JPS6248160B2 - - Google Patents
Info
- Publication number
- JPS6248160B2 JPS6248160B2 JP56152069A JP15206981A JPS6248160B2 JP S6248160 B2 JPS6248160 B2 JP S6248160B2 JP 56152069 A JP56152069 A JP 56152069A JP 15206981 A JP15206981 A JP 15206981A JP S6248160 B2 JPS6248160 B2 JP S6248160B2
- Authority
- JP
- Japan
- Prior art keywords
- heat
- hydrogen gas
- metal hydride
- storage tank
- holding container
- 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
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 34
- 229910052987 metal hydride Inorganic materials 0.000 claims description 30
- 150000004681 metal hydrides Chemical class 0.000 claims description 30
- 238000005338 heat storage Methods 0.000 claims description 8
- 238000010438 heat treatment Methods 0.000 claims 1
- 239000001257 hydrogen Substances 0.000 description 7
- 229910052739 hydrogen Inorganic materials 0.000 description 7
- 239000012530 fluid Substances 0.000 description 5
- 230000001052 transient effect Effects 0.000 description 4
- 238000000034 method Methods 0.000 description 3
- 230000007423 decrease Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 150000002431 hydrogen Chemical class 0.000 description 2
- 229910010340 TiFe Inorganic materials 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
- 239000002918 waste heat Substances 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
- F28D20/003—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using thermochemical reactions
-
- 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)
- 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)
Description
【発明の詳細な説明】
この発明は、金属水素化物を利用した蓄熱シス
テムに関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a heat storage system using metal hydrides.
TiFe.CaNi5等の水素貯蔵金属は活性化(水素
化)することにより金属水素化物となり、大量の
水素を吸・脱蔵し、吸蔵過程では発熱し、脱蔵過
程では吸熱することが知られている。金属水素化
物のこの性質を利用して、太陽熱、風力等の自然
エネルギーや工場廃熱等を水素ガスの形で蓄積
し、必要に応じて安定した熱を取出すことの出来
る蓄熱システムを作ることができる。 It is known that hydrogen storage metals such as TiFe.CaNi 5 become metal hydrides when activated (hydrogenated) and absorb and devolatilize large amounts of hydrogen, emitting heat during the occlusion process and endothermic during the devolatilization process. ing. Utilizing this property of metal hydrides, it is possible to create a heat storage system that can store natural energy such as solar heat, wind power, industrial waste heat, etc. in the form of hydrogen gas and extract stable heat as needed. can.
この原理にもとずく従来の蓄熱システムは、第
1図に示す如く、金属水素化物1の保持容器2と
水素ガス貯槽3及びこれらを接続する水素ガス導
管4を有し、金属保持容器2の熱交換部5には、
太陽熱等の外部熱源6及び温室等の熱利用装置7
内の放熱器8と夫々熱媒体流体管を介して接続さ
れる熱交換手段9,10が設けられており、又前
記の水素ガス導管4には止弁11が設けられてい
る。 A conventional heat storage system based on this principle, as shown in FIG. In the heat exchange section 5,
External heat source 6 such as solar heat and heat utilization device 7 such as a greenhouse
Heat exchange means 9 and 10 are provided which are connected to the radiator 8 inside via heat medium fluid pipes, and the hydrogen gas conduit 4 is provided with a stop valve 11.
このシステムを利用して太陽熱等の熱を蓄積
し、利用するには外部熱源6の熱を熱媒体流体を
介して熱交換手段9より保持容器2内の金属水素
化物1に伝達して加熱し、金属水素化物1より水
素ガスを脱蔵させ、止弁11を開いた水素ガス導
管4を経て、水素ガス貯槽3に貯蓄し、熱を利用
する場合は水素ガス貯槽より保持容器2に水素ガ
スを流入させて金属水素化物1に吸蔵させ、その
際発生する熱を熱交換手段10を介して熱媒体流
体に伝達し、放熱器8より熱利用装置7内に放出
して利用する。 This system is used to accumulate and utilize heat such as solar heat by transmitting the heat from the external heat source 6 to the metal hydride 1 in the holding container 2 through the heat transfer means 9 via the heat medium fluid to heat it. , hydrogen gas is devolatilized from the metal hydride 1, stored in the hydrogen gas storage tank 3 through the hydrogen gas conduit 4 with the stop valve 11 opened, and when heat is to be used, hydrogen gas is transferred from the hydrogen gas storage tank to the holding container 2. is caused to flow into the metal hydride 1, and the heat generated at this time is transferred to the heat medium fluid via the heat exchange means 10, and is released from the radiator 8 into the heat utilization device 7 for use.
上記の従来の熱利用方法においては、水素吸蔵
運転時の初期の生成熱は金属水素化物1自体及び
耐圧容器として構成された熱容量の大きい金属水
素化物保持容器2の昇温に費やされ、熱利用装置
7に熱を運搬する熱媒体流体によつて目標温度の
熱が定常的に取出される迄、かなり長い過渡特性
域が出来る。 In the conventional heat utilization method described above, the initial heat generated during hydrogen storage operation is used to raise the temperature of the metal hydride 1 itself and the metal hydride holding container 2, which has a large heat capacity and is configured as a pressure-resistant container. A fairly long transient characteristic region is created until heat at the target temperature is steadily extracted by the heat carrier fluid that conveys the heat to the utilization device 7.
熱利用の面からは、過度特性域を極力短かく
し、目標温度の熱が長時間定常的に得られること
が好都合であり、又、金属水素化物の有限な発熱
量の有効利用の点からもそれが望ましい。 From the perspective of heat utilization, it is advantageous to shorten the transient characteristic range as much as possible so that heat at the target temperature can be obtained steadily for a long period of time, and from the point of view of effective use of the limited calorific value of metal hydrides. That's desirable.
本発明は、従来の金属水素化物を利用した蓄熱
システムの上述の欠点にかんがみ、過渡特性域を
なくして常に所定の目標温度の熱を取出すことの
出来る、金属水素化物を利用した蓄熱システムを
提供することを目的とする。 In view of the above-mentioned drawbacks of conventional heat storage systems using metal hydrides, the present invention provides a heat storage system using metal hydrides that eliminates transient characteristic regions and can always extract heat at a predetermined target temperature. The purpose is to
以下に本発明を、その実施例を示す図面にもと
ずいて詳細に説明する。 The present invention will be described in detail below based on drawings showing embodiments thereof.
第2図は、本発明を第1図で説明したシステム
に適用した実施例であつて、金属水素化物保持容
器2と水素ガス貯槽3とを接続する水素ガス導管
4に従来のシステムでは設けられていた止め弁1
1の代りにオリフイス12と、水素ガス貯槽3か
ら金属水素化物保持容器2に向う方向にのみ流通
可能な逆止弁14とが直列に金属水素化物保持容
器2から水素ガス貯槽3に向う方向にのみ流通可
能な逆止弁13がそれらと並列に設けられてい
る。上記オリフイス12は、金属水素化物保持容
器2への水素ガスの流入量を制限し、金属水素化
物の水素吸蔵による発熱量を制御するためのもの
である。その他の構成は前述の従来のシステムと
同様である。 FIG. 2 shows an embodiment in which the present invention is applied to the system described in FIG. Stop valve 1
1, an orifice 12 and a check valve 14 that can flow only in the direction from the hydrogen gas storage tank 3 to the metal hydride storage container 2 are connected in series in the direction from the metal hydride storage container 2 to the hydrogen gas storage tank 3. A check valve 13 that allows only flow is provided in parallel thereto. The orifice 12 is used to limit the amount of hydrogen gas flowing into the metal hydride holding container 2 and to control the amount of heat generated by hydrogen storage in the metal hydride. The rest of the configuration is similar to the conventional system described above.
以上の如く構成されたシステムは次の如く使用
される。熱利用装置7に熱を必要とするときに、
太陽熱等による外部熱源6から熱が得られる場合
は、熱交換手段9より金属水素化物に与えられた
熱は、もう一方の熱交換手段10より熱媒体流体
に回収されると同時に残余の熱は金属水素化物を
加熱して水素ガスを分離し、水素ガス導管4を経
て水素ガス貯槽3に貯蔵される。この際水素ガス
は逆止弁13を自由に通過することができる。熱
利用装置7が熱を利用しないときは、熱源からの
熱はすべて金属水素化物の水素脱蔵に使われる。 The system configured as described above is used as follows. When the heat utilization device 7 requires heat,
When heat is obtained from an external heat source 6 such as solar heat, the heat given to the metal hydride by the heat exchange means 9 is recovered by the heat medium fluid from the other heat exchange means 10, and at the same time the remaining heat is removed. The metal hydride is heated to separate hydrogen gas, which is stored in a hydrogen gas storage tank 3 via a hydrogen gas conduit 4. At this time, hydrogen gas can freely pass through the check valve 13. When the heat utilization device 7 does not utilize heat, all the heat from the heat source is used for hydrogen devolatilization of the metal hydride.
熱源6は太陽熱、風力等の自然エネルギーや工
場廃熱を利用しているので、天候、昼夜、工場の
操業状態によつて発生熱量が変動する。熱利用装
置7が利用する熱量又は非使用時に金属水素化物
1を所定の温度に維持するに必要とする熱量より
も、熱源6の発生熱量が不足する場合は金属水素
化物の温度が低下し、水素を吸蔵し保持容器2内
の水素ガス圧力が下るので、水素ガス貯槽3より
オリフイス12を通つて水素ガスが金属水素化物
保持容器2に供給され、金属水素化物1に吸蔵さ
れて発熱し、所定の温度を維持することができ
る。この場合、逆止弁13は閉じているので水素
ガスの流量はオリフイス12により適度に制御さ
れ金属水素化物保持容器の圧力の過昇、過熱は防
止される。 Since the heat source 6 uses natural energy such as solar heat or wind power or factory waste heat, the amount of heat generated fluctuates depending on the weather, day and night, and the operating status of the factory. If the amount of heat generated by the heat source 6 is insufficient than the amount of heat used by the heat utilization device 7 or the amount of heat required to maintain the metal hydride 1 at a predetermined temperature when not in use, the temperature of the metal hydride decreases, As hydrogen is stored and the hydrogen gas pressure in the holding container 2 decreases, hydrogen gas is supplied from the hydrogen gas storage tank 3 to the metal hydride holding container 2 through the orifice 12, is stored in the metal hydride 1, and generates heat. A predetermined temperature can be maintained. In this case, since the check valve 13 is closed, the flow rate of hydrogen gas is appropriately controlled by the orifice 12, and excessive rise in pressure and overheating of the metal hydride holding container are prevented.
以上の如く、本発明によれば熱利用装置が熱を
利用する場合にも非利用時にも、熱源の余剰熱量
が水素の形で貯蓄され、不足時に熱として放出さ
れ、あたかも液圧装置におけるアキユムレータの
如く働き、変動の多い熱源の熱を必要時に過渡特
性域を経ることなく常に所定の目標温度の定常的
な熱に変換して利用することができる。 As described above, according to the present invention, the surplus heat of the heat source is stored in the form of hydrogen, whether the heat utilization device uses heat or not, and is released as heat when there is a shortage. It works as follows, and the heat from the heat source, which fluctuates frequently, can be converted into steady heat at a predetermined target temperature and used whenever necessary without passing through the transient characteristic range.
第1図は従来の金属水素化物利用蓄熱システム
の一例を示す系統図、第2図は本発明の実施例の
系統図である。
1……金属水素化物、2……保持容器、3……
水素ガス貯槽、4……水素ガス導管、6……熱
源、7……熱利用装置、12……オリフイス、1
3,14……逆止弁。
FIG. 1 is a system diagram showing an example of a conventional heat storage system using metal hydrides, and FIG. 2 is a system diagram of an embodiment of the present invention. 1... Metal hydride, 2... Holding container, 3...
Hydrogen gas storage tank, 4...Hydrogen gas conduit, 6...Heat source, 7...Heat utilization device, 12...Orifice, 1
3,14...Check valve.
Claims (1)
よりこれを加熱して水素ガスを脱蔵させ、水素ガ
ス導管を介して水素ガス貯槽に移送して蓄積し、
必要に応じて該水素ガス貯槽より上記水素ガス導
管を通じて上記金属水素化物保持容器に水素ガス
を流入させ金属水素化物に吸蔵させてその際発生
する反応熱を利用する蓄熱システムにおいて、前
記の水素ガス導管にオリフイスと上記水素ガス貯
槽から金属水素化物保持容器に向う方向にのみ流
通可能な逆止弁とを直列に金属水素化物保持容器
から水素ガス貯槽に向う方向にのみ流通可能な逆
止弁をそれらと並列に設けたことを特徴とする蓄
熱システム。1. Holding a metal hydride in a container, heating it with an external heat source to devolatilize hydrogen gas, and transferring it to a hydrogen gas storage tank via a hydrogen gas conduit to accumulate it;
In a heat storage system in which hydrogen gas is caused to flow into the metal hydride holding container from the hydrogen gas storage tank through the hydrogen gas conduit as necessary, the hydrogen gas is occluded by the metal hydride, and the reaction heat generated at that time is utilized. A check valve that allows flow only in the direction from the metal hydride holding container to the hydrogen gas storage tank is connected in series with an orifice in the conduit and a check valve that allows flow only in the direction from the hydrogen gas storage tank to the metal hydride holding container. A heat storage system characterized by being installed in parallel with these.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56152069A JPS5855688A (en) | 1981-09-28 | 1981-09-28 | Heat accumulating system utilizing hydrogenated metal |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56152069A JPS5855688A (en) | 1981-09-28 | 1981-09-28 | Heat accumulating system utilizing hydrogenated metal |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5855688A JPS5855688A (en) | 1983-04-02 |
JPS6248160B2 true JPS6248160B2 (en) | 1987-10-12 |
Family
ID=15532369
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP56152069A Granted JPS5855688A (en) | 1981-09-28 | 1981-09-28 | Heat accumulating system utilizing hydrogenated metal |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5855688A (en) |
Cited By (1)
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Families Citing this family (40)
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---|---|---|---|---|
JPS6055769U (en) * | 1983-09-26 | 1985-04-18 | マツダ株式会社 | engine heating device |
JPS61202051A (en) * | 1985-03-01 | 1986-09-06 | Daido Steel Co Ltd | Solar energy utilizing device |
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-
1981
- 1981-09-28 JP JP56152069A patent/JPS5855688A/en active Granted
Cited By (1)
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---|---|---|---|---|
US9733106B2 (en) | 2013-05-24 | 2017-08-15 | Allegro Microsystems, Llc | Magnetic field sensor to detect a magnitude of a magnetic field in any direction |
Also Published As
Publication number | Publication date |
---|---|
JPS5855688A (en) | 1983-04-02 |
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