JPS6048234B2 - Solidification treatment method for municipal waste dust - Google Patents
Solidification treatment method for municipal waste dustInfo
- Publication number
- JPS6048234B2 JPS6048234B2 JP56150521A JP15052181A JPS6048234B2 JP S6048234 B2 JPS6048234 B2 JP S6048234B2 JP 56150521 A JP56150521 A JP 56150521A JP 15052181 A JP15052181 A JP 15052181A JP S6048234 B2 JPS6048234 B2 JP S6048234B2
- Authority
- JP
- Japan
- Prior art keywords
- municipal waste
- dust
- waste dust
- treatment method
- solidification treatment
- 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 23
- 238000000034 method Methods 0.000 title claims description 18
- 239000002699 waste material Substances 0.000 title claims description 15
- 238000007711 solidification Methods 0.000 title claims description 8
- 230000008023 solidification Effects 0.000 title claims description 8
- 239000011396 hydraulic cement Substances 0.000 claims description 9
- 150000003839 salts Chemical class 0.000 claims description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- 238000005096 rolling process Methods 0.000 claims description 4
- 239000011148 porous material Substances 0.000 claims description 3
- 239000004568 cement Substances 0.000 description 10
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 6
- 238000000465 moulding Methods 0.000 description 6
- 239000000047 product Substances 0.000 description 5
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 4
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 4
- 238000005469 granulation Methods 0.000 description 4
- 230000003179 granulation Effects 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 229910052782 aluminium Inorganic materials 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 238000005266 casting Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229910001385 heavy metal Inorganic materials 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- -1 Friedel salt Chemical class 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 239000011400 blast furnace cement Substances 0.000 description 1
- 229910052793 cadmium Inorganic materials 0.000 description 1
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 1
- 238000005056 compaction Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 229910052593 corundum Inorganic materials 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000010828 elution Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000010881 fly ash Substances 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000004056 waste incineration Methods 0.000 description 1
- 229910001845 yogo sapphire Inorganic materials 0.000 description 1
Landscapes
- Processing Of Solid Wastes (AREA)
Description
【発明の詳細な説明】
本発明は固結後にガス発生を伴い膨脹するため破壊し
易い性質を有する都市こみダストを安定に固形化処理す
る方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for stably solidifying municipal waste, which tends to be easily destroyed because it expands with gas generation after solidification.
都市こみを焼却処理する工程では、粗大な焼却残滓の
他に、排ガスに伴なわれて移送され、焼却炉以後の工程
として設けられたサイクロン、または電気収塵機等の収
塵系て捕集回収される粉末状の回収ダストがある。In the process of incinerating municipal waste, in addition to coarse incineration residue, it is transported along with exhaust gas and collected in a dust collection system such as a cyclone or an electric dust collector, which is installed as a process after the incinerator. There is recovered dust in powder form.
都市こみの焼却方式には種々のものがあるが、主要な類
型としては、火格子を用いる機械炉、焼却媒体として珪
砂を用いる流動床炉との2種類がある。機械炉ダストは
一般に微細であり、流動床炉ダストは排ガスに伴なわ。
れる熱媒体の砂が混入するため一般に粗大である。しか
し両者に共通する特徴は、都市こみ由来の金属アルミニ
ウム粉末、可溶性塩類を含有する点である。 本発明の
対象とする処理物てある都市ごみダス2卜は都市こみの
焼却工程における収塵系て回収された粉末ダストである
。There are various methods of incinerating municipal waste, but there are two main types: mechanical furnaces that use a grate and fluidized bed furnaces that use silica sand as the incineration medium. Mechanical furnace dust is generally fine, and fluidized bed furnace dust is associated with exhaust gas.
Generally, it is coarse because it is mixed with sand, which is a heat transfer medium. However, the common feature of both is that they contain metal aluminum powder and soluble salts derived from municipal waste. Two volumes of municipal waste, which is the object of the present invention, is powder dust collected in the dust collection system during the municipal waste incineration process.
この都市ごみダストには カドミウム、鉛、その他の重
金属が含有されており、上記ダストを廃棄する場合など
にはこれら重金属の溶出、拡散を防止するための固形化
処理が必要である。従前このような固形化処理としては
、ダストに水硬性セメントおよび水を添加して混合し、
固形化する方法が一般的である。そしてその成形方法と
しては加圧してノズルから押し出す押し出し成形法、一
定寸法の型枠に加圧して成形する加圧成形法、割型を設
けたダブルロールを)回転させて連続加圧成形するフリ
ケツト方式、更には添加水量を増加して流動性とし、一
定寸法の型枠に流し込む流し込み成形法等がある。とこ
ろが上記都市ごみダストには金属アルミニウム、塩化石
灰、塩化ナトリウム等可溶性塩類が含まれており、水硬
性セメントと水とを添加する場合には、金属アルミニウ
ムはアルカリ性の領域で加水分解によつて水素ガスを発
生し、可溶性塩類は、水硬性セメントの化学成分と反応
して、複塩、たとえばフリーデルソルト、−3CaO)
Al2O3、CaCl)210H。O)クロルーエトリ
ンガイド3CaO、、Al2o3cacl。18H。O
などを生成する。これら複塩は膨脹性の化合物であり、
金属アルミニウムによる水素ガスの発生とともに、成形
物を膨脹させ処理物の構造を、短期、長期にわたつて脆
化する性質を有する。このため従前の各種成形方法によ
れば、成形物は一般に緻密な構造体であることから例え
ば流し込み成形法では、水素ガスの発泡により成形物が
著しく膨潤して強度を失ない、又加圧成形物では、緻密
な皮殻組織が形成されるため、内部から発生する水素ガ
スの圧力、および緻密な皮殻部に生成析出する複塩結晶
により破壊、崩壊する傾向があり、この傾向は強固、緻
密な成形物ほど著しいという問題がある。本発明は上記
都市ごみダストを安定に固形化処理する方法を提供する
ものであつて、その要旨は、都市ごみグストに対し、水
硬性セメント5〜40重量部と、水分10〜2喧量部を
混合して該ダストを転動造粒し、開放気孔を有する成球
にすることを特徴とする。以下に本発明を詳細に説明す
る。This municipal waste dust contains cadmium, lead, and other heavy metals, and when disposing of the dust, it is necessary to solidify it to prevent the elution and diffusion of these heavy metals. Previously, this type of solidification treatment involved adding and mixing hydraulic cement and water to dust.
A common method is solidification. The molding methods include extrusion molding in which the mold is pressed out through a nozzle under pressure, pressure molding in which the mold is molded under pressure in a mold of a fixed size, and friquet molding in which double rolls with split molds are rotated to form the mold continuously under pressure. There is also a casting method in which the amount of added water is increased to make it fluid and the mixture is poured into a mold of a certain size. However, the above-mentioned municipal waste dust contains soluble salts such as metal aluminum, lime chloride, and sodium chloride, and when hydraulic cement and water are added, metal aluminum becomes hydrogen by hydrolysis in an alkaline region. The soluble salts react with the chemical components of the hydraulic cement to form double salts, e.g. Friedel salt, -3CaO).
Al2O3, CaCl)210H. O) Chloruethrine guide 3CaO,, Al2o3cacl. 18H. O
etc. These double salts are expansive compounds;
As hydrogen gas is generated by metal aluminum, the molded product expands and the structure of the processed product becomes brittle over a short and long term. For this reason, according to various conventional molding methods, the molded product is generally a dense structure, so in the case of casting molding, for example, the molded product does not swell significantly due to hydrogen gas foaming and lose its strength, and pressure molding Since a dense shell structure is formed in materials, it tends to break and collapse due to the pressure of hydrogen gas generated from inside and the double salt crystals that form and precipitate in the dense shell.This tendency is strong. The problem becomes more pronounced in denser molded products. The present invention provides a method for stably solidifying the above-mentioned municipal waste dust. It is characterized in that the dust is mixed and granulated by rolling to form spheres having open pores. The present invention will be explained in detail below.
本発明の固形化処理方法において上記都市ごみダストに
混入するセメントとして水硬性セメントを用いる。In the solidification treatment method of the present invention, hydraulic cement is used as the cement mixed in the municipal waste dust.
該水硬性セメントは普通ボルトランドセメント、超早強
ボルトランドセメント、早強ボルトランドセメント、中
庸熱ボルトランドセメント等のボルトランドセメント、
高炉セメント、シリカセメント、フライアッシュセメン
ト等の混合セメント、超速硬セメントを用いることがで
きる。該水硬性セメントのダストに対する混合割合は成
球の期待強度によつて異なるが一般に都市ごみダスト1
00重量部に対し5重量部から4喧量部の範囲であり、
普通20〜3鍾量部であれはよい。又添加水量は造粒に
適する水量であつて都市ごみダストおよび上記水硬性セ
メントの粉末度、ダストの漏れ性によつても異なるが通
常10〜2腫量部であればよい。次に転動造粒方法とし
ては自転円筒型造粒方式、皿型転動造粒方式等が用いら
れる。本発明の固形化処理方法によれば都市ごみダスト
を水硬性セメントの固結作用により連結しながら均一に
皮殻を積み重ねるように造粒し、球の全面に均等な圧密
効果を与えて成球することができ、この過程で成球内部
に開放気孔に富む構造が形成される。The hydraulic cement includes bolt land cement such as ordinary bolt land cement, ultra-early strength bolt land cement, early strength bolt land cement, moderate heat bolt land cement, etc.
Mixed cements such as blast furnace cement, silica cement, and fly ash cement, and ultra-fast hardening cements can be used. The mixing ratio of the hydraulic cement to the dust varies depending on the expected strength of the mature ball, but generally municipal waste dust 1
The range is from 5 parts by weight to 4 parts by weight per 00 parts by weight,
Normally, 20 to 3 parts is fine. The amount of water to be added is a water amount suitable for granulation, which varies depending on the fineness of the municipal waste dust and the above-mentioned hydraulic cement, and the leakability of the dust, but is usually 10 to 2 parts by volume. Next, as the rolling granulation method, a rotating cylinder type granulation method, a dish type rolling granulation method, etc. are used. According to the solidification treatment method of the present invention, municipal waste dust is granulated so that the shells are evenly piled up while being connected by the solidification effect of hydraulic cement, and a uniform compaction effect is given to the entire surface of the sphere to form a sphere. During this process, a structure rich in open pores is formed inside the grown bulb.
Claims (1)
スト100重量部に対し、水硬性セメント5〜40重量
部と水分10〜20重量部とを混合して該ダストを転動
造粒し、開放気孔を有する成球にすることを特徴とする
都市ごみダストの固形化処理方法。1. For 100 parts by weight of municipal waste dust that expands due to gas generation and double salt after solidification, 5 to 40 parts by weight of hydraulic cement and 10 to 20 parts by weight of water are mixed and the dust is granulated by rolling. , a method for solidifying municipal waste dust, characterized by forming it into mature balls having open pores.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56150521A JPS6048234B2 (en) | 1981-09-25 | 1981-09-25 | Solidification treatment method for municipal waste dust |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56150521A JPS6048234B2 (en) | 1981-09-25 | 1981-09-25 | Solidification treatment method for municipal waste dust |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5851970A JPS5851970A (en) | 1983-03-26 |
JPS6048234B2 true JPS6048234B2 (en) | 1985-10-25 |
Family
ID=15498675
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP56150521A Expired JPS6048234B2 (en) | 1981-09-25 | 1981-09-25 | Solidification treatment method for municipal waste dust |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6048234B2 (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2657793B2 (en) * | 1995-10-04 | 1997-09-24 | 住金鹿島鉱化株式会社 | How to treat incinerated fly ash or molten fly ash |
JP3780402B2 (en) * | 2000-03-23 | 2006-05-31 | 日立造船株式会社 | Detoxification method for incineration fly ash |
JP2013123691A (en) * | 2011-12-15 | 2013-06-24 | Daikyogumi:Kk | Hydrothermally solidified foam made mainly of incineration ash, and method for producing the same |
JP5843329B2 (en) * | 2014-04-23 | 2016-01-13 | 株式会社大協組 | Method for producing foamed hydrothermal solidified product using incinerated ash as the main raw material |
JP6587278B2 (en) * | 2015-04-16 | 2019-10-09 | 国立研究開発法人国立環境研究所 | Method for producing incinerated fly ash solidified body and method for suppressing hydrogen gas generation |
-
1981
- 1981-09-25 JP JP56150521A patent/JPS6048234B2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS5851970A (en) | 1983-03-26 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0188371B1 (en) | Artificial lightweight aggregate | |
JPS6048234B2 (en) | Solidification treatment method for municipal waste dust | |
JP5443010B2 (en) | Method for producing hydrothermal solidified body of paper sludge incineration ash | |
JP2005320188A (en) | Inorganic foamed, fired body and its production method | |
US3811898A (en) | Heat-insulating antipiping compositions | |
JP4589652B2 (en) | Method for producing hydrothermal solidified product of paper sludge incineration ash | |
JP2003313553A (en) | Soil-stabilizing material and molded product made of soil | |
JPH08301641A (en) | Production of artificial lightweight aggregate | |
JP3086200B2 (en) | Solidification and stabilization of molten fly ash | |
JPH0812413A (en) | Production of water-permeable block | |
JPH1029841A (en) | Production of artificial aggregate | |
JPH0693260A (en) | Soil additive | |
JP2000034179A (en) | Production of water-holding granular sintered compact | |
JPH0311826B2 (en) | ||
JPS607554B2 (en) | Method for solidifying fine powder incineration residue | |
JPH1160328A (en) | Production of water absorbing brick using fly ash and its caked body | |
JPH06106153A (en) | Cement solidification of incineration ash and cement solidified product of incineration ash | |
JP6587278B2 (en) | Method for producing incinerated fly ash solidified body and method for suppressing hydrogen gas generation | |
JPS5837269B2 (en) | Molding method for inorganic materials | |
JP3204104B2 (en) | Manufacturing method of artificial lightweight aggregate | |
JPS567641A (en) | Manufacture of granulated powder for continuous casting of steel | |
JP2001009418A (en) | Treatment of combustion ash containing heavy metal | |
JPS5820283A (en) | Caking method for coal ash | |
JP2000247701A (en) | Production of artificial lightweight aggregate and artificial aggregate | |
JPH1067547A (en) | Production of artificial lightweight aggregate using incinerated ash |