JPH0442404B2 - - Google Patents
Info
- Publication number
- JPH0442404B2 JPH0442404B2 JP7954382A JP7954382A JPH0442404B2 JP H0442404 B2 JPH0442404 B2 JP H0442404B2 JP 7954382 A JP7954382 A JP 7954382A JP 7954382 A JP7954382 A JP 7954382A JP H0442404 B2 JPH0442404 B2 JP H0442404B2
- Authority
- JP
- Japan
- Prior art keywords
- gas
- distribution plate
- gas distribution
- cap
- polymerization
- 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
- 238000006116 polymerization reaction Methods 0.000 claims description 17
- 238000009826 distribution Methods 0.000 claims description 16
- 238000005192 partition Methods 0.000 claims description 8
- 230000002093 peripheral effect Effects 0.000 claims description 6
- 238000012685 gas phase polymerization Methods 0.000 claims description 4
- 239000006185 dispersion Substances 0.000 claims 1
- 239000002245 particle Substances 0.000 description 6
- 150000001336 alkenes Chemical class 0.000 description 5
- 229920000642 polymer Polymers 0.000 description 5
- 239000003054 catalyst Substances 0.000 description 4
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 4
- 229920000098 polyolefin Polymers 0.000 description 3
- 239000011148 porous material Substances 0.000 description 3
- 229910052723 transition metal Inorganic materials 0.000 description 2
- 150000003624 transition metals Chemical class 0.000 description 2
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 238000007334 copolymerization reaction Methods 0.000 description 1
- 229920001519 homopolymer Polymers 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
- B01J8/44—Fluidisation grids
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Polymerisation Methods In General (AREA)
Description
【発明の詳細な説明】
この発明は気相重合装置とりわけオレフイン類
の気相重合に好適な重合装置の流動層重合槽若く
は撹拌流動層重合槽に使用されるガス分散板に関
する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a gas distribution plate used in a fluidized bed polymerization tank or a stirred fluidized bed polymerization tank of a gas phase polymerization apparatus, particularly a polymerization apparatus suitable for gas phase polymerization of olefins.
なお、本明細書中で使用される「重合」及び
「重合体」なる用語は、それぞれ「単独重合」並
びに「共重合」及び「単独重合体」並びに「共重
合体」を含む意味で用いられる。 In addition, the terms "polymerization" and "polymer" used in this specification are used to include "homopolymerization", "copolymerization", "homopolymer", and "copolymer", respectively. .
近年オレフイン重合用の遷移金属触媒の改良に
より単位遷移金属当りのオレフイン重合体生産能
力が飛躍的に向上し、その結果重合後における触
媒除去操作が省略されうるようになつた。 In recent years, improvements in transition metal catalysts for olefin polymerization have dramatically improved the production capacity of olefin polymers per unit transition metal, and as a result, it has become possible to omit the catalyst removal operation after polymerization.
こうした高活性触媒を用いるときには重合後の
操作が最も簡単なところから一般にはオレフイン
重合を気相で行う方法が採用されている。かゝる
気相重合においては通常、重合を円滑に進めるた
めに流動層重合槽が多用され導入管を経て重合槽
下部より導入されたオレフイン若くはオレフイン
含有ガスがガス分散板で均一に分散されて上昇し
流動層内でオレフイン重合体と触媒粒子からなる
固体粒子とともに流動しつゝ重合を行うようにな
つている。 When such highly active catalysts are used, a method is generally adopted in which olefin polymerization is carried out in the gas phase because it is the simplest to operate after polymerization. In such gas phase polymerization, a fluidized bed polymerization tank is usually used in order to smoothly proceed with the polymerization, and the olefin or olefin-containing gas introduced from the bottom of the polymerization tank through an introduction pipe is uniformly dispersed by a gas distribution plate. The olefin polymer rises and flows together with solid particles consisting of the olefin polymer and catalyst particles in the fluidized bed, and polymerization is carried out.
この際、ガス分散板の孔径が小さいと、生成し
た重合体粒子の付着によつて孔部での目詰りが生
じ易く、また該孔径が大きいと重合体粒子がガス
分散板下に落下し易く、ガス分散板下で壁への付
着や塊状化を起し易い。 At this time, if the pore size of the gas distribution plate is small, the pores are likely to become clogged due to adhesion of generated polymer particles, and if the pore size is large, the polymer particles tend to fall under the gas distribution plate. , it tends to stick to the wall or form lumps under the gas distribution plate.
後者の欠点は、ガス分散板の孔の上にキヤツプ
を取りつけることによつて、ある程度解消するこ
とができるが、キヤツプを取りつけるに当つて配
慮しなければならない点の一つはガスが重合槽壁
面にも充分に吹き付けられるようにすることであ
る。そのため、第1図に示す如く壁面近くのキヤ
ツプは左右のガスを流出する開口のうちの一方が
壁面に向けられるが、ガス分散板の孔より供給さ
れるガスの大半は他方、すなわち径方向内方の開
口より流出して壁面側にはほとんど流出せず、こ
れがため壁付近の流れが澱んで該部で重合体粒子
が塊状化する傾向にあり、ひいては壁面側開口部
の閉塞にまで進展し易かつた。 The latter drawback can be overcome to some extent by attaching a cap over the hole in the gas distribution plate, but one of the points that must be taken into consideration when attaching the cap is that the gas does not reach the wall of the polymerization tank. The aim is to ensure that the area is sufficiently sprayed. Therefore, as shown in Figure 1, in the cap near the wall, one of the left and right gas outflow openings is directed toward the wall, but most of the gas supplied from the holes in the gas distribution plate is directed to the other side, that is, inward in the radial direction. As a result, the flow near the wall stagnates and the polymer particles tend to form agglomerates in that area, which can even lead to blockage of the wall opening. It was easy.
本発明はこうした問題を解消するため壁面近く
のキヤツプを中間部で仕切壁により仕切つてガス
分散板の孔をその両側に配置し、或いは仕切壁が
孔を縦断するように形成し、該孔より噴出するガ
スを壁面側の開口部に確実に流出させるようにし
たものである。 In order to solve these problems, the present invention divides the cap near the wall surface with a partition wall in the middle and arranges the holes of the gas distribution plate on both sides of the cap, or alternatively, the partition wall is formed to cut through the hole vertically, and the cap is This ensures that the ejected gas flows out through the opening on the wall side.
以下図面によつて説明すると、第1図は重合槽
(図示しない)下部に取りつけられ、かつ孔1の
上にキヤツプ2を取りつけたガス分散板3の一例
を示すもので、キヤツプ2は、その断面形状が三
角形、半円形、その他任意形状をなすほか、両側
の開口4より流出するガスがガス分散板の各所に
満遍なく、かつ均一に行き渡るようにするた互い
違いに配置され、周縁のキヤツプは一方の開口4
1が外向きをなし、ガスが重合槽内壁面にも吹き
つけられるようにしてある。 To explain the following with reference to the drawings, FIG. 1 shows an example of a gas distribution plate 3 attached to the lower part of a polymerization tank (not shown) and with a cap 2 attached above the hole 1. In addition to having a triangular, semicircular, or other arbitrary cross-sectional shape, the caps are arranged in a staggered manner so that the gas flowing out from the openings 4 on both sides is distributed evenly and evenly to all parts of the gas distribution plate, with the caps on the periphery being on one side. opening 4
1 faces outward so that the gas can also be blown onto the inner wall surface of the polymerization tank.
本発明は上述する如く、一方の開口41が外向
きをなす周縁のキヤツプ2において、中間部を仕
切壁5で仕切り、その両側にそれぞれ孔10,1
1を設けたもので、外向きの開口41に通ずる孔
11は他方の孔10よりも好ましくは径大に形成
され(第2図)充分な量のガスが該孔を通して流
出されうるようになつている。 As described above, in the peripheral cap 2 in which one opening 41 faces outward, the middle part is partitioned by a partition wall 5, and holes 10 and 1 are formed on both sides of the cap 2, respectively.
1, the hole 11 leading to the outward opening 41 is preferably made larger in diameter than the other hole 10 (FIG. 2) so that a sufficient amount of gas can flow out through it. ing.
第3図は別の態様を示すもので、周縁の孔1を
比較的大径好ましくは長円形に形成し、仕切壁7
を好ましくは1の内側寄りに孔1をまたぐように
して縦断して設けたものである。 FIG. 3 shows another embodiment, in which the peripheral hole 1 is formed into a relatively large diameter, preferably an oval shape, and the partition wall 7
The hole 1 is preferably provided inwardly so as to straddle the hole 1.
本発明によれば、周縁部に設けたキヤツプの外
向きの開口よりも確実にガスが流出するようにな
り、壁面付近での重合体粒子の塊状化が解消され
る。 According to the present invention, gas flows out more reliably through the outward opening of the cap provided at the peripheral edge, and agglomeration of polymer particles near the wall surface is eliminated.
第1図は孔の上にキヤツプを取りつけたガス分
散板の平面図、第2図は周縁部のキヤツプの拡大
平面図、第3図は別の態様の拡大平面図である。
1……孔、2……キヤツプ、3……ガス分散
板、4……開口、5,7……仕切壁、10,11
……孔、41……開口。
FIG. 1 is a plan view of a gas distribution plate with a cap attached over the hole, FIG. 2 is an enlarged plan view of the peripheral edge of the cap, and FIG. 3 is an enlarged plan view of another embodiment. 1... Hole, 2... Cap, 3... Gas distribution plate, 4... Opening, 5, 7... Partition wall, 10, 11
...hole, 41...opening.
Claims (1)
つけられるキヤツプのうち、周縁部のキヤツプは
両側に設けた開口のうちの一方が外向きをなすよ
う配置され、該開口よりガスを重合槽壁面に向つ
て流出させるようにした気相重合装置における重
合槽内に設けられるガス分散板において、周縁部
のキヤツプ2は中間部で仕切壁5,7によつて仕
切られ、ガス分散板3の孔1,10,11が上記
仕切壁の両側に形成されるか或いは上記仕切壁7
で左右に仕切られるようになつているガス分散
板。 2 外向きの開口41に通ずる孔は内向きの開口
に通ずる孔よりも大である特許請求の範囲第1項
記載のガス分散板。[Scope of Claims] 1. Among the caps attached to the holes through which the gas of the gas distribution plate disperses and flows out, the peripheral cap is arranged such that one of the openings provided on both sides faces outward, and In a gas dispersion plate provided in a polymerization tank in a gas phase polymerization apparatus designed to cause gas to flow out toward the wall surface of the polymerization tank, a peripheral cap 2 is partitioned at an intermediate part by partition walls 5 and 7, The holes 1, 10, 11 of the gas distribution plate 3 are formed on both sides of the partition wall or the partition wall 7
A gas distribution plate that is divided into left and right sides. 2. The gas distribution plate according to claim 1, wherein the holes communicating with the outward openings 41 are larger than the holes communicating with the inward openings.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7954382A JPS58196205A (en) | 1982-05-11 | 1982-05-11 | Gas dispersion plate in vapor phase polymerization apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7954382A JPS58196205A (en) | 1982-05-11 | 1982-05-11 | Gas dispersion plate in vapor phase polymerization apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58196205A JPS58196205A (en) | 1983-11-15 |
| JPH0442404B2 true JPH0442404B2 (en) | 1992-07-13 |
Family
ID=13692906
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7954382A Granted JPS58196205A (en) | 1982-05-11 | 1982-05-11 | Gas dispersion plate in vapor phase polymerization apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58196205A (en) |
-
1982
- 1982-05-11 JP JP7954382A patent/JPS58196205A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58196205A (en) | 1983-11-15 |
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