Desulfurization of hydrocarbons

Claim 2

A process comprising (a) contacting a hydrocarbon feedstock containing organo-sulfur compounds with a reduced catalytic absorbent comprising one or more nickel components a molybdenum or tungsten component and one or more platinum group metal promoters composited with a porous refractory oxide, said contacting being under substantially non-hydrogenative conditions including an elevated temperature such that a substantial proportion of said organo-sulfur compounds is removed from said feedstock and said catalytic absorbent increases in sulfur content; and (b) recovering a hydrocarbon product stream containing less organo-sulfur compounds than are contained in said feedstock.

Claim 3

The process as defined in claim 1 wherein said feedstock is a reformer feed containing more than about 0.1 ppmw sulfur and said product stream contains less than 0.1 ppmw sulfur.

Claim 4

The process as defined in claim 1 wherein said catalytic absorbent comprises between about 5 and 50 wt.% nickel components, calculated as NiO.

Claim 5

The process as defined in claim 3 wherein said catalytic absorbent comprises nickel and one or more platinum group metals in an atomic ratio between 1:1 to 5000:1, nickel to platinum group metals.

Claim 6

The process as defined in claim 4 wherein said contacting is accomplished in the absence of hydrogen.

Claim 7

The process as defined in claim 5 wherein said organo-sulfur compounds comprise a substantial proportion of mercaptans.

Claim 8

The process as defined in claim 1 or 3 wherein said catalytic absorbent is reduced with hydrogen.

Claim 9

A process comprising (a) contacting a reformer feedstock containing mercaptans with a catalytic absorbent comprising between about 5 and 50% by weight of nickel components, calculated as NiO, a molybdenum or tungsten component and one or more platinum group metal promoters composited with a porous refractory oxide, said catalytic absorbent having been reduced by hydrogen at an elevated temperature, said contacting being under substantially non-hydrogenative conditions including a temperature between 100° F. and 600° F. such that a substantial proportion of said mercaptans is removed from said feedstock; and (b) recovering a product stream containing less mercaptans than are contained in said feedstock.

Claim 10

A process comprising (a) contacting a reformer feedstock containing mercaptans with a catalytic absorbent comprising between about 5 and 50% by weight of nickel components, calculated as NiO, a molybdenum or tungsten component and one or more platinum group metal promoters composited with a porous refractory oxide, said catalytic absorbent having been reduced by hydrogen at an elevated temperature, said contacting being under substantially non-hydrogenative conditions including a temperature between 100° F. and 600° F. such that a substantial proportion of said mercaptans is removed from said feedstock; and (b) recovering a product stream containing less mercaptans than are contained in said feedstock.

Claim 11

The process as defined in claim 8 wherein said feedstock contains more than about 0.1 ppmw sulfur and said product stream contains less than 0.1 ppmw sulfur.

Claim 12

The process as defined in claim 9 wherein said catalytic absorbent comprises nickel and one or more platinum group metals in an atomic ratio between 1:1 to 5000:1, nickel to platinum group metal.

Claim 13

The process as defined in claim 10 wherein said contacting is accomplished in the absence of hydrogen.

Claim 14

A process comprising (a) contacting, in the absence of hydrogen and at a temperature in the range of about 200° F. to 400° F., a reformer feedstock containing more than 0.1 ppmw sulfur comprising a substantial proportion of mercaptans with a catalytic absorbent comprising between about 5 and 50 wt.% of nickel components, calculated as NiO, a molybdenum or tungsten component and one or more platinum group metal promoters in an atomic ratio between about 1:1 to 5000:1, nickel to platinum group metal, composited with a porous refractory oxide consisting essentially of alumina, said catalytic absorbent having been reduced with hydrogen at a temperature between 500° F. and 900° F., such that a substantial proportion of said mercaptans is removed from said feedstock while said catalytic absorbent increases in sulfur content; and (b) recovering a product stream containing less than about 0.1 ppmw sulfur.

Claim 15

A process comprising (a) contacting, in the absence of hydrogen and at a temperature in the range of about 200° F. to 400° F., a reformer feedstock containing more than 0.1 ppmw sulfur comprising a substantial proportion of mercaptans with a catalytic absorbent comprising between about 5 and 50 wt.% of nickel components, calculated as NiO, a molybdenum or tungsten component and one or more platinum group metal promoters in an atomic ratio between about 1:1 to 5000:1, nickel to platinum group metal, composited with a porous refractory oxide consisting essentially of alumina, said catalytic absorbent having been reduced with hydrogen at a temperature between 500° F. and 900° F., such that a substantial proportion of said mercaptans is removed from said feedstock while said catalytic absorbent increases in sulfur content; and (b) recovering a product stream containing less than about 0.1 ppmw sulfur.

Claim 16

A process comprising (a) contacting a hydrocarbon feedstock containing organo-sulfur compounds with a reduced catalytic absorbent comprising one or more nickel components a molybdenum or tungsten component and one or more platinum or palladium metal promoters, composited with a porous refractory oxide, said contacting being under substantially non-hydrogenative conditions including an elevated temperature such that a substantial proportion of said organo-sulfur compounds is removed from said feedstock and said catalytic absorbent increases in sulfur content; and (b) recovering a hydrocarbon product stream containing less organo-sulfur compounds than are contained in said feedstock.

Claim 17

A process comprising (a) contacting a hydrocarbon feedstock containing organo-sulfur compounds with a reduced catalytic absorbent comprising one or more nickel components a molybdenum or tungsten component and one or more platinum or palladium metal promoters, composited with a porous refractory oxide, said contacting being under substantially non-hydrogenative conditions including an elevated temperature such that a substantial proportion of said organo-sulfur compounds is removed from said feedstock and said catalytic absorbent increases in sulfur content; and (b) recovering a hydrocarbon product stream containing less organo-sulfur compounds than are contained in said feedstock.

Claim 18

The process as defined in claim 13 wherein said feedstock is a reformer feed containing more than about 0.1 ppmw sulfur and said product stream contains less than 0.1 ppmw sulfur.

Claim 19

The process as defined in claim 14 wherein said catalytic absorbent comprises between about 5 and 50 wt.% nickel components, calculated as NiO.

Claim 20

The process as defined in claim 15 wherein said catalytic absorbent comprises nickel and platinum or palladium in an atomic ratio between 1:1 to 5000:1, nickel to platinum or palladium metal.

Claim 21

The process as defined in claim 16 wherein said contacting is accomplished in the absence of hydrogen.

Claim 22

The process as defined in claim 17 wherein said organo-sulfur compounds comprise a substantial proportion of mercaptans.

Claim 23

The process as defined in claim 18 wherein said catalytic absorbent is reduced with hydrogen.

Claim 24

A process comprising (a) contacting a reformer feedstock containing mercaptans with a catalytic absorbent comprising between about 5 and 50% by weight of nickel components calculated as NiO, a molybdenum or tungsten component and one or more platinum metal promoters composited with a porous refractory oxide, said catalytic absorbent having been reduced by hydrogen at an elevated temperature, said contacting being under substantially non-hydrogenative conditions including a temperature between 100° F. and 600° F., such that a substantial proportion of said mercaptans is removed from said feedstock; and (b) recovering a product stream containing less mercaptans than are contained in said feedstock.

Claim 25

A process comprising (a) contacting a reformer feedstock containing mercaptans with a catalytic absorbent comprising between about 5 and 50% by weight of nickel components calculated as NiO, a molybdenum or tungsten component and one or more platinum metal promoters composited with a porous refractory oxide, said catalytic absorbent having been reduced by hydrogen at an elevated temperature, said contacting being under substantially non-hydrogenative conditions including a temperature between 100° F. and 600° F., such that a substantial proportion of said mercaptans is removed from said feedstock; and (b) recovering a product stream containing less mercaptans than are contained in said feedstock.

Claim 26

The process as defined in claim 20 wherein said feedstock contains more than about 0.1 ppmw sulfur and said product stream contains less than 0.1 ppmw sulfur.

Claim 27

The process as defined in claim 21 wherein said catalytic absorbent comprises nickel and platinum metal in an atomic ratio between 1:1 to 5000:1, nickel to platinum metal.

Claim 28

The process as defined in claim 22 wherein said contacting is accomplished in the absence of hydrogen.

Claim 29

A process comprising (a) contacting, in the absence of hydrogen and at a temperature in the range of about 200° F. to 400° F., a reformer feedstock containing more than 0.1 ppmw sulfur comprising a substantial proportion of mercaptans with a catalytic absorbent comprising between about 5 and 50 wt.% of nickel components calculated as NiO, a molybdenum or tungsten component and one or more platinum metal promoters in an atomic ratio between 1:1 to 5000:1, nickel to platinum metal, composited with a porous refractory oxide consisting essentially of alumina, said catalytic absorbent having been reduced with hydrogen at a temperature between 500° F. and 900° F., such that a substantial proportion of said mercaptans is removed from said feedstock while said catalytic absorbent increases in sulfur content; and (b) recovering a product stream containing less than about 0.1 ppmw sulfur.

Claim 30

A process comprising (a) contacting, in the absence of hydrogen and at a temperature in the range of about 200° F. to 400° F., a reformer feedstock containing more than 0.1 ppmw sulfur comprising a substantial proportion of mercaptans with a catalytic absorbent comprising between about 5 and 50 wt.% of nickel components calculated as NiO, a molybdenum or tungsten component and one or more platinum metal promoters in an atomic ratio between 1:1 to 5000:1, nickel to platinum metal, composited with a porous refractory oxide consisting essentially of alumina, said catalytic absorbent having been reduced with hydrogen at a temperature between 500° F. and 900° F., such that a substantial proportion of said mercaptans is removed from said feedstock while said catalytic absorbent increases in sulfur content; and (b) recovering a product stream containing less than about 0.1 ppmw sulfur.