JPH105715A - Treatment of heavy metal-containing ash - Google Patents

Treatment of heavy metal-containing ash

Info

Publication number
JPH105715A
JPH105715A JP8159779A JP15977996A JPH105715A JP H105715 A JPH105715 A JP H105715A JP 8159779 A JP8159779 A JP 8159779A JP 15977996 A JP15977996 A JP 15977996A JP H105715 A JPH105715 A JP H105715A
Authority
JP
Japan
Prior art keywords
ferrite
ash
heavy metal
kneaded
added
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.)
Withdrawn
Application number
JP8159779A
Other languages
Japanese (ja)
Inventor
Kenichi Nagai
健一 長井
Toshio Hama
利雄 濱
Naoko Hirata
直子 平田
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.)
Hitachi Zosen Corp
Original Assignee
Hitachi Zosen Corp
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 Hitachi Zosen Corp filed Critical Hitachi Zosen Corp
Priority to JP8159779A priority Critical patent/JPH105715A/en
Publication of JPH105715A publication Critical patent/JPH105715A/en
Withdrawn legal-status Critical Current

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  • Processing Of Solid Wastes (AREA)

Abstract

PROBLEM TO BE SOLVED: To surely stabilize heavy metals in ash even when the amts. of a chelating agent and a ferrite forming salt used are small. SOLUTION: Heavy metal-contg. ash is kneaded with water, a ferrite forming agent is added and they are kneaded at 50-100 deg.C. After ferrite formation reaction proceeds, a chelating agent is further added and they are kneaded. When the pH of the kneaded ash is <7 at the time of adding the ferrite forming agent, the pH is preferably adjusted to >=7 by adding alkali. The ferrite forming agent is preferably ferrous chloride and/or ferrous sulfate.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、都市ごみや産業廃
棄物などの固形廃棄物の焼却あるいは溶融処理によって
排出される焼却灰や、排ガス集塵灰等の重金属含有灰の
処理方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for treating incinerated ash discharged from incineration or melting of solid waste such as municipal solid waste and industrial waste, and ash containing heavy metals such as exhaust gas collection ash.

【0002】都市ごみの焼却処理設備から発生する排ガ
ス中のダストは、電気集塵機やバクフィルターで捕集さ
れている。この捕集ダストは飛散性に富み、六価クロム
鉛等の人体に有害な重金属を含んでいるので、これを取
扱いが便利な且つ有害金属が溶出しない形態のものに変
える必要がある。本発明はこのような重金属含有灰の処
理方法に関する。
[0002] Dust in exhaust gas generated from municipal solid waste incineration equipment is collected by an electric dust collector or a back filter. Since this collected dust is highly scattered and contains heavy metals harmful to the human body, such as lead hexavalent chromium, it is necessary to change this to a form that is convenient to handle and does not elute harmful metals. The present invention relates to a method for treating such heavy metal-containing ash.

【0003】[0003]

【従来の技術】従来、重金属含有灰の処理方法として
は、ごみ焼却処理設備における集塵装置で分離された集
塵ダストに所要量の水、キレート剤およびフェライト形
成塩を加えて混練し、pHおよび温度をフェライト形成
条件に設定することを特徴とするごみ焼却処理設備にお
けるダストの処理法が知られている(特開平7−757
66号公報参照)。
2. Description of the Related Art Conventionally, as a method for treating heavy metal-containing ash, a required amount of water, a chelating agent, and a ferrite-forming salt are added to a collected dust separated by a dust collector in a refuse incineration plant, and the mixture is kneaded. A method of treating dust in a refuse incineration plant characterized by setting the temperature and ferrite formation conditions is known (Japanese Patent Laid-Open No. 7-757).
No. 66).

【0004】[0004]

【発明が解決しようとする課題】しかしながら、重金属
含有灰中の重金属をキレート剤によって固定化する方法
では、特に集塵灰処理時に多量のキレート剤を使用しな
いと重金属の固定化が難しい。また、集塵ダストにキレ
ート剤とフェライト形成塩を同時に加えて重金属含有灰
を処理する方法では、フェライト形式塩の使用量を多く
しないと処理効果が低い。
However, in the method of immobilizing heavy metals in heavy metal-containing ash using a chelating agent, it is difficult to immobilize heavy metals unless a large amount of a chelating agent is used, especially during dust collection ash treatment. In addition, in the method of treating a heavy metal-containing ash by simultaneously adding a chelating agent and a ferrite-forming salt to dust collection dust, the treatment effect is low unless the amount of ferrite-type salt used is increased.

【0005】本発明の目的は、上記の点に鑑み、キレー
ト剤およびフェライト形成塩の使用量が少なくても、灰
中の重金属を確実に処理することができる重金属含有灰
の処理方法を提供することにある。
[0005] In view of the above, an object of the present invention is to provide a method for treating heavy metal-containing ash which can reliably treat heavy metals in ash even when the amounts of chelating agents and ferrite-forming salts used are small. It is in.

【0006】[0006]

【課題を解決するための手段】本発明による重金属含有
灰の処理方法は、重金属含有灰に水を加えて混練した
後、フェライト形成剤を加えて温度50℃〜100℃で
さらに混練して、フェライト化反応が進行した後にキレ
ート剤を加えて混練することを特徴とするものである。
According to the method for treating heavy metal-containing ash according to the present invention, water is added to the heavy metal-containing ash and kneaded, and then a ferrite forming agent is added and further kneaded at a temperature of 50 ° C to 100 ° C. It is characterized in that a chelating agent is added and kneaded after the ferrite-forming reaction proceeds.

【0007】本発明方法においては、フェライト形成剤
添加時のpHが7未満である場合に、さらにアルカリを
加えてフェライト形成剤を加えてpHを7以上にするこ
とが好ましい。アルカリとしては水酸化ナトリウム、水
酸化カルシウムなどがよく用いられる。
In the method of the present invention, when the pH at the time of adding the ferrite forming agent is less than 7, it is preferable to further add an alkali and add the ferrite forming agent to make the pH 7 or more. As the alkali, sodium hydroxide, calcium hydroxide and the like are often used.

【0008】好ましいフェライト形成剤は2価鉄化合物
である。
The preferred ferrite former is a ferrous compound.

【0009】[0009]

【発明の実施の形態】本発明方法で用いる薬剤の使用量
は、たとえば、重金属含有灰100重量部に対して水3
0〜50重量部、フェライト形成剤4〜15重量部(フ
ェライトを形成する重金属と等モル比以上であればよ
い)、キレート剤1〜5重量部である。
BEST MODE FOR CARRYING OUT THE INVENTION The amount of the chemical used in the method of the present invention is, for example, 100 parts by weight of heavy metal-containing ash and water
0 to 50 parts by weight, 4 to 15 parts by weight of ferrite-forming agent (the molar ratio should be at least equimolar to heavy metal forming ferrite), and 1 to 5 parts by weight of chelating agent.

【0010】フェライト形成剤添加後の混練温度は50
℃〜100℃、好ましくは65℃〜85℃の範囲であ
る。この温度が低すぎると、フェライト化反応が進行し
難く、逆に高過ぎると、水分の蒸発が激しくなり、いず
れの場合も好ましくない。
The kneading temperature after adding the ferrite forming agent is 50.
C. to 100.degree. C., preferably 65.degree. If the temperature is too low, the ferrite-forming reaction does not easily proceed, while if it is too high, the evaporation of water becomes severe, which is not preferable in any case.

【0011】フェライト形成剤としては、塩化第1鉄、
硫酸第1鉄のような2価鉄化合物が好ましい。これらは
単独で用いても組み合わせで用いても良い。
Ferrite forming agents include ferrous chloride,
Ferrous compounds such as ferrous sulfate are preferred. These may be used alone or in combination.

【0012】混練手段としては、複数のロッドを装入し
た振動式混練機あるいは2軸混練押出成形機を用いるの
が好ましい。
As the kneading means, it is preferable to use a vibratory kneader or a twin-screw kneading extruder in which a plurality of rods are loaded.

【0013】キレート剤の代表例としてはミヨシ油脂社
製の「エポルバ」が挙げられる。
A typical example of the chelating agent is "Epolva" manufactured by Miyoshi Oil & Fats Co., Ltd.

【0014】[0014]

【実施例】つぎに、本発明方法を実施例によって具体的
に説明する。
Next, the method of the present invention will be specifically described with reference to examples.

【0015】実施例1 都市ごみの焼却処理設備から発生する排ガス中のダスト
をバクフィルターで捕集した集塵灰A100gに水10
0gを加え、混合しながら70℃に昇温した。次にこの
混合物に硫酸第1鉄(FeSO4 として)を4g加え、
混合物に空気を1リットル/min通気して暴気しなが
ら2時間攪拌(300rpm)し、フェライト化反応を
させた。次にこの反応液にキレート剤を集塵灰100g
に対して1g添加し、5分間攪拌を継続した後、沈殿物
を1昼夜放置した。なお、捕集した集塵灰Aの重金属含
有量は、Pb=0.39重量%、Zn=1.35重量
%、T−Cr=150mg/kg、Cd=120mg/
kg、T−Hg=8.4mg/kg、As=12mg/
kgであった。
Example 1 100 g of dust ash A obtained by collecting dust in flue gas generated from municipal solid waste incineration equipment with a back filter was added water 10
0 g was added and the temperature was raised to 70 ° C. while mixing. Next, 4 g of ferrous sulfate (as FeSO 4 ) was added to the mixture,
The mixture was stirred (300 rpm) for 2 hours while passing air through the mixture at 1 liter / min and violently to cause a ferrite-forming reaction. Next, a chelating agent was added to the reaction solution to collect 100 g of dust ash.
After stirring for 5 minutes, the precipitate was left for one day. The heavy metal content of the collected dust ash A was as follows: Pb = 0.39 wt%, Zn = 1.35 wt%, T-Cr = 150 mg / kg, Cd = 120 mg /
kg, T-Hg = 8.4 mg / kg, As = 12 mg / kg
kg.

【0016】実施例2〜4 キレート剤の使用量を集塵灰100gに対してそれぞれ
2、3、4gに変えた点を除いて、実施例1と同様の操
作を行った。
Examples 2 to 4 The same operation as in Example 1 was carried out except that the amount of the chelating agent was changed to 2, 3, and 4 g for 100 g of dust ash, respectively.

【0017】実施例5 集塵灰Aとは別の集塵灰B100gに水100gを加
え、混合しながら70℃に昇温した。次にこの混合物に
硫酸第1鉄(FeSO4 として)を4g加え、pHを7
に調整した後、混合物に空気を1リットル/min通気
して暴気しながら2時間攪拌(300rpm)し、フェ
ライト化反応をさせた。次にこの反応液にキレート剤を
集塵灰100gに対して2g添加し、5分間攪拌を継続
した後、沈殿物を1昼夜放置した。なお、捕集した集塵
灰Bの重金属含有量は、Pb=1.2重量%、Zn=
3.1重量%、T−Cr=340mg/kg、Cd=9
8mg/kg、T−Hg=1mg/kg、As=11m
g/kgであった。
Example 5 100 g of water was added to 100 g of dust ash B different from dust ash A, and the temperature was raised to 70 ° C. while mixing. Next, 4 g of ferrous sulfate (as FeSO 4 ) was added to the mixture and the pH was adjusted to 7
After the mixture was adjusted to 1, the mixture was stirred for 2 hours (300 rpm) while passing air at 1 liter / min and violently to allow a ferrite formation reaction. Next, 2 g of a chelating agent was added to 100 g of dust collection ash to the reaction solution, and stirring was continued for 5 minutes. The heavy metal content of the collected dust ash B was Pb = 1.2% by weight, Zn =
3.1% by weight, T-Cr = 340mg / kg, Cd = 9
8 mg / kg, T-Hg = 1 mg / kg, As = 11 m
g / kg.

【0018】比較例1 キレート剤を添加しなかった点を除いて、実施例1と同
様の操作を行った。
Comparative Example 1 The same operation as in Example 1 was performed except that no chelating agent was added.

【0019】比較例2 キレート剤を添加しなかった点を除いて、実施例5と同
様の操作を行った。
Comparative Example 2 The same operation as in Example 5 was performed except that no chelating agent was added.

【0020】比較例3〜6 硫酸第1鉄の添加を行わず、かつ、空気暴気下の攪拌を
行わなかった点を除いて、実施例1〜4と同様の操作を
行った。
Comparative Examples 3 to 6 The same operations as in Examples 1 to 4 were carried out except that ferrous sulfate was not added and stirring was not performed under air storm.

【0021】溶出テスト 実施例1〜5および比較例1〜6でそれぞれ得られた沈
殿物について、また、硫酸第1鉄もキレート剤も添加し
なかった場合の集塵灰A点について、重金属溶出テスト
を行った。テスト方法は環境庁告示第13号(アメリカ
TCL法)に従った。
Dissolution test The precipitates obtained in Examples 1 to 5 and Comparative examples 1 to 6 and the dust ash A point when neither ferrous sulfate nor a chelating agent was added were used to dissolve heavy metals. Tested. The test method followed the Notification of the Environment Agency No. 13 (TCL in the United States).

【0022】これらの溶出テスト結果を表1にまとめて
示す。
The results of these dissolution tests are summarized in Table 1.

【0023】[0023]

【表1】 表1から分かるように、実施例で得られた沈殿物の重金
属溶出量は、燃え殻、煤塵、汚泥の埋立処分に係る判定
基準値以下である。
[Table 1] As can be seen from Table 1, the amount of heavy metal eluted from the precipitate obtained in the example is equal to or less than the criterion value for landfill disposal of cinders, dust, and sludge.

【0024】[0024]

【発明の効果】本発明の集塵灰の処理法は、以上の如く
構成されているので、高価な試薬であるキレート剤およ
びフェライト形成塩の使用量が少なくても、灰中の重金
属を確実に処理することができて、経済的であり、ま
た、Hg2+をはじめとするフェライトになりにくい重金
属の固定化も可能である。しかも、従来の方法では困難
とされたpHが12以上の集塵灰をも支障なく処理する
ことができる。
As described above, the method for treating dust ash of the present invention is constructed as described above. Therefore, even if the amounts of expensive reagents such as chelating agents and ferrite forming salts are small, heavy metals in the ash can be reliably removed. It is economical and can fix Hg 2+ and other heavy metals that are unlikely to become ferrite. Moreover, it is possible to treat dust ash having a pH of 12 or more, which has been difficult with the conventional method, without any problem.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 重金属含有灰に水を加えて混練した後、
フェライト形成剤を加えて温度50℃〜100℃でさら
に混練して、フェライト化反応が進行した後にキレート
剤を加えて混練することを特徴とする重金属含有飛灰の
処理方法。
Claims 1. After adding and kneading water to a heavy metal-containing ash,
A method for treating heavy metal-containing fly ash, comprising adding a ferrite-forming agent, further kneading at a temperature of 50 ° C. to 100 ° C., and kneading by adding a chelating agent after the ferrite-forming reaction proceeds.
【請求項2】 フェライト形成剤添加時のpHが7未満
である場合には、さらにアルカリを加えてpHを7以上
にすることを特徴とする請求項1記載の重金属含有灰の
処理方法。
2. The method for treating heavy metal-containing ash according to claim 1, wherein when the pH at the time of adding the ferrite forming agent is less than 7, the pH is adjusted to 7 or more by further adding an alkali.
【請求項3】 フェライト形成剤が塩化第1鉄および/
または硫酸第1鉄である請求項1に記載の重金属含有灰
の処理方法。
3. The method of claim 1, wherein the ferrite forming agent is ferrous chloride and / or
The method for treating heavy metal-containing ash according to claim 1, wherein the method is ferrous sulfate.
JP8159779A 1996-06-20 1996-06-20 Treatment of heavy metal-containing ash Withdrawn JPH105715A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8159779A JPH105715A (en) 1996-06-20 1996-06-20 Treatment of heavy metal-containing ash

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8159779A JPH105715A (en) 1996-06-20 1996-06-20 Treatment of heavy metal-containing ash

Publications (1)

Publication Number Publication Date
JPH105715A true JPH105715A (en) 1998-01-13

Family

ID=15701088

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8159779A Withdrawn JPH105715A (en) 1996-06-20 1996-06-20 Treatment of heavy metal-containing ash

Country Status (1)

Country Link
JP (1) JPH105715A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11236548A (en) * 1998-02-19 1999-08-31 Miyoshi Oil & Fat Co Ltd Metal scavenger composition and metal scavenging method
CN109719110A (en) * 2017-10-27 2019-05-07 永清环保股份有限公司 A method of processing incineration of refuse flyash

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11236548A (en) * 1998-02-19 1999-08-31 Miyoshi Oil & Fat Co Ltd Metal scavenger composition and metal scavenging method
CN109719110A (en) * 2017-10-27 2019-05-07 永清环保股份有限公司 A method of processing incineration of refuse flyash

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