초록 ▼

Fuels containing fixed-nitrogen chemical species are combusted in a multi-stage process. The process which converts substantially all of the fixed-nitrogen into molecular nitrogen (and thus avoids the formation of significant amounts of nitrogen oxides from the fixed-nitrogen) consists of four steps

Fuels containing fixed-nitrogen chemical species are combusted in a multi-stage process. The process which converts substantially all of the fixed-nitrogen into molecular nitrogen (and thus avoids the formation of significant amounts of nitrogen oxides from the fixed-nitrogen) consists of four steps: (a) mixing said fuel with at least one first oxidizing agent in amounts such that the equivalence ratio of said fuel to said oxidizing agent is at least about 1.4; (b) partially combusting the mixture resulting from step (a) in at least one first stage at a first temperature of about 1850°to about 2150°K., with a residence time of at least 0.03 second; (c) mixing the combustion products resulting from step (b) with at least one second oxidizing agent in an amount such that the equivalence ratio of combustion products to the total amount of oxidizing agents in the mixture will be about 1.0 or less, such mixing taking place under conditions such that the temperature of the mixture will not exceed about 1800°K.; and (d) completely combusting the mixture resulting from step (c) in at least one second stage at a second temperature of less than about 1800°K.

대표청구항 ▼

A multi-stage process for combusting a fuel containing fixed-nitrogen chemical species which comprises the steps of: (a) mixing said fuel which is preheated with at least one first oxidizing agent which is preheated in amounts such that the equivalence ratio of said fuel to said oxidizing agent is a

A multi-stage process for combusting a fuel containing fixed-nitrogen chemical species which comprises the steps of: (a) mixing said fuel which is preheated with at least one first oxidizing agent which is preheated in amounts such that the equivalence ratio of said fuel to said oxidizing agent is at least about 1.6; (b) partially combusting the mixture resulting from step (a) in at least one first stage at a first temperature of about 1850°to about 2150°K., with a residence time of at least 0.03 second; (c) mixing the combustion products resulting from step (b) with at least one second oxidizing agent in an amount such that the equivalence ratio of combustion products to the total amount of oxidizing agents in the mixture will be about 1.0 or less, such mixing taking place under nonadiabatic means such that the temperature of the mixture will not exceed about 1800°K.; and (d) completely combusting the mixture resulting from step (c) in at least one second stage at a second temperature of less than about 1800°K.