Method of emulsion polymerization

Abstract: A method is described for making a silicone emulsion. According to the method, there is formed a mixture of water, a cyclic siloxane, optionally a nonionic surfactant and a cationic surfactant. There is then added to the mixture a polymerization initiator which can be a silanolate or an organosilanolate. The mixture is heated and agitated and the cyclic siloxane is allowed to polymerize until an emulsion is formed. The benefit of this emulsion polymerization method is that the rate of emulsion polymer formation is enhanced. Thus, the method provides for the production of emulsions in a new and more efficient manner. The silicone emulsion will produce an elastomeric product when water is removed under ambient conditions.

Description: This invention is directed to a method of emulsion polymerization and to enhancement in the rate of polymer formation. More particularly, a method is introduced for the production of emulsions in a new and more efficient manner. EP-A 0 459 500 describes a stable, oil-free polysiloxane emulsion prepared from a mixture comprising a cyclic siloxane, a non-ionic surfactant, an ionic surfactant, water, and a condensation polymerization catalyst. From EP-A 0 529 883 a conditioning composition for hair and/or skin comprising a stable microemulsion of a conditioning oil is known wherein the conditioning oil is selected from volatile and non-volatile silicones, siloxane gums and resins. This microemulsion of the conditioning agent is stabilized by an anionic, cationic or non-ionic surfactant. EP-A 0 514 934 concerns hair care compositions containing emulsion polymers. The problem solved by this invention is the provision of a method of making an emulsion containing a silicone polymer of a high viscosity, in a shorter period of time than is possible with existing techniques known in the art. Thus, standard techniques of emulsion polymerization, while effective in the production of silicone emulsions, suffer from the disadvantage of yielding suitable emulsions only after periods of time for polymerization which are often in excess of several days. According to some standard techniques, two to five days are required to enable the polymerization to proceed for the silicone polymer in the emulsion to reach a desired high viscosity. This time problem is solved in this invention, by the use of a certain unique initiator in the emulsion polymerization technique. These initiators are silanolates and organosilanolates and the emulsions produced contain silicone polymers of equivalent or higher viscosity than achieved by standard techniques. Yet, our rate of emulsion polymer formation is achieved in a much shorter period of time, typically only three hours. In comparison to the time required for emulsion polymer formation under conditions of standard techniques, this is significant. The silicone emulsions of our invention have been found to be especially useful as additives in the personal care market. This invention provides a method of making a silicone emulsion in a much shorter period of time. The emulsion is made by dispersing a siloxane in water by forming a mixture of water, a cyclic siloxane, a nonionic surfactant and a cationic surfactant. To the mixture is added a polymerization initiator which is a silanolate or an organosilanolate. The method includes the additional steps of heating the mixture of water, cyclic siloxane, surfactants and initiator; agitating the heated mixture; and allowing the cyclic siloxane to polymerize until an emulsion is formed. In an alternate embodiment, the emulsion is made without adding a nonionic surfactant; and therein, the polymerization is conducted using only the cyclic siloxane, a cationic surfactant and the polymerization initiator. The surprising benefit derived from our invention is the production of an emulsion in less time by shortening the polymerization time with use of our unique initiator system. An additional benefit obtained is that it is now possible to produce microemulsions containing amine functional siloxanes of high viscosity, typically a viscosity in excess of one hundred thousand centistokes (mm 2 /s) measured at 25°C. For this invention, a "microemulsion" is considered to be a composition in which the continuous portion of the emulsion contains a noncontinuous silicone phase which is in the form of droplets in the continuous phase of an average diameter of less than 140 nanometers. Such emulsions are particularly useful in the personal care arena for imparting conditioning benefits to hair. Emulsions are mixtures of at least two components which are substantially immiscible in each other and a surfactant which lowers interfacial tension between the two phases. A microscopic view of aqueous emulsions reveals two phases, an oil phase and a water phase. Depending upon the proportion of each component, the emulsion is characterized as an oil-in-water emulsion or a water-in-oil emulsion. The chief distinction between the two is which component, the oil or water phase, comprises the continuous portion of the emulsion. The noncontinuous phase is in the form of droplets within the other phase. Methods for making aqueous emulsions of polydiorganosiloxanes are well known in the art and are separated into two types. Thus, emulsions are made by mechanical means and emulsions are made by emulsion polymerization means. Emulsions made by mechanical means typically involve homogenizing a mixture of polydiorganosiloxane, surfactant and water using milling machinery to obtain the desired droplet sizes. In contrast, emulsion polymerization methods for making emulsions of high viscosity polymers involve starting with low viscosity polymer precursors, i.e., monomers or reactive oligomers, which are immiscible in water; a surfactant to stabilize the polymer precursor droplet in water; and a water soluble polymerization catalyst. Typically, the catalyst is a strong mineral acid such as hydrochloric acid or a strong alkaline catalyst such as sodium hydroxide. These components are added to water, the mixture is stirred and polymerization is allowed to advance until the reaction is complete or the desired degree of polymerization is reached and an emulsion of the polymer is formed. One example of an emulsion polymerization process is taught in U.S. Patent 2,891,920, which shows a method of making aqueous emulsions of a polydimethylsiloxane, starting with precursor molecules of the polydimethylsiloxane. Another example of such a process is described in EP-A2 0 459 500. Polydiorganosiloxane precursors which are used in the practice of our invention include cyclic siloxanes which are relatively insoluble in water and which are polymerized using emulsion polymerization techniques. The preferred cyclic siloxanes have the formula: in which R and R' denote methyl, ethyl, propyl, vinyl, allyl or phenyl; and n is 3, 4, 5 or 6. The cyclic precursors are the pure species such as octamethylcyclotetrasiloxane, hexamethylcyclotrisiloxane, decamethylcyclopentasiloxane, tetramethyltetravinylcyclotetrasiloxane and tetramethyltetraphenylcyclotetrasiloxane or mixtures of the species can be used. For example, a mixture of cyclopolydimethylsiloxanes having three, four and five siloxane units could be used. If desired, the reaction medium may also include a small portion of other organosilicon compounds which contain a hydrolyzable or silanol group in the molecule which is capable of polymerization. Suitable compounds include amine functional silanes, vinyl functional silanes or halogenalkyl functional silanes. Representative silanes are N-(2-aminoethyl)-3-(aminopropyl)trimethoxysilane, vinyltriethoxysilane, vinyltriacetoxysilane and 3-chloropropyltrimethoxysilane. The polymerization medium used in our invention comprises water, an effective amount of surfactant to stabilize the polydiorganosiloxane droplets formed therein and an effective amount of initiator to polymerize the polydiorganosiloxane precursor. The preferred amount of initiator used to catalyze the polymerization of the precursor is between 0.5 to 15 weight percent, based on the total weight of the composition depending upon the initiator employed. The initiator used as the polymerization catalyst in the present invention is a silanolate or an organosilanolate. These alkali-metal salts are metal derivatives of organosilanols and have the formula R'' x Si(OM) 4-x . In the formula, R'' is an alkyl radical having from one to six carbon atoms, an aryl radical, an alkenyl radical, an alkylamino radical or an epoxy radical; and x has a value of zero to three. Suitable alkyl and aryl R'' radicals are methyl, ethyl and phenyl. Suitable alkenyl R'' radicals are vinyl, allyl, propenyl and hexenyl. Suitable aminoalkyl R'' radicals are aminopropyl and ethylene diaminopropyl. Suitable epoxy R'' radicals are 3-glycidoxypropyl and 2-(3,4-epoxycyclohexyl)-ethyl. M is an alkali metal in Group IA of the Periodic Table, such as lithium, sodium, potassium, rubidium and cesium. Sodium is the preferred alkali metal. For this invention, the value of x is preferably two or three. The most suitable initiators are sodium trimethylsilanolate NaOSi(CH 3 ) 3 , sodium triphenylsilanolate (C 6 H 5 ) 3 SiONa, disodium dimethylsilanolate (CH 3 ) 2 Si(ONa) 2 and disodium methylaminopropylsilanolate (CH 3 ) [H 2 NCH 2 CH 2 CH 2 ]Si(ONa) 2 . The sodium salts of the triorganosilanols are obtained from the reaction of the corresponding hexaorganodisiloxane and sodium hydroxide in an alcoholic solution. Trimethylsilanolates are obtained by the reaction of hexamethyldisiloxane with sodamide or potassamide in liquid ammonia or absolute ether. Silanolates are also obtained by the reaction of triorganoalkoxysilanes with alkali-metal hydroxides or triorganosilanols with alkali metals or alkalimetal hydroxides. As noted above, the mixture preferably contains a nonionic surfactant, although it may be omitted in an alternate emodiment of the invention. Most preferred for this invention is an ethoxylated fatty alcohol, although other types of nonionic emulsifiers can be employed. Such fatty alcohol ethoxylates contain in their molecule the characteristic group -(OCH 2 CH 2 ) a OH, which is attached to a fatty hydrocarbon residue of eight to twenty carbon atoms, such as lauryl (C 12 ), cetyl (C 16 ) and stearyl (C 18 ). The integer "a" can have a value of one to one hundred, but typically has a value of 12 to 40. Examples of commercial products found to be suitable in the present invention, include the various polyoxyethylene fatty alcohols sold under the tradename BRIJ by ICI Americas Incorporated, of Wilmington, Delaware; the tradename EMERY by the Henkel Corporation/Emery Group, of Ambler, Pennsylvania; the trademark ETHOSPERSE® by Lonza Incorporated, of Fairlawn, New Jersey; and the trademark PROMULGEN® by the Amerchol Corporation, of Edison, New Jersey. A particularly preferred nonionic surfactant is BRIJ 35 Liquid. This polyoxyethylene (23) lauryl ether has a hydrophobic/lipophobic balance (HLB) value of about 16.9 and a structure corresponding to the formula C 12 H 25 (OCH 2 CH 2 ) 23 OH. Laureth-23 is the International Nomenclature Cosmetic Ingredient (INCI) name assigned by The Cosmetic, Toiletry and Fragrance Association, Washington, D.C., (CTFA) to polyoxyethylene (23) lauryl ether. Laureth-23 is also sold under the trademark AMEROXOL® LE-23 by the Amerchol Corporation; the tradename EMTHOX 5877 by the Henkel Corporation; the trademark MACOL® LA-23 by PPG/Mazer of Gurnee, Illinois; and the trademark WITCONOL® 5964 by the Witco Corporation, of New York, New York. Other polyoxyethylene fatty alcohols which are employed in the present invention are polyoxyethylene (4) lauryl ether, polyoxyethylene (2) cetyl ether, polyoxyethylene (10) cetyl ether, polyoxyethylene (20) cetyl ether, polyoxyethylene (2) stearyl ether, polyoxyethylene (10) stearyl ether, polyoxyethylene (20) stearyl ether, polyoxyethylene (21) stearyl ether, polyoxyethylene (100) stearyl ether, polyoxyethylene (2) oleyl ether, polyoxyethylene (10) oleyl ether and polyoxyethylene (20) oleyl ether. Other suitable nonionic surfactants which are either ethoxylated alcohols or ethoxylated alkyl phenols are sold under the trademarks TERGITOL® and TRITON® by Union Carbide Corporation, Danbury, Connecticut; NEODOL® by Shell Chemical Company, Houston, Texas; MACOL® by PPG Industries; and under the tradenames TRYCOL by Henkel Corporation; and BRIJ by ICI Americas Incorporated, Wilmington, Delaware. In addition, some other nonionic surfactants which are used are fatty acid alkanolamides or amine oxides. The fatty acid alkanolamides are nonionic surfactants obtained by reacting alkanolamines such as monoethanolamine, diethanolamine, monoisopropanolamine or diisopropanolamine, with a fatty acid or fatty acid ester to form the amide. The hydrophobic portion of the nonionic surfactant is provided by a fatty acid hydrocarbon chain which generally has from ten to twenty-one carbon atoms. The fatty acid alkanolamide surfactants include fatty acid diethanolamides such as isostearic acid diethanolamide, lauric acid diethanolamide, capric acid diethanolamide, coconut fatty acid diethanolamide, linoleic acid diethanolamides, myristic acid diethanolamide, oleic acid diethanolamide and stearic acid diethanolamide; fatty acid monoethanolamides such as coconut fatty acid monoethanolamide; and fatty acid monoisopropanolamides such as oleic acid monoisopropanolamide and lauric acid monoisopropanolamide. Representative of a suitable such nonionic surfactant is a product sold under the trademark WITCAMIDE® by Witco Corporation. The amine oxides are nonionic surfactants obtained by oxidizing a tertiary amine to form the amine oxide. Amine oxide surfactants include the N-alkyl amine oxides such as N-cocodimethylamine oxide, N-lauryl dimethylamine oxide, N-myristyl dimethylamine oxide and N-stearyl dimethylamine oxide; the N-acyl amine oxides such as N-cocamidopropyl dimethylamine oxide and N-tallowamidopropyl dimethylamine oxide; and N-alkoxyalkyl amine oxides such as bis(2-hydroxyethyl) C12-15 alkoxy-propylamine oxide. The hydrophobic portion of the amine oxide surfactants is generally provided by a fatty hydrocarbon chain containing from ten to twenty-one carbon atoms. Representative amine oxide surfactants include lauric acid diethanolamide, N-lauryl dimethylamine oxide, coconut acid diethanolamide, myristic acid diethanolamide and oleic acid diethanolamide. Suitable commercial materials are those products sold under tradenames and trademarks such as AMMONYX by the Stephan Company, Northfield, Illinois; BARLOX® by Lonza Incorporated; and MACKAMINE by The McIntyre Group Limited, University Park, Illinois. Sorbitan derivatives sold under the tradenames SPAN and TWEEN by ICI Americas Incorporated; and propylene oxide-ethylene oxide block polymers sold under the trademark PLURONIC® by BASF Corporation, Parsippany, New Jersey; may also be employed. The mixture also contains a cationic surfactant in addition to the nonionic surfactant. However, in an alternate embodiment of the invention, polymerization is conducted with only the cationic surfactant. Cationic surfactants which are useful include compounds which contain amino or quaternary ammonium hydrophilic moieties in the molecule and which are positively charged, such as quaternary ammonium salts. Representative quaternary ammonium salts which may be employed are ditallowdimethyl ammonium chloride, ditallowdimethyl ammonium methyl sulfate, dihexadecyl dimethyl ammonium chloride, di(hydrogenated tallow) dimethyl ammonium chloride, dioctadecyl dimethyl ammonium chloride, dieicosyl dimethyl ammonium chloride, didocosyl dimethyl ammonium chloride, di(hydrogenated tallow) dimethyl ammonium acetate, dihexadecyl dimethyl ammonium acetate, ditallow dipropyl ammonium phosphate, ditallow dimethyl ammonium nitrate, di(coconutalkyl) dimethyl ammonium chloride and stearyl dimethyl benzyl ammonium chloride. Suitable cationic surfactants are sold under tradenames or trademarks such as ADOGEN by Sherex Chemical Company Incorporated, Dublin, Ohio; EMCOL® by Witco Corporation; TOMAH by Tomah Products Incorporated, Milton, Wisconsin; and ARQUAD and ETHOQUAD by Akzo Chemicals Incorporated. One especially useful cationic surfactant in this invention is an N-alkyl-trimethyl ammonium chloride sold under the tradename ARQUAD T-27W by Akzo. The polymerization mixture which is used according to our invention preferably contains 50 to 80 percent by weight of water, 10 to 50 percent by weight of the cyclic siloxane, 5 to 15 percent by weight of the nonionic surfactant and the cationic surfactant and 0.5 to 15 percent by weight of a silanolate or organosilanolate initiator. The method of this invention is most preferably carried out by creating a mixture comprising a cyclic siloxane, a nonionic surfactant, a cationic surfactant, water and the initiator; although as noted above, the method can also be carried out with only the cyclic siloxane, cationic surfactant, water and the initiator. The mixture is then heated with agitation at a polymerization reaction temperature, until essentially all of the cyclic siloxane is reacted and a stable oil-free emulsion is formed. The mixture of cyclic siloxane, nonionic surfactant, cationic surfactant, water and initiator, is not stable and will separate without some means of agitation. Although it is not necessary to have all of the cyclic siloxane fully dispersed into the mixture during the reaction, some means of agitation must be provided throughout its course. Combining the cyclic siloxane, nonionic surfactant, cationic surfactant, water and initiator and then reacting the cyclic siloxanes to form the emulsion can take place in several ways. The first is to combine all of the ingredients with agitation, in any given order, and to heat to the desired polymerization temperature with agitation, thereby allowing the cyclic siloxanes to react and form an emulsion. Another way is to combine all of the ingredients with agitation, except for the initiator, heat to the desired polymerization temperature, add the initiator and thereafter to heat and agitate at the desired polymerization temperature, thereby allowing the cyclic siloxanes to react and form an emulsion. A further way is to combine all of the ingredients with agitation, except for the cyclic siloxane, heat to the desired polymerization temperature, add or feed in the cyclic siloxane and thereafter to heat and agitate at the desired polymerization temperature, thereby allowing the cyclic siloxanes to react and form an emulsion. It is not essential that the ingredients used in producing our emulsions be combined in any given order. However, it is essential to have agitation during and following the addition of the ingredients and to have achieved or heated to the polymerization temperature, when all of the ingredients have been combined. The preferred method for forming our emulsions is to create a mixture by combining the cyclic siloxane or mixture of cyclic siloxanes, preferably at least one nonionic surfactant, at least one cationic surfactant and water; providing agitation such that the cyclic siloxane is fully dispersed in the mixture; heating to the polymerization temperature; and adding the initiator. The mixture is then held at the polymerization temperature with agitation until a stable oil-free emulsion is formed. The method of this invention may also be carried out by combining and mechanically emulsifying at least the siloxane reactant, nonionic surfactant, cationic surfactant and part of the water. Additional water, the initiator and the surfactants can be added to the pre-emulsion with agitation. The mixture is then heated to the polymerization reaction temperature and held optionally with agitation, until the monomer is consumed in forming the emulsion. Polymerization reaction temperatures useful in this invention are typically above the freezing point and below the boiling point of water. Pressures above or below atmospheric pressure may allow operation outside of this range. The preferred temperature range is at least 50°C. but less than 95°C. The polymerization reaction is stopped at the desired level of conversion of cyclic siloxane and particle size, by using methods known in the art. It is preferred to stop the reaction when the largest amount of cyclic siloxane has been reacted or when the ring-chain equilibrium for the system and the desired particle size have been obtained. Reaction times, typically of three hours, are sufficient to achieve the desired particle size and level of conversion, according to this invention. The methods for stopping the reaction typically encompass neutralization of the initiator by the addition of an equal or slightly greater stoichiometric amount of acid. Either a strong or a weak acid may be used. Care must be taken when using a strong acid however not to over neutralize, as it may be possible to re-catalyze the reaction. It is preferred to neutralize with sufficient quantities of acid such that the resulting emulsion has a pH of about 7. Example 1 Preparation of Saponified Aminosilane The aminopropylmethyldisodium silanolate H 2 N(CH 2 ) 3 Si(CH 3 )(ONa) 2 was prepared in a 500 ml glass flask by adding 80 grams (2 moles) of sodium hydroxide and 350 grams of deionized water and mixing the contents until the sodium hydroxide dissolved. The contents of the flask were heated to 70°C. and 191 grams of aminopropylmethyldiethoxysilane (1 mole) was slowly added at a rate to maintain the temperature less than 80°C. while stirring. Ethanol was generated during the reaction and was removed by distillation. Example 2 Preparation of Saponified Dimethyldimethoxysilane The disodium dimethylsilanolate (CH 3 ) 2 Si(ONa) 2 was prepared in a 500 ml glass flask by adding 80 grams (2 moles) of sodium hydroxide and 250 grams of deionized water and mixing the contents until the sodium hydroxide dissolved. The contents of the flask were heated to 70°C. and 120 grams of dimethyldimethoxysilane (1 mole) was added at a rate to maintain the temperature less than 80°C. with stirring. Methanol was generated during the reaction and was removed by distillation. Example 3 - Comparison Preparation of Control Emulsion A control emulsion was prepared for purposes of comparison with the emulsions produced according to the invention. The control emulsion was prepared in a three-neck 1 liter flask by charging the flask with 337.5 grams of deionized water, 56.25 grams of Arquad T-27W cationic surfactant, 37.5 grams of Brij 35 Liquid nonionic surfactant and 195 grams of octamethylcyclotetrasiloxane. The flask was heated to 90°C. To the flask was added a preblend of 11.25 grams of aminopropylmethyldiethoxysilane (2 mole % amino), 22.5 grams of octamethylcyclotetrasiloxane and 5.25 grams of a 14.3 % sodium hydroxide solution as the catalyst, instead of a silanolate. The mixture in the flask was stirred for 5-6 hours and 1.125 grams of acetic acid and 85 grams of additional deionized water, were added to neutralize the mixture. The mixture was cooled to room temperature and 5 ppm of a preservative was added. The product was a clear emulsion having a mean particle size of siloxane droplets of sixty-six nanometers, as determined by measurement on a NICOMP™ Particle Size Analyzer. The viscosity at 25°C. of the siloxane polymer produced by the method of this comparison example was measured to be 1,900 centipoise (mPas) by solvent extraction of the siloxane from the emulsion water phase and then removing the solvent prior to measurement on a Brookfield Viscometer. ARQUAD T-27W is an N-alkyl-trimethyl ammonium chloride and the tradename of a product sold by Akzo Chemicals Incorporated. BRIJ 35 Liquid is a tradename for a polyoxyethylene (23) lauryl ether having an HLB value of 16.9 and a structure corresponding to C 12 H 25 (OCH 2 CH 2 ) 23 OH. Laureth-23 is its CTFA adopted name and this product is sold as a water solution containing 72 percent of the active ingredient, by ICI Americas Incorporated. Example 4 Emulsion Preparation Using Saponified Aminosilane Example 3 was repeated except that instead of using the aminopropylmethyldiethoxysilane, the aminopropylmethyldisodium silanolate H 2 N(CH 2 ) 3 Si(CH 3 )(ONa) 2 prepared in Example 1 was utilized. In this example, the aminopropylmethyldisodium silanolate was added prior to the addition of octamethylcyclotetrasiloxane. The amount of aminopropylmethyldisodium silanolate used corresponded to 2 mole % amino functionality, which is the same level used in Example 3. After the mixture in the flask was stirred for 5 hours at 90°C., an acetic acid solution was added to neutralize the mixture. The mixture was cooled to room temperature and 5 ppm of a preservative was added. The product was a slightly hazy emulsion having a mean particle size of siloxane droplets of 78.6 nanometers, as determined by measurement on a NICOMP™ Particle Size Analyzer. The viscosity of the siloxane polymer produced could not be measured due to the limitations of the viscometer, but the viscosity was estimated to be greater than 1 million centipoise (mPas) at 25°C. Example 5 Emulsion Preparation Using Saponified Aminosilane Example 3 was repeated except that instead of using the sodium hydroxide catalyst solution and aminopropylmethyldiethoxysilane, the aminopropylmethyldisodium silanolate H 2 N(CH 2 ) 3 Si(CH 3 )(ONa) 2 prepared in Example 1 was utilized. The amount of aminopropylmethyldisodium silanolate used corresponded to 2 mole % amino functionality, which is the same level used in Example 3. In this example, the aminopropylmethyldisodium silanolate was added prior to the addition of octamethylcyclotetrasiloxane. The mixture in the flask was heated to 85°C. and stirred for 2.5 hours before being neutralized with an acetic acid solution. The mixture was cooled to room temperature and 5 ppm of a preservative was added. The product was a clear emulsion, with a very slight haze present, having a mean particle size of siloxane droplets of sixty-six nanometers, as determined by measurement on a NICOMP™ Particle Size Analyzer. The viscosity of the siloxane polymer produced was measured to be 133,000 centipoise (mPas) at 25°C. Example 6 Emulsion Preparation Using Saponified Aminosilane Example 5 was repeated except that instead of using 2 mole % aminopropylmethyldisodium silanolate, the level was reduced by half to 1 mole percent. The mixture was heated to 90°C. and stirred for 3 hours before being neutralized with an acetic acid solution. The product was a clear emulsion having a mean particle size of siloxane droplets of 52.9 nanometers, as determined by measurement on a NICOMP™ Particle Size Analyzer. The viscosity of the siloxane polymer produced was measured to be 81,000 centipoise (mPas) at 25°C. Example 7 Emulsion Preparation Using Saponified Aminosilane Example 6 was repeated except that instead of using 2 mole % aminopropylmethyldisodium silanolate, the level was doubled to 4 mole percent. The mixture was heated to 85°C. and stirred for 2 hours before being neutralized with an acetic acid solution. The product was a slightly hazy emulsion having a mean particle size of siloxane droplets of 102.5 nanometers, as determined by measurement on a NICOMP™ Particle Size Analyzer. The viscosity of the siloxane polymer produced could not be measured due to the limitations of the viscometer, but the viscosity was estimated to be greater than 1 million centipoise (mPas) at 25°C. Example 8 Emulsion Preparation Using Saponified Dimethylsilane Example 3 was repeated except that instead of using the sodium hydroxide catalyst solution and aminopropylmethyldiethoxysilane, the disodium dimethylsilanolate prepared in Example 2 was utilized. The amount of dimethylsilanolate used was 2 mole % based on the amount of actives, which is the same percent of an actives level as the aminosilane used in Example 3. In this example, the disodium dimethylsilanolate was added prior to the addition of octamethylcyclotetrasiloxane. The mixture in the flask was heated to 90°C. and stirred for 2.5 hours before being neutralized with an acetic acid solution. The mixture was cooled to room temperature and 5 ppm of a preservative was added. The product was a clear emulsion, with a very slight haze present, having a mean particle size of siloxane droplets of 47.6 nanometers, as determined by measurement on a NICOMP™ Particle Size Analyzer. The viscosity of the siloxane polymer produced was measured to be 1,670 centipoise (mPas) at 25°C. Example 9 Emulsion Preparation Using Saponified Dimethylsilane Example 8 was repeated except that octamethylcyclotetrasiloxane was replaced with decamethylcyclopentasiloxane. The mixture in the flask was heated to 95°C. and stirred for 2.5 hours before being neutralized with an acetic acid solution. The mixture was cooled to room temperature and 5 ppm of a preservative was added. The product was a clear emulsion, with a very slight haze present, having a mean particle size of siloxane droplets of 79.9 nanometers, as determined by measurement on a NICOMP™ Particle Size Analyzer. The viscosity of the siloxane polymer produced was measured to be 1,700 centipoise (mPas) at 25°C. With the advent of consumer trends toward daily hair washing, conditioning products such as shampoos have emerged which are designed to render the hair easy to comb and tangle free in the wet state, as well as glossy and soft when dry. Such conditioning is provided by cationic polymers, which upon rinsing, produce a thin film on the hair. The film functions as a lubricant when the hair is wet and prevents static charge and "flyaway" when the hair is dry. Conditioning may also be provided by hair conditioning products designed solely for that purpose, such as rinses, mousses, aerosols and pump sprays. These conditioners are applied following shampooing. These conditioning products are rinsed from the hair a short time following their application. Such conditioners prevent excessive split ends and other mechanical hair damage and roughening and seek to neutralize the adverse effects which hair undergoes due to humidity, temperature, exposure to sunlight, frequent washing, combing and brushing and cosmetic treatments such as bleaching, dyeing and waving. The emulsions produced by methods of this invention were formulated into conditioning products to illustrate their utility in the personal care arena. The conditioning products of the invention were tested by standard industry techniques. In these tests, dark brown "virgin" European human hair was used for testing the conditioning efficacy of the products. A master hank of hair 20.3 cm (eight inches) in length was subdivided into a series of individual hair tresses. Each tress weighed about 2.5 grams. The top 2.5 cm (one inch) portion of the hair tress was trimmed and glued to a 2'' x 2'' (5.1 x 5.1 cm) plastic tab using DUCO CEMENT®. The cement was allowed to dry and the hair tress was combed and trimmed to a length such that 15.2 cm (six inches) of hair extended below the bottom of the plastic tab. Each "virgin" tress was rinsed for thirty seconds with 40°C. tap water. The tress was shampooed and lathered with two milliliters of a fifty percent solution of PRELL® shampoo for sixty seconds by stroking the tress downwardly. The tress was rinsed for sixty seconds with tap water. Excess water was removed from the tress by passing the tress between the index and middle fingers. Instead of employing a commercial shampoo for treating the "virgin" tress, a cleaning solution can be prepared by combining 450 grams of distilled water with 450 grams of ammonium lauryl sulfate, which is an anionic surfactant sold under the tradename STANDAPOL A in the form of a liquid containing 30 percent of the active ingredient by Henkel Corporation, Ambler, Pennsylvania. Following treatment of the tress, the tress is hand combed and evaluated using the INSTRON™ "WET" and the INSTRON™ "DRY" COMBING procedures. INSTRON™ COMBING is an industry recognized test for determining hair conditioning by the ease of wet combing and the ease of dry combing. The test employs an INSTRON™ strain gauge which is equipped to measure the force required to comb the hair. Conditioning performance is based on the ability of a particular hair treating formulation such as a shampoo or a hair conditioner, to reduce the force required to comb the hair with the INSTRON™ strain gauge. The force is reported as Average Combing Load (ACL). The lower the (ACL) value, the better is the conditioning effect imparted by the formulation being evaluated. Typically, (ACL) base lines are initially established with "untreated" tresses. The Average Combining Load (ACL) is defined as the area under the force curve divided by the length or distance traveled by the INSTRON™ comb. This number is reported in grams or kilograms of force. The effectiveness of a treatment is the percent change in (ACL) after treatment and this value is calculated as % Change ACL = treated hair ACL - untreated hair ACL x 100 % / untreated ACL. An effective treatment is expressed as a negative number. A positive number indicates that treated hair is more difficult to comb than untreated hair. For tests involving a conditioning shampoo, the hair tress is rinsed with tap water at 40°C. for thirty seconds. The test shampoo is applied to the tress in the amount of 0.5 milliliters and lathered for thirty seconds by stroking the tress downwardly. The tress is rinsed for thirty seconds with 40°C. tap water and 0.5 milliliters of the test shampoo are applied to the tress for a second time and lathered for thirty seconds by stroking the tress downwardly. The tress is rinsed for thirty seconds with 40°C. tap water and excess water is removed by passing the tress between the index and middle fingers. For tests involving a hair conditioner, the hair tress is rinsed with tap water at 40°C. for thirty seconds. The test conditioner is applied to the tress in the amount of one milliliter and the tress is stroked for thirty seconds. The tress is rinsed for thirty seconds with 40°C. tap water and excess water is removed by passing the tress between the index and middle fingers. According to the INSTRON™ WET COMBING method, each hair tress is soaked for 15-30 minutes in distilled water. Excess water is removed by passing the tress through the index and middle fingers. The tress is untangled by combing the tress by hand three times. The tress is retangled by dipping the tress in distilled water three times and excess water is removed by passing the tress through the index and middle fingers twice. The tress is placed on a hanger and INSTRON™ combed. According to the INSTRON™ DRY COMBING method, each hair tress is stored overnight in a constant environment to normalize the water content of the hair. The tress is untangled by combing the tress by hand three times. The tress is retangled by swirling the tress three times clockwise and three times counter-clockwise. The tress is placed on a hanger and INSTRON™ combed. The results of the INSTRON™ WET & DRY COMBING tests conducted with conditioning products of this invention and with comparison conditioning products, are shown below in the Tables. INSTRON™ WET COMBING Conditioner Applied Percent Change (ACL) Blank Conditioner -11 Silicone 1 -62 Silicone 2 -74 Silicone 3 -80 Silicone 4 -73 Silicone 5 -79 Commercial Silicone -67 INSTRON™ DRY COMBING Conditioner Applied Percent Change (ACL) Blank Conditioner -34 Silicone 1 -48 Silicone 2 -56 Silicone 3 -65 Silicone 4 -67 Silicone 5 -70 Commercial Silicone -71 It is seen from the above Tables, that the conditioners containing Silicones 1-5 which were the emulsions prepared according to the present invention, achieved a significantly better rating under both INSTRON™ Wet and Dry Combing tests; in comparison to a Blank Conditioner which was non-silicone containing. It is also seen from the above Tables, that the conditioners containing Silicones 1-5, achieved a significantly better rating under the INSTRON™ Wet Combing test; with respect to the comparison conditioner containing a Commercial Silicone. The conditioning products were further tested in a subjective evaluation with the aid of a panel of ten volunteers. The volunteers were each asked to test treated tresses by feeling the dry tress and then by passing a comb through the tress. The volunteers assigned a number between one and five to each tress tested, with five being the tress which felt the best or was easiest to comb and one being the tress which felt the worst or was the hardest to comb. Tables III and IV show the results of these subjective evaluations. SUBJECTIVE EVALUATION Conditioner Applied DRY COMB Silicone 1 2.5 Silicone 2 1.7 Silicone 3 2.5 Silicone 4 1.4 Silicone 5 1.5 Commercial Silicone 1.1 SUBJECTIVE EVALUATION Conditioner Applied DRY FEEL Silicone 1 2.2 Silicone 2 2.7 Silicone 3 2.2 Silicone 4 1.7 Silicone 5 1.9 Commercial Silicone 1.3 It is seen from the above Tables, that the conditioners containing Silicones 1-5 which were the emulsions prepared according to the present invention, achieved a significantly better rating under both subjective tests; in comparison to the conditioner containing the Commercial Silicone. The Commercial Silicone used to formulate the conditioner used for comparison in the above Tables, was an amine substituted siloxane polymer containing reactive silanol functionality (≡SiOH), stabilized in an aqueous emulsion by a cationic and a nonionic surfactant. This siloxane polymer has the formula HO[(CH 3 ) 2 SiO] x [(OH)QSiO] y H in which Q is -CH 2 CH 2 CH 2 NHCH 2 CH 2 NH 2 and x and y are numbers depending on the molecular weight of the polymer. This polymer contains about 0.6 percent amine functionality and has an initial viscosity of two thousand Centistokes (mm 2 /s) measured at 25°C. The Commercial Silicone polymer has been assigned the INCI name AMODIMETHICONE by The Cosmetic, Fragrance & Toiletry, Association (CTFA). It is described in numerous U.S. patents such as 5,326,483. An emulsion form of the polymer is available commercially from the Dow Corning Corporation, Midland, Michigan. Silicone 1 in the Tables was a microemulsion produced according to this invention as shown in Example 4. The microemulsion contained 30 percent by weight of a silicone polymer having two mole percent of amine functionality in the molecule, an average particle diameter of 78.6 nanometers and a viscosity in excess of one million Centistokes (mm 2 /s) at 25°C. Silicone 2 in the Tables was a microemulsion produced by the method of our invention as shown in Example 5. The microemulsion contained 30 percent by weight of a silicone polymer having two mole percent of amine functionality in the molecule, an average particle diameter of 66 nanometers and a viscosity of 133,000 Centistokes (mm 2 /s) at 25°C. Silicone 3 in the Tables was a microemulsion produced by the method of the present invention. The microemulsion contained 30 percent by weight of a silicone polymer having one mole percent of amine functionality in the molecule, an average particle diameter of 44 nanometers and a viscosity of 21,100 Centistokes (mm 2 /s) at 25°C. Silicone 4 in the Tables was a microemulsion produced by our method as shown in Example 6. The microemulsion contained 30 percent by weight of a silicone polymer having one mole percent of amine functionality in the molecule, an average particle diameter of 52.9 nanometers and a viscosity of 81,000 Centistokes (mm 2 /s) at 25°C. Silicone 5 in the Tables was a microemulsion produced by our method as shown in Example 7. The microemulsion contained 30 percent by weight of a silicone polymer having four mole percent of amine functionality in the molecule, an average particle diameter of 102.5 nanometers and a viscosity in excess of one million Centistokes (mm 2 /s) at 25°C. These silicone microemulsions of the invention are shown in the Table below as Nos. 1 to 5, respectively. No. Weight Percent Mole Percent Amine Polymer Viscosity (mm 2 /s) Particle Size (nanometer) 1 30 2 > million 78.6 2 30 2 133,000 66 3 30 1 21,100 44 4 30 1 81,000 52.9 5 30 4 > million 102.5 6 30 2 2,000 66 Silicone 6 in Table V was the microemulsion produced in Example 3 which is a method not according to our invention and in which a silanolate or an organosilanolate was not used as the polymerization initiator. Under otherwise equivalent processing conditions, however, it can be seen that the viscosity of the resulting polymer was much less than the viscosity of the polymers obtained by practicing the method of this invention. This demonstrates that our emulsion polymerization method unexpectedly enhances the rate of emulsion polymer formation and that our method is capable of providing higher viscosity microemulsions in a shorter period of time than is possible with equivalent techniques known in the art. The conditioner used in Tables I-IV to evaluate the various silicone emulsions contained 92 percent by weight of water, 1.5 percent by weight of a nonionic surfactant, one percent by weight of a thickener, three percent by weight of a consistency regulator and co-emulsifier for providing body and texture to the formulation, 0.5 percent by weight of a preservative and sufficient of an acid for adjusting the pH. The Blank Conditioner contained no silicone. For the conditioners containing a silicone, two percent by weight of the water was replaced by a silicone emulsion. The procedure for making these conditioners involved predispersing the thickener in two-thirds of the water and heating the predispersion to 75°C. The remaining one-third of the water was heated to 75°C. and used to melt the nonionic surfactant and the co-emulsifier. The two portions of water were combined, subjected to high shear for five minutes and mixed for another five minutes. The mixture was cooled to 40°C., the silicone emulsion was added and mixing was continued for ten more minutes. The mixture was allowed to cool to room temperature, the preservative was added and the pH of the conditioner was adjusted with the acid. The nonionic surfactant used to prepare these conditioners was an ethoxylated fatty alcohol sold under the tradename EUMULGIN B2 by Pulcra, S.A., of Barcelona, Spain. CETEARETH-20 is the CTFA INCI name for this polyoxyethylene (20) cetyl ether. This compound has the formula R(OCH 2 CH 2 ) n OH in which n is about twenty and R is a blend of alkyl groups derived from cetyl and stearyl alcohol. The thickener used to prepare the conditioners was hydroxyethylcellulose which is sold under the tradename NATROSOL 250 HHR by Aqualon of Wilmington, Delaware. The consistency regulator and co-emulsifier was cetyl alcohol. The preservative was a mixture of diazolidinyl urea and parabens which is sold under the trademark GERMABEN® II-E by Sutton Laboratories of Chatham, New Jersey. Citric acid was used for adjusting the pH. The details of the conditioner set forth above is not intended as limiting the present invention, but is merely provided for the purpose of illustrating its utility as it relates to the hair care arena. The invention is applicable to any formulation intended to impart conditioning benefits to the hair and can contain by way of example, 75-95 percent by weight of water, 1-40 percent by weight of one or more surfactants and co-emulsifiers, 1-3 percent by weight of a thickener, 0.1-1 percent by weight of a preservative and 0.5-15 percent by weight of a silicone emulsion as one of the conditioning agents. Thus, the hair conditioning compositions prepared according to the invention may contain other types of adjuvants than are enumerated above. For example, the composition may include adjuvants necessary to provide products which are aesthetically pleasant to the consumer, such as perfumes, colorants, electrolytes, foam boosters and builders, foam stabilizers, antimicrobials, antioxidants, ultraviolet light absorbers, pearlescent agents such as ethylene glycol monostearate and ethylene glycol distearate and medicaments. Thickeners used to facilitate the hand application of the composition to the hair, may be added in sufficient quantities to provide more luxurious effects. Other types of representative thickening agents which are used are sodium alignate; gum arabic; guar gum; hydroxypropyl guar gum; cellulose derivatives such as methylcellulose, hydroxypropyl methylcellulose and hydroxypropylcellulose; starch and starch derivatives such as hydroxyethylamylose and starch amylose; locust bean gum; electrolytes such as sodium chloride and ammonium chloride; saccharides such as fructose and glucose; and derivatives of saccharides such as PEG-120 methyl glucose dioleate. Only cosmetically acceptable perfumes and fragrances should be used to prepare the composition. Colorants may be added where it is desired to confer a hue to the composition. Acids can be employed to adjust the pH within the range of five to nine. Any water soluble carboxylic acid or mineral acid may be employed. Other suitable acidic compounds include mineral acids such as hydrochloric acid, sulfuric acid and phosphoric acid; monocarboxylic acids such as acetic acid, lactic acid and propionic acid; and polycarboxylic acids such as succinic acid and adipic acid. Additional organic cationic conditioning agents may be added to the composition for the purpose of providing more hair grooming benefit. Such organic cationic conditioning agents may include quaternary nitrogen derivatives of cellulose ethers; homopolymers of dimethyldiallyl ammonium chloride; copolymers of acrylamide and dimethyldiallyl ammonium chloride; homopolymers or copolymers derived from acrylic acid or methacrylic acid which contain cationic nitrogen functional groups attached to the polymer by ester or amide linkages; polycondensation products of N,N'-bis-(2,3-epoxypropyl)-piperazine or piperazine-bis-acrylamide and piperazine; and copolymers of vinylpyrrolidone and acrylic acid esters with quaternary nitrogen functionality. Specific materials include the various polyquats known under the INCI names of Polyquaternium-7, Polyquaternium-8, Polyquaternium-10, Polyquaternium-11 and Polyquaternium-23. Cationic surfactants such as cetyl trimethylammonium chloride, cetyl trimethylammonium bromide and stearyltrimethylammonium chloride, may also be employed in the compositions as the organic cationic conditioning agent. Other types of preservatives may be required and representative compounds which may be employed include formaldehyde, DMDM hydantoin, 5-bromo-5-nitro-1,3-dioxane, methyl paraben, propyl paraben, sorbic acid, imidazolidinyl urea and 5-chloro-2-methyl-4-isothiazolin-3-one which is a product sold under the trademark KATHON® LX by the Rohm and Haas Company, Philadelphia, Pennsylvania. The concept of the present invention is applicable to any hair care product intended to impart conditioning benefits to the hair, whether classified as a conditioner, a shampoo or a so-called "two-in-one shampoo/conditioner" which both cleans and conditions. The following examples are set forth for the purpose of illustrating in detail the alternate embodiment of the present invention, in which the nonionic surfactant is omitted. In this alternate method, a silicone emulsion is made by forming a mixture comprising water, a cyclic siloxane and a cationic surfactant. There is added to the mixture a silanolate or organosilanolate polymerization initiator and the mixture is heated and agitated. The cyclic siloxane is then allowed to polymerize until an emulsion is formed. No nonionic surfactant is required during polymerization in accordance with this alternate embodiment, although a nonionic surfactant can be added after polymerization, to stabilize the emulsion which is formed. Example 10 Preparation of Sodium Saponified Aminoethyl-aminopropylmethyldimethoxysilane The disodium aminoethylaminopropyl methylsilanolate NH2(CH2)2NH(CH2)3SiCH3(ONa)2 was prepared in a 1000 milliliter glass flask by adding 80 grams (2 moles) of sodium hydroxide and 350 grams of deionized water and mixing until the sodium hydroxide was dissolved. The contents of the flask were heated to 70°C. and 206 grams of aminoethylaminopropylmethyldimethoxysilane (1 mole) was added at a rate keeping the temperature less than 80°C. with stirring. Methanol generated during the reaction was removed by distillation. The percent non-volatile content was measured to be 51.6%. Example 11 Preparation of Potassium Saponified Aminoethyl-aminopropylmethyldimethoxysilane The dipotassium aminoethylaminopropyl methylsilanolate NH2(CH2)2NH(CH2)3SiCH3(OK)2 was prepared in a 1000 millilter glass flask by adding 112.2 grams (2 moles; formula weight of 56.1 grams) of potassium hydroxide and 350 grams of deionized water and mixing until the potassium hydroxide was dissolved. The contents of the flask was heated to 70°C. and 206 grams of aminoethyl-aminopropylmethyldimethoxysilane (1 mole) was added at a rate keeping the temperature less than 80°C. with stirring. Methanol generated during the reaction was removed by distillation. The percent non-volatile content was measured to be 51.66%. Example 12 Emulsion Preparation Using Sodium Saponified Aminoethyl-aminopropylmethyldimethoxysilane An emulsion was prepared by charging a flask with 402 grams of deionized water, 66 grams of ARQUAD T-27W, an N-alkyl trimethyl ammonium chloride cationic surfactant sold by Akzo Chemicals Incorporated and 262.5 grams of a blend of dodecamethylcyclohexasiloxane, decamethylcyclopentasiloxane and octamethylcyclotetrasiloxane. The contents of the flask were mixed for 20 minutes before processing the material through a homogenizer shear device using two passes at 7500 psi (51,711 kPa). The sheared material in the amount of 730.5 grams was added to a three-neck one liter flask, heated to 84°C. with stirring and 9.46 grams of the disodium aminoethyl-aminopropyl methylsilanolate prepared in Example 10 was added. The contents of the flask were mixed at 84°C. for 8.75 hours before being cooled to 40°C., at which point the contents were neutralized with acetic acid to a pH of 7.0 to 7.5. Then 12.75 grams of a nonionic alkylphenoxypolyoxyethylene ethanol surfactant MAKON 10 sold by the Stephan Company was added to stabilize the emulsion. The product was a white emulsion having a mean particle size of siloxane droplets of 170.9 nanometers as determined by measurement on a NICOMP™ Particle Size Analyzer. The viscosity of the siloxane polymer was measured to be 10,900 centistokes (mm 2 /s) at 25°C. by solvent extraction of the siloxane from the emulsion water phase and then removing the solvent prior to measurement on a Brookfield Viscometer. Example 13 Emulsion Preparation Using Potassium Saponified Aminoethyl-aminopropylmethyldimethoxysilane An emulsion was prepared by charging a flask with 402 grams of deionized water, 66 grams of ARQUAD T-27W an N-alkyl trimethyl ammonium chloride cationic surfactant sold by Akzo Chemicals Incorporated and 262.5 grams of a blend of dodecamethylcyclohexasiloxane, decamethylcyclopentasiloxane and octamethylcyclotetrasiloxane. The contents of the flask were mixed for 20 minutes before processing the material through a homogenizer shear device using two passes at 7500 psi (51,711 kPa). The sheared material in the amount of 730.5 grams was added to a three-neck one liter flask, heated to 84°C. with stirring and 10.82 grams of the dipotassium aminoethyl-aminopropylmethylsilanolate prepared in Example 11 was added to the flask. The contents of the flask were mixed at 84°C. for 8.75 hours before cooling to 40°C., at which point the contents were neutralized with acetic acid to a pH of 7.0 to 7.5. Then 12.75 grams of a nonionic alkylphenoxypolyoxyethylene ethanol surfactant MAKON 10 sold by the Stephan Company of Northfield Illinois was added to stabilize the emulsion. The product was a white emulsion having a mean particle size of siloxane droplets of 177.1 nanometers as determined by measurement on a NICOMP™ Particle Size Analyzer. The viscosity of the siloxane polymer was measured to be 12,700 centistokes (mm 2 /s) at 25°C. by solvent extraction of the siloxane from the emulsion water phase and then removing the solvent prior to measurement on a Brookfield Viscometer. Surprisingly and quite unexpectedly, it has been found that silicone emulsions prepared according to the methods of this invention, provide an elastomeric product. Thus, the silicone emulsion produces an elastomeric product when water is removed under ambient conditions. When the silicone emulsion is spread out to form a coating, the water evaporates to leave a cured silicone elastomer. Heating the silicone emulsion can produce the elastomeric product and other methods of removal of water other than evaporation can be employed, such as coagulation. Preferably however, films are prepared and cast from the silicone emulsions by spreading the silicone emulsion and allowing the water to evaporate at room temperature. Such films find utility as coatings for substrates to impart water repellent properties. Examples 14 and 15 are set forth below to illustrate this alternate embodiment of the invention. EXAMPLE 14 Twenty-five grams of the emulsion prepared according to Example 4 were placed in a 100 X 15 millimeter standard polystyrene Petri dish and allowed to dry at room temperature for 72 hours. Upon removal of the water by evaporation, a one millimeter thick white film resulted. The whitish film was not sticky to the touch and could be peeled cleanly away from the dish. This soft rubbery film was removed from the dish and was observed to have elastomeric characteristics, in that the film could be stretched slightly with full recovery upon release. EXAMPLE 15 Twenty-five grams of the emulsion prepared according to Example 7 were placed in a 100 X 15 millimeter standard polystyrene Petri dish and allowed to dry at room temperature for 72 hours. Upon removal of the water by evaporation, a one millimeter thick white film resulted. The whitish film was not sticky to the touch and could be peeled cleanly away from the dish. This soft rubbery film was removed from the dish and was observed to have elastomeric characteristics, in that the film could be stretched slightly with full recovery upon replease.

Claims: A method of making a silicone emulsion including the steps of (i) forming a mixture comprising water, a cyclic siloxane, a nonionic surfactant and a cationic surfactant; (ii) adding to the mixture a polymerization initiator which is a silanolate or an organosilanolate; (iii) heating the mixture; (iv) agitating the heated mixture; and (v) allowing the cyclic siloxane to polymerize until an emulsion is formed. A method according to claim 1 in which the polymerization initiator is a compound selected from the group consisting of sodium trimethylsilanolate NaOSi(CH 3 ) 3 , sodium triphenylsilanolate (C 6 H 5 ) 3 SiONa, disodium dimethylsilanolate (CH 3 ) 2 Si(ONa) 2 and disodium methylaminopropylsilanolate (CH 3 )[NH 2 CH 2 CH 2 CH 2 ]Si(ONa) 2 . A method according to claim 1 in which the nonionic surfactant is an ethoxylated alcohol selected from the group consisting of polyoxyethylene (4) lauryl ether, polyoxyethylene (23) lauryl ether, polyoxyethylene (2) cetyl ether, polyoxyethylene (10) cetyl ether, polyoxyethylene (20) cetyl ether, polyoxyethylene (2) stearyl ether, polyoxyethylene (10) stearyl ether, polyoxyethylene (20) stearyl ether, polyoxyethylene (21) stearyl ether, polyoxyethylene (100) stearyl ether, polyoxyethylene (2) oleyl ether, polyoxyethylene (10) oleyl ether and polyoxyethylene (20) oleyl ether. A method according to claim 1 in which the cationic surfactant is a quaternary ammonium salt selected from the group consisting of ditallowdimethyl ammonium chloride, ditallow dimethyl ammonium methyl sulfate, dihexadecyl dimethyl ammonium chloride, di(hydrogenated tallow) dimethyl ammonium chloride, dioctadecyl dimethyl ammonium chloride, dieicosyl dimethyl ammonium chloride, didocosyl dimethyl ammonium chloride, di(hydrogenated tallow) dimethyl ammonium acetate, dihexadecyl dimethyl ammonium acetate, ditallow dipropyl ammonium phosphate, ditallow dimethyl ammonium nitrate, di(coconutalkyl) dimethyl ammonium chloride, stearyl dimethyl benzyl ammonium chloride and N-alkyl-trimethyl ammonium chlorides. A method according to claim 1 in which the mixture is heated to a temperature within the range of 50 to less than 95°C. and the cyclic siloxane is allowed to polymerize for a period of time of less than five hours inclusive. A method of making a silicone emulsion including the steps of (i) forming a mixture comprising water, a cyclic siloxane and a cationic surfactant; (ii) adding to the mixture a polymerization initiator which is a silanolate or an organosilanolate; (iii) heating the mixture; (iv) agitating the heated mixture; and (v) allowing the cyclic siloxane to polymerize until an emulsion is formed.

Inventors: KOSAL JEFFREY ALAN, KOSAL, JEFFREY ALAN
Applicants: DOW CORNING, DOW CORNING CORPORATION
Application year: 1995
Main classification: C08G77
IPC codes: A61K8, C08L83, C08G77, A61Q5