JPH01169213A - Fluidized bed combustion furnace - Google Patents
Fluidized bed combustion furnaceInfo
- Publication number
- JPH01169213A JPH01169213A JP32872287A JP32872287A JPH01169213A JP H01169213 A JPH01169213 A JP H01169213A JP 32872287 A JP32872287 A JP 32872287A JP 32872287 A JP32872287 A JP 32872287A JP H01169213 A JPH01169213 A JP H01169213A
- Authority
- JP
- Japan
- Prior art keywords
- fluidized bed
- bottom plate
- furnace
- furnace body
- 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.)
- Pending
Links
Landscapes
- Fluidized-Bed Combustion And Resonant Combustion (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野]
本発明は流動層燃焼炉に係り、特に燃料物中に混在する
不燃異物の抜き出しが容易な流動層燃焼炉に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a fluidized bed combustion furnace, and more particularly to a fluidized bed combustion furnace from which non-flammable foreign matter mixed in fuel can be easily extracted.
[従来の技術]
近年、流動層では、石炭、オイルコークスなどの他、ご
み、産業廃棄物など低品質のものが燃焼されており、こ
れらの中には鉄屑等の不燃異物が混入している場合が多
い。これらの不燃異物は流動化状態を悪化させ、安定し
た燃焼の継続を困難にするため、層内から定期的または
連続的に抜き出す必要がある。[Conventional technology] In recent years, in addition to coal and oil coke, low-quality materials such as garbage and industrial waste have been burned in fluidized beds, and non-flammable foreign materials such as iron scraps have been mixed in with these materials. There are many cases. These non-flammable foreign substances deteriorate the fluidization state and make it difficult to continue stable combustion, so they must be periodically or continuously extracted from the bed.
第3図は、従来技術による流動層燃焼炉の部分断面図で
ある。この装置は、炉1内の流動層2と、該炉1の底部
中心に設けられる異物抜出管5と、該異物抜出管5に向
かって傾斜して設けられる円錐状または四角錐状の流動
層炉底板6と、該流動層炉底板6に鉛直に上向きに設け
られる空気ノズル3と、該空気ノズルの先端に設けられ
る空気噴出口8と、流動面部周壁および流動層炉底板6
上部に設けられる断熱材9と、風箱4とを有する。FIG. 3 is a partial sectional view of a fluidized bed combustion furnace according to the prior art. This device consists of a fluidized bed 2 in a furnace 1, a foreign matter extraction pipe 5 provided at the center of the bottom of the furnace 1, and a conical or square pyramid-shaped foreign material extraction pipe 5 provided at an angle toward the foreign material extraction pipe 5. A fluidized bed furnace bottom plate 6, an air nozzle 3 provided vertically upward on the fluidized bed furnace bottom plate 6, an air outlet 8 provided at the tip of the air nozzle, a fluidized bed peripheral wall, and a fluidized bed furnace bottom plate 6.
It has a heat insulating material 9 provided at the top and a wind box 4.
断熱材9は、低品質燃料を燃焼する際の熱用失をできる
だけ少なくするために設けられる。このような構成にお
いて、流動用空気IOは、風箱4より流動層炉底板6お
よび空気ノズル3を経て、空気噴出口8から流動層2内
に供給される。不燃異物は、燃料に混在して流動層上部
の炉側壁または炉頂部(図示せず)から供給され、流動
層内に落下し、流動層炉底板6上に堆積する。この際、
不燃異物は、流動層炉底板6の(頃斜によって炉1最下
部の異物抜出管5まで移動し、流動媒体とともに排出さ
れる。The insulation 9 is provided to minimize heat loss when burning low quality fuel. In such a configuration, the fluidizing air IO is supplied from the wind box 4 through the fluidized bed furnace bottom plate 6 and the air nozzle 3 into the fluidized bed 2 from the air outlet 8. The non-flammable foreign matter is mixed with the fuel and supplied from the furnace side wall or the furnace top (not shown) above the fluidized bed, falls into the fluidized bed, and is deposited on the fluidized bed furnace bottom plate 6. On this occasion,
The non-flammable foreign matter moves to the foreign matter extraction pipe 5 at the lowest part of the furnace 1 by the slope of the fluidized bed furnace bottom plate 6, and is discharged together with the fluidized medium.
不燃異物は傾斜した流動層炉底板6に沿って移動するた
め、流動層炉底板6の傾斜角度が大きいほど移動し易く
なるが、炉を大型化した場合、中心部と周壁部との流動
層高差が大きくなり、流動化空気が層高の低い周壁部に
集中して流動化不良を起こす問題がある。Non-flammable foreign matter moves along the inclined fluidized bed bottom plate 6, so the larger the inclination angle of the fluidized bed bottom plate 6, the easier it is to move. There is a problem in that the height difference becomes large and the fluidized air concentrates on the peripheral wall portion where the layer height is low, causing poor fluidization.
また空気ノズル3は傾斜した流動層炉底板6に鉛直上向
きに取り付ける必要があるため製作が難しく、さらに低
品質燃料を燃焼するため流動層炉底部に断熱材を打張り
する必要があり、加工工数が多くなる欠点がある。In addition, the air nozzle 3 needs to be installed vertically upward on the inclined fluidized bed furnace bottom plate 6, which makes it difficult to manufacture.Furthermore, since low-quality fuel is burned, it is necessary to put a heat insulating material on the bottom of the fluidized bed furnace, which increases the processing time. The disadvantage is that there are many
(発明が解決しようとする問題点〕
本発明の目的は、上記従来技術の問題点を解決し、流動
層炉底部の底板および空気ノズルの製作が容易で、かつ
炉を大型化した場合でも流動化不良を起こすことがない
流動層燃焼炉を提供することにある。(Problems to be Solved by the Invention) An object of the present invention is to solve the above-mentioned problems of the prior art, to make it easy to manufacture the bottom plate and air nozzle at the bottom of the fluidized bed furnace, and to ensure that even when the furnace is enlarged, there is no fluid flow. An object of the present invention is to provide a fluidized bed combustion furnace that does not cause oxidation failure.
〔問題点を解決するための手段)
本発明は、炉本体底板に設けられた複数の空気ノズルと
、異物抜出管とを有する流動層燃焼炉において、前記炉
本体底板が水平であり、前記空気ノズルが該炉本体底板
と垂直であって、かつその高さが前記異物抜出管に近づ
くに従って順に低くなるように設置されたことを特徴と
する。[Means for Solving the Problems] The present invention provides a fluidized bed combustion furnace having a plurality of air nozzles provided on the bottom plate of the furnace body and a foreign matter extraction pipe, wherein the bottom plate of the furnace body is horizontal, and the bottom plate of the furnace body is horizontal. The air nozzle is installed perpendicularly to the bottom plate of the furnace main body, and the height of the air nozzle decreases as it approaches the foreign matter extraction pipe.
〔作用]
流動用空気の空気噴出口の高さを、異物抜出管に近づ(
に従い順に低くすることによって、空気噴出口上部では
流動媒体の活発な流動が行われ、一方、空気噴出口下部
では流動媒体の流動は行われず、固定層(流動停止層)
が形成される。該固定層は空気噴出口に沿って傾斜をつ
くるため、不燃異物はこの固定層の傾斜に沿って移動し
、底部に位置する異物抜出管から抜き出される。[Function] Adjust the height of the air outlet of the fluidizing air to be closer to the foreign matter extraction pipe (
By gradually lowering the air outlet, active flow of the fluid medium occurs at the upper part of the air outlet, while no flow of the fluid medium occurs at the lower part of the air outlet, resulting in a fixed bed (flow stop layer).
is formed. Since the fixed layer forms an inclination along the air outlet, the non-flammable foreign matter moves along the inclination of the fixed layer and is extracted from the foreign matter extraction pipe located at the bottom.
上記固定層は、通常、熱伝達が非常に悪く、断熱材の役
目をするため、従来の炉本体底板■の断熱材を省くこと
ができる。また炉本体底板は水平であるため、その製作
が簡単であるとともに、空気ノズルも炉本体底板に対し
て垂直に取りつければよく、取りつけ作業が容易となり
、加工工数および作業工数を大幅に低減することができ
る。さらに異物抜出口に向かって空気ノズルの空気噴出
口を例えば四角錐状に配列した底板を組み合わせれば炉
の大型化が容易に可能となる。すなわち、炉を大型化し
ても中心部と炉周壁部の層高差を小さくすることができ
るので、従来技術で見られたような流動化空気の偏流に
よる流動化不良を起こすことがない。The fixed layer usually has very poor heat transfer and serves as a heat insulating material, so the conventional heat insulating material in the bottom plate of the furnace body can be omitted. In addition, since the bottom plate of the furnace body is horizontal, it is easy to manufacture, and the air nozzle only needs to be installed perpendicularly to the bottom plate of the furnace body, making the installation process easy and greatly reducing the number of processing steps and work hours. be able to. Further, by combining a bottom plate in which the air jet ports of the air nozzles are arranged in, for example, a quadrangular pyramid shape toward the foreign matter extraction port, it becomes possible to easily increase the size of the furnace. That is, even if the furnace is enlarged, the difference in layer height between the center and the peripheral wall of the furnace can be made small, so that fluidization failure due to uneven flow of fluidization air, as seen in the prior art, does not occur.
〔実施例] 以下、本発明を実施例により詳細に説明する。〔Example] Hereinafter, the present invention will be explained in detail with reference to Examples.
第1図は、本発明の一実施例を示す流動層燃焼炉の断面
図である。図において第3図と異なる点は、流動面部周
壁にのみ断熱材9を設け、断熱材を設置しない炉本体底
板6を炉本体1底部に水平に設け、空気ノズル3を該炉
本体底板6に垂直、かつ異物抜出管5に最も近い空気ノ
ズル3の高さが最も低くなるように順に高さを変えて階
段状に設置し、該階段状に設けられた空気ノズル3の空
気噴出口8の下部に固定層7を形成させたことである。FIG. 1 is a sectional view of a fluidized bed combustion furnace showing one embodiment of the present invention. The difference between this figure and FIG. 3 is that a heat insulating material 9 is provided only on the peripheral wall of the flow surface, a bottom plate 6 of the furnace body without any heat insulating material is provided horizontally at the bottom of the furnace body 1, and an air nozzle 3 is attached to the bottom plate 6 of the furnace body 1. The air nozzles 3 are installed vertically and in a stepwise manner, with the heights being changed in order so that the height of the air nozzle 3 closest to the foreign matter extraction pipe 5 is the lowest, and the air jet ports 8 of the air nozzles 3 provided in the stepwise manner are installed in a stepwise manner. The fixed layer 7 is formed below the .
空気ノズル3が、炉本体底板6上部に垂直に取りつけら
れ、しかも空気ノズル3の空気噴出口8の高さが異物抜
出管5に向かって階段状に低く設けられることによって
、運転時、空気噴出口8のL部では流動層2が形成され
、空気噴出口8の下部では異物抜出管5に向かって固定
層7が傾斜して形成される。The air nozzle 3 is vertically attached to the upper part of the bottom plate 6 of the furnace main body, and the height of the air jet port 8 of the air nozzle 3 is lowered in a stepped manner toward the foreign matter extraction pipe 5, so that the air is not removed during operation. A fluidized bed 2 is formed at the L portion of the air jet port 8, and a fixed bed 7 is formed at the lower part of the air jet port 8 so as to be inclined toward the foreign matter extraction pipe 5.
不燃異物の混在した燃料11は、図示しない層上バーナ
または熱風炉などの手段によって燃料の燃焼可能な温度
に予熱された流動層に供給され、可燃分が燃焼し、燃焼
ガス12が炉外に排出される。一方、燃料に混在した不
燃異物は、流動層内を沈陣し、炉本体底板6に設けられ
た異物抜出管5に向かって傾斜した固定層7に沿って移
動し、異物抜出管5から容易に抜き出される。固定層7
の傾斜角度は、空気ノズル3の空気噴出口8の高さを変
えることによって簡単に調整することができる。The fuel 11 mixed with non-combustible foreign matter is supplied to a fluidized bed preheated to a temperature at which the fuel can be combusted by means such as a bed burner or a hot blast furnace (not shown), where the combustible components are combusted and the combustion gas 12 is released outside the furnace. It is discharged. On the other hand, the non-flammable foreign matter mixed in the fuel settles in the fluidized bed, moves along the fixed bed 7 inclined toward the foreign matter extraction pipe 5 provided on the bottom plate 6 of the furnace body, and moves to the foreign matter extraction pipe 5. easily extracted from. Fixed layer 7
The inclination angle of can be easily adjusted by changing the height of the air outlet 8 of the air nozzle 3.
本発明に使用される炉本体1の形状は円形、または四角
形などでもよい。また固定層7は、停止流動層で形成す
ることが好ましいが、所望により部分的に断熱材(耐火
材)で形成してもよい。The shape of the furnace body 1 used in the present invention may be circular or square. The fixed bed 7 is preferably formed of a stopped fluidized bed, but may be partially formed of a heat insulating material (refractory material) if desired.
第2図は、本発明の他の実施例による流動層燃焼炉の部
分断面図である。この装置は、炉本体の底部に第1図に
示す小型の四角形炉本体底板6を数個組み合わせた流動
層燃焼炉である。本実施例によれば炉が大型化しても流
動化空気の偏流による流動化不良を起こすことがない。FIG. 2 is a partial sectional view of a fluidized bed combustion furnace according to another embodiment of the present invention. This apparatus is a fluidized bed combustion furnace in which several small rectangular furnace main body bottom plates 6 shown in FIG. 1 are combined at the bottom of the furnace main body. According to this embodiment, even if the furnace becomes large-sized, fluidization failure due to uneven flow of fluidization air will not occur.
本発明によれば、流動層内の不燃異物を円滑に抜き出す
ことができるため、安定した燃焼の継続が可能であり、
また流動層燃焼炉の加工製作が容易であるとともに、装
置の大型化が可能である。According to the present invention, since non-flammable foreign matter in the fluidized bed can be smoothly extracted, stable combustion can be continued,
Further, the fluidized bed combustion furnace is easy to process and manufacture, and the device can be made larger.
第1図は、本発明の一実施例を示す流動層燃焼炉の断面
図、第2図は、本発明の実施例による流動層燃焼炉の部
分断面図、第3図は、従来技術による流動層燃焼炉の部
分断面図である。
1・・・炉本体、2・・・流動層、3・・・空気ノズル
、4・・・風箱、5・・・異物抜出管、6・・・炉本体
底板、7・・・固定層、8・・・空気吹出口、9・・・
断熱材、10・・・流動用空気、11・・・燃料、12
・・・燃焼ガス。
代理人 弁理士 川 北 武 長FIG. 1 is a sectional view of a fluidized bed combustion furnace according to an embodiment of the present invention, FIG. 2 is a partial sectional view of a fluidized bed combustion furnace according to an embodiment of the present invention, and FIG. 3 is a fluidized bed combustion furnace according to the prior art. FIG. 2 is a partial cross-sectional view of a bed combustion furnace. 1... Furnace body, 2... Fluidized bed, 3... Air nozzle, 4... Wind box, 5... Foreign matter extraction pipe, 6... Furnace main body bottom plate, 7... Fixed Layer, 8...Air outlet, 9...
Heat insulating material, 10... Fluidizing air, 11... Fuel, 12
...Combustion gas. Agent Patent Attorney Takeshi Kawakita
Claims (1)
物抜出管とを有する流動層燃焼炉において、前記炉本体
底板が水平であり、前記空気ノズルが該炉本体底板と垂
直であって、かつその高さが前記異物抜出管に近づくに
従って順に低くなるように設置されたことを特徴とする
流動層燃焼炉。(1) In a fluidized bed combustion furnace having a plurality of air nozzles provided on the bottom plate of the furnace body and a foreign matter extraction pipe, the bottom plate of the furnace body is horizontal, and the air nozzles are perpendicular to the bottom plate of the furnace body. A fluidized bed combustion furnace characterized in that the furnace is installed such that its height gradually decreases as it approaches the foreign matter extraction pipe.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32872287A JPH01169213A (en) | 1987-12-25 | 1987-12-25 | Fluidized bed combustion furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32872287A JPH01169213A (en) | 1987-12-25 | 1987-12-25 | Fluidized bed combustion furnace |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH01169213A true JPH01169213A (en) | 1989-07-04 |
Family
ID=18213448
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP32872287A Pending JPH01169213A (en) | 1987-12-25 | 1987-12-25 | Fluidized bed combustion furnace |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01169213A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2000088225A (en) * | 1998-09-17 | 2000-03-31 | Hitachi Zosen Corp | Large fluidized bed incinerator |
WO2017086037A1 (en) * | 2015-11-18 | 2017-05-26 | 住友重機械工業株式会社 | Reacting furnace |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS49113472A (en) * | 1973-03-03 | 1974-10-29 |
-
1987
- 1987-12-25 JP JP32872287A patent/JPH01169213A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS49113472A (en) * | 1973-03-03 | 1974-10-29 |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2000088225A (en) * | 1998-09-17 | 2000-03-31 | Hitachi Zosen Corp | Large fluidized bed incinerator |
WO2017086037A1 (en) * | 2015-11-18 | 2017-05-26 | 住友重機械工業株式会社 | Reacting furnace |
JP2017094227A (en) * | 2015-11-18 | 2017-06-01 | 住友重機械工業株式会社 | Reactor |
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