Patent Application
20080020334
Staged combustion systems are used to improve combustion by introducing successive portions of fuel into the combustion process to allow the oxidant and fuel to react in multiple zones or stages. This produces lower peak flame temperatures and other favorable combustion conditions that reduce the generation of nitrogen oxides (NOx). A wide variety of staged combustion methods are known and used in combustion applications including process heaters, furnaces, steam boilers, gas turbine combustors, coal-fired power generation units, and many other combustion systems in the metallurgical and chemical process industries.
The combustion of a gaseous fuel with oxygen in an oxygen-containing gas such as air occurs when a fuel-oxygen-inert gas mixture having a composition in the combustible region reaches its autoignition temperature or is ignited by a separate ignition source. When the combustion occurs in a three-dimensional process space such as a furnace, the degree of mixing is another important variable in the combustion process. The degree of mixing in the furnace, especially in the regions near the burners, affects localized gas compositions and temperatures, and therefore is an important factor in operating stability.
In combustion processes, particularly in staged combustion processes for NOx reduction, it is important to have good flame stability and proper location of the flame front relative to the points at which staging fuel is introduced into the combustion space. In conventional combustion systems, flame stability may be maintained by the use of fuel injection devices and internal recirculation patterns to improve the contact of the fuel stream with the combustion atmosphere and to provide the ignition energy required to sustain flame stability. Improper control of flame stability and flame location in staged combustion systems, particularly during cold startup, process upsets, or turndown conditions, may result in undesirable combustion performance, higher NOx emissions, and/or unburned fuel. This latter condition could lead to substantial pockets of fuel in the furnace and the possibility of an uncontrolled energy release.
There is a need in staged combustion processes for improved flame stability and complete fuel combustion, particularly during unsteady-state operating periods such as cold startup, process upsets, or process turndown conditions. Improved staged combustion systems to meet these needs are disclosed by embodiments of the present invention described below and defined by the claims that follow.
An embodiment of the invention relates to a combustion system comprising a furnace having a thermal load and a combustion atmosphere disposed therein; one or more fuel lances adapted to inject fuel into the combustion atmosphere; and one or more igniters associated with the one or more fuel lances and adapted to ignite the fuel injected by the one or more fuel lances into the combustion atmosphere. The one or more igniters may be selected from the group consisting of intermittent spark igniters, continuous spark igniters, DC arc plasmas, microwave plasmas, RF plasmas, high energy laser beams, and oxidant-fuel pilot burners. In this embodiment, at least one of the igniters may be disposed adjacent to a fuel lance and may be adapted to ignite fuel discharged therefrom. Alternatively, at least one of the igniters may be integrated into a fuel lance and adapted to ignite fuel discharged therefrom. The number of fuel lances may be equal to or less than the number of igniters.
Another embodiment relates to a fuel lance comprising a nozzle body having an inlet face, an outlet face, and an inlet flow axis passing through the inlet and outlet faces, and two or more slots extending through the nozzle body from the inlet face to the outlet face, each slot having a slot axis, wherein the slot axis of at least one of the slots is not parallel to the inlet flow axis of the nozzle body, and wherein the slots are adapted to discharge a fuel at the outlet face of the nozzle body; and an igniter associated with the nozzle body and adapted to ignite the fuel discharged at the outlet face of the nozzle body. The igniter may be disposed adjacent the outlet face of the nozzle body; alternatively, the igniter may be integrated into the nozzle body and passes through the outlet face of the nozzle body.
An alternative embodiment pertains to a fuel lance comprising a nozzle body having an inlet face, an outlet face, and an inlet flow axis passing through the inlet and outlet faces, two or more slots extending through the nozzle body from the inlet face to the outlet face, each slot having a slot axis and a slot center plane, wherein none of the slots intersect other slots and all of the slots are in fluid flow communication with a common fuel supply conduit; and an igniter associated with the nozzle body and adapted to ignite the fuel discharged at the outlet face of the nozzle body. The igniter may be disposed adjacent the outlet face of the nozzle body; alternatively, the igniter may be integrated into the nozzle body and passes through the outlet face of the nozzle body.
In another alternative embodiment, the fuel lance may comprise a nozzle body having an inlet face, an outlet face, and an inlet flow axis passing through the inlet and outlet faces and two or more slots extending through the nozzle body from the inlet face to the outlet face, each slot having a slot axis and a slot center plane, wherein a first slot of the two or more slots is intersected by each of the other slots and the slot center plane of at least one of the slots intersects the inlet flow axis of the nozzle body; and an igniter associated with the nozzle body and adapted to ignite the fuel discharged at the outlet face of the nozzle body. The igniter may be disposed adjacent the outlet face of the nozzle body; alternatively, the igniter may be integrated into the nozzle body and passes through the outlet face of the nozzle body.
A related embodiment of the invention includes a combustion system comprising a furnace comprising an enclosure and a thermal load disposed within the enclosure; one or more oxidant gas injectors mounted in the enclosure and adapted to introduce an oxidant gas into the furnace; one or more fuel lances mounted in the enclosure and spaced apart from the one or more oxidant gas injectors, wherein the one or more fuel lances are adapted to inject fuel into the furnace; and one or more igniters associated with the one or more fuel lances and adapted to ignite the fuel injected by the fuel lances.
In this embodiment, the one or more igniters may be selected from the group consisting of intermittent spark igniters, continuous spark igniters, DC arc plasmas, microwave plasmas, RF plasmas, high energy laser beams, and oxidant-fuel pilot burners. At least one of the igniters may be adjacent to a fuel lance and adapted to ignite fuel discharged therefrom. Alternatively, at least one of the igniters may be integrated into a fuel lance and adapted to ignite fuel discharged therefrom. The number of fuel lances may be equal to or less than the number of igniters. The distance between the periphery of one of the one or more oxidant gas injectors and the periphery of an adjacent fuel lance may be in the range of 2 to 50 inches.
Another related embodiment of the invention pertains to a combustion system comprising a furnace having a thermal load and a combustion atmosphere disposed therein; a central burner having an axis, a primary fuel inlet, an oxidant gas inlet, and a combustion gas outlet adapted to introduce the combustion gas into the furnace; one or more staging fuel lances disposed radially from the axis of the central burner and adapted to inject a staging fuel into the combustion atmosphere in the furnace; and one or more igniters associated with the one or more staging fuel lances and adapted to ignite the staging fuel injected therefrom.
In this embodiment, the one or more igniters may be selected from the group consisting of intermittent spark igniters, continuous spark igniters, DC arc plasmas, microwave plasmas, RF plasmas, high energy laser beams, and oxidant-fuel pilot burners. At least one of the igniters may be adjacent to a fuel lance and adapted to ignite fuel discharged therefrom. Alternatively, at least one of the igniters may be integrated into a fuel lance and adapted to ignite fuel discharged therefrom. The number of fuel lances may be equal to or less than the number of igniters.
The system of this embodiment may further comprise main fuel piping adapted to provide the primary fuel to the central burner and staging fuel piping adapted to provide the staging fuel to the one or more staging fuel lances. The primary fuel to the central burner and the staging fuel to the one or more staging fuel lances are identical in composition; alternatively, the primary fuel to the central burner and the staging fuel to the one or more staging fuel lances are different in composition. The one or more staging fuel lances may be disposed outside of the central burner and may be disposed radially from the axis of the central burner.
An alternative related embodiment of the invention includes a combustion process comprising
In this embodiment, the fuel may be selected from natural gas, refinery offgas, associated gas from crude oil production, and combustible process waste gas. A plurality of fuel lances may be used and fuels of different compositions may be used in the plurality of fuel lances.
Another alternative related embodiment of the invention pertains to a combustion process comprising:
In this embodiment, the primary fuel and the secondary fuel may be gases having different compositions. The primary fuel may be natural gas or refinery offgas and the secondary fuel may comprise hydrogen, methane, carbon monoxide, and carbon dioxide obtained from a pressure swing adsorption system. Alternatively, the primary fuel and the secondary fuel may be gases having the same compositions.
A different embodiment of the invention relates to a combustion process comprising
Combustion-based processes utilize the combustion of fuel streams with oxygen to generate process heat and, in some cases, to consume combustible off-gas streams from other process systems. In the establishment of a combustion reaction with these various fuels, autoignition will occur if the temperature of the fuel-oxidant mixture is above the autoignition temperature of the mixture. In air/natural gas mixtures, for example, the autoignition temperature is about 1,000° F. An ignition source is required to initiate the combustion reaction if the temperature of the fuel-oxidant mixture is below its autoignition temperature.
An additional variable, the extent of mixing in the combustion atmosphere or combustion region, can affect the stability of the combustion process with a gaseous or vaporized fuel. Stabilization of the combustion process becomes complicated when fuel staging is used to limit formation of NOx. In fuel staging, raw fuel (without air or oxygen) is introduced into the combustion atmosphere containing excess oxygen remaining from an earlier step of combustion. Although the fuel for each stage of combustion typically is identical, different fuel sources may be used, and the use of different staging fuels may affect the operating stability of the combustion process. In order to minimize formation of NOx, it is desirable to introduce the staging fuel into the combustion atmosphere at or near a location having a minimum concentration of oxygen.
The maintenance of flame stability and flame location in staged fuel combustion systems may be difficult during unsteady-state process conditions that occur in a furnace during cold startup, process upsets, or turndown conditions. During such conditions, localized temperatures may fall below the autoignition temperature of the fuel-oxidant mixture and may result in unstable flames and/or regions containing unburned fuel. This is undesirable and may lead to the possibility of an uncontrolled energy release in the furnace.
Flame stability, which is the proper location of the flame front relative to the point of introduction of the fuel stream in the combustion atmosphere, is a key aspect of the successful application of fuel staging. In conventional staged combustion systems, flame stability is maintained by the use of combinations of fuel injection devices and mixing patterns to improve the contact between the fuel-rich jet and the source of oxygen, which could be the inlet combustion air stream or unreacted oxygen contained in the gaseous atmosphere in the furnace. The proper location and amount of ignition energy also is important. Designs for fuel injection devices typically attempt to anchor the flame at the flame holder tip, which can be the fuel injector itself, a separate bluff body device (such as an external surface of refractory tile), or a swirl stabilizer nozzle. The drawback of conventional bluff body type flame stabilizers is that they have a limited turndown ratio, which limits their stability performance during cold start-up and process upset conditions. Any substantial distance or lift-off height between the staged fuel jet flame front and the flame holder surface will cause oscillation in the flame and result in undesirable combustion performance, including NOx emissions and/or the presence of unburned fuel.
When non-steady state conditions such as start-up or process upsets occur while flow through the conventional fuel staging system is maintained, the volume of fuel that exists at high concentrations can increase substantially within the combustion system. The regions near the fuel-rich jets from the injection devices may be outside of the flammability limits (e.g., between 5 and 15 vol % for natural gas) and there may be insufficient ignition energy available in the cold furnace. When multiple elements of these fuel staging systems are included in one piece of equipment or when the flame is re-established from a single burner, additional sources of ignition may be present in the furnace. These ignition sources may be, for example, radicals formed in the combustion reactions at the burner and/or the staged fuel injection devices. An uncontrolled energy release promoted by the reaction of these radicals with the volume of unburned fuel in a process heater, boiler, reformer, or other similar unit operation is a safety and operability concern.
Conventional burner technology cannot provide flame stability for individual fuel staging lances during cold start-up, at low furnace temperatures, and during upset or turndown conditions. Lack of stability during these periods could lead to flame lift-off and subsequent uncontrolled energy release as discussed above. A robust solution is needed to address these potentially unsafe conditions. The preferred solution should utilize changes and enhancements to the combustion equipment itself rather than require the execution of specific operating and control steps by process operating personnel. Such a solution is disclosed in embodiments of the present invention wherein one or more ignition sources are used in conjunction with the fuel injection lances that introduce staging fuel into a combustion region or zone.
Ignition-assisted fuel lances are used in various embodiments of the invention in order to ensure ignition of the fuel injected into oxygen-containing gases in a combustion atmosphere in a process heater, furnace, steam boiler, gas turbine combustor, or other gas-fired combustion system. A fuel lance is defined herein as a device for injecting fuel at an elevated velocity into a combustion atmosphere. The combustion atmosphere contains an oxidant gas, and the staging fuel injected into the oxidant gas is combusted with oxygen in the oxidant gas. The oxidant gas may be air, oxygen-enriched air, or a combustion gas containing combustion products and excess unreacted oxygen. For example, ignition-assisted fuel lances may be installed in a furnace boundary, wall, or enclosure adjacent to but separate from a burner wherein the fuel lances inject fuel into the combustion atmosphere generated by the burner to effect staged combustion. Alternatively, ignition-assisted fuel lances may be installed adjacent to but separate from a source of oxidant gas such as air, wherein the fuel lances inject portions of the fuel into the oxidant gas or the combustion atmosphere to effect parallel staged combustion.
The term “combustion atmosphere” as used herein means the atmosphere within the enclosure or boundaries of a furnace. The overall combustion atmosphere within the boundaries of the furnace comprises oxygen, fuel, combustion gas containing combustion reaction products (e.g., carbon oxides, nitrogen oxides, and water), and inert gases (e.g., nitrogen and argon). The source of the oxygen and inert gases typically is air; an alternative or additional source of oxygen may be an oxygen injection system which introduces oxygen-enriched air and/or high purity oxygen to enhance the combustion process. The combustion atmosphere is heterogenous because the concentration of the components varies throughout the furnace. For example, the concentration of oxygen may be higher near oxidant injection points and the concentration of fuel may be higher near the fuel injection points. In other regions of the combustion atmosphere, there may be no fuel present. The concentration of oxygen and combustion reaction products will vary depending on the extent of combustion at various locations within the combustion atmosphere. At certain locations, injected fuel may react directly with oxygen in the oxidant gas injected into the combustion atmosphere; at other locations, injected fuel may react with unreacted oxygen from combustion occurring elsewhere in the combustion atmosphere.
A thermal load is disposed in the combustion atmosphere within the interior of the furnace, wherein a thermal load is defined as (1) the heat absorbed by material transported through the furnace combustion atmosphere wherein the heat is transferred from the combustion atmosphere to the material as it is transported through the furnace or (2) the heat exchange apparatus adapted to transfer heat from the combustion atmosphere to the material being heated.
An exemplary concentrically-staged combustion burner system is illustrated in sectional view in
In the operation of this central burner, oxidant gas (typically air or oxygen-enriched air) 15 flows into the interior of outer pipe 3, a portion of this air flows through the interior of inner pipe 7, and the remaining portion of this air flows through annular space 9. Primary fuel 15 flows through pipe 13 and through annular space 11, and is combusted initially in combustion zone 17 with air from inner pipe 7. Combustion gas from combustion zone 17 mixes with additional air in combustion zone 19. Combustion in this zone is typically extremely fuel-lean. A visible flame typically is formed in combustion zone 19 and in combustion zone 21 as combustion gas 23 enters furnace interior 25. The term “combustion zone” as used here means a region within the burner in which combustion occurs.
A staging fuel system comprises inlet pipe 27, manifold 29, and a plurality of staging fuel lances 31. The ends of the staging fuel lances may be fitted with injection nozzles 33 of any desired type. Staging fuel 35 flows through inlet pipe 27, manifold 29, and staging fuel injection lances 31. Staging fuel streams 37 from nozzles 33 mix rapidly and combust with the oxidant-containing combustion gas 23. The cooler combustion atmosphere in furnace interior 25 is rapidly entrained by staging fuel streams 37 by the intense mixing action promoted by nozzles 33, and the concentrically-injected staging fuel is combusted with the oxidant-containing combustion atmosphere downstream of the exit of central burner 1. The primary fuel may be 5 to 30% of the total fuel flow rate (primary plus staging) and the staging fuel may be 70 to 95% of the total fuel flow rate.
The primary and staging fuels may have the same composition or may have different compositions and either fuel may be any gaseous, vaporized, or atomized hydrocarbon-containing material. For example, the fuel may be selected from the group consisting of natural gas, refinery offgas, associated gas from crude oil production, and combustible process waste gas. An exemplary process waste gas is the tail gas or waste gas from a pressure swing adsorption system in a process for generating hydrogen from natural gas.
An exemplary type of nozzle 33 is illustrated in
The term “slot” as used herein is defined as an opening through a nozzle body or other solid material wherein any slot cross-section (i.e., a section perpendicular to the inlet flow axis defined below) is non-circular and is characterized by a major axis and a minor axis. The major axis is longer than the minor axis and the two axes are generally perpendicular. For example, the major cross-section axis of any slot in
A slot may be further characterized by a slot axis defined as a straight line connecting the centroids of all slot cross-sections. In addition, a slot may be characterized or defined by a center plane which intersects the major cross-section axes of all slot cross-sections. Each slot cross-section may have perpendicular symmetry on either side of this center plane. The center plane extends beyond either end of the slot and may be used to define the slot orientation relative to the nozzle body inlet flow axis as described below.
Axial section I-I of the nozzle of
The term “inlet flow axis” as used herein is an axis defined by the flow direction of fluid entering the nozzle at the inlet face, wherein this axis passes through the inlet and outlet faces. Typically, but not in all cases, the inlet flow axis is perpendicular to the center of nozzle inlet face 303 and/or outlet nozzle face 217, and meets the faces perpendicularly. When nozzle inlet pipe 302 is a typical cylindrical conduit as shown, the inlet flow axis may be parallel to or coincident with the conduit axis.
The axial slot length is defined as the length of a slot between the nozzle inlet face and outlet face, for example, between inlet face 303 and outlet face 217 of
The multiple slots in a nozzle body may intersect in a plane perpendicular to the inlet flow axis. As shown in
Alternative, a nozzle body may be envisioned in which none of the slots intersect each other in any plane perpendicular to axis 301. In this alternative embodiment, for example, all slots viewed perpendicular to the nozzle body face are separate and do not intersect other slots. Such a nozzle could, for example, be similar to the nozzle of
Other types of nozzle configurations may be used for nozzle body 203 (
The exemplary concentrically-staged combustion burner system of
The location of the igniters in
Igniter 501 (
An exemplary igniter is a pilot device shown in
An alternative type of igniter pilot may be used as an alternative to
The pilot igniters described above may be operated continuously, for example, during operation of a furnace fired by a plurality of burners, for example, as in burner 1 of
A pilot igniter of
Fuel 919 enters the lance inlet end, flows through an interior fuel passage (not seen), and exits slots 907, 909, 911, 913, and 915 at nozzle face 917. Pilot fuel 921, which may be the same or different than lance fuel 919, flows into and through inner pipe 904. Pilot oxidant gas 923, (for example, air or oxygen-enriched air) flows into and through the annulus between outer pipe 903 and inner pipe 904. Ignition electrode 905 is used to ignite the mixture of pilot fuel and oxidant gas as described above.
Instead of the pilot flame igniter discussed above as part of the ignition-assisted lance of
An alternative embodiment of the invention relates to a combustion system having oxidant injectors for injecting oxidant gas into a furnace and separate ignition-assisted fuel lances for injecting fuel into the furnace. No individual burners are used in this embodiment, which may be considered a matrix combustion system. The system comprises a furnace having an enclosure and a thermal load disposed within the enclosure; one or more oxidant gas injectors mounted in the enclosure and adapted to introduce an oxygen-containing gas into the furnace; one or more fuel lances mounted in the enclosure and spaced apart from the one or more oxidant gas injectors, wherein the one or more fuel lances are adapted to inject fuel into the furnace; and one or more igniters associated with the one or more fuel lances and adapted to ignite the fuel injected by the fuel lances. When one or more oxidant gas injectors and a plurality of fuel lances are used, the combustion system may be defined as a matrix-staged combustion system.
This embodiment is illustrated schematically in
Ignition-assisted fuel lance 1013 is disposed in furnace wall 1005 apart from oxidant gas injector 1003 and operates to inject fuel gas 1015 into furnace interior 1011 and form distributed fuel gas jet 1017. Ignition-assisted fuel lance 1013 is shown here as a sectional view of the lance described above with reference to
Pilot flame 1019 ignites the fuel-oxidant mixture formed by fuel 1017 and oxidant 1009 in combustion atmosphere 1011 in the furnace interior if the temperature of the fuel-oxidant mixture is below its autoignition temperature. Typically a flame (not shown) is formed immediately downstream of distributed fuel gas jet 1017. If the temperature of the fuel-oxidant mixture is above its autoignition temperature, operation of the pilot flame igniter may not be needed; however, operation of the pilot flame may be continued to provide ignition of the fuel-oxidant mixture if needed in the event of an operating upset in the furnace operation.
Additional ignition-assisted fuel lances may be disposed at other spaced-apart locations in furnace wall 1005; for example, a lance identical to lance 1013 may be installed in opening 1025 shown on the opposite side of oxidant gas injector 1003. In the embodiment of
An exemplary matrix-staged installation utilizing multiple oxidant gas injectors and ignition-assisted fuel lances is illustrated in the embodiment of
The injected fuel gas is combusted with the oxidant gas, and combustion may be initiated by the pilot flames in the ignition-assisted lances as earlier described with reference to
A thermal load typically will exist in furnace 1101 to absorb a portion of the combustion heat generated therein. In this illustration, schematic heat exchanger 1119 is shown in the bottom of the furnace to heat process feed stream 1121 and convert it to process effluent stream 1123 exiting the furnace. Process feed stream 1121 may be heated in the furnace with or without accompanying chemical reaction. Phase change in the process stream may or may not occur, depending on the particular application. Instead of a process stream comprising the thermal load, articles may be conveyed through the furnace and absorb heat therein, for example, in a metallurgical heat treating process. Regardless of the type of material passing through the furnace, the system and process are characterized by a thermal load which absorbs heat from the hot combustion atmosphere in the furnace. In all embodiments of the invention, the generic meaning of “thermal load” as earlier described is (1) the heat absorbed by material transported through the furnace combustion atmosphere wherein the heat is transferred from the combustion atmosphere to the material as it is transported through the furnace or (2) the heat exchange apparatus adapted to transfer heat from the combustion atmosphere to the material being heated. The combustion atmosphere is contained within the furnace, wherein the furnace is defined as an enclosure within which combustion of injected oxidant and fuel occurs.
While the embodiment of
This application is a divisional application and claims the benefit of priority under 35 USC 120 of U.S. application Ser. No. 10/883,349, filed Jul. 1, 2004, the specification and claims which are incorporated by reference and made a part of this application.
| Number | Date | Country | |
|---|---|---|---|
| Parent | 10883349 | Jul 2004 | US |
| Child | 11831381 | Jul 2007 | US |
