Ammonia-based desulfurization process and apparatus

• US 10,413,865 B2
• Filed: 11/13/2018
• Issued: 09/17/2019
• 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:
  US16/188,816
• Publication Number:
  US 20190076780A1
• Time in Patent Office: 308 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:

receiving a current of sulfur dioxide containing gas;

directing the current 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; and

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

2. The method of claim 1 wherein the receiving comprises receiving the gas current from a coal combustion process.

3. The method of claim 1 wherein the receiving comprises receiving the gas current from a fluid catalytic cracking process.

4. The method of claim 1 wherein the ammonia source comprises anhydrous ammonia.

5. The method of claim 1 wherein the ammonia source comprises gaseous ammonia.

6. The method of claim 1 wherein the ammonia source comprises aqueous ammonia.

7. The method of claim 1 further comprising, after the spraying the first and second ammonia-containing liquids, mixing the first and second ammonia-containing liquids to form a mixed reflux liquid.

8. The method of claim 7 further comprising circulating the reflux liquid into the oxidation chamber.

9. The method of claim 7 further comprising passing between 30% and 85% of the reflux liquid into the ammonia-mixing chamber.

10. The method of claim 7 further comprising circulating between 70% and 15% of the reflux liquid into the oxidation chamber.

11. The method of claim 7 further comprising, before a subsequent spraying of the second ammonia-containing liquid in the vessel against the current, cooling the current by contacting the current with recirculated sprayed ammonia-containing liquid.

12. The method of claim 1 wherein the oxygen-containing gas is pure molecular oxygen.

13. The method of claim 1 wherein the oxygen-containing gas is oxygen-poor air.

14. The method of claim 1 wherein the oxygen-containing gas is oxygen-enriched air.

15. The method of claim 1 wherein the oxidation rate of the first ammonia-containing liquid within the ammonia-mixing chamber is in the range 93% to 99.5%.

16. The method of claim 1 wherein the oxidation rate of the second ammonia-containing liquid within the oxidation chamber is greater than or equal to 98.5%.

17. The method of claim 1 wherein the spraying the first ammonia-containing liquid in the vessel against the current occurs before the spraying the second ammonia-containing liquid in the vessel against the current.

18. 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;

wherein;

the ammonia-mixing chamber has a first cross-sectional area;

the oxidation chamber has a second cross-sectional area; and

the second cross-sectional area is larger than the first cross-sectional area.

19. The apparatus of claim 18 wherein the oxidation chamber and the ammonia-mixing chamber are in fluid communication.

20. The apparatus of claim 19 wherein the oxidation chamber and the ammonia-mixing chamber are in fluid communication via the balance hole, the balance hole disposed in a partition between the oxidation chamber and the ammonia-mixing chamber.

21. The apparatus of claim 19 wherein the oxidation chamber and the ammonia-mixing chamber are in fluid communication via a conduit extending between the oxidation chamber and the ammonia-mixing chamber.

22. The apparatus of claim 18 further comprising a conduit having a first end and a second end, the first end configured to be joined to a primary spray absorption section upstream from the first spray assembly, the second end being bifurcated and configured to be joined to:

the oxidation chamber; and

the ammonia-mixing chamber.

23. The apparatus of claim 18 wherein the surface is a top of the ammonia-mixing chamber.

24. The apparatus of claim 18 wherein the first cross-sectional area is about 75% of the second cross-sectional area.

25. The apparatus of claim 18 wherein the first cross-sectional area is about 85% of the second cross-sectional area.

26. The apparatus of claim 18 wherein the first cross-sectional area is no more than 60% of the second cross-sectional area.

27. The apparatus of claim 18 wherein the first cross-sectional area is no more than 40% of the second cross-sectional area.

28. The apparatus of claim 18 wherein the first cross-sectional area is within the range 18-50% of the second cross-sectional area.

29. The apparatus of claim 18 wherein the first cross-sectional area is within the range 8-40% of the second cross-sectional area.

30. The apparatus of claim 18 wherein the first cross-sectional area is within the range 10-35% of the second cross-sectional area.