JPH09318035A - Device for melting and processing ignited ashe - Google Patents

Device for melting and processing ignited ashe

Info

Publication number
JPH09318035A
JPH09318035A JP13982896A JP13982896A JPH09318035A JP H09318035 A JPH09318035 A JP H09318035A JP 13982896 A JP13982896 A JP 13982896A JP 13982896 A JP13982896 A JP 13982896A JP H09318035 A JPH09318035 A JP H09318035A
Authority
JP
Japan
Prior art keywords
melting furnace
ash
melting
dust collector
water
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
JP13982896A
Other languages
Japanese (ja)
Other versions
JP3603083B2 (en
Inventor
Kinichi Watanabe
錦一 渡辺
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP13982896A priority Critical patent/JP3603083B2/en
Publication of JPH09318035A publication Critical patent/JPH09318035A/en
Application granted granted Critical
Publication of JP3603083B2 publication Critical patent/JP3603083B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/82Recycling of waste of electrical or electronic equipment [WEEE]

Landscapes

  • Processing Of Solid Wastes (AREA)
  • Vertical, Hearth, Or Arc Furnaces (AREA)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
  • Chimneys And Flues (AREA)
  • Gasification And Melting Of Waste (AREA)

Abstract

PROBLEM TO BE SOLVED: To simplify a structure of a device, enable the device to be mounted at a low cost and further facilitate its maintenance by a method wherein a heat exchanger is installed between a multi-cyclone dust collector and a melting furnace and discharged smoke passed through the dust collector is washed with water by a Theisen washing machine. SOLUTION: Raw material ashes stored at a raw material ash stock yard 1 are combusted again and/or dried within the stock yard 1 as required and they are transferred into a hopper 5a by a predetermined amount by a transferring means 4 while they are being broken into fine substances by a screw conveyor 2c. They are fed into a melting furnace 5 by a specified amount through means 5b for cutting a specified amount and melted there. The ashes in a water- curushing type device are crushed with water and cooled and in turn the ashes in an air-cooling type device are naturally cooled. Discharged smoke containing a large amount of flying ashes discharged from the melting furnace 5 is cooled by a heat exchanger 10, reaches a multi-cyclone dust collector 12, garbages containing flying ashes are removed and reach a Theisen washing machine 13, washed with water there and further the garbages are removed.

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】この発明は、主として一般廃
棄物或は産業廃棄物等のゴミを焼却した際に生じる焼却
灰を、環境を汚染しないように、或は再利用を図れるよ
うに処理する焼却灰の溶融処理装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention mainly treats incinerated ash generated when incinerating waste such as general waste or industrial waste so as not to pollute the environment or to be reused. The present invention relates to a melting treatment device for incinerated ash.

【0002】[0002]

【従来の技術】一般家庭や各種工場から出るゴミは、環
境破壊や汚染を防止するためにこれをそのまま投棄する
わけには行かないので焼却処分することが行われてい
る。しかし、その際に生じる焼却灰もこれをそのまま投
棄すると、水中に溶け出して水を汚染したり、或は風で
焼却灰が空気中に飛散したりして生活環境を汚染するの
で、これを溶融させて水中に落下させ、スラグにして回
収してこれを埋め立てにしたり、或は建築資材の骨材と
して再利用を図ることが考えられている。
2. Description of the Related Art Garbage discharged from ordinary households and various factories is incinerated because it cannot be discarded as it is in order to prevent environmental damage and pollution. However, if the incineration ash generated at that time is discarded as it is, it will dissolve into the water and pollute the water, or the incineration ash will be scattered into the air by the wind and pollute the living environment. It is considered to melt and drop into water to recover slag for landfilling, or to reuse it as an aggregate of building materials.

【0003】そのための装置として、焼却灰を溶融炉で
溶融させた後水中に落下させて水砕させるようにした装
置が種々公知であるが、いずれも焼却灰の原灰を溶融炉
の受け入れ装置で受け入れる前に、粉砕して細かくする
破砕機や再焼却させるための焼却乾燥炉を溶融炉の他に
備えている他、飛灰を多く含んでいる排煙をクリーンに
するために、バグフィルターや電気集塵機、さらには高
温の排煙の温度を下げるための何層にも渡る冷却装置等
をも備えている。
As a device therefor, various devices are known in which the incinerated ash is melted in a melting furnace and then dropped into water to be water-granulated. In addition to the melting furnace, a crusher for crushing and finely crushing, and an incinerator / dryer for re-incineration are also provided before being accepted in. It is also equipped with a dust collector, an electric dust collector, and multiple layers of cooling devices for lowering the temperature of high-temperature smoke.

【0004】[0004]

【発明が解決しようとする課題】したがって、この従来
公知のものは、装置全体が必然的に大型化し、製作コス
トが高くつく他、清掃、部品交換等のメンテナンスも頻
繁に行わなくてはならないという問題点があった。
Therefore, in the known device, the whole device inevitably becomes large in size, the manufacturing cost is high, and maintenance such as cleaning and parts replacement must be frequently performed. There was a problem.

【0005】この発明の目的は、構造を簡単にして安い
製作コストで設置でき、しかもメンテナンスも容易であ
るという、焼却灰の溶融処理装置を提供せんとするにあ
る。
An object of the present invention is to provide a melting treatment apparatus for incinerated ash, which has a simple structure, can be installed at a low manufacturing cost, and is easy to maintain.

【0006】[0006]

【課題を解決するための手段】上述した目的を達成する
ためにこの発明は、スクリューコンベヤーを備えた耐火
構造の原灰受入ストックヤードと、原灰を溶融させる溶
融炉と、この溶融炉に取り付けられた定量切出手段を備
えた原灰受け入れ用のホッパーと、前記ストックヤード
内の原灰を前記ホッパーへ移送する移送手段と、前記溶
融炉より排出される排煙内の飛灰を含む塵芥を分離する
マルチサイクロン集塵機と、この集塵機と前記溶融炉と
の間に設けられた熱交換器と、前記集塵機を通過した排
煙を水洗いするタイゼンワッシャーとを含むものであ
る。
In order to achieve the above-mentioned object, the present invention provides a raw ash receiving stock yard having a refractory structure equipped with a screw conveyor, a melting furnace for melting raw ash, and a melting furnace attached to the melting furnace. A hopper for receiving raw ash provided with a fixed amount cutting means, a transfer means for transferring the raw ash in the stockyard to the hopper, and a dust containing fly ash in the flue gas discharged from the melting furnace. And a heat exchanger provided between the dust collector and the melting furnace, and a Taizen washer for washing the flue gas passing through the dust collector with water.

【0007】その際にこの発明は、溶融炉に溶融灰の水
砕手段か、或は空冷手段のどちらかを備えさせるもので
ある。
In this case, the present invention provides the melting furnace with either a water crushing means for molten ash or an air cooling means.

【0008】そして、熱交換器を空冷式とし、その際の
生ずる熱風を溶融炉へ還元させたり、或は未燃焼の原灰
を再燃焼及び又は乾燥させるために、原灰ストックヤー
ドへ送るものである。
Then, the heat exchanger is of an air cooling type, and the hot air generated at that time is sent to a raw ash stockyard in order to reduce it to a melting furnace or reburn and / or dry unburned raw ash. Is.

【0009】この発明はまた、溶融炉より排出される排
煙の成分を自動的に検出する手段を排煙の煙道に設置す
ることができる。
Further, according to the present invention, means for automatically detecting the components of the flue gas discharged from the melting furnace can be installed in the flue gas flue.

【0010】[0010]

【作用】請求項1のように構成すると、原灰受入ストッ
クヤードへ貯留された原灰は、耐火構造の該ストックヤ
ード内で必要に応じて再燃焼及び又は乾燥させられて、
スクリューコンベヤーによって細かく破砕されつつ移送
手段によって所定量ずつホッパー内へ移送される。ここ
で定量切り出し手段によって一定量ずつを溶融炉内へ送
り込まれて溶融され、水砕式のものは水砕されて冷却さ
れるが、空冷式のものは自然冷却される。溶融炉より排
出される飛灰を多く含んだ排煙は、熱交換器により冷却
されてマルチサイクロン集塵機に至り、これで飛灰を含
む塵芥を除却されてタイゼンウォッシャーに至り、さら
に水洗いされてサイクロン集塵機で補足し損なった塵芥
を除去し、冷却されて大気へ放出されることになる。
According to the first aspect of the invention, the raw ash stored in the raw ash receiving stockyard is reburned and / or dried in the stockyard of the fireproof structure, if necessary,
While being finely crushed by the screw conveyor, it is transferred into the hopper by a predetermined amount by the transfer means. Here, a fixed amount is sent into the melting furnace by a constant amount cutting means and melted, and the water granulation type is water granulated and cooled, while the air cooling type is naturally cooled. Exhaust smoke containing a large amount of fly ash discharged from the melting furnace is cooled by a heat exchanger and reaches a multi-cyclone dust collector, which removes dust containing fly ash and reaches a Taizen washer, which is further washed with water. Cyclone dust collector removes dust that has failed to be captured, and it is cooled and released to the atmosphere.

【0011】請求項2のように構成すると、溶融炉内で
溶融された原灰は水中へ投下されることによって水砕さ
れ、細かい砂利状のスラグとなって回収されることにな
る。
According to the second aspect of the invention, the raw ash melted in the melting furnace is dropped into water to be water granulated and recovered as fine gravel-like slag.

【0012】請求項3のように構成すると、溶融炉内で
溶融された原灰は例えばバケットのようなものの中へ貯
留され、塊りとなって固化する。
According to the third aspect of the invention, the raw ash melted in the melting furnace is stored in, for example, a bucket, and is solidified as a lump.

【0013】請求項4のように構成すると、熱風が溶融
炉内へ還元されるので、溶融炉内の温度低下を防止でき
ることにより、燃料を省略することができる。
According to the present invention, the hot air is reduced to the inside of the melting furnace, so that the temperature inside the melting furnace can be prevented from lowering and the fuel can be omitted.

【0014】請求項5のように構成すると、原灰受入ス
トックヤード内にある原灰の中で未焼却のものは焼却さ
れ、全体が溶融炉内で溶融し易いように乾燥させられる
ことになる。
According to the present invention, the unburned raw ash in the raw ash receiving stockyard is incinerated, and the whole raw ash is dried so as to be easily melted in the melting furnace. .

【0015】請求項6のように構成すると、排煙内の有
害物質の濃度を自動的に検出できるので、これにより処
理装置全体を制御することが可能となる。
According to the sixth aspect of the present invention, the concentration of the harmful substance in the flue gas can be automatically detected, so that the entire processing apparatus can be controlled.

【0016】[0016]

【発明の実施の形態】図面はこの発明の一実施例を示
し、図1乃至図2において、1は原灰受入ストックヤー
ドである。この原灰受入ストックヤード1は、コンクリ
ートで作った穴1a内に設置された鉄板フレームの収納
槽2を有しており、この収納槽2の開放上部には固定式
の蓋2aと開閉式の可動蓋2bが取り付けられている。
この収納槽2の内底部には、一対のスクリューコンベヤ
ー2c,2cが並設されており、内部に収納した原灰3
を細かく破砕しつつ送出口2dへ送り出す。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The drawings show an embodiment of the present invention. In FIGS. 1 and 2, reference numeral 1 is a raw ash receiving stockyard. This raw ash receiving stockyard 1 has a storage tank 2 of an iron plate frame installed in a hole 1a made of concrete, and a fixed lid 2a and an opening / closing type storage tank 2 are provided at an open upper portion of the storage tank 2. The movable lid 2b is attached.
A pair of screw conveyors 2c, 2c are arranged side by side on the inner bottom of the storage tank 2, and the raw ash 3 stored inside is stored.
Is crushed into small pieces and sent to the outlet 2d.

【0017】5は流下式の表面溶融式の溶融炉であり、
この溶融炉5の一側に定量切出手段5b付きのホッパー
5aが取り付けられており、原灰3の収納槽2のスクリ
ューコンベヤー2c,2cを介して送出口2dより送り
出された原灰を、例えばベルトコンベヤーのような移送
手段4を介して所定量ずつ受け入れる。
Reference numeral 5 denotes a surface-flow-type melting furnace of a flow-down type,
A hopper 5a with a quantitative cutting means 5b is attached to one side of the melting furnace 5, and the raw ash sent from the outlet 2d via the screw conveyors 2c, 2c of the storage tank 2 for the raw ash 3 is A predetermined amount is received via a transfer means 4 such as a belt conveyor.

【0018】ホッパー5a内に供給された原灰は、例え
ばプランジャー装置のような定量切出手段5bを介して
溶融炉5内へ送り込まれ、ここにおいて図示はしてない
が、傾斜している炉床を流下する間に、バーナー5cよ
り噴射される高温の炎によって溶融され、さらに自然流
下してスクリューコンベアー6aを収装した水槽6内へ
落下し、こので細かく水砕された後、スクリューコンベ
アー6aで取り出され、さらに、ベルトコンベヤー7を
介してスラグフトックヤード8へ貯留されることにな
る。尚、図示はしてないが、このスラグスットックヤー
ド8の下部に,例えばダンプカーのようなトラックを誘
導してホッパーを開き、内部の細かく破砕されたスラッ
グを積み込むことになる。
The raw ash supplied into the hopper 5a is fed into the melting furnace 5 through a fixed amount cutting means 5b such as a plunger device, and is inclined here though not shown here. While flowing down the hearth, it is melted by the high-temperature flame injected from the burner 5c, further flows down naturally, and falls into the water tank 6 accommodating the screw conveyor 6a. It is taken out by the conveyor 6 a, and further stored in the slag hook yard 8 via the belt conveyor 7. Although not shown, a truck such as a dump truck is guided to the lower portion of the slag stockyard 8 to open the hopper and load the finely crushed slug inside.

【0019】10は空冷式の熱交換器であり、その内部
構造は図示はしてないが例えば細管の中に溶融炉5より
排出されて来る高温度の排煙を通し、ブロワー10aに
よって外部よりこの細管を冷却する構造となっている。
そして、その際に生ずる熱風の一部は連通管10bを介
して溶融炉5内へ還元するようになっている。また、さ
らにこの熱風の一部は、想像線で示した連通管20を介
してストックヤード1内の収納槽2内へ送り込まれるよ
うに構成されてもいる。さらに、この熱交換器を水冷式
とすると、蒸気を製造することも可能となろう。
Reference numeral 10 denotes an air-cooling type heat exchanger, the internal structure of which is not shown, but for example, high-temperature flue gas discharged from the melting furnace 5 is passed through a thin tube, and is blown from outside by a blower 10a. It has a structure for cooling this thin tube.
Then, a part of the hot air generated at that time is reduced into the melting furnace 5 through the communication pipe 10b. Further, a part of the hot air is also sent into the storage tank 2 in the stockyard 1 via the communication pipe 20 shown by the imaginary line. Furthermore, if the heat exchanger is water-cooled, it will be possible to produce steam.

【0020】12はマルチサイクロン集塵機である。こ
のマルチサイクロン集塵機12は従来公知のサイクロン
集塵機を改良したもので、図示してはないが煙道エリア
を3〜4分割して煙の回転半径が小さくなるようにし
て、従来のものよりも粉塵を補集できるように工夫して
ある。このマルチサイクロン集塵機は電気集塵機に較べ
て排煙を極端に冷却させる必要がない。熱交換器10に
よりある程度冷却された排煙は、煙管11を介してこの
マルチサイクロン集塵機12へ送り込まれ、ここにおい
て飛灰を含む塵芥が分離され、さらに煙管9を介してタ
イゼンウォッシャー13へ送られる。ここでさらにマル
チサイクロン集塵機12で補集できなかった飛灰を含む
塵芥が排煙より洗い出され、温度降下させられる。この
タイゼンウォッシャー13は硝石灰等の中和剤を混入し
た循環水槽17より循環されて使用されており、ここに
おいてイオウ酸化物、窒素酸化物、或は一酸化炭素のよ
うな有害物質も取り除かれ、クリーンな低温の水蒸気と
なってさらに煙管19を介し煙突16より大気へ放出さ
せられる。
Reference numeral 12 is a multi cyclone dust collector. This multi-cyclone dust collector 12 is an improvement of the conventionally known cyclone dust collector. Although not shown, the flue area is divided into 3 to 4 parts so that the radius of smoke rotation becomes smaller, and the dust particles are more dusty than the conventional ones. It has been devised so that it can be collected. Compared with the electric dust collector, this multi cyclone dust collector does not need to cool the exhaust gas extremely. The flue gas cooled to some extent by the heat exchanger 10 is sent to the multi-cyclone dust collector 12 through the smoke pipe 11, where dust including fly ash is separated, and further sent to the Taizen washer 13 through the smoke pipe 9. To be Here, the dust containing fly ash that could not be collected by the multi-cyclone dust collector 12 is washed out from the flue gas and the temperature is lowered. This Taizen washer 13 is used by being circulated from a circulating water tank 17 containing a neutralizing agent such as lime nitrate, in which harmful substances such as sulfur oxides, nitrogen oxides or carbon monoxide are also removed. As a result, clean, low-temperature water vapor is further emitted to the atmosphere from the chimney 16 through the smoke pipe 19.

【0021】尚、煙管9と11には、排煙内の有害物質
を検出する、例えば島津製作所製のIRA107型機に
よるイオウ酸化物検出手段、CGT101A型機による
一酸化炭素検出手段、或はNOA305A型機による窒
素酸化物検出手段のような検出手段が取り付けられてお
り、図示してないコントロール盤へ信号を送り、有害物
質の濃度を表示すると共に、この信号に基づいて溶融炉
内の温度や原灰の供給量、供給速度等を自動的に制御す
ることもできることになる。そして、18は水砕手段を
備えた溶融炉の場合の水槽へ落下した溶融物より生ずる
飛灰を含んだ水蒸気を送り出すパイプであり、溶融炉5
の排気口5dより煙突16に近い煙管19へ接続させて
いる。
The smoke pipes 9 and 11 are for detecting harmful substances in the flue gas, for example, sulfur oxide detection means by IRA107 type machine manufactured by Shimadzu Corporation, carbon monoxide detection means by CGT101A type machine, or NOA305A. A detector such as a nitrogen oxide detector by a mold machine is attached to the control panel (not shown) to display the concentration of harmful substances and to display the temperature in the melting furnace based on this signal. It is also possible to automatically control the supply amount and supply rate of raw ash. Further, reference numeral 18 is a pipe for sending out water vapor containing fly ash generated from the molten material dropped into the water tank in the case of a melting furnace equipped with water granulating means.
The exhaust pipe 5d is connected to the smoke pipe 19 near the chimney 16.

【0022】図3は空冷手段を備えた溶融炉21であ
り、この溶融炉21内で溶融された原灰は、溶融炉21
外に設置した例えばバケット22内へ流下貯留させら
れ、自然放置して冷却されることになる。
FIG. 3 shows a melting furnace 21 equipped with air cooling means. Raw ash melted in the melting furnace 21 is melted by the melting furnace 21.
For example, the water is stored in the bucket 22 installed outside and stored down, and naturally left to be cooled.

【0023】[0023]

【発明の効果】この発明は以上のように構成したので、
次のような作用効果を奏し得る。
Since the present invention is constructed as described above,
The following operational effects can be obtained.

【0024】請求項1のように構成すると、原灰ストッ
クヤードは同時にスクリューコンベヤーによる破砕と耐
火構造の収納槽へ熱交換器或は溶融炉からの熱風の供給
を受けることにより、専用の破砕手段や焼却乾燥炉を省
略することができる上に、マルチサイクロン集塵機によ
り高温の排煙を冷却できる何層にも設けた冷却手段を必
要としないので、構成が簡単となり、安価に製造するこ
とができるものである。このように一度溶融させて固化
させたものは、水に溶け出さないので、これを廃棄して
も環境を汚染したり、破壊したりする恐れがないもので
ある。
According to the first aspect of the present invention, the raw ash stockyard is simultaneously crushed by the screw conveyor and is supplied with hot air from the heat exchanger or the melting furnace to the storage tank of the refractory structure, so that a dedicated crushing means is provided. And an incinerator / dryer can be omitted, and since the cooling means provided in multiple layers that can cool high-temperature flue gas by the multi-cyclone dust collector is not required, the structure is simple and the manufacturing cost is low. It is a thing. Such a material which is once melted and solidified does not dissolve in water, and therefore there is no fear of polluting or destroying the environment even if it is discarded.

【0025】請求項2のように構成すると、焼却灰は細
粒状のスラグとなるので、これをコンクリートなどの建
築資材の骨材として再利用を図ることができるものであ
る。
According to the second aspect of the invention, since the incineration ash becomes fine-grained slag, it can be reused as an aggregate for building materials such as concrete.

【0026】請求項3のように構成すると、固化したス
ラグを適当な大きさに破砕することにより、大粒のスラ
グとすることができ、コンクリートの骨材、道路用の砂
利その他の建築資材として用いることができる。
According to the third aspect of the present invention, the solidified slag can be crushed into an appropriate size to obtain a large-sized slag, which can be used as concrete aggregate, gravel for roads and other building materials. be able to.

【0027】請求項4と5のように構成すると、熱風を
再利用することにより、溶融炉内を加熱するための燃料
や原灰を再燃焼させたり、乾燥させたりするための燃料
を節約することができるものである。
According to the fourth and fifth aspects, the hot air is reused to save the fuel for heating the inside of the melting furnace and the fuel for reburning or drying the raw ash. Is something that can be done.

【0028】請求項6のように構成すると、大気へイオ
ウ酸化物や窒素酸化物、或は一酸化炭素のような有害物
質が放出されるのを未然に防止することが可能となるも
のである。
According to the sixth aspect, it is possible to prevent the release of harmful substances such as sulfur oxides, nitrogen oxides, or carbon monoxide into the atmosphere. .

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

【図1】本願発明に係るゴミの焼却灰の溶融処理装置を
概略的に説明する平面図である。
FIG. 1 is a plan view schematically illustrating a melting incineration ash melting apparatus according to the present invention.

【図2】図1に示した装置の一部断面正面図である。2 is a partial cross-sectional front view of the device shown in FIG.

【図3】溶融炉の他の実施例を示す説明図である。FIG. 3 is an explanatory view showing another embodiment of the melting furnace.

【符号の説明】[Explanation of symbols]

1 原灰受入ストックヤード 2 収納槽 2c スクリューコンベアー 3 灰 4 移送手段 5,21 溶融炉 5a ホッパー 8 スラグストックヤード 9 煙管 10 熱交換器 10a ブロワー 11 煙管 12 マルチサイクロン集塵機 13 タンゼンウォッシャー 14 排煙検出器 15 排煙検出器 16 煙突 1 raw ash receiving stockyard 2 storage tank 2c screw conveyor 3 ash 4 transfer means 5,21 melting furnace 5a hopper 8 slag stockyard 9 smoke pipe 10 heat exchanger 10a blower 11 smoke pipe 12 multi-cyclone dust collector 13 Tanzen washer 14 smoke detection Unit 15 Smoke emission detector 16 Chimney

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 スクリューコンベヤーを備えた耐火構造
の原灰受入ストックヤードと、原灰を溶融させる溶融炉
と、この溶融炉に取り付けられた定量切出手段を備えた
原灰受け入れ用のホッパーと、前記ストックヤード内の
原灰を前記ホッパーへ移送する移送手段と、前記溶融炉
より排出される排煙内の飛灰を含む塵芥を分離するマル
チサイクロン集塵機と、この集塵機と前記溶融炉との間
に設けられた熱交換器と、前記集塵機を通過した排煙を
水洗いするタイゼンワッシャーとを含むことを特徴とす
る、焼却灰の溶融処理装置。
1. A refractory raw ash receiving stockyard equipped with a screw conveyor, a melting furnace for melting raw ash, and a hopper for receiving raw ash equipped with a fixed amount cutting means attached to the melting furnace. , A transfer means for transferring the raw ash in the stockyard to the hopper, a multi-cyclone dust collector for separating dusts containing fly ash in the flue gas discharged from the melting furnace, and the dust collector and the melting furnace An incineration ash melting treatment apparatus comprising a heat exchanger provided between the dust collector and a Taizen washer for washing the flue gas passing through the dust collector with water.
【請求項2】 溶融炉が溶融物の水砕手段を備えている
ことを特徴とする、請求項1記載の焼却灰の溶融処理装
置。
2. The incinerator ash melting treatment apparatus according to claim 1, wherein the melting furnace is provided with a water granulating means for the molten material.
【請求項3】 溶融炉が溶融物の空冷手段を備えている
ことを特徴とする、請求項1記載の焼却灰の溶融処理装
置。
3. The apparatus for melting incineration ash according to claim 1, wherein the melting furnace is provided with a means for cooling the melt.
【請求項4】 熱交換器は空冷式であり、その際の生ず
る熱風を溶融炉へ還元させる手段をさらに備えているこ
とを特徴とする、請求項1乃至3のいずれかに記載の焼
却灰の溶融処理装置。
4. The incinerator ash according to any one of claims 1 to 3, wherein the heat exchanger is an air-cooled type, and further comprises means for reducing hot air generated at that time to a melting furnace. Melt processing equipment.
【請求項5】熱交換器は空冷式であり、その際の生ずる
熱風を原灰ストックヤードへ導き、未燃焼の原灰を再燃
焼及び又は乾燥させる手段を備えていることを特徴とす
る、請求項1乃至4のいずれかに記載の焼却灰の溶融処
理装置。
5. The heat exchanger is an air-cooled type, and is provided with a means for guiding hot air generated at that time to a raw ash stockyard and reburning and / or drying unburned raw ash. The incineration ash melting treatment apparatus according to any one of claims 1 to 4.
【請求項6】溶融炉より排出される排煙の成分を自動的
に検出する手段が、排煙の煙道に設置されていることを
特徴とする、請求項1乃至5のいずれかに記載の焼却炉
の溶融処理装置。
6. The method according to claim 1, wherein means for automatically detecting the components of the flue gas emitted from the melting furnace is installed in the flue gas duct of the flue gas. Incinerator melting treatment equipment.
JP13982896A 1996-06-03 1996-06-03 Melting equipment for incinerated ash Expired - Lifetime JP3603083B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13982896A JP3603083B2 (en) 1996-06-03 1996-06-03 Melting equipment for incinerated ash

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13982896A JP3603083B2 (en) 1996-06-03 1996-06-03 Melting equipment for incinerated ash

Publications (2)

Publication Number Publication Date
JPH09318035A true JPH09318035A (en) 1997-12-12
JP3603083B2 JP3603083B2 (en) 2004-12-15

Family

ID=15254437

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13982896A Expired - Lifetime JP3603083B2 (en) 1996-06-03 1996-06-03 Melting equipment for incinerated ash

Country Status (1)

Country Link
JP (1) JP3603083B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104296546A (en) * 2014-05-05 2015-01-21 山东省能源与环境研究院 Rotary cement kiln waste heat utilization system with flue gas separator

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104296546A (en) * 2014-05-05 2015-01-21 山东省能源与环境研究院 Rotary cement kiln waste heat utilization system with flue gas separator
CN104296546B (en) * 2014-05-05 2016-03-30 山东省能源与环境研究院 A kind of cement rotary kiln bootstrap system that smoke separator is set

Also Published As

Publication number Publication date
JP3603083B2 (en) 2004-12-15

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