Hydroprocessing method with high liquid mass flux
In a method of hydroprocessing, hydrogen gas for the hydroprocessing reaction is combined with a liquid feed composition comprising a feedstock to be treated and a diluent to form a feed stream, at least a portion of the hydrogen gas being dissolved in the liquid feed composition of the feed stream, with non-dissolved hydrogen gas being present in the feed stream in an amount of from 1 to 70 SCF/bbl of the liquid feed composition. The feed stream is contacted with a hydroprocessing catalyst, within a reactor while maintaining a liquid mass flux within the reactor of at least 5000 lb/hr·ft 2 to form a hydroprocessed product.
1. A method of hydroprocessing comprising:
combining hydrogen gas for the hydroprocessing reaction with a liquid feed composition comprising a feedstock to be treated and a diluent to form a feed stream, a portion of the hydrogen gas being dissolved in the liquid feed composition of the feed stream, with non-dissolved hydrogen gas being present in the feed stream in an amount of from 1 SCF to 70 SCF per bbl of the liquid feed composition; and
contacting the feed stream with a hydroprocessing catalyst of a catalyst bed while the liquid feed composition flows through a volume of nearly stagnant gas within a reactor while maintaining a liquid mass flux within the reactor of at least 5000 lb/hr·ft 2 to form a hydroprocessed product.
2. The method of claim 1 , wherein:
the feedstock comprises at least one of a petroleum feedstock, a non-petroleum feedstock, a bio oil, a pyrolysis oil, a high-contaminant feedstock, and a high-olefinic feedstock.
3. The method of claim 1 , wherein:
the feed stream is contacted with a hydroprocessing catalyst contained in at least two catalyst beds within the reactor.
4. The method of claim 1 , wherein:
the non-dissolved hydrogen gas in the feed stream is present in an amount of from 1 SCF to 50 SCF per bbl of the liquid feed composition.
5. The method of claim 1 , wherein:
the liquid mass flux within the reactor is maintained at from 5000 lb/hr·ft 2 to 100,000 lb/hr·ft 2 .
6. The method of claim 1 , wherein:
the liquid mass flux within the reactor is maintained at from 6000 lb/hr·ft 2 to 100,000 lb/hr·ft 2 .
7. The method of claim 1 , wherein:
the liquid mass flux within the reactor is maintained at from 10,000 lb/hr·ft 2 or more.
8. The method of claim 1 , wherein:
the liquid mass flux within the reactor is maintained at from 30,000 lb/hr·ft 2 or more.
9. The method of claim 1 , wherein:
at least a portion of the hydroprocessed product is used to form the diluent.
10. The method of claim 1 , further comprising:
separating gas from liquid hydroprocessed product in a separator located within the reactor.
11. The method of claim 10 , wherein:
the separated gas is removed from the reactor at a rate so that the volume of gas within the reactor is maintained in the near stagnant condition.
12. The method of claim 10 , further comprising:
maintaining a liquid level within the reactor by controlling the amount of hydrogen gas added to the feedstream.
13. The method of claim 1 , wherein:
the volume of gas within the reactor is maintained in the near stagnant condition by controlling the removal of gas from the reactor so that hydrogen gas is at or less than 5 ACF/hr per ft 3 of reactor volume.
14. A method of hydroprocessing comprising:
combining hydrogen gas for the hydroprocessing reaction with a liquid feed composition comprising a feedstock to be treated and a diluent to form a feed stream, a portion of the hydrogen gas being dissolved in the liquid feed composition of the feed stream, with non-dissolved hydrogen gas being present in the feed stream in an amount of from 1 SCF to 50 SCF per bbl of the liquid feed composition; and
contacting the feed stream with a hydroprocessing catalyst contained in at least two catalyst beds contained within a reactor while the liquid feed composition flows through a volume of nearly stagnant gas while maintaining a liquid mass flux within the reactor of from 10,000 lb/hr·ft 2 to 100,000 lb/hr·ft 2 to form a hydroprocessed product.
15. The method of claim 14 , wherein:
the feedstock comprises at least one of a petroleum feedstock, a non-petroleum feedstock, a bio oil, a pyrolysis oil, a high-contaminant feedstock, and a high-olefinic feedstock.
16. The method of claim 14 , wherein:
the liquid mass flux within the reactor is maintained from 30,000 lb/hr·ft 2 to 100,000 lb/hr·ft 2 .
17. The method of claim 14 , wherein:
at least a portion of the hydroprocessed product is used to form the diluent.
18. The method of claim 14 , further comprising:
separating gas from liquid hydroprocessed product in a separator located within the reactor.
19. The method of claim 14 , wherein:
the separated gas is removed from the reactor at a rate so that the volume of gas within the reactor is maintained in the near stagnant condition.
20. The method of claim 14 , further comprising:
maintaining a liquid level within the reactor by controlling the amount of hydrogen gas added to the feedstream.