Low emission and low excess air steam generating system and method

Claim 1

A method of operating a pulverized coal fired steam generator comprising the steps of: a) pulverizing coal to a selected particle size and firing said pulverized coal and primary air into a furnace of said steam generator in such a manner that streams of said pulverized coal and said primary air are directed tangentially to an inner imaginary, substantially horizontal circle in the center of said furnace; b) introducing secondary combustion air into said furnace in such a manner that the streams of said secondary combustion air are directed tangentially to an outer imaginary circle concentric with and surrounding said inner circle to reduce NO x in the flue gases and maintain an oxidizing atmosphere adjacent the furnace walls; c) introducing overfire combustion air into said furnace at a location above said pulverized coal, primary combustion air and secondary combustion air to further reduce NO x in the flue gases; d) measuring the operating efficiency of said steam generator; e) adjusting the amount of said primary, secondary and overfire combustion air to a level below 15% above stoichiometric to maximize the operating efficiency of said steam generator and adjusting the ratio of said secondary combustion air and said overfire combustion air so as to minimize the NO x in the flue gas; f) measuring the percentage of unburned carbon in flyash; g) establishing a desired maximum percentage of unburned carbon in the flyash by optimizing the energy required for finer grinding against the energy saved from reduced carbon loss; and h) adjusting the particle size of said pulverized coal to maintain said desired percentage of unburned carbon in the flyash.

Claim 2

A method of operating a pulverized coal fired steam generator comprising the steps of: a) pulverizing coal to a selected particle size and firing said pulverized coal and primary air into a furnace of said steam generator in such a manner that streams of said pulverized coal and said primary air are directed tangentially to an inner imaginary, substantially horizontal circle in the center of said furnace; b) introducing secondary combustion air into said furnace in such a manner that the streams of said secondary combustion air are directed tangentially to an outer imaginary circle concentric with and surrounding said inner circle to reduce NO x in the flue gases and maintain an oxidizing atmosphere adjacent the furnace walls; c) introducing overfire combustion air into said furnace at a location above said pulverized coal, primary combustion air and secondary combustion air to further reduce NO x in the flue gases; d) measuring the operating efficiency of said steam generator; e) adjusting the amount of said primary, secondary and overfire combustion air to a level below 15% above stoichiometric to maximize the operating efficiency of said steam generator and adjusting the ratio of said secondary combustion air and said overfire combustion air so as to minimize the NO x in the flue gas; f) measuring the percentage of unburned carbon in flyash; g) establishing a desired maximum percentage of unburned carbon in the flyash by optimizing the energy required for finer grinding against the energy saved from reduced carbon loss; and h) adjusting the particle size of said pulverized coal to maintain said desired percentage of unburned carbon in the flyash.