To treat organic sludge while keeping facility costs, cement production efficiency, and a reduction in clinker production amount to a minimum. An organic sludge treatment device includes: a fractionation device 7 that fractionates a preheated raw material R2 from a preheater cyclone 4C excluding a bottommost cyclone of a cement burning device 1; a mixing device 8 that mixes an organic sludge S with the fractionated preheated raw material, and that dries the organic sludge using sensible heat of the preheated raw material; and a supply device (mixture chute 12, double-flap damper 13, shut damper 14) that supplies a mixture M from the mixing device to a calciner furnace 5 of the cement burning device or to a duct disposed between a kiln inlet portion of a cement kiln 2 and the calciner furnace. The treatment device may be provided with an introduction device for introducing an exhaust gas G2 including dust, odor and water vapor from the mixing device to a gas outlet of a bottommost cyclone 4A of the cement burning device.

Provided are a vacuum freeze-drying apparatus and a method capable of continuously performing vacuum freeze-drying in a short time. A vacuum freeze-drying apparatus 1 of this invention having an exhaust path for performing vacuum suction, while a drying device 3 comprises a tubular member 31 provided an inlet portion and an outlet portion formed of a tubular shape, a temperature adjusting means 30a to 30j provided in a plurality of regions formed from the inlet portion toward the outlet portion in a peripheral portion of the tubular member 31 wherein the plurality of regions are at least three or more regions whose temperature is capable of being controlled, for adjusting temperatures of a plurality of regions 40a to 40j in outer surface of the tubular member, a temperature control unit 8 for independently controlling the temperature adjusting means, and a rotating portion 7 for rotating the tubular member 31, wherein the tubular member 31 has a spiral transfer means 31a continuously provided adjacent to an inner wall of the tubular member from the inlet portion toward the outlet portion, and the transfer means 31a transfers the frozen substance sequentially to locations corresponding to the plurality of regions in the tubular member so as to continuously sublimate and dry.

Provided are a vacuum freeze-drying apparatus and a method capable of continuously performing vacuum freeze-drying in a short time. A vacuum freeze-drying apparatus 1 of this invention having an exhaust path for performing vacuum suction, while a drying device 3 comprises a tubular member 31 provided an inlet portion and an outlet portion formed of a tubular shape, a temperature adjusting means 30a to 30j provided in a plurality of regions formed from the inlet portion toward the outlet portion in a peripheral portion of the tubular member 31 wherein the plurality of regions are at least three or more regions whose temperature is capable of being controlled, for adjusting temperatures of a plurality of regions 40a to 40j in outer surface of the tubular member, a temperature control unit 8 for independently controlling the temperature adjusting means, and a rotating portion 7 for rotating the tubular member 31, wherein the tubular member 31 has a spiral transfer means 31a continuously provided adjacent to an inner wall of the tubular member from the inlet portion toward the outlet portion, and the transfer means 31a transfers the frozen substance sequentially to locations corresponding to the plurality of regions in the tubular member so as to continuously sublimate and dry.

Systems and methods of processing biomass include a conveyor unit associated with an inlet and/or outlet, a microwave generator, a microwave guide connecting the microwave generator to the conveyor unit that includes a microwave opening configured to receive microwave energy via the microwave guide, and a microwave suppression system including a tunnel associated with the material inlet and/or outlet, and including at least one flexible and/or movable microwave reflecting component within the tunnel, the microwave reflecting component configured to be deflected as biomass material passes through the tunnel and then returning to a resting, closed position when the biomass material is no longer passing through the tunnel. The conveyor unit is configured to receive and process the biomass material, including heating the biomass material to at least a first temperature by applying microwave energy to the biomass material.

The present disclosure relates to a rotating-screw drying reactor for filtering and drying a fluid-containing material, and to a method for continuously filtering and drying a fluid-containing material by means of the rotating-screw drying reactor.

The present disclosure relates to a rotating-screw drying reactor for filtering and drying a fluid-containing material, and to a method for continuously filtering and drying a fluid-containing material by means of the rotating-screw drying reactor.

Disclosed herein is a sludge drying system comprising: a system input for receiving a wet sludge stream, wherein the wet sludge stream comprises water and solid material; a first dryer arranged to receive, at an input of the first dryer, the wet sludge stream and to heat the wet sludge stream such that at least part of the water in the wet sludge stream is evaporated to thereby generate evaporate and a partially dry sludge stream, wherein the first dryer is an indirectly heated rotating disc dryer that comprises a first output for outputting evaporate and a second output for outputting the partially dry sludge stream; a second dryer that is an indirectly heated rotating disc dryer and is arranged to receive, at a first input of the second dryer, a stream that is dependent on the partially dry sludge stream output from the first dryer and to receive, at a second input of the second dryer, the evaporate from the first dryer, wherein the second dryer is arranged to use to the received evaporate to indirectly heat the received stream at the first input to thereby generate and output a substantially dry sludge stream; and a system output for outputting at least part of the substantially dry sludge stream from the system.

Disclosed herein is a sludge drying system comprising: a system input for receiving a wet sludge stream, wherein the wet sludge stream comprises water and solid material; a first dryer arranged to receive, at an input of the first dryer, the wet sludge stream and to heat the wet sludge stream such that at least part of the water in the wet sludge stream is evaporated to thereby generate evaporate and a partially dry sludge stream, wherein the first dryer is an indirectly heated rotating disc dryer that comprises a first output for outputting evaporate and a second output for outputting the partially dry sludge stream; a second dryer that is an indirectly heated rotating disc dryer and is arranged to receive, at a first input of the second dryer, a stream that is dependent on the partially dry sludge stream output from the first dryer and to receive, at a second input of the second dryer, the evaporate from the first dryer, wherein the second dryer is arranged to use to the received evaporate to indirectly heat the received stream at the first input to thereby generate and output a substantially dry sludge stream; and a system output for outputting at least part of the substantially dry sludge stream from the system.

Provided are a vacuum freeze-drying apparatus and a method capable of continuously performing vacuum freeze-drying in a short time. A vacuum freeze-drying apparatus 1 of this invention having an exhaust path for performing vacuum suction, while a drying device 3 comprises a tubular member 31 provided an inlet portion and an outlet portion formed of a tubular shape, a temperature adjusting means 30a to 30j provided in a plurality of regions formed from the inlet portion toward the outlet portion in a peripheral portion of the tubular member 31 wherein the plurality of regions are at least three or more regions whose temperature is capable of being controlled, for adjusting temperatures of a plurality of regions 40a to 40j in outer surface of the tubular member, a temperature control unit 8 for independently controlling the temperature adjusting means, and a rotating portion 7 for rotating the tubular member 31, wherein the tubular member 31 has a spiral transfer means 31a continuously provided adjacent to an inner wall of the tubular member from the inlet portion toward the outlet portion, and the transfer means 31a transfers the frozen substance sequentially to locations corresponding to the plurality of regions in the tubular member so as to continuously sublimate and dry.

Provided are a vacuum freeze-drying apparatus and a method capable of continuously performing vacuum freeze-drying in a short time. A vacuum freeze-drying apparatus 1 of this invention having an exhaust path for performing vacuum suction, while a drying device 3 comprises a tubular member 31 provided an inlet portion and an outlet portion formed of a tubular shape, a temperature adjusting means 30a to 30j provided in a plurality of regions formed from the inlet portion toward the outlet portion in a peripheral portion of the tubular member 31 wherein the plurality of regions are at least three or more regions whose temperature is capable of being controlled, for adjusting temperatures of a plurality of regions 40a to 40j in outer surface of the tubular member, a temperature control unit 8 for independently controlling the temperature adjusting means, and a rotating portion 7 for rotating the tubular member 31, wherein the tubular member 31 has a spiral transfer means 31a continuously provided adjacent to an inner wall of the tubular member from the inlet portion toward the outlet portion, and the transfer means 31a transfers the frozen substance sequentially to locations corresponding to the plurality of regions in the tubular member so as to continuously sublimate and dry.