CROSS-REFERENCE TO RELATED APPLICATIONS

[0001] The present application claims priority to co-pending U.S. Provisional Patent Application Number 62/042,738, entitled "LOW NO _x TURBINE EXHAUST FUEL BURNER ASSEMBLY," filed August 27, 2014, the disclosure of which is incorporated herein by reference in its entirety.

FIELD

[0002] The present invention is related generally to a low ΝΟχ burner assembly and more particularly, but not by way of limitation, to a low ΝΟχ burner that can operate utilizing either fresh air or a variable mixture of turbine exhaust gas (TEG) and fresh air.

BACKGROUND

[0003] Very large burner assemblies are used in a variety of applications. Such applications include, but are not limited to, heating air for air heaters and dryers, heating water to generate steam in boilers, or as part of combined cycle systems. Combined cycle systems typically generate both electricity and steam. In such combined cycle systems, a gas turbine typically generates the electrical power by burning a gaseous hydrocarbon fuel with air.

[0004] The present disclosure relates to particular burners, namely Low NO _x burners; and the general term, "ΝΟχ" (nitrogen oxides) is used to describe a group of molecules that contain varying amounts of nitrogen and oxygen at certain ratios. NOx generally forms at high temperatures during fossil fuel combustion of some sort. In the United States, the primary sources of NOx emissions are motor vehicles, power plants, and other commercial, industrial, and residential sources that combust fossil fuels. Direct ΝΟχ emissions from these sources include several different forms, such as nitrogen dioxide (N0 ₂ ), nitrous oxide (N ₂ 0), and nitric oxide (NO), however, ΝΟχ generated during combustion is primarily produced in the form of NO. NO _x emissions react with other compounds, such as those compounds considered or classified as volatile organic compounds in the troposphere to form secondary products that include ozone (0 ₃ ), nitric acid (HNO3), nitrate particles, and the like. ΝΟχ emissions are generally considered to be air pollutants by themselves, as well as precursors to the formation of ozone (i.e., smog) and acid rain. [0005] To protect public health, concentrations of ΝΟχ and ozone in the ambient atmosphere are often subject to air quality standards established in the United States by the Environmental Protection Agency (EPA). Because of the potentially negative health and environmental impacts associated with ΝΟχ emissions and their role in generating tropospheric ozone, ΝΟχ emissions producers are often highly regulated by the EPA, as well as by state and local environmental authorities. Regulations by federal and state authorities have engendered the development of low ΝΟχ burners for industrial applications. One example of a low ΝΟχ burner is described in U.S. Patent No. 5,460,512. One version of this burner, commercially referred to as a QLN™ burner, is available from John Zink Company, LLC (www.johnzink.com) and provides for reduced NOx emissions.

[0006] One way to reduce ΝΟχ emissions in known burner systems is by introducing inert gases (e.g. C0 ₂ , H ₂ 0) into a combustion reaction to reduce peak flame temperature. Most commonly, this type of reduction is accomplished by recirculating direct products of combustion, such as flue exhaust gases, back into a combustion process, and is commonly referred to as Flue Gas Recirculation (FGR). Alternatively, exhaust gases from gas turbines may be used for combustion.

[0007] As noted above, in combined cycle systems, gas turbines burn hydrocarbon gases to generate electricity. Due to certain design constraints and operating requirements of gas turbines, the combustion process usually only partially depletes the available oxygen in air. Consequently, the resulting Turbine Exhaust Gas (TEG) often contains an elevated concentration of oxygen compared to typical exhaust gas found in boilers. This relatively large quantity of oxygen in TEG can be used as an oxidizer source for subsequent downstream fuel combustion.

[0008] Such downstream fuel combustion typically involves placing burners across a cross- section of a TEG exhaust duct. These burners, commonly referred to as duct burners, further deplete the TEG oxygen and generate sensible heat or thermal energy, which elevates the exhaust gas temperature. A Heat Recovery Steam Generator (HRSG) recovers the residual heat (present when exiting the turbine) of the TEG and the sensible heat added by the duct burner and uses these sources of heat to produce steam. Alternatively, and less commonly, the TEG can be ducted to a standard burner and boiler. SUMMARY

[0009] Important design criteria of a boiler are that the burner flame profile fit the furnace such that the flame does not impinge on a surface and that the fuel is sufficiently oxidized, thus preventing high levels of unburned fuel and/or preventing high levels of ΝΟχ in the exhaust. The flame profile is determined, at least in part, by the fuel heat input and the exit velocity of the TEG. Relative to the fresh air often used in air-oxidized Low ΝΟχ burners, the TEG used in TEG- oxidized Low ΝΟχ burners has a depleted oxygen concentration and an elevated temperature. Thus, achieving equivalent amounts of oxygen in a TEG-oxidized burner typically requires the volumetric flow of TEG to be about double the volumetric flow of fresh air in an air-oxidized burner. Due to these differences, when all other variables are constant, the exit velocity and pressure of the TEG- burner is typically much higher using TEG as an oxidizer rather than fresh air.

[0010] In combined cycle systems, the source of oxygen for the downstream duct burners is typically TEG. The volume and composition (in particular oxygen concentration) of the TEG flow depends on the size of the gas turbine and the often variable electrical load demand of that gas turbine. As a result, the volume and composition of TEG flow in combined systems is often variable. To counter this variability in composition and volume of TEG flow, these systems may operate with much higher stack exhaust excess oxygen relative to a standard boiler.

[0011] Embodiments of the present systems and methods are configured to counteract the variability in the flow rate and oxygen composition of TEG supplied as an oxidizer to a low NOx burner while still being able to operate the low NOx burner with low exhaust excess oxygen. In some of the present embodiments, variable auxiliary fresh air is added to the low NOx burner based on the flow and composition of TEG to the low NOx burner. In some of the present embodiments, when the rate of TEG flow reduces to zero or to a pre-determined level close to zero, the low NOx burner is configured to switch to a mode in which only fresh air is used as an oxidizer. Thus, embodiments of the present burners are configured to utilize, as an oxidizer, either a mixture of fresh air and TEG or fresh air without TEG.

[0012] Some embodiments of the present burner assemblies (e.g., low-ΝΟχ turbine exhaust fuel burner assemblies) are configured to operate with an oxidizer of either fresh air or a combination of turbine exhaust gas (TEG) and fresh air, and comprise: a windbox comprising a sidewall defining a chamber and a fresh air inlet through the sidewall of the windbox in fluid communication with the chamber; a TEG plenum coupled to the windbox, the TEG plenum comprising a sidewall defining a chamber and a TEG inlet through the sidewall of the TEG plenum in fluid communication with the chamber; a burner barrel coupled to the windbox and the TEG plenum, the burner barrel having a sidewall defining a plurality of openings and a channel extending between a first end and a second end, the channel in fluid communication with the chamber of the windbox separately from the plurality of openings, the plurality of openings configured to permit TEG to flow from the TEG plenum into the channel of the burner barrel; one or more fuel injectors coupled to the burner barrel and configured to inject fuel for combustion; and one or more dampers coupled to the burner barrel and configured to be moved between at least: (i) a first configuration in which the one or more dampers cover the plurality of openings to substantially prevent TEG from entering the burner barrel through the plurality of openings; and (ii) a second configuration in which the one or more dampers do not cover at least a portion of the plurality of openings to permit TEG to enter the burner barrel through the plurality of openings.

[0013] Some embodiments of the present burner assemblies further comprise: an air mover adapted to flow fresh air through the fresh air inlet. In some embodiments, the air mover comprises a fan, a compressor, or a fan and a compressor.

[0014] In some embodiments of the present burner assemblies, the TEG plenum is disposed within the windbox. Some embodiments further comprise: a duct coupled to the TEG plenum in fluid communication with the TEG inlet. In some embodiments, the burner barrel is at least partially disposed within the chamber of the TEG plenum.

[0015] In some embodiments of the present burner assemblies, the one or more dampers comprise a slide damper disposed around the burner barrel such that the slide damper is slidable between the first configuration and the second configuration.

[0016] Some embodiments of the present burner assemblies further comprise: a burner plate coupled to the second end of the burner barrel; and a center fire gas gun fuel spud that extends in a downstream direction, which extends from the first end of the burner barrel toward the second end, through the burner barrel and burner plate into a first fuel zone. Some embodiments further comprise: a plurality of core fuel spuds extending from in the downstream direction and to a second fuel zone; a plurality of inner fuel spuds extending in the downstream direction and to a third fuel zone; and a plurality of outer fuel spuds extending in the downstream direction to a fourth fuel zone. Some embodiments further comprise; a port ring having an annular body coupled to the TEG plenum and encircling the second end of the burner barrel, the body defining a plurality of ports configured to permit TEG to flow from the turbine exhaust gas plenum to a boiler. In some embodiments, outlets of the ports are angled inward relative to a longitudinal axis of the burner barrel.

[0017] Some embodiments of the present apparatuses (e.g., for use in low-ΝΟχ turbine exhaust fuel burner assemblies) comprise: a burner barrel having a sidewall defining a plurality of openings and a channel extending between a first end and a second end, the burner barrel configured to be coupled to a windbox of the burner assembly and a TEG plenum of the burner assembly such that: (i) the channel of the burner barrel is in fluid communication with the chamber of the windbox separately from the plurality of openings, and (ii) the plurality of openings is configured to permit TEG to flow from the TEG plenum into the channel of the burner barrel. Some embodiments further comprise: one or more dampers coupled to the burner barrel and configured to be moved between at least: (i) a first configuration in which the one or more dampers cover the plurality of openings to substantially prevent TEG from entering the burner barrel through the plurality of openings; and (ii) a second configuration in which the one or more dampers do not cover at least a portion of the plurality of openings to permit TEG to enter the burner barrel through the plurality of openings. In some embodiments, the one or more dampers comprise a slide damper disposed around the burner barrel such that the slide damper is slidable between the first configuration and the second configuration.

[0018] Some embodiments of the present methods (e.g., of operating a low-ΝΟχ turbine exhaust fuel burner) comprise: in a turbine exhaust gas (TEG) mode in which TEG and fresh air are flowing to a burner barrel of the burner to burn fuel, regulating the flow of the fresh air based on one or more characteristics of the flowing TEG; switching from the TEG mode to a fresh air mode, in which fresh air but not TEG is flowing to the burner barrel of the burner to burn the fuel, by stopping the flow of TEG to the burner barrel while continuing the flow of fresh air to the burner barrel to burn the fuel; and resuming the TEG mode by resuming the flow of TEG to the burner barrel in combination with the flow of fresh air to the burner barrel to burn the fuel.

[0019] In some embodiments of the present methods, in the TEG mode, the TEG flows through a duct to a TEG plenum, from the TEG plenum to the burner barrel, at least a portion of the burner barrel being disposed within the turbine exhaust plenum; fresh air flows from an air mover into the burner barrel; and the one or more characteristics of the flowing TEG comprise one or more characteristics selected from the list consisting of: a concentration of oxygen in the TEG, an amount of flow of the TEG, temperature of the flowing TEG, rate of flow of fuel to a turbine supplying the TEG, temperature of the fuel flowing to the turbine, rate of flow of air to the turbine, temperature of the air flowing to the turbine. Some embodiments further comprise: in the TEG mode, regulating the rate of flow of the TEG to the TEG plenum by adjusting position of a damper relative to the burner barrel to cover or at least partially uncover openings defined by a sidewall of the burner barrel in communication with a channel of the burner barrel. In some embodiments, switching from the TEG mode to the fresh air mode comprises adjusting the damper to cover the openings. In some embodiments, the switching is completed in response to a turbine supplying the TEG ceasing to operate. Some embodiments further comprise: flowing the fresh air to a windbox encompassing the turbine exhaust gas plenum, where the flowing of the fresh air cools the turbine exhaust gas plenum.

[0020] Some embodiments of the present methods (e.g., of operating a low-ΝΟχ turbine exhaust fuel burner) comprise: in response to detection of a gas turbine trip while operating the burner in a turbine exhaust gas (TEG) mode in which TEG and fresh air are flowing to a burner barrel of the burner to burn fuel; switching operation of the burner from the TEG mode to a fresh air mode in which fresh air but not TEG flows to the burner barrel of the burner to burn the fuel. In some embodiments, switching from the TEG mode to the fresh air mode comprises increasing the flow of fresh air to the burner barrel.

[0021] In some embodiments of the present methods, switching operation of the burner assembly from the TEG mode to the fresh air only mode is performed according to a sequence of operations configured to achieve a pre-determined amount of thermal energy to be generated by the burner assembly. In some embodiments, the sequence of operation includes: reducing the rate of burning the fuel to a TEG low fire state; moving fuel flow control valves to a fresh air light-off position; closing a damper of the burner to prevent TEG from flowing into the burner barrel; and adjusting an air mover to supply fresh air to the burner barrel at a fresh air light-off rate.

[0022] Some embodiments of the present methods (e.g., of operating a low-ΝΟχ turbine exhaust fuel burner) comprise: adjusting a combustion air source supplying air to the burner based on one or more characteristics of a source of turbine exhaust gas (TEG) for the burner. In some embodiments, the one or more characteristics comprise flow and temperature parameters of fuel and air flowing to a turbine that is a source of TEG for the burner. In some embodiments, adjusting the airflow set point includes: determining a TEG equivalent airflow (e.g., based on: a measured volumetric flow of combustion air supplying the gas turbine, corrected for ambient temperature and normalized to standard temperature and pressure; and a measured volumetric flow of fuel supplying the gas turbine, normalized to standard temperature and pressure); and subtracting the TEG equivalent airflow from a desired total airflow to determine an airflow set point for adjustment of the combustion air source. In some embodiments, the combustion air source comprises a fan, and where adjusting the combustion air source includes controlling a variable frequency drive (VFD) and a control damper of the fan to adjust for variations in TEG flow and TEG 0 ₂ to maintain a low stack exhaust 0 ₂ setpoint.

[0023] The foregoing has outlined rather broadly certain features and technical advantages of the present disclosure in order that the detailed description of the disclosure that follows may be better understood. Additional features and advantages of the disclosure are described below. It should be appreciated by those skilled in the art that the conception and specific embodiments disclosed may be readily utilized as a basis for modifying or designing other structures for carrying out the same purposes of the present disclosure, without departing from the spirit and scope of the disclosure as set forth in the claims. The features that are believed to be characteristic of the disclosure, both as to its organization and method of operation, together with further objects and advantages will be better understood from the following description when considered in connection with the accompanying figures. It is to be expressly understood, however, that each of the figures is provided for the purpose of illustration and description only and is not intended as a definition of the limits of the present disclosure. [0024] The term "coupled" is defined as connected, although not necessarily directly, and not necessarily mechanically; two items that are "coupled" may be unitary with each other. The terms "a" and "an" are defined as one or more unless this disclosure explicitly requires otherwise. The term "substantially" is defined as largely but not necessarily wholly what is specified (and includes what is specified; e.g., substantially 90 degrees includes 90 degrees and substantially parallel includes parallel), as understood by a person of ordinary skill in the art. In any disclosed embodiment, the terms "substantially," "approximately," and "about" may be substituted with "within [a percentage] of what is specified, where the percentage includes .1, 1, 5, and 10 percent.

[0025] Further, a device or system that is configured in a certain way is configured in at least that way, but it can also be configured in other ways than those specifically described.

[0026] The feature or features of one embodiment may be applied to other embodiments, even though not described or illustrated, unless expressly prohibited by this disclosure or the nature of the embodiments.

[0027] Some details associated with the embodiments described above and others are described below.

BRIEF DESCRIPTION OF THE DRAWINGS

[0028] The following drawings illustrate by way of example and not limitation. For the sake of brevity and clarity, every feature of a given structure is not always labeled in every figure in which that structure appears. Identical reference numbers do not necessarily indicate an identical structure. Rather, the same reference number may be used to indicate a similar feature or a feature with similar functionality, as may non-identical reference numbers. The figures are drawn to scale (with the exception of flowcharts and block diagrams, or unless otherwise noted), meaning the sizes of the depicted elements are accurate relative to each other for at least the embodiment depicted in the figures.

[0029] FIGS. 1 and 2 show front and side views, respectively, of an embodiment of the present burner assemblies.

[0030] FIG. 3 shows partially cutaway right side view of the burner assembly of FIGS. 1 and 2. [0031] FIG. 4 shows a perspective view of a burner barrel and firing components of the burner assembly of FIGS. 1 and 2.

[0032] FIG. 5 shows a cross-sectional side view of the burner barrel and firing components of FIG. 4

[0033] FIG. 6 shows a front view of a port ring of some embodiments of the present burners, such as the burner of FIGS. 1 and 2.

[0034] FIG. 7 shows a cross-sectional side view of the port ring of FIG. 6.

[0035] FIG. 8 shows a front view with hidden lines of the port ring of FIG. 6.

[0036] FIG. 9 shows a cross-sectional side view of the burner barrel and firing components of FIG. 4 in combination with the port ring of FIG. 6, showing the path of TEG flow in TEG mode;

[0037] FIG. 10 shows a block diagram of an embodiment of the present burner assembly control systems.

[0038] FIG. 11 shows a flowchart illustrating an embodiment of the present methods of operating a low ΝΟχ burner, such as one of the present low ΝΟχ burner assemblies.

[0039] FIG. 12 shows a flowchart illustrating a second embodiment of the present methods operating a low- ΝΟχ burner assembly, such as one of the present low ΝΟχ burner assemblies.

DETAILED DESCRIPTION

[0040] In the present low ΝΟχ burners, the amount of air flow to the burner can be adjusted based on one or more characteristics of turbine exhaust gas (TEG) flow (e.g., a lack of TEG flow) to the burner. The present low-ΝΟχ burners are thus configured to operate with a variable mixture of TEG and fresh air while maintaining low exhaust excess air, such as, for example, in a fresh air mode with either fresh air (without TEG) as the oxidizer or a TEG mode with a mixture of fresh air and TEG as an oxidizer. Some embodiments are configured to switch between these modes seamlessly without interruption to the operation of the burner. [0041] At least some of the present burner assemblies comprise a fresh air windbox and a TEG plenum coupled to a burner barrel (e.g., with the TEG plenum disposed in the windbox). Some of the present burners also comprise mechanisms for operating the burner in multiple modes, including the fresh air mode or the TEG mode. For such embodiments, in the TEG mode, fresh air is supplied to a windbox and is funneled into a burner barrel to mix with TEG, after which the mixture flows to a burn zone to burn fuel. The TEG is supplied to the TEG plenum from a gas turbine, and may be injected both through staged TEG ports and into the burner barrel via openings (e.g., slots) to mix with the fresh air. A damper, such as a slide damper, may be disposed in an "open" position or configuration to allow free flow of TEG into the burner barrel through the openings. For such embodiments, in the fresh air mode, fresh air is supplied to the windbox and is funneled into the burner barrel and from the barrel burner into a burn zone to burn fuel. In this fresh air mode, an upstream damper in the TEG supply line may be closed so that TEG flow is isolated from the TEG plenum, while a TEG vent damper is opened allowing the TEG to discharge to atmosphere. The damper may also be disposed in a "closed" position or configuration to prevent TEG from flowing into the burner barrel. In some of the present embodiments, these operational modes may allow for similar exit velocities for both modes despite much higher volumetric flow of TEG in the TEG mode. This similarity of exit velocities may be accomplished with a larger effective exit area (total cross-sectional area for flow) in the TEG mode. For example, in the TEG mode, both the burner barrel and a plurality of TEG staged ports may be used to pass flow; while, in the fresh air mode, only the burner barrel may be used to pass flowing air (not TEG). As described above, in the fresh air mode, the damper may isolate the TEG plenum from the burner barrel such that substantially all fresh air flow (e.g., less a small leakage flow, such as, for example, less than 10 percent of all fresh air flow entering the windbox) passes down the burner barrel. The TEG staged ports and the openings may be configured (e.g., via respective cross-sectional areas inversely proportional to their expected respective flow velocities).

[0042] Certain burner configurations are described in U.S. Patent No. 5,460,512 ("the '512 patent"), referenced above, the entirety of which is incorporated herein by reference. This burner assembly reduces ΝΟχ emissions by rapid entrainment of gases from the furnace volume into the combustion region. Aspects disclosed in the '512 Patent involve using the burner assembly as catalytic combustor in a cogeneration gas turbine system in which chemical energy is converted to mechanical, electrical, and/or thermal energy. Aspects disclosed in the '512 Patent may also be suited for applications in chemical processes that involve the oxidation of organic waste at high temperatures and pressures.

[0043] The '512 patent discloses single-stage and two-stage burner configurations. The single stage burner configurations operate with a large amount of excess combustion air, i.e., more than stoichiometric, supplied through burner plate slots, to keep the flame relatively cool to minimize the generation of ΝΟχ. Although excess-air burners are useful for duct heaters, they may be relatively inefficient for heating furnaces, boilers, and/or the like. For these latter applications, the '512 patent discloses a two-stage burner assembly having a secondary fuel gas and flue gas injection assembly.

[0044] The single-stage burner configurations disclosed by the '512 patent reduce ΝΟχ formation by as much as 80%. These effects are achieved by an arrangement of burner tubes and slots that envelopes gas with air and create desirable turbulence to produce a cone shape of an expanding gas stream. Under these conditions, ignition starts from the periphery of the cone shaped jets discharging from the burner plate slots, where fuel gas concentration is close to the lean flammability limit, and propagates by turbulent mixing of the recombustion gases to the jet centers. Thus, local fuel-air ratios during combustion do not exceed the average, based on total fuel and air input to the burner, and ΝΟχ formation is thereby diminished. As a result of the burner tube and slot arrangement, the width of the recirculating air zones between slots varies significantly in the radial direction. Thus, the recirculating areas of hot combustion products in the wake of the plates between slots vary significantly in the radial direction, so that local ignition patterns also vary. As a result, local oscillations of flame fronts tend to occur at different frequencies and are not synchronized.

[0045] The two-stage burner configurations disclosed by the '512 Patent also exhibit further reduction of ΝΟχ formation by as much as 95%. These effects are achieved by provision of a plurality of discrete secondary fuel gas injection tubes and forced recirculation flue gas injection tubes, both arranged around the primary air and fuel gas discharge assembly. Each injection tube has a discharge end portion that is radially spaced from the primary air and fuel gas discharge assembly. The secondary fuel gas injection tubes include an inlet portion adapted for coupling to a secondary fuel gas source, while the flue gas injection tubes include an inlet portion adapted for coupling to a flue gas recirculation line. During operation of the two-stage burner assembly, the flue gases generated in the combustion chamber flow to a flue gas stack where a portion of those gases are drawn into a recirculation line including a fan which feeds into the flue gas injection tubes. The secondary fuel gas, together with the recirculated flue gas, is then injected under pressure into the combustion flame at a particular region of the flame. Since the recirculated flue gases, as well as the secondary fuel gas, are discharged in a forced draft, the direction of the flue and fuel gas jets or streams discharged from the flue gas and secondary fuel gas tubes can be controlled to reach the combustion flame at the desired location. In this manner, two combustion zones can be generated in the combustion chamber such that ΝΟχ formation is minimized and a relatively high heat capacity maintained when low excess air burner input is required.

[0046] As may be readily appreciated, the burner configurations of the '512 Patent have certain features that may be implemented in embodiments of the present burners, such as, for example, a burner barrel, multiple gas spuds, and a burner plate with port slots for channeling combustion air and injected fuel into a combustion chamber. The present burner assemblies may achieve yet further reduction of ΝΟχ formation by using TEG as described in this disclosure.

[0047] Some embodiments of the present burner assemblies may be suited for use in a Steam Assisted Gravity Drainage (SAGD) processes for extracting oil from tar sand fields, but can also be utilized in other operations. Unlike related-but-similar combined cycle power generation or other similar applications that have high power output requirements and low steam production requirements, the unique requirement of the SAGD type of system is the requirement for high steam production and lower power production. Due to this set of requirements, the fuel turbine for generating electricity may be small in comparison to the once-through steam generator (boiler), such that TEG generated by the turbine only provides a fraction (60-70%) of the oxygen required for the Max Combustion Rating (MCR) of the boiler. This allows the system to run with low excess air rates from 70-100% loads, with a combustion air fan providing the rest of the air. At lower than -70% load, the total airflow remains constant, since the TEG flow is fixed.

[0048] FIGS. 1-2 show a first embodiment 10 of one of the present low-ΝΟχ turbine exhaust fuel burner assemblies configured to operate in either of (i) a fresh air mode with an oxidizer of fresh air or (ii) a TEG mode with an oxidizer of a combination of TEG and fresh air. In the embodiment shown, assembly 10 comprises a windbox 14, a combustion air source 18 configured to supply fresh air to windbox 14 via a fresh air inlet 22, and a TEG duct 26 defining a TEG inlet 30 configured to receive TEG from a turbine exhaust duct. In the embodiment shown, combustion air source 18 comprises a fan. In other embodiments, combustion air source can comprise any of various air movers (e.g., a fan, an air compressor, a fan and an air compressor, and/or the like). In addition to providing an oxidizer for combustion, fresh air flowing from combustion air source 18 can also play an important role in cooling internal components of the burner assembly and/or the windbox itself, such as, for example, due to convective cooling from combustion air, driven by the fan, flowing between the interior of the windbox and components of the burner assembly that are disposed within the windbox (e.g., TEG plenum 54). In some embodiments, such an air mover is driven and/or controlled by a variable frequency drive (VFD) configured to vary the output of the air mover, and/or combustion air source further comprises a control damper that is configured to vary the cross-sectional area available for flow out of the air mover (e.g., to vary the rate or speed of air flowing from the air mover).

[0049] In the embodiment shown, TEG duct 26 extends through windbox 14 via an opening 34. More particularly, in this configuration, TEG duct 26 is coupled to sidewall 38 of the windbox by an expansion joint 42. Expansion joint 42 is configured to both seal the interface between sidewall 38 and TEG duct 26, and provide a degree of mechanical isolation to allow for thermal expansion of (and resulting variations in relative positions of) TEG duct 26 and windbox 14.

[0050] FIG. 3 shows a side view of assembly 10 with a portion of sidewall 38 of windbox 14 cut away to reveal certain additional details of the assembly. As shown, in this embodiment, sidewall 38 of the windbox defines a chamber 46 and defines fresh air inlet 22 through the sidewall in fluid communication with the chamber. As also shown, the depicted assembly further comprises a TEG plenum 54 coupled to windbox 14 and in fluid communication with TEG plenum inlet 30. In this way, TEG may be ducted from a gas turbine to TEG inlet 30, where it passes into TEG duct 26 via TEG inlet 30, and through TEG duct 26 through the a portion of combustion air windbox 14 into TEG plenum 54. As shown, TEG does not mix with the contents (fresh air) of the outer portions of combustion air windbox 14. [0051] In the embodiment shown, TEG plenum 54 is disposed within the chamber (46) of windbox 14. More particularly, in this embodiment, TEG plenum 54 is coupled to a front wall 58 (FIG. 9) of windbox 14, and assembly 10 further comprises a slip connection 62 between windbox 14 and TEG plenum 54 to provide structural support of the TEG plenum and to allow for axial thermal expansion of the TEG plenum when hot TEG gases are present therein. For example, thermal expansion may be significant due to what may be significant temperature difference (e.g., nearly a 1000°F) in the TEG plenum between the TEG mode and the fresh air mode. In the embodiment shown, TEG plenum 54 comprises a sidewall 66 defining a chamber 70 and an inlet 74 through the sidewall of the TEG plenum that is in fluid communication with the chamber. In some embodiments, TEG plenum 54 (e.g., sidewall 66) can comprise un-insulated stainless steel and/or any of various other materials (e.g., metals and/or alloys) that retain sufficient strength at high temperatures. In at least some embodiments, TEG plenum 54 need not be insulated because windbox 14 encompasses or surrounds the TEG plenum and thereby protects users of the assembly from the hot uninsulated surfaces of the TEG plenum. In the embodiment shown, windbox 14 has a circular cylindrical shape; but may, in other embodiments, have any other shape (e.g., square or rectangular) that permits the functionality described in this disclosure. Similarly, TEG plenum 54 is shown with a circular cylindrical shape, but may have any other shape (e.g., square or rectangular) that permits the functionality described in this disclosure. Windbox 54 may comprise a variety of materials, such as, for example, standard carbon steel with several inches of insulation to protect users of the burner assembly.

[0052] FIGS. 4 and 5 show cutaway perspective and cross-sectional side views, respectively, of a burner barrel 78 and firing components of assembly 10. In the embodiment shown, burner barrel 78 comprises a sidewall 82 defining a plurality of openings 86 and a channel 90 extending between a first end (left) and a second end (right). In the depicted configuration, burner barrel 78 is coupled to windbox 14 and TEG plenum 54. More particularly, burner barrel 78 is coupled to windbox such that channel 90 is in fluid communication with the chamber of the windbox separately from or independent of openings (86); and the burner barrel is coupled to TEG plenum 54 such that openings can permit TEG to flow from the TEG plenum (chamber 70) into the channel of the burner barrel . In this embodiment, burner barrel 78 is disposed at least partially within (e.g., in a coaxial relationship, as shown, with) TEG plenum 54, and at least partially within (e.g., in a coaxial relationship, as shown, with) windbox 14. In the embodiment shown, a windbox mounting flange 94 comprises a back wall of TEG plenum 54, and includes a hole in its center that is configured to, as shown, receive and support burner barrel 78 relative to the mounting flange and TEG plenum.

[0053] In the embodiment shown, burner barrel 78 comprises an elongated tubular shape, and openings 86 are shaped as elongated slots spaced circumferentially around the perimeter of the burner bailer. In this embodiment, slots 26 are elongated coaxially with the length of the burner barrel, and extend through sidewall 82 in communication with channel 90 to enable fluid communication between TEG plenum 54 (chamber 70) and the burner barrel 22 (channel 90). In the embodiment shown, assembly 10 further comprises one or more dampers 98 coupled to the burner barrel and configured to be moved between at least: (i) a first configuration in which the damper(s) cover openings 86 to substantially prevent TEG from entering the burner barrel through the openings; and (ii) a second configuration in which the damper(s) do not cover at least a portion of the openings to permit TEG to enter the burner barrel through the openings. More particularly, in the embodiment shown, the one or more dampers comprise a slide damper 98 disposed around burner barrel 78 such that the slide damper is slidable between the first configuration and the second configuration. More particularly, as shown, slide damper 98 comprises a cylindrical ring slidable coaxially along a portion of the length of the burner barrel between the two configurations to completely cover slots 86 when closed and to completely expose or uncover slots 86 when opened. In the embodiment shown, damper 98 is configured to be moved by damper lever 102 that extends out of TEG plenum 54 through flange 94 such that the damper lever can be coupled to an actuator (e.g., a linear actuator, servo, rack-and-pinion, and/or the like), such as, to enable automated actuation of the damper. When in the "open" position or configuration, damper 98 may have no operational impact and may cause no restriction of flow through slots 86.

[0054] In the embodiment shown, assembly 10 further comprises a burner plate 106 coupled to the end of burner barrel 78, a CFG gun fuel spud 110, a plurality of core fuel spuds 114, a plurality of inner fuel spuds 118, and a plurality of outer fuel spuds 122. In this embodiment, CFG gun fuel spud 1 10 extends from outside windbox 14, along and through the center of burner barrel 78, and out through a central hole in burner plate 106; six core fuel spuds 114 extend from a core fuel ring 126 through openings in burner plate 106; thirty-six inner fuel spuds 1 18 extend from an inner fuel ring 130 up to slot ports 134 in burner plate 106; and six outer fuel spuds 122 extend from an outer fuel ring 138 that encircles burner barrel 78. As shown, outer fuel spuds 122 extend beyond and about burner plate 106.

[0055] As best shown in FIG. 5, assembly 10 includes four fuel zones defined by the nozzle outlets of the fuel spuds, including a CFG gun zone, a core zone, and inner and outer zones, respectively corresponding to the outlets of CFG gun fuel spud 110, core fuel spuds 114, inner fuel spuds 118, and outer fuel spuds 122. This arrangement allows for dramatically different fuel splits based on firing condition (Fresh Air or TEG mode), providing optimal mixing and operation. Other configurations for the fuel spuds are possible, including variations in the length to which the fuel spuds extend into, about, or out of burner barrel 78, the spatial location of the fuel spuds with respect to each other and other components of the burner assembly, and/or the number and type of fuel spuds themselves.

[0056] FIGS. 6-8 show a refractory port ring 142 having an aperture 146 in its center and staged ports 150 that penetrate port ring 142. Staged ports 150 may function to inject TEG directly into a boiler via angled, round ports passing through a refractory front wall of the boiler. In some embodiments, staged ports 150 may be disposed circumferentially around the burner centerline, and contain an exit angle so TEG flow is injected inward toward a central, longitudinal axis of the port ring. In this embodiment, port ring 142 also has six fuel spud holes 154 so port ring 142 can be installed over outer fuel spuds 122 such that port ring 142 aligns with burner barrel 78 and surrounds burner plate 106. As shown in FIG. 7, staged ports 150 and fuel spud holes 154 extend from front to back through ring 142, to cooperate with a combustion chamber wall 158. Staged ports 150 may be angled and, in this embodiment, are angled in a direction toward the centerline of the burner barrel 78. Fuel spud holes 154 may longitudinally extend in a same direction as outer fuel spuds 122. As shown in FIG. 8, staged ports 150 may be arranged circumferentially around aperture 146. When TEG flows through TEG plenum 154, TEG can enter the burner barrel through slots 82 in the burner barrel, and can also through staged ports 150 of port ring 142. In other embodiments, staged ports 150 can be modified to produce different results by adjusting the angle, penetration, pitch, and/or the like. [0057] FIG. 9 shows the flow of TEG through assembly 10 in the TEG mode. As shown, TEG plenum 54, mounted to burner barrel 78 by windbox mounting flange 94, delivers TEG both through angled staged ports 150 through port ring 142, and through slots 86 around burner barrel 78 to mix with fresh air from the combustion air windbox 14. As mentioned above, staged ports 150 in port ring 142 can be modified to produce different results by adjusting the angle, penetration, and pitch. For slots 86, the aspect ratio, and penetration can also be modified to affect results. Configuring these features in accordance with the present disclosure may ensure that burner assembly 10 sufficiently mixes fuel and oxygen to produce only trace quantities of unburned combustion products while operating with low excess air for both Fresh Air and TEG modes of operation.

10058] Slots 86 can be isolated with slide damper 98 by actuation of damper lever 102. When so isolated, large flows of fresh air are prevented from passing through staged ports 150 when operating in fresh air mode. When closed, slide damper 98 may permit a small amount of leakage for cooling of staged ports 150. In the embodiment shown, the volumetric flow when firing with TEG is roughly twice the flow compared to fresh air firing. Ports 150, slots 86, and slide damper 98, working in conjunction, allow the burner to run burner pressure drops that are very similar for both TEG and fresh air modes. With these very similar pressure drops, the burner can operate with very similar flame envelopes.

[0059] CFG gun fuel spud 110 extends through a central hole in burner plate 106. The configuration of the CFG gun fuel spud 1 10, core fuel spuds 1 14, inner fuel spuds 1 18, and outer fuel spuds 122, provide assembly 10 with the ability to operate with significantly different fuel zone splits based on firing condition (Fresh Air or TEG mode), and thereby optimize mixing and operation in both modes.

[0060] Functionally, assembly 10 can be operated in a fresh air mode, particularly for initial firing of the burner, as well as in a TEG mode that includes drawing TEG into burner barrel 78 and combustion chamber along with combustion air via both combustion air windbox 14 and TEG plenum 54. As previously described, the combustion air can be driven by a forced draft fan as a combustion air source 18. About 10-15% of maximum capacity combustion air is desirable from a forced draft fan to keep windbox 14 cool. In the fresh air mode, the fan forces fresh air into windbox 14 and the fresh air is then taken into burner barrel 78 through barrel air inlet 162. The fresh air is forced through burner barrel 78 past the fuel zones and fuel spud outlets for ignition when mixed with injected fuel.

[0061] FIG. 10 shows a block diagram of an embodiment of the present burner assembly control systems. In this embodiment, burner assembly 1000 may have many or all of the features described above, such as a TEG plenum receiving TEG from gas turbine 1012. The TEG plenum may be configured to introduce TEG, as governed by a damper, to a burner of burner assembly 1000 via openings in a burner barrel, and to introduce TEG to a boiler via one or more TEG ports. Turbine duct damper 1010 may regulate flow of TEG to the TEG plenum, and a damper may regulate flow from the TEG plenum to the burner barrel as described above. Vent damper 1008 allows the discharge of TEG to atmosphere when the turbine is running and the burner system is not operating in TEG mode. A fresh air source, such as a fan 1004, may receive air from combustion air intake 1002 and supply air to the fresh air windbox of burner assembly 1000. Fan 1004 may have variable frequency drive 1022 and fan control damper 1006 that may be operated, by one or more electronic control units 1018, to control the rate of airflow to the fresh air windbox.

[0062] One or more electronic control units 1018 may include computer processors and computer-readable media that receive flow data signals FT and temperature data signals TT from combustion air intake 1002. Electronic control units 1018 may also receive flow data signals FT and temperature data signals TT from turbine air line 1014 and turbine fuel line 1016 supplying gas turbine 1012. Electronic control units 1018 may further receive a turbine trip status signal from turbine breaker 1020 supplying electrical power to gas turbine 1012. As further detailed below, electronic control units 1018 may generate (e.g., based on the flow data signals FT, the temperature data signals TT, and the turbine trip status signal) various control signals SI to S5 that respectively implement control of variable frequency drive 1022, fan control damper 1006, vent damper 1008, burner assembly 1000, and turbine duct damper 1010.

[0063] FIG. 11 shows a flowchart illustrating an embodiment 1 100 of the present methods for operating a low ΝΟχ burner assembly (e.g., 10). Method 1 100 may begin at block 1 101 , which includes flowing TEG from a gas turbine through a TEG duct (e.g., 26) to a TEG plenum (e.g., 54). From the TEG plenum, at block 1 102, TEG flows to burner barrel (e.g., 78), which is coupled to (and may be disposed within) the turbine exhaust plenum. [0064] Block 1 103 involves the flow of TEG and fresh air to a burner barrel of the low ΝΟχ burner to burn fuel, in a TEG mode. The TEG flows from the gas turbine through a TEG inlet (e.g.., 30), through a TEG duct (e.g., 26), and into the TEG plenum. TEG then flows from the TEG plenum proceeds to flow into the burner barrel (e.g., via slots 86), if a TEG damper (e.g., 86) is in an open position (i.e. not covering slots 86). In the burner barrel, the TEG mixes with fresh air which enters the burner barrel (e.g., through air inlets 162). The mixture of TEG and fresh air in the burner barrel is then fed to one or more fuel zones via (e.g., an end of) the burner barrel. Concurrent with the feeding of the mixture of fresh air and TEG to the one or more fuel zones via the burner barrel, TEG is flowed from TEG plenum to the one or more fuel zones via staged ports (e.g., 150). The flow of TEG and the flow of the mixture of TEG and air to the one or more fuel zones collectively serve as the oxidizer in burning fuel in the one or more fuel zones, in a TEG mode.

[0065] At block 1104, the flow of fresh air to the burner barrel is regulated based on the flow of TEG to the burner barrel. In this way, just enough fresh air is supplied to the burner assembly to supplement the TEG as an oxidizer. In some aspects, the regulation of air flow may be implemented by measuring the temperature of the TEG, the differential flow of the TEG, and/or the oxygen concentration of the TEG to determine how much fresh air should be supplied to burner assembly 22. Alternatively, and as explained in greater detail below with reference to FIG. 12, in lieu of a differential pressure flowmeter used in the TEG exhaust, fuel flow and air flow to the fuel turbine may be measured and temperature compensated. Because the correct amount of fresh air supply is determined during operation of the low ΝΟχ burner, with corresponding changes to the flow of fresh air from the fresh air source, the low ΝΟχ burner can be operated with low exhaust excess air.

[0066] At least some of the present burners can be configured to seamlessly switch to and operate in a fresh air mode. Consistent with this, block 1 105 involves switching from the TEG mode to a fresh air mode by, in part, ceasing TEG flow to the burner barrel. This may be implemented by moving the damper (e.g., 98) relative to (e.g., along the longitudinal axis of) the burner barrel to cover the slots (e.g., 86). The fresh air mode also involves continuing the flow and, typically, increasing the flow of fresh air to the burner barrel via air inlets (e.g., 162). The fresh air then flows to the burner zone where it is used to burn fuel in the fresh air mode. [0067] Block 1 106 involves switching back to the TEG mode from the fresh air mode. To resume the TEG mode, flow of TEG to the burner barrel is resumed by moving the damper relative to the burner barrel to uncover the slots (e.g., sliding damper 98 along the longitudinal axis of the burner barrel in the opposite direction as previously described) to reopen the slots. Resumption of the TEG mode involves continuing the flow and, typically, decreasing the flow of fresh air to the burner barrel via the air inlets. The mixture of fresh air and TEG then flows to the one or more fuel zones where it resumes burning fuel in the TEG mode.

[0068] FIG. 12 shows another flowchart illustrating another embodiment of the present methods of operating a burner assembly, such as, for example, as may implement an algorithm operable to switch the burner assembly to and/or from a fresh air only mode and a TEG mode of operation. Beginning at block 1200, the burner assembly may operate in a fresh air only mode. Operating the burner assembly at block 1200 may include operating with a damper closed to prevent, reduce, or restrict introduction of turbine exhaust gas (TEG) to a burner of the burner assembly. With a TEG source disabled, closing of the damper may also prevent too much fresh air from being misdirected from the burner barrel to the TEG plenum. Processing may proceed from block 1200 to block 1202.

[0069] At block 1202, the one or more computer processors may make a determination whether to switch from the fresh air only mode of operation to a TEG mode of operation. For example, the one or more computer processors may determine that an input has been received, from a human machine interface, to trigger a switch from the fresh air only mode to the TEG mode. If it is determined, at block 1202, not to switch to the TEG mode, then processing may return from block 1202 to block 1200. However, if it is determined, at block 1202, to switch to the TEG mode, then processing may continue to block 1204.

[0070] At block 1204, a sequence may be carried out to switch from fresh air only mode to TEG mode without requiring a shutdown. In operation, it is envisioned that a burner light off sequence may occur in either fresh air mode or in TEG mode. For example, fuel may be injected from one of more of the fuel spuds while combustion air may be forced through the burner barrel across a pilot light and a flame is ignited. When the burner is at lower firing rates (<40%), a Human Machine Interface (HMI) allows the operator to switch between Fresh Air mode and TEG mode or vice versa. Switching between these modes involves a sequence of operation. In some aspects, the sequence for switching from fresh air mode to TEG mode, at block 1204, may be carried out as follows:

1. TEG ducting line must be at or above a minimum temperature;

2. Operator initiates a change-over;

3. Burner modulates to Fresh- Air low fire;

4. TEG mode output from burner management system (BMS) is energized;

5. Fan control damper and VFD move to TEG light-off position;

6. Burner Slide Damper opens;

7. Fuel flow control valves (FCVs) move to a TEG light-off position; and

8 Turbine Duct Damper and vent damper move in concert to introduce TEG to the system by movement of the vent damper to a closed position and opening of the duct damper.

Processing may proceed from block 1204 to block 1206.

[0071] At block 1206, the one or more computer processors may operate the burner assembly in the TEG mode, including operating with the damper open, thereby allowing introduction of TEG to the burner of the burner assembly. It is also envisioned that operating the burner assembly in the TEG mode, at block 1206, may include adjusting an airflow set point of a combustion air source supplying a fresh air windbox of the burner assembly based on flow and temperature data. To this end, block 1206 may include metering both the oxygen from the combustion air fan and from the TEG to determine total air flow. It is desirable for TEG pressure drop to be minimized. In lieu of a differential pressure flowmeter used in the TEG exhaust, the fuel flow and air flow to the fuel turbine may be measured and temperature compensated. Thus, adjusting the airflow set point, at block 1206, may include determining a TEG equivalent airflow based on a measured volumetric flow of combustion air supplying a gas turbine that is a source of the TEG, and based on a measured volumetric flow of fuel supplying the gas turbine. Both of these volumetric flows may be corrected for ambient temperature and normalized to standard temperature and pressure. Adjusting the airflow set point, at block 1206, may also include subtracting the TEG equivalent airflow from a desired total airflow to determine the airflow set point of the combustion air source. [0072] In certain aspects, the operations carried out at block 1206 may include using the measured flows to determine the equivalent mass flow of combustion air employing the following Equations [l]-[4].

Input Variables:

QGT,Air : The measured volumetric flow of the combustion air supplying the Gas Turbine, corrected for ambient temperature, and normalized to standard temperature and pressure.

QcT.Fuei : The measured volumetric flow of the natural gas fuel supplying the Gas Turbine, normalized to standard temperature and pressure.

Calculated Variables:

QcT.Totai : The total volumetric flow of the Gas Turbine exhaust gas, normalized to standard temperature and pressure.

Φ : The stoichiometry of the Gas Turbine combustion reaction. This is the ratio of air to fuel, corrected for the airflow required to burn a given amount of fuel. A Φ >1 would have an excess of air to burn a set amount of fuel, a Φ <1 would have insufficient air to burn a set amount of fuel, and a Φ =1 would have exactly the amount of air required to burn a set amount of fuel.

%02xEG vol,wet · The volumetric percentage of oxygen in the Turbine Exhaust Gas. "Wet" designates that water is included, rather than compared to "Dry" when water is not included in the calculation.

Qi Air Flow Equiv ^: The equivalent fresh air flow in the TEG, normalized for standard temperature and pressure. Required to compare and summarize the oxygen contribution of fresh air and TEG Q, GT,Total = 0, GT, Air + 0, GT, Fuel [1] , A _i r 9.57xQ _{GT Fuel}

Φ = + 1

, Air [2]

%02 TEG, vol wet = 21.3649 x (Φ - 1) - 0.8459 [3]

%02 _TEG , vol wet

Q A, ir Flow Equiv 20.7% [4]

[0073] Since the TEG is a fixed uncontrollable flow, the operations carried out at block 1206 may subtract the flow of TEG equivalent airflow from a desired total airflow to determine the airflow set point of the combustion air fan. In aspects implementing a fan as a combustion air source, then a control loop may be implemented on a variable frequency drive (VFD) and damper control on the fan to adjust for variations in TEG flow and TEG 0 ₂ and thereby maintain a desired (e.g., low) 0 ₂ . Processing may proceed from block 1206 to block 1208.

[0074] At block 1208, the one or more computer processors may make a determination whether to switch from the TEG mode of operation to the fresh air only mode of operation. For example, the one or more computer processors may determine that an input has been received, from a human machine interface, to trigger a switch from the TEG mode to the fresh air only mode. Alternatively or additionally, the one or more computer processors may detect a gas turbine trip while operating in the TEG mode, and determine to perform switching of the burner assembly from the TEG mode to the fresh air only mode in response to detecting the gas turbine trip. If it is determined, at block 1208, not to switch to the TEG mode, then processing may return from block 1208 to block 1206. However, if it is determined, at block 1208, to switch to the fresh air only mode, then processing m ay proceed to bl ock 1210.

[0075] At block 1210, a sequence may be carried out to switch from the TEG mode to the fresh air only mode without requiring a shutdown of the burner assembly. An example sequence for switching back from TEG mode to fresh air mode, at block 1212, is as follows:

1. Operator initiates change-over; 2. Burner modulates to TEG low fire;

3. Turbine Duct Damper and vent damper move in concert to remove TEG from the system, by movement of the vent damper to an open position and closing of the duct damper;

4. TEG mode output from BMS is de-energized;

5. FCVs move to a Fresh-Air light-off position;

6. Burner Slide damper closes;

7. Fan control damper and VFD move to Fresh-air light-off position; and

8. System delays release to modulate for a predetermined time interval to allow the system to stabilize.

[0076] If any part of the sequence fails, the system may revert to the previous operating mode. This sequence involves adjusting airflow, dramatically changing the split of fuel flow, moving damper 9, as well as operating TEG ducting dampers (external to the burner assembly).

[0077] In summary implementing the methods and systems of the present disclosure provide solutions that, alone or in combination, achieve one or more technological advantages. For example, because there is seamless switch between TEG mode and fresh air mode, low ΝΟχ burners can be operated so as to minimize a design unscheduled shutdowns. Because of this, low ΝΟχ burners may operate with fresh air only so that steam may be generated even when a gas turbine is not running in a combined cycle system. This advantage is significant because the loss of heat and steam in certain applications, for even a short period, may cause a significant impact on production, and thus can be extremely costly. Additionally, low ΝΟχ burners according to embodiments of the disclosure further reduce combustion exhaust levels of burners for environmental and health reasons as well as to meet governmental regulations for low ΝΟχ emissions of commercial burners, while operating combustion equipment with a minimal amount of excess air. Further yet, the configuration of the four fuel zones as described herein optimizes thermal efficiency of operation of industrial boilers.

[0078] The above description is illustrative and is not restrictive. Many variations of the disclosure will become apparent to those skilled in the art upon review of the disclosure. One or more features from any aspect described herein may be combined with one or more features of any other aspect without departing from the scope of the disclosure. The scope of the disclosure should, therefore, be not determined with reference solely to the above description, but instead should be determined with reference to the pending claims along with their full scope or equivalents in view of the above description.

[0079] Although the present disclosure and its advantages have been described in detail, it should be understood that various changes, substitutions and alterations can be made herein without departing from the spirit and scope of the disclosure as defined by the appended claims. Moreover, the scope of the present application is not intended to be limited to the particular aspects of the process, machine, manufacture, composition of matter, means, methods and steps described in the specification. As one of ordinary skill in the art will readily appreciate from the disclosure of the present disclosure, processes, machines, manufacture, compositions of matter, means, methods, or steps, presently existing or later to be developed that perform substantially the same function or achieve substantially the same result as the corresponding aspects described herein may be utilized according to the present disclosure. Accordingly, the appended claims are intended to include within their scope such processes, machines, manufacture, compositions of matter, means, methods, or steps.