JPS5854627B2 - Dust treatment method in waste incineration treatment - Google Patents

Dust treatment method in waste incineration treatment

Info

Publication number
JPS5854627B2
JPS5854627B2 JP52009518A JP951877A JPS5854627B2 JP S5854627 B2 JPS5854627 B2 JP S5854627B2 JP 52009518 A JP52009518 A JP 52009518A JP 951877 A JP951877 A JP 951877A JP S5854627 B2 JPS5854627 B2 JP S5854627B2
Authority
JP
Japan
Prior art keywords
dust
waste incineration
granular solid
treatment
incineration
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
Application number
JP52009518A
Other languages
Japanese (ja)
Other versions
JPS5395171A (en
Inventor
勇 森
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.)
Ebara Corp
Original Assignee
Ebara Infilco Co Ltd
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 Ebara Infilco Co Ltd filed Critical Ebara Infilco Co Ltd
Priority to JP52009518A priority Critical patent/JPS5854627B2/en
Publication of JPS5395171A publication Critical patent/JPS5395171A/en
Publication of JPS5854627B2 publication Critical patent/JPS5854627B2/en
Expired legal-status Critical Current

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  • Processing Of Solid Wastes (AREA)
  • Glanulating (AREA)
  • Gasification And Melting Of Waste (AREA)

Description

【発明の詳細な説明】 本発明は、都市ごみや汚泥のごとく燃焼時に多量のダス
トを発生する廃棄物の焼却炉のダストを処分する方法に
関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for disposing of dust from an incinerator for wastes such as municipal waste and sludge that generate a large amount of dust when burned.

一般に焼却炉では発生するダストは煙道中の集じん機で
分離されるが、このダストの取扱いは種種の障害があっ
て困難なものである。
Generally, the dust generated in an incinerator is separated by a dust collector in the flue, but handling this dust is difficult due to various obstacles.

従来の焼却炉では、炉下から灰貯槽までの焼却灰輸送コ
ンベアに載荷されて、族ホッパーや灰ピットに併合貯留
している。
In conventional incinerators, ash is loaded onto a conveyor that transports ash from the bottom of the furnace to an ash storage tank, and then is stored in a group hopper or ash pit.

しかるにコンベアやピット内で焼却灰の消火や炉圧シー
ルに用いられた水が灰と同伴し、ダストと混合しスラリ
ー状となり輸送中に漏洩し作業場内や輸送経路の環境を
汚染することがしばしばあって公害防止上問題があった
However, the water used for extinguishing the incinerated ash and sealing the furnace pressure inside the conveyor and pit is often accompanied by the ash, mixed with dust, forms a slurry, and leaks during transportation, contaminating the environment in the workplace and along the transportation route. This caused problems in terms of pollution prevention.

また、ダストのみを別途に搬出することもあるが、この
場合は風や振動で飛散し易く、これを防止するため水を
噴霧して加湿する方法もあるが、その水量はダスト重量
の50%にも達するので輸送効率が低下するばかりでな
く事後処理を困難として多大の費用を要することとなる
欠点がある。
In addition, sometimes the dust is transported separately, but in this case it is easily blown away by wind and vibrations.To prevent this, there is a method of humidifying by spraying water, but the amount of water is 50% of the weight of the dust. This not only reduces transport efficiency but also makes post-processing difficult and requires a large amount of cost.

さらに、ダストが水に浸漬または水中を通過する際に、
ダストに含まれる微粒子、無機塩類、有機酸、未燃カー
ボン、金属化合物などによりピット排水やコンベア排水
が汚染されて、その水処理をも困難なものにしている。
Furthermore, when dust is immersed in or passes through water,
The pit drainage and conveyor drainage are contaminated by fine particles, inorganic salts, organic acids, unburned carbon, metal compounds, etc. contained in the dust, making it difficult to treat the water.

近年は、セメントと水とダストを混合し固化成形する方
法も実施されているが、養生に長日数と大スペースを必
要とするほか比較的高い媒材を必要とするためコスト割
り高となって経済性に難点がある。
In recent years, methods have been implemented in which cement, water, and dust are mixed and solidified, but this method requires many days and a large space for curing, and requires relatively expensive media, making it expensive. There is a problem with economic efficiency.

本発明は、これら従来の欠点を除去しようとするもので
、廃棄物焼却処理に際して生ずるダストの処分のための
作業上の取扱いが便利で、運搬中および投棄地で飛散せ
ず、湿式コンベアや、灰貯留所内で冠水により泥ねいと
なるのを防ぎ無公害処理と併せて再利用度を著しく高め
られる処理方法を提供することを目的としたものである
The present invention aims to eliminate these conventional drawbacks, and it is convenient to handle the dust generated during waste incineration, does not scatter during transportation or at the dumping site, and uses a wet conveyor. The object of the present invention is to provide a treatment method that can prevent ash storage from becoming muddy due to flooding and can significantly increase the degree of reuse as well as pollution-free treatment.

また本発明では、従来の不経済な処理を行なうことなく
大量に一度に処理でき処理操作条件も良好にし経済的費
用で作業性も著しく向上できる処理方法とすることにあ
る。
Another object of the present invention is to provide a processing method that can process a large amount at once without carrying out the conventional uneconomical processing, has good processing operating conditions, and can significantly improve workability at an economical cost.

本発明は、廃棄物焼却炉の煙道中に設けられるダスト分
離のための重力式沈降装置、慣性力式沈降装置、静電式
沈降装置などの乾式ダスト分離設備廃熱ボイラなとで捕
集したダストを該ダスト分離設備から引抜き後、焼却灰
と併合輸送又は貯留する前に最大辺長1007n7n〜
10u+程度の粒状固形物体に水や薬剤などの他物質の
添加をすることなく直接圧搾成形するため、クラッシャ
、篩分機、定量フィーダを経て圧搾成形機を通過させて
固化することを特徴とした廃棄物焼却炉の集塵装置から
排出されるダストの処理方法である。
The present invention deals with the collection of dust by dry dust separation equipment such as a gravity settling device, an inertial force settling device, an electrostatic settling device, etc. for dust separation installed in the flue of a waste incinerator, such as a waste heat boiler. After extracting the dust from the dust separation equipment and before transporting or storing it together with the incinerated ash, the maximum side length is 1007n7n~
In order to directly compress and mold a granular solid object of about 10U+ without adding other substances such as water or chemicals, it is passed through a crusher, sieve, quantitative feeder, and then through a compression molding machine and solidified. This is a method for processing dust discharged from the dust collector of a material incinerator.

本発明の実施例を図面を参照して説明すると、焼却炉1
の煙道に設けたダスト分離設備3例えば重力式沈降型、
慣性力式沈降型又は静電式沈降型の集塵装置で燃焼排ガ
ス中のダストを捕集し、この集塵装置からのダスト取出
しの直後に固化成形処理装置8を設け、水に浸漬しても
潮解せず風に吹かれても飛散しないための処理を講じた
後に、焼却灰搬出コンベアやダスト貯留槽に投入処理す
る。
An embodiment of the present invention will be described with reference to the drawings.
Dust separation equipment installed in the flue 3 e.g. gravity settling type,
Dust in the combustion exhaust gas is collected by an inertial force sedimentation type or electrostatic sedimentation type dust collector, and immediately after the dust is taken out from this dust collector, a solidification molding treatment device 8 is installed, and the dust is immersed in water. After taking steps to ensure that the ash does not deliquesce and will not scatter even when blown by the wind, it is placed on the incineration ash conveyor or into the dust storage tank.

例えば前記電気集塵装置で除去された都市ごみ焼却炉煙
道ガスダストのね径分布は第1表の通りである。
For example, the diameter distribution of municipal waste incinerator flue gas dust removed by the electrostatic precipitator is shown in Table 1.

このような微粒子粉体を集塵装置から取出した姿のまま
、伺らの添加物や予備処理なしに固形化する方法として
前記固化成形処理装置8としてプリケラティングマシン
即ち、同速度で内側に向って回転する2個のロールの表
面にポケットが刻まれており、このロールの間に粉体を
供給するとロールの回転にともない圧縮され造粒され粒
が連続的に排出する造粒機を用いて、レンズ状、アーモ
ンド状または乾パン状の直交3軸対称形状の粒体で、そ
の寸法は、−辺長10mmから1007Itπのものを
製造する。
As a method of solidifying such fine particle powder as it is taken out from the dust collector without any additives or pre-treatment, a pre-kerating machine, that is, a pre-kerating machine as the solidification molding processing device 8, is used to solidify the powder at the same speed. Pockets are cut into the surface of two rolls that rotate facing each other, and when the powder is fed between these rolls, it is compressed and granulated as the rolls rotate, and the granules are continuously discharged using a granulator. Then, granules having a lens-like, almond-like or hardtack-like shape that is symmetrical with three orthogonal axes and whose dimensions are from −10 mm to 1007 Itπ are manufactured.

この粒状固形物体が100闘以上になると極端にもろく
なるので100mm以下に成形するのがよくまた10闘
以下となると細かすぎて成形上問題があるし作業性が低
下するので避けた方がよい。
If this granular solid object exceeds 100 mm, it becomes extremely brittle, so it is best to mold it to a size of 100 mm or less, and if it is less than 10 mm, it is too fine, causing problems in molding and reducing workability, so it is better to avoid it.

なお前記固化成形処理装置8で用いられる圧搾のための
加圧成形圧力として、i、o o o〜5,000kg
/補程度の高圧力を用いるのがよくこの高圧力では粒子
間の固結が強く製造される粒状固形物体は、その表面は
ち密で光沢を持ち、粒体を2mの高さからコンクリート
床面に自然落下させても破壊しない程度に強度は犬とな
り、水没させても容易に崩壊しない固結度が生じる物体
とすることが容易にできる。
Note that the compression molding pressure for compression used in the solidification molding processing device 8 is i, o o o ~ 5,000 kg.
It is best to use a pressure as high as 2m to compensate for the granular solid objects that are manufactured at this high pressure, where the solidification between particles is strong. It is easy to create an object that has enough strength to not break even if it is dropped naturally, and has a degree of consolidation that does not easily collapse even if it is submerged in water.

図示例では、焼却炉1より発生する燃焼ガスを減温室と
なるガス冷却室2で加湿冷却された後、ダスト沈降分離
設備3に流入するが、このダスト沈降分離設備3で分離
されたダストは、クラッシャー4で混入している粗大塊
などを砕き、さらに篩分機5でレンガ片や鉄片を篩上に
分離して焼却残渣貯留ピット6へ落下させ、粉末ダスト
のみ定量フィーダー7を経て所定量をブリケラティング
マシンの固化成形処理装置8へ供給する。
In the illustrated example, the combustion gas generated from the incinerator 1 is humidified and cooled in the gas cooling chamber 2, which serves as an attenuation chamber, and then flows into the dust settling and separation equipment 3. The dust separated in the dust settling and separation equipment 3 is A crusher 4 crushes coarse lumps, etc., and a sieve 5 separates brick pieces and iron pieces onto a sieve and drops them into an incineration residue storage pit 6, and only the powder dust passes through a metering feeder 7 to a predetermined amount. It is supplied to the solidification molding processing device 8 of the briquetting machine.

該装置8で成形固化されたダスト粒は、ピット6へ焼却
灰を移送するコンベア9へ載せるか、あるいは直接ピッ
ト6へ投入する。
The dust particles formed and solidified by the device 8 are placed on a conveyor 9 that transports the incinerated ash to the pit 6, or are directly thrown into the pit 6.

クラッシャー4と篩分機5の順序を逆にして、篩上の粗
大物のみをクラッシャー4にて粉砕処理することもある
The order of the crusher 4 and the sieve machine 5 may be reversed so that only the coarse particles on the sieve are crushed by the crusher 4.

図中10は灰導出部、11は排風ファン、12は煙突、
13,14,15,16はベルトコンベアなどのコンベ
アで必要に応じ設けられる。
In the figure, 10 is an ash outlet, 11 is an exhaust fan, 12 is a chimney,
13, 14, 15, and 16 are conveyors such as a belt conveyor, and are provided as necessary.

17はピット内で走行されるクレーンである。17 is a crane that travels within the pit.

本発明は、廃棄物焼却処理の際に生ずるダストをダスト
分離設備において捕集し、該ダスト分離設備からダスト
を引抜き後焼却灰と併合輸送または貯留する前に、水や
薬剤などの他物質の添加をすることなく、粒状固形物体
に高圧力で圧搾成形させて、焼却残渣貯留ピットに排出
処理することにより、都市ごみなどの焼却処分時に発生
する多量のダストを作業上の取扱いが便利で運搬中や投
棄地で飛散しないで作業環境も悪化することなく処分で
き、しかも湿式コンベアや灰貯留所で冠水により泥ねい
となって事後処理を難しくする虞れもないし、薬剤など
の他の添加物質lζよって処理されるものでないので操
作条件も良好で経済的な処分が可能で、また処理困難な
ごみ関係の汚水の処理を少なくでき、しかも水に浸漬し
ても崩壊せず風に吹かれても飛び散らないので周囲の環
境保全のために極めて有益であり、公害問題をも惹起し
ないように処理利用でき、その操作も簡単で大量処理に
適し、極めて効率的で簡単かつ経済的に処理することが
できると共に、処理のための運転管理も簡便である利益
がある。
The present invention collects dust generated during waste incineration processing in a dust separation facility, extracts the dust from the dust separation facility, and then collects other substances such as water and chemicals before transporting or storing the dust together with the incinerated ash. By compressing granular solid objects under high pressure and discharging them into an incineration residue storage pit without adding additives, large amounts of dust generated during incineration of municipal waste can be easily handled and transported. It can be disposed of without being scattered inside or at the dumping site, and without deteriorating the working environment, and there is no risk of it becoming muddy due to flooding on a wet conveyor or ash storage site, making post-processing difficult, and other additives such as chemicals can be disposed of. Because it is not treated by lζ, it has good operating conditions and can be disposed of economically. It also reduces the need to dispose of difficult-to-dispose wastewater, and it does not disintegrate even when immersed in water and can be blown by the wind. Because it does not scatter, it is extremely useful for protecting the surrounding environment, and can be used for treatment without causing pollution problems.It is easy to operate, suitable for large-scale treatment, and can be treated extremely efficiently, easily, and economically. There is an advantage that the operation management for treatment is also simple.

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

図面は本発明の実施例を示す系統説明図である。 1・・・・・・焼却炉、2・・・・・・ガス冷却室、3
・・・・・・ダスト沈降分離設備、4・・・・・・クラ
ッシャー 5・・・・・・篩分機、6・・・・・・焼却
残渣貯留ピット、7・・・・・・定量フィーダー 8・
・・・・・固化成形処理装置、9・・・・・・コンベア
The drawing is a system explanatory diagram showing an embodiment of the present invention. 1... Incinerator, 2... Gas cooling room, 3
...Dust sedimentation separation equipment, 4 ... Crusher 5 ... Sieve machine, 6 ... Incineration residue storage pit, 7 ... Quantitative feeder 8・
...Solidification molding processing device, 9... Conveyor.

Claims (1)

【特許請求の範囲】 1 廃棄物焼却処理の際に生ずるダストをダスト分離設
備において捕集し、該ダスト分離設備からダストを引抜
き後焼却灰と併合輸送または貯留する前に、水や薬剤な
どの他物質の添加をすることなく、粒状固形物体に高圧
力で圧搾成形させて、焼却残渣貯留ピットに排出処理す
ることを特徴とする廃棄物焼却処理におけるダスト処理
方法。 2 前記ダストの圧搾成形でできる粒状固形物体が最大
辺長100mm以下の粒状固形物体に製造される特許請
求の範囲第1項記載の廃棄物焼却処理におけるダスト処
理方法。 3 前記粒状固形物体に圧搾成形されるダストが少くと
もクラッシャ、篩分機、定量フィーダの一つを通過させ
て処理される特許請求の範囲第1項又は第2項記載の廃
棄物焼却処理におけるダスト処理方法。 4 前記粒状固形物体に圧搾成形される際にダストが一
対の回転ロール間に供給され、ロール間で加圧されロー
ル表面のポケット内で1000〜50001y/iの加
圧力で圧縮され成形固化処理される特許請求の範囲第2
項又は第3項記載の廃棄物焼却処理におけるダスト処理
方法。 5 前記成形固化されたダスト粒が焼却灰を移送するコ
ンベアに載せて焼却残渣貯留ピット内に混合排出する特
許請求の範囲第4項記載の廃棄物焼却処理におけるダス
ト処理方法。
[Claims] 1. Dust generated during waste incineration processing is collected in a dust separation facility, and after the dust is extracted from the dust separation facility and before being combined with incinerated ash and transported or stored, water, chemicals, etc. A method for treating dust in waste incineration processing, which comprises compressing granular solid objects under high pressure and discharging them into an incineration residue storage pit without adding other substances. 2. The dust treatment method for waste incineration treatment according to claim 1, wherein the granular solid objects formed by compression molding of the dust are manufactured into granular solid objects having a maximum side length of 100 mm or less. 3. Dust in the waste incineration treatment according to claim 1 or 2, wherein the dust to be compressed into the granular solid object is processed by passing through at least one of a crusher, a sieve, and a quantitative feeder. Processing method. 4 When being compressed into the granular solid object, the dust is supplied between a pair of rotating rolls, pressurized between the rolls, compressed with a pressing force of 1000 to 50001 y/i in the pockets on the roll surface, and subjected to a molding and solidification treatment. Claim 2
Dust treatment method in waste incineration treatment according to item 1 or 3. 5. The dust treatment method in waste incineration treatment according to claim 4, wherein the shaped and solidified dust particles are placed on a conveyor for transporting incineration ash and mixed and discharged into an incineration residue storage pit.
JP52009518A 1977-01-31 1977-01-31 Dust treatment method in waste incineration treatment Expired JPS5854627B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP52009518A JPS5854627B2 (en) 1977-01-31 1977-01-31 Dust treatment method in waste incineration treatment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP52009518A JPS5854627B2 (en) 1977-01-31 1977-01-31 Dust treatment method in waste incineration treatment

Publications (2)

Publication Number Publication Date
JPS5395171A JPS5395171A (en) 1978-08-19
JPS5854627B2 true JPS5854627B2 (en) 1983-12-06

Family

ID=11722469

Family Applications (1)

Application Number Title Priority Date Filing Date
JP52009518A Expired JPS5854627B2 (en) 1977-01-31 1977-01-31 Dust treatment method in waste incineration treatment

Country Status (1)

Country Link
JP (1) JPS5854627B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63274955A (en) * 1987-05-06 1988-11-11 Fuji Photo Film Co Ltd Drying temperature control method for photographic film processing machine
JPH0233240Y2 (en) * 1984-07-02 1990-09-07

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0233240Y2 (en) * 1984-07-02 1990-09-07
JPS63274955A (en) * 1987-05-06 1988-11-11 Fuji Photo Film Co Ltd Drying temperature control method for photographic film processing machine

Also Published As

Publication number Publication date
JPS5395171A (en) 1978-08-19

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