Abstract A process for the continuous preparation of ABS polymers by free-radical-initiated polymerization of, in particular, styrene and acrylonitrile in the presence of polybutadiene, in the presence or absence of a solvent, in a reactor cascade comprising at least 3 stirred reactors operating essentially without back-mixing, at least some of which contain internal cooling tubes for dissipating the heat of polymerization, at from 50 to 180° C., phase inversion taking place in one of the reactors which contains means for generating a high shear force, and an apparatus for carrying out the process comprising an essentially cylindrical/tubular vessel jacket and a cylindrical internal element connected to a stirrer shaft by rotational force and having an external diameter which is slightly less than the internal diameter of the vessel jacket.
A process for the continuous preparation of ABS polymers by fre radical-initiated polymerization of a mixture of from 60 to 90% by weight of at least one vinylaromatic momomer and from 10 to 40% by weight of at least one different ethylenically unsaturated momomer, in the presence of from 5 to 30% by weight, based on the total of momomers, of polybutadiene having a solution viscosity as measured in 5% strength by weight in styrene at 25° C. of from 25 to 95 mPa.s, in the presence or absence of a solvent, in a reactor cascade comprising at least 3 stirred reactors operating essentially without back-mixing and at least some of which having internal cooling tubes for dissipating the heat of polymerization, at from 50 to 180° C., phase inversion takes place under a high shear force in a reactor which contains means for generating such a shear force.
Claim 2
Dependent Claim
149 words
A process for the continuous preparation of ABS polymers by fre radical-initiated polymerization of a mixture of from 60 to 90% by weight of at least one vinylaromatic momomer and from 10 to 40% by weight of at least one different ethylenically unsaturated momomer, in the presence of from 5 to 30% by weight, based on the total of momomers, of polybutadiene having a solution viscosity as measured in 5% strength by weight in styrene at 25° C. of from 25 to 95 mPa.s, in the presence or absence of a solvent, in a reactor cascade comprising at least 3 stirred reactors operating essentially without back-mixing and at least some of which having internal cooling tubes for dissipating the heat of polymerization, at from 50 to 180° C., phase inversion takes place under a high shear force in a reactor which contains means for generating such a shear force.
Claim 3
Dependent Claim
19 words
A process as defined in claim 1, wherein the vinylaromatic monomer is styrene and the different monomer is acrylonitrile.
Claim 4
Dependent Claim
9 words
The process of claim, wherein the solvent is ethylbenzene.