JP2005298300A - Hydrogen reformer - Google Patents

Hydrogen reformer Download PDF

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JP2005298300A
JP2005298300A JP2004120328A JP2004120328A JP2005298300A JP 2005298300 A JP2005298300 A JP 2005298300A JP 2004120328 A JP2004120328 A JP 2004120328A JP 2004120328 A JP2004120328 A JP 2004120328A JP 2005298300 A JP2005298300 A JP 2005298300A
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hydrogen
catalyst
liquid fuel
amount
storage unit
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Yukio Kasahara
幸雄 笠原
Tsutomu Miyamoto
勉 宮本
Yuji Fujimori
裕司 藤森
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Seiko Epson Corp
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Seiko Epson Corp
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    • 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
    • Y02E60/50Fuel cells

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Abstract

<P>PROBLEM TO BE SOLVED: To provide a hydrogen reforming device where hydrogen generation can be precisely controlled and miniaturization can be certainly promoted. <P>SOLUTION: A catalyst supporting part 4 is moved vertically and directly by a moving part 6 being physically connected to it. A catalyst 5 is in contact with a hydrogen liquid fuel 7 and then a catalytic reaction is caused. Therefore the contacting area of the catalyst 5 with the hydrogen liquid fuel 7 can be certainly controlled by its moving distance and then the amount of generated hydrogen is precisely controlled. As an additional mechanism to regulate the supplying amount of a reaction object is not necessary, the hydrogen reforming device 1 being easy to be handled can be obtained. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、水素液体燃料に触媒を接触させて水素を発生させる水素改質装置に関する。   The present invention relates to a hydrogen reformer that generates hydrogen by bringing a catalyst into contact with hydrogen liquid fuel.

水素を利用する例として、燃料電池は、外部から燃料(水素)と空気(酸素)とを連続的に別々の電極に供給し、これらを電極に含ませた触媒を利用して、電気化学的に反応させて電気エネルギーを取り出すものである。その中でも高分子固体電解質膜を用いたものは、低温で作動できて小型化が可能なので期待されている。   As an example of using hydrogen, a fuel cell supplies fuel (hydrogen) and air (oxygen) from the outside continuously to separate electrodes, and uses a catalyst containing these in an electrochemical cell. To extract electric energy. Among them, those using polymer solid electrolyte membranes are expected because they can operate at low temperatures and can be miniaturized.

本来、このような燃料電池では、電極に直接水素を供給するのがよいが、気体の水素は取り扱いが面倒で、高圧容器が必要になるなどの問題があった。従って、液体のメタノールを燃料として供給して、電極内で触媒によって水素を発生させるダイレクトメタノール方式(Direct Methanol Fuel Cell,DMFC)が主流となっている。この方式は、液体のメタノールを燃料としているため、小型燃料カートリッジによって燃料補給が可能で、システムをコンパクトにできて取り扱いやすい。しかし、高分子固体電解質膜をメタノールが透過する現象(クロスオーバ現象)があり、水素を直接供給する燃料電池と比較して、発電能力が20〜30%に低下するという問題があった。   Originally, in such a fuel cell, it is preferable to supply hydrogen directly to the electrode, but there is a problem that gaseous hydrogen is troublesome to handle and requires a high-pressure vessel. Accordingly, a direct methanol fuel cell (DMFC), in which liquid methanol is supplied as fuel and hydrogen is generated by a catalyst in an electrode, has become the mainstream. Since this system uses liquid methanol as fuel, fuel can be replenished with a small fuel cartridge, and the system can be made compact and easy to handle. However, there is a phenomenon that methanol permeates through the polymer solid electrolyte membrane (crossover phenomenon), and there is a problem that the power generation capacity is reduced to 20 to 30% as compared with a fuel cell that directly supplies hydrogen.

以上のような燃料電池の例に限らず、高圧容器が不要で、水素を必要に応じて供給できる装置はいろいろな分野で望まれている。その中で、液体の燃料を必要に応じて改質して気体の水素を発生させる装置が工夫されている。
例えば、水の収められた容器内で、水に落下させるMg粒子の供給量を調節して水素を発生させる装置が知られている(例えば、特許文献1参照)。
また、固体の触媒を容器内の下方に位置させて、滴下する金属水素錯化合物のアルカリ水溶液の供給量を調整することにより、水素を発生させる装置が知られている(例えば、特許文献2参照)。
さらに、容器内に液体の金属水素錯化合物をポンプで供給量を調節しながら注入して、容器内に設けられた触媒と反応させて、水素を発生させる装置が知られている(例えば、特許文献3参照)。
An apparatus capable of supplying hydrogen as needed is desired in various fields, without being limited to the fuel cell example described above. Among them, an apparatus for generating gaseous hydrogen by reforming liquid fuel as necessary has been devised.
For example, an apparatus that generates hydrogen by adjusting the supply amount of Mg particles dropped into water in a container containing water is known (see, for example, Patent Document 1).
Also, an apparatus for generating hydrogen by positioning a solid catalyst below the inside of the container and adjusting the supply amount of the alkaline aqueous solution of the metal hydride complex to be dropped is known (for example, see Patent Document 2). ).
Furthermore, an apparatus is known in which a liquid metal hydride complex compound is injected into a container while adjusting the supply amount by a pump, and reacted with a catalyst provided in the container to generate hydrogen (for example, a patent) Reference 3).

特開2003−292302号公報(第1〜第2頁、図1)Japanese Patent Laying-Open No. 2003-292302 (first and second pages, FIG. 1) 特開2003−146605号公報(第2〜第3頁、図1)JP 2003-146605 A (2nd to 3rd pages, FIG. 1) 特開2002−29702号公報(第2〜第3頁、図1)JP 2002-29702 A (2nd to 3rd pages, FIG. 1)

ところで、上記各文献では、水素発生反応に必要な反応対象物の供給量を調節することによって、水素発生量を調節している。しかし、これら反応対象物は粒子や粉体の集合物および液体などの流動体であるために、その供給量を精度よく制御することは困難であり、水素発生量を精密に調節できないという問題がある。特に、特許文献3では、液体を容器に注入するためのポンプも必要となり、装置の小型化が難しいという問題がある。   By the way, in each of the above documents, the hydrogen generation amount is adjusted by adjusting the supply amount of the reaction object necessary for the hydrogen generation reaction. However, since these reaction objects are aggregates of particles and powders and fluids such as liquids, it is difficult to accurately control the supply amount, and the amount of hydrogen generation cannot be precisely adjusted. is there. In particular, Patent Document 3 requires a pump for injecting a liquid into a container, and there is a problem that it is difficult to reduce the size of the apparatus.

本発明の目的は、発生水素量のコントロールを精密にでき、小型の水素改質装置を提供することにある。   An object of the present invention is to provide a small-sized hydrogen reforming apparatus that can precisely control the amount of generated hydrogen.

本発明の水素改質装置は、水素液体燃料貯蔵部と、前記水素液体燃料貯蔵部内の水素液体燃料に浸漬自在に設けられて触媒を保持する触媒保持部と、前記水素液体燃料および前記触媒の反応により発生した水素の水素量を検出する検出手段と、この検出手段での検出結果に応じて前記触媒保持部の浸漬量を調節するコントローラとを備えていることを特徴とする。   The hydrogen reforming apparatus of the present invention includes a hydrogen liquid fuel storage unit, a catalyst holding unit that is provided so as to be immersed in the hydrogen liquid fuel in the hydrogen liquid fuel storage unit, and holds the catalyst, the hydrogen liquid fuel, and the catalyst. It is characterized by comprising a detecting means for detecting the amount of hydrogen generated by the reaction, and a controller for adjusting the amount of immersion of the catalyst holding part according to the detection result of the detecting means.

この発明によれば、触媒が保持された触媒保持部が、直接移動して水素液体燃料中に浸漬し、反応する構成なので、この浸漬量を水素発生量に応じて制御することにより、水素液体燃料と触媒との接触面積の調節が確実に行なわれ、水素発生量が精密にコントロールされる。また、反応の対象物の供給量を調節する付帯機構が必要ないので、小型の水素改質装置が得られる。   According to this invention, since the catalyst holding part holding the catalyst moves directly and is immersed in the hydrogen liquid fuel and reacts, the hydrogen liquid can be controlled by controlling the amount of immersion according to the amount of hydrogen generated. The contact area between the fuel and the catalyst is reliably adjusted, and the amount of hydrogen generation is precisely controlled. In addition, since there is no need for an incidental mechanism for adjusting the supply amount of the reaction object, a small hydrogen reformer can be obtained.

本発明では、前記触媒保持部が略直線上を移動する構成が好ましい。
この発明では、触媒保持部が略直線上を移動する動きであるので、移動機構が簡単になり、より小型化が可能である。従って、装置全体としても小型になる。
In the present invention, a configuration in which the catalyst holding part moves on a substantially straight line is preferable.
In this invention, since the catalyst holding part moves in a substantially straight line, the moving mechanism is simplified and the size can be further reduced. Therefore, the overall apparatus is also small.

本発明では、前記検出手段は圧力センサである構成が好ましい。
この発明では、検出手段が圧力センサであることによって、水素改質装置内の圧力に応じた水素発生量の精密なコントロールが可能になる。また、圧力を必要最小限の適正な圧力に設定すれば、耐圧構造も必要でなくなり装置全体が小型になる。
In the present invention, the detection means is preferably a pressure sensor.
In the present invention, since the detection means is a pressure sensor, it is possible to precisely control the amount of hydrogen generated according to the pressure in the hydrogen reforming apparatus. Moreover, if the pressure is set to a necessary minimum appropriate pressure, the pressure-resistant structure is not necessary, and the entire apparatus is reduced in size.

本発明では、前記水素液体燃料貯蔵部が脱着可能である構成が好ましい。
この発明では、水素液体燃料貯蔵部が脱着可能であるので、使用済み燃料の補充や交換の操作を水素液体燃料貯蔵部である容器ごと行えて、バルブやポンプ等の供給機構の操作が不要となり、取り扱いが簡便になる。
In the present invention, a configuration in which the hydrogen liquid fuel storage section is detachable is preferable.
In this invention, since the hydrogen liquid fuel storage part is detachable, the spent fuel can be replenished and replaced for each container as the hydrogen liquid fuel storage part, and the operation of supply mechanisms such as valves and pumps becomes unnecessary. , Handling becomes simple.

以下、本発明の実施形態を図面に基づいて説明する。
図1には、本実施形態に係る水素改質装置1の水素が発生していない状態の全体概念図を、図2には、水素が発生している状態の全体概念図を示した。
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
FIG. 1 shows an overall conceptual diagram of the hydrogen reforming apparatus 1 according to this embodiment in a state where hydrogen is not generated, and FIG. 2 shows an overall conceptual diagram of a state where hydrogen is generated.

図1において、水素改質装置1は、燃料電池13に供給する水素を水素液体燃料7と触媒5との反応により生じさせるものであって、内部に水素液体燃料7が貯蔵された水素液体燃料貯蔵部3と、発生した水素が一時的に貯蔵される水素貯蔵部2とを備えており、止め具14を用いることで、水素液体燃料貯蔵部3が水素貯蔵部2に対して脱着可能に設けられている。この二つの接続部分には、発生する水素が漏れないように、パッキン15が設けられている。これら主要構成部の構造は、数気圧に耐える構造でよい。   In FIG. 1, a hydrogen reformer 1 generates hydrogen to be supplied to a fuel cell 13 by a reaction between a hydrogen liquid fuel 7 and a catalyst 5, and the hydrogen liquid fuel in which the hydrogen liquid fuel 7 is stored. The storage unit 3 and the hydrogen storage unit 2 in which the generated hydrogen is temporarily stored are provided, and the hydrogen liquid fuel storage unit 3 can be detached from the hydrogen storage unit 2 by using the stopper 14. Is provided. A packing 15 is provided at the two connection portions so that generated hydrogen does not leak. The structure of these main components may be a structure that can withstand several atmospheric pressures.

ここで、水素液体燃料7としては、メタノール、シクロヘキサン、デカリン等の炭化水素やホウ素化水素ナトリウム、水素化アルミニウムリチュウム等の金属水素錯化合物のアルカリ水溶液を使用できる。   Here, as the hydrogen liquid fuel 7, an alkaline aqueous solution of a hydrocarbon such as methanol, cyclohexane or decalin, or a metal hydride complex compound such as sodium borohydride or lithium aluminum hydride can be used.

水素貯蔵部2と水素液体燃料貯蔵部3が接続されて形成された空間内部には、触媒5が保持された触媒保持部4が設けられている。触媒保持部4は、上下に移動する可動部6に連結されていて、水素貯蔵部2と水素液体燃料貯蔵部3との間を、図1の矢印で示すように直線的に移動し、水素液体燃料7に浸漬自在となっている。ここで、可動部6と水素貯蔵部2との摺動部は、パッキン等で気密性が確保されている(図示せず)。   Inside a space formed by connecting the hydrogen storage unit 2 and the hydrogen liquid fuel storage unit 3, a catalyst holding unit 4 holding the catalyst 5 is provided. The catalyst holding unit 4 is connected to a movable unit 6 that moves up and down, and moves linearly between the hydrogen storage unit 2 and the hydrogen liquid fuel storage unit 3 as shown by the arrows in FIG. The liquid fuel 7 can be immersed freely. Here, the sliding portion between the movable portion 6 and the hydrogen storage portion 2 is secured by packing or the like (not shown).

触媒5が保持された触媒保持部4の構造は、メッシュ状等の隙間がある構造で、水素液体燃料7が容易に触媒保持部4に浸入できるようになっており、触媒5と効率よく接触する。そして、図2に示すように、触媒保持部4が水素燃料貯蔵部3に入って、触媒5と水素液体燃料7が接触すると、その接触面積に応じた量の水素が発生し、発生した水素は、矢印で示すように水素貯蔵部2に貯蔵される。   The structure of the catalyst holding part 4 holding the catalyst 5 is a structure having a mesh-like gap, so that the hydrogen liquid fuel 7 can easily enter the catalyst holding part 4, and efficiently contact the catalyst 5. To do. Then, as shown in FIG. 2, when the catalyst holding unit 4 enters the hydrogen fuel storage unit 3 and the catalyst 5 and the hydrogen liquid fuel 7 come into contact with each other, an amount of hydrogen corresponding to the contact area is generated, and the generated hydrogen Is stored in the hydrogen storage unit 2 as indicated by arrows.

触媒5は、ニッケル、コバルト、ジルコニウム、ロジウム、白金、パラジウム、白金、金、銀あるいはこれらを含んだ合金など公知のものが使用できる。また、これらをカーボン微粉体に担持したものであってもよいし、これらの表面をフッ化処理したものも使用できる。   As the catalyst 5, a known catalyst such as nickel, cobalt, zirconium, rhodium, platinum, palladium, platinum, gold, silver, or an alloy containing these can be used. Moreover, what carried these on the carbon fine powder may be sufficient, and what carried out the fluorination treatment of these surfaces can also be used.

また、触媒5の単位体積当りの表面積を大きくすれば、水素液体燃料7との接触面積も広がり、水素発生の効率がよくなり、触媒保持部4の小型化も可能になる。触媒の単位体積あたりの表面積を広げるには、粒子状や粉末状であってもよいし、その他多孔質構造やフラクタクル構造など、種々のよく知られた面積を広げる構造を使用することができる。
ここで、粒子や粉末の密度あるいは前述の構造を浸漬の深さ方向に対して均一にすれば、浸漬量に対して接触面積が比例することになり、水素発生量の制御も行いやすい。
Further, if the surface area per unit volume of the catalyst 5 is increased, the contact area with the hydrogen liquid fuel 7 is increased, the efficiency of hydrogen generation is improved, and the catalyst holding unit 4 can be downsized. In order to increase the surface area per unit volume of the catalyst, it may be in the form of particles or powder, and various other well-known structures such as a porous structure or a fractal structure can be used.
Here, if the density of the particles or powder or the above-described structure is made uniform in the immersion depth direction, the contact area is proportional to the immersion amount, and the hydrogen generation amount can be easily controlled.

可動部6は、小型のピエゾ素子を利用した超音波モータ8で駆動される。可動部6の駆動は、ラックおよびピニオン等の回転運動を直線運動に変換するものであってもよい。超音波モータ8は、コントローラ9に電気的に接続されており、このコントローラ9からの駆動信号によって駆動される。   The movable part 6 is driven by an ultrasonic motor 8 using a small piezo element. The drive of the movable part 6 may be one that converts a rotational motion of a rack and pinion into a linear motion. The ultrasonic motor 8 is electrically connected to the controller 9 and is driven by a drive signal from the controller 9.

コントローラ9には、水素貯蔵部2内部に設けられた検出手段としての圧力センサ10、および水素改質装置1と燃料電池13とを結ぶ供給路12の途中に設けられた供給弁11も接続されている。   Also connected to the controller 9 are a pressure sensor 10 as a detecting means provided in the hydrogen storage unit 2 and a supply valve 11 provided in the middle of a supply path 12 connecting the hydrogen reformer 1 and the fuel cell 13. ing.

水素発生量の調整方法を以下に述べる。
まず、水素改質装置1、燃料電池13が搭載された装置の起動は、次に述べる方法で行うことができる。
供給弁11に、水素貯蔵部2の内部が所定の圧力以上になったら自動的に弁を開放する差圧作動弁としての機能を持たせておき、起動のときのみ、一次、二次電池等を電源として超音波モータ8を駆動し、触媒保持部4を下に下げて水素を発生させる。水素貯蔵部2の内部が所定の圧力に達すると、発生した水素は燃料電池13に供給されて、燃料電池13が発電を開始する。ここで、コントローラ9および超音波モータ8の電源を燃料電池13に切換可能に設けておけば、起動後の動作が燃料電池13を電源として行える。このようにすれば、起動用の二次電池の容量を少なくでき、装置が小型になる。
A method for adjusting the amount of hydrogen generation will be described below.
First, the hydrogen reformer 1 and the device on which the fuel cell 13 is mounted can be started by the method described below.
The supply valve 11 has a function as a differential pressure operation valve that automatically opens the valve when the internal pressure of the hydrogen storage unit 2 becomes a predetermined pressure or higher. Is used as a power source to drive the ultrasonic motor 8 and lower the catalyst holding unit 4 downward to generate hydrogen. When the inside of the hydrogen storage unit 2 reaches a predetermined pressure, the generated hydrogen is supplied to the fuel cell 13 and the fuel cell 13 starts power generation. Here, if the power source of the controller 9 and the ultrasonic motor 8 is provided so as to be switchable to the fuel cell 13, the operation after startup can be performed using the fuel cell 13 as a power source. In this way, the capacity of the start-up secondary battery can be reduced, and the device can be downsized.

起動後、触媒5が劣化する等によって水素の発生量が減少し、水素貯蔵部2内の圧力が下がった場合、コントローラ9は、圧力センサ10で検出される水素貯蔵部2内の圧力に応じた電気信号を処理して、超音波モータ8に可動部6を下方に移動させる信号を出力し、触媒保持部4を下げる。これにより浸漬量が増加すると、発生する水素量が再び増加する。また、コントローラ9は、供給弁11を絞る信号も供給弁11に出力して水素貯蔵部2内の圧力を上げる。   After the start-up, when the amount of hydrogen generated decreases due to deterioration of the catalyst 5 and the pressure in the hydrogen storage unit 2 decreases, the controller 9 responds to the pressure in the hydrogen storage unit 2 detected by the pressure sensor 10. The electric signal is processed, and a signal for moving the movable portion 6 downward is output to the ultrasonic motor 8 to lower the catalyst holding portion 4. As a result, when the amount of immersion increases, the amount of generated hydrogen increases again. The controller 9 also outputs a signal to throttle the supply valve 11 to the supply valve 11 to increase the pressure in the hydrogen storage unit 2.

また、圧力が必要以上に上昇すると、コントローラ9は、圧力センサ10で検出される水素貯蔵部2内の圧力に応じた電気信号を処理して、超音波モータ8に可動部6を上方に移動させる信号を出力して触媒保持部4を引き上げる。触媒保持部4が引き上げられると、浸漬量が減少し、水素発生量が直ちに減少する。また、コントローラ9は、供給弁11をさらに開く信号をも出力し、燃料電池13に水素を多く供給するとともに、水素貯蔵部2の内部の圧力を下げる。
以上の二つのフィードバック処理により、水素改質装置1内の起動後の圧力は一定に保たれ、水素の供給も安定的に行われる。
本実施形態では、水素の供給先として燃料電池13を示したが、供給先はこれに限られるものではない。
When the pressure rises more than necessary, the controller 9 processes an electrical signal corresponding to the pressure in the hydrogen storage unit 2 detected by the pressure sensor 10 and moves the movable unit 6 upward to the ultrasonic motor 8. The catalyst holding part 4 is pulled up by outputting the signal to be made. When the catalyst holding part 4 is pulled up, the amount of immersion decreases and the amount of hydrogen generation decreases immediately. The controller 9 also outputs a signal for further opening the supply valve 11 to supply a large amount of hydrogen to the fuel cell 13 and reduce the pressure inside the hydrogen storage unit 2.
By the above two feedback processes, the pressure after startup in the hydrogen reforming apparatus 1 is kept constant, and hydrogen is also supplied stably.
In the present embodiment, the fuel cell 13 is shown as a hydrogen supply destination, but the supply destination is not limited to this.

このような本実施形態によれば、以下の効果がある。
(1)触媒保持部4が、物理的に連結された可動部6によって直接移動して水素液体燃料7と接触して反応する構成なので、接触面積の調節を確実に行うことができ、水素発生量が精密にコントロールできる。また、反応の対象物の供給量を調節する付帯機構が必要ないので、取り扱いの簡便な小型の水素改質装置1が得ることができる。
According to this embodiment, there are the following effects.
(1) Since the catalyst holding part 4 moves directly by the physically connected movable part 6 and contacts and reacts with the hydrogen liquid fuel 7, the contact area can be adjusted reliably, and hydrogen is generated. The amount can be precisely controlled. Moreover, since an incidental mechanism for adjusting the supply amount of the reaction object is not necessary, a small hydrogen reforming apparatus 1 that is easy to handle can be obtained.

(2)可動部6が略直線上を移動する動きであるので、可動構造を簡単にでき、小型にできる。従って、装置全体としても小型にできる。 (2) Since the movable part 6 moves substantially on a straight line, the movable structure can be simplified and reduced in size. Accordingly, the entire apparatus can be reduced in size.

(3)水素貯蔵部2に圧力センサ10を備えることによって、水素貯蔵部2内の圧力によって水素発生量のコントロールでき、高圧に保つ必要がないので耐圧構造も必要でなく水素改質装置1が小型にできる。また、水素改質装置1内の圧力を一定にでき、安定して水素を供給できる。 (3) By providing the hydrogen storage unit 2 with the pressure sensor 10, the amount of hydrogen generated can be controlled by the pressure in the hydrogen storage unit 2, and it is not necessary to maintain a high pressure. Can be small. Moreover, the pressure in the hydrogen reforming apparatus 1 can be made constant, and hydrogen can be supplied stably.

(4)水素液体燃料貯蔵部3が脱着可能に接続されるので、使用済み燃料の補充や交換の操作を水素液体燃料貯蔵部3である容器ごと行うことができ、バルブやポンプ等の供給機構の操作が不要となり、取り扱いを簡便にできる。 (4) Since the hydrogen liquid fuel storage unit 3 is detachably connected, replenishment and replacement of spent fuel can be performed for each container as the hydrogen liquid fuel storage unit 3, and a supply mechanism such as a valve or a pump Is unnecessary, and handling can be simplified.

なお、本発明は前述の実施形態に限定されるものではなく、本発明の目的を達成できる範囲での変形、改良等は本発明に含まれるものである。
例えば、前記実施形態では、触媒保持部4に触媒5が保持され、水素液体燃料7との接触によって水素を発生させていたが、本発明では、触媒5の代わりに粒子状のMgを用いて、水と反応させて水素を発生させてもよい。
また、本発明では、触媒反応をより効率的にするために、触媒担持部4に加熱機構をつけてもよい。
It should be noted that the present invention is not limited to the above-described embodiments, and modifications, improvements, and the like within the scope that can achieve the object of the present invention are included in the present invention.
For example, in the above embodiment, the catalyst 5 is held in the catalyst holding unit 4 and hydrogen is generated by contact with the hydrogen liquid fuel 7. In the present invention, particulate Mg is used instead of the catalyst 5. Alternatively, hydrogen may be generated by reacting with water.
In the present invention, in order to make the catalytic reaction more efficient, the catalyst support 4 may be provided with a heating mechanism.

本発明を実施するための最良の構成、方法などは、以上の記載で開示されているが、本発明は、これに限定されるものではない。すなわち、本発明は、主に特定の実施形態に関して特に図示され、かつ、説明されているが、本発明の技術的思想および目的の範囲から逸脱することなく、以上述べた実施形態に対し、形状、材質、数量、その他の詳細な構成において、当業者が様々な変形を加えることができるものである。
したがって、上記に開示した形状、材質などを限定した記載は、本発明の理解を容易にするために例示的に記載したものであり、本発明を限定するものではないから、それらの形状、材質などの限定の一部もしくは全部の限定を外した部材の名称での記載は、本発明に含まれるものである。
The best configuration, method and the like for carrying out the present invention have been disclosed in the above description, but the present invention is not limited to this. That is, the invention has been illustrated and described primarily with respect to particular embodiments, but may be configured for the above-described embodiments without departing from the scope and spirit of the invention. Various modifications can be made by those skilled in the art in terms of materials, quantity, and other detailed configurations.
Therefore, the description limited to the shape, material, etc. disclosed above is an example for easy understanding of the present invention, and does not limit the present invention. The description by the name of the member which remove | excluded the limitation of one part or all of such restrictions is included in this invention.

水素改質装置の全体概念図。1 is an overall conceptual diagram of a hydrogen reformer. 水素改質装置で水素発生時の全体概念図。The whole conceptual diagram at the time of hydrogen generation with a hydrogen reformer.

符号の説明Explanation of symbols

1…水素改質装置、2…水素貯蔵部、3…水素液体燃料貯蔵部、4…触媒保持部、5…触媒、6…可動部、7…水素液体燃料、8…超音波モータ、9…コントローラ、10…検出手段である圧力センサ、11…供給弁、12…供給路、13…燃料電池。

DESCRIPTION OF SYMBOLS 1 ... Hydrogen reformer, 2 ... Hydrogen storage part, 3 ... Hydrogen liquid fuel storage part, 4 ... Catalyst holding part, 5 ... Catalyst, 6 ... Movable part, 7 ... Hydrogen liquid fuel, 8 ... Ultrasonic motor, 9 ... Controller, 10 ... Pressure sensor as detection means, 11 ... Supply valve, 12 ... Supply path, 13 ... Fuel cell.

Claims (4)

水素液体燃料貯蔵部と、
前記水素液体燃料貯蔵部内の水素液体燃料に浸漬自在に設けられて触媒を保持する触媒保持部と、
前記水素液体燃料および前記触媒の反応により発生した水素の水素量を検出する検出手段と、
この検出手段での検出結果に応じて前記触媒保持部の浸漬量を調節するコントローラとを備えていることを特徴とする水素改質装置。
A hydrogen liquid fuel storage unit;
A catalyst holding unit that is provided so as to be immersed in the hydrogen liquid fuel in the hydrogen liquid fuel storage unit and holds the catalyst; and
Detecting means for detecting a hydrogen amount of hydrogen generated by a reaction between the hydrogen liquid fuel and the catalyst;
A hydrogen reforming apparatus, comprising: a controller that adjusts the amount of immersion of the catalyst holding unit according to the detection result of the detection means.
請求項1に記載の水素改質装置において、
前記触媒保持部が略直線上を移動することを特徴とする水素改質装置。
The hydrogen reformer according to claim 1,
The hydrogen reforming apparatus, wherein the catalyst holding part moves on a substantially straight line.
請求項1または請求項2に記載の水素改質装置において、
前記検出手段は圧力センサであることを特徴とする水素改質装置。
In the hydrogen reforming apparatus according to claim 1 or 2,
The hydrogen reforming apparatus characterized in that the detection means is a pressure sensor.
請求項1〜請求項3のいずれかに記載の水素改質装置において、
前記水素液体燃料貯蔵部が脱着可能であることを特徴とする水素改質装置。


In the hydrogen reforming apparatus according to any one of claims 1 to 3,
The hydrogen reforming apparatus, wherein the hydrogen liquid fuel storage unit is detachable.


JP2004120328A 2004-04-15 2004-04-15 Hydrogen reformer Withdrawn JP2005298300A (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100670388B1 (en) * 2005-12-21 2007-01-17 한국생산기술연구원 Portable hydrogen generator
KR100757273B1 (en) * 2006-03-27 2007-09-10 (주)오선텍 Self-Activating Hydrogen Cartridge
US7574122B2 (en) 2005-05-26 2009-08-11 Sanyo Electric Co., Ltd. Image stabilizing device
JP2011140420A (en) * 2010-01-07 2011-07-21 Seiko Instruments Inc Hydrogen generating apparatus and fuel cell system
JP2018502719A (en) * 2014-12-19 2018-02-01 ザ コミッサリア タ レネルジ アトミーク エ オ ザルターナテイヴズ(シイ・イー・エイ) Gas generator with buoyant catalyst support

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7574122B2 (en) 2005-05-26 2009-08-11 Sanyo Electric Co., Ltd. Image stabilizing device
KR100670388B1 (en) * 2005-12-21 2007-01-17 한국생산기술연구원 Portable hydrogen generator
KR100757273B1 (en) * 2006-03-27 2007-09-10 (주)오선텍 Self-Activating Hydrogen Cartridge
JP2011140420A (en) * 2010-01-07 2011-07-21 Seiko Instruments Inc Hydrogen generating apparatus and fuel cell system
JP2018502719A (en) * 2014-12-19 2018-02-01 ザ コミッサリア タ レネルジ アトミーク エ オ ザルターナテイヴズ(シイ・イー・エイ) Gas generator with buoyant catalyst support

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