A process for producing granulated polymer materials from polymer solutions of thermoplastic polymers by pre-concentration of the polymer solution by means of heat exchange or stripping the solvent with steam in a holding tube or a heat exchanger to form concentrated polymer solution or paste, further concentration and drying in a drying apparatus, extrusion and granulation of the dried polymer, wherein the polymer solution, with a polymer concentration of 3 to 30% by weight in an organic solvent, is heated to 50.degree. to 300.degree. C. under a pressure of 1 to 15 bar in one or more heat exchangers, the total heat exchange surface of which is 0.02 m.sup.2 /100 kg/hr solvent to 2 m.sup.2 /100 kg/hr solvent, or is heated by mixing with superheated steam at a solvent to steam ratio of .gtoreq.10:1 in a heated or unheated holding tube having a length to diameter ratio of 100 to 10,000, or is heated by mixing with steam at a temperature of 100.degree. to 300.degree. C. and at a pressure of 1 to 100 bar in a heat exchanger, the heat exchange surface of which is 0.02 m.sup.2 /100 kg/hr solvent to 2 m.sup.2 /100 kg/hr solvent, and the mixture heated in this manner is separated by flashing into a separator with separation of the vapours to form a concentrated polymer solution or paste with a concentration of 25 to 80% by weight of the concentrated paste or solution with respect to the polymer,
- that the concentrated polymer solution or paste is heated and is further concentrated or degassed in a drying apparatus, which is provided with rotating built-in components for mechanically cleaning off the apparatus walls and for mass transfer, by heating the housing jacket or by heating the rotating built-in components or by heating the housing jacket and the rotating built-in components, and by the shearing caused by the built-in components moving in the separated material, wherein the temperature of the apparatus wall or of the built-in components is from 150.degree. to 400.degree. C.,
- concentration and degassing are effected at an internal pressure of 1 mbar to 5 bar, wherein in addition the total energy input expressed as the specific kneading energy
- with respect to the discharge throughput is 0.01 to 1 kWh per kg of dry polymer melt, and the dwell time in the drier is from 5 to 90 minutes.