Aqueous suspension polymerization process

Claim 2

A process for forming a copolymer of styrene and butadiene comprising providing an aqueous phase comprising an aqueous mixture comprising water, styrene monomer, butadiene monomer, a suspension stabilizing agent, and a chain propogating amount of a free radical polymerization initiator insoluble in water, soluble in said styrene monomer, soluble in said butadiene monomer and having a 1 hour half-life between about 50° C. and about 130° C., the ratio of said styrene monomer and said butadiene monomer being between about 80:20 and about 95:5 by weight, the weight proportion of water to the combination of said styrene monomer and said butadiene monomer is between about 08:1 and about 2:1, said suspension stabilizing agent consisting essentially of a finely-divided, difficultly water-soluble powder and a vapour phase comprising an inert gas and butadiene monomer, heating said aqueous phase and said vapor phase to a temperature between about 50° C. and about 130° C. at a pressure between about 20 psi and about 140 psi in the absence of redox initiators and mercaptan compounds, removing butadiene monomer from said vapour phase after at least about 75 percent by weight of said butadiene monomer and said styrene monomer in said aqueous phase are converted to a copolymer and prior to conversion of more than about 98 percent by weight of said butadiene monomer and said styrene monomer to a copolymer in said aqueous phase, and heating said aqueous phase at a temperature between about 50° C. and about 130° C. at a pressure between about 20 psi and about 140 psi until at least about 90 percent by weight of said sytrene monomer and said butadiene monomer are copolymerized to form an aqueous suspension of discrete copolymer particles having a Tg value of between about 45° C. and about 65° C., a weight average molecular weight of between about 10,000 and about 400,000, a molecular weight distribution of said copolymer between about 2 and about 9 and a butadiene monomer concentration of less than about 10 parts per million by weight.

Claim 3

A process according to claim 1 including heating said aqueous mixture to a temperature less than about 100° C.

Claim 4

A process according to claim 1 including heating said aqueous mixture for less than about 8 hours.

Claim 5

A process according to claim 1 wherein said aqueous mixture comprises from about 0.05 percent to about 6.5 percent by weight of said free radical polymerization initiator based on the total weight of said styrene monomer and said butadiene monomer, said initiator having a one hour half-life at a temperature between about 50° C. and about 100° C.

Claim 6

A process according to claim 1 wherein said aqueous mixture comprises from about 0.5 percent to about 6.0 percent by weight of said suspension stabilizing agent based on the total weight of said styrene monomer and said butadiene monomer.

Claim 7

A process according to claim 1 including agitating said aqueous mixture while heating.

Claim 8

A process according to claim 1 including removing sufficient butadiene monomer from said vapour phase to reduce the butadiene monomer in said vapour phase to less than about 0.05 percent by volume.

Claim 9

A process according to claim 1 including removing said butadiene monomer from said vapour phase by venting, raising the pressure and venting, said raising the pressure and venting being repeated at least once.

Claim 10

A process according to claim 1 including heating said aqueous mixture in accordance with a predetermined heating profile comprising heating said aqueous mixture to a first temperature between about 50° C. and less than about 100° C., maintaining said first temperature in accordance with said predetermined heating profile, heating said aqueous mixture to a second temperature at least about 15° C. greater than said first temperature and greater than about 90° C. and less than about 130° C. in accordance with said predetermined heating profile and maintaining said second temperature in accordance with said predetermined heating profile.

Claim 11

A process according to claim 9 including introducing in said aqueous mixture prior to said heating at least two free radical polymerization initiators of which at least one becomes practically active only in the second temperature stage which is greater than about 90° C.

Claim 12

A process according to claim 9 including polymerizing between about 70 percent and about 95 percent of the total weight of said styrene monomer and said butadiene monomer at said first temperature prior to heating said aqueous mixture to said second temperature.

Claim 13

A process according to claim 9 including introducing additional styrene monomer, butadiene monomer and suspension stabilizing agent to said aqueous mixture at least one after heating to said first temperature, the proportions of said additional styrene monomer and butadiene monomer being between about 80:20 and about 95:5 by weight and polymerizing said additional styrene monomer and butadiene monomer at said second temperature until at least about 90 percent of said additional styrene monomer and butadiene monomer copolymerize.

Claim 14

A process according to claim 9 including introducing in said aqueous mixture after heating to said first temperature between about 0.05 and about 6.5 percent by weight based on the total weight of said monomers of at least one free radical polymerization initiator which becomes practically active only at said second temperature to extend the molecular weight distribution of the copolymer.

Claim 15

A process according to claim 1 including introducing additional styrene monomer, butadiene monomer, free radical polymerization initiator and suspension stabilizing agent to said aqueous mixture at least once after heating to said temperature, the proportions of said additional styrene monomer and butadiene monomer being between about 80:20 and about 95:5 by weight, and said additional free radical polymerization initiator being between about 0.05 and about 6.5 percent by weight based on the total weight of said monomers to extend the molecular weight distribution of said copolymer.

Claim 16

A process according to claim 14 including introducing said additional styrene monomer, butadiene monomer and suspension stabilizing agent to said aqueous suspension midway between initiation and termination of said heating step.

Claim 17

A process according to claim 14 wherein said suspension stabilizing agent is introduced immediately prior to or simultaneously with said additional styrene monomer and butadiene monomer.

Claim 18

A process according to claim 14 wherein said molecular weight distribution of said copolymer is between about 2 and about 8.

Claim 19

A process according to claim 14 wherein said additional styrene monomer and butadiene monomer comprise between about 60 percent and about 30 percent by weight of the total weight of the monomers introduced into said aqueous mixture.

Claim 20

A process for forming a copolymer of styrene and butadiene comprising providing an aqueous phase comprising an aqueous mixture comprising water, styrene monomer, butadiene monomer, a suspension stabilizing agent, and a chain propogating amount of a free radical polymerization initiator insoluble in water, soluble in said styrene monomer, soluble in said butadiene monomer and having a 1 hour half-life between about 50° C. and about 130° C., the ratio of said styrene monomer and said butadiene monomer being between about 80:20 and about 95:5 by weight, the weight proportion of water to the combination of said styrene monomer and said butadiene monomer is between about 0.8:1 and about 2:1, said suspension stabilizing agent consisting essentially of a finely-divided, difficultly water-soluble powder and a vapour phase comprising an inert gas and butadiene monomer, heating said aqueous phase and said vapour phase in accordance with a predetermined heating profile comprising heating said aqueous mixture to a first temperature between about 50° C. and less than about 100° C. at a pressure between about 20 psi and about 140 psi, maintaining said first temperature in accordance with said predetermined heating profile, removing butadiene monomer from said vapour phase after at least about 75 percent by weight of said butadiene monomer and said styrene monomer in said aqueous phase are converted to a copolymer and prior to conversion of more than about 98 percent by weight of said butadiene monomer and said styrene monomer to a copolymer in said aqueous phase, heating said aqueous mixture to a second temperature at least about 15° C. greater than said first temperature and greater than about 90° C. and less than about 130° C. in accordance with said predetermined heating profile, and maintaining said second temperature in accordance with said predetermined heating profile at a pressure between about 20 psi and about 140 psi until at least about 90 percent by weight of said styrene monomer and said butadiene monomer are copolymerized to form an aqueous suspension of discrete copolymer particles having a Tg value of between about 45° C. and about 65° C., a weight average molecular weight of between about 10,000 and about 400,000, a molecular weight distribution of said copolymer between about 2 and about 9 and a butadiene monomer concentration of less than about 10 parts per million by weight.

Claim 21

A process for forming a copolymer of styrene and butadiene comprising providing an aqueous phase comprising an aqueous mixture comprising water, styrene monomer, butadiene monomer, a suspension stabilizing agent, and a chain propogating amount of a free radical polymerization initiator insoluble in water, soluble in said styrene monomer, soluble in said butadiene monomer and having a 1 hour half-life between about 50° C. and about 130° C., the ratio of said styrene monomer and said butadiene monomer being between about 80:20 and about 95:5 by weight, the weight proportion of water to the combination of said styrene monomer and said butadiene monomer is between about 0.8:1 and about 2:1, said suspension stabilizing agent consisting essentially of a finely-divided, difficultly water-soluble powder and a vapour phase comprising an inert gas and butadiene monomer, heating said aqueous phase and said vapour phase in accordance with a predetermined heating profile comprising heating said aqueous mixture to a first temperature between about 50° C. and less than about 100° C. at a pressure between about 20 psi and about 140 psi, maintaining said first temperature in accordance with said predetermined heating profile, removing butadiene monomer from said vapour phase after at least about 75 percent by weight of said butadiene monomer and said styrene monomer in said aqueous phase are converted to a copolymer and prior to conversion of more than about 98 percent by weight of said butadiene monomer and said styrene monomer to a copolymer in said aqueous phase, heating said aqueous mixture to a second temperature at least about 15° C. greater than said first temperature and greater than about 90° C. and less than about 130° C. in accordance with said predetermined heating profile, and maintaining said second temperature in accordance with said predetermined heating profile at a pressure between about 20 psi and about 140 psi until at least about 90 percent by weight of said styrene monomer and said butadiene monomer are copolymerized to form an aqueous suspension of discrete copolymer particles having a Tg value of between about 45° C. and about 65° C., a weight average molecular weight of between about 10,000 and about 400,000, a molecular weight distribution of said copolymer between about 2 and about 9 and a butadiene monomer concentration of less than about 10 parts per million by weight.

Claim 22

A process according to claim 19 including introducing in said aqueous mixture prior to said heating at least two free radical polymerization initiators of which at least one becomes partially active only in the second temperature stage which is greater than about 90° C.

Claim 23

A process for forming a copolymer of styrene and butadiene comprising providing an aqueous phase comprising an aqueous mixture comprising water, styrene monomer, butadiene monomer, a suspension stabilizing agent, and a chain propogating amount of a free radical polymerization initiator insoluble in water, soluble in said styrene monomer, soluble in said butadiene monomer and having a 1 hour half-life between about 50° C. and about 130° C., the ratio of said styrene monomer and said butadiene monomer being between about 80:20 and about 95:5 by weight, the weight proportion of water to the combination of said styrene monomer and said butadiene monomer is between about 08:1 and about 2:1, said suspension stabilizing agent consisting essentially of a finely-divided, difficultly water-soluble powder and a vapour phase comprising an inert gas and butadiene monomer, heating said aqueous phase and said vapour phase to a temperature between about 50° C. and about 130° C. at a pressure between about 20 psi and about 140 psi in the absence of redox initiators and mercaptan compounds, introducing additional styrene monomer, butadiene monomer, free radical polymerization initiator and suspension stabilizing agent to said aqueous mixture at least once after heating to said temperature, the proportions of said additional styrene monomer and butadiene monomer being between about 80:20 and about 95:5 by weight, and said additional free radical polymerization initiator being between about 0.05 and about 6.5 percent by weight based on the total weight of said monomers to extend the molecular weight distribution of said copolymer, heating said aqueous phase and said vapour phase to a temperature between about 50° C. and about 130° C. at a pressure between about 20 psi and about 140 psi in the absence of redox initiators and mercaptan compounds until said styrene monomer and said butadiene monomer form an aqueous suspension of discrete copolymer particles, removing butadiene monomer from said vapour phase after at least about 75 percent by weight of said butadiene monomer and said styrene monomer in said aqueous phase are converted to a copolymer and prior to conversion of more than about 98 percent by weight of said butadiene monomer and said styrene monomer to a copolymer in said aqueous phase, and heating said aqueous phase at a temperature between about 50° C. and about 130° C. at a pressure between about 20 psi and about 140 psi until at least about 90 percent by weight of said styrene monomer and said butadiene monomer are copolymerized to form an aqueous suspension of discrete copolymer particles having a Tg value of between about 45° C. and about 65° C., a weight average molecular weight of between about 10,000 and about 400,000, a molecular weight distribution of said copolymer between about 2 and about 9 and a butadiene monomer concentration of less than about 10 parts per million by weight.

Claim 24

A process for forming a copolymer of styrene and butadiene comprising providing an aqueous phase comprising an aqueous mixture comprising water, styrene monomer, butadiene monomer, a suspension stabilizing agent, and a chain propogating amount of a free radical polymerization initiator insoluble in water, soluble in said styrene monomer, soluble in said butadiene monomer and having a 1 hour half-life between about 50° C. and about 130° C., the ratio of said styrene monomer and said butadiene monomer being between about 80:20 and about 95:5 by weight, the weight proportion of water to the combination of said styrene monomer and said butadiene monomer is between about 08:1 and about 2:1, said suspension stabilizing agent consisting essentially of a finely-divided, difficultly water-soluble powder and a vapour phase comprising an inert gas and butadiene monomer, heating said aqueous phase and said vapour phase to a temperature between about 50° C. and about 130° C. at a pressure between about 20 psi and about 140 psi in the absence of redox initiators and mercaptan compounds, introducing additional styrene monomer, butadiene monomer, free radical polymerization initiator and suspension stabilizing agent to said aqueous mixture at least once after heating to said temperature, the proportions of said additional styrene monomer and butadiene monomer being between about 80:20 and about 95:5 by weight, and said additional free radical polymerization initiator being between about 0.05 and about 6.5 percent by weight based on the total weight of said monomers to extend the molecular weight distribution of said copolymer, heating said aqueous phase and said vapour phase to a temperature between about 50° C. and about 130° C. at a pressure between about 20 psi and about 140 psi in the absence of redox initiators and mercaptan compounds until said styrene monomer and said butadiene monomer form an aqueous suspension of discrete copolymer particles, removing butadiene monomer from said vapour phase after at least about 75 percent by weight of said butadiene monomer and said styrene monomer in said aqueous phase are converted to a copolymer and prior to conversion of more than about 98 percent by weight of said butadiene monomer and said styrene monomer to a copolymer in said aqueous phase, and heating said aqueous phase at a temperature between about 50° C. and about 130° C. at a pressure between about 20 psi and about 140 psi until at least about 90 percent by weight of said styrene monomer and said butadiene monomer are copolymerized to form an aqueous suspension of discrete copolymer particles having a Tg value of between about 45° C. and about 65° C., a weight average molecular weight of between about 10,000 and about 400,000, a molecular weight distribution of said copolymer between about 2 and about 9 and a butadiene monomer concentration of less than about 10 parts per million by weight.

Claim 25

A process according to claim 21 including introducing in said aqueous mixture prior to said heating at least two free radical polymerization initiators of which at least one becomes spractically active only in the second temperature stage which is greater than about 90° C.