Combined catalytic and alkali metal hydrodesulfurization and conversion process

Claim 2

A process for the combined desulfurization and conversion of a sulfur- and asphaltene-containing feedstock which comprises a. contacting said feedstock with a desulfurization catalyst comprising at least one metallic hydrogenation component selected from the metals consisting of Group VIB and Group VIII of the Periodic Table supported on a porous base, said porous base having a pore diameter ranging from between about 10 to 100 Angstroms, under hydrodesulfurization conditions, so that said feedstock is at least partially desulfurized, and further so that hydrogen sulfide is generated therein; and b. contacting said at least partially desulfurized feedstock from step (a) with an alkali metal in a conversion zone, at elevated temperatures, and in the presence of added hydrogen, so that at least 50 percent of the sulfur content of said feedstock is removed therefrom, and further so that at least about 50 percent of the heavy bottoms fraction of said at least partially desulfurized feedstock, boiling above about 1050°F, is converted to lower-boiling products and c. withdrawing said lower-boiling products and desulfurized feedstock from step (b).

Claim 3

The process of claim 1 wherein said porous base comprises an alumina-containing gel.

Claim 4

The process of claim 1 wherein said hydrodesulfurization catalyst includes at least two hydrogenation components, including a metal from Group VI of the Periodic Table and a metal from Group VIII of the Periodic Table, and further wherein said porous support comprises a porous support selected from the group consisting of alumina, aluminum phosphate-alumina, alumina-boria and mixtures thereof.

Claim 5

The process of claim 1 wherein said alkali metal comprises sodium.

Claim 6

The process of claim 1 wherein said hydrodesulfurization conditions include a temperature of between about 550° and 800°F, a hydrogen pressure of between about 200 and 2000 psig, and a liquid hourly space velocity of between about 0.2 and 5.0 V/V/Hr.

Claim 7

The process of claim 1 wherein said elevated temperature is greater than about 750°F.

Claim 8

The process of claim 1 wherein sufficient hydrogen is added to said conversion zone to maintain a hydrogen pressure of between about 1000 and 5000 psig.

Claim 9

The process of claim 1 wherein said contacting of said at least partially desulfurized feedstock with said alkali metal in said conversion zone results in the generation of alkali metal sulfide, and wherein said alkali metal sulfide is contacted with hydrogen sulfide, in order to convert said alkali metal sulfide into the corresponding alkali metal hydrosulfide.

Claim 10

The process of claim 1 wherein said feedstock comprises a residuum feedstock including about 30% asphaltenes.

Claim 11

A process for the combined hydrodesulfurization and hydroconversion of a sulfur- and asphaltene-containing feedstock, said feedstock including more than about 30% asphaltenes, which comprises a. contacting said feedstock with a hydrodesulfurization catalyst comprising a hydrogenation component selected from the metals of Group VIII of the Periodic Table, a hydrogenation component selected from the metals of Group VIB of the Periodic Table, and a porous alumina-containing support, said hydrodesulfurization catalyst having a pore diameter ranging from between about 20 to 80 Angstroms, under hydrodesulfurization conditions including a temperature of between about 550° and 850°F, and a hydrogen pressure of from 200 to 2000 psig, so that at least 40 percent of the sulfur contained in said feedstock is removed therefrom, and b. contacting said at least partially desulfurized feedstock from step (a) with an alkali metal in a conversion zone, said conversion zone being maintained at a temperature above about 750°F, and in the presence of added hydrogen sufficient to maintain said conversion zone at a pressure of from 1000 to 5000 psig, so that at least 50 percent of the heavy feed components boiling above 1050°F in said at least partially desulfurized feedstock are converted to lower-boiling products, and further so that at least 50 percent of the sulfur content of said feedstock is removed therefrom, with the resultant formation of alkali metal sulfide in said conversion zone, and c. withdrawing said lower-boiling products and desulfurized feedstock from step (b).

Claim 12

A process for the combined hydrodesulfurization and hydroconversion of a sulfur- and asphaltene-containing feedstock, said feedstock including more than about 30% asphaltenes, which comprises a. contacting said feedstock with a hydrodesulfurization catalyst comprising a hydrogenation component selected from the metals of Group VIII of the Periodic Table, a hydrogenation component selected from the metals of Group VIB of the Periodic Table, and a porous alumina-containing support, said hydrodesulfurization catalyst having a pore diameter ranging from between about 20 to 80 Angstroms, under hydrodesulfurization conditions including a temperature of between about 550° and 850°F, and a hydrogen pressure of from 200 to 2000 psig, so that at least 40 percent of the sulfur contained in said feedstock is removed therefrom, and b. contacting said at least partially desulfurized feedstock from step (a) with an alkali metal in a conversion zone, said conversion zone being maintained at a temperature above about 750°F, and in the presence of added hydrogen sufficient to maintain said conversion zone at a pressure of from 1000 to 5000 psig, so that at least 50 percent of the heavy feed components boiling above 1050°F in said at least partially desulfurized feedstock are converted to lower-boiling products, and further so that at least 50 percent of the sulfur content of said feedstock is removed therefrom, with the resultant formation of alkali metal sulfide in said conversion zone, and c. withdrawing said lower-boiling products and desulfurized feedstock from step (b).

Claim 13

The process of claim 10 wherein said hydrodesulfurization catalyst comprises a Group VI metal selected from the group consisting of cobalt, molybdenum, and tungsten, and said Group VIII metal comprises a metal selected from the group consisting of nickel and cobalt, and where said alumina-containing porous support comprises a porous support selected from the group consisting of alumina, silica-alumina, aluminum phosphate-alumina, boria-alumina, and mixtures thereof.

Claim 14

The process of claim 10 wherein the hydrogen sulfide generated in said hydrodesulfurization zone is removed from said at least partially desulfurized feedstock prior to contacting said at least partially desulfurized feedstock with said alkali metal.

Claim 15

The process of claim 10 wherein said hydrogen sulfide is stripped from said partially desulfurized feedstock by contacting said at least partially desulfurized hydrocarbon feedstock with added hydrogen.

Claim 16

The process of claim 10 wherein said lower-boiling products and the desulfurized feedstock withdrawn from said conversion zone are contacted with hydrogen sulfide in order to convert said alkali metal sulfides to the corresponding alkali metal hydrosulfides.

Claim 17

The process of claim 10 wherein said hydrogen sulfide separated from said at least partially desulfurized hydrocarbon feedstock from step (a) is contacted with said lower-boiling products and the desulfurized feedstock withdrawn from said conversion zone.

Claim 18

The process of claim 10 wherein said alkali metal hydrosulfides are separated from the said lower-boiling products and the desulfurized feedstock withdrawn from said conversion zone.

Claim 19

The process of claim 16 wherein alkali metal is regenerated from said alkali metal hydrosulfides.

Claim 20

The process of claim 17 wherein said alkali metal is regenerated by the electrolysis of said alkali metal hydrosulfides.

Claim 21

The process of claim 16 wherein said alkali metal comprises sodium, and said sodium is regenerated by contacting said sodium hydrosulfides with steam and carbon dioxide so that sodium carbonate is produced therein, and further wherein sodium carbonate is thermally reduced in the presence of coke, to produce said sodium therefrom.