JP3303251B2 - How to treat incinerated ash - Google Patents
How to treat incinerated ashInfo
- Publication number
- JP3303251B2 JP3303251B2 JP10877795A JP10877795A JP3303251B2 JP 3303251 B2 JP3303251 B2 JP 3303251B2 JP 10877795 A JP10877795 A JP 10877795A JP 10877795 A JP10877795 A JP 10877795A JP 3303251 B2 JP3303251 B2 JP 3303251B2
- Authority
- JP
- Japan
- Prior art keywords
- incinerated ash
- heavy metal
- ash
- fly ash
- present
- 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
Landscapes
- Gasification And Melting Of Waste (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、焼却灰の処理方法に係
り、特に都市ごみ焼却処理施設等から排出される飛灰を
はじめとする焼却灰を埋め立て等に使用した際の重金属
の溶出を防止することができる焼却灰の処理方法に関す
るものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for treating incinerated ash, and more particularly, to the elution of heavy metals when incinerated ash including fly ash discharged from municipal solid waste incineration facilities is used for landfill. The present invention relates to a method for treating incinerated ash that can be prevented.
【0002】[0002]
【従来の技術】ごみ焼却炉から排出される焼却飛灰は、
特別管理一般廃棄物の煤塵に指定され、その中間処理法
としては、(1)溶融固化による重金属の安定化処理、
(2)セメント固化による重金属の安定化処理、(3)
薬剤処理による重金属の安定化処理および(4)酸抽出
による重金属の安定化処理の4つの方法が指定されてお
り、薬剤による重金属の安定化処理は比較的広範囲に使
用されている。2. Description of the Related Art Incineration fly ash discharged from refuse incinerators is
It is designated as dust of special management municipal waste, and its intermediate treatment methods include (1) stabilization treatment of heavy metals by melting and solidification,
(2) Stabilization of heavy metals by solidification of cement, (3)
Four methods of stabilization of heavy metals by chemical treatment and (4) stabilization of heavy metals by acid extraction are specified, and stabilization of heavy metals by chemicals is used in a relatively wide range.
【0003】しかしながら、薬剤による重金属の安定化
処理は、排ガス中の塩化水素を処理するために煙道内
に、例えば消石灰等を噴霧したアルカリ飛灰を処理する
場合、溶出液のpHが高アルカリ側にシフトするため
に、重金属である例えば鉛(Pb)が溶出し易くなり、
これを抑制するためには多量の薬剤が必要となるか、ま
たは別途pH調整剤を添加する必要があり、ランニング
コストが嵩むという問題があった。[0003] However, the stabilization treatment of heavy metals by chemicals involves treating alkaline fly ash sprayed with slaked lime or the like in a flue to treat hydrogen chloride in exhaust gas. , The heavy metal, for example, lead (Pb) is easily eluted,
In order to suppress this, a large amount of drug is required, or it is necessary to separately add a pH adjuster, and there is a problem that running costs increase.
【0004】[0004]
【発明が解決しようとする課題】本発明の目的は、上記
従来技術の問題点を解決し、薬剤使用量が少なく、しか
も重金属を効果的に閉じ込めてその溶出量を低減するこ
とができる焼却灰の処理方法を提供することにある。SUMMARY OF THE INVENTION An object of the present invention is to solve the above-mentioned problems of the prior art, to reduce the amount of chemicals used, and to effectively confine heavy metals to reduce the amount of incinerated ash. Is to provide a processing method.
【0005】[0005]
【課題を解決するための手段】上記目的を達成するため
本発明者は、焼却灰の薬剤処理による重金属の安定化方
法と処理後の重金属の溶出量との関係について鋭意研究
した結果、重金属固定剤を添加する前の焼却灰を所定温
度で加熱処理することにより、重金属の溶出量が低減す
ること、および重金属を添加して混練した後、加圧成形
することにより重金属の溶出量がさらに低減することを
見出し、本発明に到達した。Means for Solving the Problems In order to achieve the above object, the present inventors have conducted intensive studies on the relationship between the method of stabilizing heavy metals by chemical treatment of incinerated ash and the amount of heavy metal eluted after the treatment. Heating the incinerated ash before adding the agent at a predetermined temperature reduces the amount of heavy metal eluted, and further reduces the amount of heavy metal eluted by adding and kneading the heavy metal and then press forming. And arrived at the present invention.
【0006】すなわち本願で特許請求される発明は、以
下のとおりである。 (1)焼却灰を400〜550℃で加熱処理し、前記焼
却灰中の未燃カーボンの燃焼によって生じた炭酸ガスと
焼却灰中のアルカリ成分とを反応させた後、該反応生成
物に重金属固定剤と水を加えて混練し、成形固化するこ
とを特徴とする焼却灰の処理方法。 (2)重金属固定剤と水を加えて混練した後、加圧成形
することを特徴とする上記(1)記載の焼却灰の処理方
法。That is, the invention claimed in the present application is as follows. (1) Heating the incinerated ash at 400 to 550 ° C. to cause a reaction between carbon dioxide gas generated by burning unburned carbon in the incinerated ash and an alkali component in the incinerated ash. A method for treating incinerated ash, comprising adding a fixing agent and water, kneading the mixture, and solidifying the mixture. (2) The method for treating incinerated ash according to the above (1), wherein the mixture is kneaded by adding a heavy metal fixing agent and water and then kneaded.
【0007】[0007]
【作用】図1および図2は、本発明の原理を示す説明図
であり、図1は流動床式都市ごみ焼却飛灰を加熱脱塩素
化装置(ダイオブレーカ)で加熱処理した後、溶出試験
を行った際の加熱処理温度と溶出液のpHとの関係を示
すものである。なお、加熱時間は所定温度に達してから
それぞれ15分である。図において、焼却飛灰を400
℃以上、550℃以下で加熱処理することにより、溶出
液のpHが1以上減少しており、灰中の重金属が溶出し
にくくなっていることが分かる。これは、加熱処理する
ことにより、飛灰中のアルカリ成分が、未燃カーボンの
燃焼等によって生じた炭酸ガスによって炭酸化され、こ
れによって溶出液のpHが低下したものである。従って
溶出液のpHが重金属が安定化する範囲に保持され、重
金属は、例えば安定な水酸化物として固定されると考え
られる。FIG. 1 and FIG. 2 are explanatory views showing the principle of the present invention. FIG. 1 shows a leaching test after heat treatment of fluidized bed municipal solid waste incineration fly ash with a heat dechlorination apparatus (Die Breaker). Is a graph showing the relationship between the heat treatment temperature and the pH of the eluate at the time of carrying out the above. The heating time is 15 minutes after reaching the predetermined temperature. In the figure, the incineration fly ash is 400
By performing the heat treatment at a temperature of 550 ° C. or more, the pH of the eluate is decreased by 1 or more, and it is found that heavy metals in the ash are hardly eluted. This is because the alkali component in fly ash is carbonated by carbon dioxide gas generated by burning unburned carbon or the like by heat treatment, thereby lowering the pH of the eluate. Therefore, it is considered that the pH of the eluate is maintained in a range in which the heavy metal is stabilized, and the heavy metal is fixed, for example, as a stable hydroxide.
【0008】また図2は、流動床式都市ごみ焼却飛灰を
450℃で15分間加熱処理した後、重金属固定剤とし
てキレート剤を1重量%添加して混練し、次いで圧縮成
形した際の成形圧力と重金属であるカドミウム(Cd)
の溶出量との関係を示すものである。溶出試験は環境庁
告示第13号に準じて行い、溶媒として純水に塩酸を加
えpH5.8〜6.3に調整したものを用い、それぞれ
飛灰成形品を粉砕し、直径0.5〜5mmに粒度調整し
たものを重量体積比で10%になるように混合し、6時
間連続して振とうし、試験終了後の溶媒中のカドミウム
(Cd)を検出した。図において、圧縮成形するとCd
の溶出量が確実に低減し、圧縮圧力の増加とともに溶出
量が減少していることが分かる。FIG. 2 shows that the fluidized bed municipal solid waste incineration fly ash is heated at 450 ° C. for 15 minutes, added with 1% by weight of a chelating agent as a heavy metal fixing agent, kneaded, and then subjected to compression molding. Cadmium (Cd) which is pressure and heavy metal
The figure shows the relationship with the amount of eluted. The dissolution test was performed in accordance with the Notification of the Environment Agency No. 13, and hydrochloric acid was added to pure water as a solvent and the pH was adjusted to 5.8 to 6.3. The particles adjusted to a particle size of 5 mm were mixed so that the weight / volume ratio became 10%, and the mixture was shaken continuously for 6 hours to detect cadmium (Cd) in the solvent after the test was completed. In the figure, Cd
It can be seen that the elution amount of was surely reduced, and the elution amount was reduced as the compression pressure was increased.
【0009】すなわち本発明は、図3に処理フローを示
すように、薬剤処理する前の焼却灰をあらかじめ加熱処
理して脱塩素化した後、重金属添加剤および水を添加し
て混練し、次いで成形または圧縮成形するものである。
本発明において、焼却灰を加熱処理するための加熱温度
は400〜550℃であり、好ましくは420〜460
℃である。加熱温度が低すぎると溶出液のpH減少幅が
小さくて重金属の溶出を抑制する効果が小さくなる。一
方、加熱温度が高すぎるとエネルギの損失を招きランニ
ングコストが高くなる。また、加熱時間は所定温度に達
してから1〜30分であり、好ましくは5〜15分であ
る加熱時間が短すぎると重金属の溶出を抑制する効果が
得られず、長すぎるとランングコストが嵩む。焼却灰の
加熱装置としては、特に限定されず、例えば図5〜図7
に示すような竪型の連続式加熱装置、横型の加熱装置、
ロータリーキルン式加熱装置等公知のものが使用され
る。That is, according to the present invention, as shown in the processing flow of FIG. 3, incineration ash before chemical treatment is preheat-treated and dechlorinated, and then a heavy metal additive and water are added and kneaded. Molding or compression molding.
In the present invention, the heating temperature for heat-treating the incinerated ash is 400 to 550 ° C, preferably 420 to 460.
° C. If the heating temperature is too low, the pH decrease of the eluate is small and the effect of suppressing the elution of heavy metals is reduced. On the other hand, if the heating temperature is too high, energy is lost and running costs are increased. Further, the heating time is 1 to 30 minutes after reaching the predetermined temperature, preferably 5 to 15 minutes If the heating time is too short, the effect of suppressing the elution of heavy metals is not obtained, if too long, the running cost is reduced. Bulky. The apparatus for heating the incinerated ash is not particularly limited.
Vertical continuous heating device, horizontal heating device, as shown in
A known device such as a rotary kiln type heating device is used.
【0010】本発明において、加圧成形時の圧力は特に
限定されないが、例えば10〜30Mpaが好ましい。
本発明においては、飛灰中の水硬系成分を利用して成形
固化することができるので、セメント等の固化剤を用い
る必要はない。In the present invention, the pressure at the time of pressure molding is not particularly limited, but is preferably, for example, 10 to 30 Mpa.
In the present invention, it is not necessary to use a solidifying agent such as cement, because the molding and solidification can be performed using the hydraulic component in the fly ash.
【0011】[0011]
【実施例】次に、本発明を実施例によってさらに詳細に
説明する。 実施例1 表1に示す組成の流動床式都市ごみ焼却飛灰を図5に示
した竪型連続加熱装置を用い、450℃で10分間加熱
した後、重金属固定剤としてキレート剤を1〜5重量%
と、水を10重量%添加して5分間混練し、次いで圧縮
成形器を用いて30Mpaで圧縮成形して飛灰成形物を
得た。Next, the present invention will be described in more detail by way of examples. Example 1 Fluid-bed municipal solid waste incineration fly ash having the composition shown in Table 1 was heated at 450 ° C. for 10 minutes using the vertical continuous heating apparatus shown in FIG. 5, and then 1 to 5 chelating agents were used as heavy metal fixing agents. weight%
And 10% by weight of water and kneaded for 5 minutes, and then compression molded at 30 MPa using a compression molding machine to obtain a fly ash molded product.
【0012】[0012]
【表1】 実施例2 圧縮成形しなかったこと(混練のみ)以外は上記実施例
1と同様にして同様の飛灰混練物を得た。[Table 1] Example 2 The same fly ash kneaded material was obtained in the same manner as in Example 1 except that compression molding was not performed (only kneading).
【0013】比較例1 加熱処理しない以外は上記実施例2と同様にして同様の
飛灰混練物を得た。実施例1〜2および比較例1で得ら
れた飛灰成形物をそれぞれ100g採取し、純水に塩酸
を加えpH5.8〜6.3に調整した溶媒を用いて環境
庁告示第13号に準じて6時間振とうして溶出試験を行
い、溶媒中に溶出したPbを定量した。結果を図4に示
す。Comparative Example 1 The same fly ash mixture was obtained in the same manner as in Example 2 except that no heat treatment was performed. 100 g of each of the fly ash molded products obtained in Examples 1 and 2 and Comparative Example 1 was collected, and hydrochloric acid was added to pure water to adjust the pH to 5.8 to 6.3. The dissolution test was performed by shaking for 6 hours according to the method, and Pb eluted in the solvent was quantified. FIG. 4 shows the results.
【0014】図において、薬剤処理に加えて、加熱処理
および圧縮成形した実施例1の飛灰成形物は鉛(Pb)
の溶出量が極めて少なく、Pb溶出量の目標値である
0.3mg/リットルをクリアするための重金属固定剤
の使用量はわずかに1%以下で良いことが分かる。ま
た、加熱処理し、圧縮成形しなかった実施例2の飛灰混
練物はPb溶出量の基準値を達成するのに1〜2%の重
金属固定剤が必要であった。一方、加熱処理および圧縮
成形のいずれも行わなかった従来の薬品処理法による比
較例1の飛灰混練物は前記基準値を達成するために3%
以上の重金属固定剤が必要であった。In the figure, the fly ash molded product of Example 1 which was subjected to heat treatment and compression molding in addition to chemical treatment was lead (Pb).
It can be seen that the amount of heavy metal fixing agent used to clear the target value of Pb elution amount of 0.3 mg / liter is only slightly less than 1%. Further, the fly ash kneaded product of Example 2 which was not subjected to the heat treatment and compression molding required 1-2% of the heavy metal fixing agent to achieve the reference value of the Pb elution amount. On the other hand, the fly ash kneaded material of Comparative Example 1 by the conventional chemical treatment method in which neither the heat treatment nor the compression molding was performed was 3% in order to achieve the reference value.
The above heavy metal fixing agent was required.
【0015】[0015]
【発明の効果】本願の請求項1記載の発明によれば、重
金属固定剤を添加する前の焼却灰をあらかじめ400〜
550℃で加熱処理することにより、外部からセメント
等の固化剤を添加することなく良好に成形、固化するこ
とができ、しかも重金属固定剤の使用量を低減しても飛
灰成形物における金属溶出量を効果的に減少して長時間
安定に重金属を閉じ込めることができる。また加熱処理
することにより、ダイオキシン等の有害な有機塩素化合
物を効果的に分解除去することもできる。According to the invention of claim 1 of the present application, the incinerated ash before adding the heavy metal fixing agent is 400 to 400 in advance.
By heat treatment at 550 ° C, it can be molded and solidified well without adding a solidifying agent such as cement from the outside, and even if the amount of heavy metal fixing agent used is reduced, metal elution in the fly ash molded product The amount can be effectively reduced to stably confine heavy metals for a long time. By performing the heat treatment, harmful organic chlorine compounds such as dioxin can be effectively decomposed and removed.
【0016】本願の請求項2記載の発明によれば、加熱
処理に加え、重金属固定剤を添加して混練した後、圧縮
成形したことにより重金属が物理的に閉じ込められるの
で、上記発明の効果に加え、より少ない重金属固定剤に
よって重金属を安定化することができる。According to the invention as set forth in claim 2 of the present application, in addition to the heat treatment, a heavy metal fixing agent is added and kneaded, followed by compression molding, whereby the heavy metal is physically confined. In addition, heavy metals can be stabilized with less heavy metal fixing agents.
【図1】本発明の原理を示す説明図。FIG. 1 is an explanatory view showing the principle of the present invention.
【図2】本発明の原理を示す説明図。FIG. 2 is an explanatory diagram showing the principle of the present invention.
【図3】本発明の処理フローを示す図。FIG. 3 is a diagram showing a processing flow of the present invention.
【図4】本発明における実施例の効果を示す図。FIG. 4 is a diagram showing the effect of the embodiment of the present invention.
【図5】、FIG.
【図6】、FIG.
【図7】本発明に用いられる加熱装置を示す図。FIG. 7 is a diagram showing a heating device used in the present invention.
───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) F23J 1/00 ──────────────────────────────────────────────────続 き Continued on front page (58) Field surveyed (Int.Cl. 7 , DB name) F23J 1/00
Claims (2)
し、前記焼却灰中の未燃カーボンの燃焼によって生じた
炭酸ガスと焼却灰中のアルカリ成分とを反応させた後、
該反応生成物に重金属固定剤と水を加えて混練し、成形
固化することを特徴とする焼却灰の処理方法。An incinerated ash is heated at 400 to 550 ° C. to react carbon dioxide gas generated by burning unburned carbon in the incinerated ash with an alkali component in the incinerated ash.
A method for treating incinerated ash, comprising adding a heavy metal fixing agent and water to the reaction product, kneading the mixture, and solidifying the mixture.
加圧成形することを特徴とする請求項1記載の焼却灰の
処理方法。2. After adding a heavy metal fixing agent and water and kneading,
2. The method for treating incinerated ash according to claim 1, wherein the incineration ash is formed by pressure molding.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10877795A JP3303251B2 (en) | 1995-05-02 | 1995-05-02 | How to treat incinerated ash |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10877795A JP3303251B2 (en) | 1995-05-02 | 1995-05-02 | How to treat incinerated ash |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH08303741A JPH08303741A (en) | 1996-11-22 |
| JP3303251B2 true JP3303251B2 (en) | 2002-07-15 |
Family
ID=14493219
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10877795A Expired - Fee Related JP3303251B2 (en) | 1995-05-02 | 1995-05-02 | How to treat incinerated ash |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3303251B2 (en) |
-
1995
- 1995-05-02 JP JP10877795A patent/JP3303251B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH08303741A (en) | 1996-11-22 |
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