SILYLAMINES AS ADDITIVES IN GROUP TRANSFER POLYMERIZATION

Abstract: Group Transfer Polymerization process comprising contacting under polymerizing conditions at least one monomer selected from acrylic and maleimide monomers with (i) a tetracoordinate organosilicon, organotin or organogermanium polymerization initiator having at least one initiating site, and (ii) a co-catalyst which is a source of fluoride, bifluoride, cyanide or azide ions or selected oxyanion, the process further characterized in that a selected silylamine is present before and/or during the polymerization, the silylamine being of the formula: wherein: each R, independently, is C₁₋₁₈ n-alkyl, n-alkenyl or n-alkynyl; X³ is -H or C₁₋₁₂ n-alkyl; Y¹ is -H, C₁₋₁₂ n-alkyl, aryl or alkaryl; a is 1, 2 or 3; b is 0 or 1; c is 1 or 2; (a + b + c) is 4; X³ and Y¹ taken together with -N form a 5- or 6-membered saturated heterocyclic ring or a 5- or 6-membered heterocyclic ring containing one or more substituents that are inert under polymerizing conditions; provided, however, if Y¹ is aryl or alkaryl, then X³ is C₁₋₁₂ n-alkyl; and provided, however, if a is 3 and c is 1, then each of X³ and Y¹, taken independently, is -H or -CH₃.

Description: BACKGROUND OF THE INVENTION Field of the Invention This invention relates to a process of polymerizing acrylic esters and, more specifically, to initiators which are useful therein. Background United States Patents 4,414,372; 4,417,034; 4,508,880; 4,524,196; 4,581,428; 4,588,795; 4,598,161; 4,605,716; 4,622,372; 4,656,233; 4,659,782; 4,659,783; 4,681,918; 4,695,607; 4,711,942; and 4,732,955; International Publication No. WO 87/07264; and EP-A-0 244 953, 0 249 436, 0 265 091, 0 276 976 and 0 291 212. referred to hereinafter as "the aforesaid patents and patent applications", disclose processes for polymerizing an acrylic or maleimide monomer to a "living" polymer in the presence of: (i) an initiator having at least one initiating site and which is a tetracoordinate organo(Si, Sn or Ge) compound, including such compound having at least one oxygen, nitrogen or sulfur atom attached to the Si, Sn or Ge; and (ii) a co-catalyst which is a source of fluoride, bifluoride, cyanide or azide ions or a suitable Lewis acid, Lewis base or selected oxyanion. Such polymerization processes have become known in the art as Group Transfer Polymerization (Webster et al., "Group Transfer Polymerization - A New and Versatile Kind of Addition Polymerization", J. Am. Chem. Soc. 105 , 5706 (1983)). Preferred monomers for use in Group Transfer Polymerization are selected from acrylic and maleimide monomers of the formula CH₂=C(Y)X and and mixture thereof, wherein: X is -CN, -CH=CHC(O)X′ or -C(O)X′; Y is -H, -CH₃, -CN or -CO₂R, provided, however, when X is -CH=CHC(O)X′, Y is -H or -CH₃; X′ is -OSi(R¹)₃, -R, -OR or -NR′R″; each R¹, independently, is a hydrocarbyl radical which is an aliphatic, alicyclic, aromatic or mixed aliphatic-aromatic radical containing up to 20 carbon atoms or -H, provided that at least one R¹ group is not -H; R is: (a) a hydrocarbyl radical which is an aliphatic, alicyclic, aromatic or mixed aliphatic-aromatic radical containing up to 20 carbon atoms; (b) a polymeric radical containing at least 20 carbon atoms; (c) a radical of (a) or (b) containing one or more ether oxygen atoms within aliphatic segments thereof; (d) a radical of (a), (b) or (c) containing one or more functional substituents that are unreactive under polymerizing conditions; or (e) a radical of (a), (b), (c) or (d) containing one or more reactive substituents of the formula -Z′(O)C-C(Y¹)=CH₂ wherein Y¹ is -H or -CH₃ and Z′ is O or NR′ wherein R′ is as defined below; and each of R′ and R″ is independently selected from C₁₋₄ alkyl. Preferred initiators are selected from tetracoordinate organsilicon, organotin and organogermanium compounds which may be represented by the formulas Q₃′MZ, Q₂′M(Z¹)₂ and [Z¹(Q′)₂M]₂O wherein: each Q′, independently, is selected from -OR¹, -SR¹, -N(R¹)₂ and -R¹; Z is an activating substituent selected from the group consisting of -SR⁶, -OP(NR′R″)₂, -OP(OR¹)₂, -OP[OSi(R¹)₃]₂ and mixtures thereof; X² is -OSi(R¹)₃, -R⁶, -OR⁶ or -NR′R″; R⁶ is (a) a hydrocarbyl radical which is an aliphatic, alicyclic, aromatic or mixed aliphatic-aromatic radical containing up to 20 carbon atoms; (b) a polymeric radical containing at least 20 carbon atoms; (c) a radical of (a) or (b) containing one or more ether oxygen atoms within aliphatic segments thereof; (d) a radical of (a), (b) or (c) containing one or more functional substituents that are unreactive under polymerizing conditions; or (e) a radical of (a), (b), (c) or (d) containing one or more initiating sites; each of R² and R³ is independently selected from -H and a hydrocarbyl or polymeric radical, defined as for R⁶ above, subparagraphs (a) to (e); R′, R″, R¹ and Z′ are as defined above for the monomer; m is 2, 3 or 4; n is 3, 4 or 5; Z¹ is wherein X², R² and R³ are as defined above; R² and R³ taken together are provided x² and either R² or R³ taken together are provided and M is Si, Sn, or Ge. Preferred initiators are those wherein M is Si. Preferred co-catalysts are selected from a source of bifluoride ions HF₂⁻; a source of fluoride, cyanide or azide ions; a source of oxyanions, said oxyanions being capable of forming a conjugate acid having a pKa (DMSO) of about 5 to about 24; a suitable Lewis acid, for example, zinc chloride, bromide or iodide, boron trifluoride, an alkylaluminum oxide or an alkylaluminum chloride; or a suitable Lewis base, for example, a Lewis base of the formula selected from (R⁴)₃M' and wherein: M' is P or As; X¹ is -N ′- or provided, however, when the monomer is a nitrile, X¹ is each R⁴, independently, is: (a) a C₁₋₁₂ alkyl, C₄₋₁₂ cycloalkyl, C₆₋₁₂ aralkyl or di(C₁₋₄ alkyl)amino group; (b) a group of (a) wherein two or three of the alkyl, cycloalkyl and/or aralkyl groups are joined together by means of one or more carbon-carbon bonds; (c) a group of (a) or (b) wherein the alkyl, cycloalkyl and/or aralkyl groups contain within aliphatic segments thereof one or more hetero atoms selected from O, N and S; or (d) a group of (a), (b) or (c) wherein the alkyl, cycloalkyl and/or aralkyl groups contain one or more substituents that are unreactive under polymerizing conditions; and each R⁵ is -CH₂CH₂- or -CH₂CH₂- containing one or more alkyl or other substituents that are unreactive under polymerizing conditions. Additional details regarding Group Transfer Polymerization can be obtained from the aforesaid patents and patent applications. U. S. Patents 4,489,191; 4,499,229; 4,503,209 and 4,539,367 disclose selected silanes, including silylamines, as scavengers of hydroxy functional materials in moisture-curable silicone room temperature vulcanizable (RTV) compositions. For example, '191 discloses silane scavengers of the formula (R¹O) 4-(a+b+c) -Si(R²) c (H) a (X) b wherein: R¹ is alkyl, alkylether, alkylester, alkylketene, alkylcyano or aralkyl; R² is hydrocarbyl or a moiety selected from Si, O, S, N, P, C, B, Sn, Pb, Ca, hydrazine, azo, CO, CO₂, organic peroxides and metal oxides; x is a hydrolyzable leaving group selected from amido, amino, carbamato, enoxy, imidato, isocyanato, oximato, thioisocyanato and ureido radicals; a is 1-4; b is 0 or 1-3; c is 0 or 1-3; 4-(a+b+c) is 0 or 1-3. It is an object of this invention to provide selected silylamines which can be used, particularly as scavengers, in Group Transfer Polymerization. Another object is to provide silylamines which are not deleterious to Group Transfer Polymerization or to the polymer produced thereby and which can be added directly to the polymerization reaction mixture or, alternatively, can be used to treat and/or purify the reactants and other ingredients employed in Group Transfer Polymerization. These and other objects will become apparent hereinafter. Commonly assigned EP-A-0 291 212 (Application number : 88 303 949.7) discloses the use of some of the silylamines described herein as initiators of (meth)acrylate polymerization. It is to be understood that the invention herein is considered separate and distinct from any invention disclosed and claimed in the commonly assigned application, about which more will be discussed hereinafter. DETAILED DESCRIPTION OF THE INVENTION The invention herein resides in a Group Transfer Polymerization process comprising contacting under polymerizing conditions at least one monomer selected from acrylic and maleimide monomers with (i) a tetracoordinate organosilicon, organotin or organogermanium polymerization initiator having at least one initiating site, and (ii) a co-catalyst which is a source of fluoride, bifluoride, cyanide or azide ions or a selected oxyanion, the process being further characterized in that a selected silylamine is present before and/or during the polymerization, the silylamine being of the formula: wherein: each R, independently, is C₁₋₁₈ n-alkyl, n-alkenyl or n-alkynyl; X³ is -H or C₁₋₁₂ n-alkyl; Y¹ is -H, C₁₋₁₂ n-alkyl, aryl or alkaryl; a is 1, 2 or 3; b is 0 or 1; c is 1 or 2; (a + b + c) is 4; X³ and Y¹ taken together with -N form a 5- or 6-membered saturated heterocyclic ring or a 5- or 6-membered heterocyclic ring containing one or more substituents that are inert under polymerizing conditions; provided, however, if Y¹ is aryl or alkaryl, then X³ is C₁₋₁₂ n-alkyl; and provided, however, if a is 3 and c is 1, then each of X³ and Y¹, taken independently, is -H or -CH₃. Preferably, X³ and Y¹ taken together with -N form the compound of the formula wherein: R, a and b are defined as above; each Z², independently, is C₁₋₂ alkylene; a′ and b′ are defined as for a and b, respectively; and (a′ + b′) is 3. Preferred silylamines are of the above formula wherein b is 1. Also preferred are silylamines of the formula wherein b and b′ are 1. Preferably, the polymerization ingredients are pre-treated with excess silylamine before use to ensure removal of Group Transfer Polymerization "poisons". In this preferred embodiment, since excess silylamine is employed, it will be present during the polymerization. In still another embodiment, for example, when the polymerization ingredients are already purified, it may be advantageous to have the silylamine present during the polymerization, for example, to ensure removal of poisons which may enter adventitiously during polymerization. The presence of the selected silylamine of the invention permits Group Transfer Polymerization to be carried out in a more reproducible and controllable manner, thus providing more reproducible polymeric products. A still further and unexpected feature of this invention is that the selected silylamine does not adversely affect the polymerization, nor does it alter the characteristics of the polymeric product normally obtained by means of Group Transfer Polymerization. The selected silylamine of the aforesaid formula is useful for removing any "poison", that is, any material that adversely affects Group Transfer Polymerization or the polymeric products produced thereby, provided the poison is reactive with the silylamine, and provided the reaction product thus formed is not itself a poison. Impurities which retard or "poison" Group Transfer Polymerization and which are removed by the scavenging action of the selected silylamine of the invention include but are not limited to hydroxyl-containing substances such as water, alcohols, carboxylic acids, phenolic compounds and the like. It should be noted that not all silylamines are operable scavengers in Group Transfer Polymerization. When the silylamine is employed in the polymerization system, that is, is present in the polymerization reaction mixture, preferably about 0.01 to 3% (by weight) of the silylamine is added to the solvent(s) and/or monomer(s) before or just at the start of the polymerization. About 0.03 to 1% of silylamine (based on the material being purified) is a more preferred amount. Preferably, a sufficient amount of silylamine, as a scavenger, is added so that there is some active material still present at the end of the polymerization. It is preferred, but not necessary, that about 10-2,000 ppm of polymerization catalyst also be present during scavenging. Although the temperature is not critical, the lower the temperature, the slower the scavenging reaction(s). It is convenient to carry out the scavenging at ambient temperature. Scavenging of the ingredients by treatment with the silylamine prior to polymerization can be carried out under an inert atmosphere (e.g., nitrogen) so as avoid introducing more poisons, such as water. Scavenging before polymerization can be carried out for a few minutes to several days, depending on the particular scavenger chosen; whether a catalyst (of the polymerization system) is used to accelerate the scavenging reactions(s); and the suspected level of poison(s). Solvent(s), initiator(s), monomer(s) and any other ingredients should preferably first undergo a preliminary purification so that very large amounts of scavenger are not needed. Such methods of pre-purification are well known to those skilled in the art and include, e.g., passage over a molecular sieve or activated alumina and removal of moisture by azeotropic distillation. The preferred method is to scavenge all major ingredients before polymerization initiator is admixed with any ingredient. Some of the silylamines which are useful in the present invention are also capable of initiating polymerization of the acrylic or maleimide monomers when polymerization catalyst is also present. With such silylamines, therefore, care must be exercised, when pre-treating monomer with the silylamine, to avoid or minimize the presence of catalyst and thus avoid the risk of uncontrolled exothermic polymerization. In particular, azide, cyanide or phenolate ions, and tetraalkylammonium fluoride and tetraalkylammonium bifluoride catalysts should not be present. It is to be understood that there is no intent to claim herein the use of any silylamine as a polymerization initiator. Not all catalysts disclosed in the aforesaid patents and applications are operable in the present polymerization process. Specifically, Lewis acids and Lewis bases should be avoided. Oxyanion catalysts which are useful in the present process are those described in U. S. 4,588,795. Monomers and initiators which are useful in the present polymerization process are those described in the aforesaid patents and applications. Some of the silylamines of the invention are more active as scavengers than others. Although not wishing to be bound by this explanation, it is believed that this is due mainly to steric effects, a concept well known to those skilled in the art. More specifically, silylamines in which the silicon atom is less sterically hindered are believed to be more reactive than those which are more sterically hindered. For example, when b in the above formula is 1, steric hinderance around the silicon is reduced. Similarly, when R is C₁₋₄ n-alkyl, preferably methyl, and/or X³ and Y¹ are H or C₁₋₄ n-alkyl, preferably methyl, steric hinderance is also reduced. Thus, less sterically hindered silylamines will require less time to remove (scavenge) poison(s). Also, the use of polymerization catalyst to assist in the scavenging process is particularly desirable with less reactive silylamines, in order to reduce the amount of time necessary to scavenge to low poison levels. With all silylamines, however, the use of catalyst shortens the scavenging process. In the following experiment and examples, unless otherwise noted, all temperatures are in degrees Celsius. All solvents and monomers were first purified by passage over Woelm neutral activated alumina. All transfers were by syringe or other similar anhydrous methods. Purified materials were stored and the reactions were carried out under nitrogen. All glassware except thermometers was heated at 155°C overnight before use. Storage vessels and glassware associated with the reaction vessel were also flamed under nitrogen. Reactions were carried out in 250 mL, 3-necked round bottomed flasks equipped with a rubber septum, thermometer, nitrogen inlet and magnetic stirring bar (Teflon encapulsated). Polymer was isolated by removing volatiles in a vacuum oven at 60-70°C. the following abbreviations are used: GPC: gel permeation chromatography M n : number average molecular weight (via GPC) M w : weight average molecular weight (via GPC) MMA: methyl methacrylate MTS: [(1-methoxy-2-methyl-1-propenyl)oxy]tri methylsilane MWD: M w / M n PMMA: poly(methyl methacrylate) TAS: a 1 molar solution of tris(dimethylamino)sulfonium bifluoride in acetonitrile THF: tetrahydrofuran In many of the following examples, methanol was added to act as a "model" poison. As disclosed in the aforesaid patents and patent applications, methanol can be used to quench the polymerization. In the following examples, enough methanol was added to completely destroy the initiator (see Experiment 1). Experiment 1 This experiment illustrates the effect of a controlled amount of "poison" (methanol) on a polymerization in the absence of the silylamine. To the reaction flask was added 100 mL of THF and 100 µL of methanol. About 2.3 h later, 0.5 mL of MTS and 100 µL of TAS were added, at which time a small (∼0.5°) exotherm occurred. Then, 35 mL of MMA was added over 34 min, during which time there was no exotherm. Removal of volatiles showed that no polymer was produced. Example 1 To the reaction flask was added 100 mL of THF, 1,0 mL of N-trimethylsilylpyrrolidine (commercially available from Petrarch Systems, Inc.), 100 µL of methanol and 50 µL of TAS. After stirring for 3.75 h, 0.50 mL (2,5 mmol) of MTS was added. Then, 35 mL of MMA was added over 57 min. After 25 mL of the MMA had been added, 50 µL of TAS was added. The reaction temperature peaked at 52°. At the end of the MMA addition, 25 µL of TAS was added. After standing overnight, 1.0 mL of methanol was added and the polymer was isolated. Yield of PMMA was 35.0 g; M n 12,700 (theoretical 13,500), MWD 1.50. The GPC curve was slightly bimodal. Example 2 This example illustrates the "living" end character of the polymer in the presence of the silylamine. To the reaction flask was added 100 mL of THF, 0.3 mL of N-trimethylsilylpyrrolidine and 50 µL of TAS. About 1.7 h later, 0.3 mL of MTS was added to the flask. Meanwhile, a solution of 0.2 mL of N-trimethylsilylpyrrolidine in 40 mL of MMA was made up, and 10 min later, addition of 20 mL of that solution to the flask was started. The addition took 16 min, during which time the temperature rose to 43°. After stirring about one h, a sample was removed for GPC analysis (Sample A), and then 15 mL more of the above MMA solution was added over 16 min. During this time another 25 µL of TAS was added and the temperature rose from 25° to 43°. After stirring overnight, Sample B was taken for GPC analysis. The polymer's "living" end character is shown by the analytical results combined with the one hour delay between MMA additions. Example 3 Into the reaction flask was added 100 mL of THF, 1.0 mL of bis(dimethylamino) methylsilane (commercially available from Petrarch Systems, Inc.) and 100 µL of methanol. About 2.5 h later, 0.5 mL of MTS and 50 µL of TAS were added. Then, 35 mL of MMA was added over 28 min. During this time, one 50 µL portion and two 25 µL portions of TAS were added and the temperature rose from 22.5° to 52.5°. About 1.3 h after the MMA addition was complete, 0.5 mL of methanol was added and a sample was taken. The yield of polymer was 31.9+g (some solution was spilled and lost); M n 12,400 (theoretical 13,500), MWD 1.20. Example 4 To the reaction flask was added 100 mL of THF, 1.0 mL of N,N′-bis(trimethylsilyl)piperazine (commercially available from Petrarch Systems, Inc.), 100 µL of methanol and 50 µL of TAS. After stirring about 3 h, 0.5 mL of MTS was added and the solution turned light pink. Then, 35 mL of MMA was added over 33 min, during which time the temperature rose from 23° to 51°. About 1.5 h later, 1.0 mL of methanol was added and the polymer was isolated. The yield of PMMA was 35.3 g; M n 12,600 (theoretical 13,500), MWD 1.20. Example 5 To the reaction vessel was added 100 mL of THF, 1.0 mL of bis(n-butylamino)methylsilane (commercially available from Petrarch Systems, Inc.) 100 µL of methanol and 50 µL of TAS. After stirring for 3 h, 0.5 mL of MTS and 50 µL of TAS were added. Then, 35 mL of MMA was added over 27 min; the temperature rose from 23° to 51°. About 1 h after the MMA addition was complete, 0.5 mL of methanol was added. The isolated polymer weighted 34.9 g; M n 14,200 (theoretical 13,500), MWD 1.28. Example 6 To the reaction flask was added 100 mL of THF, 1.0 mL of N-trimethylsilylpiperidine (commercially available from Petrarch Systems, Inc.), 100 µL of methanol and 50 µL of TAS. About 3.5 h later, 0.5 mL of MTS and 100 µL of TAS were added. Then, 35 mL of MMA was added over 29 min and the temperature rose from 24° to 53°. About 1 h after the MMA addition was complete, 0.5 mL of methanol was added. The yield of PMMA was 35.7 g; M n 17,500 (theoretical 13,500), MWD 1.28. Example 7 To the flask was added with stirring 100 mL of THF, 1.0 mL of dimethylaminotrimethylsilane (commercially available from Petrarch System, Inc.) and 100 µL of methanol. After about 3 h, 0.5 mL of MTS and 100 µL of TAS were also added. Then, 35 mL of MMA was added over 29 min, during which time the temperature rose from 22.5° to 52.5°. Then, 0.5 mL of methanol was added and the polymer was isolated. The PMMA recovered weighed 35.5 g; M n (theoretical 13,500), MWD 1.36. Example 8 This example illustrates the ability of the silylamine to remove poisons that are introduced as the polymerization is being carried out. In such cases, because of the addition of the poison(s), M n should be close to theoretical, but the MWD should be broad (higher number) because "living" ends are being destroyed during the polymerization by the added poison(s). Two experiments were carried out consecutively, one with silylamine present and one without (a control). A. To the reaction flask was added 100 mL of THF, 0.5 mL of diethylaminodimethylsilane (commercially available from Petrarch Systems, Inc.) 0.5 mL of MTS, and 100 µL of TAS. Then, 35 mL of a solution of 40 mL of MMA and 50 µL of methanol was added over 28 min. During this time, the temperature rose from 24° to 47°. After the MMA addition, 0.5 mL of methanol was added and the polymer was isolated. B. To the reaction flask was added 100 mL of THF, 0.5 mL of MTS, and 100 µL of TAS. Then, 35 mL of a solution of 40 mL of MMA and 50 µL of methanol were added over 28 min. During this time, one 50 µL and one 25 µL portion of TAS were added and the temperature rose from 23° to 52.5°. After the MMA addition was complete, 0.5 mL of methanol was added and the polymer was isolated. The properties of the isolated polymers are given below. The difference in the MWD between A and B shows that the diethylaminodimethylsilane acted as a scavenger for the methanol poison during the polymerization. Example 9 To the reaction flask was added with stirring 100 mL of THF, 1.0 mL of N-trimethylsilyl-N-methylaniline, 100 µL of methanol and 50 µL of TAS. After about 3 h, 0.5 mL of MTS and 100 µL of TAS were added. Then, 35 mL of MMA was added over 29 min, during which time 50 µL of TAS was added. The temperature rose from 23° to 34°. The polymerization was allowed to stir overnight and then 0.5 mL of methanol was added and the polymer was isolated. the yield of PMMA was 30.3 g; M n 15,900, MWD 1.53. Example 10 To the reaction flask was added 100 mL of THF, 0.1 mL of bis(dimethylamino)methylsilane (commercially available from Petrarch Systems, Inc.) and 10 µL of TAS. To 40 mL of purified (over alumina) MMA in a separate Erlenmeyer flask was added 0.2 mL of bis(dimethylamino)methylsilane and 10 µL of TAS. About 2.7 h later, 50 µL of MTS and 25 µL of TAS were added to the THF. Then, 26.5 mL of the above MMA was added by syringe to the THF over 22 min. During ths time, one 25 µL portion of TAS was added and the temperature rose to 50.5°. At the end of the MMA addition, 10 µL more of TAS was added. About 0.6 h after the MMA addition was complete, 0.5 mL of methanol was added and the polymer was isolated. The yield of PMMA was 24.5 g; M n 103,000, MWD 1.47. A similar experiment carried out without the bis(dimethylamino)methylsilane yielded no polymer, presumably due to the presence of trace amounts of poison(s). Example 11 To the reaction flask was added 100 mL of THF, 1.0 mL of dimethylsilyldimethylamine (commercially available from Petrarch Systems, Inc.), 100 µL of methanol and 10 µL of TAS. About 3.3 h later, 0.5 mL of MTS and 50 µL of TAS were added. Then, 30 mL of ethyl acrylate was added by syringe over 28 min. During this time, three 50 µL portions of TAS were added and the temperature rose to 38.5°. After the ethyl acrylate addition was complete, 3 more 50 µL portions of TAS were added. About 1.1 h after the ethyl acrylate addition was complete, 1.0 mL of methanol was added and the product was isolated; 16.5 g of poly(ethyl acrylate) was obtained; M n 9590, MWD 2.00 (using a PMMA calibration). Example 12 To the reaction flask was added 100 mL of toluene, 1.0 mL of bis(n-butylamino)dimethylsilane, 100 µL of methanol and 50 µL of TAS. After 4.3 h, 0.5 mL of MTS and 50 µL of TAS were added. Then 35 mL of 2-ethylhexyl methacrylate was added over 13 min. During this time, one 50 µL and one 25 µL portion of TAS were added and the temperature rose to 45.5°. About 1.2 h after the 2-ethylhexyl methacrylate addition was complete, 1.0 mL of methanol was added and the polymer was isolated; 30.6 g of poly(2-ethylhexyl methacrylate) was recovered; M n 8800, MWD 1.57 (using a PMMA calibration). Example 13 To the reaction flask was added 100 mL of THF, 1.0 mL of bis(dimethylamino)methylsilane, 100 µL of methanol and 50 µL of a 1 M solution of tetrabutylammomium benzoate in THF. After about 3.1 h, 0.5 mL of MTS and 100 µL of 1 M tetrabutylammonium benzoate in THF were added. Then, 35 mL of MMA was added by syringe over 28 min. During this time, the temperature rose to 54°. About 1.7 h after the MMA addition was complete, 0.5 mL of methanol was added and the polymer was isolated; 33.9 g of PMMA was recovered; M n 16,500, MWD 2.35. Example 14 To the flask was added 100 mL of THF, 100 µL of methanol, 10 µL of bis(dimethylamino)methylsilane and 10 µL of a 0.5 M solution of tetrabutylammonium m-chlorobenzoate in acetonirile. After about 3.5 h, 0.5 mL of MTS and 100 µL of the tetrabutylammonium m-chlorobenzoate were added. Then, 35 mL of MMA was added by syringe over 27 min, during which time the temperature rose from 23° to 53.5°. About 50 min after the MMA addition was complete, 0.5 mL of methanol was added and the polymer was isolated; 35.1 g of PMMA was recovered; M n 11,900 (theoretical 13,500), MWD 1.12. Example 15 To the flask was added 100 mL of THF, 100 µL of methanol, 1.0 mL of bis(dimethylamino)methysilane, and 20 µL of a saturated solution of tetrabutylammonium biacetate in acetonitrile. After about 3.3 h, 0.5 mL of MTS and 150 µL of the tetrabutylammonium biacetate solution were added. Then, 35 mL of MMA was added by syringe over 20 min, during which time the temperature rose from 21.5° to 50°. About 2 h later, 0.5 mL of methanol was added and the polymer was isolated; 35.1 g of PMMA was recovered; M n 14,900 (theoretical 13,500), MWD 2.33. Example 16 To the flask was added 100 mL of THF, 100 µL of methanol, 1.0 mL of bis(dimethylamino)methylsilane and 20 µL of a 0.5 M solution of tetrabutylammonium m-nitrophenolate in acetonitrile. Upon addition of the m-nitrophenolate the solution turned a rose' color. Four h later, 0.5 mL of MTS AND 100 µL of the m-nitrophenolate solution were added (the solution was now amber). Then, 35 mL of MMA was added over 27 min, during which time the temperature rose from 22° to 52°. About 1.2 h after the MMA addition was complete, 0.5 mL of methanol was added and the polymer was isolated; 34.4 g of PMMA was recovered; M n 16,100 (theoretical 13,500), MWD 1.60.

Claims: Group Transfer Polymerization process comprising contacting under polymerizing conditions at least one monomer selected from acrylic and maleimide monomers with (i) a tetracoordinate organosilicon, organotin or organogermanium polymerization initiator having at least one initiating site, and (ii) a co-catalyst which is a source of fluoride, bifluoride, cyanide or azide ions or selected oxyanion, the process being further characterized in that a selected silylamine is present before and/or during the polymerization, the silylamine being of the formula: wherein: each R, independently, is C₁₋₁₈ n-alkyl, n-alkenyl or n-alkynyl; X³ is -H or C₁₋₁₂ n-alkyl; Y¹ is -H, C₁₋₁₂ n-alkyl, aryl or alkaryl; a is 1, 2 or 3; b is 0 or 1; c is 1 or 2; (a + b + c) is 4; X³ and Y¹ taken together with -N form a 5- or 6-membered saturated heterocyclic ring or a 5- or 6-membered heterocyclic ring containing one or more substituents that are inert under polymerizing conditions; provided, however, if Y¹ is aryl or alkaryl, then X³ is C₁₋₁₂ n-alkyl; and provided, however, if a is 3 and c is 1, then each of X³ and Y¹, taken independently, is -H or -CH₃. Process of Claim 1 wherein X³ and Y¹ taken together with -N form the compound of the formula wherein: R, a and b are defined as in Claim 1; each Z², independently, is C₁₋₂ alkylene; a′ is 1, 2 or 3; b′ is 0 or 1; and (a′ + b′) is 3. Process of Claim 2 wherein at least one of b and b′ is 1. Process of any one of Claims 1 to 3 carried out in the presence of the silylamine. Process of any one of Claims 1 to 4 wherein ingredients used therein are pre-treated with the silylamine. Process of any one of Claims 1 to 5 wherein b is 1. Process of any one of Claims 1 to 6 wherein R is methyl. Process of any one of Claims 1 to 7 wherein X³ and Y¹, independently, are C₁₋₄ alkyl or H. Process of any one of Claims 1 to 8 wherein the monomer is an acrylic monomer.

Inventors: CITRON, JOEL DAVID
Applicants: E.I. DU PONT DE NEMOURS AND COMPANY
Application year: 1988
Main classification: C08F20
IPC codes: C08F222, C08F22, C08F4, C08F230, C08F20, C08F30, C08F2