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JP4064163B2 - Waste incinerator - Google Patents
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JP4064163B2 - Waste incinerator - Google Patents

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JP4064163B2
JP4064163B2 JP2002173482A JP2002173482A JP4064163B2 JP 4064163 B2 JP4064163 B2 JP 4064163B2 JP 2002173482 A JP2002173482 A JP 2002173482A JP 2002173482 A JP2002173482 A JP 2002173482A JP 4064163 B2 JP4064163 B2 JP 4064163B2
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Japan
Prior art keywords
secondary air
air supply
pipe
supply pipe
combustion chamber
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JP2002173482A
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Japanese (ja)
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JP2004020000A (en
Inventor
俊彦 安田
祥子 重政
一廣 遠山
稔朗 永森
義晴 吉田
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Kanadevia Corp
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Hitachi Zosen Corp
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  • Incineration Of Waste (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、ごみ焼却炉に関し、特に二次空気の供給部分に関する。
【0002】
【従来の技術】
一般に、ごみ焼却炉でごみを燃焼させた際に発生する燃焼ガス中には、ダイオキシン類の前駆物質である一酸化炭素、炭化水素、煤などの未燃分が含まれており、有害なダイオキシン類の発生を抑制するためには、未燃分を完全燃焼させる必要がある。
【0003】
ところで、従来、未燃分を完全燃焼させるのに、燃焼に必要な酸素を含む空気を二次空気として二次燃焼室内に噴出させて、燃焼ガスを十分に攪拌(混合)させるという方法が用いられている。
【0004】
例えば、特許第3052967号公報に開示されているように、焼却炉の二次燃焼室内に、燃焼ガスの流路を横切るように二次空気の空気供給管を、互いに並行に複数本配置するとともに、これら各空気供給管に、その管軸心方向に沿って所定間隔おきに多数の空気吹出口を形成したものがある。
【0005】
【発明が解決しようとする課題】
上記構成によると、複数本の空気供給管を並列にすなわち同一水平面内に配置した場合、二次燃焼室内にて燃焼ガスが下方から上方に流れる際の流路面積が狭くなるため、その流速が早くなって通過時間が短くなり、したがって燃焼ガスの攪拌(混合)が十分に行われないという問題があった。
【0006】
そこで、本発明は、二次燃焼室内にて燃焼ガスを十分に攪拌させ得るごみ焼却炉を提供することを目的とする。
【0007】
【課題を解決するための手段】
上記課題を解決するために、本発明のごみ焼却炉は、二次燃焼室の中心部に二次空気を供給する二次空気供給管体を配置するとともに、この二次空気供給管体を、二次燃焼室を構成する前後壁部間の中央位置に配置されるとともにその左右壁部に両端部が支持された水平方向の支持管と、この支持管の中心部から下方に垂設されるとともに上下に所定間隔おきで二次空気噴出口が複数個形成された上下方向の二次空気供給管とから構成し、
且つ上記支持管の一端側には二次空気を導く二次空気導入管が接続されるとともに、当該支持管内に、その中心から他端寄りにかけて、一端部が支持管の他端側に開口するとともに他端部が上記二次空気供給管の上端入口部に接続された二次空気案内管を、隙間を有して二重管状に配置したものであり、
また上記二次空気供給管体に供給する二次空気の一部または全部を燃焼排ガスとしたものである。
【0008】
上記構成によると、二次燃焼室内の中心部において且つ燃焼ガスの流れに沿って設けられた二次空気噴出口から二次空気、若しくは一部に燃焼排ガスが含まれた二次空気、または燃焼排ガスを、噴出させて燃焼ガスを攪拌するようにしているので、噴出速度をあまり早くする必要がないとともに、水平方向に複数本の空気供給管を配置した場合に比べて、流路断面積もそれ程狭くならず、すなわち燃焼ガスの通過速度が早くなり過ぎることがないので、当該二次燃焼室内にて発生した燃焼ガスを十分に攪拌することができる。したがって、未燃分の完全燃焼が促進されて、ダイオキシン類の前駆物質、例えば一酸化炭素の濃度の低減化を図り得る。
【0009】
【発明の実施の形態】
以下、本発明の実施の形態におけるごみ焼却炉を、図1〜図3に基づき説明する。
【0010】
このごみ焼却炉はストーカ式のもので、図1に示すように、炉本体1の底部には、一端側から他端側に向って、すなわち前方から後方に向って、給じん部2、乾燥段火格子部3、燃焼段火格子部4および後燃焼段火格子部5が設けられるとともに、燃焼段火格子部4の直ぐ上方には、主燃焼域となる燃焼室6が形成されるとともに、この燃焼室6の上方には、二次燃焼域となる二次燃焼室7が形成されている。燃焼ガスの流れ方向を基準にすると、燃焼室6の下流側に二次燃焼室7が配置されていると言える。
【0011】
そして、この二次燃焼室7の中心部には、二次空気(大気である)を噴出して二次燃焼を行わせるとともに当該二次燃焼室7内の燃焼ガスを攪拌(混合)するための二次空気供給管体8が設けられている。
【0012】
この二次空気供給管体8は、図1および図2に示すように、二次燃焼室7を構成する前後壁部1a,1a間の中央位置に配置されるとともにその左右壁部1b,1bに両端部が支持された水平方向の支持管11と、この支持管11の中心部から下方に垂設されるとともに上下に所定間隔おきで二次空気噴出口12が複数個形成された上下方向の二次空気供給管13とから構成されている。
【0013】
そして、上記二次空気供給管13への二次空気の供給は支持管11を介して行われる。すなわち、支持管11の一端側には、二次空気を導く二次空気導入管14が接続されるとともに、支持管11内には、その中心から他端寄りにかけて、一端部が支持管11の他端側に開口するとともに他端部が二次空気供給管13の上端入口部に接続された二次空気案内管15が二重管状に配置されている。勿論、二次空気案内管15と支持管11との間には、二次空気が移動し得る環状の隙間aが設けられている。なお、図示しないが、炉本体1内で燃焼ガスに曝される支持管11および二次空気供給管13の外面には耐熱材が設けられて、高温から保護されている。また、図示しないが、炉本体1の前後壁部には、本来の二次空気供給ノズルが設けられており、矢印bにて示すように、二次空気が供給されている。
【0014】
上記構成において、二次空気導入管14より二次空気が支持管11内に導入されると、一端側から他端側に移動しながら当該支持管11を冷却した後、二次空気案内管15を介して二次空気供給管13内に入り、当該二次空気供給管13の上下に形成された複数個の二次空気噴出口12から二次空気が二次燃焼室7内に噴出される。勿論、二次空気供給管13自身も、二次空気により冷却されている。
【0015】
このように、二次燃焼室7内の中心部において且つ上下複数箇所から前後方向に二次空気を噴出して燃焼ガスを攪拌するようにしているので、噴出速度をあまり早くする必要がないとともに、水平方向に複数本の空気供給管を配置した場合に比べて、流路断面積もそれ程狭くならず、すなわち燃焼ガスの通過速度が早くなり過ぎることがないので、当該二次燃焼室7内にて発生した燃焼ガスを十分に攪拌することができる。燃焼ガスが十分に攪拌されると、未燃分の完全燃焼が促進されて、ダイオキシン類の前駆物質、例えば一酸化炭素の濃度の低減化を図ることができる。
【0016】
ここで、一酸化炭素の等濃度面を、本実施の形態に係る場合と従来例に係る場合とで比較した結果を図3の(a)および(b)に示しておく。図3から分かるように、その等濃度面(100ppm,10ppm)が、本実施の形態に係る方(a)が、従来例に係るものよりも低い位置に現れており、一酸化炭素が早い段階で減少していることが分かる。また、二次燃焼室7出口での一酸化炭素の濃度(最高値)を比較すると、本実施の形態に係る場合では、3.9ppmであったのに対し、従来例に係る場合では、12.0ppmであった。
【0017】
ところで、上記実施の形態においては、二次空気供給管13の前後面に二次空気噴出口12を形成したが、例えば図4に示すように、同一高さ位置で二次空気噴出口12を前後に2個設けたものと、同一高さ位置で90度おきに4個設けたものとを交互に配置するとともに、4個設けたものを2個設けたものに対して、その位相を45度ずらせるようにしたものでもよい。この場合も、図5に示すように、上記実施の形態と同様に、一酸化炭素が早い段階で減少しているのが分かる。
【0018】
なお、二次空気噴出口12の個数および噴出方向については、上記以外にも種々の配置形態が考えられ、とにかく、周囲に二次空気を噴出させて、燃焼ガスをより効果的に攪拌させ得るものであればどのような配置でもよい。
【0019】
ところで、上記実施の形態においては、二次空気供給管体に二次空気を供給するように説明したが、例えば当該二次燃焼室から排出された燃焼排ガスを、二次空気に混入させるようにしてもよく、また場合によっては、二次空気の替わりに、すなわち全部を燃焼排ガスとしてもよい(この意味で、二次空気供給管体を、単に、流体供給管体ということもできる)。
【0020】
【発明の効果】
以上のように本発明のごみ焼却炉の構成によると、二次燃焼室内の中心部において且つ燃焼ガスの流れに沿って設けられた二次空気噴出口から二次空気、若しくは一部に燃焼排ガスが含まれた二次空気、または燃焼排ガスを噴出させて燃焼ガスを攪拌するようにしているので、噴出速度をあまり早くする必要がないとともに、水平方向に複数本の空気供給管を配置した場合に比べて、流路断面積もそれ程狭くならず、すなわち燃焼ガスの通過速度が早くなり過ぎることがないので、当該二次燃焼室内にて発生した燃焼ガスを十分に攪拌することができる。
【図面の簡単な説明】
【図1】本発明の実施の形態に係るごみ焼却炉の概略構成を示す斜視図である。
【図2】同ごみ焼却炉における二次空気供給管体の概略構成を示す斜視図である。
【図3】同ごみ焼却炉での燃焼室における一酸化炭素の等濃度面を示す斜視図である。
【図4】同ごみ焼却炉の変形例に係る二次空気供給管の斜視図である。
【図5】同変形例に係る二次空気供給管を用いた際の燃焼室における一酸化炭素の等濃度面を示す斜視図である。
【符号の説明】
1 炉本体
6 燃焼室
7 二次燃焼室
8 二次空気供給管体
11 支持管
12 二次空気噴出口
13 二次空気供給管
14 二次空気導入管
15 二次空気案内管
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a waste incinerator, and particularly to a secondary air supply portion.
[0002]
[Prior art]
In general, the combustion gas generated when garbage is burned in a waste incinerator contains unburned components such as carbon monoxide, hydrocarbons, and soot, which are precursors of dioxins. In order to suppress the generation of odors, it is necessary to completely burn the unburned matter.
[0003]
By the way, conventionally, in order to completely burn the unburned matter, a method of jetting air containing oxygen necessary for combustion as secondary air into the secondary combustion chamber and sufficiently stirring (mixing) the combustion gas is used. It has been.
[0004]
For example, as disclosed in Japanese Patent No. 3052967, a plurality of secondary air supply pipes are arranged in parallel to each other in the secondary combustion chamber of the incinerator so as to cross the flow path of the combustion gas. Some of these air supply pipes are formed with a large number of air outlets at predetermined intervals along the axial direction of the pipe.
[0005]
[Problems to be solved by the invention]
According to the above configuration, when a plurality of air supply pipes are arranged in parallel, that is, in the same horizontal plane, the flow area when the combustion gas flows from the lower side to the upper side in the secondary combustion chamber becomes narrower. There was a problem that the passage time was shortened and the combustion gas was not sufficiently stirred (mixed).
[0006]
Then, an object of this invention is to provide the refuse incinerator which can fully stir combustion gas in a secondary combustion chamber.
[0007]
[Means for Solving the Problems]
In order to solve the above problems, the waste incinerator of the present invention is arranged with a secondary air supply pipe for supplying secondary air to the center of the secondary combustion chamber , and this secondary air supply pipe is A horizontal support pipe disposed at the center position between the front and rear wall parts constituting the secondary combustion chamber and supported at both ends by the left and right wall parts, and suspended downward from the center part of the support pipe And a secondary air supply pipe in the vertical direction in which a plurality of secondary air outlets are formed at predetermined intervals in the vertical direction,
Further, a secondary air introduction pipe for guiding secondary air is connected to one end side of the support pipe, and one end portion opens to the other end side of the support pipe from the center to the other end in the support pipe. A secondary air guide pipe having the other end connected to the upper end inlet of the secondary air supply pipe is disposed in a double tubular shape with a gap ,
Further, a part or all of the secondary air supplied to the secondary air supply pipe body is used as combustion exhaust gas.
[0008]
According to the above configuration, secondary air from the secondary air outlet provided in the center of the secondary combustion chamber and along the flow of the combustion gas, or secondary air partially containing combustion exhaust gas, or combustion Since the exhaust gas is ejected and the combustion gas is agitated, it is not necessary to make the ejection speed so fast and the cross-sectional area of the flow path is also larger than when multiple air supply pipes are arranged in the horizontal direction. Since it does not become so narrow, that is, the passage speed of the combustion gas does not become too fast, the combustion gas generated in the secondary combustion chamber can be sufficiently stirred. Therefore, complete combustion of the unburned content is promoted, and the concentration of the precursor of dioxins such as carbon monoxide can be reduced.
[0009]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, the refuse incinerator in embodiment of this invention is demonstrated based on FIGS. 1-3.
[0010]
This waste incinerator is of a stoker type, and as shown in FIG. 1, at the bottom of the furnace body 1, from one end side to the other end side, that is, from the front to the rear, the dust supply unit 2, the drying A stage grate part 3, a combustion stage grate part 4 and a post combustion stage grate part 5 are provided, and a combustion chamber 6 serving as a main combustion zone is formed immediately above the combustion stage grate part 4. A secondary combustion chamber 7 serving as a secondary combustion region is formed above the combustion chamber 6. Based on the flow direction of the combustion gas, it can be said that the secondary combustion chamber 7 is disposed downstream of the combustion chamber 6.
[0011]
And in order to stir (mix) the combustion gas in the said secondary combustion chamber 7 while injecting secondary air (air | atmosphere) into the center part of this secondary combustion chamber 7 to perform secondary combustion. Secondary air supply pipe body 8 is provided.
[0012]
As shown in FIGS. 1 and 2, the secondary air supply pipe body 8 is disposed at a central position between the front and rear wall portions 1a and 1a constituting the secondary combustion chamber 7, and the left and right wall portions 1b and 1b. A horizontal support pipe 11 supported at both ends thereof, and a vertical direction in which a plurality of secondary air jets 12 are vertically formed at predetermined intervals while being vertically suspended from the center of the support pipe 11 Secondary air supply pipe 13.
[0013]
The secondary air is supplied to the secondary air supply pipe 13 through the support pipe 11. That is, a secondary air introduction pipe 14 that guides secondary air is connected to one end side of the support pipe 11, and one end of the support pipe 11 extends from the center toward the other end of the support pipe 11. A secondary air guide pipe 15 having an opening on the other end side and having the other end connected to the upper end inlet of the secondary air supply pipe 13 is arranged in a double tubular shape. Of course, an annular gap a in which the secondary air can move is provided between the secondary air guide tube 15 and the support tube 11. Although not shown, a heat-resistant material is provided on the outer surfaces of the support tube 11 and the secondary air supply tube 13 exposed to the combustion gas in the furnace body 1 to protect them from high temperatures. Although not shown, the front and rear walls of the furnace body 1 are provided with an original secondary air supply nozzle, and secondary air is supplied as shown by an arrow b.
[0014]
In the above configuration, when secondary air is introduced into the support tube 11 from the secondary air introduction tube 14, the support tube 11 is cooled while moving from one end side to the other end side, and then the secondary air guide tube 15 is cooled. And enters the secondary air supply pipe 13, and secondary air is jetted into the secondary combustion chamber 7 from a plurality of secondary air outlets 12 formed above and below the secondary air supply pipe 13. . Of course, the secondary air supply pipe 13 itself is also cooled by the secondary air.
[0015]
As described above, since the secondary air is jetted in the front-rear direction in the central portion of the secondary combustion chamber 7 and from a plurality of locations, the combustion gas is agitated. Compared with the case where a plurality of air supply pipes are arranged in the horizontal direction, the flow passage cross-sectional area is not so narrow, that is, the passage speed of the combustion gas does not become too fast. The combustion gas generated in can be sufficiently stirred. When the combustion gas is sufficiently agitated, complete combustion of unburned matter is promoted, and the concentration of dioxin precursors such as carbon monoxide can be reduced.
[0016]
Here, FIG. 3A and FIG. 3B show the results of comparing the equiconcentration surface of carbon monoxide between the case according to the present embodiment and the case according to the conventional example. As can be seen from FIG. 3, the equivalent concentration surface (100 ppm, 10 ppm) appears at a lower position in the case (a) according to the present embodiment than that according to the conventional example, and carbon monoxide is in an early stage. It can be seen that the number is decreasing. Further, when comparing the concentration (maximum value) of carbon monoxide at the outlet of the secondary combustion chamber 7, it was 3.9 ppm in the case of this embodiment, whereas it was 12 in the case of the conventional example. 0.0 ppm.
[0017]
By the way, in the said embodiment, although the secondary air jet nozzle 12 was formed in the front-and-back surface of the secondary air supply pipe | tube 13, as shown in FIG. 4, for example, the secondary air jet nozzle 12 is made into the same height position. The two provided before and after and the four provided at every 90 degrees at the same height position are alternately arranged, and the phase is set to 45 with respect to the two provided four. It may be designed to be deviated. Also in this case, as shown in FIG. 5, it can be seen that carbon monoxide is reduced at an early stage as in the above embodiment.
[0018]
In addition, about the number of the secondary air ejection ports 12 and the ejection direction, various arrangement forms other than the above are conceivable, and anyway, secondary air can be ejected around and the combustion gas can be stirred more effectively. Any arrangement can be used.
[0019]
By the way, in the above-described embodiment, it has been described that the secondary air is supplied to the secondary air supply pipe body. However, for example, the combustion exhaust gas discharged from the secondary combustion chamber is mixed into the secondary air. In some cases, instead of the secondary air, that is, the whole may be combustion exhaust gas (in this sense, the secondary air supply pipe body may be simply referred to as a fluid supply pipe body).
[0020]
【The invention's effect】
As described above, according to the configuration of the waste incinerator of the present invention, the secondary air or a part of the combustion exhaust gas is discharged from the secondary air outlet provided in the center of the secondary combustion chamber and along the flow of the combustion gas. When the combustion air is agitated by ejecting secondary air containing combustion gas or combustion exhaust gas, it is not necessary to make the ejection speed too fast, and when multiple air supply pipes are arranged in the horizontal direction Compared to the above, the cross-sectional area of the flow path is not so narrow, that is, the passage speed of the combustion gas does not become too fast, so that the combustion gas generated in the secondary combustion chamber can be sufficiently stirred.
[Brief description of the drawings]
FIG. 1 is a perspective view showing a schematic configuration of a waste incinerator according to an embodiment of the present invention.
FIG. 2 is a perspective view showing a schematic configuration of a secondary air supply pipe body in the waste incinerator.
FIG. 3 is a perspective view showing an equi-concentration surface of carbon monoxide in a combustion chamber in the waste incinerator.
FIG. 4 is a perspective view of a secondary air supply pipe according to a modification of the waste incinerator.
FIG. 5 is a perspective view showing an equi-concentration surface of carbon monoxide in a combustion chamber when the secondary air supply pipe according to the modification is used.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Furnace body 6 Combustion chamber 7 Secondary combustion chamber 8 Secondary air supply pipe body 11 Support pipe 12 Secondary air outlet 13 Secondary air supply pipe 14 Secondary air introduction pipe 15 Secondary air guide pipe

Claims (2)

二次燃焼室の中心部に二次空気を供給する二次空気供給管体を配置するとともに、この二次空気供給管体を、二次燃焼室を構成する前後壁部間の中央位置に配置されるとともにその左右壁部に両端部が支持された水平方向の支持管と、この支持管の中心部から下方に垂設されるとともに上下に所定間隔おきで二次空気噴出口が複数個形成された上下方向の二次空気供給管とから構成し、
且つ上記支持管の一端側には二次空気を導く二次空気導入管が接続されるとともに、当該支持管内に、その中心から他端寄りにかけて、一端部が支持管の他端側に開口するとともに他端部が上記二次空気供給管の上端入口部に接続された二次空気案内管を、隙間を有して二重管状に配置したことを特徴とするごみ焼却炉。
A secondary air supply pipe that supplies secondary air is arranged at the center of the secondary combustion chamber , and this secondary air supply pipe is arranged at a central position between the front and rear walls constituting the secondary combustion chamber. And a horizontal support pipe whose both ends are supported on the right and left wall parts, and a plurality of secondary air jets formed vertically at predetermined intervals while being suspended downward from the center part of the support pipe. Composed of a secondary air supply pipe in the vertical direction,
Further, a secondary air introduction pipe for guiding secondary air is connected to one end side of the support pipe, and one end portion opens to the other end side of the support pipe from the center to the other end in the support pipe. In addition, a secondary air guide pipe having the other end connected to the upper end inlet of the secondary air supply pipe is disposed in a double tubular shape with a gap .
二次空気の一部または全部を燃焼排ガスとしたことを特徴とする請求項1に記載のごみ焼却炉。The waste incinerator according to claim 1 , wherein a part or all of the secondary air is used as combustion exhaust gas.
JP2002173482A 2002-06-14 2002-06-14 Waste incinerator Expired - Lifetime JP4064163B2 (en)

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JP5219468B2 (en) * 2007-11-15 2013-06-26 日立造船株式会社 Blowing method of secondary combustion air in the secondary combustion chamber
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