The present disclosure provides an apparatus for thermal treatment of a pre-defined amount of organic waste. The apparatus includes a plurality of chambers to receive the pre-defined amount of organic waste. Further, the apparatus includes a double wall to encapsulate each of the plurality of chambers. Furthermore, the apparatus includes an auger accommodated within the cylindrical hollow body of each of the plurality of chambers. Moreover, each of the plurality of chambers has a cylindrical hollow body. The cylindrical body has a first diameter of a first section and a second diameter of a second section. In addition, each of the plurality of chambers is connected in succession for a continuous movement of the pre-defined amount of organic waste along a longitudinal axis. Further, the plurality of chambers includes a feed material inlet and a processed material outlet attached at a second end of the plurality of chambers.

The present invention relates to an improved food waste dryer utilizing waste heat, which includes a main frame, a dryer drum with an access door, to be positioned in the main frame, and an agitator positioned in the dryer drum. The improved food waste dryer comprises: a waste heat supply unit, a heating jacket positioned on the outer surface of the dryer drum, with a hot-air inlet to receive the waste heat from the waste heat supply unit and a hot-air outlet to discharge the waste heat inside the dryer drum, and a condensation system positioned in the main frame, to remove moisture included in the interior air of the dryer drum to increase the drying efficiency of the food waste dryer utilizing waste heat.

To provide a drying method for processing material and a horizontal rotary dryer allowing easy performance of mass processing of the processing material and enabling size reduction by improving drying performance of the dryer. In a drying method for processing material in which a horizontal rotary dryer provided with: a rotating shell having a feed port for processing material on one end side thereof and a discharge port for processing material on the other end side thereof, and capable of freely rotating around an axial center; and a group of heating tubes through which a heating medium passes, provided within the rotating shell, and configured in a manner that the processing material is lifted up in a rotational direction by the group of heating tubes in accordance with the rotation of the rotating shell, is used, and the processing material is dried, through indirect heating, by using the group of heating tubes in a process of feeding the processing material to the one end side of the rotating shell and discharging the processing material from the other end side of the rotating shell, the rotating shell is rotated to make a critical speed ratio defined by the following expression 1 and expression 2 become 30 to less than 100% to dry the processing material,
Vc=2.21D1/2Expression 1
=V/Vc.Math.100Expression 2 wherein Vc indicates a critical speed (m/s), D indicates an inside diameter (m) of the rotating shell, indicates the critical speed ratio (%), and V indicates a rotation speed (m/s).

A method and system for drying food products is disclosed. The system includes an infrared source, an ultrasonic generator, and a hydro conductive dryer. Food products are placed on a moving conveyor belt that cycles through the system and exposes the food products to infrared and ultrasonic vibration while also transferring thermal energy from heated water to the food products.

A method and system for drying food products is disclosed. The system includes an infrared source, an ultrasonic generator, and a hydro conductive dryer. Food products are placed on a moving conveyor belt that cycles through the system and exposes the food products to infrared and ultrasonic vibration while also transferring thermal energy from heated water to the food products.

A coat drying device dries a coated film that is coated on a continuously transported coating object having first and second parts, where the second part has a greater heat capacity than the first part. The coat drying device includes a drying furnace, a hot air supply device and a control unit. The coating object is conveyed inside of the drying furnace main body. The hot air supply device heats the coating object by blowing hot air to the drying furnace. The control unit controls the hot air supply device based on a heat capacity of the coating object. The control unit controls the hot air supply device such that, when heating the second part, hot air with a greater amount of heat is supplied to the second part than an amount of heat in the hot air that is supplied to heat the first part.

Serially connected heat exchange segments of a heat exchanger are stacked with ends of adjacent segments oriented oppositely. The segments have fixed pipes for heat exchange, pipe-riding shaftless auger flights for conveying feed material, and flanges for low-cost adjustment, removal and replacement of pipes and flights. Flights when arranged in arrays are arranged in pairs of counterrotating oppositely handed mutually cleaning flights. Rotary unions are unnecessary in this exchanger.

A multi-functional slurry processing system (VARCOR) and associated methods is disclosed. The present examples provide a multi-functional slurry processing system incorporating systems and methods for separating liquid and solid components in slurries. In particular the systems and methods described herein produce clean water, dried solids, and potential concentration of desirable constituents with a boiling point lower than water. At least one example of the multi-functional slurry processing system provides a self-contained processing facility configured to efficiently convert high water-content slurries into its constituent solid and liquid fractions and subsequently generating and collecting clean water and concentrating desirable constituents with a boiling point lower than water. The multi-functional slurry processing system advantageously applies thermodynamic principles in a system which may include various combinations of a preheater, a degassing unit, a dryer, a steam filter, a compressor, a concentrating tower, and a condensation unit.

The present disclosure provides an apparatus for thermal treatment of a pre-defined amount of organic waste. The apparatus includes a plurality of chambers to receive the pre-defined amount of organic waste. Further, the apparatus includes a double wall to encapsulate each of the plurality of chambers. Furthermore, the apparatus includes an auger accommodated within the cylindrical hollow body of each of the plurality of chambers. Moreover, each of the plurality of chambers has a cylindrical hollow body. The cylindrical body has a first diameter of a first section and a second diameter of a second section. In addition, each of the plurality of chambers is connected in succession for a continuous movement of the pre-defined amount of organic waste along a longitudinal axis. Further, the plurality of chambers includes a feed material inlet and a processed material outlet attached at a second end of the plurality of chambers.

To provide a drying method for processing material and a horizontal rotary dryer allowing easy performance of mass processing of the processing material and enabling size reduction by improving drying performance of the dryer. In a drying method for processing material in which a horizontal rotary dryer provided with: a rotating shell having a feed port for processing material on one end side thereof and a discharge port for processing material on the other end side thereof, and capable of freely rotating around an axial center; and a group of heating tubes through which a heating medium passes, provided within the rotating shell, and configured in a manner that the processing material is lifted up in a rotational direction by the group of heating tubes in accordance with the rotation of the rotating shell, is used, and the processing material is dried, through indirect heating, by using the group of heating tubes in a process of feeding the processing material to the one end side of the rotating shell and discharging the processing material from the other end side of the rotating shell, the rotating shell is rotated to make a critical speed ratio defined by the following expression 1 and expression 2 become 30 to less than 100% to dry the processing material,

Vc=2.21D1/2Expression 1

=V/Vc.Math.100Expression 2

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