JPS5949492A - Heat accumulating tank and heat accumulating system utilizing hydrogenated metal - Google Patents

Heat accumulating tank and heat accumulating system utilizing hydrogenated metal

Info

Publication number
JPS5949492A
JPS5949492A JP57159673A JP15967382A JPS5949492A JP S5949492 A JPS5949492 A JP S5949492A JP 57159673 A JP57159673 A JP 57159673A JP 15967382 A JP15967382 A JP 15967382A JP S5949492 A JPS5949492 A JP S5949492A
Authority
JP
Japan
Prior art keywords
heat
tank
hydrogen
temperature
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.)
Granted
Application number
JP57159673A
Other languages
Japanese (ja)
Other versions
JPS6223239B2 (en
Inventor
Kenji Nasako
名迫 賢二
Ikuro Yonezu
育郎 米津
Naojiro Honda
本田 直二郎
Takashi Sakai
貴史 酒井
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.)
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
Agency of Industrial Science and Technology
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 Agency of Industrial Science and Technology filed Critical Agency of Industrial Science and Technology
Priority to JP57159673A priority Critical patent/JPS5949492A/en
Publication of JPS5949492A publication Critical patent/JPS5949492A/en
Publication of JPS6223239B2 publication Critical patent/JPS6223239B2/ja
Granted legal-status Critical Current

Links

Classifications

    • 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
    • F28D20/003Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using thermochemical reactions
    • 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
    • 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
    • Y02E70/00Other energy conversion or management systems reducing GHG emissions
    • Y02E70/30Systems combining energy storage with energy generation of non-fossil origin

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
  • Sorption Type Refrigeration Machines (AREA)

Abstract

PURPOSE:To rise the reference temperature of the hydrogenated metal from the level of room temperature to the level of heat exhausting temperature and reduce the sensitive heat loss of a pressure resistant vessel upon heat dissipation by a constitution wherein a hydrogenated metal tank is covered by a heat insulating layer and the outside thereof is covered by a temperature keeping tank while a low-qualitied heat exhausting medium is passed through the temperature keeping tank. CONSTITUTION:The temperature keeping tank 4 is provided at the outside of the hydrogenated metal tank 2 of the pressure resistant vessel through the heat insulating layer 3 while the tank 4 is provided with a low-qualitied heat exhausting medium introducing tube 5 and the discharging tube 6 of the same. One end of the hydrogenated metal tank 2 is connected to a heat exchanger 7 provided with a heat medium introducing tube 8 and the discharging tube 9 of the same. Upon dissipating heat, the heat exhausting medium is passed previously through both of the temperature keeping tank 4 and the heat exchanger 7 by the heat medium introducing tube and the discharging tubes 5, 6, 8, 9 to rise the reference temperature of the whole of the hydrogenated metal tank 2 from the level of the room temperature to the level of the heat exhausting temperature and, thereafter, hydrogen is introduced through a hydrogen transfer tube 10.

Description

【発明の詳細な説明】 この発明は金属水素化物槽の外(il+に断熱層を介し
て低質熱源の低質排熱媒体を通過ζせうる保温槽を枠管
し、金6水素化物の基準温度を室温レベルから排熱温度
レベルまで上昇させうるようにした蓄熱槽、並びにこの
蓄熱槽を用いた蓄熱システムであって、その放熱過程に
おいて該低質排熱IIL体を月1いて水素化反応による
熱を高p1コ度レベルで有効に回収しうみように構成さ
れfc蓄熱システムに関する。
DETAILED DESCRIPTION OF THE INVENTION This invention provides a frame tube for a heat insulating tank through which a low-quality waste heat medium from a low-quality heat source can pass through a heat insulating layer outside the metal hydride tank. A heat storage tank capable of raising temperature from room temperature to exhaust heat temperature level, and a heat storage system using this heat storage tank, which uses the low-quality waste heat IIL in the heat dissipation process once a month to generate heat from hydrogenation reaction. The present invention relates to an FC heat storage system configured to effectively recover heat at high P1C levels.

あるf重の金h7!や合金は液体水素と同等あるいはそ
れ以上の密度で水素貯蔵が可能であり、新しい水素の貯
蔵側とじ−C注目さh−でいる。 ゛りた金属水素化物
は単に水素を貯蔵するという特性を有するばかりでなく
、水素という化学エネルギーを熱あるいは機械エネルギ
ーに変換するためのエネルギー変換材料としてのG、l
)能を有し、単位体積あたりの蓄熱量U従来のに1′心
9、へ型や潜熱型蓄熱材料に比べ10倍程度になるもの
もるるため、熱の貯蔵、輸送、ヒートポンプ、太陽熱利
用の冷暖房給湯システム、熱fi& +3+i+、コン
プレッサー、ポンプなどの媒体として大いに期待されて
いる。
A certain f-heavy gold h7! Hydrogen and alloys are capable of storing hydrogen at densities equal to or higher than that of liquid hydrogen, and are attracting attention as a new hydrogen storage area. Metal hydrides that have been depleted have the property of not only storing hydrogen, but also as energy conversion materials for converting the chemical energy of hydrogen into heat or mechanical energy.
), and the amount of heat storage per unit volume is about 10 times that of conventional heat storage materials. It is highly expected to be used as a medium for air conditioning, heating, and hot water systems, heat Fi&+3+i+, compressors, pumps, etc.

金属水素化物を利用したx熱システムは現在開発段階に
あるが、固体(合金)と気体(水素)の反応であるため
、気体の流量制御のみにより全体システムを制御できる
利点がある。
The x-thermal system using metal hydrides is currently in the development stage, but since it involves a reaction between a solid (alloy) and a gas (hydrogen), it has the advantage that the entire system can be controlled only by controlling the gas flow rate.

しかし加圧水素を使用するために金属水嵩化物槽は耐圧
容器でなければならないという欠点のため放熱過程で高
温度レベルの熱を敗り出す場合、蓄熱槽の’A温に費や
される熱量が犬きくなり蓄熱量に対する回収熱情の割合
が小はくなる。 オだ蓄熱(曹全体が昇温された後熱回
11qさi]、るが、この場合においても槽全体が高温
度レベルに糾持孕i7、るため、熱回収が行われている
間、周囲に散逸する熱量も無視できない程大きなものと
なる。
However, in order to use pressurized hydrogen, the metal water bulk tank must be a pressure-resistant container, so when high-temperature level heat is dissipated during the heat dissipation process, the amount of heat expended at the 'A temperature of the heat storage tank is extremely low. As a result, the ratio of recovery passion to heat storage becomes smaller. However, even in this case, the entire tank remains at a high temperature level, so while heat recovery is being performed, The amount of heat dissipated to the surroundings is too large to be ignored.

この発明は、上記のような耐圧容器の顕熱ロスおよび周
囲に散逸する熱ロスを極力少なくするためになされたも
のであって、一端に水素出入導管を有する金り水素化物
槽と、この槽の他端に接設されるj・、;シフi、換器
と、この槽の少なくとも他端を除く部分を8贋う断熱層
とを備え、更にこの断熱層の外(1111に保温槽を4
%看し、この保温槽に低質排熱媒体を通過させることに
よって金属水素化物槽の基準温度を上昇できるようにし
てなる蓄熱槽を4是供するものである。
This invention was made in order to minimize the sensible heat loss of the pressure vessel as described above and the heat loss dissipated to the surroundings. It is equipped with a heat exchanger connected to the other end, and a heat insulating layer that covers at least a portion of the tank excluding the other end, and a heat insulating tank is installed outside the heat insulating layer (1111). 4
%, and four heat storage tanks are provided in which the reference temperature of the metal hydride tank can be raised by passing a low-quality waste heat medium through the heat storage tank.

この発明の蓄熱(曹は、金属水嵩化物槽をItli熱層
で(;シいさらにその外1111に保温槽を覆着−ゼ、
この保温(i(’Iに低質排熱媒体を通過させつるよう
に構成され、金属水素化物の基準温度を室温レベルから
排熱湛〃〔レベル寸で上昇させうろことを特徴とずZ)
ものである。
The heat storage of this invention is to cover the metal water bulk compound tank with a thermal layer (;
This heat insulation (i) is configured to allow a low-quality waste heat medium to pass through it, and is characterized by scales that raise the reference temperature of the metal hydride from the room temperature level to the waste heat level.
It is something.

さらにこの発明は、上記蓄熱れ:すと、一端に水素出入
導管を有し他端に熱交換器を装着しかつ金8水素化物を
充宿しfc水素貯蔵槽とを、それぞれの水素出入導管を
開閉弁を介して連結することによって連結し;余剰熱媒
体を、蓄熱槽の熱交換器に開閉弁を介して通過さぜる余
剰熱操体移送管路、冷却媒体を、水素貯1i’−t、′
1の熱交換器に開閉弁を介して通過させる冷却媒体移送
管路、並びに低質排熱媒体を、蓄熱槽の熱交換器と該蓄
熱41ニジの保温槽と水素貯蔵槽の熱交換器とに開閉弁
を介して通過させる排熱媒体移送管路を有する蓄熱シス
テムを提供するものである。
Furthermore, the present invention provides a method for connecting the heat storage tank with a hydrogen inlet/output conduit at one end and a heat exchanger at the other end, and a fc hydrogen storage tank charged with gold 8 hydride. The excess heat medium is connected to the hydrogen storage 1i' by connecting it through an on-off valve; −t,′
A cooling medium transfer pipe to pass through the heat exchanger No. 1 via an on-off valve, and a low-quality waste heat medium to the heat exchanger of the heat storage tank, the heat storage tank of the heat storage 41, and the heat exchanger of the hydrogen storage tank. The present invention provides a heat storage system having a pipe for transferring waste heat medium through an on-off valve.

この発明の蓄熱システムは、上記の蓄熱槽を用い、放熱
過程において、低質排熱媒体を3方向に分岐させ、蓄熱
槽の保温槽と熱交P2!器および水素貯IR槽の熱交換
器に同時に通過させて水素化反応による熱を高τIA 
ll’ルベルて有効に回収できるように1占成されたも
のである。
The heat storage system of the present invention uses the above-mentioned heat storage tank, and in the heat dissipation process, branches the low-quality waste heat medium into three directions, and exchanges heat with the heat retention tank of the heat storage tank P2! The heat from the hydrogenation reaction is passed through the heat exchanger of the hydrogen storage IR tank and the hydrogen storage IR tank at the same time to achieve a high τIA.
It is occupied by one so that it can be collected effectively.

まf(この発明によれば、放熱時の耐圧q−7器のシ1
11庁・〜ロスは、低質14ト熱により予め蓄に”s 
4¥’i全体を室温レベルから排熱温度レベル寸で」二
列、させているkめに非常に小さくなる。 寸た周囲に
散迫シするrsロスは蓄熱4i’!l中の金属水嵩化物
槽1゛々の周囲温度を排??′シ渦度しベル捷で上昇さ
せているため非常に小さくなる。 さらにこの蓄熱シス
テムはヒートポンプとしても応用できる。
(According to this invention, the pressure resistant Q-7 device during heat dissipation is
11 Agency ~ Loss is stored in advance due to low quality 14 heat.
4\'i The whole is made from the room temperature level to the exhaust heat temperature level in two rows, and the kth becomes very small. RS loss scattered around the area is heat storage 4i'! Is the ambient temperature of each metal water voluminous compound tank 1 in 1 discharged? ? The vorticity becomes very small because it is raised by the bell switch. Furthermore, this heat storage system can also be used as a heat pump.

次にこの発明を図面で#Yしく説明する。Next, this invention will be explained in detail with reference to the drawings.

第1図はこの発明の一実施例の蓄熱槽(])の11キ断
面図を示す。
FIG. 1 shows a cross-sectional view of a heat storage tank ( ) according to an embodiment of the present invention.

すなわち耐圧容器の金属水素化物槽(21の外側に断熱
層(3)を介して保温槽(4)が設i?iされ、この保
温槽(4)は低質排熱媒体導入管(5)と同排出管(6
)を有する。 また金属水素化物槽(2)の一端には、
熱々(1体導入管(8)と同排出管(91を有する熱交
換器(7)が接設されている。 そして放熱時には予め
排熱媒体を保温槽(4]と熱交換器(7)との両者に、
ぞれぞれのtJシ媒媒体式入管よび排出管(5)101
 (81(91によって通過させて金属水素化物4′:
!/ (2+全体の基準温度を室温L/べルから排π1
(温度レベルまで上ゲトさせ、その後水素移送管器を通
じて水素を導入する。
That is, a heat insulating tank (4) is installed on the outside of the metal hydride tank (21) of the pressure-resistant container via a heat insulating layer (3), and this heat insulating tank (4) is connected to the low-quality waste heat medium introduction pipe (5). The same discharge pipe (6
). Also, at one end of the metal hydride tank (2),
A heat exchanger (7) having one inlet pipe (8) and one discharge pipe (91) is connected to the heat exchanger (7).When releasing heat, the waste heat medium is transferred to the heat retention tank (4) and the heat exchanger (7) in advance. and to both,
Each tJ medium type inlet and outlet pipe (5) 101
(81 (metal hydride 4' passed by 91:
! / (2 + overall reference temperature from room temperature L/bell
(Let it rise to temperature level, then introduce hydrogen through the hydrogen transfer tube.

第2図1−1この発明の一実施例の蓄執!(槽(111
の金に78水素化物槽(NJ [(+3 :断J層+ 
041 :保温131 、 OFQ :1′j′−交]
会器〕と、西”シ交換器(1Gが一端に接設された水素
貯蔵m11171とを11−閉弁+]i11を介して水
素移送管路Illで連結してなるこの発明の一実施例の
蓄熱システムの構成説明し1である。 t20+は低質
排熱媒体移送管路、121)は冷却117、体移送管路
、(〃は余剰熱媒体移送管路、シ31 (241(25
1(2r、lは開閉弁、勾は負荷部である。
Fig. 2 1-1 Aspiration of an embodiment of this invention! (tank (111
78 hydride tank (NJ [(+3: Fault J layer +
041: Heat retention 131, OFQ: 1'j'-cross]
An embodiment of the present invention in which a hydrogen storage m11171 with a west side exchanger (1G connected to one end) is connected by a hydrogen transfer pipe Ill via a 11-closed valve +]i11. The structure of the heat storage system is explained in 1. t20+ is a low-quality waste heat medium transfer pipe, 121) is a cooling 117, body transfer pipe, (〃 is a surplus heat medium transfer pipe,
1 (2r, l are on-off valves, gradient is a load section.

蓄熱時には、まず開閉弁(2)++ (251mを閉じ
開閉弁(24+を開き、低質排熱ρ11(体を、低質排
熱媒体移送管路201によって蓄熱槽(111の保温槽
04)と熱交換器09とに送って通過させて金属水素化
物槽O4の温度を低質熱媒体の温度レベルまで上昇させ
ておく。 次いで開閉弁Q4)を閉じ開閉弁島)開いて
全1jll熱媚体をそのf8送管路(イ)によって熱交
換器(liに送って通過させて金属水素化物の脱水素化
反応を起こさせ発生した水素を水ネ移送管路u9)を辿
じ開かれた開閉弁+IP−を介して水素貯蔵槽0力に送
られる。 同時に開閉弁開)を開いて冷却媒体を水素貯
蔵槽(17)のp、へ交1<(器(161に送って通過
させて水素貯蔵槽07)内の金属水素物を冷却し、蓄熱
槽(111から送られた水床による水素化が行なわれ、
蓄熱が行わ第1る。 このように蓄ρ〜僧内の金に4水
素化物を排p7%u体の潟jW寸で予め!1温ζせてか
ら蓄熱できるので余剰熱クリ□体から無#なく熱を回収
することができる。
During heat storage, first close the on-off valve (2)++ (251m), open the on-off valve (24+), and exchange heat with the heat storage tank (thermal tank 04 of 111) through the low-quality waste heat medium transfer pipe 201. The temperature of the metal hydride tank O4 is raised to the temperature level of the low-quality heat medium by passing through the metal hydride tank 09.Then, the on-off valve Q4) is closed and the on-off valve Q4) is opened to transfer all 1 jll thermal bodies to that f8. Hydrogen generated by causing a dehydrogenation reaction of the metal hydride by being sent to the heat exchanger (li) through the water transfer pipe (a) and passing through the water transfer pipe (u9) to the opened on-off valve +IP- At the same time, the opening/closing valve is opened and the cooling medium is sent to the hydrogen storage tank (17) and passed through the hydrogen storage tank (161). ) is cooled and hydrogenated using the water bed sent from the heat storage tank (111).
First, heat storage occurs. In this way, the tetrahydride is discharged to the gold in the p7% u form in advance with the size of the p7%u body! Since heat can be stored after the body has cooled by one temperature, heat can be recovered from the surplus heat cream body without waste.

一方、放熱時は、開閉弁[25+(至)を閉じ、開閉弁
(23)し4)を開いて排熱媒体を熱交換器010υと
保温槽04)に送って通過させて水素貯蔵槽+17)と
蓄熱槽(1])全体をt71熱睨1体の温度1で上昇ζ
せた後に、1ノ11閉弁(IIζ)を開き水素移送管E
1!1によって水素貯蔵槽gηから金8水素化物槽θり
に水素を移動させる。 その結果金に4水素化物4’;
V (+2中の金属水素化物の水素化が行われ熱が発生
し、その熱エネルギーμ蓄ぷIy 41”i p+、%
父ドア1器09に伝達され熱媒体は拮・熱温度レベルよ
りさらに7′!l温度になり負荷面に供給される。
On the other hand, during heat dissipation, close the on-off valve [25+ (to), open the on-off valve (23) and open the on-off valve (4) to send the waste heat medium to the heat exchanger 010υ and heat retention tank 04), and let it pass through the hydrogen storage tank +17. ) and the heat storage tank (1]), the temperature of one t71 heat lamp increases by 1 ζ
After that, open the 1/11 closing valve (IIζ) and close the hydrogen transfer pipe E.
1!1, hydrogen is transferred from the hydrogen storage tank gη to the gold 8-hydride tank θ. As a result, gold has tetrahydride 4';
The metal hydride in V (+2 is hydrogenated and heat is generated, and the thermal energy μ is stored Iy 41”i p+, %
The heat medium is transferred to the first door 09 and the temperature is 7' higher than the other heat temperature level! l temperature and is supplied to the load surface.

このようにこの蓄熱システムは従来得ることが国難でβ
つた高温度レベルの熱を効率よく回収することができる
In this way, this heat storage system has traditionally been difficult to obtain due to the national crisis.
It is possible to efficiently recover heat at a high temperature level.

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

第1図はこの発明の蓄熱槽の一実施例のtc1断面図、
第2図はこの発明の蓄を1−システムの一実施例の(j
q成装91図である。 (1) Ill 、、、蓄熱槽、(21(12−・・金
り水素化物恰、(31(1:6 =−断熱層、(41(
141−、保温槽、(7)0!′DllG・・・r?1
〜交換器、(5)(81・・・熱111.l:体導入管
路、f61t9+・・・熱媒体排出管路、(1(I +
191・・・水素移送管路、+171・・・水素貯R槽
、11111 G!:ll [24+ (δ)Q6)・
・・開閉弁、121+1・・・低質排熱媒体移送管路、
2+1・・・冷却媒体移送管路、(221・・・余11
熱媒体移送管路、シフ)・・・負荷部。
FIG. 1 is a tc1 sectional view of an embodiment of the heat storage tank of the present invention,
FIG. 2 shows the accumulation of this invention in one embodiment of the 1-system (j
It is a 91 diagram of q construction. (1) Ill, , thermal storage tank, (21(12-...gold hydride, (31(1:6 =-insulating layer, (41(
141-, heat retention tank, (7) 0! 'DllG...r? 1
~Exchanger, (5) (81...Heat 111.l: Body introduction pipe, f61t9+...Heat medium discharge pipe, (1(I +
191...Hydrogen transfer pipe, +171...Hydrogen storage R tank, 11111 G! :ll [24+ (δ)Q6)・
...Opening/closing valve, 121+1...Low quality waste heat medium transfer pipe,
2+1...Cooling medium transfer pipe, (221...Remaining 11
Heat medium transfer pipe, schiff)...Load section.

Claims (1)

【特許請求の範囲】 J、一端に水素出入導管を有する金属水素化物相と、こ
の(・17の他端に接設される熱交換器と、この槽の少
なくとも他端を除く部分を覆う断熱層とを備え、更にこ
の断熱層の外側に保温槽を覆着し、この保温も′1に低
質排熱媒体を通過させることによって金属水素化物相の
9i’; ’A〜温度を上昇できるようにしてなる蓄熱
40゜ 2、一端に水素出入者、管を有する金す水不化物槽と、
この槽の他端に接設される熱交換器と、この槽の少なく
とも他端を除く部分な拉うUr#層とを備え、更にこの
断熱層の外側に保温槽7を覆着してなる蓄熱覆j1と、
一端に水素出入導管を有し他端に熱交換器を装着しかつ
金属水素化物を充填した水素貯Xt4?ffとを、それ
ぞれの水素出入導管を開閉弁を介して連結することによ
って連結し; 余剰熱媒体を、蓄熱槽の熱交換器に開閉弁を介して通過
させる余剰熱媒体移送管路、冷却媒体を、水素貯蔵槽の
A−へ交換器に開閉弁を介して通過させる冷却媒体移送
管路、並びに低質排熱媒体を、蓄熱槽の熱交換器と該蓄
熱槽の保温槽と水素貯蔵槽の熱交換器とに開閉弁を介し
て通過させる排熱媒体移送管路を有する蓄熱システム。
[Scope of Claims] J, a metal hydride phase having a hydrogen inlet/output pipe at one end, a heat exchanger connected to the other end of this (17), and a heat insulator covering at least a portion of this tank except for the other end. Furthermore, a heat insulating tank is covered on the outside of this heat insulating layer, and the temperature of the metal hydride phase can be increased by passing a low-quality waste heat medium through '1'. a metal water impurity tank having a heat storage 40°2, a hydrogen inlet/output member, and a pipe at one end;
It is equipped with a heat exchanger connected to the other end of this tank, and an Ur# layer covering at least a portion of the tank excluding the other end, and furthermore, a heat insulating tank 7 is covered on the outside of this heat insulating layer. A heat storage cover j1,
Hydrogen storage Xt4 with a hydrogen inlet/output pipe at one end, a heat exchanger installed at the other end, and filled with metal hydride? ff by connecting each hydrogen inlet/output conduit via an on-off valve; Excess heat medium transfer pipe line for passing the excess heat medium to the heat exchanger of the heat storage tank via the on-off valve, and cooling medium. A cooling medium transfer line for passing the low-quality waste heat medium to A- of the hydrogen storage tank through an on-off valve, and a heat exchanger for the heat storage tank, a heat insulating tank for the heat storage tank, and a hydrogen storage tank. A heat storage system that has a heat exchanger and a waste heat medium transfer pipe that is passed through an on-off valve.
JP57159673A 1982-09-16 1982-09-16 Heat accumulating tank and heat accumulating system utilizing hydrogenated metal Granted JPS5949492A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57159673A JPS5949492A (en) 1982-09-16 1982-09-16 Heat accumulating tank and heat accumulating system utilizing hydrogenated metal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57159673A JPS5949492A (en) 1982-09-16 1982-09-16 Heat accumulating tank and heat accumulating system utilizing hydrogenated metal

Publications (2)

Publication Number Publication Date
JPS5949492A true JPS5949492A (en) 1984-03-22
JPS6223239B2 JPS6223239B2 (en) 1987-05-21

Family

ID=15698827

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57159673A Granted JPS5949492A (en) 1982-09-16 1982-09-16 Heat accumulating tank and heat accumulating system utilizing hydrogenated metal

Country Status (1)

Country Link
JP (1) JPS5949492A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60138330A (en) * 1983-12-26 1985-07-23 Taada:Kk Flame adjusting device of gas apparatus
JPH0350413A (en) * 1989-07-14 1991-03-05 Rinnai Corp Control device for combustion apparatus

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60138330A (en) * 1983-12-26 1985-07-23 Taada:Kk Flame adjusting device of gas apparatus
JPH02609B2 (en) * 1983-12-26 1990-01-08 Harman Co Ltd
JPH0350413A (en) * 1989-07-14 1991-03-05 Rinnai Corp Control device for combustion apparatus

Also Published As

Publication number Publication date
JPS6223239B2 (en) 1987-05-21

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