Process for producing hyperbranched polymers

Synthetic resins or natural rubbers -- part of the class 520 ser – Synthetic resins – Polymerizing in tubular or loop reactor

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526335, 526336, 526337, 526338, 526339, 526340, 526348, C08F 200, C08F 3600, C08G 8500

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active

059860200

ABSTRACT:
A method is provided for producing hyperbranched polymers comprising heating a polymerizable reaction charge comprising (a) a monomer mixture comprising 50-99.1% by weight of at least one monoethylenically unsaturated monomer and 0.1-50% by weight of one or more multiethylenically unsaturated monomers and (b) if at least one ethylenically unsaturated monomer of the monomer mixture is not a thermally initiating monomer, a free radical polymerization initiator, to a temperature in the range from about 250.degree. C. to about 400.degree. C. in a continuous reactor which allows mixing of the reactor contents for a residence time of from about 2 minutes to about 60 minutes, provided that if the total amount of multiethylenically unsaturated monomer is less than 3% by weight of the monomer mixture than at least one of said one or more multiethylenically unsaturated monomers must be tri- or greater ethylenically unsaturated. The hyperbranched polymers prepared by this process are also described.

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DeLassus,"Incorporation of Benzocyclobutene into Polystyrene Allowing Postpolymerizer Chain Extension/Branching", Macromolecules 1994, vol. 27, pp. 1307-1312.
Hamielec, "Polymerization Processes," Ullmann's Encyclopedia of Industrial Chemistry, vol. A21, 5th Ed., 1992.

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