Method for obtaining polybutadiene based aqueous dispersions
AssigneeArkema Inc.
InventorsDamien Colombie, Frederic Lemahieu, Denis Temboun N' Zudie
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Abstract
The invention relates to a method for preparing butadiene-based aqueous dispersions in the presence of at least one azocarboxylic acid ester.
Claims8
A process for obtaining aqueous dispersions of copolymers, which consists in polymerizing a blend of monomers containing at least 60% by weight of butadiene and at least one monomer chosen from styrene, acrylic esters, vinyl nitrites with optionally up to 40% by weight of one or more other copolymerizable unsaturated monomers, as an aqueous emulsion in the presence of one or more free-radical initiator(s), is characterized in that at least one of the initiators or the initiator is an azocarboxylic acid ester of formula (I):
- 2
- in which:
- R1, R2, R3 and R4, which may be identical or different, are independently selected from the group consisting of
- linear or branched alkyls containing from 1 to 9 carbon atoms and preferably from 1 to 4 carbon atoms, optionally substituted with one or more substituents selected from hydroxyl, C1 to C6 alkoxy and halogen substituents;
- C3 to C12 cycloalkyls, optionally substituted with one or more substituents selected from C1 to C6 alkyl, C1 to C6 alkoxy, hydroxyl and halogenated groups;
- aralkyls optionally substituted with one or more C1 to C6 alkyl, C1 to C6 alkoxy, hydroxyl and halogenated groups;
- aryls optionally substituted with one or more substituents selected from C1 to C6 alkyl, C1 to C6 alkoxy, hydroxyl and halogenated groups;
- with at least one of the combinations R1-R2 and R3-R4 possibly forming an aliphatic ring;
- R″ and R′ are identical or different and are independently selected from the group consisting of linear or branched C1 to C10 and preferably C1 to C4 aliphatic radicals.
The process as claimed in any one of the preceding claims, characterized in that the azocarboxylic acid ester is used in combination with the usual emulsion polymerization initiators such as persulfates and hydroperoxides.
The process as claimed in any one of the preceding claims, characterized in that the total amount of initiators is between 0.05% and 4% by weight relative to the weight of monomers.
The process as claimed in any one of the preceding claims, characterized in that the polymerization is performed in the presence of a transfer agent.
The process as claimed in any one of the preceding claims, characterized in that the polymerization temperature is between 40 and 100° C. and preferably between 50 and 90° C.
Dependencies are inferred from the claim text.