Patent Application
20120027708
This invention relates to the polymerization of organopolysiloxanes to form organopolysiloxanes of increased molecular weight and to the organopolysiloxane compositions thus produced.
Organopolysiloxanes have many uses in plastics compositions, lubricants, personal care products such as cosmetics, construction products and household care compositions. For many of these applications high molecular weight organopolysiloxanes have the best physical properties. However high molecular weight organopolysiloxanes are difficult to compound. In particular they are often difficult to disperse in a desired matrix, for example a thermoplastic resin matrix, due to their high viscosity and/or tackiness, and are often not miscible with organic ingredients.
WO-A-2006/106362 describes preparing a diluted organopolysiloxane containing polymer by the polycondensation of siloxane containing monomers and/or oligomers which comprise condensable groups in the presence of an organopolysiloxane and/or an organic based diluent material, a suitable catalyst and optionally an end-blocking agent; and where required quenching the polymerisation process. The diluent material is substantially retained within the resulting diluted organopolysiloxane. WO-A-2008/045427 describes a method of making a silicone oil-in-water emulsion comprising the further steps of introducing one or more surfactants into the diluted organopolysiloxane to form a homogenous oil phase, adding 0.1-10 percent by weight water to the homogenous oil phase to form a water-in-oil emulsion, applying shear to the water-in-oil emulsion to cause inversion of the water-in-oil emulsion to an oil-in-water emulsion; and optionally diluting the oil-in-water emulsion by adding more water. US7041088 discloses a coating composition comprising a polydimethylsiloxane and polypropylene wax without teaching polymerisation. US2005/0143282 discloses a blend or an organic wax with a polyorganosiloxane without teaching polymerisation. U.S. Pat. No. 6,258,891 discloses polymerising an organosiloxane monomer (DMS) in admixture with a molten PE wax during the polymerisation thereby forming a block PE-PDMS in PE. U.S. Pat. No. 5,403,909 discloses catalysis of organopolysiloxanes using phosphazenes.
A method of polymerizing an organopolysiloxane according to the present invention is characterized in that the organopolysiloxane is in admixture with a molten wax during the polymerization, thereby forming a blend of the wax with an organopolysiloxane of increased molecular weight.
The invention includes a blend of a wax with an organopolysiloxane which has been formed by polymerization in the presence of the wax.
The blend of wax with increased molecular weight organopolysiloxane produced by the present invention is different from the diluted organopolysiloxane produced according to WO-A-2006/106362 and has advantages in many uses. The diluent material used in WO-A-2006/106362 is a liquid, whereas the wax used in the present invention is solid at ambient temperature. The liquid diluent of WO-A-2006/106362 acts as an extender or plasticizer in the diluted organopolysiloxane, so that compositions containing the diluted organopolysiloxane are softened. The diluent needs to be compatible with the organopolysiloxane since otherwise it will exude out of the composition with time. This can for example appear as surface bleeding of a sealant. The wax has no or much less softening effect and no tendency to bleed out of the siloxane below its melting point. While softening is desirable for some uses, the harder composition containing wax has advantages for use in thermoplastic resin compositions, lubricants, cosmetics such as lipstick and building material components.
The organopolysiloxane starting material is preferably an organopolysiloxane containing at least one hydroxyl or hydrolysable group bonded to silicon and is preferably polymerized by a process comprising siloxane condensation. The organopolysiloxane starting material can for example be a substantially linear organopolysiloxane containing on average more than one hydroxyl or hydrolysable group bonded to silicon, preferably terminal hydroxyl or hydrolysable groups. The organopolysiloxane can for example have the general formula
X1-A′-X2 (1)
where X1 and X2 areindependently selected from silicon containing groups which contain hydroxyl or hydrolysable substituents and A′ represents a polymer chain. Examples of X1 or X2 groups incorporating hydroxyl and/or hydrolysable substituents include groups terminating as described below:
—Si(OH)3, —(Ra)Si(OH)2, —(Ra)2SiOH, —RaSi(ORb)2, —Si(ORb)3, —Ra2SiORb or —Ra2Si—Rc—SiRdp(ORb)3-p where each Ra independently represents a monovalent hydrocarbyl group, for example, an alkyl group, in particular having from 1 to 8 carbon atoms, (and is preferably methyl); each Rb and Rd group is independently an alkyl or alkoxy group in which the alkyl groups suitably have up to 6 carbon atoms; Rc is a divalent hydrocarbon group which may be interrupted by one or more siloxane spacers having up to six silicon atoms; and p has the value 0, 1 or 2. End blocking groups of the formula —(Ra)2SiOH may be particularly preferred. The linear organopolysiloxane can include a small amount, for example less than 20%, of unreactive endblocking groups of the formula Ra3SiO1/2.
The polymer chain A′ is preferably a polydiorganosiloxane chain comprising siloxane units of formula (2)
—(R22SiO)— (2)
in which each R2 is independently an organic group such as a hydrocarbon group having from 1 to 18 carbon atoms, a substituted hydrocarbon group having from 1 to 18 carbon atoms or a hydrocarbonoxy group having up to 18 carbon atoms.
Examples of hydrocarbon groups R2 include methyl, ethyl, propyl, butyl, vinyl, cyclohexyl, phenyl and tolyl groups. Substituted hydrocarbon groups have one or more hydrogen atoms in a hydrocarbon group replaced with another substituent, for example a halogen atom such as chlorine, fluorine, bromine or iodine, an oxygen atom containing group such as acrylic, methacrylic, alkoxy or carboxyl, a nitrogen atom containing group such as an amino, amido or cyano group, or a sulphur atom containing group such as a mercapto group. Examples of substituted hydrocarbon groups include a propyl group substituted with chlorine or fluorine such as 3,3,3-trifluoropropyl, chlorophenyl, beta-(perfluorobutyl)ethyl or chlorocyclohexyl group. Preferably, at least some and more preferably substantially all of the groups R2 are methyl. Preferably the polydiorganosiloxanes are polydialkylsiloxanes, most preferably polydimethylsiloxanes.
Polydiorganosiloxanes comprising units of the formula (2) may be homopolymers or copolymers. Mixtures of different polydiorganosiloxanes are also suitable. In the case of polydiorganosiloxane co-polymers the polymeric chain may comprise a combination of blocks made from chains of units depicted in figure (2) above where the two R2 groups are:
both alkyl groups (preferably both methyl or ethyl), or
alkyl and phenyl groups, or
alkyl and fluoropropyl, or
alkyl and vinyl or
alkyl and hydrogen groups.
Typically at least one block will comprise siloxane units in which both R2 groups are alkyl groups.
The substantially linear organopolysiloxane starting material containing at least one hydroxyl or hydrolysable group bonded to silicon generally has a degree of polymerization such that its viscosity is between 5 mPa·s and 5000 mPa·s., preferably between 10 mPa·s and 500 mPa·s. Preferably the substantially linear organopolysiloxane is a polydimethylsiloxane having terminal hydroxyl groups bonded to silicon and having a viscosity between 10 mPa·s and 500 mPa·s.
The polymer (A′) used as substantially linear polyorganosiloxane starting material may alternatively have a block copolymeric backbone comprising at least one block of siloxane groups of the type depicted in formula (2) above and at least one block comprising any suitable organic polymer chain. Examples of suitable organic polymer chains are polyacrylic, polyisobutylene and polyether chains.
According to one aspect of the invention such a substantially linear organopolysiloxane containing at least one hydroxyl or hydrolysable group bonded to silicon is polymerized by catalysed condensation of the hydroxyl or hydrolysable groups to form siloxane bonds. The substantially linear organopolysiloxane can for example be substantially the only organopolysiloxane starting material used.
Alternatively the organopolysiloxane starting material can be a cyclic organopolysiloxane, which can be polymerized by a catalysed process of ring opening of the cyclic organopolysiloxane to form siloxane bonds. The cyclic organopolysiloxane used in such a process can for example be octamethylcyclotetrasiloxane or decamethylcyclopentasiloxane.
The cyclic organopolysiloxane can be the only siloxane material in the polymerization reaction or can be used together with an organosilicon material which will react with the ring opened cyclic organopolysiloxane, for example a silane or siloxane material containing at least one hydroxyl or hydrolysable group bonded to silicon. This silane or siloxane material can for example be an organopolysiloxane such as a substantially linear organopolysiloxane containing at least one hydroxyl or hydrolysable group bonded to silicon. If such a substantially linear organopolysiloxane containing at least one hydroxyl or hydrolysable group bonded to silicon and a cyclic organopolysiloxane are polymerized together, they can for example be present in a weight ratio of 10:1 to 1:5 in the polymerization reaction mixture. Polymerisation proceeds by a catalysed process of ring opening of the cyclic organopolysiloxane and condensation of the ring opened product with the substantially linear organopolysiloxane or other silane or siloxane material containing at least one hydroxyl or hydrolysable group bonded to silicon.
According to another aspect of the invention, the organopolysiloxane starting material is a mixture of a substantially linear organopolysiloxane containing at least one hydroxyl or hydrolysable group bonded to silicon and an alkoxysilane having an average of more than two Si-bonded alkoxy groups per molecule. Such a mixture can be polymerized by catalysed siloxane condensation of the substantially linear organopolysiloxane with the alkoxysilane to form a branched organopolysiloxane structure.
The alkoxysilane which is reacted with the linear organopolysiloxane generally contains an average of more than 2 silicon-bonded alkoxy groups per molecule. The alkoxy groups preferably each have 1 to 4 carbon atoms and most preferably are methyl or ethyl groups. The alkoxysilane can for example comprise a trialkoxysilane of the formula R′Si(OR)3, where R represents an alkyl group having 1 to 4 carbon atoms and R′ represents a monovalent hydrocarbon or substituted hydrocarbon group having 1 to 18 carbon atoms. Examples of such groups R′ include alkyl groups, for example methyl, ethyl, propyl, butyl, hexyl, octyl, 2-ethylhexyl, lauryl or stearyl; cycloalkyl groups, for example cyclopentyl or cyclohexyl); alkenyl groups, for example vinyl, allyl or hexenyl; aryl groups, for example phenyl or tolyl; aralkyl groups, for example 2-phenylethyl; and groups obtained by replacing all or part of the hydrogen in the preceding organic groups with halogen, for example 3,3,3-trifluoropropyl. Examples of preferred trialkoxysilanes include methyltrimethoxysilane, methyltriethoxysilane, isobutyltrimethoxysilane, n-octyltriethoxysilane, n-octyltrimethoxysilane, ethyltrimethoxysilane, ethyltriethoxysilane, vinyltrimethoxysilane, vinyltriethoxysilane, phenyltrimethoxysilane and 3,3,3-trifluoropropyltrimethoxysilane. Trialkoxysilanes having a long chain alkyl group R′ having for example 6 to 18 carbon atoms, for example n-octyltrimethoxysilane, react with the linear organopolysiloxane to form a branched organopolysiloxane having a long chain alkyl group, for example an octyl group, at the branching point. The presence of such a long chain alkyl group increases the compatibility of the branched organopolysiloxane with organic materials, for example hydrocarbon solvents or organic polymers.
The alkoxysilane can alternatively be a tetraalkoxysilane such as tetraethoxysilane (tetraethyl orthosilicate). Reaction of the linear organoplysiloxane with a tetraalkoxysilane can form a branched organopolysiloxane having Si-alkoxy functionality in the polysiloxane chain as well as branching.
The alkoxysilane can be a partially condensed alkoxysilane in which some alkoxy groups have been hydrolysed and condensed to form siloxane linkages and some alkoxy groups remain bonded to silicon. Such a partially condensed alkoxysilane preferably contains on average more than two alkoxy groups per molecule bonded to silicon. The alkoxysilane can for example be an oligomeric partially condensed trialkoxysilane. Such an oligomer may have a branched structure as well as Si-alkoxy groups to provide further branching sites. Tetraalkoxysilanes can also be used in partially condensed form; for example partially condensed tetraethoxysilane containing SiO2 branching units is widely available.
The alkoxysilane and the substantially linear organopolysiloxane containing at least one hydroxyl or hydrolysable group bonded to silicon are preferably reacted in amounts such that the molar ratio of Si-bonded alkoxy groups in the alkoxysilane to hydroxyl or hydrolysable groups in the substantially linear organopolysiloxane is from 1:100 to 1:1, more preferably 1:40 to 1:2.
The catalyst for the polymerization of the organopolysiloxane is preferably a phosphazene catalyst. Phosphazene catalysts are effective catalysts both for siloxane condensation and for ring opening polymerization of cyclic organopolysiloxanes. The phosphazene catalyst generally contains at least one —(N═P<)— unit and is usually an oligomer having up to 10 such phosphazene units, for example having an average of from 1.5 up to 5 phosphazene units. The phosphazene catalyst can for example be a halophosphazene, particularly a chlorophosphazene (phosphonitrile chloride), an oxygen-containing halophosphazene, a phosphazene base or an ionic derivative of a phosphazene such as a phosphazenium salt, particularly an ionic derivative of a phosphonitrile halide such as a perchlorooligophosphazenium salt.
One particularly suitable type of phosphazene catalyst is an oxygen-containing halophosphazene, particularly an oxygen-containing chlorophosphazene. Such an oxygen-containing chlorophosphazene can for example have the formula Cl(PCl2═N)n—P(O)Cl or HO(PCl2═N)n—P(O)Cl2. The average value of n can for example be in the range 1 to 10, particularly 1 to 5. The catalyst may also comprise tautomers of the catalyst of the formula HO(PCl2═N)n—P(O)Cl2. Another type of suitable oxygen-containing chlorophosphazene has the formula Z′O(PCl2═N)n—P(O)Cl2 in which Z′ represents an organosilicon radical bonded to phosphorus via oxygen, for example a phosphazene catalyst of the formula R″3SiO(PCl2═N)n—P(O)Cl2 where each R″ represents a monovalent hydrocarbon or substituted hydrocarbon group having 1 to 18 carbon atoms. The catalyst may also comprise condensation products of such an organosilicon-containing phosphazene. All or some of the chlorine atoms in any of the above oxygen-containing phosphazenes can be replaced by radicals Q, in which Q represents the hydroxyl group, monovalent organic radicals, such as alkoxy radicals or aryloxy radicals, halogen atoms other than chlorine, organosilicon radicals and phosphorus-containing radicals, although this is not preferred.
Another suitable type of phosphazene catalyst is a perchlorooligophosphazenium salt of the formula
[Cl3P—(N═PCl2)nCl]+Z
where n has an average value in the range 1 to 10 and Z represents an anion. The anion is preferably a complex anion and can for example be of the formula MXv+1 in which M is an element having an electronegativity on Pauling's scale of from 1.0 to 2.0 and valency v and X is a halogen atom. The element M can for example be phosphorus or antimony. The anion Z can alternatively be a complex anion of the formula [MXv−y+1R3y]— wherein R3 is an alkyl group having 1 to 12 carbon atoms and y has a value between 0 and v, as described in U.S. Pat. No. 5,457,220.
The phosphazene catalyst can alternatively be a phosphazene base, particularly an aminated phosphazene as described in U.S. Pat. No. 6,001,928, U.S. Pat. No. 6,054,548 or U.S. Pat. No. 6,448,196. Such a phosphazene base can be formed by reaction of a perchlorooligophosphazenium salt with a secondary amine followed by ion exchange reaction with a basic nucleophile. The secondary amine is for example of the formula HNR42, and some or all of the chlorophosphazene oligomer are replaced by —NR42 groups.
The phosphazene catalyst is typically present at 1 or 2 up to 200 parts per million based on the weight of organopolysiloxane starting materials, for example at 5 to 50 parts per million. Phosphazene catalysts have the advantage that the content of undesired low molecular weight cyclic silicones in the polymerisation product is low.
Alternative catalysts which can be used for the organopolysiloxane polymerization include any of those known to catalyse siloxane condensation, such as protic acids, Lewis acids, organic and inorganic bases, metal salts and organometallic complexes. Condensation specific catalysts are preferred. These include acidic condensation catalysts of the formula R20SO3H in which R20 represents an alkyl group preferably having from 6 to 18 carbon atoms such as for example a hexyl or dodecyl group, an aryl group such as a phenyl group or an alkaryl group such as dinonyl- or didoecyl-naphthyl, for example the catalyst can be dodecylbenzenesulphonic acid. Other condensation specific catalysts include n-hexylamine, tetramethylguanidine, carboxylates of rubidium or caesium, and hydroxides of magnesium, calcium or strontium.
Further alternative catalysts include condensation catalysts incorporating tin, lead, antimony, iron, cadmium, barium, manganese, zinc, chromium, cobalt, nickel, aluminium, gallium or germanium and zirconium. Examples include metal triflates, organic tin metal catalysts such as triethyltin tartrate, tin octoate, tin oleate, tin naphthate, butyltintri-2-ethylhexoate, tinbutyrate, carbomethoxyphenyl tin trisuberate, isobutyltintriceroate, and diorganotin salts especially diorganotin dicarboxylate compounds such as dibutyltin dilaurate, dimethyltin dibutyrate, dibutyltin dimethoxide, dibutyltin diacetate, or dimethyltin bisneodecanoate.
A titanate or zirconate based catalyst can be used, for example a compound according to the general formula Ti[OR22]4 where each R22 may be the same or different and represents a monovalent, primary, secondary or tertiary aliphatic hydrocarbon group which may be linear or branched containing from 1 to 10 carbon atoms. The titanate may be chelated, for example with an alkyl acetylacetonate such as methyl or ethyl acetylacetonate.
A further alternative catalyst which might be used as the catalyst in the present invention is any suitable compound providing a source of anions comprising at least one quadri-substituted boron atom and protons capable of interaction with at least one silanol group as defined in WO 01/79330, for example tetrakis (pentafluoro phenyl) borate anion.
Alternatively polymerization of the organopolysiloxane may be by a hydrosilylation reaction between an unsaturated organic group, for example an alkenyl or alkynyl group, and an Si—H group in the presence of a suitable catalyst. In this route suitable silanes may be utilised as well as siloxane containing monomers and/or oligomers. Thus the organopolysiloxane can comprise an organopolysiloxane containing alkenyl or alkynyl groups which is polymerized with a silane or siloxane material having Si—H groups by a hydrosilylation reaction, or an organopolysiloxane having Si—H groups which is polymerized with an organic compound containing at least two alkenyl or alkynyl groups by a hydrosilylation reaction. The hydrosilylation reaction is generally effected in the presence of a platinum group catalyst.
The organopolysiloxane containing alkenyl or alkynyl groups can be linear or branched, and generally comprises Si-bonded organic groups which are hydrocarbon or substituted hydrocarbon groups containing 1 to 18 carbon atoms, at least two of which are alkenyl or alkynyl groups. The organopolysiloxane may for example contain the alkenyl or alkynyl groups as terminal groups. Each alkenyl or alkenyl group preferably has a terminal double bond. Examples of preferred alkenyl groups are H2C═CH—, H2C═CHCH2—, H2C═C(CH3)CH2—, H2C═CHCH2CH2—, H2C═CHCH2CH2CH2—, and H2C═CHCH2CH2CH2CH2—. Examples of alkynyl groups include HC≡C— and HC≡CCH2—. The other organic groups of the organopolysiloxane can for example be selected from alkyl groups such as methyl, ethyl, propyl, butyl, pentyl, hexyl, heptyl, octyl, undecyl, and octadecyl; cycloalkyl such as cyclohexyl; aryl such as phenyl, tolyl, xylyl, benzyl, and 2-phenylethyl; and halogenated hydrocarbon groups such as 3,3,3-trifiuoropropyl, 3-chloropropyl, and dichlorophenyl. Methyl groups are often preferred. The organopolysiloxane can for example be an alkeyl-terminated linear or branched polydimethylsiloxane.
The organopolysiloxane having Si—H groups can be linear or branched. The other organic groups of the organopolysiloxane can for example be selected from alkyl groups such as methyl, ethyl, propyl, butyl, pentyl, hexyl, heptyl, octyl, undecyl, and octadecyl; cycloalkyl such as cyclohexyl; aryl such as phenyl, tolyl, xylyl, benzyl, and 2-phenylethyl; and halogenated hydrocarbon groups such as 3,3,3-trifiuoropropyl, 3-chloropropyl, and dichlorophenyl. Methyl groups are often preferred. The Si—H groups can be terminal, for example the organopolysiloxane can have dimethylsilyl terminal groups, and/or the Si—H groups can be along the polymer chain, for example the organopolysiloxane can comprise methylhydrogensiloxane units. The organopolysiloxane having Si—H groups can for example be a poly(methylhydrogen)siloxane or a dimethylsiloxane methylhydrogensiloxane copolymer.
If polymerization by hydrosilylation is used, an organopolysiloxane containing alkenyl or alkynyl groups as described above is preferably reacted with an organopolysiloxane having Si—H groups as described above.
The organopolysiloxane containing alkenyl or alkynyl groups can alternatively or additionally be polymerized with a silane containing at least one Si—H group. Examples of such silanes include halosilanes such as trichlorosilane, methyldichlorosilane, dimethylchlorosilane, and phenyldichlorosilane, and alkoxysilanes such as trimethoxy silane, triethoxy silane, methyl diethoxy silane, methyl dimethoxy silane and phenyldimethoxy silane.
The organopolysiloxane containing Si—H groups can alternatively or additionally be polymerized with an organic compound containing at least two alkenyl or alkynyl groups. The alkenyl or alkynyl groups should not be conjugated and are preferably terminal groups. Suitable organic compounds include for example 1,5-hexadiene and 1,7-octadiene.
The catalyst for the hydrosilylation reaction is generally a platinum group catalyst, that is a metal selected from platinum, rhodium, palladium, osmium, iridium, or ruthenium or a compound of one of those metals. Examples of catalysts comprising platinum include chloroplatinic acid, alcohol modified chloroplatinic acids, olefin complexes of chloroplatinic acid, complexes of chloroplatinic acid and divinyltetramethyldisiloxane, fine platinum particles adsorbed on carbon carriers, platinum supported on metal oxide carriers such as Pt(Al2O3), platinum black, platinum acetylacetonate, platinous halides exemplified by PtCl2, PtCl4, Pt(CN)2, and complexes of platinous halides with unsaturated compounds exemplified by ethylene, propylene, and organovinylsiloxanes. One preferred platinum catalyst is Karstedt's catalyst, which is a platinum divinyl tetramethyl disiloxane complex typically containing one weight percent of platinum in a solvent such as toluene. Another preferred platinum catalyst is a reaction product of chloroplatinic acid and an organosilicon compound containing terminal aliphatic unsaturation as described in U.S. Pat. No. 3,419,593. A further preferred catalyst is a neutralized complex of platinous chloride and divinyl tetramethyl disiloxane, as described in U.S. Pat. No. 5,175,325.
Examples of hydrosilylation catalyst comprising ruthenium include RhCl3(Bu2S)3 and ruthenium carbonyl compounds such as ruthenium 1,1,1-trifluoroacetylacetonate, ruthenium acetylacetonate and triruthinium dodecacarbonyl or a ruthenium 1,3-ketoenolate. Examples of rhodium catalysts include [Rh(O2CCH3)2]2. Rh(O2CCH3)3, Rh2(C8H15O2)4, Rh(C5H7O2)3, Rh(C5H7O2)(CO)2, and Rh(CO)[Ph3P](C5H7O2). Examples of iridium catalysts include IrCOOCCH3)3 and Ir(C5H7O2)S.
The concentration of the hydrosilylation catalyst in the composition is usually capable of providing the equivalent of at least 1 part per million of elemental platinum group metal by weight based on the organopolysiloxane. A catalyst concentration providing the equivalent of about 3-50 parts per million of elemental platinum group metal is generally the amount preferred.
Typically the hydrosilylation polymerisation is carried out using approximately a 1:1 molar ratio of Si—H groups to alkenyl alkynyl groups. The material containing alkenyl groups may be used in slight excess to ensure all the Si—H is consumed in the reaction.
The extent of polymerization during the process of the invention is preferably such that the organopolysiloxane of increased molecular weight produced has a weight average molecular weight Mw at least five times, more preferably at least ten times the weight average molecular weight of the starting organopolysiloxane. The Mw can be measured by gel permeation chromatography (GPC). The Mw of the organopolysiloxane of increased molecular weight produced is preferably at least 10,000, more preferably at least 100,000, and may be as high as 1,000,000 or more.
By a wax we mean a material which is plastic or malleable at temperatures of 15-20° C., has a melting point of at least 20° C., and has a low viscosity when melted. Examples for waxes described in the Kirk-Othmer encyclopaedia of chemical technology (Article on Waxes by Claude Leray, John Wiley & Sons, Inc. 2006).
The wax present during the organopolysiloxane polymerization generally has a melting point of at least 20° C. and preferably has a melting point in the range 30 to 100° C., more preferably 40 to 90° C. The wax can be an organic wax containing no silicon or can be a silicone wax. For uses in which increasing the compatibility of the organopolysiloxane formulation with organic materials is important, organic waxes are usually preferred although silicone waxes containing long chain organic substituents can also increase compatibility.
The wax can for example be a hydrocarbon wax such as a petroleum-derived wax, particularly a paraffin wax or microcrystalline wax, a Fischer-Tropsch wax, ceresin wax, a polyethylene wax or a mixture thereof. Paraffin waxes contain predominantly straight-chain hydrocarbons with an average chain length of 20 to 30 carbon atoms. Examples of paraffin waxes are sold by IgiWax under the trade mark Parafflex, such as Parafflex 4750 A granules and Parafflex 4797A. Microcrystalline wax contains a higher percentage of branched hydrocarbons and naphthenic hydrocarbons. Examples of microcrystalline waxes are sold by IgiWax under the trade mark Microsere, for example Microsere 5981A. Other organic hydrocarbon waxes that can be used are montan wax (also known as lignite-wax), ozokerite or slag wax.
The wax can alternatively be a wax comprising carboxylic esters. Many natural waxes such as beeswax, lanolin, tallow, carnauba and candelilla, as well as tribehenin and waxes derived from plant seeds, fruits, nuts or kernel, such as palm wax, rice bran wax or soy wax, comprise a mixture of esters with free acids and/or alcohols. Examples of ester waxes are palm waxes derived from palm oil sold by IgiWax under the trade names RD2778A and RD2779A. Some of the softer waxes are referred to as ‘butter’. These type of products are frequently used in skin care applications and are for example derived from oilseeds as mango butter, shea butter or cocoa butter. Other examples are illipe, cupuacu, murumuru, sal and kokum butter. Such a butter can be used as all or part of the wax of the invention, provided that the wax has a melting point of at least 20° C. In general butters can be defined by having a titer point of below 40.5° C. but above 20° C. (“Oil of nature” by J. O'Lenick according to AOCS method Tr 1a-64T).
The wax can alternatively be a long chain fatty acid, a long chain fatty alcohol, a long chain fatty amine, a long chain fatty amide, an ethoxylated fatty acid or fatty alcohol, or a long chain alkyl phenol. In general the long chain of the fatty acid, alcohol, amine or amide is an alkyl group of at least 12 and preferably at least 16 carbon atoms, often up to 30 or more carbon atoms.
The wax can alternatively be a polyether wax, for example a solid polyether polyol or a waxy polyvinyl ether such as that sold by BASF under the trade mark Lumax V, or a polyetherester.
Examples of silicone waxes are polysiloxanes containing hydrocarbon substituents having 12 or more carbon atoms. The polysiloxane is preferably a polydiorganosiloxane comprising methyl alkyl siloxane units ((CH3)(R3)Si02/2), where R3 is a long chain alkyl group having 12 or more, preferably 16 to 100 carbon atoms, optionally together with dimethyl siloxane units or units of the formula ((CH3)(R4)SiO2/2) where R4 is an alkyl group having 1-11 carbon atoms, for example ethyl, a cycloalkyl group such as 2-cyclohexylethyl, a haloalkyl group, an aryl group such as phenyl or an aralkyl group such as 2-phenylpropyl, 2-phenylethyl or 2-(t-butylphenylethyl). The methyl group of the above siloxane units could be replaced by ethyl or another lower alkyl group if desired. The long chain alkyl group R3 can optionally be substituted by polar substituents such as amino, amido, alcohol, alkoxy, or ester groups. Preferably at least 20% of the silicon atoms in the silicone wax, and most preferably at least 50%, have an alkyl substituent having 16 to 100 carbon atoms, most preferably 20 to 36 carbon atoms.
Mixtures of different types of waxes can be used, for example a blend of an ester wax with a hydrocarbon wax.
The wax can be present during the polymerization in any amount from 1 or 5% based on the organopolysiloxane up to 150 or 200% based on the organopolysiloxane. Preferably the weight ratio of organopolysiloxane to wax present during the polymerization is from 95:5 to 40:60. The wax can be melted before contacting the organopolysiloxane, or solid wax can be mixed with the organopolysiloxane and heated to melt the wax while applying shear to mix.
The polymerization of the organopolysiloxane is carried out at a temperature above the melting point of the wax. Preferably the temperature of polymerization is from 5° C. to 30° C. above the melting point of the wax, for example the temperature of polymerization can be in the range 50° C. to 120° C. Most waxes, particularly organic waxes such as hydrocarbon waxes and ester waxes, are not miscible with organopolysiloxanes such as a hydroxyl-tipped polydimethylsiloxane. The wax and the silicones are thus present as a liquid/liquid dispersion and the polymerisation is therefore a dispersion polymerization.
The polymerization reaction can be terminated when a desired degree of polymerization has been reached. This can be determined for example by monitoring the viscosity of the polymerization reaction mixture or the torque required to mix it. Polymerisation catalysed by the preferred phosphazene catalysts can be terminated by adding a neutralizing agent, for example a trialkylamine such as trihexylamine in the case of the catalysts described in U.S. Pat. No. 5,457,220. The time for which polymerization is carried out can be varied within wide limits, for example from 1 or 2 minutes up to 10 hours or more. Polymerisation catalysed by the preferred phosphazene catalysts is usually carried out for 2 to 150 minutes.
An inert liquid diluent can be present during the polymerization if desired. A diluent can be a silicone based and/or organic based diluent and is generally chosen to have no groups reactive with the organopolysiloxane. The diluent if used will usually be chosen from materials whose presence is desired as an extender or plasticizer in the end product formulation based on the wax silicone blend produced.
Any suitable diluent or combination of diluents may be used in the reaction mixture. In general any of the extenders used in WO-A-2006/106362 can be used. These include each of the following alone or in combination with others from the list:
Preferred diluents include the mineral oil fractions, alkylcycloaliphatic compounds and alkybenzenes including polyalkylbenzenes. Any suitable mixture of mineral oil fractions may be used as diluent but high molecular weight extenders, for example having a molecular weight above 220, are particularly preferred. Examples include alkylcyclohexanes of molecular weight above 220), paraffinic hydrocarbons and mixtures thereof containing from 1 to 99%, preferably from 15 to 80% n-paraffinic and/or isoparaffinic hydrocarbons (linear branched paraffinic) and 1 to 99%, preferably 85 to 20% cyclic hydrocarbons (naphthenic) and a maximum of 3%, preferably a maximum of 1% aromatic carbon atoms. The cyclic paraffinic hydrocarbons (naphthenics) may contain cyclic and/or polycyclic hydrocarbons.
Alternative preferred diluents suitable for retaining in many products as an extender or plasticiser comprise non-mineral based natural oils, i.e. oils derived from animals, seeds or nuts and not from petroleum. Such natural oils are generally triglycerides of mixtures of fatty acids, particularly mixtures containing some unsaturated fatty acid. Diluents containing natural oils may for example be preferred for use in some personal care products. The diluent can be a derivative of a natural oil such as a transesterified vegetable oil, a boiled natural oil, a blown natural oil, or a stand oil (thermally polymerized oil).
The amount of diluent, if used, can for example be up to 60%, usually 5 to 40%, of the combined weight of wax, organopolysiloxane and diluent. The diluent may be miscible with either the siloxane, the molten wax phase of both of them. Many diluents are miscible with the wax and will reduce the melting point of the wax, although the amount of diluent is preferably not so much that it reduces the melting point of the wax below 25° C.
An “active material” can be added to the mixture of organopolysiloxane and wax before, during or after polymerisation but before the reaction product has been cooled to a paste or solid or emulsified. The “active material” is an organic material intended to have an effect in the formulation in which the polymerised organopolysiloxane is used. The active material can for example be selected from perfumes, sunscreens, antioxidants vitamins, drugs, biocides, pest repellents, catalysts, natural extracts, peptides, warming effect and cooling agents.
High molecular weight silicones are used in household care and personal care applications often in conjunction with organic active material ingredients such as perfumes or essential oil. However silicones are not compatible (miscible) with many organic active material ingredients causing problems to obtain fine and stable dispersions. Furthermore often significant amounts of the costly active material, for example perfume, are wasted during the application not contributing to the end users benefit. We have found that by polymerizing the organopolysiloxane in the presence of a wax according to the invention, we can to incorporate perfume in the blend of wax and polymerized organopolysiloxane yielding shelf stable products which release the perfume only slowly, and may be controlled to release the perfume or other active material in desired circumstances.
One example of an active material is a fragrance composition (perfume). The fragrance composition may be solid or liquid and may be a single fragrant compound, or a natural scented oil, or may be a mixture of fragrant compounds and/or natural oils. Examples of such natural oils and fragrant compounds are described in WO-A-01/25389; these natural oils and fragrant compounds are in particular those suitable for use in cleaning compositions for household or personal use, for example a powder or liquid laundry detergent, a fabric softener or an ironing aid, or for air fresheners. The fragrance composition may alternatively be a perfume for incorporation in a personal care product such as a skin cream, shampoo or face cream, or may be a flavour or aroma compound to be applied for example to food or food packaging. The fragrance composition can alternatively comprise a chemically protected fragrance compound such as a reaction product of the fragrance compound.
Perfumes generally dissolve easily in molten organic waxes. The perfume can be mixed with the wax and then heated to melt the wax, or the wax can be melted and then mixed with the perfume, or the molten wax can be mixed with the organopolysiloxane starting material and then mixed with the perfume. Alternatively the perfume can be mixed with the polysiloxane and wax during the polymerization reaction, that is after the catalyst has been added, or with the reaction product while the wax is still molten.
Alternative type of active material which can be incorporated in the wax silicone composition include sunscreen materials, antioxidants, vitamins, insect repellents and warming effect or cooling agents (materials which give a warming or cooling sensation to the skin). Examples of sunscreens include those which absorb ultraviolet light between about 290-320 nanometers (the UV-B region) such as para-aminobenzoic acid derivatives and cinnamates such as octyl methoxycinnamate or 2-ethoxyethyl p-methoxycinnamate; and those which absorb ultraviolet light in the range of 320-400 nanometers (the UV-A region) such is benzophenones and butyl methoxy dibenzoylmethane. Examples of vitamins are vitamins A and E, retinol and tocopherol. Menthol is an example of a cooling agent. These materials can be used in personal care products. Sunscreens and vitamins are used in skin creams and lotions and are released only slowly if they have been incorporated in a wax silicone blend according to the invention. Cooling agents incorporated in a wax silicone blend can be used in a skin care composition to give prolonged release of the cooling agent when the composition is rubbed into the skin. Insect repellent personal care products can for example be in the form of creams, sticks or sprays, and controlled release of the insect repellent from the personal care product is required after the product has been applied to the skin.
The invention can also be used to give controlled release of a drug (a pharmaceutically active material) by incorporating the drug in a wax silicone blend according to the invention and using this blend in a composition which is applied to the skin to dose the drug by transdermal delivery.
A further alternative type of active material which can be incorporated in the wax silicone blend is a biocide, for example to give prolonged protection against bacterial degradation of a composition including the blend or to give a prolonged biocidal effect to a substrate to which the composition has been applied.
A further alternative type of active material which can be incorporated in the wax silicone blend is a catalyst. A wax silicone blend in which a curing catalyst has been incorporated can for example be used in coatings or adhesives where controlled release is advantageous to give thorough cure without curing too rapidly.
The wax can be chosen so that the active material is released in response to a change in temperature or in the environment encountered by the wax silicone blend. For example the melting point of the wax can be chosen so that the perfume is released above the ironing temperature when the wax silicone blend is used in products for ironing aid. Alternatively the wax can be sparingly soluble in water so that the perfume is slowly released when the wax silicone blend is used in a product applied in water, for example in fabric softener. Polyethylene glycol polyether waxes for example are sparingly soluble in water.
After the polymerisation reaction is completed the reaction product can be cooled below the solidification temperature of the wax, for example down to room temperature. This yields a paste-like solid blend of the wax and the polymerized organopolysiloxane depending on the silicone to wax ratio, the hardness of the wax and the molecular weight of the organosiloxane. A high proportion of organopolysiloxane tends to form a softer paste with a higher penetration value as measured for example by a needle penetrometer according to ASTM D217-97. A higher proportion of wax forms a harder pasty solid with a lower penetration value.
The paste or solid is a very intimate dispersion of wax in organopolysiloxane or vice versa. The dispersion is surprisingly stable. We have found that many dispersions produced according to the invention are stable against macroscopic phase separation when reheated again above the melting point of the wax. We believe that the dispersion is so fine (such low particle size) that the molten wax can not coalesce in the silicone matrix. For the case of silicone dispersed in wax we believed that the high molecular weight (and therefore high viscosity) of the silicone prevents the coalescence. This stability against macroscopic separation is a kinetic phenomenon allowing the manufacturer to use and formulate the dispersion. Ultimately when heated, the dispersion will separate into the thermodynamically more stable macroscopic two phase system.
The dispersion of high molecular weight polyorganosiloxane and wax can be used for example in thermoplastic resin compositions, in lubricants, in cosmetic formulations, or in hydrophobing building material components.
The dispersion of high molecular weight polyorganosiloxane and wax can be used in paste or solid form for incorporation of silicone into thermoplastic resin compositions such as polypropylene or other thermoplastic polyolefins. Silicone plastic additives have been effectively employed for many years to improve lubricity and flow of thermoplastics. The polyorganosiloxane can improve processing and flow by providing better mold fill, reduced extruder torque, internal lubrication, more efficient mold release, faster throughput and less warpage, and can improve surface properties of the moulded product including better lubricity and slip from the reduced coefficient of friction, and/or greater mar and abrasion resistance. The improved thermoplastic resins can for example be used in automotive interior trim, domestic appliances, luggage and other items. However, incorporating liquid silicone additives into thermoplastic melts without specialized equipment poses many processing difficulties. The dispersion of polyorganosiloxane and wax produced according to the invention can be mixed more easily into the thermoplastic melt.
The dispersion of polyorganosiloxane and wax produced according to the invention can alternatively be used in lubricants. For example a solid dispersion of polyorganosiloxane in wax can be used as the basis of a solid lubricant, optionally mixed with micronised polypropylene wax, a fluoropolymer such as polytetrafluoroethylene (PTFE), molybdenum disulphide and/or graphite.
The dispersion of polyorganosiloxane and wax can be used in cosmetic formulations. For example a solid dispersion of polyorganosiloxane in wax can be used as the basis of colour cosmetics such as lipsticks, in admixture with suitable dyes and/or pigments and optionally perfume. Silicone wax dispersion in paste or solid form can be used as the basis of other colour cosmetics such as eye liner, blusher or mascara. In general the cosmetics can be either of the hydrous or anhydrous type.
The dispersion of polyorganosiloxane and wax can be used to render composite boards more hydrophobic. Composite boards are widely used in construction. Examples of such boards are gypsum board, fibre cement boards, OSB (oriented strand board) and wood particle boards, for example medium density fibreboard (MDF) such as chipboard and high density fibreboard (HDF) such as hardboard. The dispersion of polyorganosiloxane and wax can for example be applied to wood particles before application of a resin binder, or after application of binder and before the particles are pressed into board. The dispersion of polyorganosiloxane and wax can be applied to a gypsum slurry before it is pressed into board.
Formulations containing the dispersion of polyorganosiloxane and wax can contain various additives known in silicone formulations, for example “active materials” such as perfumes, sunscreens, vitamins, drugs, biocides, pest repellents, catalysts and cooling agents, or fillers, colouring agents such as dyes, pigments and shimmers, heat stabilizers, flame retardants, UV stabilizers, fungicides, or biocides, Such additives can be incorporated in the dispersion of polyorganosiloxane and wax before, after or during the mixing of the wax silicone dispersion with a thermoplastic resin. If controlled release of active materials from the emulsion compositions is desired, the active material such as perfume is preferably incorporated in the wax silicone phase by adding it to the mixture of organopolysiloxane and wax before, during or after polymerisation but before the reaction product has been cooled to a paste or solid.
In an alternative procedure, the reaction product of the polymerization of the organopolysiloxane in the presence of the wax can be emulsified in water in the presence of a surfactant. The blend of wax and silicone produced by the polymerization reaction is emulsified when the wax is molten. Preferably the reaction product is emulsified before the reaction product has cooled to a paste or solid. The reaction product is emulsified before any macroscopic phase separation has occurred.
Many personal care products such as face, hand and body creams, shampoos, colour cosmetics, mascara, foundations and sunscreen formulations are emulsions or other dispersions. They can be either of the oil-in-water (o/w) or water-in-oil (w/o) type. High molecular weight silicones are often used in personal care applications in conjunction with organics ingredients, often providing synergistic effects. However silicones are not compatible (miscible) with many organic ingredients causing problems in obtaining fine and stable dispersions. We have found that by polymerizing the silicone in the presence of an organic wax, silicone/organic dispersions can be obtained that can be stabilized in the form or an emulsion.
Any suitable surfactant or combination of surfactants may be used in emulsifying the wax silicone dispersion. The surfactant can in general be a non-ionic surfactant, a cationic surfactant, an anionic surfactant, or an amphoteric surfactant. The amount of surfactant used will vary depending on the surfactant, but generally is up to about 30 wt. % based on the polydiorganosiloxane, for example 0.2 to 20%.
Examples of nonionic surfactants include condensates of ethylene oxide with long chain fatty alcohols or fatty acids such as a C4-16 alcohol, condensates of ethylene oxide with an amine or an amide, condensation products of ethylene and propylene oxide, esters of glycerol, sucrose, sorbitol, fatty acid alkylol amides, sucrose esters, fluoro-surfactants, fatty amine oxides, polyoxyalkylene alkyl ethers such as polyethylene glycol long chain (12-14C) alkyl ether, polyoxyalkylene sorbitan ethers, polyoxyalkylene alkoxylate esters, polyoxyalkylene alkylphenol ethers, ethylene glycol propylene glycol copolymers and alkylpolysaccharides, for example materials of the structure R24O—(R25O)s-(G)twherein R24 represents a linear or branched alkyl group, a linear or branched alkenyl group or an alkylphenyl group, R25 represents an alkylene group, G represents a reduced sugar, s denotes 0 or a positive integer and t represent a positive integer as described in U.S. Pat. No. 5,035,832. Alternative nonionic surfactants include polymeric surfactants such as polyvinyl alcohol (PVA) and polyvinylmethylether. Surfactants containing silicon atoms can also be used.
Representative examples of suitable commercially available nonionic surfactants include polyoxyethylene fatty alcohols sold under the tradename BRIJ by Uniqema (ICI Surfactants), Wilmington, Del. Some examples are BRIJ 35 Liquid, an ethoxylated alcohol known as polyoxyethylene (23) lauryl ether, and BRIJ 30, another ethoxylated alcohol known as polyoxyethylene (4) lauryl ether. Similar materials are sold by Croda Europe under the trade marks Volpo L23 and Volpo L4. Some additional nonionic surfactants include ethoxylated alcohols sold under the trademark TERGITOL by The Dow Chemical Company, Midland, Mich., such as TERGITOL TMN-6, an ethoxylated alcohol known as ethoxylated trimethylnonanol; and various ethoxylated alcohols, i.e., C12-C14 secondary alcohol ethoxylates, sold under the trademarks TERGITOL 15-S-5, TERGITOL 15-S-12, TERGITOL 15-S-15, and TERGITOL 15-S-40.
Examples of suitable amphoteric surfactants include imidazoline compounds, alkylaminoacid salts, and betaines. Specific examples include cocamidopropyl betaine, cocamidopropyl hydroxysulfate, cocobetaine, sodium cocoamidoacetate, cocodimethyl betaine, N-coco-3-aminobutyric acid and imidazolinium carboxyl compounds.
Examples of cationic surfactants include quaternary ammonium hydroxides such as octyl trimethyl ammonium hydroxide, dodecyl trimethyl ammonium hydroxide, hexadecyl trimethyl ammonium hydroxide, octyl dimethyl benzyl ammonium hydroxide, decyl dimethyl benzyl ammonium hydroxide, didodecyl dimethyl ammonium hydroxide, dioctadecyl dimethyl ammonium hydroxide, tallow trimethyl ammonium hydroxide and coco trimethyl ammonium hydroxide as well as corresponding salts of these materials, fatty amines and fatty acid amides and their derivatives, basic pyridinium compounds, quaternary ammonium bases of benzimidazolines and polypropanolpolyethanol amines. Other representative examples of suitable cationic surfactants include alkylamine salts, sulphonium salts, and phosphonium salts.
Examples of suitable anionic surfactants include alkyl sulphates such as lauryl sulphate, polymers such as acrylic acid/C10-30 alkyl acrylate crosspolymer, alkylbenzenesulfonic acids and salts such as hexylbenzenesulfonic acid, octylbenzenesulfonic acid, decylbenzenesulfonic acid, dodecylbenzenesulfonic acid, cetylbenzenesulfonic acid and myristylbenzenesulfonic acid; the sulphate esters of monoalkyl polyoxyethylene ethers; alkylnapthylsulfonic acid; alkali metal sulforecinates, sulfonated glyceryl esters of fatty acids such as sulfonated monoglycerides of coconut oil acids, salts of sulfonated monovalent alcohol esters, amides of amino sulfonic acids, sulfonated products of fatty acid nitriles, sulfonated aromatic hydrocarbons, condensation products of naphthalene sulfonic acids with formaldehyde, sodium octahydroanthracene sulfonate, alkali metal alkyl sulphates, ester sulphates, and alkarylsulfonates. Anionic surfactants include alkali metal soaps of higher fatty acids, alkylaryl sulphonates such as sodium dodecyl benzene sulphonate, long chain fatty alcohol sulphates, olefin sulphates and olefin sulphonates, sulphated monoglycerides, sulphated esters, sulphonated ethoxylated alcohols, sulphosuccinates, alkane sulphonates, phosphate esters, alkyl isethionates, alkyl taurates, and alkyl sarcosinates. One example of a preferred anionic surfactant is sold commercially under the name Bio-Soft N-300. It is a triethanolamine linear alkylate sulphonate composition marketed by the Stephan Company, Northfield, Ill.
The above surfactants may be used individually or in combination.
The polymerisation catalyst may additionally be the surfactant, or one of the surfactants, involved in the emulsification process. A family of catalysts which can act as surfactants are acidic condensation catalysts of the formula R20SO3H, for example dodecylbenzenesulphonic acid.
In one preferred emulsification procedure according to the invention, emulsification is carried out by mixing the reaction product with 0.5 to 20% by weight of water in the presence of 1 to 30% by weight surfactant, followed by at least one step of mixing the resulting emulsion with water until the desired concentration of emulsified wax organopolysiloxane blend in water is reached. The amount of water present in the initial mixing step of the emulsification can for example be 1 to 10% based on the polymerization reaction product. In such a procedure in which only a small amount of water is initially added to the polymerization reaction product, a water-in-oil emulsion containing a continuous wax/silicone phase and a dispersed water phase can be formed, particularly if the amount of water is less than 5%. By applying shear to the water-in-oil emulsion, a phase inversion of the water-in-oil emulsion to a viscous oil-in-water emulsion is effected. The high shear mixing is preferably carried out in a mixer designed to deal with thick pastes such as a dental mixer. Further additions of small amounts of water with high shear mixing may be carried out before optionally diluting the oil-in-water emulsion by adding more water under lower shear.
The particle size of the emulsion can for example be within the range 0.1 to 100 μm. The quantity of water and surfactant used in the initial phase inversion process may have an impact on the particle size of the final emulsion. For instance, if an emulsion is formed with the same quantity of water in two instances but in the first a large quantity of water is mixed before the phase inversion step and in the second a small quantity of water is mixed before the phase inversion step followed by mixing the remaining additional water after the phase inversion step, the first emulsion will generally have a larger particle size than the second. No matter how the water is added, the total amount of water used is generally between about 1 and 99 wt. %, preferably between about 6 and about 99 wt. %, based on the weight of the emulsion.
If desired, other materials can be added to either phase of the emulsions, for example “active materials” such as perfumes, sunscreens, vitamins, drugs, biocides, pest repellents, catalysts and cooling agents, or fillers, relaxers, colorants, thickeners, preservatives, antifoams, freeze thaw stabilizers, or inorganic salts to buffer pH. If controlled release of active materials from the emulsion compositions is desired, the active material such as perfume is preferably incorporated in the wax silicone phase by adding it to the mixture of organopolysiloxane and wax before, during or after polymerisation but before the reaction product has been cooled to a paste or solid or emulsified, as described above.
The emulsions of the invention are useful in personal care applications such as on hair, skin, mucous membrane or teeth. In these applications, the silicone is lubricious and will improve the properties of skin creams, skin care lotions, moisturizers, facial treatments such as acne or wrinkle removers, personal and facial cleansers such as shower gels, liquid soap, hand sanitizers and wipes, bath oils, perfumes, fragrances, colognes, sachets, deodorants, sun protection creams, lotions and wipes, self tanning creams, lotions and wipes, pre-shave and after shave lotions, after sun lotion and creams, antiperspirant sticks, soft solid and roll-ons, shaving soaps and shaving lathers. It can likewise be use in hair shampoos, rinse-off and leave-on hair conditioners, hair styling aids, such as sprays, mousses and gels, hair colorants, hair relaxers, permanents, depilatories, and cuticle coats, for example to provide styling and conditioning benefits. In cosmetics, the silicone functions as a levelling and spreading agent for pigment in make-ups, colour cosmetics, compact gel, cream and liquid foundations (water-in-oil and oil-in-water emulsions, or anhydrous lotions), blushes, eye liners, eye shadows, mascaras, and make up removers. The emulsion of silicone and wax is likewise useful as a delivery system for oil and water soluble substances such as vitamins, fragrances, emollients, colorants, organic sunscreens, or pharmaceuticals. When the emulsion is used in personal care products, the polyorganosiloxane generally comprises about 0.01 to about 50 weight percent, preferably 0.1 to 25 wt. percent, of the personal care product.
The emulsions produced according to the invention are also useful in other applications such as paints, water based coatings, textile fibre treatment, leather lubrication, fabric softening, fabric care in laundry applications, homecare, release agents, and oil drag reduction, and in other areas where silicone emulsions are conventionally used. The wax/silicone dispersions have particular advantages in oil drag reduction resulting from increased compatibility with hydrocarbon fluids, especially when the wax is a hydrocarbon wax.
The invention is illustrated by the following Examples, in which parts and percentages are by weight. Catalyst levels are given in ppm and are based on the polysiloxane content.
The molecular weight of the siloxanes in the blends was determined by gel permeation chromatography (GPC). The analyses have been performed by GPC (Alliance Waters 2690) using triple detection (Refractive index detector, Viscometer and Light Scattering Detectors) and toluene as solvent. Molecular weight averages were determined by universal calibration relative to a triple detection calibration realized on a single point using polystyrene narrow standard (Mw 70,950 g/mol).
The consistency of blends was tested with a needle penetrometer according to ASTM D217-97 at 25° C. and results are reported in mm/10*3 sec. Viscosity of some blends were determined with a Brookfield Viscosimeter at 25° C.
20 parts of a paraffin wax of melting point 56° C. (Paraflex 4750A granules sold by IgiWax) was mixed with 80 parts of a dimethyl hydroxyl terminated polydimethylsiloxane (having a viscosity of 70 mPa·s at 25° C., a Mn of 2500 g/mol and a Mw of 3500 g/mol) to form a liquid/liquid dispersion and heated to 80° C. to melt the wax. 20 parts per million (ppm) of an ionic phosphazene [Cl(PCl2═N)xPCl3]+[PCl6]− diluted in dichloromethane was added as catalyst. The polymerisation was carried out in a 1 l glass reactor (IKA) at 80° C. under vacuum. The polymerisation was stopped, by the addition of 0.008 parts of trihexylamine, once a torque of >2.0 N/m was reached in the mixer (3 minutes polymerisation time). A liquid/liquid dispersion of the wax and a polydimethylsiloxane polymer of increased molecular weight was produced.
The dispersion produced was cooled to room temperature forming a paste of high molecular weight polydimethylsiloxane and wax. The paste has a viscosity of 1650 Pa·s. The polymerised polydimethylsiloxane has Mn 125 kg/mol and Mw 196 kg/mol. The dispersion had a penetration of 135 mm/10*3 sec.
20 parts of a microcrystalline wax of melting point 82° C. (Microsere 5981A sold by IgiWax) was melted at 90° C. and mixed at 90° C. with 80 parts of a dimethyl hydroxyl terminated polydimethylsiloxane having a viscosity of 70 mPa·s at 25° C. to form a liquid/liquid dispersion. 20 ppm [Cl(PCl2═N)xPCl3]+[PCl6]− diluted in dichloromethane was added as catalyst. The polymerisation was carried out in a 1 l glass reactor at 90° C. under vacuum and was stopped by the addition of 0.008 parts of trihexylamine after 3 minutes. A liquid/liquid dispersion of the wax and high molecular weight polydimethylsiloxane was produced and was cooled to room temperature forming a paste of viscosity 842 Pa·s. The polymerised polydimethylsiloxane has Mn 127 kg/mol and Mw 193 kg/mol. The dispersion had a penetration of 139 mm/10*3 sec.
Example 1 was repeated using a palm wax of melting point 59° C. (R2778A sold by IgiWax) in place of the Paraflex. The reaction time was 28 minutes. A liquid/liquid dispersion of the wax and high molecular weight polydimethylsiloxane was produced and was cooled to room temperature forming a paste of viscosity of 2020 Pa·s. The polymerised polydimethylsiloxane has Mn 101 kg/mol and Mw 163 kg/mol. The dispersion had a penetration of 27 mm/10*3 sec. The dispersion was stored at 70° C. during 4 hours and cooled down to room temperature without showing any signs of macroscopic phase separation.
20 parts of a polyvinylether wax of melting point 49° C. (Luwax V flakes sold by BASF) was mixed and melted at 70° C. with 80 parts of a dimethyl hydroxyl terminated polydimethylsiloxane having a viscosity of 70 mPa·s at 25° C. to form a liquid/liquid dispersion. 20 ppm [Cl(PCl2═N)xPCl3]+[PCl6]− diluted in dichloromethane was added as catalyst. The polymerisation was carried out in a 1 l glass reactor at 70° C. under vacuum and was stopped as described in Example 1 after 26 minutes. A liquid/liquid dispersion of the wax and high molecular weight polydimethylsiloxane was produced and was cooled to room temperature forming a paste of viscosity 134 Pa·s. The polymerised polydimethylsiloxane has Mn 62 kg/mol and Mw 109 kg/mol. The dispersion had a penetration of 351 mm/10*3 sec.
20 parts of a silicone wax having a melting point of about 32° C. (2503 sold by Dow Corning) was mixed and melted at 70° C. with 80 parts of a dimethyl hydroxyl terminated polydimethylsiloxane having a viscosity of 70 mPa·s at 25° C. to form a liquid/liquid dispersion. 20 ppm [Cl(PCl2═N)xPCl3]+[PCl6]− diluted in dichloromethane was added as catalyst. The polymerisation was carried out in a 1 l glass reactor at 70° C. under vacuum. The polymerisation was stopped after 8 minutes, by the addition of 0.012 parts of trihexylamine, A liquid/liquid dispersion of the wax and high molecular weight polydimethylsiloxane was produced and was cooled to room temperature forming a paste of viscosity 334 Pa·s. The polymerised polydimethylsiloxane has Mn 148 kg/mol and Mw 191 kg/mol. The dispersion had a penetration of 169 mm/10*3 sec.
The reaction from example 5 was repeated increasing the reaction time to 120 minutes. The polymerised polydimethylsiloxane has Mn 236 kg/mol and Mw 334 kg/mol. The dispersion had a penetration of 96 mm/10*3 sec. The dispersion was stored at 50° C. during 4 hours and cooled down to room temperature without showing any signs of macroscopic phase separation.
20 parts Dow Corning HY-3050 soy wax having a melting point of about 55° C. was mixed and melted at 80° C. with 80 parts of a dimethyl hydroxyl terminated polydimethylsiloxane having a viscosity of 70 mPa·s at 25° C. to form a liquid/liquid dispersion. 30 ppm [Cl(PCl2═N)xPCl3]+[PCl6]− diluted in dichloromethane was added as catalyst. The polymerisation was carried out in a 1 l glass reactor at 80° C. under vacuum. The polymerisation was stopped, by the addition of 0.012 parts of trihexylamine, after 14 minutes. The polymerised polydimethylsiloxane has Mn 96 kg/mol and Mw 131 kg/mol. The dispersion had a penetration of 121 mm/10*3 sec. The dispersion was stored at 70° C. during 4 hours and cooled down to room temperature without showing any signs of macroscopic phase separation.
An emulsion was prepared by adding 0.8 g Volpo L4 and 1.2 g Volpo L23 polyoxyethylene lauryl ether non-ionic surfactants and 1 g water to 20 g of the above dispersion at 80° C. and mixing for 20 seconds at 3000 rpm in a Hausschild dental mixer. An additional 1.0 g of water was added and mixing repeated under the same conditions. Addition of 1.0 g water and mixing was repeated 4 more times. Further additions of water and subsequent mixing were carried out until 18 g water had been added in total, yielding a milky white emulsion with 50% active content. The so obtained emulsion has a particle size of D(v, 0.5) μm=0.61 and D(v, 0.9) μm=1.13 (determined using a Malvern Mastersizer 2000).
The polymerisation reaction of Example 7 was repeated using 10 parts Dow Corning HY-3050 soy wax and 90 parts dimethyl hydroxyl terminated polydimethylsiloxane at 70° C. using 10 ppm catalyst. The reaction was stopped after 2 minutes by the addition of 0.008 parts of trihexylamine. The polymerised polydimethylsiloxane has Mn 467 kg/mol and Mw 567 kg/mol. The dispersion had a penetration of 40 mm/10*3 sec. The dispersion was stored at 70° C. during 4 hours and cooled down to room temperature without showing any signs of macroscopic phase separation.
The polymerisation reaction of Example 7 was repeated using 10 parts Dow Corning HY-3050 soy wax and 90 parts dimethyl hydroxyl terminated polydimethylsiloxane at 70° C. using 5 ppm catalyst. The reaction was stopped after 6 minutes by the addition of 0.004 parts of trihexylamine. The polymerised polydimethylsiloxane has Mn 569 kg/mol and Mw 678 kg/mol. The dispersion had a penetration of 33 mm/10*3 sec. The dispersion was stored at 70° C. during 4 hours and cooled down to room temperature without showing any signs of macroscopic phase separation.
20 parts of Dow Corning HY-3050 soy wax was mixed and melted at 60° C. with 60 parts of a dimethyl hydroxyl terminated polydimethylsiloxane having a viscosity of 70 mPa·s at 25° C. and 20 parts ‘Gemseal 25’ (supplied by Total) cosmetic grade mineral oil to form a liquid/liquid dispersion. 30 ppm [Cl(PCl2═N)xPCl3]+[PCl6]− diluted in dichloromethane was added as catalyst. The polymerisation was carried out in a 1 l glass reactor at 60° C. under vacuum. The polymerisation was stopped, by the addition of 0.009 parts of trihexylamine, after 31 minutes. The polymerised polydimethylsiloxane has Mn 73 kg/mol and Mw 103 kg/mol. The dispersion had a penetration of >500 mm/10*3 sec.
An emulsion was prepared by adding 2 g Lutensol T08 ethoxylated oxo alcohol non-ionic surfactant sold by BASF and 1 g water to 25 g of the above dispersion at 60° C. and mixing for 20 seconds at 3000 rpm in a Hausschild dental mixer. An additional 1.0 g of water was added and mixing repeated under the same conditions. Addition of 1.0g water and mixing was repeated 3 more times yielding a cream with 80% (silicone plus organics) active content. The so obtained cream has a particle size of D(v, 0.5) μm=0.28 and D(v, 0.9) μm=0.50 (determined using a Malvern Mastersizer 2000).
20 parts of a Carnauba wax having a melting point of approx 83° C. (supplied under the name SP-63 from Strahl & Pitsch) was mixed and melted at 90° C. with 80 parts of a dimethyl hydroxyl terminated polydimethylsiloxane having a viscosity of 70 mPa·s at 25° C. to form a liquid/liquid dispersion. 50 ppm [Cl(PCl2═N)xPCl3]+[PCl6]− diluted in dichloromethane was added as catalyst. The polymerisation was carried out in a 1 l glass reactor at 90° C. under vacuum. The polymerisation was stopped, by the addition of 0.02 parts of trihexylamine, after 60 minutes. A liquid/liquid dispersion of the wax and high molecular weight polydimethylsiloxane was produced and was cooled to room temperature. The polymerised polydimethylsiloxane has Mn 15 kg/mol and Mw 20 kg/mol. The dispersion had a penetration of 347 mm/10*3 sec.
Two lipsticks were prepared. The blend of example 11 was incorporated into lipstick No 2.
Copernicia Cerifera (Carnauba)
Euphorbia Cerifera (Candelilla)
The following procedure was used to prepare the lipstick.
The appearance and application of both lipsticks were good. Formulation 2 was cut in small pieces to check if there was phase separated poly siloxane polymer inside but no visible signs of separation could be seen.
The blend produced in Example 11 was also incorporated in a facial cream with a formulation indicated in the following table.
The following procedure was used to prepare the facial creme.
The facial cream formulation was homogenous and stable for at least 2 months at room temperature.
20 parts of a Mango butter having a melting range of about 25-38° C. (HY 4001 sold by Dow Corning) was mixed and melted at 70° C. with 80 parts of a dimethyl hydroxyl terminated polydimethylsiloxane having a viscosity of 70 mPa·s at 25° C. to form a liquid/liquid dispersion. 20 ppm [Cl(PCl2═N)xPCl3]+[PCl6]− diluted in dichloromethane was added as catalyst. The polymerisation was carried out in a 1 I glass reactor at 70° C. under vacuum. The polymerisation was stopped after 105 minutes, by the addition of 0.008 parts of trihexylamine, A liquid/liquid dispersion of the wax and high molecular weight polydimethylsiloxane was produced and was cooled to room temperature. The polymerised polydimethylsiloxane has Mn 54 kg/mol and Mw 74 kg/mol. The dispersion had a penetration of 352 mm/10*3 sec.
20 parts of a white beeswax having a melting range of about 62-65° C. (supplied under the name SP-422P from Strahl & Pitsch) was mixed and melted at 70° C. with 80 parts of a dimethyl hydroxyl terminated polydimethylsiloxane having a viscosity of 70 mPa·s at 25° C. to form a liquid/liquid dispersion. 20 ppm [Cl(PCl2═N)xPCl3]+[PCl6]− diluted in dichloromethane was added as catalyst. The polymerisation was carried out in a 1 l glass reactor at 70° C. under vacuum. The polymerisation was stopped after 23 minutes, by the addition of 0.013 parts of trihexylamine, A liquid/liquid dispersion of the wax and high molecular weight polydimethylsiloxane was produced and was cooled to room temperature forming a paste. The polymerised polydimethylsiloxane has Mn 298 kg/mol and Mw 379 kg/mol. The dispersion had a penetration of 23 mm/10*3 sec. The dispersion was stored at 80° C. during 4 hours and cooled down to room temperature without showing any signs of macroscopic phase separation.
20 parts of a Candelilla wax having a melting range of about 68.5-72.5° C. (supplied under the name SP75 from Strahl & Pitsch) was melted at 75° C. and mixed at 75° C. with 80 parts of a dimethyl hydroxyl terminated polydimethylsiloxane having a viscosity of 70 mPa·s at 25° C. to form a liquid/liquid dispersion. 20 ppm [Cl(PCl2═N)xPCl3]+[PCl6]− diluted in dichloromethane was added as catalyst. The polymerisation was carried out in a 1 l glass reactor at 75° C. under vacuum. The polymerisation was stopped after 29 minutes, by the addition of 0.013 parts of trihexylamine. A liquid/liquid dispersion of the wax and high molecular weight polydimethylsiloxane was produced and was cooled to room temperature The polymerised polydimethylsiloxane has Mn 221 kg/mol and Mw 285 kg/mol. The dispersion had a penetration of 19 mm/10*3 sec. The dispersion was stored at 80° C. during 4 hours and cooled down to room temperature without showing any signs of macroscopic phase separation.
20 parts of a Ceresine wax having a melting range of about 62.8-65.6° C. (supplied under the name SP1022P from Strahl & Pitsch) was mixed and melted at 70° C. with 80 parts of a dimethyl hydroxyl terminated polydimethylsiloxane having a viscosity of 70 mPa·s at 25° C. to form a liquid/liquid dispersion. 10 ppm [Cl(PCl2═N)xPCl3]+[PCl6]− diluted in dichloromethane was added as catalyst. The polymerisation was carried out in a 1 l glass reactor at 70° C. under vacuum. The polymerisation was stopped after 4 minutes, by the addition of 0.007 parts of trihexylamine. A liquid/liquid dispersion of the wax and high molecular weight polydimethylsiloxane was produced and was cooled to room temperature forming a paste. The siloxane has Mn 282 kg/mol and Mw 360 kg/mol. The dispersion had a penetration of 35 mm/10*3 sec. The dispersion was stored at 70° C. during 4 hours and cooled down to room temperature without showing any signs of macroscopic phase separation.
20 parts of a silicone resin wax having a melting range of about 64-68° C. (supplied under the name SW-8005 from Dow Corning) was mixed and melted at 70° C. with 80 parts of a dimethyl hydroxyl terminated polydimethylsiloxane having a viscosity of 70 mPa·s at 25° C. to form a liquid/liquid dispersion. 20 ppm [Cl(PCl2═N)xPCl3]+[PCl6]− diluted in dichloromethane was added as catalyst. The polymerisation was carried out in a 1 l glass reactor at 70° C. under vacuum. The polymerisation was stopped after 21 minutes, by the addition of 0.013 parts of trihexylamine. A liquid/liquid dispersion of the wax and high molecular weight polydimethylsiloxane was produced and was cooled to room temperature. The polymerised polydimethylsiloxane has Mn 318 kg/mol and Mw 404 kg/mol. The dispersion had a penetration of 57 mm/10*3 sec. The dispersion was stored at 80° C. during 4 hours and cooled down to room temperature without showing any signs of macroscopic phase separation.
20 parts of an Ozokerite wax having a melting range of about 74.4-77.2° C. (supplied under the name SP-1021D from Strahl & Pitsch) was mixed and melted at 75° C. with 80 parts of a dimethyl hydroxyl terminated polydimethylsiloxane having a viscosity of 70 mPa·s at 25° C. to form a liquid/liquid dispersion. 10 ppm [Cl(PCl2═N)xPCl3]+[PCl6]− diluted in dichloromethane was added as catalyst. The polymerisation was carried out in a 1 l glass reactor at 70° C. under vacuum. The polymerisation was stopped after 2 minutes, by the addition of 0.007 parts of trihexylamine, A liquid/liquid dispersion of the wax and high molecular weight polydimethylsiloxane was produced and was cooled to room temperature. The polymerised polydimethylsiloxane has Mn 187 kg/mol and Mw 260 kg/mol. The dispersion had a penetration of 25 mm/10*3 sec. The dispersion was stored at 90° C. during 4 hours and cooled down to room temperature without showing any signs of macroscopic phase separation.
10 parts of a shea butter having a melting range of about 28-38° C. (supplied under the name HY-3003 from Dow Corning) was mixed and melted at 70° C. with 90 parts of a dimethyl hydroxyl terminated polydimethylsiloxane having a viscosity of 70 mPa·s at 25° C. to form a liquid/liquid dispersion. 5 ppm [Cl(PCl2═N)xPCl3]+[PCl6]− diluted in dichloromethane was added as catalyst. The polymerisation was carried out in a 1 l glass reactor at 70° C. under vacuum. The polymerisation was stopped after 2 minutes, by the addition of 0.004 parts of trihexylamine, A liquid/liquid dispersion of the butter and high molecular weight polydimethylsiloxane was produced and was cooled to room temperature forming a paste. The polymerised polydimethylsiloxane has Mn 254 kg/mol and Mw 326 kg/mol. The dispersion had a penetration of 93 mm/10*3 sec. The dispersion was stored at 50° C. during 4 hours and cooled down to room temperature without showing any signs of macroscopic phase separation.
Example 18 was repeated using 20 parts of the shea butter with 80 parts dimethyl hydroxyl terminated polydimethylsiloxane, and adding 10 ppm catalyst. The polymerisation was stopped after 2 minutes, by the addition of 0.007 parts of trihexylamine. The polymerised polydimethylsiloxane produced has Mn 383 kg/mol and Mw 464 kg/mol. The dispersion had a penetration of 56 mm/10*3 sec. The dispersion was stored at 50° C. during 4 hours and cooled down to room temperature without showing any signs of macroscopic phase separation.
20 parts of Dow HY-3003 from Dow Corning shea butter was mixed and melted at 70° C. with 60 parts of a dimethyl hydroxyl terminated polydimethylsiloxane having a viscosity of 70 mPa·s at 25° C. and 20 parts ‘Gemseal 25’ (supplied by Total) cosmetic grade mineral oil to form a liquid/liquid dispersion. 20 ppm [Cl(PCl2═N)xPCl3]+[PCl6]− diluted in dichloromethane was added as catalyst. The polymerisation was carried out in a 1 l glass reactor at 70° C. under vacuum. The polymerisation was stopped, by the addition of 0.010 parts of trihexylamine, after 4 minutes. A liquid/liquid dispersion of the wax, high molecular weight polydimethylsiloxane and mineral oil was produced and was cooled to room temperature forming a paste like material. The polymerised polydimethylsiloxane has Mn 419 kg/mol and Mw 569 kg/mol. The dispersion had a penetration of 164 mm/10*3 sec.
30 parts of a paraffin wax of melting point 60-70° C. (6805 sold by Sasol) was mixed and melted at 70° C. with 70 parts of a dimethyl hydroxyl terminated polydimethylsiloxane having a viscosity of 70 mPa·s at 25° C. to form a liquid/liquid dispersion. 10 parts per million (ppm) [Cl(PCl2═N)xPCl3]+[PCl6]− diluted in dichloromethane was added as catalyst. The polymerisation was carried out in a 1 l glass reactor at 70° C. under vacuum. The polymerisation was stopped after 8 minutes, by the addition of 0.006 parts of trihexylamine. A liquid/liquid dispersion of the wax and a polydimethylsiloxane polymer of increased molecular weight was produced. The dispersion produced was cooled to room temperature. The polymerised polydimethylsiloxane in the dispersion has Mn 568 kg/mol and Mw 738 kg/mol. The dispersion had a penetration of 23 mm/10*3 sec.
20 parts Paraflex 4750A paraffin wax was mixed and melted at 70° C. with 80 parts of the dimethyl hydroxyl terminated polydimethylsiloxane of Example 1 to form a liquid/liquid dispersion. 20 ppm [Cl(PCl2═N)xPCl3]+[PCl6]− diluted in dichloromethane was added as catalyst and polymerisation was carried out in a 1 l glass reactor at 70° C. under vacuum. 3 minutes after addition of catalyst, 5 parts perfume were added (fraicheur des sommets). The polymerisation was stopped, after 5 minutes (total polymerisation time), by the addition of 0.008 parts of trihexylamine. A liquid/liquid dispersion of the wax, the perfume and a polydimethylsiloxane polymer of increased molecular weight was produced. The dispersion produced was allowed to cool to room temperature forming a dispersion of wax perfume and high molecular weight polydimethylsiloxane. The polymerised polydimethylsiloxane in the dispersion has Mn 101 kg/mol and Mw 149 kg/mol. The dispersion had a penetration of 164 mm/10*3 sec.
18 parts Paraflex 4750A paraffin wax was mixed and melted at 70° C. with 72 parts of the dimethyl hydroxyl terminated polydimethylsiloxane of Example 1 to form a liquid/liquid dispersion. 10 ppm [Cl(PCl2═N)xPCl3]+[PCl6]− diluted in dichloromethane was added as catalyst and polymerisation was carried out in a 1 l glass reactor at 70° C. under vacuum. The polymerisation was stopped, after 5 minutes (total polymerisation time), by the addition of 0.004 parts of trihexylamine. 10 parts perfume were added (lavendel oil supplied by Aldrich) to the hot dispersion under stirring A liquid/liquid dispersion of the wax, the perfume and a polydimethylsiloxane polymer of increased molecular weight was produced. The dispersion produced was allowed to cool to room temperature forming a dispersion of wax, perfume dispersed and high molecular weight polydimethylsiloxane. The polymerised polydimethylsiloxane in the dispersion has Mn 147 kg/mol and Mw 215 kg/mol. The dispersion had a penetration of 38 mm/10*3 sec. The dispersion was stored at 80° C. during 4 hours and cooled down to room temperature without showing any signs of macroscopic phase separation.
18 parts of palm wax (R2778A sold by IgiWax) was mixed and melted at 70° C. with 72 parts of the dimethyl hydroxyl terminated polydimethylsiloxane of Example 1 to form a liquid/liquid dispersion. 10 ppm [Cl(PCl2═N)xPCl3]+[PCl6]− diluted in dichloromethane was added as catalyst and polymerisation was carried out in a 1 l glass reactor at 70° C. under vacuum. The polymerisation was stopped, after 6 minutes (total polymerisation time), by the addition of 0.004 parts of trihexylamine. 10 parts perfume were added (lavendel oil supplied by Aldrich) to the hot dispersion under stirring A liquid/liquid dispersion of the wax, the perfume and a polydimethylsiloxane polymer of increased molecular weight was produced. The dispersion produced was allowed to cool to room temperature forming a dispersion of wax, perfume dispersed and high molecular weight polydimethylsiloxane. The polymerised polydimethylsiloxane in the dispersion has Mn 111 kg/mol and Mw 167 kg/mol. The dispersion had a penetration of 149 mm/10*3 sec.
Facial creams of the water in oil type were prepared using the blends prepared in Examples 8, 14 and 19. The formulations are given in the following table.
The following procedure was used:
All the facial cream formulations were homogenous and stable for at least 1 month at room temperature and at 40° C.
800 parts of the dimethylhydroxyl-terminated polydimethylsiloxane of Example 1 was mixed with 200 parts of a silicone wax having a melting point of about 32° C. (2503 sold by Dow Corning) and 0.64 parts methyltrimethoxysilane (MTM) at 70° C. 20 parts per million (ppm) [Cl(PCl2═N)xPCl3]+[PCl6]− diluted in dichloromethane was added as catalyst. The polymerisation was carried out in a 1 l glass reactor (IKA) at 70° C. under vacuum. The polymerisation was stopped after 54 minutes by the addition of 0.08 parts trihexylamine. A branched polydimethylsiloxane polymer blend with silicone wax was produced. The branched polydimethylsiloxane has Mn 112 kg/mol and Mw 176 kg/mol. The mixture has a viscosity of 324000 mPas.
| Number | Date | Country | Kind |
|---|---|---|---|
| 0905488.3 | Mar 2009 | GB | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/EP2010/054221 | 3/30/2010 | WO | 00 | 9/24/2011 |
