JPH02302512A - Incineration ash melting method and device therefor - Google Patents

Incineration ash melting method and device therefor

Info

Publication number
JPH02302512A
JPH02302512A JP12067589A JP12067589A JPH02302512A JP H02302512 A JPH02302512 A JP H02302512A JP 12067589 A JP12067589 A JP 12067589A JP 12067589 A JP12067589 A JP 12067589A JP H02302512 A JPH02302512 A JP H02302512A
Authority
JP
Japan
Prior art keywords
ash
melting
exhaust gas
chamber
incinerated ash
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
Application number
JP12067589A
Other languages
Japanese (ja)
Other versions
JPH0684812B2 (en
Inventor
Yoshitoshi Sekiguchi
善利 関口
Kunio Sasaki
邦夫 佐々木
Hideo Shitaya
下谷 英雄
Tadashi Kono
正 河野
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.)
Hitachi Zosen Corp
Original Assignee
Hitachi Zosen Corp
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 Hitachi Zosen Corp filed Critical Hitachi Zosen Corp
Priority to JP12067589A priority Critical patent/JPH0684812B2/en
Publication of JPH02302512A publication Critical patent/JPH02302512A/en
Publication of JPH0684812B2 publication Critical patent/JPH0684812B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Gasification And Melting Of Waste (AREA)

Abstract

PURPOSE:To efficiently recover the heat of combustion gas and use it effectively for reducing the running cost considerably by a method wherein incineration ash is charged into a melting furnace after granulated, and exhaust combustion gas of a melting burner is induced toward the granulated ash charging side to pre-heat the granulated ash. CONSTITUTION:Incineration ash A supplied from an ash hopper 20 to an ash granulating unit 8 is granulated into granular ash pellets A1 and fed into a pre-heating compartment 6 through a pellet feed pipe 10 by a pellet feeder 9. The ash pellets A1 filled in the pre-heating compartment 6 is sent toward a melting chamber 3 side by a pusher 11. Primary combustion exhaust gas D1 is introduced from a melting burner 2 to the pre-heating compartment 6, passes through the clearances between the ash pellets, and discharged through a first exhaust gas pipe 7A after efficiently pre-heating not only the upper portion of the pile of the ash pellets A1 but also the inside of the pile. The ash pellets A1 are heated by the melting burner 2 in the melting chamber, turned into molten slag B, and discharged together with secondary combustion exhaust gas D2 from a slag outlet 4 into a slag cooling chamber 5.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、たとえばごみ焼却炉等から排出されるごみ焼
却灰をバーナにより加熱溶融して固化し、減容化をはか
る焼却灰溶融処理方法および装置に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a method and apparatus for melting waste incineration ash, which reduces the volume by heating and melting waste incineration ash discharged from a waste incinerator or the like using a burner to solidify the waste incineration ash. Regarding.

従来の技術 ごみ焼却炉から排出される焼却灰を溶融固化して減容化
、無害化をはかるバー十方式の溶融処理装置は、従来た
とえば第2図に示すように灰ホッパ102から溶融炉1
0Gの溶融室101上流側に投入された焼却灰Aを、プ
ッシャー装置103により下流側に送り、溶融室101
の天壁に配設された溶融バーナ104により焼却灰Aを
たとえば1300℃以上に加熱して溶融させ、この溶融
スラグBを燃焼排ガスDと共に排出口105からスラグ
冷却室106に流送し、固化している。この時スラグ冷
却室に流入された燃焼排ガスDは、排ガス管108を介
して空気予熱器107に導入されて、溶融バーナに供給
される燃焼用空気Cを加熱した後、大気中に排出されて
いた。
Conventional technology A bar-type melting device that melts and solidifies incinerated ash discharged from a garbage incinerator to reduce its volume and render it harmless has conventionally been used to transport ash from an ash hopper 102 to a melting furnace 1 as shown in FIG.
The incinerated ash A put into the upstream side of the 0G melting chamber 101 is sent to the downstream side by the pusher device 103, and
The incinerated ash A is heated to, for example, 1300° C. or higher and melted by a melting burner 104 arranged on the top wall of the slag, and the molten slag B is flowed together with the combustion exhaust gas D from the exhaust port 105 to the slag cooling chamber 106, where it is solidified. are doing. The combustion exhaust gas D flowing into the slag cooling chamber at this time is introduced into the air preheater 107 via the exhaust gas pipe 108, heats the combustion air C supplied to the melting burner, and is then discharged into the atmosphere. Ta.

発明が解決しようとする課題 上記従来構成によれば、たとえば都市から排出されるご
み焼却灰では約1300℃以上に加熱して溶融されるが
、溶融バーナ104からの燃焼排ガスDの排熱は、空気
予熱器において溶融バーナ104の燃焼用空気Cの加熱
用にしか使われておらず、きわめて無駄が多かった。
Problems to be Solved by the Invention According to the above conventional configuration, for example, garbage incineration ash discharged from cities is heated to about 1300° C. or higher and melted, but the exhaust heat of the combustion exhaust gas D from the melting burner 104 is In the air preheater, it was used only for heating the combustion air C of the melting burner 104, which was extremely wasteful.

本発明は燃焼排ガスの排熱を効率よく回収して有効に利
用でき、ランニングコストを大幅に低減できる焼却灰溶
融処理方法および装置を提供することを目的とする。
An object of the present invention is to provide a method and apparatus for melting incinerated ash, which can efficiently recover and effectively utilize the exhaust heat of combustion exhaust gas, and can significantly reduce running costs.

課題を解決するための手段 上記問題点を解決するために本発明の焼却灰溶融処理方
法は、溶融バーナを備えた溶融炉を使用して焼却灰を加
熱溶融し溶融スラグを排出するに際し、焼却灰を造粒し
て溶融炉に投入し、溶融バーナの燃焼排ガスを粒状焼却
灰投入側に誘引して粒状焼却灰を予熱するらのである。
Means for Solving the Problems In order to solve the above problems, the incineration ash melting treatment method of the present invention uses a melting furnace equipped with a melting burner to heat and melt the incineration ash and discharge the molten slag. The ash is granulated and put into a melting furnace, and the combustion exhaust gas from the melting burner is drawn to the granular incinerated ash input side to preheat the granular incinerated ash.

また焼却灰の溶融処理装置は、溶融炉の溶融室に溶融バ
ーナを備え、この溶融バーナにより焼却灰を溶融しこの
溶融スラグをスラグ冷却室に排出する焼却灰溶融処理装
置において、灰投入ホッパと溶融室の間に、焼却灰を造
粒する造粒装置と、造粒された粒状焼却灰を予熱する予
熱室とを設け、前記予熱室に燃焼排ガスを誘引する排ガ
ス管を接続したことを特徴とする焼却灰溶融処理装置。
The incinerated ash melting device is equipped with a melting burner in the melting chamber of the melting furnace, and the incinerated ash is melted by the melting burner and the molten slag is discharged into the slag cooling chamber. A granulating device for granulating incinerated ash and a preheating chamber for preheating the granulated incinerated ash are provided between the melting chamber, and an exhaust gas pipe for attracting combustion exhaust gas is connected to the preheating chamber. Incineration ash melting processing equipment.

作用 上記構成によれば、誘引される燃焼排ガスは粒状焼却灰
間を通って中層部および下層部にも及んで通過し、まん
べんなく焼却灰を予熱するので、熱効率を大幅に向上す
ることができ、溶融バーナの供給熱量を減少できてラン
ニングコストを低へできる。
Effects According to the above configuration, the induced combustion exhaust gas passes through the granular incinerated ash to the middle and lower layers, and evenly preheats the incinerated ash, so thermal efficiency can be greatly improved. The amount of heat supplied to the melting burner can be reduced, reducing running costs.

実施例 以下本発明の一実施例を第1図に基づいて説明する。Example An embodiment of the present invention will be described below with reference to FIG.

1はたとえばごみの焼却灰Aを溶融バーナ2により加熱
溶融して溶融スラグBを形成する溶融炉で、下流側の溶
融室3の天壁1aに溶融バーナ2が配設されるとともに
、底壁1bにスラグ抜出口4が形成され、スラグ抜出口
4の下方にスラグ冷却室5が配設される。溶融室3の上
流側には、上流側はど上位に傾斜しさらに上方に折れ曲
りなL字状の予熱室6が形成され、予熱室6の上端部に
は燃焼排ガスのうち大部分を占める第1燃焼排ガスD1
を誘引する第1排ガス管7Aが接続される。
Reference numeral 1 denotes a melting furnace that heats and melts waste incineration ash A using a melting burner 2 to form molten slag B. The melting burner 2 is disposed on the top wall 1a of the melting chamber 3 on the downstream side, and the bottom wall A slag outlet 4 is formed in 1b, and a slag cooling chamber 5 is provided below the slag outlet 4. On the upstream side of the melting chamber 3, there is formed an L-shaped preheating chamber 6 which is inclined upward on the upstream side and further bent upward, and the upper end of the preheating chamber 6 accounts for most of the combustion exhaust gas. First combustion exhaust gas D1
A first exhaust gas pipe 7A is connected to the exhaust gas pipe 7A.

また、予熱室6の上部と焼却灰Aを供給する灰ホッパ2
0との間には、灰造粒装置8が介在され、灰造粒装置8
の吐出口にはベレットフィーダ9を介してベレット供給
管10が接続される。そして、灰ホッパ18から供給さ
れた焼却灰Aを灰造粒装置8により適当な大きさの粒状
の灰ペレットA1に形成し、ベレットフィーダ9により
ベレット供給管10から予熱室6に投入される。前記灰
逍粒装置8にはごみ焼却灰Aを適当な大きさに効率的に
造粒可能な形式のものが選択される。
In addition, the upper part of the preheating chamber 6 and the ash hopper 2 that supplies the incinerated ash A
An ash granulator 8 is interposed between the ash granulator 8 and the ash granulator 8.
A pellet supply pipe 10 is connected to the discharge port of the pellet feeder 9 via a pellet feeder 9. Then, the incinerated ash A supplied from the ash hopper 18 is formed into granular ash pellets A1 of an appropriate size by the ash granulator 8, and fed into the preheating chamber 6 from the pellet supply pipe 10 by the pellet feeder 9. The ash aggregation device 8 is selected to be of a type that can efficiently granulate the waste incineration ash A to an appropriate size.

前記予熱室6の下端コーナ部には、灰ペレットA1を下
流側に移送するブツシャ−装置11が配設され、プッシ
ャ一部材11aをプヅシャーシリンダ11bにより予熱
室6の底壁1aに沿って出退させて、ベレット供給管1
0から投入された灰ペレットA1を溶融室3111に移
動させる。
A pusher device 11 for transferring the ash pellets A1 to the downstream side is disposed at the lower end corner of the preheating chamber 6, and a pusher member 11a is moved along the bottom wall 1a of the preheating chamber 6 by a pusher cylinder 11b. Enter and exit the pellet supply pipe 1
The ash pellets A1 introduced from 0 are moved to the melting chamber 3111.

前記第1排ガス管7Aには、サイクロン型の集n器12
が介在されて第1燃焼排ガスD1中のダストが除去され
る。集塵器12によりa塵されたダストはダストフィー
ダ13によりダスト戻し管14を介して予熱室6の下流
側に戻すように構成される。
A cyclone type collector 12 is provided in the first exhaust gas pipe 7A.
is used to remove dust in the first combustion exhaust gas D1. The dust collected by the dust collector 12 is returned to the downstream side of the preheating chamber 6 by a dust feeder 13 via a dust return pipe 14.

また、前記スラグ冷却室5には溶融スラグBと共に、溶
融バーナ2の燃焼排ガスの一部である第2燃焼排ガスD
2が導入されており、この第2燃焼排ガスD2を排出す
る第2排ガス管7Bがスラグ冷却室5に接続される。こ
れにより、溶融スラグBが冷却されて凝縮されスラグ抜
出口4を閉塞するのを防止している。前記集塵器12か
ら第1燃焼排ガスD1を排出する第1排ガス管7Aと第
2排ガス管7Bは合流されて空気予熱器15に導入され
、その後大気側に排出される。また、空気ファン1Gの
吐出側に接続された空気供給管17は、空気予熱器15
を介して溶融バーナ2に接続される。18は空気供給管
17の出口に配設された空気i調整用ダンパー、19は
第2排ガス管7Bに配設された排ガス調節用ダンパーで
ある。
In addition to the molten slag B, the slag cooling chamber 5 also contains a second combustion exhaust gas D, which is a part of the combustion exhaust gas of the melting burner 2.
2 is introduced, and a second exhaust gas pipe 7B that discharges this second combustion exhaust gas D2 is connected to the slag cooling chamber 5. This prevents the molten slag B from being cooled and condensed and blocking the slag extraction port 4. The first exhaust gas pipe 7A and the second exhaust gas pipe 7B, which discharge the first combustion exhaust gas D1 from the dust collector 12, are combined and introduced into the air preheater 15, and then discharged to the atmosphere. Further, the air supply pipe 17 connected to the discharge side of the air fan 1G is connected to the air preheater 15.
It is connected to the melting burner 2 via. Reference numeral 18 indicates an air i adjustment damper disposed at the outlet of the air supply pipe 17, and 19 indicates an exhaust gas regulation damper disposed at the second exhaust gas pipe 7B.

次に作用を説明する。Next, the effect will be explained.

灰ホッパ20から灰造粒装置8に供給された焼却灰Aは
粒状の灰ベレットA1に形成されベレットフィーダ9に
よりベレット供給管10を介して予熱室6に投入される
。灰ベレットA1は、第1図に示すように予熱室6内に
充填され、プッシャー装置11により7B融室3側に送
られるが、溶融バーナ2からの第1燃焼排ガスD1が予
熱室6に誘引されて粒状の灰ベレットA1間の隙間を通
過し、灰ベレットA1を上層部だけでなく内部からも効
果的に予熱して第1排ガス管7Aから排出される。
The incinerated ash A supplied from the ash hopper 20 to the ash granulator 8 is formed into granular ash pellets A1, and is fed into the preheating chamber 6 by the pellet feeder 9 via the pellet supply pipe 10. The ash pellet A1 is filled into the preheating chamber 6 as shown in FIG. The ash pellets A1 pass through the gaps between the granular ash pellets A1, effectively preheating the ash pellets A1 not only from the upper layer but also from the inside, and are discharged from the first exhaust gas pipe 7A.

溶融室3では灰ベレヅトA1は溶融バーナ2によって加
熱されて溶融スラグBとなり、第2燃焼排ガスD2と共
にスラグ抜出口4からスラグ冷却室5に排出される。
In the melting chamber 3, the ash bead A1 is heated by the melting burner 2 to become molten slag B, which is discharged from the slag outlet 4 to the slag cooling chamber 5 together with the second combustion exhaust gas D2.

第1排ガス管7Aから排出された第1燃焼排ガスD1は
、集塵器12において同伴された焼却灰Aのダストが回
収された後、第2排ガス管7Bの第2燃焼排ガスD2と
合流して空気予熱器15に導入され、燃焼用空気Cを加
熱後大気側に排出される。
The first combustion exhaust gas D1 discharged from the first exhaust gas pipe 7A is combined with the second combustion exhaust gas D2 of the second exhaust gas pipe 7B after the entrained incineration ash A dust is collected in the dust collector 12. The combustion air C is introduced into the air preheater 15, heated, and then discharged to the atmosphere.

回収されたダストは、ダストフィーダ13によりダスト
戻し管14を介して予熱室6に戻される。
The collected dust is returned to the preheating chamber 6 by the dust feeder 13 via the dust return pipe 14.

発明の効果 以上に述べたごとく本発明によれば、焼却灰を造粒して
予熱室に投入し、溶融バーナの燃焼排ガスを粒状焼却灰
間を通過させて誘引するので、予熱室内の粒状焼却灰の
最下層にわたるまで効果的に予熱することができ、表層
のみの加熱に比べて予熱室をコンパクトにできる。した
がって、熱効率を向上できて溶融バーナによる供給熱量
を減少させることができ、ランニングコストを大幅に低
減できる。
Effects of the Invention As described above, according to the present invention, the incinerated ash is granulated and introduced into the preheating chamber, and the combustion exhaust gas of the melting burner is passed through the granular incinerated ash and attracted, so that the granular incineration in the preheating chamber is reduced. It is possible to effectively preheat all the way to the bottom layer of ash, making the preheating chamber more compact than when heating only the surface layer. Therefore, thermal efficiency can be improved, the amount of heat supplied by the melting burner can be reduced, and running costs can be significantly reduced.

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

第1図は本発明の溶融処理装置を示す概略構成図、第2
図は従来の溶融処理装置を示す概略構成図である。 A・・・焼却灰、A1・・・灰ベレット、B・・・溶融
スラグ、Dl・・・第1燃焼排ガス、D2・・・第2燃
焼排ガス、1・・・溶融炉、2・・・溶融バーナ、3・
・・溶融室、4・・・スラグ抜出口、5・・・スラグ冷
却室、6・・・予熱室、7A・・・第1排ガス管、7B
・・・第2排ガス管、8・・・灰造粒装置、20・・・
灰ホッパ。
Fig. 1 is a schematic configuration diagram showing the melt processing apparatus of the present invention, Fig. 2
The figure is a schematic configuration diagram showing a conventional melt processing apparatus. A... Incineration ash, A1... Ash pellet, B... Molten slag, Dl... First combustion exhaust gas, D2... Second combustion exhaust gas, 1... Melting furnace, 2... Melting burner, 3.
... Melting chamber, 4... Slag extraction port, 5... Slag cooling chamber, 6... Preheating chamber, 7A... First exhaust gas pipe, 7B
...Second exhaust gas pipe, 8...Ash granulator, 20...
Ash hopper.

Claims (1)

【特許請求の範囲】 1、溶融バーナを備えた溶融炉を使用して焼却灰を加熱
溶融し溶融スラグを排出するに際し、焼却灰を造粒して
溶融炉に投入し、溶融バーナの燃焼排ガスを粒状焼却灰
投入側に誘引して粒状焼却灰を予熱することを特徴とす
る焼却灰溶融処理方法。 2、溶融炉の溶融室に溶融バーナを備え、この溶融バー
ナにより焼却灰を溶融しこの溶融スラグをスラグ冷却室
に排出する焼却灰溶融処理装置において、灰投入ホッパ
と溶融室の間に、焼却灰を造粒する造粒装置と、造粒さ
れた粒状焼却灰を予熱する予熱室とを設け、前記予熱室
に燃焼排ガスを誘引する排ガス管を接続したことを特徴
とする焼却灰溶融処理装置。
[Claims] 1. When heating and melting incinerated ash and discharging molten slag using a melting furnace equipped with a melting burner, the incinerated ash is granulated and charged into the melting furnace, and the combustion exhaust gas of the melting burner is A method for melting incinerated ash characterized by preheating granular incinerated ash by attracting it to the granular incinerated ash input side. 2. In the incinerated ash melting processing equipment, which is equipped with a melting burner in the melting chamber of the melting furnace, and which melts the incinerated ash and discharges the molten slag into the slag cooling chamber, the incinerated ash is placed between the ash input hopper and the melting chamber. An incinerated ash melting processing device comprising: a granulating device for granulating ash; a preheating chamber for preheating the granulated incinerated ash; and an exhaust gas pipe for drawing combustion exhaust gas connected to the preheating chamber. .
JP12067589A 1989-05-15 1989-05-15 Method and apparatus for incineration ash melting treatment Expired - Lifetime JPH0684812B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12067589A JPH0684812B2 (en) 1989-05-15 1989-05-15 Method and apparatus for incineration ash melting treatment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12067589A JPH0684812B2 (en) 1989-05-15 1989-05-15 Method and apparatus for incineration ash melting treatment

Publications (2)

Publication Number Publication Date
JPH02302512A true JPH02302512A (en) 1990-12-14
JPH0684812B2 JPH0684812B2 (en) 1994-10-26

Family

ID=14792157

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12067589A Expired - Lifetime JPH0684812B2 (en) 1989-05-15 1989-05-15 Method and apparatus for incineration ash melting treatment

Country Status (1)

Country Link
JP (1) JPH0684812B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06174224A (en) * 1992-09-21 1994-06-24 Hitachi Zosen Corp Ash fusion furnace
JPH06341631A (en) * 1993-06-01 1994-12-13 Hitachi Zosen Corp Method and device for feeding ash in burner type ash-melting furnace
CN103994445A (en) * 2014-05-22 2014-08-20 北京中科通用能源环保有限责任公司 Feeding device and cooling system for slag cooler of fluidized bed garbage incinerator

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06174224A (en) * 1992-09-21 1994-06-24 Hitachi Zosen Corp Ash fusion furnace
JPH06341631A (en) * 1993-06-01 1994-12-13 Hitachi Zosen Corp Method and device for feeding ash in burner type ash-melting furnace
CN103994445A (en) * 2014-05-22 2014-08-20 北京中科通用能源环保有限责任公司 Feeding device and cooling system for slag cooler of fluidized bed garbage incinerator

Also Published As

Publication number Publication date
JPH0684812B2 (en) 1994-10-26

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