The present invention provides an apparatus for rapid pyrolysis reaction, which comprises: a reactor, which comprises a reactor body defining a reaction space that forms a dispersion region, a pyrolysis region, and a discharge region from top to bottom; multilayer-regenerative radiant tubes, which are distributed at an interval in the height direction of the reactor body in the pyrolysis region, and each layer of regenerative radiant tubes consists of a plurality of regenerative radiant tubes distributed at an interval in the horizontal direction, a material distributor; a material inlet arranged in the dispersion region above the material distributor; a material distribution gas inlet, which is arranged in the dispersion region and communicates with the material distributor so as to utilize a material distribution gas to blow out the material in the material distributor into the dispersion region, so that the material falls into the pyrolysis region uniformly; a plurality of pyrolysis gas outlets, which are arranged in the dispersion region and/or the pyrolysis region respectively; and a semi-coke outlet arranged in the discharge region.

The present invention provides an apparatus for rapid pyrolysis reaction, which comprises: a reactor, which comprises a reactor body defining a reaction space that forms a dispersion region, a pyrolysis region, and a discharge region from top to bottom; multilayer-regenerative radiant tubes, which are distributed at an interval in the height direction of the reactor body in the pyrolysis region, and each layer of regenerative radiant tubes consists of a plurality of regenerative radiant tubes distributed at an interval in the horizontal direction, a material distributor; a material inlet arranged in the dispersion region above the material distributor; a material distribution gas inlet, which is arranged in the dispersion region and communicates with the material distributor so as to utilize a material distribution gas to blow out the material in the material distributor into the dispersion region, so that the material falls into the pyrolysis region uniformly; a plurality of pyrolysis gas outlets, which are arranged in the dispersion region and/or the pyrolysis region respectively; and a semi-coke outlet arranged in the discharge region.

Plant for pyrolytic processing material includes a reactor, a feeding bin for solid material, a feeding auger mechanism, a feeding tank for liquid material, a feeding pump, a smoke suction, a chimney, an intermediate auger mechanism, a collecting bin for ash residue, a discharging auger mechanism, filter for a gas/vapour mixture, a heat exchanger, a cooler, a circulation pump for coolant, a knockout drum, a gas drier tower, a hydraulic trap, an accumulating tank, a residual water separator, a water tank, a fuel tank, a nitrogen source, and an air blower for the combustion chamber, tubes and pipes, fittings, valves, expansion and balance tanks, and an automated control system. The reactor is configured for thermal destruction of organic material and includes a cylinder-shaped pyrolysis chamber with a main auger mechanism that feeds the material into the pyrolysis chamber, moves the material along the pyrolysis chamber, and unloads ash residue.

Plant for pyrolytic processing material includes a reactor, a feeding bin for solid material, a feeding auger mechanism, a feeding tank for liquid material, a feeding pump, a smoke suction, a chimney, an intermediate auger mechanism, a collecting bin for ash residue, a discharging auger mechanism, filter for a gas/vapour mixture, a heat exchanger, a cooler, a circulation pump for coolant, a knockout drum, a gas drier tower, a hydraulic trap, an accumulating tank, a residual water separator, a water tank, a fuel tank, a nitrogen source, and an air blower for the combustion chamber, tubes and pipes, fittings, valves, expansion and balance tanks, and an automated control system. The reactor is configured for thermal destruction of organic material and includes a cylinder-shaped pyrolysis chamber with a main auger mechanism that feeds the material into the pyrolysis chamber, moves the material along the pyrolysis chamber, and unloads ash residue.

The present invention relates to a system and method for converting biomass and the products obtained therefrom. The system comprises a conversion unit (1) provided with an inlet (5) for introducing biomass, an inlet (6) for introducing a gas stream, an outlet (8) for removing carbonized material (9), and an outlet (10) for releasing a fluid (F3), the system further comprising a first separation unit (11), a second separation unit (15), a condensing unit (18).

The present invention relates to a system and method for converting biomass and the products obtained therefrom. The system comprises a conversion unit (1) provided with an inlet (5) for introducing biomass, an inlet (6) for introducing a gas stream, an outlet (8) for removing carbonized material (9), and an outlet (10) for releasing a fluid (F3), the system further comprising a first separation unit (11), a second separation unit (15), a condensing unit (18).

The present invention provides a system for thermal remediation and/or the processing of a feed materials like contaminated materials, waste polymeric materials, waste paper products, waste wood and biomass. The system comprises at least one thermal screw conveyor provided in a housing under pressure, a first plug screw conveyor in a housing in communication with an inlet of thermal screw conveyor housing and a second plug screw conveyor in a housing in communication with an outlet of thermal screw conveyor housing. The thermal housing is configured to heat the feed material to form one or more vaporized products and a solid residue, wherein one or more vaporized products are removed through the one or more vapor ports provided in the pressure housing, and the solid residue is discharged from an outlet of the second seal-housing.

The present invention provides a system for thermal remediation and/or the processing of a feed materials like contaminated materials, waste polymeric materials, waste paper products, waste wood and biomass. The system comprises at least one thermal screw conveyor provided in a housing under pressure, a first plug screw conveyor in a housing in communication with an inlet of thermal screw conveyor housing and a second plug screw conveyor in a housing in communication with an outlet of thermal screw conveyor housing. The thermal housing is configured to heat the feed material to form one or more vaporized products and a solid residue, wherein one or more vaporized products are removed through the one or more vapor ports provided in the pressure housing, and the solid residue is discharged from an outlet of the second seal-housing.

In a method for producing pyrolysis oil, pyrolysis gas and pyrolysis coke, a starting material substantially comprising biomass is supplied to the upper region of a pyrolysis reactor. The latter has a substantially vertically arranged reactor chamber, which is substantially tubular. The reaction chamber then contains a bed of bulk material that comprises the starting material to be pyrolyzed and, optionally, the pyrolysis coke. This bulk material is thermally treated in the pyrolysis reactor, where the pyrolysis coke, the pyrolysis gases and the pyrolysis vapors are formed from the starting material to be pyrolyzed, and where the bulk material, the pyrolysis gases and the pyrolysis vapors are guided through the reaction chamber from top to bottom. The movement of the bulk material is caused substantially by gravity and the movement of the pyrolysis gases and pyrolysis vapors by the gas pressure building up.

In a method for producing pyrolysis oil, pyrolysis gas and pyrolysis coke, a starting material substantially comprising biomass is supplied to the upper region of a pyrolysis reactor. The latter has a substantially vertically arranged reactor chamber, which is substantially tubular. The reaction chamber then contains a bed of bulk material that comprises the starting material to be pyrolyzed and, optionally, the pyrolysis coke. This bulk material is thermally treated in the pyrolysis reactor, where the pyrolysis coke, the pyrolysis gases and the pyrolysis vapors are formed from the starting material to be pyrolyzed, and where the bulk material, the pyrolysis gases and the pyrolysis vapors are guided through the reaction chamber from top to bottom. The movement of the bulk material is caused substantially by gravity and the movement of the pyrolysis gases and pyrolysis vapors by the gas pressure building up.