Hydrotreating process wherein sulfur is added to the feedstock to maintain the catalyst in sulfided form

Claim 2

A process for hydrotreating a hydrocarbon oil containing less than about 0.1 weight percent of total sulfur, calculated as S, under reaction conditions with a hydrotreating catalyst, said process comprising adding a sulfur component to said hydrocarbon oil during said hydrotreating in a concentration such that the total concentration of sulfur contacting said hydrotreating catalyst during said hydrotreating is maintained at about 0.01 to about 0.1 weight percent, calculated as S.

Claim 3

The process defined in claim 1 wherein said hydrotreating removes nitrogen from said hydrocarbon oil.

Claim 4

The process defined in claim 1 wherein said hydrocarbon oil contains less than about 15 ppmw of total contaminant metals, calculated as the free metal.

Claim 5

The process defined in claim 1 further comprising cracking a substantial proportion of the effluent hydrocarbon oil from said hydrotreating.

Claim 6

The process defined in claim 1 wherein said total concentration of sulfur contacting said hydrotreating catalyst is between about 0.025 and about 0.06 weight percent.

Claim 7

The process defined in claim 1 wherein said hydrocarbon oil comprises a synthetic crude.

Claim 8

The process defined in claim 1 wherein said sulfur component is selected from the group consisting of hydrogen sulfide, dimethyl sulfide, dimethyl disulfide, thiophene, carbon disulfide, mercaptan and elemental sulfur.

Claim 9

The process defined in claim 1 wherein said sulfur component is elemental sulfur in a solid form immediately prior to addition to said hydrocarbon oil.

Claim 10

The process defined in claim 1 wherein said hydrotreating catalyst comprises active metal hydrogenation components in a sulfided form.

Claim 11

The process defined in claim 9 wherein said active metal hydrotreating components are selected from the group consisting of Group VIB and Group VIII metals.

Claim 12

The process defined in claim 1 wherein said hydrocarbon oil contains less than about 0.01 weight percent of sulfur prior to said sulfur component addition.

Claim 13

The process defined in claim 1 wherein said hydrocarbon oil is an upgraded shale oil containing less than about 0.06 weight percent of sulfur prior to said sulfur component addition.

Claim 14

The process defined in claim 1 wherein said hydrocarbon oil comprises a full boiling range shale oil that has been successively deashed, dearsenated and hydrotreated.

Claim 15

A process for hydrodenitrogenating a hydrocarbon oil containing greater than about 30 ppmw of total nitrogen, calculated as N, less than about 0.10 weight percent of total sulfur, calculated as S, and less than about 10 ppmw of total contaminant metals, calculated as the free metals, under reaction conditions with a hydrodenitrogenation catalyst, said process comprising adding a sulfur component to said hydrocarbon oil during said hydrodenitrogenating in a concentration such that the total concentration of sulfur contacting said hydrodenitrogenation catalyst during said hydrodenitrogenating is maintained at about 0.01 to about 0.10 weight percent, calculated as S.

Claim 16

A process for hydrodenitrogenating a hydrocarbon oil containing greater than about 30 ppmw of total nitrogen, calculated as N, less than about 0.10 weight percent of total sulfur, calculated as S, and less than about 10 ppmw of total contaminant metals, calculated as the free metals, under reaction conditions with a hydrodenitrogenation catalyst, said process comprising adding a sulfur component to said hydrocarbon oil during said hydrodenitrogenating in a concentration such that the total concentration of sulfur contacting said hydrodenitrogenation catalyst during said hydrodenitrogenating is maintained at about 0.01 to about 0.10 weight percent, calculated as S.

Claim 17

The process defined in claim 14 wherein said hydrocarbon oil comprises at least one member selected from the group comprising a shale oil, an upgraded shale oil, an oil from bituminous sands and a liquid hydrocarbon obtained from a coal composition.

Claim 18

The process defined in claim 14 wherein said sulfur component is selected from the group consisting of hydrogen sulfide, dimethyl sulfide, dimethyl disulfide, thiophene, carbon disulfide, mercaptan and elemental sulfur.

Claim 19

The process defined in claim 14 wherein said sulfur component is elemental sulfur in a solid form immediately prior to addition to said hydrocarbon oil.

Claim 20

The process defined in claim 14 wherein said hydrodenitrogenation catalyst comprises hydrogention components selected from the group consisting of Group VIB and Group VIII metal components in a sulfided form.

Claim 21

The process defined in claim 18 wherein said total concentration of sulfur contacting said denitrogenation catalyst is between about 0.02 and about 0.06 weight percent.

Claim 22

The process defined in claim 18 wherein said active metal components comprise nickel or cobalt and molybdenum or tungsten.

Claim 23

The process defined in claim 14 wherein said hydrocarbon oil comprises a full boiling range shale oil that has been successively deashed, dearsenated and hydrotreated.

Claim 24

A process for hydrodenitrogenating an upgraded shale oil containing greater than about 100 ppmw of total nitrogen, calculated as N, less than about 0.025 weight percent of sulfur, calculated as S, and less than about 5 ppmw of total contaminant metals, calculated as the free metals, under reaction conditions with a hydrodenitrogenation catalyst, said process comprising adding elemental sulfur to said upgraded shale oil during said hydrodenitrogenating in a concentration such that the total concentration of sulfur contacting said hydrodenitrogenation catalyst during said hydrodenitrogenating is maintained at about 0.025 to about 0.06 weight percent, calculated as S.

Claim 25

A process for hydrodenitrogenating an upgraded shale oil containing greater than about 100 ppmw of total nitrogen, calculated as N, less than about 0.025 weight percent of sulfur, calculated as S, and less than about 5 ppmw of total contaminant metals, calculated as the free metals, under reaction conditions with a hydrodenitrogenation catalyst, said process comprising adding elemental sulfur to said upgraded shale oil during said hydrodenitrogenating in a concentration such that the total concentration of sulfur contacting said hydrodenitrogenation catalyst during said hydrodenitrogenating is maintained at about 0.025 to about 0.06 weight percent, calculated as S.

Claim 26

The process defined in claim 22 wherein said hydrodenitrogenation calalyst comprises hydrogenation components selected from the the group consisting of Group VIB and Group VIII metal components in a sulfided form.

Claim 27

The process defined in claim 22 wherein said elemental sulfur is in a solid form immediately prior to addition to said upgraded shale oil.

Claim 28

The process defined in claim 23 wherein said hydrodenitrogenation catalyst further comprises phosphorus components and said Group VIB and Group VIII metal components are selected from the group consisting of nickel, cobalt, molybdenum and tungsten.

Claim 29

The process defined in claim 23 wherein said upgraded shale oil contains less than about 0.01 weight percent of said sulfur prior to said sulfur addition.

Claim 30

The process defined in claim 23 wherein said upgraded shale oil contains less than about 2 ppmw of total contaminant metals.

Claim 31

The process defined in claim 23 wherein said upgraded shale oil has been successively deashed, dearsenated and hydrotreated.