System and method for selective catalytic reduction of nitrogen oxides in combustion exhaust gases
View Patent ↗A multi-stage selective catalytic reduction (SCR) unit ( 32 ) provides efficient reduction of NOx and other pollutants from about 50-550° C. in a power plant ( 19 ). Hydrogen ( 24 ) and ammonia ( 29 ) are variably supplied to the SCR unit depending on temperature. An upstream portion ( 34 ) of the SCR unit catalyzes NOx+NH 3 reactions above about 200° C. A downstream portion ( 36 ) catalyzes NOx+H 2 reactions below about 260° C., and catalyzes oxidation of NH 3 , CO, and VOCs with oxygen in the exhaust above about 200° C., efficiently removing NOx and other pollutants over a range of conditions with low slippage of NH 3 . An ammonia synthesis unit ( 28 ) may be connected to the SCR unit to provide NH 3 as needed, avoiding transport and storage of ammonia or urea at the site. A carbonaceous gasification plant ( 18 ) on site may supply hydrogen and nitrogen to the ammonia synthesis unit, and hydrogen to the SCR unit.
1. A method of removing nitrogen oxides (NOx) from combustion exhaust, comprising:
synthesizing a fuel gas containing hydrogen by gasification of a carbonaceous material;
separating some of the hydrogen from the fuel gas;
mixing at least some of the separated hydrogen into the combustion exhaust;
catalyzing a reaction between NOx in the combustion exhaust and the hydrogen that removes NOx from the exhaust at temperatures up to about 260° C.;
separating nitrogen from air;
synthesizing ammonia from at least some of the separated hydrogen and nitrogen;
mixing the ammonia into the combustion exhaust;
catalyzing a reduction reaction between NOx in the combustion exhaust and the ammonia that removes NOx from the exhaust at exhaust temperatures above about 200° C., wherein the catalyzing the reduction reaction between NOx and the ammonia comprises transitioning from primarily adding separated hydrogen to the combustion exhaust to primarily catalyze a reaction between NOx and the hydrogen in the combustion exhaust to primarily adding ammonia to the combustion exhaust to primarily catalyze the reduction reaction between NOx and the ammonia over a temperature range of between 200° C. and 260° C.; and
catalyzing oxidation reactions of ammonia, carbon monoxide, and volatile organic compounds in the exhaust downstream of the NOx-ammonia reaction at exhaust temperatures above about 200° C.
2. The method of claim 1 , further comprising:
sensing a temperature of the combustion exhaust;
sensing a NOx concentration in the combustion exhaust; and
proportioning the separated hydrogen between a first and a second flow of the hydrogen, the first hydrogen flow routed to an injector that mixes the hydrogen into the combustion gas, and the second hydrogen flow routed to an ammonia synthesis unit that supplies the ammonia to the injector;
wherein when the temperature of the combustion exhaust is too low for effective ammonia-NOx reaction, the first hydrogen flow is increased relative to the second hydrogen flow, and when the temperature of the combustion exhaust is in an optimal range for ammonia-NOx reaction, the second hydrogen flow is increased relative to the first hydrogen flow.
3. The method of claim 1 , further comprising:
sensing a temperature parameter of the combustion exhaust;
sensing a NOx concentration parameter in the combustion exhaust;
sensing a flow volume parameter of the combustion exhaust;
inputting the sensed parameters to a controller that automatically adjusts proportions and amounts of the hydrogen and the ammonia added into the combustion exhaust depending on operating conditions, wherein when the temperature of the combustion exhaust is too low for effective ammonia-NOx reaction, proportionally more hydrogen and less ammonia is added into the combustion exhaust, and when the temperature of the combustion exhaust is in an optimal range for ammonia-NOx reaction, proportionally more ammonia and less hydrogen is added into the combustion exhaust.