Removal of atmospheric pollutants from gas, related apparatus, processes and uses thereof
Methods related generally to the removal of atmospheric pollutants from the gas phase, are provided, as well as related apparatus, processes and uses thereof. A single-stage air scrubbing apparatus is provided that includes at least one reaction vessel, at least one introduction duct, and a turbulence component, wherein a residence time is sufficient to allow the conversion of at least one atmospheric pollution compound to at least one other compound, molecule or atom. In some embodiments, the at least one atmospheric pollution compound comprises nitrogen oxide, sulfur oxide or a combination thereof. Additionally, methods of removing atmospheric pollution compounds from a waste gas stream are disclosed that include introducing a waste gas stream and at least one additional gas stream, mist stream, liquid stream or combination thereof into a single-stage air scrubbing apparatus at a flow rate sufficient to allow for conversion of the at least one atmospheric pollution compound.
1. A system for scrubbing a waste gas of at least one of nitrogen oxides and sulfur oxides, comprising:
a reaction vessel having internal chamber;
an inlet in the reaction vessel for introducing chlorine dioxide into the internal chamber;
an inlet for introducing a stream of waste gas into the reaction vessel internal chamber, the waste gas containing at least one component selected from the group consisting of sulfur oxides and nitrogen oxides; and
wherein the chlorine dioxide is combined with the stream of waste gas to form a gaseous mixture as the waste gas passes through the internal chamber, and wherein gaseous mixture has a sufficient residence time within the reaction vessel to permit at least one component in the waste gas to be converted to a different chemical form for removal from the reaction vessel.
2. The system of claim 1 , further comprising one or more turbulence components disposed within the internal chamber to induce turbulence to at least one of the stream of waste gas and the gaseous mixture as it passes through the internal chamber.
3. The system of claim 2 , wherein the turbulence component is positioned within the internal chamber downstream of one or both of the waste gas stream inlet and the chlorine dioxide inlet.
4. The system of claim 2 , wherein the turbulence component is a static element fixed within the internal chamber selected from the group consisting of one or more vanes, baffels, blades, diffusers, tubes and combinations thereof.
5. The system of claim 2 , wherein the turbulence component is positioned within the internal chamber downstream from the waste gas inlet to induce turbulence to the waste gas before the waste gas is combined with the chlorine dioxide.
6. The system of claim 2 , wherein the turbulence component comprises a dynamic element within the internal chamber.
7. The system of claim 1 , wherein the reaction vessel includes a gas outlet in gas flow communication with the internal chamber.
8. The system of claim 1 , wherein the reaction vessel includes a liquid outlet for removing liquid from the internal chamber, wherein the liquid comprise the at least one component in the waste gas converted to a different chemical form.
9. The system of claim 1 , wherein the chlorine dioxide is provided within the internal chamber in a mist or liquid phase formed by dissolving chlorine dioxide gas in a liquid.
10. The system of claim 1 , wherein the chlorine dioxide is provided within the internal chamber in the form of a gas that is combined with the waste gas.
11. The system of claim 1 , wherein a turbulence component is disposed within the internal chamber and positioned downstream from the chlorine dioxide inlet.
12. The system of claim 11 , wherein the turbulence component is in the form of one or more fixed elements static within the internal chamber.
13. The system of claim 1 , wherein a turbulence component is placed in a duct upstream from a point where the waste gas enters the reaction vessel to induce turbulence to the waste gas before entering the internal chamber.
14. The system of claim 11 , wherein a turbulence component is positioned within the internal chamber at a position downstream from the chlorine dioxide inlet, and wherein the chlorine dioxide is in the form of a gas.
15. The system of claim 9 , wherein the liquid is a basic solution.
16. The system of claim 1 , wherein the residence time of the mixture of the waste gas and chlorine dioxide is from about 0.015 to 15 seconds.
17. The system of claim 16 , wherein the residence time is from about 0.05 to 0.3 seconds.
18. A method for scrubbing a waste gas, comprising,
introducing into a reaction vessel a waste gas containing at least one component selected from the group consisting of sulfur oxides, nitrogen oxides and combinations thereof;
introducing chlorine dioxide into the reaction vessel such that the chlorine dioxide mixes with the waste gas to form a gaseous mixture that passes through an internal chamber of the reaction vessel; and
wherein the gaseous mixture passes within the internal chamber for a residence time sufficient for the chlorine dioxide to react with the component to convert the component into at least one other compound, molecule or atom for removal from the reaction vessel.
19. The method as recited in claim 18 further comprising the step of inducing a turbulence to one or both of the waste gas stream and gaseous mixture by passing one or both of the waste gas stream and gaseous mixture along a turbulence component disposed within the internal chamber.