Patent Application
20200246245
The present invention relates to a composition, an emulsifier system comprising the composition, a personal care product comprising the emulsifier system, a method of emulsifying using the composition and use of the composition as an emulsifier. In particular, the invention relates to a composition an emulsifier system operable to emulsify formulations stably under extreme conditions, for example formulations with a high salt content or a low or high pH, or formulations requiring stability in extreme circumstances such as those subjected to high temperatures for sustained periods of time.
Alkoxylated esters have been used for many years as surface active agents (or surfactants), having emulsifying, dispersing, wetting and/or solubilising properties in a wide range of applications such as personal care, home care, industrial, food, and many others. In particular, alkoxylated esters have been used as emulsifiers in personal care applications, for example skin care, sunscreens, toiletries, decorative cosmetics, perfumes and fragrances.
Current commercially available alkoxylated esters are effective emulsifiers in many applications, but there is still a requirement to improve the properties of emulsifiers, particularly in personal care applications. These properties may include the flexibility of use of the emulsifier in different systems and the ability to emulsify in strenuous conditions such as a high internal phase content, a high or low pH or long term storage at an elevated temperature. An example of a further desirable property of an emulsifier would be if the emulsifier could be used in a particular system without the need for a co-emulsifier.
It is an object of the present invention to address at least one of the above or other disadvantages associated with the prior art.
According to a first aspect of the present invention, there is provided a composition comprising:
R1(OC2H4)n(OC3H6)m (A)
wherein R1 is a C16-C26 alkyl or alkenyl group,
n is the mean number of moles of —(OC2H4)— per molecule of formula (A) present in the compound and is between 15 and 100,
m is the mean number of moles of —(OC3H6)— per molecule of formula (A) present in the compound and is between 0 and 20,
and n+m>15 ; and
R2(OC2H4)r(OC3H6)s (B)
wherein R2 is a C16-C26 alkyl or alkenyl group,
r is the mean number of moles of —(OC2H4)— per molecule of formula (B) present in the compound and is between 0.01 and 14.99,
s is the mean number of moles of —(OC3H6)— per molecule of formula (B) present in the compound and is between 0.01 and 14.99, and
r+s≤15.
According to a second aspect of the present invention, there is provided an emulsifier system comprising a composition according to the first aspect.
According to a third aspect of the present invention, there is provided a personal care formulation comprising a composition according to the first aspect or an emulsifier system according to the second aspect.
According to a fourth aspect of the present invention, there is provided a method of stabilising an emulsion comprising the step of mixing a composition according to the first aspect or an emulsifier system according to the second aspect with the emulsion.
According to a fifth aspect of the present invention, there is provided the use of a composition according to the first aspect, or an emulsifier system according to the second aspect to stabilise an emulsion.
All of the features described herein may be combined with any of the above aspects, in any combination.
The present invention is based in part on the recognition by the inventors that a composition of the first aspect of the invention has advantageous properties due to its particular combination of components.
At room temperature, formulations comprising high concentrations of salts or having low or high pHs will be under significant stress. Traditional emulsifiers, being non-ionic, will have a reduced cloud point due to the salt concentration of the formulation, hence reducing the HLB of the emulsifiers and the overall system making them more oil soluble. This leads traditional emulsifiers to sit further in the oil phase of an emulsion, and less at the interface. When the temperature of the formulation is increased to 60° C., it is further stressed and the cloud point and HLB will be further reduced, thus pushing the emulsifiers further into the oil phase and far enough away from the interface to cause instability to be seen. Furthermore, where traditional emulsifiers are only EO based, the EO chain can curl up and start to bond with itself in preference to the water phase, thus leading to further instability.
Without being bound by theory, the composition and/or emulsifier system of the present invention provides a starting material that has a higher cloud point. Increasing the temperature and also having salt in the formulation will reduce the cloud point and HLB but, with the aid of the composition and/or emulsifier system according to the invention, not to the same degree as formulations using emulsifier systems according to the prior art. This gives the products according to the present invention a distinct advantage. Having a combination of fatty alcohols with different length alkoxylated chains, particularly the fatty alcohol with the longer alkoxylated chain, in the composition/emulsifier system also adds further stability since it provides a composition/emulsifier system with a good amount of hydrophilic and lipophilic stabilisation. The inclusion of PO at the end of the EO chain will help to prevent the EO chain curling thus helping to stabilise the system further. In addition, PO likes to sit in the oil phase of an emulsion, but also can have a tendency to sit in the water phase. Therefore pushing of the emulsifier into different emulsion phases would not affect the system as much compared to an EO only system.
It will be understood that any upper or lower quantity or range limit used herein may be independently combined.
It will be understood that, when describing the number of carbon atoms in a substituent group (e.g. ‘C1 to C6’), the number refers to the total number of carbon atoms present in the substituent group, including any present in any branched groups. Additionally, when describing the number of carbon atoms in, for example fatty acids, this refers to the total number of carbon atoms including the one at the carboxylic acid, and any present in any branch groups.
Many of the chemicals which may be used to produce the composition of the present invention are obtained from natural sources. Such chemicals typically include a mixture of chemical species due to their natural origin. Due to the presence of such mixtures, various parameters defined herein can be an average value and may be non-integral.
The term ‘residue’ as used herein is the part of a reactant molecule which remains in the reaction product compound after a reaction has occurred.
The term ‘alkyl’ is well known in the art and, when used herein, means a saturated C16 to C26, preferably C16 to C24, more preferably C18 to C24 group, and includes cetyl, stearyl, arachidyl, behenyl, lignceryl and cerotinyl groups. Unless otherwise specified, alkyl groups may be linear or branched (particularly preferred branched groups include methyl, ethyl, propyl, butyl, t-butyl and isopropyl), be cyclic, acyclic or part cyclic/acyclic, and/or be unsubstituted, substituted, terminated or interrupted by one or more substituents selected from halogen-, nitrogen- and/or oxygen-containing groups.
The term ‘alkenyl’ is also well known in the art and, when used herein, means an unsaturated C16 to C26, preferably C16 to C24, more preferably C18 to C24 group, and includes oleyl groups. Unless otherwise specified, alkenyl groups may be linear or branched (particularly preferred branched groups include methyl, ethyl, propyl, butyl, t-butyl and isopropyl), be cyclic, acyclic or part cyclic/acyclic, and/or be unsubstituted, substituted, terminated or interrupted by one or more substituents selected from halogen-, nitrogen- and/or oxygen-containing groups.
The term ‘fatty alcohol’ as used herein means long-chain primary alcohols, preferably with a chain length of 16 to 26 carbon atoms, which may be derived from natural sources such as fats and oils. Preferably, the fatty alcohols used to produce the alkoxylated fatty alcohols of the present invention are derived from vegetable sources, although it is also possible to derive the alcohols from animal sources or petrochemical sources. The alcohols used in the present invention will normally be obtained from naturally occurring esters by hydrogenation.
The fatty alcohol used in the present invention may be a mixture of alcohols of different chain lengths. In this case, the mixture may be a commercially available mixture, or may be made from a combination of different chain length alcohols.
The alcohol used in the present invention may be selected from the group comprising cetyl alcohol, cetostearyl alcohol, palmitoleyl alcohol, stearyl alcohol, isostearyl alcohol, oleyl alcohol, arachidyl alcohol, behenyl alcohol, isobehenyl alcohol, erucyl alcohol, lignceryl alcohol and cerotinyl alcohol. Preferably, the alcohol used in the present invention is selected from cetyl alcohol, cetostearyl alcohol, stearyl alcohol, isostearyl alcohol, arachidyl alcohol, behenyl alcohol, isobehenyl alcohol, lignceryl alcohol and cerotinyl alcohol. More preferably, the alcohol used in the present invention is selected from stearyl alcohol, isostearyl alcohol, behenyl alcohol and isobehenyl alcohol, most preferably from stearyl alcohol and behenyl alcohol, desirably behenyl alcohol.
Preferably, R1 is the residue of a fatty alcohol, or mixture of fatty alcohols, as defined above.
Preferably, R2 is the residue of a fatty alcohol, or mixture of fatty alcohols, as defined above.
The alkylene oxides used in the present invention are preferably ethylene oxide and propylene oxide. These oxides are readily available to the skilled person and can be derived from petrochemical sources (eg by the oxidation of ethylene or propylene obtained from hydrocarbon cracking) or from natural sources (eg by the oxidation of ethylene obtained from bioethanol from biomass).
Preferably, —(OC2H4)— is the residue of ethylene oxide as defined above.
Preferably, —(OC3H6)— is the residue of propylene oxide as defined above.
In the alkoxylated fatty alcohol compound of formula (A), preferably, R1 is a C16-C26 alkyl or alkenyl group, preferably a C16-C24 alkyl or alkenyl group, preferably a C18-C24 alkyl or alkenyl group, more preferably a C18-C22 alkyl or alkenyl group, most preferably a C22 alkyl or alkenyl group.
Preferably, R1 is an alkyl group. R1 may be branched or linear, preferably linear. R1 may be cyclic or acyclic, preferably acyclic. R1 may be present as a mixture of alkyl or alkenyl groups.
Preferably, n is the mean number of moles of —(OC2H4)— per molecule of formula (A) present in the compound and is between 15 and 100, preferably between 15 and 60, more preferably between 15 and 50, more preferably between 22 and 40, most preferably between 24 and 34.
Preferably m is the mean number of moles of —(OC3H6)— per molecule of formula (A) present in the compound and is between 0 and 20, preferably between 0 and 10, more preferably between 0 and 5. Most preferably, m is 0.
Preferably, n+m is the mean total number of moles of —(OC2H4)— and —(OC3H6)— per molecule of formula (A) present in the compound and is greater than 15, preferably greater than 22 and most preferably greater than 25. When m=0, n+m=n.
Preferably, the compound of formula (A) has the formula (A′)
R1(OC2H4)n (A′)
In the alkoxylated fatty alcohol compound of formula (B), preferably, R2 is a C16-C26 alkyl or alkenyl group, preferably a C16-C24 alkyl or alkenyl group, preferably a C18-C24 alkyl or alkenyl group, more preferably a C18-C22 alkyl or alkenyl group, most preferably a C22 alkyl or alkenyl group.
Preferably, R2 is an alkyl group. R2 may be branched or linear, preferably linear. R2 may be cyclic or acyclic, preferably acyclic. R2 may be present as a mixture of alkyl or alkenyl groups.
Preferably, R2 is the same as R1. Alternatively, R2 may be different to R1.
Preferably, r is the mean number of moles of —(OC2H4)— per molecule of formula (B) present in the compound and is between 0.01 and 14.99, preferably between 0.1 and 10, more preferably between 0.5 and 5, and most preferably between 1 and 4.
Preferably, s is the mean number of moles of —(OC3H6)— per molecule of formula (B) present in the compound and is between 0.01 and 14.99, preferably between 0.05 and 10, more preferably between 0.05 and 5, more preferably between 0.1 and 1, most preferably between 0.1 and 0.6.
Preferably r+s is the mean total number of moles of —(OC2H4)— and —(OC3H6)— per molecule of formula (B) present in the compound and is less than 15, preferably less than 10 and most preferably less than 6.
The compound of formula (B) may be a mixture of two or more components. Preferably, the compound of formula (B) may be a mixture of components (B′) and (B″) having the formulas:
R2(OC2H4)r (B′) and
R2(OC2H4)r(OC3H6)t (B″), respectively,
wherein R2 and r are as described above and t is the mean number of moles of —(OC3H6)— per molecule of formula (B″) present in the compound and is between 0.01 and 14.99, preferably between 0.05 and 10, more preferably between 0.1 and 5, most preferably between 0.5 and 3.
When present as a mixture of components (B′) and (B″), the compound of formula (B) preferably has a mean number of moles of propylene oxide per molecule (ie the mean of the total ethoxylated alcohol and ethoxy- and propoxylated alcohol components) which is equal to s.
The composition of the present invention optionally further comprises an alkoxylated fatty alcohol compound of formula (C)
R3(OC2H4)x(OC3H6)y (C)
wherein R3 is a C16-C26 alkyl or alkenyl group,
x is the mean number of moles of —(OC2H4)— per molecule of formula (C) present in the compound and is between 0.01 and 14.99,
y is the mean number of moles of —(OC3H6)— per molecule of formula (C) present in the compound and is between 0.01 and 14.99, and
x+y≤≠r+s.
In the alkoxylated fatty alcohol compound of formula (C), preferably, R3 is a C16-C26 alkyl or alkenyl group, preferably a C16-C24 alkyl or alkenyl group, preferably a C18-C24 alkyl or alkenyl group, more preferably a C18-C22 alkyl or alkenyl group, most preferably a C22 alkyl or alkenyl group.
Preferably, R3 is an alkyl group. R3 may be branched or linear, preferably linear. R3 may be cyclic or acyclic, preferably acyclic. R3 may be present as a mixture of alkyl or alkenyl groups.
Preferably, R3 is the residue of a fatty alcohol, or mixture of fatty alcohols, as defined above.
Preferably, R3 is the same as R2. Alternatively, R3 may be different to R2.
Preferably, R3 is the same as R1. Alternatively, R3 may be different to R1.
Preferably, x is the mean number of moles of —(OC2H4)— per molecule of formula (C) present in the compound and is between 0.01 and 14.99, preferably between 0.1 and 10, more preferably between 0.5 and 5, and most preferably between 1 and 4. Preferably, x is different to r.
Preferably, y is the mean number of moles of —(OC3H6)— per molecule of formula (C) present in the compound and is between 0.01 and 14.99, preferably between 0.05 and 10, more preferably between 0.05 and 5, more preferably between 0.1 and 1, most preferably between 0.1 and 0.6. y may be the same as or different to s.
Preferably x+y is mean total number of moles of —(OC2H4)— and —(OC3H6)— per molecule of formula (B) present in the compound and is less than 15, preferably less than 10 and most preferably less than 6. Preferably, x+y is different to r+s.
The compound of formula (C) may be a mixture of two or more components. Preferably, the compound of formula (C) may be a mixture of components (C′) and (C″) having the formulas:
R3(OC2H4)x (C′) and
R3(OC2H4)x(OC3H6)z (C″), respectively, and
wherein R3 and x are as described above and z is the mean number of moles of —(OC3H6)— per molecule of formula (C″) present in the compound and is between 0.01 and 14.99, preferably between 0.05 and 10, more preferably between 0.1 and 5, most preferably between 0.5 and 3. z may be the same as or different to t.
When present as a mixture of components (C′) and (C″), the compound of formula (C) preferably has a mean number of moles of propylene oxide per molecule (ie the mean of the total ethoxylated alcohol and ethoxy- and propoxylated alcohol components) which is equal to y.
Alkoxylated fatty alcohols are known in the art. As such, their production would be well known to the skilled person.
The alkoxylated fatty alcohols of the invention may be produced in a conventional alkoxylation reaction, for example by reacting a fatty alcohol with ethylene oxide and, where applicable, propylene oxide. The reaction may occur in one stage, i.e. where all of the reactants are mixed together and reacted, or in two stages, e.g. where the fatty alcohol is mixed with the ethylene oxide and reacted together, followed by subsequent addition and reaction of the propylene oxide where required. Preferably the reaction occurs in two stages.
The composition comprises:
In one embodiment, the composition consists essentially of:
Preferably, the composition is an emulsifier system.
The ratios of components may advantageously influence the properties of the composition.
Preferably, the molar amount of component b) in the composition is equal to or greater than the molar amount of component a).
Preferably the molar amount of b) in the composition is equal to or greater than the molar amount of c), when present.
The mean number of moles of component b) to component a) is suitably in the range from 0.1 to 8:1, preferably 0.5 to 6:1, more preferably 1 to 5:1, particularly 2 to 4:1, and especially 2.8 to 3.5:1.
The mean number of moles of component b) to component c), where present, is suitably in the range from 0.1 to 10:1, preferably 0.5 to 8:1, more preferably 1 to 6:1, particularly 2 to 5:1, and especially 3.5 to 4.5:1.
The mean number of moles of component a) to component c), where present, is suitably in the range from 0.1 to 5:1, preferably 0.4 to 3:1, more preferably 0.6 to 2.5:1, particularly 0.8 to 2:1, and especially 0.9 to 1.5:1.
Preferably, the composition is anhydrous. By the use of the term anhydrous herein, it is meant that the blend preferably comprises a maximum of 10% by weight water. More preferably, the blend comprises a maximum of 7% by weight water, most preferably, 5% and desirably 2% by weight. Preferably, the blend comprises 0.01% to 10% by weight water, preferably 0.05% to 5%, most preferably 0.1% to 2% by weight.
The composition of the invention may be used to stabilise an emulsion. The composition may be an emulsifier system.
The composition of the invention may have the properties of a surfactant, emulsifier, dispersant, stabiliser, solubiliser, pigment wetter and/or rheology modifier. The invention also includes the use of the composition as a surfactant, emulsifier, dispersant, stabilizer, solubiliser, pigment wetter and/or rheology modifier, preferably as a surfactant and/or emulsifier, more preferably as an emulsifier.
The composition may have an acid value (measured as described herein) in the range from 0 to 15, preferably 0 to 10, more preferably 0 to 5, particularly 0 to 2, and especially 0 to 1 mgKOH/g.
The composition may have a hydroxyl (OH) value (measured as described herein) in the range from 50 to 300, preferably 70 to 220, more preferably 80 to 190, particularly 90 to 175, and especially 100 to 165 mgKOH/g.
The composition of the invention is suitable for use in forming emulsions (and dispersions), i.e. as the, or as part of the, emulsifier system. The emulsion may be a water in oil emulsion, oil in polyol (e.g. glycerol) emulsion or oil in water emulsion. The emulsion may be a multiple emulsion, for example a water in oil in water emulsion.
The emulsifier system may be added into the water phase or the oil phase of an emulsion. Alternatively, the components of the emulsifier system may be added into different phases of the emulsion, for example, component a) may be added into the water phase whilst component b), and component c) when present, are added into the oil phase, or vice versa, component a) may be added into the oil phase whilst component b), and component c) when present, are added into the water phase.
The emulsion is preferably for use in a personal care formulation, more preferably a skin care product for example a sunscreen, cosmetic, antiperspirant, depilatory or dermatological product, or a hair care product for example a shampoo, conditioner, hair dye or hair relaxer product.
The composition of the invention is particularly suitable for the preparation of water-in-oil emulsions which contain a high concentration of salts, have a high or low pH, or require stability at elevated temperatures.
The composition of the invention may be a high performance water in oil emulsifier. It may be used at a lower wt % inclusion level than a comparative emulsifier to provide an equivalent level of emulsion stability.
The oil phase of the emulsion preferably comprises an emollient oil of the type used in a personal care formulation. The emollient is preferably an oily material which is liquid at ambient temperature (i.e. about 23° C.). Alternatively it can be solid at ambient temperature, in which case in bulk it will usually be a waxy solid, provided it is liquid at an elevated temperature at which it can be included in and emulsified in the composition. The manufacture of the formulation preferably uses temperatures up to 100° C., more preferably about 80° C., and therefore such solid emollients will preferably have melting temperatures of less than 100° C., and more preferably less than 70° C. The emulsifier may be used cold process or using a semi-hot process if required.
The oil phase of the emulsion may comprise at least one ester oil, vegetable oil, alcohol, paraffin oil or silicone.
Suitable oil phase components include non-polar oils, for example mineral or paraffin, especially isoparaffin, oils, such as that sold by Croda as Arlamol (trade mark) HD; or medium polarity oils, for example vegetable ester oils such as jojoba oil, vegetable glyceride oils, animal glyceride oils, such as that sold by Croda as Crodamol (trade mark) GTCC (caprylic/capric triglyceride), synthetic oils, for example synthetic ester oils, such as isopropyl palmitate and those sold by Croda as Crodamol IPP and Arlamol DOA, ether oils, particularly of two fatty e.g. C8 to C18 alkyl residues, such as that sold by Cognis as Cetiol OE (dicaprylether), guerbet alcohols such as that sold by Cognis as Eutanol G (octyl dodecanol), or silicone oils, such as dimethicone oil such as those sold by Dow Corning as Xiameter PMX-200, cyclomethicone oil, or silicones having polyoxyalkylene side chains to improve their hydrophilicity; or highly polar oils including alkoxylate emollients for example fatty alcohol propoxylates such as that sold by Croda as Arlamol PS15E (propoxylated stearyl alcohol). Suitable emollient materials that can be solid at ambient temperature but liquid at temperatures typically used to make the formulations of this invention include jojoba wax, tallow and coconut wax/oil. When non-polar oils are used it may be desirable to use relatively high concentrations of the composition according to the present invention, in order to achieve suitably satisfactory emulsification, particularly to obtain small oil droplets.
Mixtures of emollients can and often will be used, and in some cases solid emollients may dissolve wholly or partly in liquid emollients or in combination the freezing point of the mixture is suitably low. Where the emollient composition is a solid (such as fatty alcohols) at ambient temperature, the resulting dispersion may technically not be an emulsion (although in most cases the precise phase of the oily disperse phase cannot readily be determined) but such dispersions behave as if they were true emulsions and the term emulsion is used herein to include such compositions.
The concentration of the oil phase may vary widely. The amount of oil in the emulsion is suitably in the range from 1 to 90%, preferably 3 to 60%, more preferably 5 to 40%, particularly 8 to 20%, and especially 10 to 15% by weight of the total formulation.
The amount of water (or polyol, e.g. glycerin) present in the emulsion is suitably greater than 5%, preferably in the range from 30 to 90%, more preferably 50 to 90%, particularly 70 to 85%, and especially 75 to 80% by weight of the total formulation.
The amount of the composition or emulsifier system of the invention in an emulsion or personal care formulation according to the present invention may be at least 0.1%, preferably at least 0.5%, more preferably at least 1%, particularly preferably at least 1.5%, and especially preferably at least 2%, by weight of the total formulation.
The amount of the composition or emulsifier system of the invention in an emulsion or personal care formulation according to the present invention may be at most 10%, preferably at most 8%, more preferably at most 7%, particularly preferably at most 6%, and especially preferably at most 5.5%, by weight of the total formulation.
The amount of the composition or emulsifier system of the invention in an emulsion or personal care formulation according to the present invention is suitably in the range from 0.1 to 10%, preferably 0.5 to 8%, more preferably 1 to 7%, particularly 1.5 to 6%, and especially 2 to 5.5%, by weight of the total formulation.
The emulsions according to the present invention may also contain other additional surfactant materials which form part of the emulsifier system. Other suitable surfactants include relatively hydrophilic surfactants, e.g. having a HLB value of greater than 10, preferably greater than 12, and relatively hydrophobic surfactants e.g. having a HLB value of less than 10, preferably less than 8. Relatively hydrophilic surfactants include alkoxylate surfactants with an average in the range from about 10 to about 100 alkylene oxide, particularly ethylene oxide residues; and relatively hydrophobic surfactants include alkoxylate surfactants preferably with an average in the range from about 3 to about 10 alkylene oxide, particularly ethylene oxide residues.
Personal care formulations according to the invention can be divided by viscosity into milks and lotions, which preferably have a low shear viscosity (measured at shear rates of about 0.1 to 10 s−1 as is typically used in Brookfield viscometers) of up to 10,000 mPa.s, and creams which preferably have a low shear viscosity of more than 10,000 mPa.s. Milks and lotions preferably have a low shear viscosity in the range from 100 to 10,000, more preferably 200 to 5,000, and particularly 300 to 1,000 mPa.s. The amount of composition according to the present invention present in a milk or lotion is preferably in the range from 2 to 3.5% by weight of the total formulation.
Creams preferably have a low shear viscosity of at least 20,000, more preferably in the range from 30,000 to 80,000, and particularly 40,000 to 70,000 mPa.s, although even higher viscosities e.g. up to about 106 mPa.s, may also be used. The amount of composition according to the present invention in a cream is preferably in the range from 2 to 3.5% by weight of the total formulation.
The emulsions of the invention may be made by generally conventional emulsification and mixing methods. For example, the composition of the invention may be added to (i) the oil phase, after which the aqueous phase is then added to the oil phase, or (ii) both the combined oil and water phases, or (iii) the water phase, which is then added to the oil phase. Method (i) is preferred. In all of these methods, the resulting mixture can then be emulsified using standard techniques. It is preferred to either heat the aqueous and oil phases usually above about 60° C., e.g. to about 80 to 85° C., or to subject the aqueous phase to high intensity mixing at lower, e.g. about ambient, temperature (cold process). Vigorous mixing and the use of moderately elevated temperatures can be combined if desired. The heating and/or high intensity mixing can be carried out before, during or after addition of the water to the oil phase.
The emulsions can also be made by inverse emulsification methods, whereby the composition of the invention is added to either the oil phase or the aqueous phase, and the aqueous phase is mixed into the oil phase to initially form a water in oil emulsion. Aqueous phase addition is continued until the system inverts to form an oil in water emulsion. Plainly a substantial amount of aqueous phase will generally be needed to effect inversion and so this method is not likely to be used for high oil phase content emulsions. Vigorous mixing and the use of moderately elevated temperatures can be combined if desired. Heating can be carried out during or after addition of the aqueous phase and before, during or after inversion. High intensity mixing can be carried out during or after addition of the aqueous phase, and before or during inversion
The emulsions may for example be microemulsions or nanoemulsions, having a mean droplet size over a wide range, preferably in the range from 10 to 10,000 nm. In one embodiment, the emulsion droplet size may be reduced, for example by high pressure homogenisation, preferably to a value in the range from 100 to 1,000 nm, more preferably 300 to 600 nm.
The emulsions according to the present invention are stable, measured as described herein, preferably for longer than one month, more preferably longer than two months, particularly longer than three months, and especially longer than four months at ambient temperature, and also preferably at 40° C. The stability at even higher temperatures can be particularly important, and therefore the emulsion is stable, measured as described herein, suitably for longer than one week, preferably longer than two weeks, more preferably longer than 3 weeks, particularly longer than one month, and especially longer than two months at 50° C., and also preferably at 60° C.
The composition of the invention is preferably for use in a personal care formulation, more preferably a skin care product for example a sunscreen, cosmetic, antiperspirant, depilatory or dermatological product, or a hair care product for example a shampoo, conditioner, hair dye or hair relaxer product. In particular, the personal care formulation may be a formulation containing a high concentration of salts such as an antiperspirant deodorant, or a formulation having a low or high pH such as a depilatory or hair relaxer.
Many other components may be included in the formulation to make a personal care or cosmetic formulation or product. These components can be oil soluble, water soluble or non-soluble. Examples of such materials include:
The composition and emulsions according to the present invention are suitable for use in a wide range of formulations and end-use applications, such as moisturizers, sunscreens, after sun products, body butters, gel creams, high perfume containing products, perfume creams, baby care products, hair treatments, hair conditioners, skin toning and skin whitening products, water-free products, anti-perspirant and deodorant products, tanning products, cleansers, 2-in-1 foaming emulsions, multiple emulsions, preservative free products, mild formulations, scrub formulations e.g. containing solid beads, silicone in water formulations, pigment containing products, sprayable emulsions, cosmetics, colour cosmetics, conditioners, shower products, foaming emulsions, make-up remover, eye make-up remover, and wipes.
The formulation may be a spray, lotion, cream or ointment. When the formulation is a colour cosmetic, it may be a foundation, mascara, eyeshadow or lipstick. The formulation may be an anti-perspirant or deodorant.
Formulations containing a composition or emulsion according to the present invention may have a pH value over a wide range, preferably in the range from 2 to 14, more preferably 2 to 8 or 6 to 13, and especially 2 to 5 or 8 to 13.
The invention is illustrated by the following non-limiting examples. All parts and percentages are given by weight unless otherwise stated.
It will be understood that all tests and physical properties listed have been determined at atmospheric pressure and ambient temperature (i.e. about 23° C.), unless otherwise stated herein, or unless otherwise stated in the referenced test methods and procedures.
In this specification the following test methods have been used:
The following synthesis methods are for making behenyl alcohol alkoxylates. The methods utilise a clean dry 10 litre pressure vessel equipped with agitation, a nitrogen sparge, thermometer, pressure gauge, and vacuum capability.
Molten behenyl alcohol (1500 g, 4.65 mol) and 45% potassium hydroxide (11 g, 0.09 mol dry) were charged to the vessel, which was then purged with nitrogen and heated to 90° C. with stirring. Vacuum was applied for one hour to dry the batch. The pressure was adjusted with nitrogen and ethylene oxide (304 g, 6.9 mol) was charged and reacted at 150° C. for 2 hours. The batch was cooled to 120° C. and propylene oxide (83 g, 1.4 mol) was charged and reacted at 120° C. for 2 hours. The batch was then nitrogen stripped at 110° C. for 1.5 hours, before cooling to 80° C., neutralising with lactic acid (˜2 g) to a pH of 5.5-7.5 and discharging. The resultant product had hydroxyl value 145 mgKOH/g, with 1H NMR indicating a composition of behenyl alcohol+1.2 moles EO+0.3 moles PO.
Molten behenyl alcohol (1500 g, 4.65 mol) and 45% potassium hydroxide (11 g, 0.09 mol dry) were charged to the vessel, which was then purged with nitrogen and heated to 90° C. with stirring. Vacuum was applied for one hour to dry the batch. The pressure was adjusted with nitrogen and ethylene oxide (304 g, 6.9 mol) was charged and reacted at 150° C. for 2 hours. The batch was cooled to 120° C. and propylene oxide (83 g, 1.4 mol) was charged and reacted at 120° C. for 2 hours. The batch was then nitrogen stripped at 110° C. for 1.5 hours, before cooling to 80° C., neutralising with lactic acid (˜2 g) to a pH of 5.5-7.5 and discharging. The resultant product had hydroxyl value 143 mgKOH/g, with 1H NMR indicating a composition of behenyl alcohol +1.4 moles EO +0.2 moles PO.
Molten behenyl alcohol (985 g, 3.05 mol) and 45% potassium hydroxide (5 g, 0.04 mol dry) were charged to the vessel, which was then purged with nitrogen and heated to 90° C. with stirring. Vacuum was applied for one hour to dry the batch. The pressure was adjusted with nitrogen and ethylene oxide (180 g, 4.1 mol) was charged and reacted at 150° C. for 2 hours. The batch was cooled to 120° C. and propylene oxide (90 g, 1.55 mol) was charged and reacted at 120° C. for 2 hours. The batch was then nitrogen stripped at 110° C. for 1.5 hours, before cooling to 80° C., neutralising with lactic acid (˜2 g) to a pH of 5.5-7.5 and discharging. The resultant product had hydroxyl value 140 mgKOH/g, with 1H NMR indicating a composition of behenyl alcohol+1.3 moles EO+0.45 moles PO.
Molten behenyl alcohol (1250 g, 3.9 mol) and 45% potassium hydroxide (9 g, 0.072 mol dry) were charged to the vessel, which was then purged with nitrogen and heated to 90° C. with stirring. Vacuum was applied for one hour to dry the batch. The pressure was adjusted with nitrogen and ethylene oxide (710 g, 16.1 mol) was charged and reacted at 150° C. for 2 hours. The batch was cooled to 120° C. and propylene oxide (69 g, 1.4 mol) was charged and reacted at 120° C. for 2 hours. The batch was then nitrogen stripped at 110° C. for 1.5 hours, before cooling to 80° C., neutralising with lactic acid (-4 g) to a pH of 5.5-7.5 and discharging. The resultant product had hydroxyl value 114 mgKOH/g, with 1H NMR indicating a composition of behenyl alcohol+3.6 moles EO+0.3 moles PO.
Molten behenyl alcohol (1000 g, 3.1 mol) and 45% potassium hydroxide (11 g, 0.09 mol dry) were charged to the vessel, which was then purged with nitrogen and heated to 90° C. with stirring. Vacuum was applied for one hour to dry the batch. The pressure was adjusted with nitrogen and ethylene oxide (4100 g, 93 mol) was charged and reacted at 150° C. for 2 hours. The batch was then cooled to 80° C., neutralised with lactic acid (˜2 g) to a pH of 5.5-7.5 and discharged. The resultant product had hydroxyl value 37.4 mgKOH/g, corresponding to behenyl alcohol+26.8 moles EO.
Molten behenyl alcohol (3200 g, 9.9 mol) and 45% potassium hydroxide (11 g, 0.09 mol dry) were charged to the vessel, which was then purged with nitrogen and heated to 90° C. with stirring. Vacuum was applied for one hour to dry the batch. The pressure was adjusted with nitrogen and ethylene oxide (900 g, 20.5 mol) was charged and reacted at 150° C. for 2 hours. The batch was then cooled to 80° C., neutralised with lactic acid (˜3 g) to a pH of 5.5-7.5 and discharged. The resultant product had hydroxyl value 138.4 mgKOH/g, corresponding to behenyl alcohol+1.8 moles EO.
Molten behenyl alcohol (1970 g, 6.1 mol) and 45% potassium hydroxide (11 g, 0.09 mol dry) were charged to the vessel, which was then purged with nitrogen and heated to 90° C. with stirring. Vacuum was applied for one hour to dry the batch. The pressure was adjusted with nitrogen and ethylene oxide (1350 g, 30.7 mol) was charged and reacted at 150° C. for 2 hours. The batch was then cooled to 80° C., neutralised with lactic acid (˜4 g) to a pH of 5.5-7.5 and discharged. The resultant product had hydroxyl value 107.8 mgKOH/g, corresponding to behenyl alcohol+4.5 moles EO.
Further alcohol alkoxylates were prepared in the same way as described in Examples 1 to 5 and the products are given in Table 2 below.
The following emulsifier systems/compositions were produced by blending the compounds of Examples 1 to 4 in the proportions defined below.
The Structure Zea was dispersed in water. Phases A and B were separately mixed and heated to 75° C. Phase A was then added to phase B slowly with moderate stirring. The resulting mixture was homogenised for 1 minute at 9,500 rpm before being allowed to cool to 40° C. with moderate stirring. Phase C and then phase D were added while continuing to stir gently until the emulsion reached room temperature.
Phases A and B were separately mixed and heated to 70° C. Phase C was added to phase B just prior to emulsification. Slowly phase A was added to phase B whilst stirring intensively, and then homogenised for 1 minute. The emulsion was allowed to cool to 50° C. with moderate stirring, at which point phase D was added whilst stirring intensively. The formulation was neutralised with phase E and allowed to cool to room temperature with moderate stirring.
The Arlasilk PTM was added to the water before beginning to heat to 70-75° C. Separately the oil phase was combined and heated to 70-75° C. The oil phase was added to the water and Arlasilk PTM mixture with high speed stirring, and then homogenised for one minute. The stirring was slowed whilst the mixture cooled and the remaining ingredients added at <40° C.
The Dihydroxyacetone was pre-blended in the water of phase C. Phase A and phase B were separately mixed and heated to 75-80° C. Phases A and B were then combined with stirring and allowed to cool. Phase C and perfume was added into the mixture of phases A and B at 35-40° C. The formulation had a final pH of 4-6.
Separately phases A and B were combined. Both phases were heated to 65-70 ° C. and then mixed while stirring at 500 rpm. The stirring was then reduced to 300 rpm whilst the mixture cooled. Once cool the preservative, fragrance and lactic acid were added as required.
The magnesium aluminium silicate was hydrated in warm water. The oil phase and the rest of the water phase were then mixed separately and heated to 70-75° C. The dispersed magnesium aluminium silicate phase was added to the warm water phase, and then the oil phase was added to the water phase under stirring. Perfume was added to the formulation once it had cooled to 40° C., and the completed formulation allowed to cool while stirring.
The hydroxyethyl cellulose was hydrated in warm water (60-65° C.). The oil phase was mixed and heated to 60-65° C., then the cellulose solution was added to the oil phase whilst stirring. The mixture was stirred to cool, adding potassium thioglycollate solution once the temperature of the mixture reached 30-35° C. The calcium hydroxide was slurried into the remaining water and added to the emulsion. The pH of the emulsion was adjusted. Finally, the emulsion was stirred and cooled.
The oil phase and water phase were heated separately to 65-70° C. The water phase was then added to the oil phase with stirring. The mixture was allowed to cool while being stirred. At 35° C. the Potassium Hydroxide solution was added and the formulation filled off at 30° C.
The oil phase and water phase were mixed and heated separately to 70-75° C. The water phase was added to the oil phase with gentle stirring. Once below 50° C., the remaining ingredients were added under stirring.
Part A and Part B were separately mixed and heated to 65° C. Part B was added to Part A with mixing and cooled to 40° C. The ingredients of Part C were combined with mixing, and cooled to room temperature. The Part A/B mixer was switched to a side sweep blade. Slowly Part C was added to Part A/B, continuing mixing for 30 minutes until completely smooth and homogenous. The formulation was then cooled further to the desired fill temperature.
The oil phase and water phase were mixed and heated separately to 60-65° C. The water phase was added to the oil phase with stirring. In a separate container, the Sodium Hydroxide was premixed with the water quantity. The emulsion was stirred to cool, and the Sodium Hydroxide solution added in at 40-45° C. Stirring was continued whilst cooling to the desired fill off temperature.
Separately parts A and B were combined and heated to ˜70° C. Part A was then added to part B with stirring. The emulsion was then allowed to cool, and part C added once the temperature fell below 45° C.
It is to be understood that the invention is not to be limited to the details of the above embodiments, which are described by way of example only. Many variations are possible.
Any or all of the disclosed features, and/or any or all of the steps of any method or process described, may be combined in any combination.
Each feature disclosed herein may be replaced by alternative features serving the same, equivalent or similar purpose. Therefore, each feature disclosed is one example only of a generic series of equivalent or similar features.
The above statements apply unless expressly stated otherwise. The term specification, for these purposes, includes the description and any accompanying claims, abstract and drawings.
| Number | Date | Country | Kind |
|---|---|---|---|
| 1712844.8 | Aug 2017 | GB | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/GB2018/052285 | 8/10/2018 | WO | 00 |
