JPH04217708A - Fluidized-bed incinerator - Google Patents
Fluidized-bed incineratorInfo
- Publication number
- JPH04217708A JPH04217708A JP41087390A JP41087390A JPH04217708A JP H04217708 A JPH04217708 A JP H04217708A JP 41087390 A JP41087390 A JP 41087390A JP 41087390 A JP41087390 A JP 41087390A JP H04217708 A JPH04217708 A JP H04217708A
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- wind box
- main body
- air distribution
- distribution plate
- 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.)
- Granted
Links
- 238000005192 partition Methods 0.000 claims abstract description 37
- 239000000446 fuel Substances 0.000 claims abstract description 9
- 239000000463 material Substances 0.000 claims description 30
- 238000002485 combustion reaction Methods 0.000 claims description 25
- 239000006185 dispersion Substances 0.000 claims description 7
- 239000003245 coal Substances 0.000 abstract description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- 239000002184 metal Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 235000019738 Limestone Nutrition 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 239000006028 limestone Substances 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- 239000004927 clay Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
Landscapes
- Fluidized-Bed Combustion And Resonant Combustion (AREA)
Abstract
Description
【0001】0001
【産業上の利用分野】本発明は、粗粒灰の残る石炭、金
属片や土石等の不燃物を含む廃棄物等の燃料を燃焼し、
不燃物を確実に排出する流動床燃焼炉に関するものであ
る。[Industrial Application Field] The present invention burns fuel such as coal with coarse ash and waste containing incombustible materials such as metal pieces and rocks.
This invention relates to a fluidized bed combustion furnace that reliably discharges incombustible materials.
【0002】0002
【従来の技術】流動燃焼炉は、空気分散板から空気を噴
出させて砂(例えば硅砂)、石灰石などの流動媒体を、
流動化状態にして石炭、廃棄物等の燃料を燃焼させる。
しかし、燃料中に灰分、とくに金属片や土石等の不燃物
が含まれていると、この不燃物が空気分散板上に沈降堆
積して、良好な燃焼状態が維持できなくなる。このため
、従来から不燃物を炉外に排出するための空気分散板の
形状や排出機構に関する提案が種々なされている。[Prior Art] A fluidized combustion furnace blows out air from an air distribution plate to displace a fluidized medium such as sand (for example, silica sand) or limestone.
Burns fuel such as coal and waste in a fluidized state. However, if the fuel contains ash, especially incombustibles such as metal pieces and clay, the incombustibles settle and accumulate on the air distribution plate, making it impossible to maintain good combustion conditions. For this reason, various proposals have been made regarding the shape and discharge mechanism of the air distribution plate for discharging noncombustibles to the outside of the furnace.
【0003】従来の技術としては、例えば、特開昭63
−271016号公報に開示された技術がある。図6は
、特開昭63−271016号公報に記載されている流
動床燃焼炉の内部を示す斜視図である。図6において、
10は炉本体、12は風箱本体、12a〜12cは仕切
壁14によって区画した風箱、16は不燃物排出口、1
8は炉本体の対向する壁面の双方から中央部にむけて、
下方に傾斜させて形成した空気分散板、20は長孔形状
の開口部、22は廃棄物投入口である。[0003] As a conventional technique, for example, Japanese Patent Application Laid-Open No. 63
There is a technique disclosed in Publication No. -271016. FIG. 6 is a perspective view showing the inside of a fluidized bed combustion furnace described in JP-A-63-271016. In Figure 6,
10 is a furnace main body, 12 is a wind box main body, 12a to 12c are wind boxes partitioned by a partition wall 14, 16 is an incombustible material discharge port, 1
8 from both opposing walls of the furnace body toward the center,
The air distribution plate is formed to be inclined downward, 20 is an opening in the shape of a long hole, and 22 is a waste input port.
【0004】この公報記載の流動床燃焼炉においては、
沈降堆積した燃料中の灰分、金属片や土石等を下方に傾
斜させて形成した空気分散板18上を、炉中央部の方向
に移動させて、長孔形状の開口部20を有する不燃物排
出口16から排出させる。In the fluidized bed combustion furnace described in this publication,
The ash, metal pieces, dirt, etc. in the settled fuel are moved onto the air distribution plate 18, which is formed by slanting downward, toward the center of the furnace, and the non-combustible material waste having an elongated opening 20 is removed. It is discharged through outlet 16.
【0005】[0005]
【発明が解決しようとする課題】図6に示されたような
長孔形状の不燃物排出口16から排出する技術は種々あ
るがいずれも問題点がある。[Problems to be Solved by the Invention] There are various techniques for discharging incombustibles from the elongated hole-shaped discharge port 16 as shown in FIG. 6, but all of them have problems.
【0006】図7はその一例を示した図で、16は長孔
形状の不燃物排出口、24は円柱状の回転する歯車で、
その断面図を図8に示している。複数の歯26によって
不燃物が系外に排出される。しかしながら、この方法は
、600〜900℃と高温の流動媒体を取り扱うため耐
熱構造に多大の設備費用がかかるが、それでも信頼性の
高い構造にすることはかなり困難である。また、不燃物
が前記歯26にからまり、安定して排出することが困難
であるFIG. 7 is a diagram showing an example of this, where 16 is a long hole-shaped incombustible material discharge port, 24 is a cylindrical rotating gear,
A sectional view thereof is shown in FIG. Non-combustible materials are discharged from the system by the plurality of teeth 26. However, since this method handles a fluidized medium at a high temperature of 600 to 900° C., it requires a large amount of equipment cost for a heat-resistant structure, but it is still quite difficult to create a highly reliable structure. In addition, non-combustible materials become entangled with the teeth 26, making it difficult to discharge them stably.
【0007】また、図9は、長孔形状の不燃物排出口1
6の下部に、逆円錐台状に絞ったコ−ン部28を連設し
て、その下部に不燃物排出機としてロータリバルブ30
を設けている。この構造の欠点は、図9に示したコーン
部と水平方向との角度θは、石灰石等の流動媒体であれ
ば45度程度必要となり、逆円錐台の高さhが高くなる
ことである。このため設備全体をカサ上げするか、もし
くは、この部分の下部を地下構造にする等の対策が必要
であった。FIG. 9 also shows a long hole-shaped incombustible material discharge port 1.
A cone portion 28 constricted in the shape of an inverted truncated cone is connected to the bottom of the cone 6, and a rotary valve 30 is installed at the bottom of the cone portion 28 as a non-combustible material discharger.
has been established. A disadvantage of this structure is that the angle θ between the cone portion and the horizontal direction shown in FIG. 9 needs to be about 45 degrees for a fluid medium such as limestone, which increases the height h of the inverted truncated cone. For this reason, it was necessary to take measures such as raising the entire facility or creating an underground structure below this part.
【0008】本発明は、上記の諸点に鑑みなされたもの
で、風箱本体を仕切壁で3区画以上に分割し、空気分散
板は、風箱本体の仕切壁の左右側の炉本体の対向する双
方の側壁から、中央の風箱の左右仕切壁まで、下方に傾
斜させて形成し、かつ、中央部の空気分散板は、前記炉
本体の対向する双方の側壁と異なる対向する双方の側壁
から、炉中心部に向けて下方に傾斜させて形成し、炉中
心部に不燃物排出口を設けるか、又は中央部の空気分散
板は、前記炉本体の対向する双方の側壁と異なる対向す
る一方の側壁から、他方の側壁に向けて下方に傾斜させ
て形成し、傾斜下端部に不燃物排出口を設けることによ
り、前記のような従来技術の問題点を解消した、大型炉
にも適用可能な流動床燃焼炉を提供することを目的とす
る。The present invention has been made in view of the above points, and the wind box main body is divided into three or more sections by partition walls, and the air distribution plates are placed on opposite sides of the furnace main body on the left and right sides of the partition walls of the wind box main body. The central air distribution plate is formed to be inclined downward from both side walls of the furnace body to the left and right partition walls of the central wind box, and the air distribution plate in the central part is formed from both opposite side walls that are different from both opposite side walls of the furnace main body. The air dispersion plate is formed so as to be inclined downward toward the center of the furnace, and an incombustible material discharge port is provided in the center of the furnace, or the air distribution plate in the center is formed so as to be tilted downward toward the center of the furnace, or the air distribution plate in the center is formed in a direction different from the opposite side walls of the furnace main body. It is formed by sloping downward from one side wall to the other side wall, and by providing an incombustible material discharge port at the lower end of the slope, the problems of the conventional technology as described above are solved, and it can also be applied to large furnaces. The purpose is to provide a possible fluidized bed combustion furnace.
【0009】[0009]
【課題を解決するための手段】上記の目的を達成するた
めに、請求項1の流動床燃焼炉は、図1〜図3を参照し
て説明すれば、流動媒体を充填し流動床を形成させて燃
料を燃焼させる炉本体10と、この炉本体の下部に設け
られ炉本体に供給する空気を一時貯留する風箱本体12
とこの風箱本体と流動床との間に設けられた空気分散板
18とを備え、風箱本体を縦方向の仕切壁14で少なく
とも3区画の風箱に分割し、空気分散板18を、前記仕
切壁14に略平行な炉本体の対向する双方の側壁10a
、10bから、中央部の風箱の両側の仕切壁の上端まで
、下方に傾斜させて形成し、区画された風箱にそれぞれ
流量調節弁36を備えた空気供給管34を接続した流動
床燃焼炉において、中央部の風箱の上側の空気分散板1
9を、前記仕切壁14に略垂直な炉本体の対向する双方
の側壁10c、10dから、炉中心部に向けて下方に傾
斜させて形成し、中央部の空気分散板19の傾斜下端に
不燃物排出口40を設けたことを特徴としている。[Means for Solving the Problem] In order to achieve the above object, the fluidized bed combustion furnace of claim 1 is provided by filling a fluidized medium to form a fluidized bed, as described with reference to FIGS. 1 to 3. A furnace body 10 that burns fuel by heating the furnace body, and a wind box body 12 that is provided at the bottom of the furnace body and temporarily stores air to be supplied to the furnace body.
and an air dispersion plate 18 provided between the wind box main body and the fluidized bed, the wind box main body is divided into at least three sections of wind boxes by a vertical partition wall 14, and the air dispersion plate 18 is Both opposing side walls 10a of the furnace body substantially parallel to the partition wall 14
, 10b to the upper ends of the partition walls on both sides of the central wind box, and are formed to be inclined downward, and air supply pipes 34 each having a flow rate control valve 36 are connected to the divided wind boxes. In a furnace, the air distribution plate 1 above the central wind box
9 are formed to be inclined downward toward the center of the furnace from both opposing side walls 10c and 10d of the furnace main body that are substantially perpendicular to the partition wall 14, and a non-combustible plate is formed at the inclined lower end of the central air distribution plate 19. A feature is that a material discharge port 40 is provided.
【0010】また、請求項2の流動床燃焼炉は、図5を
参照して説明すれば、請求項1において、中央部の風箱
の上側の空気分散板19を風箱本体を区画する仕切壁1
4に略垂直な炉本体の対向する双方の側壁10c、10
dから、炉中心部にむけて下方に傾斜させて形成する代
わりに、中央部の風箱の上側の空気分散板19aを、風
箱本体を区画する仕切壁14に略垂直な炉本体の一方の
側壁10dから、他方の側壁10cに向けて下方に傾斜
させて形成し、中央部の空気分散板19aの傾斜下端に
不燃物排出口40aを設けたことを特徴としている。Further, the fluidized bed combustion furnace according to claim 2 is explained with reference to FIG. wall 1
Both opposing side walls 10c, 10 of the furnace body substantially perpendicular to 4
d, instead of forming the air dispersion plate 19a on the upper side of the central wind box to be inclined downward toward the center of the furnace, the air dispersion plate 19a on the upper side of the wind box in the center is formed on one side of the furnace main body that is substantially perpendicular to the partition wall 14 that partitions the wind box main body. The air dispersion plate 19a is formed so as to be inclined downward from the side wall 10d toward the other side wall 10c, and a noncombustible material discharge port 40a is provided at the lower end of the inclined air distribution plate 19a in the center.
【0011】さらに、請求項3の流動床燃焼炉は、図4
、図5を参照して説明すれば、請求項1又は2において
、中央部の風箱を、風箱本体を区画する仕切壁14と略
垂直な縦方向の仕切壁42で複数個の区画に仕切り、そ
れぞれの区画に流量調節弁36を備えた空気供給管34
を接続したことを特徴としている。Furthermore, the fluidized bed combustion furnace according to claim 3 has the structure shown in FIG.
, if explained with reference to FIG. 5, in claim 1 or 2, the central wind box is divided into a plurality of sections by vertical partition walls 42 that are substantially perpendicular to the partition wall 14 that partitions the wind box main body. Air supply pipe 34 with a partition and a flow control valve 36 in each compartment
It is characterized by the connection of
【0012】0012
【作用】空気分散板18は、炉本体の対向する側壁10
a、10bの双方から炉中央部にむけて下方に傾斜させ
ているので、不燃物は、炉中央部に向かって移動し、炉
中央部にまで移動した不燃物は、90度方向転換した方
向の炉中心部又は炉側部に向かって移動し、不燃物排出
口40から排出される。[Operation] The air distribution plate 18 is connected to the opposing side wall 10 of the furnace body.
Since both a and 10b are tilted downward toward the center of the furnace, the noncombustibles move toward the center of the furnace, and the noncombustibles that have moved to the center of the furnace are tilted downward by 90 degrees. The incombustible materials move toward the center or side of the furnace and are discharged from the incombustible material discharge port 40.
【0013】[0013]
【実施例】以下、図面を参照して本発明の好適な実施例
を詳細に説明する。ただしこの実施例に記載されている
構成機器の形状、その相対配置などは、とくに特定的な
記載がない限りは、本発明の範囲をそれらのみに限定す
る趣旨のものではなく、単なる説明例にすぎない。DESCRIPTION OF THE PREFERRED EMBODIMENTS Preferred embodiments of the present invention will be described in detail below with reference to the drawings. However, unless there is a specific description, the shapes of the components described in this example, their relative positions, etc. are not intended to limit the scope of the present invention to these, but are merely illustrative examples. Only.
【0014】図1は、本発明の一実施例を示す流動床燃
焼炉の縦断面説明図であり、図2は、図1におけるA−
A線断面説明図、図3は図1の流動床燃焼炉の内部を示
す斜視図である。図1において、10は角型の炉本体、
12は炉本体10の下部に設けた風箱本体、18は空気
分散板、32は空気分散板に多数設けられている空気ノ
ズル、14は風箱本体12を複数の風箱に区画するため
の仕切壁、12d〜12fは風箱、34は3系統に分岐
され風箱12d〜12fにそれぞれ接続する空気供給管
。36は空気流量を調節するための流量調節弁、38は
ブロワーである。図2の40は不燃物排出口、19は中
央部の風箱12fにおける空気分散板である。FIG. 1 is an explanatory longitudinal cross-sectional view of a fluidized bed combustion furnace showing one embodiment of the present invention, and FIG.
3 is a perspective view showing the inside of the fluidized bed combustion furnace of FIG. 1. In FIG. 1, 10 is a rectangular furnace body;
12 is a wind box body provided at the bottom of the furnace body 10, 18 is an air distribution plate, 32 is a large number of air nozzles provided on the air distribution plate, and 14 is a wind box body for dividing the wind box body 12 into a plurality of wind boxes. Partition walls, 12d to 12f are wind boxes, and 34 is an air supply pipe that is branched into three systems and connected to the wind boxes 12d to 12f, respectively. 36 is a flow control valve for adjusting the air flow rate, and 38 is a blower. 40 in FIG. 2 is an incombustible material discharge port, and 19 is an air distribution plate in the central wind box 12f.
【0015】次に、図3により炉の構造について説明す
る。空気分散板18は炉本体の対向する双方の側壁から
、すなわち、仕切壁14に略平行な双方の側壁10a、
10bから炉中央部に向かって下方に傾斜し、中央部の
風箱12fの左右の仕切壁14と接合されている。
風箱12fの空気分散板19は、前記炉本体の対向する
双方の側壁10a、10bとは異なる対向する双方の側
壁10c、10dから、炉中心部に向かって下方に傾斜
し、炉中心部で不燃物排出口40に接合されている。Next, the structure of the furnace will be explained with reference to FIG. The air distribution plate 18 extends from both opposing side walls of the furnace body, that is, from both side walls 10a substantially parallel to the partition wall 14,
It slopes downward from 10b toward the center of the furnace, and is joined to the left and right partition walls 14 of the wind box 12f in the center. The air distribution plate 19 of the wind box 12f is inclined downward toward the furnace center from both opposing side walls 10c and 10d, which are different from the opposing side walls 10a and 10b of the furnace main body. It is connected to the incombustible material discharge port 40.
【0016】このように構成した流動床燃焼炉で不燃物
を含有する燃料を燃焼すると、不燃物は下方に傾斜して
いる空気分散板18によって、炉中央部に移動し、つい
で、炉中央部の空気分散板19によって、更に、炉中心
部に移動し、不燃物排出口40から排出される。When fuel containing non-combustibles is burned in the fluidized bed combustion furnace configured as described above, the non-combustibles are moved to the center of the furnace by the downwardly inclined air distribution plate 18, and then moved to the center of the furnace. The air is further moved to the center of the furnace by the air distribution plate 19 , and is discharged from the incombustible material discharge port 40 .
【0017】各風箱12d〜12fに供給する空気量は
、流量調節弁36によって自由に制御できる。図3は風
箱本体を5分割する場合を示しているが、小容量の流動
床燃焼炉であれば3分割でも良く、大容量になれば7分
割にしても良い。また、4分割にしても良い。この場合
は、不燃物排出口は中心部に設ける必要はなく、偏った
位置に設けてもさしつかえない。The amount of air supplied to each of the wind boxes 12d to 12f can be freely controlled by a flow control valve 36. Although FIG. 3 shows the case where the wind box main body is divided into five parts, it may be divided into three parts if it is a small-capacity fluidized bed combustion furnace, and it may be divided into seven parts if the capacity is large. Alternatively, it may be divided into four parts. In this case, the incombustible material discharge port does not need to be provided in the center, and may be provided in an offset position.
【0018】図4は本発明の他の実施例を示す流動床燃
焼炉の縦断面説明図である。中央部の風箱12fを風箱
本体を区画する仕切壁14と略垂直な仕切壁42で区画
したもので、この例では4区画に風箱12fを区画して
いる。必要に応じてそれぞれの空気配分を変えることが
できる。FIG. 4 is an explanatory longitudinal sectional view of a fluidized bed combustion furnace showing another embodiment of the present invention. The wind box 12f at the center is divided by a partition wall 14 that partitions the wind box main body and a partition wall 42 that is substantially perpendicular to the wind box 12f, and in this example, the wind box 12f is divided into four sections. Each air distribution can be changed as required.
【0019】また、図5に示すように、中央部の風箱1
2fの上側の空気分散板19aを、風箱本体を区画する
仕切壁14に略垂直な炉本体の一方の側壁10dから、
他方の側壁10cにむけて下方に傾斜させて形成し、中
央部の空気分散板19aの傾斜下端、すなわち、炉壁の
片側に不燃物排出口40aを設けるようにすることもで
きる。In addition, as shown in FIG. 5, the wind box 1 in the center
2f upper air distribution plate 19a from one side wall 10d of the furnace body which is approximately perpendicular to the partition wall 14 that partitions the wind box body,
It may also be formed to be inclined downward toward the other side wall 10c, and the incombustible material discharge port 40a may be provided at the inclined lower end of the central air distribution plate 19a, that is, on one side of the furnace wall.
【0020】燃料の供給は、不燃物排出口の上方から行
うように構成すると、不燃物の移動距離が少なくなるの
で望ましい。[0020] It is preferable that the fuel be supplied from above the incombustible material discharge port, since this reduces the distance that the incombustible material moves.
【0021】[0021]
【発明の効果】本発明は上記のように構成されているの
で、つぎのような効果を奏する。
(1) 空気分散板を炉中央部にむけて下方に傾斜さ
せているので、不燃物は中央部に移動し、更に、中央部
の空気分散板によって90度方向転換した方向の炉中心
部又は炉片側に向かって移動し、不燃物排出口から円滑
に排出される。
(2) 炉中央部の空気分散板の下方傾斜によって、
コンパクトで経済的な構造で不燃物が確実に排出できる
。[Effects of the Invention] Since the present invention is constructed as described above, it has the following effects. (1) Since the air distribution plate is tilted downward toward the center of the furnace, incombustible materials move to the center, and the air distribution plate in the center moves the incombustibles to the center of the furnace or It moves toward one side of the furnace and is smoothly discharged from the incombustible material discharge port. (2) Due to the downward tilt of the air distribution plate in the center of the furnace,
Compact and economical structure allows non-combustible materials to be reliably discharged.
【図1】本発明の一実施例を示す流動床燃焼炉の縦断面
説明図である。FIG. 1 is an explanatory longitudinal cross-sectional view of a fluidized bed combustion furnace showing one embodiment of the present invention.
【図2】図1におけるA−A縦断面説明図である。FIG. 2 is an explanatory longitudinal cross-sectional view taken along line AA in FIG. 1;
【図3】図1の流動床燃焼炉の内部を示す斜視図である
。3 is a perspective view showing the inside of the fluidized bed combustion furnace of FIG. 1. FIG.
【図4】本発明の他の実施例を示す流動床燃焼炉の縦断
面説明図である。FIG. 4 is an explanatory longitudinal cross-sectional view of a fluidized bed combustion furnace showing another embodiment of the present invention.
【図5】本発明のさらに他の実施例を示す流動床燃焼炉
の縦断面説明図である。FIG. 5 is an explanatory longitudinal cross-sectional view of a fluidized bed combustion furnace showing still another embodiment of the present invention.
【図6】従来の流動床燃焼炉の一例を示す斜視図である
。FIG. 6 is a perspective view showing an example of a conventional fluidized bed combustion furnace.
【図7】従来の流動床燃焼炉における不燃物排出口まわ
りの一例を示す斜視図である。FIG. 7 is a perspective view showing an example of the vicinity of an incombustible material discharge port in a conventional fluidized bed combustion furnace.
【図8】図7における歯車の断面図である。8 is a sectional view of the gear in FIG. 7. FIG.
【図9】従来の流動床燃焼炉における不燃物排出口まわ
りの他の例を示す斜視図である。FIG. 9 is a perspective view showing another example of the area around the incombustible material discharge port in a conventional fluidized bed combustion furnace.
10 炉本体
10a 側壁
10b 側壁
10c 側壁
10d 側壁
12 風箱本体
14 仕切壁
18 空気分散板
19 中央部の風箱の上側の空気分散板19a
中央部の風箱の上側の空気分散板34 空気供
給管
36 流量調節弁
40 不燃物排出口
40a 不燃物排出口
42 仕切壁10 Furnace main body 10a Side wall 10b Side wall 10c Side wall 10d Side wall 12 Wind box main body 14 Partition wall 18 Air distribution plate 19 Air distribution plate 19a on the upper side of the central wind box
Air distribution plate 34 above the central wind box Air supply pipe 36 Flow rate control valve 40 Incombustibles discharge port 40a Noncombustibles discharge port 42 Partition wall
Claims (3)
燃料を燃焼させる炉本体(10)と、この炉本体の下部
に設けられ炉本体に供給する空気を一時貯留する風箱本
体(12)と、この風箱本体と流動床との間に設けられ
た空気分散板(18)とを備え、風箱本体を縦方向の仕
切壁(14)で少なくとも3区画の風箱に分割し、空気
分散板(18)を、前記仕切壁(14)に略平行な炉本
体の対向する双方の側壁(10a)、(10b)から、
中央部の風箱の両側の仕切壁の上端まで、下方に傾斜さ
せて形成し、区画された風箱にそれぞれ流量調節弁(3
6)を備えた空気供給管(34)を接続した流動床燃焼
炉において、中央部の風箱の上側の空気分散板(19)
を、前記仕切壁(14)に略垂直な炉本体の対向する双
方の側壁(10c)、(10d)から、炉中心部にむけ
て下方に傾斜させて形成し、中央部の空気分散板(19
)の傾斜下端に不燃物排出口(40)を設けたことを特
徴とする流動床燃焼炉。1. A furnace body (10) filled with a fluidized medium to form a fluidized bed to burn fuel, and a wind box body (12) provided at the bottom of the furnace body to temporarily store air to be supplied to the furnace body. ) and an air distribution plate (18) provided between the wind box main body and the fluidized bed, the wind box main body is divided into at least three sections of the wind box by a vertical partition wall (14), An air distribution plate (18) is inserted from both opposing side walls (10a) and (10b) of the furnace body substantially parallel to the partition wall (14),
The partition walls on both sides of the central wind box are formed by slanting downward to the upper ends, and each partitioned wind box is equipped with a flow control valve (3
In a fluidized bed combustion furnace connected to an air supply pipe (34) equipped with 6), the air distribution plate (19) above the central wind box
are formed so as to be inclined downwardly toward the center of the furnace from both opposing side walls (10c) and (10d) of the furnace body that are substantially perpendicular to the partition wall (14), and an air distribution plate ( 19
) A fluidized bed combustion furnace is characterized in that a non-combustible material discharge port (40) is provided at the lower end of the slope.
9)を、風箱本体を区画する仕切壁(14)に略垂直な
炉本体の対向する双方の側壁(10c)、(10d)か
ら、炉中心部に向けて下方に傾斜させて形成する代りに
、中央部の風箱の上側の空気分散板(19a)を、風箱
本体を区画する仕切壁(14)に略垂直な炉本体の一方
の側壁(10d)から、他方の側壁(10c)に向けて
下方に傾斜させて形成し、中央部の空気分散板(19a
)の傾斜下端に不燃物排出口(40a)を設けたことを
特徴とする請求項1記載の流動床燃焼炉。[Claim 2] Air distribution plate (1
9) is formed by slanting downward toward the center of the furnace from both opposing side walls (10c) and (10d) of the furnace main body that are substantially perpendicular to the partition wall (14) that partitions the wind box main body. The air dispersion plate (19a) on the upper side of the central wind box is moved from one side wall (10d) of the furnace main body, which is substantially perpendicular to the partition wall (14) that partitions the wind box main body, to the other side wall (10c). The central air distribution plate (19a
2. The fluidized bed combustion furnace according to claim 1, further comprising an incombustible material discharge port (40a) provided at the lower end of the incombustible material discharge port (40a).
仕切壁(14)と略垂直な縦方向の仕切壁(42)で複
数個の区画に仕切り、それぞれの区画に流量調節弁(3
6)を備えた空気供給管(34)を接続したことを特徴
とする請求項1又は2記載の流動床燃焼炉。3. The central wind box is divided into a plurality of compartments by a vertical partition wall (42) that is substantially perpendicular to the partition wall (14) that partitions the wind box main body, and each compartment is provided with a flow rate control valve. (3
3. The fluidized bed combustion furnace according to claim 1 or 2, further comprising an air supply pipe (34) having an air supply pipe (34) connected thereto.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP41087390A JP2947946B2 (en) | 1990-12-14 | 1990-12-14 | Fluidized bed combustion furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP41087390A JP2947946B2 (en) | 1990-12-14 | 1990-12-14 | Fluidized bed combustion furnace |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH04217708A true JPH04217708A (en) | 1992-08-07 |
JP2947946B2 JP2947946B2 (en) | 1999-09-13 |
Family
ID=18519964
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP41087390A Expired - Fee Related JP2947946B2 (en) | 1990-12-14 | 1990-12-14 | Fluidized bed combustion furnace |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2947946B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5957066A (en) * | 1995-04-26 | 1999-09-28 | Ebara Corporation | Fluidized-bed thermal reaction apparatus |
DE102005061298B4 (en) * | 2005-12-21 | 2010-04-22 | Mitsubishi Heavy Industries, Ltd. | Fluidized bed furnace |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100760724B1 (en) * | 2005-12-23 | 2007-09-21 | 미츠비시 쥬고교 가부시키가이샤 | Fluidized bed furnace |
CN102278744A (en) * | 2010-06-13 | 2011-12-14 | 中国科学院工程热物理研究所 | Air distribution method of primary air for circulating fluidized bed boiler |
-
1990
- 1990-12-14 JP JP41087390A patent/JP2947946B2/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5957066A (en) * | 1995-04-26 | 1999-09-28 | Ebara Corporation | Fluidized-bed thermal reaction apparatus |
US5979341A (en) * | 1995-04-26 | 1999-11-09 | Ebara Corporation | Fluidized-bed thermal reaction apparatus |
DE102005061298B4 (en) * | 2005-12-21 | 2010-04-22 | Mitsubishi Heavy Industries, Ltd. | Fluidized bed furnace |
Also Published As
Publication number | Publication date |
---|---|
JP2947946B2 (en) | 1999-09-13 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JPH04217708A (en) | Fluidized-bed incinerator | |
JP6124453B2 (en) | Circulating fluidized bed boiler | |
JP2764382B2 (en) | Circulating fluidized bed reactor for low-grade fuel | |
US5101742A (en) | Fluidized bed combustion | |
KR880002397B1 (en) | Fluidized bed combustion apparatus | |
US4268244A (en) | Fluid bed furnaces | |
US3577939A (en) | Incinerators | |
US3910207A (en) | Apparatus for pyrolytic decomposition of waste materials | |
JPH07145921A (en) | Fluidized bed incinerator | |
JPH0519044B2 (en) | ||
JP3535835B2 (en) | Fluidized bed incinerator | |
US4306854A (en) | Fluid bed furnaces | |
JPS61205720A (en) | Lateral type fluidized bed type incinerator | |
JPH0725760Y2 (en) | Radioactive waste incinerator | |
CA1119467A (en) | Fluid bed furnaces | |
US3199475A (en) | Municipal incinerators | |
CA1231271A (en) | Stoker | |
US4991519A (en) | Incinerating furnace | |
CN113242950B (en) | Burner air bar for use in a fluidized bed reactor and fluidized bed reactor | |
EP1015813B1 (en) | Solid fuel fired boiler plant and furnace unit and flue gas unit for use in such a boiler plant | |
JPH0461243B2 (en) | ||
US527703A (en) | Brick-kiln | |
JP3317791B2 (en) | Small lump fuel supply device | |
JP2564173Y2 (en) | Air diffuser for fluidized bed incinerator | |
JPS6022242B2 (en) | Fluidized bed combustion equipment |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
S111 | Request for change of ownership or part of ownership |
Free format text: JAPANESE INTERMEDIATE CODE: R313111 |
|
R350 | Written notification of registration of transfer |
Free format text: JAPANESE INTERMEDIATE CODE: R350 |
|
S111 | Request for change of ownership or part of ownership |
Free format text: JAPANESE INTERMEDIATE CODE: R313111 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080702 Year of fee payment: 9 |
|
R350 | Written notification of registration of transfer |
Free format text: JAPANESE INTERMEDIATE CODE: R350 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080702 Year of fee payment: 9 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090702 Year of fee payment: 10 |
|
LAPS | Cancellation because of no payment of annual fees |