Sulfur recovery process for treating low to medium mole percent hydrogen sulfide gas feeds with BTEX in a claus unit

Patent metadata

Field	Value
Publication number	US-9981848-B2
Application number	US-201715418936-A
Country	US
Kind code	B2
Filing date	Jan 30, 2017
Priority date	Apr 16, 2014
Publication date	May 29, 2018
Grant date	May 29, 2018

Abstract

An enrichment apparatus and process for enriching a hydrogen sulfide concentration in an acid gas stream to create a hydrogen sulfide rich stream for feed to a Claus. The enrichment apparatus comprises a hydrocarbon selective separation unit operable to separate the acid gas stream into a hydrocarbon rich stream and a purified acid gas stream, wherein the acid gas stream comprises hydrogen sulfide, carbon dioxide, and hydrocarbons, a hydrogen sulfide selective separation unit operable to separate the purified acid gas stream to create the hydrogen sulfide rich stream and a hydrogen sulfide lean stream, the hydrogen sulfide rich stream having a concentration of hydrogen sulfide, and the Claus unit operable to recover sulfur from the carbon dioxide lean stream. The enrichment apparatus can include a carbon dioxide selective separation unit in fluid communication with the hydrogen sulfide selective separation unit, operable to separate the hydrogen sulfide rich stream.

First claim

What is claimed:

1. An enrichment apparatus for enriching a hydrogen sulfide concentration in an acid gas stream to create a hydrogen sulfide rich stream for feed to a Claus unit, the enrichment apparatus comprising:
a hydrocarbon selective separation unit, the hydrocarbon selective separation unit operable to separate the acid gas stream into a hydrocarbon rich stream and a purified acid gas stream,
wherein the acid gas stream comprises aromatics selected from the group consisting of benzene, toluene, ethyl benzene, xylenes and combinations thereof; and

a hydrogen sulfide selective separation unit in fluid communication with the hydrocarbon selective separation unit, the hydrogen sulfide selective separation unit operable to separate the purified acid gas stream to create the hydrogen sulfide rich stream and a hydrogen sulfide lean stream, the hydrogen sulfide rich stream having a concentration of hydrogen sulfide.

2. The enrichment apparatus of claim 1 , further comprising:
a carbon dioxide selective separation unit in fluid communication with the hydrogen sulfide selective separation unit, the carbon dioxide selective separation unit operable to separate the hydrogen sulfide rich stream to create a carbon dioxide rich permeate and a hydrogen sulfide rich retentate, the hydrogen sulfide rich retentate having a concentration of hydrogen sulfide.

3. The enrichment apparatus of claim 2 , wherein the carbon dioxide selective separation unit is selected from the group consisting of an amorphous fluoroplastic membrane, an amorphous perfluoropolymer membrane, a random fluorocopolymer membrane, a perfluorinated copolymer membrane, and combinations thereof.

4. The enrichment apparatus of claim 1 , further comprising
a second hydrogen sulfide selective separation unit in fluid communication with the hydrogen sulfide selective separation unit, the second hydrogen sulfide selective separation unit operable to separate the hydrogen sulfide rich stream to create an enriched hydrogen sulfide stream and a carbon dioxide retentate.

5. The enrichment apparatus of claim 1 , wherein the hydrogen sulfide selective separation unit is selected from the group consisting of polyphosphazene type polymer membranes, polyether-polyamide copolymer membranes, ionic liquid membranes, ionic liquid membrane contactors, and combinations thereof.

6. The enrichment apparatus of claim 5 , wherein the second hydrogen sulfide selective separation unit is selected from the group consisting of polyphosphazene type polymer membranes, polyether-polyamide copolymer membranes, ionic liquid membranes, ionic liquid membrane contactors, and combinations thereof.

7. The enrichment apparatus of claim 1 , wherein the hydrocarbon selective separation unit comprises a PDMS type rubbery polymer membrane.

8. The enrichment apparatus of claim 1 , wherein the acid gas stream further comprises contaminants selected from the group consisting of mercaptans, thiols, carbonyl sulfide, carbon disulfide, and combinations thereof.

9. The enrichment apparatus of claim 1 , wherein the hydrogen sulfide concentration in the acid gas stream is between 15% to 55% by volume.

10. The enrichment apparatus of claim 1 , wherein the concentration of hydrogen sulfide in the hydrogen sulfide rich stream is greater than 55% by volume.

11. The enrichment apparatus of claim 1 , further including a mixer operable to mix the hydrocarbon rich stream and the hydrogen sulfide rich stream into a feed stream for a furnace of the Claus unit.

12. The enrichment apparatus of claim 11 , wherein the concentration of hydrogen sulfide in the feed stream for the furnace of the Claus unit is greater than 25% by volume.

13. A process for enriching a hydrogen sulfide concentration in an acid gas stream to create a hydrogen sulfide rich stream for feeding to a Claus unit, the process comprising the steps of:
feeding the acid gas stream to a hydrocarbon selective separation unit, the acid gas stream comprising hydrogen sulfide, carbon dioxide, and hydrocarbons;
separating the acid gas stream in the hydrocarbon selective separation unit to create a hydrocarbon rich stream and a purified acid gas stream, wherein the hydrocarbon rich stream comprises aromatics selected from the group consisting of benzene, toluene, ethyl benzene, xylene, and combinations thereof;
feeding the purified acid gas stream to a hydrogen sulfide selective separation unit fluidly connected to the hydrocarbon selective separation unit, the hydrogen sulfide selective separation unit operable to separate the purified acid gas stream; and
separating the purified acid gas stream in the hydrogen sulfide selective separation unit to create the hydrogen sulfide rich stream and a hydrogen sulfide lean stream, the hydrogen sulfide rich stream having a concentration of hydrogen sulfide.

14. The process of claim 13 , further comprising the steps of:
feeding the hydrogen sulfide rich stream to a carbon dioxide selective separation unit in fluid communication with the hydrogen sulfide selective separation unit, the carbon dioxide selective separation unit operable to separate the hydrogen sulfide rich stream;
separating the hydrogen sulfide rich stream to create a carbon dioxide rich permeate and a hydrogen sulfide rich retentate, the hydrogen sulfide rich retentate having a concentration of hydrogen sulfide; and
feeding the hydrogen sulfide rich retentate to the furnace of the Claus unit.

15. The process of claim 14 , wherein the carbon dioxide selective separation unit is selected from the group consisting of an amorphous fluoroplastic membrane, an amorphous perfluoropolymer membrane, a random fluorocopolymer membrane, a perfluorinated copolymer membrane, and combinations thereof.

16. The process of claim 13 , further comprising the steps of:
feeding the hydrogen sulfide rich stream to a second hydrogen sulfide selective separation unit fluidly connected to hydrogen sulfide selective separation unit, the second hydrogen sulfide selective separation unit operable to separate the hydrogen sulfide rich stream; and
separating the hydrogen sulfide rich stream in the second hydrogen sulfide selective separation unit to create an enriched hydrogen sulfide stream and a carbon dioxide retentate.

17. The process of claim 16 , further comprising the steps of:
mixing the hydrocarbon rich stream and the enriched hydrogen sulfide stream to create a mixed furnace feed stream; and
feeding the mixed furnace feed stream to a furnace of the Claus unit.

18. The process of claim 17 , wherein the mixed furnace feed stream has a hydrogen sulfide concentration of at least 25% by volume.

19. The process of claim 13 , wherein the hydrogen sulfide selective separation unit is selected from the group consisting of polyphosphazene type polymer membranes, polyether-polyamide copolymer membranes, ionic liquid membranes, ionic liquid membrane contactors, and combinations thereof.

20. The process of claim 13 , wherein the hydrocarbon selective separation unit comprises a PDMS type rubbery polymer membrane.

21. The process of claim 13 , wherein the acid gas stream further comprises contaminants is selected from the group consisting of mercaptans, thiols, carbonyl sulfide, carbon disulfide, and combinations thereof.

22. The process of claim 13 , wherein the hydrogen sulfide concentration in the acid gas stream is between 15% to 55% by volume.

23. The process of claim 13 , wherein the hydrogen sulfide rich stream has

Assignees

• Saudi Arabian Oil Co

Inventors

• Ballaguet Jean-Pierre R
• Vaidya Milind M
• Duval Sebastien A
• Harale Aadesh
• Khawajah Anwar H
• Tammana Veera Venkata R

Classifications

• B01D2257/504

  Carbon dioxide · CPC title

• B01D2257/7027

  Aromatic hydrocarbons · CPC title

• B01D53/047

  Pressure swing adsorption · CPC title

• B01D53/226 Primary

  in serial connexion · CPC title

• C07C7/11

  by absorption, i.e. purification or separation of gaseous hydrocarbons with the aid of liquids · CPC title