JP3236911B2 - Equipment for emulsifying and dispersing substances - Google Patents
Equipment for emulsifying and dispersing substancesInfo
- Publication number
- JP3236911B2 JP3236911B2 JP10879396A JP10879396A JP3236911B2 JP 3236911 B2 JP3236911 B2 JP 3236911B2 JP 10879396 A JP10879396 A JP 10879396A JP 10879396 A JP10879396 A JP 10879396A JP 3236911 B2 JP3236911 B2 JP 3236911B2
- Authority
- JP
- Japan
- Prior art keywords
- passage
- groove
- accelerator
- disk
- substance
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Disintegrating Or Milling (AREA)
Description
【0001】[0001]
【産業上の利用分野】この発明は、各産業分野での利用
に適する物質の乳化分散及び破砕装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for emulsifying and dispersing a substance suitable for use in various industrial fields.
【0002】[0002]
【従来の技術】物質の乳化及び分散処理は攪拌式装置に
よって、破砕はビーズミル等によって行なわれている。2. Description of the Related Art Emulsification and dispersion of substances are carried out by a stirrer, and crushing is carried out by a bead mill or the like.
【0003】[0003]
【発明が解決しようとする課題】前記従来の攪拌式の装
置は処理後の乳化及び分散の安定度は悪く前記ビーズミ
ル等の破砕装置も要求する大きさの粒子を作るのに時間
がかかるなどの問題点があった。However, the above-mentioned conventional stirring type apparatus has poor stability of emulsification and dispersion after the treatment, and the crushing apparatus such as the bead mill takes a long time to produce particles of a required size. There was a problem.
【0004】そこでこの発明は、乳化及び分散の安定度
を良くし、破砕においては時間をかけず微粒子を作り込
むことができるというような前記問題点を解決すること
を目的としている。[0004] Accordingly, an object of the present invention is to improve the stability of emulsification and dispersion, and to solve the above-mentioned problems that fine particles can be produced in a short time in crushing.
【0005】[0005]
【課題を解決するための手段】この発明は、前記目的を
達成するため、請求項1では、物質を含む液体に圧力を
加えて二枚のディスクを備えたアクセレイターに導入
し、前記各ディスクごとに面を貫通する一つの貫通通路
とこれにつながる面上形成の一つの溝状通路を面上の途
中まで設け、前記各ディスクを前記溝状通路を有する面
を以て対向させ前記貫通通路同志が重なり合わないよう
前記溝状通路同志が交叉又は連結するよう接合し、前記
接合面内に形成される前記溝状通路同志によってできる
貫通口の面積よりも前記溝状通路の流路断面積の方が大
きくなるようにして、前記貫通口の手前にて流れを角度
を以て屈曲することにより前記屈曲部の前後の区間で加
速を引き起こさせ、まして、前記屈曲部より前記貫通口
に至る距離を短く通りその後通路が拡げられることを併
せて前記加速の効果を助長しながら、前記加速による衝
撃力及び諸物理現象の相互作用により前記物質が前記各
ディスクの一連の流路を通過して微粒化され、前記アク
セレイター及びアクセレイター通過後の配管より取り出
されることを特徴とするものであり、変形例では、物質
を含む液体に圧力を加えて二枚のディスクを備えたアク
セレイターに導入し、前記各ディスクごとに面を貫通す
る一つの貫通通路を設け前記貫通通路が重なり合わない
ように二枚のディスクを接合し、それぞれのディスクの
前記貫通通路が連通するようどちらか一方のディスク面
上に流れの上流にある一枚目のディスクの前記貫通通路
の幅で前記貫通通路の流路断面積よりも小さい流路断面
積で以て面上形成の溝状通路を設け、前記溝状通路に入
る手前で流れを角度を以て屈曲することにより前記屈曲
部の前後の区間で加速を引き起こさせ、まして、前記屈
曲部より前記溝状通路の距離をできるだけ短く通り、そ
の後通路が拡げられることを併せて前記加速の効果を助
長しながら、前記加速による衝撃力及び諸物理現象の相
互作用により前記物質が前記各ディスクの一連の流路を
通過して微粒化され、前記アクセレイター及びアクセレ
イター通過後の配管より取り出されることを特徴とする
ものであり、請求項2では、物質を含む液体に圧力を加
えて二枚のディスクを備えたアクセレイターに導入し、
一枚目のディスクには面を貫通する貫通通路を二つ設
け、片側の面上にて二つの前記貫通通路を溝状通路でつ
なぎ、二枚目のディスクには面を貫通する貫通通路を一
つ設けて、これら二枚のディスクにおいて一枚目の前記
溝状通路の途中で、前記溝状通路が前記溝状通路より広
い幅の二枚目のディスクにある前記貫通通路に連通する
よう接合させ、接合面内にて形成される貫通口の面積よ
りも前記溝状通路の流路断面積の二倍の方が大きくなる
ようにして、前記貫通口の手前にて二つの前記溝状通路
の流れをそれぞれ角度を以て屈曲することにより前記屈
曲部の前後の区間で加速を引き起こさせ、まして、前記
屈曲部より前記貫通口に至る距離を短く通り、その後通
路が拡げられることを併せて前記加速の効果を助長しな
がら、前記加速による衝撃力及び諸物理現象の相互作用
により前記物質が前記各ディスクの一連の流路を通過し
て微粒化され、前記アクセレイター及びアクセレイター
通過後の配管より取り出されることを特徴とするもので
ある。According to the present invention, in order to achieve the above object, according to the first aspect of the present invention, a liquid containing a substance is applied to an accelerator provided with two disks by applying pressure to each of the disks. In each case, one through passage penetrating the surface and one groove-like passage formed on the surface connected thereto are provided halfway on the surface, and the discs are opposed to each other with the surface having the groove-like passage, and the through passages are connected to each other. The groove-shaped passages are joined so as to intersect or connect so that they do not overlap, and the cross-sectional area of the flow passage of the groove-shaped passage is smaller than the area of the through hole formed by the groove-shaped passages formed in the joint surface. And the flow is bent at an angle in front of the through-opening so as to cause acceleration in a section before and after the bent portion, and moreover, the distance from the bent portion to the through-opening is shortened. Thereafter, while promoting the effect of the acceleration in addition to the passage being expanded, the material is atomized by passing through a series of flow paths of the respective disks by the interaction of impact force and various physical phenomena due to the acceleration, It is characterized in that it is taken out from the accelerator and a pipe after passing through the accelerator, and in a modified example, a pressure is applied to a liquid containing a substance to introduce the liquid into an accelerator equipped with two disks, One through-passage penetrating the surface is provided for each disc, and two discs are joined so that the through-passages do not overlap with each other, and the flow on one of the disc surfaces so that the through-passages of the respective discs communicate with each other. Providing a groove-shaped passage formed on the surface with a flow passage cross-sectional area smaller than the flow passage cross-sectional area of the through passage at the width of the through passage of the first disk upstream of the first disk, By bending the flow at an angle just before entering the grooved passage, acceleration is caused in the section before and after the bent portion, and furthermore, the distance of the grooved passage is made as short as possible from the bent portion, and thereafter the passage is expanded. While promoting the effect of the acceleration in addition to being performed, the interaction between the impact force and various physical phenomena due to the acceleration causes the substance to pass through a series of flow paths of each of the disks and is atomized, and the accelerator and It is characterized in that it is taken out from the pipe after passing through the accelerator, and in claim 2, pressure is applied to the liquid containing the substance and the liquid is introduced into the accelerator equipped with two disks,
The first disk is provided with two through passages penetrating the surface, the two through passages are connected by a groove-like passage on one surface, and the second disk is provided with a through passage penetrating the surface. In one of the two disks, in the middle of the first groove-shaped passage in the two disks, the groove-shaped passage communicates with the through passage in the second disk having a wider width than the groove-shaped passage. Joined, so that twice the cross-sectional area of the flow path of the groove-shaped passage is larger than the area of the through-hole formed in the joint surface, and the two groove-shaped portions are formed in front of the through-hole. The flow of the passage is bent at an angle to cause acceleration in a section before and after the bent portion, and moreover, the distance from the bent portion to the through hole is reduced, and then the passage is expanded. While promoting the effect of acceleration, the acceleration Due to the interaction of impact force and various physical phenomena, the substance is atomized by passing through a series of flow paths of each disk, and is taken out from the accelerator and piping after passing through the accelerator. .
【0006】[0006]
【作用】物質を含む液体が圧力を加えられてアクセレイ
ターに導かれると、物質は液体と共に流れを整える流路
を通過して細く狭められる流路に入る。ここでは角度を
以て流路を屈曲させて細く狭めるのでこの屈曲部の前後
を通過することで短い距離で以て急激な速度の増加をも
たらす。この速度変化は物質及び液体に加速による衝撃
力を発生させる。また前記屈曲部を経た後、高速になっ
た物質を含む液体は一番狭い流路を短い距離で以て通過
し、次に流路が拡げられる。このことは物質を含む液体
の排出を容易にし前記屈曲部での効果を高める働きがあ
る。これら急激な速度変化による衝撃力及び諸物理現象
を流れの途中で発生させ、これらの相互作用により物質
が微粒化され乳化及び分散破砕処理が行なわれる。この
処理は、微粒子を作り込む力が強いため、安定性良好で
時間のかからない乳化と分散になり、破砕力もきわめて
高いものである。When a liquid containing a substance is applied with pressure to the accelerator, the substance passes through a flow path that regulates the flow with the liquid and enters a narrowed flow path. Here, since the flow path is bent at an angle and narrowed narrowly, passing the front and rear of this bent portion causes a rapid increase in speed over a short distance. This change in velocity causes an impact force on the substance and liquid due to acceleration. After passing through the bent portion, the liquid containing the substance at a high speed passes through the narrowest flow path with a short distance, and then the flow path is expanded. This has the function of facilitating the discharge of the liquid containing the substance and enhancing the effect at the bent portion. The impact force and various physical phenomena caused by these rapid changes in speed are generated in the middle of the flow, and the interaction between these causes the material to be atomized, whereby emulsification and dispersion crushing are performed. In this treatment, since the power for producing fine particles is strong, the stability and emulsification and dispersion can be improved in a short time, and the crushing power is extremely high.
【0007】[0007]
【実施例】以下この発明の実施例を図1〜図21で説明
する。図1において全体の構成を説明する。たとえば乳
化の場合をとって述べると、1は水と油の入ったタンク
であり、簡易的な攪拌機で水と油が二層に完全に分離し
ない状態に保ってあるものとし、前記水と油が弁2を通
過して4のポンプで加圧され5の配管を通してアクセレ
イター6に入り、作用を受けて7の配管から取り出され
る。所望の乳化が完成すれば8の弁を介して9で回収す
る。乳化が不完全な場合は10の配管を介して1のタン
クへ戻され、再度の処理を行なうよう装置されている。DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to FIGS. The overall configuration will be described with reference to FIG. For example, in the case of emulsification, 1 is a tank containing water and oil, and it is assumed that water and oil are not completely separated into two layers by a simple stirrer. Passes through the valve 2 and is pressurized by the pump 4 and enters the accelerator 6 through the pipe 5 and is taken out of the pipe 7 under the action. When the desired emulsification is completed, it is recovered at 9 via the 8 valve. If the emulsification is incomplete, it is returned to one tank via 10 pipes, and the processing is performed again.
【0008】図2〜図7は、請求項1のアクセレイター
についての実施例である。アクセレイター6は、円筒容
器11にディスク12を二枚図4・図5の如く配置した
ものである。ディスク12の単体は図2・図3の如くダ
イヤモンド等の硬質の耐磨耗性の材質を使用し、直径1
0mm厚さ2mmぐらいの大きさの円板である。そこに
一個の貫通通路(0.8mmφ)13があり、それに連
なって面上形成の溝(0.2mm深さ・0.1mm幅)
14が堀り刻んである。そしてこの溝が図6・図7のよ
うに直角に組み合わされるようにディスクを合わせてい
る。ここにおいてディスク同志により貫通口(0.1m
m□)15が形成され各ディスクの全流路中いちばん狭
い場所となる。圧力を加えられた物質を含む液体は貫通
口15の手前にて広い流路から狭い流路に角度を以て屈
曲させられる。広い流路の時の速度をV1狭い流路の時
の速度をV2すると、V1よりV2の方が速度が大きく
なる。この速度変化が短い距離内において行なわれるた
め、物質を含む液体に加わる力が大きなものとなる。ま
して、屈曲部より貫通口15に至る距離を短くとり通過
後通路が拡げられることを併せて加速による効果を助長
しながら、加速による衝撃力及び諸物理現象の相互作用
により物質がディスクの一連の流路を通過して微粒化さ
れ、アクセレイター及びアクセレイター通過後の配管よ
り取り出され、物質の乳化分散及び破砕を行なうことに
なる。FIGS. 2 to 7 show an embodiment of the accelerator of the first aspect. The accelerator 6 has two disks 12 arranged in a cylindrical container 11 as shown in FIGS. As shown in FIGS. 2 and 3, the disc 12 is made of a hard and abrasion-resistant material such as diamond and has a diameter of 1 mm.
It is a disc having a size of about 0 mm and a thickness of about 2 mm. There is one through passage (0.8mmφ) 13 and a groove formed on the surface (0.2mm depth and 0.1mm width) connected to it.
14 are engraved. The discs are aligned so that these grooves are combined at right angles as shown in FIGS. Here, through holes (0.1m
m □) 15 are formed, which is the narrowest place in the entire flow path of each disk. The liquid containing the substance under pressure is bent at an angle from a wide channel to a narrow channel in front of the through-hole 15. Speed V 2 Thus when the speed of V 1 narrow flow path when a wide flow path, better than V 1 of the V 2 the speed increases. Since this speed change is performed within a short distance, the force applied to the liquid containing the substance becomes large. Furthermore, while shortening the distance from the bent portion to the through hole 15 and enlarging the passage after passing, the effect of acceleration is also promoted. After passing through the flow path, the particles are atomized and taken out from the accelerator and the pipe after passing through the accelerator to emulsify, disperse, and crush the substance.
【0009】図8〜図14は変形例のアクセレイターに
ついての実施例である。アクセレイター6は円筒容器1
1にディスク16・19を図12・図13の如く配置し
たものである。ディスク16は図8・図9のように貫通
通路(0.5mmφ)17があり、面上形成の溝状通路
(0.2mm深さ・0.5mm幅)18が貫通通路17
の幅で続いている。ディスク19は図10・図11のよ
うに貫通通路(1.5mmφ)20を有している。両方
のディスクともダイヤモンド等の硬質の耐磨耗性の材質
を使用し、直径10mm厚さ2mmぐらいの大きさの円
板である。この二枚のディスクを図14のように流路が
形成されるように組み合わせている。ここにおいてディ
スク同志により貫通通路(0.2mm×0.5mm)が
つくられ、ディスクによって形成される全流路中いちば
ん狭い場所となる。圧力を加えられた物質を含む液体は
貫通通路の手前にて広い流路から狭い流路に角度を以て
屈曲させられる。広い流路の時の速度をV3狭い流路の
時の速度をV4とすると、V3よりV4の方が速度が大
きくなる。この速度変化が短い距離内において行なわれ
るため物質を含む液体に加わる力が大きなものとなる。
まして、屈曲部より貫通通路を含む距離を短くとり、通
過後通路が拡げられることを併せて加速による効果を助
長し、加速による衝撃力及び諸物理現象の相互作用によ
り、物質が前記ディスクの一連の流路を通過して微粒化
され、アクセレイター及びアクセレイター通過後の配管
より取り出され物質の乳化分散及び破砕を行なうことに
なる。FIG. 8 to FIG. 14 show an embodiment of a modified accelerator. Accelerator 6 is cylindrical container 1
1, disks 16 and 19 are arranged as shown in FIGS. The disc 16 has a through passage (0.5 mmφ) 17 as shown in FIGS. 8 and 9, and a groove-like passage (0.2 mm depth and 0.5 mm width) 18 formed on the surface has a through passage 17.
The width continues. The disk 19 has a through passage (1.5 mmφ) 20 as shown in FIGS. Both disks are made of a hard and wear-resistant material such as diamond and are disks having a diameter of about 10 mm and a thickness of about 2 mm. These two disks are combined so that a flow path is formed as shown in FIG. Here, a through passage (0.2 mm × 0.5 mm) is formed by the disks, and the narrowest passage is formed in the entire flow path formed by the disks. The liquid containing the pressurized substance is bent at an angle from a wide channel to a narrow channel before the through passage. When the speed at the wide flow channel to the speed at the V 3 narrow channel and V 4, who from V 3 of V 4 is speed increases. Since this speed change is performed within a short distance, the force applied to the liquid containing the substance becomes large.
Furthermore, the distance including the through passage is made shorter than the bent portion, and the passage is expanded after passing, which further promotes the effect of acceleration, and the interaction of the impact force and various physical phenomena due to acceleration causes the substance to be connected to the series of disks. Are passed through the flow path, and are atomized, and are taken out from the accelerator and the pipe after passing through the accelerator to emulsify, disperse, and crush the substance.
【0010】図15〜図21は請求項2のアクセレイタ
ーについての実施例である。アクセレイター6は円筒容
器11にディスク21・22を図19・図20のごとく
配置したものである。ディスクはダイヤモンド等の硬質
の耐磨耗性の材質を使用し、直径10mm厚さ2mmぐ
らいの大きさの円板である。一枚目のディスクは図15
・図16の如く二個の貫通通路(0.8mmφ)23が
あり、それに連なって面上形成の溝(0.1mm深さ・
0.1mm幅)24が堀り刻んである。二枚目のディス
クにはスリット状の貫通通路(0.1mm幅・2mm長
さ・2mm深さ)25が設けてある。そしてこれら二枚
のディスクを組み合わせることにより、接合面に貫通口
(0.1mm×0.1mm)26が形成され、図21の
左右両方から入り込む溝状通路の断面積を合せたものよ
り小さく、流路中いちばん狭い場所となる。圧力を加え
られた物質を含む液体は溝状通路24の左右両方から流
れこみ、貫通口26の手前中心付近で物質を含む液体同
志が相互に磨耗することのない壁の役割を果しながら貫
通口に向かって角度を以て屈曲させられることになる。
屈曲する前の速度をV5屈曲した後の速度をV6とする
と、V5よりV6の方が速度が大きくなる。V5′・V
6′についても同様である。この速度変化が短い距離内
において行なわれるため、物質を含む液体に加わる力が
大きなものとなる。まして、屈曲部より貫通口26に至
る距離を短くとり通過後通路が拡げられることを併せて
加速による効果を助長しながら、加速による衝撃力及び
諸物理現象の相互作用により物質がディスクの一連の流
路を通過して微粒化され、アクセレイター及びアクセレ
イター通過後の配管より取り出され、物質の乳化分散及
び破砕を行なうことになる。FIGS. 15 to 21 show embodiments of the accelerator according to the second aspect. The accelerator 6 has disks 21 and 22 arranged in a cylindrical container 11 as shown in FIGS. The disk is made of a hard and wear-resistant material such as diamond, and is a disk having a diameter of about 10 mm and a thickness of about 2 mm. Fig. 15 shows the first disk
・ There are two through passages (0.8 mmφ) 23 as shown in FIG. 16, and a groove formed on the surface (0.1 mm depth
24 (0.1 mm width) are dug. The second disk has a slit-shaped through passage (0.1 mm width, 2 mm length, 2 mm depth) 25. By combining these two disks, a through-hole (0.1 mm × 0.1 mm) 26 is formed in the joint surface, which is smaller than the cross-sectional area of the groove-like passage entering from both the left and right in FIG. It is the narrowest place in the channel. The liquid containing the substance under pressure flows from both the left and right sides of the groove-shaped passage 24 and penetrates near the center in front of the through-hole 26 while acting as a wall where the liquids containing the substance do not wear each other. It will be bent at an angle towards the mouth.
If the rate after the rate before bending and V 5 bends and V 6, towards the V 6 from V 5 is speed increases. V 5 '· V
The same applies to 6 '. Since this speed change is performed within a short distance, the force applied to the liquid containing the substance becomes large. Furthermore, while shortening the distance from the bent portion to the through hole 26 and enlarging the passage after passing, the effect of acceleration is also promoted. After passing through the flow path, the particles are atomized and taken out from the accelerator and the pipe after passing through the accelerator to emulsify, disperse, and crush the substance.
【0011】[0011]
【発明の効果】以上説明してきたように、この発明によ
れば微粒子を作り込む力が強いので安定性の良い乳化分
散が可能となり処理時間が短く微細な破砕が実現でき
る。As described above, according to the present invention, since the power to produce fine particles is strong, emulsification and dispersion with good stability can be achieved, and the processing time is short and fine crushing can be realized.
【図1】この発明の一実施例の全体的概念図である。FIG. 1 is an overall conceptual diagram of an embodiment of the present invention.
【図2】図1の請求項1による要部内ディスクの正面図
である。FIG. 2 is a front view of the main part disk according to claim 1 of FIG. 1;
【図3】図2のA−A線による断面図である。FIG. 3 is a sectional view taken along line AA of FIG. 2;
【図4】図1の請求項1による要部の正断面図である。FIG. 4 is a front sectional view of a main part according to claim 1 of FIG. 1;
【図5】図4のB−B線による断面図である。FIG. 5 is a sectional view taken along line BB of FIG. 4;
【図6】図5のC部拡大図である。FIG. 6 is an enlarged view of a portion C in FIG. 5;
【図7】図6のD−D線による断面図である。FIG. 7 is a sectional view taken along line DD of FIG. 6;
【図8】図1の変形例による要部内ディスクの正面図で
ある。FIG. 8 is a front view of a main part internal disk according to a modification of FIG. 1;
【図9】図8のE−E線による断面図である。FIG. 9 is a sectional view taken along line EE of FIG. 8;
【図10】図1の変形例による要部内ディスクの正面図
である。FIG. 10 is a front view of a main part disk according to a modification of FIG. 1;
【図11】図10のF−F線による断面図である。FIG. 11 is a sectional view taken along line FF of FIG. 10;
【図12】図1の変形例による要部の正断面図である。FIG. 12 is a front sectional view of a main part according to a modification of FIG. 1;
【図13】図12のG−G線による断面図である。13 is a sectional view taken along line GG of FIG.
【図14】図13のH部拡大図である。FIG. 14 is an enlarged view of a portion H in FIG. 13;
【図15】図1の請求項2による要部内ディスクの正面
図である。FIG. 15 is a front view of the main part disk according to claim 2 of FIG. 1;
【図16】図15のJ−J線による断面図である。16 is a sectional view taken along line JJ of FIG.
【図17】図1の請求項2による要部内ディスクの正面
図である。FIG. 17 is a front view of the main part disk according to claim 2 of FIG. 1;
【図18】図17のK−K線による断面図である。18 is a sectional view taken along line KK of FIG.
【図19】図1の請求項2による要部の正断面図であ
る。FIG. 19 is a front sectional view of a main part according to claim 2 of FIG. 1;
【図20】図19のL−L線による断面図である。20 is a sectional view taken along line LL in FIG.
【図21】図20のM部拡大図である。FIG. 21 is an enlarged view of a portion M in FIG. 20;
1 材料受入器 2 弁 3、5、7、10 配管 4 ポンプ 6 アクセレイター 8 三方弁 9 出口 11 円筒容器 12、16、19、21、22 ディスク 13、17、20、23、25 貫通通路 14、18、24、 溝状通路 15、26 貫通口 DESCRIPTION OF SYMBOLS 1 Material receiver 2 Valve 3, 5, 7, 10 Piping 4 Pump 6 Accelerator 8 Three-way valve 9 Outlet 11 Cylindrical container 12, 16, 19, 21, 22 Disk 13, 17, 20, 23, 25 Through passage 14, 18, 24, groove-shaped passage 15, 26 through hole
Claims (2)
スクを備えたアクセレイターに導入し、前記各ディスク
ごとに面を貫通する一つの貫通通路とこれにつながる面
上形成の一つの溝状通路を面上の途中まで設け、前記各
ディスクを前記溝状通路を有する面を以て対向させ前記
貫通通路同志が重なり合わないよう前記溝状通路同志が
交叉又は連結するよう接合し、前記接合面内に形成され
る前記溝状通路同志によってできる貫通口の面積よりも
前記溝状通路の流路断面積の方が大きくなるようにし
て、前記貫通口の手前にて流れを角度を以て屈曲するこ
とにより前記屈曲部の前後の区間で加速を引き起こさ
せ、まして、前記屈曲部より前記貫通口に至る距離を通
りその後通路が拡げられて前記加速の効果を助長しなが
ら、前記加速による衝撃力及び諸物理現象の相互作用に
より前記物質が前記各ディスクの一連の流路を通過して
微粒化され、前記アクセレイター及びアクセレイター通
過後の配管より取り出されることを特徴とする物質の乳
化分散破砕装置。1. A pressure is applied to a liquid containing a substance and introduced into an accelerator provided with two disks, one through-passage penetrating a surface for each said disk and one of a formation on the surface connected thereto. A groove-shaped passage is provided halfway on the surface, the discs are opposed to each other with the surface having the groove-shaped passage, and the groove-shaped passages are joined or joined so that the through passages do not overlap with each other. The flow path cross-sectional area of the groove-like passage is made larger than the area of the through-hole formed by the groove-like passages formed in the plane, and the flow is bent at an angle before the through-hole. Thereby, acceleration is caused in a section before and after the bent portion, and furthermore, a passage is extended through a distance from the bent portion to the through-hole, and the acceleration is accelerated while promoting the effect of the acceleration. The emulsification and dispersion of the substance, characterized in that the substance is atomized by passing through a series of channels of each disk by interaction of force and various physical phenomena, and is taken out from the accelerator and a pipe after passing through the accelerator. Crushing equipment.
スクを備えたアクセレイターに導入し、一枚目のディス
クには面を貫通する貫通通路を二つ設け、片側の面上に
て二つの前記貫通通路を溝状通路でつなぎ、二枚目のデ
ィスクには面を貫通する貫通通路を一つ設けて、これら
二枚のディスクにおいて一枚目の前記溝状通路の途中
で、前記溝状通路が前記溝状通路より広い幅の二枚目の
ディスクにある前記貫通通路に連通するよう接合させ、
接合面内にて形成される貫通口の面積よりも前記溝状通
路の流路断面積の二倍の方が大きくなるようにして、前
記貫通口の手前にて二つの前記溝状通路の流れをそれぞ
れ角度を以て屈曲することにより前記屈曲部の前後の区
間で加速を引き起こさせ、まして、前記屈曲部より前記
貫通口に至る距離を通り、その後通路が拡げられて前記
加速の効果を助長しながら、前記加速による衝撃力及び
諸物理現象の相互作用により前記物質が前記各ディスク
の一連の流路を通過して微粒化され、前記アクセレイタ
ー及びアクセレイター通過後の配管より取り出されるこ
とを特徴とする物質の乳化分散破砕装置。2. A pressure is applied to a liquid containing a substance, and the liquid is introduced into an accelerator provided with two disks. The first disk is provided with two through passages penetrating the surface, and the first disk is provided with a through passage. Two of the through passages are connected by a groove-like passage, a second disk is provided with one through-passage penetrating the surface, and in these two disks, in the middle of the first groove-like passage, The groove-shaped passage is joined so as to communicate with the through passage in a second disk having a wider width than the groove-shaped passage,
The flow of the two groove-shaped passages before the through-hole is set such that the area of the passage cross-section of the groove-shaped passage is twice as large as the area of the through-hole formed in the joint surface. Is caused to be accelerated in a section before and after the bent portion by bending at an angle, and moreover, passes through a distance from the bent portion to the through-hole, and then the passage is expanded to promote the effect of the acceleration. The interaction between impact force and various physical phenomena caused by the acceleration causes the substance to pass through a series of flow paths of the respective discs, to be atomized, and to be taken out from the accelerator and piping after passing through the accelerator. Equipment for emulsifying, dispersing and crushing substances.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10879396A JP3236911B2 (en) | 1996-03-25 | 1996-03-25 | Equipment for emulsifying and dispersing substances |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10879396A JP3236911B2 (en) | 1996-03-25 | 1996-03-25 | Equipment for emulsifying and dispersing substances |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH09253465A JPH09253465A (en) | 1997-09-30 |
JP3236911B2 true JP3236911B2 (en) | 2001-12-10 |
Family
ID=14493630
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10879396A Expired - Fee Related JP3236911B2 (en) | 1996-03-25 | 1996-03-25 | Equipment for emulsifying and dispersing substances |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3236911B2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1999015264A1 (en) * | 1997-09-19 | 1999-04-01 | Teruzo Kashino | Device for emulsion-dispersing and pulverizing substances |
-
1996
- 1996-03-25 JP JP10879396A patent/JP3236911B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH09253465A (en) | 1997-09-30 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US5380089A (en) | Emulsifying apparatus for solid-liquid multiphase flow and nozzle for solid-liquid multiphase flow | |
JP3634868B2 (en) | Micro mixer | |
JP3794687B2 (en) | Micro emulsifier | |
US6305834B1 (en) | Method and device for producing a dispersed mixture via crossing partial flows | |
US6000841A (en) | Static fluid flow mixing apparatus | |
EP0477845A1 (en) | In-line dispersion of gas in liquid | |
JP4343428B2 (en) | Method for producing a heat-sensitive dispersion or emulsion | |
CA2482177A1 (en) | Diffuser/emulsifier | |
US4989988A (en) | Apparatus for mixing media capable to flow | |
CA2644484C (en) | Device and method for creating hydrodynamic cavitation in fluids | |
JP2005288254A (en) | Micro-device and method for confluence of fluids | |
EP1134020A1 (en) | Mixing element body for stationary type mixer | |
JP2001514578A (en) | Homogenization valve | |
CA2350961A1 (en) | Mixer for mixing at least two flows of gas or other newtonian liquids | |
CN110869111B (en) | Static mixer with triangular mixing ducts | |
JP3236911B2 (en) | Equipment for emulsifying and dispersing substances | |
JPS59179215A (en) | Extruding die | |
GB1558575A (en) | Plate heat exchanger | |
JP3794952B2 (en) | Swivel type micro bubble generator | |
JPH02261525A (en) | Emulsifying device | |
JP2004237177A (en) | Double emulsion microcapsule former | |
JP2007044692A (en) | Double emulsion microcapsule preparation device | |
JPH07116487A (en) | Device for emulsifying and dispersing substance | |
WO1999015264A1 (en) | Device for emulsion-dispersing and pulverizing substances | |
JPH10180066A (en) | Atomizing method and device therefor |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20071005 Year of fee payment: 6 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20071005 Year of fee payment: 6 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20101005 Year of fee payment: 9 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20101005 Year of fee payment: 9 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20111005 Year of fee payment: 10 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20121005 Year of fee payment: 11 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20121005 Year of fee payment: 11 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20131005 Year of fee payment: 12 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
LAPS | Cancellation because of no payment of annual fees |