JPS63104659A - Pulverizer - Google Patents

Pulverizer

Info

Publication number
JPS63104659A
JPS63104659A JP25029186A JP25029186A JPS63104659A JP S63104659 A JPS63104659 A JP S63104659A JP 25029186 A JP25029186 A JP 25029186A JP 25029186 A JP25029186 A JP 25029186A JP S63104659 A JPS63104659 A JP S63104659A
Authority
JP
Japan
Prior art keywords
housing
supply
discharge
stator
rotor
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
JP25029186A
Other languages
Japanese (ja)
Inventor
福西 豊昭
進 仲野
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
Original Assignee
Kawasaki Heavy Industries 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 Kawasaki Heavy Industries Ltd filed Critical Kawasaki Heavy Industries Ltd
Priority to JP25029186A priority Critical patent/JPS63104659A/en
Publication of JPS63104659A publication Critical patent/JPS63104659A/en
Pending legal-status Critical Current

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  • Crushing And Grinding (AREA)
  • Crushing And Pulverization Processes (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) [Abstract] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、被粉砕物をミクロンオーダから10数ミクロ
ンの微細な粒子に微粉砕する微粉砕機に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a pulverizer that pulverizes a material to be pulverized into fine particles ranging from the order of microns to more than 10 microns.

[従来の技術] 従来、上記微粉砕機としては、例えば特開昭59−10
5853号公報所載のものが知られている。この微粉砕
機は、第5図に示すように、内周面に母線と平行な凸状
の多数の刃部1を周方向に連続させた円筒状の固定子2
の両端部に、被粉砕物(図示せず)の供給口3を有する
カップ状(又はキャップ状)の供給ハウジング4と、ト
ナーやセラミック微粉末などの製品(図示せず)の排出
口5を有するキャップ状(又はカップ状)の排出ハウジ
ング6とを連設し、回転軸7に支持され外周面に母線と
平行な凸状の多数の刃部8を周方向に連続させた円筒状
の回転子9を、前記固定子2内に微小な間隙(例えば1
711111以下)を存して嵌挿して概略構成されてい
る。
[Prior Art] Conventionally, as the above-mentioned pulverizer, for example, JP-A-59-10
The one published in Publication No. 5853 is known. As shown in FIG. 5, this pulverizer consists of a cylindrical stator 2 having a number of convex blades 1 continuous in the circumferential direction on the inner peripheral surface parallel to the generatrix.
A cup-shaped (or cap-shaped) supply housing 4 having a supply port 3 for the material to be crushed (not shown) and a discharge port 5 for products such as toner or ceramic fine powder (not shown) are provided at both ends of the housing. A cylindrical rotating body, in which a cap-shaped (or cup-shaped) discharge housing 6 is connected in series, and a number of convex blade portions 8 parallel to the generatrix are continuous in the circumferential direction on the outer circumferential surface, supported by a rotating shaft 7. The child 9 is placed inside the stator 2 with a minute gap (for example, 1
711111 and below) and are inserted into each other.

上記構成の微粉砕機においては、回転子駆動用電動機及
び排出口5に連らなる吸引送風機(共に図示せず)の運
転により、被粉砕物を空気と共に供給口3から供給ハウ
ジング4内に吸引し、回転子9の底壁下面に固設した撹
拌羽根10によって生ずる気流により供給ハウジング4
の内周面に沿わせて上昇させて固定子2と回転子9との
間に形成される粉砕室内に送り込み、高速回転される回
転子9により運動エネルギを与えて固定子2に衝突させ
て粉砕し、かつ回転子9の刃部8により打撃粉砕し、更
に固定子2の刃部と回転子9の刃部8との間で摩砕させ
て一層細かく粉砕させながら、吸引送風機による吸引と
回転子9の高速回転とによって発生した上向きの螺旋気
流に乗せて排出ハウジング6内に送り出し、これを回転
子9の土壁上面に固設した遠心羽根11により排出ハウ
ジング6の内周面に沿わせて回転させ、排出口5から機
外に排出してバグフィルタ(図示せず)に導入し、ここ
で製品と空気とが分離され、空気は吸引送風殿を経て大
気中に排気され、製品はバグフィルタからホッパー(図
示せず)に送られて貯留されるものである。
In the pulverizer configured as described above, the material to be pulverized is sucked into the supply housing 4 from the supply port 3 along with air by operating a rotor-driving electric motor and a suction blower (both not shown) connected to the discharge port 5. The supply housing 4 is heated by the airflow generated by the stirring blades 10 fixed to the lower surface of the bottom wall of the rotor 9.
The powder is raised along the inner circumferential surface of the powder and sent into the grinding chamber formed between the stator 2 and the rotor 9, and the rotor 9, which rotates at high speed, imparts kinetic energy to cause the powder to collide with the stator 2. It is pulverized and crushed by impact with the blade part 8 of the rotor 9, and further crushed between the blade part of the stator 2 and the blade part 8 of the rotor 9 to make it even finer. The air is sent into the discharge housing 6 along the upward spiral airflow generated by the high speed rotation of the rotor 9, and is sent along the inner circumferential surface of the discharge housing 6 by centrifugal blades 11 fixed to the upper surface of the earthen wall of the rotor 9. The product and air are separated here, and the air is exhausted to the atmosphere through the suction vent, and the product is is sent from the bag filter to a hopper (not shown) and stored there.

なお、第5図において12は回転軸7の端部を支承する
軸受でおり、13は回転01I7の下端部に取り付けた
プーリで、ベルト14を介し回転軸駆動用電動機のプー
リと連動されている。
In FIG. 5, 12 is a bearing that supports the end of the rotating shaft 7, and 13 is a pulley attached to the lower end of the rotating shaft 7, which is interlocked with the pulley of the electric motor for driving the rotating shaft via a belt 14. .

[発明が解決しようとする問題点] しかしながら、上記従来の微粉砕機によれば、被粉砕物
の供給口3が供給ハウジング4の底壁外周部に開口して
いるために、かつ、供給ハウジング4内に吸引された気
流(被粉砕物を含む)が撹拌羽根10によって撹拌され
ることも相俟って、固定子2と回転子9との間の粉砕室
に送り込まれる気流に脈動などの乱れを生じ、粉砕室内
における被粉砕物の濃度が不均一になり、粉砕作用にば
らつきを生ずる問題がある。又、製品の排出口5が排出
ハウジング6の周壁に直かに開口しているために、かつ
排出ハウジング6内に送り出された気流が遠心羽根11
によって排出ハウジング6の周壁に押し付けられること
も相俟って、排出ハウジング6から機外に排出される気
流に脈動などの乱れを生じ、粉砕室内における粉砕作用
にばらつきを生ずる問題があり、ひいては製品の粒度分
布に分布中が大きくなるなどの変動をもたらす。
[Problems to be Solved by the Invention] However, according to the above-mentioned conventional pulverizer, since the supply port 3 of the material to be crushed is opened at the outer circumference of the bottom wall of the supply housing 4, Coupled with the fact that the airflow (including the material to be crushed) sucked into the interior of the rotor 4 is stirred by the stirring blades 10, the airflow sent into the crushing chamber between the stator 2 and the rotor 9 is affected by pulsations, etc. There is a problem in that turbulence occurs, and the concentration of the material to be crushed in the crushing chamber becomes non-uniform, resulting in variations in the crushing action. In addition, since the product discharge port 5 opens directly into the peripheral wall of the discharge housing 6, the airflow sent into the discharge housing 6 flows through the centrifugal blades 11.
This combined with the fact that the air is pressed against the peripheral wall of the exhaust housing 6 by the exhaust housing 6 causes turbulence such as pulsation in the airflow discharged from the exhaust housing 6 to the outside of the machine, causing a problem of uneven grinding action within the grinding chamber, which in turn leads to the problem that the product This causes fluctuations in the particle size distribution, such as an increase in the size of the particles.

そこで、本発明は、出入口における気流の乱れの発生を
防止し、もって粉砕作用のばらつきを防止し、ひいては
製品の粒度分布を良好にし得るようにした微粉砕機を提
供しようとするものである。
Therefore, the present invention aims to provide a pulverizer that can prevent the occurrence of air flow turbulence at the inlet and outlet, thereby preventing variations in the pulverizing action, and thereby improving the particle size distribution of the product.

[問題点を解決するための手段] 前記問題点を解決するため、本発明は、内周面に母線と
平行な凸状の多数の刃部を有する円筒状の固定子の端部
に、供給口を有するカップ状の供給ハウジングと、排出
口を有するカップ状の排出ハウジングとを連設し、回転
軸に支持され外周面に母線と平行な凸状の多数の刃部を
有する円筒状の回転子を前記固定子内に微小な間隙を存
してなる微粉砕機において、前記供給ハウジングの供給
口を、接線方向の供給部と、渦巻状の案内部とによって
形成し、かつ前記排出ハウジングの排出口を、渦巻状の
案内部と接線方向の排出部とによって形成したものであ
る。
[Means for Solving the Problems] In order to solve the above-mentioned problems, the present invention provides a cylindrical stator having a plurality of convex blades parallel to the generatrix on its inner peripheral surface. A cylindrical rotating device in which a cup-shaped supply housing having a mouth and a cup-shaped discharge housing having a discharge port are arranged in series, and which is supported by a rotating shaft and has a number of convex blades parallel to the generatrix on its outer peripheral surface. In the pulverizer, the feed port of the feed housing is formed by a tangential feed portion and a spiral guide portion, and the feed port of the feed housing is formed by a tangential feed portion and a spiral guide portion; The discharge port is formed by a spiral guide part and a tangential discharge part.

[作 用] 上記手段によれば、供給口の供給部から吸引された気流
は、進路を急激に変えることなく、案内部によって渦巻
状に案内された後、供給ハウジングの内周面に沿って旋
回しながら粉砕室内に全周から一様に送り込まれ、又、
粉砕室から送り出された気流は、進路を急激に変えるこ
となく、排出口の案内部によって渦巻状に案内された後
、排出部を経て機外に排出され、粉砕室の前後における
気流の乱れはない。
[Function] According to the above means, the airflow sucked from the supply part of the supply port is guided in a spiral shape by the guide part without abruptly changing its course, and then is guided along the inner circumferential surface of the supply housing. It is fed into the crushing chamber uniformly from the entire circumference while rotating, and
The airflow sent out from the grinding chamber is guided in a spiral by the guide section of the discharge port without abruptly changing its course, and then is discharged outside the machine through the discharge section, and the turbulence of the airflow before and after the grinding chamber is eliminated. do not have.

[実施例] 以下、本発明の一実施例を第1図〜第4図に基づいて説
明する。
[Example] Hereinafter, an example of the present invention will be described based on FIGS. 1 to 4.

図において21は基台22上に載置されたカップ状(又
はキャップ状)の供給ハウジングで、この供給ハウジン
グ21の周壁21aは、漏斗状の内周面を有しており、
供給ハウジング21の底部には、被粉砕物(図示せず)
を空気と共に別内に供給する供給口23が設けられてい
る。供給口23は、供給ハウジング21の底部外周に対
して接線方向に伸びる供給部23aと、この供給部23
aの基部に連らなる渦巻状の案内部23bとからなる。
In the figure, 21 is a cup-shaped (or cap-shaped) supply housing placed on a base 22, and the peripheral wall 21a of this supply housing 21 has a funnel-shaped inner peripheral surface.
At the bottom of the supply housing 21, there is a material to be crushed (not shown).
A supply port 23 is provided for supplying the air and air into a separate chamber. The supply port 23 includes a supply portion 23a extending tangentially to the bottom outer periphery of the supply housing 21, and a supply portion 23a extending tangentially to the bottom outer periphery of the supply housing 21.
It consists of a spiral guide part 23b that continues to the base of a.

供給ハウジング21の開口端部には、円筒状の固定子2
4がN股されている。固定子24の内周面には、母線と
平行な凸状の多数の刃部24aが周方向に連続させて設
けられている。そして、固定子24の上端部には、キャ
ップ状(又はカップ状)の排出ハウジング25が連設さ
れており、排出ハウジング25には、製品(図示せず)
を空気と共に機外に排出する排出口26が設けられてい
る。排出口26は、固定子24の内径を最小径部とする
渦巻状の案内部26aと、この案内部26aの最大径部
に連らなる接線方向の排出部26bとからなり、排出部
261)には、図示しない吸引送風機が連らねられてい
る。
A cylindrical stator 2 is provided at the open end of the supply housing 21.
4 is N-crotched. On the inner circumferential surface of the stator 24, a large number of convex blade portions 24a parallel to the generatrix are provided continuously in the circumferential direction. A cap-shaped (or cup-shaped) discharge housing 25 is connected to the upper end of the stator 24, and a product (not shown) is attached to the discharge housing 25.
A discharge port 26 is provided for discharging the water and air to the outside of the machine. The discharge port 26 consists of a spiral guide part 26a whose minimum diameter is the inner diameter of the stator 24, and a tangential discharge part 26b connected to the maximum diameter of the guide part 26a. A suction blower (not shown) is connected to the unit.

前記固定子24内には、回転軸27に支持された円筒状
の回転子28が微小な間隙(例えば1711111以下
)を存して同心に嵌挿されている。回転子28の外周面
には、母線と平行な凸状の多数の刃部28aが、周方向
に連続させて設けられており、又、回転子28の両端壁
には、コーン状の突出部28b、 28cがそれぞれ設
けられている。一方、回転軸27は、両端部の軸受29
a、 29bを介して排出ハウジング25.基台22に
支持されており、基台22内に突出した回転軸27の端
部には、プーリ30が取り付けられている。
A cylindrical rotor 28 supported by a rotating shaft 27 is fitted concentrically into the stator 24 with a small gap (for example, 1711111 mm or less) therebetween. On the outer peripheral surface of the rotor 28, a large number of convex blades 28a parallel to the generatrix are provided continuously in the circumferential direction, and on both end walls of the rotor 28, cone-shaped protrusions are provided. 28b and 28c are provided, respectively. On the other hand, the rotating shaft 27 has bearings 29 at both ends.
a, 29b via the discharge housing 25. A pulley 30 is attached to an end of a rotating shaft 27 that is supported by the base 22 and protrudes into the base 22.

そして、このプーリ30は、ベルト31を介し、図示し
ない回転子駆動用電動機と連動されている。
This pulley 30 is interlocked with a rotor driving electric motor (not shown) via a belt 31.

なお、第1図、第2図において32は供給ハウジング2
1に設けた点検・保守用の孔で、栓体33によって閉鎖
されているものである。
In addition, in FIGS. 1 and 2, 32 is the supply housing 2.
1 is a hole for inspection and maintenance, which is closed by a stopper 33.

上記構成の微粉砕機においては、回転子駆動用電動機及
び吸引送風機を運転すると、被粉砕物は、空気と共に供
給口23の供給部23aから案内部23bによって進路
を急激に変えられることなく渦巻状に案内された後、供
給ハウジング21の内周面に沿って旋回しながら上昇し
、固定子24と回転子28との間の粉砕室の全周に一様
に送り込まれ、高速回転される回転子28によって運動
エネルギを与えられて固定子24に衝突して粉砕され、
又、回転子28の刃部28aによって打撃粉砕され、か
つ固定子24の刃部24aと回転子28の刃部28aと
の間で摩砕されて一層細かく粉砕され、更に固定子24
の刃部24a間に生ずる渦巻に乗って摩砕されつつ、上
面きの螺旋気流に乗って排出ハウジング内に送り出され
、排出口26の案内部26aによって進路を急激に変え
られることなく渦巻状に案内された後、排出部26bか
ら機外に排出されてバグフィルタ(図示せず)に導入さ
れ、ここで製品と空気とが分離され、空気は吸引送m機
を経て大気中に排気され、製品はバグフィルタからホッ
パー(図示せず)に送られて貯留されるものである。
In the pulverizer having the above configuration, when the rotor driving electric motor and the suction blower are operated, the material to be pulverized, together with the air, is moved from the supply part 23a of the supply port 23 to the guide part 23b in a spiral shape without being abruptly changed in its course. After being guided by It is given kinetic energy by the child 28 and collides with the stator 24 and is crushed,
The blades 28a of the rotor 28 impact and crush the rotor 28, and the blades 24a of the stator 24 and the blades 28a of the rotor 28 grind the blades 24a and 28a to further finely crush the stator 24.
While being ground by riding on the swirl generated between the blade parts 24a, the particles are sent into the discharge housing on the spiral airflow from the upper surface, and the guide part 26a of the discharge port 26 prevents the course from being changed abruptly and turns into a spiral shape. After being guided, the product is discharged outside the machine from the discharge part 26b and introduced into a bag filter (not shown), where the product and air are separated, and the air is exhausted to the atmosphere through a suction blower. The product is sent from the bag filter to a hopper (not shown) and stored there.

[発明の効果] 以上のように本発明によれば、供給口の供給部から吸引
された気流は、案内部によって進路を急激に変えること
なく渦巻状に案内された後、供給ハウジングの内周面に
沿って旋回しながら粉砕室内に全周から一様に送り込ま
れ、又、粉砕室から送り出された気流は、排出口の案内
部によって進路を急激に変えることなく渦巻状に案内さ
れた後、接線方向の排出部から機外に排出されるので、
従来のように粉砕室の前後における脈動などの気流の乱
れは生じない。したがって、粉砕室内における粉砕作用
が一様に行われ、製品の粒度分布中を狭くすることがで
きる。
[Effects of the Invention] As described above, according to the present invention, the airflow sucked from the supply part of the supply port is guided in a spiral shape by the guide part without abruptly changing its course, and then flows around the inner periphery of the supply housing. The airflow is uniformly sent into the grinding chamber from the entire circumference while swirling along the surface, and the airflow sent out from the grinding chamber is guided in a spiral shape by the guide part of the discharge port without abruptly changing its course. , since it is discharged outside the machine from the tangential discharge section,
Disturbances in the airflow such as pulsations before and after the grinding chamber do not occur as in the conventional case. Therefore, the crushing action within the crushing chamber is uniformly performed, and the particle size distribution of the product can be narrowed.

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

第1図は本発明の一実施例を示す微粉砕間の縦断面図、
第2図、第3図及び第4図はそれぞれ第1図におけるI
I−II線断面図、m−m線断面図及びIV −IV線
断面図、第5図は従来の微粉砕機の縦断面図である。 21・・・供給ハウジング  23・・・供給口23a
・・・供給部     23b・・・案内部24・・・
固定子      24a・・・刃部25・・・排出ハ
ウジング  26・・・排出口26a・・・案内部  
   26b・・・排出部27・・・回転軸     
 28・・・回転子28a・・・刃部 出 願 人 川崎重工業株式会社 第1図 第2図 第3図 第4図 第5図
FIG. 1 is a longitudinal cross-sectional view of a pulverization chamber showing an embodiment of the present invention;
Figures 2, 3 and 4 are I in Figure 1, respectively.
A sectional view taken along the lines I-II, MM, and IV-IV, and FIG. 5 are longitudinal sectional views of a conventional pulverizer. 21... Supply housing 23... Supply port 23a
... Supply section 23b... Guide section 24...
Stator 24a... Blade section 25... Discharge housing 26... Discharge port 26a... Guide section
26b...Discharge part 27...Rotating shaft
28...Rotor 28a...Blade Applicant Kawasaki Heavy Industries, Ltd. Figure 1 Figure 2 Figure 3 Figure 4 Figure 5

Claims (1)

【特許請求の範囲】[Claims] 内周面に母線と平行な凸状の多数の刃部を有する円筒状
の固定子の端部に、供給口を有するカップ状の供給ハウ
ジングと、排出口を有するカップ状の排出ハウジングと
を連設し、回転軸に支持され外周面に母線と平行な凸状
の多数の刃部を有する円筒状の回転子を前記固定子内に
微小な間隙を存して嵌挿してなる微粉砕機において、前
記供給ハウジングの供給口を、接線方向の供給部と、渦
巻状の案内部とによって形成し、かつ前記排出ハウジン
グの排出口を、渦巻状の案内部と、接線方向の排出部と
によつて形成したことを特徴とする微粉砕機。
A cup-shaped supply housing having a supply port and a cup-shaped discharge housing having a discharge port are connected to the end of a cylindrical stator having a large number of convex blades parallel to the generatrix line on the inner peripheral surface. In a pulverizer, a cylindrical rotor supported by a rotating shaft and having a number of convex blades parallel to the generatrix on its outer peripheral surface is inserted into the stator with a small gap. , the supply opening of the supply housing is formed by a tangential supply part and a spiral guide part, and the discharge opening of the discharge housing is formed by a spiral guide part and a tangential discharge part. A fine grinder characterized by being formed by grinding.
JP25029186A 1986-10-21 1986-10-21 Pulverizer Pending JPS63104659A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25029186A JPS63104659A (en) 1986-10-21 1986-10-21 Pulverizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25029186A JPS63104659A (en) 1986-10-21 1986-10-21 Pulverizer

Publications (1)

Publication Number Publication Date
JPS63104659A true JPS63104659A (en) 1988-05-10

Family

ID=17205720

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25029186A Pending JPS63104659A (en) 1986-10-21 1986-10-21 Pulverizer

Country Status (1)

Country Link
JP (1) JPS63104659A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5355861A (en) * 1993-12-07 1994-10-18 Kyosan Denki Co., Ltd. Evaporative emission control system
US6425380B2 (en) 1998-04-30 2002-07-30 Aisan Kogyo Kabushiki Kaisha Canister for evaporated fuel treatment apparatus

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59189944A (en) * 1983-04-13 1984-10-27 川崎重工業株式会社 Fine crusher

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59189944A (en) * 1983-04-13 1984-10-27 川崎重工業株式会社 Fine crusher

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5355861A (en) * 1993-12-07 1994-10-18 Kyosan Denki Co., Ltd. Evaporative emission control system
US6425380B2 (en) 1998-04-30 2002-07-30 Aisan Kogyo Kabushiki Kaisha Canister for evaporated fuel treatment apparatus

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