Combustion flue gas NO
Combustion flue gas containing NO X and SO X is treated to remove NO X in a multistep system in which NO X is reduced in the flue gas stream via selective catalytic reduction or selective non-catalytic reduction with ammonia or an ammonia-forming compound, followed treatment with hydrogen peroxide to remove residual ammonia and, optionally, treatment with an alkali reagent to reduce residual NO X in the flue gas stream. The NO X -depleted flue gas stream may also be subjected to a desulfurization treatment for removal of SO X .
1. A method for removing NOx from a flue gas stream comprising
subjecting an electric utility power plant combustion flue gas stream containing NOx to a selective catalytic reduction operation or selective non-catalytic reduction operation by injecting ammonia or an ammonia-forming compound into the flue gas stream as an agent for reducing the NOx, wherein an excess of ammonia is introduced to yield a flue gas stream containing unreacted residual ammonia and a reduced concentration of NOx; and
thereafter injecting hydrogen peroxide into the flue gas stream containing unreacted residual ammonia, in an amount sufficient to react with the residual ammonia present in the flue gas stream, the flue gas having a temperature of up to about 700° F. during the hydrogen peroxide injection operation, and wherein the reduction operation and the hydrogen peroxide injection operation are downstream from an economizer, to yield a flue gas stream having a reduced concentration of residual ammonia.
2. The method of claim 1 wherein the ammonia is introduced into flue gas stream in an amount sufficient to provide at least about 50% stoichiometric molar excess, based on the amount of NO X present in the flue gas stream.
3. The method of claim 1 wherein the hydrogen peroxide is employed as an aqueous hydrogen peroxide solution in combination with an activator.
4. The method of claim 1 wherein the hydrogen peroxide is injected into the ammonia-containing flue gas stream in an amount sufficient to provide at least about ¼ mole H 2 O 2 per mole NH 3 up to about 15 moles of H 2 O 2 per mole NH 3 present in the flue gas stream.
5. The method of claim 1 wherein sufficient hydrogen peroxide is contacted with the ammonia-containing flue gas stream to reduce the ammonia concentration in the H 2 O 2 -treated flue gas stream to less than about 10 ppm NH 3 .