Production of carbonaceous powders and their granulation

Claim 2

In a process for granulating a carbonaceous pulverulent body by spray-drying a slurry in heated air which can contain superheated steam, which slurry has a carbonaceous pulverulent body comprising a self-sintering carbonaceous pulverulent body dispersed in water in the presence of at least a binding agent and a wetting agent, the improvement which comprises: (1) employing, as said binding agent, a water-soluble organic compound which does not produce a foamed structure when carbonized at 1000° C. under an inert atmosphere and which provides a residual carbon yield of 10% by weight or more when carbonized at 1000° C. under an inert atmosphere, and the amount of said agent ranging in proportion from 0.01 to 5 parts by weight to 100 parts by weight of the carbonaceous pulverulent body; and (2) employing, as said wetting agent, a non-ionic surfactant having a clouding point of at least 25° C., and the amount of said agent ranging in proportion from 0.01 to 3 parts by weight to 100 parts by weight of the carbonaceous pulverulent body, thereby producing a granulated carbonaceous pulverulent body in the form of spherical particles which, upon contact with water, form a slurry which can be spray-dried.

Claim 3

The process for granulating a carbonaceous pulverulent body according to claim 1, wherein said self-sintering carbonaceous pulverulent body is at least a pitch pulverulent body selected from the group consisting of a coal-tar pitch, a petroleum pitch, a naphtha-degraded tar pitch, a mesophase-containing or heat-treated pitch and other various modified pitches and/or at least a complex pulverulent body selected from the group consisting of graphite-rich carbons, carbon-rich carbons, metals and inorganic compounds of which surface has been substantially coated with at least one of the pitches selected from said pitch group, and will give a calcined product by subjecting its room temperature press molding product to an ordinary pressure carbonization treatment at a temperature up to 500° C. in an inert atmosphere.

Claim 4

The process of claim 1, wherein said carbonaceous pulverulent body comprises a self-sintering carbonaceous pulverulent body in combination with at least one pulverulent body selected from the group consisting of mesophase-containing pitch, heat-treated pitch, graphite-rich carbons, carbon-rich carbons, metals and inorganic compounds.

Claim 5

The process for producing a self-sintering carbonaceous pulverulent body referred to in claim 2, wherein the surface of at least one element selected from the group consisting of a graphite-rich carbon, a carbon-rich carbon, a metal and an inorganic compound is coated with at least one pitch selected from a mesophase-containing pitch and a heat-treated pitch, which process comprises: (1) preparing a slurry by suspending at least one element selected from the group consisting of a graphite-rich carbon, a carbon-rich carbon, an inorganic compound, a metal and a metal compound in a tar fraction which contains a mesophase containing pitch or thermally treated pitch precursor; (2) separating a mixture comprising the element and a polynuclear aromatic polymer which contains the mesophase-containing or heat-treated precursor by adding to the slurry at least one solvent selected from the group consisting of (i) an aliphatic or alicyclic hydrocarbon having 5-20 carbon atoms and (ii) an aliphatic or alicyclic ketone compound having 3-5 carbon atoms in a mixing solvent ratio (S M ) of 2-15 (solvent weight/raw material tar weight), treating the mixture at a temperature of 0° to 60° C. to deposit a polynuclear aromatic polymer which contains the mesophase-containing or heat-treated pitch precursor on the surface of the element, separating the solvent-soluble fraction in the tar fractions together with the solvent from a solid component, subjecting the resulting cake and/or slurry to at least one washing treatment with a solvent selected from the groups consisting of (i) and (ii) referred to above in a rinsing solvent ration (S R ) of 1-15 (solvent weight/weight of raw material tar fraction) at a temperature of 0° to 60° C., and separating the solvent and the solvent soluble fraction from the obtained mixture; and (3) heat treating the mixture under an inert gas atmosphere at a temperature of 300° to 520° C. to convert the polynuclear aromatic polymer deposited on the element to a mesophase-containing or heat-treated pitch.

Claim 6

The process for granulating a carbonaceous pulverulent body according to claim 1, wherein the binding agent is selected from the group consisting of methyl cellulose and hydroxy cellulose and the wetting agent is a member selected from the group consisting of alkylphenol-ethylene oxide adducts, alkylphenolethylene oxide/propylene oxide adducts, oxyethylenepropylene block copolymers of a mean molecular weight of 2,000-8,000, alcohol ethoxylates, polyhydric alcohol esters and polyethylene glycol esters.