JP2003117371A - Medium circulation type mill - Google Patents

Medium circulation type mill

Info

Publication number
JP2003117371A
JP2003117371A JP2001315034A JP2001315034A JP2003117371A JP 2003117371 A JP2003117371 A JP 2003117371A JP 2001315034 A JP2001315034 A JP 2001315034A JP 2001315034 A JP2001315034 A JP 2001315034A JP 2003117371 A JP2003117371 A JP 2003117371A
Authority
JP
Japan
Prior art keywords
rotor
gap
medium
circulation type
type mill
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.)
Granted
Application number
JP2001315034A
Other languages
Japanese (ja)
Other versions
JP4035837B2 (en
Inventor
Masanori Inoue
政憲 井上
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.)
Inoue Mfg Inc
Original Assignee
Inoue Mfg Inc
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 Inoue Mfg Inc filed Critical Inoue Mfg Inc
Priority to JP2001315034A priority Critical patent/JP4035837B2/en
Publication of JP2003117371A publication Critical patent/JP2003117371A/en
Application granted granted Critical
Publication of JP4035837B2 publication Critical patent/JP4035837B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Mixers Of The Rotary Stirring Type (AREA)

Abstract

PROBLEM TO BE SOLVED: To prevent the sticking of a treated material on the inside surface of a rotor in a medium circulation type mill. SOLUTION: A rotor (23) is inserted into an annular treatment gap (20) formed of an outer circumferential stator (18) and an inner circumferential stator (19), and the treatment gap (20) is divided into an outside gap (21) and an inside gap (22). A medium separator (27) for separating a dispersion medium from the treated material is provided in the inner circumferential stator (19). A circulation port (26) for circulating the dispersion medium from the inside gap (22) to the outside gap (21) is provided in the rotor (23). A projecting chip (28) adjacent to the inside surface of the rotor 23 and extending in the axial direction is provided on the outside surface of the inner circumferential stator (19). The inside surface of the rotor (23) may be formed to have a hexagonal shaped cross-section instead of providing the projecting chip (28) on the inner circumferential stator. The circulating port (26) is opened to be inclined backward to the rotational direction of the rotor (23).

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、固体粒子が液体中
に懸濁している固液スラリ−溶液等の処理材料を液送ラ
インで移送中に予備分散するようにしたパイプラインビ
−ズミルや分散媒体を循環させてバッチ式に分散処理で
きるようにした浸漬型分散機等の媒体循環型ミルに関す
るものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a pipeline bead mill in which a treatment material such as a solid-liquid slurry solution in which solid particles are suspended in a liquid is pre-dispersed during transfer in a liquid feed line. The present invention relates to a medium circulation type mill, such as an immersion type dispersing machine, in which a dispersion medium is circulated so that a dispersion treatment can be carried out in a batch system.

【0002】[0002]

【従来の技術】固液スラリ−溶液等の処理材料を湿式媒
体分散機等の分散機で分散処理する際、該分散機に処理
材料を供給する前に、処理材料を攪拌する前処理(プレ
ミックス)が行われているが、この前処理だけで固体
(粉体)の一次粒子化は不可能であり、多くの二次凝集
体がパイプライン内に沈殿することが知られている。そ
こで、本願出願人は、先に、固液スラリ−溶液等の処理
材料を分散処理する場合、液送ラインを処理材料が通過
する間に二次凝集体をほぐして予備分散できるようにし
た下記の如き構成のパイプラインビ−ズミルを提案し
た。
2. Description of the Related Art When a treatment material such as a solid-liquid slurry solution is subjected to dispersion treatment by a disperser such as a wet medium disperser, a pretreatment (pretreatment) in which the treatment material is agitated before supplying the treatment material to the disperser. Mixing is performed, but it is known that solidification (powder) cannot be converted into primary particles only by this pretreatment, and many secondary aggregates are precipitated in the pipeline. Therefore, the applicant of the present invention has previously made it possible to preliminarily disperse the secondary aggregate by disentangling the secondary agglomerates while the treatment material passes through the liquid feed line when the treatment material such as a solid-liquid slurry solution is subjected to dispersion treatment. A pipeline bead mill having the above structure was proposed.

【0003】処理材料を送液する配管に接続される材料
供給口を一側に有し他側に上記送液配管の他端に接続さ
れる材料吐出口を有する分散室を形成し、上記分散室に
上記材料供給口側に開口する筒状の外周ステ−タ−と該
外周ステ−タ−の内方に存し上記材料吐出口側に開口す
る内周ステ−タ−を設け、両ステ−タ−間に処理間隙を
形成し、該処理間隙内を外側間隙と内側間隙に区画する
よう筒状のロ−タ−を上記処理間隙に挿入すると共に該
ロ−タ−を回転する駆動軸を設け、上記処理間隙に分散
媒体を収納し、上記ロ−タ−の回転に伴って上記分散媒
体が上記外側間隙を通り内側間隙に流れ上記外側間隙に
還流するよう上記ロ−タ−に循環口を形成し、上記内周
ステ−タ−に処理材料を上記吐出口へ流出する流出口を
形成し、該流出口に分散媒体を処理材料から分離するス
クリ−ンを設けたパイプラインビ−ズミル。
A dispersion chamber having a material supply port connected to a pipe for supplying a processing material on one side and a material discharge port connected to the other end of the liquid supply pipe on the other side is formed to disperse the dispersion chamber. The chamber is provided with a cylindrical outer peripheral starter opening toward the material supply port side and an inner peripheral starter located inside the outer peripheral starter and opening toward the material discharge port side. A drive shaft for forming a processing gap between the rotors, inserting a cylindrical rotor into the processing gap so as to divide the processing gap into an outer gap and an inner gap, and rotating the rotor. And a dispersion medium is accommodated in the processing gap, and the rotation of the rotor causes the dispersion medium to flow through the outer gap to the inner gap and circulate to the rotor so as to flow back to the outer gap. Forming an outlet, and forming an outlet in the inner peripheral stator for flowing the processing material to the discharge outlet, Subscription to separate the dispersion medium from the process material - pipeline bi provided down - Zumiru.

【0004】上記パイプラインビ−ズミルにおいて、外
周ステ−タ−と内周ステ−タ−により形成した処理間隙
に供給された処理材料は、該処理間隙内で分散媒体(ビ
−ズ)と混合され、ロ−タ−の回転により外周ステ−タ
−の内側面とロ−タ−の外側面間に形成された外側間隙
から該ロ−タ−の内側面と内周ステ−タ−の外側面間に
形成された内側間隙に入り、遠心力作用によりロ−タ−
に形成した循環口を通って外側間隙に戻り、該外側間隙
と内側間隙を循環して流動する間に上記分散媒体により
微粒子化される。
In the pipeline bead mill, the processing material supplied to the processing gap formed by the outer peripheral stator and the inner peripheral stator is mixed with the dispersion medium (bead) in the processing gap. The outer surface of the rotor is rotated by the rotation of the rotor, and the outer surface of the rotor is rotated by the outer surface of the rotor. Enter the inner gap formed between the side faces, and rotate by the action of centrifugal force.
It returns to the outer gap through the circulation port formed in the above, and while being circulated and flowing through the outer gap and the inner gap, it is atomized by the dispersion medium.

【0005】上記パイプラインビ−ズミルによれば、前
処理された処理材料の二次凝集体の解砕に有効であるこ
とが確認され、簡単な微粒子化をする場合には、繰り返
して上記パイプラインビ−ズミルを通過させることによ
り、所望の分散結果が得られることも認められた。ま
た、上記パイプラインビ−ズミルの分散室とほぼ同様の
構成は、バッチ式に分散処理を行うようにした特開20
01−38184号公報に記載の浸漬型分散機にも用い
られており、バッチ式でも効率よく分散処理することが
できる。
According to the above pipeline bead mill, it has been confirmed that it is effective for crushing the secondary agglomerates of the pretreated treatment material, and in the case of simple atomization, the above pipe is repeatedly used. It was also found that the desired dispersion result was obtained by passing through a line bead mill. Further, in the structure similar to that of the dispersion chamber of the pipeline bead mill, the dispersion processing is performed in a batch system.
It is also used in the immersion type disperser described in JP-A No. 01-38184, and it is possible to efficiently perform dispersion treatment even in a batch system.

【0006】上記パイプラインビ−ズミルや上記浸漬型
分散機等の媒体循環型ミルは、上述のように効率よく分
散処理等を行うことができるが、処理材料の種類や性状
によっては、内側間隙に入った処理材料がロ−タ−の内
側面に付着し、さらにはこの付着面に分散媒体(ビ−
ズ)が入り込んだりして処理能力を低下させたり、洗浄
の際に簡単に除去できなくなるという問題を生じること
があった。
The medium circulation type mill such as the pipeline bead mill and the immersion type dispersing machine can efficiently perform the dispersion treatment as described above. However, depending on the type and properties of the treated material, the inner gap The treated material that has entered the rotor adheres to the inner surface of the rotor, and further the dispersion medium (beam
There is a problem in that the processing capacity is deteriorated due to the inclusion of dust) and that it cannot be easily removed during cleaning.

【0007】[0007]

【発明が解決しようとする課題】本発明の解決課題は、
上記のような媒体循環型ミルにおいて、ロ−タ−の内側
面に処理材料が付着しないようにし、上記洗浄等の問題
を生じないようにした媒体循環型ミルを提供することで
ある。
The problems to be solved by the present invention are as follows.
It is an object of the present invention to provide a medium circulation type mill in which the treatment material is prevented from adhering to the inner surface of the rotor in the medium circulation type mill as described above and the problems such as the above cleaning are not caused.

【0008】[0008]

【課題を解決するための手段】本発明によれば、上記の
ようなロ−タ−の内側面に処理材料が付着しないように
するため、ロ−タ−の内側面に沿って流れる処理材料の
流動を変化させ若しくはロ−タ−の内側面に沿って流動
する処理材料に圧縮、解放を繰り返すことにより流れを
乱流状態にしてロ−タ−の内側面に処理材料が付着しな
いようにした媒体循環型ミルが提供される。
According to the present invention, in order to prevent the processing material from adhering to the inner surface of the rotor as described above, the processing material flowing along the inner surface of the rotor. Of the treatment material flowing along the inner surface of the rotor is repeatedly compressed and released to make the flow turbulent and prevent the treatment material from adhering to the inner surface of the rotor. A medium circulation type mill is provided.

【0009】すなわち、本発明によれば、処理材料の供
給口と吐出口を有する分散室に筒状の外周ステ−タ−と
その内方に位置する筒状の内周ステ−タ−を設けて処理
材料が流入する環状の処理間隙を形成し、該処理間隙内
を外側間隙と内側間隙に区画するよう回転可能なロ−タ
−を該処理間隙に挿入し、該ロ−タ−の回転により上記
処理材料が上記処理間隙内で分散媒体と共に上記外側間
隙を通り上記内側間隙に流れ該外側間隙に還流するよう
上記ロ−タ−に循環口を形成し、上記内周ステ−タ−に
上記分散媒体を分離して処理材料のみを吐出口へ吐出さ
せるよう媒体分離装置を設けた媒体循環型ミルにおい
て、上記内周ステ−タ−の外側面に上記ロ−タ−の内側
面に近接し該ロ−タ−の軸方向に沿って延びる突片を突
設したことを特徴とする媒体循環型ミルが提供され、上
記突片によりロ−タ−の内側面に沿って流動する処理材
料の流れが変化し、処理材料が該内側面に付着しないよ
うにでき、上記課題が解決される。
That is, according to the present invention, a cylindrical outer peripheral starter and a cylindrical inner peripheral starter located inside thereof are provided in a dispersion chamber having a processing material supply port and a discharge port. To form an annular processing gap into which the processing material flows, and a rotatable rotor is inserted into the processing gap to divide the processing gap into an outer gap and an inner gap, and the rotor is rotated. Thus, a circulating port is formed in the rotor so that the treatment material flows in the treatment gap together with the dispersion medium through the outer gap to the inner gap and returns to the outer gap. In a medium circulation type mill provided with a medium separation device for separating the dispersion medium and discharging only the processing material to a discharge port, the outer surface of the inner peripheral stator is close to the inner surface of the rotor. And a projecting piece extending along the axial direction of the rotor is provided. The above-mentioned problem is solved by providing a medium circulation type mill that can change the flow of the processing material flowing along the inner surface of the rotor by the protruding piece and prevent the processing material from adhering to the inner surface. To be done.

【0010】また、本発明によれば、上記処理材料の供
給口と吐出口を有する分散室に筒状の外周ステ−タ−と
その内方に位置する筒状の内周ステ−タ−を設けて処理
材料が流入する環状の処理間隙を形成し、該処理間隙内
を外側間隙と内側間隙に区画するよう回転可能なロ−タ
−を該処理間隙に挿入し、該ロ−タ−の回転により上記
処理材料が上記処理間隙内で分散媒体と共に上記外側間
隙を通り上記内側間隙に流れ該外側間隙に還流するよう
上記ロ−タ−に循環口を形成し、上記内周ステ−タ−に
上記分散媒体を分離して処理材料のみを吐出口へ吐出さ
せるよう媒体分離装置を設けた媒体循環型ミルにおい
て、上記ロ−タ−の内側面の断面形状を四角形、六角形
等の多角形、長円、略楕円、偏心円その他の異型断面形
状に形成したことを特徴とする媒体循環型ミルが提供さ
れ、上記ロ−タ−が回転すると内側面が異型断面形状に
形成されているので処理材料は圧縮されたり、解放され
たりし、該ロ−タ−の内側面に付着しないようになり、
上記課題を解決することができる。
Further, according to the present invention, a cylindrical outer peripheral stator and a cylindrical inner peripheral stator located inside thereof are provided in the dispersion chamber having the supply port and the discharge port for the processing material. An annular processing gap is provided through which processing material flows, and a rotatable rotor is inserted into the processing gap to divide the processing gap into an outer gap and an inner gap. A rotation port is formed in the rotor so that the treatment material flows in the treatment gap together with the dispersion medium through the outer gap to the inner gap by the rotation so as to flow back to the outer gap. In a medium circulation type mill having a medium separation device for separating the dispersion medium and discharging only the processing material to a discharge port, the inner surface of the rotor has a polygonal cross section such as a quadrangle or a hexagon. , Oval, substantially elliptical, eccentric circle, and other irregular cross-sectional shapes A medium circulation type mill as a characteristic is provided, and when the rotor is rotated, the treatment material is compressed or released because the inner surface is formed to have an irregular cross-sectional shape. It will not stick to the side,
The above problems can be solved.

【0011】[0011]

【発明の実施の形態】本発明は、上述したように送液ラ
インの途中に設けるパイプラインビ−ズミルや、バッチ
式に分散処理できるようにした浸漬型分散機等の媒体循
環型ミルに適用することができるが、図に示す実施例で
は、固液スラリ−溶液等の処理材料を送液する配管
(L)の途中に分散室(1)を設けて二次凝集体を解砕
するようにしたパイプラインビ−ズミルに適用した実施
例が示されている。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention is applied to a pipeline bead mill provided in the middle of a liquid feeding line as described above, or a medium circulation type mill such as an immersion type disperser capable of performing a batch type dispersion treatment. In the embodiment shown in the figure, the dispersion chamber (1) is provided in the middle of the pipe (L) for feeding the processing material such as the solid-liquid slurry solution so that the secondary aggregates are crushed. The example applied to the pipeline bead mill which was made into is shown.

【0012】上記分散室(1)を形成する本体(2)
は、一側に上流側の上記配管(L)に接続される材料供
給口(3)を有し、他端に下流側の配管(L)に接続さ
れる材料吐出口(4)が形成される。該本体(2)は、
入口側部材(5)と中間部材(6)と吐出側部材(7)
をそれぞれボルト(8)…で連結して構成されており、
上記入口側部材(5)には上記材料供給口(3)、流入
室(9)及びガラスビ−ズ、セラミックスビ−ズその他
の分散媒体(ビ−ズ)(10)の投入口(11)が形成され、軸
シ−ル部(12)及び蓋板(13)を通して図示を省いたモ−タ
−で駆動される駆動軸(14)が本体内に延びている。
Main body (2) forming the dispersion chamber (1)
Has a material supply port (3) connected to the upstream pipe (L) on one side and a material discharge port (4) connected to the downstream pipe (L) on the other end. It The body (2) is
Inlet side member (5), intermediate member (6) and discharge side member (7)
Are connected by bolts (8) ...
The inlet side member (5) is provided with the material supply port (3), the inflow chamber (9) and the inlet port (11) for the glass beads, the ceramic beads and other dispersion media (beads) (10). A drive shaft (14) formed and driven by a motor (not shown) extends through the shaft seal portion (12) and the cover plate (13) into the main body.

【0013】上記駆動軸(14)には、上記流入室(9)に
入った処理材料の流動に、中間部材(6)を通って材料
吐出口側へ向う軸流を生じさせるよう軸流翼(15)が設け
られている。該軸流翼(15)としては、図に示すように流
入室に入った処理材料を中間部材(6)側へ掻き下げる
作用を奏する掻下げ羽根を用いることが好ましいが、軸
流プロペラ等を用いることもできる。
Axial flow blades are provided on the drive shaft (14) so that the flow of the processing material in the inflow chamber (9) causes an axial flow toward the material discharge port side through the intermediate member (6). (15) is provided. As the axial flow blade (15), it is preferable to use a scraping blade that has the effect of scraping the processing material that has entered the inflow chamber toward the intermediate member (6) as shown in the figure, but an axial flow propeller or the like is used. It can also be used.

【0014】上記中間部材(6)には、中心に向かって
内方に突出し逆円錐状に下方に傾斜する流入口(16)を形
成するための内方突出縁(17)及び外周ステ−タ−(18)が
設けられ、また上記吐出側部材(7)には上記材料吐出
口(4)に通じる流出口(図示略)を有する内周ステ−
タ−(19)が設けられている。該外周ステ−タ−(18)及び
内周ステ−タ−(19)は、それぞれ筒状に形成され、材料
供給口側に開口する外周ステ−タ−(18)の内方に材料吐
出口側に開口する内周ステ−タ−(19)が設けられ、両ス
テ−タ−間に環状で有底の処理間隙(20)が形成されてい
る。なお、該処理間隙(20)には上記分散媒体(10)…が収
納される。
The intermediate member (6) has an inward projecting edge (17) for forming an inflow port (16) projecting inward toward the center and sloping downward in an inverted conical shape, and an outer peripheral stator. -(18) is provided, and the discharge side member (7) has an inner peripheral stage having an outlet (not shown) communicating with the material discharge port (4).
There is a switch (19). The outer peripheral stator (18) and the inner peripheral stator (19) are each formed in a tubular shape, and the material discharge port is provided inside the outer peripheral stator (18) that opens toward the material supply port. An inner peripheral stator (19) opening to the side is provided, and an annular bottomed processing gap (20) is formed between the two stators. The dispersion medium (10) ... Is housed in the processing gap (20).

【0015】上記処理間隙(20)には、該処理間隙内を外
側間隙(21)と内側間隙(22)に区画し先端側で外側間隙(2
1)と内側間隙(22)を連通するよう筒状のロ−タ−(23)が
処理間隙の開口側から挿入されている。該ロ−タ−(23)
は、上記駆動軸(14)の下端に取付けられる略截頭円錐状
のロ−タ−端面部(24)と該ロ−タ−端面部(24)に連結さ
れた筒状のロ−タ−本体(25)を有し、上記駆動軸により
上記処理間隙(20)内で回転する。なお、上記処理間隙(2
0)の幅、特に外側間隙(21)の幅は、通常のアニュラ−タ
イプの媒体分散機と同程度に形成され、上記分散媒体に
よるずり力を効率よく処理材料に作用できる幅にされて
いる。
In the processing gap (20), the inside of the processing gap is divided into an outside gap (21) and an inside gap (22), and the outside gap (2
A cylindrical rotor (23) is inserted from the opening side of the processing gap so as to connect the (1) and the inner gap (22). The rotor (23)
Is a substantially frustoconical rotor end face portion (24) attached to the lower end of the drive shaft (14) and a cylindrical rotor connected to the rotor end face portion (24). It has a body (25) and is rotated within the processing gap (20) by the drive shaft. The processing gap (2
The width of (0), particularly the width of the outer gap (21), is formed to the same extent as that of an ordinary annular-type medium disperser, and is set to a width that allows the shearing force of the dispersing medium to efficiently act on the processing material. .

【0016】上記ロ−タ−(23)が回転した際、上記処理
材料及び分散媒体(10)…は、上記ロ−タ−によって処理
間隙(20)内で流動するが、このとき外側間隙(21)を通り
内側間隙(22)に流れた分散媒体が該内側間隙(22)から上
記外側間隙(21)に還流するよう上記ロ−タ−(23)には循
環口(26)が形成されている。
When the rotor (23) rotates, the treatment material and the dispersion medium (10) flow in the treatment gap (20) by the rotor, and at this time, the outer gap ( A circulation port (26) is formed in the rotor (23) so that the dispersion medium flowing through the inner gap (22) through the inner space (21) flows back from the inner gap (22) to the outer space (21). ing.

【0017】なお、上記内周ステ−タ−(19)の流出口に
は、分散媒体(10)…を処理材料から分離するよう小孔、
スリット、網目等の流通孔を有する媒体分離装置(27)が
形成されている。図においては、説明上、網体で筒状に
形成したスクリ−ンを図示しているが、流出口にスクリ
−ンを取り付けるようにしたり、その他の適宜の媒体分
離構造に形成することができる。また上記ロ−タ−のロ
−タ−端面部の内面下部と上端に流出口を設けた内周ス
テ−タ−を組み合せ、両部材間に分散媒体の通過を阻止
する程度のギャップを形成し、いわゆるギャップセパレ
−タ−を構成するようにしてもよい(図示略)。
At the outlet of the inner peripheral stator (19), there are small holes for separating the dispersion medium (10) from the processing material.
A medium separation device (27) having a flow hole such as a slit or a mesh is formed. In the figure, for the sake of explanation, a screen formed of a net in a cylindrical shape is shown, but a screen may be attached to the outlet or formed in any other suitable medium separation structure. . Further, a lower end of the inner surface of the rotor end surface of the rotor and an inner peripheral stator having an outlet at the upper end are combined to form a gap between both members to the extent that the passage of the dispersion medium is blocked. Alternatively, a so-called gap separator may be configured (not shown).

【0018】上記処理間隙(20)には、約60〜90%程
度の分散媒体(10)…が充填され、上流側の配管(L)か
ら上記材料供給口(3)を通って分散室内に送られた処
理材料は、上記分散室(1)の流入口(16)から処理間隙
(20)の外側間隙(21)へ入り、内側間隙(22)へ流動する。
この間に、ロ−タ−(23)により運動を与えられた分散媒
体(10)は、該分散媒体間に生じる衝撃力、摩砕力によっ
て処理材料中の二次凝集体をほぐしたり固体粒子を微粒
子化し、処理材料は予備分散され、この予備分散された
処理材料のみがスクリ−ン等の媒体分離装置(27)を通っ
て上記材料吐出口(4)から下流側の配管(L)へ流れ
る。なお、分散室の周囲やロ−タ−等の適宜の部位にジ
ャケットを設けて調温するようにしてもよい。
About 60 to 90% of the dispersion medium (10) is filled in the processing gap (20), and is passed from the upstream pipe (L) through the material supply port (3) into the dispersion chamber. The sent processing material is transferred from the inflow port (16) of the dispersion chamber (1) to the processing gap.
It enters the outer gap (21) of (20) and flows into the inner gap (22).
During this period, the dispersion medium (10), which has been given a motion by the rotor (23), loosens the secondary agglomerates in the treated material and solid particles by the impact force and the grinding force generated between the dispersion medium. The processing material is atomized and pre-dispersed, and only the pre-dispersed processing material flows from the material discharge port (4) to the downstream pipe (L) through the medium separation device (27) such as a screen. . A temperature may be controlled by providing a jacket around the dispersion chamber or at an appropriate portion such as a rotor.

【0019】浸漬型分散機の場合は、上記入口側部材
(5)を除去し、タンク内に収納した処理材料中に分散
室を浸漬し、上記流入口(16)を供給口として処理材料が
直接分散室内に流入するようにし、上記処理を行った
後、タンク内に流出した処理材料を再び上記流入口から
分散室内に循環させて上記処理を繰り返し、所望の分散
処理を行うように構成すればよい。
In the case of the immersion type disperser, the inlet side member (5) is removed, the dispersion chamber is immersed in the processing material stored in the tank, and the processing material is treated with the inlet (16) as the supply port. After being subjected to the above treatment by directly flowing into the dispersion chamber, the treatment material that has flowed out into the tank is circulated again from the inflow port into the dispersion chamber and the above treatment is repeated to perform a desired dispersion treatment. Good.

【0020】而して、図1に示すように、上記ロ−タ−
(23)は、内周ステ−タ−(19)と同芯に設けられ、内側面
の断面形状は円形に形成されているが、上記内周ステ−
タ−(19)の外側面には、上記ロ−タ−(23)の内側面に近
接し、該ロ−タ−(23)の中心軸に沿って延びる突片(28)
が突設されている。該突片(28)は、図2(A),(B)に
示すように断面三角形状、四角形状等の多角形状にした
り、同図(C)に示すように表面が円形、楕円形等の曲
面に形成した棒状体に作られ、支持板(29)に取り付けら
れている。多角形状にする場合、処理材料がロ−タ−の
内側面に対して斜めに流動するように角部(30)を流れに
対向させるようにしてある(図2(A))が、図2(B)
に示すように乱流を生じさせるよう平面(31)を流れに対
向させるようにしたり、図2(D)に示すように背面側
に補助部材(32)を設けてもよい。
Then, as shown in FIG.
(23) is provided concentrically with the inner peripheral stator (19), and the inner surface has a circular cross-sectional shape.
The outer surface of the rotor (19) is adjacent to the inner surface of the rotor (23) and extends along the central axis of the rotor (23).
Is projected. As shown in FIGS. 2 (A) and 2 (B), the projecting piece (28) has a polygonal shape such as a triangular shape or a quadrangular shape, or as shown in FIG. 2 (C), the surface has a circular shape or an elliptical shape. It is made in the shape of a rod formed on the curved surface of and is attached to the support plate (29). In the case of a polygonal shape, the corner portion (30) is made to face the flow so that the processing material flows obliquely with respect to the inner surface of the rotor (FIG. 2 (A)). (B)
The flat surface (31) may be opposed to the flow so as to generate a turbulent flow, as shown in FIG. 2, or an auxiliary member (32) may be provided on the back side as shown in FIG. 2 (D).

【0021】上記突片(28)の長さは、ロ−タ−(23)の内
側面の軸方向長さ以内の適宜の長さとし、該突片(28)と
ロ−タ−(23)の内側面間の間隙は、ロ−タ−の回転に支
障を与えないよう使用分散媒体の粒径(ビ−ズ径)の少
なくとも約4倍程度とすることが好ましい。
The length of the projection piece (28) is set to an appropriate length within the axial length of the inner surface of the rotor (23), and the projection piece (28) and the rotor (23). It is preferable that the gap between the inner surfaces of the above is at least about 4 times the particle diameter (bead diameter) of the dispersion medium used so as not to hinder the rotation of the rotor.

【0022】上記構成により、ロ−タ−(23)が回転した
際、該ロ−タ−の内側面に沿って流動する処理材料は、
上記突片(28)の部分で抵抗を受けて流動が変化し、ロ−
タ−の内側面への付着が阻止される。
With the above structure, when the rotor (23) rotates, the processing material flowing along the inner surface of the rotor is
The flow changes due to resistance at the protruding piece (28),
The adhesion to the inner surface of the target is prevented.

【0023】図3は、他の実施例を示し、基本的な構成
は、図1に示す実施例と同じであるが、ロ−タ−(23)の
内側面の断面形状が相違している。すなわち、該ロ−タ
−の内側面は、ロ−タ−が回転した際、処理材料を圧縮
したり、解放したりできるよう内周ステ−タ−(19)の外
側面とロ−タ−内側面の間隔が周方向に変化する異型断
面形状に形成されている。異型断面形状としては、例え
ば図4(A),(B)に示すように四角形(33)、六角形(3
4)等の多角形状や、図4(C)の如き、長円(35)乃至略
楕円にしたり、図4(D)のようにロ−タ−の内側面の
円形の中心を内周ステ−タ−(19)の中心からずらした偏
心円(36)とすることができる。
FIG. 3 shows another embodiment, which is basically the same as the embodiment shown in FIG. 1 except that the inner surface of the rotor (23) has a different sectional shape. . That is, the inner side surface of the rotor and the outer side surface of the inner peripheral stator (19) allow the processing material to be compressed and released when the rotor rotates. The inner side surfaces are formed to have a modified cross-sectional shape in which the interval changes in the circumferential direction. As for the modified cross-sectional shape, for example, as shown in FIGS. 4 (A) and 4 (B), a square (33), a hexagon (3
4) or the like, or an ellipse (35) or an ellipse as shown in FIG. 4 (C), or the circular center of the inner surface of the rotor as shown in FIG. 4 (D). It can be an eccentric circle (36) displaced from the center of the counter (19).

【0024】上記の構成により、ロ−タ−(23)が回転す
ると、上記内周ステ−タ−(19)の外側面とロ−タ−(23)
の内側面間の間隔が広い部分(37)では、処理材料は解放
され、狭い部分(38)では圧縮され、この解放と圧縮が繰
り返して行われることにより、処理材料をロ−タ−(23)
の内側面に付着しないようにすることができる。なお、
上記実施例に示す如き突片を併用するようにしてもよ
い。
With the above construction, when the rotor (23) is rotated, the outer surface of the inner peripheral stator (19) and the rotor (23) are rotated.
The treatment material is released in the portion (37) where the distance between the inner surfaces of the blades is wide and compressed in the narrow portion (38), and the treatment material is rotated (23) by repeating this release and compression. )
It can be prevented from adhering to the inner surface of the. In addition,
You may make it use together the protrusion as shown in the said Example.

【0025】実験によれば、ロ−タ−(23)の内側面の断
面形状を六角形に形成すると、内周ステ−タ−(19)に設
けるスクリ−ン等の媒体分離装置の径を大きくとれ、吐
出流量を増大することができ、また圧縮、解放の回数も
多くなり、ロ−タ−内側面への処理材料の付着も確実に
防ぐことができた。
According to the experiment, when the inner surface of the rotor (23) is formed in a hexagonal cross-section, the diameter of the medium separating device such as a screen provided on the inner peripheral stator (19) is changed. It was possible to increase the flow rate, to increase the discharge flow rate, to increase the number of times of compression and release, and to reliably prevent the treatment material from adhering to the inner surface of the rotor.

【0026】上記ロ−タ−(23)に形成する循環口(26)
は、ロ−タ−(23)の軸径方向に沿って図4に示すように
放射状に開口させてもよいが、図2(A)や図5に示す
ようにロ−タ−(23)の回転方向、矢印(39)に対して後向
きに傾斜する開口を設けて循環口(26a) とすると、処理
材料や分散媒体の流動が円滑に行われ、好ましい結果が
得られる。特に、図5に示すように、ロ−タ−(23)の内
側面を断面多角形状に形成したときは、その多角形の辺
の延長線上(接線方向)に後向きに傾斜して開口する循
環口(26b) を設けるとよい。そのようにすると、上記処
理材料や分散媒体は、圧縮が解放されたところでロ−タ
−の内側面に沿って接線方向に少ない抵抗でロ−タ−の
外側面側(外側間隙)へ流出し、そのような流動が繰り
返され、ロ−タ−内側面への処理材料の付着が一層防止
される。
A circulation port (26) formed in the rotor (23)
May be radially opened along the axial direction of the rotor (23) as shown in FIG. 4, but as shown in FIG. 2 (A) and FIG. When the circulation port (26a) is provided with an opening inclined rearward with respect to the rotation direction of the arrow (39), the treatment material and the dispersion medium flow smoothly, and a preferable result is obtained. In particular, as shown in FIG. 5, when the inner surface of the rotor (23) is formed in a polygonal shape in cross section, the circulation is inclined backward toward the extension line (tangential direction) of the side of the polygon. A mouth (26b) should be provided. By doing so, the treatment material or dispersion medium flows out to the outer surface side (outer gap) of the rotor with a small resistance in the tangential direction along the inner surface of the rotor when the compression is released. By repeating such flow, the adhesion of the processing material to the inner surface of the rotor is further prevented.

【0027】[0027]

【発明の効果】本発明は上記のように構成され、外周ス
テ−タ−と内周ステ−タ−間に環状の処理間隙を形成
し、該処理間隙にロ−タ−を挿入して該処理間隙を外側
間隙と内側間隙に区画し、該ロ−タ−の回転により処理
材料と分散媒体を上記外側間隙と内側間隙をめぐって循
環させ分散処理するようにした媒体循環型ミルにおい
て、上記内周ステ−タ−の外側面に上記ロ−タ−の内側
面に近接し該ロ−タ−の軸方向に沿って延びる突片を突
設したので、上記ロ−タ−の内側面に沿って流動する処
理材料の流れを変化させて該ロ−タ−の内側面に処理材
料が付着しないようにすることができる。
The present invention is constructed as described above, and an annular processing gap is formed between the outer peripheral stator and the inner peripheral stator, and the rotor is inserted into the processing gap. In the medium circulation type mill, the treatment gap is divided into an outer gap and an inner gap, and the treatment material and the dispersion medium are circulated through the outer gap and the inner gap by the rotation of the rotor to perform the dispersion treatment. Since a projecting piece is provided on the outer surface of the stator so as to be close to the inner surface of the rotor and extends along the axial direction of the rotor, the projecting piece extends along the inner surface of the rotor. The flow of the flowing processing material can be changed so that the processing material does not adhere to the inner surface of the rotor.

【0028】また、上記の如き媒体循環型ミルにおい
て、上記ロ−タ−の内側面の断面形状を四角形、六角形
等の多角形、長円、略楕円、偏心円その他の異型断面形
状に形成したので、上記ロ−タ−が回転すると内周ステ
−タ−の外側面とロ−タ−の内側面の間隔が周方向で広
狭に変化し、狭い部分で処理材料は圧縮され、広い部分
で解放され、圧縮、解放を繰り返すことにより処理材料
の流動に変化を与えてロ−タ−内側面への処理材料の付
着を防止することができる。
Further, in the medium circulation type mill as described above, the cross-sectional shape of the inner side surface of the rotor is formed into a polygonal shape such as a quadrangle, a hexagon, an ellipse, a substantially ellipse, an eccentric circle or other irregular cross-sectional shape. Therefore, when the rotor is rotated, the distance between the outer surface of the inner peripheral stator and the inner surface of the rotor changes widely in the circumferential direction, and the treatment material is compressed in the narrow portion, and the wide portion is compressed. It is possible to change the flow of the processing material by repeating compression and release by preventing the adhesion of the processing material to the inner surface of the rotor.

【0029】以上のように、本発明によれば、処理材料
がロ−タ−内側面へ付着しないようにでき、分散効率を
高め、かつ洗浄作業を容易に行うことができる。
As described above, according to the present invention, the treatment material can be prevented from adhering to the inner surface of the rotor, the dispersion efficiency can be improved, and the cleaning operation can be easily performed.

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

【図1】本発明の一実施例を示す断面図。FIG. 1 is a sectional view showing an embodiment of the present invention.

【図2】内周ステ−タ−を平面からみた説明図で、
(A)はロ−タ−を含めた説明図、(B)〜(D)は他
の実施例を示す説明図。
FIG. 2 is an explanatory view of the inner circumference stator viewed from a plane,
(A) is an explanatory view including a rotor, and (B) to (D) are explanatory views showing another embodiment.

【図3】本発明の他の実施例を示す一部の断面図。FIG. 3 is a partial cross-sectional view showing another embodiment of the present invention.

【図4】ロ−タ−の内側面の断面形状を示す説明図であ
って、(A)は四角形、(B)は六角形、(C)は長
円、(D)は偏心円を示す各説明図。
FIG. 4 is an explanatory view showing a cross-sectional shape of the inner surface of the rotor, (A) shows a quadrangle, (B) shows a hexagon, (C) shows an ellipse, and (D) shows an eccentric circle. Each explanatory view.

【図5】ロ−タ−の内側面を断面六角形状にした他の実
施例の説明図。
FIG. 5 is an explanatory view of another embodiment in which the inner surface of the rotor has a hexagonal cross section.

【符号の説明】[Explanation of symbols]

1 分散室 2 本体 18 外周ステ−タ− 19
内周ステ−タ− 20 処理間隙 21 外側間隙 22 内側間隙 23
ロ−タ− 26 循環口 28 突片 33 四角形 34 六角形
35 長円 36 偏心円
1 Dispersion chamber 2 Main body 18 Peripheral stator 19
Inner circumference stator 20 Processing gap 21 Outside gap 22 Inside gap 23
Rotor 26 Circulation port 28 Projection piece 33 Square 34 Hexagon
35 Ellipse 36 Eccentric circle

Claims (10)

【特許請求の範囲】[Claims] 【請求項1】 処理材料の供給口と吐出口を有する分散
室に筒状の外周ステ−タ−とその内方に位置する筒状の
内周ステ−タ−を設けて処理材料が流入する環状の処理
間隙を形成し、該処理間隙内を外側間隙と内側間隙に区
画するよう回転可能なロ−タ−を該処理間隙に挿入し、
該ロ−タ−の回転により上記処理材料が上記処理間隙内
で分散媒体と共に上記外側間隙を通り上記内側間隙に流
れ該外側間隙に還流するよう上記ロ−タ−に循環口を形
成し、上記内周ステ−タ−に上記分散媒体を分離して処
理材料のみを吐出口へ吐出させるよう媒体分離装置を設
けた媒体循環型ミルにおいて、上記内周ステ−タ−の外
側面に上記ロ−タ−の内側面に近接し該ロ−タ−の軸方
向に沿って延びる突片を突設したことを特徴とする媒体
循環型ミル。
1. A processing material flows into a dispersion chamber having a supply port and a discharge port for the processing material by providing a cylindrical outer peripheral stator and a cylindrical inner peripheral stator located inside thereof. An annular processing gap is formed, and a rotor that is rotatable so as to divide the inside of the processing gap into an outer gap and an inner gap is inserted into the processing gap,
A rotation port is formed in the rotor so that the treatment material flows in the treatment gap with the dispersion medium through the outer gap to the inner gap by the rotation of the rotor to flow back to the outer gap. In a medium circulation type mill provided with a medium separating device for separating the dispersion medium into the inner peripheral stator and discharging only the processing material to a discharge port, the roller is attached to the outer surface of the inner peripheral stator. A medium circulation type mill characterized in that a projecting piece is provided proximate to the inner surface of the rotor and extending along the axial direction of the rotor.
【請求項2】 上記突片の先端とロ−タ−の内側面間の
間隙は、分散媒体の粒径の4倍以上の間隙である請求項
1に記載の媒体循環型ミル。
2. The medium circulation type mill according to claim 1, wherein the gap between the tip of the projecting piece and the inner surface of the rotor is 4 times or more the grain size of the dispersion medium.
【請求項3】 上記突片の断面形状は三角形、四角形等
の多角形状である請求項1または2に記載の媒体循環型
ミル。
3. The medium circulation type mill according to claim 1, wherein a cross-sectional shape of the projecting piece is a polygonal shape such as a triangle or a quadrangle.
【請求項4】 上記突片の表面は、円形、楕円形等の曲
面に形成されている請求項1または2に記載の媒体循環
型ミル。
4. The medium circulation type mill according to claim 1, wherein the surface of the projecting piece is formed into a curved surface such as a circle or an ellipse.
【請求項5】 上記循環口は、ロ−タ−の回転方向に対
し後向きに傾斜して開口している請求項1ないし4のい
ずれかに記載の媒体循環型ミル。
5. The medium circulation type mill according to claim 1, wherein the circulation port is opened so as to be inclined rearward with respect to the rotation direction of the rotor.
【請求項6】 処理材料の供給口と吐出口を有する分散
室に筒状の外周ステ−タ−とその内方に位置する筒状の
内周ステ−タ−を設けて処理材料が流入する環状の処理
間隙を形成し、該処理間隙内を外側間隙と内側間隙に区
画するよう回転可能なロ−タ−を該処理間隙に挿入し、
該ロ−タ−の回転により上記処理材料が上記処理間隙内
で分散媒体と共に上記外側間隙を通り上記内側間隙に流
れ該外側間隙に還流するよう上記ロ−タ−に循環口を形
成し、上記内周ステ−タ−に上記分散媒体を分離して処
理材料のみを吐出口へ吐出させるよう媒体分離装置を設
けた媒体循環型ミルにおいて、上記ロ−タ−の内側面の
断面形状を四角形、六角形等の多角形、長円、略楕円、
偏心円その他の異型断面形状に形成したことを特徴とす
る媒体循環型ミル。
6. A processing material flows into a dispersion chamber having a supply port and a discharge port for the processing material by providing a cylindrical outer peripheral stator and a cylindrical inner peripheral stator located inside thereof. An annular processing gap is formed, and a rotor that is rotatable so as to divide the inside of the processing gap into an outer gap and an inner gap is inserted into the processing gap,
A rotation port is formed in the rotor so that the treatment material flows in the treatment gap with the dispersion medium through the outer gap to the inner gap by the rotation of the rotor to flow back to the outer gap. In a medium circulation type mill provided with a medium separation device for separating the dispersion medium into an inner peripheral stator and discharging only a processing material to a discharge port, the inner surface of the rotor has a quadrangular cross-sectional shape. Polygon such as hexagon, oval, approximately ellipse,
A medium circulation type mill characterized by being formed into an eccentric circle or other irregular cross-sectional shape.
【請求項7】 上記ロ−タ−の内側面の断面形状は多角
形状であり、上記循環口は多角形の角部に設けられてい
る請求項6に記載の媒体循環型ミル。
7. The medium circulation type mill according to claim 6, wherein the inner surface of the rotor has a polygonal cross-section, and the circulation port is provided at a corner of the polygon.
【請求項8】 上記循環口は、ロ−タ−の回転方向に対
して後向きに傾斜して開口している請求項6に記載の媒
体循環型ミル。
8. The medium circulation type mill according to claim 6, wherein the circulation port is opened so as to be inclined rearward with respect to the rotation direction of the rotor.
【請求項9】 上記循環口は、ロ−タ−内側面の多角形
の辺の延長線上に設けられ、ロ−タ−の回転方向に対し
て後向きに傾斜して開口している請求項7に記載の媒体
循環型ミル。
9. The circulation port is provided on an extension line of a polygonal side of the inner surface of the rotor, and is opened so as to be inclined rearward with respect to the rotation direction of the rotor. The medium circulation type mill described in 1.
【請求項10】 上記ロ−タ−内側面の断面形状は、六角
形である請求項9に記載の媒体循環型ミル。
10. The medium circulation type mill according to claim 9, wherein a cross-sectional shape of the inner surface of the rotor is hexagonal.
JP2001315034A 2001-10-12 2001-10-12 Media circulation mill Expired - Fee Related JP4035837B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001315034A JP4035837B2 (en) 2001-10-12 2001-10-12 Media circulation mill

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001315034A JP4035837B2 (en) 2001-10-12 2001-10-12 Media circulation mill

Publications (2)

Publication Number Publication Date
JP2003117371A true JP2003117371A (en) 2003-04-22
JP4035837B2 JP4035837B2 (en) 2008-01-23

Family

ID=19133260

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001315034A Expired - Fee Related JP4035837B2 (en) 2001-10-12 2001-10-12 Media circulation mill

Country Status (1)

Country Link
JP (1) JP4035837B2 (en)

Also Published As

Publication number Publication date
JP4035837B2 (en) 2008-01-23

Similar Documents

Publication Publication Date Title
JP7270832B2 (en) Impeller assembly and solid-liquid mixing device using the impeller assembly
JP4451965B2 (en) Pipeline bead mill
JP3159870B2 (en) Continuously operating stirrer ball mill for fine and ultrafine grinding of materials
JP5317124B2 (en) Wet medium agitating and grinding disperser
KR101658410B1 (en) Dispersing and emulsifying apparatus for high viscosity fluid
CN108355569B (en) Solid-liquid mixing device for preparing superfine slurry
JPS6243731B2 (en)
US11059004B2 (en) Device and method for mixing, in particular dispersing
JP6584682B2 (en) Equipment for mixing
JP2007307522A (en) Medium agitation type wet dispersion machine and dispersion method of fine particle
JP4956095B2 (en) Media stirring type wet disperser
JP2013039508A (en) Medium stirring type crusher
JPH10230182A (en) Grinder
JP4035837B2 (en) Media circulation mill
JP2002028511A (en) Grinding/classifying method for cereals and the like, grinding/classifying machine for cereals and the like
JP2010005540A (en) Wet dispersion or grinding method, and wet disperser used for this method
JPWO2007141992A1 (en) Media disperser
CN208449496U (en) It is used to prepare the milling apparatus of particle dispersion
JP4918272B2 (en) Circulation type media stirring mill
JP3640994B2 (en) High-speed stirring disperser
JP4140423B2 (en) Wet medium disperser and stirring disk used therefor
JP2646111B2 (en) Continuous flow stirrer
JPH08173826A (en) Wet dispersing pulverizer and method thereof
JP2001190974A (en) Cracking filter device for powder dispersing machine
JP2002204969A (en) Bead mill for pipeline

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20040406

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20061220

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20070123

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20070319

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20070626

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20070807

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20070925

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20071019

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20101109

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20111109

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20111109

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20121109

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20121109

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20131109

Year of fee payment: 6

LAPS Cancellation because of no payment of annual fees