A production method includes a surface-crosslinking step of heating a mixture of a surface-crosslinking agent and a particulate dried polymer obtained with an acid group-containing unsaturated monomer as a main component. A moisture content of the particulate dried polymer is not greater than 15% by mass. A heating device including a rotary container and a plurality of heating tubes that are located within the rotary container, extend in an axial direction of the rotary container, and rotate together with the rotary container, is used in the surface-crosslinking step. The heating device includes a means for introducing and discharging a gas into and from the rotary container.

The present invention relates to method(s), apparatus and use(s) of apparatus for treating materials such as waste products and by-products of industrial processes e.g. slurries comprising solids and liquids, or, more particularly, slurries comprising solids, oil(s), and water. The invention further relates to method(s), apparatus and use(s) for treating slurry, the apparatus comprising a treatment chamber having a first end configured to receive slurry to be treated and a second end configured to allow egress of solids; at least one heated material conveyor configured to draw material comprising slurry and/or solids through the chamber in a direction from the first end towards the second end; the at least one heated material conveyor being further configured to heat and mix material comprising slurry and/or solids as these are drawn along; a condenser configured to receive vapours from the chamber and condense the vapours into liquid form.

The present invention relates to a new device, a system and a method for both cooking and drying or removing the water phase from material. The device of the present invention has a large area for heat exchange and scrapers which stir the material in the container rather than transferring it around in circles.

The present invention relates to a new device, a system and a method for both cooking and drying or removing the water phase from material. The device of the present invention has a large area for heat exchange and scrapers which stir the material in the container rather than transferring it around in circles.

The inventive concept relates to a sludge drying apparatus, and more particularly to a sludge drying apparatus that may improve an efficiency of drying sludge that is sewage deposit residues and simplify a drying process.

The inventive concept relates to a sludge drying apparatus, and more particularly to a sludge drying apparatus that may improve an efficiency of drying sludge that is sewage deposit residues and simplify a drying process.

The invention relates to a drying device for drying a product comprising: a housing having a drying chamber, a product inlet at a first end and an product outlet at a second end; a drying rotor arranged rotatable within the drying chamber and having at least one helical groove at the outer surface thereof; a screw having a flight with a flight channel there between and arranged rotatable within the drying chamber and substantially parallel to the drying rotor; a driving mechanism configured for driving the screw in rotation around a screw axis; and a heater for providing thermal energy to the drying chamber, wherein the drying rotor and/or the screw at least are configured for moving the product from the first end to the second end, and such that the flight of the screw engages into the at least one helical groove of the drying rotor.

To provide a drying method for terephthalic acid and a horizontal rotary dryer allowing easy performance of mass processing of the terephthalic acid and enabling size reduction by improving drying performance of the dryer. In a method of drying terephthalic acid by using a horizontal rotary dryer, a rotating shell is rotated to make a critical speed ratio defined by expression 1 and expression 2 become 17 to less than 80% to dry the processing material,

Vc=2.21D1/2 Expression 1

=V/V c.Math.100 Expression 2 wherein Vc indicates a critical speed (m/s) of the rotating shell, D indicates an inside diameter (m) of the rotating shell, indicates the critical speed ratio (%) of the rotating shell, and V indicates a rotation speed (m/s) of the rotating shell.

The present disclosure relates to a drying apparatus for a powder raw material for manufacturing a secondary cell with an electric heater. In an embodiment of the present disclosure, a plurality of independently controlled heaters are mounted on a main body of an apparatus in which a plurality of heating regions are defined, and the temperature deviation of the internal chamber can reduce by providing the amount of heat supplied to each heating region through the control of the plurality of heaters. The main body of the apparatus includes a cylindrical portion in which the powder raw material is accommodated and sidewalls on both sides of the cylindrical portion, and by installing heaters on the cylindrical portion and the sidewalls, respectively, the entire region defining the main body of the apparatus can be evenly heated.

The present disclosure relates to a drying apparatus for a powder raw material for manufacturing a secondary cell with an electric heater. In an embodiment of the present disclosure, a plurality of independently controlled heaters are mounted on a main body of an apparatus in which a plurality of heating regions are defined, and the temperature deviation of the internal chamber can reduce by providing the amount of heat supplied to each heating region through the control of the plurality of heaters. The main body of the apparatus includes a cylindrical portion in which the powder raw material is accommodated and sidewalls on both sides of the cylindrical portion, and by installing heaters on the cylindrical portion and the sidewalls, respectively, the entire region defining the main body of the apparatus can be evenly heated.