Production of pitch and coke from raw petroleum coke

Claim 2

A process for the production of a pitch useful as a binder for carbon particulate matter and as an impregnant for porous carbon solids and of a coke useful for Hall cell anodes for the electrolytic production of aluminum, comprising extraction of raw petroleum coke with from 1 to 2 parts of a solvent to 1 part of coke by wt., said solvent selected from the group consisting of tetrahydrofuran, tetralin, coker gas oil having a distillation end point of approximately 320° and mixtures thereof, said extraction carried out at or near the atmospheric boiling points of said solvent, physical separation of the solid coke from the solution thus obtained, and distillation to recover said pitch from said solution, said pitch having less than 1% quinoline insoluble, not more than 10.5% benzene insoluble, and less than 9.6% beta-resin by wt.

Claim 3

The process of claim 1 wherein the extraction process is carried out for a period of approximately 1 to 2 hours.

Claim 4

The process of claim 1 wherein the raw petroleum coke used has a volatile matter content of at least 10% by weight.

Claim 5

A process for the production of a calcined coke useful for the formation of an anode for a Hall aluminum cell comprising extracting raw petroleum coke with from 1 to 2 parts of an organic solvent to 1 part of coke by wt., at a temperature near the atmospheric boiling point of said solvent selected from the group consisting of tetrahydrofuran, petroleum thermal tar distillate with 250° C. distillation end point, tetralin, gas oil coker with 320° C. distillation end point, or mixtures thereof, separating the resulting mixture to obtain solids and a solution of soluble matter in said solvent, heating the solids at an elevated temperature to recover entrapped solvent, and calcining the solids at an elevated temperature of 1150° to 1500° C. to recover said coke.

Claim 6

A process for the production of a calcined coke useful for the formation of an anode for a Hall aluminum cell comprising extracting raw petroleum coke with from 1 to 2 parts of an organic solvent to 1 part of coke by wt., at a temperature near the atmospheric boiling point of said solvent selected from the group consisting of tetrahydrofuran, petroleum thermal tar distillate with 250° C. distillation end point, tetralin, gas oil coker with 320° C. distillation end point, or mixtures thereof, separating the resulting mixture to obtain solids and a solution of soluble matter in said solvent, heating the solids at an elevated temperature to recover entrapped solvent, and calcining the solids at an elevated temperature of 1150° to 1500° C. to recover said coke.

Claim 7

A process for the production of a petroleum pitch useful as a binder for particulate matter and as an impregnant for porous carbon solids comprising the extraction of raw petroleum coke with from 1 to 2 parts by wt. solvent to one part by wt. of coke, said solvent selected from the group consisting of tetrahydrofuran, tetralin, and coker gas oil having a distillation end point of approximately 320° C., or mixtures thereof, said extraction carried out by contacting said coke with said solvent at or near the atmospheric boiling point of said solvent for a period of from 1 to 2 hours, separation of the liquid solution thus obtained from the remaining coke solids by mechanical means, and separation of said pitch from said solvent by distillation to recover said pitch, having less than 1% quinoline insoluble, less than 10.5% benzene insoluble, and less than 9.6% beta-resin by wt.

Claim 8

A process for the production of a petroleum pitch useful as a binder for particulate matter and as an impregnant for porous carbon solids comprising the extraction of raw petroleum coke with from 1 to 2 parts by wt. solvent to one part by wt. of coke, said solvent selected from the group consisting of tetrahydrofuran, tetralin, and coker gas oil having a distillation end point of approximately 320° C., or mixtures thereof, said extraction carried out by contacting said coke with said solvent at or near the atmospheric boiling point of said solvent for a period of from 1 to 2 hours, separation of the liquid solution thus obtained from the remaining coke solids by mechanical means, and separation of said pitch from said solvent by distillation to recover said pitch, having less than 1% quinoline insoluble, less than 10.5% benzene insoluble, and less than 9.6% beta-resin by wt.