NEW FUNCTIONALIZED INITIATORS FOR ANIONIC POLYMERIZATION

Abstract: A process for the preparation of hydrocarbon solutions of monofunctional ether initiators of the following general structure: M-Z-O-C(R1R2R3) wherein M is defined as an alkali metal, preferably lithium; Z is defined as a branched or straight chain hydrocarbon tether group which contains 3-25 carbon atoms, optionally containing aryl or substituted aryl groups; and R1, R2 and R3 are independently defined as H, alkyl, substituted alkyl, aryl or substituted aryl, and their employment as initiators in the anionic polymerization of olefin containing monomers in an inert, hydrocarbon solvent comprising reacting an omega-protected-1-haloalkyl with lithium metal dispersion having a particle size between 10 and 300 millimicrons in size, at a temperature between 35 and 130 DEG C in an alkane solvent containing 5 to 10 carbon atoms.

Description: NEW FUNCTIONALIZED INITIATORS FOR ANIONIC POLYMERIZATION This invention concerns novel anionic initiators for use in polymerizing olefinic-containing monomers, a process for making the anionic initiators, a process for the polymerization of olefinic-containing monomers using the anionic initiators of this invention and polymers produced by this polymerization process. Useful polymeric products are obtained by polymerizing olefinic- containing monomers in the presence of an organo-alkali metal initiator and subsequently reacting the resulting polymer, containing an active alkali metal end group or groups, with a reagent which will couple the polymer molecules or replace the alkali metal with more stable reactive end groups. Monofunctional silyl ether initiators, containing alkali metal end groups useful in effecting such polymerization reactions are disclosed in Great Britain published patent application 2,241 ,239, published August 28, 1991. These monofunctional silyl ether initiators were demonstrated to be useful in producing polydienes having desirable characteristics such as a molecular weight of typically 1 ,000 to 10,000, 1 -4 content of typically 90%, etc. The present invention provides a process for the preparation of novel, hydrocarbon solutions of monofunctional ether initiators of the following general structure: M-Z-0-C(Rl R2R3) wherein M is defined as an alkali metal, preferably lithium; Z is defined as a branched or straight chain hydrocarbon tether group which contains 3-25 carbon atoms, optionally containing aryl or substituted aryl groups; and R1 R2 and R3 are independently defined as H, alkyl, substituted alkyl, aryl or substituted aryl, and their employment as initiators in the anionic polymerization of olefin containing monomers in an inert, hydrocarbon solvent. The process reacts selected protected omega-protected- 1- haioalkyls whose alkyl groups contain 3 to 25 carbon atoms, which are reacted with lithium metal in a liquid alkane, cycloalkane or aryl solvent, at a temperature between about 35 °C and about 130 °C. Anionic polymerizations employing the herein described monofunctional ether initiators of this invention are conducted in an inert solvent, preferably a non-polar solvent, optionally containing an ethereal modifier, using an olefinic monomer which is an alkene or a 1 ,3-diene at a temperature of about -30 °C to about +100 °C. The polymerization reaction proceeds from initiation to propagation and finally termination so that the polymer is mono¬ functional or dysfunctional terminated. The polymers have molecular weight ranges of about 1000 to 10,000. Typically 5 to 50 milli-moles of initiator is used per mole of monomer. Advantages of using the compounds containing the- protecting groups of this invention comprising the process of producing a lithium initiator and subsequently in using the said initiator to produce polymers containing the said protecting groups as compared to using substituted silyl protecting groups are as follows: 1 ) cheaper and more readily available raw materials are used in the preparation of initiators, e.g. olefins such as isobutylene or isoamylene are reacted with versus alkyl chlorosilanes, such as tert-butyldimethylchlorosilane or diphenylmethylchlorosilane. 2) The protecting groups of this invention can be removed more easily and in more ways than the substituted silyl protecting groups. Thus, for example, a tert- butyl protecting group on a hydroxy terminated polymer can be removed not only with methanesulfonic acid, but also with acid-treated Amberlyst TM resin and aqueous alcoholic HCI. 3) The by-products of the deprotection step are easy to remove from not contaminate the polymer when the protective groups of the invention are employed. For example, the by¬ product of the deprotection reaction of the tert-butyl protected hydroxypolmer is isobutylene, which is innocuous and does not require removal from the polymer, whereas the by-product of the deprotection of an alkylsilyl protected hydroxy polymer is an alkylsiloxane which is a contaminate that requires removal from the polymer. For example, a protected functional living polymer of this invention can be generated by polymerizing 1 ,3-butadiene with an initiator of formula I above, wherein M is lithium, Z is a trimethylene tether group, A is carbon and R1 , R2, and R3 are methyl groups. A living polymer is produced having the formula Li-(B)m-(l)3-(CH2)3-0-C(CH3)3 (II) where B is polymerized butadiene, and m is an integer from about 10 to 200. The living polymer II, may be reacted, for example, with ethylene oxide to yield, after hydrolysis, the compound of formula H0CH2CH2-(B)m(l)3-(CH2)3-0-C(CH3)3 (III) which may optionally be hydrogenated to the corresponding asymmetric polymer. After acidic deprotection, a dihydroxypolymer of formula HOCH2CH2-(B)m(l)3(CH2)3-OH (IV) is produced, which may be hydrogenated as described in GB2270317A to the symmetrically functionalized polymer. Additionally, other asymmetrically difunctional polymers may be produced by reacting the living polymer (II) above with, for example, carbon dioxide to produce, a polymer with one hydroxyl and one carboxyl group, or the deprotected polymer with one hydroxyl and one carboxyl group, or the living polymer II may be reacted with 1 ,5 diazabicyclo-(3.1.0) hexane as described in US 4,753,991 to produce a polymer with one protected hydroxyl and one amino group. Other asymmetrically substituted difunctional polymers may be produced having epoxy or isocyanate groups at one end for example by reacting the lithium salt of IV above (before hydrolysis), with epichlorohydrin or, by reacting IV itself with an equivalent of a diisocyanate, such as methylene 4,4-diphenyl diisocyante (2/1 NCO/OH). These unsymmetricaily substituted difunctional polymers have utility in that, on acid deprotection, the two different end groups would interact under appropriate conditions with their opposites on adjacent molecules to generate new useful elastomeric polymers or alternatively they may be reacted with reactive comonomers. Other asymmetrically substituted difunctional polymers may be produced having epoxy or isocyanate groups at one end for example by reacting the lightium salt of III above (before hydrolysis), with epichlorohydrin or, by reacting III itself with an equivalent of a diisocyanate, such as methylene4,4-diphenyl diisocyanate (2/1 NCO/OH). These unsymmetrically substituted difunctional polymers have utility in that, on acid deprotection, the two different end groups would simultaneously interact under appropriate conditions with their opposites on adjacent molecules in generate new useful elastomeric polymers of alternatively they may be reacted with reactive comonomers. The protected monohydroxy polymers (III) alone and in their hydrogenated forms, could be used as base materials to lend flexibility and higher impact strength in a number of formulas to produce use coatings, sealants, binders and block copolymers with polyesters, polyamides and polycarbonates as described in UK Patent Application GB2)70317A and in "Polytail" data sheets and * brochures (Mitsubishi Kasei America). Thus, in the presence of acidic catalysts used to promote the formation of many of these block copolymer resins, the protective group of the hydrogenated polymer is removed as well, allowing the exposed hydroxyl grouping in the base polymer molecule to simultaneously participate in the block copolymer reaction. Thus, for example, hydrogenated III polymers may be reacted with bisphenol A and phosgene in the presence of appropriate catalysts with simultaneous deprotection to yield a polycarbonate alternating block copolymer. The resulting products are useful as molding resins, for example, to prepare interior components for sutomobiles. A segmented polyamide-hydrogenatedl III block copolymer also useful as a molding composition to prepare exterior sutomotive components can be prepared by reacting hydrogenated III polymer with caprolactain and adipic acid in the presence of a catalyst. A segmented polyester-hydrogenated III block copolymer is produced by reaction of hydrogenated V polymer with dimethy terephthalate and suitable caralyst. Again, the products are useful as molding compounds for exterior automotive components. Isocyanate-terminated prepolymers can be produced from hydrogenated III polymers by reaction with suitable diisocyanates (2/1 NCO/OH) as geared above and which can be further reacted with diols and additional diisocyanates to form segmented polyurethanes useful for water and forms, low VOC coatings. Or segmented polyurethanes prepolymers may be mixed with tackidying resins and used as a moisture-curable sealant, caulk or coating. An acrylate-terminated prepolymer curable by free-radical processes can be prepared from the hydrogenated III polymer by reaction with a diisocyanate (2NCO/OH) followed by further reaction with hydroehylacrylate in the presence of a basic reagent. These processes can be applied to the protected and optionally hydrogenated polymers of formulas IV, as well. Alternatively, the protective group could be removed first from the hydrogenated polymer, and then the block copolymers formed by addition of the appropriate comonomers or the protected monohydroxy polymers can be reacted with functional comonomers and the be protected and reacted further with the same or other comonomers. In another possible application, the living polymer II may be reacted with an omega-alkenyl halosilane such as 5-hexenyldimethylchlorosilane to yield the corresponding omege-aklenyl terminated macronomomer according to directions in US5,278,244 which may be polymerized by Zieg;er-Natta techniques to yield "comb" polymers which, in deprotection, yield branched polymers with hydrosyfunctionality on the branch-ends. Such multi-functionality can be utilized to graft a water-soluble polymer such as polyethylene oxide onto a hydrophobic polyolefinic core to product hydrogels. In still another example, a living polymer analogous to II having the formula Li(B)x(S)y(CH2)3-OC(CH3)3 where B is polymerized butadiene, S is polymerized styrene and x and y can vary from 10 to 1000 or more is reacted with divinylbenzene (DVB) to produce a multi-armed star polymer, according to US4,409,357 which on deprotection would yield a star with hydroxy-functional branches which may be reacted as described above to produce hydrogels. In another possible application, the living polymer II, after reaction with DVB to form living star polymer, may be further reacted with acrylate monomers such as t-butyl methacrylate to grow additional asymmetric branches onto the star. Star polymers are useful as viscosity index improves for motor oils. Again, water-soluble polymers could be grafted onto these stars using, for example ethylene oxide, to produce useful hydrogels after deprotection. The precursor omega-protected 1 -haioalkyls (halides) are prepared from the corresponding haloaicohol by the standard literature methods. For example, 3-(1 ,1-dimethylethoxy)-1-chloropropane is synthesized by the reaction of 3-chloro-1-propanol with 2-methylpropene according to the method of A. Alexakis, M. Gardette, and S. Colin, Tetrahedron Letters, 29, 1988, 2951. The method of B. Figadere, X. Franck and A. Cave, Tetrahedron Letters, 34, 1993, 5893, which involved the reaction of the appropriate alcohol with 2-methyl-2-butene catalyzed by boron trifluoride etherate was employed for the preparation of the t-amyl ethers. The triphenylmethyl protected compounds, for example 3-(triphenylmethoxy)-1 - chloropropane, are prepared by the reaction of the haloaicohol with triphenylmethylchloride, according to the method of S. K. Chaudhary and O. Hernandez, Tetrahedron Letters, 1979, 95. The compound 4-(methoxy)-1- chlorobutane, and the higher analogues, are synthesized by the ring opening reaction of tetrahydrofuran with thionyl chloride and methanol, according to the procedure of T. Ferrari and P. Vogel, SYNLETT, 1991 , 233. Monofunctional ethers are prepared in accord with the process of this invention and such compounds can include, but are not limited to, 3-(1 ,1- dimethylethoxy)-1-propyllithium, 5-(1 ,1-dimethylethoxy)-1-pentyllithium, 3- (1 ,1-dimethylethoxy)-2,2-dimethyl-1-propylIithium, 4-(1 ,1-dimethylethoxy)-1- butyllithium, 6-(1 ,1-dimethylethoxy)-1-hexyllithium, 8-(1,1-dimethylethoxy)-1- octyllithium, 4-(ethoxy)-1 -butyllithium, 4-(1-propyloxy)-1 -butyllithium, 4-(1- methylethoxy)-1 -butyllithium, 3-(triphenylmethoxy)-2,2-dimethyl-1 - propyllithium, 4-(triphenylmethoxy)-1 -butyllithium, 5-(triphenylmethoxy)-1 - pentyllithium, 6-(triphenylmethoxy)-1 -hexyllithium, 8-(triphenylmethoxy)-1 - octyllithium, 3-(1 ,1-dimethylpropyloxy)-1 -propyllithium, 3-(1 ,1- dimethylpropyloxy)-2,2-dimethyl-1 -propyllithium, 4-(1 ,1-dimethylpropyloxy)- 1 -butyllithium, 6-(1 ,1-dimethylpropyloxy)-1 -hexyllithium, 4-methoxy-1- butyllithium, 3-methoxy-1 -butyllithium, 3-(triphenylmethoxy)-1 -propyllithium, 3-(1 ,1-dimethylethoxy)-2-methyl-1 -propyllithium, and 3-(1 ,1- dimethylpropyloxy)-2-methyl-1 -propyllithium. Lithium metal used in preparing the monofunctional ethers is used as a dispersion whose particle size usually does not exceed about 300 microns. Preferably the particle size is between 10 and 300 microns although coarser particle size lithium can be used. The lithium metal can contain 0.2 to 0.8 and preferably 0.3 to 0.5 weight percent sodium. The lithium metal is used in amounts of 90% of theoretical to a 40% excess above the theoretical amount necessary to produce the monofunctional ethers. The preferred reaction temperatures vary from compound to compound, with each compound tending to have its own preferred reaction conditions. Suprisingly, for some compounds the preferred- reacton temperature/condition is the reflux temperature of the solvent. When this is the case the preferred rection temperature is in the range of 35 to 80°C. Solvents useful in practicing this invention include but are not limited to inert liquid alkanes, cycloalkanes and aryl solvents such as alkanes and cycloalkanes containing five to 10 carbon atoms such as pentane, hexane cyclohexane.methylcyclohexane, heptane.methylcycloheptane, octane, decane and so forth and aryl solvents containing six to ten carbon atoms such as toluene, ethylbenzene, p-xylene, m-xylene, o-xylene, n- propylbenzene, isopropylbenzene, n-butylbenzene,and the like. Conjugated diene hydrocarbons useful in practicing this invention include but are not limited to isoprene, 1 ,3-butadiene, piperylene (1 ,3- pentadiene), 2,3-dimethyl-1 ,3-butadiene, 1 ,3-hexadiene, 2,4-hexadiene, 2,5-dimethylhexadiene and the like. Alkenylsubstituted aromatic hydrocarbons useful in practicing this invention include but are not limited to styrene, alpha-methyistyrene, vinyltoluene, 1 -vinylnapthalene, 3- methylstyrene, 4-methylstyrene, 1 ,1-diphenylethylene and the like. The olefinic monomer to be anionically polymerized is preferably an alkenylaromatic or a 1 ,3-diene. The alkenylaromatic or 1 ,3-diene will be chosen from the group of unsaturated organic compounds that can be polymerized anionically (i.e. in a reaction initiated by an organo- alkali metal). Suitable aikenylaromatics include the optionally-substituted styrenes and vinylnaphthalenes. Suitable 1 ,3-dienes will preferably contain from 4 to 12, especially from 4 to 8, carbon atoms per molecule. Examples of these compounds include the following : 1 ,3-butadiene, isoprene; 2,3- dimethyl-1 ,3-butadiene, 1 ,3-pentadiene, 2-methyl-3-ethyl-1 ,3-butadiene, 2- methyl-3-ethyl-1 ,3-pentadiene, 1 ,3-hexadiene, 2-methyl-1 ,3-hexadiene, 1 ,3- heptadiene, 3-methyl-1 ,3-heptadiene, 1 ,3-octadiene, 3-butyl-1 ,3-octadiene, 3,4-dimethyl-1 ,3-hexadiene; 3-n-propyl-1 ,3-pentadiene, 4,5-diethyl-1 ,3- octadiene, 2,4-diethyl-1 ,3-butadiene, 2,3-di-n-propyl-1 ,3-butadiene, and 2- methyl-3-isopropyl-1 ,3-butadiene. Among the dialkylbutadienes, it is preferred that the alkyl groups contain from 1 to 3 carbon atoms. Of the above monomers 1 ,3-butadiene, isoprene, 2,3-dimethyl-1 ,3-butadiene and 1 ,3-pentadiene are preferred with 1 ,3-butadiene being particularly preferred. The dienes may be polymerised alone, or in admixture with each other or with alkenylaromatic compounds to form random copolymers, or by charging the dienes to the reaction mixture sequentially, either with each other or with alkenylaromatic compounds, to form block copolymers. The following examples further illustrate the invention. EXAMPLE 1 PREPARATION OF 3-(1 ,1-DIMETHYLETHOXY)-1 -PROPYLLITHIUM IN CYCLOHEXANE, LOT 8888 A 500 ml., three-necked, Morton flask was fitted with a mechanical stirrer, a 125 ml pressure-equalizing addition funnel, and a Claisen adapter equipped with a thermocouple, a dry ice condenser, and an argon inlet. This apparatus was dried in an oven overnight at 125°C, assembled hot, and allowed to cool to room temperature in a stream of argon. Lithium metal dispersion, lot 8200, 0.61% sodium, was washed free of mineral oil with hexane (2 X 70 ml), and pentane (1 X 70 ml). The resultant lithium dispersion was dried in a stream of argon, weighed (4.07 grams, 0.586 mole, 2.80 equivalents), and transferred to the reaction flask with 150 ml of cyclohexane. The reaction mixture was stirred at 450 RPMs, and heated to 70°C with a heating mantle. The heat source was removed. 1-Chloro-3- (1 ,1-dimethylethoxy)-propane, 31.52 grams, (0.209 mole, 1.00 equivalent, lot 8864) was added dropwise via the addition funnel. An exotherm was detected after 5.5% of the halide feed had been added. A dry ice/hexane cooling bath was applied as needed to maintain the reaction temperature between 60-65°C. The total halide feed time was fifty-two minutes. The cooling bath was removed at the end of the halide feed. The reaction temperature fell off rapidly to room temperature. The reaction mixture was stirred for one hour at 450 RPMs, and two and one half hours at 300 RPMs. The reaction mixture was transferred with argon pressure to a dry sintered glass pressure filter. The product solution was pressure filtered with 3 psi (20.68 x 10 3 Pa) argon. The lithium chloride muds were reslurried with fresh cyclohexane (2 X 50 ml.). The filtrate was a clear, yellow solution, yield = 230 ml., 185.03 grams. Total Base = 3.85 wt. %. Active C-Li = 3.78 wt. %. Yield = 27.4 % (based on active analysis). A one ml. aliquot of this solution was carefully quenched with water. The organic phase was analyzed by Gas Chromatography (30 m. X 0.54 mm AT-1 column). 1-Chloro-3-(1 ,1-dimethylethoxy)-propane (retention time = 13.58 minutes) was not detected. The corresponding des-chloro material (retention time = 8.36 minutes) was identified by GC/MS. The very thick lithium chloride mud cake was washed with dry dibutylether (3 X 50 ml.). This afforded a clear, colorless solution, yield = 200ml., 154.76 grams. Total Base = 5.69 wt %. Active C-Li = 3.32 wt. %. Yield = 20.1 % (based on active analysis). The total yield was 47.6 %. EXAMPLE 2 PREPARATION OF 3-(1 ,1-DIMETHYLETHOXY)-2,2-DIMETHYL-1- PROPYLLITHIUM IN CYCLOHEXANE, LOT 8923 A 500 ml., three-necked, Morton flask was fitted with a mechanical stirrer, a 125 ml pressure-equalizing addition funnel, and a Claisen adapter equipped with a thermocouple, a dry ice condenser, and an argon inlet. This apparatus was dried in an oven overnight at 125°C, assembled hot, and allowed to cool to room temperature in a stream of argon. Lithium metal dispersion, lot 8200, 0.61% sodium, was washed free of mineral oil with hexane (2 X 70 ml), and pentane (1 X 70 ml). The resultant lithium dispersion was dried in a stream of argon, weighed (4.40 grams, 0.634 mole, 2.80 equivalents), and transferred to the reaction flask with 200 ml of cyclohexane. The reaction mixture was stirred at 450 RPMs, and heated to 65°C with a heating mantle. The heat source was removed. 1-Chloro-3- (1 ,1-dimethylethoxy)-2,2-dimethyl-propane, 40.42 grams, (0.226 mole, 1.00 equivalent, lot 8913) was added dropwise via the addition funnel. An exotherm was detected after 12.8% of the halide feed had been added. A dry ice/hexane cooling bath was applied as needed to maintain the reaction temperature between 60-65°C. The total halide feed time was one hour. The cooling bath was removed at the end of the halide feed. The reaction temperature fell off rapidly to room temperature. The reaction mixture was stirred for eighty minutes at 450 RPMs. The reaction mixture was then transferred with argon pressure to a dry sintered glass pressure filter. The product solution was pressure filtered with 3 psi (20.68 x 10 3 Pa) argon. The lithium chloride muds were reslurried with fresh cyclohexane (2 X 40 ml.). The filtrate was a clear, pale yellow solution, yield = 320 ml., 251.91 grams. A white solid precipitated from solution immediately after the filtration. Analysis of the supernatant solution: Total Base = 7.4 wt. %. Active C-Li = 7.0 wt. %. Yield = 52.0% (based on active analysis). Analysis of the slurry: Total Base = 12.4 wt. %. Active C-Li = 11.9 wt. %. Yield = 88.4% (based on active analysis). EXAMPLE 3 PREPARATION OF 3-(1 ,1-DIMETHYLPROPYLOXY)-1 -PROPYLLITHIUM IN CYCLOHEXANE, LOT 9135 A one liter, three-necked, Morton flask was fitted with a mechanical stirrer, a 125 ml pressure-equalizing addition funnel, and a Claisen adapter equipped with a thermocouple, a dry ice condenser, and an argon inlet. This apparatus was dried in an oven overnight at 125°C, assembled hot, and allowed to cool to room temperature in a stream of argon. Lithium metal dispersion, lot 8899, 0.43% sodium, was washed free of mineral oil with hexane (2 X 100 ml), and pentane (1 X 100 ml). The resultant lithium dispersion was dried in a stream of argon, weighed (6.35 grams, 0.915 mole, 3.67 equivalents), and transferred to the reaction flask with 180 ml of cyclohexane. The reaction mixture was stirred at 450 RPMs, and heated to 65°C With a heating mantle. The heat source was removed. 1-Chloro-3- (1 ,1-dimethylpropyloxy)-propane, 41.00 grams, (0.249 mole, 1.00 equivalent, lot 9118, 9134) was added dropwise via the addition funnel. An exotherm was detected after 13% of the feed had been added. A dry ice/hexane cooling bath was applied as needed to maintain the reaction temperature between 60-65°C. The total halide feed time was sixty-five minutes. The cooling bath was removed at the end of the halide feed. The reaction temperature fell off gradually to room temperature. The reaction mixture was stirred for one hour at 450 RPMs, and one hour at 300 RPMs. The reaction mixture was transferred with argon pressure to a dry sintered glass pressure filter. The product solution was pressure filtered with 3 psi (20.68 x 10 3 Pa) argon. The lithium chloride muds were reslurried with fresh cyclohexane (2 X 50 ml.). The filtrate was a clear, pale yellow solution, yield = 250 ml., 190.86 grams. Total Base = 6.32 wt. %. Active C-Li = 5.01 wt. %. Yield = 28.2% (based on active analysis). EXAMPLE 4 PREPARATION OF 3-(1 ,1-DIMETHYLPROPYLOXY)-2,2-DIMETHYL-1- PROPYLLITHIUM IN CYCLOHEXANE, LOT 9167 A one liter, three-necked, Morton flask was fitted with a mechanical stirrer, a 125 ml pressure-equalizing addition funnel, and a Claisen adapter equipped with a thermocouple, a dry ice condenser, and an argon inlet. This apparatus was dried in an oven overnight at 125°C, assembled hot, and allowed to cool to room temperature in a stream of argon. Lithium metal dispersion, lot 8899, 0.43% sodium, was washed free of mineral oil with hexane (2 X 100 ml), and pentane (1 X 100 ml). The resultant lithium dispersion was dried in a stream of argon, weighed (3.33 grams, 0.480 mole, 2.86 equivalents), and transferred to the reaction flask with 150 ml of cyclohexane. The reaction mixture was stirred at 450 RPMs, and heated to 65°C with a heating mantle. The heat source was removed. 1-Chloro-3- (1 ,1-dimethylpropyloxy)-2,2-dimethyl-propane, 33.00 grams, (0.168 mole, 1.00 equivalent, lot 9152) was added dropwise via the addition funnel. An exotherm was detected after 22% of the halide feed had been added. A dry ice/hexane cooling bath was applied as needed to maintain the reaction temperature between 60-65°C. The total halide feed time was fifty-three minutes. The cooling bath was removed at the end of the halide feed. The reaction temperature fell off gradually to room temperature. The reaction mixture was stirred for forty-five minutes at 450 RPMs, and seventy-five minutes at 300 RPMs. The reaction mixture was transferred with argon pressure to a dry sintered glass pressure filter. The product solution was pressure filtered with 3 psi (20.68 x 10 3 Pa) argon. The lithium chloride muds were reslurried with fresh cyclohexane (2 X 50 ml.). The filtrate was a clear, pale yellow solution, yield = 250 ml., 194.93 grams. Total Base = 12.4 wt. %. Active C-Li = 11.3 wt. %. Yield = 78.3 % (based on active analysis). EXAMPLE 5 PREPARATION OF 4-METHOXY-1 -BUTYLLITHIUM IN CYCLOHEXANE LOT 8916 A 500 ml., three-necked, Morton flask was fitted with a mechanical stirrer, a 125 ml pressure-equalizing addition funnel, and a Claisen adapter equipped with a thermocouple, a dry ice condenser, and an argon inlet. This apparatus was dried in an oven overnight at 125°C, assembled hot, and allowed to cool to room temperature in a stream of argon. Lithium metal dispersion, lot 8200, 0.61% sodium, was washed free of mineral oil with hexane (2 X 70 ml), and pentane (1 X 70 ml). The resultant lithium dispersion was dried in a stream of argon, weighed (7.25 grams, 1.045 mole, 2.80 equivalents), and transferred to the reaction flask with 200 ml of cyclohexane. The reaction mixture was stirred at 450 RPMs, and heated to 72.6°C with a heating mantle. The heat source was removed. 1-Chloro-4- methoxy-butane, 45.70 grams, (0.373 mole, 1.00 equivalent, lot 8663) was added dropwise via the addition funnel. An exotherm was detected after 7.8% of the feed had been added. Hexane/dry ice cooling was applied to maintain the reaction temperature at 60-65°C. The total halide feed time was sixty-five minutes. The cooling bath was removed at the end of the halide feed. The reaction temperature fell off rapidly to room temperature. The reaction mixture was stirred for one hour at 450 RPMs. The reaction mixture was then transferred with argon pressure to a dry sintered glass pressure filter. The product solution was pressure filtered with 3 psi (20.68 x 10*3 Pa) argon. The lithium chloride muds were reslurried with fresh cyclohexane (2 X 40 ml.). The filtrate was a clear, very pale yellow solution, yield = 300 ml., 242.28 grams. Total Base = 12.4 wt. %. Active C-Li = 12.1 wt. %. Yield = 83.6% (based on active analysis). EXAMPLE 6 PREPARATION OF 3-METHOXY-1 -BUTYLLITHIUM IN CYCLOHEXANE, LOT 8939 A 500 ml., three-necked, Morton flask was fitted with a mechanical stirrer, a 125 ml pressure-equalizing addition funnel, and a Claisen adapter equipped with a thermocouple, a dry ice condenser, and an argon inlet. This apparatus was dried in an oven overnight at 125°C, assembled hot, and allowed to cool to room temperature in a stream of argon. Lithium metal dispersion, lot 8899, 0.43% sodium, was washed free of mineral oil with hexane (2 X 70 ml), and pentane (1 X 70 ml). The resultant lithium dispersion was dried in a stream of argon, weighed (6.35 grams, 0.915 mole, 2.80 equivalents), and transferred to the reaction flask with 200 ml of cyclohexane. The reaction mixture was stirred at 450 RPMs, and heated to 68°C with a heating mantle. The heat source was removed. 1-Chloro-3- methoxy-butane, 40.03 grams, (0.327 mole, 1.00 equivalent, lot 8914) was added dropwise via the addition funnel. An exotherm was detected after 7.5% of the feed had been added. A dry ice/hexane cooling bath was applied as needed to maintain the reaction temperature between 60-65°C. The total halide feed time was eighty-three minutes. The cooling bath was removed at the end of the halide feed. The reaction temperature fell off rapidly to room temperature. The reaction mixture was stirred for one hour at 450 RPMs. The reaction mixture was then transferred with argon pressure to a dry sintered glass pressure filter. The product solution was pressure filtered with 3 psi (20.68 x 10 3 Pa) argon. The lithium chloride muds were reslurried with fresh cyclohexane (2 X 75 ml.). The filtrate was a clear, pale yellow solution, yield = 280 ml., 215.70 grams. Total Base = 13.58 wt. %. Active C-Li = 13.12 wt. %. Yield = 92.1 % (based on active analysis). Soluble chloride = 62 ppm. EXAMPLE 7 PREPARATION OF 4-(2-BUTOXY)-1 -BUTYLLITHIUM IN CYCLOHEXANE, LOT 8956 A 500 ml., three-necked, Morton flask was fitted with a mechanical stirrer, a 125 ml pressure-equalizing addition funnel, and a Claisen adapter equipped with a thermocouple, a dry ice condenser, and an argon inlet. This apparatus was dried in an oven overnight at 125°C, assembled hot, and allowed to cool to room temperature in a stream of argon. Lithium metal dispersion, lot 8899, 0.43% sodium, was washed free of mineral oil with hexane (2 X 100 ml), and pentane (1 X 100 ml). The resultant lithium dispersion was dried in a stream of argon, weighed (6.70 grams, 0.965 mole, 2.80 equivalents), and transferred to the reaction flask with 250 ml of cyclohexane. The reaction mixture was stirred at 450 RPMs, and heated to 65°C with a heating mantle. The heat source was removed. 4-(2-Butoxy)- 1-chloro-butane, 56.72 grams, (0.345 mole, 1.00 equivalent, lot 8921) was added dropwise via the addition funnel. An exotherm was detected after 15.6% of the halide feed had been added. A dry ice/hexane cooling bath was applied as needed to maintain the reaction temperature between 60- 65°C. The total halide feed time was seventy-two minutes. The cooling bath was removed at the end of the halide feed. The reaction temperature fell off rapidly to room temperature. The reaction mixture was stirred for one hour at 450 RPMs. The reaction mixture was then transferred with argon pressure to a dry sintered glass pressure filter. The product solution was pressure filtered with 3 psi (20.68 x 10 3 Pa) argon. The lithium chloride muds were reslurried with fresh cyclohexane (1 X 75 ml., 1 X 50 ml.). The filtrate was a clear, yellow solution, yield = 440 ml., 348.84 grams. Total Base = 12.1 wt. %. Active C-Li = 11.2 wt. %. Yield = 83.3 % (based on active analysis). EXAMPLE 8 PREPARATION OF 4-(1-METHYLETHOXY)-1 -BUTYLLITHIUM IN CYCLOHEXANE, LOT 9042 A 500 ml., three-necked, Morton flask was fitted with a mechanical stirrer, a 125 ml pressure-equalizing addition funnel, and a Claisen adapter equipped with a thermocouple, a dry ice condenser, and an argon inlet. This apparatus was dried in an oven overnight at 125°C, assembled hot, and allowed to cool to room temperature in a stream of argon. Lithium metal dispersion, lot 8899, 0.43% sodium, was washed free of mineral oil with hexane (2 X 70 ml), and pentane (1 X 70 ml). The resultant lithium dispersion was dried in a stream of argon, weighed (6.00 grams, 0.864 mole, 2.80 equivalents), and transferred to the reaction flask with 250 ml of cyclohexane. The reaction mixture was stirred at 450 RPMs, and heated to 80°C with a heating mantle. The heat source was removed. 1-Chloro-4-(1- methylethoxy)-butane, 46.47 grams, (0.309 mole, 1.00 equivalent, lot 8960) was added dropwise via the addition funnel. An exotherm was detected after 22.9 % of the halide feed had been added. A dry ice/hexane cooling bath was applied as needed to maintain the reaction temperature between 60-65°C. The total halide feed time was forty-five minutes. The cooling bath was removed at the end of the halide feed. The reaction temperature fell off rapidly to room temperature. The reaction mixture was stirred for ninety minutes at 450 RPMs, then for two hours at 300 RPMs. The reaction mixture was then transferred with argon pressure to a dry sintered glass pressure filter. The product solution was pressure filtered with 3 psi (20.68 x 10 3 Pa) argon. The lithium chloride muds were reslurried with fresh • cyclohexane (2 X 25 ml.). The filtrate was a clear, yellow solution, yield = 350 ml., 264.91 grams. Total Base = 12.3 wt. %. Active C-Li = 11.0 wt. %. Yield = 77.3 % (based on active analysis). POLYMERIZATION EXAMPLE POLYMERIZATION OF ISOPRENE WITH 4-METHOXY-1 -BUTYLLITHIUM, LOT 8970 A one liter, three-necked, round-bottom flask was fitted with a mechanical stirrer, a septum and a Claisen adapter equipped with a thermocouple, dry ice condenser, and an argon inlet. This apparatus was dried in an oven overnight at 125°C, assembled hot, and allowed to cool to room temperature in a stream of argon. The flask was charged with cyclohexane, 310.70 grams, and isoprene, 40.00 grams (0.587 mole). The reaction mixture was at 20.0°C. 4-Methoxy-1 -butyllithium, 16.74 grams of 11.4 wt.% solution (0.020 mole, Lot 8915) was then added with a syringe. An exotherm of 1°C was detected. The clear solution was heated to 48.4°C with a heating mantle. The heat source was removed. The reaction temperature proceeded to climb steadily to 53.4°C, at which time a dry ice/hexane cooling bath was employed for a few minutes to moderate the temperature. The cooling bath was then removed. The reaction temperature gradually declined to 24.2°C in one hour. The reaction mixture was stirred at room temperature for sixteen hours, then quenched with methanol (40 ml.) and hexane (100 ml.). The reaction mixture was transferred to a one liter separatory funnel, and the methanol layer was discarded. The hydrocarbon layer was washed with an additional 40 ml. of methanol, and concentrated to constant weight on the rotary evaporator, at a bath temperature of 35°C. This afforded a clear, somewhat viscous oil, yield = 39.00 grams (97.3%). VPO analysis, Mn = 1996. GPC analysis, MWD = 1.48. The remaining polymerization data is collected the Table. PREPARATION OF STARTING MATERIALS 1. 1-CHLORO-3-(1 ,1-DIMETHYLETHOXY)-PROPANE, LOT 8864 A two liter, three-necked round bottom flask was fitted with a mechanical stirrer, a gas inlet tube, and a Claisen adapter equipped with a dry ice condenser, and a thermocouple. This apparatus was dried in an oven overnight at 125°C, assembled hot, and allowed to cool to room temperature in a stream of argon. The flask was charged with 141.81 grams (1.50 moles, 1.00 equivalent) of 3-chloro-1-propanol and 500 ml. of cyclohexane. The resultant two-phase solution was stirred at 400 RPMs. Amberlyst 15 resin catalyst, 35 grams, was added, followed by an additional 250 ml. of cyclohexane. A total of 93 grams (1.657 moles, 1.105 equivalents) of 2-methylpropene was discharged from the cylinder in two and a third hours. A modest exotherm was noted during the addition. The reaction mixture was stirred at 20-25°C, and periodically monitored by gas chromatography (GC) for the disappearance of 3-chloro-1-propanol. After stirring at room temperature for twenty-eight hours, the conversion to the desired product was 94.7 %. The catalyst was removed by filtration through a piece of fluted filter paper. The reaction flask was rinsed with fresh cyclohexane (2 X 100 ml.). The product was purified by distillation from 10.72 grams of potassium carbonate through a twelve inch Vigreux column, at atmospheric pressure. This afforded a clear, colorless oil, yield = 158.42 grams (70.2 %). B.P. = 151.0 - 154.8°C. GC assay = 0.59 % 2-methylpropene, 2.54 % cyclohexane, 87.15 % desired product, and 9.72 % unknowns. NMR (CDCI 3 ): 3.63 (t, J = 6 Hz, 2H), 3.46 (t, J = 6 Hz, 2H), 2.28 - 1.62 (m, 2H), 1.21 (s, 9H) ppm. 2. 1-CHLORO-3-(1 ,1-DIMETHYLETHOXY)-2,2-DIMETHYL-PROPANE, LOT 8913 A one liter, three-necked round bottom flask was fitted with a mechanical stirrer, a gas inlet tube, and a Claisen adapter equipped with a dry ice condenser, and a thermocouple. This apparatus was dried in an oven overnight at 125°C, assembled hot, and allowed to cool to room temperature in a stream of argon. The flask was charged with 91.95 grams (0.75 moles, 1.00 equivalent) of 3-chloro-2,2-dimethyl-1-propanol and 200 ml. of cyclohexane. The resultant one-phase solution was stirred at 400 RPMs. Amberlyst 15 resin catalyst, 15 grams, was added, followed by an additional 50 ml. of cyclohexane. A total of 48.4 grams (0.86 moles, 1.15 equivalents) of 2-methylpropene was discharged from the cylinder in three and a half hours. A modest exotherm was noted during the addition. The reaction mixture was stirred at 20-25°C, and periodically monitored by gas chromatography (GC) for the disappearance of 3-chloro-2,2-dimethyl-1- propanol. After stirring at room temperature for twenty hours, all the starting material had been consumed, with the formation of a single, higher-boiling compound. The catalyst was removed by filtration through a piece of fluted filter paper. The reaction flask was rinsed with fresh cyclohexane (2 X 50 ml.). The product was purified by distillation from 5.07 grams of potassium carbonate through a twelve inch Vigreux column, at atmospheric pressure. This afforded a clear, colorless oil, yield = 111.21 grams (83.0 %). B.P. = 169.0 - 174.0°C. GC assay =2.98 % cyclohexane, 16.79 % 3-chloro-2,2-dimethyl-1-propanol, 78.06 % desired product, and 1.17 % unknowns. 1-CHLORO-3-(1 ,1-DIMETHYLPROPYLOXY)-PROPANE, LOT 9245 A 500 ml., three-necked round bottom flask was fitted with a reflux condenser, a thermocouple, a septum inlet, a magnetic stir bar, and an argon inlet. The flask was charged with 3-chloro-1-propanol, 94.54 grams (1.00 mole, 1.00 equivalents), pentane (50 ml.), and 2-methyl-2-butene, 70.44 grams (1.00 mole, 1.00 equivalents). This afforded a two phase solution. The reaction mixture was maintained at 20-25°C with a water cooling bath. Boron trifluoride etherate, 13.85 grams (0.098 mole, 0.098 equivalents) was added rapidly via syringe. A mild exotherm, 4-5°C, ensued, which subsided in fifteen minutes. The reaction mixture was stirred at 20-25°C, and periodically monitored by gas chromatography (GC) for the disappearance of 3-chloro-1-propanol. After forty-eight hours stirring, all the starting material had been consumed, and the reaction mixture was a single phase. The reaction mixture was diluted with pentane (100 ml.) and water (100 ml.) and transferred to a separatory funnel. The aqueous layer was discarded. The organic layer was washed with saturated sodium bicarbonate solution (2 X 50 ml.), water (1 X 50 ml.), and filter-dried over magnesium sulfate. The filtrate was concentrated on the rotary evaporator at room temperature to afford a pale yellow liquid, yield = 113.47 grams (69.0%). GC assay = 96.7 % desired product, 3.3 % unknowns. NMR (CDCI 3 ): 3.65 (t, J = 6 Hz, 2H), 3.45 (t, J = 6 Hz, 2H), 2.00 (q, J = 6 Hz, 2 H), 1.80-1.25 (m, 2H), 1.13 (s, 6H), and 0.84 (t, J = 6 Hz, 3H) ppm. 1-CHLORO-3-(1 ,1-DIMETHYLPROPYLOXY)-2,2-DIMETHYL- PROPANE, LOT 9250 A 500 ml., three-necked round bottom flask was fitted with a reflux condenser, a thermocouple, a septum inlet, a magnetic stir bar, and an argon inlet. The flask was charged with 3-chloro-2,2-dimethy.-1-propanol, 122.60 grams (1.00 mole, 1.00 equivalents), pentane (50 ml.), and 2- methyl-2-butene, 70.66 grams (1.01 mole, 1.01 equivalents). This afforded a two phase solution. The reaction mixture was maintained at 20-25°C with a water cooling bath. Boron trifluoride etherate, 13.85 grams (0.098 mole, 0.098 equivalents) was added rapidly via syringe. A mild exotherm, 4-5°C, ensued, which subsided in fifteen minutes. The reaction mixture was stirred at 20-25°C, and periodically monitored by gas chromatography (GC) for the disappearance of 3-chloro-2,2-dimethyl-1-propanol. After twenty-four hours stirring, all the starting material had been consumed, and the reaction mixture was a single phase. The reaction mixture was diluted with pentane (50 ml.) and water (100 ml.) and transferred to a separatory funnel. The aqueous layer was discarded. The organic layer was washed with saturated sodium bicarbonate solution (2 X 50 ml.), water (1 X 50 ml.), and filter-dried over magnesium sulfate. The filtrate was concentrated on the rotary evaporator at room temperature to afford a clear, almost colorless liquid, yield = 165.90 grams (86.1 %). GC assay = 87.7 % desired product, 12.3 % unknowns. NMR (CDCI3): 3.45 (s, 2H), 3.09 (s, 2H), 1.81-1.20 (m, 2H), 1.09 (s, 6H), 0.95 (s, 6H), and 0.84 (t, J = 6 Hz, 3H). 5. 1-CHLORO-4-METHOXY-BUTANE, LOT 8663 A one liter, three-necked round bottom flask was equipped with a reflux condenser, a teflon clad thermocouple, a 225 ml. pressure-equalizing addition funnel, a large egg-shaped magnetic stir bar, and a gas outlet vented to a caustic scrubber. This apparatus was dried in an oven overnight at 125°C, assembled hot, and allowed to cool to room temperature in a stream of argon. The flask was charged with methanol, 80.10 grams (2.50 moles, 1.00 equivalent) and tetrahydrofuran, 180.28 grams (2.50 moles, 1.00 equivalent). The reaction mixture was cooled to 0°C with a methanol/ice bath, then 356.91 grams (3.00 moles, 1.20 equivalents) of thionyl chloride was added dropwise via the addition funnel. There was an immediate exotherm, and a release of acidic fumes. The temperature was held below 15°C by adjustment of the feed rate. The total thionyl chloride feed time was two and a third hours. The cooling bath was removed at the end of the feed. The reaction mixture was clear and colorless. The reaction mixture was heated to reflux for three hours, at which time the temperature was 120°C, then the reaction mixture was allowed to cool to room temperature. An aliquot was withdrawn, diluted with pentane, washed with water and saturated sodium bicarbonate solution, then analyzed by gas chromatography (30 m. X 0.54 mm AT-1 column). Both of the starting materials were still present, tetrahydrofuran (retention time = 3.46 minutes), methanol (retention time = 0.85 minutes), in addition to the desired product (retention time = 8.68 minutes). The reaction mixture was heated to reflux for an additional two hours, after which time all gas evolution had ceased. The reaction mixture was allowed to cool to room temperature, then the orange reaction mixture was transferred to a one liter separatory funnel, and diluted with pentane (300 ml.). The organic layer was washed with water (2 X 300 ml.), saturated sodium bicarbonate solution (1 X 300 ml.), and finally, water (2 X 300 ml.). The organic layer was dried (magnesium sulfate), filtered, and purified by distillation through a six inch Vigreux column, at atmospheric pressure. This afforded a clear, colorless oil, yield = 187.63 grams (59.8 %). B.P. = 140.1-146.5°C. GC assay = 0.28 % methanol, 0.17 % pentane, 0.64 % tetrahydrofuran, 97.68 % desired product, and 1.23 % unknowns. NMR (D 6 Benzene): 3.43-2.89 (m, 4H), 3.12 (s, 3H), and 1.97-1.19 (m, 4H), ppm. 6. 1-CHLORO-3-METHOXY-BUTANE, LOT 8914 A 500 ml., three-necked round bottom flask was equipped with a reflux condenser, a teflon clad thermocouple, a 125 ml. pressure-equalizing addition funnel, a large egg-shaped magnetic stir bar, and a gas outlet vented to a caustic scrubber. This apparatus was dried in an oven overnight at 125°C, assembled hot, and allowed to cool to room temperature in a stream of argon. The flask was charged with thionyl chloride, 124.92 grams (1.05 moles, 1.05 equivalents). 3-Methoxy-1- butanol, 104.15 grams (1.00 mole, 1.00 equivalent) was added dropwise via the addition funnel. There was an immediate exotherm, and a release of acidic fumes. The total alcohol feed time was thirty-eight minutes. The reaction mixture was dark orange at the end of the feed. The reaction mixture was heated to reflux for four hours, then let cool to room temperature. An aliquot was withdrawn, diluted with pentane, washed with water and saturated sodium bicarbonate solution, then analyzed by gas chromatography (30 m. X 0.54 mm AT-1 column). All the starting-material had been consumed, with the formation of a slightly faster eluting compound (3-methoxy-1 -butanol retention time = 10.92 minutes, product retention time = 10.38 minutes). The reaction mixture was transferred to a one liter separatory funnel, diluted with pentane (300 ml.), and the organic layer was washed with water (2 X 300 ml.), saturated sodium bicarbonate solution (1 X 300 ml.), and finally, water (1 X 300 ml.). The organic layer was dried (magnesium sulfate), filtered, and distilled through a twelve inch Vigreux column, at atmospheric pressure. This afforded a clear, colorless oil, yield = 95.39 grams (77.9 %). B.P. = 124.0 - 126.6°C. GC assay = 1.6 % pentane, 94.2 % desired product, and 4.2 % unknowns. NMR (CDCI 3 ): 3.99-3.43 (m, 3H), 3.35 (s, 3H), 2.13-1.59 (m, 2H), and 1.15 (t, J = 6 Hz, 3H) ppm. 7. 4-(2-BUTOXY)-1 -CHLORO-BUTANE, LOT 8921 A one liter, three-necked round bottom flask was equipped with a reflux condenser, a teflon clad thermocouple, a 250 ml. pressure-equalizing addition funnel, a large egg-shaped magnetic stir bar, and a gas outlet vented to a caustic scrubber. This apparatus was dried in an oven overnight at 125°C, assembled hot, and allowed to cool to room temperature in a stream of argon. The flask was charged with 2- butanol, 185.30 grams (2.50 moles, 1.00 equivalent) and tetrahydrofuran, 180.28 grams (2.50 moles, 1.00 equivalent). The reaction mixture was cooled to -15°C, then 356.91 grams (3.00 moles, 1.20 equivalents) of thionyl chloride was added dropwise via the addition funnel. There was an immediate exotherm, and a release of acidic fumes. The temperature was held below 10°C by adjustment of the feed rate. The total thionyl chloride feed time was two and a quarter hours. The cooling bath was removed at the end of the feed. The reaction mixture was heated to reflux (95°C) for six hours, then let cool to room temperature. An aliquot was withdrawn, diluted with pentane, washed with water and saturated sodium bicarbonate solution, then analyzed by gas chromatography (30 m. X 0.54 mm AT-1 column). Both of the starting materials were still present, tetrahydrofuran (retention time = 6.09 minutes), 2-butanol (retention time = 6.62 minutes), in addition to the desired product (retention time = 16.78 minutes). The reaction mixture was heated to reflux for an additional four hours, after which time all gas evolution had ceased. The reaction mixture was allowed to cool to room temperature, then transferred to a one liter separatory funnel, and diluted with pentane (300 ml.). The organic layer was washed with water (2 X 300 ml.), saturated sodium bicarbonate solution (1 X 300 ml.), and finally, water (1 X 300 ml.). The organic layer was dried (magnesium sulfate), filtered, and purified by distillation from 3.00 grams of potassium carbonate through a twelve inch Vigreux column, at atmospheric pressure. This afforded a clear, colorless oil, yield = 207.34 grams (50.4 %). B.P. = 180.0 - 189.6°C. GC assay = 96.0 % desired product, and 4.0 % unknowns. NMR (CDCI3): 3.72-2.91 (m, 5H), 2.03-1.12 (m, 6H), 0.99 (d, J = 6 Hz, 3H), and 0.74 (t, J = 6 Hz, 3H) ppm. 8. 1-CHL0R0-4-(1-METHYLETH0XY)-BUTANE, LOT 8960 A one liter, three-necked round bottom flask was equipped with a reflux condenser, a teflon clad thermocouple, a 250 ml. pressure-equalizing addition funnel, a large egg-shaped magnetic stir bar, and a gas outlet vented to a caustic scrubber. This apparatus was dried in an oven overnight at 125°C, assembled hot, and allowed to cool to room temperature in a stream of argon. The flask was charged with 2- propanol, 150.25 grams (2.50 moles, 1.00 equivalent) and tetrahydrofuran, 180.28 grams (2.50 moles, 1.00 equivalent). The reaction mixture was cooled to 0°C, then 356.91 grams (3.00 moles, 1.20 equivalents) of thionyl chloride was added dropwise via the addition funnel. There was an immediate exotherm, and a release of acidic fumes. The temperature was held below 15°C by adjustment of the feed rate. The total thionyl chloride feed time was two and a half hours. The cooling bath was removed at the end of the feed. The reaction mixture was heated to reflux (119°C) for five hours, after which time all gas evolution had ceased, then let cool to room temperature. The orange reaction mixture was transferred to a one liter separatory funnel, and diluted with pentane (300 ml.). The organic layer was washed with water (2 X 400 ml.), saturated sodium bicarbonate solution (1 X 300 ml.), and finally, water (1 X 300 ml.). The organic layer was dried (magnesium sulfate), filtered, and purified by distillation from 3.00 grams of potassium carbonate through a twelve inch Vigreux column, at atmospheric pressure. This afforded a clear, colorless oil, yield = 234.22 grams (61.8%). B.P. = 160.0 - 169.0°C. GC assay = 88.0 % desired product, and 12.0 % unknowns. KCΠRED SHEET m t 91) TABLE SYNTHESIS POLYMERS VIA FUNCTIONAL INITIATORS EXP. INITIATOR MONOMER POLYMER NO. NO. % YIELD Ms fTh) Mn (VPO) Mn (GPC) Mw(GPC) M WD (GPC) 8970 8815 ISOPRENE 97.3 2472 1996 2472 3646 1.48 8993 8944 ISOPRENE 100.0 2034 2645 2493 5752 2.31 9244 9135 ISOPRENE 95.1 2107 2825 3943 4482 1.13 9267 9167 ISOPRENE 97.3 2200 2668 2618 3007 1.15 RECCED SHEET (RULE 91)

Claims: Claims: 1. A process for the preparation of hydrocarbon solutions of monofunctional ether initiators of the following general structure: characterized in that M is defined as an alkali metal, preferably lithium; Z is defined as a branched or straight chain hydrocarbon tether group which contains 3-25 carbon atoms, optionally containing aryl or substituted aryl groups; and R * ι , R2, and R3 are independently defined as H, alkyl, substituted alkyl, aryl or substituted aryl, comprising reacting an omega-protected-1-haloalkyl with lithium metal dispersion having a particle size between 10 and 300 millimicrons in size, under an inert atmosphere, at a temperature between 35 and 130 °C in an inert liquid hydrocarbon solvent containing 5 to 10 carbon atoms. 2. The process of claim 1 characterized in that the reaction temperature is the reflux temperature of the solvent. 3. The process of claim 1 characterized in that the omega- protected-1-haloalkyl is selected from 3-(1 ,1-dimethylethoxy)-1- propylhalide,3-(1 ,1-dimethylethoxy)-2-methyl-1 -propylhalide, 3-(1 ,1- dimethylethoxy)-2,2-dimethyl-1 -propylhalide, 5-(1 ,1 -dimethylethoxy)-1 - pentylhalide, 4-(1 ,1-dimethylethoxy)-1-butylhalide, 6-(1 ,1- dimethylethoxy)-1-hexylhalide, 8-(1 ,1-dimethylethoxy)-1-octylhalide, 4- (ethoxy)-1 -butylhalide, 4-(1 -propyloxy)-1 -butylhalide, 4-(1 -methylethoxy)- 1 -butylhalide, 3-(triphenylmethoxy)-2,2-dimethyl-1 -propylhalide, 4- (triphenylmethoxy)-l -butylhalide, 5-(triphenylmethoxy)-1 -pentylhalide, 6- (triphenylmethoxy)-l -hexylhalide, 8-(triphenylmethoxy)-1 -octylhalide, 3- (1 ,1 -dimethylpropyloxy)-1 -propylhalide, 3-(1 ,1 -dimethylpropyloxy)-2,2- dimethyl-1 -propylhalide, 4-(1 ,1-dimethylpropyloxy)-1 -butylhalide, 6-(1 ,1- dimethylpropyloxy)-1 -hexylhalide, 4-methoxy-1 -butylhalide, 3-methoxy- 1 -butylhalide, 3-(triphenylmethoxy)-1 -propylhalide, and 3-(1 ,1- dimethylpropyloxy)-2-methyl-1 -propylhalide. 4. The process of claim 3 characterized in that the halide is bromine or chlorine. 5. The process of claim 1 characterized in that the reaction temperature is between 20 °C and 100 °C. 6. A process for the anionic polymerization of an olefinic- containing monomer comprising the steps of: polymerization of a conjugated polyene hydrocarbon having 4 to 30 carbon atoms in a hydrocarbon or mixed hydrocarbon-polar solvent media at a temperature of 10-70°C with an initiator having the formula M-Z-0-C(R, R2R3) wherein M is defined as an alkali metal, preferable lithium; Z is defined as a branched or straight chain hydrocarbon tether group which contains 3-25 carbon atoms, and R-j , R2 and R3 are independently defined as H, alkyl, substituted alkyl, aryl or substituted airy to produce an intermediate polymer. 7. The process of claim 6 further characterized by reacting the intermediate polymer with a compound selected from the group consisting of ethylene oxide, carbon dioxide, 1 ,5-diazabicyclo (3.1.0) hexane, N-benzylidene trimethylsilylamide, allyl chloride, allyl bromide, water, sulfur, alkanols containing 1 to 10 carbon atoms, omega- alkenylhalosilanes as exemplified by 5-hexenyl-dimethylchlorosilane, isomeric divinylbenzenes, chlorosilanes as exemplified by silicon tetrachloride and dimethyldichlorosilane, and chlorostannanes as exemplified by tin tetrachloride and dibutyltin dichloride and recovering a linear or branched polymer having one or more terminal functional groups. 8. Hydrogenation of the recovered polymers of claim 7. 9. The process of claim 6 characterized in that the conjugated diene hydrocarbon is selected from the group consisting of 1.3- butadiene; isoprene;2,3-dimethyl-1 ,3-butadiene; 1 ,3-pentadiene (piperylene), 2-methyl-3-ethyl-1 ,3-butadiene, 3-methyl-1 ,3-pentadiene, 1 ,3-hexadiene, 2,5-dimethylhexadiene and 1 ,3-octadiene. 10. The process of claim 6 further characterized by the step of removing the protecting group from the polymer. 11. The process of claim 6 characterized in that the polar solvent is selected from the group consisting of diethyl ether, triethylamine, methyl tert-butyl ether, dibutyl ether, and tributylamine. 12. The process of claim 7 characterized by further reaction of the polymers of claim 7 produced from isomeric divinyl benzenes with monomers selected from the group consisting of conjugated 1 ,3-dienes, vinylaromatic compounds, alkyl acrylates, alkyl methacrylates and dialkylacrylamides. 13. The process of claim 7 characterized by deprotection and hydrogenation of the polymers of claim 7 produced from isomeric divinylbenzenes. 14. The process of claim 13 further characterized by reaction of the hydrogenated deprotected polymers of claim 13 with ethylene oxide and potassium alkoxides to produce hydrogels. 15. The process of claim 13 further characterized by reaction of the hydrogenated and deprotected polymers of claim 13 with acryloyl chloride and methacryloyl chloride 16. The process of claim 15 further characterized by reacting the polymers of claim 15 with alkyl acrylates, methacrylatee and dialkylacrylamides to produce hydrogels. 17. The process of claim 7 further characterized by reaction of the polymers of claim 7 produced from allyl chloride, allyl bromide and omega-alkenyl halosilanes with monomers selected from the group of alkyl acrylates, alkyl methacrylates, and dialkylacrylamides. 18. The process of claim 7 further characterized reacting the hydrogenated polymer of claim 7 produced from ethylene oxide with compounds selected from the group of epichlorohydrin and diisocyanates exemplified by methylene-4,4-diphenyldiisocyanate (2:1 NCO/OH to produce epoxide and isocyanate-terminated polymers 19. The process of claim 18 further characterized by deprotection of the isocyanate and epoxy-terminated polymers of claim 18 and further polymerization of the deprotected polymers. 20. The process of claim 7 further characterized by reaction of the hydrogenated polymer of claim 7 produced from ethylene oxide with compounds selected from the group of dialkylterephthalates, alpha- omega alkane diols, diisocyanates exemplified by methylene-4,4- diphenyldiisocyanate, and caprolactam, followed by deprotection of the resulting polymers and further polymerization and copolymerization of the deprotected polymers resulting therefrom. 21. A functionalized polymer produced by a process characterized by polymerization of a conjugated polyene hydrocarbon having 4 to 30 carbon atoms in a hydrocarbon or mixed hydrocarbon-polar solvent media at a temperature of 10-70°C with an initiator having the formula M-Z-0-C(R,R2R3) wherein M is defined as an alkali metal, Z is defined as a branched or straight chain hydrocarbon tether group which contains 3-25 carbon atoms, and R1 , R2 and R3 are independently defined as H alkyl, substituted alkyl, aryl or substituted aryl to produce an intermediate polymer. 22. A functionalized polymer produced by a process characterized by polymerization of a conjugated polyene hydrocarbon having 4 to 30 carbon atoms in a hydrocarbon or mixed hydrocarbon-polar solvent media at a temperature of 10-70°C with an initiator having the formula M-Z-0-CR(R,R2R3) wherein M is defined as an alkali metal Z is defined as a branched or straight chain hydrocarbon tether group which contains 3-25 carbon atoms, and R1 ,R2 and R3 are independently defined as H alkyl, substituted alkyl, aryl or substituted aryl to produce an intermediate polymer and reacting the intermediate polymer with a compound selected from the goup consisting of ethylene oxide, carbon dioxide, 1 ,5- diazabicyclo (3.1.0) hexane, N-benzylidene trimethylsilylamide, allyl chloride, alkyl bormide, water, sulfur, alkanols containing 1 to 10 carbon atoms, omega-aklenylhalosilanes as exemplified by 5-hexanyl- dimethylchlorosilane, isomeric divinlybensone, chlorosilanes as examplified by silicon tetrachloride and dimethylcidhlorosilane and chlorostannanes as exemplified by tin tetrachloride and butyitin dichloride and recovering a linear or branched polymer having one or more terminal functional groups. 23. The polymer of claim 22 characterized by hydrogenation of the polymerized polyene hydrocarbon 24. The polymers of claim 13 produced by deprotection and hydrogenation of the polymers of claim 7 produced from isomeric divinylbenzenes. 25. The hydrogel polymers of claim 14 produced by reaction of the hydrogenated and deprotected polymers of claim 13 with ethylene oxide and potassium alkoxides. 26. The polymers of claim 14 produced by reaction of the hydrogenated and deprotected polymers of claim 13 with acryloyi chloride and methacryloly chloride in the presence of a basic reagent 27. The hydrogel polymers of claim 16 produced by reacting polymers of claim 15 with aklylacrylates, methacrylates and dialkylacrylamides 28. The epoxide-terminated polymers of claim 18 produced by reacting the hydrogenated polymers of claim 8 with epichlorohydrin 29. The isocyanate terminated polymers of claim 18 produced by reacting the hydrogenated polymers of claim 8 with diisocyanates 30. The epoxide and isocyanate terminated polymers of claims 28 and 29 produced by deprotection

Inventors: ENGEL JOHN F, GRANGER ERIC J, SCHWINDEMAN JAMES A, ENGEL, JOHN, F., GRANGER, ERIC, J., SCHWINDEMAN, JAMES, A.
Applicants: FMC CORP, FMC CORPORATION
Application year: 1995
Main classification: C08F4
IPC codes: C07F1, C08C19, C08F4, C08F8, C08F36, C08F279