PROCESS FOR THE MANUFACTURE OF SILICON CARBIDE

Abstract: Novel branched polysilahydrocarbon precursors for sili­ con carbide are prepared by reacting a halosilane monomer and a hydrocarbon olefin monomer in the presence of an active metal, such as potassium. The novel branched polysilahydrocarbon precursors are effective in the produc­ tion of silicon carbide ceramic compositions.

Description: BRANCHED POLYB I LANYDROCARBON BRECURSORS FOR SILICON CARBIDE FIELD OF THE INVENTION The present invention relates to novel branched polysilahydrocarbon compositions, to their production from selected monomer systems, and to their use in the production of silicon carbide ceramic compositions. The U.S. Government has rights in this invention pursuant to Contract N-00014-81-C-0682, awarded by the Office of Naval Research, Department of the Navy. DESCRIPTION OF THE PRIOR ART Silicon carbide has long been known and appreciated for its chemical inertness, high temperature stability, semi-conductor properties, and especially its extreme hardness. In fact. the hardness of silicon carbide approaches that of diamond and boron nitride. Silicon carbide was originally prepared by reacting inorganic.silicon materials, such as silica or sand, with a carbon source, such as coke or graphite, at extremely high temperatures. The silicon carbide from such reactions was generally intractable and infusible and could only be shaped into articles by mixing with an appropriate binder and reprocessing at high temperatures once again. A lower temperature crystalline modification of silicon carbide has also been prepared in powdered form. either by gas phase or solid state reaction. While this form of silicon carbide is more sinterable than the high temperature form mentioned above, it is still unsuitable for the formation of finely shaped articles such as fibers. Silicon carbide also has been prepared by vapor deposition from chlorosilanes (see U.S. Patent No. 3,157,541). This approach is useful for the electronics industries, and has been used for the preparation of shaped articles1 such as fibers. Still more recently, Japanese workers have reported in U.S. Patent No. 411001233 the preparation of shaped articles, particularly fibers by pyrolysis of preshaped polycarbosilanes. The latter are soluble and thermoformable by standard methods and are prepared by a prepyrolysisS rearrangement/polymerization of cyclic or linear polydimethylsilanes, which in turn can be prepared from Me2SiCl2 and active metals (see U.S. Patent 4,052,430). These polycarbosilanes have numerous uses, being convertible to SiC in a variety of moldings and composites as taught in U.S. Patent Nos. 4.110,386;4.117;057; 4,122,139; 4,134,759; and 4,147,538. Other routes to preparing such polycarbosilanes have been disclosed by the same inventors in U.S. Patent No. 4,1591259. Another group of Japanese inventors has disclosed in U.S. Patent No. 4.105,455 silicon carbide compositions derived from insoluble polycarbosilanes, which are also prepared by prepyrolysis of polydimethylsilanes. A third Japanese group discloses in Chemical Abstracts, 91, (1979) 215596P the preparation of presumably branched polydimethylsilanes from mixtures of Me3SiCl, Me2SiCl2, and MeSiCl3; however, these polydimethylsilanes still require a prepyrolytic conversion to polycarbosilane before ultimate conversion to silicon carbide. The latter research group also discloses reaction of a mixture of Me2SiC12 and CH2sCHSiMeC12 with sodiumZpotassium dispersion to give a copolymer in which the monomer units are connected by SiSi bonds [see Chem. Abstr., 91, l24210s (1979)). Other approaches to silicon carbide precursors include copolymers of Me2sicl2 and XMeSiC12 by R. West and co-workers (U.S. Patent Nos. 4,260,780 and 4,324,901) and a polymeric residue from higher boiling by-products of the well known direct reaction of MeCl with silicon metal (U.S. Patent No. 4,310,651). Silicon carbide has been prepared by pyrolysis of silicone resins and by pyrolysis of rice hulls, both of which would be low yield processes on a weight basis. In related work, polycarbosilanes have been pyrolyzed to shaped articles containing silicon carbide and silicon nitride, (see U.S. Patent No. 3,853,567) with the polycarbosilazanes being prepared from prepyrolysis of carbosilazanes. Polysilazanes have been mixed with standard organic polymers and spun to fibers, which have been pyrolyzed to silicon nitride/silicon carbide fibers (see U.S. Patent No. 3,892,583). The polymeric residue employed as a silicon carbide source has been modified with a variety of agents to reduce chlorine content and increase safety toward handling or increase silicon carbide yields. These modifications are disclosed in U.S. Patent Nos. 4,310,481; 4,310,482: 4,298,588; 4,314,956: 4,298,559; 4,340,619; and 4,312,970. Recent work has shown that branched polycarbosilanes can be prepared in one step, and are directly convertible to silicon carbide by atmospheric pressure pyrolysis (U.S. Patent Application Serial No. 361,106 filed March 23, 1982). The one-step preparation of polysilanes containing reactive olefinic groups, and the direct conversion of such polysilanes to silicon carbide, has also been discovered (U.S. Patent Application 480,700 filed March 31, 1983). Branched polysilahydrocarbons have been prepared by free radical polymerization of unsaturated silanes such as MexSi(CHzCH=CH2)4-x where x = 0-2, or Ne3SiC6H4 CH=CH2. These materials are highly crosslinked, infusible, and insoluble, but are thermally convertible to carbonizeed substances containing silicon" (including SiC). They also differ substantially in composition from the polysilahydrocarbons of the instant invention (see U.S. Patent 2,697,029). Thus, there are now a variety of organosilicon approaches to silicon carbide, none of which involve coreactions of hydrocarbon olefins with halosilanes in the presence of active metals. There is, however, unrelated prior art involving coreactions of hydrocarbon olefins with halosA anes in the presence of active metals. The products from such prior art reactions are not effective precursors for silicon carbide, as will be demonstrated in the examples which follow. U.S. Patents 3,187,031 and 3,187,032 disclose silahydrocarbon polymers prepared from monohalo-or dihalosilanes and hydrocarbon olefins in the presence of an active metal and a solvent. These two patents, however, disclose only linear polysilahydrocarbons, which are not effective SiC precursors when compared to the branched polysilahydrocarbons of the instant invention. Russian workers have also reacted hydrocarbon olefins with halosilanes in the presence of active metal and a solvent [see Proc. Acad. Sci. USSR, 1962, p 1228; 1964, p 840; Bull, Acad. Sci. USER, 154, 76 (1964)). These workers prepared either linear polysilahydrocarbons or used 2/1 molar ratios of hydrocarbon olefins to halosilane reactants, such that the products would not be effective SiC precursors when compared to the polysilahydrocarbons of the instant invention. French workers have reacted MeSiHCl2 with isoprene in the presence of magnesium metal tSynth. React. Inorg. Metal-Org. Chem., 4, 133 (1974)), obtaining a silacyclopentene product and a polysilahydrocarbon polymer. It will be shown that that polymer, prepared with magnesium, differs from a polysilahydrocarbon according to the instant invention prepared with potassium, and that the latter polymer is a much more effective precursor for SiC. SUMMARY OF THE INVENTION It has been found that novel branched polysilahydrocarbons which can be pyrolyzed to improved yields of SiC ceramic compositions can be prepared in a one-step reaction from mixtures of hydrocarbon olefins and halosilane monomers. More particularly, this invention consists of a process for the production of silicon carbide ceramic compositions which comprises, first, reacting at least one compound of formula (I). (I) (CH2=CH) aRbSXc(CH2X)dHe wherein R is lower alkyl, Xis halo, a is O or 1, b is 0-3, c is 1-4, d is 0-4, e is 0-2, a+b+c+d+e totals 4, and a+c+d+e totals at least 3, and at least one compound of formula (II), (Il) R' '2C = CHR'' wherein the R$' groups are individually selected from hydrogen,methyl, phenyl, and vinyl groups, such that at least one R'' group is phenyl or vinyl; with active metal or metals in an inert solvent medium at an elevated temperature to form a branched polysilahydrocarbon and, subsequently, pyrolyzing the branched polysilahydrocarbon in an inert atmosphere to form ceramic compositions consisting primarily of silicon carbide. The novel branched polysilahydrocarbons themselves constitute a key part of the invention. DESCRIPTION OF THE PREFERRED EMBODIMENTS In a broad aspect, this invention contemplates a process for the production of novel branched polysilabydrocarbons which comprises reacting. with active metal or metals in an an inert solvent medium1 a compound system comprising at least one silyl monomer of formula (I), (CH2=CH) aRbSiXc (CH2X)dHe (I) wherein R, X, a, b, c,d, and e are as defined above and at least one hydrocarbon oleo in monomer of formula (II), R'',C=CHR'' (II) wherein R'' is as defined above. The preferred hydrocarbon olefin monomers are styrene, a-methylstyrene, butadiene, and isoprene. The compound system contains at least two different monomers. one of formula (I) and one of formula (II). such compound system being selected to favor formation of #SiC# and #SiSi# bonds. The novel branched polysilahydrocarbons may be described as compositions which comprise units of the formula: EMI7.1 wherein R is lower alkyl (preferably methyl), x is halo (preferably chloro), a is O or 1. b is 0-3, c is 1-4, d is 0-4, e is 0-2, a+b+c+d+e totals 4, with the provision that in each of the plural units. a,b,c,d,e, and R may differ (depending on the monomers from which they originate). and that in a plurality of the units. a+c+d+e totals at least 3. such that those units are branching sites. and units derived from the hydrocarbon olefin monomers. For example. styrene provides -CH2CH°- units, a-methylstyrene provides -CH2CMe°- units, isoprene provides -CH2CMe=CHCH2- units and butadiene provides -CH2CH-CHCH2 - units. A further aspect of the invention consists in pyrolyzing, by means in themselves known to those skilled in the art, the novel branched polysilahydrocarbon compositions of the present invention in order to produce silicon carbide and products containing silicon carbide. The following formulas (wherein R and X have the meanings indicated above) illustrate classes of compounds which can be utilized in the formation of the novel branched polysilahydrocarbons of the present invention: Monomers of Formula (I) CH2=CHSiX2(CH2X) CH2=CHSiX3 CH2=CHSiR2(CH2X) R3Si(CH2X) CH2=CHRSiX(CH2X) R2Si(CH2X)2 SiX4 RSi(CH2X)3 R3Six RSiX(CH2x)2 CH2=CHR3Si RSiX2(CH2X) Six(CH2X)3 CH2=CHRSiX2 SiX2(CH2X)2 CH2=CHR2SiX R2SiX(CH2X) RSiX3 R2SiX2 SiX3(CH2X) X3SiH RSiHX2 X2SiH2 R2SiHX Monomers of Formula II Butadiene CH2=CHCH=CH2 Isoprene CH2=CMeCH=CH2 Styrene CH2=CH# &alpha; ;-Methylstyrene CH2=CMe# Piperylene MeCH=CHCH=CH2 As indicated, it is preferred to use a mixture (i.e., two or more monomer compounds selected from different classes) to make the novel branched polysilahydrocarbons. Such mixtures include, but are not limited to: MeSiC13/isoprene, MeSiC13/styrene, Me3SiCl/isoprene/CH2=CHSiMeCl2 MeSiHCl2/isoprene, MeSiHCl2/styrene, ClCH2SiMeC12/isoprene, ClCH2SiMeCl2/styrene, and the like. The preferred silyl monomers for providing branching are thus MeSiCl3 MeSiHC12, ClCH2SiMeCl2, and CH2 =CHSiMeCl2. Molar ratios of silyl and hydrocarbon monmers are selected to promote formation of -SiC- and =SiSi= bonds as opposed to =CCE bonds, to maximize content of branched silyl units while maintaining tractability, and to maximize the yield of SiC ceramic composition on pyrolysis. Molar ratios thus depend on the monomers used and may vary from a minimum of 0.67, as for MeSiCl3/styrene, to 2.0 or higher for ClCH2SiMeCl2/isoprene, for example. Ratios below 0.67, such as 0.5 or less, provide polymers too deficient in contained silicon to be effective SiC precursors. When hydrosilyl monomers, such as MeSiHC12 and Me SiHCl are used, particularly 2 when the active metal is potassium, a portion of the hydrosilyl groups survive the reactions and yield branched, hydrosilyl-modified polysilahydrocarbons. Another portion of the hydrosilyl groups undergo reactions wherein the hydrogen (H) is lost and a new bond to silicon or carbon is formed. Hydrosilyl group retention (1) or loss (2) are shown with methyldichlorosilane as a model. EMI10.1 Thus, NeSiHCl2 provides trifunctional MeSi branching sites during polysilahydrocarbon preparation, as well as providing -SiMeH- units which create additional branching sites during the thermal conversion of polysilahydrocarbon to SiC ceramic compositions. The property which the branched polysilahydrocarbons of the instant invention possess, namely their ability to be converted into silicon carbide ceramic compositionsin higher yields than prior art polysilahydrocarbons is believed to be due to the presence of branched silyl units in the polymer backbone. The degree of branching and the molecular weight can be controlled by appropriate choices of starting monomer systems and the molar ratios within such monomer systems, such that the products range from soluble oils to soluble solids to insoluble, infusible solids. Since the branching structures of the polysilahydrocarbons of the present invention derive from the inherent functionalities of the monomers used, the yield of silicon carbide derived from such polycarbosilanes increases with the relative content of branched units, whether such units derived from the preparative chemistry or are created during the pyrolysis process. While not wishing to be bound by speculative theory, it appears that branching during pyrolysis occurs by reactions between hydrosilyl groups, generating -SiSi- bonds, or between hydrosilyl groups and unsaturated groups such as vinyl groups, generating ,SiCSbonas. PROCESSING In the present invention, a monomer system is reacted with an active metal in an inert solvent medium at an elevated temperature to generate novel branched polysilahydrocarbons. The preferred active metal is potassium for reasons of high reactivity and low melting point. Other active metals are less reactive; they may be used if longer reaction times are acceptable. Alloys such as potassium/sodium may also be used. According to the prior art, lithium may destroy all hydrosilyl functionality. The preferred solvent is anhydrous tetrahydrofuran. However, higher boiling solvents such as dioxane, 1,2-dimethoxyethane, and the like, or hydrocarbons such as toluene, xylene, or octane, and the like, can be used, particularly with the less reactive metals. Hexamethylphosphoramide may also be used, but it is more costly and is a suspected carcinogen. Blends of the above solvents can be used, as can typical promoters for these types of reactions such as naphthalene or crown ethers. The combination of potassium as the active metal and tetrahydrofuran as the solvent allows reactions to occur at the reflux temperature of tetrahydrofuran. which is just above the melting point of potassium. This combination does not allow significant reaction of chlorosilyl groups with the tetrahydrofuran solvent; such reactions have been observed with sodium and magnesium. The combination also allows retention of a portion of the charged hydrosilyl groups. In the present invention, potassium provides polymers having different structures than those prepared with magnesium. The potassium-prepared polymers are much more effective precursors for SiC. The polysilahydrocarbon-forming reactions of the present invention can be run in standard laboratory glassware or chemical equipment, under inert atmospheres at atmospheric pressures, with provisions for external heating and cooling. stirring. and for incremental addition of mixtures of monomers. Thus, the process of the present invention regarding polysilahydrocarbon preparation is not narrowly critical with regard to equipment and requires no extraordinary equipment. In a typical preparation, a weighed amount of potassium metal is placed in anhydrous tetrahydrofuran under an inert atmosphere. Heat is applied to reflux, melting the potassium. and addition of the monomer system is begun. with stirring. The reactions are often sufficiently exothermic at controlled addition rates to maintain reflux without application of external heat. After completion of addition. heat may be reapplied for any specified time period. Illustrative examples are supplied below. Reaction conditions are thus not narrowly critical except that reaction temperature should be maintained above the melting point of the active metal and stirring should be maintained to prevent caking of by-product salts. A slight excess of the active metal is desired to insure consumption of a majority of halosilyl groups. Reactions can be terminated by addition of an alkylating agent. such as methyl chloride, or a protic material, such as water. Salt by-products are removed by filtration or water washing. and the mother liquor concentrated by stripping. The resultant polysilahydrocarbon solution can be added to a non-solvent medium such as a methanol/acetone. precipitating the tractable solid fraction, which is collected and dried. The non-solvent mixture can be stripped to recover the liquid polysilahydrocarbon residue0 while the filtered salt can be water-washed to isolate insoluble polysilahydrocarbons. if any. These reaction procedures are familiar to those skilled in the art and are typical of numerous active metal reactions. SILICON CARBIDE The novel branched polysilahydrocarbons of the present invention, ranging from soluble oils to insoluble solids, can be converted to silicon carbide compounds by themselves or in mixture with other components as disclosed for prior art polycarbosilanes, simply by heating in an inert atmosphere over specified time periods up to 1200-C or beyond. Most useful of the branched polysilahydrocarbons of the present invention are those which are, at room temperature, normally solid and soluble in non-protic organic solvents. They can be thermoformed into a variety of shapes such as pellets, fibers, films, etc., or can be dissolved in a variety of solvents including carbon tetrachloride, methylene dichloride, trichloromethane, toluene, tetrahydrofuran, dioxane, and the like, to be cast from solution as films or spun from solution as fibers. The range of polysilahydrocarbons, however, can be used as binders for the shaping of infusible insoluble powders such as silicon carbide or silicon nitride in the same fashion as prior art polycarbosilanes. Both shaped polysilahydrocarbon articles and shaped polysilahydrocarbon-bound articles can be converted to silicon carbide compositions by atmospheric pressure pyrolysis. The shaping, spinning, and casting of the polysilahydrocarbons of the present invention can be performed in commercially available equipment designed for such purposes and known to those skilled in the art. Similarly. the pyrolyses are also performed in commercially available equipment designed for such work and also known to those skilled in the art. Sintering aids typical of such high temperature reactions may be employed if desired. Whereas the exact scope of the instant invention is set forth in the appended claims, the following specified examples illustrate certain aspectseof the present invention and, more particularly, point out methods of evaluating the same. However, the examples are set forth for illustration only and are not to be construed as limitations on the present invention except as set forth in the appended claims. All parts and percentages are by weight unless otherwise specified. EXAMPLES All reactions were run in standard laboratory glassware of various sizes using heating mantles, mechanical stirrers with glass or stainless steel blades, thermometers, wet ice or cooled liquid condensers. and provisions for maintenance of nitrogen or argon atmospheres. Temperatures are reported in Centigrade degrees, and the abbreviations Me, g, mm, ml, min, hr, and THF represent methyl, gram, millimeter, milliliter, minute, hour, and tetrahydrofuran, respectively. Reported yields are based on theoretical yields calculated from the silane mixture charged. Laboratory pyrolyses were run in quartz reactors in a tube furnace up to 8000C, and in alumina reactors in a second tube furnace from 800do to 1200 C. No attempt was made to maximize yields by varying pyrolysis conditions. Example A: Reaction of 1/1 Me2SiC12/CH =CH with K in THF Under an inert atmosphere , 21.3g (0.54 mol) of K metal and 179.3g of anhydrous THF were combined in a 50 ml 3-necked round-bottomed flask, which was then fitted with mechanical stirrer (stainless steel blade), thermometer, addition funnel, and Dewar condenser (wet ice). with provisions for maintaining the inert atmosphere. The addition funnel was charged with a mixture of 33.5g (0.26 mol) of Me2SiCl2 and 27.Og (0.26 mol) of styrene and contents of the flask heated to reflux melting the K. Addition of the monomer mixture was completed in 31 min, and the reaction mixture then heated at reflux for 3 hrs., followed by cooling, termination with 6.63g H20/17.24g THF, and neutralized with 2.5g conc. HC1. Removal of solvent by vacuum stripping left 41.2g (97.8%) of soluble solid product. Pyrolysis of this material to only 700' left only 3.4% of residue, confirming that linear polymeric products of U.S. 3,187,031 are not effective SiC precursors. Example B: Reaction of 1/1 Ne2SiCl2/CH2=CMeCH=CH2 with K in THF The procedure of Example A was repeated using 23.5g (0.60 mol) of K metal. 421.7g anhydrous THF, and a mixture of 36.6g (0.29 mol) of Me2SiC12 and 19.4g (0.29 mol) of isoprene. Reaction mixture was heated at reflux for 5 hrs. after completion of addition. Workup yielded 10.6g (29.6S) of polymeric residue, b.p. greater than 0.7 mbar 88 /##### mbar Pyrolysis of this product to 700 left only 0.8% of residue, confirming that the linear polysilahydrocarbon product of U.S. Patent 3,187,032 is not an effective siC precursor. Example C: Reaction of 1/1 MeSiHCl2/CH2=CMeCH=CH2 with Mg in THF In a 250 ml apparatus assembled as in Example A were combined 60 ml THF and 2.4g (0.1 mol) of Mg powder. Isoprene (6.4g, 0.094 mol) was added rapidly, followed by dropwise addition of 10.0g (0.087 mol) of MeSiHC12. After an exothermic reaction to 470, , the mixture was stirred at room temperature for 2 hrs. Workup yielded 5.34g (55%) of nonvolatile polymer, b.p. greater than 1 1 mbar 44 /#####. Pyrolysis of this product to 700 yielded 10.6% of SiC composition. Instrumental analyses Showed this product to differ substantially from that of Example 6 in terms of the structural units present in the polymers. SiC yield was substantially below that of Example 6. Example 1: Reaction of 2/3 MeSiCl3/CH2=CH# with K in THF She procedure of Example A was followed using 22.8g (0.58 mol) of K metal 172.9g anhydrous THF. and a mixture of 27.5g (0.18 mol) osf MeSiC13 and 28.8g (0.28 mol) of styrene. Reaction was heated at reflux for 4 hrs after end of addition. Workup yielded 50.0% of soluble solid polysilahydrocarbon and 34.4% insoluble solAid polysilahydrocarbon. Pyrolysis of the soluble slid to 12000 yielded 28,0S of SiC composition. The product of this example. with branching introduced by units derived from MeSiCl3. confirms that branched structures are needed for conversion to SiC when results are compared to those of-Example A. Example 2: Reaction of 2/3 MeSiCl3/CH2=CMeHC=CH2 with K in THF The procedure of Example 1 was followed using 27.6g (0.71 mol) of K metal. 408.8 anhydrous THF, and a mixture of 33.5g (0.22 mol) of MeSiCl3 and 22.8g (0.34 mol) of isoprene. Workup yielded Z8.2g (85.2t) of soluble solid polycarbosilane, b.p. greater than 28 /0.08mm. Pyrolysis up to 1200 yielded -25.0% of SiC composition. The product of this example. with branching introduced by units derived from MeSiCl3, confirms that branched structures are needed for conversion of SiC when results are compared to those of Example B. Example 3: Reaction of 0.85/0.3/1.0 Me3SiCl/CH2=CMeCH=CH2/ CH2=CHSiMeCl2 with K in THF The procedure of Example 1 was followed using 23.6g (0.60 mol) of K metal. 289.4g of anhydrous THF, and a mixture of 18.6g (0.17 mol) of Me3SiCl, 4.1g (0.06 mol) of isoprene, and 28.5g (0.20 mol) of CH2=CHSiMeCl2. Workup yielded 18.8g (61.1%)of soluble solid polycarbosilane. Pyrolysis to 700- yielded 24.9% of SiC composition, confirming that branching units derived from CH2=CHSiMeCl2 are needed for effective conversion to SiC when results are compared with Example B. Example 4: Reaction of 1/1 MeSiCl2/CH2=CHSiMe3 with K in THF The procedure of Example 1 was followed using 31.64g (0.81 mol) of K metal. 422.9g of anhydrous RF, and a mixture of 44.3g (0.385 mol) of MeSiHCla and 38.5g (0.395 mol) of CH2=CHSiMe3. Workup yielded 24.36g of soluble 1.3 mbar solid (44%) b.p. greater than 35 /###### mbar Pyrolysis of this material to 1200 yielded 28.5% of SiC composition. Analytical data and pyrolysis results confirm that the use of MeSiHC12 in this reaction let to formation of trifunctional branching sites in the polymer backbone resulting in effective thermal conversion to SiC. While the product of this example does not contain units derived from a hydrocarbon olefin, it is included to demonstrate both formation of trifunctional units during reaction of MeSiHCl2 and formation of trifunctional units on pyrolysis by interaction of residual #SiH groups vith olefinic groups (see next example). Example 5: Copyrolysis of Products of Examples 3 and 4 Equal weights of soluble solid products from Example 4 and Example 5 were dissolved in THE and the solutions mixed. The resultant clear solution was stripped to remove the solvent and the resultant solid pyrolyzed to 1200-. The yield of Sic composition was 38.7%. well above that obtained in either Example 3 or Example 4. The results confirm generation of new trifunctional (crosslinking) sites during pyrolysis from reaction of residual =SiH groups in the product of Example 4 vith unsaturated groups present in the product of Example 3. Example 6: Reaction of 1/1 MeSiCl2/CH2=CMeCH=CH2 with K in THF The procedure of Example 2 was followed using 31.42g (0.804 mol) of K metal, 373.5g of THF, 43.7g (0.38 mol) of MeSiHCl2, and 25.5g (0.38 mol) of isoprene. An additional 280 ml of"THF was added after completion of addition, which required 205 min with heat on, due to viscosity buildup. Workup yielded 58.9% of volatile product, b.p. up to 158 /0.32 mbar, and 8.93g (25.2%) of heavies. Pyrolysis of the latter to 1200 yielded 49.5% of SiC composition. Analysis of the heavies before pyrolysis showed that 80% of the MeSiHCl2 had reacted to form trifunctional MeSi# units, while 20% reacted to form difunctional -MeSiH- units. Analysis also confirmed that the heavies differed substantially in structure from the product of Example C. Results show that the polymeric product of this example, made with potassium, provides a much higher yield of silicon-carbide ceramic composition than does the polymeric product of Example C0 made'withmagne'sium. Example 7: Reaction of 1/1 MeSiHCl2/CH2=CH# with K in THF The procedure of Example 3 was followed using 60.22g (1.54 mol) of K metal, 802.lg of THE0 84.46g t0,734 mol) of MeSiHCl2 and 76.5g (0.734 mol) of styrene. Workup yielded 96.95g (89%) of nonvolatile polymer. Pyrolysis, of this, material to 1200 yielded 25.1% of SiC composition. This example demonstrates the effectiveness of MeSiHCl2 in forming polysilahydrocarbons which are effective precursors for SiC relative to Me2SiC12 as used in Example A. Example 8: Reaction of 2/1 ClCH2SiMeCl2/CH2=CH# with K in THF The procedure of Example 1 was followed using 49.31g (1.26 mol) of K metal0 1,409.8g of THF, 65.88g (0.4 mol) of-ClCH25iMeC12, and 20.86g (0.2 mol) of styrene. Workup yielded 67.7% of insoluble solid product plus 7.2S of soluble product. Pyrolysis of the insoluble solid to 1200 provided 57.7S of SiC composition. This example demonstrates the effectiveness of ClCH2SiMeC12 in forming branched polysilahydrocarbons which are effective precursors for SiC. when compared to the Me SiCi used in Example A. 2 2 Example 9: Reaction of 2/1 ClCH2SiMeCl2/CH2 -CMeCH=CH2 with K in THE The procedure of Example 2 was followed using 22.25 g (0.57 mol) of K metal0 413.0g of THF, 29.53g (0.18 mol) of ClCH2SiMeCl2, and 6.14g (0.09 mol) of isoprene. An additional 120ml of THE was added during the reaction to reduce viscosity. Workup yielded 37.7% of soluble fluid, 40.6% of soluble solid. and 4.5t of insoluble solid products. Pyrolysis of the soluble solid to 1200 provided 45.5% of sic composition. This example demonstrates that ClCH2SiMeCl2 provides effective branched polysilahydrocarbon precursors for SiC, while Me2SiCl2 (Example B) does not. Example 10: Reaction of 1/1 MeSiCl3/CH2=CH# with K in THE Example 1 was repeated except that a 1/1 molar ratio of MeSiCl3/CH2=CH# was used. Workup yielded 6.6% of soluble solid and 91.0% of insoluble solid product. Pyrolysis of the latter to 1200 provided 30.9S of SiC composition.

Claims: CLAIMS: 1, A branched polysilahydrocarbon comprising silyl units of the formula: EMI23.1 wherein R-1s a lower alkyl, a is O or 1, b is 0-3, c is 1-s. a represents the number of -CH2- groups individually bonded to Si and is 0-4. e is 0-2, a+b+c+d+e = 4 with the provisions that, in each of the plural units, a,b,c,d,e and H may differ (depending on the monomers from which they originate), and that in a plurality of such units0 a+c+d+e must total at least 3 (such that branching derives from silyl units), and hydrocarbon units derived from the hydrocarbon olefin monomers of the formula R''2C = CHR'' wherein the R* groups are selected from H, Me, phenyl. or vinyl such that at least one R'' group is phenyl or vinyl. and the monomers are selected to favor formation of #SiSi#and#SiC# bonds. 2. The branched polysilahydrocarbon of claim 1 wherein R is methyl and c=3. 3. A process for producing branched polysilahydrocarbons which comprises, reacting, with active metal preferably potassium, sodium or an alloy of both in an inert solvent medium, preferably tetrahydrofuran at an elevated temperature, a compound comprising at least one silyl monomer of formula (I) (I) (CH2=CH)aRbSiXc(CH2X)dHe wherein R is lower alkyl, preferably methyl, X is halo. preferably chloro, a is O or 1, b is 0-3, c is 1-4. d is 0-4, e is 0-2, a+b+c+d+e equals 4, and a+c+d+e totals at least 3. with or without other silyl monomers of formula (I) wherein a+c+d+e totals 1 or 2, and at least one hydrocarbon olefin monomer of formula (to) (II) R''2C = CHR' wherein the '' groups are-selected from H, Me, phenyl, or vinyl such that at least one B'' group is phenyl or vinyl0 and the monomers are selected to favor formation of #SiSi#and#SiC# bonds. 4. The process as in claim 3 wherein the elevated temperature is the reflux temperature of the solvent medium. 5. A branched polysilahydrocarbon prepared according to the process of claim 3 wherein the molar ratio of silyl monomers to hydrocarbon monomers in the compound system is at least 0.67. 6. A branched polysilahydrocarbon prepared according to the process of claim 3 wherein the compound system comprises a 2/3 molar ratio of MeSiCl3 and styrene or isoprene. 7. A branched polysilahydrocarbon prepared according to the process of claim 3 wherein the compound system comprises MeSiHCl2 and isoprene or styrene. 8. A branched polysilahydrocarbon prepared according to the process of claim 3 wherein the hydrocarbon olefin monomer is styrene, isoprene or butadiene. 9. A branched polysilahydrocarbon prepared according to the process of claim 3 wherein the silyl monomer is ClCH2SiMeCl2. 10. A branched polysilahydrocarbon prepared according to the process of claim 3 wherein the compound system comprises Me3SiCl, isoprene and CH2=CHSiMeCl2. 11. The process for producing silicon carbide ceramic compositions which comprises pyrolyzing in an inert atmosphere a branched polysilahydrocarbon as claimed in claim 1 or produced in accordance with claim 3. 12. The silicon carbide ceramic composition produced by the process of claim 11. CLAIMS FOR AUSTRIA: 1. A process for producing a branched polysilahydrocarbon comprising silyl units of the formula: EMI26.1 wherein H is a lower alkyl, a is O or 1, b is 0-3, c is 1-4, d represents the number of -CH2- groups individually bonded to Si and is 0-4, e is 0-2. a+b+c+d+e . 4 with the provisions that, in each of the plural units, a,b,c,d,e and R may differ (depending on the monomers from which they originate), and that in a plurality of such units. a+c+d+e must total at least 3 (such that branching derives from silyl units), and hydrocarbon units derived from the hydrocarbon olefin monomers of the formula R''2C s wherein the R'' groups are selected from H, He, phenyl, or vinyl such that at least one R'' group is phenyl or vinyl. and the monomers are selected to favor formation of #SiSi#and#SiC# bonds which comprises reacting, with active metal preferably potassium, sodium or an alloy of both in an inert solvent medium preferably tetrahydrofuran at an elevated temperature, a compound comprising at least one silyl monomer of formula (I) (I) (CH2=CH)aRbSiXc(CH2X)dHe wherein R is lower alkyl preferably methyl, X is halo, preferably chloro, a is O or 1, b is 0-3, c ii 1-4, d is 0-4, e is 0-2, a+b+c+d+e equals 4. ana a+c+d+e totals at least 3, with or without other silyl monomers of formula (I) wherein a+c+a+e totals 1 or 2, and ot least one hydrocarbon olefin monomer of formula (11) (II) R''2C = CHR'' wherein the R" groups are selected from H, Me, phenyl, or vinyl such that at least one R'' group is phenyl or vinyl, and the monomers are selected to favor formation of #SiSi#and#SiC# bonds. 2. The process of claim 1 wherein R is methyl and c=3. 3. The process is in claim 1 wherein the elevated temperature is the reflux temperature of the solvent medium. 4. The process of claim 1 wherein the molar ratio of silyl monomers to hydrocarbon monomers in the compound system is at least 0.67. 5. The process of claim 1 wherein the compound system comprises a 2/3 molar ratio of MeSiC13 and styrene or isoprene. 6. The process of claim 1 wherein the compound system comprises MeSiHCl2 and isoprene or styrene. 7. The process of claim 1 wherein the hydrocarbon olefin monomer is styrene, isoprene or butadiene. 8. The process of claim 1 wherein the silyl monomer is ClCH2SiMeC12. 9. The process of claim 1 wherein the compound system comprises Me3SiCl, isoprene and CH2-CHSiMeC12. 10. The process for producing silicon carbide ceramic compositions which comprises pyrolyzing in an inert atmosphere a branched polysilahydrocarbon produced in accordance with claim 1. 11. The silicon carbide ceramic composition produced by the process of claim 10.

Inventors: SCHILLING, CURTIS LOUIS, JR., WILLIAMS, THOMAS CHARLES
Applicants: UNION CARBIDE CORPORATION
Application year: 1984
Main classification: C08G77
IPC codes: C08G77, C07F7, C01B31, C04B35