JP2955068B2 - Fluidized bed combustion furnace - Google Patents

Fluidized bed combustion furnace

Info

Publication number
JP2955068B2
JP2955068B2 JP17242391A JP17242391A JP2955068B2 JP 2955068 B2 JP2955068 B2 JP 2955068B2 JP 17242391 A JP17242391 A JP 17242391A JP 17242391 A JP17242391 A JP 17242391A JP 2955068 B2 JP2955068 B2 JP 2955068B2
Authority
JP
Japan
Prior art keywords
fluidized bed
combustion furnace
heat transfer
transfer tube
foreign matter
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
JP17242391A
Other languages
Japanese (ja)
Other versions
JPH0518513A (en
Inventor
一二 山田
邦弘 井久保
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP17242391A priority Critical patent/JP2955068B2/en
Publication of JPH0518513A publication Critical patent/JPH0518513A/en
Application granted granted Critical
Publication of JP2955068B2 publication Critical patent/JP2955068B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Fluidized-Bed Combustion And Resonant Combustion (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】本発明は異物を含む燃料を使用す
る産業用流動層ボイラあるいはゴミ焼却炉等に適用され
る流動層燃焼炉に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a fluidized bed combustion furnace applied to an industrial fluidized bed boiler or a waste incinerator using a fuel containing foreign matter.

【0002】[0002]

【従来の技術】図4は従来の流動層燃焼炉の一例として
の廃タイヤ燃焼装置の断面図である。図において、1は
流動層燃焼炉、4は同燃焼炉の下部に設けられている風
室、10は同風室に空気を供給する空気供給管、3は同
風室の上部に設けられている空気分散板、5は同燃焼炉
の上部に設けられている燃料供給装置、2は同燃焼炉の
中に生じる流動層、6は同燃焼炉の中から下方へ伸びる
異物抜き出し管である。
2. Description of the Related Art FIG. 4 is a sectional view of a waste tire combustion apparatus as an example of a conventional fluidized bed combustion furnace. In the figure, 1 is a fluidized bed combustion furnace, 4 is an air chamber provided at a lower part of the combustion furnace, 10 is an air supply pipe for supplying air to the air chamber, and 3 is an upper part of the air chamber. Numeral 5 denotes a fuel supply device provided in the upper part of the combustion furnace, numeral 2 denotes a fluidized bed formed in the combustion furnace, and numeral 6 denotes a pipe for extracting foreign matters extending downward from the combustion furnace.

【0003】本装置では、流動層燃焼炉1の上部側方に
燃料供給装置5が設けられていて、燃料(例えば細かく
切断された廃タイヤ等であって、ワイヤー、メタルクロ
ス等の異物が含まれているもの)が、スクリューフィー
ダー等によって、定量的に流動層2の上方へ投入される
構造となっている。この流動層2の下部には、多少傾斜
した下方側に異物抜き出し管6を備えた空気分散板3が
設けられていて、その下部は風室4を形成し、空気供給
管10より、空気が流動用空気及び燃焼用空気として供
給され、これによって炉内で燃料が流動燃焼を行う。異
物は空気分散板3の傾斜に沿ってすべり落ち、異物抜き
出し管6から排出される。
In this apparatus, a fuel supply device 5 is provided on the upper side of the fluidized-bed combustion furnace 1, and the fuel (for example, a finely cut waste tire or the like containing foreign matters such as wires and metal cloth) is included. ) Is quantitatively charged above the fluidized bed 2 by a screw feeder or the like. At the lower part of the fluidized bed 2, an air distribution plate 3 provided with a foreign matter extraction pipe 6 on the slightly inclined lower side is provided, and the lower part thereof forms an air chamber 4, and air is supplied from an air supply pipe 10. The fuel is supplied as flowing air and combustion air, whereby the fuel undergoes flowing combustion in the furnace. The foreign matter slides down along the inclination of the air distribution plate 3 and is discharged from the foreign matter extraction pipe 6.

【0004】[0004]

【発明が解決しようとする課題】従来の流動層燃焼炉に
おいては、燃料中に含まれる異物が流動層内全体に沈降
し、また一部は流動する。廃タイヤ燃焼装置の場合は、
タイヤに含まれるワイヤやメタルクロスが沈降したり流
動したりする異物である。もし伝熱管を流動層内に設置
したとすれば、上述の異物が伝熱管にからみつきながら
流動するので、伝熱管の磨耗が生じたり、あるいは伝熱
の阻害が生じる。したがって従来は流動層内に伝熱管を
設置することができなかった。
In a conventional fluidized bed combustion furnace, foreign substances contained in the fuel are settled in the whole of the fluidized bed, and a part thereof flows. In the case of waste tire combustion equipment,
It is a foreign substance that sinks or flows a wire or metal cloth contained in a tire. If the heat transfer tube is installed in the fluidized bed, the above-described foreign matter flows while clinging to the heat transfer tube, and thus the heat transfer tube is worn or the heat transfer is hindered. Therefore, conventionally, a heat transfer tube cannot be installed in the fluidized bed.

【0005】本発明は、炉内温度を調節するために、異
物を流動層から排除するようにして流動層内に伝熱管の
設置を可能にした、流動層燃焼炉を提供しようとするも
のである。
An object of the present invention is to provide a fluidized bed combustion furnace in which heat transfer tubes can be installed in the fluidized bed by removing foreign matter from the fluidized bed in order to control the furnace temperature. is there.

【0006】[0006]

【課題を解決するための手段】本発明は前記課題を解決
したものであって、針金や石などの不燃性異物が混入し
た燃料を使用する流動層燃焼炉において、流動層内に伝
熱管を配置し、同伝熱管の上方に流動層を上下に隔てる
傾斜した隔壁を設け、同隔壁には、流動材は通過しうる
が異物は通過しえない寸法で形成され、かつその幅は上
側が狭く下側が広いスリットを全面に千鳥状に配設した
ことを特徴とする流動層燃焼炉に関するものである。
SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems. In a fluidized-bed combustion furnace using a fuel mixed with non-combustible foreign matter such as wire or stone, a heat transfer tube is provided in the fluidized bed. arrangement, and the inclined partition wall separating the fluidized bed vertically above the same heat transfer tube provided in the partition wall is fluidized material can pass through the foreign matter is formed in dimensions that can not be passed, and the width of the upper
The present invention relates to a fluidized bed combustion furnace, wherein slits having narrow sides and wide bottom sides are arranged in a zigzag pattern on the entire surface .

【0007】[0007]

【作用】伝熱管の上方に設けられた隔壁は流動層を上下
に隔てるが、隔壁の有するスリットにより流動材は流動
層の上下を自由に流動できる。しかもこのスリットは
流動材は通過できるが異物通過できない寸法で形成さ
れ、かつその幅は上側が狭く下側が広い形状で隔壁の全
面に千鳥状に配設されているため、流動材は前記のよう
に隔壁を通して自由に流動できるが、異物は隔壁の下方
には沈降せず、流動材とは分離され、隔壁の傾斜に沿っ
て異物の抜き出し管へ運ばれて排出される。この結果、
この種のボイラでは問題となる異物による伝熱管の磨耗
や異物の伝熱管へのからみつきを防止することができ、
流動層内への伝熱管の配置が可能となる。
The partition provided above the heat transfer tube separates the fluidized bed up and down, but the fluidized material can freely flow above and below the fluidized bed by the slits provided in the partition. And this slit ,
It is formed in dimensions but flowing material can pass through the foreign matter can not pass
The width of the partition is narrow at the top and wide at the bottom.
The fluid material is placed in a zigzag pattern on the
Can flow freely through the partition wall, but the foreign matter does not settle below the partition wall, is separated from the flowing material, and is carried along the slope of the partition wall to a discharge pipe for discharging the foreign matter and discharged. As a result,
In this type of boiler, it is possible to prevent abrasion of the heat transfer tube due to foreign matter and foreign matter sticking to the heat transfer tube, which is a problem,
The arrangement of the heat transfer tube in the fluidized bed becomes possible.

【0008】[0008]

【実施例】図1は本発明の流動層燃焼炉の一実施例の断
面図である。図において、7は本発明に基いて流動層内
に付設されたスリット付隔壁、8は同じく流動層内に付
設された層内伝熱管である。スリット付隔壁は流動層を
上下に分ける位置に傾斜して設けられ、その下方へ下っ
た端部は異物抜き出し管6に連っている。層内伝熱管8
は上記スリット付隔壁7と空気分散板3との間に設けら
れている。上記以外の部分は従来技術と同じである。
FIG. 1 is a sectional view of an embodiment of a fluidized bed combustion furnace according to the present invention. In the figure, 7 is a partition wall with a slit provided in the fluidized bed according to the present invention, and 8 is a heat transfer tube in the bed also provided in the fluidized bed. The partition wall with a slit is provided at a position where the fluidized bed is divided into upper and lower parts, and the lower end thereof is connected to the foreign matter extraction pipe 6. In-layer heat transfer tube 8
Is provided between the partition wall with slit 7 and the air distribution plate 3. The other parts are the same as in the prior art.

【0009】図2は上記スリット付隔壁の部分拡大平面
図、図3は図2のA─A断面図である。図において、9
はスリットである。図に示されるようにスリット9の幅
は上側が狭く(3mm)、下側が広い(5mm)貫通穴
となっており、その長さは20〜30mmであり、その
方向は傾斜の方向と平行であり、隔壁全面に千鳥状に配
置されている。
FIG. 2 is a partially enlarged plan view of the partition wall with a slit, and FIG. 3 is a sectional view taken along the line AA of FIG. In the figure, 9
Is a slit. As shown in the figure, the width of the slit 9 is narrow (3 mm) on the upper side and wide (5 mm) on the lower side, and the length is 20 to 30 mm. The direction is parallel to the direction of the inclination. Yes, they are arranged in a staggered pattern on the entire wall.

【0010】上記燃焼炉において、層内伝熱管8は、流
動層2の中で熱吸収を行って、流動層内を脱硫、低NO
x化、および燃焼に最も適した温度(800〜900
℃)に保つ働きをする。層内伝熱管8の上方に設けられ
ているスリット付隔壁7は、炉の上部から供給される燃
料の中の異物の下方への移動を阻止する。異物は同隔壁
7の傾斜に沿って移動し、異物抜き出し管から排出され
る。燃料や流動材粒子は、スリット付隔壁7に設けられ
ているスリット9を経て自由に上下に移動し、燃焼する
ことができる。
In the combustion furnace, the in-bed heat transfer tube 8 absorbs heat in the fluidized bed 2 to desulfurize the inside of the fluidized bed and reduce the NO
x and the most suitable temperature for combustion (800-900
℃). The partition wall 7 with slits provided above the in-layer heat transfer tube 8 prevents foreign substances in the fuel supplied from the upper part of the furnace from moving downward. The foreign matter moves along the slope of the partition 7 and is discharged from the foreign matter extraction pipe. Fuel and fluid material particles can freely move up and down through the slits 9 provided in the slit-equipped partition walls 7 and burn.

【0011】以上詳述したように、本実施例の流動層燃
焼炉においては、スリット付隔壁によって異物のからみ
付きによる伝熱管の磨耗の恐れがなくなるので、流動層
内に伝熱管を設置することができ、これによって炉内を
最適な燃焼温度に保持することが可能となり、流動層燃
焼炉の高負荷化を図ることができる。
As described in detail above, in the fluidized-bed combustion furnace of the present embodiment, the heat-transfer tube is not installed in the fluidized-bed because the partition wall with the slit eliminates the risk of abrasion of the heat-transfer tube due to sticking of foreign matter. This makes it possible to maintain the inside of the furnace at an optimum combustion temperature, and to increase the load of the fluidized bed combustion furnace.

【0012】[0012]

【発明の効果】本発明の流動層燃焼炉においては、流動
層内に伝熱管を配置し、かつ同伝熱管の上方に流動層を
上下に隔てる傾斜した隔壁を設け、さらにその隔壁に流
動材は通過しうるが異物は通過できない寸法で形成さ
れ、かつその幅は上側が狭く下側が広い形状で隔壁の全
面に千鳥状に配設されているため、流動材から異物を適
切に分離し、同異物が伝熱管にからみつくことを防止す
るので、流動層内に伝熱管の設置が可能となり、炉内温
度を適切に調節することができる。
According to the fluidized bed combustion furnace of the present invention, a heat transfer tube is disposed in the fluidized bed, and an inclined partition wall is provided above the heat transfer tube so as to vertically separate the fluidized bed. Is formed so that it can pass
The width of the partition is narrow at the top and wide at the bottom.
Are arranged in a zigzag pattern on the surface so that foreign substances can be
To prevent the foreign matter from clinging to the heat transfer tube.
Therefore, the heat transfer tube can be installed in the fluidized bed, and the temperature in the furnace can be appropriately adjusted.

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

【図1】本発明の流動層燃焼炉の一実施例の断面図。FIG. 1 is a sectional view of one embodiment of a fluidized bed combustion furnace of the present invention.

【図2】同実施例に用いられるスリット付隔壁の部分平
面図。
FIG. 2 is a partial plan view of a partition with a slit used in the embodiment.

【図3】図2のA─A断面図。FIG. 3 is a sectional view taken along line AA of FIG. 2;

【図4】従来の流動層燃焼炉の断面図。FIG. 4 is a sectional view of a conventional fluidized bed combustion furnace.

【符号の説明】[Explanation of symbols]

1 流動層燃焼炉 2 流動層 3 空気分散板 4 風室 5 燃料供給装置 6 異物抜き出し管 7 スリット付隔壁 8 層内伝熱管 9 スリット 10 空気供給管 DESCRIPTION OF SYMBOLS 1 Fluidized bed combustion furnace 2 Fluidized bed 3 Air dispersion plate 4 Air chamber 5 Fuel supply device 6 Foreign matter extraction pipe 7 Slit partition wall 8 In-layer heat transfer pipe 9 Slit 10 Air supply pipe

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.6,DB名) F23C 11/02 F23G 5/30 ──────────────────────────────────────────────────続 き Continued on front page (58) Field surveyed (Int.Cl. 6 , DB name) F23C 11/02 F23G 5/30

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 針金や石などの不燃性異物が混入した燃
料を使用する流動層燃焼炉において、流動層内に伝熱管
を配置し、同伝熱管の上方に流動層を上下に隔てる傾斜
した隔壁を設け、同隔壁には、流動材は通過しうるが異
物は通過しえない寸法で形成され、かつその幅は上側が
狭く下側が広いスリットを全面に千鳥状に配設したこと
を特徴とする流動層燃焼炉。
1. A fluidized bed combustion furnace using fuel mixed with non-combustible foreign matter such as wire or stone. A heat transfer tube is arranged in the fluidized bed, and the fluidized bed is inclined above and below the heat transfer tube so as to vertically separate the fluidized bed. A partition is provided, and the partition is formed in such a size that the flowable material can pass therethrough but foreign matter cannot pass through , and the width thereof is on the upper side.
A fluidized bed combustion furnace characterized by having narrow slits with wide bottoms arranged in a zigzag pattern on the entire surface .
JP17242391A 1991-07-12 1991-07-12 Fluidized bed combustion furnace Expired - Fee Related JP2955068B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17242391A JP2955068B2 (en) 1991-07-12 1991-07-12 Fluidized bed combustion furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17242391A JP2955068B2 (en) 1991-07-12 1991-07-12 Fluidized bed combustion furnace

Publications (2)

Publication Number Publication Date
JPH0518513A JPH0518513A (en) 1993-01-26
JP2955068B2 true JP2955068B2 (en) 1999-10-04

Family

ID=15941697

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17242391A Expired - Fee Related JP2955068B2 (en) 1991-07-12 1991-07-12 Fluidized bed combustion furnace

Country Status (1)

Country Link
JP (1) JP2955068B2 (en)

Also Published As

Publication number Publication date
JPH0518513A (en) 1993-01-26

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