし、周方向にずらせてもよい。 As shown in Figure 5(a), the first recess 6a is formed using multiple movable pieces 21, and then, as shown in Figure 5(b), the outer tube 2 is moved axially to form a second recess 6a, and this process is repeated multiple times. The axial length s of the recess 6a previously formed by the multiple movable pieces 21 and the axial length s of the recess 6a subsequently formed are arranged to overlap by a predetermined dimension ΔL. By repeatedly forming recesses 6a of length s multiple times, recesses 6a are formed within a predetermined range L, as shown in Figure 5(c). Note that the recesses 6a of length s may be spaced apart in the axial direction so as not to overlap, or may be offset circumferentially.
図7に示すように、複数の可動片21の複数回の押圧により、外管2の外面に軸方向に延びる複数の凹部6aが形成され、外管2の内面の複数箇所Pが内管3の波型形状部10の頂部10bに、直線状に接触する。周方向に隣接する凹部6aの間には、複数の可動片21で押圧されなかったために、軸方向に延びる凸部13が形成される。 As shown in Figure 7, multiple pressing operations by the multiple movable pieces 21 form multiple axially extending recesses 6a on the outer surface of the outer tube 2, and multiple locations P on the inner surface of the outer tube 2 come into linear contact with the peaks 10b of the corrugated portion 10 of the inner tube 3. Between circumferentially adjacent recesses 6a, which are not pressed by the multiple movable pieces 21, axially extending protrusions 13 are formed.
図1に示すように、内管3の両端部の波型形状部10が形成されていない範囲の外周部に、外管2の両端部を径方向に締め付けた後、ろう付け又は溶接により固定する。続いて、外管2の一端側に外管流入口8を取り付け、他端側に外管流出口9を取り付ける。 As shown in Figure 1, both ends of the outer pipe 2 are radially fastened to the outer periphery of the inner pipe 3 in the area where the corrugated portions 10 are not formed, and then secured by brazing or welding. Next, an outer pipe inlet 8 is attached to one end of the outer pipe 2, and an outer pipe outlet 9 is attached to the other end.
第1実施形態の二重管式熱交換器1の製造方法によれば、径方向に移動可能な複数の可動片21により外管2を径方向内方に押圧するだけで、外管2の縮径加工を容易に行える。 According to the manufacturing method of the double-pipe heat exchanger 1 of the first embodiment, the outer pipe 2 can be easily reduced in diameter simply by pressing the outer pipe 2 radially inward with multiple movable pieces 21 that can move radially.
<第2実施形態>
第2実施形態以下の実施形態では、外管2を内管3に挿入及び配置する工程、及び外管2を内管3に固定する工程は、第1実施形態と同様であるので、説明を省略し、外管2を内管3に接触させる工程のみ説明する。
Second Embodiment
In the second embodiment and the following embodiments, the process of inserting and positioning the outer tube 2 into the inner tube 3 and the process of fixing the outer tube 2 to the inner tube 3 are the same as those in the first embodiment, so the explanation will be omitted and only the process of bringing the outer tube 2 into contact with the inner tube 3 will be explained.
図8は、外管2を内管3に接触させる第2実施形態の複数のローラ22を示す。複数のローラ22は、外管2の回りに等間隔に4つ配置されている。各ローラ22は、外管2の中心軸と直交する平面上であって、外管2の中心を通る直線に対して直交する回転軸22aを有し、この回転軸22aの回りに回転可能である。ローラ22は、中央部は径が小さく、両端に向かって径が大きくなる、所謂鼓形の外周面を有する。ローラ22の軸芯を含む断面の円弧形状は、外管2の曲率半径より少し小さく、外管2の外周の約4分の1の長さを有する。各ローラ22は、外管2の径方向に移動可能で、外管2を同時に押し付けることができる。ここで、複数のローラ22は、内管3の波型形状部10の頂部10bと対向するようにすることが好ましい。 Figure 8 shows a second embodiment of rollers 22 that bring the outer tube 2 into contact with the inner tube 3. Four rollers 22 are arranged at equal intervals around the outer tube 2. Each roller 22 has a rotation axis 22a that is perpendicular to the central axis of the outer tube 2 and perpendicular to a line passing through the center of the outer tube 2, and is rotatable around this rotation axis 22a. The rollers 22 have a small diameter in the center and a larger diameter toward both ends, creating a so-called hourglass-shaped outer surface. The cross section of the roller 22, including its axis, is slightly smaller than the radius of curvature of the outer tube 2 and has a length approximately one-quarter of the outer circumference of the outer tube 2. Each roller 22 is movable radially around the outer tube 2 and can simultaneously press the outer tube 2. Preferably, the rollers 22 face the crests 10b of the corrugated portions 10 of the inner tube 3.
図9(a)に示すように、外管2を縮径する所定範囲Lの一端にローラ22を位置させ、複数のローラ22を径方向内方に移動し、外管2を押圧すると、外管2は、径方向内方に内管3の波型形状部10の頂部10bに向かって塑性変形し、図10に示すように、外管2の内面の複数箇所Pが内管3の頂部10bに接触する。図9(b)に示すように、ローラ22を内管3に押し付けたまま、外管2を軸方向にスライドさせると、図11に示すように、ローラ22により、外管2の外面に軸方向に延びる凹部6bが形成され、管2の内面の複数箇所が内管3の波型形状部10の頂部10bに、直線状に接触する。周方向に隣接する凹部6bの間には、複数のローラ22で押圧されなかったために、軸方向に延びる凸部14が形成される。 As shown in Figure 9(a), rollers 22 are positioned at one end of the predetermined range L within which the outer tube 2 is reduced in diameter. The rollers 22 are then moved radially inward to press against the outer tube 2. The outer tube 2 undergoes plastic deformation radially inward toward the crests 10b of the corrugated portion 10 of the inner tube 3, and as shown in Figure 10, multiple locations P on the inner surface of the outer tube 2 come into contact with the crests 10b of the inner tube 3. As shown in Figure 9(b), when the outer tube 2 is slid axially while the rollers 22 are pressed against the inner tube 3, the rollers 22 form axially extending recesses 6b on the outer surface of the outer tube 2, as shown in Figure 11. Multiple locations on the inner surface of the tube 2 come into linear contact with the crests 10b of the corrugated portion 10 of the inner tube 3. Axial protrusions 14 are formed between circumferentially adjacent recesses 6b because they are not pressed by the rollers 22.
第2実施形態の二重管式熱交換器1の製造方法によれば、径方向に移動可能な複数のローラ22により外管2を径方向内方に押圧し、外管2を軸方向に移動させるだけで、外管2の縮径加工を容易に行える。 According to the manufacturing method of the double-pipe heat exchanger 1 of the second embodiment, the outer pipe 2 can be easily reduced in diameter simply by pressing the outer pipe 2 radially inward with a plurality of radially movable rollers 22 and moving the outer pipe 2 in the axial direction.
<第3実施形態>
図12は、外管2を内管3に接触させる第3実施形態の複数のローラ23を示す。複数のローラ23は、外管2の回りに等間隔に4つ配置されている。各ローラ23は、外管2の中心軸と直交する平面上であって、外管2の中心を通る直線に対して直交する回転軸23aを有し、この回転軸23aの回りに回転可能である。ローラ23は、第2実施形態のローラ22よりも幅が狭く、円弧又は平面の外周面を有する。各ローラ23は、外管2の径方向に移動可能で、外管2を同時に押し付けることができる。ここで、複数のローラ23は、内管3の波型形状部10の頂部10bと対向するようにすることが好ましい。
Third Embodiment
12 shows a third embodiment of rollers 23 for bringing the outer tube 2 into contact with the inner tube 3. Four rollers 23 are arranged at equal intervals around the outer tube 2. Each roller 23 has a rotation axis 23a that is on a plane perpendicular to the central axis of the outer tube 2 and perpendicular to a line passing through the center of the outer tube 2, and is rotatable around this rotation axis 23a. The rollers 23 are narrower than the rollers 22 of the second embodiment and have an arcuate or flat outer peripheral surface. Each roller 23 is movable in the radial direction of the outer tube 2 and can simultaneously press the outer tube 2. Preferably, the rollers 23 face the crests 10b of the corrugated portion 10 of the inner tube 3.
図13(a)に示すように、外管2を縮径する所定範囲Lの一端に複数のローラ23を位置させ、複数のローラ23を径方向内方に移動し、外管2を押圧すると、外管2は、径方向内方に内管3の波型形状部10の頂部10bに向かって塑性変形し、図14に示すように、外管2の内面の複数箇所Pが内管3の波型形状部10の頂部10bに接触する。図13(b)に示すように、ローラ23を内管3に押し付けたまま、外管2を軸方向にスライドさせると、図15に示すように、ローラ23により、外管2の外面に軸方向に延びる凹溝6cが形成され、外管2の内面の複数箇所が内管3の波型形状部10の頂部10bに、直線状に接触する。 As shown in Figure 13(a), when multiple rollers 23 are positioned at one end of a predetermined range L within which the outer tube 2 is reduced in diameter, and the multiple rollers 23 are moved radially inward to press against the outer tube 2, the outer tube 2 undergoes plastic deformation radially inward toward the crests 10b of the corrugated portions 10 of the inner tube 3. As shown in Figure 14, multiple locations P on the inner surface of the outer tube 2 come into contact with the crests 10b of the corrugated portions 10 of the inner tube 3. As shown in Figure 13(b), when the outer tube 2 is slid axially while the rollers 23 are pressed against the inner tube 3, the rollers 23 form axially extending grooves 6c on the outer surface of the outer tube 2, as shown in Figure 15. Multiple locations on the inner surface of the outer tube 2 come into linear contact with the crests 10b of the corrugated portions 10 of the inner tube 3.
第3実施形態の二重管式熱交換器1の製造方法によれば、径方向に移動可能な複数のローラ23により外管2を径方向内方に押圧し、外管2を軸方向に移動させるだけで、外管2の縮径加工を容易に行える。また、外管2の内面の複数箇所を内管3の波型形成部10の頂部10bに接触させるので、外管2と内管3との間の第1流路4が狭くならない。 According to the manufacturing method of the double-pipe heat exchanger 1 of the third embodiment, the outer pipe 2 can be easily reduced in diameter simply by pressing the outer pipe 2 radially inward with a plurality of radially movable rollers 23 and then moving the outer pipe 2 axially. Furthermore, because multiple points on the inner surface of the outer pipe 2 come into contact with the crests 10b of the corrugated portions 10 of the inner pipe 3, the first flow path 4 between the outer pipe 2 and inner pipe 3 does not become narrow.
第3実施形態では、図12に示すように、波型形状部10の頂部10bにローラ23が対向するように周方向に配置し、複数のローラ23により外管2を径方向内方に押圧して、外管2を塑性変形させて、外管2の内面の複数箇所を内管3の波型形成部10の頂部10bに接触させているが、図16に示すように、波型形状部10の底部10aにローラ23が対向するように周方向に配置し、複数のローラ23により外管2を径方向内方に押圧して、外管2を塑性変形させて、図17に示すように、ローラ23の両側の外管2の内面の複数箇所Pを、内管3の波型形成部10の頂部10bに接触させてもよい。 In the third embodiment, as shown in FIG. 12, rollers 23 are arranged circumferentially to face the crests 10b of the corrugated portions 10, and the outer tube 2 is pressed radially inward by the multiple rollers 23, plastically deforming the outer tube 2 and bringing multiple locations on the inner surface of the outer tube 2 into contact with the crests 10b of the corrugated portions 10 of the inner tube 3. However, as shown in FIG. 16, rollers 23 may be arranged circumferentially to face the bottoms 10a of the corrugated portions 10, and the outer tube 2 is pressed radially inward by the multiple rollers 23, plastically deforming the outer tube 2, bringing multiple locations P on the inner surface of the outer tube 2 on both sides of the rollers 23 into contact with the crests 10b of the corrugated portions 10 of the inner tube 3, as shown in FIG. 17.
<第4実施形態>
図18は、外管2を内管3に接触させる第4実施形態の複数のローラ24を示す。複数のローラ24は、外管2の回りに等間隔に4つ配置されている。各ローラ24は、外管2の中心軸と平行な回転軸24aを有し、この回転軸24aの回りに回転可能である。ローラ24は、第2実施形態のローラ22よりも幅が狭く、円弧又は平面の外周面を有する。各ローラ24は、外管2の径方向に移動可能で外管2を同時に押し付けることができるとともに、外管2の回りに旋回可能になっている。図18では、ローラ24の数は4つに限らず、任意であるが、3つであることが好ましい。
Fourth Embodiment
FIG. 18 shows a fourth embodiment of rollers 24 that bring the outer tube 2 into contact with the inner tube 3. Four rollers 24 are arranged at equal intervals around the outer tube 2. Each roller 24 has a rotation axis 24a parallel to the central axis of the outer tube 2 and is rotatable around this rotation axis 24a. The rollers 24 are narrower than the rollers 22 of the second embodiment and have an arcuate or flat outer peripheral surface. Each roller 24 is movable in the radial direction of the outer tube 2, allowing the rollers 24 to simultaneously press against the outer tube 2, and is also capable of rotating around the outer tube 2. In FIG. 18, the number of rollers 24 is not limited to four and can be any number, but three is preferred.
図19(a)に示すように、ローラ24を外管2に押し付けたまま、ローラ24を外管2の回りに旋回させ、かつ、外管2を軸方向にスライドさせると、ローラ24により、図19(b)、図21に示すように、外管2の外面に軸方向に延びる螺旋状の凹溝6dが形成され、図20に示すように、外管2の内面の複数箇所Pが内管3の頂部10bに接触する。 As shown in Figure 19(a), when the roller 24 is rotated around the outer tube 2 while pressed against the outer tube 2 and the outer tube 2 is slid in the axial direction, the roller 24 forms a spiral groove 6d extending in the axial direction on the outer surface of the outer tube 2, as shown in Figures 19(b) and 21, and multiple points P on the inner surface of the outer tube 2 come into contact with the top 10b of the inner tube 3, as shown in Figure 20.
第4実施形態の二重管式熱交換器1の製造方法によれば、径方向に移動可能な複数のローラ24により外管2を径方向内方に押圧して外管2の回りに旋回させながら、外管2を軸方向に移動させるだけで、外管2の縮径加工を容易に行える。 According to the manufacturing method of the double-pipe heat exchanger 1 of the fourth embodiment, the outer pipe 2 can be easily reduced in diameter simply by moving the outer pipe 2 in the axial direction while pressing the outer pipe 2 radially inward with a plurality of radially movable rollers 24 and rotating them around the outer pipe 2.
本発明は、以上の実施形態に限るものではなく、種々変更が可能である。
例えば、前記実施形態では、内管3に8つの波型形状部10を設けたが、8つに限るものではなく、複数設ければよい。また、波型形状部10の底部10aと頂部10bとの間の高さも適宜変更することができる。さらに、波型形状部10は、軸方向に螺旋状に延びる複数の底部10aと頂部10bとが、周方向に繰り返すようにしてもよい。
The present invention is not limited to the above-described embodiment, and various modifications are possible.
For example, in the above embodiment, eight corrugated portions 10 are provided on the inner pipe 3, but the number is not limited to eight and any number may be provided. The height between the bottom 10a and the crest 10b of each corrugated portion 10 can also be changed as appropriate. Furthermore, the corrugated portion 10 may have a plurality of bottoms 10a and crests 10b extending spirally in the axial direction, repeated in the circumferential direction.
1…二重管式熱交換器
2…外管
3…内管
4…第1流路
5…第2流路
6…縮径部
6a、6b…凹部
6c、6d…凹溝
7…内面
8…外管流入口
9…外管流出口
10…波型形状部
10a…底部
10b…頂部
11…内管流入口
12…内管流出口
13、14…凸部
21…可動片
22、23、24…ローラ
1...Double tube heat exchanger 2...Outer tube 3...Inner tube 4...First channel 5...Second channel 6...Reduced diameter section 6a, 6b...Concave section 6c, 6d...Concave groove 7...Inner surface 8...Outer tube inlet 9...Outer tube outlet 10...Wave shaped part 10a...Bottom part 10b...Top part 11...Inner tube inlet 12...Inner tube outlet 13, 14... Convex portion 21... Movable piece 22, 23, 24... Roller
Claims (4)
前記外管の回りに等間隔に配置された複数の可動片を前記外管に径方向内方に押し付けて、前記外管と前記内管とを軸方向に移動させ、これを複数回繰り返すことで、前記外管の外面に軸方向に延びる凹部を形成することにより、外面に複数の底部と頂部とが形成された前記内管に対して、前記外管を縮径し、前記外管の内面の複数箇所を前記内管の頂部に接触させることを特徴とする二重管式熱交換器の製造方法。 A method for manufacturing a double-pipe heat exchanger including an outer pipe and an inner pipe inserted into the outer pipe,
A method for manufacturing a double-pipe heat exchanger, characterized in that a plurality of movable pieces arranged at equal intervals around the outer pipe are pressed radially inward against the outer pipe, and the outer pipe and the inner pipe are moved axially, and this is repeated multiple times to form axially extending recesses on the outer surface of the outer pipe, thereby reducing the diameter of the outer pipe relative to the inner pipe, which has a plurality of bottoms and tops formed on its outer surface, and bringing multiple points on the inner surface of the outer pipe into contact with the tops of the inner pipe .
前記外管の中心軸と直交する平面上に回転軸を有する複数のローラを前記外管に押し付けたまま、前記外管と前記内管とを軸方向に移動させて、前記ローラにより、前記外管の外面に軸方向に延びる凹部を形成することにより、外面に複数の底部と頂部とが形成された前記内管に対して、前記外管を縮径し、前記外管の内面の複数箇所を前記内管の頂部に接触させることを特徴とする二重管式熱交換器の製造方法。 A method for manufacturing a double-pipe heat exchanger including an outer pipe and an inner pipe inserted into the outer pipe,
A method for manufacturing a double-pipe heat exchanger, characterized in that: while pressing a plurality of rollers, each having a rotation axis on a plane perpendicular to the central axis of the outer tube, against the outer tube, the outer tube and the inner tube are moved axially, and the rollers form recesses extending in the axial direction on the outer surface of the outer tube, thereby reducing the diameter of the outer tube relative to the inner tube, which has a plurality of bottoms and tops formed on its outer surface, and bringing multiple points on the inner surface of the outer tube into contact with the tops of the inner tube .
前記外管の中心軸と直交する平面上に回転軸を有する複数のローラを前記外管に押し付けたまま、前記外管と前記内管とを軸方向に移動させて、前記ローラにより、前記外管の外面に軸方向に延びる凹溝を形成することにより、外面に複数の底部と頂部とが形成された前記内管に対して、前記外管を縮径し、前記外管の内面の複数箇所を前記内管の頂部に接触させることを特徴とする二重管式熱交換器の製造方法。 A method for manufacturing a double-pipe heat exchanger including an outer pipe and an inner pipe inserted into the outer pipe,
A method for manufacturing a double-pipe heat exchanger, characterized in that a plurality of rollers having rotation axes on a plane perpendicular to the central axis of the outer tube are pressed against the outer tube, and the outer tube and the inner tube are moved axially, so that the rollers form axially extending grooves on the outer surface of the outer tube, thereby reducing the diameter of the outer tube relative to the inner tube, which has a plurality of bottoms and tops formed on its outer surface, and bringing multiple points on the inner surface of the outer tube into contact with the tops of the inner tube .
前記外管の中心軸と平行な回転軸を有する複数のローラを前記外管に押し付けたまま、前記ローラを前記外管の回りに旋回させるとともに、前記外管と前記内管とを軸方向に移動させて、前記ローラにより、前記外管の外面に軸方向に延びる螺旋状の凹溝を形成することにより、外面に複数の底部と頂部とが形成された前記内管に対して、前記外管を縮径し、前記外管の内面の複数箇所を前記内管の頂部に接触させることを特徴とする二重管式熱交換器の製造方法。
A method for manufacturing a double-pipe heat exchanger including an outer pipe and an inner pipe inserted into the outer pipe,
A method for manufacturing a double-pipe heat exchanger, comprising the steps of: pressing a plurality of rollers, each having a rotation axis parallel to the central axis of the outer tube, against the outer tube; rotating the rollers around the outer tube while moving the outer tube and the inner tube axially; forming a spiral groove extending in the axial direction on the outer surface of the outer tube with the rollers; thereby reducing the diameter of the outer tube relative to the inner tube, which has a plurality of bottoms and tops formed on its outer surface, and bringing multiple points on the inner surface of the outer tube into contact with the tops of the inner tube .
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Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20080141665A1 (en) | 2005-01-21 | 2008-06-19 | T. Rad Co., Ltd. | Double Pipe Heat Exchanger and Method of Manufacturing the Same |
| JP2014055748A (en) | 2012-09-13 | 2014-03-27 | Calsonic Kansei Corp | Internal heat exchanger and method for producing the same |
| JP2016053469A (en) | 2015-09-04 | 2016-04-14 | 株式会社ヴァレオジャパン | Manufacturing method of double pipe |
| JP2016095132A (en) | 2016-02-26 | 2016-05-26 | 株式会社ヴァレオジャパン | Method for manufacturing double pipe |
| US20190353427A1 (en) | 2018-05-18 | 2019-11-21 | Denso International America, Inc. | Double-tube internal heat exchanger |
| JP2021096011A (en) | 2019-12-13 | 2021-06-24 | 株式会社Uacj | Double pipe for heat exchanger |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3012031B2 (en) * | 1991-05-28 | 2000-02-21 | 三和テッキ株式会社 | Elevator switching device |
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Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20080141665A1 (en) | 2005-01-21 | 2008-06-19 | T. Rad Co., Ltd. | Double Pipe Heat Exchanger and Method of Manufacturing the Same |
| JP2014055748A (en) | 2012-09-13 | 2014-03-27 | Calsonic Kansei Corp | Internal heat exchanger and method for producing the same |
| JP2016053469A (en) | 2015-09-04 | 2016-04-14 | 株式会社ヴァレオジャパン | Manufacturing method of double pipe |
| JP2016095132A (en) | 2016-02-26 | 2016-05-26 | 株式会社ヴァレオジャパン | Method for manufacturing double pipe |
| US20190353427A1 (en) | 2018-05-18 | 2019-11-21 | Denso International America, Inc. | Double-tube internal heat exchanger |
| JP2021096011A (en) | 2019-12-13 | 2021-06-24 | 株式会社Uacj | Double pipe for heat exchanger |
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| JP2023070469A (en) | 2023-05-19 |
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