JPH0689735A - Hybrid fuel cell power generation device - Google Patents

Hybrid fuel cell power generation device

Info

Publication number
JPH0689735A
JPH0689735A JP4237498A JP23749892A JPH0689735A JP H0689735 A JPH0689735 A JP H0689735A JP 4237498 A JP4237498 A JP 4237498A JP 23749892 A JP23749892 A JP 23749892A JP H0689735 A JPH0689735 A JP H0689735A
Authority
JP
Japan
Prior art keywords
fuel cell
carbon monoxide
phosphoric acid
anode
supplied
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
JP4237498A
Other languages
Japanese (ja)
Inventor
Yoshiaki Ozawa
芳明 小澤
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.)
Fuji Electric Co Ltd
Original Assignee
Fuji 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 Fuji Electric Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP4237498A priority Critical patent/JPH0689735A/en
Publication of JPH0689735A publication Critical patent/JPH0689735A/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 use the energy of CO effectively by installing a fuel cell which converts the CO energy into electricity at the pre-stage of a phosphoric acid type fuel cell, wherein, however, the CO concentration of the fuel supplied to the phosphoric acid type fuel cell is reduced by means of denaturing of the CO. CONSTITUTION:A solid electrolyte type fuel cell 11 is installed at the rear stage of a modifier 3, and power generation is conducted using a fuel which consists of CO and hydrogen from the modifier 3, wherein the CO is converted into CO2 with the resultant CO concentration reduction, and the gas containing the residual hydrogen is cooled by a cooler 15 and supplied to the anode 7 of a phosphoric acid type fuel cell 6, and thus power generation takes place.

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、リン酸電解質を有する
リン酸型燃料電池と固体電解質を有する固体電解質型燃
料電池とを併設したハイブリッド燃料電池発電装置に関
する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a hybrid fuel cell power generator having a phosphoric acid fuel cell having a phosphoric acid electrolyte and a solid electrolyte fuel cell having a solid electrolyte.

【0002】[0002]

【従来の技術】LNG,LPG等の炭化水素系やメタノ
ール等のアルコール系の原燃料を水蒸気改質したガスを
燃料ガスとして使用するリン酸電解質を有するリン酸型
燃料電池発電装置として、例えば炭化水素系の原燃料を
改質する燃料改質装置とリン酸型燃料電池とからなる図
3に示す系統のものが知られている。図3において、燃
料改質装置は脱硫器2とバーナ4を備える改質器3と一
酸化炭素変成器5とから構成される。リン酸型燃料電池
6はリン酸電解質層と、これを挟持するアノード7及び
カソード8と、発電時生じる熱を除熱する冷却媒体が通
流する冷却通路を有する冷却板9とを備えて構成され
る。
2. Description of the Related Art A phosphoric acid fuel cell power generator having a phosphoric acid electrolyte using a gas obtained by steam reforming a hydrocarbon-based raw fuel such as LNG or LPG or an alcohol-based raw fuel such as methanol as a fuel gas is, for example, carbonized. There is known a system shown in FIG. 3 including a fuel reformer for reforming a hydrogen-based raw fuel and a phosphoric acid fuel cell. In FIG. 3, the fuel reformer comprises a desulfurizer 2, a reformer 3 having a burner 4, and a carbon monoxide shift converter 5. The phosphoric acid fuel cell 6 includes a phosphoric acid electrolyte layer, an anode 7 and a cathode 8 that sandwich the same, and a cooling plate 9 having a cooling passage through which a cooling medium that removes heat generated during power generation flows. To be done.

【0003】このような構成によりLNG,LPG等の
原燃料は脱硫器2を通流して改質器3内の改質触媒に被
毒を与える原燃料に含まれる硫黄分を脱硫する。脱硫し
た原燃料は改質器3に流入し、リン酸型燃料電池6のア
ノード7から排出されるオフガスを燃料としてバーナ4
にて燃焼した燃焼ガスにより加熱されて改質触媒の下に
水素と一酸化炭素とを含むガスに水蒸気改質される。こ
の水蒸気改質されたガスは一酸化炭素変成器5を通流し
て一酸化炭素を二酸化炭素に変成して一酸化炭素濃度の
低い水素に富む改質ガスにし、この改質ガスをリン酸型
燃料電池6のアノード7に供給する。
With such a structure, raw fuel such as LNG and LPG flows through the desulfurizer 2 to desulfurize the sulfur content contained in the raw fuel that poisons the reforming catalyst in the reformer 3. The desulfurized raw fuel flows into the reformer 3, and the burner 4 uses the off-gas discharged from the anode 7 of the phosphoric acid fuel cell 6 as fuel.
The fuel gas is heated by the combustion gas burned at 1, and steam reformed into a gas containing hydrogen and carbon monoxide under the reforming catalyst. The steam-reformed gas is passed through the carbon monoxide shift converter 5 to convert carbon monoxide into carbon dioxide to form a hydrogen-rich reformed gas having a low carbon monoxide concentration. It is supplied to the anode 7 of the fuel cell 6.

【0004】リン酸型燃料電池6は、上記の供給された
改質ガスとカソード8に供給される空気とにより電池反
応を起こして発電する。
The phosphoric acid fuel cell 6 generates a power by causing a cell reaction by the supplied reformed gas and the air supplied to the cathode 8.

【0005】[0005]

【発明が解決しようとする課題】上記の燃料電池発電装
置において、改質器3にて水蒸気改質したガスに含まれ
る一酸化炭素はエネルギーレベルが高い。しかしなが
ら、一酸化炭素は燃料電池の電極触媒に被毒を与えると
ともに、大気中に放出すると人体に有害なため、一酸化
炭素変成器5により一酸化炭素を二酸化炭素に変成して
いるので、一酸化炭素の高いエネルギーを有効に利用し
てないという問題がある。
In the above fuel cell power generator, carbon monoxide contained in the gas reformed by the steam reformer 3 has a high energy level. However, since carbon monoxide poisons the electrode catalyst of the fuel cell and is harmful to the human body if it is released into the atmosphere, carbon monoxide is converted into carbon dioxide by the carbon monoxide transformer 5. There is a problem that the high energy of carbon oxide is not effectively used.

【0006】本発明の目的は、改質器から送出される水
蒸気改質したガスに含まれるエネルギーの高い一酸化炭
素を有効に利用することのできる燃料電池をリン酸型燃
料電池に併設したハイブリッド燃料電池発電装置を提供
することである。
An object of the present invention is to provide a hybrid fuel cell, which is capable of effectively utilizing carbon monoxide having a high energy contained in the steam reformed gas delivered from the reformer, in a phosphoric acid fuel cell. A fuel cell power generator is provided.

【0007】[0007]

【課題を解決するための手段】上記課題を解決するため
に、本発明によれば原燃料を水素と一酸化炭素とを含む
ガスに水蒸気改質する改質器と、この改質器からの改質
ガスがアノードに供給される固体電解質を有する固体電
解質型燃料電池と、この燃料電池のアノードから排出さ
れる排ガスが供給されるアノードを備え、リン酸電解質
を有するリン酸型燃料電池とを備えてハイブリッド燃料
電池発電装置を構成するものとする。
In order to solve the above problems, according to the present invention, a reformer for steam reforming a raw fuel into a gas containing hydrogen and carbon monoxide, and a reformer from this reformer A phosphoric acid fuel cell having a phosphoric acid electrolyte, comprising a solid oxide fuel cell having a solid electrolyte in which reformed gas is supplied to the anode, and an anode supplied with exhaust gas discharged from the anode of the fuel cell. The hybrid fuel cell power generator is provided.

【0008】また、上記のハイブリッド燃料電池発電装
置において、リン酸型燃料電池の前段に、固体電解質型
燃料電池のアノードから排出される排ガスに含まれる一
酸化炭素を変成する一酸化炭素変成器を設けるものとす
る。
Further, in the above hybrid fuel cell power generation device, a carbon monoxide transformer for transforming carbon monoxide contained in the exhaust gas discharged from the anode of the solid oxide fuel cell is provided in the preceding stage of the phosphoric acid fuel cell. Shall be provided.

【0009】[0009]

【作用】原燃料を改質器で水蒸気改質した水素と一酸化
炭素を含むガスは固体電解質型燃料電池のアノードに供
給される。そして固体電解質型燃料電池は前記アノード
に供給されたガスと別にカソードに供給される空気とに
より電池反応を起こして発電する。この際水素及び一酸
化炭素と空気中の酸素とは下記の反応をする。
The gas containing hydrogen and carbon monoxide obtained by steam reforming the raw fuel in the reformer is supplied to the anode of the solid oxide fuel cell. Then, the solid oxide fuel cell causes a cell reaction by the gas supplied to the anode and the air supplied to the cathode separately to generate electricity. At this time, hydrogen and carbon monoxide react with the oxygen in the air as follows.

【0010】 2H2 +O2 →2H2 O ──────────────(1) 2CO+O2 →2CO2 ──────────────(2) ここで、固体電解質型燃料電池のアノードから排出され
る排ガスは電池反応に寄与しない水素と(2)式により
一酸化炭素が変成された二酸化炭素等を含むガスとな
る。そしてこの排ガスはリン酸型燃料電池のアノードに
供給され、別にカソードに供給される空気とにより、リ
ン酸型燃料電池は電池反応を起こして発電する。この際
の水素と空気中の酸素との反応は(1)式による。
2H 2 + O 2 → 2H 2 O ────────────── (1) 2CO + O 2 → 2CO 2 ─────────────── (2) Here, the exhaust gas discharged from the anode of the solid oxide fuel cell becomes a gas containing hydrogen that does not contribute to the cell reaction and carbon dioxide in which carbon monoxide is modified by the formula (2). The exhaust gas is supplied to the anode of the phosphoric acid fuel cell, and the air is separately supplied to the cathode, whereby the phosphoric acid fuel cell causes a cell reaction to generate electricity. The reaction between hydrogen and oxygen in the air at this time is according to the equation (1).

【0011】ところで、改質器からの水素と一酸化炭素
とを含む水蒸気改質したガスを固体電解質型燃料電池に
て(1),(2)式のような反応を行なわせて発電する
が、この際一酸化炭素を二酸化炭素に変成して得られる
電力も取出すことができるので、燃料電池発電装置の電
気変換効率が向上する。なおこの際、(2)式の2CO
+O2 →2CO2 の反応によっても発電する固体電解質
型燃料電池の一酸化炭素の利用率を上げれば、リン酸型
燃料電池の電極触媒に被毒を与える一酸化炭素の濃度を
低くすることができるので、一酸化炭素変成器を設置す
る必要がなくなる。
By the way, the steam-reformed gas containing hydrogen and carbon monoxide from the reformer is subjected to the reactions as in formulas (1) and (2) in the solid oxide fuel cell to generate electricity. At this time, since the electric power obtained by converting carbon monoxide into carbon dioxide can also be taken out, the electric conversion efficiency of the fuel cell power generator is improved. At this time, 2CO of the formula (2)
Increasing the utilization rate of carbon monoxide that generates electricity also by the reaction of + O 2 → 2CO 2 can reduce the concentration of carbon monoxide that poisons the electrode catalyst of the phosphoric acid fuel cell. This eliminates the need to install a carbon monoxide transformer.

【0012】なお、固体電解質型燃料電池において一酸
化炭素の利用率が低い場合でも、従来に比べて含有する
一酸化炭素量が少ないため、一酸化炭素変成器を設置し
ても小型化することができる。
Even when the utilization rate of carbon monoxide in the solid oxide fuel cell is low, the amount of carbon monoxide contained in the solid oxide fuel cell is smaller than in the conventional case. Therefore, the carbon monoxide transformer should be downsized. You can

【0013】[0013]

【実施例】以下図面に基づいて本発明の実施例について
説明する。図1は本発明の実施例によるリン酸型燃料電
池と固体電解質型燃料電池とを併設したハイブリッド燃
料電池発電装置の系統図である。なお、図1において図
3の従来例と同一部品には同じ符号を付し、その説明を
省略する。図1において従来例と異なるのは下記の通り
である。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a system diagram of a hybrid fuel cell power generator having a phosphoric acid fuel cell and a solid oxide fuel cell according to an embodiment of the present invention. In FIG. 1, the same parts as those in the conventional example of FIG. 3 are designated by the same reference numerals, and the description thereof will be omitted. 1 is different from the conventional example as follows.

【0014】図3の一酸化炭素変成器5を取除き、改質
器3の後段に固体電解質型燃料電池11を設置する。固
体電解質型燃料電池11は図示しない固体電解質と、こ
れを挟持するアノード12及びカソード13とを備えて
構成される。また、固体電解質型燃料電池11とリン酸
型燃料電池6との間に固体電解質型燃料電池11のアノ
ード12から排出される排ガスを冷却する冷却器15を
設置する。
The carbon monoxide shift converter 5 shown in FIG. 3 is removed, and the solid oxide fuel cell 11 is installed at the subsequent stage of the reformer 3. The solid oxide fuel cell 11 includes a solid electrolyte (not shown), and an anode 12 and a cathode 13 that sandwich the solid electrolyte. Further, a cooler 15 for cooling the exhaust gas discharged from the anode 12 of the solid oxide fuel cell 11 is installed between the solid oxide fuel cell 11 and the phosphoric acid fuel cell 6.

【0015】このような構成により、改質器3から水蒸
気改質された水素と一酸化炭素とを含むガスは固体電解
質型燃料電池11のアノード12に供給され、別にカソ
ード13に供給される空気とにより電池反応を起こして
発電する。この際発電時生じる熱は前記供給される空気
により除熱され、高温の運転温度に保持される。固体電
解質型燃料電池11の発電時アノード12から排出され
る排ガスは電池反応に寄与しない水素と、二酸化炭素等
を含むガスになっている。この際、一酸化炭素の利用率
を高くすることにより一酸化炭素濃度を低くすることが
できるので、従来の一酸化炭素を変成する一酸化炭素変
成器は不要となる。
With such a configuration, the steam-reformed gas containing hydrogen and carbon monoxide from the reformer 3 is supplied to the anode 12 of the solid oxide fuel cell 11 and separately supplied to the cathode 13. Generates power by causing a battery reaction. At this time, the heat generated during power generation is removed by the supplied air, and is maintained at a high operating temperature. The exhaust gas discharged from the anode 12 during power generation of the solid oxide fuel cell 11 is a gas containing hydrogen, carbon dioxide, and the like that do not contribute to the cell reaction. At this time, since the concentration of carbon monoxide can be lowered by increasing the utilization rate of carbon monoxide, the conventional carbon monoxide transformer for converting carbon monoxide is unnecessary.

【0016】この排ガスは、運転温度に近い高温なの
で、冷却器15にてリン酸型燃料電池6の運転温度にま
で冷却されてリン酸型燃料電池6のアノード7に供給さ
れ、別にカソード8に供給される空気とにより電池反応
を起こして発電する。なお、発電時生じる熱は冷却板9
の冷却通路を通流する冷却媒体により除熱されて運転温
度が保持される。
Since this exhaust gas is at a high temperature close to the operating temperature, it is cooled to the operating temperature of the phosphoric acid fuel cell 6 by the cooler 15 and supplied to the anode 7 of the phosphoric acid fuel cell 6 and separately to the cathode 8. The supplied air causes a battery reaction to generate power. The heat generated during power generation is the cooling plate 9
The operating temperature is maintained by removing the heat from the cooling medium flowing through the cooling passage.

【0017】図2は、本発明の異なる実施例によるリン
酸型燃料電池と固体電解質型燃料電池とを併設したハイ
ブリッド燃料電池発電装置の系統図である。図2におい
て冷却器15とリン酸型燃料電池6との間に一酸化炭素
変成器18を設置した他は図1と同じである。このよう
な構成により、固体電解質型燃料電池11にて電池反応
時、一酸化炭素の利用率が低い場合、二酸化炭素に変成
しない一酸化炭素の利用率に応じた濃度を有するガスが
アノード12から排出されるので、この排ガスを冷却器
15にて冷却した後一酸化炭素変成器18により、一酸
化炭素を二酸化炭素に変成して一酸化炭素濃度が低く、
水素を含むガスをリン酸型燃料電池6のアノード7に供
給することにより、前述のように発電することができ
る。
FIG. 2 is a system diagram of a hybrid fuel cell power generator having a phosphoric acid fuel cell and a solid oxide fuel cell according to another embodiment of the present invention. 2 is the same as FIG. 1 except that a carbon monoxide shifter 18 is installed between the cooler 15 and the phosphoric acid fuel cell 6. With such a configuration, during the cell reaction in the solid oxide fuel cell 11, when the utilization rate of carbon monoxide is low, a gas having a concentration according to the utilization rate of carbon monoxide that does not convert to carbon dioxide is emitted from the anode 12. Since the exhaust gas is discharged, after the exhaust gas is cooled by the cooler 15, the carbon monoxide shifter 18 shifts the carbon monoxide into carbon dioxide to reduce the carbon monoxide concentration,
By supplying a gas containing hydrogen to the anode 7 of the phosphoric acid fuel cell 6, it is possible to generate power as described above.

【0018】なお、上記の場合、固体電解質型燃料電池
11のアノード12から排出されるガスに含まれる一酸
化炭素濃度は従来に比べて低いので、一酸化炭素変成器
18は小型化することができる。本実施例では炭化水素
系の原燃料を水蒸気改質した改質ガスについて説明した
が、メタノール等のアルコール系の原燃料を改質器で水
蒸気改質した水素と一酸化炭素とを含むガスを使用して
も同じ効果が得られる。
In the above case, the concentration of carbon monoxide contained in the gas discharged from the anode 12 of the solid oxide fuel cell 11 is lower than in the conventional case, so that the carbon monoxide transformer 18 can be miniaturized. it can. In this example, the reformed gas obtained by steam reforming a hydrocarbon-based raw fuel was described. However, a gas containing hydrogen and carbon monoxide obtained by steam reforming an alcohol-based raw fuel such as methanol in a reformer was used. The same effect can be obtained when used.

【0019】[0019]

【発明の効果】以上の説明から明らかなように、本発明
によれば前述の構成により、原燃料を改質器で水蒸気改
質した水素と一酸化炭素とを含むガスを固体電解質型燃
料電池に供給して電池反応を行なわせるとき、一酸化炭
素は二酸化炭素になる反応により発電するので、一酸化
炭素の高いエネルギーを有効に利用でき、電気変換効率
を高めることができる。
As is apparent from the above description, according to the present invention, the solid electrolyte fuel cell according to the above-mentioned structure is provided with the gas containing hydrogen and carbon monoxide obtained by steam reforming the raw fuel in the reformer. When carbon dioxide is supplied to the battery to cause a battery reaction, carbon monoxide generates electricity by the reaction of becoming carbon dioxide, so that the high energy of carbon monoxide can be effectively used and the electric conversion efficiency can be increased.

【0020】また、固体電解質型燃料電池にて一酸化炭
素を二酸化炭素にするので、リン酸型燃料電池には一酸
化炭素濃度の低い燃料ガスが供給され、このため一酸化
炭素変成器が不要になるという効果がある。なお、固体
電解質型燃料電池にて一酸化炭素を二酸化炭素にする一
酸化炭素の利用率が低い場合、一酸化炭素変成器を設け
ても、小型化することができる。
Further, since carbon monoxide is converted to carbon dioxide in the solid oxide fuel cell, the phosphoric acid fuel cell is supplied with the fuel gas having a low carbon monoxide concentration, and thus the carbon monoxide transformer is unnecessary. Has the effect of becoming. When the utilization rate of carbon monoxide that converts carbon monoxide into carbon dioxide is low in a solid oxide fuel cell, the size can be reduced even if a carbon monoxide transformer is provided.

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

【図1】本発明の実施例によるリン酸型燃料電池と固体
電解質型燃料電池とを併設したハイブリッド燃料電池発
電装置の系統図
FIG. 1 is a system diagram of a hybrid fuel cell power generator in which a phosphoric acid fuel cell and a solid oxide fuel cell according to an embodiment of the present invention are provided side by side.

【図2】本発明の異なる実施例によるリン酸型燃料電池
と固体電解質型燃料電池とを併設したハイブリッド燃料
電池発電装置の系統図
FIG. 2 is a system diagram of a hybrid fuel cell power generator including a phosphoric acid fuel cell and a solid oxide fuel cell according to another embodiment of the present invention.

【図3】従来のリン酸型燃料電池発電装置の系統図FIG. 3 is a system diagram of a conventional phosphoric acid fuel cell power generator.

【符号の説明】[Explanation of symbols]

2 脱硫器 3 改質器 6 リン酸型燃料電池 7 アノード 8 カソード 11 固体電解質型燃料電池 12 アノード 13 カソード 18 一酸化炭素変成器 2 Desulfurizer 3 Reformer 6 Phosphoric acid fuel cell 7 Anode 8 Cathode 11 Solid electrolyte fuel cell 12 Anode 13 Cathode 18 Carbon monoxide converter

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】原燃料を水素と一酸化炭素とを含むガスに
水蒸気改質する改質器と、この改質器からの改質ガスが
アノードに供給される固体電解質を有する固体電解質型
燃料電池と、この燃料電池のアノードから排出される排
ガスが供給されるアノードを備え、リン酸電解質を有す
るリン酸型燃料電池とを備えたことを特徴とするハイブ
リッド燃料電池発電装置。
1. A solid electrolyte fuel comprising a reformer for steam reforming a raw fuel into a gas containing hydrogen and carbon monoxide, and a solid electrolyte in which the reformed gas from the reformer is supplied to an anode. A hybrid fuel cell power generator comprising a cell and an anode to which exhaust gas discharged from the anode of the fuel cell is supplied, and a phosphoric acid fuel cell having a phosphoric acid electrolyte.
【請求項2】請求項1記載のものにおいて、リン酸型燃
料電池の前段に、固体電解質型燃料電池のアノードから
排出される排ガスに含まれる一酸化炭素を変成する一酸
化炭素変成器を設けたことを特徴とするハイブリッド燃
料電池発電装置。
2. The carbon monoxide shifter for transforming carbon monoxide contained in exhaust gas discharged from the anode of a solid oxide fuel cell according to claim 1, wherein the phosphoric acid fuel cell is provided in front of the phosphoric acid fuel cell. A hybrid fuel cell power generator characterized in that
JP4237498A 1992-09-07 1992-09-07 Hybrid fuel cell power generation device Pending JPH0689735A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4237498A JPH0689735A (en) 1992-09-07 1992-09-07 Hybrid fuel cell power generation device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4237498A JPH0689735A (en) 1992-09-07 1992-09-07 Hybrid fuel cell power generation device

Publications (1)

Publication Number Publication Date
JPH0689735A true JPH0689735A (en) 1994-03-29

Family

ID=17016212

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4237498A Pending JPH0689735A (en) 1992-09-07 1992-09-07 Hybrid fuel cell power generation device

Country Status (1)

Country Link
JP (1) JPH0689735A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2829296A1 (en) * 2001-09-05 2003-03-07 Renault DEVICE AND METHOD FOR SUPPLYING A FUEL CELL WITH HYDROGEN AND USE FOR ELECTRIC TRACTION OF A VEHICLE
JP2004311168A (en) * 2003-04-04 2004-11-04 Central Res Inst Of Electric Power Ind Power generation method by fuel cell and fuel cell power generation system
KR101117631B1 (en) * 2004-10-04 2012-02-29 삼성에스디아이 주식회사 Fuel cell system

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2829296A1 (en) * 2001-09-05 2003-03-07 Renault DEVICE AND METHOD FOR SUPPLYING A FUEL CELL WITH HYDROGEN AND USE FOR ELECTRIC TRACTION OF A VEHICLE
WO2003021704A2 (en) * 2001-09-05 2003-03-13 Renault S.A.S. Device and method for supplying hydrogen to a fuel cell and the use thereof for electric vehicle traction
WO2003021704A3 (en) * 2001-09-05 2004-02-12 Renault Sa Device and method for supplying hydrogen to a fuel cell and the use thereof for electric vehicle traction
US7311985B2 (en) 2001-09-05 2007-12-25 Renault S.A.S. Device and method for supplying hydrogen to a fuel cell, and the use thereof for electric vehicle traction
JP2004311168A (en) * 2003-04-04 2004-11-04 Central Res Inst Of Electric Power Ind Power generation method by fuel cell and fuel cell power generation system
KR101117631B1 (en) * 2004-10-04 2012-02-29 삼성에스디아이 주식회사 Fuel cell system

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