The present invention relates to the field of combustion technology for gas turbines. It also relates to a method for the combustion of hydrogen-rich, gaseous fuels in the burner of a gas turbine, as well as to a burner for carrying out the method.
Lowering the emission of greenhouse gases into the atmosphere will call for a major effort, especially to reduce the amount of anthropogenic CO2 emissions. Approximately one-third of the CO2 released by humans into the atmosphere stems from the production of energy, a process during which mostly fossil fuels are burned in power plants in order to generate electricity. Particularly the use of modern technologies as well as additional political initiatives will translate into a considerable savings potential in the energy-producing sector in terms of avoiding a further increase in CO2 emissions.
A technically feasible way to reduce CO2 emissions in thermal power plants consists of extracting carbon from the fuels used for combustion processes. This requires an appropriate pretreatment of the fuel involving, for example, partial oxidation of the fuel with oxygen and/or a pretreatment of the fuel with steam. Such pretreated fuels usually have a high content of H2 and CO and, depending on the mixing ratios, exhibit heating values that, as rule, are below those of natural gas (NG). Consequently, such synthetically produced gases are referred to as MBtu gases or LBtu gases, depending on their heating value.
Due to their properties, such gases do not readily lend themselves for use in conventional burners designed for the combustion of natural gas of the type described, for example, in European patent specification EP 0 321 809 B1, European patent application EP 0 780 629 A2, international patent specification WO 93/17279 or European patent application EP 1 070 915 A1. In these burners, which work with a fuel premix, a conically widening vortex flow consisting of combustion air and admixed fuel is generated in the direction of flow, and this vortex flow becomes increasingly unstable in the direction of flow after exiting from the burner, preferably having been completely and homogenously mixed by means of the increasing swirling, and it then makes a transition to an annular vortex flow with backflow in the core.
In an embodiment, the present invention provides a method for the combustion of hydrogen-rich, gaseous fuels in combustion air in a burner of a gas turbine. The hydrogen-rich, gaseous fuel is injected at least partially isokinetically with respect to the combustion air such that the partially hydrogen-rich, gaseous fuel is injected at least partially in the same direction and at least partially at the same velocity as the combustion air.
The present invention will be described in even greater detail below based on the exemplary figures, which are schematic and not to scale. The invention is not limited to the exemplary embodiments. Features described and/or represented in the various figures can be used alone or combined in embodiments of the present invention. Other features and advantages of various embodiments of the present invention will become apparent by reading the following detailed description with reference to the attached drawings which illustrate the following:
Depending on the burner concept and as a function of the burner capacity, liquid and/or gaseous fuel is fed into the vortex flow that is forming inside a premix burner in order to create a fuel-air mixture that is as homogeneous as possible. However, as mentioned above, if, for purposes of attaining reduced CO2 emissions, the objective is to use synthetically processed, gaseous fuels that have a high content of hydrogen as an alternative to or in combination with the combustion of conventional types of fuel, then special requirements will be made of the structural design of the premix burner systems employed. For instance, in order for synthesis gases to be fed into burner systems, the volume flow rate of the fuel has to be far greater than in comparable burners operated with natural gas, resulting in markedly different flow pulse conditions. Due to the high percentage of hydrogen in the synthesis gas and the associated low ignition temperature and high flame velocity of the hydrogen, the fuel has a strong tendency to react, and this increases the risk of re-ignition. In order to avoid this, the mean retention time of the ignitable fuel-air mixture in the burner should be reduced to the greatest extent possible.
Today's combustion installations for gas turbines and the like, which are designed for the combustion of hydrogen-rich fuels, are based on a pronounced dilution of diffusion flames (with inert media such as, for instance, N2 and/or steam). The approach of lowering the output, that is to say, reducing the flame temperature, is also often employed. There are also efforts aimed at developing combustion systems with a lean premix combustion for hydrogen-rich fuels in order to further reduce the emissions and to minimize the use of expensive diluting media. Such systems require a high level of premixing. Unfortunately, however, the hydrogen-rich fuels are so reactive that considerable changes are necessary in order to burn these fuels safely and cleanly. These changes such as, for instance, raising the burner speed by selecting very high velocities for the fuel jets and/or for the combustion air, however, are usually incompatible with the requirements made of modern gas turbine burners, namely, low pressure losses in the burner as well as low losses in the fuel pressure.
The pursuit of the main objective regarding burners for hydrogen-rich fuels encounters the problem of safely filling the interior of the burner with the fuel in order to minimize the NOx emissions. The underlying design criteria for achieving this goal are:
Within the scope of developing lean premix burners for hydrogen-rich fuels, various approaches have been taken with the aim of improving the burners in terms of NOx emissions and the safeguards against flashback.
In another approach (
Lean premix burners are fundamentally plagued by re-ignition problems when they are operated with hydrogen-rich fuels. A particular challenge encountered with the lean premix burners that are operated with hydrogen-rich fuels is the need to meet the criterion of “forced re-ignition”. Here, a high-energy ignition is employed in an attempt to intentionally cause a re-ignition. If this cannot be done, the burner operation is stable. Up until now, none of the lean premix burners developed for hydrogen-rich fuels has met this criterion.
In an embodiment, the present invention provides a method for the combustion of hydrogen-rich fuels in a lean premix burner of a gas turbine, which avoids the drawbacks of the approaches known so far and provides a high level of safety against re-ignition, and, in another embodiment, a burner for carrying out the method.
The method according to an embodiment of the invention is characterized in that the hydrogen-rich, gaseous fuel is injected at least partially isokinetically with respect to the combustion air, that is to say, partially in the same direction and at the same velocity as the combustion air.
The phrase “partially isokinetic injection” refers to injection that, under the practical boundary conditions of a burner chamber, approximates an injection in the direction and at the velocity of the combustion air. In practical terms, partially isokinetic injection refers to injection at the velocity of the combustion air±50%. Typically, the isokinetic injection is performed at the velocity of the combustion air±20%.
In particular, the isokinetic injection takes place at a high burner load, that is to say, at high mass flow rates of the fuel gas and at high hot-gas temperatures close to the design point. In conventional premix burners for gas turbines, the fuel gas is typically injected at a velocity that is at least twice as high as the velocity of the combustion air.
When the fuel gas is injected from a wall of a burner, a directional component perpendicular to the wall surface is needed, even with isokinetic injection. Injection perpendicular to the wall surface or to the flow, however, is avoided. The angle between the direction of injection and the vertical is kept≧20° for the isokinetic injection. As long as a sufficient penetration depth of the fuel gas into the combustion air can be achieved, an angle of 30° to 50° is selected. The injection vector here is slanted by≧20° from the vertical in the flow direction. Typically, the deviation of the velocity component of the fuel gas and of the combustion air in the plane of the burner wall should amount to less than±20°. A deviation of less than±10°, for example, is achieved in the design point.
With isokinetic injection from the trailing edge of a part, the deviation between the injection direction and the flow direction of the combustion air in each plane can be less than±20°. In the design point, a deviation of less than±10° is achieved, for example, for each plane.
Isokinetic injection can be employed in burners with a vortex flow such as, for instance, in a double-cone burner, as well as in burners with a vortex-free through-flow.
Another embodiment of the method according to the invention is characterized in that the hydrogen-rich, gaseous fuel is injected into the combustion air through elongated rounded openings in a partially isokinetic manner. Here, the main axis of each of the elongated rounded openings is oriented parallel to the local air flow, and the hydrogen-rich, gaseous fuel is injected through the elongated rounded openings at a slant that, vis-à-vis the vertical of the vortex air flow, is oriented in the direction of the vortex air flow. In particular, the slant here is≧20°. As long as a sufficient penetration depth of the fuel gas into the combustion air can be achieved, an angle of 30° to 50° is selected. For the isokinetic injection, the velocity component of the injection of the fuel gas parallel to the plane of the burner wall should ideally be identical to the velocity component of the combustion air in this plane. Deviations cannot be avoided in actual practice. For instance, they can occur during operation at partial load due to changes in the velocity direction of the combustion air. Typically, the deviation of the velocity component of the fuel gas and of the combustion air in the plane of the burner wall should amount to less than±20°. A deviation of less than±10°, for example, is achieved in the design point. Accordingly, a perfect orientation cannot be ensured for all operating states when it comes to the orientation of the main axis of the elongated rounded opening. The deviation between the flow direction and the orientation of the main axis should be less than±20°. A deviation of less than±10°, for example, is achieved in the design point.
An elongated rounded opening is an opening that has an extension in one direction that is greater than in a second direction oriented perpendicular thereto. A slot or an oval are examples of an elongated rounded opening. As a special configuration of an oval, the elongated rounded opening can be configured as an ellipsis. Typically, the elongated rounded openings are configured with an axis of symmetry in their greatest longitudinal extension. They have a so-called main axis that extends in the greatest longitudinal direction and a secondary axis that extends at a right angle to the main axis. The main axis is typically also an axis of symmetry of the elongated rounded opening.
A further improvement can be attained in that the burner wall is effusion-cooled directly downstream from the elongated rounded openings by numerous effusion holes.
One embodiment of the method according to the invention is characterized in that the hydrogen-rich, gaseous fuel is injected through elongated rounded openings in a partially isokinetic manner into the vortex air flow of the combustion air of a double-cone burner. Here, the main axis of the elongated rounded openings is oriented parallel to the local vortex air flow. The hydrogen-rich, gaseous fuel is injected through the elongated rounded openings, for instance, at a slant that, vis-à-vis the vertical of the vortex air flow, is oriented in the direction of the vortex air flow. In particular, the slant here is≧20°. As long as a sufficient penetration depth of the fuel gas into the combustion air can be achieved, an angle of 30° to 50° is selected. For the isokinetic injection, the velocity component of the injection of the fuel gas in the plane of the burner wall should ideally be identical to the velocity component of the combustion air in the plane of the burner wall. Deviations cannot be avoided in actual practice. For instance, they can occur during operation at partial load due to changes in the velocity direction of the combustion air. Typically, the deviation of the velocity component of the fuel gas and of the combustion air in the plane of the burner wall should amount to less than±20°. A deviation of less than±10°, for example, is achieved in the design point. Accordingly, a perfect orientation cannot be ensured for all operating states when it comes to the orientation of the main axis of the elongated rounded opening. The deviation between the flow direction and the orientation of the main axis should be less than±20°. A deviation of less than±10°, for example, is achieved in the design point.
The ratio of the main axis to the secondary axis of the elongated rounded openings is greater than 2:1. A range of 2:1 to 5:1 can be readily achieved in actual practice. In a typical embodiment, the ratio of the main axis to the secondary axis of the elongated rounded openings is 3:1.
Typically, the cross-sectional surface area of the elongated rounded openings corresponds to the cross-sectional surface area of circular openings having a diameter between 2 mm and 6 mm.
In particular, the elongated rounded openings are arranged in the vicinity of the outlet of the double cone. In this context, the vicinity of the outlet comprises, for example, the rear one-third of the lengthwise extension of the burner as seen in the direction of the main flow; typically, the vicinity is even restricted to the rear one-fifth of the burner.
A further improvement can be achieved in that the double cone is effusion-cooled directly downstream from the elongated rounded openings by numerous effusion holes.
Another embodiment of the invention is characterized in that the hydrogen-rich, gaseous fuel is injected into the vortex air flow through elongated rounded openings in a fuel lance that projects into the interior of the double cone in the axial direction. The fuel lance is typically configured as a so-called long fuel lance. This is a lance which extends at least into the half of the double cone that is far way from the flow.
Within the scope of the invention, it is also conceivable for a mixing tube to be arranged in the axial direction downstream from the double cone and for the hydrogen-rich, gaseous fuel to be injected into the vortex air flow through elongated rounded openings in the wall of the mixing tube.
Another embodiment of the method according to the invention is characterized in that the hydrogen-rich, gaseous fuel is injected isokinetically with respect to the combustion air, that is to say, in the same direction and at the same velocity.
In this context, the combustion air preferably enters the interior of the double cone through air slits in the double cone, and the hydrogen-rich, gaseous fuel is injected isokinetically into the incoming combustion air in the area of the air slits.
Advantageously, the isokinetic injection can take place by means of a comb injector. A comb injector is a hollow element having essentially the structure of a comb through which the fuel gas is introduced and distributed, and also having hollow teeth extending from this hollow element, through which the fuel gas is conveyed to the injection openings at the ends of the teeth. Instead of individual teeth, the comb injector can be a hollow element that tapers like a wedge and that, on the side of the tip of the wedge, has a row of injection openings through which the fuel gas is injected. The structure of this embodiment corresponds in principle to that of the trailing edge of an air-cooled turbine blade having cooling-air holes on the trailing edge of the turbine blade. In the flow pattern, the row of fuel gas streams that exit from the injection openings then looks like the teeth of a comb. In order to carry out an isokinetic injection, the comb injector is oriented parallel to the direction of flow of the combustion air, whereby the teeth point in the direction of flow. However, it is likewise conceivable for the isokinetic injection to take place by means of a piggyback injector that is placed on top of the double cone. An example of a piggyback injector is a hollow element that has been placed on the side of the air feed on a half shell of a double cone, through which the fuel gas is then fed. This hollow element tapers like a wedge in the direction of flow. Fuel gas is isokinetically injected into the combustion air via a row of injection openings from the downstream edge. Analogously to the trailing edge of an air-cooled turbine blade having cooling-air holes on the trailing edge of the turbine blade, the trailing edge of the half shell facing downstream can also be configured with injection openings.
The burner according to an embodiment of the invention is characterized in that the burner has means to partially isokinetically or isokinetically inject a hydrogen-rich, gaseous fuel into the combustion air entering the double cone, and in that the injection means are connected to a source of fuel that supplies hydrogen-rich, gaseous fuel.
One embodiment of the burner according to the invention is characterized in that the means to partially isokinetically or isokinetically inject a hydrogen-rich, gaseous fuel into the combustion air entering the burner comprise elongated rounded openings, in that the main axis of each of the elongated rounded openings is oriented parallel to the local air flow, and in that the elongated rounded openings or lines and/or perforations or holes leading to the elongated rounded openings are configured in such a way that the hydrogen-rich, gaseous fuel is injected through the elongated rounded openings at a slant that, vis-à-vis the vertical of the local vortex air flow, is oriented in the direction of the vortex air flow. For this purpose, for example, the perforations or holes through which the fuel gas is conveyed through the burner wall to the elongated rounded openings are configured with a slant or at an angle to the normal of the burner wall.
As an alternative, for instance, feed lines are suitable which pass through the burner wall at an orientation normal to the burner surface and which are configured with a deflection in the area of the elongated rounded openings.
Preferably, the slant is≧20°. The ratio of the main axis to the secondary axis of the elongated rounded openings is greater than 2:1. A range of 2:1 to 5:1 can be readily achieved in actual practice. In a typical embodiment, the ratio of the main axis to the secondary axis of the elongated rounded openings is 3:1.
In an embodiment, the cross-sectional surface area of the elongated rounded openings corresponds to the cross-sectional surface area of circular openings having a diameter between 2 mm and 6 mm.
According to another embodiment, the elongated rounded openings are arranged in the vicinity of the outlet of the burner.
In one embodiment, the burner according to the invention is a double-cone burner. The double-cone burner according to the invention is characterized in that the double-cone burner has a double cone as well as means to partially isokinetically or isokinetically inject a hydrogen-rich, gaseous fuel into the combustion air entering the double cone, and in that the injection means are connected to a source of fuel that supplies hydrogen-rich, gaseous fuel.
One embodiment of the double-cone burner according to the invention is characterized in that the means to partially isokinetically or isokinetically inject a hydrogen-rich, gaseous fuel into the combustion air entering the double cone comprise elongated rounded openings, in that the main axis of each of the elongated rounded openings is oriented parallel to the local vortex air flow, and in that the elongated rounded openings are configured in such a way that the hydrogen-rich, gaseous fuel is injected through the elongated rounded openings at a slant that, vis-à-vis the vertical of the vortex air flow, is oriented in the direction of the vortex air flow.
Preferably, the slant is≧20°. The ratio of the main axis to the secondary axis of the elongated rounded openings is greater than 2:1. A range of 2:1 to 5:1 is advantageous in actual practice. In a typical embodiment, the ratio of the main axis to the secondary axis of the elongated rounded openings is 3:1.
Typically, the cross-sectional surface area of the elongated rounded openings corresponds to the cross-sectional surface area of circular openings having a diameter between 2 mm and 6 mm.
According to another embodiment, the elongated rounded openings are arranged in the vicinity of the outlet of the double cone.
According to another embodiment, the elongated rounded openings are arranged in the vicinity of the outlet of a mixing tube of a double-cone burner that adjoins the double cone.
Another embodiment of the double-cone burner according to the invention is characterized in that the double cone has air slits for the combustion air to enter the interior of the double cone, and in that the means to partially isokinetically or isokinetically inject a hydrogen-rich, gaseous fuel into the combustion air entering the double cone comprise a plurality of tangentially oriented fuel nozzles arranged in the area of the air slits.
Here, the fuel nozzles are preferably part of a comb injector or of a piggyback injector that is placed on top of the double cone.
Furthermore, it is also possible to provide a fuel lance that projects into the interior of the double cone and that has elongated rounded openings in the axial direction.
Within the scope of the invention, the term combustion air refers not only to pure combustion air but also to a mixture of air and re-circulated exhaust gases, or to an air mixture mixed with inert gas.
Experiments with injection devices that resist a forced re-ignition have shown that there are numerous configuration features that prevent anchoring of hydrogen-rich flames when fuels are injected into a crosswise flow. The design rules demonstrate that the partially isokinetic injection of fuel is best suited for meeting the criteria based on forced re-ignition. Fuel injection which is done in the same direction and which also has an injection velocity that is similar to that of the local combustion-air flow is the safest injection method for hydrogen-rich fuels.
Consequently, the solution for the problems outlined above lies in applying these design rules to conical burners, especially to double-cone burners of the EV or AEV type. In this context, there are two main methods for transferring these rules to conical burners. One method aims at a re-ignition-proof diffusive burner for hydrogen-rich fuels wherein H2>>50%. The other method allows a re-ignition-proof, purely premix operation with hydrogen-rich fuels with a low NOx emission and slight dilution.
On the basis of a burner for MBtu fuel, as shown in
In the final analysis, this type of injection constitutes an injection into a crosswise flow. However, it can also be referred to as “partially isokinetic” since, due to the slant, to the shape and to the dimensions of the opening, the interaction between the fuel jet and the crosswise flowing air is minimized at the injection point, as a result of which recirculation and stagnation zones as well as initial shear stresses are minimized.
It has also been found that effusion cooling directly downstream from the elongated rounded openings 24 considerably reduces the tendency of the injectors to hold the flame. This is done by means of appropriate finely distributed outflow holes 25 of the type depicted in
With another injection method, the fuel is injected into the air slits of a double-cone burner (e.g. of the EV or AEV type), whereby the injection direction is oriented precisely towards the local air flow, and the injection velocity is in the same order of magnitude as the local flow velocity of the air (see
It is also recommended for the hydrogen-rich fuel to be injected in stages (in the present example of
If the fuel jets are not perfectly oriented towards the local air flow, then elliptical openings according to
Due to the injection according to the invention of the hydrogen-rich fuel, the burner parts used for the premixing of natural gas and for the injection of liquid fuels such as oil, remain unaffected, so that the burners can operate as three-fuel burners.
It is also possible to use the described partially isokinetic injection (
Thus, for instance, as shown in
Finally, similar to the case of
Downstream from the elongated rounded openings 24, for the isokinetic injection of the hydrogen-rich, gaseous fuel, effusion cooling 3 of the burner wall is carried out by a field of effusion holes 25 through which the cooling air is injected.
All of the advantages elaborated upon can be used not only in the combinations given but also in other combinations or on their own, without departing from the scope of the invention. For instance, instead of a rectangular flow cross section, as shown in
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This application is a continuation of International Patent Application No. PCT/EP2010/063461, filed on Sep. 14, 2010 which claims priority to Swiss Patent Application No. CH 01438/09, filed on Sep. 17, 2009. The entire disclosure of both applications is hereby incorporated by reference herein.
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Number | Date | Country | |
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Number | Date | Country | |
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Parent | PCT/EP2010/063461 | Sep 2010 | US |
Child | 13405396 | US |