Embodiments of the invention relate generally to pulverized fuel power plants. Certain embodiments relate to systems and methods for increasing the concentration of pulverized fuel in a pre-ignition conduit of a pulverized fuel burner.
Pulverized fuel power plants have typically burned oil or natural gas to initially ignite the pulverized fuels, e.g., coal, that are to be combusted. As will be appreciated, this results in the consumption of large amounts of oil and gas. To reduce such consumption, plasma ignition systems have been developed to replace oil or gas ignition systems. More specifically, many plasma ignition systems use multi-stage, i.e., ‘stage-by-stage’ ignition technology to ignite pulverised fuels. In stage-by-stage systems, a relatively long pulverized fuel nozzle is employed that includes at least one and typically two or more ignition chambers located within the nozzle.
More specifically, in such systems, primary airflow containing pulverized fuel is ignited through the action of plasma generator to produce a plasma cloud in a first ignition chamber thereby generating a ‘first stage’ pulverized fuel flame. The first stage flame then ignites the pulverized fuel containing primary airflow in a second stage chamber, thereby forming a ‘second stage’ pulverized fuel flame. Finally, the ignited fuel enters into the furnace and reacts with oxygen in combustion air supplied through the burner, thereby forming a final stage flame.
Generally, the concentration of pulverized fuel in the ignition chambers is determined by a guide plate located in an elbow portion of a pulverized fuel nozzle. More specifically, the guide plate aligns the flow of pulverized fuel and primary air flow such that they are parallel to the plasma cloud. The guide plate also concentrates the pulverized fuel in proximity to a central axis of the burner and plasma cloud via a centrifugal separation effect. This, in turn, increases the concentration of the pulverized fuel entering the chamber, which facilitates ignition.
Due to space limitations within pulverized fuel nozzles, however, the pulverised fuel concentration in the chambers cannot easily be increased without affecting ignition behavior. As such, there is a need for a system and method for increasing the concentration of pulverized fuel that differs from those systems that are currently available.
In an embodiment, a pre-ignition conduit for a pulverized fuel nozzle includes a duct having first and second opposing end portions, the first end portion configured to face an outlet of an igniter. The conduit further includes a cone-shaped concentrator for collecting and forwarding pulverized fuel into the duct for ignition, the cone-shaped concentrator being secured to the first end portion and located between the outlet of the igniter and the duct. The pre-ignition conduit functions as an ignition chamber within the pulverized fuel nozzle.
In another embodiment, a pulverized fuel nozzle for a burner includes an igniter having an outlet, a pre-ignition conduit that includes a duct have first and second opposing end portions, the first end portion configured to face the outlet of the igniter and a cone-shaped concentrator for collecting and forwarding pulverized fuel into the duct for ignition, the cone-shaped concentrator being secured to the first end portion and located between the outlet of the igniter and the duct. The pre-ignition conduit functions as an ignition chamber within the pulverized fuel nozzle.
In yet another embodiment, a pre-ignition conduit for a pulverized fuel nozzle includes a duct having first and second opposing end portions, the first end portion configured to face an outlet of an igniter, a cone-shaped concentrator for collecting and forwarding pulverized fuel into the duct for ignition, the cone-shaped concentrator being secured to the first end portion and located between the outlet of the igniter and the duct. The duct further including an ignition inlet for receipt of an ignition source.
The present invention will be better understood from reading the following description of non-limiting embodiments, with reference to the attached drawings, wherein below:
Reference will be made below in detail to exemplary embodiments of the invention, examples of which are illustrated in the accompanying drawings. Wherever possible, the same reference characters used throughout the drawings refer to the same or like parts. While embodiments of the invention are described as suitable for use with pulverized coal burners, embodiments of the invention may be suitable for use with various fuels, such as fossil fuels or biomass. Accordingly, the term “pulverised fuel” or “PF” as used herein includes, but is not limited to, the aforementioned exemplary fuels. Moreover, while embodiments are described as being configured for use with a plasma generator/torch, embodiments may be used with other igniters, such as oil/gas igniters, e.g., an oil/gas gun or “micro” oil/gas burner. Moreover, embodiments may be equally suitable for use with multi-stage, e.g., stage-by-stage ignition systems, or single stage systems.
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Embodiments of the present invention provide improved concentration of pulverized fuel in the pre-ignition conduit through the use of the cone-shaped concentrator and/or one or more geometric relationships between the nozzle 14, duct 16, cone-shaped concentrator 12 and igniter/plasma generator 20. In view of the improved concentration of PF in the pre-ignition conduit, in embodiments, the inventive pre-ignition conduit functions itself as an ignition chamber within a pulverized fuel nozzle. As a result, a stage-by-stage system can be achieved via a nozzle that includes the present pre-ignition conduit and a single conventional ignition chamber, such as chamber 26 in
Referring again to
In certain embodiments, the cone-shaped concentrator 12 has a concentrator angle β which is between about 5° to about 45° and further between about 15° to about 30° to optimize pressure drop, concentrator erosion, and pulverised fuel concentration. More specifically, it has been determined that if the concentrator angle β is <15° , the pressure drop and erosion are minimal, but pulverised fuel concentration in the pre-ignition conduit is decreased. If the angle β is >30° , the pulverised fuel concentration is enhanced, but pressure drop and erosion are increased. As such, in certain embodiments, the aforementioned ranges optimize these parameters. As will be appreciated, however, in other embodiments concentrator angles varying from the above may be employed, as long as the aforementioned factors are suitably optimized.
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Embodiments of the invention also include specific geometric relationships between components of the pre-ignition conduit and pulverized fuel nozzle. In particular, the internal diameter D of the pulverized fuel nozzle is an important burner design parameter. As such, embodiments utilize geometric relationships between the inner diameter D and various other parameters, such as, for example, an internal diameter d of the duct of the pre-ignition conduit.
More specifically, in certain embodiments, the geometry of the inner diameter D of the pulverized fuel nozzle is such that if D is smaller than 500 mm, than the internal diameter of the duct d is be greater than that of the half of D. In other words, if D<500 mm, then d≧D/2. With respect to this relationship, it has been determined that if the diameter d is smaller than that of D/2, the temperature of the pre-ignition conduit will increase too rapidly and remain high during ignition and boiler start-up process, i.e, when the igniter is in operation. As will be appreciated, this can potentially damage and/or decrease the lifespan of the pulverized fuel nozzle.
Moreover, in aspects, if the pulverized fuel nozzle internal diameter D is between 500 mm and 600 mm, then the internal diameter d of the duct 16 is between 250 mm and 300 mm. That is, if 500 mm≦D≦600 mm, then 250 mm≦d≦300 mm. This relationship is significant in that if the diameter d is smaller than 250 mm, the temperature of the pre-ignition conduit can again increase too quickly and remain high during ignition and boiler start up, potentially decreasing the lifespan of the pulverized fuel nozzle. Conversely, if the diameter d is greater than 300 mm, the temperature of the pre-ignition conduit will remain low during ignition and boiler start up process, potentially decreasing coal ignition performance.
In other aspects, if the pulverized fuel nozzle internal diameter D is greater than 600 mm, then the internal diameter d of the duct 16 is smaller than that of the half of the pulverized nozzle internal diameter D, i.e., if D>600 mm, then d≦D/2. Here, if the diameter d is greater than that of D/2, the temperature of the pre-ignition conduit will remain low during ignition and boiler start up, again potentially decreasing coal ignition performance.
In certain embodiments, the internal diameter d of the duct 16 is smaller than that of the one third of the pulverized fuel nozzle double inner diameter D. That is, d≦2D/3.This relationship is notable in that if the diameter d is greater than that of the 2D/3, it will affect ignition such that the concentration of the pulverised fuel is decreased. Additionally, it is recommended to have an inner diameter of the second or subsequent downstream stage ignition conduit greater than one third of the pulverized-fuel nozzle inner double diameter D.
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Moreover, in aspects, the cone-shaped concentrator 12 has an internal diameter, M, that is greater than an inner diameter d of the duct by factor of about 1.1 to about 1.3. In particular embodiments, the internal diameter M of the cone-shaped concentrator 12 is greater than that of the internal diameter d by factor 1.2. In other words, the relationship between the internal diameter M and d can be expressed as d×1.1≦M≦d×1.3. Here, it has been determined that if the factor is greater or less than 1.2, the pulverized fuel concentration and the collection and transport of the pulverised fuel into the duct can be negatively affected.
Additionally, in embodiments, the internal diameter of the duct d is greater than an outer diameter P of the igniter outlet, i.e., d≧P. This is significant in that if the diameter d is smaller, the concentration of pulverized fuel, e.g., coal, decreases and the ignition process may be negatively affected.
In certain embodiments, the pre-ignition conduit has an overall length L which is greater than the internal diameter D of the nozzle, i.e., L≧D. This relationship is notable in that if the length L is smaller, the residence time of the pulverized fuel in the pre-ignition conduit decreases, thereby affecting ignition.
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In embodiments, a pre-ignition conduit for a pulverized fuel nozzle includes a duct having first and second opposing end portions, the first end portion configured to face an outlet of an igniter, a cone-shaped concentrator secured to the first end portion and located between the outlet of the igniter and the duct and configured to collect and forward pulverized fuel into the duct for ignition within the duct. The pre-ignition conduit functions as an ignition chamber within a pulverized fuel nozzle. The cone-shaped concentrator may include an eccentric cone or have a circumferential edge portion that is discontinuous. The cone-shaped concentrator can be located at a distance of about 50 mm to about 150 mm from the igniter outlet. The pulverized fuel nozzle has an inner diameter D and the duct of the pre-ignition conduit has an inner diameter d; and if D>500 mm then d≧D/2. In embodiments, if 500 mm≦D≦600 mm then 250 mm≦d≦300 mm. Moreover, in aspects, if D>600 mm then d≦D/2 and d can be ≦2D/3. In embodiments, the outlet of the igniter has an outer diameter P and d≧P. The pre-ignition conduit has an overall length L and L≧D. The cone-shaped concentrator can have a cone angle β that is between 5 and 45 degrees and between 15 and 30 degrees. The cone-shaped concentrator has an inner diameter M and the duct of the pre-ignition conduit has an inner diameter d and d×1.1≦M<d×1.3.
In embodiments, a pulverized fuel nozzle includes an igniter having an outlet, a pre-ignition conduit that includes a duct have first and second opposing end portions, the first end portion configured to face the outlet of the igniter and a cone-shaped concentrator secured to the first end portion between the outlet and the duct, the cone-shaped concentrator configured to collect and forward pulverized fuel into the duct for ignition within the duct. The pre-ignition conduit functions as an ignition chamber within the pulverized fuel nozzle. The cone-shaped concentrator may include an eccentric cone or have a circumferential edge portion that is discontinuous. The cone-shaped concentrator can be located at a distance of about 50 mm to about 150 mm from the igniter outlet. The pulverized fuel nozzle has an inner diameter D and the duct of the pre-ignition conduit has an inner diameter d; and if D>500 mm then d≧D/2.In embodiments, if 500 mm≦D≦600 mm then 250 mm≦d≦300 mm. Moreover, in aspects, if D>600 mm then d≦D/2 and d can be ≦2D/3. In embodiments, the outlet of the igniter has an outer diameter P and d≧P. The pre-ignition conduit has an overall length L and L≧D. The cone-shaped concentrator can have a cone angle β that is between 5 and 45 degrees and between 15 and 30 degrees. The cone-shaped concentrator has an inner diameter M and the duct of the pre-ignition conduit has an inner diameter d and d×1.1≦M≦d×1.3. The pulverized fuel nozzle may include a tilt mechanism.
In yet another embodiment, a pre-ignition conduit for a pulverized fuel nozzle includes a duct having first and second opposing end portions, the first end portion configured to face an outlet of an igniter. The duct further includes an ignition outlet or side access duct for installation of an ignition source onto the pre-ignition conduit. The ignition outlet is at an angle a that ranges from between about 30 and 90 degrees, in other words, 30°<α<90° . The conduit can also include a concentrator secured to the first end portion and located between the outlet of the igniter and the duct and configured to collect and forward pulverized fuel into the duct for ignition within the duct.
It is to be understood that the above description is intended to be illustrative, and not restrictive. For example, the above-described embodiments (and/or aspects thereof) may be used in combination with each other. In addition, many modifications may be made to adapt a particular situation or material to the teachings of the invention without departing from its scope. While the dimensions and types of materials described herein are intended to define the parameters of the invention, they are by no means limiting and are exemplary embodiments. Many other embodiments will be apparent to those of skill in the art upon reviewing the above description. The scope of the invention should, therefore, be determined with reference to the appended claims, along with the full scope of equivalents to which such claims are entitled. In the appended claims, the terms “including” and “in which” are used as the plain-English equivalents of the respective terms “comprising” and “wherein.” Moreover, in the following claims, terms such as “first,” “second,” “third,” “upper,” “lower,” “bottom,” “top,” etc. are used merely as labels, and are not intended to impose numerical or positional requirements on their objects. Further, the limitations of the following claims are not written in means-plus-function format unless and until such claim limitations expressly use the phrase “means for” followed by a statement of function void of further structure.
This written description uses examples to disclose several embodiments of the invention, including the best mode, and also to enable one of ordinary skill in the art to practice the embodiments of invention, including making and using any devices or systems and performing any incorporated methods. The patentable scope of the invention is defined by the claims, and may include other examples that occur to one of ordinary skill in the art. Such other examples are intended to be within the scope of the claims if they have structural elements that do not differ from the literal language of the claims, or if they include equivalent structural elements with insubstantial differences from the literal languages of the claims.
As used herein, an element or step recited in the singular and proceeded with the word “a” or “an” should be understood as not excluding plural of said elements or steps, unless such exclusion is explicitly stated. Furthermore, references to “one embodiment” of the present invention are not intended to be interpreted as excluding the existence of additional embodiments that also incorporate the recited features. Moreover, unless explicitly stated to the contrary, embodiments “comprising,” “including,” or “having” an element or a plurality of elements having a particular property may include additional such elements not having that property.
Since certain changes may be made in the above-described system and method without departing from the spirit and scope of the invention herein involved, it is intended that all of the subject matter of the above description or shown in the accompanying drawings shall be interpreted merely as examples illustrating the inventive concept herein and shall not be construed as limiting the invention.