JPH0438998B2 - - Google Patents

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Publication number
JPH0438998B2
JPH0438998B2 JP60172545A JP17254585A JPH0438998B2 JP H0438998 B2 JPH0438998 B2 JP H0438998B2 JP 60172545 A JP60172545 A JP 60172545A JP 17254585 A JP17254585 A JP 17254585A JP H0438998 B2 JPH0438998 B2 JP H0438998B2
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Japan
Prior art keywords
heat
heat storage
filling
material system
molten
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JPS6152588A (en
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    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K5/00Heat-transfer, heat-exchange or heat-storage materials, e.g. refrigerants; Materials for the production of heat or cold by chemical reactions other than by combustion
    • C09K5/02Materials undergoing a change of physical state when used
    • C09K5/06Materials undergoing a change of physical state when used the change of state being from liquid to solid or vice versa
    • C09K5/063Materials absorbing or liberating heat during crystallisation; Heat storage materials
    • 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
    • F28D20/025Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using latent heat the latent heat storage material being in direct contact with a heat-exchange medium or with another heat storage material
    • 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

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Thermal Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Materials Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Central Heating Systems (AREA)
  • Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
  • Structure Of Emergency Protection For Nuclear Reactors (AREA)
  • Thermotherapy And Cooling Therapy Devices (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
  • Investigating Or Analyzing Materials Using Thermal Means (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

〔発明の利用分野〕 非分解溶融物質を有する潜熱式蓄熱装置は、通
常のエネルギ発生系の負荷を軽減又は補足し、エ
ネルギ発生量とエネルギ需要量間の時間変動を調
節する有効な系である。 従つて、この発明による潜熱式蓄熱装置は、特
に熱消費系をエネルギ源によつて定まる熱量の利
用条件に合わせるため、即ち熱の発生量と熱の需
要量とを時間的に調節するため、及び蓄熱するた
めに使用される。 〔従来技術の解決策の特徴〕 通常の蓄熱装置は、主として検出できる熱に基
づいて動作する。 これに利用する水、油、岩石、鋳鉄、マグネサ
イト、土壌等のような蓄熱材料は何れも熱容量が
少ないので、このような蓄熱系を採用すると、特
に大きな熱量を蓄熱する際、異常に大きな蓄熱容
積となり、不経済な浪費状況になる。実際的見地
から、通常の蓄熱系には次の重大な欠点がある。 − 蓄熱装置の蓄熱と放熱は蓄熱温度の上昇又
は低下につながり、蓄熱と放出時に実際には非
常に不利であるが、蓄熱温度と熱伝達効率を常
に変化させ、採用すべき制御技術のコストを増
加させることになる。 − 蓄熱材料に共通する低い熱容量のため、重
量/出力の比が以後に説明する潜熱式蓄熱装置
に比べて非常に不利である。 − 大きな熱量を蓄積することは、大きな蓄熱装
置の容積に結び付き、この容積は今日の技術で
しばしば実現不可能か、あるいは多額の費用を
掛けてのみ実現する(補助建築物の構築)か、
又はコストに非常に不利な影響を与える。 − 蓄熱容積を技術的に実現可能な程度に低減さ
せるには、蓄熱と放熱状態の間の大きな温度差
を許容する必要があり、その場合に必要な蓄熱
温度を必要な熱消費系の運転温度以上に高め、
熱源のエネルギ特質(蓄熱量)を無にすること
を甘受することになる。 − 最も頻繁に利用される蓄熱材料として水を使
用する場合には、特に工業利用に必要な蓄熱温
度が、例えば暖房設備に対して90〜70℃のよう
な温度上限(常圧で約90℃)に位置する場合、
特に多量のエネルギを蓄積することが大切にな
る。水温を上げて蓄熱能力を高めることは、常
圧で不可能で、技術及び装置上の大きな出費に
通じ、そうでなくても不利なコスト状況を更に
悪化させる。 これ等の欠点を克服できる可能性は、検出でき
る熱にあまり基づかず、溶解熱、凝固熱、気化
熱、凝縮熱、反応熱、水和熱、溶解熱、結晶化熱
等のような潜熱に基づいて動作する蓄熱装置によ
つて提供される。 この種の蓄熱装置は文献で「潜熱式蓄熱装置」
と称されている。 これ等の蓄熱装置には、通常の蓄熱装置に比べ
て以下の欠点がある。 − 蓄熱及び放熱を行う場合、蓄熱温度が吸熱又
は放熱中狭い範囲で一定に維持される。 − 熱伝達効率も技術解決策の各々に応じて狭い
範囲で一定に維持される。 − 通常の蓄熱装置に比べて、吸熱能力は使用さ
れる蓄熱材料に応じて、また吸熱と放熱が生じ
る全温度範囲の幅に応じて、2〜40倍大きい。 最も明確な改善は、特に融解熱と凝固熱に基づ
いて動作するような潜熱式蓄熱装置である。この
ような蓄熱装置に対して、溶融性材料を伴い、よ
く知られた熱物理及び物理化学的な問題を排除す
る一連の解決策がある。 これ等の解決策には、西独特許第2648678号、
東独特許第154125号、西独特許第1928694号、西
独特許第2523234号、西独特許第2517920号及び西
独特許第2517921号並びに東独経済特許出願WP
C 09K/243619号明細書が属している。これ等
は蓄熱材料の材質選別、過冷却、層状化等の抑制
に関する改良を開示している。 以下の問題は未だ解決されていない。 非分解溶融する、例えば共晶状態又は定組成状
態の種々の溶融物質は、凝固する時に生じる結晶
が体積の大きい集塊になる傾向、熱の出入りで著
しく低下した熱伝達効率を生じる傾向、被膜形成
を生じる傾向、溶融物の不透過、蓄熱装置内部の
熱応力と圧力上昇が生じる傾向がある。 更に、文献から、弗素を含有する表面活性物質
を添加すると、非定組成状態で溶融したグラウバ
ー塩(Na2SO4・10H2O)が凝固する時に生じる
結晶の大きさを小さくできることが知られてい
る。この対応特許は、米国特許第4267879号明細
書である。 これに反して、分解せずに(例えば定組成)溶
融する蓄熱材料の結晶粒径を小さくする具体的な
解決策は知られていない。Na2S・5H2Oのよう
な定組成溶融する材料への移行は成功していな
い。 〔発明の目的〕 この発明の目的は、機械的手段を使用すること
なく、大容積の集塊、被膜形成及び不透過が生じ
ることを阻止すると同時に、放熱・吸熱効率を高
める非分解溶融物質を有する潜熱式の蓄熱装置を
提供することにある。 〔発明の本質の説明〕 例えば、定組成状態及び共晶状態で溶融する物
質のような非分解溶融物質を有する潜熱式蓄熱装
置は、凝固する時、体積の大きい集塊となる結晶
を形成する傾向がある。このことは、低い放熱・
吸熱効率と蓄熱装置内部の熱応力との原因にな
る。上記難点を抑制するには、この発明により4
種の物質から成る活性蓄熱充填物によつて行われ
る。 物質系 融解熱(又は一般的な変換熱)と顕著な熱容量
により蓄熱特性を示し、非分解溶融し、しかも蓄
熱材料として採用できる一つ又はそれ以上の物質
から成る。 活性蓄熱充填物の全容積での物質系の割合は
この発明では50〜95vol%になる。 物質系 前記物質系が不溶か、あるいはただ制限され
た下で可溶性である一つ又はそれ以上の成分で構
成されている液状の熱媒体から成る。この場合、
物質系の密度(ρII)と物質系の溶融した液
相密度(ρI)とは、この発明により、 ρI≦ρII,例えば0.8ρI, の条件を満たし、物質系の蒸気圧PDIと物質系
の蒸気圧PDIIとはこの発明により、 PDI≪PDII の条件を満たす。物質系の割合は蓄熱装置の活
性蓄熱充填物の全体積に対して5〜50vol%にな
る。 物質系 一つ又はそれ以上の表面活性物質から成る。潜
熱式蓄熱装置の活性蓄熱充填物の全体積に対する
物質系の割合は、0.01〜5vol%になる。物質系
には、物質系が凝固するとき微結晶を形成さ
せず、成長及び被膜形成を防止する役目がある。 物質系 格子構造のため核形成現象を誘起するか、異種
核形成を開始させる一つ又はそれ以上の核形成物
から成る。この発明によれば、潜熱式蓄熱装置の
活性蓄熱充填物の全体積に対する物質系の割合
は0〜20vol%である。 物質系を過冷却又は僅かに過冷却する場合に
は、活性蓄熱充填物に対する物質系の割合は零
になる。 〔実施例〕 この発明による潜熱式蓄熱装置は三種の蓄熱充
填物に対して以下の13種の変形種に基づき説明す
る。
[Field of Application of the Invention] Latent heat storage devices with non-decomposable molten substances are effective systems for relieving or supplementing the load on conventional energy generation systems and adjusting the temporal fluctuations between energy generation and energy demand. . Therefore, the latent heat type heat storage device according to the present invention is particularly designed to adjust the heat consumption system to the usage conditions of the amount of heat determined by the energy source, that is, to temporally adjust the amount of heat generation and the amount of heat demanded. and used to store heat. Characteristics of prior art solutions Typical heat storage devices operate primarily on the basis of detectable heat. The heat storage materials used for this purpose, such as water, oil, rock, cast iron, magnesite, and soil, all have low heat capacity, so if such a heat storage system is used, especially when storing a large amount of heat, an abnormally large amount of heat will be required. This becomes a heat storage volume, resulting in an uneconomical waste situation. From a practical point of view, conventional heat storage systems have the following important drawbacks: − The heat storage and heat dissipation of the heat storage device will lead to the increase or decrease of the heat storage temperature, which is actually very disadvantageous during heat storage and release, but it is possible to constantly change the heat storage temperature and heat transfer efficiency, and reduce the cost of the control technology to be adopted. This will result in an increase. - Due to the low heat capacity common to heat storage materials, the weight/power ratio is very unfavorable compared to the latent heat storage devices described below. - the storage of a large amount of heat is associated with a large volume of the heat storage device, which is often not possible with today's technology or can only be realized at great expense (construction of auxiliary buildings);
or have a very unfavorable cost impact. − In order to reduce the heat storage volume to a technically feasible extent, it is necessary to allow large temperature differences between heat storage and heat dissipation conditions, in which case the required heat storage temperature can be reduced to the required operating temperature of the heat dissipating system. higher than that,
This means that we have to accept that the energy characteristics (heat storage amount) of the heat source are nullified. − When water is used as the most frequently used heat storage material, the storage temperature required for industrial applications in particular must be at an upper temperature limit of 90-70°C for heating equipment (approximately 90°C at normal pressure). ), if
It is particularly important to store large amounts of energy. Increasing the heat storage capacity by increasing the water temperature is not possible at normal pressure and leads to large technical and equipment expenditures, further exacerbating an otherwise disadvantageous cost situation. The possibility of overcoming these drawbacks is based less on detectable heat and more on latent heats such as heat of solution, heat of solidification, heat of vaporization, heat of condensation, heat of reaction, heat of hydration, heat of solution, heat of crystallization, etc. provided by a thermal storage device that operates based on This type of heat storage device is referred to as a "latent heat storage device" in the literature.
It is called. These heat storage devices have the following drawbacks compared to normal heat storage devices. - When performing heat storage and heat dissipation, the heat storage temperature is maintained constant within a narrow range during heat absorption or heat dissipation. − The heat transfer efficiency is also kept constant within a narrow range depending on each technological solution. - Compared to conventional heat storage devices, the heat absorption capacity is 2 to 40 times greater, depending on the heat storage material used and the width of the total temperature range in which heat absorption and heat release occur. The most obvious improvement is in latent heat storage devices, in particular those operating on the basis of the heat of fusion and solidification. There are a range of solutions for such heat storage devices that involve fusible materials and eliminate the well-known thermophysical and physicochemical problems. These solutions include West German Patent No. 2648678,
East German Patent No. 154125, West German Patent No. 1928694, West German Patent No. 2523234, West German Patent No. 2517920 and West German Patent No. 2517921, and East German Economic Patent Application WP
C 09K/243619 belongs to this patent. These disclose improvements regarding selection of heat storage materials, suppression of supercooling, stratification, etc. The following issues are still unresolved. Various molten substances that melt non-decompositionally, e.g. in the eutectic or isocratic state, have a tendency for the crystals formed to form bulky agglomerates when solidified, a tendency to produce significantly reduced heat transfer efficiency as heat enters and exits, and coatings. There is a tendency for formation, impermeability of the melt, thermal stress and pressure build-up inside the heat storage device. Furthermore, it is known from the literature that the addition of fluorine-containing surface-active substances can reduce the size of crystals that form when Glauber's salt (Na 2 SO 4 .10H 2 O) molten in a non-isocratic state solidifies. ing. This corresponding patent is US Pat. No. 4,267,879. On the other hand, there is no known concrete solution for reducing the crystal grain size of a heat storage material that melts without decomposition (eg, isocratic). The transition to isocratic melting materials such as Na 2 S.5H 2 O has not been successful. [Object of the Invention] The object of the present invention is to provide a non-decomposable molten material that prevents large volume agglomerates, film formation and impermeability from occurring, and at the same time increases heat dissipation and heat absorption efficiency, without using mechanical means. An object of the present invention is to provide a latent heat type heat storage device having the following properties. [Description of the essence of the invention] A latent heat storage device having a non-decomposed molten material, such as a material that melts in an isocratic state and a eutectic state, when solidified, forms crystals that form agglomerates with a large volume. Tend. This means low heat dissipation and
This causes heat absorption efficiency and thermal stress inside the heat storage device. In order to suppress the above-mentioned difficulties, this invention provides four
This is done by means of an active heat storage filling consisting of a type of material. Substance system Consists of one or more substances that exhibit heat storage properties due to heat of fusion (or general heat of conversion) and significant heat capacity, are non-decompositionally molten, and can be employed as heat storage materials. The proportion of the material system in the total volume of the active heat storage filling amounts to 50 to 95 vol.% in the present invention. Substance System The substance system consists of a liquid heat transfer medium composed of one or more components which are insoluble or only soluble to a limited extent. in this case,
According to the present invention, the density of the material system (ρ II ) and the density of the molten liquid phase of the material system (ρ I ) satisfy the condition ρ I ≦ρ II , for example, 0.8ρ I , and the vapor pressure P of the material system According to this invention, DI and the vapor pressure P DII of a material system satisfy the condition of P DI <<P DII . The proportion of the material system is between 5 and 50 vol% relative to the total volume of the active heat storage filling of the heat storage device. Material system Consisting of one or more surface-active substances. The proportion of the material system to the total volume of the active heat storage filling of the latent heat storage device is 0.01 to 5 vol%. The material system has the role of preventing the formation of microcrystals and preventing growth and film formation when the material system solidifies. Material system Consists of one or more nucleators that induce nucleation phenomena due to their lattice structure or initiate heterogeneous nucleation. According to the invention, the proportion of the material system to the total volume of the active heat storage fill of the latent heat storage device is 0 to 20 vol%. If the material system is supercooled or slightly supercooled, the ratio of material system to active heat storage filling is zero. [Example] The latent heat type heat storage device according to the present invention will be explained based on the following 13 types of variations of three types of heat storage fillers.

【表】【table】

【表】 これ等の物質系の作用を第1図の基本構造を有
する潜熱式蓄熱装置に基づき説明する。 四つの物質系は熱絶縁された耐圧容器1ちゆに
活性蓄熱充填物の混合物として充填されている。
熱の導入は蓄熱充填物で取り囲まれた熱伝達装置
3を介して行われ、熱の放出は熱伝達媒体の蒸気
に取り囲まれた熱伝達装置4を介して行われる。
熱の出入りは三種の相変換の下に進行する。溶融
温度以上での熱が導入される場合には、物質系
が気化する。物質系の未だ溶融していない物質
に出会うと、この系は凝縮し物質系を溶融させ
る。物質系から出た凝縮熱は物質系によつて
溶融熱として受け取られる。 溶融温度以下で熱を放出する場合には、再び物
質系が気化し、この場合、熱を導入する時より
も低い圧力である。 これに必要な気化熱は蓄熱物質(物質系)か
ら取り出す。この物質はこのとき凝固する。物質
系の蒸気は熱伝達装置4のところで凝縮し、生
じた凝縮熱がこの熱伝達装置によつて受け取られ
る。 熱の伝達は、両方の場合、蓄熱充填物を強力に
混合させて著しい発泡形成の下に進行する。従つ
て、蓄熱物質全体にわたつて一様に分布した熱の
受入と放出が生じる。このそれ自体公知の過程は
非分解溶融物質の場合、物質系の存在しないけ
れば大きな体積の集塊の形成、成長及び層状化の
下に進行する。 物質系を添加すると、上記の状況は防止され
る。発泡形成の強度と物質系の量に応じて、目
の粗い透過性の隙間を蓄熱装置内部に形成する小
さい結晶が生じる。 物質系は、熱を取り出す時、結晶形成を開始
させ、過冷却を防止するために必要である。 他の実施例は、物質系として以下の非分解溶
融物質を用いて実現できる。 −KF・2H2O −Na2S2O3・5H2O −CH3COONa・3H2O 熱を蓄積する物質(物質系)はこの活性蓄熱
充填物の主成分を決定する。物質系の品位は判
定基準条件、 −ρII<ρI −PDI≪PDII −物質が混合しないこと、 に応じて物質系〜を選定するので、特許請求
の範囲に記載した活性蓄熱充填物となる。
[Table] The effects of these material systems will be explained based on a latent heat type heat storage device having the basic structure shown in FIG. The four material systems are filled in a thermally insulated pressure vessel as a mixture with an active heat storage fill.
The introduction of heat takes place via a heat transfer device 3 surrounded by a heat storage filling, and the release of heat takes place via a heat transfer device 4 surrounded by vapor of a heat transfer medium.
Heat transfer proceeds through three types of phase transformations. If heat above the melting temperature is introduced, the material system will vaporize. When it encounters an unmolten substance in a system of matter, the system condenses and melts the system of matter. The heat of condensation released from the material system is received by the material system as heat of fusion. If heat is released below the melting temperature, the material system is vaporized again, in this case at a lower pressure than when the heat is introduced. The heat of vaporization required for this is extracted from the heat storage material (material system). This material then solidifies. The vapor of the material system condenses in the heat transfer device 4, and the resulting heat of condensation is received by this heat transfer device. The heat transfer takes place in both cases with intensive mixing of the heat storage filling and significant foam formation. A uniformly distributed heat reception and release throughout the heat storage material therefore occurs. This process, which is known per se, proceeds in the case of non-decomposed molten substances, with the formation, growth and stratification of large volume agglomerates in the absence of a substance system. Addition of the substance system prevents the above situation. Depending on the intensity of the foam formation and the amount of material system, small crystals form which form coarse permeable gaps inside the heat storage device. A material system is needed to initiate crystal formation and prevent supercooling when heat is extracted. Other embodiments can be realized using the following non-decomposable molten materials as material systems. -KF.2H2O -Na2S2O3.5H2O -CH3COONa.3H2O The heat accumulating substance ( substance system ) determines the main component of this active heat storage filling . The quality of the material system is selected according to the criterion condition: −ρ III −P DI ≪P DII − The substances do not mix, so the active heat storage filling described in the claims becomes.

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

第1図、この発明による一実施例の潜熱式の蓄
熱送致の模式断面図。 図中引用記号:1……容器、2……四種の物質
系を含む充填物、3……熱供給用の熱伝達装置、
4……熱取り出し用の熱伝達装置、5……中空
室。
FIG. 1 is a schematic sectional view of a latent heat type heat storage and transmission according to an embodiment of the present invention. Reference symbols in the figure: 1... Container, 2... Filling containing four types of material systems, 3... Heat transfer device for heat supply,
4... Heat transfer device for heat extraction, 5... Hollow chamber.

Claims (1)

【特許請求の範囲】 1 閉じた蓄熱容器中に非分解溶融物質と混合す
べき活性充填物を有する潜熱式蓄熱装置におい
て、 活性充填物は物質系,,と場合によつて
を保有し、その場合、 − 物質系は、共晶状態又は定組成状態で溶融
し、蓄熱充填物の全体積の50〜95vol%である
一つ又はそれ以上の蓄熱物質から成り、 −物質系は、物質系には溶解しなく、条件 ρII>ρIの溶融相で、 PDI≪PDII を満たし、蓄熱充填物の全体積の3〜50vol%で
ある熱媒体から成り、 − 物質系は、蓄熱充填物の全体積の0.01〜
5vol%である表面活性物質から成り、 − 物質系は、蓄熱充填物の全体積の0〜
20vol%で、物質系が過冷却しない場合には
0vol%である核形成物質である、 ことを特徴とする潜熱式蓄熱装置。
[Scope of Claims] 1. A latent heat storage device having an active filling to be mixed with a non-decomposed molten substance in a closed heat storage container, wherein the active filling has a substance system, and optionally, - the system of matter consists of one or more heat storage substances that are molten in a eutectic or isocratic state and represent 50 to 95 vol% of the total volume of the heat storage filling; does not melt, is in the molten phase with the condition ρ II > ρ I , satisfies P DI ≪ P DII , and consists of a heating medium that is 3 to 50 vol% of the total volume of the heat storage filling, - the material system is the heat storage filling 0.01 of the total volume of
5 vol% of surface-active substances;
At 20vol%, if the material system is not supercooled,
A latent heat type heat storage device characterized in that the nucleation material is 0vol%.
JP60172545A 1984-08-09 1985-08-07 Latent heat accumulator having substance melting without decomposing Granted JPS6152588A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DD28D/266128-6 1984-08-09
DD84266128A DD236862A3 (en) 1984-08-09 1984-08-09 LATE SWAN MEMORY WITH NON-CRUSHING FABRICS

Publications (2)

Publication Number Publication Date
JPS6152588A JPS6152588A (en) 1986-03-15
JPH0438998B2 true JPH0438998B2 (en) 1992-06-26

Family

ID=5559521

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60172545A Granted JPS6152588A (en) 1984-08-09 1985-08-07 Latent heat accumulator having substance melting without decomposing

Country Status (9)

Country Link
JP (1) JPS6152588A (en)
AT (1) AT391555B (en)
BG (1) BG48415A1 (en)
CH (1) CH669206A5 (en)
CS (1) CS497385A1 (en)
DD (1) DD236862A3 (en)
DE (1) DE3521548A1 (en)
HU (1) HU204299B (en)
SE (1) SE463623B (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4042268A1 (en) * 1990-12-31 1992-07-02 Gerd Hoermansdoerfer STORAGE SALT MIXTURES
JP2943609B2 (en) * 1994-06-21 1999-08-30 トヨタ自動車株式会社 Heat storage device
AU7510600A (en) 1999-08-28 2001-03-26 Schumann Sasol Gmbh Latent heat accumulator material
WO2001038453A1 (en) 1999-11-23 2001-05-31 SCHÜMANN SASOL GmbH Dynamic latent heat accumulator
DE102008029972A1 (en) 2008-06-26 2009-12-31 Bayerisches Zentrum für Angewandte Energieforschung e.V. Method for intermixing partially fluid latent heat storage materials in a storage container, comprises introducing gas or gas mixture, which is oxygen free, into the partially fluid latent heat storage materials
DE102010028676A1 (en) 2010-05-06 2011-11-10 Deutsches Zentrum für Luft- und Raumfahrt e.V. Heat receiving, delivering and storing method for latent heat storage, involves transferring energy on fluid to be heated, and conveying solid heat storage medium into solid memory for closing circuit of latent heat storage

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2917192A1 (en) * 1979-04-26 1980-11-06 Kay Laboratories Inc Heat-releasing supercooled melt compsns. - contg. crystallisable material and exsolving liq. additive
US4272392A (en) * 1979-11-02 1981-06-09 The Dow Chemical Company Hydrated Mg(NO3)2 /MgCl2 reversible phase change compositions
CA1160443A (en) * 1980-12-22 1984-01-17 George A. Lane Hydrated mgc1.sub.2 reversible phase change compositions hydrated mg(no.sub.3).sub.2 reversible phase change compositions
JPS58195786A (en) * 1982-05-08 1983-11-15 Matsushita Electric Ind Co Ltd Heat accumulating apparatus of latent heat type
JPS58219395A (en) * 1982-06-15 1983-12-20 Matsushita Electric Ind Co Ltd Heat accumulating apparatus of latent heat type
DD225857A3 (en) * 1982-09-30 1985-08-07 Bauakademie D Ddr Inst Fuer He HOCHLEISTUNGSWAERMESPEICHER

Also Published As

Publication number Publication date
ATA180885A (en) 1990-04-15
DD236862A3 (en) 1986-06-25
SE8503748L (en) 1986-02-10
HU204299B (en) 1991-12-30
DE3521548A1 (en) 1986-02-20
SE8503748D0 (en) 1985-08-08
AT391555B (en) 1990-10-25
JPS6152588A (en) 1986-03-15
CS497385A1 (en) 1987-09-17
CH669206A5 (en) 1989-02-28
HUT42174A (en) 1987-06-29
BG48415A1 (en) 1991-02-15
SE463623B (en) 1990-12-17

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