Abstract Pitch having a Kramer-Sarnow softening point between 70° and 190° C is heated to a temperature in the range of 40° to 100° C above the softening point thereof. There is thus obtained a molten mass having non-molten particles distributed therein. A filtering operation under a pressure greater than atmospheric pressure is carried out to remove the particles from the molten mass. The molten mass may then be treated in different ways. According to one embodiment, the molten mass is held at a temperature between 280° and 350° C to distill off low molecular weight components of the pitch and the resulting product is thereafter shaped by extrusion to the form of strands. According to another embodiment, the molten mass is cooled, ground to particulate form and contacted with an aliphatic solvent having a boiling point between 60° and 70° C. This solvent dissolves a portion of the ground mass and, after separation of the solvent from the residue, the latter is heated to a molten state and thereafter extruded into the form of strands. In either embodiment, the previously mentioned filtering operation provides for a greater homogeneity of the strands since the non-molten particles, which could form a second phase, are substantially completely eliminated. In both embodiments, the strands obtained are dusted with finely divided activated carbon which has been impregnated with a liquid oxidizing agent. The dusted strands are oxidized in an oxidizing atmosphere at temperatures between 300° and 400° C. The oxidation increases the melt-resistance of the strands. The oxidized strands are next carbonized, the increased melt-resistance thereof preventing melting of the strands during the carbonizing treatment. If desired, the strands may also be graphitized. The method described enables carbon-containing or graphite-containing strands suitable for many applications to be produced in a much shorter time than was possible heretofore.
A method for producing carbonaceous articles in the form of fibers or strands comprising a. heating pitch having a Kramer-Sarnow softening point between about 70° and 190° C to a temperature about 40° to 100° C above its softening point so that part of the pitch is molten; b. filtering the thus-obtained molten mass so as to remove substantially all solid particles and to increase the homogeneity of the molten mass; c. then cooling the remaining mass and grinding it to small particles followed by contacting the particles with an aliphatic solvent adapted to dissolve a portion of the said particles; d. removing at least the major part of the solvent; e. passing the remaining aliphatic solvent-insoluble portion of the mass under application of heat and pressure through a forming head so as to shape it to fibers, strands or threads; f. sprinkling the fibers or strands with finely ground activated carbon which has been impregnated with a liquid oxidizing agent; g. then heating the thus-treated fiber strands or fibers to about 350° C to improve their melt-resistance, and h. finally carbonizing the strands or fibers at a temperature of about 1000° C.
Claim 2
Independent Claim
193 words
A method for producing carbonaceous articles in the form of fibers or strands comprising a. heating pitch having a Kramer-Sarnow softening point between about 70° and 190° C to a temperature about 40° to 100° C above its softening point so that part of the pitch is molten; b. filtering the thus-obtained molten mass so as to remove substantially all solid particles and to increase the homogeneity of the molten mass; c. then cooling the remaining mass and grinding it to small particles followed by contacting the particles with an aliphatic solvent adapted to dissolve a portion of the said particles; d. removing at least the major part of the solvent; e. passing the remaining aliphatic solvent-insoluble portion of the mass under application of heat and pressure through a forming head so as to shape it to fibers, strands or threads; f. sprinkling the fibers or strands with finely ground activated carbon which has been impregnated with a liquid oxidizing agent; g. then heating the thus-treated fiber strands or fibers to about 350° C to improve their melt-resistance, and h. finally carbonizing the strands or fibers at a temperature of about 1000° C.
Claim 3
Dependent Claim
34 words
The process of claim 1 wherein the size of the particles to which the cooled mass is ground in step [c] is below about 0.2 mm for about 90 to 100% of the particles.
Claim 4
Dependent Claim
21 words
The process of claim 1 wherein the aliphatic solvent in step [c] has a melting point between 60° and 70° C.
Claim 5
Dependent Claim
27 words
The process of claim 1 wherein the filtration in step [b] is effected at about the temperature to which the pitch has been heated in step [a].
Claim 6
Dependent Claim
17 words
The process of claim 1 wherein the filtration is effected in the presence of a filter aid.
Claim 7
Dependent Claim
26 words
The process of claim 1 wherein the filtration in step [b] is effected by forcing the molten pitch through the filter by means of pressurized nitrogen.
Claim 8
Dependent Claim
31 words
The process of claim 1 wherein the fiber or strands which have been sprinkled with the ground activated carbon are heated in an oxidizing atmosphere at about 300° to 400° C.
Claim 9
Dependent Claim
15 words
The process of claim 1 wherein the impregnating agent in step [f] is sulfuric acid.