JPS5843318A - Discharging device for fluidized bed incinerator - Google Patents
Discharging device for fluidized bed incineratorInfo
- Publication number
- JPS5843318A JPS5843318A JP14208881A JP14208881A JPS5843318A JP S5843318 A JPS5843318 A JP S5843318A JP 14208881 A JP14208881 A JP 14208881A JP 14208881 A JP14208881 A JP 14208881A JP S5843318 A JPS5843318 A JP S5843318A
- Authority
- JP
- Japan
- Prior art keywords
- screw
- incinerator
- fluidized bed
- sand
- casing
- 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
- 238000007599 discharging Methods 0.000 title claims description 11
- 239000004576 sand Substances 0.000 claims abstract description 37
- 239000000463 material Substances 0.000 claims description 28
- 230000005484 gravity Effects 0.000 claims description 7
- 239000000428 dust Substances 0.000 abstract description 7
- 239000000126 substance Substances 0.000 abstract 3
- 238000007789 sealing Methods 0.000 description 8
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- 239000010813 municipal solid waste Substances 0.000 description 6
- 238000002485 combustion reaction Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000012530 fluid Substances 0.000 description 4
- 230000003068 static effect Effects 0.000 description 4
- 238000005243 fluidization Methods 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 238000004056 waste incineration Methods 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 239000006185 dispersion Substances 0.000 description 2
- 238000012856 packing Methods 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- 241000272201 Columbiformes Species 0.000 description 1
- 208000012868 Overgrowth Diseases 0.000 description 1
- 241000251131 Sphyrna Species 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 210000004907 gland Anatomy 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000009877 rendering Methods 0.000 description 1
- 239000003566 sealing material Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/30—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having a fluidised bed
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Gasification And Melting Of Waste (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は都市とみなどを焼却する流動層焼却炉から出る
不燃物を排出する排出装置に関す:るも′のである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a discharge device for discharging incombustible materials from a fluidized bed incinerator for incinerating urban areas.
”近年、ごみなどの焼却炉においては、ストー′カ炉よ
シも燃焼効率のよい流動層炉が用い虻れてきている。特
に最近開発されている、は埋垂直面内に関して旋回する
垂直面旋回流動層を有。``In recent years, fluidized bed incinerators, which have better combustion efficiency than stoker incinerators, have come into use as waste incinerators. Has a swirling fluidized bed.
する流動層焼却炉においては、比較的大寸法の不燃物が
混入しても流動層の流動化が阻害□されないi長かあ)
、また可燃物も破砕を行なわなくとも十分効率のよい燃
焼を行な佼こと□がで1 。In a fluidized bed incinerator, the fluidization of the fluidized bed is not inhibited even if relatively large incombustibles are mixed in.
Also, combustible materials can be burned efficiently without crushing them.
るので、この形式□の炉が多く用い゛られるよ5になり
た。−
しかしながら、不燃物の排出装置として通常用いられて
いるスクリューコンベヤにおいては、大寸法の11受は
入れる不燃物中の鉄片などが噛み込んで破損を招き、或
いは運転不能となる。Therefore, furnaces of this type □ are often used5. - However, in a screw conveyor that is normally used as a device for discharging non-combustible materials, the large size 11 receivers may become jammed with iron pieces contained in the non-combustible materials, causing damage or rendering the conveyor inoperable.
一方、炉内圧のシールが不完全であるとグランドパツキ
ンからのガス漏洩が生じ事故を招くおそれがある。On the other hand, if the sealing of the furnace internal pressure is incomplete, gas leakage from the gland packing may occur, leading to an accident.
従来スクリューコンベヤのスクリューにては、流動媒体
である砂と不燃物(砂中to−Jo@)。In the conventional screw conveyor, the fluid medium is sand and non-combustible materials (to-Jo in the sand).
輸送と、炉内圧シールの二つの機能を持九せていたため
に、ねじ羽根とケーシングとの間のタリャランスを極力
小さくする゛ことが望まれ、J〜10−程度にとられて
いた。このため、炉内圧のシール作用は確保されるもの
の、狭い隙間は鉄片などが噛み込むと一転不能となシ、
再起動も困難となシ、作−能率、t−著しく低下せしめ
、また保守も容易でなかつ殖。Since it had two functions: transportation and furnace pressure sealing, it was desired to make the tally balance between the screw vane and the casing as small as possible, and it was set to about J~10-. For this reason, although the sealing effect of the furnace internal pressure is ensured, if a piece of iron gets caught in the narrow gap, it may become impossible to change the situation.
It is difficult to restart, which significantly reduces production efficiency, and it is not easy to maintain and overgrowth.
本発明は・焼却炉0不一:i排出01C接続す1シエー
ドの高さを焼却炉中の流動層静止高さよ)も大きくとる
(好ましくは流動層静止高さ×砂の見掛比重よシも大き
くとシ)ことによシ。In the present invention, the height of the incinerator 0: i discharge 01C connection 1 shade is set to be larger than the static height of the fluidized bed in the incinerator (preferably the height of the fluidized bed at rest x the apparent specific gravity of sand). Also big and shi) especially shi.
従来のものの上記の欠点を除き、かなシの大暑さの不燃
物が混入しても噛み込みを生ずることなく、しかも炉内
圧のシールを十分性なうことができる排出装置を提供す
ることを目的とするものである。It is an object of the present invention to provide a discharge device which eliminates the above-mentioned drawbacks of the conventional device, does not cause jamming even when extremely hot non-combustible materials are mixed in, and is capable of sufficiently sealing the furnace internal pressure. That is.
本発明は流動層焼却炉の不燃物を排出する排出装置にお
いて、前記流動層焼却炉の不燃物排出口に上端が接続さ
れ、不燃物を重力により降下せしめるよう案内するシュ
ートと、該シュートの下端に入口が接続されるスクリュ
ーコンベヤとを備え、前記シェードの高さは、前記流動
層焼却炉中の流動静止高さよルも大きくと夛。The present invention provides a discharge device for discharging noncombustibles from a fluidized bed incinerator, including a chute whose upper end is connected to a noncombustibles discharge port of the fluidized bed incinerator and which guides the noncombustibles to fall by gravity, and a lower end of the chute. a screw conveyor with an inlet connected to the incinerator, and the height of the shade is greater than the static height of the fluid in the fluidized bed incinerator.
スクリューコンベヤの入口の輸送方向側の側壁より輸送
方向側の位置にて砂、不燃物の輸送用のねじ羽根が始、
まるよ5にスクリューを設けてなル、更に前記・入口直
下よシ始まる反軸送方向!″
に小直径のねじ・、:嬰根を備えるか又はねじ羽根なし
とし、砂の流堕を円滑にする丸めの傾斜ケーシングを設
け、輸送用のねじ羽根とスクリューコンベヤのケーシン
グ間の空隙を十分大としたlf#徽を有するものである
。The screw blades for transporting sand and non-combustible materials start at a position on the transport direction side from the side wall on the transport direction side of the entrance of the screw conveyor.
A screw is installed in Maruyo 5, and furthermore, the counter-axial feed direction starts just below the inlet! ″ with small diameter screws: with or without screw blades, with a rounded inclined casing for smooth sand flow, and with sufficient air space between the screw blades for transportation and the casing of the screw conveyor. It has a large lf# image.
本発明を実施例につき図面を用いて説明、すれば、第1
図は都市ごみ焼却設備に、おける−例であり、ピッ)/
に貯留され九と、みをクレーン−のパケットJによ〕ホ
ッパ亭に投じ、給じん装置、!によシ焼却炉6に供給す
るように−っている。焼却炉6においては、プ、ロワフ
によシ供給された流動化空気が、分散板tから上方に炉
内に、噴出し、傾斜壁デに当たっては埋垂直面内の旋回
流ioとなり、砂などの流動媒体をこれに桐って流、動
せしめて、旋回流動層が形成される。The present invention will be explained using the drawings with reference to the embodiments.
The figure is an example of what can be installed in a municipal waste incineration facility.
The 9 and 9 stored in the hopper were dumped into the hopper by the crane's packet J, and the dust supply device,! It is intended to be supplied to the incinerator 6. In the incinerator 6, the fluidized air supplied by the blower blows out from the dispersion plate t upward into the furnace, and when it hits the inclined wall, it becomes a swirling flow io in the buried vertical plane, dispersing sand, etc. A swirling fluidized bed is formed by flowing and moving a fluidized medium through this.
さらに、炉内中央、K下降移動層が!成され、この旋回
流動層及び下降移動、層管よつ、てごみは短時間に嵐好
な燃焼を行ない、破砕が、予め行なわれなくとも、流動
化を阻害することなく高i燃焼効率を得ることができる
。Furthermore, there is a downwardly moving K layer in the center of the furnace! This swirling fluidized bed, descending movement, layer pipes, and waste can be burned efficiently in a short period of time, and even if crushing is not performed in advance, high combustion efficiency can be achieved without impeding fluidization. Obtainable.
llは燃焼排ガスダクト、lコは不燃物排出口置、/J
は振動篩、/41は塊状不燃物排出用のコンベヤ、/に
は砂などの流動媒体の回収用のエレベータである。ll is the combustion exhaust gas duct, l is the incombustible material discharge port, /J
is a vibrating sieve, /41 is a conveyor for discharging lumpy incombustibles, and / is an elevator for collecting fluidized media such as sand.
給しん装置!において、16はごみの入口、lりは砂袋
、破壊され九あとのごみの出口、ig唸焼却炉6に入れ
ることが許されない大きな不燃物の排出口、19は戻し
シュートである。Feeding device! , 16 is an inlet for garbage, 1 is a sand bag, an outlet for destroyed and leftover garbage, an outlet for large non-combustible materials that are not allowed to enter the incinerator 6, and 19 is a return chute.
給じん装置Iは、例えば発明者らが発明し、先−゛昭和
j!年//月17日付で出願した給じん装置の明細書に
示す如き構造のものが用いら□れるi即ち、互に逆ねじ
れ方向の一本のスクリューが平行にJかつ互に逆方向に
回転するように゛配備され、該一本のスクリューの軸間
距離に対して、挾み込まれるごみによシ、該一本のスク
リューi押し広げようとする拡大力が、所定の許容拡大
力を越えないように軸−距離調節が行なわれ、また、こ
の2本のスクリューの軸間゛距離が、所定の定常時最大
軸間距離に達しても前記拡大力が゛なお前記許容拡大力
を越えている鳩舎に杜、前記一本のスクリューは、□逆
移送のための逆回転を行ない、前記軸間距離は前記定常
時最大軸間距離よ1拡大せしめられ、異物を逆移送し排
出するようにしである。The dust supply device I was invented by the inventors, for example, in the Showa era! A structure as shown in the specification of the dust supply device filed on 17th January 2015 is used.In other words, one screw with opposite helical directions rotates in parallel and in opposite directions. The expansion force that tries to push and spread the one screw i due to the trapped debris exceeds a predetermined allowable expansion force for the distance between the axes of the one screw. The axis-to-axis distance is adjusted so that the distance between the two screws does not exceed the allowable expansion force, and even if the distance between the two screws reaches the maximum distance in steady state, the expansion force still exceeds the allowable expansion force. In the pigeon house, the single screw rotates in the opposite direction for reverse transport, and the distance between the shafts is increased by 1 from the maximum distance between the shafts in the steady state, so that the foreign matter is reversely transported and discharged. It's Nishide.
このような構成の給じん装置3により、ごみは予め破砕
をすることを必要とせず、給じん装置Sにより破袋、破
壊を行なう程度でごみを焼却炉6に供給することができ
、可燃物も不燃物もかなシ寸法の大きい“ものでも通過
を許す。With the dust supply device 3 having such a configuration, it is not necessary to crush the garbage in advance, and the garbage can be supplied to the incinerator 6 by simply tearing and destroying the bags by the dust supply device S, and combustible materials can be Even non-combustible items and large items are allowed to pass through.
上記の如き構成の一対のスクリューを豪数対並べて配備
してもよい。A pair of screws configured as described above may be arranged side by side.
次に本発明の不燃物排出装置/Jの実施例につき述べる
。Next, an embodiment of the incombustible material discharging device/J of the present invention will be described.
第2図及び第3図において、焼却炉6の炉底の傾斜した
分散板tの最下端に、不燃物を排出する排出口J/に接
続し、不燃物を重力により降下せしめるよう案内する急
勾配のシエートコーが設ゆられている。シエートコーの
下端にはスクリューコンベヤJJが接続している。In FIGS. 2 and 3, a steep slope is connected to the lowest end of the inclined dispersion plate t at the bottom of the incinerator 6, and is connected to a discharge port J/ for discharging noncombustibles, and guides the noncombustibles to fall by gravity. A sloping slope has been established. A screw conveyor JJ is connected to the lower end of the sheet conveyor.
第参図はスクリューコンづヤの縦断面図、第″9は第“
@1″一部−@ 、、’、第”1は第“図0”−”W′
″I!!Q、II7@t″シー0”−”−である。機台
J41に固定され・九円筒形のケーシングJ!には軸コ
ロに外周の直径の大きい一対の互に逆方向にねじれ九ね
じ羽根J7を備え九スクリエーコtが挿通してお9、ケ
ーシングJj外にて機台Jlに固定された台コ、Oに固
定され九軸受コデに軸J6の両端に(支)定されたジャ
ーナル部コ4aが嵌入して軸コロは支持されており、ジ
ャーナル部コAIL端には図示されない駆動源よシ駆動
されるチェンホイルJlが固定されている。スクリュー
コlの軸方向の中央はねじ羽根を有せずその下方に出口
JJが設けである。The 9th figure is a vertical cross-sectional view of the screw conveyor, and the 9th figure is the 9th one.
@1″Part-@ ,,',The 1st is the 1st part of the figure 0-W′
"I!!Q, II7@t"C0"-"-. Fixed to machine base J41, nine cylindrical casing J! The shaft roller is equipped with a pair of nine threaded blades J7 having a large diameter on the outer periphery and twisted in opposite directions, and nine screw blades t are inserted into the shaft roller. A journal part 4a fixed to both ends of the shaft J6 is fitted into the nine bearings, and the shaft rollers are supported, and the journal part AIL end is driven by a drive source (not shown). Chain wheel Jl is fixed. The axial center of the screw col has no screw blades, and an outlet JJ is provided below it.
ねじ羽根コブの外周とケーシングコ!の内壁との間の空
11Gは比較的大きく中径方向に!θ〜−〇〇−程度を
有する。ケーシングコIの両端には砂の流れに沿った傾
斜(am−411〜700)の゛傾斜JIIJJを持つ
傾斜ケーシングJ4Iが嵌入してお9、傾斜ケーシング
J4Iの7ランジを間にしてケーシングJ9□□Iの台
J0と一体の端板sjを重ねて傾斜ケ→−でングJ参、
端板3!がケーシングJ!に固定去れている・
端板J!の中心にはスタフイングボックスJ4が形成さ
れ、スタフイングボックスJ6には軸封材3りが嵌入し
ており、スタフイングボックスJ6に嵌入して図示され
ない植ボルトとナツトによシスタフイングボックスJ6
に向って推進させられるようにパツキン押えダlが設け
である。The outer circumference of the screw vane knob and the casing! The air space 11G between the inner wall of It has about θ~-〇〇-. Slanted casing J4I with an inclination JIIJJ of slope (am-411 to 700) following the flow of sand is fitted into both ends of casing Co.9, and casing J9 □Overlap the end plate sj that is integrated with the stand J0 of I, and attach the inclined cage → −Deng J,
End plate 3! is casing J! It is fixed to the end plate J! A stuffing box J4 is formed in the center of the stuffing box J6, and a shaft sealing material 3 is fitted into the stuffing box J6.
A packing presser l is provided so that it can be propelled towards.
傾斜ケーシングJ#は前述した取付のための端部フラン
ジ部分よ〕ケーシングJ!に若干の隙間おい九円筒形外
周材とねじ羽@、ioの外周とは隙間を少くした円筒形
内周材と第7図に示すように上部が方形で下部が楕円形
の平面の傾斜壁JJよりなっている。ねじ羽根30は図
示のようにシュートココ下方に若干出ている。ねじ羽t
lJtはケーシングJjの入口Jj&の扱い物がねじ羽
根−りによシ送られる方向の側の側壁Jjt)のほぼ直
下よシも輸送方向側にて始まっている。Inclined casing J# is the end flange part for installation mentioned above] Casing J! There is a slight gap between the 9 cylindrical outer circumferential material and the outer periphery of the screw wing @, and the cylindrical inner circumferential material with a small gap between the two and the slanted wall whose upper part is square and whose lower part is oval as shown in Figure 7. It is made from J.J. The screw blade 30 protrudes slightly below the chute as shown. screw wing t
lJt starts on the transport direction side, almost directly below the side wall Jjt) of the inlet Jj& of the casing Jj in the direction in which the objects to be handled are conveyed by the screw blades.
ねじ羽根J0の作用はスタフイングボックスJ6に向け
て砂が移動し軸封装置を讐傷するのを防止するためのも
のでそのねじれ方向は同一側にあるねじ羽根コクと同じ
ねじれ方向である。The action of the screw blade J0 is to prevent sand from moving toward the stuffing box J6 and damaging the shaft sealing device, and its twisting direction is the same as that of the screw blade on the same side.
従ってねじ羽@SOをなくして傾斜ケーシングJ41の
内周管軸−6と隙間を少くして嵌合しスタフイングボッ
クスJ4に向けて砂が移動しないようにしてもよい、J
t、410はケーシングJjの点検口を蔽ってケーシン
グ−!に固定せられたカバーである。41Jはジャーナ
ル部JAaoyyyy外周に設けた一対り′グ1あ6・
トStを弄して振動篩/Jに接続する。第1図に示す如
く、振動篩/Jの篩上分(大寸法の一一片などの不燃物
)はコンベヤ/411によ〕移送され、篩下分(流動媒
体その他細粉の不燃物)は、必要に応じて流動媒体を分
離再生してエレベータl!により再び焼却炉6に投入さ
れる。Therefore, it is possible to eliminate the screw wing @SO and fit it with the inner circumferential tube shaft -6 of the inclined casing J41 with a small gap to prevent the sand from moving toward the stuffing box J4.
t, 410 covers the inspection port of casing Jj and casing-! This is a cover fixed to the 41J is a pair of grooves 1A6 provided on the outer periphery of the journal part JAaoyyyy.
Adjust St to connect to vibrating sieve/J. As shown in Fig. 1, the upper part of the vibrating sieve/J (non-combustible materials such as large pieces) is transferred to the conveyor/411, and the lower part (fluid medium and other non-combustible materials such as fine powder) is transferred to the conveyor/411. Separates and regenerates the fluid medium as needed to make the elevator l! It is then put into the incinerator 6 again.
作用につき説明する。The effect will be explained.
先ず炉内圧シール作用につき説明すれば、焼却炉6の流
動層最下部(排出口J/の下端)におけ本圧力Pは風量
Qに関して第1図に示す癲く変化する。□第を図におい
て横軸は風量Qm7B(立方米/時間)を縦軸は圧力P
を示す。□シエ−ト11の下端は大気圧にあるものとす
る。First, to explain the furnace internal pressure sealing effect, the main pressure P at the lowest part of the fluidized bed of the incinerator 6 (the lower end of the discharge port J/) changes slightly with respect to the air volume Q as shown in FIG. □ In the figure, the horizontal axis is the air volume Qm7B (cubic meter/hour) and the vertical axis is the pressure P.
shows. □The lower end of seat 11 is assumed to be at atmospheric pressure.
流動層最下部における圧力Pは流動層が形成される状態
で約コ000 mmAqとなる。炉内砂の静止高さがh
であるときのP−Qの関係は第を図の曲線人にて示す如
くである。Gmfは流動化開始が行なわれる風量である
。Qが/ Gmfに達するまではPはQにほぼ比例して
上昇するが、lGmfに達すると流動化を開始し、その
後社終末速度(砂が吹き上げられ飛散し始める前の速釦
壕での間はPはほぼ一室となる。The pressure P at the bottom of the fluidized bed is approximately 0.000 mmAq when the fluidized bed is formed. The static height of the sand in the furnace is h
The relationship between P-Q when , is as shown by the curved line in the figure. Gmf is the air volume at which fluidization starts. Until Q reaches /Gmf, P increases almost in proportion to Q, but when it reaches lGmf, it starts to fluidize, and then the terminal velocity (during the time at the speed button trench before the sand starts to be blown up and scattered) P is almost one room.
流動層とシュートJλ部の砂径が同一である丸め、第1
図に示されゐシュー)JJ部の砂高さH,によってシュ
ートJ一部のP−Qの関係はIs>hなるときは第HH
の曲線Bの如く、tたH、(hなるとき社曲線Cの如く
なる。Rounding, the first sand diameter in the fluidized bed and the chute Jλ part is the same.
As shown in the figure, depending on the sand height H of the JJ part, the relationship between P-Q of the part of the chute J is Is>h, then the HHth
When tH becomes h, the curve becomes like curve C.
即ち、シュート21部の砂高さHlが11.(h′&;
b@4rawttrao′″″°、、、、、i、]、□
msbm*vs+”Pとの交点にて示す如くンユ・1−
トコ一部の砂高さHlによる抵抗が流動層最下部りによ
る圧力pmmAqに負け、通風抵抗を加味した風量Q、
が会は、第1図の曲lsBと流動層最下部圧力Pとの交
点にて示す如く、シュート22部の砂高さH,による抵
抗が流動層一層高りによる圧力PmmAqに打ち勝ち、
シュート内の砂は流出(流動化)することなく、風量Q
、 Nm”/Hの極めてわずかな風量のみが、漏れるだ
けのものとなる。That is, the sand height Hl of the chute 21 section is 11. (h′&;
b@4rawttrao′″″°,,,,,i,],□
msbm*vs+”Nyu・1− as shown at the intersection with “P”
The resistance due to the sand height Hl of the part is overcome by the pressure pmmAq due to the lowest part of the fluidized bed, and the air volume Q, which takes into account the ventilation resistance,
As shown at the intersection of the curve lsB and the pressure P at the bottom of the fluidized bed in Figure 1, the resistance due to the sand height H of the chute 22 overcomes the pressure PmmAq due to the further height of the fluidized bed.
The sand in the chute does not flow out (fluidize) and the air volume Q
, Nm''/H, which is only a very small amount of air that leaks.
シュートココ部砂高さH,(hの場合には、第1図よ〕
、シュー)JJ部砂高さH8による通風抵抗Pma流動
層圧力Pより小さいため流動層の流動化空気はシ、エー
トココ部の方へ流れ易くなル、シュートコ一部の砂は下
向きの流動化状態とな夛、下降し、もはやシール機能を
果し得なくなる。Shoot bottom sand height H, (in case of h, see Figure 1)
, shoe) Since the ventilation resistance Pma due to the sand height H8 in the JJ section is smaller than the fluidized bed pressure P, the fluidized air in the fluidized bed tends to flow toward the bottom part, and some sand is in a downward fluidized state. The seal gradually descends and is no longer able to perform its sealing function.
なお、従来のスクリューコンベヤではケーシングとスク
リエニ羽根との間隙を数−として砂を充満させてシA−
)部の砂高さを稼いでいた、−”’l’X
ものであるが、本発明のものは不燃物の噛込み防止のた
め空隙を大きく開けるため、シールとしての砂層は期待
できない、従ってシュート部砂層高のみで十分な高さを
保つことが必要となる。In addition, in conventional screw conveyors, the gap between the casing and the screener blades is set to 1, and the gap between the casing and the screener blades is filled with sand.
), the height of the sand in the area of -"'l' It is necessary to maintain a sufficient height only with the sand layer height of the chute.
シュー)JJの高さH8は、流動層内の砂の静止高さを
り、砂の見掛比重を8とするとき、a8.’>h−s
なることが一層好ましい。Shoe) JJ height H8 is greater than the static height of sand in the fluidized bed, and when the apparent specific gravity of sand is 8, a8. It is more preferable that '>h−s.
次に噛み込み防止作用につき説明する。Next, the jamming prevention effect will be explained.
前述の如く、垂直面内に旋回流を有する流動層炉におい
ては、かな多大寸法の不燃物が投入されても流動層の形
成を阻害することきく、その不燃物を通過せしめること
d!できるので、排出装置としては、この大寸法の不燃
物を円滑に移送し排出することが必要、となる。As mentioned above, in a fluidized bed furnace having a swirling flow in a vertical plane, even if noncombustible materials of a large size are introduced, the formation of the fluidized bed will be inhibited, and it is difficult to allow the noncombustible materials to pass through! Therefore, as a discharge device, it is necessary to smoothly transfer and discharge this large-sized incombustible material.
前述の如き給しん装置−においては、一本のスクリュー
軸間の間隙は通常は成る特定寸法(例えばlコ!−程度
)であシ、一本きな異物を噛み込んだとき、定常時最大
@−距離に相序する軸間の最大間II(例え、ば200
wm一度)tで拡がpながら移送を行なうようになって
い畢ので、この最大間隙を通過する程度の寸法の異物が
スクリューコンベヤJJに投入される。In the above-mentioned feeding device, the gap between each screw shaft is usually a specific size (for example, about 1 cm), and when a foreign object is caught, the maximum gap under normal conditions @-maximum distance II between axes in phase order with distance (for example, 200
Since the foreign matter is transferred while expanding at times (wm once) and t, a foreign object having a size that can pass through this maximum gap is thrown into the screw conveyor JJ.
スp 9 &−コンベヤーJの入口コ!aよシケーシン
グJj内に入つ九異物は入口直下のねじ羽IIJデのな
い位置へ入る。従ってケーシングJjと軸16間には充
分な隙間があ第、異物はねじ羽根コクの始まる位置よシ
軸方向にねじ羽根コツ間と空I!iG間を占めてねじ羽
根コクの回転につれて軸方向に中央へ送られる。とあ入
口Jj&直下にねじ羽根コクがないため空l!iGよ1
も大きい異物−進入した場合“に入口直下ではもしその
位置にねじ羽根コクがあるとねじ羽根コクの外周とケ゛
−Vングコ!内壁との間で異物は噛み込まれる場合が生
ずる。II#に入口コj!Lのスクリュー軸lによる輸
送物進行方向のケーシングJjの上半円の入口角コIC
においてはねじ羽根コツの回転とねじ羽IJJ?の軸方
向推進″作用があるから噛み込みが生じ易い、処がこの
発明では入口JAIL直下にはねじ羽根17はないから
、異物はねじ羽根コク軸方向の一部から入る′b・ら空
llGよ多大きい異物もねじ羽根コク間に入る。Sp 9 &-Conveyor J entrance! Foreign matter that enters into the casing Jj enters the position directly below the entrance where there is no screw wing IIJ. Therefore, if there is sufficient clearance between the casing Jj and the shaft 16, foreign objects can be kept between the screw blades and the air in the axial direction from the starting position of the screw blades. iG and is sent to the center in the axial direction as the screw blade rotates. Toa entrance JJ & directly below it is empty because there is no screw blade richness! iGyo1
If a large foreign object enters, if there is a screw blade in that position, the foreign object may get caught between the outer periphery of the screw blade and the inside wall of the cage. Inlet corner corner of the upper semicircle of the casing Jj in the direction of transport transport due to the screw shaft l of L
What about the rotation of the screw blade tip and the screw blade IJJ? However, in this invention, since there is no screw blade 17 directly below the inlet JAIL, foreign matter enters from a part of the screw blade in the axial direction. Even large foreign objects can get in between the screw blades.
空llGより小さい物はスクリュ−11が焼却後の廃棄
物、砂でうずまるから軸方向に移動してケーシング間S
の中央に向5.従ってスクリューJfのねじ羽1!J?
のねじ羽根間の輸送物は比較的急速度で送られ、ねじ羽
根J7の外周よ)ケーシングコ!内壁に離れるにつれて
速度は遅くなる。従って、ケーシングJ!の摩耗は著し
く滅する。又、空隙Gの小さい従来例で祉ケーシング−
5の内壁とねじ羽IIコデ外周間の隙間に挾まれた砂に
より著しい摩耗を生じる。If the screw is smaller than the empty 11G, the screw 11 will be covered with waste and sand after incineration, so it will move in the axial direction and move between the casings S.
5. toward the center of the Therefore, screw wing 1 of screw Jf! J?
The transported object between the screw vanes is sent at a relatively rapid speed, and the outer periphery of the screw vane J7) casing co! The speed decreases as it moves away from the inner wall. Therefore, casing J! wear is significantly reduced. In addition, in the conventional example with a small gap G, the welfare casing
Sand trapped in the gap between the inner wall of No. 5 and the outer periphery of the screw wing II causes significant wear.
しかし本発明ではこの現象が解消する。However, the present invention eliminates this phenomenon.
異物のうち、かさ、大型缶類、なぺなどのものは高熱て
軟化しており、スクリエーコンベヤaJ中のねじ羽根コ
ツによシ加圧され且つ異物同志とも加圧−押されて簡−
につぶされて排出/9−)ブロック、鋼材ζアイロン、
へンマーの頭、砲丸、機械部品など)は噛み込むことな
くそのまま移送、排出される。Among the foreign objects, those such as umbrellas, large cans, and pans are softened by high heat, and are pressed by the screw blades in the screw conveyor aJ, and are easily pressed and pressed together with other foreign objects.
Crushed and discharged/9-) Block, steel ζ iron,
(hammer heads, bullets, mechanical parts, etc.) are transported and ejected as they are without being caught.
入口JjlLとスタフィンダボツク336間において外
周の小さいねじ羽@JOを備えて傾斜ケーシングJ4+
の内周と該ねじ羽$JOの外周を接近して設けたのてス
タフイングボックスJ6より離れる方向に砂は移動させ
られる。Inclined casing J4+ with small screw wings @JO between inlet JjlL and stuffing dowel 336
Since the inner periphery of the stuffing box J6 and the outer periphery of the screw wing J6 are provided close to each other, the sand is moved in a direction away from the stuffing box J6.
かくして中央のねじ羽根コクのない位置に送られてくる
と出ロJコ上部はねじ羽根はなく、重力て両側のねじ羽
根Jf側よシ出ロJコに砂、異物、焼却灰等は落下する
。入口コjlLへはシエー)JJ中の砂が重力によりす
べ9込み傾斜壁JJによシ滑かにケーシングJ!内に入
夛輸送のための押込み力を41に必要としない。In this way, when the screw blades in the center are sent to a position where there is no depth, there are no screw blades on the upper part of the exit hole J, and due to gravity, sand, foreign matter, incinerated ash, etc. fall from the screw blades on both sides to the exit hole J. do. The sand in the JJ slides smoothly into the sloping wall JJ due to gravity. 41 does not require any pushing force for repeated transportation.
以上のとお夛1本発明は流動層焼却炉の不燃物を排出す
るスクリュー形式の排出装置において排出のためのムじ
羽根をスクリエー=ンベヤのケーシング人−より輸送方
向側のほぼ側壁位為−とコンベヤのケーシング間におけ
るかみ込みが生じない、ねじ羽根外周とコンベヤのケー
シング間に!!隙を大きくあけたから該ケーシングとス
クリューの摩耗が著しく減少する。入口の反輸送方向側
@壁より入口直下に向けて傾斜壁を設けたからスクリ二
−コンベヤ入口直上のシェードよりの砂が滑かにねじ羽
iJf間に送り込まれる。傾斜壁を形成する傾斜ケーシ
ング内周とは隙間少く接する外周の小さいねじ羽根をス
クリューの軸に設けたから軸封装置への砂の進行が防止
される。In addition to the above, the present invention provides a screw-type discharge device for discharging incombustible materials from a fluidized bed incinerator, in which a screw blade for discharging is located almost on the side wall of the casing of the conveyor in the transport direction. No jamming occurs between the conveyor casing and between the screw blade outer periphery and the conveyor casing! ! Since the gap is wide open, wear of the casing and screw is significantly reduced. Since an inclined wall is provided directly below the entrance from the wall opposite to the transport direction of the entrance, the sand from the shade directly above the entrance of the screen conveyor is smoothly fed between the screw blades iJf. Sand is prevented from advancing toward the shaft sealing device because a screw blade with a small outer circumference that contacts the inner circumference of the inclined casing forming the inclined wall with a small gap is provided on the shaft of the screw.
第1図はごみ焼却設備の断面正面図、第Jll及び第3
図は本発明の実施例の断面正面図及び断面側面図、第参
図はごみ焼却設備の排出スクリューコンベヤ付近の縦断
面正面図、第3図は第参図の一部拡大図、第6図は一参
図のA−A断面図、第7図は第参図0B−BIlfr面
図、第を図は流動層下部圧力Pと風量Qとの関係1sW
Jである。
l・・ビット コ・・クレーン J・・パケット ダ・
・ホッパ !・・給しん装置 6・・IJl却F ?
・・プロワ l・・分散板 デ・・傾斜壁 io・・旋
回流 //・・燃焼排ガスダク) /J・・不燃物排
出装置 /J・・振111篩/4’・・コンベヤ l!
・・エレベータ /4−・どみの入口 17・拳ごみの
出口it・・排出口 11・・戻しシェード J/・・
排出口 ココ・・シェード コJ・・スクリエープンベ
ヤ コク・Φ機台 1t・・ケーシング 2!r&a−
人口 −jb・・側壁−6・・軸 −り・拳ねじ羽根
Jf・・スクリュー コク・・軸受 JO・・ねじ羽根
Jl・・チェンホイル 3コ争・出口 JJ・・傾斜壁
31M−・・傾斜ケーシング SZ・・端板 J6・
・スタフイングボックス 3り−・軸m材 Jt・・カ
バー Jf−・シュート4IO・eカバー 41/・・
パツキン押え。
特許出願人 株式会社荏原製作所
代理人新 井 −部
第1図
第3【
第2図
9
司
第5図
第6図 第7図
第8図
、7′Figure 1 is a cross-sectional front view of the waste incineration facility, Jll and 3
The figures are a cross-sectional front view and a cross-sectional side view of an embodiment of the present invention, Fig. 3 is a vertical cross-sectional front view of the vicinity of the discharge screw conveyor of the waste incineration facility, Fig. 3 is a partially enlarged view of Fig. 6, and Fig. 6 Figure 7 is the A-A sectional view of Figure 1, Figure 7 is the sectional view of Figure 0B-BIlfr, and Figure 7 is the relationship between fluidized bed lower pressure P and air volume Q, 1sW.
It is J. l...Bit Co...Crane J...Packet Da...
・Hoppa! ...Feeding device 6...IJl?F?
...Prower L...Distribution plate D...Slanted wall IO...Swirling flow //...Combustion exhaust gas duct) /J...Incombustibles discharge device /J...Shake 111 sieve /4'...Conveyor l!
・・Elevator /4−・Entrance of garbage 17・Exit of trash it・・Discharge port 11・・Return shade J/・・
Discharge port Coco...shade CoJ...screapunveyor Coco/Φ machine stand 1t...casing 2! r&a-
Population −jb・・Side wall−6・・Axis −ri・Fist screw blade
Jf...Screw Body...Bearing JO...Screw vane Jl...Chain wheel 3-way battle/Exit JJ...Slanted wall 31M-...Slanted casing SZ...End plate J6...
・Stuffing box 3-・Shaft m material Jt・・Cover Jf-・Chute 4IO・e cover 41/・・
Patchkin presser. Patent Applicant Ebara Corporation Agent Arai - Department Figure 1 Figure 3 [ Figure 2 9 Tsukasa Figure 5 Figure 6 Figure 7 Figure 8, 7'
Claims (1)
燃物及び砂を重力により降下せしめるよう案内するシェ
ードと、該シェードの下端に入口が接続されて、流動層
焼却炉の不燃物を排出するスクリュータイプの不燃物排
出装置において、前記入口の輸送方向側の、Ilの。 位置よ)輸送方向側の位置にて輸送のためのねじ羽根が
始まるスクリューを備え些不燃物排出装置。 ユ 前記スクリュー外周とケーシング間の空隙を十分に
開けた特許請求の範囲第1項5記載の不燃物排出装置。 1 人口の反軸送方向側壁下端の中央よ〕入口直下に向
けて砂の流れに沿った傾斜壁をもった傾斜ケーシングを
設けた。4I許請求の範囲第1項記載の不燃物排出装置
。 排出するため小さな径のねじ羽根をスクリュ一端部に設
けた特許請求の範囲第1項記載の不燃物排出装置。[Scope of Claims] l A shade whose upper end is connected to the incombustible material discharge port of the fluidized bed incinerator and guides the incombustible material and sand to fall by gravity; and an inlet connected to the lower end of the shade, which In a screw-type noncombustible material discharge device for discharging noncombustible materials from an incinerator, Il on the transportation direction side of the inlet. position) A device for discharging non-combustible materials equipped with a screw whose screw blades for transportation start at a position on the transportation direction side. The incombustible material discharge device according to claim 1, wherein a gap between the outer periphery of the screw and the casing is sufficiently opened. 1. An inclined casing with an inclined wall along the flow of sand was provided directly below the entrance from the center of the lower end of the side wall in the anti-axial direction. 4I The incombustible material discharge device according to claim 1. 2. The incombustible material discharge device according to claim 1, wherein a screw blade having a small diameter is provided at one end of the screw for discharge.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14208881A JPS5843318A (en) | 1981-09-09 | 1981-09-09 | Discharging device for fluidized bed incinerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14208881A JPS5843318A (en) | 1981-09-09 | 1981-09-09 | Discharging device for fluidized bed incinerator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5843318A true JPS5843318A (en) | 1983-03-14 |
| JPS6146725B2 JPS6146725B2 (en) | 1986-10-15 |
Family
ID=15307144
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP14208881A Granted JPS5843318A (en) | 1981-09-09 | 1981-09-09 | Discharging device for fluidized bed incinerator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5843318A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS606946U (en) * | 1983-06-25 | 1985-01-18 | 株式会社荏原製作所 | Incinerator incombustible material removal device |
| WO1999043985A1 (en) * | 1998-02-27 | 1999-09-02 | Ebara Corporation | Fluidized bed gasification furnace |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6255155B2 (en) * | 2012-12-26 | 2017-12-27 | 川崎重工業株式会社 | Dust supply system and operation method thereof |
-
1981
- 1981-09-09 JP JP14208881A patent/JPS5843318A/en active Granted
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS606946U (en) * | 1983-06-25 | 1985-01-18 | 株式会社荏原製作所 | Incinerator incombustible material removal device |
| WO1999043985A1 (en) * | 1998-02-27 | 1999-09-02 | Ebara Corporation | Fluidized bed gasification furnace |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6146725B2 (en) | 1986-10-15 |
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