System and method for urea decomposition to ammonia in a side stream for selective catalytic reduction
View Patent ↗A method for reducing NOx emissions in the exhaust of a combined cycle gas turbine equipped with a heat recovery boiler and a catalyst effective for NOx reduction, wherein a slip stream of hot flowing exhaust gases is withdrawn from the primary gas flow after the catalyst at a temperature of 500° F. to 900° F. and directed through a fan to a continuous duct into which an aqueous based reagent is injected for decomposition to ammonia gas and the outlet of the continuous duct is connected to an injection grid positioned in the primary exhaust for injection of ammonia gas into the primary exhaust stream at a location upstream of the catalyst.
1. A method for reducing NOx emissions from an exhaust of a combined cycle gas turbine equipped with a heat recovery boiler, said method comprising the steps of:
providing a plurality of heat exchanger sections spatially separated from one another in a direction of flow of primary exhaust gases, said plurality of heat exchanger sections comprising at least a first heat exchanger section and a second heat exchanger section;
providing a catalyst effective for NOx reduction downstream of the second heat exchanger section;
providing an injection grid downstream of the first heat exchanger section and upstream of the second heat exchanger section;
causing the primary exhaust gases to flow over the first heat exchanger section, then the injection grid, then the second heat exchanger section and then the catalyst;
withdrawing a slip stream of the primary exhaust gases from a location downstream of the catalyst at a temperature of 500° F. to 900° F. and through a fan or blower to a continuous duct;
injecting aqueous based reagent into the slip stream flowing through the continuous duct such that the aqueous based reagent decomposes to ammonia gas;
injecting the slip stream, carrying the ammonia gas, into the flow of the primary exhaust gases through the injection grid, whereby a mixture of the slip stream, carrying the ammonia gas, and the primary exhaust gases are caused to flow over the catalyst, and
wherein the gases withdrawn in the slip stream are maintained such that a temperature of the gases in the continuous duct is kept above 650° F. immediately downstream of the point of reagent injection;
wherein a residence time in the continuous duct is less than one second from the point of reagent injection into the continuous duct to the point of injecting the slip stream, carrying the ammonia gas, into the flow of primary exhaust gases.
2. The method of claim 1 , wherein a portion of the slip stream comprises gases repeatedly re-passed over the second heat exchanger section.
3. The method of claim 2 wherein no heat exchange section of the combined cycle gas turbine is bypassed by the gases withdrawn in the slip stream.
4. The method of claim 1 wherein the temperature of the gases in the continuous duct is kept above 650° F. by way of heating the gases withdrawn in the slip stream upstream of the point of reagent injection and downstream of the fan or blower.
5. The method of claim 1 , wherein the aqueous based reagent is a 25-50% aqueous solution of urea.
6. The method of claim 1 , wherein the aqueous based reagent is an aqueous based ammonia solution of 19-30%.
7. A method for reducing NOx emissions in an exhaust of a combined cycle gas turbine equipped with a heat recovery boiler and a catalyst effective for NOx reduction, wherein a slip stream of hot flowing exhaust gases is withdrawn from a primary gas flow after the catalyst at a temperature of 500° F. to 900° F. and directed through a fan to a continuous duct into which an aqueous based reagent is injected for decomposition to ammonia gas and the outlet of the continuous duct is connected to an injection grid positioned in the primary gas flow for injection of ammonia gas into the primary gas flow at a location upstream of the catalyst, wherein the gases withdrawn in the slip stream are maintained such that the gases in the continuous duct maintain a temperature above 650° F. immediately downstream of the point of reagent injection, and wherein a residence time in the continuous duct is less than one second from the point of reagent injection into the continuous duct to the point of injecting the slip stream, carrying the ammonia gas, into the primary gas flow.
8. A combined cycle gas turbine equipped with a heat recovery boiler and having reduced NOx emissions, said system comprising:
a plurality of heat exchanger sections spatially separated from one another in a direction of flow of primary exhaust gases, said plurality of heat exchanger sections comprising at least a first heat exchanger section and a second heat exchanger section;
a catalyst effective for NOx reduction disposed downstream of the second heat exchanger section;
an injection grid disposed downstream of the first heat exchanger section and upstream of the second heat exchanger section;
wherein the first heat exchanger section, the injection grid, the second heat exchanger section and the catalyst are disposed such that the primary exhaust gases flow over the first heat exchanger section, then the injection grid, then the second heat exchanger section and then the catalyst;
a slip stream inlet positioned to withdraw a slip stream of the primary exhaust gases from a location downstream of the catalyst at a temperature of 500° F. to 900° F. and through a fan or blower to a continuous duct;
an injector positioned in the continuous duct, said injector injecting aqueous based reagent into the slip stream flowing through the continuous duct such that the aqueous based reagent decomposes to ammonia gas;
wherein the gases withdrawn in the slip stream are maintained such that a temperature of the gases in the continuous duct is kept above 650° F. immediately downstream of the point of reagent injection;
wherein the slip stream, carrying the ammonia gas, is injected into the flow of the primary exhaust gases through the injection grid, whereby a mixture of the slip stream, carrying the ammonia gas, and the primary exhaust gases are caused to flow over the catalyst; and
wherein a residence time in the continuous duct is less than one second from the point of reagent injection into the continuous duct to the point of injecting the slip stream, carrying the ammonia gas, into the flow of the primary exhaust gases.
9. The system of claim 8 , wherein a portion of the slip stream comprises gases repeatedly re-passed over the second heat exchanger section.
10. The system of claim 9 wherein no heat exchange section of the combined cycle gas turbine is bypassed by the gases withdrawn in the slip stream.
11. The system of claim 8 further comprising a heater disposed in the continuous duct upstream of the point of reagent injection and downstream of the fan or blower.
12. The system of claim 8 , wherein the aqueous based reagent is a 25-50% aqueous solution of urea.
13. The system of claim 8 , wherein the aqueous based reagent is an aqueous based ammonia solution of 19-30%.