JPS5851970A - Treatment for caking inflatable dust - Google Patents
Treatment for caking inflatable dustInfo
- Publication number
- JPS5851970A JPS5851970A JP56150521A JP15052181A JPS5851970A JP S5851970 A JPS5851970 A JP S5851970A JP 56150521 A JP56150521 A JP 56150521A JP 15052181 A JP15052181 A JP 15052181A JP S5851970 A JPS5851970 A JP S5851970A
- Authority
- JP
- Japan
- Prior art keywords
- dust
- cement
- granulating
- rotation
- gas
- 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
Links
Landscapes
- Processing Of Solid Wastes (AREA)
Abstract
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張するため破壊し易
い性質を有する膨張性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 expandable dust, which has a property of being easily destroyed because it expands with gas generation after solidification.
固結後ガス発生のために膨張するダストとして代表的な
ものの一例は都市ごみ焼却工程で排出されるダストであ
る。A typical example of dust that expands to generate gas after solidification is dust discharged during the municipal waste incineration process.
都市ご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、または電気収車機等の収車
系で捕集回収される粉末状の回収ダストがある。都市ご
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、火格子を用いる機棹炉、燃焼媒体として硼砂を用
いる流動床炉との2種類がある。機械炉ダストは一般に
微細であシ、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、都市ごみ由来の金洟アルミニウム粉末
、可涜性塩類を含有する点である。In the process of incinerating municipal waste, in addition to coarse incineration residue, it is transported along with exhaust gas and collected by a cyclone installed as a process after the incinerator or by a vehicle collection system such as an electric vehicle collection machine. There is recovered dust in powder form. There are various methods of incinerating municipal waste, but there are two main types: a machine furnace using a grate and a fluidized bed furnace using borax as a combustion medium. Mechanical furnace dust is generally fine, and fluidized bed furnace dust is generally coarse because it is mixed with sand, which is a heating medium accompanying exhaust gas. However, the common feature of both is that they contain Kanazawa aluminum powder and sacrificial salts derived from municipal waste.
本発明の対象とする処理物は、都市ごみの焼却工程にお
ける収車系で回収された粉末状ダストである。これらダ
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
の工粗士、拡散を防止するための固形化処理が必要であ
る。The object of the present invention is powdered dust collected by a vehicle collection system in the municipal waste incineration process. These dusts contain cadmium, lead, and other heavy metals, and when the dusts are to be disposed of, they must be solidified to prevent these heavy metals from dispersing.
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Σ。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jt
a圧゛して成形f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ブリケット方式、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3、ところが上記都市
ごみから生ずる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9、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って水素ガスを発生
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、3CaO1At
203、CaCl2101(20、クロル−エトリンガ
イド30aO1At20a CaCtz 18 H2O
などを生成する。これら複塩は膨張性の化合物であり、
金桐アルミニウムによる水嵩ガスの発生とともに、成形
物を膨張させ処理物の構造を、短期、長期にわたって脆
化する性質を有する。このため従前の各種成形力法によ
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夫々い、又加圧成形物では、緻密
々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
によシ破壊、崩壊する傾向があり、この傾向は強固、緻
密な成形物はど著1〜いという問題がある、1
本発明は上記膨張性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って、その要旨は、固結後にガス発
生や複塩のため膨張するダストに対し、水硬性セメント
と適せの水分とを混合して該ダストを転動造粒し、開放
気孔を有する放球にすることを特徴とする。In the past, a common method for such solidification treatment was to add hydraulic cement and water to dust, mix it, and solidify it. The molding method is an extrusion molding method in which the material is extruded from a nozzle under pressure, and the molding method is to pressurize it and extrude it from a nozzle.
Pressure molding method in which the molding is carried out under pressure, briquette method in which double rolls with split molds are rotated to continuously pressurize molding, and furthermore, the amount of added water is increased to make it fluid and formwork of a certain size is formed. However, the dust generated from the above-mentioned municipal waste contains soluble salts such as metal aluminum, lime chloride, and sodium chloride9, and when adding hydraulic cement and water, metal Aluminum generates hydrogen gas by hydrolysis in alkaline regions, and soluble salts react with the chemical components of hydraulic cement to form double salts, such as Friedel salt, 3CaO1At
203, CaCl2101 (20, chloro-ethrine guide 30aO1At20a CaCtz 18 H2O
etc. These double salts are expansive compounds;
Kanetou aluminum generates watery gas, which expands the molded product and embrittles the structure of the processed product over short and long periods of time. For this reason, according to the various conventional forming force methods, since the molded product is generally a dense structure, for example, in the casting method, the molded product swells significantly due to hydrogen gas foaming, increasing the strength and pressure. Molded products have a dense shell structure, so they tend 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. The present invention provides a method for stably solidifying the above-mentioned expandable dust, and its gist is that after solidification, the gas For dust that expands due to generation or double salt, the dust is mixed with hydraulic cement and an appropriate amount of moisture, and the dust is rolled and granulated to form balls with open pores.
以下に本発明の詳細な説明する。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膨張性ダストに混
入するセメントとして水硬性セメントを用いる。該水硬
性セメントには普通ポルトランドセメント、超早強7t
′ルトシンl′セメント、早強ポルトランドセメント、
中j市ポルトランドセメント等のポ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
放球の期待強度によって異なるが一般にダスト重量に対
し5重量部から40重量部の範囲であり、普通20〜3
0重量部であればよい。又添加水量は造粒に適する水景
であってダストおよび上記水硬性セメントの粉末度、ダ
ストの濡れ性によっても異なるが通常10〜20重i%
であればよい。次に転勤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。In the solidification treatment method of the present invention, hydraulic cement is used as the cement mixed in the expandable dust. The hydraulic cement is ordinary Portland cement, ultra-early strength 7t.
'Lutocin l' cement, early strength portland cement,
Portland cement such as Nakaj City Portland cement, mixed cement such as blast furnace cement, silica cement, fly ash cement, and ultra-fast hardening cement can be used. The mixing ratio of the hydraulic cement to the dust varies depending on the expected strength of the ball, but it is generally in the range of 5 to 40 parts by weight, and usually 20 to 3 parts by weight, based on the weight of the dust.
It may be 0 parts by weight. The amount of water added varies depending on the aquascape suitable for granulation, the powderiness of the dust and the above-mentioned hydraulic cement, and the wettability of the dust, but is usually 10 to 20% by weight.
That's fine. Next, as a transfer granulation method, a rotating cylindrical granulation method, a dish-type rolling granulation method, etc. are used.
本発明の固形化処理方法によれば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放
球することができ、この過程で放球内部に開放気孔に富
む構造が形成される。このようにして造粒された放球の
空隙率は30〜35%に及びその殆んどが開放気孔であ
る。このため放球内部で発生する水素ガスはこの気孔を
通じて無理なく放出され、又塩類との反応によって生ず
る膨張性の可溶性地類も空隙の多い横糸体中で安定に保
持される。According to the solidification treatment method of the present invention, the dust is granulated so as to uniformly pile up the shells while being connected by the solidification effect of hydraulic cement, and the ball is released with a uniform compaction effect on the entire surface of the ball. During this process, a structure rich in open pores is formed inside the ball. The porosity of the balls thus granulated is 30 to 35%, and most of them are open pores. For this reason, the hydrogen gas generated inside the ball is easily released through the pores, and the expandable soluble matrix produced by the reaction with salts is also stably retained in the weft body, which has many voids.
特許出願人 小野目1セメント株式会社代理人弁理士
光石士部 (他1名)Patent applicant: Onome 1 Cement Co., Ltd. Representative patent attorney: Shibu Mitsuishi (1 other person)
Claims (1)
水硬性セメントと適量の水分とを混合して該ダストを転
動造粒し、開放気孔を有する放球に↑ることを特徴とす
る膨張性ダストの固形化処理方法。For dust that expands due to gas generation and double salt after solidification,
1. A method for solidifying expandable dust, which comprises mixing hydraulic cement and an appropriate amount of water and granulating the dust by rolling to form spherical particles 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 true JPS5851970A (en) | 1983-03-26 |
JPS6048234B2 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) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH09100146A (en) * | 1995-10-04 | 1997-04-15 | Sumikin Kashima Kouka Kk | Treatment of burnt or fused scattered ash |
JP2001259596A (en) * | 2000-03-23 | 2001-09-25 | Hitachi Zosen Corp | Method for making incineration fly ash harmless |
JP2013123691A (en) * | 2011-12-15 | 2013-06-24 | Daikyogumi:Kk | Hydrothermally solidified foam made mainly of incineration ash, and method for producing the same |
JP2014176847A (en) * | 2014-04-23 | 2014-09-25 | Daikyogumi:Kk | Manufacturing method of foam hydrothermally-solidified body using incineration ash as main raw material and foam hydrothermally-solidified body |
JP2016203044A (en) * | 2015-04-16 | 2016-12-08 | 国立研究開発法人国立環境研究所 | Method for producing solidified body of incineration fly ash and method for inhibiting hydrogen gas generation |
-
1981
- 1981-09-25 JP JP56150521A patent/JPS6048234B2/en not_active Expired
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH09100146A (en) * | 1995-10-04 | 1997-04-15 | Sumikin Kashima Kouka Kk | Treatment of burnt or fused scattered ash |
JP2001259596A (en) * | 2000-03-23 | 2001-09-25 | Hitachi Zosen Corp | Method for making incineration fly ash harmless |
JP2013123691A (en) * | 2011-12-15 | 2013-06-24 | Daikyogumi:Kk | Hydrothermally solidified foam made mainly of incineration ash, and method for producing the same |
JP2014176847A (en) * | 2014-04-23 | 2014-09-25 | Daikyogumi:Kk | Manufacturing method of foam hydrothermally-solidified body using incineration ash as main raw material and foam hydrothermally-solidified body |
JP2016203044A (en) * | 2015-04-16 | 2016-12-08 | 国立研究開発法人国立環境研究所 | Method for producing solidified body of incineration fly ash and method for inhibiting hydrogen gas generation |
Also Published As
Publication number | Publication date |
---|---|
JPS6048234B2 (en) | 1985-10-25 |
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