JPH067005B2 - Rotary two-stage incinerator - Google Patents
Rotary two-stage incineratorInfo
- Publication number
- JPH067005B2 JPH067005B2 JP25818288A JP25818288A JPH067005B2 JP H067005 B2 JPH067005 B2 JP H067005B2 JP 25818288 A JP25818288 A JP 25818288A JP 25818288 A JP25818288 A JP 25818288A JP H067005 B2 JPH067005 B2 JP H067005B2
- Authority
- JP
- Japan
- Prior art keywords
- rotary
- incinerator
- furnace
- drying
- rotary furnace
- 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.)
- Expired - Lifetime
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- Incineration Of Waste (AREA)
Description
【発明の詳細な説明】 産業上の利用分野 この発明は、工場その他から出る産業廃棄物や、都市ご
みのような生活廃棄物、汚泥などの各種廃棄物の焼却炉
に関し、さらに詳しくは、回転式焼却炉の改良に関す
る。Description: TECHNICAL FIELD The present invention relates to an incinerator for industrial wastes from factories and other sources, domestic wastes such as municipal solid wastes, and various wastes such as sludge. Type improvement of incinerator.
従来技術およびその問題点 上記の如き廃棄物の焼却処理装置としては、従来から回
転式焼却炉、流動床式焼却炉などが知られている。2. Description of the Related Art Conventional technology and its problems As a waste incinerator as described above, a rotary incinerator, a fluidized bed incinerator, etc. have been conventionally known.
このうち、回転式焼却炉は、第2図に示すように、始端
側の乾燥ゾーン(51a)および終端側の焼却ゾーン(51b)よ
り成る回転炉(51)と、これの始端部に設けられた廃棄物
投入口(52)と、回転炉(51)の終端部に設けられたバーナ
(53)および燃焼用空気供給口(54)と、回転炉(51)の終端
底部に設けられた灰分排出口(55)と、回転炉(51)の始端
頂部に設けられた排ガス排出路(56)とを主構成要素とす
る。回転炉(51)の回転に伴って固体の装入物が横断面円
弧状の炉内面に沿って持ち上げられて、ついでこれが落
ちて新しい面が露出し、乾燥および焼却が促進される。
そして、廃棄物は乾燥ゾーン(51a)で乾燥され、ついで
焼却ゾーン(51b)へ移りここで焼却される。焼却に伴っ
て生じた排ガスは臭気を含み、300℃程度まで温度降
下する。これを未処理のまま大気へ放出しては臭気によ
る公害問題を生じるので、ついで排ガスを脱臭炉(57)で
800℃程度まで再加熱して脱臭し、さらに集塵器(58)
を経て煙突(59)から系外へ放出する。Of these, as shown in FIG. 2, the rotary incinerator is provided with a rotary furnace (51) including a drying zone (51a) on the starting end side and an incineration zone (51b) on the ending side, and a starting end portion thereof. Waste input port (52) and a burner installed at the end of the rotary furnace (51).
(53) and the combustion air supply port (54), the ash discharge port (55) provided at the bottom end of the rotary furnace (51), and the exhaust gas discharge path (at the top end of the start point of the rotary furnace (51) ( 56) and are the main components. As the rotary furnace (51) rotates, the solid charge is lifted along the inner surface of the furnace having an arc-shaped cross section, which then falls to expose a new surface, which promotes drying and incineration.
Then, the waste is dried in the drying zone (51a) and then moved to the incineration zone (51b) where it is incinerated. Exhaust gas generated by incineration contains odor and its temperature drops to about 300 ° C. If untreated, it will be emitted into the atmosphere, causing pollution problems. Therefore, the exhaust gas is reheated to about 800 ° C in the deodorization furnace (57) to deodorize it, and the dust collector (58)
Through the chimney (59) to the outside of the system.
回転式焼却炉は上記のように作動するが、これは流動床
式焼却炉に比べて建設費、維持管理費および設置面積の
大きさなどの点で劣るとされている。The rotary incinerator operates as described above, but it is said to be inferior to the fluidized bed incinerator in terms of construction cost, maintenance cost, and size of installation area.
この発明は、回転式焼却炉の利点を損なうことなく、上
記欠点を大巾に改善することができる回転式焼却炉を提
供することを目的とする。An object of the present invention is to provide a rotary incinerator capable of greatly improving the above drawbacks without impairing the advantages of the rotary incinerator.
問題点の解決手段 この発明による回転式焼却炉は、上記目的の達成のため
に、 上側に配置されかつ始端部に廃棄物投入口(2)を有し
た乾燥用回転炉(1)と、 下側に配置されかつ終端部にバーナ(4)および燃焼用
空気供給口(5)を有した焼却用回転炉(3)と、 乾燥用回転炉(1)の終端部から焼却用回転炉(3)の
始端部に設けられた乾燥物搬送路(6)と、 焼却用回転炉(3)の始端部から乾燥用回転炉(1)の
終端部に連通状に設けられかつ燃焼用空気の供給量に相
当する分の排ガスを煙突(8)へ残分を乾燥用回転炉
(1)へそれぞれ送る排ガス分流室(7)と、 乾燥用回転炉(1)の始端部から焼却用回転炉(3)の
終端部に連通状に設けられた通気室(9)とを具備して
成る。Means for Solving the Problems The rotary incinerator according to the present invention has, in order to achieve the above object, a rotary rotary incinerator (1) arranged at an upper side and having a waste input port (2) at a starting end, A rotary incinerator (3) having a burner (4) and a combustion air supply port (5) at the end, and a rotary incinerator (3) from the end of the rotary drier (1) for drying. ) Is provided at the starting end of the rotary incinerator (3) and the end of the rotary incinerator (1) is connected to the incinerator and the supply of combustion air is provided. Exhaust gas flow dividing chamber (7) for sending the exhaust gas corresponding to the amount to the stack (8) to the drying rotary furnace (1) respectively, and the incinerator rotary furnace (from the starting end of the drying rotary furnace (1) ( And a ventilation chamber (9) provided at the end of (3) so as to communicate with each other.
この明細書において、回転炉の「始端」および「終端」
なる用語は、処理すべき廃棄物の流れを基準にして用い
ることとする。In this specification, the "starting end" and "terminating end" of a rotary furnace
Shall be used with reference to the waste stream to be treated.
装置が大規模なものとなる場合には、煙突(8)の上端
部に空気予熱用の熱交換器(12)が外装され、これによっ
て予熱された燃焼用空気が焼却用回転炉(3)に供給さ
れる。In the case of large-scale equipment, a heat exchanger (12) for preheating air is installed on the upper end of the chimney (8), and the combustion air preheated by the heat exchanger (3) is incinerator rotary furnace (3). Is supplied to.
実施例 つぎに、この発明の実施例について、図面を基に具体的
に説明する。Example Next, an example of the present invention will be specifically described with reference to the drawings.
この発明による回転式焼却炉の構成主体を成す炉は、上
側に配置された乾燥用回転炉(1)と、下側に配置され
た焼却用回転炉(3)との上下2基の別体の回転炉より
成る。乾燥用回転炉(1)の始端部には下向き傾斜状の
廃棄物投入口(2)が設けられ、焼却用回転炉(3)の
終端部には内側のバーナ(4)と外側の燃焼用空気供給
口(5)とが同心状に設けられている。The rotary incinerator according to the present invention is mainly composed of a drying rotary furnace (1) arranged on the upper side and an incinerator rotary furnace (3) arranged on the lower side. It consists of a rotary furnace. At the start end of the rotary oven for drying (1), a waste inlet (2) with a downward slope is provided, and at the end of the rotary oven for incineration (3), an internal burner (4) and an external burner are provided. The air supply port (5) is provided concentrically.
乾燥用回転炉(1)の終端部から焼却用回転炉(3)の
始端部にかけて乾燥物搬送路(6)が設けられている。
焼却用回転炉(3)の始端部から乾燥用回転炉(1)の
終端部に連通状に排ガス分流室(7)が設けられてい
る。この排ガス分流室(7)によって、焼却用回転炉
(3)で生じた排ガスのうち燃焼用空気の供給量に相当
する分が煙突(8)へ送られ、残分が乾燥用回転炉
(1)へ送られる。乾燥用回転炉(1)の始端部から焼
却用回転炉(3)の終端部に連通状に通気室(9)が設
けられている。この通気室(9)によって、乾燥に使用
されたガスが乾燥用回転炉(1)から焼却用回転炉
(3)へ燃焼用の二次空気として導入される。排ガス分
流室(7)および通気室(9)の各下端にはそれぞれ灰
分排出口(10)(11)が設けられている。A dry material transport path (6) is provided from the end of the rotary oven for drying (1) to the start of the rotary oven for incineration (3).
An exhaust gas distribution chamber (7) is provided in communication from the starting end of the incinerator rotary furnace (3) to the terminal end of the drying rotary furnace (1). By this exhaust gas distribution chamber (7), a portion of the exhaust gas generated in the incinerator rotary furnace (3) corresponding to the supply amount of combustion air is sent to the chimney (8), and the remainder is the drying rotary furnace (1). ) Is sent to. An aeration chamber (9) is provided so as to communicate from the start end of the rotary rotary oven (1) to the end of the rotary rotary furnace (3) for incineration. The gas used for drying is introduced from the rotary oven for drying (1) into the rotary oven for incineration (3) as secondary air for combustion by the ventilation chamber (9). Ash exhaust ports (10) and (11) are provided at the lower ends of the exhaust gas distribution chamber (7) and the ventilation chamber (9), respectively.
上記構成の焼却炉において、廃棄物投入口(2)から乾
燥用回転炉(1)の始端部に投入された廃棄物は、まず
同回転炉(1)の回転に伴って高温の排ガスによって乾
燥される。ついで乾燥した廃棄物は、乾燥物搬送路
(6)によって乾燥用回転炉(1)から焼却用回転炉
(3)へ運ばれ、ここで同回転炉(3)の回転に伴って
燃焼用空気によって焼却される。焼却に伴って生じた排
ガスのうち、燃焼用空気の供給量に相当する分は煙突
(8)から大気へ放出される。また、残分は乾燥用回転
炉(1)へ送られ、ここで乾燥用ガスとして使用された
後、通気室(9)を経て焼却用回転炉(3)へ燃焼用の
二次空気として導入される。In the incinerator having the above-mentioned configuration, the waste put into the starting end of the rotary rotary oven (1) from the waste input port (2) is first dried by high-temperature exhaust gas as the rotary furnace (1) rotates. To be done. Then, the dried waste is conveyed from the rotary dryer for drying (1) to the rotary furnace for incineration (3) by the dry material transport path (6), and the combustion air is accompanied by the rotation of the rotary furnace (3). Burned by. Of the exhaust gas generated by the incineration, a portion corresponding to the supply amount of combustion air is discharged from the chimney (8) to the atmosphere. In addition, the residue is sent to the rotary oven for drying (1), used there as a gas for drying, and then introduced as secondary air for combustion into the rotary oven for incineration (3) through the ventilation chamber (9). To be done.
このように、排ガスの一部を大気放出し残部を焼却ゾー
ンへ再循環するメリットとしては、つぎのような点が挙
げられる。Thus, the following points can be cited as the advantages of releasing a part of the exhaust gas into the atmosphere and recirculating the remaining part to the incineration zone.
イ)乾燥用回転炉(1)通過後の臭気を帯びた排ガスを
焼却用回転炉(3)へ再循環することによって、同炉
(3)において臭気成分を酸化し、脱臭を行なうことが
できる。そのため脱臭炉の設置を省略することができ
る。B) By recirculating the odorous exhaust gas that has passed through the drying rotary furnace (1) to the incinerator rotary furnace (3), the odorous components can be oxidized and deodorized in the same furnace (3). . Therefore, installation of a deodorizing furnace can be omitted.
ロ)排ガスの再循環によって焼却用回転炉(3)の廃熱
を乾燥用回転炉(1)において回収することができる。(B) The waste heat of the incinerator rotary furnace (3) can be recovered in the drying rotary furnace (1) by recirculating the exhaust gas.
ハ)煙突(8)への排ガスは焼却用回転炉(3)の出口
から出るので、臭気のない排ガスを大気へ放出すること
ができる。そのためこの点でも脱臭炉の設置を省略する
ことができる。C) Since the exhaust gas to the chimney (8) exits from the outlet of the rotary incinerator (3), the exhaust gas without odor can be released to the atmosphere. Therefore, also in this respect, the installation of the deodorizing furnace can be omitted.
なお、装置が大規模なものとなる場合には、煙突(8)
の上端部には空気予熱用の熱交換器(12)が外装され、こ
れによって予熱された燃焼用空気が焼却用回転炉(3)
に供給される。こうして省エネルギーを図ることによっ
て、装置の維持管理費の節減が達成される。In addition, when the device is large-scale, the chimney (8)
A heat exchanger (12) for air preheating is installed on the upper end of the so that combustion air preheated by the heat exchanger (3) is incinerated.
Is supplied to. By thus saving energy, the maintenance cost of the device can be reduced.
発明の効果 この発明による回転式焼却炉は、上側に配置された乾燥
用回転炉(1)と下側に配置された焼却用回転炉(3)
とを主体とするので、本書冒頭で述べた従来の回転式焼
却炉のように始端側の乾燥ゾーンと終端側の焼却ゾーン
とより成るものに比べて、装置の設置面積を大巾に縮小
することができる。さらに、上記構造によって、装置の
コンパクト化を果たすことができ、建設費の節減を達成
することができる。EFFECTS OF THE INVENTION The rotary incinerator according to the present invention is a rotary rotary incinerator (1) arranged on the upper side and a rotary incinerator (3) arranged on the lower side.
Since it mainly consists of and, compared with the conventional rotary incinerator described at the beginning of this document that consists of a drying zone on the start side and an incineration zone on the end side, the installation area of the device is greatly reduced. be able to. Further, with the above structure, the device can be made compact and the construction cost can be reduced.
また、この回転式焼却炉は、焼却用回転炉(3)の始端
部から乾燥用回転炉(1)の終端部に連通状に設けられ
かつ燃焼用空気の供給量に相当する分の排ガスを煙突
(8)へ残分を乾燥用回転炉(1)へそれぞれ送る排ガ
ス分流室(7)と、乾燥用回転炉(1)の始端部から焼
却用回転炉(3)の終端部に連通状に設けられた通気室
(9)とを具備しているので、乾燥用回転炉(1)通過
後の臭気を帯びた排ガスを焼却用回転炉(3)へ再循環
することによって、同炉(3)において気成分を酸化
し、脱臭を行なうことができるとともに、焼却用回転炉
(3)の出口から臭気のない排ガスを大気放出すること
ができる。そのため脱臭炉の設置を省略することがで
き、この点でも装置の設置面積の縮小を果たすことがで
きる。さらに、脱臭炉の省略によって、従来の装置のよ
うな脱臭炉からの熱放散が全くなくなり、その分燃料費
が節減でき、省エネルギーを達成することができる。In addition, this rotary incinerator is provided so as to communicate from the start end of the incinerator rotary furnace (3) to the end of the rotary rotary furnace (1) and to generate an amount of exhaust gas equivalent to the supply amount of combustion air. An exhaust gas flow dividing chamber (7) for sending the residue to the chimney (8) respectively to the drying rotary furnace (1), and a communication form from the start end of the drying rotary furnace (1) to the end of the incinerator rotary furnace (3). Since it is equipped with a ventilation chamber (9) provided in, the odorous exhaust gas that has passed through the drying rotary furnace (1) is recirculated to the incinerator rotary furnace (3), thereby In 3), gas components can be oxidized to deodorize, and odorless exhaust gas can be released to the atmosphere from the outlet of the incinerator rotary furnace (3). Therefore, the installation of the deodorizing furnace can be omitted, and the installation area of the device can be reduced also in this respect. Further, by omitting the deodorizing furnace, heat dissipation from the deodorizing furnace unlike the conventional device is completely eliminated, fuel cost can be reduced accordingly, and energy saving can be achieved.
また、廃棄物投入口(2)は乾燥用回転炉(1)の始端
部に設けられるとともに、バーナ(4)および燃焼用空
気供給口(5)は焼却用回転炉(3)の終端部に設けら
れているので、廃棄物投入口(2)とバーナ(4)およ
び燃焼用空気供給口(5)とが装置の同一端部に位置す
る。そのため、この発明の回転式焼却炉を操作性よく稼
働させることができる。Further, the waste inlet (2) is provided at the beginning of the drying rotary furnace (1), and the burner (4) and the combustion air supply port (5) are provided at the end of the incinerator rotary furnace (3). Since it is provided, the waste inlet (2), the burner (4) and the combustion air supply (5) are located at the same end of the device. Therefore, the rotary incinerator of the present invention can be operated with good operability.
第1図はこの発明の実施例を示す回転式焼却炉の垂直縦
断面図、第2図は従来技術を示す回転式焼却炉の垂直縦
断面図である。 (1)…乾燥用回転炉、(2)…廃棄物投入口、(3)
…焼却用回転炉、(4)…バーナ、(5)…燃焼用空気
供給口、(6)…乾燥物搬送路、(7)…排ガス分流
室、(8)…煙突、(9)…通気室。FIG. 1 is a vertical vertical sectional view of a rotary incinerator showing an embodiment of the present invention, and FIG. 2 is a vertical vertical sectional view of a rotary incinerator showing a conventional technique. (1) ... Rotary oven for drying, (2) ... Waste input port, (3)
... Rotating furnace for incineration, (4) ... Burner, (5) ... Combustion air supply port, (6) ... Dry material transport passage, (7) ... Exhaust gas distribution chamber, (8) ... Chimney, (9) ... Aeration Room.
Claims (1)
(2)を有した乾燥用回転炉(1)と、 下側に配置されかつ終端部にバーナ(4)および燃焼用
空気供給口(5)を有した焼却用回転炉(3)と、 乾燥用回転炉(1)の終端部から焼却用回転炉(3)の
始端部に設けられた乾燥物搬送路(6)と、 焼却用回転炉(3)の始端部から乾燥用回転炉(1)の
終端部に連通状に設けられかつ燃焼用空気の供給量に相
当する分の排ガスを煙突(8)へ残分を乾燥用回転炉
(1)へそれぞれ送る排ガス分流室(7)と、 乾燥用回転炉(1)の始端部から焼却用回転炉(3)の
終端部に連通状に設けられた通気室(9)とを具備し
た、回転二段式焼却炉。1. Drying rotary furnace (1) arranged on the upper side and having a waste inlet (2) at the start end, and a burner (4) and combustion air supply arranged on the lower side and at the end. An incinerator rotary furnace (3) having a mouth (5), and a dry matter transport path (6) provided from the end of the dryer rotary furnace (1) to the start of the incinerator rotary furnace (3). The exhaust gas, which is provided in communication from the starting end of the incinerator rotary furnace (3) to the end of the drying rotary furnace (1) and corresponds to the supply amount of combustion air, dries the residue to the chimney (8). Exhaust gas diversion chamber (7) for sending to the rotary kiln (1) for ventilation, and a ventilation chamber (9) provided in communication from the start end of the rotary kiln for drying (1) to the end of the rotary kiln (3) for incineration A rotary two-stage incinerator equipped with.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP25818288A JPH067005B2 (en) | 1988-10-12 | 1988-10-12 | Rotary two-stage incinerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP25818288A JPH067005B2 (en) | 1988-10-12 | 1988-10-12 | Rotary two-stage incinerator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02103309A JPH02103309A (en) | 1990-04-16 |
| JPH067005B2 true JPH067005B2 (en) | 1994-01-26 |
Family
ID=17316655
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP25818288A Expired - Lifetime JPH067005B2 (en) | 1988-10-12 | 1988-10-12 | Rotary two-stage incinerator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH067005B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0727315A (en) * | 1992-08-31 | 1995-01-27 | Tanabe Kogyo Kk | Rotary kiln incinerator |
-
1988
- 1988-10-12 JP JP25818288A patent/JPH067005B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH02103309A (en) | 1990-04-16 |
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