Reduced nitrogen content of hydrocarbon fraction by catalytic polymerization

Claim 3

The method of claim 1 wherein said feedstock is derived from oil shale.

Claim 4

The method of claim 2 wherein said feedstock contains at least about 3,000 ppm. of nitrogen and boils primarily in the range from about 350° F. to about 1000° F.

Claim 5

The method of claim 1 wherein said contacting takes place in the presence of added free molecular hydrogen in an amount from about 50 s.c.f./b. to about 10,000 s.c.f./b. of feedstock and said fraction enriched in said polymerized nitrogen-containing compounds is normally liquid and comprises from about 1% to about 20% based on the weight of said feedstock.

Claim 6

The method of claim 3 wherein said contacting takes place in the presence of added free molecular hydrogen in an amount from about 300 s.c.f./b. to about 7,000 s.c.f./b. of feedstock and said fraction enriched in said polymerized nitrogen-containing compounds is normally liquid and comprises from about 5% to about 20% based on the weight of said feedstock.

Claim 7

The method of claim 4 wherein said metal is selected from the group consisting of iron, cobalt, nickel, aluminum, molybdenum and mixtures thereof, and said contacting takes place at a temperature in the range from about 400° F. to about 1000° F. and at a pressure in the range from about 0 psig. to about 3000 psig.

Claim 8

The method of claim 5 wherein said metal is selected from the group consisting of iron, cobalt, nickel, aluminum, molybdenum and mixtures thereof, and said contacting takes place at a temperature in the range from about 500° F. to about 800° F. and at a pressure in the range from about 300 psig. to about 3000 psig.

Claim 9

The method of claim 6 wherein said metal is iron and step (2) is carried out by flashing said effluent.

Claim 10

The method of claim 7 wherein said metal is iron and step (2) is carried out by flashing said effluent.

Claim 11

In a hydrocarbon hydrotreating process which includes contacting a hydrocarbon feedstock containing sulfur and nitrogen compounds therein with hydrogen and with a hydrotreating catalyst at conditions such that hydrogen forms compounds with at least one of said contaminants and recovering a hydrotreated product having a reduced content of at least one of said contaminants relative to said hydrocarbon feedstock, the improvement which comprises: (1) contacting said feedstock, prior to said hydrotreating step with a catalyst effective to promote the polymerization of at least a portion of the nitrogen-containing compounds in said feedstock at conditions sufficient to polymerize at least a portion of said nitrogen-containing compounds and form a reaction effluent, said feedstock boiling primarily in the range from about 200° F. to about 1000° F. and containing at least about 1000 ppm. of nitrogen, said catalyst of step (1) comprises at least one metal selected from the group consisting of Group IB metals, Group IIB metals, Group III metals, Group IV metals, Group VI metals, Group VIII metals, the rare earth metals and mixtures thereof; and (2) separating from effluent a fraction enriched in said polymerized nitrogen-containing compounds and a hydrocarbon fraction from said step (1) having a reduced nitrogen content relative to said feedstock.

Claim 12

In a hydrocarbon hydrotreating process which includes contacting a hydrocarbon feedstock containing sulfur and nitrogen compounds therein with hydrogen and with a hydrotreating catalyst at conditions such that hydrogen forms compounds with at least one of said contaminants and recovering a hydrotreated product having a reduced content of at least one of said contaminants relative to said hydrocarbon feedstock, the improvement which comprises: (1) contacting said feedstock, prior to said hydrotreating step with a catalyst effective to promote the polymerization of at least a portion of the nitrogen-containing compounds in said feedstock at conditions sufficient to polymerize at least a portion of said nitrogen-containing compounds and form a reaction effluent, said feedstock boiling primarily in the range from about 200° F. to about 1000° F. and containing at least about 1000 ppm. of nitrogen, said catalyst of step (1) comprises at least one metal selected from the group consisting of Group IB metals, Group IIB metals, Group III metals, Group IV metals, Group VI metals, Group VIII metals, the rare earth metals and mixtures thereof; and (2) separating from effluent a fraction enriched in said polymerized nitrogen-containing compounds and a hydrocarbon fraction from said step (1) having a reduced nitrogen content relative to said feedstock.

Claim 13

The method of claim 10 wherein said feedstock is derived from oil shale.

Claim 14

The method of claim 11 wherein said feedstock contains at least about 3,000 ppm. of nitrogen and boils primarily in the range from about 350° F. to about 1000° F.

Claim 15

The method of claim 10 wherein said contacting of step (1) takes place in the presence of added free molecular hydrogen in an amount from about 50 s.c.f./b. to about 10,000 s.c.f./b. of feedstock and said fraction enriched in said polymerized nitrogen-containing compounds is normally liquid and comprises from about 1% to about 20% based on the weight of said feedstock.

Claim 16

The method of claim 12 wherein said contacting of step (1) takes place in the presence of added free molecular hydrogen in an amount from about 300 s.c.f./b. to about 7,000 s.c.f./b. of feedstock and said fraction enriched in said polymerized nitrogen-containing compounds is normally liquid and comprises from about 5% to about 20% based on the weight of said feedstock.

Claim 17

The method of claim 13 wherein said metal of step (1) is selected from the group consisting of iron, cobalt, nickel, aluminum, molybdenum and mixtures thereof, and said contacting of step (1) takes place at a temperature in the range from about 400° F. to about 1000° F. and at a pressure in the range from about 0 psig. to about 3000 psig.

Claim 18

The method of claim 14 wherein said metal of step (1) is selected from the group consisting of iron, cobalt, nickel, aluminum, molybdenum and mixtures thereof, and said contacting of step (1) takes place at a temperature in the range from about 500° F. to about 800° F. and at a pressure in the range from about 300 psig. to about 3000 psig.

Claim 19

The method of claim 15 wherein said metal of step (1) is iron and step (2) is carried out by flashing said effluent.

Claim 20

The method of claim 16 wherein said metal of step (1) is iron and step (2) is carried out by flashing said effluent.