JPS6240622B2 - - Google Patents

Info

Publication number
JPS6240622B2
JPS6240622B2 JP54160568A JP16056879A JPS6240622B2 JP S6240622 B2 JPS6240622 B2 JP S6240622B2 JP 54160568 A JP54160568 A JP 54160568A JP 16056879 A JP16056879 A JP 16056879A JP S6240622 B2 JPS6240622 B2 JP S6240622B2
Authority
JP
Japan
Prior art keywords
heat
storage container
pipe
heat storage
medium
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
Application number
JP54160568A
Other languages
Japanese (ja)
Other versions
JPS5682387A (en
Inventor
Takashi Sakai
Naojiro Pponda
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.)
Sanyo Electric Co Ltd
Original Assignee
Sanyo Electric Co 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 Sanyo Electric Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP16056879A priority Critical patent/JPS5682387A/en
Publication of JPS5682387A publication Critical patent/JPS5682387A/en
Publication of JPS6240622B2 publication Critical patent/JPS6240622B2/ja
Granted 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
    • Y02E10/00Energy generation through renewable energy sources
    • Y02E10/40Solar thermal energy, e.g. solar towers
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/14Thermal energy storage

Landscapes

  • Other Air-Conditioning Systems (AREA)

Description

【発明の詳細な説明】 この発明は太陽熱冷暖房蓄熱装置に関し、さら
に詳しくは蓄熱材として金属水素化物を充填した
蓄熱容器と貯蔵容器とからなる蓄熱システム、こ
れら2種類の容器にそれぞれ熱交換用ヒートパイ
プが内設され、各ヒートパイプが各容器より外部
に延出され、それぞれの端部が各々2分された熱
交換器室にまたがつて内設され、さらに前記2容
器が、開閉弁を介して水素輸送管で連結されると
共に前記の貯蔵容器用の2分された熱交換器室の
一つの室内を通過し開閉弁を有するもう一つの水
素輸送管で連結され、前記熱交換器室を太陽熱コ
レクターシステムに連結したことを特徴とする太
陽熱冷暖房蓄熱装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a solar heating and cooling heat storage device, and more specifically, a heat storage system consisting of a heat storage container filled with a metal hydride as a heat storage material and a storage container, and a heat exchanger heat storage system for each of these two types of containers. A pipe is installed inside, each heat pipe is extended to the outside from each container, each end is installed inside the heat exchanger chamber divided into two, and the two containers further have an on-off valve. The heat exchanger chamber is connected to the heat exchanger chamber through a hydrogen transport pipe, and is connected to the heat exchanger chamber by another hydrogen transport pipe which passes through one of the two halves of the heat exchanger chamber for the storage container and has an on-off valve. The present invention relates to a solar heating and cooling heat storage device, characterized in that it is connected to a solar heat collector system.

この発明は、近年注目されている太陽熱冷暖房
蓄熱装置において、その蓄熱系として長期蓄熱が
可能な特定の化学物質を用いる化学蓄熱システム
が組込まれたものであり、現在使用されている水
蓄熱法よりも優れた太陽熱冷暖房蓄熱装置を提供
するものである。
This invention incorporates a chemical heat storage system that uses a specific chemical substance capable of long-term heat storage as a heat storage system in a solar heating and cooling heat storage device that has been attracting attention in recent years, and is superior to the currently used water heat storage method. It also provides an excellent solar heating, cooling, and heat storage device.

この発明による装置の特徴は(イ)蓄熱材料として
アンモニウム化合物、水酸化物、金属水素化物等
の中から、太陽熱の集熱温度の観点から金属水素
化物を選定したこと、(ロ)金属水素化物の熱交換に
際して、熱負荷を作動させる熱媒体で直接熱交換
させずに蓄熱室および貯蔵室に内設したヒートパ
イプを通じて熱交換を行なうよう構成したこと、
(ハ)前記2室より延出させたヒートパイプの端部に
熱交換器室を設けたこと、(ニ)熱交換器室は場合に
より2分して高温熱媒体(例えば油)と低温媒体
(例えば水)との二つの異なる熱媒体を通じて太
陽熱の蓄熱および放熱のための熱交換を可能なら
しめるよう構成したこと、(ホ)蓄熱容器と貯蔵容器
とが開閉弁を介して水素輸送管で連結されると共
に貯蔵容器用の2分された熱交換器室の一つの室
内を通過し開閉弁を有するもう一つの水素輸送管
で連結されたこと等が挙げられる。
The features of the device according to this invention are (a) metal hydrides are selected from among ammonium compounds, hydroxides, metal hydrides, etc. as heat storage materials from the viewpoint of solar heat collection temperature, and (b) metal hydrides are used as heat storage materials. When exchanging heat, the heat exchange is performed through heat pipes installed in the heat storage chamber and the storage chamber, without directly exchanging heat with the heat medium that operates the heat load;
(c) A heat exchanger chamber is provided at the end of the heat pipe extending from the two chambers, and (d) the heat exchanger chamber may be divided into two parts to accommodate a high-temperature heat medium (e.g. oil) and a low-temperature medium. (e) The heat storage container and the storage container are connected to a hydrogen transport pipe via an on-off valve. For example, the two hydrogen transport pipes are connected to each other and pass through one of the two divided heat exchanger rooms for the storage container, and are connected by another hydrogen transport pipe having an on-off valve.

この発明の特徴の中で(ホ)の2種類の水素輸送管
を設置するには、蓄熱時と熱再生時に対応させて
区別して使用することができ、熱再生時に生成す
る水素化熱をより有効に取り出すことが可能とな
る効果を有する。
Among the features of this invention, in order to install two types of hydrogen transport pipes (e), they can be used separately for heat storage and heat regeneration, and the heat of hydrogenation generated during heat regeneration can be used more efficiently. This has the effect of making it possible to take it out effectively.

この発明の装置の利点その他は更に以下の説明
で明らかにされるであろう。
Advantages and other advantages of the device of the invention will become clearer from the description below.

第1図を用いてこの発明を説明するが、この発
明の装置は、蓄熱システムと太陽熱コレクターシ
ステムに大別される。
The present invention will be explained using FIG. 1, and the apparatus of the present invention can be broadly classified into a heat storage system and a solar heat collector system.

先ず蓄熱システムについて述べれば、水素化反
応熱の大きい金属水素化物M1H(M1:金属また
は合金、H:水素)3、例えばCaNi5H6等を収納
した蓄熱容器1、水素化反応熱の比較的小さい金
属水素化物M2H4、例えばLaNi5H6等を収納した
貯蔵容器2によつて基本的に構成されている。蓄
熱容器1と貯蔵容器2には、それぞれ熱交換用ヒ
ートパイプ(好ましくはフイン付)7,8が内設
され、また前記各容器から外部へ延出させたヒー
トパイプの端部が熱交換器室9,10に内設され
るよう構成されている。また熱交換器室9,10
は、それぞれ仕切り板11,12によつて2室に
分けられ、ヒートパイプ7,8の端部は仕切り板
11,12を貫通して内設されている。また蓄熱
容器1と貯蔵容器2とは開閉弁5を介して水素輸
送管6で連結されると共に貯蔵容器用の2分され
た熱交換器室210の一つの室(後期の高温熱媒
体が循環する室)内を通過し開閉弁24を有する
もう一つの水素輸送管25で連結されている。前
記各熱交換器室の2分された各室には、高温熱媒
体または低温熱媒体が別々に循環し、ヒートパイ
プへの熱交換を可能ならしめるよう太陽熱コレク
ターシステムに連結されている。
First, let's talk about the heat storage system: a heat storage container 1 containing a metal hydride M 1 H (M 1 : metal or alloy, H: hydrogen) 3, e.g. CaNi 5 H 6 , which has a large hydrogenation reaction heat; It basically consists of a storage vessel 2 containing a relatively small metal hydride M2H4 , such as LaNi5H6 . Heat exchange heat pipes (preferably with fins) 7 and 8 are installed inside the heat storage container 1 and the storage container 2, respectively, and the ends of the heat pipes extending outside from each of the containers serve as heat exchangers. It is configured to be installed inside the chambers 9 and 10. In addition, heat exchanger rooms 9 and 10
is divided into two chambers by partition plates 11 and 12, respectively, and the ends of the heat pipes 7 and 8 are installed inside by penetrating the partition plates 11 and 12. In addition, the heat storage container 1 and the storage container 2 are connected by a hydrogen transport pipe 6 via an on-off valve 5, and one chamber of a heat exchanger chamber 210 divided into two for the storage container (in which the high-temperature heat medium in the latter half is circulated). The hydrogen transport pipe 25 passes through the inside of the hydrogen transport chamber) and is connected to the hydrogen transport pipe 25 by another hydrogen transport pipe 25 having an on-off valve 24. Each of the two halves of the heat exchanger chambers is connected to a solar collector system in which a high temperature heat medium or a low temperature heat medium is circulated separately and allows heat exchange to the heat pipes.

一方、太陽熱コレクターシステムは、太陽熱コ
レクター13で集めた熱エネルギーを熱媒体によ
つて輸送する循環熱媒体輸送管14,15,16
および熱負荷17より基本的に構成されている。
前記輸送管14,15,16には熱媒体を輸送す
るためのポンプ18,19,20が設置されてい
る。前記輸送管14,15は高温熱媒体、例えば
油を、また16は低温熱媒体、例えば水を循環輸
送するためのものである。
On the other hand, the solar heat collector system includes circulating heat medium transport pipes 14, 15, 16 that transport the heat energy collected by the solar heat collector 13 using a heat medium.
and a heat load 17.
Pumps 18, 19, 20 for transporting the heat medium are installed in the transport pipes 14, 15, 16. The transport pipes 14 and 15 are for circulating and transporting a high-temperature heat medium, such as oil, and the pipe 16 is for circulating and transporting a low-temperature heat medium, such as water.

太陽熱コレクターとしては特に限定はないが、
高性能のコレクターの使用が望ましく、例えばフ
レネルレンズの併用、ヒートパイプとフレネルレ
ンズとの併用が挙げられる。この場合温度レベル
が100℃以上になるので、集熱媒体〔前記循環熱
媒体輸送管14,15内を循環する熱媒体〕とし
ては油を使用するのが便利であり、150〜200℃の
集熱も可能である。このような温度レベルにおい
て冷房は通常の吸収式冷凍機等で行なうことがで
き、一方暖房は市水と熱交換することによつて適
温まで下げて行なうことができる。
There are no particular limitations as a solar collector, but
It is desirable to use a high-performance collector, such as a combination of a Fresnel lens or a combination of a heat pipe and a Fresnel lens. In this case, since the temperature level is 100°C or higher, it is convenient to use oil as the heat collecting medium [the heating medium circulating in the circulating heat medium transport pipes 14 and 15], and the temperature level is 150 to 200°C. Heat is also possible. At such a temperature level, cooling can be performed using a normal absorption refrigerator, etc., while heating can be performed by lowering the temperature to an appropriate level by exchanging heat with city water.

以下、このシステムの作動について述べる。 The operation of this system will be described below.

(a) 太陽熱により加熱された熱媒体の熱量が、熱
負荷(冷暖房機)を稼動させてなお余る場合 太陽熱コレクター13により加熱された熱媒
体(油)は、ポンプ18によつて循環熱媒体輸
送管14(実線)を循環し熱負荷17を作動さ
せ、次いで熱交換器室19の2分された一室を
通つて熱交換された余剰の熱量は、ヒートパイ
プ7を通じて蓄熱容器1に移動する。この熱量
によつて蓄熱容器1内の蓄熱材M1H3が分解
し発生した水素は、開閉弁5を開いて水素輸送
管6を通つて貯蔵容器2に送られる。なお熱交
換器室19を出た熱媒体(油)は循環熱媒体輸
送管14によつて太陽熱コレクター13にもど
される。M1Hより発生した水素は貯蔵容器2
内のM2と反応し反応熱を放出するので〔但
し、蓄熱容器1内の金属水素化物M1Hによる
熱量の放出速度より遅い〕、M2を冷却してでき
るだけ低い水素圧で放出させるようにする。こ
のためポンプ21によつて冷却水輸送管22を
通じて冷却水を熱交換室210の2分された一
室に送つてヒートパイプ8を通じてM2を冷却
し、排水管23にて排水する。かようにして
M1Hの分解によつて発生した水素が円滑にM2
と結合し蓄熱が行なわれる。
(a) When the amount of heat of the heat medium heated by solar heat remains even after operating the heat load (air conditioner) The heat medium (oil) heated by the solar heat collector 13 is circulated and transported by the pump 18 The excess heat circulated through the pipe 14 (solid line) to activate the heat load 17 and then exchanged heat through one of the two halves of the heat exchanger chamber 19 is transferred to the heat storage container 1 through the heat pipe 7. . The heat storage material M 1 H3 in the heat storage container 1 is decomposed by this amount of heat, and the generated hydrogen is sent to the storage container 2 through the hydrogen transport pipe 6 by opening the on-off valve 5 . Note that the heat medium (oil) leaving the heat exchanger chamber 19 is returned to the solar heat collector 13 by the circulating heat medium transport pipe 14. The hydrogen generated from M 1 H is stored in storage container 2.
Since the reaction heat is released by reacting with M 2 in the heat storage container 1 (however, the rate of release of heat is slower than that of the metal hydride M 1 H in the heat storage container 1), it is necessary to cool M 2 and release it at the lowest possible hydrogen pressure. Make it. For this purpose, the pump 21 sends cooling water through the cooling water transport pipe 22 to one of the two halves of the heat exchange chamber 210, cools M 2 through the heat pipe 8, and drains it through the drain pipe 23. like this
Hydrogen generated by the decomposition of M 1 H is smoothly converted to M 2
Heat is stored by combining with

(b) 太陽熱により加熱された熱媒体の熱量が熱負
荷(冷暖房機)を稼動させるのに不足する場合 この場合、太陽熱コレクター13で集めた熱
エネルギーを直接、冷暖房負荷17には使用で
きないので、貯蔵容器2中にM2Hとして貯え
られている水素を蓄熱容器1に移動させM1
反応させて発生した熱量を使用する。このた
め、太陽熱コレクター13で加熱された熱媒体
(油)はポンプ19によつて循環熱媒体輸送管
15を通つて熱交換器室210の2分されたも
う一つの室に送られ熱交換して循環する。交換
された熱エネルギーは、ヒートパイプ8を通つ
て貯蔵容器2内の金属水素化物M2H4に供給
されM2Hより水素が速やかに放出される。こ
の水素は、開閉弁24を開き水素輸送管25に
よつて、熱交換器室210の2分された室のう
ち熱媒体(油)が循環されている方の室に送ら
れ、室温近傍まで加熱されてから蓄熱容器1に
送られる。かくして蓄熱容器1内でM1+H→
M1H+△Hの反応が起り△Hの熱量が発生す
る。この時、貯蔵容器2中でM2Hより水素を
発生させる反応が吸熱反応であるため発生した
水素は冷却されている。それ故にこの水素をそ
のまゝ蓄熱容器1に送つてM1と反応させる
と、発生する水素化熱の熱量は前記吸熱反応で
失われた熱量分だけ少ないことになる。従つて
本発明の装置では、前記したように、貯蔵容器
2内でM2Hより発生させた水素を、水素輸送
管25によつて熱交換器室2に送り一旦室温近
傍まで加熱することによつて前記吸熱反応によ
る熱量の減少を補い集熱した太陽熱を有効に利
用するものである。またあまり高温の水素は金
属M1を速やかに加熱しH+M1→M1H+△Hの
反応をおさえるようになるが室温近傍の温度の
水素はかえつてこの反応を速やかに行わせる。
(b) When the amount of heat of the heat medium heated by solar heat is insufficient to operate the heat load (air-conditioning machine) In this case, the thermal energy collected by the solar collector 13 cannot be directly used for the air-conditioning load 17. Hydrogen stored as M 2 H in the storage container 2 is transferred to the heat storage container 1 and reacted with M 1 to use the generated heat. For this reason, the heat medium (oil) heated by the solar collector 13 is sent by the pump 19 through the circulating heat medium transport pipe 15 to another chamber divided into two parts of the heat exchanger chamber 210 for heat exchange. and circulate. The exchanged thermal energy is supplied to the metal hydride M 2 H4 in the storage container 2 through the heat pipe 8, and hydrogen is rapidly released from the M 2 H. This hydrogen is sent to the chamber in which the heat medium (oil) is circulated among the two halves of the heat exchanger chamber 210 by opening the on-off valve 24 and sending it through the hydrogen transport pipe 25 until it reaches near room temperature. After being heated, it is sent to the heat storage container 1. Thus, M 1 +H→ in the heat storage container 1
The reaction of M 1 H + △H occurs and the amount of heat of △H is generated. At this time, since the reaction that generates hydrogen from M 2 H in the storage container 2 is an endothermic reaction, the generated hydrogen is cooled. Therefore, if this hydrogen is directly sent to the heat storage container 1 and reacted with M1 , the amount of heat of hydrogenation generated will be reduced by the amount of heat lost in the endothermic reaction. Therefore, in the apparatus of the present invention, as described above, hydrogen generated from M 2 H in the storage container 2 is sent to the heat exchanger chamber 2 through the hydrogen transport pipe 25 and heated to near room temperature. Therefore, the reduction in heat due to the endothermic reaction is compensated for and the collected solar heat is effectively utilized. Further, hydrogen at too high a temperature quickly heats the metal M 1 and suppresses the reaction H+M 1 →M 1 H+△H, but hydrogen at a temperature near room temperature instead causes this reaction to occur quickly.

このようにして発生させた熱エネルギーは、ヒ
ートパイプ7を通つて熱交換器室19の2分した
もう一つの室に移動し、熱媒体(水)を加熱しこ
の熱媒体はポンプ20によつて循環熱媒体輸送管
16を通つて熱負荷17に送られこの熱負荷を作
動させる。このように、集熱量が不足する場合
は、集熱量が熱負荷を作動させるのに必要な量を
越える際に蓄熱しておいた熱エネルギーを放出し
て熱負荷を作動させることができる。
The heat energy generated in this way moves through the heat pipe 7 to another chamber divided into two parts of the heat exchanger chamber 19, heats the heat medium (water), and this heat medium is pumped by the pump 20. The heat medium is then sent to the heat load 17 through the circulating heat medium transport pipe 16 to operate this heat load. In this manner, when the amount of heat collection is insufficient, the stored thermal energy can be released to operate the heat load when the amount of heat collection exceeds the amount required to operate the heat load.

この発明においては、上記に説明したようにヒ
ートパイプを熱交換に用いているが、これによつ
て次のような利点が得られる。即ち熱媒体輸送管
を直接蓄熱容器および貯蔵容器に挿入した場合
は、前記輸送管が細くなることから、特に水を熱
媒体として使用する場合、錆や水垢が付着しやす
くなり、充分な加熱、冷却効果が期待できず、ま
た輸送管が細くなると熱媒体に加わる圧力損失が
大きく熱媒体の流量が減少して熱交換を充分に行
ないにくい。これに対してヒートパイプは熱伝導
率、均熱性が良好で水垢等が発生せず熱輸送に対
して極めて有利である。
In this invention, a heat pipe is used for heat exchange as explained above, and the following advantages can be obtained thereby. That is, when a heat medium transport pipe is directly inserted into a heat storage container or a storage container, the transport pipe becomes thin, so rust and water scale are likely to adhere, especially when water is used as a heat medium, and sufficient heating or No cooling effect can be expected, and if the transport pipe becomes thin, the pressure loss applied to the heat medium will be large and the flow rate of the heat medium will decrease, making it difficult to perform sufficient heat exchange. On the other hand, heat pipes have good thermal conductivity and heat uniformity, do not generate limescale, and are extremely advantageous for heat transport.

さらに前記のごとく、蓄熱容器、貯蔵容器とは
別個に熱交換器室を設けたことによる利点として
は、次のようなものがある。即ち金属水素化物を
収納した各容器とヒートパイプを一体化してお
き、熱交換器室を取換え可能な構造とすれば、金
属水素化物を収納した容器自体の掃除等のメイン
テナンスの必要がなく、熱交換器室だけの掃除で
充分であり、システム全体のメインテナンスが容
易になる。
Furthermore, as mentioned above, the advantages of providing the heat exchanger chamber separately from the heat storage container and the storage container include the following. In other words, if each container containing metal hydride and the heat pipe are integrated and the heat exchanger chamber is constructed to be replaceable, there is no need for maintenance such as cleaning the container itself containing metal hydride. It is sufficient to clean only the heat exchanger room, making maintenance of the entire system easier.

また前記熱交換器室は仕切り板で2分され、高
温熱媒体または低温熱媒体が別々に循環して熱交
換が行なわれ、同一の熱交換器室で種類の異なる
熱媒体(水と油等)によつて熱交換を行なう場合
のように熱媒体が混合し、太陽熱コレクターの性
能に悪影響を与えるということがなくメインテナ
ンス上極めて有利である。
The heat exchanger room is divided into two by a partition plate, and heat exchange is performed by circulating high-temperature heat medium or low-temperature heat medium separately, and different types of heat medium (water, oil, etc.) can be used in the same heat exchanger room. ), unlike when heat exchange is performed, the heat medium is mixed and does not adversely affect the performance of the solar heat collector, which is extremely advantageous in terms of maintenance.

以上のごとく、この発明の太陽熱冷暖房蓄熱装
置は、従来用いられている水蓄熱法に代つて長期
蓄熱システムを組込んだ太陽熱冷暖房蓄熱装置と
して画期的な装置であると言える。
As described above, the solar heating and cooling heat storage device of the present invention can be said to be an epoch-making device as a solar heating and cooling heat storage device that incorporates a long-term heat storage system in place of the conventionally used water heat storage method.

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

第1図は本発明の太陽熱冷暖房蓄熱装置の具体
例を示す説明図である。 1…蓄熱容器、2…貯蔵容器、3,4…金属水
素化物、5,24…開閉弁、6,25…水素輸送
管、7,8…ヒートパイプ、9,10…熱交換器
室1及び2、11,12…仕切り板、13…太陽
熱コレクター、14,15,16…循環熱媒体輸
送管、17…冷暖房熱負荷、18,19,20,
21…ポンプ、22…冷却水輸送管、23…排水
管。
FIG. 1 is an explanatory diagram showing a specific example of the solar heating and cooling heat storage device of the present invention. 1... Heat storage container, 2... Storage container, 3, 4... Metal hydride, 5, 24... Open/close valve, 6, 25... Hydrogen transport pipe, 7, 8... Heat pipe, 9, 10... Heat exchanger chamber 1 and 2, 11, 12... Partition plate, 13... Solar heat collector, 14, 15, 16... Circulating heat medium transport pipe, 17... Air conditioning heat load, 18, 19, 20,
21... Pump, 22... Cooling water transport pipe, 23... Drain pipe.

Claims (1)

【特許請求の範囲】 1 蓄熱材として金属水素化物を充填した蓄熱容
器と貯蔵容器とからなる蓄熱システム、これら2
種類の容器にそれぞれ熱交換用ヒートパイプが内
設され、各ヒートパイプが各容器より外部に延出
され、それぞれの端部が各々2分された熱交換器
室にまたがつて内設され、さらに前記2容器が、
開閉弁を介して水素輸送管で連結されると共に前
記の貯蔵容器用の2分された熱交換器室の一つの
室内を通過し開閉弁を有するもう一つの水素輸送
管で連結され、前記熱交換器室を太陽熱コレクタ
ーシステムに連結したことを特徴とする太陽熱冷
暖房蓄熱装置。 2 熱交換器室が高温熱媒体と低温熱媒体とをそ
れぞれ独立に循環しうるよう2分され、蓄熱容器
および貯蔵容器より外部へ延出させた各ヒートパ
イプの端部が2分されたそれぞれの室にまたがつ
て内設してなる特許請求の範囲第1項記載の太陽
熱冷暖房蓄熱装置。
[Scope of Claims] 1. A heat storage system consisting of a heat storage container filled with metal hydride as a heat storage material and a storage container;
A heat exchange heat pipe is installed in each type of container, each heat pipe is extended to the outside from each container, and each end is installed internally astride a heat exchanger chamber divided into two, Furthermore, the two containers are
The hydrogen transport pipe is connected via an on-off valve, and the hydrogen transport pipe passes through one of the two halves of the heat exchanger chamber for the storage container and is connected with another hydrogen transport pipe having an on-off valve. A solar heating and cooling heat storage device characterized in that an exchanger room is connected to a solar heat collector system. 2 The heat exchanger room is divided into two parts so that the high temperature heat medium and the low temperature heat medium can be circulated independently, and the ends of the heat storage container and each heat pipe extending outside from the storage container are divided into two parts. 2. A solar heating and cooling heat storage device according to claim 1, which is installed internally across a room.
JP16056879A 1979-12-10 1979-12-10 Regenerator for solar-heat heating and cooling Granted JPS5682387A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16056879A JPS5682387A (en) 1979-12-10 1979-12-10 Regenerator for solar-heat heating and cooling

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16056879A JPS5682387A (en) 1979-12-10 1979-12-10 Regenerator for solar-heat heating and cooling

Publications (2)

Publication Number Publication Date
JPS5682387A JPS5682387A (en) 1981-07-06
JPS6240622B2 true JPS6240622B2 (en) 1987-08-28

Family

ID=15717781

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16056879A Granted JPS5682387A (en) 1979-12-10 1979-12-10 Regenerator for solar-heat heating and cooling

Country Status (1)

Country Link
JP (1) JPS5682387A (en)

Also Published As

Publication number Publication date
JPS5682387A (en) 1981-07-06

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