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Mill-dryer technology attributes

  • Maximum possible exposure of the product surface to the air stream
  • High efficiency energy transfer from the hot air with split second residence times
  • High efficiency milling or de-agglomeration and coating
  • Outlet temperatures generally controlled at a lower value than other types of dryers
  • Improving thermal efficiency with lower dry product temperatures
Coating of fine mineral powders

Mineral powders are coated with a variety of materials as a surface modifier, in most cases to improve the dispersion performance of the mineral when used as a filler in products such as PVC extrusions. Stearic acid is commonly used with carbonates and amines are applied to kaolin. Silanes and titanates are used for application specific duties. Methods vary according to both the degree of coating accuracy required and the application. In some cases the accuracy of application must be within+1% error; in others it may be as low as +10% of the weight of coating agent. The coating method in each case is designed to suit the application. Coating levels can vary from as low 0.5% to over 2%.

Slurry feeds

Mill-dryer coating technology is now applied by the world's leading suppliers of high quality fillers and coated minerals. Slurry injection systems play an important part in its success as it is possible to simultaneously dry, de-agglomerate and coat the mineral, fed as a slurry from the wet milling stage, the dry powder typically being all less than 35µm with high efficiency de-agglomeration of sub 2µm particles.

In some dryer types this involves a 2-fluid injector system with high pressure steam or hot compressed air as an atomising medium to spray the wet-milled mineral slurry, pumped from a buffer vessel, into the mill-dryer. The slurry typically enters from the injector into the lower body of the mill-dryer mixing with the incoming process hot air at around 400ºC. Any surfactant is typically fed higher up the body from a compressed air assisted venture system. The feeding method is as sophisticated as required by the level of accuracy demanded for the application and can vary from simple volumetric feeders to co-ordinated loss-in-weight feeding systems.

Sample performance data

Dry coated powder production rates for a range of mill-dryers are typically as follows:


MILL SIZE DRYING & COATING COATING ONLY MILL MOTOR HOT AIR FLOW FOR DRYING FOR COATING ONLY
CM500 0.95t/h 1.7t/h 45kW 6,000 m3/h 3,500 m3/h
CM750 1.6t/h 2.8t/h 75kW 10,000 m3/h 6,000 m3/h
CM1000 2.2t/h 4.0t/h 90kW 14,000 m3/h 8,500 m3/h
CM1250 3.0t/h 5.0t/h 132kW 18,500 m3/h 10,500 m3/h
CM1500 4.0t/h 7.0t/h 160kW 25,000 m3/h 14,000 m3/h
CM2250 6.0t/h 10.5t/h 260kW 37,000 m3/h 21,500 m3/h


The air heater output varies over this range of drying duties from 500kW to 3MW. Specific energy for the plant other than the heater is~70kWh/t (kWh - kilowatt hours; kWh/t is a measure of electrical energy input in a given year) for simultaneous drying & coating from 35% moisture feed. For the same plant, the air heater specific energy is~500kWh/t. The total specific energy for simultaneous drying and coating for the plant is ~570kWh/t.

Slurries vary from 28-50% moisture. The above drying & coating specific energies are based on 35% moisture. Higher power motors as well as integral classifiers are also features of this type of unit if for instance it is to be used for drying and primary milling rather than just de-agglomeration. In some cases the classifier option is chosen for drying& de-agglomeration applications where quality assurance demands an absolute control of top size.


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