JPS59166231A - Emulsion producer - Google Patents
Emulsion producerInfo
- Publication number
- JPS59166231A JPS59166231A JP58039155A JP3915583A JPS59166231A JP S59166231 A JPS59166231 A JP S59166231A JP 58039155 A JP58039155 A JP 58039155A JP 3915583 A JP3915583 A JP 3915583A JP S59166231 A JPS59166231 A JP S59166231A
- Authority
- JP
- Japan
- Prior art keywords
- partition walls
- radial direction
- stator
- walls
- fixed disk
- 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.)
- Granted
Links
Classifications
-
- 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
- B01F27/27—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices
- B01F27/271—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices with means for moving the materials to be mixed radially between the surfaces of the rotor and the stator
- B01F27/2711—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices with means for moving the materials to be mixed radially between the surfaces of the rotor and the stator provided with intermeshing elements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/80—Mixing plants; Combinations of mixers
- B01F33/81—Combinations of similar mixers, e.g. with rotary stirring devices in two or more receptacles
- B01F33/811—Combinations of similar mixers, e.g. with rotary stirring devices in two or more receptacles in two or more consecutive, i.e. successive, mixing receptacles or being consecutively arranged
-
- 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
- B01F2025/91—Direction of flow or arrangement of feed and discharge openings
- B01F2025/912—Radial flow
-
- 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
- B01F27/19—Stirrers with two or more mixing elements mounted in sequence on the same axis
- B01F27/191—Stirrers with two or more mixing elements mounted in sequence on the same axis with similar elements
Abstract
Description
【発明の詳細な説明】
この発明は乳化剤を用いずに混合した重油と水のエマル
ジョンが経時的に分離することなく高安定性を保持でき
る等の石油・燃料関係の分野あるいはフレンチドレッシ
ングのブレンド。DETAILED DESCRIPTION OF THE INVENTION This invention is applicable to the field of petroleum/fuels or French dressing blends, in which an emulsion of heavy oil and water mixed without the use of an emulsifier can maintain high stability without separating over time.
マヨネーズの乳化、牛乳のホモゲナイズ、チョコレート
原料のブレンド等の食品・薬品工業関係その他化粧水の
添加混合等の化粧品工業、さらには化学工業等あらゆる
工業分野において経時的に分離することのない高安定性
のエマルジョンを作ることのできるエマルジョン製造機
に関する。High stability that does not separate over time in all industrial fields such as the food and pharmaceutical industry such as emulsification of mayonnaise, homogenization of milk, blending of chocolate raw materials, cosmetic industry such as addition and mixing of lotions, and even chemical industry. This invention relates to an emulsion making machine that can make emulsions.
従来、例えば重油に水を約１０〜３０条の割合で混合し
てエマルジョンを作るといった技術は、燃焼特性の向上
、省エネルギ一対策及び排気ガス公害対策上等各種優れ
た効果を奏することが明らかであるが、これらはいずれ
も分離防止のだめの乳化剤を添加してお９、これなしで
はすぐに水と重油が分離してしまい安定なエマルジョン
が得られなかった。Conventional technology, such as mixing heavy oil with water at a ratio of about 10 to 30 parts to create an emulsion, has been shown to have various excellent effects such as improving combustion characteristics, saving energy, and countering exhaust gas pollution. However, in all of these, an emulsifier was added to prevent separation.9 Without this, water and heavy oil would separate immediately and a stable emulsion could not be obtained.
ところがこの乳イ１剤は非常に高価であるために、上記
効果を奏するに拘らずその実用化は未だ十分になされて
い々い実情である。その他の工業分野においても乳化剤
を使用しないときには、二液が混合して一時的にエマル
ジョンとなっても経時的に二液に分離してしまうという
難点があった。However, since this emulsion is very expensive, it has not yet been put to practical use in spite of the above-mentioned effects. In other industrial fields as well, when emulsifiers are not used, there is a problem in that even if two liquids are mixed to temporarily form an emulsion, they will separate into two liquids over time.
こρ発明は上記の点に鑑みなされたもので、その目的と
するところは、二液を混合してエマルジョンを作るに際
して高価な乳化剤を一切使用することなく、一方の液体
を超微粉砕して他方の液体中に浮遊せしめ経時的に安定
なエマルジョンを作り、省エネルギー、省資源化、製品
の高均質化等を図９、安価な製品が得られるようにした
エマルジョン製造機を一般に提供することにある。This invention was made in view of the above points, and its purpose is to create an emulsion by mixing two liquids, without using any expensive emulsifiers, and by ultrafinely pulverizing one of the liquids. To provide the general public with an emulsion manufacturing machine that makes it possible to create an emulsion that is suspended in the other liquid and is stable over time, thereby saving energy, saving resources, and making the product highly homogeneous. be.
以下、この発明の一実施例を図面により説明するＯ
Ｊは密閉型の円筒状ケースで、その胴部１ａの端部寄り
に入口２を備え、かつその人口２から離れたケースｌの
一端面の中央部に出口３を形成する。４はケース１の軸
心上に内挿した高速回転する回転軸で、ケースｌに固着
した軸受箱５内の軸受６にて回転自在に支承されている
。Hereinafter, an embodiment of the present invention will be described with reference to the drawings. OJ is a closed cylindrical case, which has an inlet 2 near the end of its body 1a, and has one end face of the case l away from the body 2. An outlet 3 is formed in the central part of. Reference numeral 4 denotes a rotating shaft that rotates at high speed and is inserted on the axis of the case 1, and is rotatably supported by a bearing 6 in a bearing box 5 fixed to the case 1.
７はケースｌの外側にある回転軸４の軸端に形成した■
プーリである。回転軸４の回転数は４．０００から１２
，０００ ｒ、ｐ、ｍとするが、重油を対象とする場合
７，０００から１０．００Ｏｒ、ｐ、ｍ位とする。８は
入口２付近から出口３付近に至るまでのケーシング１内
に取付けた一個捷たは相互に密着する二個以上の固定子
で、通常はケース１の内壁に取付けた冷却用あるいは加
熱用ジャケット１０の内側に取付けられている。この固
定子８は回転軸４を遊嵌させる中心孔８ｂを備えた固定
円盤８ａの入口２側の片面に第１図示の如く彎曲状の切
欠部８Ｃを設け、かつ該固定円盤の反対側の片面に多数
の同心円を描いた同高の環状仕切壁８ｄを配設し、該各
仕切壁に固定円盤８ａの中心を通る放射方向か又は固定
円盤８ａの中心を通らずに刃先を形成するように一定の
角度だけ偏心した放射方向に向けて連通ずる連絡溝８ｅ
を等配設してなる（第４図ａ＋ｂ参照）。互いに同心円
をなす仕切壁８ｄ間の間隔や連絡溝８ｅの巾は対象とす
る液体の種類や性状等に応じて適宜決定する。９は前記
固定子８の数に対応してそれぞれに嵌合状態で回転する
如く回転軸４に固着した回転子である。この回転子９は
、前記固定円盤８ａの仕切壁８ｄ間の空隙にそれぞれ嵌
合する如く多数の同心円を描いた同高の環状隔壁９ｂを
、回転軸４に固着した円形の回転盤９ａ例えば重油と水
の混合を対象とした場合、直径約１５（ニア７１位の回
転円盤に配設し、かつ該隔壁の一部が鋭角の刃先となる
如く回転盤９ａの中心線から一定の角度をもって偏心し
た放射方向に向けて連通する放射溝９ｃを前記隔壁に等
配設してなる（第３図参照）。図中、１１は入口側と最
初の一組の固定子８２回転子９との間に位置する回転軸
４に固着したインペラーで、液体を入口２からケース１
内に吸引する作用を行わせるものである。この吸引を一
層効果的に行うために、前面が次第に狭搾するようにテ
ーパ１２ａを、後面が前記固定円盤８ａにバッキング１
３を介して密着し、かつ前記固定円盤８ａの切欠部８ｃ
と対応する切欠部１２ｂを備えた環状コア１２を、前記
ジャケット１０の内側に取付ける。7 is formed at the shaft end of the rotating shaft 4 outside the case l.
It's a pulley. The rotation speed of the rotating shaft 4 is 4,000 to 12
,000 r, p, m, but in the case of heavy oil, it should be around 7,000 to 10.00 Or, p, m. 8 is a single stator or two or more stators that are in close contact with each other installed in the casing 1 from the vicinity of the inlet 2 to the vicinity of the outlet 3, and is usually a cooling or heating jacket attached to the inner wall of the case 1. It is installed inside the 10. This stator 8 has a fixed disk 8a with a center hole 8b into which the rotating shaft 4 is loosely fitted, and a curved notch 8C provided on one side of the entrance 2 side as shown in the first figure, and a curved notch 8C on the opposite side of the fixed disk. An annular partition wall 8d of the same height with a large number of concentric circles drawn on one side is arranged, and a cutting edge is formed on each partition wall in a radial direction passing through the center of the fixed disk 8a or not passing through the center of the fixed disk 8a. A communication groove 8e that communicates in a radial direction that is eccentric by a certain angle
are arranged equally (see Figure 4 a+b). The distance between the partition walls 8d that are concentric with each other and the width of the communication groove 8e are appropriately determined depending on the type and properties of the liquid to be treated. A rotor 9 is fixed to the rotary shaft 4 so as to rotate in a fitted state corresponding to the number of the stators 8. This rotor 9 has a circular rotary disk 9a fixed to a rotary shaft 4, with annular partition walls 9b of the same height drawing a large number of concentric circles so as to fit into the gaps between the partition walls 8d of the fixed disk 8a, respectively. When the target is a mixture of water and water, it is installed on a rotating disk with a diameter of about 15 (near 71), and is eccentric from the center line of the rotating disk 9a at a certain angle so that a part of the partition wall becomes an acute cutting edge. radial grooves 9c communicating in the radial direction are equally arranged on the partition wall (see Fig. 3). An impeller fixed to the rotating shaft 4 located at
This is to create a suction effect within the body. In order to perform this suction more effectively, the taper 12a is formed so that the front surface is gradually narrowed, and the back surface is attached to the fixed disk 8a by the backing 12a.
3, and the notch 8c of the fixed disk 8a.
An annular core 12 having a corresponding notch 12b is attached to the inside of the jacket 10.
１４は最終の固定円盤８ａの後面に密着し、該固定円盤
８ａの切欠部８ｃに対応する切欠部１４ａを備え、かつ
内面が出口側に向けて次第に狭搾するようなテーパ１４
ｂを有した案内コアで、前記ジャケット１０およびケー
ス１内壁に亘って取付けられている。14 is a taper 14 that is in close contact with the rear surface of the final fixed disk 8a, has a cutout 14a corresponding to the cutout 8c of the fixed disk 8a, and has an inner surface that gradually narrows toward the exit side.
A guide core having a diameter b is attached across the jacket 10 and the inner wall of the case 1.
を混合機（図示せず）で攪拌混合した液をポンプ（図示
せず）で入口２側へと圧送する。回転軸４はＶプーリ７
によッ’−ｒ ７，０（１０から１０．ＯＯＯｒ、ｐ、
ｍといった回転数で高速回転しており、この回転軸４の
回転数と同じ回転数でインペラー１１および−又はエリ
上の回転子９も回転するとと＼カる。インペラー１１の
回転により混合液は入口２から環状コア１２の次第に狭
搾するテーバ１２ａに沿って吸引され、該コアの切欠部
１２ｂと最初の固定円盤８ａの切欠部８ｃとによって構
成される空間内でインペラー１１の中心部から放射方向
に向って流れ、こ＼で壁に当って反転し、再び最初の固
定円盤８ａの切欠部８ｃに沿って流れ、該固定円盤の中
心孔８ｂへと進む。中心孔８ｂに進んだ混合液は固定子
８とこれに嵌合する回転子９の中心部から放射方向に向
って仕切壁８ｄの連絡溝８ｅおよび環状隔壁９ｂの放射
溝９ｃを伝わって次々に上方へと拡散する。混合液が放
射方向に流出する過程において、回転盤９ａに形成した
環状隔壁９ｂの偏心した放射溝９’ｅによって一種の鋭
い刃先が構成され、これが仕切壁８ｄ間を通る液体の分
子をさらに超微粒子となる如く高速切断することＸなる
。なお、固定円盤８ａの仕切壁８ｄに対して連絡溝８ｅ
を形成するに際しても回転刃の刃先と同様の鋭角の刃先
を形成することにより、さらに一層細かな粒子の混合液
が得られること＼なる。こうして固定子８とこれに嵌合
する回転子９を一組としたー又はエリ上を通過させるこ
とにより、出口３から流出する混合液は、粒、子の一層
細かな分散しにくいエマルジョンが得られること＼なる
。The mixture is stirred and mixed using a mixer (not shown), and the liquid is pumped to the inlet 2 side using a pump (not shown). The rotating shaft 4 is a V pulley 7
Yo'-r 7,0 (10 to 10.OOOr,p,
The impeller 11 and the rotor 9 on the rim also rotate at the same rotation speed as the rotating shaft 4. By the rotation of the impeller 11, the mixed liquid is sucked from the inlet 2 along the tapered bar 12a of the annular core 12, and enters the space formed by the notch 12b of the core and the notch 8c of the first fixed disk 8a. It flows in the radial direction from the center of the impeller 11, then it hits the wall and turns around, flows again along the notch 8c of the first fixed disk 8a, and advances to the center hole 8b of the fixed disk. The mixed liquid that has advanced to the center hole 8b travels in the radial direction from the center of the stator 8 and the rotor 9 fitted therein through the communication groove 8e of the partition wall 8d and the radial groove 9c of the annular partition wall 9b, one after another. Diffuse upward. In the process of the mixed liquid flowing out in the radial direction, a kind of sharp cutting edge is formed by the eccentric radial groove 9'e of the annular partition wall 9b formed on the rotary disk 9a, which further exceeds the liquid molecules passing between the partition walls 8d. The goal is to cut at high speed so that it becomes fine particles. Note that the communication groove 8e is connected to the partition wall 8d of the fixed disk 8a.
By forming an acute-angled cutting edge similar to the cutting edge of a rotary blade, a mixed liquid containing even finer particles can be obtained. By forming the stator 8 and the rotor 9 fitted therein as a set or passing over the area, the mixed liquid flowing out from the outlet 3 becomes an emulsion with finer particles and particles that are difficult to disperse. To be/become.
この発明は上記の説明から判るように、入口および出口
を備えた密閉型ケーシング内の中心軸線上に、高速回転
する回転軸を配設し、前記ケーシングの入口から出口間
に位置する回転軸に、固定子と該固定子に嵌合状態で回
転する回転子の一組を−又はエリ上設け、該固定子は回
転軸を遊嵌させる中心孔を備えた固定円盤の片面に、多
数の同心円を描いた同高の環状仕切壁を配設し、該各仕
切壁に固定円盤の中心を通る放射方向か又は固定円盤の
中心を通らずに一定の角度だけ偏心した放射方向に向け
て連通ずる連絡溝を等配設してなり、また上記回転子は
前記固定円盤の仕切壁間の空隙にそれぞれ嵌合する如く
多数の同心円を描いた同高の環状隔壁を、回転軸に固着
した円形回転盤に配設、し、かつ該隔壁の一部が鋭角の
刃先となる如く回転盤の中心線から一定の角度をもって
偏心した放射方向に向けて連通ずる放射溝を前記隔壁に
等配設してなるものであるから、入口から流入してきた
混合液は、固定子とこれに嵌合状態で嵌合する回転子を
一組とした中心部から放射方向に拡散される過程で、固
定円盤の最内殻に位置する仕切壁間に嵌合している鋭い
刃先をもった回転盤によって同−流路内で何回も何回も
繰り返し混合液の粒子を一次通路で切断した後、次に最
内殻の隣に位置する仕切壁面に嵌合している同様の鋭い
刃先をもった回転盤によって前記同様にして二次通路で
も切断され、こうして次々と最外殻に位置する仕切壁間
に向うに従い、回転盤の周速も増し、一層粒子との切断
回数も増えることメなって、混合液が内側から外側に移
動する間にｎ次の通路を通って切断されるとと＼なり、
最終の出口側では非常に細かな粒子となったエマルジョ
ンが得られること＼なり、乳化剤を一切要することなく
、また経時的に分離することの′ない均質なエマルジョ
ンが得られるという優れた効果を奏する。その結果、省
エネルギー化、省資源化等が図られること＼なり、あら
ゆる工業分野において利用され、その実用上の価値は極
めて高いものといえる。As can be seen from the above description, the present invention includes a rotating shaft that rotates at high speed is disposed on the central axis of a closed casing having an inlet and an outlet, and a rotary shaft located between the inlet and the outlet of the casing. , a set of a stator and a rotor that rotates in a fitted state with the stator is provided on one side or the other, and the stator has a plurality of concentric circles on one side of a fixed disk having a center hole into which a rotating shaft is loosely fitted. Annular partition walls of the same height are provided, and each of the partition walls communicates in a radial direction passing through the center of the fixed disk, or in a radial direction eccentric by a certain angle without passing through the center of the fixed disk. The rotor is a circular rotor in which a plurality of annular partition walls of the same height are fixed to the rotating shaft, and annular partition walls of the same height are drawn so as to fit into the gaps between the partition walls of the fixed disk. The partition wall is provided with radial grooves that communicate in the radial direction eccentrically at a certain angle from the center line of the rotary disk so that a part of the partition wall forms an acute-angled cutting edge. Therefore, the liquid mixture that flows in from the inlet is diffused in the radial direction from the center, which consists of a stator and a rotor that is fitted to the stator, until it reaches the outermost part of the fixed disk. After the particles of the mixed liquid are cut in the primary passage repeatedly in the same flow path by a rotary disk with a sharp cutting edge fitted between the partition walls located in the inner shell, the particles of the mixed liquid are cut in the primary passage. The secondary passages are also cut in the same way as described above by a rotary disc with a similar sharp cutting edge fitted to the partition wall located next to the inner shell, and thus the cut is successively made between the partition walls located in the outermost shell. Accordingly, the circumferential speed of the rotary disk increases, and the number of cuts with the particles also increases, and when the mixed liquid passes through the n-th path while moving from the inside to the outside, it is cut.
At the final outlet side, an emulsion with very fine particles is obtained, which has the excellent effect of not requiring any emulsifier and producing a homogeneous emulsion that does not separate over time. . As a result, it is possible to save energy and resources, and it is used in all industrial fields, and its practical value can be said to be extremely high.
第１図はこの発明の一実施例を示す断面図。
第２図はその側面図、第３図は回転子の平面図。
第４図ａ＋ｂは固定子の平面図を示す。
ｌ・・・ケース、２・・・入口、３・・・出口、４・・
・回転軸、８・・固定子） Ｓａ・・・固定円盤、 ８
ｂ・・中心孔。
８ｄ・・・仕切壁ｙ ８８・・連絡溝、９・・・回転子
＋ ｃｉａ・・・回転盤、 ９ｂ・・・環状隔壁ｙ ｃ
ｉｃ・・・放射溝。
第３図FIG. 1 is a sectional view showing an embodiment of the present invention. FIG. 2 is a side view thereof, and FIG. 3 is a plan view of the rotor. FIG. 4a+b shows a plan view of the stator. l...Case, 2...Inlet, 3...Exit, 4...
・Rotating shaft, 8... Stator) Sa... Fixed disk, 8
b. Central hole. 8d...Partition wall y 88...Communication groove, 9...Rotor + cia...Rotary disk, 9b...Annular partition wall y c
ic...Radial groove. Figure 3
Claims (1)
上に、高速回転する回転軸を配設し、前記ケーシングの
入口から出口間に位置する回転軸に、固定子と該固定子
に嵌合状態で回転する回転子の一組を−又はエリ上設け
、該固定子は回転軸を遊嵌させる中心孔を備えた固定円
盤の片面に、多数の同心円を描いた同高の環状仕切壁を
配設し、該各仕切壁に固定円盤の中心を通る放射方向か
又は固定円盤の中心を通らずに一定の角度だけ偏心した
放射方向に向けて連通ずる連絡溝を等配設してなり、ま
た上記回転子は前記固定円盤の仕切壁間の空隙にそれぞ
れ嵌合する如く多数の同心円を描いた同高の環状隔壁を
、回転軸に固着した円形回転盤に配設し、かつ該隔壁の
一部が鋭角の刃先となる如く回転盤の中心線から一定の
角度をもって偏心した放射方向に−向けて連通ずる放射
溝を前記隔壁に等配設してなることを特徴とするエマル
ジョン製造機。A rotary shaft that rotates at high speed is disposed on the central axis of a closed casing having an inlet and an outlet, and a stator is fitted to the rotary shaft located between the inlet and the outlet of the casing. A set of rotors that rotate at a speed is provided on one or more sides, and the stator has an annular partition wall of the same height with a number of concentric circles on one side of a fixed disk having a center hole into which a rotating shaft is loosely fitted. and each partition wall is provided with communicating grooves that communicate in a radial direction passing through the center of the fixed disk or in a radial direction eccentric by a certain angle without passing through the center of the fixed disk, and The rotor has a circular rotating disk fixed to a rotating shaft, and has annular partition walls of the same height each having a large number of concentric circles so as to fit into the gaps between the partition walls of the fixed disk, and one part of the partition walls. An emulsion manufacturing machine characterized in that radial grooves are equidisposed on the partition wall and communicate in a radial direction that is eccentric from the center line of the rotary disk at a certain angle so that the cutting edge is at an acute angle.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58039155A JPS59166231A (en) | 1983-03-11 | 1983-03-11 | Emulsion producer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58039155A JPS59166231A (en) | 1983-03-11 | 1983-03-11 | Emulsion producer |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59166231A true JPS59166231A (en) | 1984-09-19 |
| JPS6214330B2 JPS6214330B2 (en) | 1987-04-01 |
Family
ID=12545214
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58039155A Granted JPS59166231A (en) | 1983-03-11 | 1983-03-11 | Emulsion producer |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59166231A (en) |
Cited By (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0431469A (en) * | 1990-05-25 | 1992-02-03 | Kanebo Nsc Ltd | Production of high-softening point emulsion |
| EP0842695A1 (en) * | 1996-11-14 | 1998-05-20 | Nippon Shokubai Co., Ltd. | Production process, production apparatus, and product of resin particle |
| JP2001514959A (en) * | 1997-08-18 | 2001-09-18 | ナイコムド イメージング エーエス | Preparation of vesicles |
| EP1247562A1 (en) * | 2001-03-28 | 2002-10-09 | Fuji Photo Film Co., Ltd. | In-line mixing apparatus, process for mixing reactive chemical solutions, and process for producing microcapsules |
| US7237943B2 (en) * | 2000-11-10 | 2007-07-03 | Maelstrom Advanced Process Technologies, Ltd. | Dynamic fluid mixer |
| JP2007307494A (en) * | 2006-05-19 | 2007-11-29 | Yamazaki Co Ltd | Gas-mixing water producing device and humidifying device |
| KR100913875B1 (en) * | 2008-09-24 | 2009-08-26 | 박노성 | Dispersing pump |
| JP2011067794A (en) * | 2009-09-28 | 2011-04-07 | Sintokogio Ltd | High-shearing-type continuous dispersion apparatus |
| WO2011089715A1 (en) * | 2010-01-22 | 2011-07-28 | アイシン精機 株式会社 | Micro-bubble group generator and bubble bath apparatus |
| US20120257988A1 (en) * | 2011-04-08 | 2012-10-11 | Marcel Depault | Apparatus for mixing and pumping manure slurries |
| CN103055753A (en) * | 2012-12-27 | 2013-04-24 | 镇江市港南电子有限公司 | A novel stirring device for wafer polishing solutions |
| US8985844B2 (en) * | 2007-11-12 | 2015-03-24 | Ika-Werke Gmbh & Co. Kg | Device for dispersing or homogenizing with a magnetic coupling drive for rotors in a chamber |
| WO2015059759A1 (en) * | 2013-10-21 | 2015-04-30 | 株式会社長野セラミックス | Mixing nozzle |
| CN105561832A (en) * | 2015-12-31 | 2016-05-11 | 倪商伟 | Multilayer combined emulsification unit, emulsification machine using emulsification unit, and emulsification method |
| JP2019195760A (en) * | 2018-05-09 | 2019-11-14 | 株式会社愛工舎製作所 | Disc type mixing head having water cooling structure |
| CN112295481A (en) * | 2020-10-10 | 2021-02-02 | 孟广寻 | Liquid medicament secondary agitated vessel for bio-pharmaceuticals |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| PT3367809T (en) * | 2015-10-19 | 2019-04-30 | Nestle Sa | Apparatus and method for aeration of a food product |
-
1983
- 1983-03-11 JP JP58039155A patent/JPS59166231A/en active Granted
Cited By (21)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0431469A (en) * | 1990-05-25 | 1992-02-03 | Kanebo Nsc Ltd | Production of high-softening point emulsion |
| EP0842695A1 (en) * | 1996-11-14 | 1998-05-20 | Nippon Shokubai Co., Ltd. | Production process, production apparatus, and product of resin particle |
| US5965676A (en) * | 1996-11-14 | 1999-10-12 | Nippon Shokubai Co., Ltd. | Production process, production apparatus, and product of resin particle |
| JP2001514959A (en) * | 1997-08-18 | 2001-09-18 | ナイコムド イメージング エーエス | Preparation of vesicles |
| JP4808842B2 (en) * | 1997-08-18 | 2011-11-02 | ジーイー・ヘルスケア・アクスイェ・セルスカプ | Vesicle preparation method |
| US7237943B2 (en) * | 2000-11-10 | 2007-07-03 | Maelstrom Advanced Process Technologies, Ltd. | Dynamic fluid mixer |
| EP1247562A1 (en) * | 2001-03-28 | 2002-10-09 | Fuji Photo Film Co., Ltd. | In-line mixing apparatus, process for mixing reactive chemical solutions, and process for producing microcapsules |
| JP2007307494A (en) * | 2006-05-19 | 2007-11-29 | Yamazaki Co Ltd | Gas-mixing water producing device and humidifying device |
| US8985844B2 (en) * | 2007-11-12 | 2015-03-24 | Ika-Werke Gmbh & Co. Kg | Device for dispersing or homogenizing with a magnetic coupling drive for rotors in a chamber |
| KR100913875B1 (en) * | 2008-09-24 | 2009-08-26 | 박노성 | Dispersing pump |
| JP2011067794A (en) * | 2009-09-28 | 2011-04-07 | Sintokogio Ltd | High-shearing-type continuous dispersion apparatus |
| WO2011089715A1 (en) * | 2010-01-22 | 2011-07-28 | アイシン精機 株式会社 | Micro-bubble group generator and bubble bath apparatus |
| JPWO2011089715A1 (en) * | 2010-01-22 | 2013-05-20 | アイシン精機株式会社 | Fine foam group generating device and foam bathing device |
| US8939637B2 (en) * | 2011-04-08 | 2015-01-27 | Marcel Depault | Apparatus for mixing and pumping manure slurries |
| US20120257988A1 (en) * | 2011-04-08 | 2012-10-11 | Marcel Depault | Apparatus for mixing and pumping manure slurries |
| CN103055753A (en) * | 2012-12-27 | 2013-04-24 | 镇江市港南电子有限公司 | A novel stirring device for wafer polishing solutions |
| WO2015059759A1 (en) * | 2013-10-21 | 2015-04-30 | 株式会社長野セラミックス | Mixing nozzle |
| JPWO2015059759A1 (en) * | 2013-10-21 | 2017-03-09 | 株式会社長野セラミックス | Mixing nozzle |
| CN105561832A (en) * | 2015-12-31 | 2016-05-11 | 倪商伟 | Multilayer combined emulsification unit, emulsification machine using emulsification unit, and emulsification method |
| JP2019195760A (en) * | 2018-05-09 | 2019-11-14 | 株式会社愛工舎製作所 | Disc type mixing head having water cooling structure |
| CN112295481A (en) * | 2020-10-10 | 2021-02-02 | 孟广寻 | Liquid medicament secondary agitated vessel for bio-pharmaceuticals |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6214330B2 (en) | 1987-04-01 |
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