JP3415065B2 - Method for producing desalted solidified waste incineration ash - Google Patents
Method for producing desalted solidified waste incineration ashInfo
- Publication number
- JP3415065B2 JP3415065B2 JP11951499A JP11951499A JP3415065B2 JP 3415065 B2 JP3415065 B2 JP 3415065B2 JP 11951499 A JP11951499 A JP 11951499A JP 11951499 A JP11951499 A JP 11951499A JP 3415065 B2 JP3415065 B2 JP 3415065B2
- Authority
- JP
- Japan
- Prior art keywords
- solidified body
- water
- solidified
- waste incineration
- incineration ash
- 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 - Fee Related
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/91—Use of waste materials as fillers for mortars or concrete
Landscapes
- Processing Of Solid Wastes (AREA)
Description
【0001】[0001]
【発明の属する技術分野】本発明は、都市ごみ、産業廃
棄物、RDF(Refuse DerivedFue
l、ごみ固形燃料)等の廃棄物を焼却する際に発生する
廃棄物焼却灰及び/又は廃棄物焼却飛灰(以下、「廃棄
物焼却灰」又は「焼却灰」と総称する)の脱塩(脱塩化
物)固化体を製造する方法に関するものである。TECHNICAL FIELD The present invention relates to municipal waste, industrial waste, and RDF (Refuse Derived Fue).
desalination of waste incineration ash and / or waste incineration fly ash (hereinafter collectively referred to as "waste incineration ash" or "incineration ash") generated when incinerating waste such as l, solid waste fuel) (Dechlorinated product) The present invention relates to a method for producing a solidified product.
【0002】[0002]
【従来の技術】焼却灰にはPb、Cd等の重金属類及び
塩化カルシウム、塩化カリウム、塩化ナトリウム等のア
ルカリ金属・アルカリ土類金属塩化物を主体とする無機
塩化物(以下、塩化物)が多く含まれている。特に、焼
却飛灰には重金属類、塩化物ともに多く含まれており、
この重金属のために直接埋立処分ができず、特別管理一
般廃棄物として、重金属の溶出を抑制するための処理と
して溶融固化、セメント固化、薬剤(キレート)処理、
溶媒抽出のいずれかによる中間処理が義務づけられてい
るが、塩化物については埋立基準等による規制値がない
ため、溶出に対する特別な処理は行われていない。2. Description of the Related Art Incinerated ash contains heavy metals such as Pb and Cd, and inorganic chlorides (hereinafter, chlorides) mainly composed of alkali metal and alkaline earth metal chlorides such as calcium chloride, potassium chloride and sodium chloride. Many are included. In particular, incineration fly ash contains a lot of heavy metals and chlorides,
Due to this heavy metal, direct landfill disposal is not possible, and as specially controlled general waste, melting and solidification, cement solidification, chemical (chelate) treatment, as treatment to suppress elution of heavy metals,
Although an intermediate treatment by either solvent extraction is obligatory, no special treatment for elution is performed for chlorides because there is no regulation value based on landfill standards.
【0003】これらの処理の内、溶融処理では塩化物の
ほとんどが溶融飛灰側に行くので、有効利用対象である
スラグ中に塩化物はほとんど含まれず、溶出もなくなる
が、設備費ならびに多くのエネルギーが必要となる。ま
た、焼却灰を有効利用するために水熱反応を利用した固
化体製造方法が各種提案されているが、これらは強度の
発現と重金属類の安定化に主眼がおかれており、有効利
用の際の塩化物の溶出については考慮されていない。さ
らに、特開昭55−134687号公報に示されるよう
に、固化前に焼却灰を水等で洗浄し、脱水工程を経てカ
ルシウム成分の存在下で固化させる方法も考えられる
が、この場合、
(1) 灰中の固化に必要な成分も洗浄水中に溶出す
る。
(2) 重金属の安定化処理が行われていないことか
ら、重金属が多量に溶出する恐れがある。
(3) 灰を脱水する装置などが必要になる。
等の問題点がある。Among these treatments, most of the chlorides in the melting treatment go to the molten fly ash side, so the chlorides are hardly contained in the slag, which is the object of effective use, and the elution is also eliminated, but the equipment cost and many Energy is needed. In addition, various methods for producing a solidified body using a hydrothermal reaction have been proposed in order to effectively utilize the incinerated ash, but these are focused on the development of strength and the stabilization of heavy metals. The elution of chloride at this time is not considered. Further, as disclosed in JP-A-55-134687, a method of washing incinerated ash with water or the like before solidification and solidifying in the presence of a calcium component through a dehydration step is also conceivable. 1) The components necessary for solidification in ash are also eluted in the wash water. (2) Since heavy metals are not stabilized, heavy metals may be eluted in large amounts. (3) A device for dehydrating ash is required. There are problems such as.
【0004】[0004]
【発明が解決しようとする課題】上記のように、焼却灰
中には塩化物が多く含まれており、この灰を水熱反応を
利用して固化体とした場合、塩化物のほとんどはその固
化体中に存在する。そのため、この固化体をそのまま土
木資材等として有効利用した場合、雨水等によって固化
体から塩化物が溶出し、付近の土壌に塩害をもたらす恐
れがある。本発明は上記の諸点に鑑みなされたもので、
本発明の目的は、焼却灰に添加剤として消石灰やセメン
ト等のアルカリ剤、シリカやアルミナを含む物質、例え
ば、シリカヒューム、粘土、浚渫汚泥等を加え、水熱固
化反応を利用して固化体を製造した後、この固化体を一
定期間に水に浸す等、水を用いてこの固化体の脱塩素
(脱塩化物)を行い、重金属及び塩化物の溶出のない固
化体を得て、この脱塩固化体を有効利用することができ
る廃棄物焼却灰脱塩固化体の製造方法を提供することに
ある。As described above, the incinerated ash contains a large amount of chloride, and when this ash is solidified by utilizing the hydrothermal reaction, most of the chloride is It exists in the solidified body. Therefore, when the solidified body is effectively used as it is as a civil engineering material, chloride may be eluted from the solidified body by rainwater or the like, which may cause salt damage to nearby soil. The present invention has been made in view of the above points,
The object of the present invention is to add an alkaline agent such as slaked lime or cement as an additive to the incinerated ash, a substance containing silica or alumina, for example, silica fume, clay, dredged sludge, etc. After manufacturing, the solidified body is dechlorinated (dechlorinated) with water by immersing the solidified body in water for a certain period of time to obtain a solidified body without elution of heavy metals and chlorides. An object of the present invention is to provide a method for producing a desalted and solidified waste incineration ash that can effectively utilize the desalted and solidified body.
【0005】[0005]
【課題を解決するための手段】上記の目的を達成するた
めに、本発明の廃棄物焼却灰脱塩固化体の製造方法は、
廃棄物焼却灰にアルカリ剤及びシリカやアルミナを含む
物質を添加剤として加え、水熱固化反応を利用して、洗
浄水と接触中に固化体が崩壊したり、洗浄水に重金属が
溶出しないように圧縮強度が50kgf/cm2以上の固化体
とした後、この固化体を水と接触させ固化体中の塩化物
を水に溶解させて除去し、強度を保った重金属及び塩化
物が溶出しない脱塩固化体とするように構成される。In order to achieve the above object, the method for producing a waste incineration ash desalted and solidified product of the present invention comprises:
Waste incineration ash was added to <br/> Substance containing an alkali agent and silica or alumina as an additive, by using the hydrothermal solidification reactions, or solid material in contact with the washing water to disintegrate, in the wash water After forming a solidified body with a compressive strength of 50 kgf / cm 2 or more so that the heavy metal does not elute, the solidified body is brought into contact with water to dissolve the chloride in the solidified body and remove it to remove heavy metal and It is configured to be a desalted and solidified body in which chloride is not eluted.
【0006】本発明の方法は、上記のように、焼却灰に
添加剤及び適量の水を加えて混練し、水熱反応を利用し
て固化体を製造し、有効利用に必要な強度の発現と重金
属類の安定化を図った後、固化体中の塩化物を水に溶出
させて除去するために一定期間、固化体と水(以下、脱
塩用洗浄水又は洗浄水と記す場合がある)と接触させ
る。このようにして、塩化物の溶出が一定値以下になる
ようにして得た固化体を土木資材等として有効利用す
る。この時、洗浄水中には塩化物以外に重金属等の有害
物質は溶出していないので、その処理も容易である。な
お、本発明の方法を実施する場合、固化体の強度が不十
分であると、洗浄水と接触中に固化体が崩壊したり、洗
浄水に重金属類が多量に溶出する恐れがあることから、
水と接触させる前の固化体の圧縮強度は少なくとも50
kgf /cm2 以上、望ましくは100kgf /cm2 以上ある
ことが必要である。In the method of the present invention, as described above, the additive and an appropriate amount of water are added to the incinerated ash, and the mixture is kneaded to produce a solidified body by utilizing hydrothermal reaction, and the strength required for effective utilization is expressed. After stabilizing the solid metal and heavy metals, the solidified body and water (hereinafter referred to as desalination washing water or washing water may be referred to as desalination washing water for a certain period of time in order to elute and remove chloride in the solidified body by elution into water. ) Contact. In this way, the solidified body obtained by elution of chloride to a certain value or less is effectively used as a civil engineering material or the like. At this time, since harmful substances such as heavy metals other than chlorides are not eluted in the wash water, the treatment is easy. When carrying out the method of the present invention, if the strength of the solidified product is insufficient, the solidified product may collapse during contact with the wash water, or a large amount of heavy metals may be eluted in the wash water. ,
The compressive strength of the solidified body before contact with water is at least 50
It is necessary that the pressure is at least kgf / cm 2 , preferably at least 100 kgf / cm 2 .
【0007】上記の方法において、アルカリ剤として
は、消石灰、生石灰、石灰石、石こう、鉄鋼スラグ及び
セメントの少なくともいずれかが用いられる。また、シ
リカやアルミナを含む物質としては、シリカヒューム、
粘土、石炭灰、珪砂、スラグ及び浚渫汚泥の少なくとも
いずれかが用いられる。In the above method, at least one of slaked lime, quick lime, limestone, gypsum, steel slag and cement is used as the alkaline agent. Further, as the substance containing silica or alumina, silica fume,
At least one of clay, coal ash, silica sand, slag, and dredging sludge is used.
【0008】[0008]
【発明の実施の形態】以下、本発明の実施の形態につい
て説明するが、本発明は下記の実施の形態に何ら限定さ
れるものではなく、適宜変更して実施することができる
ものである。図1は本発明の実施の第1形態による廃棄
物焼却灰脱塩固化体の製造方法を実施する装置を示して
いる。この装置は、廃棄物焼却灰、アルカリ剤及びシリ
カやアルミナを含む物質の少なくともいずれかの添加
剤、及び水を混練し養生して固化体とするための固化体
製造装置10と、固化体製造装置10で得られた固化体
を水と接触させて固化体中の塩化物を水に溶解させるた
めの洗浄槽12と、塩化物が溶解した水を洗浄槽12か
ら抜き出して清浄水と塩化物とに分離するための排水処
理装置14とを備えている。16は固化体である。排出
処理装置14としては、例えばイオン交換膜を用いた装
置、焼却炉等の廃熱を利用した蒸留装置等を挙げること
ができる。排出処理装置14からの洗浄水は循環使用さ
れるか、又は放流される。なお、排出処理装置14を設
けずに、洗浄槽12からの排水を放流することも可能で
ある。BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, embodiments of the present invention will be described. However, the present invention is not limited to the following embodiments, and can be appropriately modified and implemented. FIG. 1 shows an apparatus for carrying out a method for producing a waste incineration ash desalted and solidified body according to a first embodiment of the present invention. This apparatus includes a solidified body manufacturing apparatus 10 for kneading and curing waste incineration ash, an alkaline agent and at least one additive of a substance containing silica or alumina, and water to form a solidified body, and a solidified body manufacturing apparatus. A cleaning tank 12 for contacting the solidified body obtained by the apparatus 10 with water to dissolve chloride in the solidified body in water, and water in which chloride is dissolved is extracted from the cleaning tank 12 to obtain clean water and chloride. And a wastewater treatment device 14 for separating into 16 is a solidified body. Examples of the discharge treatment device 14 include a device using an ion exchange membrane, a distillation device using waste heat from an incinerator, and the like. The wash water from the discharge treatment device 14 is either recycled or discharged. It is also possible to discharge the waste water from the cleaning tank 12 without providing the discharge processing device 14.
【0009】図2は、図1における固化体製造装置10
での製造工程を示している。廃棄物焼却灰、アルカリ
剤、シリカやアルミナを含む物質及び水が混練機に供給
されて混練される。これらは別々に混練機に供給されて
もよく、又は2種以上が予め混合された状態で混練機に
供給されてもよい。混練物は成形機(例えば型枠成形
機)に導入されて成形された後、前養生室で前養生さ
れ、ついで脱型される。脱型された前養生物は本養生室
で水蒸気養生されて固化体となる。さらに破砕機でこの
固化体を破砕し、砕石状固化体とする場合もある。これ
ら一連の装置で固化体製造装置(水熱固化反応装置)が
構成される。なお、成形工程及び脱型工程を省略した
り、前養生工程を省略したり、造粒工程又は加圧成形工
程等を加えたりすることも可能である。混練物を養生す
ることで、水和固化反応(水熱固化反応)によってエト
リンガイト(3CaO・Al2 O3 ・3CaSO4 ・3
2H2 O)、C−S−H(ケイ酸カルシウム水和物)等
を生成して固化し、水和反応(水熱反応)による固化体
となる。そして、必要に応じて破砕する。得られた固化
体は、安定化している上に強度も大きく、かつ、重金属
及び塩化物の溶出のない脱塩固化体であるので、路盤材
等の土木資材、建築資材として有効利用することができ
る。FIG. 2 shows a solidified body manufacturing apparatus 10 in FIG.
Shows the manufacturing process in. Waste incineration ash, an alkali agent, a substance containing silica and alumina, and water are supplied to a kneader and kneaded. These may be supplied to the kneading machine separately, or may be supplied to the kneading machine in a state where two or more kinds are mixed in advance. The kneaded product is introduced into a molding machine (for example, a mold molding machine) to be molded, then pre-cured in a pre-curing chamber, and then demolded. The demolded pre-cured organism is steam-cured in the main curing room to become a solidified body. Further, the solidified body may be crushed by a crusher to form a crushed stone-like solidified body. A solidified body manufacturing apparatus (hydrothermal solidification reaction apparatus) is constituted by these series of apparatuses. It should be noted that it is possible to omit the molding step and the demolding step, omit the pre-curing step, add a granulation step, a pressure molding step, or the like. By curing the kneaded product, ettringite (3CaO.Al 2 O 3 3CaSO 4 .3) is formed by hydration solidification reaction (hydrothermal solidification reaction).
2H 2 O), C—S—H (calcium silicate hydrate), etc. are generated and solidified to be a solidified body by a hydration reaction (hydrothermal reaction). Then, it is crushed if necessary. The obtained solidified body is stable and has high strength, and since it is a desalted solidified body without elution of heavy metals and chlorides, it can be effectively used as a civil engineering material such as a roadbed material or a construction material. it can.
【0010】図3は本発明の実施の第2形態による廃棄
物焼却灰脱塩固化体の製造方法を実施する装置を示して
いる。本実施形態は、洗浄水として雨水を利用するよう
に構成されたものである。他の構成及び作用は実施の第
1形態の場合と同様である。FIG. 3 shows an apparatus for carrying out the method for producing a waste incineration ash desalted and solidified product according to the second embodiment of the present invention. The present embodiment is configured to use rainwater as cleaning water. Other configurations and operations are similar to those of the first embodiment.
【0011】[0011]
【実施例】以下に実施例及び比較例を示し、本発明の特
徴とするところをより一層明確にする。
実施例1、比較例1
表1に示す組成のRDF焼却飛灰を用いて試験を行っ
た。EXAMPLES Examples and comparative examples will be shown below to further clarify the features of the present invention. Example 1 and Comparative Example 1 Tests were carried out using RDF incineration fly ash having the composition shown in Table 1.
【0012】[0012]
【表1】 [Table 1]
【0013】試験に用いた固化体(固化体1、2)は図
4に示すフローに従って製造した。なお、アルカリ剤と
して消石灰、シリカやアルミナを含む物質としてシリカ
ヒュームを用いた。表2に固化体1、2の性状を示す。
試験は、粒度を9.5〜16.0mmに調整した粒状固化
体100g を、図5に示すカラム試験装置のガラス製カ
ラム20内に入れ、pH4(硝酸で調整)の水250ml中
に浸漬した。これを、常温で一定期間(この場合は、2
週間)静置して溶出を行った後、溶出液を抜き出し、さ
らに、新しい所定pH(pH4)の水250mlを入れ、同じ
操作を計6回繰り返した。図5において、22は固化
体、24は水、26はメンブランフィルタ(0.45μ
m )である。水をpH4に調整したのは、雨水を用いる場
合を想定したことによる。The solidified bodies (solidified bodies 1 and 2) used in the test were manufactured according to the flow shown in FIG. Note that slaked lime was used as the alkaline agent, and silica fume was used as the substance containing silica and alumina. Table 2 shows the properties of the solidified bodies 1 and 2.
In the test, 100 g of the granular solidified body whose particle size was adjusted to 9.5 to 16.0 mm was put in the glass column 20 of the column test apparatus shown in FIG. 5 and immersed in 250 ml of water of pH 4 (adjusted with nitric acid). . This is done at room temperature for a certain period (in this case 2
After elution was carried out by standing still, the eluate was extracted, 250 ml of water having a new predetermined pH (pH 4) was further added, and the same operation was repeated 6 times in total. In FIG. 5, 22 is a solidified body, 24 is water, and 26 is a membrane filter (0.45 μm).
m). The reason for adjusting the pH to 4 is that it is assumed that rainwater will be used.
【0014】[0014]
【表2】 [Table 2]
【0015】浸漬前後の固化体1、2の性状を表3に、
洗浄水の性状を表4に示す。また、図6に固化体1を洗
浄した場合の水量と重金属溶出量との関係を示し、図7
に固化体1を洗浄した場合の水量とCl等溶出量との関
係を示し、図8に固化体2を洗浄した場合の水量と重金
属溶出量との関係を示し、図9に固化体2を洗浄した場
合の水量とCl等溶出量との関係を示す。Table 3 shows the properties of the solidified bodies 1 and 2 before and after the immersion.
Table 4 shows the properties of the wash water. Further, FIG. 6 shows the relationship between the amount of water and the amount of heavy metal eluted when the solidified body 1 is washed.
Fig. 8 shows the relationship between the amount of water when the solidified body 1 was washed and the elution amount of Cl, etc., Fig. 8 shows the relationship between the amount of water when the solidified body 2 was washed and the elution amount of heavy metals, and Fig. 9 shows the solidified body 2 The relationship between the amount of water and the amount of Cl and the like eluted when washed is shown.
【0016】[0016]
【表3】 [Table 3]
【0017】[0017]
【表4】 [Table 4]
【0018】表3より、どちらの固化体も洗浄により重
量減少しているが、元素組成より塩化物の溶出がその主
要因であることが分かる。また、洗浄による固化体の崩
壊は初期圧縮強度が高いほど少なく、洗浄による強度の
低下も認められなかった。洗浄水の性状を示す表4及び
図6〜図9より、塩化物の溶出は初期に著しく、洗浄水
を替えるごとに急激に減少し、2〜4回で塩素濃度が5
00mg/l (500ppm )以下に減少し、固化体の初期
圧縮強度が高いほど塩素濃度が低く、重金属(Pb、C
d)の溶出は初期の性状のまま著しい変化は認められな
かった。From Table 3, it can be seen that the weight of both solidified bodies is reduced by washing, but the elution of chloride is the main factor from the elemental composition. Further, the higher the initial compression strength, the less the collapse of the solidified body due to washing, and the lowering of the strength due to washing was not observed. From Table 4 showing the properties of the wash water and Figs. 6 to 9, the chloride elution was remarkable at the initial stage, and it was sharply reduced each time the wash water was changed.
It decreases to less than 00 mg / l (500 ppm), and the higher the initial compressive strength of the solidified body, the lower the chlorine concentration.
The elution of d) did not show any significant change with the initial properties.
【0019】これより、適正に製造された固化体に対し
て本発明の方法を用いることで、固化体の性能(強度、
重金属の溶出抑制)を保ったまま、塩化物のみを除去す
ることができ、塩化物の溶出のない固化体を得ることが
出来、さらに、洗浄液中には塩化物以外に有害な重金属
等が溶出することがないので洗浄水の処理も容易であ
る。なお、洗浄水として用いる水は、一般の水道水、工
業用水、雨水等特別な制限はない。From the above, the performance (strength, strength, etc.) of the solidified body can be obtained by using the method of the present invention for the appropriately manufactured solidified body.
It is possible to remove chloride only while maintaining the suppression of heavy metal elution, and to obtain a solidified product without chloride elution. In addition, harmful heavy metals other than chloride are eluted in the cleaning liquid. Since it does not occur, the treatment of washing water is easy. The water used as washing water is not particularly limited, such as general tap water, industrial water, and rainwater.
【0020】[0020]
【発明の効果】本発明は上記のように構成されているの
で、つぎのような効果を奏する。
(1) 水熱固化反応を利用して固化体とした後に、水
と接触させて脱塩処理を行うことにより、固化体の強度
低下がなく、洗浄水中への重金属の溶出なしに脱塩する
ことができ、洗浄排水の処理を容易に行うことができ
る。
(2) 固化体からの塩化物の溶出がないので、この固
化体を土木資材等として有効利用した場合、付近の土壌
に対して塩害を引き起こすおそれがなく、その結果、有
効利用できる範囲が大幅に広がる。Since the present invention is configured as described above, it has the following effects. (1) After the solidified body is formed by utilizing the hydrothermal solidification reaction, desalting treatment is performed by bringing it into contact with water, so that the strength of the solidified body does not decrease and the desalination is performed without elution of heavy metals into the wash water. Therefore, the cleaning wastewater can be easily treated. (2) Since there is no chloride elution from the solidified body, when this solidified body is effectively used as a civil engineering material, there is no risk of causing salt damage to the soil in the vicinity, and as a result, the effective use range is greatly increased. Spread to.
【図1】本発明の実施の第1形態による廃棄物焼却灰脱
塩固化体の製造方法を実施する装置を示す概略構成図で
ある。FIG. 1 is a schematic configuration diagram showing an apparatus for carrying out a method for producing a waste incineration ash desalted and solidified body according to a first embodiment of the present invention.
【図2】図1における固化体製造装置での製造工程を示
す工程図である。FIG. 2 is a process drawing showing a manufacturing process in the solidified body manufacturing apparatus in FIG.
【図3】本発明の実施の第2形態による廃棄物焼却灰脱
塩固化体の製造方法を実施する装置を示す概略構成図で
ある。FIG. 3 is a schematic configuration diagram showing an apparatus for carrying out a method for producing a waste incineration ash desalted and solidified body according to a second embodiment of the present invention.
【図4】実施例及び比較例における廃棄物焼却灰固化体
の製造方法を示す工程図である。FIG. 4 is a process drawing showing a method for producing a solidified waste incineration ash in Examples and Comparative Examples.
【図5】実施例で用いたカラム試験装置の立面説明図で
ある。FIG. 5 is an elevational explanatory view of a column test apparatus used in Examples.
【図6】固化体1を洗浄した場合の水量と重金属溶出量
との関係を示すグラフである。FIG. 6 is a graph showing the relationship between the amount of water and the amount of heavy metal eluted when the solidified body 1 is washed.
【図7】固化体1を洗浄した場合の水量とCl等溶出量
との関係を示すグラフである。FIG. 7 is a graph showing the relationship between the amount of water and the amount of Cl and the like eluted when the solidified body 1 is washed.
【図8】固化体2を洗浄した場合の水量と重金属溶出量
との関係を示すグラフである。FIG. 8 is a graph showing the relationship between the amount of water and the amount of heavy metal eluted when the solidified body 2 is washed.
【図9】固化体2を洗浄した場合の水量とCl等溶出量
との関係を示すグラフである。FIG. 9 is a graph showing the relationship between the amount of water and the amount of Cl and the like eluted when the solidified body 2 is washed.
10 固化体製造装置 12 洗浄槽 14 排水処理装置 16、22 固化体 20 ガラス製カラム 24 水 26 メンブランフィルタ 10 Solidified body manufacturing equipment 12 washing tank 14 Wastewater treatment equipment 16,22 Solidified 20 glass columns 24 water 26 Membrane Filter
フロントページの続き (56)参考文献 特開 平7−155724(JP,A) 特開 平9−94548(JP,A) 特開 平10−99816(JP,A) 特開 平9−271752(JP,A) 特開 平10−28950(JP,A) 実開 平2−1292(JP,U) (58)調査した分野(Int.Cl.7,DB名) B09B 3/00 301 - 304 C04B 7/24 - 7/28 C04B 18/06 - 18/08 Continuation of front page (56) Reference JP-A-7-155724 (JP, A) JP-A-9-94548 (JP, A) JP-A-10-99816 (JP, A) JP-A-9-271752 (JP , A) JP-A-10-28950 (JP, A) Actual development 2-1292 (JP, U) (58) Fields investigated (Int.Cl. 7 , DB name) B09B 3/00 301-304 C04B 7 / 24-7/28 C04B 18/06-18/08
Claims (3)
アルミナを含む物質を添加剤として加え、水熱固化反応
を利用して、洗浄水と接触中に固化体が崩壊したり、洗
浄水に重金属が溶出しないように圧縮強度が50kgf/c
m2以上の固化体とした後、この固化体を水と接触させ固
化体中の塩化物を水に溶解させて除去し、強度を保った
重金属及び塩化物が溶出しない脱塩固化体とすることを
特徴とする廃棄物焼却灰脱塩固化体の製造方法。1. A added quality ones containing an alkali agent and silica or alumina in waste incineration ash as an additive, by using the hydrothermal solidification reaction, or collapse solidified body in contact with the wash water, the wash water Compressive strength is 50kgf / c so that heavy metals do not elute
After forming a solidified body of m 2 or more, the solidified body is brought into contact with water to dissolve the chloride in the solidified body and remove it to obtain a desalted solidified body that retains strength and does not elute heavy metals and chlorides. A method for producing a waste incineration ash desalination solidified product, which is characterized by the above.
石、石こう、鉄鋼スラグ及びセメントの少なくともいず
れかである請求項1記載の廃棄物焼却灰脱塩固化体の製
造方法。Wherein the alkali agent is slaked lime, quick lime, limestone, gypsum, manufacturing method of waste incineration ash desalted solidified body according to claim 1, wherein at least one of steel slag and cement.
ヒューム、粘土、石炭灰、珪砂、スラグ及び浚渫汚泥の
少なくともいずれかである請求項1又は2記載の廃棄物
焼却灰脱塩固化体の製造方法。3. A material containing silica and alumina, the production of silica fume, clay, coal ash, silica sand, slag and at least either of dredging sludge claim 1 or 2 waste incineration ash desalted solidified body according Method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11951499A JP3415065B2 (en) | 1999-04-27 | 1999-04-27 | Method for producing desalted solidified waste incineration ash |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11951499A JP3415065B2 (en) | 1999-04-27 | 1999-04-27 | Method for producing desalted solidified waste incineration ash |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2000308865A JP2000308865A (en) | 2000-11-07 |
| JP3415065B2 true JP3415065B2 (en) | 2003-06-09 |
Family
ID=14763166
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11951499A Expired - Fee Related JP3415065B2 (en) | 1999-04-27 | 1999-04-27 | Method for producing desalted solidified waste incineration ash |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3415065B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4759667B2 (en) * | 2005-09-12 | 2011-08-31 | 独立行政法人国立高等専門学校機構 | Paper sludge incinerated ash granulated hydrothermal solidified body-aluminum composite material |
| JP2008239428A (en) * | 2007-03-28 | 2008-10-09 | Taiheiyo Cement Corp | Fired product |
-
1999
- 1999-04-27 JP JP11951499A patent/JP3415065B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JP2000308865A (en) | 2000-11-07 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Bertos et al. | A review of accelerated carbonation technology in the treatment of cement-based materials and sequestration of CO2 | |
| CN113633921B (en) | Fly ash dechlorination method | |
| KR100490731B1 (en) | A Method for constuction material and civil engineering using waste materials | |
| CN110668747A (en) | Recycled regeneration material for treating polluted bottom mud and preparation method thereof | |
| JP2583729B2 (en) | Detoxification and stabilization of waste containing hazardous heavy metals | |
| JP3415065B2 (en) | Method for producing desalted solidified waste incineration ash | |
| CN110372168A (en) | A kind of method of river sludge resource utilization | |
| KR100375407B1 (en) | method of manufacturing solity for preventing heavy metals from being occurred in wastes and solity manufactured by the same | |
| TWI418393B (en) | Processing method for fly ash of large-scale incineration plant and product thereof | |
| CN1165356C (en) | Mixture for treating waste material | |
| KR20030049396A (en) | A method to reuse ash and dust containing heavy metals as materials for civil engineering and construction | |
| FR2302970A1 (en) | Treating effluent sludge containing hydroxides of heavy metals - by mixing into solidifying insol. material for safe disposal | |
| JP2005028343A (en) | Methods for preventing leaching of toxic metals from hazardous metal contaminated waste | |
| JP2004008945A (en) | Hazardous substance insolubilization method | |
| JP2002029794A (en) | Manufacturing method of fine aggregate and the like using waste glass and sintered body | |
| JP2003171160A (en) | Industrial waste recycled aggregate | |
| JP2004105783A (en) | Soil solidification treatment material and solidification treatment method | |
| JPH05185096A (en) | Treatment of waste muddy water in construction | |
| KR100357524B1 (en) | Solidity material for reapplication of assignment waste harding foam having excellent compressive strength using the solidity material | |
| JP3415066B2 (en) | Manufacturing method of solidified waste incineration ash | |
| JPH09122620A (en) | Waste treatment material and waste treatment method | |
| JP5754819B2 (en) | Calcium elution prevention method at final disposal site | |
| JP4277590B2 (en) | Solidification method of sludge | |
| JP2020511584A (en) | Binder production method for conditioning soil containing sludge and water, and for neutralizing acid | |
| JP3443653B2 (en) | Civil engineering and construction materials |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| LAPS | Cancellation because of no payment of annual fees |