JPH0229960B2 - - Google Patents
Info
- Publication number
- JPH0229960B2 JPH0229960B2 JP57045317A JP4531782A JPH0229960B2 JP H0229960 B2 JPH0229960 B2 JP H0229960B2 JP 57045317 A JP57045317 A JP 57045317A JP 4531782 A JP4531782 A JP 4531782A JP H0229960 B2 JPH0229960 B2 JP H0229960B2
- Authority
- JP
- Japan
- Prior art keywords
- heat
- storage material
- heat storage
- pipe
- source
- 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 - Lifetime
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D15/00—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies
- F28D15/02—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D20/00—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00
- F28D20/02—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using latent heat
- F28D20/021—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using latent heat the latent heat storage material and the heat-exchanging means being enclosed in one container
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/14—Thermal energy storage
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Central Heating Systems (AREA)
Description
【発明の詳細な説明】
この発明は熱交換器に関し、特にヒートパイプ
と固相−液相の相変化をする蓄熱材とを具備した
熱交換器に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a heat exchanger, and more particularly to a heat exchanger equipped with a heat pipe and a heat storage material that undergoes a phase change between solid and liquid phases.
ヒートパイプはその内部に密封した作動液体の
蒸発潜熱として熱輸送を行なうものであつて、熱
伝導率の最も高い金属である銅に較べて、数十倍
ないし数百十倍の熱伝導率を有していることは、
周知のとおりであり、従来ではその優れた特性を
生かしてヒートパイプを熱交換器等の種々の機器
に採用している。 Heat pipes transport heat as the latent heat of vaporization of the working liquid sealed inside, and have thermal conductivity that is tens to hundreds of times higher than that of copper, the metal with the highest thermal conductivity. What you have is
As is well known, heat pipes have conventionally been used in various devices such as heat exchangers by taking advantage of their excellent properties.
ところで、通常のヒートパイプでは、その両端
部の間で温度差があれば熱輸送が自然に生じるか
ら、例えばいずれかの部材もしくは部分を冷却す
る場合、熱を運び去る吸熱源の温度が何らかの原
因で上昇すると、冷却すべき部材もしくは部分を
冷却し得なくなるか、もしくは逆に加熱してしま
うことになる。また、いずれかの部材もしくは部
分を加熱する場合にも上記の事情は同様であつ
て、熱源の温度が何らかの原因で降下すると加熱
すべき部材もしくは部分を加熱し得ないか、もし
くは逆に冷却することになつてしまう。そこで従
来では、上記のような不都合を解消するために、
蓄熱材を用い、吸熱源の温度が上昇した場合に蓄
熱材を吸熱源として作用させ、あるいは加熱源の
温度が降下した場合に蓄熱材を熱源として作用さ
せるよう構成した熱交換器が提案されている。 By the way, in a normal heat pipe, if there is a temperature difference between the two ends, heat transport will naturally occur, so for example, when cooling any member or part, the temperature of the heat absorbing source that carries away the heat may be caused by some reason. If the temperature rises, the component or part to be cooled will not be able to be cooled or, on the contrary, will be heated. Furthermore, the above situation is the same when heating any member or part; if the temperature of the heat source drops for some reason, the member or part that should be heated cannot be heated, or conversely, it cools down. It becomes a thing. Therefore, in order to solve the above-mentioned inconvenience, conventionally,
A heat exchanger has been proposed that uses a heat storage material and is configured so that the heat storage material acts as a heat absorption source when the temperature of the heat absorption source increases, or the heat storage material acts as a heat source when the temperature of the heating source decreases. There is.
この種の熱交換器において用いる蓄熱材として
は、水等熱容量を利用したものや固相−液相の相
変化の際の蓄熱を利用したもの、あるいは蒸発潜
熱を利用したものが考えられるが、熱容量を利用
した蓄熱材では蓄熱容量が小さすぎる問題があ
り、また蒸発潜熱を利用した蓄熱材では蒸発の際
の体積変化が大きくなりすぎる問題があり、結局
固相−液相の相変化の際の潜熱を利用した蓄熱材
が好ましいと考えられる。 The heat storage materials used in this type of heat exchanger include those that utilize heat capacity such as water, those that utilize heat storage during phase change between solid and liquid phases, or those that utilize latent heat of vaporization. Heat storage materials that utilize heat capacity have the problem that their heat storage capacity is too small, and heat storage materials that utilize latent heat of vaporization have the problem that the volume change during evaporation is too large, and as a result, during the solid-liquid phase change, It is considered preferable to use a heat storage material that utilizes the latent heat of .
従来、このような固相−液相の相変化の際の潜
熱を利用した常温用蓄熱材として、塩化カルシウ
ム・6水和物(CaCl2・6H2O、融点=29.92℃、
潜熱=45Kcal/Kg)、チオ硫酸ナトリウム・5水
和物(Na2S2O3・5H2O、融点=48.2℃)あるい
はオクタデカン(C18H38、融点=28℃、潜熱=
58.2Kcal/Kg)等が知られている。これらの蓄熱
材は、相変化が完了するまで全体的に温度が一定
に保たれることが理想的な挙動であるが、実際に
は部分的な過冷却状態が現れ、当初想定した温度
状態を得られないばかりか、蓄熱材の全量を有効
に利用し得ない場合があつた。 Conventionally, calcium chloride hexahydrate (CaCl 2 6H 2 O, melting point = 29.92℃,
latent heat = 45Kcal/Kg), sodium thiosulfate pentahydrate (Na 2 S 2 O 3 5H 2 O, melting point = 48.2°C) or octadecane (C 18 H 38 , melting point = 28°C, latent heat =
58.2Kcal/Kg) etc. are known. The ideal behavior of these heat storage materials is for the temperature to remain constant throughout until the phase change is completed, but in reality, a partial supercooled state appears and the temperature state initially assumed is not reached. Not only was the heat storage material not obtained, but there were also cases where the entire amount of heat storage material could not be used effectively.
この発明は上記の事情に鑑みてなされたもの
で、固相−液相の相変化の際の潜熱を利用する蓄
熱材の挙動を可及的に理想状態に近づけ、その有
効利用を図ることのできる蓄熱式熱交換器を提供
することを目的とするものである。 This invention was made in view of the above circumstances, and aims to bring the behavior of a heat storage material that utilizes latent heat during a solid-liquid phase change as close to the ideal state as possible, and to utilize it effectively. The purpose of this invention is to provide a regenerative heat exchanger that can
以下この発明の実施例を添付の図面を参照して
説明する。 Embodiments of the present invention will be described below with reference to the accompanying drawings.
この発明の熱交換器の一実施例を第1図および
第2図を参照して説明すると、これらの図中符号
1はヒートパイプを示し、このヒートパイプ1は
通常のヒートパイプと同様にその内周面にウイツ
ク2が添設されるとともに、適宜の作動流体が封
入されている。そのヒートパイプ1の一端外周所
定個所に一定長さに亙つて、その端部を包囲する
ように同心状に密閉容器3が設けられ、その密閉
容器3の内部に、固相−液相の相変化をする蓄熱
材4が封入され、したがつてその蓄熱材4は前記
ヒートパイプ1の一端部外周面に所定長さに亙つ
て密着している。さらに、前記密閉容器3の外周
に金属製のカバー5が同心状に設けられ、その内
周面と密閉容器3の外周面とに、金鋼等からなる
ウイツク6が設けられるとともに、カバー5と密
閉容器3とによつて形成された空間内に、適宜の
作動流体が封入されてなるヒートパイプ7が形成
されている。 One embodiment of the heat exchanger of the present invention will be described with reference to FIGS. 1 and 2. In these figures, reference numeral 1 indicates a heat pipe, and this heat pipe 1 is similar to a normal heat pipe. A wick 2 is attached to the inner peripheral surface, and an appropriate working fluid is sealed therein. A sealed container 3 is provided concentrically at a predetermined location on the outer periphery of one end of the heat pipe 1 over a certain length so as to surround the end. A variable heat storage material 4 is enclosed, and therefore the heat storage material 4 is in close contact with the outer peripheral surface of one end of the heat pipe 1 over a predetermined length. Further, a metal cover 5 is provided concentrically around the outer circumference of the sealed container 3, and a wick 6 made of metal or the like is provided on the inner peripheral surface of the cover 5 and the outer peripheral surface of the sealed container 3. A heat pipe 7 is formed in a space formed by the closed container 3 and is filled with an appropriate working fluid.
以上のように構成した熱交換器において、ヒー
トパイプ1の他端部(第1図では下端部)を加熱
源Hに配置するとともに、前記第2のヒートパイ
プ7を吸熱源Cに配置し、さらに蓄熱材4として
融点が前記加熱源Hの温度よりも若干低い物質を
選べば、ヒートパイプ1の他端部に加熱源Hから
与えられた熱は、ヒートパイプ1内の作動流体に
よつてその潜熱として一端部側に運ばれ、その熱
によつて蓄熱材4が融解し、その際の潜熱として
熱を蓄える。蓄熱材4に与えられた熱の一部は、
その外周に設けたヒートパイプ7によつて吸熱源
Cに運ばれるが、蓄熱材4にはヒートパイプ1に
よつて常時加熱源Hから熱が与えられるから、結
局現象的には加熱源Hの有する熱が各ヒートパイ
プ1,7および蓄熱材4を介して吸熱源Cに伝達
される状態になる。 In the heat exchanger configured as above, the other end of the heat pipe 1 (lower end in FIG. 1) is placed at the heat source H, and the second heat pipe 7 is placed at the heat absorption source C, Furthermore, if a material whose melting point is slightly lower than the temperature of the heating source H is selected as the heat storage material 4, the heat given from the heating source H to the other end of the heat pipe 1 is transferred by the working fluid inside the heat pipe 1. The latent heat is carried to the one end side, the heat storage material 4 is melted by the heat, and the heat is stored as the latent heat at that time. A part of the heat given to the heat storage material 4 is
The heat is carried to the heat absorption source C by the heat pipe 7 provided on the outer periphery of the heat storage material 4, but since heat is always given to the heat storage material 4 from the heat source H by the heat pipe 1, the phenomenon is that the heat source H The heat is transferred to the heat absorption source C via the heat pipes 1 and 7 and the heat storage material 4.
そして上記の熱交換器において、加熱源Hの温
度が蓄熱材4の融点の温度程度まで降下すると、
ヒートパイプ1における両端部間の温度差がなく
なるので、ヒートパイプ1における熱輸送が生じ
なくなるが、蓄熱材4はヒートパイプ7の働きに
よつて温度の均一化が促進され、更に蓄熱材4と
吸熱源Cとの間には温度差があるので、蓄熱材4
と吸熱源Cとの間でヒートパイプ7を介して熱受
授が生じ、その結果蓄熱材4は次第に放熱して凝
固する。その場合においても、蓄熱材4はヒート
パイプ7に広い面積で接触しているので、過冷却
状態が生じることなく、全体的に均一凝固する。
またヒートパイプはその特性上均温化するから蓄
熱材4の外周側の表面積がヒートパイプ7によつ
て実質的に拡大され、そのため熱交換特性が向上
する。 In the above heat exchanger, when the temperature of the heating source H falls to about the melting point of the heat storage material 4,
Since there is no temperature difference between the two ends of the heat pipe 1, no heat transport occurs in the heat pipe 1, but the temperature of the heat storage material 4 is promoted to be uniform due to the action of the heat pipe 7, and the temperature difference between the heat storage material 4 and the heat pipe 7 is promoted. Since there is a temperature difference between the heat absorbing source C and the heat storage material 4,
Heat exchange occurs between the heat absorbing source C and the heat pipe 7, and as a result, the heat storage material 4 gradually radiates heat and solidifies. Even in this case, since the heat storage material 4 is in contact with the heat pipe 7 over a wide area, a supercooled state does not occur, and uniform solidification occurs throughout.
Further, since the heat pipe has a uniform temperature due to its characteristics, the surface area of the outer peripheral side of the heat storage material 4 is substantially expanded by the heat pipe 7, thereby improving the heat exchange characteristics.
したがつて上記の熱交換器では、加熱源Hの温
度が降下しても、蓄熱材4がほぼ完全に凝固する
までの間は、吸熱源Cに対して熱を与えることが
でき、またその場合の蓄熱材4から吸熱源Cに対
する伝熱時間は、蓄熱材4の種類を適宜選定し、
またその量を多くすることにより、長くすること
ができる。 Therefore, in the above heat exchanger, even if the temperature of the heating source H falls, until the heat storage material 4 is almost completely solidified, heat can be given to the heat absorbing source C, and the The heat transfer time from the heat storage material 4 to the heat absorption source C in this case is determined by selecting the type of the heat storage material 4 as appropriate,
Moreover, by increasing the amount, the length can be increased.
なお、上記の熱交換器では、各ヒートパイプ
1,7の間に蓄熱材4を介在させた構造であるか
ら、上述した場合とは逆に、蓄熱材4を設けた端
部側を加熱源とし、それとは反対の端部側を吸熱
源としても、前述したと同様に作用させることが
できる。 In addition, since the above heat exchanger has a structure in which the heat storage material 4 is interposed between the heat pipes 1 and 7, contrary to the above case, the end side where the heat storage material 4 is provided is connected to the heat source. Even if the opposite end side is used as a heat absorption source, the same effect as described above can be obtained.
第3図はこの発明の熱交換器の他の実施例を示
すもので、この図では蓄熱材4の外周側のヒート
パイプが省略されており、この熱交換器は、蓄熱
材4内に埋没するようにヒートパイプ1の一端部
にフイン8を設けたものである。このような構成
では、ヒートパイプ1と蓄熱材4との間の伝熱面
積が更に広くなるから、蓄熱材4を局部的な過熱
や過冷却を生じさせることなく有効に利用するこ
とができる。 FIG. 3 shows another embodiment of the heat exchanger of the present invention. In this figure, the heat pipe on the outer peripheral side of the heat storage material 4 is omitted, and this heat exchanger is buried in the heat storage material 4. A fin 8 is provided at one end of the heat pipe 1 so as to do so. In such a configuration, the heat transfer area between the heat pipe 1 and the heat storage material 4 becomes wider, so that the heat storage material 4 can be used effectively without causing local overheating or supercooling.
以上説明したようにこの発明によれば、ヒート
パイプの外周所定個所に同心状に密着配置した蓄
熱材の外周に、更に他のヒートパイプを同心状に
密着させて設けたので、蓄熱材に対する入熱およ
び放熱の面積が広くなつて蓄熱材の局部的な過熱
状態や過冷却状態を防止でき、したがつて蓄熱材
が理想状態に近い挙動を示すことによりその有効
利用を図り、また当初想定した作用をさせること
ができるなどの効果が得られる。 As explained above, according to the present invention, another heat pipe is provided concentrically and closely on the outer periphery of the heat storage material which is concentrically arranged in close contact with a predetermined location on the outer periphery of the heat pipe. The area for heat and heat dissipation is expanded, preventing local overheating and overcooling of the heat storage material, which allows the heat storage material to behave close to the ideal state, allowing for effective use of the material, and improving the effectiveness of the heat storage material as expected. It is possible to obtain effects such as being able to act.
第1図は本発明の実施例を示す断面図、第2図
は第1図の−線矢視図、第3図は他の実施例
の断面図である。
1:ヒートパイプ、3:密閉容器、4:蓄熱
材、7:ヒートパイプ。
FIG. 1 is a sectional view showing an embodiment of the present invention, FIG. 2 is a view taken along the - line in FIG. 1, and FIG. 3 is a sectional view of another embodiment. 1: heat pipe, 3: airtight container, 4: heat storage material, 7: heat pipe.
Claims (1)
た密閉容器を、ヒートパイプの外周所定個所に一
定長さに亙つて同心状に密着配置し、さらにその
密閉容器の外周側にヒートパイプを同心状に密着
させて配置し、かつその蓄熱材に蓄えられた熱を
所定の吸熱源に取出すよう構成したことを特徴と
する蓄熱式熱交換器。1. A sealed container filled with a heat storage material that undergoes a phase change between solid and liquid phases is placed concentrically and tightly at a predetermined location on the outer periphery of a heat pipe, and heat is applied to the outer periphery of the sealed container. A regenerative heat exchanger characterized in that pipes are arranged concentrically in close contact with each other and the heat stored in the heat storage material is extracted to a predetermined heat absorption source.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57045317A JPS58164993A (en) | 1982-03-19 | 1982-03-19 | Accumulation type heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57045317A JPS58164993A (en) | 1982-03-19 | 1982-03-19 | Accumulation type heat exchanger |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62011284A Division JPS62294897A (en) | 1987-01-22 | 1987-01-22 | Heat accumulation type heat exchanger |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58164993A JPS58164993A (en) | 1983-09-29 |
| JPH0229960B2 true JPH0229960B2 (en) | 1990-07-03 |
Family
ID=12715920
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57045317A Granted JPS58164993A (en) | 1982-03-19 | 1982-03-19 | Accumulation type heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58164993A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH04343929A (en) * | 1991-05-20 | 1992-11-30 | Kadouchi Seisakusho:Kk | Unit bath and unit bath installation method |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2772072B2 (en) * | 1989-11-14 | 1998-07-02 | 株式会社フジクラ | Heat pipe equipment |
| CN102538533A (en) * | 2012-02-28 | 2012-07-04 | 湖南省汇通热源技术有限责任公司 | Phase change heat storage element and heat storage and supply device adopting same |
| JP6004766B2 (en) * | 2012-06-13 | 2016-10-12 | 古河電気工業株式会社 | Heat storage device |
| CN103185367A (en) * | 2013-03-15 | 2013-07-03 | 青岛奥环新能源科技发展有限公司 | Heat pipe-type movable heating phase-change heat storage device |
| CN108917446B (en) * | 2018-07-03 | 2020-10-09 | 北京交通大学 | Phase-change heat storage capsule and phase-change heat storage device with heat pipe assisting in strengthening heat exchange |
| CN109340876B (en) * | 2018-11-20 | 2024-03-26 | 赵春雷 | Dual-phase electromagnet heat storage device and use method thereof |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5847640B2 (en) * | 1977-02-03 | 1983-10-24 | 大阪瓦斯株式会社 | Regenerative heat exchange device |
| JPS5440560U (en) * | 1977-08-26 | 1979-03-17 | ||
| JPS5575184A (en) * | 1978-11-30 | 1980-06-06 | Mitsui Eng & Shipbuild Co Ltd | Heat accumulator |
| JPS5953480B2 (en) * | 1980-07-24 | 1984-12-25 | 工業技術院長 | Capsule type heat storage device |
-
1982
- 1982-03-19 JP JP57045317A patent/JPS58164993A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH04343929A (en) * | 1991-05-20 | 1992-11-30 | Kadouchi Seisakusho:Kk | Unit bath and unit bath installation method |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58164993A (en) | 1983-09-29 |
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