JPH0261463A - Latent-heat storage device - Google Patents
Latent-heat storage deviceInfo
- Publication number
- JPH0261463A JPH0261463A JP63208041A JP20804188A JPH0261463A JP H0261463 A JPH0261463 A JP H0261463A JP 63208041 A JP63208041 A JP 63208041A JP 20804188 A JP20804188 A JP 20804188A JP H0261463 A JPH0261463 A JP H0261463A
- Authority
- JP
- Japan
- Prior art keywords
- heat
- heat storage
- fluid
- heat transfer
- capsules
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 238000005338 heat storage Methods 0.000 title claims abstract description 68
- 239000012530 fluid Substances 0.000 claims abstract description 35
- 239000002775 capsule Substances 0.000 claims abstract description 32
- 238000012546 transfer Methods 0.000 claims abstract description 24
- 239000007788 liquid Substances 0.000 claims description 30
- 239000013529 heat transfer fluid Substances 0.000 claims description 23
- 239000011232 storage material Substances 0.000 claims description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 16
- 238000009835 boiling Methods 0.000 abstract description 4
- 239000000126 substance Substances 0.000 abstract description 4
- 239000000463 material Substances 0.000 abstract description 2
- 239000007787 solid Substances 0.000 abstract description 2
- 238000010438 heat treatment Methods 0.000 abstract 2
- 230000006641 stabilisation Effects 0.000 abstract 1
- 238000011105 stabilization Methods 0.000 abstract 1
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 238000000605 extraction Methods 0.000 description 6
- 238000004891 communication Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 3
- 230000002939 deleterious effect Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 239000000284 extract Substances 0.000 description 2
- 235000011121 sodium hydroxide Nutrition 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 239000012212 insulator Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000007096 poisonous effect Effects 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 230000008646 thermal stress Effects 0.000 description 1
- 230000001131 transforming effect Effects 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、潜熱蓄熱材を用いて蓄熱し必要に応じてその
熱を取出して利用する潜熱蓄熱器に関する。DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a latent heat storage device that stores heat using a latent heat storage material and extracts and utilizes the heat as needed.
従来技術
深夜電力や産業廃熱等の非定常的なエネルギーを熱とし
て蓄え、必要に応じて温水や蒸気としてその熱を取出す
ための蓄熱器としては、単位質量当りの蓄熱量が大きく
、熱取出し中、温度が変化しない利点があるところから
物質の融解潜熱を利用した潜熱蓄熱材を使用する潜熱蓄
熱器が有利である。Conventional technology A heat storage device that stores unsteady energy such as late-night electricity or industrial waste heat as heat and extracts that heat as hot water or steam as needed has a large amount of heat storage per unit mass and is suitable for heat extraction. Among them, a latent heat storage device using a latent heat storage material that utilizes the latent heat of fusion of a substance is advantageous because the temperature does not change.
潜熱蓄熱器の一つの方式として、潜熱蓄熱材を封入した
多数のカプセルを蓄熱槽内に設は加熱して利用する水等
の流体をカプセル間に流し、カプセル内の蓄熱材の熱を
流体に伝達するものが知られている。(先行例;′84
新テクノロジーシンポジウムPART5 最新の蓄熱
と温度・熱交換技術の開発と実例「日本の蓄熱技術の研
究開発」(日本能率協会))
しかし、この型式の蓄熱器は、カプセル壁を介して潜熱
蓄熱材と利用流体(例えば水)とが接しているので、カ
プセルに熱応力の腐食等により亀裂やピンホール等が発
生すれば、利用流体に潜熱蓄熱材が混入する。潜熱蓄熱
材として有望と目されている苛性ソーダは、毒物及び劇
物取締法の劇物に指定され(許容濃度2mg/rn’)
でいるので、潜熱蓄熱材として苛性ソーダを使用する場
合は、上記構成の潜熱蓄熱器は安全上に問題がある。One method of latent heat storage is to place a large number of capsules filled with latent heat storage material in a heat storage tank, and then heat a fluid such as water to be used between the capsules and convert the heat from the heat storage material inside the capsules into the fluid. What is communicated is known. (precedent example; '84
New Technology Symposium PART 5 Development and Examples of the Latest Heat Storage and Temperature/Heat Exchange Technology "Research and Development of Japanese Heat Storage Technology" (Japan Management Association) Since the capsule is in contact with the fluid to be used (for example, water), if cracks or pinholes occur in the capsule due to corrosion due to thermal stress, the latent heat storage material will be mixed into the fluid to be used. Caustic soda, which is considered to be a promising latent heat storage material, is designated as a deleterious substance under the Poisonous and Deleterious Substances Control Law (permissible concentration 2 mg/rn').
Therefore, when caustic soda is used as the latent heat storage material, the latent heat storage device having the above configuration poses a safety problem.
この問題を解決するため、利用流体を直接潜熱蓄熱材カ
プセルに接触させず、熱媒体流体を潜熱蓄熱材カプセル
と接触させて熱交換を行ない、熱媒体流体の流路又はス
ペース中に利用流体が内部を流れる熱交換配管を設け、
熱媒体流体を介して潜熱蓄熱材に蓄熱された熱を利用流
体に回収することが提案されている。In order to solve this problem, heat exchange is performed by bringing the heat transfer fluid into contact with the latent heat storage material capsule without directly contacting the use fluid with the latent heat storage material capsule, so that the use fluid is contained in the flow path or space of the heat transfer fluid. Install heat exchange piping that flows inside,
It has been proposed to recover heat stored in a latent heat storage material into a utilization fluid via a heat transfer fluid.
上記の熱媒体流体としては従来、この蓄熱器の達する温
度範囲で、液状を維持する特殊な流体が用いられるが、
このような液体は価格が高く、経済性の観点より極小化
を考慮する必要がある。熱の取出し過程で温度が変動し
たり、あるいは伝熱管が蓄熱槽内の上部にある場合は熱
媒体流体の量が充分でない場合は伝熱管に一様に熱媒体
流体が接触せず、熱伝達が安定して効率良く行なわれな
い欠点があった。Conventionally, the above-mentioned heat transfer fluid is a special fluid that maintains a liquid state within the temperature range reached by the heat storage device.
Such liquids are expensive, and miniaturization must be considered from an economic standpoint. If the temperature fluctuates during the heat extraction process, or if the heat transfer tubes are located at the top of the heat storage tank and the amount of heat transfer fluid is insufficient, the heat transfer tubes will not be uniformly contacted with the heat transfer fluid, resulting in poor heat transfer. However, this method has the disadvantage that it cannot be performed stably and efficiently.
発明が解゛すべき課題
本発明は、安定性を考慮し、熱媒体流体を使用して熱交
換を行なうようにした、上記構成の従来提案されている
潜熱蓄熱器の上記の欠点にがんがみ、蓄熱された熱の取
出し過程で、熱媒体流体が一定の温度を保って、伝熱管
に一様に接触して安定して効率良く熱を取出すことので
きる蓄熱器を提供することを目的とする。Problems to be Solved by the Invention The present invention solves the above-mentioned drawbacks of the conventional latent heat storage device having the above-mentioned configuration, which uses a heat transfer fluid to perform heat exchange in consideration of stability. It is an object of the present invention to provide a heat storage device that can maintain a constant temperature of the heat transfer fluid and uniformly contact the heat transfer tubes in the process of extracting the stored heat, thereby stably and efficiently extracting the heat. purpose.
課題解決のための手段
本発明は、上記の課題を解決させるため、上記構成の蓄
熱器において、加熱すべき流体が内部を貫流する伝熱管
が潜熱蓄熱材を封入したカプセルの上端よりも上方に配
置され、熱媒体流体として潜熱蓄熱材の蓄熱温度以下の
温度で蒸発する流体を用い、その液面が伝熱管よりも下
方にくるように充填されたことを特徴とする。Means for Solving the Problems In order to solve the above problems, the present invention provides a heat storage device having the above structure, in which the heat transfer tube through which the fluid to be heated flows is located above the upper end of the capsule in which the latent heat storage material is enclosed. A fluid that evaporates at a temperature below the heat storage temperature of the latent heat storage material is used as the heat transfer fluid, and the fluid is filled so that the liquid level is below the heat transfer tube.
作用
本発明の潜熱蓄熱器は上記の如く構成されているので、
利用流体が潜熱蓄熱材と熱交換壁を介して直接接するこ
となく、熱媒体流体を介して熱交換を行なうことにより
安全性が確保されていることはもとより、熱媒体流体は
、潜熱蓄熱材カプセルからの輻射熱により、又は接触に
よる熱伝達により加熱されて昇温し、蒸発し、上昇して
伝熱管に接触し、その内部の流体に熱を与えて温度の上
昇した液又は蒸気として利用に供する。一方、伝熱管内
流体に熱を与えた熱媒体流体は液化して蓄熱槽内を下方
に落下し、蓄熱材カプセルにより再度加熱され上記の作
用を繰返す。Function: Since the latent heat storage device of the present invention is constructed as described above,
Not only is safety ensured by exchanging heat through the heat transfer fluid without the fluid in direct contact with the latent heat storage material through the heat exchange wall, but the heat transfer fluid is also used in the latent heat storage material capsules. The liquid is heated by radiant heat from the tube or by heat transfer through contact, evaporates, rises, contacts the heat transfer tube, gives heat to the fluid inside, and becomes available for use as a heated liquid or vapor. . On the other hand, the heat medium fluid that has given heat to the fluid in the heat transfer tube is liquefied and falls downward in the heat storage tank, is heated again by the heat storage material capsule, and the above action is repeated.
この場合、伝熱管に接する熱媒体流体は、蒸気の状態か
ら液体に変態しながら熱を伝熱管及び内部の流体に与え
るので、その時の温度は、その流体のその圧力での気化
温度を維持する。又、蒸気となって伝熱管に接するので
、伝熱管の全表面にムラなく一様に接触する。したがっ
て、熱の取出し中、安定した熱を効率良く取出すことが
できる。In this case, the heat transfer fluid in contact with the heat transfer tube gives heat to the heat transfer tube and the internal fluid while transforming from a vapor state to a liquid, so the temperature at that time maintains the vaporization temperature of the fluid at that pressure. . In addition, since it becomes steam and comes into contact with the heat exchanger tube, it evenly and uniformly contacts the entire surface of the heat exchanger tube. Therefore, stable heat can be efficiently extracted during heat extraction.
本発明の上記以外の目的及びそれを達成するための構成
は2以下に図面を参照して詳細に述べる実施例の説明に
より明らかにされよう。Other objects of the present invention and structures for achieving them will be made clear by the detailed description of embodiments below with reference to the drawings.
実施例 第1図は本発明の実施例を示す図である。Example FIG. 1 is a diagram showing an embodiment of the present invention.
蓄熱槽1内には、潜熱蓄熱材を封入した多数の円筒状カ
プセル2が鉛直方向に平行に取付けられている。蓄熱槽
1の内部空間の上記カプセル群の上方には、加熱して温
水又は蒸気として利用する水が内部を流れる伝熱管3が
設けられている。この実施例では、伝熱管3は2段の渦
巻状に形成され夫々笠状の部材4の下面に固設されてお
り、給水管5及び温水又は蒸気取出し管6に直列又は並
列に接続されている。Inside the heat storage tank 1, a large number of cylindrical capsules 2 filled with a latent heat storage material are installed in parallel in the vertical direction. Above the group of capsules in the internal space of the heat storage tank 1, there are provided heat transfer tubes 3 through which water to be heated and used as hot water or steam flows. In this embodiment, the heat transfer tubes 3 are formed in a two-stage spiral shape, each fixed to the lower surface of a shade-shaped member 4, and connected in series or parallel to a water supply pipe 5 and a hot water or steam extraction pipe 6. There is.
蓄熱槽の外面は断熱后7で囲繞されている。蓄熱槽内空
間の下部には熱媒体流体8が充填されている。熱媒体流
体8としては、蓄熱温度以下で蒸発し、蓄熱器の達する
最低温度でも固層とならない流体が採用され、水を利用
することも可能である。The outer surface of the heat storage tank is surrounded by a heat insulator 7. A heat medium fluid 8 is filled in the lower part of the space inside the heat storage tank. As the heat medium fluid 8, a fluid that evaporates below the heat storage temperature and does not become a solid layer even at the lowest temperature reached by the heat storage device is used, and it is also possible to use water.
なお、蓄熱槽1の頂部には安全弁9が設けられている
この実施例では、熱媒体流体8、例えば水はその液面が
カプセル2の下端よりも下になる程度に充填されている
。In this embodiment, in which a safety valve 9 is provided at the top of the heat storage tank 1, the heat medium fluid 8, for example water, is filled to such an extent that its liquid level is below the lower end of the capsule 2.
したがって、熱媒体流体8はカプセル2からの輻射熱に
よって加熱されて昇温し、沸点に達すれば蒸発して蒸気
になりカプセル2の間隙を上昇し。Therefore, the heat transfer fluid 8 is heated by the radiant heat from the capsule 2 and rises in temperature, and when it reaches its boiling point, it evaporates into steam and rises through the gap in the capsule 2.
カプセル2の表面に接触する。ことにより加熱されて過
熱蒸気になりカプセルの間を抜けて伝熱管3に接触しそ
の内部の水と熱交換を行なう。Contact the surface of capsule 2. As a result, it is heated and becomes superheated steam, which passes through the space between the capsules and comes into contact with the heat transfer tube 3, where it exchanges heat with the water inside.
この実施例では、熱媒体流体は過熱蒸気の状態で伝熱管
に接触するので、どの部分も確実に沸点以上の温度とな
っており、熱交換によりすぐに所定の沸点温度となり、
この温度で継続的に熱交換が行なわれる。熱を失なって
液化した熱媒体流体は傘4の下面に沿って周囲に移動し
、下方に落下し再び気化して上昇し、熱の搬送を行なう
。In this example, since the heat transfer fluid contacts the heat transfer tube in the state of superheated steam, the temperature at all parts is definitely above the boiling point, and the temperature quickly reaches the predetermined boiling point through heat exchange.
Continuous heat exchange takes place at this temperature. The heat transfer fluid that has lost heat and liquefied moves to the surroundings along the lower surface of the umbrella 4, falls downward, vaporizes again, rises, and transfers heat.
又、この実施例では、熱媒体流体の液体はカプセルに接
していないため、外部放熱ロスが減る利点もある。Further, in this embodiment, since the heat medium fluid is not in contact with the capsule, there is an advantage that external heat radiation loss is reduced.
第2図に示す他の実施例に示す如く、熱媒体流体8をそ
の液体がカプセル2の一部又は全部が浸る高さにくるよ
うに充填した場合は、カプセルの液に浸る深さを変える
ことによりカプセル2から熱媒体流体8への伝熱量を変
えて蒸気発生量を変えることができるので、伝熱管3で
取出す熱量に応じて、熱媒体流体の液面の高さを、蒸気
発生量が熱取出し量と平衡するように調整することがで
きる。As shown in another embodiment shown in FIG. 2, when the heat transfer fluid 8 is filled to a level where part or all of the capsule 2 is immersed, the depth at which the capsule is immersed in the liquid is changed. By changing the amount of heat transferred from the capsule 2 to the heat transfer fluid 8, the amount of steam generated can be changed. can be adjusted so that it is in equilibrium with the amount of heat extraction.
第3図に示すさらに他の実施例では、蓄熱槽1と別に液
体槽10を設け、蓄熱槽1と夫々の下部で連通管11に
より連通させ、熱媒体流体8が連通管11を通って両槽
間を往来できるようになっている。In still another embodiment shown in FIG. 3, a liquid tank 10 is provided separately from the heat storage tank 1, and is communicated with the heat storage tank 1 through a communication pipe 11 at the lower part of each tank, so that the heat medium fluid 8 passes through the communication pipe 11 and is connected to both the heat storage tank 1 and the heat storage tank 1. It is possible to go back and forth between the tanks.
液体槽10の頂部には空気抜き12が設けられている。An air vent 12 is provided at the top of the liquid tank 10.
したがって、蓄熱槽1内の熱媒体流体8が加熱されて昇
温し気化して蒸気量が増加すると、蒸気で液面が押し下
げられ、当初実線の位置にあったものが破線で示す位置
に下り、液は液体槽1o内に移動する。Therefore, when the heat transfer fluid 8 in the heat storage tank 1 is heated, the temperature rises, and the amount of steam increases, the steam pushes down the liquid level, and the liquid level, which was initially at the solid line, drops to the position shown by the broken line. , the liquid moves into the liquid tank 1o.
したがって、カプセル2に接触する液体の接触面積が減
少し、液の蒸発量が低下する。この蒸発量と伝熱管内の
水に熱に与え液体になる量とが均衡した所に液面は維持
され、この状態で熱交換が行なわれる。Therefore, the contact area of the liquid that contacts the capsule 2 is reduced, and the amount of liquid evaporated is reduced. The liquid level is maintained at a balance between the amount of evaporation and the amount of heat applied to the water in the heat transfer tube to turn it into a liquid, and heat exchange is performed in this state.
なお、この実施例で連通管11にポンプを介装すれば、
蓄熱槽内の液位を任意に調整することが可能となるので
取出し管6の取出し量及び取出し温水の温度に応じて蓄
熱槽1内の熱媒体流体の液位を調整することができる。In addition, if a pump is interposed in the communication pipe 11 in this embodiment,
Since the liquid level in the heat storage tank can be arbitrarily adjusted, the liquid level of the heat medium fluid in the heat storage tank 1 can be adjusted according to the amount taken out from the takeout pipe 6 and the temperature of the hot water taken out.
なお、液体槽は蓄熱槽と壁で仕切って一体に設けてもよ
い。Note that the liquid tank may be separated from the heat storage tank by a wall and provided integrally.
効 果
以上の如く、本発明によれば利用流体は潜熱蓄熱材と熱
媒体を介して熱交換を行なうので安全性が高く、伝熱管
に接する熱媒体流体の温度を一定に維持し、かつ均一に
接触させることができ安定して熱交換効率高く蓄熱され
た熱を取出すことができる。Effects As described above, according to the present invention, the fluid used exchanges heat via the latent heat storage material and the heat medium, so it is highly safe, and the temperature of the heat medium fluid in contact with the heat transfer tubes is maintained constant and uniform. The heat can be brought into contact with the heat exchanger and the stored heat can be extracted stably and with high heat exchange efficiency.
熱媒体流体の液面をカプセルの下端よりも下位にするこ
とにより、所定の蒸発温度を確実に得ることができる。By setting the liquid level of the heat transfer fluid below the lower end of the capsule, a predetermined evaporation temperature can be reliably obtained.
熱媒体流体の液面を変化させることにより熱取出し量と
蒸気発生量とを均衡させることができる。又、蓄熱槽と
連通させて液体槽を設けることにより、取出し熱量に応
じて自動的に蒸気発生量を変えることができ、又蓄熱槽
と液体槽との間にポンプを介在させることにより、取出
し熱量を変えることができる。By changing the liquid level of the heat transfer fluid, the amount of heat extracted and the amount of steam generated can be balanced. In addition, by providing a liquid tank in communication with the heat storage tank, the amount of steam generated can be automatically changed according to the amount of heat extracted, and by interposing a pump between the heat storage tank and the liquid tank, the amount of steam generated can be changed automatically according to the amount of heat extracted. You can change the amount of heat.
第1図は本発明の実施例を示す断面図、第2図は本発明
の他の実施例を示す断面図、第3図は本発明の更に他の
実施例を示す断面図である。
1・・・蓄熱槽
2・・・菩熱材カプセル
3・・・伝熱管
5・・・給水管
6・・・温水又は蒸気取出し管
8・・・熱媒体流体
10・・・液体槽
(ほか1名)
第
図FIG. 1 is a sectional view showing an embodiment of the invention, FIG. 2 is a sectional view showing another embodiment of the invention, and FIG. 3 is a sectional view showing still another embodiment of the invention. 1... Heat storage tank 2... Heat material capsule 3... Heat transfer tube 5... Water supply pipe 6... Hot water or steam extraction pipe 8... Heat medium fluid 10... Liquid tank (etc. 1 person) Figure
Claims (5)
する流体が内部を貫流する伝熱管とが蓄熱槽内に設けら
れ、カプセル内の潜熱蓄熱材の蓄熱する熱を伝熱管内の
流体に伝達する熱媒体流体が蓄熱槽内に充填された潜熱
蓄熱器において、上記の伝熱管はカプセルの上端よりも
上方に配置され、上記の熱媒体流体は上記の潜熱蓄熱材
の蓄熱温度以下の温度で蒸発する流体であり、その液面
が上記伝熱管よりも下方にくるように充填されたことを
特徴とする潜熱蓄熱器。(1) A capsule enclosing a latent heat storage material and a heat transfer tube through which a fluid to be heated and used flows through are provided in a heat storage tank, and the heat stored in the latent heat storage material in the capsule is transferred to the fluid in the heat transfer tube. In a latent heat storage device in which a heat storage tank is filled with a heat transfer fluid that transfers to A latent heat storage device characterized in that it is a fluid that evaporates at a certain temperature and is filled so that its liquid level is below the heat transfer tube.
りも下方にくる如く充填されたことを特徴とする請求項
1に記載の潜熱蓄熱器。(2) The latent heat storage device according to claim 1, wherein the heat transfer fluid is filled so that its liquid level is below the capsule.
全部がこれに浸るように充填されたことを特徴とする請
求項1に記載の潜熱蓄熱器。(3) The latent heat storage device according to claim 1, wherein the heat transfer fluid is filled so that part or all of the capsule is immersed therein.
有する液体槽を設けたことを特徴とする請求項1に記載
の潜熱蓄熱器。(4) The latent heat storage device according to claim 1, further comprising a liquid tank communicating with the heat storage tank at a lower part thereof and having an air vent.
装したことを特徴とする請求項4に記載の潜熱蓄熱器。(5) The latent heat storage device according to claim 4, characterized in that a pump is interposed between the heat storage tank and the liquid tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63208041A JPH0261463A (en) | 1988-08-24 | 1988-08-24 | Latent-heat storage device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63208041A JPH0261463A (en) | 1988-08-24 | 1988-08-24 | Latent-heat storage device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0261463A true JPH0261463A (en) | 1990-03-01 |
Family
ID=16549668
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63208041A Pending JPH0261463A (en) | 1988-08-24 | 1988-08-24 | Latent-heat storage device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0261463A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102297515A (en) * | 2011-07-07 | 2011-12-28 | 王文生 | Electromagnetic-induction heating high-temperature fused salt heat carrier furnace |
CN104697170A (en) * | 2015-03-25 | 2015-06-10 | 广州迪森热能技术股份有限公司 | Biomass double square coil pipe heat conduction oil furnace |
-
1988
- 1988-08-24 JP JP63208041A patent/JPH0261463A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102297515A (en) * | 2011-07-07 | 2011-12-28 | 王文生 | Electromagnetic-induction heating high-temperature fused salt heat carrier furnace |
CN104697170A (en) * | 2015-03-25 | 2015-06-10 | 广州迪森热能技术股份有限公司 | Biomass double square coil pipe heat conduction oil furnace |
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