WO2011040620A1 - Processing device - Google Patents

Processing device Download PDF

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Publication number
WO2011040620A1
WO2011040620A1 PCT/JP2010/067309 JP2010067309W WO2011040620A1 WO 2011040620 A1 WO2011040620 A1 WO 2011040620A1 JP 2010067309 W JP2010067309 W JP 2010067309W WO 2011040620 A1 WO2011040620 A1 WO 2011040620A1
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WO
WIPO (PCT)
Prior art keywords
processing apparatus
mixing tank
tank
stirring blade
blade
Prior art date
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PCT/JP2010/067309
Other languages
French (fr)
Japanese (ja)
Inventor
要介 中野
良章 小矢島
石川 修
靖由 関根
雄介 高橋
Original Assignee
日本コークス工業株式会社
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Application filed by 日本コークス工業株式会社 filed Critical 日本コークス工業株式会社
Priority to CN201080042447.5A priority Critical patent/CN102574084B/en
Priority to KR1020127009945A priority patent/KR101378068B1/en
Priority to DE112010003894.5T priority patent/DE112010003894B4/en
Priority to JP2011534354A priority patent/JP5575139B2/en
Publication of WO2011040620A1 publication Critical patent/WO2011040620A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2/00Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
    • B01J2/10Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic in stationary drums or troughs, provided with kneading or mixing appliances
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/60Mixing solids with solids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/05Stirrers
    • B01F27/11Stirrers characterised by the configuration of the stirrers
    • B01F27/112Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades
    • B01F27/1123Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades sickle-shaped, i.e. curved in at least one direction
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • B01F27/808Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with stirrers driven from the bottom of the receptacle
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • B01F27/90Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with paddles or arms 
    • B01F27/902Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with paddles or arms  cooperating with intermeshing elements fixed on the receptacle walls
    • B01F27/9021Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with paddles or arms  cooperating with intermeshing elements fixed on the receptacle walls the elements being vertically arranged, e.g. fixed on the bottom
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/18Stationary reactors having moving elements inside

Definitions

  • Patent Document 1 describes a processing apparatus as shown in FIG.
  • the processing apparatus 110 includes a horizontal cylindrical mixing tank 120, a rotary shaft 130 provided through one side wall, and a plurality of stirring blades 140 provided on the rotary shaft 130. Since the treatment of the powder is accompanied by a large heat generation, the mixing tank 120 is provided with a jacket 193 so that it can be cooled by passing water.
  • Patent Document 2 describes a processing apparatus as shown in FIG.
  • the processing apparatus 210 includes a rotary shaft 230 provided inside the vertical mixing tank 220 through the tank bottom of the mixing tank 220.
  • the rotating shaft 230 is provided with a cylindrical rotating body 281 and a plurality of stirring blades 240.
  • the rotating body 281 is provided with a plurality of openings 282, and the inner surface thereof is pressed by a press head 283.
  • the mixing tank 220 is provided with a jacket 293 so that it can be cooled by water flow.
  • the processing device 210 performs batch processing.
  • An object of the present invention is a processing apparatus that performs advanced processing such as compounding and coating by applying a strong compressive force and shearing force to a processed product of a granular material, and has a simple structure and a flow of the processed product It is an object of the present invention to provide a processing apparatus that can easily control the processing conditions and can easily find the optimum processing conditions.
  • a processing apparatus is provided with a bowl-shaped mixing tank, a rotating shaft provided through the tank bottom of the mixing tank, and the rotating shaft.
  • a powder processing apparatus comprising a plurality of stirring blades and a plurality of collision plates fixed to the mixing tank, wherein the diameter of the mixing tank is d and the stirring blades and the collision plates The shortest distance between and is 0.1d or less.
  • the processing apparatus according to claim 2 of the present invention is the processing apparatus according to claim 1, wherein the collision plate has a width of 0.05d to 0 when the diameter of the mixing tank is d. .25d and the height is 0.05d to 0.2d.
  • the processing apparatus according to claim 3 of the present invention is the processing apparatus according to claim 1 or 2, wherein the mixing tank is cylindrical and the bottom corner of the tank is round and smoothly formed.
  • a means having a radius of curvature of 0.05 d or more is adopted.
  • a processing apparatus according to claim 4 of the present invention is the processing apparatus according to any one of claims 1 to 3, wherein the stirring blades are arranged on an inclined surface of a boss portion formed in a substantially conical shape. Adopting means.
  • the processing apparatus according to claim 5 of the present invention is the processing apparatus according to claim 4, wherein the upper part of the stirring blade is connected by a ring-shaped upper plate, and the ring-shaped upper plate and the inclined surface are connected.
  • the processing apparatus according to claim 6 of the present invention employs means in the processing apparatus according to claim 4 or 5, wherein the rotation shaft includes an auxiliary blade positioned above the stirring blade. ing.
  • the processing apparatus according to a seventh aspect of the present invention is the processing apparatus according to any one of the first to third aspects, wherein the rotating shaft includes an inclined blade positioned inside the stirring blade. Adopted.
  • the processing apparatus of the present invention has a simple structure and can apply a strong compressive force or shearing force to the processed material, such as compounding and coating of powder particles. Advanced processing can be performed. And it is easy to control the flow of a processed material, and the optimal process conditions can be found easily.
  • FIG. 1 shows an example of the processing apparatus of the present invention, wherein (1) is a schematic longitudinal sectional view, and (2) is a schematic transverse sectional view.
  • 2 shows the processing apparatus of FIG. 1 in detail, (1) is a schematic longitudinal sectional view, and (2) is a detailed view of part A of (1).
  • FIG. 3 shows another example of the processing apparatus of the present invention, where (1) is a schematic longitudinal sectional view, (2) is a detailed view of a portion B of (1), and (3) is a view taken along arrows XX in (2). It is sectional drawing.
  • FIG. 4 shows still another example of the processing apparatus of the present invention, where (1) is a schematic longitudinal sectional view, and (2) is a detail view of part C of (1).
  • FIG. 1 shows an example of the processing apparatus of the present invention, wherein (1) is a schematic longitudinal sectional view, and (2) is a schematic transverse sectional view. 2 shows the processing apparatus of FIG. 1 in detail, (1) is a schematic longitudinal sectional view, and (2) is a detailed view of
  • FIG. 1 shows an embodiment of a processing apparatus according to the present invention.
  • FIG. 1 (1) is a longitudinal sectional view
  • FIG. 1 (2) is a transverse sectional view
  • 2 is a detailed explanatory view of FIG. 1
  • FIG. 2 (1) is a longitudinal sectional view
  • FIG. 2 (2) is a detailed view of part A of (1).
  • the processing apparatus 10 is fixed to the bowl-shaped mixing tank 20, a rotating shaft 30 provided through the tank bottom of the mixing tank 20, a plurality of stirring blades 40 provided on the rotating shaft 30, and the mixing tank 20.
  • a plurality of collision plates 50 are provided.
  • a lid 60 is provided at the top of the mixing tank 20 and is connected by a flange 61.
  • the lid 60 is provided with a processed material inlet, and the mixing tank 20 is provided with a product outlet, which is not shown in the figure.
  • the processing apparatus 10 of the present invention is characterized in that a circulating flow of powder particles is formed in the mixing tank 20, thereby promoting the mixing process. That is, an inertia force is given to the granular material by the rotation of the stirring blade 40, and the granular material is discharged upward along the tank wall from the vicinity of the tank bottom corner. The granular material rises near the tank wall and descends near the tank center, thereby forming a circulating flow in the mixing tank.
  • the mixing tank 20 is not limited to a cylindrical shape, and may have a shape in which the diameter gradually decreases from the lower part to the upper part, a spherical shape, or the like. However, in any shape, the mixing tank 20 is limited to a vertical shape in which the rotation shaft 30 is provided substantially vertically.
  • the diameter inside the mixing tank 20 is demonstrated as d. And when the diameter of the mixing tank 20 changes with height, the diameter d shall show a maximum diameter.
  • the mixing tank 20 is cylindrical, it is preferable that the bottom corner of the tank is round and smoothly formed. This is because the granular material subjected to the inertial force by the stirring blade 40 is smoothly discharged upward. As shown in FIG.
  • the shape and number of the stirring blades 40 are not particularly limited, but it is desirable that the stirring blades 40 give a strong inertial force to the powder and strongly release upward from the vicinity of the bottom of the tank along the tank wall.
  • the diameter I of the stirring blade 40 is preferably as large as possible at the bottom of the tank. That is, when the mixing tank 20 is cylindrical, the diameter I of the stirring blade 40 is preferably 0.7 d or more, and more preferably 0.85 d or more.
  • the processing apparatus 10 of this invention is equipped with the some collision board 50 fixed to the mixing tank 20, and is characterized by the above-mentioned.
  • the rotational speed of the stirring blade 40 is preferably as high as possible. However, if the rotational speed is too high, the coated particles may be peeled off or the base particles as a base may be destroyed. Become. Therefore, the practical tip speed of the stirring blade 40 is in the range of 20 to 150 m / s, and preferably in the range of 30 to 100 m / s.
  • the shape and number of the collision plates 50 are not particularly limited, but it is necessary to give a strong impact to the circulating flow of the granular material and not to disturb the circulating flow of the granular material. Therefore, the number is preferably about 4 to 12. Further, as shown in FIG.
  • FIG. 3 shows another embodiment of the processing apparatus according to the present invention.
  • FIG. 3 (1) is a longitudinal sectional view
  • FIG. 3 (2) is a detailed view of part B of FIG. It is XX arrow sectional drawing in 2).
  • the processing apparatus 11 is different from the processing apparatus 10 in that an inner intubation 51 including a collision plate 50 is inserted into the mixing tank 20.
  • the flange 52 of the inner tube 51 is sandwiched between the flanges 61 of the mixing tank 20. Therefore, by preparing a plurality of intubation tubes 51, it is possible to perform processing while changing the shape of the collision plate 50 and the like.
  • FIG. 3 (3) showing a cross section taken along the line XX in FIG. 3 (2) shows the positional relationship between the stirring blade 40 and the collision plate 50 that are provided close to each other.
  • the angle between the rotation direction of the stirring blade 40 indicated by the arrow and the collision surface of the collision plate 50 is defined as ⁇ .
  • the angle ⁇ ranges from 30 degrees to 90 degrees.
  • FIG. 5 shows still another embodiment of the processing apparatus according to the present invention.
  • FIG. 5 (1) is a longitudinal sectional view and
  • FIG. 5 (2) is a transverse sectional view.
  • the processing apparatus of the present invention has a simple structure, and the processed material is processed by forming a simple circulating flow. Therefore, it is easy to grasp the characteristics of the flow of the processed material, and it is easy to control this. Moreover, although the change of the processing conditions depends on the shape and rotation speed of the stirring blades and the shape of the collision plate, all can be performed relatively easily, and the optimal processing conditions can be easily found.
  • the processing apparatus of the present invention is considered to be usable in a very wide field.
  • lithium cobaltate As an electrode material in a lithium ion battery, it is possible to coat lithium cobaltate with carbon. Moreover, it is possible to coat nylon with titanium dioxide as a cosmetic material. It is also possible to coat a pigment on PMMA powder used as a substitute for inorganic glass. Further, as a powder coating material, it is possible to coat a pigment on the surface of particles such as an epoxy resin. Moreover, it is possible to spheroidize graphite particles as a battery material. For electronic printing, it is possible to coat the surface of toner particles with ultrafine silica or titanium dioxide.

Abstract

Disclosed is a processing device that performs processes such as compositing by applying strong pressure or shear force to granular materials. Said processing device, which has a simple structure and can easily find optimal processing conditions, is provided with: a vertical mixing vessel (20); a rotating shaft (30) inserted through the bottom of the mixing vessel (20); a plurality of stirring blades (40) provided on the rotating shaft (30); and a plurality of impact plates (50) affixed to the mixing vessel (20). Letting the diameter of the mixing vessel (20) be d, the minimum distance between the stirring blades (40) and the impact plates (50) is at most 0.1d.

Description

処理装置Processing equipment
 本発明は、粉粒体を処理する処理装置であって、特に複合化や球形化などの高度な処理を行うことができる処理装置に関する。 The present invention relates to a processing apparatus for processing powder particles, and more particularly to a processing apparatus capable of performing advanced processing such as compounding and spheroidization.
 粒径がミクロンオーダー又はナノオーダーの粉粒体を取り扱う処理において、アスペクト比の大きな粒子を球形化したり、粒径の大きな粒子の表面上に粒径の小さな粒子をコーティングしたり、複数種類の粒子を一体化された球状粒子に複合化したりするような、粉粒体の処理が広く要求されている。
 例えば、特許文献1には、図10に示すような処理装置が記載されている。この処理装置110は、横型円筒状の混合槽120と、一方の側壁を挿通して設けられる回転軸130と、回転軸130に設けられる複数の撹拌羽根140を備えている。粉粒体の処理は大きな発熱を伴うので、混合槽120にはジャケット193を設け、通水により冷却できるようになっている。
 また、混合槽120の両側には粉粒体の投入口191と排出口192が設けられ、連続処理ができるようになっている。撹拌羽根140は、回転によって処理物を排出口192に向って送るような傾斜を備える「送り羽根」と、回転によって処理物を投入口191に向って戻すような傾斜を備える「戻り羽根」とが交互に組み合わされている。
 処理装置110では、「送り羽根」と「戻り羽根」とによって交互に、処理物に繰り返し強い力を与えることができる。そして、粉粒体の複合化やコーティングなどの処理を行うことができる。粉粒体に対する作用効果は、撹拌羽根140の形状や配列などの構造的要素によって、大きく影響されるものと考えられる。しかしながら、構造的要素を変更することは容易でなく、処理条件を簡単には変更できず、最適処理条件を見つけることが難しいという問題がある。
 特許文献2には、図11に示すような処理装置が記載されている。この処理装置210は、竪型の混合槽220の内部に、混合槽220の槽底を挿通して設けられる回転軸230を備えている。回転軸230には、筒状の回転体281及び複数の撹拌羽根240が設けられている。回転体281には複数の開口282が設けられ、その内面はプレスヘッド283で押圧されるようになっている。また、混合槽220にはジャケット293が設けられ、通水により冷却できるようになっている。
 この処理装置210ではバッチ処理が行われる。混合槽220に投入された処理物は、回転体281の内外を循環流動しながら処理を受ける。すなわち、処理物は、開口282を通して回転体281の内側から外側に向って流れ、回転体281の外側で撹拌羽根240によって上方へ押し流され、回転体281の上部で外側から内側に戻ってくる。そして、回転体281の内側において、プレスヘッド283によって処理物に強い圧縮力及び剪断力を与え、粉粒体の複合化やコーティングなどの処理を行うことができる。
 しかしながら、処理装置210は構造が複雑であるために高価な装置となる。また、構造が複雑であるために、処理物の流れを制御することが難しく、最適処理条件を見つけることが難しいという問題がある。
When processing particles with micron-order or nano-order particle sizes, particles with a large aspect ratio are spheroidized, particles with a large particle size are coated on the surface of particles, and multiple types of particles There is a wide demand for the treatment of powder particles, such as compounding them into integrated spherical particles.
For example, Patent Document 1 describes a processing apparatus as shown in FIG. The processing apparatus 110 includes a horizontal cylindrical mixing tank 120, a rotary shaft 130 provided through one side wall, and a plurality of stirring blades 140 provided on the rotary shaft 130. Since the treatment of the powder is accompanied by a large heat generation, the mixing tank 120 is provided with a jacket 193 so that it can be cooled by passing water.
In addition, on both sides of the mixing tank 120, a powder inlet 191 and an outlet 192 are provided so that continuous processing can be performed. The stirring blade 140 includes a “feed blade” having an inclination to send the processed material toward the discharge port 192 by rotation, and a “return blade” having an inclination to return the processed material to the input port 191 by rotation. Are combined alternately.
In the processing apparatus 110, a strong force can be repeatedly applied to the processing object alternately by the “feed blade” and the “return blade”. And processing, such as compounding and coating of a granular material, can be performed. It is considered that the action and effect on the granular material is greatly influenced by structural elements such as the shape and arrangement of the stirring blades 140. However, there is a problem that it is not easy to change the structural element, the processing conditions cannot be changed easily, and it is difficult to find the optimum processing conditions.
Patent Document 2 describes a processing apparatus as shown in FIG. The processing apparatus 210 includes a rotary shaft 230 provided inside the vertical mixing tank 220 through the tank bottom of the mixing tank 220. The rotating shaft 230 is provided with a cylindrical rotating body 281 and a plurality of stirring blades 240. The rotating body 281 is provided with a plurality of openings 282, and the inner surface thereof is pressed by a press head 283. The mixing tank 220 is provided with a jacket 293 so that it can be cooled by water flow.
The processing device 210 performs batch processing. The processed material put into the mixing tank 220 is subjected to processing while circulating and flowing inside and outside the rotating body 281. That is, the processed material flows from the inside to the outside of the rotating body 281 through the opening 282, is pushed upward by the stirring blade 240 outside the rotating body 281, and returns from the outside to the inside at the top of the rotating body 281. And inside the rotary body 281, the press head 283 gives a strong compressive force and a shearing force to a processed material, and processings, such as a composite and coating of a granular material, can be performed.
However, the processing device 210 is an expensive device due to its complicated structure. Further, since the structure is complicated, there is a problem that it is difficult to control the flow of the processed material and it is difficult to find the optimum processing condition.
特開2005−270955号公報JP 2005-270955 A 特開2005−15910号公報JP 2005-15910 A
 本発明の課題は、粉粒体の処理物に強い圧縮力や剪断力を与えることにより、複合化やコーティングなどの高度な処理を行う処理装置であって、構造が簡単で、処理物の流れを制御することが容易であり、最適な処理条件を容易に見つけることができる処理装置を提供することにある。 An object of the present invention is a processing apparatus that performs advanced processing such as compounding and coating by applying a strong compressive force and shearing force to a processed product of a granular material, and has a simple structure and a flow of the processed product It is an object of the present invention to provide a processing apparatus that can easily control the processing conditions and can easily find the optimum processing conditions.
 上記の課題を解決するために、本発明の請求項1に係る処理装置は、竪型の混合槽と、前記混合槽の槽底を挿通して設けられる回転軸と、前記回転軸に設けられる複数の撹拌羽根と、前記混合槽に固定して設けられる複数の衝突板とを備える粉粒体の処理装置であって、前記混合槽の直径をdとするとき、前記撹拌羽根と前記衝突板との最短距離が0.1d以下である手段を採用している。
 また、本発明の請求項2に係る処理装置は、請求項1に記載の処理装置において、前記衝突板の大きさは、前記混合槽の直径をdとするとき、幅が0.05d~0.25dであり、高さが0.05d~0.2dである手段を採用している。また、本発明の請求項3に係る処理装置は、請求項1又は2に記載の処理装置において、前記混合槽が円筒状であって槽底隅部が丸く滑らかに形成され、前記混合槽の直径をdとするとき、その曲率半径が0.05d以上である手段を採用している。
 また、本発明の請求項4に係る処理装置は、請求項1乃至3の何れかに記載の処理装置において、前記撹拌羽根が、略円錐状に形成されたボス部の傾斜面に配列されている手段を採用している。また、本発明の請求項5に係る処理装置は、請求項4に記載の処理装置において、前記撹拌羽根の上部がリング状上板で連結され、該リング状上板と前記傾斜面との間を、内側から外側に向かって粉粒体が流動する手段を採用している。
 また、本発明の請求項6に係る処理装置は、請求項4又は5に記載の処理装置において、前記回転軸が、前記撹拌羽根よりも上部に位置する補助羽根を備えている手段を採用している。さらに、本発明の請求項7に係る処理装置は、請求項1乃至3の何れかに記載の処理装置において、前記回転軸が、前記撹拌羽根の内側に位置する傾斜羽根を備えている手段を採用している。
In order to solve the above-mentioned problems, a processing apparatus according to claim 1 of the present invention is provided with a bowl-shaped mixing tank, a rotating shaft provided through the tank bottom of the mixing tank, and the rotating shaft. A powder processing apparatus comprising a plurality of stirring blades and a plurality of collision plates fixed to the mixing tank, wherein the diameter of the mixing tank is d and the stirring blades and the collision plates The shortest distance between and is 0.1d or less.
The processing apparatus according to claim 2 of the present invention is the processing apparatus according to claim 1, wherein the collision plate has a width of 0.05d to 0 when the diameter of the mixing tank is d. .25d and the height is 0.05d to 0.2d. Moreover, the processing apparatus according to claim 3 of the present invention is the processing apparatus according to claim 1 or 2, wherein the mixing tank is cylindrical and the bottom corner of the tank is round and smoothly formed. When the diameter is d, a means having a radius of curvature of 0.05 d or more is adopted.
A processing apparatus according to claim 4 of the present invention is the processing apparatus according to any one of claims 1 to 3, wherein the stirring blades are arranged on an inclined surface of a boss portion formed in a substantially conical shape. Adopting means. The processing apparatus according to claim 5 of the present invention is the processing apparatus according to claim 4, wherein the upper part of the stirring blade is connected by a ring-shaped upper plate, and the ring-shaped upper plate and the inclined surface are connected. The means by which the granular material flows from the inside toward the outside is adopted.
Further, the processing apparatus according to claim 6 of the present invention employs means in the processing apparatus according to claim 4 or 5, wherein the rotation shaft includes an auxiliary blade positioned above the stirring blade. ing. Furthermore, the processing apparatus according to a seventh aspect of the present invention is the processing apparatus according to any one of the first to third aspects, wherein the rotating shaft includes an inclined blade positioned inside the stirring blade. Adopted.
 上記のような構成としたことにより、本発明の処理装置は、構造が簡単であるとともに処理物に強い圧縮力や剪断力を与えることが可能であり、粉粒体の複合化やコーティングなどの高度な処理を行うことができる。そして、処理物の流れを制御することが容易であり、最適な処理条件を簡単に見つけることができる。 By adopting the above-described configuration, the processing apparatus of the present invention has a simple structure and can apply a strong compressive force or shearing force to the processed material, such as compounding and coating of powder particles. Advanced processing can be performed. And it is easy to control the flow of a processed material, and the optimal process conditions can be found easily.
 図1は本発明の処理装置の一例を示し、(1)は概略縦断面図、(2)は概略横断面図である。
 図2は図1の処理装置を詳細に示し、(1)は概略縦断面図、(2)は(1)のA部詳細図である。
 図3は本発明の処理装置の他の例を示し、(1)は概略縦断面図、(2)は(1)のB部詳細図、(3)は(2)におけるX−X矢視断面図である。
 図4は本発明の処理装置のさらに他の例を示し、(1)は概略縦断面図、(2)は(1)のC部詳細図である。
 図5は本発明の処理装置のさらに他の例を示し、(1)は概略縦断面図、(2)は概略横断面図である。
 図6は本発明の処理装置のさらに他の例を示し、(1)は概略縦断面図、(2)は(1)のY−Y矢視図である。
 図7は本発明の処理装置のさらに他の例を示し、(1)は概略縦断面図、(2)は概略横断面図である。
 図8は本発明の処理装置で得られた製品のサンプル写真である。
 図9は従来の処理装置で得られた製品のサンプル写真である。
 図10は従来の処理装置の一例を示す概略断面図である。
 図11は従来の処理装置の他の例を示す概略断面図である。
FIG. 1 shows an example of the processing apparatus of the present invention, wherein (1) is a schematic longitudinal sectional view, and (2) is a schematic transverse sectional view.
2 shows the processing apparatus of FIG. 1 in detail, (1) is a schematic longitudinal sectional view, and (2) is a detailed view of part A of (1).
FIG. 3 shows another example of the processing apparatus of the present invention, where (1) is a schematic longitudinal sectional view, (2) is a detailed view of a portion B of (1), and (3) is a view taken along arrows XX in (2). It is sectional drawing.
FIG. 4 shows still another example of the processing apparatus of the present invention, where (1) is a schematic longitudinal sectional view, and (2) is a detail view of part C of (1).
FIG. 5 shows still another example of the processing apparatus of the present invention, wherein (1) is a schematic longitudinal sectional view, and (2) is a schematic transverse sectional view.
FIG. 6 shows still another example of the processing apparatus of the present invention. (1) is a schematic longitudinal sectional view, and (2) is a view taken in the direction of arrows Y-Y in (1).
FIG. 7 shows still another example of the processing apparatus of the present invention, wherein (1) is a schematic longitudinal sectional view, and (2) is a schematic transverse sectional view.
FIG. 8 is a sample photograph of the product obtained with the processing apparatus of the present invention.
FIG. 9 is a sample photograph of a product obtained with a conventional processing apparatus.
FIG. 10 is a schematic sectional view showing an example of a conventional processing apparatus.
FIG. 11 is a schematic sectional view showing another example of a conventional processing apparatus.
 以下、図面に示す本発明の実施の形態について説明する。図1には本発明による処理装置の一実施形態が示され、図1(1)は縦断面図、図1(2)は横断面図である。図2は、図1の詳細説明図であり、図2(1)は縦断面図、図2(2)は(1)のA部詳細図である。
 この処理装置10は、竪型の混合槽20と、混合槽20の槽底を挿通して設けられる回転軸30と、回転軸30に設けられる複数の撹拌羽根40と、混合槽20に固定して設けられる複数の衝突板50を備えている。混合槽20の上部には蓋60を備え、フランジ61で接続されている。なお、蓋60には処理物の投入口が設けられ、混合槽20の槽底には製品の排出口が設けられるが、これらは図に示していない。
 本発明の処理装置10は、混合槽20内に粉粒体の循環流を形成し、これによって混合処理を促進することを特徴としている。すなわち、撹拌羽根40の回転によって粉粒体に慣性力を与え、粉粒体を槽底隅部付近から槽壁に沿って上方へ放出する。粉粒体は、槽壁付近で上昇し槽中心付近で下降することにより、混合槽内に循環流を形成する。
 混合槽20は円筒状に限らず、下部から上部に向って直径が漸次小さくなる形状や、球状などとすることもできる。しかし、何れの形状であっても、混合槽20は回転軸30が略垂直に設けられる竪型に限定される。以下、混合槽20の内部の直径をdとして説明する。そして、混合槽20の直径が高さによって変化する場合には、直径dは最大直径を示すものとする。
 混合槽20が円筒状である場合には、槽底隅部が丸く滑らかに形成されていることが好ましい。これは、撹拌羽根40により慣性力を受けた粉粒体が、滑らかに上方へ向かって放出されるためである。図2(2)に示すように、槽底隅部の丸みにおける曲率半径をRとすると、Rは0.05d以上であることが好ましく、0.1d以上であることがより好ましい。ただし、Rには上限があり、0.5d以下である。
 回転軸30は、混合槽20に対して、図示していないグランドシールやエアシールなどによりシールされている。また、回転軸30は電動機などにより駆動されるが、回転数を可変として設定条件の一つとすることが好ましい。
 処理装置10では、撹拌羽根40は、略円錐状に形成されたボス部41の傾斜面に配置されて回転軸30に取り付けられ、混合槽20の槽底に近接して配置される。撹拌羽根40は、その形状及び数について特に限定されないが、粉粒体に強い慣性力を与え、槽底隅部付近から槽壁に沿って上方へ強く放出することが望まれる。
 粉粒体に与える慣性力を大きくするために、撹拌羽根40の直径Iは、槽底において出来る限り大きな形状であることが好ましい。すなわち、混合槽20が円筒状である場合には、撹拌羽根40の直径Iは、0.7d以上とすることが好ましく、0.85d以上とすることがより好ましい。
 また、本発明の処理装置10は、混合槽20に固定して設けられる複数の衝突板50を備えることを特徴としている。循環流の一部に衝突板50を置くことにより、粉粒体に強い圧縮力及び剪断力を与え、粉粒体の複合化やコーティングなどの処理を行うことができる。処理装置10では、衝突板50は混合槽20の槽壁に溶接されている。
 撹拌羽根40の近傍は、循環流の中でも慣性力が最も強い場所となる。したがって、衝突板50は、撹拌羽根40に近接して置くことが好ましい。図2(2)に隙間e1で示すように、撹拌羽根40と衝突板50との最短距離は、0.1d以下とすることが好ましく、0.01d以下とすることがより好ましい。
 粉粒体に強い慣性力を与えるためには、撹拌羽根40の回転速度は高速であるほど好ましいが、あまり高速であるとコーティングした粒子の剥離、或いはベースとなる母粒子の破壊を起こすことになる。したがって、撹拌羽根40の実用的な先端速度は20~150m/sの範囲であり、好ましく30~100m/sの範囲である。
 衝突板50は、その形状及び数については特に限定されないが、粉粒体の循環流に対して強い衝撃を与えるとともに、粉粒体の循環流を阻害しないようにする必要がある。したがって、その数は4~12枚程度とすることが好ましい。また、その大きさは、図2(2)に示すように、その幅Wが0.05d~0.25dであり、その高さHが0.05d~0.2dであることが好ましい。
 図3には本発明による処理装置の他の実施形態が示され、図3(1)は縦断面図、図3(2)は(1)のB部詳細図、図3(3)は(2)におけるX−X矢視断面図である。
 この処理装置11は、衝突板50を備えた内挿管51が混合槽20内に挿入されている点で処理装置10とは相違している。内挿管51は、その鍔部52が混合槽20のフランジ61に挟み込まれている。したがって、複数の内挿管51を用意することにより、衝突板50の形状などを変えて処理を行うことができる。
 処理装置11を用いて、衝突板50の取付け角度θについて説明する。図3(2)におけるX−X矢視断面を示す図3(3)は、近接して設けられる撹拌羽根40と衝突板50との位置関係を示している。そして、矢印で示す撹拌羽根40の回転方向と、衝突板50の衝突面とがなす角度をθとしている。
 角度θは30度~90度の範囲である。このような角度を設けることにより、粉粒体が衝突板50に衝突したときに、その循環流には混合槽20の底面に向かう力が与えられ、特に強い剪断力が発生する。角度θが90度を超える場合は剪断力が小さくなり、30度未満の場合は循環流を阻害する作用が大きくなる。最適な角度θは、粉粒体の性状によって異なり、流動性の良好な粉粒体では45度~75度、流動性が悪い粉粒体では60度~90度となる。
 図4には本発明による処理装置のさらに他の実施形態が示され、図4(1)は縦断面図、図4(2)は(1)のC部詳細図である。
 この処理装置12の特徴は、衝突板50が、支持部55及び支持環56などによって蓋60に固定されていることである。図示していないが、この構造は、例えば、蓋60に対して支持部55を取外し可能とすることができる。したがって、複数種類の衝突板50を用意して、条件を変えた処理を行うことができる。
 処理装置12では、衝突板50と槽壁の間に隙間e2を設けている。隙間e2を設けることにより、隙間e2部分も循環流路の一部となって処理物が流れることになる。衝突板50に対して処理物が衝突する衝突面の裏側(裏面)には、デッドスペースとなって処理物が付着することがあるが、隙間e2を設けることによりこの問題を解消することができる。e2の値は、通常10mm程度で十分である。
 図5には本発明による処理装置のさらに他の実施形態が示され、図5(1)は縦断面図、図5(2)は横断面図である。
 この処理装置13は、処理装置10と同様に、混合槽20に固定して設けられる複数の衝突板50を備えている。また、処理装置13は、処理装置10と同様に、撹拌羽根40が、略円錐状に形成されたボス部41の傾斜面に配置されているが、さらに、各撹拌羽根40の上部がリング状上板42で連結されている。これによって、リング状上板42とボス部41の傾斜面との間には処理物の流路が形成されることになり、内側から外側に向かって安定した状態で粉粒体が流動することになる。
 図6には本発明による処理装置のさらに他の実施形態が示され、図6(1)は縦断面図、図6(2)は(1)のY−Y矢視図である。
 この処理装置14は、衝突板50が支持部55及び支持環56を備えている点で、処理装置12と類似しているが、上部に鍔部52を備えている点では、処理装置11に類似している。また、処理装置14は、撹拌羽根40が、略円錐状に形成されたボス部41の傾斜面に配置されるとともに、各撹拌羽根40の上部がリング状上板42で連結されている点で処理装置13に類似しているが、さらに、回転軸30が、撹拌羽根40よりも上部に補助羽根45を備えている。
 補助羽根45は、図6(2)に示すように、矢印の方向に回転すると周囲の処理物を混合槽20の中心に引き込む作用を備えている。この結果、補助羽根45は、処理物の循環流を促進することになり、流動性の悪い粉粒体の処理に適している。
 図7には本発明による処理装置のさらに他の実施形態が示され、図7(1)は縦断面図、図7(2)は横断面図である。
 この処理装置15は、撹拌羽根40に特徴を備え、リング状底板43の上面に配列された撹拌羽根40と、ボス部41に設けられる傾斜羽根46を備えている。ここで、傾斜羽根46は、撹拌羽根40の内側に位置するとともに、処理物を掻き込むように傾斜を備えている。したがって、傾斜羽根46は、図7(2)に示すように、矢印の方向に回転すると、混合槽20の中央部で粉粒体を上から下に掻き込んで、処理物の循環流を促進することになる。
 以上のように、本願発明の処理装置は構造が簡単であり、処理物も単純な循環流を形成して処理される。したがって、処理物の流れの特徴を把握することが容易であり、これを制御することも容易である。また、処理条件の変更は、撹拌羽根の形状と回転速度、及び衝突板の形状などによるが、何れも比較的簡単に行うことが可能であり、最適な処理条件を簡単に見つけることができる。
 本願発明の処理装置は非常に広い分野で利用可能と考えられる。例えば、リチウムイオン電池における電極材料として、コバルト酸リチウムにカーボンをコーティングすることが可能である。また、化粧品材料として、ナイロンに二酸化チタンをコーティングすることが可能である。また、無機ガラスの代用として使用されるPMMAの粉に顔料をコーティングすることが可能である。
 また、粉体塗料として、エポキシ樹脂などの粒子表面に顔料をコーティングすることが可能である。また、電池材料として、黒鉛粒子を球形化することが可能である。また、電子印刷用として、トナー粒子の表面に超微粒子シリカや二酸化チタンをコーティングすることが可能である。
Hereinafter, embodiments of the present invention shown in the drawings will be described. FIG. 1 shows an embodiment of a processing apparatus according to the present invention. FIG. 1 (1) is a longitudinal sectional view, and FIG. 1 (2) is a transverse sectional view. 2 is a detailed explanatory view of FIG. 1, FIG. 2 (1) is a longitudinal sectional view, and FIG. 2 (2) is a detailed view of part A of (1).
The processing apparatus 10 is fixed to the bowl-shaped mixing tank 20, a rotating shaft 30 provided through the tank bottom of the mixing tank 20, a plurality of stirring blades 40 provided on the rotating shaft 30, and the mixing tank 20. A plurality of collision plates 50 are provided. A lid 60 is provided at the top of the mixing tank 20 and is connected by a flange 61. The lid 60 is provided with a processed material inlet, and the mixing tank 20 is provided with a product outlet, which is not shown in the figure.
The processing apparatus 10 of the present invention is characterized in that a circulating flow of powder particles is formed in the mixing tank 20, thereby promoting the mixing process. That is, an inertia force is given to the granular material by the rotation of the stirring blade 40, and the granular material is discharged upward along the tank wall from the vicinity of the tank bottom corner. The granular material rises near the tank wall and descends near the tank center, thereby forming a circulating flow in the mixing tank.
The mixing tank 20 is not limited to a cylindrical shape, and may have a shape in which the diameter gradually decreases from the lower part to the upper part, a spherical shape, or the like. However, in any shape, the mixing tank 20 is limited to a vertical shape in which the rotation shaft 30 is provided substantially vertically. Hereinafter, the diameter inside the mixing tank 20 is demonstrated as d. And when the diameter of the mixing tank 20 changes with height, the diameter d shall show a maximum diameter.
When the mixing tank 20 is cylindrical, it is preferable that the bottom corner of the tank is round and smoothly formed. This is because the granular material subjected to the inertial force by the stirring blade 40 is smoothly discharged upward. As shown in FIG. 2 (2), when the radius of curvature at the roundness at the bottom corner of the tank is R, R is preferably 0.05 d or more, and more preferably 0.1 d or more. However, R has an upper limit and is 0.5 d or less.
The rotating shaft 30 is sealed with respect to the mixing tank 20 by a ground seal or an air seal not shown. Moreover, although the rotating shaft 30 is driven by an electric motor or the like, it is preferable that the rotation speed is variable and is set as one of setting conditions.
In the processing apparatus 10, the stirring blade 40 is disposed on the inclined surface of the boss portion 41 formed in a substantially conical shape, is attached to the rotary shaft 30, and is disposed in the vicinity of the tank bottom of the mixing tank 20. The shape and number of the stirring blades 40 are not particularly limited, but it is desirable that the stirring blades 40 give a strong inertial force to the powder and strongly release upward from the vicinity of the bottom of the tank along the tank wall.
In order to increase the inertial force applied to the powder body, the diameter I of the stirring blade 40 is preferably as large as possible at the bottom of the tank. That is, when the mixing tank 20 is cylindrical, the diameter I of the stirring blade 40 is preferably 0.7 d or more, and more preferably 0.85 d or more.
Moreover, the processing apparatus 10 of this invention is equipped with the some collision board 50 fixed to the mixing tank 20, and is characterized by the above-mentioned. By placing the impingement plate 50 in a part of the circulating flow, it is possible to apply a strong compressive force and shearing force to the granular material, and to perform processing such as compounding and coating of the granular material. In the processing apparatus 10, the collision plate 50 is welded to the tank wall of the mixing tank 20.
The vicinity of the stirring blade 40 is a place having the strongest inertial force in the circulating flow. Therefore, it is preferable to place the collision plate 50 close to the stirring blade 40. As indicated by a gap e1 in FIG. 2 (2), the shortest distance between the stirring blade 40 and the collision plate 50 is preferably 0.1 d or less, and more preferably 0.01 d or less.
In order to give a strong inertial force to the granular material, the rotational speed of the stirring blade 40 is preferably as high as possible. However, if the rotational speed is too high, the coated particles may be peeled off or the base particles as a base may be destroyed. Become. Therefore, the practical tip speed of the stirring blade 40 is in the range of 20 to 150 m / s, and preferably in the range of 30 to 100 m / s.
The shape and number of the collision plates 50 are not particularly limited, but it is necessary to give a strong impact to the circulating flow of the granular material and not to disturb the circulating flow of the granular material. Therefore, the number is preferably about 4 to 12. Further, as shown in FIG. 2 (2), the width W is preferably 0.05d to 0.25d and the height H is preferably 0.05d to 0.2d.
FIG. 3 shows another embodiment of the processing apparatus according to the present invention. FIG. 3 (1) is a longitudinal sectional view, FIG. 3 (2) is a detailed view of part B of FIG. It is XX arrow sectional drawing in 2).
The processing apparatus 11 is different from the processing apparatus 10 in that an inner intubation 51 including a collision plate 50 is inserted into the mixing tank 20. The flange 52 of the inner tube 51 is sandwiched between the flanges 61 of the mixing tank 20. Therefore, by preparing a plurality of intubation tubes 51, it is possible to perform processing while changing the shape of the collision plate 50 and the like.
The mounting angle θ of the collision plate 50 will be described using the processing device 11. FIG. 3 (3) showing a cross section taken along the line XX in FIG. 3 (2) shows the positional relationship between the stirring blade 40 and the collision plate 50 that are provided close to each other. The angle between the rotation direction of the stirring blade 40 indicated by the arrow and the collision surface of the collision plate 50 is defined as θ.
The angle θ ranges from 30 degrees to 90 degrees. By providing such an angle, when the granular material collides with the collision plate 50, a force toward the bottom surface of the mixing tank 20 is given to the circulating flow, and a particularly strong shearing force is generated. When the angle θ exceeds 90 degrees, the shearing force decreases, and when it is less than 30 degrees, the effect of inhibiting the circulation flow increases. The optimum angle θ varies depending on the properties of the powder and is 45 ° to 75 ° for a powder having good fluidity and 60 ° to 90 ° for a powder having poor fluidity.
FIG. 4 shows still another embodiment of the processing apparatus according to the present invention. FIG. 4 (1) is a longitudinal sectional view, and FIG. 4 (2) is a detailed view of part C of (1).
The processing device 12 is characterized in that the collision plate 50 is fixed to the lid 60 by a support portion 55 and a support ring 56. Although not shown, this structure can make the support part 55 removable with respect to the lid | cover 60, for example. Therefore, it is possible to prepare a plurality of types of collision plates 50 and perform processing with different conditions.
In the processing apparatus 12, a gap e2 is provided between the collision plate 50 and the tank wall. By providing the gap e <b> 2, the gap e <b> 2 part also becomes a part of the circulation flow path and the processed material flows. On the back side (back side) of the collision surface where the processed object collides with the collision plate 50, the processed object may become a dead space, but this problem can be solved by providing the gap e2. . A value of about 10 mm is usually sufficient for e2.
FIG. 5 shows still another embodiment of the processing apparatus according to the present invention. FIG. 5 (1) is a longitudinal sectional view and FIG. 5 (2) is a transverse sectional view.
Similar to the processing apparatus 10, the processing apparatus 13 includes a plurality of collision plates 50 that are fixed to the mixing tank 20. Further, in the processing device 13, as in the processing device 10, the stirring blade 40 is disposed on the inclined surface of the boss portion 41 formed in a substantially conical shape, and the upper portion of each stirring blade 40 is further ring-shaped. The upper plate 42 is connected. As a result, a flow path for the processed material is formed between the ring-shaped upper plate 42 and the inclined surface of the boss portion 41, and the powder particles flow stably from the inside toward the outside. become.
FIG. 6 shows still another embodiment of the processing apparatus according to the present invention. FIG. 6 (1) is a longitudinal sectional view, and FIG. 6 (2) is a view taken in the direction of arrows YY of (1).
This processing device 14 is similar to the processing device 12 in that the collision plate 50 includes a support portion 55 and a support ring 56, but is different from the processing device 11 in that the upper portion includes a flange portion 52. It is similar. Further, the processing device 14 is such that the stirring blades 40 are arranged on the inclined surface of the boss portion 41 formed in a substantially conical shape, and the upper portions of the stirring blades 40 are connected by the ring-shaped upper plate 42. Although it is similar to the processing apparatus 13, the rotating shaft 30 further includes an auxiliary blade 45 above the stirring blade 40.
As shown in FIG. 6 (2), the auxiliary blade 45 has an action of drawing the surrounding processed material into the center of the mixing tank 20 when rotated in the direction of the arrow. As a result, the auxiliary blade 45 promotes the circulation flow of the processed material, and is suitable for processing a granular material having poor fluidity.
FIG. 7 shows still another embodiment of the processing apparatus according to the present invention. FIG. 7 (1) is a longitudinal sectional view, and FIG. 7 (2) is a transverse sectional view.
The processing device 15 is characterized by the stirring blade 40 and includes a stirring blade 40 arranged on the upper surface of the ring-shaped bottom plate 43 and an inclined blade 46 provided on the boss portion 41. Here, the inclined blades 46 are located inside the stirring blades 40 and have an inclination so as to scrape the processed material. Therefore, as shown in FIG. 7B, when the inclined blade 46 rotates in the direction of the arrow, the granular material is scraped from the top to the bottom at the center of the mixing tank 20 to promote the circulation flow of the processed material. Will do.
As described above, the processing apparatus of the present invention has a simple structure, and the processed material is processed by forming a simple circulating flow. Therefore, it is easy to grasp the characteristics of the flow of the processed material, and it is easy to control this. Moreover, although the change of the processing conditions depends on the shape and rotation speed of the stirring blades and the shape of the collision plate, all can be performed relatively easily, and the optimal processing conditions can be easily found.
The processing apparatus of the present invention is considered to be usable in a very wide field. For example, as an electrode material in a lithium ion battery, it is possible to coat lithium cobaltate with carbon. Moreover, it is possible to coat nylon with titanium dioxide as a cosmetic material. It is also possible to coat a pigment on PMMA powder used as a substitute for inorganic glass.
Further, as a powder coating material, it is possible to coat a pigment on the surface of particles such as an epoxy resin. Moreover, it is possible to spheroidize graphite particles as a battery material. For electronic printing, it is possible to coat the surface of toner particles with ultrafine silica or titanium dioxide.
 図8は、処理装置10で処理された製品の顕微鏡写真である。処理物は、平均粒径約5μmの架橋PMMA(70%)と二酸化チタン(30%)との混合物である。図9は、衝突板を備えない従来の処理装置で処理された製品の顕微鏡写真であり、処理物は同じである。両者の比較により、衝突板の効果が明確に示されている。すなわち、図8では、全ての粒子が球形であるとともに、その表面が滑らかに処理されている。これに対して、図9では、粒子の形状が必ずしも球形ではなく、その表面が粗い状態に止まっている。 FIG. 8 is a photomicrograph of the product processed by the processing apparatus 10. The treated product is a mixture of crosslinked PMMA (70%) and titanium dioxide (30%) having an average particle size of about 5 μm. FIG. 9 is a photomicrograph of a product processed by a conventional processing apparatus that does not include a collision plate, and the processed product is the same. By comparing the two, the effect of the collision plate is clearly shown. That is, in FIG. 8, all the particles are spherical, and the surface is processed smoothly. On the other hand, in FIG. 9, the shape of the particles is not necessarily spherical, and the surface remains rough.
10、11、12、13、14、15、110、210  処理装置
20、120、220  混合槽
30、130、230  回転軸
40、140、240  撹拌羽根
41  ボス部
42  リング状上板
43  リング状底板
45  補助羽根
46  傾斜羽根
50  衝突板
51  内挿管
52  鍔部
55  支持部
56  支持環
60  蓋
61  フランジ
191  投入口
192  排出口
193、293  ジャケット
281  回転体
282  開口
283  プレスヘッド
10, 11, 12, 13, 14, 15, 110, 210 Processing device 20, 120, 220 Mixing tank 30, 130, 230 Rotating shaft 40, 140, 240 Stirrer blade 41 Boss portion 42 Ring-shaped top plate 43 Ring-shaped bottom plate 45 Auxiliary blade 46 Inclined blade 50 Collision plate 51 Inner tube 52 Gutter 55 Support portion 56 Support ring 60 Cover 61 Flange 191 Input port 192 Discharge port 193, 293 Jacket 281 Rotating body 282 Opening 283 Press head

Claims (7)

  1.  竪型の混合槽と、前記混合槽の槽底を挿通して設けられる回転軸と、
     前記回転軸に設けられる複数の撹拌羽根と、
     前記混合槽に固定して設けられる複数の衝突板とを備える粉粒体の処理装置であって、
     前記混合槽の直径をdとするとき、前記撹拌羽根と前記衝突板との最短距離が0.1d以下であることを特徴とする処理装置。
    A bowl-shaped mixing tank, and a rotary shaft provided through the tank bottom of the mixing tank;
    A plurality of stirring blades provided on the rotating shaft;
    A processing apparatus for a granular material comprising a plurality of collision plates fixedly provided in the mixing tank,
    When the diameter of the mixing tank is d, the shortest distance between the stirring blade and the collision plate is 0.1 d or less.
  2.  前記衝突板の大きさは、前記混合槽の直径をdとするとき、幅が0.05d~0.25dであり、高さが0.05d~0.2dであることを特徴とする請求項1に記載の処理装置。 The impact plate has a width of 0.05d to 0.25d and a height of 0.05d to 0.2d, where d is the diameter of the mixing tank. The processing apparatus according to 1.
  3.  前記混合槽が円筒状であって槽底隅部が丸く滑らかに形成され、前記混合槽の直径をdとするとき、その曲率半径が0.05d以上であることを特徴とする請求項1又は2に記載の処理装置。 2. The mixing tank according to claim 1, wherein the mixing tank has a cylindrical shape, the bottom corner of the tank is round and smoothly formed, and when the diameter of the mixing tank is d, the radius of curvature is 0.05 d or more. 2. The processing apparatus according to 2.
  4.  前記撹拌羽根が、略円錐状に形成されたボス部の傾斜面に配列されていることを特徴とする請求項1乃至3の何れかに記載の処理装置。 The processing apparatus according to any one of claims 1 to 3, wherein the stirring blades are arranged on an inclined surface of a boss portion formed in a substantially conical shape.
  5.  前記撹拌羽根の上部がリング状上板で連結され、該リング状上板と前記傾斜面との間を、内側から外側に向かって粉粒体が流動することを特徴とする請求項4に記載の処置装置。 The upper part of the stirring blade is connected by a ring-shaped upper plate, and the granular material flows between the ring-shaped upper plate and the inclined surface from the inside toward the outside. Treatment device.
  6.  前記回転軸が、前記撹拌羽根よりも上部に位置する補助羽根を備えていることを特徴とする請求項4又は5に記載の処理装置。 The processing apparatus according to claim 4 or 5, wherein the rotating shaft includes an auxiliary blade positioned above the stirring blade.
  7.  前記回転軸が、前記撹拌羽根の内側に位置する傾斜羽根を備えていることを特徴とする請求項1乃至3の何れかに記載の処理装置。 The processing apparatus according to any one of claims 1 to 3, wherein the rotation shaft includes an inclined blade located inside the stirring blade.
PCT/JP2010/067309 2009-10-02 2010-09-27 Processing device WO2011040620A1 (en)

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JP2014202964A (en) * 2013-04-05 2014-10-27 キヤノン株式会社 Toner processing device
JP2014202966A (en) * 2013-04-05 2014-10-27 キヤノン株式会社 Toner processing device
JP2014202965A (en) * 2013-04-05 2014-10-27 キヤノン株式会社 Toner processing device
JP2016038460A (en) * 2014-08-07 2016-03-22 キヤノン株式会社 Processing device for toner and toner manufacturing method
CN113117564A (en) * 2021-05-15 2021-07-16 龙从新 Antiseized agitated vessel of epoxy
CN115960580A (en) * 2023-01-19 2023-04-14 深圳市东信硅材料有限公司 Flame-retardant sealant for new energy automobile and preparation process thereof
CN116272811A (en) * 2023-04-21 2023-06-23 英德市新联化工有限公司 Water-based acrylic resin emulsion synthesis reaction device

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