JP4019494B2 - Fluidized bed incinerator dust feeder. - Google Patents

Fluidized bed incinerator dust feeder. Download PDF

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Publication number
JP4019494B2
JP4019494B2 JP09068298A JP9068298A JP4019494B2 JP 4019494 B2 JP4019494 B2 JP 4019494B2 JP 09068298 A JP09068298 A JP 09068298A JP 9068298 A JP9068298 A JP 9068298A JP 4019494 B2 JP4019494 B2 JP 4019494B2
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Japan
Prior art keywords
waste
drum
fluidized bed
chute
screw
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Expired - Fee Related
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JP09068298A
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Japanese (ja)
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JPH11270826A (en
Inventor
幹夫 茂木
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IHI Corp
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IHI Corp
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Description

【0001】
【発明の属する技術分野】
本発明は都市ごみ等の廃棄物を流動床式焼却炉内へ供給するための給じん装置に関するものである。
【0002】
【従来の技術】
都市ごみ等の廃棄物を焼却処理する流動床式焼却炉1は、図2に概略を示す如く、上部に廃棄物を投入するためのシュート2を設けた炉体1a内の下部に、流動媒体としての砂4を充填した流動層3を設け、且つ該流動層3に複数の散気管5を水平状態に配して、該散気管5内を通し流動層3内に流動化空気を導入させることにより流動層3を流動化させ、流動層3中で廃棄物を焼却させるようにしてあるのが一般的である。又、この流動床式焼却炉1内へ上記シュート2を通して廃棄物6を供給させるようにする給じん機7としては、流動床式焼却炉1での燃焼において、シール性を保ちながら連続的に廃棄物6を供給する必要があることから、一般的にケーシング7a内でスクリュー7bを回転させることにより廃棄物6を搬送させるようにする、いわゆるスクリュー式給じん機が採用されており、図示しない搬送手段で投入ホッパ8内へ送られて来た廃棄物6をスクリュー式給じん機7で送りながら流動床式焼却炉1内へシュート2を通して投入させるようにしてある。9は頂部に設けた排ガス出口、10は底部に設けた不燃物排出機、11は不燃物とともに落下して排出されて不燃物から分離された流動砂4を流動床式焼却炉1内へ戻すようにする砂循環コンベアである。
【0003】
流動床式焼却炉1では、炉内に投入された廃棄物が急激に短時間で燃焼するため、燃焼を安定させるためには、炉内への廃棄物6の投入を連続的に且つ定量的に行わせることが重要である。
【0004】
【発明が解決しようとする課題】
ところが、都市ごみ等の廃棄物6は、各種大きさの異なる袋に詰められて廃棄されており、給じん機7で流動床式焼却炉1内へ投入させる都市ごみ等の廃棄物6は、袋のままであるため、個々の形状が大きい上に、圧縮性や再膨張性があり、更に、ごみ同士がからみ合ったりしているのが実状である。そのため、従来のスクリュー式給じん機7でかかる都市ごみ等の廃棄物6を連続的に供給する場合は、長時間的に見れば定量性は確保されているように見えるが、短時間で見ると、個々のごみの形状の大きさ等により供給量のばらつきが生じ、供給量の脈動が避けられず、時には、流動床式焼却炉1内へのごみ供給が一時的に中断したり、逆に多量に落ちる、いわゆる、どか落ちが起きてしまう。
【0005】
このような条件では、炉側の制御可能範囲を越える運転条件となってしまうため、本来は完全燃焼性が高い流動床式焼却炉1でありながら瞬時的な温度低下や不完全燃焼が発生して炉の安定燃焼が阻害され、結果的にダイオキシンの発生を招く要因ともなっている。
【0006】
特に、小型炉では、供給されるごみの大きさが大型炉に供給されるごみの大きさと変りはないことから、スクリュー式給じん機7自体も供給量に見合ったスクリューの小型化ができず、大型炉に適用されているものとほとんど同じ規模のものが使用されるため、大型のスクリューを低速回転で使用せざるを得なくなり、ごみの連続的な供給がますますできなくなり、上述した如き炉の安定燃焼性を阻害してダイオキシン発生を招くというようなおそれがより顕著になる、という問題がある。
【0007】
そこで、本発明は、大型炉、小型炉を問わず、都市ごみ等の廃棄物の炉内への供給を、短時間でみても連続的で定量的に行えるようにして、燃焼の安定性を確保してダイオキシンの発生を抑制できるようにしようとするものである。
【0008】
【課題を解決するための手段】
本発明は、上記課題を解決するために、流動床式焼却炉への廃棄物供給のために炉壁に設けられたシュートの入口側と、該シュートを介して炉内へ廃棄物を供給するスクリュー式給じん機の出口側との間に、上記スクリュー式給じん機の出口側に取り付けた入口室と、上記シュートの入口側に取り付けた出口室と、一端を上記入口室に他端を上記出口室にそれぞれシール材を介在させた回転継手で回転自在に接続させた回転ドラムとからなるドラム式搬送機を介在させ、上記スクリュー式給じん機から供給された廃棄物がドラム内に移されると、該廃棄物を回転ドラム内に滞留させながら搬送するようにした上記ドラム式搬送機の出口室からシュートの入口側へ廃棄物を連続的に落下させるようにした構成とする。
【0009】
スクリュー式給じん機から間欠的に送られた廃棄物は、ドラム式搬送機の回転するドラム内で滞留されながら搬送されるので、平均化される。これによりシュートから流動床式焼却炉内への廃棄物の供給は、連続的且つ定量的に行われることになり、炉内での燃焼の安定性が得られる。
【0010】
【発明の実施の形態】
以下、本発明の実施の形態を図面を参照して説明する。
【0011】
図1は本発明の実施の一形態を示すもので、図2に示した流動床式焼却炉1と同様に、炉体1a上部の側壁部に廃棄物投入用のシュート2を設け、且つ炉内下部に砂4を充填してなる流動層3を設け、該流動層3に散気管5を配設して、散気管5から炉内へ吹き込まれる空気により流動層3が流動化されてごみの燃焼が行われるようにしてあり、且つ上記スクリュー式給じん機7で送られる都市ごみ等の廃棄物6をシュート2より炉内へ落下させて供給するようにしてある構成において、横方向に円形の入口14を設け且つ下端に出口15を設けて上記シュート2の上端に出口15をフランジ16で接合できるようにしてある出口室13と、スクリュー式給じん機7のケーシング7a出口側端部の外周に嵌めて固定するようにし且つ上記出口室13の入口14と同じ径の出口18を設けた円筒状の入口室17と、一端を上記出口室13の入口14に回転自在に接続するようにすると共に他端を上記入口室17の出口18に回転自在に接続させるようにする回転ドラム19と、からなるドラム式搬送機12を構成し、該ドラム式搬送機12を、スクリュー式給じん機7とシュート2との間に介在させ、スクリュー式給じん機7から出された都市ごみ等の廃棄物6をドラム式搬送機12の回転ドラム19内に移し、該回転ドラム19を外部からの動力で回転させながら廃棄物6を出口側へと移動させて出口室13よりシュート2内へ落下投入させるようにする。
【0012】
そのために、ドラム式搬送機12は、回転ドラム19を入口側よりも出口側が低くなるように、約3度位傾斜させて配置して、入口側は入口室17の出口18にシール材を介在させた回転継手20で接続すると共に出口側を出口室13の入口14に同様にシール材を介在させた回転継手20で接続し、且つ回転ドラム19の所要個所の外周面にリングギヤ又はタイヤ等21を取り付けて、モータ22の出力軸に取り付けたピニオン又はローラ等23を噛合又は接触させ、モータ22により回転ドラム19を低速で回転させるようにする。
【0013】
更に、シュート2の途中位置に、常時は閉じる方向へ付勢されていて、廃棄物6の落下荷重で下方へ開くようにしてあるシールダンパ24を設置する。
【0014】
スクリュー式給じん機7の投入ホッパ8に、都市ごみ等の廃棄物6が袋に入れられたまま大小異なる大きさで投入されると、スクリュー7bの回転によりホッパ8からケーシング7a内へ廃棄物6は押し込まれて出口側へと搬送される。
【0015】
スクリュー式給じん機7で供給される廃棄物6は、ケーシング内を押されて搬送されるので、連続性があるが、廃棄物6は上述したように大きさもばらばらで圧縮され絡みあっているため、廃棄物6は間欠的にスクリュー式給じん機7を出ることになり、供給量が脈動することになるが、本発明では、スクリュー式給じん機7の出口側にドラム式搬送機12を置いているので、スクリュー式給じん機7による供給量の脈動を、ドラム式搬送機12内でなくして供給量の平均化をすることができる。すなわち、入口室17と出口室13とその間の回転ドラム19とからなるドラム式搬送機12は、回転ドラム19を出口側が若干低くなるように傾斜させて回転させながら徐々に出口側へと廃棄物6を搬送させるようにしてあるので、ドラム式搬送機12の入口室17から回転ドラム19内に移された廃棄物6は、圧縮から解放され該回転ドラム19の回転で円周方向へ移動されて撹拌されながら徐々に出口側へと送られることにより、スクリュー式給じん機7による供給量の脈動が平均化されて行き、回転ドラム19から出口室13に移された廃棄物6は連続的にほぼ定量づつシュート2へ落されることになる。
【0016】
上記において、ドラム式搬送機12の回転ドラム19は、スクリュー式給じん機7から間欠的に供給される廃棄物6の供給量の脈動を吸収するだけの充分な長さを有していればよく、廃棄物の滞留時間から見れば、約5分程度の滞留時間を確保するだけでよい。
【0017】
なお、本発明は上記実施の形態のみに限定されるものではなく、たとえば、大型炉のごみ供給においては、ドラム式搬送機12のドラム19の内部に複数本に分割したドラムを平行に配して、各ドラムに分割してごみを搬送させるようにしてもよい。
【0018】
【発明の効果】
以上述べた如く、本発明の流動床式焼却炉の給じん装置によれば、流動床式焼却炉への廃棄物供給のために炉壁に設けられたシュートの入口側と、該シュートを介して炉内へ廃棄物を供給するスクリュー式給じん機の出口側との間に、上記スクリュー式給じん機の出口側に取り付けた入口室と、上記シュートの入口側に取り付けた出口室と、一端を上記入口室に他端を上記出口室にそれぞれシール材を介在させた回転継手で回転自在に接続させた回転ドラムとからなるドラム式搬送機を介在させ、上記スクリュー式給じん機から供給された廃棄物がドラム内に移されると、該廃棄物を回転ドラム内に滞留させながら搬送するようにした上記ドラム式搬送機の出口室からシュートの入口側へ廃棄物を連続的に落下させるようにした構成としてあるので、次の如き優れた効果を奏し得る。
(1) スクリュー式給じん機による供給量の脈動を、ドラム式搬送機内で平均化し、スクリュー式給じん機で炉内へ供給する場合に発生し易い瞬時的な供給中断や一時的に多量に落ちるという現象があってもドラム内で平均化されて炉内への直接的な影響を及ぼすことがなくなる。
(2) ドラム式搬送機の回転ドラムを回転させながら廃棄物を搬送できるので、廃棄物をシュートへ連続的に且つ定量的に落して供給ができると共に、ドラム内の撹拌によって均質化が期待できる。
(3) 上記(2) により炉内で制御不能になるような状態を皆無にすることができて、燃焼の安定化が確保され、ダイオキシンの発生を抑制できる。
(4) プラント全体的には変動幅が小さくなるため、炉の大きさや通風、排ガス処理系統の機器に過剰な余裕をもたせる必要がなくなる。
(5) 小型炉にスクリュー式給じん機を使用する場合の問題をなくすことができる。
【図面の簡単な説明】
【図1】本発明の流動床式焼却炉の給じん装置の概要を示す概略側面図である。
【図2】従来の流動床式焼却炉の給じん装置の概略側面図である。
【符号の説明】
1 流動床式焼却炉
2 シュート
3 流動層
5 散気管
6 廃棄物
7 スクリュー式給じん機
12 ドラム式搬送機
13 出口室
17 入口室
19 回転ドラム
20 回転継手
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a dust supply device for supplying waste such as municipal waste into a fluidized bed incinerator.
[0002]
[Prior art]
As shown schematically in FIG. 2, a fluidized bed incinerator 1 for incinerating waste such as municipal waste is provided with a fluidized medium in a lower part in a furnace body 1a provided with a chute 2 for introducing waste into the upper part. A fluidized bed 3 filled with sand 4 is provided, and a plurality of diffuser tubes 5 are arranged horizontally in the fluidized bed 3, and fluidized air is introduced into the fluidized bed 3 through the diffuser tubes 5. In general, the fluidized bed 3 is fluidized, and the waste is incinerated in the fluidized bed 3. Further, as a dust feeder 7 for supplying the waste 6 through the chute 2 into the fluidized bed incinerator 1, the combustion in the fluidized bed incinerator 1 is continuously performed while maintaining the sealing performance. Since it is necessary to supply the waste 6, a so-called screw-type dust feeder is generally employed in which the waste 6 is conveyed by rotating the screw 7 b in the casing 7 a, not shown. The waste 6 sent into the charging hopper 8 by the conveying means is fed through the chute 2 into the fluidized bed incinerator 1 while being fed by the screw type feeder 7. 9 is an exhaust gas outlet provided at the top, 10 is an incombustible material discharge machine provided at the bottom, 11 is returned to the fluidized bed incinerator 1 with the fluidized sand 4 that has fallen and discharged together with the incombustible material and separated from the incombustible material. It is a sand circulation conveyor.
[0003]
In the fluidized bed incinerator 1, the waste thrown into the furnace burns rapidly and in a short time. Therefore, in order to stabilize the combustion, the waste 6 is continuously and quantitatively charged into the furnace. It is important to let
[0004]
[Problems to be solved by the invention]
However, the waste 6 such as municipal waste is packed and discarded in bags of various sizes, and the waste 6 such as municipal waste that is thrown into the fluidized bed incinerator 1 by the feeder 7 is Since it remains a bag, the individual shapes are large, and there are compressibility and re-expansion properties, and the fact is that the garbage is entangled with each other. Therefore, when the waste 6 such as municipal waste is continuously supplied by the conventional screw-type dust feeder 7, it seems that the quantitativeness is ensured in a long time, but it is seen in a short time. In addition, the amount of supply varies depending on the size of the individual waste, and the pulsation of the amount of supply is unavoidable. Sometimes, the supply of waste into the fluidized bed incinerator 1 is temporarily interrupted, A so-called "fallen" fall occurs.
[0005]
Under such conditions, the operating conditions exceed the controllable range on the furnace side, so that although the fluidized bed incinerator 1 is originally highly combustible, an instantaneous temperature drop or incomplete combustion occurs. As a result, stable combustion of the furnace is hindered, resulting in the generation of dioxins.
[0006]
In particular, in a small furnace, since the size of the supplied garbage is the same as the size of the garbage supplied to the large furnace, the screw type feeder 7 itself cannot reduce the size of the screw in accordance with the supply amount. Because almost the same scale as that used in large furnaces is used, large screws have to be used at low speed, and continuous supply of waste becomes increasingly impossible. There is a problem that the risk of inhibiting the stable flammability of the furnace and causing dioxin generation becomes more prominent.
[0007]
Therefore, the present invention enables continuous and quantitative supply of waste such as municipal waste into a furnace regardless of whether it is a large furnace or a small furnace, thereby improving the stability of combustion. It is intended to ensure that dioxin generation can be suppressed.
[0008]
[Means for Solving the Problems]
In order to solve the above problems, the present invention supplies waste into the furnace through the chute inlet side provided on the furnace wall for supplying waste to the fluidized bed incinerator and the chute. Between the outlet side of the screw-type dust feeder, an inlet chamber attached to the outlet side of the screw-type feeder, an outlet chamber attached to the inlet side of the chute, one end to the inlet chamber and the other end A drum-type transporter composed of a rotary drum that is rotatably connected to each of the outlet chambers by a rotary joint having a sealant interposed therebetween is interposed, and waste supplied from the screw-type dust feeder is transferred into the drum. are the, and so the configuration is continuously falling waste from the outlet chamber of the drum-type conveyor which is adapted to convey while staying the waste in the rotary drum to the inlet side of the chute.
[0009]
Since the waste sent intermittently from the screw type feeder is transported while being retained in the rotating drum of the drum type transporter, it is averaged. Thereby, the supply of waste from the chute into the fluidized bed incinerator is performed continuously and quantitatively, and the stability of combustion in the furnace is obtained.
[0010]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
[0011]
FIG. 1 shows an embodiment of the present invention. Like the fluidized bed incinerator 1 shown in FIG. 2, a chute 2 for introducing waste is provided on the side wall of the furnace body 1a, and the furnace A fluidized bed 3 filled with sand 4 is provided in the inner and lower part, a diffuser pipe 5 is provided in the fluidized bed 3, and the fluidized bed 3 is fluidized by the air blown from the diffuser pipe 5 into the furnace. In a configuration in which wastes 6 such as municipal waste sent by the screw feeder 7 are dropped from the chute 2 into the furnace and supplied in the horizontal direction. An outlet chamber 13 provided with a circular inlet 14 and an outlet 15 at the lower end so that the outlet 15 can be joined to the upper end of the chute 2 with a flange 16; and an end portion on the outlet side of the casing 7a of the screw type dust feeder 7. Fitted and fixed to the outer periphery of the outlet A cylindrical inlet chamber 17 provided with an outlet 18 having the same diameter as the inlet 14 of the thirteen, and one end rotatably connected to the inlet 14 of the outlet chamber 13 and the other end of the outlet 18 of the inlet chamber 17. A drum-type transporter 12 comprising a rotary drum 19 that is rotatably connected to the screw-type transporter 12, the drum-type transporter 12 being interposed between the screw-type dust feeder 7 and the chute 2, and a screw Waste 6 such as municipal waste discharged from the type dust feeder 7 is transferred into the rotary drum 19 of the drum type transporter 12, and the waste 6 is moved to the outlet side while rotating the rotary drum 19 with external power. And is dropped into the chute 2 from the outlet chamber 13.
[0012]
For this purpose, the drum-type transport machine 12 is arranged so that the rotary drum 19 is inclined by about 3 degrees so that the outlet side is lower than the inlet side, and a sealing material is interposed at the outlet 18 of the inlet chamber 17 on the inlet side. The rotary joint 20 is connected and the outlet side is connected to the inlet 14 of the outlet chamber 13 by a rotary joint 20 having a sealing material interposed therebetween. Is attached, and a pinion or roller 23 attached to the output shaft of the motor 22 is engaged or brought into contact with the motor 22 so that the rotary drum 19 is rotated at a low speed by the motor 22.
[0013]
Further, a seal damper 24 that is normally urged in the closing direction and is opened downward by a drop load of the waste 6 is installed at a position in the middle of the chute 2.
[0014]
When waste 6 such as municipal waste is put in the bag hopper 8 of the screw-type dust feeder 7 in different sizes, the waste is put into the casing 7a from the hopper 8 by the rotation of the screw 7b. 6 is pushed and conveyed to the exit side.
[0015]
Since the waste 6 supplied by the screw type dust feeder 7 is pushed and conveyed in the casing, there is continuity. However, as described above, the waste 6 is compressed in various sizes and entangled. For this reason, the waste 6 intermittently exits the screw type feeder 7 and the supply amount pulsates. In the present invention, the drum type conveyor 12 is disposed at the outlet side of the screw type feeder 7. Therefore, the pulsation of the supply amount by the screw type dust feeder 7 can be averaged without the pulsation of the supply amount in the drum type transporter 12. That is, the drum-type transport machine 12 including the inlet chamber 17, the outlet chamber 13, and the rotating drum 19 between them gradually disposes the waste toward the outlet side while rotating the rotating drum 19 so that the outlet side is slightly lowered. 6, the waste 6 transferred from the inlet chamber 17 of the drum type transporter 12 into the rotary drum 19 is released from compression and moved in the circumferential direction by the rotation of the rotary drum 19. By gradually feeding to the outlet side while being stirred, the pulsation of the supply amount by the screw type feeder 7 is averaged, and the waste 6 transferred from the rotary drum 19 to the outlet chamber 13 is continuously produced. Will be dropped to the chute 2 almost every time.
[0016]
In the above, if the rotary drum 19 of the drum type transporter 12 has a sufficient length to absorb the pulsation of the amount of waste 6 supplied intermittently from the screw type feeder 7. Well, from the viewpoint of waste residence time, it is only necessary to secure a residence time of about 5 minutes.
[0017]
The present invention is not limited to the above-described embodiment. For example, in the case of garbage supply for a large furnace, a plurality of divided drums are arranged in parallel inside the drum 19 of the drum-type transporter 12. Then, the waste may be conveyed by being divided into each drum.
[0018]
【The invention's effect】
As described above, according to the feeder of the fluidized bed incinerator of the present invention, the chute inlet side provided on the furnace wall for supplying waste to the fluidized bed incinerator, and the chute An inlet chamber attached to the outlet side of the screw type feeder, an outlet chamber attached to the inlet side of the chute, between the outlet side of the screw type feeder that supplies waste into the furnace, Supplied from the screw-type dust feeder by interposing a drum-type transporter composed of a rotary drum that is rotatably connected by a rotary joint with one end at the inlet chamber and the other end at the outlet chamber with a sealant interposed therebetween. When the discharged waste is transferred into the drum, the waste is continuously dropped from the outlet chamber of the drum-type transporter, which is transported while staying in the rotating drum , to the inlet side of the chute. configuration and Citea that way So, it can achieve the following of such excellent effect.
(1) The pulsation of the supply amount by the screw type dust feeder is averaged in the drum type transporter, and momentary supply interruption or a temporary large amount that easily occurs when the screw type feeder is fed into the furnace. Even if there is a phenomenon of falling, it is averaged in the drum and does not directly affect the furnace.
(2) Since the waste can be transported while rotating the rotating drum of the drum type transporter, the waste can be supplied continuously and quantitatively to the chute, and homogenization can be expected by stirring in the drum. .
(3) According to the above (2), it is possible to eliminate the state in which control is impossible in the furnace, to ensure the stabilization of combustion, and to suppress the generation of dioxins.
(4) Since the fluctuation range of the plant as a whole is small, it is not necessary to provide an excessive margin for the size of the furnace, ventilation and equipment of the exhaust gas treatment system.
(5) The problem when using a screw type duster in a small furnace can be eliminated.
[Brief description of the drawings]
FIG. 1 is a schematic side view showing an outline of a dust feeding device of a fluidized bed incinerator according to the present invention.
FIG. 2 is a schematic side view of a conventional fluidized bed incinerator dust feeder.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Fluidized bed incinerator 2 Chute 3 Fluidized bed 5 Aeration pipe 6 Waste 7 Screw type feeder 12 Drum-type transport machine 13 Outlet chamber 17 Inlet chamber 19 Rotating drum 20 Rotating joint

Claims (1)

流動床式焼却炉への廃棄物供給のために炉壁に設けられたシュートの入口側と、該シュートを介して炉内へ廃棄物を供給するスクリュー式給じん機の出口側との間に、上記スクリュー式給じん機の出口側に取り付けた入口室と、上記シュートの入口側に取り付けた出口室と、一端を上記入口室に他端を上記出口室にそれぞれシール材を介在させた回転継手で回転自在に接続させた回転ドラムとからなるドラム式搬送機を介在させ、上記スクリュー式給じん機から供給された廃棄物がドラム内に移されると、該廃棄物を回転ドラム内に滞留させながら搬送するようにした上記ドラム式搬送機の出口室からシュートの入口側へ廃棄物を連続的に落下させるようにしたことを特徴とする流動床式焼却炉の給じん装置。Between the inlet side of the chute provided on the furnace wall for supplying the waste to the fluidized bed incinerator and the outlet side of the screw type dust feeder that supplies the waste into the furnace through the chute , An inlet chamber attached to the outlet side of the screw-type dust feeder, an outlet chamber attached to the inlet side of the chute, and rotation with one end interposed in the inlet chamber and the other end in the outlet chamber. When a waste material supplied from the screw type dust feeder is moved into the drum by interposing a drum-type transporter composed of a rotary drum that is rotatably connected by a joint, the waste material stays in the rotary drum . feeding dust device fluidized bed incinerator, characterized in that from the outlet chamber of the drum-type conveyor which is adapted to convey while so as to continuously drop the waste into the inlet side of the chute.
JP09068298A 1998-03-20 1998-03-20 Fluidized bed incinerator dust feeder. Expired - Fee Related JP4019494B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP09068298A JP4019494B2 (en) 1998-03-20 1998-03-20 Fluidized bed incinerator dust feeder.

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Application Number Priority Date Filing Date Title
JP09068298A JP4019494B2 (en) 1998-03-20 1998-03-20 Fluidized bed incinerator dust feeder.

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JP4019494B2 true JP4019494B2 (en) 2007-12-12

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JP6292149B2 (en) * 2015-03-11 2018-03-14 Jfeスチール株式会社 Gas seal device and gas seal method for rotary kiln
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