JP5269404B2 - Jet mill - Google Patents

Jet mill Download PDF

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JP5269404B2
JP5269404B2 JP2007320467A JP2007320467A JP5269404B2 JP 5269404 B2 JP5269404 B2 JP 5269404B2 JP 2007320467 A JP2007320467 A JP 2007320467A JP 2007320467 A JP2007320467 A JP 2007320467A JP 5269404 B2 JP5269404 B2 JP 5269404B2
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raw material
flange
hollow chamber
cavity chamber
zone
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JP2008168291A (en
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一郎 高林
正弘 浦
盛佳 小波
高広 石川
栄一 宮越
保 石綿
晴彦 堀
洋介 海内
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Nisso Engineering Co Ltd
Nippon Soda Co Ltd
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Nisso Engineering Co Ltd
Nippon Soda Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a jet mill which keeps simpler and more compact structure than conventional one and provides improved classification precision by preventing so-called plunging phenomenon (the phenomenon wherein uncrushed matter flows into a classification zone). <P>SOLUTION: The jet mill is provided with: a mill body 1 having a hollow chamber a; a raw material supplying means 3 introducing a raw material to the hollow chamber a; a discharging part 2 installed nearly in the center of the hollow chamber a; and a jetting means 4 forming a swirling flow in the hollow chamber a, and the jet mill forms a crushing zone for crushing the raw material introduced by the swirling flow and the classification zone for classifying the crushed matter and discharging it from the discharging part 2, wherein the discharging part 2 has a cylindrical part 20 protruded into the hollow chamber a and provided in a standing condition nearly in the center of the lower wall part 11, and a flange 5 disposed on the outer circumference of the cylinder part. <P>COPYRIGHT: (C)2008,JPO&amp;INPIT

Description

本発明は、粉砕機のうち、特に高圧流体を利用した旋回流により粉砕ゾーンと共に分級ゾーンを形成する超微粉砕や解砕に好適な水平旋回流型のジェットミルに関する。   The present invention relates to a horizontal swirling flow jet mill suitable for ultra-fine pulverization and pulverization, in which a classification zone is formed together with a pulverization zone by a swirling flow using a high-pressure fluid among pulverizers.

図5(a),(b)のジェットミルは特許文献1に挙げられている水平旋回流型の基本例(特開昭52−44450号に開示のもの)である。この構造では、ミル本体が円環状の空洞室(粉砕室)43を形成し、空洞室43に原料を導入する原料供給手段(ホッパ41及びノズル42等)と、空洞室43の略中心に設けられた排出部(空洞室内に突出している筒部49付きの排出管48等)と、空洞室43に高圧流体の旋回流を形成する噴射手段(給気管44、空気室45、環状壁46に設けられているノズル47等)とを備えている。そして、空洞室43には、高圧流体が給気管44から空気室45に供給され、環状壁46に噴射角βを持って配置されたノズル47から噴射されて旋回流、つまり外側の粉砕ゾーンと内側の分級ゾーンとを形成する。ホッパ41の原料は、空洞室43内の外周側において、空洞室43の半径に対して角度αを持って配置されたノズル42から空洞室内の粉砕ゾーン側へ噴射供給される。すると、原料は、粉砕ゾーンの旋回流中で専ら原料同士の衝突によって粉砕される。この粉砕物は、内側の分級ゾーンに運ばれ、目的の微粒子は旋回流に乗って筒部49の入口に入って排出され、分級径以上の粗大粒は旋回空気流の遠心力によって再び粉砕ゾーンに飛ばされて再粉砕が行われる。   The jet mill shown in FIGS. 5 (a) and 5 (b) is a basic example of a horizontal swirling flow type disclosed in Japanese Patent Application Laid-Open No. 52-44450. In this structure, the mill main body forms an annular cavity chamber (crushing chamber) 43, provided with raw material supply means (hopper 41, nozzle 42, etc.) for introducing the raw material into the cavity chamber 43, and provided substantially at the center of the cavity chamber 43. And a discharge means (such as a discharge pipe 48 with a cylindrical portion 49 protruding into the hollow chamber) and an injection means (a supply pipe 44, an air chamber 45, an annular wall 46) that forms a swirling flow of high-pressure fluid in the hollow chamber 43. Provided nozzle 47 and the like). Then, the high-pressure fluid is supplied to the hollow chamber 43 from the air supply pipe 44 to the air chamber 45 and is jetted from a nozzle 47 arranged with an injection angle β on the annular wall 46, so that a swirling flow, that is, an outer grinding zone and And an inner classification zone. The raw material of the hopper 41 is injected and supplied from the nozzle 42 arranged at an angle α to the radius of the cavity chamber 43 on the outer peripheral side in the cavity chamber 43 to the grinding zone side in the cavity chamber. Then, the raw material is pulverized exclusively by the collision of the raw materials in the swirling flow of the pulverization zone. This pulverized product is carried to the inner classification zone, and the target fine particles ride on the swirling flow and enter and exit from the inlet of the cylindrical portion 49, and coarse particles having a diameter larger than the classification diameter are again pulverized by the centrifugal force of the swirling air flow. It is skipped and re-pulverized.

特公平7−67541号公報Japanese Patent Publication No. 7-67541

以上のジェットミルでは、例えば、粉砕分級用の高圧旋回流が原料供給用の気流によって乱されることなどに起因し、原料の粉体が粉砕されないまま分級ゾーンに流れ込み、粉砕物と一緒に排出される、いわゆる飛込現象を完全に無くすことは困難であり、そのような飛込現象から分級精度が悪くなったり品質管理に煩わされる。そこで、特許文献1の技術は、そのような対策として、原料供給口を排出部の真上に設けるとともに、モータ及び駆動軸で回転される分散板等からなるロータを備え、原料が原料供給口から回転している分散板上に落下して遠心力により空洞室の外周側へ移動分散されるようにしたものである。しかし、この構造では、ロータの支持機構及びロータ用のモータが必須となり複雑化するため、例えば、洗浄時の分解が困難となる。また、設置スペースが拡大し、装置コストも高くなる。   In the above jet mill, for example, the high-pressure swirling flow for pulverization and classification is disturbed by the air flow for supplying the raw material, so that the raw material powder flows into the classification zone without being pulverized and is discharged together with the pulverized product. In other words, it is difficult to completely eliminate the so-called jump-in phenomenon, and the classification accuracy is deteriorated due to such jump-in phenomenon, and the quality control is bothered. Therefore, the technology of Patent Document 1 includes, as such a countermeasure, a raw material supply port provided directly above the discharge unit, a rotor including a motor and a dispersion plate rotated by a drive shaft, and the raw material is supplied to the raw material supply port. It is dropped onto a rotating dispersion plate from above and is moved and dispersed to the outer peripheral side of the cavity chamber by centrifugal force. However, in this structure, the support mechanism for the rotor and the motor for the rotor are indispensable and complicated, so that, for example, disassembly during cleaning becomes difficult. In addition, the installation space is expanded, and the apparatus cost is increased.

本発明は、水平旋回流型のジェットミルを対象とし、従来構造に比べ装置の簡明化やコンパクト化を維持しながら、飛込現象を防止し、分級精度を向上して粉砕物の粒度バラツキをより小さくできるようにすることを目的としている。   The present invention is directed to a horizontal swirl type jet mill, and while maintaining simplification and compactness of the apparatus as compared with the conventional structure, it prevents a jumping phenomenon, improves classification accuracy, and reduces pulverized particle size variation. The purpose is to make it smaller.

上記目的を達成するため本発明は、上下壁部及び周囲の環状壁で区画された略円環状の空洞室を有したミル本体と、前記空洞室に原料を導入する原料供給手段と、前記空洞室の略中心に設けられた排出部と、前記空洞室に旋回流を形成する噴射手段とを備え、前記旋回流により前記導入される原料を粉砕する粉砕ゾーン、及び粉砕物を分級し(設計上の粒径ないしは粒度に達したものを排出部側へ送り、それ以外のものを再び粉砕ゾーンへ戻す作用)ながら前記排出部より排出可能にする分級ゾーンを形成するジェットミルにおいて、前記排出部は、前記空洞室を区画している上下壁部のうち下壁部の略中心に立設されて前記空洞室に突出している筒部、及び該筒部の先端外周に略水平に配置されているフランジ、並びに前記筒部の外周に設けられて前記空洞室の上下壁部のうち下壁部から前記フランジに向かって張出量を次第に減じる溜まり防止用張出部(図3(a)を参照)を有し To achieve the above object, the present invention provides a mill main body having a substantially annular cavity chamber defined by upper and lower walls and a surrounding annular wall, a raw material supply means for introducing a raw material into the hollow chamber, and the cavity A discharge section provided substantially at the center of the chamber, and an injection means for forming a swirl flow in the hollow chamber, and classifying a pulverization zone and a pulverized product by crushing the introduced raw material by the swirl flow (design) In the jet mill that forms a classification zone that allows discharge from the discharge part while feeding the upper particle size or the one that has reached the particle size to the discharge part side and returning the other particles to the grinding zone again) is cylindrical portion is erected in the substantial center protrudes into the cavity chamber of the inner lower wall section of the upper and lower wall portion which defines a pre-Symbol hollow chamber, and a substantially horizontally disposed to the distal end outer periphery of the cylindrical portion and it has a flange, and set on the outer periphery of the tubular portion Is a prevention protruding portion reservoir reduces progressively projecting amount toward the flange from the lower wall portion out of the upper and lower walls of the hollow chamber (see FIG. 3 (a)),

前記原料供給手段は、前記空洞室を区画している上壁部及び前記フランジを貫通した状態、或いは前記空洞室を区画している周囲の環状壁を貫通した状態に設けられた供給管を有し、前記供給管の吐出口が前記原料を前記フランジと前記ん下壁部との間に噴射するよう前記フランジの下面と略面一か該下面より下方に配置されていることを特徴としている。The raw material supply means has a supply pipe provided in a state penetrating the upper wall portion and the flange defining the hollow chamber, or in a state penetrating the peripheral annular wall defining the hollow chamber. The discharge port of the supply pipe is disposed substantially flush with the lower surface of the flange or below the lower surface so as to inject the raw material between the flange and the lower wall portion. .

請求項1の発明は、フランジを追加するという簡易な構成により、原料供給手段から噴射導入される原料が粉砕されないまま排出部の筒部入口に流れ込んで粉砕物と一緒に排出される飛込現象をほぼ解消することができ、それにより分級精度を向上したり品質管理を簡易化できる。ここで、本発明のフランジは、排出部の筒部入口より下位置で空洞室の粉砕ゾーンまで到達するように原料供給手段から噴射された原料を排出部の筒部入口側へ飛ばないよう規制するものであればよく、形状や取付構造などは任意である。   The invention of claim 1 has a simple structure in which a flange is added, so that the raw material injected from the raw material supply means flows into the cylindrical portion inlet of the discharge portion without being pulverized and is discharged together with the pulverized material. Can be almost eliminated, thereby improving classification accuracy and simplifying quality control. Here, the flange of the present invention is restricted so that the raw material injected from the raw material supply means does not fly to the cylindrical portion inlet side of the discharge portion so as to reach the crushing zone of the hollow chamber at a position below the cylindrical portion inlet of the discharge portion. Any shape and mounting structure may be used.

また、この発明は、フランジが空洞室に略水平に配置されることで噴射手段で形成される旋回流を極力乱さないようにし、しかも、図3(a)の例のように、空洞室内に生じ易いデッドスペース(渦流や乱流などで旋回流が行き渡らない箇所)を溜まり防止用張出部によって無くして粉砕効率を向上する。 Further, the present invention prevents the swirling flow formed by the injection means from being disturbed as much as possible by arranging the flange substantially horizontally in the cavity chamber , and, as shown in the example of FIG. The dead space (location where the swirling flow does not spread due to vortex or turbulent flow) that is likely to occur in a is eliminated by the accumulation preventing overhanging portion 9 to improve the grinding efficiency.

本発明の好適な形態例を図面を参照しながら説明する。図1は形態例のジェットミルを示す模式断面図、図2はフランジの変形例を示す模式図、図3は空洞室の変形例を示し、図4は原料供給手段及び噴射手段の変形例を示している。なお、以下の説明では、作用的に同じ部材や部位に同じ符号を付して、極力重複した説明を省く。勿論、本発明は、以下の形態及び変形例により何ら制約されるものではない。   A preferred embodiment of the present invention will be described with reference to the drawings. 1 is a schematic cross-sectional view showing a jet mill according to an embodiment, FIG. 2 is a schematic view showing a modification of the flange, FIG. 3 shows a modification of the hollow chamber, and FIG. 4 is a modification of the raw material supply means and the injection means. Show. In addition, in the following description, the same code | symbol is attached | subjected to the same member and site | part operatively, and the overlapping description is omitted as much as possible. Of course, this invention is not restrict | limited at all by the following forms and modifications.

(装置構造)形態のジェットミルは、図1に示されるように、中心側の主空洞室a及びその外周囲の副空洞室bを形成しているミル本体1と、主空洞室aの略中心に設けられて粉砕(解砕を含む)及び分級された粉砕物(製品)を取り出す排出部2と、空洞室a,bを区画している上下壁部10,11と、上下壁部10,11のうち上壁部10を貫通した状態に配設されて主空洞室a内に原料(粉体原料)を導入する原料供給手段3と、主空洞室a内に高圧流体による旋回流を形成する噴射手段4などを備え、主空洞室aにあって、噴射手段4を介して形成される旋回流により主空洞室a内に導入される原料である粉体を粉砕する粉砕ゾーン、及び該粉砕ゾーンで粉砕された粉砕物を分級しながら排出部2より排出可能にする分級ゾーンを形成する。なお、発明対象のジェットミルは以上のような水平旋回流型であればよい。 As shown in FIG. 1, the jet mill in the form of (apparatus structure) includes a mill main body 1 that forms a main cavity chamber a on the center side and a sub-cavity chamber b on the outer periphery thereof, and an abbreviation of the main cavity chamber a. The discharge part 2 which takes out the pulverized material (product) crushed (including crushing) and classified by being provided in the center, the upper and lower wall parts 10 and 11 partitioning the cavity chambers a and b, and the upper and lower wall part 10 , 11 are disposed in a state of penetrating the upper wall portion 10 to introduce a raw material (powder raw material) into the main cavity chamber a, and a swirling flow by a high-pressure fluid is introduced into the main cavity chamber a. A pulverization zone for pulverizing powder, which is a raw material introduced into the main cavity chamber a by a swirling flow formed through the injection means 4, including the injection means 4 to be formed, and the like A classification zone is formed that enables discharge from the discharge section 2 while classifying the pulverized material pulverized in the pulverization zone. To. Note that the jet mill of the invention may be a horizontal swirl type as described above.

以上のジェットミルは、要部構造として、排出部2が上下壁部10,11のうち下壁部11の略中心に立設されて主空洞室aに突出している内筒部材20を有しているとともに、該内筒部材20の外周に取り付けられて、該原料供給手段3から導入される原料が内筒部材20の入口側に飛ばないよう規制するフランジ5を有している。   The jet mill described above has, as a main part structure, an inner cylinder member 20 in which the discharge part 2 is erected substantially at the center of the lower wall part 11 of the upper and lower wall parts 10 and 11 and protrudes into the main cavity chamber a. The flange 5 is attached to the outer periphery of the inner cylinder member 20 and regulates the raw material introduced from the raw material supply means 3 so as not to fly to the inlet side of the inner cylinder member 20.

ここで、ミル本体1は、上壁部10と下壁部11との間に環状内側壁12及び環状外側壁13を配設することにより、内側壁12の内側に主空洞室aを区画形成し、内側壁12と外側壁13との間に給気室用の副空洞室bを区画形成している。図1の下壁部11には、貫通孔6が略中心に設けられているとともに、下壁部11の内側に貫通孔6を中心とする凹所11aが設けられている。但し、本発明のミル本体は、図4の変形例のように副空洞室bを省略する構成でもよい。   Here, the mill main body 1 forms a main cavity chamber a inside the inner wall 12 by disposing the annular inner wall 12 and the annular outer wall 13 between the upper wall 10 and the lower wall 11. In addition, a sub-cavity chamber b for the air supply chamber is defined between the inner wall 12 and the outer wall 13. In the lower wall portion 11 of FIG. 1, a through hole 6 is provided substantially at the center, and a recess 11 a centering on the through hole 6 is provided inside the lower wall portion 11. However, the mill main body of the present invention may have a configuration in which the sub-cavity b is omitted as in the modification of FIG.

排出部2は、下壁部11の凹所11aに突設されて主空洞室a内に突設されている内筒部材20と、内筒部材20と連通した状態で下壁部11の外側に突設されている接続用筒部材21とを有している。内筒部材20と接続用筒部材21は、対応取り付け端側を折り曲げたフランジ部20a,21aを有している。そして、内筒部材20は、下壁部11の内面に対しフランジ部20aが凹所11aに面一に嵌合された状態に配置される。接続用筒部材21は、下壁部11の外面に対しフランジ部21aの内径が貫通孔6及び内筒部材20と同軸線上に配置される。その状態から、留め具Sがフランジ部21a、下壁部11の対応部、フランジ部20aに締め付け係止されることで、下壁部11に対し内筒部材20及び接続用筒部材21が一体的に結合されている。なお、以上の内筒部材20や接続用筒部材21の取付構造としては、接着や溶着等の他の手段であってもよい。   The discharge part 2 protrudes in the recess 11a of the lower wall part 11 and protrudes in the main cavity chamber a, and the outer part of the lower wall part 11 is in communication with the inner cylinder member 20. And a connecting cylinder member 21 projecting from the connector. The inner cylinder member 20 and the connecting cylinder member 21 have flange portions 20a and 21a in which the corresponding attachment end side is bent. And the inner cylinder member 20 is arrange | positioned in the state by which the flange part 20a was fitted by the recess 11a with respect to the inner surface of the lower wall part 11. FIG. In the connecting cylinder member 21, the inner diameter of the flange portion 21 a is arranged coaxially with the through hole 6 and the inner cylinder member 20 with respect to the outer surface of the lower wall portion 11. From that state, the fastener S is fastened and locked to the flange portion 21 a, the corresponding portion of the lower wall portion 11, and the flange portion 20 a, so that the inner cylindrical member 20 and the connecting cylindrical member 21 are integrated with the lower wall portion 11. Combined. The mounting structure of the inner cylinder member 20 and the connecting cylinder member 21 may be other means such as adhesion or welding.

原料供給手段3は、上壁部10又は内側壁12に対して所定位置及び角度に接続されている供給管30と、該供給管30に連結されたホッパ31と、ノズル32等によって構成されている。そして、原料は、ホッパ31から供給管30に入ると、ノズル32から圧送される高圧流体とともに主空洞室aの粉砕ゾーンへ噴射供給される。なお、原料供給手段3は、これ以外にも、例えば、高圧流体供給管及び加速管を組み合わせたラバールノズル構成にしたり、原料粉末の物性や供給量等によって複数箇所に設けられる構成を含む。   The raw material supply means 3 includes a supply pipe 30 connected to the upper wall 10 or the inner wall 12 at a predetermined position and angle, a hopper 31 connected to the supply pipe 30, a nozzle 32, and the like. Yes. When the raw material enters the supply pipe 30 from the hopper 31, the raw material is jetted and supplied to the pulverization zone of the main cavity chamber a together with the high-pressure fluid pumped from the nozzle 32. In addition, the raw material supply means 3 includes, for example, a Laval nozzle configuration in which a high-pressure fluid supply pipe and an acceleration pipe are combined, or a configuration provided at a plurality of locations depending on the physical properties and supply amount of the raw material powder.

噴射手段4は、副空洞室bと、外部から副空洞室bに高圧流体を導入する給気管41と、内側壁12に組み付けられて副空洞室b内の高圧流体を主空洞室aへ噴射するノズル40とにより構成されている。ノズル40は、内側壁12の周囲に対し等分した箇所にそれぞれ付設されるとともに、内側壁12の直径方向に対し所定角度傾斜した状態に設けられている。   The injection means 4 is assembled to the sub-cavity b, the air supply pipe 41 for introducing the high-pressure fluid from the outside into the sub-cavity b, and the high-pressure fluid in the sub-cavity b being injected into the main cavity a. And a nozzle 40 that performs the above operation. The nozzles 40 are respectively attached to portions equally divided with respect to the periphery of the inner wall 12, and are provided in a state inclined at a predetermined angle with respect to the diameter direction of the inner wall 12.

以上の噴射手段4は、高圧流体をノズル40から噴射すると、該噴射による旋回流により主空洞室a内にあって、中心から離れる周囲側に粉砕ゾーンを形成し、中央側に分級ゾーンを形成する構成であればよく、例えば、副空洞室bを省略して高圧流体を各ノズル40へ直接供給するようにしてもよい。粉砕ゾーンでは、原料が加速されて互いに衝突したり周囲壁面に衝突して粉砕されるが、その場合、特許第3087201号公報に示されているように粉砕ゾーンに粉砕促進用の衝突板や整流板を付設してもよい。分級ゾーンでは、粉砕ゾーンで粉砕された粉砕物のうち、所定粒径ないしは粒度に達したものが粉砕ゾーンから移行し分級された後、排出部2を構成している内筒部材20及び接続用筒部材21を介して外部へ排出される。   When the high-pressure fluid is jetted from the nozzle 40, the above jetting means 4 forms a pulverization zone in the main cavity chamber a by the swirling flow caused by the jetting, away from the center, and forms a classification zone in the central side. For example, the subcavity b may be omitted and the high pressure fluid may be directly supplied to each nozzle 40. In the pulverization zone, the raw materials are accelerated and collide with each other or collide with the surrounding wall surface and are pulverized. In this case, as shown in Japanese Patent No. 3087201, the pulverization zone includes a collision plate for promoting pulverization and rectification. A plate may be attached. In the classification zone, among the pulverized products pulverized in the pulverization zone, those having reached a predetermined particle size or particle size are transferred from the pulverization zone and classified, and then the inner cylinder member 20 constituting the discharge unit 2 and the connection It is discharged outside through the cylindrical member 21.

フランジ5は、概楕円形などの滑らかな平板であり、内筒部材20の上端側を通す大孔5aを有し、内筒部材20に対してほぼ水平状態に結合されている。また、フランジ部5は、供給管30の先端側を通す小孔5bを有し、内筒部材20に対し該内筒部材の上端外周を大孔5aに係合し、かつ周囲を溶着することでほぼ水平状態に結合される場合もある。小孔5bは、供給管30の先端部を差し込んで係合する斜めの孔であるが、楕円の一部を小円弧に切り欠いて供給管30の先端部をその切り欠きに沿ってフランジ上方からフランジ下面側へ配置してもよい。この場合、供給管30の先端は、吐出口から噴射される原料の噴射方向を乱さないように、フランジ5の小孔5bを貫通した状態でフランジ5の下面と略面一、又は、フランジ5より若干量だけ下方へ突出させることが好ましい。   The flange 5 is a smooth flat plate such as an elliptical shape, has a large hole 5 a that passes through the upper end side of the inner cylinder member 20, and is coupled to the inner cylinder member 20 in a substantially horizontal state. Further, the flange portion 5 has a small hole 5b through which the distal end side of the supply pipe 30 is passed, the upper end outer periphery of the inner cylinder member is engaged with the large hole 5a with respect to the inner cylinder member 20, and the periphery is welded. In some cases, they are coupled in a substantially horizontal state. The small hole 5b is an oblique hole into which the distal end portion of the supply pipe 30 is inserted and engaged. However, a part of the ellipse is cut into a small arc, and the distal end portion of the supply pipe 30 is located above the flange along the notch. To the flange lower surface side. In this case, the tip of the supply pipe 30 is substantially flush with the lower surface of the flange 5 in a state of passing through the small hole 5b of the flange 5 so as not to disturb the injection direction of the raw material injected from the discharge port, or the flange 5 It is preferable to protrude downward by a slight amount.

ここで、フランジ5は、供給管30の噴射方向に長くなっていて、原料が供給管30から噴射されたとき、フランジ5の存在により内筒部材20の入口、つまりフランジ5より上側へ飛ばないようして、空洞室aの粉砕ゾーンまで導くものである。このため、供給管30(原料供給手段3のノズル32)から噴射された原料は、フランジ5によって排出部側内筒部材20の入口側へ飛ばないよう確実に規制される。   Here, the flange 5 is elongated in the injection direction of the supply pipe 30, and when the raw material is injected from the supply pipe 30, the flange 5 does not fly to the inlet of the inner cylinder member 20, that is, above the flange 5. Thus, it leads to the pulverization zone of the hollow chamber a. For this reason, the raw material injected from the supply pipe 30 (the nozzle 32 of the raw material supply means 3) is reliably regulated by the flange 5 so as not to fly to the inlet side of the discharge portion side inner cylinder member 20.

(作動)以上のジェットミルにおいて、原料は、原料供給手段3から主空洞室aに供給されると、上述したフランジ5の存在により主空洞室aの粉砕ゾーンまで確実に供給されて、複数のノズル40から噴射させている高圧流体の旋回流のうち、主空洞室aの外周囲側に形成される粉砕ゾーンで加速されて互いに衝突したり内側壁12に衝突しながら粉砕される。粉砕されたものは、主空洞室aの中央側に形成される分級ゾーンで分級されて、内筒部材20及び接続用筒部材21を通って外部へ排出される。すなわち、この構造では、フランジ5を追加するだけで、従来のごとく粉砕されないまま内筒部材20の入口に流れ込んで粉砕物と一緒に排出されるという飛込現象の発生を無くし、それにより分級精度を向上したり品質管理を簡易化できるようにする。 (Operation) In the above jet mill, when the raw material is supplied from the raw material supply means 3 to the main cavity chamber a, the presence of the flange 5 described above ensures that the raw material is supplied to the pulverization zone of the main cavity chamber a. Of the swirling flow of the high-pressure fluid ejected from the nozzle 40, the high-speed fluid is accelerated in the crushing zone formed on the outer peripheral side of the main cavity chamber a and collides with each other or collides with the inner wall 12. The crushed material is classified in a classification zone formed at the center side of the main cavity chamber a, and is discharged to the outside through the inner cylinder member 20 and the connecting cylinder member 21. That is, in this structure, the addition of the flange 5 eliminates the occurrence of a jumping phenomenon that flows into the inlet of the inner cylinder member 20 without being pulverized as in the prior art and is discharged together with the pulverized material, thereby improving the classification accuracy. To improve quality and simplify quality control.

(図2の変形例)図2(a)は原料供給手段3を2つ付設したときの例を示している。この例では、フランジ5Aは、略円盤状の滑らかな平板であり、大孔5aが中心部に設けられるとともに、小孔5bが大孔5aを挟んで対に設けられている。各小孔5bは、対応する供給管30の先端部を差し込んで係合する斜めの孔であるが、円の一部を小円弧に切り欠いて供給管30の先端部をその切り欠きに沿ってフランジ上方からフランジ下面側へ配置してもよい。 (Modification of FIG. 2) FIG. 2 (a) shows an example in which two raw material supply means 3 are provided. In this example, the flange 5A is a substantially disk-shaped smooth flat plate, and a large hole 5a is provided at the center, and a small hole 5b is provided in pairs with the large hole 5a interposed therebetween. Each small hole 5b is an oblique hole to which the tip end portion of the corresponding supply pipe 30 is inserted and engaged, but a part of a circle is cut into a small arc and the tip end portion of the supply pipe 30 is along the cutout. It may be arranged from the upper side of the flange to the lower side of the flange.

図2(b)はフランジ5Bを原料供給手段3側に取り付けたときの例である。この例では、フランジ5Bは、扇状の滑らかな平板であり、内筒部材20の外周に当接する内側の円弧状切欠部5cと、供給管30の先端側を通す小孔5bとを有し、供給管30に対し該供給管30の先端を小孔5bに係合し、かつ周囲を溶着することでほぼ水平状態に結合されている。小孔5bは、供給管30の先端部を差し込んで係合する斜めの孔であるが、扇形の外側の一部を切り欠いて供給管30の先端部をその切り欠きに沿ってフランジ上方からフランジ下面側へ配置してもよい。このように、本発明のフランジ5,5A,5Bはその形状だけではなく、取付構造も色々変形可能である。   FIG. 2B is an example when the flange 5B is attached to the raw material supply means 3 side. In this example, the flange 5B is a fan-shaped smooth flat plate, and has an inner arcuate cutout portion 5c that abuts the outer periphery of the inner cylinder member 20, and a small hole 5b that passes the distal end side of the supply pipe 30. The front end of the supply pipe 30 is engaged with the small hole 5b and welded to the supply pipe 30 in a substantially horizontal state. The small hole 5b is an oblique hole into which the distal end portion of the supply pipe 30 is inserted and engaged. However, a part of the fan-shaped outer side is notched, and the distal end portion of the supply pipe 30 is formed along the notch from above the flange. You may arrange | position to the flange lower surface side. As described above, the flanges 5, 5 </ b> A, 5 </ b> B of the present invention can be variously deformed in addition to their shapes.

(図3の変形例)図3(a)はミル本体1を構成している上壁部10をハット形状にした例である。すなわち、このミル本体1では、上壁部10の中央部に貫通孔7を形成するとともに、該貫通孔7を逆凹状の外筒部材8で閉じた構成となっている。貫通孔7は下壁部11の貫通孔6より大径の孔である。外筒部材8は、取り付け端側を折り曲げたフランジ部8aを有し、フランジ部8aの内径が貫通孔7及び内筒部材20と同軸線上に位置するよう配置された後、フランジ部8aが留め具S1により上壁部11の対応部に締め付け係止されることで、上壁部10に対し一体的に結合されている。この構造では、例えば、上壁部10とフランジ5との間に形成される分級ゾーンが外筒部材8の逆凹状により拡張され、それに起因して分級効率の向上が期待される。 (Modification of FIG. 3) FIG. 3 (a) shows an example in which the upper wall portion 10 constituting the mill body 1 is hat-shaped. In other words, the mill body 1 has a configuration in which the through hole 7 is formed in the central portion of the upper wall portion 10 and the through hole 7 is closed by the reverse concave outer cylinder member 8. The through hole 7 is a hole having a larger diameter than the through hole 6 of the lower wall portion 11. The outer cylinder member 8 has a flange portion 8a bent at the attachment end side, and is arranged so that the inner diameter of the flange portion 8a is positioned on the same axis as the through hole 7 and the inner cylinder member 20, and then the flange portion 8a is fastened. By being fastened and locked to the corresponding portion of the upper wall portion 11 by the tool S1, the upper wall portion 10 is integrally coupled. In this structure, for example, the classification zone formed between the upper wall portion 10 and the flange 5 is expanded by the reverse concave shape of the outer cylinder member 8, and as a result, improvement in classification efficiency is expected.

図3(b)は更に外筒部材8Aが深い逆凹状に形成されるとともに、内筒部材20の全寸を長くし、該長くなった筒上延長部25を外筒部材8Aの逆凹状内に突出した構成となっている。すなわち、この排出部2は、内筒部材20が下壁部11に突設されて、空洞室aを縦方向に横切るよう上壁部10側へ延び、かつ該上壁部10に付設されている外筒部材8Aの逆凹状内に排出補助経路用隙間c、及び二次分級用隙間dを保って配置されている排出用筒上延長部25を有している。このため、粉砕ゾーンで粉砕された粉砕物のうち、空洞室aの分級ゾーンに入った粉砕物を当該分級ゾーンで分級した後、排出補助経路用隙間c及び二次分級用隙間dを通ることにより精度よく分級して筒上延長部25内から排出可能にする。この構造は、特願2006−18375号に開示したもので、分級ゾーンに入った粉砕物について、分級ゾーンでの一次分級に加え、排出補助経路用隙間c及び二次分級用隙間dを通すことにより再度精度よく分級(二次分級)されるようにし、それにより従来構造に比べて装置の簡明化やコンパクト化を損なうことなく粒径又は粒度のバラツキを抑えて分級精度を向上したものである。   In FIG. 3B, the outer cylindrical member 8A is further formed in a deep reverse concave shape, and the entire length of the inner cylindrical member 20 is lengthened, and the elongated cylindrical upper portion 25 is formed inside the reverse concave shape of the outer cylindrical member 8A. It has a configuration protruding. In other words, the discharge portion 2 includes an inner cylinder member 20 protruding from the lower wall portion 11, extending toward the upper wall portion 10 so as to cross the cavity chamber a in the vertical direction, and attached to the upper wall portion 10. The outer cylinder member 8 </ b> A has a discharge cylinder upper extension 25 disposed in a reverse concave shape with the discharge auxiliary path gap c and the secondary classification gap d maintained. For this reason, among the pulverized materials pulverized in the pulverization zone, the pulverized material that has entered the classification zone of the hollow chamber a is classified in the classification zone, and then passes through the discharge auxiliary path gap c and the secondary classification gap d. Therefore, it is possible to classify with high accuracy and discharge from the cylinder extension 25. This structure is disclosed in Japanese Patent Application No. 2006-18375. In addition to the primary classification in the classification zone, the pulverized material entering the classification zone is passed through the discharge auxiliary path gap c and the secondary classification gap d. The classification accuracy is improved again (secondary classification), thereby improving the classification accuracy by suppressing the variation in particle size or particle size without impairing the simplification and compactness of the device compared to the conventional structure. .

(図4の変形例)この変形例は、図1のジェットミルに対し副空洞室bを省略して、主空洞室aを区画している環状壁14(この環状壁は図1の内側壁12に対応している)に噴射手段4Aを構成しているノズル装置42を周囲4等分した箇所にそれぞれ設けたものである。各ノズル装置42は、不図示の高圧流体供給部に配管などで接続されて高圧流体を図1のノズル40と同様に噴射する。また、この変形例では、原料供給手段3の供給管30を主空洞室aを区画している環状壁12に所定の角度を持って配置した、いわゆる接線供給方式を採用している。このように、供給管30が環状壁12を介して配設されている場合にも、原料が供給管30から噴射されたとき、フランジ5の存在により原料が内筒部材20の入口、つまりフランジ5より上側へ飛ばないようになり、主空洞室aの粉砕ゾーンまで導かれる。このため、この場合も、原料供給手段3の供給管30から噴射された原料は、フランジ5によって排出部側内筒部材20の入口側へ飛ばないよう確実に規制される。なお、供給管30は、先端を環状壁12の内周面とほぼ一致した状態に設けられているが、フランジ5の下側まで突出するようにしてもよい。また、以上のフランジ5の形状としては、周囲部が多少下や上側に湾曲した傘や皿状であってもよい。 (Modification of FIG. 4) In this modification, the subcavity b is omitted from the jet mill of FIG. 1, and the annular wall 14 defining the main cavity chamber a (this annular wall is the inner wall of FIG. 1). 12), the nozzle device 42 constituting the injection means 4A is provided at each of the four equally divided locations. Each nozzle device 42 is connected to a high-pressure fluid supply unit (not shown) by piping or the like, and injects high-pressure fluid in the same manner as the nozzle 40 in FIG. Further, in this modification, a so-called tangential supply method is adopted in which the supply pipe 30 of the raw material supply means 3 is arranged with a predetermined angle on the annular wall 12 defining the main cavity chamber a. As described above, even when the supply pipe 30 is disposed via the annular wall 12, when the raw material is injected from the supply pipe 30, the raw material is introduced into the inlet of the inner cylinder member 20, that is, the flange due to the presence of the flange 5. 5 so that it does not fly above 5, and is guided to the grinding zone of the main cavity chamber a. For this reason, also in this case, the raw material injected from the supply pipe 30 of the raw material supply means 3 is reliably regulated by the flange 5 so as not to fly to the inlet side of the discharge portion side inner cylinder member 20. The supply pipe 30 is provided with a tip substantially coincident with the inner peripheral surface of the annular wall 12, but may be protruded to the lower side of the flange 5. Further, the shape of the flange 5 described above may be an umbrella or a dish shape in which the peripheral portion is curved slightly downward or upward.

(実施例)次に、以上のジェットミルを用いて微粉砕を行った試験例により本発明の有効性を明らかにする。 (Embodiment) Next, the effectiveness of the present invention will be clarified by a test example in which fine pulverization is performed using the above jet mill.

この試験例において、使用したジェットミルは図4に示す接線供給方式であり、空洞室(図4の主空洞室aつまり粉砕室である)の内径が直径312mm、空洞室の外周部の高さが50mm、空洞室中心底部にある排出部の内径が直径70mmであり、空洞室外周部にあって周囲4等分する箇所に設けられた噴射手段用ノズル(図4のノズル装置)が4個、及び原料供給手段用ノズル(図4の供給管)が1個とを備えたタイプであり、副空洞室のない構成である。原料としては、炭酸カルシウム(丸尾カルシウム株式会社製で、メディアン径115μmのもの)を用い、以下の条件で粉砕を行った。   In this test example, the jet mill used has the tangential supply system shown in FIG. 4, the inside diameter of the hollow chamber (the main hollow chamber a in FIG. 4, that is, the grinding chamber) is 312 mm in diameter, and the height of the outer peripheral portion of the hollow chamber is Is 50 mm, the inner diameter of the discharge part at the center bottom of the cavity chamber is 70 mm in diameter, and there are four nozzles for injection means (nozzle device in FIG. 4) provided at the outer periphery of the cavity chamber and divided into four equal parts. , And a nozzle for raw material supply means (supply pipe in FIG. 4), and has no sub-cavity chamber. As a raw material, calcium carbonate (manufactured by Maruo Calcium Co., Ltd., having a median diameter of 115 μm) was used and pulverized under the following conditions.

すなわち、実施例1と2では、前記排出部が空洞室の上下壁部のうち下壁部の中心に立設されて該空洞室に突出している高さ(突出寸法)53mmの筒部からなるとともに、該筒部の突出端側外周にフランジ(材質がSUS304製で、直径212mm、厚さ5mmの円形フランジ)を取り付けた構成であり、粉砕条件として粉砕圧6kg/cm、風量2.5〜2.6m/minの設定で行った。これに対し、比較例1と2では、排出部が筒部外周にフランジを有しない構成以外は前記実施例と同じ粉砕条件で行った。粒子径分布は、マイクロトラック(Microtrac)粒度分布測定装置MT3300EXII(日機装株式会社製)で測定した、表1にはその粉砕結果を一覧表示した。 That is, in the first and second embodiments, the discharge portion is a cylindrical portion having a height (projection dimension) of 53 mm that stands upright at the center of the lower wall portion of the upper and lower wall portions of the hollow chamber and protrudes into the hollow chamber. In addition, a flange (a circular flange made of SUS304, having a diameter of 212 mm and a thickness of 5 mm) is attached to the outer periphery of the protruding end side of the cylindrical portion. The pulverization conditions are 6 kg / cm 2 , the air volume is 2.5 It was performed at a setting of ˜2.6 m 3 / min. On the other hand, in the comparative examples 1 and 2, it performed on the same grinding | pulverization conditions as the said Example except the structure to which a discharge part does not have a flange in a cylinder part outer periphery. The particle size distribution was measured with a Microtrac particle size distribution measuring device MT3300EXII (manufactured by Nikkiso Co., Ltd.). Table 1 lists the pulverization results.

(表1)

Figure 0005269404
(Table 1)

Figure 0005269404

以上の実施例1,2と比較例1,2より明らかなように、ジェットミルの排出部が本発明のごとく空洞室に突出している筒部の外周に配置されたフランジを有していることにより、これまで問題となっていた粗い粒子の混入が大幅に改善されて、メディアン径も小さくなり、粒度分布がシャープな粉砕物が得られた。このようにジェットミルとしては、排出部の筒部が外周にフランジを有することにより、分級性能が向上し、処理速度の向上にもつながることが判明した。   As is clear from Examples 1 and 2 and Comparative Examples 1 and 2, the jet mill discharge part has a flange disposed on the outer periphery of the cylindrical part protruding into the hollow chamber as in the present invention. As a result, mixing of coarse particles, which has been a problem until now, has been greatly improved, a median diameter has been reduced, and a pulverized product having a sharp particle size distribution has been obtained. As described above, it has been found that, as the jet mill, the cylinder portion of the discharge portion has the flange on the outer periphery, thereby improving the classification performance and improving the processing speed.

(a)は本発明形態のジェットミルを示す模式縦断面図、(b)は(a)のA−A線矢視断面図である。(A) is a schematic longitudinal cross-sectional view which shows the jet mill of this invention form, (b) is an AA arrow directional cross-sectional view of (a). (a)と(b)はフランジの変形例を示す模式図である。(A) And (b) is a schematic diagram which shows the modification of a flange. (a)と(b)はミル本体又は排出部の変形例を示す模式断面図である。(A) And (b) is a schematic cross section which shows the modification of a mill main body or a discharge part. (a)と(b)は噴射手段等を変更した変形例を示す模式断面図である。(A) And (b) is a schematic cross section which shows the modification which changed the injection means etc. FIG. (a)と(b)は特許文献1に開示の水平旋回流型ジェットミルの基本形を示す図である。(A) And (b) is a figure which shows the basic form of the horizontal swirling flow type jet mill disclosed by patent document 1. FIG.

符号の説明Explanation of symbols

1…ミル本体(10と11は上・下壁部、12と13は内・外側壁)
2…排出部(21は接続用筒部材)
3…原料供給手段(30は供給管、31はホッパ、32はノズル)
4,4A…噴射手段(bは副空洞室、40はノズル、41は給気管)
5,5A,5B…フランジ
6,7…貫通孔
8,8A…外筒部材
9…溜まり防止用張出部
14…ミル本体の環状壁
42…ノズル装置
20…内筒部材(筒部)
a…主空洞室(空洞室)
b…副空洞室
c…排出補助経路用隙間
d…二次分級用隙間
1 ... Mill body (10 and 11 are upper and lower walls, 12 and 13 are inner and outer walls)
2 ... discharge part (21 is a cylinder member for connection)
3. Raw material supply means (30 is a supply pipe, 31 is a hopper, 32 is a nozzle)
4, 4A ... injection means (b is a sub-cavity chamber, 40 is a nozzle, 41 is an air supply pipe)
5, 5A, 5B ... Flange 6, 7 ... Through hole 8, 8A ... Outer cylinder member
DESCRIPTION OF SYMBOLS 9 ... Overhang | projection part 14 for pool prevention ... The annular wall of a mill main body 42 ... Nozzle apparatus 20 ... Inner cylinder member (cylinder part)
a ... Main cavity (cavity)
b ... Sub-cavity chamber c ... Clearance for auxiliary discharge path d ... Clearance for secondary classification

Claims (1)

上下壁部及び周囲の環状壁で区画された略円環状の空洞室を有したミル本体と、前記空洞室に原料を導入する原料供給手段と、前記空洞室の略中心に設けられた排出部と、前記空洞室に旋回流を形成する噴射手段とを備え、前記旋回流により前記導入される原料を粉砕する粉砕ゾーン、及び粉砕物を分級しながら前記排出部より排出可能にする分級ゾーンを形成するジェットミルにおいて、
前記排出部は、前記空洞室を区画している上下壁部のうち下壁部の略中心に立設されて前記空洞室に突出している筒部、及び該筒部の先端外周に略水平に配置されているフランジ、並びに前記筒部の外周に設けられて前記空洞室の上下壁部のうち下壁部から前記フランジに向かって張出量を次第に減じる溜まり防止用張出部を有し
前記原料供給手段は、前記空洞室を区画している上壁部及び前記フランジを貫通した状態、或いは前記空洞室を区画している周囲の環状壁を貫通した状態に設けられた供給管を有し、前記供給管の吐出口が前記原料を前記フランジと前記下壁部との間に噴射するよう前記フランジの下面と略面一か該下面より下方に配置されていることを特徴とするジェットミル。
A mill main body having a substantially annular cavity chamber defined by an upper and lower wall part and a surrounding annular wall, a raw material supply means for introducing a raw material into the cavity chamber, and a discharge part provided substantially at the center of the cavity chamber And a pulverizing zone for pulverizing the raw material introduced by the vortex flow, and a classification zone for discharging the pulverized material from the discharge part while classifying the pulverized material. In the forming jet mill,
The discharge section, front Symbol cylindrical portion is erected in the substantial center protrudes into the cavity chamber of the inner lower wall section of the upper and lower wall portion which defines a cavity chamber, and a substantially horizontal at the tip outer periphery of the cylindrical portion It has arranged to have flanges, as well as the prevention protruding portion reservoir reduces progressively projecting amount from the lower wall portion toward the flange out of the upper and lower walls of the hollow chamber is provided on the outer periphery of the tubular portion ,
The raw material supply means has a supply pipe provided in a state penetrating the upper wall portion and the flange defining the hollow chamber, or in a state penetrating the peripheral annular wall defining the hollow chamber. And a discharge port of the supply pipe is disposed substantially flush with or below the lower surface of the flange so as to inject the raw material between the flange and the lower wall portion. mill.
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CN103785515B (en) * 2012-10-30 2016-04-13 高国儒 Multi-cavity tandem eddy flow pulverizer

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