JPH07138001A - Vaporizer for fuel-reforming apparatus - Google Patents

Vaporizer for fuel-reforming apparatus

Info

Publication number
JPH07138001A
JPH07138001A JP5283336A JP28333693A JPH07138001A JP H07138001 A JPH07138001 A JP H07138001A JP 5283336 A JP5283336 A JP 5283336A JP 28333693 A JP28333693 A JP 28333693A JP H07138001 A JPH07138001 A JP H07138001A
Authority
JP
Japan
Prior art keywords
fuel
vaporizer
heated air
outer cylinder
reformer
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.)
Granted
Application number
JP5283336A
Other languages
Japanese (ja)
Other versions
JP3011590B2 (en
Inventor
Osamu Tajima
収 田島
Kazunari Okita
一成 大北
Mitsuo Karakane
光雄 唐金
Masatoshi Ueda
雅敏 上田
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 JP5283336A priority Critical patent/JP3011590B2/en
Publication of JPH07138001A publication Critical patent/JPH07138001A/en
Application granted granted Critical
Publication of JP3011590B2 publication Critical patent/JP3011590B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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

Landscapes

  • Hydrogen, Water And Hydrids (AREA)

Abstract

PURPOSE:To provide a vaporizer for a fuel-reforming apparatus excellent in efficiency of heat exchange between hot air and a liquid fuel and having a long service life and improve the reforming efficiency of the fuel-reforming apparatus. CONSTITUTION:In this fuel-reforming apparatus 1, a fuel pipeline 20 where a liquid fuel is allowed to pass is set in an outer cylinder 11 where hot air (X) is allowed to pass. The fuel pipeline 20 has a coiled-shape in which mutually adjacent fuel pipes are close to each other and the whole body has a cylindrical shape 21 along the inside wall of the outer cylinder 11. The cylindrical body 21 is equipped with the first partition plate 13 having a shape capable of clogging a gap between the cylindrical body 21 and the outer cylinder 11 along the inside wall of the outer cylinder 11 in the neighborhood of the hot air inlet side end. This cylindrical body 21 is also equipped with the second partition plate 12 having a shape capable of closing the opening part of the cylindrical body 21 in the neighborhood of the hot air outlet side end.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は燃料改質装置用気化器に
関し、特に燃料管路の改良に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a vaporizer for a fuel reformer, and more particularly to improvement of a fuel line.

【0002】[0002]

【従来の技術】燃料改質装置は、天然ガス、メタノー
ル、ナフサなどの液体燃料を改質して、水素リッチな改
質燃料を得る装置であり、得られた改質燃料は燃料電池
の燃料として利用される。燃料改質装置の構成は、燃料
の種類や処理する規模によって異なるが、メタノール燃
料を使用する燃料電池用改質装置の場合は、一般的に図
3に示すように断熱性の外容器102内において、空気
加熱用のバーナー104、加熱空気によって液体燃料を
加熱気化させる気化器110が収納され、その周りに触
媒層を有する複数の改質器130…が配置されている。
2. Description of the Related Art A fuel reformer is a device for reforming a liquid fuel such as natural gas, methanol or naphtha to obtain a hydrogen-rich reformed fuel. The reformed fuel obtained is a fuel for a fuel cell. Used as. The structure of the fuel reformer differs depending on the type of fuel and the scale of processing, but in the case of a fuel cell reformer that uses methanol fuel, generally, as shown in FIG. 2, a burner 104 for heating air, a vaporizer 110 for heating and vaporizing liquid fuel by heated air are housed, and a plurality of reformers 130 having a catalyst layer are arranged around the burner 104.

【0003】このような燃料改質装置において、液体燃
料が改質されるメカニズムは、まず含水メタノール等の
液体燃料が気化器110内に導かれる一方、バーナー1
04で加熱された加熱空気が、気化器110の断熱円筒
111内を通過し、上記液体燃料に熱を供給する。液体
燃料は、受けた熱により気化して気化燃料となり、気化
器110から排出された後、分岐管140を通って改質
器130…に送り込まれ、改質器130内の触媒層を通
過する。一方、気化器110の周囲を通過した加熱空気
は、改質器130…の周囲を通過しながら、余熱によっ
て改質器130を加熱する。改質器130内において
は、気化燃料が化学反応(改質反応)を起こし、水素リ
ッチな燃料ガスが生成される。
In such a fuel reformer, the mechanism of reforming the liquid fuel is such that the liquid fuel such as hydrous methanol is first introduced into the vaporizer 110, while the burner 1 is used.
The heated air heated in 04 passes through the heat insulating cylinder 111 of the vaporizer 110 and supplies heat to the liquid fuel. The liquid fuel is vaporized by the heat received to become vaporized fuel, is discharged from the vaporizer 110, is then sent to the reformers 130 through the branch pipe 140, and passes through the catalyst layer in the reformer 130. . On the other hand, the heated air that has passed around the vaporizer 110 heats the reformer 130 with residual heat while passing around the reformers 130 .... In the reformer 130, the vaporized fuel causes a chemical reaction (reforming reaction), and hydrogen-rich fuel gas is generated.

【0004】このような従来の気化器110内におい
て、主に熱交換が行われるところは、気化円筒管121
であって、加熱空気は、その内側面127の内側及び外
側面126と断熱円筒111の間を通過し、液体燃料
は、外側面126と内側面127に挟まれた円筒管路1
28を下るようになっている。この円筒管路128の中
には、熱交換の効率を良くするために、銅などからなる
リング状あるいはスパイラル状(図においてはリング
状)の金属伝熱体129が入れられており、円筒管路1
28内で液体燃料はこの金属伝熱体129を伝って流れ
流れながら熱を受けるようになっている。
In such a conventional vaporizer 110, a vaporizing cylindrical tube 121 is mainly used for heat exchange.
That is, the heated air passes between the inside and outside surfaces 126 of the inner side surface 127 and the heat insulating cylinder 111, and the liquid fuel passes through the cylindrical conduit 1 sandwiched between the outside surface 126 and the inner side surface 127.
It goes down 28. A ring-shaped or spiral (ring-shaped in the figure) metal heat transfer member 129 made of copper or the like is placed in the cylindrical pipe path 128 in order to improve heat exchange efficiency. Road 1
The liquid fuel in 28 receives heat while flowing through the metal heat transfer member 129.

【0005】[0005]

【発明が解決しようとする課題】従来の気化器110
は、上記のように、熱交換の効率をよくするための工夫
がなされてはいるが、加熱空気が上記の外側面126と
断熱円筒111との間隙、及び内側面127によって囲
まれる管路を直線的に通過してしまうので、通過する加
熱空気の一部は外側面126又は内側面127と接触せ
ずに通り過ぎてしまう他、加熱空気から断熱円筒111
への熱の損失もあり、加熱空気の熱が十分に液体燃料の
気化に利用されないまま気化器110から放出されると
いう問題があった。
A conventional carburetor 110 is used.
Has been devised to improve the efficiency of heat exchange, as described above, but the heated air flows through the gap between the outer surface 126 and the heat insulating cylinder 111, and the conduit surrounded by the inner surface 127. Since it passes straightly, a part of the heated air passing therethrough passes without coming into contact with the outer side surface 126 or the inner side surface 127, and also the heat insulating cylinder 111 from the heated air.
There is also a problem that heat of the heated air is released from the vaporizer 110 without being sufficiently utilized for vaporizing the liquid fuel.

【0006】また、改質反応がよくなされるためには、
改質器130に入る気化燃料の温度がある程度高温でな
ければならないので、上記のように気化器における熱損
失が大きい場合、それを補うためバーナーでの燃焼を大
きくしなくてはならず、結果的に燃料のロスが大きくな
っていた。例えば、このような燃料改質装置を燃料電池
に使用する場合、通常、改質燃料を燃料電池で使用した
残りの排ガスをバーナーの燃料として使うが、メタノー
ル水溶液を改質して生じた改質燃料の内、40%程度し
か燃料電池に利用できず、残りはバーナーでの燃焼に使
用されるという結果を招いていた。
In order to improve the reforming reaction,
Since the temperature of the vaporized fuel entering the reformer 130 must be high to some extent, if the heat loss in the vaporizer is large as described above, combustion in the burner must be increased to compensate for it, resulting in The loss of fuel was increasing. For example, when such a fuel reformer is used in a fuel cell, normally, the remaining exhaust gas used in the fuel cell as reformed fuel is used as the fuel for the burner. Only about 40% of the fuel can be used in the fuel cell, and the rest is used for combustion in the burner.

【0007】また、上記のように、燃料改質装置用気化
器内にリング状の金属伝熱体を使用する場合、このリン
グ状の金属伝熱体が多数積み重ねられているため、装置
を繰り返して使用するうちに、割れが生じやすいという
問題、即ち燃料改質装置用気化器の劣化の問題もあっ
た。本発明は上記課題に鑑みて、加熱空気と液体燃料の
熱交換の効率がよく、合わせて耐久性の優れた燃料改質
装置用気化器を提供し、燃料改質装置の改質効率を向上
させることを目的とする。
Further, as described above, when a ring-shaped metal heat transfer body is used in the vaporizer for a fuel reformer, since the ring-shaped metal heat transfer bodies are stacked in large numbers, the apparatus is repeated. There was also a problem that cracks are likely to occur during use as a result, that is, deterioration of the vaporizer for the fuel reformer. In view of the above problems, the present invention provides a vaporizer for a fuel reformer, which has high efficiency of heat exchange between heated air and liquid fuel, and also has excellent durability, and improves the reforming efficiency of the fuel reformer. The purpose is to let.

【0008】[0008]

【課題を解決するための手段】本発明は上記課題を解決
するため、加熱空気がその中を通過する外筒の中に、液
体燃料が通過する燃料管路が設置された燃料改質装置用
気化器において、燃料管路は、隣合う燃料管路同志が近
接するコイル状であり、かつ全体が前記外筒の内壁に沿
った筒体を形成する燃料管路であって、筒体の加熱空気
入口側の端近傍には、外筒の内壁に沿って、筒体と外筒
との間隙を塞ぐ形状の第1の仕切り板を備え、筒体の加
熱空気出口側の端近傍には、筒体の口を塞ぐ形状の第2
の仕切り板を備えることを特徴とする。
In order to solve the above problems, the present invention is for a fuel reformer in which a fuel pipe through which liquid fuel passes is installed in an outer cylinder through which heated air passes. In the carburetor, the fuel pipeline is a coil shape in which adjacent fuel pipelines are adjacent to each other, and is a fuel pipeline that entirely forms a tubular body along the inner wall of the outer cylinder, and the heating of the tubular body is performed. A first partition plate having a shape that closes the gap between the cylinder and the outer cylinder is provided near the end on the air inlet side along the inner wall of the outer cylinder, and near the end on the heated air outlet side of the cylinder, Second shape that closes the mouth of the cylinder
It is characterized by including a partition plate.

【0009】[0009]

【作用】上記構成の燃料改質装置用気化器であれば、液
体燃料が通過する燃料管路は、全体が外筒の内壁に沿っ
た筒体を形成するので、外筒を通過する加熱空気は、こ
の筒体を通り抜ける方向に流れる。筒体の加熱空気入口
側の端近傍に備えられた第一の仕切り板は、外筒の内壁
に沿って、筒体と外筒との間隙を塞ぐ形状であるので、
加熱空気は、第1の仕切り板によって、流れが規制さ
れ、筒体の内側に入り込むように流れる。また、筒体の
加熱空気出口側の端近傍に備えられた第2の仕切り板
は、筒体の口を塞ぐ形状であるので、筒体の内側に入り
込んだ加熱空気は、そのまま筒体の内側を抜け出ること
はできない。
In the carburetor for a fuel reformer having the above-described structure, the entire fuel pipe line through which the liquid fuel passes forms a cylinder along the inner wall of the outer cylinder, so that the heating air passing through the outer cylinder is heated. Flows in a direction passing through this cylinder. The first partition plate provided near the end of the tubular body on the heated air inlet side has a shape that closes the gap between the tubular body and the outer barrel along the inner wall of the outer barrel.
The flow of the heated air is regulated by the first partition plate and flows so as to enter the inside of the cylindrical body. Further, since the second partition plate provided near the end on the heated air outlet side of the tubular body has a shape that closes the mouth of the tubular body, the heated air that has entered the inside of the tubular body remains inside the tubular body. You can't get out.

【0010】ここで、燃料管路は、コイル状であるの
で、上記の筒体の内側に入り込んだ加熱空気は、燃料管
路と燃料管路の隙間を通って、筒体の外側へ抜けでるこ
とになる。そして、隣合う燃料管路同志は近接している
ので、加熱空気が燃料管路と燃料管路の隙間を通過する
とき、燃料管路と接触する。従って、加熱空気が筒体を
通過する間において、必ず燃料管路と接触し、熱交換が
有効に行われる。また、加熱空気が筒体を通過する間に
おいて、この隙間を通過する前には、外筒に接触するこ
とはないので、外筒への熱の損失を防ぐことができる。
Since the fuel pipe has a coil shape, the heated air that has entered the inside of the cylinder passes through the gap between the fuel pipe and the fuel pipe and escapes to the outside of the cylinder. It will be. Since the adjacent fuel pipes are close to each other, the heated air comes into contact with the fuel pipes when passing through the gap between the fuel pipes. Therefore, while the heated air passes through the tubular body, it always comes into contact with the fuel pipeline, and heat exchange is effectively performed. Further, since the heated air does not come into contact with the outer cylinder before passing through the gap while the heated air passes through the cylindrical body, heat loss to the outer cylinder can be prevented.

【0011】また、燃料管路は、コイル形状の管路であ
るため、一本の管を巻くことにより形成することがで
き、耐久性に問題のあるリング状あるいはスパイラル状
の金属伝熱体を用いる必要がない。
Further, since the fuel pipeline is a coil-shaped pipeline, it can be formed by winding a single pipe, and a ring-shaped or spiral-shaped metal heat transfer body having a problem of durability is formed. No need to use.

【0012】[0012]

【実施例】【Example】

(実施例)図1は、本発明の一実施例に係わる燃料改質
装置の斜視図(一部断面)である。この燃料改質装置1
は、外部の燃料電池(不図示)に改質燃料を供給するも
のである。
(Embodiment) FIG. 1 is a perspective view (partial cross section) of a fuel reformer according to an embodiment of the present invention. This fuel reformer 1
Is for supplying reformed fuel to an external fuel cell (not shown).

【0013】燃料改質装置1は、断熱材からなる円筒型
状の外容器2の中に、装置本体が収納されており、大き
さは、例えば高さ600mm、直径300mmである。
装置本体は、空気を加熱する円筒形のバーナー4が外容
器2の底面3上の中央部に設置され、加熱空気によって
液体燃料を気化させる円筒形の気化器10がバーナー4
の上に設置され、気化燃料を改質する4本の円筒状の改
質器30…が気化器10の周囲に設置され、気化器10
から出た気化燃料を改質器30…に分岐する分岐管40
が気化器10の上方に設置されて構成されている。
The fuel reforming apparatus 1 has a main body housed in a cylindrical outer container 2 made of a heat insulating material, and has a size of, for example, 600 mm in height and 300 mm in diameter.
In the apparatus main body, a cylindrical burner 4 for heating air is installed in the central portion on the bottom surface 3 of the outer container 2, and a cylindrical vaporizer 10 for vaporizing liquid fuel by the heated air is provided by the burner 4
Are installed on the upper part of the carburetor, and four cylindrical reformers 30 ... Reforming vaporized fuel are installed around the carburetor 10.
Branch pipe 40 for branching vaporized fuel from the reformer 30 ...
Is installed above the vaporizer 10.

【0014】バーナー4は、定常運転時においては、燃
料改質装置1から出た水素リッチな改質燃料を外部の燃
料電池で使用した残りの燃料排ガスを燃焼させることに
よって、底面3を下から上へ貫通してバーナー4に連通
する燃焼空気用配管5からバーナー4内に吹き込まれる
空気を加熱し、上方に加熱空気を吹き出すようになって
いる。また、初期運転時においては、燃焼量を増やすた
めに液体燃料の一部を補助的に燃焼させることができる
ようになっている。このようにしてバーナー4で加熱さ
れた加熱空気は、円筒形の気化器10に吹き入れられ
る。
During steady operation, the burner 4 burns the hydrogen-rich reformed fuel discharged from the fuel reforming apparatus 1 with the remaining fuel exhaust gas used in the external fuel cell, so that the bottom surface 3 is pushed from below. The air blown into the burner 4 from the combustion air pipe 5 penetrating upward and communicating with the burner 4 is heated, and the heated air is blown upward. In addition, during the initial operation, part of the liquid fuel can be supplementarily burned in order to increase the amount of combustion. The heated air thus heated by the burner 4 is blown into the cylindrical vaporizer 10.

【0015】気化器10は、バーナー4から送られた加
熱空気の上方への通路を形成する円筒状の断熱円筒11
が、バーナー4の上に設置されており、その断熱円筒1
1の中に、液体燃料が通過するコイル状の燃料管路20
が設置されて構成されている。この燃料管路20は、断
熱円筒11の内壁に沿った円筒管状の主コイル部21
と、この主コイル部21とバーナー4との間に形成され
たスパイラル部22と、主コイル部21の中央を上下に
通る直管23とが、連続して形成されており、気化器1
0の上方から燃料管路20に入れられた液体燃料は、主
コイル部21を下りながら加熱空気によって加熱されて
気化し、さらにスパイラル部22を通過し直管23を上
昇する間に加熱され、高温の気化燃料として気化器10
の上部から排出される。
The carburetor 10 has a cylindrical heat insulating cylinder 11 which forms an upward passage of the heated air sent from the burner 4.
Is installed on the burner 4, and its insulating cylinder 1
1, a coiled fuel conduit 20 through which liquid fuel passes
Is installed and configured. The fuel line 20 includes a cylindrical tubular main coil portion 21 along the inner wall of the heat insulating cylinder 11.
The spiral portion 22 formed between the main coil portion 21 and the burner 4 and the straight pipe 23 passing vertically through the center of the main coil portion 21 are continuously formed, and the vaporizer 1
The liquid fuel that has entered the fuel conduit 20 from above 0 is vaporized by being heated by the heated air while descending the main coil portion 21, further heated while passing through the spiral portion 22 and rising in the straight pipe 23, Vaporizer 10 as high temperature vaporized fuel
Is discharged from above.

【0016】4方向に分岐する分岐管40は、気化器1
0の上部から排出された気化燃料を均等に分岐して、4
つの改質器30…に導く。4本の円筒状の改質器30
は、断熱円筒11と外容器2の側面に挟まれた空間に、
断熱円筒11を取り囲むように配置されている。この改
質器30は、金属の円筒容器の中に、改質用触媒(例え
ば、市販の銅/亜鉛系メタノール改質用触媒)が詰めら
れて触媒層31が形成されているものである。改質器3
0…の下部は、底面3を貫通して合流管32と連通し、
合流管32は外部の燃料電池と連通している。従って、
分岐管40から改質器30…の上部に入った気化燃料
は、触媒層31…を下降しながら改質反応を起こして改
質燃料となり、合流管32で集められて、外部の燃料電
池に送られる。
The branch pipe 40 that branches in four directions is a carburetor 1.
The vaporized fuel discharged from the upper part of 0 is evenly divided into 4
One reformer 30 ... Four cylindrical reformer 30
Is a space between the heat insulating cylinder 11 and the side surface of the outer container 2,
It is arranged so as to surround the heat insulating cylinder 11. In the reformer 30, a catalyst layer 31 is formed by packing a reforming catalyst (for example, a commercially available copper / zinc-based methanol reforming catalyst) in a metal cylindrical container. Reformer 3
The lower part of 0 ... penetrates the bottom surface 3 and communicates with the confluence pipe 32,
The merging pipe 32 communicates with an external fuel cell. Therefore,
The vaporized fuel that has entered the upper portion of the reformer 30 from the branch pipe 40 causes a reforming reaction while descending in the catalyst layers 31 to become reformed fuel, which is collected by the confluent pipe 32 and is supplied to an external fuel cell. Sent.

【0017】図2は、気化器10の要部断面図である。
上記気化器10において、燃料管路20は、一本のステ
ンレス管(外径9.5mm)で形成されており、主コイ
ル部21は、図2に示すように外径100mm、高さ1
90mmの円筒管状であって、コイル全長約5m、コイ
ル巻数18巻、隣合う管と管の間隔が1mmである。ま
た、主コイル部21の上端には、この円筒管状の主コイ
ル部21上面を覆う円板状の上仕切板12が設置され、
主コイル部21の下端には、主コイル部21と断熱円筒
11との間の間隙を覆うドーナツ状の下仕切板13が設
置されている。
FIG. 2 is a sectional view of the main part of the vaporizer 10.
In the carburetor 10, the fuel conduit 20 is formed of a single stainless steel pipe (outer diameter 9.5 mm), and the main coil portion 21 has an outer diameter 100 mm and a height 1 as shown in FIG.
It is a cylindrical tube of 90 mm, the total length of the coil is about 5 m, the number of coil turns is 18, and the interval between adjacent tubes is 1 mm. Further, at the upper end of the main coil portion 21, a disc-shaped upper partition plate 12 that covers the upper surface of the cylindrical tubular main coil portion 21 is installed,
At the lower end of the main coil portion 21, a donut-shaped lower partition plate 13 that covers the gap between the main coil portion 21 and the heat insulating cylinder 11 is installed.

【0018】図1及び図2中において、矢印Xは加熱空
気の流れを示し、矢印Yは、液体燃料または気化燃料ま
たは改質燃料の流れを示している。図に示されるよう
に、上記のような気化器10の構造により、断熱円筒1
1内を上昇する加熱空気は、主コイル部21の下端にお
いて、下仕切板13により、主コイル部21と断熱円筒
11との間の外側空間24へ直接流れ込むことができな
いよう規制されているため、下仕切板13の内側を通っ
て主コイル部21の内側空間25に流れ込む。一方、主
コイル部21の上端において、上仕切板12により内側
空間25から直接上へ抜けでることができないよう規制
されているので、主コイル部21の内側空間25に流れ
込んだ上記加熱空気は、主コイル部21の隣合うステン
レス管の間隙26…を通って、外側空間24に抜け出
し、上仕切板12と断熱円筒11の間を通って上方へ抜
ける。従って、気化器10を通過する加熱空気は、必
ず、液体燃料が中を流れる管と管に挟まれた間隙26…
を通過することとなる。この間隙26…は1mmしかな
いので、加熱空気が間隙26…を通過するときに、燃料
管路20と接触し、加熱空気と液体燃料との効率的な熱
交換がなされる。
1 and 2, the arrow X indicates the flow of heated air, and the arrow Y indicates the flow of liquid fuel, vaporized fuel or reformed fuel. As shown in the figure, the heat insulating cylinder 1 has the structure of the vaporizer 10 as described above.
Since the heated air rising inside 1 is prevented from directly flowing into the outer space 24 between the main coil portion 21 and the heat insulating cylinder 11 by the lower partition plate 13 at the lower end of the main coil portion 21. , And flows into the inner space 25 of the main coil portion 21 through the inside of the lower partition plate 13. On the other hand, at the upper end of the main coil portion 21, the upper partition plate 12 is regulated so as not to be able to directly escape upward from the inner space 25. Therefore, the heated air flowing into the inner space 25 of the main coil portion 21 is It passes through the gaps 26 between adjacent stainless steel pipes of the main coil portion 21 and escapes to the outer space 24, and then passes upward between the upper partition plate 12 and the heat insulating cylinder 11. Therefore, the heated air passing through the carburetor 10 is always a pipe in which the liquid fuel flows, and a gap 26 sandwiched between the pipes.
Will pass through. Since the gaps 26 ... Are only 1 mm, when the heated air passes through the gaps 26 ..., the heated air comes into contact with the fuel conduit 20 and efficient heat exchange between the heated air and the liquid fuel is performed.

【0019】(比較例)図3は、従来の燃料改質装置の
一例を示す概略斜視図(一部断面)である。この燃料改
質装置101は、実施例の円筒型外容器2と同様の外容
器102内に、装置本体が収納されており、装置本体
は、外容器102の上面103の下に設置された空気加
熱用のバーナー104と、このバーナー104の下に設
置された円筒形の気化器110と、気化器110の周囲
に設置された改質器130…と、気化器110の下方に
設置された分岐管140とにより構成されている。
(Comparative Example) FIG. 3 is a schematic perspective view (partial cross section) showing an example of a conventional fuel reformer. This fuel reforming apparatus 101 has an apparatus main body housed in an outer container 102 similar to the cylindrical outer container 2 of the embodiment, and the apparatus main body is air installed below an upper surface 103 of the outer container 102. A burner 104 for heating, a cylindrical vaporizer 110 installed under the burner 104, a reformer 130 installed around the vaporizer 110, and a branch installed below the vaporizer 110. It is composed of a tube 140.

【0020】バーナー104は、実施例のバーナー4と
同様の機能を持つものであるが、空気を上方の燃焼空気
用配管105から取入れ、加熱空気を下方へ吹き出す。
気化器110は、加熱空気の通路を形成する断熱円筒1
11の中に、液体燃料が通過する気化円筒管121と、
スパイラル部122と、気化円筒管121の中央を上下
に通る直管123・124とが連通して形成されてお
り、気化器110の上部パイプ125から気化円筒管1
21に入れられた液体燃料は、気化円筒管121内を下
った後、直管124を上昇してスパイラル部122を通
過し、直管123を降下する間に加熱空気によって加熱
され気化燃料となり、気化器110の下方へ排出され
る。
The burner 104 has the same function as the burner 4 of the embodiment, but takes in air from the upper combustion air pipe 105 and blows heated air downward.
The vaporizer 110 is a heat insulating cylinder 1 that forms a passage for heated air.
11, a vaporization cylindrical tube 121 through which liquid fuel passes,
The spiral portion 122 and the straight pipes 123 and 124 passing vertically through the center of the vaporization cylindrical pipe 121 are formed to communicate with each other, and the upper pipe 125 of the vaporizer 110 is connected to the vaporization cylindrical pipe 1.
The liquid fuel put in 21 goes down the inside of the vaporizing cylindrical pipe 121, rises in the straight pipe 124, passes through the spiral portion 122, and is heated by heated air while descending the straight pipe 123 to become vaporized fuel, It is discharged below the vaporizer 110.

【0021】分岐管140、改質器130…、集合管1
32は、それぞれ上記実施例の分岐管140、改質器1
30…、集合管132と同様の機能を有し、気化器11
0から出た気化燃料は、分岐管140から改質器130
…のに入った気化燃料は、改質反応を起こして改質燃料
となり、合流管132で集められて、外部の燃料電池に
送られる。
Branch pipe 140, reformer 130 ..., Collecting pipe 1
32 is the branch pipe 140 and the reformer 1 of the above embodiment, respectively.
30 ..., having the same function as the collecting pipe 132,
The vaporized fuel that has flowed out of 0 is supplied from the branch pipe 140 to the reformer 130.
The vaporized fuel that has entered the ... causes a reforming reaction to become reformed fuel, which is collected by the confluence pipe 132 and sent to the external fuel cell.

【0022】上記気化器110において、気化円筒管1
21は、外側面126と内側面127を有し、その外側
面126と断熱円筒111との間隙、及び内側面127
によって囲まれる管路を加熱空気が上から下へ通過す
る。一方、パイプ124から気化円筒管に入った液体燃
料は、外側面126と内側面127に挟まれた円筒管路
128内を降下しながら、加熱空気から熱を受ける。こ
こで、円筒管路128の中には熱交換の効率を良くする
ために、銅などからなるリング状あるいはスパイラル状
(図においてはリング状)の金属伝熱体129が積み重
ねて入れられている。円筒管路128内を下降するメタ
ノール燃料は、この金属伝熱体129を上から順に伝っ
て流れ落ちるので、加熱空気から熱を受けやすくなって
いる。
In the vaporizer 110, the vaporizing cylindrical tube 1
21 has an outer side surface 126 and an inner side surface 127, and a gap between the outer side surface 126 and the heat insulating cylinder 111, and an inner side surface 127.
The heated air passes from top to bottom in a line surrounded by. On the other hand, the liquid fuel that has entered the vaporized cylindrical pipe from the pipe 124 receives heat from the heated air while descending in the cylindrical conduit 128 sandwiched between the outer surface 126 and the inner surface 127. Here, in order to improve the efficiency of heat exchange, a ring-shaped or spiral (ring-shaped in the figure) metal heat transfer member 129 made of copper or the like is stacked in the cylindrical conduit 128. . Since the methanol fuel descending in the cylindrical pipe 128 flows down along the metal heat transfer member 129 in order from the top, it is easy to receive heat from the heated air.

【0023】[実験]上記実施例の燃料改質装置1と比
較例の燃料改質装置101を用いて、所定の条件でメタ
ノール水溶液の改質を行い、実施例の気化器10と比較
例の気化器110の受熱効率を比較するテストを行っ
た。燃料改質装置の運転条件は、気化器10及び気化器
110に供給されるメタノールの供給速度を80ml/mi
nとし、また、バーナー4及びバーナー104の燃焼熱
量を44.3kcal/minとした。そのテスト結果を表1
に示す。
[Experiment] Using the fuel reforming apparatus 1 of the above embodiment and the fuel reforming apparatus 101 of the comparative example, an aqueous methanol solution was reformed under predetermined conditions, and the vaporizer 10 of the embodiment and the comparative example were compared. A test was conducted to compare the heat receiving efficiency of the vaporizer 110. The operating condition of the fuel reformer is that the supply rate of methanol supplied to the vaporizer 10 and the vaporizer 110 is 80 ml / mi.
Further, the heat of combustion of the burner 4 and the burner 104 was set to 44.3 kcal / min. The test results are shown in Table 1.
Shown in.

【0024】[0024]

【表1】 [Table 1]

【0025】表1からわかるように、燃料改質装置1は
燃料改質装置101と比べて、液体燃料の受熱効率、即
ちバーナーの燃焼熱量に対する液体燃料の受熱量が大き
く向上している。これは、気化器10が気化器110と
比べて、熱交換の効率が向上したためであると考えられ
る。また、このように熱交換の効率が向上した主な理由
は、上述したように気化器10を通過する加熱空気が、
必ず狭い間隙26…を通過し、そのとき液体燃料が中を
流れる管と接触するためであると考えられる。
As can be seen from Table 1, in the fuel reformer 1, the heat receiving efficiency of the liquid fuel, that is, the heat receiving amount of the liquid fuel with respect to the combustion heat quantity of the burner is greatly improved as compared with the fuel reformer 101. It is considered that this is because the vaporizer 10 has improved heat exchange efficiency as compared with the vaporizer 110. In addition, the main reason why the efficiency of heat exchange is improved is that the heated air passing through the vaporizer 10 is
It is considered that this is because the liquid fuel always passes through the narrow gaps 26, and at that time, the liquid fuel comes into contact with the pipe flowing therein.

【0026】なお、上記実施例の燃料改質装置1は、バ
ーナー4が下部に設置されているが、上部に設置されて
いる場合であっても、気化器10の受熱効率に関しては
同様の効果が得られる。また、上記実施例においては、
気化器10は円筒形であり、主コイル部21は円筒管状
であるが、角型の気化器及び角筒形の主コイル部であっ
ても同様に実施することができる。また、上記実施例で
は、液体燃料としてメタノールを用いる例を示したが、
天然ガス、ナフサ等においても同様の効果を得ることが
できる。
In the fuel reformer 1 of the above embodiment, the burner 4 is installed in the lower part, but even when the burner 4 is installed in the upper part, the same effect is obtained with respect to the heat receiving efficiency of the carburetor 10. Is obtained. Further, in the above embodiment,
The carburetor 10 has a cylindrical shape and the main coil portion 21 has a cylindrical tubular shape, but the same can be applied to a rectangular vaporizer and a rectangular tube-shaped main coil portion. Further, in the above embodiment, an example in which methanol is used as the liquid fuel has been shown,
Similar effects can be obtained with natural gas, naphtha, and the like.

【0027】[0027]

【発明の効果】以上の本発明によれば、加熱空気と液体
燃料の熱交換の効率がよく、合わせて耐久性の優れた燃
料改質装置用気化器を提供することができる。この燃料
改質装置用気化器は、燃料改質装置の改質効率を向上す
るので、燃料電池等に用いると液体燃料を節減でき経済
的である。
As described above, according to the present invention, it is possible to provide a vaporizer for a fuel reformer, which has a high efficiency of heat exchange between the heated air and the liquid fuel and is also excellent in durability. Since this fuel reformer vaporizer improves the reforming efficiency of the fuel reformer, it is economical because it can save liquid fuel when used in a fuel cell or the like.

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

【図1】本発明の一実施例に係わる燃料改質装置の斜視
図(一部断面)である。
FIG. 1 is a perspective view (partial cross section) of a fuel reformer according to an embodiment of the present invention.

【図2】気化器10の要部断面図である。FIG. 2 is a sectional view of a main part of the vaporizer 10.

【図3】従来の燃料改質装置の一例を示す概略斜視図
(一部断面)である。
FIG. 3 is a schematic perspective view (partial cross section) showing an example of a conventional fuel reformer.

【符号の説明】[Explanation of symbols]

10 気化器 11 断熱円筒 12 上仕切板 13 下仕切板 20 燃料管路 21 主コイル部 10 Vaporizer 11 Insulating cylinder 12 Upper partition plate 13 Lower partition plate 20 Fuel line 21 Main coil part

───────────────────────────────────────────────────── フロントページの続き (72)発明者 上田 雅敏 守口市京阪本通2丁目5番5号 三洋電機 株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Masatoshi Ueda 2-5-5 Keihan Hondori, Moriguchi City Sanyo Electric Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 加熱空気がその中を通過する外筒の中
に、液体燃料が通過する燃料管路が設置された燃料改質
装置用気化器において、 前記燃料管路は、隣合う燃料管路同志が近接するコイル
状であり、かつ全体が前記外筒の内壁に沿った筒体を形
成する燃料管路であり、 前記筒体の加熱空気入口側の端近傍には、前記外筒の内
壁に沿って、前記筒体と外筒との間隙を塞ぐ形状の第1
の仕切り板を備え、 前記筒体の加熱空気出口側の端近傍には、前記筒体の口
を塞ぐ形状の第2の仕切り板を備えることを特徴とする
燃料改質装置用気化器。
1. A carburetor for a fuel reformer in which a fuel pipe through which liquid fuel passes is installed in an outer cylinder through which heated air passes, wherein the fuel lines are adjacent fuel pipes. The fuel tubes are coiled so that the passages are in close proximity to each other, and the whole forms a cylinder along the inner wall of the outer cylinder, and in the vicinity of the end on the heated air inlet side of the cylinder, the outer cylinder A first shape that closes the gap between the cylindrical body and the outer cylinder along the inner wall
And a second partition plate having a shape that closes the mouth of the tubular body in the vicinity of the end of the tubular body on the heated air outlet side.
JP5283336A 1993-11-12 1993-11-12 Vaporizer for fuel reformer Expired - Lifetime JP3011590B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5283336A JP3011590B2 (en) 1993-11-12 1993-11-12 Vaporizer for fuel reformer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5283336A JP3011590B2 (en) 1993-11-12 1993-11-12 Vaporizer for fuel reformer

Publications (2)

Publication Number Publication Date
JPH07138001A true JPH07138001A (en) 1995-05-30
JP3011590B2 JP3011590B2 (en) 2000-02-21

Family

ID=17664162

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5283336A Expired - Lifetime JP3011590B2 (en) 1993-11-12 1993-11-12 Vaporizer for fuel reformer

Country Status (1)

Country Link
JP (1) JP3011590B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004319330A (en) * 2003-04-17 2004-11-11 Idemitsu Kosan Co Ltd Vaporization method of kerosene fuel for fuel cell
KR100834102B1 (en) * 2007-04-26 2008-06-02 한국기계연구원 Fuel vaporizer

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102218416B1 (en) * 2019-10-07 2021-02-22 주식회사 세원계전 Vaporization device liquefied gas

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004319330A (en) * 2003-04-17 2004-11-11 Idemitsu Kosan Co Ltd Vaporization method of kerosene fuel for fuel cell
JP4634013B2 (en) * 2003-04-17 2011-02-16 出光興産株式会社 Kerosene fuel vaporization method for fuel cells
KR100834102B1 (en) * 2007-04-26 2008-06-02 한국기계연구원 Fuel vaporizer

Also Published As

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