JPS61141927A - alcohol reformer - Google Patents
alcohol reformerInfo
- Publication number
- JPS61141927A JPS61141927A JP26390484A JP26390484A JPS61141927A JP S61141927 A JPS61141927 A JP S61141927A JP 26390484 A JP26390484 A JP 26390484A JP 26390484 A JP26390484 A JP 26390484A JP S61141927 A JPS61141927 A JP S61141927A
- Authority
- JP
- Japan
- Prior art keywords
- combustion chamber
- tube
- wall
- reaction
- reaction tube
- 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
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J12/00—Chemical processes in general for reacting gaseous media with gaseous media; Apparatus specially adapted therefor
- B01J12/005—Chemical 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)
Abstract
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.
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5図は従来の改質器の要部構造の断面図であり、第6
図は第5図のC−C断面図である。第5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1こ設けられている。FIG. 5 is a cross-sectional view of the main structure of a conventional reformer, and FIG.
The figure is a sectional view taken along the line CC in FIG. In FIG. 5, a burner 8 equipped with an outlet (not shown) for supplying fuel and combustion air is provided in the center of the upper wall 1a of the combustion chamber 1. As shown in FIG.
さらに燃焼室上部壁1a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
ICに沿って第6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の底部の開口にピッグティル
15を接続し、これらのピッグティル15の他端をマニ
ホールドとしてのヘッダ16に接続し、ヘッダ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を設けて燃焼ガスを
案内し、燃焼室胴壁ICには燃焼ガスの出口11を設け
ている。Further, an exhaust manifold 17 is provided on the upper wall 1a of the combustion chamber to exhaust the hydrogen-containing gas produced by reforming. 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 IC as shown in FIG. Pig tills 15 are connected to the bottom openings of each reaction tube 2, the other ends of these pig tills 15 are connected to a header 16 as a manifold, and the reformed fuel inlet pipe 12 connected to the bottom opening of the header 16 is used for combustion. It penetrates through 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 combustion gas, and an outlet 11 for the combustion gas is provided in the combustion chamber body wall IC.
上記の構造番こより改質燃料入口管12にアルコール、
例えはエタノールと水との混合液を送入しヘッダ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
ッグティル15に吸収させている。このためピッグティ
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。From the above structure number, alcohol is added to the reformed fuel inlet pipe 12.
For example, a mixture of ethanol and water is fed into each reaction tube 2 through the header 16, and the temperature of the reaction tube 2 is raised to about 250°C by the flame and combustion gas burned by the burner 8.
When the temperature rises to a certain level, the reforming reaction is promoted in the reaction tube under the action of the catalyst to generate hydrogen, and at the same time, the reformed gas exits the reformed gas outlet 13 through the manifold 17 along with the generated carbon dioxide etc. due to combustion. A difference in thermal expansion occurs due to a temperature difference or a temperature difference between the reaction tubes, and this difference in thermal expansion is absorbed by the pig till 15. For this reason, the pig till 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、ピッグティル1
5を反応管2やヘッダ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。またピッグティル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, if the reformer is to be made smaller, pig till 1
It is necessary to hermetically weld the tube 5 to the reaction tube 2 and the header 16, but since it is small, it does not take up enough space, which makes it difficult to perform hermetic welding and reduces the reliability of the welded part. There is also the problem that the length of the pig till 15 is not long enough to absorb the difference in thermal expansion due to its small size.
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.
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、この反応管に連通ずる供
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臭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、前記管板を葎ってそれぞ
れ供給。According to the present invention, a plurality of reaction tubes filled with a catalyst are arranged vertically in a combustion chamber, and alcohol and water are communicated to the reaction tubes through supply and discharge manifolds. In an alcohol reformer that generates a watery odor-containing gas from a mixed liquid with alcohol, elastic tube sheets are provided at the upper and lower ends of the reaction tube, respectively, and the tube sheets are peeled off for supply.
排出マニホールドを配設し、前記管板の少なくとも一方
の周縁部の周囲を燃焼室壁に固定して取付け、反応管と
燃焼室との熱膨脹差をこの反応管と燃焼室との少なくと
も一方の自由膨脹により吸収させる構造とすることによ
り達成される。A discharge manifold is provided, and the periphery of at least one of the tube sheets is fixedly attached to the wall of the combustion chamber, and the difference in thermal expansion between the reaction tube and the combustion chamber is absorbed by the freedom of at least one of the reaction tube and the combustion chamber. This is achieved by creating a structure that allows absorption through expansion.
以下図面屹基づいて本発明の詳細な説明する。 The present invention will be described in detail below with reference to the drawings.
第1図は本発明の実施f!IJこ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A−A断面図である
。第1図、第2図および後出する第3図。FIG. 1 shows the implementation of the present invention f! 2 is a sectional view of an alcohol reformer manufactured by IJ, and FIG. 2 is a sectional view taken along line AA in FIG. 1. FIG. 1, FIG. 2, and FIG. 3, which will be described later.
第4図1こおいて第5図、第6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2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。In FIG. 4, the same parts as in the conventional example shown in FIGS. 5 and 6 are given the same reference numerals. In FIGS. 1 and 2, the structure 2 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.
なお上部。Furthermore, the upper part.
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。そして上部管板3の周縁部の周囲を燃焼室1のフラ
ンジ1dに取付けて固定している。The lower tube plates 3 and 5 have low rigidity to facilitate elastic deformation. The periphery of the upper tube plate 3 is attached and fixed to the flange 1d of the combustion chamber 1.
一方供給マニホールド16の管としての入口管12は燃
焼室1の燃焼室下部壁1bを軸シール材としてのグラン
ドパツキン14を介して貫通している。グランドパツキ
ン14は石綿繊維とグラファイトの混合物を成形し外部
を綿糸であらく袋編みして被覆したリング状の成形品、
例えばパルカー製のリング成形品であり、これを数段に
してグランドパツキン溝に挿入し押え板14aにより締
付け、入口管12〆の摺動を可能にしている。On the other hand, the inlet pipe 12 as a pipe of the supply manifold 16 passes through the combustion chamber lower wall 1b of the combustion chamber 1 via a gland packing 14 as a shaft sealing material. Grand Patsukin 14 is a ring-shaped molded product made of a mixture of asbestos fiber and graphite and covered with cotton thread by loosely knitting the outside.
For example, it is a ring molded product made by Pulcar, and is inserted into a gland packing groove in several stages and tightened by a presser plate 14a to enable sliding of the inlet pipe 12.
そして、反応管2の底部にはメソシュプレート18を設
け、供給マニホールド16からのエ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16.17はいづれも耐食性、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 the mixture of ethanol and water from the supply manifold 16 to flow into the reaction tube 2 and to hold the catalyst 9 therein. The combustion chamber 1, reaction tube 2) supply and discharge manifolds 16, 17 are all 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
出されて燃焼を行なわさ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
エタノールと水との混合液は反応管2において改質反応
が行なわれ、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, fuel and combustion air are sent out from the burner 8 to cause combustion, and as described in the prior art section, the mixed liquid of ethanol and water sent from the inlet pipe 12 to the supply manifold 16 reacts. A reforming reaction takes place in tube 2 and hydrogen-containing gas is produced and removed from outlet tube 13 via exhaust manifold 17 .
この場合反応管2と燃焼室胴壁ICとの間に生じる温度
差による熱膨脹差は、入口管12と燃焼室1の燃焼室下
部壁1bとの間に介装したグランドパツキン14におい
て摺動して吸収することができる。才たグランドパツキ
ン14により燃焼ガスの漏洩を防止することができる。In this case, the difference in thermal expansion caused by the temperature difference between the reaction tube 2 and the combustion chamber body wall IC slides in the gland packing 14 interposed between the inlet pipe 12 and the lower combustion chamber wall 1b of the combustion chamber 1. can be absorbed. The long gland packing 14 can prevent combustion gas from leaking.
また反応管2相互の温度差に基づく熱膨脹差は弾性変形
しやすい上部、下部管板3,5の変形により吸収される
。Further, the thermal expansion difference due to the temperature difference between the reaction tubes 2 is absorbed by the deformation of the upper and lower tube sheets 3 and 5, which are easily elastically deformed.
第3図は本発明の異なる実施例によるアルコール改質器
の断面図であり、第4図は第3図のB−B断面図である
。第3図、第4図に示す本実施例では反応管2の上部管
板3と下部管板5との周縁部の周囲を燃焼室胴壁ICに
固定して取付けている。しかし反応管2の中心線に直角
方向に燃焼室胴壁ICを二分し、この個所にベローズ1
0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IC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IC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
。FIG. 3 is a sectional view of an alcohol reformer according to a different embodiment of the present invention, and FIG. 4 is a sectional view taken along line BB in FIG. In this embodiment shown in FIGS. 3 and 4, the peripheries 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 IC. However, the combustion chamber body wall IC is bisected in the direction perpendicular to the center line of the reaction tube 2, and the bellows 1 is placed at this point.
0 is inserted and installed. Therefore, the thermal expansion difference due to the temperature difference between the reaction tube 2 and the combustion chamber body wall IC can be absorbed by the free expansion of the combustion chamber body wall IC 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.
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っ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リ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
は少なくも一方の周縁部の周囲を燃焼室に固定して取付
けられるが、反応管と燃焼室との少なくとも一方を自由
膨脹させて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り吸収できるの
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 real alcohol reformer can be downsized by providing supply and discharge manifolds covering the tube sheets provided at both ends of the reaction tube. effective. The tube sheet is fixedly attached around at least one peripheral edge to the combustion chamber, but at least one of the reaction tubes and the combustion chamber is allowed to freely expand to absorb the thermal expansion difference due to temperature difference, and the reaction tubes are connected to each other. Since the difference in thermal expansion can be absorbed by the elastic tube sheet, the thermal stress due to the difference in thermal expansion that can lead to damage to the reformer can be reduced, and a reliable alcohol reformer can be obtained.
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A、 −A断面図、第3図は本発
明の異なる実施例によるアルコール改質器の断面図、第
4図は第3図におけるH−B断面図、第5図は従来のア
ルコール改質器の断面図、第6図は第5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、12:管、14:軸シール材、16:供給
マニホールド、17:排出マニホ第1図
第3図
特開口RGI−141927(4)
第5図FIG. 1 is a cross-sectional view of an alcohol reformer according to an embodiment of the present invention, FIG. 2 is a cross-sectional view of A and -A in FIG. 1, and FIG. 3 is a cross-section of an alcohol reformer according to a different embodiment of the present invention. 4 is a cross-sectional view taken along line HB in FIG. 3, FIG. 5 is a cross-sectional view of a conventional alcohol reformer, and FIG. 6 is a cross-sectional view taken along line CC in FIG. 1: Combustion chamber, 2: Reaction tube, 3: Upper tube sheet, 5: Lower tube sheet, 9: Catalyst, 12: Tube, 14: Shaft seal material, 16: Supply manifold, 17: Discharge manifold Figure 1, Figure 3 Figure special opening RGI-141927 (4) Figure 5
Claims (1)
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
管板を覆ってそれぞれ供給および排出マニホールドを配
設し、前記管板の少なくとも一方の周縁部の周囲を燃焼
室壁に固定して取付け、前記反応管と燃焼室との熱膨脹
差を該反応管と燃焼室との少なくとも一方の自由膨脹に
より吸収させる構造としたことを特徴とするアルコール
改質器。 2)特許請求の範囲第1項記載のアルコール改質器にお
いて、一方の管板の周縁部の周囲を燃焼室壁に固定して
取付けて反応管を懸架し、他方の管板に配されるマニホ
ールドに連通する管を燃焼室壁を貫通して設け、前記管
と該燃焼室壁との間に軸シール材を介装して摺動可能に
したことを特徴とするアルコール改質器。 2)特許請求の範囲第1項記載のアルコール改質器にお
いて、反応管の両端に設けた管板の周縁部の周囲をそれ
ぞれ燃焼室壁に固定して取付け、該燃焼室壁を前記反応
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。[Scope of Claims] 1) A plurality of reaction tubes filled with a catalyst are arranged vertically in a combustion chamber, and a mixed liquid of alcohol and water is flowed into the reaction tubes through a supply manifold communicating with the reaction tubes. In an alcohol reformer that generates a hydrogen-containing gas, elastic tube sheets are provided at the upper and lower ends of the reaction tube, and supply and discharge manifolds are provided covering the tube sheets, respectively, and The periphery of at least one of the peripheral edges is fixedly attached to the wall of the combustion chamber, and the structure is such that the difference in thermal expansion between the reaction tube and the combustion chamber is absorbed by free expansion of at least one of the reaction tube and the combustion chamber. Alcohol reformer. 2) In the alcohol reformer according to claim 1, the periphery of one tube sheet is fixedly attached to the combustion chamber wall to suspend the reaction tube, and the reaction tube is arranged on the other tube sheet. An alcohol reformer characterized in that a pipe communicating with a manifold is provided passing through a wall of a combustion chamber, and a shaft sealing material is interposed between the pipe and the wall of the combustion chamber to enable sliding. 2) In the alcohol reformer according to claim 1, the periphery of the tube sheet provided at both ends of the reaction tube is fixedly attached to the combustion chamber wall, and the combustion chamber wall is attached to the reaction tube. An alcohol reformer characterized in that the alcohol reformer is divided into two parts in a direction perpendicular to the center line thereof, and a bellows is inserted into the part.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP26390484A JPS61141927A (en) | 1984-12-14 | 1984-12-14 | alcohol reformer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP26390484A JPS61141927A (en) | 1984-12-14 | 1984-12-14 | alcohol reformer |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS61141927A true JPS61141927A (en) | 1986-06-28 |
JPH0425059B2 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 reformer |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61141927A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH03127A (en) * | 1989-01-24 | 1991-01-07 | Mannesmann Ag | Indirect heating in reaction room for endothermic reaction and apparatus for performing it |
JP2010047436A (en) * | 2008-08-20 | 2010-03-04 | Nissan Motor Co Ltd | Hydrogen producing method and hydrogen producing apparatus |
-
1984
- 1984-12-14 JP JP26390484A patent/JPS61141927A/en active Granted
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH03127A (en) * | 1989-01-24 | 1991-01-07 | Mannesmann Ag | Indirect heating in reaction room for endothermic reaction and apparatus for performing it |
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 |
---|---|
JPH0425059B2 (en) | 1992-04-28 |
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