JPH0615193A - Jet mill - Google Patents

Jet mill

Info

Publication number
JPH0615193A
JPH0615193A JP11320392A JP11320392A JPH0615193A JP H0615193 A JPH0615193 A JP H0615193A JP 11320392 A JP11320392 A JP 11320392A JP 11320392 A JP11320392 A JP 11320392A JP H0615193 A JPH0615193 A JP H0615193A
Authority
JP
Japan
Prior art keywords
air
air supply
flow path
main body
annular flow
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Withdrawn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
JP11320392A
Other languages
Japanese (ja)
Inventor
Seiya Sakurai
誠也 櫻井
Kazunari Ikuta
一成 生田
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.)
SHIYUUEI TSUSHO KK
Kyowa Shokuhin KK
Original Assignee
SHIYUUEI TSUSHO KK
Kyowa Shokuhin 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 SHIYUUEI TSUSHO KK, Kyowa Shokuhin KK filed Critical SHIYUUEI TSUSHO KK
Priority to JP11320392A priority Critical patent/JPH0615193A/en
Publication of JPH0615193A publication Critical patent/JPH0615193A/en
Withdrawn legal-status Critical Current

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Abstract

PURPOSE:To improve pulverizing performance and energy efficiency by providing a cylinder and annular flow passages within a body constituting a hollow circular truncated cone shape and pulverizing the raw materials supplied into the respective flow passages by collision against wall surfaces, etc., then bringing the raw materials into vigorous collision against each other in the confluent part of the two flow passages. CONSTITUTION:The body 1 constituting the hollow circular truncated cone shape, a discharge pipe 7 inserted inward from the central part atop the body 1 and an inside cylindrical part 6 of the hollow circular truncated cone shape provided to enclose the discharge pipe 7 within the upper space of the body 1 are provided. The outer annular flow passage R1 and the inner annular flow passage R2 are formed in the body 1. Further, a first air feed pipe 12 for feeding air from approximately the tangential direction of the inside of the flow passage R1 into the flow passage, a second air feed pipe 13 which feeds the air into the flow passage 2 from its approximately tangential direction, raw material supply ports 8, 9 formed in the body 1 and an air feeder 10 for feeding the air into the air feed pipes 12, 13 are provided. The air is fed from the air feed pipes 12, 13 into the flow passages R1, R2 by the air feeder 10 and is swirled in opposite directions within the respective routes.

Description

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

【0001】[0001]

【産業上の利用分野】この発明は、固形原料などを細分
化し、より微小な粉体を得るための粉砕装置に関し、特
に、中空の本体内に高速気流を発生させ、その気流によ
って本体内に送給された原料を粉砕するジェットミルに
関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a pulverizing apparatus for subdividing a solid raw material or the like to obtain finer powder, and in particular, a high-speed air flow is generated in a hollow main body, and the air flow causes the high speed air flow in the main body. The present invention relates to a jet mill that grinds fed raw materials.

【0002】[0002]

【従来の技術】粉砕加工は、製粉、顔料製造、鉱石処
理、食品加工のなどの様々な分野において古来より頻繁
に行われてきた単位操作の一つであり、時代の進展と共
にその重要性は増している。殊に、様々な味、形状、色
彩、などを求められる今日の食品加工技術には、粉砕加
工は不可欠な工程となっており、その粉砕工程の効率が
生産性の良否に大きな影響を及ぼす。このため、現在の
食品加工工場などにおいては種々の粉砕装置が設備され
おり、粉砕工程の自動化、効率化が図られている。
2. Description of the Related Art Crushing is one of the unit operations that have been frequently performed since ancient times in various fields such as milling, pigment production, ore processing, and food processing. It is increasing. In particular, crushing is an indispensable step in today's food processing technology, which requires various tastes, shapes, colors, etc., and the efficiency of the crushing step has a great influence on the quality of productivity. For this reason, various crushing devices are installed in current food processing factories, etc., and the crushing process is automated and efficient.

【0003】この粉砕装置としては、現在、機械的可動
部分によって原材料を粉砕するものが主として知られて
いるが、この種の粉砕装置を用いる場合、乾燥した紛粒
を得るためには、その前工程あるいは後工程において原
材料あるいは粉砕した原材料の乾燥工程が必要とされ、
製造工程全体としての効率化には限界があった。例え
ば、こんにゃく芋を製造する場合には、まず、こんにゃ
く芋を乾燥させ、その後乾燥させたこんにゃく芋を粉砕
装置にかけることにより乾燥した粉粒を製造し、その噴
流に水や添加剤などを加えて混練し冷却して製造する。
この製造工程の中で、こんにゃく芋の乾燥には極めて多
くの時間を要するため、製造工程全体を効率化する上
で、粉砕装置のみに多くの効果を期待することはできな
かった。
[0003] As this crushing device, a crushing device for crushing raw materials by mechanically moving parts is mainly known at present, but when a crushing device of this kind is used, in order to obtain dried powder particles, Drying process of raw material or crushed raw material is required in the process or the post process,
There was a limit to the efficiency improvement of the whole manufacturing process. For example, in the case of producing konjac potato, first, dried konjac potato, to produce a dried powder particles by applying the dried konjac potato to a pulverizer, then add water and additives to the jet. It is manufactured by kneading and cooling.
Since it takes a very long time to dry the konjac potato in this manufacturing process, it was not possible to expect many effects only from the crushing device in order to improve the efficiency of the entire manufacturing process.

【0004】一方、上記のような機械的可動部分を持た
ず、空気流の作用によって原材料を粉砕するようにした
いわゆるジェットジェットミルの開発もなされている。
このジェットミルは、円錐台状の本体内に高速空気を吹
き込んで一定方向へ旋回する旋回気流を発生させ、その
旋回気流によって本体内に供給された原材料を撹拌し、
原材料同士の衝突及び本体内面と原材料の衝突などによ
って原材料を粉砕するようにしたものである。この装置
においては、旋回気流によって発生する摩擦熱により原
材料の乾燥が粉砕と同時に行われるため、粉砕工程と乾
燥工程とを1工程で行うことが可能となり、製造工程の
簡略化を図り得るものとして評価されている。
On the other hand, a so-called jet jet mill has been developed, which does not have the above-mentioned mechanically movable parts and crushes raw materials by the action of an air flow.
This jet mill blows high-speed air into a frustoconical body to generate a swirling airflow that swirls in a certain direction, and agitates the raw materials supplied into the body by the swirling airflow.
The raw materials are crushed by collision between the raw materials and collision between the inner surface of the main body and the raw materials. In this device, since the raw material is dried at the same time as the pulverization by the frictional heat generated by the swirling air flow, the pulverization step and the drying step can be performed in one step, and the manufacturing process can be simplified. Has been evaluated.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、これま
でに開発されているジェットミルにおいては、一定方向
への旋回気流によって原材料を粉砕する構成となってい
るため、十分な粉砕状態を得るには、かなり大きな動力
エネルギーを要し、また、粉砕能力などの点においても
いまだ十分なものとは言えず、実用化にはさらに改善を
必要とした。
However, in the jet mills developed so far, since the raw material is crushed by the swirling airflow in a certain direction, it is necessary to obtain a sufficient crushed state. It requires a considerably large amount of power energy, and it cannot be said that it is sufficient in terms of crushing capacity, etc., and further improvement was required for its practical application.

【0006】この発明は、前記問題点に着目してなされ
たもので、空気流によって原材料を粉砕するジェットミ
ルにおいて優れたエネルギー効率及び粉砕能力を達成す
ることを目的とする。
The present invention has been made in view of the above problems, and an object thereof is to achieve excellent energy efficiency and crushing ability in a jet mill which crushes raw materials by an air flow.

【0007】[0007]

【課題を解決するための手段】この発明は、下方へ向か
うに従って縮径する中空円錐台形状をなすと共に下端部
に粉砕物排出口を形成してなる本体と、前記本体の上面
中央部から内方へ挿入された排気管と、前記本体の上部
空間内において前記排気等を囲繞するよう設けられた中
空円錐台状の内筒と、を設けることにより前記内筒外面
と本体内面との間に外側環流路を形成すると共に、内筒
と排気等のとの間に内側環流路を形成し、さらに前記外
側環状流路内にその略接戦方向から空気を送給させる第
1の送気管と、前記内側還流路内にその略接戦方向から
空気を送給させる第2の送気管と、前記本体に形成した
原料供給口と、第1、第2の送気管に空気を送給する送
気装置とを設け、前記送気装置によって前記各送気管か
ら空気を各環状流路内に送給することにより、各環状流
路内にそれぞれ相反する方向へ旋回する高速旋回気流を
発生させるようにしたものである。
According to the present invention, there is provided a main body having a hollow truncated cone shape whose diameter is reduced as it goes downward and a crushed material discharge port is formed at a lower end portion, and an inner portion from a central portion of an upper surface of the main body. Between the outer surface of the inner cylinder and the inner surface of the main body by providing an exhaust pipe inserted in one direction and a hollow frustoconical inner cylinder provided so as to surround the exhaust gas in the upper space of the main body. A first air supply pipe that forms an outer ring flow path, forms an inner ring flow path between the inner cylinder and exhaust gas, and further supplies air into the outer ring flow path from a substantially close direction thereof, A second air supply pipe for supplying air into the inner return passage from a substantially close direction, a raw material supply port formed in the main body, and an air supply device for supplying air to the first and second air supply pipes. Is provided, and air is supplied from each of the air supply pipes to each annular flow by the air supply device. By feeding within, it is obtained so as to generate a high-speed swirling airflow swirling to the respective opposite directions to each annular flow path.

【0008】[0008]

【作用】この発明においては、各流路内に供給された原
材料をそれぞれ壁面との衝突や原材料同志の衝突により
粉砕した後、さらに両流路の合流部分において異なる方
向へ流動する原材料同志を激しく衝突させて粉砕する。
In the present invention, after the raw materials supplied into the respective flow paths are crushed by the collision with the wall surface and the collision of the raw materials with each other, the raw materials which flow in different directions at the confluent portion of both the flow paths are violently violent. Collide and crush.

【0009】[0009]

【実施例】以下、この発明の一実施例を図面に基づき説
明する。図において、1は脚体Lによって保持された本
体である。この本体1は下方に向かうに従って縮径する
円錐台形状をなし、上方部2,中間部3,下端部4を連
結した構造となっている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings. In the figure, 1 is a main body held by a leg L. The main body 1 has a frustoconical shape whose diameter decreases as it goes downward, and has a structure in which an upper portion 2, an intermediate portion 3, and a lower end portion 4 are connected.

【0010】また、5は前記上方部2の上側開口部を閉
塞する蓋体であり、その蓋体5の中央部には、内筒6が
固定されている。この内筒5は下方に向かうに従って縮
径する円錐台形状をなしており、上方部2内に挿入され
ている。これにより、前記上方部2の内面と内筒5との
間には、図2及び図3に示すように環状の空気流路(以
下、この流路を外側流路と称す)R1が形成される。7
は前記内筒6の中心部に挿入・固定された排気管であ
り、その上端部は内筒6より上方に突出し、下端部は内
筒6よりやや下方に位置している。そして、この排気管
7の外周面と内筒3の内周面との間には、図2及び図3
に示すように環状の空気流路(以下、この流路を内側環
状流路と称す)R2が形成されている。また、8は前記
外側環状流路R1ないに原材料を送給するための第1の
供給筒であり、前記蓋体5に形成された供給口5bに連
通している。9は前記内側環状流路R2内に原材料を供
給するための第2の供給筒であり、前記内筒6に形成さ
れた供給口5aに連通している。
Reference numeral 5 is a lid for closing the upper opening of the upper portion 2, and an inner cylinder 6 is fixed to the central portion of the lid 5. The inner cylinder 5 has a truncated cone shape whose diameter decreases as it goes downward, and is inserted into the upper portion 2. As a result, an annular air passage (hereinafter, this passage is referred to as an outer passage) R1 is formed between the inner surface of the upper portion 2 and the inner cylinder 5 as shown in FIGS. 2 and 3. It 7
Is an exhaust pipe inserted and fixed in the center of the inner cylinder 6, the upper end of which projects above the inner cylinder 6 and the lower end of which is located slightly below the inner cylinder 6. 2 and 3 are provided between the outer peripheral surface of the exhaust pipe 7 and the inner peripheral surface of the inner cylinder 3.
As shown in FIG. 3, an annular air flow path (hereinafter, this flow path is referred to as an inner annular flow path) R2 is formed. Reference numeral 8 is a first supply cylinder for feeding the raw material into the outer annular flow path R1 and communicates with a supply port 5b formed in the lid body 5. Reference numeral 9 denotes a second supply cylinder for supplying the raw material into the inner annular flow path R2, which communicates with a supply port 5a formed in the inner cylinder 6.

【0011】一方、図3において、11は送気装置とし
てのコンプレッサー10に接続された主送気管であり、
この主送気管11の先端部には、第1の送気管12と第
2の送気管13とがV字状に接続されている。このう
ち、第1の送気管12は前記上方部2の上部周壁に形成
した第1の送気口2aに接続され、第2の送気管13は
内筒3の上部周壁に形成した第2の送気口3aに接続さ
れている。また、第1,第2の送気管12,13は、各
環状流路に対して接戦方向へと空気を送給し、かつ送給
した空気が各環状流路R1,R2内で異なる方向へ旋回
するよう接続されている(図3参照)。なお、V1,V
2,V3は前記各送気管12,13における空気流量を
制限するためのバルブである。
On the other hand, in FIG. 3, 11 is a main air supply pipe connected to the compressor 10 as an air supply device,
A first air supply pipe 12 and a second air supply pipe 13 are connected to the tip of the main air supply pipe 11 in a V-shape. Of these, the first air supply pipe 12 is connected to the first air supply port 2a formed in the upper peripheral wall of the upper portion 2, and the second air supply pipe 13 is the second air supply pipe 13 formed in the upper peripheral wall of the inner cylinder 3. It is connected to the air supply port 3a. Further, the first and second air supply pipes 12 and 13 supply air to the respective annular flow paths in a close-to-close direction, and the supplied air is directed to different directions in the respective annular flow paths R1 and R2. It is connected to rotate (see FIG. 3). In addition, V1, V
Reference numerals 2 and V3 are valves for limiting the air flow rate in each of the air supply pipes 12 and 13.

【0012】以上の構成に基づき次に作用を説明する。
コンプレッサ10から主送気管11に送出された圧縮空
気は、第1の送気管12と第2の送気管13とに分流さ
れた後、各送気管12,13から前記各環状流路R1,
R2内へ噴出される。この各環状流路R1,R2内に噴
出される空気は各環状流路R1,R2の接戦方向へ向け
て噴出されるため、各流路R1,R2の壁面に沿って約
100m/sec程度の高速で旋回する渦状の気流とな
る。またその各気流の旋回方向は、互いに異なる方向と
なる。
Next, the operation will be described based on the above configuration.
The compressed air sent from the compressor 10 to the main air supply pipe 11 is divided into the first air supply pipe 12 and the second air supply pipe 13, and then the respective air supply pipes 12 and 13 make the respective annular flow paths R1.
Ejected into R2. The air jetted into each of the annular flow passages R1 and R2 is jetted toward the close battle direction of each of the annular flow passages R1 and R2, so that about 100 m / sec along the wall surface of each of the flow passages R1 and R2. A swirling air flow that swirls at high speed. The swirling directions of the respective air flows are different from each other.

【0013】ここで、粉砕すべき原材料、例えば生のこ
んにゃく芋Mをそのまま各供給筒8,9から各還流路R
1,R2内に投入すると、それらは、各還流路R1,R
2内に発生している気流に従って高速で旋回移動し、各
還流路の壁面との衝突及び原材料同志の衝突などによっ
て粉砕されながら各還流路の下方へと移動して行く。そ
してさらに、各還流路R1,R2の下方では、相反する
方向へ旋回する気流に従って原材料両同志の激しい衝突
が繰り返されると共に、中間部3の内壁との衝突も加わ
って極めて微小な粒子にまで粉砕され、最終的に排気口
から排出される。
Here, the raw material to be crushed, for example, raw konjac potato M is directly supplied from each supply cylinder 8 and 9 to each reflux path R.
1 and R2, when they are put into the respective return paths R1 and R
It swirls at a high speed according to the airflow generated in the inside of the 2, and moves to the lower side of each return passage while being crushed by the collision with the wall surface of each return passage and the collision of raw materials. Further, below each of the reflux paths R1 and R2, the violent collisions of the raw materials with each other are repeated according to the air currents that swirl in opposite directions, and the collision with the inner wall of the intermediate portion 3 is also added to pulverize the particles into extremely fine particles. And finally discharged from the exhaust port.

【0014】また、以上の粉砕過程において、高速に流
動する空気の摩擦、特に中間部3における旋回方向の異
なる気流同志の摩擦により本体1内には熱が発生する。
このため、原材料はその摩擦熱によって過熱・乾燥され
ながら粉砕されることとなり、最終的に排出口から排出
される粉粒にはほぼ完全な乾燥状態が得られる。なお、
各還流路R1,R2から中間部3に送球された空気は高
温となるため、排気筒内を上昇して外部へ排出される。
Further, in the above pulverization process, heat is generated in the main body 1 due to the friction of the air flowing at high speed, especially the friction between the air streams having different swirling directions in the intermediate portion 3.
Therefore, the raw material is pulverized while being overheated and dried by the frictional heat, and the powder particles finally discharged from the discharge port can be almost completely dried. In addition,
The air sent to the intermediate portion 3 from each of the recirculation paths R1 and R2 has a high temperature, and thus rises in the exhaust cylinder and is discharged to the outside.

【0015】このように、この実施例においては、ま
ず、内外の環状流路内R1,R2で原材料を粉砕した
後、さらに、各環状流路R1,R2を通過してきた原材
料を互いに衝突させるようにしたため、従来のような本
体内に一方向に旋回する気流を発生させるものに比べ、
粉砕能力及びエネルギー効率は大幅に向上する。
As described above, in this embodiment, first, the raw materials are crushed in the inner and outer annular flow passages R1 and R2, and then the raw materials that have passed through the respective annular flow passages R1 and R2 are made to collide with each other. Therefore, compared with the conventional one that generates an air flow that swirls in one direction,
Grinding capacity and energy efficiency are greatly improved.

【0016】なお、上記実施例においては、各環状流路
R1,R2内への原材料の供給を各供給筒8,9から別
個に行うようにしたが、この供給筒8,9に替えて、図
4に示すように二股状の供給筒15を設けても良く、こ
れによれば、単一の原料投入口15aから原材料を投入
することで各環状流路R1,R2内に原材料を供給する
ことができ、原材料の投入作業を簡略化することができ
る。
In the above embodiment, the raw materials are supplied into the annular flow paths R1 and R2 separately from the supply cylinders 8 and 9, but instead of the supply cylinders 8 and 9, As shown in FIG. 4, a bifurcated supply cylinder 15 may be provided, and according to this, the raw material is supplied into each of the annular flow paths R1 and R2 by charging the raw material from a single raw material input port 15a. Therefore, the work of charging the raw materials can be simplified.

【0017】なお、この発明に係る破砕装置は、こんに
ゃく芋などのような軟質のものに限らず、コンクリート
片などのような高い剛性を有するものの破砕にも適用可
能である。
The crushing device according to the present invention is not limited to soft ones such as konjac potato, but can also be applied to crushing concrete pieces having high rigidity.

【0018】[0018]

【発明の効果】以上説明したとおり、この発明に係るジ
ェットミルは、中空円錐台形状をなす本体内に内筒を設
けることにより、本体内に内外2個の環状流路を形成す
ると共に、各流路内にその接戦方向から空気を送給する
ことにより、各流路に沿ってそれぞれ相反する方向へ旋
回する高速旋回気流を発生させるようにしたため、従来
のような本体内に一方向に旋回する気流を発生させるも
のに比べ、粉砕能力及びエネルギー効率は大幅に向上
し、ランニングコストを著しく低減させることができ
る。
As described above, in the jet mill according to the present invention, by providing the inner cylinder in the hollow frustoconical body, two inner and outer annular flow passages are formed in the body and By sending air into the flow passage from the close direction, high-speed swirling air currents that swirl in opposite directions along each flow passage are generated. The crushing capacity and energy efficiency are significantly improved, and the running cost can be significantly reduced, as compared with the one generating the air flow.

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

【図1】この発明の一実施例における本体を示す分解斜
視図である。
FIG. 1 is an exploded perspective view showing a main body according to an embodiment of the present invention.

【図2】図1に示したものの縦断側面図である。FIG. 2 is a vertical sectional side view of what is shown in FIG.

【図3】同上実施例の平面図である。FIG. 3 is a plan view of the above embodiment.

【図4】同上実施例における供給管の変更例を示す側面
図である。
FIG. 4 is a side view showing a modification of the supply pipe in the above embodiment.

【符号の説明】[Explanation of symbols]

1 本体 2 上方部 4a 粉砕物排出口 6 内筒 7 排気筒 10 コンプレッサー(送気装置) 12 第1の送気管 13 第2の送気管 R1 第1の環状流路 R2 第2の環状流路 1 Main Body 2 Upper Part 4a Crushed Material Discharge Port 6 Inner Cylinder 7 Exhaust Cylinder 10 Compressor (Air Supply Device) 12 First Air Supply Pipe 13 Second Air Supply Pipe R1 First Annular Flow Path R2 Second Annular Flow Path

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 下方へ向かうに従って縮径する中空円錐
台形状をなすと共に下端部に粉砕物排出口を形成してな
る本体と、 前記本体の上面中央部から内方へ挿入された排気管と、 前記本体の上部空間内において前記排気等を囲繞するよ
う設けられた中空円錐台状の内筒と、を設けることによ
り、 前記内筒外面と本体内面との間に外側還流路を、内筒と
排気等のとの間に内側環流路をそれぞれ形成すると共
に、 前記各環状流路に粉砕すべき原料を供給する原料供給口
と、 前記外側環状流路内にその略接戦方向から空気を送給さ
せる第1の送気管と、 前記内側環状流路内にその略接戦方向から空気を送球さ
せる第2の送気管と、 第1、第2の送気管に空気を送給する送気装置とを設け
てなり、 前記送気装置によって前記各送気管から空気を各環状流
路内に送給することにより、各環状流路内にそれぞれ相
反する方向へ旋回する渦巻状の高速気流を発生させ、各
高速気流によって本体内に供給された原料を粉砕するよ
うにしたことを特徴とする粉砕装置。
1. A main body having a hollow truncated cone shape whose diameter decreases as it goes downward and having a crushed material discharge port formed at a lower end thereof, and an exhaust pipe inserted inward from a central portion of an upper surface of the main body. A hollow circular truncated cone-shaped inner cylinder provided so as to surround the exhaust gas and the like in the upper space of the main body, thereby providing an outer return path between the outer surface of the inner cylinder and the inner surface of the main body. An inner ring flow path between the inner ring flow path and the exhaust gas, and a raw material supply port for supplying the raw material to be crushed to each of the ring flow paths, and an air flow in the outer ring flow path from a substantially close direction. A first air supply pipe for supplying air, a second air supply pipe for supplying air into the inner annular flow path from a substantially close direction, and an air supply device for supplying air to the first and second air supply pipes Is provided, and air is supplied from each of the air supply pipes by the air supply device. The high-speed air currents of the spiral shape that swirl in opposite directions are generated in each annular flow path by feeding into the annular flow path, and the raw material supplied into the main body is crushed by each high-speed air flow. A crushing device characterized by the above.
JP11320392A 1992-04-07 1992-04-07 Jet mill Withdrawn JPH0615193A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11320392A JPH0615193A (en) 1992-04-07 1992-04-07 Jet mill

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11320392A JPH0615193A (en) 1992-04-07 1992-04-07 Jet mill

Publications (1)

Publication Number Publication Date
JPH0615193A true JPH0615193A (en) 1994-01-25

Family

ID=14606175

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11320392A Withdrawn JPH0615193A (en) 1992-04-07 1992-04-07 Jet mill

Country Status (1)

Country Link
JP (1) JPH0615193A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6543710B2 (en) * 2000-07-11 2003-04-08 Hosokawa Alpine Aktiengesellschaft & Co. Ohg Separator mill

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6543710B2 (en) * 2000-07-11 2003-04-08 Hosokawa Alpine Aktiengesellschaft & Co. Ohg Separator mill

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Effective date: 19990608