JP2011189311A - Raw material particle miniaturization apparatus and method for producing miniaturized particle-containing material - Google Patents

Raw material particle miniaturization apparatus and method for producing miniaturized particle-containing material Download PDF

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JP2011189311A
JP2011189311A JP2010058930A JP2010058930A JP2011189311A JP 2011189311 A JP2011189311 A JP 2011189311A JP 2010058930 A JP2010058930 A JP 2010058930A JP 2010058930 A JP2010058930 A JP 2010058930A JP 2011189311 A JP2011189311 A JP 2011189311A
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raw material
material particle
rotating body
particle
particles
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JP5757689B2 (en
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Toru Taniguchi
徹 谷口
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Reika Kogyo KK
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<P>PROBLEM TO BE SOLVED: To provide a raw material particle miniaturization apparatus for easily and continuously miniaturizing particles and a method for producing a miniaturized particle-containing material. <P>SOLUTION: The raw material particle miniaturization apparatus 1 has a rotary body 2 having a plurality of recessed parts 3 just like circles and a jetting part 4 for jetting a mixed liquid of raw material particles and a liquid toward the recessed parts 3 of the rotary body 2. The recessed parts 3 have recessed faces 33 dented in the rotation direction R of the rotary body 2 and the recessed faces 33 are continuous through cutout parts 31 and the mixed liquid jetted from the jetting part 4 is successively supplied to the respective recessed faces 33 along with the rotation of the rotary body 2. <P>COPYRIGHT: (C)2011,JPO&INPIT

Description

本発明は、粒子及び液体の混合液から微細化粒子を製造する技術に関する。   The present invention relates to a technique for producing fine particles from a mixture of particles and liquid.

原料粒子を微細化させる装置としては、特許文献1に示すようなボールミルが知られている。ボールミルは、粉砕したい原料粒子と一緒にセラミックや金属等の硬質ボールを円筒形のドラムを入れ、ドラムを回転させて硬質ボール同士がぶつかり合うことで原料粒子を粉砕して微細化する装置である。   As a device for refining raw material particles, a ball mill as shown in Patent Document 1 is known. A ball mill is a device that pulverizes and refines raw material particles by putting a hard drum such as ceramic or metal together with raw material particles to be pulverized into a cylindrical drum and rotating the drums so that the hard balls collide with each other. .

一方、特許文献2には、液体と原料粒子とを混合撹拌して成分を微粒化して乳化し、分散させる高速撹拌装置が開示されている。この高速撹拌装置は、内周面に凹凸が形成された円筒状の撹拌槽と、この撹拌槽の底面を含む外周面に冷却水を供給かつ排出する水冷配管が接続された外層と、撹拌槽の内周面と僅かの間隙を有して撹拌槽と同心にて高速回転可能な回転羽根と、この回転羽根を端部に支持して正逆高速回転駆動可能なシャフトと、堰板を介して撹拌槽の上部に設けられ製品を排出する排出管を有する上部容器と、この上部容器を密閉する蓋とを備え、撹拌槽の内部面に設けられた凸凹により被処理液の流れを乱して撹拌作用を一段と大きくする。   On the other hand, Patent Document 2 discloses a high-speed stirring device that mixes and stirs liquid and raw material particles to atomize and emulsify and disperse components. This high-speed stirring device includes a cylindrical stirring tank having irregularities formed on the inner peripheral surface, an outer layer connected with a water cooling pipe for supplying and discharging cooling water to the outer peripheral surface including the bottom surface of the stirring tank, and a stirring tank. A rotating blade that can be rotated at high speed concentrically with the agitation tank with a slight gap from the inner peripheral surface of the shaft, a shaft that can be driven forward and reverse at high speed by supporting this rotating blade at the end, and a weir plate The upper container having a discharge pipe for discharging the product provided at the upper part of the stirring tank and a lid for sealing the upper container are provided, and the flow of the liquid to be treated is disturbed by the unevenness provided on the inner surface of the stirring tank. To further increase the stirring action.

しかし、ボールミルは、微小な原料粒子を均一化させるには粗い方法であり、別途フィルタを備える必要がある。また、粘度のある原料粒子の微細化は難しいという問題がある。また、特許文献1の技術では撹拌の際に発生する熱を冷却する必要があり、装置が過大
となるという問題がある。
However, the ball mill is a rough method for homogenizing minute raw material particles, and it is necessary to provide a separate filter. Moreover, there is a problem that it is difficult to make finer raw material particles. Moreover, in the technique of patent document 1, it is necessary to cool the heat which generate | occur | produces in the case of stirring, and there exists a problem that an apparatus becomes excessive.

特許第2837789号公報Japanese Patent No. 2737789 特開2007−125454号公報JP 2007-125454 A

そこで、本発明者は、凝集した原料粒子を分離して容易に連続して微細化させ、粒径の大きな原料粒子を分割して容易に連続して微細化する装置を開示している(非公知の特願2009−204318号)。この装置は、外縁に歯が設けられて回転する回転体と、原料粒子及び液体の混合液を回転体の接近する歯に向けて噴射するノズルと、を備え、混合液を回転体の歯に衝突させて液体内に分散している原料粒子を微細化させる。   In view of this, the present inventor has disclosed an apparatus that separates and aggregates raw material particles easily and continuously and finely divides raw material particles having a large particle size and easily and continuously refines them (non-) Known Japanese Patent Application No. 2009-204318). This device includes a rotating body that is provided with teeth on the outer edge and rotates, and a nozzle that injects a mixture of raw material particles and liquid toward the approaching tooth of the rotating body, and the mixed liquid is applied to the teeth of the rotating body. The raw material particles dispersed in the liquid are made fine by colliding.

本発明は、粒子をより容易に連続して微細化できる原料粒子微細化装置及び微細化粒子含有物の製造方法を提供することを目的とする。   An object of this invention is to provide the raw material particle | grain refiner | miniaturization apparatus which can refine | pulverize a particle | grain continuously more easily, and the manufacturing method of a refined particle containing material.

本発明者らは、回転体の形状と、混合液の噴射方向とを適切化することで、混合液が順次凹部に供給され、凹部内で混合液により強い力が負荷できることを見出し、本発明を完成するに至った。具体的に、本発明は以下のものを提供する。   The present inventors have found that by appropriately adjusting the shape of the rotating body and the injection direction of the mixed liquid, the mixed liquid is sequentially supplied to the recesses, and a strong force can be applied to the mixed liquid in the recesses. It came to complete. Specifically, the present invention provides the following.

(1) 円周状に複数の凹部が配置された回転体と、この回転体の凹部に向けて原料粒子及び液体の混合液を噴射する噴射手段と、を備え、
前記凹部は、前記回転体の回転方向に対して窪んだ凹面を有し、
前記凹面同士は、切り欠け部を介して連続し、
前記噴射手段から噴射される混合液が、前記回転体の回転に伴って前記凹面の各々に順次供給される原料粒子微細化装置。
(1) a rotating body in which a plurality of recesses are arranged circumferentially, and an injection unit that injects a mixture of raw material particles and liquid toward the recesses of the rotating body,
The concave portion has a concave surface that is recessed with respect to the rotational direction of the rotating body,
The concave surfaces are continuous through a notch,
A raw material particle refining apparatus in which the liquid mixture sprayed from the spraying means is sequentially supplied to each of the concave surfaces as the rotating body rotates.

(2) 前記複数の凹部は、前記回転体の円周面に設けられている(1)記載の原料粒子微細化装置。   (2) The raw material particle refining apparatus according to (1), wherein the plurality of recesses are provided on a circumferential surface of the rotating body.

(3) 前記複数の凹部は、前記回転体の側面に設けられている(1)又は(2)記載の原料粒子微細化装置。   (3) The raw material particle refinement apparatus according to (1) or (2), wherein the plurality of recesses are provided on a side surface of the rotating body.

(4) 前記回転体は、放射状に設けられた複数の羽根を備える(1)から(3)いずれか記載の原料粒子微細化装置。   (4) The raw material particle refiner according to any one of (1) to (3), wherein the rotating body includes a plurality of blades provided radially.

(5) 前記回転体を包囲し、前記凹部から排出された微細化粒子が導出される導出口部を有する捕集体を更に備える(1)から(4)いずれか記載の原料粒子微細化装置。   (5) The raw material particle refining apparatus according to any one of (1) to (4), further including a collecting body that surrounds the rotating body and has a lead-out port portion through which the fine particles discharged from the concave portion are led out.

(6) 前記導出口部は、前記回転体の回転軸上に位置する(5)記載の原料粒子微細化装置。   (6) The raw material particle refining device according to (5), wherein the outlet port portion is located on a rotation axis of the rotating body.

(7) 前記捕集体は、前記導出口部の他に外部に連通する排気口部を有する(5)又は(6)記載の原料粒子微細化装置。   (7) The raw material particle refining apparatus according to (5) or (6), wherein the collector has an exhaust port portion communicating with the outside in addition to the outlet port portion.

(8) 排気口部を介して前記捕集体の内気を吸引する吸気手段を更に備える(7)記載の原料粒子微細化装置。   (8) The raw material particle refining device according to (7), further comprising an intake means for sucking the inside air of the collector through an exhaust port.

(9) (1)から(8)いずれか記載の原料粒子微細化装置を用い、
原料粒子及び液体の混合液を前記凹部に向けて噴射し、凹部から排出された微細化粒子を回収する工程を有する微細化粒子含有物の製造方法。
(9) Using the raw material particle refining device according to any one of (1) to (8),
The manufacturing method of the refined particle containing material which has the process of injecting the liquid mixture of a raw material particle and a liquid toward the said recessed part, and collect | recovering the refined particles discharged | emitted from the recessed part.

本発明によれば、凹部が回転体の回転方向に対して窪んだ凹面を有するため、凹部内に供給された混合液が回転体の回転による遠心力を受けて流動し、粒子が微細化される。また、回転体の回転に伴って混合液が供給される凹面が変わる間、混合液は切り欠け部により切り欠けられた部分を通ることで円滑に次に凹面に供給されるので、凹部内に供給されず微細化が不充分なままである粒子が製造されにくい。これにより、粒子をより容易に連続して微細化することができる。   According to the present invention, since the concave portion has a concave surface that is recessed with respect to the rotation direction of the rotating body, the liquid mixture supplied into the concave portion flows under the centrifugal force due to the rotation of the rotating body, and the particles are refined. The In addition, while the concave surface to which the liquid mixture is supplied changes with the rotation of the rotating body, the liquid mixture is smoothly supplied to the concave surface by passing through the portion notched by the notch portion, Particles that are not supplied and remain insufficiently refined are difficult to produce. Thereby, particle | grains can be continuously refined more easily.

本発明の一実施形態に係る原料粒子微細化装置の平面図及び説明図である。It is a top view and explanatory drawing of a raw material particle refining device concerning one embodiment of the present invention. 図1の原料粒子微細化装置のA−A線断面図である。It is the sectional view on the AA line of the raw material particle | grain refiner | miniaturization apparatus of FIG. 図1の原料粒子微細化装置が有する凹部への混合液の供給状態を示す図である。It is a figure which shows the supply state of the liquid mixture to the recessed part which the raw material particle | grain refiner | miniaturization apparatus of FIG. 1 has. 本発明の第2実施形態に係る原料粒子微細化装置の説明図である。It is explanatory drawing of the raw material particle refinement | miniaturization apparatus which concerns on 2nd Embodiment of this invention. 本発明の第3実施形態に係る原料粒子微細化装置の説明図である。It is explanatory drawing of the raw material particle refinement | miniaturization apparatus which concerns on 3rd Embodiment of this invention. 本発明の第4実施形態に係る原料粒子微細化装置の説明図である。It is explanatory drawing of the raw material particle | grain refiner | miniaturization apparatus which concerns on 4th Embodiment of this invention. 図6の原料粒子微細化装置が有する凹部への混合液の供給状態を示す図である。It is a figure which shows the supply state of the liquid mixture to the recessed part which the raw material particle | grain refiner | miniaturization apparatus of FIG. 6 has.

以下、本発明の実施形態について図面を参照しながら説明する。なお、第1実施形態以外の各実施形態の説明において、第1実施形態と共通するものについては、同一符号を付し、その説明を省略する。   Hereinafter, embodiments of the present invention will be described with reference to the drawings. In addition, in description of each embodiment other than 1st Embodiment, the same code | symbol is attached | subjected about what is common in 1st Embodiment, and the description is abbreviate | omitted.

図1は本発明の一実施形態に係る原料粒子微細化装置1の平面図及び説明図であり、図2は原料粒子微細化装置1のA−A線断面図である。原料粒子微細化装置1は、回転体2及び噴射手段としての噴射部4を備える。図3は、原料粒子微細化装置1が有する凹部3への混合液の供給状態を示す図である。   FIG. 1 is a plan view and an explanatory view of a raw material particle refining apparatus 1 according to an embodiment of the present invention, and FIG. 2 is a cross-sectional view of the raw material particle refining apparatus 1 taken along line AA. The raw material particle refining device 1 includes a rotating body 2 and an injection unit 4 as injection means. FIG. 3 is a diagram illustrating a supply state of the mixed liquid to the recess 3 included in the raw material particle refining device 1.

回転体2は円板状部材であり、その中央には回転軸15が直交して設けられている。この回転軸15は駆動源としての回転モータ10に接続され、この回転モータ10の駆動力により回転し、この回転により回転体2が回転方向Rの方向に回転する。   The rotating body 2 is a disk-shaped member, and a rotating shaft 15 is provided orthogonally at the center thereof. The rotating shaft 15 is connected to a rotating motor 10 as a driving source, and is rotated by a driving force of the rotating motor 10, and the rotating body 2 is rotated in the rotation direction R by this rotation.

回転体2は、円周状に複数の凹部3が配置され、これら凹部3のうち、回転体2が回転し噴射部4に対して所定位置にきたものに対し、噴射部4から原料粉体及び液体の混合液が供給される。このとき、原料粉体は凹部3への衝突の衝撃により微細化される。   The rotating body 2 has a plurality of recesses 3 arranged in a circumferential shape. Among these recesses 3, the rotating body 2 rotates and comes to a predetermined position with respect to the injection unit 4. And a liquid mixture is supplied. At this time, the raw material powder is refined by the impact of the collision with the recess 3.

ここで、噴射部4は、回転体2に対して所定箇所に設けられており、回転体2の凹部3に向けて混合液を噴射する。本実施形態における噴射部4は、4個設けられているが、これに限られず、単数又は複数の任意の個数であってよい。ただし、複数の噴射部4を設ける場合、得られる微細化粒子が均質なものになるよう、各噴射部4を、凹部3との位置関係(つまり、距離、角度)がいずれも同等になるように配置することが望ましい。噴射部4の具体的な構成は、その噴射方向が規定される限りにおいて特に限定されず、従来周知のものであってよい。   Here, the injection unit 4 is provided at a predetermined location with respect to the rotating body 2 and injects the liquid mixture toward the concave portion 3 of the rotating body 2. Although the four injection parts 4 in this embodiment are provided, it is not restricted to this, The number of single or several arbitrary may be sufficient. However, when a plurality of injection units 4 are provided, the positional relationship (that is, distance and angle) between the injection units 4 and the recesses 3 is the same so that the obtained fine particles are uniform. It is desirable to arrange in. The specific configuration of the injection unit 4 is not particularly limited as long as the injection direction is defined, and may be a conventionally known one.

原料粒子は、リチウムイオン電池の電極材料等の無機質の粉体である。この原料粒子を構成する複数の粒子6が凝集して粒子径が大きくなっている場合があり、粒子径を均一化させるために凝集した原料粒子を分離して微細化させる必要がある。また、原料粒子を構成する粒子には、粒子径の大きなものがある場合があり、粒子を分割して微細化させる必要もある。このように、原料粒子微細化装置1が対象とする原料粒子は、微細化させて粒度分布を均一化させる必要のあるものであれば、特に限定されない。   The raw material particles are inorganic powders such as electrode materials for lithium ion batteries. In some cases, the plurality of particles 6 constituting the raw material particles are aggregated to increase the particle diameter. In order to make the particle diameter uniform, the aggregated raw material particles need to be separated and refined. In addition, there are cases where the particles constituting the raw material particles have a large particle diameter, and it is necessary to divide the particles to make them finer. Thus, the raw material particles targeted by the raw material particle refining apparatus 1 are not particularly limited as long as the raw material particles need to be refined to make the particle size distribution uniform.

液体は、樹脂製のポリマー、水、溶剤等である。この液体は原料粒子を繋ぐ役割を有し、紛体の分散を促進させる分散剤、例えばいわゆる三相乳化剤(特許第3855203号参照)等や、不粘着化剤等を含んでもよい。   The liquid is a polymer made of resin, water, a solvent, or the like. This liquid has a role of connecting the raw material particles, and may contain a dispersing agent that promotes dispersion of the powder, for example, a so-called three-phase emulsifier (see Japanese Patent No. 3855203), an anti-tacking agent, and the like.

原料粒子が油性物であり、液体が水であってもよい。この場合には、混合液に含まれる原料粒子である油性物が原料粒子微細化装置1により微細化されて乳化する。また、他の例として、混合液がアクリル及びウレタンから構成されるハイブリッド・ポリマーであってもよい。   The raw material particles may be oily and the liquid may be water. In this case, the oily substance that is the raw material particles contained in the mixed solution is refined by the raw material particle refining device 1 and emulsified. As another example, the mixed liquid may be a hybrid polymer composed of acrylic and urethane.

本発明における凹部3は、回転方向Rに対して窪んだ凹面33を有している。このため、凹部30内の混合液は、噴射力及び遠心力の相乗効果により凹面33を回りつつ力を負荷される。これにより、原料粒子がさらに微細化されて、凹部3から排出される。凹面33の形状は、特に限定されないが、遠心力が効率的に負荷されるように、噴射方向に沿った断面が円弧状であることが好ましい。また、混合液が凹面33を回らずに排出されることを抑制するべく、凹面33の側方には側壁21が立設されていることが好ましい。   The concave portion 3 in the present invention has a concave surface 33 that is recessed with respect to the rotation direction R. For this reason, the liquid mixture in the concave portion 30 is loaded with a force while rotating around the concave surface 33 due to the synergistic effect of the injection force and the centrifugal force. Thereby, the raw material particles are further refined and discharged from the recess 3. The shape of the concave surface 33 is not particularly limited, but the cross section along the injection direction is preferably an arc shape so that centrifugal force is efficiently loaded. In order to prevent the mixed liquid from being discharged without rotating around the concave surface 33, it is preferable that the side wall 21 is provided upright on the side of the concave surface 33.

複数の凹部3は、円周状(つまり、回転軸15から略均等の距離)に配置される限りにおいていずれの箇所に設けられていてもよい。本実施形態の複数の凹部3は、回転体2の円周面(つまり、回転軸15が設けられている面及びその背面でない面)に設けられている。ただし、これに限られず、後述のように回転体2の側面(つまり、回転軸15が設けられている面及びその背面)に設けられていてもよい。   The plurality of recesses 3 may be provided at any location as long as they are arranged in a circumferential shape (that is, a substantially equal distance from the rotation shaft 15). The plurality of recesses 3 of the present embodiment are provided on the circumferential surface of the rotating body 2 (that is, the surface on which the rotation shaft 15 is provided and the surface that is not the back surface thereof). However, it is not restricted to this, You may provide in the side surface (namely, the surface in which the rotating shaft 15 is provided, and its back surface) as mentioned later.

ここで、窪んでいる凹面33は互いに離して設けざるを得ない(凹面同士が連通してしまうため)ところ、混合液の噴射流がある凹面から次の凹面に移る間、混合液が凹面に供給されず、微細化が不充分なまま回収されてしまうことが懸念される。   Here, the depressed concave surfaces 33 must be provided apart from each other (because the concave surfaces communicate with each other). However, while the mixed liquid jet flows from one concave surface to the next concave surface, the mixed liquid becomes concave. There is a concern that it will not be supplied and will be recovered with insufficient miniaturization.

しかし、本発明では、図3に示されるように、複数の凹面33同士が、噴射部4から混合液を供給される位置において噴射方向(図3における左方向)に沿うように切り欠けられた切り欠け部31を介して連続している。これにより、回転体2の回転に伴って混合液が供給されるのが凹面33aから凹面33bへと変わる間、混合液は切り欠け部31bにより切り欠けられた部分を通ることで円滑に次に凹面33bに供給されるので、凹面33内に供給されず微細化が不充分なままである粒子が製造されにくい。これにより、粒子をより容易に連続して微細化することができる。   However, in the present invention, as shown in FIG. 3, the plurality of concave surfaces 33 are cut out along the injection direction (left direction in FIG. 3) at the position where the mixed liquid is supplied from the injection unit 4. It continues through the notch 31. As a result, while the liquid mixture is supplied from the concave surface 33a to the concave surface 33b as the rotating body 2 rotates, the liquid mixture passes smoothly through the part cut out by the cutout part 31b. Since it is supplied to the concave surface 33b, it is difficult to produce particles that are not supplied into the concave surface 33 and remain insufficiently refined. Thereby, particle | grains can be continuously refined more easily.

なお、円周面からの切り欠け部31の切り欠け角度Θは、過小であると混合液の凹面への供給が阻害されやすい一方、過大であると凹面33の長さが制限され、粒子の微細化が非効率化しやすい。そこで、切り欠け部は噴射方向と略平行であることが好ましく、切り欠け角度Θが−15°以上15°以下であることが好ましく、より好ましくは5°以下である。   Note that if the notch angle Θ of the notch 31 from the circumferential surface is too small, supply of the mixed liquid to the concave surface tends to be hindered, whereas if too large, the length of the concave surface 33 is limited, and the particle Miniaturization tends to be inefficient. Therefore, the cutout portion is preferably substantially parallel to the injection direction, and the cutout angle Θ is preferably −15 ° to 15 °, more preferably 5 ° or less.

原料粒子微細化装置1は、回転体2を包囲する捕集体14を更に備え、この捕集体14は凹部3から排出された微細化粒子が導出される導出口部16を有する。この導出口部16には回収容器8が接続されており、捕集体14に捕集された微細化粒子は導出口部16を介して回収容器8へと導出される。本実施形態における捕集体14は導出口部16に向かって縮径された円錐形状を有し、これにより微細化粒子の導出口部16への移動が誘導され、捕集体14内での滞留を抑制できる。   The raw material particle refining device 1 further includes a collecting body 14 surrounding the rotating body 2, and the collecting body 14 has a lead-out port 16 through which the fine particles discharged from the recess 3 are led out. The recovery container 8 is connected to the outlet 16, and the fine particles collected by the collector 14 are guided to the recovery container 8 through the outlet 16. The collector 14 in the present embodiment has a conical shape that is reduced in diameter toward the outlet port 16, whereby the movement of the fine particles to the outlet port 16 is induced, and the retention in the collector 14 is prevented. Can be suppressed.

導出口部16は、微細化粒子の導出が促進されやすい点で、回転体2の回転軸15上(つまり、回転軸の延長線上)に位置することが好ましい。ここで、導出口部16が回転軸上に位置するとは、導出口部16が形成する開口の少なくとも一部(好ましくは開口の中心)が回転軸の延長線上にあることを指す。   The outlet 16 is preferably located on the rotating shaft 15 of the rotating body 2 (that is, on the extended line of the rotating shaft) in terms of facilitating the derivation of fine particles. Here, that the outlet 16 is located on the rotation axis means that at least a part of the opening (preferably the center of the opening) formed by the outlet 16 is on an extension line of the rotation axis.

また、捕集体14は、導出口部16の他に外部に連通する排気口部19を有することが好ましい。これにより、混合液中に含まれる気体が混合液から離脱することを促進できる。排気口部19の位置は、気体の排出効率の観点から、本実施形態のように周縁、より具体的には回転体2よりも上方でかつ周縁であることが好ましい。   In addition to the outlet 16, the collector 14 preferably has an exhaust port 19 that communicates with the outside. Thereby, it can accelerate | stimulate that the gas contained in a liquid mixture isolate | separates from a liquid mixture. From the viewpoint of gas discharge efficiency, the position of the exhaust port portion 19 is preferably a peripheral edge as in the present embodiment, more specifically, above the rotating body 2 and at the peripheral edge.

混合液中に含まれる気体は、液体中に含まれる気体と、原料粒子中に含まれる気体(つまり、微細化粒子同士の間に挟まれている気体)との二つで構成され、前者の気体は比較的容易に離脱する一方、後者の気体は離脱しにくい。そこで、本発明における原料粒子微細化装置1は、排気口部19を介して捕集体14の内気を吸引する吸気手段(図示せず)を備えることが好ましい。これにより、原料粒子中に含まれる気体の離脱が促進され、微細化をより促進できる。後述する図4又は5に示す実施形態のように、捕集体14内の気体に渦流を形成する場合には、比重の大きい被処理物5が中央に、比重の小さい気体が外方に分離される。この気体を吸引する気流が渦流を阻害しない点で、排気口部19は回転体2よりも上方でかつ周縁であることが好ましい。なお、吸気手段の具体的な構成は、従来周知の真空ポンプ等であってよく、説明を省略する。   The gas contained in the mixed liquid is composed of two gases, that is, the gas contained in the liquid and the gas contained in the raw material particles (that is, the gas sandwiched between the fine particles). While the gas is released relatively easily, the latter gas is difficult to release. Therefore, the raw material particle refining device 1 according to the present invention preferably includes an intake means (not shown) that sucks the inside air of the collector 14 through the exhaust port 19. Thereby, detachment | desorption of the gas contained in raw material particle | grains is accelerated | stimulated, and refinement | miniaturization can be promoted more. When an eddy current is formed in the gas in the collector 14 as in the embodiment shown in FIG. 4 or 5 to be described later, the object 5 having a large specific gravity is separated in the center and the gas having a small specific gravity is separated outward. The It is preferable that the exhaust port 19 is located above the rotator 2 and at the periphery in that the airflow for sucking the gas does not inhibit the vortex. The specific configuration of the intake means may be a conventionally known vacuum pump or the like, and the description thereof is omitted.

回収容器8には、微細化された粒子6及び液体7を含む被処理物5が収容される。原料粒子微細化装置1による粒子の微細化が終了した場合には、被処理物5は回収容器8の取出し口17から放出される。粒子の微細化を再度行う場合には、供給配管18を通じて噴射部4に被処理物5が供給される。供給配管18には、ポンプ12及びバルブ13が設けられ、被処理物5の供給量の調節が行われる。   In the collection container 8, an object to be processed 5 containing the refined particles 6 and the liquid 7 is accommodated. When the refining of particles by the raw material particle refining device 1 is completed, the workpiece 5 is discharged from the take-out port 17 of the collection container 8. When the particles are refined again, the workpiece 5 is supplied to the injection unit 4 through the supply pipe 18. The supply pipe 18 is provided with a pump 12 and a valve 13, and the supply amount of the workpiece 5 is adjusted.

図4は、本発明の第2実施形態に係る原料粒子微細化装置の説明図である。図4に示されるように、本発明における回転体2Aは、放射状に設けられた複数の羽根23を備えることが好ましい。回転体2Aの回転に伴って羽根23が回転し、捕集体14内の気体の渦流が形成される。これにより、凹部3から排出された微細粒子が渦流にのって導出口部16へと誘導されるため、捕集体14内での滞留をより確実に抑制できる。また、羽根23を回転体2Aに設けることで、羽根23独自の駆動源が不要であるため、構造を簡素化することもできる。なお、複数の羽根23の具体的な構成は、従来周知の扇風機等と同様であり、個数、配置、傾斜角度、形状等は適宜設定されてよい。   FIG. 4 is an explanatory view of a raw material particle refining device according to the second embodiment of the present invention. As shown in FIG. 4, the rotating body 2 </ b> A according to the present invention preferably includes a plurality of blades 23 provided radially. The blades 23 rotate with the rotation of the rotating body 2A, and a gas vortex in the collector 14 is formed. Thereby, since the fine particle discharged | emitted from the recessed part 3 is induced | guided | derived to the outlet port part 16 on a vortex | eddy_current, the residence in the collection body 14 can be suppressed more reliably. Further, by providing the blades 23 on the rotating body 2A, a driving source unique to the blades 23 is unnecessary, and thus the structure can be simplified. In addition, the specific structure of the some blade | wing 23 is the same as that of a conventionally well-known electric fan etc., A number, arrangement | positioning, an inclination angle, a shape, etc. may be set suitably.

また、図4では導出口部16の反対側に設けられているが、これに限られず、同じ側であってもよい。図5は本発明の第3実施形態に係る原料粒子微細化装置の説明図であり、図5に示される羽根23Bは、導出口部16と同じ側に設けられている。羽根23Bは、微細化粒子が羽根23B上に累積することを抑制するため、導出口部16側、本実施形態では下方に傾斜することが好ましい。   Moreover, although it provided in the other side of the outlet port part 16 in FIG. 4, it is not restricted to this, The same side may be sufficient. FIG. 5 is an explanatory view of a raw material particle refining device according to the third embodiment of the present invention, and the blades 23B shown in FIG. 5 are provided on the same side as the outlet port portion 16. In order to prevent the fine particles from accumulating on the blades 23B, the blades 23B are preferably inclined downward in the lead-out port 16 side, in this embodiment.

図6は本発明の第4実施形態に係る原料粒子微細化装置の説明図であり、図7は図6の原料粒子微細化装置が有する凹部への混合液の供給状態を示す図である。本実施形態における凹部3Cは、回転体2Cの側面(つまり、回転軸15が設けられている面及びその背面)に円周状に設けられており、噴射部4はその凹部3Cの位置に対応して設けられている。この態様でも、図7に示されるように、噴射部4から噴射された混合液が、切り欠け部31Cによって切り欠けられた部分により絶え間なく凹面33aC、33bCへと順次供給され、また、回転方向Rへの回転体2Cの回転に伴う遠心力が凹部3C内の粒子に負荷される。このため、より容易に連続して粒子を微細化することができる。   FIG. 6 is an explanatory view of a raw material particle refining apparatus according to a fourth embodiment of the present invention, and FIG. 7 is a view showing a supply state of a mixed liquid to a recess of the raw material particle refining apparatus of FIG. The recess 3C in the present embodiment is provided circumferentially on the side surface of the rotating body 2C (that is, the surface on which the rotation shaft 15 is provided and the back surface thereof), and the injection unit 4 corresponds to the position of the recess 3C. Is provided. Also in this aspect, as shown in FIG. 7, the mixed liquid injected from the injection unit 4 is continuously supplied to the concave surfaces 33aC and 33bC continuously by the part cut out by the cutout part 31C, and also in the rotation direction. Centrifugal force accompanying rotation of the rotating body 2C to R is loaded on the particles in the recess 3C. For this reason, it is possible to finer the particles more easily and continuously.

なお、本発明における凹部や凹面とは、相対的な表現であり、回転体が以上の形状を有する限りにおいて、その製造過程は特に限定されない。即ち、凹部や凹面は窪みを作ることで直接的に形成してもよいが、これに限られず、周囲に凸部を設けることにより間接的に形成してもよい。   In addition, the recessed part and concave surface in this invention are relative expressions, and as long as a rotary body has the above shape, the manufacturing process is not specifically limited. That is, the concave portion or the concave surface may be formed directly by making a recess, but is not limited thereto, and may be indirectly formed by providing a convex portion around the periphery.

本発明は、以上の原料粒子微細化装置を用い、原料粒子及び液体の混合液を凹部に向けて噴射し、凹部から排出された微細化粒子を回収する工程を有する微細化粒子含有物の製造方法も提供する。   The present invention uses the above raw material particle refining apparatus to produce a fine particle-containing material having a step of injecting a mixture of raw material particles and a liquid toward a concave portion and collecting the fine particles discharged from the concave portion. A method is also provided.

本発明は前記実施形態に限定されるものではなく、本発明の目的を達成できる範囲での変形、改良等は本発明に含まれるものである。   The present invention is not limited to the above-described embodiment, and modifications, improvements, and the like within the scope that can achieve the object of the present invention are included in the present invention.

1 原料粒子微細化装置
2 回転体
21 側壁
23 羽根
3 凹部
31 切り欠け部
33 凹面
4 噴射部(噴射手段)
5 被処理物
6 粒子
7 液体
8 回収容器
10 回転モータ
12 ポンプ
13 バルブ
14 捕集体
15 回転軸
16 導出口部
17 取出し口
18 供給配管
19 排気口部
DESCRIPTION OF SYMBOLS 1 Raw material particle refiner 2 Rotating body 21 Side wall 23 Blade 3 Recessed part 31 Notch part 33 Concave surface 4 Injection | pouring part (injection means)
DESCRIPTION OF SYMBOLS 5 To-be-processed object 6 Particle | grains 7 Liquid 8 Collection | recovery container 10 Rotation motor 12 Pump 13 Valve 14 Collecting body 15 Rotating shaft 16 Outlet part 17 Extraction port 18 Supply piping 19 Exhaust part

Claims (9)

円周状に複数の凹部が配置された回転体と、この回転体の凹部に向けて原料粒子及び液体の混合液を噴射する噴射手段と、を備え、
前記凹部は、前記回転体の回転方向に対して窪んだ凹面を有し、
前記凹面同士は、切り欠け部を介して連続し、
前記噴射手段から噴射される混合液が、前記回転体の回転に伴って前記凹部の各々に順次供給される原料粒子微細化装置。
A rotating body in which a plurality of recesses are arranged circumferentially, and an injection means for injecting a mixture of raw material particles and liquid toward the recesses of the rotating body,
The concave portion has a concave surface that is recessed with respect to the rotational direction of the rotating body,
The concave surfaces are continuous through a notch,
A raw material particle refining apparatus in which the liquid mixture sprayed from the spraying means is sequentially supplied to each of the recesses as the rotating body rotates.
前記複数の凹部は、前記回転体の円周面に設けられている請求項1記載の原料粒子微細化装置。   The raw material particle refining device according to claim 1, wherein the plurality of concave portions are provided on a circumferential surface of the rotating body. 前記複数の凹部は、前記回転体の側面に設けられている請求項1又は2記載の原料粒子微細化装置。   The raw material particle refining apparatus according to claim 1, wherein the plurality of recesses are provided on a side surface of the rotating body. 前記回転体は、放射状に設けられた複数の羽根を備える請求項1から3いずれか記載の原料粒子微細化装置。   The said rotary body is a raw material particle | grain refiner | miniaturization apparatus in any one of Claim 1 to 3 provided with the several blade | wing provided radially. 前記回転体を包囲し、前記凹部から排出された微細化粒子が導出される導出口部を有する捕集体を更に備える請求項1から4いずれか記載の原料粒子微細化装置。   The raw material particle | grain refiner | miniaturization apparatus in any one of Claim 1 to 4 further equipped with the collection body which has the derivation | leading-out part which surrounds the said rotary body and the refined particle discharged | emitted from the said recessed part is derived | led-out. 前記導出口部は、前記回転体の回転軸上に位置する請求項5記載の原料粒子微細化装置。   The raw material particle refining device according to claim 5, wherein the outlet port portion is located on a rotation axis of the rotating body. 前記捕集体は、前記導出口部の他に外部に連通する排気口部を有する請求項5又は6記載の原料粒子微細化装置。   The raw material particle refining device according to claim 5 or 6, wherein the collector has an exhaust port portion communicating with the outside in addition to the outlet port portion. 排気口部を介して前記捕集体の内気を吸引する吸気手段を更に備える請求項7記載の原料粒子微細化装置。   The raw material particle refining device according to claim 7, further comprising an intake means for sucking the inside air of the collector through an exhaust port. 請求項1から8いずれか記載の原料粒子微細化装置を用い、
原料粒子及び液体の混合液を前記凹部に向けて噴射し、凹部から排出された微細化粒子を回収する工程を有する微細化粒子含有物の製造方法。
Using the raw material particle refining device according to any one of claims 1 to 8,
The manufacturing method of the refined particle containing material which has the process of injecting the liquid mixture of a raw material particle and a liquid toward the said recessed part, and collect | recovering the refined particles discharged | emitted from the recessed part.
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Citations (2)

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Publication number Priority date Publication date Assignee Title
JPH03131333A (en) * 1989-03-22 1991-06-04 Itsuo Onaka Method and apparatus for preparing powder
JP2002229266A (en) * 2001-02-07 2002-08-14 Canon Inc Method for producing toner

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03131333A (en) * 1989-03-22 1991-06-04 Itsuo Onaka Method and apparatus for preparing powder
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