JPS5966362A - Ultra-finely crushing machine - Google Patents

Ultra-finely crushing machine

Info

Publication number
JPS5966362A
JPS5966362A JP17575182A JP17575182A JPS5966362A JP S5966362 A JPS5966362 A JP S5966362A JP 17575182 A JP17575182 A JP 17575182A JP 17575182 A JP17575182 A JP 17575182A JP S5966362 A JPS5966362 A JP S5966362A
Authority
JP
Japan
Prior art keywords
rotor
jet
stator
crushed
casing
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
JP17575182A
Other languages
Japanese (ja)
Other versions
JPS6136457B2 (en
Inventor
萩原 達雄
長野 昭治
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.)
Kawasaki Heavy Industries Ltd
Kawasaki Motors Ltd
Original Assignee
Kawasaki Heavy Industries Ltd
Kawasaki Jukogyo 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 Kawasaki Heavy Industries Ltd, Kawasaki Jukogyo KK filed Critical Kawasaki Heavy Industries Ltd
Priority to JP17575182A priority Critical patent/JPS5966362A/en
Publication of JPS5966362A publication Critical patent/JPS5966362A/en
Publication of JPS6136457B2 publication Critical patent/JPS6136457B2/ja
Granted legal-status Critical Current

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  • Crushing And Grinding (AREA)
  • Disintegrating Or Milling (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 本発明は、被粉砕物の粒子を数ミクロンオーダーの超微
細な粒子に微粉砕する為の超微粉砕機に係るものである
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an ultrafine pulverizer for pulverizing particles of a material to be pulverized into ultrafine particles on the order of several microns.

従来、被粉砕物の粒子を微粉砕するには、高速回転衝撃
形の竪型粉砕機又はジェットミル若しくは両者を併用し
た微粉砕設備にで行っていた。
Conventionally, the particles of the material to be crushed have been pulverized using a high-speed rotational impact type vertical crusher, a jet mill, or a pulverization equipment using a combination of both.

前記製型粉砕機は、外側表面の母線に沿って多数の凸部
を有する円筒状同転子を垂直回転軸に支持し、この円筒
状回転子との間に一定間隙を存して内側表面の母線に沿
って多数の凸部を有する固定子を嵌装したもので、円筒
状回転子と固定子との間の間隙に被粉砕物を供給し、前
記円筒状回転子を高速回転することにより被粉砕物を粉
砕するものである。
The mold crusher has a cylindrical rotor having a large number of protrusions along the generatrix of the outer surface supported on a vertical rotating shaft, and a fixed gap between the cylindrical rotor and the inner surface. A stator having a large number of convex portions is fitted along the generatrix of the rotor, and the material to be crushed is supplied to the gap between the cylindrical rotor and the stator, and the cylindrical rotor is rotated at high speed. The material to be crushed is crushed by this method.

この被粉砕物の粉砕過程は、り゛−シング下方に設けら
れた供給口から円筒状回転子と固定子との間の環状間隙
内に被粉砕物が供給され、高速回転している円筒・状回
転子の回転力によつヤ・□被粉砕、港に速度エネルギー 衝突踵粉砕されが臥ら円筒状回転子の自転によつそ生じ
る環状間隙内d上向き螺旋気流によ−っでE方に運ばれ
、ケーシング上方の排出口必・1.5 ら粉砕製品として排出される。
In the process of crushing the material to be crushed, the material to be crushed is supplied into the annular gap between the cylindrical rotor and the stator from a supply port provided below the grinder, and the cylindrical material is rotated at high speed. Due to the rotational force of the cylindrical rotor, the heel is crushed, and the heel is crushed due to the upward spiral airflow inside the annular gap created by the rotation of the cylindrical rotor. The crushed product is then discharged as a pulverized product through a discharge port located above the casing.

このような粉砕過程をとる竪型粉砕機では、ある程度ま
で被粉砕物が粉砕されると、環状間。
In a vertical crusher that uses this type of crushing process, once the material to be crushed has been crushed to a certain extent, the annular gap will form.

隙内の上向き螺旋気流に乗って円筒状回転子と共に粉砕
製品も回転1.てしまい、円筒状回転子の周速と粉砕製
品と9.間の相対速度が減少し、その結果衝撃効界が減
少し、下しまりので、数ミクロンオーダーの超微粉を、
得ることは不可能である。
The pulverized product also rotates along with the cylindrical rotor riding the upward spiral airflow in the gap.1. 9. The peripheral speed of the cylindrical rotor and the crushed product. As the relative velocity between the
It is impossible to obtain.

まだジェットミルは、圧縮空気又は高熱蒸気を粉砕室に
設けられたノズルを通し、速度エネルギーに変え、高速
気流の軌跡を作り、この超音速ジェット気流中に被粉砕
物である粉粒体を連続且つ自動的に供給して、強い衝撃
、摩擦を生じしめて粉砕を行うもので、数ミクロンオー
ダ」の超微粉を得ることが可能である。
Jet mills pass compressed air or high-temperature steam through a nozzle installed in the grinding chamber, convert it into velocity energy, create a trajectory of high-speed airflow, and continuously transport the powder and granules to be ground into this supersonic jet stream. Moreover, by automatically supplying the powder and pulverizing it by generating strong impact and friction, it is possible to obtain ultrafine powder on the order of several microns.

園 しか、し、被粉砕物である粉粒体の粒子の大きさが
矢″きくなると、極端に処理能力が低下し、その為被粉
砕物:i・□kpを処理す乏為α弓ンブレッを一駆動の
電力消費量KW f”h/hp (苑iる被粉砕物の種
類及びミルの大きさにもよるが一般的には1〜4 KW
 −h/、である。)が増大するものである。  、。
Sono However, when the particle size of the granular material that is the material to be crushed becomes large, the processing capacity will be extremely reduced, and as a result, the α-bow unit will be insufficient to process the material to be crushed: i・□kp. Power consumption per drive KW f”h/hp (depending on the type of material to be crushed and the size of the mill, but generally 1 to 4 KW)
-h/. ) increases. ,.

さらに前記竪型粉砕機とジエン1ソミ、ビレを別置きし
た微粉砕設備は、単に空気輸送設備等で竪型粉砕機とシ
ェフ 1− 、ミルを結合したもので、これの微粉砕処
理工程を第1図によってd)古明・すると、竪型粉砕機
1に、供給さ、れ尼、・被粉□砕物が・□粉砕、され−
その粉砕製品が排風機4の駆動により排出管24通って
バッグフィルター3に空気輸送され、ここで空気と粉砕
製品が分離され、空気が排風機4を経て排気管5から排
気され、粉砕製品がホッパー6に一時貯留される。ホッ
パー6内の粉砕製品はフィーダ7により輸送管8に送り
出され、隔った位置に設けられている排風機10の駆動
によシ輸送管8を通ってバッグフィルター9に空気輸送
され、ここf空気と粉砕製品が分離され、空気が排風機
1oを経て排気管11から排気され、粉砕製品がホッパ
ー12に一時貯留される。このホッパー12内の粉砕製
品はフィーダ13によりジェットミルト4に供給され、
圧縮空気の噴出にょシ微粉砕される。
Furthermore, the fine grinding equipment in which the vertical grinder, the diene mill, and the mill are installed separately is simply a combination of the vertical grinder, the chef 1-mill, and the mill using air conveyance equipment, etc., and the fine grinding process is According to Figure 1, d) Ancient and Ming Dynasty: Then, the material to be crushed is fed to the vertical crusher 1, and the crushed material is crushed.
The pulverized product is air-transported to the bag filter 3 through the exhaust pipe 24 by the drive of the exhaust fan 4, where the air and the pulverized product are separated, and the air is exhausted from the exhaust pipe 5 through the exhaust fan 4, and the pulverized product is It is temporarily stored in the hopper 6. The pulverized product in the hopper 6 is sent to a transport pipe 8 by a feeder 7, and is pneumatically transported through the transport pipe 8 to a bag filter 9 by the drive of an exhaust fan 10 provided at a separate position. Air and the pulverized product are separated, the air is exhausted from the exhaust pipe 11 through the exhaust fan 1o, and the pulverized product is temporarily stored in the hopper 12. The pulverized product in this hopper 12 is fed to the jet mill 4 by a feeder 13,
It is pulverized by a jet of compressed air.

そして排風機17の駆動にょシ輸送管15を通してバッ
グフィルター16に空気輸送され、ここで空気と微粉砕
製品が分離:され、空気が排風a17を経て排気管18
か□ら排気され、微粉砕製品がホッパー19に貯留さ□
れる1、このように被粉砕物を先ず竪型拐砕機1で粉砕
し、次にジェットミル14・で微粉砕するというように
2段に微粉砕処理する設備で・は、空気輸送設備が大が
かシとなり、1.・そ゛の設備費ならび・に運転費が膨
大となるばかシではなく・、保守、点検、整備等に多大
な労力と時間・が費やされるものである。
The air is then transported to the bag filter 16 through the drive transport pipe 15 of the exhaust fan 17, where the air and the finely pulverized product are separated, and the air passes through the exhaust pipe 18 through the exhaust air a17.
It is exhausted from the □, and the finely pulverized product is stored in the hopper 19 □
1. In this type of equipment where the material to be crushed is first crushed in the vertical crusher 1 and then finely crushed in the jet mill 14, the pneumatic transportation equipment is very important. Became a Gakashi, 1.・It's not just that the equipment costs and operating costs are huge, but that a huge amount of effort and time is spent on maintenance, inspection, maintenance, etc.

本発明は上記諸事情に鑑みなされたものであり、設備費
ならびに運転費が低床で:、保守:′2点検、整備等も
簡単で、しかも被粉砕物を数ミクロンオーダーの超微粉
に効率良く容蔦に微粉砕するこ□とのできる超微粉砕機
を提襖せん表するものである。・   :    1□
   □ □以下本発明による超微粉砕機の一実施例を
第2図乃至第5図によって説明すると、20は円筒状の
回転子で、軸受21.□22によって、1−i2aに回
転可能に支持された垂直回転軸24′61部に支持され
ている。との回転子′20′の列側表面にはその母線(
C沿って多数の6部ツ5′が藤けられて凹凸面が形成さ
れている。自転−Fh□0′の上端板26上の外貢部て
は遠心羽根27が設けられ、□その1上備に第Y砕室デ
ィスク28が設けられ、回転子20の下端板29の下面
には攪拌羽根3’0が設けられている。31は前記回転
子20′とあ間に一定間隙:32を存して嵌装した固定
子であって、その内側表面には母線に沿っ□て多数の凸
部33が設けられて凹凸面が形成されている。
The present invention has been developed in view of the above circumstances, and has low equipment costs and operating costs, easy maintenance, easy inspection and maintenance, and is efficient in converting materials to be crushed into ultra-fine powder on the order of several microns. This article represents an ultra-fine grinder that can finely grind particles into fine particles.・ : 1□
□ □Hereinafter, one embodiment of the ultrafine crusher according to the present invention will be described with reference to FIGS. 2 to 5. Reference numeral 20 represents a cylindrical rotor, and bearing 21. □22 is supported by a vertical rotating shaft 24'61 which is rotatably supported by 1-i2a. The row side surface of the rotor '20' has its generatrix (
A large number of six parts 5' are carved along C to form an uneven surface. A centrifugal blade 27 is provided on the outer part of the upper end plate 26 of the rotation-Fh A stirring blade 3'0 is provided. Reference numeral 31 denotes a stator that is fitted with a certain gap 32 between the rotor 20' and the stator, and the inner surface of the stator is provided with a large number of convex portions 33 along the generatrix line to form an uneven surface. It is formed.

固定子31の上端には前記遠心羽根27に対応して逆円
錐状ケーシング34が前記粉砕室ディスク28よりも高
く設けられている。逆円錐状ケーシング34の上端には
6個のジェットノズル35を等間隔に接線方向中心寄り
に向けたジェットミル36のジェットリング37が設け
られ、このジェットリング37の上面には中心に製品排
出[]38を有するケーシング上蓋39が設けられて粉
砕室ディスク28との間にジェットミル36の粉砕室4
0が形成されている。ジェットリング37の外周側には
ジェットミル36の環状の圧縮空気分配管4】2か設け
られて、ジェットノズル35と連通されている。42は
圧縮空気分配管41の圧縮空気入10である。前記固定
−0r−31の下端に連なる逆円錐状の下部ケーシング
43は攪拌羽根30を覆うように設けられ、これの下面
に空気導入口兼用の被粉砕物供給[]44が設けられて
いる。そして下部ケーシング43は攪拌羽根30の回転
によって起る気流によって、祖粉砕物供給口44か供給
されだ被粉砕物を回転子20と固定子31との間の間隙
32に入れる為の風箱の役割を果だずようになっている
。45は垂直回転軸24の下端に固着さ′iまたプーリ
、46は駆動ベルトであり、この駆動ベルト46は電動
機の回転軸上のプーリ(図示省略)と前記プーリ45に
掛は渡されている。
At the upper end of the stator 31, an inverted conical casing 34 is provided higher than the grinding chamber disk 28, corresponding to the centrifugal blades 27. At the upper end of the inverted conical casing 34, there is provided a jet ring 37 of a jet mill 36, in which six jet nozzles 35 are equally spaced and directed toward the center in the tangential direction. ] A casing upper lid 39 having a diameter of 38 is provided between the grinding chamber disc 28 and the grinding chamber 4 of the jet mill 36.
0 is formed. An annular compressed air distribution pipe 4]2 of the jet mill 36 is provided on the outer peripheral side of the jet ring 37 and communicates with the jet nozzle 35. 42 is a compressed air inlet 10 of the compressed air distribution pipe 41. An inverted conical lower casing 43 connected to the lower end of the fixing-0r-31 is provided so as to cover the stirring blade 30, and a ground material supply [] 44 which also serves as an air inlet is provided on the lower surface of this lower casing 43. The lower casing 43 is operated by the air current generated by the rotation of the agitating blades 30 through the pulverized material supply port 44, which is a wind box for introducing the pulverized material into the gap 32 between the rotor 20 and the stator 31. It has become impossible to fulfill its role. 45 is a pulley fixed to the lower end of the vertical rotating shaft 24, and 46 is a drive belt, which is connected to a pulley (not shown) on the rotating shaft of the electric motor and the pulley 45. .

尚、図示せぬが製品排出口38には、排出管が接続され
、これにバッグフィルターが設けられ、バッグフィルタ
ーに排風機付排気管及びホッパーが接続されるものであ
り、゛またジェットミル36にコンプレッサーが設けら
れるものである。
Although not shown, a discharge pipe is connected to the product discharge port 38, a bag filter is provided to this, and an exhaust pipe with an exhaust fan and a hopper are connected to the bag filter. A compressor is installed in the

次に上記の如く構成さtlだ本発明の超微粉砕機の作用
について説明する。先ず図示せぬ排風機を運転して下部
ケーシング43の下面の被粉砕物供給口44がら空気を
吸入し7、−またジェットミル36に付設のコンプレッ
サーを駆動して圧縮空気”を圧縮空気入口42から環状
の圧縮空気分配管41に入れ、ジェットリング37の6
個のジェットノズル35から噴射し、さらに図示せぬ電
動機を駆動し、駆動ベルト46により回転子20を高速
回転した時の超微粉砕機内の空気流について説明する。
Next, the operation of the ultrafine pulverizer of the present invention constructed as described above will be explained. First, a blower (not shown) is operated to draw in air from the material supply port 44 on the lower surface of the lower casing 43 (7), and a compressor attached to the jet mill 36 is driven to supply compressed air to the compressed air inlet 42. 6 of the jet ring 37.
The air flow inside the ultrafine pulverizer will be described when the rotor 20 is rotated at high speed by the drive belt 46 by injecting air from the jet nozzles 35, driving an electric motor (not shown), and rotating the rotor 20 at high speed.

被粉砕物供給口44から吸入されて機内に垂直に入つf
c空気は、回転子20と一体に高速回転する攪拌羽根3
0により外向き旋回気流となって下部ケーシング43の
逆円錐状の内面に沿って上昇し、回転子20と固定子3
1との間の間隙32内に入る。この間隙32内に入った
気流は回転子20の高速回転により上向きの螺旋気流と
なる。そして遠心羽根27の付近壕で上昇してきた気流
は、高速回転の遠心羽根27によシ更に回転作用を受け
るのであるが、この時その外側に逆円錐状ケーシング3
4を有するので、気流はその逆円錐状ケーシング34の
内面に沿って手刀へ移動しながら外向き旋回気流と′な
り、ジェットリング37の内面即ちノズル面37a壕で
述する。ノズル面37aに開口している6個のジェット
ノズル35からは圧縮空気が噴射され、その噴流方向が
中心向きでしかも前記外向き旋回気流の旋回方向である
。前述のノズル面37aK達しだ外向き旋回気流はその
後ジェット粉砕ゾーン40を通過して製品排出口38か
ら機外へ排気されるが、ジェット粉砕室40を通過する
時、ジェットノズル35からの圧縮空気の高速噴流と合
流する為、ここでは内向き旋回気流となる。
The material to be crushed is sucked from the supply port 44 and enters the machine vertically.
c The air is fed by stirring blades 3 that rotate at high speed together with the rotor 20.
0, the airflow becomes an outward swirling airflow that rises along the inverted conical inner surface of the lower casing 43, and the rotor 20 and stator 3
1 into the gap 32 between the two. The airflow that has entered this gap 32 becomes an upward spiral airflow due to the high speed rotation of the rotor 20. The airflow rising in the trench near the centrifugal vane 27 is further rotated by the high-speed centrifugal vane 27, and at this time an inverted conical casing 3 is placed on the outside of the centrifugal vane 27.
4, the airflow moves along the inner surface of the inverted conical casing 34 and becomes an outward swirling airflow, which will be described at the inner surface of the jet ring 37, that is, the nozzle surface 37a groove. Compressed air is injected from the six jet nozzles 35 that are open to the nozzle surface 37a, and the direction of the jet direction is toward the center and also in the swirling direction of the outward swirling airflow. The outward swirling airflow that has reached the nozzle surface 37aK described above then passes through the jet crushing zone 40 and is exhausted outside the machine from the product discharge port 38, but when passing through the jet crushing chamber 40, the compressed air from the jet nozzle 35 Because it merges with the high-speed jet of air, it becomes an inward swirling airflow.

次にこのような超微粉砕機内の空気流の中に被粉砕物が
供給された場合の粉砕作用について説明する。被粉砕物
供給口44から供給された被粉砕物である粉粒体は攪拌
羽根30の高速回転によって発生した外向き旋回気流に
乗って下部ケーシング43の逆円錐状の内面に沿って上
昇し、回転子20と固定子31との間の間隙32内に入
る。この間隙32内に入った被粉砕物は高速回転してい
る回転子200回転力によって速度エネルギが与えられ
て固定子31に衝突し、粉砕され且つ回転子20の凸部
25と固定子31の凸部33との間で摩砕作用を受けて
更に細かく粉砕されながら、回転子20や高速回転朽よ
シ発生した上向、き蝉旋気流に*つて上方に運はれる。
Next, a description will be given of the pulverizing action when the material to be pulverized is supplied into the air flow inside such a superfine pulverizer. The granular material, which is the material to be crushed, supplied from the material supply port 44 rises along the inverted conical inner surface of the lower casing 43 on the outward swirling airflow generated by the high-speed rotation of the stirring blades 30. It enters the gap 32 between the rotor 20 and the stator 31. The object to be crushed that has entered this gap 32 is given velocity energy by the rotational force of the rotor 200 rotating at high speed, collides with the stator 31, is crushed, and is crushed between the protrusions 25 of the rotor 20 and the stator 31. It is subjected to a grinding action between the convex portion 33 and is further pulverized into fine pieces, and is carried upward by the rotor 20 and the upward whirling air current generated by the high-speed rotation.

そして間隙孕2内よシ出た微粉は、遠心羽根27の高速
[g]転によ如逆円錐状ケーシング34の内面に沿う外
向き旋回気流に乗ってジェットリング37の内面即ちノ
ズル面37aまで運、ばれ、ノズル面37aに沿って回
転する間に6個のジェットノズル35からの圧縮空気の
噴射によシ強い@撃、摩擦を受けて微粉砕さ、れ、この
微粉砕製品がジェットノズル35かラノ圧縮突気の噴射
により生じた内向き旋回気流に乗ってジェット粉砕室4
0の中心部に運ばれ、製品排出口38がら空気流と共に
排出され、図示せぬ排出管を通ってパックフィルタ〒に
空気輸送され、ここで空気と微粉砕製品に分離され、空
気は排風機を経て排気管から排気され、微粉砕製品はホ
ッパーに貯留される。
Then, the fine powder coming out of the gap 2 rides on the outward swirling airflow along the inner surface of the inverted conical casing 34 due to the high speed [g] rotation of the centrifugal blade 27, and reaches the inner surface of the jet ring 37, that is, the nozzle surface 37a. During the rotation along the nozzle surface 37a, the compressed air jets from the six jet nozzles 35 apply strong blows and friction to pulverize the product, and this pulverized product becomes the jet nozzle. Jet crushing chamber 4 rides on the inward swirling airflow generated by the injection of 35 or Rano compressed air.
The product is transported to the center of the product discharge port 38 along with the air flow, and is air-transported through a discharge pipe (not shown) to the pack filter 〒, where it is separated into air and pulverized product, and the air is passed through an exhaust fan. The pulverized product is then exhausted from the exhaust pipe and stored in a hopper.

このように本発明の超微粉砕機は、回転子20と固定子
31との間の環状の間隙32内で被粉砕物を粉砕した後
、遠心羽根27の高速回転により逆円錐状ケーシング3
4に沿う外向き旋回気流に乗せてノズル面37aiで運
び、ジェット粉砕室′40内でジェットミル36にて微
粉砕するので、そのジェット粉砕には次のようガ特長が
ある3、即ち、  、 、      ・1)ジ」−ッ
トミル36に供給される被粉砕物で□ある微粉は、環状
間隙32内で粉砕作用を受□けて粒子が細かいので、ジ
ェットミル36の粉砕能力が高く、従って同一原料供給
量(”4)に対して噴出空振量が少なくて済み、コンプ
レッサーは容量の小さいもので良い。
In this way, the ultrafine pulverizer of the present invention pulverizes the material to be pulverized within the annular gap 32 between the rotor 20 and the stator 31, and then crushes the inverted conical casing 3 by high-speed rotation of the centrifugal blades 27.
The jet pulverization has the following features:・1) Since the fine powder that is the material to be crushed that is supplied to the jet mill 36 is subjected to the crushing action in the annular gap 32 and has fine particles, the crushing capacity of the jet mill 36 is high, and therefore the same The amount of air blowing is small compared to the amount of raw material supplied (4), and the compressor can have a small capacity.

2)逆円錐状ケーシング34に沿う外向き旋回気流に乗
って微粉がノズル面378全体に均一・に供給されるの
で、6個のジェットノズル35の粉砕負荷が均等化する
2) Since the fine powder is uniformly supplied to the entire nozzle surface 378 on the outward swirling airflow along the inverted conical casing 34, the crushing load of the six jet nozzles 35 is equalized.

3)微粉の供給される位置が、高速噴流のジェットノズ
ル35から、の出口部近辺であるので、ジェット粉砕の
効果が最も高い。  □4)供給された微粉がノズル面
37aに沿って旋回気流と共に回転するので、全ての供
給さ・れた微粉は、短時間の内にジェット粉砕の作用を
受けることになる。
3) Since the position where the fine powder is supplied is near the outlet of the high-speed jet nozzle 35, the effect of jet pulverization is the highest. □4) Since the supplied fine powder rotates along the nozzle surface 37a with the swirling airflow, all the supplied fine powder is subjected to the action of jet pulverization within a short time.

以上の説明で判るように本発明の超微粉砕機  −によ
れば、被粉砕物を高速回転する回転子と固定子との間の
環状空隙内で粉砕し、引き続きその微粉を外向き旋回気
流によって上部のジェットミルのノズル面まで運び、最
適条件で微粉をジェット粉砕できるので、数ミクロンオ
ータ、−の超微粉を効率良く容易に得ることができる。
As can be seen from the above description, according to the ultrafine pulverizer of the present invention, the material to be pulverized is pulverized in the annular gap between the rotor and the stator, which rotate at high speed, and the fine powder is then transferred to the outward swirling air stream. Since the fine powder can be transported to the nozzle surface of the upper jet mill and jet-pulverized under optimal conditions, ultrafine powder of several microns in size can be obtained efficiently and easily.

まだ本発明の超微粉砕機は1.竪製粉砕機とジェットミ
ルとを別置きとし、その間を空気輸送設備等で結合した
従来の微粉砕処理設備に比べ、保守2点検、整備が容易
であシ、且つ設備費が安価である。さら、に本発明の超
微粉砕機はその機内のジェットミルのコンブ、レッサー
容量が従来の微粉砕処理設備に於けるジェットミルのコ
ンプレッサー容量よりも小さくて良く、シかも空気輸送
設備は製品取出しの排出管、バッグフィルター、排風機
、夾ツバ−の各−基だけであるので、電気代等の運転費
は従来の微粉砕処理設備に比べ著しく低減できる等の優
れた効果がある。
The ultrafine grinder of the present invention still has 1. Compared to conventional fine pulverization processing equipment in which a vertical pulverizer and a jet mill are installed separately and connected by pneumatic transportation equipment or the like, maintenance, inspection and maintenance are easier, and equipment costs are lower. Furthermore, the ultra-fine pulverizer of the present invention has a jet mill with a smaller compressor capacity than the compressor capacity of the jet mill in conventional pulverization processing equipment, and the pneumatic conveying equipment may not be able to take out the product. Since only a discharge pipe, a bag filter, an exhaust fan, and a catcher are required, operating costs such as electricity costs can be significantly reduced compared to conventional pulverization equipment.

1、図面の簡単な説明        □笥1図は竪型
粉砕機とジェットミルを別置きして空気輸送設備等で結
合して成る従来の微粉砕設備を示す概略図、第2図は本
発明による超微粉砕機の一実施例を示す縦断面図、□1
3図は第、2図のA−A線横断面図、第4図は第2図の
B−BAI横断面図、第5図は絹2図のc−c線横断面
図である。         ′   □・20・・・
円筒状の回転子 24・・・垂直回転軸  25・・・
凸 部  26・・・上端板27・・・遠心羽根′ 2
8・・・粉砕1テイスク2゛9・・・下端板  3o・
・・攪拌弱視31・・・固定子  32′・・・間@ 
 33・・・凸部  34・・・逆円錐状ケーシング3
5 ・・・ジェットノズル  36・・・ジェットミル
37・・・ジェットリング  38・・・製品排出凸3
9・・・ケーシング上蓋  4o・・□・ジェットミル
の粉砕室  43・・・下部ケーシング□44・・・空
気導入口兼用の被粉砕物供給口式 理 人  弁理士 
高  雄次部 第2図 3日 第3図 111 第4図 第5図
1. Brief explanation of the drawings □Figure 1 is a schematic diagram showing a conventional pulverization equipment consisting of a vertical pulverizer and a jet mill installed separately and connected by pneumatic conveyance equipment, etc. Figure 2 is a schematic diagram showing a conventional pulverization equipment according to the present invention. Vertical cross-sectional view showing an example of an ultrafine pulverizer, □1
3 is a cross-sectional view taken along line A--A of FIG. 2, FIG. 4 is a cross-sectional view taken along line B-BAI of FIG. 2, and FIG. ' □・20...
Cylindrical rotor 24... Vertical rotation axis 25...
Convex portion 26... Upper end plate 27... Centrifugal blade' 2
8...Crushing 1 take 2゛9...Lower end plate 3o.
... Stirring amblyopia 31 ... Stator 32' ... Between @
33...Convex portion 34...Inverted conical casing 3
5...Jet nozzle 36...Jet mill 37...Jet ring 38...Product discharge convex 3
9...Casing upper lid 4o...□-Crushing chamber of jet mill 43...Lower casing □44...Crushed material supply port that also serves as air intake port Attorney Patent attorney
Taka Yujibe Figure 2 3rd Figure 3 111 Figure 4 Figure 5

Claims (1)

【特許請求の範囲】[Claims] 垂直回転軸に支持され外側表面の母線に沿って多数の凸
部を有する円筒状の回転子と、該回転子との間に一定間
隙を存して嵌装され内側表面の母線に沿って多数の凸部
を有する固定子との間で被粉砕物を粉砕する竪型粉砕機
に於いて、前記回転子の上端板外周に遠心羽根を設は且
つその上端に粉砕室ディスクを設け、前記遠心羽根に対
応して固定子の上端に前記粉砕室ディスクよりも高く逆
円錐状ケーシングを設け、この逆円錐状ケーシングの上
端に接線方向中心寄りにジェットノズルを複数個等間隔
に向けた環状のジェットミルを設け、このジェットミル
の上側に中心に製品排出口を有するケーシング上蓋を設
けて前記粉砕室ディスクとの間にジェットミルの粉砕室
を形成し、回転子の下端板に攪拌羽根を設け、固定子の
下端に連なる下部ケーシングに空気導入口兼用の被粉砕
物供給口を設けたこと4特徴とする超微粉砕機。
A cylindrical rotor supported by a vertical rotating shaft and having a large number of protrusions along the generatrix of the outer surface; In a vertical crusher that crushes a material to be crushed between a stator and a stator having a convex portion, a centrifugal blade is provided on the outer periphery of the upper end plate of the rotor, and a crushing chamber disk is provided at the upper end of the rotor. An inverted conical casing is provided at the upper end of the stator corresponding to the blades, higher than the grinding chamber disk, and a plurality of annular jets are provided at the upper end of the inverted conical casing with jet nozzles oriented tangentially toward the center at equal intervals. a mill is provided, a casing top lid having a product discharge port in the center is provided above the jet mill to form a grinding chamber of the jet mill between the grinding chamber disk, and stirring blades are provided on the lower end plate of the rotor; An ultrafine pulverizer characterized by four features: a lower casing connected to the lower end of the stator is provided with a material supply port that also serves as an air introduction port.
JP17575182A 1982-10-06 1982-10-06 Ultra-finely crushing machine Granted JPS5966362A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17575182A JPS5966362A (en) 1982-10-06 1982-10-06 Ultra-finely crushing machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17575182A JPS5966362A (en) 1982-10-06 1982-10-06 Ultra-finely crushing machine

Publications (2)

Publication Number Publication Date
JPS5966362A true JPS5966362A (en) 1984-04-14
JPS6136457B2 JPS6136457B2 (en) 1986-08-19

Family

ID=16001611

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17575182A Granted JPS5966362A (en) 1982-10-06 1982-10-06 Ultra-finely crushing machine

Country Status (1)

Country Link
JP (1) JPS5966362A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60178128U (en) * 1984-05-07 1985-11-26 株式会社ケンウッド Magnetic shield decorative sheet

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60178128U (en) * 1984-05-07 1985-11-26 株式会社ケンウッド Magnetic shield decorative sheet

Also Published As

Publication number Publication date
JPS6136457B2 (en) 1986-08-19

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