JPS6037392B2 - Heat storage device that uses fusion enthalpy - Google Patents
Heat storage device that uses fusion enthalpyInfo
- Publication number
- JPS6037392B2 JPS6037392B2 JP52068010A JP6801077A JPS6037392B2 JP S6037392 B2 JPS6037392 B2 JP S6037392B2 JP 52068010 A JP52068010 A JP 52068010A JP 6801077 A JP6801077 A JP 6801077A JP S6037392 B2 JPS6037392 B2 JP S6037392B2
- Authority
- JP
- Japan
- Prior art keywords
- heat storage
- heat
- storage device
- transfer liquid
- storage material
- 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.)
- Expired
Links
- 238000005338 heat storage Methods 0.000 title claims description 126
- 230000004927 fusion Effects 0.000 title description 2
- 239000007788 liquid Substances 0.000 claims description 82
- 239000011232 storage material Substances 0.000 claims description 69
- 230000005484 gravity Effects 0.000 claims description 25
- 239000007787 solid Substances 0.000 claims description 16
- 239000000155 melt Substances 0.000 claims description 6
- 238000010438 heat treatment Methods 0.000 claims description 5
- 239000000463 material Substances 0.000 claims description 5
- 239000000203 mixture Substances 0.000 claims description 5
- 239000013078 crystal Substances 0.000 claims description 4
- 230000002093 peripheral effect Effects 0.000 claims description 4
- 238000000926 separation method Methods 0.000 claims description 4
- 230000007704 transition Effects 0.000 claims description 3
- 238000004891 communication Methods 0.000 claims description 2
- 238000011144 upstream manufacturing Methods 0.000 claims 1
- 150000003839 salts Chemical class 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 230000017525 heat dissipation Effects 0.000 description 3
- 230000001133 acceleration Effects 0.000 description 2
- 229920002545 silicone oil Polymers 0.000 description 2
- 239000012798 spherical particle Substances 0.000 description 2
- RQXXCWHCUOJQGR-UHFFFAOYSA-N 1,1-dichlorohexane Chemical compound CCCCCC(Cl)Cl RQXXCWHCUOJQGR-UHFFFAOYSA-N 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 150000008280 chlorinated hydrocarbons Chemical class 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000005191 phase separation Methods 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D20/00—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00
- F28D20/02—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using latent heat
- F28D20/025—Heat 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
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/14—Thermal energy storage
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E70/00—Other energy conversion or management systems reducing GHG emissions
- Y02E70/30—Systems combining energy storage with energy generation of non-fossil origin
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Central Heating Systems (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Description
【発明の詳細な説明】
本発明は、固体から液体への相転移に際して潜熱を蓄え
る蓄熱材料の入った蓄熱容器と、この蓄えられた熱を放
熱部材に送り込むための熱運搬液体循環回路とを有する
蓄熱器に関する。Detailed Description of the Invention The present invention comprises a heat storage container containing a heat storage material that stores latent heat during phase transition from solid to liquid, and a heat transport liquid circulation circuit for sending the stored heat to a heat radiating member. The present invention relates to a heat storage device having a heat storage device.
固体から液体への相転移に際しての熱を蓄えることので
きる蓄熱材料を用いた篭熱器が幾つか公知である。Several cage heaters are known that use heat storage materials that can store heat during a phase transition from solid to liquid.
これらの蓄熱器から熱が取り出され、その際熱運搬液体
として液体状態の上記蓄熱材料と混ざり合わない液体が
用いられて、これが蓄熱材料を直接通し、次いで放熱部
材を通してポンプ給送される。この場合に下記のような
欠点を示すことが知られている。‘ィ’蓄熱材料とこれ
を通して流れる熱運搬液体との間の熱交換が、凝固した
蓄熱材料の層厚の増大と共に益々困難になる。Heat is extracted from these heat accumulators, using a liquid immiscible with the heat storage material in liquid state as heat transfer liquid, which is pumped directly through the heat storage material and then through the heat dissipation element. In this case, it is known that the following drawbacks are exhibited. Heat exchange between the heat storage material and the heat transfer liquid flowing through it becomes increasingly difficult with increasing layer thickness of the solidified heat storage material.
{口’蓄熱材料の溶融相と凝固相との間の容積の差がそ
の装置部材、即ち蓄熱容器や熱交換器の機械的要求条件
の増大をもたらす。The difference in volume between the molten and solidified phases of the heat storage material results in increased mechanical requirements for its equipment components, ie heat storage vessels and heat exchangers.
し一 蓄熱部材が放熱に際して単一の固形体に凝固し、
これが蓄熱に際して熱伝導に高い熱抵抗をもたらす。1) The heat storage member solidifies into a single solid body during heat dissipation,
This results in high thermal resistance to heat conduction during heat storage.
本発明はこのような欠点を除くことを課題とするもので
ある。The object of the present invention is to eliminate such drawbacks.
本発明はこの課題を、蓄熱材料溶融物と混ざり合わない
か又はほんの僅かしか相港せず、そして比重が蓄熱材料
溶融物の比重と大きく異っていて2層を形成する程であ
るような熱運搬液体を用い、そして熱運搬液体の届中に
ポンプロータ又はミキサーロータが渦流を生ずるように
配置されていて、それにより上記蓄熱材料溶融物と熱運
搬液体との混合物が吸い込まれるようにすることによっ
て解決するものである。これによって、第1にその凝固
した蓄熱材料が極めて微小な粒状に分割され、そして第
2にその蓄熱材料と熱運搬液体との間のより強力な熱交
換が保証される。本発明の第1の実施形態において、熱
運搬液体は蓄熱材料溶融物の上方に存在する。The present invention solves this problem by using a heat storage material that does not mix or only slightly interacts with the heat storage material melt, and whose specific gravity is so different from that of the heat storage material melt that it forms two layers. A heat transfer liquid is used, and a pump rotor or a mixer rotor is arranged to create a vortex flow within the reach of the heat transfer liquid, so that the mixture of the heat storage material melt and the heat transfer liquid is sucked. This can be solved by This firstly divides the solidified heat storage material into extremely fine particles and secondly ensures a stronger heat exchange between the heat storage material and the heat transfer liquid. In a first embodiment of the invention, the heat transfer liquid is present above the heat storage material melt.
第2の実施形態においては蓄熱材料はより比重の重い熱
運搬液体の上方に浮んでいる。上記第1の実施形態の場
合には、蓄熱容器内の上方に、また上記第2の実施形態
の場合には篭熱容器内の下方にポンプo−夕が配置され
ており、これが渦流による液面くぼみをもたらす。第3
の実施形態においては熱運搬液体は蓄熱材料の溶融物と
固体との間に存在し、従ってポンプロータはこれらの蓄
熱材料層の間に配置されている。液状の蓄熱材料はポン
プロータによる渦流くぼみ中に入り込む。ポンプロー外
こよってこの材料は極めて微細な液瓶に分割され、これ
らは表面張力によって球状の形をとり、次いでその熱を
熱運搬液体に伝える。この球状液滴は凝固した後、重力
の加速度及び遠○力によって再び蓄熱材料層中に戻る。
円筒形の誓熱容器の全内容物が旋回流動を行なっている
ので、上記球状粒は特に外側に向って投げ出され、従っ
て渦流つぼみ中に入り込んだ溶融物の全ての部分はこれ
ら球状粒と隔てられている。逆の相分離は、例えば水の
場合のようにその融解物の比重が固体のときよりも重い
蓄熱材料において現われる。蓄熱の際には場合によって
はポンプロ−夕を停めておくことが可能である。In a second embodiment, the heat storage material floats above the heavier heat transfer liquid. In the case of the first embodiment, a pump is disposed above the heat storage container, and in the case of the second embodiment, a pump is disposed below the heat storage container, which causes the liquid to flow through the vortex. It causes a dimpled face. Third
In this embodiment, the heat transfer liquid is present between the melt and the solid heat storage material, and the pump rotor is therefore arranged between these layers of heat storage material. The liquid heat storage material enters into the vortex depression created by the pump rotor. This material is broken up by the pump into extremely fine liquid bottles which, due to surface tension, take on a spherical shape and then transfer their heat to the heat-carrying liquid. After the spherical droplets solidify, they return to the heat storage material layer due to the acceleration of gravity and the far force.
Since the entire contents of the cylindrical thermal vessel are undergoing a swirling flow, the spherical particles are thrown especially towards the outside, so that all the parts of the melt that have entered the swirl buds are separated from these spherical particles. It is being Reverse phase separation occurs in heat storage materials whose melt has a higher specific gravity than when it is a solid, as is the case, for example, with water. In some cases, it is possible to park the pump generator during heat storage.
しかしながらこれは蓄熱の場合にも駆動するのが好まし
い。これは最初充分な蓄熱材料が溶融されたときに熱交
換を促進し、それにより熱異里搬液体と蓄熱材料との間
の温度落差を減少させ、次いで熱運搬液体による蓄熱に
も達し得る。熱連亀磯液体としては例えば水が、また蓄
熱材料としてはワックスが対象となり得る。However, it is preferably also activated in the case of heat storage. This facilitates heat exchange when initially sufficient heat storage material is melted, thereby reducing the temperature drop between the heat transfer liquid and the heat storage material, which can then also reach heat storage by the heat transfer liquid. For example, water can be used as the heat-retaining liquid, and wax can be used as the heat storage material.
しかしながらまたこの発明は溶融塩、就中水和金属塩に
対しても適用することができる。この場合、熱運搬液体
には、上記塩よりも重いものとしては例えば塩素化炭化
水素、または上記塩より軽いものとしては、例えばベン
ジンや軽油のような炭化水素、シリコーン油、ケトン類
、ジクロヘキサン、トルオール或はキシロールを用いる
ことができる。蓄熱材料が水の場合には熱運搬液体とし
てシリコーン油があげられよう。ポンプランナーは渦流
を発生させる。However, the invention can also be applied to molten salts, especially hydrated metal salts. In this case, the heat transfer liquid may be heavier than the above salt, such as chlorinated hydrocarbons, or lighter than the above salt, such as hydrocarbons such as benzene or light oil, silicone oil, ketones, dichlorohexane, etc. , toluene or xylol can be used. When the heat storage material is water, silicone oil may be used as the heat transfer liquid. The pump runner generates a vortex.
これはその上に、吸い込んだ蓄熱材料の機械的な細分割
の作用をもたらす。更にこれはまたその蓄熱容器の内容
物を旋回流動させる働きをする。この旋回流動作用は熱
運搬液体の外部熱交換循環回路からの帰還流を切線方向
から導入することによって補助することができ、それに
より固体状蓄熱材料、液状篭熱材料、及び熱運搬液体の
遠心力場に於ける分離が起り、それより中心軸の部分に
おいて蓄熱材料が外部熱交換循環回路中に一緒に送り込
まれるのを防止する。オーバヘッドリザーバ又は柔軟材
料よりなる容積補償体を熱運搬液体と蓮通させることに
よって容積の補償が行われる。This additionally results in a mechanical subdivision of the sucked-in heat storage material. Furthermore, it also serves to swirl the contents of the storage vessel. This swirling flow effect can be assisted by tangentially introducing a return flow from the external heat exchange circuit of the heat transfer liquid, thereby centrifuging the solid heat storage material, the liquid cage heat material, and the heat transfer liquid. Separation in the force field takes place, thereby preventing the heat storage material in the region of the central shaft from being co-fed into the external heat exchange circuit. Volume compensation is achieved by placing an overhead reservoir or a volume compensator of flexible material in communication with the heat transfer liquid.
以下に本発明を添付図に示した若干の実施例の参照のも
とに更に詳細に説明する。The invention will be explained in more detail below with reference to some embodiments shown in the accompanying drawings.
第1及び2図は比重の軽い熱運搬液体を用いる一つの実
施形態を表わし、第3図は比重の重い熱運搬液体を用い
る場合を示す。1 and 2 depict one embodiment using a heat transfer liquid with a light specific gravity, and FIG. 3 shows the case where a heat transfer liquid with a high specific gravity is used.
第4図はポンプロータの一例を示す。第1図は本発明に
従う篭熱器の一具体例を示すもので、蓄熱容器1は円錐
状に僅かに拡がっていて、輸送上の理由から設置場所で
粗立てることのできるセクションla乃至lcよりなっ
ている。FIG. 4 shows an example of a pump rotor. FIG. 1 shows a specific example of a basket heat device according to the present invention, in which the heat storage container 1 has a slightly expanded conical shape and has sections la to lc that can be roughly erected at the installation site for transportation reasons. It has become.
この篭熱容器のカバー2にモーター3が配直されていて
、これがポンプロータ4を駆動する。このロータは部分
的に渦巻状ハウジング5によって取囲まれておりこれが
導管7を介して熱交換器7aに導く。畜熱容器1の底に
スパイラル状管7bが配置されていてこれが下向きに開
いた多数の管7cを有し、これらを通して熱運搬液体が
再び蓄熱容器中に送りもどされる。空間6a中に比重の
軽い熱運搬液体が存在し、空間6b中に蓄熱材料溶融物
が、また空間6c中に固体の蓄熱材料が存在する。関口
7cは若し管7bが厳密に水平面7d内にあるときは蓄
熱材料溶融物の管7b中への流入を阻止する。比較的長
時間の冷却期間の後に蓄熱材料6b及び6cが凝固して
一つの固形体になってしまっているときは、蓄熱容器1
の下方部分における上記熱交換器7aにより加温された
熱運搬液体の静過圧が上記圃形体をこれが完成に溶融さ
れてしまうまで持ち上げて熱運搬液体がこれを迂回して
流れるような作用をもたらす。これに対して短時間の放
熱に際しては均一固形体は全く形成されず、蓄熱材料の
結晶と溶融物との混合物が生じ、これはこれらの比重の
差に基づき上記閉口7cから流入する熱運搬液体の流れ
によって貫流される。この蓄熱材料の固体と溶融物との
比重差は、充満して場合により外気と運通している膜体
8によって補償される。循環回路9は例えば太陽熱コレ
クター又はヒートポンプからの熱供給、更にはまた例え
ば家屋の熱水循環系を通じての放熱に用いられる。第2
図において、本発明に従う篭熱容器11は下端は中空壁
12を有し、これは管継手13及び14を通して蓄熱の
ために熱運搬液体により貫流される。A motor 3 is mounted on the cover 2 of the heating vessel, which drives a pump rotor 4. This rotor is partially surrounded by a spiral housing 5 which leads via a conduit 7 to a heat exchanger 7a. A spiral tube 7b is arranged at the bottom of the heat storage container 1 and has a number of downwardly opening tubes 7c through which the heat-carrying liquid is conveyed back into the heat storage container. A heat transfer liquid with a light specific gravity is present in the space 6a, a molten heat storage material is present in the space 6b, and a solid heat storage material is present in the space 6c. The entrance 7c prevents the heat storage material melt from flowing into the tube 7b if the tube 7b lies strictly in the horizontal plane 7d. When the heat storage materials 6b and 6c have solidified into one solid body after a relatively long cooling period, the heat storage container 1
The static overpressure of the heat transfer liquid heated by the heat exchanger 7a in the lower part of the field lifts the field shape until it is completely melted, causing the heat transfer liquid to flow around it. bring. On the other hand, when heat is dissipated for a short period of time, no homogeneous solid body is formed at all, but a mixture of crystals of the heat storage material and the melt is formed, and this is caused by the difference in specific gravity between the heat transfer liquid flowing in from the closed opening 7c. flowed through by the current. This difference in specific gravity between the solid and molten heat storage material is compensated by the membrane 8, which is filled and optionally communicated with the outside air. The circulation circuit 9 serves for heat supply, for example from a solar collector or a heat pump, and also for heat dissipation, for example through a hot water circulation system of a house. Second
In the figure, the cage heat vessel 11 according to the invention has at its lower end a hollow wall 12 through which a heat-carrying liquid flows for heat storage through pipe fittings 13 and 14.
容器周壁11はこの場合に下向きに広がった円錐形状1
5を示し、それにより蓄熱材料固化体が蓄熱に際して器
壁から離れるようになっている。上方部分にポンプロー
タ17があり、これは渦巻ハウジング18と協働する。
このポンプロータ17の駆動は蓄熱容器の外部に設けた
モーター19により行なわれる。ポンプの渦巻ハウジン
グ18内の渦巻状導溝20(第4図)は導管21中に開
□している。近似的に円筒形の蓄熱容器に切線方向から
入り込む導管22と23とによって熱運搬液体が蓄熱容
器11の内部に送り戻される。熱交換器24を介してこ
の装置は熱消費系25と連結されている。蓄熱容器の上
部26は分離面27まで軽比重の熱運搬液体で満されて
いる。モ−夕19が駆動されると、熱運搬液体中に渦流
が生じ、その中心28に溶融蓄熱材料29が重力の加速
度に抗して引き込まれ、ロータ17中に達する。ロータ
17は第4図に見られるように、開放して構成されてお
り、そして扇形室30を有している。誓熱材溶融物は矢
印34のように周縁部・31の輪郭をたどり、そしてそ
れにより渦巻状導溝20中に投げ出される。蓄熱材料の
液と熱運搬液体との接触により結晶化しつつある液滴3
2が形成される。これら結晶しつつある液滴32はその
高い比重に基づいて渦巻状ハウジングの下方にあるロー
タ水準において外向きに投げ出され、次いで下方に沈降
し、従って液状部分35は或回転体表面37で固体状部
分36と分離されている。この表面37は蓄熱材料の全
てが遂に結晶化されてしまうまで次第に小さくなる。蓄
熱のために循環回路13,12,14を通して、結晶の
全てが再び溶融してしまうまで熱運搬液体が導入される
。固体状蓄熱材料16の重さによって、その生じた熔融
物は側部を流れ、それにより蓄熱材料と加溢された壁面
との間の常に殆んど直線の接触が起る。更にもう一つの
本発明に従う篭熱方法としては、蓄熱材料の融点以上の
温度にある熱運搬液体を切線方向に開□している管22
及び中でも管23を通して蓄熱容器11の下部に戻すの
である。In this case, the container peripheral wall 11 has a conical shape 1 expanding downward.
5, thereby allowing the solidified heat storage material to separate from the vessel wall during heat storage. In the upper part there is a pump rotor 17, which cooperates with a volute housing 18.
The pump rotor 17 is driven by a motor 19 provided outside the heat storage container. A spiral channel 20 (FIG. 4) in the pump's spiral housing 18 opens into a conduit 21. The heat-carrying liquid is conveyed back into the interior of the heat storage vessel 11 by conduits 22 and 23 which enter the approximately cylindrical heat storage vessel tangentially. A heat exchanger 24 connects the device to a heat consumption system 25 . The upper part 26 of the heat storage vessel is filled up to the separation surface 27 with a light specific gravity heat transfer liquid. When the motor 19 is driven, a vortex is generated in the heat transfer liquid, and the molten heat storage material 29 is drawn into the center 28 of the vortex against the acceleration of gravity and reaches the rotor 17 . The rotor 17, as seen in FIG. 4, is of open construction and has a sector-shaped chamber 30. The thermal material melt follows the contour of the peripheral edge 31 as shown by the arrow 34 and is thereby thrown into the spiral channel 20. Droplet 3 crystallizing due to contact between heat storage material liquid and heat transport liquid
2 is formed. Due to their high specific gravity, these crystallizing droplets 32 are thrown outward at the rotor level below the spiral housing and then settle downwards, so that the liquid portion 35 forms a solid at a certain rotating body surface 37. It is separated from the section 36. This surface 37 becomes smaller and smaller until all of the heat storage material has finally been crystallized. For heat storage, a heat-carrying liquid is introduced through the circulation circuits 13, 12, 14 until all of the crystals have melted again. Due to the weight of the solid heat storage material 16, the resulting melt flows to the sides, so that a nearly straight contact between the heat storage material and the flooded wall surface always takes place. Yet another cage heating method according to the present invention includes a tube 22 that opens in the tangential direction and passes through a heat transfer liquid at a temperature higher than the melting point of the heat storage material.
Among other things, it is returned to the lower part of the heat storage container 11 through the pipe 23.
第3図には逆の層形成の場合を示してある。高比重の熱
運搬液体40が下部にあり、その上に蓄熱材料51が浮
んでいる。ロータ42もこれに対応して蓄熱容器43の
下部に配置されており、そして電気モーター44によっ
て磁気透過性の壁45を通して駆動される。熱交換器4
6によって加熱回路が熱運搬液体回路と分離されている
。上部48において開放している管47を通して蓄熱材
料溶融物41がロータ42に達する。結晶化しつつある
液滴50は上昇して51の部分に集まる。蓄熱には熱運
搬液体を熱交換器46により加熱する。最初は熱運搬液
体だけがロータ42に吸い込まれるが、蓄熱材料の一部
が融解した後で液状の蓄熱材料も一諸に吸い込まれて加
熱され、それにより未だ結晶化している蓄熱材料に熱運
搬液体のみならず既に融解した蓄熱材料によっても融解
熱が供給される。第5図は、蓄熱材料溶融物50の比重
が熱運搬液体51のそれよりも大きく、一方結晶化した
蓄熱材料52の比重が軽い場合の配置を示す。FIG. 3 shows the case of reverse layer formation. A high specific gravity heat transfer liquid 40 is at the bottom, and a heat storage material 51 is floating above it. A rotor 42 is also correspondingly arranged in the lower part of the heat storage container 43 and is driven through a magnetically permeable wall 45 by an electric motor 44 . heat exchanger 4
6 separates the heating circuit from the heat transporting liquid circuit. The heat storage material melt 41 reaches the rotor 42 through a tube 47 which is open in the upper part 48 . The droplet 50 that is crystallizing rises and collects at a portion 51. For heat storage, the heat transfer liquid is heated by a heat exchanger 46. Initially, only the heat transfer liquid is sucked into the rotor 42, but after some of the heat storage material melts, the liquid heat storage material is also sucked in and heated, thereby transferring heat to the still crystallized heat storage material. Heat of fusion is supplied not only by the liquid but also by the already melted heat storage material. FIG. 5 shows an arrangement in which the specific gravity of the heat storage material melt 50 is greater than that of the heat transfer liquid 51, while the specific gravity of the crystallized heat storage material 52 is lighter.
旋回支承部54を有する旋回アーム管53を介して熱運
搬液体が導管55中に導入される。同じ旋回管53にお
いて熱運搬液体が開口56を通して再び排出する。ポン
プロータ57はモータ59により駆動される。平衡錘6
0がモータ59の重量にほぼつり合う。浮子61は液体
分離水準62とポンプロータ57との間に一定の間隔6
3を存在させる役目をする。旋回支承部55内で2本の
導管が開□しており、これらは例えば第3図の46に従
う熱交換器に通じている。図面の簡単な説明第1及び2
図は軽比重の熱運搬液体を用いる本発明に従う蓄熱器の
2つの具体例の図式断面図、第3図は重比重の熱運搬液
体を用いる本発明に従う蓄熱器の具体例の図式断面図、
第4図は本発明において用いられるポンプロータ部の1
具体例の拡大説明図、第5図は熱運搬液体の比重が蓄熱
材料の固体状態及び液体状態のそれの中間にあるものを
用いる本発明に従う蓄熱器のもう一つの具体例の図式説
明図である。Heat transfer liquid is introduced into conduit 55 via a pivot arm tube 53 having a pivot bearing 54 . In the same swirl tube 53 the heat transfer liquid exits again through the opening 56. Pump rotor 57 is driven by motor 59. Balance weight 6
0 approximately balances the weight of the motor 59. The float 61 has a constant spacing 6 between the liquid separation level 62 and the pump rotor 57.
It plays the role of making 3 exist. Two conduits are open in the pivot bearing 55, which lead to a heat exchanger according to 46 in FIG. 3, for example. Brief explanation of drawings 1 and 2
FIG. 3 is a schematic cross-sectional view of two embodiments of a heat storage device according to the invention using a heat transfer liquid of light specific gravity; FIG.
Figure 4 shows one of the pump rotor parts used in the present invention.
FIG. 5 is a schematic illustration of another embodiment of a heat storage device according to the present invention in which the specific gravity of the heat transfer liquid is intermediate between that of the solid state and liquid state of the heat storage material. be.
参照記号の説明:第1乃至4図において:1,11,4
3:審熱容器、2:カバー、3,19,44:モータ、
4,17,42:ロータ、6a,26,40:熱運搬液
体部、6b,35,41ミ液体蓄熱材料部、6c,16
,51:団体蓄熱材料部、7a,24,46:熱交換器
、8:中空体、21,22,23,24:外部熱交換回
路、30:羽根、31:外側環状部、第5図において:
50:液体蓄熱材料部、51:熱運搬液体、52:閥体
蓄熱材料部、53:旋回アーム管、57:ロータ、61
:浮子。Explanation of reference symbols: In figures 1 to 4: 1, 11, 4
3: Heat evaluation container, 2: Cover, 3, 19, 44: Motor,
4, 17, 42: Rotor, 6a, 26, 40: Heat transport liquid section, 6b, 35, 41 Liquid heat storage material section, 6c, 16
, 51: Group heat storage material part, 7a, 24, 46: Heat exchanger, 8: Hollow body, 21, 22, 23, 24: External heat exchange circuit, 30: Vane, 31: Outer annular part, In FIG. :
50: Liquid heat storage material section, 51: Heat transport liquid, 52: Combined heat storage material section, 53: Swivel arm tube, 57: Rotor, 61
: Float.
FIG.l FIG.2 FIG.3 FIG・ム FIG.5FIG. l FIG. 2 FIG. 3 FIG・mu FIG. 5
Claims (1)
熱材料が存在し、(b) 上記蓄熱材料と混ざり合わな
い熱運搬液体が存在し、そして(c) 上記熱運搬液体
が外部循環回路を貫流する蓄熱器において、熱運搬液体
の比重が上記蓄熱材料の溶融物の比重と異つており、そ
して上記熱運搬液体の層中に渦流を発生させるロータが
配置されていて、これに溶融蓄熱材料と熱運搬液体との
混合物が吸い込まれることを特徴とする、上記蓄熱器。 2 熱運搬液体の比重が蓄熱材料の溶融物の比重よりも
小であり、そしてロータ17が蓄熱容器11の上部に配
置されている、上記特許請求の範囲第1項に従う蓄熱器
。 3 熱運搬液体の比重が蓄熱材料溶融物の比重よりも大
であつて、ロータ42が蓄熱容器の下部に存在する、前
記特許請求の範囲第1項に従う蓄熱器。 4 熱運搬液体の比重が蓄熱材料溶融物の比重よりも小
であつて且つ蓄熱材料固体の比重よりも大であり、そし
て、ロータ57が熱運搬液体と蓄熱材料溶融物との境界
面の上方にある、前記特許請求の範囲第1項に従う蓄熱
器。 5 分離装置31を備え、これによつて熱運搬液体と蓄
熱材料の液滴とが2つの流出水準に分離される、上記特
許請求の範囲第1乃至4項の何れかに従う蓄熱器。 6 熱運搬液体の外部熱交換循環回路21,24,22
,23,55を通しての輸送をポンプにより行ない、こ
れが熱運搬液体を蓄熱容器中に送り戻す、上記特許請求
の範囲第5項に従う蓄熱器。 7 蓄熱容器1,43からの熱運搬液体の上記外部循環
回路への流出が蓄熱容器の中心軸28,53の部分で行
なわれる。 上記特許請求の範囲第1乃至6項の何れかに従う蓄熱器
。8 ロータ4,17,42,67がアキシヤルランナ
ーである、上記特許請求の範囲第1乃至7項の何れかに
従う蓄熱器。 9 ロータ4,17,42,57がラジアルランナーで
あり、そして羽根30のついた内側部分と羽根のない外
側環状部31とを有し、これが熱運搬液体の流れをポン
プハウジング18中に導く役目をする、上記特許請求の
範囲第1乃至8項の何れかに従う蓄熱器。 10 蓄熱容器1,11,43の周壁が円錐状に上向き
に広がつて、それにより蓄熱材料の結晶からなる固体6
cが容器底から圧入される熱運搬液体の流れの圧力によ
つて僅かしか持ち上げられないようになつている、前記
特許請求の範囲第1項に従う蓄熱器。 11 熱運搬液体6a,26,40中に蓄熱材料結晶と
熱運搬液体とを分離するために渦流を生じさせる、前記
特許請求の範囲第1項に従う蓄熱器。 12 上流渦流が蓄熱容器1,11,43の垂直軸に配
置されたロータ4,17,42によつて生ぜしめられる
、上記特許請求の範囲第11項に従う蓄熱器。 13 ロータ4,17,42,57が同時に熱運搬液体
を循環させる循環ポンプのロータである、上記特許請求
の範囲第12項に従う蓄熱器。 14 蓄熱材料溶融物を重層化防止のために循環させる
、前記特許請求の範囲第1項に従う蓄熱器。 15 蓄熱容器11の下部に加熱底11a,13,14
を配置した、上記特許請求の範囲第1乃至14項の何れ
かに従う蓄熱器。 16 蓄熱容器周壁11が上記加熱底の方向に向い円錐
状に拡大している、上記特許請求の範囲第15項に従う
蓄熱器。 17 下方に存在する蓄熱材料溶融物6cの下部又は上
方に存在する蓄熱材料溶融物41の上部に管系が配置さ
れており、これが開口を有し、これらの開口は上記溶融
物に向つて別方向を向いていてこれらを通して熱運搬液
体が導かれる、上記特許請求の範囲第1乃至16項の何
れかに従う蓄熱器。 18 蓄熱容器中に柔軟材料からなるガス充満中空体8
が配置されている、上記特許請求の範囲第1乃至17項
の何れかに従う蓄熱器。 19 補償用容器が熱運搬液体6a,26,40,51
と連通している、上記特許請求の範囲第1乃至18項の
何れかに従う蓄熱器。[Claims] 1. A heat storage container, in which (a) there is a heat storage material that stores latent heat upon transition from solid to liquid, and (b) there is a heat transfer liquid that does not mix with the heat storage material. and (c) in a heat storage device through which said heat transfer liquid flows through an external circulation circuit, the specific gravity of the heat transfer liquid is different from the specific gravity of the melt of said heat storage material, and there is a vortex flow in the layer of said heat transfer liquid. A heat storage device as described above, characterized in that a rotor is arranged to generate a heat storage material, into which a mixture of molten heat storage material and heat transfer liquid is sucked. 2. A heat storage device according to claim 1, wherein the specific gravity of the heat transfer liquid is lower than the specific gravity of the melt of the heat storage material, and the rotor 17 is arranged in the upper part of the heat storage container 11. 3. A heat storage device according to claim 1, wherein the specific gravity of the heat transfer liquid is greater than the specific gravity of the heat storage material melt, and the rotor 42 is located in the lower part of the heat storage container. 4. The specific gravity of the heat transfer liquid is smaller than the specific gravity of the heat storage material melt and larger than the specific gravity of the heat storage material solid, and the rotor 57 is located above the interface between the heat transfer liquid and the heat storage material melt. A heat storage device according to claim 1. 5. A heat storage device according to any one of the preceding claims, comprising a separation device 31, by means of which the heat transfer liquid and the droplets of heat storage material are separated into two outflow levels. 6 External heat exchange circulation circuit for heat transport liquid 21, 24, 22
, 23, 55 is carried out by a pump, which pumps the heat transfer liquid back into the heat storage container. 7. The outflow of the heat transfer liquid from the heat storage containers 1, 43 into the external circulation circuit takes place at the central axes 28, 53 of the heat storage containers. A heat storage device according to any one of claims 1 to 6 above. 8. A heat storage device according to any one of claims 1 to 7, wherein the rotors 4, 17, 42, 67 are axial runners. 9. The rotor 4, 17, 42, 57 is a radial runner and has an inner part with vanes 30 and an outer annular part 31 without vanes, which serves to direct the flow of heat-transferring liquid into the pump housing 18. A heat storage device according to any one of claims 1 to 8 above. 10 The peripheral walls of the heat storage containers 1, 11, 43 expand upward in a conical shape, thereby forming a solid body 6 made of crystals of the heat storage material.
2. A heat storage device according to claim 1, wherein the heat transfer liquid is only slightly lifted by the pressure of the flow of heat-transfer liquid that is forced into the bottom of the container. 11. A heat storage device according to claim 1, wherein a vortex is created in the heat transfer liquid 6a, 26, 40 to separate the heat storage material crystals and the heat transfer liquid. 12. Regenerator according to claim 11, in which the upstream vortex is generated by a rotor 4, 17, 42 arranged on the vertical axis of the regenerator container 1, 11, 43. 13. A heat storage device according to claim 12, wherein the rotors 4, 17, 42, 57 are rotors of a circulation pump that simultaneously circulates a heat-transferring liquid. 14. A heat storage device according to claim 1, in which a molten heat storage material is circulated to prevent layering. 15 Heating bottom 11a, 13, 14 at the bottom of the heat storage container 11
A heat storage device according to any one of claims 1 to 14 above, wherein the heat storage device is provided with: 16. The heat storage device according to claim 15, wherein the heat storage container peripheral wall 11 widens conically in the direction of the heating bottom. 17 At the bottom of the heat storage material melt 6c located below or in the upper part of the heat storage material melt 41 located above, a pipe system is arranged, which has openings, these openings being separate towards said melt. 17. Regenerators according to any of the preceding claims, oriented in a direction through which a heat transfer liquid is conducted. 18 Gas-filled hollow body made of flexible material in heat storage container 8
A heat storage device according to any one of claims 1 to 17 above, wherein: 19 Compensation container is heat transport liquid 6a, 26, 40, 51
19. A heat storage device according to any one of claims 1 to 18, in communication with a heat storage device according to any one of claims 1 to 18.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AT3176A AT349270B (en) | 1975-01-09 | 1976-01-05 | DEVICE FOR REGULATING A TEMPERATURE-DEPENDENT OPERATING PARAMETER OF AN OPERATING UNIT CONSISTING OF A COMBUSTION ENGINE AND AN EXHAUST-GAS AFTERBURN DEVICE |
| AT3176/77 | 1977-05-04 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS53136736A JPS53136736A (en) | 1978-11-29 |
| JPS6037392B2 true JPS6037392B2 (en) | 1985-08-26 |
Family
ID=3479690
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP52068010A Expired JPS6037392B2 (en) | 1976-01-05 | 1977-06-10 | Heat storage device that uses fusion enthalpy |
Country Status (2)
| Country | Link |
|---|---|
| JP (1) | JPS6037392B2 (en) |
| DE (1) | DE2725658C2 (en) |
Families Citing this family (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AT356846B (en) * | 1978-07-20 | 1980-05-27 | Holztrattner Heinrich | CLOSED CONTAINER FOR STORING AND / OR GENERATING HEAT OR COLD WITH BUILT-IN CHAMBERS AND TUBES |
| NL7905277A (en) * | 1979-07-05 | 1981-01-07 | Doomernik Bv | ACCUMULATOR FOR STORING HEAT OR COLD. |
| SE414504B (en) * | 1979-08-22 | 1980-08-04 | Bo Carlsson | SET AND DEVICE FOR STORAGE AND RECOVERY OF HEAT THROUGH Melting and crystallization of one or more chemical compounds |
| JPS5642099A (en) * | 1979-09-14 | 1981-04-20 | Kubota Ltd | Regenerative tank |
| JPS5986894A (en) * | 1982-11-10 | 1984-05-19 | Agency Of Ind Science & Technol | Regenerating method and regenerator |
| DE19533622A1 (en) * | 1995-09-12 | 1997-03-13 | Deutsche Forsch Luft Raumfahrt | Latent heat storage system based on e.g. hydrated salts |
| JP5728272B2 (en) | 2011-03-31 | 2015-06-03 | 本田技研工業株式会社 | Electric vehicle |
| DE102018217204A1 (en) * | 2018-10-09 | 2020-04-09 | Zf Friedrichshafen Ag | Temperature control device and test bench arrangement |
| EP3680596A1 (en) * | 2019-01-11 | 2020-07-15 | Yara International ASA | Storage container for a heat storage mass, heat storage system and heat transfer system comprising such a storage container |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2996894A (en) * | 1956-12-13 | 1961-08-22 | Gen Electric | Method and apparatus for the recovery of latent heat of fusion |
-
1977
- 1977-06-06 DE DE2725658A patent/DE2725658C2/en not_active Expired
- 1977-06-10 JP JP52068010A patent/JPS6037392B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| DE2725658A1 (en) | 1978-11-09 |
| DE2725658C2 (en) | 1986-11-13 |
| JPS53136736A (en) | 1978-11-29 |
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