Vinylene carbonate polymers, a process for their preparation and their use

Claim 2

A polymer essentially composed of units which are derived from vinylene carbonate or a derivative thereof which is substituted by a monovalent hydrocarbon radical having up to 8 carbon atoms, and of at least one other monomer which can be copolymerized with it, the mean particle size of the polymer particles being in the range from 20 to 800 um, wherein the polymer particles have an essentially spherical shape and a mean pore diameter of 5 to 1,000 nm.

Claim 3

The polymer as claimed in claim 1, wherein the mean pore diameter is 10 to 500 nm.

Claim 4

The polymer as claimed in claim 1, wherein the amount of vinylene carbonate units is 5 to 90 mole-% relative to the total polymer.

Claim 5

The polymer as claimed in claim 1, which, in addition to the vinylene carbonate units, contains units which are derived from monomers having hydrophilic groups.

Claim 6

The polymer as claimed in claim 4, which, as a consequence of incorporation of crosslinking monomer units, is crosslinked.

Claim 7

A process for the preparation of the polymer as claimed in claim 1, by polymerization of vinylene carbonate or a derivative thereof which is substituted by a monovalent hydrocarbon radical having up to 8 carbon atoms with at least one monomer which can be copolymerized with vinylene carbonate, in a liquid dispersing medium, which does not dissolve the monomers and the polymer under the polymerization conditions, in the presence of a radical initiator and a dispersion stabilizer, which comprises using, as the dispersion stabilizer, a copolymer of maleic anhydride and a vinyl alkyl ether having 6 to 30 carbon atoms in the alkyl group, or a vinyl ester having 6 to 30 carbon atoms in the carboxylic acid group, or a relatively long-chain α-olefin having 8 to 30 carbon atoms.

Claim 8

The process as claimed in claim 6, wherein the dispersion stabilizer is used in amounts of 0.005 to 10% by weight relative to the mixture of monomers.

Claim 9

The process as claimed in claim 6, wherein the dispersion stabilizer is an alternating copolymer.

Claim 10

The process as claimed in claim 6, wherein the RSV value of the copolymer employed as a dispersion stabilizer is between 0.01 and 1.0 [dl/g] (measured in 0.6% strength solution in toluene at 25° C.).

Claim 11

The process as claimed in claim 6, wherein the vinyl alkyl ether is vinyl stearyl ether and the relatively long-chain α-olefin is 1-octadecene.

Claim 12

The process as claimed in claim 6, wherein hydrocarbons having 6 to 20 carbon atoms, or low viscosity liquid paraffin is employed as the liquid dispersing agent.

Claim 13

The process as claimed in claim 6, wherein, in order to increase the porosity of the bead polymer, the polymerization system contains materials which are readily soluble in or miscible with the monomers and are virtually insoluble in the dispersing medium.