as shown in fig1 the main burner generally referred to by reference 10 comprises a catalytic pilot generally referred to by reference number 11 positioned within a main mixer generally referred to by reference number 12 that is positioned within a housing 14 . the catalytic pilot 11 is comprised of catalytic reactor generally referred to by reference number 16 in fluid communication with a first duct 18 . the main mixer 12 is comprised of a mixer 20 with an integral fuel injector 22 in fluid communication with a second duct 24 . the first duct 18 and the second duct 24 are in fluid communication . the catalytic pilot 11 is comprised of a housing 26 that defines an interior area 28 and an inlet 30 in fluid communication therewith . the interior area 28 defines an exit 32 . positioned within the interior area 28 is a plurality of tubes 34 , each having an exterior surface 36 . the housing 26 has an interior surface 38 that in cooperation with the exterior surfaces 36 defines a single flow channel 40 . each tube 34 has an exit 42 . as shown in fig2 the tube exits 42 cooperate to define an exit 44 from the single flow channel 40 . continuing with fig1 the inlet 30 is in fluid communication with the single flow channel 40 . positioned on the exterior surface 36 between the inlet 30 and the single flow channel exit 44 is a catalyst 50 , such that a first mixture 48 enters the single flow channel 40 through the inlet 30 and passes over the catalyst 50 before exiting the single flow channel 40 through the exit 44 . the catalyst 50 is application specific ; however , in a gas turbine utilizing a hydrocarbon based fuel a precious metal based catalyst such as platinum or palladium , i . e . a catalyst having a platinum or palladium element whether individually or in compound , would be appropriate . the single flow channel exit 44 and the tube exits 42 are in fluid communication with the first duct 18 . the single flow channel exit 44 and the tube exits 42 are coincident with each other , i . e . in the same plane . the tube exits 42 , however , can be spatially downstream from the single flow channel exit 44 . as shown in fig2 the single flow channel exit 44 is subdivided into multiple openings , which are preferably discrete , with the openings interspersed around the tube exits 42 . the multiple discrete openings subdivide the first reacted mixture as it exits the single flow channel exit 44 and permits the interspersal of these openings around the tube exits 42 thereby promoting more rapid mixing of the first reacted mixture 48 exiting the single flow channel 40 and the second air 46 exiting the tubes 34 within the first duct 18 . the openings are defined by the outer surface of the tubes 34 . in the preferred embodiment , flared ends of the tubes 34 position the tubes 34 within the housing 26 ; however , other structures such as a grid could be used . referring back to fig1 the first duct 18 is defined by a portion of the interior surface 38 of the housing 26 . the first duct 18 has a length l 1 that is non - zero and sufficient to permit the second air 46 exiting the tubes 34 and the first reacted mixture 48 exiting the single flow channel 40 through exit 44 to mix to a desired degree of unmixedness forming a second mixture 49 , which exits the catalytic pilot 11 through the exit 32 . the inlet 30 is in fluid communication with a conduit 56 . it is the conduit 56 through which the first mixture 48 flows into the single flow channel 40 such that the first mixture 48 exclusively enters the single flow channel 40 and not a tube 34 . the first mixture 48 is comprised of first air 52 and first fuel 54 that has been injected therein . the first mixture 48 should be well mixed . mixing can be accomplished by any means such as swirlers ( not shown ) or entrainment . as an option , a plenum 57 can be imposed between the conduit 56 and the inlet 30 . when a plenum 57 is used , the plenum 57 should extend around the exterior surface 64 and there should be additional inlets 30 such that the first mixture 48 can enter the single flow channel 40 at multiple locations . the use of a plenum 57 allows for a better entering flow distribution of the first mixture 48 within the single flow channel 40 . the tubes 34 , each of which have an entrance 58 , are positioned such that the second air 46 exclusively enters the tubes 34 , and does not enter the single flow channel 40 . in the preferred embodiment , the tubes 34 penetrate the housing 26 such that the tube entrances 58 are not within interior area 28 . where the tubes 34 penetrate the housing 26 , the penetration is sealed such that leakage is prevented from the single flow channel 40 around the tubes 34 . this assures that the second air 46 will exclusively enter the tubes 34 and the first mixture 48 will exclusively enter the single flow channel 40 . the housing 14 has an inner surface 62 and the housing 26 has an exterior surface 64 that cooperate to define a region 66 wherein the main mixer 12 is positioned . in the preferred embodiment , the main mixer 12 is comprised of a mixer 20 with an integral fuel injector 22 in fluid communication with the second duct 24 . as shown in fig3 the mixer 20 is a swirler that fills the cross - section of the region 66 . other main burners such as those where the mixer and fuel injector are not integrated are considered within the scope of the invention . it is also not a requirement of the present invention that the mixer 20 completely fill the cross - section of the region 66 . continuing with fig1 the second duct 24 must be of sufficient length l 2 to permit mixing of a third air 68 with a second fuel 70 . the length l 2 is measured from where the third air 68 and the second fuel 70 are brought into contact to the point at which a third mixture 72 is created , which has the degree of unmixedness desired . fluids mixing within the first duct 18 and the second duct 24 must be isolated one from the other , until of course the fluids are combusted . while a first air 52 , a second air 46 and a third air 68 have been discussed , it is understood that these airs could be derived from a single primary air 74 . similarly , it is understood that the first fuel 54 and the second fuel 70 could both be obtained from the same fuel source . in the method of the current invention as applied to the above main burner 11 , a first air 52 , a second air 46 , and third air 68 as well as a first fuel 54 and second fuel 70 are provided . the first fuel 54 and the first air 52 are proportioned such that if traveling together and intermixed a first mixture 48 would be formed having a fuel / air equivalence ratio greater than 1 . 0 . the first fuel 54 , the first air 52 , and the second air 46 are proportioned such that if traveling together and intermixed a second mixture 49 would be formed having a fuel / air equivalence ratio less than 1 . 0 . finally , if the second fuel 70 and the third air 68 are proportioned such that if traveling together and intermixed a third mixture 72 would be formed having a fuel / air equivalence ratio less than 1 . 0 . the first fuel 54 and the first air 52 are introduced into a first common area , such as a conduit 56 where the first fuel 54 and the first air 52 travel together and intermix to form the first mixture 48 . the first mixture 48 is then oxidized in the presence of the catalyst 50 as the first mixture flows over and comes in contact therewith producing the first reacted mixture 48 . in the case of a gas turbine employing standard hydrocarbon fuels , the oxidation will be exothermic generating a heat of reaction . the first reacted mixture 48 is then introduced into a second common area such as the first duct 18 , which also serves as a post mixing chamber for the cooling air flow 60 and the first reacted mixture 48 , along with the second air 46 where the first reacted mixture 48 and the second air 46 travel along and intermix to form the second mixture 49 . to form the second mixture 49 , the first reacted mixture 48 must not auto - ignite upon exiting the single flow channel exit 44 and contacting the second air 46 . whether the first reacted mixture 48 will auto - ignite upon contact with the second air 46 is application specific and dependent upon such factors as the temperature and flow velocity of the first reacted mixture 48 . for a more complete discussion see u . s . patent application ser . no . 09 / 527 , 708 titled “ method and apparatus for a fuel rich catalytic reactor ” that is assigned to the same assignee as the present application , namely precision combustion , inc ., and the disclosure of which is incorporated herein in its entirety . the second mixture 49 is then combusted . depending upon the conditions , the second mixture 49 may have to be ignited to begin combustion . the first duct 18 while depicted as being generally cylindrical , may in certain situations be non - cylindrical and even have a decreasing cross - section . a decreasing cross - section could assist in increasing the velocity of the first reacted mixture 48 and the second air 46 as the two mix to form the second mixture 49 , thereby decreasing potential of an autoignition event within the first duct 18 . if the cross - section is decreased as described above , a flame stabilizer such as a dump might be required at the end of the decreasing cross - section to anchor the combustion of the second mixture 49 . simultaneously with the above , the third air 68 and the second fuel 70 are introduced into a common area of mixer 20 so that the third air 68 and the second fuel 70 travel together and intermix to form the third mixture 72 . the third mixture 72 is then combusted . the combusting second mixture 49 is combusted in contact with the combusting third mixture 72 . as those skilled in the art of combustion engineering will appreciate , adjustment of the fuel / air equivalence ratios within the parameters discussed above will determine the amount of no x produced by the main burner . as discussed above , no x formation occurs at elevated temperatures and fuel / air equivalence ratios can be adjusted to limit the resulting combustion temperatures resulting from the second and third mixtures . to achieve these no x reductions however , the mixtures must be highly mixed . the first and second ducts must be of sufficient lengths to permit the desired degree of mixing . generally , the second fuel and third air , and the first reacted mixture and the second air must have an unmixedness no greater than about 20 percent with a range of between 2 and 10 percent being desired . above these limits , the mixtures will not be burning as substantially premixed mixtures thus no x reductions will be minimized by significant high - temperature combustion within the mixture . an additional consideration is the velocity of the second fuel and third air and the first reacted mixture and second air through the main mixer and the catalytic pilot , respectively . these mixtures must travel at sufficient velocity to prevent flashback , i . e . a flame traveling toward the fuel source of the flame , in this case entering the first and / or second duct . velocity is also critical for the second and third mixtures . the velocity of these mixtures must allow for stable combustion . these velocities and calculations thereof are well within the knowledge and skill of those in combustion engineering . as an option , a portion of the heat of reaction can be transferred into the second air 46 . the heat of reaction raises the temperature of the first reacted mixture 48 . if some of this heat of reaction is transferred to the second air 46 , the temperature of the second air 46 will be increased . as disclosed in u . s . patent application ser . no . 09 / 527 , 708 , the incorporation of the heat of reaction into the second air 46 will lower overall no x formation of the catalytic pilot . while preferred embodiments have been shown and described , various modification and substitutions may be made without departing from the spirit and scope of the invention . accordingly , it is understood that the present invention has been described by way of example , and not by limitation .