JP5344897B2 - Swirl combustion boiler - Google Patents

Description

  The present invention relates to a swirl combustion boiler applied to a boiler that burns pulverized fuel such as pulverized coal.

Conventionally, swirl combustion boilers and counter combustion boilers are known as pulverized coal fired boilers.
Of these, in the pulverized coal-fired swirl combustion boiler, secondary air input ports for secondary air input are installed above and below the primary air input from the coal burner together with the pulverized coal of fuel. The flow rate is adjusted for the secondary air. The secondary air input port for supplying secondary air may also serve as an oil burner.

The primary air described above is an amount of air necessary for conveying pulverized coal as fuel, and the amount of air is defined in a roller mill device that pulverizes coal into pulverized coal.
The secondary air mentioned above blows in the air quantity required in order to form the whole flame in a swirl combustion boiler. Therefore, the secondary air amount of the swirl combustion boiler is approximately the total air amount necessary for the combustion of the pulverized coal minus the primary air amount.

On the other hand, in the burner of the opposed combustion boiler, it has been proposed to finely adjust the air introduction amount by introducing secondary air and tertiary air outside the primary air (pulverized coal supply). (For example, see Patent Document 1)
JP 2006-189188 A

  By the way, in the conventional swirl combustion boiler described above, there is one secondary air input port for secondary air input provided above and below the coal burner, and the amount of secondary air input from the secondary air input port. This is a configuration that cannot be finely adjusted. For this reason, a high temperature oxygen residual region is formed on the outer periphery of the flame, and particularly in a region where the secondary air is concentrated, the high temperature oxygen residual region becomes strong and causes an increase in the amount of NOx generation.

  On the other hand, counter-fired boilers have been devised to further diffuse air to the outer periphery by installing tertiary air around the burner and swirling the secondary air or tertiary air. In addition, it was necessary to finely adjust the turning angle.

From such a background, in the conventional swirl combustion boiler, it is desired to suppress the high temperature oxygen remaining region formed on the outer periphery of the flame and reduce the amount of NOx generated.
The present invention has been made in view of the above circumstances, and its object is to reduce the amount of NOx generated by suppressing (weakening) the high temperature oxygen remaining region formed on the outer periphery of the flame. An object of the present invention is to provide a swirl combustion boiler.

In order to solve the above problems, the present invention employs the following means.
In the swirl combustion boiler according to the present invention, the burner for charging pulverized fuel and air into the furnace is a burner unit of a swirl combustion method in which each burner portion is disposed at each corner portion or wall surface portion. In a swirl combustion boiler in which a plurality of swirl flames are formed, the burner is provided so as to surround a primary port of a call for supplying pulverized fuel conveyed by primary air and the periphery of the primary port of the call. A fuel burner for supplying powdered fuel and air with a secondary port for injecting a part of secondary air, and a fuel burner disposed above and below the fuel burner , having flow rate adjusting means, and above and below the fuel burner and a secondary air injection port is divided into a plurality of flow paths multistage independent toward secondary air injection for the secondary air to be introduced from the secondary air injection port, a desired secondary air amount The flow rate is distributed to the pulverized fuel and the air in the same direction as the pulverized fuel and the air, and the flame burner is inserted into the outer periphery of the flame. And the secondary air inlet port is provided with an angle adjusting mechanism .

According to such a swirl combustion boiler, the burner is provided so as to surround the primary port of the call where the pulverized fuel transported by the primary air is introduced and the primary port of the coal. A fuel burner for supplying powdered fuel and air with a secondary port for injecting part of the fuel, and a fuel burner disposed above and below the fuel burner , having flow rate adjusting means, and having multiple independent stages in the vertical direction of the fuel burner Secondary air input port for secondary air input divided into a plurality of flow paths, and the secondary air input from the secondary air input port distributes the amount of secondary air to a desired value. Since it is thrown into the outer periphery of the flame in the same direction as the pulverized fuel and air, it is desired to operate the flow rate adjusting means for each of the divided flow paths for the secondary air amount to be put into the outer circumference of the flame. Distribute the flow rate so that It becomes possible. Therefore, the formation of the high temperature oxygen remaining region can be suppressed or prevented by optimizing the amount of secondary air supplied to the flame periphery.

Further, since the burner includes one or a plurality of secondary air input ports on the left and right of the fuel burner , the secondary air can be distributed to the left and right of the flame. Therefore, it is possible to prevent the secondary air from becoming excessive above and below the flame and to distribute the flow rate of the secondary air supplied to the outer periphery of the flame more precisely.

Furthermore, since the fuel burner is provided with a split at the tip of the nozzle , flame holding can be strengthened to prevent or suppress the formation of a high-temperature oxygen residual region.

And since the said secondary air injection | throwing-in port is equipped with the angle adjustment mechanism, the secondary air supply to the flame outer side is attained. Further, since the swirl is not used, the formation of the high-temperature oxygen remaining region can be prevented or suppressed while preventing the flame from spreading excessively.

  In the swirl combustion boiler of the present invention, it is preferable that the distribution of the air amount input from the secondary air input port is feedback-controlled based on the unburned component and the nitrogen oxide (NOx) discharge amount. Secondary air distribution can be automatically optimized. In this case, when there is a large amount of unburnt, the secondary air distribution to the inside near the outer peripheral surface of the flame is increased, and when the amount of nitrogen oxide is high, the distribution to the outer side far from the outer peripheral surface of the flame is increased. Increase secondary air distribution. In addition, about the measurement of an unburned part, what is necessary is just to employ | adopt the meter which measures carbon concentration from scattering of a laser beam, for example.

  In the swirl combustion boiler of the present invention, the amount of air input from the secondary air input port is distributed between multistage input of air having a reducing atmosphere in the region from the burner unit to the additional air input unit. In this way, the synergistic effect of reducing nitrogen oxides by suppressing the high temperature oxygen remaining region formed around the flame periphery and reducing the nitrogen oxides in the combustion exhaust gas in a reducing atmosphere, the nitrogen oxides The generation amount can be further reduced.

  According to the swirl combustion boiler of the present invention described above, by adjusting the input of the secondary air, it becomes possible to prevent or suppress the concentration of the secondary air with respect to the flame outer periphery, and as a result, formed on the flame outer periphery. It is possible to reduce the generation amount of nitrogen oxide (NOx) by suppressing the high temperature oxygen remaining region.

Hereinafter, an embodiment of a swirl combustion boiler according to the present invention will be described with reference to the drawings.
The swirl combustion boiler 10 shown in FIG. 5 has a reducing atmosphere in a region from the burner unit 12 to the additional air input unit (hereinafter referred to as “AA unit”) 14 by inputting air into the furnace 11 in multiple stages. It aims to reduce NOx in combustion exhaust gas. As for the distance from the burner section 12 to the AA section 14 serving as the reducing atmosphere, that is, the distance (height) of the reducing combustion zone, the longer the residence time of the combustion gas becomes, the smaller the NOx generation amount becomes. In the figure, reference numeral 20 is a burner for charging powdered fuel such as pulverized coal and air, and 15 is an additional air charging nozzle for charging additional air. In the following description, the swirl combustion boiler 10 is a pulverized fuel. Use pulverized coal as pulverized coal.

  In this way, the above-described swirl combustion boiler 10 is a swirl combustion type burner unit 12 in which the burners 20 for introducing pulverized coal (powder fuel) and air into the furnace 11 are arranged at each corner of each stage. The swirl combustion method is used in which one or more swirl flames are formed in each stage. And each burner 20 of the burner part 12 is each arrange | positioned above and below the pulverized coal burner 21, and pulverized coal burner 21, and inputs secondary air, for example, as shown in FIG. And a secondary air input port 30.

The pulverized coal burner 21 is provided so as to surround the rectangular primary coal port 22 for introducing the pulverized coal conveyed by the primary air and the primary coal port 22, and a part of the secondary air is introduced. The call secondary port 23 is provided.
A secondary air input port 30 is provided above and below the pulverized coal burner 21 for supplying secondary air. The secondary air input port 30 is divided into a plurality of independent flow paths and ports, and each flow path is provided with a damper 40 capable of adjusting the opening degree as secondary air flow rate adjusting means. Yes.

  In the illustrated configuration example, the secondary air input ports 30 arranged above and below the pulverized coal burner 21 are all divided into three in the vertical direction, and the internal secondary is directed from the inside close to the pulverized coal burner 21 to the outside. The air ports 31a and 31b, the intermediate secondary air ports 32a and 32b, and the external secondary air ports 33a and 33b are arranged in this order. In addition, the division | segmentation number of such a secondary air injection | throwing-in port 30 is not limited to 3 division | segmentation, It can change suitably according to various conditions.

  The above-described call secondary port 23, internal secondary air ports 31a and 31b, intermediate secondary air ports 32a and 32b, and external secondary air ports 33a and 33b are, for example, as shown in FIG. An independent secondary air supply for each port is connected to an air supply line 50 having an air supply source (not shown) and the opening degree of the damper 40 provided in each flow path communicating with each port is adjusted. The amount can be adjusted.

  According to such a swirl combustion boiler 10, each burner 20 includes a pulverized coal burner 21 that inputs pulverized coal and air, and a three-part secondary air input port that is disposed above and below the pulverized coal burner 21. Therefore, by adjusting the opening degree of the damper 40 for each of the divided secondary air input ports 30, the amount of secondary air input to the outer periphery of the flame F can be distributed to a desired value. Therefore, for example, the distribution ratio is reduced for the secondary air input amount of the internal secondary air ports 31a and 31b closest to the outer periphery of the flame F, and the intermediate secondary air ports 32a and 32b and the external secondary air ports 33a and 33b are correspondingly reduced. By sequentially increasing the charging rate of the secondary air amount to be introduced into the region, the local high-temperature oxygen remaining region (hatched portion in the figure) H formed on the outer periphery of the flame F can be suppressed.

  That is, the diffusion rate of the secondary air is slowed by increasing the injection rate of the secondary air amount with respect to the outer side away from the flame F and reducing the injection rate of the secondary air amount injected near the outer periphery of the flame F. Can do. As a result, it becomes possible to prevent or suppress the concentration of secondary air around the flame F, and therefore the local high temperature oxygen residual region H becomes weak and small. Therefore, the amount of NOx generated in the swirl combustion boiler 10 Can be reduced. In other words, by optimizing the amount of secondary air introduced into the outer periphery of the flame F, the formation of the high temperature oxygen residual region H can be suppressed or prevented, and the NOx reduction of the swirl combustion boiler 10 can be achieved.

  On the other hand, when the secondary air needs to be diffused due to the properties of the pulverized coal, etc., the distribution ratio of the internal secondary air ports 31a and 31b is increased by reversing the flow rate distribution of the secondary air input port 30 inside and outside. do it. That is, even when using pulverized coal obtained by pulverizing coal having a different fuel ratio such as a large amount of volatile matter, the flow distribution of the secondary air supplied from each of the divided secondary air input ports 30 is appropriately adjusted. By doing so, it is possible to select appropriate combustion with reduced NOx or unburned content.

By the way, the pulverized coal burner 21 described above is preferably provided with a split 24 that divides the opening area vertically at the nozzle tip, as in the first modification shown in FIG. The illustrated split 24 has a triangular cross section, and is arranged so as to separate and diffuse the pulverized coal and primary air flowing in the nozzle in the vertical direction, thereby strengthening the flame holding and the high temperature oxygen remaining region H. The formation of is suppressed or prevented.
That is, by passing through the split 24, a flow having a high pulverized coal concentration is formed on the outer periphery of the split 24, which is effective in strengthening flame holding. Further, the flow of the pulverized coal concentration that has passed through the split 24 flows into a negative pressure region formed on the downstream side of the split 24, as indicated by a broken-line arrow fa in the figure. As a result, the flame F is also drawn into the negative pressure region by this air flow, so that the flame holding is further strengthened. As a result, combustion is promoted and oxygen can be consumed quickly. Note that the split 24 may be formed of a plurality of bodies or may be appropriately devised in shape.

Moreover, it is preferable that the burner 20 mentioned above is equipped with the 1 or several side part secondary air ports 34L and 34R on the right and left of the pulverized coal burner 21, for example like the 2nd modification shown in FIG. In the illustrated configuration example, one side secondary air port 34L, 34R each provided with a damper (not shown) is provided on the left and right sides of the pulverized coal burner 21, but each is divided into a plurality of flow rates. Control may be performed.
With this configuration, the secondary air can be distributed to the left and right sides of the flame F, so that the secondary air can be prevented from becoming excessive above and below the flame F. That is, with respect to the amount of secondary air introduced into the outer periphery of the flame F, the vertical and horizontal distribution can be adjusted as appropriate, so that more precise flow rate distribution is possible.

In addition, in the above-described swirl combustion boiler 10, as shown in FIG. 4, for example, the secondary air input port 30 is a tilt mechanism as an angle adjustment mechanism that changes the input direction of the secondary air into the furnace 11 up and down. It is desirable to have. This tilt mechanism changes the tilt angle θ of the secondary air input port 30 up and down with respect to the horizontal, and promotes the diffusion of the secondary air to prevent or suppress the formation of the high temperature oxygen residual region H. be able to. In this case, a suitable tilt angle θ is about ± 30 degrees.
By providing such a tilt mechanism, it becomes possible to adjust the angle of the secondary air introduced from the secondary air entry port 30 toward the flame F in the furnace 11, so that the air diffusion in the furnace 11 is more precise. Control becomes possible. In particular, when the coal type of the pulverized coal fuel is extremely changed, the effect of reducing NOx can be further improved by changing the input angle of the secondary air.

Further, in the above-described swirl combustion boiler 10, the distribution of the air amount input from the secondary air input port 30 is adjusted by feedback control of the opening degree of the damper 40 based on the unburned amount and the NOx discharge amount. Is desirable. That is, when there is a large amount of unburned fuel in the swirl combustion boiler 10, the secondary air distribution of the internal secondary air ports 31a and 31b close to the outer peripheral surface of the flame F is increased, and when the NOx emission amount is high, the flame The secondary air distribution of the external secondary air ports 33a and 33b far from the outer peripheral surface of F is increased. In this case, an instrument for measuring the carbon concentration from the scattering of the laser light may be employed for the measurement of the unburned content, and a known measuring instrument may be employed for the NOx emission amount.
By performing such feedback control, the swirl combustion boiler 10 can automatically optimize the distribution of secondary air according to the combustion state.

  Further, in the above-described swirl combustion boiler 10, the amount of secondary air input from the secondary air input port 30 is distributed between the multistage input of air having a reducing atmosphere in the region from the burner unit 12 to the AA unit 14. It is desirable that That is, the secondary air amount input from the divided secondary air input port 30 is input from the secondary air input port 30 by the combined use with the two-stage combustion in which air is input in multiple stages from the AA section 14. The amount of secondary air can be reduced. Therefore, the amount of NOx generated is further reduced by the synergistic effect of reducing NOx by suppressing the high temperature oxygen residual region H formed on the outer periphery of the flame F and reducing NOx of the combustion exhaust gas in a reducing atmosphere. can do.

As described above, according to the swirl combustion boiler 10 of the present invention described above, the secondary air amount introduced from the divided secondary air introduction port 30 is adjusted for each port, whereby the secondary to the outer periphery of the flame F is adjusted. As a result, the concentration of air can be prevented or suppressed, and as a result, the high-temperature oxygen remaining region H formed on the outer periphery of the flame F can be suppressed and the amount of NOx generated can be reduced.
Further, in the above-described embodiment, the swirl combustion boiler 10 in which the region from the burner unit 12 to the AA unit 14 is used as the reducing atmosphere is described as a swirl combustion boiler 10, but the present invention is not limited to this.
In addition, this invention is not limited to embodiment mentioned above, For example, pulverized fuel is not limited to pulverized coal, For example, it can change suitably in the range which does not deviate from the summary.

It is a figure which shows one Embodiment of the turning combustion boiler which concerns on this invention, (a) is a longitudinal cross-sectional view which shows the structural example of a burner, (b) is the front view which looked at the burner of (a) from the inside of a furnace, (c ) Is a diagram showing an air supply system. As a first modification of the swirl combustion boiler shown in FIG. 1, (a) is a longitudinal sectional view showing a configuration example of a burner provided with a split, and (b) is a front view of the burner of (a) as seen from inside a furnace. It is. FIG. 6 is a front view of a burner provided with a side secondary air port as seen from the furnace as a second modification of the swirl combustion boiler shown in FIG. 1. It is a longitudinal cross-sectional view which shows the structural example in which the secondary air injection | throwing-in port of the burner shown to Fig.1 (a) is provided with the tilt mechanism. It is a figure which shows the structural example of the swirl | burning combustion boiler which is equipped with an additional air injection | throwing-in part, and introduce | transduces air in multistage.

Explanation of symbols

DESCRIPTION OF SYMBOLS 10 Swirling combustion boiler 11 Furnace 12 Burner part 14 Additional air injection part (AA part)
20 Burner 21 Pulverized coal burner 22 Cole primary port 23 Cole secondary port 24 Split 30 Secondary air input port 31a, 31b Internal secondary air port 32a, 32b Intermediate secondary air port 33a, 33b External secondary air port 34L, 34R Side secondary air port 40 Damper F Flame H High temperature oxygen remaining area

Claims (3)

The burner for charging pulverized fuel and air into the furnace is a swirl combustion type burner portion disposed at each corner portion or wall surface portion of each stage, and the swirl where one or more swirl flames are formed at each stage. In the combustion boiler,
A call primary port for supplying the pulverized fuel conveyed by the primary air and a call secondary port provided so as to surround the periphery of the call primary port and input a part of the secondary air And a fuel burner for charging pulverized fuel and air,
A secondary air input port for secondary air input, which is disposed above and below the fuel burner , has flow rate adjusting means, and is divided into a plurality of independent multiple flow paths in the vertical direction of the fuel burner ,
The secondary air input from the secondary air input port is distributed to the outer periphery of the flame in the same direction as the pulverized fuel and air by distributing the flow amount of the secondary air to a desired value,
The fuel burner comprises one or more secondary air input ports on the left and right of the fuel burner, and a split at the nozzle tip,
The swirl combustion boiler, wherein the secondary air input port includes an angle adjustment mechanism . 2. The swirl combustion boiler according to claim 1 , wherein the distribution of the amount of air input from the secondary air input port is feedback-controlled based on the unburned amount and the nitrogen oxide (NOx) discharge amount. The amount of air injected from the secondary air injection ports, claim 1, characterized in that it is distributed between multistage introduction of air to the reducing atmosphere region from the burner portion to the additional air injection unit or 2. A swirl combustion boiler according to 2.

Images