Process for the production of white oils

Claim 2

A single reaction step hydrogenation process for producing a hydrocarbon white oil which process comprises contacting a feed stream comprising C 15 -C 50 hydrocarbons obtained directly from an aromatic alkylation process without any intermediate hydrotreating steps for the purpose of removing sulfurous components with a hydrogenation catalyst comprising a platinum group metal component that has been surface impregnated upon an alumina support to form an alumina catalyst particle in such a manner that the concentration of the platinum group metal on the outer 25 volume percent [vol. %] of the alumina catalyst particle is at least twice as great as the concentration of the platinum group metal component on the inner 25 volume per cent [vol. %] of the alumina catalyst particle with the contacting occurring in a hydrogenation reaction zone operating at a temperature of from 125° to 300° C., a pressure of from 10 to 150 atmospheres, a liquid hourly space velocity of from 0.05 to 5 hr -1 ,and a hydrogen-to-hydrocarbon molar feed ratio of from 2 to 15, and recovering the white oil produced in the hydrogenation reaction zone.

Claim 3

The process of claim 1 further characterized in that the catalyst particle is a sphere or an extrudate.

Claim 4

The process of claim 1 further characterized in that the C 15 -C 50 hydrocarbon feedstock comprises from 70 to 100 wt. % alkylaromatic hydrocarbons and from 0 to 30 wt. % paraffinic, and 0 to 30 wt. % olefinic and naphthenic hydrocarbons.

Claim 5

The process of claim 1 further characterized in that the platinum group metal component is present in the catalyst in an amount ranging from 0.05 to 5.0 wt. %.

Claim 6

The process of claim 4 further characterized in that the platinum group metal component is platinum.

Claim 7

The process of claim 5 further characterized in that the hydrogenation catalyst comprises an alkali group metal component.

Claim 8

The process of claim 6 further characterized in that the alkali group metal component is selected from the group sodium, potassium, lithium, or mixtures thereof.

Claim 9

The process of claim 7 further characterized in that the alkali group metal component selected from the group sodium, potassium, lithium, or mixtures thereof is present in the catalyst in an amount ranging from 0.1 to 5.0 wt. %.

Claim 10

A hydrogenation process for producing a hydrocarbon white oil which comprises contacting a feed stream which is essentially free of sulfur and which comprises 70 to 100 wt. % alkylaromatic and 0 to 30 wt. % paraffinic, olefinic and naphthenic C 15 -C 50 hydrocarbons obtained from an aromatic alkylation process with a hydrogenation catalyst comprising from 0.05 to 5.0 wt. % of a surface-impregnated platinum component and from 0.1 to 5.0 wt. % of a lithium, sodium, or potassium component on a gamma-alumina support particle where the surface-impregnated platinum is located on the gamma-alumina particle in such a manner that the platinum concentration on the outer 25 vol. % of the gamma-alumina catalyst particle is at least twice that of the platinum concentration in the inner 25 vol. % of the gamma-alumina catalyst particle with the contacting occurring in a hydrogenation reaction zone operating at hydrogenation reaction conditions including a temperature of from 125° to 300° C., a pressure of from 10 to 150 atmospheres, a liquid hourly space velocity of from 0.1 to 5.0 hr -1 , and a hydrogen-to-hydrocarbon molar feed ratio of from 2 to 15 and recovering the white oil product produced therefrom.

Claim 11

A hydrogenation process for producing a hydrocarbon white oil which comprises contacting a feed stream which is essentially free of sulfur and which comprises 70 to 100 wt. % alkylaromatic and 0 to 30 wt. % paraffinic, olefinic and naphthenic C 15 -C 50 hydrocarbons obtained from an aromatic alkylation process with a hydrogenation catalyst comprising from 0.05 to 5.0 wt. % of a surface-impregnated platinum component and from 0.1 to 5.0 wt. % of a lithium, sodium, or potassium component on a gamma-alumina support particle where the surface-impregnated platinum is located on the gamma-alumina particle in such a manner that the platinum concentration on the outer 25 vol. % of the gamma-alumina catalyst particle is at least twice that of the platinum concentration in the inner 25 vol. % of the gamma-alumina catalyst particle with the contacting occurring in a hydrogenation reaction zone operating at hydrogenation reaction conditions including a temperature of from 125° to 300° C., a pressure of from 10 to 150 atmospheres, a liquid hourly space velocity of from 0.1 to 5.0 hr -1 , and a hydrogen-to-hydrocarbon molar feed ratio of from 2 to 15 and recovering the white oil product produced therefrom.

Claim 12

The process of claim 9 further characterized in that the hydrogenation reaction occurs in a mixed phase of gas and liquid.

Claim 13

The process of claim 9 further characterized in that the catalyst support particle is spherical or an extrudate.