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JPS5827221B2 - garbage collection - Google Patents
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JPS5827221B2 - garbage collection - Google Patents

garbage collection

Info

Publication number
JPS5827221B2
JPS5827221B2 JP49118355A JP11835574A JPS5827221B2 JP S5827221 B2 JPS5827221 B2 JP S5827221B2 JP 49118355 A JP49118355 A JP 49118355A JP 11835574 A JP11835574 A JP 11835574A JP S5827221 B2 JPS5827221 B2 JP S5827221B2
Authority
JP
Japan
Prior art keywords
particle size
mixed
ash
cement
crushed
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
JP49118355A
Other languages
Japanese (ja)
Other versions
JPS5159770A (en
Inventor
義之 羽生
頴明 横見
隆 渡辺
洸一 渡辺
仁太郎 鈴木
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.)
Kawasaki Heavy Industries Ltd
Original Assignee
Kawasaki Heavy Industries 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 Kawasaki Heavy Industries Ltd filed Critical Kawasaki Heavy Industries Ltd
Priority to JP49118355A priority Critical patent/JPS5827221B2/en
Publication of JPS5159770A publication Critical patent/JPS5159770A/en
Publication of JPS5827221B2 publication Critical patent/JPS5827221B2/en
Expired 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P40/00Technologies relating to the processing of minerals
    • Y02P40/10Production of cement, e.g. improving or optimising the production methods; Cement grinding
    • 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
    • Y02W30/91Use of waste materials as fillers for mortars or concrete

Landscapes

  • Processing Of Solid Wastes (AREA)

Description

【発明の詳細な説明】 本発明は、ごみ焼却灰の有効利用法に関するものである
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for effectively utilizing waste incineration ash.

ごみ焼却炉からの焼却灰を処理するにあたり、従来の方
法によれば、焼却灰をごみ焼却炉に付設した水槽に落下
させたるのらコンベアにより排出し、埋立て処理などを
行っていた。
According to the conventional method of processing incinerated ash from a garbage incinerator, the incinerated ash is dropped into a water tank attached to the garbage incinerator, then discharged by a conveyor, and then disposed of in a landfill.

この方法では、用水の汚染をもたらし有害であるために
、排水処理を必要とするのみならず、焼却灰自体も有害
物質を含み、これらの輸送、取扱いが困難である欠点を
有していた。
This method not only requires wastewater treatment because it contaminates the water and is harmful, but the incineration ash itself also contains harmful substances, making it difficult to transport and handle them.

又、焼却灰は未燃分とくに紙、プラスチックス、皮革、
繊維、鉄屑、非鉄金属、土砂、陶磁器、ガラス屑、ダス
トなどの多種多様なものを含んでおり、例等の手段を加
えることなく、無公害の状態にして埋立て処理をするこ
とは困難であった。
In addition, incineration ash is unburned, especially paper, plastics, leather,
It contains a wide variety of materials such as fibers, iron scraps, nonferrous metals, earth and sand, ceramics, glass scraps, and dust, and it is difficult to dispose of it in a landfill in a pollution-free state without adding other measures. Met.

本発明においては、ごみ焼却炉からの焼却灰の取り出し
は、水を使用することなく乾式にて取出しを行い、一次
破砕を行ったのらに磁選により鉄屑を分離し、篩分けに
より未燃分を分離して不用な成分を除去し、又、中間粒
度材料と製品粒度材料とに分離したのら、中間粒度材料
を二次破砕により微細な粒度を有する有用な材料に変換
せしめ、これと製品粒度材料とを混合し、これに砂、セ
メント、ポリビニールアルコールおよび水を配合して均
一に混練したるのら、所定の形状および寸法からなる型
に供給してプレスにより圧縮成型加工させるものである
In the present invention, incineration ash is removed from a garbage incinerator using a dry method without using water, and after primary crushing, iron scrap is separated by magnetic separation, and unburned by sieving. After separating the components and removing unnecessary components, and separating the intermediate particle size material and the product particle size material, the intermediate particle size material is converted into a useful material with a fine particle size by secondary crushing, and this Product particle size Materials are mixed with sand, cement, polyvinyl alcohol, and water, mixed uniformly, and then fed into a mold with a predetermined shape and size and compressed by a press. It is.

従来からも、ごみ焼却灰を細分してセメントなどの安定
剤を配合し圧縮成型するなどの処理方法は公知であるが
、本発明は、これらの処理方法の改善をはかり、材料中
の有害物質の溶出を防止し、さらに高強度の品位を有す
る製品を得んとするものである。
Conventionally, processing methods have been known in which waste incineration ash is finely divided, mixed with a stabilizer such as cement, and compression molded, etc., but the present invention aims to improve these processing methods and eliminate harmful substances in the material. The aim is to prevent the elution of the metal and to obtain a product that has high strength and quality.

焼却灰を微細な粒度を有する材料に変換することは、材
料の輸送、貯蔵、供給などの取扱いを容易ならしめ、砂
、セメント、ポリビニールアルコールおよび水との混合
を均一ならしめ、これらの混合物の充填状態を緻密なら
しめるものである。
Converting incineration ash into a material with a fine particle size makes the material easier to transport, store, feed, etc., and allows for uniform mixing with sand, cement, polyvinyl alcohol, and water, making these mixtures easier to handle. This is to make the filling state denser.

さらに焼却炉の集じん装置などから捕集した煙灰なとも
配合すれば、混合物の充填状態ならびに混合、混線状態
はさらに改善され、焼却灰は上記の材料と均一に分散さ
れているので、圧縮成型ならびに固化した成型品は、材
料中の有害物質の溶出を防止し得るのみならず高強度の
成型品の製造を可能ならしめるものである。
Furthermore, if it is mixed with smoke ash collected from the dust collector of the incinerator, the filling condition of the mixture, mixing, and crosstalk will be further improved, and since the incineration ash is evenly dispersed with the above materials, it can be compressed and molded. In addition, the solidified molded product not only prevents the elution of harmful substances from the material, but also makes it possible to manufacture a high-strength molded product.

本発明による、焼却灰から変換した微細な粒度を有する
材料からの有害物質の溶出防止を目標としたセメント混
合物に要求される性質としては、1)圧縮成型は乾式、
半乾式成型として施工し得ること。
The properties required for the cement mixture according to the present invention, which aims to prevent the elution of harmful substances from the material with fine particle size converted from incineration ash, are as follows: 1) Compression molding is dry type;
Can be constructed as semi-dry molding.

2)混合物は緻密に充填されており、小量の水分によっ
て水利、凝固を生ずるものであること。
2) The mixture must be densely packed and cause water retention and coagulation with a small amount of water.

3)混合物は高分子結合材の添加により、被着材との結
合を増大し得ること。
3) The mixture can be increased in bonding to adherends by the addition of polymeric binders.

4)混合物は圧縮成型により、充分な結合力が得られ、
高い破壊強度を示すこと。
4) The mixture is compression molded to obtain sufficient bonding strength,
Show high breaking strength.

5)材料は混合物に均一に分散されており、圧縮成型固
化後において有害物質の溶出を防止し得ること。
5) The material is uniformly dispersed in the mixture to prevent harmful substances from leaching out after compression molding and solidification.

などが挙げられる。Examples include.

本発明者らが得た知見によれば、普通セメントの使用O
こより希望するセメント混合物を得ることができた。
According to the knowledge obtained by the present inventors, the use of ordinary cement O
From this, the desired cement mixture could be obtained.

以下、本発明の実施例を図面とともに説明する。Embodiments of the present invention will be described below with reference to the drawings.

ごみ焼却炉1からの焼却灰は乾式排出装置2により取出
し、一次破砕機3にて破砕したのら、磁気分離器4によ
り鉄屑6を除去し、鉄屑槽7から製鋼原料などに利用さ
れる。
Incineration ash from the garbage incinerator 1 is taken out by a dry discharge device 2, crushed by a primary crusher 3, iron scraps 6 are removed by a magnetic separator 4, and the iron scraps 6 are removed from the iron scrap tank 7 and used as raw materials for steelmaking. Ru.

篩分は機8においては、未燃分14、中間粒度材料10
および製品粒度材料9に分離し、未燃分14はごみ焼却
炉1に返送され、ごみ15とともに焼却を行う。
In machine 8, the sieve fraction is 14 unburned fractions and 10 medium particle size materials.
and product particle size materials 9, and the unburned matter 14 is returned to the waste incinerator 1 and incinerated together with the waste 15.

中間粒度材料10は、さらに第二次破砕機11により破
砕し、これらの破砕品12と製品粒度材料9とを混合し
、中間貯槽13に導く。
The intermediate particle size material 10 is further crushed by a secondary crusher 11, and the crushed products 12 and the product particle size material 9 are mixed and introduced into an intermediate storage tank 13.

かくして得られた粒径はぼ2mmJJ、下の材料19は
、混合機14に供給し、このさい砂15、セメント16
、水17、ポリビニールアルコール18を配合し、一定
時間にわたり撹拌混合をなし、均一な混合物が得られる
The particle size obtained in this way is approximately 2 mm JJ, and the lower material 19 is supplied to the mixer 14, where it is mixed with sand 15 and cement 16.
, water 17, and polyvinyl alcohol 18 are blended and stirred and mixed for a certain period of time to obtain a homogeneous mixture.

さらに混合物20は、成型プレス21の金型に供給して
所定の形状を有する成型品22が得られ、引続き養生工
程23を経て製品24が得られる。
Further, the mixture 20 is supplied to a mold of a molding press 21 to obtain a molded product 22 having a predetermined shape, and subsequently undergoes a curing step 23 to obtain a product 24.

焼却灰から、製品を得る。Obtain products from incineration ash.

までの操作は、次の通りであった。The operations up to this point were as follows.

一次破砕: 破砕機ローフ周速 全土スクリーン開口 破砕品粒径 −25朋 51n范 45m/5 75X100u+ 85% 59% 磁 選: 磁力 鉄屑見かけ密度 篩分け: 供給量 未燃分(+10mm) 中間粒度材料(10mrtr−2mm) 製品粒度材料(−2關) 二次破砕: 破砕機ローフ周速 全土スクリーン開口 破砕品粒径−2mm −0,59mm 材料性状: 強熱減量 灰分 粒径−2mrrt −0,59mm 見かけ密度 成型機ニ ア 50 GaUSS 1、Og/cc 80kg 30.1に9 48.6kg 110.3kg 60 m/ S X15mm 95% 52% 7.7% 92.3% 98.8% 50.8% 0、85 ji /cc 焼却灰の粒径の影響は、/161,2に見られ、はぼ2
關以下とすることにより高強度の成型品が得られている
Primary crushing: Crusher loaf circumferential speed Whole screen opening Crushed product particle size -25 to 51n 45m/5 75X100u+ 85% 59% Magnetic selection: Magnetic iron scrap apparent density Sieving: Supply amount unburned matter (+10mm) Intermediate particle size material (10mrtr-2mm) Product particle size Material (-2mm) Secondary crushing: Crusher loaf circumferential speed Whole screen opening Crushed product particle size -2mm -0,59mm Material properties: Ignition loss ash particle size -2mrrt -0,59mm Apparent Density Forming Machine Near 50 GaUSS 1, Og/cc 80kg 30.1 to 9 48.6kg 110.3kg 60 m/S X15mm 95% 52% 7.7% 92.3% 98.8% 50.8% 0 , 85 ji /cc The effect of the particle size of incinerated ash is seen in /161,2, and
A high-strength molded product can be obtained by setting the thickness to less than 100 mm.

砂の配合の影響は、/V;3.4に見られ、砂の配合が
有効であることを示している。
The influence of the sand mixture is seen in /V; 3.4, indicating that the sand mixture is effective.

さらに別の実施例では、焼却炉の集じん装置などから捕
集した煙灰を配合することにより、83.2kg/−の
強度を有する成型品が得られている。
In yet another example, a molded product having a strength of 83.2 kg/- was obtained by blending smoke ash collected from an incinerator's dust collector.

セメントの配合比率の影響は、/16.5,6に見られ
ており、配合比率が低い場合では高強度の成型品は得ら
れていない。
The influence of the blending ratio of cement was seen at /16.5 and /16.6, and when the blending ratio was low, a molded product with high strength was not obtained.

又、ポリビニールアルコールをはじめポリビニールアセ
テートなどからなる接着剤を添加すれば、さらに高強度
の成型品が得られることは/%7,8゜9に示されてい
る。
Further, it is shown in /%7.8°9 that a molded product with even higher strength can be obtained by adding an adhesive made of polyvinyl alcohol or polyvinyl acetate.

微細な材料は、Pb2900p西、Cd12pへCr6
50ppmなど重金属を含有しているが、/I66の例
では成型品を粉砕した試料による有害物質溶出試験結果
によれば、上記は倒れも不検出であった。
The fine material is Pb2900p west, Cr6 to Cd12p
Although it contains heavy metals such as 50 ppm, in the case of /I66, according to the results of a hazardous substance elution test using a sample obtained by crushing a molded product, no collapse was detected in the above case.

本発明によれば、公知の方法に比して微細な材料に変換
したのら、上述の如き配合により高強度の品位を有する
製品が得られるのみならず、材料中の有害物質の溶出を
防止することができ、さらに用水を必要としない乾式処
理法による焼却灰の取出しにより、水質の汚濁を回避し
得る効果を有している。
According to the present invention, by converting the material into a finer material than in the known method, not only can a product with high strength and quality be obtained by the above-mentioned formulation, but also the elution of harmful substances in the material can be prevented. Furthermore, by removing the incinerated ash using a dry treatment method that does not require water, it has the effect of avoiding water pollution.

又、本発明によれば、セメント混合物を得るために配合
すべき材料は汎用されているものであるので、経済的に
成型品を得ることが可能である。
Further, according to the present invention, since the materials to be mixed to obtain the cement mixture are commonly used materials, it is possible to economically obtain a molded product.

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

第1図は本発明の一実施例を示す工程図である。 FIG. 1 is a process diagram showing an embodiment of the present invention.

Claims (1)

【特許請求の範囲】 1 ごみ焼却炉からの焼却灰を乾式にて取出し破砕、磁
選および篩分けによる中間粒度材料を、さらに二次破砕
して粒径をほぼ21nrft以下からなる材料となし、
これと前記篩分けによる製品粒度材料とを混合し、これ
に重量比において砂11.5〜17.5%、セメント1
5.5〜22.5%および水5.0〜12.5%を残部
を焼却灰にして配合・混練し、型に供給して圧縮成型す
ることを特徴とするごみ焼却灰の成型加工法。 2 ごみ焼却炉からの焼却灰を乾式にて取出し破砕、磁
選および篩分けによる中間粒度材料を、さらに二次破砕
して粒径をほぼ2鼎以下からなる材料となし、これと前
記篩分けによる製品粒度材料とを混合し、これに重量比
において砂11.5〜17.5%、セメント15.5〜
22.5%、ポリビニールアルコール若しくはポリビニ
ールアセテート0.8〜2.0%および水5.0〜12
.5%を残部を焼却灰にして配合・混練し、型に供給し
て圧縮成型することを特徴とするごみ焼却灰の成型加工
法。
[Scope of Claims] 1. Incinerated ash from a garbage incinerator is dry-removed, crushed, magnetically separated, and sieved to produce intermediate particle size material, which is further crushed secondary to a material with a particle size of approximately 21 nrft or less,
This is mixed with the product particle size material obtained by the sieving, and this is mixed with 11.5 to 17.5% sand and 1% cement by weight.
5.5 to 22.5% and water 5.0 to 12.5% with the remainder being incinerated ash, blended and kneaded, and then supplied to a mold for compression molding. . 2. The incinerated ash from the garbage incinerator is dry-removed, crushed, magnetically separated, and sieved to produce intermediate particle size material, which is further crushed secondary to a material with a particle size of approximately 2 mm or less, and this and the sieved material obtained by the above-mentioned sieving. The product particle size is mixed with the material, and the weight ratio of sand is 11.5 to 17.5%, and cement is 15.5 to 15%.
22.5%, polyvinyl alcohol or polyvinyl acetate 0.8-2.0% and water 5.0-12%
.. A method for molding waste incineration ash, which is characterized by mixing and kneading 5% with the remainder being incineration ash, feeding it into a mold, and compressing it.
JP49118355A 1974-10-15 1974-10-15 garbage collection Expired JPS5827221B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP49118355A JPS5827221B2 (en) 1974-10-15 1974-10-15 garbage collection

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP49118355A JPS5827221B2 (en) 1974-10-15 1974-10-15 garbage collection

Publications (2)

Publication Number Publication Date
JPS5159770A JPS5159770A (en) 1976-05-25
JPS5827221B2 true JPS5827221B2 (en) 1983-06-08

Family

ID=14734639

Family Applications (1)

Application Number Title Priority Date Filing Date
JP49118355A Expired JPS5827221B2 (en) 1974-10-15 1974-10-15 garbage collection

Country Status (1)

Country Link
JP (1) JPS5827221B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5339666A (en) * 1976-09-22 1978-04-11 Takuma Co Ltd Treatment of ashes produced by incineration of refuse
JPS5419471A (en) * 1977-07-13 1979-02-14 Hitachi Zosen Corp Method of treating cinders of municipal refuse
JPH02144185A (en) * 1988-11-21 1990-06-01 Kounenshiyou Kk Utilizing treatment of waste material and treatment plant thereof
JP2646312B2 (en) * 1992-05-29 1997-08-27 三井建設株式会社 Treatment method of municipal waste incineration ash

Also Published As

Publication number Publication date
JPS5159770A (en) 1976-05-25

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