JPS6147570B2 - - Google Patents

Info

Publication number
JPS6147570B2
JPS6147570B2 JP57154372A JP15437282A JPS6147570B2 JP S6147570 B2 JPS6147570 B2 JP S6147570B2 JP 57154372 A JP57154372 A JP 57154372A JP 15437282 A JP15437282 A JP 15437282A JP S6147570 B2 JPS6147570 B2 JP S6147570B2
Authority
JP
Japan
Prior art keywords
oil
dispersion medium
dispersed phase
emulsion
recovery tank
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
Application number
JP57154372A
Other languages
Japanese (ja)
Other versions
JPS5946118A (en
Inventor
Hisashi Sugimoto
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Asahi Sunac Corp
Original Assignee
Asahi Okuma Industrial Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Asahi Okuma Industrial Co Ltd filed Critical Asahi Okuma Industrial Co Ltd
Priority to JP57154372A priority Critical patent/JPS5946118A/en
Publication of JPS5946118A publication Critical patent/JPS5946118A/en
Publication of JPS6147570B2 publication Critical patent/JPS6147570B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/40Mixing liquids with liquids; Emulsifying
    • B01F23/41Emulsifying
    • B01F23/411Emulsifying using electrical or magnetic fields, heat or vibrations
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00Other mixers; Mixing plants; Combinations of mixers
    • B01F33/05Mixers using radiation, e.g. magnetic fields or microwaves to mix the material

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Mixers With Rotating Receptacles And Mixers With Vibration Mechanisms (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、連続相となる油等の分散媒液体中に
水、食酢等の液体を分散してなるいわゆるW/O
型乳化物の製造法及び製造装置に関する。 互いに溶解しない油、水等の液体を混合して、
乳化物を製造するには、従来乳化剤となる界面活
性剤や、安定剤などを添加し、該乳化剤を油と水
の界面に配位することによりその界面張力を著し
く低下して界面自由エネルギーの増加をおさえる
ことにより施している。または、場合によつて
は、機械的撹拌によつて一時的に乳化物を製造す
る等による場合もある。 例えば、サラダドレツシングを製造するには、
互いに溶解しないサラダ油と、食酢の水溶液とを
卵黄を乳化剤として使用して混合することにより
施したり、または容器中で二相に分離した液体
を、使用直前で振つて物理的撹拌により一時的に
乳化させて施したりする。 このため、前者の乳化剤を使用する場合には、
該乳化剤に、食品としての制限から他の非食品性
の有機物を使用することができず、卵黄の使用に
よつて味覚が限定される。また乳化剤(界面活性
剤)は、そもそも界面自由エネルギーの増加速度
を緩和して完全分離までの時間を延長するだけの
ものであつて、前記卵黄の使用では長期間の乳化
状態を保持することができない。 また、後者の撹拌による場合は、極めて短期間
の乳化状態を実現する場合のみ有効であるから、
使用の度に撹拌する必要があつて煩に堪えない。 このように、従来の乳化方法には種々の欠点や
制約がある。 ところで、前記サラダドレツシングのような油
中に水等が分散するいわゆるW/O型乳化物にあ
つては、分散媒となる油は難導電性であり、分散
相となる水等は導電性であるから、水等の微粒子
に同極性の静電気を帯電すれば、各分散相微粒子
相互が反発して液層の分離過程である分散粒子相
互の融合が阻止され、しかも前記の帯電状態は、
油によつて絶縁保持されるから、乳化状態は長期
間に亘つて継続することが考えられる。 本発明は前記知見に基づいた、乳化物を必ずし
も要しない新たな乳化物の製造方法及び製造装置
の提供を目的とするものである。 本発明の一実施例を添付図面について説明す
る。 底面にバルブ3によつて適宜量の採取を可能と
した回収用流通管4を設けた球形の回収槽2を支
持柱1に固定し、かつ該回収槽2を電気的にアー
スする。前記回収槽2には、油を噴射する噴霧器
5と、水等の油と融合しない液体を噴射する噴霧
器6とを交互に多数設ける。 前記噴霧器5,6は無気式、空気式のいずれで
もよく、静電塗装などに使用する公知の噴霧器を
用いることができる。 前記噴霧器5は、貯溜槽7から配管8を通つて
エアレスポンプ9により、油が圧送され、エアー
作動弁等によつて、その弁の開閉を制御され、開
弁によつてノズルからポンプ9の圧力で油を微粒
状にして、噴出する。前記噴霧器5、貯溜槽7及
びエアレスポンプ9等はアースされ、これにより
噴出する油に電荷を生じないようにする。 前記噴霧器6は、同じく貯溜槽10から配管1
1を通つてエアレスポンプ12により水等の液体
が圧送され、該水等を微粒状にして噴出する。前
記液体は、直流高電圧発生装置13によつて正又
は負のいずれかの極で2KV以上の高電圧を印加さ
れる。前記貯溜槽10、エアレスポンプ12及び
その圧送配管11は、前記電流が漏電するのを防
止するため、夫々絶縁されている。 噴霧器5,6の噴射口は夫々回収槽2中に向け
られていて、このため、各噴霧器5,6から微粒
化して噴出する油、水の噴霧流は、回収槽2の中
心付近で衝突し、その噴出力によつてよく混合す
る。混合しながら回収槽2中に回収された液体は
該回収槽内でミキサー14によつてさらに混合さ
れ、水等の微粒子は、油中で均一に分散すること
となる。 前記のように油中で機械的に分散された水等の
分散相微粒子は、直流高電圧発生装置13による
電圧印加によつて、正又は負の同極の静電気が帯
電している。このため、各微粒子間に反発力が働
き、微粒子のブラウン運動等によつて生ずる分散
粒子相互の融合が阻止される。このとき油は、難
導電性であつて、前記分散相微粒子の帯電状態を
外部と電気的に遮断することによつて保持し、こ
のため、水等の分散相微粒子が油等の分散媒中で
長期間分散状態が保持され、乳化物が製造され
る。 前記の装置を用いて、製造した乳化物の分離時
間と、印加した電圧との関係を下記に示す。
The present invention uses so-called W/O, which is made by dispersing a liquid such as water or vinegar in a dispersion medium liquid such as oil, which becomes a continuous phase.
The present invention relates to a method and apparatus for producing a type emulsion. By mixing liquids such as oil and water that do not dissolve in each other,
Conventionally, to produce emulsions, surfactants and stabilizers are added to act as emulsifiers, and the emulsifiers are coordinated to the interface between oil and water, thereby significantly lowering the interfacial tension and increasing the interfacial free energy. This is done by suppressing the increase. Alternatively, in some cases, an emulsion may be temporarily produced by mechanical stirring. For example, to make salad dressing,
It can be applied by mixing salad oil and an aqueous solution of vinegar, which do not dissolve in each other, using egg yolk as an emulsifier, or the liquid separated into two phases in a container can be temporarily emulsified by shaking and physically stirring just before use. Let them do it and give it to you. Therefore, when using the former emulsifier,
Due to food restrictions, other non-food organic substances cannot be used as the emulsifier, and the use of egg yolk limits the taste. In addition, emulsifiers (surfactants) only slow down the rate of increase in interfacial free energy and extend the time until complete separation, and when using egg yolk, it is difficult to maintain an emulsified state for a long period of time. Can not. In addition, the latter method of stirring is effective only when achieving an emulsified state for an extremely short period of time.
It is unbearable to have to stir it every time it is used. As described above, conventional emulsification methods have various drawbacks and limitations. By the way, in the case of so-called W/O emulsions where water etc. are dispersed in oil such as the salad dressing mentioned above, the oil serving as the dispersion medium is poorly conductive, and the water etc. serving as the dispersed phase is conductive. Therefore, if fine particles such as water are charged with static electricity of the same polarity, each dispersed phase fine particle will repel each other, and the fusion of the dispersed particles with each other, which is the liquid layer separation process, will be prevented. ,
It is thought that the emulsified state continues for a long period of time because it is insulated and maintained by the oil. The present invention is based on the above findings and aims to provide a new method and apparatus for producing an emulsion that does not necessarily require an emulsion. An embodiment of the invention will be described with reference to the accompanying drawings. A spherical recovery tank 2, which has a recovery flow pipe 4 on the bottom that allows collection of an appropriate amount by means of a valve 3, is fixed to a support column 1, and the recovery tank 2 is electrically grounded. The recovery tank 2 is alternately provided with a large number of sprayers 5 for spraying oil and sprayers 6 for spraying a liquid such as water that does not fuse with oil. The sprayers 5 and 6 may be either airless type or air type, and known sprayers used for electrostatic coating can be used. The sprayer 5 is supplied with oil by an airless pump 9 from a storage tank 7 through a pipe 8, and the opening and closing of the valve is controlled by an air-operated valve or the like. The pressure turns the oil into fine particles and squirts it out. The atomizer 5, reservoir 7, airless pump 9, etc. are grounded to prevent electrical charge from being generated in the ejected oil. The sprayer 6 is also connected to the pipe 1 from the storage tank 10.
A liquid such as water is pumped through the pump 1 by an airless pump 12, and the water or the like is pulverized and ejected. A high voltage of 2 KV or more is applied to the liquid by a DC high voltage generator 13 at either the positive or negative pole. The storage tank 10, the airless pump 12, and its pressure-feeding pipe 11 are each insulated to prevent the current from leaking. The spray ports of the sprayers 5 and 6 are each directed into the recovery tank 2, so that the atomized oil and water sprays ejected from the sprayers 5 and 6 collide near the center of the recovery tank 2. , mixes well by its jet power. The liquid collected into the recovery tank 2 while being mixed is further mixed within the recovery tank by the mixer 14, and fine particles such as water are uniformly dispersed in the oil. As described above, the dispersed phase fine particles such as water, which are mechanically dispersed in oil, are charged with static electricity of the same positive or negative polarity by the voltage application by the DC high voltage generator 13. Therefore, a repulsive force acts between each fine particle, and fusion of dispersed particles caused by Brownian motion of fine particles or the like is prevented. At this time, oil has poor electrical conductivity and maintains the charged state of the dispersed phase fine particles by electrically insulating them from the outside, so that the dispersed phase fine particles such as water are contained in the dispersion medium such as oil. The dispersion state is maintained for a long period of time to produce an emulsion. The relationship between the separation time of the emulsion produced using the above-mentioned apparatus and the applied voltage is shown below.

【表】 上記のように、電圧の増加とともに分離時間が
長くなり、30KV以上になると、その分離に極め
て長時間を要することが解かる。 前記分離時間をさらに延長するために、既知の
乳化剤を併用して用いてもよい。 前記の説明で明らかにしたように、第一の発明
は、油等の難導電性分散媒液体と、高電圧の印加
により同極性の静電気を帯電させた水等の導電性
分散相液体とを夫々微粒化し、かつ夫々の噴霧流
を相互に衝突させることによつて、機械的に分散
媒中に分散相微粒子を分散させ、その静電反発力
によつて微粒子の融合凝集を阻止し、長期的に安
定な乳化物を製造するものであるから、乳化剤を
使用することなく乳化物を製造でき、例えばサラ
ダドレツシングのような食品の製造に際して乳化
剤添加による味覚の制約や、乳化剤による食品汚
染等の問題を解決でき、さらに、もつぱら物理的
操作によつて乳化物を製造するものであるから設
備が簡単となり、かつ製造単価が低廉となる等の
優れた効果がある。 また第二の発明は、分散媒、分散相を静電塗装
等で通常使用されるような噴霧器5を使用して、
微粒化し、かつその噴霧流を回収槽2上で衝突さ
せて、前記第一の発明を実施し得るようにしたも
のであつて、装置が簡単でかつ量産に向く等の優
れた効果がある。
[Table] As shown above, as the voltage increases, the separation time increases, and when the voltage exceeds 30KV, it can be seen that the separation takes an extremely long time. In order to further extend the separation time, known emulsifiers may be used in combination. As clarified in the above description, the first invention uses a poorly conductive dispersion medium liquid such as oil and a conductive dispersed phase liquid such as water that is charged with static electricity of the same polarity by applying a high voltage. By atomizing each particle and causing the respective spray streams to collide with each other, the dispersed phase particles are mechanically dispersed in the dispersion medium, and the electrostatic repulsion prevents the particles from coalescing and agglomerating, resulting in a long-term Because it produces a stable emulsion, it is possible to produce an emulsion without using an emulsifier.For example, when producing foods such as salad dressings, there are no restrictions on taste due to the addition of emulsifiers, and food contamination caused by emulsifiers. In addition, since the emulsion is produced solely through physical operations, it has excellent effects such as simple equipment and low manufacturing cost. Further, the second invention uses a sprayer 5 such as the one normally used in electrostatic coating to spray the dispersion medium and the dispersed phase.
The first invention can be carried out by atomizing the particles and colliding the spray stream on the recovery tank 2, which has excellent effects such as a simple device and suitable for mass production.

【図面の簡単な説明】[Brief explanation of the drawing]

添付図面は本発明装置の一実施例を示し、第1
図は縦断側面図、第2図は平面図である。 2:回収槽、5,6:噴霧器、7:(油の)貯
溜槽、10:(水の)貯溜槽、13:直流高電圧
発生装置。
The attached drawings show one embodiment of the device of the present invention, and the first
The figure is a longitudinal side view, and FIG. 2 is a plan view. 2: recovery tank, 5, 6: sprayer, 7: (oil) storage tank, 10: (water) storage tank, 13: DC high voltage generator.

Claims (1)

【特許請求の範囲】 1 油等の難導電性分散媒液体と、高電圧の印加
により同極性の静電気を帯電させた一種類以上の
導電性分散相液体とを夫々噴霧微粒化し、かつ、
夫々の噴霧流を相互に衝突させて混合し、分散相
微粒子を相互の静電反発力により分散媒中に均一
に分散させるようにしたことを特徴とする乳化物
の製造法。 2 回収槽の開口周囲に、難導電性分散媒液体を
噴出する噴霧器と、高電圧の印加により同極性の
静電気を帯電させた分散相液体を噴出する噴霧器
とを、その噴霧口を回収槽中心付近に向けて配設
してなり、該両噴霧器によつて噴霧微粒化した噴
霧流を回収槽上で衝突させ、該回収槽に回収する
構成としたことを特徴とする乳化物の製造装置。
[Scope of Claims] 1 A poorly conductive dispersion medium liquid such as oil and one or more conductive dispersed phase liquids charged with static electricity of the same polarity by applying a high voltage are respectively atomized by atomization, and
A method for producing an emulsion, characterized in that the respective spray streams are mixed by colliding with each other so that dispersed phase fine particles are uniformly dispersed in a dispersion medium by mutual electrostatic repulsion. 2. Place a sprayer that sprays a non-conductive dispersion medium liquid around the opening of the recovery tank, and a sprayer that sprays a dispersed phase liquid that has been electrostatically charged with the same polarity by applying a high voltage, with the spray port placed in the center of the recovery tank. 1. An emulsion manufacturing apparatus, characterized in that the emulsion manufacturing apparatus is arranged to face nearby, and has a configuration in which the spray streams atomized by the two atomizers collide on a collection tank and are collected in the collection tank.
JP57154372A 1982-09-03 1982-09-03 Method and apparatus for preparing emulsion Granted JPS5946118A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57154372A JPS5946118A (en) 1982-09-03 1982-09-03 Method and apparatus for preparing emulsion

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57154372A JPS5946118A (en) 1982-09-03 1982-09-03 Method and apparatus for preparing emulsion

Publications (2)

Publication Number Publication Date
JPS5946118A JPS5946118A (en) 1984-03-15
JPS6147570B2 true JPS6147570B2 (en) 1986-10-20

Family

ID=15582713

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57154372A Granted JPS5946118A (en) 1982-09-03 1982-09-03 Method and apparatus for preparing emulsion

Country Status (1)

Country Link
JP (1) JPS5946118A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013095884A (en) * 2011-11-03 2013-05-20 Hiroshi Yamashita Apparatus and method for generating emulsion fuel
JP2013245299A (en) * 2012-05-25 2013-12-09 Hiroshi Yamashita Apparatus and method of producing mixed fuel

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013095884A (en) * 2011-11-03 2013-05-20 Hiroshi Yamashita Apparatus and method for generating emulsion fuel
JP2013245299A (en) * 2012-05-25 2013-12-09 Hiroshi Yamashita Apparatus and method of producing mixed fuel

Also Published As

Publication number Publication date
JPS5946118A (en) 1984-03-15

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