Water-in-oil emulsions

Abstract

The invention concerns a process for producing a water-in-oil emulsion comprising mixing an oil dispersion of particles of a metallic oxide having a primary particle size less than 0.2 micron with one or more emulsifiers and an aqueous phase.The method enables the production of such emulsions containing relatively small quantities of emulsifiers and a novel emulsion made available by the invention contains less than 1% by weight of emulsifiers, 10 to 60% by weight of an oil phase and at least 40% by weight of an aqueous phase.The emulsions so formed are useful in preparing UV absorbing compositions such as sunscreens, skin protectants, moisturizers and after-sun lotions.

Description

This invention relates to water-in-oil emulsions and especially to water-in-oil emulsions containing metallic oxides having a small particle size.

Water-in-oil emulsions containing metallic oxides with a small particle size are known in which the amount of emulsifier present is, typically, 5 to 10% by weight of the emulsion.

It is an object of this invention to provide stable water-in-oil emulsions containing a smaller amount of emulsifier than has been possible hitherto. It is a further object of this invention to provide a convenient process for the production of stable water-in-oil emulsions containing small quantities of emulsifiers.

According to the invention a process for preparing a water-in-oil emulsion comprises mixing a dispersion in an oil of particles of a metallic oxide having an average primary particle size of less than 0.2 micron with one or more emulsifiers and an aqueous phase under conditions in which a water-in-oil emulsion is formed wherein the total amount of emulsifiers present in the water-in-oil emulsion so formed is less than 5 percent by weight, the particles of metallic oxide comprise from 0.5 percent to 30 percent by weight of the emulsion, an oil phase comprises from 10 percent to 60 percent by weight of the emulsion and the aqueous phase comprises at least 40 percent by weight of the emulsion.

Also according to the invention a water-in-oil emulsion comprises 0.5 percent to 30 percent by weight with respect to total weight of emulsion of particles of a metallic oxide having an average primary particle size of less than 0.2 micron, said emulsion containing one or more emulsifiers, said one or more emulsifiers being present in an amount of less than 1 percent by weight with respect to the total weight of emulsion, from 10 to 60 percent by weight with respect to total weight of emulsion of an oil phase and at least 40 percent by weight with respect to total weight of emulsion of an aqueous phase.

In preferred embodiments of the process and the product of the invention the metallic oxide comprises an oxide of titanium, zinc or iron.

The average primary particle size of the particles of metallic oxide used in the preparation of the water-in-oil emulsion according to the invention is less than 0.2 micron and where the particles are substantially spherical then this size will be taken to represent the diameter. However, the invention also encompasses particles of metallic oxides which are non-spherical and in such cases the average primary particle size refers to the largest dimension.

Preferably the average primary particle size of the particles is from 0.01 to 0.15 micron and more preferably from 0.01 to 0.06 micron when they are substantially spherical. Particularly useful products are obtained using substantially spherical particles having an average primary particle size between 0.01 and 0.03 micron. For particles having an acicular shape the average largest dimension of the primary particles is preferably less than 0.15 micron and more preferably from 0.02 to 0.10 micron.

When the metallic oxide is titanium dioxide the particles are preferably acicular in shape and have a ratio of largest dimension to shortest dimension of from 8:1 to 2:1.

When the metallic oxide is zinc oxide the particles preferably have an average primary particle size of 0.005 to 0.15 micron and more preferably have an average primary particle size of 0.03 to 0.07 micron.

The particles of metallic oxide may comprise substantially pure metallic oxide but may also carry an inorganic coating or organic coating. For example, particles of titanium dioxide can be coated with oxides of other elements such as oxides of aluminium, silicon or zirconium and a form of acicular, coated titanium dioxide which is especially useful in the products of this invention is disclosed in UK Patent GB 2 205 088.

The particles of metallic oxides may also carry, if desired, a coating of one or more organic materials such as polyols, amines, alkanolamines, polymeric organic silicon compounds, hydrophilic polymers such as polyacrylamide, polyacrylic acid, carboxymethyl cellulose and xanthan gum or surfactants.

Emulsifiers suitable for use in the process of the invention include silicone-based emulsifiers and lipid emulsifiers such as fatty alcohols, fatty acids, glyceryl esters, sorbitan esters, methylglycoside esters and sucrose esters. Many of these emulsifiers are easy to produce from renewable raw materials, are readily bio-degradable and do not contain toxic side products.

In carrying out the process of the invention a dispersion in oil of a metallic oxide having a primary particle size as hereinbefore defined is used. Typically, the dispersion is prepared by milling the metallic oxide in oil in the presence of a particulate grinding medium and in the presence of a dispersing agent.

UK Patent GB 2 206 339 discloses a dispersion in oil of titanium dioxide having an average particle size of from 0.01 to 0.15 micron containing an organic dispersing agent. The dispersions described in GB 2 206 339 are particularly suitable for use in the method of the current invention when it is desired to produce a water-in-oil emulsion containing titanium dioxide.

The technique described in GB 2 206 339 can be used to prepare dispersions in oil of metallic oxides other than titanium dioxide which are suitable for use in the method of the invention.

Suitable dispersing agents which can be used to prepare dispersions of metallic oxides include those disclosed in GB 2 206 339 such as dispersing agents having the formula X.CO.AR in which A is a divalent bridging group, R is a primary, secondary or tertiary amino group or a salt thereof with an acid or a quaternary ammonium salt group and X is the residue of a polyester chain which together with the --CO-- group is derived from a hydroxy carboxylic acid of the formula HOR.sup.1 COOH in which R.sup.1 represents a saturated or unsaturated hydrocarbyl group. Typical dispersing agents are based on ricinoleic acid, hydroxystearic acid and hydrogenated castor oil fatty acid.

Dispersing agents based on one or more polyesters or salts of a hydroxy carboxylic acid or a carboxylic acid free of hydroxy groups can also be used. Other suitable dispersing agents are those monoesters of fatty acid alkanolamides and carboxylic acids and their salts based on C.sub.6 -C.sub.22 saturated or unsaturated fatty acids. For example alkanolamides can be based on ethanolamine, propanolamine or aminoethyl ethanolamine. Alternative dispersing agents are those based on polymers or copolymers of acrylic or methacrylic acids, or dispersing agents having ethoxy groups in the constituent radicals such as those based on ethoxylated phosphate esters.

The total quantity of emulsifier used in the process of the current invention is less than 5% by weight of emulsion and preferably less than 1% and suitable emulsifiers are as hereinbefore described. The process of the invention provides a means of producing water-in-oil emulsions containing metal oxide particles using smaller quantities of emulsifiers than has been possible previously. A novel water-in-oil emulsion according to one aspect of the invention contains less than 1% emulsifiers in total.

The composition of the oil phase is chosen to suit the proposed use for the emulsion. For example, when the emulsion is intended for use as a sunscreen the oil phase will generally comprise paraffin oils, triglyceride esters, esters of fatty acids and fatty alcohols or silicone oils.

The water-in-oil emulsions are prepared according to the process of the current invention by mixing an aqueous phase with an oil phase under such conditions that a water-in-oil emulsion is formed.

Typically, the dispersion in oil of metallic oxide is mixed with the emulsifier and, when desired, any other oleophilic components to form the oil phase. This oil phase is subsequently mixed with an aqueous phase to form the water-in-oil emulsion. Alternatively, the dispersion of metallic oxide can be mixed with an emulsion which has previously been prepared by mixing an oil phase containing emulsifier with an aqueous phase.

The emulsions may be prepared at room temperature but it is preferred to use a temperature of at least 40.degree. C. and when components which are solid at room temperature are present it is usually necessary to heat one or both phases before mixing.

Other ingredients can be added to the emulsion depending upon the intended use. These ingredients may be mixed with the emulsion or added to the dispersion, the oil phase or the aqueous phase before these components are mixed together. As examples, perfumes, antioxidants, moisturisers and thickeners are normally added to emulsions which are intended for use as cosmetics.

The water-in-oil emulsions of this invention find use, for example, as sunscreens, as skin protectants, as moisturisers and as after-sun lotions and are particularly useful in preparing products which are transparent to visible light but absorbent to UV light.

The emulsions use smaller quantities of emulsifiers than known emulsions and the emulsifiers which are preferred are easily produced and readily bio-degradable.

The invention is illustrated by the following examples.

EXAMPLE 1

______________________________________ Parts by weight______________________________________1) Paraffin Oil 12.52) Dispersion of titanium dioxide in a 1:1 mixture 12.5 of mineral oil and capric/caprylic triglyceride (sold under the trade name Tioveil MOTG)3) Sorbitan monooleate (sold under the trade 0.9 name Span 80)4) Magnesium sulphate heptahydrate 0.65) Propylene glycol 5.06) Demineralised water to 100______________________________________

Ingredients 1 to 3 were mixed together and heated to 75.degree. C. to form an oil component which was placed in a thermostatted mixing vessel at 75.degree. C. Ingredients 4 to 6 were mixed together and heated to 75.degree. C. to form an aqueous component. The aqueous component was slowly added to the oil component with vigorous stirring (motor-driven paddle stirrer) to form an emulsion. The emulsion was cooled to room temperature over a period of approximately 15 minutes with continuous vigorous stirring. The resulting emulsion was stable for at least four days at 50.degree. C.

EXAMPLE 2

______________________________________ % by weight______________________________________Phase APEG-1 Glyceryl Sorbitan Isostearate 3.25(Trade Name Arlacel 582)PEG-40 Sorbitan Peroleate 0.75(Trade Name Arlatone T)Paraffin Oil 8.00Sunflower Oil 8.00Caprylic-capric triglyceride 4.00(Trade Name Miglyol 812N)Magnesium stearate 1.00Dispersion of titanium dioxide in a 1:1 10.00mixture of mineral oil and caprylic/caprictriglyceride (Trade Name TIOVEIL MOTG)Phase BGlycerol 4.00Magnesium Sulphate Heptahydrate 0.70Demineralised Water 59.785-Chloro-2-methyl-4-isothiazolin-3-one 0.02(and) 2-methyl-4-isothiazolin-3-one(Trade Name Kathon CG)Phase CFumed silicon dioxide (Trade Name 0.50Aerosil R972)______________________________________

Phases A and B were separately heated to 80.degree. C. Phase B was added to Phase A under intensive stirring using a paddle stirrer in a heated vessel. Phase C was added with intensive stirring, and the product was cooled down to 25.degree. C. with stirring at 300 rpm.

EXAMPLE 3

A suncream was prepared as a water-in-oil emulsion according to the following formulation.

______________________________________ % by weight______________________________________Phase ALaurylmethicone Copolyol (DC Q2-5200.sup.[5]) 0.833PEG-40 Sorbitan Peroleate 0.147(Trade Name Arlatone .sup.[1])Isohexadecane (Arlamol HD.sup.[1]) 6.00Sunflower Oil 6.00Caprylic-capric Triglyceride 3.00(Trade Name Miglyol 812N.sup.[4])Titanium Dioxide dispersion in Mineral Oiland Caprylic-capric Triglyceride 10.00(Tioveil MOTG .sup.[2])Phase BSodium Chloride 1.00Glycerin 4.00Allantoin 0.20D-Panthenol.sup.[3] 0.80Demineralised Water 68.02______________________________________ [1] ICI Specialty Chemicals, [2] Tioxide Specialties Limited, [3] Hoffmann La Roche, [4] Huls, [5] Dow Corning. Suppliers

Phases A and B were separately heated to 75.degree. C., Phase B was added to Phase A and the two phases were mixed by intensive stirring. The resultant mixture was cooled to 25.degree. C. over 45 minutes whilst the rapid stirring was maintained.

EXAMPLE 4

A suncream was prepared as a water-in-oil emulsion according to the following formulation.

______________________________________ % by weight______________________________________Phase ACetyl Dimethicone Copolyol (Abil EM 90.sup.[4]) 0.833PEG-40 Sorbitan Peroleate 0.147(Trade Name Arlatone .sup.[1]Hydrogenated Castor Oil (Castor Wax) 0.30Stearyl Alcohol 0.10Magnesium Stearate 0.20Mineral Oil 11.00Isopropyl Myristate 4.00Titanium Dioxide dispersion in Mineral Oil andCaprylic-Capric Triglyceride (Tioveil MOTG.sup.[2]) 10.00Phase BSodium Chloride 0.80Magnesium Sulphate Heptahydrate 0.20Glycerin 4.00Allantoin 0.20D-Panthenol.sup.[3] 0.80Demineralised Water 67.42______________________________________ [1] ICI Specialty Chemicals, [2] Tioxide Specialties Limited, [3] Hoffmann La Roche, [4] Th Goldschmidt AG. Suppliers

Phases A and B were separately heated to 75.degree. C. and Phase B was added to Phase A in a heated vessel. The two phases were mixed with a blade stirrer having a circulation speed of 3.115 m/s. After mixing the product was cooled to 25.degree. C. over 45 minutes while the stirring was maintained.

EXAMPLE 5

A sunlotion was prepared as a water-in-oil emulsion according to the following formulation.

______________________________________ % by weight______________________________________Phase ALaurylmethicone Copolyol (DC Q2-5200.sup.[5]) 0.833PEG-40 Sorbitan Peroleate 0.147(Trade Name Arlatone T.sup.[1])Sunflower Oil 14.00Mineral Oil 14.00Caprylic-Capric Triglyceride (Miglyol 812N.sup.[4]) 7.00Titanium Dioxide dispersion in Mineral Oil andCaprylic-Capric Triglyceride (Tioveil MOTG.sup.[2]) 10.00Phase BSodium Chloride 1.00Glycerol 4.00Allantoin 0.20D-Panthenol.sup.[3] 0.80Demineralised Water 48.02______________________________________ [1] ICI Specialty Chemicals, [2] Tioxide Specialties Limited, [3] Hoffmann La Roche, [4] Huls, [5] Dow Corning. Suppliers

Phases A and B were separately heated to 75.degree. C. and Phase B was added to Phase A in a heated vessel. The two phases were mixed with a blade stirrer having a circulation speed of 3.115 m/s. After mixing the product was cooled to 25.degree. C. over 45 minutes while the stirring was maintained.

EXAMPLE 6

A sunlotion was prepared as a water-in-oil emulsion according to the following formulation.

______________________________________ % by weight______________________________________Phase ALaurylmethicone Copolyol (DC Q2-5200.sup.[5]) 0.833PEG-40 Sorbitan Peroleate(Trade Name Arlatone T.sup.[1]) 0.147Sunflower Oil 12.80Mineral Oil 12.80Caprylic-Capric Triglyceride (Miglyol 812N.sup.[4]) 6.40Titanium Dioxide dispersion in Mineral Oil andCaprylic-Capric Triglyceride(Tioveil MOTG.sup.[2]) 10.00Isoamyl p-Methoxycinnamate (Neo HeliopanType E 1000.sup.[6]) 3.00Phase BSodium Chloride 1.00Glycerol 4.00Allantoin 0.20D-Panthenol.sup.[3] 0.80Demineralised Water 48.02______________________________________ [1] ICI Specialty Chemicals, [2] Tioxide Specialties Limited, [3] Hoffmann La Roche, [4] Huls, [5] Dow Corning, [6] Haarmann & Reimer.

Phases A and B were separately heated to 75.degree. C. and Phase B was added to Phase A in a heated vessel. The two phases were mixed with a blade stirrer having a circulation speed of 3.115 m/s. After mixing the product was cooled to 25.degree. C. over 45 minutes while the stirring was maintained.

Claims

1. A process for preparing a water-in-oil emulsion comprising the steps of:

forming a dispersion in an oil of particles of a metallic oxide having an average particle size of less than 0.2 micron, said mixing oxide is an oxide of an element selected from the group consisting of titanium, zinc and iron; and

b) mixing said dispersion with one or more emulsifiers and an aqueous phase to form the water-in-oil emulsion wherein the total amount of emulsifiers present in the emulsion is less than 5 percent by weight, the particles of metallic oxide comprise from 0.5 percent to 30 percent by weight of the emulsion, an oil phase comprises from 10 percent to 60 percent by weight of the emulsion and the aqueous phase comprises at least 40 percent by weight of the emulsion.

2. A process according to claim 1 in which the particles of metallic oxide are substantially spherical and have an average primary particle size of from 0.01 to 0.15 micron.

3. A process according to claim 2 in which the average primary particle size is from 0.01 to 0.06 micron.

4. A process according to claim 2 in which the average primary particle size is from 0.01 to 0.03 micron.

5. A process according to claim 1 in which the particles of metallic oxide are acicular and have an average largest dimension of the primary particles of less than 0.15 micron.

6. A process according to claim 5 in which the average largest dimension of the primary particles is from 0.02 to 0.10 micron.

7. A process according to claim 1 in which the metallic oxide is titanium dioxide, the particles are acicular in shape and have a ratio of largest dimension to shortest dimension of from 8:1 to 2:1.

8. A process according to claim 1 in which the metallic oxide is zinc oxide and the particles have an average primary particle size of from 0.005 to 0.15 micron.

9. A process according to claim 7 in which the average primary particle size is from 0.03 to 0.07 micron.

10. A process according to claim 1 in which the particles of metallic oxide carry an inorganic or an organic coating.

11. A process according to claim 10 in which the metallic oxide is titanium dioxide and the particles thereof are coated with an oxide of an element selected from the group consisting of aluminium, silicon and zirconium.

12. A process according to claim 11 in which the particles of metallic oxide carry a coating of an organic compound selected from the group consisting of polyols, amines, alkanolamines, polyacrylamide, polyacrylic acid, carboxymethyl cellulose and xanthan gum.

13. A process according to claim 1 in which at least one of the emulsifiers used is selected from the group consisting of silicone-based emulsifiers, fatty alcohols, fatty acids, glyceryl esters, sorbitan esters, methylglycoside esters and sucrose esters.

14. A process according to claim 1 in which the dispersion of metallic oxide is prepared by milling the metallic oxide in oil in the presence of a particulate grinding medium and in the presence of a dispersing agent.

15. A process according to claim 14 in which the metallic oxide is titanium dioxide and the particles have an average particle size of from 0.01 to 0.15 micron.

16. A process according to claim 14 in which the dispersing agent has the formula X.CO.AR in which A is a divalent bridging group, R is selected from the group consisting of primary, secondary and tertiary amino groups, salts of primary, secondary and tertiary amino groups with an acid and quaternary ammonium salt groups and X is the residue of a polyester chain which together with the --CO-- group is derived from a hydroxy carboxylic acid of the formula HOR'COOH in which R' represents a saturated or unsaturated hydrocarbyl group.

17. A process according to claim 16 in which the dispersing agent is based on an acid selected from the group consisting of ricinoleic acid, hydroxystearic acid and hydrogenated castor oil fatty acid.

18. A process according to claim 14 in which the dispersing agent is based on a derivative of an acid selected from the group consisting of polyesters and salts of acids selected from the group consisting of hydroxy carboxylic acids and carboxylic acids free of hydroxy groups.

19. A process according to claim 14 in which the dispersing agent is selected from the group consisting of monoesters of fatty acid alkanolamides and carboxylic acids and salts thereof based on C.sub.6 to C.sub.22 saturated or unsaturated fatty acids.

20. A process according to claim 14 in which the dispersing agent is a polymer or copolymer of an acid selected from the group consisting of acrylic acids and methacrylic acids.

21. A process according to claim 14 in which the dispersing agent is an ethoxylated phosphate ester.

22. A process according to claim 1 in which the total amount of emulsifier used is less than 1 percent by weight of the emulsion.

23. A process according to claim 1 in which the oil phase comprises an oil selected rom the group consisting of paraffin oils, triglyceride esters, esters of fatty acids and fatty alcohols and silicone oils.

24. A process according to claim 1 in which the dispersion of metallic oxide particles is mixed with the emulsifier or emulsifiers and any other oleophilic components of the emulsion to form an oil phase and said oil phase is subsequently mixed with an aqueous phase to form a water-in-oil emulsion.

25. A process according to claim 24 in which at least one of the oil phase and the aqueous phase is heated to at least 40.degree. C. before the oil phase and the aqueous phase are mixed.