JPS6316979B2 - - Google Patents

Info

Publication number
JPS6316979B2
JPS6316979B2 JP16049780A JP16049780A JPS6316979B2 JP S6316979 B2 JPS6316979 B2 JP S6316979B2 JP 16049780 A JP16049780 A JP 16049780A JP 16049780 A JP16049780 A JP 16049780A JP S6316979 B2 JPS6316979 B2 JP S6316979B2
Authority
JP
Japan
Prior art keywords
injection nozzle
wall surface
collision
collision member
crushing
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
JP16049780A
Other languages
Japanese (ja)
Other versions
JPS5784756A (en
Inventor
Kyoshi Urayama
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 MIKURON KK
Original Assignee
HOSOKAWA MIKURON 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 HOSOKAWA MIKURON KK filed Critical HOSOKAWA MIKURON KK
Priority to JP16049780A priority Critical patent/JPS5784756A/en
Priority to GB8133898A priority patent/GB2091127B/en
Priority to CA000389860A priority patent/CA1181052A/en
Priority to FR8121302A priority patent/FR2493730B1/en
Priority to DE19813145209 priority patent/DE3145209A1/en
Publication of JPS5784756A publication Critical patent/JPS5784756A/en
Priority to US06/545,101 priority patent/US4451005A/en
Publication of JPS6316979B2 publication Critical patent/JPS6316979B2/ja
Granted legal-status Critical Current

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  • Disintegrating Or Milling (AREA)

Description

【発明の詳細な説明】 本発明は空気流式の粉砕機に係り、単一の粉砕
室内において粉砕と同時に旋回気流によつて分級
する旋回流型粉砕機に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an air flow type pulverizer, and more particularly, to a swirl flow type pulverizer that performs pulverization and classification using a swirling air flow in a single pulverization chamber.

流体エネルギーを利用して粉粒体を粉砕する粉
砕機は超微粉砕用として知られ、利用されてい
る。また反面、該粉砕機は所要動力に対する粉砕
能力の低さの面においてもよく知られており、如
何に粉砕の効率を上げるかが問題であつた。また
所望の製品量を得るためには粉砕装置としては該
粉砕機の低い粉砕能力を補わせるべく分級機との
連結を行わせるため、きわめて大型化する傾向が
あつた。
A pulverizer that uses fluid energy to pulverize granular material is known and used for ultrafine pulverization. On the other hand, this pulverizer is also well known for its low pulverizing capacity relative to the required power, and the problem has been how to improve the pulverizing efficiency. In addition, in order to obtain the desired amount of product, the crushing equipment tends to be extremely large in size because it must be connected to a classifier to compensate for the low crushing capacity of the crusher.

本発明はこうした点に鑑み、第一に粉砕効率を
向上させ、よつてこれに伴う粉砕装置自体の小型
化、および運転経費の減少を目的とするものであ
る。
In view of these points, the present invention aims first to improve the pulverization efficiency, thereby downsizing the pulverizer itself and reducing operating costs.

そして、その構成は中心部に微粉排出口を、内
周壁面に粉粒体材料(以下単に材料という)を圧
力空気と共に噴射させる噴射ノズルを具備してな
る旋回型の空気流式粉砕機であつて、該噴射ノズ
ルに対応し、かつ内周壁面と適当な間隔位置に配
設された衝突部材の衝突面を外周方向に傾斜させ
るほか、内周壁面の一部に開孔を穿設し、該開孔
と前記噴射ノズルとを連通させる経路を構成させ
てなるものである。
The configuration is a rotating air flow type crusher, which is equipped with a fine powder outlet in the center and an injection nozzle on the inner peripheral wall that injects powder and granular material (hereinafter simply referred to as material) together with pressurized air. The collision surface of the collision member, which corresponds to the injection nozzle and is disposed at an appropriate distance from the inner peripheral wall surface, is inclined in the outer peripheral direction, and an opening is formed in a part of the inner peripheral wall surface, A path is configured to communicate the opening and the injection nozzle.

以下に本発明を実施例によつて説明する。第1
図乃至第3図において、粉砕機1のケーシング3
は中心上部に微粉排出口7を有する上部円板4
と、中心部に円錐状の整流部材8を上向きに具備
した下部円板5と、半球状、あるいはU字状の断
面を形成する内周壁面4とによつて粉砕室2を構
成している。一方該粉砕室2内においては、噴射
ノズル10が内周壁面4に対し、内周壁面4の接
線方向よりもわずか中心方向に向けて貫通して配
設されるほか、該噴射ノズル10の噴出口11先
端とわずかな間隙をもつて対応させて衝突部材9
を配設させている。該衝突部材9噴出口11に対
応する衝突面aは熱処理、あるいは超硬質材の付
設によつて耐摩耗性を高めるほか、外周方向に幾
分傾斜させ、かつ内周壁面6と適当な間隔位置を
維持させて設けられている。なお、該衝突部材9
の形状、材質は種々設計変更が可能であり、また
多角形をした衝突部材9の各面を順次移行させる
ように構成することも可能である。次に噴射ノズ
ル6は圧空源17に連結された圧空管12と、供
給機18と連結される原料入口14および後述す
る分級機19での粗粉粒子を導入する粗粒子入口
15とをエジエクター部bに有する噴出管13と
でなるほか、噴出口11と圧空管12先端との間
には材料を加速させるための加速区間lが設けら
れている。また内周壁面6の一部には前記衝突部
材と隔てられ開孔16が穿設され、該開孔16は
前記噴射ノズル10と、該噴射ノズル10とを連
通させる経路としての連通管20を介して接続さ
れている。なお、本発明においては開孔16の位
置は接線方向に設けられているが、これに限定さ
れるものではない。21は捕集器である。22は
ネジで粉砕室2を構成する一部材である前記上部
円板4を上下調節可能にするもので、これによつ
て粉砕室2内における向心気流風量とこれにとも
なく風速の加減をすることによつて分級粒径を調
節させる。また、粉砕室2内に複数の噴射ノズル
10および衝突部材9を配設させることのほか、
これとは別に圧空を導入させ、粉砕、分級の両作
用を向上させるべく構成することも実施可能であ
る。
The present invention will be explained below by way of examples. 1st
In Figures to Figures 3, the casing 3 of the crusher 1
is an upper disk 4 having a fine powder discharge port 7 at the upper center.
A grinding chamber 2 is constituted by a lower disk 5 having a conical straightening member 8 facing upward in the center thereof, and an inner circumferential wall surface 4 forming a hemispherical or U-shaped cross section. . On the other hand, in the crushing chamber 2, an injection nozzle 10 is disposed to penetrate through the inner circumferential wall surface 4 slightly toward the center of the inner circumferential wall surface 4 than in a tangential direction of the inner circumferential wall surface 4. Collision member 9 corresponds to the tip of outlet 11 with a slight gap.
are being set up. The collision surface a corresponding to the jet nozzle 11 of the collision member 9 is heat-treated or coated with a super hard material to improve wear resistance, and is also slightly inclined in the outer circumferential direction and positioned at an appropriate distance from the inner circumferential wall surface 6. It is set up to maintain. Note that the collision member 9
The shape and material of the collision member 9 can be changed in various ways, and it is also possible to configure the polygonal collision member 9 so that each side of the collision member 9 is moved sequentially. Next, the injection nozzle 6 connects a compressed air pipe 12 connected to a compressed air source 17, a raw material inlet 14 connected to a feeder 18, and a coarse particle inlet 15 for introducing coarse powder particles to a classifier 19, which will be described later, into an ejector. In addition to the ejection pipe 13 provided in section b, an acceleration section l is provided between the ejection port 11 and the tip of the compressed air pipe 12 for accelerating the material. Further, an opening 16 is formed in a part of the inner circumferential wall surface 6 so as to be separated from the collision member, and the opening 16 has a communication pipe 20 as a path for communicating the injection nozzle 10 with the injection nozzle 10. connected via. In addition, in the present invention, the position of the opening 16 is provided in the tangential direction, but the position is not limited to this. 21 is a collector. Reference numeral 22 is a screw that allows the upper disk 4, which is a part of the grinding chamber 2, to be adjusted up and down. By doing this, the classified particle size can be adjusted. In addition to disposing a plurality of injection nozzles 10 and collision members 9 in the crushing chamber 2,
Apart from this, it is also possible to introduce a structure in which compressed air is introduced to improve both the crushing and classification functions.

次に作用について述べる。供給機18により原
料入口14から投入された材料は、圧空源17か
らの高圧空気と共に噴射ノズル10により噴出口
11から高速度で噴射され、粉砕室2内に配設さ
れた衝突部材9に衝突させられる。なお、材料粒
子は噴射ノズル10に設けられた粒子の加速区間
lで充分な速度まで加速された後、衝突部材9の
衝突面aに激突させられるため、その際の衝撃に
よつて材料粒子は粉砕される。なお、材料粒子は
衝突部材9との衝撃による粉砕作用のほか、噴射
ノズル10に設けられた加速区間l内での粒子相
互の衝突や接触、および粉砕室2内への旋回に伴
う粉砕作用をも受ける。一方、衝突面aに当つて
跳ね反る粒子は、該衝突面aが噴射ノズル10に
対し、外周方向に幾分傾斜して配置されているた
め、噴出口11部を損傷させたり、噴出口11よ
りの噴射流jを乱すことなく、内周壁面6に沿つ
て流れる旋回流rと合流される。そして、この時
微粉化された粒子は粉砕室2中心上部の微粉排出
口7より機外に排出、分級機18へと移送され
る。他方、旋回流r中の粗粒子の一部は、内周壁
面6の一部に穿設された前記開孔16より粉砕室
2外に取り出され、前記連通管20を経て原料入
口14からの新な材料と共に再度噴射ノズル10
によつて粉砕室2内に噴射され、前述の粉砕作用
を付与される。このように粉砕作用を繰返し付加
されて微粉化された粒子は前記同様、微粉排出口
7より、分級機19に送られる。そして該分級機
19によつて分級され、微粉は捕集器21によつ
て捕集、粗粉は機外に取り出された後、エジエク
ター部bに設けられた前記粗粒子入口15へ投入
され、再び粉砕室2内で前記粉砕作用を付与され
る。なお、開孔16からの抜き取り量は、該開孔
16の開口面積や開口の方向、位置によつて異る
ほか、連通管20内の圧力調節によつても調節可
能で、この場合、連通管20の一部に調節弁を設
ければよい。
Next, we will discuss the effect. The material input from the raw material inlet 14 by the feeder 18 is injected at high speed from the jet nozzle 11 by the jet nozzle 10 together with high-pressure air from the compressed air source 17, and collides with the collision member 9 disposed in the crushing chamber 2. I am made to do so. Note that, after the material particles are accelerated to a sufficient speed in the particle acceleration section l provided in the injection nozzle 10, they are made to collide with the collision surface a of the collision member 9, so that the material particles are Shattered. In addition to the pulverizing action caused by the impact with the collision member 9, the material particles also undergo pulverizing action due to collisions and contact between the particles within the acceleration section 1 provided in the injection nozzle 10, and as they swirl into the pulverizing chamber 2. I will also receive it. On the other hand, particles that bounce off the collision surface a may damage the jet nozzle 11 or cause damage to the jet nozzle 11 because the collision surface a is arranged with a slight inclination toward the outer circumferential direction with respect to the jet nozzle 10. The jet flow j from 11 is merged with the swirl flow r flowing along the inner circumferential wall surface 6 without disturbing it. Then, the particles pulverized at this time are discharged outside the machine from the fine powder outlet 7 at the upper center of the crushing chamber 2 and transferred to the classifier 18. On the other hand, some of the coarse particles in the swirling flow r are taken out of the grinding chamber 2 through the opening 16 formed in a part of the inner peripheral wall surface 6, and are taken out from the raw material inlet 14 through the communication pipe 20. Spray nozzle 10 again with new material
is injected into the crushing chamber 2 by the pulverizer, and is given the above-mentioned crushing action. The particles thus pulverized by repeated pulverization are sent to the classifier 19 through the pulverizer outlet 7, as described above. After being classified by the classifier 19, the fine powder is collected by the collector 21, and the coarse powder is taken out of the machine, it is introduced into the coarse particle inlet 15 provided in the ejector part b, The above-mentioned pulverizing action is applied again within the pulverizing chamber 2. Note that the amount extracted from the opening 16 varies depending on the opening area of the opening 16, the opening direction, and the position, and can also be adjusted by adjusting the pressure inside the communication pipe 20. A regulating valve may be provided in a part of the pipe 20.

以上のように本発明によれば、粉砕室2と噴射
ノズル10とを連通管20によつて連通させるこ
とによつて、粉砕室2内の旋回流r中の粗粒子を
機外に別に付加された手段によらず直接噴射ノズ
ル10へ移送返還し、粉砕と分級の両作用を交互
に繰り返し付与させるための循環経路が著しく短
縮され、しかも衝突部材9の配設による効果的な
粉砕作用を相俟つて当該粉砕装置自体の小型化を
実現させるものである。また、粉砕性能の向上と
小型化に伴う当該装置の運転経費の減少と、装置
自体の製作費の低減が得られるなど本発明の効果
は著大である。
As described above, according to the present invention, by communicating the grinding chamber 2 and the injection nozzle 10 through the communication pipe 20, coarse particles in the swirling flow r in the grinding chamber 2 are separately added to the outside of the machine. The circulation path for alternately and repeatedly applying both the crushing and classifying actions by directly transferring the material to the injection nozzle 10 without using any other means is significantly shortened, and moreover, the effective crushing action is achieved by the arrangement of the collision member 9. Together, this makes it possible to downsize the crushing device itself. Furthermore, the effects of the present invention are significant, such as improved crushing performance and reduced operating costs of the device due to its miniaturization, as well as a reduction in the manufacturing cost of the device itself.

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

第1図は本発明の実施例を示す系統図、第2図
は要部断面図、第3図は第2図A−A′断面視図
である。 図において1……粉砕機、2……粉砕室、6…
…内周壁面、9……衝突部材、10……噴射ノズ
ル、16……開孔、20……連通管である。
FIG. 1 is a system diagram showing an embodiment of the present invention, FIG. 2 is a sectional view of essential parts, and FIG. 3 is a sectional view taken along line A-A' in FIG. In the figure, 1...Crusher, 2...Crushing chamber, 6...
...Inner peripheral wall surface, 9...Collision member, 10...Injection nozzle, 16...Open hole, 20...Communication pipe.

Claims (1)

【特許請求の範囲】[Claims] 1 中心部に微粉排出口7を、内周壁面6に粉粒
体材料を圧力空気と共に噴射させる噴射ノズル1
0を具備してなる旋回型の空気流式粉砕機であつ
て、該噴射ノズル10に対応し、かつ内周壁面6
と適当な間隔位置に配設された衝突部材9の衝突
面aを外周方向に傾斜させるほか、内周壁面6の
一部に開孔16を穿設し、該開孔16と前記噴射
ノズル10とを連通させる経路を構成させてなる
ことを特徴とする空気流式粉砕機。
1 Injection nozzle 1 having a fine powder discharge port 7 in the center and injecting powder and granular material together with pressurized air onto the inner peripheral wall surface 6
0, which corresponds to the injection nozzle 10 and has an inner circumferential wall surface 6.
In addition to tilting the collision surface a of the collision member 9 disposed at an appropriate distance from the collision member 9 in the outer circumferential direction, an aperture 16 is formed in a part of the inner peripheral wall surface 6, and the aperture 16 and the injection nozzle 10 An air flow type crusher characterized by comprising a path that communicates with the air flow type crusher.
JP16049780A 1980-11-13 1980-11-13 Air current type crusher Granted JPS5784756A (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
JP16049780A JPS5784756A (en) 1980-11-13 1980-11-13 Air current type crusher
GB8133898A GB2091127B (en) 1980-11-13 1981-11-10 Jet pulverizes
CA000389860A CA1181052A (en) 1980-11-13 1981-11-12 Gas flow type crushing and classifying apparatus
FR8121302A FR2493730B1 (en) 1980-11-13 1981-11-13 FLUID VEIN GRINDING AND GRADING APPARATUS
DE19813145209 DE3145209A1 (en) 1980-11-13 1981-11-13 "CRUSHING AND CLASSIFICATION DEVICE"
US06/545,101 US4451005A (en) 1980-11-13 1983-10-21 Gas flow type crushing and classifying apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16049780A JPS5784756A (en) 1980-11-13 1980-11-13 Air current type crusher

Publications (2)

Publication Number Publication Date
JPS5784756A JPS5784756A (en) 1982-05-27
JPS6316979B2 true JPS6316979B2 (en) 1988-04-12

Family

ID=15716208

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16049780A Granted JPS5784756A (en) 1980-11-13 1980-11-13 Air current type crusher

Country Status (1)

Country Link
JP (1) JPS5784756A (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6031838A (en) * 1983-08-03 1985-02-18 工業技術院長 Semi-wet finely crushing machine
US5277369A (en) * 1990-10-02 1994-01-11 Fuji Xerox Co., Ltd. Micromilling device
US5547135A (en) * 1990-10-02 1996-08-20 Fuji Xerox Co., Ltd. Micromilling apparatus
US7258290B2 (en) 2003-09-05 2007-08-21 Nisshin Engineering Inc. Jet mill

Also Published As

Publication number Publication date
JPS5784756A (en) 1982-05-27

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