JP2003130562A - Hot heat storage apparatus - Google Patents

Hot heat storage apparatus

Info

Publication number
JP2003130562A
JP2003130562A JP2001325275A JP2001325275A JP2003130562A JP 2003130562 A JP2003130562 A JP 2003130562A JP 2001325275 A JP2001325275 A JP 2001325275A JP 2001325275 A JP2001325275 A JP 2001325275A JP 2003130562 A JP2003130562 A JP 2003130562A
Authority
JP
Japan
Prior art keywords
heat
heat storage
medium
storage tank
storage device
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.)
Granted
Application number
JP2001325275A
Other languages
Japanese (ja)
Other versions
JP3873229B2 (en
Inventor
Yukio Uchiki
幸夫 内木
Kiyoshi Mineura
潔 峯浦
Nobukimi Kanai
延王 金井
Akito Machida
明登 町田
Hideo Inaba
英男 稲葉
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kansai Electric Power Co Inc
Mayekawa Manufacturing Co
Original Assignee
Kansai Electric Power Co Inc
Mayekawa Manufacturing Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kansai Electric Power Co Inc, Mayekawa Manufacturing Co filed Critical Kansai Electric Power Co Inc
Priority to JP2001325275A priority Critical patent/JP3873229B2/en
Publication of JP2003130562A publication Critical patent/JP2003130562A/en
Application granted granted Critical
Publication of JP3873229B2 publication Critical patent/JP3873229B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D20/00Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00
    • F28D20/02Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using latent heat
    • 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

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Heat-Pump Type And Storage Water Heaters (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a hot heat storage apparatus, capable of recovering exhaust heat or effectively using late-night electric power using a specified heat storage material and a specified heating medium capable of giving and receiving an enthalpy change of the heat storage material. SOLUTION: This hot heat storage apparatus is equipped with a latent heat storage body storing high-density polyethylene or the like as a latent heat storage material in a vessel, a heat storage tank storing propylene glycol or the like as a heating medium, a heating means for heating the heating medium in the heat storage tank and a heat recovery heat exchanger for heat recovery from the heating medium. The quantity of heat given from the heating means is stored and recovered by a heat absorbing means.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術の分野】本発明は物質の潜熱を利用
した蓄熱装置に関する。更に詳しくは、温度の高い領域
の廃熱の回収若しくは深夜電力の有効利用などを可能と
する温蓄熱装置に関する。
TECHNICAL FIELD The present invention relates to a heat storage device utilizing latent heat of a substance. More specifically, the present invention relates to a heat storage device capable of recovering waste heat in a high temperature region or effectively using late-night power.

【0002】[0002]

【従来の技術】潜熱蓄熱装置については、各種工業や廃
棄物回収過程で排出する廃熱の回収、深夜電力の貯蔵な
どにとって、有効な手段であるので、適切、高効率であ
る蓄熱材と、該蓄熱材のエンタルピ変化を円滑に授受可
能な熱媒体の選択を含むその装置構成が従来多数の研究
対象となってきた。
2. Description of the Related Art A latent heat storage device is an effective means for recovery of waste heat discharged in various industries and waste recovery processes, storage of late-night power, etc. A lot of researches have hitherto been made on the device configuration including selection of a heat medium capable of smoothly transferring the enthalpy change of the heat storage material.

【0003】潜熱蓄熱材は、該物質の持つ得意な相転移
点におけるエンタルピ変化を利用して、熱を吸収させる
ことにより、相変化した該物質に蓄熱し、必要時に、逆
の相変化をさせて、熱を取り出す機能を果たす材料であ
る。従来、この相転移点は物質の持つ融点を利用するケ
−スがこの種の目的では大多数であるが、結晶転移点そ
の他を利用する例もある。従って、前者の場合は、エン
タルピ変化は融解熱(若しくは結晶化熱)であり、後者
の場合は結晶転移熱である。
The latent heat storage material utilizes the enthalpy change at the phase transition point of the substance, which absorbs heat, to store heat in the substance that has undergone a phase change, and to cause an opposite phase change when necessary. It is a material that functions to extract heat. Conventionally, the majority of cases in which this phase transition point utilizes the melting point of a substance are for this purpose, but there are also examples in which the crystal transition point or the like is utilized. Therefore, in the former case, the enthalpy change is heat of fusion (or heat of crystallization), and in the latter case, it is heat of crystal transition.

【0004】従来、蓄熱材として知られ、利用されてい
る物質は、無機系と有機系とに大別できる。無機系のも
のには、硫酸ナトリウム、塩化カルシウム、酢酸ナトリ
ウムなどの無機塩水和物があり、これらは比較的低温度
の相転移点を利用できるが、100℃付近で相変化する
ものには、水酸化バリウム、硝酸マグネシウム、などの
無機塩水和物がある。
The substances conventionally known and used as heat storage materials can be roughly classified into inorganic type and organic type. Inorganic compounds include hydrates of inorganic salts such as sodium sulfate, calcium chloride, and sodium acetate, which can utilize the phase transition point at a relatively low temperature, but those that undergo a phase change near 100 ° C include: There are inorganic salt hydrates such as barium hydroxide and magnesium nitrate.

【0005】これら、無機塩水和物は溶融状態から、次
第に降温させていくと、本来の融点を過ぎても固化(結
晶化)せず、放熱しない(熱を取り出せない)という過
冷却現象を呈し、同時に融解時に不溶性物質が晶出し、
融解〜固化のヒートサイクルを繰り返すことにより、不
溶性物質が増加し続け、延いては相分離現象を来たす。
これらの分離、過冷却対策も各種なされているが、未だ
完全ではない。
When these inorganic salt hydrates are gradually cooled from the molten state, they do not solidify (crystallize) even after passing the original melting point and do not release heat (cannot take out heat), which is a supercooling phenomenon. , At the same time, the insoluble substance crystallizes during melting,
By repeating the heat cycle from melting to solidification, the amount of insoluble substances continues to increase, which eventually causes a phase separation phenomenon.
Various measures have been taken to separate these and supercool, but they are not yet complete.

【0006】一方、有機系の蓄熱材には、低分子結晶性
ポリオレフィン若しくは高分子ポリオレフィンがあり、
熱的安定性は良好で腐食性・毒性はなく、潜熱も大だ
が、粘度が高く自体流動せず、熱伝導も低いので、工夫
が必要である。例えばペレット、ストランド、フィルム
などの形状で利用するが、そのままでは形状が保持でき
ないので、コストのかかる放射線、電子線、シラン架橋
などが行われている。これらの分子構造における操作
は、自ずと分子構造を変化させることにほかならないの
で、融点などの物理特性が変化してしまう。また、架橋
高分子ポリオレフィンに結晶性物質を担持させて用いる
ケースもみうけられるが、該結晶性物質を溶出せずに、
エンタルピ変化を取り出すための熱媒体の選定も問題で
ある。
On the other hand, organic heat storage materials include low-molecular crystalline polyolefin or high-molecular polyolefin.
It has good thermal stability, is not corrosive or toxic, and has a large latent heat, but it has a high viscosity, does not flow itself, and has a low thermal conductivity. For example, it is used in the shape of pellets, strands, films, etc., but since the shape cannot be retained as it is, costly radiation, electron beam, silane cross-linking, etc. are performed. Since the operation on these molecular structures is nothing but to change the molecular structures, the physical properties such as the melting point change. In addition, there are cases where a crosslinked high molecular polyolefin is used by supporting a crystalline substance, but without eluting the crystalline substance,
There is also a problem in selecting a heat medium for extracting the enthalpy change.

【0007】前記したように、蓄熱材・熱媒体の選定と
相俟って、それら特定な物質を有効に機能させるため
の、装置構成がさらに問題であって、それぞれの物性に
適った装置の工夫がなされなけらばならない。
As described above, in combination with the selection of the heat storage material and the heat medium, the structure of the device for effectively functioning those specific substances is a further problem, and the device structure suitable for each physical property is required. It has to be devised.

【0008】[0008]

【発明が解決しようとする課題】本発明はかかる従来の
問題点に鑑みてなされたものであって、特定の蓄熱材と
該蓄熱材のエンタルピ変化を授受可能な特定の熱媒体と
を用いて、廃熱の回収若しくは深夜電力の有効利用など
を可能とする温蓄熱装置の提供を目的とする。
SUMMARY OF THE INVENTION The present invention has been made in view of the above conventional problems and uses a specific heat storage material and a specific heat medium capable of exchanging enthalpy changes of the heat storage material. Another object of the present invention is to provide a heat storage device capable of recovering waste heat or effectively using late-night power.

【0009】[0009]

【課題を解決するための手段】本発明の温蓄熱装置は、
潜熱蓄熱材として高密度ポリエチレンを容器に収納して
なる潜熱蓄熱体と、熱媒体としてプロピレングリコール
とを収容する蓄熱槽と、蓄熱槽中の熱媒体を加熱する加
熱手段と該熱媒体から熱回収を行う熱回収用熱交換器と
を備え、加熱手段より与えられた熱量を蓄熱し、熱回収
用熱交換器より回収するよう構成したことを特徴とす
る。
The heat storage device of the present invention comprises:
A latent heat storage body containing high-density polyethylene as a latent heat storage material in a container, a heat storage tank containing propylene glycol as a heat medium, heating means for heating the heat medium in the heat storage tank, and heat recovery from the heat medium. And a heat recovery heat exchanger for carrying out the above, and configured to store the amount of heat given by the heating means and recover the heat from the heat recovery heat exchanger.

【0010】廃棄物の焼却廃熱やボイラ廃熱など、熱回
収を必要とする廃熱源の温度は比較的高温で、少なくと
も150℃を超えるケースが多い。これら廃熱源より有
効に熱を吸収して蓄熱するには、熱源温度付近で、相転
移を起して、大きなエンタルピ変化で吸熱する蓄熱材を
用いるのが最も好ましい。また、深夜電力若しくは余剰
電力などを熱源として蓄積する目的に置いても、適度な
高温で行ったほうが、蓄熱槽の容積が小さくて済み効率
的である。かかる第一条件に加えて、蓄熱材のヒートサ
イクル安定性、熱伝導性、価格、毒性、爆発火災に対す
る安全性、腐食性等を勘案し、更に蓄熱材の融解前後の
形態変化に対応した装置構成を考案する必要がある。そ
して、かくして案出した蓄熱体と熱を円滑に授受できる
熱媒体の選定も蓄熱材の場合と同様な選定要素を勘案す
る必要がある。
[0010] The temperature of a waste heat source such as waste incineration waste heat or boiler waste heat that requires heat recovery is relatively high, and often exceeds at least 150 ° C. In order to effectively absorb heat from these waste heat sources and store the heat, it is most preferable to use a heat storage material that undergoes a phase transition near the heat source temperature and absorbs a large enthalpy change. Further, even for the purpose of storing late-night power or surplus power as a heat source, it is more efficient to carry out at a moderately high temperature because the volume of the heat storage tank is small. In addition to the first condition, heat cycle stability, thermal conductivity, price, toxicity, safety against explosion fire, corrosiveness, etc. of the heat storage material are taken into consideration, and a device that responds to morphological changes before and after melting of the heat storage material A configuration needs to be devised. Then, it is necessary to consider the same selection factors as in the case of the heat storage material in the selection of the heat medium that can smoothly transfer heat to and from the heat storage body thus devised.

【0011】本発明者等は、各種の蓄熱材を検討した結
果、本発明の目的に適うには、高密度エチレンを蓄熱材
に用い、プロピレングリコールを熱媒体として用いる組
み合わせが最もよいことを見出した。しかも、高密度ポ
リエチレンは後記するように、適切な選別が施されてい
れば、廃プラスチックスの利用が可能であり、資源の有
効利用にもなる。
As a result of studying various heat storage materials, the present inventors have found that a combination of using high-density ethylene as the heat storage material and propylene glycol as the heat medium is the best for the purpose of the present invention. It was Moreover, as will be described later, if the high-density polyethylene is properly sorted, the waste plastics can be used and the resources can be effectively used.

【0012】本発明に使用する高密度ポリエチレンは密
度が0.94〜0.97g/ccの範囲であり、チーグ
ラー・ナッタ系の触媒で重合された、結晶性の高いポリ
エチレンであって、その融点は約120℃と好ましい高
さであり、その溶融潜熱は約50kcal/kgの大き
さを持っている。また、毒性、腐食性はなく、適切な酸
化防止措置さえあれば、ヒートサイクルに対する安定性
は良好である。
The high-density polyethylene used in the present invention has a density in the range of 0.94 to 0.97 g / cc and is a highly crystalline polyethylene polymerized with a Ziegler-Natta type catalyst and has a melting point of Has a preferable height of about 120 ° C., and its latent heat of fusion has a magnitude of about 50 kcal / kg. In addition, it is not toxic and corrosive, and it has good stability against heat cycles as long as it has appropriate antioxidant measures.

【0013】そして、溶融後は当然流体となるので、高
密度ポリエチレンを容器に収納して用いる。容器の材質
は特に問わないが、少なくとも200℃以上の温度に耐
え、熱媒体に侵食されない材質である必要がある。通常
金属が適当であり、好ましくは防錆性の金属板を溶接な
どの加工で缶体に加工して用いる。
Since it naturally becomes a fluid after it is melted, high-density polyethylene is stored in a container for use. The material of the container is not particularly limited, but it must be a material that can withstand a temperature of at least 200 ° C. or higher and is not corroded by the heat medium. Usually, a metal is suitable, and preferably, a rust-preventive metal plate is processed into a can body by a process such as welding and used.

【0014】容器即ち蓄熱体の形状及び蓄熱槽内での配
置方法は限定されないが、充分な伝熱面積が確保され、
熱媒体の循環が出来るようにするのが必要である。更
に、外部の熱源による加熱、蓄熱槽からの吸熱の手段が
可能なように構成されねばならない。
Although the shape of the container, that is, the heat storage body and the arrangement method in the heat storage tank are not limited, a sufficient heat transfer area is secured,
It is necessary to allow circulation of the heat medium. Further, it must be constructed so that it can be heated by an external heat source and absorb heat from the heat storage tank.

【0015】なお、蓄熱槽内に熱媒体として収容される
プロピレングリコールは、外部とは連絡のない収容のし
かたである自然対流方式と、外部と連絡のある強制循環
方式がある。
The propylene glycol stored as a heat medium in the heat storage tank is classified into a natural convection system, which is a communication method without communication with the outside, and a forced circulation system, which is connected with the outside.

【0016】更に本発明の温蓄熱装置は、前記蓄熱槽が
内部に厚板形状の前記潜熱蓄熱体の複数枚を等間隔に配
置し、それにより形成される内部空間に前記熱媒体を満
たしてなることを特徴とする。
Further, in the heat storage apparatus of the present invention, the heat storage tank has a plurality of thick plate-shaped latent heat storage bodies arranged at equal intervals therein, and an internal space formed by the heat storage tank is filled with the heat medium. It is characterized by

【0017】即ち、薄い箱型の容器を作成し、これに高
密度ポリエチレンを充填して厚板状の潜熱蓄熱体とす
る。
That is, a thin box-shaped container is prepared and filled with high density polyethylene to form a thick latent heat storage body.

【0018】更に本発明の温蓄熱装置は、前記蓄熱槽が
内部に肉厚中空円筒形状の前記潜熱蓄熱体の複数個を同
軸に配置し、それにより形成される内部空間に熱媒体を
満たしてなることを特徴とする。
Further, in the heat storage device of the present invention, the heat storage tank has a plurality of the hollow hollow cylindrical heat storage units coaxially arranged therein, and an internal space formed thereby is filled with a heat medium. It is characterized by

【0019】即ち、蓄熱体を同心円状に配置する構成で
あり、蓄熱槽を円筒型にする場合有用な構成である。こ
の場合の蓄熱体間距離においても、前記同様である。
That is, the heat storage bodies are arranged concentrically, which is useful when the heat storage tank is of a cylindrical type. The same applies to the distance between the heat storage bodies in this case.

【0020】更に本発明の温蓄熱装置は、前記蓄熱槽が
直方体であって、該直方体の方形断面を碁盤目状の隔壁
で仕切って形成される複数の室を、交互に前記潜熱蓄熱
材の容器とし、前記潜熱蓄熱材を収納し、別の室内に前
記熱媒体を満たしてなることを特徴とする。
Further, in the heat storage device of the present invention, the heat storage tank is a rectangular parallelepiped, and a plurality of chambers formed by partitioning a rectangular cross section of the rectangular parallelepiped by a grid-like partition are alternately formed of the latent heat storage material. A container is provided, which contains the latent heat storage material, and is filled with the heat medium in another chamber.

【0021】なお、前記で説明した、先ず所望形状の容
器を作成して該容器中にポリエチレンを充填した構成に
限らず、例えば、所望形状の蓄熱体にポリエチレンを成
形加工し、しかる後に被覆をした構成も、形状によって
は可能であり、本発明の機能を果たしさえすれば差し支
えない。
It is to be noted that, as described above, the container of a desired shape is first prepared, and the container is not filled with polyethylene. For example, a heat storage material of a desired shape is molded with polyethylene and then covered. The configuration described above is also possible depending on the shape, and is sufficient as long as the function of the present invention is fulfilled.

【0022】更に本発明の温蓄熱装置は、前記加熱手段
が電気ヒーターであることを特徴とする。
Further, the heat storage apparatus of the present invention is characterized in that the heating means is an electric heater.

【0023】また、本発明の温蓄熱装置は、前記電気ヒ
ーターが、廃熱により蓄熱槽中の熱媒体を加熱する予備
蓄熱を行ったのち、蓄熱温度の調整を行う調整手段であ
ることを特徴とする。
Further, in the heat storage apparatus of the present invention, the electric heater is an adjusting means for adjusting the heat storage temperature after performing preliminary heat storage for heating the heat medium in the heat storage tank with waste heat. And

【0024】蓄熱すべき熱源が、深夜電力及び補助熱源
としての廃熱の場合であり、電気ヒータを(伝熱壁を介
して)蓄熱槽内部熱媒体内に挿入して、加熱手段とす
る。
In the case where the heat source to be stored heat is the midnight power and the waste heat as the auxiliary heat source, an electric heater is inserted into the heat storage tank internal heat medium (via the heat transfer wall) to serve as a heating means.

【0025】更に本発明の温蓄熱装置は、前記加熱手段
が加熱側熱交換手段であることを特徴とする。
Further, the heat storage device of the present invention is characterized in that the heating means is a heating side heat exchange means.

【0026】この場合二つの方式が可能であり、その一
つは蓄熱槽と外部の熱交換器との連絡手段を設け、本発
明の熱媒体であるプロピレングリコールを強制循環し、
外部の熱交換器で熱源と本発明の熱媒体との熱交換を行
って加熱する方式である。前記連絡手段は例えば管路
と、開閉弁と循環ポンプなどで形成される。
In this case, two methods are possible, one of which is provided with a means for connecting a heat storage tank and an external heat exchanger, and forcibly circulates propylene glycol, which is the heat medium of the present invention,
This is a method of heating by exchanging heat between the heat source and the heat medium of the present invention by an external heat exchanger. The communication means is formed of, for example, a pipe line, an opening / closing valve, a circulation pump, and the like.

【0027】他の一つは、本発明の熱媒体であるプロピ
レングリコールは蓄熱槽に封じおいて自然対流型の熱媒
体として機能させ、蓄熱槽内に外部と連絡手段を持つ別
の伝熱面を備え、外部から該連絡手段を通じて、熱源流
体そのものを流通させ若しくは、熱源流体と熱交換した
二次熱媒を流通させて、本発明の熱媒体との熱交換を行
って加熱する方式である。やはり、前記連絡手段は例え
ば管路と、開閉弁と循環ポンプなどで形成される。
The other one is that propylene glycol, which is the heat medium of the present invention, is sealed in a heat storage tank to function as a natural convection type heat medium, and another heat transfer surface having a means for communicating with the outside in the heat storage tank. And a heat source fluid itself is circulated from the outside through the communication means, or a secondary heat medium that has exchanged heat with the heat source fluid is circulated, and heat is exchanged with the heat medium of the present invention for heating. . Again, the connecting means is formed by, for example, a pipe line, an on-off valve, a circulation pump, and the like.

【0028】蓄熱槽から吸熱して熱を回収する側の熱交
換手段も加熱側同様二つの方式が可能であり、その一つ
は蓄熱槽と外部の熱交換器との連絡手段を設け、本発明
の熱媒体であるプロピレングリコールを強制循環し、外
部の熱交換器で回収熱量の利用側と熱交換して、吸熱す
る方式である。
The heat exchange means on the side for absorbing heat from the heat storage tank to recover the heat can also be of two types as on the heating side, one of which is to provide a communication means between the heat storage tank and an external heat exchanger. This is a system in which propylene glycol, which is the heat medium of the invention, is forcedly circulated, and heat is exchanged with the user side of the recovered heat quantity by an external heat exchanger to absorb heat.

【0029】他の一つは、本発明の熱媒体であるプロピ
レングリコールは蓄熱槽に封じおいて自然対流型の熱媒
体として機能させ、蓄熱槽内に外部と連絡手段を持つ別
の伝熱面を備え、外部から該連絡手段を通じて、利用側
の熱供給すべき流体そのものを流通させ若しくは、利用
側と熱交換した二次熱媒を流通させて、本発明の熱媒体
との熱交換を行って加熱する方式である。
The other one is that propylene glycol, which is the heat medium of the present invention, is sealed in a heat storage tank to function as a natural convection type heat medium, and another heat transfer surface having means for communicating with the outside in the heat storage tank. Through the communication means from the outside, the fluid itself to be heat-supplied on the use side is circulated, or the secondary heat medium that has exchanged heat with the user side is circulated to perform heat exchange with the heat medium of the present invention. It is a method of heating.

【0030】更に本発明の温蓄熱装置は、前記蓄熱槽中
の前記潜熱蓄熱材間を満たす前記熱媒体層が少なくとも
3mmを有することを特徴とする。これは本発明者等が
各種検討実験の中で経験的に見出した数値であり、蓄熱
槽内の配置間隔は少なくとも自然対流方式の場合、隣接
間距離を3mm以上保つ必要があるのは、熱媒体の自然
対流現象に関わる蓄熱体壁面での、温度勾配も含めての
総括伝熱係数のなせる業に関連するものと考えられる。
Further, the heat storage device of the present invention is characterized in that the heat medium layer filling the space between the latent heat storage materials in the heat storage tank has at least 3 mm. This is a numerical value that the present inventors have empirically found in various examination experiments. The arrangement interval in the heat storage tank is at least 3 mm or more in the case of the natural convection method. It is considered to be related to the work of making the overall heat transfer coefficient including the temperature gradient on the wall surface of the heat storage body related to the natural convection phenomenon of the medium.

【0031】更に高密度ポリエチレンが廃プラスチック
スであることを特徴とする。これにより廃棄物の再資源
化が促進され、本発明の根底にあるエネルギの有効利用
とともに、資源枯渇、地球温暖化の対策をさらに促進す
る。なお、廃ポリエチレンを利用する際には、特に塩素
含有ポリマーの混入を避けることが肝要である。
Further, the high-density polyethylene is a waste plastic. As a result, the recycling of waste is promoted, and the effective use of energy, which is the basis of the present invention, is further promoted as a measure against resource depletion and global warming. When using waste polyethylene, it is important to avoid mixing chlorine-containing polymers.

【0032】[0032]

【発明の実施の形態】次に図面を参照しつつ、本発明の
実施の形態を例示的に詳述する。ただし、この実施例に
記載されている構成部品の寸法、形状、その相対的位置
等は特に特定的な記載がないかぎりは、この発明の範囲
をそれに限定する趣旨ではなく、単なる説明例にすぎな
い。
Embodiments of the present invention will now be illustratively described in detail with reference to the drawings. However, unless otherwise specified, the dimensions, shapes, relative positions, etc. of the components described in this embodiment are not intended to limit the scope of the present invention thereto, but are merely illustrative examples. Absent.

【0033】[実施例1]図1は本発明の温蓄熱装置の
第1の例の略図である。図1において、15は保温され
た蓄熱槽で、上部と下部に伝熱良好な仕切り板で区分さ
れ、上部は熱交換室14とし、二次熱媒として水を供給
する供給口、及び蓄熱槽から吸熱した高温の水を取り出
す取り出し口を備えている。下部には前記仕切り板か
ら、容器に高密度ポリエリチレンを充填した厚板状蓄熱
体10が複数枚等間隔で下方に延在している。同時に板
状良熱伝導体からなる放熱・吸熱フィン13が複数枚前
記蓄熱体間を下方に延在し熱回収側熱交換手段を構成
し、更に、該蓄熱槽底部付近には加熱手段として電気ヒ
ータ12が装備されている。残りの蓄熱槽下部空間は、
プロピレングリコールからなる熱媒体11で満たされて
いる。
[Embodiment 1] FIG. 1 is a schematic view of a first example of a heat storage apparatus of the present invention. In FIG. 1, reference numeral 15 is a heat storage tank that is kept warm, and is divided into upper and lower partition plates with good heat transfer. The upper part is a heat exchange chamber 14, a supply port for supplying water as a secondary heat medium, and a heat storage tank. It is equipped with a take-out port for taking out high-temperature water that has absorbed heat from. In the lower part, a plurality of thick plate-shaped heat storage bodies 10 in which a container is filled with high-density polyerythrylene extend downward from the partition plate at equal intervals. At the same time, a plurality of heat-dissipating / heat-absorbing fins 13 made of a good plate-shaped heat conductor extend downwardly between the heat storage bodies to form a heat recovery side heat exchange means, and further near the bottom of the heat storage tank, an electric means as heating means The heater 12 is equipped. The space under the remaining heat storage tank is
It is filled with a heat medium 11 made of propylene glycol.

【0034】電気ヒータ12を加熱手段として用い、深
夜電力により蓄熱槽内熱媒体11を150℃以上の所定
温度に加熱した。それにより蓄熱体の高密度ポリエチレ
ンを溶融し、溶融熱として蓄熱した。なお、当然なが
ら、熱媒体及び蓄熱体の顕熱分も貯えられている。昼間
になって、ポンプPを稼動して調節弁16を調節しつ
つ、二次熱媒体としての熱回収前の水17(約25℃)
を熱交換室14に導入し、約50℃の温水(熱回収後水
18)を得た。なお、二次熱媒体は水に限らず、熱利用
側の事情によって、適宜変更ができる。
The electric heater 12 was used as a heating means, and the heat medium 11 in the heat storage tank was heated to a predetermined temperature of 150 ° C. or higher by the midnight power. Thereby, the high-density polyethylene of the heat storage body was melted and stored as the heat of fusion. Of course, the sensible heat of the heat medium and the heat storage body is also stored. During the daytime, the pump P is operated to adjust the control valve 16, and the water 17 (about 25 ° C.) before heat recovery as the secondary heat medium is adjusted.
Was introduced into the heat exchange chamber 14 to obtain hot water of about 50 ° C. (water 18 after heat recovery). The secondary heat medium is not limited to water, but can be changed appropriately depending on the circumstances of the heat utilization side.

【0035】[実施例2]図2は本発明の温蓄熱装置の
第2の例の略図である。本例は実施例1の構成を基本
に、更に熱交換手段の伝熱面積及び総括伝熱係数を改善
したものである。図2において、Aは本発明の温蓄熱装
置の第2の例の立面図、Bは平面図、CはA−A’矢視
図である。図において、他の図と共通の部材、部品には
同じ記号を付してある。本例では、熱交換室14が隔壁
21で区分され、Aにおいて手前、即ちBにおいては下
方(Cにおいては左方)の室に水(二次熱媒体)17が
流入し、熱交換パイプへの開口22(複数)からパイプ
20(複数)を通過し、Aにおいて向こう、即ちBにお
いては上方(Cにおいては右方)の室に熱交換パイプへ
の開口22(複数)から流出し、熱回収後水(二次熱媒
体)18として熱が得られるよう構成されている。
[Embodiment 2] FIG. 2 is a schematic view of a second example of the heat storage apparatus of the present invention. This example is based on the configuration of the first embodiment and further improves the heat transfer area and the overall heat transfer coefficient of the heat exchange means. In FIG. 2, A is an elevation view of a second example of the heat storage apparatus of the present invention, B is a plan view, and C is a view taken along the line AA ′. In the drawings, members and parts common to other drawings are given the same symbols. In this example, the heat exchange chamber 14 is divided by the partition wall 21, and the water (secondary heat medium) 17 flows into the front chamber in A, that is, the lower chamber in B (the left side in C), and flows into the heat exchange pipe. From the openings 22 to the heat exchange pipe, passing through the pipes 20 from the openings 22 to the other side at A, that is, in the upper chamber in B (to the right in C). After recovery, heat is obtained as water (secondary heat medium) 18.

【0036】即ち、実施例1のフィンに変わって、仕切
り板からは、熱交換パイプが下垂して蛇行し、二次熱媒
体が流通するようになっている。更に、パイプ間にはパ
イプ間フィン23を設けて伝熱面積を増やしている。な
お、熱交換手段の諸元はすべて実施例1と同一である。
That is, instead of the fins of the first embodiment, the heat exchange pipe hangs down from the partition plate and meanders so that the secondary heat medium flows. Further, inter-pipe fins 23 are provided between the pipes to increase the heat transfer area. The specifications of the heat exchange means are all the same as in the first embodiment.

【0037】本装置で、電気ヒータ12を加熱手段とし
て用い、深夜電力により蓄熱槽内熱媒体11を150℃
以上の所定温度に加熱した。それにより蓄熱体の高密度
ポリエチレンを溶融し、溶融熱として蓄熱した。なお、
当然ながら、熱媒体及び蓄熱体の顕熱分も貯えられてい
る。昼間になって、ポンプPを稼動して調節弁16を調
節して流速を実施例1と同じにしつつ、二次熱媒体とし
ての熱回収前の水17(約25℃)を熱交換室14に導
入し、約80℃の温水(熱回収後水18)を得た。な
お、この場合も、二次熱媒体は水に限らず、熱利用側の
事情によって、適宜変更ができる。
In this apparatus, the electric heater 12 is used as a heating means, and the heat medium 11 in the heat storage tank is heated to 150 ° C. by the midnight power.
It was heated to the above predetermined temperature. Thereby, the high-density polyethylene of the heat storage body was melted and stored as the heat of fusion. In addition,
Of course, the sensible heat of the heat medium and the heat storage body is also stored. In the daytime, the pump P is operated to adjust the control valve 16 to make the flow rate the same as in Example 1, while the water 17 (about 25 ° C.) before heat recovery as the secondary heat medium is exchanged with the heat exchange chamber 14. To obtain hot water of about 80 ° C. (water 18 after heat recovery). In this case as well, the secondary heat medium is not limited to water, but can be appropriately changed depending on the circumstances of the heat utilization side.

【0038】[実施例3]図3は本発明の温蓄熱装置の
第3の例の概念図であって、蓄熱槽に熱を付与、若しく
は吸収する本発明の熱交換手段の変化について説明した
図である。
[Embodiment 3] FIG. 3 is a conceptual diagram of a third example of the heat storage apparatus of the present invention. The change of the heat exchange means of the present invention for applying or absorbing heat to the heat storage tank has been described. It is a figure.

【0039】図3において(A)は、蓄熱槽内に伝熱壁
を熱媒体内に浸漬した一つの加熱側熱回収側兼用熱交換
手段31を備えており、11はプロピレングリコールか
らなる熱媒体、10は高密度ポリエチレンからなる蓄熱
体、15は蓄熱槽である。先ず蓄熱プロセスではバルブ
32の切り換えにより加熱源流体33のみが加熱側熱回
収側兼用熱交換手段31に流れるようにして、それによ
り熱媒体11を蓄熱体10の溶融温度以上に加熱する。
取り出しプロセスでは、バルブ32の切り換えにより熱
回収源流体34のみが該加熱側熱回収側兼用熱交換手段
31に流れるようにして、それにより蓄熱体10等の熱
を熱媒体11から取り出す。
In FIG. 3, (A) is provided with one heating-side heat-recovery-side heat exchange means 31 in which a heat transfer wall is immersed in a heat medium in a heat storage tank, and 11 is a heat medium made of propylene glycol. 10 is a heat storage body made of high-density polyethylene, and 15 is a heat storage tank. First, in the heat storage process, by switching the valve 32, only the heating source fluid 33 is caused to flow to the heating side heat recovery side / heat exchange means 31, thereby heating the heat medium 11 to a temperature above the melting temperature of the heat storage body 10.
In the take-out process, by switching the valve 32, only the heat recovery source fluid 34 is caused to flow to the heating side heat recovery side combined heat exchange means 31, whereby the heat of the heat storage body 10 and the like is taken out from the heat medium 11.

【0040】図3において(B)は、蓄熱槽内に伝熱壁
を熱媒体内に浸漬した一対の加熱側交換手段37と熱回
収用熱交換器38を備えており、同じく11はプロピレ
ングリコールからなる熱媒体、10は高密度ポリエチレ
ンからなる蓄熱体、15は蓄熱槽である。蓄熱プロセス
では加熱源流体33を加熱側交換手段37に流して、そ
れにより熱媒体を蓄熱体10の溶融温度以上に加熱す
る。取り出しプロセスでは、熱回収源流体34を熱回収
用熱交換器38に流して、それにより蓄熱体10等の熱
を熱媒体11から取り出す。
In FIG. 3, (B) is provided with a pair of heating side exchange means 37 in which a heat transfer wall is immersed in a heat medium and a heat recovery heat exchanger 38 in the heat storage tank, and 11 is also propylene glycol. Is a heat medium, 10 is a heat storage body made of high-density polyethylene, and 15 is a heat storage tank. In the heat storage process, the heating source fluid 33 is caused to flow through the heating side exchange means 37, thereby heating the heat medium to the melting temperature of the heat storage body 10 or higher. In the extraction process, the heat recovery source fluid 34 is caused to flow through the heat recovery heat exchanger 38, and thereby the heat of the heat storage body 10 or the like is extracted from the heat medium 11.

【0041】図3において(C)は、蓄熱槽内に伝熱壁
を熱媒体内に浸漬した一対の加熱側交換手段37と熱回
収用熱交換器38を備えており、更に加熱側熱交換手段
37と管路で接続された、加熱側二次熱交換手段39
と、熱回収用熱交換器38と管路で接続された、熱回収
側二次熱交換手段40とを備えている。前記同様、11
はプロピレングリコールからなる熱媒体、10は高密度
ポリエチレンからなる蓄熱体、15は蓄熱槽である。ま
た、35は二次熱媒体であり、36は35と同じ若しく
は別の二次熱媒体である。蓄熱プロセス、取り出しプロ
セスともこの場合は間接的に熱交換器39、40を介し
て蓄熱、取り出しを行う。加熱源流体33若しくは熱回
収源流体34が腐食性などの理由で、直接蓄熱槽15に
通したくないない場合に適切な構成である。
In FIG. 3, (C) is provided with a pair of heating side exchange means 37 in which a heat transfer wall is immersed in a heat medium and a heat recovery heat exchanger 38 in the heat storage tank, and further heat side heat exchange. Heating-side secondary heat exchange means 39 connected by pipe 37 to the means 37
And a heat recovery side secondary heat exchange means 40 connected to the heat recovery heat exchanger 38 by a pipe line. 11 as above
Is a heat medium made of propylene glycol, 10 is a heat storage body made of high-density polyethylene, and 15 is a heat storage tank. Further, 35 is a secondary heat medium, and 36 is the same or different secondary heat medium as 35. In both the heat storage process and the take-out process, in this case, heat is indirectly stored and taken out via the heat exchangers 39 and 40. This configuration is suitable when the heating source fluid 33 or the heat recovery source fluid 34 does not want to directly pass through the heat storage tank 15 due to reasons such as corrosiveness.

【0042】[実施例4]図4は本発明の温蓄熱装置の
第4の例の略図であって、蓄熱体の形体の変化について
説明したものである。
[Embodiment 4] FIG. 4 is a schematic view of a fourth embodiment of the heat storage apparatus of the present invention, which illustrates changes in the shape of the heat storage body.

【0043】図において(A)は厚板状の蓄熱体10を
複数枚等間隔で蓄熱槽15内に配置して、熱媒体11を
満たしたもので、実施例1、2の場合に相当する。
In the figure, (A) shows a case in which a plurality of thick plate-shaped heat storage bodies 10 are arranged in the heat storage tank 15 at equal intervals and filled with the heat medium 11, which corresponds to the case of the first and second embodiments. .

【0044】図において(B)は肉厚円筒状の蓄熱体1
0を複数個同軸に円筒状蓄熱槽15内に配置して、熱媒
体11を満たしたものである。
In the figure, (B) is a thick-walled cylindrical heat storage body 1.
A plurality of 0s are coaxially arranged in the cylindrical heat storage tank 15 to fill the heat medium 11.

【0045】図において(C)は直方体の蓄熱槽15の
断面碁盤目状に、縦方向の隔壁で仕切り、これにより形
成される室に、図のように交互に蓄熱材である高密度ポ
リエチレンを充填して蓄熱体10とし別の室にプロピレ
ングリコールの熱媒体11を満たして蓄熱槽15を構成
したものである。
In the figure, (C) is a rectangular parallelepiped heat storage tank 15 having a cross-sectional cross-section and is partitioned by vertical partition walls, and in the chamber formed by this, high density polyethylene as a heat storage material is alternately provided as shown in the figure. A heat storage body 10 is filled with the heat storage body 10 by filling a separate chamber with a heat medium 11 of propylene glycol.

【0046】[0046]

【発明の効果】以上説明したように、本発明により、高
密度ポリエチレンを蓄熱材とし、該蓄熱材のエンタルピ
変化を授受可能なプロピレングリコールを熱媒体として
用い、廃熱の回収若しくは深夜電力の有効利用などを可
能とする温蓄熱装置の提供を可能とした。
As described above, according to the present invention, high-density polyethylene is used as a heat storage material, and propylene glycol capable of exchanging the enthalpy change of the heat storage material is used as a heat medium. It has become possible to provide a heat storage device that can be used.

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

【図1】 本発明の温蓄熱装置の第1の例の略図であ
る。
FIG. 1 is a schematic view of a first example of a heat storage device of the present invention.

【図2】 本発明の温蓄熱装置の第2の例の略図であ
る。
FIG. 2 is a schematic view of a second example of the heat storage device of the present invention.

【図3】 本発明の温蓄熱装置の第3の例の概念図であ
る。
FIG. 3 is a conceptual diagram of a third example of the heat storage device of the present invention.

【図4】 本発明の温蓄熱装置の第4の例の略図であ
る。
FIG. 4 is a schematic view of a fourth example of the heat storage device of the present invention.

【符号の説明】[Explanation of symbols]

10 蓄熱体(高密度ポリエチレン) 11 熱媒体(プロピレングリコール) 12 電気ヒータ 13 放熱・吸熱フィン 14 熱交換室 15 蓄熱槽 16 調節弁 17 熱回収前水(二次熱媒体) 18 熱回収後水(二次熱媒体) 20 熱交換パイプ 21 熱交換室仕切り 22 熱交換パイプへの開口 23 パイプ間フィン 31 加熱側熱回収側兼用熱交換手段 32 切り換え兼調節バルブ 33 加熱源流体 34 熱回収源流体 35 加熱側二次熱媒体 36 熱回収側二次熱媒体 37 加熱側熱交換手段 38 熱回収用熱交換器 39 加熱側二次熱交換手段 40 熱回収側二次熱交換手段 10 Heat storage (high density polyethylene) 11 Heat medium (propylene glycol) 12 Electric heater 13 Heat dissipation / heat absorption fins 14 heat exchange room 15 heat storage tank 16 Control valve 17 Water before heat recovery (secondary heat medium) 18 Water after heat recovery (secondary heat medium) 20 heat exchange pipes 21 heat exchange room partition 22 Opening to heat exchange pipe 23 Fins between pipes 31 Heat exchange means for heating side and heat recovery side 32 Switching and adjusting valve 33 Heat source fluid 34 Heat recovery source fluid 35 Secondary heating medium on heating side 36 Heat Recovery Side Secondary Heat Medium 37 Heating side heat exchange means 38 Heat Recovery Heat Exchanger 39 Heating side secondary heat exchange means 40 Heat recovery side secondary heat exchange means

フロントページの続き (72)発明者 峯浦 潔 東京都江東区牡丹2丁目13番1号 株式会 社前川製作所内 (72)発明者 金井 延王 東京都江東区牡丹2丁目13番1号 株式会 社前川製作所内 (72)発明者 町田 明登 東京都江東区牡丹2丁目13番1号 株式会 社前川製作所内 (72)発明者 稲葉 英男 岡山県岡山市津島中1丁目3番1―404号Continued front page    (72) Inventor Kiyoshi Minoura             2-13-1, Peony, Koto-ku, Tokyo Stock market             Shamaegawa Works (72) Inventor Kanou Nobuo             2-13-1, Peony, Koto-ku, Tokyo Stock market             Shamaegawa Works (72) Inventor Akito Machida             2-13-1, Peony, Koto-ku, Tokyo Stock market             Shamaegawa Works (72) Inventor Hideo Inaba             1-3-1, Tsushimachu, Okayama City, Okayama Prefecture

Claims (11)

【特許請求の範囲】[Claims] 【請求項1】 潜熱蓄熱材として高密度ポリエチレンを
容器に収納してなる潜熱蓄熱体と、熱媒体としてプロピ
レングリコールとを収容する蓄熱槽と、蓄熱槽中の熱媒
体を加熱する加熱手段と該熱媒体から熱回収を行う熱回
収用熱交換器とを備え、加熱手段より与えられた熱量を
蓄熱し、熱回収用熱交換器より回収するよう構成したこ
とを特徴とする温蓄熱装置。
1. A latent heat storage body containing high-density polyethylene as a latent heat storage material in a container, a heat storage tank containing propylene glycol as a heat medium, and heating means for heating the heat medium in the heat storage tank. A heat storage device comprising: a heat recovery heat exchanger that recovers heat from a heat medium, and configured to store the amount of heat given by a heating means and recover the heat from the heat recovery heat exchanger.
【請求項2】 前記蓄熱槽内に熱媒体として収容される
プロピレングリコールが、外部とは連絡のない収容のし
かたである自然対流方式若しくは外部と連絡のある強制
循環方式であることを特徴とする請求項1記載の温蓄熱
装置。
2. The propylene glycol housed as a heat medium in the heat storage tank is of a natural convection system, which is a method of storage that does not communicate with the outside, or a forced circulation system, which communicates with the outside. The heat storage device according to claim 1.
【請求項3】 前記蓄熱槽が内部に高密度ポリエチレン
を容器に収納してなる厚板形状の前記潜熱蓄熱体の複数
枚を等間隔に配置し、それにより形成される内部空間に
前記熱媒体を満たしてなることを特徴とする請求項1記
載の温蓄熱装置。
3. A plurality of thick plate-shaped latent heat storage bodies, each having a high-density polyethylene contained in a container, are arranged at equal intervals in the heat storage tank, and the heat medium is formed in an internal space formed by the heat storage bodies. The heat storage device according to claim 1, characterized in that
【請求項4】 前記蓄熱槽が内部に高密度ポリエチレン
を容器に収納してなる肉厚中空円筒形状の前記潜熱蓄熱
体の複数個を同軸に配置し、それにより形成される内部
空間に前記熱媒体を満たしてなることを特徴とする請求
項1記載の温蓄熱装置。
4. A plurality of the above-mentioned latent heat storage bodies having a thick hollow cylindrical shape, in which the high-density polyethylene is housed in a container, are arranged coaxially in the heat storage tank, and the heat is stored in an internal space formed thereby. The heat storage device according to claim 1, wherein the heat storage device is filled with a medium.
【請求項5】 前記蓄熱槽が直方体であって、該直方体
の方形断面を碁盤目状の隔壁で仕切って形成される複数
の室を、交互に前記潜熱蓄熱材の容器とし、高密度ポリ
エチレンからなる前記潜熱蓄熱材を収納し、別の室内に
前記熱媒体を満たしてなることを特徴とする請求項1記
載の温蓄熱装置。
5. The heat storage tank is a rectangular parallelepiped, and a plurality of chambers formed by partitioning a rectangular cross section of the rectangular parallelepiped with a grid-like partition are alternately used as the latent heat storage material containers, and are made of high-density polyethylene. The heat storage device according to claim 1, wherein the latent heat storage material is stored and the heat medium is filled in another room.
【請求項6】 潜熱蓄熱材として中密度ポリエチレン、
低密度ポリエチレン、ポリプロピレンからなる群から選
ばれる少なくとも一つの高分子化合物を容器に収納して
なる潜熱蓄熱体と、熱媒体として鉱油、廃油、動植物
油、重油からなる群から選ばれる少なくとも一つの液体
とを収容する蓄熱槽と、蓄熱槽中の熱媒体を加熱する加
熱手段と該熱媒体から熱回収を行う熱回収用熱交換器と
を備え、加熱手段より与えられた熱量を蓄熱し、熱回収
用熱交換器より回収するよう構成したことを特徴とする
温蓄熱装置。
6. A medium density polyethylene as a latent heat storage material,
Low-density polyethylene, latent heat storage material containing at least one polymer compound selected from the group consisting of polypropylene in a container, and at least one liquid selected from the group consisting of mineral oil, waste oil, animal and vegetable oils, heavy oil as a heat medium. And a heat storage tank that accommodates, a heating unit that heats the heat medium in the heat storage tank, and a heat recovery heat exchanger that recovers heat from the heat medium, and stores the amount of heat given by the heating unit. A heat storage device characterized in that it is configured to be recovered from a recovery heat exchanger.
【請求項7】 前記加熱手段が電気ヒーターであること
を特徴とする請求項1記載の温蓄熱装置。
7. The heat storage device according to claim 1, wherein the heating means is an electric heater.
【請求項8】 前記電気ヒーターが、廃熱により蓄熱槽
中の熱媒体を加熱する予備蓄熱を行ったのち、蓄熱温度
の調整を行う調整手段であることを特徴とする請求項7
記載の温蓄熱装置。
8. The electric heater is adjusting means for adjusting the heat storage temperature after performing preliminary heat storage for heating the heat medium in the heat storage tank with waste heat.
The heat storage device described.
【請求項9】 前記加熱手段が加熱側熱交換手段である
ことを特徴とする請求項1記載の温蓄熱装置。
9. The heat storage device according to claim 1, wherein the heating means is a heating side heat exchange means.
【請求項10】 前記蓄熱槽中の前記潜熱蓄熱材間を満
たす前記熱媒体層が少なくとも3mmを有することを特
徴とする請求項2乃至4何れかの項記載の温蓄熱装置。
10. The heat storage device according to claim 2, wherein the heat medium layer that fills the space between the latent heat storage materials in the heat storage tank has at least 3 mm.
【請求項11】 高密度ポリエチレンが廃プラスチック
スであることを特徴とする請求項1記載の温蓄熱装置。
11. The heat storage device according to claim 1, wherein the high-density polyethylene is waste plastics.
JP2001325275A 2001-10-23 2001-10-23 Thermal storage device Expired - Fee Related JP3873229B2 (en)

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JP2010127505A (en) * 2008-11-26 2010-06-10 Keio Gijuku Method of forming hydrate, heat storage material and heat storage device
JP2011038750A (en) * 2009-08-18 2011-02-24 Ngk Insulators Ltd Honeycomb type latent-heat heat reservoir
KR101185449B1 (en) 2010-07-23 2012-10-02 삼성중공업 주식회사 Heat exchanger
JP2012530642A (en) * 2009-06-25 2012-12-06 リ−テック・バッテリー・ゲーエムベーハー Vehicle having drive device
CN105222345A (en) * 2015-10-27 2016-01-06 江苏启能新能源材料有限公司 A kind of phase-change heat-storage material heating system
CN109631127A (en) * 2018-12-06 2019-04-16 天津大学 A kind of phase change thermal storage heat exchanger

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