JP2649626B2 - Fluidized bed combustion device with integrated exhaust gas passage - Google Patents

Fluidized bed combustion device with integrated exhaust gas passage

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Publication number
JP2649626B2
JP2649626B2 JP4032973A JP3297392A JP2649626B2 JP 2649626 B2 JP2649626 B2 JP 2649626B2 JP 4032973 A JP4032973 A JP 4032973A JP 3297392 A JP3297392 A JP 3297392A JP 2649626 B2 JP2649626 B2 JP 2649626B2
Authority
JP
Japan
Prior art keywords
combustion
combustion chamber
partition wall
fluidized bed
secondary air
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP4032973A
Other languages
Japanese (ja)
Other versions
JPH05203132A (en
Inventor
秀一 永東
正司 神定
孝裕 大下
啓一 佐藤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ebara Corp
Original Assignee
Ebara Corp
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Filing date
Publication date
Application filed by Ebara Corp filed Critical Ebara Corp
Priority to JP4032973A priority Critical patent/JP2649626B2/en
Publication of JPH05203132A publication Critical patent/JPH05203132A/en
Application granted granted Critical
Publication of JP2649626B2 publication Critical patent/JP2649626B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Incineration Of Waste (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、流動層燃焼装置に係
り、特に、産業廃棄物や都市ゴミ及び石炭など固形状物
質を燃焼するに際し、装置をコンパクト化し、かつ未燃
ガスの発生を最小限に抑制することのできる排ガス通路
を一体化した流動層燃焼装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a fluidized bed combustion apparatus and, more particularly, to a compact apparatus for burning solid substances such as industrial waste, municipal waste and coal, and to minimize the generation of unburned gas. The present invention relates to a fluidized bed combustion apparatus that integrates an exhaust gas passage that can be suppressed to a minimum.

【0002】[0002]

【従来の技術】従来、廃棄物等の燃焼における未燃ガス
を抑制する技術としては、種々のものが提案されてい
る。図6は、従来の都市ゴミ、産業廃棄物の焼却等を用
途とする一般的な流動層燃焼装置を示すものであり、燃
焼炉1は炉壁2で囲まれ、下方からウィンドボックス
6、空気分散板5、流動層部4、燃焼室3で構成されて
おり、例えばスクリュウフィーダ8aで供給口8bから
炉内へ投入された被焼却物は、流動層4の内部で流動空
気7により流動しつつ燃焼したあと、未燃ガスや未燃物
質を含んだ燃焼ガスが上部に隣接した燃焼室3内に流入
し、ノズル9から吹き込まれる二次空気によって燃焼が
継続され、その後出口ダクト10を経由して廃熱ボイラ
11に導かれ所定の熱量を蒸気に変換した後空気予熱器
あるいは節炭器等の余熱回収設備12を経由し集塵設備
13を通過した後、誘引送風機14により煙突15に送
り込まれ大気中に放出される。
2. Description of the Related Art Conventionally, various techniques have been proposed for suppressing unburned gas in the combustion of waste and the like. FIG. 6 shows a conventional fluidized bed combustion apparatus for incineration of municipal garbage and industrial waste, etc., in which a combustion furnace 1 is surrounded by a furnace wall 2 and a wind box 6 and an air The object to be incinerated is composed of a dispersion plate 5, a fluidized bed section 4, and a combustion chamber 3. For example, the incineration material put into the furnace from the supply port 8b by the screw feeder 8a flows by the fluidized air 7 inside the fluidized bed 4. After burning while burning, unburned gas or combustion gas containing unburned material flows into the combustion chamber 3 adjacent to the upper portion, and the combustion is continued by the secondary air blown from the nozzle 9, and thereafter, passes through the outlet duct 10. After being guided to a waste heat boiler 11 and converting a predetermined amount of heat into steam, the dust passes through a dust collecting facility 13 through a residual heat recovery facility 12 such as an air preheater or a economizer, and then is passed to a chimney 15 by an induction blower 14. Sent and released into the atmosphere That.

【0003】このような設備においては燃焼ガス中の未
燃ガス、あるいは未燃物質を最大限に燃焼させるために
燃焼室3の容積を大きくして燃焼ガスの滞留時間を長く
取り、酸素との反応率を向上させようとしているが、そ
のために必然的に燃焼炉1の塔高が高くなりがちであ
り、その出口に付随する廃熱ボイラ11の取り付け位置
も高くなる結果、廃熱ボイラ11を支える架構も高く組
まざるを得ず、建設費も高価になりがちであった。ま
た、その際炉の高さを低くしようとしても、未燃ガスや
未燃物質の発生を抑制するためには一定の限界があっ
た。
In such a facility, the volume of the combustion chamber 3 is increased to maximize the combustion of unburned gas or unburned substances in the combustion gas, so that the residence time of the combustion gas is increased and the oxygen and oxygen are removed. Although the reaction rate is to be improved, the tower height of the combustion furnace 1 tends to be necessarily increased, and the installation position of the waste heat boiler 11 attached to the outlet thereof is also increased. The supporting frame had to be set high, and the construction costs tended to be expensive. At that time, even if an attempt was made to lower the height of the furnace, there was a certain limit in suppressing the generation of unburned gas and unburned substances.

【0004】[0004]

【発明が解決しようとする課題】流動層燃焼装置におい
ては、流動層部で発生した燃焼ガスは未燃ガスや物質を
含むため、上部に隣接する燃焼室にて二次空気と混合さ
せ一定の滞留時間を保持させて燃焼を完結させる必要が
あり、従って、所定の滞留時間を確保するために燃焼炉
の高さが高くなり、その結果としてその後段に位置する
廃熱ボイラについてはそれを支える架台を高くするか、
あるいはダクトによって燃焼排ガスを下方に導かざるを
得ず構造的に無駄な面が見られた。そこで、本発明は前
記のような欠点を解決し、装置をコンパクト化し、かつ
未燃ガスの発生を最小限に抑制することのできる排ガス
通路を一体化した流動層燃焼装置を提供することを課題
とする。
In a fluidized bed combustion apparatus, since the combustion gas generated in the fluidized bed contains unburned gas and substances, the combustion gas is mixed with secondary air in a combustion chamber adjacent to the upper part to maintain a certain level. It is necessary to maintain the residence time to complete the combustion, and therefore, the height of the combustion furnace is increased in order to secure a predetermined residence time, and as a result, the waste heat boiler located at the subsequent stage is supported. Either raise the mount or
Alternatively, the combustion exhaust gas had to be guided downward by a duct, and a structurally useless surface was observed. SUMMARY OF THE INVENTION Accordingly, an object of the present invention is to provide a fluidized bed combustion apparatus which solves the above-mentioned disadvantages, makes the apparatus compact, and integrates an exhaust gas passage capable of minimizing generation of unburned gas. And

【0005】[0005]

【課題を解決するための手段】上記課題を解決するため
に、本発明では、焼却物を流動層部で燃焼させ発生した
燃焼ガスを上部に隣接する燃焼室に導入し、該燃焼室で
二次空気と混合させ一定の滞留時間を保持させて燃焼を
完結させるように構成した流動燃焼装置において、前
記燃焼室に隣接して仕切壁を介して燃焼排ガス通路を該
燃焼室と一体に設け、該排ガス通路と燃焼室とは仕切壁
の上端で連絡する構造とし、前記仕切壁は、下部を燃焼
室側に向かって三角形状又は台形状に張り出した構造と
すると共に、前記燃焼室の仕切壁に対向した炉壁には、
複数の二次空気ノズルを吹き出し方向を斜め下方の流動
層部に向けて設けられており、また、前記仕切壁には、
上端部分に複数の二次空気ノズルが上部燃焼室側に斜め
下方へ向けて配置されていることとしたものである。
In order to solve the above-mentioned problems, in the present invention, a combustion gas generated by burning an incinerated material in a fluidized bed portion is introduced into a combustion chamber adjacent to the upper portion, and the combustion gas is removed by the combustion chamber. In a fluidized bed combustion apparatus configured to complete combustion by mixing with the next air and maintaining a certain residence time, a combustion exhaust gas passage is provided integrally with the combustion chamber via a partition wall adjacent to the combustion chamber. The exhaust gas passage and the combustion chamber are connected at an upper end of a partition wall, and the partition wall has a lower portion burning.
With a structure that protrudes in a triangular or trapezoidal shape toward the room side
And at the furnace wall facing the partition wall of the combustion chamber,
Flows obliquely downward from multiple secondary air nozzles
It is provided facing the layer portion, and the partition wall has
Multiple secondary air nozzles at the upper end are inclined toward the upper combustion chamber
It is to be arranged downward .

【0006】そして、前記流動燃焼装置において、仕
切壁は、水管で構成され、かつ耐火材で被覆することも
でき、また、前記仕切壁には、仕切壁に対向する炉壁か
ら燃焼室を縦断して該炉壁と仕切壁を連結しあるいはそ
のまま延長して排ガス通路の側壁も連結する1以上の梁
を設置することもできる。
[0006] In the fluidized bed combustion apparatus, specification <br/> Setsukabe is composed of a water pipe, and can also be coated with a refractory material, also on the partition wall, the furnace facing the partition wall It is also possible to install one or more beams connecting the furnace wall and the partition wall by traversing the combustion chamber from the wall or extending the furnace wall and the partition wall and connecting the side wall of the exhaust gas passage.

【0007】[0007]

【作用】本発明によれば、燃焼炉内部に燃焼排ガス通路
を燃焼炉と一体になるように組み込み、かつ該通路と燃
焼室を隔てる仕切壁を利用して燃焼室における燃焼ガス
の整流を行うようにすることにより、燃焼炉からの燃焼
排ガス出口位置を適切な位置まで下げることが可能とな
る。また、該仕切り壁下部に張り出し部を設け、かつ二
次空気の吹き込みノズルを、該仕切り壁に相対する燃焼
室前壁から、流動層部に向かって吹き出すように配置
し、別の二次空気ノズルを該仕切り壁上部に燃焼室側斜
め下方に向けて吹き出すように配置することにより、前
壁に配置したノズルから噴出した二次空気は前壁に沿う
ように降下し、上昇してきた燃焼ガスと衝突混合した
後、今度は仕切り壁下の張り出し部に沿って上昇し、結
果的に燃焼室内に垂直旋回流を発生させるようにして二
次空気と燃焼ガスの攪拌混合を促進させ、かつ、仕切り
壁の張り出し部で燃焼ガス流路が絞られ、流速を上げた
ところへ、仕切り壁上部に形成したもう一つの二次空気
ノズル群から該張り出し部に向けて斜め下方へ吹き出さ
れた二次空気は、張り出し部上面を高速で流れたあと、
張り出し部先端で下方から吹き上げてくる燃焼ガス流れ
に衝突する。
According to the present invention, the flue gas passage is incorporated in the combustion furnace so as to be integral with the combustion furnace, and the combustion gas in the combustion chamber is rectified by using a partition wall separating the passage from the combustion chamber. By doing so, it becomes possible to lower the position of the outlet of the combustion exhaust gas from the combustion furnace to an appropriate position. Further, an overhanging portion is provided below the partition wall, and a secondary air blowing nozzle is disposed so as to blow out from the front wall of the combustion chamber facing the partition wall toward the fluidized bed portion , and another secondary air is provided. By arranging the nozzle on the upper part of the partition wall so as to blow diagonally downward on the combustion chamber side, the secondary air ejected from the nozzle arranged on the front wall descends along the front wall, and the rising combustion gas After collision and mixing, this time it rises along the overhang under the partition wall, thereby generating a vertical swirling flow in the combustion chamber to promote agitation and mixing of the secondary air and the combustion gas, and The secondary gas blown obliquely downward from the other secondary air nozzle group formed at the upper part of the partition wall to the place where the combustion gas flow path is narrowed and the flow velocity is increased at the overhang part of the partition wall toward the overhang part Air overhang After flowing through the top at high speed,
The tip of the overhang collides with the combustion gas flow blown up from below.

【0008】それによって、激しい攪拌混合を引き起こ
し、かつ上部燃焼室内で再び旋回流を発生させることに
よって、燃焼室容積を最大限に活用しつつ燃焼し、さら
には仕切り壁上部を越えて燃焼排ガス通路に流入する際
には燃焼ガス流が反転することにより、該燃焼ガス流の
有する運動エネルギーを利用してさらに混合度を高め、
充分に燃焼したあと該燃焼排ガス通路より外部へ排出す
るため、完全燃焼の度合いが高く、未燃ガスや未燃物質
の発生を最小限に抑制するものである。また仕切り壁の
補強部材として燃焼室前壁から仕切り壁に向い、ガス流
れ方向に沿って内部が中空で通常空冷されており耐火材
等で被覆されているような単数、もしくは複数の梁を渡
す場合は、燃焼ガス流が該梁により流れに対して幅方向
に分断され梁を通過した後再び衝突集合することによ
り、それが更に攪拌混合効果を高め未燃ガスと酸素との
燃焼反応を、急速かつ確実に進行させ、未燃ガスの排出
を最小限に抑えることが可能である。
[0008] This causes vigorous stirring and mixing and generates a swirling flow again in the upper combustion chamber, so that combustion is performed while making the most of the volume of the combustion chamber, and furthermore, the flue gas passage over the upper part of the partition wall. When flowing into the combustion gas flow is reversed, utilizing the kinetic energy of the combustion gas flow to further increase the degree of mixing,
After sufficient combustion, the exhaust gas is discharged to the outside through the flue gas passage. Therefore, the degree of complete combustion is high, and the generation of unburned gas and unburned substances is suppressed to a minimum. Also, as a reinforcing member for the partition wall, pass one or more beams from the front wall of the combustion chamber to the partition wall, the inside of which is generally air-cooled and covered with a refractory material or the like along the gas flow direction. In this case, the combustion gas flow is divided by the beam in the width direction with respect to the flow, and after the beam passes through the beam, they collide again, thereby further enhancing the stirring and mixing effect, and the combustion reaction between the unburned gas and oxygen, It is possible to proceed quickly and reliably and to minimize the emission of unburned gas.

【0009】[0009]

【実施例】以下、本発明を図面を用いて具体的に説明す
参考 例1先ず 、本発明の基礎となった装置を図で説明する。図1
は図6における燃焼炉に燃焼排ガス通路を組み込んだも
のであり、図1における燃焼排ガス通路17は、炉壁2
によって構成される燃焼炉1の中に一体となって組み込
まれており、燃焼室3とは仕切壁16によって仕切られ
ている。該仕切り壁16は燃焼ガスの流れに対して直角
方向に横断して、左右の炉壁2と連結するように構成さ
れており、該仕切り壁16上部で燃焼室3と燃焼排ガス
通路17が連絡している。該仕切り壁16は通常、中空
の部材で構成され外面は耐火材で被覆されており、中空
部分21を空気等が流れることにより、冷却効果を与え
ている。これによって、燃焼排ガス出口18を適切な位
置まで下げることが可能となることから、廃熱ボイラの
設置位置も低くなり、架構重量の低減等に寄与する。ま
た燃焼ガスが燃焼室3から燃焼排ガス通路17へ流入す
る際に仕切り壁16上部で燃焼排ガス流が反転すること
によりガス流自身の持つ運動エネルギーによって燃焼ガ
スと二次空気との十分な混合により燃焼が促進され、そ
の結果未燃ガスの排出が抑制される。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be specifically described below with reference to the drawings . Reference Example 1 First , an apparatus on which the present invention is based will be described with reference to the drawings. FIG.
6 shows a combustion furnace in which a combustion exhaust gas passage is incorporated in the combustion furnace shown in FIG. 6, and a combustion exhaust gas passage 17 shown in FIG.
, And is separated from the combustion chamber 3 by a partition wall 16. The partition wall 16 is configured to connect to the left and right furnace walls 2 in a direction perpendicular to the flow of the combustion gas and to connect the combustion chamber 3 and the flue gas passage 17 at the upper part of the partition wall 16. doing. The partition wall 16 is usually formed of a hollow member, and its outer surface is covered with a refractory material, and a cooling effect is given by flowing air or the like through the hollow portion 21. As a result, the combustion exhaust gas outlet 18 can be lowered to an appropriate position, so that the installation position of the waste heat boiler is also lowered, which contributes to a reduction in frame weight and the like. Further, when the combustion gas flows from the combustion chamber 3 into the combustion exhaust gas passage 17, the combustion exhaust gas flow is reversed at the upper part of the partition wall 16, so that the kinetic energy of the gas flow itself allows the combustion gas and the secondary air to be sufficiently mixed. Combustion is promoted, and as a result, emission of unburned gas is suppressed.

【0010】しかしながら図1における燃焼炉1のよう
な構造の場合、流動層部4から出た燃焼ガスは燃焼室3
において仕切り壁16の近傍に偏って流れ、ノズル9か
らの二次空気の吹き込みにもかかわらず、該二次空気と
の混合が不十分な状態のまま、仕切り壁16の上部から
燃焼排ガス通路17に流入する可能性も有り得るが、そ
の場合には、図2のように構成することが効果的であ
る。すなわち、燃焼室3と燃焼排ガス通路17を隔てる
仕切り壁16の下部に、燃焼室に向かって三角形もしく
は台形の形をなす張り出し部20を設け、それによって
燃焼室を実質的に下部燃焼室3aと上部燃焼室3bとに
分ける。一方、二次空気ノズルは燃焼炉1の前壁下部の
傾斜に沿って斜め下方、すなわち流動層部4に向けて噴
出するように配置され、噴出した二次空気は下部燃焼室
の下方において、上昇してくる燃焼ガスと衝突混合し燃
焼の促進に寄与しつつ、燃焼ガスは張り出し部20の下
面の傾斜に沿って斜め上方に吹き上がり、結果として下
部燃焼室3a内において前壁から流動層に向い、次に反
転して張り出し部20の下面に沿って吹き上がる旋回流
が生ずることになり、燃焼ガスと酸素とのより効果的な
混合が実現され、かつ仕切り壁16に沿って上部連絡口
から燃焼排ガス通路へ流れる短絡した偏流を防止できる
ことから上部燃焼室3bにおいて十分な燃焼を行うこと
が可能である。
However, in the case of a structure such as the combustion furnace 1 shown in FIG.
Flows in the vicinity of the partition wall 16, and despite the blowing of the secondary air from the nozzle 9, the combustion exhaust gas passage 17 from the upper part of the partition wall 16 with insufficient mixing with the secondary air. However, in such a case, the configuration as shown in FIG. 2 is effective. That is, a projection 20 having a triangular or trapezoidal shape is provided at a lower portion of the partition wall 16 separating the combustion chamber 3 and the flue gas passage 17 toward the combustion chamber, thereby substantially dividing the combustion chamber into the lower combustion chamber 3a. And the upper combustion chamber 3b. On the other hand, the secondary air nozzle is disposed obliquely downward along the inclination of the lower portion of the front wall of the combustion furnace 1, that is, so as to be ejected toward the fluidized bed portion 4, and the ejected secondary air is provided below the lower combustion chamber. The combustion gas blows up obliquely upward along the slope of the lower surface of the overhang portion 20 while colliding and mixing with the rising combustion gas, thereby contributing to the promotion of combustion. As a result, the fluidized bed flows from the front wall in the lower combustion chamber 3a. , And then swirl to reverse and blow up along the underside of the overhang 20 to achieve more effective mixing of the combustion gas and oxygen, and to communicate with the upper portion along the partition 16. Since short-circuited drift flowing from the mouth to the flue gas passage can be prevented, sufficient combustion can be performed in the upper combustion chamber 3b.

【0011】実施例 図3は、本発明の燃焼装置の一例を示す説明図である。
図3では、図2の燃焼室3と燃焼排ガス通路17を隔て
る仕切り壁16の下部に、燃焼室に向かって三角形もし
くは台形の形をなす張り出し部20を設けて燃焼室を実
質的に下部燃焼室3aと上部燃焼室3bとに分け、二次
空気ノズルを燃焼炉1の前壁下部の傾斜に沿って斜め下
方、すなわち流動層部4に向けて噴出するように配置す
ると共に、上部燃焼室3bにおいても.下部燃焼室とお
なじく、旋回流を発生させるように構成し、図2の効果
に加えて、より効果的な燃焼を行うように構成した実施
例である。即ち、二次空気の導入に関して前壁に設けた
二次空気ノズル9だけでなく、中空構造で耐火材で被覆
されている仕切り壁16を利用してその上端部分の中空
部を二次空気ダクト21aとし耐火材を通して上部燃焼
室3b側に斜め下方へ向けて複数の二次空気ノズル22
を配置し二次空気を噴出させるものである。噴出した二
次空気は仕切り壁16に沿って下方に流れ、さらに張り
出し部20の上面に沿って中心部に向きを変えるが、張
り出し部20の先端を出たところで下部燃焼室3a側か
ら張り出し部20下面に沿って上昇してきた燃焼ガス流
と激しく衝突したあと、双方のガス流れが混合しながら
前壁寄りを上昇するため、燃焼排ガス通路へ短絡するこ
ともなく、上部燃焼室内部容積を十分に利用して燃焼す
るため、未燃ガス、未燃物質の排出を最小限に抑制する
ものである。
Embodiment 1 FIG. 3 is an explanatory view showing an example of the combustion apparatus of the present invention.
In FIG. 3, the combustion chamber 3 of FIG.
At the bottom of the partition wall 16,
The combustion chamber is realized by providing an overhang 20 having a trapezoidal shape.
Qualitatively divided into lower combustion chamber 3a and upper combustion chamber 3b,
Attach the air nozzle obliquely downward along the inclination of the lower part of the front wall of the combustion furnace 1.
, That is, in such a manner as to be ejected toward the fluidized bed section 4.
And also in the upper combustion chamber 3b. Like the lower combustion chamber, and constructed so that to generate a swirling flow, the effect of 2
In addition to the above, the present embodiment is configured to perform more effective combustion. That is, regarding the introduction of the secondary air, not only the secondary air nozzle 9 provided on the front wall but also the partition wall 16 having a hollow structure and covered with a refractory material, and the hollow portion at the upper end portion is formed in the secondary air duct. 21a and a plurality of secondary air nozzles 22 obliquely downward toward the upper combustion chamber 3b through the refractory material.
And ejects secondary air. The ejected secondary air flows downward along the partition wall 16 and changes its direction to the center along the upper surface of the overhanging portion 20. When the secondary air exits the tip of the overhanging portion 20, it projects from the lower combustion chamber 3a side. 20 After violently colliding with the combustion gas flow that has risen along the lower surface, the two gas flows rise near the front wall while mixing, so there is no short circuit to the combustion exhaust gas passage, and the internal combustion chamber volume is sufficient. Therefore, the emission of unburned gas and unburned substances is minimized.

【0012】実施例 また図4は、より大型の燃焼炉になった場合、仕切り壁
16に対する補強及び燃焼ガスの攪拌混合をさらに促進
する必要性から、図3に示す燃焼炉にさらに工夫を加え
たものであり、前側の炉壁2から仕切り壁16の上端部
に向けて、すなわち燃焼ガスの流れ方向に沿って単数も
しくは複数の補強梁23を通すものである。この梁23
は仕切り壁16で止まっても、あるいは延長して燃焼排
ガス通路17を横切り、後側の炉壁まで到達してもよ
い。該梁23は中空構造で、外側は耐火材で被覆されて
おり、仕切り壁16の補強の役割を果たすと共に、図5
に断面a−aを示すように上部燃焼室3bにおいて燃焼
ガス流れを2つ、もしくはそれ以上に分流し、流速を上
げさらに梁23を通過した後激しく再混合する結果、そ
れまで縦方向にのみ旋回混合してきた燃焼ガスの流れに
対して、それとは直角方向への拡散、旋回、混合を行う
ことは、より一層の燃焼反応を促進するものであり、未
燃ガスや未燃物質排出量の抑制に大きく寄与するもので
ある。
Embodiment 2 FIG. 4 shows that in the case of a larger combustion furnace, the combustion furnace shown in FIG. 3 is further devised because it is necessary to reinforce the partition wall 16 and further promote stirring and mixing of the combustion gas. In addition, one or a plurality of reinforcing beams 23 are passed from the front furnace wall 2 toward the upper end of the partition wall 16, that is, along the flow direction of the combustion gas. This beam 23
May stop at the partition wall 16 or may extend and traverse the flue gas passage 17 to reach the furnace wall on the rear side. The beam 23 has a hollow structure, and the outer side is covered with a refractory material.
In the upper combustion chamber 3b, the combustion gas flow is divided into two or more in the upper combustion chamber 3b as shown in the cross section a, the flow velocity is increased, and the fuel gas is remixed vigorously after passing through the beam 23. Spreading, swirling, and mixing in a direction perpendicular to the swirling and mixing combustion gas flow promotes a further combustion reaction, and reduces the amount of unburned gas and unburned substance emissions. This greatly contributes to suppression.

【0013】すなわち、図4において再度全体説明を行
うと、被焼却物、あるいは燃料は投入口8bから炉内へ
供給される。一方燃焼用一次空気は流動空気7として炉
下より供給され、ウィンドボックス6に入り、空気分散
板5を通過して流動層部4を流動化し被焼却物あるいは
燃料を燃焼する。揮発分や、未燃ガス、未燃物質を含む
燃焼ガスは流動層部4から出て下部燃焼室3aに入る
が、前壁に斜め下向きに配置された二次空気ノズル9か
ら吹き込まれ前壁の傾斜に沿うようにして流下してきた
二次空気と激しく衝突混合しながら、張り出し部20の
下面に沿って上昇し、さらに仕切り壁16上部に設けら
れた別の二次空気ノズル22から上部燃焼室側に斜め下
方へ向けて吹き出され、張り出し部20の上面に沿って
流下してきた二次空気と張り出し部20の先端部で、出
会い頭に激しく衝突混合し、その後上部燃焼室3b内部
を渦巻くようにして燃焼しながら上昇し、さらに上部で
梁23によって分断、再混合されて一層燃焼の度合を高
めることになり未燃ガスの排出量を最小限に押えつつ、
燃焼排ガス通路17へと流入し外部へ導出するものであ
る。なお、上記実施例において、燃焼炉1は、鉄皮と耐
火材の組合せ又はボイラ水管と耐火材の組合せ等で構成
することができる。
That is, if the whole description is given again in FIG. 4, the incineration material or fuel is supplied from the inlet 8b into the furnace. On the other hand, the primary air for combustion is supplied from the lower part of the furnace as flowing air 7, enters the wind box 6, passes through the air dispersion plate 5, fluidizes the fluidized bed portion 4, and burns the incineration material or the fuel. Combustion gas containing volatile matter, unburned gas, and unburned matter exits the fluidized bed portion 4 and enters the lower combustion chamber 3a, but is blown from the secondary air nozzle 9 obliquely downwardly directed to the front wall to blow the front wall. While rising and falling along the lower surface of the overhang portion 20 while violently colliding and mixing with the secondary air flowing down along the inclination of The secondary air that has been blown obliquely downward toward the chamber side and has flowed down along the upper surface of the overhanging portion 20 and violently impacts and mixes at the tip of the overhanging portion 20 at the tip of the overhanging portion 20 and then swirls inside the upper combustion chamber 3b. As it rises while burning, it is further separated and remixed by the beams 23 at the upper part, further increasing the degree of combustion, and minimizing the emission of unburned gas,
It flows into the flue gas passage 17 and is led out. In the above embodiment, the combustion furnace 1 can be constituted by a combination of a steel shell and a refractory material or a combination of a boiler water pipe and a refractory material.

【0014】[0014]

【発明の効果】以上の説明で明らかなように本発明によ
る効果はつぎの通りである。 1)燃焼排ガス通路を燃焼炉に組み込むことにより燃焼
排ガス出口の位置を任意に設定することが可能となり廃
熱ボイラ取り付け位置を適切な位置まで下げることが可
能となり建設費の低減に寄与する。 2)燃焼排ガス通路を燃焼室を隔てる仕切り壁を利用し
てその下部に張り出し部を設け、さらに前壁側と仕切り
壁上部の二次空気ノズルにより燃焼室内部に旋回流を発
生させることにより燃焼室内部で、未燃ガスと二次空気
との混合が効果的に行われる結果、未燃ガスの排出量を
下げ、あるいは二次空気量を減らすことが可能となるほ
か、燃焼室の温度を高温に維持できるという効果もあ
り、高温で分解するような有害物質の抑制にも効果的で
ある。
As apparent from the above description, the effects of the present invention are as follows. 1) By incorporating the flue gas passage into the combustion furnace, the position of the flue gas outlet can be set arbitrarily, and the mounting position of the waste heat boiler can be lowered to an appropriate position, contributing to a reduction in construction costs. 2) Combustion by using a partition wall that separates the combustion chamber from the flue gas passage, providing a projecting portion below the partition wall, and generating a swirling flow inside the combustion chamber by the secondary air nozzles on the front wall side and the upper part of the partition wall. As a result of effective mixing of the unburned gas and the secondary air inside the room, it is possible to reduce the amount of unburned gas discharged or the amount of secondary air, and to reduce the temperature of the combustion chamber. It has the effect of being able to be maintained at a high temperature, and is also effective in controlling harmful substances that decompose at high temperatures.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の基礎となった装置の一例を示す概略断
面図である。
FIG. 1 is a schematic sectional view showing an example of an apparatus on which the present invention is based .

【図2】本発明の基礎となった装置の他の例を示す概略
断面説明図である。
FIG. 2 is a schematic sectional view showing another example of the device on which the present invention is based .

【図3】本発明の装置の一例を示す概略断面説明図であ
る。
FIG. 3 is a schematic sectional explanatory view showing an example of the apparatus of the present invention.

【図4】本発明の装置のの例を示す概略断面説明図で
ある。
FIG. 4 is a schematic sectional explanatory view showing another example of the device of the present invention.

【図5】図4のa−a断面説明図である。FIG. 5 is an explanatory sectional view taken along the line aa in FIG. 4;

【図6】従来の流動層燃焼装置を示す概略説明図であ
る。
FIG. 6 is a schematic explanatory view showing a conventional fluidized bed combustion device.

【符号の説明】[Explanation of symbols]

1:燃焼炉、2:炉壁、3:燃焼室、4:流動層部、
5:空気分散板、6:ウィンドボックス、7:流動空
気、8a:スクリューフィーダ、8b:被焼却物供給
口、9:二次空気ノズル、10:出口ダクト、16:仕
切壁、17:燃焼排ガス通路、18:排ガス出口、1
9:排ガス、20:張り出し部、21:中空部分、2
2:二次空気ノズル、23:補強梁。
1: combustion furnace, 2: furnace wall, 3: combustion chamber, 4: fluidized bed,
5: air dispersion plate, 6: wind box, 7: flowing air, 8a: screw feeder, 8b: incineration material supply port, 9: secondary air nozzle, 10: outlet duct, 16: partition wall, 17: combustion exhaust gas Passage, 18: exhaust gas outlet, 1
9: exhaust gas, 20: overhang, 21: hollow part, 2
2: Secondary air nozzle, 23: Reinforcement beam.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 佐藤 啓一 東京都大田区羽田旭町11番1号 株式会 社荏原製作所内 (56)参考文献 特開 昭61−17810(JP,A) 特公 昭34−3689(JP,B1) ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Keiichi Sato 11-1 Haneda Asahimachi, Ota-ku, Tokyo Inside Ebara Works Co., Ltd. (56) References JP-A-61-17810 (JP, A) Akira Tokubo 34-3689 (JP, B1)

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 焼却物を流動層部で燃焼させ発生した燃
焼ガスを上部に隣接する燃焼室に導入し、該燃焼室で二
次空気と混合させ一定の滞留時間を保持させて燃焼を完
結させるように構成した流動燃焼装置において、前記
燃焼室に隣接して仕切壁を介して燃焼排ガス通路を該燃
焼室と一体に設け、該排ガス通路と燃焼室とは仕切壁の
上端で連絡する構造とし、前記仕切壁は、下部を燃焼室
側に向かって三角形状又は台形状に張り出した構造とす
ると共に、前記燃焼室の仕切壁に対向した炉壁には、複
数の二次空気ノズルが吹き出し方向を斜め下方の流動層
部に向けて設けられており、また、前記仕切壁には、上
端部分に複数の二次空気ノズルが上部燃焼室側に斜め下
方へ向けて配置されていることを特徴とする流動燃焼
装置。
1. Combustion gas generated by burning incinerated material in a fluidized bed is introduced into a combustion chamber adjacent to the upper part, mixed with secondary air in the combustion chamber to maintain a certain residence time to complete combustion. In the fluidized bed combustion apparatus configured to perform the combustion, a flue gas passage is provided integrally with the combustion chamber via a partition wall adjacent to the combustion chamber, and the flue gas passage and the combustion chamber communicate with each other at an upper end of the partition wall. The partition wall has a lower part in a combustion chamber.
Triangular or trapezoidal structure
And the furnace wall facing the partition wall of the combustion chamber has multiple
Number of secondary air nozzles obliquely blow down the fluidized bed
And the partition wall has an upper part.
Multiple secondary air nozzles at the end diagonally below the upper combustion chamber
Fluidized bed combustion device, characterized in that the device is arranged in a direction to the direction .
【請求項2】 前記仕切壁には、仕切壁に対向する炉壁
から燃焼室を縦断して該炉壁と仕切壁を連結しあるいは
そのまま延長して排ガス通路の側壁も連結する1以上の
梁を設置したことを特徴とする請求項記載の流動
焼装置。
2. The partition wall has at least one beam that longitudinally traverses a combustion chamber from a furnace wall facing the partition wall and connects the furnace wall and the partition wall or extends the same and also connects a side wall of an exhaust gas passage. The fluidized- bed combustion apparatus according to claim 1, wherein the apparatus is installed.
【請求項3】 前記仕切壁は、水管で構成され、かつ耐
火材で被覆されていることを特徴とする請求項1又は2
記載の流動層燃焼装置。
Wherein said partition wall, according to claim 1 or 2 consists of water pipes, and characterized by a Turkey covered with a refractory material
A fluidized bed combustion device as described.
JP4032973A 1992-01-24 1992-01-24 Fluidized bed combustion device with integrated exhaust gas passage Expired - Fee Related JP2649626B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4032973A JP2649626B2 (en) 1992-01-24 1992-01-24 Fluidized bed combustion device with integrated exhaust gas passage

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4032973A JP2649626B2 (en) 1992-01-24 1992-01-24 Fluidized bed combustion device with integrated exhaust gas passage

Publications (2)

Publication Number Publication Date
JPH05203132A JPH05203132A (en) 1993-08-10
JP2649626B2 true JP2649626B2 (en) 1997-09-03

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP4032973A Expired - Fee Related JP2649626B2 (en) 1992-01-24 1992-01-24 Fluidized bed combustion device with integrated exhaust gas passage

Country Status (1)

Country Link
JP (1) JP2649626B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102017008123A1 (en) * 2017-08-30 2019-02-28 Martin GmbH für Umwelt- und Energietechnik Furnace and method for operating a furnace
JP7137333B2 (en) * 2018-03-29 2022-09-14 川崎重工業株式会社 waste incinerator
JP7027227B2 (en) * 2018-03-30 2022-03-01 川崎重工業株式会社 Waste incinerator

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5992311U (en) * 1982-12-09 1984-06-22 川重冷熱工業株式会社 Fluidized bed boiler combustion chamber structure
JPS6117810A (en) * 1984-07-04 1986-01-25 Babcock Hitachi Kk Multi-stage fluidized bed layer boiler
JPH02113949U (en) * 1989-02-27 1990-09-12
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Also Published As

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