JPH06313688A - Heat storage system - Google Patents

Heat storage system

Info

Publication number
JPH06313688A
JPH06313688A JP5101252A JP10125293A JPH06313688A JP H06313688 A JPH06313688 A JP H06313688A JP 5101252 A JP5101252 A JP 5101252A JP 10125293 A JP10125293 A JP 10125293A JP H06313688 A JPH06313688 A JP H06313688A
Authority
JP
Japan
Prior art keywords
heat storage
heat
storage system
latent
pump
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP5101252A
Other languages
Japanese (ja)
Inventor
Masasuke Tsukamoto
政介 塚本
Masashi Urano
雅司 浦野
Toshinao Tsutsui
利尚 筒井
Shigeru Douno
茂 堂埜
Toshiki Tamura
俊樹 田村
Noriyuki Kitachi
範行 北地
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.)
Panasonic Electric Works Co Ltd
Original Assignee
Matsushita Electric Works Ltd
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 Matsushita Electric Works Ltd filed Critical Matsushita Electric Works Ltd
Priority to JP5101252A priority Critical patent/JPH06313688A/en
Publication of JPH06313688A publication Critical patent/JPH06313688A/en
Pending legal-status Critical Current

Links

Classifications

    • 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

Abstract

PURPOSE:To provide a heat storage system in which latent heat storage material to be used can be reemulsified in the system for storing heat or transferring heat by using the material using latent heat generated by state change. CONSTITUTION:A heat storage system comprises a heat storage tank 1 having emulsion emulsified from a dispersive state of higher melting point than that of continuous state in the continuous state as latent heat storage material 2, a stirrer for stirring the material 2, a heat exchanger 5 by a heat pump 4 as a heat storage heat source, a tube 8 for circulating via a heat dissipating fan coil 7 and a conveying pump 6 as a heat dissipating mechanism, and a tube 9 for circulating to an emulsifier 10 for reemulsifying the separated latent heat storage material 2.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、相変化に伴って発生す
る潜熱を利用した潜熱蓄熱材を用いて蓄熱または熱搬送
する蓄熱システムの、当該潜熱蓄熱材の再乳化機構に関
する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a re-emulsification mechanism for a latent heat storage material in a heat storage system that stores or transfers heat using a latent heat storage material that utilizes latent heat generated by a phase change.

【0002】この蓄熱システムは空調システム等として
利用されている。
This heat storage system is used as an air conditioning system or the like.

【0003】[0003]

【従来の技術】従来のPCMを用いた蓄熱システムは、
潜熱蓄熱材の分散相成分の再乳化のシステムや、潜熱蓄
熱材自体の破壊を防ぐシステムは付加されていなかっ
た。
2. Description of the Related Art A conventional PCM-based heat storage system is
A system for re-emulsifying the dispersed phase components of the latent heat storage material and a system for preventing the destruction of the latent heat storage material itself were not added.

【0004】[0004]

【発明が解決しようとする課題】上記従来のものは分散
相材の凝固による蓄熱を繰り返すことで潜熱蓄熱材の乳
化皮膜の破壊が起こり、分散相の相分離が起こる場合に
分離状態を再生させる機能がなく、熱交換性能の低下
や、分散相の露出による材料の危険物化の問題があっ
た。
SUMMARY OF THE INVENTION In the above-mentioned prior art, when the heat storage due to the solidification of the dispersed phase material is repeated, the emulsion film of the latent heat storage material is destroyed and the separated state is regenerated when the phase separation of the dispersed phase occurs. There was no function, and there was a problem that the heat exchange performance deteriorated and the material became a hazardous material due to the exposure of the dispersed phase.

【0005】本発明は上記事由に鑑みてなしたものでそ
の目的とするところは潜熱蓄熱材の乳化状態を安定化
し、熱交換性能の安定化を図り、材料の危険物化を防ぐ
ことを目的とする。
The present invention has been made in view of the above circumstances, and its purpose is to stabilize the emulsified state of the latent heat storage material, to stabilize the heat exchange performance, and to prevent the material from becoming a hazardous material. To do.

【0006】[0006]

【課題を解決する手段】連続相にこの連続相より融点の
高い分散相を乳化させたエマルジョンの潜熱蓄熱材2と
して有している蓄熱槽1と、この潜熱蓄熱材2の撹拌用
スターラー3と、蓄熱用熱源7としてのヒートポンプ4
による熱交換器5と、放熱機構として放熱用ファンコイ
ル及び搬送用ポンプ6を循環させる配管8と、分離した
潜熱蓄熱材2を再乳化する乳化装置10に循環させる配
管9とで構成させる蓄熱システム。
A heat storage tank 1 having a latent heat storage material 2 of an emulsion obtained by emulsifying a dispersed phase having a higher melting point than the continuous phase in a continuous phase, and a stirrer 3 for stirring the latent heat storage material 2. , Heat pump 4 as heat source 7 for heat storage
A heat storage system constituted by a heat exchanger 5 according to the above, a pipe 8 for circulating a heat radiation fan coil and a transfer pump 6 as a heat radiation mechanism, and a pipe 9 for circulating the separated latent heat storage material 2 to an emulsification device 10 for re-emulsification. .

【0007】[0007]

【作 用】本発明は、ヒートポンプ4により蓄熱された
蓄熱槽1内の潜熱蓄熱材2が、放熱用配管8を通って放
熱する過程で、蓄放冷の繰り返しにより分離した潜熱蓄
熱材を蓄熱槽上部等に吸い込口を持つ配管9にて乳化装
置10へと搬送し、分散槽を微粒化することにより再乳
化を行い安定分散状態を得る。
[Operation] In the present invention, the latent heat storage material 2 stored in the heat storage tank 1 that has been stored by the heat pump 4 radiates heat through the heat radiating pipe 8, and the latent heat storage material separated by repeated storage and cooling is stored. It is conveyed to the emulsification device 10 through a pipe 9 having a suction port at the upper part of the tank or the like and re-emulsified by atomizing the dispersion tank to obtain a stable dispersion state.

【0008】一般に分離した分散相は比重が水より軽い
ため蓄熱槽1上部で層を形成する。蓄熱層1上部より乳
化装置10へ搬送された分散相材を微粒化する際温度条
件によって粒径が変化するが、当該システムでは通常使
用界面剤の溶解状態が得られる温度に潜熱蓄熱材の温度
を調節し、際乳化を行うものである。
In general, the separated dispersed phase has a specific gravity lighter than that of water, and thus forms a layer above the heat storage tank 1. When atomizing the dispersed phase material conveyed from the upper part of the heat storage layer 1 to the emulsification device 10, the particle size changes depending on the temperature condition. Is to be emulsified.

【0009】[0009]

【実施例】以下、本件出願に係る発明の実施例を図に基
づいて説明する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the invention according to the present application will be described below with reference to the drawings.

【0010】エマルジョンの潜熱蓄熱材2は、分散相の
融点が連続相の融点よりも高いものである。
In the latent heat storage material 2 of emulsion, the melting point of the dispersed phase is higher than the melting point of the continuous phase.

【0011】蓄熱槽1内にある潜熱蓄熱材2をスターラ
ー3により撹拌しながら、ヒートポンプ4を有する熱交
換器5にて蓄熱し、搬送用ポンプ6にて放熱用ファンコ
イル7へ送り潜熱利用し、利用後配管8を通り潜熱蓄熱
材2を循環させる。
While stirring the latent heat storage material 2 in the heat storage tank 1 with the stirrer 3, the heat exchanger 5 having the heat pump 4 stores heat, and the transfer pump 6 sends it to the fan coil 7 for radiating heat to utilize the latent heat. After use, the latent heat storage material 2 is circulated through the pipe 8.

【0012】当該サイクルの繰り返しにより分離した分
散相材を配管9にて乳化装置10へ搬送し、際乳化を行
い蓄熱槽1へ戻す。
The dispersed phase material separated by repeating the cycle is conveyed to the emulsifying device 10 through the pipe 9 and emulsified again to be returned to the heat storage tank 1.

【0013】図1に示す実施例の乳化装置10はギヤポ
ンプもしくはマグネットポンプであり、当該ポンプのせ
ん断応力により分離した分散相材の微粒化を図るもので
ある。
The emulsifying apparatus 10 of the embodiment shown in FIG. 1 is a gear pump or a magnet pump, which is intended to atomize the dispersed phase material separated by the shear stress of the pump.

【0014】図2に示す実施例の乳化装置10はホモジ
ナイザーもしくはホモミキサーであり、配管9には搬送
用ポンプ11が取り付けられる。
The emulsifying apparatus 10 of the embodiment shown in FIG. 2 is a homogenizer or a homomixer, and a pipe 9 is provided with a transfer pump 11.

【0015】図3は本件出願に係るの発明の更に他の実
施例である。この図に基づき発明を開示していく。
FIG. 3 shows still another embodiment of the invention according to the present application. The invention will be disclosed based on this figure.

【0016】2はエマルジョンの潜熱蓄熱材である。こ
れは、結晶性の直鎖アルキルハイドロカーボン、高級脂
肪酸、高級脂肪酸エステル、高級脂肪族アルコール等の
結晶性有機化合物(パラフィン)が界面活性剤によって
連続相たる水中に分散相として分散されてなるエマルジ
ョンの潜熱蓄熱材2で、分散相の融点は連続相の融点よ
りも高いものであり、パラフィンの含有率は40〜50
重量%が適当なものである。これ以上の含有率になると
粘性が上がり流動性に支障をきたすからである。
Reference numeral 2 is an emulsion latent heat storage material. This is an emulsion obtained by dispersing crystalline organic compounds (paraffins) such as crystalline linear alkyl hydrocarbons, higher fatty acids, higher fatty acid esters, and higher aliphatic alcohols in a continuous phase of water as a dispersed phase by a surfactant. In the latent heat storage material 2 of No. 3, the melting point of the dispersed phase is higher than that of the continuous phase, and the paraffin content is 40 to 50.
Weight percent is suitable. This is because if the content is higher than this, the viscosity increases and the fluidity is impaired.

【0017】21はエマルジョンの潜熱蓄熱材2の分離
層で熱的・機械的シェアにより分散状態を保持してきた
界面活性剤の核がはずれパラフィン層が浮遊したもので
ある。分離がひどくなると完全にパラフィン層だけが析
出し透明な層となる。
Reference numeral 21 is a separation layer of the latent heat storage material 2 of the emulsion, in which the core of the surfactant which has maintained the dispersed state by thermal / mechanical shear is released and the paraffin layer is suspended. When the separation is severe, only the paraffin layer is completely deposited and becomes a transparent layer.

【0018】1は蓄熱槽で、3LDK家屋の熱負荷とし
て、40〜50重量%のエマルジョンの潜熱蓄熱材2で
600リッター程度のものである。
A heat storage tank 1 is a latent heat storage material 2 of emulsion of 40 to 50% by weight, which is about 600 liters as a heat load of a 3LDK house.

【0019】蓄熱槽1の形状としては蓄熱時の均一かつ
効率的な熱交換を実現するため縦型円筒形が望ましい。
形状が円筒形であれば内部のエマルジョンの潜熱蓄熱材
2の流動が均一になり、蓄熱ムラがなくなるだけでなく
過蓄熱による熱的シェアが原因のエマルジョン分離も少
なくなるからである。
The shape of the heat storage tank 1 is preferably a vertical cylindrical shape in order to realize uniform and efficient heat exchange during heat storage.
This is because if the shape is cylindrical, the flow of the latent heat storage material 2 of the emulsion inside becomes uniform, the uneven heat storage is eliminated, and the emulsion separation due to the thermal share due to excessive heat storage is reduced.

【0020】4は加熱・冷却装置で、蓄熱槽1内に熱交
換器5を設置し熱交換するヒートポンプが用いられてい
る。更に昇温時エマルジョンの潜熱蓄熱材2を50°C
以上に蓄熱する場合は他のヒーター(図示略)も兼用さ
れる。
Reference numeral 4 denotes a heating / cooling device, which is provided with a heat exchanger 5 in the heat storage tank 1 and uses a heat pump for exchanging heat. When the temperature is raised, the latent heat storage material 2 of the emulsion is heated to 50 ° C.
When the heat is stored above, another heater (not shown) is also used.

【0021】3はスターラーである。スターラー3を蓄
熱のために蓄熱槽1内のエマルジョンの潜熱蓄熱材2の
流動の目的のみで使用するならば、600リッアースケ
ールの蓄熱槽1で回転数70〜100rpm、羽根の枚
数2枚、羽根の長さは、タンク円筒径の約2分の1が賞
用される。
Reference numeral 3 is a stirrer. If the stirrer 3 is used only for the purpose of flowing the latent heat storage material 2 of the emulsion in the heat storage tank 1 for heat storage, the rotation speed is 70 to 100 rpm and the number of blades is 2 in the 600 ria scale heat storage tank 1. About half the diameter of the tank cylinder is used as the blade length.

【0022】蓄熱された潜熱蓄熱材2は搬送ポンプ6で
放熱用ファンコイル7へ搬送される。もちろん搬送に関
しては、潜熱蓄熱材2を直接搬送せず、蓄熱槽1内で2
次熱媒体(水・ブライン等)と熱交換し2次媒体を端末
へ搬送するようにしてもよい。以上説明した部位に関し
ては従来からあるものと同じである。
The latent heat storage material 2 in which the heat is stored is transported by the transport pump 6 to the fan coil 7 for heat radiation. Regarding transportation, of course, the latent heat storage material 2 is not directly transported,
You may make it heat-exchange with a secondary heat medium (water, brine, etc.), and may convey a secondary medium to a terminal. The parts described above are the same as those conventionally used.

【0023】部位9、11、12、13で構成されるの
がこの実施例の要部をなす乳化装置である。
It is the emulsifying device that is the main part of this embodiment that is composed of the parts 9, 11, 12, and 13.

【0024】蓄熱槽1内で分離した潜熱蓄熱材2はその
上部に分離層21となって表れる。配管9はポンプ11
によって分離エマルジョンをバッファータンク12へ送
るためのものであるから蓄熱槽1内のエマルジョン液面
近傍に設置するのが望ましい。
The latent heat storage material 2 separated in the heat storage tank 1 appears as a separation layer 21 on the upper part thereof. Piping 9 is pump 11
Since it is for sending the separated emulsion to the buffer tank 12, it is desirable to install it in the vicinity of the emulsion liquid level in the heat storage tank 1.

【0025】12は分離槽21をためこむバッファータ
ンクである。バッファータンク12の形状・材質は蓄熱
槽1と同じで大きさは蓄熱槽1の600リッターに対し
て10リッター程のものが使用される。
Reference numeral 12 is a buffer tank for accommodating the separation tank 21. The shape and material of the buffer tank 12 are the same as those of the heat storage tank 1, and the size of the buffer tank 12 is about 10 liters with respect to 600 liters of the heat storage tank 1.

【0026】バッファータンク12に蓄えられた分離エ
マルジョンは加熱装置22で昇温され撹拌装置13で高
速撹拌される。加熱装置22としては70°C レベルま
での昇温なので電気ヒーターの使用が適当であろう。
The separated emulsion stored in the buffer tank 12 is heated by the heating device 22 and is rapidly stirred by the stirring device 13. As the heating device 22, it is appropriate to use an electric heater because the temperature rises to 70 ° C level.

【0027】撹拌装置13はエマルジョンの再分散が目
的であるので撹拌装置3とは仕様が異なる。モーターの
回転数は200rpm前後、羽根の枚数も10リッター
レベルのタンクでは4枚程必要となる。
The stirrer 13 has a specification different from that of the stirrer 3 because the purpose is to redisperse the emulsion. The rotation speed of the motor is around 200 rpm, and the number of blades is about 4 in a tank of 10 liter level.

【0028】また撹拌装置13としてはスターラーモー
ターを使用せず、ホモジナイザー等の分散専用機械を用
いてもよい。再分散が終了したバッファータンク12で
はエマルジョンの潜熱蓄熱材2を戻し配管9を経由して
蓄熱槽1へと戻す。
As the stirring device 13, a stirrer motor may not be used, but a dispersion-dedicated machine such as a homogenizer may be used. In the buffer tank 12 where the redispersion is completed, the latent heat storage material 2 of the emulsion is returned to the heat storage tank 1 via the return pipe 9.

【0029】[0029]

【発明の効果】本発明によれば蓄放冷を繰り返しても分
離した材料を再乳化することができるので、熱交換性能
が安定する。
According to the present invention, the separated material can be re-emulsified even after repeated storage and cooling, so that the heat exchange performance becomes stable.

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

【図 1】本発明の蓄熱システムの一実施例を示す概略
図。
FIG. 1 is a schematic diagram showing an embodiment of a heat storage system of the present invention.

【図 2】本発明の蓄熱システムの異なる実施例を示す
概略図。
FIG. 2 is a schematic view showing another embodiment of the heat storage system of the present invention.

【図 3】本発明の蓄熱システムのさらに異なる実施例
を示す概略図。
FIG. 3 is a schematic view showing still another embodiment of the heat storage system of the present invention.

【符号の説明】[Explanation of symbols]

1 蓄熱槽 2 潜熱蓄熱材 3 スターラー 4 ヒートポンプ 5 蓄熱用熱交換器 6 搬送用ポンプ 7 放熱用ファンコイル 8 配管 9 配管 10 乳化装置 11 ポンプ 1 Heat Storage Tank 2 Latent Heat Storage Material 3 Stirrer 4 Heat Pump 5 Heat Storage Heat Exchanger 6 Transport Pump 7 Heat Dissipating Fan Coil 8 Piping 9 Piping 10 Emulsifier 11 Pump

─────────────────────────────────────────────────────
─────────────────────────────────────────────────── ───

【手続補正書】[Procedure amendment]

【提出日】平成6年1月10日[Submission date] January 10, 1994

【手続補正1】[Procedure Amendment 1]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0008[Correction target item name] 0008

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0008】一般に分離した分散相は比重が水より軽い
ため蓄熱槽1上部で層を形成する。蓄熱1上部より乳
化装置10へ搬送された分散相材を微粒化する際温度条
件によって粒径が変化するが、当該システムでは通常使
用界面剤の溶解状態が得られる温度に潜熱蓄熱材の温度
を調節し、乳化を行うものである。
In general, the separated dispersed phase has a specific gravity lighter than that of water, and thus forms a layer above the heat storage tank 1. When the dispersed phase material conveyed from the upper part of the heat storage tank 1 to the emulsification device 10 is atomized, the particle size changes depending on the temperature condition. Is adjusted and re- emulsification is performed.

【手続補正2】[Procedure Amendment 2]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0012[Correction target item name] 0012

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0012】当該サイクルの繰り返しにより分離した分
散相材を配管9にて乳化装置10へ搬送し、乳化を行
い蓄熱槽1へ戻す。
The dispersed phase material separated by repeating the cycle is conveyed to the emulsification device 10 through the pipe 9, re- emulsified and returned to the heat storage tank 1.

【手続補正3】[Procedure 3]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0015[Name of item to be corrected] 0015

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0015】図3は本件出願に係る発明の更に他の実施
例である。この図に基づき発明を開示していく。
[0015] FIG. 3 is a further embodiment of the engagement Ru inventions in the present application. The invention will be disclosed based on this figure.

【手続補正3】[Procedure 3]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0015[Name of item to be corrected] 0015

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0015】図3は本件出願に係る発明の更に他の実施
例である。この図に基づき発明を開示していく。
[0015] FIG. 3 is a further embodiment of the engagement Ru inventions in the present application. The invention will be disclosed based on this figure.

【手続補正4】[Procedure amendment 4]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0017[Correction target item name] 0017

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0017】21はエマルジョンの潜熱蓄熱材2の分離
層で、蓄熱および放熱の繰り返し並びに機械的シェアに
より分散状態を保持してきた界面活性剤がはずれパラフ
ィン層が浮遊したものである。分離がひどくなると完全
にパラフィン層だけが析出し透明な層となる。
Reference numeral 21 is a separation layer of the latent heat storage material 2 of the emulsion, which is a layer in which the surface active agent which has maintained the dispersed state due to repeated heat storage and heat release and mechanical shear is removed and the paraffin layer floats. When the separation is severe, only the paraffin layer is completely deposited and becomes a transparent layer.

【手続補正5】[Procedure Amendment 5]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0019[Correction target item name] 0019

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0019】蓄熱槽1の形状としては蓄熱時の均一かつ
効率的な熱交換を実現するため縦型円筒形が望ましい。
形状が円筒形であれば内部のエマルジョンの潜熱蓄熱材
2の流動が均一になり、蓄熱ムラがなくなるだけでなく
過蓄熱による界面活性剤機構の破壊が原因のエマルジョ
ン分離も少なくなるからである。
The shape of the heat storage tank 1 is preferably a vertical cylindrical shape in order to realize uniform and efficient heat exchange during heat storage.
This is because if the shape is cylindrical, the flow of the latent heat storage material 2 of the emulsion inside becomes uniform, the uneven heat storage is eliminated, and the emulsion separation due to the destruction of the surfactant mechanism due to excessive heat storage is reduced.

【手続補正6】[Procedure correction 6]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0021[Correction target item name] 0021

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0021】3はスターラーである。スターラー3を蓄
熱のために蓄熱槽1内のエマルジョンの潜熱蓄熱材2の
流動の目的のみで使用するならば、600リッースケ
ールの蓄熱槽1で回転数70〜100rpm、羽根の枚
数2枚、羽根の長さは、タンク円筒径の約2分の1が使
用される。
Reference numeral 3 is a stirrer. If you use the stirrer 3 purposes only flow of latent heat storage material 2 emulsion in the heat storage tank 1 for heat storage, the rotational speed 70~100Rpm, 2 sheets number of blades in 600 liter te scale of the heat storage tank 1, the length of the blade is about one-half of the tank cylinder diameter is used <br/>.

【手続補正7】[Procedure Amendment 7]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0029[Name of item to be corrected] 0029

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0029】本発明によれば蓄放冷を繰り返しても分離
した材料を再乳化することができるので、分離層の露出
による材料の危険物化を防ぐとともに熱交換性能が安定
する。
According to the present invention, the separated material can be re-emulsified even after repeated storage and cooling, so that the separation layer is exposed.
This prevents the material from becoming a hazardous material and stabilizes the heat exchange performance.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 堂埜 茂 大阪府門真市大字門真1048番地松下電工株 式会社内 (72)発明者 田村 俊樹 大阪府門真市大字門真1048番地松下電工株 式会社内 (72)発明者 北地 範行 大阪府門真市大字門真1048番地松下電工株 式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Shigeru Dono, 1048, Kadoma, Kadoma, Osaka Prefecture, Matsushita Electric Works Co., Ltd. (72) Toshiki Tamura, 1048, Kadoma, Kadoma, Osaka Prefecture 72) Inventor Noriyuki Kitachi 1048, Kadoma, Kadoma City, Osaka Prefecture Matsushita Electric Works Co., Ltd.

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 連続相にこの連続相より融点の高い分散
相を乳化させたエマルジョンの潜熱蓄熱材2として有し
ている蓄熱槽1と、この潜熱蓄熱材2の撹拌用スターラ
ー3と、蓄熱用熱源としてのヒートポンプ4による熱交
換器5と、放熱機構として放熱用ファンコイル7及び搬
送用ポンプ6を循環させる配管8と、分離した潜熱蓄熱
材2を再乳化する乳化装置10に循環させる配管9とで
構成される蓄熱システム。
1. A heat storage tank 1 having a latent heat storage material 2 of an emulsion obtained by emulsifying a disperse phase having a melting point higher than that of the continuous phase, a stirrer 3 for stirring the latent heat storage material 2, and heat storage. A heat exchanger 5 using a heat pump 4 as a heat source for heat supply, a pipe 8 for circulating a fan coil 7 for heat radiation and a pump 6 for transportation as a heat radiation mechanism, and a pipe for circulating the separated latent heat storage material 2 to an emulsifying device 10 for re-emulsifying. Heat storage system consisting of 9 and.
【請求項2】 乳化装置10としてギャポンプを用いた
請求項1記載の蓄熱システム。
2. The heat storage system according to claim 1, wherein a gas pump is used as the emulsifying device 10.
【請求項3】 乳化装置10としてマグネットポンプを
用いた請求項1記載の蓄熱システム。
3. The heat storage system according to claim 1, wherein a magnet pump is used as the emulsifying device 10.
【請求項4】 乳化装置10としてホモジナイザーを用
いた請求項1記載の蓄熱システム。
4. The heat storage system according to claim 1, wherein a homogenizer is used as the emulsifying device 10.
【請求項5】 乳化装置10としてホモミキサーを用い
た請求項1記載の蓄熱システム。
5. The heat storage system according to claim 1, wherein a homomixer is used as the emulsifying device 10.
【請求項6】 乳化装置10として撹拌装置13及び加
熱装置22を用いた請求項1記載の蓄熱システム。
6. The heat storage system according to claim 1, wherein a stirring device 13 and a heating device 22 are used as the emulsifying device 10.
JP5101252A 1993-04-27 1993-04-27 Heat storage system Pending JPH06313688A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5101252A JPH06313688A (en) 1993-04-27 1993-04-27 Heat storage system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5101252A JPH06313688A (en) 1993-04-27 1993-04-27 Heat storage system

Publications (1)

Publication Number Publication Date
JPH06313688A true JPH06313688A (en) 1994-11-08

Family

ID=14295730

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5101252A Pending JPH06313688A (en) 1993-04-27 1993-04-27 Heat storage system

Country Status (1)

Country Link
JP (1) JPH06313688A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003091356A1 (en) * 2002-04-26 2003-11-06 Nippon Shokubai Co., Ltd. Heat storage medium, process for producing heat storage medium and heat storage system including heat storage medium
JP2004198022A (en) * 2002-12-18 2004-07-15 Ishikawajima Harima Heavy Ind Co Ltd Middle temperature exhaust heat recovery system
JP2005172342A (en) * 2003-12-10 2005-06-30 Kitakyushu Foundation For The Advancement Of Industry Science & Technology Heat exchanging system and heat exchanging method using heat storage material
KR101650325B1 (en) * 2015-02-24 2016-08-24 한국기계연구원 Boiling Apparatus using reciprocating motion device
JP6818942B1 (en) * 2019-10-18 2021-01-27 三菱電機株式会社 Heat storage type water heater

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003091356A1 (en) * 2002-04-26 2003-11-06 Nippon Shokubai Co., Ltd. Heat storage medium, process for producing heat storage medium and heat storage system including heat storage medium
JP2004198022A (en) * 2002-12-18 2004-07-15 Ishikawajima Harima Heavy Ind Co Ltd Middle temperature exhaust heat recovery system
JP2005172342A (en) * 2003-12-10 2005-06-30 Kitakyushu Foundation For The Advancement Of Industry Science & Technology Heat exchanging system and heat exchanging method using heat storage material
KR101650325B1 (en) * 2015-02-24 2016-08-24 한국기계연구원 Boiling Apparatus using reciprocating motion device
JP6818942B1 (en) * 2019-10-18 2021-01-27 三菱電機株式会社 Heat storage type water heater
WO2021075040A1 (en) * 2019-10-18 2021-04-22 三菱電機株式会社 Heat storage type water heater

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