Multifunctional abatement of air pollutants in flue gas
View Patent ↗An apparatus and a method that uses generated alkaline, alkaline-earth, and/or silica/alumina aerosols as a multifunctional additive to scavenge sulfur oxides in flue gas, minimize poisoning effects of sulfur oxides on mercury sorbent performance, and enhance particulate matter capture in electrostatic precipitators and other particulate filter devices by conditioning the fly ash.
1. A method for controlling particulate and sulfurous emissions in a gas stream of a fuel fired system comprising:
providing a main flue coupled to an outlet of the fuel fired system for carrying the gas stream
producing a reactive aerosol in a chamber of a thermal aerosol generator by nucleation, condensation and particle coagulation, wherein the thermal aerosol generator is connected, via a passageway to the main flue;
introducing the reactive aerosol to the main flue via the passageway, whereby at least a portion of the reactive aerosol is reacted via chemical reaction with particulate sulfurous species in the gas stream, producing reacted aerosol particles; and
removing at least a portion of the reacted aerosol particles from the main flue.
2. The method according to claim 1 , wherein producing a reactive aerosol further comprises:
introducing a precursor to the chamber; and
heating the precursor in the chamber to a temperature of at least about 575° F. (300° C.).
3. The method according to claim 2 , wherein the precursor is selected from the group consisting of: NaBr, CaBr 2 , Na 2 CO 3 , NaNO 3 , MgBr 2 , NaCl, calcium acetate, calcium magnesium acetate, sodium acetate, SiCl 4 , Al(iPrO) 3 alkaline, alkaline-earth compounds, silica/alumina-based materials, and combinations thereof.
4. The method according to claim 2 , wherein heating the precursor comprises heating to a temperature of at least about 1200° F. (688° C.).
5. The method according to claim 2 , wherein heating the precursor comprises heating to a temperature of at least about 1620° F. (882° C.).
6. The method according to claim 2 , wherein heating the precursor comprises heating to a temperature of at least about 2000° F. (1093° C.).
7. The method according to claim 1 , further comprising introducing a sorbent to the main flue, whereby the sorbent captures mercury from the gas stream.
8. The method according to claim 7 , wherein the reactive aerosol and the sorbent are introduced into the main flue via the passageway.
9. The method according to claim 7 , wherein the sorbent is a carbonaceous material selected from the group consisting of carbon black, char, soot, and combinations thereof.
10. The method according to claim 1 , further comprising providing an air preheater in the main flue, and introducing the reactive aerosol to the main flue between the fuel fired system and the air preheater.
11. The method according to claim 10 , further comprising providing a pollution control device downstream of the air preheater.
12. The method according to claim 11 , wherein the pollution control device is selected from the group consisting of electrostatic precipitators, fabric filters, wet flue gas desulfurization devices, spray dryers, baghouses, and combinations thereof.
13. The method according to claim 1 , further comprising providing an air preheater in the main flue, and supplying the reactive aerosol and a sorbent to the main flue between the fuel fired system and the air preheater.
14. The method according to claim 13 , further comprising providing a sorbent bed downstream of the location where the reactive aerosol is supplied to the main flue.
15. The method according to claim 1 , further comprising providing an air preheater in the main flue, wherein the passageway is connected to the main flue between the air preheater and a pollution control device.
16. A The method according to claim 15 , wherein the pollution control device is a particulate capture device.
17. The method according to claim 16 , wherein the particulate capture device comprises an electrostatic particulate capture device.
18. The method according to claim 1 , wherein producing a reactive aerosol comprises producing an aerosol that is less than about 2 μm in diameter.
19. The method according to claim 1 , wherein producing a reactive aerosol comprises producing an aerosol that is less than about 1 μm in diameter.
20. The method according to claim 2 , wherein the precursor is introduced to the chamber as a phase selected from the group consisting of liquids, solids, vapors, and combinations thereof.
21. The method according to claim 16 , wherein the particulate capture device comprises a fabric filter device.
22. The method according to claim 16 , wherein the particulate capture device comprises a wet flue gas desulfurization (WFGD) device.
23. The method of claim 1 further comprising introducing dissociated halogen species into the main flue.
24. The method of claim 23 wherein the dissociated halogen species are introduced into the passageway downstream of the aerosol generator.