JPH01203814A - Fluidized bed combustion device - Google Patents
Fluidized bed combustion deviceInfo
- Publication number
- JPH01203814A JPH01203814A JP2949688A JP2949688A JPH01203814A JP H01203814 A JPH01203814 A JP H01203814A JP 2949688 A JP2949688 A JP 2949688A JP 2949688 A JP2949688 A JP 2949688A JP H01203814 A JPH01203814 A JP H01203814A
- Authority
- JP
- Japan
- Prior art keywords
- wall
- nozzle
- furnace
- discharge groove
- flow
- 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
- 238000002485 combustion reaction Methods 0.000 title claims abstract description 20
- 238000007664 blowing Methods 0.000 claims description 9
- 239000012530 fluid Substances 0.000 abstract description 7
- 238000000034 method Methods 0.000 abstract description 3
- 238000005243 fluidization Methods 0.000 abstract description 2
- 239000000126 substance Substances 0.000 abstract description 2
- 230000000630 rising effect Effects 0.000 abstract 1
- 238000010586 diagram Methods 0.000 description 10
- 230000002950 deficient Effects 0.000 description 4
- 238000009825 accumulation Methods 0.000 description 3
- 239000000123 paper Substances 0.000 description 3
- 239000010893 paper waste Substances 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C10/00—Fluidised bed combustion apparatus
- F23C10/02—Fluidised bed combustion apparatus with means specially adapted for achieving or promoting a circulating movement of particles within the bed or for a recirculation of particles entrained from the bed
- F23C10/12—Fluidised bed combustion apparatus with means specially adapted for achieving or promoting a circulating movement of particles within the bed or for a recirculation of particles entrained from the bed the particles being circulated exclusively within the combustion zone
- F23C10/14—Fluidised bed combustion apparatus with means specially adapted for achieving or promoting a circulating movement of particles within the bed or for a recirculation of particles entrained from the bed the particles being circulated exclusively within the combustion zone the circulating movement being promoted by inducing differing degrees of fluidisation in different parts of the bed
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、異物が混入した廃棄物を燃焼させる流動層燃
焼装置に係り、特に異物を流動媒体とともに炉底から容
易に抜出すことを可能とした流動層燃焼装置に関するも
のである。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a fluidized bed combustion device for burning waste mixed with foreign matter, and in particular, it is possible to easily extract foreign matter from the bottom of the furnace together with a fluidized medium. The present invention relates to a fluidized bed combustion apparatus.
第2図は、故紙の再生過程より発生する異物が混入した
廃棄物である製紙粕を燃焼する従来の流動層燃焼装置の
全体説明図、第3図は、上記流動層燃焼装置の火炉底部
の詳細説明図である。この装置は、傾斜底面1とこれに
連続する垂直壁21を有する火炉14と、該火炉14に
充填された流動媒体5と、該火炉14の傾斜底面1に設
けられた空気吹込みノズル2と、該傾斜底面1の最下部
に設けられた排出溝9とを有するものである。垂直壁2
1には、流動媒体5、スラッジ16および製紙粕17の
投入口がそれぞれ設けられている。Figure 2 is an overall explanatory diagram of a conventional fluidized bed combustion equipment that burns paper lees, which is waste mixed with foreign matter generated during the recycling process of waste paper, and Figure 3 shows the bottom of the furnace of the fluidized bed combustion equipment. It is a detailed explanatory diagram. This device includes a furnace 14 having an inclined bottom surface 1 and a vertical wall 21 continuous thereto, a fluidized medium 5 filled in the furnace 14, and an air blowing nozzle 2 provided on the inclined bottom surface 1 of the furnace 14. , and a discharge groove 9 provided at the lowest part of the inclined bottom surface 1. vertical wall 2
1 is provided with inlets for the fluid medium 5, sludge 16, and paper waste 17, respectively.
なお、18は煙道15に設けられた蒸発水管、13は火
炉壁面に配置された温度針、1′9はキャスタブルであ
る。In addition, 18 is an evaporation water pipe provided in the flue 15, 13 is a temperature needle arranged on the furnace wall surface, and 1'9 is a castable.
このような構成において、火炉14に投入された製紙粕
17は、流動媒体とともに燃焼に最適な循環流を形成し
、図示されてないバーナによって点火されて燃焼する。In such a configuration, the paper lees 17 introduced into the furnace 14 form a circulating flow suitable for combustion together with the fluidized medium, and are ignited by a burner (not shown) and combusted.
このとき前記製紙粕17とともに炉内に投入される不燃
性の異物は、傾斜底面1を最下部に移動し、排出溝9か
ら炉外へ抜出される。At this time, the non-flammable foreign matter thrown into the furnace together with the paper dregs 17 moves to the lowest part on the inclined bottom surface 1 and is extracted out of the furnace through the discharge groove 9.
しかしながら、上記従来技術の炉底構造では、異物が、
例えば石炭中の燃えない固形分(ズリ)や空缶などのよ
うに、異物同士が絡み合うことのない場合には、流動媒
体の流動に伴って容易に移動して排出溝から排出される
が、例えばステッチと称される第3図に示すようなダン
ボール箱の止め金具のようにお互いが絡み合う特質があ
る異物が混入した場合には、その絡み合いの度合が成長
し、炉内の流動不良となり易い個所、例えば壁面近傍お
よび排出溝部で停滞し、経時的に堆積するという問題が
ある。However, in the above-mentioned conventional hearth bottom structure, foreign matter
For example, when foreign objects do not get entangled with each other, such as unburnable solids (sludge) in coal or empty cans, they easily move with the flow of the fluid medium and are discharged from the discharge groove. For example, if foreign substances that have the characteristic of intertwining with each other, such as the fasteners of a cardboard box shown in Figure 3, which are called stitches, are mixed in, the degree of intertwining will grow and cause poor flow in the furnace. There is a problem in that it stagnates in places such as near walls and in discharge grooves and accumulates over time.
第5図および第6図は、炉壁面流動不良部7に発生した
ステッチの初期の堆積状況を示す説明図、第7図および
第8図は、第5図および第6図から絡み合いが成長した
ステッチ堆積状況を示す説明図である。第5図および第
6図には、傾斜底面1にせり上がるように堆積して移動
しなくなったステッチ20が、また第7図および第8図
には、上記ステッチ20の絡まりが経時的に成長し、排
出溝9の両側に垂直に堆積し、流れ落ちなくなった状態
がそれぞれ示されている。このように火炉内にステッチ
が堆積すると流動しなくなり、このステッチを完全に抜
出すためには燃焼装置の運転を停止させねばならず、連
続運転ができないという不都合があった。Figures 5 and 6 are explanatory diagrams showing the initial accumulation of stitches that occurred in the flow failure area 7 on the furnace wall surface, and Figures 7 and 8 show the growth of entanglements from Figures 5 and 6. FIG. 3 is an explanatory diagram showing a stitch accumulation situation. Figures 5 and 6 show stitches 20 that have piled up on the inclined bottom surface 1 and have stopped moving, and Figures 7 and 8 show stitches 20 that have grown entangled over time. However, the state in which the particles are deposited vertically on both sides of the discharge groove 9 and no longer flows down is shown. If the stitches accumulate in the furnace in this way, they will not flow, and in order to completely remove the stitches, the operation of the combustion device must be stopped, which is disadvantageous in that continuous operation cannot be performed.
本発明の目的は、上記従来技術の課題を解決し、流動不
良となり易い炉壁面近傍および炉底排出溝部の流動を活
性化した、ステッチの移動が容易な流動層燃焼装置を提
供することにある。An object of the present invention is to solve the above-mentioned problems of the prior art and to provide a fluidized bed combustion device that activates the flow in the vicinity of the furnace wall surface and in the furnace bottom discharge groove where poor flow tends to occur, and in which the stitches can be easily moved. .
上記目的を達成するため本発明は、傾斜底面とこれに連
続する垂直壁を有する火炉と、該火炉に充填された流動
媒体と、該火炉の傾斜底面に設けられた空気吹込みノズ
ルと、該傾斜底面の最下部に設けられた排出溝とを有す
る流動層燃焼装置において、前記傾斜底面に沿って空気
を噴出させる傾斜面ブローノズルと、前記排出溝の対向
する側壁から横方向に空気を噴出させる横吹きノズルと
、前記傾斜底面と前記垂直壁の間に設けられた傾斜壁と
を有し、前記空気吹込みノズルが炉壁側と排出溝側とで
異なるノズルであることを特徴とするものである。In order to achieve the above object, the present invention provides a furnace having an inclined bottom surface and a vertical wall continuous thereto, a fluidized medium filled in the furnace, an air blowing nozzle provided on the inclined bottom surface of the furnace, and a fluidized medium filled in the furnace. In a fluidized bed combustion apparatus having an exhaust groove provided at the lowest part of an inclined bottom surface, an inclined surface blow nozzle blows out air along the inclined bottom surface, and air is jetted laterally from opposing side walls of the exhaust groove. and an inclined wall provided between the inclined bottom surface and the vertical wall, and the air blowing nozzle is a different nozzle on the furnace wall side and the exhaust groove side. It is something.
傾斜底面と垂直壁の間に傾斜壁を設けたことにり、第6
図に示す炉壁面流動不良部7がなくなるので、異物は傾
斜壁土を滑り落ち、傾斜底面に沿って傾斜面ブローノズ
ルを設けたことにより、該傾斜面ブローノズルから噴出
された空気により、傾斜壁近傍の傾斜底面に停滞するス
テッチが傾斜底面の最下部方向に吹き飛ばされ、排出溝
近傍に移動する。さらに、排出溝の対向する側壁に横吹
きノズルを設けたことにより、該横吹きノズルから噴出
される空気が排出溝を上向きに流れるので、第8図に示
す排出溝流動不良部8がなくなり、加えて、前記空気吹
込みノズルの排出溝側の方を炉壁側より多くの空気が出
るようにすることにより、炉内の循環流を助け、前記循
環流に伴って排出溝の入口まで移動してきたステッチは
排出溝から抜出される流動媒体に同伴して容易に炉外に
抜出される。By providing an inclined wall between the inclined bottom surface and the vertical wall, the sixth
Since the flow defective part 7 on the furnace wall surface shown in the figure disappears, the foreign matter slides down the sloped wall soil, and since the sloped blow nozzle is provided along the sloped bottom surface, the air blown out from the sloped blow nozzle will cause the foreign matter to slide down the sloped wall soil. Stitches stagnant on the nearby sloped bottom surface are blown away toward the bottom of the sloped bottom surface and moved to the vicinity of the discharge groove. Furthermore, by providing the side blow nozzles on the opposite side walls of the discharge groove, the air ejected from the side blow nozzles flows upward through the discharge groove, so that the discharge groove flow defective portion 8 shown in FIG. 8 is eliminated. In addition, by allowing more air to come out from the exhaust groove side of the air blowing nozzle than from the furnace wall side, the circulating flow within the furnace is aided, and the air moves to the entrance of the exhaust groove along with the circulating flow. The stitches that have been formed are easily extracted out of the furnace along with the fluid medium that is extracted from the discharge groove.
次に、本発明を実施例によりさらに詳細に説明する。 Next, the present invention will be explained in more 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装置の要
部説明図である。FIG. 1 is an explanatory diagram of the main parts of a fluidized bed combustion apparatus showing one embodiment of the present invention.
この装置は、第3図の傾斜底面1と垂直壁21の間に傾
斜壁10を設けるとともに、傾斜底面lに沿って傾斜面
ブローノズル11を設け、さらに、傾斜底面1の最下部
に設けられた排出溝9の対向する側壁に横吹きノズル1
2を設けたものである。This device is provided with an inclined wall 10 between the inclined bottom surface 1 and the vertical wall 21 shown in FIG. A horizontal blow nozzle 1 is installed on the opposite side wall of the discharge groove 9.
2.
このような構成において、火炉内に供給された製紙粕1
7は、空気吹込みノズル2を排出溝側を炉壁側よりノズ
ル穴を大きくするか、または同じノズル穴ならノズルを
密に配置し、排出溝側の上昇流を大きくすることにより
、流動媒体5とともに燃焼に最適な循環流6となり、図
示されていない点火バーナにより点火されて燃焼する。In such a configuration, paper waste 1 supplied into the furnace
7, by making the nozzle hole of the air blowing nozzle 2 larger on the discharge groove side than on the furnace wall side, or if the nozzle holes are the same, by arranging the nozzles densely and increasing the upward flow on the discharge groove side, the fluidized medium is Together with 5, the circulating flow 6 becomes optimal for combustion, and is ignited by an ignition burner (not shown) to cause combustion.
このとき、傾斜底面1と垂直壁21の間に設けられた傾
斜壁10の作用により、スムーズな循環流が形成される
。また傾斜面ブローノズル11から噴出される空気によ
り、前記傾斜壁10近傍での流動化が活発化するので、
傾斜壁10近傍に停滞するステッチ20は傾斜底面1の
最下部に向かって移動する。さらに、排出溝9の側壁に
設けられた横吹きノズル12から噴出された空気が前記
排出溝9を上昇することにより、排出溝部の流動媒体5
等の流動が活発化するので、前記排出溝部まで移動して
きたステッチ20は排出溝9を経て容易に抜出される
本実施例によれば、炉壁面流動不良部7および排出溝流
動不良部8がなくなるので、燃料とともに火炉14内に
導入された異物を燃焼装置の運転を停止することなく完
全に抜出すことができる。At this time, due to the action of the inclined wall 10 provided between the inclined bottom surface 1 and the vertical wall 21, a smooth circulating flow is formed. Furthermore, the air ejected from the inclined surface blow nozzle 11 activates the fluidization near the inclined wall 10, so that
The stitches 20 stagnant near the inclined wall 10 move toward the bottom of the inclined bottom surface 1. Further, the air ejected from the side blow nozzle 12 provided on the side wall of the discharge groove 9 rises in the discharge groove 9, thereby causing the fluidized medium 5 in the discharge groove portion to
According to this embodiment, the stitches 20 that have moved to the discharge groove are easily pulled out through the discharge groove 9. According to this embodiment, the furnace wall surface flow defective portion 7 and the discharge groove flow defective portion 8 are removed. Therefore, the foreign matter introduced into the furnace 14 along with the fuel can be completely extracted without stopping the operation of the combustion apparatus.
本発明によれば、ステッチのようにお互いに絡み合う特
質を有する金物異物を流動媒体とともに容易に、しかも
完全に抜出すことができるので、ステッチ抜出しのため
の停止が不要となり、流動層燃焼装置を長期連続運転す
ることができる。According to the present invention, it is possible to easily and completely extract metal foreign objects that have the characteristic of intertwining with each other like stitches together with the fluid medium, so there is no need to stop for stitch extraction, and the fluidized bed combustion apparatus can be Can be operated continuously for a long period of time.
第1図は、本発明の一実施例を示す流動層燃焼装置の要
部説明図、第2図は、従来の流動層燃焼装置の全体説明
図、第3図は、第2図の要部説明図、第4図は、廃棄物
に含まれる金物異物であるステッチを示す図、第5〜8
図は、従来技術の炉底構造において発生するステッチ堆
積状況を示す図である。
1・・・傾斜底面、2・・・空気吹込みノズル、6・・
・循環流、9・・・排出溝、10・・・傾斜壁、11・
・・傾斜壁ブローノズル、12・・・横吹きノズル。
代理人 弁理士 川 北 武 長
1:傾斜底面
3:流動化空気
6:循環流
9:排出溝
lO:傾斜壁
11:傾斜面ブローノズル
第1図FIG. 1 is an explanatory diagram of the main parts of a fluidized bed combustion apparatus showing an embodiment of the present invention, FIG. 2 is an overall explanatory diagram of a conventional fluidized bed combustion apparatus, and FIG. 3 is the main part of FIG. 2. Explanatory diagram, Figure 4 is a diagram showing stitches, which are foreign metal objects contained in waste, Figures 5 to 8
The figure is a diagram showing a stitch accumulation situation that occurs in a conventional hearth structure. 1... Inclined bottom surface, 2... Air blowing nozzle, 6...
・Circulating flow, 9... Discharge groove, 10... Inclined wall, 11.
... Inclined wall blow nozzle, 12... Side blow nozzle. Agent Patent Attorney Takeshi Kawakita Cho 1: Inclined bottom 3: Fluidized air 6: Circulating flow 9: Discharge groove lO: Inclined wall 11: Inclined blow nozzle Figure 1
Claims (1)
、該火炉に充填された流動媒体と、該火炉の傾斜底面に
設けられた空気吹込みノズルと、該傾斜底面の最下部に
設けられた排出溝とを有する流動層燃焼装置において、
前記傾斜底面に沿って空気を噴出させる傾斜面ブローノ
ズルと、前記排出溝の対向する側壁から横方向に空気を
噴出させる横吹きノズルと、前記傾斜底面と前記垂直壁
の間に設けられた傾斜壁とを有し、前記空気吹込みノズ
ルが炉壁側と排出溝側とで異なるノズルであることを特
徴とする流動層燃焼装置。(1) A furnace having an inclined bottom surface and a vertical wall continuous thereto, a fluidized medium filled in the furnace, an air blowing nozzle provided on the inclined bottom surface of the furnace, and an air blowing nozzle provided at the lowest part of the inclined bottom surface. In a fluidized bed combustion apparatus having a discharge groove,
an inclined blow nozzle that blows out air along the inclined bottom surface; a side blow nozzle that blows out air laterally from opposing side walls of the discharge groove; and an inclined surface provided between the inclined bottom surface and the vertical wall. 1. A fluidized bed combustion apparatus, characterized in that the air blowing nozzle is a different nozzle on the furnace wall side and on the exhaust groove side.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2949688A JPH01203814A (en) | 1988-02-10 | 1988-02-10 | Fluidized bed combustion device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2949688A JPH01203814A (en) | 1988-02-10 | 1988-02-10 | Fluidized bed combustion device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH01203814A true JPH01203814A (en) | 1989-08-16 |
Family
ID=12277678
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2949688A Pending JPH01203814A (en) | 1988-02-10 | 1988-02-10 | Fluidized bed combustion device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01203814A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH07301411A (en) * | 1992-11-13 | 1995-11-14 | Foster Wheeler Energy Corp | Fluidized bed reactor and combustion method |
JP2005226870A (en) * | 2004-02-10 | 2005-08-25 | Mitsubishi Heavy Ind Ltd | Fluidized bed incinerator |
WO2013035615A1 (en) | 2011-09-07 | 2013-03-14 | 荏原環境プラント株式会社 | Fluidized bed furnace and waste disposal method using fluidized bed furnace |
WO2017086037A1 (en) * | 2015-11-18 | 2017-05-26 | 住友重機械工業株式会社 | Reacting furnace |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5731712A (en) * | 1980-06-16 | 1982-02-20 | Ahlstroem Oy | Method of and apparatus for burning matter containing non-combustible substance |
JPS57150720A (en) * | 1981-03-11 | 1982-09-17 | Kobe Steel Ltd | Fluid bed type combustion device for waste containing incombustible |
JPS59197715A (en) * | 1983-04-25 | 1984-11-09 | Babcock Hitachi Kk | Fluidized-bed incinerator with foreign matter discharge port being sealed |
-
1988
- 1988-02-10 JP JP2949688A patent/JPH01203814A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5731712A (en) * | 1980-06-16 | 1982-02-20 | Ahlstroem Oy | Method of and apparatus for burning matter containing non-combustible substance |
JPS57150720A (en) * | 1981-03-11 | 1982-09-17 | Kobe Steel Ltd | Fluid bed type combustion device for waste containing incombustible |
JPS59197715A (en) * | 1983-04-25 | 1984-11-09 | Babcock Hitachi Kk | Fluidized-bed incinerator with foreign matter discharge port being sealed |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH07301411A (en) * | 1992-11-13 | 1995-11-14 | Foster Wheeler Energy Corp | Fluidized bed reactor and combustion method |
JP2005226870A (en) * | 2004-02-10 | 2005-08-25 | Mitsubishi Heavy Ind Ltd | Fluidized bed incinerator |
WO2013035615A1 (en) | 2011-09-07 | 2013-03-14 | 荏原環境プラント株式会社 | Fluidized bed furnace and waste disposal method using fluidized bed furnace |
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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