JP2010270991A - Coal burning boiler - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a coal burning boiler for burning fine powder coal (solid fuel) capable of reducing an NOx generation amount by suppressing a high-temperature oxygen remaining area formed around the periphery of flame. <P>SOLUTION: In the coal burning boiler, a burner 20 for putting the fine powder coal and air into a furnace is made to be a turning combustion type burner arranged at each corner of each stage or on a wall surface, and one or a plurality of turning flames are formed in each stage. The burner 20 includes a fuel burner 21 for putting the fine powder coal and air, and secondary air input ports 30 formed at upper/lower sides or at right/left sides of the fuel burner 21 and having a flow rate adjustment means. One or a plurality of split members 24 are provided at a flow passage edge of the fuel burner 21. A separation distance L is set between the fuel burner 21 and the secondary air input port 30 at such a degree that secondary air put from the secondary air input port 30 does not interfere with the flame formed from the fuel burner 21 into the furnace. <P>COPYRIGHT: (C)2011,JPO&INPIT

Description

  The present invention relates to a coal fired boiler that uses coal such as pulverized coal as fuel.

Conventionally, solid fuel-fired boilers include, for example, pulverized coal-fired boilers that burn pulverized coal as solid fuel. In such a pulverized coal fired boiler, two types of combustion systems are known: a swirl combustion boiler and an opposed combustion boiler.
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. (For example, see Patent Document 1)

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 2)

Japanese Patent No. 3679998 JP 2006-189188 A

By the way, in the conventional coal fired boiler described above, in order to reduce nitrogen oxides (NOx), in general, two-stage combustion using additional air (AA) is performed, and reduction combustion is performed near the burner. Has been done.
Further, in the conventional burner, a flame holding mechanism (adjustment of the tip corner, turning, etc.) is installed on the outer periphery of the pulverized coal burner, and further, the secondary air or the tertiary air is adjacent to the outer periphery of the pulverized coal burner. In general, a configuration in which an air input port for supplying air is installed is provided. For this reason, in the pulverized coal burner, the charged pulverized coal is ignited on the outer periphery of the flame, and a large amount of air is mixed in the ignition region on the outer periphery of the flame.

As a result, in the flame of the pulverized coal burner, a high-temperature oxygen residual region that generates NOx is formed on the outer periphery of the flame. This high temperature oxygen residual region is a flame outer periphery region where the oxygen concentration becomes high and combustion at a high temperature proceeds, and therefore, it is a combustion environment in which NOx is likely to be generated. Therefore, in the flame formed in the conventional pulverized coal burner, the amount of NOx generated from the outer periphery of the flame forming the high temperature oxygen residual region increases.
In this way, NOx generated from the outer periphery of the flame of the pulverized coal burner passes through the outer periphery of the flame as it is, so that the reduction is delayed as compared with the inside of the flame having a different combustion environment. As a result, the NOx generated outside the flame remains without being reduced, and the remaining NOx causes NOx generation in the conventional pulverized coal burner and coal fired boiler.

From such a background, in a coal fired boiler that burns solid fuel such as pulverized coal, it is desirable 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. It is to provide a solid fuel-fired coal fired boiler.

In order to solve the above problems, the present invention employs the following means.
In the coal fired boiler according to the present invention, a burner for charging pulverized fuel and air into a furnace is a burner unit of a swirl combustion system in which each burner part is disposed at each corner part or wall face part. In a coal fired boiler in which a plurality of swirling flames are formed, the burner has a fuel burner for charging pulverized fuel and air, and a secondary air input having flow rate adjusting means disposed above and below or on the left and right of the fuel burner. And one or a plurality of split members provided at the front end of the flow path of the fuel burner, and formed between the fuel burner and the secondary air input port from the fuel burner into the furnace. A separation distance is set such that the secondary air introduced from the secondary air introduction port does not interfere with the flame to be produced.

According to such a coal fired boiler of the present invention, a burner is provided with a fuel burner for charging pulverized fuel and air, and a secondary air input port having flow rate adjusting means disposed above and below or on the left and right of the fuel burner. 1 or a plurality of split members are provided at the front end of the flow path of the fuel burner, and a flame formed between the fuel burner and the secondary air input port from the fuel burner into the furnace 2 Since the separation air is provided so as not to interfere with the secondary air that is input from the secondary air input port, the flow of the pulverized fuel passes through the split member, which causes the turbulence in the flow inside the flame and causes the pulverized fuel. Is formed. Therefore, the split member functions as a flame holding mechanism that ensures stable ignition of the pulverized fuel, and the spread of the flame is suppressed and the pulverized fuel is ignited inside the flame. Generated internally and reduced quickly.
Further, since a separation distance is provided between the secondary air input port and the fuel burner so that the secondary air does not interfere with the flame, the secondary air supplied to the flame from the secondary air input port. The oxygen concentration in the flame can be lowered by slowing the supply of gas.

As a result, the temperature drop (cooling) of the flame due to the low-temperature secondary air can be minimized by slowly supplying the secondary air from the secondary air input port arranged so as not to interfere with the flame. Despite the fact that the flame is short of air, the flame is heated to a stable temperature and continues to ignite stably, enabling combustion at a high temperature and a low oxygen concentration. That is, the high-temperature oxygen remaining region formed on the outer periphery of the flame is suppressed, and combustion with significantly reduced NOx and unburned content becomes possible.
When a plurality of split members functioning as a flame holding mechanism are installed, a predetermined interval is provided between adjacent split members.

  In the above coal fired boiler, it is preferable to provide the split member in a plurality of directions, whereby a plurality of pulverized fuel concentrations are formed in the flame, so that the flame holding function can be further improved. it can. The plural directions in this case include, for example, combinations of left and right directions and up and down directions.

  In the coal fired boiler described above, it is preferable to concentrate the split member at the central portion of the cross section of the flow path, so that the density formation of the pulverized fuel is concentrated at the central portion of the flame. Is further promoted, and the distance from the secondary air can be kept effective.

In the coal fired boiler described above, the secondary air input port is preferably installed so as to have an outward angle with respect to the axial center of the fuel burner, whereby the installation position of the secondary air input port is determined. Even if it is close to the fuel burner, the secondary air input from the secondary air input port does not interfere with the flame formed from the fuel burner into the furnace, so that the burner height can be reduced.
Further, when the secondary air input port is adjacent, the mixing of the secondary air and the flame can be delayed by injecting the secondary air obliquely with respect to the flame.

In the coal fired boiler described above, a rib may be provided inside the flow path of the secondary air input port, or a swirl blade may be provided.
Here, by providing a rib inside the flow path of the secondary air input port, for example, on the inner side (fuel burner side) of the flow path, the mixing of the secondary air to the flame can be adjusted. Further, by providing a swirling impeller inside the flow path, it is possible to suppress the burner height and separate the flow so that the flow of secondary air does not interfere with the flame.

According to the present invention described above, in a coal fired boiler that burns solid fuel such as pulverized coal, a remarkable effect of suppressing the amount of NOx generated by suppressing the high temperature oxygen remaining region formed on the outer periphery of the flame is obtained.
That is, the fuel burner of the present invention is provided with a split member having a flame holding function in the fuel flow path for supplying the pulverized fuel into the furnace to suppress the spread of the flame, and the pulverized fuel even in a low oxygen concentration environment. Can be stably burned. Since the pulverized fuel is ignited inside the flame, the NOx generated inside the flame is quickly reduced and the emission amount is reduced.

  In addition, since the secondary air is slowly supplied from the secondary air input port arranged so as not to interfere with the flame, the temperature drop (cooling) of the flame due to the low temperature secondary air is minimized, Despite the lack of air in the flame, stable ignition is continued while maintaining a high temperature flame. Therefore, the coal fired boiler according to the present invention can be combusted in an environment of high temperature and low oxygen concentration, and can be combusted with both NOx and unburned components greatly reduced.

It is a figure which shows one Embodiment of the coal fired boiler which concerns on this invention, (a) is a longitudinal cross-sectional view which shows a burner structure, (b) is the front view which looked at the burner of (a) from the inside of a furnace. It is a figure which shows the supply system of secondary air about the burner structure shown in FIG. It is a longitudinal section showing an example of composition of a coal fired boiler concerning the present invention. FIG. 4 is a horizontal (horizontal) cross-sectional view of FIG. 3. 2A and 2B are views showing a modification of the split member shown in FIG. 1, in which FIG. 1A is a cross-sectional view showing a split member having a Y-shaped cross section, and FIG. The 1st modification of the burner structure shown in FIG. 1 is shown, (a) is a longitudinal cross-sectional view, (b) is the front view which looked at the burner of (a) from the inside of a furnace. It is a figure which shows the 2nd modification of the burner structure shown in FIG. 1, and is the front view which looked at the burner from the inside of a furnace. It is a longitudinal cross-sectional view which shows the 3rd modification of the burner structure shown in FIG. It is a longitudinal cross-sectional view which shows the 4th modification of the burner structure shown in FIG. It is a figure which shows the 5th modification of the burner structure shown in FIG. 1, (a) is a top view, (b) is the front view which looked at the burner from the inside of a furnace. It is a top view which shows the 6th modification of the burner structure shown in FIG. It is a longitudinal cross-sectional view which shows the 7th modification of the burner structure shown in FIG.

Hereinafter, an embodiment of a coal fired boiler according to the present invention will be described with reference to the drawings.
The coal fired boiler 10 shown in FIG. 3 and FIG. 4 reduces the 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. The atmosphere is designed 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 denotes a burner that inputs pulverized fuel such as pulverized coal and air, and 15 is an additional air input nozzle that inputs additional air.

  In the following embodiment, although the coal fired boiler 10 demonstrates as pulverized coal burning using pulverized coal as a pulverized fuel, it is not limited to this. Therefore, the pulverized coal-burning burner 20 is connected to the pulverized coal mixture transport pipe 16 that transports the pulverized coal with primary air and the air supply duct 17 that supplies the secondary air. An air supply duct 17 for supplying secondary air is connected.

  As described above, the coal fired boiler 10 described above is a swirl combustion type burner unit 12 in which the burner 20 for introducing pulverized coal (powder fuel) and air into the furnace 11 is disposed at each corner of each stage. In each stage, a swirl combustion method is employed in which one or a plurality of swirl flames (one in the illustrated example) are formed. That is, in the coal fired boiler 10 shown in FIG. 3 and FIG. 4, the burner 20 that inputs pulverized coal and air into the furnace 11 (inside the furnace) has each section in the furnace 11 having a substantially square cross section. One swirl flame is formed by being arranged at each corner. However, in the present invention described below, for example, by arranging the burner 20 on the corner portion and the wall surface portion in the furnace 11 having a rectangular cross-sectional shape, the burner portion or the like of the swirl combustion method that forms two swirl flames. Is also applicable and is not particularly limited.

In the coal fired boiler 10 of the present embodiment, each burner 20 of the burner unit 12 includes, for example, a pulverized coal burner (fuel burner) 21 for introducing pulverized coal and air, and a pulverized coal burner 21 as shown in FIG. And a secondary air inlet port 30 for injecting secondary air, which is arranged above and below.
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. The pulverized coal charged from the pulverized coal burner 21 flows substantially straight toward the furnace 11.

Secondary air input ports 30 are provided substantially in parallel above and below the pulverized coal burner 21 for supplying secondary air. The secondary air input port 30 is divided into independent flow paths and ports, and the secondary air input from the secondary air input port 30 flows substantially straight into the furnace 11.
As shown in FIG. 2, for example, as shown in FIG. 2, the flow rate adjusting means of the secondary air supplied to each flow path of the secondary air input port 30 and the call secondary port 23 through flow paths branched from the air supply duct 17. As shown in FIG. In addition, about the position of the secondary air injection | throwing-in port 30, it is not limited to the upper and lower sides of the pulverized coal burner 21, and may be right and left.

In the illustrated configuration example, the pulverized coal burner 21 of the burner 20 is charged with primary air because the pulverized coal and air are injected into the furnace 11 of the pulverized coal burning boiler using the swirl combustion method and burned. A split material 24 that functions as a flame holding mechanism is provided at a primary port 22 of a coal that serves as a fuel flow path to be introduced into the furnace 11. One split material 24 is installed at the end of the flow path of the primary coal port 22 (near the outlet on the furnace 11 side) so as to horizontally traverse the center of the cross-sectional area of the flow path. In this case, the split member 24 has a cross-sectional shape in a horizontal direction obtained by rotating a substantially T shape by 90 degrees. Therefore, the pulverized coal that has been transported to the primary air through the primary port 22 of the coal is split up and down by the split member 24 at the center of the cross section of the flow path.
Note that the split member 24 is not limited to the illustrated substantially T-shaped cross section, and for example, the substantially Y-shaped cross section illustrated in FIG. 5A or the triangular cross section illustrated in FIG. A shape or the like may be adopted.

As a result, when the flow of pulverized coal passes through the split member 24, the flow is disturbed inside the flame formed in the furnace 11, and the density of the pulverized coal is formed.
In other words, in the downstream of the split member 24, shade is formed in the flow of pulverized coal. As for this density, in the two flows divided into the split members 24, the concentration of pulverized coal increases in a region near the center of the flow path cross section. In other words, the flow of the pulverized coal that has been split up and down through the split member 24 is formed with a dense region C having the highest pulverized coal concentration slightly above the center of the flow path cross section above the split member 24. The pulverized coal concentration gradually decreases upward from the concentrated region C. Similarly, a dense region C having the highest pulverized coal concentration is formed below the split member 24 and slightly below the center of the flow path cross section, and the pulverized coal concentration gradually decreases downward from the concentrated region C.

  Therefore, the split member 24 functions as a flame holding mechanism that ensures stable ignition of the pulverized coal, and suppresses the flame from spreading greatly. For this reason, the pulverized coal thrown into the flame ensures that the pulverized coal in the rich region C ignites stably. As a result, the pulverized coal is combusted inside the flame, and NOx generated by the combustion is generated inside the flame and quickly reduced.

Further, between the fuel burner 21 and the secondary air input port 30, the secondary air input from the secondary air input port 30 does not interfere with the flame formed from the fuel burner 21 into the furnace 11. The separation distance L is provided. This separation distance L is used to slow down the supply of secondary air introduced from the secondary air introduction port 30 to lower the oxygen concentration in the flame. In other words, the separation distance L is low temperature secondary air. Is a moderate distance that is difficult to reach the flame. That is, the separation distance L is a distance that can suppress mixing of the secondary air into the flame, and the height dimension h of the fuel burner 21 depends on various conditions such as the pressure at which the secondary air is introduced. About 1 h to 3 h are required on the basis of (see FIG. 1).
By providing such a separation distance L, the amount of secondary air mixed into the flame is reduced, so that the oxygen concentration in the flame is reduced, and the temperature of the flame is kept relatively low while minimizing the drop in the flame temperature. Can be maintained.

  Further, by providing the secondary air input port 30 with a separation distance L so that the secondary air does not interfere with the flame, the temperature drop (cooling) of the flame due to the low-temperature secondary air can be minimized. it can. For this reason, although the flame is in a state of air shortage, the flame is heated to a high temperature and continues stable ignition, so that combustion at a high temperature and a low oxygen concentration is possible. That is, the high-temperature oxygen remaining region formed on the outer periphery of the flame is suppressed, and combustion with significantly reduced NOx and unburned content becomes possible.

  By the way, the pulverized coal burner 21 of the burner 20 described above may be provided with the split members 24 in a plurality of directions as in the first modification shown in FIG. In the illustrated example, a total of five split members 24 are installed by two in the left and right (horizontal) direction and three in the up and down (vertical) direction. When a plurality of split members 24 are installed in the same direction, it is necessary to provide a predetermined interval between adjacent split members 24.

According to such an arrangement of the split member 24, the density of the pulverized coal is formed in the flame by the number of the split members 24, so that the flame holding function can be further improved. In addition, the multiple directions in this case are not limited to the combination of the left-right direction and the up-down direction mentioned above.
Further, the arrangement of the plurality of split members 24 may employ, for example, a configuration in which a plurality of split members 24 are arranged only in one direction in the left-right direction.

Further, in the pulverized coal burner 21 of the burner 20 described above, it is preferable that the split members 24 are concentratedly arranged at the center of the cross section of the flow path as in the second modification shown in FIG. That is, in the case where a plurality of lines are installed, it is desirable that they be arranged densely with respect to the central part of the channel cross section, rather than being uniformly arranged over the entire channel cross section.
By adopting such a concentrated arrangement, the concentration of pulverized coal and the turbulence of the flow can be concentrated in the center of the flame, so that the ignition of the center of the flame is further promoted and the distance from the secondary air Can be kept effective. That is, the separation distance L provided between the secondary air input port 30 and the secondary air formed by the separation distance L can be reliably ensured and used effectively.

  Further, in the pulverized coal burner 21 of the burner 20 described above, for example, as in the third modification shown in FIG. 8, the secondary air input port 30 </ b> A of the burner 20 </ b> A is directed outward in the vertical direction from the axial center of the pulverized coal burner 21. The installation may be inclined at an angle θ. In the configuration example shown in FIG. 8, the secondary air input port 30 shown in the first modified example of FIG. 6 is brought closer to the pulverized coal burner 21 side, and the secondary air input port 30 is moved outward in the vertical direction to an angle θ. Although it is inclined, the third modification can be applied to other embodiments and modifications in the same manner.

As described above, when the secondary air input port 30 </ b> A that is inclined outward in the vertical direction is employed, even if the installation position of the secondary air input port 30 </ b> A is close to the pulverized coal burner 21, the pulverized coal burner 21 enters the furnace 11. Since the secondary air that is input from the secondary air input port 30A does not interfere with the flame that is formed to face the burner, the burner height can be reduced. That is, since the secondary air input from the secondary air input port 30A flows in a direction away from the flame, when comparing with the same specifications, the maximum separation distance L1 shown in FIG. It becomes possible to set smaller than the distance L.
As a result, the burner 20A in which the secondary air input port 30A is disposed above and below the pulverized coal nozzle 21 can reduce the overall height of the burner 20A by reducing the separation distance L1.

  Moreover, in the 4th modification shown in FIG. 9, the rib 31 is provided in the inside of the flow path of 30 A of secondary air input ports inclined. That is, in the illustrated example, the rib 31 is provided inside the outlet of the secondary air input port 30A (the pulverized coal nozzle 21 side), and the flow of the secondary air is caused by colliding the flow of the secondary air with the rib 31. Changes have been made. In particular, the rib 31 provided inside the outlet of the secondary air input port 30A changes the flow of the secondary air in a direction away from the flame. Therefore, by appropriately adjusting the height of the rib 31 and the like, The mixing of the secondary air can be adjusted.

Further, the fifth modification shown in FIG. 10 is a case where the secondary air input port 30C includes the adjacent left outlet 30L and right outlet 30R, and the secondary air is input obliquely with respect to the flame. Thereby, mixing of secondary air and a flame can be delayed.
That is, in the fifth modification shown in FIG. 10 (a), the secondary air inlet port for injecting secondary air into the furnace 11 from the left outlet 30L and the right outlet 30R when the plan view branches in a Y shape. The left air outlet 30L and the right air outlet 30R that are inclined to the left and right direction from the axis of the pulverized coal burner 21 are disposed adjacent to each other, so the secondary air flows out in a direction away from the flame. Mixing is delayed.

  Also in such a secondary air input port 30C, as in the sixth modification shown in FIG. 11, for example, inside the left outlet 30L and the right outlet 30R (on the axial center side of the pulverized coal nozzle 21). Ribs 31 may be provided. By providing such a rib 31, the flow of secondary air collides with the rib 31 and changes the flow. Therefore, when the delay in mixing the secondary air is large, the height of the rib 31 is appropriately adjusted. Thus, the mixing of secondary air to the flame can be adjusted.

Further, in the seventh modification shown in FIG. 12, a plurality of swirl vanes 32 are provided in the flow path of the secondary air input port 30B. The secondary air input port 30 </ b> B in this case is formed in parallel with the axis of the pulverized coal burner 21. A swirl vane 32 is provided in the flow path of the secondary air input port 30B. The swirl vane 32 has, for example, an airfoil cross section, and can efficiently separate the secondary air flow from the flame.
By adopting such a configuration, it is possible to keep the burner height to a minimum and to separate the secondary air flow so as not to interfere with the flame.

  Thus, according to the coal fired boiler 10 of the above-described embodiment and each modified example, in the coal fired boiler that burns solid fuel such as pulverized coal, the high-temperature oxygen residual region H formed on the outer periphery of the flame is suppressed. The amount of NOx generated can be reduced. In other words, the pulverized coal (pulverized fuel) introduced from the pulverized coal burner 21 is formed with a shade in the center of the flame by the split member 24 serving as a flame holding mechanism, so that stable ignition can be ensured. . For this reason, pulverized fuel such as pulverized coal can be stably combusted inside the flame in a low oxygen concentration environment.

  Further, since the secondary air is slowly supplied from the secondary air input port 30 arranged so as not to interfere with the flame, the temperature drop (cooling) of the flame due to the low-temperature secondary air is minimized. be able to. For this reason, even in a flame in which the supply of secondary air is slow and air is insufficient, stable ignition can be continued while maintaining a high-temperature flame. Therefore, the coal fired boiler 10 of the present invention can burn pulverized fuel such as pulverized coal even in an environment of high temperature and low oxygen concentration, and combustion with significantly reduced NOx and unburned content is possible. become.

By the way, each embodiment and modification mentioned above can be combined suitably besides having been demonstrated based on illustration. In the above-described embodiment, the description has been given of the coal fired boiler 10 in which the region from the burner unit 12 to the AA 14 is used as the reducing atmosphere, but the present invention is not limited thereto.
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.

10 Coal-fired boiler 11 Furnace 12 Burner section 14 Additional air input section (AA section)
20, 20A Burner 21 Pulverized coal burner (fuel burner)
22 Cole primary port (fuel flow path)
23 Cole secondary port 24, 24A, 24B Split member 30, 30A, 30B, 30C Secondary air input port 31 Rib 32 Swivel blade

Claims (6)

Coal in which pulverized fuel and air are introduced into the furnace is a burner portion of a swirl combustion system that is disposed at each corner portion or wall surface portion of each step, and one or more swirl flames are formed at each step In a firewood boiler,
The burner includes a fuel burner for charging pulverized fuel and air, and a secondary air charging port disposed on the top and bottom or the left and right of the fuel burner and having a flow rate adjusting means,
Providing one or more split members at the front end of the flow path of the fuel burner;
A separation distance between the fuel burner and the secondary air input port is such that the secondary air input from the secondary air input port does not interfere with a flame formed from the fuel burner into the furnace. A coal fired boiler characterized by being provided.   The coal fired boiler according to claim 1, wherein the split member is provided in a plurality of directions.   The coal fired boiler according to claim 1 or 2, wherein the split members are concentratedly arranged at a central portion of a flow path cross section.   The coal fired boiler according to any one of claims 1 to 3, wherein the secondary air input port is installed so as to have an outward angle from an axial center of the fuel burner.   The coal fired boiler according to any one of claims 1 to 4, wherein a rib is provided inside a flow path of the secondary air input port. The coal fired boiler according to any one of claims 1 to 4, wherein swirl vanes are provided inside a flow path of the secondary air input port.

Images