JPS6265902A - Reactor for decomposing methanol - Google Patents
Reactor for decomposing methanolInfo
- Publication number
- JPS6265902A JPS6265902A JP20290985A JP20290985A JPS6265902A JP S6265902 A JPS6265902 A JP S6265902A JP 20290985 A JP20290985 A JP 20290985A JP 20290985 A JP20290985 A JP 20290985A JP S6265902 A JPS6265902 A JP S6265902A
- Authority
- JP
- Japan
- Prior art keywords
- catalyst
- methanol
- vapor
- supporting plate
- reactor
- 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
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 title claims abstract description 96
- 239000003054 catalyst Substances 0.000 claims abstract description 39
- 238000010438 heat treatment Methods 0.000 claims abstract description 7
- 238000000354 decomposition reaction Methods 0.000 claims description 7
- 125000006850 spacer group Chemical group 0.000 abstract 1
- 239000006185 dispersion Substances 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 238000002407 reforming Methods 0.000 description 1
Landscapes
- 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.
従来は反応管の内部に触媒を充填し、かつ、メタノール
蒸気は反応管内部を流れる構造になっており、触媒層内
での流れの均一化はそれほど問題とされなかったが、加
熱管の外部に触媒を充填するメタノール分解反応器にお
いては触媒層内に均一にメタノール蒸気を供給すること
が重要である。Conventionally, the inside of the reaction tube was filled with a catalyst and the methanol vapor flowed inside the reaction tube, and uniformity of the flow within the catalyst layer was not so much of a problem. In a methanol decomposition reactor filled with a catalyst, it is important to uniformly supply methanol vapor into the catalyst bed.
加熱管の外部に触媒を充填する構造を有する反応器にお
いては、性能面からできるだけ触媒層の内部にメタノー
ル蒸気の均一な流れを確保することが必要となる。メタ
ノール蒸気が反応器に供給されると触媒受皿の役目も兼
用している多孔板にあけられた孔から触媒層へとメタノ
ール蒸気が流れていくが、この多孔板にはメタノール側
の圧力損失が小さく、かつ、メタノール蒸気を均一に分
配する機能が要求される。In a reactor having a structure in which a catalyst is packed outside a heating tube, it is necessary to ensure as uniform a flow of methanol vapor as possible inside the catalyst layer from a performance standpoint. When methanol vapor is supplied to the reactor, it flows into the catalyst layer through holes in a perforated plate that also serves as a catalyst tray, but this perforated plate has a pressure loss on the methanol side. It is required to be small and have the ability to evenly distribute methanol vapor.
本発明は上記の機能を満足する圧力損失の小さい蒸気分
配機構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。An object of the present invention is to provide a methanol decomposition reactor having a steam distribution mechanism with low pressure loss that satisfies the above-mentioned functions.
触媒を加熱管の外部に充填する構造を有するメタノール
分解反応器において、触媒層の端部に多段に設けられた
触媒支持板と該触媒支持板の段差間に張装された低圧損
の間隙ある部材とからなる蒸気分配機構を具備すること
を特徴とするメタノール分解反応器、メタノール蒸気を
均一に触媒層へ流入させるだめには2つの点での考慮が
必要となる。1つは供給メタノール蒸気側の外乱(流量
変動、圧力変動等)をある程度吸収できることと各触媒
層への分配に対して圧損が少ないことである。In a methanol decomposition reactor having a structure in which a catalyst is packed outside a heating tube, there is a catalyst support plate provided in multiple stages at the end of the catalyst layer and a low pressure drop gap stretched between the steps of the catalyst support plate. In order to uniformly flow methanol vapor into the catalyst layer, it is necessary to consider two points. One is that disturbances on the supplied methanol vapor side (flow rate fluctuations, pressure fluctuations, etc.) can be absorbed to some extent, and pressure loss is small with respect to distribution to each catalyst layer.
本発明では、この2点を満足する構造を考慮したもので
あり、低圧損の間隙ある部材としては金網、スリット、
格子、ハニカム構造部材等があげられる。In the present invention, a structure that satisfies these two points is considered, and members with low pressure loss and gaps include wire mesh, slits,
Examples include lattices, honeycomb structural members, and the like.
多孔板のかわりに蒸気分配機構をもうけ、かつ、この蒸
気分配機構自体が触媒の受は皿となり低圧力損失である
ので触媒層内にメタノール蒸気の均一な供給が行なわれ
る。A vapor distribution mechanism is provided in place of the perforated plate, and this vapor distribution mechanism itself serves as a tray for the catalyst, resulting in low pressure loss, so that methanol vapor is uniformly supplied into the catalyst layer.
本発明の実施態様例を第1図〜第3図に示す。 Embodiments of the present invention are shown in FIGS. 1 to 3.
第1図は竪型の分解反応器の例示図、第2図は蒸気分散
機構の縦断面図、第3図は蒸気分散機構の斜視図である
。FIG. 1 is an illustrative diagram of a vertical decomposition reactor, FIG. 2 is a longitudinal sectional view of a vapor dispersion mechanism, and FIG. 3 is a perspective view of the vapor dispersion mechanism.
第1図〜第5図においてメタノール蒸気はメタノール蒸
気入口管台■より反応器本体■へ導びかれるが、最初は
メタノール蒸気は管板■と触媒支持下板■の間にたまる
。この空間の圧力が所定の圧力になれば、メタノール蒸
気は触媒支持上板■と触媒支持下板■の段差間に張装さ
れた金網[相]を通して触媒層へ均一に供給される。In FIGS. 1 to 5, methanol vapor is led from the methanol vapor inlet nozzle stub 1 to the reactor main body 2, but initially the methanol vapor accumulates between the tube plate 2 and the catalyst support lower plate 2. When the pressure in this space reaches a predetermined pressure, methanol vapor is uniformly supplied to the catalyst layer through the wire mesh [phase] stretched between the steps of the catalyst support upper plate (1) and the catalyst support lower plate (2).
なお触媒支持板■、■は第5図のように加熱管の外側に
スリーブ[相]をもうけ、これによって支持する構造で
ある。The catalyst support plates (1) and (2) have a sleeve (phase) on the outside of the heating tube, as shown in FIG. 5, and are supported by this.
本発明のメタノール分解反応器によればメタノール蒸気
を均一に供給できるだけでなく、メタノール系の圧力損
失も少くてすみ、かつ、蒸気分配機構が触媒受皿として
の機能をもつだめ装置の単純化がはかられ信頼性も向上
する。According to the methanol decomposition reactor of the present invention, not only can methanol vapor be uniformly supplied, but also the pressure loss of the methanol system can be reduced, and the storage device in which the vapor distribution mechanism functions as a catalyst tray can be simplified. This also improves reliability.
第1図は本発明の装置の実施態様例の例示図、第2図は
蒸気分散機構の縦断面図、第3図は蒸気分散機構の斜視
図である。
■・・・反応器本体、■・・・熱媒人口管台、■・・・
熱媒出口管台、■・・・メタノール蒸気入口管台、■・
・・ガス出口管 、■・・・管板、■・・・触媒支持下
板、■・・・触媒支持上板、■・・・触媒層、0・・・
加熱管、■・・・仕切板、■・・・金網、@・・・支持
台、■・・・触媒搬出人孔、[相]・・・金網、[相]
・・・スリーブ第+1fiFIG. 1 is an illustrative view of an embodiment of the apparatus of the present invention, FIG. 2 is a longitudinal sectional view of a vapor dispersion mechanism, and FIG. 3 is a perspective view of the vapor dispersion mechanism. ■・・・Reactor main body, ■・・・Heat medium control stand, ■・・・
Heat medium outlet nozzle, ■... Methanol vapor inlet nozzle, ■.
...Gas outlet pipe, ■...Tube sheet, ■...Catalyst support lower plate, ■...Catalyst support upper plate, ■...Catalyst layer, 0...
Heating tube, ■... Partition plate, ■... Wire mesh, @... Support stand, ■... Catalyst delivery hole, [Phase]... Wire mesh, [Phase]
... Sleeve No. +1 fi
Claims (1)
分解反応器において、触媒層の端部に多段に設けられた
触媒支持板と該触媒支持板の段差間に張装された低圧損
の間隙ある部材とからなる蒸気分配機構を具備すること
を特徴とするメタノール分解反応器。In a methanol decomposition reactor having a structure in which a catalyst is packed outside a heating tube, there is a catalyst support plate provided in multiple stages at the end of the catalyst layer and a low pressure drop gap stretched between the steps of the catalyst support plate. 1. A methanol decomposition reactor, characterized in that it is equipped with a vapor distribution mechanism consisting of members.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20290985A JPS6265902A (en) | 1985-09-13 | 1985-09-13 | Reactor for decomposing methanol |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20290985A JPS6265902A (en) | 1985-09-13 | 1985-09-13 | Reactor for decomposing methanol |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS6265902A true JPS6265902A (en) | 1987-03-25 |
Family
ID=16465182
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP20290985A Pending JPS6265902A (en) | 1985-09-13 | 1985-09-13 | Reactor for decomposing methanol |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6265902A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH089831A (en) * | 1994-06-30 | 1996-01-16 | Katsuo Otsuka | Purification of wafer in water tank |
| CN110075763A (en) * | 2019-04-22 | 2019-08-02 | 西安交通大学 | Grill support particle orderly accumulation structure fixed bed reactors |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5347096U (en) * | 1976-09-24 | 1978-04-21 |
-
1985
- 1985-09-13 JP JP20290985A patent/JPS6265902A/en active Pending
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5347096U (en) * | 1976-09-24 | 1978-04-21 |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH089831A (en) * | 1994-06-30 | 1996-01-16 | Katsuo Otsuka | Purification of wafer in water tank |
| CN110075763A (en) * | 2019-04-22 | 2019-08-02 | 西安交通大学 | Grill support particle orderly accumulation structure fixed bed reactors |
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