Dearsenating of shale oil with polyacrylamides

Claim 2

A process for removing at least a portion of arsenic impurities from a hydrocarbon-containing feed stream, which contains arsenic compounds, comprising the step (a) of contacting said feed stream with an aqueous extractant, which contains at least one substantially dissolved polyacrylamide, under suitable dearsenating conditions so as to produce a hydrocarbon-containing stream having a reduced level of arsenic.

Claim 3

A process in accordance with claim 1 wherein said hydrocarbon-containing feed stream is shale oil.

Claim 4

A process in accordance with claim 1 wherein said aqueous extractant contains at least one substantially dissolved polyacrylamide at a concentration ranging from about 5 ppmw to about 5000 ppmw.

Claim 5

A process in accordance with claim 3 wherein the weight ratio of the substantially dissolved polyacrylamide to the hydrocarbon-containing feed stream ranges from about 0.05:1 to about 20:1.

Claim 6

A process in accordance with claim 4 wherein said hydrocarbon-containing feed stream is shale oil.

Claim 7

A process in accordance with claim 3 wherein said substantially dissolved polyacrylamide has a molecular weight ranging from about 1×1O 3 to about 1×1O 8 and a degree of hydrolysis of about 0% to 50%.

Claim 8

A process in accordance with claim 6 wherein the weight ratio of the substantially dissolved polyacrylamide to the hydrocarbon-containing feed stream ranges from about 0.05:1 to about 20:1.

Claim 9

A process in accordance with claim 7 wherein said weight ratio ranges from about 0.1:1 to about 2:1.

Claim 10

A process in accordance with claim 7 wherein the hydrocarbon-containing feed stream is shale oil.

Claim 11

A process in accordance with the process of claim 8 wherein the hydrocarbon-containing feed stream is shale oil, and wherein the polyacrylamide has a molecular weight ranging from about 2×1O 6 to about 2×10 7 and having a degree of hydrolysis ranging from about 10% to about 40%.

Claim 12

A process in accordance with claim 7 wherein the reaction time ranges from about 0.05 to about 50 hours, and the reaction temperature ranges from about 10° C. to about 200° C.

Claim 13

A process in accordance with claim 10 wherein the reaction time ranges from about 0.05 to about 50 hours, and the reaction temperature ranges from about 10° C. to about 200° C.

Claim 14

A process in accordance with claim 11 wherein the reaction time ranges from about 0.1 to about 5 hours, and the reaction temperature ranges from about 20° C. to about 90° C.

Claim 15

A process in accordance with claim 12 wherein the reaction time ranges from about 0.1 to about 5 hours, and the reaction temperature ranges from about 20° C. to about 90° C.

Claim 16

A process in accordance with claim 1 comprising the additional step (b) of separating the hydrocarbon-containing stream having a reduced level of arsenic from the aqueous extractant.

Claim 17

A process in accordance with claim 2 comprising the additional step (b) of separating the hydrocarbon-containing stream having a reduced level of arsenic from the aqueous extractant.

Claim 18

A process in accordance with claim 16 wherein said separating step comprises settling and decanting.

Claim 19

A process in accordance with claim 16 wherein the hydrocarbon-containing stream having a reduced level of arsenic contains sulfur and nitrogen impurities.

Claim 20

A process in accordance with claim 18 comprising the additional step (c) of catalytically hydrotreating the hydrocarbon-containing stream having a reduced level of arsenic so as to remove at least a portion of sulfur and nitrogen impurities.

Claim 21

A process for reducing the arsenic content of an arsenic containing hydrocarbon feed stream, said process comprising: (a) contacting said feed stream with an aqueous extractant, which contains at least on substantially dissolved polyacrylamide, to form a two-phase liquid mixture, (b) separating said two-phase liquid mixture first into a hydrocarbon material having reduced arsenic content (as compared to said hydrocarbon feed stream) and an aqueous stream, and then (c) recovering said hydrocarbon material having a reduced arsenic content.

Claim 22

A process for reducing the arsenic content of an arsenic containing hydrocarbon feed stream, said process comprising: (a) contacting said feed stream with an aqueous extractant, which contains at least on substantially dissolved polyacrylamide, to form a two-phase liquid mixture, (b) separating said two-phase liquid mixture first into a hydrocarbon material having reduced arsenic content (as compared to said hydrocarbon feed stream) and an aqueous stream, and then (c) recovering said hydrocarbon material having a reduced arsenic content.

Claim 23

A process in accordance with claim 20 comprising the additional step of (d) subjecting said hydrocarbon material having a reduced arsenic content to heating under cracking conditions so as to produce gasoline and other useful fuel products.