JPS593235B2 - Dust treatment method in waste incineration treatment - Google Patents
Dust treatment method in waste incineration treatmentInfo
- Publication number
- JPS593235B2 JPS593235B2 JP52011112A JP1111277A JPS593235B2 JP S593235 B2 JPS593235 B2 JP S593235B2 JP 52011112 A JP52011112 A JP 52011112A JP 1111277 A JP1111277 A JP 1111277A JP S593235 B2 JPS593235 B2 JP S593235B2
- Authority
- JP
- Japan
- Prior art keywords
- dust
- waste incineration
- water
- treatment
- molded object
- 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
Links
- 239000000428 dust Substances 0.000 title claims description 62
- 238000000034 method Methods 0.000 title claims description 17
- 238000004056 waste incineration Methods 0.000 title claims description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 28
- 239000004568 cement Substances 0.000 claims description 16
- 238000000465 moulding Methods 0.000 claims description 8
- 238000000926 separation method Methods 0.000 claims description 6
- 239000000843 powder Substances 0.000 claims description 5
- 238000007711 solidification Methods 0.000 claims description 3
- 230000008023 solidification Effects 0.000 claims description 3
- 238000012545 processing Methods 0.000 claims description 2
- 229920006395 saturated elastomer Polymers 0.000 claims description 2
- 238000000748 compression moulding Methods 0.000 claims 1
- 238000007654 immersion Methods 0.000 claims 1
- 239000002344 surface layer Substances 0.000 claims 1
- 239000002245 particle Substances 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- 239000008187 granular material Substances 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000000567 combustion gas Substances 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000010828 elution Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 238000013019 agitation Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000003673 groundwater Substances 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000004449 solid propellant Substances 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 239000004071 soot Substances 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Landscapes
- Processing Of Solid Wastes (AREA)
- Glanulating (AREA)
Description
【発明の詳細な説明】
本発明は、都市ごみや汚泥又は主として固形燃料若しく
は廃棄物を燃焼処分する際に燃焼排ガス中に含まれる煤
塵を除去分離するために設置されるダスト分離設備から
排出されるダスト及び/又は小粒径の燃焼残渣を処理す
る方法に関するものである
一般に廃棄物焼却処理の際に発生するダストは集塵設備
で分離されるがこの集塵設備から取り出されるダストは
特別な処理をされることがなく、輸送中や投棄処分後に
風で飛散し環境を損ない作業に阻害を及ぼしていた。DETAILED DESCRIPTION OF THE INVENTION The present invention is directed to a dust separation system installed to remove and separate soot and dust contained in combustion exhaust gas when municipal waste, sludge, or mainly solid fuel or waste is incinerated. Generally speaking, the dust generated during waste incineration treatment is separated by dust collection equipment, but the dust extracted from this dust collection equipment is treated in a special manner. The waste was not treated, and was scattered by the wind during transportation or after being dumped, damaging the environment and hindering work.
従来では水を添加して練り混ぜ飛散防止手段を講じても
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し、一旦加湿しても投棄地におい
て天日で水分が蒸発してしまえばその効果はなくなり、
逆に降雨や地下水により泥ねいとなることもあるなど、
根本的対策とはならなかった。Conventionally, even if water is added to mix and prevent scattering, the amount of water reaches 50% of the dust weight, which not only reduces transportation efficiency but also makes post-treatment difficult and requires a large amount of cost. Even if humidification is done once, the effect will disappear once the moisture evaporates in the sun at the dumping site.
On the other hand, it may become muddy due to rainfall or groundwater.
It was not a fundamental countermeasure.
根本的なダスト処理としては、セメントと水で混練し、
成形、養生、固化する方法があり、効果としては完全な
ものに近いが、養生時間が10日間程度かかり成形製品
のストックに広い面積の建屋を要し、固化するまでの養
生中は強度がないため、取扱いも困難であり、実用に供
する上で、経済面、労力面などからも多くの障害がある
。For basic dust treatment, mix cement and water,
There is a method of forming, curing, and solidifying, and the effect is almost perfect, but the curing time takes about 10 days, and a large building is required to stock the molded products, and there is no strength during curing until solidification. Therefore, it is difficult to handle, and there are many obstacles in terms of economy and labor in putting it into practical use.
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や残渣の処分のた
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、灰貯留所内その他で冠水によ
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 seeks to eliminate these conventional drawbacks,
It is convenient to handle the dust and residue generated during waste incineration, does not scatter during transportation or at the dumping site, and prevents it from becoming muddy due to flooding on wet conveyors, in ash storage facilities, and elsewhere. The purpose is to provide a treatment method that can significantly increase the degree of reuse as well as non-polluting 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し投棄光の環境を適確に保
全できる処理方法とすることにある。In addition, the present invention provides a process that can process a large amount at once without performing the conventional uneconomical process, has favorable processing operating conditions, is economical, significantly improves workability, and can appropriately maintain the environment of the dumping light. It lies in the method.
本発明は、廃棄物焼却炉の煙道中に設けられる燃焼ガス
ダスト分離用集塵装置や廃熱ホイラから排出されるダス
トを成形固化する設備において、ダスト粉末とセメント
とを水を添加することなく混合し加圧成形固化した後に
、成形品の表面を水で湿潤させてセメント硬化用の水分
を補給することによって成形品表層面の硬化を計り、粉
じんの飛散や水中での崩壊、あるいはダスト含有成分の
溶出の抑制を適確にしたことを特徴とする有効な処理方
法である。The present invention mixes dust powder and cement without adding water in equipment that molds and solidifies dust discharged from a combustion gas dust separation dust collector installed in the flue of a waste incinerator or a waste heat foiler. After the molded product is solidified by pressure molding, the surface of the molded product is moistened with water to replenish moisture for cement hardening. This is an effective treatment method characterized by precisely suppressing the elution of.
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2で燃焼排ガ
ス中のダストを捕集し、この集塵装置2から排出される
ダストに、セメントを5〜15%重量比で混合する。An embodiment of the present invention will be described with reference to the drawings.
A dust separation device installed in the flue, for example, a gravity settling type, an inertial force settling type, or an electrostatic settling type dust collector 2 collects dust in the combustion exhaust gas, and the dust is discharged from the dust collector 2. Cement is mixed into the dust at a weight ratio of 5 to 15%.
この際、水は全く添加しない。At this time, no water is added.
このダストとセメントの混合物に、10kg/−以上5
0kg/−までの範囲の圧力を加え、601rLl以下
好ましくは60〜51nlのサイズに成形する。In this mixture of dust and cement, more than 10 kg/-5
A pressure in the range of up to 0 kg/- is applied and the product is molded to a size of 601 rLl or less, preferably 60 to 51 nl.
そして成形後、飽和状態もしくはそれに近い水蒸気の常
温の雰囲気下に30se以上10騙以下の時間曝露する
、あるいは、55ect上1騙以下の時間浸水させるが
散水し成形物表面を湿潤させる。After molding, the molded product is exposed to an atmosphere of water vapor at room temperature in a saturated state or close to it for a time of 30 seconds or more and 10 times or less, or immersed in water for a time of 1 time or less over 55 ects, but is sprinkled with water to moisten the surface of the molded product.
即ちダストを高圧力で加圧成形するとダスト棟内で発熱
し、表面温度が30℃から50℃に上昇するのでこの表
面に水分が耐着すると、熱により蒸発し潜熱量だけダス
ト塊表面温度が低下し、ダスト塊内部の微粒子間の間隙
にある空気が収縮し、塊表面に通じる毛細管に水を吸込
む。That is, when dust is compacted under high pressure, heat is generated within the dust ridge, and the surface temperature rises from 30℃ to 50℃.If moisture adheres to this surface, it will evaporate due to the heat, and the surface temperature of the dust mass will increase by the amount of latent heat. As the temperature decreases, the air in the interstices between particles inside the dust mass contracts, drawing water into the capillaries leading to the surface of the mass.
ダスト微粒子同志の圧着を損ねることなく、セメント粒
子と侵入した水とが接触して水利反応を生せせしめる。The cement particles come into contact with the invading water, causing a water utilization reaction, without damaging the pressure bond between the dust particles.
水利反応、強度発生期間中の運搬、貯蔵時の取扱い上要
求される強度は、前述のダスト微粒子圧着強度で十分で
あり、水中に投棄された場合の水のダスト塊の中心部ま
での浸透による崩壊を防止するところの表面硬化不透水
層を形成する時間は、運転、貯蔵期間中に得られる。The strength required for handling during water utilization, transportation during the strength generation period, and storage is sufficient with the dust particle compression strength described above, and is due to the penetration of water into the center of the dust mass when it is dumped into water. Time is provided during operation and storage to form a hardened, water-impermeable layer that prevents disintegration.
一方、焼却炉1から排出される燃焼ガスは、集塵装置2
を通過しダストが除去されて誘引排風機3により煙突4
から、大気へ放散される。On the other hand, the combustion gas discharged from the incinerator 1 is collected by the dust collector 2.
The dust is removed from the chimney 4 by the induced exhaust fan 3.
is emitted into the atmosphere.
また集塵装置2で分離除去されたダストは、ダストコン
ベア5で一ケ所に集められ、攪拌混合機6に投入する。Further, the dust separated and removed by the dust collector 2 is collected in one place by a dust conveyor 5 and is fed into an agitating mixer 6.
この攪拌混合機6にはダストに対し一定の比率でセメン
トを連続的に供給するための、定量フィーダ7や、セメ
ントコンベア8が附属している。This stirring mixer 6 is attached with a quantitative feeder 7 and a cement conveyor 8 for continuously supplying cement at a constant ratio to dust.
そして該攪拌混合機6内でダストとセメントを乾式混合
し、成形固化機9へ投入する。Then, the dust and cement are dry mixed in the stirring mixer 6 and then fed into the shaping and solidifying machine 9.
この成形固化機9としては例えばブ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60rIll以下に成形する。This forming and solidifying machine 9 is, for example, a briquetting machine, in which pockets are carved on the surface of two rolls that rotate inwardly at the same speed, and when powder is fed between these rolls, the rotation of the rolls Using a granulator that continuously discharges the granules after they are compressed and granulated, the granules are shaped into lenticular, almond-shaped or hardtack-shaped granules that are symmetrical about three orthogonal axes.
It is molded to a size of 60 rIll or less.
この粒状固形物体が601111以上になると極端にも
ろくなるので60威以下に成形するのがよく、また5m
l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 601111, it becomes extremely brittle, so it is best to form it to a size of 60 mm or less, and 5 m
If it is less than 1, it will be too fine, causing problems in molding and reducing workability, so it is better to avoid it.
かくして、成形固化されたダストは、成形固化ダストコ
ンベア10によって、加湿室11を通過する。The molded and solidified dust thus passes through the humidification chamber 11 by the molded and solidified dust conveyor 10.
該加湿室11内には、高圧ポンプ12で加圧された水が
、噴霧ノズル13で微粒化され、必要に応じ加温しつつ
成形固化ダストを湿潤する。In the humidifying chamber 11, water pressurized by a high-pressure pump 12 is atomized by a spray nozzle 13, and moistens the molded and solidified dust while being heated as necessary.
セメント硬化に必要な水分を与えられた成形品は、貯留
所13に移送され硬化作用が生じ運搬中および投棄光で
作用は続行して処理される。The molded product, which has been given the moisture necessary for cement hardening, is transferred to the reservoir 13, where a hardening action takes place, and the action continues during transportation and in the dumping light.
図中14は加熱器で必要に応じ設けられる。In the figure, reference numeral 14 denotes a heater, which is provided as necessary.
15゜16は駆動装置、17は攪拌器、18は駆動装置
、19は攪拌器である。15 and 16 are driving devices, 17 is a stirrer, 18 is a drive device, and 19 is a stirrer.
本発明は、ダスト分離設備からダストを引き抜きこのダ
スト粉末に水を添加することなくセメントを添加混合し
て加圧成形固化したのちに、固化成形物体の表面を水で
湿潤させてセメント硬化による成形物体表層面を硬化し
て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や残渣が容易に成形固化され、その
成形品表層面の硬化をはかり、粉塵の飛散や水中での崩
壊もなく、ダスト含有成分の溶出をも適確に防止でき、
投棄光の環境を保全するための処理方法として有用であ
り、しかも固化過程における水利反応、強度発生期間中
の運搬、貯蔵時の取扱い上要求される強度は、前述のダ
スト微粒子圧着強度で十分であり、水中に投棄された場
合の水のダスト塊の中心部までの浸透による崩壊を防止
する吉ころの表面硬化不透水層を形成する時間は、運転
、貯蔵期間中に得られるので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処分作業環境も悪化するこ
となく処理でき、しかも湿式コンベアや灰貯留所内で冠
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、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 extracts dust from dust separation equipment, adds and mixes cement to this dust powder without adding water, solidifies it by pressure molding, and then moistens the surface of the solidified molded object with water and molds it by cement hardening. By hardening and treating the surface of the object, a large amount of dust and residue generated during incineration of municipal waste can be easily molded and solidified, and the surface of the molded product is hardened to prevent dust from scattering and from being submerged in water. There is no disintegration, and the elution of dust-containing components can be accurately prevented.
It is useful as a treatment method for preserving the environment of dumped light, and the strength required for water use reactions during the solidification process, transportation during the strength generation period, and handling during storage is sufficient for the dust particulate compression strength described above. However, the time required to form an impermeable surface hardening layer that prevents collapse due to water penetrating into the center of the dust mass when it is dumped into water is obtained during operation and storage, so there is no need for operational considerations. It is convenient to handle, does not scatter during transportation or at the dumping site, and can be processed without deteriorating the disposal work environment.Furthermore, there is no risk of sludge due to flooding on wet conveyors or ash storage facilities, making post-processing difficult. The conditions are good and it can be disposed of economically, reducing the amount of waste water that is difficult to dispose of, and it does not disintegrate even when immersed in water and does not scatter even when blown by the wind, so it helps protect the surrounding environment. It is extremely useful for treatment, can be used in a manner that does not cause pollution problems, is easy to operate, is suitable for large-scale treatment, is extremely efficient, simple and economical, and can be operated and managed for treatment. It also has the advantage of being simple.
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・・・・・集塵装置、3・・
・・・・誘引排風機、4・・・・・・煙突、5・・・・
・・ダストコンベア、6・・・・・・攪拌混合機、7・
・・・・・定量フィーダー、8・・・・・・セメントコ
ンベア、9・・・・・・成形固化機、10・・・・・・
コンベア、11・・・・・・加湿室、12・・・・・・
高圧ポンプ、13・・・・・・噴霧ノズル。The drawing is a system explanatory diagram showing an embodiment of the present invention. 1... Incinerator, 2... Dust collector, 3...
...Induced draft fan, 4...Chimney, 5...
...Dust conveyor, 6...Agitation mixer, 7.
...Quantitative feeder, 8...Cement conveyor, 9...Molding and solidifying machine, 10...
Conveyor, 11... Humidification room, 12...
High pressure pump, 13... spray nozzle.
Claims (1)
備において捕集し、該ダスト分離設備からダストを引き
抜きこのダスト粉末に水を添加することなくセメントを
添加混合して加圧成形固化したのちに、固化成形物体の
表面を水で湿潤させてセメント硬化による成形物体表層
面を硬化して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 前記ダスト粉末に添加されるセメントが5〜15重
量%の範囲で混合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 前記固化成形物体が、10 kg /xi〜50k
g/niiの範囲の圧力で圧縮成形固化される特許請求
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 前記固化成形物体が、成形後飽和状態若しくはこれ
に近い水蒸気の常温の雰囲気下であって30secLl
上1〇−以下の時間曝露する特許請求の範囲第1項、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 前記固化成形物体が、成形後、常温下で5 SeC
以上1頭以下の時間浸水又は散水して成形物表面を湿潤
させる特許請求の範囲第1項、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。 6 前記固化成形物体が60TLl〜5解の大きさに成
形される特許請求の範囲第4項又は第5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 treatment is collected in a dust separation facility, the dust is extracted from the dust separation facility, and cement is added and mixed to this dust powder without adding water. 1. A method for treating dust in waste incineration processing, which is characterized in that after solidification by pressure molding, the surface of the solidified molded object is moistened with water to harden the surface layer of the molded object by cement hardening. 2. The dust treatment method in waste incineration treatment according to claim 1, wherein the cement added to the dust powder is mixed in a range of 5 to 15% by weight. 3 The solidified molded object weighs 10 kg/xi to 50 kg
The method for treating dust in waste incineration according to claim 1 or 2, wherein the dust is solidified by compression molding at a pressure in the range of g/nii. 4. The solidified molded object is placed in a saturated state after molding or in an atmosphere of water vapor at room temperature close to this state for 30 sec Ll.
A dust treatment method in waste incineration treatment according to claim 1, 2 or 3, wherein the dust treatment method is exposed for a period of time of 10 or less. 5. The solidified molded object is 5 SeC at room temperature after molding.
The method for treating dust in waste incineration according to claim 1, 2 or 3, wherein the surface of the molded product is moistened by immersion in water or water sprinkling for at least one head. 6. The dust treatment method in waste incineration treatment according to claim 4 or 5, wherein the solidified molded object is molded to a size of 60TL1 to 5mm.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP52011112A JPS593235B2 (en) | 1977-02-03 | 1977-02-03 | Dust treatment method in waste incineration treatment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP52011112A JPS593235B2 (en) | 1977-02-03 | 1977-02-03 | Dust treatment method in waste incineration treatment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5395876A JPS5395876A (en) | 1978-08-22 |
JPS593235B2 true JPS593235B2 (en) | 1984-01-23 |
Family
ID=11768918
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP52011112A Expired JPS593235B2 (en) | 1977-02-03 | 1977-02-03 | Dust treatment method in waste incineration treatment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS593235B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111014241A (en) * | 2019-12-13 | 2020-04-17 | 湖州三新汽车环保科技有限公司 | Industry collection system that gives up admittedly |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5895285U (en) * | 1981-12-18 | 1983-06-28 | 大平洋機工株式会社 | Solidification treatment equipment for powdered waste |
JP5020665B2 (en) * | 2007-03-13 | 2012-09-05 | 鹿島建設株式会社 | Spraying method |
-
1977
- 1977-02-03 JP JP52011112A patent/JPS593235B2/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111014241A (en) * | 2019-12-13 | 2020-04-17 | 湖州三新汽车环保科技有限公司 | Industry collection system that gives up admittedly |
Also Published As
Publication number | Publication date |
---|---|
JPS5395876A (en) | 1978-08-22 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4886393A (en) | Pretreatment of solid wastes, and wastes to be compacted, for introduction into underground salt cavities of salt caverns via a downpipe under the force of gravity | |
JP5008507B2 (en) | Dust collector having powder mixing processing means and powder mixing processing method | |
JPH05295347A (en) | Process, system and composition for rendering waste substance harmless | |
JPS593235B2 (en) | Dust treatment method in waste incineration treatment | |
US6887389B2 (en) | Method and apparatus for recycling sewage sludge utilizing spent water-softener lime | |
TW422731B (en) | Exhaust processing agent, its preparation and exhaust processing method | |
JP4789410B2 (en) | Waste stabilization treatment solidified material and processing equipment | |
EP0405124A2 (en) | Method for thermal disposal or waste material or residual material such as ashes, sludge or the like | |
JP3840371B2 (en) | Steelmaking slag and sand-washed sludge treatment method | |
JPH05277465A (en) | Completely closed-type treating method of oozing out water or treatment wastewater in control-type and stable-type terminal treatment site of general and industrial waste | |
JP2809366B2 (en) | Method for collecting harmful metals in exhaust gas and method for treating collected ash | |
JPH1029841A (en) | Production of artificial aggregate | |
CN209991467U (en) | Waste incineration fly ash solidification device | |
JPH0693260A (en) | Soil additive | |
JPS6251157B2 (en) | ||
JP3019297B2 (en) | Treatment method of sulfuric acid pitch | |
JP2005313032A (en) | Manufacturing method for hydrothermally solidified material of paper sludge incineration ash | |
JP4224373B2 (en) | Method of molding and incineration of aggregate solidified body | |
JPS5874794A (en) | Safe transportation of acidic sludge obtained from petroleum fraction and conversion thereof to solid fuel | |
JPS595359B2 (en) | Molding solidification method for municipal waste incineration residue | |
JPH06254528A (en) | Method and device for treating dust | |
JPS6212475Y2 (en) | ||
JPS5854627B2 (en) | Dust treatment method in waste incineration treatment | |
JPH0230752B2 (en) | ||
JPS5520345A (en) | Exhaust gas disposing device for incinerating furnace and the like |