Ammonia-based desulfurization process and apparatus

• US 10,406,478 B2
• Filed: 06/26/2018
• Issued: 09/10/2019
• Est. Priority Date: 05/25/2017
• Status: Active Grant

• Current Assignee: Jiangnan Environmental Protection Group Inc.
• Original Assignee: Jiangnan Environmental Protection Group Inc.
• Inventors: Luo, Jing, Xu, Changxiang, Xu, Xiangjun, Luo, Yongying
• Primary Examiner(s): Vanoy, Timothy C
• Application Number:
  US16/018,386
• Publication Number:
  US 20180339267A1
• Time in Patent Office: 441 Days
• CPC Class Codes: B01D 2251/11 Air
• CPC Class Codes: B01D 2252/102 Ammonia
• CPC Class Codes: B01D 2258/0283 Flue gases
• CPC Class Codes: B01D 53/504 characterised by a specific device
• CPC Class Codes: B01D 53/507 by treating the gases with other liquids
• CPC Class Codes: B01D 53/78 with gas-liquid contact
• CPC Class Codes: Y02A 50/20 Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

Abstract

Apparatus and methods for desulfurization of a sulfur-oxide containing gas by treatment with ammonia containing liquids. The apparatus and methods may utilize two distinct circuits of two different ammonia containing liquids which are applied in two distinct chambers. The gas may be cooled prior to entry into the circuits. There may be fluid communication between the two circulation circuits.

Claims

1. A method of ammonia-based oxidative desulfurization comprising:

directing a current of sulfur dioxide containing gas through a vessel;

mixing, in an ammonia-mixing chamber, a liquid and an ammonia source to produce a first ammonia-containing liquid that has a first pH;

contacting, in an oxidation chamber, an oxygen-containing gas with a second ammonia-containing liquid that has a second pH that is lower than the first pH;

spraying the first ammonia-containing liquid in the vessel against the current;

after the spraying the first ammonia-containing liquid, recirculating the first ammonia-containing liquid to the ammonia-mixing chamber;

spraying the second ammonia-containing liquid in the vessel against the current;

after the spraying the second ammonia-containing liquid, recirculating the second ammonia-containing liquid to the oxidation chamber; and

transferring material between the oxidation chamber and the ammonia-mixing chamber through a balance hole defined in a partition between the oxidation chamber and the ammonia-mixing chamber.

2. The method of claim 1 wherein the transferring includes transferring at a location in a top surface of the ammonia-mixing chamber.

3. The method of claim 1 wherein the transferring includes transferring at a location in a lower third of a height of the ammonia-mixing chamber.

4. The method of claim 1 wherein the transferring includes transferring through the balance hole that is no more than 0.25 m².

5. The method of claim 1 wherein the transferring includes transferring through the balance hole that is no more than 0.1 m².

6. The method of claim 1 wherein the transferring includes transferring through the balance hole that is no more than 0.05 m².

7. The method of claim 1 wherein the transferring includes transferring through the balance hole that is no more than 0.01 m².

8. The method of claim 1 wherein the transferring includes transferring through the balance hole that is round.

9. The method of claim 1 wherein the transferring includes transferring through the balance hole that is rectangular.

10. The method of claim 1 wherein the transferring includes transferring through the balance hole that is square.

11. The method of claim 1 wherein the transferring includes transferring through the balance hole that is oval.

12. The method of claim 1 wherein the transferring includes transferring through the balance hole that is hexagonal.

13. The method of claim 1 wherein:

the mixing comprises receiving in the ammonia-mixing chamber, at a material transfer port disposed in a surface of the ammonia-mixing chamber, ammonia; and

the spraying the first ammonia-containing liquid comprises drawing, from the ammonia-mixing chamber, the first ammonia-containing liquid;

wherein;

the material transfer port is in fluid communication with an elongated conduit leading away from the ammonia-mixing chamber; and

the port is distant from the balance hole.

14. The method of claim 1 further comprising, before the spraying the first ammonia-containing liquid in the vessel against the current, cooling the current by contacting it with recirculated sprayed ammonia-containing liquid.

15. The method of claim 1 further comprising, before the spraying the first ammonia-containing liquid in the vessel against the current, cooling the current by contacting the current with ammonium sulfate slurry.

16. An apparatus for removing sulfur from a gas stream, the apparatus comprising:

a first sprayer circuit configured to spray a first liquid countercurrent to the gas stream, the first sprayer circuit including;

a first sprayer assembly; and

an ammonia-mixing chamber including;

an ammonia input port;

a first-liquid return port;

a first-liquid supply port configured to supply first liquid to the first sprayer assembly; and

a surface that defines a balance hole that places material from inside the ammonia-mixing chamber in diffusive communication with material from outside of the ammonia-mixing chamber, and

a second sprayer circuit configured to spray a second liquid countercurrent to the gas stream, the second sprayer circuit including;

a second sprayer assembly downstream, relative to the gas stream, from the first sprayer assembly; and

an oxidation chamber having;

a gas input configured for contacting an oxygen-containing gas with an ammonia-containing liquid in the oxidation chamber;

a second-liquid return port configured to receive second liquid after the second liquid is sprayed; and

a second-liquid supply port configured to supply second liquid to the second sprayer assembly.

17. The apparatus of claim 16 wherein the surface comprises a top of the ammonia-mixing chamber.

18. The apparatus of claim 16 wherein the balance hole is disposed in a lower third of a height of the ammonia-mixing chamber.

19. The apparatus of claim 16 wherein the balance hole is no more than 0.25 m².

20. The apparatus of-claim 16 wherein the balance hole is no more than 0.1 m².

21. The apparatus of claim 16 wherein the balance hole is no more than 0.05 m².

22. The apparatus of claim 16 wherein the balance hole is no more than 0.01 m².

23. The apparatus of claim 16 wherein the balance hole is round.

24. The apparatus of claim 16 wherein the balance hole is rectangular.

25. The apparatus of claim 16 wherein the balance hole is square.

26. The apparatus of claim 16 wherein the balance hole is oval.

27. The apparatus of claim 16 wherein the balance hole is hexagonal.

28. The apparatus of claim 16 wherein the ammonia-mixing chamber further includes a material transfer port that is disposed in a surface of the mixing chamber and is distant from the balance hole, the material transfer port in fluid communication with an elongated conduit leading away from the mixing chamber.

29. The apparatus of claim 28 wherein the distant port is a port closer to the balance hole than any other material transfer port in any surface of the mixing chamber, the any other port in fluid communication with an other elongated conduit leading away from the mixing chamber.

30. The apparatus of claim 16 further comprising a cooling chamber in which the gas stream is cooled, before spraying the first liquid countercurrent to the gas stream, by contacting the gas stream with recirculated sprayed ammonia-containing liquid.