JPS5932178B2 - Multi-hole tube-encased screen tube - Google Patents
Multi-hole tube-encased screen tubeInfo
- Publication number
- JPS5932178B2 JPS5932178B2 JP56177901A JP17790181A JPS5932178B2 JP S5932178 B2 JPS5932178 B2 JP S5932178B2 JP 56177901 A JP56177901 A JP 56177901A JP 17790181 A JP17790181 A JP 17790181A JP S5932178 B2 JPS5932178 B2 JP S5932178B2
- Authority
- JP
- Japan
- Prior art keywords
- catalyst
- pipe
- screen
- tube
- distributor
- 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
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
- B01J4/00—Feed or outlet devices; Feed or outlet control devices
-
- 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
- B01J8/0278—Feeding reactive fluids
-
- 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
- B01J8/04—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 the fluid passing successively through two or more beds
- B01J8/0492—Feeding reactive fluids
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)
- Physical Or Chemical Processes And Apparatus (AREA)
Description
【発明の詳細な説明】
この発明は充填塔式の触媒反応装置、脱臭装置などにお
いて充填塔内に設置されるディストリビュータ(液分配
器)あるいはコレクター(果液器)として用いることが
できるスクリーン筒に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a screen tube that can be used as a distributor (liquid distributor) or collector (juice container) installed in a packed column in a packed column type catalytic reaction device, deodorizing device, etc. .
充填塔式の触媒反応装置は例えば第1図に示すように、
塔1内に設置されたスクリーン状の触媒受2上に触媒3
を充填し、その上方に液体、ガス等所定の流体(ここで
は便宜上液体を例にとって説明する)を供給するディス
トリビュ−タ4を設置して構成されるもので、ディスト
リビュータ4に形成した多数の小孔4aから液体を分散
滴下させ、触媒3を適して反応させ、反応液を触媒受2
を介して出口1aから取出すようにしている。For example, as shown in Fig. 1, a packed column type catalytic reaction apparatus
A catalyst 3 is placed on a screen-shaped catalyst receiver 2 installed in the column 1.
The device is constructed by installing a distributor 4 above which supplies a predetermined fluid such as liquid or gas (here, liquid will be explained as an example for convenience). The liquid is dispersed and dripped from the small hole 4a, the catalyst 3 is reacted appropriately, and the reaction liquid is transferred to the catalyst receiver 2.
The sample is taken out from the outlet 1a via the outlet 1a.
このように従来の触媒反応装置はディストリビュータと
触媒受が別々に設置される構造となっているが、このよ
うな構造は充填塔が大規模となり、充填する触媒層が多
層になると触媒受も多数必要となり、構造が複雑でコス
ト高となる上に、触媒が多層に分断されると触媒が充填
されていない空間も多(なり充填塔内の空間の利用効率
も良(ない。In this way, conventional catalytic reaction equipment has a structure in which the distributor and catalyst receiver are installed separately, but in such a structure, the packed tower is large-scale, and when the number of catalyst layers to be packed becomes multi-layered, the number of catalyst receivers becomes large. In addition, if the catalyst is divided into multiple layers, there will be many spaces that are not filled with catalyst, and the space in the packed column will not be used efficiently.
またディストリビュータは液が均等に流出することを必
要とするためその取付工事は極めて面倒でありディスト
リビュータを多数取付けるための工事に要する労力は極
めて大きい。Furthermore, since the distributor requires that the liquid flow out evenly, the installation work is extremely troublesome, and the work required to install a large number of distributors is extremely large.
この発明は多層触媒充填塔型触媒反応装置の上記難点を
解決することを目的としてなされたものであって、流体
の分配、集合機能と触媒保持機能とを兼ね備えた新規な
構成のスクリーン筒を触媒中に埋設することにより、従
来必須とされていた触媒受けを必要とせず、またディス
トリビュータの取付工事に多大の労力を必要とせず、し
かも触媒を一層化することにより充填塔内の空間利用率
を大幅に改善しようとするものである。This invention was made with the aim of solving the above-mentioned difficulties of the multilayer catalyst-packed tower type catalytic reaction apparatus, and it uses a screen cylinder with a novel configuration that has both fluid distribution and collection functions and catalyst holding functions as a catalytic converter. By embedding the catalyst inside the column, there is no need for a catalyst receiver, which was previously considered essential, and there is no need for a large amount of labor to install the distributor.Furthermore, by arranging the catalyst in one layer, the space utilization rate inside the packed column can be improved. This is a major improvement.
ディストリビュータを触媒中に埋設する場合問題となる
のは、ディストリビュータから放散される流体が乱流を
生じると触媒中に均一に分布されないこと、および特に
触媒を常時移動させる方式の反応装置においては触媒の
移動が円滑に行われずまた目Δ吉りを起すおそれがある
ことである。The problem when embedding a distributor in a catalyst is that if the fluid dissipated from the distributor causes turbulence, it will not be uniformly distributed in the catalyst, and especially in a reactor where the catalyst is constantly moved, There is a risk that the movement will not be carried out smoothly and that a mishap may occur.
本発明においては、多孔パイプを所定の間隔をおいて包
囲するスクリーン筒を適宜のピッチで巻かれたワイヤと
これを支持するサポート部材で形成することにより乱流
と目詰りを完全に防止することができる。In the present invention, turbulent flow and clogging can be completely prevented by forming a screen tube that surrounds the porous pipe at a predetermined interval from wire wound at an appropriate pitch and a support member that supports the screen tube. Can be done.
以下、この発明の実施例を添付図面を参照して詳しく説
明する。Embodiments of the present invention will be described in detail below with reference to the accompanying drawings.
第2図はこの発明の基本的な実施例を示すものf−丸A
−笛9[ヅのスフ1j−ン僧Inπ松(5、て サポー
トロッド11はワイヤ12を支持するためのもので、複
数本が適宜の間隔で円筒状に配置されている。Figure 2 shows a basic embodiment of this invention f-circle A
The support rods 11 are for supporting the wires 12, and a plurality of them are arranged in a cylindrical shape at appropriate intervals.
ワイヤには断面が(さび形のものでロッド11上に適宜
のピッチ(触媒等が入り込まない間隔)でらせん状に巻
付けており、各ワイヤ内にはスリット12aが形成され
ている。The wires have a wedge-shaped cross section and are spirally wound around the rod 11 at an appropriate pitch (an interval that does not allow the catalyst or the like to enter), and a slit 12a is formed in each wire.
ロッド11とワイヤ12とにより構成される円筒(両端
は閉じられている)内にはその軸上にパイプ13が配置
されている。A pipe 13 is disposed on the axis of a cylinder (closed at both ends) made up of a rod 11 and a wire 12.
このパイプ13には内周から外周に通じる貫通孔13a
が全面にわたって多数開設されている。This pipe 13 has a through hole 13a that communicates from the inner circumference to the outer circumference.
are being opened in large numbers throughout the area.
パイプ13の末端は閉じられている。パイプ13には枝
管14が取付けられ、配管15から結合フランジ16、
枝管14を介してパイプ13につながる連通路が形成さ
れている。The end of the pipe 13 is closed. A branch pipe 14 is attached to the pipe 13, and a connecting flange 16,
A communication path connected to the pipe 13 via the branch pipe 14 is formed.
パイプ13にはサポートディスク17が適宜の間隔をお
いて固定されている。Support disks 17 are fixed to the pipe 13 at appropriate intervals.
このサポートディスク17はサポートロッド11を内側
から支持するとともに、パイプ13を円筒の軸上に保持
する働きをするものである。This support disk 17 functions to support the support rod 11 from the inside and to hold the pipe 13 on the axis of the cylinder.
サポートディスク17にはそれによって隔絶された円筒
内の空間を連通させるだめの流通孔17aが開設されて
いる。The support disk 17 is provided with a communication hole 17a for communicating the isolated space within the cylinder.
第2図のスクリーン筒12を製造する場合は、まずパイ
プ13にサポートディスク17を適宜の間隔で差込み、
次いでサポートディスク17のまわりにサポートロッド
11を適宜の間隔でスポット溶接などにより固定し、更
にそのまわりにワイヤ2を適宜のピッチで巻付けてスポ
ット溶接などにより固定すればよい。When manufacturing the screen tube 12 shown in FIG. 2, first insert the support disks 17 into the pipe 13 at appropriate intervals,
Next, the support rods 11 are fixed around the support disk 17 at appropriate intervals by spot welding or the like, and the wires 2 are further wound around the support rods 11 at appropriate pitches and fixed by spot welding or the like.
またワイヤ12をサポートロッド11のまわりに巻回し
てワイヤ120弾性により固定するようにすれば溶接を
省くことも可能である。Furthermore, welding can be omitted by winding the wire 12 around the support rod 11 and fixing it by the elasticity of the wire 120.
第2図のスクリーン筒10を充填塔式の触媒反応装置の
ディストリビュータ(分配管)として使用する場合の一
例を第3図に示す(aは正面図、bはaのA−A断面図
、CはaのB−B断面図である)。An example of the case where the screen tube 10 shown in FIG. 2 is used as a distributor (distribution pipe) of a packed column type catalytic reaction device is shown in FIG. is a BB sectional view of a).
この実施例においては、テイス) IJピユータ21を
上下2段に配列している。In this embodiment, the IJ computers 21 are arranged in two stages, upper and lower.
ディストリビュータ21は第3図すに示すように配管1
5からフランジ16および枝管14を介して、複数のス
クリーン筒10を枝状に配している。The distributor 21 is connected to the piping 1 as shown in Figure 3.
A plurality of screen cylinders 10 are arranged in a branch shape from 5 through flanges 16 and branch pipes 14.
各スクリーン筒10は両端がそれぞれ蓋23により閉じ
られ、充填塔20の内面に形成された7ランジ20a上
に固定されている。Each screen cylinder 10 is closed at both ends with a lid 23, and is fixed on seven flanges 20a formed on the inner surface of the packed tower 20.
ディストリビュータ21を以上のように設置ししたら、
充填塔20の頂部に開設された開口部20cから触媒2
5をディストリビュータ21が完全に埋もれる高さまで
注入する。After installing the distributor 21 as above,
The catalyst 2 is introduced through the opening 20c provided at the top of the packed tower
5 to the height where the distributor 21 is completely buried.
これにより、充填塔20内の準備はすべて完了し、ディ
ストリビュータ21の配管15に所定の液体を注入すれ
ば、各スクリーン筒10内においてパイプ13の孔13
aからこの液体が四方に放散される。As a result, all the preparations in the packed tower 20 are completed, and when the predetermined liquid is injected into the pipe 15 of the distributor 21, the hole 13 of the pipe 13 in each screen cylinder 10 is
This liquid is diffused in all directions from a.
この状態を第4図に示す。この図に示すようにパイプ1
3からワイヤ12までは距離があるので、単にパイプ1
3をそのまま埋め込んで放散する場合に比べて、広い範
囲に均一に放散することができる。This state is shown in FIG. Pipe 1 as shown in this figure
Since there is a distance from wire 3 to wire 12, simply connect pipe 1
Compared to the case where 3 is directly embedded and diffused, it can be uniformly diffused over a wide range.
また液体は上下のスリット12aから上下各方向に放散
されるので上下方向に著るしい整流効果を有する。Further, since the liquid is dispersed in each direction up and down from the upper and lower slits 12a, it has a significant rectifying effect in the up and down direction.
ディストリビュータ21により放散された液体は触媒2
5内を所定の反応を行いながら下降する。The liquid diffused by the distributor 21 is transferred to the catalyst 2
5 while performing a predetermined reaction.
反応を完了した液は充填塔20の下部に配置された触媒
受げ22の開口22aを通って充填塔出口20dから取
り出される。The liquid that has completed the reaction passes through the opening 22a of the catalyst receiver 22 located at the bottom of the packed column 20 and is taken out from the packed column outlet 20d.
この実施例においては、触媒25は一層となり、途中に
空間を設ける必要がなく、充填塔内の触媒の占める容積
が増大する上に触媒受け22は一段だけ設ければすむの
で従来の装置に比べ触媒受けの設置数を減少することが
できる。In this embodiment, the catalyst 25 is in one layer, there is no need to provide a space in the middle, the volume occupied by the catalyst in the packed column increases, and only one stage of the catalyst receiver 22 is required, compared to conventional equipment. The number of catalyst receivers installed can be reduced.
上記実施例はディストリビュータ21を上下2列にした
ものであるが、ディストリビュータの列数を増加するほ
ど上記のメリットは増大することは明らかであろう。In the above embodiment, the distributors 21 are arranged in two rows, one above the other, but it is obvious that the above advantages increase as the number of rows of distributors increases.
本発明にかかる多孔管内包スクリーン筒はディストリビ
ュータとしてのみでなくコレクター(集液管)としても
用いることができる。The screen tube containing a porous tube according to the present invention can be used not only as a distributor but also as a collector (liquid collection tube).
この場合はたとえば第3図において下段のディストリビ
ュータ21をコレクターとして用い触媒層の下部に下降
した反応ずみの液をスクリーン筒を通してパイプ13内
に吸入し外部に取出すようにすればよい。In this case, for example, the lower distributor 21 in FIG. 3 may be used as a collector, and the reacted liquid that has descended to the lower part of the catalyst layer may be drawn into the pipe 13 through the screen tube and taken out to the outside.
なおこの場合第3図に示すような開口22aを有する触
媒受け22は使用せず充填塔の下部出口20dは閉じて
置(ようにする。In this case, the catalyst receiver 22 having an opening 22a as shown in FIG. 3 is not used, and the lower outlet 20d of the packed column is closed.
またこのような装置において、上下各段の多孔管内包ス
クリーン筒を一定時間ディストリピユータとして使用し
、触媒層に液を供給して所定の反応を終了した後今度は
同じ多孔管内包スクリーン筒をコレクターとして使用し
、反応ずみの液を回収するようにして、この操作を反復
するように利用することもできる。In addition, in such an apparatus, the upper and lower perforated screen cylinders are used as a distributor for a certain period of time, and after the liquid is supplied to the catalyst layer and the specified reaction is completed, the same perforated screen cylinders are used again. This operation can also be repeated by using it as a collector to collect the reacted liquid.
なお、スクリーン筒10の配列は第3図のような横置き
にかぎらず、第5図aのようにスクリーンに第1図のス
クリーン2を用い、その上にディストリビュータ10を
縦置きにしたり、第5図すのように千鳥格子状に置くこ
ともできる。Note that the arrangement of the screen tubes 10 is not limited to the horizontal arrangement as shown in FIG. 3, but also the screen 2 of FIG. They can also be arranged in a houndstooth pattern as shown in Figure 5.
あるいは同じ横置きでも第5図Cのようにジグザグにす
ることもできる。Alternatively, even if it is placed horizontally, it can be placed in a zigzag pattern as shown in FIG. 5C.
第6図の実施例はサポートディスク17の相互間にサポ
ートビーム30を渡して更に強度を高めるようにしたも
のである。In the embodiment shown in FIG. 6, a support beam 30 is provided between the support disks 17 to further increase the strength.
第7図の実施例はサポートビームとして幅の広いもの3
1A、31Bを用い、半円状に分断したワイヤ2を一方
のサポートビーム31Aから他方のサポートビーム31
Bにかけてそれぞれ固着するようにしたものである。The embodiment shown in Fig. 7 has a wide support beam 3.
1A and 31B, the wire 2 divided into semicircles is connected from one support beam 31A to the other support beam 31.
B is fixed to each other.
第8図の実施例はサポートビーム32により円筒内の空
間を2つに分割し、それぞれにパイプ13−1,112
を配置するようにしたものである。In the embodiment shown in FIG. 8, the space inside the cylinder is divided into two by the support beam 32, and the pipes 13-1 and 112 are respectively divided into two parts.
It is arranged so that
なお、上記実施例のスクリーン筒は断面を円筒状とした
がこれに限らず、だ円あるいはその8角筒、6角筒等他
の筒形とすることもできる。Although the screen cylinder in the above embodiment has a cylindrical cross section, the cross section is not limited to this, but it can also be an ellipse, or other cylindrical shapes such as an octagonal cylinder or a hexagonal cylinder.
またワイヤ12の断面形状は(さび形のものが好適であ
るがこれに限らず、方形、円形等適宜の形状のものを用
いることができる。Further, the cross-sectional shape of the wire 12 is preferably wedge-shaped, but is not limited to this, and any suitable shape such as rectangular or circular can be used.
また、上記実施例では触媒反応装置に適用した場合につ
いて示したが、その他の化学プロセス例えば脱臭装置、
沢過装置等広い範囲の用途に用いることができる。In addition, although the above example shows the case where it is applied to a catalytic reaction device, it is also applicable to other chemical processes such as a deodorizing device,
It can be used in a wide range of applications such as filtration equipment.
第9図はp過装置に適用する場合の一例で、沈でん層4
1の底部42にスクリーン筒10を縦に置き、この底部
42をつきぬけてパイプ13を引出し、ワイヤ10で沢
過した液をこのパイプ13を経て取出すようにしたもの
である。Figure 9 shows an example of the case where it is applied to a p-filtration device.
A screen tube 10 is placed vertically on the bottom 42 of a pipe 1, a pipe 13 is drawn out through the bottom 42, and the liquid that has passed through the wire 10 is taken out through the pipe 13.
第10図は攪拌しながら流体を分配および集合させるよ
うにしたものである。FIG. 10 shows a system in which the fluid is distributed and collected while being stirred.
ここでは配管51を塔52の中心に置き、その下端にス
クリーン筒10を放射状に取付けて、配管51を回転し
て攪拌しながら分配および集合を行なうようにしている
。Here, the pipe 51 is placed at the center of the column 52, and the screen cylinders 10 are radially attached to the lower end of the pipe 51, so that the pipe 51 is rotated to perform distribution and collection while stirring.
第11図はワイヤ12−1 、12−2 。12−3を
多層に巻き、それぞれの間に異なる触媒を注入し、パイ
プ2から放出された液体が外方向に広がるにしたがって
各層で順次反応が行なわれるようにしたものである。FIG. 11 shows wires 12-1 and 12-2. 12-3 is wound in multiple layers, and a different catalyst is injected between each layer, so that as the liquid discharged from the pipe 2 spreads outward, reactions occur in each layer in sequence.
以上説明したようにこの発明のスクリーン筒はディスト
リビュータとしても、あるいはコレクターとしても用い
ることができ広範囲の目的に使用することができる。As explained above, the screen cylinder of the present invention can be used both as a distributor and as a collector, and can be used for a wide range of purposes.
特にディストリビュータとして利用した場合触媒層が分
断されず充填塔内の空間の利用率を高めることができる
上に多数の触媒受けを節約することができる。Particularly when used as a distributor, the catalyst bed is not divided, which increases the space utilization rate in the packed column and also saves a large number of catalyst receivers.
また多孔パイプを所定の間隔を置いて包囲するスクリー
ン筒を適宜のピッチで巻かれたワイヤとこれを支持する
サポート部材で形成したので、流体の分配および集合が
非常に効率良(行うことができ、乱流の発生を完全に防
止することができる。In addition, since the screen tubes that surround the porous pipes at predetermined intervals are formed using wires wound at appropriate pitches and support members that support the screen tubes, fluid distribution and collection are extremely efficient. , the occurrence of turbulence can be completely prevented.
さらに触媒移動方式の装置に用いても触媒の移動が円滑
に行われ目詰りを生じない等の優れた効果を有するもの
である。Furthermore, even when used in a catalyst transfer type device, the catalyst has excellent effects such as smooth transfer of the catalyst and no clogging.
第1図は従来における充填塔式触媒反応装置を示す縦断
面図、第2図はこの発明の一実施例を示す一部切欠き斜
視図、第3図は第3図のスクリーン筒を充填塔式触媒反
応装置に適用した一例を示す図でaは正面図、bは平面
図、CはaのA−A断面図、第4図は第3図のディスト
リビュータ21から流体が放散される状態を示す図、第
5図は充填塔内におけるスクリーン筒の配列し方の別の
例を示す図、第6図、第7図、第8図はこの発明の他の
実施例を示す一部切欠き斜視図、第9図、第10図、第
11図はこの発明の他の応用例を示す縦断面図である。
10・・・・・・スクリーン筒、11・・・・・・サポ
ートロッド、12・・・・・・ワイヤ、13・・−・・
・パイプ、14・−・・−枝管、15・−・・・配管、
17・・・・・・サポートディスク。FIG. 1 is a vertical cross-sectional view showing a conventional packed column type catalytic reaction apparatus, FIG. 2 is a partially cutaway perspective view showing an embodiment of the present invention, and FIG. Figure 4 shows an example of the application to a type catalytic reaction device, in which a is a front view, b is a plan view, C is a sectional view taken along line A-A in a, and Figure 4 shows a state in which fluid is dissipated from the distributor 21 in Figure 3. Figure 5 is a diagram showing another example of how the screen tubes are arranged in the packed column, and Figures 6, 7, and 8 are partially cutaway diagrams showing other embodiments of the present invention. The perspective view, FIG. 9, FIG. 10, and FIG. 11 are longitudinal sectional views showing other application examples of the present invention. 10... Screen tube, 11... Support rod, 12... Wire, 13...
・Pipe, 14... Branch pipe, 15... Piping,
17...Support disk.
Claims (1)
まわりに適宜のピッチで巻かれたワイヤと、内周から外
周にわたって複数の貫通孔が開設され、前記ロッドとワ
イヤとにより形成される筒内の空間にどいて核部の内面
と適宜の間隔をおいた位置に核部に沿って配置されたパ
イプと、前記筒内において核部に沿って適宜の間隔で配
置され、核部の内面を支持するとともに、前記パイプを
前記空間内の位置に保持するサポート部材とを具えた多
孔管内包式スクリーン筒。1 A plurality of rods arranged in a cylindrical shape, a wire wound around the rods at an appropriate pitch, and a plurality of through holes are opened from the inner circumference to the outer circumference, and are formed by the rods and the wires. A pipe is placed along the core at an appropriate distance from the inner surface of the core in the space inside the cylinder, and a pipe is placed along the core at an appropriate distance within the cylinder and is located at an appropriate distance from the inner surface of the core. A perforated tube-enclosing screen tube comprising a support member that supports an inner surface and holds the pipe in a position within the space.
Priority Applications (11)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56177901A JPS5932178B2 (en) | 1981-11-06 | 1981-11-06 | Multi-hole tube-encased screen tube |
AU90062/82A AU537473B2 (en) | 1981-11-06 | 1982-11-01 | Distributor/collector assembly for catalyst reactor |
GB08231214A GB2110106B (en) | 1981-11-06 | 1982-11-01 | Distributor/collector assembly |
KR8204942A KR880001995B1 (en) | 1981-11-06 | 1982-11-02 | Distributor or collector assembly |
BR8206427A BR8206427A (en) | 1981-11-06 | 1982-11-05 | DISTRIBUTOR / COLLECTOR SET |
CA000415019A CA1201876A (en) | 1981-11-06 | 1982-11-05 | Distributor/collector assembly |
FR8218569A FR2515982B1 (en) | 1981-11-06 | 1982-11-05 | DISTRIBUTOR OR COLLECTOR DEVICE, PARTICULARLY FOR A COLUMN-TYPE CATALYTIC REACTOR OR THE LIKE |
DE3240987A DE3240987C2 (en) | 1981-11-06 | 1982-11-05 | Distribution and collection device |
IT24109/82A IT1218329B (en) | 1981-11-06 | 1982-11-05 | COLLECTOR DISTRIBUTOR COMPLEX FOR USE IN A COLUMN REACTOR FOR CATALYTIC PROCESSES OR SIMILAR DEVICES |
BE2/59900A BE894919A (en) | 1981-11-06 | 1982-11-05 | DISTRIBUTOR-COLLECTOR ASSEMBLY |
AR291213A AR228692A1 (en) | 1981-11-06 | 1982-11-05 | SUITABLE DISTRIBUTOR / COLLECTOR ASSEMBLY FOR USE IN A TYPE OF CATALYST REACTOR COLUMN, DEODORIZATION DEVICE, OR SIMILAR DEVICE |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56177901A JPS5932178B2 (en) | 1981-11-06 | 1981-11-06 | Multi-hole tube-encased screen tube |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5879537A JPS5879537A (en) | 1983-05-13 |
JPS5932178B2 true JPS5932178B2 (en) | 1984-08-07 |
Family
ID=16039037
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP56177901A Expired JPS5932178B2 (en) | 1981-11-06 | 1981-11-06 | Multi-hole tube-encased screen tube |
Country Status (11)
Country | Link |
---|---|
JP (1) | JPS5932178B2 (en) |
KR (1) | KR880001995B1 (en) |
AR (1) | AR228692A1 (en) |
AU (1) | AU537473B2 (en) |
BE (1) | BE894919A (en) |
BR (1) | BR8206427A (en) |
CA (1) | CA1201876A (en) |
DE (1) | DE3240987C2 (en) |
FR (1) | FR2515982B1 (en) |
GB (1) | GB2110106B (en) |
IT (1) | IT1218329B (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101147852B (en) * | 2006-09-20 | 2010-09-01 | 中国石油化工股份有限公司 | Multistage insulation fixed bed reactor |
DE102006060507A1 (en) * | 2006-12-19 | 2008-06-26 | Basf Se | Reactor for carrying out a reaction between two fluid educts on a catalyst bed with premixing of the fluid educts in a mixing device |
DE102006060509A1 (en) * | 2006-12-19 | 2008-06-26 | Basf Se | Reactor for continuous oxide hydrogenation of feed gas flow of saturated hydrocarbons on moving catalyst bed, comprises four reactor sections, which are separated from each other and split into sub-sections by alternating deflector plates |
TW200936245A (en) * | 2007-10-30 | 2009-09-01 | Basf Se | Horizontal reactor for reacting a fluid feed stream with a fluid oxidant stream in the presence of a solid catalyst |
FR2974739B1 (en) * | 2011-05-03 | 2016-03-11 | Commissariat Energie Atomique | SOLID REACTOR MODULE / HEAT PUMP COMPRISING GAS DIFFUSERS WITH REDUCED SHUTDOWN HAZARDS |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AT139112B (en) * | 1931-10-17 | 1934-10-25 | Houdry Process Corp | Device for distributing a medium in a contact mass filling a reaction device. |
FR1529137A (en) * | 1966-10-28 | 1968-06-14 | Exxon Research Engineering Co | Fluid flow distributor |
US3592613A (en) * | 1968-12-30 | 1971-07-13 | Universal Oil Prod Co | Apparatus for fluid distribution in a fluid-solids contacting chamber |
GB2065492B (en) * | 1979-12-21 | 1983-10-19 | Uop Inc | Fluid distributor for fixed-bed catalytic reaction zones |
-
1981
- 1981-11-06 JP JP56177901A patent/JPS5932178B2/en not_active Expired
-
1982
- 1982-11-01 GB GB08231214A patent/GB2110106B/en not_active Expired
- 1982-11-01 AU AU90062/82A patent/AU537473B2/en not_active Ceased
- 1982-11-02 KR KR8204942A patent/KR880001995B1/en active
- 1982-11-05 IT IT24109/82A patent/IT1218329B/en active
- 1982-11-05 AR AR291213A patent/AR228692A1/en active
- 1982-11-05 DE DE3240987A patent/DE3240987C2/en not_active Expired
- 1982-11-05 BE BE2/59900A patent/BE894919A/en not_active IP Right Cessation
- 1982-11-05 CA CA000415019A patent/CA1201876A/en not_active Expired
- 1982-11-05 FR FR8218569A patent/FR2515982B1/en not_active Expired
- 1982-11-05 BR BR8206427A patent/BR8206427A/en not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
DE3240987C2 (en) | 1985-09-19 |
KR880001995B1 (en) | 1988-10-11 |
KR840002257A (en) | 1984-06-25 |
GB2110106A (en) | 1983-06-15 |
FR2515982A1 (en) | 1983-05-13 |
JPS5879537A (en) | 1983-05-13 |
CA1201876A (en) | 1986-03-18 |
BE894919A (en) | 1983-03-01 |
BR8206427A (en) | 1983-09-27 |
DE3240987A1 (en) | 1983-07-14 |
IT8224109A0 (en) | 1982-11-05 |
IT1218329B (en) | 1990-04-12 |
AR228692A1 (en) | 1983-03-30 |
FR2515982B1 (en) | 1987-04-30 |
AU537473B2 (en) | 1984-06-28 |
GB2110106B (en) | 1985-04-24 |
AU9006282A (en) | 1983-05-26 |
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