JP2000230709A - Multi-fuel fired furnace for sludge having rotary sludge cutting device - Google Patents

Multi-fuel fired furnace for sludge having rotary sludge cutting device

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Publication number
JP2000230709A
JP2000230709A JP11028810A JP2881099A JP2000230709A JP 2000230709 A JP2000230709 A JP 2000230709A JP 11028810 A JP11028810 A JP 11028810A JP 2881099 A JP2881099 A JP 2881099A JP 2000230709 A JP2000230709 A JP 2000230709A
Authority
JP
Japan
Prior art keywords
sludge
chamber
cutting device
supply chamber
combustion
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
Application number
JP11028810A
Other languages
Japanese (ja)
Inventor
Yoshikatsu Yoshida
佳克 吉田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Plantec Inc
Original Assignee
Plantec Inc
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Plantec Inc filed Critical Plantec Inc
Priority to JP11028810A priority Critical patent/JP2000230709A/en
Publication of JP2000230709A publication Critical patent/JP2000230709A/en
Pending legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To provide a multi-fuel fired furnace for sludge causing no environmental pollution, which is able to completely combust sludge having high water content without checking a combusting condition of the furnace and does not require auxiliary combustion. SOLUTION: A sludge cutting device 3 which is mounted on a ceiling 12 made of a refractory material of an incinerator body 1, comprises a sludge feeding chamber 31 having a sludge feeding port 36 for evenly feeding the sludge, a sludge receiving face 32 forming a bottom face of the chamber 31 and punched with a plurality of dropping holes 33 therein which are communicated with the inside of the body 1, a rotary blade 34 which is located in the chamber 31 and rotated while being slid on the face 32 by a drive means 4, and a discharge tube 35 for discharging a gas W in the chamber 31 to a recombusting chamber. Water-containing sludge Sw is fed to the face 32 whose temperature has been raised by the combustion of refuse R, and thinly extended by the rotary blade 34 while being heated and dried to fill the dropping holes 33 therewith, followed by injecting compressed air from an air injection hole in the rotary blade 34. In this way, half dried sludge Sd in the dropping holes 33 is completely combusted together with the refuse R.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、一般廃棄物や産業
廃棄物などのごみと汚泥とを、同時に焼却する汚泥混焼
炉に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a sludge co-firing furnace for simultaneously incinerating refuse and sludge such as general waste and industrial waste.

【0002】[0002]

【従来の技術】従来、下水処理場やし尿処理場等から排
出される汚泥は、各処理場で専用の焼却炉で焼却される
か、同一自治体で設置するごみ焼却炉に搬入されて、一
般廃棄物と混合して焼却されるのが一般的であった。
2. Description of the Related Art Conventionally, sludge discharged from a sewage treatment plant or human waste treatment plant is incinerated in a dedicated incinerator at each treatment plant or carried into a garbage incinerator installed by the same local government. It was common to incinerate by mixing with waste.

【0003】[0003]

【発明が解決しようとする課題】しかし、特開平1−3
05214号公報に開示された如く、汚泥分散投入装置
によって汚泥をごみ層表面上に分散投入しても、各処理
場で脱水処理後に搬入される汚泥の含有水分が、75〜
85%と非常に高いために、各焼却炉の燃焼状態は低下
して非常に不安定になる。
However, Japanese Patent Application Laid-Open No. Hei.
As disclosed in Japanese Patent No. 05214, even when sludge is dispersed and charged on the surface of a garbage layer by a sludge dispersion charging device, the water content of the sludge carried in after each dewatering treatment in each treatment plant is 75 to
Since it is as high as 85%, the combustion state of each incinerator decreases and becomes very unstable.

【0004】そのため、不完全燃焼による悪臭やばいじ
ん排出等の公害を発生させるだけでなく、焼却灰中に残
留する未燃分が増加する事態を招き、その対策として、
助燃バーナで炉内や排ガスの昇温を行っても、燃料費が
嵩む割に上述の各公害を完全に消滅させる事はできなか
った。
[0004] Therefore, not only does it cause pollution such as foul odors and dust emission due to incomplete combustion, but also causes an increase in unburned components remaining in the incineration ash.
Even if the temperature of the exhaust gas and the inside of the furnace was increased by using the auxiliary burner, the above-mentioned pollutions could not be completely eliminated despite the increased fuel cost.

【0005】図5は、特開昭64−54113号公報に
開示された「乾燥汚泥と都市ごみの混焼方法」であり、
含水汚泥Swは乾燥機Dに投入されて脱水乾燥された
後、乾燥機Dの出口に設置された加圧ローラPによって
圧縮成形されて板状の乾燥汚泥Sdとなる。
FIG. 5 shows a "method of co-firing dry sludge and municipal solid waste" disclosed in JP-A-64-54113.
The hydrated sludge Sw is put into the dryer D, dehydrated and dried, and then compression-molded by the pressure roller P installed at the outlet of the dryer D to become a plate-shaped dry sludge Sd.

【0006】都市ごみRは、焼却炉F内で焼却されてい
るが、この燃焼中の都市ごみR層上に、上述の板状の乾
燥汚泥Sdを投入して混合燃焼する方式である。
The municipal solid waste R is incinerated in the incinerator F. In this method, the plate-shaped dry sludge Sd is mixed and burned on the burning municipal solid waste R layer.

【0007】上述の方式により、従来の課題とされてい
た水分を多量に含む汚泥が火格子の隙間から滴下する問
題や、粉末状に乾燥させた場合に汚泥粉が排ガス流に乗
って未燃焼のまま排出される問題は解決するものの、燃
焼状態を改善するために汚泥乾燥設備を前置する必要が
あり、設備費と設置面積が増加するとともに、汚泥乾燥
時に発生する臭気の処理が困難であるという問題があっ
た。
According to the above-mentioned method, sludge containing a large amount of water, which has been a problem of the prior art, drops from the gap of the grate, and when dried into a powder form, sludge powder rides on the exhaust gas stream and is not burned. Although it solves the problem of being discharged as it is, it is necessary to install a sludge drying facility in order to improve the combustion state, equipment costs and installation area increase, and it is difficult to treat the odor generated during sludge drying. There was a problem.

【0008】[0008]

【課題を解決するための手段】請求項1に係る発明の回
転式汚泥切出装置を有する汚泥混焼炉は、一般廃棄物や
産業廃棄物などのごみに汚泥を混入させて、同時に焼却
する汚泥混焼炉において、焼却炉本体の耐火物製天井部
上に汚泥切出装置が載置され、該汚泥切出装置は、汚泥
を平均的に供給する汚泥投入口を有する汚泥供給室と、
この汚泥供給室の底面を形成し、焼却炉本体内に連通す
る複数の滴下穴が穿孔された汚泥受面と、汚泥供給室内
に配置され、上記汚泥受面上を駆動手段により摺動しな
がら回転する回転羽根と、汚泥供給室内で発生するガス
を再燃室に排出する排出管とを備えたものである。
According to the first aspect of the present invention, there is provided a sludge co-firing furnace having a rotary sludge cutting device, wherein sludge is mixed with refuse such as general waste and industrial waste and simultaneously incinerated. In the co-firing furnace, a sludge cutting device is mounted on the refractory ceiling of the incinerator main body, and the sludge cutting device has a sludge supply chamber having a sludge inlet for supplying sludge on average,
A sludge receiving surface, which forms the bottom surface of the sludge supply chamber and is provided with a plurality of drip holes communicating with the inside of the incinerator main body, is disposed in the sludge supply chamber, and slides on the sludge receiving surface by driving means. It comprises a rotating blade and a discharge pipe for discharging gas generated in the sludge supply chamber to the reburn chamber.

【0009】請求項2に係る発明の回転式汚泥切出装置
を有する汚泥混焼炉は、前記回転羽根は、回転方向に対
して一定の角度を持って傾斜して配置され、該回転羽根
の下端には、汚泥を滴下穴から下方に放出させるととも
に、この後の滴下穴を清掃するための圧縮空気を供給す
る複数の空気噴射孔が穿孔されたものである。
According to a second aspect of the present invention, there is provided a sludge co-firing furnace having a rotary sludge cutting device, wherein the rotary blades are arranged to be inclined at a certain angle with respect to a rotation direction, and a lower end of the rotary blades is provided. Has a plurality of air injection holes for discharging sludge downward from the dropping holes and supplying compressed air for cleaning the subsequent dropping holes.

【0010】請求項3に係る発明の回転式汚泥切出装置
を有する汚泥混焼炉は、前記滴下穴には、前記汚泥受面
に交換可能に配置された排出部材が嵌入されており、処
理する汚泥の性状によって形状の異なるものを配置でき
るようになされたものである。
According to a third aspect of the present invention, there is provided a sludge co-firing furnace having a rotary sludge cutting device, wherein a discharge member replaceably disposed on the sludge receiving surface is fitted into the dropping hole for processing. It is designed to arrange different shapes depending on the properties of sludge.

【0011】[0011]

【発明の実施の形態】以下、本発明の実施の一形態を図
面を参照して説明する。
An embodiment of the present invention will be described below with reference to the drawings.

【0012】図1は、本発明に係る回転式汚泥切出装置
を有する汚泥混焼炉の概略構成を示した断面図であり、
図2は汚泥供給室の上部平面図、図3は汚泥供給室内の
回転羽根と汚泥受面の平面図、図4は図3のX−X断面
図である。
FIG. 1 is a sectional view showing a schematic configuration of a sludge co-firing furnace having a rotary sludge cutting device according to the present invention.
2 is a plan view of the upper part of the sludge supply chamber, FIG. 3 is a plan view of the rotating blades and the sludge receiving surface in the sludge supply chamber, and FIG. 4 is a sectional view taken along line XX of FIG.

【0013】図1において、1は耐火物11で囲繞され
た竪型の焼却炉本体であり、焼却炉本体1の直上方に天
井部12、天井部12の下方に1次燃焼室13、1次燃
焼室13に隣接して2次燃焼室14が形成されている。
In FIG. 1, reference numeral 1 denotes a vertical incinerator main body surrounded by a refractory 11, and a ceiling 12 is provided immediately above the incinerator main body 1, and primary combustion chambers 13 and 1 are provided below the ceiling 12 below the ceiling 12. A secondary combustion chamber 14 is formed adjacent to the secondary combustion chamber 13.

【0014】1次燃焼室13に連なる焼却炉本体1の下
部には、燃焼の進行によって境界が変動する主燃焼帯1
5、おき燃焼帯16、燃焼完結帯17がそれぞれ形成さ
れており、2次燃焼室14の上部には、ガス旋回手段1
8を経て再燃室19が連接されている。
The lower part of the incinerator main body 1 connected to the primary combustion chamber 13 has a main combustion zone 1 whose boundary fluctuates as combustion proceeds.
5, a combustion zone 16 and a combustion completion zone 17 are formed respectively.
A recombustion chamber 19 is connected via 8.

【0015】焼却炉本体1の側壁には、通常構造の上部
ダンパ21と耐熱構造の下部ダンパ22を備えたごみ投
入ホッパ23が取付けられており、焼却炉本体1の下方
となる燃焼完結帯17の中程の位置には出没自在のごみ
支持板24、24が、同じく燃焼完結帯17の下端には
反転自在の焼却灰排出板25、25がそれぞれ配設され
ている。
A refuse input hopper 23 having an upper damper 21 having a normal structure and a lower damper 22 having a heat-resistant structure is attached to a side wall of the incinerator main body 1, and a combustion complete zone 17 below the incinerator main body 1 is provided below the incinerator main body 1. At the middle position, garbage support plates 24, 24 which can come and go, and invertible ash discharge plates 25, 25, which are also reversible, are provided at the lower end of the combustion completion zone 17.

【0016】また、上記各燃焼帯及び燃焼室に対して、
主燃焼空気26、後燃焼空気27、2次燃焼空気28及
び再燃焼空気29がそれぞれ供給されている。
Further, for each of the above combustion zones and combustion chambers,
Main combustion air 26, post-combustion air 27, secondary combustion air 28, and re-combustion air 29 are supplied, respectively.

【0017】ここで、上記焼却炉本体1の耐火物11で
構成された天井部12上には汚泥切出装置3が載置され
ている。
Here, a sludge cutting device 3 is mounted on a ceiling portion 12 of the incinerator main body 1 which is made of a refractory material 11.

【0018】汚泥切出装置3は、汚泥供給室31と、こ
の汚泥供給室31の底面を形成し、焼却炉本体1内に連
通する複数の滴下穴33が穿孔された汚泥受面32と、
上記汚泥供給室31内に配置され、汚泥受面32上を駆
動手段4により摺動しながら回転する回転羽根34と、
汚泥供給室31内で発生するガスWを再燃室19に排出
する排出管35とを備えてなる。
The sludge extracting device 3 includes a sludge supply chamber 31, a sludge receiving surface 32 forming a bottom surface of the sludge supply chamber 31, and having a plurality of drip holes 33 formed therein and communicating with the inside of the incinerator main body 1.
Rotating blades 34 disposed in the sludge supply chamber 31 and rotating while sliding on the sludge receiving surface 32 by the driving means 4;
A discharge pipe 35 for discharging gas W generated in the sludge supply chamber 31 to the reburn chamber 19;

【0019】前記汚泥供給室31は、前記天井部12上
に設置された外枠31aで囲繞することによって形成さ
れてなり、この外枠31aの上面には該汚泥供給室31
内に汚泥を平均的に供給する例えば側面視が台形をした
汚泥投入口36が形成されている。この汚泥投入口36
には汚泥供給管37が接続されている。よって、汚泥供
給管37、汚泥投入口36を通じて含水汚泥Swが汚泥
供給室31内に供給され、当該汚泥供給室31内に受け
入れた含水汚泥Swを加熱し、後述する滴下穴33を通
じて焼却炉本体1内に供給する。
The sludge supply chamber 31 is formed by being surrounded by an outer frame 31a installed on the ceiling portion 12, and the upper surface of the outer frame 31a is provided with the sludge supply chamber 31.
For example, a sludge inlet 36 having a trapezoidal side view for supplying sludge into the inside is formed. This sludge inlet 36
Is connected to a sludge supply pipe 37. Accordingly, the wet sludge Sw is supplied into the sludge supply chamber 31 through the sludge supply pipe 37 and the sludge inlet 36, and heats the wet sludge Sw received in the sludge supply chamber 31. Supply within 1.

【0020】前記汚泥受面32は、SUS等の耐磨耗材
で構成されており、この汚泥受面32に複数の滴下穴3
3が、例えば図3に示す如く後述する下部駆動軸41を
基準として放射状に形成されている。
The sludge receiving surface 32 is made of a wear-resistant material such as SUS.
3, are formed radially with reference to a lower drive shaft 41 described later, for example, as shown in FIG.

【0021】前記滴下穴33は、図4に示す如く前記汚
泥受面32に形成された取付穴32aにボルト等の適宜
な固定手段により取り外し自在に上部から嵌入された排
出部材38、38…に形成された上部滴下穴33aと、
この上部滴下穴33aに対応して前記天井部12に形成
された下部滴下穴33bとで形成されている。
As shown in FIG. 4, the drip holes 33 are formed on discharge members 38, 38,... Which are removably fitted from above in mounting holes 32a formed in the sludge receiving surface 32 by appropriate fixing means such as bolts. An upper drip hole 33a formed;
A lower dropping hole 33b formed in the ceiling portion 12 corresponds to the upper dropping hole 33a.

【0022】そして、このように汚泥受面32に設けら
れた排出部材38、38…は、その上部滴下穴33aが
図4に一例を示す如く含水汚泥Swの性状に応じた最適
な形状にそれぞれ形成され、各排出部材38、38…が
交換可能になされている。
The discharge members 38, 38,... Provided on the sludge receiving surface 32 have their upper drip holes 33a formed in an optimum shape according to the properties of the hydrous sludge Sw, as shown in an example in FIG. Are formed and each of the discharge members 38, 38,... Is replaceable.

【0023】前記回転羽根34は、例えば、駆動手段4
の一部を構成する下部駆動軸41を中心にして汚泥受面
32に沿って水平方向に例えば図3に示す如く2枚が対
称位置に配置されており、支持手段41aによって下部
駆動軸41にそれぞれ連結されている。
The rotating blades 34 are, for example,
For example, two sheets are horizontally arranged along the sludge receiving surface 32 around the lower drive shaft 41 which constitutes a part of the lower drive shaft 41 as shown in FIG. Each is connected.

【0024】また、これら回転羽根34は、図4に示す
如く回転方向に対して汚泥受面32から上方に一定角度
αで傾斜した状態で配設されている。
The rotating blades 34 are arranged so as to be inclined upward by a certain angle α from the sludge receiving surface 32 with respect to the rotating direction as shown in FIG.

【0025】この回転羽根34は、中空状に形成された
1枚または複数枚(図示例は2枚)で構成されており、
汚泥受面32との摺動面となる下端面には消耗部品であ
る磨耗板34aがネジ止め等の固定手段で固定されると
ともに、磨耗板34a及び下端面には複数の空気噴射孔
34bが穿孔されている。
The rotating blades 34 are composed of one or a plurality (two in the illustrated example) formed in a hollow shape.
A wear plate 34a, which is a consumable part, is fixed to a lower end surface serving as a sliding surface with the sludge receiving surface 32 by fixing means such as a screw, and a plurality of air injection holes 34b are provided on the wear plate 34a and the lower end surface. Perforated.

【0026】空気噴射孔34bは、前記滴下穴33と対
応して形成されている。詳しくは、前述した汚泥受面3
2に放射状に形成された複数の滴下穴33のうち、放射
方向一列の滴下穴33と合致するように形成されてい
る。つまり、図4では滴下穴33が放射方向一列に4個
形成されており、これに対応して4個の空気噴射孔34
bが回転羽根34の下端面に形成されている。
The air injection holes 34b are formed corresponding to the drop holes 33. For details, see the sludge receiving surface 3 described above.
2, a plurality of radially formed dropping holes 33 are formed so as to coincide with a row of dropping holes 33 in the radial direction. That is, in FIG. 4, four drip holes 33 are formed in a line in the radial direction, and four air injection holes 34 are correspondingly formed.
b is formed on the lower end surface of the rotary blade 34.

【0027】前記排出管35は、外枠31aの上部と再
燃室19とを連通するもので、汚泥供給室31内での含
水汚泥Swの加熱に伴い発生する高温の水分と臭気成分
を含むガスWを当該排出管35を通じて再燃室19に排
出する。
The discharge pipe 35 communicates the upper portion of the outer frame 31a with the reburning chamber 19, and is a gas containing high-temperature moisture and odor components generated when the wet sludge Sw is heated in the sludge supply chamber 31. W is discharged to the reburning chamber 19 through the discharge pipe 35.

【0028】前記駆動手段4は、回転羽根34の軸心部
に連結された下部駆動軸41と、この下部駆動軸41に
連結された上部駆動軸42と、上部駆動軸42に連結さ
れた可変速の減速電動機43とを備えてなる。
The driving means 4 includes a lower drive shaft 41 connected to the axis of the rotary blade 34, an upper drive shaft 42 connected to the lower drive shaft 41, and a lower drive shaft 42 connected to the upper drive shaft 42. And a speed reduction motor 43.

【0029】下部駆動軸41は、図4に示す如くその内
部が前記回転羽根34内に連通する空気通路44に形成
されるとともに、該空気通路44に向けて穿孔された空
気流入孔45が設けられ、この空気流入孔45が形成さ
れた下部駆動軸41の上部の外周が圧縮空気管46に連
結された空気供給部47で取巻かれている。
As shown in FIG. 4, the lower drive shaft 41 is formed with an air passage 44 communicating with the inside of the rotary blade 34, and an air inflow hole 45 drilled toward the air passage 44. The outer periphery of the upper part of the lower drive shaft 41 in which the air inlet hole 45 is formed is surrounded by an air supply part 47 connected to a compressed air pipe 46.

【0030】また、駆動手段4には、上記減速電動機4
3の駆動により回転する回転羽根の回転位置を検出する
位置検出器48が設けられている。
The drive means 4 includes the above-described reduction motor 4
3 is provided with a position detector 48 for detecting the rotational position of the rotary blade rotating by the driving of the third blade.

【0031】さらに、焼却炉本体1等の高温部には、図
示しない断熱材及び保温材がそれぞれ装備されている。
Further, a high-temperature portion such as the incinerator body 1 is provided with a heat insulating material and a heat insulating material (not shown).

【0032】次に、このように構成された回転式汚泥切
出装置を有する汚泥混焼炉の運転状況について説明す
る。
Next, a description will be given of the operation of the sludge co-firing furnace having the rotary sludge cut-off device configured as described above.

【0033】ごみ投入ホッパ23から投入されたごみR
は、上部ダンパ21及び下部ダンパ22の開閉によっ
て、高温で燃焼中の焼却炉本体1内に順次投入され、主
燃焼空気26の供給を受けて主燃焼帯15で燃焼され
る。
The refuse R input from the refuse input hopper 23
Is sequentially injected into the incinerator body 1 burning at a high temperature by opening and closing the upper damper 21 and the lower damper 22, and is supplied with the main combustion air 26 and burned in the main combustion zone 15.

【0034】主燃焼帯15から排出された未燃焼ガスG
aは、1次燃焼室13でガス化燃焼されて燃焼ガスGb
となり、引き続き2次燃焼室14で2次燃焼空気28に
よって2次燃焼される。そして、ガス旋回手段18を通
過することにより混合された2次燃焼ガスGcは、再燃
室19に導入され、再燃焼空気29の供給を受けて完全
燃焼される。
Unburned gas G discharged from main combustion zone 15
a is gasified and combusted in the primary combustion chamber 13 and the combustion gas Gb
Then, secondary combustion is performed by the secondary combustion air 28 in the secondary combustion chamber 14. Then, the secondary combustion gas Gc mixed by passing through the gas swirling means 18 is introduced into the reburning chamber 19, and is completely burned by receiving the supply of the reburning air 29.

【0035】一方、図示しないポンプ等で汚泥供給管3
7から供給された水分を多量に含む含水汚泥Swは、汚
泥投入口36から汚泥供給室31内に平均的に供給さ
れ、汚泥の性状によって速度を調整する可変速の減速電
動機43で回転される回転羽根34により、汚泥受面3
2上で薄く延伸されながら、汚泥受面32上に配置され
た排出部材38、38…及び天井部12に形成された複
数の滴下穴33…内に充填される。
On the other hand, a sludge supply pipe 3
7 is supplied from the sludge inlet 36 into the sludge supply chamber 31 on average, and is rotated by the variable speed reduction motor 43 that adjusts the speed according to the properties of the sludge. Sludge receiving surface 3 by rotating blades 34
While being stretched thinly on the second 2, the discharge members 38, 38,... Arranged on the sludge receiving surface 32 and the plurality of drip holes 33,.

【0036】この際、前述した燃焼によって天井部12
は高温になっており、上面に載置された汚泥供給室31
内に延伸されている含水汚泥Swが加熱・乾燥されると
ともに、滴下穴33…内に充填された含水汚泥Swも適
度に乾燥されて燃焼し易い状態の半乾燥汚泥Sdとな
る。
At this time, the burning of the ceiling 12
Is hot, and the sludge supply chamber 31 placed on the upper surface
The hydrated sludge Sw stretched therein is heated and dried, and the hydrated sludge Sw filled in the drip holes 33 is also appropriately dried to be semi-dry sludge Sd in a state where it is easily burned.

【0037】この含水汚泥Swの加熱・乾燥過程で蒸発
する水分及び臭気成分であるガスWは、汚泥供給室31
から排出管35を経由して再燃室19に排出されて、2
次燃焼ガスGcとともに、熱分解処理される。
The water W and the gas W, which is an odor component, evaporate in the heating and drying process of the wet sludge Sw are supplied to the sludge supply chamber 31.
From the re-combustion chamber 19 via the discharge pipe 35,
A thermal decomposition process is performed together with the next combustion gas Gc.

【0038】そして、回転羽根34が滴下穴33の放射
方向一列上に来たときに、位置検出器48の信号により
図示しない電磁弁を開放して、図示しない空気源から圧
縮空気管46、空気流入孔45、空気通路44を経て回
転羽根34の下端に設けられた複数の空気噴射孔34b
から圧縮空気Aを噴射すれば、滴下穴33…内で加熱・
乾燥された半乾燥汚泥Sdは、短い筒状になってこの滴
下穴33から主燃焼帯15上に放出されて、ごみRとと
もに焼却される。
When the rotary blades 34 are positioned in a line in the radial direction of the drip holes 33, the solenoid valve (not shown) is opened by the signal of the position detector 48, and the compressed air pipe 46, the air A plurality of air injection holes 34b provided at the lower end of the rotary blade 34 via the inflow hole 45 and the air passage 44
If compressed air A is injected from the
The dried semi-dry sludge Sd is formed into a short cylindrical shape, discharged from the drip hole 33 onto the main combustion zone 15, and incinerated together with the refuse R.

【0039】ここで、半乾燥汚泥Sdの燃焼により排出
された汚泥燃焼ガスGdは、ごみRからの燃焼ガスGa
と混合されて2次燃焼室14、ガス旋回手段18を経由
して、再燃室19に導入されて完全燃焼された後、図示
しないガス冷却設備・排ガス処理設備等を経て、外部に
放出される。
Here, the sludge combustion gas Gd discharged by the combustion of the semi-dry sludge Sd is the combustion gas Ga from the refuse R.
Is mixed into the re-combustion chamber 19 via the secondary combustion chamber 14 and the gas swirling means 18 and completely burned, and then discharged to the outside via a gas cooling facility, an exhaust gas treatment facility and the like (not shown). .

【0040】また、上記の圧縮空気Aの噴射動作は、半
乾燥汚泥Sdの放出だけでなく、下部駆動軸41の冷却
を行うとともに、滴下穴33…等の清掃も併せて行うも
のである。
The above-described operation of injecting the compressed air A not only discharges the semi-dry sludge Sd but also cools the lower drive shaft 41 and cleans the drip holes 33.

【0041】このようにして、主燃焼帯15で燃焼され
たごみRと半乾燥汚泥Sdとの焼却残渣は、主燃焼帯1
5の下方に存在するおき燃焼帯16と燃焼完結帯17と
で後燃焼空気27の供給を受けて完全燃焼されて無害の
焼却灰となり、ごみ支持板24を実線の位置から一点鎖
線の位置まで突出させることにより焼却灰の上半分を保
持した後、焼却灰排出板25を実線の位置から一点鎖線
の位置に開放して下半分の焼却済の灰を、図示しない焼
却灰冷却装置に排出する。
Thus, the incineration residue of the refuse R and the semi-dry sludge Sd burned in the main combustion zone 15 is removed from the main combustion zone 1
5, the combustion zone 16 and the combustion complete zone 17 receive the supply of the post-combustion air 27 and are completely burned to produce harmless incinerated ash. The garbage support plate 24 is moved from the position indicated by the solid line to the position indicated by the alternate long and short dash line. After the upper half of the incinerated ash is held by projecting, the incinerated ash discharge plate 25 is opened from the position of the solid line to the position of the alternate long and short dash line, and the incinerated ash of the lower half is discharged to an incineration ash cooling device (not shown). .

【0042】よって、この操作を繰り返すことにより、
ごみR及び含水汚泥Swを混合燃焼させることができ
る。
Therefore, by repeating this operation,
The refuse R and the hydrated sludge Sw can be mixed and burned.

【0043】上述の混合燃焼が終了したら、汚泥供給管
37から水を供給して、汚泥切出装置3の汚泥供給室3
1内部に固着する汚泥の乾燥物を洗浄したあと、汚泥供
給室31に連結された冷却配管39からこの汚泥供給室
31内に空気を連続送入して、汚泥供給室31内等の温
度上昇を防ぐ。
When the mixed combustion described above is completed, water is supplied from the sludge supply pipe 37 and the sludge supply chamber 3 of the sludge cutting device 3 is supplied.
1 After washing the dried sludge adhered to the inside, air is continuously fed into the sludge supply chamber 31 from a cooling pipe 39 connected to the sludge supply chamber 31 to increase the temperature in the sludge supply chamber 31 and the like. prevent.

【0044】なお、本実施の形態では、回転羽根34の
下端面に形成された空気噴射孔34bから圧縮空気を滴
下穴33に噴射することで、滴下穴33内に充填された
半乾燥汚泥Sdを焼却炉本体1内の主燃焼帯15上に放
出するものについて説明したが、回転羽根34の回転の
みによっても滴下穴33に汚泥を順次充填させながらこ
の滴下穴33の下方から半乾燥汚泥Sdを順次滴下させ
ることも可能である。従って、この場合には滴下穴33
に圧縮空気を噴射するために構成された前述の手段が不
要になる。
In the present embodiment, the compressed air is injected into the drip hole 33 from the air injection hole 34b formed on the lower end surface of the rotary blade 34, so that the semi-dry sludge Sd filled in the drip hole 33 is filled. Is discharged onto the main combustion zone 15 in the incinerator main body 1. However, the semi-dry sludge Sd is filled from below the dropping hole 33 while the dropping hole 33 is sequentially filled with the sludge only by the rotation of the rotary blades 34. Can be sequentially dropped. Therefore, in this case, the drip hole 33
This eliminates the need for the above-described means configured to inject compressed air.

【0045】また、焼却炉本体1は竪型焼却炉で説明し
たが、通常の横型ストーカ炉でもよく、また、滴下穴3
3を図3に示す如く下部駆動軸41から放射状に配列し
て、滴下穴33上に回転羽根34が来たときに、圧縮空
気Aを噴射するように説明したが、滴下穴33の配置は
図示に限らず、さらに、圧縮空気Aの噴射は連続でも、
タイマによる間欠制御でも差し支えない。
Although the incinerator body 1 has been described as a vertical incinerator, it may be an ordinary horizontal stoker furnace.
3 are arranged radially from the lower drive shaft 41 as shown in FIG. 3 so that the compressed air A is jetted when the rotary blade 34 comes over the drip hole 33. Not only the illustration, but also the injection of the compressed air A is continuous,
Intermittent control using a timer is acceptable.

【0046】[0046]

【発明の効果】以上述べたように、本発明の汚泥切出装
置を有する汚泥混焼炉を使用することにより、特別な乾
燥装置を付加しなくても水分含有率の高い汚泥を天井部
の熱で乾燥できるために、焼却炉内におけるごみの燃焼
状態を阻害することなく、汚泥及びごみの安定燃焼が図
れ、これにより公害を出さずに焼却できるだけでなく、
排ガス昇温用の助燃バーナを設ける必要がなく燃料費が
節約できる。また、簡単な設備であるために、設備費や
設置面積を増加させる必要もない。さらに、含水汚泥の
乾燥による悪臭は、再燃室で熱分解されるために、外部
に悪臭を放出することはない。
As described above, by using the sludge co-firing furnace having the sludge cutting device of the present invention, sludge having a high moisture content can be removed from the ceiling without using a special drying device. Because it can be dried in the incinerator, stable combustion of sludge and garbage can be achieved without disturbing the combustion state of the garbage in the incinerator.
There is no need to provide an auxiliary burner for raising the temperature of the exhaust gas, and fuel costs can be saved. In addition, since the equipment is simple, there is no need to increase equipment costs and installation area. Further, since the malodor due to the drying of the hydrous sludge is thermally decomposed in the reburning chamber, the malodor is not released to the outside.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明に係る回転式汚泥切出装置を有する汚泥
焼却炉の概略構成を示した断面図である。
FIG. 1 is a cross-sectional view showing a schematic configuration of a sludge incinerator having a rotary sludge cutting device according to the present invention.

【図2】汚泥供給室の上部平面図である。FIG. 2 is a top plan view of a sludge supply chamber.

【図3】汚泥供給室内の回転羽根と汚泥受面の平面図で
ある。
FIG. 3 is a plan view of a rotating blade and a sludge receiving surface in a sludge supply chamber.

【図4】図3のX−X断面図である。FIG. 4 is a sectional view taken along line XX of FIG. 3;

【図5】従来の汚泥混焼炉の概略構成を示した断面図で
ある。
FIG. 5 is a cross-sectional view showing a schematic configuration of a conventional sludge co-firing furnace.

【符号の説明】[Explanation of symbols]

1 焼却炉本体 12 天井部 3 汚泥切出装置 31 汚泥供給室 32 汚泥受面 33 滴下穴 34 回転羽根 35 排出管 36 汚泥投入口 4 駆動手段 R ごみ Sd 半乾燥汚泥 Sw 含水汚泥 W ガス DESCRIPTION OF SYMBOLS 1 Incinerator main body 12 Ceiling part 3 Sludge extraction device 31 Sludge supply chamber 32 Sludge receiving surface 33 Dripping hole 34 Rotating blade 35 Discharge pipe 36 Sludge inlet 4 Driving means R Garbage Sd Semi-dry sludge Sw Wet sludge W Gas

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 一般廃棄物や産業廃棄物などのごみに汚
泥を混入させて、同時に焼却する汚泥混焼炉において、 焼却炉本体の耐火物製天井部上に汚泥切出装置が載置さ
れ、該汚泥切出装置は、汚泥を平均的に供給する汚泥投
入口を有する汚泥供給室と、この汚泥供給室の底面を形
成し、焼却炉本体内に連通する複数の滴下穴が穿孔され
た汚泥受面と、汚泥供給室内に配置され、上記汚泥受面
上を駆動手段により摺動しながら回転する回転羽根と、
汚泥供給室内で発生するガスを再燃室に排出する排出管
とを備えたことを特徴とする回転式汚泥切出装置を有す
る汚泥混焼炉。
Claims: 1. A sludge co-incinerator for mixing and incinerating sludge into garbage such as general waste and industrial waste, wherein a sludge extracting device is mounted on a refractory ceiling of the incinerator body; The sludge cutting device includes a sludge supply chamber having a sludge inlet for supplying sludge averagely, and a sludge formed with a bottom surface of the sludge supply chamber and a plurality of drip holes communicating with the inside of the incinerator main body. Receiving surface, rotating blades disposed in the sludge supply chamber and rotating while sliding on the sludge receiving surface by the driving means,
And a discharge pipe for discharging gas generated in the sludge supply chamber to the reburning chamber.
【請求項2】 前記回転羽根は、回転方向に対して一定
の角度を持って傾斜して配置され、該回転羽根の下端に
は、汚泥を滴下穴から下方に放出させるとともに、この
後の滴下穴を清掃するための圧縮空気を供給する複数の
空気噴射孔が穿孔されたことを特徴とする請求項1記載
の回転式汚泥切出装置を有する汚泥混焼炉。
2. The rotating blade is arranged to be inclined at a certain angle with respect to the rotation direction, and at the lower end of the rotating blade, sludge is discharged downward from a drip hole, and the subsequent dripping is performed. 2. A sludge co-firing furnace having a rotary sludge cutting device according to claim 1, wherein a plurality of air injection holes for supplying compressed air for cleaning the holes are perforated.
【請求項3】 前記滴下穴には、前記汚泥受面に交換可
能に配置された排出部材が嵌入されており、処理する汚
泥の性状によって形状の異なるものを配置できるように
なされたことを特徴とする請求項1又は2記載の回転式
汚泥切出装置を有する汚泥混焼炉。
3. A discharge member replaceably disposed on the sludge receiving surface is fitted into the drip hole, so that a sludge having a different shape can be disposed depending on the properties of the sludge to be treated. A sludge co-firing furnace having the rotary sludge cutting device according to claim 1.
JP11028810A 1999-02-05 1999-02-05 Multi-fuel fired furnace for sludge having rotary sludge cutting device Pending JP2000230709A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11028810A JP2000230709A (en) 1999-02-05 1999-02-05 Multi-fuel fired furnace for sludge having rotary sludge cutting device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11028810A JP2000230709A (en) 1999-02-05 1999-02-05 Multi-fuel fired furnace for sludge having rotary sludge cutting device

Publications (1)

Publication Number Publication Date
JP2000230709A true JP2000230709A (en) 2000-08-22

Family

ID=12258780

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11028810A Pending JP2000230709A (en) 1999-02-05 1999-02-05 Multi-fuel fired furnace for sludge having rotary sludge cutting device

Country Status (1)

Country Link
JP (1) JP2000230709A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002235913A (en) * 2000-12-04 2002-08-23 Mitsui Eng & Shipbuild Co Ltd Method and apparatus for mixing wastes with sludge
JP2006220365A (en) * 2005-02-10 2006-08-24 Mitsui Eng & Shipbuild Co Ltd Waste gasifying device
US20100043246A1 (en) * 2008-08-25 2010-02-25 Smith David N Rotary biomass dryer
CN113154398A (en) * 2021-04-30 2021-07-23 北京高安屯垃圾焚烧有限公司 Burn burning furnace mud back spray and mix burning system
CN115010339A (en) * 2022-06-16 2022-09-06 广东福利龙复合肥有限公司 Sludge treatment system and sludge treatment method

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5249649A (en) * 1975-10-20 1977-04-20 Babcock Hitachi Kk Sludge-measuring feeder
JPS5710016A (en) * 1980-06-23 1982-01-19 Babcock Hitachi Kk Screw type constant rate feeder
JPS6086729U (en) * 1983-11-15 1985-06-14 三菱重工業株式会社 Incinerator for sludge, etc.
JPS6454113A (en) * 1987-08-24 1989-03-01 Kubota Ltd Method of burning dry sludge and city rubbish in combination
JPH01305214A (en) * 1988-05-31 1989-12-08 Sanki Eng Co Ltd Fuel mixing burning device for refuse and sewage sludge
JPH05277500A (en) * 1992-04-03 1993-10-26 Akira Nishida Sludge processing device
JPH09206795A (en) * 1996-02-07 1997-08-12 Sumiyoshi Heavy Ind Co Ltd Crushing device for dehydrated sludge

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5249649A (en) * 1975-10-20 1977-04-20 Babcock Hitachi Kk Sludge-measuring feeder
JPS5710016A (en) * 1980-06-23 1982-01-19 Babcock Hitachi Kk Screw type constant rate feeder
JPS6086729U (en) * 1983-11-15 1985-06-14 三菱重工業株式会社 Incinerator for sludge, etc.
JPS6454113A (en) * 1987-08-24 1989-03-01 Kubota Ltd Method of burning dry sludge and city rubbish in combination
JPH01305214A (en) * 1988-05-31 1989-12-08 Sanki Eng Co Ltd Fuel mixing burning device for refuse and sewage sludge
JPH05277500A (en) * 1992-04-03 1993-10-26 Akira Nishida Sludge processing device
JPH09206795A (en) * 1996-02-07 1997-08-12 Sumiyoshi Heavy Ind Co Ltd Crushing device for dehydrated sludge

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002235913A (en) * 2000-12-04 2002-08-23 Mitsui Eng & Shipbuild Co Ltd Method and apparatus for mixing wastes with sludge
JP2006220365A (en) * 2005-02-10 2006-08-24 Mitsui Eng & Shipbuild Co Ltd Waste gasifying device
US20100043246A1 (en) * 2008-08-25 2010-02-25 Smith David N Rotary biomass dryer
US8667706B2 (en) * 2008-08-25 2014-03-11 David N. Smith Rotary biomass dryer
CN113154398A (en) * 2021-04-30 2021-07-23 北京高安屯垃圾焚烧有限公司 Burn burning furnace mud back spray and mix burning system
CN115010339A (en) * 2022-06-16 2022-09-06 广东福利龙复合肥有限公司 Sludge treatment system and sludge treatment method
CN115010339B (en) * 2022-06-16 2023-09-12 广东福利龙复合肥有限公司 Sludge treatment system and sludge treatment method

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