JP5625216B2 - Distributed method and distributed system - Google Patents
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- JP5625216B2 JP5625216B2 JP2011122554A JP2011122554A JP5625216B2 JP 5625216 B2 JP5625216 B2 JP 5625216B2 JP 2011122554 A JP2011122554 A JP 2011122554A JP 2011122554 A JP2011122554 A JP 2011122554A JP 5625216 B2 JP5625216 B2 JP 5625216B2
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- 238000000034 method Methods 0.000 title claims description 11
- 239000000843 powder Substances 0.000 claims description 91
- 230000007246 mechanism Effects 0.000 claims description 83
- 239000007791 liquid phase Substances 0.000 claims description 63
- 239000002612 dispersion medium Substances 0.000 claims description 62
- 239000012530 fluid Substances 0.000 claims description 54
- 239000006185 dispersion Substances 0.000 claims description 50
- 238000007790 scraping Methods 0.000 claims description 40
- 238000005192 partition Methods 0.000 claims description 36
- 230000002093 peripheral effect Effects 0.000 claims description 25
- 239000000203 mixture Substances 0.000 claims description 24
- 229920006395 saturated elastomer Polymers 0.000 claims description 17
- 238000000926 separation method Methods 0.000 claims description 6
- 238000004519 manufacturing process Methods 0.000 claims description 2
- 239000002904 solvent Substances 0.000 description 71
- 239000002002 slurry Substances 0.000 description 33
- 238000009835 boiling Methods 0.000 description 18
- 238000003756 stirring Methods 0.000 description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 17
- 239000007788 liquid Substances 0.000 description 10
- 230000009471 action Effects 0.000 description 8
- 238000010008 shearing Methods 0.000 description 7
- 238000009834 vaporization Methods 0.000 description 6
- 230000008016 vaporization Effects 0.000 description 6
- 239000002994 raw material Substances 0.000 description 5
- 239000007790 solid phase Substances 0.000 description 4
- 241000283014 Dama Species 0.000 description 3
- 238000004891 communication Methods 0.000 description 3
- JNSGIVNNHKGGRU-JYRVWZFOSA-N diethoxyphosphinothioyl (2z)-2-(2-amino-1,3-thiazol-4-yl)-2-methoxyiminoacetate Chemical compound CCOP(=S)(OCC)OC(=O)C(=N/OC)\C1=CSC(N)=N1 JNSGIVNNHKGGRU-JYRVWZFOSA-N 0.000 description 3
- 239000000839 emulsion Substances 0.000 description 3
- 235000013305 food Nutrition 0.000 description 3
- 229920002134 Carboxymethyl cellulose Polymers 0.000 description 2
- 241000209140 Triticum Species 0.000 description 2
- 235000021307 Triticum Nutrition 0.000 description 2
- 238000013459 approach Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000006073 displacement reaction Methods 0.000 description 2
- 239000007772 electrode material Substances 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 235000013312 flour Nutrition 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 230000001737 promoting effect Effects 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 235000020183 skimmed milk Nutrition 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- QMGYPNKICQJHLN-UHFFFAOYSA-M Carboxymethylcellulose cellulose carboxymethyl ether Chemical compound [Na+].CC([O-])=O.OCC(O)C(O)C(O)C(O)C=O QMGYPNKICQJHLN-UHFFFAOYSA-M 0.000 description 1
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 239000003990 capacitor Substances 0.000 description 1
- 239000013064 chemical raw material Substances 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 229910001416 lithium ion Inorganic materials 0.000 description 1
- 239000006166 lysate Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000011812 mixed powder Substances 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 238000005498 polishing Methods 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000012795 verification Methods 0.000 description 1
Classifications
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- 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
- B01F25/60—Pump mixers, i.e. mixing within a pump
-
- 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
- B01F23/50—Mixing liquids with solids
- B01F23/51—Methods thereof
-
- 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
- B01F27/05—Stirrers
- B01F27/11—Stirrers characterised by the configuration of the stirrers
- B01F27/119—Stirrers with rigid wires or flexible rods
- B01F27/1191—Stirrers with rigid wires or flexible rods with a bent rod of non-helical configuration supported at one end
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
- B01F35/717—Feed mechanisms characterised by the means for feeding the components to the mixer
- B01F35/7173—Feed mechanisms characterised by the means for feeding the components to the mixer using gravity, e.g. from a hopper
- B01F35/71731—Feed mechanisms characterised by the means for feeding the components to the mixer using gravity, e.g. from a hopper using a hopper
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
- B01F35/717—Feed mechanisms characterised by the means for feeding the components to the mixer
- B01F35/71775—Feed mechanisms characterised by the means for feeding the components to the mixer using helical screws
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
- B01F35/717—Feed mechanisms characterised by the means for feeding the components to the mixer
- B01F35/71805—Feed mechanisms characterised by the means for feeding the components to the mixer using valves, gates, orifices or openings
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/80—Forming a predetermined ratio of the substances to be mixed
- B01F35/83—Forming a predetermined ratio of the substances to be mixed by controlling the ratio of two or more flows, e.g. using flow sensing or flow controlling devices
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/80—Forming a predetermined ratio of the substances to be mixed
- B01F35/83—Forming a predetermined ratio of the substances to be mixed by controlling the ratio of two or more flows, e.g. using flow sensing or flow controlling devices
- B01F35/834—Forming a predetermined ratio of the substances to be mixed by controlling the ratio of two or more flows, e.g. using flow sensing or flow controlling devices the flow of substances to be mixed circulating in a closed circuit, e.g. from a container through valve, driving means, metering means or dispensing means, e.g. 3-way valve, and back to the container
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
- B01F2101/48—Mixing water in water-taps with other ingredients, e.g. air, detergents or disinfectants
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Dispersion Chemistry (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
- Accessories For Mixers (AREA)
- Colloid Chemistry (AREA)
- Structures Of Non-Positive Displacement Pumps (AREA)
Description
本発明は、流体が供給される導入室と、導入室の外周側に配置され複数の絞り透孔を周方向に並べて備えた円筒状のステータと、ステータの外周側に形成された吐出部に通じる環状の翼室と、翼室で回転駆動可能な回転翼とを、本体ケーシング内に配置し、回転翼の回転駆動により、導入室から絞り透孔を通じて翼室に流体を吸引し、翼室から吐出部に流体を吐出する遠心式の吸引ポンプ機構部を用い、吸引ポンプ機構部に分散質と液相分散媒との混合流体を通過させ、液相分散媒に分散質を分散させたゾルを生成する分散方法及び分散システムに関する。 The present invention includes an introduction chamber to which a fluid is supplied, a cylindrical stator that is arranged on the outer circumferential side of the introduction chamber and includes a plurality of throttle through holes arranged in the circumferential direction, and a discharge portion that is formed on the outer circumferential side of the stator. An annular blade chamber that communicates with a rotor blade that can be driven to rotate in the blade chamber is disposed in the main body casing, and by rotating the rotor blade, fluid is sucked from the introduction chamber into the blade chamber through the throttle hole, and the blade chamber is A sol in which a mixed fluid of a dispersoid and a liquid phase dispersion medium is passed through the suction pump mechanism and the dispersoid is dispersed in the liquid phase dispersion medium. The present invention relates to a distributed method and a distributed system for generating a message.
液相分散媒に対し固相分散質(分散質の一例)を分散させてなるスラリー(ゾルの一例)は、リチウムイオン二次電池や電気二重層キャパシタ等の電極やセパレータ、塗料、トナー、研磨剤等の用途に多く利用される。一方、液相分散媒に対し液相分散質(分散質の一例)を分散させてなるエマルジョン(ゾルの一例)は、食品、シート材、エマルジョン燃料等に利用される。
このようなゾルにおいて、液相分散媒中への分散質の分散が不十分であると、その性能低下につながる場合があり、特に、二次電池電極として利用する場合には、サイクル特性の低下につながる。
ちなみに、液相分散媒としては、例えば、水等の溶媒が挙げられ、分散質としては粉体等の固相分散質や油等の液相分散質が挙げられる。
なお、粉体としては、粉体であれば特に除外されるものではないが、例えば、電池電極材料等の化学原料、脱脂粉乳や小麦粉等の食品原料、医薬原料等であって、顆粒、粉体、細粒等の粉体(これら粉体の混合物を含む)を例示することができる。粉体には、粉粒体も含まれる。
A slurry (an example of a sol) in which a solid phase dispersoid (an example of a dispersoid) is dispersed in a liquid phase dispersion medium is an electrode or separator such as a lithium ion secondary battery or an electric double layer capacitor, paint, toner, and polishing. It is often used for applications such as chemicals. On the other hand, an emulsion (an example of a sol) in which a liquid phase dispersoid (an example of a dispersoid) is dispersed in a liquid phase dispersion medium is used for foods, sheet materials, emulsion fuels, and the like.
In such a sol, if the dispersion of the dispersoid in the liquid phase dispersion medium is insufficient, the performance may be deteriorated, particularly when used as a secondary battery electrode, the cycle characteristics are deteriorated. Leads to.
Incidentally, examples of the liquid phase dispersion medium include solvents such as water, and examples of the dispersoid include solid phase dispersoids such as powder and liquid phase dispersoids such as oil.
The powder is not particularly excluded as long as it is a powder. Examples thereof include chemical raw materials such as battery electrode materials, food raw materials such as skim milk powder and wheat flour, pharmaceutical raw materials, etc. Examples thereof include powders such as bodies and fine particles (including a mixture of these powders). The powder includes a granular material.
従来、液相分散媒に対し分散質を分散させたゾル(分散液)を生成する分散システムとして、流体が供給される導入室と、導入室の外周側に配置され複数の絞り透孔を周方向に並べて備えた円筒状のステータと、ステータの外周側に形成された吐出部に通じる環状の翼室と、翼室で回転駆動可能な回転翼とを、本体ケーシング内に配置し、回転翼の回転駆動により、導入室から絞り透孔を通じて翼室に流体を吸引し、翼室から吐出部に流体を吐出する遠心式の吸引ポンプ機構部を備えたものが知られている(例えば、特許文献1〜3参照)。 Conventionally, as a dispersion system for generating a sol (dispersion liquid) in which a dispersoid is dispersed in a liquid phase dispersion medium, an introduction chamber to which a fluid is supplied, and a plurality of throttling through holes arranged around the outer periphery of the introduction chamber. A cylindrical stator arranged in a direction, an annular blade chamber communicating with a discharge portion formed on the outer peripheral side of the stator, and a rotary blade that can be driven to rotate in the blade chamber are arranged in the main body casing, and the rotary blade Is known to have a centrifugal suction pump mechanism that sucks fluid from the introduction chamber into the blade chamber through the throttle hole and discharges the fluid from the blade chamber to the discharge portion (for example, patents) References 1-3).
この種の分散システムは、液相分散媒と分散質との混合流体を導入室に供給して回転翼を回転駆動させる状態で、吸引ポンプ機構部に混合流体を通過させることで、混合流体に対し回転翼によるせん断力及び衝撃力が与えられ、混合流体に含まれる分散質の凝集物(いわゆるダマ)が適度に解砕されるので、適切に液相分散媒中に分散質を分散させることができるとされる。
また、この種の分散システムでは、翼室において高速で回転駆動する回転翼の背面部で急激な圧力低下が生じるため、絞り透孔を通過して回転翼の背面部付近に存在する混合流体に局所沸騰(キャビテーション)を起こさせ、この混合流体に含まれる気泡の膨張とそれによって生じる衝撃により、分散質の凝集物(ダマ)が良好に解砕され、液相分散媒中での分散質の分散を促進させることができるとされる。
In this type of dispersion system, a mixed fluid of a liquid phase dispersion medium and a dispersoid is supplied to an introduction chamber, and a rotating blade is driven to rotate. On the other hand, the shear force and impact force of the rotor blade are applied, and the dispersoid aggregates (so-called lumps) contained in the mixed fluid are appropriately crushed, so that the dispersoid is appropriately dispersed in the liquid phase dispersion medium. It is supposed to be possible.
Also, in this type of dispersion system, a sudden pressure drop occurs at the back of the rotor blades that are driven to rotate at high speed in the blade chamber, so that the mixed fluid that exists near the back of the rotor blades passes through the throttle hole. By causing local boiling (cavitation), the expansion of bubbles contained in the mixed fluid and the impact caused thereby, the aggregates (dama) of the dispersoids are crushed well, and the dispersoids in the liquid dispersion medium are disintegrated. It is said that dispersion can be promoted.
上述の従来の分散システム及び分散方法では、翼室において回転駆動する回転翼の背面部での急激な圧力低下により、混合流体の一部、すなわち、絞り透孔を通過して回転翼の背面部付近に存在する混合流体では、局所沸騰(キャビテーション)が発生するが、一方で、絞り透孔を通過した直後の混合流体には沸騰が発生することなくそのまま吐出部に吐出されるものも存在するため、液相分散媒中への分散質の分散を十分に促進することは困難であった。
ここで、例えば、ステータの絞り透孔の大きさを極度に小さくすることにより、絞り透孔を通過した混合流体の圧力を大幅に低下させることで液相分散媒中への分散質の分散を促進することも考えられるが、混合流体中の分散質である粉体が絞り透孔に詰り流通不良を起こして、逆に分散質の分散が悪化する虞があった。
In the above-described conventional dispersion system and dispersion method, a part of the mixed fluid, that is, the back surface portion of the rotor blade passes through the throttle hole due to a rapid pressure drop at the back surface portion of the rotor blade that is driven to rotate in the blade chamber. In the mixed fluid existing in the vicinity, local boiling (cavitation) occurs. On the other hand, some mixed fluid immediately after passing through the throttle through-hole does not generate boiling and is directly discharged to the discharge portion. Therefore, it has been difficult to sufficiently promote the dispersion of the dispersoid in the liquid phase dispersion medium.
Here, for example, by greatly reducing the size of the throttle through hole of the stator, the pressure of the mixed fluid that has passed through the throttle through hole is greatly reduced, thereby dispersing the dispersoid in the liquid phase dispersion medium. Although it is conceivable to promote, there is a possibility that the powder as the dispersoid in the mixed fluid may clog the throttling pores and cause poor flow, and conversely, the dispersion of the dispersoid may deteriorate.
特に、液相分散媒に対する分散質(特に、粉体)の割合が高くなるほど流動性は低くなり、分散質の凝集物(いわゆるダマ)が発生し易く、しかも、発生する分散質の凝集物が大きくなり易いので、分散質の液相分散媒への分散が十分に行えない場合があり、改善が望まれていた。
即ち、液相分散媒に分散質が分散されたゾル(分散液)の用途として、例えば、対象物に分散質を主成分とする膜や部材を形成する用途がある。この用途では、例えば、分散液を対象物に塗布した後に加熱する等の処理を実行することにより、液相分散媒を蒸発させて、分散質を主成分とする膜や部材を形成する。このような用途においては、予備混合物中の液相分散媒の比率を低くして、処理の効率化を図ることが望まれる。しかしながら、処理の効率化を図るために、予備混合物中の液相分散媒の比率を低くすると、上述のように、予備混合物の流動性が低くなるので、従来の分散システムでは、分散質の凝集物の問題が特に顕著となり、分散質を液相分散媒に十分に分散させることができなかった。
In particular, the higher the ratio of the dispersoid (particularly powder) to the liquid phase dispersion medium, the lower the fluidity, and the easier it is to generate dispersoid aggregates (so-called lumps). Since it tends to be large, the dispersion of the dispersoid in the liquid phase dispersion medium may not be sufficiently performed, and an improvement has been desired.
That is, as an application of a sol (dispersion liquid) in which a dispersoid is dispersed in a liquid phase dispersion medium, for example, there is an application in which a film or a member having a dispersoid as a main component is formed on an object. In this application, for example, a liquid phase dispersion medium is evaporated by performing a process such as heating after applying the dispersion liquid to the object, thereby forming a film or member mainly composed of the dispersoid. In such an application, it is desired to reduce the ratio of the liquid phase dispersion medium in the preliminary mixture to improve the processing efficiency. However, if the ratio of the liquid phase dispersion medium in the premix is lowered in order to increase the efficiency of the process, the fluidity of the premix becomes low as described above. The problem of the product became particularly remarkable, and the dispersoid could not be sufficiently dispersed in the liquid phase dispersion medium.
本発明は、かかる実情に鑑みてなされたものであり、その目的は、ステータの絞り透孔を通過した混合流体全体に亘って良好に液相分散媒中における分散質の分散を促進して、高品質のゾルを生成することができる分散方法及び分散システムを確立する点にある。 The present invention has been made in view of such circumstances, and the object thereof is to promote the dispersion of the dispersoid in the liquid dispersion medium satisfactorily over the entire mixed fluid that has passed through the throttle through hole of the stator. The object is to establish a dispersion method and a dispersion system capable of producing a high-quality sol.
上記目的を達成するための本発明に係る分散方法は、
流体が供給される導入室と、前記導入室の外周側に配置され複数の絞り透孔を周方向に並べて備えた円筒状のステータと、前記ステータの外周側に形成された吐出部に通じる環状の翼室と、当該翼室で回転駆動可能な回転翼とを、本体ケーシング内に配置し、前記回転翼の回転駆動により、前記導入室から前記絞り透孔を通じて前記翼室に流体を吸引し、前記翼室から前記吐出部に流体を吐出する遠心式の吸引ポンプ機構部を用い、前記吸引ポンプ機構部に分散質と液相分散媒との混合流体を通過させ、前記液相分散媒に前記分散質を分散させたゾルを生成する分散方法であって、その特徴構成は、
前記導入室の入口部に絞り部を設け、
前記絞り部の内径は、前記導入室へ流体を供給する循環路よりも小径であり、
前記導入室に対し区画板により区画されて形成され、前記ステータの絞り透孔を通じて前記翼室に通じる供給室を設け、
前記分散質と前記液相分散媒とを予備混合した予備混合物を前記供給室に供給するとともに、前記吐出部から吐出されたゾルの一部を前記混合流体として前記導入室に循環供給しながら、
前記ステータの絞り透孔の出口領域の圧力が当該出口領域の全周に亘って前記液相分散媒の飽和蒸気圧以下となるように前記回転翼の回転数を設定し、前記供給機構部と前記再循環機構部とを作動させながら前記設定された回転数で前記回転翼を回転して、前記翼室内の少なくとも前記ステータの絞り透孔を通過した直後の領域を、前記液相分散媒の微細気泡が多数発生した微細気泡領域として形成する点にある。
In order to achieve the above object, the dispersion method according to the present invention comprises:
An introduction chamber to which a fluid is supplied, a cylindrical stator that is arranged on the outer peripheral side of the introduction chamber and includes a plurality of throttle through holes arranged in the circumferential direction, and an annular shape that leads to a discharge portion formed on the outer peripheral side of the stator The blade chamber and a rotor blade that can be rotationally driven in the blade chamber are disposed in the main body casing, and fluid is sucked from the introduction chamber to the blade chamber through the throttle through-hole by the rotational drive of the rotor blade. Using a centrifugal suction pump mechanism that discharges fluid from the blade chamber to the discharge unit, and passing a mixed fluid of a dispersoid and a liquid phase dispersion medium through the suction pump mechanism unit, A dispersion method for producing a sol in which the dispersoid is dispersed, the characteristic configuration of which is
A throttle is provided at the inlet of the introduction chamber,
The inner diameter of the throttle portion is smaller than the circulation path for supplying fluid to the introduction chamber,
The supply chamber is formed by being partitioned by a partition plate with respect to the introduction chamber, and is provided with a supply chamber that communicates with the blade chamber through the throttle through hole of the stator.
While supplying a premixture prepared by premixing the dispersoid and the liquid phase dispersion medium to the supply chamber and circulatingly supplying a part of the sol discharged from the discharge section to the introduction chamber as the mixed fluid,
The rotation speed of the rotor blade is set so that the pressure in the outlet region of the throttle through hole of the stator is equal to or lower than the saturated vapor pressure of the liquid phase dispersion medium over the entire circumference of the outlet region, and the supply mechanism unit Rotating the rotary blade at the set rotational speed while operating the recirculation mechanism, and at least a region immediately after passing through the throttle aperture of the stator in the blade chamber, This is in the point of forming as a fine bubble region where a large number of fine bubbles are generated.
上記目的を達成するための本発明に係る分散システムは、
流体が供給される導入室と、前記導入室の外周側に配置され複数の絞り透孔を周方向に並べて備えた円筒状のステータと、前記ステータの外周側に形成された吐出部に通じる環状の翼室と、当該翼室で回転駆動可能な回転翼とを、本体ケーシング内に配置し、前記回転翼の回転駆動により、前記導入室から前記絞り透孔を通じて前記翼室に流体を吸引し、前記翼室から前記吐出部に流体を吐出する遠心式の吸引ポンプ機構部を備え、前記吸引ポンプ機構部に分散質と液相分散媒との混合流体を通過させ、前記液相分散媒に前記分散質を分散させたゾルを生成する分散システムであって、その特徴構成は、
前記導入室の入口部に絞り部を備え、
前記絞り部の内径は、前記導入室へ流体を供給する循環路よりも小径であり、
前記導入室に対し区画板により区画されて形成され、前記ステータの絞り透孔を通じて前記翼室に通じる供給室を備え、
前記分散質と前記液相分散媒とを予備混合した予備混合物を前記供給室に供給する供給機構部と、前記吐出部から吐出されたゾルの一部を前記混合流体として前記導入室に循環供給する再循環機構部とを備え、
運転を制御する制御部が、前記ステータの絞り透孔の出口領域の圧力が当該出口領域の全周に亘って前記液相分散媒の飽和蒸気圧以下となるように前記回転翼の回転数を設定し、前記供給機構部と前記再循環機構部とを作動させながら前記設定された回転数で前記回転翼を回転させて、前記翼室内の少なくとも前記ステータの絞り透孔を通過した直後の領域が、前記液相分散媒の微細気泡が多数発生した微細気泡領域として形成される点にある。
In order to achieve the above object, a distributed system according to the present invention includes:
An introduction chamber to which a fluid is supplied, a cylindrical stator that is arranged on the outer peripheral side of the introduction chamber and includes a plurality of throttle through holes arranged in the circumferential direction, and an annular shape that leads to a discharge portion formed on the outer peripheral side of the stator The blade chamber and a rotor blade that can be rotationally driven in the blade chamber are disposed in the main body casing, and fluid is sucked from the introduction chamber to the blade chamber through the throttle through-hole by the rotational drive of the rotor blade. A centrifugal suction pump mechanism that discharges fluid from the blade chamber to the discharge unit, and a fluid mixture of a dispersoid and a liquid phase dispersion medium is passed through the suction pump mechanism unit, and the liquid phase dispersion medium A dispersion system for generating a sol in which the dispersoid is dispersed.
Provided with a throttle at the inlet of the introduction chamber,
The inner diameter of the throttle portion is smaller than the circulation path for supplying fluid to the introduction chamber,
A supply chamber that is formed by being partitioned by a partition plate with respect to the introduction chamber, and that communicates with the blade chamber through an aperture hole of the stator;
A supply mechanism for supplying a premixed mixture of the dispersoid and the liquid phase dispersion medium to the supply chamber, and a part of the sol discharged from the discharge section is circulated and supplied to the introduction chamber as the mixed fluid. And a recirculation mechanism that
The controller for controlling the operation adjusts the rotational speed of the rotor blades so that the pressure in the outlet region of the throttle through hole of the stator is equal to or lower than the saturated vapor pressure of the liquid phase dispersion medium over the entire circumference of the outlet region. An area immediately after passing through at least the stator aperture in the stator chamber by rotating the rotor blade at the set rotational speed while operating the supply mechanism section and the recirculation mechanism section. However, the liquid phase dispersion medium is formed as a fine bubble region where a large number of fine bubbles are generated.
上記特徴構成によれば、導入室の入口部に絞り部を設けるとともに、導入室の下流側(外周側)にステータの絞り透孔が設けられているので、回転翼の回転駆動により翼室に吸引される混合流体が、絞り部、導入室、絞り透孔を順に通過することになり、略大気圧となりうる導入室の一次側(入口部の上流側)圧力より導入室内の圧力が低くなり、さらに、その導入室内の圧力よりもステータの絞り透孔の出口領域の圧力が低くなる。
特に、回転翼の回転数設定により、ステータの絞り透孔の出口領域の圧力は当該出口領域の全周に亘って液相分散媒の飽和蒸気圧(25℃の水の場合、3.169kPa)以下となるから、翼室内の少なくとも絞り透孔を通過した直後の領域では、液相分散媒の気化による微細気泡(マイクロバブル)の発生が促進され、当該領域を、翼室内の全周に亘って連続して当該微細気泡が多数発生した微細気泡領域として形成することができる。
よって、翼室内の全周に亘って、分散質の凝集物(いわゆるダマ)に浸透した液相分散媒が発泡することで凝集物の解砕が促進され、さらに、その発生した微細気泡が翼室において加圧され消滅する際の衝撃力によりさらに分散質の分散が促進されることになり、結果、翼室内に存在する混合流体のほぼ全体に亘って、液相分散媒中での分散質の分散が良好な高品質のゾル(分散液)を生成することができる。
According to the above characteristic configuration, the throttle portion is provided at the inlet portion of the introduction chamber, and the stator through hole is provided on the downstream side (outer peripheral side) of the introduction chamber. The sucked mixed fluid sequentially passes through the throttle part, the introduction chamber, and the throttle through hole, and the pressure in the introduction chamber becomes lower than the pressure on the primary side of the introduction chamber (upstream side of the inlet), which can be almost atmospheric pressure. In addition, the pressure in the outlet region of the throttle through hole of the stator becomes lower than the pressure in the introduction chamber.
In particular, depending on the setting of the rotational speed of the rotor blade, the pressure in the outlet region of the stator throttling hole is the saturated vapor pressure of the liquid phase dispersion medium over the entire circumference of the outlet region (3,169 kPa for water at 25 ° C.). Therefore, at least in the region immediately after passing through the throttle hole in the blade chamber, the generation of fine bubbles (microbubbles) due to the vaporization of the liquid phase dispersion medium is promoted, and the region covers the entire circumference of the blade chamber. Thus, it can be formed as a fine bubble region where a large number of the fine bubbles are continuously generated.
Therefore, the liquid phase dispersion medium that has permeated the dispersoid aggregates (so-called lumps) foams around the entire circumference of the blade chamber, thereby promoting the crushing of the aggregates. Dispersion of the dispersoid is further promoted by the impact force when it is pressurized and extinguished in the chamber, and as a result, the dispersoid in the liquid phase dispersion medium over almost the entire mixed fluid existing in the blade chamber. It is possible to produce a high-quality sol (dispersion liquid) with good dispersion.
この点について、例えば、図8に基づいて説明を加える。図8は、本体ケーシングを透明の樹脂で構成し、吸引ポンプ機構部内に流体としての水を通過させて、回転翼が回転する翼室内を外周側から観察した状態を示し、図8(a)から(c)に行くに従って、回転翼の回転数を増加させた状態を示す。図8(a)にて判明するように、回転翼の回転数が比較的低い状態では、絞り透孔の出口領域の圧力は水の飽和蒸気圧(25℃の水の場合、3.169kPa)よりも大きくなっており、絞り透孔を通過した直後の流体においては、回転翼の背面部での急激な圧力低下により、流体の一部、すなわち、絞り透孔を通過して回転翼の背面部付近に存在する流体のみに、局所沸騰(キャビテーション)が周方向に断続的な状態で発生するだけで、絞り透孔を通過した流体の全体に沸騰が発生することなく吐出部にそのまま吐出されるものも存在している状態である。即ち、この状態は、図8(a)において翼室内に存在する白く見える領域が非常に少ない状態である。
一方で、図8(b)にて判明するように、回転翼の回転数が比較的高い状態では、絞り透孔の出口領域の圧力は全周に亘って水の飽和蒸気圧(25℃の水の場合、3.169kPa)以下となっており、翼室内の少なくとも絞り透孔を通過した直後の領域では、回転翼の背面部での急激な圧力低下により、翼室内において回転翼の背面部付近に存在する流体の局所沸騰(キャビテーション)に加え、流体の気化による微細気泡(本願にいう微細気泡であるマイクロバブル)の発生が促進され、当該領域が、翼室内の全周に亘って連続して微細気泡が多数発生した微細気泡領域として形成されている状態である。即ち、この状態は、図8(b)において翼室内に存在する白く見える領域が雲状に非常に多く発生している状態である。更に、図8(c)にて判明するように、回転翼の回転数がより高い状態では、翼室内の全周に亘る流体中の液相分散媒の気化による微細気泡(マイクロバブル)が、より多く発生し、微細気泡が多数発生した微細気泡領域がより鮮明に形成されている状態となっている。即ち、この状態は、図8(c)において翼室内に存在する白く見える領域が、雲状に非常に多く(図8(b)よりも多く)発生している状態である。
This point will be described with reference to FIG. 8 , for example. Figure 8 constitutes a main casing with a transparent resin, by passing the water as a fluid to a suction pump mechanism portion, showing a state in which rotary blade was observed wings chamber rotates from the outer circumferential side shown in FIG. 8 (a) From (1) to (c), the rotational speed of the rotor blade is increased. As can be seen from FIG. 8 (a), when the rotational speed of the rotor blade is relatively low, the pressure in the outlet region of the throttle hole is the saturated vapor pressure of water (3.169 kPa for water at 25 ° C.). In the fluid immediately after passing through the throttle through hole, a part of the fluid, that is, the back of the rotor blade passes through the throttle through hole due to a sudden pressure drop at the back surface of the rotor blade. Only local fluid (cavitation) occurs in the circumferential direction intermittently only in the fluid existing in the vicinity of the head, and the fluid that has passed through the throttle hole is discharged to the discharge section as it is without boiling. Something exists. That is, this condition appears white region present blade chamber is very small state in FIG. 8 (a).
On the other hand, as can be seen in FIG. 8B , in the state where the rotational speed of the rotor blade is relatively high, the pressure in the outlet region of the throttle through-hole is the saturated vapor pressure of water (25 ° C. In the case of water, it is 3.169 kPa) or less, and at least in the region immediately after passing through the throttle hole in the blade chamber, due to a sudden pressure drop at the back surface of the rotor blade, the back surface portion of the rotor blade in the blade chamber In addition to local boiling (cavitation) of the fluid existing in the vicinity, the generation of microbubbles (microbubbles, which are the microbubbles referred to in the present application) due to the vaporization of the fluid is promoted, and this region is continuous over the entire circumference of the blade chamber In this state, a fine bubble region in which many fine bubbles are generated is formed. That is, this state is a state in which a large number of white-like regions existing in the blade chamber in FIG. 8B are generated in a cloud shape. Moreover, as found in FIG. 8 (c), the at higher state rotational speed of the rotor blades, fine bubbles due to vaporization of the liquid dispersion medium in the fluid over the entire circumference of the blade chamber (microbubbles) is, More fine bubbles are generated, and a fine bubble region in which many fine bubbles are generated is formed more clearly. That is, this condition appears white region existing blade chamber in FIG. 8 (c) it is very much (more than FIG. 8 (b)) to the cloud is a state that is occurring.
このように、通常、吸引ポンプ機構部内では、絞り透孔の出口領域において翼室内の回転翼の背面部のみに発生する局所沸騰(キャビテーション)のみで分散質を液相分散媒に分散させることで十分とされていたが(図8(a)の状態)、本発明者らは、例えば、液相分散媒に対する分散質の割合が比較的多く、より分散性能を向上させることが必要となったことに鑑みて、上述のとおり、回転翼の回転数設定により、ステータの絞り透孔の出口領域の圧力を当該出口領域の全周に亘って液相分散媒の飽和蒸気圧以下とし、翼室内において、より広範囲に液相分散媒の沸騰を発生させることを可能とし(図8の(b),(c)の状態)、翼室内の全周に存在する混合流体のほぼ全体に亘って、液相分散媒中での分散質の分散が良好な高品質のゾル(分散液)を生成することが可能であることを見出して、本願発明を完成したのである。 As described above, normally, in the suction pump mechanism, the dispersoid is dispersed in the liquid phase dispersion medium only by local boiling (cavitation) generated only at the back surface of the rotor blade in the blade chamber in the exit region of the throttle hole. Although sufficient (state of FIG. 8 (a)), the present inventors, for example, have a relatively large ratio of the dispersoid to the liquid phase dispersion medium, and it is necessary to further improve the dispersion performance. In view of the above, as described above, by setting the rotation speed of the rotor blade, the pressure in the outlet region of the stator throttling hole is set to be equal to or lower than the saturated vapor pressure of the liquid phase dispersion medium over the entire periphery of the outlet region. , It is possible to generate boiling of the liquid phase dispersion medium in a wider range (states (b) and (c) of FIG. 8 ), and over almost the entire mixed fluid existing in the entire circumference of the blade chamber, High quality with good dispersoid dispersion in liquid phase dispersion medium The present invention was completed by finding that it is possible to produce a sol (dispersion).
加えて上記特徴構成によれば、分散質と液相分散媒とを予備混合した予備混合物は、供給機構部により供給室から翼室側に供給されて、絞り透孔を通過するときにせん断作用を受けて混合され、翼室内に吸引される。一方、吐出部から吐出されたゾルの一部は、再循環機構部により導入室に循環供給されて、絞り透孔を通過するときにせん断作用を受けて混合され、翼室内に吸引される。 In addition, according to the above-described characteristic configuration, the premixture obtained by premixing the dispersoid and the liquid phase dispersion medium is supplied from the supply chamber to the blade chamber side by the supply mechanism unit, and is sheared when passing through the throttle through hole. And mixed and sucked into the blade chamber. On the other hand, a part of the sol discharged from the discharge unit is circulated and supplied to the introduction chamber by the recirculation mechanism unit, and is mixed by being subjected to a shearing action when passing through the throttle hole, and is sucked into the blade chamber.
そして、供給室から絞り透孔を通過して翼室に流入した予備混合物と、導入室から絞り透孔を通過して翼室に流入した混合流体(ゾルの一部を含む)とは、翼室を周回する回転翼により混合されて吐出部から吐出される。従って、より分散質の凝集物(ダマ)の発生を極力抑制しながら、液相分散媒に対して分散質を、より確実に分散させることができる。 The preliminary mixture that flows from the supply chamber through the throttle hole into the blade chamber and the mixed fluid (including part of the sol) that flows from the introduction chamber through the throttle hole into the blade chamber are the blade It is mixed by a rotating blade that circulates around the chamber and discharged from the discharge section. Accordingly, it is possible to more reliably disperse the dispersoid in the liquid phase dispersion medium while suppressing generation of more dispersoid aggregates (dama) as much as possible.
本発明に係る分散方法の更なる特徴構成は、前記分散質は粉体であり、前記粉体を前記液相分散媒に溶解させたゾルを生成する点にある。 A further characteristic configuration of the dispersion method according to the present invention is that the dispersoid is a powder, and a sol in which the powder is dissolved in the liquid phase dispersion medium is generated.
本発明に係る分散システムの更なる特徴構成は、前記分散質は粉体であり、前記粉体を前記液相分散媒に溶解させたゾルを生成する点にある。 A further characteristic configuration of the dispersion system according to the present invention is that the dispersoid is a powder, and a sol in which the powder is dissolved in the liquid phase dispersion medium is generated.
本発明に係る分散システムの更なる特徴構成は、前記再循環機構部に、前記導入室に循環供給するゾルから気泡を分離する分離部を備えた点にある。 A further characteristic configuration of the dispersion system according to the present invention is that the recirculation mechanism section includes a separation section that separates bubbles from the sol that is circulated and supplied to the introduction chamber.
上記特徴構成によれば、吐出部から吐出され導入室に循環供給されるゾルから気泡(液相分散媒の気泡)が分離されるので、導入室において、当該気泡の存在により、分散質の凝集物に対する液相分散媒の浸透が抑制されてしまうことを防止でき、また、絞り部による減圧が抑制されてしまうことを防止できる。更に、当該気泡の存在により、回転翼の回転によって生じる吸引ポンプ機構部内でのポンプ効果が低下することを防止できる。加えて、上述のとおり、翼室内の全周に亘って液相分散媒の微細気泡(マイクロバブル)が発生するが、分離部にて当該微細気泡を分離して、当該微細気泡が吐出部を介して導入室に循環供給されてしまうことを有効に抑制することができる。 According to the above characteristic configuration, since bubbles (bubbles of the liquid phase dispersion medium) are separated from the sol discharged from the discharge unit and circulated and supplied to the introduction chamber, the dispersoid aggregates due to the presence of the bubbles in the introduction chamber. It is possible to prevent the permeation of the liquid phase dispersion medium into the object from being suppressed, and to prevent the pressure reduction by the throttle part from being suppressed. Furthermore, the presence of the bubbles can prevent the pumping effect in the suction pump mechanism generated by the rotation of the rotor blades from being lowered. In addition, as described above, fine bubbles (microbubbles) of the liquid phase dispersion medium are generated over the entire circumference of the blade chamber, but the fine bubbles are separated by the separation unit, and the fine bubbles form the discharge unit. It is possible to effectively suppress the circulating supply to the introduction chamber.
本発明に係る分散システムの更なる特徴構成は、前記区画板を、前記回転翼が設けられたロータに接続して回転駆動可能とし、
前記供給室の入口部の予備混合物を前記供給室側に掻き出す掻出翼を、前記区画板に備えた点にある。
A further characteristic configuration of the distributed system according to the present invention is such that the partition plate is connected to a rotor provided with the rotor blades and can be rotated.
The partition plate is provided with a scraping blade for scraping the preliminary mixture at the inlet of the supply chamber toward the supply chamber.
上記特徴構成によれば、回転翼が設けられたロータの回転駆動に伴って、区画板に設けられた掻出翼が回転するので、供給室の上流側から供給され入口部に存在する予備混合物を、供給室側に良好に掻き出すことができる。特に、掻き出される予備混合物は、掻出翼のせん断作用を受けて混合されるとともに、掻出翼の背面部に発生する局所沸騰(キャビテーション)により、液相分散媒に対する分散質の分散がより良好に行われることとなる。 According to the above characteristic configuration, the scraping blade provided on the partition plate rotates as the rotor provided with the rotary blade rotates, so that the preliminary mixture that is supplied from the upstream side of the supply chamber and exists in the inlet portion Can be satisfactorily scraped to the supply chamber side. In particular, the preliminary mixture to be scraped is mixed under the shearing action of the scraping blade, and the dispersoid is more dispersed in the liquid phase dispersion medium due to local boiling (cavitation) generated on the back surface of the scraping blade. It will be done well.
以下、図面に基づいて、本発明の実施形態を説明する。
図1は本発明に係る遠心式の吸引ポンプ機構部Yを備えた分散システム100を示す。
この分散システム100は、分散質として粉体Pを用い、液相分散媒として溶媒Rを用いて、粉体Pを溶媒Rに溶解させてゾルとしてのスラリーFを生成するものである。
本実施形態においては、例えば、粉体P(固相分散質)としてCMC(カルボキシルメチルセルロース)を用い、溶媒R(液相分散媒)として水を用いた。
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
FIG. 1 shows a dispersion system 100 having a centrifugal suction pump mechanism Y according to the present invention.
This dispersion system 100 uses a powder P as a dispersoid, a solvent R as a liquid phase dispersion medium, and dissolves the powder P in the solvent R to generate a slurry F as a sol.
In the present embodiment, for example, CMC (carboxyl methylcellulose) is used as the powder P (solid phase dispersoid), and water is used as the solvent R (liquid phase dispersion medium).
図1に示すように、分散システム100は、粉体Pを定量供給する定量供給装置Xと、溶媒Rを定量供給する溶媒供給部50と、定量供給装置Xから定量供給される粉体Pと溶媒供給部50から定量供給される溶媒Rとを負圧吸引して分散混合する吸引ポンプ機構部Yと、吸引ポンプ機構部Yから吐出されたスラリーFから、完全に溶解していない粉体Pを含む溶媒R(以下、未溶解スラリーFr)を吸引ポンプ機構部Yに循環供給する再循環機構部70等を備えて構成されている。 As shown in FIG. 1, the dispersion system 100 includes a quantitative supply device X that supplies powder P in a fixed amount, a solvent supply unit 50 that supplies solvent R in a fixed amount, and a powder P that is supplied in a fixed amount from the quantitative supply device X. A suction pump mechanism Y that sucks and mixes the solvent R that is quantitatively supplied from the solvent supply unit 50 by negative pressure, and a powder P that is not completely dissolved from the slurry F discharged from the suction pump mechanism Y. And a recirculation mechanism 70 that circulates and supplies the solvent R (hereinafter, undissolved slurry Fr) to the suction pump mechanism Y.
〔定量供給装置〕
図1に示すように、定量供給装置Xは、上部開口部31aから受け入れた粉体Pを下部開口部31bから排出させるホッパ31と、ホッパ31内の粉体Pを攪拌する攪拌機構32と、ホッパ31の上部開口部31aが大気開放された状態で、下部開口部31bの下流側に接続された吸引ポンプ機構部Yの吸引により下部開口部31bに作用する負圧吸引力によって、下部開口部31bから排出された粉体Pを吸引ポンプ機構部Yに定量供給する容積式の定量供給部40とを備えて構成されている。
[Quantitative supply device]
As shown in FIG. 1, the quantitative supply device X includes a hopper 31 that discharges the powder P received from the upper opening 31a from the lower opening 31b, an agitation mechanism 32 that agitates the powder P in the hopper 31, With the upper opening 31a of the hopper 31 open to the atmosphere, the lower opening is caused by the negative pressure suction force acting on the lower opening 31b by the suction of the suction pump mechanism Y connected to the downstream side of the lower opening 31b. A positive displacement quantitative supply unit 40 that supplies the powder P discharged from 31b to the suction pump mechanism Y is provided.
ホッパ31は、上部から下部へ向かうに連れて縮径する逆円錐形状に構成され、その中心軸A1が鉛直方向に沿う姿勢で配設されている。そのホッパ31の上部開口部31a及び下部開口部31b夫々の横断面形状は、図1の上下方向視で、中心軸A1を中心とする円形状とされ、又、ホッパ31における逆円錐形状の内側壁面の傾斜角度は、水平面に対して略60度とされる。 The hopper 31 is formed in an inverted conical shape that is reduced in diameter as it goes from the upper part to the lower part, and its central axis A1 is arranged in a posture along the vertical direction. The cross-sectional shape of each of the upper opening 31a and the lower opening 31b of the hopper 31 is a circular shape centered on the central axis A1 when viewed in the vertical direction in FIG. The inclination angle of the wall surface is approximately 60 degrees with respect to the horizontal plane.
攪拌機構32は、ホッパ31内に配設されて、ホッパ31内の粉体Pを攪拌する攪拌羽根32Aと、当該攪拌羽根32Aをホッパ31の中心軸A1周りに回転させる羽根駆動モータM1と、羽根駆動モータM1をホッパ31の上部開口部31aの上方に位置させて支持する取付部材32Bと、羽根駆動モータM1の回転駆動力を攪拌羽根32Aに伝動させる伝動部材32Cとを備えて構成される。 The stirring mechanism 32 is disposed in the hopper 31 and has a stirring blade 32A that stirs the powder P in the hopper 31, a blade driving motor M1 that rotates the stirring blade 32A around the central axis A1 of the hopper 31, An attachment member 32B that supports the blade drive motor M1 positioned above the upper opening 31a of the hopper 31 and a transmission member 32C that transmits the rotational driving force of the blade drive motor M1 to the stirring blade 32A are configured. .
攪拌羽根32Aは、棒状部材を概略V字形状に屈曲して構成され、その一方の辺部がホッパ31の内側壁面に沿う状態で、他方の辺部の端部がホッパ31の中心軸A1と同軸で回転自在に枢支されて配設されている。また、当該攪拌羽根32Aは、横断面形状が三角形に形成されており、三角形の一辺を形成する面がホッパ31の内側壁面と略平行となるように配設されている。これにより、攪拌羽根32Aは、ホッパ31の内側壁面に沿って中心軸A1周りに回転可能に配設されている。 The stirring blade 32A is configured by bending a rod-like member into a substantially V-shape, with one side portion thereof being along the inner wall surface of the hopper 31, and the other side portion being at the center axis A1 of the hopper 31. It is coaxially and rotatably supported. Further, the stirring blade 32A has a triangular cross-sectional shape, and is disposed so that a surface forming one side of the triangle is substantially parallel to the inner wall surface of the hopper 31. Accordingly, the stirring blade 32A is disposed so as to be rotatable around the central axis A1 along the inner wall surface of the hopper 31.
図1〜図3に示すように、容積式の定量供給部40は、ホッパ31の下部開口部31bから供給される粉体Pを下流側の吸引ポンプ機構部Yに所定量ずつ定量供給する機構である。
具体的には、ホッパ31の下部開口部31bに接続される導入部41と、供給口43a及び排出口43bを備えたケーシング43と、ケーシング43内に回転可能に配設された計量回転体44と、計量回転体44を回転駆動する計量回転体駆動モータM2とを備えて構成される。
As shown in FIGS. 1 to 3, the positive displacement quantitative supply unit 40 is a mechanism for supplying a predetermined amount of powder P supplied from the lower opening 31 b of the hopper 31 to the suction pump mechanism Y on the downstream side. It is.
Specifically, the introduction part 41 connected to the lower opening part 31 b of the hopper 31, the casing 43 provided with the supply port 43 a and the discharge port 43 b, and the measuring rotator 44 rotatably disposed in the casing 43. And a metering rotator drive motor M2 that rotationally drives the metering rotator 44.
導入部41は、ホッパ31の下部開口部31bとケーシング43の上部に形成された供給口43aとを連通する筒状に形成され、最下端には、ケーシング43の供給口43aと同形状のスリット状の開口が形成されている。この導入部41は、ケーシング43の供給口43a側ほど細くなる先細り状に形成されている。当該スリット状の開口の形状は、ホッパ31の大きさ、粉体Pの供給量、粉体Pの特性等に応じて適宜設定することができるが、例えば、スリット状の開口の長さ方向の寸法を20〜100mm程度、幅方向の寸法を1〜5mm程度に設定するようにする。 The introduction part 41 is formed in a cylindrical shape that communicates the lower opening 31b of the hopper 31 and the supply port 43a formed in the upper part of the casing 43, and has a slit having the same shape as the supply port 43a of the casing 43 at the lowermost end. A shaped opening is formed. The introduction portion 41 is formed in a tapered shape that becomes thinner toward the supply port 43 a side of the casing 43. The shape of the slit-shaped opening can be appropriately set according to the size of the hopper 31, the supply amount of the powder P, the characteristics of the powder P, and the like. The dimension is set to about 20 to 100 mm, and the dimension in the width direction is set to about 1 to 5 mm.
ケーシング43は、概略直方体形状に形成され、水平方向(図1の左右方向)に対して45度傾斜した姿勢で、導入部41を介してホッパ31に接続されている。
図2及び図3に示すように、ケーシング43の上面には、導入部41のスリット状の開口に対応したスリット状の供給口43aが設けられ、ホッパ31の下部開口部31bからの粉体Pをケーシング43内に供給可能に構成されている。傾斜状に配置されたケーシング43の下方側の側面(図2において右側面)の下部には、計量回転体44にて定量供給された粉体Pを膨張室47を介して下流側の吸引ポンプ機構部Yに排出する排出口43bが設けられ、その排出口43bには、粉体排出管45が接続されている。当該膨張室47は、供給口43aから計量回転体44の粉体収容室44bに供給された粉体Pが定量供給されるケーシング43内の位置に設けられ、排出口43bから作用する負圧吸引力によって、供給口43aよりも低圧に維持される(例えば、−0、06MPa程度)。すなわち、排出口43bは、吸引ポンプ機構部Yの一次側に接続されることによって、負圧吸引力が膨張室47に作用し供給口43bよりも低圧状態に維持されるようにしている。計量回転体44の回転に伴って、各粉体収容室44bの状態が負圧状態(例えば、−0、06MPa程度)と当該負圧状態よりも高圧の状態に変化するように構成されている。
The casing 43 is formed in a substantially rectangular parallelepiped shape, and is connected to the hopper 31 via the introduction portion 41 in a posture inclined by 45 degrees with respect to the horizontal direction (left-right direction in FIG. 1).
As shown in FIGS. 2 and 3, the upper surface of the casing 43 is provided with a slit-shaped supply port 43 a corresponding to the slit-shaped opening of the introduction portion 41, and the powder P from the lower opening 31 b of the hopper 31 is provided. Can be supplied into the casing 43. At the lower part of the lower side surface (right side surface in FIG. 2) of the casing 43 arranged in an inclined manner, the powder P, which is quantitatively supplied by the metering rotator 44, is supplied to the downstream suction pump via the expansion chamber 47. A discharge port 43b for discharging to the mechanism part Y is provided, and a powder discharge pipe 45 is connected to the discharge port 43b. The expansion chamber 47 is provided at a position in the casing 43 to which the powder P supplied from the supply port 43a to the powder storage chamber 44b of the measuring rotator 44 is supplied in a fixed amount, and is operated by the negative pressure acting from the discharge port 43b. The force is maintained at a lower pressure than the supply port 43a (for example, about −0, 06 MPa). That is, the discharge port 43b is connected to the primary side of the suction pump mechanism Y so that the negative pressure suction force acts on the expansion chamber 47 and is maintained at a lower pressure than the supply port 43b. As the measurement rotating body 44 rotates, the state of each powder storage chamber 44b is changed to a negative pressure state (for example, about −0, 06 MPa) and a higher pressure state than the negative pressure state. .
計量回転体44は、計量回転体駆動モータM2の駆動軸48に配設した円盤部材49に、複数(例えば、8枚)の板状隔壁44aを円盤部材49の中心部を除いて放射状に等間隔に取り付けて構成され、周方向で等間隔に粉体収容室44bを複数区画(例えば、8室)形成するように構成されている。粉体収容室44bは、計量回転体44の外周面及び中心部において開口するように構成されている。計量回転体44の中心部には、開口閉鎖部材42が周方向に偏在して固定状に配設され、各粉体収容室44bの中心部側の開口をその回転位相に応じて閉塞或いは開放可能に構成されている。なお、粉体Pの供給量は、計量回転体44を回転駆動する計量回転体駆動モータM2による計量回転体44の回転数を変化させることで、調整できる。 The measuring rotator 44 has a disk member 49 disposed on the drive shaft 48 of the measuring rotator driving motor M <b> 2, and a plurality of (e.g., eight) plate-shaped partition walls 44 a radially excluding the central portion of the disk member 49. A plurality of powder storage chambers 44b (for example, eight chambers) are formed at equal intervals in the circumferential direction. The powder storage chamber 44 b is configured to open at the outer peripheral surface and the center portion of the measuring rotary body 44. An opening closing member 42 is unevenly distributed in the central direction of the measuring rotating body 44 and is fixedly arranged. The opening on the center side of each powder storage chamber 44b is closed or opened according to the rotation phase. It is configured to be possible. The supply amount of the powder P can be adjusted by changing the number of rotations of the measuring rotator 44 by the measuring rotator driving motor M2 that rotationally drives the measuring rotator 44.
計量回転体44の回転に伴って、各粉体収容室44bが、膨張室47に開放される膨張室開放状態、膨張室47及び供給口43aと連通しない第1密閉状態、供給口43aに開放される供給口開放状態、供給口43a及び膨張室47と連通しない第2密閉状態の順で、その状態が繰り返して変化するように構成されている。なお、計量回転体44の外周面側の開口が第1密閉状態及び第2密閉状態において閉鎖されるようにケーシング43が形成されるとともに、計量回転体44の中心部側の開口が第1密閉状態、供給口開放状態及び第2密閉状態において閉鎖されるように、開口閉鎖部材42がケーシング43に固定して配設される。 With the rotation of the measuring rotator 44, each powder storage chamber 44b is opened to the expansion chamber 47, opened to the expansion chamber 47, the first sealed state not communicating with the expansion chamber 47 and the supply port 43a, and opened to the supply port 43a. The supply port is opened and the supply port 43a and the expansion chamber 47 are communicated with each other in the order of the second sealed state. The casing 43 is formed such that the opening on the outer peripheral surface side of the measuring rotator 44 is closed in the first sealed state and the second sealed state, and the opening on the center side of the measuring rotator 44 is the first sealed. The opening closing member 42 is fixedly disposed on the casing 43 so as to be closed in the state, the supply port open state, and the second sealed state.
従って、定量供給装置Xにおいては、ホッパ31内に貯留された粉体Pが攪拌羽根32Aにより攪拌されながら定量供給部40に供給され、定量供給部40により、粉体Pが排出口43bから粉体排出管45を通して吸引ポンプ機構部Yに定量供給される。 Therefore, in the quantitative supply device X, the powder P stored in the hopper 31 is supplied to the quantitative supply unit 40 while being stirred by the stirring blade 32A, and the powder P is discharged from the discharge port 43b by the quantitative supply unit 40. A fixed amount is supplied to the suction pump mechanism Y through the body discharge pipe 45.
具体的に説明すると、定量供給部40の排出口43bの下流側に接続された吸引ポンプ機構部Yからの負圧吸引力により、ケーシング43内における膨張室47の圧力が負圧状態(例えば、−0、06MPa程度)となる。一方で、ホッパ31の上部開口部31aは大気開放されているので、ホッパ31内は大気圧程度の状態となる。膨張室47と計量回転体44の隙間を介して連通する導入部41の内部及び下部開口部31bの近傍は、上記負圧状態と大気圧状態との間の圧力状態となる。 More specifically, the pressure of the expansion chamber 47 in the casing 43 is in a negative pressure state (for example, for example, due to the negative pressure suction force from the suction pump mechanism Y connected to the downstream side of the discharge port 43b of the constant supply unit 40) −0, about 06 MPa). On the other hand, since the upper opening 31a of the hopper 31 is open to the atmosphere, the inside of the hopper 31 is in a state of about atmospheric pressure. The inside of the introduction part 41 and the vicinity of the lower opening 31b communicating with each other through the gap between the expansion chamber 47 and the metering rotator 44 are in a pressure state between the negative pressure state and the atmospheric pressure state.
この状態で、ホッパ31の内壁面及び下部開口部31bの近傍の粉体Pが、攪拌機構32の攪拌羽根32Aにより攪拌されることで、攪拌羽根32Aによるせん断作用によりホッパ31内の粉体Pが解砕され、一方、計量回転体44は計量回転体駆動モータM2により回転させられることで、空の粉体収容室44bが次々と供給口43aに連通する状態となる。そして、ホッパ31内の粉体Pは下部開口部31bから導入部41を流下し、次々と供給口43aに連通する状態となる計量回転体44の粉体収容室44bに所定量ずつ収容されて、その粉体収容室44bに収容された粉体Pは膨張室47に流下し、排出口43bから排出される。従って、定量供給装置Xにより、粉体Pを粉体排出管45を通して所定量ずつ連続して吸引ポンプ機構部Yの供給口11に定量供給することができる。 In this state, the powder P in the vicinity of the inner wall surface of the hopper 31 and the lower opening 31b is stirred by the stirring blade 32A of the stirring mechanism 32, whereby the powder P in the hopper 31 is sheared by the stirring blade 32A. On the other hand, the metering rotator 44 is rotated by the metering rotator drive motor M2, so that the empty powder storage chambers 44b are in continuous communication with the supply port 43a. Then, the powder P in the hopper 31 flows down through the introduction portion 41 from the lower opening 31b and is stored in a predetermined amount in the powder storage chamber 44b of the measuring rotary body 44 that is in communication with the supply port 43a one after another. The powder P stored in the powder storage chamber 44b flows down to the expansion chamber 47 and is discharged from the discharge port 43b. Therefore, the fixed amount supply device X can continuously supply the powder P to the supply port 11 of the suction pump mechanism Y continuously by a predetermined amount through the powder discharge pipe 45.
図1に示すように、粉体排出管45には、吸引ポンプ機構部Yの供給口11への粉体Pの供給を停止可能なシャッタバルブ46が配設されている。 As shown in FIG. 1, the powder discharge pipe 45 is provided with a shutter valve 46 that can stop the supply of the powder P to the supply port 11 of the suction pump mechanism Y.
〔溶媒供給部〕
図1に示すように、溶媒供給部50は、溶媒源51からの溶媒Rを、設定流量で吸引ポンプ機構部Yの供給口11に連続的に供給するように構成されている。
具体的には、溶媒供給部50は、溶媒Rを送出する溶媒源51と、溶媒源51から溶媒Rが送出される溶媒供給管52と、溶媒源51から溶媒供給管52に送出される溶媒Rの流量を設定流量に調整する流量調整バルブ(図示せず)と、設定流量に調整された溶媒Rを定量供給部40から定量供給される粉体Pに混合して供給口11に供給するミキシング機構60とを備えて構成されている。
(Solvent supply unit)
As shown in FIG. 1, the solvent supply unit 50 is configured to continuously supply the solvent R from the solvent source 51 to the supply port 11 of the suction pump mechanism unit Y at a set flow rate.
Specifically, the solvent supply unit 50 includes a solvent source 51 that sends the solvent R, a solvent supply pipe 52 that sends the solvent R from the solvent source 51, and a solvent that is sent from the solvent source 51 to the solvent supply pipe 52. A flow rate adjustment valve (not shown) that adjusts the flow rate of R to a set flow rate, and the solvent R adjusted to the set flow rate are mixed with powder P that is quantitatively supplied from the quantitative supply unit 40 and supplied to the supply port 11. And a mixing mechanism 60.
図4に示すように、ミキシング機構60は、粉体排出管45と溶媒供給管52とを供給口11に連通接続するミキシング部材61を備えて構成されている。
このミキシング部材61は、円筒状の供給口11よりも小径に構成されて、供給口11との間に環状のスリット63を形成すべく供給口11に挿入状態で配設される筒状部62、及び、環状のスリット63に全周にわたって連通する状態で供給口11の外周部に環状流路64を形成する環状流路形成部65を備えて構成されている。
ミキシング部材61には、粉体排出管45が筒状部62に連通する状態で接続されると共に、溶媒供給管52が環状流路64に対して溶媒Rを接線方向に供給するように接続される。
粉体排出管45、ミキシング部材61の筒状部62及び供給口11は、それらの軸心A2を供給方向が下向きとなる傾斜姿勢(水平面(図1の左右方向)に対する角度が45度程度)となるように傾斜させて配置されている。
As shown in FIG. 4, the mixing mechanism 60 includes a mixing member 61 that connects the powder discharge pipe 45 and the solvent supply pipe 52 to the supply port 11.
The mixing member 61 is configured to have a smaller diameter than the cylindrical supply port 11, and a cylindrical portion 62 disposed in an inserted state in the supply port 11 so as to form an annular slit 63 between the mixing member 61 and the supply port 11. And the annular flow path forming part 65 which forms the annular flow path 64 in the outer peripheral part of the supply port 11 in a state communicating with the annular slit 63 over the entire circumference is provided.
The powder discharge pipe 45 is connected to the mixing member 61 in a state of communicating with the cylindrical portion 62, and the solvent supply pipe 52 is connected to supply the solvent R to the annular flow path 64 in the tangential direction. The
The powder discharge pipe 45, the cylindrical portion 62 of the mixing member 61, and the supply port 11 are inclined such that the supply direction of the axis A2 is downward (the angle with respect to the horizontal plane (left and right direction in FIG. 1) is about 45 degrees). It is arranged so as to be inclined.
つまり、定量供給部40の排出口43bから粉体排出管45に排出された粉体Pは、ミキシング部材61の筒状部62を通して軸心A2に沿って供給口11に導入される。一方、溶媒Rは、環状流路64に接線方向から供給されるので、環状流路64の内周側に形成される環状のスリット63を介して、切れ目のない中空円筒状の渦流の状態で供給口11に供給される。
従って、円筒状の供給口11により、粉体Pと溶媒Rとが均等に予備混合され、その予備混合物Fpが吸引ポンプ機構部Yの供給室13内に吸引導入される。
That is, the powder P discharged from the discharge port 43b of the fixed amount supply unit 40 to the powder discharge tube 45 is introduced into the supply port 11 along the axis A2 through the cylindrical portion 62 of the mixing member 61. On the other hand, since the solvent R is supplied to the annular flow path 64 from the tangential direction, the solvent R is in a state of a hollow cylindrical vortex without a break through the annular slit 63 formed on the inner peripheral side of the annular flow path 64. It is supplied to the supply port 11.
Accordingly, the powder P and the solvent R are uniformly premixed by the cylindrical supply port 11 and the premixed mixture Fp is sucked into the supply chamber 13 of the suction pump mechanism Y.
〔吸引ポンプ機構部〕
図1、図4〜図7に基づいて、吸引ポンプ機構部Yについて説明を加える。
図4に示すように、吸引ポンプ機構部Yは、両端開口が前壁部2と後壁部3とで閉じられた円筒状の外周壁部4を備えた本体ケーシング1を備え、その本体ケーシング1の内部に同心状で回転駆動自在に設けられたロータ5と、その本体ケーシング1の内部に同心状で前壁部2に固定配設された円筒状のステータ7と、ロータ5を回転駆動するポンプ駆動モータM3等を備えて構成されている。
[Suction pump mechanism]
The suction pump mechanism Y will be described based on FIGS. 1 and 4 to 7 .
As shown in FIG. 4, the suction pump mechanism Y includes a main casing 1 having a cylindrical outer peripheral wall 4 whose both ends are closed by a front wall 2 and a rear wall 3. 1 is a concentric rotor 5 that is concentrically provided within the main body casing 1, a cylindrical stator 7 that is concentrically fixed to the front wall 2 inside the main body casing 1, and the rotor 5. And a pump drive motor M3 and the like.
図5にも示すように、ロータ5の径方向の外方側には、複数の回転翼6が、前壁部2側である前方側(図4の左側)に突出し且つ周方向に等間隔で並ぶ状態でロータ5と一体的に備えられている。
円筒状のステータ7には、複数の透孔7a,7bが周方向に夫々並べて備えられ、そのステータ7が、ロータ5の前方側(図4の左側)で且つ回転翼6の径方向の内側に位置させて前壁部2に固定配設されて、そのステータ7と本体ケーシング1の外周壁部4との間に、回転翼6が周回する環状の翼室8が形成される。
As shown also in FIG. 5, on the radially outer side of the rotor 5, a plurality of rotary blades 6 protrude to the front side (left side in FIG. 4) that is the front wall portion 2 side and are equally spaced in the circumferential direction. Are provided integrally with the rotor 5.
The cylindrical stator 7 is provided with a plurality of through holes 7a and 7b arranged in the circumferential direction, and the stator 7 is on the front side of the rotor 5 (left side in FIG. 4) and on the inner side in the radial direction of the rotor blades 6. An annular blade chamber 8 around which the rotor blade 6 circulates is formed between the stator 7 and the outer peripheral wall portion 4 of the main body casing 1.
図4〜図6に示すように、ミキシング機構60にて粉体Pと溶媒Rとが予備混合された予備混合物Fpを回転翼6の回転により本体ケーシング1の内部に吸引導入する供給口11が、前壁部2の中心軸(本体ケーシング1の軸心A3)よりも外周側に偏移した位置に設けられている。
図4、図6に示すように、ケーシング1の前壁部2の内面に環状溝10が形成され、環状溝10と連通する状態で供給口11が設けられている。
図4及び図5に示すように、粉体Pと溶媒Rとが混合されて生成されたスラリーFを吐出する円筒状の吐出部12が、本体ケーシング1の円筒状の外周壁部4の周方向における1箇所に、その外周壁部4の接線方向に延びて翼室8に連通する状態で設けられている。
As shown in FIGS. 4 to 6 , the supply port 11 for sucking and introducing the premixed mixture Fp, in which the powder P and the solvent R are premixed by the mixing mechanism 60, into the inside of the main casing 1 by the rotation of the rotor blades 6. The center wall of the front wall 2 (the axis A3 of the main body casing 1) is shifted to the outer peripheral side.
As shown in FIGS. 4 and 6 , an annular groove 10 is formed on the inner surface of the front wall portion 2 of the casing 1, and a supply port 11 is provided in communication with the annular groove 10.
As shown in FIGS. 4 and 5, the cylindrical discharge portion 12 that discharges the slurry F generated by mixing the powder P and the solvent R is a peripheral portion of the cylindrical outer peripheral wall portion 4 of the main body casing 1. It is provided at one location in the direction so as to extend in the tangential direction of the outer peripheral wall 4 and communicate with the blade chamber 8.
図1及び図4に示すように、この実施形態では、吐出部12から吐出されたスラリーFは、吐出路18を通して再循環機構部70に供給され、その再循環機構部70の分離部71にて気泡が分離された未溶解スラリーFrを、循環路16を介して本体ケーシング1内に循環供給する導入口17が本体ケーシング1の前壁部2の中央部(軸心A3と同心状)に設けられている。
又、図4〜図6に示すように、ステータ7の内周側を前壁部2側の供給室13とロータ5側の導入室14とに区画する区画板15が、ロータ5の前方側に当該ロータ5と一体回転する状態で設けられると共に、区画板15の前壁部2側に掻出翼9が設けられている。掻出翼9は、同心状に、周方向において均等間隔で複数(図6では、4つ)備えられ、各掻出翼9がその先端部9Tを環状溝10内に進入した状態でロータ5と一体的に周回可能に配設されている。
As shown in FIGS. 1 and 4, in this embodiment, the slurry F discharged from the discharge unit 12 is supplied to the recirculation mechanism unit 70 through the discharge path 18 and is supplied to the separation unit 71 of the recirculation mechanism unit 70. undissolved slurry Fr, central portion of the front wall 2 of the circulation path 16 to circulate and supply inlet 17 in the body casing 1 through the main body casing 1 which bubbles have been separated Te (axis a 3 concentrically) Is provided.
4 to 6 , a partition plate 15 that divides the inner peripheral side of the stator 7 into a supply chamber 13 on the front wall 2 side and an introduction chamber 14 on the rotor 5 side is provided on the front side of the rotor 5. And a scraping blade 9 on the front wall 2 side of the partition plate 15. A plurality of scraping blades 9 are concentrically provided at equal intervals in the circumferential direction (four in FIG. 6), and each of the scraping blades 9 enters the annular groove 10 in the state where each of the scraping blades 9 enters the annular groove 10. And are arranged so as to be able to circulate integrally.
供給室13及び導入室14は、ステータ7の複数の透孔7a,7bを介して翼室8と連通されるように構成され、供給口11が供給室13に連通し、導入口17が導入室14に連通するように構成されている。
具体的には、供給室13と翼室8とは、ステータ7における供給室13に臨む部分に周方向に等間隔で配設された複数の供給室側透孔7aにて連通され、導入室14と翼室8とは、ステータ7における導入室14に臨む部分に周方向に等間隔で配設された複数の導入室側透孔7bにて連通されている。
The supply chamber 13 and the introduction chamber 14 are configured to communicate with the blade chamber 8 through a plurality of through holes 7 a and 7 b of the stator 7, the supply port 11 communicates with the supply chamber 13, and the introduction port 17 is introduced. It is configured to communicate with the chamber 14.
Specifically, the supply chamber 13 and the blade chamber 8 are communicated with each other through a plurality of supply chamber side through-holes 7a arranged at equal intervals in the circumferential direction at a portion facing the supply chamber 13 in the stator 7, and the introduction chamber. 14 and the blade chamber 8 are communicated with each other through a plurality of introduction chamber side through-holes 7b disposed at equal intervals in the circumferential direction at a portion facing the introduction chamber 14 in the stator 7.
吸引ポンプ機構部Yの各部について、説明を加える。
図4に示すように、ロータ5は、その前面が概ね円錐台状に膨出する形状に構成されると共に、その外周側に、複数の回転翼6が前方に突出する状態で等間隔に並べて設けられている。なお、図5では、周方向に等間隔に10個の回転翼6が配設されている。また、この回転翼6は、内周側から外周側に向かうに連れて、回転方向後方に傾斜するようにロータ5の外周側から内周側に突出形成されており、回転翼6の先端部の内径は、ステータ7の外径よりも若干大径に形成されている。
このロータ5が、本体ケーシング1内において本体ケーシング1と同心状に位置する状態で、後壁部3を貫通して本体ケーシング1内に挿入されたポンプ駆動モータM3の駆動軸19に連結されて、そのポンプ駆動モータM3により回転駆動される。
このロータ5が、その軸心方向視(図5に示すような図4のV−V方向視)において回転翼6の先端部が前側となる向きに回転駆動されることにより、回転翼6の回転方向の後側となる面(背面)6aには、いわゆる局所沸騰(キャビテーション)が発生するように構成されている。
A description will be given of each part of the suction pump mechanism Y.
As shown in FIG. 4, the rotor 5 is configured to have a shape in which the front surface bulges substantially in a truncated cone shape, and is arranged on the outer peripheral side at equal intervals with a plurality of rotating blades 6 protruding forward. Is provided. In FIG. 5, ten rotating blades 6 are arranged at equal intervals in the circumferential direction. Further, the rotor blade 6 is formed to project from the outer periphery side of the rotor 5 to the inner periphery side so as to incline backward in the rotation direction from the inner periphery side toward the outer periphery side. The inner diameter is slightly larger than the outer diameter of the stator 7.
The rotor 5 is connected to a drive shaft 19 of a pump drive motor M3 that passes through the rear wall portion 3 and is inserted into the main body casing 1 in a state of being concentric with the main body casing 1 in the main body casing 1. The pump drive motor M3 is rotationally driven.
The rotor 5 is rotationally driven in a direction in which the tip end portion of the rotor blade 6 becomes the front side when viewed in the axial direction (viewed in the direction VV in FIG. 4 as shown in FIG. 5). A so-called local boiling (cavitation) is generated on the rear surface (back surface) 6a in the rotational direction.
図4、図6及び図7に示すように、区画板15は、ステータ7の内径よりも僅かに小さい外径を有する概ね漏斗状に構成されている。この漏斗状の区画板15は、具体的には、その中央部に、頂部が円筒状に突出する筒状摺接部15aにて開口された漏斗状部15bを備えると共に、その漏斗状部15bの外周部に、前面及び後面共に本体ケーシング1の軸心A3に直交する状態となる環状平板部15cを備える形状に構成されている。
そして、図4及び図5に示すように、この区画板15が、頂部の筒状摺接部15aが本体ケーシング1の前壁部2側を向く姿勢で、周方向に等間隔を隔てた複数箇所(この実施形態では、4箇所)に配設された間隔保持部材20を介して、ロータ5の前面の取付部5aに取り付けられる。
As shown in FIGS. 4, 6, and 7 , the partition plate 15 is configured in a generally funnel shape having an outer diameter that is slightly smaller than the inner diameter of the stator 7. Specifically, the funnel-shaped partition plate 15 includes a funnel-shaped portion 15b opened at a central sliding portion of a cylindrical sliding contact portion 15a protruding in a cylindrical shape, and the funnel-shaped portion 15b. The outer peripheral portion of the main body casing 1 is configured to have an annular flat plate portion 15c that is in a state orthogonal to the axis A3 of the main body casing 1.
As shown in FIGS. 4 and 5, the partition plate 15 has a plurality of cylindrical plates 15 which are spaced at equal intervals in the circumferential direction with the top cylindrical sliding contact portion 15 a facing the front wall 2 side of the main casing 1. It is attached to the attachment portion 5a on the front surface of the rotor 5 via the spacing members 20 arranged at the places (four places in this embodiment).
図5及び図7(c)に示すように、区画板15を複数箇所夫々で間隔保持部材20を介してロータ5に取り付ける際には、攪拌羽根21が、本体ケーシング1の後壁部3側に向く姿勢で区画板15に一体的に組み付けられ、ロータ5が回転駆動されると、4枚の攪拌羽根21がロータ5と一体的に回転するように構成されている。 As shown in FIG. 5 and FIG. 7 (c), the in mounting the rotor 5 via a spacing member 20 the partition plate 15 at each of the plurality locations husband stirring blade 21, the wall portion 3 side after the main casing 1 When the rotor 5 is rotationally driven, the four stirring blades 21 are configured to rotate integrally with the rotor 5.
図4及び図6に示すように、この実施形態では、円筒状の導入口17が、本体ケーシング1と同心状で、その本体ケーシング1の前壁部2の中心部に設けられている。この導入口17には、循環路16の内径よりも小径で、区画板15の筒状摺接部15aよりも小径となり流路面積が小さな絞り部14aが形成されている。ロータ5の回転翼6が回転することにより、吐出部12を介してスラリーFが吐出され、導入口17の絞り部14aを介して未溶解スラリーFrが導入されることになるので、吸引ポンプ機構部Y内が減圧される。 As shown in FIGS. 4 and 6 , in this embodiment, the cylindrical introduction port 17 is concentric with the main body casing 1 and is provided at the center of the front wall portion 2 of the main body casing 1. The introduction port 17 is formed with a narrowed portion 14a that is smaller in diameter than the inner diameter of the circulation path 16 and smaller in diameter than the cylindrical sliding contact portion 15a of the partition plate 15 and has a small flow path area. By rotating the rotor blade 6 of the rotor 5, the slurry F is discharged through the discharge unit 12, and the undissolved slurry Fr is introduced through the throttle unit 14 a of the introduction port 17. The portion Y is depressurized.
図4〜図6に示すように、供給口11は、その本体ケーシング1内に開口する開口部(入口部)が、環状溝10における周方向の一部を内部に含む状態で、本体ケーシング1内に対する導入口17の開口部の横側方に位置するように、前壁部2に設けられている。又、供給口11は、平面視(図1及び図4の上下方向視)において軸心A2が本体ケーシング1の軸心A3と平行となり、且つ、ケーシング1の軸心A3に直交する水平方向視(図1及び図4の紙面表裏方向視)において、軸心A2が本体ケーシング1の前壁部2に近付くほど本体ケーシング1の軸心A3に近づく下向きの傾斜姿勢で、本体ケーシング1の前壁部2に設けられている。ちなみに、供給口11の水平方向(図1及び図4の左右方向)に対する下向きの傾斜角度は、上述したように45度程度である。 As shown in FIGS. 4 to 6 , the supply port 11 is configured so that the opening (inlet portion) that opens into the main body casing 1 includes a part of the annular groove 10 in the circumferential direction inside. It is provided in the front wall part 2 so that it may be located in the side of the opening part of the inlet 17 with respect to the inside. Further, the supply port 11 is viewed in a horizontal direction in which the axis A2 is parallel to the axis A3 of the main casing 1 and is orthogonal to the axis A3 of the casing 1 in a plan view (viewed in the vertical direction in FIGS. 1 and 4). 1 and 4, the front wall of the main body casing 1 is in a downward inclined posture that approaches the axis A3 of the main body casing 1 as the axial center A2 approaches the front wall portion 2 of the main body casing 1. Part 2 is provided. Incidentally, the downward inclination angle of the supply port 11 with respect to the horizontal direction (left-right direction in FIGS. 1 and 4) is about 45 degrees as described above.
図4及び図6に示すように、ステータ7は、本体ケーシング1の前壁部2の内面(ロータ5に対向する面)に取り付けられて、本体ケーシング1の前壁部2とステータ7とが一体となるように固定されている。ステータ7において、供給室13に臨む部分に配設された複数の供給室側透孔7aは、概略円形状に形成され、供給室13の流路面積よりも複数の供給室側透孔7aの合計流路面積が小さくなるように設定されており、また、導入室14に臨む部分に配設された複数の導入室側透孔7bは、概略楕円形状に形成され、導入室14の流路面積よりも複数の供給室側透孔7bの合計流路面積が小さくなるように設定されている。ロータ5の回転翼6が回転することにより、吐出部12を介してスラリーFが吐出され、供給室13の供給室側透孔7aを介して予備混合物Fpが供給されるとともに、導入口17を介して未溶解スラリーFrが導入されることになるので、吸引ポンプ機構部Y内が減圧される。 As shown in FIGS. 4 and 6 , the stator 7 is attached to the inner surface (the surface facing the rotor 5) of the front wall portion 2 of the main body casing 1, and the front wall portion 2 of the main body casing 1 and the stator 7 are connected. It is fixed so as to be integrated. In the stator 7, the plurality of supply chamber side through-holes 7 a disposed in the portion facing the supply chamber 13 are formed in a substantially circular shape, and the plurality of supply chamber side through-holes 7 a are larger than the flow passage area of the supply chamber 13. The total flow passage area is set to be small, and the plurality of introduction chamber side through holes 7b disposed in the portion facing the introduction chamber 14 are formed in a substantially elliptical shape, and the flow passage of the introduction chamber 14 is formed. The total flow passage area of the plurality of supply chamber side through holes 7b is set to be smaller than the area. As the rotor blades 6 of the rotor 5 rotate, the slurry F is discharged through the discharge unit 12, the preliminary mixture Fp is supplied through the supply chamber side through hole 7 a of the supply chamber 13, Since the undissolved slurry Fr is introduced through the suction pump mechanism Y, the pressure in the suction pump mechanism Y is reduced.
図6及び図7に示すように、この実施形態では、各掻出翼9が棒状に形成され、ロータ5の径方向視(図7(b)の紙面表裏方向視)で、当該棒状の掻出翼9の先端側ほど前壁部2側に位置し、且つ、ロータ5の軸心方向視(図7(a)の紙面表裏方向視)で、当該棒状の掻出翼9の先端側ほどロータ5の径方向内方側に位置する傾斜姿勢で、当該棒状の掻出翼9の基端部9Bがロータ5と一体回転するように固定され、ロータ5が、その軸心方向視(図7(a)の紙面表裏方向視)において掻出翼9の先端が前側となる向き(図4〜図7において矢印にて示す向き)に回転駆動される。 As shown in FIGS. 6 and 7, in this embodiment, the raking blades 9 is formed into a rod, viewed in the radial direction of the rotor 5 (the paper front and rear direction as viewed in FIG. 7 (b)), of the rod-like take- located on the distal end side as the front wall portion 2 side of the Detsubasa 9, and, in the axial direction when viewed in the rotor 5 (the paper front and rear direction as viewed in FIG. 7 (a)), as the distal end side of the raking blades 9 of the rod-like The base end portion 9B of the rod-shaped scraping blade 9 is fixed so as to rotate integrally with the rotor 5 in an inclined posture located on the radially inner side of the rotor 5, and the rotor 5 is viewed in the axial direction (see FIG. 7 (a) when viewed from the front and back of the paper surface), the scraping blade 9 is rotationally driven in a direction (the direction indicated by an arrow in FIGS. 4 to 7 ) in which the tip of the scraping blade 9 is the front side.
図5〜図7に基づいて、掻出翼9について説明を加える。
掻出翼9は、区画板15に固定される基端部9B、供給室13に露呈する状態となる中間部9M、環状溝10に嵌め込まれる(即ち、進入する)状態となる先端部9Tを基端から先端に向けて一連に備えた棒状に構成されている。
Based on FIGS. 5 to 7 , the raking blade 9 will be described.
The scraping blade 9 includes a base end portion 9B fixed to the partition plate 15, an intermediate portion 9M that is exposed to the supply chamber 13, and a tip end portion 9T that is fitted in (that is, enters) the annular groove 10. It is configured in a rod shape provided in a series from the proximal end to the distal end.
図5、図6、図7(b)に示すように、掻出翼9の基端部9Bは、概ね矩形板状に構成されている。
図5、図6、図7(a)及び(b)に示すように、掻出翼9の中間部9Mは、横断面形状が概ね三角形状になる概ね三角柱状に構成されている(特に、図5参照)。そして、掻出翼9が上述の如き傾斜姿勢で設けられることにより、三角柱状の中間部9Mの三側面のうちのロータ5の回転方向前側を向く一側面9m(以下、放散面と記載する場合がある)は、ロータ5の回転方向前側に向けて傾斜する前下がり状で、しかも、ロータ5の径方向に対して径方向外方側に向く(以下、斜め外向きと記載する場合がある)ように構成されている(特に、図6、図7参照)。
As shown in FIGS. 5, 6 , and 7 (b), the base end portion 9 </ b > B of the scraping blade 9 is generally formed in a rectangular plate shape.
As shown in FIGS. 5, 6 , 7 (a) and 7 (b ), the intermediate portion 9M of the scraping blade 9 is configured in a generally triangular prism shape with a substantially triangular cross-sectional shape (in particular, (See FIG. 5). Then, by providing the scraping blade 9 in the inclined posture as described above, one side surface 9m (hereinafter referred to as a radiating surface) facing the front side in the rotational direction of the rotor 5 among the three side surfaces of the triangular columnar intermediate portion 9M. Is downwardly inclined toward the front side in the rotational direction of the rotor 5 and is directed radially outward with respect to the radial direction of the rotor 5 (hereinafter sometimes referred to as diagonally outward). (See FIGS. 6 and 7 in particular).
つまり、棒状の掻出翼9が、上述の如き傾斜姿勢で設けられることにより、掻出翼9のうち供給室13に露呈する中間部9Mが環状溝10に嵌め込まれる先端部9Tよりもロータ5の径方向外方に位置し、しかも、その中間部9Mの回転方向前側を向く放散面9mが、ロータ5の回転方向前側に向けて傾斜する前下がり状で、しかも、ロータ5の径方向に対して斜め外向きに傾斜している。これにより、掻出翼9の先端部9Tにより環状溝10から掻き出された予備混合物Fpは、掻出翼9の中間部9Mの放散面9mにより、供給室13内においてロータ5の径方向外方側に向けて流動するように案内される。 That is, by providing the bar-like scraping blade 9 in the inclined posture as described above, the intermediate portion 9M exposed to the supply chamber 13 of the scraping blade 9 is more than the tip portion 9T in which the annular groove 10 is fitted. Further, the radiating surface 9m facing the front side in the rotational direction of the intermediate portion 9M is in a front-falling shape inclined toward the front side in the rotational direction of the rotor 5, and in the radial direction of the rotor 5. It is inclined diagonally outward. Thereby, the preliminary mixture Fp scraped from the annular groove 10 by the tip portion 9T of the scraping blade 9 is radially outside the rotor 5 in the supply chamber 13 by the diffusion surface 9m of the intermediate portion 9M of the scraping blade 9. Guided to flow toward the other side.
図6、図7(a)及び(b)に示すように、掻出翼9の先端部9Tは、横断面形状が概ね矩形状になる概ね四角柱状であり、ロータ5の軸心方向視(図7(a)の紙面表裏方向視)において、四側面のうちのロータ5の径方向外方側に向く外向き側面9oが環状溝10の内面における径方向内方側を向く内向き内面に沿い、且つ、四側面のうちのロータ5の径方向内方側に内向き側面9iが環状溝10の内面における径方向外方側を向く外向き内面に沿う状態となる弧状に構成されている。
又、四角柱状の先端部9Tの四側面のうちの、ロータ5の回転方向前側を向く掻き出し面9fは、ロータ5の回転方向前側に向けて傾斜する前下がり状で、しかも、ロータ5の径方向に対して径方向外方側に向く(以下、斜め外向きと記載する場合がある)になるように構成されている。
これにより、掻出翼9の先端部9Tにより環状溝10から掻き出された予備混合物Fpは、掻出翼9の先端部9Tの掻き出し面9fにより、ロータ5の径方向外方側に向けて供給室13内に放出されることになる。
更に、掻出翼9の先端部9Tの先端面9tは、その先端部9Tが環状溝10に嵌め込まれた状態で環状溝10の底面と平行になるように構成されている。
6, as shown in FIG. 7 (a) and (b), the tip portion 9T of raking blades 9, Ri generally quadrangular prism der the cross-sectional shape is a generally rectangular shape, the axial direction view of the rotor 5 In (the front and back directions in FIG. 7 (a)), the inwardly facing inner surface in which the outwardly facing side surface 9o facing the radially outward side of the rotor 5 among the four side surfaces faces the radially inward side of the inner surface of the annular groove 10 And the inward side surface 9i is formed in an arc shape along the outward inner surface facing the radially outer side of the inner surface of the annular groove 10 on the radially inner side of the rotor 5 of the four side surfaces. Yes.
Of the four side surfaces of the quadrangular columnar tip portion 9T, the scraped surface 9f facing the front side in the rotational direction of the rotor 5 is in a front-falling shape inclined toward the front side in the rotational direction of the rotor 5, and the diameter of the rotor 5 It is configured to face radially outward with respect to the direction (hereinafter sometimes referred to as diagonally outward).
Thereby, the preliminary mixture Fp scraped from the annular groove 10 by the tip portion 9T of the scraping blade 9 is directed radially outward of the rotor 5 by the scraping surface 9f of the tip portion 9T of the scraping blade 9. It will be discharged into the supply chamber 13.
Furthermore, the tip surface 9t of the tip portion 9T of the scraping blade 9 is configured to be parallel to the bottom surface of the annular groove 10 in a state where the tip portion 9T is fitted in the annular groove 10.
また、ロータ5が、その軸心方向視(図7(a)の紙面表裏方向視)において掻出翼9の先端が前側となる向きに回転駆動されると、掻出翼9の基端部9B、中間部9M、先端部9Tそれぞれに、回転方向の後側となる面(背面)9aが形成される。この背面9aには、掻出翼9が回転することにより、いわゆる局所沸騰(キャビテーション)が発生するように構成されている。 The rotor 5 is, if the axial direction when viewed from the tip of the scraping blade 9 in (paper front and rear direction as viewed in FIG. 7 (a)) is driven to rotate in the direction as the front, proximal end of the raking blades 9 A surface (back surface) 9a which is the rear side in the rotation direction is formed on each of 9B, the intermediate portion 9M, and the tip portion 9T. The rear surface 9a is configured such that so-called local boiling (cavitation) occurs when the scraping blade 9 rotates.
上述のような形状に構成された4個の掻出翼9が、上述の如き傾斜姿勢で、中心角で90度ずつ間隔を隔てて周方向に並べた形態で、夫々、基端部9Bを区画板15の環状平板部15cに固定して設けられている。 The four scraped wings 9 configured in the above-described shape are arranged in the circumferential direction at intervals of 90 degrees at the central angle in the inclined posture as described above, and the base end portions 9B are respectively arranged. It is fixed to the annular flat plate portion 15 c of the partition plate 15.
図4に示すように、掻出翼9が設けられた区画板15が、間隔保持部材20によりロータ5の前面と間隔を隔てた状態でロータ5の前面の取付部5aに取り付けられ、このロータ5が、区画板15の筒状摺接部15aが導入口17に摺接回転可能に嵌めこまれた状態で、本体ケーシング1内に配設される。
すると、ロータ5の膨出状の前面と区画板15の後面との間に、本体ケーシング1の前壁部2側ほど小径となる先細り状の導入室14が形成され、導入口17が区画板15の筒状摺接部15aを介して導入室14に連通するように構成されている。
又、本体ケーシング1の前壁部2と区画板15の前面との間に、供給口11に連通する環状の供給室13が形成される。
As shown in FIG. 4, the partition plate 15 provided with the scraping blades 9 is attached to the attachment portion 5 a on the front surface of the rotor 5 in a state of being separated from the front surface of the rotor 5 by the interval holding member 20. 5 is disposed in the main body casing 1 in a state where the cylindrical sliding contact portion 15a of the partition plate 15 is fitted in the introduction port 17 so as to be slidable and rotatable.
Then, a tapered introduction chamber 14 having a smaller diameter toward the front wall 2 side of the main casing 1 is formed between the bulging front surface of the rotor 5 and the rear surface of the partition plate 15, and the introduction port 17 serves as the partition plate. It is configured to communicate with the introduction chamber 14 via 15 cylindrical sliding contact portions 15a.
An annular supply chamber 13 communicating with the supply port 11 is formed between the front wall portion 2 of the main casing 1 and the front surface of the partition plate 15.
そして、ロータ5が回転駆動されると、筒状摺接部15aが導入口17に摺接する状態で、区画板15がロータ5と一体的に回転することになり、ロータ5及び区画板15が回転する状態でも、導入口17が区画板15の筒状摺接部15aを介して導入室14に連通する状態が維持されるように構成されている。 When the rotor 5 is rotationally driven, the partition plate 15 rotates integrally with the rotor 5 in a state where the cylindrical sliding contact portion 15a is in sliding contact with the introduction port 17, and the rotor 5 and the partition plate 15 are Even in a rotating state, the state where the introduction port 17 communicates with the introduction chamber 14 via the cylindrical sliding contact portion 15a of the partition plate 15 is maintained.
〔再循環機構部〕
再循環機構部(分離部の一例)70は、円筒状容器71内において比重によって溶解液を分離するように構成され、図1に示すように、吸引ポンプ機構部Yの吐出部12から吐出路18を通して供給されるスラリーFから、完全に溶解していない粉体Pを含む可能性がある状態の未溶解スラリーFrを循環路16に、粉体Pが略完全に溶解した状態のスラリーFを排出路22にそれぞれ分離するように構成されている。吐出路18及び循環路16は、夫々、円筒状容器71の下部に接続され、排出路22は、円筒状容器71の上部とスラリーFの供給先80とに接続される。
ここで、再循環機構部70は、図示しないが、吐出路18が接続される導入パイプを円筒状容器71の底面から内部に突出して配設し、円筒状容器71の上部に排出路22に接続される排出部を備えるとともに、下部に循環路16に接続される循環部を備え、導入パイプの吐出上端に、導入パイプから吐出されるスラリーFの流れを旋回させる捻り板を配設して構成されている。これにより、スラリーF内から溶媒Rの気泡を分離して、循環路16に循環供給される未溶解スラリーFrから溶媒Rの気泡を分離した状態で導入室14内に供給することができる。
[Recirculation mechanism]
The recirculation mechanism part (an example of a separation part) 70 is configured to separate the lysate by specific gravity in the cylindrical container 71, and as shown in FIG. 1, the discharge path from the discharge part 12 of the suction pump mechanism part Y The undissolved slurry Fr that may contain the powder P that is not completely dissolved is supplied to the circulation path 16 from the slurry F that is supplied through the slurry F. It is comprised so that it may isolate | separate into the discharge path 22, respectively. The discharge path 18 and the circulation path 16 are each connected to the lower part of the cylindrical container 71, and the discharge path 22 is connected to the upper part of the cylindrical container 71 and the supply destination 80 of the slurry F.
Here, although not shown, the recirculation mechanism unit 70 is provided with an introduction pipe to which the discharge path 18 is connected protruding from the bottom surface of the cylindrical container 71, and is connected to the discharge path 22 at the upper part of the cylindrical container 71. A twisting plate for turning the flow of the slurry F discharged from the introduction pipe is provided at the upper discharge end of the introduction pipe with a discharge portion connected to the circulation path 16 at the lower part. It is configured. Thereby, the bubbles of the solvent R can be separated from the slurry F, and the bubbles of the solvent R can be supplied into the introduction chamber 14 in a state of being separated from the undissolved slurry Fr circulated and supplied to the circulation path 16.
〔制御部〕
分散システム100に備えられる制御部は、図示しないが、CPUや記憶部等を備えた公知の演算処理装置からなり、分散システム100を構成する定量供給装置X、吸引ポンプ機構部Y、溶媒供給部50等の各機器の運転を制御可能に構成されている。
特に、制御部は、ロータ5(回転翼6)の回転数を制御可能に構成され、ステータ7の供給室側透孔7a及び導入室側透孔7b(絞り透孔)の出口領域の圧力が当該出口領域の全周に亘って溶媒Rの飽和蒸気圧(25℃の水の場合、3.169kPa)以下となるように回転翼6の回転数を設定し、当該設定された回転数で回転翼6を回転することで、少なくともステータ7の供給室側透孔7a及び導入室側透孔7bを通過した直後の翼室8内の領域を、翼室8内の全周に亘って連続して、溶媒Rの微細気泡(マイクロバブル)が多数発生した微細気泡領域として形成させることができるように構成されている。
(Control part)
Although not shown, the control unit provided in the dispersion system 100 includes a known arithmetic processing device including a CPU, a storage unit, and the like, and includes a quantitative supply device X, a suction pump mechanism unit Y, and a solvent supply unit that constitute the dispersion system 100. The operation of each device such as 50 can be controlled.
In particular, the control unit is configured to be able to control the rotation speed of the rotor 5 (rotary blade 6), and the pressure in the outlet region of the supply chamber side through hole 7a and the introduction chamber side through hole 7b (throttle through hole) of the stator 7 is controlled. The rotation speed of the rotor blade 6 is set so that the saturated vapor pressure of the solvent R (3.169 kPa in the case of water at 25 ° C.) or less is set over the entire circumference of the outlet region, and the rotation speed is set. By rotating the blade 6, at least the region in the blade chamber 8 immediately after passing through the supply chamber side through hole 7 a and the introduction chamber side through hole 7 b of the stator 7 is continued over the entire circumference of the blade chamber 8. Thus, the microbubble region of the solvent R can be formed as a microbubble region where a large number of microbubbles are generated.
〔分散システムの動作〕
次に、この分散システム100の動作について説明する。
まず、定量供給装置Xを停止し、シャッタバルブ46を閉止して粉体排出管45を介する粉体Pの吸引を停止した状態で、溶媒供給部50から溶媒Rのみを供給しながらロータ5を回転させ、吸引ポンプ機構部Yの運転を開始する。所定の運転時間が経過して、吸引ポンプ機構部Y内が、負圧状態(例えば、−0.06MPa程度の真空状態)となると、シャッタバルブ46を開放する。これによって、定量供給装置Xの膨張室47を負圧状態(−0.06MPa程度)とし、導入部41の内部及びホッパ31の下部開口部31b近傍を当該負圧状態と大気圧状態との間の圧力状態にする。
[Distributed system operation]
Next, the operation of the distributed system 100 will be described.
First, the quantitative supply device X is stopped, the shutter valve 46 is closed, and the suction of the powder P through the powder discharge pipe 45 is stopped, and the rotor 5 is moved while supplying only the solvent R from the solvent supply unit 50. Rotate and start the operation of the suction pump mechanism Y. When the predetermined operating time has elapsed and the inside of the suction pump mechanism Y is in a negative pressure state (for example, a vacuum state of about −0.06 MPa), the shutter valve 46 is opened. As a result, the expansion chamber 47 of the quantitative supply device X is brought into a negative pressure state (about −0.06 MPa), and the inside of the introduction part 41 and the vicinity of the lower opening 31b of the hopper 31 are between the negative pressure state and the atmospheric pressure state. To the pressure state.
そして、定量供給装置Xを作動させ、ホッパ31内に貯留された粉体Pを、攪拌羽根32Aの攪拌作用及び吸引ポンプ機構部Yの負圧吸引力により、ホッパ31の下部開口部31bから定量供給部40の膨張室47を介してミキシング機構60のミキシング部材61に所定量ずつ連続的に定量供給する。並行して、溶媒供給部50を作動させ、吸引ポンプ機構部Yの負圧吸引力により、溶媒Rをミキシング機構60のミキシング部材61に所定量ずつ連続的に定量供給する。
ミキシング機構60のミキシング部材61からは、粉体Pがミキシング部材61の筒状部62を通して供給口11に供給されると共に、溶媒Rが、環状のスリット63を通して切れ目のない中空円筒状の渦流の状態で供給口11に供給され、供給口11により、粉体Pと溶媒Rとが予備混合され、その予備混合物Fpが環状溝10に導入される。
Then, the quantitative supply device X is operated, and the powder P stored in the hopper 31 is quantified from the lower opening 31b of the hopper 31 by the stirring action of the stirring blade 32A and the negative pressure suction force of the suction pump mechanism Y. Through the expansion chamber 47 of the supply unit 40, a predetermined amount is continuously supplied in a predetermined amount to the mixing member 61 of the mixing mechanism 60. In parallel, the solvent supply unit 50 is operated, and the solvent R is continuously supplied in a predetermined amount to the mixing member 61 of the mixing mechanism 60 by the negative pressure suction force of the suction pump mechanism unit Y.
From the mixing member 61 of the mixing mechanism 60, the powder P is supplied to the supply port 11 through the cylindrical portion 62 of the mixing member 61, and the solvent R has a hollow cylindrical vortex flow without a break through the annular slit 63. The powder P and the solvent R are preliminarily mixed through the supply port 11 in a state, and the preliminary mixture Fp is introduced into the annular groove 10.
ロータ5が回転駆動されて、そのロータ5と一体的に区画板15が回転すると、その区画板15に同心状に設けられた掻出翼9が、環状溝10に先端部9Tが嵌め込まれた状態で周回する。
すると、図4及び図5において実線矢印にて示すように、供給口11を流動して環状溝10に導入された予備混合物Fpは、環状溝10に嵌め込まれて周回する掻出翼9の先端部9Tにより掻き出され、その掻き出された予備混合物Fpは、概略的には、供給室13内を区画板15における漏斗状部15bの前面と環状平板部15cの前面とに沿いながらロータ5の回転方向に流動し、更に、ステータ7の供給室側透孔7aを通過して翼室8に流入し、その翼室8内をロータ5の回転方向に流動して、吐出部12から吐出される。
When the rotor 5 is driven to rotate and the partition plate 15 rotates integrally with the rotor 5, the scraping blade 9 provided concentrically on the partition plate 15 is inserted into the annular groove 10 with the tip 9 </ b> T. Circulate in a state.
Then, as shown by solid line arrows in FIGS. 4 and 5, the preliminary mixture Fp flowing through the supply port 11 and introduced into the annular groove 10 is fitted into the annular groove 10 and the tip of the scraping blade 9 that circulates. The preliminary mixture Fp that is scraped out by the portion 9T is roughly divided into the rotor 5 while being along the front surface of the funnel-shaped portion 15b and the front surface of the annular flat plate portion 15c in the partition plate 15 in the supply chamber 13. , Further flows through the supply chamber side through hole 7a of the stator 7 and flows into the blade chamber 8, flows in the blade chamber 8 in the rotation direction of the rotor 5, and is discharged from the discharge section 12. Is done.
環状溝10に導入された予備混合物Fpは、掻出翼9の先端部9Tにより掻き出されるときに、せん断作用を受ける。この場合、掻出翼9の先端部9Tの外向き側面9oと内側の環状溝10の内向き内面との間、及び、掻出翼9の先端部9Tの内向き側面9iと内側の環状溝10の外向き内面との間においてせん断作用が働く。同時に、掻出翼9の回転方向背面側の背面9aにおいては、掻出翼9が回転することにより、いわゆる局所沸騰(キャビテーション)が発生する。また、ステータ7の供給室側透孔7aを通過する際に、せん断作用が働く。
つまり、供給室13内の予備混合物Fpにせん断力を作用させるとともに、局所沸騰を発生させることができるので、掻き出される予備混合物Fpは、掻出翼9及び供給室側透孔7aからせん断作用を受けて混合されるとともに、掻出翼9の背面9aに発生する局所沸騰(キャビテーション)により、溶媒Rに対する粉体Pの分散がより良好に行われることとなる。よって、このような予備混合物Fpを供給することができ、翼室8内において溶媒Rに対する粉体Pの良好な分散を期待することができる。
The preliminary mixture Fp introduced into the annular groove 10 undergoes a shearing action when it is scraped by the tip portion 9T of the scraping blade 9. In this case, between the outward side surface 9o of the tip portion 9T of the scraping blade 9 and the inward inner surface of the inner annular groove 10, and the inward side surface 9i of the tip portion 9T of the scraping blade 9 and the inner annular groove. A shearing action acts between the 10 outward inner surfaces. At the same time, the so-called local boiling (cavitation) occurs on the rear surface 9a on the rear side in the rotational direction of the scraping blade 9 as the scraping blade 9 rotates. Further, when passing through the supply chamber side through hole 7 a of the stator 7, a shearing action works.
That is, since a shear force can be applied to the preliminary mixture Fp in the supply chamber 13 and local boiling can be generated, the preliminary mixture Fp to be scraped is sheared from the scraping blade 9 and the supply chamber side through hole 7a. As a result, the powder P is more favorably dispersed in the solvent R due to local boiling (cavitation) generated on the back surface 9 a of the scraping blade 9. Therefore, such a preliminary mixture Fp can be supplied, and good dispersion of the powder P with respect to the solvent R in the blade chamber 8 can be expected.
吐出部12から吐出されたスラリーFは、吐出路18を通して再循環機構部70に供給され、再循環機構部70において、完全に溶解していない粉体Pを含む状態の未溶解スラリーFrと、粉体Pが略完全に溶解した状態のスラリーFとに分離されるとともに、溶媒Rの気泡が分離されて、未溶解スラリーFrは循環路16を通して再び吸引ポンプ機構部Yの導入口17に供給され、スラリーFは排出路22を通して供給先80に供給される。 The slurry F discharged from the discharge unit 12 is supplied to the recirculation mechanism unit 70 through the discharge path 18, and in the recirculation mechanism unit 70, the undissolved slurry Fr in a state containing the powder P that is not completely dissolved, The powder P is separated into the slurry F in a substantially completely dissolved state, and the bubbles of the solvent R are separated. The undissolved slurry Fr is supplied again to the inlet 17 of the suction pump mechanism Y through the circulation path 16. Then, the slurry F is supplied to the supply destination 80 through the discharge path 22.
未溶解スラリーFrは、導入口17の絞り部14aを介して流量が制限された状態で導入室14内に導入される。その導入室14内においては、回転する複数の攪拌羽根21によりせん断作用を受けて、更に細かく解砕され、更に、導入室側透孔7bの通過の際にもせん断作用を受けて解砕される。この際には、導入室側透孔7bを介して流量が制限された状態で翼室8に導入される。そして、翼室8内において、高速で回転する回転翼6によりせん断作用を受けて解砕され、粉体Pの凝集物(ダマ)が更に少なくなったスラリーFが供給室13からのスラリーFと混合されて吐出部12から吐出される。 The undissolved slurry Fr is introduced into the introduction chamber 14 through the throttle portion 14a of the introduction port 17 in a state where the flow rate is limited. In the introduction chamber 14, it is shattered by a plurality of rotating stirring blades 21 to be further finely crushed, and is further shattered by the shearing action when passing through the introduction chamber side through hole 7 b. The At this time, the air is introduced into the blade chamber 8 in a state where the flow rate is limited via the introduction chamber side through hole 7b. Then, in the blade chamber 8, the slurry F, which is crushed by the shearing action by the rotating blade 6 rotating at a high speed, and the aggregate (dama) of the powder P is further reduced, is the slurry F from the supply chamber 13. It is mixed and discharged from the discharge part 12.
ここで、制御部により、ステータ7の供給室側透孔7a及び導入室側透孔7bの出口領域である翼室8内の圧力がその全周に亘って溶媒Rの飽和蒸気圧以下となるように回転翼6の回転数が設定され、当該設定された回転数で回転翼6を回転させる。
これにより、回転翼6の回転数設定により、当該出口領域である翼室8内の圧力は、その全周に亘って溶媒Rの飽和蒸気圧(25℃の水の場合、3.169kPa)以下となるから、少なくともステータ7の供給室側透孔7a及び導入室側透孔7bを通過した直後の翼室8内の領域では、溶媒Rの気化による微細気泡(マイクロバブル)の発生が促進され、当該領域が、翼室8内の全周に亘って連続して微細気泡が多数発生した微細気泡領域として形成される状態となる。
よって、翼室8内の全周に亘って、粉体Pの凝集物(いわゆるダマ)に浸透した溶媒Rが発泡することで当該凝集物の解砕が促進され、さらに、その発生した微細気泡が翼室8において加圧され消滅する際の衝撃力によりさらに粉体Pの分散が促進されることになり、結果、翼室8内の全周に存在するスラリーFのほぼ全体に亘って、溶媒R中での粉体Pの分散が良好な高品質のスラリーFを生成することができる。
Here, the pressure in the blade chamber 8 which is the exit region of the supply chamber side through hole 7a and the introduction chamber side through hole 7b of the stator 7 becomes equal to or lower than the saturated vapor pressure of the solvent R over the entire circumference by the control unit. Thus, the rotational speed of the rotary blade 6 is set, and the rotary blade 6 is rotated at the set rotational speed.
Thereby, the pressure in the blade chamber 8 which is the said exit area | region is below the saturated vapor pressure (3.169kPa in the case of 25 degreeC water) of the solvent R over the perimeter by the rotation speed setting of the rotary blade 6 by this. Therefore, at least in the region in the blade chamber 8 immediately after passing through the supply chamber side through-hole 7a and the introduction chamber side through-hole 7b of the stator 7, generation of fine bubbles (microbubbles) due to evaporation of the solvent R is promoted. In this state, the region is formed as a fine bubble region in which a large number of fine bubbles are generated continuously over the entire circumference of the blade chamber 8.
Therefore, the crushing of the aggregate is promoted by foaming of the solvent R permeating the aggregate (so-called lumps) of the powder P over the entire circumference of the blade chamber 8, and the generated fine bubbles are further promoted. The dispersion of the powder P is further promoted by the impact force at the time when the blade chamber 8 is pressurized and disappears, and as a result, over almost the entire slurry F existing in the entire circumference of the blade chamber 8, A high-quality slurry F with good dispersion of the powder P in the solvent R can be produced.
次に、図8に基づいて、本実施形態の構成を採用して、導入口17に絞り部14aを設け、ステータ7に供給室側透孔7a及び導入室側透孔7bを設けるとともに、ロータ5(回転翼6)の回転数を適切に制御した場合における実証試験結果について説明する。 Next, based on FIG. 8 , the configuration of the present embodiment is adopted, the throttle port 14 a is provided in the introduction port 17, the supply chamber side through hole 7 a and the introduction chamber side through hole 7 b are provided in the stator 7, and the rotor The verification test result in the case where the rotational speed of 5 (rotary blade 6) is appropriately controlled will be described.
図8では、本体ケーシング1を透明の樹脂で構成し、吸引ポンプ機構部Y内に溶媒Rとしての水を通過させて、回転翼6が回転する翼室8内を外周側から観察した状態を示し、図8(a)から(c)に行くに従って、回転翼6の回転数を増加させた状態を示し、回転翼6の回転数を、(a)では630rpm、(b)では1800rpm、(c)では2400rpmとした例を示す。 In FIG. 8 , the main body casing 1 is made of a transparent resin, water as a solvent R is passed through the suction pump mechanism Y, and the inside of the blade chamber 8 in which the rotating blade 6 rotates is observed from the outer peripheral side. 8 (a) to 8 (c), the rotational speed of the rotor blades 6 is increased. The rotational speed of the rotor blades 6 is 630 rpm in (a), 1800 rpm in (b), ( c) shows an example of 2400 rpm.
図8(a)にて判明するように、回転翼6の回転数が比較的低い状態では、ステータ7の供給室側透孔7a及び導入室側透孔7b(絞り透孔)の出口領域である翼室8内の圧力は水の飽和蒸気圧(25℃の水の場合、3.169kPa)よりも大きくなっており、これら供給室側透孔7a及び導入室側透孔7bを通過した直後の溶媒Rにおいては、回転翼6の背面6aでの急激な圧力低下により、溶媒Rの一部、すなわち、供給室側透孔7a及び導入室側透孔7bを通過して回転翼6の背面6a付近に存在する溶媒Rのみに、局所沸騰(キャビテーション)が周方向に断続的な状態で発生するだけで、供給室側透孔7a及び導入室側透孔7bを通過した溶媒Rの全体には沸騰が発生することなく吐出部12にそのまま吐出されるものも存在している状態である。即ち、この状態は、図8(a)において翼室8内に存在する白く見える領域が非常に少ない状態である。
一方で、図8(b)にて判明するように、回転翼6の回転数が比較的高い状態では、供給室側透孔7a及び導入室側透孔7bの出口領域である翼室8内の圧力は全周に亘って水の飽和蒸気圧(25℃の水の場合、3.169kPa)以下となっており、翼室8内の少なくとも供給室側透孔7a及び導入室側透孔7bを通過した直後の領域では、回転翼6の背面6aでの急激な圧力低下により、翼室8内において回転翼6の背面6a付近に存在する溶媒Rの局所沸騰(キャビテーション)に加え、溶媒Rの気化による微細気泡(本願にいう微細気泡であるマイクロバブル)の発生が促進され、当該領域が、翼室8内の全周に亘って連続して微細気泡が多数発生した微細気泡領域として形成されている状態である。即ち、この状態は、図8(b)において翼室8内に存在する白く見える領域が雲状に非常に多く発生している状態である。更に、図8(c)にて判明するように、回転翼6の回転数がより高い状態では、翼室8内の全周に亘る溶媒Rの気化による微細気泡(マイクロバブル)が、より多く発生し、微細気泡が多数発生した微細気泡領域がより鮮明に形成されている状態となっている。即ち、この状態は、図8(c)において翼室8内に存在する白く見える領域が、雲状に非常に多く(図8(b)よりも多く)発生している状態である。
As can be seen in FIG. 8 (a), in the rotational speed is relatively low state of the rotating blades 6, at the exit region of the feed chamber side through hole 7a and the introduction chamber side through hole 7b of the stator 7 (stop hole) The pressure in a certain blade chamber 8 is higher than the saturated vapor pressure of water (in the case of water at 25 ° C., 3.169 kPa), and immediately after passing through the supply chamber side through hole 7a and the introduction chamber side through hole 7b. In the solvent R, a part of the solvent R, that is, the supply chamber side through-hole 7a and the introduction chamber side through-hole 7b passes through a part of the solvent R due to a rapid pressure drop on the back surface 6a of the rotary blade 6. Only in the solvent R existing in the vicinity of 6a, local boiling (cavitation) occurs only in an intermittent state in the circumferential direction, and in the entire solvent R that has passed through the supply chamber side through hole 7a and the introduction chamber side through hole 7b. May be discharged as it is to the discharge unit 12 without boiling. It is in a state. That is, this condition appears white region existing blade chamber 8 in FIG. 8 (a) is a very small state.
On the other hand, as can be seen in FIG. 8B , in the state where the rotational speed of the rotary blade 6 is relatively high, the inside of the blade chamber 8 which is the outlet region of the supply chamber side through hole 7a and the introduction chamber side through hole 7b. Is at or below the saturated vapor pressure of water (3.169 kPa in the case of water at 25 ° C.) over the entire circumference, and at least the supply chamber side through hole 7 a and the introduction chamber side through hole 7 b in the blade chamber 8. In the region immediately after passing through, the solvent R in addition to the local boiling (cavitation) of the solvent R existing in the vicinity of the back surface 6a of the rotor blade 6 in the blade chamber 8 due to a rapid pressure drop at the back surface 6a of the rotor blade 6. The generation of microbubbles (microbubbles, which are microbubbles referred to in the present application) is promoted by vaporization of the gas, and the region is formed as a microbubble region in which many microbubbles are generated continuously over the entire circumference of the blade chamber 8. It is a state that has been. Namely, this condition appears white region existing blade chamber 8 is in a state of very many occurred cloud in FIG. 8 (b). Moreover, as found in FIG. 8 (c), the at higher state rotational speed of the rotor blades 6, the fine air bubbles due to vaporization of the solvent R over the entire circumference of the blade chamber 8 (microbubbles) are more A fine bubble region where a large number of fine bubbles are generated is formed more clearly. That is, this condition appears white region existing blade chamber 8 in FIG. 8 (c) it is very much (more than FIG. 8 (b)) to the cloud is a state that is occurring.
このように、通常、吸引ポンプ機構部Y内では、供給室側透孔7a及び導入室側透孔7bの出口領域において翼室8内の回転翼6の背面6aのみに発生する局所沸騰(キャビテーション)のみで粉体Fを溶媒Rに分散させることで十分とされていたが(図8(a)の状態)、本発明者らは、例えば、溶媒Rに対する粉体Pの割合が比較的多く、より分散性能を向上させることが必要となる場合でも、上述のとおり、回転翼6の回転数設定により、ステータ7の供給室側透孔7a及び導入室側透孔7bの出口領域である翼室8内の圧力をその全周に亘って溶媒Rの飽和蒸気圧以下とし、翼室8内において、より広範囲に溶媒Rの沸騰を発生させることを可能とし(図8の(b),(c)の状態)、翼室8内の全周に存在するスラリーFのほぼ全体に亘って、溶媒R中での粉体Pの分散が良好な高品質のスラリーFを生成することを可能としたのである。従って、上述の結果から、上記実施形態に係る構成では、ロータ5の回転数を少なくとも1800rpm以上に設定すると、翼室8内の圧力がその全周に亘って溶媒Rの飽和蒸気圧以下となり、翼室8内の全周に亘って微細気泡(マイクロバブル)を発生させることが可能であると確認できた。 Thus, normally, in the suction pump mechanism Y, local boiling (cavitation) that occurs only on the back surface 6a of the rotary blade 6 in the blade chamber 8 in the outlet region of the supply chamber side through hole 7a and the introduction chamber side through hole 7b. ) While the powder F had been a sufficient be dispersed in a solvent R only the state (FIG. 8 (a)), the present inventors have, for example, the proportion of the powder P in the solvent R is relatively large Even when it is necessary to further improve the dispersion performance, as described above, the blades which are the outlet regions of the supply chamber side through-hole 7a and the introduction chamber-side through hole 7b of the stator 7 are set by setting the rotation speed of the rotary blade 6. the pressure in the chamber 8 over its entire circumference and saturated vapor pressure of a solvent R, in the wing chamber 8, possible to generate a more extensive boiling solvent R (in FIG. 8 (b), ( c) state), almost all of the slurry F existing all around the blade chamber 8 It was possible to produce a high-quality slurry F with good dispersion of the powder P in the solvent R over the body. Therefore, from the above results, in the configuration according to the above embodiment, when the rotation speed of the rotor 5 is set to at least 1800 rpm or more, the pressure in the blade chamber 8 becomes equal to or lower than the saturated vapor pressure of the solvent R over the entire circumference. It was confirmed that fine bubbles (micro bubbles) could be generated over the entire circumference of the blade chamber 8.
〔別実施形態〕
(A)上記実施形態では、制御部が、ロータ5の回転数を、供給室側透孔7a及び導入室側透孔7bの出口領域の圧力が全周に亘って溶媒Rの飽和蒸気圧以下となるように適切に設定した。しかしながら、これに限らず、ロータ5の回転数を、供給室側透孔7a及び導入室側透孔7bの出口領域の圧力が全周に亘って飽和蒸気圧よりも所定圧力だけ低くなるように設定して、当該出口領域である翼室8内の全周に亘って連続して、溶媒Rの気化による微細気泡(マイクロバブル)の発生を促進し、当該微細気泡が多数発生した微細気泡領域を形成することもできる。この場合、ロータ5の回転数を1800rpmよりも幾分大きく設定することとなる。
[Another embodiment]
(A) In the above embodiment, the controller controls the number of rotations of the rotor 5, and the pressure in the outlet region of the supply chamber side through hole 7a and the introduction chamber side through hole 7b is equal to or lower than the saturated vapor pressure of the solvent R over the entire circumference. Was set appropriately. However, the rotational speed of the rotor 5 is not limited to this, so that the pressure in the outlet region of the supply chamber side through hole 7a and the introduction chamber side through hole 7b is lower than the saturated vapor pressure by a predetermined pressure over the entire circumference. The fine bubble region that is set and promotes the generation of fine bubbles (micro bubbles) due to the vaporization of the solvent R continuously throughout the entire circumference of the blade chamber 8 that is the outlet region. Can also be formed. In this case, the rotational speed of the rotor 5 is set somewhat larger than 1800 rpm.
(B)上記の実施形態では、区画板15をロータ5の前方側に当該ロータ5と一体回転する状態で設けて、掻出翼9を区画板15に設けたが、吐出部12から吐出されるスラリーFの一部を循環供給させなくても、粉体Pを溶媒Rに適切に分散させることができる場合は、再循環機構部70を省略したり、区画板15を省略することもでき、この場合、掻出翼9をロータ5に直接設けても良い。 (B) In the above embodiment, the partition plate 15 is provided on the front side of the rotor 5 so as to rotate integrally with the rotor 5, and the scraping blade 9 is provided on the partition plate 15. If the powder P can be appropriately dispersed in the solvent R without circulating part of the slurry F to be circulated, the recirculation mechanism 70 can be omitted or the partition plate 15 can be omitted. In this case, the scraping blade 9 may be provided directly on the rotor 5.
(C)上記の実施形態では、粉体Pとして単一種類のCMC粉体を用いたが、必要に応じて、複数種類の粉体を混合した混合粉体を粉体Pとして用いることができる。また、同様に、溶媒Rとして単一種類の水を用いたが、必要に応じて、複数種類の液体を混合した混合液体を溶媒Rとして用いることができる。
また、粉体Pとしては、粉体であれば特に除外されるものではなく、電池電極材料等の化学原料、脱脂粉乳や小麦粉等の食品原料、医薬原料等であって、顆粒、粉体、細粒等の粉体(これら粉体の混合物を含む)を例示することができる。粉体には、粉粒体も含まれる。
さらに、分散質としては、上記の実施形態において例示した粉体P(固相分散質)に限定されるものではなく、液状(液相分散質)のものとしてエマルジョンを生成するようにしても良い。例えば、液相分散質としての油を液相分散媒としての水に分散させる場合にも、本発明を適用することができる。
(C) In the above embodiment, a single type of CMC powder is used as the powder P. However, a mixed powder obtained by mixing a plurality of types of powder can be used as the powder P if necessary. . Similarly, although a single type of water is used as the solvent R, a mixed liquid obtained by mixing a plurality of types of liquid can be used as the solvent R as necessary.
Further, the powder P is not particularly excluded as long as it is a powder, and is a chemical raw material such as a battery electrode material, a food raw material such as skim milk powder or wheat flour, a pharmaceutical raw material, etc. Examples thereof include fine particles (including a mixture of these powders). The powder includes a granular material.
Furthermore, the dispersoid is not limited to the powder P (solid phase dispersoid) exemplified in the above embodiment, and the emulsion may be generated as a liquid (liquid phase dispersoid). . For example, the present invention can also be applied to the case where oil as a liquid phase dispersoid is dispersed in water as a liquid phase dispersion medium.
以上説明したように、ステータの絞り透孔を通過した混合流体全体に亘って良好に液相分散媒中における分散質の分散を促進して、高品質のゾルを生成することができる分散方法及び分散システムを確立できる。 As described above, a dispersion method capable of promoting the dispersion of the dispersoid in the liquid phase dispersion medium well over the entire mixed fluid that has passed through the throttle aperture of the stator, and generating a high-quality sol, and A distributed system can be established.
1 本体ケーシング(吸引ポンプ機構部)
5 ロータ
6 回転翼
6a 背面部
7 ステータ
7a 供給室側透孔(絞り透孔)
7b 導入室側透孔(絞り透孔)
8 翼室(出口領域)
9 掻出翼
12 吐出部(出口領域)
13 供給室
14 導入室
14a 絞り部
15 区画板
60 ミキシング機構(供給機構部)
70 再循環機構部
71 分離部(円筒状容器)
100 分散システム
Y 吸引ポンプ機構部
F スラリー(ゾル)
Fp 予備混合物
Fr 未溶解スラリー(ゾルの一部)
P 粉体(分散質)
R 溶媒(液相分散媒)
1 Body casing (suction pump mechanism)
5 Rotor 6 Rotor blade 6a Back surface part 7 Stator 7a Supply chamber side through hole (diaphragm through hole)
7b Introduction chamber side through hole (diaphragm through hole)
8 Wing chamber (exit area)
9 Scraping blade 12 Discharge part (exit area)
13 Supply chamber 14 Introduction chamber 14a Restriction section 15 Partition plate 60 Mixing mechanism (supply mechanism section)
70 Recirculation mechanism part 71 Separation part (cylindrical container)
100 Dispersion system Y Suction pump mechanism part F Slurry (sol)
Fp Premix Fr Undissolved slurry (part of sol)
P powder (dispersoid)
R solvent (liquid phase dispersion medium)
Claims (6)
前記導入室の入口部に絞り部を設け、
前記絞り部の内径は、前記導入室へ流体を供給する循環路よりも小径であり、
前記導入室に対し区画板により区画されて形成され、前記ステータの絞り透孔を通じて前記翼室に通じる供給室を設け、
前記分散質と前記液相分散媒とを予備混合した予備混合物を前記供給室に供給するとともに、前記吐出部から吐出されたゾルの一部を前記混合流体として前記導入室に循環供給しながら、
前記ステータの絞り透孔の出口領域の圧力が当該出口領域の全周に亘って前記液相分散媒の飽和蒸気圧以下となるように前記回転翼の回転数を設定し、当該設定された回転数で前記回転翼を回転して、前記翼室内の少なくとも前記ステータの絞り透孔を通過した直後の領域を、前記液相分散媒の微細気泡が多数発生した微細気泡領域として形成する分散方法。 An introduction chamber to which a fluid is supplied, a cylindrical stator that is arranged on the outer peripheral side of the introduction chamber and includes a plurality of throttle through holes arranged in the circumferential direction, and an annular shape that leads to a discharge portion formed on the outer peripheral side of the stator The blade chamber and a rotor blade that can be rotationally driven in the blade chamber are disposed in the main body casing, and fluid is sucked from the introduction chamber to the blade chamber through the throttle through-hole by the rotational drive of the rotor blade. Using a centrifugal suction pump mechanism that discharges fluid from the blade chamber to the discharge unit, and passing a mixed fluid of a dispersoid and a liquid phase dispersion medium through the suction pump mechanism unit, A dispersion method for producing a sol in which the dispersoid is dispersed,
A throttle is provided at the inlet of the introduction chamber,
The inner diameter of the throttle portion is smaller than the circulation path for supplying fluid to the introduction chamber,
The supply chamber is formed by being partitioned by a partition plate with respect to the introduction chamber, and is provided with a supply chamber that communicates with the blade chamber through the throttle through hole of the stator.
While supplying a premixture prepared by premixing the dispersoid and the liquid phase dispersion medium to the supply chamber and circulatingly supplying a part of the sol discharged from the discharge section to the introduction chamber as the mixed fluid,
The rotational speed of the rotor blade is set so that the pressure in the outlet region of the throttle through hole of the stator is equal to or lower than the saturated vapor pressure of the liquid phase dispersion medium over the entire circumference of the outlet region, and the set rotation A dispersion method in which the rotor blades are rotated by a number to form at least a region immediately after passing through the apertures of the stator in the blade chamber as a fine bubble region in which a large number of fine bubbles of the liquid phase dispersion medium are generated.
前記導入室の入口部に絞り部を備え、
前記絞り部の内径は、前記導入室へ流体を供給する循環路よりも小径であり、
前記導入室に対し区画板により区画されて形成され、前記ステータの絞り透孔を通じて前記翼室に通じる供給室を備え、
前記分散質と前記液相分散媒とを予備混合した予備混合物を前記供給室に供給する供給機構部と、前記吐出部から吐出されたゾルの一部を前記混合流体として前記導入室に循環供給する再循環機構部とを備え、
運転を制御する制御部が、前記ステータの絞り透孔の出口領域の圧力が当該出口領域の全周に亘って前記液相分散媒の飽和蒸気圧以下となるように前記回転翼の回転数を設定し、
前記供給機構部と前記再循環機構部とを作動させながら前記設定された回転数で前記回転翼を回転させて、前記翼室内の少なくとも前記ステータの絞り透孔を通過した直後の領域が、前記液相分散媒の微細気泡が多数発生した微細気泡領域として形成される分散システム。 An introduction chamber to which a fluid is supplied, a cylindrical stator that is arranged on the outer peripheral side of the introduction chamber and includes a plurality of throttle through holes arranged in the circumferential direction, and an annular shape that leads to a discharge portion formed on the outer peripheral side of the stator The blade chamber and a rotor blade that can be rotationally driven in the blade chamber are disposed in the main body casing, and fluid is sucked from the introduction chamber to the blade chamber through the throttle through-hole by the rotational drive of the rotor blade. A centrifugal suction pump mechanism that discharges fluid from the blade chamber to the discharge unit, and a fluid mixture of a dispersoid and a liquid phase dispersion medium is passed through the suction pump mechanism unit, and the liquid phase dispersion medium A dispersion system for producing a sol in which the dispersoid is dispersed,
Provided with a throttle at the inlet of the introduction chamber,
The inner diameter of the throttle portion is smaller than the circulation path for supplying fluid to the introduction chamber,
A supply chamber that is formed by being partitioned by a partition plate with respect to the introduction chamber, and that communicates with the blade chamber through an aperture hole of the stator;
A supply mechanism for supplying a premixed mixture of the dispersoid and the liquid phase dispersion medium to the supply chamber, and a part of the sol discharged from the discharge section is circulated and supplied to the introduction chamber as the mixed fluid. And a recirculation mechanism that
The controller for controlling the operation adjusts the rotational speed of the rotor blades so that the pressure in the outlet region of the throttle through hole of the stator is equal to or lower than the saturated vapor pressure of the liquid phase dispersion medium over the entire circumference of the outlet region. Set,
The region immediately after passing through at least the stator through hole of the stator in the blade chamber by rotating the rotary blade at the set rotation speed while operating the supply mechanism unit and the recirculation mechanism unit , A dispersion system formed as a fine bubble region in which a large number of fine bubbles of a liquid phase dispersion medium are generated.
前記供給室の入口部の予備混合物を前記供給室側に掻き出す掻出翼を、前記区画板に備えた請求項4又は5に記載の分散システム。 The partition plate is connected to a rotor provided with the rotor blades and is rotatable.
The dispersion system according to claim 4 or 5, wherein a scraping blade that scrapes the preliminary mixture at the inlet of the supply chamber toward the supply chamber is provided on the partition plate.
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TW201309381A (en) | 2013-03-01 |
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