A method of processing particulate carbon comprises combining pyrolysis carbon with water to form a mixture to form an initial slurry having 1-35 wt % solids and milling the pyrolysis carbon to form a milled slurry comprising wet milled reclaimed carbon and water; wherein a volume weighted particle size distribution of the wet milled reclaimed carbon measured via scanning electron microscopy has one or more of D50 no greater than 2700 nm and no more than 15% of particles having a particle diameter greater than 5 microns.

A method of processing particulate carbon comprises combining pyrolysis carbon with water to form a mixture to form an initial slurry having 1-35 wt % solids and milling the pyrolysis carbon to form a milled slurry comprising wet milled reclaimed carbon and water; wherein a volume weighted particle size distribution of the wet milled reclaimed carbon measured via scanning electron microscopy has one or more of D50 no greater than 2700 nm and no more than 15% of particles having a particle diameter greater than 5 microns.

A granulation method may include feeding a graded powder into a granulator. The powder may have a particle size distribution (PSD) of at least 98% 115 mesh and at most 50% 200 mesh. The powder may have a PSD of at least 98% less than or equal to 4.2% of a median product particle size and at most 50% less than or equal to 2.5% of the median product particle size. The powder may have a PSD of between 40% and 80% between 3% and 6% of the median product particle size, between 5% and 30% between 2% and 4% of the median product particle size, and between 10% and 40% between 1% and 3% of the median product particle size. A liquid binder may be fed into the granulator. Wet granules may be discharged from the granulator and may have a moisture content of between 7% and 12%.

A granulation method may include feeding a graded powder into a granulator. The powder may have a particle size distribution (PSD) of at least 98% 115 mesh and at most 50% 200 mesh. The powder may have a PSD of at least 98% less than or equal to 4.2% of a median product particle size and at most 50% less than or equal to 2.5% of the median product particle size. The powder may have a PSD of between 40% and 80% between 3% and 6% of the median product particle size, between 5% and 30% between 2% and 4% of the median product particle size, and between 10% and 40% between 1% and 3% of the median product particle size. A liquid binder may be fed into the granulator. Wet granules may be discharged from the granulator and may have a moisture content of between 7% and 12%.

A method for preparing a preblend of nano-structured carbon, such as nanotubes, fullerenes, or graphene, and a particulate solid, such as carbon black, graphitic particles or glassy carbon involving wet-mixing and followed by optional drying to remove the liquid medium. The preblend may be in the form of a core-shell powder material with the nano-structured carbon as the shell on the particulate solid core. The preblend may provide particularly improved dispersion of single-wall nanotubes in ethylene--olefin elastomer compositions, resulting in improved reinforcement from the nanotubes. The improved elastomer compositions may show simultaneous improvement in both modulus and in elongation at break. The elastomer compositions may be formed into useful rubber articles.

The present invention relates to a pelleted acetylene black having a mass strength measured according to ASTM D 1937-10 of 200 N at most and an average pellet size measured according to ASTM D 1511-10 of at least 1.0 mm, to the use of any of said pelleted acetylene blacks to produce a compound comprising a resin or polymer or rubber matrix and the acetylene black dispersed in said matrix and to a method for producing such a compound.

The present invention relates to a process for the production of oxidized wet beaded carbon black. It has been found that carbon black can be wet beaded and oxidized subsequently. This process allows a better control of the degree of oxidation without damaging the beads. Moreover, the oxidized wet beaded carbon black can be beneficially used in a rubber composition to increase the properties of the resulting rubber product.

The present invention relates to a process for the production of oxidized wet beaded carbon black. It has been found that carbon black can be wet beaded and oxidized subsequently. This process allows a better control of the degree of oxidation without damaging the beads. Moreover, the oxidized wet beaded carbon black can be beneficially used in a rubber composition to increase the properties of the resulting rubber product.

A carbon material granulated product contains a carbon black having a particle size D.sub.50, as determined by a laser diffraction/scattering method specified in ISO 13320, of 250 m or less, a carbon nanotube having a particle size D.sub.50, as determined by the laser diffraction/scattering method specified in ISO 13320, of 50 m or less, and a solvent-soluble polymer impregnated into the carbon black and the carbon nanotube. In the carbon material granulated product, the solvent-soluble polymer is at least one selected from the group consisting of ether polymers, vinyl polymers, amine polymers, cellulose polymers, and starch polymers, and the content of the solvent-soluble polymer is in a range from 1 part by mass to 15 parts by mass relative to a total content of the carbon black and the carbon nanotube taken as 100 parts by mass.

A carbon material granulated product contains a carbon black having a particle size D.sub.50, as determined by a laser diffraction/scattering method specified in ISO 13320, of 250 m or less, a carbon nanotube having a particle size D.sub.50, as determined by the laser diffraction/scattering method specified in ISO 13320, of 50 m or less, and a solvent-soluble polymer impregnated into the carbon black and the carbon nanotube. In the carbon material granulated product, the solvent-soluble polymer is at least one selected from the group consisting of ether polymers, vinyl polymers, amine polymers, cellulose polymers, and starch polymers, and the content of the solvent-soluble polymer is in a range from 1 part by mass to 15 parts by mass relative to a total content of the carbon black and the carbon nanotube taken as 100 parts by mass.