FIELD: polymer production. SUBSTANCE: method is implemented on tubular reactor at pressure 500 to 4000 bar and maximum temperature 218 C in presence of catalyst-initiator. Radical-type polymerization is initiated in by at least two tubular reactor sites. Temperature profile in reactor is controlled such that maximum temperature behind catalyst-initiator addition point is limited by 199 and 218 C and differ from each other by less than +/- 3 C. Pigment concentrates prepared from subject copolymers are used for dyeing plastics. EFFECT: increased homogeneity and thermal stability. 5 cl, 1 tbl, 5 ex
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Authors
Dates
2004-02-27—Published
1998-09-05—Filed