JP2022062717A - Combined combustion furnace, and combined combustion boiler - Google Patents

Combined combustion furnace, and combined combustion boiler Download PDF

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JP2022062717A
JP2022062717A JP2022002575A JP2022002575A JP2022062717A JP 2022062717 A JP2022062717 A JP 2022062717A JP 2022002575 A JP2022002575 A JP 2022002575A JP 2022002575 A JP2022002575 A JP 2022002575A JP 2022062717 A JP2022062717 A JP 2022062717A
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furnace
carbon fuel
burners
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ammonia
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隆政 伊藤
Takamasa Ito
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IHI Corp
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Abstract

PROBLEM TO BE SOLVED: To prevent emissivity of flame from decreasing upon combusting carbon fuel mixed with low carbon fuel.
SOLUTION: There is provided a combined combustion furnace comprising a furnace, a first burner that injects carbon fuel to the furnace to burn the same, and a second burner that injects low carbon fuel of a lower carbon concentration relative to the carbon fuel to the furnace to burn the same. The first burner injects the carbon fuel in such a manner that carbon fuel flame is formed in a closer vicinity of the furnace wall relative to low carbon fuel flame resulting from the combustion of the low carbon fuel.
SELECTED DRAWING: Figure 1
COPYRIGHT: (C)2022,JPO&INPIT

Description

本発明は、複合燃焼炉及び複合燃焼ボイラに関する。 The present invention relates to a combined combustion furnace and a combined combustion boiler.

下記特許文献1、2には、微粉炭とアンモニアとを複合燃焼させるボイラが開示されている。これらボイラでは、二酸化炭素(CO)の排出量を低減するため、従来から燃料として用いていた微粉炭に加え、水素キャリアであるアンモニアを燃料として燃焼させるものである。 The following Patent Documents 1 and 2 disclose a boiler for combined combustion of pulverized coal and ammonia. In these boilers, in order to reduce carbon dioxide (CO 2 ) emissions, in addition to the pulverized coal that has been conventionally used as fuel, ammonia, which is a hydrogen carrier, is burned as fuel.

特開2016-041990号公報Japanese Unexamined Patent Publication No. 2016-041990 特開2016-183640号公報Japanese Unexamined Patent Publication No. 2016-183640

ところで、周知のように、ボイラは火炉で発生した熱を主に水に伝熱させて水蒸気を発生させる伝熱装置である。炉壁の水管に流れる水に輻射伝熱により入熱する熱量Qは、火炉の燃焼ガス温度Tgas、炉壁温度Twall、火炎の放射率ε、またステファンボルツマン定数σに関して下式(1)で表される。この式(1)が示すように、ボイラの性能つまりボイラの収熱性能は、火炎の放射率εに比例する。
Q=σε(Tgas -Twall ) (1)
By the way, as is well known, a boiler is a heat transfer device that mainly transfers heat generated in a fireplace to water to generate steam. The amount of heat Q that enters the water flowing through the water pipe of the furnace wall by radiant heat transfer is the following equation (1) with respect to the combustion gas temperature T gas of the furnace, the furnace wall temperature T wall , the emissivity ε of the flame, and the Stefan-Boltzmann constant σ. It is represented by. As shown by this equation (1), the boiler performance, that is, the heat collection performance of the boiler is proportional to the emissivity ε of the flame.
Q = σε (T gas 4 -T wall 4 ) (1)

一方、上記火炎の放射率εは燃料に含まれる炭素濃度に依存することが知られている。したがって、炭素を構成元素として含まないアンモニアのような低炭素燃料を微粉炭や石炭のような炭素燃料に混合させて火炉で燃焼させた場合、炭素燃料を単独燃料として燃焼させた場合に比較して火炎の放射率εが低下し、この結果としてボイラの収熱性能が低下することが懸念される。 On the other hand, it is known that the emissivity ε of the flame depends on the carbon concentration contained in the fuel. Therefore, when a low carbon fuel such as ammonia that does not contain carbon as a constituent element is mixed with a carbon fuel such as pulverized coal or coal and burned in a furnace, compared with the case where the carbon fuel is burned as a single fuel. Therefore, there is a concern that the radiation coefficient ε of the flame will decrease, and as a result, the heat collection performance of the boiler will decrease.

本発明は、上述した事情に鑑みてなされたものであり、炭素燃料と低炭素燃料と同時に燃焼させる場合における火炎の放射率の低下抑制を目的とするものである。 The present invention has been made in view of the above circumstances, and an object of the present invention is to suppress a decrease in the emissivity of a flame when burning a carbon fuel and a low carbon fuel at the same time.

上記目的を達成するために、本発明では、複合燃焼炉に係る第1の解決手段として、火炉と、炭素燃料を前記火炉に噴射して燃焼させる第1のバーナと、前記炭素燃料よりも炭素濃度が低い低炭素燃料を前記火炉に噴射して燃焼させる第2のバーナとを備え、前記第1のバーナは、前記低炭素燃料の燃焼による低炭素燃料火炎よりも前記火炉の炉壁の近くに炭素燃料火炎が形成されるように前記炭素燃料を噴射する、という手段を採用する。 In order to achieve the above object, in the present invention, as a first solution for a combined combustion furnace, a furnace, a first burner for injecting carbon fuel into the furnace for combustion, and carbon rather than the carbon fuel are used. It is equipped with a second burner that injects and burns a low carbon fuel having a low concentration into the furnace, and the first burner is closer to the furnace wall of the furnace than the low carbon fuel flame due to the combustion of the low carbon fuel. The means of injecting the carbon fuel so as to form a carbon fuel flame is adopted.

本発明では、複合燃焼炉に係る第2の解決手段として、上記第1の解決手段において、前記第1のバーナは、前記第2のバーナの周囲に複数配置される、という手段を採用する。 In the present invention, as the second solution for the combined combustion furnace, in the first solution, a plurality of the first burners are arranged around the second burner.

本発明では、複合燃焼炉に係る第3の解決手段として、上記第1の解決手段において、前記第1のバーナ及び前記第2のバーナは、内側から前記低炭素燃料を噴射すると共に外側から前記炭素燃料を噴射する複合バーナである、という手段を採用する。 In the present invention, as a third solution relating to the combined combustion furnace, in the first solution, the first burner and the second burner inject the low carbon fuel from the inside and the low carbon fuel from the outside. It adopts the means of being a composite burner that injects carbon fuel.

本発明では、複合燃焼炉に係る第4の解決手段として、上記第1~第3のいずれかの解決手段において、前記炭素燃料は微粉炭である、という手段を採用する。 In the present invention, as the fourth solution means for the combined combustion furnace, in any of the first to third solutions, the means that the carbon fuel is pulverized coal is adopted.

本発明では、複合燃焼炉に係る第5の解決手段として、上記第1~第4のいずれかの解決手段において、前記低炭素燃料はアンモニアである、という手段を採用する。 In the present invention, as a fifth solution relating to the combined combustion furnace, in any of the first to fourth solutions, the means that the low carbon fuel is ammonia is adopted.

本発明では、ボイラに係る解決手段として、上記第1~第5のいずれかの解決手段に係る複合燃焼炉を備える、という手段を採用する。 In the present invention, as a solution for the boiler, a means for providing a combined combustion furnace according to any one of the first to fifth solutions is adopted.

本発明によれば、低炭素燃料の燃焼による火炎よりも火炉の炉壁の近くに火炎が生成されるように炭素燃料を噴射するので、炭素燃料と低炭素燃料と同時に燃焼させる場合における火炎の放射率の低下を抑制することが可能である。 According to the present invention, since the carbon fuel is injected so that the flame is generated closer to the furnace wall of the furnace than the flame caused by the combustion of the low carbon fuel, the flame in the case of burning the carbon fuel and the low carbon fuel at the same time is used. It is possible to suppress the decrease in radiation rate.

本発明の第1実施形態に係る複合燃焼炉A及び当該複合燃焼炉Aを備えるボイラの要部構成を示す正面図である。It is a front view which shows the main part structure of the composite combustion furnace A which concerns on 1st Embodiment of this invention, and the boiler which comprises the composite combustion furnace A. 図1のX-X線における矢視図である。It is an arrow view in the X-ray line of FIG. 本発明の第2実施形態に係る複合燃焼炉B及び当該複合燃焼炉Bを備えるボイラの要部構成を示す第1の断面図である。It is a 1st sectional view which shows the main part structure of the combined combustion furnace B which concerns on 2nd Embodiment of this invention, and the boiler which comprises the said combined combustion furnace B. 本発明の第2実施形態に係る複合燃焼炉B及び当該複合燃焼炉Bを備えるボイラの要部構成を示す第2の断面図である。It is a 2nd sectional view which shows the main part structure of the combined combustion furnace B which concerns on 2nd Embodiment of this invention, and the boiler which comprises the said combined combustion furnace B. 本発明の第2実施形態に係る複合燃焼炉B及び当該複合燃焼炉Bを備えるボイラの要部構成を示す第3の断面図である。It is a 3rd sectional view which shows the main part structure of the combined combustion furnace B which concerns on 2nd Embodiment of this invention, and the boiler which comprises the said combined combustion furnace B.

以下、図面を参照して、本発明の実施形態について説明する。
〔第1実施形態〕
最初に、本発明の第1実施形態に係る複合燃焼炉A及び当該複合燃焼炉Aを備えるボイラについて、図1及び図2を参照して説明する。
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
[First Embodiment]
First, the combined combustion furnace A according to the first embodiment of the present invention and the boiler including the combined combustion furnace A will be described with reference to FIGS. 1 and 2.

この第1実施形態に係るボイラは、火炉1、熱交換機器2、複数のバーナM11~M33、N11~N33(第1のバーナ兼第2のバーナ)、アンモニア供給装置3及び微粉炭供給装置4を要部として備えている。なお、これら複数の構成要素のうち、火炉1の一部(下部)及び複数のバーナM11~M33、N11~N33は、第1実施形態に係る複合燃焼炉Aを構成している。 The boiler according to the first embodiment includes a fireplace 1, a heat exchange device 2, a plurality of burners M11 to M33, N11 to N33 (first burner and second burner), an ammonia supply device 3, and a pulverized coal supply device 4. Is provided as a key part. Of these plurality of components, a part (lower part) of the furnace 1 and a plurality of burners M11 to M33 and N11 to N33 constitute the combined combustion furnace A according to the first embodiment.

火炉1は、垂直かつ筒状に設けられた炉壁によって構成され、燃料を燃焼させて燃焼熱を発生させる炉体である。この火炉1では、燃料が燃焼することによって高温の燃焼ガスが発生する。このような火炉1の後段には、図示しない煙道が設けられている。上記燃焼ガスは、上記煙道を介して大気中に放出されるが、煙道を通過する間に窒素酸化物(NOx)や硫化物(SOx)が除去される。なお、このような火炉1の底部には、燃料の燃焼によって発生する灰分を外部に排出する排出口1aが設けられている。 The furnace 1 is composed of a furnace wall provided vertically and in a tubular shape, and is a furnace body that burns fuel to generate combustion heat. In this fireplace 1, high-temperature combustion gas is generated by burning fuel. A flue (not shown) is provided in the subsequent stage of such a fireplace 1. The combustion gas is released into the atmosphere through the flue, but nitrogen oxides (NOx) and sulfides (SOx) are removed while passing through the flue. The bottom of such a fireplace 1 is provided with a discharge port 1a for discharging ash generated by combustion of fuel to the outside.

熱交換機器2は、上記火炉1の上部や炉壁に設けられた複数の伝熱管から構成されており、内部に水が流通している。この熱交換機器2は、過熱器や再熱器等、ボイラに設けられる熱交換機器を総称するものであり、燃焼ガスが有する燃焼熱を伝熱管内の水と熱交換させることにより水蒸気を発生させる。 The heat exchange device 2 is composed of a plurality of heat transfer tubes provided on the upper part of the fireplace 1 and the furnace wall, and water is circulated inside. This heat exchange device 2 is a general term for heat exchange devices provided in a boiler such as a superheater and a reheater, and generates water vapor by exchanging heat of combustion contained in combustion gas with water in a heat transfer tube. Let me.

複数のバーナM11~M33、N11~N33は、火炉1の下部に二次元状かつ対向配置されており、火炉1内に燃料を噴射して燃焼させる。これら複数のバーナM11~M33、N11~N33は、何れもアンモニア(低炭素燃料)及び微粉炭(炭素燃料)を燃料として火炉1内に噴射する複合バーナであり、本発明における第1のバーナ兼第2のバーナである。 The plurality of burners M11 to M33 and N11 to N33 are two-dimensionally and opposed to each other in the lower part of the fireplace 1, and fuel is injected into the fireplace 1 to burn it. These plurality of burners M11 to M33 and N11 to N33 are all composite burners that inject ammonia (low carbon fuel) and pulverized coal (carbon fuel) into the furnace 1 as fuels, and also serve as the first burner in the present invention. The second burner.

なお、図示しないが、火炉1には複数のバーナM11~M33、N11~N33から噴射された燃料(アンモニア及び微粉炭)を着火させる着火装置が設けられている。各バーナM11~M33、N11~N33から火炉1内に噴射された燃料(アンモニア及び微粉炭)は、上記着火装置の働きによって着火して燃焼する。 Although not shown, the fireplace 1 is provided with an ignition device for igniting fuels (ammonia and pulverized coal) injected from a plurality of burners M11 to M33 and N11 to N33. The fuel (ammonia and pulverized coal) injected into the furnace 1 from the burners M11 to M33 and N11 to N33 are ignited and burned by the action of the ignition device.

アンモニア供給装置3は、上記複数のバーナM11~M33、N11~N33にアンモニアを低炭素燃料として供給する一方の燃料供給装置である。微粉炭供給装置4は、上記複数のバーナM11~M33、N11~N33に微粉炭を炭素燃料として供給する他方の燃料供給装置である。 The ammonia supply device 3 is one of the fuel supply devices for supplying ammonia as a low carbon fuel to the plurality of burners M11 to M33 and N11 to N33. The pulverized coal supply device 4 is the other fuel supply device that supplies pulverized coal as carbon fuel to the plurality of burners M11 to M33 and N11 to N33.

ここで、上記アンモニアは、分子式(NH)によって示されるように水素(H)と窒素(N)との化合物であり、構成原子として炭素(C)を含まない。また、このアンモニア(低炭素燃料)は、難燃性の物質として知られるものの、メタン(CH)と同様に3つの水素原子を有する水素キャリア物質である。一方、微粉炭は、化石燃料である石炭を数マイクロメートル程度の大きさまで粉砕処理したものであり、ボイラ用の燃料として一般的に使用されている。すなわち、アンモニアは、微粉炭(炭素燃料)よりも炭素濃度が低い低炭素燃料である。 Here, the ammonia is a compound of hydrogen (H) and nitrogen (N) as shown by the molecular formula (NH 3 ), and does not contain carbon (C) as a constituent atom. Although this ammonia (low carbon fuel) is known as a flame-retardant substance, it is a hydrogen carrier substance having three hydrogen atoms like methane (CH 3 ). On the other hand, pulverized coal is a fossil fuel obtained by pulverizing coal to a size of about several micrometers, and is generally used as a fuel for boilers. That is, ammonia is a low carbon fuel having a lower carbon concentration than pulverized coal (carbon fuel).

上記複数のバーナM11~M33、N11~N33についてさらに詳しく説明すると、本第1実施形態に係る複合燃焼炉Aでは、火炉1の下部において垂直姿勢で平行に対向する一対の炉壁のうち、一方の炉壁に9個のバーナM11~M33が設けられ、他方の炉壁に同じく9個のバーナN11~N33が設けられている。各々9個のバーナM11~M33、N11~N33は、何れも上下方向に三段、左右方向に三列、つまり二次元状に設けられている。 The plurality of burners M11 to M33 and N11 to N33 will be described in more detail. In the combined combustion furnace A according to the first embodiment, one of a pair of furnace walls facing each other in a vertical posture in the lower part of the furnace 1. Nine burners M11 to M33 are provided on the furnace wall of the same, and nine burners N11 to N33 are also provided on the other furnace wall. Each of the nine burners M11 to M33 and N11 to N33 are provided in three stages in the vertical direction and in three rows in the horizontal direction, that is, in a two-dimensional shape.

すなわち、各々9個のバーナM11~M33、N11~N33のうち、各々3個のバーナM11~M13、N11~N13は上段に設けられ、各々3個のバーナM21~M23、N21~N23は中段に設けられ、各々3個のバーナM31~M33、N31~N33は下段に設けられている。また、これら9個のバーナM11~M33、N11~N33のうち、各々3個のバーナM11~M31、N11~N31は、火炉1の外側から見た場合に右側に位置し、各々3個のバーナM12~M32、N12~N32は中央に位置し、各々3個のバーナM13~M33、N13~N33は左側に位置する。 That is, of the nine burners M11 to M33 and N11 to N33, three burners M11 to M13 and N11 to N13 are provided in the upper stage, and three burners M21 to M23 and N21 to N23 are provided in the middle stage, respectively. Three burners M31 to M33 and N31 to N33 are provided in the lower stage, respectively. Of these nine burners M11 to M33 and N11 to N33, three burners M11 to M31 and N11 to N31 are located on the right side when viewed from the outside of the furnace 1, and three burners each are located. M12 to M32 and N12 to N32 are located in the center, and three burners M13 to M33 and N13 to N33 are located on the left side, respectively.

上段に位置する各々3個の各バーナM11~M13、N11~N13は何れも同一高さに設けられ、中段に位置する各々3個の各バーナM21~M23、N21~N23は何れも同一高さに設けられ、下段に位置する各々3個の各バーナM31~M33、N31~N33は何れも同一高さに設けられている。また、右側に位置する各々3個のバーナM11~M31、N11~N31は上下方向に一列に設けられ、中央に位置する各々3個のバーナM12~M32、N12~N32は上下方向に一列に設けられ、左側に位置する各々3個のバーナM13~M33、N13~N33は上下方向に一列に設けられている。すなわち、各々9個のバーナM11~M33、N11~N33は、火炉1の鉛直面に直交配置されている。 The three burners M11 to M13 and N11 to N13 located in the upper row are all provided at the same height, and the three burners M21 to M23 and N21 to N23 located in the middle row are all provided at the same height. The three burners M31 to M33 and N31 to N33, which are located in the lower stage, are all provided at the same height. Further, three burners M11 to M31 and N11 to N31 located on the right side are provided in a row in the vertical direction, and three burners M12 to M32 and N12 to N32 located in the center are provided in a row in the vertical direction. The three burners M13 to M33 and N13 to N33 located on the left side are provided in a row in the vertical direction. That is, the nine burners M11 to M33 and N11 to N33, respectively, are arranged orthogonally to the vertical plane of the furnace 1.

また、各々9個のバーナM11~M33、N11~N33のうち、符号の数字が同一のもの同士は、互いに対向する位置関係になっている。すなわち、バーナM11とバーナN11とは同一水平面内において対向し、バーナM12とバーナN12とは同一水平面内において対向し、バーナM13とバーナN13とは同一水平面内において対向し、バーナM21とバーナN21とは同一水平面内において対向し、バーナM22とバーナN22とは同一水平面内において対向し、バーナM23とバーナN23とは同一水平面内において対向し、またバーナM31とバーナN31とは同一水平面内において対向し、バーナM32とバーナN32とは同一水平面内において対向し、バーナM33とバーナN33とは同一水平面内において対向している。 Further, among the nine burners M11 to M33 and N11 to N33, the ones having the same code number are in a positional relationship facing each other. That is, the burner M11 and the burner N11 face each other in the same horizontal plane, the burner M12 and the burner N12 face each other in the same horizontal plane, the burner M13 and the burner N13 face each other in the same horizontal plane, and the burner M21 and the burner N21 face each other. Face each other in the same horizontal plane, the burner M22 and the burner N22 face each other in the same horizontal plane, the burner M23 and the burner N23 face each other in the same horizontal plane, and the burner M31 and the burner N31 face each other in the same horizontal plane. , The burner M32 and the burner N32 face each other in the same horizontal plane, and the burner M33 and the burner N33 face each other in the same horizontal plane.

このように火炉1の各炉壁に配置された9個のバーナM11~M33、N11~N33には、アンモニア供給装置3からアンモニア(低炭素燃料)が供給され、また微粉炭供給装置4から微粉炭(炭素燃料)が供給される。個々のバーナM11~M33、N11~N33は、内側(中心側)からアンモニアを噴射し、また外側(外周側)から微粉炭を噴射する複合バーナ(第1のバーナ兼第2のバーナ)である。 Ammonia (low carbon fuel) is supplied from the ammonia supply device 3 to the nine burners M11 to M33 and N11 to N33 arranged on each furnace wall of the furnace 1 in this way, and fine powder is supplied from the pulverized coal supply device 4. Charcoal (carbon fuel) is supplied. The individual burners M11 to M33 and N11 to N33 are composite burners (first burner and second burner) that inject ammonia from the inside (center side) and pulverized coal from the outside (outer peripheral side). ..

例えば、個々のバーナM11~M33、N11~N33は三重管状に形成されており、内側管にアンモニアが供給され、中央管に微粉炭が供給され、外側管に燃焼用空気が供給される。したがって、火炉1内には、図示するように各々のバーナM11~M33、N11~N33について、アンモニアの燃焼によって形成されるアンモニア火炎Sa(低炭素燃料火炎)の周囲に微粉炭の燃焼によって形成される微粉炭火炎Sb(炭素燃料火炎)が形成される。 For example, the individual burners M11 to M33 and N11 to N33 are formed in a triple tubular shape, and ammonia is supplied to the inner pipe, pulverized coal is supplied to the central pipe, and combustion air is supplied to the outer pipe. Therefore, in the furnace 1, as shown in the figure, for each of the burners M11 to M33 and N11 to N33, they are formed by burning pulverized coal around the ammonia flame Sa (low carbon fuel flame) formed by burning ammonia. A pulverized coal flame Sb (carbon fuel flame) is formed.

すなわち、火炉1において対向する2つの炉壁に設けられた各バーナM11~M33、N11~N33は、アンモニアの燃焼によるアンモニア火炎Saよりも火炉1の炉壁の近くに微粉炭火炎Sbが生成されるように微粉炭を噴射する。換言すると、各バーナM11~M33、N11~N33は、アンモニア火炎Saが微粉炭火炎Sbよりも火炉1の炉壁から遠ざかるようにアンモニアを噴射する。 That is, in the burners M11 to M33 and N11 to N33 provided on the two facing furnace walls in the furnace 1, the pulverized coal flame Sb is generated closer to the furnace wall of the furnace 1 than the ammonia flame Sa due to the combustion of ammonia. Inject pulverized coal so as to. In other words, the burners M11 to M33 and N11 to N33 inject ammonia so that the ammonia flame Sa is farther from the furnace wall of the furnace 1 than the pulverized coal flame Sb.

続いて、本第1実施形態に係る複合燃焼炉A及びボイラの動作について詳しく説明する。
この複合燃焼炉A及びボイラでは、各々のバーナM11~M33、N11~N33にアンモニア供給装置3からアンモニアが供給され、また微粉炭供給装置4から微粉炭が供給される。
Subsequently, the operation of the combined combustion furnace A and the boiler according to the first embodiment will be described in detail.
In the combined combustion furnace A and the boiler, ammonia is supplied from the ammonia supply device 3 to the burners M11 to M33 and N11 to N33, respectively, and pulverized coal is supplied from the pulverized coal supply device 4.

そして、各々のバーナM11~M33、N11~N33から火炉1内にアンモニア及び微粉炭が噴射されて燃焼することにより、火炉1内に燃焼熱を伴った燃焼ガスが発生する。そして、この燃焼ガスが火炉1内を上昇して熱交換機器2に作用することにより、燃焼ガスの燃焼熱によって水が気化して水蒸気が発生する。ボイラは、このようにして発生させた水蒸気を発電機等の外部機器に供給する。なお、熱交換機器2と熱交換された後の燃焼ガスは、火炉1から煙道を経由して外気に放出される。 Then, ammonia and pulverized coal are injected into the fireplace 1 from the burners M11 to M33 and N11 to N33 and burned, so that combustion gas with combustion heat is generated in the fireplace 1. Then, the combustion gas rises in the furnace 1 and acts on the heat exchange device 2, so that the water is vaporized by the combustion heat of the combustion gas and steam is generated. The boiler supplies the steam generated in this way to an external device such as a generator. The combustion gas after heat exchange with the heat exchange device 2 is released from the fireplace 1 to the outside air via the flue.

ここで、本第1実施形態に係る複合燃焼炉A及びボイラでは、各々のバーナM11~M33、N11~N33は、アンモニア火炎Saの周りに微粉炭火炎Sbが形成されるようにアンモニア及び微粉炭を火炉1内に噴射する。周知のようにアンモニアは、微粉炭よりも燃焼性が低く、一般に燃え難いが、燃焼性に優れた微粉炭がアンモニアより先行して燃焼することにより、火炉1内に噴射されたアンモニアの周囲には、微粉炭の燃焼によって微粉炭火炎Sbが形成される。 Here, in the combined combustion furnace A and the boiler according to the first embodiment, the burners M11 to M33 and N11 to N33 have ammonia and pulverized coal so that the pulverized coal flame Sb is formed around the ammonia flame Sa. Is injected into the furnace 1. As is well known, ammonia has lower flammability than pulverized coal and is generally hard to burn, but pulverized coal having excellent combustibility burns before ammonia, so that the surrounding of ammonia injected into the furnace 1 The pulverized coal flame Sb is formed by the combustion of the pulverized coal.

この微粉炭火炎Sbは、アンモニアよりも炭素濃度が高い微粉炭の燃焼によって形成されたものであり、よって輝度がアンモニア火炎Saの輝度よりも高い。また、このような微粉炭火炎Sbは、各々のバーナM11~M33、N11~N33について、輝度が比較的低いアンモニア火炎Saを取り囲むように形成されるので、火炉1の炉壁には輝度が比較的高い微粉炭火炎Sbによる輻射熱が主に照射される。 The pulverized coal flame Sb is formed by burning pulverized coal having a carbon concentration higher than that of ammonia, and therefore the brightness is higher than the brightness of the ammonia flame Sa. Further, since such a pulverized coal flame Sb is formed so as to surround the ammonia flame Sa having a relatively low brightness for each of the burners M11 to M33 and N11 to N33, the brightness is compared on the furnace wall of the furnace 1. The radiant heat from the high-targeted pulverized coal flame Sb is mainly irradiated.

すなわち、第1実施形態によれば、アンモニアと微粉炭とを同時に燃焼させるに際して、微粉炭のみを燃料として燃焼させる場合に比較して、火炉1の炉壁における火炎の放射率の低下を抑制することが可能である。したがって、この第1実施形態によれば、微粉炭のみを燃料として燃焼させる場合に対してボイラの収熱性能の低下を抑制することが可能である。 That is, according to the first embodiment, when the ammonia and the pulverized coal are burned at the same time, the decrease in the emissivity of the flame in the furnace wall of the furnace 1 is suppressed as compared with the case where only the pulverized coal is burned as fuel. It is possible. Therefore, according to this first embodiment, it is possible to suppress a decrease in the heat collection performance of the boiler as compared with the case where only pulverized coal is burned as fuel.

〔第2実施形態〕
次に、本発明の第2実施形態に係る複合燃焼炉B及び当該複合燃焼炉Bを備えるボイラについて、図3~図5を参照して説明する。なお、図3~図5では、上述した図1及び図2に示した構成要素と同一の構成要素には同一符号を付している。
[Second Embodiment]
Next, the combined combustion furnace B according to the second embodiment of the present invention and the boiler provided with the combined combustion furnace B will be described with reference to FIGS. 3 to 5. In FIGS. 3 to 5, the same components as those shown in FIGS. 1 and 2 described above are designated by the same reference numerals.

本第2実施形態に係る複合燃焼炉Bは、第1実施形態に係る複合燃焼炉Aと同一の構成要素を備えているが、各々のバーナM11~M33、N11~N33に対するアンモニア(低炭素燃料)及び微粉炭(炭素燃料)の供給が第1実施形態に係る複合燃焼炉Aとは異なっている。この複合燃焼炉Bは、第1実施形態に係る複合燃焼炉Aと同様にアンモニア供給装置3及び微粉炭供給装置4を備えているが、図3~図5では、アンモニア供給装置3及び微粉炭供給装置4を便宜上省略している。 The combined combustion furnace B according to the second embodiment has the same components as the combined combustion furnace A according to the first embodiment, but has ammonia (low carbon fuel) for the burners M11 to M33 and N11 to N33, respectively. ) And the supply of pulverized coal (carbon fuel) are different from those of the combined combustion furnace A according to the first embodiment. The combined combustion furnace B includes an ammonia supply device 3 and a pulverized coal supply device 4 as in the combined combustion furnace A according to the first embodiment, but in FIGS. 3 to 5, the ammonia supply device 3 and the pulverized coal are provided. The supply device 4 is omitted for convenience.

図3~図5を対比すると分かるように、本第2実施形態に係る複合燃焼炉Bは、一方側の炉壁において、アンモニアを噴射する1つのバーナM22の周囲に微粉炭を噴射する8つ(複数)のバーナM11~M21、M23~M33が配置されている。また、他方側の炉壁においては、アンモニアを噴射する1つのバーナN22の周囲に微粉炭を噴射する8つ(複数)のバーナN11~N21、N23~N33が配置されている。 As can be seen by comparing FIGS. 3 to 5, in the combined combustion furnace B according to the second embodiment, eight pulverized coals are injected around one burner M22 that injects ammonia on the furnace wall on one side. (Multiple) burners M11 to M21 and M23 to M33 are arranged. Further, on the other side of the furnace wall, eight (plural) burners N11 to N21 and N23 to N33 for injecting pulverized coal are arranged around one burner N22 for injecting ammonia.

すなわち、この複合燃焼炉Bでは、バーナM22,N22が本発明における第1のバーナであり、またバーナM11~M21、M23~M33,N11~N21、N23~N33が本発明における第2のバーナである。 That is, in this combined combustion furnace B, the burners M22 and N22 are the first burners in the present invention, and the burners M11 to M21, M23 to M33, N11 to N21 and N23 to N33 are the second burners in the present invention. be.

このような複合燃焼炉Bでは、図4に示すように、2つのバーナM22、N22からアンモニアが噴射されることによって、火炉1内のバーナM22、N22に対応する位置にアンモニア火炎Saが形成される。また、図3~図5に示すように、他のバーナM11~M13、M21、M23、M31~M33、N11~N13、N21、N23、N31~N33から微粉炭(炭素燃料)が噴射されることによって、火炉1内のバーナM11~M13、M21、M23、M31~M33、N11~N13、N21、N23、N31~N33に対応する位置に微粉炭火炎Sbが形成される。 In such a combined combustion furnace B, as shown in FIG. 4, ammonia is injected from the two burners M22 and N22 to form an ammonia flame Sa in the furnace 1 at a position corresponding to the burners M22 and N22. To. Further, as shown in FIGS. 3 to 5, pulverized coal (carbon fuel) is injected from other burners M11 to M13, M21, M23, M31 to M33, N11 to N13, N21, N23, and N31 to N33. A pulverized carbon flame Sb is formed at positions corresponding to the burners M11 to M13, M21, M23, M31 to M33, N11 to N13, N21, N23, and N31 to N33 in the furnace 1.

すなわち、この第2実施形態では、対向する両方の炉壁において、輝度が比較的低いアンモニア火炎Saを取り囲むように輝度が比較的高い微粉炭火炎Sbが形成されるので、火炉1の炉壁には微粉炭火炎Sbによる輻射熱が主に照射される。したがって、このような第2実施形態によれば、上述した第1実施形態に係る複合燃焼炉Aと同様に、アンモニアと微粉炭とを同時に燃焼させるに際して、火炉1の炉壁における火炎の放射率の低下を抑制することが可能である。 That is, in this second embodiment, the pulverized coal flame Sb having a relatively high brightness is formed so as to surround the ammonia flame Sa having a relatively low brightness in both the facing furnace walls, so that the furnace wall of the furnace 1 has a relatively high brightness. Is mainly irradiated with radiant heat from the pulverized coal flame Sb. Therefore, according to such a second embodiment, the emissivity of the flame in the furnace wall of the furnace 1 when the ammonia and the pulverized coal are burned at the same time as in the combined combustion furnace A according to the first embodiment described above. It is possible to suppress the decrease in.

なお、本発明は上記各実施形態に限定されるものではなく、例えば以下のような変形例が考えられる。
(1)上記各実施形態では、炭素燃料として微粉炭を採用し、低炭素燃料としてアンモニアを採用したが、本発明はこれに限定されない。炭素燃料と比べて低炭素燃料の炭素濃度が低ければよく、低炭素燃料として微粉炭以外の燃料を採用してもよいし、低炭素燃料としてアンモニア以外の燃料を採用してもよい。例えば、炭素燃料として微粉炭を採用した場合に、低炭素燃料としてバイオマスやメタンや水素を採用してもよい。また、例えば炭素燃料としてバイオマスを採用し、低炭素燃料としてアンモニアや水素を採用してもよい。
The present invention is not limited to each of the above embodiments, and for example, the following modifications can be considered.
(1) In each of the above embodiments, pulverized coal is adopted as the carbon fuel and ammonia is adopted as the low carbon fuel, but the present invention is not limited thereto. As long as the carbon concentration of the low carbon fuel is lower than that of the carbon fuel, a fuel other than pulverized coal may be adopted as the low carbon fuel, or a fuel other than ammonia may be adopted as the low carbon fuel. For example, when pulverized coal is adopted as the carbon fuel, biomass, methane, or hydrogen may be adopted as the low carbon fuel. Further, for example, biomass may be adopted as the carbon fuel, and ammonia or hydrogen may be adopted as the low carbon fuel.

(2)上記各実施形態では、ボイラの複合燃焼炉A、Bに本発明を適用した場合について説明したが、本発明はこれに限定されない。本発明は、二次元状に配置される複数のバーナを備える複合燃焼炉であれば、ボイラ以外にも適用可能である。 (2) In each of the above embodiments, the case where the present invention is applied to the combined combustion furnaces A and B of the boiler has been described, but the present invention is not limited thereto. The present invention can be applied to other than boilers as long as it is a combined combustion furnace provided with a plurality of burners arranged in a two-dimensional manner.

(3)上記各実施形態では、火炉1の下部において平行に対向する炉壁に各々9個のバーナM11~M33、N11~N33を設けたが、本発明はこれに限定されない。本発明における複数のバーナの個数は9個以外でもよく、また配置は二次元状に配置されていれば直交配置でなくてもよい。例えば同心円状に設けてもよい。 (3) In each of the above embodiments, nine burners M11 to M33 and N11 to N33 are provided on the furnace walls facing each other in parallel at the lower part of the furnace 1, but the present invention is not limited thereto. The number of the plurality of burners in the present invention may be other than 9, and the arrangement may not be orthogonal as long as it is arranged in a two-dimensional manner. For example, they may be provided concentrically.

(4)上記各実施形態では、バーナM11~M33、N11~N33から噴射する微粉炭あるいは/及びアンモニアの噴射速度について言及しなかったが、例えばアンモニアの噴射速度を微粉炭の噴射速度よりも大きく設定することにより、アンモニア火炎Saを微粉炭火炎Sbよりも火炉1の奥側(中心側)に形成させても良い。 (4) In each of the above embodiments, the injection speed of pulverized coal and / or ammonia injected from the burners M11 to M33 and N11 to N33 is not mentioned, but for example, the injection speed of ammonia is made larger than the injection speed of pulverized coal. By setting, the ammonia flame Sa may be formed on the inner side (center side) of the furnace 1 with respect to the pulverized coal flame Sb.

(5)上記各実施形態では、火炉1の対向する二壁面に微粉炭あるいは/及びアンモニアを噴射するバーナM11~M33、N11~N33を設けたが、本発明はこれに限定されない。例えば、火炉の角部(4ヶ所)に上下方向に延在すると共に所定間隔の燃料噴射孔を設け、これら燃料噴射孔から炉壁に対して所定の噴射角度で燃料を噴射することにより火炉内に旋回流を形成する燃料噴射形態を採用し、この燃料噴射形態においてアンモニアの噴射角度を微粉炭の噴射角度よりも大きく設定することによりアンモニア火炎を微粉炭火炎の内側(火炉の中心側)に形成させるようにしてもよい。 (5) In each of the above embodiments, burners M11 to M33 and N11 to N33 for injecting pulverized coal or / and ammonia are provided on the two facing wall surfaces of the furnace 1, but the present invention is not limited thereto. For example, fuel injection holes are provided at the corners (4 places) of the fireplace in the vertical direction and at predetermined intervals, and fuel is injected from these fuel injection holes to the furnace wall at a predetermined injection angle to inside the fireplace. By adopting a fuel injection form that forms a swirling flow and setting the injection angle of ammonia to be larger than the injection angle of pulverized coal in this fuel injection form, the ammonia flame is placed inside the pulverized coal flame (on the center side of the fireplace). It may be formed.

(6)上記各実施形態では、火炉1の対向する二壁面に微粉炭あるいは/及びアンモニアを噴射するバーナM11~M33、N11~N33を設けたが、本発明はこれに限定されない。例えば、アンモニアを噴射するバーナのみを上記二壁面に直交する壁面に配置してもよい。また、火炉においてバーナの上方(ガス流れの下流側)に二段燃焼用の空気供給ポートを備える形態のボイラでは、この空気供給ポートからアンモニアを噴射してもよい。 (6) In each of the above embodiments, burners M11 to M33 and N11 to N33 for injecting pulverized coal or / and ammonia are provided on the two facing wall surfaces of the furnace 1, but the present invention is not limited thereto. For example, only the burner that injects ammonia may be arranged on the wall surface orthogonal to the above two wall surfaces. Further, in a boiler having an air supply port for two-stage combustion above the burner (downstream side of the gas flow) in the fireplace, ammonia may be injected from this air supply port.

(7)上記第1実施形態では個々のバーナM11~M33、N11~N33を三重管状 に形成したが、本発明はこれに限定されない。バーナM11~M33、N11~N33の構造としては二重状の管状であれば十分である。 (7) In the first embodiment, the individual burners M11 to M33 and N11 to N33 are formed into a triple tubular shape, but the present invention is not limited thereto. As the structure of the burners M11 to M33 and N11 to N33, a double tubular structure is sufficient.

A、B 複合燃焼炉
M11~M33、N11~N33 バーナ
Sa アンモニア火炎
Sb 微粉炭火炎
1 火炉
2 熱交換機器
3 アンモニア供給装置
4 微粉炭供給装置
A, B Combined combustion furnace M11 to M33, N11 to N33 Burner Sa Ammonia flame Sb Microcharcoal flame 1 Fireplace 2 Heat exchange equipment 3 Ammonia supply device 4 Microcoal supply device

Claims (6)

火炉と、
炭素燃料を前記火炉に噴射して燃焼させる第1のバーナと、
前記炭素燃料よりも炭素濃度が低い低炭素燃料を前記火炉に噴射して燃焼させる第2のバーナとを備え、
前記第1のバーナは、前記低炭素燃料の燃焼による低炭素燃料火炎よりも前記火炉の炉壁の近くに炭素燃料火炎が形成されるように前記炭素燃料を噴射することを特徴とする複合燃焼炉。
With a fireplace
A first burner that injects carbon fuel into the fireplace and burns it,
It is equipped with a second burner that injects a low carbon fuel having a lower carbon concentration than the carbon fuel into the fireplace and burns it.
The first burner is a composite combustion characterized in that the carbon fuel is injected so that the carbon fuel flame is formed closer to the furnace wall of the furnace than the low carbon fuel flame due to the combustion of the low carbon fuel. Furnace.
前記第1のバーナは、前記第2のバーナの周囲に複数配置されることを特徴とする請求項1に記載の複合燃焼炉。 The combined combustion furnace according to claim 1, wherein a plurality of the first burners are arranged around the second burner. 前記第1のバーナ及び前記第2のバーナは、内側から前記低炭素燃料を噴射すると共に外側から前記炭素燃料を噴射する複合バーナであることを特徴とする請求項1に記載の複合燃焼炉。 The composite combustion furnace according to claim 1, wherein the first burner and the second burner are composite burners that inject the low carbon fuel from the inside and the carbon fuel from the outside. 前記炭素燃料は微粉炭であることを特徴とする請求項1~3のいずれか一項に記載の複合燃焼炉。 The combined combustion furnace according to any one of claims 1 to 3, wherein the carbon fuel is pulverized coal. 前記低炭素燃料はアンモニアであることを特徴とする請求項1~4のいずれか一項に記載の複合燃焼炉。 The combined combustion furnace according to any one of claims 1 to 4, wherein the low carbon fuel is ammonia. 請求項1~5のいずれか一項に記載の複合燃焼炉を備えることを特徴とするボイラ。 A boiler comprising the combined combustion furnace according to any one of claims 1 to 5.
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