JPS6265902A - Reactor for decomposing methanol - Google Patents

Reactor for decomposing methanol

Info

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
Application number
JP20290985A
Other languages
Japanese (ja)
Inventor
Masamichi Kashiwazaki
柏崎 正道
Satoki Toki
甕 聰樹
Kouichirou Ootsubo
大坪 浩一朗
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP20290985A priority Critical patent/JPS6265902A/en
Publication of JPS6265902A publication Critical patent/JPS6265902A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To uniformly supply methanol vapor into a catalyst bed with a low pressure drop by providing a low-pressure drop spacer member such as a wire mesh between the upper catalyst supporting plate and the lower supporting plate in the title reactor for decomposing methanol wherein the catalyst is packed on the outside of a heating tube. CONSTITUTION:The vapor of methanol is supplied from an inlet 4 of the methanol decomposing reactor 1 wherein a catalyst bed 9 is provided on the outside of the heating tube 10. The methanol vapor is accumulated between a tube plate 6 and the catalyst supporting plate 7. When the pressure of the methanol vapor in the space increases to a specified pressure, the vapor is uniformly supplied to the catalyst bed 9 through the opening of a wire mesh spread on the stepped part between the lower catalyst supporting plate 7 and the upper supporting plate 8, a slit, a grid, etc., 15. Since the catalyst 9 is also supported by the methanol vapor distributing mechanism consisting of the wire mesh, slit, grid., etc., 15, methanol vapor can be uniformly supplied into the catalyst 9 with a low pressure drop.

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.

〔従来の技術〕[Conventional technology]

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.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

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.

〔問題点を解決するための手段〕[Means for solving problems]

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.

〔作用〕[Effect]

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.

〔実施例〕〔Example〕

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.

〔発明の効果〕〔Effect of the invention〕

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.

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

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+1fi
FIG. 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)

【特許請求の範囲】[Claims] 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。
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.
JP20290985A 1985-09-13 1985-09-13 Reactor for decomposing methanol Pending JPS6265902A (en)

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)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5347096U (en) * 1976-09-24 1978-04-21

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5347096U (en) * 1976-09-24 1978-04-21

Cited By (2)

* Cited by examiner, † Cited by third party
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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