JPS642156Y2 - - Google Patents

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Publication number
JPS642156Y2
JPS642156Y2 JP18298483U JP18298483U JPS642156Y2 JP S642156 Y2 JPS642156 Y2 JP S642156Y2 JP 18298483 U JP18298483 U JP 18298483U JP 18298483 U JP18298483 U JP 18298483U JP S642156 Y2 JPS642156 Y2 JP S642156Y2
Authority
JP
Japan
Prior art keywords
discharge port
fluidized bed
discharge pipe
lid body
downcomer
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
JP18298483U
Other languages
Japanese (ja)
Other versions
JPS6092097U (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 JP18298483U priority Critical patent/JPS6092097U/en
Publication of JPS6092097U publication Critical patent/JPS6092097U/en
Application granted granted Critical
Publication of JPS642156Y2 publication Critical patent/JPS642156Y2/ja
Granted legal-status Critical Current

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  • Crucibles And Fluidized-Bed Furnaces (AREA)

Description

【考案の詳細な説明】 〔考案の技術分野〕 本考案は容器内に充填された粉粒体をガス体の
流入によつて流動化する流動層装置において、再
生装置等へ向つて排出される粉粒体中に大塊が混
入するのを防止する装置に関するものである。
[Detailed Description of the Invention] [Technical Field of the Invention] The present invention is a fluidized bed device that fluidizes powder and granular material filled in a container by the inflow of gas, which is discharged toward a regenerator or the like. The present invention relates to a device that prevents large lumps from being mixed into powder or granular materials.

〔従来技術〕[Prior art]

容器内に粉粒体を充填し、多孔板などの整流器
を経てガス体を流入させると、流速が小さい間は
粒子層が静止しているが、流速が増加するにした
がつて粒子群の運動が活発になり、遂には液体が
沸騰しているように流動する。このような状態に
する装置を流動層装置と称し、粒体としての触媒
を流動させるようにした流動層装置は、反応装置
など各種の化学装置類に広く用いられている。
When a container is filled with powder and granular material and a gas is introduced through a perforated plate or other flow straightener, the particle layer remains stationary while the flow rate is low, but as the flow rate increases, the particle group's movement becomes more active and eventually the liquid begins to flow as if it were boiling. An apparatus that creates this state is called a fluidized bed apparatus, and fluidized bed apparatuses that fluidize granular catalysts are widely used in various chemical equipment such as reactors.

この種の流動層装置においては、劣化した触媒
を再生装置へ導いて再生することが行なわれてお
り、この劣化した触媒は、一般に排出口からダウ
ンカマと称する搬送管内に落下してダウンカマ内
を再生装置へ搬送される。しかしながら、従来の
流動層装置においては、ダウンカマ内へ大塊が混
入することがあつて、これがダウンカマに詰り搬
送を阻害するという欠点があつた。
In this type of fluidized bed equipment, the deteriorated catalyst is guided to a regenerator to be regenerated, and the deteriorated catalyst generally falls from the discharge port into a conveying pipe called a downcomer and is regenerated inside the downcomer. Transported to the device. However, the conventional fluidized bed apparatus has the disadvantage that large lumps may get mixed into the downcomer, clogging the downcomer and hindering conveyance.

〔考案の概要〕[Summary of the idea]

本考案は以上のような点に鑑みなされたもの
で、流動層内で開口する排出管の上向開口端縁
と、この端縁に支持体で支持させた蓋体との間に
形成される側方への円筒状開口部に、この開口部
側が上下同幅の短冊状で外端側が下端へ向つて小
幅となるくさび状に形成された複数個の分級体を
並設し、所定粒度以下の粒体は隣接分級体間のす
き間から排出管内へ流入させ所定粒度以上の大塊
は分級体に沿つて排出管外へ落下させるように構
成することにより、排出管内へ大塊が混入排出さ
れることによる排出管の詰りを解消した流動層装
置の排出口における大塊混入防止装置を提供する
ものである。以下、本考案の実施例を図面に基い
て詳細に説明する。
The present invention was developed in view of the above points, and is formed between the upward opening edge of the discharge pipe that opens in the fluidized bed and the lid body supported on this edge by a support body. In a cylindrical opening to the side, a plurality of wedge-shaped classification bodies are arranged side by side, with the opening side having the same width on the top and bottom, and the outer end side becoming narrower toward the bottom end. By configuring the system so that the particles flow into the discharge pipe through the gaps between adjacent classified bodies, and the large lumps larger than a predetermined particle size fall out of the discharge pipe along the classified bodies, large lumps are mixed into the discharge pipe and discharged. The present invention provides a device for preventing large lumps from being mixed in at the discharge port of a fluidized bed apparatus, which eliminates the clogging of the discharge pipe caused by the clogging of the discharge pipe. Embodiments of the present invention will be described in detail below with reference to the drawings.

〔実施例〕 第1図ないし第4図は本考案に係る大塊混入防
止装置の一実施例を示し、第1図はこれを実施し
た流動層装置の概略構成図、第2図は排出管上端
部の拡大正面図、第3図は分級体の正面図と平面
図、第4図は同じく斜視図である。図において、
流動層装置1の密閉タンク2内に設けられた格子
3上には、触媒4が蓄えられており、タンク2の
下端部には、ガス入口5が開口されている。6は
再生装置7に接続された排出管としてのダウンカ
マであつて、タンク2内の格子3上方に係入され
ており、その上端排出口には、第2図に拡大して
示す大塊混入防止装置8が設けられている。すな
わち、ダウンカマ6の排出口端縁6aを円周方向
に3等分する箇所には、支持体9が溶着によつて
立設されていて、傘下に形成された蓋体10が、
この支持体9の上端部に溶着支持されており、蓋
体10の下端部内側には、ダウンカマ6の排出口
と同径の環状に形成された支持環10aが一体形
成されている。こうすることによつて支持環10
aと排出口端縁6aとの間には、円筒状の空間部
が側方へ向つて開口され、この開口部には複数個
の分級体としてのスリツタ11が、上下両端部を
支持環10aと排出口端縁6aとに溶着されて所
定の等間隔で並列されている。なお第2図ではこ
のスリツタ11を2個のみ示し残りの図示が省略
されている。スリツタ11は全体がほゞ角柱状を
なしており、その上端部には、蓋体10の下端部
裏側に形成された断面三角形状の空間部へ係入さ
れる傾斜面11aが形成されているとともに、正
面視において開口部側が短冊状で手前側である外
側が下端へ向つて小幅となるようなくさび状に形
成されている。こうすることにより隣接するスリ
ツタ11間の間隔は、開口部側では上から下まで
同幅であるが、外側では図に符号t1,t2で示すよ
うに下端へ向うにしたがつて大きくなつている。
なお、最大間隔t2は大きく図示されているが、実
施例の場合2〜3mmであつて触媒の粒径によつて
t1,t2が設定される。
[Example] Figures 1 to 4 show an example of the large lump contamination prevention device according to the present invention. FIG. 3 is an enlarged front view of the upper end, a front view and a plan view of the classification body, and FIG. 4 is a perspective view. In the figure,
A catalyst 4 is stored on a grid 3 provided in a closed tank 2 of the fluidized bed apparatus 1, and a gas inlet 5 is opened at the lower end of the tank 2. Reference numeral 6 denotes a downcomer as a discharge pipe connected to the regenerating device 7, which is inserted above the lattice 3 in the tank 2, and the upper end discharge port is filled with large lumps mixed in as shown in an enlarged view in Fig. 2. A prevention device 8 is provided. That is, a support body 9 is erected by welding at a location that divides the discharge port edge 6a of the downcomer 6 into three equal parts in the circumferential direction, and a lid body 10 formed under the support body 9 is erected by welding.
It is supported by welding to the upper end of the support body 9, and a support ring 10a formed in an annular shape having the same diameter as the discharge port of the downcomer 6 is integrally formed inside the lower end of the lid body 10. By doing this, the support ring 10
A cylindrical space is opened laterally between the outlet edge 6a and the outlet edge 6a, and a plurality of slitters 11 as classifiers are installed in this opening with support rings 10a at both upper and lower ends. and the outlet edge 6a, and are arranged in parallel at predetermined equal intervals. In addition, in FIG. 2, only two of these slitters 11 are shown, and illustration of the remaining slitters 11 is omitted. The slit 11 has a substantially prismatic shape as a whole, and an inclined surface 11a is formed at the upper end thereof to be inserted into a space having a triangular cross section formed on the back side of the lower end of the lid body 10. In addition, when viewed from the front, the opening side is shaped like a strip, and the outer side, which is the front side, is formed into a wedge shape that becomes narrower toward the lower end. By doing this, the spacing between adjacent slits 11 is the same width from top to bottom on the opening side, but becomes larger on the outside as it goes toward the bottom end, as shown by symbols t 1 and t 2 in the figure. ing.
Although the maximum spacing t 2 is shown large in the diagram, it is 2 to 3 mm in the example and varies depending on the particle size of the catalyst.
t 1 and t 2 are set.

以上のように構成された流動層装置において、
タンク2内の格子3上に触媒4を充填してガス入
口からガス体を流入させると、流速が増加するに
したがつて触媒4が流動化し、この流動化した触
媒4は化学反応などに用いられる。そして劣化し
た触媒4はダウンカマ6内を再生装置7へ搬送さ
れて再生される。この場合、触媒4は隣接するス
リツタ11間の間隙からダウンカマ6の排出口へ
流入するが、この間隙の寸法t1が触媒4の粒子径
にしたがつて設定されているので、粒子径t1以下
のもののみがダウンカマ6内へ流入する。粒子径
がt1以上の触媒4は、スリツタ11に衝突すると
間隙t1を通過できないので、下方へ向つて拡がる
スリツタ11のくさび状テーパ面に沿つて落下
し、タンク2内に戻される。
In the fluidized bed apparatus configured as above,
When a catalyst 4 is filled on a grid 3 in a tank 2 and a gas is allowed to flow in from the gas inlet, the catalyst 4 becomes fluidized as the flow rate increases, and this fluidized catalyst 4 is used for chemical reactions, etc. It will be done. The deteriorated catalyst 4 is then conveyed inside the downcomer 6 to the regenerator 7 and regenerated. In this case, the catalyst 4 flows into the discharge port of the downcomer 6 from the gap between the adjacent slitters 11, but since the dimension t 1 of this gap is set according to the particle diameter of the catalyst 4, the particle diameter t 1 Only the following items flow into the downcomer 6. When the catalyst 4 having a particle size of t 1 or more collides with the slitter 11 , it cannot pass through the gap t 1 , so it falls along the wedge-shaped tapered surface of the slitter 11 that expands downward, and is returned into the tank 2 .

〔考案の効果〕[Effect of idea]

以上の説明により明らかなように本考案によれ
ば流動層装置において、流動層内で開口する排出
管の上向開口端と、この端縁に支持体で支持させ
た蓋体との間に形成される側方への円筒状開口部
に、この開口部側が上下同幅の短冊状で外端側が
下端へ向つて小幅となるくさび状に形成された複
数個の分級体を並設することにより、所定粒度以
下の粒体のみが隣接分級体間のすき間から排出管
内へ流入し、所定粒度以上の大塊粒体は分級体に
衝突したのち、これに付着することなく下方へ向
つて拡がるスリツタのテーパ面に沿つてきわめて
円滑に落下し、タンク内へ戻されるので、排出管
内へ流入することがなく管内への大塊の詰りを完
全に防止することができ、排出管内の粒体搬送が
きわめて円滑に行なわれる。
As is clear from the above explanation, according to the present invention, in the fluidized bed apparatus, a discharge pipe is formed between the upwardly opening end of the discharge pipe that opens in the fluidized bed and the lid supported by the support on this end. By arranging in parallel a plurality of wedge-shaped classifying bodies in a cylindrical opening to the side where the opening is in the form of a strip with the same width on the top and bottom and the outer end becoming narrower toward the bottom. , only particles with a predetermined particle size or less flow into the discharge pipe through the gaps between adjacent classified bodies, and large particles with a predetermined particle size or more collide with the classified bodies and then spread downward without adhering to the slitter. Since the particles fall extremely smoothly along the tapered surface and are returned into the tank, they do not flow into the discharge pipe, completely preventing large particles from clogging the pipe, and reducing the transport of particles within the discharge pipe. It is carried out extremely smoothly.

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

第1図ないし第4図は本考案に係る流動層装置
の排出口における大塊混入防止装置の一実施例を
示し、第1図はこれを実施した流動層装置の概略
構成図、第2図は排出管上端部の拡大正面図、第
3図は分級体の正面図と平面図、第4図は同じく
斜視図である。 1……流動層装置、2……タンク、4……触
媒、6……ダウンカマ、6a……排出口端縁、8
……大塊混入防止装置、9……支持体、10……
蓋体、11……スリツタ。
1 to 4 show an embodiment of a device for preventing large lumps from being mixed in at the discharge port of a fluidized bed device according to the present invention, and FIG. 1 is a schematic configuration diagram of a fluidized bed device implementing this device, and FIG. 3 is an enlarged front view of the upper end of the discharge pipe, FIG. 3 is a front view and a plan view of the classifier, and FIG. 4 is a perspective view. DESCRIPTION OF SYMBOLS 1... Fluidized bed apparatus, 2... Tank, 4... Catalyst, 6... Downcomer, 6a... Discharge port edge, 8
...Large lump contamination prevention device, 9...Support, 10...
Lid body, 11...Suritsuta.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 排出口を上向けて流動層内に配設された排出管
の排出口端縁から複数個の支持体を上方へ突出さ
せて蓋体を支持させ、前記排出口端縁と蓋体との
間に形成される側方への円筒状開口部に、この開
口部側が上下同幅の短冊状で外端側が下端へ向つ
て小幅となるくさび状に形成された複数個の分級
体を、所定の間隔で並設したことを特徴とする流
動層装置の排出口における大塊混入防止装置。
A plurality of supports are made to protrude upward from the discharge port edge of a discharge pipe arranged in the fluidized bed with the discharge port facing upward to support the lid body, and between the discharge port edge and the lid body. A plurality of classified bodies each having a wedge-like shape with the opening side having the same width up and down and the outer end becoming narrower toward the lower end are inserted into the lateral cylindrical opening formed in the cylindrical opening. A large lump contamination prevention device at a discharge port of a fluidized bed device, characterized in that the devices are arranged in parallel at intervals.
JP18298483U 1983-11-29 1983-11-29 Large lump prevention device at the discharge port of fluidized bed equipment Granted JPS6092097U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18298483U JPS6092097U (en) 1983-11-29 1983-11-29 Large lump prevention device at the discharge port of fluidized bed equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18298483U JPS6092097U (en) 1983-11-29 1983-11-29 Large lump prevention device at the discharge port of fluidized bed equipment

Publications (2)

Publication Number Publication Date
JPS6092097U JPS6092097U (en) 1985-06-24
JPS642156Y2 true JPS642156Y2 (en) 1989-01-18

Family

ID=30396137

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18298483U Granted JPS6092097U (en) 1983-11-29 1983-11-29 Large lump prevention device at the discharge port of fluidized bed equipment

Country Status (1)

Country Link
JP (1) JPS6092097U (en)

Also Published As

Publication number Publication date
JPS6092097U (en) 1985-06-24

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