Electrolytic recovery from bituminous materials

Claim 2

A process for treating bituminous material for recovery of chemicals therefrom, comprising: slurrying said material with an aqueous alkaline electrolytic solution; defining an electrolytic cell having a cathode chamber electrolytically operative with an anode chamber, an anode in said anode chamber in contact with said slurry and a cathode in said cathode chamber; and applying a direct current potential across said anode and cathode chambers at a current density of above about about 15 A/m 2 for a time sufficient to effect substantial oxidative electrolysis of said material whereby to obtain a water-soluble product, and a residue, therefrom; and separating said water-soluble product from said residue.

Claim 3

The process of claim 1 in which the electrolyte in said slurry is an hydroxide of a metal.

Claim 4

The process of claim 1 in which said slurry has an electrolyte concentration of greater than 1.0 N.

Claim 5

The process of claim 1 in which said bituminous material contains kerogen as its major organic component.

Claim 6

The process of claim 4 in which said bituminous material comprises a kerogen concentrate obtained by extraction of organic solvent-soluble bitumen, and leaching of carbonate minerals, from oil shale.

Claim 7

The process of claim 1 in which said bituminous material comprises bitumen as its major organic component.

Claim 8

The process of claim 1 in which said bituminous material comprises leached oil shale as its major organic component.

Claim 9

The process of claim 1 in which said bituminous material comprises asphaltene as its major organic component.

Claim 10

The process of claim 1 in which said water-soluble product is separated from said residue by filtration of said residue, precipitation of product by acidification of the resultant filtrate and extraction with a non-aqueous solvent of further product from the filtrate resulting from said precipitation.

Claim 11

A process for treating raw oil shale for recovery of chemicals therefrom, comprising: grinding said oil shale to pass at least a 60 mesh screen, U.S. Standard; adding organic solvent for bitumen to said ground shale to solubilize bitumen in said shale, and extracting said solubilized bitumen; adding a mineral acid to said extracted shale for leaching carbonate minerals; washing to remove residual acid and reaction products of said leaching to obtain a kerogen concentrate; slurrying said kerogen concentrate with a dilute aqueous solution of alkali metal hydroxide as electrolyte at a concentration of greater than 1.0 N; placing said slurry into the anode chamber of an electrolytic cell having a cathode chamber electrolytically operative with said anode chamber; applying a direct current potential across said anode and cathode chambers at a current density of at least 15 A/m 2 for at least one hour to effect electrolysis of said kerogen concentrate whereby to obtain a water-soluble product, and a residue, therefrom; and separating said water-soluble product from said residue by filtration of said residue, precipitation of product by acidification of the resultant filtrate and extraction with non-aqueous solvent of further product from the filtrate resulting from said precipitation.

Claim 12

A process for treating raw oil shale for recovery of chemicals therefrom, comprising: grinding said oil shale to pass at least a 60 mesh screen, U.S. Standard; adding organic solvent for bitumen to said ground shale to solubilize bitumen in said shale, and extracting said solubilized bitumen; adding a mineral acid to said extracted shale for leaching carbonate minerals; washing to remove residual acid and reaction products of said leaching to obtain a kerogen concentrate; slurrying said kerogen concentrate with a dilute aqueous solution of alkali metal hydroxide as electrolyte at a concentration of greater than 1.0 N; placing said slurry into the anode chamber of an electrolytic cell having a cathode chamber electrolytically operative with said anode chamber; applying a direct current potential across said anode and cathode chambers at a current density of at least 15 A/m 2 for at least one hour to effect electrolysis of said kerogen concentrate whereby to obtain a water-soluble product, and a residue, therefrom; and separating said water-soluble product from said residue by filtration of said residue, precipitation of product by acidification of the resultant filtrate and extraction with non-aqueous solvent of further product from the filtrate resulting from said precipitation.