US2015353835A1PendingUtilityA1
Systems and methods for recovering hydrocarbons
Est. expiryMar 1, 2032(~5.6 yrs left)· nominal 20-yr term from priority
C10G 1/045C10G 27/12C10G 1/047
47
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Claims
Abstract
A method for recovering hydrocarbons from an aqueous hydrocarbonaceous slurry comprises pumping a mixture of the slurry and an oxidizing agent through a conduit, wherein the conduit comprises a plurality of stationary interior projections defining a non-linear path through the conduit, and thereby agitating the mixture to release the hydrocarbons from the slurry; and separating the hydrocarbons from the slurry.
Claims
exact text as granted — not AI-modifiedWhat is claimed is:
1 . A method for recovering hydrocarbons from an aqueous hydrocarbonaceous slurry, the method comprising:
pumping a mixture of the slurry and an oxidizing agent through a conduit, wherein the conduit comprises a plurality of stationary interior projections defining a non-linear path through the conduit, and thereby agitating the mixture to release the hydrocarbons from the slurry; and separating the hydrocarbons from the slurry.
2 . The method of claim 1 , further comprising mixing the slurry and the oxidizing agent together in a reactor to form the mixture, prior to pumping the mixture through the conduit.
3 . The method of claim 2 , further comprising heating the mixture to a temperature of from about 50° C. to about 100° C. in the reactor.
4 . The method of claim 3 , wherein the temperature is about 85° C.
5 . The method of claim 1 , further comprising treating the mixture with a pH-correcting agent selected from the group consisting of calcium oxide, calcium hydroxide, calcium carbonate, hydrochloric acid, carbon dioxide, and combinations thereof.
6 . The method of claim 1 , further comprising agitating and heating the hydrocarbonaceous slurry in a slurry hopper to a temperature of from about 50° C. to about 90° C.
7 . The method of claim 1 , wherein particles in the hydrocarbonaceous slurry have a diameter of less than about 2 mm.
8 . The method of claim 1 , further comprising mixing water with a hydrocarbonaceous feedstock to produce the hydrocarbonaceous slurry, wherein the water and feedstock are mixed in a weight proportion of water to feedstock solids of from about 2:1 to about 1:1.
9 . The method of claim 1 , wherein negligible froth is produced in the conduit.
10 . The method of claim 1 , wherein the projections are baffles that project into the bore of the conduit from alternating walls of the conduit.
11 . The method of claim 1 , wherein the oxidizing agent is selected from the group consisting of hydrogen peroxide, potassium permanganate, sodium peroxide, and combinations thereof.
12 . The method of claim 1 , wherein the oxidizing agent is used in an amount of between about 0.1% to about 10% in water phase by weight.
13 . The method of claim 1 , wherein the conduit is parallel to the ground.
14 . The method of claim 1 , further comprising separating remaining solids from the hydrocarbonaceous slurry, wherein the solids comprise less than about 1% hydrocarbons.
15 . A method for recovering hydrocarbons from an aqueous hydrocarbonaceous slurry, the method comprising:
mixing the slurry with an oxidizing agent at a temperature of from about 80° C. to about 100° C. to form a mixture and thereby release the hydrocarbons from the slurry; and separating the hydrocarbons from the slurry.
16 . The method of claim 15 , further comprising pumping the mixture through a conduit, wherein the conduit comprises a plurality of stationary interior projections defining a non-linear path through the conduit, and thereby agitating the mixture to release the hydrocarbons from the slurry.
17 . The method of claim 15 , further comprising mixing the slurry and the oxidizing agent together in a reactor to form the mixture, prior to pumping the mixture through the conduit.Join the waitlist — get patent alerts
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