Plastic conversion vessels such as pyrolytic reactors convert plastic waste materials such as polymers, or hydrocarboneous material, or both, via in situ chemical reactions comprising cracking, recombination, reforming, recracking, and the like, to usable chemical compounds such as naphtha, diesel fuel, heavy oil, wax, and the like. Inherent within the polymers and/or carbonaceous material are generally solid, inert residues such as various fillers, pigments, flame retardants, silica, aluminum, talc, glass, clay, and so forth. Such solid inert residues (SIR) must be treated to remove residual volatile organic material therefrom in order to meet acceptable environmental standards and/or limits. A heated dryer for treating the SIR comprises heating units to remove excessive volatile organic material therefrom as when moved along a conveyor that transfers said material to a collection area. The collection area comprises one or more pistons that are capable of compacting and discharging said SIR material. Another collection area embodiment comprises a plurality of plungers that transfer the SIR material from said collection area to a plunger collection area, and subsequently to a collection container.

A treatment system for solid bulk materials such as limestone or mineral ore is provided having a belt conveyor configured for receiving the solid bulk material upon a transportation surface thereof and for displacing the material from a charging region to a discharging region according to a rectilinear path and a heating chamber, configured to receive a solar radiation conveyed by an external field of heliostats. A length portion of the transportation surface passes within or below the heating chamber so that thermal energy associated with the solar radiation is transferred to the bulk material by direct impingement or by reflection or re-irradiation by internal surfaces or walls of the heating chamber.

A treatment system for solid bulk materials such as limestone or mineral ore is provided having a belt conveyor configured for receiving the solid bulk material upon a transportation surface thereof and for displacing the material from a charging region to a discharging region according to a rectilinear path and a heating chamber, configured to receive a solar radiation conveyed by an external field of heliostats. A length portion of the transportation surface passes within or below the heating chamber so that thermal energy associated with the solar radiation is transferred to the bulk material by direct impingement or by reflection or re-irradiation by internal surfaces or walls of the heating chamber.

A material drying system, method, and control system therefor that provides for consistent and efficient drying of various materials is disclosed. In certain embodiments, a vacuum kiln can use various temperature measurements to reduce the chance of overheating the materials. In certain embodiments, a vacuum kiln (or a control system therefore) can use sensed information, such as the temperature differential across a platen assembly or the duty cycle of a vacuum pump, to determine when a large group of material has reached a substantially uniform dryness level. In certain embodiments, a vacuum kiln as disclosed herein can reduce checking, splitting, over-drying, and under-drying of material without requiring parameters from a user.

A material drying system, method, and control system therefor that provides for consistent and efficient drying of various materials is disclosed. In certain embodiments, a vacuum kiln can use various temperature measurements to reduce the chance of overheating the materials. In certain embodiments, a vacuum kiln (or a control system therefore) can use sensed information, such as the temperature differential across a platen assembly or the duty cycle of a vacuum pump, to determine when a large group of material has reached a substantially uniform dryness level. In certain embodiments, a vacuum kiln as disclosed herein can reduce checking, splitting, over-drying, and under-drying of material without requiring parameters from a user.

A material drying and cooling integrated machine, comprising a heating module, a drying module, a dust removal filter module, a temperature-lowering and dehumidifying module, and a cooling module. Dry hot air generated in the heating module can enter the drying module to dry materials; the temperature-lowering and dehumidifying module can conduct temperature lowering and dehumidification on air entering the interior thereof so as to form dry cold air, and the dry cold air can enter the cooling module to cool materials in the cooling module; the dry hot air enters the drying module to dry the materials in the drying module, then damp hot air is formed, and part of the damp hot air can be heated by the heating module again; the other part of the damp hot air can sequentially pass through the dust removal filter module and the temperature-lowering and dehumidifying module, and dry cold air can be formed.

A material drying and cooling integrated machine, comprising a heating module, a drying module, a dust removal filter module, a temperature-lowering and dehumidifying module, and a cooling module. Dry hot air generated in the heating module can enter the drying module to dry materials; the temperature-lowering and dehumidifying module can conduct temperature lowering and dehumidification on air entering the interior thereof so as to form dry cold air, and the dry cold air can enter the cooling module to cool materials in the cooling module; the dry hot air enters the drying module to dry the materials in the drying module, then damp hot air is formed, and part of the damp hot air can be heated by the heating module again; the other part of the damp hot air can sequentially pass through the dust removal filter module and the temperature-lowering and dehumidifying module, and dry cold air can be formed.

A back-blowing unblocking device for the dustproof screen of the dryer, a dustproof equipment, and a dryer are provided. The back-blowing unblocking device for the dustproof screen of the dryer utilizes a closed compartment space of the dryer. The back-blowing unblocking device for the dustproof screen of the dryer includes a high-pressure air main pipe, a high-pressure air horizontal pipe, high-pressure air branch pipes, a shunt connecting pipe, and back-blowing fan-shaped nozzles. A length of each high-pressure air branch pipe is equal to a length of an A-shaped dustproof screen. Both ends of the each high-pressure air branch pipe are closed and an upper center opening is welded to the shunt connecting pipe. Both sides of the each high-pressure air branch pipe are densely arranged with the back-blowing fan-shaped nozzles.

A back-blowing unblocking device for the dustproof screen of the dryer, a dustproof equipment, and a dryer are provided. The back-blowing unblocking device for the dustproof screen of the dryer utilizes a closed compartment space of the dryer. The back-blowing unblocking device for the dustproof screen of the dryer includes a high-pressure air main pipe, a high-pressure air horizontal pipe, high-pressure air branch pipes, a shunt connecting pipe, and back-blowing fan-shaped nozzles. A length of each high-pressure air branch pipe is equal to a length of an A-shaped dustproof screen. Both ends of the each high-pressure air branch pipe are closed and an upper center opening is welded to the shunt connecting pipe. Both sides of the each high-pressure air branch pipe are densely arranged with the back-blowing fan-shaped nozzles.

The present invention provides improved apparatus and methods for the monitoring and control of apparatus designed to remove moisture from an initially wet product, such as a continuous dryer (14). The net rate of water removal from the wet product (16) is determined during drying thereof, preferably on a real-time basis. A control assembly (20) is operatively coupled with the dryer (14) and includes sensors (24, 26, 28, 34), which are operatively coupled with a digital controller (38). The controller (38) has a PID controller operable to continuously determine the average net rate of water removal from the product (16).