Neomesophase formation

Claim 2

In a process of preparing an optically anisotropic deformable pitch by treating a carbonaceous isotropic pitch with an organic solvent system having a solubility parameter between 8.0 and 9.5, said solvent being in an amount sufficient to provide a solvent insoluble fraction which is capable of being converted into an optically anisotropic pitch having greater than 75% of a liquid crystalline phase in less than 10 minutes when heated at about 30° C. above the point where the material becomes liquid, the improvement comprising heating the isotropic carbonaceous pitch before treatment with said organic solvent system at temperatures in the range of about 350° C. to 450° C. for a time sufficient to increase the solvent insoluble fraction of the pitch and thereafter terminating said heating.

Claim 3

The process of claim 1 wherein said heating is terminated just prior to the point in time when spherules would be visible upon polarized light microscopic examination of samples of the pitch.

Claim 4

The improvement of claim 2 wherein said heating is conducted at a temperature in the range of about 350° C. to 480° C.

Claim 5

The improvement of claim 3 wherein said heating is conducted at pressures of 1 psi to 20 psi and at temperatures of from about 380° C. to 450° C.

Claim 6

The process of claim 4 wherein said heating is continued for from about 1 hour to about 20 hours.

Claim 7

A process for preparing carbonaceous pitch containing greater than 75% of an optically anisotropic oriented phase having less than about 25 wt. % quinoline insolubles comprising heating a carbonaceous isotropic pitch containing less than 5 wt. % quinoline insolubles at a temperature in the range of from about 350° C. to about 480° C. until polarized light microscopic examination of samples of said pitch indicates the formation of spherules therein; thereafter terminating said heating and extracting said carbonaceous isotropic pitch with an organic solvent system selected from organic solvents and mixtures thereof, said organic solvent system having a solubility parameters of between about 8.0 to about 9.5, the ratio of said organic solvent system to said isotropic carbonaceous pitch being sufficient to provide a solvent insoluble fraction which is capable of being thermally converted to a pitch containing greater than 75% of an optically anisotropic phase in a time less than 10 minutes when said pitch is heated at about 30° C. above the point where the material becomes liquid; separating said solvent insoluble fraction from said solvent system; drying said separated solvent insoluble fraction; and thereafter heating said dried solvent insoluble fraction at a temperature in the range of from about 230° C. to about 400° C., whereby said solvent insoluble fraction is converted to a pitch containing greater than 75% of an optically anisotropic oriented phase and less than about 25 wt. % quinoline insolubles.

Claim 8

A process for preparing carbonaceous pitch containing greater than 75% of an optically anisotropic oriented phase having less than about 25 wt. % quinoline insolubles comprising heating a carbonaceous isotropic pitch containing less than 5 wt. % quinoline insolubles at a temperature in the range of from about 350° C. to about 480° C. until polarized light microscopic examination of samples of said pitch indicates the formation of spherules therein; thereafter terminating said heating and extracting said carbonaceous isotropic pitch with an organic solvent system selected from organic solvents and mixtures thereof, said organic solvent system having a solubility parameters of between about 8.0 to about 9.5, the ratio of said organic solvent system to said isotropic carbonaceous pitch being sufficient to provide a solvent insoluble fraction which is capable of being thermally converted to a pitch containing greater than 75% of an optically anisotropic phase in a time less than 10 minutes when said pitch is heated at about 30° C. above the point where the material becomes liquid; separating said solvent insoluble fraction from said solvent system; drying said separated solvent insoluble fraction; and thereafter heating said dried solvent insoluble fraction at a temperature in the range of from about 230° C. to about 400° C., whereby said solvent insoluble fraction is converted to a pitch containing greater than 75% of an optically anisotropic oriented phase and less than about 25 wt. % quinoline insolubles.

Claim 9

The process of claim 6 wherein said heated pitch is first allowed to cool to ambient temperatures before extracting said solvent system.

Claim 10

An improved process for converting an isotropic carbonaceous pitch to an optically anisotropic deformable carbonaceous pitch comprising: (a) selecting a graphitizable carbonaceous pitch containing less than 0.3 wt. % of substances which are insoluble in boiling quinoline; (b) determining for said pitch the point in time at which spherules visible under polarized light begin to appear in said pitch when heated isothermally at a selected temperature in the range of about 350° C. to 480° C. by heating each of a plurality of samples of said pitch isothermally at said selected temperature but for different time periods and then examining said samples under polarized light at a magnification factor of from about 10 to about 1000; (c) thereafter heating said isotropic pitch at a temperature in the range of from about 350° C. to about 480° C. for a time sufficient to increase that fraction of the pitch which is insoluble in an organic solvent system having a solubility parameter between 8.0 and 9.5 and less than the time in which visible spherules begin to appear as determined in step (b); (d) extracting said heated pitch with an organic solvent system having a solubility parameter at 25° C. of between 8.0 and 9.5 in an amount sufficient to provide a solvent insoluble fraction of said pitch which when heated to a temperature in the range of from about 230° C. to about 400° C. is converted to a pitch containing greater than 75% of an optically anisotropic phase and 25 wt. % or less of which pitch is insoluble in boiling quinoline.

Claim 11

An improved process for converting an isotropic carbonaceous pitch to an optically anisotropic deformable carbonaceous pitch comprising: (a) selecting a graphitizable carbonaceous pitch containing less than 0.3 wt. % of substances which are insoluble in boiling quinoline; (b) determining for said pitch the point in time at which spherules visible under polarized light begin to appear in said pitch when heated isothermally at a selected temperature in the range of about 350° C. to 480° C. by heating each of a plurality of samples of said pitch isothermally at said selected temperature but for different time periods and then examining said samples under polarized light at a magnification factor of from about 10 to about 1000; (c) thereafter heating said isotropic pitch at a temperature in the range of from about 350° C. to about 480° C. for a time sufficient to increase that fraction of the pitch which is insoluble in an organic solvent system having a solubility parameter between 8.0 and 9.5 and less than the time in which visible spherules begin to appear as determined in step (b); (d) extracting said heated pitch with an organic solvent system having a solubility parameter at 25° C. of between 8.0 and 9.5 in an amount sufficient to provide a solvent insoluble fraction of said pitch which when heated to a temperature in the range of from about 230° C. to about 400° C. is converted to a pitch containing greater than 75% of an optically anisotropic phase and 25 wt. % or less of which pitch is insoluble in boiling quinoline.

Claim 12

The process of claim 1 wherein said heating is terminated at a point in time when spherules are visible in the pitch under polarized light.