Method for producing silyl-functionalized polyolefins and silyl-functionalized polyolefins with silyl monomer incorporation
View Patent ↗Methods for producing a silyl-functionalized polyolefin with silyl monomer incorporation are provided. The method includes reacting a silicon-containing olefin with an α-olefin, in the presence of a catalytic amount of a group IV catalyst for a time sufficient to produce a silyl-functionalized polyolefin.
1. A method of producing a silyl-functionalized polyolefin comprising reacting a first functionalized olefin having the formula:
R″CH═CH—(Z) m —(CH 2 ) n SiR a R′ (3-a)
where Z is an electron withdrawing moiety, m is 0 or 1, n is an integer from 0-30, R is independently selected from the group consisting of alkoxy group and amine group, a has a value in the range 1 to 3 inclusive; R′ represents an hydrocarbyl group, R″ represents H or a group having an electron withdrawing effect or any other activation effect with respect to the —CH═CH—bond or a moiety containing an aromatic ring or a C═C bond conjugated with the —CH═CH—with an α-olefin having the general formula C x H 2x , where x is an integer between 1-30, in the presence of a catalytic amount of a group IV catalyst, wherein the group IV catalyst comprises a group IV metallocene complex, for a time sufficient to produce a silyl-functionalized polyolefin, wherein the first functionalized olefin is incorporated in the silyl-functionalized polyolefin in from about 0.1 to about 25 mole %, wherein the group IV metallocene complex has the formula: [(C 5 Me 5 ) 2 ZrMe][MeB(C 6 F 5 ) 3 ]; [(1,2—C 5 Me 2 H 3 ) 2 ZrMe][MeB(C 6 F 5 ) 3 ]; or [(C 5 H 5 ) 2 ZrMe][MeB(C 6 F 5 ) 3 ].
2. The method of claim 1 wherein the α-olefin is selected from the group consisting of ethylene and propylene.
3. The method of claim 1 wherein the co-catalyst comprises methylalumoxane.
4. A method of producing a silyl-functionalized polyolefin comprising reacting a first functionalized olefin having the formula:
R″CH═CH—(Z) m —(CH 2 ) n SiRaR a R′ (3-a)
where Z is an electron withdrawing moiety, m is 0 or 1, n is an integer from 0-30, R is independently selected from the group consisting of alkoxy group and amine group, a has a value in the range 1 to 3 inclusive; R′ represents an hydrocarbyl group, R″ represents H or a group having an electron withdrawing effect or any other activation effect with respect to the —CH═CH— bond or a moiety containing an aromatic ring or a C═C bond conjugated with the —CH═CH— with an α-olefin having the general formula C x H 2x , where x is an integer between 1-30, in the presence of a catalytic amount of a group IV catalyst, for a time sufficient to produce a silyl-functionalized polyolefin, wherein the first functionalized olefin is incorporated in the silyl-functionalized polyolefin in from about 0.1 to about 25 mole % , wherein the group IV catalyst comprises a group IV constrained geometry catalyst (CGC) and wherein the group IV CGC has the formula: Me 2 Si(C 5 Me 4 )(NtBu)MCl 2 ; or Me 2 Si(C 5 Me 4 )(NtBu)MCH 3 ][CH 3 B(C 6 F 5 ) 3 ]; where M is selected from the group consisting of titanium and zirconium.
5. A method of producing a silyl-functionalized polyolefin comprising reacting a first functionalized olefin having the formula:
R″CH═CH—(Z) m —(CH 2 ) n SiR a R′ (3-a)
where Z is an electron withdrawing moiety, m is 0 or 1, n is an integer from 0-30, R is independently selected from the group consisting of alkoxy group and amine group, a has a value in the range 1 to 3 inclusive; R′ represents an hydrocarbyl group, R″ represents H or a group having an electron withdrawing effect or any other activation effect with respect to the —CH═CH—bond or a moiety containing an aromatic ring or a C═C bond conjugated with the —CH═CH—with an α-olefin having the general formula C x H 2x , where x is an integer between 1-30, in the presence of a catalytic amount of a group IV catalyst, for a time sufficient to produce a silyl-functionalized polyolefin, wherein the first functionalized olefin is incorporated in the silyl-functionalized polyolefin in from about 0.1 to about 25 mole % , wherein m is 1, Z is C(O)O—and n is comprised between 1 and 6, a is 3 and R is an alkoxy group.
6. The method of claim 1 wherein the silyl monomer incorporation is greater than 0.5 molar percent in the resulting polymer.
7. The method of claim 4 wherein the CGC is mixed with a co-catalyst comprising methylalumoxane at a molar ratio of 1:50 or higher.
8. The method of claim 1 ,
wherein a solvent is present and the solvent is selected from the group consisting of toluene, xylene, mesitylene, hexane, heptane, octane, and combinations thereof.