WO1990012639A1 - Emulsion liquide sans emulsifiant; procede et dispositif pour la preparer - Google Patents

Emulsion liquide sans emulsifiant; procede et dispositif pour la preparer Download PDF

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Publication number
WO1990012639A1
WO1990012639A1 PCT/EP1990/000636 EP9000636W WO9012639A1 WO 1990012639 A1 WO1990012639 A1 WO 1990012639A1 EP 9000636 W EP9000636 W EP 9000636W WO 9012639 A1 WO9012639 A1 WO 9012639A1
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WO
WIPO (PCT)
Prior art keywords
mixture
chamber
chamber portion
flow
axis
Prior art date
Application number
PCT/EP1990/000636
Other languages
English (en)
Inventor
Armando Ulrich
Walter H. +di OTT
Original Assignee
'harrier' Gmbh Gesellschaft Für Den Vertrieb Medizinischer Und Technischer Geräte
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
Priority claimed from DE8905075U external-priority patent/DE8905075U1/de
Application filed by 'harrier' Gmbh Gesellschaft Für Den Vertrieb Medizinischer Und Technischer Geräte filed Critical 'harrier' Gmbh Gesellschaft Für Den Vertrieb Medizinischer Und Technischer Geräte
Priority to DE69011679T priority Critical patent/DE69011679T2/de
Priority to SU905010224A priority patent/RU2072891C1/ru
Priority to EP90906170A priority patent/EP0469014B1/fr
Publication of WO1990012639A1 publication Critical patent/WO1990012639A1/fr

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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/40—Mixing liquids with liquids; Emulsifying
    • B01F23/41—Emulsifying
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/10—Mixing by creating a vortex flow, e.g. by tangential introduction of flow components
    • 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
    • B01F25/10—Mixing by creating a vortex flow, e.g. by tangential introduction of flow components
    • B01F25/102—Mixing by creating a vortex flow, e.g. by tangential introduction of flow components wherein the vortex is created by two or more jets introduced tangentially in separate mixing chambers or consecutively in the same mixing chamber
    • 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
    • B01F2025/919—Direction of flow or arrangement of feed and discharge openings characterised by the disposition of the feed and discharge openings
    • B01F2025/9191—Direction of flow or arrangement of feed and discharge openings characterised by the disposition of the feed and discharge openings characterised by the arrangement of the feed openings for one or more flows, e.g. for the mainflow and the flow of an additional component

Definitions

  • Emulgator-free liquid emulsion and method and device for producing the emulsion are provided.
  • the present invention relates to a preparation method and device " for stably mixing a plurality of substances differing in the physical properties, especially a liquid and a liquid, and a mixture emulsion formed thereby.
  • Another object of the present invention is to provide a mixing device for use in carrying out this mixing method.
  • Still another object of the present invention is to provide a stable mixture emulsion of at least one hydrophobic liquid phase and at least one hydrophilic liquid phase and prepared or preparable by this mixing apparatus.
  • the e ulgator-free emulsion, the method and the mixing device in accordance with the present invention have especially the features as described in the claims.
  • a colloidal emulgator-free emulsion comprising a hydrophilic liquid, especially water, and a hydrophobic liquid, wherein fine liquid drops of the disperse liquid phase are homogeneously and stably distributed in the emulsion without the aid of an emulsifier.
  • the preferred composition of the water/hydrophobic liquid mixture is such that the amount of the hydrophobic liquid is up to 20% by volume based- on water.
  • a mixture comprising water and a hydrophobic liquid, wherein fine liquid drops of the water are homogeneously and stably distributed in the hydrophobic liquid without the aid of an emulsifier.
  • the preferred composition of the water/hydrophobic liquid mixture is such that the amount of the water is 5-35% by volume based on the hydrophobic liquid.
  • a colloidal mixture comprising a hydrophilic liquid and a hydrophobic liquid, wherein fine liquid drops are homogeneously and stably distributed without the aid of an emulsifier.
  • the preferred composition of the hydrophilic liquid and the hydrophobic liquid is such that the amount of the hydrophobic liquid is up to 20% by volume based on the hydrophilic liquid.
  • the term "colloid" or "colloidal" state means a state in which colloidal particles having a size of about 1,000 nm or less are contained, the existence of the colloidal particles and the occurrence of a Brownian movement are confirmed by an ultramicroscope, and a Tyndall phenomenon is observed.
  • Fig. 1 is a diagram illustrating a general layout of a preferred first embodiment of the mixing device comprising a mixing apparatus used in the present invention.
  • Fig. 2 is an elevation sectional view of the mixing apparatus 1 shown in Fig. 1.
  • Fig. 3 is a cross sectional view of the top portion of the mixing apparatus 1 shown in Fig. 1.
  • Fig. 4 is a diagram illustrating a second embodiment of the mixing device used in the present invention.
  • Fig. 5 is a diagram illustrating a third embodiment of the mixing device used in the present invention .
  • Fig. 6 is a diagram illustrating the structure of an example of the cylindrical housing defining the hollow interior space of the jet pump 50 of the mixing device shown in Fig. 5.
  • Fig. 7 is a diagram illustrating a mixing device resembling the mixing apparatus shown in Fig. 4.
  • Fig. 8 is a diagram illustrating an example of the apparatus used for measuring the stability of a mixture containing a saturation amount of a gas in a hydrophobic liquid or hydrophilic liquid.
  • FIG. 1 A general device according to the first embodiment of the device for use in carrying out the present invention is shown in Fig. 1.
  • the elevation of a mixing apparatus 1 is shown in Fig. 2 and the top section of the mixing apparatus 1 in the plane of a hole of the mixing apparatus 1 is shown in Fig. 3.
  • the mixing apparatus 1 is described with reference to Figs. 2 and 3.
  • the mixing apparatus 1 comprises a cylindrical wall which is opened at one end 10 and closed at the opposite end 11. Within this cylinder, there is defined a hollow element 13 comprising a first portion 14 having a circular rim 12 connected to the central part thereof and a second portion 17. The first portion
  • the 14 of this element 13 has a shape of a substantially hollow parabolic surface arranged in a closed chamber formed between the rim 12 and the closed end 11 of the mixing apparatus 1.
  • the first portion 14 has a shape of a completely hollow parabolic surface. A certain number of holes
  • the elements 13 include the second portion 17 communicating with the first portion 14 at the plane of the rim 12, and this portion has a substantially tapered shape which is continuous as a short cylindrical duct 18. In a preferred embodiment, the portion 17 has a shape of a complete hyperbola.
  • the mixing apparatus 1 is formed of glass.
  • a fluid component is caused to flow to the first portion 14 through the inclined duct 16 while being rotated, and in the first portion 14, the majority of the fluid component introduced into the holes 15 is caused to flow along the inner wall of the fist portion 14 toward the top (downward in Fig. 2) while being further rotated. At the top, the flow is reflected and the flow speed is gradually increased, and a vortex state is formed on the central axis toward the second portion. Different substances are mixed by this vortex state.
  • a liquid mixture of a hydrophobic liquid phase and an hydrophilic liquid phase is introduced through-the inlet duct 16. Owing to the off-axis and oblique arrangement of the inlet duct 16 the inflowing fluid will rotate around the central .axis of the mixing apparatus 1 and the rotating fluid enters in through the tangential openings 15 in the wall 14 of the first chamber portion.
  • a focal line is formed where pressure is at minimum, and along the axis the pressure decreases in axial direction towards the outlet opening. This means that pressure is decreasing gradually both in radial and axial direction, and the fluid rotates around the axis and flows in axial direction.
  • the speed of flow and the velocity of rotation increases gradually toward the outlet duct portion 18 and in radial direction the pressure decreases towards the axis and a minimum is experienced along the axis. It is preferred if the rotational hyperboloid function has the same grade as the paraboloid function of the first chamber portion has.
  • the flow will have a structure which can be visualized in such a way as if the fluid mass consisted of an infinitely high numbers of annular hollow tubes having a form substantially following that of the tapering section 17, and the speed of rotation was different in case of each tube so that the elementary tubes were sliding on each other during their rotational movements. Moreover, the elementary tubes slide with respect to each other not only due to their differing speeds of rotation but they are moving and sliding in axial direction as well.
  • the flow rate should be adjusted in such a way that phase transition (i.e. vaporization of any component) do not take place, nevertheless the minimum pressure should be just above the vapour pressure of the liquid mixture.
  • this condition should relate to the one which has the highest vapor pressure at the given temperature.
  • This condition is equivalent to the statement that cavitation cannot occur in the flow.
  • the mixing apparatus being preferably of glass, said condition can be adjusted by increasing the flow velocity up to a measure at which fine gas bubbles appear in the duct portion 18, and then lowering the flow velocitity by a small amount just until the gas bubbles dissappear again.
  • a closed circulation passage comprising a pump 2 and a vessel 3, which are connected to each other through conduits 4, 5, 6 and 7, is formed.
  • Reference numeral 8 represents a withdrawal opening for the withdrawal of a mixture, which has a cock. The opening is always closed except at the time of the withdrawal of the mixture.
  • the vessel 3 has a cock-provided duct 31 and a cock-provided duct 32 for charging starting materials to be formed into a mixture. The fluid flows- as indicated by arrows.
  • the cock of the duct 31 is opened and 9 1 of distilled water is filled in the vessel 3. Then, the cock of the duct 3Z is opened and 1 1 of a vitamin A oil as the starting oil is filled in the vessel 3 and the cocks of the ducts 31 and 32 are closed.
  • the vessel 3 is fully filled with water and vitamin A oil, or the upper portion of the vessel 3 may be vacant.
  • the pump 2 is started.
  • This pump has a flow quantity of 25 1/min.
  • the inner diameters of the conduits 4, 5, 6 and 7 are equally about 14 mm.
  • the flow direction is indicated by arrows in Fig. 1.
  • Water and vitamin A oil are introduced into the mixing apparatus 1, and in the mixing apparatus 1, water and vitamin A oil flow into the interior of the cylindrical wall from the inclined duct 16 while being rotated and flow in the first portion 14 through the tangential holes 15 to form a vortex in the hollow element 13. This will now be described in detail.
  • the majority of the rotating fluid component first flows to the closed top of the paraboloid and is reflected forward therefrom, and because of the exponentially tapered shape of the second portion 17 of the hollow element 13, the fluid component is promptly rotated together with the other component and the fluid component is advanced in the conduit 5 toward the vessel 3.
  • the fluid component is circulated in the closed system until the pump 2 is turned off.
  • the cock is opened and the water/vitamin A oil mixture is withdrawn from the withdrawal opening 8.
  • a hydrophilic liquid is mixed with a hydrophobic liquid by using the mixing device of the embodiment shown in Fig. 1
  • the cock of the duct 31 is opened, and the vessel 3 is filled with 9 1 of ethyl alcohol, and then the cock of the duct 32 is opened and 1 1 of of a vitamin oil is filled in the vessel 3.
  • the subsequent procedures are the same as described above.
  • a mixture of 9 1 of a vitamin A oil and 1 1 of ethyl alcohol is similarly prepared according to the above-mentioned method.
  • the obtained mixture formed by mixing ethyl alcohol and vitamin A oil without the aid of an emulsified according to the above-mentioned method can be widely used for cosmetic lotions and cosmetic creams.
  • the second .embodiment is different from the -first embodiment mainly in that a vessel 9 for forming a second vortex is used instead of the mixing apparatus 3.
  • the vessel 9 has a substantially spherical upper part 91, a lower part 93 tapered downwardly and an intermediate part 92 connected smoothly to the spherical upper part 91 and the lower part 93.
  • the upper part 91 and intermediate part 92 have a convex face and the lower part 93 has a concave face.
  • an inflection face is formed between the intermediate part 92 and the lower part 93.
  • the vessel 9 is formed of glass so that the process occurring in the vessel 9 can be observed.
  • Three ducts 95, 96 and 97 are formed on the top wall of the upper part 91 and they are sealed.
  • the vessel 9 is filled with starting substances.
  • the vessel 9 further has two openings. At a substantial height where the vessel has a maximum diameter, a duct 98 extends obliquely from the upper portion of the intermediate 92.
  • the duct 98 forms an acute angle to each of equator and tangent planes of the vessel 9 and the axis of the duct 98 is slightly inclined inwardly and upwardly in the interior direction of the vessel 9. In general, these angles are smaller than 30°.
  • the second opening is the end of the open bottom of the lower part 93 of the vessel 9.
  • a circulation passage comprising the pump 2, the mixing apparatus 1 and four conduits 4, 5, 6' and 7 is arranged between the lower part 93 and the inclined duct 98.
  • Fig. 4 In the mixing apparatus 1, a closed circulation passage is formed through the pump 2, the vessel 9, withdrawal opening 8 and the conduits 4, 5, 6' and 7. How a water/hydrophobic liquid can be prepared without the aid of an emulsifier by using the device shown in Fig. 4 is described.
  • 9.5 1 of distilled water is filled in the vessel 9 through the duct 97.
  • 0.5 1 of squalane is filled in the vessel 9 through the duct 95.
  • the ducts 95 and 97 are sealed.
  • the vessel 9 may be completely filled with water and squalane, or the upper part of the vessel 9 may be left vacant.
  • the pump 2 is started.
  • the flow direction is indicated by arrows in Fig. 4.
  • the same members as in the first embodiment are represented by the same reference numerals.
  • the third embodiment is different from the first embodiment mainly in that a jet pump 50 connected to the mixing apparatus 1 is arranged in the closed system.
  • a vessel 30 comprising a cover and ducts 31 and 32 is used.
  • the vessel 30 is filled with starting substances.
  • the vessel 30 is connected to the pump 2 through the conduit 6' , withdrawal opening 8 and conduit 7 located at the lower portion of the vessel 30.
  • the flowout conduit 4 is connected to the inlet of the jet pump 50.
  • the internal structure of the jet pump 50 is shown in Fig. 6.
  • An inlet duct 54 of the jet pump 50 communicates with the vessel 30 through a duct 51.
  • the jet pump 50 exerts a function of promoting the mixing of two different liquids.
  • the jet pump 50 has a substantially cylindrical housing 52 having a hollow internal space, as shown in Fig. 6.
  • a nozzle 53 is inserted in the hollow internal space of the housing 52 and the top end of the nozzle 52 is connected to the duct 4.
  • a cylindrical space is formed in the vincinity of the top end of the nozzle 53 and an inlet duct 54 is inserted in the wall of the housing 52, and as the result, the hollow internal space of the inlet duct 54 communicates with the cylindrical space in the vincinity of the top end of the nozzle 53.
  • the water jet pump is used, but there may be adoped a method in which a branched pipe is used instead of the water jet pump and the outlet side of this tube is connected to the inlet side of the mixing apparatus 1.
  • the cock of the duct 31 is opened and the vessel 31 is filled with 9.5 1 of ethyl alcohol. Then, the cock of the duct 32 is opened and 0.5 1 of squalane as the starting oil is filled in the vessel 30. The cock of the ducts 31 and 32 are closed.
  • a squalane-rich liquid in the vessel 30 is sucked into the pump 2 and is caused to flow in the vessel 30 through the conduit 4, jet pump 50, mixing apparatus 1 and conduit 5.
  • a closed system is formed.
  • an alcohol-rich liquid in the vessel 30 is injected into the jet pump 50 through the conduit 51. In this closed system, ethyl alcohol and squalane are mixed by the circulation. In this manner, a mixture of ethyl alcohol and squalane is formed.
  • this mixing apparatus 1 if this mixing apparatus 1 is used, at least two kinds of liquids can be stably and homogeneously mixed.
  • Fig. 7 show a device resembling the device shown in Fig. 4.
  • the pump 2 and mixing apparatus 1 are those used in the first embodiment, and the vessel 9 is that used in the second embodiment.
  • An oxygen-supplying gas source 60 and an injector (with no needle) 61 are used.
  • the gas source 60, injector 61 and duct 97 are connected to conduits 68 (68a, 68b and 68c) provided with glass cocks 62, 63 and 64, respectively.
  • the duct 95 is connected to a conduit 65, the end of the conduit 65 is contained in a trap 66 filled with water, and the trap 66 is connected to a glass cock 67.
  • a duct 96 is opened and 10 1 of octane as the hydrophobic liquid is filled in the vessel 9, and the duct 96 is closed.
  • the glass cock 62 and 64 are opened and a pressing member (piston) 61a of the injector 61 is taken out from the injector 61.
  • the glass cock 63 is opened to inject oxygen into the circulation passage for expelling air present in the interior.
  • the pressing member is set at the injector 6 so that the measurement scale is 200 ml.
  • the level of water in the trap 66 is made in agreement with the water level in the conduit 65, and the glass cock 67 is closed.
  • the pump 2 is started, the pressure in the vessel 9 is reduced, and a reduced pressure is also maintained in the conduit 65 and the water level in the conduit becomes higher than the water level in the trap 66.
  • the pump 2 is stopped twice a day, and oxygen in the injector 61 is pressed into the circulation passage through the pressing member 61a so that the water level in the trap 66 is made equal to the water level in the conduit 65.
  • oxygen in the injector 61 is exhausted, in the same manner as described above, the glass cock 63 is opened and the gas source 60 is connected to the injector and oxygen is injected into the injector 61.
  • a series of experiments were carried out in the above-mentioned manner.
  • the intake of oxygen gas for 28 days' operation was 7440 ml/10 1 (21°C). This value corresponds to about 2.4 times the saturation solubility.
  • the intake of oxygen gas for 28 hours' operation was 6640 ml/10 1 (21°C). This value corresponds to about 2.8 times the saturation solubility.
  • the pump 2 was stopped and the system was allowed to stand still. After 12 hours' stoppage of the pump 2, the water level of the trap 66 was measured. No change was observed. Accordingly, it can be said that methyl alcohol containing the excessive amount of oxygen was very small.
  • the vessel 9 for forming the second vortex was used, but any device capable of supplying a liquid and a gas into the mixing apparatus 1 can be used.
  • FIG. 8 An embodiment of the apparatus for measuring the stability of a gas-containing mixture of a hydrophobic liquid or hydrophilic liquid is illustrated in Fig. 8.
  • An Erlenmeyer flask 76 is charge with 100 ml of octane containing an excessive amount of oxygen gas, and the upper space is filled with air.
  • the Erlenmeyer flask 76 is arranged on a stand 77 and can be heated from below by a burner 78.
  • the top end portion of the Erlenmeyer flask 76 is connected to a hose type cooling tube 74 by using a fitting glass.
  • This hose type cooling tube 74 is perpetually cooled by cooling water not shown in the drawings.
  • the top end of the hose type cooling tube 74 is sealed by a plug and is connected to an injector 70 through a glass tube 72 and a silicone tube 71.
  • a piston is set at a scale of "0".
  • the concentration of oxygen in the open air is measured by a gas detector for the measurement of the oxygen concentration (supplied by Gastec co.), it is found that the concentration is 20.8%. Then, octance containing an excessive amount of oxygen gas is charged in the Erlenmeyer flask 76 and is boiled by the burner 78. By this boiling, the pressing member of the injector 70 is pressed back. The injector 70 is taken out, and the oxygen gas concentration in air in the injector 70 is measured. The oxygen concentration is 22.1%. The same sample is boiled for 2 hours and the measurement is conducted in the same manner as described above. The oxygen concentration is 22.1%.
  • oxygen contained in octane is stable in a super-saturated state (about 2.3 times).
  • the stability measurement test is similarly carried out with respect to methyl alcohol containing an excessive amount of oxygen gas by using the same measurement equipment as mentioned above.
  • the oxygen concentration in the open air is 20.8% and the oxygen concentration after 1 hour's boiling is 21.9%. Furthermore, the oxygen concentration after 2 hours' boiling is 21.9%. Accordingly, it can be said that oxygen contained in methyl alcohol in a super-saturated state (about 2.7 times) is in a stable state.
  • the volume of carbon dioxide contained in methyl alcohol is about 1.8 times the saturation solubility, and at the stability test, a stable state is observed at a concentration about 1.35 times the saturation solubility. Accordingly, it is understood that if the mixing apparatus of the present example is used, a gas is stably incorporated in other gas in a super-saturation state.
  • a laser beam source unit i.e., GL-803N, manufactured by Nakamura Rika Ko o K. .
  • the cubic cell was set on a microscope (BH-2 manufactured by Olympus optical co., Ltd.) and a ultramicroscope was composed, together with the above-mentioned laser beam source unit.
  • the cubic cell was irradiated with a laser beam via the above-mentioned slit from the laser beam source unit.
  • the existence of oil drops was confirmed and the occurrence of a Brownian movement was also confirmed.
  • the resultant mixture was allowed to stand at room temperature for one day under a tightly sealed condition. As a result, it was confirmed that the water and the vitamin A oil in the vessel were separated and the underpositioned water was transparent and was not turbid. On the other hand, when one drop each of the upperp ⁇ sitioned vitamin A oil and the underpositioned water placed on a separate preparation was observed by the above-mentioned optical microscope, it was confirmed that neither the water drops nor the oil drops were a mixture of water and oil. Furthermore, neither oil in the water drops nor water in the oil drops were observed by the above-mentioned ultramicroscope.
  • the 16 upper oil-in-water portion and the lower water-in-oil portion are stably existed as a colloidal condition.
  • the resultant mixtures were centrifugally separated for 5 minutes at 3,000 rpm, it was confirmed by the above-mentioned optical microscope that the occurrence of the Tyndall phenomenon was confirmed in the resultant centrifugally separated portion although the present of the water drops was not observed.
  • the centrifugally separated portion was observed by a ultramicroscope, the existence of the water drops and the occurrence of the Brownian movement were confirmed. Accordingly, the size of the water drops was estimated to be about 100 nm.
  • the ethyl alcohol/vitamin A oil mixture prepared according to the first embodiment as the hydrophilic liquid/hydrophobic mixture was photographed by the microscope according to the above-mentioned method, it was confirmed that the droplet size of the vitamin A oil in ethyl alcohol was about 500 nm. No substantial change of the state was observed with respect to the distribution of ethyl alcohol and vitamin A oil between the mixture just after the mixing and the mixture which had been stored in a thermostat tank maintained at 50°C for 20 days.
  • the ethyl alcohol/vitamin A oil mixture on the preparation was warmed to evaporate water, adhesion of the oily substance onto the preparation was confirmed.
  • illustration has also been made with respect to the combina ⁇ ,ion of one liquid and one gas.
  • the present embodiment is not limited to this combination and a combination of a plurality of liquids and one gas or a combination of a plurality of liquids and a plurality of gases can be used.
  • a plurality of mixing apparatuss 1 can be arranged in series or in parallel in one closed flow passage, and other substance can be supplied linearly or in the reversely rotated state in a vortex formed within the mixing apparatus. Furthermore, the. mixing method, mixing device and mixture are not limited to those specifically disclosed in the examples.
  • hydrophobic liquid oily materials such as carnauba wax and liquid paraffin and fossil fuels such as benzene, decane, and gas oil, vegetable oils such as sesame oil, and by the term “hydrophilic liquid” are meant various alcohols such as monohydric and dihydric alcohols.
  • the obtained mixture is advantageous in the cost because an emulsifier need not be used, and hence, the limitations by the use of the emulsifier or the like are eliminated and the mixture can be widely used.
  • a hydrophilic liquid containing oxygen is used for cosmetic lotions or cosmetic creams, an effect of activating the skin can be attained.
  • hydrophobic liquids e.g., vegetable oil
  • hydrophilic liquids e.g., ethyl alcohol, propylene glycol

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Polymerisation Methods In General (AREA)
  • Medicinal Preparation (AREA)
  • Agricultural Chemicals And Associated Chemicals (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
  • Colloid Chemistry (AREA)
  • Cosmetics (AREA)
  • Processing Of Solid Wastes (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

Cette émulsion consiste en au moins une phase liquide hydrophobe et en au moins une phase liquide hydrophile, l'une de ces phases étant une phase dispersée de l'émulsion, dont l'état colloïdal est stable et dont les particules ont une taille de 1000 nm au maximum. Le procédé pour produire cette émulsion liquide sans émulsifiant consiste à faire recirculer en continu les phases liquides mélangées à travers une chambre de mélange dont la forme est axialement symétrique et dans laquelle on fait circuler le mélange de manière à ce qu'il tourne autour de l'axe, avec une composante d'écoulement parallèle à l'axe; on réduit la pression d'écoulement du mélange dans le sens de l'écoulement en augmentant progressivement la vitesse du mélange sur son parcours vers l'endroit où le mélange en rotation est coaxialement évacué de la chambre de mélange jusqu'à ce que cette pression d'écoulement atteigne une pression minimum proche de la pression de vapeur du mélange, sans atteindre cette pression de vapeur ni tomber en dessous de cette pression de vapeur. Dans le dispositif correspondant, l'appareil de mélange (1) comprend une chambre de mélange dont la forme est à symétrie de rotation et qui est agencée dans un élément creux (14) doté d'une pluralité d'ouvertures d'entrée tangentielles (15); ces ouvertures d'entrée débouchent sur une première portion de chambre reliée à une seconde portion de chambre, dont la section va en diminuant dans le sens de l'écoulement et qui comporte une sortie axiale coaxiale à l'axe de la chambre de mélange. La première portion de la chambre est de forme rotativement paraboloïde tandis que la seconde section de chambre est de forme rotativement hyperboloïde inverse. Ladite sortie axiale est une portion de conduite cylindrique (18). La paroi parabolique (14) de la première portion de chambre définit une ligne focale coïncidant avec l'axe de rotation. Les ouvertures d'entrée (15) sont arrangées dans la partie à section transversale large de la première portion de chambre, qui est reliée à la seconde portion de chambre à l'endroit où la section transversale de cette seconde portion est la plus large. La somme des sections transversales des ouvertures d'entrée (15) correspond en gros à la section transversale de la portion de conduite (18).
PCT/EP1990/000636 1989-04-21 1990-04-20 Emulsion liquide sans emulsifiant; procede et dispositif pour la preparer WO1990012639A1 (fr)

Priority Applications (3)

Application Number Priority Date Filing Date Title
DE69011679T DE69011679T2 (de) 1989-04-21 1990-04-20 Flüssigemulsion ohne emulgator und verfahren und vorrichtung zum verfertigen der emulsion.
SU905010224A RU2072891C1 (ru) 1989-04-21 1990-04-20 Жидкая эмульсия без применения эмульгатора, способ ее получения и устройство для его осуществления
EP90906170A EP0469014B1 (fr) 1989-04-21 1990-04-20 Emulsion liquide sans emulsifiant; procede et dispositif pour la preparer

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
DEG8905075.4U 1989-04-21
DE8905075U DE8905075U1 (de) 1989-04-21 1989-04-21 Mischvorrichtung für Strömungsmedien
JP10326889 1989-04-22
JP1/103268 1989-04-22

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WO1990012639A1 true WO1990012639A1 (fr) 1990-11-01

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EP (2) EP0469014B1 (fr)
AT (1) ATE110001T1 (fr)
AU (1) AU5422990A (fr)
CA (1) CA2051438A1 (fr)
DD (1) DD299620A5 (fr)
DE (1) DE69011679T2 (fr)
DK (1) DK0469014T3 (fr)
ES (1) ES2057555T3 (fr)
HU (1) HUT61909A (fr)
IL (1) IL94162A (fr)
PT (1) PT93846A (fr)
RU (1) RU2072891C1 (fr)
WO (1) WO1990012639A1 (fr)

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EP0263443A2 (fr) * 1986-10-08 1988-04-13 Zugol AG Procédé et dispositif pour produire une émulsion eau-en-huile
EP0312642A1 (fr) * 1987-10-23 1989-04-26 "Harrier" Gmbh Gesellschaft Für Den Vertrieb Medizinischer Und Technischer Geräte Procédé pour introduire du gaz dans de l'eau en quantité au-dessus de l'équilibre, appareil pour exécuter le procédé et eau obtenue à partir de ce procédé

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FR2461515A1 (fr) * 1979-07-24 1981-02-06 Robert Guerin Dispositif de traitement d'au moins deux fluides comprenant un liquide, notamment pour la realisation d'emulsion de deux liquides non solubles l'un dans l'autre
AU541324B2 (en) * 1979-08-01 1985-01-03 Exxon Research And Engineering Company Emulsifying immiscible liquids
EP0045008A2 (fr) * 1980-07-24 1982-02-03 Bayer Ag Procédé pour la préparation de dispersions pharmaceutiques et cosmétiques
GB2092025A (en) * 1981-01-30 1982-08-11 Ici Plc Spraying emulsions
WO1983001210A1 (fr) * 1981-09-29 1983-04-14 Patterson, William, P. Emulseur de grande puissance
EP0263443A2 (fr) * 1986-10-08 1988-04-13 Zugol AG Procédé et dispositif pour produire une émulsion eau-en-huile
EP0312642A1 (fr) * 1987-10-23 1989-04-26 "Harrier" Gmbh Gesellschaft Für Den Vertrieb Medizinischer Und Technischer Geräte Procédé pour introduire du gaz dans de l'eau en quantité au-dessus de l'équilibre, appareil pour exécuter le procédé et eau obtenue à partir de ce procédé

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RU2072891C1 (ru) 1997-02-10
IL94162A0 (en) 1991-01-31
IL94162A (en) 1995-08-31
DK0469014T3 (da) 1994-09-19
EP0469014A1 (fr) 1992-02-05
AU5422990A (en) 1990-11-16
ES2057555T3 (es) 1994-10-16
EP0393715A1 (fr) 1990-10-24
ATE110001T1 (de) 1994-09-15
HUT61909A (en) 1993-03-29
EP0469014B1 (fr) 1994-08-17
DE69011679T2 (de) 1995-02-16
DE69011679D1 (de) 1994-09-22
DD299620A5 (de) 1992-04-30
PT93846A (pt) 1990-11-20
CA2051438A1 (fr) 1990-10-22
HU903661D0 (en) 1991-12-30

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