Promoters in the polymerization of monovinyl-aromatic compounds with primary lithium initiators

Claim 2

The process which comprises polymerizing at least one first monovinyl-substituted aromatic compound monomer with a primary hydrocarbyl lithium polymerization initiator and a 1,1-dialkyl-ethylene promoter under solution polymerization conditions of temperature and pressure, wherein said process employs an amount of said promoter effective to promote said polymerization of said monovinyl-substituted aromatic monomer with said primary hydrocarbyl lithium initiator, and said 1,1-dialkylethylene promoter contains up to 8 carbon atoms per molecule, adding a polymerizable conjugated diene monomer to said polymerization prior to termination and after substantially complete conversion of said first monomer, and polymerizing said conjugated diene monomer to substantially complete conversion, and thereafter prior to termination adding a second monovinyl-substituted aromatic compound monomer to said polymerization and polymerizing said second monovinyl aromatic compound monomer thereby preparing an A--B--A block copolymer, wherein each A represents a block of polymerized monovinyl-substituted aromatic compound, and said B represents said block of polymerized conjugated diene, and wherein a weight ratio A--B--A of about 5--90--5:25--50--25 is represented.

Claim 3

The process according to claim 1 wherein said monovinyl-substituted aromatic hydrocarbon contains 8 to 12 carbon atoms per molecule.

Claim 4

The process according to claim 2 wherein said monovinyl-substituted aromatic compound is styrene, 1-vinylnaphthalene, 2-vinyl-naphthalene, 3-methylstyrene, alpha-methylstyrene, 4-ethylstyrene, 4-n-propylstyrene, 3-fluorostyrene, or 4-methoxystyrene.

Claim 5

The process according to claim 1 wherein said conjugated diene monomer is 1,3-butadiene, isoprene, 2,3-dimethyl-1,3-butadiene, piperylene, 3-butyl-1,3-octadiene, or 2-phenyl-1,3-butadiene.

Claim 6

The process according to claim 4 wherein said 1,1-dialkylethylene promoter is represented by the formula: ##STR2## wherein each R is selected from hydrogen, methyl, or ethyl.

Claim 7

The process according to claim 5 wherein said 1,1-dialkylethylene is isobutene, 2-methyl-1-butene, 2-methyl-1-pentene, 2-ethyl-1-butene, 2-ethyl-1-pentene, 2-propyl-1-pentene, or mixture.

Claim 8

The process according to claim 5 wherein said effective amount of said 1,1-dialkylethylene is in the range of about 50:1 to 7500:1 weight ratio relative to said primary hydrocarbyl lithium compound.

Claim 9

The process according to claim 1 wherein said primary hydrocarbyl lithium compound is represented by R'(CH 2 Li) x wherein R' is a valence bond, hydrogen, saturated aliphatic radical, monoolefinic aliphatic radical, which radicals can be aromatic or saturated cycloaliphatic substituted, x is an integer of 1 to 4, and R' contains 1 to 18 carbon atoms.

Claim 10

The process according to claim 8 wherein said primary hydrocarbyl lithium compound is methyllithium, ethyllithium, n-propyllithium, n-butyllithium, n-dodecyllithium, 4-phenylbutyllithium, 4-cyclohexylbutyllithium, 1,2-dilithioethane, 1,4-dilithiobutane, 1,4-dilithio-2-butene, 1,10-dilithiodecane, 1,20-dilithioeicosane, 1,3-dilithio-2-(lithiomethyl)propane, or 1,4-dilithio-2,3-di(lithiomethyl)butane.

Claim 11

The process according to claim 1 wherein said A--B--A block copolymer represents a weight ratio of about 10:80:10 to 20:60:20.

Claim 12

The process according to claim 1 wherein is employed a ratio of said 1,1-dialkylethylene promoter:said primary hydrocarbon/lithium initiator of about 150:1 to 1000:1.

Claim 13

The process according to claim 11 wherein said polymerization conditions include a polymerization temperature in the range of about 0° to 150° C., and under a pressure sufficient to maintain polymerization components substantially in the liquid phase, and polymerization in a polymerization diluent.

Claim 14

The process according to claim 1 wherein said activator is isobutylene and said initiator is n-butyllithium.

Claim 15

The process according to claim 13 employing styrene as said first monovinyl-substituted aromatic monomer, butadiene as said conjugated diene, and styrene as said second monovinyl-substituted aromatic monomer, such that the resulting A--B--A product is a polystyrene-polybutadienepolystyrene block copolymer.

Claim 16

A process for the preparation of an A--B--A thermoplastic block copolymer which comprises the steps of polymerizing under solution polymerization conditions a first monomer charge selected from monovinyl-substituted hydrocarbons of 8 to 12 carbon atoms per molecule employing a primary hydrocarbyl lithium initiator a 1,1-dialkylethylene promoter of the formula ##STR3## wherein each R is hydrogen, methyl, or ethyl, effective to promote the polymerization of said first monomer with said primary hydrocarbyl lithium initiator, employing a ratio of said promoter:primary hydrocarbyl lithium initiator in the range of about 50:1 to 7500:1, thereby preparing a living A--Li block polymer, thereafter, after substantially complete polymerization of said first monovinyl-substituted aromatic hydrocarbon adding to the living A--Li block polymer so prepared a second monomer charge selected from conjugated dienes of 4 to 12 carbon atoms per molecule, and polymerizing said so added conjugated diene monomer to such thereby forming a living A--B--Li block copolymer, adding to the so-prepared A--B--Li block copolymer a third monomer charge selected from monovinyl-substituted aromatic hydrocarbons of 8 to 12 carbon atoms per molecule, and continuing polymerization thereby preparing an A--B--A--Li block copolymer, terminating said polymerization process, thereby preparing an A--B--A block copolymer, and wherein the weight ratio of the A--B--A blocks in the ratio of about 5--90--5 to 25--50--25.

Claim 17

A process for the preparation of an A--B--A thermoplastic block copolymer which comprises the steps of polymerizing under solution polymerization conditions a first monomer charge selected from monovinyl-substituted hydrocarbons of 8 to 12 carbon atoms per molecule employing a primary hydrocarbyl lithium initiator a 1,1-dialkylethylene promoter of the formula ##STR3## wherein each R is hydrogen, methyl, or ethyl, effective to promote the polymerization of said first monomer with said primary hydrocarbyl lithium initiator, employing a ratio of said promoter:primary hydrocarbyl lithium initiator in the range of about 50:1 to 7500:1, thereby preparing a living A--Li block polymer, thereafter, after substantially complete polymerization of said first monovinyl-substituted aromatic hydrocarbon adding to the living A--Li block polymer so prepared a second monomer charge selected from conjugated dienes of 4 to 12 carbon atoms per molecule, and polymerizing said so added conjugated diene monomer to such thereby forming a living A--B--Li block copolymer, adding to the so-prepared A--B--Li block copolymer a third monomer charge selected from monovinyl-substituted aromatic hydrocarbons of 8 to 12 carbon atoms per molecule, and continuing polymerization thereby preparing an A--B--A--Li block copolymer, terminating said polymerization process, thereby preparing an A--B--A block copolymer, and wherein the weight ratio of the A--B--A blocks in the ratio of about 5--90--5 to 25--50--25.

Claim 18

The process of claim 15 wherein said monovinyl-substituted aromatic monomer is styrene; said conjugated diene is butadiene; said 1,1-dialkylethylene is isobutene, and said primary hydrocarbyl lithium initiator is n-butyllithium.