Device and method for degassing solvent-containing polycarbonate solutions
The invention relates to an apparatus and a process for devolatilizing solvent-containing polycarbonate solutions. By employing the inventive apparatus, polycarbonates with low residual values of volatile constituents are produced from solvent-containing polymer melts, which improved optical properties, especially yellowness index, with the aid of an apparatus combination of a flash devolatilizer and a vented extruder.
1. An apparatus for devolatilizing solvent-containing polycarbonate melts, wherein a flash devolatilizer, comprising an inlet having one or more pipes with orifices, is combined with a vented extruder, said flash devolatilizer being arranged directly above said extruder.
2. The apparatus as claimed in claim 1 , wherein vapor lines are mounted on the flash devolatilizer.
3. The apparatus as claimed in claim 1 , wherein the flash devolatilizer is heated by means of condensing steam, by means of a condensing organic heat carrier or by means of a liquid organic heat carrier.
4. The apparatus as claimed in claim 1 , wherein the combination of a flash devolatilizer and vented extruder is upstream of at least one further flash devolatilizer.
5. The apparatus as claimed in claim 1 , wherein the vented extruder is of two- or four-shaft design.
6. The apparatus as claimed in claim 1 , wherein the vented extruder is a closely intermeshing, corotatory twin-screw extruder.
7. The apparatus as claimed in claim 1 , wherein the extruder has several devolatilizing zones in a conveying direction.
8. A process for devolatilizing polycarbonate solutions as claimed in claim 1 , wherein a polycarbonate solution comprising at least one organic solvent and at least one polycarbonate is prepared by the interfacial process and, in a second step, this polycarbonate solution is supplied to a flash devolatilizer in combination with a vented extruder, said flash devolatilizer being arranged directly above the extruder such that the polymer solution falls directly into the vented extruder.
9. The process as claimed in claim 8 , wherein the solvent-containing vapors formed in the flash devolatilizer are removed directly from the housing of the flash devolatilizer by means of vapor lines.
10. The process as claimed in claim 8 , wherein inert gases as entraining agents are injected into and mixed into the polymer melt stream upstream of the flash devolatilizer.
11. The process as claimed in claim 8 , wherein inert gas is injected as entraining agent in one or more housings of the vented extruder.
12. The process as claimed in claim 8 , wherein the input concentration of the polycarbonate into the flash devolatilizer is between 60% by weight and 95% by weight.
13. The process as claimed in claim 8 , wherein the polymer is heated by means of a heat exchanger before entering the flash devolatilizer.
14. The process as claimed in claim 8 , wherein the polycarbonates obtained have a residual solvent content of 20 ppm to 1000 ppm.