METHOD FOR DRYING BULK MATERIAL
The invention relates to a method for drying bulk goods, in particular solids, such as granular materials, powders, grains, films, shreds, or the like, preferably plastic granular material, in a drying silo ( 7 ) by means of an air flow. The moistened returned air or the process air flow ( 10 ) that emerges from the drying silo ( 7 ) is dried in a drying cell containing a drying or adsorbent agent and returned in the form of a drying air flow ( 12 ) to the bulk goods again. The drying cell is preferably a wheel dryer ( 11 ) consisting of an air distribution cover and an air distribution floor having a rotatable drum arranged therebetween. The adsorbent agent is furthermore regenerated in the wheel dryer ( 11 ). The drum of the wheel dryer ( 11 ) is divided by the air distribution cover and the air distribution floor into two regions through which air is able to flow. One region ( 5 ) is used to regenerate the adsorbent agent and the other region ( 6 ) is used for drying or dehumidifying the process air flow ( 10 ). The region ( 6 ) for drying or dehumidifying the process air flow ( 10 ) adjoins the region ( 5 ) for regenerating the adsorbent agent, wherein the hot adsorbent agent is introduced uncooled into the region ( 6 ) for drying or dehumidifying the process air flow ( 10 ).
1 . Method for drying bulk material, in particular solids, such as granulates, powder, grains, foils, chips, or the like, preferably plastic granulate, in a drying silo ( 7 ) by means of an air flow, wherein the moistened returned air or the process air flow ( 10 ) that emerges from the drying silo ( 7 ) is dried in a drying cell containing a drying or adsorbent agent, said drying cell preferably being a wheel dryer ( 11 ) consisting of an air distribution cover and an air distribution floor having a rotatable drum arranged therebetween, and returned in the form of a drying air flow ( 12 ) to the bulk goods again and the adsorbent agent is furthermore regenerated in the wheel dryer ( 11 ), characterized in that the drum of the wheel dryer ( 11 ) is divided by the air distribution cover and the air distribution floor into just two regions through which air is able to flow, wherein one region ( 5 ) is used to regenerate the adsorbent agent and the other region ( 6 ) is used for drying or dehumidifying the process air flow ( 10 ) and that the region ( 6 ) for drying or dehumidifying the process air flow ( 10 ) directly adjoins the region ( 5 ) for regenerating the adsorbent agent, wherein the hot adsorbent agent is introduced uncooled into the region ( 6 ) for drying or dehumidifying the process air flow ( 10 ).
2 . Method in accordance with claim 1 , characterized in that the regeneration air flow ( 13 ) for regenerating the adsorbent agent is taken from the process air flow ( 10 ) as partial air flow.
3 . Method in accordance with claim 1 , characterized in that the drying and dehumidifying for the process air flow ( 10 ) and the regenerating of the adsorbent agent occur in parallel, in particular in a continuous manner during permanent operation.
4 . Method in accordance with claim 1 , characterized in that the regenerating of the adsorbent agent is carried out during operation at intervals, whereby the drum of the wheel dryer ( 11 ) is stopped and advanced to a selectable region, preferably the region for regenerating, after the regenerating.
5 . Method in accordance with claim 4 , characterized in that, during operation at intervals, while the drum stands still, the heater ( 2 ) for the regenerating is switched off after the regeneration and the unheated partial flow of the process air flow ( 10 ) flows through the region for regenerating.
6 . Method in accordance with claim 1 , characterized in that the region ( 5 ) for regenerating is defined smaller than the region ( 6 ) for drying or dehumidifying the process air flow ( 10 ).
7 . Method in accordance with claim 1 , characterized in that the region ( 6 ) for drying or dehumidifying amounts to approximately 260 to 300 arc degrees and the region ( 5 ) for heating amounts to approximately 60 to 100 arc degrees.
8 . Method in accordance with claim 1 , characterized in that, by means of the airflow predefined by the air distribution cover or air distribution floor, multiple units, consisting of a region ( 5 ) for regenerating and a region ( 6 ) for drying and dehumidifying, are provided on the rotatable drum of the wheel dryer ( 11 ).