JP6628490B2 - Combustion device and method for preventing dust generation in combustion device - Google Patents

Combustion device and method for preventing dust generation in combustion device Download PDF

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JP6628490B2
JP6628490B2 JP2015080756A JP2015080756A JP6628490B2 JP 6628490 B2 JP6628490 B2 JP 6628490B2 JP 2015080756 A JP2015080756 A JP 2015080756A JP 2015080756 A JP2015080756 A JP 2015080756A JP 6628490 B2 JP6628490 B2 JP 6628490B2
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岩佐 直樹
直樹 岩佐
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Mitsubishi Power Ltd
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Description

本開示は、石炭をボイラで燃焼させた際に発生する粉塵がボイラ内に設けられた熱交換器やボイラ内壁に付着するのを防止可能な燃焼装置及び燃焼装置の粉塵発生防止方法に関する。   The present disclosure relates to a combustion device capable of preventing dust generated when coal is burned in a boiler from adhering to a heat exchanger provided in the boiler or an inner wall of the boiler, and a dust generation prevention method for the combustion device.

近年、石油価格の上昇に伴い、埋蔵量の豊富さや経済性の面から石炭火力が再び見直されてきている。しかしながら、火力発電の燃料としての石炭は性状が個体であり、また石炭焚ボイラ内での燃焼により粉塵が発生し、この粉塵がボイラに設けられた熱交換器の伝熱面に衝突したり付着すると、伝熱面が損傷したり熱の吸収が困難になる虞が生じる。   In recent years, with the rise in oil prices, coal-fired thermal power has been reviewed again from the viewpoint of abundant reserves and economic efficiency. However, coal as a fuel for thermal power generation is solid in nature, and the combustion in the coal-fired boiler generates dust, which collides with or adheres to the heat transfer surface of the heat exchanger installed in the boiler. Then, there is a possibility that the heat transfer surface may be damaged or heat absorption may be difficult.

一方、特許文献1には、ボイラ内での石炭の燃焼により生じる粉塵(灰)に対して、ボイラ外から発生させたイオンをボイラ内に注入して粉塵とイオンの反応から粉塵に電荷を生じさせるとともに、熱交換の伝熱面にも同種の電荷を生じさせて、双方に作用する静電的な反発力を利用して伝熱面への粉塵の付着を防止する灰付着防止方法が提案されている。   On the other hand, in Patent Document 1, ions generated from outside the boiler are injected into the boiler with respect to dust (ash) generated by the combustion of coal in the boiler, and charge is generated in the dust from the reaction between the dust and the ions. In addition, a method of preventing ash adhesion is proposed, in which the same kind of charge is generated on the heat transfer surface of heat exchange, and the electrostatic repulsion acting on both surfaces is used to prevent dust from adhering to the heat transfer surface. Have been.

昭和63−204013Showa 63-202013

この特許文献1に記載の灰付着防止方法は、粉砕された石炭の微粉炭をボイラに供給するための流路に放電電極を設け、この放電電極から発生する帯電用イオンをボイラに注入して、ボイラ内での微粉炭の燃焼によって生じた粉塵(灰)に帯電用イオンを付着して粉塵を帯電させる。しかしながら、発生する粉塵はボイラ内を熱交換器側へ向かって流動しているので、注入された帯電用イオンがすべての粉塵(灰)に付着して帯電させるのは困難である。したがって、粉塵(灰)が伝熱面に衝突したり付着する場合があり、伝熱面が損傷し、また熱の吸収が困難になる等の問題が生じる虞がある。   In the method for preventing ash deposition described in Patent Document 1, a discharge electrode is provided in a flow path for supplying pulverized coal pulverized coal to a boiler, and charging ions generated from the discharge electrode are injected into the boiler. Then, charging ions are attached to the dust (ash) generated by the combustion of the pulverized coal in the boiler to charge the dust. However, since the generated dust flows in the boiler toward the heat exchanger, it is difficult for the injected charging ions to adhere to all the dust (ash) and charge. Therefore, dust (ash) may collide with or adhere to the heat transfer surface, causing a problem that the heat transfer surface is damaged and that heat absorption becomes difficult.

上述の事情に鑑みて、本発明の少なくとも幾つかの実施形態は、石炭を燃料とする燃料装置において、ボイラ内での石炭の燃焼時に発生する粉塵が熱交換器の伝熱面に衝突したり付着したりする虞のない燃焼装置及び燃焼装置の粉塵発生防止方法を提供することを目的とする。   In view of the above circumstances, at least some embodiments of the present invention relate to a fuel device using coal as fuel, and dust generated when burning coal in a boiler collides with a heat transfer surface of a heat exchanger. An object of the present invention is to provide a combustion device and a method for preventing generation of dust in the combustion device, which are not likely to adhere.

本発明の幾つかの実施形態に係わる燃焼装置は、
石炭を粉砕する粉砕装置と、
前記粉砕装置によって粉砕された前記石炭の微紛炭を供給するための燃料供給装置と、
前記燃料供給装置から供給される前記微粉炭を燃焼させ内部に熱交換器が設けられているボイラと、を備える燃焼装置であって、
前記燃料供給装置は、
前記粉砕装置によって粉砕された前記石炭の前記微紛炭から、所定粒径以下の微紛炭を分級する分級手段と、
前記分級手段により分離された所定粒径以下の前記微紛炭のうち、マイナスに帯電している前記微粉炭を分別除去する分別除去手段と、を有するように構成される。
The combustion device according to some embodiments of the present invention includes:
A crushing device for crushing coal,
A fuel supply device for supplying the pulverized coal of the coal pulverized by the pulverization device,
A boiler in which a heat exchanger is provided for burning the pulverized coal supplied from the fuel supply device,
The fuel supply device,
From the pulverized coal of the coal pulverized by the pulverizer, classification means for classifying pulverized coal having a predetermined particle size or less,
And separating and removing the negatively charged pulverized coal from the pulverized coal having a predetermined particle size or less separated by the classification means.

上記燃焼装置によれば、粉砕装置によって石炭が粉砕されると、石炭は炭素(c)とその他の成分(例えば、二酸化ケイ素、酸化アルミニウム等)の微粉体に分離される。そして、分離された炭素の微粉炭とその他の成分の微粉炭は粉砕時における撹拌等によって摩擦帯電して、炭素はプラス(+)に帯電し、その他の成分の微粉炭はマイナス(−)に帯電する性質を有する。粉砕装置によって粉砕された微紛炭は分級手段によって所定粒径以下の微紛炭に分級される。そして、分別除去手段によって、分級手段で分級された微紛炭のうちマイナスに帯電している微粉炭を分別除去する。このため、ボイラには、プラスに帯電した微粉炭が供給されるので、ボイラに供給される微紛体には炭素成分が多く含まれる。したがって、ボイラでの微紛炭の燃焼時における粉塵の発生を抑制することができ、粉塵が熱交換器に衝突したり付着したりする虞を抑制することができる。よって、ボイラ内での石炭の燃焼時に発生する粉塵が熱交換器の伝熱面に衝突したり付着したりする虞のない燃焼装置を実現できる。   According to the combustion apparatus, when the coal is pulverized by the pulverizer, the coal is separated into fine powder of carbon (c) and other components (for example, silicon dioxide, aluminum oxide, and the like). Then, the pulverized coal of the separated carbon and the pulverized coal of the other components are frictionally charged by stirring or the like at the time of pulverization, the carbon is charged to a plus (+), and the pulverized coal of the other components is set to a minus (-). It has the property of being charged. The pulverized coal pulverized by the pulverizer is classified into pulverized coal having a predetermined particle size or less by a classification means. Then, the pulverized coal that is negatively charged among the pulverized coal classified by the classification means is separated and removed by the separation and removal means. For this reason, since the pulverized coal charged positively is supplied to the boiler, the fine powder supplied to the boiler contains a large amount of carbon components. Therefore, it is possible to suppress the generation of dust when the fine coal is burned in the boiler, and it is possible to suppress the possibility that the dust collides with or adheres to the heat exchanger. Therefore, it is possible to realize a combustion device in which dust generated when burning coal in the boiler does not collide with or adhere to the heat transfer surface of the heat exchanger.

また、幾つかの実施形態では、
前記分別除去手段は、プラスの電荷を生じさせて、前記マイナスに帯電している前記微粉炭を静電的に付着させる付着部材を有するように構成される。
Also, in some embodiments,
The separation and removal unit is configured to have an attachment member that generates a positive charge and electrostatically attaches the negatively charged pulverized coal.

この場合、分別除去手段は、プラスの電荷を生じさせて、マイナスに帯電している微粉炭を静電的に付着させる付着部材を有するので、マイナスに帯電している微粉炭を効果的に付着部材に付着させることができる。したがって、分別除去手段からボイラ内に供給される微粉炭に含有するマイナスに帯電している微粉炭の割合を少なくすることができる。よって、ボイラ内に供給される微粉炭の燃焼時に発生する粉塵の発生量を確実に少なくすることができる。   In this case, the separation / removal means has an attaching member that generates a positive charge and electrostatically attaches the negatively charged pulverized coal, so that the negatively charged pulverized coal is effectively attached. It can be attached to a member. Therefore, the ratio of the negatively charged pulverized coal contained in the pulverized coal supplied into the boiler from the separation and removal means can be reduced. Therefore, the amount of dust generated during the combustion of the pulverized coal supplied into the boiler can be reliably reduced.

また、幾つかの実施形態では、
前記分級手段は、前記粉砕装置によって粉砕された石炭の微紛炭のうち所定粒径以下の微紛体のみを通過可能な孔部を有したフィルタと、該フィルタを通過できない微粉炭を前記粉砕装置に戻して再粉砕させるための戻し流路を備えているように構成される。
Also, in some embodiments,
The classifying means includes a filter having a hole portion capable of passing only fine powder having a predetermined particle size or less among fine coals of coal pulverized by the pulverizer, and a pulverizer that pulverizes coal that cannot pass through the filter. It is configured to have a return flow path for returning the powder to re-grinding.

この場合、分級手段には、フィルタを通過できない微粉炭を粉砕装置に戻して再粉砕させるための戻し流路を備えているので、粒径の比較的に大きな石炭は粉砕装置に戻されて再粉砕される。したがって、粉砕される石炭を確実に粒径の小さい微粉炭にすることができ、ボイラ内での微粉炭の燃焼をより向上させることができる。   In this case, the classification means is provided with a return flow path for returning the pulverized coal that cannot pass through the filter to the pulverizing device and re-pulverizing the coal. Crushed. Therefore, the pulverized coal can be reliably turned into pulverized coal having a small particle size, and the combustion of the pulverized coal in the boiler can be further improved.

また、幾つかの実施形態では、
前記ボイラには、プラスの電荷を前記ボイラ壁に印加可能な電荷供給手段が設けられているように構成される。
Also, in some embodiments,
The boiler is configured to be provided with a charge supply unit capable of applying a positive charge to the boiler wall.

この場合、ボイラには、プラスの電荷をボイラ壁に印加可能な電荷供給手段が設けられているので、ボイラ内に供給されるプラスに帯電した微粉炭は、静電的な反発力によってボイラ壁に付着する虞を防止することができる。よって、ボイラ内に供給されたプラスに帯電した微粉炭の燃焼をより向上させることができる。   In this case, since the boiler is provided with charge supply means capable of applying a positive charge to the boiler wall, the positively charged pulverized coal supplied into the boiler is charged by the electrostatic repulsion force. Can be prevented. Therefore, the combustion of the positively charged pulverized coal supplied into the boiler can be further improved.

本発明の幾つかの実施形態に係わる燃焼装置の粉塵発生防止方法は、
燃料となる石炭を粉砕させて帯電させた微紛炭を生成し、
前記微粉炭を所定粒径以下に分級し、
分級された所定粒径以下の微紛炭のうちマイナスに帯電している微粉炭を分別して除去し、
前記マイナスに帯電した微粉炭を分別除去して残されたプラスに帯電した微粉炭を燃焼装置のボイラに供給して、該ボイラ内で前記プラスに帯電した微粉炭を燃焼させる。
A method for preventing dust generation of a combustion device according to some embodiments of the present invention includes:
Pulverizing coal as fuel to produce charged fine pulverized coal,
Classifying the pulverized coal to a predetermined particle size or less,
Negatively charged pulverized coal among the pulverized coal having a predetermined particle size or less is separated and removed,
The positively charged pulverized coal is separated and removed, and the positively charged pulverized coal remaining is supplied to a boiler of a combustion device to burn the positively charged pulverized coal in the boiler.

上記燃焼装置の粉塵発生防止方法によれば、石炭を粉砕すると、石炭は炭素(c)とその他の成分(例えば、二酸化ケイ素、酸化アルミニウム等)の微粉体に分離される。そして、分離された炭素の微粉炭とその他の成分の微粉炭は粉砕時における撹拌等によって摩擦帯電して、炭素はプラス(+)に帯電し、その他の成分の微粉炭はマイナス(−)に帯電する性質を有する。粉砕された微紛炭は所定粒径以下の微紛炭に分級され、この分級された微紛炭のうちマイナスに帯電している微粉炭が分別除去される。このため、ボイラには、プラスに帯電した微粉炭を多く含んだ微粉炭が供給されることになり、ボイラでの微紛炭の燃焼時における粉塵の発生を抑制することができ、粉塵が熱交換器に衝突したり付着したりする虞を抑制することができる。よって、ボイラ内での石炭の燃焼時に発生する粉塵が熱交換器の伝熱面に衝突したり付着したりする虞のない燃焼装置の粉塵発生防止方法を実現できる。   According to the dust generation preventing method of the combustion apparatus, when the coal is pulverized, the coal is separated into fine powder of carbon (c) and other components (for example, silicon dioxide, aluminum oxide, and the like). Then, the pulverized coal of the separated carbon and the pulverized coal of the other components are frictionally charged by stirring or the like at the time of pulverization, the carbon is charged to a plus (+), and the pulverized coal of the other components is set to a minus (-). It has the property of being charged. The pulverized pulverized coal is classified into pulverized coal having a predetermined particle size or less, and of the classified pulverized coal, negatively charged pulverized coal is separated and removed. As a result, pulverized coal containing a large amount of pulverized coal that is positively charged is supplied to the boiler, and the generation of dust during the combustion of the pulverized coal in the boiler can be suppressed, and the dust is not heated. The possibility of colliding with or adhering to the exchanger can be suppressed. Therefore, it is possible to realize a method of preventing generation of dust in a combustion device in which dust generated when burning coal in the boiler does not collide with or adhere to the heat transfer surface of the heat exchanger.

本発明の少なくとも幾つかの実施形態によれば、石炭を燃料とする燃料装置において、ボイラ内での石炭の燃焼時に発生する粉塵が熱交換器の伝熱面に衝突したり付着したりする虞のない燃焼装置及び燃焼装置の粉塵発生防止方法を提供することができる。   According to at least some embodiments of the present invention, in a fuel device using coal as fuel, there is a possibility that dust generated when burning coal in a boiler collides with or adheres to a heat transfer surface of a heat exchanger. And a method for preventing generation of dust in a combustion device.

本発明の一実施形態に係わる燃焼装置の概略構成図である。It is a schematic structure figure of a combustion device concerning one embodiment of the present invention. 燃焼装置の分級装置及び分別除去装置の概略構成図である。It is a schematic structure figure of a classification device and a separation removal device of a combustion device. 分別除去装置の作動原理を説明するための説明図である。It is explanatory drawing for demonstrating the operation principle of a separation removal apparatus. 石炭がボイラに供給されるまでの流れを説明するための説明図である。It is explanatory drawing for demonstrating the flow until coal is supplied to a boiler.

以下、添付図面に従って本発明の燃焼装置及び燃焼装置の粉塵発生防止方法の実施形態について、図1〜図4を参照しながら説明する。なお、この実施形態に記載されている構成部品の材質、形状、その相対的配置等は、本発明の範囲をこれに限定する趣旨ではなく、単なる説明例にすぎない。   Hereinafter, an embodiment of a combustion device and a method of preventing generation of dust in a combustion device according to the present invention will be described with reference to FIGS. Note that the materials, shapes, relative arrangements, and the like of the components described in this embodiment are not intended to limit the scope of the present invention, but are merely illustrative examples.

まず、本発明の実施形態である燃焼装置の粉塵発生防止方法を説明する前に、燃焼装置について説明する。燃焼装置1は、図1(説明図)に示すように、粉砕装置40と燃料供給装置37とボイラ10とを有してなる。   First, before describing a method for preventing generation of dust in a combustion apparatus according to an embodiment of the present invention, the combustion apparatus will be described. The combustion device 1 includes a crushing device 40, a fuel supply device 37, and the boiler 10, as shown in FIG.

粉砕装置40は、石炭を粉砕して粒径の小さい微粉炭を生成する。粉砕装置40は複数のブレード42を備えて回転可能な回転刃41を備える。この回転刃41の回転によって、石炭は粒径の小さい微粉炭に粉砕されるとともに、粉砕された微粉炭同士の接触によって微粉炭が摩擦帯電する。ここで、粉砕装置40によって石炭が粉砕されると、石炭は炭素(c)とその他の成分(例えば、二酸化ケイ素、酸化アルミニウム等)の微粉体に分離される。そして、分離された炭素の微粉炭とその他の成分の微粉炭は、粉砕時における撹拌等によって摩擦帯電して、炭素はプラス(+)に帯電し、その他の成分はマイナス(−)に帯電する性質を有する。本実施形態の燃焼装置1は、このような石炭の帯電に関する性質を利用したものである。   The pulverizing device 40 pulverizes the coal to generate pulverized coal having a small particle size. The pulverizing device 40 includes a rotary blade 41 having a plurality of blades 42 and rotatable. By the rotation of the rotary blade 41, the coal is pulverized into pulverized coal having a small particle size, and the pulverized coal is frictionally charged due to contact between the pulverized pulverized coal. Here, when the coal is pulverized by the pulverizer 40, the coal is separated into fine powder of carbon (c) and other components (for example, silicon dioxide, aluminum oxide, etc.). Then, the pulverized coal of the separated carbon and the pulverized coal of the other components are frictionally charged by stirring or the like at the time of pulverization, so that the carbon is positively (+) charged and the other components are negatively (-) charged. Has properties. The combustion device 1 of the present embodiment utilizes such a property relating to the charging of coal.

燃料供給装置37は、分級装置3及び分別除去装置20を有してなる。分級装置30及び分別除去装置20は、図1及び図2に示すように、互いに隣接して配設されている。分級装置30は、内部が中空な箱状に形成された分級本体部31を備える。分級本体部31内には、粉砕装置40によって粉砕された石炭の微紛炭のうち所定粒径以下の微紛体のみを通過可能な孔部を有したフィルタ33が設けられている。フィルタ33を透過した微粉炭は分別除去装置20に送られ、フィルタ33を透過できない石炭は、分級本体部31の底部に一端が接続されて他端が粉砕装置40に連通する戻し流路35を介して粉砕装置40に戻されて再粉砕される。なお、石炭は、その粒径が比較的に大きいと、燃焼性が悪くなる。このため、粉砕装置40を用いて石炭を微細化した微粉炭にする。   The fuel supply device 37 includes the classification device 3 and the separation and removal device 20. As shown in FIGS. 1 and 2, the classification device 30 and the separation and removal device 20 are disposed adjacent to each other. The classification device 30 includes a classification main body 31 having a hollow box shape inside. A filter 33 having a hole through which only fine powder having a predetermined particle size or less among fine coals of coal pulverized by the pulverizer 40 is provided in the classification main body 31. The pulverized coal that has passed through the filter 33 is sent to the separation / removal device 20, and the coal that cannot pass through the filter 33 passes through the return channel 35, one end of which is connected to the bottom of the classification main body 31 and the other end of which communicates with the crusher 40. It is returned to the crushing device 40 through the crushing device 40 and crushed again. In addition, if the particle size of coal is relatively large, flammability deteriorates. For this reason, the pulverized coal is pulverized by using the pulverizing device 40.

分別除去装置20は、内部が中空な箱状に形成された分別除去本体部21を備える。分別除去本体部21内には、図3に示すように、横方向に並んで上下方向に延びる一対の極板23が設けられている。これらの極板23は金属材料製であり、電源25に電気的に接続されている。これらの極板23には、電源25によってプラスの電荷(電位)が印加されている。また、これらの極板23間には、分級装置30によって分級された微紛炭が通流可能な空間部23aが形成されている。   The separation and removal apparatus 20 includes a separation and removal main body 21 having a hollow box shape inside. As shown in FIG. 3, a pair of pole plates 23 arranged in the horizontal direction and extending in the vertical direction are provided in the separation removal main body 21. These electrode plates 23 are made of a metal material, and are electrically connected to a power supply 25. A positive charge (potential) is applied to these electrode plates 23 by a power supply 25. A space 23a through which fine coal classified by the classifier 30 can flow is formed between the electrode plates 23.

この空間部23aを通過する微粉炭50は、前述したようにプラス(+)に帯電した炭素の微粉炭50aと、マイナス(−)に帯電した微粉炭50bである。これらの微粉炭50のうちマイナス(−)に帯電した微粉炭50bは、プラスの電荷(電位)を有する極板23に静電的に吸引されて極板23に付着する。このため、一対の極板23間を通過する際に、一対の極板23によってマイナス(−)に帯電した微粉炭50bが分別されて除去され、プラス(+)に帯電した炭素の微粉炭50aが空間部23aを通過する。なお、電源25は、微粉炭50の流量等に応じてプラスの電荷(電位)を変更可能なものや、電荷(電位)を一定にするようなものでもよい。   The pulverized coal 50 passing through the space 23a is the pulverized coal 50a of carbon charged positively (+) and the pulverized coal 50b charged negatively (-) as described above. Of these pulverized coals 50, the pulverized coal 50b charged negatively (-) is electrostatically attracted to the electrode plate 23 having a positive charge (potential) and adheres to the electrode plate 23. For this reason, when passing between the pair of electrode plates 23, the pulverized coal 50b charged negatively (−) by the pair of electrode plates 23 is separated and removed, and the pulverized coal 50a of carbon charged positively (+) is removed. Pass through the space 23a. In addition, the power supply 25 may be capable of changing the positive charge (potential) according to the flow rate of the pulverized coal 50 or the like, or may be capable of keeping the charge (potential) constant.

分別除去装置20には、分級装置30から送られた微紛炭50の流通の際等に、微粉炭同士が結合して粒径が大きくなった場合に、結合した微粉炭を粉砕装置40に戻して再粉砕させるための戻し流路26(図1参照)が設けられている。また、分別除去装置20は2次風路14を介してボイラ10に連通している。   When the pulverized coal is combined with each other to increase the particle size when the pulverized coal 50 sent from the classification device 30 is distributed, the separated pulverized coal is sent to the pulverizing device 40. A return channel 26 (see FIG. 1) for returning and re-grinding is provided. In addition, the separation and removal device 20 communicates with the boiler 10 via the secondary air passage 14.

ボイラ10は、図1に示すように、ボイラ10の幅方向一方側にバーナ11を備えるウィンドウボックス12を有して、2次風路14を介して燃料となる微粉炭50aをボイラ炉15内に流入させてバーナ11で燃焼させる。ボイラ炉15の上部には、燃焼排ガスを排出するための排ガス通路16が設けられ、またボイラ炉15内の上部には熱交換器17が設けられている。この熱交換器17は、熱媒(例えば、水)を流すためのボイラ管17aを備えている。本実施形態の熱交換器17は、図示しない発電機を駆動させるためのタービンに供給する蒸気を生成する。   As shown in FIG. 1, the boiler 10 has a window box 12 provided with a burner 11 on one side in the width direction of the boiler 10, and pulverized coal 50 a serving as fuel through a secondary air passage 14 is placed in a boiler furnace 15. And burned by the burner 11. An exhaust gas passage 16 for discharging combustion exhaust gas is provided in an upper portion of the boiler furnace 15, and a heat exchanger 17 is provided in an upper portion of the boiler furnace 15. The heat exchanger 17 includes a boiler tube 17a for flowing a heat medium (for example, water). The heat exchanger 17 of the present embodiment generates steam to be supplied to a turbine for driving a generator (not shown).

次に、本発明の実施形態である燃焼装置の粉塵発生防止方法について、図1及び図4を参照しながら説明する。先ず、図4に示すように、石炭を粉砕装置40に投入し、粉砕装置40によって石炭を粉砕する。石炭の粉砕時に、石炭は炭素(c)とその他の成分(例えば、二酸化ケイ素、酸化アルミニウム等)の微粉炭に分離される。そして、分離された炭素の微粉炭とその他の成分の微粉炭は粉砕時における撹拌等によって摩擦帯電して、炭素はプラス(+)の微粉炭50aに帯電し、その他の成分はマイナス(−)の微粉炭50bに帯電する。   Next, a method for preventing generation of dust in a combustion device according to an embodiment of the present invention will be described with reference to FIGS. First, as shown in FIG. 4, coal is charged into a pulverizing device 40, and the coal is pulverized by the pulverizing device 40. During the comminution of the coal, the coal is separated into pulverized coal of carbon (c) and other components (eg, silicon dioxide, aluminum oxide, etc.). Then, the pulverized coal of the separated carbon and the pulverized coal of the other components are frictionally charged by stirring or the like at the time of pulverization, and the carbon is charged to the pulverized coal 50a of plus (+), and the other components are minus (-). Of the pulverized coal 50b.

粉砕装置40により生成された微紛炭50は、燃料供給装置37の一部である分級装置30によって所定粒径以下の微紛炭に分級される。所定粒径を超える石炭は、戻し流路35を介して粉砕装置40に戻されて再粉砕される。所定粒径以下の微紛炭50は燃料供給装置37の一部である分別除去装置20に送られる。分別除去装置20に送られた微紛炭50のうちマイナス(−)に帯電した微粉炭50bは、分別除去装置20によって分別除去される。従って、プラスに帯電した微粉炭50aのみがボイラ10に送られる。なお、分別除去装置20に送られた微紛炭50の流通の際等において、結合して粒径が大きくなった微粉炭は、自重により落下、またはハンマリングにより強制落下させ、戻し流路26を介して粉砕装置40に戻されて再粉砕される。   The pulverized coal 50 generated by the pulverizer 40 is classified into pulverized coal having a predetermined particle size or less by the classification device 30 which is a part of the fuel supply device 37. Coal exceeding a predetermined particle size is returned to the pulverizing device 40 via the return channel 35 and re-pulverized. Pulverized coal 50 having a predetermined particle size or less is sent to the separation and removal device 20 which is a part of the fuel supply device 37. Of the pulverized coal 50 sent to the separation and removal device 20, the pulverized coal 50 b charged negatively (−) is separated and removed by the separation and removal device 20. Therefore, only the pulverized coal 50 a that is positively charged is sent to the boiler 10. When the pulverized coal 50 sent to the separation / removal apparatus 20 is distributed, the pulverized coal having a larger particle size due to the binding is dropped by its own weight or forcedly dropped by hammering. And returned to the crushing device 40 to be crushed again.

分別除去装置20から送られる微粉炭50はボイラ炉15a内に供給される。このボイラ炉15a内に供給される微粉炭50は、プラス(+)の微粉炭50aである。このため、ボイラ10での微紛炭50aの燃焼時には、炭素成分の石炭が主に燃焼されるので、粉塵の発生量を少なくすることができる。このため、粉塵が熱交換器17のボイラ管17aに衝突したり付着したりする虞を抑制することができる。したがって、ボイラ管17aが損傷し、またボイラ管17aからの熱の吸収が困難になる虞を防止することができる。   The pulverized coal 50 sent from the separation and removal device 20 is supplied into the boiler furnace 15a. The pulverized coal 50 supplied into the boiler furnace 15a is positive (+) pulverized coal 50a. Therefore, when the pulverized coal 50a is burned in the boiler 10, the coal of the carbon component is mainly burned, so that the amount of generated dust can be reduced. For this reason, it is possible to suppress the possibility that the dust collides with or adheres to the boiler tube 17a of the heat exchanger 17. Therefore, it is possible to prevent the boiler tube 17a from being damaged and the heat from the boiler tube 17a from becoming difficult to be absorbed.

以上、本発明の実施形態について説明したが、本発明は上記の形態に限定されるものではなく、本発明の目的を逸脱しない範囲での種々の変更が可能である。例えば、上述した各種実施形態を適宜組み合わせてもよい。   As described above, the embodiments of the present invention have been described. However, the present invention is not limited to the above embodiments, and various changes can be made without departing from the object of the present invention. For example, the various embodiments described above may be appropriately combined.

1 燃焼装置
10 ボイラ
11 バーナ
12 ウィンドウボックス
14 2次風路
15 ボイラ炉
16 排ガス流路
17 熱交換器
17a ボイラ管
20 分別除去装置(分別除去手段)
21 分別除去本体部
23 極板
23a 空間部
25 電源
26、35 戻し流路
30 分級装置(分級手段)
31 分級本体部
33 フィルタ
37 燃料供給装置
40 粉砕装置
41 回転刃
42 ブレード
50 微粉炭
50a 炭素成分の微粉炭
50b マイナス(−)に帯電した微粉炭
DESCRIPTION OF SYMBOLS 1 Combustion apparatus 10 Boiler 11 Burner 12 Window box 14 Secondary wind path 15 Boiler furnace 16 Exhaust gas flow path 17 Heat exchanger 17a Boiler tube 20 Separation removal device (separation removal means)
21 Separation removal main body 23 Electrode plate 23a Space 25 Power supply 26, 35 Return flow path 30 Classification device (classification means)
31 Classification main body 33 Filter 37 Fuel supply device 40 Crushing device 41 Rotary blade 42 Blade 50 Pulverized coal 50a Pulverized coal of carbon component 50b Pulverized coal charged negatively (-)

Claims (4)

石炭を粉砕する粉砕装置と、
前記粉砕装置によって粉砕された前記石炭の微粉炭を供給するための燃料供給装置と、
前記燃料供給装置から供給される前記微粉炭を燃焼させ内部に熱交換器が設けられているボイラと、を備える燃焼装置であって、
前記燃料供給装置は、
前記粉砕装置によって粉砕された前記石炭の前記微粉炭から、所定粒径以下の微粉炭を分級する分級手段と、
前記分級手段により分離された所定粒径以下の前記微粉炭のうち、マイナスに帯電している前記微粉炭を分別除去する分別除去手段であって、内部が中空に形成された分別除去本体部を備える分別除去手段と、を有し、
前記分別除去本体部の内部には、プラスの電位が印加された一対の極板が設けられ、前記一対の極板間に前記分級手段により分離された前記所定粒径以下の微粉炭が通流可能な空間部が形成され、
前記空間部を通過した前記微粉炭のうちのプラスに帯電している微粉炭が、前記分別除去本体部に連通されている2次風路を介してボイラに供給されるように構成される
ことを特徴とする燃焼装置。
A crushing device for crushing coal,
A fuel supply device for supplying pulverized coal of the coal pulverized by the pulverization device,
A boiler in which a heat exchanger is provided for burning the pulverized coal supplied from the fuel supply device,
The fuel supply device,
From the pulverized coal of the coal pulverized by the pulverizer, classification means for classifying pulverized coal having a predetermined particle size or less,
Among the pulverized coal having a predetermined particle size or less separated by the classification means, the pulverized coal that is negatively charged is a separation and removal means for separating and removing the pulverized coal, the separation and removal main body portion having a hollow inside. Separation removal means provided,
A pair of electrode plates to which a positive potential is applied are provided inside the separation and removal main body, and pulverized coal having a predetermined particle size or less separated by the classification means flows between the pair of electrode plates. A possible space is formed,
Positively charged pulverized coal among the pulverized coal that has passed through the space is configured to be supplied to the boiler via a secondary air passage that is communicated with the separation and removal main body. A combustion device characterized by the following.
前記分級手段は、前記粉砕装置によって粉砕された石炭の微粉炭のうち所定粒径以下の微粉体のみを通過可能な孔部を有したフィルタと、該フィルタを通過できない微粉炭を前記粉砕装置に戻して再粉砕させるための戻し流路を備えている
ことを特徴とする請求項1に記載の燃焼装置。
The classification means, a filter having a hole portion that can pass only fine powder having a predetermined particle size or less among the pulverized coal of coal pulverized by the pulverizing device, and pulverized coal that cannot pass through the filter to the pulverizing device The combustion device according to claim 1, further comprising a return flow path for returning and re-grinding.
前記ボイラには、プラスの電荷をボイラ壁に印加可能な電荷供給手段が設けられている
ことを特徴とする請求項1又は2に記載の燃焼装置。
The said boiler is provided with the electric charge supply means which can apply a positive electric charge to a boiler wall. The combustion apparatus of Claim 1 or 2 characterized by the above-mentioned.
燃料となる石炭を粉砕させて帯電させた微粉炭を生成し、
前記微粉炭を所定粒径以下に分級し、
分級された所定粒径以下の微粉炭を、プラスの電位が印加された一対の極板の間に形成される空間部に通流させることで、分級された所定粒径以下の微粉炭のうちマイナスに帯電している微粉炭を分別して除去し、
前記マイナスに帯電した微粉炭を分別除去して残されたプラスに帯電した微粉炭を、2次風路を介して燃焼装置のボイラに供給して、該ボイラ内で前記プラスに帯電した微粉炭を燃焼させる
ことを特徴とする燃焼装置の粉塵発生防止方法。
Pulverizing coal as fuel to produce charged pulverized coal,
Classifying the pulverized coal to a predetermined particle size or less,
By passing the classified pulverized coal having a predetermined particle size or less through a space formed between a pair of electrode plates to which a positive potential is applied , the classified pulverized coal having a predetermined particle size or less becomes negative. Separating and removing charged pulverized coal,
Positively charged pulverized coal remaining after separating and removing the negatively charged pulverized coal is supplied to a boiler of a combustion device via a secondary air path, and the positively charged pulverized coal is A method for preventing the generation of dust in a combustion device, characterized by burning gas.
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