Styrenic polymers having reduced trimer content
Disclosed are styrenic polymers made by a mass or solution process, where the amount of trimer consisting of styrene and/or acrylonitrile is less than about 0.50 weight percent. Also disclosed is a method of minimizing the amount of trimer consisting of styrene and/or acrylonitrile in styrenic polymers made by a mass or solution process. The method includes the steps of lowering the temperature of the polymerization reaction mixture and including more than one initiator in the polymerization reaction mixture.
1. A method of reducing the amount of trimers consisting of styrene and/or acrylonitrile in a styrenic polymer made by mass or solution process comprising:
providing a polymerization reaction mixture comprised of styrene, acrylonitrile, and more than one initiator, and
reacting the polymerization reaction mixture at a polymerization temperature within a range of 112° C. to 250° C., with at least one polymerization temperature being at least 160° C. wherein the polymerization reaction mixture is further comprised of N-phenyl maleimide, the one or more initiators of the polymerization reaction mixture is comprised of a first and a second initiator, the second initiator having a T (1 hr) half-life that is higher than the T (1 hr) half-life of the first initiator, the T (1 hr) half-life of the second initiator being at least 20° C. higher than the T (1 hr) half-life of the first initiator, and the second initiator is present in an amount that is greater than the first initiator.
2. The method of claim 1 , wherein the amount of trimers is less than 0.5 weight percent of the styrenic polymer.
3. The method of claim 2 , wherein the amount of trimers is greater than 0.1 weight percent of the styrenic polymer.
4. The method of claim 2 , wherein the amount of trimers is less than 0.4 weight percent of the styrenic polymer.
5. The method of claim 1 , wherein the first initiator is present in an amount of 60 to 115 ppm and the second initiator is present in an amount from 200 ppm to 800 ppm to.
6. The method of claim 5 , wherein the amount of the second initiator is 200 ppm to 300 ppm, the T (1 hr) half-life of the first initiator being at least 112° C., and the T (1 hr) half-life the second initiator being at least 134° C.
7. A method of reducing the amount of trimers consisting of styrene and/or acrylonitrile in a styrenic polymer made by mass or solution process comprising:
providing a polymerization reaction mixture comprised of styrene, acrylonitrile, and more than one initiator, and
reacting the polymerization reaction mixture at a polymerization temperature within a range of 60° C. to 250° C., wherein the polymerization reaction mixture is further comprised of N-phenyl maleimide, and one or more of maleic acid, fumaric acid, maleic anhydride, dimethyl maleate, diethyl maleate, dibutyl maleate, dimethyl fumarate, diethyl fumarate or dibutyl fumarate.
8. The method of claim 1 , wherein the polymerization temperature range is from 112° C. to 200° C.
9. The method of claim 1 , wherein the reacting is raised from a lower temperature to a higher temperature within the range of polymerization reaction temperatures.