Systems and methods for recycling waste plastics are provided, including a system for recovering styrene monomer from waste polystyrene. The system includes a mixing, heating and compacting apparatus to receive a supply of waste polystyrene and to output a densified polystyrene containing melt; a pyrolysis reactor configured to receive the densified polystyrene containing melt and a supply of recycled oligomers, pyrolyze the densified polystyrene containing melt and the recycled oligomers, and output a hydrocarbon gas stream and a solids residue stream; a quenching apparatus configured to receive the hydrocarbon gas stream output from the pyrolysis reactor and condense out oligomers for routing upstream to the pyrolysis reactor to be combined as the supply of recycled oligomers with the densified polystyrene containing melt, and to discharge an altered hydrocarbon gas stream for further processing; and a condenser configured to receive the altered hydrocarbon gas stream from the quenching apparatus and condense out styrene to form a styrene monomer oil product.

Systems and methods for recycling waste plastics are provided, including a system for recovering styrene monomer from waste polystyrene. The system includes a mixing, heating and compacting apparatus to receive a supply of waste polystyrene and to output a densified polystyrene containing melt; a pyrolysis reactor configured to receive the densified polystyrene containing melt and a supply of recycled oligomers, pyrolyze the densified polystyrene containing melt and the recycled oligomers, and output a hydrocarbon gas stream and a solids residue stream; a quenching apparatus configured to receive the hydrocarbon gas stream output from the pyrolysis reactor and condense out oligomers for routing upstream to the pyrolysis reactor to be combined as the supply of recycled oligomers with the densified polystyrene containing melt, and to discharge an altered hydrocarbon gas stream for further processing; and a condenser configured to receive the altered hydrocarbon gas stream from the quenching apparatus and condense out styrene to form a styrene monomer oil product.

Systems and methods for recycling waste plastics are provided, including a system for recovering styrene monomer from waste polystyrene. The system includes a mixing, heating and compacting apparatus to receive a supply of waste polystyrene and to output a densified polystyrene containing melt; a pyrolysis reactor configured to receive the densified polystyrene containing melt and a supply of recycled oligomers, pyrolyze the densified polystyrene containing melt and the recycled oligomers, and output a hydrocarbon gas stream and a solids residue stream; a quenching apparatus configured to receive the hydrocarbon gas stream output from the pyrolysis reactor and condense out oligomers for routing upstream to the pyrolysis reactor to be combined as the supply of recycled oligomers with the densified polystyrene containing melt, and to discharge an altered hydrocarbon gas stream for further processing; and a condenser configured to receive the altered hydrocarbon gas stream from the quenching apparatus and condense out styrene to form a styrene monomer oil product.

Systems and methods for recycling waste plastics are provided, including a system for recovering styrene monomer from waste polystyrene. The system includes a mixing, heating and compacting apparatus to receive a supply of waste polystyrene and to output a densified polystyrene containing melt; a pyrolysis reactor configured to receive the densified polystyrene containing melt and a supply of recycled oligomers, pyrolyze the densified polystyrene containing melt and the recycled oligomers, and output a hydrocarbon gas stream and a solids residue stream; a quenching apparatus configured to receive the hydrocarbon gas stream output from the pyrolysis reactor and condense out oligomers for routing upstream to the pyrolysis reactor to be combined as the supply of recycled oligomers with the densified polystyrene containing melt, and to discharge an altered hydrocarbon gas stream for further processing; and a condenser configured to receive the altered hydrocarbon gas stream from the quenching apparatus and condense out styrene to form a styrene monomer oil product.

Systems, methods and apparatus for the thermal conversion of carbonaceous feedstock material into biochar. The carbonaceous feedstock material may be harvested, preprocessed and pyrolyzed. An amount of carbonaceous feedstock material is received. An amount of a catalyst is applied to the carbonaceous feedstock material. The carbonaceous feedstock material and the applied catalyst is heated in an anaerobic environment to a temperature of at least 300 C. The biochar material is then generated.

Systems, methods and apparatus for the thermal conversion of carbonaceous feedstock material into biochar. The carbonaceous feedstock material may be harvested, preprocessed and pyrolyzed. An amount of carbonaceous feedstock material is received. An amount of a catalyst is applied to the carbonaceous feedstock material. The carbonaceous feedstock material and the applied catalyst is heated in an anaerobic environment to a temperature of at least 300 C. The biochar material is then generated.

A successive thermal pyrolysis apparatus for waste rubber has a pyrolysis furnace unit and a steam heating unit. The pyrolysis furnace unit is a tube chain type pyrolysis furnace and substantially has conveyor tubes and a chain disc conveyor mounted through the conveyor tubes for conveying waste rubber along the conveyor tubes. The steam heating unit encloses a segment of the conveyor tubes and has multiple baffles mounted therein to form a tortuous flowing path for steam passing through to heat the pyrolysis furnace unit. The successive thermal pyrolysis apparatus can prevent the carbonized fragments from sticking to and blocking inner surfaces of the conveyor tubes. The waste rubber fragments are successively thermally decomposed while being conveyed through the conveyor tubes.

A successive thermal pyrolysis apparatus for waste rubber has a pyrolysis furnace unit and a steam heating unit. The pyrolysis furnace unit is a tube chain type pyrolysis furnace and substantially has conveyor tubes and a chain disc conveyor mounted through the conveyor tubes for conveying waste rubber along the conveyor tubes. The steam heating unit encloses a segment of the conveyor tubes and has multiple baffles mounted therein to form a tortuous flowing path for steam passing through to heat the pyrolysis furnace unit. The successive thermal pyrolysis apparatus can prevent the carbonized fragments from sticking to and blocking inner surfaces of the conveyor tubes. The waste rubber fragments are successively thermally decomposed while being conveyed through the conveyor tubes.

Electric-powered, closed-loop, continuous-feed, endothermic energy-conversion systems and methods are disclosed. In one embodiment, the presently disclosed energy-conversion system includes a shaftless auger. In another embodiment, the presently disclosed energy-conversion system includes a drag conveyor. In yet another embodiment, the presently disclosed energy-conversion system includes a distillation and/or fractionating stage. The endothermic energy-conversion systems and methods feature mechanisms for natural resource recovery, refining, and recycling, such as secondary recovery of metals, minerals, nutrients, and/or carbon char.

Coke oven door sealing unit for sealing a coke oven door against a sealing surface of a coke oven door frame of a coke oven chamber, the coke oven door sealing unit including: a coke oven door for fitting into the coke oven door frame of the coke oven chamber; a fixture device for holding a sealing piece opposite to the coke oven door frame in a peripheral area of the coke oven door; the sealing piece, where the sealing piece is configured to be operated in a first operating state or a second operating state; a seal protection element for isolating the sealing piece from the coke oven chamber; where, in a first operating state, the sealing piece is spaced at a first distance from a sealing surface arranged opposite of the sealing piece; and where, in a second operating state, the sealing piece contacts the sealing surface; such that in the second operating state, the sealing piece and the seal protection element at least partially form a cavity.