Method for preparation of potassium silanolates

Abstract: A method for preparation of potassium silanolate comprises reacting a mixture comprising a solid potassium hydroxide component and a polyorganosiloxane component described by formula R 1 R 2 2 SiO(R 2 2 SiO) m R 3 or (R 2 2 SiO) n , where m is an integer from 1 to 1000, n is an integer from 3 to 20, R 1 is hydroxyl or alkoxy group of 1 to 8 carbon atoms, R 2 is hydrogen atom or an independently selected substituted or unsubstituted monovalent hydrocarbon group of 1 to 8 carbon atoms and R 3 is a hydrogen atom or an alkyl group of 1 to 8 carbon atoms in the presence of an organic solvent which forms an azeotrope with water at a temperature of 90°C. to 150°C. to thereby form said potassium silanolates.

Description: The invention is a method for the preparation of potassium silanolates which comprises reacting a mixture comprising a solid potassium hydroxide component and a polyorganosiloxane component in the presence of an organic solvent that forms an azeotrope with water at a temperature of 90°C. to 150°C. to thereby form said potassium silanolates. U.S. Patent 3,641,090 teaches the preparation of hexamethylphosphoramide complexes made by contacting hexamethylphosphoramide and an alkali metal silanolate. The hexamethylphosphoramide complex is useful as polymerization initiators for polyorganosiloxanes and polyorganosiloxane block copolymers. Said patent does not teach making potassium silanolates using solid hydroxide. EP-A-15366 relates to a method for preparing alkali-silanolates by using an aqueous NaOH or KOH solution. In the aforementioned patented process, large quantities of water must be removed in order to drive the reaction to completion and to minimize problems with phase separation, poor shelf-life, high branching and quality variance. Water and residual solvent are typically removed from the reaction by distillation followed by high temperature stripping. However, under these conditions batch time is about 24 hours and the prolonged elevated temperatures during distillation and stripping can cause excessive cleavage of carbon-silicon bonds resulting in phase separation, poor shelf-life, quality variance and high branching in the final product. The present inventors have discovered that preparing potassium silanolates with solid potassium hydroxide eliminates the need to remove large quantities of water at elevated temperatures which is believed to cause the above problems. Another advantage is that the time to prepare potassium silanolates can be shortened from 24 hours to about 12 hours. A further advantage is that water can be removed from the potassium silanolate by azeotropic distillation at lower temperatures than with conventional distillation methods, thus reducing the degree of branching in the final product. A still further advantage is that residual water and solvent can be stripped from the potassium silanolate at lower temperatures and in a shorter time period than for conventional stripping methods. Another advantage is that the potassium silanolates can be stored over an extended time period without the phase separation problems of known silanolate preparations. The present invention is a method for the preparation of potassium silanolate which comprises reacting a mixture comprising a solid potassium hydroxide component and a polyorganosiloxane component, described by the formula R 1 R 2 2 SiO(R 2 2 SiO) m R 3 or (R 2 2 SiO) n , where m is an integer from 1 to 1000, n is an integer from 3 to 20, R 1 is a hydroxyl group or an alkoxy group of 1 to 8 carbon atoms, R 2 is hydrogen atom or an independently selected substituted or unsubstituted monovalent hydrocarbon group of 1 to 8 carbon atoms and R 3 is a hydrogen atom or an alkyl group of 1 to 8 carbon atoms; in the presence of an organic solvent which forms an azeotrope with water at a temperature of 90°C. to 150°C. to thereby form said potassium silanolates. Reacting the mixture comprising solid potassium hydroxide and a polyorganosiloxane in the presence of an organic solvent which forms an azeotrope with water may be effected in standard reactors suitable for running equilibration type reactions. The potassium hydroxide found to be useful in the present invention is in solid form rather than in aqueous solution. The solid potassium hydroxide can be in the form of pellets, flakes or shavings, which are all commercially available. Using solid potassium hydroxide in the present method eliminates the need to remove large quantities of water in order to obtain stable potassium silanolate. Preferably, the solid potassium hydroxide should be completely dry, but commonly may contain up to 15 weight percent water. Solid potassium hydroxide containing more than 15 weight percent water may be used, but is undesirable because as more water is added to the reaction, longer distillation periods at higher temperatures are required to remove the additional water. The method is conducted in the presence of an organic solvent which forms an azeotrope with water, thereby allowing water removal at lower temperatures than the temperatures used in conventional distillation methods. It is preferred that the organic solvent comprise 10 to 40 weight percent of the weight of the mixture comprising solid potassium hydroxide and polyorganosiloxane and that the azeotrope have a boiling point of 90°C. to 120°C. Most preferred is when the organic solvent comprises 20 to 30 weight percent of the weight of the mixture comprising solid potassium hydroxide and polyorganosiloxane. Organic solvents useful in the present method are solvents which form an azeotrope with water and from which water can be separated. Examples of organic solvents useful in the present method are cyclohexane, toluene, xylene, diethyl ether, benzene, butanol and methanol. The preferred organic solvent is cyclohexane at a concentration of 10 to 40 weight percent of the weight of the mixture comprising solid potassium hydroxide and polyorganosiloxane. The most preferred cyclohexane concentration is 25 to 35 weight percent of the weight of the mixture comprising solid potassium hydroxide and polyorganosiloxane. The particular organic solvent and concentration can also be selected to control the temperature at which water is removed by azeotropic distillation and the rate at which water is removed. The polyorganosiloxanes useful in the present method may be cyclic, linear or a mixture of cyclic and linear polyorganosiloxanes. The cyclic polyorganosiloxanes have the formula (R 2 2 SiO) n , where n is an integer from 3 to 20, R 2 is a hydrogen atom or an independently selected substituted or unsubstituted monovalent hydrocarbon group comprising from 1 to 8 carbon atoms. R 2 is, for example, an alkyl group such as methyl, ethyl and propyl; a cycloalkyl group such as cyclohexyl and cyclopentyl; an alkenyl group such as vinyl and allyl; an aryl group such as phenyl and diphenyl; an alkaryl group such as tolyl and xylyl; an aralkyl group such as benzyl and phenylethyl. The monovalent hydrocarbon group represented by R 2 may be unsubstituted or substituted by one or more groups such as halogen atoms and amine groups. Examples of such substituted hydrocarbon groups include amine-substituted hydrocarbon groups such as propylamine or n-(2-aminoethyl)-3-aminopropyl groups; halogenated alkyl groups such as 3,3,3-trifluoropropyl and 4-chlorobutyl; and halogenated aryl groups such as chlorophenyl and dibromophenyl. Examples of cyclic polyorganosiloxanes useful in the present method are hexamethylcyclotrisiloxane, octamethylcyclotetrasiloxane, heptamethylcyclotetrasiloxane, hexaethylcyclotrisiloxane and octaethylcyclotetrasiloxane. The preferred cyclic polyorganosiloxane for use in the present method is octamethylcyclotetrasiloxane. The linear polyorganosiloxanes useful in the method are described by formula R 1 R 2 2 SiO(R 2 2 SiO) m R 3 , where m, R 1 , R 2 and R 3 are as previously described. The linear polyorganosiloxanes can be for example, hexamethyldisiloxane, hexaethyldisiloxane, pentamethyldisiloxane and heptamethyltrisiloxane. The preferred linear polyorganosiloxane is hexamethyldisiloxane. The molar ratio of solid potassium hydroxide to polyorganosiloxane is typically 4 to 1. Preferred is when the molar ratio of said hydroxide to polyorganosiloxane is 3 to 1. Most preferred is a molar ratio of 2 to 1. The mixture comprising solid potassium hydroxide and a polyorganosiloxane in the presence of an organic solvent that forms an azeotrope with water, is heated to a temperature of 90°C. to 150°C. to facilitate reaction of the potassium hydroxide with the polyorganosiloxane thereby forming a potassium silanolate. Preferred is when the mixture in the presence of an organic solvent which forms an azeotrope with water is heated to a temperature of 110°C. to 130°C. Preferably, the reaction is effected in an inert gas atmosphere, such as nitrogen, to prevent the mixture from absorbing moisture from the atmosphere which would later require removal from the mixture. Herein the method of recovering the potassium silanolate is not critical. For example, the potassium silanolate can be drained or poured from a reactor or kettle. In the preferred embodiment, water is removed from the potassium silanolate by azeotropic distillation. An organic solvent which forms an azeotrope with water at a temperature within a range of 90°C. to 150°C. is employed. Thereby water is removed from the mixture and the organic solvent is condensed and returned to the mixture. The azeotropic distillation is continued until the water is removed. It is preferred that the azeotropic distillation be conducted within a temperature range of 95°C. to 125°C. for 4 to 5 hours. It is more preferred that the azeotropic distillation occur at a temperature of 100°C. to 120°C. Most preferred is conducting the azeotropic distillation at a temperature of 100°C. to 110°C. If stripping is required, residual organic solvent and water contained in the organic solvent is removed from the potassium silanolate. The stripping method is not critical, for example, the organic solvent may be stripped by distillation. The organic solvent is stripped from the potassium silanolate at a temperature of 80°C. to 150°C., at atmospheric pressure under a nitrogen blanket. More preferred is stripping the organic solvent at a temperature of 80°C. to 110°C. and at a pressure of 13.30 kPa (100 mm Hg). The preferred stripping parameters are a temperature of 90°C. to 100°C. and a pressure of 5.32 kPa (40 mm Hg). The following examples are provided to illustrate the present invention. Example 1 Preparation of a potassium silanolate having low branching using solid potassium hydroxide was evaluated. Octamethylcyclotetrasiloxane (200 g, 0.68 mole) was dissolved in cyclohexane (69 g) in a flask equipped with a mechanical stirrer, heating mantle and a condenser. Solid potassium hydroxide pellets (9.9 g) were added to the flask under a nitrogen purge and moderate agitation. The mixture was heated to remove water by azeotropic distillation at a temperature of 110°C. and distillation continued for 4 to 5 hours. At the end of azeotropic distillation the mixture temperature was 120°C. A total of 2.5 grams of water were removed from the flask by azeotropic distillation. Cyclohexane and water were stripped from the product by distilling at 150°C. for one hour at 5.32 kPa (40 mm Hg). The resulting product was a clear, viscous potassium silanolate. The potassium silanolate was analyzed using gas chromatography and determined to have a degree of branching of 800 ppm. Example 2 Preparation of potassium silanolate using aqueous potassium hydroxide was evaluated. Octamethylcyclotetrasiloxane (200 g, 0.68 mole) was dissolved in cyclohexane (69 g) in a flask equipped with a mechanical stirrer, heating mantle and a condenser at 90°C. Then an aqueous potassium hydroxide solution (22 g) consisting of 45 weight percent KOH in water (9.9 grams KOH, 0.18 mole) was added to the flask over a 0.5 hour period. The mixture was heated to remove water by azeotropic distillation at a temperature of about 95°C. and distillation continued for 12 hours. At the end of azeotropic distillation, the temperature was 125°C. During the 12 hour distillation, a total of 12.6 grams of water were removed from the flask by azeotropic distillation. Table 1 lists the quantity of water removed in one hour increments and the percent water removed. Cyclohexane was stripped from the product by distilling at 150°C. for 9 hours at atmospheric pressure. The resulting product was a clear, viscous potassium silanolate. The potassium silanolate was analyzed using gas chromatography and determined to have a degree of branching of 9550 ppm. Within a few days the potassium silanolate became cloudy and separated into three distinct phases. Water Removal At Elapsed Time (hours) Water Removed (ml) Percent Water Removed (%) 1 2.5 18.2 2 4.8 34.7 3 5.8 42.0 4 6.5 47.4 5 7.0 51.1 6 7.4 54.1 8 12.0 87.6 9 12.5 91.2 10 12.5 91.2 11 12.5 91.2 12 12.6 91.7

Claims: A method for the preparation of potassium silanolate which comprises reacting a mixture comprising a solid potassium hydroxide component and a polyorganosiloxane component of formula R 1 R 2 2 SiO(R 2 2 SiO) m R 3 or (R 2 2 SiO) n , where m is an integer from 1 to 1000, n is an integer from 3 to 20, R 1 is a hydroxyl group or an alkoxy group of 1 to 8 carbon atoms, R 2 is a hydrogen atom or an independently selected substituted or unsubstituted monovalent hydrocarbon group of 1 to 8 carbon atoms and R 3 is a hydrogen atom or an alkyl group of 1 to 8 carbon atoms; in the presence of an organic solvent which forms an azeotrope with water at a temperature of 90°C. to 150°C. thereby to form said potassium silanolate. A method according to claim 1, where the organic solvent comprises 10 to 40 weight percent of the weight of the mixture and the azeotrope has a boiling point within a range of 90°C. to 120°C. A method according to claim 1 or 2, where the molar ratio of the solid potassium hydroxide to the polyorganosiloxane is 4 to 1. A method according to any of claims 1 to 3, further comprising stripping said organic solvent from said potassium silanolate at a temperature of 80°C. to 150°C.

Inventors: GRAIVER DANIEL, LOMAS ARNOLD WADE, RASMUSSEN EDWARD THOMAS JR, WALL KELLY JAMES, GRAIVER, DANIEL, LOMAS, ARNOLD WADE, RASMUSSEN, EDWARD THOMAS JR., WALL, KELLY JAMES
Applicants: DOW CORNING, DOW CORNING CORPORATION
Application year: 1998
Main classification: C08G77
IPC codes: C08G77, C07F7