The present disclosure relates to a carbon-based nanomaterial composition that may be formed from a gas mixture. The gas mixture may include acetylene gas at a molar ratio AG.sub.mol/GM.sub.mol of at least about 0.25 and not greater than about 0.99, oxygen gas at a molar ratio OG.sub.mol/GM.sub.mol of at least about 0.01 and not greater than about 0.50, hydrogen gas at a molar ratio HG.sub.mol/GM.sub.mol of at least about 0.05 and not greater than about 0.70, and methane gas at a molar ratio MG.sub.mol/GM.sub.mol of at least about 0.25 and not greater than about 0.99. The carbon-based nanomaterial composition may have a carbon hybridization ratio P.sub.sp3/P.sub.sp2 of at least about 0.0 and not greater than about 5.0, where P.sub.sp3 is the percent of carbon within the carbon-based nanomaterial composition having a sp3 hybridization and P.sub.sp2 is the percent of carbon within the carbon-based nanomaterial composition having a sp2 hybridization.

Combustion apparatuses (e.g., burners) and methods, such as those configured to encourage mixing of fluid, flame stability, and synthesis of materials (e.g., nano-particles), among other things.

Combustion apparatuses (e.g., burners) and methods, such as those configured to encourage mixing of fluid, flame stability, and synthesis of materials (e.g., nano-particles), among other things.

The disclosed is a method for producing a carbon material dispersion which removes efficiently and reliably metallic components from carbon materials, and that provides a carbon material dispersion of a high product quality and stable electrical properties. The method comprises a first magnetic separation step in which the powdered and/or granulated carbon material C is applied to the surface of a rotating magnetic roll 130 to remove the metallic component M from the carbon material in the dry state of the powdered and granulated carbon material C; and a second magnetic separation step in which a magnet element 310 is placed in a carbon material dispersion D, in which the carbon material from which the metallic component has been removed in the first magnetic separation step is dispersed in a dispersing medium, in advance of the second magnetic separation step.

Systems and methods are provided for converting plastic waste into carbon pigment. Received polymer material such as plastic waste is degraded at 350-600° C. to form carbon-rich liquid and non-condensable syngas, and the carbon-rich liquid is then pyrolyzed at 1100-2200° C. to form carbon nanoparticles that may be used as carbon pigment. The syngas and possibly some of the form carbon-rich liquid may be used to provide heat to the system.

Systems and methods are provided for converting plastic waste into carbon pigment. Received polymer material such as plastic waste is degraded at 350-600° C. to form carbon-rich liquid and non-condensable syngas, and the carbon-rich liquid is then pyrolyzed at 1100-2200° C. to form carbon nanoparticles that may be used as carbon pigment. The syngas and possibly some of the form carbon-rich liquid may be used to provide heat to the system.

An electrode catalyst support, capable of improving the power of a fuel cell, and an electrode catalyst and a solid polymer fuel cell using the same. Provided is carbon black wherein pores which are at most 6 nm in pore diameter have a cumulative pore volume of less than 0.25 cm.sup.3/g, a specific surface area by BET is 500 to 900 m.sup.2/g, and a volatile matter content is 1.0 to 10.0%. Also provided are an electrode catalyst for a fuel cell comprising a support which includes this carbon black, and a solid polymer fuel cell having the electrode catalyst.

An electrode catalyst support, capable of improving the power of a fuel cell, and an electrode catalyst and a solid polymer fuel cell using the same. Provided is carbon black wherein pores which are at most 6 nm in pore diameter have a cumulative pore volume of less than 0.25 cm.sup.3/g, a specific surface area by BET is 500 to 900 m.sup.2/g, and a volatile matter content is 1.0 to 10.0%. Also provided are an electrode catalyst for a fuel cell comprising a support which includes this carbon black, and a solid polymer fuel cell having the electrode catalyst.

Secondary heat may be added to a particle production process. The particles may be, for example, carbon particles. Among other things, the secondary heat addition may result in change in surface area of the carbon particle(s), change in structure of the carbon particle(s), reduced wall fouling, reduced energy consumption and/or increased throughput. Apparatus for performing the process is also described.

Secondary heat may be added to a particle production process. The particles may be, for example, carbon particles. Among other things, the secondary heat addition may result in change in surface area of the carbon particle(s), change in structure of the carbon particle(s), reduced wall fouling, reduced energy consumption and/or increased throughput. Apparatus for performing the process is also described.