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JPS648574B2 - - Google Patents
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JPS648574B2 - - Google Patents

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Publication number
JPS648574B2
JPS648574B2 JP20174582A JP20174582A JPS648574B2 JP S648574 B2 JPS648574 B2 JP S648574B2 JP 20174582 A JP20174582 A JP 20174582A JP 20174582 A JP20174582 A JP 20174582A JP S648574 B2 JPS648574 B2 JP S648574B2
Authority
JP
Japan
Prior art keywords
classification
impeller
pipe
crushing
injection pipe
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.)
Expired
Application number
JP20174582A
Other languages
Japanese (ja)
Other versions
JPS5992041A (en
Inventor
Seizaburo Akyama
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.)
Hosokawa Micron Corp
Original Assignee
Hosokawa Micron Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hosokawa Micron Corp filed Critical Hosokawa Micron Corp
Priority to JP20174582A priority Critical patent/JPS5992041A/en
Publication of JPS5992041A publication Critical patent/JPS5992041A/en
Publication of JPS648574B2 publication Critical patent/JPS648574B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は粉粒体の粉砕と分級を連続的に行なわ
せる粉砕分級装置に関するものであり、詳しくは
ジエツトミル式の粉砕部と回転分級羽根車を具備
する分級部とをコンパクトに、かつ効果的に結合
させてよりすぐれた粉砕分級性能を持つ装置を提
供するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a crushing and classifying device that continuously crushes and classifies powder and granules, and more specifically, it includes a jet mill-type crushing section and a classifying section equipped with a rotating classification impeller. The purpose of the present invention is to provide a device that is compact and effectively combined and has superior pulverization and classification performance.

従来、ジエツトミル式の粉砕機構を有する粉砕
分級装置においては、粉砕部と分級部とが別個
に、しかも幾分、離されて設けられていた。これ
は、粉砕部及び分級部における互いの作用面での
干渉を抑え、両機構部の持つ性能を確保する上で
必要であるものの、粉砕部と分級部間の距離が長
くなることは装置自体を大型化させ、かつ、移送
に伴い動力面での増大を来たすものである。ま
た、該装置での粉砕及び分級の性能を発揮させる
ためには、粉砕部及び分級部における粉粒体原料
(以下単に原料と云う)の滞留量や導入空気量等
に対してそれぞれに微妙な調整を必要とし、か
つ、両部内をバランスさせて初めて所望の性能が
得られるわけである。たとえば、第1図はその一
例で、上方に分級部bを、下方に粉砕部aを配設
させ、粉砕部aにおいて粉砕された原料を空気流
により分級部bに送つて分級選別し、製品として
の微粉は分級羽根車c内を通過させて排出、捕集
させ、他方、粗粉は再度前記粉砕部aに循環させ
て粉砕するように構成された装置である。しか
し、こうした装置においては、次第に機内での滞
留量が増え、原料濃度が高くなるに連れて粉砕、
分級の両効果が低下し、又、新規原料の供給量も
減少して当初の性能の確保が困難となり易いもの
であつた。つまり、こうした機内における多量な
原料の滞留は、粉砕部aにおける粉砕効果の低
減、分級部bにおける処理量及び空気量の変動に
伴う分級精度の低下などにより処理能力の減少を
余儀無くされ、又、動力損失の増大からも改良の
必要があつた。本発明はこうした点に鑑み、粉砕
部と分級部とを簡潔、かつ効果的に結合し構成さ
せることによつて良好な粉砕、分級性能に所要動
力の低減を併わせ持つた粉砕分級装置を提供する
ものである。即ち、縦型円筒状の機胴内に上方中
心より排気管を挿設し、下端に仕切盤を具備させ
て境とし、上部には原料噴射管と該噴射管に対向
させて衝突部材を配設し、下部には仕切盤に接近
させて分級羽根車と該分級羽根車に対応する外周
壁面全周に多数の微細な流入口を具備させるほ
か、下方粗粉排出口と前記噴射管とを接続管を以
つて連通させて構成したものである。以下、本発
明を実施例により説明する。
Conventionally, in a crushing and classifying apparatus having a jet mill type crushing mechanism, a crushing section and a classifying section have been provided separately and somewhat separated from each other. Although this is necessary to suppress interference between the working surfaces of the crushing section and the classifying section and to ensure the performance of both mechanical sections, the longer distance between the crushing section and the classifying section does not affect the equipment itself. This increases the size of the equipment and increases the power required to transport it. In addition, in order to maximize the crushing and classification performance of this equipment, subtle changes must be made to the amount of granular raw material (hereinafter simply referred to as raw material) retained in the crushing section and the classification section, the amount of air introduced, etc. Adjustment is required, and the desired performance can only be achieved by balancing both parts. For example, Fig. 1 shows an example in which a classifying section b is arranged above and a crushing section a is arranged below, and the raw material crushed in the crushing section a is sent to the classifying section b by an air flow to be classified and sorted. This device is configured so that the fine powder is passed through the classification impeller c to be discharged and collected, while the coarse powder is circulated to the crushing section a again and crushed. However, in these devices, the amount of stagnation inside the machine gradually increases, and as the concentration of raw materials increases, the grinding and
Both the effects of classification were reduced, and the amount of new raw materials supplied was also reduced, making it difficult to maintain the original performance. In other words, the accumulation of a large amount of raw material in the machine inevitably reduces the processing capacity due to a reduction in the crushing effect in the crushing section a, a decrease in classification accuracy due to fluctuations in the throughput and air amount in the classifying section b, etc. Improvements were also needed due to increased power loss. In view of these points, the present invention provides a pulverizing and classifying device that combines a pulverizing and classifying performance with good pulverizing and classifying performance while reducing the required power by simply and effectively combining and configuring a pulverizing section and a classifying section. It is something to do. That is, an exhaust pipe is inserted into the vertical cylindrical fuselage from the center above, a partition board is provided at the lower end to form a boundary, and a raw material injection pipe and a collision member are arranged opposite to the injection pipe at the upper part. The lower portion is provided with a classification impeller close to the partition panel and a large number of fine inlets all around the outer peripheral wall corresponding to the classification impeller, and a lower coarse powder discharge port and the injection pipe are provided. It is constructed by communicating with each other using a connecting pipe. The present invention will be explained below with reference to Examples.

第2図及至第4図において、縦型円筒状の機胴
1は上方中心より排気管6を挿設させて排気口7
を上部に配置し、側面部には空気導入口10を、
下方には粗粉排出口9を具備し、かつ電動機18
と下部で連結されて架台20上に載置させてい
る。機胴1内には前記電動機18に連結され多数
の分級羽根4を放射状に配列させて構成させた分
級羽根車3と、該分級羽根車3の上部に接近させ
て仕切盤5が配設されている。該仕切盤5は中心
部を排気管6によつて支持され、前記排気口7と
分級羽根車3内とを連通させて設けられるほか、
分級羽根車3よりも幾分大径で、その外周縁部5
aを下方に曲折させ分級羽根車3を上端より覆う
ようにわずかな隙間を以つて分級羽根4に幾分重
なり合うように構成されている。なお、仕切盤5
に対する分級羽根車3及び分級羽根4の構造や形
状については特に限定されるものではなく、たと
えば、分級羽根車3は上方より下方に連れて次第
に小径となる載頭円錐形状であつてもよく、又、
分級羽根4も放射状配列から第5図のように回転
方向下手側に適度にずらせることにより羽根面を
傾斜させて配列してもよい。そして、該仕切板5
を境として上方側の壁面2には圧力空気の噴射管
12を衝突部材13と適当な間隔を以つて対応さ
せて配置している。該噴射管12には仕切弁22
を介し原料ホツパ8と、図示省略の圧力空気源と
してのコンプレツサとが接続される。他方、下方
側の壁面2には全周に亘つて分級羽根4とほぼ等
しい長さを持ち、多数のスリツト状の流入口15
を有する整流部材14を配設させ、その外周囲に
は空気室11を設けて空気導入口10に連通させ
ている。該流入口15の構成については、本実施
例ではリングの中心に対し適度な傾斜角θを以つ
て順次微細な多数の切欠きdを入れることによつ
てスリツト状の流入口15を持つ整流部材14を
構成させているが、第6図に示すように多数の板
状の整流板14aを所定の間隔毎に順次配列させ
ることによつて流入口15aを構成させるほか、
該整流板14aを可動式とし流入口15aの傾斜
角度θを任意に調節可能としてもよく、さらには
整流部材14として適度な開口を持つた多孔板を
用いてもよい。また、前記噴射管12に対しても
衝突部材13に噴射流を衝突させ、衝突後の噴射
流に旋回成分を与えるべく衝突部材13を適度に
傾斜させるほか、噴射管12自体の取付け向きを
適度に変えてもよい。次に壁面2下方には前記の
粗粉排出口9が設けられ、排出管17がこれに接
続されるが、粗粉排出口9に対しては第7図に示
すような案内部材21を旋回方向の下流側縁部に
付設させてもよい。そして、排出管17の一部に
は接続管16を前記噴射管12に連通させるべく
取付けており、又、その経路には調節弁23が具
備されている。なお、前記衝突部材13の形状及
び取付位置は特に限定されるものではなく、たと
えば第8図に示すようなリング状のものであつて
もよく、回転移動させることにより逐次衝突面の
位置を替えることができ、磨耗に対して有効であ
り、長期間の使用にも適応可能である。そして、
排気口7にはサイクロンやバツグフイルター等の
図示省略の捕集器が、排出管17にはロータリバ
ルブ等の排出機が接続される。また、本実施例で
は分級羽根車3を直接電動機18に取付け、回転
数の変更にはインバータ19を組み込んで周波数
変換方式による構成とされており、これによつて
動力の伝達部を簡略化することができる。
2 to 4, a vertical cylindrical fuselage 1 has an exhaust pipe 6 inserted from the center above and an exhaust port 7.
is placed on the top, and an air inlet 10 is placed on the side.
A coarse powder discharge port 9 is provided at the bottom, and an electric motor 18 is provided.
It is connected at the lower part and placed on a pedestal 20. Inside the machine body 1, a classification impeller 3 is connected to the electric motor 18 and is configured by arranging a large number of classification blades 4 in a radial manner, and a partition plate 5 is disposed close to the top of the classification impeller 3. ing. The partition board 5 is supported at its center by an exhaust pipe 6, and is provided so that the exhaust port 7 and the inside of the classification impeller 3 are communicated with each other.
It has a somewhat larger diameter than the classification impeller 3, and its outer peripheral edge 5
a is bent downward so as to overlap the classification impeller 4 with a slight gap so as to cover the classification impeller 3 from the upper end. In addition, the partition board 5
The structure and shape of the classification impeller 3 and the classification blades 4 are not particularly limited. For example, the classification impeller 3 may have a truncated conical shape whose diameter gradually decreases from the top to the bottom. or,
The classification blades 4 may also be arranged with the blade surfaces inclined by appropriately shifting the classification blades 4 from the radial arrangement toward the downstream side in the rotational direction as shown in FIG. And the partition plate 5
A pressurized air injection pipe 12 is disposed on the wall surface 2 on the upper side of the collision member 13 in correspondence with a collision member 13 at an appropriate distance. A gate valve 22 is provided in the injection pipe 12.
The raw material hopper 8 is connected to a compressor as a pressure air source (not shown) via the hopper 8. On the other hand, the lower wall surface 2 has a number of slit-shaped inlets 15 that have approximately the same length as the classification blades 4 over the entire circumference.
An air chamber 11 is provided around the outer periphery of the rectifying member 14, which communicates with the air inlet 10. Regarding the configuration of the inlet 15, in this embodiment, a flow regulating member having a slit-shaped inlet 15 is created by sequentially inserting a large number of fine notches d at an appropriate inclination angle θ with respect to the center of the ring. However, as shown in FIG. 6, the inlet 15a is constructed by sequentially arranging a large number of plate-shaped current plates 14a at predetermined intervals.
The rectifying plate 14a may be movable so that the inclination angle θ of the inlet 15a can be arbitrarily adjusted.Furthermore, a perforated plate having appropriate openings may be used as the rectifying member 14. In addition, the collision member 13 is made to collide with the jet flow against the jet pipe 12, and the collision member 13 is appropriately inclined to give a swirling component to the jet flow after the collision, and the mounting direction of the jet pipe 12 itself is adjusted appropriately. You may change it to Next, the above-mentioned coarse powder discharge port 9 is provided below the wall surface 2, and the discharge pipe 17 is connected to this. It may be attached to the downstream edge of the direction. A connecting pipe 16 is attached to a part of the discharge pipe 17 so as to communicate with the injection pipe 12, and a regulating valve 23 is provided in the path thereof. Note that the shape and mounting position of the collision member 13 are not particularly limited; for example, it may be ring-shaped as shown in FIG. 8, and the position of the collision surface can be sequentially changed by rotationally moving the collision member 13. It is effective against wear and can be used for long periods of time. and,
A collector (not shown) such as a cyclone or a bag filter is connected to the exhaust port 7, and a discharge device such as a rotary valve is connected to the exhaust pipe 17. In addition, in this embodiment, the classification impeller 3 is directly attached to the electric motor 18, and an inverter 19 is incorporated to change the rotation speed, resulting in a frequency conversion system, thereby simplifying the power transmission section. be able to.

以上の構成において、噴射管12より機胴1内
に供給される原料は、圧力空気と共にきわめて高
速度化された噴射流jとなつて噴射、衝突部材1
3に激しく衝突される。この時の衝撃により、
又、噴射管12よりの噴射直後の噴射流j中で発
生する粒子間の衝突や接触による磨砕効果によつ
て粉砕がなされる。この後、原料は噴射流jの持
つ旋回成分により、あるいは分級羽根車3の回転
に伴う旋回気流rにより、粒子同士の接触や衝突
による磨砕衝撃作用を繰り返しつつ壁面2に沿つ
て下降する。こうして、仕切盤5よりも下方に到
り、分級羽根車3による分級選別作用を受ける。
即ち、分級羽根車3の回転に伴う遠心力と、該分
級羽根車3を通過し向心気流eに伴う求心力とを
受け、これら両作用力差によつて分級選別がなさ
れるわけであり、遠心力よりも求心力の影響をよ
り受ける微粉粒子は、流出気流eと共に分級羽根
車3を通過して排気口7より機外に排出、捕集さ
れる。他方、求心力よりも遠心力の方をより受け
る粗粉粒子は、壁面2に押しやられ旋回降下す
る。ところで、分級羽根車3の外周囲の壁面2に
は整流部材14に具備させた多数のスリツト状の
流入口15が設けられており、しかも、該流入口
15よりの気流iは比較的速い速度で流入するこ
ともあつて、壁面2に沿つて旋回降下して来る原
料粒子に対して有効に分散力を付与することとな
り、分級羽根車3による分級選別を促進させるこ
とができる。また、選別され粗粉として壁面2近
くを旋回している粗粉粒子中に混在する付着、あ
るいは凝集した微粉粒子を分離させて再度分級さ
せるため、粗粉中への微粉の混入が防げ、微粉の
回収率を高めることができる。さらに、分級羽根
車3に対する仕切盤5は、分級羽根車3の上端を
覆うようにその外周縁部5aを曲折させ、わずか
な隙間を以つて分級羽根4に幾分重なり合うよう
に構成させているため、当該回転分級羽根車にお
いては、最も洩れ込みの起き易いとされる該分級
羽根車3端部よりの洩れ込みを阻止でき、空気及
び微粉粒子以外のもの、即ち、微粉中への粗粉の
混入を防止し、粗粉及び微粉共に良質な製品が得
られる。このことから、分級羽根車3によるすぐ
れた分級特性を生かして分級羽根車3と、壁面2
及び整流部材14との間隔を狭め、原料粒子に対
してより効果的な分級選別機構により分級処理速
度の向上を計り、機胴1内における原料の滞留を
抑えて安定した分級性能を維持させ、又、当該装
置の小型化を可能とする。ところで、こうして選
別分級され、分級羽根車3を通過されないで残つ
た原料は、粗粉として壁面2下方の粗粉排出口9
より排出管17を経て機外に排出されるが、該排
出管17には、他端を前記の噴射管12に連通さ
せた接続管16が配設されており、噴射管12よ
りの圧力空気の噴出に伴う誘引作用によつて粗粉
粒子の全部、あるいは一部を返送し、再度の粉砕
を行なわせるほか、分級時の原料の分散化を促す
ための媒体として利用させることもできる。
In the above configuration, the raw material supplied into the fuselage 1 from the injection pipe 12 becomes an extremely high-velocity injection flow j together with pressure air, and is injected into the collision member 1.
3 violently collided. Due to the shock at this time,
Further, the particles are pulverized by a grinding effect caused by collisions and contact between particles generated in the jet flow j immediately after injection from the injection pipe 12. Thereafter, the raw material descends along the wall surface 2 due to the swirling component of the jet flow j or due to the swirling airflow r caused by the rotation of the classification impeller 3, while repeating the grinding impact effect due to contact and collision between particles. In this way, it reaches below the partition panel 5 and is subjected to the classification and sorting action by the classification impeller 3.
That is, they receive centrifugal force due to the rotation of the classification impeller 3 and centripetal force associated with the centripetal airflow e passing through the classification impeller 3, and classification and sorting is performed based on the difference between these forces. Fine powder particles, which are more influenced by centripetal force than by centrifugal force, pass through the classification impeller 3 together with the outflow airflow e, and are discharged and collected outside the machine through the exhaust port 7. On the other hand, coarse powder particles that are more affected by centrifugal force than by centripetal force are pushed toward the wall surface 2 and spiral downward. By the way, a large number of slit-shaped inflow ports 15 provided in the flow regulating member 14 are provided on the wall surface 2 around the outer periphery of the classification impeller 3, and the airflow i from the inflow ports 15 has a relatively high velocity. As a result, a dispersion force is effectively applied to the raw material particles whirling down along the wall surface 2, and classification by the classification impeller 3 can be promoted. In addition, since the adhering or agglomerated fine particles mixed in the coarse powder particles that are sorted and swirling near the wall surface 2 as coarse powder are separated and classified again, it is possible to prevent the fine powder from being mixed into the coarse powder, and the fine powder can increase the recovery rate. Further, the partition plate 5 for the classification impeller 3 has its outer peripheral edge 5a bent so as to cover the upper end of the classification impeller 3, and is configured to overlap the classification blade 4 to some extent with a slight gap. Therefore, in the rotary classification impeller, leakage from the 3 ends of the classification impeller, which is said to be the most prone to leakage, can be prevented, and anything other than air and fine powder particles, that is, coarse powder into the fine powder, can be prevented. This prevents the contamination of particles and produces high-quality products for both coarse and fine powders. For this reason, by taking advantage of the excellent classification characteristics of the classification impeller 3, the classification impeller 3 and the wall surface 2
and the rectifying member 14, the classification processing speed is improved by a classification mechanism that is more effective for raw material particles, and retention of raw materials in the machine body 1 is suppressed to maintain stable classification performance. Furthermore, it is possible to downsize the device. By the way, the raw material that has been sorted and classified in this way and remains without passing through the classification impeller 3 is discharged as coarse powder to the coarse powder discharge port 9 below the wall surface 2.
The air is discharged to the outside of the machine via an exhaust pipe 17, and the exhaust pipe 17 is provided with a connecting pipe 16 whose other end communicates with the injection pipe 12. All or part of the coarse powder particles are returned by the attraction effect caused by the ejection of the powder to be pulverized again, and can also be used as a medium to promote the dispersion of raw materials during classification.

以上のように本発明は、 分級羽根車3の上部に排気管6を接近させて
下端に仕切盤5を配設し、 該仕切盤5を境として、上方側には原料ホツ
パ8に接続させた圧力空気の噴射管12と、衝
突部材13とを互いに対向させて配設し、 下方側には、分級羽根車3の外周壁面2に沿
つて全周に多数のスリツト状の流入口15を具
備させ、 壁面2下方に設けられた粗粉排出口9と、前
記噴射管12とを接続管16を以つて連通させ
て構成した粉砕分級装置であり、 加えて、前記仕切盤5の外周縁部5aがわず
かな隙間を以つて分級羽根4に幾分重なり合う
よう下面を凹状に形成させたこと、 により粉砕部と分級部とを適切、かつ、効果的に
結合させることによつて、それぞれの作用工程を
連継させ、それによつて効率よい粉砕分級作用を
可能とし、粉砕分級装置としての性能の向上を計
ることができる。即ち、粉砕部においては粉砕さ
れた微粉粒子はすみやかに、又、充分粉砕されて
いない粗粉粒子も順次排出させて粉砕部内での余
剰な滞留を抑え、常に粉砕部内を粉砕に適した状
態に保持させることによつて効率よい粉砕を安定
して行なわせることができ、しかも、粉砕精度の
向上にも有効である。他方、分級装置として性能
面で大きな要素を示める原料粒子の分散化を強力
に、かつ、繰り返し計ることによつて付着凝集し
た微粉粒子の単粒子化を促進して、分級選別を効
率よく行なわせ、加えて、微粉粒子の粗粉中への
混入を抑えると共に、分級羽根車3に対する前記
仕切盤5の洩れ込み防止構造により、微粉中への
粗粉粒子の混入を防止して粗粉、微粉共に良質な
製品を得ることができる。このように、一枚の仕
切盤5を隔て粉砕部と分級部とを構成し、粉砕部
において粉砕された微粉は速やかに回収させ、未
粉砕の粗粒は、より粉砕効果の大きい噴射管12
と衝突部材13による粉砕工程へと順次循環させ
ることにより、機胴1内への原料の滞留を抑え、
粉砕と分級の両工程において共にすぐれた性能が
得られる。その結果、当該装置の小型化と所要動
力の低減を可能とするものである。
As described above, in the present invention, the exhaust pipe 6 is brought close to the upper part of the classification impeller 3, the partition board 5 is arranged at the lower end, and the upper side of the partition board 5 is connected to the raw material hopper 8. A jet pipe 12 of pressurized air and a collision member 13 are arranged to face each other, and a large number of slit-shaped inlets 15 are provided along the entire circumference of the outer peripheral wall surface 2 of the classification impeller 3 on the lower side. This is a crushing and classifying device configured by connecting a coarse powder discharge port 9 provided below the wall surface 2 and the injection pipe 12 through a connecting pipe 16; By forming the lower surface into a concave shape so that the portion 5a overlaps the classification blade 4 with a slight gap, the crushing portion and the classification portion are appropriately and effectively connected. By repeating the action steps, it is possible to perform efficient crushing and classifying operations, thereby improving the performance of the crushing and classifying device. In other words, in the crushing section, fine powder particles that have been crushed are quickly discharged, and coarse particles that have not been sufficiently crushed are also sequentially discharged to prevent excess accumulation in the crushing section, and the inside of the crushing section is always kept in a state suitable for crushing. By holding it, efficient pulverization can be carried out stably, and it is also effective in improving the pulverization accuracy. On the other hand, by strongly dispersing the raw material particles, which is a major factor in terms of performance as a classification device, and by repeatedly measuring, it promotes the formation of adhered and agglomerated fine powder particles into single particles, making classification and sorting more efficient. In addition, the mixing of fine powder particles into the coarse powder is suppressed, and the leakage prevention structure of the partition plate 5 with respect to the classification impeller 3 prevents the mixing of coarse powder particles into the fine powder. Both fine powder and fine powder can be obtained. In this way, the crushing section and the classification section are separated by a single partition plate 5, and the fine powder crushed in the crushing section is quickly recovered, and the unpulverized coarse particles are transferred to the injection pipe 12, which has a greater crushing effect.
By sequentially circulating the material through the crushing process using the collision member 13, the retention of the raw material in the machine body 1 is suppressed,
Excellent performance can be obtained in both the grinding and classification processes. As a result, it is possible to downsize the device and reduce the required power.

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

第1図は従来例の概略図、第2図は本発明を示
す実施例の要部断面図、第3図は第2図A―
A′断面視図、第4図は整流部材14の斜視図、
第5図及至第8図は他の実施例を示す。 図において、1……機胴、2……壁面、3……
分級羽根車、4……分級羽根、5……仕切盤、5
a……外周縁部、6……排気管、8……原料ホツ
パ、9……粗粉排出口、12……噴射管、13…
…衝突部材、14……整流部材、15,15a…
…流入口、16……接続管である。
Fig. 1 is a schematic diagram of a conventional example, Fig. 2 is a sectional view of essential parts of an embodiment showing the present invention, and Fig. 3 is Fig. 2A-
A′ sectional view, FIG. 4 is a perspective view of the rectifying member 14,
5 to 8 show other embodiments. In the figure, 1... fuselage, 2... wall surface, 3...
Classifying impeller, 4... Classifying impeller, 5... Partition plate, 5
a... Outer peripheral edge, 6... Exhaust pipe, 8... Raw material hopper, 9... Coarse powder discharge port, 12... Injection pipe, 13...
... Collision member, 14... Rectifying member, 15, 15a...
...Inflow port, 16... Connection pipe.

Claims (1)

【特許請求の範囲】 1 縦型円筒状の機胴1内に上方中心より排気管
6を挿設し、下端に仕切盤5を具備させて境と
し、上部には原料噴射管12と該噴射管12に対
向させて衝突部材13を配設し、下部には仕切盤
5に接近させて分級羽根車3と該分級羽根車3に
対応する外周壁面2全周に多数の微細な流入口1
5を具備させるほか、下方粗粉排出口9と前記噴
射管12とを接続管16を以つて連通させたこと
を特徴とする粉砕分級装置。 2 前記仕切盤5は分級羽根車3よりも大径で、
その外周縁部5aがわずかな隙間を以つて分級羽
根4に幾分重なり合うよう下面を凹状に形成させ
た前記第1項記載の粉砕分級装置。
[Claims] 1. An exhaust pipe 6 is inserted into the vertical cylindrical fuselage 1 from the center above, a partition plate 5 is provided at the lower end to define the boundary, and a raw material injection pipe 12 and the injection pipe are provided at the upper part. A collision member 13 is disposed facing the pipe 12, and a classification impeller 3 and a large number of fine inflow ports 1 are provided on the entire circumference of the outer peripheral wall surface 2 corresponding to the classification impeller 3 at the bottom close to the partition panel 5.
5, and the lower coarse powder discharge port 9 and the injection pipe 12 are communicated with each other through a connecting pipe 16. 2. The partition plate 5 has a larger diameter than the classification impeller 3,
The crushing and classifying device according to item 1 above, wherein the lower surface is formed in a concave shape so that the outer peripheral edge portion 5a overlaps the classification blade 4 somewhat with a slight gap.
JP20174582A 1982-11-17 1982-11-17 Grinding and classifying apparatus Granted JPS5992041A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20174582A JPS5992041A (en) 1982-11-17 1982-11-17 Grinding and classifying apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20174582A JPS5992041A (en) 1982-11-17 1982-11-17 Grinding and classifying apparatus

Publications (2)

Publication Number Publication Date
JPS5992041A JPS5992041A (en) 1984-05-28
JPS648574B2 true JPS648574B2 (en) 1989-02-14

Family

ID=16446234

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20174582A Granted JPS5992041A (en) 1982-11-17 1982-11-17 Grinding and classifying apparatus

Country Status (1)

Country Link
JP (1) JPS5992041A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6549062B2 (en) * 2016-05-10 2019-07-24 ラサ工業株式会社 Vertical mill

Also Published As

Publication number Publication date
JPS5992041A (en) 1984-05-28

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