The invention relates to a method for drying a wet polymer composition obtained from a polymerization process, comprising: a) introducing the wet polymer composition and a drying gas into a fluidized bed dryer to form a fluidized bed of the wet polymer composition and b) heating the fluidized bed to obtain a dry polymer composition, wherein the fluidized bed further comprises an anti-fouling agent comprising inert nanoparticles.

The invention relates to a method for drying a wet polymer composition obtained from a polymerization process, comprising: a) introducing the wet polymer composition and a drying gas into a fluidized bed dryer to form a fluidized bed of the wet polymer composition and b) heating the fluidized bed to obtain a dry polymer composition, wherein the fluidized bed further comprises an anti-fouling agent comprising inert nanoparticles.

A magnetic field thermal generator has one or more heat elements comprised of rotating pipes placed so they travel across the magnetic field generated by the magnetic field chamber, with said magnetic field being generated by either permanent magnets or electromagnets. The relative motion of the heat element to the magnetic flux from the magnetic field magnets results in heat generation, as well as in the generation of Oxyhydrogen (HHO). An optional hydrogen separator may be used to separate the HHO into the Hydrogen and Oxygen components.

A magnetic field thermal generator has one or more heat elements comprised of rotating pipes placed so they travel across the magnetic field generated by the magnetic field chamber, with said magnetic field being generated by either permanent magnets or electromagnets. The relative motion of the heat element to the magnetic flux from the magnetic field magnets results in heat generation, as well as in the generation of Oxyhydrogen (HHO). An optional hydrogen separator may be used to separate the HHO into the Hydrogen and Oxygen components.

A circulating mill, comprising primary mills (47, 57) and secondary mills (49, 61), and first and second inner circulation pipes (48, 58, 52, 64). The first inner circulation pipes (48, 58) are connected to air outlets of the primary mills (47, 57) and inner circulation pipe interfaces (3, 11), and the second inner circulation pipes (52, 64) are connected to air outlets of the secondary mills (49, 61) and the inner circulation pipe interfaces (3, 11); the inner circulation pipe interfaces (3, 11) are located on a housing (1) of the primary mills (47, 57) or the secondary mills (49, 61), or located on feed pipes (56, 60) of which one end is connected to the air inlet of the housing (1); a kinetic energy recovery device is mounted in the feed pipes (56, 60), and the kinetic energy recovery device is connected to an impeller in the housing (1).

A circulating mill, comprising primary mills (47, 57) and secondary mills (49, 61), and first and second inner circulation pipes (48, 58, 52, 64). The first inner circulation pipes (48, 58) are connected to air outlets of the primary mills (47, 57) and inner circulation pipe interfaces (3, 11), and the second inner circulation pipes (52, 64) are connected to air outlets of the secondary mills (49, 61) and the inner circulation pipe interfaces (3, 11); the inner circulation pipe interfaces (3, 11) are located on a housing (1) of the primary mills (47, 57) or the secondary mills (49, 61), or located on feed pipes (56, 60) of which one end is connected to the air inlet of the housing (1); a kinetic energy recovery device is mounted in the feed pipes (56, 60), and the kinetic energy recovery device is connected to an impeller in the housing (1).

A reflective particulate material comprises a particulate substrate, and a coating on the particulate substrate. The coated reflective particulate material may have a relative error of an amount of the coating on the particulate substrate of about 5% to about 15%, and/or a dust index of about 5 or lower, and/or a staining loss of about 8% to about 11%. A method of manufacturing the reflective particulate material comprises mixing the particulate substrate with a liquid coating composition to form a wet particulate mixture, passing the wet particulate mixture through at least one heat zone to remove water and/or moisture, and curing the coating material in the coating composition.

A reflective particulate material comprises a particulate substrate, and a coating on the particulate substrate. The coated reflective particulate material may have a relative error of an amount of the coating on the particulate substrate of about 5% to about 15%, and/or a dust index of about 5 or lower, and/or a staining loss of about 8% to about 11%. A method of manufacturing the reflective particulate material comprises mixing the particulate substrate with a liquid coating composition to form a wet particulate mixture, passing the wet particulate mixture through at least one heat zone to remove water and/or moisture, and curing the coating material in the coating composition.

A method for preparing a dried powder is provided. The facility includes a first drying chamber having a heating element and a second drying chamber. A mixture of powder and diluent is introduced into the first drying chamber. A pre-dried powder is transferred from the first drying chamber into the second drying chamber. A dried powder, including a recirculated amount of powder and a discharge amount of powder, is formed in the second drying chamber. The recirculated amount of the dried powder is transferred by a conveyor device from the second drying chamber into the first drying chamber. The discharge amount of the dried powder is discharged from the second drying chamber.

A method for preparing a dried powder is provided. The facility includes a first drying chamber having a heating element and a second drying chamber. A mixture of powder and diluent is introduced into the first drying chamber. A pre-dried powder is transferred from the first drying chamber into the second drying chamber. A dried powder, including a recirculated amount of powder and a discharge amount of powder, is formed in the second drying chamber. The recirculated amount of the dried powder is transferred by a conveyor device from the second drying chamber into the first drying chamber. The discharge amount of the dried powder is discharged from the second drying chamber.