referring to the drawings , generally where like numerals designate the same or functionally similar features , throughout the several views and first to fig1 , there is shown a schematic diagram view of a conventional fuel reburning method . fuel and air are supplied to the boiler via burner apparatus 1 and combusted , forming a combustion zone 2 . excess air is generally supplied to the combustion zone in order to create a fuel - lean environment having a stoichiometric ratio ( oxidant - to - fuel basis ) above about 1 . 0 . a second fuel and air stream are supplied to the boiler via a second burner apparatus 3 and combusted , forming a fuel - rich reburn zone 4 downstream of the combustion zone 2 having a combined stoichiometric ratio below about 1 . 0 . a third air stream is supplied to the boiler via an overfire air port 5 , forming a burnout zone 6 , wherein the third air stream combusts remaining combustible matter for complete combustion . referring now to fig2 , a schematic diagram of an oxygen fuel reburning no x emission reducing method in accordance with the present invention is shown . a first fuel and first air stream are supplied to the boiler via a burner apparatus 7 and combusted , forming a combustion zone 8 . excess first air is generally supplied to the combustion zone in order to create a fuel - lean environment having a stoichiometric ratio of about 1 . 0 , and preferably between about 0 . 9 and about 1 . 2 . a second fuel and an oxygen stream are supplied to the boiler via a second burner apparatus 9 and combusted , forming a fuel - rich reburn zone 10 downstream of the combustion zone 9 having a combined stoichiometric ratio below about 1 . 0 , and preferably between about 0 . 6 and 1 . 0 . injection of an oxygen stream into the reburn zone 10 increases the local flame temperature via reducing the dilutent effect of nitrogen and other inert gas of which air comprises . higher flame temperature enhances fuel pyrolysis and generation of no x reducing precursors , including but not limited to hydrocarbon radicals , amines , and cyanic compounds . increased no x reducing precursors concentrations facilitate improved removal of no x emission generated in the combustion zone 8 . additional no x emissions generated in the reburn zone 10 are minimized as nitrogen introduced though the prior art air stream is no longer present , thus not capable of producing no x emissions which would otherwise compete for the limited supply of no x reducing precursors generated . in an alternative embodiment of the present invention a burnout zone 12 may be positioned downstream of the reburn zone 10 for combusting remaining combustible matter not combusted in either the combustion zone 8 or reburn zone 10 . the burnout zone 12 may be formed by providing a second air stream to an overfire air port 13 , and allowing combustion of remaining combustibles to ensue . in another alternative embodiment , pulverized coal may be utilized as the second fuel and provided to the reburn burner 9 via a carrier gas . the second fuel carrier gas can be air , oxygen , recirculated flue gas , or any other gas known to one of skill in the boiler arts . conduits may be installed anywhere along the boiler system , in recirculated flue gas embodiments , to allow desired quantities of flue gas to be recirculated into the boiler and obtain further no x reduction via quenching of the reburn zone 10 . the oxygen stream can then be premixed with the recirculated flue gas , or injected via an oxygen delivery means into the reburn zone 10 . in another alternative embodiment of the present invention oxygen is delivered to the reburn zone 10 by an oxygen delivery means inside a reburn burner 9 . the oxygen deliver means may be any spud or lance commonly know in the art . alternatively , referring to fig3 , the oxygen deliver means may by a multi - bladed injection device wherein oxygen is provided to the reburn zone 10 through a plurality of hollow blade conduits 14 in fluid connection with a hollow guide pipe conduit 15 . in another embodiment wherein fuel oil is used as the second fuel , fuel oil can be sprayed into the reburn zone 10 using oxygen as the atomizing medium . in yet another embodiment natural gas or other gaseous fuels can be injected with oxygen by separate delivery means within a reburn burner 9 .