Two-stage process for the manufacture of thermoplastic polycarbonate

Abstract

The present invention provides a two-stage melt process for the manufacture of thermoplastic, solvent-free, low-branched polycarbonates with low OH end-group contents with the use of ammonium or phophonium catalysts in the first stage and alkali and alkaline earth catalysts in the second stage.

Description

Claims

1. Two-stage, solvent-free, process for the manufacture of low-branched polycarbonate having a content of phenolic OH groups of less than 20%, and an average molecular weight of 9,000 to 24,000, by melt transesterification of diphenols, carbonic acid diaryl esters, catalysts and optionally branching agents at temperatures between 80.degree. C. and 400.degree. C. and pressures of 1000 mbar to 0.01 mbar, characterized in that for the first stage, the oligocarbonate synthesis, nitrogen or phosphorus bases are used in amounts of 10.sup.-2 to 10.sup.-8 mole, relative to 1 mole diphenol, and after addition of the catalyst and application of vacuum (from atmospheric pressure to 0.5 mbar) and raising of the temperature (up to 300.degree. C.) an oligocarbonate is produced by distillation-off of monophenols, and the oligocarbonate is polycondensed in the second phase to the polycarbonate with the addition of alkali metal salts and alkaline earth metal salts in amounts of 10.sup.-4 to 10.sup.-8 mole, relative to 1 mole diphenol, at temperatures between 250.degree. C. and 400.degree. C. and pressures of less than 500 mbar to 0.01 mbar in a time less than 15 min, the oligocarbonate formed as an intermediate having an OH end-group content of more than 10% and less than 35% and further characterized in that the diphenols used or the carbonic acid diaryl esters used or the diphenols and the carbonic acid diaryl esters used have not passed through the solid phase after their manufacture or after their purification.

2. Process for the manufacture of aromatic polycarbonate in the melt according to claim 1, characterized in that the polycondensation is carried out in a high-viscosity reactor in less than 10 min.

3. Process for the manufacture of aromatic polycarbonate in the melt according to claim 1, characterized in that the polycondensation is carried out in a ZSK twin-screw kneader in less than 10 min.

4. Process for the manufacture of aromatic polycarbonate in the melt according to claim 1, characterized in that the oligocarbonate is isolated and thereafter polycondensed.