IP Library Granted Patent US 11,655,424
Granted Patent B2
US 11,655,424 · App. 17/497,284 · Granted May 23, 2023

Process for producing jet fuel from a biorenewable feed

Inventors: Andrea G. Bozzano (Northbrook, IL); Haiyan Wang (Hoffman Estates, IL); Krishna Mani (Gurgaon, IN); Stanley Joseph Frey (Palatine, IL)
Assignee: UOP LLC
C10G69/04C10G3/42C10G3/50C10G7/00C10G45/58C10G2300/1011C10G2300/4081C10G2400/04C10G2400/08
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Quick Facts
Patent No.
US 11,655,424
App. No.
17/497,284
Granted
May 23, 2023
Kind
B2
Abstract

The process produces a diesel stream from a biorenewable feedstock by hydrotreating to remove heteroatoms and hydroisomerization to improve cold flow properties. Heavy diesel can be hydrocracked to jet fuel range material or further hydroisomerized to increase its value lower its freeze point while light diesel may be taken as a motor fuel.

Claims (34)

1. A process for hydroprocessing a biorenewable feedstock, the process comprising:

hydrotreating said biorenewable feed stream in the presence of hydrogen over a hydrotreating catalyst to hydrodeoxygenate said biorenewable feed stream to provide a hydrotreated stream;

hydroisomerizing a hydroisomerization feed stream in a hydroisomerization reactor taken from said hydrotreated stream in the presence of hydrogen over a hydroisomerization catalyst to provide a hydroisomerized stream;

separating said hydrotreated stream and/or said hydroisomerized stream into a hydroprocessed vapor stream and a hydroprocessed liquid stream;

distilling said hydroprocessed liquid stream or said hydroisomerized stream, optionally after stripping, to produce a jet fuel stream and a diesel stream; and

hydrocracking said diesel stream in a hydrocracking reactor to provide a hydrocracked stream comprising jet fuel.

2. The process of claim 1 further comprising distilling said hydroisomerized stream and said hydrocracked stream.

3. The process of claim 1 further comprising distilling said hydroisomerized stream.

4. The process of claim 3 further comprising hydroisomerizing said hydrocracked stream.

5. The process of claim 1 further comprising hydroisomerizing said hydrocracked stream.

6. The process of claim 1 further comprising distilling said hydrocracked stream.

7. The process of claim 5 further comprising hydroisomerizing said hydrotreated steam in the presence of hydrogen over said hydroisomerization catalyst to provide said hydroisomerized stream.

8. The process of claim 6 further comprising separating said hydroisomerized stream in said separation step.

9. The process of claim 5 further comprising distilling said hydrocracked stream with said hydroprocessed liquid stream.

10. The process of claim 1 wherein said diesel stream is a heavy diesel stream and further comprising producing a light diesel stream in said distillation step.

11. The process of claim 1 further comprising separating said hydrotreated stream in said separation step; distilling said hydroprocessed liquid stream; hydroisomerizing said jet fuel stream and hydrocracking said diesel stream.

12. The process of claim 10 further comprising hydroisomerizing said hydrocracked stream with said jet fuel stream.

13. The process of claim 11 further comprising separating said hydroisomerized stream into a hydroisomerized liquid stream and a hydroisomerized vapor stream.

14. The process of claim 12 further comprising stripping said hydroisomerized liquid stream into a naphtha stream and a jet fuel product stream.

15. The process of claim 1 further comprising enriching the concentration of normal paraffins of a given carbon number by a factor of at least two in the diesel stream relative to the hydroisomerized stream.

16. A process for hydroprocessing a biorenewable feedstock, the process comprising:

hydrotreating said biorenewable feed stream in the presence of hydrogen over a hydrotreating catalyst to hydrodeoxygenate said biorenewable feed stream to provide a hydrotreated stream;

hydroisomerizing in a hydroisomerization reactor a hydroisomerization feed stream taken from said hydrotreated stream in the presence of hydrogen over a hydroisomerization catalyst to provide a hydroisomerized stream;

enriching the concentration of normal paraffins of a given carbon number by a factor of at least two in a diesel stream taken from said hydroisomerized stream relative to said hydroisomerized stream; and

hydrocracking or hydroisomerizing said diesel stream in a hydrocracking reactor to provide a hydrocracked stream comprising jet fuel.

17. The process of claim 16 wherein said enriching step is achieved by distillation of a hydroisomerized liquid stream.

18. The process of claim 16 further comprising hydrocracking said diesel stream and hydroisomerizing said hydrocracked stream.

19. A process for hydroprocessing a biorenewable feedstock, the process comprising:

hydrotreating said biorenewable feed stream in the presence of hydrogen over a hydrotreating catalyst to hydrodeoxygenate said biorenewable feed stream to provide a hydrotreated stream;

hydroisomerizing said hydrotreated stream in a hydroisomerization reactor in the presence of hydrogen over a hydroisomerization catalyst to provide a hydroisomerized stream;

separating said hydroisomerized stream into a hydroprocessed vapor stream and a hydroprocessed liquid stream;

distilling said hydroprocessed liquid stream or said hydroisomerized stream, optionally after stripping, to produce a jet fuel stream and a diesel stream; and

hydrocracking said diesel stream in a hydrocracking reactor to provide a hydrocracked stream comprising jet fuel.

20. The process of claim 19 further comprising hydroisomerizing said hydrocracked stream.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 8, 2021
From: BOZZANO, ANDREA G.; WANG, HAIYAN; MANI, KRISHNA; FREY, STANLEY JOSEPH
To: UOP LLC
Reel/Frame 057741/0858 →
Priority Claims (1)
IN 202011046430 · Oct 24, 2020 · national
Continuity (1)
Related Publication 20220127537A1 · Apr 28, 2022
Cited By (1)
US 12,630,773