JPS61250409A - Apparatus for catalytic combustion - Google Patents

Apparatus for catalytic combustion

Info

Publication number
JPS61250409A
JPS61250409A JP60092558A JP9255885A JPS61250409A JP S61250409 A JPS61250409 A JP S61250409A JP 60092558 A JP60092558 A JP 60092558A JP 9255885 A JP9255885 A JP 9255885A JP S61250409 A JPS61250409 A JP S61250409A
Authority
JP
Japan
Prior art keywords
air
combustion
gas
catalytic combustion
combustion catalyst
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
JP60092558A
Other languages
Japanese (ja)
Inventor
Tomoki Eguchi
江口 知己
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.)
JAPAN FUEL TECHNOL CORP
Toshiba Corp
Original Assignee
JAPAN FUEL TECHNOL CORP
Toshiba Corp
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 JAPAN FUEL TECHNOL CORP, Toshiba Corp filed Critical JAPAN FUEL TECHNOL CORP
Priority to JP60092558A priority Critical patent/JPS61250409A/en
Publication of JPS61250409A publication Critical patent/JPS61250409A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C13/00Apparatus in which combustion takes place in the presence of catalytic material
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/06Combination of fuel cells with means for production of reactants or for treatment of residues
    • H01M8/0606Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
    • H01M8/0612Combination 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
    • H01M8/0625Combination 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
    • H01M8/0631Reactor construction specially adapted for combination reactor/fuel cell
    • 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 surely prevent a backfire and to make possible a stable catalytic combustion, by providing porous solid substances of high porosity and permeability on the introducing side of mixed gases. CONSTITUTION:Combustible gases 2 are introduced into a gas mixer 1 together with air or exhaust air 3 whose oxygen concentration is lower than that of the ordinary air. A gas mixture of the combustible gases 2, having being mixed in the gas mixer 1, and air or the exhaust air 3 are passed through permeable, porous solid substances 6 of extremely high porosity, causing almost no pressure drop, and then introduced into a catalytic combustion chamber 4. In the catalytic combustion chamber 4 the combustible gases 2 burn with air or the exhaust air 3 in the presence of combustion catalysts 41 and forwarded to gas users as high-temperature combustion gases. Backfires being thus prevented, and being also capable of a low-load operation, a stable catalytic combustion can be carried out together with low energy loss.

Description

【発明の詳細な説明】 [発明の技術分野] 本発明は可燃性ガスを、燃焼触媒の存在下で空気または
酸素濃度が通常の空気よりも低い空気により燃焼させる
触媒燃焼装置の改良に関する。
DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to an improvement in a catalytic combustion device for burning flammable gas in the presence of a combustion catalyst using air or air having a lower oxygen concentration than normal air.

[発明の技術的背景とその問題点] 近年、燃料の有している化学的エネルギーを直接電気的
エネルギーに変換するものとして、燃料電池発電システ
ムの開発が盛んに進められてきている。この燃料電池発
電システムは通常、電解質を挟んで一対の多孔質電橋を
配置するとともに、一方の電極の背面に水素等の燃料ガ
スを接触させ、また他方の電極の背面に空気等の酸化剤
ガスを接触させ、このとき起こる電気化学的反応を利用
して上記電極間から電気エネルギーを取出すようにした
もので、上記燃料ガスと酸化剤ガスが供給されている限
り高い変換効率で電気エネルギーを取出すことができる
ものである。
[Technical Background of the Invention and Problems thereof] In recent years, development of fuel cell power generation systems has been actively promoted as systems that directly convert chemical energy contained in fuel into electrical energy. This fuel cell power generation system usually arranges a pair of porous electric bridges with an electrolyte in between, and contacts a fuel gas such as hydrogen on the back of one electrode, and an oxidizing agent such as air on the back of the other electrode. Electrical energy is extracted from between the electrodes by bringing gas into contact and utilizing the electrochemical reaction that occurs.As long as the fuel gas and oxidant gas are supplied, electrical energy can be extracted with high conversion efficiency. It is something that can be taken out.

一方、この種の燃料電池発電システム゛ではシステムの
総合効率を高めるための方法として、燃料電池での電気
化学的反応に使用した後に排出される酸素濃度の低い空
気を、上記燃料電池用の燃料である水素製造を目的とし
た改質装置における改質反応の加熱源用空気として利用
することが提案されてきている(特開昭57−3678
4号公報)。
On the other hand, in this type of fuel cell power generation system, as a method to increase the overall efficiency of the system, air with a low oxygen concentration that is exhausted after being used for the electrochemical reaction in the fuel cell is used as the fuel for the fuel cell. It has been proposed to use the air as a heating source for the reforming reaction in a reformer for producing hydrogen (Japanese Patent Laid-Open No. 57-3678).
Publication No. 4).

また、環境保全上の問題からNox排出規制が厳しくな
り、かかる燃料電池発電システムでも改質装置からの燃
焼排ガス中のNoxを低減する必要がある。そのため最
近では、バーナー燃焼法に比べてNox発生の少ない触
媒燃焼法を、改質装置における加熱方法として採用する
技術の開発が実用化されつつある。すなわちこの触媒燃
焼法は、燃料電池の一方の電極から排出される排空気と
、他方の′jIl極から排出される排燃料とを混合し、
これを燃焼触媒の存在下で燃焼させるものである。
In addition, NOx emission regulations have become stricter due to environmental conservation issues, and it is necessary to reduce Nox in the combustion exhaust gas from the reformer even in such fuel cell power generation systems. Therefore, recently, a technology has been put into practical use that employs a catalytic combustion method, which generates less Nox than a burner combustion method, as a heating method in a reformer. That is, this catalytic combustion method mixes exhaust air discharged from one electrode of a fuel cell and exhaust fuel discharged from the other electrode,
This is combusted in the presence of a combustion catalyst.

ところで、この種の触媒燃焼法により触媒燃焼を行なう
場合、従来では排空気と排燃料とを混合器により予め混
合し、この混合ガスを燃焼触媒が充填された燃焼触媒室
へ導入して、この燃焼触媒の存在下で上記排燃料を燃焼
させるように装置構成している。そしてこの場合、燃焼
触媒室へ導入する混合ガスの流速は、混合ガスへの逆火
を防止するために火焔伝播速度よりも速くする必要があ
る。しかしこのような触媒燃焼装置では、低負荷での運
転を行なうことができないという致命的な問題がある。
By the way, when performing catalytic combustion using this type of catalytic combustion method, conventionally, exhaust air and exhaust fuel are mixed in advance in a mixer, and this mixed gas is introduced into a combustion catalyst chamber filled with a combustion catalyst. The apparatus is configured to combust the exhaust fuel in the presence of a combustion catalyst. In this case, the flow rate of the mixed gas introduced into the combustion catalyst chamber needs to be faster than the flame propagation speed in order to prevent backfire to the mixed gas. However, such a catalytic combustion device has a fatal problem in that it cannot be operated at low loads.

また、混合ガスの流速を高めるためのエネルギー損失が
あり、システム効率向上の点から好ましくない。
Furthermore, there is energy loss due to increasing the flow rate of the mixed gas, which is not preferable from the point of view of improving system efficiency.

一方、これらのMI題を解消するために、空気または酸
素濃度が通常の空気よりも低い排空気と可燃性ガスとを
、可燃限界に入らぬように混合して燃焼触媒室へ導入し
て燃焼させ、その後で不足分の空気、可燃性ガス、排空
気を燃焼触媒室へ導入するようにすることも可能である
が、かかるものでは必要とする燃焼触媒の量が多くなっ
て不経済であり、またガスの導入部が一層増えて装置構
成が複雑となり好ましくない。
On the other hand, in order to solve these MI problems, air or exhaust air with a lower oxygen concentration than normal air and flammable gas are mixed together without exceeding the flammability limit and introduced into the combustion catalyst chamber for combustion. It is also possible to introduce the insufficient amount of air, combustible gas, and exhaust air into the combustion catalyst chamber after that, but such a method requires a large amount of combustion catalyst and is uneconomical. Moreover, the number of gas introduction parts increases further, making the device configuration complicated, which is not preferable.

[発明の目的コ 本発明は上記のような問題を解決するために成されたも
ので、その目的は燃焼触媒室へ導入する混合ガスの流速
を速くすることなく逆火を確実に防止し、低負荷運転に
も耐えかつエネルギー損失が少ない状態で安定した触媒
燃焼を行なうことが可能な安価でしかも構成の簡単な触
媒燃焼装置を提供することにある。
[Purpose of the Invention] The present invention has been made to solve the above-mentioned problems, and its purpose is to reliably prevent flashback without increasing the flow rate of the mixed gas introduced into the combustion catalyst chamber, To provide a catalytic combustion device that is inexpensive and has a simple configuration, capable of withstanding low-load operation and performing stable catalytic combustion with little energy loss.

[発明の概要J 上記目的を達成するために本発明では、空気または酸素
濃度が通常の空気よりも低い空気と可燃性ガスとを混合
器により混合し、この混合ガスを燃焼触媒が充填された
燃焼触媒室へ導入してこの燃焼触媒の存在下で上記可燃
性ガスを燃焼させる触媒燃焼装置において、上記燃焼触
媒室の混合ガス導入側に、空隙率の高い透過性のある多
孔性固体物質を設けて構成するようにしたことを特徴と
する。
[Summary of the Invention J In order to achieve the above object, the present invention mixes air or air with a lower oxygen concentration than normal air with a flammable gas in a mixer, and mixes this mixed gas with a combustion catalyst filled with a combustion catalyst. In a catalytic combustion device that introduces the combustible gas into a combustion catalyst chamber and burns it in the presence of the combustion catalyst, a porous solid material with high porosity and permeability is provided on the mixed gas introduction side of the combustion catalyst chamber. It is characterized in that it is configured by providing the following information.

[発明の実施例] 以下、本発明を図面に示す一実施例について説明する。[Embodiments of the invention] An embodiment of the present invention shown in the drawings will be described below.

図は1本発明による触媒燃焼装置の構成例を示すもので
ある。図において、1は可燃性ガス2と、空気または酸
素濃度が通常の空気よりも低い(図示しない燃料電池か
らの)排空気3とを混合する混合器である。また、4は
燃焼触媒41が容器42内に充填されて成り、上記混合
器1h1らの混合ガスを導入する燃焼触媒室で、この燃
焼触媒41の存在下で上記可燃性ガス2を燃焼させ、そ
の高温燃焼ガス5を改質装置の改質管など所望のガス利
用対象へ供給するように−している。さらに、6は空隙
率の極めて高い透過性のあるセラミックス等の多孔性固
体物質であり、上記燃焼触媒室4と混合器1との間つま
り燃焼触媒室4の混合ガス導入側に設けている。なおこ
の場合、可燃性ガス2.空気または排空気3は約400
℃まで予熱されている。また混合器1は、圧力損失が少
ない効率のよい混合器を用いている。
The figure shows an example of the configuration of a catalytic combustion device according to the present invention. In the figure, 1 is a mixer that mixes combustible gas 2 and air or exhaust air 3 (from a fuel cell, not shown), which has a lower oxygen concentration than normal air. Further, 4 is a combustion catalyst chamber in which a combustion catalyst 41 is filled in a container 42 and into which the mixed gas from the mixer 1h1 is introduced, in which the combustible gas 2 is combusted in the presence of this combustion catalyst 41, The high-temperature combustion gas 5 is supplied to a desired gas utilization target such as a reforming pipe of a reforming device. Further, reference numeral 6 is a porous solid material such as ceramic having extremely high porosity and permeability, and is provided between the combustion catalyst chamber 4 and the mixer 1, that is, on the mixed gas introduction side of the combustion catalyst chamber 4. In this case, combustible gas 2. Air or exhaust air 3 is approximately 400
Preheated to ℃. Further, as the mixer 1, an efficient mixer with low pressure loss is used.

かかる構成の触媒燃焼装置において、可燃性ガス2は空
気または酸素濃度が通常の空気よりも低い排空気3とと
もに混合器1に導入される。この混合器1で混合された
可燃性ガス2と空気または排空気3との混合ガスは、空
隙率の極め゛て高い透過性のある多孔性固体物質6中を
圧力損失をほとんど生ずることなく通過し、これより燃
焼触媒室4内に導入される。そしてこの燃焼触媒室4に
おいて、可燃性ガス2は懲焼触I[41の存在下で空気
または排空気3により燃焼し、高温燃焼ガス5となって
図示しないガス利用対象へ排出され種々の目的に使用さ
れることになる。
In a catalytic combustion device having such a configuration, combustible gas 2 is introduced into mixer 1 together with air or exhaust air 3 whose oxygen concentration is lower than that of normal air. The mixed gas of combustible gas 2 and air or exhaust air 3 mixed in this mixer 1 passes through a permeable porous solid material 6 with extremely high porosity with almost no pressure loss. From this point, it is introduced into the combustion catalyst chamber 4. In this combustion catalyst chamber 4, the combustible gas 2 is combusted by air or exhaust air 3 in the presence of a combustion catalyst I [41], and becomes a high-temperature combustion gas 5 which is discharged to a gas utilization target (not shown) for various purposes. It will be used for

さてこの場合、もし多孔性固体物質6がないと高温にな
った燃焼触媒41の上部からの熱輻射のために、混合器
1内部のガス流速が火焔伝播速度よりも遅くなると逆火
し混合器1の内部で燃焼が起こる。そうなると、この燃
焼はもはや触媒燃焼ではなく通常のバーナー燃焼と同様
になり、高温燃焼ガス5中のNoxが触媒燃焼に比べて
増大する。この点本実施例構成のものでは、図示のよう
に燃焼触媒室4の混合ガス導入側に多孔性固体物質6が
存在していることから、混合器1内部のガス流速が火焔
伝播速度より遅くなっても、燃焼触媒室4で燃焼が起こ
る際の高温度の影響が多孔性固体物質6で妨げられるこ
とになり、燃焼触媒室4より混合室1への逆火現象は発
生しない。従って、触媒燃焼装置としての機能が十分に
維持され、たとえ低負荷であっても安定した低NOX燃
焼を実現することができる。なお上記で、混合ガスは当
該ガスが着火しない程度に予熱されていても、機能上は
何ら差支えないものである。
In this case, if the porous solid material 6 were not present, backfire would occur if the gas flow rate inside the mixer 1 became slower than the flame propagation speed due to heat radiation from the upper part of the combustion catalyst 41, which had reached a high temperature. Combustion occurs inside 1. In this case, this combustion is no longer catalytic combustion but similar to normal burner combustion, and the amount of Nox in the high temperature combustion gas 5 increases compared to catalytic combustion. In this regard, in the configuration of this embodiment, since the porous solid material 6 is present on the mixed gas introduction side of the combustion catalyst chamber 4 as shown in the figure, the gas flow velocity inside the mixer 1 is slower than the flame propagation velocity. Even if this occurs, the effect of high temperature when combustion occurs in the combustion catalyst chamber 4 is blocked by the porous solid material 6, and no flashback phenomenon from the combustion catalyst chamber 4 to the mixing chamber 1 occurs. Therefore, the function as a catalytic combustion device is sufficiently maintained, and stable low NOx combustion can be achieved even under low load. In the above, even if the mixed gas is preheated to such an extent that the gas does not ignite, there is no functional problem.

以上述べたように本実施例構成の触媒燃焼装置によれば
、次のような効果を得ることができるものである。
As described above, according to the catalytic combustion apparatus configured in this embodiment, the following effects can be obtained.

(a)燃焼触媒室4の混合ガス導入側に、空隙率の高い
透過性のある多孔性固体物質6を設けていることから、
従来のように燃焼触媒室4へ導入する混合ガスの流速を
速くすることなく逆火を確実に防止することが可能とな
る。その結果、低負荷での運転を行なうことができると
共に、エネルギー損失が少ない状態で安定した触媒燃焼
を行なうことができる。
(a) Since a porous solid material 6 with high porosity and permeability is provided on the mixed gas introduction side of the combustion catalyst chamber 4,
It becomes possible to reliably prevent flashback without increasing the flow rate of the mixed gas introduced into the combustion catalyst chamber 4 as in the conventional case. As a result, it is possible to operate at a low load and to perform stable catalytic combustion with little energy loss.

(b)上記(a)項の理由により、低負荷での運転不可
能および混合ガスの流速を高めるためのエネルギー損失
の問題を解消するために、従来のように空気または排空
気と可燃性ガスとを、可燃限界に入らぬように混合して
燃焼触媒室へ導入して燃焼させ、その後で不足分の空気
、可燃性ガス、排空気を燃焼触媒室へ導入するようなこ
とも一切不要となる。その結果、これに要する燃焼触媒
を省略してコストダウンを図り、またガスの導入部を減
らして装置構成の簡単化をも図ることができる。
(b) Due to the reason in paragraph (a) above, in order to solve the problem of inability to operate at low loads and energy loss due to increasing the flow rate of mixed gas, air or exhaust air and flammable gas There is no need to mix the mixture without exceeding the flammability limit and introduce it into the combustion catalyst chamber for combustion, and then introduce the insufficient air, combustible gas, and exhaust air into the combustion catalyst chamber. Become. As a result, it is possible to reduce costs by omitting the combustion catalyst required for this, and it is also possible to simplify the device configuration by reducing the number of gas introduction sections.

尚、本発明は上記実施例に限定されるものではなく、そ
の要旨を変更しない範囲で種々に変形して実施すること
ができるものである。
It should be noted that the present invention is not limited to the above embodiments, and can be implemented with various modifications without changing the gist thereof.

[発明の効果] 以上説明したように本発明によれば、空気または酸素濃
度が通常の空気よりも低い空気と可燃性ガスとを混合器
により混合し、この混合ガスを燃焼触媒が充填された燃
焼触媒室へ導入してこの燃焼触媒の存在下で上記可燃性
ガスを燃焼させる触媒燃焼装置において、上記燃焼触媒
室の混合ガス導入側に、空隙率の高い透過性のある多孔
性固体物質を設けて構成するようにしたので、燃焼触媒
室へ導入する混合ガスの流速を速くすることなく逆火を
確実に防止し、低負荷運転にも耐えかつエネルギー損失
が少ない状態で安定した触媒燃焼を行なうことが可能な
安価でしかも構成の簡単な触媒燃焼装置が提供できる。
[Effects of the Invention] As explained above, according to the present invention, air or air with a lower oxygen concentration than normal air is mixed with a flammable gas, and this mixed gas is mixed with a combustion catalyst filled with a combustion catalyst. In a catalytic combustion device that introduces the combustible gas into a combustion catalyst chamber and burns it in the presence of the combustion catalyst, a porous solid material with high porosity and permeability is provided on the mixed gas introduction side of the combustion catalyst chamber. This structure reliably prevents flashback without increasing the flow rate of the mixed gas introduced into the combustion catalyst chamber, and allows stable catalytic combustion to withstand low-load operation and with little energy loss. It is possible to provide a catalytic combustion device that is inexpensive and has a simple configuration.

【図面の簡単な説明】[Brief explanation of the drawing]

図は本発明の一実施例を示す構成図である。 1・・・混合器、2・・・可燃性ガス、3・・・空気ま
たは酸素濃度の低い排空気、4・・・燃焼触媒室、41
・・・燃焼触媒、42・・・容器、5・・・^温燃焼ガ
ス、6・・・多孔性固体物質。
The figure is a configuration diagram showing an embodiment of the present invention. 1... Mixer, 2... Flammable gas, 3... Air or exhaust air with low oxygen concentration, 4... Combustion catalyst chamber, 41
... Combustion catalyst, 42... Container, 5... ^ Warm combustion gas, 6... Porous solid material.

Claims (1)

【特許請求の範囲】[Claims] 空気または酸素濃度が通常の空気よりも低い空気と可燃
性ガスとを混合器により混合し、この混合ガスを燃焼触
媒が充填された燃焼触媒室へ導入してこの燃焼触媒の存
在下で前記可燃性ガスを燃焼させる触媒燃焼装置におい
て、前記燃焼触媒室の混合ガス導入側に、空隙率の高い
透過性のある多孔性固体物質を設けて成ることを特徴と
する触媒燃焼装置。
Air or air with a lower oxygen concentration than normal air is mixed with a combustible gas in a mixer, and this mixed gas is introduced into a combustion catalyst chamber filled with a combustion catalyst. A catalytic combustion device for combusting a reactive gas, characterized in that a permeable porous solid material with a high porosity is provided on the mixed gas introduction side of the combustion catalyst chamber.
JP60092558A 1985-04-30 1985-04-30 Apparatus for catalytic combustion Pending JPS61250409A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60092558A JPS61250409A (en) 1985-04-30 1985-04-30 Apparatus for catalytic combustion

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60092558A JPS61250409A (en) 1985-04-30 1985-04-30 Apparatus for catalytic combustion

Publications (1)

Publication Number Publication Date
JPS61250409A true JPS61250409A (en) 1986-11-07

Family

ID=14057744

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60092558A Pending JPS61250409A (en) 1985-04-30 1985-04-30 Apparatus for catalytic combustion

Country Status (1)

Country Link
JP (1) JPS61250409A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6410007A (en) * 1987-07-01 1989-01-13 Toshiba Corp Catalytic burning apparatus
JPH04108A (en) * 1990-03-14 1992-01-06 Mitsubishi Heavy Ind Ltd Combustion device
WO1995001532A1 (en) * 1993-07-02 1995-01-12 Applikations- Und Technik Zentrum Für Energieverfahrens-, Umwelt Und Strömungstechnik Burner
EP0924786A2 (en) * 1997-11-20 1999-06-23 General Motors Corporation Fuel cell system combustor
JP2009536143A (en) * 2006-05-08 2009-10-08 コンパクトジーティーエル パブリック リミテッド カンパニー Catalytic reactor with alternating first and second flow channels
JP2015014499A (en) * 2013-07-04 2015-01-22 ダイハツ工業株式会社 Hydrogen-oxygen coupler

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5217964A (en) * 1975-07-30 1977-02-10 Matsushita Electric Ind Co Ltd Cooking equipment
JPS59173622A (en) * 1983-03-23 1984-10-01 Matsushita Electric Ind Co Ltd Catalytic substance burner

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5217964A (en) * 1975-07-30 1977-02-10 Matsushita Electric Ind Co Ltd Cooking equipment
JPS59173622A (en) * 1983-03-23 1984-10-01 Matsushita Electric Ind Co Ltd Catalytic substance burner

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6410007A (en) * 1987-07-01 1989-01-13 Toshiba Corp Catalytic burning apparatus
JPH04108A (en) * 1990-03-14 1992-01-06 Mitsubishi Heavy Ind Ltd Combustion device
WO1995001532A1 (en) * 1993-07-02 1995-01-12 Applikations- Und Technik Zentrum Für Energieverfahrens-, Umwelt Und Strömungstechnik Burner
EP0924786A2 (en) * 1997-11-20 1999-06-23 General Motors Corporation Fuel cell system combustor
EP0924786A3 (en) * 1997-11-20 2000-07-26 General Motors Corporation Fuel cell system combustor
JP2009536143A (en) * 2006-05-08 2009-10-08 コンパクトジーティーエル パブリック リミテッド カンパニー Catalytic reactor with alternating first and second flow channels
JP2015014499A (en) * 2013-07-04 2015-01-22 ダイハツ工業株式会社 Hydrogen-oxygen coupler

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