JP2007309607A - Burner device for burning pulverized coal - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide self-burning property even with pulverized coal of low volatility coal. <P>SOLUTION: The burner device for pulverized coal is provided with a first jetting part 1 linearly or spirally jetting out primary combustion air A1 along with the pulverized coal B, and a second jetting part 2 jetting out secondary combustion air A2 so as to swirl around the primary combustion air A1 jetted out from the first jetting part 1. The pulverized coal B is ignited to form flame. A mixing suppressing means 31 is provided for suppressing mixing of the primary combustion air A1 and the secondary combustion air A2 before the pulverized coal B is ignited. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

  The present invention relates to a burner device for pulverized coal combustion.

For example, a pulverized coal combustion burner device used in a pulverized coal boiler or the like forms a low speed or reverse flow region at the center of the flame by swirling combustion air, thereby stabilizing the flame. Specifically, as combustion air, primary combustion air that is ejected in a linear or swirling flow and secondary combustion air that is ejected so as to swirl around the primary combustion air. Used, pulverized coal is ejected together with primary combustion air, and the pulverized coal is ignited to stably form a flame.
Chinese utility model application patent grant publication No. 2273373

By the way, in the burner device for pulverized coal combustion, bituminous coal is usually used as fuel, that is, pulverized coal. Then, such a volatile component of pulverized coal is ignited, and then the pulverized coal itself is ignited to form a flame.
However, in the conventional burner apparatus for pulverized coal combustion, when low volatile coals such as anthracite, semi-anthracite or oil coke are used as pulverized coal, it is difficult to perform self-sustained combustion. This is because low-volatile coal emits less volatile components than bituminous coal, and does not release volatile components at high temperatures, making it impossible to form a flammable mixture with sufficient concentration for ignition. This is due to poor ignitability and combustion stability.

  In addition, the fact that the volatile component is not released unless the temperature is high means that it takes time until the ignition is performed after the pulverized coal is ejected from the ejection port, so that the base of the flame is separated from the ejection port. In such a case, the secondary combustion air having a temperature lower than the furnace temperature of the boiler is mixed with the primary combustion air containing the pulverized coal, and the temperature of the pulverized coal is lowered and the pulverized powder is reduced. Charcoal concentration is diluted, combustion stability is further deteriorated, and misfire may occur.

  The present invention has been made in view of the above-described problems, and an object of the present invention is to provide a pulverized coal combustion burner device capable of self-combustion even with pulverized coal having low volatile content.

In order to achieve the above object, in the pulverized coal combustion burner apparatus of the present invention, as a first means, a first ejection part that ejects primary combustion air in a linear or swirling flow together with the pulverized coal; A pulverized coal that forms a flame by igniting the pulverized coal, comprising: a second ejection portion that ejects secondary combustion air so as to swirl around the primary combustion air ejected from one ejection portion The combustion burner device employs a configuration that includes mixing suppression means for suppressing mixing of the primary combustion air and the secondary combustion air before the pulverized coal is ignited.
According to the pulverized coal combustion burner device of the present invention employing such a configuration, the primary combustion air and the secondary combustion air are mixed by the mixing suppression means before the pulverized coal is ignited. Is deterred.

  As a second means, a configuration is adopted in which the high temperature gas in the flame is mixed with the primary combustion air before the pulverized coal is ignited in the first means.

  As a third means, in the second means, the chamber has a chamber disposed around the ejection port of the first ejection part, and the high-temperature gas is drawn into the chamber by generating a circulation flow. A configuration is adopted in which the high-temperature gas is mixed with the primary combustion air before the pulverized coal is ignited.

  As a fourth means, a configuration is adopted in which, in the third means, the cross-sectional diameter of the chamber is larger than the diameter of the ejection port of the first ejection part.

  As a fifth means, in the fourth means, a configuration is adopted in which the ejection port of the first ejection part is arranged eccentrically from the cross-sectional center of the chamber.

  According to the burner apparatus for pulverized coal combustion of the present invention, the pulverized coal is mixed with the primary combustion air before the pulverized coal is ignited to mix the pulverized coal with the volatile component emission temperature. Preheating as described above facilitates ignition. That is, the mixing suppression means can suppress a decrease in the concentration of pulverized coal caused by mixing the primary combustion air and the secondary combustion air before the pulverized coal is ignited. For this reason, ignitability and combustion stability are improved, and even pulverized coal with low volatile content can be self-combusted.

  Hereinafter, an embodiment of a burner device for pulverized coal combustion according to the present invention will be described with reference to the drawings.

(First embodiment)
FIG. 1 is a cross-sectional view schematically showing a schematic configuration of a pulverized coal combustion burner apparatus S1 of the present embodiment, and FIG. 2 schematically shows a schematic configuration of the pulverized coal combustion burner apparatus S1 of the present embodiment. FIG.
A plurality of burner apparatuses S1 for pulverized coal combustion of this embodiment are installed in a furnace of a pulverized coal boiler, for example. And as shown in FIG.1 and FIG.2, the burner apparatus S1 for pulverized coal combustion of this embodiment is the primary combustion air ejection part 1 (1st ejection part), and the secondary combustion air ejection part 2 ( (Second ejection part), a preparation chamber 3 (chamber), and a temperature adjusting air ejection part 4 are provided.

The primary combustion air ejection section 1 ejects the primary combustion air A1 in a straight line toward the furnace, and ejects pulverized coal B as fuel on the flow of the primary combustion air A1. Is. The jet port 11 of the primary combustion air jet part 1 is formed at a position eccentric with respect to the center of the preparation chamber 3 having a larger diameter than the jet port 11.
With such a configuration, the primary combustion air A1 and the pulverized coal B ejected from the primary combustion air ejection section 1 are ejected into the furnace through the preparation chamber 3.

  The preparation chamber 3 is connected to a temperature adjustment air ejection portion 4 for supplying temperature adjustment air A3 into the preparation chamber 3. By supplying the temperature adjusting air A3 from the temperature adjusting air ejection portion 4 into the preparation chamber 3, the temperature in the preparation chamber 3 is prevented from being overheated.

  The preparation chamber 3 is a room for heating the pulverized coal B ejected together with the primary combustion air A1 from the ejection port 11 of the primary combustion air ejection section 1 to a temperature at which ignition is possible. 1 is configured as a room having such a length that the pulverized coal supplied from the right side in FIG. 1 is heated to a temperature capable of being ignited before being discharged from the left side.

  The secondary combustion air ejection section 2 is for supplying the secondary combustion air A2 to the flame formed by the pulverized coal combustion burner device S1 of the present embodiment, as shown in FIG. A jet port 21 formed along the circumference surrounding the jet port 11 of the primary combustion air jet unit 1, the preparation chamber 3 and the jet port 41 of the temperature adjusting air jet unit 4 is provided. In addition, a plurality of fins 22 are disposed in the back of the ejection port 21, and the secondary combustion air A <b> 2 ejected from the secondary combustion air ejection part 2 by the fins 22 is swirled. Further, the fin 22 is rotatably supported by a shaft 23 extending in the radial direction of the preparation chamber 3. And the intensity | strength of a turning flow can be changed by changing the rotation amount (angle) of the fin 22 as shown in FIG.

  As shown in FIG. 1, in the pulverized coal combustion burner apparatus S <b> 1 of the present embodiment, a partition that separates the space in the preparation chamber 3 and the flow path of the secondary combustion air ejection section 2, that is, the preparation chamber. The third wall 31 functions as a mixing deterring means for preventing the primary combustion air and the secondary combustion air from being mixed before the pulverized coal is ignited.

  Next, operation | movement of the burner apparatus S1 for pulverized coal combustion of this embodiment comprised in this way is demonstrated.

  First, when the primary combustion air A1 and the pulverized coal B are ejected from the primary combustion air ejection part 1 through the ejection port 11, the ejected primary combustion air A1 and the pulverized coal B are prepared. The chamber 3 moves from the right side to the left side in FIG. Here, in the burner device S1 for pulverized coal combustion of the present embodiment, the ejection port 11 of the primary combustion air ejection part 1 is formed at a position eccentric with respect to the center of the preparation chamber 3. For this reason, when the primary combustion air A1 ejected from the ejection port 11 flows linearly, the primary combustion air A1 circulates between the primary combustion air A1 and the wall portion 31 of the preparation chamber 3 as shown in FIG. A stream R is formed.

Then, by forming such a circulation flow R, the high-temperature gas inside the flame flows into the preparation chamber 3 and is mixed with the primary combustion air A1, so that the inside of the preparation chamber 3 and the primary combustion are performed. The working air A1 is heated. Accordingly, it is possible to raise the temperature of the preparation chamber 3 and the primary combustion air A1 without installing a heating device such as a heater and to heat the pulverized coal B to a temperature at which ignition is possible.
When the temperature in the preparation chamber 3 is overheated, the temperature adjustment air A3 is supplied into the preparation chamber 3 through the outlet 41 from the temperature adjustment air ejection section 4, thereby preparing the preparation chamber 3. It is possible to prevent overheating inside.

  In this way, a sufficient amount of volatile components are released from the pulverized coal B heated to a temperature capable of being ignited in the preparation chamber 3. For this reason, the pulverized coal B discharged from the preparation chamber 3 is immediately ignited.

  Here, in the burner device S1 for pulverized coal combustion of the present embodiment, when the pulverized coal B is discharged from the preparation chamber 3 by the wall portion 31 (mixing suppression means) of the preparation chamber 3, that is, the pulverized coal B is ignited. Until this is done, mixing of the primary combustion air A1 and the secondary combustion air A2 is suppressed. Therefore, the temperature fall of pulverized coal B before ignition can be suppressed. For this reason, combustion stability is improved, and even if it is a pulverized coal of a low volatile coal, it becomes possible to carry out self-sustained combustion.

  After that, the secondary combustion air A2 swirling from the secondary combustion air ejection section 2 is supplied to the flame ignited by the pulverized coal B, whereby the flame is stably formed.

  According to the burner device S1 for pulverized coal combustion of this embodiment as described above, the temperature decrease of the pulverized coal B before ignition can be suppressed, and the ignitability and the combustion stability are improved and reduced. Even volatile coal pulverized coal can be self-sustained.

In the pulverized coal combustion burner apparatus S1 of the present embodiment, the high-temperature gas in the flame is mixed with the primary combustion air A1 before the pulverized coal B is ignited. This makes it possible to heat the pulverized coal B without using an external device such as a heater.
Moreover, when the pulverized coal B is heated by mixing the high temperature gas in the flame with the primary combustion air A1, the pulverized coal B is rapidly pyrolyzed, and more volatile components are generated from the pulverized coal B. As it is released, many nitrogen components are also released. And it becomes possible to form a strong reduction | restoration area | region with a flame, and produced | generated NOx is reduce | _restored . Therefore, it is possible to achieve a low NO _X reduction.

  Furthermore, since the jet outlet 11 of the primary combustion air jet section 1 is formed at a position eccentric with respect to the center of the preparation chamber 3, a circulation flow R that draws high temperature gas into the preparation chamber 3 is easily formed. can do.

In order to efficiently draw the high temperature gas inside the flame into the preparation chamber 3, it is preferable that the circulation flow R is applied to a region where the high temperature gas circulates inside the flame. As a result, the hot gas can easily flow into the circulation flow R, so that the hot gas can be efficiently drawn into the preparation chamber 3.
Depending on the swirling state of the secondary combustion air A2, the circulation flow R can be applied to the region where the exchange gas circulates.

(Second Embodiment)
Next, a second embodiment of the present invention will be described. In the description of the second embodiment, the description of the same parts as in the first embodiment will be omitted or simplified.

FIG. 3 is a cross-sectional view schematically showing a schematic configuration of the pulverized coal combustion burner device S2 of the present embodiment.
As shown in this figure, in the pulverized coal combustion burner device S2 of the present embodiment, the diameter of the preparation chamber 3 is made sufficiently larger than the outlet 11 of the primary combustion air jetting section 1, and A spout 11 is formed in alignment with the center of the preparation chamber 3.

In the pulverized coal combustion burner apparatus S2 of this embodiment having such a configuration, since the diameter of the preparation chamber 3 is sufficiently larger than the outlet 11, the formation position of the outlet 11 is set as the preparation chamber 3. It is possible to form the circulation flow R as shown in FIG.
Therefore, in the pulverized coal combustion burner apparatus S2 of the present embodiment, similarly to the pulverized coal combustion burner apparatus S1 of the first embodiment, a temperature decrease of the pulverized coal B before ignition can be suppressed, and the ignition is performed. And combustion stability are improved, and even pulverized coal with low volatile content can be self-combusted.

  In the pulverized coal combustion burner device S2 of the present embodiment, when the temperature adjustment air A3 is supplied into the preparation chamber 3, the injection of the wall portion 31 of the preparation chamber 3 and the primary combustion air ejection portion 1 is performed. What is necessary is just to form the jet outlet of the air jet part for temperature adjustment between the outlets 11.

  As mentioned above, although preferred embodiment of the burner apparatus for pulverized coal combustion concerning this invention was described referring an accompanying drawing, it cannot be overemphasized that this invention is not limited to the said embodiment. Various shapes, combinations, and the like of the constituent members shown in the above-described embodiments are examples, and various modifications can be made based on design requirements and the like without departing from the gist of the present invention.

  For example, a part of the primary combustion air A1 or a part of the secondary combustion air A2 may be used as the temperature adjustment air A3 of the above embodiment. In this case, a part of the flow path of the primary combustion air A1 or a part of the flow path of the secondary combustion air A2 is branched, and one part of the primary combustion air A1 flowing into the branched flow path. Or a part of the secondary combustion air A2 may be ejected from the ejection port 41 of the temperature adjusting air ejection portion 4.

  Moreover, in the said embodiment, primary combustion air A1 was ejected linearly from the primary combustion air ejection part 1 toward the inside of a furnace. However, the present invention is not limited to this, and the primary combustion air A1 may be ejected in a swirling flow toward the furnace.

It is sectional drawing which showed typically schematic structure of the burner apparatus for pulverized coal combustion which is 1st Embodiment of this invention. It is the front which showed typically the schematic structure of the burner apparatus for pulverized coal combustion which is 1st Embodiment of this invention. It is sectional drawing which showed typically schematic structure of the burner apparatus for pulverized coal combustion which is 2nd Embodiment of this invention.

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 ... Primary combustion air ejection part 11 ... Outlet 2 ... Secondary combustion air ejection part 21 ... Outlet 22 ... Fin 3 ... Preparation chamber (chamber)
31 …… Wall (mixing suppression means)
4 ... Air outlet for temperature adjustment 41 ... Outlet S1, S2 ... Burner device for pulverized coal combustion A1 ... Air for primary combustion A2 ... Air for secondary combustion A3 ... Air for temperature adjustment B ... ... Pulverized coal R ... Circulating flow

Claims (5)

The primary combustion air is jetted together with the pulverized coal in a straight line or swirl flow, and the secondary combustion is swirled around the primary combustion air ejected from the first jet part. A burner device for burning pulverized coal, comprising a second jetting portion for jetting air, and forming a flame by igniting the pulverized coal,
A pulverized coal combustion burner apparatus comprising mixing suppression means for suppressing mixing of the primary combustion air and the secondary combustion air before the pulverized coal is ignited. The burner device for pulverized coal combustion according to claim 1, wherein the high-temperature gas in the flame is mixed with the primary combustion air before the pulverized coal is ignited. The chamber has a chamber disposed around the ejection port of the first ejection part, and the hot gas is drawn into the chamber by generating a circulating flow before the pulverized coal is ignited. The burner device for pulverized coal combustion according to claim 2, wherein the burner device is mixed with the primary combustion air. The burner device for pulverized coal combustion according to claim 3, wherein a cross-sectional diameter of the chamber is larger than a diameter of the ejection port of the first ejection part. The burner device for pulverized coal combustion according to claim 4, wherein the jet outlet of the first jet part is arranged eccentrically from the cross-sectional center of the chamber.

Images