JPH0436081B2 - - Google Patents

Info

Publication number
JPH0436081B2
JPH0436081B2 JP60010775A JP1077585A JPH0436081B2 JP H0436081 B2 JPH0436081 B2 JP H0436081B2 JP 60010775 A JP60010775 A JP 60010775A JP 1077585 A JP1077585 A JP 1077585A JP H0436081 B2 JPH0436081 B2 JP H0436081B2
Authority
JP
Japan
Prior art keywords
metal hydride
heat
heat transfer
holder
hydrogen
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 - Lifetime
Application number
JP60010775A
Other languages
Japanese (ja)
Other versions
JPS61171998A (en
Inventor
Masayuki Kurooka
Kenji Nasako
Naojiro Pponda
Takashi Sakai
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 JP60010775A priority Critical patent/JPS61171998A/en
Publication of JPS61171998A publication Critical patent/JPS61171998A/en
Publication of JPH0436081B2 publication Critical patent/JPH0436081B2/ja
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen; Reversible storage of hydrogen
    • C01B3/0005Reversible storage of hydrogen, e.g. by hydrogen getters or electrodes
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C11/00Use of gas-solvents or gas-sorbents in vessels
    • F17C11/005Use of gas-solvents or gas-sorbents in vessels for hydrogen
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/12Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
    • F28F1/24Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely
    • 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
    • F28D21/00Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D2021/0019Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
    • F28D2021/0047Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for hydrogen or other compressed gas storage tanks
    • 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
    • Y02E60/30Hydrogen technology
    • Y02E60/32Hydrogen 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • Y02P20/129Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Organic Chemistry (AREA)
  • Thermal Sciences (AREA)
  • Geometry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
  • Hydrogen, Water And Hydrids (AREA)

Description

【発明の詳細な説明】 (イ) 産業上の利用分野 本発明は水素貯蔵器、蓄熱器、ヒートポンプ等
に好適な金属水素化物容器に関する。
DETAILED DESCRIPTION OF THE INVENTION (a) Field of Industrial Application The present invention relates to a metal hydride container suitable for hydrogen storage devices, heat storage devices, heat pumps, and the like.

(ロ) 従来の技術 金属水素化物は大量の水素ガスを吸収、放出す
る能力を有し、その水素ガスの吸収、放出の際に
は、かなりの熱量を放出、吸収することが知られ
ている。これらの性質を利用して現在、金属水素
化物の蓄熱器や水素貯蔵器等への適用が盛んに試
みられている。尚、金属水素化物は脱水素化して
金属となるが、この場合も含めて本明細書中では
金属水素化物と称する。
(b) Prior art Metal hydrides have the ability to absorb and release large amounts of hydrogen gas, and are known to release and absorb a considerable amount of heat when absorbing and releasing hydrogen gas. . Utilizing these properties, there are currently many attempts to apply metal hydrides to heat storage devices, hydrogen storage devices, and the like. Note that a metal hydride becomes a metal by dehydrogenation, and this case is also referred to as a metal hydride in this specification.

この場合、金属水素化物は水素圧力下での反応
が進められることから耐圧容器が必要となる。ま
た、金属水素化物の特性用効率を上げるには容器
全体の顕熱による熱損失を抑制する必要がある。
In this case, since the metal hydride undergoes a reaction under hydrogen pressure, a pressure-resistant container is required. Furthermore, in order to increase the efficiency of the properties of the metal hydride, it is necessary to suppress heat loss due to sensible heat throughout the container.

これらの点を考慮して、従来、例えば特開昭58
―90号公報に見られるように、耐圧容器内部に断
熱材層を形成し、その内部に金属水素化物を熱交
換用流体管と共に収納するようにしたものが提案
されている。
Taking these points into consideration, conventionally, for example,
- As seen in Publication No. 90, it has been proposed that a heat insulating material layer is formed inside a pressure-resistant container, and a metal hydride is housed therein together with a heat exchange fluid pipe.

しかしながら、一般に金属水素化物は水素の吸
収、放出を繰り返すうちに微粉化し、最終的には
数ミクロンの粉末になる。このため、上記従来の
容器構造によると、金属水素化物の粉末の一部が
断熱材層の間隙に飛散侵入し、設計通りの熱交換
効率が得られなくなる。また、一般に金属水素化
物は熱伝導率が小さいため、伝熱促進を図るため
の伝熱フインを設けることが必要となるが、上記
従来構造のものに複雑な形状の伝熱フインを設け
ると、金属水素化物を容器内部に均一に分配収納
することが困難になる欠点があつた。
However, metal hydrides generally become pulverized as they repeatedly absorb and release hydrogen, eventually becoming a powder of several microns. Therefore, according to the conventional container structure described above, a part of the metal hydride powder scatters and enters the gap between the heat insulating layers, making it impossible to obtain the designed heat exchange efficiency. In addition, since metal hydrides generally have low thermal conductivity, it is necessary to provide heat transfer fins to promote heat transfer, but if heat transfer fins with a complicated shape are provided in the conventional structure described above, There was a drawback that it was difficult to uniformly distribute and store the metal hydride inside the container.

(ハ) 発明が解決しようとする問題点 本発明は上記従来技術の欠点を除き、熱交換効
率の優れた金属水素化物容器を提供することを目
的とする。
(c) Problems to be Solved by the Invention An object of the present invention is to eliminate the drawbacks of the above-mentioned prior art and provide a metal hydride container with excellent heat exchange efficiency.

(ニ) 問題点を解決するための手段 このため本発明は、耐圧容器内に水素流路を介
在させて金属水素化物を保持する保持体を設け水
素流路への金属水素化物粉末の飛散を防止すると
共に、前記金属水素化物保持体上面には金属水素
化物投入口を設け、容器内部の熱媒経路に取り付
けた伝熱フイン間に金属水素化物を均一に分配収
納し得るようにしたことを特徴としている。
(d) Means for Solving the Problems Therefore, the present invention provides a holder for holding metal hydride with a hydrogen flow path interposed in a pressure-resistant container to prevent metal hydride powder from scattering into the hydrogen flow path. In addition, a metal hydride inlet is provided on the top surface of the metal hydride holder, so that the metal hydride can be evenly distributed and stored between the heat transfer fins attached to the heat medium path inside the container. It is a feature.

(ホ) 作用 金属水素化物保持体を設け、金属水素化物を伝
熱フイン付き伝熱管と共にその内部に納めること
により、金属水素化物の飛散を防止することがで
きると共に、伝熱管を流れる熱媒と金属水素化物
との間の熱伝達は伝熱フインを介して円滑に行な
われる。また、耐圧容器と金属水素化物保持体と
の間は水素流路が存在することにより耐圧容器へ
の熱流出が防止され、容器による顕熱損失が抑制
される。また、金属水素化物は保持体上面に設け
た投入口より保持体内部に伝熱フインの存在にも
拘わらず均一に収納することができる。
(E) Effect By providing a metal hydride holding body and storing the metal hydride therein together with the heat transfer tube with heat transfer fins, it is possible to prevent the metal hydride from scattering, and also to prevent the heat medium flowing through the heat transfer tube. Heat transfer between the metal hydride and the metal hydride is carried out smoothly through the heat transfer fins. Further, since a hydrogen flow path exists between the pressure vessel and the metal hydride holder, heat leakage to the pressure vessel is prevented, and sensible heat loss due to the vessel is suppressed. Furthermore, the metal hydride can be uniformly stored inside the holder through the inlet provided on the upper surface of the holder despite the presence of heat transfer fins.

(ヘ) 実施例 以下、本発明の実施例を図面を参照して説明す
る。
(f) Examples Examples of the present invention will be described below with reference to the drawings.

第1図は本発明の一実施例に係る金属水素化物
容器の断面図を示したもので、1は耐圧容器であ
る。この耐圧容器1は金属水素化物2を収納する
容器本体部11と蓋部12とから成り、そのフラ
ンジ部11a,12aをボルト3、ナツト4で接
合することにより、内部を気密、耐圧的に保持し
ている。その耐圧容器1の本体側端面11bと蓋
部12のほぼ中央部を気密に貫通して熱媒を流す
伝熱管5が配設されると共に、更に蓋部12には
水素ガスを供給、排出する水素出入導管6が形成
されている。
FIG. 1 shows a sectional view of a metal hydride container according to an embodiment of the present invention, and 1 is a pressure container. This pressure-resistant container 1 consists of a container body 11 that stores a metal hydride 2 and a lid 12, and its flange portions 11a and 12a are joined with bolts 3 and nuts 4 to maintain an airtight and pressure-resistant interior. are doing. A heat transfer tube 5 is disposed that airtightly penetrates the main body side end surface 11b of the pressure vessel 1 and the approximate center of the lid 12 to flow a heat medium, and further supplies and discharges hydrogen gas to the lid 12. A hydrogen inlet/outlet conduit 6 is formed.

耐圧容器1内部には水素流路7が形成されてお
り、その内側に金属水素化物2が伝熱フイン8と
共に金属水素化物保持体9によつて伝熱管5の周
囲に保持されている。
A hydrogen flow path 7 is formed inside the pressure vessel 1, and the metal hydride 2 is held around the heat transfer tube 5 by a metal hydride holding body 9 together with heat transfer fins 8 inside the hydrogen flow path 7.

第2図a〜cは、それぞれ上記金属水素化物保
持体9の平面図、正面図、右側面図を示したもの
で、金属水素化物保持体9は金属水素化物2を保
持する本体部9aと蓋部9bより成り、本体部9
aは、例えば金属水素化物保持体9の直径10cm、
長さ1m規模の場合、厚み1mm程度のステンレス
板で形成され、その円筒面上には金属水素化物投
入口10が設けられる。但し、この金属水素化物
投入口10は後述するように金属水素化物保持体
9内に金属水素化物2を投入充填後閉鎖される。
蓋部9bは水素を通すが金属水素化物は通し得な
いフイルタ板で構成される。なお、この場合、本
体部9aの端面9cもフイルタ板で構成しても良
く、更に、本体部9aを含めて全体をフイルタ板
で構成しても良い。
2a to 2c show a plan view, a front view, and a right side view of the metal hydride holder 9, respectively, and the metal hydride holder 9 has a main body portion 9a that holds the metal hydride 2 It consists of a lid part 9b and a main body part 9.
a is, for example, the diameter of the metal hydride support 9 of 10 cm,
In the case of a scale of 1 m in length, it is formed of a stainless steel plate with a thickness of about 1 mm, and a metal hydride inlet 10 is provided on the cylindrical surface of the stainless steel plate. However, this metal hydride inlet 10 is closed after the metal hydride 2 is charged and filled into the metal hydride holding body 9, as will be described later.
The lid portion 9b is composed of a filter plate that allows hydrogen to pass through but not metal hydrides. In this case, the end surface 9c of the main body portion 9a may also be constructed from a filter plate, and furthermore, the entire body including the main body portion 9a may be constructed from a filter plate.

以上の構成で、金属水素化物容器を組み立てる
場合は、先ず、伝熱管5に例えばアルミ合金製の
伝熱フイン8を溶接する。この伝熱フイン8は、
中心部に伝熱管5の外径寸法に対応する穴を設け
て円板状に形成しておき、これを伝熱管5に通
し、一定間隔に配置した上溶接することにより、
簡単に配置、形成することができる。
When assembling a metal hydride container with the above configuration, first, heat transfer fins 8 made of, for example, an aluminum alloy are welded to the heat transfer tube 5. This heat transfer fin 8 is
By forming a disk shape with a hole corresponding to the outer diameter of the heat transfer tube 5 in the center, passing it through the heat transfer tube 5, and welding it at regular intervals,
Easy to place and form.

次に、端面9cの中心部に伝熱フイン8と同様
の穴を有する保持体9の本体部9aを伝熱管5に
通すと同時に、その反対側からは保持体9の蓋部
9bを伝熱管5に通し、内部に伝熱フイン8を収
容した状態で、本体部側面9c、蓋部9b、伝熱
管5間の接合部を溶接し、保持体9を形成する。
Next, the main body part 9a of the holder 9, which has a hole similar to the heat transfer fins 8 in the center of the end surface 9c, is passed through the heat exchanger tube 5, and at the same time, from the opposite side, the lid part 9b of the holder 9 is inserted into the heat exchanger tube. 5, and with the heat transfer fins 8 housed inside, the joints between the main body side surface 9c, the lid portion 9b, and the heat transfer tubes 5 are welded to form the holder 9.

その保持体9の本体部9aの円筒面上に設けら
れる金属水素化物投入口10から金属水素化物2
を各伝熱フイン8間に均一に入れる。金属水素化
物2を収納後は金属水素化物の保持を完全にする
ため、金属水素化物投入口10を閉塞する。
The metal hydride 2 is fed from the metal hydride inlet 10 provided on the cylindrical surface of the main body 9a of the holder 9.
Evenly place between each heat transfer fin 8. After storing the metal hydride 2, the metal hydride inlet 10 is closed in order to completely retain the metal hydride.

次に、伝熱管5上に保持体9を形成するのと同
じ要領で、耐圧容器1の本体部11と蓋部12と
を互いに伝熱管5に反対方向から通す。そのフラ
ンジ部11a,12aをボルト3、ナツト4で締
め付け接合すると共に、容器本体側端面11b、
蓋部12と伝熱管5との間を溶接等で接合するこ
とにより金属水素化物容器を組み立てることがで
きる。
Next, in the same manner as forming the holder 9 on the heat exchanger tube 5, the main body 11 and the lid 12 of the pressure container 1 are passed through the heat exchanger tube 5 from opposite directions. The flanges 11a and 12a are tightened and joined with bolts 3 and nuts 4, and the container body side end surface 11b,
The metal hydride container can be assembled by joining the lid portion 12 and the heat exchanger tube 5 by welding or the like.

尚、金属水素化物2は水素ガスの吸収、放出を
繰り返すうち次第に微粉化して熱交換効率が低下
して来るので、金属水素化物2の交換等を行なう
ため、金属水素化物容器を分解したい場合は、上
述した組み立ての場合と逆の手法で簡単に分解で
きることは言う迄もない。
In addition, as the metal hydride 2 repeatedly absorbs and releases hydrogen gas, it gradually becomes pulverized and the heat exchange efficiency decreases, so if you want to disassemble the metal hydride container in order to exchange the metal hydride 2, etc. Needless to say, it can be easily disassembled by reversing the assembly method described above.

次に、以上のようにして組み立てられた金属水
素化物容器の熱交換作用について説明する。即
ち、畜熱時、伝熱管5を流れる熱媒からの熱は、
伝熱フイン8を介して金属水素化物2に均一に伝
達される。この熱媒からの給熱により、金属水素
化物2は脱水素化し、元の金属に戻る。また、発
生する水素ガスは保持体9のフイルタ部を介して
水素流路7から水素出入導管6へと取り出され、
図示せぬ水素ボンベへ貯えられる。一方、放熱
時、水素出入導管6から水素流路7を経て保持体
9のフイルタ部を介して供給される水素ガスは、
金属水素化物2と結合して熱を発生する。この発
生した熱は伝熱フイン8を介して伝熱管5から熱
媒へと伝達され外部に取り出され利用される。
Next, the heat exchange function of the metal hydride container assembled as described above will be explained. That is, during heat storage, the heat from the heat medium flowing through the heat transfer tubes 5 is
The heat is uniformly transferred to the metal hydride 2 via the heat transfer fins 8. By supplying heat from this heating medium, the metal hydride 2 is dehydrogenated and returns to the original metal. Further, the generated hydrogen gas is taken out from the hydrogen flow path 7 to the hydrogen inlet/output conduit 6 via the filter part of the holder 9,
It is stored in a hydrogen cylinder (not shown). On the other hand, during heat dissipation, hydrogen gas supplied from the hydrogen in/out conduit 6 through the hydrogen flow path 7 and through the filter section of the holder 9 is
It combines with metal hydride 2 to generate heat. This generated heat is transferred from the heat transfer tube 5 to the heat medium via the heat transfer fins 8, and is taken out and used outside.

このように本実施例の金属水素化物容器におい
ては、金属水素化物2は保持体9により保持され
て耐圧容器1内に収納される。これにより、金属
水素化物2の水素流路7への飛散が防止されると
共に、伝熱管5を流れる熱媒と金属水素化物2と
の間の熱伝達は伝熱フイン8を介して円滑に行な
われる。また、水素流路7の存在により保持体9
から耐圧容器1への熱流出が防止され、容器によ
る顕熱損失が抑制される。しかも、金属水素化物
2は保持体9の円筒面に設けた金属水素化物投入
口10より保持体9内部の伝熱フイン8間に均一
に分配収納され、金属水素化物の水素化、脱水素
化が効率良く行なわれる。この結果、熱交換効率
が従来のものに比べて格段に向上する。
In this way, in the metal hydride container of this embodiment, the metal hydride 2 is held by the holder 9 and housed in the pressure container 1. This prevents the metal hydride 2 from scattering into the hydrogen flow path 7, and allows smooth heat transfer between the heat medium flowing through the heat transfer tube 5 and the metal hydride 2 via the heat transfer fins 8. It will be done. Also, due to the presence of the hydrogen flow path 7, the holding body 9
Heat leakage from the pressure vessel 1 to the pressure vessel 1 is prevented, and sensible heat loss due to the vessel is suppressed. In addition, the metal hydride 2 is uniformly distributed and stored between the heat transfer fins 8 inside the holder 9 through the metal hydride inlet 10 provided on the cylindrical surface of the holder 9, allowing hydrogenation and dehydrogenation of the metal hydride. is carried out efficiently. As a result, heat exchange efficiency is significantly improved compared to conventional ones.

第3図は本発明の他の実施例を示したもので、
図中、第1図と同一符号は同一または相当部分を
示す。第3図の構成で第1図と異なる点は水素流
路7を水素は通すが金属水素化物は通し得ない断
熱材70で充填した点および保持体9の円筒面上
に設けた投入口10をその断熱材70で閉塞する
ようにした点である。
FIG. 3 shows another embodiment of the present invention,
In the figure, the same reference numerals as in FIG. 1 indicate the same or corresponding parts. The configuration of FIG. 3 differs from that of FIG. 1 in that the hydrogen channel 7 is filled with a heat insulating material 70 that allows hydrogen to pass through but not metal hydride, and that an inlet 10 is provided on the cylindrical surface of the holder 9. This is because the heat insulating material 70 is used to close the area.

この実施例のように耐圧容器1と保持体9間に
断熱材70を介在させることにより、保持体9内
から耐圧容器1への熱流出がより完全に防止さ
れ、容器による顕熱損失を先の実施例の場合より
も小さく抑えることができる。また、保持体9の
円筒面上に設けた投入口10を断熱材70で塞ぐ
ことにより、先の実施例のように投入口10を閉
鎖する加工工程を省略することができる。しか
し、保持体9内の金属水素化物2への水素ガスの
供給、排出の点では先の実施例の方が効率が良い
と言える。その他の作用効果は、先の実施例と同
等である。
By interposing the heat insulating material 70 between the pressure vessel 1 and the holder 9 as in this embodiment, heat leakage from the inside of the holder 9 to the pressure vessel 1 can be more completely prevented, and sensible heat loss due to the vessel can be prevented first. This can be suppressed to a smaller value than in the case of the embodiment. Further, by closing the input port 10 provided on the cylindrical surface of the holder 9 with the heat insulating material 70, the processing step of closing the input port 10 as in the previous embodiment can be omitted. However, it can be said that the previous embodiment is more efficient in supplying and discharging hydrogen gas to and from the metal hydride 2 in the holder 9. Other effects are the same as in the previous embodiment.

(ト) 発明の効果 以上のように本発明によれば、金属水素化物保
持体を設け、その内部に伝熱フインと共に金属水
素化物を収納保持するようにしたので、金属水素
化物の飛散を防止することができると同時に、金
属水素化物はその保持体の円筒表面に投入口を設
けて、そこから内部に入れ収納保持するようにし
たので、保持体内部の伝熱フイン間に均一に分配
収納され、極めて熱交換効率の優れた金属水素化
物容器が得られる。
(G) Effects of the Invention As described above, according to the present invention, the metal hydride holding body is provided and the metal hydride is housed and held therein together with the heat transfer fins, thereby preventing the metal hydride from scattering. At the same time, the metal hydride is stored and stored evenly between the heat transfer fins inside the holder by providing an inlet on the cylindrical surface of the holder and entering the metal hydride from there. A metal hydride container with extremely high heat exchange efficiency can be obtained.

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

第1図は本発明の一実施例に係る金属水素化物
容器の断面図、第2図は金属水素化物保持体の構
成図で、aはその平面図、bはその正面図、cは
その右側面図、第3図は本発明の他の実施例に係
る金属水素化物容器の断面図である。 1……耐圧容器、2……金属水素化物、3……
ボルト、4……ナツト、5……伝熱管、6……水
素出入導管、7……水素流路、8……伝熱フイ
ン、9……保持体、10……投入口、70……断
熱材。
FIG. 1 is a sectional view of a metal hydride container according to an embodiment of the present invention, and FIG. 2 is a configuration diagram of a metal hydride holder, in which a is a plan view thereof, b is a front view thereof, and c is a right side thereof. The plan view and FIG. 3 are cross-sectional views of a metal hydride container according to another embodiment of the present invention. 1...Pressure container, 2...Metal hydride, 3...
Bolt, 4... Nut, 5... Heat transfer tube, 6... Hydrogen in/out conduit, 7... Hydrogen channel, 8... Heat transfer fin, 9... Holder, 10... Inlet, 70... Heat insulation Material.

Claims (1)

【特許請求の範囲】 1 伝熱管と水素出入導管とを備える耐圧容器内
部に前記伝熱管と共にその周囲に金属水素化物を
収納して成る金属水素化物容器において、前記伝
熱管は前記耐圧容器を気密に貫通して設けると共
に、その伝熱管の耐圧容器内に存在する部分に伝
熱フインを取り付け、その外側を水素は通すが金
属水素化物は通し得ない円筒フイルタで被覆して
金属水素化物保持体を形成し、その表面に投入口
を設けて内部の伝熱フイン間に金属水素化物を収
納すると共に、前記金属水素化物保持体と耐圧容
器との間には空間を設けてそこを水素流路とする
ことを特徴とする金属水素化物容器。 2 特許請求の範囲第1項記載において、前記空
間に水素は通すが金属水素化物は通し得ない断熱
材を介在せしめ、この断熱材によつて前記投入口
を閉塞してなることを特徴とする金属水素化物容
器。
[Scope of Claims] 1. A metal hydride container comprising a heat exchanger tube and a metal hydride stored around the heat exchanger tube in a pressure vessel equipped with a hydrogen inlet/output conduit, wherein the heat exchanger tube airtightly seals the pressure vessel. At the same time, a heat transfer fin is attached to the part of the heat transfer tube that exists inside the pressure vessel, and the outside of the heat transfer fin is covered with a cylindrical filter that allows hydrogen to pass through but not metal hydride. An inlet is provided on the surface of the metal hydride holder to store the metal hydride between the internal heat transfer fins, and a space is provided between the metal hydride holder and the pressure vessel to form a hydrogen flow path. A metal hydride container characterized by: 2. Claim 1 is characterized in that a heat insulating material is interposed in the space that allows hydrogen to pass through but not metal hydride, and the inlet port is closed by this heat insulating material. Metal hydride container.
JP60010775A 1985-01-25 1985-01-25 Metal hydride container Granted JPS61171998A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60010775A JPS61171998A (en) 1985-01-25 1985-01-25 Metal hydride container

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60010775A JPS61171998A (en) 1985-01-25 1985-01-25 Metal hydride container

Publications (2)

Publication Number Publication Date
JPS61171998A JPS61171998A (en) 1986-08-02
JPH0436081B2 true JPH0436081B2 (en) 1992-06-15

Family

ID=11759701

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60010775A Granted JPS61171998A (en) 1985-01-25 1985-01-25 Metal hydride container

Country Status (1)

Country Link
JP (1) JPS61171998A (en)

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JPH02140427A (en) * 1988-11-21 1990-05-30 Toyota Autom Loom Works Ltd Hydrogen storage alloy tank
FR2693542B1 (en) * 1992-07-10 1994-09-09 Bernier Jacques Reactor for chemical or solid / gas adsorption machine.
US6991770B2 (en) * 2000-04-11 2006-01-31 Honda Giken Kogyo Kabushiki Kaisha Hydrogen storage tank
US20030042008A1 (en) * 2001-06-29 2003-03-06 Robert Schulz Method for storing hydrogen in an hybrid form
CA2413834A1 (en) * 2002-12-10 2004-06-10 1017975 Alberta Limited Nitric oxide gas generator
US9138707B2 (en) 2002-12-10 2015-09-22 Sy Kimball Portable, nitric oxide generator
JP5876678B2 (en) 2011-07-01 2016-03-02 Kyb株式会社 Hydrogen storage container
US10517817B2 (en) 2013-05-09 2019-12-31 Syk Technologies, Llc Deep topical systemic nitric oxide therapy apparatus and method
WO2017132275A1 (en) 2016-01-27 2017-08-03 Syk Technologies, Llc Nitric oxide topical application apparatus and methods
USD869656S1 (en) 2016-04-12 2019-12-10 Jason P. Adams Single strand bi-directional barb suture with coating shield
USD844140S1 (en) 2016-04-12 2019-03-26 Jason P. Adams Single-shield, bi-directional-barb, double-strand-twist suture
USD870283S1 (en) 2016-04-12 2019-12-17 Jason P. Adams Single strand bi-directional suture with coating shield
USD867591S1 (en) 2016-04-12 2019-11-19 Jason P. Adams Single strand mono-directional barb loop suture with single coating shield
USD870282S1 (en) 2016-04-12 2019-12-17 Jason P. Adams Single strand bi-directional barb suture with coating shield
USD872861S1 (en) 2016-04-12 2020-01-14 Jason P. Adams Double strand twist bi-directional barb suture with single coating shield
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JP2023135059A (en) * 2022-03-15 2023-09-28 日新電機株式会社 heat storage device

Also Published As

Publication number Publication date
JPS61171998A (en) 1986-08-02

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