WO2014102906A1 - 攪拌処理装置及び処理方法 - Google Patents
攪拌処理装置及び処理方法 Download PDFInfo
- Publication number
- WO2014102906A1 WO2014102906A1 PCT/JP2012/083502 JP2012083502W WO2014102906A1 WO 2014102906 A1 WO2014102906 A1 WO 2014102906A1 JP 2012083502 W JP2012083502 W JP 2012083502W WO 2014102906 A1 WO2014102906 A1 WO 2014102906A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- fluid
- stirring
- flow
- screen
- outside
- Prior art date
Links
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/40—Static mixers
- B01F25/44—Mixers in which the components are pressed through slits
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/40—Mixers with rotor-rotor system, e.g. with intermeshing teeth
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/40—Mixing liquids with liquids; Emulsifying
- B01F23/41—Emulsifying
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
- B01F27/81—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis the stirrers having central axial inflow and substantially radial outflow
- B01F27/811—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis the stirrers having central axial inflow and substantially radial outflow with the inflow from one side only, e.g. stirrers placed on the bottom of the receptacle, or used as a bottom discharge pump
- B01F27/8111—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis the stirrers having central axial inflow and substantially radial outflow with the inflow from one side only, e.g. stirrers placed on the bottom of the receptacle, or used as a bottom discharge pump the stirrers co-operating with stationary guiding elements, e.g. surrounding stators or intermeshing stators
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
- B01F27/84—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with two or more stirrers rotating at different speeds or in opposite directions about the same axis
Definitions
- the present invention relates to an agitation processing apparatus and a processing method, and more particularly to a processing apparatus and a processing method for immersing an agitation chamber in a fluid and applying a shearing force to the fluid.
- Patent Documents 1 and 2 relate to a processing device that immerses the stirring chamber in a fluid and applies a shearing force to the fluid. Further, as disclosed in Patent Document 3, various methods for producing toner using this apparatus have been proposed.
- the agitation processing apparatus includes an agitation chamber disposed in a fluid to be processed, and a rotary blade disposed in the agitation chamber, and the agitation chamber is configured to cause the fluid to flow from the outside by rotation of the rotary blade. And a discharge port for discharging the fluid from the inside to the outside by the rotation of the rotary blades at positions adjacent to each other in the axial direction of the rotary blades. And the said rotary blade performs the process which applies a shear force with respect to the said fluid by rotating at high speed inside the stirring chamber.
- the shearing force is applied to the fluid between the rotating blades, so that the fluid is emulsified, dispersed or mixed. Can be processed.
- Patent Document 3 there is a difference between an angle formed by the direction in which the fluid is introduced into the stirring chamber and the rotation axis of the stirring blade, and an angle formed by the discharge direction from the stirring chamber and the rotation shaft of the stirring blade. It is proposed to be within a range of ⁇ 25 degrees. Thus, when both angles are changed, the suction flow and the discharge flow may interfere with each other regardless of the viscosity of the fluid.
- the present invention comprises a stirring blade provided with a stirring blade rotating at high speed and a screen provided so as to surround the stirring blade, and the stirring chamber is disposed in a fluid to be processed,
- the stirring processing device in which at least one of the screen and the stirring blade is rotated, the screen and the stirring blade are rotated relative to each other, and a shearing force is applied to the fluid.
- the present invention can be carried out on the assumption that the suppressing body protrudes from the tip side of the stirring chamber.
- the present invention can be implemented as the suppressor that moves away from the discharge port in the rotation axis direction of the relative rotation as it goes from the proximal end side to the distal end side.
- the present invention can be implemented on the assumption that the suppressor is continuous in the circumferential direction.
- the suppressor has a cylindrical shape, and the tip end side is away from the discharge port in the direction of the rotation axis of the relative rotation beyond the suction port. be able to.
- the present invention includes an introduction fin for guiding the fluid by rotating, and in the direction of the rotation axis of the relative rotation, the end portion on the distal end side of the suppressing body is closest to the suction port.
- the present invention can be carried out assuming that the position is farther from the suction port than the end of the fin.
- the present invention includes a stirring chamber and a stirring blade disposed in the stirring chamber, and the stirring chamber includes a suction port and a discharge port at positions adjacent to each other in the axial direction of the stirring blade.
- the stirring chamber is disposed in the fluid, and at least one of the screen and the stirring blade is rotated.
- a suppressor that restricts the flow of the fluid is disposed between the suction flow that is the flow of the fluid to the discharge flow and the discharge flow that is the flow of the fluid discharged to the outside from the discharge port, and the suction flow
- the stirring device includes an introduction fin for guiding the fluid by rotating, and the suppression body guides the introduction flow of the fluid by the rotation of the introduction fin to the suction port.
- the present invention can be implemented as the fluid contains a toner raw material composition.
- the present invention has been able to provide an agitation processing apparatus and an agitation processing method that can realize good fluid processing regardless of the properties of the fluid.
- the stirring treatment apparatus has a stirring chamber 18 in a processing tank 11 containing a fluid to be processed. It is arranged to perform a fluid stirring process.
- the treatment tank 11 has a lid 12 that is detachably disposed at the open upper end.
- upper, lower, left, and right only indicate relative positions, and do not specify absolute positions.
- the stirring chamber 18 is provided with a suction chamber 19 in the upper part and a shear chamber 20 in the lower part in this example.
- the two are partitioned by a partition wall 21, but an opening is provided at the center of the partition wall 21, so that fluid can be sufficiently conducted between the suction chamber 19 and the shear chamber 20.
- the suction chamber 19 includes at least one suction port 24, and the shear chamber 20 includes at least one discharge port 25.
- the outer wall of the shear chamber 20 is constituted by the screen 23, and the slit provided in the screen 23 constitutes the discharge port 25, but a separate wall member is provided outside the screen 23,
- the discharge port 25 may be formed in the wall member.
- the stirring chamber 18 is provided with a stirring blade 22 that rotates at a high speed in the interior thereof, in particular in the shear chamber 20 in this example, and between the stirring blade 22 and a screen 23 that rotates in the opposite direction, A shearing force is applied to the fluid (see FIG. 2B).
- This makes it possible to increase the relative rotational speed between the stirring blade 22 and the inner wall of the screen 23.
- the screen 23 is moved in the reverse direction. By rotating, it is possible to increase the relative rotational speed between the stirring blade 22 and the inner wall of the screen 23 in a state where cavitation is not generated, thereby increasing the shear strength, the amount of energy, the number of passes, and the processing capacity.
- the stirring blade 22 is rotated by the first shaft 13, and the screen 23 is rotated in the reverse direction by the second shaft 14. Both the first shaft 13 and the second shaft 14 extend in the vertical direction.
- the second shaft 14 is a hollow cylindrical shaft, and the first shaft 13 is rotatably inserted into the second shaft 14.
- the first shaft 13 and the second shaft 14 are rotated by a rotational drive source (not shown) such as an electric motor provided on the top of the lid 12. It is preferable that both rotation speeds can be variably controlled by an inverter or the like. These rotational speeds can be appropriately changed within a range in which the fluid can be sheared.
- the stirring chamber 18 is provided at the lower end of the second shaft 14, and the suction chamber 19, the shear chamber 20, and the screen 23 rotate together.
- the introduction fin 16 can be provided in the portion of the second shaft 14 above the stirring chamber 18, but as shown in FIG. It is also possible to carry out without providing 16.
- the introduction fins 16 are formed in a spiral shape on the outer periphery of the second shaft 14, and are rotated together with the second shaft 14 to generate an induced flow 28 that sends the fluid above the processing tank 11 downward.
- circulation fins 17 are provided.
- the circulation fins 17 are provided outside the introduction fins 16 and rotate together with the second shaft 14 and the introduction fins 16.
- the circulation fins 17 extend in a spiral shape in the opposite direction to the introduction fins 16, and generate a circulation flow 29 that sends the fluid in the treatment tank 11 upward from below.
- the fluid in the processing tank 11 is repeatedly circulated up and down by the induction flow 28 and the circulation flow 29, and the shearing treatment by the stirring chamber 18 is performed in the repetition.
- the stirring blade 22 rotates in the direction opposite to the screen 23, whereby fluid is sucked into the stirring chamber 18 from the suction port 24 (suction flow 26), and from the discharge port 25 to the stirring chamber 18. Discharged outward (discharge flow 27).
- the suction flow 26 that has entered from the suction port 24 enters the suction chamber 19 at one end, and is sucked into the lower shear chamber 20 from the opening provided in the center of the partition wall 21.
- a shearing process is performed between the agitating blade 22 and the screen 23 described above, and the processed fluid is discharged from the discharge port 25.
- the present invention is characterized in that in the above apparatus, interference between the suction flow 26 and the discharge flow 27 before and after the shearing process is suppressed.
- the suction port 24 disposed above and the discharge port 25 below the suction port 24 and the rotation shaft direction (hereinafter simply referred to as the rotation shaft direction of the first shaft 13).
- the suppression body 31 is formed.
- the suppressing body 31 in this example has a cylindrical shape having a distal end opening 34 on the upper side, and the base end side 32 is fixed to the outer wall of the stirring chamber 18 between the suction port 24 and the discharge port 25.
- the tip side 33 protrudes outside the stirring chamber 18. More specifically, it moves away from the lower discharge port 25 in the rotation axis direction as it goes outward.
- the suppressing body 31 in this example has a substantially inverted truncated cone shape that increases in diameter toward the upper tip side 33.
- the distal end side 33 of the suppressing body 31 extends upward beyond the suction port.
- the introduction fin 16 described above extends spirally from above to below around the second shaft 14, and the tip (lower end) reaches the vicinity of the suction port 24. As a result, the lower end side of the introduction fin 16 enters the inside of the suppressing body 31 from the tip opening 34 of the cylindrical suppressing body 31.
- the end portion (upper end) on the distal end side 33 of the suppressing body 31 is positioned above the end portion on the distal end side (lower end side) of the introduction fin 16.
- the induced flow 28 by the introduction fin 16 is introduced into the cylindrical suppressing body 31 and is smoothly sucked into the suction port 24 without receiving interference from the discharge flow 27. Therefore, even when the viscosity of the fluid is high, the fluid becomes a good suction flow 26 and is sucked from the suction port 24, and the above-described shearing process is continuously performed satisfactorily.
- the suppressing body 31 rotates at a high speed together with the stirring chamber 18, but the rotation of the fluid flows when the shape of the suppressing body 31 in the cross section intersecting the rotation axis is circular.
- the cross section does not prevent the cross section from being implemented in a shape other than a circle, such as a polygonal shape.
- the top end opening 34 of the upper end of the suppressing body 31 is stopped until it reaches substantially the same height as the upper end of the suction port 24.
- the suppressing body 31 27, while guiding interference to the suction port 24.
- the suppressor 31 of the present invention is continuous in the circumferential direction, it can be divided into a plurality of suppressors 31 in plan view as shown in FIG.
- the suppressor 31 of the present invention can be implemented so as to extend downward (in the direction of the discharge port 25) from the proximal end 32 toward the distal end 33 in the rotational axis direction.
- FIG. 5 shows still another example, and in this example, an auxiliary wing 35 is provided outside the cylindrical suppressing body 31.
- the auxiliary wing 35 rotates together with the suppressing body 31 to perform the action of stirring the fluid inside the processing tank 11 (particularly, near the bottom) while moving upward.
- one auxiliary blade 35 can be implemented, it is preferable to provide a plurality of auxiliary blades.
- the stirring treatment device remains immersed in the fluid of the treatment tank 11 and does not move as a whole.
- the first shaft 13 and the second shaft 14 and their driving means are mounted on a rotating body 36 above the processing tank 11, and the rotating body 36 is rotated by the third shaft 15, whereby the processing tank 11 orbiting.
- FIG. 6 shows still another example.
- the rotation driving means of the second shaft 14 for rotating the screen 23 is provided at the bottom of the processing tank 11.
- shaft 14 is penetrated upwards from a bottom part, and it rotates while supporting the screen 23 from the downward direction.
- shaft 13 which rotates the stirring blade 22 is extended above the processing tank 11, and is rotated by the rotational drive means provided above similarly to the previous example.
- the suction chamber 19 provided with the suction port 24 is not rotated, and the stirring blade 22 and the screen 23 stop rotating in opposite directions. Therefore, when the suppression body 31 is fixed to the suction chamber 19 side, it can be implemented as non-rotating, and when it is fixed to the screen 23 side, it can be implemented as rotating.
- the present invention can be implemented with various modifications.
- the angle between the suction port 24 and the discharge port 25 is set upward for the suction port 24 and downward for the discharge port 25, respectively.
- the suction flow 26 is introduced obliquely downward from above, and the discharge flow 27 is discharged obliquely downward from below the suppressor.
- these angles may be changed in various ways. Can do. For example, both can be carried out substantially horizontally (in a direction substantially orthogonal to the rotation axis direction). Even in this case, the suppressing body 31 is disposed between the suction port 24 and the discharge port 25. Thus, interference between the suction flow 26 and the discharge flow 27 can be suppressed.
- the suppressing body 31 is supported by the stirring chamber 18, but can also be supported by the second shaft 14 and can be supported by the processing tank 11 and the lid body 12.
- the stirring blade 22 and the screen 23 were rotated in the mutually reverse direction, you may rotate only any one among both. In other words, it is sufficient if the stirring blade 22 and the screen 23 are rotated relative to each other so that a shearing force can be applied to the fluid.
- Fluids to be treated include liquids containing synthetic resin such as toner particles and metal particles, liquids containing no particles, two kinds of fluids such as oil and moisture, etc., and emulsification, dispersion or mixing treatment is required. It can be used for various fluids.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Dispersion Chemistry (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
- Developing Agents For Electrophotography (AREA)
Abstract
Description
第2軸14の下端には、上記の攪拌室18が設けられており、吸入室19、せん断室20、スクリーン23が一体となって回転する。
具体的には、上方に配置された吸入口24と、これと回転軸方向(以下、単に回転軸方向という時には第1軸13の回転軸方向を意味する)に隣合う下方に吐出口25との間に、抑制体31を形成する。この例における抑制体31は、上方に先端開口34を有する筒状をなしており、その基端側32が吸入口24と吐出口25との間の攪拌室18の外壁に固定されている。そして、先端側33が攪拌室18の外側に突出しているものである。より具体的には、外方向に向かうに従って、回転軸方向における下方の吐出口25から、上方に遠ざかるものである。従って、この例における抑制体31は、上方の先端側33に向かうに従って、径が大きくなる略逆円錐台形状の筒状をなしている。特に、この例では、抑制体31の先端側33は、前記吸入口を越えて、上方に伸びている。他方、前述の導入フィン16は第2軸14の回りに上方から下方に螺旋状に伸びており、その先端(下端)は、吸入口24付近にまで達している。その結果、導入フィン16の下端側は筒状の抑制体31の先端開口34から、抑制体31の内部に入り込んでいる。言い換えれば、回転軸方向において、抑制体31の先端側33の端部(上端)は、導入フィン16の先端側(下端側)の端部よりも、上方に位置している。これによって、導入フィン16による誘導流28は、筒状の抑制体31内に導入され、吐出流27からの干渉を受けることなく、円滑に吸入口24内に吸入される。そのため、流体の粘度が高い場合にあっても、流体は、良好な吸入流26となって、吸入口24から吸入され、前記のせん断処理が良好に継続的に行なわれる。
本発明の抑制体31は、周方向に連続していることが望ましいが、図4(B)に示すように、平面視複数の抑制体31に分割することもできる。
13 第1軸
14 第2軸
15 第3軸
16 導入フィン
17 循環フィン
18 攪拌室
19 吸入室
20 せん断室
22 攪拌羽根
23 スクリーン
24 吸入口
25 吐出口
26 吸入流
27 吐出流
28 誘導流
29 循環流
31 抑制体
32 基端側
33 先端側
35 補助翼
Claims (9)
- 高速回転する攪拌羽根と、前記攪拌羽根を囲うように設けられたスクリーンとを備えた攪拌室とを備え、
前記攪拌室が処理を予定する流体内に配された状態で、前記スクリーンと前記攪拌羽根との少なくとも何れか一方が回転することによって、前記スクリーンと前記攪拌羽根とが相対的回転をなし前記流体に対してせん断力を加える処理をなす攪拌処理装置において、
前記撹拌室は、前記流体を外部から内部へ吸入する吸入口と、前記相対的回転によって前記流体を内部から外部へ吐出する吐出口とを、前記相対的回転の回転軸方向に異なる位置に備え、
前記吸入口と前記吐出口との間に前記流体の流れを規制する抑制体を備え、
前記抑制体は、外部から前記吸入口への前記流体の流れである吸入流と、前記吐出口から外部に吐出した前記流体の流れである吐出流との間に介在し、前記吸入流と前記吐出流との干渉を抑制するものであることを特徴とする攪拌処理装置。 - 前記抑制体は、その先端側が前記攪拌室の外側に突出するものであることを特徴とする請求項1記載の攪拌処理装置。
- 前記抑制体は、基端側から前記先端側に向かうに従って、前記相対的回転の回転軸方向において前記吐出口から遠ざかるものであることを特徴とする請求項2記載の攪拌処理装置。
- 前記抑制体は、周方向に連続するものであることを特徴とする請求項1~3の何れかに記載の攪拌処理装置。
- 前記抑制体は、筒状をなしており、
前記先端側が、前記吸入口を越えて、前記相対的回転の回転軸方向において前記吐出口から遠ざかるものであることを特徴とする請求項3記載の攪拌処理装置。 - 回転することによって前記流体を導くための導入フィンを備え、
前記相対的回転の回転軸方向において、前記抑制体の先端側の端部が、前記吸入口に最も近い前記導入フィンの端部よりも、前記吸入口から遠い位置にあることを特徴とする請求項1~5の何れかに記載の攪拌処理装置。 - 撹拌室と、前記撹拌室内に配置された攪拌羽根とを備え、
前記撹拌室は、吸入口と、吐出口とを、前記攪拌羽根の軸方向へ隣り合う位置に備えると共に、複数のスリットを有するスクリーンを備えた攪拌装置を用いて、流体の攪拌を行う処理方法において、
前記攪拌室を、流体内に配置し、
前記スクリーンと前記攪拌羽根との少なくとも何れか一方を回転させて、前記スクリーンと前記攪拌羽根とに相対的回転を行なわせることにより、前記流体を前記攪拌室の外部から内部へ吸入すると共に、前記流体を前記吐出口から外部へ吐出する流体移動工程と、
前記流体移動工程中の前記相対的回転により、前記攪拌羽根と前記スクリーンとの間で前記流体に対してせん断力を加えるせん断処理工程とを備え、
外部から前記吸入口への前記流体の流れである吸入流と、前記吐出口から外部に吐出した前記流体の流れである吐出流との間に、前記流体の流れを規制する抑制体を配置し、前記吸入流と前記吐出流との干渉を抑制することを特徴とする攪拌処理方法。 - 前記攪拌装置は、回転することによって前記流体を導くための導入フィンを備え、
前記抑制体によって、前記導入フィンの回転による前記流体の導入流を、前記吸入口に案内させることを特徴とする請求項7記載の攪拌処理方法。 - 前記流体がトナーの原料組成物を含むことを特徴とする請求項7又は8記載の攪拌処理方法。
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020157012145A KR20150100629A (ko) | 2012-12-25 | 2012-12-25 | 교반 처리 장치 및 처리 방법 |
CN201280077578.6A CN104853836B (zh) | 2012-12-25 | 2012-12-25 | 搅拌处理装置和处理方法 |
JP2014553916A JP6207091B2 (ja) | 2012-12-25 | 2012-12-25 | 攪拌処理装置及び処理方法 |
EP12891151.8A EP2939734B1 (en) | 2012-12-25 | 2012-12-25 | Stirring device and method |
PCT/JP2012/083502 WO2014102906A1 (ja) | 2012-12-25 | 2012-12-25 | 攪拌処理装置及び処理方法 |
US14/655,291 US9925503B2 (en) | 2012-12-25 | 2012-12-25 | Stirring-processing apparatus and processing method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/JP2012/083502 WO2014102906A1 (ja) | 2012-12-25 | 2012-12-25 | 攪拌処理装置及び処理方法 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2014102906A1 true WO2014102906A1 (ja) | 2014-07-03 |
Family
ID=51020066
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP2012/083502 WO2014102906A1 (ja) | 2012-12-25 | 2012-12-25 | 攪拌処理装置及び処理方法 |
Country Status (6)
Country | Link |
---|---|
US (1) | US9925503B2 (ja) |
EP (1) | EP2939734B1 (ja) |
JP (1) | JP6207091B2 (ja) |
KR (1) | KR20150100629A (ja) |
CN (1) | CN104853836B (ja) |
WO (1) | WO2014102906A1 (ja) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110917917A (zh) * | 2019-12-13 | 2020-03-27 | 武汉工程大学 | 一种印刷用原料筛选搅拌装置 |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
NL2011600C2 (nl) * | 2013-10-11 | 2015-04-14 | Pharmafilter B V | Werkwijze en inrichting voor het vermalen van afval. |
EP3275534B1 (en) * | 2015-03-24 | 2020-04-22 | M. Technique Co., Ltd. | Stirrer |
CN108884178B (zh) * | 2016-03-23 | 2021-06-04 | 日立化成株式会社 | 反应装置、以及树脂粒子、导电性粒子、各向异性导电材料和连接结构体的制造方法 |
CN106268410A (zh) * | 2016-08-17 | 2017-01-04 | 福建农林大学 | 一种混匀器 |
KR102277767B1 (ko) * | 2017-09-07 | 2021-07-15 | 주식회사 엘지화학 | 반응기 |
DE202018102804U1 (de) * | 2018-05-18 | 2019-08-22 | Symex Gmbh & Co. Kg | Vorrichtung zum Homogenisieren fließfähiger Stoffe |
JP6601862B1 (ja) * | 2019-04-15 | 2019-11-06 | エム・テクニック株式会社 | 攪拌機 |
CN114097856B (zh) * | 2021-11-26 | 2023-07-18 | 厚德食品股份有限公司 | 一种冷冻芝士蛋饼的制备方法及其生产设备 |
CN118356695B (zh) * | 2024-06-20 | 2024-08-27 | 福建省蓝深环保技术股份有限公司 | 一种装配式玻璃钢污水处理池 |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04114724A (ja) | 1990-09-01 | 1992-04-15 | M Technic Kk | 攪拌機 |
JPH04114725A (ja) | 1990-09-01 | 1992-04-15 | M Technic Kk | 撹拌機及び流体の撹拌方法 |
JP2004528973A (ja) * | 2001-04-19 | 2004-09-24 | アンノバ・アンビロンヌマン | 処理容器内の液体を攪拌および曝気するための装置 |
JP2006221023A (ja) * | 2005-02-14 | 2006-08-24 | Canon Inc | トナーの製造方法 |
JP2011123236A (ja) | 2009-12-10 | 2011-06-23 | Canon Inc | トナーの製造方法 |
Family Cites Families (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2875897A (en) * | 1953-06-22 | 1959-03-03 | Booth Lionel Earl | Flotation machine |
US3393802A (en) * | 1964-02-03 | 1968-07-23 | Denver Equip Co | Aerating assembly for froth flotation cells |
DE2702183A1 (de) | 1977-01-20 | 1978-07-27 | Ystral Gmbh Maschinenbau Und P | Misch- und dispergiervorrichtung |
FR2466271A1 (fr) | 1979-10-05 | 1981-04-10 | Trailigaz | Dispositif pour melanger deux fluides, notamment de l'air ozone avec de l'eau |
US4570863A (en) * | 1983-01-10 | 1986-02-18 | C. Arthur Knox | Wet grinding machine |
JPS6090052A (ja) * | 1983-10-24 | 1985-05-21 | 特殊機化工業株式会社 | 循環式微粒化分散装置 |
DE3517655A1 (de) * | 1985-05-15 | 1986-11-20 | Ystral Gmbh Maschinenbau Und Processtechnik, 7801 Ballrechten-Dottingen | Vorrichtung zum mischen und dispergieren mindestens zweier medien |
US4813617A (en) * | 1988-06-17 | 1989-03-21 | Knox Jr Arthur C | Wet grinding machine |
US5522553A (en) * | 1994-09-29 | 1996-06-04 | Kady International | Method and apparatus for producing liquid suspensions of finely divided matter |
CA2201224C (en) | 1997-03-27 | 2004-12-07 | Annette Lynn Burke | Dual shear mixing element |
CN1265051A (zh) * | 1997-06-24 | 2000-08-30 | 卡迪国际公司 | 用于溶解污物及分离液体悬浮剂中的固体的方法和装置 |
US6412714B1 (en) * | 1999-08-16 | 2002-07-02 | Anthony Witsken | Apparatus for mixing, grinding, dispersing or emulsifying |
JP4521953B2 (ja) | 2000-09-13 | 2010-08-11 | キヤノン株式会社 | トナーの製造方法 |
JP4174000B2 (ja) * | 2003-02-27 | 2008-10-29 | 株式会社荒木鉄工 | 分散装置 |
JP4713321B2 (ja) * | 2005-12-02 | 2011-06-29 | シャープ株式会社 | トナーの製造方法 |
FR2929133B1 (fr) | 2008-03-31 | 2010-12-10 | Vmi | Dispositif de melange comprenant un conduit d'amenee de particules debouchant dans la zone de turbulences |
JP5146661B2 (ja) * | 2008-05-08 | 2013-02-20 | 株式会社リコー | トナーの製造方法及びトナー |
-
2012
- 2012-12-25 JP JP2014553916A patent/JP6207091B2/ja active Active
- 2012-12-25 KR KR1020157012145A patent/KR20150100629A/ko not_active Application Discontinuation
- 2012-12-25 EP EP12891151.8A patent/EP2939734B1/en active Active
- 2012-12-25 CN CN201280077578.6A patent/CN104853836B/zh active Active
- 2012-12-25 US US14/655,291 patent/US9925503B2/en active Active
- 2012-12-25 WO PCT/JP2012/083502 patent/WO2014102906A1/ja active Application Filing
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04114724A (ja) | 1990-09-01 | 1992-04-15 | M Technic Kk | 攪拌機 |
JPH04114725A (ja) | 1990-09-01 | 1992-04-15 | M Technic Kk | 撹拌機及び流体の撹拌方法 |
JP2004528973A (ja) * | 2001-04-19 | 2004-09-24 | アンノバ・アンビロンヌマン | 処理容器内の液体を攪拌および曝気するための装置 |
JP2006221023A (ja) * | 2005-02-14 | 2006-08-24 | Canon Inc | トナーの製造方法 |
JP2011123236A (ja) | 2009-12-10 | 2011-06-23 | Canon Inc | トナーの製造方法 |
Non-Patent Citations (1)
Title |
---|
See also references of EP2939734A4 |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110917917A (zh) * | 2019-12-13 | 2020-03-27 | 武汉工程大学 | 一种印刷用原料筛选搅拌装置 |
Also Published As
Publication number | Publication date |
---|---|
EP2939734A1 (en) | 2015-11-04 |
EP2939734B1 (en) | 2024-04-03 |
JPWO2014102906A1 (ja) | 2017-01-12 |
JP6207091B2 (ja) | 2017-10-04 |
EP2939734A4 (en) | 2016-08-24 |
US20150328602A1 (en) | 2015-11-19 |
US9925503B2 (en) | 2018-03-27 |
KR20150100629A (ko) | 2015-09-02 |
EP2939734C0 (en) | 2024-04-03 |
CN104853836A (zh) | 2015-08-19 |
CN104853836B (zh) | 2018-01-12 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP6207091B2 (ja) | 攪拌処理装置及び処理方法 | |
KR101954110B1 (ko) | 교반기 | |
TW201924775A (zh) | 攪拌裝置 | |
US9205389B2 (en) | Agitating vessel using baffles and agitator having improved agitating capability and including the same | |
JP7212965B2 (ja) | 攪拌機 | |
JP7049793B2 (ja) | 微粒化装置 | |
JP6069707B2 (ja) | 流体処理装置及び流体処理方法 | |
KR102703317B1 (ko) | 교반기 | |
JP5572311B2 (ja) | 攪拌・脱泡装置及び攪拌・脱泡方法 | |
JPWO2020213184A1 (ja) | 攪拌機 | |
KR20210150949A (ko) | 교반기 | |
JP5597315B1 (ja) | 攪拌装置 | |
JP2021122784A (ja) | 撹拌機 | |
JP2022107704A (ja) | 撹拌翼および撹拌装置 | |
WO2020108816A1 (de) | Küchengerät | |
RU2578153C1 (ru) | Перемешивающее устройство | |
Dickey | Fundamentals of High-Shear Dispersers. | |
KR20200095942A (ko) | 재료의 하강유도 기능을 갖는 교반장치 | |
JP2005279606A (ja) | 分散等の処理装置 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 12891151 Country of ref document: EP Kind code of ref document: A1 |
|
ENP | Entry into the national phase |
Ref document number: 2014553916 Country of ref document: JP Kind code of ref document: A |
|
ENP | Entry into the national phase |
Ref document number: 20157012145 Country of ref document: KR Kind code of ref document: A |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2012891151 Country of ref document: EP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 14655291 Country of ref document: US |
|
NENP | Non-entry into the national phase |
Ref country code: DE |