The present disclosure relates to a plastic pyrolysis/emulsification system for pyrolyzing waste plastic in a high-temperature/high-vacuum environment, the plastic pyrolysis/emulsification system being characterized by comprising: an introduction portion having a hopper for introducing plastic; a heating furnace having a burner mounted thereon so as to establish a high-temperature environment therein and having a combustion gas outlet; a melting furnace penetrating the heating furnace such that one end of the melting furnace is connected to the introduction portion, and both ends thereof are exposed to the outside, a transferring/compressing means being mounted in the melting furnace along the longitudinal direction so as to transfer and compress the plastic in one direction, thereby transferring, compressing, and melting the plastic, and the melting furnace having a vapor outlet for discharging water vapor resulting from compression and melting of the plastic; a first transfer portion connected to the other end of the melting furnace so as to transfer the melt of the plastic; a vacuum pyrolysis furnace penetrating the heating furnace such that one end of the vacuum pyrolysis furnace is connected to the first transfer portion, and both ends thereof are exposed to the outside, a transfer means being mounted in the vacuum pyrolysis furnace along the longitudinal direction so as to transfer the melt in one direction, thereby transferring and pyrolyzing the melt, and the vacuum pyrolysis furnace having an oil vapor outlet for discharging oil vapor resulting from transfer and pyrolysis of the melt; a second transfer portion connected to the other end of the vacuum pyrolysis furnace so as to transfer the pyrolysis remnant of the melt; a discharge portion connected to the second transfer portion so as to discharge the pyrolysis remnant; a first condenser connected to the vapor outlet so as to condense the water vapor; a second condenser connected to the other end of the vacuum pyrolysis furnace so as to transfer the pyrolysis remnant of the melt; a discharge portion connected to the second transfer portion so as to discharge the pyrolysis remnant; a first condenser connected to the vapor outlet so as to condense is the water vapor; a second condenser connected to the oil vapor outlet so as to condense the oil vapor; multiple third condensers connected to the second condenser via first, second, and third valves, respectively; a vacuum pump connected to the multiple third condensers via fourth, fifth, and sixth valves, respectively; and a fourth condenser connected to the vacuum pump.

A method of manufacturing a part, includes: obtaining recycled fibers; mixing the recycled fibers with a thermoplastic to obtain a fiber-reinforced intermediate; and manufacturing the part with the fiber-reinforced intermediate. The recycled fibers may come from a grinding operation of recycled composite parts. A feedstock may be manufactured using recycled fibers. The feedstock may then be used in subsequent manufacturing.

Provided herein is a method of recycling additively manufactured articles or recovered coating material that comprises a crosslinked polymer formed from a single-cure resin comprising a reactive blocked prepolymer, into a regenerated resin useful for additive manufacturing. Recyclable light-polymerizable resins, methods of making recyclable objects from such resins, and methods for sustainable manufacturing are also provided.

Provided herein is a method of recycling additively manufactured articles or recovered coating material that comprises a crosslinked polymer formed from a single-cure resin comprising a reactive blocked prepolymer, into a regenerated resin useful for additive manufacturing. Recyclable light-polymerizable resins, methods of making recyclable objects from such resins, and methods for sustainable manufacturing are also provided.

A method of recovering filler material from a polymer material comprises (a) heating the polymer material to a first temperature; (b) heating the polymer material to a second temperature higher than the first temperature resulting in a pyrolyzed material; (c) elutriating the pyrolyzed material to obtain a separated mixture; and (d) filtering the separated mixture to obtain the filler material.

System and methods for recycling a material comprising a polymer in an expanded state is disclosed. The system can include a shredder, a heating chamber operatively connected to the shredder, a condenser operatively connected to the heating chamber, a solvent tank operatively connected to the condenser, and a circulation unit operatively connected to the solvent tank and the heating chamber.

High surface area 3D mesoporous carbon nanocomposites can be derived from Zn dust and PET bottle mixed waste with a high surface area. Simultaneous transformation of Zn metal into ZnO nanoparticles and PET bottle waste to porous carbon materials can be achieved by thermal treatment at preferably 600 to 800° C., and reaction times of from 15 to 60 minutes, after optionally de-aerating the reaction mixtures with N.sub.2 gas. The waste-based carbon materials can have surface areas of 650 to 725 m.sup.2/g, e.g., 684.5 m.sup.2/g and pore size distributions of 12 to 18 nm. The carbon materials may have 3D porous dense layers with a gradient pore structure, which may have enhanced photocatalytic performance for degrading, e.g., organic dyes, such as methylene blue and malachite green. Sustainable methods make ZnO-mesoporous carbon materials from waste for applications including photocatalysis, upcycling mixed waste materials.

High surface area 3D mesoporous carbon nanocomposites can be derived from Zn dust and PET bottle mixed waste with a high surface area. Simultaneous transformation of Zn metal into ZnO nanoparticles and PET bottle waste to porous carbon materials can be achieved by thermal treatment at preferably 600 to 800° C., and reaction times of from 15 to 60 minutes, after optionally de-aerating the reaction mixtures with N.sub.2 gas. The waste-based carbon materials can have surface areas of 650 to 725 m.sup.2/g, e.g., 684.5 m.sup.2/g and pore size distributions of 12 to 18 nm. The carbon materials may have 3D porous dense layers with a gradient pore structure, which may have enhanced photocatalytic performance for degrading, e.g., organic dyes, such as methylene blue and malachite green. Sustainable methods make ZnO-mesoporous carbon materials from waste for applications including photocatalysis, upcycling mixed waste materials.

A method of upcycling fiber reinforced polymer source material by disassembling the source material into sections; planking the sections into longitudinal pieces; separating core material from the source material in the longitudinal pieces to make composite strips; preparing the composite strips; and remanufacturing the prepared composite strips into an article.

A method of upcycling fiber reinforced polymer source material by disassembling the source material into sections; planking the sections into longitudinal pieces; separating core material from the source material in the longitudinal pieces to make composite strips; preparing the composite strips; and remanufacturing the prepared composite strips into an article.