JPS63166421A - Dispersion machine - Google Patents

Dispersion machine

Info

Publication number
JPS63166421A
JPS63166421A JP61271232A JP27123286A JPS63166421A JP S63166421 A JPS63166421 A JP S63166421A JP 61271232 A JP61271232 A JP 61271232A JP 27123286 A JP27123286 A JP 27123286A JP S63166421 A JPS63166421 A JP S63166421A
Authority
JP
Japan
Prior art keywords
cylinder
dispersion
wall
pressure gas
gas
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
JP61271232A
Other languages
Japanese (ja)
Inventor
Kimihiro Ko
洪 公弘
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.)
Sankyo Dengyo Corp
Original Assignee
Sankyo Dengyo Corp
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 Sankyo Dengyo Corp filed Critical Sankyo Dengyo Corp
Priority to JP61271232A priority Critical patent/JPS63166421A/en
Publication of JPS63166421A publication Critical patent/JPS63166421A/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
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/30Mixing gases with solids

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)

Abstract

PURPOSE:To disperse fine powder constituted of submicron particles by enabling pressure gas to be discharged from the inner face of a dispersion cylinder or the like. CONSTITUTION:Pressure gas can be discharged from the inner face of a dispersion cylinder or the like. For example, an outer cylinder 8 and an inner cylinder 9 constituted of a porous material are installed in the dispersion cylinder, and pressure gas is introduced into a space constituted of said cylinders 8 and 9 through a nipple 11, thereby pressure air is discharged out of the inner wall of the inner cylinder 9. As a result, in case fine ceramic powder constituted of submicron particles is dispersed, agglomeration of particles and adhesion of powder to the inner wall of the dispersion cylinder are practically unobserved, and the primary purpose of the dispersion can be achieved. Also, dispersion effect can be improved by installing a plurality of dispersion vanes 6 inside the dispersion cylinder.

Description

【発明の詳細な説明】 産業上の利用分野 この発明は粉体の粒子を、できるだけ完全に分散した状
態で含む気流を発生する、粉体の分散機に関するもので
ある。この気流は各種の医学実験や産業上の分級機ある
いは粒度分散測定機に利用される。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a powder disperser which generates an air stream containing powder particles in as completely a dispersed state as possible. This airflow is used in various medical experiments and industrial classifiers or particle size dispersion measuring machines.

従来の技術 第1図に従来の分散機を示す、粉体は投入口lより供給
機やエジェクタで送入される。
BACKGROUND OF THE INVENTION FIG. 1 shows a conventional dispersion machine. Powder is fed into the dispersion machine through an inlet l using a feeder or an ejector.

分散W2内にはモータ3によりプーリ4及び5を介して
高速で回転する分散羽根6が設けられている。第2図は
A−A矢視図であり、分散羽根6の形状を示している0
分散羽根6により分散W2内には強力な旋回気流が発生
し、分散W2内へ送入された粉体は、凝集を解かれ個々
の粒子に分散させられ、旋回気流と共に、放出ロアより
排出される。第3図はB−I3断面を示しており放出口
の形状を示している。すなわち、粉体の粒子を分散した
状態で含む気流が放出ロアより発生することになる。こ
の気流が上記の各種分野で利用されることになる。ここ
で粉体の粒子はより完全に個々の粒子に分散しているこ
とが必要であるが、微粒子になればなる程、分散性が悪
くなるという特性がある。
A dispersion vane 6 is provided within the dispersion W2 and is rotated at high speed by a motor 3 via pulleys 4 and 5. FIG.
A strong swirling airflow is generated within the dispersion W2 by the dispersion vanes 6, and the powder fed into the dispersion W2 is deagglomerated and dispersed into individual particles, which are discharged from the discharge lower along with the swirling airflow. Ru. FIG. 3 shows a B-I3 cross section and shows the shape of the discharge port. That is, an airflow containing dispersed powder particles is generated from the discharge lower. This airflow will be used in the various fields mentioned above. Here, it is necessary that the powder particles are more completely dispersed into individual particles, but the finer the particles, the worse the dispersibility becomes.

発明が解決しようとする問題点 しかしながら、従来の分散機では、粉体の粒子が微粒子
になればなる程、分散が不完全となり、あたかも粗大粒
子のように凝集した粒子群が、放出ロアより排出される
気流中に含まれるという欠点があった。この原因の一つ
は、粉体の粒子が微粒子になればなる程、分散W2の内
壁に付着し、ある程度付着量が成長すると、旋回気流の
作用によって、分散筒2の内壁からはくすし、放出ロア
より気流に含まれた状態で排出することである。すなわ
ち、分散1i12の内壁に粉体の粒子が付着するという
問題点があった。
Problems to be Solved by the Invention However, in conventional dispersing machines, the finer the powder particles, the more incomplete the dispersion becomes, and the aggregated particles, which look like coarse particles, are discharged from the discharge lower. The disadvantage is that it is included in the airflow. One of the reasons for this is that the finer the powder particles, the more they adhere to the inner wall of the dispersion tube 2, and when the amount of adhesion grows to a certain extent, they are smudged from the inner wall of the dispersion tube 2 due to the action of the swirling airflow. It is to discharge the air contained in the airflow from the discharge lower. That is, there was a problem in that powder particles adhered to the inner wall of the dispersion 1i12.

問題点を解決するための手段 以下、この発明を図面に基づいて説明する。Means to solve problems The present invention will be explained below based on the drawings.

第4図は、第1図の分散筒2に相当する部分を示してい
る。外W8の内面に更に内筒9が設けられており、内筒
9と外1:I8により構成される空間10へは、ニップ
ル11を介して圧力気体例えば圧力空気が導入される。
FIG. 4 shows a portion corresponding to the dispersion tube 2 in FIG. 1. An inner cylinder 9 is further provided on the inner surface of the outer W8, and a pressurized gas such as pressurized air is introduced through a nipple 11 into a space 10 formed by the inner cylinder 9 and the outer W8.

内筒9はポーラスな材質で製作されている為、内筒9の
内壁からは、圧力空気が放出されることになる。尚、放
出口12は、第4図のC−C矢視図に示されているよう
に、内筒9から接線方向に設けられており、粉体の粒子
を含んだ旋回気流を排出する構造となっている。勿論、
放出口12の内側を内W9と同一な材質で形成し、一定
の空間をおいて更に外側な外筒8と同一材質で形成する
ことも出来る。
Since the inner cylinder 9 is made of a porous material, pressurized air is released from the inner wall of the inner cylinder 9. The discharge port 12 is provided in a tangential direction from the inner cylinder 9, as shown in the C-C arrow view of FIG. 4, and has a structure for discharging the swirling airflow containing powder particles. It becomes. Of course,
The inside of the discharge port 12 can be made of the same material as the inner W9, and the outer tube 8, which is located further outside, can be made of the same material after a certain space.

本発明は、この圧力空気の放出によって、内W9の内壁
あるいは必要に応じて放出口12の内壁への粉体の付着
を防止することにある。
The purpose of the present invention is to prevent powder from adhering to the inner wall of the inner W9 or, if necessary, the inner wall of the discharge port 12, by releasing this pressurized air.

勿論、内筒9等をポーラスな材質で製作する替わりに、
細孔を多数段は圧力空気を放出する構造とすることも出
来る。いづれにしても圧力空気を放出する方法は色々考
えられる。
Of course, instead of making the inner cylinder 9 etc. from porous material,
It is also possible to have a structure in which the pores are arranged in multiple stages to release pressurized air. In any case, there are various ways to release pressurized air.

作用 次に作用を第5図とともに説明する。第5図は、本発明
のl実施例である。この場合内筒9の内径は7抛Iであ
り、分散羽根6の回転速度は15,000rpmであっ
た。これを駆動するモータ3は約70Wであった。ニッ
プル+1には約lにg/cm″の圧力空気が導入され、
焼結金属製の内筒9から放出された。分散結果は、第1
図に示す従来型のものと比較した場合、かなりの改善が
認められた。特に、サブミクロン粒子で構成されたファ
インセラミック粉を分散させた場合、第1図の従来型で
は、凝集粒子の排出がかなり認められたが、更に分散筒
内にファインセラミック粉が粘着し、やがて分散作用が
停止するに到フた。しかし、本発明の1実施例である第
5図の場合、かかる凝集及び付着は殆ど認められず、分
散結果も初期の目的を達することが出来た。
Function Next, the function will be explained with reference to FIG. FIG. 5 is an embodiment of the present invention. In this case, the inner diameter of the inner cylinder 9 was 7 mm I, and the rotation speed of the dispersing blade 6 was 15,000 rpm. The motor 3 driving this had a power of about 70W. Pressure air of approximately 1 g/cm'' is introduced into the nipple +1,
It was released from the inner cylinder 9 made of sintered metal. The variance result is the first
When compared to the conventional model shown in the figure, a considerable improvement was observed. In particular, when fine ceramic powder composed of submicron particles was dispersed, in the conventional type shown in Figure 1, a considerable amount of agglomerated particles were observed to be discharged, but the fine ceramic powder also stuck inside the dispersion cylinder, and eventually The dispersion effect had finally ceased. However, in the case of FIG. 5, which is an example of the present invention, such aggregation and adhesion were hardly observed, and the dispersion results also achieved the initial objective.

実施例 第5図はこの発明の一実施例を示す図である。内径70
si+の内筒9はステンレス製の焼結金属で製作されて
おり、多孔質であって、ニップル10より導入された圧
力空気が、分散筒の内部へ放出される構造となっている
。外筒8はステンレス製であって、空間10へはニップ
ル11を介して約I Kg/cWrの圧力空気が導入さ
れた。粉体は、投入口1より特殊@量供給フィーダによ
り5 Kg/hで供給された。分散羽根6は、モータ3
によりプーリ4及び5を介して15,000rpmの回
転速度で回転した。放出口12の部分は、第1図の方式
と同様の構造とした0分散の結果は、作用の項で示した
ように著しい改善が認められた。この場合必要に応じて
分散筒内の底部13からも圧力空気を放出する構造とす
ることも出来る。又、第6図に示すように、複数個の分
散羽根6を設けて分散効果の改善をはかることも出来る
Embodiment FIG. 5 is a diagram showing an embodiment of the present invention. Inner diameter 70
The inner cylinder 9 of the si+ is made of sintered stainless steel metal, is porous, and has a structure in which pressurized air introduced from the nipple 10 is released into the interior of the dispersion cylinder. The outer cylinder 8 was made of stainless steel, and pressurized air of about I kg/cWr was introduced into the space 10 through a nipple 11. The powder was fed at 5 kg/h from the input port 1 by a special @quantity feeder. The dispersion blade 6 is connected to the motor 3
was rotated at a rotational speed of 15,000 rpm via pulleys 4 and 5. The discharge port 12 had a structure similar to that of the method shown in FIG. 1, and the results of zero dispersion showed a significant improvement as shown in the section of the effect. In this case, it is also possible to have a structure in which pressurized air is also released from the bottom 13 within the dispersion cylinder as required. Further, as shown in FIG. 6, it is also possible to provide a plurality of dispersion vanes 6 to improve the dispersion effect.

発明の効果 サブミクロン粒子で構成される微粉体の分散が、本発明
によフて可能とな゛った。
Effects of the Invention The present invention has made it possible to disperse fine powder composed of submicron particles.

その結果、 1、動物実験等において、サブミクロンダストを含んだ
エアロゾルに関する実験が、より正確となる。
As a result: 1. In animal experiments, experiments involving aerosols containing submicron dust become more accurate.

2、サブミクロン粒子の分級機において、完全に分散し
た粒子群が、同分級機に供給されるため、分級効果が著
しく向上する。
2. In a submicron particle classifier, completely dispersed particle groups are supplied to the classifier, so the classification effect is significantly improved.

等、各種産業分野に及ぼす利益は非常に大なるものがあ
るということが出来る。
It can be said that the benefits to various industrial fields are extremely large.

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

第1図〜第3図は、従来型の説明図であり、第4図は本
発明の詳細な説明しており、第5図及び第6図は本発明
の一実施例である。 図において、 1:投入口     2:分散筒 3:モータ     4:プーリ 5:プーリ     6:分散羽根 7:放出口     8:外 筒 9:内 筒    lO:空 間 ■:ニップル    12:放出口 13:底 部 オ 1 図 第2図 第3図 Ay 4 図 f′5  口 手  続  補  正  書 (自 発)1.事件の表
示  昭和61年特許願第271232号2、発明の名
称 分散機 3、補正をする者 事件との関係   特許出願人 4、補正の対象  特許請求の範囲第1項〜第5項。 5、補正の内容  明細書の特許請求の範囲を別紙のご
とく補正する。 明細書 1、発明の名称 分散機 2、特許請求の範囲 (1)  投入口と放出口を設けた分散筒と分散羽根よ
り構成される分散機において、分散筒の内面、放出口の
内面、底部の内面鳥」Lい」L没ノ。 f”             /’  1  仔塵匹
lから圧力気体を放出する構造を、特長とする分散機。 (2)複数の分散羽根を設けることを特長とする特許請
求の範囲第1項記載の分散機。
1 to 3 are explanatory diagrams of a conventional type, FIG. 4 is a detailed explanation of the present invention, and FIGS. 5 and 6 are one embodiment of the present invention. In the figure, 1: Inlet 2: Dispersion cylinder 3: Motor 4: Pulley 5: Pulley 6: Dispersion vane 7: Discharge port 8: Outer cylinder 9: Inner cylinder lO: Space ■: Nipple 12: Discharge port 13: Bottom Part O 1 Figure 2 Figure 3 Ay 4 Figure f'5 Written amendment to oral proceedings (voluntary) 1. Indication of the case Patent Application No. 271232 filed in 1986 2, Title of the invention Dispersing machine 3, Person making the amendment Relationship to the case Patent applicant 4, Subject of the amendment Claims 1 to 5. 5. Contents of the amendment The scope of claims in the specification will be amended as shown in the attached sheet. Description 1, Title of the Invention Dispersing Machine 2, Claims (1) In a dispersing machine composed of a dispersing cylinder provided with an input port and a discharge port, and a dispersing blade, the inner surface of the dispersing cylinder, the inner surface of the discharge port, and the bottom part The inner bird "L" L is dead. f''/' 1 A disperser characterized by a structure that releases pressurized gas from the small particles 1. (2) A disperser according to claim 1, characterized by being provided with a plurality of dispersing blades.

Claims (5)

【特許請求の範囲】[Claims] (1)投入口と放出口を設けた分散筒と分散羽根より構
成される分散機において、分散筒の内面、あるいは該内
面に放出口の内面も含めた内面あるいは更に底部も含め
た内面から圧力気体を放出する構造を特長とする分散機
(1) In a disperser consisting of a dispersion cylinder with an input port and a discharge port, and a dispersion blade, pressure is applied from the inner surface of the dispersion cylinder, or the inner surface including the inner surface of the discharge port, or the inner surface including the bottom. A dispersion machine featuring a structure that releases gas.
(2)複数の分散羽根を設けることを特長とする特許請
求の範囲第1項記載の分散機。
(2) The disperser according to claim 1, characterized in that a plurality of dispersing blades are provided.
(3)内筒と外筒より構成される空間に圧力気体を導入
し、該内筒より該圧力気体を放出する構造の分散筒を設
けることを特長とする特許請求の範囲第1項又は第2項
記載の分散機。
(3) Claim 1 or 2, characterized in that a dispersion cylinder is provided with a structure that introduces pressurized gas into a space constituted by an inner cylinder and an outer cylinder, and releases the pressurized gas from the inner cylinder. Dispersing machine according to item 2.
(4)内壁と外壁より構成される空間に圧力気体を導入
し、該内壁より該圧力気体を放出する構造の放出口と、
内筒と外筒より形成される空間に圧力気体を導入し、該
内筒より該圧力気体を放出する構造の分散筒を設けるこ
とを特長とする特許請求の範囲第1項又は第2項記載の
分散機。
(4) a discharge port configured to introduce pressurized gas into a space made up of an inner wall and an outer wall and release the pressurized gas from the inner wall;
Claim 1 or 2, characterized in that a dispersion cylinder is provided with a structure for introducing pressurized gas into the space formed by the inner cylinder and the outer cylinder and releasing the pressurized gas from the inner cylinder. dispersion machine.
(5)内底と外底とより構成される空間に圧力気体を導
入し、該内底より分散筒内へ該圧力気体を放出する構造
の底部と、内壁と外壁より構成される空間に圧力気体を
導入し、該内壁より該圧力気体を放出する構造の放出口
と、内筒と外筒より形成される空間に圧力気体を導入し
、該内筒より該圧力気体を放出する構造の分散筒を設け
ることを特長とする、特許請求の範囲第1項又は第2項
記載の分散機。
(5) Pressure gas is introduced into a space made up of an inner bottom and an outer bottom, and the pressure gas is released from the inner bottom into the dispersion cylinder. A discharge port with a structure that introduces gas and releases the pressure gas from the inner wall, and a dispersion structure that introduces pressure gas into the space formed by the inner cylinder and the outer cylinder and releases the pressure gas from the inner cylinder. The disperser according to claim 1 or 2, characterized in that a cylinder is provided.
JP61271232A 1986-11-14 1986-11-14 Dispersion machine Pending JPS63166421A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61271232A JPS63166421A (en) 1986-11-14 1986-11-14 Dispersion machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61271232A JPS63166421A (en) 1986-11-14 1986-11-14 Dispersion machine

Publications (1)

Publication Number Publication Date
JPS63166421A true JPS63166421A (en) 1988-07-09

Family

ID=17497196

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61271232A Pending JPS63166421A (en) 1986-11-14 1986-11-14 Dispersion machine

Country Status (1)

Country Link
JP (1) JPS63166421A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010247096A (en) * 2009-04-16 2010-11-04 Ryuki Engineering:Kk Gas treatment apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010247096A (en) * 2009-04-16 2010-11-04 Ryuki Engineering:Kk Gas treatment apparatus

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