Preparation of polyorganosiloxanes by interfacial polymerization

Abstract: A process is disclosed for manufacturing high number average molecular weight polysiloxane copolymers by interfacial polymerization. These polysiloxanes contain phenylmethyl siloxane blocks and dimethyl siloxane blocks, alternately polymerized together to form an (A m B n ) x type copolymer. Our interfacial polymerization process is fast, proceeds smoothly at room temperature and is not reversible, i.e., no cyclic siloxane species are generated. The polysiloxanes are formed as thermoplastic elastomers suitable for use as sealants, fillers and films.

Description: This invention is directed to silicone copolymers prepared by nonaqueous interfacial polymerization, where polycondensation takes place at the interface between reactive starting materials dissolved in separate and immiscible solvents. A major advantage of interfacial polymerization of silicon containing monomers is the ability to control the structure of the resulting polymer chain and the composition of the copolymer, without the need for a conventional catalyst and without problems associated with rearrangement during polymerization. Interfacial polymerization of certain organic monomers is a known polycondensation reaction wherein monomers are dissolved in immiscible solvents. Polymerization occurs when the monomer in one phase diffuses from the bulk of the solution into the interface and reacts with the monomer from the other phase. The polymerization rate depends on the diffusion rate and reactivity of the functional groups on the monomers. With respect to our invention, a nonaqueous interfacial polymerization is conducted using a dihalopolysiloxane (preferably a dichloropolysiloxane) dissolved in one phase and a potassium silanolate or other metal silanolate is dissolved in the other phase. High molecular weight polysiloxanes and potassium chloride, or other chloride salt, are formed at the interface. Since the inorganic salt by-product is not soluble in the organic solvent phases, it precipitates and does not interfere with polycondensation. If the copolymer is insoluble in either solvent phase, it also precipitates and is removed from the interface. Among conventional interfacial polymerization reactions are the polycondensation of amines with acetyl chloride to form nylon (i.e., polyamides) and the reaction of alcohols with acids to form polyesters. Interfacial polymerization of these organic monomers typically provides faster polymerization rates than other types of polymerization reactions such as bulk or solution polymerization. Even more important is the fact that because stoichiometry between the monomers need not be precise, a higher number average molecular weight polymer is obtained. This is particularly critical for organic polycondensation reactions where an imbalance of a fraction of a percent causes the extent of polymerization to be greatly affected. Another advantage of interfacial polymerization is the formation of high number average molecular weight polymers at the interface, regardless of the overall percent conversion of the bulk amounts of the two monomeric reactants still in solution. Among other of the advantages offered by interfacial polymerization reactions in the synthesis of organic polymers are (i) the ability to prepare infusible polymers; (ii) the ability to synthesize polymers with chemically active substituents as well as heteroatoms; (iii) controlled crosslinking of the polymer structure; (iv) the ability to use cis- and trans- conformation without rearrangement; (v) the ability to prepare optically active polymers without decomposition of the intermediates; (vi) the ability to use short-chain and ortho-substituted ring intermediates; (vii) the ability to use thermally unstable intermediates to form thermally stable polymers; (viii) the ability to form block and ordered copolymers; (ix) the ability to form synthetic elastomers; (x) a direct method of forming polymer solutions and dispersions; (xi) a direct method for the polymerization and formation of polymer coatings and encapsulants; and (xii) a direct method for polymerization of monomers into fibrous particulates, fibers and films. We have unexpectedly found that many of these advantages are directly correlated and applied to the interfacial polymerization of silicon containing monomers in forming siloxane copolymers. Our invention relates to a method of making block copolymers by (A) reacting (i) a first nonaqueous organic solvent solution of an alpha, omega-dihalopolydiorganosiloxane at an interface formed with (ii) a second immiscible nonaqueous organic solvent solution of a silanolate or an organosilanolate of the formula R'' x Si(OM) 4-x or MO(R'' 2 SiO) n M, where R'' is an alkyl radical of 1-6 carbon atoms, an aryl radical, an alkenyl radical or an alkylamino radical; x is 0-2; n is at least one; and M is an alkali metal; and (B) recovering a block copolymer from the interface. A process is disclosed for manufacturing high number average molecular weight polysiloxane copolymers by interfacial polymerization. These polysiloxanes contain phenylmethyl siloxane blocks and dimethyl siloxane blocks, alternately polymerized together to form an (A m B n ) x type copolymer. Our interfacial polymerization process is fast, proceeds smoothly at room temperature and is not reversible, i.e., no cyclic siloxane species are generated. The polysiloxanes are formed as thermoplastic elastomers suitable for use as sealants, fillers and films. Our interfacial polymerization of organosilicon monomer and oligomer reactants provides structures and combinations of structures which cannot be obtained by other routes. One example is a well-defined structure of a dimethyldimethyl/phenylmethyl siloxane block copolymer. Block copolymers contain linear sequences of comonomer or oligomer A joined to linear sequences of comonomer or oligomer B. By "block copolymer" we mean a sequence distribution in copolymers of the type (A m B n ) x or -BBBAABBBAABBBBAAABBBBAAA-, where AA is a dimethyl block and BBB is a diphenyl block or a phenylmethyl block. By "dimethyl block", "diphenyl block and "phenylmethyl block", we mean a sequence of siloxane units shown below: One representative example of a block copolymer is: However, a major difference exists between interfacial polymerization of organosilicon reactants according to our invention, compared to previous methods used to polymerize organic monomers and that is in the use of water as one of the solvents. Although water has been used in many organic systems, no water is used in our interfacial polymerization method. This is because the use of water in the polycondensation of organosilicon monomers could be detrimental and lead to a low number average molecular weight, a complete loss of control over the polymer structure due to rearrangement and re-equilibration of the polymer in the presence of any residual soluble acid or base. Thus, water is detrimental if either an acid or base is formed, which leads to rearrangement and equilibrium polymerization, i.e., including some formation of cyclic siloxane species. Further, excess water can lead to low molecular weight silanol terminated end products. Another difference between our method and previous methods is the fact that if water is present, organosilicon monomers such as those used in this invention react with themselves; whereas in previous methods of organic polymer synthesis, the water soluble organic reactants were stable in the aqueous solution and reacted only across the interface. But, similar to organic polymers prepared by interfacial polymerization, the overall rate of conversion to the polymers herein is higher than by bulk polymerization, provided the polymer is continuously removed from the interface to sustain a constant rate. Removal of the polymer formed at the interface is relatively simple if the polymer has sufficient mechanical strength. In that case, it can be pulled out of the interface as with polyamides and polyesters. However, removal is more difficult if the polymer is a viscous liquid or a low modulus solid. As noted, we react an alpha, omega-dihaloorganosiloxane, (i.e., an alpha, omega-dichloropolydiorgano-siloxane) in mutually immiscible solvents across the interface with a silanolate or an organosilanolate. The silanolates are alkali-metal salts of organosilanols having the formula R'' x Si(OM) 4-x or the formula MO(R'' 2 SiO) n M. In the formulas, R'' is an alkyl radical of 1-6 carbon atoms, an aryl radical, an alkenyl radical or an alkylamino radical; x is 0-2; and n is at least one. Suitable alkyl and aryl radicals of R'' are methyl, ethyl and phenyl. Suitable alkenyl R'' radicals are vinyl, allyl, butenyl and hexenyl. Suitable aminoalkyl R'' radicals are aminopropyl and ethylene diaminopropyl. M is an alkali metal such as lithium, sodium, potassium, rubidium and cesium. Sodium and potassium are the preferred alkali metals. For purposes of our invention, the value of x is preferably 2; and the value of n is preferably to 20, more preferably 3-10, and most preferably 4-8. Examples of some suitable silanolate compounds are disodium diphenylsilanolate (C 6 H 5 ) 2 Si(ONa) 2 , disodium dimethylsilanolate (CH 3 ) 2 Si(ONa) 2 , disodium methylaminopropylsilanolate (CH 3 ) [H 2 NCH 2 CH 2 CH 2 ]Si (ONa) 2 , their potassium equivalents, potassium dimethylsilanolate KO[(CH 3 ) 2 SiO] n K and potassium phenylmethylsilanolate KO[(C 6 H 5 )(CH 3 )SiO] n K where n is defined above. Silanolates are obtained by the reaction of diorganoalkoxysilanes with alkali-metal hydroxides or diorganosilanols with alkali metals or alkali-metal hydroxides. Such methods and their details are found, for example, in British Patent 631,506 (November 3, 1949) and in US Patent 3,641,090 (February 8, 1972). Synthesis of potassium dimethylsilanolates are also achieved by the equilibration reaction of octamethylcyclotetrasiloxane with potassium hydroxide. While high viscosities are common when preparing potassium dimethylsilanolates having K:Si mole ratios greater than 1:6, significant lower viscosity silanolates are made by the incremental addition of the metal hydroxide. This method has the advantage that it is possible to prepare relatively short chain sizes of potassium dimethylsilanolate polymers. This is accomplished with a 2K:8Si ratio (16 mole % K) or with a siloxane chain length of eight dimethylsiloxy units. Other potassium dimethylsilanolates can be prepared with lower ratios, i.e., 2K:5Si, 2K:4Si and 2K:3Si. Potassium phenylmethylsilanolate polymers are prepared in a similar fashion to that described above for potassium dimethylsilanolate. In addition, potassium phenylmethylsilanolate polymers are prepared by condensing KOH with phenylmethylsiloxane hydrolysates, i.e., HO((C 6 H 5 ) (CH 3 )SiO] x H. Silanolates were prepared by the equilibration reaction of potassium hydroxide or lithium hydroxide with octamethylcyclotetrasiloxane or tetraphenyltetramethylcyclotetrasiloxane for use in our interfacial polymerization reactions. These silanolates are shown in Table I. In the table, the abbreviations "diMe" and PhMe" indicate dimethylsilanolate and phenylmethylsilanolate, respectively. Some alpha, omega-dichloropolydiorganosiloxanes usable herein are l,3-dichloro-1,3-dimethyl-1,3-diphenyldisiloxane, 1,5-dichlorohexamethyltrisiloxane, 1,71,7-dichlorooctamethyltetrasiloxane, 1,3-dichlorotetraisopropyldisiloxane, 1, 3-dichlorotetramethyldisiloxane and 1,3-dichlorotetramethyldisiloxane There are several criteria for establishing the suitability of any solvent for use in our invention. First, solvent I and solvent II are not miscible. Second, solvent I and solvent II are nonaqueous. Third, solvent I is a good solvent for monomer or oligomer I but not for monomer or oligomer II. Fourth, solvent II is a good solvent for monomer or oligomer II but not for monomer or oligomer I. Fifth, the resulting products are insoluble in at least one of the phases. Generally, a polar solvent in combination with a non-polar solvent may satisfy these five conditions. Given these criteria, we found that a suitable polar solvent for the alpha, omega-dihaloorganosiloxane phase was acetonitrile CH 3 CN and a suitable non-polar solvent for the silanolate or organosilanolate phase was cyclohexane C 6 H 12 . Generally, reactions of organohalosiloxanes with metal silanolates proceed according to the scheme: ≡Si-X + MO-Si≡ → ≡Si-O-Si≡ + MX where M is a Group IA metal such as Na or K and X is halogen. Thus, where M is Na and X is Cl, for example, the reaction is: ≡Si-Cl + NaO-Si≡ → ≡Si-O-Si≡ + NaCl Such reactions when performed by our methods are conducted without stirring and at temperatures generally in the range of 10-95°C. Typically, interfacial polymerization reactions are carried out when the alpha,omega-dichloropolydiorganosiloxane solution is slowly added to the alkali metal silanolate solution. The solutions are then allowed to stand at room temperature for 24 hours. Quite unexpectedly, we found that in some of the reactions of potassium phenylmethylsilanolate in cyclohexane and 1,5-dichlorohexamethyltrisiloxane in acetonitrile, elastomeric products (gels) were produced. Further, the polymers contained only low amounts of cyclic siloxane species which were present in the silanolate prior to polymerization. However, in other interfacial polymerizations utilizing potassium phenylmethylsilanolate in cyclohexane with 1,5-dichlorohexamethyltrisiloxane in acetonitrile, the yield was an oil, depending upon the amount of ionic character of the silanolate. In these reactions, we used various potassium phenylmethylsilanolate chain lengths containing different amounts of ionic character such as 2K:8Si, 2K:5Si and 2K:4Si. We surprisingly found that the larger silanolate chain species (i.e., 2K:85i) formed viscous oily products, while the smaller silanolate chain species formed elastomeric products, i.e., gels, after interfacial polymerization. In all cases, the by-product potassium chloride precipitated and was analyzed by X-Ray Diffraction (XRD). The following examples illustrate our use of potassium phenylmethylsilanolates in an interfacial polymerization reaction. Example I A potassium phenylmethylsilanolate having the ratio 2K:8Si of potassium to silicon, was prepared by adding to a flask 157.7 grams of phenylmethylsiloxane hydrolysate HO[(C 6 H 5 )(CH 3 )SiO] 8 H, 60 grams of cyclohexane and 19 grams of 45% potassium hydroxide (8.55 grams KOH, 0.153 M). After reaction, water was removed and the flask was cooled to 60°C. Using a syringe, 60 milliliters of dry acetonitrile was added to the flask as a top layer. Then a solution of 32.32 grams (0.117 M or 0.233 equivalents C1 - ) of 1,5-dichlorohexamethyltrisiloxane in 20 milliliters of acetonitrile, was slowly transferred to the top layer of the flask. Upon reaction of the potassium phenylmethylsilanolate in cyclohexane with the 1,5-dichlorohexamethyltrisiloxane in acetonitrile, there was obtained a clear polymeric oil with a number average molecular weight of 9,455. Nuclear Magnetic Resonance (NMR) and Fourier-Transform Infrared Spectroscopy (FTIR) analysis confirmed formation of the polymer. Infrared analysis showed an increase in methyl groups to phenyl groups, which evidences addition of the trisiloxane backbone to the silanolate. NMR showed only a small amount of polymer branching (i.e., 0.5 mole %) and 16 % of cyclic siloxane species. The polymer contained two different difunctional R 2 SiO 2/2 "D" blocks. One block was (CH 3 ) 2 SiO 2/2 and the other block was (C 6 H 5 ) (CH 3 )SiO 2/2 , in a ratio of three to eight, respectively. Example II We repeated Example I using phenylmethylsiloxane hydrolysate HO[(C 6 H 5 ) (CH 3 )SiO] 5 H and adjusted the amount of KOH to prepare a potassium phenylmethylsilanolate containing two potassium species to five silicon units (2K:5Si) in cyclohexane. This silanolate yielded a very viscous polymeric fluid when reacted with 1,5-dichlorohexamethyltrisiloxane in acetonitrile. An exotherm was noted during the interfacial polymerization reaction. A polymer number average molecular weight of 95,500 was determined by Gel Permeation Chromatography (GPC) analysis. NMR showed that the polymer contained (CH 3 ) 2 SiO 2/2 and (C 6 H 5 ) (CH 3 )SiO 2/2 blocks in the ratio 3:5, with some polymer branching (i.e., 0.92%) and no new formation of cyclic siloxane species over the 8.5% cyclic siloxane species present in the silanolate prior to the reaction. Example III We repeated Example I using phenylmethylsiloxane hydrolysate HO[(C 6 H 5 ) (CH 3 )SiO] 4 H and again adjusted the amount of KOH to prepare a potassium phenylmethylsilanolate containing two potassium species to four silicon units (2K:4Si) in cyclohexane. This silanolate, when reacted with a solution of 64.1 grams (0.231 M or 0.463 equivalents Cl - ) of 1,5-dichlorohexamethyltrisiloxane in 30 milliliters of acetonitrile, yielded a polymer that was a clear gel. This elastomeric product was soluble in N-methylpyrrolidone. An exotherm due to the formation of potassium chloride was observed during the reaction. By using the above procedures and reacting potassium dimethylsilanolate or potassium phenylmethylsilanolate in cyclohexane with an alpha, omega-dichloropolydiorganosiloxane in acetonitrile, one can prepare block copolymers of various block sizes. This is achieved by using potassium silanolates of various ratios of Si:K.

Claims: A method of making a block copolymer comprising (A) reacting (i) a first nonaqueous organic solvent solution of an alpha, omega-dihalopolydiorganosiloxane at or near an interface formed by the first nonaqueous organic solvent solution and (ii) a second immiscible nonaqueous organic solvent solution of a silanolate or organosilanolate of formula R'' x Si(OM) 4-x or MO(R'' 2 SiO) n M where R'' is an alkyl radical of 1-6 carbon atoms, an aryl radical, an alkenyl radical or an alkylamino radical; x is 0-2; n is at least one; and M is an alkali metal; the second solvent being immiscible in the first solvent and organic groups on the alpha,omegaalpha,omega-dihalopolydiorganosiloxane being different from organo groups on the silanolate or organosilanolate, and (B) recovering the block copolymer at or near the interface. A method according to Claim 1 in which the first organic solvent is acetonitrile and the second organic solvent is cyclohexane. A method according to claims 1 or 2 in which the alpha,omega-dihalopolydiorganosiloxane is selected from the group consisting of 1,3-dichloro-1,3-dimethyl-1,3-diphenyldisiloxane. 1,5-dichlorohexamethyltrisiloxane, 1,71,7-dichlorooctamethyltetrasiloxane, 1,3-dichlorotetra-isopropyldisiloxane, 1,3-dichlorotetramethyldisiloxane and 1,3-dichlorotetraphenyldisiloxane. A method according to claims 1 or 2 in which the silanolate or organosilanolate has the formula MO(R" 2 SiO) n M where R'' is an alkyl radical of 1-6 carbon atoms, an aryl radical, an alkenyl radical or an alkylamino radical; n is 1-20; and M is an alkali metal. A method according to claim 4 in which the silanolate or organosilanolate is potassium phenylmethylsilanolate of the formula KO[(C 6 H 5 )(CH 3 )SiO] n K where n is 4-8. A block copolymer obtainable by the method defined in any of claims 1 to 5. Sealants, fillers or films obtainable from the block copolymer in claim 6.

Inventors: GRAIVER DANIEL, MATISONS JANI G, PROVATAS ARTHUR, WADE LOMAS ARNOLD, GRAIVER, DANIEL, MATISONS, JANI G., PROVATAS, ARTHUR, WADE LOMAS, ARNOLD
Applicants: DOW CORNING, UNIV SOUTH AUSTRALIA, DOW CORNING CORPORATION, UNIVERSITY OF SOUTH AUSTRALIA
Application year: 1997
Main classification: C08G77
IPC codes: C08G77