Process for the preparation of hydrocarbon oil distillates

Claim 2

A process for the production of hydrocarbon oil distillates from a hydrocarbon mixture feed stream containing asphaltenes, said process comprising (a) solvent deasphalting said feed stream in a deasphalting zone to obtain a deasphalted oil fraction and an asphaltic bitumen fraction; (b) catalytically hydrotreating said asphaltic bitumen fraction in a hydrotreating zone, therein producing a first product stream having a reduced asphaltenes content; (c) fractionating said first product stream into one or more light distillate fractions and a first heavy distillate fraction; (d) thermally cracking said first heavy distillate fraction and said deasphalted oil fraction in a thermal cracking zone into a second product stream containing less than 20 percent by weight C 4 to C 1 hydrocarbons;

Claim 3

(e) fractionating said second product stream into one or more light distillate fractions and a second heavy distillate fraction; and (f) routing said second heavy distillate fraction to said hydrotreating zone wherein said second heavy distillate fraction is catalytically hydrotreated.

Claim 4

(e) fractionating said second product stream into one or more light distillate fractions and a second heavy distillate fraction; and (f) routing said second heavy distillate fraction to said hydrotreating zone wherein said second heavy distillate fraction is catalytically hydrotreated.

Claim 5

A process for the production of hydrocarbon oil distillates from a hydrocarbon mixture feed stream containing asphaltenes, said process comprising (a) solvent deasphalting said feed stream in a deasphalting zone to obtain a deasphalted oil fraction and an asphaltic bitumen fraction; (b) catalytically hydrotreating said asphaltic bitumen fraction in a hydrotreating zone, therein producing a first product stream having a reduced asphaltenes content; (c) fractionating said first product stream into one or more light distillate fractions and a first heavy distillate fraction; (d) routing said first heavy distillate fraction to said deasphalting zone wherein said first heavy distillate fraction is solvent deasphalted; (e) thermally cracking said deasphalted oil fraction in a thermal cracking zone into a second product stream containing less than 20 percent by weight C 4 to C 1 hydrocarbons; (f) fractionating said second product stream into one or more light distillate fractions and a second heavy distillate fraction; and (g) routing said second heavy distillate fraction to said hydrotreating zone wherein said second heavy distillate fraction is catalytically hydrotreated.

Claim 6

A process for the production of hydrocarbon oil distillates from a hydrocarbon mixture feed stream containing asphaltenes, said process comprising (a) solvent deasphalting said feed stream in a deasphalting zone to obtain a deasphalted oil fraction and an asphaltic bitumen fraction; (b) catalytically hydrotreating said asphaltic bitumen fraction in a hydrotreating zone, therein producing a first product stream having a reduced asphaltenes content; (c) fractionating said first product stream into one or more light distillate fractions and a first heavy distillate fraction; (d) routing said first heavy distillate fraction to said deasphalting zone wherein said first heavy distillate fraction is solvent deasphalted; (e) thermally cracking said deasphalted oil fraction in a thermal cracking zone into a second product stream containing less than 20 percent by weight C 4 to C 1 hydrocarbons; (f) fractionating said second product stream into one or more light distillate fractions and a second heavy distillate fraction; and (g) routing said second heavy distillate fraction to said hydrotreating zone wherein said second heavy distillate fraction is catalytically hydrotreated.

Claim 7

The process according to claims 1 or 2 wherein said feed stream is a hydrocarbon mixture which boils substantially above 350° C., more than 35 percent by weight of which boils above 520° C., and which has an RCT of more than 7.5 percent by weight.

Claim 8

The process according to claims 1 or 2 wherein said feed stream is a residue obtained in the vacuum distillation of an atmospheric distillation residue from a crude mineral oil.

Claim 9

The process according to claims 1 or 2 wherein said catalytic hydrotreating comprises contacting said asphaltic bitumen fraction with a catalyst comprising at least one metal selected from the group consisting of nickel, cobalt and mixtures thereof and in addition, at least one metal selected from the group consisting of molybdenum, tungsten and mixtures thereof, deposited on a carrier, which carrier comprises more than 40% by weight alumina.

Claim 10

The process according to claim 5 wherein said catalyst is selected from the group consisting of nickel/molybdenum on alumina and cobalt/molybdenum on alumina.

Claim 11

The process according to claims 1 or 2 wherein said catalytic hydrotreatment is carried out at a temperature of from 350° to 450° C., a pressure of from 75 to 200 bar, a space velocity of from 0.1 to 2 g.g -1 .hour -1 and a H 2 /feed ratio of from 500 to 2000 Nl.kg -1 .

Claim 12

The process according to claims 1 or 2 wherein said solvent deasphalting is carried out using n-butane as the solvent at a pressure of from 35 to 45 bar and a temperature of from 100° to 150° C.

Claim 13

The process according to claims 1 or 2 wherein said thermal cracking is carried out at a temperature of from 400° to 525° C. and a space velocity of from 0.01 to 5 kg feed per liter of cracking reactor volume per minute.