JP2000140675A - Pulverizer - Google Patents

Pulverizer

Info

Publication number
JP2000140675A
JP2000140675A JP32366198A JP32366198A JP2000140675A JP 2000140675 A JP2000140675 A JP 2000140675A JP 32366198 A JP32366198 A JP 32366198A JP 32366198 A JP32366198 A JP 32366198A JP 2000140675 A JP2000140675 A JP 2000140675A
Authority
JP
Japan
Prior art keywords
inlet
throat
diffuser
pulverized
compressed 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
JP32366198A
Other languages
Japanese (ja)
Inventor
Kaoru Inui
薫 乾
Hirokazu Nakamura
裕計 中村
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.)
Nippon Pneumatic Manufacturing Co Ltd
Original Assignee
Nippon Pneumatic Manufacturing Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nippon Pneumatic Manufacturing Co Ltd filed Critical Nippon Pneumatic Manufacturing Co Ltd
Priority to JP32366198A priority Critical patent/JP2000140675A/en
Publication of JP2000140675A publication Critical patent/JP2000140675A/en
Pending legal-status Critical Current

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  • Disintegrating Or Milling (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a pulverizer by which material to be pulverized is effectively ground. SOLUTION: Compressed air fed to an inlet 13 of an accelerating nozzle 12 is throttled at a throat part 14 and is expanded at a diffuser part 15 installed on the downstream side of the throat part 14 to form a jet air current. Material to be pulverized is fed into the jet flow current from a feeding port 17 formed in the peripheral wall of the diffuser part 15 to hit the material to be pulverized against an impingement plate 4 to pulverize it. In the throat part 14, a circular- arcuate inner surface 14a smoothly connecting with the inner surface of the inlet 13, and the tapered inner surface of the diffuser part 15 is formed to prevent turbulence from being generated in the compressed gas flowing from the inlet 13 to the throat part 14, and by formation of the fast jet air current, pulverizing efficiency of the material to be pulverized is increased and also fine grinding is enabled.

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】この発明は、圧縮気体を用い
る衝突式の粉砕装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a collision type pulverizer using a compressed gas.

【0002】[0002]

【従来の技術】衝突式の粉砕装置は、圧縮気体によって
ジェット噴流を形成し、そのジェット噴流中にトナー等
の被粉砕物を供給し、この被粉砕物を衝突部材に衝突さ
せ、衝突時の衝撃により被粉砕物を粉砕するようにして
いる。
2. Description of the Related Art A collision type pulverizing apparatus forms a jet jet by a compressed gas, supplies an object to be pulverized such as toner into the jet jet, and makes the object to collide with a collision member. The object to be crushed is crushed by the impact.

【0003】上記粉砕装置として、図5に示したものが
従来から知られている。この粉砕装置は、圧縮気体の供
給ノズル1の先端に加速ノズル2を接続し、その加速ノ
ズル2の前側に設けられた粉砕室3内に衝突部材4を設
けている。
[0003] As the above-mentioned pulverizing apparatus, the one shown in FIG. 5 has been conventionally known. In this pulverizing apparatus, an acceleration nozzle 2 is connected to the tip of a compressed gas supply nozzle 1, and a collision member 4 is provided in a pulverization chamber 3 provided in front of the acceleration nozzle 2.

【0004】加速ノズル2は、供給ノズル1に連通する
入口5の下流側にスロート部6を形成し、このスロート
部6によって入口5に供給される圧縮気体を絞り込んで
圧力を高め、そのスロート部6の下流側に形成されたテ
ーパ状のデイフューザ部7において減圧し、加速してジ
ェット気流を形成するようにしている。
The accelerating nozzle 2 forms a throat 6 downstream of the inlet 5 communicating with the supply nozzle 1. The throat 6 narrows down the compressed gas supplied to the inlet 5 to increase the pressure, thereby increasing the pressure. The pressure is reduced and accelerated in a tapered diffuser section 7 formed downstream of the jet diffuser 6 to form a jet stream.

【0005】デイフューザ部7の周壁上部には供給口8
が設けられ、その供給口8にホッパ9の下端出口を接続
し、このホッパ9内の被粉砕物を上記供給口8からデイ
フューザ部7内のジェット気流中に供給し、この被粉砕
物を前記衝突部材4の円錐形の衝突面4aに衝突させて
衝撃力により粉砕するようにしている。
A supply port 8 is provided at the upper part of the peripheral wall of the diffuser section 7.
The lower end outlet of the hopper 9 is connected to the supply port 8, and the material to be ground in the hopper 9 is supplied from the supply port 8 into the jet stream in the diffuser unit 7, and the material to be ground is It is made to collide with the conical collision surface 4a of the collision member 4 and to be ground by an impact force.

【0006】また、粉砕後の被粉砕物を衝突部材4の半
径方向に飛散させ、その被破砕物を粉砕室3の内周に設
けられたライナー10に衝突させて二次粉砕するように
している。
Further, the crushed material is scattered in the radial direction of the collision member 4, and the crushed material collides with a liner 10 provided on the inner periphery of the crushing chamber 3 to perform secondary crushing. I have.

【0007】なお、粉砕後の粉砕物は、粉砕室3の出口
11から分級機に送り込んで粗粉と細粉とに分級し、粗
粉を前記ホッパ9内に戻して再度粉砕し、細粉を製品と
している。
The pulverized material after pulverization is sent to a classifier through an outlet 11 of the pulverizing chamber 3 to be classified into coarse powder and fine powder, and the coarse powder is returned to the hopper 9 and pulverized again. Is the product.

【0008】ここで、複写機に用いられる画像形成用の
トナーにおいては、鮮明な画像を得るうえにおいて、そ
の体積平均粒子径が13μm以下の微細なものが好まし
く、そのような微細なトナーを得るためには、加速ノズ
ル2内で形成されるジェット気流の流速を高め、衝突部
材4に対する衝突力を高める必要がある。
In order to obtain a clear image, a fine toner having a volume average particle diameter of 13 μm or less is preferable for obtaining a clear image, and such a fine toner is obtained. For this purpose, it is necessary to increase the flow velocity of the jet airflow formed in the acceleration nozzle 2 and increase the collision force against the collision member 4.

【0009】[0009]

【発明が解決しようとする課題】ところで、ジェット気
流を形成する従来の加速ノズル2においては、圧縮気体
の圧力を高めるスロート部6の内表面が、入口5におけ
る内周面との接続部およびデイフューザ部6におけるテ
ーパ状内面の接続部にエッジを形成する円筒状であるた
め、圧縮気体がそのスロート部6に流れるときに乱れが
生じ、エネルギ損失が生じ易い。
By the way, in the conventional acceleration nozzle 2 for forming a jet stream, the inner surface of the throat portion 6 for increasing the pressure of the compressed gas has a connection portion with the inner peripheral surface at the inlet 5 and a diffuser. Since the compressed gas flows into the throat portion 6, turbulence occurs and energy loss is likely to occur due to the cylindrical shape forming an edge at the connection portion of the tapered inner surface of the portion 6.

【0010】また、スロート部6を通過した圧縮気体
は、デイフューザ部7での膨張により加速され、超音速
まで加速されるが、上記デイフューザ部7は加速ノズル
2の出口まで拡がりをもつテーパ状であるため、供給口
8付近において衝撃波が形成され、その位置からは圧縮
流体というよりむしろ非圧縮流体の挙動となり、加速ノ
ズル2の断面積の増加に伴ってジェット気流の流速が低
下する。
The compressed gas that has passed through the throat section 6 is accelerated by expansion in the diffuser section 7 and accelerated to supersonic speed. The diffuser section 7 has a tapered shape expanding to the outlet of the acceleration nozzle 2. Therefore, a shock wave is formed in the vicinity of the supply port 8, and the position of the shock wave becomes an incompressible fluid rather than a compressed fluid from that position, and the flow velocity of the jet stream decreases with an increase in the sectional area of the acceleration nozzle 2.

【0011】このため、ジェット気流に同伴される被破
砕物の衝突エネルギが低下し、被粉砕物を微小な領域ま
で微粉砕することができず、粉砕効率も低いという不都
合があった。
For this reason, the collision energy of the object to be crushed accompanying the jet stream is reduced, so that the object to be crushed cannot be finely crushed to a minute area, and the crushing efficiency is low.

【0012】この発明の課題は、被粉砕物を微小な領域
まで効率よく微粉砕することができる粉砕装置を提供す
ることである。
An object of the present invention is to provide a pulverizing apparatus capable of efficiently pulverizing an object to be pulverized to a minute area.

【0013】[0013]

【課題を解決するための手段】上記の課題を解決するた
めに、この発明においては、入口に供給される圧縮気体
を、その入口の下流側に設けられたスロート部において
絞ると共に、そのスロート部の下流側に設けられたテー
パ状のデイフューザ部において膨張させてジェット気流
を形成する加速ノズル内に被粉砕物を供給し、この被粉
砕物を加速ノズルの先端出口から、その出口と間隔をお
いて対向配置した衝突部材に衝突させて粉砕する粉砕装
置において、前記スロート部の内面を、入口の内表面と
デイフューザ部のテーパ状内面のそれぞれに滑らかに連
続する円弧状内面とした構成を採用している。
In order to solve the above-mentioned problems, according to the present invention, compressed gas supplied to an inlet is throttled at a throat provided downstream of the inlet and the throat is provided. The material to be crushed is supplied to an acceleration nozzle that expands in a tapered diffuser portion provided on the downstream side of the nozzle and forms a jet airflow, and the material to be crushed is spaced from the outlet of the acceleration nozzle from the tip outlet of the acceleration nozzle. In the crushing device for crushing by colliding with the colliding member disposed oppositely, the inner surface of the throat portion adopts an arc-shaped inner surface that is smoothly continuous with each of the inner surface of the inlet and the tapered inner surface of the diffuser portion. ing.

【0014】上記のように、スロート部の内面を円弧状
内面とすると、圧縮気体はその円弧状内面に沿って滑ら
かに流れるため、エネルギの損失を抑え、スロート部に
続くデイフューザ部において、流速の速いジェット気流
の形成が可能となり、そのジェット気流に同伴される被
粉砕物に大きい速度エネルギを付与することができる。
As described above, when the inner surface of the throat portion is an arc-shaped inner surface, the compressed gas flows smoothly along the arc-shaped inner surface, so that the loss of energy is suppressed, and the flow velocity of the gas in the diffuser portion following the throat portion is reduced. A fast jet stream can be formed, and a large velocity energy can be imparted to the object to be ground entrained in the jet stream.

【0015】ここで、前記デイフューザの出口側に断面
積が軸方向の全長にわたって同一大きさのストレート部
を設けると、デイフューザ部において形成されるジェッ
ト気流の流速を略一定に保つことができ、被粉砕物の速
度エネルギの低下を抑制することができる。 〔発明の詳細な説明〕
If a straight section having the same cross-sectional area is provided on the outlet side of the diffuser over the entire length in the axial direction, the flow velocity of the jet airflow formed in the diffuser section can be kept substantially constant, and It is possible to suppress a reduction in velocity energy of the pulverized material. [Detailed description of the invention]

【0016】以下、この発明の実施の形態を図1乃至図
4に基づいて説明する。
An embodiment of the present invention will be described below with reference to FIGS.

【0017】図1は、この発明に係る粉砕装置を示す。
この粉砕装置と、先に述べた図5に示す従来の粉砕装置
とは加速ノズル12の構成が相違するのみであるため、
同一の部品に同一符号を付して説明を省略する。
FIG. 1 shows a pulverizing apparatus according to the present invention.
Since this pulverizing apparatus differs from the conventional pulverizing apparatus shown in FIG. 5 only in the configuration of the acceleration nozzle 12,
The same components are denoted by the same reference numerals and description thereof will be omitted.

【0018】加速ノズル12は、図2に示すように、入
口13、スロート部14、デイフューザ部15およびス
トレート部16を有し、上記デイフューザ部15の周壁
上部に被粉砕物の供給口17が設けられている。
As shown in FIG. 2, the accelerating nozzle 12 has an inlet 13, a throat portion 14, a diffuser portion 15, and a straight portion 16, and a supply port 17 for the material to be ground is provided on the upper peripheral wall of the diffuser portion 15. Have been.

【0019】スロート部14の内面14aは、入口13
の内表面13aとデイフューザ部15のテーパ状内面1
5aに滑らかに連続する円弧状とされている。
The inner surface 14a of the throat portion 14 is
Inner surface 13a and the tapered inner surface 1 of the diffuser portion 15
The shape of the arc is smoothly continuous with 5a.

【0020】ここで、スロート部14における円弧状内
面14aの曲率半径rは、小さ過ぎると、角ばってスロ
ート部14を流動する圧縮気体の流れに乱れが生じ、一
方、大きくなり過ぎると、スロート部14の軸方向長さ
が長くなり、管路抵抗が増大して圧縮気体のエネルギロ
スが大きくなる。このため、上記曲率半径は、スロート
部14における通路半径の2〜5倍程度が好ましい。
Here, if the radius of curvature r of the arc-shaped inner surface 14a of the throat portion 14 is too small, the flow of the compressed gas flowing through the throat portion 14 becomes turbulent. The axial length of the portion 14 is increased, the pipe resistance is increased, and the energy loss of the compressed gas is increased. Therefore, the radius of curvature is preferably about 2 to 5 times the radius of the passage in the throat portion 14.

【0021】上記のように、スロート部14の内面14
aを円弧状とすると、入口13に供給された圧縮気体が
スロート部14を流れるとき、圧縮気体は乱れを生じる
ことなく滑らかに流れてデイフューザ部15に流入す
る。
As described above, the inner surface 14 of the throat 14
When a is formed in an arc shape, when the compressed gas supplied to the inlet 13 flows through the throat portion 14, the compressed gas flows smoothly without generating turbulence and flows into the diffuser portion 15.

【0022】このため、スロート部14において圧縮気
体にエネルギ損失が生じるのを防止することができる。
Therefore, it is possible to prevent the compressed gas from losing energy in the throat portion 14.

【0023】スロート部14において圧縮された気体
は、デイフューザ部15に流入すると、膨張し、流速が
増大して超音速の状態となり、ジェット気流が形成され
る。このジェット気流の流れにより供給口7に吸引力が
作用し、ホッパ9内の被粉砕物はデイフューザ部15に
吸引されてジェット気流中に供給される。
When the gas compressed in the throat section 14 flows into the diffuser section 15, it expands, the flow velocity increases, and the state becomes supersonic, and a jet stream is formed. A suction force acts on the supply port 7 by the flow of the jet airflow, and the material to be ground in the hopper 9 is sucked by the diffuser unit 15 and supplied into the jet airflow.

【0024】ここで、デイフューザ部15が加速ノズル
12の出口に至るまでの長さであると、供給口17の下
流側において衝撃波が生じ、あるいは圧縮気体が膨張し
過ぎてジェット気流の流速が大幅に低下する。
If the diffuser 15 is long enough to reach the outlet of the acceleration nozzle 12, a shock wave is generated on the downstream side of the supply port 17, or the compressed gas expands too much, and the flow velocity of the jet gas flow becomes large. To decline.

【0025】しかしながら、実施の形態における加速ノ
ズル12においては、供給口17の下流側に断面積が軸
方向の全長にわたって均一のストレート部16を設けて
いるため、ジェット気流の流速の大幅な低下が防止され
る。
However, in the acceleration nozzle 12 according to the embodiment, the straight portion 16 having a uniform cross-sectional area over the entire length in the axial direction is provided on the downstream side of the supply port 17, so that the flow velocity of the jet stream is significantly reduced. Is prevented.

【0026】このため、ジェット気流に同伴される被粉
砕物は大きい速度エネルギをもち、加速ノズル12の出
口から高速度で噴射されて衝突板4と激しく衝突するこ
とになり、衝突時のエネルギが大きいため、きわめて効
果的に微粉砕される。
For this reason, the material to be crushed entrained in the jet stream has a large velocity energy, is jetted at a high speed from the outlet of the acceleration nozzle 12 and collides violently with the collision plate 4, and the energy at the time of collision is reduced. Due to their large size, they are very effectively pulverized.

【0027】いま、図3に示すように、3本の形状の異
なる加速ノズルを用意し、その加速ノズルを図1に示す
粉砕装置中に組付けて、平均粒径30μmのトナーの粉
砕を行なったところ、図4に示す結果を得た。
Now, as shown in FIG. 3, three accelerating nozzles having different shapes are prepared, and the accelerating nozzles are assembled in the pulverizing apparatus shown in FIG. 1 to pulverize a toner having an average particle diameter of 30 μm. As a result, the result shown in FIG. 4 was obtained.

【0028】ここで、図3(I)に示す加速ノズル(発
明品I)は、図1に示す加速ノズルを示し、各部の寸法
は、表1のとおりである。
Here, the acceleration nozzle (invention I) shown in FIG. 3 (I) shows the acceleration nozzle shown in FIG. 1, and the dimensions of each part are as shown in Table 1.

【0029】[0029]

【表1】 [Table 1]

【0030】図3(II)に示す加速ノズル(発明品II)
は、スロート部に円弧状内面を形成し、デイフューザ部
をノズル先端で開口させた加速ノズルを示し、各部の寸
法は図3(I)に示す加速ノズルの各部の寸法と等しく
なっている。
The acceleration nozzle shown in FIG. 3 (II) (Invention product II)
Indicates an acceleration nozzle having an arcuate inner surface formed in the throat portion and a diffuser portion opened at the nozzle tip, and the dimensions of each portion are equal to those of the acceleration nozzle shown in FIG.

【0031】図3(III )に示す加速ノズル(従来品)
は、図5に示す粉砕装置の加速ノズルを示し、スロート
部6の軸方向長さL4 は10mmとされ、残りの各部の
寸法は、図3(I)に示す加速ノズルの各部の寸法と同
一とされている。
The acceleration nozzle shown in FIG. 3 (III) (conventional product)
5 shows an acceleration nozzle of the pulverizing device shown in FIG. 5, the axial length L 4 of the throat portion 6 is 10 mm, and the dimensions of the remaining parts are the same as those of the acceleration nozzle shown in FIG. It is the same.

【0032】また、粉砕条件として、供給ノズル1に供
給する高圧気体の圧力PをP=6kg/cm2 とし、粉
砕室3の出口11から排出される粉砕物を分級機で粗粉
と細粉に分級して粗粉をホッパ9内に戻し、回収された
細粉をコールター株式会社製のコールターマルチサイザ
IIで測定した。
As the pulverization conditions, the pressure P of the high-pressure gas supplied to the supply nozzle 1 is set to P = 6 kg / cm 2, and the pulverized material discharged from the outlet 11 of the pulverization chamber 3 is separated into coarse powder and fine powder by a classifier. The coarse powder is returned to the hopper 9 and the collected fine powder is collected by a Coulter Multisizer manufactured by Coulter Co., Ltd.
Measured in II.

【0033】図5から明らかなように、スロート部14
に円弧状内面14aを形成した加速ノズル(発明品I、
発明品II)を用いてトナーを粉砕することにより、スロ
ート部14の円筒状の加速ノズル(従来品)を用いた場
合よりも、平均粒子径の小さい粉砕物を得ることができ
る。
As is apparent from FIG. 5, the throat portion 14
Nozzle having an arcuate inner surface 14a formed therein (Invention I,
By pulverizing the toner using the invention product II), a pulverized product having a smaller average particle diameter can be obtained than when a cylindrical acceleration nozzle (conventional product) of the throat portion 14 is used.

【0034】[0034]

【発明の効果】以上のように、この発明においては、加
速ノズルのスロート部に入口の内表面とデイフューザ部
のテーパ状内面に滑らかに連続する円弧状内面を形成し
たことにより、入口からスロート部に流れる圧縮気体の
乱れを防止し、圧縮気体のエネルギロスを小さくするこ
とができる。
As described above, according to the present invention, the throat portion of the acceleration nozzle is formed with an arc-shaped inner surface that is smoothly continuous with the inner surface of the inlet and the tapered inner surface of the diffuser portion. The turbulence of the compressed gas flowing through the compressed gas can be prevented, and the energy loss of the compressed gas can be reduced.

【0035】このため、スロート部に続くデイフューザ
部において流速の速いジェット気流を形成することがで
き、そのジェット気流に同伴される被粉砕物を衝突板に
対する衝突によって効率よく微粉砕することができる。
Therefore, a jet stream having a high flow velocity can be formed in the diffuser section following the throat section, and the object to be crushed accompanying the jet stream can be efficiently pulverized by collision with the collision plate.

【0036】また、デイフューザの出口側にストレート
部を設けることによって、被粉砕物をより効果的に微粉
砕することができる。
Further, by providing a straight portion on the outlet side of the diffuser, the material to be ground can be finely ground.

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

【図1】この発明に係る粉砕装置の断面図FIG. 1 is a cross-sectional view of a crusher according to the present invention.

【図2】同上の加速ノズルを示す断面図FIG. 2 is a sectional view showing the accelerating nozzle according to the first embodiment;

【図3】(I)乃至(III )は各種の加速ノズルを示す
断面図
FIGS. 3A to 3C are cross-sectional views showing various acceleration nozzles.

【図4】図3(I)乃至(III )に示す加速ノズルを用
いた被粉砕物の粉砕効果を示すグラフ
FIG. 4 is a graph showing a pulverizing effect of an object to be pulverized using the acceleration nozzle shown in FIGS. 3 (I) to (III).

【図5】従来の粉砕装置を示す断面図FIG. 5 is a cross-sectional view showing a conventional crusher.

【符号の説明】[Explanation of symbols]

3 粉砕室 4 衝突部材 12 加速ノズル 13 入口 14 スロート部 15 デイフューザ部 16 ストレート部 Reference Signs List 3 crushing chamber 4 collision member 12 acceleration nozzle 13 inlet 14 throat section 15 diffuser section 16 straight section

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 入口に供給される圧縮気体を、その入口
の下流側に設けられたスロート部において絞ると共に、
そのスロート部の下流側に設けられたテーパ状のデイフ
ューザ部において膨張させてジェット気流を形成する加
速ノズル内に被粉砕物を供給し、この被粉砕物を加速ノ
ズルの先端出口から、その出口と間隔をおいて対向配置
した衝突部材に衝突させて粉砕する粉砕装置において、
前記スロート部の内面を、入口の内表面とデイフューザ
部のテーパ状内面のそれぞれに滑らかに連続する円弧状
内面としたことを特徴とする粉砕装置。
1. A compressed gas supplied to an inlet is throttled at a throat provided downstream of the inlet,
The material to be crushed is supplied to an acceleration nozzle that expands in a tapered diffuser portion provided on the downstream side of the throat portion to form a jet airflow, and the material to be crushed is supplied from the tip outlet of the acceleration nozzle to the outlet thereof. In a crushing device that crushes by colliding with a colliding member arranged oppositely at an interval,
A pulverizing device, wherein the inner surface of the throat portion is an arc-shaped inner surface that smoothly continues to each of the inner surface of the inlet and the tapered inner surface of the diffuser portion.
【請求項2】 前記デイフューザ部の出口側に断面積が
軸方向の全長にわたって同一大きさのストレート部を設
けたことを特徴とする請求項1に記載の粉砕装置。
2. The crushing device according to claim 1, wherein a straight portion having a same cross-sectional area over the entire length in the axial direction is provided on an outlet side of the diffuser portion.
JP32366198A 1998-11-13 1998-11-13 Pulverizer Pending JP2000140675A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP32366198A JP2000140675A (en) 1998-11-13 1998-11-13 Pulverizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP32366198A JP2000140675A (en) 1998-11-13 1998-11-13 Pulverizer

Publications (1)

Publication Number Publication Date
JP2000140675A true JP2000140675A (en) 2000-05-23

Family

ID=18157208

Family Applications (1)

Application Number Title Priority Date Filing Date
JP32366198A Pending JP2000140675A (en) 1998-11-13 1998-11-13 Pulverizer

Country Status (1)

Country Link
JP (1) JP2000140675A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
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JP2005296873A (en) * 2004-04-14 2005-10-27 Sankemikkusu Tokai:Kk Solid-gas mixing ejector and jet mill
US7866581B2 (en) 2004-02-10 2011-01-11 Kao Corporation Method of manufacturing toner
JP2013223858A (en) * 2012-03-21 2013-10-31 Ricoh Co Ltd Method and apparatus for manufacturing toner
US9327288B2 (en) 2011-02-28 2016-05-03 Nisshin Engineering Inc. Method of grinding powder
JP2017070903A (en) * 2015-10-07 2017-04-13 日本ニューマチック工業株式会社 Pulverizing apparatus
CN106993667A (en) * 2017-04-04 2017-08-01 绍兴御茶村茶业有限公司 One kind smears tea production technology and equipment
DE102005046765B4 (en) 2004-10-01 2022-09-15 Kao Corp. Process for producing a toner and toner

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7866581B2 (en) 2004-02-10 2011-01-11 Kao Corporation Method of manufacturing toner
JP2005296873A (en) * 2004-04-14 2005-10-27 Sankemikkusu Tokai:Kk Solid-gas mixing ejector and jet mill
JP4575017B2 (en) * 2004-04-14 2010-11-04 株式会社ナノプラス Solid-gas mixing ejector and jet mill
DE102005046765B4 (en) 2004-10-01 2022-09-15 Kao Corp. Process for producing a toner and toner
US9327288B2 (en) 2011-02-28 2016-05-03 Nisshin Engineering Inc. Method of grinding powder
JP2013223858A (en) * 2012-03-21 2013-10-31 Ricoh Co Ltd Method and apparatus for manufacturing toner
US9022307B2 (en) 2012-03-21 2015-05-05 Ricoh Company, Ltd. Pulverizer
JP2017070903A (en) * 2015-10-07 2017-04-13 日本ニューマチック工業株式会社 Pulverizing apparatus
CN106993667A (en) * 2017-04-04 2017-08-01 绍兴御茶村茶业有限公司 One kind smears tea production technology and equipment
CN106993667B (en) * 2017-04-04 2020-07-28 绍兴御茶村茶业有限公司 Matcha production process and equipment

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