JPS5829242B2 - hydrogen generator - Google Patents
hydrogen generatorInfo
- Publication number
- JPS5829242B2 JPS5829242B2 JP55014569A JP1456980A JPS5829242B2 JP S5829242 B2 JPS5829242 B2 JP S5829242B2 JP 55014569 A JP55014569 A JP 55014569A JP 1456980 A JP1456980 A JP 1456980A JP S5829242 B2 JPS5829242 B2 JP S5829242B2
- Authority
- JP
- Japan
- Prior art keywords
- hydrogen
- reactor
- reaction
- water
- metal hydride
- 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
Classifications
-
- 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
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
Landscapes
- Hydrogen, Water And Hydrids (AREA)
- Fuel Cell (AREA)
Description
【発明の詳細な説明】
本発明は金属水素化物と水とを反応させて水素を得る水
素発生装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a hydrogen generating device that generates hydrogen by reacting a metal hydride with water.
水素化リチウムや水素化カルシウムなどの金属水素化物
に水を反応させると水素が発生することは古くから知ら
れており、たとえば移動用の通信機の電源として好適な
空気−水素燃料電池のための簡易水素源としてその実用
的な用途が見出されている。It has long been known that hydrogen is generated when water reacts with metal hydrides such as lithium hydride and calcium hydride. It has found practical use as a simple hydrogen source.
第1図はこの種の簡易形水素発生装置の一例の原理図で
あり、手動空気ポンプ1にて水タンク2内の水を反応器
3に圧送し、この水(以下「反応水」と呼ぶ)と反応器
3内の水素化カルシウム4とを反応させ、
CaH2+2H20→Ca(OH)2+2H2なる反応
式に基づいて発生する水素を調圧器5を介して水素消費
機器、たとえば空気−水素燃料電池に供給するものであ
る。FIG. 1 is a diagram showing the principle of an example of this type of simple hydrogen generator. Water in a water tank 2 is fed under pressure to a reactor 3 using a manual air pump 1, and this water (hereinafter referred to as "reaction water") is shown in FIG. ) is reacted with calcium hydride 4 in the reactor 3, and the hydrogen generated based on the reaction formula CaH2+2H20→Ca(OH)2+2H2 is sent to a hydrogen consuming device, such as an air-hydrogen fuel cell, via a pressure regulator 5. supply.
第1図には逆止弁、調節弁、安全弁等が特に符号を付け
ずに示されているが、説明は省略する。In FIG. 1, check valves, control valves, safety valves, etc. are shown without particular reference numerals, but their explanations will be omitted.
ところで、かかる原理に基つく水素発生装置を実用に供
する場合、反応の初期には高純度の水素ガスが得られる
が、反応の末期に到ったときに水素ガスに少なからぬ水
蒸気が混入して水素ガス純度を低減させるという問題点
が存する。By the way, when a hydrogen generator based on this principle is put into practical use, highly pure hydrogen gas is obtained at the beginning of the reaction, but at the end of the reaction, a considerable amount of water vapor is mixed into the hydrogen gas. There is a problem of reducing hydrogen gas purity.
この理由は前述の反応式において反応に伴なう発熱が存
することを起因するもので、反応の初期には逆にこの反
応熱を利用して、供給される反応水を直ちに水蒸気化さ
せて反応速度を速めるべく、反応水を反応器3内の水素
化カルシウム堆積部の下方に導くようにしているが、反
応が進んで未反応の金属水素化物が少なくなると、反応
に与らない水蒸気が水素ガスとともに外部に流出すると
いう事態を招くのである。The reason for this is that there is heat generated by the reaction in the above reaction equation, and in the early stages of the reaction, this reaction heat is used to immediately vaporize the supplied reaction water and cause the reaction. In order to speed up the reaction, the reaction water is guided below the calcium hydride deposit in reactor 3, but as the reaction progresses and the amount of unreacted metal hydride decreases, the water vapor that does not participate in the reaction becomes hydrogen. This results in a situation where the gas leaks out to the outside together with the gas.
そこで、本発明は上述のごとき欠点を除去して水蒸気の
混入することのない水素を供給し得る水素発生装置を提
供することを目的とするものである。SUMMARY OF THE INVENTION Therefore, an object of the present invention is to provide a hydrogen generator capable of eliminating the above-mentioned drawbacks and supplying hydrogen without contamination with water vapor.
本発明の他の目的は、水素消費機器に連続的に水素を供
給し得る水素発生装置を提供することにある。Another object of the present invention is to provide a hydrogen generator that can continuously supply hydrogen to hydrogen consuming equipment.
すなわち、金属水素化物の反応が進んで、そのすべてが
金属水酸化物に変換された場合には、反応器3への金属
水素化物の再投入、ないしは未反応金属水素化物の充填
された新たな反応器との交換等を行なう必要があるが、
1台の水素発生装置ではかかる作業を行なう間、水素の
供給の中断を余儀なくされる。That is, when the reaction of metal hydride progresses and all of it is converted to metal hydroxide, the metal hydride is reinjected into the reactor 3, or a new one filled with unreacted metal hydride is added. It is necessary to replace the reactor, etc.
In one hydrogen generator, the supply of hydrogen is forced to be interrupted while such work is performed.
この問題を解決するには、反応器を二装置いて切り換え
て使用すればよいが、単純な切り換えだけでは水蒸気の
混入という問題は依然として解決されない。To solve this problem, it is possible to use two reactors and switch between them, but the problem of water vapor contamination still cannot be solved by simple switching.
そこで本発明は反応器を二台置き、それぞれ単独でも運
転が可能なようにするとともに、通常運転時には二台の
反応器を直列に、すなわち、一方の反応器の発生水素を
他方の反応器の反応水供給路に供給し、当該他方の反応
器を通過した水素を水素消費機器に与えるようにする。Therefore, in the present invention, two reactors are installed so that each reactor can be operated independently, and during normal operation, the two reactors are connected in series, that is, the hydrogen generated in one reactor is transferred to the other reactor. The reaction water is supplied to the reaction water supply line, and the hydrogen that has passed through the other reactor is supplied to the hydrogen consuming equipment.
かくすることにより、前記一方の反応器の反応が進んで
発生水素中に水蒸気が含まれたとしても、この水蒸気は
後段の反応器内の金属水素化物に吸収されるため、最終
的な出力ガスには混入しない。By doing this, even if the reaction in one of the reactors progresses and the generated hydrogen contains water vapor, this water vapor is absorbed by the metal hydride in the subsequent reactor, so the final output gas is It will not be mixed in.
後段の反応器においては当然のことながら水蒸気の吸収
に伴なう水素の発生が付加的に生じるが、前述の反応式
からも明らかなとおり、2モルの水蒸気ガスに対して2
モルの水素ガスが発生するわけであるから、総合的な水
素発生量は常に均一に保たれる。Naturally, in the latter reactor, hydrogen is additionally generated due to the absorption of water vapor, but as is clear from the above reaction equation, 2 moles of water vapor gas
Since moles of hydrogen gas are generated, the overall amount of hydrogen generated is always kept uniform.
従って本発明によれは前述の二つの目的を一挙に解決で
きることになる。Therefore, according to the present invention, the above two objects can be solved at once.
次に本発明の実施例を図面に基づいて説明する。Next, embodiments of the present invention will be described based on the drawings.
第2図は本発明の実施例の配管系統図であり、第3図な
いし第6図は各種運転モード時に反応水および水素ガス
が流れる管路のみを抽出して示した配管系統図であって
、すべての図において共通な部分には共通な符号を付し
である。Fig. 2 is a piping system diagram of an embodiment of the present invention, and Figs. 3 to 6 are piping system diagrams showing only the pipes through which reaction water and hydrogen gas flow during various operation modes. , common parts in all figures are given common reference numerals.
、第2図において、6は水タンクで適当な水の圧送用の
圧力を加える手段(図示せず)を具備しているものとす
る。In FIG. 2, 6 is a water tank and is equipped with means (not shown) for applying appropriate pressure for pumping water.
7は水供給弁、8は絞りである。絞り8を通過した一定
量の反応水は三方切換弁9により、二つの系統に選択的
に供給される。7 is a water supply valve, and 8 is a throttle. A certain amount of reaction water that has passed through the throttle 8 is selectively supplied to two systems by a three-way switching valve 9.
一方の系は反応器10を有する系であり、他方の系は反
応器20を有する系である。One system is a system with reactor 10 and the other system is a system with reactor 20.
これらの反応器はたとえば第1図の反応器3と同じ形式
のものであってよい。These reactors may be of the same type as reactor 3 in FIG. 1, for example.
10a 、20aは反応水供給管、10b。20bは水
素排出管である。10a and 20a are reaction water supply pipes, and 10b. 20b is a hydrogen discharge pipe.
また、11.21および13.23は逆止弁、12.2
2は三方切換弁、24は水素ガス供給弁で、水素ガス供
給弁24を通った水素ガスは場合によってはサージタン
クを介して、そして好ましくは調圧器を介して水素消費
機器、たとえは空気−水素燃料電池に供給される。Also, 11.21 and 13.23 are check valves, 12.2
2 is a three-way switching valve, 24 is a hydrogen gas supply valve, and the hydrogen gas that has passed through the hydrogen gas supply valve 24 is optionally passed through a surge tank, and preferably via a pressure regulator to a hydrogen consuming device, such as an air- Supplied to hydrogen fuel cells.
三個の三方切換弁9,12.22を有する第2図の実施
例の装置は、以下に述べる四つの運転モードでの運転が
可能である。The device of the embodiment of FIG. 2 with three three-way valves 9, 12, 22 can be operated in four operating modes as described below.
第1の運転モードは、第3図に示すように、三方切換弁
9を逆止弁11側に切り換えて反応水を反応器10に供
給し、三方切換弁12を逆止弁13側に切り換えて反応
器10における発生水素を反応器20の反応水供給管2
0aに導き、その水素排出管20bから三方切換弁22
を介して水素ガス供給弁24に高純度の水素を導くモー
ドである。As shown in FIG. 3, in the first operation mode, the three-way switching valve 9 is switched to the check valve 11 side to supply reaction water to the reactor 10, and the three-way switching valve 12 is switched to the check valve 13 side. The hydrogen generated in the reactor 10 is transferred to the reaction water supply pipe 2 of the reactor 20.
0a, and the three-way switching valve 22 from the hydrogen discharge pipe 20b.
This is a mode in which high-purity hydrogen is introduced to the hydrogen gas supply valve 24 through the hydrogen gas supply valve 24.
この運転モードにおいては反応器10で発生する水素に
含まれる水蒸気は反応器20内の金属水素化物に吸収さ
れ、付加的に発生した水素とともに高純度な水素ガスと
して水素消費機器に供給される。In this mode of operation, the water vapor contained in the hydrogen generated in the reactor 10 is absorbed by the metal hydride in the reactor 20, and together with additionally generated hydrogen, is supplied to hydrogen consuming equipment as high purity hydrogen gas.
反応器10内の金属水素化物の反応がほとんど完了した
場合には、たとえば調圧器に設けられた圧力計ないし圧
力警報装置により圧力低下を知ることができるので、次
の運転モードである反応器20のみによる運転を行なう
(第4図)。When the reaction of the metal hydride in the reactor 10 is almost completed, the pressure drop can be detected by, for example, a pressure gauge or a pressure alarm device installed in the pressure regulator, and the reactor 20 is in the next operation mode. Perform operation using a chisel (Fig. 4).
第4図の運転モードでは、反応水は三方切換弁9から逆
止弁21を介して反応器20の反応水供給管20aに供
給される。In the operation mode shown in FIG. 4, reaction water is supplied from the three-way switching valve 9 to the reaction water supply pipe 20a of the reactor 20 via the check valve 21.
第3図における三方切換弁12はその除閉じられ、反応
器10から既反応金属水素化物が取り出されて新しい金
属水素化物が充填される。The three-way valve 12 in FIG. 3 is opened and the reactor 10 is removed from reacted metal hydride and filled with fresh metal hydride.
反応器20内の金属水素化物は大半が未反応であるから
、この運転モードの切り換えにより、反応器10の運転
中止にもかかわらず連続的にかつ水蒸気を全く混入させ
ることなしに水素ガスを供給することが可能となる。Since most of the metal hydride in the reactor 20 is unreacted, by switching the operation mode, hydrogen gas can be supplied continuously and without mixing any water vapor even though the operation of the reactor 10 is stopped. It becomes possible to do so.
反応器10の準備が完了した時点で、第5図に示す第3
の運転モードに入る。When the preparation of the reactor 10 is completed, the third
enters driving mode.
この運転モードは、第3図に示す第1の運転モードとは
反応器10および20の順番が入れ換わった形となる。In this mode of operation, the order of reactors 10 and 20 is reversed from the first mode of operation shown in FIG.
すなわち、反応器20で発生した水素ガスが水素排出管
20bから三方切換弁22、逆止弁23を介して反応器
10の反応水供給管10aに供給され、徐徐に水蒸気を
含むことになる反応器20の発生水素を反応器10内の
ほとんど未反応である金属水素化物にて吸湿して高純度
な水素ガスとして水素排出管10b1三方切換弁12、
水素供給弁24を介して水素消費機器に供給する。That is, hydrogen gas generated in the reactor 20 is supplied from the hydrogen discharge pipe 20b to the reaction water supply pipe 10a of the reactor 10 via the three-way switching valve 22 and the check valve 23, and the reaction gradually contains water vapor. The hydrogen generated in the reactor 20 is absorbed by the almost unreacted metal hydride in the reactor 10 and converted into high-purity hydrogen gas, a hydrogen discharge pipe 10b1, a three-way switching valve 12,
The hydrogen is supplied to the hydrogen consuming equipment via the hydrogen supply valve 24.
このモードでの運転を続けていくうちに、反応器20内
の金属水素化物がほとんど反応を完了する時点が到来す
るので、これを前述の如く圧力低下等にて検知して、次
なる運転モード、すなわち第6図に示す反応器10のみ
の運転モードに入る。As the operation continues in this mode, a time will come when the metal hydride in the reactor 20 has almost completed its reaction, so this is detected by the pressure drop as described above, and the next operation mode is started. That is, the operation mode of only the reactor 10 shown in FIG. 6 is entered.
この運転モードは第4図の反応器20の単独運転モード
の裏返しであるので、詳細な説明は省略する。Since this operation mode is the reverse of the independent operation mode of the reactor 20 shown in FIG. 4, detailed explanation will be omitted.
そして反応器10の単独運転時に反応器20内の金属水
素化物の入れ換えを行なって第3図に示す最初の運転モ
ードに入る。Then, when the reactor 10 is operated independently, the metal hydride in the reactor 20 is replaced and the first operation mode shown in FIG. 3 is entered.
以下は上記の繰り返しである。The following is a repetition of the above.
以上述べた四つの運転モードのうち、本発明の最も特徴
とするところlま第3図および第5図に示す反応器10
.20の直列運転モードにあることは明らかであろう。Among the four operation modes described above, the most distinctive feature of the present invention is the reactor 10 shown in FIGS. 3 and 5.
.. It will be clear that there are 20 series operating modes.
この直列運転モードを常時の運転モードとすることによ
って、水蒸気を含まない高純度の水素ガスを得ることが
可能となり、派生的な効果として、ガス系の配管中に水
分が凝縮することがなくなったために腐食の問題点も軽
減され、配管構成がきわめて楽になる利点を享受できる
。By making this series operation mode the constant operation mode, it is possible to obtain high-purity hydrogen gas that does not contain water vapor, and as a secondary effect, moisture does not condense in the gas system piping. The problem of corrosion is also reduced, and the piping configuration becomes extremely easy.
なお、本発明の実施に当って、特に三方切換弁の切換時
における一時的な出力ガス圧低下を心配する場合には、
前述したごとくサージタンクを付設するか、あるいは水
素消費機器が空気−水素撚7料電池である場合には燃料
電池に並列に通常の蓄電池を接続しておくなどの措置を
講ずれば良い。Note that when implementing the present invention, if you are particularly concerned about a temporary drop in output gas pressure when switching the three-way switching valve,
As mentioned above, measures may be taken such as attaching a surge tank or, if the hydrogen consuming device is an air-hydrogen twisted 7-fuel cell, connecting a normal storage battery in parallel to the fuel cell.
第1図は従来の水素発生装置の原理を示す系統図、第2
図は本発明の実施例の配管系統図、第3図〜第6図は第
2図の実施例の四つの運転モードに対応してそれぞれ関
与する配管系および機器のみを抽出して示した配管系統
図である。
6・・・・・・水タンク、9,12,22・・・・・・
三方切換弁、10.20・・・・・・反応器、11.1
3,21゜23・・・・・・逆止弁、24・・・・・・
水素供給弁。Figure 1 is a system diagram showing the principle of a conventional hydrogen generator;
The figure shows a piping system diagram of an embodiment of the present invention, and Figures 3 to 6 show only the piping system and equipment involved in each of the four operating modes of the embodiment of Figure 2. It is a system diagram. 6...Water tank, 9,12,22...
Three-way switching valve, 10.20... Reactor, 11.1
3,21゜23...Check valve, 24...
Hydrogen supply valve.
Claims (1)
せる少なくとも二台の反応器と、該反応器の各々に選択
的に反応水を供給する配管系と、それぞれ一方の反応器
の発生水素を他方の反応器の反応水供給路と水素消費機
器との選択的に供給する配管系とを備え、通常運転時に
は各々の反応器を直列に接続して運転することを特徴と
する水素発生装置。 2、特許請求の範囲第1項記載の装置において、各配管
系の選択的供給を司る部分が三方切換弁であることを特
徴とする水素発生装置。[Scope of Claims] 1. At least two reactors that generate hydrogen through a reaction between a metal hydride and reaction water; a piping system that selectively supplies reaction water to each of the reactors; It is equipped with a piping system that selectively supplies the hydrogen generated from one reactor to the reaction water supply line of the other reactor and the hydrogen consuming equipment, and is characterized in that during normal operation, each reactor is connected in series. hydrogen generator. 2. A hydrogen generator according to claim 1, wherein the portion controlling selective supply of each piping system is a three-way switching valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55014569A JPS5829242B2 (en) | 1980-02-08 | 1980-02-08 | hydrogen generator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55014569A JPS5829242B2 (en) | 1980-02-08 | 1980-02-08 | hydrogen generator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS56114803A JPS56114803A (en) | 1981-09-09 |
| JPS5829242B2 true JPS5829242B2 (en) | 1983-06-21 |
Family
ID=11864780
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP55014569A Expired JPS5829242B2 (en) | 1980-02-08 | 1980-02-08 | hydrogen generator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5829242B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6117934U (en) * | 1984-07-06 | 1986-02-01 | ヤンマー農機株式会社 | threshing equipment |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CH692879A5 (en) * | 1997-12-18 | 2002-11-29 | Dch Technology Inc | Apparatus for converting energy using fuel cells with integrated hydrogen gas generation. |
| JP4843845B2 (en) | 2000-07-03 | 2011-12-21 | トヨタ自動車株式会社 | Fuel cell system and control method thereof |
-
1980
- 1980-02-08 JP JP55014569A patent/JPS5829242B2/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6117934U (en) * | 1984-07-06 | 1986-02-01 | ヤンマー農機株式会社 | threshing equipment |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS56114803A (en) | 1981-09-09 |
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