A method supplies reactants, including fuel gas, to burners that discharge the reactants into a furnace process chamber. In a stable flame mode of operation, stable flames are projected from the burners into the furnace process chamber. At a time when the furnace process chamber has a temperature at
A method supplies reactants, including fuel gas, to burners that discharge the reactants into a furnace process chamber. In a stable flame mode of operation, stable flames are projected from the burners into the furnace process chamber. At a time when the furnace process chamber has a temperature at or above an autoignition temperature of the fuel gas, a diffuse combustion mode is initiated by supplying a selected burner with additional reactants, including reactants diverted from another burner, to blow off the stable flame at the selected burner.
대표청구항▼
1. A method comprising: supplying reactants, including fuel and combustion air, to burners that discharge the reactants into a furnace process chamber;projecting stable flames from the burners into the furnace process chamber; andat a time when the furnace process chamber has a temperature at or abo
1. A method comprising: supplying reactants, including fuel and combustion air, to burners that discharge the reactants into a furnace process chamber;projecting stable flames from the burners into the furnace process chamber; andat a time when the furnace process chamber has a temperature at or above an autoignition temperature of the fuel, initiating flameless combustion in the furnace process chamber by supplying a selected burner, of the burners, with additional reactants diverted from a burner, of the burners, other than the selected burner, to blow off the stable flame at the selected burner. 2. A method as defined in claim 1 wherein the additional reactants consist of reactants diverted from one or more burners, of the burners, other than the selected burner. 3. A method as defined in claim 1 wherein the initiating step turns off the burner from which reactants are diverted to the selected burner. 4. A method as defined in claim 1 wherein the initiating step does not reduce a total rate at which the reactants are supplied to the burners. 5. A method as defined in claim 1 further comprising the subsequent step of diverting reactants from the selected burner to provide the selected burner with reactants at a reduced rate at which a stable flame reignites at the autoignition temperature. 6. A method as defined in claim 5 wherein the reduced rate is provided without reducing a total rate at which the reactants are supplied to the burners. 7. A method comprising: firing burners into a furnace process chamber by supplying the burners with reactants, including fuel and combustion air, at a total rate that supports stable flames at the burners;at a time when the furnace process chamber has a temperature at or above autoignition temperature, initiating flameless combustion without reducing the total rate at which the reactants are supplied to the burners, diverting reactants from one or more selected burners, of the burners, to one or more burners other than the selected burners to blow off the stable flame at one or more of the burners to which reactants are diverted; andcontinuing to supply reactants including fuel and combustion air to one or more of the burners at which the stable flame has been blown off. 8. A method as defined in claim 7 wherein the diverting step blows off the stable flame at each burner to which reactants are diverted. 9. A method as defined in claim 7 wherein the diverting step turns off one or more of the selected burners from which reactants are diverted. 10. A method comprising: supplying reactants, including fuel and combustion air, to burners that discharge the reactants into a furnace process chamber;projecting stable flames from the burners into the furnace process chamber;blowing off the stable flame at a selected burner, of the burners, by supplying the selected burner with additional reactants diverted from one or more other burners of the burners other than the selected burner at a time when the furnace process chamber has a temperature at or above an autoignition temperature of the fuel;continuing to supply reactants including fuel and combustion air to the selected burner after the stable flame has been blown off while the temperature remains at or above an autoignition temperature of the fuel; andsubsequently diverting reactants from the selected burner to the one or more burners other than the selected burner to provide the selected burner with reactants at a reduced rate at which a stable flame reignites at the autoignition temperature. 11. A method as defined in claim 10 wherein the diverting step blows off the stable flame at one or more of the burners to which reactants are diverted. 12. A method comprising: supplying reactants, including fuel and combustion air, to burners that discharge the reactants into a furnace process chamber;projecting stable flames from the burners into the furnace process chamber; andat a time when the furnace process chamber has a temperature at or above an autoignition temperature of the fuel, initiating flameless combustion in the furnace process chamber by supplying a selected burner, of the burners, with additional reactants diverted from a burner, of the burners, other than the selected burner, to blow off the stable flame at the selected burner;wherein the additional reactants include reactants diverted from more than one burner other than selected burner. 13. A method comprising: supplying reactants, including fuel and combustion air, to burners that discharge the reactants into a furnace process chamber;projecting stable flames from the burners into the furnace process chamber; andat a time when the furnace process chamber has a temperature at or above an autoignition temperature of the fuel, initiating flameless combustion in the furnace process chamber by supplying a selected burner, of the burners, with additional reactants diverted from one or more burners, of the burners, other than the selected burner, to blow off the stable flame at the selected burner;wherein initiating step does not turn off any burner from which reactants are diverted to the selected burner. 14. A method comprising; firing burners into a furnace process chamber by supplying the burners with reactants, including fuel and combustion air, at a total rate that supports stable flames at the burners;at a time when the furnace process chamber has a temperature at or above autoignition temperature, initiating flameless combustion without reducing the total rate at which the reactants are supplied to the burners, diverting reactants from one or more selected burners, of the burners, to one or more burners, of the burners, other than the selected burners to blow off the stable flame at one or more of the burners to which reactants are diverted; andcontinuing to supply reactants including fuel and combustion air to the burners at which the stable flame has been blown off. 15. A method comprising: firing burners into a furnace process chamber by supplying the burners with reactants, including fuel and combustion air, at a total rate that supports stable flames at the burners;at a time when the furnace process chamber has a temperature at or above autoignition temperature, initiating flameless combustion without reducing the total rate at which the reactants are supplied to the burners, diverting reactants from one or more selected burners, of the burners, to one or more burners, of the burners, other than the selected burners to blow off the stable flame at one or more of the burners to which reactants are diverted;wherein the diverting step does not turn off any burner from which reactants are diverted; andcontinuing to supply reactants including fuel and combustion air to the burners at which the stable flame has been blown off;wherein, at a burner of the burners where the stable flame has been blown off, reactants are diverted from that burner to one or more burners, of the burners, other than that burner to provide that burner with reactants at a reduced rate that supports a stable flame. 16. A method as defined in claim 15 wherein the reduced rate is provided without reducing a total rate at which the reactants are supplied to the burners. 17. A method comprising: supplying reactants, including fuel and combustion air, to burners that discharge the reactants into a furnace process chamber;projecting stable flames from the burners into the furnace process chamber;blowing off the stable flame at a selected burner, of the burners, by supplying the selected burner with additional reactants diverted from one or more burners, of the burners, other than the selected burner at a time when the furnace process chamber has a temperature at or above an autoignition temperature of the fuel;continuing to supply reactants including fuel and combustion air to the burners at which the stable flames have been blown off while the temperature remains at or above an autoignition temperature of the fuel gas; andsubsequently diverting reactants from the selected burner to one or more of the burners other than the selected burner to provide the selected burner with reactants at a reduced rate at which a stable flame reignites at the autoignition temperature;wherein the diverting step does not blow off the stable flame at any burner to which reactants are diverted. 18. A method comprising: supplying reactants, including fuel and combustion air, to burners that discharge the reactants into a furnace process chamber;protecting stable flames from the burners into the furnace process chamber;blowing off the stable flame at a selected burner, of the burners, by supplying the selected burner with additional reactants diverted from one or more burners, of the burners, other than the selected burner at a time when the furnace process chamber has a temperature at or above an autoignition temperature of the fuel;continuing to supply reactants including fuel and combustion air to the burners at which the stable flames have been blown off while the temperature remains at or above an autoignition temperature of the fuel gas; andsubsequently diverting reactants from the selected burner to one or more of the burners other than the selected burner to provide the selected burner with reactants at a reduced rate at which a stable flame reignites at the autoignition temperature;wherein the diverting step does not blow of the stable flame at any burner to which reactants are diverted.
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이 특허에 인용된 특허 (9)
Widmer, Neil Colin; Payne, Roy; Seeker, William Randall; Gauthier, Philippe Jean, Combustion optimization for fossil fuel fired boilers.
Anderson John E. (Somers NY) Farrenkopf Dennis R. (Bethel CT) Francis ; Jr. Arthur W. (Monroe NY) Slader Steven L. (New York NY) Snyder William J. (Ossining NY), Luminous combustion system.
Wagner Matthew Lincoln ; Bergman ; Jr. Thomas John, Method and apparatus for direct oxygen injection with a reactant stream into a fluidized bed reactor.
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