JPS6256302A - Reactor for decomposing methanol - Google Patents
Reactor for decomposing methanolInfo
- Publication number
- JPS6256302A JPS6256302A JP19682485A JP19682485A JPS6256302A JP S6256302 A JPS6256302 A JP S6256302A JP 19682485 A JP19682485 A JP 19682485A JP 19682485 A JP19682485 A JP 19682485A JP S6256302 A JPS6256302 A JP S6256302A
- Authority
- JP
- Japan
- Prior art keywords
- catalyst
- heating tube
- reactor
- methanol
- decomposing
- 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
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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/06—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds in tube reactors; the solid particles being arranged in tubes
- B01J8/067—Heating or cooling the reactor
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】
〔産業上の利用分野〕
本発明はメタノールを分解又は改質するだめの反応器に
関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a reactor for decomposing or reforming methanol.
加熱管の外側に触媒を充填するメタノール分解反応器に
おける一番の重要な点は触媒層内に均一なメタノール蒸
気の流れを形成することである。従来は反応管の内部に
触媒を充填し、かつメタノール蒸気は反応管内を流れる
構造のものであり、今回のような管の外側に触媒を充填
したものはない。The most important point in a methanol decomposition reactor in which a catalyst is packed on the outside of a heating tube is to form a uniform flow of methanol vapor within the catalyst layer. Conventionally, the inside of the reaction tube was filled with a catalyst, and the methanol vapor flowed through the reaction tube, but there is no such structure in which the outside of the tube is filled with a catalyst like this one.
加熱管の外側に触媒を充填する場合、触媒が均一に充填
されないとメタノール蒸気が偏流をおこし、所定の性能
が発揮されない。When filling the outside of the heating tube with a catalyst, if the catalyst is not filled uniformly, methanol vapor will flow unevenly and the desired performance will not be achieved.
又、加熱管から触媒に対しても均一に熱交換が行われな
いと2反応器としては所定の性能が発揮されない。Furthermore, unless heat exchange is uniformly performed from the heating tube to the catalyst, the two reactors will not exhibit the desired performance.
本発明は加熱管としても伝熱効果もよく、かつ触媒の均
一充填が行える構造を有するメタノール分解反応器を提
供することを目的とするものである。It is an object of the present invention to provide a methanol decomposition reactor having a structure that has a good heat transfer effect as a heating tube and can be uniformly filled with a catalyst.
メタノールを分解又は改質する反応器においで、加熱管
の外周壁に軸方向にストレートフィンをもうけてなるメ
タノール分解反応器。A methanol decomposition reactor for decomposing or reforming methanol, in which straight fins are provided in the axial direction on the outer peripheral wall of a heating tube.
まず触媒内をメタノール蒸気が均一に流れるためにはあ
る程度触媒が均一充填できるような区画を触媒層内にも
うける必要がある。一方。First, in order for methanol vapor to flow uniformly within the catalyst, it is necessary to provide a section within the catalyst layer that allows the catalyst to be uniformly filled to some extent. on the other hand.
加熱管から触媒への熱交換を増加させるには。To increase the heat exchange from the heating tube to the catalyst.
触媒と加熱管の接触面積を大きくとる必要がある。従っ
て両者を満足する′ようなものと17で。It is necessary to increase the contact area between the catalyst and the heating tube. Therefore, it is 17 that satisfies both.
加熱管の軸方向にストレートフィンをつけることにより
触媒層内にある程度の区画を構成し。By attaching straight fins in the axial direction of the heating tube, a certain degree of division is created within the catalyst layer.
これにより触媒の均一な充填が可能となる。This allows uniform loading of the catalyst.
加熱管(でストし・−トフィンをつけるこ)−(〆C」
。Heating tube (stop and attach tofin) - (〆C'
.
り区画が構成され、触媒が均一に充填され伝熱特性が向
上し、これにともない装置のコ゛・くクト化、コストダ
ウンにつながる。The catalyst is uniformly filled with the catalyst, improving heat transfer characteristics, which leads to smaller equipment and lower costs.
本発明の実施態様例を第1図〜第3図(C示す1、第1
図には1例として竪型の分解反応器をガスす、−第1図
においてメタノール蒸気はメタノール蒸気入口管台4よ
り反応器本体1へ導入されるが。Examples of embodiments of the present invention are shown in FIGS.
The figure shows, as an example, a vertical decomposition reactor. In FIG. 1, methanol vapor is introduced into the reactor body 1 from a methanol vapor inlet nozzle 4.
その後2多孔板8.金網7全通って触媒層9へと流れ、
この間に加熱管10より加熱されるためメタノ−・ル蒸
気は分解又は改質されてガス出口管台5から排出される
。第2図は触媒層の充填部の縦断面図を示す。第3図は
触媒層の充填部の横断面図である。第3図から明らかな
ように第3図(a)は千鳥配列の場合(b)は正方配列
の場合を示すことにより小さな区画を構成できるため、
触媒の均一充填が可能となる。Then 2 perforated plate8. It passes through the entire wire mesh 7 and flows to the catalyst layer 9.
During this time, the methanol vapor is heated by the heating pipe 10, so that it is decomposed or reformed and is discharged from the gas outlet nozzle 5. FIG. 2 shows a longitudinal sectional view of the packed portion of the catalyst bed. FIG. 3 is a cross-sectional view of the packed portion of the catalyst bed. As is clear from Fig. 3, Fig. 3 (a) shows the case of staggered arrangement and Fig. 3 (b) shows the case of square arrangement, so that small sections can be constructed.
Uniform packing of catalyst becomes possible.
触媒の均一充填ができることとストレートフィン付きの
加熱管のため伝熱特性がよく、全体として装置のコンパ
クト化、コスト低減につながる。The ability to uniformly charge the catalyst and the heating tube with straight fins provides good heat transfer characteristics, leading to a more compact and cost-effective device as a whole.
なお2反応器を横置きにし5、でも同一の効果を発揮す
る。Note that the same effect can be obtained even if the two reactors are placed horizontally.
第1図は本発明のメタノ−・ル分解反応器の1実施B様
例の例示図、第2図は触媒層の充填部の縦断面図、第3
図は触媒層の充填部の横断面図である。FIG. 1 is an illustrative view of a first embodiment B of the methanol decomposition reactor of the present invention, FIG. 2 is a longitudinal sectional view of the packed part of the catalyst bed, and FIG.
The figure is a cross-sectional view of the packed portion of the catalyst layer.
Claims (1)
の外周壁に軸方向にストレートフィンをもうけてなるこ
とを特徴とするメタノール分解反応器。A methanol decomposition reactor for decomposing or reforming methanol, characterized in that a straight fin is provided in the axial direction on the outer peripheral wall of a heating tube.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19682485A JPS6256302A (en) | 1985-09-05 | 1985-09-05 | Reactor for decomposing methanol |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19682485A JPS6256302A (en) | 1985-09-05 | 1985-09-05 | Reactor for decomposing methanol |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6256302A true JPS6256302A (en) | 1987-03-12 |
Family
ID=16364272
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP19682485A Pending JPS6256302A (en) | 1985-09-05 | 1985-09-05 | Reactor for decomposing methanol |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6256302A (en) |
-
1985
- 1985-09-05 JP JP19682485A patent/JPS6256302A/en active Pending
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