JP2002053302A - Burner for fuel reformer - Google Patents

Burner for fuel reformer

Info

Publication number
JP2002053302A
JP2002053302A JP2000241433A JP2000241433A JP2002053302A JP 2002053302 A JP2002053302 A JP 2002053302A JP 2000241433 A JP2000241433 A JP 2000241433A JP 2000241433 A JP2000241433 A JP 2000241433A JP 2002053302 A JP2002053302 A JP 2002053302A
Authority
JP
Japan
Prior art keywords
fuel
gas
burner
pipe
fuel 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.)
Pending
Application number
JP2000241433A
Other languages
Japanese (ja)
Inventor
Akira Fujio
昭 藤生
Taketoshi Ouki
丈俊 黄木
Keigo Miyai
恵吾 宮井
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.)
Sanyo Electric Co Ltd
Original Assignee
Sanyo 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 Sanyo Electric Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP2000241433A priority Critical patent/JP2002053302A/en
Publication of JP2002053302A publication Critical patent/JP2002053302A/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

PROBLEM TO BE SOLVED: To provide an inexpensive and high reliability burner for fuel reformer which is capable of stably combusting a fuel gas with simple structure by preventing the problems such as the instability of flame due to condensed water, the generation of noise or accidental fire. SOLUTION: The burner is used for heating a fuel reformer to reform a hydrocarbon-based fuel into a hydrogen enriched reformed gas. The fuel gas supply pipe for supplying the fuel gas to a burner combustion part is formed into a double tube structure, the inside tube of the double tube is used as a fuel gas supply pipe line for supplying the fuel gas to a burner combustion part and the outside tube of the double tube is used as a condensed water discharge pipe line for discharging the condensed water in the burner combustion part to the outside.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、燃料改質器用バー
ナに関し、さらに詳しくは炭化水素系燃料を水素リッチ
な改質ガスに改質するための燃料改質器用バーナに関す
る。
The present invention relates to a burner for a fuel reformer, and more particularly to a burner for a fuel reformer for reforming a hydrocarbon-based fuel into a hydrogen-rich reformed gas.

【0002】[0002]

【従来の技術】炭化水素系燃料、例えばメタンと水蒸気
の混合ガス[例えば、スチーム/炭素(モル比)=2.
5程度]を燃料改質器に供給して水蒸気改質して燃料電
池などの用途に使用する水素リッチな改質ガスに改質す
る場合、燃料改質器における化学反応は吸熱反応である
ので、バーナによって常時加熱しながら化学反応が行わ
れる。
2. Description of the Related Art A hydrocarbon-based fuel, for example, a mixed gas of methane and steam [for example, steam / carbon (molar ratio) = 2.
5) is supplied to a fuel reformer to reform it into a hydrogen-rich reformed gas for use in fuel cells and the like, because the chemical reaction in the fuel reformer is an endothermic reaction. The chemical reaction is performed while constantly heating with a burner.

【0003】図4は従来の燃料改質器の断面説明図であ
り、図5は図4に示した従来の燃料改質器のバーナの断
面説明図である。図4において、燃料改質器1は、改質
管外筒2、改質管内筒3、改質管内筒上板4、改質管外
筒上板5、この改質管外筒上板5に設けられた改質原燃
料入口6、改質ガス出口7などを備えるとともに、その
中央に設けられた中空部に加熱するための燃焼ガスを導
入する加熱部8を備えた改質管9と、改質管9の内部に
装着された触媒管10と、改質管内筒3と触媒管10と
の間に充填されるとともに改質管内筒上板4の上にも配
設された改質触媒11(例えば、アルミナに担持したN
i、ルテニウム触媒など)と、改質管9の外部に燃焼排
ガスを接触させて導いた後、燃焼排ガス出口12から外
部に排出する燃焼排ガス管13と、加熱部8内に燃焼ガ
スを導入するために延在して挿入された燃焼ガス管14
と、燃焼ガス管14下部に設けられた燃料ガスを燃焼さ
せるバーナ15などを備えている。
FIG. 4 is a sectional view of a conventional fuel reformer, and FIG. 5 is a sectional view of a burner of the conventional fuel reformer shown in FIG. In FIG. 4, a fuel reformer 1 includes a reforming tube outer tube 2, a reforming tube inner tube 3, a reforming tube inner tube upper plate 4, a reforming tube outer tube upper plate 5, and a reforming tube outer tube upper plate 5. A reforming pipe 9 provided with a reforming raw fuel inlet 6, a reformed gas outlet 7 and the like, and a heating unit 8 for introducing a combustion gas for heating into a hollow portion provided at the center thereof; , A catalyst tube 10 mounted inside the reforming tube 9, and a reformer filled between the reforming tube inner tube 3 and the catalyst tube 10 and also disposed on the reforming tube inner tube upper plate 4. Catalyst 11 (for example, N supported on alumina
i, a ruthenium catalyst, etc.) and the flue gas coming into contact with the outside of the reforming pipe 9 and leading it, and then the flue gas pipe 13 discharged outside from the flue gas outlet 12 and the combustion gas into the heating unit 8. Gas tube 14 extending and inserted for
And a burner 15 provided at a lower portion of the combustion gas pipe 14 for burning fuel gas.

【0004】図4において、バーナ15へ燃料ガスと空
気を導入して燃料ガスを燃焼させ、燃焼ガスを破線矢印
で示したように燃焼ガス管14を経て加熱部8へ導いて
改質触媒11を加熱した後、燃焼排ガスは改質管外筒2
と燃焼排ガス管13の間を通って燃焼排ガス出口12か
ら排出される。一方、原燃料入口6から炭化水素系燃
料、例えば、メタンを水蒸気とともに矢印で示したよう
に燃料改質器1内に導入して加熱された改質触媒11に
接触させて改質する。燃料改質器1の運転温度はおよそ
700℃(改質触媒11の出口温度)に制御されて運転
される。生成した改質ガス(スチーム/炭素(モル比)
=2.5程度の原料を改質すると、水素約75%、一酸
化炭素約10数%、二酸化炭素約10数%程度、残部メ
タンガスおよび水分を含有する改質ガスが得られる)は
矢印で示したように改質管外筒2と触媒管10との間を
通って改質ガス出口7から排出される。
In FIG. 4, a fuel gas and air are introduced into a burner 15 to burn the fuel gas, and the combustion gas is led to a heating unit 8 through a combustion gas pipe 14 as shown by a dashed arrow, thereby forming a reforming catalyst 11. After heating the flue gas, the combustion exhaust gas
The exhaust gas is discharged from the combustion exhaust gas outlet 12 through the space between the exhaust gas and the combustion exhaust gas pipe 13. On the other hand, a hydrocarbon-based fuel, for example, methane is introduced into the fuel reformer 1 together with water vapor from the raw fuel inlet 6 as shown by an arrow, and is brought into contact with the heated reforming catalyst 11 for reforming. The operation temperature of the fuel reformer 1 is controlled to be approximately 700 ° C. (the outlet temperature of the reforming catalyst 11). Generated reformed gas (steam / carbon (molar ratio)
Reforming a raw material of about 2.5 = about 75% of hydrogen, about 10% of carbon monoxide, about 10% of carbon dioxide, and the remaining methane gas and reformed gas containing water are obtained. As shown, the gas is discharged from the reformed gas outlet 7 through the space between the outer tube 2 of the reforming tube and the catalyst tube 10.

【0005】図5に示すように、バーナ15は、先端に
ガス拡散板16を備えこのガス拡散板16の下方に多数
のガス噴出孔17を設けた燃料ガス供給管18と、この
燃料ガス供給管18とバーナケース19に固定され、多
数の炎孔20を設けた空気噴射部21と、バーナケース
19内に燃焼用空気を導入する空気供給管22と、を備
えている。
[0005] As shown in FIG. 5, the burner 15 has a gas diffusion plate 16 at its tip and a fuel gas supply pipe 18 provided with a large number of gas ejection holes 17 below the gas diffusion plate 16. An air injection unit 21 fixed to the pipe 18 and the burner case 19 and provided with a large number of flame holes 20, and an air supply pipe 22 for introducing combustion air into the burner case 19 are provided.

【0006】上記の構成のバーナ15において、燃料ガ
ス供給管18を経て供給された燃料ガスは先端のガス噴
射孔17から噴射され、実線矢印で示したようにガス拡
散板16と空気噴射部21の底部21−1との間を通っ
てバーナ燃焼部23へ噴出される。一方、実線矢印で示
したように空気供給管22を経て供給された燃焼用空気
は燃焼用空気室24を通り空気噴射部21の炎孔20か
らバーナ燃焼部23へ噴射され燃料ガスと混合して燃料
ガスの燃焼が行われる。
In the burner 15 having the above-described structure, the fuel gas supplied through the fuel gas supply pipe 18 is injected from the gas injection hole 17 at the tip, and as shown by the solid arrow, the gas diffusion plate 16 and the air injection section 21 are provided. And is ejected to the burner combustion part 23 through the space between the bottom part 21-1. On the other hand, as shown by the solid line arrows, the combustion air supplied through the air supply pipe 22 passes through the combustion air chamber 24, is injected from the flame hole 20 of the air injection unit 21 to the burner combustion unit 23, and mixes with the fuel gas. Combustion of the fuel gas is performed.

【0007】前記燃料ガスとして、メタンガスやプロパ
ンガスなどの炭化水素系燃料を使用する場合は特に問題
がないが、燃料電池や燃料改質器の始動時あるいは安定
運転時などにおいては、燃料ガスとして改質ガス自身を
使用したり、あるいは、改質ガスを燃料電池で使用した
後の未反応水素ガスであるオフガス(例えば、水素約3
0%、残部二酸化炭素、メタンガスおよび水分を含有す
るオフガス)を使用したり、あるいはメタンガスやプロ
パンガスなどの炭化水素系燃料と燃料電池のオフガスと
の混合物を使用したりする必要が生じるが、改質ガスや
燃料電池のオフガスには水分が含まれているために次の
ようなトラブルが発生する。
There is no particular problem when using a hydrocarbon-based fuel such as methane gas or propane gas as the fuel gas. However, when the fuel cell or the fuel reformer is started or when it is operated stably, the fuel gas is not used. Off-gas which is unreacted hydrogen gas after using the reformed gas itself or after using the reformed gas in a fuel cell (for example, about 3% hydrogen)
However, it is necessary to use an off-gas containing 0% and the balance carbon dioxide, methane gas and moisture, or use a mixture of a hydrocarbon-based fuel such as methane gas and propane gas and an off-gas of a fuel cell. Since the quality gas and the off-gas of the fuel cell contain moisture, the following troubles occur.

【0008】すなわち、図5に示したように水分を含む
改質ガスや燃料電池のオフガスなどの燃料ガスが、燃料
ガス供給管18を経て先端のガス噴射孔17から噴射さ
れ、実線矢印で示したようにガス拡散板16と空気噴射
部21の底部21−1との間を通ってバーナ燃焼部23
へ噴出される間に、燃料ガス中に含まれる水分が凝縮し
て液体の水になり、底部21−1上に溜り、そして溜っ
た水量が多くなると、ガス噴出孔17が水で詰まり、ガ
ス噴出孔17が水で詰まると燃料ガスの噴出速度が部分
的に大きくなって、火炎が不安定になり、騒音が発生
し、最悪の場合は失火する問題があった。
That is, as shown in FIG. 5, a fuel gas such as a reformed gas containing water or an off-gas of a fuel cell is injected from a gas injection hole 17 at a tip through a fuel gas supply pipe 18, and is indicated by a solid arrow. As described above, the burner combustion part 23 passes between the gas diffusion plate 16 and the bottom 21-1 of the air injection part 21.
While the fuel gas is ejected, the water contained in the fuel gas condenses into liquid water and accumulates on the bottom 21-1. When the amount of accumulated water increases, the gas ejection holes 17 are clogged with water, When the ejection holes 17 are clogged with water, the ejection speed of the fuel gas partially increases, the flame becomes unstable, noise is generated, and in the worst case, there is a problem of misfiring.

【0009】[0009]

【発明が解決しようとする課題】本発明の目的は、従来
の問題を解決し、水分を含む改質ガスや燃料電池のオフ
ガスなどを燃料ガスとして使用しても、安定して燃料ガ
スの燃焼を行うことができる、簡単な構成で、コストが
かからず安価で、信頼性が高い燃料改質器用バーナを提
供することである。
SUMMARY OF THE INVENTION An object of the present invention is to solve the conventional problems and to stably combust a fuel gas even when a reformed gas containing water or an off-gas of a fuel cell is used as the fuel gas. It is an object of the present invention to provide a highly reliable burner for a fuel reformer with a simple configuration, low cost, low cost, and high reliability.

【0010】[0010]

【課題を解決するための手段】上記課題を解決するため
請求項1の燃料改質器用バーナは、炭化水素系燃料を水
素リッチな改質ガスに改質するための燃料改質器の加熱
に用いるバーナであって、バーナ燃焼部へ燃料ガスを供
給する燃料ガス供給管を2重管構造とし、この2重管の
内管はバーナ燃焼部へ燃料ガスを供給する燃料ガス供給
管路として使用し、この2重管の外管はバーナ燃焼部の
凝縮水を外部に排出する凝縮水排出管路として使用する
ことを特徴とする。
According to a first aspect of the present invention, there is provided a fuel reformer burner for heating a fuel reformer for reforming a hydrocarbon-based fuel into a hydrogen-rich reformed gas. A burner to be used, wherein a fuel gas supply pipe for supplying fuel gas to the burner combustion section has a double pipe structure, and an inner pipe of the double pipe is used as a fuel gas supply pipe for supplying fuel gas to the burner combustion section. The outer pipe of the double pipe is used as a condensed water discharge pipe for discharging the condensed water in the burner combustion section to the outside.

【0011】請求項2の燃料改質器用バーナは、請求項
1記載の燃料改質器用バーナにおいて、前記燃料ガス
が、炭化水素系燃料と燃料電池のオフガスの混合物もし
くは燃料電池のオフガスもしくは改質ガスであることを
特徴とする。
According to a second aspect of the present invention, there is provided a burner for a fuel reformer according to the first aspect, wherein the fuel gas is a mixture of a hydrocarbon fuel and an off-gas of a fuel cell or an off-gas or reforming of a fuel cell. It is a gas.

【0012】請求項3の燃料改質器用バーナは、請求項
1あるいは請求項2記載の燃料改質器用バーナにおい
て、前記外管にドレイン排出管を連結して設置したこと
を特徴とする。
According to a third aspect of the present invention, there is provided a burner for a fuel reformer according to the first or second aspect, wherein a drain discharge pipe is connected to the outer pipe.

【0013】[0013]

【発明の実施の形態】以下、本発明の実施の形態を図面
を用いて詳細に説明する。図1はこの発明の燃料改質器
用バーナの一実施の形態の断面説明図であり、図2はこ
の発明の他の燃料改質器用バーナの断面説明図であり、
図3は図2に示した燃料改質器用バーナの平面説明図で
ある。図1〜図3において従来技術と同じ構成部分には
同一参照符号を付すことにより、重複した説明を省略す
る。
Embodiments of the present invention will be described below in detail with reference to the drawings. FIG. 1 is an explanatory sectional view of an embodiment of a burner for a fuel reformer of the present invention, and FIG. 2 is an explanatory sectional view of a burner for another fuel reformer of the present invention;
FIG. 3 is an explanatory plan view of the burner for a fuel reformer shown in FIG. 1 to 3, the same components as those of the related art are denoted by the same reference numerals, and redundant description will be omitted.

【0014】図1において、本発明のバーナ15Aは、
燃料ガス供給管18を2重管構造にしてあり、この2重
管の内管18−1をバーナ燃焼部23へ燃料ガスを供給
する燃料ガス供給管路として使用し、そしてこの2重管
の外管18−2をバーナ燃焼部23で凝縮した凝縮水を
排出する凝縮水排出管路として使用するようにしてあ
り、かつ、外管18−2の下部に凝縮水を外部に排出す
るためのドレイン排出管25を連結して設置してある以
外は、図5に示したバーナ15と同様になっている。
In FIG. 1, a burner 15A according to the present invention comprises:
The fuel gas supply pipe 18 has a double pipe structure, and the inner pipe 18-1 of the double pipe is used as a fuel gas supply pipe for supplying fuel gas to the burner combustion section 23. The outer pipe 18-2 is used as a condensed water discharge conduit for discharging the condensed water condensed in the burner combustion section 23, and is provided at a lower portion of the outer pipe 18-2 for discharging the condensed water to the outside. It is the same as the burner 15 shown in FIG. 5, except that the drain discharge pipe 25 is connected and installed.

【0015】図1に示したように外管18−2の上部は
バーナ燃焼部23に通じるように開口して空気噴出部2
1の底部21−1に固定して設置してある。したがっ
て、水分を含む改質ガスや燃料電池のオフガスなどの燃
料ガスが、燃料ガス供給管18を経て先端のガス噴射孔
17から噴射され、図1に実線矢印で示したようにガス
拡散板16と空気噴射部21の底部21−1との間を通
ってバーナ燃焼部23へ噴出される間に、燃料ガス中に
含まれる水分が凝縮して液体の水になって底部21−1
上に移行してきても、この凝縮水は破線矢印で示したよ
うに2重管の外管18−2の前記開口を経て外管18−
2と内管18−1との間隙dを通って下方に流れ、ドレ
イン排出管25を経て外部に排出される。このように底
部21−1上に凝縮水が溜ってガス噴出孔17が水で詰
まることがなくなるので、安定して燃料ガスの燃焼を行
うことができる。
As shown in FIG. 1, the upper portion of the outer tube 18-2 is opened so as to communicate with the burner combustion portion 23, and the air ejection portion 2 is opened.
1 is fixedly installed on the bottom 21-1. Therefore, a fuel gas such as a reformed gas containing water or an off-gas of a fuel cell is injected from the gas injection hole 17 at the tip through the fuel gas supply pipe 18, and the gas diffusion plate 16 shown in FIG. The water contained in the fuel gas is condensed to become liquid water while being ejected to the burner combustion section 23 through the space between the bottom 21-1 and the bottom section 21-1 of the air injection section 21.
Even when moving upward, the condensed water passes through the opening of the outer pipe 18-2 of the double pipe as shown by the dashed arrow, and
It flows downward through the gap d between the inner pipe 2 and the inner pipe 18-1, and is discharged to the outside via the drain discharge pipe 25. As described above, since the condensed water does not accumulate on the bottom 21-1 and the gas ejection holes 17 are not clogged with water, the fuel gas can be stably burned.

【0016】外管18−2と内管18−1との間隙d
は、狭過ぎると凝縮水を排出できないので、凝縮水の排
出のためには広い方が好ましいが、あまり広いと空気の
流れや炎に悪影響がでるので、これらを考慮して設計し
て決めることが望ましい。
The gap d between the outer tube 18-2 and the inner tube 18-1
If the width is too narrow, condensed water cannot be discharged, so it is preferable to widen it for discharging condensed water.However, if it is too wide, air flow and flame will be adversely affected. Is desirable.

【0017】本発明のバーナ15Aの材質は特に限定さ
れないが、耐久性、耐腐食性、強度などを考慮してステ
ンレス系鋼を使用することが好ましい。
Although the material of the burner 15A of the present invention is not particularly limited, it is preferable to use stainless steel in consideration of durability, corrosion resistance, strength and the like.

【0018】図2に示した本発明の燃料改質器用バーナ
15Bは、空気噴出部を上方に行くに従って内径が広が
る漏斗型の空気噴出部21−2とし、空気噴出部21−
2の下部を直接2重管の外管18−2の上部先端に固定
して設置した以外は、図1に示したバーナ15Aと同様
になっている。
The burner 15B for a fuel reformer according to the present invention shown in FIG. 2 has a funnel-shaped air ejection part 21-2 whose inner diameter increases as the air ejection part goes upward, and the air ejection part 21-
The burner 15A is the same as the burner 15A shown in FIG. 1 except that the lower part of the burner 15 is directly fixed to the upper end of the outer pipe 18-2 of the double pipe.

【0019】本発明の燃料改質器用バーナ15Bは漏斗
型の空気噴出部21−2を用いたので、水分を含む改質
ガスや燃料電池のオフガスなどの燃料ガスを使用した際
に発生する凝縮水が流れ易く、凝縮水を2重管の外管1
8−2の前記開口を経て外管18−2と内管18−1と
の間隙dを通って下方に流し、ドレイン排出管25を経
て外部に容易に排出できる。
Since the burner 15B for the fuel reformer of the present invention uses the funnel-shaped air ejection portion 21-2, condensation generated when a fuel gas such as a reformed gas containing water or an off-gas of a fuel cell is used. Water is easy to flow and condensed water is transferred to the outer pipe 1
The liquid flows downward through the gap d between the outer pipe 18-2 and the inner pipe 18-1 through the opening 8-2, and can be easily discharged to the outside through the drain discharge pipe 25.

【0020】上記実施の形態の説明は、本発明を説明す
るためのものであって、特許請求の範囲に記載の発明を
限定し、或は範囲を減縮するものではない。又、本発明
の各部構成は上記実施の形態に限らず、特許請求の範囲
に記載の技術的範囲内で種々の変形が可能である。
The description of the above embodiments is for describing the present invention, and does not limit the scope of the invention described in the claims or reduce the scope thereof. Further, the configuration of each part of the present invention is not limited to the above embodiment, and various modifications can be made within the technical scope described in the claims.

【0021】[0021]

【発明の効果】本発明の請求項1の燃料改質器用バーナ
は、バーナ燃焼部へ燃料ガスを供給する燃料ガス供給管
を2重管構造とし、この2重管の内管をバーナ燃焼部へ
燃料ガスを供給する燃料ガス供給管路として使用し、こ
の2重管の外管はバーナ燃焼部の凝縮水を外部に排出す
る凝縮水排出管路として使用するので、凝縮水に起因す
る火炎の不安定、騒音の発生、失火などの問題を防止で
き、安定して燃料ガスの燃焼を行うことができる上、簡
単構成で、コストがかからず安価で、信頼性が高いとい
う顕著な効果を奏する。
According to a first aspect of the present invention, there is provided a burner for a fuel reformer, wherein a fuel gas supply pipe for supplying fuel gas to a burner combustion section has a double pipe structure, and an inner pipe of the double pipe is connected to the burner combustion section. Since the outer pipe of the double pipe is used as a condensed water discharge pipe for discharging the condensed water of the burner combustion part to the outside, the flame caused by the condensed water is used. In addition to being able to prevent problems such as instability, noise generation, and misfire, it can stably burn fuel gas, and has a remarkable effect of simple configuration, low cost, low cost, and high reliability. To play.

【0022】本発明の請求項2の燃料改質器用バーナ
は、燃料ガスが、炭化水素系燃料と燃料電池のオフガス
の混合物もしくは燃料電池のオフガスもしくは改質ガス
などの水分を含む燃料ガスであっても、凝縮水に起因す
る火炎の不安定、騒音の発生、失火などの問題を防止で
き、安定して燃料ガスの燃焼を行うことができるという
顕著な効果を奏する。
In the burner for a fuel reformer according to a second aspect of the present invention, the fuel gas is a fuel gas containing water such as a mixture of a hydrocarbon-based fuel and an off-gas of a fuel cell or an off-gas or a reformed gas of a fuel cell. However, it is possible to prevent problems such as flame instability, noise generation, and misfire caused by condensed water, and to achieve a remarkable effect that fuel gas can be stably burned.

【0023】本発明の請求項3の燃料改質器用バーナ
は、外管にドレイン排出管を連結して設置したので、外
管を経て流れた凝縮水を次いでドレイン排出管を経て外
部に容易に排出できるという顕著な効果を奏する。
In the fuel reformer burner according to the third aspect of the present invention, since the drain discharge pipe is connected to the outer pipe, the condensed water flowing through the outer pipe can be easily discharged to the outside through the drain discharge pipe. It has a remarkable effect that it can be discharged.

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

【図1】本発明の燃料改質器用バーナの一実施の形態の
断面説明図である。
FIG. 1 is an explanatory sectional view of one embodiment of a burner for a fuel reformer of the present invention.

【図2】本発明の他の燃料改質器用バーナの断面説明図
である。
FIG. 2 is an explanatory sectional view of another burner for a fuel reformer of the present invention.

【図3】図2に示した燃料改質器用バーナの平面説明図
である。
FIG. 3 is an explanatory plan view of the burner for a fuel reformer shown in FIG. 2;

【図4】従来の燃料改質器の断面説明図である。FIG. 4 is an explanatory sectional view of a conventional fuel reformer.

【図5】図4に示した従来の燃料改質器用バーナの断面
説明図である。
5 is an explanatory sectional view of the conventional burner for a fuel reformer shown in FIG. 4;

【符号の説明】[Explanation of symbols]

1 燃料改質器 15、15A、15B 燃料改質器用バーナ 16 ガス拡散板 17 ガス噴出孔 18 燃料ガス供給管 18−1 内管 18−2 外管 20 炎孔 21 空気噴出部 21−1 底部 22 空気供給管 23 バーナ燃焼部 24 空気室 25 ドレイン排出管 DESCRIPTION OF SYMBOLS 1 Fuel reformer 15, 15A, 15B Burner for fuel reformers 16 Gas diffusion plate 17 Gas ejection hole 18 Fuel gas supply pipe 18-1 Inner tube 18-2 Outer tube 20 Flame hole 21 Air ejection portion 21-1 Bottom 22 Air supply pipe 23 Burner combustion part 24 Air chamber 25 Drain discharge pipe

フロントページの続き (72)発明者 宮井 恵吾 大阪府守口市京阪本通2丁目5番5号 三 洋電機株式会社内 Fターム(参考) 3K019 AA02 AA08 BA04 BB02 BD09 4G040 EA03 EA06 EB14 5H027 BA01 BA09 Continued on the front page (72) Inventor Keigo Miyai 2-5-5 Keihanhondori, Moriguchi-shi, Osaka F-term in Sanyo Electric Co., Ltd. (reference) 3K019 AA02 AA08 BA04 BB02 BD09 4G040 EA03 EA06 EB14 5H027 BA01 BA09

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 炭化水素系燃料を水素リッチな改質ガス
に改質するための燃料改質器の加熱に用いるバーナであ
って、バーナ燃焼部へ燃料ガスを供給する燃料ガス供給
管を2重管構造とし、この2重管の内管はバーナ燃焼部
へ燃料ガスを供給する燃料ガス供給管路として使用し、
この2重管の外管はバーナ燃焼部の凝縮水を外部に排出
する凝縮水排出管路として使用することを特徴とする燃
料改質器用バーナ。
1. A burner used for heating a fuel reformer for reforming a hydrocarbon-based fuel into a hydrogen-rich reformed gas, comprising a fuel gas supply pipe for supplying a fuel gas to a burner combustion section. The inner pipe of this double pipe is used as a fuel gas supply pipe for supplying fuel gas to the burner combustion section.
The burner for a fuel reformer, wherein the outer pipe of the double pipe is used as a condensed water discharge pipe for discharging condensed water in a burner combustion section to the outside.
【請求項2】 前記燃料ガスが、炭化水素系燃料と燃料
電池のオフガスの混合物もしくは燃料電池のオフガスも
しくは改質ガスであることを特徴とする請求項1記載の
燃料改質器用バーナ。
2. The burner for a fuel reformer according to claim 1, wherein the fuel gas is a mixture of a hydrocarbon-based fuel and a fuel cell off-gas, or a fuel cell off-gas or reformed gas.
【請求項3】 前記外管にドレイン排出管を連結して設
置したことを特徴とする請求項1あるいは請求項2記載
の燃料改質器用バーナ。
3. The burner for a fuel reformer according to claim 1, wherein a drain discharge pipe is connected to the outer pipe.
JP2000241433A 2000-08-09 2000-08-09 Burner for fuel reformer Pending JP2002053302A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000241433A JP2002053302A (en) 2000-08-09 2000-08-09 Burner for fuel reformer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000241433A JP2002053302A (en) 2000-08-09 2000-08-09 Burner for fuel reformer

Publications (1)

Publication Number Publication Date
JP2002053302A true JP2002053302A (en) 2002-02-19

Family

ID=18732619

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000241433A Pending JP2002053302A (en) 2000-08-09 2000-08-09 Burner for fuel reformer

Country Status (1)

Country Link
JP (1) JP2002053302A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007157407A (en) * 2005-12-02 2007-06-21 Fuji Electric Holdings Co Ltd Fuel reforming system
JP2008019160A (en) * 2006-07-11 2008-01-31 Samsung Sdi Co Ltd Reformer burner
JP2008159373A (en) * 2006-12-22 2008-07-10 Matsushita Electric Works Ltd Hydrogen manufacturing device and fuel cell electric power generation system
KR100986598B1 (en) 2002-06-28 2010-10-11 산요덴키가부시키가이샤 Burner
WO2016181596A1 (en) * 2015-05-11 2016-11-17 パナソニック株式会社 Fuel cell system
EP3012529B1 (en) * 2013-06-18 2021-03-10 Panasonic Intellectual Property Management Co., Ltd. Power generation system and method for operating power generation system

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100986598B1 (en) 2002-06-28 2010-10-11 산요덴키가부시키가이샤 Burner
JP2007157407A (en) * 2005-12-02 2007-06-21 Fuji Electric Holdings Co Ltd Fuel reforming system
JP2008019160A (en) * 2006-07-11 2008-01-31 Samsung Sdi Co Ltd Reformer burner
JP2008159373A (en) * 2006-12-22 2008-07-10 Matsushita Electric Works Ltd Hydrogen manufacturing device and fuel cell electric power generation system
EP3012529B1 (en) * 2013-06-18 2021-03-10 Panasonic Intellectual Property Management Co., Ltd. Power generation system and method for operating power generation system
WO2016181596A1 (en) * 2015-05-11 2016-11-17 パナソニック株式会社 Fuel cell system
JPWO2016181596A1 (en) * 2015-05-11 2017-09-28 パナソニック株式会社 Fuel cell system

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