Process and apparatus for selectively hydrogenating naphtha

Patent metadata

Field	Value
Publication number	US-9822317-B2
Application number	US-201414511877-A
Country	US
Kind code	B2
Filing date	Oct 10, 2014
Priority date	Oct 10, 2014
Publication date	Nov 21, 2017
Grant date	Nov 21, 2017

Abstract

The process and apparatus of the present invention selectively hydrogenates a heavier olefinic naphtha stream in an upstream catalyst bed and the hydrogenated effluent and a lighter olefinic naphtha stream in a downstream catalyst bed. The heavier di-alkenes are less re-active and are contacted with more hydrogenation catalyst than the lighter di-alkenes which are more re-active.

First claim

The invention claimed is:

1. A process for selective hydrogenation comprising:
separating a naphtha stream into a lighter naphtha stream and heavy naphtha stream, said heavy naphtha stream being a bottoms stream;
mixing hydrogen with said heavy naphtha stream containing di-alkenes and having a first end point, wherein a mole ratio of hydrogen to di-alkenes present in the heavy naphtha stream is from about 1:1 to about 5:1;
selectively hydrogenating said heavy naphtha stream over a hydrogenation catalyst to produce a heavy hydrogenated naphtha stream with a lower concentration of di-alkenes;
adding said lighter naphtha stream containing di-alkenes and having a second end point that is lower than the first end point to the heavy hydrogenated naphtha stream; and
selectively hydrogenating the heavy hydrogenated naphtha stream and the lighter naphtha stream over hydrogenation catalyst to produce a product naphtha stream depleted of di-alkenes.

2. The process of claim 1 wherein the cut point between said lighter naphtha stream and said heavy naphtha stream is between about 55° and about 75° C.

3. The process of claim 1 further comprising hydrodesulfurizing said product naphtha stream over a hydrodesulfurization catalyst.

4. The process of claim 1 further comprising contacting said naphtha stream with an alkaline stream to produce sulfides before the separation step.

5. The process of claim 1 further comprising separating said naphtha stream into a light naphtha stream, an intermediate naphtha stream which is said lighter naphtha stream, and said heavy naphtha stream.

6. The process of claim 5 further comprising selectively hydrogenating said light naphtha stream separately from selectively hydrogenating the heavy naphtha stream and the lighter hydrogenated naphtha stream to provide a hydrogenated light naphtha stream.

7. The process of claim 6 further comprising refluxing said hydrogenated light naphtha stream to said separation step.

8. The process of claim 5 further comprising contacting said light naphtha stream with an alkaline stream to produce sulfides.

9. A process for selectively hydrogenating naphtha comprising:
separating a naphtha stream into a light naphtha stream, an intermediate naphtha stream, and a heavy naphtha stream, said heavy naphtha stream being a bottoms stream;
mixing hydrogen with said heavy naphtha stream containing di-alkenes and having a first end point, wherein a mole ratio of hydrogen to di-alkenes present in the heavy naphtha stream is from about 1:1 to about 5:1;
selectively hydrogenating said heavy naphtha stream over a first bed of hydrogenation catalyst to produce a heavy hydrogenated naphtha stream with a lower concentration of di-alkenes;
adding said intermediate naphtha stream containing di-alkenes and having a second end point that is lower than the first end point to said heavy hydrogenated naphtha stream; and
selectively hydrogenating the heavy hydrogenated naphtha stream and said intermediate naphtha stream over a second bed of hydrogenation catalyst to produce a product naphtha stream depleted of di-alkenes.

10. The process of claim 9 wherein the cut point between said intermediate naphtha stream and said heavy naphtha stream is between about 55° and about 75° C.

11. The process of claim 9 further comprising hydrodesulfurizing said product naphtha stream over a hydrodesulfurization catalyst.

12. The process of claim 9 further comprising mixing said light naphtha stream with hydrogen and selectively hydrogenating said light naphtha stream to produce a hydrogenated light naphtha stream.

13. The process of claim 12 further comprising refluxing said hydrogenated light naphtha stream to said separation step.

14. The process of claim 9 further comprising contacting said naphtha stream with an alkaline stream to produce sulfides prior to said separation step.

15. The process of claim 9 further comprising contacting said light naphtha stream with an alkaline stream to produce sulfides.

16. A process for selectively hydrogenating naphtha comprising:
separating a debutanized naphtha stream into a lighter naphtha stream and a heavy naphtha stream;
mixing hydrogen with said heavy naphtha stream containing di-alkenes and having a first end point, wherein a mole ratio of hydrogen to di-alkenes present in the heavy naphtha stream is from about 1:1 to about 5:1;
selectively hydrogenating said heavy naphtha stream over a first bed of hydrogenation catalyst to produce a heavy hydrogenated naphtha stream with a lower concentration of di-alkenes;
adding said lighter naphtha stream containing di-alkenes and having a second end point that is lower than the first end point to the heavy hydrogenated naphtha stream; and
selectively hydrogenating the lighter naphtha stream and the heavy hydrogenated naphtha stream over a second bed of hydrogenation catalyst to produce a product naphtha stream depleted of di-alkenes.

17. The process of claim 16 further comprising contacting said naphtha stream with an alkaline stream to produce sulfides prior to said separation step.

18. The process of claim 16 further comprising separating said naphtha stream into a light naphtha stream, an intermediate naphtha stream which is said lighter naphtha stream, and said heavy naphtha stream.

19. The process of claim 16 further comprising selectively hydrogenating said light naphtha stream separately from selectively hydrogenating said heavy naphtha stream and said lighter hydrogenated naphtha stream to provide a hydrogenated light naphtha stream.

Assignees

• Uop Llc

Inventors

• Kumar Avnish
• Zink Steven F
• Banerjee Soumendra M

Classifications

• C10G45/32 Primary

  Selective hydrogenation of the diolefin or acetylene compounds · CPC title

• C10G65/06

  at least one step being a selective hydrogenation of the diolefins · CPC title

• C10G65/02 Primary

  plural serial stages only · CPC title

• C10G2300/1044

  Heavy gasoline or naphtha having a boiling range of about 100 - 180 °C · CPC title

• C10G65/00

  Treatment of hydrocarbon oils by two or more hydrotreatment processes only · CPC title