Halogenated terpolymers of isobutylene, diolefin monomer and styrenic monomer
View Patent ↗A halogenated butyl polymer having improved properties, the butyl polymer derived from a monomer mixture comprising a C 4 to C 8 monoolefin monomer, a C 4 to C 14 multiolefin monomer and a styrenic monomer with a catalyst system to produce the butyl polymer. The improved properties include faster cure, higher maximum torque, higher delta torque, relatively stable modulus over time, improved hot air aging properties and improved aged flexure properties. These improved properties are believed to result from direct interaction between the styrenic moieties in the polymer backbone with a crosslinking agent added to vulcanize the halogenated butyl rubber.
1. A process for improving the heat resistance of a polymer comprising adding a styrene monomer to a mixture comprising a C 4 to C 8 monoolefin monomer, a C 4 to C 14 multiolefin monomer and polymerizing the resulting monomer mixture in the presence of a catalyst system to produce a terpolymer and halogenating the terpolymer to produce a halogenated butyl polymer.
2. The process according to claim 1 , wherein the C 4 to C 8 monoolefin monomer is selected from the group consisting of isobutylene, 2-methylpropene-1, 3-methylbutene-1, 4-methylpentene-1, 2-methylpentene-1, 4-ethylbutene-1, 4-ethylpentene-1 and mixtures thereof.
3. The process according to claim 2 , wherein the C 4 to C 8 monoolefin monomer comprises isobutylene.
4. The process according to claim 1 , wherein the C 4 to C 14 multiolefin monomer is selected from the group comprising isoprene, butadiene-1,3, 2,4-dimethylbutadiene-1,3, piperyline, 3-methylpentadiene-1,3, hexadiene-2,4, 2-neopentylbutadiene-1,3, 2-methlyhexadiene-1,5, 2,5-dimethlyhexadiene-2,4, 2-methylpentadiene-1,4, 2-methylheptadiene-1,6, cyclopentadiene, methylcyclopentadiene, cyclohexadiene, 1-vinyl-cyclohexadiene and mixtures thereof.
5. The process according to claim 4 wherein the C 4 to C 14 multiolefin monomer comprises isoprene.
6. The process according to claim 1 , wherein the styrenic monomer is selected from the group consisting of p-methylstyrene, styrene, α-methylstyrene, p-chlorostyrene, p-methoxystyrene and mixtures thereof.
7. The process according to claim 6 , wherein the styrenic monomer is selected from the group consisting of styrene, p-methylstyrene and mixtures thereof.
8. The process according to claim 1 , wherein the monomer mixture comprises from about 80% to about 99% by weight C 4 to C 8 monoolefin monomer, from about 0.5% to about 5% by weight C 4 to C 14 multiolefin monomer and from about 0.5% to about 15% by weight styrenic monomer.
9. The process according to claim 8 , wherein the monomer mixture comprises from about 85% to about 99% by weight C 4 to C 8 monoolefin monomer, from about 0.5% to about 5% by weight C 4 to C 14 multiolefin monomer and from about 0.5% to about 10% by weight styrenic monomer.
10. The process according to claim 9 , wherein the monomer mixture comprises from about 87% to about 94% by weight C 4 to C 8 monoolefin monomer, from about 1% to about 3% by weight C 4 to C 14 multiolefin monomer and from about 5% to about 10% by weight styrenic monomer.
11. The process according to claim 1 , wherein the halogenated butyl polymer is brominated.
12. The process according to claim 11 , wherein the halogenated butyl polymer is chlorinated.
13. The process according to claim 1 , wherein the amount of halogen in the halogenated butyl polymer is in the range of from about 0.1 to about 8% by weight of the polymer.
14. The halogenated butyl polymer defined in claim 13 , wherein the amount of halogen in the butyl polymer is in the range of from about 0.5 to about 4% by weight of the polymer.
15. The process according to claim 14 , wherein the amount of halogen in the butyl polymer is in the range of from about 1.5 to about 3% by weight of the polymer.