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JP5009833B2 - Heat storage device - Google Patents
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JP5009833B2 - Heat storage device - Google Patents

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JP5009833B2
JP5009833B2 JP2008042900A JP2008042900A JP5009833B2 JP 5009833 B2 JP5009833 B2 JP 5009833B2 JP 2008042900 A JP2008042900 A JP 2008042900A JP 2008042900 A JP2008042900 A JP 2008042900A JP 5009833 B2 JP5009833 B2 JP 5009833B2
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heat storage
heat
storage material
transfer oil
latent
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JP2009198138A (en
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博臣 釜野
由季子 藤田
篤 河合
良勝 大地
徹治 定塚
武志 千田
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Sanki Engineering Co Ltd
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    • YGENERAL 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
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    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/14Thermal energy storage

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Description

この発明は、発電所や廃棄物焼却場などの熱源施設で発生する廃熱を蓄熱する蓄熱装置に関する。   The present invention relates to a heat storage device that stores waste heat generated in a heat source facility such as a power plant or a waste incineration plant.

熱源施設(例えば、発電所や廃棄物焼却場、製鉄所、化学プラント)で生じる廃熱を、熱利用施設(例えば、オフィスビルや病院、ホテル、クアハウス)で有効利用するため、熱源施設の廃熱を蓄熱タンク内に蓄熱し、その蓄熱タンクを熱利用施設に運搬し、その蓄熱タンクを熱源として給湯や暖房等を行なうことを可能とした蓄熱装置が知られている(特許文献1)。   Waste heat generated in heat source facilities (for example, power plants, waste incinerators, steelworks, chemical plants) is effectively discarded in heat utilization facilities (for example, office buildings, hospitals, hotels, and Kurhaus). There is known a heat storage device that stores heat in a heat storage tank, transports the heat storage tank to a heat utilization facility, and performs hot water supply, heating, or the like using the heat storage tank as a heat source (Patent Document 1).

この蓄熱装置は、潜熱蓄熱材と熱媒油とを上下二層に分離した状態で収容する蓄熱タンクと、その蓄熱タンク内の潜熱蓄熱材層中に熱媒油を供給する供給管と、前記蓄熱タンク内の熱媒油層から熱媒油を回収する回収管とを有し、その供給管と回収管を通じて、熱源施設(または熱利用施設)と蓄熱タンクの間で熱媒油を循環させて使用する。このとき、供給管から潜熱蓄熱材層中に供給された熱媒油は、熱媒油と潜熱蓄熱材の比重差により潜熱蓄熱材層中を上昇しながら、潜熱蓄熱材と直接接触して熱交換を行なう。   The heat storage device includes a heat storage tank that stores the latent heat storage material and the heat transfer oil in a state separated into upper and lower layers, a supply pipe that supplies the heat transfer oil into the latent heat storage material layer in the heat storage tank, and A recovery pipe for recovering the heat transfer oil from the heat transfer oil layer in the heat storage tank, and circulating the heat transfer oil between the heat source facility (or heat utilization facility) and the heat storage tank through the supply pipe and the recovery pipe use. At this time, the heat transfer oil supplied from the supply pipe into the latent heat storage material layer is heated in direct contact with the latent heat storage material while rising in the latent heat storage material layer due to the specific gravity difference between the heat transfer oil and the latent heat storage material. Exchange.

ここで、潜熱蓄熱材は、物質が固相と液相の間で相変化するときに吸収・排出する熱(潜熱)を利用して蓄熱と放熱を行なう蓄熱材であり、固相から液相に相変化するときに周りから熱を吸収し、液相から固相に相変化するときに放熱する。また、潜熱蓄熱材は、固相と液相の間で相変化するときに温度が変化しないので、一定した温度での放熱が可能である。このような潜熱蓄熱材として、例えば、酢酸ナトリウム三水和物や、塩化マグネシウム六水和物、エリスリトール、マンニトールが用いられる。   Here, the latent heat storage material is a heat storage material that stores and releases heat using heat (latent heat) that is absorbed and exhausted when a substance undergoes a phase change between a solid phase and a liquid phase. When the phase changes, the heat is absorbed from the surroundings, and when the phase changes from the liquid phase to the solid phase, the heat is dissipated. Moreover, since the temperature of the latent heat storage material does not change when the phase changes between the solid phase and the liquid phase, it is possible to radiate heat at a constant temperature. As such a latent heat storage material, for example, sodium acetate trihydrate, magnesium chloride hexahydrate, erythritol, and mannitol are used.

また、蓄熱タンクの形状としては、例えば、中心軸が略水平の筒状であり、かつ、その中心軸に直交する断面が円形、楕円形、または下部が窄まる多角形のものが挙げられる。
特開2007−132569号公報
Examples of the shape of the heat storage tank include a cylindrical shape whose central axis is substantially horizontal and whose cross section perpendicular to the central axis is circular, elliptical, or polygonal whose bottom is narrowed.
JP 2007-13269 A

ところで、上記の蓄熱装置に蓄熱する場合、図5に示すように、蓄熱タンク31内の潜熱蓄熱材層32には、供給管33から供給された熱媒油の通過する領域34と通過しない領域35とが生じ、熱媒油の通過する領域34にある固相の潜熱蓄熱材36は、熱媒油と直接接触して熱を受け取るので、短時間で融けるが、熱媒油の通過しない領域35にある固相の潜熱蓄熱材37は、熱媒油の通過する領域34にある液相の潜熱蓄熱材38を介して熱を受け取るので、なかなか融けない。そのため、潜熱蓄熱材37がすべて融けるまで長時間を要し、熱媒油の通過しない領域35にある潜熱蓄熱材を無駄なく利用するのが難しかった。   By the way, when storing heat in said heat storage apparatus, as shown in FIG. 5, in the latent heat storage material layer 32 in the heat storage tank 31, the area | region 34 where the heat transfer oil supplied from the supply pipe | tube 33 passes, and the area | region which does not pass 35, and the solid phase latent heat storage material 36 in the region 34 through which the heat transfer oil passes is in direct contact with the heat transfer oil and receives heat, so it melts in a short time, but the region through which the heat transfer oil does not pass Since the solid phase latent heat storage material 37 in 35 receives heat via the liquid phase latent heat storage material 38 in the region 34 through which the heat transfer oil passes, it hardly melts. Therefore, it takes a long time until all the latent heat storage material 37 is melted, and it is difficult to use the latent heat storage material in the region 35 through which the heat transfer oil does not pass without waste.

この発明が解決しようとする課題は、短時間で無駄なく蓄熱することが可能な蓄熱装置を提供することである。   The problem to be solved by the present invention is to provide a heat storage device capable of storing heat in a short time without waste.

上記の課題を解決するため、前記蓄熱タンクの形状が、潜熱蓄熱材層中の熱媒油の通過しない領域にある固相の潜熱蓄熱材を、熱媒油の通過する領域に滑り落とすように傾斜した傾斜内面を有する形状であり、その傾斜内面に、固相の潜熱蓄熱材との摩擦を低減する摩擦低減手段を設けた構成を蓄熱装置に採用した。   In order to solve the above problems, the shape of the heat storage tank is such that the solid phase latent heat storage material in the region where the heat transfer oil in the latent heat storage material layer does not pass slides down to the region through which the heat transfer oil passes. A configuration having an inclined inner surface and a friction reducing means for reducing friction with a solid phase latent heat storage material is provided in the inclined inner surface of the heat storage device.

この蓄熱装置は、潜熱蓄熱材層がほぼすべて固相になった状態から、廃熱をもつ熱媒油を供給管から潜熱蓄熱材層中に供給すると、潜熱蓄熱材層中の熱媒油が通過する領域では、潜熱蓄熱材が短時間で融けて液相になるが、熱媒油の通過しない領域では、潜熱蓄熱材が固相のまま、蓄熱タンクの傾斜内面に乗った状態となる。ここで、傾斜内面の摩擦力は摩擦低減手段で低く抑えられているので、熱媒油の通過しない領域にある固相の潜熱蓄熱材は、その自重で熱媒油の通過する領域に滑り落ち、熱媒油と直接接触して短時間で融ける。   In this heat storage device, when heat medium oil with waste heat is supplied from the supply pipe into the latent heat storage material layer from a state where the latent heat storage material layer is almost in a solid phase, the heat medium oil in the latent heat storage material layer is In the passing region, the latent heat storage material melts in a short time into a liquid phase, but in the region where the heat transfer oil does not pass, the latent heat storage material remains in a solid phase and rides on the inclined inner surface of the heat storage tank. Here, since the frictional force of the inclined inner surface is kept low by the friction reducing means, the solid phase latent heat storage material in the area where the heat transfer oil does not pass slides down to the area where the heat transfer oil passes by its own weight. It melts in a short time in direct contact with the heat transfer oil.

前記摩擦低減手段としては、例えば、前記傾斜内面に形成した低摩擦皮膜、前記傾斜内面に形成した研磨面、前記傾斜内面を加熱する加熱機構などが挙げられる。前記加熱機構としては、例えば、蓄熱タンクの外面に沿って設けた熱源流体の流路が挙げられる。   Examples of the friction reducing means include a low friction film formed on the inclined inner surface, a polished surface formed on the inclined inner surface, a heating mechanism for heating the inclined inner surface, and the like. Examples of the heating mechanism include a heat source fluid flow path provided along the outer surface of the heat storage tank.

また、前記蓄熱装置から熱を取り出すときに、熱媒油の通過しない領域にある固相の潜熱蓄熱材が、熱媒油の通過する領域に滑り落ちると、その潜熱蓄熱材が成長することにより、供給管からの熱媒油の供給が妨げられる恐れがある。そのため、前記加熱機構による加熱は解除可能とすると好ましい。このようにすると、蓄熱装置から熱を取り出すときは、加熱機構による加熱を解除することにより、傾斜内面と固相の潜熱蓄熱材との間の摩擦力を確保することができ、その結果、潜熱蓄熱材の滑り落ちを防止することが可能となる。   Further, when extracting heat from the heat storage device, if the solid phase latent heat storage material in the region through which the heat transfer oil does not pass slides down to the region through which the heat transfer oil passes, the latent heat storage material grows, There is a possibility that the supply of the heat transfer oil from the supply pipe may be hindered. Therefore, it is preferable that heating by the heating mechanism can be released. In this way, when the heat is taken out from the heat storage device, the frictional force between the inclined inner surface and the solid phase latent heat storage material can be secured by releasing the heating by the heating mechanism. It becomes possible to prevent the heat storage material from slipping down.

また、前記蓄熱タンクの形状としては、例えば、中心軸が略水平の筒状であり、かつ、その中心軸に直交する断面が円形、楕円形、または下部が窄まる多角形のものが挙げられる。ここで、略水平とは、厳密な意味での水平である必要がなく、蓄熱タンク内の液体を排出するための傾斜を許容する意味での水平である。   In addition, examples of the shape of the heat storage tank include a cylindrical shape whose central axis is substantially horizontal and whose cross section perpendicular to the central axis is circular, elliptical, or polygonal whose bottom is narrowed. . Here, “substantially horizontal” does not need to be horizontal in a strict sense, but is horizontal in a sense that allows inclination for discharging the liquid in the heat storage tank.

この発明の蓄熱装置は、潜熱蓄熱材層中の熱媒油の通過しない領域にある固相の潜熱蓄熱材が、熱媒油の通過する領域に滑り落ちやすく、滑り落ちた潜熱蓄熱材は、熱媒油と直接接触して短時間で融ける。そのため、この蓄熱装置は、蓄熱タンク内の潜熱蓄熱材に、短時間で無駄なく蓄熱することができる。   In the heat storage device of the present invention, the solid phase latent heat storage material in the region where the heat transfer oil in the latent heat storage material layer does not pass easily slides down to the region through which the heat transfer oil passes, Melts in a short time by direct contact with heat transfer oil. Therefore, this heat storage device can store heat in the latent heat storage material in the heat storage tank in a short time without waste.

図1に、熱源施設1(例えば、発電所や廃棄物焼却場、製鉄所、化学プラント)で生じる廃熱を、熱源施設1から離れた熱利用施設2(例えば、オフィスビル、病院、ホテル、クアハウス)で利用可能とする熱搬送システムを示す。   In FIG. 1, waste heat generated in a heat source facility 1 (for example, a power plant, a waste incineration plant, a steel mill, a chemical plant) is converted into a heat utilization facility 2 (for example, an office building, a hospital, a hotel, This shows a heat transfer system that can be used in Kurhaus.

この熱搬送システムは、熱源施設1側に、熱源管3と、熱媒管4と、熱源管3と熱媒管4の間で熱交換を行なう熱交換器5とが設けられている。熱源管3は熱源施設1に接続されており、熱源施設1と熱交換器5の間で、廃熱を有する熱源流体(例えば、温水や蒸気)が循環するようになっている。熱媒管4は、この発明の実施形態の蓄熱装置6に着脱可能に接続されており、熱媒管4の途中に設けた循環ポンプ7を作動させると、熱交換器5と蓄熱装置6の間で熱媒油が循環し、その熱媒油を介して熱源管3から蓄熱装置6に熱が伝達され、蓄熱される。   In this heat transfer system, a heat source pipe 3, a heat medium pipe 4, and a heat exchanger 5 that performs heat exchange between the heat source pipe 3 and the heat medium pipe 4 are provided on the heat source facility 1 side. The heat source pipe 3 is connected to the heat source facility 1, and a heat source fluid (for example, hot water or steam) having waste heat circulates between the heat source facility 1 and the heat exchanger 5. The heat medium pipe 4 is detachably connected to the heat storage device 6 according to the embodiment of the present invention. When the circulation pump 7 provided in the middle of the heat medium pipe 4 is operated, the heat exchanger 5 and the heat storage device 6 are connected. Heat medium oil circulates between them, heat is transmitted from the heat source pipe 3 to the heat storage device 6 through the heat medium oil, and heat is stored.

また、この熱搬送システムは、熱利用施設2側に、熱利用管8と、熱媒管9と、熱利用管8と熱媒管9の間で熱交換を行なう熱交換器10とが設けられている。熱利用管8は、熱利用施設2に接続されており、熱利用施設2と熱交換器10の間で、熱利用媒体(例えば、給湯用水や暖房用水)が循環するようになっている。熱媒管9は、蓄熱装置6に着脱可能に接続されており、熱媒管9の途中に設けた循環ポンプ11を作動させると、蓄熱装置6と熱交換器10の間で熱媒油が循環し、その熱媒油を介して蓄熱装置6から熱利用管8に熱が伝達され、その熱を利用して熱利用施設2での給湯や暖房が可能となる。   Moreover, this heat transfer system is provided with a heat utilization pipe 8, a heat medium pipe 9, and a heat exchanger 10 that performs heat exchange between the heat utilization pipe 8 and the heat medium pipe 9 on the heat utilization facility 2 side. It has been. The heat utilization pipe 8 is connected to the heat utilization facility 2, and a heat utilization medium (for example, hot water supply water or heating water) is circulated between the heat utilization facility 2 and the heat exchanger 10. The heat medium pipe 9 is detachably connected to the heat storage device 6. When the circulation pump 11 provided in the middle of the heat medium pipe 9 is operated, the heat medium oil is exchanged between the heat storage device 6 and the heat exchanger 10. It circulates and heat is transmitted from the heat storage device 6 to the heat utilization pipe 8 via the heat transfer oil, and hot water supply or heating in the heat utilization facility 2 becomes possible using the heat.

この熱搬送システムは、上述した熱源施設1と熱利用施設2の間で、蓄熱装置6を行き来させることにより、熱源施設1の廃熱を熱利用施設2の熱エネルギーとして利用することができる。   In this heat transfer system, the waste heat of the heat source facility 1 can be used as the heat energy of the heat utilization facility 2 by moving the heat storage device 6 between the heat source facility 1 and the heat utilization facility 2 described above.

蓄熱装置6は、図2、図3に示すように、中心軸が略水平の筒状であり、かつ、その中心軸に直交する断面が円形の蓄熱タンク12を有する。蓄熱タンク12内には、潜熱蓄熱材13と熱媒油14とが上下二層に分離した状態で収容されている。潜熱蓄熱材13は、固相から液相に相変化するときに周りから熱を吸収し、液相から固相に相変化するときに放熱する。このような潜熱蓄熱材13として、例えば、エリスリトールやマンニトール、酢酸ナトリウム三水和物、塩化マグネシウム六水和物などを用いることができる。   As shown in FIGS. 2 and 3, the heat storage device 6 includes a heat storage tank 12 having a substantially horizontal cylindrical central axis and a circular cross section perpendicular to the central axis. In the heat storage tank 12, the latent heat storage material 13 and the heat transfer oil 14 are accommodated in a state of being separated into upper and lower layers. The latent heat storage material 13 absorbs heat from the surroundings when the phase changes from the solid phase to the liquid phase, and dissipates heat when the phase changes from the liquid phase to the solid phase. As such latent heat storage material 13, for example, erythritol, mannitol, sodium acetate trihydrate, magnesium chloride hexahydrate, or the like can be used.

熱媒油14は、潜熱蓄熱材13よりも比重が小さいものが用いられ、潜熱蓄熱材13との比重差によって潜熱蓄熱材13の表面に浮いた状態となっている。また、蓄熱タンク12内には空気層15が設けられており、その空気層15が、潜熱蓄熱材層16と熱媒油層17の体積変化を吸収するようになっている。   The heat medium oil 14 has a specific gravity smaller than that of the latent heat storage material 13 and floats on the surface of the latent heat storage material 13 due to a difference in specific gravity with the latent heat storage material 13. Further, an air layer 15 is provided in the heat storage tank 12, and the air layer 15 absorbs volume changes of the latent heat storage material layer 16 and the heat transfer oil layer 17.

また、蓄熱タンク12には、潜熱蓄熱材層16中に熱媒油14を供給する供給管18と、熱媒油層17から熱媒油14を回収する回収管19とが設けられている。供給管18は、蓄熱タンク12の中心軸と略平行に配置され、潜熱蓄熱材層16中に熱媒油14を吐出する下向きの吐出口20が、長手方向に間隔をおいて多数形成されている。   Further, the heat storage tank 12 is provided with a supply pipe 18 for supplying the heat medium oil 14 into the latent heat storage material layer 16 and a recovery pipe 19 for recovering the heat medium oil 14 from the heat medium oil layer 17. The supply pipe 18 is disposed substantially parallel to the central axis of the heat storage tank 12, and a number of downward discharge ports 20 for discharging the heat transfer oil 14 into the latent heat storage material layer 16 are formed at intervals in the longitudinal direction. Yes.

蓄熱タンク12内の潜熱蓄熱材層16には、図3に示すように、供給管18から供給された熱媒油14が通過する領域21と、その熱媒油14が通過しない領域22とがある。蓄熱タンク12は、熱媒油14が通過しない領域22にある固相の潜熱蓄熱材13を、潜熱蓄熱材層16中の熱媒油14の通過する領域21に滑り落とすように傾斜した傾斜内面23を有し、その傾斜内面23を含む蓄熱タンク12の内面全体に、固相の潜熱蓄熱材13との摩擦を低減する低摩擦皮膜(例えば、フッ素樹脂コーティングやシリコン樹脂コーティング等の疎水性皮膜)24が施されている。   As shown in FIG. 3, the latent heat storage material layer 16 in the heat storage tank 12 includes a region 21 through which the heat transfer oil 14 supplied from the supply pipe 18 passes and a region 22 through which the heat transfer oil 14 does not pass. is there. The heat storage tank 12 is inclined so that the solid phase latent heat storage material 13 in the region 22 through which the heat transfer oil 14 does not pass slides down to the region 21 through which the heat transfer oil 14 passes in the latent heat storage material layer 16. A low-friction film (for example, a hydrophobic film such as a fluororesin coating or a silicon resin coating) that reduces friction with the solid-phase latent heat storage material 13 on the entire inner surface of the heat storage tank 12 including the inclined inner surface 23. ) 24 is given.

この蓄熱装置6に熱を蓄えるときは、蓄熱装置6の供給管18と回収管19を、熱源施設1の熱媒管4に接続し、その状態で循環ポンプ7を作動させ、蓄熱装置6と熱交換器5の間で熱媒油14を循環させる。このとき、供給管18から潜熱蓄熱材層16中に熱媒油14が吐出され、その熱媒油14が、潜熱蓄熱材13との比重差によって潜熱蓄熱材層16中を上昇する。その上昇過程において、熱媒油14が通過する領域21の潜熱蓄熱材13は、熱媒油14と直接接触して熱を受け取り、固相から液相に変化する。また、熱媒油14が通過しない領域22にある固相の潜熱蓄熱材13は、蓄熱タンク12の傾斜内面23に沿って、熱媒油14が通過する領域21に滑り落ち、滑り落ちた潜熱蓄熱材13は、供給管18から吐出された熱媒油14と直接接触して短時間で融ける。また、固相の潜熱蓄熱材13が滑り落ちるときに生じる蓄熱タンク12内の流動により、潜熱蓄熱材13と熱媒油14との間の接触が促進される。   When heat is stored in the heat storage device 6, the supply pipe 18 and the recovery pipe 19 of the heat storage device 6 are connected to the heat medium pipe 4 of the heat source facility 1, and the circulation pump 7 is operated in that state. The heat transfer oil 14 is circulated between the heat exchangers 5. At this time, the heat transfer oil 14 is discharged from the supply pipe 18 into the latent heat storage material layer 16, and the heat transfer oil 14 rises in the latent heat storage material layer 16 due to the specific gravity difference with the latent heat storage material 13. In the rising process, the latent heat storage material 13 in the region 21 through which the heat transfer oil 14 passes directly contacts the heat transfer oil 14 to receive heat, and changes from the solid phase to the liquid phase. Further, the solid phase latent heat storage material 13 in the region 22 through which the heat transfer oil 14 does not pass slides down to the region 21 through which the heat transfer oil 14 passes along the inclined inner surface 23 of the heat storage tank 12, and the latent heat that has slipped down. The heat storage material 13 directly contacts the heat transfer oil 14 discharged from the supply pipe 18 and melts in a short time. Moreover, the contact between the latent heat storage material 13 and the heat transfer oil 14 is promoted by the flow in the heat storage tank 12 generated when the solid phase latent heat storage material 13 slides down.

一方、この蓄熱装置6から熱を取り出すときは、蓄熱装置6の供給管18と回収管19を、熱利用施設2の熱媒管9に接続し、その状態で循環ポンプ11を作動させ、蓄熱装置6と熱交換器10の間で熱媒油14を循環させる。このとき、供給管18から潜熱蓄熱材層16中に熱媒油14が吐出され、その熱媒油14が、潜熱蓄熱材13との比重差によって潜熱蓄熱材層16中を上昇し、その上昇過程において、潜熱蓄熱材13と直接接触して熱を受け取る。   On the other hand, when extracting heat from the heat storage device 6, the supply pipe 18 and the recovery pipe 19 of the heat storage device 6 are connected to the heat medium pipe 9 of the heat utilization facility 2, and the circulation pump 11 is operated in this state to store the heat. The heat transfer oil 14 is circulated between the device 6 and the heat exchanger 10. At this time, the heat transfer oil 14 is discharged from the supply pipe 18 into the latent heat storage material layer 16, and the heat transfer oil 14 rises in the latent heat storage material layer 16 due to the specific gravity difference with the latent heat storage material 13, and the rise. In the process, heat is received in direct contact with the latent heat storage material 13.

この蓄熱装置6は、熱媒油14が通過しない領域22にある固相の潜熱蓄熱材13が、蓄熱タンク12の傾斜内面23に沿って、潜熱蓄熱材層16中の熱媒油14の通過する領域21に滑り落ちやすく、滑り落ちた固相の潜熱蓄熱材13は、熱媒油14と直接接触して短時間で融ける。そのため、この蓄熱装置6は、熱媒油14が通過しない領域22にある潜熱蓄熱材13に、短時間で無駄なく蓄熱することが可能である。   In this heat storage device 6, the solid-phase latent heat storage material 13 in the region 22 through which the heat transfer oil 14 does not pass passes along the inclined inner surface 23 of the heat storage tank 12 through the heat transfer oil 14 in the latent heat storage material layer 16. The solid-phase latent heat storage material 13 that easily slides down to the region 21 to be melted in direct contact with the heat transfer oil 14 and melts in a short time. Therefore, the heat storage device 6 can store heat in the latent heat storage material 13 in the region 22 where the heat transfer oil 14 does not pass in a short time without waste.

上記実施形態では、蓄熱タンク12の内面全体に低摩擦皮膜24を施しているが、低摩擦皮膜24は、蓄熱タンク12の内面のうち、少なくとも、熱媒油14の通過しない領域22にある固相の潜熱蓄熱材13を、熱媒油14の通過する領域21に滑り落とすように傾斜した部分に施していればよい。   In the above embodiment, the low friction coating 24 is applied to the entire inner surface of the heat storage tank 12, but the low friction coating 24 is at least in the region 22 where the heat transfer oil 14 does not pass among the inner surface of the heat storage tank 12. The phase latent heat storage material 13 may be applied to the inclined portion so as to slide down to the region 21 through which the heat transfer oil 14 passes.

また、上記実施形態では、固相の潜熱蓄熱材13との摩擦を低減するため、傾斜内面23に低摩擦皮膜24を形成したが、低摩擦皮膜24にかえて、研磨面を形成してもよい。このようにしても、その研磨面に沿って、熱媒油14の通過しない領域22にある固相の潜熱蓄熱材13が、潜熱蓄熱材層16中の熱媒油14の通過する領域21に滑り落ちやすくなる。   In the above embodiment, the low friction film 24 is formed on the inclined inner surface 23 in order to reduce the friction with the solid phase latent heat storage material 13, but even if a polished surface is formed instead of the low friction film 24. Good. Even in this case, the solid phase latent heat storage material 13 in the region 22 through which the heat transfer oil 14 does not pass passes along the polished surface to the region 21 through which the heat transfer oil 14 passes in the latent heat storage material layer 16. It becomes easy to slip off.

また、傾斜内面23に低摩擦皮膜24を形成するかわりに、図4に示すように、蓄熱タンク12の外面に沿って熱源流体(温水や蒸気など)の流路25を設けてもよい。このようにすると、蓄熱装置6に熱を蓄えるときは、熱源施設1の廃熱を有する熱源流体を流路25に流すことによって、蓄熱タンク12の傾斜内面23を加熱することができ、その傾斜内面23に沿って融けた液相の潜熱蓄熱材が、固相の潜熱蓄熱材13と傾斜内面23との間に介在することによって、固相の潜熱蓄熱材13と傾斜内面23との間の摩擦を低減することができる。   Further, instead of forming the low friction film 24 on the inclined inner surface 23, a flow path 25 for heat source fluid (hot water, steam, etc.) may be provided along the outer surface of the heat storage tank 12, as shown in FIG. In this way, when storing heat in the heat storage device 6, the inclined inner surface 23 of the heat storage tank 12 can be heated by flowing a heat source fluid having waste heat of the heat source facility 1 through the flow path 25, and the inclination thereof. The liquid phase latent heat storage material melted along the inner surface 23 is interposed between the solid phase latent heat storage material 13 and the inclined inner surface 23, so that the solid phase latent heat storage material 13 and the inclined inner surface 23 are interposed. Friction can be reduced.

一方、蓄熱装置6から熱を取り出すときは、熱媒油14の通過しない領域22にある固相の潜熱蓄熱材13が、熱媒油14の通過する領域21に滑り落ちると、その潜熱蓄熱材13が成長することにより、供給管18からの熱媒油14の吐出が妨げられる恐れがある。そこで、蓄熱装置6から熱を取り出すときは、流路25に熱源流体を流さないことによって、傾斜内面23と固相の潜熱蓄熱材13との間の摩擦力を確保し、潜熱蓄熱材13の滑り落ちを防止する。   On the other hand, when extracting heat from the heat storage device 6, if the solid phase latent heat storage material 13 in the region 22 through which the heat transfer oil 14 does not pass slides down to the region 21 through which the heat transfer oil 14 passes, the latent heat storage material 13. , The discharge of the heat transfer oil 14 from the supply pipe 18 may be hindered. Therefore, when extracting heat from the heat storage device 6, the heat source fluid is not passed through the flow path 25, thereby ensuring a frictional force between the inclined inner surface 23 and the solid phase latent heat storage material 13. Prevent sliding down.

上記実施形態では、蓄熱タンク12の形状として、中心軸が略水平の筒状であり、かつ、中心軸に直交する断面が円形のものを例に挙げて説明したが、この発明は、中心軸に直交する断面が楕円形の蓄熱タンクや、中心軸に直交する断面が、下部が窄まる多角形の蓄熱タンクにも適用することができる。要は、蓄熱タンクの形状が、潜熱蓄熱材層16中の熱媒油14の通過しない領域22にある固相の潜熱蓄熱材13を、潜熱蓄熱材層16中の熱媒油14の通過する領域21に滑り落とすように傾斜した傾斜内面23を有する形状であればよい。   In the above embodiment, the shape of the heat storage tank 12 has been described by taking as an example the case where the central axis is a substantially horizontal cylindrical shape and the cross section perpendicular to the central axis is circular. It can also be applied to a heat storage tank having an elliptical cross section orthogonal to the polygonal shape, and a polygonal heat storage tank having a cross section orthogonal to the central axis narrowed at the bottom. The point is that the shape of the heat storage tank passes through the solid phase latent heat storage material 13 in the region 22 where the heat transfer medium oil 14 in the latent heat storage material layer 16 does not pass through the heat transfer medium oil 14 in the latent heat storage material layer 16. Any shape having an inclined inner surface 23 inclined so as to slide into the region 21 may be used.

上記実施形態は、本発明の実施形態の一例であり、本発明の技術的範囲は、上記実施形態に限定されない。本発明の技術的範囲は、特許請求の範囲によって示され、特許請求の範囲の記載と均等の意味及びその範囲内でのすべての変形を含むものである。   The said embodiment is an example of embodiment of this invention, and the technical scope of this invention is not limited to the said embodiment. The technical scope of the present invention is defined by the claims, and includes the meaning equivalent to the description of the claims and all modifications within the scope.

この発明の実施形態の蓄熱装置を利用した熱搬送システムを示す図The figure which shows the heat transfer system using the heat storage apparatus of embodiment of this invention 図1に示す蓄熱装置の断面図Sectional view of the heat storage device shown in FIG. 図2のIII−III線に沿った断面図Sectional view along line III-III in FIG. 図3の蓄熱装置の変形例を示す断面図Sectional drawing which shows the modification of the heat storage apparatus of FIG. 従来の蓄熱装置を示す断面図Sectional view showing a conventional heat storage device

符号の説明Explanation of symbols

6 蓄熱装置
12 蓄熱タンク
13 潜熱蓄熱材
14 熱媒油
16 潜熱蓄熱材層
17 熱媒油層
18 供給管
19 回収管
21 熱媒油の通過する領域
22 熱媒油の通過しない領域
23 傾斜内面
24 低摩擦皮膜
25 流路
6 heat storage device 12 heat storage tank 13 latent heat storage material 14 heat medium oil 16 latent heat storage material layer 17 heat medium oil layer 18 supply pipe 19 recovery pipe 21 area through which heat medium oil passes 22 area through which heat medium oil does not pass 23 inclined inner surface 24 low Friction coating 25

Claims (7)

潜熱蓄熱材(13)とその潜熱蓄熱材(13)よりも比重の小さい熱媒油(14)とを上下二層に分離した状態で収容する蓄熱タンク(12)と、その蓄熱タンク(12)内の潜熱蓄熱材層(16)中に熱媒油(14)を供給する供給管(18)と、前記蓄熱タンク(12)内の熱媒油層(17)から熱媒油(14)を回収する回収管(19)とを有し、前記供給管(18)から潜熱蓄熱材層(16)中に供給された熱媒油(14)を潜熱蓄熱材(13)に直接接触させて熱交換を行なう蓄熱装置(6)において、前記蓄熱タンク(12)の形状が、潜熱蓄熱材層(16)中の熱媒油(14)の通過しない領域(22)にある固相の潜熱蓄熱材(13)を、熱媒油(14)の通過する領域(21)に滑り落とすように傾斜した傾斜内面(23)を有する形状であり、その傾斜内面(23)に、固相の潜熱蓄熱材(13)との摩擦を低減する摩擦低減手段(24)を設けたことを特徴とする蓄熱装置。   A heat storage tank (12) for accommodating the latent heat storage material (13) and the heat transfer oil (14) having a specific gravity smaller than that of the latent heat storage material (13) in a state where the latent heat storage material (13) is separated into upper and lower layers, and the heat storage tank (12) The heat transfer oil (14) is recovered from the supply pipe (18) for supplying the heat transfer oil (14) into the latent heat storage material layer (16) and the heat transfer oil layer (17) in the heat storage tank (12). The heat transfer oil (14) supplied from the supply pipe (18) into the latent heat storage material layer (16) is brought into direct contact with the latent heat storage material (13) for heat exchange. In the heat storage device (6), the solid-phase latent heat storage material (in the region (22) where the heat transfer oil (14) does not pass through the latent heat storage material layer (16) has a shape of the heat storage tank (12). 13) inclined inner surface (23 inclined to slide down to the region (21) through which the heat transfer oil (14) passes. The a shape with, its inclined inner surface (23), thermal storage, characterized in that a friction reducing means for reducing friction between the solid phase latent heat storage material (13) (24) device. 前記摩擦低減手段が、前記傾斜内面(23)に形成した低摩擦皮膜(24)である請求項1に記載の蓄熱装置。   The heat storage device according to claim 1, wherein the friction reducing means is a low friction film (24) formed on the inclined inner surface (23). 前記摩擦低減手段が、前記傾斜内面(23)に形成した研磨面である請求項1に記載の蓄熱装置。   The heat storage device according to claim 1, wherein the friction reducing means is a polished surface formed on the inclined inner surface (23). 前記摩擦低減手段が、前記傾斜内面(23)を加熱する加熱機構(25)である請求項1に記載の蓄熱装置。   The heat storage device according to claim 1, wherein the friction reducing means is a heating mechanism (25) for heating the inclined inner surface (23). 前記加熱機構が、蓄熱タンク(12)の外面に沿って設けた熱源流体の流路(25)である請求項4に記載の蓄熱装置。   The heat storage device according to claim 4, wherein the heating mechanism is a flow path (25) of a heat source fluid provided along an outer surface of the heat storage tank (12). 前記加熱機構(25)による加熱を解除可能とした請求項4または5に記載の蓄熱装置。   The heat storage device according to claim 4 or 5, wherein heating by the heating mechanism (25) can be released. 前記蓄熱タンク(12)の形状が、中心軸が略水平の筒状であり、かつ、その中心軸に直交する断面が円形、楕円形、または下部が窄まる多角形である請求項1から6のいずれかに記載の蓄熱装置。   The shape of the heat storage tank (12) is a cylindrical shape whose central axis is substantially horizontal, and a cross section perpendicular to the central axis is circular, elliptical, or a polygon whose bottom is narrowed. The thermal storage apparatus in any one of.
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