JPH10281432A - Gas straightening structure of secondary combustion chamber for incinerating furnace - Google Patents

Gas straightening structure of secondary combustion chamber for incinerating furnace

Info

Publication number
JPH10281432A
JPH10281432A JP8311797A JP8311797A JPH10281432A JP H10281432 A JPH10281432 A JP H10281432A JP 8311797 A JP8311797 A JP 8311797A JP 8311797 A JP8311797 A JP 8311797A JP H10281432 A JPH10281432 A JP H10281432A
Authority
JP
Japan
Prior art keywords
combustion chamber
gas
fluid supply
combustion air
secondary combustion
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.)
Withdrawn
Application number
JP8311797A
Other languages
Japanese (ja)
Inventor
Junichi Kamiya
順一 上谷
Toru Izumiya
亨 泉屋
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.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP8311797A priority Critical patent/JPH10281432A/en
Publication of JPH10281432A publication Critical patent/JPH10281432A/en
Withdrawn legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To stably ensure a mixing agitating efficiency by disposing a plurality of liquid supply tubes in parallel or lattice state in a secondary combustion chamber, and diffusing combustion air to unburnt gas rising from a combustion air diffusing hole at a downstream of the supply tube. SOLUTION: A plurality of fluid supply tubes 2 are horizontally disposed at an interval in parallel across a secondary combustion chamber 1 to form parallel gas channels 3. Gas generated in a fluidized bed (primary combustion chamber) is exhausted from a top of a furnace via the channels 3 of the tubes 2. Unburnt gas of the rising gas is burnt while bearing mixed with combustion air diffused down from combustion air holes 4 of a liquid supply tube 2, combustion gas is uniformly distributed via the channels 3 of the tubes 2 disposed in parallel, and exhausted from the top without drift. Thus, mixing agitating efficiency of the unburnt gas can be stably held, and hence combustibility is improved.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、都市ごみ、産業廃
棄物を焼却処理する焼却炉の2次燃焼室のガス整流構造
に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a gas rectification structure for a secondary combustion chamber of an incinerator for incinerating municipal waste and industrial waste.

【0002】[0002]

【従来の技術】廃棄物の焼却処理に用いられている焼却
炉の一例として流動床焼却炉がある。流動床式焼却炉は
炉床部に熱砂の流動層(1次燃焼室)を形成し、焼却炉
に装入されたごみを流動層内に分散させ、流動層の下方
から第1送風機により供給される燃焼用空気により燃焼
させる。
2. Description of the Related Art A fluidized bed incinerator is an example of an incinerator used for incineration of waste. The fluidized bed incinerator forms a fluidized bed (primary combustion chamber) of hot sand on the hearth, disperses the refuse charged in the incinerator in the fluidized bed, and supplies it from below the fluidized bed with a first blower. The combustion air is used for combustion.

【0003】流動層内で発生したガスは炉頂から炉外に
排出されるが、未燃ガスは重複焼却炉上部のフリーボー
ド(2次燃焼室)において第2送風機により供給される
燃焼用空気により2次燃焼させた後、炉外に排出される
ようになっている。
The gas generated in the fluidized bed is discharged from the furnace top to the outside of the furnace, while the unburned gas is supplied to the free board (secondary combustion chamber) above the double incinerator by the combustion air supplied by the second blower. After the secondary combustion, the fuel is discharged outside the furnace.

【0004】ところが、2次燃焼室内のガスの流速がき
わめて遅いために、対流時間が長くても未燃ガスと燃焼
用空気との混合が充分に行われず、未燃ガスが完全に2
次燃焼しないという問題があった。
[0004] However, since the flow velocity of the gas in the secondary combustion chamber is extremely low, even if the convection time is long, the unburned gas and the combustion air are not sufficiently mixed, and the unburned gas is completely removed.
There was a problem that it would not burn next.

【0005】そこで、未燃ガスと燃焼用空気との撹拌混
合効率を上げるため、2次燃焼室内に邪魔板を設けた流
動床式焼却炉が特開平1−225802号公報に開示さ
れている。
Japanese Patent Laid-Open Publication No. 1-225802 discloses a fluidized bed incinerator in which a baffle plate is provided in a secondary combustion chamber in order to increase the stirring and mixing efficiency of unburned gas and combustion air.

【0006】図3は従来の2次燃焼室内に邪魔板を設け
た流動床式焼却炉の断面図で、流動床式焼却炉の2次燃
焼室1に邪魔板7を設けたもので、第1送風機8により
供給された燃焼用空気で流動化された流動層9において
可燃性ごみの燃焼により発生した未燃ガスは、そのガス
流れが邪魔板7によって分割された後、再度合流するこ
とによって、2次燃焼室内に第2送風機10により供給
される燃焼用空気と激しく混合撹拌されて、完全に2次
燃焼し、炉外へ排出される。
FIG. 3 is a cross-sectional view of a conventional fluidized bed incinerator having a baffle plate in a secondary combustion chamber, in which a baffle plate 7 is provided in a secondary combustion chamber 1 of a fluidized bed incinerator. 1 The unburned gas generated by the combustion of combustible waste in the fluidized bed 9 fluidized by the combustion air supplied by the blower 8 is reunited after the gas flow is divided by the baffle plate 7 The mixture is vigorously mixed and agitated with the combustion air supplied by the second blower 10 into the secondary combustion chamber, completely secondary-combusted, and discharged out of the furnace.

【0007】[0007]

【発明が解決しようとする課題】前記の邪魔板を設けた
流動床式焼却炉では、ガス流れを邪魔板の両側へ大きく
分岐させているため、邪魔板通過後のガス偏流が大き
く、均一な燃焼が得られにくい。
In the fluidized bed incinerator provided with the baffle plate, since the gas flow is largely branched to both sides of the baffle plate, the gas drift after passing through the baffle plate is large and uniform. It is difficult to obtain combustion.

【0008】本発明は、2次燃焼室内でのガス偏流を防
止して混合撹拌効率を安定的に確保できる整流構造を設
けた焼却炉の2次燃焼室のガス整流構造を提供するもの
である。
[0008] The present invention provides a gas rectification structure of a secondary combustion chamber of an incinerator provided with a rectification structure capable of preventing gas drift in the secondary combustion chamber and stably ensuring mixing and stirring efficiency. .

【0009】[0009]

【課題を解決するための手段】本発明の焼却炉の2次燃
焼室のガス整流構造は、焼却炉の2次燃焼室を水平に横
切って平行に、または格子状に複数の流体供給管を配置
し、流体供給管には下方に燃焼用空気を吹き出す複数の
燃焼用空気吹出孔を一定の間隔で設けたことを特徴とす
る。
The gas rectifying structure of the secondary combustion chamber of the incinerator according to the present invention comprises a plurality of fluid supply pipes which are horizontally parallel to the secondary combustion chamber of the incinerator or in a grid. The fluid supply pipe is provided with a plurality of combustion air blowing holes for blowing combustion air downward at regular intervals.

【0010】[0010]

【発明の実施の形態】図1は本発明のガス整流構造の第
1実施例を示し、図1−(a)は平行に流体供給管を配
置した状態を示す一部切欠き断面の斜視図、図1−
(b)は縦断面図である。
FIG. 1 shows a first embodiment of a gas rectifying structure according to the present invention, and FIG. 1 (a) is a partially cutaway perspective view showing a state in which fluid supply pipes are arranged in parallel. Figure 1
(B) is a longitudinal sectional view.

【0011】2次燃焼室1を水平に横切って複数の流体
供給管2を平行に間隔をおいて水平に配置して平行なガ
ス流路3を形成する。流体供給管2の下側には管軸方向
に燃焼用空気を吹き出す燃焼用空気吹出孔4を一定間隔
で設ける。流体供給管2の材質は、耐熱性が要求される
ので、セラミックス等の耐熱材料を用いる。
A plurality of fluid supply pipes 2 are horizontally arranged across the secondary combustion chamber 1 at parallel intervals to form a parallel gas flow path 3. On the lower side of the fluid supply pipe 2, combustion air blow holes 4 for blowing combustion air in the pipe axis direction are provided at regular intervals. Since the fluid supply pipe 2 is required to have heat resistance, a heat resistant material such as ceramics is used.

【0012】前記構成において、流動層内(1次燃焼室
内)で発生し上昇するガスは、流体供給管2のガス流路
3を通って炉頂から排出されるが、上昇するガスのう
ち、未燃ガスは流体供給管2の燃焼用空気吹出孔4から
下方に吹き出す燃焼空気で混合されながら燃焼し、燃焼
ガスは平行に配置された流体供給管2のガス流路3を通
って偏流することなく上昇し、炉頂から排出される。し
たがって、上昇するガスは平行に配置された流体供給管
2により均一に分流され偏流することなく上昇するの
で、未燃ガスの混合撹拌効率を安定的に保持することが
できる。
In the above structure, the gas generated and rising in the fluidized bed (primary combustion chamber) is discharged from the furnace top through the gas passage 3 of the fluid supply pipe 2. The unburned gas burns while being mixed with the combustion air blown downward from the combustion air outlet 4 of the fluid supply pipe 2, and the combustion gas drifts through the gas passage 3 of the fluid supply pipe 2 arranged in parallel. Rises without being discharged from the furnace top. Therefore, the rising gas is uniformly diverted by the fluid supply pipes 2 arranged in parallel and rises without drifting, so that the mixing and stirring efficiency of the unburned gas can be stably maintained.

【0013】また、燃焼用空気吹出孔4から下方に吹き
出す燃焼空気が流体供給管を冷却するため、流体供給管
自体へのクリンカやダスト付着を防止することができ
る。
Further, since the combustion air blown downward from the combustion air outlet 4 cools the fluid supply pipe, it is possible to prevent the clinker and dust from adhering to the fluid supply pipe itself.

【0014】図2は本発明のガス整流構造の第2実施例
を示し、図2−(a)は格子状に流体供給管を配置した
状態を示す一部切欠き断面の斜視図、図2−(b)は縦
断面図である。
FIG. 2 shows a second embodiment of the gas rectification structure of the present invention, and FIG. 2A is a perspective view of a partially cut-away section showing a state in which fluid supply pipes are arranged in a grid. -(B) is a longitudinal sectional view.

【0015】前記第1実施例と同じく、複数の流体供給
管2を平行に間隔をおいて2次燃焼室内に水平に配置
し、流体供給管2の下側には管軸方向に燃焼用空気を吹
き出す燃焼空気吹出孔4を一定間隔で設ける。
As in the first embodiment, a plurality of fluid supply pipes 2 are arranged horizontally in parallel in the secondary combustion chamber at intervals, and combustion air is provided below the fluid supply pipes 2 in the pipe axial direction. Are provided at regular intervals.

【0016】さらに、前記平行に配置した流体供給管2
の上側に直交して複数の流体供給管5を平行に間隔をお
いて配置し、上側の流体供給管5と下側の流体供給管2
とで格子状のガス流路6を形成する。各流体供給管2,
5の下側には管軸方向に燃焼用空気を吹き出す燃焼空気
用吹出孔4を一定間隔で設ける。
Further, the fluid supply pipes 2 arranged in parallel with each other
A plurality of fluid supply pipes 5 are arranged in parallel at a right angle to the upper side of the fluid supply pipe 5, and the upper fluid supply pipe 5 and the lower fluid supply pipe 2
Thus, a lattice-shaped gas flow path 6 is formed. Each fluid supply pipe 2,
5, combustion air blowout holes 4 for blowing out combustion air in the tube axis direction are provided at regular intervals.

【0017】前記構成において、流動層内(1次燃焼室
内)で発生し上昇するガスは、格子状に配置された流体
供給管2,5のガス流路6を通って炉頂から排出される
が、上昇するガスのうち、未燃ガスは格子状に配置され
た流体供給管2,5の燃焼用空気吹出孔4から下方に吹
き出す燃焼空気で混合されながら燃焼し、燃焼ガスは格
子状に配置された流体供給管2,5のガス流路6を通っ
て偏流することなく上昇し、炉頂から排出される。した
がって、上昇するガスは格子状に配置された流体供給管
2,5により均一に分流されて偏流することなく上昇す
るので、未燃ガスの混合撹拌効率を安定的に保持するこ
とができる。
In the above configuration, the gas generated and rising in the fluidized bed (primary combustion chamber) is discharged from the furnace top through the gas passages 6 of the fluid supply pipes 2 and 5 arranged in a grid. However, of the rising gas, the unburned gas burns while being mixed with the combustion air blown downward from the combustion air blowing holes 4 of the fluid supply pipes 2 and 5 arranged in a grid, and the combustion gas is formed in a grid. It rises without drifting through the gas flow path 6 of the disposed fluid supply pipes 2 and 5, and is discharged from the furnace top. Accordingly, the rising gas is uniformly diverted by the fluid supply pipes 2 and 5 arranged in a grid and rises without being drifted, so that the mixing and stirring efficiency of the unburned gas can be stably maintained.

【0018】また、第1実施例と同様に、燃焼用空気吹
出孔4から吹き出す燃焼空気による冷却効果により、流
体供給管自体へのクリンカやダスト付着を防止すること
ができる。なお、本実施例においては焼却炉の一例とし
て流動床焼却炉を上げて詳述したが、本願発明はこれに
限られることなく、下部に一次燃焼室、その上部に二次
燃焼室が配設された焼却炉であれば全てに適用可能であ
りストーカー炉、ロータリーキルン炉等幅広く適用さ
れ、同様な作用の効果を奏する。
Further, as in the first embodiment, the cooling effect of the combustion air blown out from the combustion air blow-out hole 4 can prevent the clinker and dust from adhering to the fluid supply pipe itself. In the present embodiment, a fluidized bed incinerator has been described as an example of an incinerator, but the present invention is not limited thereto, and a primary combustion chamber is provided at a lower portion, and a secondary combustion chamber is provided at an upper portion thereof. The incinerator can be applied to any incinerator, and is widely applied to stoker furnaces, rotary kiln furnaces, etc., and has the same effect.

【0019】[0019]

【発明の効果】複数の流体供給管を平行あるいは格子状
に2次燃焼室内に配置し、流体供給管の下側の燃焼空気
吹出孔から上昇する未燃ガスに燃焼用空気を吹き出すこ
とにより、混合撹拌を促進するとともに、上昇するガス
を複数の流体供給管により均一に分流されて偏流するこ
となく上昇するので、燃焼性が向上する。
According to the present invention, a plurality of fluid supply pipes are arranged in parallel or in a grid in the secondary combustion chamber, and the combustion air is blown out to the unburned gas rising from the combustion air outlet below the fluid supply pipes. The mixing and agitation is promoted, and the rising gas is uniformly diverted by the plurality of fluid supply pipes and rises without drifting, so that the combustibility is improved.

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

【図1】本発明のガス整流構造の第1実施例を示し、図
1−(a)は平行に流体供給管を配置した状態を示す一
部切欠き断面の斜視図、図1−(b)は縦断面図であ
る。
FIG. 1 shows a first embodiment of a gas rectification structure of the present invention, and FIG. 1- (a) is a partially cutaway perspective view showing a state where fluid supply pipes are arranged in parallel, and FIG. ) Is a longitudinal sectional view.

【図2】本発明のガス整流構造の第2実施例を示し、図
2−(a)は格子状に流体供給管を配置した状態を示す
一部切欠き断面の斜視図、図2−(b)は縦断面図であ
る。
FIG. 2 shows a second embodiment of the gas rectification structure of the present invention, and FIG. 2- (a) is a partially cutaway perspective view showing a state where fluid supply pipes are arranged in a grid, and FIG. b) is a longitudinal sectional view.

【図3】従来の燃焼室内に邪魔板を設けた流動床式焼却
炉の断面図である。
FIG. 3 is a cross-sectional view of a conventional fluidized bed incinerator provided with a baffle plate in a combustion chamber.

【符号の説明】[Explanation of symbols]

1 2次燃焼室 2 流体供給管 3 ガス流路 4 燃焼用空気吹出孔 5 上側の流体供給管 6 ガス流路 7 邪魔板 8 第1送風機 9 流動層(1次燃焼室) 10 第2送風機 DESCRIPTION OF SYMBOLS 1 Secondary combustion chamber 2 Fluid supply pipe 3 Gas flow path 4 Air supply hole for combustion 5 Upper fluid supply pipe 6 Gas flow path 7 Baffle plate 8 First blower 9 Fluidized bed (primary combustion chamber) 10 Second blower

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 下部に可燃物を燃焼させる1次燃焼室、
上部に前記1次燃焼室にて発生した未燃ガスを燃焼させ
る2次燃焼室を備えた焼却炉において、前記2次燃焼室
内を水平に横切って平行に複数の流体供給管を配置し、
流体供給管には下方に燃焼用空気を吹き出す複数の燃焼
用空気吹出孔を一定の間隔で設けたことを特徴とする焼
却炉の2次燃焼室のガス整流構造。
1. A primary combustion chamber for burning combustibles in a lower part.
In an incinerator having a secondary combustion chamber for burning unburned gas generated in the primary combustion chamber at an upper part, a plurality of fluid supply pipes are arranged in parallel across the secondary combustion chamber horizontally,
A gas rectifying structure for a secondary combustion chamber of an incinerator, wherein a plurality of combustion air outlets for blowing out combustion air are provided at predetermined intervals in a fluid supply pipe below.
【請求項2】 下部に可燃物を燃焼させる1次燃焼室、
上部に前記1次燃焼室にて発生した未燃ガスを燃焼させ
る2次燃焼室を備えた焼却炉において、前記2次燃焼室
内を水平に横切って格子状に複数の流体供給管を配置
し、流体供給管には下方に燃焼用空気を吹き出す複数の
燃焼用空気吹出孔を一定の間隔で設けたことを特徴とす
る流動床式焼却炉の燃焼室のガス整流構造。
2. A primary combustion chamber for burning combustibles in a lower portion,
In an incinerator provided with a secondary combustion chamber for burning unburned gas generated in the primary combustion chamber at an upper portion, a plurality of fluid supply pipes are arranged in a grid pattern horizontally across the secondary combustion chamber, A fluid rectifying structure for a combustion chamber of a fluidized bed incinerator, wherein a plurality of combustion air blow-off holes for blowing combustion air are provided below the fluid supply pipe at regular intervals.
JP8311797A 1997-04-01 1997-04-01 Gas straightening structure of secondary combustion chamber for incinerating furnace Withdrawn JPH10281432A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8311797A JPH10281432A (en) 1997-04-01 1997-04-01 Gas straightening structure of secondary combustion chamber for incinerating furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8311797A JPH10281432A (en) 1997-04-01 1997-04-01 Gas straightening structure of secondary combustion chamber for incinerating furnace

Publications (1)

Publication Number Publication Date
JPH10281432A true JPH10281432A (en) 1998-10-23

Family

ID=13793269

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8311797A Withdrawn JPH10281432A (en) 1997-04-01 1997-04-01 Gas straightening structure of secondary combustion chamber for incinerating furnace

Country Status (1)

Country Link
JP (1) JPH10281432A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018017423A (en) * 2016-07-26 2018-02-01 株式会社プランテック Secondary combustion air supply device of trash incinerator, and trash incineration device
CN108295764A (en) * 2018-04-19 2018-07-20 周仕祥 A kind of production calcium superphosphate fluorine removal reforming unit mixing device and mixing method

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018017423A (en) * 2016-07-26 2018-02-01 株式会社プランテック Secondary combustion air supply device of trash incinerator, and trash incineration device
CN108295764A (en) * 2018-04-19 2018-07-20 周仕祥 A kind of production calcium superphosphate fluorine removal reforming unit mixing device and mixing method
CN108295764B (en) * 2018-04-19 2024-01-23 周仕祥 Mixing device and mixing method for fluorine-removing conversion device for producing calcium superphosphate

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