The production method includes: a gel-crushing step of grinding a crosslinked hydrogel polymer to obtain a particulate crosslinked hydrogel polymer; a heating drying step of obtaining dried particles from the particulate crosslinked hydrogel polymer by using a continuous stirring drying machine; a post-crosslinking step of post-crosslinking the particulate crosslinked hydrogel polymer or the dried particles; and a sizing step of adjusting a particle size of the dried particles or the post-crosslinked dried particles to obtain water-absorbent resin powder. The particulate crosslinked hydrogel polymer contains a gel fluidizer. A gel temperature of the particulate crosslinked hydrogel polymer containing the gel fluidizer, the gel temperature being measured by a contact thermometer, is not lower than 50 C. In the production method, the dried particles or the post-crosslinked dried particles is forcedly cooled before the sizing step.

The production method includes a drying step of drying a particulate crosslinked hydrogel polymer obtained by polymerizing a monomer, which is a material of a water-absorbent resin, using a heating device to obtain dried particles. The heating device includes: a rotary container that contains the particulate crosslinked hydrogel polymer therein and rotates; 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. A gel temperature of the particulate crosslinked hydrogel polymer to be subjected to the drying step, the gel temperature being measured by a contact thermometer, is not lower than 50 C.

There is provided an apparatus for use in drying a sample of geological material having a substantial moisture content. In one aspect, the apparatus comprises a means for providing a flow of heated fluid, and a means for managing the thermal state of the flow of heated fluid. The means for managing the thermal state of the flow of heated fluid is arranged operable with the means for providing a flow of heated fluid so that exposure of the sample to the flow of heated fluid facilitates a reduction of the moisture content of a portion of the sample while substantially preserving one or more chemical and/or physical properties of the portion.

Provided are systems and methods for drying a cereal grass, such as alfalfa, barley, clover, rye grass, Timothy grass, and the stalks, stems, grains and leaves of a cereal grass, such as oats, wheat, buckwheat, maize, millet, rice and sorghum. The systems include a first pressing roll and a second pressing roll that form a nip through which the cereal grass or forage crop can be pressed, pressing the liquid out of the cereal grass or forage crop to form a first product stream comprising a dewatered cereal grass or forage crop and a second product stream comprising liquid pressed out of the cereal grass or forage crop; at least one suction device for collecting the second product stream; an atomizer for converting the second product stream into droplets that can be applied to the surface of the first product stream; a drying chamber; and a circulation system for moving a drying medium through the drying chamber.

An apparatus (10) for producing reshaped plastic granules from a plurality of initial granules (12) with a predetermined shape is disclosed comprising: a feeding unit (20) for continuously receiving a plurality of said initial granules (12), a pressing unit (30) for mechanically reshaping the initial granules, said pressing unit comprising at least two opposite pressing surfaces (32) with a gap (34) therebetween, the width (W) of said gap ranging from 0 mm to 0.5 mm, a receiving chamber (40) for receiving the reshaped final granules (13) from the pressing unit, and a frame (50) for supporting the feeding unit, the pressing unit and the receiving chamber. A method is also provided to produce final granules by mechanically reshaping the initial granule, each final granule having a certain surface-to-volume ratio and a primary thickness of at most 0.7 mm within substantially the entire volume of the final granules.

A method, a system and devices are for processing of at least one substance into a dried, fragmented and fluidized end product. The at least one substance is delivered in fragmented state from a fragmenting device to a fluidizing, drying and filtering unit. The at least one fragmented substance is subjected to fluidizing action from at least one set of rotary shovels while blowing a drying agent (DA), e.g. hot gas, hot air, vapor or superheated steam into a space of the unit. The drying agent, having passed through fluidized, fragmented substance(s), is sucked and filtered to let it exit a space at an upper end or lateral region thereof. Further, the fragmented, fluidized and dried substance(s) are caused to leave the space at a lower region thereof as the product. Humid drying agent exiting the space is at least partly de-hydrated and/or heated before re-entering the space.

Disclosed is a food waste treating apparatus including: a housing including a food inlet opening on its upper surface; and a rotating shaft assembly provided within the housing and configured to mix food waste within the housing. The rotating shaft assembly includes: a rotating shaft; a plurality of supporting bars evenly spaced and extended from the rotating shaft in a perpendicular direction to the rotating shaft; a plurality of agitating blades provided at ends of the plurality of supporting bars respectively; a motor configured to supply power to rotate the rotating shaft; and a torque transferring structure connected to both ends of the rotating shaft and configured to transfer torque from the motor.

A system for drying a wet lactose product stream includes a disperser configured to disperse agglomerated lactose particulates in a wet lactose stream into a dispersed wet lactose stream. A back-mixed partial drying zone is configured to at least partially dry the dispersed wet lactose stream by recirculating a partially dried lactose stream with the dispersed wet lactose stream. A plug-flow secondary drying zone is configured to dry the partially dried lactose stream to generate a substantially dried lactose stream.

The system for drying lignite according to the present disclosure includes a mill configured to crush the lignite; a dryer configured to receive crushed lignite from the mill, to dry the lignite by heat-exchange with steam and to discharge dried lignite; a condensing-precipitating evaporator in fluid communication with the dryer so as to receive vapor which is evaporated when the lignite is dried, and which is discharged from the dryer. The evaporator is configured to condense the vapor discharged from the dryer by heat-exchange with water. The coal dust contained in the vapor is precipitated into a condensed aqueous solution when the vapor is being condensed, and the condensed aqueous solution is discharged. The system includes a Mechanical Vapor Re-Compression (MVR) configured to receive steam generated from the condensing-precipitating evaporator, to compress the steam into superheated steam, and to supply the compressed superheated steam to the dryer.

A feeding device is provided for a belt drying installation for dump or sewage sludge material dewatered down to a pasty consistency. In the conveying path of the sludge material, a first roller having transverse grooves that are set back relative to the outer diameter of the roller and a guide device are arranged relative to the outer diameter of the first roller such that when the roller is rotated the sludge material is drawn into the transverse grooves and is shaped to elongated extrudates. The first roller is associated with a comb which has teeth that rigidly engage the transverse grooves and which sweeps the extrudates from the transverse grooves, wherein the tips of the teeth which rigidly engage the transverse grooves define a line of engagement. The tooth tips which rigidly engage the transverse grooves are beveled towards the tooth neck.