Electric-field-based combustion control systems use electric fields to manipulate the movement of electrically charged molecules (e.g., ions) that are a natural production of the combustion process. The controlled electric field creates electrostatic forces (e.g., Coulombic body forces) within a gas cloud created by the combustion process that can be manipulated to control flame shape, heat transfer, and other flame characteristics. At the same time, the controlled electric field can help influence combustion chemistry to suppress formation of pollutants at the flame source.
Generally, these combustion control systems involve the use of one or two or more tubular, planar, or post-type electrodes fabricated from macroscopic metallic sheets, pipes, or rods. However, the ability of such electrodes to control electric fields can be limited and lacking in precision. Moreover, such electrodes can be susceptible to heat-induced failure and/or significant wear.
Therefore, developers and users of combustion control systems continue to seek improved designs for combustion control systems and methods of manufacturing of combustion control systems.
Embodiments of the invention relate to combustion control electrode assemblies, combustion control systems using such electrode assemblies, and methods of manufacturing and using such electrode assemblies. The electrode assemblies may include one or more electrodes formed from and/or including a sintered refractory metal material exhibiting enhanced heat and/or wear resistance.
In an embodiment, an electrode assembly for a combustion control system may include at least one substrate and at least one electrode formed on the at least one substrate. The at least one electrode may include a sintered refractory metal material. The at least one electrode may be configured to be mounted proximate to or contacting a flame. The electrode assembly may further include at least one voltage source operatively coupled to the at least one electrode. The at least one electrode and the at least one voltage source may be collectively configured to apply an electric field to one or more regions at least proximate to the flame.
In an embodiment, a combustion control system may include a combustion chamber including one or more walls at least partially defined by at least one electrode assembly. The at least one electrode assembly includes at least one substrate having at least one electrode formed thereon. The at least one electrode may include a sintered refractory metal material. The at least one electrode may be configured to be positioned proximate to or contacting a flame. The combustion control system may further include at least one voltage source operatively coupled to the at least one electrode. The at least one electrode and the at least one voltage source may be collectively configured to apply an electric field to one or more regions at least proximate to the flame.
In an embodiment, a method of manufacturing an electrode assembly for a combustion control system may include providing one or more precursor refractory metal materials on a substrate. The one or more precursor refractory metal materials may include a plurality of refractory metal material particles. The method may further include sintering at least a portion of the one or more precursor refractory metal materials on the substrate to form one or more electrodes. The one or more electrodes may be configured to be operatively coupled to one or more voltage sources so that an electric field can be applied to one or more regions at least proximate to a flame to control one or more combustion characteristics of the flame.
In an embodiment, a method of controlling combustion characteristics of a flame includes providing at least one electrode assembly including at least one substrate having a plurality of electrodes formed thereon that are positioned proximate to or contacting a flame. At least a number of the plurality of electrodes may include a sintered refractory metal material. The method may further include applying an electric field to one or more regions at least proximate to the flame via one or more voltage sources operatively coupled to the electrodes. The method may additionally include varying application of the electric field to control one or more combustion characteristics of the flame.
Features from any of the disclosed embodiments may be used in combination with one another, without limitation. In addition, other features and advantages of the present disclosure will become apparent to those of ordinary skill in the art through consideration of the following detailed description and the accompanying drawings.
Embodiments of the invention relate to combustion control electrode assemblies, combustion control systems using such electrode assemblies, and methods of manufacturing and using such electrode assemblies. The electrode assemblies may include one or more electrodes formed from and/or including a sintered refractory metal material exhibiting enhanced heat and/or wear resistance. In the following detailed description, reference is made to the accompanying drawings, which form a part hereof. In the drawings, similar symbols typically identify similar components, unless context dictates otherwise. Other embodiments may be used and/or other changes may be made without departing from the spirit or scope of the disclosure.
In the illustrated embodiment, each of the electrodes 104 is formed in a generally strip or bar-like geometry. However, in other embodiments, the electrodes 104 may be formed in a variety of different geometries. Moreover, while twelve electrodes are shown, in other embodiments, the combustion control system 100 may include one, two, three, six, ten, or any other suitable number of electrodes. Additionally, while the combustion control assembly 100 is shown including only a single row of the electrodes 104, in other embodiments, the electrodes 104 may be arranged in one or more different patterns. For example, the electrodes 104 may be arranged in two rows, three rows, five rows, or any other suitable number of rows. In other embodiments, the electrodes 104 may be arranged in a generally circular pattern, a generally spiraling pattern, a generally rectilinear pattern, along one or more linear paths, along one or more arcuate paths, combinations thereof, or in any other suitable pattern or arrangement. Such configurations may help the electrodes 104 control the characteristics of the flame 106 at different locations and/or times during the combustion process.
At least one, two or more, or each of the electrodes 104 may be formed from and/or include a sintered refractory metal material. In an embodiment, the sintered refractory metal material includes sintered molybdenum, tungsten, niobium, tantalum, rhenium, alloys of one or more of the foregoing metals, combinations thereof, or any other suitable sintered material. For example, the alloys may be solid solution alloys, multi-phase alloys, intermetallic compounds (e.g., molybdenum disilicide, MoSi2), or combinations thereof. Such sintered refractory metal materials may enable the electrodes 104 to resist heat and/or wear due to the material properties of the sintered refractory metal materials. For example, the sintered refractory metal material may exhibit a melting temperature or temperature range (e.g., a solidus temperature or a liquidus temperature) of about 1600° C., about 1800° C., about 2000° C., about 2200° C., 2400° C., 2600° C., 2800° C., 3000° C., 3000° C., or about 3200° C. In other embodiments, the sintered refractory metal material may exhibit a melting temperature or temperature range between about 1600° C. and about 3500° C.; about 1800° C. and about 3200° C.; about 2000° C. and about 3000° C.; or about 2300° C. and about 2800° C. In other embodiments, the sintered refractory metal material may exhibit higher or lower melting temperatures or temperature ranges. Thus, the electrodes 104 may be configured to withstand relatively high temperatures making them particular well suited for use in the combustion control system 100. In an embodiment, a sintered metal material or a sintered refractory metal material may be interchanged.
In an embodiment, at least one, two or more, or each of the electrodes 104 may include one or more electrically conductive coatings formed thereon. For example, the one or more conductive coatings exhibit an electrical resistivity less than an electrical resistivity of the sintered refractory metal material. Such electrically conductive coatings may include, for example, tin, manganese, vanadium, cobalt, zinc, cadmium, rhodium, chromium, titanium, nickel, silver, gold, alloys of one or more of the foregoing metals, combinations thereof, or any other suitable electrically conductive material. Such coatings may increase the electrical conductivity of the overall/composite electrodes 104 having the coating thereon. The one or more conductive coatings may be formed and/or deposited on the electrodes 104 via electroplating, electroless plating, combinations thereof, or via any other suitable application technique. For example, as the substrate 108 is relatively electrically insulative, the one or more conductive coatings may be preferentially deposited via electroplating on the electrodes 104 without electroplating coating material on intervening portions of the substrate 108 between the electrodes 104.
Referring still to
The substrate 108 may further exhibit any suitable thickness. For example, in an embodiment, the substrate 108 may exhibit a thickness of about 0.001 inches to about 0.8 inches; about 0.005 inches to about 0.25 inches; about 0.01 inches to about 0.02 inches; or about 0.1 inches to about 0.3 inches. In other embodiments, the substrate 108 may include one or more portions exhibiting a larger or smaller thickness. Thus, the substrate 108 may be configured to provide structural support to the electrodes 104, the combustion control system 100, one or more components of a combustion system, or combinations thereof. For example, in an embodiment, the substrate 108 may form at least a portion of a burner body, a support surface, a furnace wall, a combustion chamber wall, combinations thereof, or any other suitable support structure.
The substrate 108 may be made from a number of different heat-resistant materials. In an embodiment, the substrate 108 may be made from and/or include one or more ceramic materials, such as, beryllium oxide (“BeO”), alumina (“Al2O3”), an alumina-based ceramic, aluminum nitride (“AlN”), silicon carbide (“SiC”), silicon nitride (“Si3N4”), boron carbide (“BC”), boron nitride (“BN”), combinations thereof, or any other suitable ceramic material. Such materials may help the substrate 108 provide dimensional or structural stability to the electrodes 104. For example, the substrate 108 and the materials from which the substrate 108 are formed may exhibit a thermal expansion coefficient of less than about 4 ppm/K; less than about 5 ppm/K; less than about 7 ppm/K; less than about 10 ppm/K; or less than about 12 ppm/k. In an embodiment, the substrate 108 and the materials from which the substrate 108 are formed may exhibit a thermal expansion coefficient between about 3 ppm/K and about 12 ppm/K; between about 4 ppm/K and about 11 ppm/K; between about 5 ppm/k and about 10 ppm/K; or between about 6 ppm/K or about 9 ppm/K. In other embodiments, the substrate 108 may include one or more ceramic materials exhibiting higher or lower thermal expansion coefficients, as desired or needed for a particular application. Thus, the material properties of the substrate 108 may be selected to help support the electrodes 104, the combustion control system 100, and one or more components of a combustion system.
In other embodiments, the substrate 108 may be configured to help limit heat transfer through the combustion control system 100. For example, where limited or relatively minimal heat transfer through substrate 108 is desired, the substrate 108 may include one or more ceramic materials (e.g., silicon nitride, boron carbide, combinations thereof, or the like) exhibiting a thermal conductivity at about 600° C. of less than about 60 W/mK, less than about 50 W/mK, less than about 40 W/mK, or less than about 30 W/mK. In other embodiments, the substrate 108 may include one or more ceramic materials exhibiting a thermal conductivity at about 600° C. of between about 20 W/mK and about 60 W/mK; between about 30 W/mK and about 50 W/mK; or between about 35 W/mK and about 45 W/mK so that the substrate 108 may help insulate the combustion control system 100.
In other embodiments, the substrate 108 may include one or more ceramic materials exhibiting higher or lower thermal conductivities. For example, in an embodiment, the substrate 108 may include one or more ceramic materials (e.g., beryllium oxide, aluminum nitride, silicon carbide, combinations thereof, or any other suitable material) configured to help enable heat transfer through the combustion control system 100. In an embodiment, the substrate 108 may include one or more ceramic materials exhibiting a thermal conductivity greater than about 60 W/mK, greater than about 70 W/mK, greater than about 100 W/mK, or greater than about 220 W/mK. In other embodiments, the substrate 108 may include one or more materials exhibiting a thermal conductivity at about 600° C. of between about 60 W/mK and about 220 W/mK; between about 80 W/mK and about 180 W/mK; between about 100 W/mK and about 160 W/mK; or between about 120 W/mK and about 140 W/mK. In other embodiments, the substrate 108 may include one or more ceramic materials exhibiting higher or lower thermal conductivities. Thus, the substrate 108 may be made from selected ceramic materials to help the combustion control system 100 dissipate heat.
Referring still to
The electric field may be at least partially controlled to manipulate movement of electrically charged molecules (ions) that are a natural product of the combustion process. For example, the controlled electric field may create electrostatic forces (e.g., Coulombic body forces) within a gas cloud of the flame 106 that may be manipulated to control flame shape, combustion chemistry, heat transfer through or away from a surface, or combinations thereof, as desired. For example, in an embodiment, the voltage source 110 may be configured to apply a substantially constant voltage or time-varying voltage to one or more of the electrodes 104 to generate a substantially constant or time-varying electric field strength. In another embodiment, the voltage source 110 and the electrodes 104 may be collectively configured to vary application of the electric field to the flame 106 at selected times and/or locations. In other embodiments, the voltage source 110 may be configured to change a polarity of the voltage applied to the one or more of the electrodes 104. In an embodiment, the voltage source 110 may be configured to vary a magnitude or frequency of a voltage applied by the voltage source 110 to one or more of the electrodes 104 at selected times and/or locations.
By controlling a timing, a direction, a strength, a location, a wave form, or a frequency spectrum of the electric field, or combinations thereof, the combustion control system 100 may be configured to influence combustion characteristics of the flame 106, flame shape of the flame 106, heat transfer from the flame 106, or combinations thereof. Causing a response in the flame 106 may include causing a visible response in the flame 106. Additionally or alternatively, causing a response in the flame 106 may include causing increased mixing of fuel and oxidizer in the flame 106. Causing the increased mixing of fuel and oxidizer may increase a rate of combustion. Additionally or alternatively, causing the increased mixing of fuel and oxidizer may increase fuel and air contact in the flame 106. Additionally or alternatively, causing the increased mixing of fuel and oxidizer may decrease a flame temperature. Additionally or alternatively, causing the increased mixing of fuel and oxidizer may decrease an evolution of oxides of nitrogen (“NOx”) by the flame 106. Additionally or alternatively, causing the increased mixing of fuel and oxidizer may decrease an evolution of carbon monoxide (“CO”) by the flame 106. Causing the increased mixing of fuel and oxidizer may increase flame stability and/or decrease a chance of flame blow-out. Additionally or alternatively, causing the increased mixing of fuel and oxidizer may increase flame emissivity. Additionally or alternatively, causing the increased mixing of fuel and oxidizer may decrease flame size for a given fuel flow rate.
While only one of the voltage sources 110 is shown in the illustrated embodiment, in other embodiments, the combustion control system 100 may include two, three, four, six, or any other suitable number of voltage sources. For example, in an embodiment, each of or some of the electrodes 104 may be coupled to a respective one of the voltage sources 110.
In an embodiment, the combustion control system 100 may include a burner 114 configured to support the flame 106. The burner 114 may be configured as another electrode and may be in electrical contact with a conductive surface of the flame 106. In other embodiments, the burner 114 may be configured to provide a counter voltage to cooperate with the electrodes 104 to produce the electric field. In other embodiments, the electric potential of the burner 114 may be isolated from the ground and from the voltage source 110 such that the burner 114 is electrically floating. While one burner 114 is shown, in other embodiments, the combustion control system 100 may include two, three, five, thirty, or any other suitable number of burners 114. Moreover, the burner 114 may comprise a gas burner, an oil burner, an electric burner, a can burner, a cannular burner, an annular burner, a double annular burner, or any other suitable type of burner.
The electrode assembly 102 may be formed by a number of different processes. For example, the electrode assembly 102 may be formed via a thick-film process, an inkjet-type deposition process, a selective laser sintering process, a liquid deposition process, combinations thereof, or any other suitable process.
The method 200 includes an act 252 of positioning a stencil 260 on a substrate 208. The stencil 260 may include one or more openings 261 (e.g., slots or holes) formed therein that may define one or more patterns that at least partially determines the placement and/or physical dimensions of electrodes 204 to be formed on the substrate 208. For example, The stencil 260 may typically be made from a durable material, such as stainless steel or other suitable material. For example, the one or more openings 261 may be formed in one or more patterns, such as lines, curves, rectangles, geometric shapes, irregular geometric shapes, waves, combinations thereof, or the like. In an embodiment, the stencil 260 may exhibit a uniform thickness that may at least partially determine the thickness of the electrodes 204. In other embodiments, the stencil 260 may include one or more portions exhibiting varying thicknesses such that the thicknesses of the electrodes 204 may vary from one electrode to another or the thickness of one electrode 204 may vary. In addition, the stencil 260 may include one or more generally planar and/or curved surfaces. Accordingly, the stencil 260 may be configured such that the electrodes 204 may be formed on the substrate 208 from simple to complex patterns, fine patterns, combinations thereof, or in any suitable pattern. The stencil 260 may be formed of stainless steel or any other suitable material.
Next, the method 200 may include an act 254 of depositing a quantity of thick film paste 264 or other one or more precursor refractory metal materials on the stencil 260 that is now supported on the substrate 208. In another embodiment, a screen may placed over the stencil 260 and the thick film past 264 may be deposited on the screen. In an embodiment, the one or more precursor refractory metal materials of the thick film paste 264 may include one or more types of refractory metal material particles that have been pulverized into particulate form (e.g., a powder having an average particle size from nanometer-size scale to micron scale) and mixed with an organic binder that may have optional other glass and ceramic particles. For example, the one or more types of refractory metal material particles may include molybdenum particles, tungsten particles, niobium particles, tantalum particles, rhenium particles, particles made from alloys of one or more of the foregoing metals, combinations thereof, or any other suitable material.
As shown in
Next, the method 200 includes an act 256 of removing the stencil 260 from the substrate 208, thereby leaving the deposited thick film paste 264 on the substrate 208 in a selected pattern as precursor electrodes. The deposit height of the thick film paste 264 may be at least partially determined by the thickness of the stencil 260. In addition, the viscosity of the formed thick film paste 264 is sufficient such that the deposited thick film paste 264 substantially maintains the shape of the one or more openings 261 of the stencil 260.
In act 258, the deposited thick film paste 264 and the substrate 208 may be heated at a temperature between about 600° C. and about 2200° C. (e.g., about 1400° C. and about 2100° C. or about 1700° C. and about 2000° C.) for a time sufficient to effectively sinter the refractory metal material particles in the thick film paste 264 together. For example, the heating may be performed in a vacuum furnace, other generally inert atmosphere, or a non-inert atmosphere. In an embodiment, the thermal profile of the heat treatment may affect the sintering and densification of thick film paste 264. For example, an initial thermal ramp may be employed to burn off the organic binder in the thick film paste 264 and a peak soak period may be designed to sinter the refractory metal material particles together into a substantially continuous and dense network of bonded together refractory metal material particles that forms the electrodes 204. Feature dimensions (e.g., length, width, thickness, or combinations thereof) ranging from about 10 μm to about 1000 μm (e.g., about 20 μm to about 50 μm) may be formed using the thick-film process in addition to larger feature sizes such as in the millimeter scale. In other embodiments, the sintering may be effected using microwave sintering by application of microwave energy to the thick film paste 264.
In other embodiments, the process parameters may be adjusted in the method 200 to affect the electrical and/or thermal properties of the electrodes 204. Suitable examples of process parameters that may be adjusted include, but are not limited to, refractory metal material particle size and/or composition used to form the electrodes, refractory metal material particulate concentration in the thick film paste 264, glass content in the thick film paste 264, densification and porosity of the final sintered electrodes, level of sintering, combinations thereof, or another suitable process parameter. For example, sintering the refractory metal material particles together forms physical contact/electrical connections between the sintered particles. Thus, by varying the extent of sintering, the number of electrical connections between the refractory metal particles and the electrical conductivity levels through the electrodes 204 may be influenced. For example, the porosity of the final sintered electrodes 204 may be less than about 2 volume %, about 2 volume % to about 5 volume %, or about 1 volume % to about 3 volume %. As the porosity decreases, the electrical conductivity may increase.
The microstructure of the sintered refractory metal material forming the electrodes 204 is characteristic of being sintered, such as some porosity, surface roughness, distinct grain structure, or combinations thereof. In some embodiments, the surface roughness of the electrodes 204 so formed by sintering may be sufficient to initiate corona discharge according to Peek's Law when biased by a voltage source. In general, in corona discharge, ejecting ions is more likely to occur from sharply angled/pointed surface features, such as angular exterior surface grains or other surface features causing surface roughness on the electrodes 204 at least partially due to the sintered microstructure because the electric field divergence has its greatest magnitude close to such features. In Peek's Law, a sharp electrode feature has a lower corona inception voltage for ejecting ions than a dull feature.
As discussed above, in other embodiments, the refractory metal material particles may be selectively deposited in any selected electrode pattern using an ink jet type of deposition system. The as-deposited refractory metal material particles may be sintered by heating for a suitable amount of time at a suitable temperature, as discussed above in relation to
In other embodiments, the refractory metal material particles may be formed into a selected electrode pattern using a selective laser sintering (“SLS”) processes. Selective laser sintering uses a high power laser (e.g., a carbon dioxide laser) to fuse/sinter small refractory metal material particles into a mass that has a desired three-dimensional shape. The laser selectively fuses/sinters the powdered refractory metal material by scanning cross-sections generated from a three-dimensional digital description of the electrode pattern (e.g., a CAD file or other scan data) on the surface of a powder bed of the refractory metal material particles.
In an embodiment, the method 200 may include an act of depositing or forming one or more conductive coatings on the sintered refractory metal material of the electrodes 204. Such a conductive coating may help decrease the electrical resistance of the electrodes 204, as previously discussed. The one or more conductive coatings may be formed or deposited on the electrodes 204 via electroplating, electroless plating, screen printing, combinations thereof, or via any other suitable technique. Such conductive coatings may include, for example, tin, manganese, vanadium, cobalt, zinc, cadmium, rhodium, chromium, titanium, nickel, silver, gold, alloys of one or more of the foregoing metals, combinations thereof, or any other suitable conductive material.
In other embodiments, the electrodes 204 need not be formed on a substrate. For example, any of the electrode formation techniques may be used, such as screen printing, hot isostatic pressing, or SLC, to form the electrodes 204 on a surface from which the electrodes 204 may be removed and separated therefrom. For example, the surface may comprise a surface having a coating from which the electrodes are relatively easily removed, such as a diamond coating or other suitable coating. In yet another embodiment, the substrate on which the electrodes 204 may be formed may be removed from the electrode assembly via machining, grinding, or combinations thereof in order to separate the electrodes from the substrate.
As previously discussed, the electrodes may be formed in a number of different patterns. For example,
The electrodes 304 and the one or more voltage sources may be collectively configured to help influence combustion characteristics of a flame (not shown). The electrodes 304 may be biased independently or collectively, as previously described with respect to
Referring still to
The electrode assemblies disclosed herein may be arranged to form a number of different hollow three-dimensional structures (e.g., a hollow parallelepipeds) that at least partially surround a flame to help control one or more combustion characteristics of the flame. For example,
Referring now to the partial cross-sectional view of
Referring again to
The respective rows of the electrodes 404 and one or more voltage sources (not shown) may be collectively configured to help influence combustion characteristics of a flame (not shown). For example, the rows of the electrodes 404 may be biased independently or collectively via one or more voltage sources (not shown), as previously described with respect to
The electrodes 504 may be configured to be positioned proximate to or contacting the flame 506. In an embodiment, one or more of the electrodes 504 may be formed in a generally strip or bar-like pattern extending in a radial direction from a center of each of the substrates 508. Two or more of the electrodes 504 may exhibit different dimensions, such as length, width, thickness, or combinations thereof. Such a configuration may help the electrodes 504 control combustion characteristic of the flame 506 at different locations and/or times. While the electrodes 504 are illustrated being formed in a bar-like pattern, in other embodiments, one or more portions of the electrodes 504 may be formed in other suitable patterns.
Each of the electrode assemblies 502 may include a respective voltage source 510 operatively coupled to one or more of the electrodes 504. In an embodiment, two or more of the electrodes 504 may be selectively, electrically isolated such that the voltage sources 510 may apply a voltage to individual electrodes 504. In other embodiments, two or more of the electrodes 504 may be selectively, electrically connected to each other such that one or more of the voltage sources 510 may apply a voltage to two or more of the electrodes 504 simultaneously or nearly simultaneously. Like the voltage source 110 and the electrodes 104, one or more of the voltage sources 510 and the electrodes 504 may be collectively configured to apply an electric field to one or more regions 512 at least proximate to the flame 506.
In an embodiment, the combustion control system 500 may include one or more controllers 520 configured to control activation of at least one of the voltage sources 510. The combustion control system 500 may further include one or more sensors 522 configured to communicate with the controller 520 in response to a sensed condition of the flame 506. The sensors 522 may be configured to detect pressure, position, direction of movement of the flame 506, temperature, combustion chemical species, oxygen levels, flame dimensions or shape, flame electrical conductivity, flame electrical current, flame electrical charge distribution, combinations thereof, or any other suitable flame characteristics. For example, flame conductivity and flame current, may be measured using a-Langmuir probe, In other embodiments, the sensors 522 may be configured to detect one or more conditions associated with the electrode assembly 502, such as temperature, one or more electrical properties, position, direction, or any other suitable characteristic.
The combustion control system 500 may further include a wired or wireless transmitter (not shown) in communication with the sensors 522 and/or the controller 520, wherein the transmitter may be configured to report activity of the combustion control system 500 to an external source. The transmitter, in communication with the sensor 522 and the controller 520, may also be configured to send an activation signal to at least one of the voltage sources. In an embodiment, the controller 520 may be configured to receive an input signal (remote or local) to activate at least one of the voltage sources 510. In an embodiment, the input signal may come from operator input, a computer system, the sensor 522, or combinations thereof. Such a configuration may allow the combustion control system 500 to control one or more characteristics of the flame 506 based on one or more sensed properties or one or more signals from an external source.
Next, the method 600 may include the act 604 of applying an electric field to one or more regions at least proximate to the flame by biasing one or more of the electrodes via one or more voltage sources operatively coupled to the electrodes. The method 600 may further include the act 606 of varying application of the electric field to control one or more combustion characteristics of the flame.
In an embodiment, varying application of the electric field may include selectively charging one or more of the electrodes. In another embodiment, varying application of the electric field may include varying application of the electric field at selected locations proximate to and/or contacting the flame and/or selected times. In yet other embodiments, varying application of the electric field may include varying a voltage applied to the one or more electrodes by one or more of the voltage sources. For example, varying a voltage applied by one or more of the voltage sources may include varying a voltage applied by at least one of the voltage sources at selected times and/or locations. In other embodiments, varying a voltage applied by one or more of the voltage sources may include varying a magnitude or frequency of a voltage applied by at least one of the one or more voltage sources. For example, in an embodiment, applying a voltage to at least one of the electrodes may include applying a periodic voltage waveform having about a frequency of about 50 to about 10,000 Hz. Applying a time-varying voltage may include applying a square waveform, a sine waveform, a triangular waveform, a truncated triangular waveform, a sawtooth waveform, a logarithmic waveform, a convoluted waveform function, an arbitrary waveform function, a pulsed waveform, or an exponential waveform. Generation of such electric fields may help influence combustion characteristics of the flame, such as heat transfer or flame shape.
In an embodiment, any of the methods described herein may be performed by a computer system having at least one processor configured to execute computer-executable instructions and process operational data. For example, the processor may be operably coupled to a memory storing an application including computer-executable instructions and operational data constituting a computer program to perform acts 604 and/or 606 of the method 600 and incorporated in a controller such as the controller 520 of
The memory may be embodied as a computer readable medium, such as a random access memory (“RAM”), a hard disk drive, a static storage medium such as a compact disk, DVD, or other non-transitory storage medium. The memory may further store property data describing properties of the flame and/or electrode assemblies determined as described hereinabove. The computer system may further include a display coupled to the processor. The processor may be operable to display the images of the flame and other graphical illustrations of the characteristics of the flame on the display.
In some embodiments, the processor may also be operably coupled to and control operation of one or more voltage sources that apply a charge to one or more of the electrodes. For example, the memory may have computer-executable instructions stored thereon for having the processor direct one or more voltage sources to apply a charge to the electrodes such that the one or more voltage sources and the electrodes collectively apply an electric field to one or more regions at least proximate to a flame as performed in act 604 of the method 600. It will be appreciated that the computer systems described herein may include any suitable computer system including personal computers, desktop computers, laptop computers, hand-held devices, multi-processor systems, microprocessor-based or programmable consumer electronics, network PCs, minicomputers, mainframe computers, PDAs, tablets, combinations thereof, or the like.
There are numerous other embodiments, that the sintered refractory material electrodes and electrode assemblies disclosed herein may be used in. In an embodiment, a sintered refractory metal material may operate as a voltage, charge, or electric field conveyance (e.g., electrode) to or from a solid fuel. For example, a lump coal grate (an example of an assembly for delivering and/or holding solid fuel(s)) may at least support the sintered metal or refractory metal material. In an embodiment, a sintered refractory metal material may be deposited (such as electrodeposited) to contact or nearly contact a flowing fuel stream. The sintered refractory metal material deposition may include a plurality of ion ejection sources configured to ionize or convey voltage to a passing gaseous, liquid, or solid (perhaps most easily as powdered) fuel.
In an embodiment, an electrode made at least partly of sintered refractory metal metal material may be formed as a Coanda surface. In an embodiment, an electrode made at least partly of sintered refractory metal material may be formed as a fuel nozzle. In an embodiment, an electrode made at least partly of sintered refractory metal material may be formed as a fuel deflector. In an embodiment, an electrode made at least partly of sintered refractory metal material may be formed as a fuel mixer. In an embodiment, an electrode made at least partly of sintered refractory metal material may be formed as a conductive flame support surface. In an embodiment, an electrode made at least partly of sintered refractory metal material may be formed as a turbine blade. In an embodiment, an electrode made at least partly of sintered refractory metal material may be formed as a combustor wall. In an embodiment, an electrode made at least partly of sintered refractory metal material may be formed as a turbine wall, stator, or other relatively stationary part. In an embodiment, an electrode made at least partly of sintered refractory metal material may be formed as a spark arrester. In an embodiment, an electrode made at least partly of sintered refractory metal material may be formed as a flue electrode. In an embodiment, an electrode made at least partly of sintered refractory metal material may be formed as an electrostatic collection surface, scraper, or related component. In an embodiment, an electrode made at least partly of sintered refractory metal material may be formed as an arc discharge electrode. In an embodiment, an electrode made at least partly of sintered refractory metal material may be formed as a field electrode. In an embodiment, an electrode made at least partly of sintered refractory metal material may be formed as a fuel charger. In an embodiment, an electrode made at least partly of sintered refractory metal material may be formed as an electrical repulsion surface and/or as an electrical attraction surface.
One specific application is the use of the sintered refractory metal material electrodes and/or electrode assemblies in a counter electrode of an ionizer mechanism that may be incorporated into any of the combustion control systems disclosed herein, according to an embodiment. The sintered refractory metal material electrodes may exhibit a relatively high ratio of point resistance to area resistance, which makes them well suitable for counter electrode applications. An ionizer mechanism may be configured to ionize charge carriers that are then introduced to the combustion reaction for applying an electrical charge to the combustion reaction. The charge carriers can be drawn from any appropriate material or combination of materials, including, for example, components of the combustion reaction, such as oxidizer gas (e.g., air), fuel, flue gas, reactants, etc. According to an embodiment, the ionizing mechanism may include a corona electrode and counter electrode pair immersed in a flow of dielectric fluid, such as a gas, which is then introduced into the combustion volume. The corona electrode and counter electrode pair are configured to create ions from molecules of the dielectric fluid, or from other donor substances carried by the fluid.
Referring to the embodiment shown in
A transport fluid 710 flows along the ion flow path 705 carrying ions along the flow path toward the combustion reaction. The transport fluid 710 is most commonly the substance from which the charge carriers are drawn, but in some cases, it can be a fluid in which another material is suspended, the other material being more susceptible to ionization, and thus more likely to contribute the charge carriers. For example, the transport fluid 710 is a combustion component, such as air, fuel, or EGR flue gas. The transport fluid 710 may be a dielectric or, at least has a very low electrical conductivity, in order for proper operation of the ionizer stages 702a, 702b.
In the illustrated embodiment, the first ionizer stage 702a is positioned upstream from the second ionizer stage 702b along the ion flow path 705. Further downstream from the second ionizer stage 702b, the ion flow path 705 merges with the combustion reaction. The relative positions, flow-wise (i.e., along the ion flow path 705), of the electrodes of each of the ionizer stages 702a, 702b may vary, according to the design of the system. For example, the corona electrode 702 may be aligned with the upstream edge of the counter electrode 704, or may be positioned further up- or downstream than shown. Additionally, the first and second ionizer stages 702a, 702b are spaced by an inter-ionizer separation distance 708, which represents the nearest flow-wise approach between an electrode element of the first ionizer stage 702a and an electrode element of the second ionizer stage 702b. According to an embodiment, the first and second ionizer stages 702a, 702b are positioned such that the inter-ionizer separation distance 708 is greater than the electrode separation distance 706 of the first ionizer stage 702a.
According to an embodiment, the inter-ionizer separation distance 708 is between about 1.5 times and about 2.5 times the electrode separation 706 of the first ionizer stage 702a. For example, according to an embodiment, the inter-ionizer separation distance 708 is about 2 times the electrode separation 706 of the first ionizer stage 702a. An inter-ionizer separation distance 708 that is greater than the electrode separation distance 706 tends to prevent a corona electrode 702 of one ionizer stage from interacting with a counter electrode of another ionizer stage.
Additionally, in systems in which the ionizer mechanism includes more than two ionizer stages 702a, 702b, for each adjacent pair of ionizer stages, the inter-ionizer separation 708 is, according to an embodiment, between about 1.5 and 2.5 times—more specifically about 2 times—the electrode separation 706 of the upstream one of the respective pair of ionizer stages 702. The number of ionizer stages in the plurality of ionizer stages 702 can be any number that is sufficient to produce a desired quantity of ions, including 3, 4, 5, 6, 7, 8, 9, 10, 11, or 12, for example. More details about ionizer stages in which the sintered refractory metal material electrodes and electrode assemblies may be used are disclosed in U.S. application Ser. No. 14/092,896 filed on 27 Nov. 2013, the disclosure of which is incorporated herein, in its entirety, by this reference.
While various aspects and embodiments have been disclosed herein, other aspects and embodiments are contemplated. The various aspects and embodiments disclosed herein are for purposes of illustration and are not intended to be limiting.
This application claims priority to U.S. Provisional Application No. 61/737,033 filed on 13 Dec. 2012, the disclosure of which is incorporated herein, in its entirety, by this reference.
Number | Date | Country | |
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61737033 | Dec 2012 | US |