Electrolytic recovery of economic values from shale oil retort water

Claim 2

A process for the recovery of economic values from shale oil retort water, said retort water including soluble material comprising substantial portions of inorganic, acidic organic and basic organic components, said process comprising: defining an electrolytic cell having a cathode chamber electrolytically operative with an anode chamber, an anode in said anode chamber and a cathode in said cathode chamber, each disposed for contacting aqueous solution therein; delivering said shale oil retort water to said cell as said aqueous solution; applying a direct current potential across said anode and cathode chambers at a current density above about 50 A/m 2 for a time sufficient to effect a substantial decrease of organic compounds in the retort water in said anode chamber and to evolve a substantial amount of ammonia from the retort water in said cathode chamber; and recovering said evolved ammonia.

Claim 3

The process of claim 1 in which said retort water includes suspended particles of shale oil and acid salts, and including the step, prior to said electrolysis, of separating said suspended particles from said retort water.

Claim 4

The process of claim 1 in which said evolved ammonia is recovered by venting of said cathode chamber.

Claim 5

The process of claim 1 in which carbon dioxide is vented from said anode chamber.

Claim 6

The process of claim 1 in which said anode and cathode chambers are separated by a cation-porous membrane which is substantially impermeable to said organic components.

Claim 7

The process of claim 1 in which said aqueous solution consists essentially of said shale oil retort water.

Claim 8

The process of claim 1 in which the soluble material of said oil shale retort water comprises about 67-75 weight percent inorganic components and about 25-33 weight percent organic components, based on said soluble material.

Claim 9

The process of claim 1 in which said organic components comprise about 10-15 weight percent acidic organics, about 7-10 weight percent basic organic components and about 3-5 weight percent neutral organic components, based on said soluble material.

Claim 10

A process for the recovery of economic values from shale oil retort water, said retort water including soluble material comprising about 67-75 weight percent inorganic components, about 10-15 weight percent acidic organic components, about 7-10 weight percent basic organic components and about 3-5 weight percent neutral organics, and containing suspended particles of shale oil and acid salts, said process comprising: defining an electrolytic cell having a cathode chamber electrolytically operative with an anode chamber, separated by a cation-porous membrane which is substantially impermeable to said organic components, an anode in said anode chamber and a cathode in said cathode chamber, each disposed for contacting aqueous solution therein; separating said suspended particles from said retort water; delivering an aqueous solution, consisting essentially of said shale oil retort water, to said cell; applying a direct current potential across said anode and cathode chambers at a current density above about 50 A/m 2 for a time sufficient to effect a substantial decrease of organic compounds in said retort water in said anode chamber and to evolve a substantial amount of ammonia from the retort water in said cathode chamber; venting carbon dioxide from said anode chamber; and venting said cathode chamber and recovering said evolved ammonia therefrom.

Claim 11

A process for the recovery of economic values from shale oil retort water, said retort water including soluble material comprising about 67-75 weight percent inorganic components, about 10-15 weight percent acidic organic components, about 7-10 weight percent basic organic components and about 3-5 weight percent neutral organics, and containing suspended particles of shale oil and acid salts, said process comprising: defining an electrolytic cell having a cathode chamber electrolytically operative with an anode chamber, separated by a cation-porous membrane which is substantially impermeable to said organic components, an anode in said anode chamber and a cathode in said cathode chamber, each disposed for contacting aqueous solution therein; separating said suspended particles from said retort water; delivering an aqueous solution, consisting essentially of said shale oil retort water, to said cell; applying a direct current potential across said anode and cathode chambers at a current density above about 50 A/m 2 for a time sufficient to effect a substantial decrease of organic compounds in said retort water in said anode chamber and to evolve a substantial amount of ammonia from the retort water in said cathode chamber; venting carbon dioxide from said anode chamber; and venting said cathode chamber and recovering said evolved ammonia therefrom.