Process for producing vinyl aromatic (co)polymer incorporating post-consumer and/or post-industrial recycled polystyrene
The present invention is related to a process for the production of a vinyl aromatic (co)polymer comprising the steps of: a) mixing a fraction (A) comprising one or more monomers selected from the group consisting of styrene, alpha-methyl styrene, acrylonitrile, methyl (meth)acrylate, (meth)acrylic acid and butadiene with a fraction (B) comprising post-consumer recycled vinyl aromatic (co)polymer, wherein the weight ratio of fraction (B) to fraction (A) is comprised between 0.01/1 and 1/1, preferably between 0.05/1 and 0.5/1 b) subjecting the resulting mixture to a free-radical polymerization and polymerizing to a monomer conversion up to 90%, to obtain a polymerized mixture comprising vinyl aromatic (co)polymer; c) vacuum devolatizing the polymerized mixture and recovering vinyl aromatic (co)polymer characterized by a weight average molecular weight comprised between 100,000 and 400,000 g/mol; wherein one or more bromine derivative capture agents are added before, and/or during and/or after at least one of the steps a) to c); and wherein 100 parts of one or more bromine derivative capture agents comprises at least 50 parts by weight of hydrotalcite of the formula: [Mg 1-x Al x (OH) 2 ] x+ (CO 3 ) x/2 ·m H 2 O wherein: 0 <x≤0.5, and m is a positive number. The present invention is also related to expandable and extruded expanded vinyl aromatic (co)polymer compositions obtained from vinyl aromatic (co)polymers comprising post-consumer and/or post-industrial vinyl aromatic (co)polymer and to a process for the production of said expandable and extruded expanded vinyl aromatic (co)polymer compositions.
1 . A process for the production of a vinyl aromatic (co) polymer comprising:
a) mixing
a fraction (A) comprising one or more monomers selected from the group consisting of styrene, alpha-methyl styrene, acrylonitrile, methyl (meth)acrylate, (meth)acrylic acid and butadiene with
a fraction (B) comprising recycled vinyl aromatic (co) polymer comprising post-consumer recycled polystyrene (PCR-PS) and/or post-industrial recycled polystyrene (PIR-PS) comprising halogenated flame retardant, wherein the recycled vinyl aromatic (co) polymer of fraction (B) is characterized by a weight average molecular weight comprised between 100,000 and 400.00 g/mol, wherein fraction (B) comprises bromine containing flame retardant and flame-retardant synergists, and wherein the weight ratio of fraction (B) to fraction (A) is comprised between 0.01/1 and 1/1;
b) subjecting the resulting mixture to a free-radical polymerization, and polymerizing to a monomer conversion of up to 90%, to obtain a polymerized mixture comprising vinyl aromatic (co) polymer;
c) vacuum devolatizing the polymerized mixture and recovering vinyl aromatic (co) polymer characterized by a weight average molecular weight comprised between 100,000 and 400,000 g/mol;
wherein one or more bromine derivative capture agents are added in an amount of from 0.01 to 6 parts for 100 parts of (co) polymer, PCR/PIR-PC, oligomers and/or monomers before and/or during and/or after at least one of the steps a) to b) and before the devolatizing step c); and
wherein 100 parts of one or more bromine derivative capture agents comprises at least 50 parts by weight of hydrotalcite of the formula:
[Mg 1-x Al x (OH) 2 ] x+ (CO 3 ) x/2 ·m H 2 O
wherein:
0<x≤0.5, and m is a positive number.
2 . The process according to claim 1 comprising the additional step of filtering the mixture of step a) over a filter with a mesh size comprised between 10 and 1000, before initiating step b).
3 . The process according to claim 1 wherein fraction (B) comprises between 100 and 40,000 ppm of bromine.
4 . The process according to claim 1 wherein the one or more bromine derivative capture agents are added in such an amount that the weight ratio of bromine derivative capture agent over bromine of the bromine containing flame retardant of fraction (B) is 4 or less.
5 . The process according to claim 1 wherein the polymerization in step b) is performed in a continuous multi reactor process, starting at a temperature comprised between 115° C. and 150° C. and stepwise increasing to a temperature comprised between 145° C. and 190° C.
6 . The process according to claim 1 wherein vacuum devolatilizing of step c) is performed at a temperature comprised between 210° C. and 255° C. and a pressure comprised between 1 and 50 mbar·abs.