JPH0240227A - Agitation device - Google Patents

Agitation device

Info

Publication number
JPH0240227A
JPH0240227A JP63188276A JP18827688A JPH0240227A JP H0240227 A JPH0240227 A JP H0240227A JP 63188276 A JP63188276 A JP 63188276A JP 18827688 A JP18827688 A JP 18827688A JP H0240227 A JPH0240227 A JP H0240227A
Authority
JP
Japan
Prior art keywords
plane plate
reaction
agitated
plate blades
vessel
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
JP63188276A
Other languages
Japanese (ja)
Inventor
Takahiro Oshida
押田 孝博
Takeyo Kajiwara
梶原 健世
Etsuro Matsumoto
松本 悦郎
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 Kasei Polytec Co
Original Assignee
Mitsubishi Monsanto Chemical Co
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 Monsanto Chemical Co filed Critical Mitsubishi Monsanto Chemical Co
Priority to JP63188276A priority Critical patent/JPH0240227A/en
Publication of JPH0240227A publication Critical patent/JPH0240227A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/05Stirrers
    • B01F27/11Stirrers characterised by the configuration of the stirrers
    • B01F27/112Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades
    • B01F27/1125Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades with vanes or blades extending parallel or oblique to the stirrer axis
    • B01F27/11251Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades with vanes or blades extending parallel or oblique to the stirrer axis having holes in the surface
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/05Stirrers
    • B01F27/11Stirrers characterised by the configuration of the stirrers
    • B01F27/112Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades
    • B01F27/1125Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades with vanes or blades extending parallel or oblique to the stirrer axis

Abstract

PURPOSE:To obtain high mixing capacity for viscous matter and to reduce the agitation power by providing such plural plane plate blades radially around the revolving shaft in the center of a vessel that extend to the near part of the inner wall surface of the vessel and have a number of small holes uniformly distributed on the surface. CONSTITUTION:When the revolving shaft 5 is driven by a driving, unit, the contents are moved upward or downward accompanied with the movement of each plane plate blade 6, 7, and at the same time, a part of the contents is passed through a number of small holes 11 provided in the plane plate blades 6, 7 and mixed turbulently in the backside of the plane plate blades 6, 7. Thus, strong and complicated flows of the material to be agitated are formed all over the inside of the vessel 1 as well as near the surface of the plane plate blades 6, 7. Consequently, the solid-like revolution or the retaining state of the material to be agitated is eliminated and the agitation effect and the reaction effect are sharply improved. Namely, the agitating and mixing function for the material to be agitated is superior and the construction of the device is simpler compared with the reaction device of one shaft. when this device is used for a polymerizing reaction, the reaction is efficiently proceeded and the quality of the polymer is stable and excellent.

Description

【発明の詳細な説明】 〈産業上の利用分野〉 本発明は、高粘度の液状またはスラリー状物質を撹拌混
合して均一な製品を得るための混合に用いられたり、撹
拌条件下で低粘度物質を重合させて高粘度の高分子物質
を得るための重合反応に用いられる撹拌装置に関するも
のである。
[Detailed Description of the Invention] <Industrial Application Field> The present invention can be used for mixing high viscosity liquid or slurry substances by stirring to obtain a uniform product, or The present invention relates to a stirring device used in a polymerization reaction for polymerizing substances to obtain a high-viscosity polymeric substance.

〈従来の技術〉 高分子物質製造プロセスでは、一般に、反応混合物は反
応初期では粘度が低く、反応中期から終期にかけて粘度
が高くなる。高粘度の反応混合物は均一混合が困難にな
り、その撹拌装置の選定如何により製品品質に影響を与
えるので、その構造の決定に際しては、慎重に検討する
必要がある。
<Prior Art> In a process for producing a polymeric substance, a reaction mixture generally has a low viscosity at the beginning of the reaction, and increases in viscosity from the middle to the end of the reaction. Highly viscous reaction mixtures are difficult to mix uniformly, and product quality is affected by the selection of a stirring device, so careful consideration is required when determining the structure.

また、高粘度液を均一に混合するには、撹拌翼の構造に
よっては、極めて大きい撹拌力が必要となることもあり
、撹拌翼の材質、撹拌動力等の観点からも、効率の良い
混合性能をもった撹拌装置を選定することが必要である
In addition, to uniformly mix high viscosity liquids, depending on the structure of the stirring blade, an extremely large stirring force may be required, and from the viewpoint of the material of the stirring blade, stirring power, etc., it is necessary to achieve efficient mixing performance. It is necessary to select a stirring device with

従来より高粘度物質の撹拌装置としては、大型パドル翼
、錨型質、螺旋帯翼(ヘリカルリボン翼)及び螺旋軸翼
(へりカルスクリュウ翼)が多用されている。
Conventionally, large paddle impellers, anchor-type impellers, helical ribbon impellers, and helical screw impellers have been widely used as stirring devices for highly viscous substances.

〈発明が解決しようとする課題〉 しかしながら、大型パドル翼及び錨型質は構造が簡単で
、製作や清掃が容易である利点はあるものの、高粘度物
質に対する混合性能が悪く、更に、撹拌動力が大きくな
るという問題点があった。
<Problems to be Solved by the Invention> However, although large paddle blades and anchor-type blades have the advantage of being simple in structure and easy to manufacture and clean, they have poor mixing performance for high viscosity substances, and furthermore, they have poor stirring power. There was a problem with the size.

また、ヘリカルリボン翼及びへりカルスクリュウ翼は高
粘度物質に対する混合性能は良好で、撹拌動力も、それ
ほど大きくならない等の優れた性能を発揮するが、構造
が複雑であるため製作が困難でコスト高となり、清掃も
容易でないという問題点があった。
In addition, helical ribbon blades and helical screw blades have good mixing performance for high viscosity substances, and the stirring power does not increase too much. However, they have a complicated structure, making it difficult to manufacture and expensive. Therefore, there was a problem that cleaning was not easy.

本発明は、上記の問題点に鑑みて、 (1)比較的簡単な構造で、 (2)高粘度物質に対し、高い混合性能を発揮し、(3
)シかも、撹拌動力の小さい新規な撹拌装置を提供する
ことを目的とする。
In view of the above problems, the present invention (1) has a relatively simple structure, (2) exhibits high mixing performance for high viscosity substances, and (3) has a relatively simple structure.
) Another object of the present invention is to provide a new stirring device with low stirring power.

〈課題を解決するための手段〉 上記の目的達成のため、本発明では、容器内に、その中
心に回転軸を備えると共に、この回転軸周りにほぼ等間
隔で配置され、それぞれ回転軸から放射状に外方に向か
って容器の内周壁面にほぼ近接する位置まで延在し、且
つ面上にほぼ一様に分布した多数の小孔を有する複数の
平板翼を備える構成とする。
<Means for Solving the Problems> In order to achieve the above object, in the present invention, a rotating shaft is provided in the center of the container, and the containers are arranged at approximately equal intervals around the rotating shaft, and radially from the rotating shaft. The container is configured to include a plurality of flat plate wings extending outwardly to a position substantially close to the inner circumferential wall surface of the container and having a large number of small holes substantially uniformly distributed on the surface.

また、平板翼に形成された小孔の合計面積が平板翼面積
の1/3〜1/2の範囲になるようにする。
Further, the total area of the small holes formed in the flat blade is set to be in the range of 1/3 to 1/2 of the area of the flat blade.

く作用〉 上記の構成では、内容物は、各平板翼の回転と共にその
回転方向に移動させられると同時に、−部は平板翼面上
に設けられた多数の小孔をすり抜け、平板翼の裏側にて
乱流気味に再混合される。
In the above configuration, the contents are moved in the direction of rotation of each flat blade, and at the same time, the contents pass through a number of small holes provided on the flat blade surface, and the contents are transferred to the back side of the flat blade. The mixture is remixed in a slightly turbulent manner.

これによると、共回りを生じることもなく、滞留現象も
防止できるため、効率良く撹拌・混合でき、重合反応に
用いた場合には、得られる製品の品質も安定して優れた
ものとなる。
According to this, co-rotation does not occur and stagnation phenomenon can be prevented, so that stirring and mixing can be performed efficiently, and when used in a polymerization reaction, the quality of the obtained product is also stable and excellent.

また、1軸で構造が簡単で、省力化にも優れている。In addition, it has a simple structure with a single shaft, and is excellent in labor saving.

〈実施例〉 以下に、本発明の一実施例を図面に基づいて説明するが
、本発明は、その要旨を超えない限り、以下の例に限定
されるものではない。
<Example> An example of the present invention will be described below based on the drawings, but the present invention is not limited to the following example unless it exceeds the gist thereof.

第1図は、本発明の一実施例を示す概略断面図である。FIG. 1 is a schematic sectional view showing one embodiment of the present invention.

横型円筒状の容器1は、その外周壁を温度調節のための
ジャケット2で囲まれている。
A horizontal cylindrical container 1 has its outer peripheral wall surrounded by a jacket 2 for temperature regulation.

容器l内には、容器1両端壁を軸封部3.4を介して回
転可能に貫通する回転軸5が設けられ、この回転軸5周
りに放射状に1対の平板翼6.7を取付けて、パドル装
置8を構成している。尚、この例では、平板翼を1対と
したが、複数の平板翼を回転軸周りにほぼ等間隔に配置
し、それぞれ回転軸から放射状に真っ直ぐ外方に向かっ
て延在させてもよい。
A rotating shaft 5 rotatably penetrates both end walls of the container 1 via shaft seals 3.4, and a pair of flat blades 6.7 are attached radially around this rotating shaft 5. This constitutes a paddle device 8. In this example, there is one pair of flat plate blades, but a plurality of flat plate blades may be arranged at approximately equal intervals around the rotation axis, and each may extend radially straight outward from the rotation axis.

平板翼6.7は、それらの端縁が容器1内周壁に近接し
ており、それぞれ斜めに対向する部分に欠損部9.10
を形成しである。欠損部面積の大きさと位置は広範囲に
変えることができる。また、平板翼6,7面上には多数
の小孔11がほぼ一様に形成されており、小孔11の合
計面積及び位置も広範囲に変えることができるが、合計
面積は平板翼6.7面積の1/3〜1/2の範囲にある
のが好ましい。
The flat plate wings 6.7 have their edges close to the inner circumferential wall of the container 1, and have defective parts 9.10 at diagonally opposing parts.
It is formed. The size and location of the defect area can vary widely. Further, a large number of small holes 11 are formed almost uniformly on the surfaces of the flat blades 6 and 7, and the total area and position of the small holes 11 can be varied over a wide range, but the total area is the same as that of the flat blades 6. The area is preferably in the range of 1/3 to 1/2 of the area.

ここで、回転軸5を図示しない駆動装置により回転させ
た場合、内容物(被撹拌物質)は各平板翼6.7の動き
と共に上方あるいは下方に移動させられると同時に、一
部は平板翼6,7に設けられた多数の小孔11をすり抜
け、平板翼6.7の裏側にて乱流気味に再混合される。
Here, when the rotating shaft 5 is rotated by a drive device (not shown), the contents (substance to be stirred) are moved upward or downward with the movement of each flat plate blade 6. , 7, and are remixed in a somewhat turbulent flow on the back side of the flat plate blades 6.7.

よって、平板翼6.7表面付近はもとより、容器l内金
体にわたって、被撹拌物質の強力且つ、複雑な流れが形
成されることになる。
Therefore, a strong and complicated flow of the substance to be stirred is formed not only near the surface of the flat blade 6.7 but also over the metal body inside the container l.

これにより、被撹拌物質の共周りや滞留現象を回避する
ことができ、撹拌効果9反応効果を大幅に向上させるこ
とができる。即ち、この装置においては、従来の1軸の
反応装置に比して、装置の構造が簡単な上、被撹拌物質
を撹拌混合する機能が優れているので、重合反応に用い
た場合には、効率良く重合反応を進めることができ、得
られる重合物の品質も安定して優れたものとなる。
Thereby, it is possible to avoid the co-circulation and stagnation phenomenon of the substance to be stirred, and the stirring effect 9 reaction effect can be significantly improved. In other words, this apparatus has a simpler structure than a conventional single-shaft reactor, and has an excellent ability to stir and mix the substances to be stirred, so when used in a polymerization reaction, The polymerization reaction can proceed efficiently, and the quality of the resulting polymer is stable and excellent.

(発明の効果) 以上説明したように、本発明の装置は、次のような効果
を奏し、本発明の工業上の利用価値は極めて大である。
(Effects of the Invention) As explained above, the apparatus of the present invention has the following effects, and the industrial utility value of the present invention is extremely large.

本発明装置によると、装置の構造が簡単な上、従来の1
軸の撹拌装置にみられる撹拌軸及び撹拌翼近傍での内容
物の共同りゃ滞留現象も防止でき、被撹拌物質を撹拌混
合する機能が優れているおり、且つ撹拌動力が少なくて
すむので、省電力の要請にも適合している。
According to the device of the present invention, the structure of the device is simple and the conventional one
It is possible to prevent the content from stagnation in the vicinity of the stirring shaft and stirring blades that occurs in shaft stirring devices, and it has an excellent function of stirring and mixing the materials to be stirred, and because it requires less stirring power, it is economical. It also meets the electricity requirements.

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

第1図は本発明の一実施例を示す概略断面図である。 ■・・・容器  3,4・・・軸封部  5・・・回転
軸6.7・・・平板翼  訃・・パドル装置  9.1
0・・・欠損部  11・・・小孔
FIG. 1 is a schematic sectional view showing an embodiment of the present invention. ■...Container 3, 4...Shaft seal 5...Rotating shaft 6.7...Flat wing End...Paddle device 9.1
0... Defect part 11... Small hole

Claims (2)

【特許請求の範囲】[Claims] (1)容器内に、その中心に回転軸を備えると共に、こ
の回転軸周りにほぼ等間隔で配置され、それぞれ回転軸
から放射状に外方に向かって容器の内周壁面にほぼ近接
する位置まで延在し、且つ面上にほぼ一様に分布した多
数の小孔を有する複数の平板翼を備えることを特徴とす
る撹拌装置。
(1) A rotary shaft is provided at the center of the container, and they are arranged at approximately equal intervals around the rotary shaft, and are arranged radially outward from the rotary shaft to a position that is almost close to the inner circumferential wall surface of the container. A stirring device comprising a plurality of flat plate blades extending and having a large number of small holes substantially uniformly distributed over the surface.
(2)平板翼に形成された小孔の合計面積が平板翼面積
の1/3〜1/2の範囲にあることを特徴とする請求項
1記載の撹拌装置。
(2) The stirring device according to claim 1, wherein the total area of the small holes formed in the flat blade is in the range of 1/3 to 1/2 of the area of the flat blade.
JP63188276A 1988-07-29 1988-07-29 Agitation device Pending JPH0240227A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63188276A JPH0240227A (en) 1988-07-29 1988-07-29 Agitation device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63188276A JPH0240227A (en) 1988-07-29 1988-07-29 Agitation device

Publications (1)

Publication Number Publication Date
JPH0240227A true JPH0240227A (en) 1990-02-09

Family

ID=16220825

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63188276A Pending JPH0240227A (en) 1988-07-29 1988-07-29 Agitation device

Country Status (1)

Country Link
JP (1) JPH0240227A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5183332A (en) * 1991-03-26 1993-02-02 Kenji Maeda Kneading method of concrete
WO2007011027A1 (en) * 2005-07-22 2007-01-25 Daikin Industries, Ltd. Agitator for horizontal polymerization apparatus and process for producing fluoropolymer
JP2014028367A (en) * 2012-07-04 2014-02-13 Furukawa Electric Co Ltd:The Reaction method and reactor

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5183332A (en) * 1991-03-26 1993-02-02 Kenji Maeda Kneading method of concrete
US5302018A (en) * 1991-03-26 1994-04-12 Kenji Maeda Concrete kneading apparatus
WO2007011027A1 (en) * 2005-07-22 2007-01-25 Daikin Industries, Ltd. Agitator for horizontal polymerization apparatus and process for producing fluoropolymer
JP2014028367A (en) * 2012-07-04 2014-02-13 Furukawa Electric Co Ltd:The Reaction method and reactor

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