JPH09206578A - Agitating mixer - Google Patents

Agitating mixer

Info

Publication number
JPH09206578A
JPH09206578A JP1980596A JP1980596A JPH09206578A JP H09206578 A JPH09206578 A JP H09206578A JP 1980596 A JP1980596 A JP 1980596A JP 1980596 A JP1980596 A JP 1980596A JP H09206578 A JPH09206578 A JP H09206578A
Authority
JP
Japan
Prior art keywords
container
fluid
flow passage
fluid guide
gap
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.)
Withdrawn
Application number
JP1980596A
Other languages
Japanese (ja)
Inventor
Setsuo Omoto
節男 大本
Keiji Fujikawa
圭司 藤川
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 Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
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 Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP1980596A priority Critical patent/JPH09206578A/en
Publication of JPH09206578A publication Critical patent/JPH09206578A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/18Stationary reactors having moving elements inside
    • B01J19/20Stationary reactors having moving elements inside in the form of helices, e.g. screw reactors

Abstract

PROBLEM TO BE SOLVED: To apply uniform and strong shear on a fluid passing through a flow passage consisting of a clearance to uniformize deposited particles by installing a flow passage resistant plate fitted to supporting bars in a clearance between a cylindrical vessel and a fluid guiding cylinder. SOLUTION: A fluid guiding cylinder 8 is fixed by legs 9 concentrically with a vessel 1 leaving a clearance, and a fluid passes through between the legs 9. In a clearance between the fluid guiding cylinder 8 and the vessel 1, a spiral helical ribbon blade 10 is fitted to supporting bars 7. The supporting bars 7 are provided with a doughnut flow passage resistant body 13 near the upper part of the fluid guiding cylinder 8 so that it may close a quarter to three quarters of the section of the flow passage. In this way, uniform and strong shear force is applied on a fluid passing through the flow passage to deposit particles such as uniform and particulate rubber.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は液状物質を攪拌混合
し、均一な製品を得るための混合器や、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装
置、また、耐衝撃性ボリスチレン(HIPS)のゴム粒
子析出工程の転相反応器として用いられる攪拌混合装置
に関する。
TECHNICAL FIELD The present invention relates to a mixer for stirring and mixing a liquid substance to obtain a uniform product, a polymerization reaction device for polymerizing a low-viscosity substance to obtain a high-viscosity polymer substance, and The present invention relates to a stirring and mixing apparatus used as a phase inversion reactor in a rubber particle precipitation step of high impact polystyrene (HIPS).

【0002】[0002]

【従来の技術】従来より攪拌混合装置は数多くの種類が
用いられており、低粘度液では、プロペラ、タービン、
パドルが一般的であり、高粘度液ではらせん帯翼(ヘリ
カルリボン翼)、ヘリカルスクリュウ翼、錘型翼が一般
的である。
2. Description of the Related Art Conventionally, many types of agitation mixers have been used. For low-viscosity liquids, propellers, turbines,
Paddles are common, and for viscous liquids, spiral band wings (helical ribbon wings), helical screw wings, and cone-shaped wings are common.

【0003】特に、高分子製造プロセスで往々にして取
扱う高粘度液は低粘度液に比べて混合しにくく、攪拌混
合装置の選定如何により製品々質が左右されるため、慎
重に形状を選定する必要がある。
In particular, a high viscosity liquid, which is often handled in a polymer manufacturing process, is more difficult to mix than a low viscosity liquid, and the quality of the product depends on the selection of the agitation mixer, so the shape should be carefully selected. There is a need.

【0004】低粘度液から高粘度液までの広範囲に使用
出来る攪拌混合装置としては、容器内に流体案内筒(ド
ラフトチューブ)を有するヘリカルスクリュウ翼やヘリ
カルリボン翼がある。
As a stirring and mixing apparatus which can be used in a wide range from low viscosity liquid to high viscosity liquid, there are a helical screw blade and a helical ribbon blade having a fluid guide cylinder (draft tube) in a container.

【0005】ドラフトチューブ付きのヘリカルリボン翼
は、容器内壁とドラフトチューブ外壁との間隙にヘリカ
ルリボン翼を設置した形状であり、液の循環性能が極め
て高く、高性能の攪拌混合装置である。
The helical ribbon impeller with a draft tube has a shape in which the helical ribbon impeller is installed in the gap between the inner wall of the container and the outer wall of the draft tube, and is a high performance stirring and mixing device with extremely high liquid circulation performance.

【0006】図2に、従来のドラフトチューブ付きヘリ
カルリボン翼を用いた攪拌混合装置を示す。攪拌装置の
円筒状容器1、蓋2には、それぞれ液の供給口3、排出
口4が設けられており、上部より同容器1と同芯に回転
軸5が挿入されている。回転軸5には、直角に、すなわ
ち水平に配向されたアーム6が取付けられており、アー
ム6の両端から下方へ向って支持棒7が取付けられてい
る。
FIG. 2 shows a conventional stirring and mixing apparatus using a helical ribbon blade with a draft tube. The cylindrical container 1 and the lid 2 of the stirrer are provided with a liquid supply port 3 and a liquid discharge port 4, respectively, and a rotary shaft 5 is inserted concentrically with the container 1 from above. An arm 6 oriented at a right angle, that is, horizontally, is attached to the rotary shaft 5, and a support rod 7 is attached downward from both ends of the arm 6.

【0007】また、前記容器1と同芯になるように、か
つ、容器1との間に間隙をおいて円筒状の流体案内筒
(ドラフトチューブ)8が複数本の脚9により容器1に
固定されており、各々の脚9の間は流体が通過できるよ
うになっている。流体案内筒8と容器1の間隙にらせん
帯状のヘリカルリボン翼10が設置されており、同ヘリ
カルリボン翼10は支持棒7に取付けられていて、ヘリ
カルリボン翼10は、矢印12の方向に回転する回転軸
5と共に回転するようになっている。
Further, a cylindrical fluid guide cylinder (draft tube) 8 is fixed to the container 1 by a plurality of legs 9 so as to be concentric with the container 1 and with a gap from the container 1. Fluid is allowed to pass between the legs 9. A spiral ribbon-shaped helical ribbon blade 10 is installed in the gap between the fluid guide cylinder 8 and the container 1, the helical ribbon blade 10 is attached to the support rod 7, and the helical ribbon blade 10 rotates in the direction of arrow 12. It rotates with the rotating shaft 5.

【0008】前記2例の従来の攪拌混合装置は、共に槽
内の液の循環性能を高めるため液の循環流路への障害物
を出来るだけ設けないようにしてある。しかしながら、
例えば、図2に示される従来のドラフトチューブ付きヘ
リカルリボン翼を用いた攪拌混合装置の場合では、円筒
状容器1と流体案内筒8の間に設けられたヘリカルリボ
ン翼10の回転により、流体は円筒状容器1と流体案内
筒8の間を抵抗なしに上昇することになり、ヘリカルリ
ボン翼10と円筒状容器1または流体案内筒8の隙間に
おいて流体に剪断を与える頻度が小さい難点がある。
In both of the conventional stirring and mixing apparatuses of the above-mentioned two examples, in order to improve the circulation performance of the liquid in the tank, obstacles are not provided to the liquid circulation passage as much as possible. However,
For example, in the case of the conventional stirring and mixing device using the helical ribbon blade with the draft tube shown in FIG. 2, the fluid is generated by the rotation of the helical ribbon blade 10 provided between the cylindrical container 1 and the fluid guide tube 8. Since it rises without resistance between the cylindrical container 1 and the fluid guide cylinder 8, there is a drawback that the frequency of shearing the fluid is small in the gap between the helical ribbon blade 10 and the cylindrical container 1 or the fluid guide cylinder 8.

【0009】[0009]

【発明が解決しようとする課題】耐衝撃性ポリスチレン
(以下HIPSと略す)を製造する場合、スチレン中に
溶解しているゴムを微粒子として晶析させる工程がある
が、この工程では、微粒子の均一(粒径)生成のために
は、流体に均質に剪断を与えてある必要がある。しかし
前述のように、従来の攪拌混合装置では、流路を通過す
る際に流体に剪断を与える頻度が小さく(流路を流れる
流体のうち、数%程度しか強力な剪断力が加わらな
い。)析出ゴム粒子が均一化しないという問題点があっ
た。
In the production of impact-resistant polystyrene (hereinafter abbreviated as HIPS), there is a step of crystallizing rubber dissolved in styrene as fine particles. In order to generate (particle size), it is necessary that the fluid be uniformly sheared. However, as described above, in the conventional stirring and mixing apparatus, the frequency of shearing the fluid when passing through the flow channel is small (only a few percent of the fluid flowing through the flow channel receives a strong shearing force). There is a problem that the deposited rubber particles are not uniform.

【0010】本発明は、以上の問題点を解消することを
目的としてなされたものである。
The present invention has been made for the purpose of solving the above problems.

【0011】[0011]

【課題を解決するための手段】本発明の攪拌混合装置
は、円筒状の容器、同円筒状容器内部に同容器と同芯
に、かつ、同容器との間に間隙をおいて設置された円筒
状の流体案内筒、同容器と同芯に設置された回転軸、同
回転軸に実質的に直角に取付けられたアーム、同アーム
に取付けられた支持棒により前記容器と前記流体案内筒
との間隙に挿入された攪拌翼、及び前記支持棒に取付け
られ前記円筒状の容器と前記流体案内筒との間隙に配置
された流路抵抗板を有してなることを特徴とする。
The stirring and mixing apparatus of the present invention is installed in a cylindrical container, inside the cylindrical container, concentric with the container, and with a gap between the container and the container. The container and the fluid guide tube are formed by a cylindrical fluid guide tube, a rotary shaft that is installed concentrically with the same container, an arm that is mounted substantially at a right angle to the rotary shaft, and a support rod that is mounted on the arm. And a flow path resistance plate which is attached to the support rod and is disposed in the gap between the cylindrical container and the fluid guide cylinder.

【0012】前記のように、本発明では、円筒状の容器
と流体案内筒との間隙に流路抵抗板を設けているので、
同間隙によって形成される流路内の圧力損失が増し、ヘ
リカルリボン翼と円筒状容器または流体案内筒間の隙間
を逆流(循環)する流れが著しく増加し、その結果、こ
の流路を通過する流体に剪断の加わる頻度が向上し、均
質に流体に剪断が与えられるためゴム等の析出した粒子
の粒径が均一となる。
As described above, according to the present invention, since the flow path resistance plate is provided in the gap between the cylindrical container and the fluid guide cylinder,
The pressure loss in the flow passage formed by the gap increases, and the flow that flows backward (circulates) through the gap between the helical ribbon blade and the cylindrical container or fluid guide cylinder increases significantly, and as a result, passes through this flow passage. The frequency of shearing is increased in the fluid, and the fluid is uniformly sheared, so that the particle size of the precipitated particles such as rubber becomes uniform.

【0013】[0013]

【発明の実施の形態】以下本発明の実施の第1の形態
を、図1によって説明する。
BEST MODE FOR CARRYING OUT THE INVENTION A first embodiment of the present invention will be described below with reference to FIG.

【0014】攪拌装置の円筒状容器1、蓋2には、それ
ぞれ液の供給口3、排出口4が設けられており、上部よ
り同容器1と同芯に回転軸5が挿入されている。回転軸
5には直角に、すなわち水平に配向されたアーム6が取
付けられており、アーム6の両端から下方へ向って支持
棒7が取付けられている。
A cylindrical container 1 and a lid 2 of the stirring device are provided with a liquid supply port 3 and a liquid discharge port 4, respectively, and a rotary shaft 5 is inserted coaxially with the container 1 from above. An arm 6 oriented at a right angle, that is, horizontally, is attached to the rotating shaft 5, and a support rod 7 is attached downward from both ends of the arm 6.

【0015】また、前記容器1と同芯となるように、か
つ容器1との間に間隙をおいて円筒状の(ドラフトチュ
ーブ)8が複数本の脚9により前記容器1に固定されて
おり、各々の脚の間は流体が通過できるようになってい
る。流体案内筒8と容器1の間隙にらせん状のヘリカル
リボン翼10が設置されており、同ヘリカルリボン翼1
0は支持棒7に取付けられていて、ヘリカルリボン翼1
0は、矢印12の方向に回転する回転軸5と共に回転す
るようになっている。
A cylindrical (draft tube) 8 is fixed to the container 1 by a plurality of legs 9 so as to be concentric with the container 1 and with a gap from the container 1. , Fluid is allowed to pass between the legs. A helical helical ribbon blade 10 is installed in a gap between the fluid guide cylinder 8 and the container 1, and the helical ribbon blade 1 is provided.
0 is attached to the support rod 7, and the helical ribbon wing 1
0 rotates together with the rotary shaft 5 which rotates in the direction of arrow 12.

【0016】前記支持棒7には、流体案内筒8の上部近
傍にドーナッツ状の流路抵抗板13が円筒状容器1と流
体案内筒8との間隙に形成される流路の断面積に対して
1/4〜3/4の断面積を塞ぐように設けられている。
この流路抵抗板13の流路に対する断面積の比は、流体
の粘度や、ヘリカルリボン翼の回転数または、巻数など
により調整される。
A doughnut-shaped flow path resistance plate 13 is formed in the support rod 7 near the upper portion of the fluid guide cylinder 8 in the gap between the cylindrical container 1 and the fluid guide cylinder 8 with respect to the cross-sectional area of the flow path. It is provided so as to close the cross-sectional area of 1/4 to 3/4.
The ratio of the cross-sectional area of the flow path resistance plate 13 to the flow path is adjusted by the viscosity of the fluid, the number of revolutions of the helical ribbon blade, the number of turns, or the like.

【0017】本実施の形態では、回転軸5を図示されな
い駆動装置により矢印12のように回転させた場合、液
体は流体案内筒8の外側を上昇し、内側を下降する流れ
が生じる。
In this embodiment, when the rotary shaft 5 is rotated by a drive unit (not shown) as shown by an arrow 12, the liquid rises outside the fluid guide cylinder 8 and descends inside.

【0018】このとき、流体案内筒8の上部近傍の円筒
状容器1と流体案内筒8との間隙に形成される流路には
流路抵抗板13が設けられているために、円筒状容器1
と流体案内筒8を流体が通過するとき、その隙間に逆流
が生じるため流体に均一に強力な剪断が加わり、この時
析出するゴム等の粒子が微粒化、均一化される。
At this time, since the flow path resistance plate 13 is provided in the flow path formed in the gap between the cylindrical container 1 near the upper part of the fluid guide tube 8 and the fluid guide tube 8, the cylindrical container is formed. 1
When the fluid passes through the fluid guide cylinder 8, a backflow is generated in the gap, so that the fluid is uniformly and strongly sheared, and the particles of rubber or the like precipitated at this time are atomized and made uniform.

【0019】[0019]

【発明の効果】本発明では、特許請求の範囲に記載した
ように、円筒状の容器と流体案内筒との間隙に支持棒に
取付けられた流路抵抗板を設置しているので、前記間隙
で形成される流路を通過する流体に均一なしかも強力な
剪断が加わり、均質でしかも微粒のゴム等の粒子を析出
することが可能となる。
According to the present invention, as described in the claims, since the flow path resistance plate attached to the support rod is installed in the gap between the cylindrical container and the fluid guide cylinder, the above-mentioned gap is provided. Uniform and strong shearing is applied to the fluid passing through the flow path formed in step (3), and it becomes possible to deposit particles of rubber and the like that are homogeneous and fine.

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

【図1】本発明の実施の第1の形態の縦断面図である。FIG. 1 is a longitudinal sectional view of a first embodiment of the present invention.

【図2】従来の攪拌混合装置を示す縦断面図である。FIG. 2 is a vertical sectional view showing a conventional stirring and mixing apparatus.

【符号の説明】[Explanation of symbols]

1 円筒状容器 2 蓋 3 供給口 4 排出口 5 回転軸 6 アーム 7 支持棒 8 流体案内筒 9 脚 10 ヘリカルリボン翼 13 流体抵抗板 DESCRIPTION OF SYMBOLS 1 Cylindrical container 2 Lid 3 Supply port 4 Discharge port 5 Rotating shaft 6 Arm 7 Support rod 8 Fluid guide tube 9 Leg 10 Helical ribbon blade 13 Fluid resistance plate

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 円筒状の容器、同容器内部に同容器と同
芯に、かつ、同容器との間に間隙をおいて設置された円
筒状の流体案内筒、同容器と同芯に設置された回転軸、
同回転軸に実質的に直角に取付けられたアーム、同アー
ムに取付けられた支持棒により前記容器と前記流体案内
筒との間隙に挿入された攪拌翼、及び前記支持棒に取付
けられ前記円筒状の容器と前記流体案内筒との間隙に配
置された流路抵抗板を有してなることを特徴とする攪拌
混合装置。
1. A cylindrical container, a cylindrical fluid guide cylinder provided inside the same container and coaxial with the same container, and a cylindrical fluid guide cylinder provided with a gap between the cylindrical container and the same container, and coaxially with the same container. Rotation axis,
An arm mounted substantially at a right angle to the rotary shaft, a stirring blade inserted in a gap between the container and the fluid guide cylinder by a support rod mounted on the arm, and the cylindrical shape mounted on the support rod. An agitating / mixing device comprising a flow path resistance plate disposed in a gap between the container and the fluid guide cylinder.
JP1980596A 1996-02-06 1996-02-06 Agitating mixer Withdrawn JPH09206578A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1980596A JPH09206578A (en) 1996-02-06 1996-02-06 Agitating mixer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1980596A JPH09206578A (en) 1996-02-06 1996-02-06 Agitating mixer

Publications (1)

Publication Number Publication Date
JPH09206578A true JPH09206578A (en) 1997-08-12

Family

ID=12009560

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1980596A Withdrawn JPH09206578A (en) 1996-02-06 1996-02-06 Agitating mixer

Country Status (1)

Country Link
JP (1) JPH09206578A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20070159919A1 (en) * 2006-01-12 2007-07-12 In-Seon Kim Apparatus for mixing viscous material
CN103042598A (en) * 2012-12-26 2013-04-17 张家港保税区多元机械设备制造有限公司 Guide device for stirrer
JP2020526644A (en) * 2017-07-12 2020-08-31 アランセオ・ドイチュランド・ゲーエムベーハー Reactor and continuous polymerization method

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20070159919A1 (en) * 2006-01-12 2007-07-12 In-Seon Kim Apparatus for mixing viscous material
US8398293B2 (en) * 2006-01-12 2013-03-19 Lg Chem, Ltd. Apparatus having sweeping impeller for mixing viscous material
CN103042598A (en) * 2012-12-26 2013-04-17 张家港保税区多元机械设备制造有限公司 Guide device for stirrer
JP2020526644A (en) * 2017-07-12 2020-08-31 アランセオ・ドイチュランド・ゲーエムベーハー Reactor and continuous polymerization method

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