JPH0133152Y2 - - Google Patents

Info

Publication number
JPH0133152Y2
JPH0133152Y2 JP1983199457U JP19945783U JPH0133152Y2 JP H0133152 Y2 JPH0133152 Y2 JP H0133152Y2 JP 1983199457 U JP1983199457 U JP 1983199457U JP 19945783 U JP19945783 U JP 19945783U JP H0133152 Y2 JPH0133152 Y2 JP H0133152Y2
Authority
JP
Japan
Prior art keywords
trough
catalyst
tube
hopper
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.)
Expired
Application number
JP1983199457U
Other languages
Japanese (ja)
Other versions
JPS60112338U (en
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 filed Critical
Priority to JP19945783U priority Critical patent/JPS60112338U/en
Publication of JPS60112338U publication Critical patent/JPS60112338U/en
Application granted granted Critical
Publication of JPH0133152Y2 publication Critical patent/JPH0133152Y2/ja
Granted legal-status Critical Current

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  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)

Description

【考案の詳細な説明】 〔技術分野〕 本考案は粒状の触媒充填機に関するものであ
る。
[Detailed Description of the Invention] [Technical Field] The present invention relates to a granular catalyst filling machine.

〔従来技術〕[Prior art]

多管式熱交型反応器は、発熱の大きい気相接触
反応において最も代表的な反応器の一つとして良
く知られている。しかしながら、この反応器は大
型のものにあつては数千本の触媒を充填した反応
管よりなるものもあり、それぞれの管について反
応ガスの流通抵抗が、ある一定の範囲内で均一で
あることが要求される。これが不均一である場合
は、各管について反応ガスの流通速度が異り、反
応率も不均一となり、場合によつては反応器全体
としての制御が全く出来なくなつてしまうことに
もなる。従つて、この反応器の各管への触媒充填
については均一な充填を行うために、多大の労力
が費やされ、熟練と時間を必要としてきた。
A shell-and-tube heat exchange reactor is well known as one of the most typical reactors for gas-phase catalytic reactions that generate a large amount of heat. However, some large-sized reactors consist of several thousand catalyst-filled reaction tubes, and the flow resistance of the reaction gas in each tube must be uniform within a certain range. is required. If this is non-uniform, the flow rate of the reaction gas will be different for each tube, the reaction rate will also be non-uniform, and in some cases, the reactor as a whole may not be able to be controlled at all. Therefore, in order to uniformly charge the catalyst into each tube of this reactor, a great deal of effort has been expended, and skill and time have been required.

また、特開昭55−24516号公報に水平に設けた
振動式フイーダー付トラフによりダストを分離さ
せて触媒を抜出しできるようにしたものが開示さ
れている。しかし、水平に設けた振動式フイーダ
ー付トラフでは、その振動の振幅により供給速度
を調整してみても、この場合の供給速度は水平方
向の速度であり、上下方向の落下速度にはなんら
寄与し得ず、したがつて所定の落下速度が得られ
ず、従来のトラフを反応器への触媒充填に使用し
たとしても、調整可能で均一な充填密度を確保す
ることが困難であるという問題があつた。
Further, Japanese Patent Application Laid-Open No. 55-24516 discloses a system in which a trough with a vibrating feeder installed horizontally allows dust to be separated and the catalyst to be extracted. However, in a horizontally installed trough with a vibrating feeder, even if the feeding speed is adjusted by the amplitude of the vibration, the feeding speed in this case is the horizontal speed and does not contribute to the vertical falling speed. Therefore, even if a conventional trough is used to charge the catalyst into the reactor, it is difficult to ensure an adjustable and uniform packing density. Ta.

〔考案の目的〕[Purpose of invention]

そこで、本考案の目的は、上記従来技術の欠点
ないし不都合を解消することである。
Therefore, an object of the present invention is to eliminate the drawbacks or inconveniences of the above-mentioned prior art.

本考案者らは、この様な経験のうえに鋭意研究
を重ねた結果、反応管に触媒を充填するにあた
り、一定量の触媒粒子を一定速度で送入すること
により、各反応管について均一な充填状態が得ら
れることを見い出し、また、前記一定速度が上下
方向に延びるシユートおよびビニールチユーブに
よる落下速度と、傾斜角調整可能な電磁式フイー
ダー付トラフによるシユートへの調整可能な上下
方向の供給速度との和より得られることに着目
し、本考案を完成したものである。
As a result of extensive research based on this experience, the inventors of the present invention discovered that when filling a reaction tube with catalyst, by feeding a certain amount of catalyst particles at a constant speed, each reaction tube is uniformly filled. It has been found that a filled state can be obtained, and the above-mentioned constant speed is the falling speed by a chute extending in the vertical direction and the vinyl tube, and the adjustable vertical feeding speed to the chute by a trough with an electromagnetic feeder whose inclination angle is adjustable. This invention was completed by focusing on what can be obtained from the sum of

〔考案の要旨〕[Summary of the idea]

本考案に係る触媒充填機はホツパーとこのホツ
パーの下方に配置された反応管との間に傾斜角調
整可能な電磁式フイーダー付トラフと、このトラ
フの出口部に垂下して設けられていて粒状触媒を
一定の落差で反応管に落し込むシユートおよびビ
ニールチユーブとを設けたことを特徴とする。
The catalyst filling machine according to the present invention has a trough with an electromagnetic feeder whose inclination angle can be adjusted between a hopper and a reaction tube placed below the hopper, and a trough with an electromagnetic feeder that hangs down from the outlet of this trough to form particles. It is characterized by the provision of a chute and a vinyl tube through which the catalyst is dropped into the reaction tube at a constant head.

〔考案の構成〕[Structure of the idea]

以下に本考案を図によつて説明する。 The present invention will be explained below using figures.

触媒を充填する反応管14に斗状のシユート
13を挿入し、これに触媒充填機のシユート8及
びビニールチユーブ9が中心を合せてシユート1
3に或る程度差し込まれる様に触媒充填機を置
く。尚、触媒充填機のホツパー1のダンパー12
の開度及びトラフ3の傾斜角、コントローラー4
によるフイーダー2の振幅は予備テストに於て定
め、あらかじめ設定しておく。
A funnel-shaped chute 13 is inserted into the reaction tube 14 to be filled with a catalyst, and the chute 8 and vinyl tube 9 of the catalyst filling machine are aligned with the center of the chute 13.
3. Place the catalyst filling machine so that it is inserted to some extent. In addition, the damper 12 of the hopper 1 of the catalyst filling machine
opening degree and inclination angle of trough 3, controller 4
The amplitude of the feeder 2 is determined in a preliminary test and set in advance.

次いで、ホツパーに反応管1本分の計量した触
媒を入れた後、コントローラー4のスイツチを入
れて充填を開始する。触媒は設定された速度でト
ラフの前後振動により送り出され、シユートを経
て反応管に一定速度で充填される。取扱上発生す
る少量の触媒粉末は、トラフの一部に設けた網面
による篩部分7で落とし粉受け6に受ける。ホツ
パー内の触媒が全部充填されたならば、次の反応
管について同様な手順を繰り返し触媒の充填を行
う。
Next, after putting the weighed amount of catalyst for one reaction tube into the hopper, the controller 4 is turned on to start filling. The catalyst is delivered at a set speed by the back-and-forth vibration of the trough, and is filled into the reaction tube through the chute at a constant speed. A small amount of catalyst powder generated during handling is received in a powder receiver 6 by a sieve part 7 formed by a mesh surface provided in a part of the trough. Once the hopper is completely filled with catalyst, the same procedure is repeated for the next reaction tube to fill it with catalyst.

〔考案の効果〕[Effect of idea]

本考案によれば、上記のようにして充填を行う
ことにより、数千本ある反応管の充填作業につい
ても、特に熟練等を必要とせず、最短の時間で各
管について均一な充填密度とすることが出来る。
しかも、ホツパーとこのホツパーの下方に配置さ
れた反応管との間に傾斜角調整可能な電磁式フイ
ーダー付トラフと、このトラフの出口部に垂下し
て設けられていて粒状触媒を一定の落差で反応管
に落し込むシユートおよびビニールチユーブとを
設けた構成としたので、調整可能な落下速度が得
られ、この落下速度によつて調整可能でかつ均一
な充填密度が得られる。
According to the present invention, by performing the filling process as described above, it is possible to achieve a uniform packing density for each tube in the shortest possible time without requiring special skill, even when filling thousands of reaction tubes. I can do it.
In addition, there is a trough with an electromagnetic feeder whose inclination angle can be adjusted between the hopper and the reaction tube placed below the hopper, and a trough with an electromagnetic feeder that hangs down from the outlet of the trough to feed the granular catalyst at a constant height. Since the structure includes a chute and a vinyl tube for dropping into the reaction tube, an adjustable falling speed can be obtained, and an adjustable and uniform packing density can be obtained by this falling speed.

〔実施例〕〔Example〕

本考案の充填機を酸化エチレンプラントに於て
反応器の触媒詰め替え作業に使用したところ、口
径38mm、長さ12mの反応管4000本に外径7mm、長
さ10mmのリング状触媒の充填を行つて各管の空気
による流通抵抗を測定し、充填密度のチエツクを
行つたところ、全反応管の96%はバラツキの巾が
±3%以内であつた。これは酸化エチレンプロセ
スの基準値に充分入るものであり、従来の他の充
填機では全反応管の80〜90%が±3%以内に入る
のと比較して非常に好成積であつた。尚、この作
業に於て特定の熟練者は全く必要としなかつた。
When the filling machine of the present invention was used for catalyst refilling of reactors at an ethylene oxide plant, 4,000 reaction tubes with a diameter of 38 mm and a length of 12 m were filled with ring-shaped catalysts with an outer diameter of 7 mm and a length of 10 mm. When the flow resistance due to air in each tube was measured and the packing density was checked, it was found that 96% of all reaction tubes had variations within ±3%. This is well within the standard value for the ethylene oxide process, and compared to other conventional filling machines where 80 to 90% of all reaction tubes fall within ±3%, this was an extremely favorable filling rate. . Note that this work did not require any specific skilled personnel.

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

第1図は本考案の実施の1例を示す説明図であ
る。 1……ホツパー、2……電磁式フイーダー、3
……トラフ、4……コントローラー、5……トラ
フ傾斜角調節ハンドル、6……粉受け、7……金
網部分、8……上部シユート、9……ビニルチユ
ーブ、10……スプリング、11……架台、12
……触媒量調節ダンパー、13……反応管側シユ
ート、14……反応管。
FIG. 1 is an explanatory diagram showing one example of implementation of the present invention. 1...Hopper, 2...Electromagnetic feeder, 3
... Trough, 4 ... Controller, 5 ... Trough inclination angle adjustment handle, 6 ... Powder receiver, 7 ... Wire mesh part, 8 ... Upper chute, 9 ... Vinyl tube, 10 ... Spring, 11 ... trestle, 12
... Catalyst amount adjustment damper, 13 ... Reaction tube side chute, 14 ... Reaction tube.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] ホツパーとこのホツパーの下方に配置された反
応管との間に傾斜角調整可能な電磁式フイーダー
付トラフと、このトラフの出口部に垂下して設け
られていて粒状触媒を一定の落差で反応管に落し
込むシユートおよびビニールチユーブとを設けた
ことを特徴とする触媒充填機。
A trough with an electromagnetic feeder whose inclination angle can be adjusted is installed between the hopper and the reaction tube placed below the hopper, and a trough with an electromagnetic feeder is provided hanging from the outlet of the trough to feed the granular catalyst into the reaction tube at a constant height. A catalyst filling machine characterized by being equipped with a chute and a vinyl tube.
JP19945783U 1983-12-28 1983-12-28 catalyst filling machine Granted JPS60112338U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19945783U JPS60112338U (en) 1983-12-28 1983-12-28 catalyst filling machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19945783U JPS60112338U (en) 1983-12-28 1983-12-28 catalyst filling machine

Publications (2)

Publication Number Publication Date
JPS60112338U JPS60112338U (en) 1985-07-30
JPH0133152Y2 true JPH0133152Y2 (en) 1989-10-09

Family

ID=30759397

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19945783U Granted JPS60112338U (en) 1983-12-28 1983-12-28 catalyst filling machine

Country Status (1)

Country Link
JP (1) JPS60112338U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998032529A1 (en) * 1997-01-23 1998-07-30 Nippon Shokubai Co., Ltd. Method of feeding granular material and its feeder
US7850928B2 (en) 2001-01-25 2010-12-14 Nippon Shokubai Co., Ltd. Fixed-bed shell-and-tube reactor and its usage

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009521370A (en) * 2005-12-21 2009-06-04 キャタリスト・サービシーズ・インコーポレイテッド Providing automatic supply of catalyst and / or particulates to any filling system used to fill the tube
FR2996784B1 (en) * 2012-10-17 2015-10-16 IFP Energies Nouvelles SYSTEM FOR CHARGING CATALYST DENSE IN BAIONNETTE TUBES FOR VAPOREFORMING EXCHANGER REACTOR USING SOFT AND REMOVABLE SLOW RETRACTORS

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5524516A (en) * 1978-08-10 1980-02-21 Babcock Hitachi Kk Drawing off unit for dust-containing particle

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5524516A (en) * 1978-08-10 1980-02-21 Babcock Hitachi Kk Drawing off unit for dust-containing particle

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998032529A1 (en) * 1997-01-23 1998-07-30 Nippon Shokubai Co., Ltd. Method of feeding granular material and its feeder
CN1120039C (en) * 1997-01-23 2003-09-03 株式会社日本触媒 Method of feeding granular material and its feeder
US7850928B2 (en) 2001-01-25 2010-12-14 Nippon Shokubai Co., Ltd. Fixed-bed shell-and-tube reactor and its usage

Also Published As

Publication number Publication date
JPS60112338U (en) 1985-07-30

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