JPH07320763A - Power generating method, power generating device, and automobile loaded with power generating device - Google Patents

Power generating method, power generating device, and automobile loaded with power generating device

Info

Publication number
JPH07320763A
JPH07320763A JP6108626A JP10862694A JPH07320763A JP H07320763 A JPH07320763 A JP H07320763A JP 6108626 A JP6108626 A JP 6108626A JP 10862694 A JP10862694 A JP 10862694A JP H07320763 A JPH07320763 A JP H07320763A
Authority
JP
Japan
Prior art keywords
hydrogen
fuel cell
fuel
containing gas
reforming
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.)
Pending
Application number
JP6108626A
Other languages
Japanese (ja)
Inventor
Shinji Kawasaki
真司 川崎
Tomonori Takahashi
知典 高橋
Manabu Isomura
学 磯村
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.)
NGK Insulators Ltd
Original Assignee
NGK Insulators 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 NGK Insulators Ltd filed Critical NGK Insulators Ltd
Priority to JP6108626A priority Critical patent/JPH07320763A/en
Publication of JPH07320763A publication Critical patent/JPH07320763A/en
Pending legal-status Critical Current

Links

Classifications

    • 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

Abstract

PURPOSE:To provide a power generating device which is conformable to a sudden load fluctuation and requires no auxiliary device such as high output battery at starting by providing a buffer means and a means for supplying a fuel of fixed pressure from the buffer means to a fuel cell. CONSTITUTION:Methanol 1 is mixed with water 2 and evaporated in an evaporator 3, and the evaporated methanol and steam are guided into a reformer 4 to generate a reformed gas consisting of hydrogen, carbon monoxide, and carbon dioxide. The reformed gas is then supplied to a hydrogen separating device 5 consisting of a hydrogen separating film to separate only hydrogen gas from the other gases, and the resulting hydrogen gas is stored in a buffer device 8 through a pressure reducing device 6 and a pressure raising device 7. The hydrogen stored in the device 8 is supplied to a solid polymer electrolytic fuel cell 9, with a prescribed quantity and prescribed pressure, through a hydrogen supplying device 10 such as a pressure reducing valve as the fuel of the cell 9. Thus, the supplying gas pressure to the cell 9 is stabilized, and conformable to a sudden load fluctuation, and a high output battery at starting can be dispensed with.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】 本発明は、メタン、プロパン、
メタノール、エタノール、石油等の炭化水素および/ま
たは酸素原子を含む炭化水素などの燃料から水素を得、
これを燃料電池に供給することからなる発電方法と発電
装置及び該発電装置を搭載した自動車に関する。
The present invention relates to methane, propane,
Obtaining hydrogen from hydrocarbons such as methanol, ethanol, petroleum and / or hydrocarbons containing oxygen atoms,
The present invention relates to a power generation method including supplying the fuel cell to a fuel cell, a power generation device, and an automobile equipped with the power generation device.

【0002】[0002]

【従来の技術】 近年、公害防止などの観点から、リン
酸型燃料電池や固体高分子電解質型燃料電池などの燃料
電池が注目をあつめている。このような燃料電池の例と
して、例えば、特開平4−121973号公報には、燃
料改質器内で改質され、生成した水素含有ガスから水素
のみを分離し、この水素をバイパスラインに設けた水素
吸蔵合金システムで貯蔵することが記載されている。こ
の例では、起動時に吸蔵合金を暖めて水素を放出させ、
燃料として利用するもので、起動速度を最大限にするた
めに用いるものである。
2. Description of the Related Art In recent years, fuel cells such as phosphoric acid fuel cells and solid polymer electrolyte fuel cells have been attracting attention from the viewpoint of pollution prevention. As an example of such a fuel cell, for example, in Japanese Patent Laid-Open No. 4-121973, only hydrogen is separated from a hydrogen-containing gas reformed in a fuel reformer and the hydrogen is provided in a bypass line. It is described to store in a hydrogen storage alloy system. In this example, at startup, the storage alloy is warmed to release hydrogen,
It is used as fuel and is used to maximize the startup speed.

【0003】 また、特開平4−325402号公報に
は、炭化水素等を水蒸気改質して水素を製造するに際
し、水蒸気改質で生成する水素を逐次水素分離膜により
透過させ、水素透過側を減圧吸引することにより、水素
分離速度、水素分離効率を高める方法が記載されてい
る。
Further, in Japanese Unexamined Patent Publication No. 4-325402, when hydrogen is produced by steam reforming a hydrocarbon or the like, hydrogen produced by steam reforming is sequentially permeated through a hydrogen separation membrane, and the hydrogen permeation side is A method for increasing the hydrogen separation rate and the hydrogen separation efficiency by suctioning under reduced pressure is described.

【0004】[0004]

【発明が解決しようとする課題】 しかしながら、上記
特開平4−121973号公報に記載の技術では、水素
を吸蔵合金より取り出すために、温水を貯えておく必要
があり、経済的でない点、水素吸蔵合金の重量が大きい
ため全体のシステムも大規模にする必要が生じるという
欠点があるほか、通常運転時において燃料電池への水素
の供給ガス圧が不安定であり、又急速な負荷変動に対応
ができないという問題があった。例えば、この燃料電池
を自動車に適用した場合には、急発進などにこのままで
は対応できず、高出力バッテリとのハイブリッド化が必
要になる。さらに、水素の分離効率が低いという問題も
あった。
However, in the technique described in Japanese Patent Laid-Open No. 4-121973, it is necessary to store hot water in order to take out hydrogen from the storage alloy, which is uneconomical. Since the weight of the alloy is large, the whole system needs to be large-scaled. In addition, the pressure of hydrogen supply gas to the fuel cell is unstable during normal operation, and it is not possible to cope with rapid load changes. There was a problem that I could not. For example, when this fuel cell is applied to an automobile, it cannot cope with sudden start or the like as it is, and a hybrid with a high output battery is required. Further, there is a problem that the hydrogen separation efficiency is low.

【0005】 一方、上記特開平4−325402号公
報に記載の技術においても、前記と同様に、通常運転時
において燃料電池への水素の供給ガス圧が不安定であ
り、又急速な負荷変動に対応ができないという問題があ
る。
On the other hand, in the technique described in Japanese Patent Laid-Open No. 4-325402, similarly to the above, the hydrogen supply gas pressure to the fuel cell is unstable during normal operation, and rapid load fluctuations occur. There is a problem that we can not respond.

【0006】[0006]

【課題を解決するための手段】 そこで、本発明者は上
記した従来技術の問題を解決するため種々検討行なった
結果、燃料電池などの発電システム(方法、装置)にお
いて、改質器と燃料電池の間に燃料を一旦貯蔵するバッ
ファ手段およびこのバッファ手段より一定圧力の燃料を
燃料電池へ供給する手段を設けることにより、上記従来
技術の問題点が解決できることを見出し、本発明に到達
した。
Therefore, as a result of various studies to solve the above-mentioned problems of the prior art, the present inventors have found that in a power generation system (method, device) such as a fuel cell, a reformer and a fuel cell. The inventors have found that the problems of the above-mentioned conventional techniques can be solved by providing a buffer means for temporarily storing fuel during this period and a means for supplying fuel of a constant pressure from the buffer means to the fuel cell, and arrived at the present invention.

【0007】 即ち、本発明によれば、燃料を改質手段
により改質して水素含有ガスを得、得られた水素含有ガ
スを燃料電池に供給する発電方法において、前記改質手
段と前記燃料電池の間にバッファ手段を設けて、このバ
ッファ手段に水素含有ガスを一旦貯蔵し、次いで該バッ
ファ手段より所定圧力の水素含有ガスを前記燃料電池へ
供給することを特徴とする発電方法が提供される。ま
た、本発明によれば、燃料を改質して水素含有ガスを製
造する改質手段、改質手段により製造された水素含有ガ
スを燃料とする燃料電池を備えた発電装置において、前
記改質手段と前記燃料電池の間に水素含有ガスを一旦貯
蔵するバッファ手段およびこのバッファ手段より所定圧
力の水素含有ガスを前記燃料電池へ供給する水素供給手
段を設けたことを特徴とする発電装置が提供される。
That is, according to the present invention, in the power generation method of reforming the fuel by the reforming means to obtain the hydrogen-containing gas and supplying the obtained hydrogen-containing gas to the fuel cell, the reforming means and the fuel There is provided a power generation method characterized in that a buffer means is provided between cells, the hydrogen-containing gas is temporarily stored in the buffer means, and then the hydrogen-containing gas having a predetermined pressure is supplied from the buffer means to the fuel cell. It Further, according to the present invention, in a power generation device including a reforming unit that reforms a fuel to produce a hydrogen-containing gas, and a fuel cell that uses the hydrogen-containing gas produced by the reforming unit as a fuel, There is provided a power generation device characterized in that a buffer means for temporarily storing a hydrogen-containing gas and a hydrogen supply means for supplying the hydrogen-containing gas of a predetermined pressure from the buffer means to the fuel cell are provided between the means and the fuel cell. To be done.

【0008】 本発明においては、改質手段とバッファ
手段の間に水素分離手段を設け、水素分離手段により改
質手段で生成した水素含有ガスから水素を分離すること
が好ましい。また、水素分離手段が、パラジウム金属又
はパラジウムを含有する合金を水素分離膜として備える
ものからなることが水素分離能の点から好ましく、水素
分離手段より分離された水素を減圧手段により減圧し、
次いでこの減圧手段で減圧された水素を所定圧力まで昇
圧手段により昇圧することが、水素分離速度を向上さ
せ、また装置全体の効率向上の点から好ましい。又、バ
ッファ手段から燃料電池へ水素または水素含有ガスを所
定の圧力で供給する水素供給手段としては、減圧弁であ
ることが好ましい。
In the present invention, it is preferable that a hydrogen separating unit is provided between the reforming unit and the buffer unit, and the hydrogen separating unit separates hydrogen from the hydrogen-containing gas generated by the reforming unit. Further, the hydrogen separating means, preferably comprising a palladium metal or an alloy containing palladium as a hydrogen separation membrane from the viewpoint of hydrogen separation ability, the hydrogen separated by the hydrogen separating means is decompressed by the decompressing means,
Next, it is preferable to increase the pressure of the hydrogen reduced by the pressure reducing means to the predetermined pressure by the pressure increasing means from the viewpoint of improving the hydrogen separation rate and improving the efficiency of the entire apparatus. Further, the hydrogen supply means for supplying hydrogen or hydrogen-containing gas from the buffer means to the fuel cell at a predetermined pressure is preferably a pressure reducing valve.

【0009】 さらに、燃料電池としてはリン酸型燃料
電池、固体高分子電解質型燃料電池を使用できるが、固
体高分子電解質型燃料電池であることが作動温度が10
0℃以下と低いことから好ましく、燃料としては炭化水
素であれば良いが、メタノール、エタノールであること
が液体であり貯蔵、輸送等に好適であることからより好
ましい。本発明の発電装置は、上記のように、水素分離
速度、分離能が向上し、燃料電池への水素含有ガス又は
水素ガスの圧力が安定し、急速な負荷変動にも対応可能
であるため、自動車用として極めて好適である。
Further, a phosphoric acid type fuel cell and a solid polymer electrolyte type fuel cell can be used as the fuel cell, but a solid polymer electrolyte type fuel cell has an operating temperature of 10
The fuel is preferably hydrocarbon because it is as low as 0 ° C. or lower, and methanol and ethanol are more preferable because they are liquid and suitable for storage and transportation. As described above, the power generation device of the present invention has improved hydrogen separation speed and separability, the pressure of the hydrogen-containing gas or hydrogen gas to the fuel cell is stable, and it is possible to cope with rapid load changes. Very suitable for automobiles.

【0010】[0010]

【作用】 本発明では、改質手段と燃料電池の間に水素
含有ガス又は水素を一旦貯蔵するバッファ手段およびこ
のバッファ手段より一定圧力の水素含有ガス又は水素を
燃料電池へ供給する手段を設けたので、燃料電池への供
給ガス圧が安定し、急速な負荷変動にも対応可能であ
り、起動時に、高出力バッテリ等の補助装置が不要であ
る。また、改質手段とバッファ手段の間に水素分離手段
を設けた場合には、水素分離効率が高く、自動車用とし
て極めて好適である。
In the present invention, the buffer means for temporarily storing the hydrogen-containing gas or hydrogen and the means for supplying the hydrogen-containing gas or hydrogen at a constant pressure from the buffer means to the fuel cell are provided between the reforming means and the fuel cell. Therefore, the pressure of the gas supplied to the fuel cell is stable, it is possible to cope with rapid load fluctuations, and an auxiliary device such as a high-power battery is not required at the time of startup. Further, when the hydrogen separating means is provided between the reforming means and the buffer means, the hydrogen separating efficiency is high and it is extremely suitable for automobiles.

【0011】[0011]

【実施例】 次に、本発明を図示の実施例に基づき更に
詳細に説明するが、本発明はこれらの実施例に限られる
ものではない。図1は、本発明に係る発電装置の一実施
例を示すフロー図で、燃料であるメタノール1は水2と
混合し、気化器3にて気化される。気化器3で気化され
たメタノールと水蒸気は、改質器4に導入され、水素、
一酸化炭素および二酸化炭素等からなる改質ガスが生成
される。次いで、得られた改質ガスは水素分離膜からな
る水素分離装置5により水素ガスのみが他のガスから分
離される。水素ガスは、次いで減圧装置6および昇圧装
置7を介してバッファ装置8に貯蔵される。バッファ装
置8に貯蔵された水素は、固体高分子電解質型燃料電池
9の燃料として、所定量および所定圧力にて、減圧弁な
どの水素供給装置10を介して該燃料電池9へ供給され
る。
EXAMPLES Next, the present invention will be described in more detail based on the illustrated examples, but the present invention is not limited to these examples. FIG. 1 is a flow chart showing an embodiment of a power generator according to the present invention, in which methanol 1 as a fuel is mixed with water 2 and vaporized in a vaporizer 3. The methanol and steam vaporized in the vaporizer 3 are introduced into the reformer 4, and hydrogen,
A reformed gas composed of carbon monoxide and carbon dioxide is generated. Then, in the obtained reformed gas, only the hydrogen gas is separated from other gases by the hydrogen separation device 5 including the hydrogen separation membrane. The hydrogen gas is then stored in the buffer device 8 via the pressure reducing device 6 and the pressure increasing device 7. The hydrogen stored in the buffer device 8 is supplied to the fuel cell 9 as a fuel for the solid polymer electrolyte fuel cell 9 at a predetermined amount and a predetermined pressure via a hydrogen supply device 10 such as a pressure reducing valve.

【0012】 なお、燃料電池9へは、燃料として水素
以外に空気11が供給される。また、バッファ装置8か
らは水素供給装置10を介して適当量の水素がライン1
2を通ってバイパスされ、これに空気13が添加されて
(燃焼して)、前記した気化器3、改質器4、または水
素分離装置5における必要熱量を賄うことができる。
In addition to hydrogen, air 11 is supplied to the fuel cell 9 as fuel. In addition, an appropriate amount of hydrogen is supplied from the buffer device 8 via the hydrogen supply device 10 to the line 1.
By passing through 2 and adding air 13 (burning) to this, it is possible to cover the required heat amount in the vaporizer 3, the reformer 4, or the hydrogen separation device 5.

【0013】 以上は本発明の実施例を示したが、これ
に限られない。例えば、燃料1としては、メタノールで
なく、メタン、エタン、エタノール、石油等の炭化水素
であればよい。水素分離装置5の水素分離膜としては、
パラジウム金属又はパラジウムを含有する合金が好まし
く、さらに多孔質基体によりパラジウム金属膜などを支
持する構成のものが好ましい。
Although the embodiment of the present invention has been described above, the present invention is not limited to this. For example, the fuel 1 may be hydrocarbons such as methane, ethane, ethanol and petroleum, instead of methanol. As the hydrogen separation membrane of the hydrogen separation device 5,
Palladium metal or an alloy containing palladium is preferable, and a structure in which a palladium metal film or the like is supported by a porous substrate is preferable.

【0014】 水素分離装置5の下流側で水素を減圧す
る減圧装置6は、これにより水素分離装置5の水素分離
速度、分離効率を向上させることができるものであり、
例えばロータリーポンプ等が用いられる。昇圧装置7と
してはコンプレッサーなどが使用できる。また、バッフ
ァ装置8としては、水素含有ガス又は水素を一旦貯蔵す
ることができるものであれば特に限定されず、例えば、
所定容量の圧力容器や水素吸蔵合金などが用いられる。
圧力が2〜9atm 、容量が1〜50リットル程度の圧力
容器が好ましい。燃料電池9へ所定圧力で水素(水素分
離装置を有さない場合には、水素含有ガス)を供給する
水素供給装置10としては、通常の減圧弁、例えば、ダ
イヤフラム形減圧弁のほか、ピストン形減圧弁、レリー
フ形減圧弁などを用いることができる。
The decompression device 6 for decompressing hydrogen on the downstream side of the hydrogen separation device 5 can improve the hydrogen separation speed and the separation efficiency of the hydrogen separation device 5.
For example, a rotary pump or the like is used. A compressor or the like can be used as the booster 7. Further, the buffer device 8 is not particularly limited as long as it can temporarily store the hydrogen-containing gas or hydrogen, and, for example,
A pressure vessel having a predetermined capacity, a hydrogen storage alloy, or the like is used.
A pressure vessel having a pressure of 2 to 9 atm and a volume of about 1 to 50 liters is preferable. As the hydrogen supply device 10 for supplying hydrogen (hydrogen-containing gas in the case of not having a hydrogen separation device) to the fuel cell 9 at a predetermined pressure, a normal pressure reducing valve, for example, a diaphragm type pressure reducing valve, or a piston type A pressure reducing valve, a relief type pressure reducing valve or the like can be used.

【0015】 以下、本発明の具体的な実施結果を説明
する。 (実施例)図1に示す構成の発電装置を用いた。容量6
0リットルのメタノール燃料タンクを用い、メタノール
1と水2を気化器3に導入し、300℃で気化させた。
気化器3で気化したメタノールと水の混合ガスは、内径
9mmφ、外径11mmφ、長さ500mmのパラジウム膜を
被覆した多孔質のアルミナ管50本からなる水素分離装
置5を内蔵した100mmφ×500mmの改質器4に導入
した。水素分離装置5と改質器4は300℃、10atm
に保持した。次に、水素分離装置5から分離した水素
は、ロータリーポンプ6で0.2atm まで減圧し、次い
でコンプレッサー7で5atm まで昇圧して、容量10リ
ットルで圧力5atm の圧力容器(バッファ装置)8に貯
蔵した。圧力容器8に貯蔵された水素は、ダイヤフラム
形減圧弁9により3atm まで減圧され、固体高分子電解
質型燃料電池9に供給した。
The concrete results of the present invention will be described below. (Example) The power generator having the configuration shown in FIG. 1 was used. Capacity 6
Using a 0 liter methanol fuel tank, methanol 1 and water 2 were introduced into the vaporizer 3 and vaporized at 300 ° C.
The mixed gas of methanol and water vaporized in the vaporizer 3 has an inner diameter of 9 mmφ, an outer diameter of 11 mmφ and a length of 500 mm, and has a built-in hydrogen separation device 5 consisting of 50 porous alumina tubes covered with a palladium membrane. It was introduced into the reformer 4. Hydrogen separator 5 and reformer 4 are 300 ° C, 10 atm
Held in. Next, the hydrogen separated from the hydrogen separator 5 is depressurized to 0.2 atm by the rotary pump 6, then boosted to 5 atm by the compressor 7, and stored in a pressure vessel (buffer device) 8 having a capacity of 10 liters and a pressure of 5 atm. did. The hydrogen stored in the pressure vessel 8 was depressurized to 3 atm by the diaphragm type pressure reducing valve 9 and supplied to the solid polymer electrolyte fuel cell 9.

【0016】 以上の条件で燃料電池を運転したとこ
ろ、通常運転時において、出力は4±0.1kWで安定
していた。また、出力20%から100%までが3秒で
到達できた。さらに、何ら高出力バッテリ等の補助装置
を必要とせず、起動することができ、しかも1秒で起動
することが可能であった。
When the fuel cell was operated under the above conditions, the output was stable at 4 ± 0.1 kW during normal operation. Also, the output could reach from 20% to 100% in 3 seconds. Further, it can be started without requiring any auxiliary device such as a high-power battery, and can be started in 1 second.

【0017】(比較例)図1に示す発電装置からバッフ
ァ装置8を除いた以外は、実施例と同一の装置、条件で
燃料電池を運転した。その結果、通常運転時は、出力は
4±0.1kWで安定していたが、出力20%から10
0%まで到達するのに30秒が必要であった。また、起
動時に、起動用バッテリが必要であり、しかも起動用バ
ッテリを使用した場合であっても、起動まで20秒を要
した。
(Comparative Example) A fuel cell was operated under the same apparatus and conditions as in Example except that the buffer device 8 was omitted from the power generator shown in FIG. As a result, the output was stable at 4 ± 0.1 kW during normal operation, but the output was 20% to 10%.
It took 30 seconds to reach 0%. Further, at the time of starting, a starting battery is required, and even when the starting battery is used, it took 20 seconds to start.

【0018】[0018]

【発明の効果】 以上説明したように、本発明によれ
ば、改質手段と燃料電池の間に水素含有ガス又は水素を
一旦貯蔵するバッファ手段およびこのバッファ手段より
一定圧力の水素含有ガス又は水素を燃料電池へ供給する
手段を設けたので、燃料電池への供給ガス圧が安定し、
急速な負荷変動にも対応が可能であるという利点を有す
る。また、起動時において、高出力バッテリ等の補助装
置が不要である。従って、本発明の発電方法、発電装置
は自動車に適用または搭載することにより、排ガス中の
有害物質の少ない自動車が得られ、環境上でも極めて意
義の大きなものである。
As described above, according to the present invention, the buffer means for temporarily storing the hydrogen-containing gas or hydrogen between the reforming means and the fuel cell, and the hydrogen-containing gas or hydrogen having a constant pressure from the buffer means. Since the means for supplying the fuel cell to the fuel cell is provided, the gas pressure supplied to the fuel cell is stable,
It has an advantage that it can cope with a rapid load change. Further, at the time of startup, an auxiliary device such as a high output battery is unnecessary. Therefore, by applying or mounting the power generation method and power generation device of the present invention to a vehicle, a vehicle with less harmful substances in the exhaust gas can be obtained, which is extremely significant in terms of the environment.

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

【図1】 本発明に係る発電装置の一実施例を示すフロ
ー図である。
FIG. 1 is a flow chart showing an embodiment of a power generator according to the present invention.

【符号の説明】[Explanation of symbols]

1:メタノール、2:水、3:気化器、4:改質器、
5:水素分離装置、6:減圧装置、7:昇圧装置、8:
バッファ装置、9:固体高分子電解質型燃料電池、1
0:水素供給装置、11:空気、12:ライン、13:
空気。
1: Methanol, 2: Water, 3: Vaporizer, 4: Reformer,
5: hydrogen separator, 6: depressurizer, 7: booster, 8:
Buffer device, 9: solid polymer electrolyte fuel cell, 1
0: Hydrogen supply device, 11: Air, 12: Line, 13:
air.

Claims (14)

【特許請求の範囲】[Claims] 【請求項1】 燃料を改質手段により改質して水素含有
ガスを得、得られた水素含有ガスを燃料電池に供給する
発電方法において、 前記改質手段と前記燃料電池の間にバッファ手段を設け
て、このバッファ手段に水素含有ガスを一旦貯蔵し、次
いで該バッファ手段より所定圧力の水素含有ガスを前記
燃料電池へ供給することを特徴とする発電方法。
1. A power generation method for reforming a fuel by a reforming means to obtain a hydrogen-containing gas and supplying the obtained hydrogen-containing gas to a fuel cell, wherein a buffer means is provided between the reforming means and the fuel cell. Is provided, the hydrogen-containing gas is temporarily stored in the buffer means, and then the hydrogen-containing gas having a predetermined pressure is supplied from the buffer means to the fuel cell.
【請求項2】 前記改質手段と前記バッファ手段の間に
水素分離手段を設け、該水素分離手段により前記改質手
段で生成した水素含有ガスより水素を分離し、該水素を
前記燃料電池へ供給する請求項1記載の発電方法。
2. A hydrogen separating unit is provided between the reforming unit and the buffer unit, the hydrogen separating unit separates hydrogen from the hydrogen-containing gas produced by the reforming unit, and the hydrogen is transferred to the fuel cell. The power generation method according to claim 1, wherein the power is supplied.
【請求項3】 前記水素分離手段が、パラジウム金属又
はパラジウムを含有する合金を水素分離膜として備える
請求項2記載の発電方法。
3. The power generation method according to claim 2, wherein the hydrogen separation means comprises palladium metal or an alloy containing palladium as a hydrogen separation membrane.
【請求項4】 前記水素分離手段より分離された水素を
減圧し、その後昇圧する請求項2または3記載の発電方
法。
4. The power generation method according to claim 2, wherein the hydrogen separated by the hydrogen separating means is depressurized and then pressurized.
【請求項5】 前記燃料電池が、固体高分子電解質型燃
料電池である請求項1〜4のいずれかに記載の発電方
法。
5. The power generation method according to claim 1, wherein the fuel cell is a solid polymer electrolyte fuel cell.
【請求項6】 前記燃料が、メタノールである請求項1
〜5のいずれかに記載の発電方法。
6. The fuel is methanol as claimed in claim 1.
The power generation method according to any one of 1 to 5.
【請求項7】 燃料を改質して水素含有ガスを製造する
改質手段、改質手段により製造された水素含有ガスを燃
料とする燃料電池を備えた発電装置において、 前記改質手段と前記燃料電池の間に水素含有ガスを一旦
貯蔵するバッファ手段およびこのバッファ手段より所定
圧力の水素含有ガスを前記燃料電池へ供給する水素供給
手段を設けたことを特徴とする発電装置。
7. A power generation device comprising a reforming means for reforming a fuel to produce a hydrogen-containing gas, and a fuel cell using the hydrogen-containing gas produced by the reforming means as a fuel. A power generator comprising a buffer means for temporarily storing a hydrogen-containing gas between the fuel cells and a hydrogen supply means for supplying the hydrogen-containing gas at a predetermined pressure from the buffer means to the fuel cell.
【請求項8】 前記改質手段と前記バッファ手段の間に
水素分離手段を設けた請求項7記載の発電装置。
8. The power generator according to claim 7, further comprising hydrogen separating means provided between the reforming means and the buffer means.
【請求項9】 前記水素分離手段が、パラジウム金属又
はパラジウムを含有する合金を水素分離膜として備えた
ものである請求項8記載の発電装置。
9. The power generator according to claim 8, wherein the hydrogen separation means comprises palladium metal or an alloy containing palladium as a hydrogen separation membrane.
【請求項10】 前記水素供給手段が減圧弁から構成さ
れる請求項7〜9のいずれかに記載の発電装置。
10. The power generator according to claim 7, wherein the hydrogen supply unit is composed of a pressure reducing valve.
【請求項11】 前記水素分離手段より分離された水素
を減圧する減圧手段と、該減圧手段で減圧された水素を
所定圧力まで昇圧する昇圧手段とを有する請求項8〜1
0のいずれかに記載の発電装置。
11. A depressurizing unit for depressurizing the hydrogen separated by the hydrogen separating unit, and a boosting unit for boosting the hydrogen depressurized by the depressurizing unit to a predetermined pressure.
The power generation device according to any one of 0.
【請求項12】 前記燃料電池が、固体高分子電解質型
燃料電池である請求項7〜11のいずれかに記載の発電
装置。
12. The power generator according to claim 7, wherein the fuel cell is a solid polymer electrolyte fuel cell.
【請求項13】 前記燃料がメタノールである請求項7
〜12のいずれかに記載の発電装置。
13. The fuel of claim 7, wherein the fuel is methanol.
The power generator according to any one of to 12.
【請求項14】 請求項7〜13のいずれかに記載の発
電装置を搭載してなる自動車。
14. An automobile equipped with the power generation device according to claim 7.
JP6108626A 1994-05-23 1994-05-23 Power generating method, power generating device, and automobile loaded with power generating device Pending JPH07320763A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6108626A JPH07320763A (en) 1994-05-23 1994-05-23 Power generating method, power generating device, and automobile loaded with power generating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6108626A JPH07320763A (en) 1994-05-23 1994-05-23 Power generating method, power generating device, and automobile loaded with power generating device

Publications (1)

Publication Number Publication Date
JPH07320763A true JPH07320763A (en) 1995-12-08

Family

ID=14489569

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6108626A Pending JPH07320763A (en) 1994-05-23 1994-05-23 Power generating method, power generating device, and automobile loaded with power generating device

Country Status (1)

Country Link
JP (1) JPH07320763A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0813262A2 (en) * 1996-06-15 1997-12-17 Daimler-Benz Aktiengesellschaft Process for operating a device for steam reforming of methanol
US5984986A (en) * 1996-06-15 1999-11-16 Daimlerchrysler Ag Process for operating a system for the water vapor reforming of methanol
JP2000323157A (en) * 1999-05-14 2000-11-24 Hitachi Ltd Fuel cell power generation system and control method thereof
FR2816759A1 (en) * 2000-11-10 2002-05-17 Renault Utilisation of a palladium and/or polymer based membrane between the reformer and the hydrogen plug reservoir of a device for feeding hydrogen to a fuel cell for electric traction of a vehicle
JP2003282122A (en) * 2002-02-19 2003-10-03 Proton Energy Systems Inc Energy storage and recovery system and its use method
JP2004525488A (en) * 2001-02-21 2004-08-19 アイダテック, エル.エル.シー. Fuel cell system using stored hydrogen
WO2004049486A3 (en) * 2002-11-27 2005-01-27 Hydrogenics Corp Reactant supply for a fuel cell power system
WO2008062806A1 (en) * 2006-11-24 2008-05-29 Toyota Jidosha Kabushiki Kaisha Fuel cell system and fuel cell vehicle
US11289726B2 (en) * 2015-06-09 2022-03-29 Honeywell International Inc. Systems for hybrid fuel cell power generation

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0813262A3 (en) * 1996-06-15 1999-06-30 dbb fuel cell engines GmbH Process for operating a device for steam reforming of methanol
US5984986A (en) * 1996-06-15 1999-11-16 Daimlerchrysler Ag Process for operating a system for the water vapor reforming of methanol
US6048473A (en) * 1996-06-15 2000-04-11 Daimlerchrysler Ag Process for operating a system for the water vapor reforming of methanol
EP0813262A2 (en) * 1996-06-15 1997-12-17 Daimler-Benz Aktiengesellschaft Process for operating a device for steam reforming of methanol
JP2000323157A (en) * 1999-05-14 2000-11-24 Hitachi Ltd Fuel cell power generation system and control method thereof
FR2816759A1 (en) * 2000-11-10 2002-05-17 Renault Utilisation of a palladium and/or polymer based membrane between the reformer and the hydrogen plug reservoir of a device for feeding hydrogen to a fuel cell for electric traction of a vehicle
JP2004525488A (en) * 2001-02-21 2004-08-19 アイダテック, エル.エル.シー. Fuel cell system using stored hydrogen
JP2003282122A (en) * 2002-02-19 2003-10-03 Proton Energy Systems Inc Energy storage and recovery system and its use method
WO2004049486A3 (en) * 2002-11-27 2005-01-27 Hydrogenics Corp Reactant supply for a fuel cell power system
WO2008062806A1 (en) * 2006-11-24 2008-05-29 Toyota Jidosha Kabushiki Kaisha Fuel cell system and fuel cell vehicle
JP2008130492A (en) * 2006-11-24 2008-06-05 Toyota Motor Corp Fuel cell system and fuel cell vehicle
US8741497B2 (en) 2006-11-24 2014-06-03 Toyota Jidosha Kabushiki Kaisha Fuel cell system and fuel cell hybrid vehicle
DE112007002813B4 (en) * 2006-11-24 2016-09-22 Toyota Jidosha Kabushiki Kaisha Fuel cell system and fuel cell hybrid vehicle
US11289726B2 (en) * 2015-06-09 2022-03-29 Honeywell International Inc. Systems for hybrid fuel cell power generation

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