Amorphous polyester composition and method of making
AssigneeDdp Specialty Electronic Materials US, LLC
InventorsMark Alan Barger, Stephane Costeux, Michal Elizabeth Porter, Patrick Heider
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Abstract
An amorphous polyester or copolyester composition comprises the reaction product of a crystalline or semicrystalline polyester or copolyester, optionally derived from a recycled waste stream, at least one diol or aromatic diacid or an ester of a diacid or a hydroxycarboxylic acid or a lactone or a dianhydride, and a catalyst, wherein the amorphous composition has a weight average molecular weight of at least 10,000 g/mol (polystyrene equivalent molecular weight) as measured by gel permeation chromatography.
Claims15
A foamable composition comprising an amorphous polyester or copolyester composition comprising the reaction product of crystalline or semicrystalline polyester or copolyester, optionally derived from a recycled waste stream, at least one diol or aromatic diacid or an ester of a diacid or a hydroxycarboxylic acid or a lactone or a dianhydride, and
- a catalyst,
- wherein the amorphous composition has a weight average molecular weight of at least 10,000 g/mol, polystyrene equivalent molecular weight, as measured by gel permeation chromatography, and one or more blowing agents.
A method of making an amorphous polyester foamable resin composition comprising the steps of:
- combining at room temperature in a reactor, a crystalline or semi-crystalline polyester, optionally derived from a recycled waste stream, with at least one diol or aromatic diacid or an ester of a diacid or a hydroxycarboxylic acid or a lactone or a dianhydride, and in the presence of a catalyst,
- sealing and purging the reactor with an inert gas,
- mixing the contents,
- evacuating the reactor of volatile components,
- flushing the reactor at least once with an inert gas,
- increasing the temperature of the reactor to between 250-350 degrees C. over a period of from 30 to 90 minutes,
- mixing the molten material combination
- maintaining a temperature of between 250-350 degrees C. for between 20 to 150 minutes,
- evacuating the reactor to minus 25 inches of mercury or lower,
- continuing the reaction at a temperature of from 250-350 degrees C. for between 100 to 300 minutes, optionally while removing volatile species via a distillation column, and
- stopping the reaction by ceasing mixing, purging the reactor with an inert gas, returning the reactor to atmospheric pressure and reducing the temperature to 100 degrees C. or lower,
- wherein the resultant composition has a weight average molecular weight of at least 10,000 g/mol (polystyrene equivalent molecular weight) as measured by gel permeation chromatography) and a degree of crystallinity no greater than 5% as determined by differential scanning calorimetry.
Dependencies are inferred from the claim text.