JP5192260B2 - Heat storage device - Google Patents

Heat storage device Download PDF

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JP5192260B2
JP5192260B2 JP2008042694A JP2008042694A JP5192260B2 JP 5192260 B2 JP5192260 B2 JP 5192260B2 JP 2008042694 A JP2008042694 A JP 2008042694A JP 2008042694 A JP2008042694 A JP 2008042694A JP 5192260 B2 JP5192260 B2 JP 5192260B2
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heat
heat storage
heat transfer
storage material
transfer oil
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JP2009198134A (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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • 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

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。
特開2007−132569号公報
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, heat is dissipated. In addition, 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.
JP 2007-13269 A

ところで、蓄熱タンク内の潜熱蓄熱材層には、供給管から供給された熱媒油が通過する領域と通過しない領域とがあり、熱媒油が通過する領域の潜熱蓄熱材は、熱媒油と直接接触して熱交換を行なうが、熱媒油が通過しない領域の潜熱蓄熱材は、熱媒油が通過する領域の潜熱蓄熱材を介して熱交換を行なう。そのため、熱媒油が通過しない領域の潜熱蓄熱材は、蓄放熱させるのに長時間を要し、その領域の潜熱蓄熱材を十分に活用することが難しかった。   By the way, the latent heat storage material layer in the heat storage tank has a region through which the heat medium oil supplied from the supply pipe passes and a region through which the heat medium oil passes, and the latent heat storage material in the region through which the heat medium oil passes is the heat medium oil. The latent heat storage material in the region through which the heat transfer oil does not pass performs heat exchange through the latent heat storage material in the region through which the heat transfer oil passes. Therefore, the latent heat storage material in the region where the heat transfer oil does not pass takes a long time to store and release heat, and it is difficult to fully utilize the latent heat storage material in that region.

例えば、図9に示すように、蓄熱タンク31内の潜熱蓄熱材32を融かして蓄熱する場合、供給管33から供給された熱媒油の通過する領域34の潜熱蓄熱材32は、その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、熱媒油が通過しない領域35の潜熱蓄熱材32は、熱媒油と直接接触しないので、なかなか融けない。そのため、蓄熱タンク31内の潜熱蓄熱材32がすべて融けるまで長時間を要し、蓄熱タンク31内の潜熱蓄熱材32を無駄なく利用するのが難しかった。   For example, as shown in FIG. 9, when the latent heat storage material 32 in the heat storage tank 31 is melted and stored, the latent heat storage material 32 in the region 34 through which the heat transfer oil supplied from the supply pipe 33 passes is Since the heat is received in direct contact with the heat transfer oil, it melts in a short time. However, the latent heat storage material 32 in the region 35 through which the heat transfer oil does not pass does not come in direct contact with the heat transfer oil, and therefore does not melt easily. Therefore, it takes a long time until all the latent heat storage material 32 in the heat storage tank 31 is melted, and it is difficult to use the latent heat storage material 32 in the heat storage tank 31 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放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 and radiating heat without waste in a short time.

上記の課題を解決するため、前記蓄熱タンク内に、前記供給管から潜熱蓄熱材層中に供給された熱媒油と、その熱媒油が通過しない領域の潜熱蓄熱材との間で熱交換を行なう伝熱部材を設けた。この伝熱部材は、前記熱媒油層に至るように設けることができる。   In order to solve the above-mentioned problem, heat exchange is performed between the heat transfer oil supplied from the supply pipe into the latent heat storage material layer and the latent heat storage material in a region through which the heat transfer oil does not pass. The heat-transfer member which performs is provided. This heat transfer member can be provided so as to reach the heat transfer oil layer.

この発明の蓄熱装置は、蓄熱タンク内に設けた伝熱部材が、供給管から潜熱蓄熱材層中に供給された熱媒油と、その熱媒油が通過しない領域の潜熱蓄熱材との間で熱交換を行なうので、熱媒油が通過しない領域の潜熱蓄熱材を蓄放熱させるのに必要な時間が短い。そのため、この発明の蓄熱装置は、蓄熱タンク内の潜熱蓄熱材を、短時間で無駄なく利用することができる。   In the heat storage device of the present invention, the heat transfer member provided in the heat storage tank is between the heat transfer oil supplied from the supply pipe into the latent heat storage material layer and the latent heat storage material in the region through which the heat transfer oil does not pass. Therefore, the time required for storing and radiating the latent heat storage material in the region where the heat transfer oil does not pass is short. Therefore, the heat storage device of the present invention can use the latent heat storage material in the heat storage tank in a short time without waste.

さらに、前記伝熱部材を、前記熱媒油層に至るように設けたものは、その伝熱部材を介して、熱媒油が通過しない領域の潜熱蓄熱材と、熱媒油層中の熱媒油との間でも熱交換が行われるので、蓄放熱の効率が高い。   Furthermore, what provided the said heat-transfer member so that it may reach the said heat-medium oil layer is the latent-heat storage material of the area | region where heat-medium oil does not pass through the heat-transfer member, and the heat-medium oil in a heat-medium oil layer Since heat exchange is also performed between the two, the efficiency of heat storage and dissipation is high.

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、中心軸を略水平とする円筒状の蓄熱タンク12を有する。蓄熱タンク12は、断熱壁で覆われており、その蓄熱タンク12内に、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 cylindrical heat storage tank 12 whose central axis is substantially horizontal. The heat storage tank 12 is covered with a heat insulating wall, and the latent heat storage material 13 and the heat transfer oil 14 are accommodated in the heat storage tank 12 in a state of being separated into two 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内には、金属製(例えば、銅製)の伝熱板21が設けられている。伝熱板21は、図3に示すように、供給管18から下向きに吐出された熱媒油14と接触する位置から、蓄熱タンク12の内面に沿って上方に延びており、その伝熱板21を介して、供給管18から潜熱蓄熱材層16中に供給された熱媒油14と、その熱媒油14が通過しない領域22の潜熱蓄熱材13との間で熱交換を行なうようになっている。また、伝熱板21は、熱媒油層17に至るように設けられており、その伝熱板21を介して、熱媒油14が通過しない領域22の潜熱蓄熱材13と、熱媒油層17中の熱媒油14との間でも熱交換を行なうようになっている。伝熱板21は、潜熱蓄熱材13に対する接触面積が大きくなるように、蓄熱タンク12の内面に対して直角となる姿勢で配置されている。   A metal (for example, copper) heat transfer plate 21 is provided in the heat storage tank 12. As shown in FIG. 3, the heat transfer plate 21 extends upward along the inner surface of the heat storage tank 12 from a position in contact with the heat transfer oil 14 discharged downward from the supply pipe 18. The heat transfer oil 14 supplied from the supply pipe 18 into the latent heat storage material layer 16 via the supply pipe 18 and the latent heat storage material 13 in the region 22 through which the heat transfer oil 14 does not pass are exchanged. It has become. The heat transfer plate 21 is provided so as to reach the heat transfer oil layer 17, and the latent heat storage material 13 in the region 22 where the heat transfer oil 14 does not pass through the heat transfer oil plate 17 and the heat transfer oil layer 17. Heat exchange is also performed with the heat transfer oil 14 inside. The heat transfer plate 21 is arranged in a posture perpendicular to the inner surface of the heat storage tank 12 so that a contact area with the latent heat storage material 13 is increased.

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23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の潜熱蓄熱材13は、供給管18から潜熱蓄熱材層16中に吐出された熱媒油14から、伝熱板21を介して熱を受け取り、固相から液相に変化する。   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 23 through which the heat transfer oil 14 passes is in direct contact with the heat transfer oil 14 to receive heat and change from a solid phase to a liquid phase. The latent heat storage material 13 in the region 22 through which the heat transfer oil 14 does not pass receives heat from the heat transfer oil 14 discharged from the supply pipe 18 into the latent heat storage material layer 16 via the heat transfer plate 21, Change from phase to liquid phase.

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。また、供給管18から潜熱蓄熱材層16中に吐出された熱媒油14は、伝熱板21を介して、熱媒油14が通過しない領域22の潜熱蓄熱材13からも熱を受け取る。   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. The heat transfer oil 14 discharged from the supply pipe 18 into the latent heat storage material layer 16 also receives heat from the latent heat storage material 13 in the region 22 where the heat transfer oil 14 does not pass through the heat transfer plate 21.

このように、蓄熱装置6は、蓄熱タンク12内に設けた伝熱板21が、供給管18から潜熱蓄熱材層16中に吐出された熱媒油14と、その熱媒油14が通過しない領域22の潜熱蓄熱材13との間で熱交換を行なうので、熱媒油14が通過しない領域22の潜熱蓄熱材13を蓄放熱させるのに必要な時間が短い。そのため、蓄熱タンク12内の潜熱蓄熱材13を、短時間で無駄なく利用することができる。   As described above, in the heat storage device 6, the heat transfer plate 21 provided in the heat storage tank 12 does not pass through the heat transfer oil 14 discharged from the supply pipe 18 into the latent heat storage material layer 16 and the heat transfer oil 14. Since heat exchange is performed with the latent heat storage material 13 in the region 22, the time required to store and dissipate the latent heat storage material 13 in the region 22 through which the heat transfer oil 14 does not pass is short. Therefore, the latent heat storage material 13 in the heat storage tank 12 can be used in a short time without waste.

また、この蓄熱装置6は、伝熱板21を介して、熱媒油14が通過しない領域22の潜熱蓄熱材13と、熱媒油層17中の熱媒油14との間でも熱交換を行なうので、蓄放熱の効率が高い。   The heat storage device 6 also exchanges heat between the latent heat storage material 13 in the region 22 where the heat transfer oil 14 does not pass and the heat transfer oil 14 in the heat transfer oil layer 17 via the heat transfer plate 21. Therefore, the efficiency of heat storage and dissipation is high.

上記実施形態では、伝熱板21は、蓄放熱の効率を高めるため、熱媒油層17に至るように配置しているが、図4に示すように、熱媒油層17に至らないように配置してもよい。   In the above embodiment, the heat transfer plate 21 is disposed so as to reach the heat medium oil layer 17 in order to increase the efficiency of heat storage and release, but as illustrated in FIG. 4, it is disposed so as not to reach the heat medium oil layer 17. May be.

また、上記実施形態の伝熱板21を設けるかわりに、図5に示すように、供給管18から吐出された熱媒油14と接触する位置に配置した銅板24と、熱媒油14が通過しない領域22の潜熱蓄熱材13の位置に配置した銅板25とを、ヒートパイプ26で連結し、そのヒートパイプ26を介して、供給管18から供給された熱媒油14と、その熱媒油14が通過しない領域22の潜熱蓄熱材13との間で熱交換が行われるようにしてもよい。   Further, instead of providing the heat transfer plate 21 of the above-described embodiment, as shown in FIG. 5, the copper plate 24 disposed at a position in contact with the heat transfer oil 14 discharged from the supply pipe 18 and the heat transfer oil 14 pass therethrough. The copper plate 25 arranged at the position of the latent heat storage material 13 in the region 22 not to be connected is connected by a heat pipe 26, the heat transfer oil 14 supplied from the supply pipe 18 through the heat pipe 26, and the heat transfer oil Heat exchange may be performed with the latent heat storage material 13 in the region 22 where the 14 does not pass.

ここで、ヒートパイプ26は、金属製のパイプ内に作動液を封入し、そのパイプ内を減圧したものであり、パイプ内の作動液の蒸発潜熱によって熱を吸収し、その蒸気がパイプ内を移動することにより熱を移動させ、その蒸気の凝縮潜熱によって熱を放出する。   Here, the heat pipe 26 is obtained by enclosing a working fluid in a metal pipe and depressurizing the inside of the pipe. The heat pipe 26 absorbs heat by the latent heat of vaporization of the working fluid in the pipe, and the steam passes through the pipe. The heat is transferred by moving, and the heat is released by the latent heat of condensation of the vapor.

また、上記実施形態の伝熱板21を設けるかわりに、図6、図7に示すように、蓄熱タンク12の内面に沿って分岐しながら上方に延びる金属製の伝熱体27を、蓄熱タンク12内に設け、その伝熱体27を介して熱交換が行われるようにしてもよい。このようにすると、供給管18から吐出された熱媒油14の熱が分岐して伝達するので、供給管18の吐出口20の設置間隔が広い場合にも、潜熱蓄熱材13を満遍なく蓄放熱させることができる。伝熱体27の分岐部27aは、蓄熱タンク12内における潜熱蓄熱材13の移動を妨げないように、薄肉に形成すると好ましい。   Moreover, instead of providing the heat transfer plate 21 of the above embodiment, as shown in FIGS. 6 and 7, a metal heat transfer body 27 extending upward while branching along the inner surface of the heat storage tank 12 is replaced with a heat storage tank. The heat exchange may be performed via the heat transfer body 27. In this way, since the heat of the heat transfer oil 14 discharged from the supply pipe 18 is branched and transmitted, the latent heat storage material 13 is uniformly stored and dissipated even when the installation interval of the discharge ports 20 of the supply pipe 18 is wide. Can be made. The branch portion 27a of the heat transfer body 27 is preferably formed thin so as not to hinder the movement of the latent heat storage material 13 in the heat storage tank 12.

また、上記実施形態の伝熱板21を設けるかわりに、図8に示すように、蓄熱タンク12内に銅線28を垂らし、その銅線28を介して、供給管18から潜熱蓄熱材層16中に供給された熱媒油14と、その熱媒油14が通過しない領域22の潜熱蓄熱材13との間で熱交換が行われるようにしてもよい。   Further, instead of providing the heat transfer plate 21 of the above embodiment, as shown in FIG. 8, a copper wire 28 is hung in the heat storage tank 12, and the latent heat storage material layer 16 is supplied from the supply pipe 18 through the copper wire 28. Heat exchange may be performed between the heat transfer oil 14 supplied therein and the latent heat storage material 13 in the region 22 through which the heat transfer oil 14 does not pass.

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. 図3の蓄熱装置の他の変形例を示す断面図Sectional drawing which shows the other modification of the thermal storage apparatus of FIG. 図3の蓄熱装置の更に他の変形例を示す断面図Sectional drawing which shows the further another modification of the heat storage apparatus of FIG. 図6のVII−VII線に沿った断面図Sectional drawing along the VII-VII line of FIG. 図3の蓄熱装置の更に他の変形例を示す断面図Sectional drawing which shows the further another 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 伝熱板
22 熱媒油が通過しない領域
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 heat transfer plate 22 area through which heat transfer oil does not pass

Claims (2)

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中心軸を略水平とする円筒状の蓄熱タンク(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た供給管(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)内に、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)と、その熱媒油(14)が通過しない領域(22)の潜熱蓄熱材(13)との間で熱交換を行なう伝熱部材(21)を、前記供給管(18)から下向きに吐出された熱媒油(14)と接触する位置から、前記蓄熱タンク(12)の円筒状の内面に沿って上方に延びるように設けたことを特徴とする蓄熱装置。
Cylindrical heat storage tank having a substantially horizontal central axis 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 two upper and lower layers. 12) and a supply in which a number of downward discharge ports (20) for discharging the heat transfer oil (14) are formed at intervals in the longitudinal direction in the latent heat storage material layer (16) in the heat storage tank (12) A pipe (18) and a recovery pipe (19) for recovering the heat transfer oil (14) from the heat transfer oil layer (17) in the heat storage tank (12), and the latent heat storage material from the supply pipe (18). In the heat storage device (6) that performs heat exchange by directly contacting the heat transfer oil (14) supplied in the layer (16) with the latent heat storage material (13),
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) and the region (22) through which the heat transfer oil (14) does not pass. From the position where the heat transfer member (21) that exchanges heat with the latent heat storage material (13) is in contact with the heat transfer oil (14) discharged downward from the supply pipe (18), the heat storage tank (12) A heat storage device provided so as to extend upward along the cylindrical inner surface .
前記伝熱部材(21)を、前記熱媒油層(17)に至るように設けた請求項1に記載の蓄熱装置。   The heat storage device according to claim 1, wherein the heat transfer member (21) is provided so as to reach the heat transfer oil layer (17).
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