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JPH0425059B2 - - Google Patents
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JPH0425059B2 - - Google Patents

Info

Publication number
JPH0425059B2
JPH0425059B2 JP59263904A JP26390484A JPH0425059B2 JP H0425059 B2 JPH0425059 B2 JP H0425059B2 JP 59263904 A JP59263904 A JP 59263904A JP 26390484 A JP26390484 A JP 26390484A JP H0425059 B2 JPH0425059 B2 JP H0425059B2
Authority
JP
Japan
Prior art keywords
combustion chamber
tube
reaction
reaction tube
alcohol
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP59263904A
Other languages
Japanese (ja)
Other versions
JPS61141927A (en
Inventor
Takashi Oochi
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.)
Fuji Electric Co Ltd
Original Assignee
Fuji 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 Fuji Electric Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP26390484A priority Critical patent/JPS61141927A/en
Publication of JPS61141927A publication Critical patent/JPS61141927A/en
Publication of JPH0425059B2 publication Critical patent/JPH0425059B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J12/00Chemical processes in general for reacting gaseous media with gaseous media; Apparatus specially adapted therefor
    • B01J12/005Chemical processes in general for reacting gaseous media with gaseous media; Apparatus specially adapted therefor carried out at high temperatures, e.g. by pyrolysis

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Hydrogen, Water And Hydrids (AREA)

Description

【発明の詳細な説明】 〔発明の属する技術分野〕 本発明はアルコールと水とを加熱して反応させ
水素ガスを生成するアルコール改質器に関する。
DETAILED DESCRIPTION OF THE INVENTION [Technical field to which the invention pertains] The present invention relates to an alcohol reformer that heats and reacts alcohol and water to generate hydrogen gas.

〔従来技術とその問題点〕[Prior art and its problems]

水素ガスを生成する方法としてアルコールと水
とを加熱して水素ガスを含有したガスを生成する
改質器が知られている。以下従来の改質器につい
て図面を用いて説明する。
As a method for producing hydrogen gas, a reformer is known that heats alcohol and water to produce a gas containing hydrogen gas. A conventional reformer will be described below with reference to the drawings.

第3図は従来の改質器の要部構造の断面図であ
り、第4図は第3図のC−C断面図である。第3
図において燃料と燃焼空気との図示しない送出口
を備えたバーナ8が燃焼室1の燃焼室上部壁1a
の中央に設けられている。さらに燃焼室上部壁1
aには改質されて生成した水素含有ガスを排出す
る排出マニホールド17が設けられている。排出
マニホールド17には改質用触媒9、例えば酸化
銅と酸化亜鉛の微粉末を充填した反応管が燃焼室
胴壁1cに沿つて第4図に示すように複数個鉛直
に配列されている。そして各反応管2の底部の開
口にピツグテイル15を接続し、これらのピツク
テイル15の他端をマニホールドとしてのヘツダ
16に接続し、ヘツダ16の底部の開口に接続す
る改質燃料入口管12を燃焼室下部壁1bに貫通
させている。燃焼室1内にはバーナ8からの火焔
8aを覆うように通風ガイド7を設けて燃料ガス
を案内し、燃焼室胴壁1cには燃焼ガスの出口1
1を設けている。
FIG. 3 is a sectional view of the main structure of a conventional reformer, and FIG. 4 is a sectional view taken along the line CC in FIG. Third
In the figure, a burner 8 equipped with an outlet (not shown) for supplying fuel and combustion air is connected to an upper wall 1a of the combustion chamber 1.
is located in the center of the Furthermore, the combustion chamber upper wall 1
A is provided with an exhaust manifold 17 for discharging the reformed and generated hydrogen-containing gas. In the exhaust manifold 17, a plurality of reforming catalysts 9, such as reaction tubes filled with fine powders of copper oxide and zinc oxide, are arranged vertically along the combustion chamber body wall 1c as shown in FIG. Then, a pigtail 15 is connected to the opening at the bottom of each reaction tube 2, the other end of these picktails 15 is connected to a header 16 as a manifold, and the reformed fuel inlet pipe 12 connected to the opening at the bottom of the header 16 is used for combustion. It penetrates the lower room wall 1b. A ventilation guide 7 is provided in the combustion chamber 1 to cover the flame 8a from the burner 8 to guide the fuel gas, and an outlet 1 for the combustion gas is provided in the combustion chamber body wall 1c.
1 is provided.

上記の構造により改質燃料入口管12にアルコ
ール、例えばメタノールと水との混合液を送入
し、ヘツダ16を介して各反応管2内に送入し、
バーナ8により燃焼した火焔および燃焼ガスによ
り反応管2の温度を約250℃程度に上昇させると
触媒の作用の下に反応管中で改質反応が促進され
て水素が生成され、同時に生成される炭酸ガス等
とともにマニホールド17を介して改質ガス出口
13から水素含有ガスを取出すことができる。
With the above structure, alcohol, for example, a mixture of methanol and water is fed into the reformed fuel inlet pipe 12 and into each reaction tube 2 via the header 16.
When the temperature of the reaction tube 2 is raised to about 250°C by the flame and combustion gas burned by the burner 8, the reforming reaction is promoted in the reaction tube under the action of the catalyst and hydrogen is generated at the same time. Hydrogen-containing gas can be taken out from the reformed gas outlet 13 through the manifold 17 along with carbon dioxide and the like.

ところで、この場合反応管2と燃焼室胴壁1c
とは燃焼に伴う温度差、あるいは各反応管相互の
温度差に起因する熱膨脹差が生じるが、この熱膨
脹差はピツクテイル15に吸収させている。この
ためピツクテイル15は靭性に富む耐食性の材料
からなり、剛性の低い構造としている。
By the way, in this case, the reaction tube 2 and the combustion chamber body wall 1c
A difference in thermal expansion occurs due to a temperature difference due to combustion or a difference in temperature between the reaction tubes, but this difference in thermal expansion is absorbed by the picktail 15. For this reason, the picktail 15 is made of a material with high toughness and corrosion resistance, and has a structure with low rigidity.

しかしながら改質器を小型にする場合、ピツグ
テイル15を反応管2やヘツダ16に気密溶接す
る必要があるが、小型のためスペースが充分とさ
れないので気密溶接作業が困難となり、溶接部の
信頼性が低下するという問題がある。またピツグ
テイル15の長さも小型のため熱膨脹差を吸収す
るに必要な程充分にとれないという問題もある。
However, when making the reformer smaller, it is necessary to hermetically weld the pigtail 15 to the reaction tube 2 and header 16, but since there is not enough space due to the small size, it is difficult to perform airtight welding, and the reliability of the welded part is reduced. There is a problem with the decline. There is also the problem that the length of the pigtail 15 is not long enough to absorb the difference in thermal expansion due to its small size.

〔発明の目的〕[Purpose of the invention]

本発明は、前述のような点に鑑み、熱膨脹差を
吸収でき、しかも小型にすることのできるアルコ
ール改質器を提供することを目的とする。
In view of the above-mentioned points, it is an object of the present invention to provide an alcohol reformer that can absorb differences in thermal expansion and can be made smaller.

〔発明の要旨〕[Summary of the invention]

上記の目的は、本発明によれば燃焼室内に触媒
を充填した複数の反応管を鉛直に配し、この反応
管に連通する供給、排出マニホールドを介してこ
の反応管に通流するアルコールと水との混合液か
ら水素含有ガスを生成するアルコール改質器にお
いて、前記反応管の上、下端に弾性を有する管板
をそれぞれ設け、前記管板を覆つてそれぞれ供
給、排出マニホールドを配設し、前記反応管の両
端に設けた管板の周縁部を燃焼室胴壁に固定して
取付け、該燃焼室胴壁を前記反応管の中心線に直
角方向に二分し、該個所にベローズを挿着したこ
とにより達成される。
According to the present invention, a plurality of reaction tubes filled with catalyst are arranged vertically in a combustion chamber, and alcohol and water are passed to the reaction tubes through supply and discharge manifolds communicating with the reaction tubes. In an alcohol reformer that generates a hydrogen-containing gas from a mixed liquid with a reaction tube, elastic tube sheets are provided at the upper and lower ends of the reaction tube, and supply and discharge manifolds are respectively provided covering the tube sheets, The circumferential edges of the tube sheets provided at both ends of the reaction tube are fixedly attached to the combustion chamber body wall, the combustion chamber body wall is bisected in a direction perpendicular to the center line of the reaction tube, and a bellows is inserted in the part. achieved by doing.

〔発明の実施例〕[Embodiments of the invention]

以下図面に基づいて本発明の実施例を説明す
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アルコール改質
器の断面図であり、第2図は第1図のB−B断面
図である。第1図、第2図において第3図、第4
図の従来例と同一部分には同じ符号を付してい
る。第1図、第2図においてバーナ8、通風ガイ
ド7、燃焼ガス出口11の構成、作用は従来技術
のものと同一であるが、本実施例では従来技術の
ものと同じ触媒を充填した複数の反応管2の両端
を取付けた下部管板5と上部管板3とにそれぞれ
供給マニホールド16と排出マニホールド17と
を取付けている。なお上部、下部管板3,5は剛
性を抑えて弾性変形しやすくしている。
FIG. 1 is a sectional view of an alcohol reformer according to an embodiment of the present invention, and FIG. 2 is a sectional view taken along line BB in FIG. Figures 1 and 2, Figures 3 and 4
The same parts as in the conventional example in the figure are given the same reference numerals. In FIGS. 1 and 2, the structure and function of the burner 8, ventilation guide 7, and combustion gas outlet 11 are the same as those of the prior art, but in this embodiment, a plurality of A supply manifold 16 and a discharge manifold 17 are attached to a lower tube sheet 5 and an upper tube sheet 3, respectively, to which both ends of the reaction tube 2 are attached. Note that the upper and lower tube plates 3 and 5 have low rigidity to facilitate elastic deformation.

一方供給マニホールド16の入口としての入口
管12は供給マニホールド16の底部を気密に貫
通している。
On the other hand, the inlet pipe 12 serving as the inlet of the supply manifold 16 passes through the bottom of the supply manifold 16 in an airtight manner.

そして、反応管2の底部にはメツシユプレート
18を設け、供給マニホールド16からのメタノ
ールと水との混合液を反応管2内に通流させると
ともに、触媒9を保持するようにしている。なお
燃焼室1、反応管2、供給と排出マニホールド1
6,17はいずれも耐食性、耐高温性のある材
料、例えばオーステナイト系ステンレス鋼から製
作されている。
A mesh plate 18 is provided at the bottom of the reaction tube 2 to allow a mixture of methanol and water from the supply manifold 16 to flow into the reaction tube 2 and to hold the catalyst 9 therein. Furthermore, combustion chamber 1, reaction tube 2, supply and discharge manifold 1
6 and 17 are both made of corrosion-resistant and high-temperature resistant materials, such as austenitic stainless steel.

上記の構造によりバーナ8から燃料および燃焼
空気が送出されて燃焼を行わせると従来技術の項
で述べたように入口管12から供給マニホールド
16に送入されたメタノールと水との混合液は反
応管2において改質反応が行われ、水素含有ガス
が生成されて排出マニホールド17を介して出口
管13から取出される。
With the above structure, when fuel and combustion air are sent from the burner 8 to perform combustion, the mixture of methanol and water sent from the inlet pipe 12 to the supply manifold 16 reacts. A reforming reaction takes place in pipe 2 and hydrogen-containing gas is produced and removed from outlet pipe 13 via exhaust manifold 17 .

さらに、反応管2の上部管板3と下部管板5と
の周縁部は燃焼室胴壁1cに固定して取付けてい
る。そして反応管2の中心線に直角方向に燃焼室
胴壁1cを二分しこの個所にベローズ10を挿入
して取付けている。このため反応管2と燃焼室胴
壁1cの温度差による熱膨脹差はベローズ10に
おける燃焼室胴壁1cの自由膨脹により吸収する
ことができる。また反応管2相互の熱膨脹差も剛
性を低く抑えた上部、下部管板3,5の変形によ
り吸収することができる。
Furthermore, the peripheral edges of the upper tube sheet 3 and lower tube sheet 5 of the reaction tube 2 are fixedly attached to the combustion chamber body wall 1c. Then, the combustion chamber body wall 1c is divided into two parts in a direction perpendicular to the center line of the reaction tube 2, and a bellows 10 is inserted and attached to this part. Therefore, the difference in thermal expansion due to the temperature difference between the reaction tube 2 and the combustion chamber body wall 1c can be absorbed by the free expansion of the combustion chamber body wall 1c in the bellows 10. Further, the difference in thermal expansion between the reaction tubes 2 can be absorbed by deformation of the upper and lower tube plates 3 and 5, which have low rigidity.

〔発明の効果〕〔Effect of the invention〕

以上の説明から明らかなように、本発明によれ
ば反応管の両端に設けられる管板を覆つてそれぞ
れ供給および排出マニホールドを設けたことによ
りアルコール改質器を小型化することができると
いう効果がある。そして管板の周縁部は燃焼室に
固定して取付けられるが、燃焼室胴壁を上下二分
しベローズを挿着することにより、反応管と燃焼
室との温度差による熱膨脹差を吸収させ、また反
応管相互の熱膨脹差も弾性のある管板による吸収
できるので改質器の損傷につながる熱膨脹差によ
る熱応力を小さくし、信頼性のあるアルコール改
質器が得られるという効果がある。
As is clear from the above explanation, according to the present invention, the alcohol reformer can be made smaller by providing supply and discharge manifolds covering the tube sheets provided at both ends of the reaction tube. be. The peripheral edge of the tube sheet is fixedly attached to the combustion chamber, but by dividing the combustion chamber body wall into upper and lower halves and inserting bellows, the difference in thermal expansion due to the temperature difference between the reaction tube and the combustion chamber can be absorbed. Since the thermal expansion difference between the reaction tubes can be absorbed by the elastic tube sheet, the thermal stress caused by the thermal expansion difference that can lead to damage to the reformer can be reduced, and a reliable alcohol reformer can be obtained.

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

第1図は本発明の実施例によるアルコール改質
器の断面図、第2図は第1図のB−B断面図、第
3図は従来のアルコール改質器の断面図、第4図
は第3図のC−C断面図である。 1:燃焼室、2:反応管、3:上部管板、5:
下部管板、9:触媒、10:ベローズ、12:
管、16:供給マニホールド、17:排出マニホ
ールド。
FIG. 1 is a sectional view of an alcohol reformer according to an embodiment of the present invention, FIG. 2 is a sectional view taken along line BB in FIG. 1, FIG. 3 is a sectional view of a conventional alcohol reformer, and FIG. FIG. 4 is a sectional view taken along line CC in FIG. 3; 1: Combustion chamber, 2: Reaction tube, 3: Upper tube sheet, 5:
Lower tube plate, 9: catalyst, 10: bellows, 12:
Pipe, 16: Supply manifold, 17: Discharge manifold.

Claims (1)

【特許請求の範囲】[Claims] 1 燃焼室内に触媒を充填した複数の反応管を鉛
直に配し、該反応管に連通する供給マニホールド
を介して前記反応管に通流するアルコールと水と
の混合液から水素含有ガスを生成するアルコール
改質器において、前記反応管の上、下端に弾性を
有する管板をそれぞれ設け、前記管板を覆つてそ
れぞれ供給および排出マニホールドを配設し、前
記反応管の両端に設けた管板の周縁部をそれぞれ
燃焼室胴壁に固定して取付け、該燃焼室胴壁を前
記反応管の中心線に直角方向に二分し、該個所に
ベローズを挿着したことを特徴とするアルコール
改質器。
1. A plurality of reaction tubes filled with a catalyst are arranged vertically in a combustion chamber, and a hydrogen-containing gas is generated from a mixed liquid of alcohol and water that flows into the reaction tubes via a supply manifold communicating with the reaction tubes. In the alcohol reformer, elastic tube sheets are provided at the upper and lower ends of the reaction tube, supply and discharge manifolds are respectively provided covering the tube sheets, and the tube sheets provided at both ends of the reaction tube are provided with elastic tube sheets. An alcohol reformer characterized in that each of the peripheral edges is fixedly attached to a combustion chamber body wall, the combustion chamber body wall is divided into two in a direction perpendicular to the center line of the reaction tube, and a bellows is inserted in the part. .
JP26390484A 1984-12-14 1984-12-14 Alcohol reforming device Granted JPS61141927A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26390484A JPS61141927A (en) 1984-12-14 1984-12-14 Alcohol reforming device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26390484A JPS61141927A (en) 1984-12-14 1984-12-14 Alcohol reforming device

Publications (2)

Publication Number Publication Date
JPS61141927A JPS61141927A (en) 1986-06-28
JPH0425059B2 true JPH0425059B2 (en) 1992-04-28

Family

ID=17395874

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26390484A Granted JPS61141927A (en) 1984-12-14 1984-12-14 Alcohol reforming device

Country Status (1)

Country Link
JP (1) JPS61141927A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
IT1232200B (en) * 1989-01-24 1992-01-28 Kinetics Technology ISOTHERMAL CATALYTIC REACTOR FOR ENDOTHERMAL REACTIONS
JP2010047436A (en) * 2008-08-20 2010-03-04 Nissan Motor Co Ltd Hydrogen producing method and hydrogen producing apparatus

Also Published As

Publication number Publication date
JPS61141927A (en) 1986-06-28

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