JPS6144383B2 - - Google Patents

Info

Publication number
JPS6144383B2
JPS6144383B2 JP54144309A JP14430979A JPS6144383B2 JP S6144383 B2 JPS6144383 B2 JP S6144383B2 JP 54144309 A JP54144309 A JP 54144309A JP 14430979 A JP14430979 A JP 14430979A JP S6144383 B2 JPS6144383 B2 JP S6144383B2
Authority
JP
Japan
Prior art keywords
catalyst
container
plug
gas
storage battery
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
JP54144309A
Other languages
Japanese (ja)
Other versions
JPS5669778A (en
Inventor
Toshio Matsushima
Shintaro Hayashi
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.)
Nippon Telegraph and Telephone Corp
Original Assignee
Nippon Telegraph and Telephone Corp
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 Nippon Telegraph and Telephone Corp filed Critical Nippon Telegraph and Telephone Corp
Priority to JP14430979A priority Critical patent/JPS5669778A/en
Publication of JPS5669778A publication Critical patent/JPS5669778A/en
Publication of JPS6144383B2 publication Critical patent/JPS6144383B2/ja
Granted legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/42Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
    • H01M10/52Removing gases inside the secondary cell, e.g. by absorption
    • 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
    • Y02E60/10Energy storage using batteries

Landscapes

  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Secondary Cells (AREA)

Description

【発明の詳細な説明】 本発明は蓄電池用触媒栓、詳しくは過充電によ
つて蓄電池から発生する酸素、水素等の混合ガス
を、白金族系の金属触媒によつて結合させる気相
反応用触媒栓装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a catalyst plug for a storage battery, and more specifically, a gas phase applied catalyst that combines a mixed gas such as oxygen and hydrogen generated from a storage battery due to overcharging using a platinum group metal catalyst. This invention relates to a plug device.

従来、この種の据置蓄電池用の触媒栓として
は、第1図に示すように容器1内に下方開口部2
を介して蓄電池から発生するガスを導入するよう
になつており、この容器1内のほぼ中央部には内
部に触媒が収容された単一の触媒容器3が配設さ
れて構成されている。
Conventionally, a catalyst plug for this type of stationary storage battery has a lower opening 2 in a container 1, as shown in FIG.
Gas generated from the storage battery is introduced through the container 1, and a single catalyst container 3 containing a catalyst is disposed approximately in the center of the container 1.

しかるに、このような構造の触媒栓では収容す
る触媒量によつて反応ガス量が制限され、また、
生成水蒸気の凝縮は容器内の表面積に依存する。
その結果、処理できる混合ガス量が制限される。
すなわち、蓄電池から発生するガスは電池の容量
に比例して増加する。従つて、この種の触媒栓も
触媒量を増し、容器1も大型化することである程
度の容量の蓄電池には対処することができる。し
かし、ガス発生量の多い大容量蓄電池に対して
は、装置全体が極めて大形となり、使用困難とな
る。また、単に容器1は小型のまま触媒量を増加
させた場合には、ガス反応量は増加するが、冷却
能力が不足し、生成水蒸気の凝縮が妨げられてし
まう。さらに、冷却力不足の結果、触媒温度が上
昇し触媒栓の破壊、ガスへの点火といつた事故に
至る欠点がある。
However, in a catalyst plug with such a structure, the amount of reaction gas is limited by the amount of catalyst accommodated, and
Condensation of the produced water vapor depends on the surface area within the vessel.
As a result, the amount of mixed gas that can be processed is limited.
That is, the gas generated from the storage battery increases in proportion to the capacity of the battery. Therefore, by increasing the amount of catalyst in this type of catalyst plug and increasing the size of the container 1, it is possible to cope with a storage battery having a certain capacity. However, for large-capacity storage batteries that generate a large amount of gas, the entire device becomes extremely large, making it difficult to use. Furthermore, if the amount of catalyst is simply increased while keeping the container 1 small, the amount of gas reaction will increase, but the cooling capacity will be insufficient and the condensation of the generated steam will be hindered. Furthermore, as a result of insufficient cooling power, the catalyst temperature rises, leading to accidents such as destruction of the catalyst plug and ignition of the gas.

以上の事から、従来型の触媒栓は多量のガスが
発生した場合、触媒の過熱から事故に結びつく欠
点があり、さらに、単に触媒量を増加させたり、
容器の寸法を大型化しただけでは、大容量蓄電池
に対しては、対処できないという種々の欠点を有
していた。
From the above, conventional catalyst plugs have the disadvantage that when a large amount of gas is generated, the catalyst overheats, leading to an accident.
Merely increasing the size of the container has various drawbacks, such as not being able to cope with large-capacity storage batteries.

本発明は上記の欠点を改善し、蓄電池からの混
合ガスと触媒との反応に伴う栓内の発生熱を効果
的に放散し、触媒の過熱を防ぐと共に、水蒸気の
凝縮を促進し得る小型で、かつ効率の良い多段型
触媒栓を提供することを目的とするものである。
The present invention improves the above-mentioned drawbacks, effectively dissipates the heat generated in the stopper due to the reaction between the mixed gas from the storage battery and the catalyst, prevents the catalyst from overheating, and is a small and compact device that can promote the condensation of water vapor. It is an object of the present invention to provide a multi-stage catalyst plug with high efficiency.

本発明を要約すると触媒栓容器内にヒートパイ
プを融着し且つ任意の位置に通気用小孔を有する
複数の分離板によつて触媒栓容器内の空間を複数
の室に分割区画し、これら複数のそれぞれの室内
に触媒物質を収容したことを特徴としている。す
なわち、本発明は、触媒栓の性能は酸素と水素と
を反応させる触媒の量と容器の容積,形状等に支
配され、また触媒温度の上限値も触媒栓の構造で
定まる最大ガス反応量より決定されること、およ
び1個の触媒栓で処理できる量を越えるガス量を
処理する場合、触媒栓を複数個直列に接続するこ
とで対応できるとの知見に基づき提案されたもの
で、特に大容量蓄電池用の触媒栓において問題と
なる触媒の温度上昇の抑制と水蒸気の凝集に
有効な容器の表面積を増加させて液化の促進を図
つた点に特徴がある。そのため本発明では触媒を
分割配置し、放熱表面積を拡大し、触媒の温度上
昇を抑制する手段をとり、触媒栓内には液化用の
金属板さらなる分離板を設け、その分離板の熱を
ヒートパイプにより触媒栓外部に放熱する処置を
とつている。さらに、両者の機能をより高めるた
め、分離板で隔室を形成し、それぞれの内部に触
媒を分割して配置している。これらの処置により
触媒の温度上昇が抑制され、また発生した水蒸気
を有効に液化することができるので、小型で性能
の良い触媒栓を得ることができる。
To summarize the present invention, a heat pipe is fused within a catalyst plug container, and the space inside the catalyst plug container is divided into a plurality of chambers by a plurality of separation plates having small ventilation holes at arbitrary positions. It is characterized by containing a catalyst substance in each of a plurality of chambers. That is, in the present invention, the performance of the catalyst plug is controlled by the amount of catalyst for reacting oxygen and hydrogen, the volume of the container, the shape, etc., and the upper limit of the catalyst temperature is also determined by the maximum gas reaction amount determined by the structure of the catalyst plug. It was proposed based on the knowledge that when processing a gas amount that exceeds the amount that can be treated with a single catalyst plug, it can be handled by connecting multiple catalyst plugs in series. It is characterized by promoting liquefaction by suppressing the temperature rise of the catalyst, which is a problem in catalyst plugs for capacity storage batteries, and by increasing the surface area of the container, which is effective for condensing water vapor. Therefore, in the present invention, the catalyst is divided and arranged to expand the heat dissipation surface area and suppress the temperature rise of the catalyst.In addition, a metal plate for liquefaction and a separation plate are provided inside the catalyst plug, and the heat of the separation plate is transferred to heat. Measures are taken to radiate heat to the outside of the catalyst plug using a pipe. Furthermore, in order to further enhance the functions of both, compartments are formed using separation plates, and the catalyst is divided and placed inside each compartment. These measures suppress the temperature rise of the catalyst and effectively liquefy the generated water vapor, making it possible to obtain a small-sized catalyst plug with good performance.

さらに添附図面を参照しつつ本発明の構成を説
明すると、図において11は中空状の容器で、こ
の容器11の上方部には内部の過剰ガスを外部へ
排気するための排気孔12が形成され、かつ排気
孔12には多孔質のアルミナ磁器からなる有底円
筒状の防爆フイルタ13が設けられている。ま
た、容器11の下方部には外周部に形成されたネ
ジ部14を介して蓄電池(図示せず)ケースと螺
合せしめ、蓄電池と本発明にかかる触媒栓とを一
体に結合するための取付口15が形成されてお
り、この取付口15の相対向する内周壁には互い
違いに延びる隔離板16がそれだれ突出するよう
に形成され、これによつて隔離板付還水口17が
形成されている。
Further, the structure of the present invention will be explained with reference to the attached drawings. In the drawings, reference numeral 11 denotes a hollow container, and an exhaust hole 12 is formed in the upper part of the container 11 for exhausting excess gas inside to the outside. , and the exhaust hole 12 is provided with a bottomed cylindrical explosion-proof filter 13 made of porous alumina porcelain. Further, the lower part of the container 11 is screwed to a storage battery (not shown) case via a threaded part 14 formed on the outer periphery, and a mounting is provided for integrally connecting the storage battery and the catalyst plug according to the present invention. A port 15 is formed, and separator plates 16 extending alternately are formed on the opposing inner circumferential walls of the mounting port 15 so as to protrude from each other, thereby forming a return water port 17 with a separator plate. .

18は容器11の触媒栓の使用形態の高さ方向
に沿つて所定の間隔を介して配設された分離板
で、容器11内はこれらの分離板18によつて複
数の室に区画形成され、各室内にはアルミナ磁器
からなる触媒容器19に収納された触媒がそれぞ
れ配設されている。分離板18は熱伝導性を考慮
して金属性の材質から形成され、かつ円錐形に形
成されている。しかして、分離板18の頂部には
この分離板18によつて形成された容器11内の
各室、すなわち各空間部間を連通する通気用の小
孔20が形成され、かつ通気用小孔20の周囲に
は分離板18の表面積を増加させる目的で中央部
から外周部にわたつて放射状に延びる蛇腹21が
形成されている。また、周辺部には生成水の還流
用として作用するスリツト22が周辺に沿つて適
数個形成されている。23は分離板18に融着さ
れ外気との熱交率を効果的に行うためのヒートパ
イプで、一端部は小孔20近傍に、また他端部は
容器11の外部に露出するようにして設けられ、
外部の露出した部分には放熱フイン24が設けら
れている。なお、図示の例ではヒートパイプ23
は90゜毎に設けられているが、必要に応じ適宜ヒ
ートパイプ23の数、配列を変更することも可能
である。また、通気用小孔20も上記の説明にお
いては頂部に形成した例を示したが、必ずしも頂
部のみに限定されるべきものではなく、ヒートパ
イプ部分を除いた分離板18の任意の位置に形成
することも許容するものである。さらに、分離板
18の数も2枚に限定されるものでなく、組み合
わせて用いられる対象蓄電池の容量等に合わせ、
適宜増減し得るものである。
Separation plates 18 are arranged at predetermined intervals along the height direction of the catalyst stopper of the container 11, and the interior of the container 11 is divided into a plurality of chambers by these separation plates 18. A catalyst housed in a catalyst container 19 made of alumina porcelain is disposed in each chamber. The separation plate 18 is made of a metallic material and has a conical shape in consideration of thermal conductivity. Therefore, a small ventilation hole 20 is formed at the top of the separation plate 18 to communicate between each chamber, that is, each space, in the container 11 formed by the separation plate 18. A bellows 21 is formed around the separation plate 20 and extends radially from the center to the outer periphery for the purpose of increasing the surface area of the separation plate 18. Further, an appropriate number of slits 22 are formed along the periphery, which serve as reflux of generated water. A heat pipe 23 is fused to the separation plate 18 to effectively exchange heat with the outside air, with one end exposed near the small hole 20 and the other end exposed outside the container 11. provided,
A heat dissipation fin 24 is provided on the externally exposed portion. In addition, in the illustrated example, the heat pipe 23
are provided every 90 degrees, but the number and arrangement of the heat pipes 23 can be changed as necessary. In addition, although the above description shows an example in which the small ventilation holes 20 are formed at the top, they are not necessarily limited to the top, and may be formed at any position on the separation plate 18 excluding the heat pipe portion. It is also permissible to do so. Furthermore, the number of separation plates 18 is not limited to two, and may be arranged according to the capacity of the target storage battery used in combination.
It can be increased or decreased as appropriate.

次に上記の如く構成された本発明の動作を説明
する。
Next, the operation of the present invention configured as described above will be explained.

本発明の触媒栓は栓内が数段の室に分割され、
通気用小孔20のみで各室は連通している。その
結果、各室間でのガスの自由な流通が妨げられ、
各室はそれと同じ規模の触媒栓として作用する。
すなわち各室では触媒量とその容積で規定される
最大反応ガス量をもつてガス反応量が制限される
ので、蓄電池から多量のガスが発生しても、下方
の室から反応を開始する。つまり、下方の第一室
をオーバーフローしたガスはその上方の第2室へ
流入し反応し、第2室でも処理しきれないガスは
第3室で反応する。
In the catalyst plug of the present invention, the inside of the plug is divided into several chambers,
Each chamber communicates only with a small ventilation hole 20. As a result, the free flow of gas between each chamber is impeded,
Each chamber acts as a catalyst plug of the same size.
That is, in each chamber, the amount of gas reaction is limited by the maximum amount of reaction gas defined by the amount of catalyst and its volume, so even if a large amount of gas is generated from the storage battery, the reaction will start from the lower chamber. In other words, gas that overflows the first chamber below flows into the second chamber above and reacts therein, and gas that cannot be processed even in the second chamber reacts in the third chamber.

このように本発明においては、多量のガスも各
室に分散して反応するので、触媒の過熱も防止で
きる。また、ヒートパイプ23付の分離板18の
使用により反応熱を外部へ速みやかに除去するこ
とができるので、栓内の熱の蓄積もなく、生成水
蒸気も分離板18、容器11内壁により凝縮する
ことができる。
In this way, in the present invention, since a large amount of gas is also dispersed in each chamber and reacted, overheating of the catalyst can also be prevented. In addition, by using the separation plate 18 with the heat pipe 23, the reaction heat can be quickly removed to the outside, so there is no accumulation of heat inside the plug, and the generated water vapor is also condensed by the separation plate 18 and the inner wall of the container 11. can do.

叙上のように本発明によれば、栓体内の空間部
をヒートパイプを有する分離板で区画形成して複
数の室に分割し、各室に触媒を分散配置して構成
しているため、この結果、各室における最大反応
量は制限され、多量のガスの発生があつても、各
室内で分割して反応させることができ、触媒の過
熱による事故に到ることがない。また、ヒートパ
イプにより効果的に放熱できるため、従来型に比
べ小型の容器で触媒栓を構成することができる。
さらに、積重ね式を採用している結果、蓄電池の
容量に合わせた触媒栓を自由に組立てることがで
きる等の利点がある。
As described above, according to the present invention, the space inside the stopper is divided into a plurality of chambers by partitioning the space inside the plug with a separation plate having a heat pipe, and the catalyst is distributed in each chamber. As a result, the maximum amount of reaction in each chamber is limited, and even if a large amount of gas is generated, it can be divided and reacted in each chamber, and accidents due to overheating of the catalyst will not occur. Furthermore, since heat can be effectively dissipated by the heat pipe, the catalyst plug can be configured with a smaller container than the conventional type.
Furthermore, as a result of adopting the stacking type, there are advantages such as the ability to freely assemble catalyst plugs that match the capacity of the storage battery.

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

第1図は従来の触媒栓、第2図は本発明にかか
る蓄電池用触媒栓の一実施例を示す断面説明図、
第3図は本発明に適用される分離板の平面説明図
を示す。 18…分離板、19…触媒容器、20…通気用
小孔、23…ヒートパイプ。
FIG. 1 is a conventional catalyst plug, and FIG. 2 is a cross-sectional explanatory diagram showing an embodiment of a catalyst plug for a storage battery according to the present invention.
FIG. 3 shows a plan view of a separation plate applied to the present invention. 18... Separation plate, 19... Catalyst container, 20... Small ventilation hole, 23... Heat pipe.

Claims (1)

【特許請求の範囲】[Claims] 1 容器内に充電時に蓄電池から発生する酸素・
水素等の混合ガスを再結合させる触媒物質を収容
してなる触媒栓において、ヒートパイプを融着し
且つ任意の位置に通気用小孔を有する複数の分離
板によつて前記容器内空間を階層をなす複数の室
に分割区画し、前記各室内に触媒物質をそれぞれ
収容してなることを特徴とする蓄電池用触媒栓。
1 Oxygen generated from the storage battery during charging is contained in the container.
In a catalyst stopper containing a catalyst material for recombining a mixed gas such as hydrogen, the space inside the container is layered by a plurality of separation plates having heat pipes fused to each other and having small holes for ventilation at arbitrary positions. 1. A catalyst plug for a storage battery, characterized in that the catalyst plug is divided into a plurality of chambers forming a shape, and each chamber contains a catalyst substance.
JP14430979A 1979-11-09 1979-11-09 Catalyst plug for storage battery Granted JPS5669778A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14430979A JPS5669778A (en) 1979-11-09 1979-11-09 Catalyst plug for storage battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14430979A JPS5669778A (en) 1979-11-09 1979-11-09 Catalyst plug for storage battery

Publications (2)

Publication Number Publication Date
JPS5669778A JPS5669778A (en) 1981-06-11
JPS6144383B2 true JPS6144383B2 (en) 1986-10-02

Family

ID=15359080

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14430979A Granted JPS5669778A (en) 1979-11-09 1979-11-09 Catalyst plug for storage battery

Country Status (1)

Country Link
JP (1) JPS5669778A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58100376A (en) * 1981-12-08 1983-06-15 Nippon Telegr & Teleph Corp <Ntt> Catalitic gas treatment apparatus

Also Published As

Publication number Publication date
JPS5669778A (en) 1981-06-11

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