Premixed/high-velocity fuel jet low no burner

Claim 2

A process for combusting a gaseous fuel in a burner having low NO x emissions comprising: (a) feeding a gaseous fuel stream and an air stream to a premixer wherein said fuel and air streams are substantially fully mixed to form a fuel-air mixture wherein said fuel and air streams are fed to said premixer at a fuel to air equivalence ratio of less that 1; (b) passing said fuel-air mixture to a combustion chamber wherein said fuel is substantially combusted to produce a combustion chamber jet and flue gases whereby said combustion chamber jet and flue gases pass into a heating zone selected from a furnace, heater, or boiler; (c) passing to said heating zone, comtemporaneously with said combustion chamber jet and flue gases, at least two high-velocity fuel streams, wherein said high-velocity fuel streams are diluted by up to about 300% wt. based on the weight of the high-velocity fuel streams with a nonreactive thermal ballast selected from water, steam, recycled or recirculated flue gas, or mixtures thereof, prior to coming into contact with said combustion chamber jet, wherein said high-velocity fuel streams entrain at least a portion of said flue gases, wherein the fuel in the high-velocity fuel streams is substantially combusted prior to coming into contact with the combustion chamber jet; and (d) removing said flue gases from said heating zone.

Claim 3

The process according to claim 1 wherein the equivalence ratio of fuel to air in step (a) is between about 0.4 and 0.7.

Claim 4

The process according to claim 2 wherein said heating zone comprises a radiant section and wherein said high-velocity fuel streams are passed, in step (c), into said radiant section.

Claim 5

The process according to claim 3 wherein step (c) said high-velocity fuel streams are diluted with said nonreactive thermal ballast by way of a compound injection nozzle and wherein said high-velocity fuel streams substantially entrain said ballast and entrain a recirculated flue gas prior to coming into contact with said combustion chamber jet.

Claim 6

The process according to claim 4 wherein in step (c) the nonreactive thermal ballast is steam or water.

Claim 7

The process according to claim 1 wherein said flue gases entrained by said high-velocity fuel streams in step (c) contains at most about 3% wt. oxygen.

Claim 8

The process according to claim 1 wherein in step (b) there is sufficient recirculation of the fuel-air mixture in the combustion chamber to maintain combustion of the fuel-lean, fuel-air mixture.

Claim 9

The process according to claim 2 wherein in step (c) velocity is imparted to said high-velocity fuel streams by high pressure expansion of steam or fuel through a convergent/divergent nozzle.

Claim 10

The process according to claim 2 wherein in step (c) velocity is imparted to said high-velocity fuel streams by admixture of the fuel with a high-velocity water stream.

Claim 11

The process according to claim 6 wherein the concentration of NO x in the flue gases removed in step (d) is less than about 10 ppm.

Claim 12

The process according to claim 1 wherein said fuel-air mixture includes a recycled flue gas.

Claim 13

A process for combusting a gaseous fuel in a burner having low NO x emissions comprising: (a) feeding a gaseous fuel stream, an air stream and a recycled flue gas stream to a premixer wherein said fuel and air streams are substantially fully mixed to form a fuel-air mixture wherein said fuel and air streams are fed to said premixer at a fuel to air equivalence ratio of between about 0.4 and 0.7; (b) passing said fuel-air mixture to a combustion chamber, wherein said fuel is substantially combusted to produce a combustion chamber jet and flue gases, wherein there is sufficient recirculation of the fuel-air mixture in the combustion chamber to maintain combustion of the fuel-lean, fuel-air mixture, whereby said combustion chamber jet and flue gases pass into a heating zone selected from a furnace, heater, or boiler; (c) passing into a radiant section of said heating zone, contemporaneously with the combustion chamber jet and flue gases, at least two high-velocity fuel streams, wherein the velocity is imparted to said high-velocity fuel streams by expansion of high pressure steam or fuel through a convergent/divergent nozzle, or by admixture of the fuel with high-velocity water; said high-velocity fuel streams are diluted by up to about 300% wt. based on the weight of the high-velocity fuel streams with non-reactive thermal ballast selected from steam, water, recycled or recirculated flue gas, or mixtures thereof, by way of a compound injection nozzle and wherein said high-velocity fuel streams partially entrain said ballast prior to coming into conduct with said combustion chamber jet, said high-velocity fuel streams entraining at least a portion of said flue gases wherein said flue gases contain about or less than 3% wt. oxygen and wherein the fuel in the high-velocity fuel streams is partially combusted prior to coming into contact with the combustion chamber jet; and (d) removing said flue gases from said heating zone wherein said flue gases contain less than about 10 ppm NO x .

Claim 14

A process for combusting a gaseous fuel in a burner having low NO x emissions comprising: (a) feeding a gaseous fuel stream, an air stream and a recycled flue gas stream to a premixer wherein said fuel and air streams are substantially fully mixed to form a fuel-air mixture wherein said fuel and air streams are fed to said premixer at a fuel to air equivalence ratio of between about 0.4 and 0.7; (b) passing said fuel-air mixture to a combustion chamber, wherein said fuel is substantially combusted to produce a combustion chamber jet and flue gases, wherein there is sufficient recirculation of the fuel-air mixture in the combustion chamber to maintain combustion of the fuel-lean, fuel-air mixture, whereby said combustion chamber jet and flue gases pass into a heating zone selected from a furnace, heater, or boiler; (c) passing into a radiant section of said heating zone, contemporaneously with the combustion chamber jet and flue gases, at least two high-velocity fuel streams, wherein the velocity is imparted to said high-velocity fuel streams by expansion of high pressure steam or fuel through a convergent/divergent nozzle, or by admixture of the fuel with high-velocity water; said high-velocity fuel streams are diluted by up to about 300% wt. based on the weight of the high-velocity fuel streams with non-reactive thermal ballast selected from steam, water, recycled or recirculated flue gas, or mixtures thereof, by way of a compound injection nozzle and wherein said high-velocity fuel streams partially entrain said ballast prior to coming into conduct with said combustion chamber jet, said high-velocity fuel streams entraining at least a portion of said flue gases wherein said flue gases contain about or less than 3% wt. oxygen and wherein the fuel in the high-velocity fuel streams is partially combusted prior to coming into contact with the combustion chamber jet; and (d) removing said flue gases from said heating zone wherein said flue gases contain less than about 10 ppm NO x .