Membrane separation for sulfur reduction

• US 7,048,846 B2
• Filed: 03/06/2003
• Issued: 05/23/2006
• Est. Priority Date: 02/16/2001
• Status: Expired due to Term

• Current Assignee: W.R. Grace & Co.-Conn. (WR Grace & Company)
• Original Assignee: W.R. Grace & Co.-Conn. (WR Grace & Company)
• Inventors: Wormsbecher, Richard Franklin, Lesemann, Markus, White, Lloyd Steven
• Primary Examiner(s): GRIFFIN, WALTER DEAN
• Application Number:
  US10/382,409
• Publication Number:
  US 20030173255A1
• Time in Patent Office: 1,174 Days
• Field of Search: 208/211, 208/208.R, 208/301, 585/818, 210/649
• US Class Current: 208/208.00R
• CPC Class Codes: C10G 31/11 by dialysis
• CPC Class Codes: C10G 53/02 plural serial stages only
• CPC Class Codes: C10G 53/08 including at least one sorption step
• CPC Class Codes: C10G 67/02 plural serial stages only

Abstract

A membrane process for the removal of sulfur species from a naphtha feed, in particular, a FCC light cat naphtha, without a substantial loss of olefin yield is disclosed. The process involves contacting a naphtha feed stream with a membrane having sufficient flux and selectivity to separate a sulfur deficient retentate fraction from a sulfur enriched permeate fraction, preferably, under pervaporation conditions. Sulfur deficient retentate fractions are useful directly into the gasoline pool. Sulfur-enriched permeate fractions are rich in sulfur containing aromatic and nonaromatic hydrocarbons and are further treated with conventional sulfur removal technologies, e.g. hydrotreating, to reduce sulfur content. The process of the invention provides high quality naphtha products having a reduced sulfur content and a high content of olefin compounds.

Claims

1. A method for lowering the sulfur content of a naphtha hydrocarbon feed stream while substantially maintaining the yield of olefin compounds in the feed stream, said method comprising

i) contacting a naphtha feed with a membrane separation zone, said separation zone containing a membrane having a sufficient flux and selectivity to separate a sulfur-enriched permeate fraction and a sulfur deficient retentate fraction, said sulfur deficient retentate fraction having a sulfur content of less than 100 ppm sulfur and comprising at least 50 wt % of olefins present in the naphtha feed under pervaporation conditions, said membrane having a sulfur enrichment factor of greater than 1.5, said naphtha feed being selected from the group consisting of a light naphtha, an intermediate naphtha, a coker naphtha, a straight run naphtha and mixtures thereof, and comprising sulfur containing aromatic hydrocarbons, sulfur containing non-aromatic hydrocarbon and olefin compounds, said sulfur enriched permeate fraction being enriched in sulfur containing aromatic hydrocarbons and sulfur containing non-aromatic hydrocarbons as compared to the naphtha feed;

ii) recovering the sulfur deficient retentate fraction as a product stream;

iii) subjecting the sulfur enriched permeate fraction to a non-membrane process to reduce sulfur content; and

iv) recovering a reduced sulfur permeate product stream.

2. The method of claim 1 wherein the membrane is an asymmetric membrane selected from the group consisting of a polyimide membrane, a polyureaurethane membrane and a polysiloxane membrane.

3. The method of claim 1 wherein the membrane is a polyimide membrane.

4. The method of claim 1 wherein the membrane is a polyurea urethane membrane.

5. The method a claim 1 wherein the membrane is a polysiloxane membrane.

6. The method of claim 1 wherein the sulfur content of the sulfur deficient fraction is less than 50 ppm.

7. The method of claim 1 wherein the sulfur content of the sulfur deficient retentate fraction is less than 30 ppm.

8. The method of claim 1 wherein the naphtha feed stream is cracked naphtha.

9. The method of claim 8 wherein the naphtha is a FCC naphtha.

10. The method of claim 9 wherein the naphtha is a FCC light cat naphtha having a boiling range from about 50°

C. to about 105°

C.

11. The method of claim 1 wherein the naphtha is a coker naphtha.

12. The method of claim 1 wherein the naphtha is a straight run naphtha.

13. The method of claim 1 wherein the sulfur deficient retentate fraction comprises at least 50 wt % of the total feed.

14. The method of claim 13 wherein the sulfur deficient retentate fraction comprises at least 70 wt % of the total feed.

15. The method of claim 1 wherein the non-membrane process is a hydrotreating process to reduce sulfur content.

16. The method of claim 1 wherein the non-membrane process is an adsorption process to reduce sulfur content.

17. The method of claim 1 wherein the non-membrane process is a catalytic distillation process to reduce sulfur content.

18. The method of claim 1 wherein the membrane has a sulfur enrichment factor of greater than 2.

19. The method of claim 1 wherein the membrane has a sulfur enrichment factor ranging from about 2 to about 20.

20. The method of claim 1 wherein the total amount of olefin compounds in the retentate product stream and the reduced sulfur permeate product stream is from about 50 to about 90 wt % of olefin compounds present the feed.

21. The method of claim 1 further comprising combining the sulfur deficient retentate product stream and the reduced sulfur permeate product stream.

22. A method for lowering the sulfur content of a naphtha hydrocarbon feed stream while substantially maintaining the yield of olefin compounds in the feed stream, said method comprising

i) contacting a naphtha feed with a membrane separation zone, said separation zone containing a membrane having a sufficient flux and selectivity to separate a sulfur-enriched permeate fraction and a sulfur deficient retentate fraction having a sulfur content of less than 100 ppm sulfur, said sulfur deficient retentate fraction comprising at least 50 wt % of the naphtha feed and at least 50 wt % of olefins present in the naphtha feed under pervaporation conditions, said membrane having a sulfur enrichment factor of greater than 1.5, said naphtha feed being selected from the group consisting of a light naphtha, an intermediate naphtha, a coker naphtha, a straight run naphtha and mixtures thereof, and comprising sulfur containing aromatic hydrocarbons, sulfur containing non-aromatic hydrocarbons and olefin compounds, said sulfur enriched permeate fraction being enriched in sulfur containing aromatic hydrocarbons and sulfur containing non-aromatic hydrocarbons as compared to the naphtha feed;

ii) recovering the sulfur deficient retentate fraction as a product stream;

iii) subjecting the sulfur enriched permeate fraction to a non-membrane process to reduce sulfur content; and

iv) recovering a reduced sulfur permeate product stream.