Method of regenerating NO
View Patent ↗The method includes a pretreatment step during an operation of a boiler in which in a predetermined period of time before shutdown of the boiler, a part of combustion gas that has bypassed an economizer provided in a flue gas duct for flue gas from the boiler is supplied to an upstream of a NO x removal device having a NO x removal catalyst and mixed with the combustion flue gas from the economizer to generate mixed gas having a predetermined temperature equal to or higher than 360° C. (360° C. to 450° C.), the mixed gas is introduced into the NO x removal catalyst, thereby decomposing VOSO 4 adhering to and accumulating on the NO x removal catalyst into V 2 O 5 .
1. A method of regenerating a NO x removal catalyst for removing nitrogen oxide in flue gas at a time of combustion in a boiler by using heavy oil, wherein
in a predetermined period of time before shutdown of a boiler, a decomposing step is performed during an operation of the boiler, at which a part of combustion gas that has bypassed an economizer provided in a flue gas duct for flue gas from the boiler is supplied to an upstream of a NO x removal device having a NO x removal catalyst and mixed with flue gas from the economizer, a temperature of mixed gas is increased to a predetermined temperature equal to or higher than 360° C. to have the NO x removal device in a high-temperature denitration condition, so that vanadyl sulfate (VOSO 4 ) adhering to and accumulating on the NO x removal catalyst is decomposed into vanadium pentoxide (V 2 O 5 ).
2. The method of regenerating a NO x removal catalyst according to claim 1 , comprising an acid washing step after the decomposing step, at which an operation of the boiler is stopped, and thereafter the NO x removal catalyst taken out from the NO x removal device is subjected to acid washing.
3. The method of regenerating a NO x removal catalyst according to claim 1 , wherein in a boiler operation period at the decomposing step, fuel is changed to oil fuel with a low sulfur (S) content and is burned in the boiler.
4. The method of regenerating a NO x removal catalyst according to claim 2 , wherein acid used at the acid washing step is any aqueous solution of oxalic acid, hydrochloric acid, and sulfuric acid.
5. The method of regenerating a NO x removal catalyst according to claim 2 , comprising a water washing step of performing finish water washing and a drying step after the acid washing step.
6. The method of regenerating a NO x removal catalyst according to claim 3 , wherein oil fuel with a low sulfur (S) content is oil fuel that contains 1% by weight or less of sulfur (S).
7. The method of regenerating a NO x removal catalyst according to claim 2 , wherein in a boiler operation period at the decomposing step, fuel is changed to oil fuel with a low sulfur (S) content and is burned in the boiler.
8. The method of regenerating a NO x removal catalyst according to claim 4 , comprising a water washing step of performing finish water washing and a drying step after the acid washing step.