JPH02219987A - Heat accumulator - Google Patents
Heat accumulatorInfo
- Publication number
- JPH02219987A JPH02219987A JP1041400A JP4140089A JPH02219987A JP H02219987 A JPH02219987 A JP H02219987A JP 1041400 A JP1041400 A JP 1041400A JP 4140089 A JP4140089 A JP 4140089A JP H02219987 A JPH02219987 A JP H02219987A
- Authority
- JP
- Japan
- Prior art keywords
- heat storage
- heat
- agent
- tube
- exchanger
- 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
Links
Classifications
-
- 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
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
Description
【発明の詳細な説明】 [発明の目的] (産業上の利用分野) 本発明は、蓄熱装置に関する。[Detailed description of the invention] [Purpose of the invention] (Industrial application field) The present invention relates to a heat storage device.
(従来の技術)
チューブ外周面に板状フィンを形成してなるフィンアン
ドチューブ形熱交換器を潜熱蓄熱剤中に配して蓄熱装置
を構成する場合には、蓄熱剤の相転移に伴う体積変化に
よる力で熱交換器がバラバラになる可能性がある。(Prior art) When configuring a heat storage device by disposing a fin-and-tube heat exchanger in which plate-shaped fins are formed on the outer peripheral surface of a tube in a latent heat storage agent, the volume due to the phase transition of the heat storage agent increases. The force of the change could cause the heat exchanger to fall apart.
そこで、例えば特公昭61−45159号公報に示され
る蓄熱装置では、蓄熱容器内においてフィンアンドチュ
ーブ形熱交換器を低温蓄熱のための潜熱蓄熱剤向上部に
配し、下部にヒータを配している。Therefore, for example, in the heat storage device disclosed in Japanese Patent Publication No. 61-45159, a fin-and-tube heat exchanger is arranged in the latent heat storage agent improvement section for low-temperature heat storage in the heat storage container, and a heater is arranged at the bottom. There is.
この蓄熱装置では、蓄熱剤結晶が熱交換器に付着するつ
どヒータ通電を行って結晶を熱交換器から離脱させ、こ
の結晶を蓄熱容器下部に順次受溜めていく。In this heat storage device, each time the heat storage agent crystals adhere to the heat exchanger, the heater is energized to separate the crystals from the heat exchanger, and the crystals are sequentially stored in the lower part of the heat storage container.
(発明が解決しようとする課題)
特公昭61−45159号公報に示された前記従来の蓄
熱装置は、蓄熱剤結晶離脱用ヒータが必要であり、この
ヒータの制御が面倒であった。(Problems to be Solved by the Invention) The conventional heat storage device disclosed in Japanese Patent Publication No. 61-45159 requires a heater for separating heat storage agent crystals, and the control of this heater is troublesome.
また、蓄熱容器内に蓄熱剤結晶を受溜めるスペースが必
要であり、装置が大型化する問題があった。Further, a space is required to receive the heat storage agent crystals in the heat storage container, which causes a problem of increasing the size of the device.
また、板状フィンでは熱交換器表面積をあまり大きくす
ることができないから蓄熱に長時間を要するばかりでな
く、更に加熱エネルギが必要であることから、蓄熱に必
要なエネルギに対する回収工ネルギの比率すなわち蓄熱
効率があまり良くなかった。In addition, with plate-shaped fins, the surface area of the heat exchanger cannot be made very large, so not only does it take a long time to store heat, but additional heating energy is required, so the ratio of recovered energy to the energy required for heat storage is Heat storage efficiency was not very good.
本発明は、以上の事情を考慮してなされたものであって
、蓄熱剤結晶離脱用ヒータを必要とせず、コンパクトで
あって、しかも蓄熱速度及び蓄熱効率を改良した蓄熱装
置を提供することを目的とする。The present invention has been made in consideration of the above circumstances, and it is an object of the present invention to provide a heat storage device that does not require a heater for removing heat storage agent crystals, is compact, and has improved heat storage speed and heat storage efficiency. purpose.
[発明の構成]
(課題を解決するための手段)
本発明に係る蓄熱装置は、前記の目的を達成するために
、チューブ外周面に多数の針状フィンを形成してなる2
つの熱交換器を蓄熱剤中に平行に配したものであって、
一方の熱交換器のフィンが他方の熱交換器のフィン間に
入込む位置に側熱交換器を配設している。[Structure of the Invention] (Means for Solving the Problems) In order to achieve the above-mentioned object, a heat storage device according to the present invention includes a heat storage device including a plurality of needle-like fins formed on the outer peripheral surface of a tube.
Two heat exchangers are arranged in parallel in a heat storage agent,
A side heat exchanger is disposed at a position where the fins of one heat exchanger fit between the fins of the other heat exchanger.
(作 用)
一方の熱交換器は蓄熱用であり、他方の熱交換器は蓄熱
回収用である。(Function) One heat exchanger is for heat storage, and the other heat exchanger is for heat storage and recovery.
水等の低温蓄熱剤を使用する場合には、蓄熱用熱交換器
のチューブ内に低温流体を供給する。When using a low temperature heat storage agent such as water, the low temperature fluid is supplied into the tubes of the heat storage heat exchanger.
この際、蓄熱剤が冷却されて低温蓄熱がなされる。At this time, the heat storage agent is cooled and low-temperature heat storage is performed.
蓄熱用熱交換器はチューブ外周面に多数の針状フィンを
形成してなり蓄熱剤との接触面積が非常に大きいから、
蓄熱が急速に高効率で進行する。潜熱蓄熱剤への蓄熱の
進行につれて蓄熱剤結晶が蓄熱用熱交換器のチューブ及
び針状フィン上に成長する場合であっても、この結晶を
離脱させなくとも熱交換器が破壊されることはない。こ
の際、蓄熱回収用熱交換器の針状フィンが蓄熱用熱交換
器の針状フィンの間に入込んでいるから、成長した蓄熱
剤結晶は蓄熱回収用熱交換器の針状フィンに接触する。The heat exchanger for heat storage has many needle-like fins formed on the outer circumferential surface of the tube, and the contact area with the heat storage agent is very large.
Heat storage progresses rapidly and with high efficiency. Even if heat storage agent crystals grow on the tubes and acicular fins of the heat storage heat exchanger as heat storage progresses in the latent heat storage agent, the heat exchanger will not be destroyed even if these crystals are not removed. do not have. At this time, since the needle-like fins of the heat exchanger for heat storage and recovery are inserted between the needle-like fins of the heat exchanger for heat storage, the grown heat storage agent crystals come into contact with the needle-like fins of the heat exchanger for heat storage and recovery. do.
したがって、蓄熱エネルギの回収も高効率で行われる。Therefore, the recovery of thermal energy is also performed with high efficiency.
パラフィン等の高温蓄熱剤を使用する場合には、蓄熱用
熱交換器のチューブ内に高温流体を供給する。この際、
蓄熱剤が加熱されて高温蓄熱がなされる。この場合にも
蓄熱が急速に高効率で進行するばかりでなく、蓄熱エネ
ルギの回収も高効率で行われる。When using a high temperature heat storage agent such as paraffin, a high temperature fluid is supplied into the tubes of the heat storage heat exchanger. On this occasion,
The heat storage agent is heated and high temperature heat is stored. In this case as well, not only heat storage progresses rapidly and with high efficiency, but also heat storage energy recovery is performed with high efficiency.
側熱交換器のチューブを平行に引揃え、これらチューブ
を蓄熱剤全体中に屈曲するようにくまなく配することが
でき、低温蓄熱剤と高温蓄熱剤とを問わず蓄熱剤のすみ
ずみまで側熱交換器を蓄熱剤に接触させ、蓄熱剤を残ら
ず利用することができる。The tubes of the side heat exchanger can be arranged in parallel, and these tubes can be arranged crookedly throughout the entire heat storage agent. By bringing the heat exchanger into contact with the heat storage agent, all of the heat storage agent can be utilized.
(実施例)
第1図及び第2図は、ともに本発明の実施例に係る冷暖
房用潜熱蓄熱装置の縦断面図であり、互いに直交する2
鉛直面で切断した状態をそれぞれ示す。(Example) FIG. 1 and FIG. 2 are both longitudinal cross-sectional views of a latent heat storage device for heating and cooling according to an example of the present invention, and two
Each figure shows the state cut on a vertical plane.
断熱材からなる蓄熱容器10の上部開口は、同様に断熱
材からなる蓋板12で閉じられ、蓋板12の側方に通気
孔14が形成されている。蓄熱容器10の中には低温蓄
熱のための蓄熱剤16として水が充填されているが、容
器上部は蓄熱剤1Bの相転移に伴う体積変化を吸収する
ために空気層18が形成されている。The upper opening of the heat storage container 10 made of a heat insulating material is closed with a cover plate 12 also made of a heat insulating material, and a ventilation hole 14 is formed on the side of the cover plate 12. The heat storage container 10 is filled with water as a heat storage agent 16 for low-temperature heat storage, and an air layer 18 is formed in the upper part of the container to absorb the volume change accompanying the phase transition of the heat storage agent 1B. .
蓄熱剤16の中には、蓄熱用熱交換器20と蓄熱回収用
熱交換器30との2つの熱交換器が浸漬されている。蓄
熱用熱交換器2oのチューブ22は、蓄熱容器lOに入
った後、水平部分が例えば3層をなすように屈曲しなが
ら蓄熱剤16中をくまなく走行する。チューブ22の水
平部分外周面には、多数の針状フィン24が放射状に形
成されている。1本の針状フィン24の寸法は、例えば
長さ9〜11m】、幅0.8mmが適当であり、このフ
ィンがチューブ長さl0CIIIあたり約3000本形
成されている。チューブ22は、アキュムレータ2Bを
介して蓄熱容器10外に出る。蓄熱回収用熱交換器30
のチューブ32は、蓄熱容器10に入った後、蓄熱用熱
交換器20のチューブ22に対して平行に走行する。チ
ューブ32は、水平部分の外周面に同様の針状フィン3
4が形成されており、この水平部分が例えば2層をなす
ように蓄熱剤16中を走行する。この際、両チューブ2
2.32は交互に水平層をなすように配設され、両者の
針状フィン24.34が互いの間に入込む。ただし、第
1図及び第2図では針状フィン24.34の一部の図示
を省略している。蓄熱回収用熱交換器30のチューブ3
2はアキュムレータを介さずに蓄熱容器lO外に出る。Two heat exchangers, a heat exchanger 20 for heat storage and a heat exchanger 30 for heat storage and recovery, are immersed in the heat storage agent 16. After the tube 22 of the heat storage heat exchanger 2o enters the heat storage container 1O, the tube 22 runs throughout the heat storage agent 16 while being bent so that the horizontal portion forms, for example, three layers. A large number of needle-like fins 24 are formed radially on the outer peripheral surface of the horizontal portion of the tube 22 . Appropriate dimensions of one needle-like fin 24 are, for example, a length of 9 to 11 m and a width of 0.8 mm, and approximately 3000 fins are formed per tube length l0CIII. The tube 22 exits from the heat storage container 10 via the accumulator 2B. Heat exchanger 30 for heat storage and recovery
After entering the heat storage container 10, the tube 32 runs parallel to the tube 22 of the heat storage heat exchanger 20. The tube 32 has similar needle-like fins 3 on the outer peripheral surface of the horizontal portion.
4 is formed, and this horizontal portion runs through the heat storage agent 16 so as to form, for example, two layers. At this time, both tubes 2
2.32 are arranged in alternating horizontal layers, and their needle-like fins 24.34 are inserted between each other. However, in FIGS. 1 and 2, some of the needle fins 24, 34 are omitted. Tube 3 of heat exchanger 30 for heat storage and recovery
2 exits from the heat storage container IO without passing through the accumulator.
蓄熱を実行する際には、蓄熱用熱交換器20のチューブ
22に例えば低温低圧のフロン系液冷媒を供給する。こ
の蓄熱用熱交換器20に接する蓄熱剤1Bが低温液冷媒
によって冷却されて凝固し、ここに潜熱蓄熱がなされる
。つまり、蓄熱温度は0℃である。この際、針状フィン
24の総表面積が大きいから、蓄熱が急速に高効率で進
行する。蓄熱用熱交換器20のチューブ22及び針状フ
ィン24は蓄熱剤16のすみずみまでこれに接触するか
ら、蓄熱剤1Bへの蓄熱の進行につれてチューブ22及
び針状フィン24上に蓄熱剤結晶が良く成長し、蓄熱剤
1Bが有効利用される。蓄熱が完了に近づくとチューブ
22内の液冷媒がオーバーチャージとなるが、アキュム
レータ2Bを設けているのでこれに対処することができ
る。この際、蓄熱用熱交換器20から蓄熱剤結晶を離脱
させなくともこの熱交換器が破壊されることはない。ま
た、この潜熱蓄熱によって蓄熱剤16の体積が増加する
が、蓄熱容器10の上部に空気層18を設けるとともに
上面に通気孔14を設けているので、蓄熱容器10が破
壊する□こともない。When performing heat storage, for example, a low-temperature, low-pressure fluorocarbon-based liquid refrigerant is supplied to the tubes 22 of the heat exchanger 20 for heat storage. The heat storage agent 1B in contact with the heat storage heat exchanger 20 is cooled and solidified by the low-temperature liquid refrigerant, and latent heat is stored here. In other words, the heat storage temperature is 0°C. At this time, since the total surface area of the needle fins 24 is large, heat storage progresses rapidly and with high efficiency. Since the tubes 22 and acicular fins 24 of the heat storage heat exchanger 20 come into contact with every corner of the heat storage agent 16, heat storage agent crystals are formed on the tubes 22 and acicular fins 24 as heat storage progresses in the heat storage agent 1B. It grows well and the heat storage agent 1B is effectively used. When heat storage approaches completion, the liquid refrigerant in the tube 22 becomes overcharged, but since the accumulator 2B is provided, this can be dealt with. At this time, even if the heat storage agent crystals are not removed from the heat storage heat exchanger 20, this heat exchanger will not be destroyed. Further, although the volume of the heat storage agent 16 increases due to this latent heat storage, since the air layer 18 is provided in the upper part of the heat storage container 10 and the ventilation hole 14 is provided in the upper surface, the heat storage container 10 will not be destroyed.
通気孔14に圧力調節弁を設けても良い。A pressure regulating valve may be provided in the vent hole 14.
さて、同熱交換器20 、30の針状フィン24.34
が互いの間に入込んでいるから、成長した蓄熱剤結晶は
蓄熱回収用熱交換器30の針状フィン34に接触する。Now, the same heat exchanger 20, 30 needle fins 24.34
are inserted between each other, the grown heat storage agent crystals come into contact with the needle-like fins 34 of the heat storage and recovery heat exchanger 30.
したがって、蓄熱剤16の蓄熱エネルギは、蓄熱回収用
熱交換器30内の伝熱媒体に効率良く伝えられ、蓄熱エ
ネルギの回収が高効率で行われる。Therefore, the heat storage energy of the heat storage agent 16 is efficiently transmitted to the heat transfer medium in the heat storage and recovery heat exchanger 30, and the heat storage energy is recovered with high efficiency.
この際、蓄熱剤結晶が融解して再蓄熱が可能となる。な
お、同熱交換器20.30は、蓄熱剤16の相転移すな
わち凝固と融解との繰返しに伴う体積変化に対しても、
針状フィン24.34がばらばらになることがない。At this time, the heat storage agent crystals melt and re-storage of heat becomes possible. The heat exchangers 20 and 30 also respond to volume changes due to phase transition of the heat storage agent 16, that is, repeated solidification and melting.
The needle fins 24, 34 do not come apart.
蓄熱剤16としては、以上の説明のように使用温度下で
相転移を起す潜熱蓄熱剤が適切である。As the heat storage agent 16, a latent heat storage agent that undergoes a phase transition at the operating temperature as described above is suitable.
潜熱蓄熱剤を使用すれば、蓄熱剤16の単位体積あたり
の蓄熱エネルギ量を大きくとることができ、蓄熱装置を
コンパクトにすることができる。ただし、蓄熱剤teと
しては、潜熱蓄熱剤以外のものを使用しても良い。If a latent heat storage agent is used, a large amount of thermal energy can be stored per unit volume of the heat storage agent 16, and the heat storage device can be made compact. However, as the heat storage agent te, other than the latent heat storage agent may be used.
第3図〜第5図は、蓄熱用熱交換器20のチューブ22
と蓄熱回収用熱交換器30のチューブ32との配置の変
更例を示す模式図であって、白丸が蓄熱用熱交換器チュ
ーブ22を、黒丸が蓄熱回収用熱交換器チューブ32を
それぞれ示す。ただし、これらの図では針状フィン24
.34の図示を省略している。3 to 5 show the tube 22 of the heat storage heat exchanger 20.
FIG. 3 is a schematic diagram illustrating an example of a change in the arrangement of the heat exchanger tube 32 of the heat storage and recovery heat exchanger 30, with white circles indicating the heat storage heat exchanger tube 22 and black circles indicating the heat storage and recovery heat exchanger tube 32, respectively. However, in these figures, the needle fin 24
.. The illustration of 34 is omitted.
第3図の場合は、チューブ22.82を千鳥状に高密度
配置したものであって、1本の蓄熱回収用熱交換器チュ
ーブ32が4本の蓄熱用熱交換器チューブ22に隣接す
る。この場合には、第2図に示した場合よりも蓄熱装置
を更にコンパクト化でき、フィンどおしのラップ代を大
きくとることができる。また、第4図及び第5図に示す
ように、水平層をなす各チューブの隣どおしを蓄熱用2
2と蓄熱回収用32とにした配列でも良い。チューブ2
2.32は、それぞれシリーズに接続しても良いし、パ
ラレル方式であっても良い。なお、以上の説明ではチュ
ーブ22.32を水平方向に平行に引揃えていたが、蓄
熱剤結晶離脱用ヒータを使用する従来の場合とは違って
、これらのチューブ22.32を垂直方向に平行に引揃
えても支障がない。したがって、熱交換器20.30の
設計自由度が高い。In the case of FIG. 3, the tubes 22, 82 are arranged in a staggered manner with high density, and one heat exchanger tube 32 for heat storage and recovery is adjacent to four heat exchanger tubes 22 for heat storage. In this case, the heat storage device can be made more compact than the case shown in FIG. 2, and the amount of wrap between the fins can be increased. In addition, as shown in Figures 4 and 5, heat storage 2
2 and 32 for heat storage and recovery may be used. tube 2
2.32 may be connected in series or in parallel. In the above explanation, the tubes 22, 32 are arranged parallel to each other in the horizontal direction, but unlike the conventional case of using a heater for removing heat storage agent crystals, these tubes 22, 32 are arranged parallel to each other in the vertical direction. There is no problem even if it is aligned. Therefore, the degree of freedom in designing the heat exchangers 20 and 30 is high.
例えばパラフィン系や水和塩類等の材料を蓄熱剤IBと
して使用すれば、他の部分に変更を加えないで、以上に
説明した装置を高効率の高温蓄熱装置として使用するこ
とができる。For example, if a material such as paraffin or hydrated salts is used as the heat storage agent IB, the device described above can be used as a highly efficient high temperature heat storage device without making any changes to other parts.
[発明の効果コ
以上に説明したように、本発明に係る蓄熱装置は、チュ
ーブ外周面に多数の針状フィンを形成してなる2つの熱
交換器を蓄熱剤中に平行に配したものであって、一方の
熱交換器のフィンが他方の熱交換器のフィン間に入込む
位置に同熱交換器を配設しているから、本発明によれば
、蓄熱剤結晶離脱用ヒータを必要とせず、コンパクトで
あって、しかも蓄熱速度及び蓄熱効率を改良した蓄熱装
置を提供することができる。[Effects of the Invention] As explained above, the heat storage device according to the present invention has two heat exchangers each having a large number of needle-like fins formed on the outer peripheral surface of a tube arranged in parallel in a heat storage agent. Since the heat exchanger is arranged at a position where the fins of one heat exchanger fit between the fins of the other heat exchanger, according to the present invention, a heater for separating the heat storage agent crystals is not required. It is possible to provide a heat storage device that is compact and has improved heat storage speed and heat storage efficiency.
第1図は本発明の実施例に係る蓄熱装置の縦断面図、第
2図は前回の蓄熱装置の他の方向の縦断面図、第3図は
蓄熱用熱交換器チューブと蓄熱回収用熱交換器チューブ
との配置の変更例を示す模式図、第4図は蓄熱用熱交換
器チューブと蓄熱回収用熱交換器チューブとの配置の他
の変更例を示す模式図、第5図は蓄熱用熱交換器チュー
ブと蓄熱回収用熱交換器チューブとの配置の更に他の変
更例を示す模式図である。
符号の説明
10・・・蓄熱容器、16・・・蓄熱剤、20・・・蓄
熱用熱交換器、22・・・チューブ、24・・・針状フ
ィン、3G・・・蓄熱回収用熱交換器、32・・・チュ
ーブ、34・・・針状フィン。
第8図
第4図
第5図Fig. 1 is a longitudinal sectional view of a heat storage device according to an embodiment of the present invention, Fig. 2 is a longitudinal sectional view of the previous heat storage device in another direction, and Fig. 3 is a heat exchanger tube for heat storage and heat storage and recovery heat. A schematic diagram showing an example of a change in the arrangement with the exchanger tube, FIG. 4 is a schematic diagram showing another example of a change in the arrangement of the heat exchanger tube for heat storage and the heat exchanger tube for heat storage and recovery, and FIG. It is a schematic diagram which shows yet another example of a change of arrangement|positioning of the heat exchanger tube for heat storage and recovery, and the heat exchanger tube for heat storage and recovery. Explanation of symbols 10... Heat storage container, 16... Heat storage agent, 20... Heat exchanger for heat storage, 22... Tube, 24... Acicular fin, 3G... Heat exchanger for heat storage and recovery vessel, 32... tube, 34... needle-like fin. Figure 8 Figure 4 Figure 5
Claims (1)
2つの熱交換器を蓄熱剤中に平行に配した蓄熱装置であ
って、一方の熱交換器のフィンが他方の熱交換器のフィ
ン間に入込む位置に両熱交換器を配設したことを特徴と
する蓄熱装置。1. A heat storage device in which two heat exchangers each having a large number of needle-shaped fins formed on the outer peripheral surface of a tube are arranged in parallel in a heat storage agent, and the fins of one heat exchanger are connected to the fins of the other heat exchanger. A heat storage device characterized in that both heat exchangers are arranged at positions that fit between fins.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1041400A JPH02219987A (en) | 1989-02-20 | 1989-02-20 | Heat accumulator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1041400A JPH02219987A (en) | 1989-02-20 | 1989-02-20 | Heat accumulator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH02219987A true JPH02219987A (en) | 1990-09-03 |
Family
ID=12607329
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1041400A Pending JPH02219987A (en) | 1989-02-20 | 1989-02-20 | Heat accumulator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH02219987A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5259214A (en) * | 1990-11-08 | 1993-11-09 | Mitsubishi Denki Kabushiki Kaisha | Air conditioning system |
| WO2017183413A1 (en) * | 2016-04-22 | 2017-10-26 | 三菱電機株式会社 | Regenerative heat exchanger |
-
1989
- 1989-02-20 JP JP1041400A patent/JPH02219987A/en active Pending
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5259214A (en) * | 1990-11-08 | 1993-11-09 | Mitsubishi Denki Kabushiki Kaisha | Air conditioning system |
| WO2017183413A1 (en) * | 2016-04-22 | 2017-10-26 | 三菱電機株式会社 | Regenerative heat exchanger |
| JPWO2017183413A1 (en) * | 2016-04-22 | 2018-04-26 | 三菱電機株式会社 | Thermal storage heat exchanger |
| JP2018105616A (en) * | 2016-04-22 | 2018-07-05 | 三菱電機株式会社 | Thermal storage heat exchanger |
| CN109073327A (en) * | 2016-04-22 | 2018-12-21 | 三菱电机株式会社 | Accumulation of heat heat-exchange device |
| EP3428566A4 (en) * | 2016-04-22 | 2019-04-10 | Mitsubishi Electric Corporation | HEAT EXCHANGER WITH REGENERATION |
| CN109073327B (en) * | 2016-04-22 | 2020-09-04 | 三菱电机株式会社 | Heat storage and exchange device |
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