Enhancement of Claus tail gas treatment by sulfur dioxide-selective membrane technology

Patent metadata

Field	Value
Publication number	US-10106410-B2
Application number	US-201715455847-A
Country	US
Kind code	B2
Filing date	Mar 10, 2017
Priority date	Mar 10, 2017
Publication date	Oct 23, 2018
Grant date	Oct 23, 2018

Abstract

A method for increasing sulfur recovery from an acid gas feed comprising the steps of introducing the acid gas feed and a sulfur dioxide enriched air stream to a Claus process to produce a product gas stream, introducing the product gas stream to a thermal oxidizer to produce a flue gas stream, cooling the flue gas stream to produce a cooled take-off stream, separating the cooled take-off stream into a saturated gas stream, heating the saturated gas stream to produce a membrane gas stream, introducing the membrane gas stream to a membrane sweeping unit, the membrane sweeping unit comprises a membrane, the sulfur dioxide in the membrane gas stream permeates the membrane of the membrane sweeping unit, introducing a sweep air stream, the sweep air stream collects the sulfur dioxide to create the sulfur dioxide enriched air stream.

First claim

What is claimed:

1. A method for increasing sulfur recovery from an acid gas feed, the method comprising the steps of:
introducing the acid gas feed and a sulfur dioxide enriched air stream to a Claus process to produce a product gas stream and a recovered sulfur stream, wherein the acid gas feed comprises hydrogen sulfide, wherein the hydrogen sulfide is present in a hydrogen sulfide concentration, wherein the sulfur dioxide enriched air stream comprises sulfur dioxide and air;
introducing the product gas stream to a thermal oxidizer to produce a flue gas stream, the thermal oxidizer configured to convert sulfur containing compounds in the product gas stream to sulfur dioxide;
cooling the flue gas stream in a cooler to produce a cooled take-off stream;
separating the cooled take-off stream in a liquid-gas separation unit to produce a condensed water and a saturated gas stream, wherein the saturated gas stream comprises sulfur dioxide;
heating the saturated gas stream in a heater to produce a membrane gas stream;
introducing the membrane gas stream to a membrane sweeping unit, wherein the membrane sweeping unit comprises a membrane, wherein the membrane sweeping unit is configured to produce a sulfur dioxide depleted stream, wherein the sulfur dioxide in the membrane gas stream permeates the membrane of the membrane sweeping unit to a permeate side; and
introducing a sweep air stream to the permeate side, wherein the sweep air stream collects the sulfur dioxide that permeates the membrane of the membrane sweeping unit to create the sulfur dioxide enriched air stream.

2. The method of claim 1 , further comprising the step of feeding the sulfur dioxide depleted stream to an incinerator stack.

3. The method of claim 1 , further comprising the steps of heating the sulfur dioxide depleted stream in a reheater to produce a heated stack feed, wherein the heated stack feed is at a stack temperature; and
feeding the heated stack feed to an incinerator stack.

4. The method of claim 1 , wherein the membrane is an [emim][BF4] ionic liquid supported on a polyethersulfone.

5. The method of claim 1 , wherein the membrane is selected from the group consisting of polydimethylsiloxane (PDMS), polyphosphazenes, PEBAX® (polyether block amide), polyamide-polyether block copolymers, cellulose acetate, cellulose acetate impregnated with TEG-DME, cellulose diacetate, cellulose triacetate, Nafion® 117 (perfluorosulfonic acid), rubbery Nafion® (perfluorosulfonic acid), sulfonated polyimides, sulfonated polymers, supported ionic liquid membranes (SILMs), polycarbonate, membrane contactors, polyethylene glycol (PEG), polyacrylate, sulfolane, polytrimethylsilyl methyl methacrylate (PTMSMMA), and 3-methylsulfolane blend membranes.

6. The method of claim 1 , wherein the hydrogen sulfide concentration is greater than 25%.

7. The method of claim 1 , wherein a sulfur recovery is greater than 99.2 wt %.

8. An apparatus for increasing sulfur recovery from an acid gas feed, the apparatus comprising:
a Claus process, the Claus process configured to receive the acid gas feed and a sulfur dioxide enriched air stream to produce a product gas stream and a recovered sulfur stream, wherein the acid gas feed comprises hydrogen sulfide, wherein the hydrogen sulfide is present in a hydrogen sulfide concentration, wherein the sulfur dioxide enriched air stream comprises sulfur dioxide and air, wherein the product gas stream comprises sulfur containing compounds;
a thermal oxidizer, the thermal oxidizer configured to convert the sulfur containing compounds to sulfur dioxide to produce a flue gas stream, wherein the flue gas stream comprises sulfur dioxide, water vapor, oxygen, nitrogen, and carbon dioxide;
a cooler, the cooler configured to reduce the temperature of the flue gas stream below the dew point temperature of water to produce a cooled take-off stream;
a gas-liquid separator unit, the gas-liquid separator unit configured to condense the water vapor in the cooled take-off stream to produce a condensed water and a saturated gas stream, wherein the saturated gas stream comprises sulfur dioxide;
a heater, configured to heat the saturated gas stream to produce a membrane gas stream; and
a membrane sweeping unit, wherein the membrane sweeping unit comprises a membrane, wherein the membrane sweeping unit is configured to produce a sulfur dioxide depleted stream, wherein the sulfur dioxide in the membrane gas stream permeates the membrane of the membrane sweeping unit to a permeate side, wherein a sweep air stream fed to the permeate side of the membrane sweeping unit is operable to collect the sulfur dioxide that permeates the membrane of the membrane sweeping unit to create the sulfur dioxide enriched air stream.

9. The apparatus of claim 8 , further comprising an incinerator stack, the incinerator stack configured to disseminate the sulfur dioxide depleted stream to the atmosphere.

10. The apparatus of claim 8 , wherein the membrane is an [emim][BF4] ionic liquid supported on a polyethersulfone.

11. The apparatus of claim 8 , wherein the membrane is selected from the group consisting of polydimethylsiloxane (PDMS), polyphosphazenes, PEBAX® (polyether block amide), polyamide-polyether block copolymers, cellulose acetate, cellulose acetate impregnated with TEG-DME, cellulose diacetate, cellulose triacetate, Nafion® 117 (perfluorosulfonic acid), rubbery Nafion® (perfluorosulfonic acid), sulfonated polyimides, sulfonated polymers, supported ionic liquid membranes (SILMs), polycarbonate, membrane contactors, polyethylene glycol (PEG), polyacrylate, sulfolane, polytrimethylsilyl methyl methacrylate (PTMSMMA), and 3-methylsulfolane blend membranes.

12. The apparatus of claim 8 , wherein the hydrogen sulfide concentration is greater than 25%.

13. The apparatus of claim 8 , wherein a sulfur recovery is greater than 99.2 wt %.

14. The apparatus of claim 8 , wherein the Claus process comprises a thermal stage and a catalytic stage.

Assignees

• Saudi Arabian Oil Co

Inventors

• Ballaguet Jean-Pierre R
• Vaidya Milind M
• Charry-Prada Iran D
• Duval Sebastien A

Classifications

• Y02C20/30

  of perfluorocarbons [PFC], hydrofluorocarbons [HFC] or sulfur hexafluoride [SF6] · CPC title

• B01D2257/302

  Sulfur oxides · CPC title

• B01D53/228

  characterised by specific membranes · CPC title

• B01D2257/304

  Hydrogen sulfide · CPC title

• C01B17/0447

  Separation of the obtained sulfur · CPC title