JPS60202724A - Dispersing apparatus - Google Patents

Dispersing apparatus

Info

Publication number
JPS60202724A
JPS60202724A JP59057464A JP5746484A JPS60202724A JP S60202724 A JPS60202724 A JP S60202724A JP 59057464 A JP59057464 A JP 59057464A JP 5746484 A JP5746484 A JP 5746484A JP S60202724 A JPS60202724 A JP S60202724A
Authority
JP
Japan
Prior art keywords
dispersion
container
screw
medium
suspension
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
JP59057464A
Other languages
Japanese (ja)
Other versions
JPS6253214B2 (en
Inventor
Taro Mori
太郎 森
Moto Yagi
八木 本
Yoshio Michizoe
道添 良男
Yuji Takehara
竹原 佑爾
Kazuo Minami
南 量夫
Fusao Inoue
井上 房男
Tatsuo Tamura
田村 達雄
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.)
Dai Nippon Toryo KK
Original Assignee
Dai Nippon Toryo KK
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 Dai Nippon Toryo KK filed Critical Dai Nippon Toryo KK
Priority to JP59057464A priority Critical patent/JPS60202724A/en
Publication of JPS60202724A publication Critical patent/JPS60202724A/en
Publication of JPS6253214B2 publication Critical patent/JPS6253214B2/ja
Granted 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
    • B01F27/19Stirrers with two or more mixing elements mounted in sequence on the same axis
    • B01F27/192Stirrers with two or more mixing elements mounted in sequence on the same axis with dissimilar elements
    • 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
    • B01F27/60Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis

Abstract

PURPOSE:To obtain an excellent dispersion efficiency by providing a flat-plate disk and a screw to a driving rotary shaft which is provided at the center of the symmetry axis of a cylindrical dispersing vessel, and directing the propelling direction of the screw to the charge side of a suspension. CONSTITUTION:In an apparatus for dispersing a suspension of solid particles into a colloidal state,the inner surface of a dispersing vessel 1 is shaped in the form of a cylinder, and a driving a rotary shaft 2 is provided at the center of the symmetry axis of the cylindrical form in the vessel 1. A flat-plate disk 4 and a screw 5 are equipped to the shaft 2. A dispersing medium can be charged into the vessel 1 through a device, and a charge part 8 of a suspension is provided to one end part of the vessel 1 along the shaft 2 and a discharge part 9 of the dispersed liquid to the other end part. In addition, the propelling direction of the screw 5 is directed to the charge part 8 of the suspension. A satisfactory dispersing effect can be obtained with said comparatively simple mechanism.

Description

【発明の詳細な説明】 〔技術分野〕 本発明は、塗料、インキ等の固体粒子懸濁液(以下、「
ミルペース」という場合がある)をコロイド状にするた
めの分散装置に関する。
[Detailed Description of the Invention] [Technical Field] The present invention relates to solid particle suspensions (hereinafter referred to as "
This invention relates to a dispersion device for making a colloid (sometimes referred to as "MIL-PACE") into a colloidal state.

〔従来技術〕[Prior art]

上記の如き分散装置としては、従来、種々のものが知ら
れており、たとえばミルペース中に比較的小さな粒体(
分散媒体)を多数混合して、これらを強制攪拌すること
Kより分散を行なう装置がある。ところが、この様な従
来の分散装置においては、強制攪拌は密閉容器内で複数
のディスクを付設した駆動回転軸を一方向に回転するこ
とにより行なわれるため、ミルペースと媒体とは同一方
向に流れ分散効率があまり良好でない。また、密閉状態
で攪拌が行なわれるため液流によって内圧が上昇し、回
転軸回りに液漏れ防止の精巧なシール機構を設ける必要
があυ、またシール部での液漏れ監視のためシール液を
封入するか又は7−ル液を循環させることが必要となる
。更に、従来の分散装置においては分散媒体と分散液と
の分離を回転軸回りに付設したスクリーンにより行なう
方式のものがあるが、この様な方式では分散液の通過面
積が小さく内圧がかかるため分散媒体によるスクリーン
の摩耗が著しい。
Various types of dispersion devices such as those described above have been known in the past. For example, relatively small particles (
There is an apparatus that performs dispersion by mixing a large number of dispersion media and forcibly stirring them. However, in such conventional dispersion devices, forced agitation is performed by rotating a drive shaft equipped with multiple disks in one direction in a closed container, so the MillPace and medium flow in the same direction and are not dispersed. Efficiency is not very good. In addition, since stirring is performed in a sealed state, the internal pressure increases due to the liquid flow, and it is necessary to install a sophisticated sealing mechanism around the rotation axis to prevent liquid leakage. It is necessary to encapsulate or circulate the liquid. Furthermore, some conventional dispersion devices separate the dispersion medium and the dispersion liquid using a screen attached around the rotating shaft, but in this type of system, the area through which the dispersion liquid passes is small and internal pressure is applied, making it difficult to disperse. Significant wear of the screen by the media.

〔発明の目的〕[Purpose of the invention]

本発明は、以上の如き従来技術に鑑み、分散効率が良好
で、且つ精密なシール機構等を要することなく、また分
散媒体分離手段の摩耗の少ない分散4装置を提供するこ
とを目的とする。
In view of the above-mentioned prior art, it is an object of the present invention to provide a dispersion device 4 that has good dispersion efficiency, does not require a precise sealing mechanism, and has less wear on the dispersion medium separation means.

〔発明の要旨〕 本発明は、以上の如き目的達1jXのため、固体粒子の
懸濁液をコロイド状に分散せしめるだめの装置において
、分散容器内面が円筒形状であシ、該容器内にその円筒
形状の対称軸心に駆動回転動が設けられており、該駆動
回転軸には平板ディスクとスクリー−とが付設されてお
り、分散容器内には分散媒体を装入することができ、該
容器にはその回転軸に沿っての一端部に@濁液送入部が
付設されており且つ他端部に分散液排出部が付設されて
おシ、上記スクリューの推進方向は@濁液送入部側へと
向いていることを特徴とする、分散装置を提供する。
[Summary of the Invention] To achieve the above-mentioned objects 1jX, the present invention provides an apparatus for dispersing a suspension of solid particles in a colloidal form, in which the inner surface of the dispersion container is cylindrical, and the inside of the dispersion container is cylindrical. A driving rotation is provided at the symmetrical axis of the cylindrical shape, and a flat plate disk and a scree are attached to the driving rotation axis, and a dispersion medium can be charged into the dispersion container. The container is provided with a turbid liquid inlet at one end along its axis of rotation, and a dispersion liquid outlet at the other end, and the propelling direction of the screw is in the direction of the turbid liquid feed. To provide a dispersion device characterized in that it faces toward an entrance side.

〔発明の実施例〕[Embodiments of the invention]

以下、図面を参照しながら本発明分散装置の具体的実施
例を説明する。
Hereinafter, specific embodiments of the dispersion apparatus of the present invention will be described with reference to the drawings.

第1図は本発明装置の一実施例を示す縦断面図である。FIG. 1 is a longitudinal sectional view showing an embodiment of the device of the present invention.

分散容器1の内面は円筒形状であシ、その内径と長さと
の比はたとえば174程度である。
The inner surface of the dispersion container 1 has a cylindrical shape, and the ratio of its inner diameter to length is, for example, about 174.

容器1内には回転軸2が貫入しており、該回転軸2は容
器1の内面円筒形状の対称軸のまわりに回転可能である
。容器1内における回転軸2の外径はたとえば容器1の
内径の1/2程度である。回転軸2は駆動手段3により
駆動せしめられる。回転軸2の容器1内部分には、ディ
スク4が9枚程度とスクリー−5が3個程度取付けられ
ている。
A rotating shaft 2 penetrates into the container 1, and the rotating shaft 2 is rotatable around an axis of symmetry of the cylindrical inner surface of the container 1. The outer diameter of the rotating shaft 2 inside the container 1 is, for example, about 1/2 of the inner diameter of the container 1. The rotating shaft 2 is driven by a driving means 3. Approximately nine disks 4 and approximately three screes 5 are attached to the rotating shaft 2 inside the container 1.

これらのディスク4及びスクリー−5は回転軸2に対し
着脱し得る如くに敗付けられており、6はこれらの間隔
保持のためのカラーである。尚、スクリュー5は全て推
進方向が同一となる様なものが使用されている。ディス
ク4及びスクリ=−5の配置は適宜設定し得るが、ミル
ペースの送入量。
These disks 4 and scree 5 are attached to and detachable from the rotating shaft 2, and 6 is a collar for maintaining the distance between them. Incidentally, the screws 5 are all propelled in the same direction. Although the arrangement of the disk 4 and the screen = -5 can be set as appropriate, the feeding amount of MilPace.

温度上昇度1分散度等を考慮すれば第1図の如き配置が
好ましい。また、容器1の内径とディスク4及びスクリ
ュー5の外径との比は415〜7/8が好ましい。
Considering the degree of temperature rise, degree of dispersion, etc., the arrangement as shown in FIG. 1 is preferable. Moreover, the ratio of the inner diameter of the container 1 to the outer diameter of the disk 4 and the screw 5 is preferably 415 to 7/8.

第2図及び第3図はディスク4の斜戊図であり、第2図
のものは円周方向に対称的に4〜8個の孔あきのもので
あり、第3図のものは孔なしのものである。第2図のも
のと第3図のものを組合わせて使用することにより容器
1内の温度上昇を抑制できる。第4図及び第5図はスク
リ、−5のf+祝図であり、第4図のものは連続した螺
条が1〜2周設けられており、筑5図の本のけ2〜4個
の独立した暉条が設けられている。尚、第6図はカラー
6の斜視図である。
Figures 2 and 3 are oblique views of the disc 4. The disc in Figure 2 has 4 to 8 holes symmetrically in the circumferential direction, and the disc in Figure 3 has no holes. It is something. By using a combination of the one shown in FIG. 2 and the one shown in FIG. 3, the temperature rise inside the container 1 can be suppressed. Figures 4 and 5 are Screw, -5 f + congratulatory map, and the one in Figure 4 has 1 to 2 continuous threads around it, and 2 to 4 bookmarks in Chiku5. An independent sanction has been established. 6 is a perspective view of the collar 6. FIG.

第1図において、容器1の内部には多数の分散媒体7が
収容されている。媒体7としてはこの種の分散装置にお
いて通常使用されているもの全てが使用できるが、好ま
しくは比較的低密度のがラスビーズを用いる。媒体7の
粒径はたとえば0.5〜3WII++である。
In FIG. 1, a large number of dispersion media 7 are housed inside a container 1. As the medium 7, any medium commonly used in this type of dispersion device can be used, but preferably lath beads having a relatively low density are used. The particle size of the medium 7 is, for example, 0.5 to 3 WII++.

容器1の一端部にはミルペース送入部8が設けられてお
り、ここからミルペースを連続的に供給する。容器1の
他端部には分散液排出部9が設けられている。該排出部
9は前室9a及び後室9bを有する。前室9aは円筒形
の多孔板(たとえば)母ンチングメタル)10により容
器1内と仕切られている。第7図に多孔体10の斜視図
を示す。
A mil-paste feeding section 8 is provided at one end of the container 1, from which mil-paste is continuously supplied. A dispersion liquid discharge part 9 is provided at the other end of the container 1 . The discharge section 9 has a front chamber 9a and a rear chamber 9b. The front chamber 9a is separated from the inside of the container 1 by a cylindrical perforated plate (for example, machining metal) 10. FIG. 7 shows a perspective view of the porous body 10.

該多孔板10の孔径は媒体7の通過を阻止し得る様なも
のである。前室9aと後室9bとは隔壁11によシ仕切
られている。尚、多孔版1oは該隔壁11にその一端を
保持されている。後室9bと容器1内部との間には媒体
通過阻止体12が設けられており、該阻止体12は後室
9b内を貫通せる回転軸のまわシに摺接せしめられた筒
状部を介して後室9b外の外部へと連なっておシ、位置
調節手段13とネジにより接続せしめられている。
The hole diameter of the perforated plate 10 is such that the passage of the medium 7 can be prevented. The front chamber 9a and the rear chamber 9b are separated by a partition wall 11. Note that one end of the perforated plate 1o is held by the partition wall 11. A medium passage blocking body 12 is provided between the rear chamber 9b and the inside of the container 1, and the blocking body 12 has a cylindrical portion that is brought into sliding contact with a rotary shaft that can pass through the inside of the rear chamber 9b. It is connected to the outside of the rear chamber 9b via the rear chamber 9b, and is connected to the position adjustment means 13 by screws.

尚、14は該ネジに接続された位置固定用ナツトである
。該位置調節手段13を操作することによシ阻止体12
が回転軸2に沿って移動し、阻止体12と隔壁11との
間隔が調節できる。15.16は位置調節手段13の抜
は止めである。17は阻止体12と外壁18との間に設
けられたオーリングであり、19は阻止体12と回転軸
2との間に設けられたオーリングである。前室9a及び
後室9bには下部に分散液取出口が設けられており、そ
の下方にはシー−ター20が付設されている。
Note that 14 is a position fixing nut connected to the screw. By operating the position adjusting means 13, the blocking body 12
moves along the rotating shaft 2, and the distance between the blocking body 12 and the partition wall 11 can be adjusted. Reference numerals 15 and 16 indicate a stop for removing the position adjustment means 13. 17 is an O-ring provided between the blocking body 12 and the outer wall 18, and 19 is an O-ring provided between the blocking body 12 and the rotating shaft 2. The front chamber 9a and the rear chamber 9b are provided with a dispersion liquid outlet at the bottom, and a sheeter 20 is attached below the outlet.

分散容器1の円筒形状外周壁には冷却水通路21が形成
されており、22及び23はそれぞれ冷却水入口及び出
口である。また、24及び25はそれぞれ分散媒体、投
入口及び取出口である。
A cooling water passage 21 is formed in the cylindrical outer peripheral wall of the dispersion container 1, and 22 and 23 are a cooling water inlet and an outlet, respectively. Further, 24 and 25 are a dispersion medium, an input port, and an output port, respectively.

以上の分散装置の使用に当っては、先ず分散容器1内に
分散媒体投入口24から適宜の量の分散媒体7を投入し
くもちろん、分散媒体取出口25は閉めておく)、該投
入口を閉め、冷却水通路21に冷却水を通しながら、ミ
ルペース送入部8からミルペースを容器1内に送入する
。同時に駆動手段3によシ回転軸2を回転せしめ、ディ
スク4及びスクリー−5を回転せしめる。この際、スク
リュー5の推進方向がミルペース送入部8の方へ向く様
に回転軸2が駆動せしめられる。また、位置調節手段1
3を操作することにより、媒体通過阻止体12と隔壁1
1との間に媒体通過を阻止し得る程度の間隙を形成して
おく。容器1内のミルペース及び媒体7は、ディスク4
により攪拌され円周方向に運動せしめられるとともに、
スクリュー5によりミルペース送入部8の方へと戻され
る様に直線方向に運動せしめられる。このスクリー−5
の作用はミルペースに対してよりも媒体7に対してより
効率的に作用し、従って媒体7が分散液排出部9の方へ
と進むのを阻止し媒体7が分散容器内にほぼ均質に分布
する様にする。従って、分散液排出部側に媒体7が集め
られて滞留する様なことはなく、更にミルペースと媒体
7との相対運動量も大きくなるので分散効率が向上する
。分散された液体は、その一部が多孔体10を通って前
室9a内に入り、他の一部は阻止体12と隔壁11との
間隙を通って後室9b内に入る。前室9a及び後室9b
内の分散液はそれぞれの取出口からシュータ−20へと
取出され回収される。この装置においては分散液排出部
9は外気圧に対し開放状態であるため、容器1内の排出
部近くの圧力はあまり上昇せず、従って該排出部9にお
けるシール機構は比較的簡単なものでよい。また、この
装置においては容器1内からの分散液の排出は比較的大
きな液通過面積をもって前室9a及び後室9bへとなさ
れるため、媒体7と分散液との分離がスムーズに行なわ
れる。
When using the above-mentioned dispersion device, first put an appropriate amount of dispersion medium 7 into the dispersion container 1 from the dispersion medium inlet 24 (of course, keep the dispersion medium outlet 25 closed), and then close the dispersion medium outlet 25. The container is closed, and while cooling water is passed through the cooling water passage 21, MilPase is fed into the container 1 from the MilPase feeding section 8. At the same time, the drive means 3 rotates the rotary shaft 2, thereby rotating the disk 4 and the screen 5. At this time, the rotating shaft 2 is driven so that the direction of propulsion of the screw 5 is directed toward the millpaste feeding section 8. Moreover, the position adjustment means 1
3, the medium passage blocker 12 and the partition wall 1
1 to form a gap large enough to prevent passage of the medium. The millpace and medium 7 in the container 1 are transferred to the disk 4
is stirred and moved in the circumferential direction,
It is caused to move in a linear direction by the screw 5 so as to be returned to the milpace feed section 8. This scree-5
acts more efficiently on the medium 7 than on the mill-pace, thus preventing the medium 7 from proceeding towards the dispersion outlet 9 and ensuring a substantially homogeneous distribution of the medium 7 in the dispersion vessel. do as you like. Therefore, the medium 7 is not collected and retained on the dispersion liquid discharge part side, and the relative momentum between the mill paste and the medium 7 is also increased, so that the dispersion efficiency is improved. Part of the dispersed liquid passes through the porous body 10 and enters the front chamber 9a, and the other part passes through the gap between the blocking body 12 and the partition wall 11 and enters the rear chamber 9b. Front chamber 9a and rear chamber 9b
The dispersion liquid inside is taken out from each outlet to the shooter 20 and collected. In this device, the dispersion liquid discharge part 9 is open to external pressure, so the pressure near the discharge part in the container 1 does not increase much, and therefore the sealing mechanism in the discharge part 9 is relatively simple. good. Further, in this device, the dispersion liquid from the container 1 is discharged into the front chamber 9a and the rear chamber 9b with a relatively large liquid passage area, so that the medium 7 and the dispersion liquid are smoothly separated.

〔発明の効果〕〔Effect of the invention〕

以上の如く、本発明分散装置によれば、比較的簡単な機
構により良好な分散効率を得ることができる。
As described above, according to the dispersion device of the present invention, good dispersion efficiency can be obtained with a relatively simple mechanism.

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

第1図は本発明分散装置の縦断面図であり、第2図及び
第3図はディスクの斜視図であシ、第4図及び第5図は
スクリューの斜視図であシ、第6図はカラーの斜視図で
あシ、第7図は多孔体の斜視図である。 1・・・分散容器、2・・・回転軸、4・・・ディスク
、5・・・スクリ=−16・・・カラー、7・・・分散
媒体、8・・・ミルペース送入部、9・・・分散液排出
部、9a・・・前室、9b・・・後室、10・・・多孔
体、11・・・隔壁、12・・・媒体通過阻止体、13
・・位置調節手段、17.19・・・オーリング。 第2図 第3図 @ 4 図 IK5 図 I!6図 第7図
FIG. 1 is a longitudinal sectional view of the dispersing device of the present invention, FIGS. 2 and 3 are perspective views of the disk, FIGS. 4 and 5 are perspective views of the screw, and FIG. 7 is a perspective view of the collar, and FIG. 7 is a perspective view of the porous body. DESCRIPTION OF SYMBOLS 1... Dispersion container, 2... Rotating shaft, 4... Disk, 5... Screen=-16... Collar, 7... Dispersion medium, 8... Milpase feeding part, 9 ...Dispersion liquid discharge part, 9a... Front chamber, 9b... Back chamber, 10... Porous body, 11... Partition wall, 12... Medium passage blocker, 13
... Position adjustment means, 17.19... O-ring. Figure 2 Figure 3 @ 4 Figure IK5 Figure I! Figure 6 Figure 7

Claims (3)

【特許請求の範囲】[Claims] (1)固体粒子の懸濁液をコロイド状に分散せしめるだ
めの装置゛において、分散容器内面が円筒形状であQ1
該容器内にその円筒形状の対称軸心に駆動回転軸が設け
られており、該駆動回転軸には平板ディスクとスクリュ
ーとが付設されており、分散容器内には分散媒体を装入
することができ、該容器にはその回転軸に沿っての一端
部に懸濁液送入部が付設されており巨つ他端部に分散液
排出部が付設されており、上記スクリューの推進方向は
懸濁液送入部側へと向いていることを特徴とする、分散
装置。
(1) In a device for dispersing a suspension of solid particles into a colloid, the inner surface of the dispersion container is cylindrical and Q1
A drive rotation shaft is provided in the container at the symmetrical axis of the cylindrical shape, and a flat disk and a screw are attached to the drive rotation shaft, and a dispersion medium is charged into the dispersion container. The container has a suspension inlet at one end along its rotation axis and a dispersion outlet at the other end, and the direction of propulsion of the screw is A dispersion device, characterized in that it is oriented toward the suspension inlet side.
(2)分散容器が横型円筒形である、第1項の分散装置
(2) The dispersion device according to item 1, wherein the dispersion container has a horizontal cylindrical shape.
(3)分散液排出部が、前室と後室とを有し、該前室は
分散媒体通過阻止用円筒形多孔体により、千の内(il
llの4+−薩g器と仕切られており、H記後室は回転
軸に沿って前室と併置されており、且つ前室と後室との
隔壁部に回転軸に沿って移動することにより後室と分散
容器との間隙の大きさを調節し得る媒体通過阻止体が設
けられており、上記前室及び後室にはそれぞれ分散液取
出口が設けられている、第1項の分散装置。
(3) The dispersion liquid discharge part has a front chamber and a rear chamber, and the front chamber has a cylindrical porous body for preventing passage of the dispersion medium.
It is separated from the 4+-satsugaki of ll, and the rear chamber of h is located side by side with the front chamber along the axis of rotation, and there is a partition wall between the front and rear chambers that allows movement along the axis of rotation. The dispersion device according to item 1, wherein a medium passage blocking body capable of adjusting the size of the gap between the rear chamber and the dispersion container is provided, and a dispersion liquid outlet is provided in each of the front chamber and the rear chamber. Device.
JP59057464A 1984-03-27 1984-03-27 Dispersing apparatus Granted JPS60202724A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59057464A JPS60202724A (en) 1984-03-27 1984-03-27 Dispersing apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59057464A JPS60202724A (en) 1984-03-27 1984-03-27 Dispersing apparatus

Publications (2)

Publication Number Publication Date
JPS60202724A true JPS60202724A (en) 1985-10-14
JPS6253214B2 JPS6253214B2 (en) 1987-11-09

Family

ID=13056396

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59057464A Granted JPS60202724A (en) 1984-03-27 1984-03-27 Dispersing apparatus

Country Status (1)

Country Link
JP (1) JPS60202724A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08337737A (en) * 1995-06-14 1996-12-24 Nippon Shokubai Co Ltd Surface modification of solid fine particle
JP2002153743A (en) * 2000-11-21 2002-05-28 Nippon Airitsuhi Kk Screw for agitation and agitation disintegration apparatus for medium
JP2005270955A (en) * 2004-02-23 2005-10-06 Hosokawa Funtai Gijutsu Kenkyusho:Kk Treatment apparatus and powder treatment method
JP2020006306A (en) * 2018-07-06 2020-01-16 アシザワ・ファインテック株式会社 Media agitation type crusher

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08337737A (en) * 1995-06-14 1996-12-24 Nippon Shokubai Co Ltd Surface modification of solid fine particle
JP2002153743A (en) * 2000-11-21 2002-05-28 Nippon Airitsuhi Kk Screw for agitation and agitation disintegration apparatus for medium
JP2005270955A (en) * 2004-02-23 2005-10-06 Hosokawa Funtai Gijutsu Kenkyusho:Kk Treatment apparatus and powder treatment method
JP4669253B2 (en) * 2004-02-23 2011-04-13 ホソカワミクロン株式会社 Processing apparatus and powder processing method
JP2020006306A (en) * 2018-07-06 2020-01-16 アシザワ・ファインテック株式会社 Media agitation type crusher

Also Published As

Publication number Publication date
JPS6253214B2 (en) 1987-11-09

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