JPH11216443A - Method of removing lead compound from incineration ash - Google Patents

Method of removing lead compound from incineration ash

Info

Publication number
JPH11216443A
JPH11216443A JP1726398A JP1726398A JPH11216443A JP H11216443 A JPH11216443 A JP H11216443A JP 1726398 A JP1726398 A JP 1726398A JP 1726398 A JP1726398 A JP 1726398A JP H11216443 A JPH11216443 A JP H11216443A
Authority
JP
Japan
Prior art keywords
incineration ash
incinerated ash
lead compound
ash
compound
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.)
Pending
Application number
JP1726398A
Other languages
Japanese (ja)
Inventor
Kaoru Masuda
薫 増田
Shigehisa Endo
茂寿 遠藤
Hiroyuki Iwata
博行 岩田
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.)
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
Agency of Industrial Science and Technology
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 Agency of Industrial Science and Technology filed Critical Agency of Industrial Science and Technology
Priority to JP1726398A priority Critical patent/JPH11216443A/en
Publication of JPH11216443A publication Critical patent/JPH11216443A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Abstract

PROBLEM TO BE SOLVED: To provide a method of removing efficiently a Pb compound in incineration ash at a low cost. SOLUTION: In a method of removing a Pb compound contained in incineration ash from it, the incineration ash is kept under an alkali hydrothermal condition, the Pb compound in the incineration ash is subjected to the alkali hydrothermal reaction, and the resultant is dissolved in an alkali aqueous solution.

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、焼却場から排出さ
れる焼却灰からそれに含まれる鉛化合物を効率よく除去
する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 efficiently removing lead compounds contained in incinerated ash discharged from an incineration plant.

【0002】[0002]

【従来の技術】重金属を含む焼却灰は年々増加の傾向に
あり、その処分・処理は主に埋立処分されているが、重
金属の溶出と残余埋立場な年々確実に減少しており新た
な対応が求められている。その他の処理・処分法として
コンクリート固化法、酸化燃焼法、高温プラズマ法およ
び溶融固化法等が行われているが、二次汚染やコストの
面から検討課題が多い。特に、焼却灰中に含まれる鉛化
合物は、その除去が困難であり、その鉛化合物を低コス
トで効率的に除去する方法の開発が望まれている。
2. Description of the Related Art Incinerated ash containing heavy metals is increasing year by year, and its disposal and disposal is mainly landfilled. Is required. Other methods of treatment and disposal include concrete solidification, oxidative combustion, high-temperature plasma, and melt solidification, but there are many issues to be studied in terms of secondary pollution and cost. In particular, it is difficult to remove a lead compound contained in incineration ash, and it is desired to develop a method for efficiently removing the lead compound at low cost.

【0003】[0003]

【発明が解決しようとする課題】本発明は、焼却灰中の
鉛化合物を低コストでかつ効率よく除去する方法を提供
することをその課題とする。
SUMMARY OF THE INVENTION An object of the present invention is to provide a method for efficiently and efficiently removing a lead compound from incinerated ash at low cost.

【0004】[0004]

【課題を解決するための手段】本発明者は、前記課題を
解決すべく鋭意研究を重ねた結果、本発明を完成するに
至った。即ち、本発明によれば、焼却灰からそれに含ま
れている鉛化合物を除去する方法において、該焼却灰を
アルカリ水熱条件下に保持し、該焼却灰中の鉛化合物を
アルカリ水熱反応させてアルカリ水溶液中に溶解させる
ことを特徴とする方法が提供される。
Means for Solving the Problems The inventors of the present invention have conducted intensive studies to solve the above-mentioned problems, and as a result, have completed the present invention. That is, according to the present invention, in the method for removing lead compounds contained in incinerated ash, the incinerated ash is maintained under alkaline hydrothermal conditions, and the lead compound in the incinerated ash is subjected to alkaline hydrothermal reaction. And dissolving it in an aqueous alkaline solution.

【0005】[0005]

【発明の実施の形態】本発明において被処理原料として
用いる焼却灰は、鉛化合物を含むものである。このよう
な焼却灰には、都市ゴミ焼却プラントから排出される焼
却灰等が包含される。焼却灰中の鉛化合物は、酸化鉛P
bO2等として存在し、その含有量は、通常、Pb金属
として、600〜4950mg/kg程度である。な
お、前記焼却灰には、通常の炉底焼却灰の他、焼却飛灰
も包含される。
BEST MODE FOR CARRYING OUT THE INVENTION The incinerated ash used as a raw material to be treated in the present invention contains a lead compound. Such incinerated ash includes incinerated ash discharged from a municipal waste incineration plant. The lead compound in the incinerated ash is lead oxide P
It is present as bO 2 and the like, and its content is usually about 600 to 4950 mg / kg as Pb metal. The incineration ash includes incineration fly ash in addition to ordinary furnace bottom incineration ash.

【0006】本発明においては、この焼却灰からそれに
含まれる鉛化合物を除去するために、焼却灰をアルカリ
水熱条件下に保持し、その焼却灰中の鉛化合物をアルカ
リ水熱反応させる。これにより、焼却灰中の鉛化合物
は、水溶性の水酸化鉛となってアルカリ水溶液中に溶解
し、焼却灰から除去される。アルカリ水熱条件は、耐圧
容器に、水と水酸化アルカリとを加え、高温、高圧に保
持することにより形成することができる。この場合の水
熱条件における温度は、473K以上、好ましくは50
0〜550Kであり、その圧力は、その温度における飽
和水蒸気圧以上、通常20Mpa以上である。耐圧容器
内は、必要に応じ、空気や不活性ガスで加圧することも
でき、これによって容器内の圧力を調節することができ
る。水酸化アルカリとしては、水酸化ナトリウムや水酸
化カリウムが用いられるが、水酸化ナトリウムの使用が
好ましい。水に対する水酸化アルカリの添加量は、水1
リットル当り、0.25〜2.0モル、好ましくは1.
0〜1.5モルの割合である。また、焼却灰の使用量
は、水1リットル当り、0.5〜3kg、好ましくは
1.0〜1.5kgの割合である。
In the present invention, in order to remove the lead compounds contained in the incinerated ash, the incinerated ash is maintained under alkaline hydrothermal conditions, and the lead compound in the incinerated ash is subjected to an alkaline hydrothermal reaction. As a result, the lead compound in the incineration ash becomes water-soluble lead hydroxide, dissolves in the alkaline aqueous solution, and is removed from the incineration ash. The alkaline hydrothermal condition can be formed by adding water and an alkali hydroxide to a pressure-resistant container, and maintaining the temperature at a high temperature and a high pressure. In this case, the temperature under hydrothermal conditions is 473K or more, preferably 50K or more.
0 to 550K, and the pressure is at least the saturated steam pressure at that temperature, usually at least 20 Mpa. The inside of the pressure-resistant container can be pressurized with air or an inert gas, if necessary, so that the pressure in the container can be adjusted. As the alkali hydroxide, sodium hydroxide or potassium hydroxide is used, but sodium hydroxide is preferably used. The amount of alkali hydroxide added to water is
0.25 to 2.0 mol per liter, preferably 1.
The ratio is 0 to 1.5 mol. The amount of incinerated ash used is 0.5 to 3 kg, preferably 1.0 to 1.5 kg, per liter of water.

【0007】本発明を実施する場合に必要とされるエネ
ルギーは、その焼却灰を排出する焼却プラント、例え
ば、都市ゴミ焼却プラントで発生する熱エネルギーを有
効利用することができる。これにより、焼却灰からの鉛
化合物の除去を低コストで行うことができる。
The energy required for carrying out the present invention can effectively utilize thermal energy generated in an incineration plant that discharges the incinerated ash, for example, a municipal waste incineration plant. This makes it possible to remove the lead compound from the incinerated ash at low cost.

【0008】本発明においては、焼却灰中の鉛化合物
は、水溶性の水酸化鉛として水中に溶解し、焼却灰から
除去される。この場合、他の重金属、たとえば、Zn
や、Ni、Al、Cd等が存在すると、それらの重金属
も水中に溶解除去される。水中に溶解した鉛及び他の重
金属は、従来公知の方法により水中から回収し、資源と
して再利用することができる。
In the present invention, the lead compound in the incinerated ash is dissolved in water as water-soluble lead hydroxide and removed from the incinerated ash. In this case, other heavy metals, for example, Zn
When Ni, Al, Cd, etc. are present, their heavy metals are also dissolved and removed in water. Lead and other heavy metals dissolved in water can be recovered from water by a conventionally known method and reused as resources.

【0009】[0009]

【実施例】次に本発明を実施例によりさらに詳細に説明
する。
Next, the present invention will be described in more detail with reference to examples.

【0010】実施例1 焼却灰として、ZnO:2508、PbO2:689.
1、NiO2:13.01、CdO:324.3、Mn
2:247.2、Fe23:2150、CuO:15
2.2、MgO:235.3、Na2O:2547、C
aO:3040(mg/kg)を含有するものを用い、
その10g、蒸留水245cc、水酸化ナトリウム1.
5molをオートクレーブ(耐圧力50MPa、耐熱温
度750k、内容積300cc)内に入れて、523k
まで昇温し、圧力を20MPaのアルカリ水熱条件で1
時間処理した。焼却灰中に含有されるPb化合物は、水
酸化アルカリの存在しない水熱条件(温度523k、圧
力20MPa)下での1時間処理ではほとんど除去され
なかった。これに対し、水酸化ナトリウムを0.25、
0.5、0.75、1.0、1.5molの範囲で加え
たアルカリ水熱条件下での1時間処理では、そのPb除
去率は、それぞれ、37%、55%、64%、78%、
87%となり、Pb化合物が除去されることが確認され
た。他の重金属除去率を示すと、水酸化ナトリウム1.
5モルを添加したアルカリ水熱条件下での1時間処理で
は、ZnO除去率:50%、NiO2除去率:84%、
CdO除去率:31%、MnO2除去率:32%、Fe2
3除去率:29%、CuO除去率:62%である。
Example 1 As incineration ash, ZnO: 2508, PbO 2 : 689.
1, NiO 2 : 13.01, CdO: 324.3, Mn
O 2 : 247.2, Fe 2 O 3 : 2150, CuO: 15
2.2, MgO: 235.3, Na 2 O: 2547, C
aO: 3040 (mg / kg) containing
10 g thereof, 245 cc of distilled water, and 1.
5 mol was put into an autoclave (withstand pressure 50 MPa, heat-resistant temperature 750 k, internal volume 300 cc) and 523 k
And the pressure was increased to 1 under alkaline water heat conditions of 20 MPa.
Time processed. The Pb compound contained in the incineration ash was hardly removed by the one-hour treatment under hydrothermal conditions (temperature: 523 k, pressure: 20 MPa) in the absence of alkali hydroxide. In contrast, 0.25 sodium hydroxide,
In 1 hour treatment under alkaline hydrothermal conditions added in the range of 0.5, 0.75, 1.0 and 1.5 mol, the Pb removal rates were 37%, 55%, 64% and 78%, respectively. %,
87%, and it was confirmed that the Pb compound was removed. Other heavy metal removal rates are shown as sodium hydroxide 1.
In 1 hour treatment under alkaline hydrothermal conditions to which 5 mol was added, ZnO removal rate: 50%, NiO 2 removal rate: 84%,
CdO removal rate: 31%, MnO 2 removal rate: 32%, Fe 2
O 3 removal rate: 29%, CuO removal rate: 62%.

【0011】[0011]

【発明の効果】本発明は、焼却場の廃熱を利用し、アル
カリ水熱状態を作り出すことで、焼却灰中に含まれるP
b化合物を含む重金属を除去出来る。また、酸化燃焼法
や高温プラズマのように多大のエネルギーや大型の設備
や装置等を必要とせず、簡易型で低コストで実施出来
る。
The present invention utilizes the waste heat of the incineration plant to create an alkaline hydrothermal state, thereby reducing the P contained in the incineration ash.
Heavy metals including the b compound can be removed. In addition, a large amount of energy and large-scale equipment and devices are not required unlike the oxidizing combustion method and the high-temperature plasma, so that the method can be performed simply and at low cost.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 焼却灰からそれに含まれる鉛化合物を除
去する方法において、該焼却灰をアルカリ水熱条件下に
保持し、該焼却灰中の鉛化合物をアルカリ水熱反応させ
てアルカリ水溶液中に溶解させることを特徴とする方
法。
1. A method for removing lead compounds contained in incinerated ash, wherein the incinerated ash is maintained under alkaline hydrothermal conditions, and the lead compound in the incinerated ash is subjected to alkaline hydrothermal reaction to form an alkaline aqueous solution. A method characterized by dissolving.
JP1726398A 1998-01-29 1998-01-29 Method of removing lead compound from incineration ash Pending JPH11216443A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1726398A JPH11216443A (en) 1998-01-29 1998-01-29 Method of removing lead compound from incineration ash

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1726398A JPH11216443A (en) 1998-01-29 1998-01-29 Method of removing lead compound from incineration ash

Publications (1)

Publication Number Publication Date
JPH11216443A true JPH11216443A (en) 1999-08-10

Family

ID=11939091

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1726398A Pending JPH11216443A (en) 1998-01-29 1998-01-29 Method of removing lead compound from incineration ash

Country Status (1)

Country Link
JP (1) JPH11216443A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006255501A (en) * 2005-03-15 2006-09-28 Mitsui Eng & Shipbuild Co Ltd Method of removing heavy metal in flying ash
JP2010059489A (en) * 2008-09-04 2010-03-18 Sumitomo Metal Mining Co Ltd Pressure adjustment method for autoclave

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006255501A (en) * 2005-03-15 2006-09-28 Mitsui Eng & Shipbuild Co Ltd Method of removing heavy metal in flying ash
JP2010059489A (en) * 2008-09-04 2010-03-18 Sumitomo Metal Mining Co Ltd Pressure adjustment method for autoclave

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