Combustion NOx reduction method

1. A method of increasing the droplet half-life of water reagent droplets in a stream injected into a droplet environment having a droplet environment temperature within a combustion furnace having a combustion space, the water reagent droplets comprising water and at least one reagent solute, the method comprising the steps of:

a) increasing the relative humidity of the droplet environment in the furnace through the injection of a liquid humidifying agent in a separate stream into the combustion space wherein said humidifying injection is performed substantially simultaneously with the droplet injection; and

b) adjusting the injection location and injection rate of the humidifying agent to improve effectiveness of the reagent solute by increasing the efficiency of a reaction of the reagent within the furnace to reduce the evaporation rate of the droplets and increase the half-life of the droplets in the combustion furnace.

2. The method of claim 1 , further including the step of adjusting the humidification agent injection rate to retard reagent availability until the droplets reach the furnace location where the furnace temperature is between about 1600 degrees F. (about 871 degrees C.) and about 2600 degrees F. (about 1427 degrees C).

3. The method of claim 1 , wherein the humidifying agent includes water.

4. The method of claim 1 , further including the step of dispersing the humidifying agent in the droplet environment through the injection of high-velocity secondary air.

5. The method of claim 4 , wherein the high-velocity secondary air and humidifying agent are injected in a co-axial manner.

6. The method of claim 4 , wherein the high-velocity secondary air is injected in a coordinated, reinforcing, tangential manner.

7. The method of claim 1 , wherein the humidifying agent is injected at an injection point selected from the group consisting of prior to reagent droplet injection, proximal to reagent droplet injection, after reagent droplet injection, and combinations thereof.

8. The method of claim 1 , wherein the water reagent droplets contain at least one NO x -reducing reagent.

9. The method of claim 8 , wherein the NO x -reducing reagent is selected from the group consisting of NH 3 -releasing reagents.

10. The method of claim 9 , wherein the NO x -reducing reagent is urea.

11. The method of claim 10 , wherein the urea is greater than about 20% aqueous urea w/w.

12. The method of claim 1 , wherein the water droplets contain at least one SO x -reducing reagent.

13. The method of claim 12 , wherein the SO x -reducing reagent is selected from the group consisting of bases.

14. The method of claim 13 , wherein the SO x -reducing reagent is selected from the group consisting of alkaline carbonates, such as lime, limestone; hydrated lime; quick lime; soda, trona and combinations thereof.

15. The method of claim 1 , further including the step of adjusting the humidification agent injection rate to retard reagent availability until the droplets are proximal to a catalyst.

16. A method for reducing NOx in a combustion furnace, the method steps comprising:

a) injecting water into a combustion space of the combustion furnace in a liquid stream;

b) injecting high-velocity air in the path of the injected water to disperse and evaporate the water; thereby humidifying and cooling a space in the combustion furnace to form a humidified space; and

c) injecting a NOx-reducing agent dissolved in water in a separate stream into the humidified space in the combustion furnace substantially simultaneously with said water injection in a manner to form droplets, the droplets having an droplet environment and the droplet environment having a droplet environment temperature; wherein the humidification and cooling of the droplet environment extends the droplet half-life in the combustion furnace to permit the reagent to reach the desired reaction location in the furnace; thereby reducing the NOx emissions of the combustion furnace.

17. A method for reducing SOx in a combustion furnace, the method steps comprising:

a) injecting water into a combustion space of the combustion furnace in a liquid stream;

b) injecting high-velocity air in the path of the injected water to disperse and evaporate the water; thereby humidifying and cooling a space in the combustion furnace to provide a humidified and cooled space; and

c) injecting a SOx-reducing agent dissolved in water in a separate stream into the humidified space in the combustion furnace substantially simultaneously with said water injection in a manner to form droplets, the droplets having a droplet environment; wherein the humidification and cooling of the droplet environment extends the droplet half-life in the combustion furnace to permit the reagent to reach the desired reaction location in the furnace; thereby reducing the SOx emissions of the combustion furnace.

18. A method of increasing the half-life of water reagent droplets in a droplet environment having a temperature in a combustion furnace comprising the steps of:

a) injecting the water reagent droplets into a droplet environment from a reagent stream;

b) injecting a liquid humidifying agent into the combustion furnace from a separate, reagent free stream substantially simultaneously with said water reagent droplet injection to increase the relative humidity and reduce the temperature of the droplet environment in the furnace; and

c) adjusting an injection location and an injection rate of the humidifying agent to improve effectiveness of the reagent solute by increasing the half-life of the droplets in the combustion furnace.

19. The method of claim 18 further including changing the injection rate of the liquid humidifying agent to accommodate changing furnace loads.

20. The method of claim 19 further including the step of dispersing the humidifying agent in the droplet environment through the injection of high-velocity secondary air.

21. The method of claim 18 further comprising retarding reagent availability until the water reagent droplets reach a furnace location where the temperature is between about 1600 degrees F. (about 871 degrees C.) and about 2600 degrees F. (about 1427 degrees C.).