JP3344991B2 - Heat exchange panel - Google Patents

Heat exchange panel

Info

Publication number
JP3344991B2
JP3344991B2 JP2000160984A JP2000160984A JP3344991B2 JP 3344991 B2 JP3344991 B2 JP 3344991B2 JP 2000160984 A JP2000160984 A JP 2000160984A JP 2000160984 A JP2000160984 A JP 2000160984A JP 3344991 B2 JP3344991 B2 JP 3344991B2
Authority
JP
Japan
Prior art keywords
heat
heat exchange
exchange panel
plate
contact
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.)
Expired - Fee Related
Application number
JP2000160984A
Other languages
Japanese (ja)
Other versions
JP2001336777A (en
Inventor
重治 橋本
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.)
SASSOH KOGYO CO.,LTD
Original Assignee
SASSOH KOGYO 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 SASSOH KOGYO CO.,LTD filed Critical SASSOH KOGYO CO.,LTD
Priority to JP2000160984A priority Critical patent/JP3344991B2/en
Publication of JP2001336777A publication Critical patent/JP2001336777A/en
Application granted granted Critical
Publication of JP3344991B2 publication Critical patent/JP3344991B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Steam Or Hot-Water Central Heating Systems (AREA)
  • Domestic Hot-Water Supply Systems And Details Of Heating Systems (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、建物の床や壁等の
構造物に付設される熱交換パネルに係り、熱伝達性に優
れた熱交換パネルに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat exchange panel provided on a structure such as a floor or a wall of a building, and more particularly to a heat exchange panel having excellent heat transferability.

【0002】[0002]

【従来の技術】従来、この種の熱交換パネルとしては、
例えば、図4に示すように、特開平10−19287号
公報に記載のものが挙げられる。この熱交換パネルP
は、床板100が敷設される金属製の外板101を有し
外板101に熱を伝達する熱交換体102と、この熱交
換体102の裏面側に付設された断熱材103とを備え
ている。熱交換体102は、外板101の裏面側に形成
され熱交換媒体が充填された充填部104と、熱源を供
給する熱伝達管105とで構成され、充填部104には
長手方向中央にU溝106が形成され、U溝106内に
熱伝達管105が配置されている。また、充填部104
においては、U溝106に向けて熱交換媒体が移動する
ように底部108が傾斜形成されている。充填部104
の内部には、U溝106の長手方向に直角に敷居107
を複数備えている。この従来の熱交換パネルPによれ
ば、熱伝達管105に熱源が供給されるとU溝106に
在る液体の熱交換媒体が気化し、充填部104内に充満
する。気化した熱交換媒体は、充填部104外部に熱を
放熱し、液化して充填部104内壁に付着する。付着し
た熱交換媒体は、重みにより流下し底部の傾斜に沿って
U溝106に移動し、再度熱源に接触する。このよう
に、充填部104内で、熱交換媒体の気化−液化が繰り
返されて熱の伝達が行なわれる。
2. Description of the Related Art Conventionally, as this type of heat exchange panel,
For example, as shown in FIG. 4, the one described in JP-A-10-19287 can be mentioned. This heat exchange panel P
Is provided with a heat exchanger 102 having a metal outer plate 101 on which a floor plate 100 is laid and transmitting heat to the outer plate 101, and a heat insulating material 103 attached to the back side of the heat exchanger 102. I have. The heat exchange body 102 includes a filling portion 104 formed on the back side of the outer plate 101 and filled with a heat exchange medium, and a heat transfer tube 105 for supplying a heat source. A groove 106 is formed, and the heat transfer tube 105 is disposed in the U groove 106. The filling unit 104
, The bottom 108 is formed so as to be inclined so that the heat exchange medium moves toward the U groove 106. Filling section 104
Sill 107 perpendicular to the longitudinal direction of the U-groove 106
Are provided. According to this conventional heat exchange panel P, when a heat source is supplied to the heat transfer tube 105, the liquid heat exchange medium in the U groove 106 is vaporized and filled in the filling portion 104. The vaporized heat exchange medium radiates heat to the outside of the filling section 104, liquefies, and adheres to the inner wall of the filling section 104. The attached heat exchange medium flows down due to the weight, moves to the U-shaped groove 106 along the slope of the bottom, and comes into contact with the heat source again. As described above, in the filling section 104, the heat exchange medium is repeatedly vaporized and liquefied to transfer heat.

【0003】[0003]

【発明が解決しようとする課題】ところで、この従来の
熱交換パネルPにおいては、熱伝達率を向上させるた
め、充填部104の体積を拡大して放熱面積を広げては
いるが、充填部104内部に複数の敷居107を設け、
更に底部108に傾斜を与えるという複雑な構造とな
り、製造に手間を要するという問題があった。このよう
に、複雑な構造にしなければならない理由は、気化した
熱交換媒体は、放熱すると放熱した箇所で液化し、液化
した熱交換媒体はそのままではU溝106に還元しない
ため、熱伝達管105に接触する熱交換媒体が減少する
ことになり、この熱交換媒体の減少は、熱伝達率の低下
をもたらすことから、液化した熱交換媒体が熱源の元へ
移動し易い構造にする必要が生じ、そのため、液化した
熱交換媒体が複数の敷居107を伝わって、傾斜した底
部108を流れてU溝106に至り易くするためであ
る。
In the conventional heat exchange panel P, the volume of the filling portion 104 is increased to increase the heat radiation area in order to improve the heat transfer coefficient. A plurality of thresholds 107 are provided inside,
Furthermore, there is a problem in that the bottom portion 108 has a complicated structure in which an inclination is provided, and it takes time and effort to manufacture. The reason why such a complicated structure is required is that the vaporized heat exchange medium is liquefied at the place where the heat is radiated when the heat is radiated, and the liquefied heat exchange medium is not reduced to the U groove 106 as it is, so The heat exchange medium that comes into contact with the heat exchange medium decreases, and this decrease in heat exchange medium causes a decrease in the heat transfer coefficient. Therefore, it is necessary to adopt a structure in which the liquefied heat exchange medium easily moves to the heat source. Therefore, the liquefied heat exchange medium is transmitted through the plurality of thresholds 107, flows on the inclined bottom portion 108, and easily reaches the U groove 106.

【0004】本発明は、このような問題点に鑑みてなさ
れたもので、簡易な構造で放熱面積を増大し、熱伝達性
に優れた熱交換パネルを提供することを目的とする。
[0004] The present invention has been made in view of such problems, and has as its object to provide a heat exchange panel which has a simple structure, has an increased heat dissipation area, and has excellent heat transferability.

【0005】[0005]

【課題を解決するための手段】このような課題を解決す
るための本発明の技術的手段は、金属製の外板と、該外
板の裏側に設けられ外板に熱を伝達する熱交換体と、上
記外板の裏側に設けられるとともに上記熱交換体が埋設
される断熱材とを備えた熱交換パネルにおいて、上記熱
交換体を、熱交換媒体を充填した断面円形の外管及び該
外管内に設けられ、該熱交換媒体を気化もしくは液化さ
せる熱伝達管を備えて構成し、該熱交換体の外管を上記
外板に接触させた構成とした。これにより、熱伝達管と
外板とを接触した簡易な構造で放熱面積を増大して、熱
伝達性を向上することができる。この熱交換パネルにお
いて、熱交換媒体が気化したときには、熱交換体から放
熱が生じ、熱は熱交換体に接触している外板に伝達され
る。外板はその金属の比熱に応じて略均一に全体から放
熱を行なう。熱交換媒体が液化したときには、熱交換体
は吸熱を行ない、熱が熱交換体に接触している外板から
伝達される。外板はその金属の比熱に応じて略均一に全
体から吸熱を行なう。また、必要に応じ、上記熱交換体
の外管が接触する上記外板の接触部を、該外管の外周に
沿った円弧面に形成した構成とした。熱交換体は、断面
円形の簡易な形状であり、液化した熱交換媒体は内壁面
を移動して循環的に熱交換可能になる。これにより、単
に外板面と外周とを接触するときよりも接触面積が拡大
するので、熱伝達効率を向上することができる。
The technical means of the present invention for solving the above problems is to provide a metal outer plate and a heat exchanger provided on the back side of the outer plate for transferring heat to the outer plate. A heat exchange panel comprising a body and a heat insulating material provided on the back side of the outer plate and in which the heat exchanger is embedded, wherein the heat exchanger is an outer tube having a circular cross section filled with a heat exchange medium, and A heat transfer tube is provided in the outer tube for vaporizing or liquefying the heat exchange medium, and the outer tube of the heat exchanger is brought into contact with the outer plate. Thus, the heat transfer area can be increased with a simple structure in which the heat transfer tube and the outer plate are in contact with each other, and the heat transfer property can be improved. In this heat exchange panel, when the heat exchange medium is vaporized, heat is released from the heat exchange body, and the heat is transmitted to the outer plate in contact with the heat exchange body. The outer plate radiates heat from the whole substantially uniformly according to the specific heat of the metal. When the heat exchange medium is liquefied, the heat exchanger absorbs heat and heat is transferred from the skin in contact with the heat exchanger. The outer plate absorbs heat from the whole substantially uniformly according to the specific heat of the metal. In addition, if necessary, the contact portion of the outer plate with which the outer tube of the heat exchanger comes into contact is formed on an arc surface along the outer periphery of the outer tube. The heat exchange body has a simple shape with a circular cross section, and the liquefied heat exchange medium moves on the inner wall surface so that heat can be exchanged cyclically. Accordingly, the contact area is larger than when the outer plate surface and the outer periphery are simply in contact with each other, so that the heat transfer efficiency can be improved.

【0006】更に、必要に応じ、上記接触部と該接触部
に連続する一般部との境界に、表側に露出する凹部を設
けた構成とした。凹部は、保熱空間となり外板側の保熱
性を向上することができる。更にまた、必要に応じ、上
記接触部及び該接触部に連続する一般部の板厚を略同じ
に形成し、かつ該接触部の表側頂部と一般部の表面とを
同位に形成した構成とした。板厚を均一にすることによ
り熱伝達率を一定にし、接触部の表側頂部と一般部の表
面とを同位にしたので、外板への接触面を平面状にし板
状体の接触を安定させる。
Further, if necessary, a concave portion exposed on the front side is provided at a boundary between the contact portion and a general portion connected to the contact portion. The concave portion serves as a heat retaining space and can improve the heat retaining property on the outer plate side. Furthermore, if necessary, the contact portion and the general portion continuing to the contact portion are formed to have substantially the same thickness, and the top of the contact portion and the surface of the general portion are formed at the same level. . The heat transfer coefficient is constant by making the plate thickness uniform, and the top of the contact part and the surface of the general part are at the same level, so that the contact surface to the outer plate is flat and the contact of the plate-like body is stabilized. .

【0007】また、必要に応じ、上記接触部の表側頂部
に、伝熱板を設けた構成とした。伝熱板の設置は、放熱
面積の拡大となる。更に、必要に応じ、上記伝熱板を、
上記接触部の表側頂部の左右に延設した構成とした。伝
熱板の面積が拡大するので、放熱面積も拡大する。更に
また、必要に応じ、上記伝熱板の上面と、上記一般部の
表面とを面一にした構成とした。同一面に揃えると、そ
の面に放熱を介在する平板を密着させることができる。
[0007] If necessary, a heat transfer plate is provided on the top of the front side of the contact portion. Installation of the heat transfer plate increases the heat radiation area. Further, if necessary, the heat transfer plate
The contact portion was extended right and left from the top on the front side. Since the area of the heat transfer plate increases, the heat radiation area also increases. Further, if necessary, the upper surface of the heat transfer plate and the surface of the general portion are made flush. When aligned on the same surface, a flat plate that intervenes heat radiation can be brought into close contact with that surface.

【0008】また、必要に応じ、上記一般部の裏面に、
上記熱交換体の長手方向に平行なリブを設けた構成とし
た。リブは断熱材内部に嵌入し、断熱材を確固に保持す
る。更に、必要に応じ、上記外板を、アルミニウム製の
成形品とした構成とした。アルミニウムの優れた熱伝達
性により、放熱作用が高まる。
[0008] If necessary, on the back of the above-mentioned general part,
The heat exchanger was provided with ribs parallel to the longitudinal direction. The ribs fit inside the insulation and hold the insulation firmly. Further, if necessary, the outer plate was configured to be a molded product made of aluminum. The excellent heat transfer of aluminum enhances the heat dissipation effect.

【0009】[0009]

【発明の実施の形態】以下、添付図面に基づいて本発明
の実施の形態に係る熱交換パネルを説明する。尚、上記
と同様のものには、同一の符号を付して説明する。図1
に示すように、熱交換パネルPは、金属製の外板1と、
外板1の裏側に設けられ外板1に熱を伝達する熱交換体
2と、外板1の裏側に設けられるとともに熱交換体2が
埋設される断熱材3とを備えて構成される。熱交換パネ
ルPは、通常、外板1を覆う床板や壁板等の被覆板Hを
配して利用される(図1の(b)参照)。外板1は、熱
交換体2の外管4に接触する接触部aと外管4に接触し
ない一般部bで構成される。外板1は、熱伝達性に優れ
た金属製品であることが好ましく、特に軽量で成形性に
富んだアルミニウム製の成形品がより好ましい。接触部
aの形態は、特に限定されないが、実施の形態では、接
触する外管4の外周に沿った円弧面に形成し、外管4の
外周に直接接触する部分を大きくしている。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, a heat exchange panel according to an embodiment of the present invention will be described with reference to the accompanying drawings. Note that the same components as described above are denoted by the same reference numerals and described. FIG.
As shown in the figure, the heat exchange panel P has a metal outer plate 1 and
The heat exchanger 2 is provided on the back side of the outer plate 1 and transmits heat to the outer plate 1, and the heat insulator 3 is provided on the back side of the outer plate 1 and has the heat exchanger 2 embedded therein. The heat exchange panel P is usually used by disposing a cover plate H such as a floor plate or a wall plate that covers the outer plate 1 (see FIG. 1B). The outer plate 1 includes a contact portion a that contacts the outer tube 4 of the heat exchanger 2 and a general portion b that does not contact the outer tube 4. The outer plate 1 is preferably a metal product having excellent heat transfer properties, and more preferably a light-weight, highly moldable aluminum molded product. Although the form of the contact portion a is not particularly limited, in the embodiment, the contact portion a is formed on an arcuate surface along the outer periphery of the outer tube 4 to be in contact, and the portion directly in contact with the outer periphery of the outer tube 4 is enlarged.

【0010】また、接触部aと接触部aに連続する一般
部bとの境界cには、表側に露出する凹部5を設けた。
また、接触部a及び接触部aに連続する一般部bの板厚
を略同じに形成し、かつ接触部aの表側頂部6と一般部
bの表面とを同位に形成している。凹部5の存在によ
り、一般部bと被覆板Hとが直接接触した際に空間を形
成することができる。空間には外板より比熱が大きい空
気で満ちていることから、空間の存在は保温性に効を奏
する。更に、接触部aの表側頂部6には、伝熱板7を設
けている。伝熱板7の形態は、被覆板Hの外板1表部へ
の設置に支障を来さない形状であればよく、実施の形態
では、接触部aの表側頂部6の左右に板状に形成してい
る。また、伝熱板7の上面と一般部bの表面とを面一に
している。このように伝熱板7を形成すれば、外板1表
部に凸部を生じさせて被覆板Hの一般部bへの接触を阻
害することなく熱の伝達域を拡大することができる。一
般部bの裏面には、熱交換体の長手方向に平行なリブ8
を設けて、断熱材3を固定している。
Further, a concave portion 5 exposed on the front side is provided at the boundary c between the contact portion a and the general portion b continuing to the contact portion a.
Further, the contact portion a and the general portion b continuous to the contact portion a have substantially the same plate thickness, and the front side top portion 6 of the contact portion a and the surface of the general portion b are formed at the same level. Due to the presence of the concave portion 5, a space can be formed when the general portion b and the cover plate H come into direct contact. Since the space is filled with air having higher specific heat than the outer plate, the presence of the space has an effect on heat retention. Further, a heat transfer plate 7 is provided on the top part 6 on the front side of the contact part a. The form of the heat transfer plate 7 may be any shape that does not hinder the installation of the cover plate H on the outer surface of the outer plate 1. Has formed. Further, the upper surface of the heat transfer plate 7 and the surface of the general portion b are flush with each other. By forming the heat transfer plate 7 in this manner, a heat transfer region can be expanded without causing a convex portion to be formed on the surface portion of the outer plate 1 and hindering the contact of the cover plate H with the general portion b. Ribs 8 parallel to the longitudinal direction of the heat exchanger are provided on the back surface of the general portion b.
Are provided to fix the heat insulating material 3.

【0011】熱交換体2は、図2に示すように、熱交換
媒体Wを充填した断面円形の外管4と、外管4内に熱交
換媒体Wを気化もしくは液化させる熱伝達管9とを備え
る。外管4は、真直な形状であり外板1と同じ材質であ
ることが好ましい。外管4に充填する熱交換媒体Wは、
気化または液化を容易に行なうものであれば良く、水を
利用することができる。ここでは、外管4内部を常圧よ
り減圧した状態にすることにより水の沸点を下げ、低温
で気化させることができる。熱伝達管9は、熱交換媒体
Wに熱を供給する熱供給管とすることができる。熱供給
管を流れる熱源は、所望の温度を熱交換媒体Wに供給で
きる流体であればよく温水または蒸気を利用できる。熱
供給管を備えた熱交換体2は、放熱作用を奏する。ま
た、熱伝達管9は、熱交換媒体Wから熱を吸収する熱吸
収管とすることができる。熱吸収管を流れる吸熱源は、
所望の温度を熱交換媒体Wに供給できる流体であればよ
く冷水を利用できる。熱吸収管を備えた熱交換体2は、
吸熱作用を奏する。熱伝達管9を、熱供給管及び熱吸収
管として共用してもよく、または熱供給管と熱吸収管と
して別個に設けてもよい。断熱材3は、外板1の裏面に
熱交換体2を埋設するように接着している。熱交換体2
の外管4の両端からは、熱伝達管9の流入部9aと流出
部9bとが断熱材3を貫通して外部に露出している。図
3には熱交換パネルPを6部平板状に配置した一例の平
面図が示される。複数の熱交換パネルPを接続して用い
るときは、熱伝達管9の流出部9bと流入部9aとを接
続管10で連絡することができる。断熱材3の材質とし
ては、断熱性に優れた高発泡ウレタンフォームが好まし
い。高発泡ウレタンフォームを利用することは、軽量で
あり設置施工において特殊な技術や工具も必要としない
利点を有する。
As shown in FIG. 2, the heat exchanger 2 includes an outer tube 4 having a circular cross section filled with a heat exchange medium W, and a heat transfer tube 9 for vaporizing or liquefying the heat exchange medium W inside the outer tube 4. Is provided. The outer tube 4 has a straight shape and is preferably made of the same material as the outer plate 1. The heat exchange medium W filled in the outer tube 4 is
Any material can be used as long as it can be easily vaporized or liquefied, and water can be used. Here, the boiling point of water can be lowered by evacuation of the inside of the outer tube 4 below normal pressure, and it can be vaporized at a low temperature. The heat transfer pipe 9 can be a heat supply pipe that supplies heat to the heat exchange medium W. The heat source flowing through the heat supply pipe may be any fluid that can supply a desired temperature to the heat exchange medium W, and hot water or steam can be used. The heat exchanger 2 provided with the heat supply pipe has a heat radiation effect. Further, the heat transfer tube 9 may be a heat absorption tube that absorbs heat from the heat exchange medium W. The heat absorption source flowing through the heat absorption tube
As long as the fluid can supply a desired temperature to the heat exchange medium W, cold water can be used. The heat exchanger 2 provided with a heat absorption tube
It has an endothermic effect. The heat transfer pipe 9 may be shared as a heat supply pipe and a heat absorption pipe, or may be separately provided as a heat supply pipe and a heat absorption pipe. The heat insulating material 3 is bonded so that the heat exchanger 2 is embedded on the back surface of the outer panel 1. Heat exchanger 2
From both ends of the outer tube 4, the inflow portion 9a and the outflow portion 9b of the heat transfer tube 9 penetrate the heat insulating material 3 and are exposed to the outside. FIG. 3 is a plan view showing an example in which the heat exchange panels P are arranged in a six-part flat plate shape. When connecting and using a plurality of heat exchange panels P, the outflow portion 9b and the inflow portion 9a of the heat transfer tube 9 can be connected by the connection tube 10. As a material of the heat insulating material 3, a highly foamed urethane foam having excellent heat insulating properties is preferable. Utilization of a highly foamed urethane foam has advantages that it is lightweight and does not require special techniques or tools in installation work.

【0012】従って、この実施の形態に係る熱交換パネ
ルPによれば、以下のようにして熱を効率良く伝達す
る。ここで、熱交換パネルPが熱を放出するときと、熱
交換パネルPが熱を吸収するときとに分けて説明する。 A.熱交換パネルPが熱を放出するとき 熱供給管(熱伝達管9)に供給される熱源は温水とし、
外管4内部は熱交換媒体Wとして水を常温,減圧状態で
液化するように充填している。熱供給管に供給する温水
は、外管4に充填された熱交換媒体Wを気化することが
できる温度にしている。熱交換媒体Wを気化して熱伝達
を行なうので、熱伝達範囲を広げることができる。 (A−1)温水供給 外部から熱供給管に熱源となる温水が供給されると、温
水は熱交換パネルPにおける熱供給管の流入部9aから
流出部9bへ、次いで他の熱交換パネルPの流入部9a
から流出部9bへと熱供給管間を接続する接続管10を
介して供給される。温水は、接続管10で接続したすべ
ての熱供給管を循環した後、加温されて再度熱供給管に
供給される。温水の供給径路は、接続管10部分以外は
真直なので、放熱ロスを最小限にして熱供給管を循環す
るようになっている。
Therefore, according to the heat exchange panel P according to this embodiment, heat is efficiently transmitted as follows. Here, the case where the heat exchange panel P emits heat and the case where the heat exchange panel P absorbs heat will be described separately. A. When the heat exchange panel P emits heat, the heat source supplied to the heat supply pipe (heat transfer pipe 9) is hot water,
The inside of the outer tube 4 is filled with water as a heat exchange medium W so as to be liquefied at normal temperature and reduced pressure. The hot water supplied to the heat supply pipe has a temperature at which the heat exchange medium W filled in the outer pipe 4 can be vaporized. Since heat transfer is performed by vaporizing the heat exchange medium W, the heat transfer range can be expanded. (A-1) Hot Water Supply When hot water as a heat source is supplied to the heat supply pipe from the outside, the hot water flows from the inlet 9a of the heat supply pipe to the outlet 9b of the heat exchange panel P, and then to another heat exchange panel P. Inflow section 9a
The heat is supplied to the outlet 9b through a connection pipe 10 connecting the heat supply pipes. The hot water circulates through all the heat supply pipes connected by the connection pipes 10, is heated, and is supplied to the heat supply pipes again. Since the hot water supply path is straight except for the connection pipe 10, the heat supply pipe is circulated with the heat radiation loss minimized.

【0013】(A−2)熱交換処理 熱供給管に接触している熱交換媒体Wは、熱供給管に温
水が供給されると気化し、外管4内に充満する。外管4
に熱交換媒体Wが接触することにより熱交換媒体Wから
熱が伝達され外管4自体の温度が上昇する。熱を与えた
熱交換媒体Wは、液化して外管4の内壁に付着し凝集し
て内壁を下降し底部に移動し熱供給管に接触する。温水
が供給されている間、熱交換体2内部では熱交換媒体W
の気化−液化が繰り返され、熱が外管4へ伝達し続け
る。 (A−3)放熱 外管4に接触している外板1には、外管4の温度上昇に
伴って熱が伝達され、外板1の比熱に基づいて放熱が行
なわれる。外板1の接触部aが外管4の外周に沿った面
となり伝達率を向上させている。また、一般部bに設け
た凹部5は、一般部bの表面に被覆板Hが接触すると比
熱の大きい空気層を形成するので保温性を高めることが
できる。更に、接触部aの表側頂部6に伝熱板7を設け
ているので、外板1の表面積が拡大して熱伝達範囲が広
がり放熱量が増加する。具体的に、熱供給管の中に60
℃の温水を流入させると、熱交換媒体Wは瞬時に気化し
て外管4内に充満する。この現象によって熱交換体2全
体が流入した温水よりわずかに低い温度に加温される。
これまでに実験した結果では、外板1の表面は供給した
温水温度より約20℃低くなる。
(A-2) Heat Exchange Processing When the hot water is supplied to the heat supply pipe, the heat exchange medium W in contact with the heat supply pipe is vaporized and filled in the outer pipe 4. Outer tube 4
When the heat exchange medium W comes into contact with the heat exchange medium W, heat is transmitted from the heat exchange medium W, and the temperature of the outer tube 4 itself increases. The heat exchange medium W to which the heat has been applied is liquefied, adheres to the inner wall of the outer pipe 4 and aggregates, moves down the inner wall, moves to the bottom, and contacts the heat supply pipe. While the hot water is being supplied, the heat exchange medium W
Is repeated, and heat continues to be transmitted to the outer tube 4. (A-3) Heat Dissipation Heat is transmitted to the outer plate 1 in contact with the outer tube 4 as the temperature of the outer tube 4 rises, and heat is radiated based on the specific heat of the outer plate 1. The contact portion a of the outer plate 1 becomes a surface along the outer periphery of the outer tube 4 to improve the transmission rate. In addition, the concave portion 5 provided in the general portion b forms an air layer having a large specific heat when the cover plate H comes into contact with the surface of the general portion b, so that the heat retention can be improved. Further, since the heat transfer plate 7 is provided on the front side top portion 6 of the contact portion a, the surface area of the outer plate 1 is enlarged, the heat transfer range is widened, and the amount of heat radiation is increased. Specifically, 60 in the heat supply pipe
When hot water of ° C. is flowed, the heat exchange medium W evaporates instantaneously and fills the outer tube 4. Due to this phenomenon, the entire heat exchanger 2 is heated to a temperature slightly lower than the flow of warm water.
According to the results of experiments so far, the surface of the outer panel 1 is lower by about 20 ° C. than the supplied hot water temperature.

【0014】B.熱交換パネルPが熱を吸収するとき 熱交換パネルPが熱を吸収するときに、熱吸収管(熱伝
達管9)に供給される熱源は冷水とし、外管4内部は熱
交換媒体Wとして水を常温+α,減圧状態で気化するよ
うに充填している。熱吸収管に供給する冷水は、外管4
に充填された熱交換媒体Wを液化することができる温度
にしている。ここで冷水の供給は、外管4内部の温度が
常温+α以上になり、熱交換媒体Wが気化しているとき
に有効である。 (B−1)冷水供給 外部から熱吸収管に吸熱源となる冷水が供給されると、
冷水は熱交換パネルPにおける熱吸収管の流入部9aか
ら流出部9bへ、次いで他の熱交換パネルPの流入部9
aから流出部9bへと熱吸収管間を接続する接続管10
を介して供給される。冷水は、接続管10で接続したす
べての熱吸収管を循環した後、減温されて再度熱吸収管
に供給される。冷水の供給径路は、接続管10部分以外
は真直なので、吸熱ロスを最小限にして熱吸収管を循環
するようになっている。 (B−2)熱交換処理 熱吸収管に接触した熱交換媒体Wは、液化して外管4の
内壁に付着し凝集して外管4の底部に降下する。熱交換
媒体Wが気化している間、熱交換体2内部では熱交換媒
体Wの気化−液化が繰り返され、熱が熱吸収管に吸収し
続ける。
B. When the heat exchange panel P absorbs heat When the heat exchange panel P absorbs heat, the heat source supplied to the heat absorption tube (heat transfer tube 9) is cold water, and the inside of the outer tube 4 is heat exchange medium W. Water is charged so as to evaporate at normal temperature + α and reduced pressure. The cold water supplied to the heat absorbing tube is
Is set to a temperature at which the heat exchange medium W filled in can be liquefied. Here, the supply of the cold water is effective when the temperature inside the outer tube 4 becomes equal to or higher than the normal temperature + α and the heat exchange medium W is vaporized. (B-1) Cold Water Supply When cold water as a heat absorbing source is supplied to the heat absorbing tube from the outside,
The cold water flows from the inlet 9a of the heat absorbing tube in the heat exchange panel P to the outlet 9b, and then to the inlet 9 of another heat exchange panel P.
a connecting pipe 10 for connecting the heat absorbing pipes from a to the outlet 9b
Is supplied via The cold water circulates through all the heat absorption pipes connected by the connection pipes 10, is cooled down, and is supplied to the heat absorption pipes again. Since the supply path of the cold water is straight except for the connection pipe 10, the heat absorption pipe is circulated with the heat absorption loss minimized. (B-2) Heat Exchange Treatment The heat exchange medium W in contact with the heat absorption tube liquefies, adheres to the inner wall of the outer tube 4, aggregates, and descends to the bottom of the outer tube 4. While the heat exchange medium W is being vaporized, the vaporization-liquefaction of the heat exchange medium W is repeated inside the heat exchange body 2, and the heat continues to be absorbed in the heat absorption tube.

【0015】(B−3)吸熱 外管4に接触している外板1は、外板1の比熱に基づい
て吸熱する。また、外板1の接触部aが外管4の外周に
沿った面となり伝達率を向上させている。また、一般部
bに設けた凹部5は、一般部bの表面に床板が接触する
と比熱の大きい空気層を形成するので保冷性を高めるこ
とができる。更に、接触部aの表側頂部6に伝熱板7を
設けているので、外板1の表面積が拡大して熱伝達範囲
が広がり吸熱量が増加する。
(B-3) Heat Absorption The outer plate 1 in contact with the outer tube 4 absorbs heat based on the specific heat of the outer plate 1. In addition, the contact portion a of the outer plate 1 becomes a surface along the outer periphery of the outer tube 4 to improve the transmission rate. In addition, the concave portion 5 provided in the general portion b forms an air layer having a large specific heat when the floor plate comes into contact with the surface of the general portion b, so that it is possible to enhance the cooling performance. Further, since the heat transfer plate 7 is provided on the top portion 6 on the front side of the contact portion a, the surface area of the outer plate 1 is increased, the heat transfer range is widened, and the heat absorption amount is increased.

【0016】尚、上記実施の形態に係る熱交換パネルP
において、熱交換媒体Wとして水を用いたが、これに限
定されず、アルコール類等の低沸点物質も利用すること
ができる。また、上記実施の形態に係る熱交換パネルP
において、熱交換パネルPを床板用に利用しても良く、
また、熱交換体2を構成する外管4と熱伝達管9の配置
を調整すれば熱交換パネルPの配置に所定の角度を与え
ることができるので、側壁用にも利用することができ、
種々に用いて良い。このような熱交換パネルPの利用例
としては、道路融雪用パネル,屋根融雪用パネル,食物
乾燥用パネル等が挙げられる。
The heat exchange panel P according to the above embodiment
In the above, water was used as the heat exchange medium W, but the present invention is not limited to this, and low boiling substances such as alcohols can also be used. In addition, the heat exchange panel P according to the above embodiment
In, the heat exchange panel P may be used for floorboards,
Further, by adjusting the arrangement of the outer tube 4 and the heat transfer tube 9 constituting the heat exchange body 2, a predetermined angle can be given to the arrangement of the heat exchange panel P, so that the heat exchange panel P can be used for the side wall.
It may be used in various ways. Examples of use of such a heat exchange panel P include a road snow melting panel, a roof snow melting panel, and a food drying panel.

【0017】[0017]

【発明の効果】以上説明したように、本発明の熱交換パ
ネルによれば、熱交換体を、熱交換媒体を充填した断面
円形の外管及び外管内に設けられ、熱交換媒体を気化も
しくは液化させる熱伝達管を備え、熱交換体の外管を外
板に接触させたので、熱伝達管と外板とを接触した簡易
な構造で放熱面積を増大して、熱伝達性を向上すること
ができる。また、熱交換体の外管が接触する外板の接触
部を、外管の外周に沿った円弧面に形成した場合には、
単に外板面と外周とを接触するときよりも接触面積が拡
大するので、熱伝達効率を向上することができる。更
に、接触部と接触部に連続する一般部との境界に、表側
に露出する凹部を設けた場合には、凹部を保熱空間とす
ることができる。更にまた、接触部及び接触部に連続す
る一般部の板厚を略同じに形成し、かつ接触部の表側頂
部と一般部の表面とを同位に形成した場合には、外板と
被覆板とを密に接触することができるので、熱伝達効率
を向上することができる。
As described above, according to the heat exchange panel of the present invention, the heat exchanger is provided in the outer tube having a circular cross section filled with the heat exchange medium and the outer tube, and the heat exchange medium is vaporized or A heat transfer tube to be liquefied is provided, and the outer tube of the heat exchanger is brought into contact with the outer plate, so the heat transfer area is increased with a simple structure in which the heat transfer tube and the outer plate are in contact with each other to improve heat transfer. be able to. Further, when the contact portion of the outer plate with which the outer tube of the heat exchanger contacts is formed on an arc surface along the outer periphery of the outer tube,
Since the contact area is larger than when simply contacting the outer plate surface and the outer periphery, the heat transfer efficiency can be improved. Further, when a concave portion exposed on the front side is provided at the boundary between the contact portion and the general portion continuous with the contact portion, the concave portion can be used as a heat retaining space. Furthermore, when the thickness of the contact portion and the general portion continuous to the contact portion is formed substantially the same, and the top of the contact portion and the surface of the general portion are formed at the same level, the outer plate and the cover plate Can be brought into close contact, so that the heat transfer efficiency can be improved.

【0018】また、接触部の表側頂部に、伝熱板を設け
た場合には、熱伝達面積が増えるので熱伝達性を向上す
ることができる。更に、伝熱板を、接触部の表側頂部の
左右に延設した場合には、伝熱板の面積が増えるので熱
伝達性を向上することができる。更にまた、伝熱板の上
面と、一般部の表面とを面一にした場合には、外板全体
に平板を密着させることができ、平板への熱伝達性を向
上することができる。また、一般部の裏面に、熱交換体
の長手方向に平行なリブを設けた場合には、外板と断熱
材との接着性を高めることができる。更に、外板を、ア
ルミニウム製の成形品とした場合は、熱伝達性を向上し
かつ軽量化を行なうことができる。また、耐久性におい
ても優れている。
When a heat transfer plate is provided on the top of the contact portion on the front side, the heat transfer area can be increased, so that the heat transfer property can be improved. Further, when the heat transfer plate is extended to the left and right of the top portion on the front side of the contact portion, the area of the heat transfer plate increases, so that the heat transfer property can be improved. Furthermore, when the upper surface of the heat transfer plate and the surface of the general portion are flush with each other, the flat plate can be brought into close contact with the entire outer plate, and the heat transfer to the flat plate can be improved. Further, when a rib parallel to the longitudinal direction of the heat exchanger is provided on the back surface of the general portion, the adhesiveness between the outer plate and the heat insulating material can be improved. Furthermore, when the outer plate is made of an aluminum molded product, the heat transfer can be improved and the weight can be reduced. Also, it is excellent in durability.

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

【図1】本発明の実施の形態に係る熱交換パネルを示す
図であり、(a)は斜視図であり、(b)は断面図であ
る。
FIG. 1 is a diagram showing a heat exchange panel according to an embodiment of the present invention, wherein (a) is a perspective view and (b) is a cross-sectional view.

【図2】本発明の実施の形態に係る熱交換パネルの構成
要素である熱交換体の説明図である。
FIG. 2 is an explanatory diagram of a heat exchanger that is a component of the heat exchange panel according to the embodiment of the present invention.

【図3】本発明の実施の形態に係る熱交換パネルの利用
形態を示す説明図である。
FIG. 3 is an explanatory diagram showing a use form of the heat exchange panel according to the embodiment of the present invention.

【図4】従来の熱交換パネルの一例を示す斜視図であ
る。
FIG. 4 is a perspective view showing an example of a conventional heat exchange panel.

【符号の説明】[Explanation of symbols]

P 熱交換パネル W 熱交換媒体 H 被覆板 a 接触部 b 一般部 c 境界 1 外板 2 熱交換体 3 断熱材 4 外管 5 凹部 6 表側頂部 7 伝熱板 8 リブ 9 熱伝達管 10 接続管 P Heat exchange panel W Heat exchange medium H Coated plate a Contact part b General part c Boundary 1 Outer plate 2 Heat exchanger 3 Insulation material 4 Outer tube 5 Concave 6 Front side top 7 Heat transfer plate 8 Rib 9 Heat transfer tube 10 Connection tube

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) F24D 19/00 F24D 3/12 F24F 5/00 101 F28D 15/02 ──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int. Cl. 7 , DB name) F24D 19/00 F24D 3/12 F24F 5/00 101 F28D 15/02

Claims (9)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 金属製の外板と、該外板の裏側に設けら
れ外板に熱を伝達する熱交換体と、上記外板の裏側に設
けられるとともに上記熱交換体が埋設される断熱材とを
備えた熱交換パネルにおいて、 上記熱交換体を、熱交換媒体を充填した断面円形の外管
及び該外管内に設けられ該熱交換媒体を気化もしくは液
化させる熱伝達管を備えて構成し、 該熱交換体の外管を上記外板に接触させたことを特徴と
する熱交換パネル。
1. A metal outer plate, a heat exchanger provided on the back side of the outer plate for transferring heat to the outer plate, and heat insulation provided on the back side of the outer plate and embedded with the heat exchanger. A heat exchange panel comprising: an outer tube having a circular cross section filled with a heat exchange medium; and a heat transfer tube provided in the outer tube for vaporizing or liquefying the heat exchange medium. A heat exchange panel, wherein an outer tube of the heat exchanger is brought into contact with the outer plate.
【請求項2】 上記熱交換体の外管が接触する上記外板
の接触部を、該外管の外周に沿った円弧面に形成したこ
とを特徴とする請求項1記載の熱交換パネル。
2. The heat exchange panel according to claim 1, wherein a contact portion of the outer plate with which the outer tube of the heat exchanger comes into contact is formed on an arc surface along an outer periphery of the outer tube.
【請求項3】 上記接触部と該接触部に連続する一般部
との境界に、表側に露出する凹部を設けたことを特徴と
する請求項2記載の熱交換パネル。
3. The heat exchange panel according to claim 2, wherein a concave portion exposed on the front side is provided at a boundary between the contact portion and a general portion connected to the contact portion.
【請求項4】 上記接触部及び該接触部に連続する一般
部の板厚を略同じに形成し、かつ該接触部の表側頂部と
一般部の表面とを同位に形成したことを特徴とする請求
項3記載の熱交換パネル。
4. The contact portion and the general portion continuous with the contact portion are formed to have substantially the same thickness, and the top of the front side of the contact portion and the surface of the general portion are formed at the same level. The heat exchange panel according to claim 3.
【請求項5】 上記接触部の表側頂部に、伝熱板を設け
たことを特徴とする請求項3または4記載の熱交換パネ
ル。
5. The heat exchange panel according to claim 3, wherein a heat transfer plate is provided on a top portion on a front side of the contact portion.
【請求項6】 上記伝熱板を、上記接触部の表側頂部の
左右に延設したことを特徴とする請求項5記載の熱交換
パネル。
6. The heat exchange panel according to claim 5, wherein the heat transfer plate extends to the left and right of the top portion on the front side of the contact portion.
【請求項7】 上記伝熱板の上面と、上記一般部の表面
とを面一にしたことを特徴とする請求項5または6記載
の熱交換パネル。
7. The heat exchange panel according to claim 5, wherein an upper surface of the heat transfer plate is flush with a surface of the general portion.
【請求項8】 上記一般部の裏面に、上記熱交換体の長
手方向に平行なリブを設けたことを特徴とする請求項
3,4,5,6または7記載の熱交換パネル。
8. The heat exchange panel according to claim 3, wherein a rib parallel to a longitudinal direction of the heat exchanger is provided on a back surface of the general portion.
【請求項9】 上記外板を、アルミニウム製の成形品と
したことを特徴とする請求項1,2,3,4,5,6,
7または8記載の熱交換パネル。
9. The method according to claim 1, wherein said outer plate is a molded product made of aluminum.
The heat exchange panel according to 7 or 8.
JP2000160984A 2000-05-30 2000-05-30 Heat exchange panel Expired - Fee Related JP3344991B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000160984A JP3344991B2 (en) 2000-05-30 2000-05-30 Heat exchange panel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000160984A JP3344991B2 (en) 2000-05-30 2000-05-30 Heat exchange panel

Publications (2)

Publication Number Publication Date
JP2001336777A JP2001336777A (en) 2001-12-07
JP3344991B2 true JP3344991B2 (en) 2002-11-18

Family

ID=18665097

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000160984A Expired - Fee Related JP3344991B2 (en) 2000-05-30 2000-05-30 Heat exchange panel

Country Status (1)

Country Link
JP (1) JP3344991B2 (en)

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JP2015094498A (en) * 2013-11-11 2015-05-18 日本公営株式会社 Indoor temperature control system
JP2021104300A (en) * 2019-12-27 2021-07-26 颯爽工業株式会社 Body cooling and warming device

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Publication number Priority date Publication date Assignee Title
CN101836567A (en) * 2009-03-12 2010-09-22 飒爽工业株式会社 Cultivation apparatus

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