JPH0711136Y2 - Fuel cell fuel reformer - Google Patents
Fuel cell fuel reformerInfo
- Publication number
- JPH0711136Y2 JPH0711136Y2 JP1989011216U JP1121689U JPH0711136Y2 JP H0711136 Y2 JPH0711136 Y2 JP H0711136Y2 JP 1989011216 U JP1989011216 U JP 1989011216U JP 1121689 U JP1121689 U JP 1121689U JP H0711136 Y2 JPH0711136 Y2 JP H0711136Y2
- Authority
- JP
- Japan
- Prior art keywords
- gas
- burner
- inner cylinder
- fuel
- combustion gas
- 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 - Lifetime
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
- Y02E60/50—Fuel cells
Landscapes
- Hydrogen, Water And Hydrids (AREA)
Description
【考案の詳細な説明】 〔産業上の利用分野〕 この考案は、燃料電池発電システムに組込まれ、メタノ
ールと水蒸気からなる原燃料ガスを水素リッチな改質ガ
スに改質して燃料電池に供給する燃料改質器の構造に関
する。[Detailed Description of the Invention] [Industrial field of application] This invention is incorporated into a fuel cell power generation system, reforms a raw fuel gas composed of methanol and steam into a hydrogen-rich reformed gas, and supplies it to a fuel cell. And a structure of a fuel reformer.
小型の燃料電池発電システムにおいて、燃料電池に供給
する水素リッチな改質ガスを生成する燃料改質器には天
然ガスを原燃料とする改質器に比べて水蒸気改質反応温
度が200℃ないし300℃と低くかつ脱硫器や変成器を必要
とせず、したがってその始動時における予熱時間が短か
く小型ですむメタノールを原燃料とする水蒸気改質器
(以上改質器と略称する)が注目されている。In a small fuel cell power generation system, the fuel reformer that generates hydrogen-rich reformed gas to be supplied to the fuel cell has a steam reforming reaction temperature of 200 ° C or more compared to a reformer that uses natural gas as a raw fuel. Attention is focused on a steam reformer (hereinafter referred to as reformer) that uses methanol as a raw fuel, which has a low temperature of 300 ° C and does not require a desulfurizer or a transformer, and therefore has a short preheating time at the time of starting and is compact. ing.
第2図は改質器の従来構造を示す側断面図であり、図の
場合有底の円筒状の炉体1はこれと同軸状で底板との間
に間隙長Gを有する内筒2と、上蓋1Bから内筒2の中央
部に支持されたバーナ3を備え、入口3Aから流入する燃
料ガス8Aと入口3Bから流入する支燃空気8Bとの混合ガス
がバーナ3で燃焼して下向きの火炎8Fおよび高温の燃焼
(排)ガス8Cとが発生する。燃焼ガス8Cは燃焼筒3Gおよ
び内筒2に案内されて炉底に至り、その一部は炉底中央
に開口した排気管4に流入する燃焼ガス8Sと、内筒2の
外側に形成される逆向き通路5を通ってその上部に開口
した排気管5Bに流入する燃焼ガス8Rとに分流する。燃焼
ガス8Rと8Sの分流比は主に排気管4に設けられた電磁式
ダンパー4Aによって制御され、電磁ダンパー4Aを通過し
た高温の燃焼排ガスSが持つ熱エネルギーは例えば原燃
料および水の気化器4Bの熱源として利用され、所定の水
蒸気比の原燃料ガス9Aを生成する。FIG. 2 is a side sectional view showing a conventional structure of a reformer. In the figure, a bottomed cylindrical furnace body 1 is coaxial with this and an inner cylinder 2 having a gap length G between the bottom and the bottom plate. A burner 3 supported by the central portion of the inner cylinder 2 from the upper lid 1B is provided, and a mixed gas of the fuel gas 8A flowing from the inlet 3A and the combustion-supporting air 8B flowing from the inlet 3B is burned in the burner 3 and is directed downward. Flame 8F and high temperature combustion (exhaust) gas 8C are generated. The combustion gas 8C is guided by the combustion cylinder 3G and the inner cylinder 2 to reach the furnace bottom, and a part of the combustion gas 8C is formed outside the inner cylinder 2 with the combustion gas 8S flowing into the exhaust pipe 4 opened at the center of the furnace bottom. It splits into the combustion gas 8R which flows through the reverse passage 5 and flows into the exhaust pipe 5B opened at the upper part thereof. The split ratio of the combustion gases 8R and 8S is mainly controlled by the electromagnetic damper 4A provided in the exhaust pipe 4, and the thermal energy of the high temperature combustion exhaust gas S passing through the electromagnetic damper 4A is, for example, a vaporizer of raw fuel and water. It is used as a heat source for 4B and produces a raw fuel gas 9A with a predetermined steam ratio.
一方、6は内筒2の内側に同軸状に配され、バーナ3が
発する火炎8Fまたは高温の燃焼ガス8Cによって加熱され
る蛇管であり、例えば気化器4Bで生成した原燃料ガス9A
を入口6Aから受け、所定温度に再加熱した後、内筒外側
の逆向き通路5内に設けられた改質反応管7の下部に供
給する。改質反応管7は内筒2と炉体1との間の燃焼ガ
スの逆向き通路5内に設けられた2重の筒状容器または
上下端にマニホールドを有する複数の並列管からなり、
筒状容器または並列管内には水蒸気改質触媒としての銅
−亜鉛系,銅−クロ−ム系,あるいはこれらに第3成分
を加えた改質触媒7Bが充填され、この改質触媒層7Bを上
向きに通過する原燃料ガス9Aとの間で生ずる吸熱反応で
ある水蒸気改質反応が、改質反応管7をその外側から加
熱する高温の燃焼ガス8Rを熱源として反応に必要な温度
200℃ないし300℃を保持して行われることにより、水素
リッチな改質ガス10が改質管上部に開口した改質ガス供
給系7Cを介して図示しない燃料電池に供給される。On the other hand, 6 is a spiral tube which is coaxially arranged inside the inner cylinder 2 and is heated by the flame 8F emitted by the burner 3 or the high-temperature combustion gas 8C, for example, the raw fuel gas 9A produced by the vaporizer 4B.
From the inlet 6A, reheated to a predetermined temperature, and then supplied to the lower part of the reforming reaction tube 7 provided in the reverse passage 5 outside the inner cylinder. The reforming reaction tube 7 comprises a double tubular container provided in the reverse passage 5 of the combustion gas between the inner cylinder 2 and the furnace body 1 or a plurality of parallel tubes having manifolds at the upper and lower ends,
A cylindrical container or a parallel pipe is filled with a reforming catalyst 7B which is a steam reforming catalyst such as a copper-zinc system, a copper-chrome system, or a third component added to these, and this reforming catalyst layer 7B The steam reforming reaction, which is an endothermic reaction that occurs with the raw fuel gas 9A passing upward, uses the high temperature combustion gas 8R that heats the reforming reaction tube 7 from the outside as a heat source, and the temperature required for the reaction.
By maintaining the temperature at 200 ° C. to 300 ° C., the hydrogen-rich reformed gas 10 is supplied to the fuel cell (not shown) through the reformed gas supply system 7C opened at the upper part of the reforming tube.
従来装置において、改質反応管7および気化器4Bの温度
制御は、主としてバーナ3への燃料ガス8Aおよび支燃空
気8Bとの供給量と、電磁ダンパー4Aによる燃焼ガス8R,8
Sへの配分制御とによって行われるが、冷えた状態にあ
る改質器および燃料電池を始動しようとする場合、バー
ナ3の燃料消費量を一時的に急増させ、気化器4B,蛇管
6,および改質反応管7をそれぞれの作動温度にまで急加
熱して発電待機時間を短縮することが求められる。この
ような状態ではバーナが発する火炎8Fが長く伸びて電磁
ダンパーにまで達することが間々あり、電磁ダンパー4A
の例えばボール弁状の開閉機構部が火炎8Fの熱影響を直
接受けて赤熱状態となり、可動部が拘束状態となってそ
の開口制御が困難になるという問題が生じやすく、これ
が原因で燃焼ガス8R,8Sの分流制御,いいかえれば気化
器4Bと改質反応管7の温度制御ができなくなるという問
題が発生する。In the conventional apparatus, the temperature control of the reforming reaction tube 7 and the vaporizer 4B is performed mainly by supplying the fuel gas 8A and the combustion-supporting air 8B to the burner 3 and the combustion gas 8R, 8 by the electromagnetic damper 4A.
When the cold reformer and the fuel cell are to be started, the fuel consumption of the burner 3 is temporarily increased rapidly, and the carburetor 4B and the flexible pipe are controlled.
It is required to rapidly heat 6, 6 and the reforming reaction tube 7 to their respective operating temperatures to shorten the power generation standby time. In such a state, the flame 8F emitted by the burner may extend for a long time to reach the electromagnetic damper, and the electromagnetic damper 4A
For example, the ball valve-shaped opening / closing mechanism is directly affected by the heat of the flame 8F and becomes a red heat state, which easily causes a problem that the movable part is in a restricted state and its opening control becomes difficult. Then, there arises a problem that it becomes impossible to control the split flow of 8S, that is, the temperature control of the vaporizer 4B and the reforming reaction tube 7.
この考案の目的は、電磁ダンパーに対する火炎の熱影響
を排除することにより、始動時における燃焼ガスの配分
制御を円滑化することにある。An object of the present invention is to smooth the distribution control of the combustion gas at the time of starting by eliminating the thermal influence of the flame on the electromagnetic damper.
上記課題を解決するために、この考案によれば、火炎お
よび高温の燃焼ガスを下向きに発するバーナを上蓋の中
央部に支持する筒状の炉体が同軸状の内筒を持ち、内筒
に案内されて炉底に達した燃焼ガスが炉体の底部を貫通
する排気管、および内筒の外側を通る逆向き通路に分流
して排出されるとともに、所定の水蒸気比の原燃料ガス
をバーナの下方に配した蛇管で加熱し、前記逆向き通路
に配された改質反応管で水蒸気改質された改質ガスとし
て改質反応管上部から燃料電池に向けて送り出すものに
おいて、前記排気管を前記バーナに向けて所定長さ突出
してなる延長管部と、この延長管部を空隙を保持して開
口部側から覆うキャップ部とからなる燃焼ガス通路の延
長手段を前記蛇管の内側に備えるものとする。In order to solve the above problems, according to the present invention, a tubular furnace body that supports a burner that emits flames and high-temperature combustion gas downward in a central portion of an upper lid has a coaxial inner tube, and The combustion gas that is guided and reaches the bottom of the furnace is diverted into the exhaust pipe that penetrates the bottom of the furnace body and the reverse passage that passes through the outside of the inner cylinder, and is discharged, and the raw fuel gas with a predetermined steam ratio is burned. Which is heated by a flexible pipe disposed below the exhaust gas and is sent out from the upper portion of the reforming reaction tube toward the fuel cell as reformed gas which is steam-reformed by the reforming reaction tube disposed in the reverse passage. Is provided inside the flexible tube with an extension means for the combustion gas passage, which comprises an extension pipe portion projecting toward the burner by a predetermined length and a cap portion that holds the extension pipe portion from the opening side while holding a gap. I shall.
炉体底部に開口した排気管の延長管部、および延長管部
を燃焼排ガスの通路となる空隙を保持して開口側から覆
う有底筒状のキャップ部とからなる燃焼排ガス通路の延
長手段を内筒と同軸状に配された蛇管のさらに内側に配
したことにより、バーナの燃料消費量を増すことによっ
て長大化した火炎はまずキャップ部の上面で内筒の内壁
面側に広がり、内筒とキャップの側壁との隙間に配され
た蛇管に熱伝達することによって火炎温度が下がり、キ
ャップ部の下縁で延長管部との隙間に折り返すことによ
って炎が吹き消され、さらに冷却された燃焼排ガスが延
長管部を介して電磁ダンパーが配された排気管に流入す
るので、電磁ダンパーに火炎が直接あたることによって
生ずる電磁ダンパーの動作渋滞が排除され、したがって
改質反応管側および気化器側への燃焼ガスの配分が円滑
化されると同時に、蛇管および改質反応管の下部がより
高温の燃焼ガスによって加熱されて、水蒸気改質が効率
よく行われることにより、燃焼改質器の始動に必要な時
間を短縮することができる。A means for extending a combustion exhaust gas passage, which comprises an extension pipe portion of an exhaust pipe opened at the bottom of the furnace body, and a bottomed cylindrical cap portion that covers the extension pipe portion from the opening side while holding a gap that serves as a passage for combustion exhaust gas, is provided. By arranging it further inside the flexible pipe that is coaxial with the inner cylinder, the flame lengthened by increasing the fuel consumption of the burner first spreads to the inner wall surface side of the inner cylinder on the upper surface of the cap, And the side wall of the cap, heat is transferred to the flexible pipe, which lowers the flame temperature, and the bottom edge of the cap folds back into the gap between the extension pipe to extinguish the flame and further cool combustion. Since the exhaust gas flows into the exhaust pipe where the electromagnetic damper is arranged through the extension pipe section, the operational congestion of the electromagnetic damper caused by the direct impact of the flame on the electromagnetic damper is eliminated. The distribution of combustion gas to the carburetor side is smoothed, and at the same time, the lower parts of the flexible pipe and the reforming reaction pipe are heated by the higher temperature combustion gas, and steam reforming is performed efficiently, which results in combustion reforming. The time required to start the vessel can be shortened.
以下この考案を実施例に基づいて説明する。 The present invention will be described below based on embodiments.
第1図はこの考案の実施例装置を示す側断面図であり、
従来装置と同じ機能部分には同一参照符号を用いること
により詳細な説明を省略する。図において、20は燃焼ガ
ス通路の延長手段であり、炉体1の底部中央部に開口し
た排気管4をバーナ3に向けて所定長さ突出させた延長
管部21と、この延長管部21をその開口側から覆う下向き
に開口した有底筒状のキャップ部22とで構成され、延長
管部21とキャップ部22との間には燃焼ガスの通路となる
空隙23が保持されるとともに、キャップ部22の外周を包
囲するよう蛇管6が配され、さらに蛇管6を包囲する内
筒2との間にも燃焼ガス通路となる空隙24が保持され
る。また、バーナ3の燃焼筒3Gの下縁とキャップ部22の
上面との間にも燃焼ガスの通路となる間隔が保持され
る。また、延長管部21の長さはその上縁とキャップ部と
の間に燃焼ガス通路となる間隔を保持できる寸法に決め
られる。FIG. 1 is a side sectional view showing an apparatus according to an embodiment of the present invention,
The same functional parts as those of the conventional device are designated by the same reference numerals and detailed description thereof will be omitted. In the figure, reference numeral 20 is an extension means of a combustion gas passage, and an extension pipe portion 21 in which an exhaust pipe 4 opened at a central portion of a bottom portion of a furnace body 1 is protruded toward a burner 3 by a predetermined length, and the extension pipe portion 21. It is configured with a bottomed cylindrical cap portion 22 that opens downwardly covering the opening side, and a gap 23 that serves as a passage for combustion gas is held between the extension pipe portion 21 and the cap portion 22, The flexible pipe 6 is arranged so as to surround the outer periphery of the cap portion 22, and a gap 24 serving as a combustion gas passage is also held between the flexible pipe 6 and the inner cylinder 2 surrounding the flexible pipe 6. Further, a space serving as a passage for the combustion gas is maintained between the lower edge of the combustion cylinder 3G of the burner 3 and the upper surface of the cap portion 22. In addition, the length of the extension pipe portion 21 is determined to be a dimension that can maintain a space serving as a combustion gas passage between the upper edge of the extension pipe portion 21 and the cap portion.
上述のような実施例装置の始動時において、バーナの燃
料消費量を一時的に増加させることによって発生する火
炎8Fの長さが増加した場合、火炎8Fはキャップ部22の上
面で内筒2側に広げられ、空隙24を通る過程で蛇管6内
を通る所定の水蒸気比の原燃料ガス9Aに熱エネルギーを
供給することによって冷却され、キャップ部22の下縁で
空隙23側に折返えす時点では火炎は吹き消されて高温の
燃焼ガス28Sとなり、延長管部21を介して排気管4に流
入するので、排気管4に配された電磁ダンパー4Aを通過
する時点では燃焼ガス28Sの温度は適度に下がり、電磁
ダンパーが赤熱されることによって生ずる拘束などの悪
影響が排除される。したがって、電磁ダンパー4Aはその
マグネットコイルに加えられる制御電流に対応してその
開口が円滑に制御されるので、気化器4B側への燃焼ガス
28Sと逆向き通路5側への燃焼ガス28Rとの分岐量を要望
の割合に制御することができる。When the length of the flame 8F generated by temporarily increasing the fuel consumption of the burner is increased at the time of starting the apparatus of the embodiment as described above, the flame 8F is on the upper surface of the cap portion 22 on the inner cylinder 2 side. And is cooled by supplying heat energy to the raw fuel gas 9A having a predetermined water vapor ratio passing through the flexible tube 6 in the process of passing through the void 24, and is turned back to the void 23 side at the lower edge of the cap portion 22. Since the flame is blown out to become high-temperature combustion gas 28S and flows into the exhaust pipe 4 via the extension pipe portion 21, the temperature of the combustion gas 28S is appropriate when passing through the electromagnetic damper 4A arranged in the exhaust pipe 4. The negative effects such as restraint caused by the electromagnetic damper being red-heated are eliminated. Therefore, the opening of the electromagnetic damper 4A is smoothly controlled according to the control current applied to the magnet coil, so that the combustion gas to the carburetor 4B side
The branch amount of 28S and the combustion gas 28R to the reverse passage 5 side can be controlled at a desired ratio.
また、原燃料ガス9Aを再加熱する蛇管6および再加熱さ
れた原燃料ガス9Aが流入する改質反応管7の下側部分
は、火炎を含む高温の燃焼ガス8Cまたは22Rにより加熱
され、改質触媒層7Bにおける水蒸気改質反応に必要な熱
エネルギーを効率よく供給できるので、始動時における
改質器の予熱時間が短縮され、改質ガス10を図示しない
燃料電池に早期に供給することができる。Further, the flexible pipe 6 for reheating the raw fuel gas 9A and the lower portion of the reforming reaction pipe 7 into which the reheated raw fuel gas 9A flows are heated by the high-temperature combustion gas 8C or 22R containing flame, Since the heat energy required for the steam reforming reaction in the high quality catalyst layer 7B can be efficiently supplied, the preheating time of the reformer at the time of starting is shortened, and the reformed gas 10 can be supplied to the fuel cell (not shown) early. it can.
この考案は前述のように、炉体底部に開口した電磁ダン
パーを有する排気管をバーナに向けて延長した延長管部
と、これを空隙を保持して開口部側から覆うキャップ部
とからなる燃焼ガス通路の延長手段を原燃料ガス再加熱
用の蛇管の内側に設けるよう構成した。その結果、始動
時に長く延びたバーナの火炎はキャップ部の上面で蛇管
が配された空隙に案内されて原燃料ガスに熱エネルギー
を供給し、キャップ部の下縁で延長管部との間の空隙に
折り返す時点で消炎されて排気管に流入するので、従来
装置において火炎が電磁ダンパーを赤熱することによっ
てダンパーに拘束が生ずるという問題点が排除され、し
たがって燃焼ガスを改質反応管が配された逆向き通路と
ダンパーの下流に配された気化器とに分流させるダンパ
ーの機能が円滑化されるとともに、蛇管および改質反応
管の下部が火災を含む高温の燃焼ガスによって効率よく
加熱されるので、始動時における予熱時間が短縮された
始動特性を有する燃料電池の燃料改質器を提供すること
ができる。As described above, this invention is composed of an extension pipe portion, which extends an exhaust pipe having an electromagnetic damper opened at the bottom of the furnace body toward the burner, and a cap portion which holds a gap and covers it from the opening side. The gas passage extension means is provided inside the flexible pipe for reheating the raw fuel gas. As a result, the flame of the burner that has been elongated for a long time at the time of starting is guided to the gap where the flexible pipe is arranged on the upper surface of the cap portion to supply heat energy to the raw fuel gas, and between the extension pipe portion at the lower edge of the cap portion. Since the flame is extinguished and flows into the exhaust pipe at the time of turning back to the gap, the problem that the flame restrains the damper due to the red heat of the electromagnetic damper in the conventional device is eliminated. The function of the damper that divides the flow into the reverse passage and the carburetor arranged downstream of the damper is smoothed, and the lower part of the flexible pipe and the reforming reaction pipe is efficiently heated by the high-temperature combustion gas including fire. Therefore, it is possible to provide the fuel reformer of the fuel cell having the starting characteristic in which the preheating time at the time of starting is shortened.
第1図はこの考案の実施例装置を示す側断面図、第2図
は従来装置を示す側断面図である。 1……炉体、2……内筒、3……バーナ、4……排出
管、4A……電磁ダンパー、4B……気化器、5……逆向き
通路、6……蛇管、7……改質反応管、7B……改質触媒
層、8,28……燃焼ガス、8F……火炎、9A……原燃料ガ
ス、10……改質ガス、20……燃焼ガス通路の延長手段、
21……延長管部、22……キャップ部、23,24……空隙。FIG. 1 is a side sectional view showing an apparatus according to an embodiment of the present invention, and FIG. 2 is a side sectional view showing a conventional apparatus. 1 ... Furnace body, 2 ... Inner cylinder, 3 ... Burner, 4 ... Discharge pipe, 4A ... Electromagnetic damper, 4B ... Vaporizer, 5 ... Reverse passage, 6 ... Snake pipe, 7 ... Reforming reaction tube, 7B ... Reforming catalyst layer, 8,28 ... Combustion gas, 8F ... Flame, 9A ... Raw fuel gas, 10 ... Reforming gas, 20 ... Combustion gas passage extension means,
21 …… extension pipe part, 22 …… cap part, 23,24 …… void.
Claims (1)
るバーナを上蓋の中央部に支持する筒状の炉体が同軸状
の内筒を持ち、内筒に案内されて炉底に達した燃焼ガス
が炉体の底部を貫通する排気管、および内筒の外側を通
る逆向き通路に分流して排出されるとともに、所定の水
蒸気比の原燃料ガスをバーナの下方に配した蛇管で加熱
し、前記逆向き通路に配された改質反応管で水蒸気改質
された改質ガスとして改質反応管上部から燃料電池に向
けて送り出すものにおいて、前記排気管を前記バーナに
向けて所定長さ突出してなる延長管部と、この延長管部
を空隙を保持して開口部側から覆うキャップ部とからな
る燃焼ガス通路の延長手段を前記蛇管の内側に備えたこ
とを特徴とする燃料電池の燃料改質器。Claim: What is claimed is: 1. A cylindrical furnace body that supports a burner that emits flames and high-temperature combustion gas downward at the center of the upper lid has a coaxial inner cylinder, and the combustion reaches the furnace bottom by being guided by the inner cylinder. The gas is diverted and discharged into an exhaust pipe that penetrates the bottom of the furnace body and a reverse passage that passes outside the inner cylinder, and the raw fuel gas with a prescribed steam ratio is heated by a serpentine pipe arranged below the burner. In the case where the reformed reaction tube arranged in the reverse passage sends the reformed gas steam-reformed from the upper portion of the reforming reaction tube toward the fuel cell, the exhaust pipe is directed toward the burner by a predetermined length. A fuel cell is provided with an extending means for a combustion gas passage, which is formed by a protruding extension pipe portion and a cap portion which holds the extension pipe portion with a gap and covers the opening from the opening side. Fuel reformer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1989011216U JPH0711136Y2 (en) | 1989-02-01 | 1989-02-01 | Fuel cell fuel reformer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1989011216U JPH0711136Y2 (en) | 1989-02-01 | 1989-02-01 | Fuel cell fuel reformer |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02102428U JPH02102428U (en) | 1990-08-15 |
| JPH0711136Y2 true JPH0711136Y2 (en) | 1995-03-15 |
Family
ID=31219575
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1989011216U Expired - Lifetime JPH0711136Y2 (en) | 1989-02-01 | 1989-02-01 | Fuel cell fuel reformer |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0711136Y2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2013188889A1 (en) * | 2012-06-15 | 2013-12-19 | Clearsign Combustion Corporation | Electrically stabilized down-fired flame reactor |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2008159373A (en) * | 2006-12-22 | 2008-07-10 | Matsushita Electric Works Ltd | Hydrogen production apparatus and fuel cell power generation system |
-
1989
- 1989-02-01 JP JP1989011216U patent/JPH0711136Y2/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2013188889A1 (en) * | 2012-06-15 | 2013-12-19 | Clearsign Combustion Corporation | Electrically stabilized down-fired flame reactor |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH02102428U (en) | 1990-08-15 |
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