JPS6344931A - Fuel reforming apparatus - Google Patents
Fuel reforming apparatusInfo
- Publication number
- JPS6344931A JPS6344931A JP61189851A JP18985186A JPS6344931A JP S6344931 A JPS6344931 A JP S6344931A JP 61189851 A JP61189851 A JP 61189851A JP 18985186 A JP18985186 A JP 18985186A JP S6344931 A JPS6344931 A JP S6344931A
- Authority
- JP
- Japan
- Prior art keywords
- fuel
- gas
- vaporizer
- holes
- combustion
- 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
Links
- 239000000446 fuel Substances 0.000 title claims abstract description 73
- 238000002407 reforming Methods 0.000 title abstract description 13
- 239000007789 gas Substances 0.000 claims abstract description 27
- 239000006200 vaporizer Substances 0.000 claims abstract description 22
- 239000007788 liquid Substances 0.000 claims abstract description 19
- 239000000567 combustion gas Substances 0.000 claims abstract description 14
- 238000002485 combustion reaction Methods 0.000 claims abstract description 14
- 239000001257 hydrogen Substances 0.000 claims abstract description 9
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 9
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 8
- 239000003054 catalyst Substances 0.000 claims abstract description 6
- 230000003197 catalytic effect Effects 0.000 claims description 24
- 239000002994 raw material Substances 0.000 abstract description 12
- 238000007084 catalytic combustion reaction Methods 0.000 abstract 3
- 239000008246 gaseous mixture Substances 0.000 abstract 2
- 239000002737 fuel gas Substances 0.000 description 6
- 238000009834 vaporization Methods 0.000 description 5
- 230000008016 vaporization Effects 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 238000010248 power generation Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 2
- 239000002828 fuel tank Substances 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 239000012495 reaction gas Substances 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
- H01M8/0606—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
- H01M8/0612—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material
- H01M8/0625—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material in a modular combined reactor/fuel cell structure
- H01M8/0631—Reactor construction specially adapted for combination reactor/fuel cell
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
- H01M8/0606—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
- H01M8/0612—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material
-
- 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
Abstract
Description
【発明の詳細な説明】
〔発明の属する技術分野〕
本発明は、燃料電池発電システムに組み込まれて改質原
料の液体燃料を水素に富む改質ガスにする燃料改質装置
に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of the Invention] The present invention relates to a fuel reformer that is incorporated into a fuel cell power generation system and converts liquid fuel as a reforming raw material into hydrogen-rich reformed gas.
燃料電池に供給する燃料は水素であるが、この燃料とし
て燃料改質装置により改質原料の液体燃料を水素に冨む
カスに改質して得られる改質ガスが使用される。このた
めに燃料改質装置と燃料電池とを組み合わせてなる燃料
電池発電システムが知られている。The fuel supplied to the fuel cell is hydrogen, and the fuel used is a reformed gas obtained by reforming liquid fuel, which is a raw material for reforming, into hydrogen-rich residue using a fuel reformer. For this purpose, a fuel cell power generation system that combines a fuel reformer and a fuel cell is known.
第２図は従来のこの種の燃料電池発電システムの系統図
である。図においてｌは燃料室な、２は改質原料である
アルコール等の液体燃料を収容した燃料タンクであり、
この燃料タンク２と燃料電池１との間の燃料供給系路内
に燃料改質装置ｆ３が介装設置されている。かかる燃料
改質装置３はバーナ４を装備した炉容器５の燃焼室内に
液体燃料をガス化する気化器６と、燃料ガスを触媒との
接触反応により水素に富むガスに改質する改質器７とを
内蔵しており、燃料電池１から排出されるオフガスをバ
ーナ４に供給して炉内で燃焼し、この除虫じる火焔や燃
焼ガスからなる熱媒体の熱により気化器６にて液体燃料
を気化して原料ガスとし、この原料ガスを改質器７にて
ガス改質を行なう。FIG. 2 is a system diagram of a conventional fuel cell power generation system of this type. In the figure, l is a fuel chamber, 2 is a fuel tank containing liquid fuel such as alcohol, which is a raw material for reforming,
A fuel reformer f3 is interposed in the fuel supply line between the fuel tank 2 and the fuel cell 1. Such a fuel reformer 3 includes a vaporizer 6 for gasifying liquid fuel in a combustion chamber of a furnace vessel 5 equipped with a burner 4, and a reformer for reforming the fuel gas into hydrogen-rich gas through a catalytic reaction with a catalyst. 7, the off-gas discharged from the fuel cell 1 is supplied to the burner 4 and burned in the furnace, and the heat of the heat medium consisting of the insect-repelling flame and combustion gas is used in the vaporizer 6. The liquid fuel is vaporized to form a raw material gas, and this raw material gas is reformed in a reformer 7.
なお８は液体燃料の供給ポンプ、９は燃料電池１へ酸化
剤反応ガスとしての空気を供給するブロアである。Note that 8 is a liquid fuel supply pump, and 9 is a blower that supplies air as an oxidant reaction gas to the fuel cell 1.
ところで燃料電池ｌの運転に際しては、燃料電池本体へ
供給する反応ガスとしての空気および燃料ガスの供給圧
力を一定に保持してバランスを図ることが電池本体の寿
命低下防止の点からも極めて重要なことである。このた
めには燃料ガス供給系の燃料改質装置を通じて燃料電池
本体へ供給する燃料ガスの供給圧力を常に一定に保持す
る必要がある。By the way, when operating a fuel cell, it is extremely important to keep the supply pressures of air as a reaction gas and fuel gas supplied to the fuel cell main body constant and balanced in order to prevent shortening of the life of the cell main body. That's true. For this purpose, it is necessary to always keep the supply pressure of the fuel gas supplied to the fuel cell main body through the fuel reformer of the fuel gas supply system constant.
一般に液体燃料をガス化させる際には大きな気化潜熱を
必要とし、かつ燃料はガス化に伴って大きな体積変化が
生じる。これに対し炉容器５の燃焼室内に気化器６を単
純に配管して燃焼ガスの熱で気化器６を加熱するように
した従来の改質装置の構成のままでは気化器部分の熱容
量が比較的小さい。このために液体燃料のガス化に要す
る大きな気化滴熱を炉側から気化器の全域に亘って絶え
ず安定補給することが困難であり、気化器内においては
液体燃料がガス化した部分で気化潜熱を奪われるために
局部的に温度が低下する等、燃料液体の気化する箇所お
よびその領域が気化器内で絶えず変動し、このことが原
因となって気化器の出口から送出される燃料ガスに圧力
変動を生じる。Generally, when a liquid fuel is gasified, a large latent heat of vaporization is required, and the fuel undergoes a large volume change as it is gasified. On the other hand, if the configuration of the conventional reformer is maintained, in which the vaporizer 6 is simply piped into the combustion chamber of the furnace vessel 5 and the vaporizer 6 is heated by the heat of the combustion gas, the heat capacity of the vaporizer portion is comparatively low. The target is small. For this reason, it is difficult to constantly and stably replenish the large droplet heat of vaporization required for gasifying liquid fuel from the furnace side to the entire area of the vaporizer. The locations and regions where the fuel liquid is vaporized constantly fluctuate within the vaporizer, such as a local temperature drop due to deprivation of fuel, which causes the fuel gas delivered from the vaporizer outlet to change. Causes pressure fluctuations.
このために従来の燃料電池システムでは、燃料カス供給
系内で第２図の図示のように改質装置３の出口側に絞り
１０を設置して燃料電池１へ供給する燃料ガスの圧力変
動を小さくするような方法が採用されている。しかしな
がらこのように系内に絞り１０を介挿する方式では改質
装置３内の圧力を大きく上昇させることになり、耐圧性
の点で好ましくない。また別な解決策として改質装置３
と燃料電池１との間に図示しない改質ガス専用のバッフ
ァタンクを設置して燃料電池１への供給ガス圧の変動を
低く抑えるようにした方式も試みられているが、このよ
うに専用のバッファタンクを設置することはシステム全
体が大形化する難点がある。To this end, in the conventional fuel cell system, a throttle 10 is installed in the fuel scum supply system on the outlet side of the reformer 3 as shown in FIG. 2 to reduce pressure fluctuations in the fuel gas supplied to the fuel cell 1. A method has been adopted to reduce the size. However, this method of inserting the throttle 10 into the system significantly increases the pressure inside the reformer 3, which is not preferable in terms of pressure resistance. Another solution is the reformer 3.
A method has also been attempted in which a buffer tank (not shown) exclusively for reformed gas is installed between the fuel cell 1 and the fuel cell 1 to suppress fluctuations in the gas pressure supplied to the fuel cell 1; Installing a buffer tank has the disadvantage of increasing the size of the entire system.
また、上記のような燃料改質装置の燃焼器として火焔バ
ーナあるいは触媒式バーナが用いられるが、いずれの場
合もバーナは気化器と別置されているので、バーナから
の火焔や燃焼ガスの乱れ等により気化器に熱を安定して
与えないので、前述の液体の気化潜熱に起因する圧力変
動が生じやすいという欠点もある。In addition, a flame burner or a catalytic burner is used as the combustor in the fuel reformer as described above, but in either case, the burner is installed separately from the carburetor, so there is no possibility of turbulence in the flame or combustion gas from the burner. Since heat cannot be stably applied to the vaporizer due to the above-mentioned factors, there is also the drawback that pressure fluctuations are likely to occur due to the latent heat of vaporization of the liquid.
本発明は、前述のような点に鑑み改質原料の液体燃料を
気化器にて燃料電池から排出されるオフガスの燃焼によ
り安定した気化を行なわせ、燃料電池に供給する改質ガ
スの圧力変動を少なくすることのできる燃料改質装置を
提供することを目的とする。In view of the above-mentioned points, the present invention stably vaporizes liquid fuel as a reforming raw material in a vaporizer by burning off gas discharged from a fuel cell, and reduces pressure fluctuations in the reformed gas supplied to the fuel cell. It is an object of the present invention to provide a fuel reformer that can reduce the amount of fuel.
上記の目的は本発明によれば、燃焼器からの熱媒体によ
り改質液体燃料を気化して水素に富むガスに改質する燃
料改質装置において、ケース状の炉体の内側壁に沿わせ
て燃焼ガス流路の孔を有する触媒燃焼器を設け、該触媒
燃焼器に外部に連通ずる気化器を埋設し、前記触媒燃焼
器の人口領域に燃料供給管と燃焼空気供給管を開口させ
、出口領域に燃焼ガス排気管を開口させることにより達
成される。According to the present invention, the above object is achieved by a fuel reformer that vaporizes reformed liquid fuel using a heat medium from a combustor to reform it into hydrogen-rich gas. a catalytic combustor having a hole for a combustion gas flow path, a vaporizer communicating with the outside is buried in the catalytic combustor, and a fuel supply pipe and a combustion air supply pipe are opened in an artificial region of the catalytic combustor, This is achieved by opening a combustion gas exhaust pipe in the outlet area.
以下図面に基づいて本発明の実施例について説明する。 Embodiments of the present invention will be described below based on the drawings.
第１図は本発明の実施例による燃料改質装置の触媒燃焼
器と気化器の断面図である。図において触媒燃焼器２６
はケース状の炉体Ｉの内側壁に沿って配され、内壁方向
に白金等の触媒を表面に担持した多数の孔ｒが設けられ
、さらに管からなる気化器内を埋設し得る孔四が同じ方
向に複数設けられている。なおこのような孔γ、訃を有
する触媒燃焼器２６はアルミナ等の成型体から作られて
いる。FIG. 1 is a sectional view of a catalytic combustor and a carburetor of a fuel reformer according to an embodiment of the present invention. In the figure, the catalytic combustor 26
is arranged along the inner wall of the case-shaped furnace body I, and is provided with a large number of holes r whose surfaces support catalysts such as platinum in the direction of the inner wall, and further has holes 4 in which the inside of the vaporizer made of tubes can be buried. Multiple locations are provided in the same direction. Note that the catalytic combustor 26 having such holes γ and ends is made of a molded body of alumina or the like.
気化器２９の管は触媒燃焼器２６の孔路に挿入されて蛇
行しており、気化器内の人口管２Ｌ］と出口管２９ｂと
はケース加を貫通して外部に連通している。The tube of the vaporizer 29 is inserted into the hole of the catalytic combustor 26 and meandering, and the artificial tube 2L in the vaporizer and the outlet tube 29b pass through the case and communicate with the outside.
なお図では気化器２９は縦方向に蛇行しているが横方向
に蛇行させたり、ら旋状にして埋設してもよＧ）。触媒
燃焼器２６の入口領域にそれぞれ開口してケース加を貫
通する燃料供給管３１と炉体（ト）に接続する燃焼空気
供給管３２が設けられている。また、触媒燃焼器あの出
口領域に開口して触媒燃焼器かによる燃焼ガスを排出す
る燃焼ガス排気管おが設けられ、この管から排出される
燃焼ガスは気化器四の出口管２９Ｉ）に接続される改質
触媒を充填した図示しない改質器を加熱するようにして
いる。In the figure, the carburetor 29 is shown meandering in the vertical direction, but it may also be buried in a meandering manner in the horizontal direction or in a spiral shape. A fuel supply pipe 31 and a combustion air supply pipe 32 are provided which open in the inlet region of the catalytic combustor 26 and pass through the case, and a combustion air supply pipe 32 which connects to the furnace body. In addition, a combustion gas exhaust pipe is provided which opens at the outlet area of the catalytic combustor and discharges the combustion gas from the catalytic combustor, and the combustion gas discharged from this pipe is connected to the outlet pipe 29I of the carburetor 4. A reformer (not shown) filled with a reforming catalyst is heated.
このような構成により、燃料電池から排出される高温の
オフガス（未反応水素を含む改質ガス）が燃料供給管３
１を通り、また燃焼空気が燃焼空気供給管３２を通って
触媒燃焼器２６に流入すると、これらの混合気は触媒燃
焼器２６の多数の孔ｎを通る。With this configuration, high-temperature off-gas (reformed gas containing unreacted hydrogen) discharged from the fuel cell is transferred to the fuel supply pipe 3.
1 and the combustion air enters the catalytic combustor 26 through the combustion air supply pipe 32, these mixtures pass through a number of holes n of the catalytic combustor 26.
この開孔ｎの内壁面に担持された触媒のもとて内壁面で
酸化、すなわち燃焼して発熱する。この熱は触媒燃焼器
あの成型体を伝導して成型体に埋設された気化器２９に
伝熱する。この結果気化６２９に供給されて逆流する改
質原料の液体燃料は気化されて原料ガスとなる。なお燃
焼ガスは触媒燃焼器がの多数の孔υを通って燃慎、ガス
排気管品を経て前述の改質器を加熱する。したがって気
化器酋で生じた原料ガスは改質器で水素に富むガスに改
質されて改質ガスとなり燃料電池に供給される。The catalyst supported on the inner wall surface of the opening n oxidizes, that is, burns, and generates heat on the inner wall surface. This heat is conducted through the molded body of the catalytic combustor and transferred to the vaporizer 29 embedded in the molded body. As a result, the reforming raw material liquid fuel supplied to the vaporizer 629 and flowing backward is vaporized and becomes raw material gas. The combustion gas passes through the numerous holes υ of the catalytic combustor, passes through the combustion chamber, the gas exhaust pipe, and heats the aforementioned reformer. Therefore, the raw material gas produced in the vaporizer is reformed into a hydrogen-rich gas in the reformer, and the reformed gas is supplied to the fuel cell.
葛
ところで触媒燃焼器２６に埋設された気化Ｗ ２９ ＠
ン加熱する方法は上述のように触媒燃焼器部での燃焼に
よる熱を成型体の伝導伝熱により行なうので気化器２９
を通流する液体燃料は局部的な加熱をうけることなく、
かつすみやかに加熱されるので安定した液体燃料の気化
が行なわれ、燃料電池へ供給する改質ガスの圧力変動を
小さくすることができる。また、触媒燃焼器２６の成型
体に多数の孔苔を設けたことにより燃焼ガスは多数の孔
ｎを通って流れるので圧力損失は小さい。By the way, the vaporized W 29 buried in the catalytic combustor 26 @
As mentioned above, the heating method is to use the heat generated by combustion in the catalytic combustor section through conductive heat transfer through the molded body.
The liquid fuel flowing through it is not locally heated,
Since the liquid fuel is heated quickly, stable vaporization of the liquid fuel is performed, and pressure fluctuations in the reformed gas supplied to the fuel cell can be reduced. Further, by providing a large number of hole moss in the molded body of the catalytic combustor 26, combustion gas flows through a large number of holes n, so that pressure loss is small.
上記の説明から明らかなように本発明によれば、燃料改
質装置の気化器を触媒燃焼器に埋設したことにより、触
媒燃焼器の燃焼ガスの熱が触媒燃焼器内の伝導伝熱によ
り気化器を通流する液体燃料を局部的に加熱することな
く、かつすみやかに加熱するので、気化が安定に行なわ
れ、燃料電池に供給する改質ガスの圧力変動が少なくな
るという効果がある。As is clear from the above description, according to the present invention, by embedding the vaporizer of the fuel reformer in the catalytic combustor, the heat of the combustion gas in the catalytic combustor is vaporized by conductive heat transfer within the catalytic combustor. Since the liquid fuel flowing through the device is heated quickly without being locally heated, vaporization is performed stably and pressure fluctuations in the reformed gas supplied to the fuel cell are reduced.
第１図は本発明の実施例による燃料改質装置の燃焼器と
気化器との断面図、第２図は燃料改質装置と燃料電池と
からなる燃料電池発電システムの系統図である。FIG. 1 is a sectional view of a combustor and a carburetor of a fuel reformer according to an embodiment of the present invention, and FIG. 2 is a system diagram of a fuel cell power generation system comprising a fuel reformer and a fuel cell.
Claims (1)
に富むガスに改質する燃料改質装置において、ケース状
の炉体の内側壁に沿わせて燃焼ガス流路の孔を有する触
媒燃焼器を設け、該触媒燃焼器に外部に連通する気化器
を埋設し、前記触媒燃焼器の入口領域に燃料供給管と燃
焼空気供給管を開口させ、出口領域に燃焼ガス排気管を
開口させたことを特徴とする燃料改質装置。In a fuel reformer that vaporizes reformed liquid fuel using a heat transfer medium from a combustor to reform it into hydrogen-rich gas, a catalyst that has holes for a combustion gas flow path along the inner wall of a case-shaped furnace body. A combustor is provided, a vaporizer communicating with the outside is buried in the catalytic combustor, a fuel supply pipe and a combustion air supply pipe are opened in an inlet region of the catalytic combustor, and a combustion gas exhaust pipe is opened in an outlet region of the catalytic combustor. A fuel reformer characterized by:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61189851A JPS6344931A (en) | 1986-08-13 | 1986-08-13 | Fuel reforming apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61189851A JPS6344931A (en) | 1986-08-13 | 1986-08-13 | Fuel reforming apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS6344931A true JPS6344931A (en) | 1988-02-25 |
Family
ID=16248249
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61189851A Pending JPS6344931A (en) | 1986-08-13 | 1986-08-13 | Fuel reforming apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6344931A (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1996032753A1 (en) * | 1995-04-12 | 1996-10-17 | International Fuel Cells Corporation | Fuel processing apparatus having a furnace for fuel cell power plant |
| US6077620A (en) * | 1997-11-26 | 2000-06-20 | General Motors Corporation | Fuel cell system with combustor-heated reformer |
| WO2000045456A1 (en) * | 1999-01-27 | 2000-08-03 | Xcellsis Gmbh | Device for evaporating and/or overheating a hydrocarbon |
| EP1075035A2 (en) * | 1999-08-06 | 2001-02-07 | XCELLSIS GmbH | Combined component for the after-burning of anode exhaust gases of a fuel cell system and for evaporating of precursors fed to the fuel cell system |
| US6838063B2 (en) | 2000-10-06 | 2005-01-04 | Denso Corporation | Hydrogen supply device |
| US6919055B2 (en) | 2000-08-30 | 2005-07-19 | Denso Corporation | Hydrogen supply device |
| JP2007070180A (en) * | 2005-09-08 | 2007-03-22 | Casio Comput Co Ltd | Reactor |
| JP2011155011A (en) * | 2011-03-22 | 2011-08-11 | Honda Motor Co Ltd | Fuel cell system |
-
1986
- 1986-08-13 JP JP61189851A patent/JPS6344931A/en active Pending
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1996032753A1 (en) * | 1995-04-12 | 1996-10-17 | International Fuel Cells Corporation | Fuel processing apparatus having a furnace for fuel cell power plant |
| US6077620A (en) * | 1997-11-26 | 2000-06-20 | General Motors Corporation | Fuel cell system with combustor-heated reformer |
| WO2000045456A1 (en) * | 1999-01-27 | 2000-08-03 | Xcellsis Gmbh | Device for evaporating and/or overheating a hydrocarbon |
| US6696188B1 (en) | 1999-01-27 | 2004-02-24 | Ballard Power Systems Ag | Device for evaporating and/or overheating a hydrocarbon in a fuel cell |
| EP1075035A2 (en) * | 1999-08-06 | 2001-02-07 | XCELLSIS GmbH | Combined component for the after-burning of anode exhaust gases of a fuel cell system and for evaporating of precursors fed to the fuel cell system |
| EP1075035A3 (en) * | 1999-08-06 | 2004-10-06 | Ballard Power Systems AG | Combined component for the after-burning of anode exhaust gases of a fuel cell system and for evaporating of precursors fed to the fuel cell system |
| US6919055B2 (en) | 2000-08-30 | 2005-07-19 | Denso Corporation | Hydrogen supply device |
| US6838063B2 (en) | 2000-10-06 | 2005-01-04 | Denso Corporation | Hydrogen supply device |
| JP2007070180A (en) * | 2005-09-08 | 2007-03-22 | Casio Comput Co Ltd | Reactor |
| JP2011155011A (en) * | 2011-03-22 | 2011-08-11 | Honda Motor Co Ltd | Fuel cell system |
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