JPH07109533A - Method for recovering heavy metals in molten fly ash - Google Patents
Method for recovering heavy metals in molten fly ashInfo
- Publication number
- JPH07109533A JPH07109533A JP25353593A JP25353593A JPH07109533A JP H07109533 A JPH07109533 A JP H07109533A JP 25353593 A JP25353593 A JP 25353593A JP 25353593 A JP25353593 A JP 25353593A JP H07109533 A JPH07109533 A JP H07109533A
- Authority
- JP
- Japan
- Prior art keywords
- fly ash
- molten fly
- heavy metals
- suspension
- water
- 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
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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Processing Of Solid Wastes (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
(57)【要約】
【構成】 溶融炉から排出される溶融飛灰を処理槽に導
入して槽内の水に懸濁し、この懸濁液を酸またはアルカ
リの添加によりアルカリ域の適当値にpH調整した後、
生成した沈殿物を分離する。
【効果】 溶融飛灰中に含まれるZn,Pb,Cd,C
u等の重金属はpH10〜10.5で水酸化物として沈
殿するので、溶融飛灰からこのような有害な重金属を除
去回収できる。回収した重金属は、山元還元等における
金属原料として再利用できる。
(57) [Summary] [Structure] The molten fly ash discharged from the melting furnace is introduced into a treatment tank and suspended in water in the tank, and this suspension is adjusted to an appropriate value in the alkaline range by the addition of acid or alkali. After adjusting the pH
The precipitate formed is separated. [Effect] Zn, Pb, Cd, C contained in the molten fly ash
Since heavy metals such as u precipitate as hydroxides at a pH of 10 to 10.5, such harmful heavy metals can be removed and recovered from the molten fly ash. The recovered heavy metal can be reused as a metal raw material in Yamamoto reduction and the like.
Description
【0001】[0001]
【産業上の利用分野】本発明は、廃棄物等を溶融処理す
るときに発生する溶融飛灰中の重金属回収方法に関す
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for recovering heavy metals in molten fly ash generated when melting wastes and the like.
【0002】[0002]
【従来の技術】従来、重金属を含む廃水や溶融飛灰等の
ダストは、重金属処理が施されることにより重金属スラ
ッジとされ、セメント固化、薬剤によるキレート固定化
等の中間処理の後に埋立て処理されている。2. Description of the Related Art Conventionally, wastewater containing heavy metals and dust such as molten fly ash are treated as heavy metal sludge by being subjected to heavy metal treatment, and are then landfilled after intermediate treatment such as cement solidification and chelate fixation by chemicals. Has been done.
【0003】[0003]
【発明が解決しようとする課題】しかしながら、重金属
スラッジの中間処理としてセメント固化を行う場合、廃
棄物処理法における規制値以下とするためには、含まれ
る重金属の濃度に応じて数倍〜数十倍のセメント量が必
要となリ、埋立てる処理物の容積が増大する問題があ
る。また、セメント固化して埋立てても、酸性雨等の影
響により長期的には重金属が溶出する恐れがある。さら
に、キレート固定化する場合には、薬剤のコストが高
く、経済的に有利でない。However, when cement solidification is carried out as an intermediate treatment of heavy metal sludge, in order to keep it below the regulation value in the waste treatment method, several times to several tens of times are required depending on the concentration of heavy metal contained. There is a problem that the amount of cement required is doubled and the volume of the landfilled material increases. Even if the cement is solidified and landfilled, heavy metals may be eluted in the long term due to the influence of acid rain and the like. Further, when the chelate is immobilized, the cost of the drug is high and it is not economically advantageous.
【0004】本発明は上記問題を解決するもので、溶融
飛灰を処理するに際し、処理物の量を増大させることな
く経済的に有利な形で溶融飛灰中の重金属を除去回収で
きるようにすることを目的とするものである。The present invention solves the above problems, and when treating the molten fly ash, the heavy metal in the molten fly ash can be removed and recovered in an economically advantageous manner without increasing the amount of the treated material. The purpose is to do.
【0005】[0005]
【課題を解決するための手段】上記問題を解決するため
に本発明は、溶融炉から排出される溶融飛灰を処理槽に
導入して槽内の水に懸濁し、この懸濁液を酸またはアル
カリの添加によりアルカリ域の適当値にpH調整するこ
とによって溶融飛灰中の重金属を水酸化物として沈殿さ
せ、沈殿物を回収することを特徴とする。In order to solve the above problems, the present invention introduces molten fly ash discharged from a melting furnace into a treatment tank and suspends it in water in the tank. Alternatively, it is characterized in that the heavy metal in the molten fly ash is precipitated as a hydroxide by adjusting the pH to an appropriate value in the alkaline range by adding an alkali, and the precipitate is recovered.
【0006】また本発明は、溶融炉から排出される溶融
飛灰を処理槽に導入して槽内の水に懸濁し、この懸濁液
に水溶性硫化物を添加することによって溶融飛灰中の重
金属を硫化物として沈殿させ、沈殿物を回収することを
特徴とする。In the present invention, the molten fly ash discharged from the melting furnace is introduced into a treatment tank, suspended in water in the tank, and a water-soluble sulfide is added to this suspension to remove the molten fly ash. The heavy metal of (1) is precipitated as a sulfide, and the precipitate is recovered.
【0007】さらに本発明は、溶融炉から排出される溶
融飛灰を処理槽に導入して槽内の水に懸濁し、この懸濁
液を酸またはアルカリの添加によりアルカリ域の適当値
にpH調整した後、懸濁液に水溶性硫化物を添加するこ
とによって、溶融飛灰中の重金属を水酸化物および硫化
物として沈殿させ、沈殿物を回収することを特徴とす
る。Further, in the present invention, the molten fly ash discharged from the melting furnace is introduced into a treatment tank and suspended in water in the tank, and the suspension is adjusted to a suitable pH in the alkaline range by adding an acid or an alkali. After the adjustment, the water-soluble sulfide is added to the suspension to precipitate the heavy metal in the molten fly ash as hydroxide and sulfide, and the precipitate is recovered.
【0008】[0008]
【作用】上記構成によれば、溶融飛灰を回収して処理槽
内で水に懸濁し、この懸濁液を酸またはアルカリの添加
によりアルカリ域の適当値、10〜10.5にpH調整
することで、溶融飛灰中に通常塩化物の形態で含まれて
いるPb,Zn,Cd,Cuなどの重金属を、次式に示
したように水酸化物として沈殿させることができる。し
たがって、この沈殿物を回収することによって溶融飛灰
中の重金属を除去回収できる。According to the above construction, the molten fly ash is collected and suspended in water in the treatment tank, and the pH of this suspension is adjusted to an appropriate value in the alkaline range, 10 to 10.5, by adding an acid or an alkali. By doing so, heavy metals such as Pb, Zn, Cd, and Cu, which are usually contained in the molten fly ash in the form of chloride, can be precipitated as hydroxides as shown in the following formula. Therefore, the heavy metal in the molten fly ash can be removed and collected by collecting the precipitate.
【0009】[0009]
【化1】 懸濁液に水溶性硫化物を添加した場合は、溶融飛灰中の
重金属Mは次式に示したように硫化物として沈殿する。[Chemical 1] When the water-soluble sulfide is added to the suspension, the heavy metal M in the molten fly ash precipitates as sulfide as shown in the following equation.
【0010】[0010]
【化2】 また、懸濁液を酸またはアルカリの添加によりアルカリ
域の適当値にpH調整し、次に懸濁液に水溶性硫化物を
添加した場合は、溶融飛灰中の重金属Mは水酸化物およ
び硫化物として沈殿する。[Chemical 2] Further, when the pH of the suspension is adjusted to an appropriate value in the alkaline range by adding an acid or an alkali and then a water-soluble sulfide is added to the suspension, the heavy metal M in the molten fly ash is Precipitates as sulfide.
【0011】[0011]
【実施例】以下、本発明の実施例を図面に基づいて説明
する。図1は本発明の重金属回収方法が行われる処理装
置の全体構成を示した概略図であり、1は溶解槽、2は
第1の反応槽、3は第2の反応槽、4は沈殿槽である。Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a schematic diagram showing the overall configuration of a processing apparatus in which the heavy metal recovery method of the present invention is performed. 1 is a dissolution tank, 2 is a first reaction tank, 3 is a second reaction tank, and 4 is a precipitation tank. Is.
【0012】溶融炉から排出された溶融飛灰を溶解槽1
に投入して水と混合し、攪拌装置5で攪拌して、溶融飛
灰中に含まれる水溶性物質を水に十分溶解させる。得ら
れた懸濁液6を反応槽2に送り、pH計7でモニターし
つつ、かつ攪拌装置8で攪拌しながら、酸またはアルカ
リを添加してpH10〜10.5に調節する。すると、
懸濁液6中に水溶性物質すなわち重金属の塩化物などが
溶解しているため、重金属水酸化物の沈殿が生成する。The molten fly ash discharged from the melting furnace is melted into a tank 1.
And mixed with water and stirred by the stirrer 5 to sufficiently dissolve the water-soluble substance contained in the molten fly ash in water. The obtained suspension 6 is sent to the reaction tank 2, and while monitoring with the pH meter 7 and stirring with the stirrer 8, acid or alkali is added to adjust the pH to 10 to 10.5. Then,
Since a water-soluble substance, that is, a chloride of heavy metal, is dissolved in the suspension 6, a precipitate of heavy metal hydroxide is generated.
【0013】沈殿を含んだ懸濁液9を反応槽3に送り、
攪拌装置10で攪拌しながら水溶性硫化物としてのNa
HS水溶液を添加する。同時に、pH計11でモニター
しながら、反応槽3内の懸濁液12のpHを10〜1
0.5に維持する。これによって、懸濁液12中に含ま
れている未反応の重金属がNaHSと反応し、重金属硫
化物の沈殿が生成する。The suspension 9 containing the precipitate is sent to the reaction tank 3,
Na as a water-soluble sulfide while stirring with a stirrer 10.
Add aqueous HS solution. At the same time, while monitoring with the pH meter 11, the pH of the suspension 12 in the reaction tank 3 is 10 to 1
Keep at 0.5. As a result, the unreacted heavy metal contained in the suspension 12 reacts with NaHS to generate a heavy metal sulfide precipitate.
【0014】沈殿を含んだ懸濁液12を沈殿槽4に送
り、重金属水酸化物と重金属硫化物からなる沈殿物13
と上澄水14とに分離する。上記のようにして処理する
ことにより、有害な重金属を沈殿物13として分離除去
して溶融飛灰を無害化できる。沈殿物13は、溶融飛灰
中の重金属が濃縮された状態となっているので、山元還
元等における重金属原料として利用できる。The suspension 12 containing the precipitate is sent to the settling tank 4, and a precipitate 13 composed of heavy metal hydroxide and heavy metal sulfide is formed.
And supernatant water 14 are separated. By processing as described above, harmful heavy metals can be separated and removed as the precipitate 13 to render the molten fly ash harmless. Since the heavy metal in the molten fly ash is concentrated, the precipitate 13 can be used as a heavy metal raw material in Yamamoto reduction or the like.
【0015】上記の構成に代えて、反応槽2において重
金属水酸化物の沈殿を生成させた後に、同じ槽2で重金
属硫化物の沈殿を生成させる構成としてもよいし、反応
槽2において懸濁液9から重金属水酸化物の沈殿を取り
出すか、または、懸濁液6を反応槽2に通すことなく反
応槽3に送り、反応槽3において懸濁液12から重金属
硫化物の沈殿を取り出す構成としてもよい。水溶性硫化
物としてのNaHsに代えて、Cas、Na2 Sなどを
用いてもよい。Instead of the above structure, the heavy metal hydroxide may be precipitated in the reaction tank 2 and then the heavy metal sulfide may be precipitated in the same tank 2, or the heavy metal sulfide may be suspended in the reaction tank 2. A configuration in which the precipitation of heavy metal hydroxide is taken out from the liquid 9 or the suspension 6 is sent to the reaction tank 3 without passing through the reaction tank 2 and the precipitation of heavy metal sulfide is taken out from the suspension 12 in the reaction tank 3. May be Instead of NaHs as the water-soluble sulfide, Cas, Na 2 S, etc. may be used.
【0016】以下、溶融飛灰から重金属を回収する具体
例を示す。この例は小規模な処理を示したものであっ
て、溶融飛灰50gに水450mlを加えて30分間攪
拌し、この飛灰/水の懸濁液にNaHS(1.23g,
15%)を添加して1時間攪拌した後に濾過することに
よって、固形物(重金属スラッジ)およびろ液を回収し
た。下記の表1に示した分析結果からわかるように、重
金属は固形物中に、その他の成分はろ液中に含まれてお
り、両者はほぼ完全に分離されている。このときの固形
物中の重金属含有率は、Pb10.8%,Zn26.3
%,Cd0.35%,Cu1.89%であり、溶融飛灰
に比して10〜12倍に濃縮されている。これは焼却飛
灰に比べて100倍の濃縮に相当するので、分離した固
形物は非鉄金属原料として十分再利用できる状態と言え
る。なお、表2は溶融飛灰の成分の一例である。A specific example of recovering heavy metals from molten fly ash will be shown below. This example shows a small-scale treatment, in which 450 ml of water was added to 50 g of molten fly ash and stirred for 30 minutes, and NaHS (1.23 g,
15%) was added, and the mixture was stirred for 1 hour and then filtered to recover a solid matter (heavy metal sludge) and a filtrate. As can be seen from the analysis results shown in Table 1 below, the heavy metal is contained in the solid matter and the other components are contained in the filtrate, and the two are almost completely separated. The heavy metal content in the solid at this time was Pb 10.8%, Zn 26.3
%, Cd 0.35%, Cu 1.89%, and is 10 to 12 times more concentrated than the molten fly ash. This corresponds to a 100-fold concentration compared to incinerated fly ash, so it can be said that the separated solid matter can be sufficiently reused as a non-ferrous metal raw material. Table 2 is an example of the components of the molten fly ash.
【0017】[0017]
【表1】 [Table 1]
【0018】[0018]
【表2】 [Table 2]
【0019】[0019]
【発明の効果】以上のように本発明によれば、溶融飛灰
を捕集して水に懸濁し、この懸濁液を酸またはアルカリ
の添加によりアルカリ域の適当値にpH調整し、溶融飛
灰中の重金属を水酸化物として沈殿させることによっ
て、有害な重金属を分離除去して溶融飛灰を無害化でき
るとともに、分離した重金属を山元還元することで重金
属の再利用を図ることができる。As described above, according to the present invention, the molten fly ash is collected and suspended in water, and the pH of this suspension is adjusted to an appropriate value in the alkaline range by adding an acid or an alkali, and the molten fly ash is melted. By precipitating heavy metals in fly ash as hydroxides, harmful heavy metals can be separated and removed to render molten fly ash harmless, and the heavy metals can be reused by reducing the separated heavy metals. .
【0020】また、懸濁液に水溶性硫化物を添加し、溶
融飛灰中の重金属を硫化物として沈殿させることによっ
ても、溶融飛灰から重金属を除去回収できる。また、懸
濁液を酸またはアルカリの添加によりアルカリ域の適当
値にpH調整した後に、懸濁液に水溶性硫化物を添加
し、溶融飛灰中の重金属を水酸化物および硫化物として
沈殿させることによっても、溶融飛灰から重金属を除去
回収できる。The heavy metal can be removed and recovered from the molten fly ash by adding a water-soluble sulfide to the suspension and precipitating the heavy metal in the molten fly ash as a sulfide. After adjusting the pH of the suspension to an appropriate value in the alkaline range by adding acid or alkali, add water-soluble sulfide to the suspension and precipitate the heavy metals in the molten fly ash as hydroxides and sulfides. The heavy metal can be removed and recovered from the molten fly ash also by the above.
【図1】本発明の重金属回収方法が行われる処理装置の
構成を示した概略図である。FIG. 1 is a schematic diagram showing a configuration of a processing apparatus in which a heavy metal recovery method of the present invention is performed.
1 溶解槽 2 第1の反応槽 3 第2の反応槽 4 沈殿槽 9 懸濁液 12 懸濁液 13 沈殿物 1 Dissolution tank 2 1st reaction tank 3 2nd reaction tank 4 Precipitation tank 9 Suspension 12 Suspension 13 Precipitate
Claims (3)
に導入して槽内の水に懸濁し、この懸濁液を酸またはア
ルカリの添加によりアルカリ域の適当値にpH調整する
ことによって溶融飛灰中の重金属を水酸化物として沈殿
させ、沈殿物を回収することを特徴とする溶融飛灰中の
重金属回収方法。1. A method in which molten fly ash discharged from a melting furnace is introduced into a treatment tank and suspended in water in the tank, and the pH of the suspension is adjusted to an appropriate value in an alkaline region by adding an acid or an alkali. A method for recovering heavy metals in molten fly ash, characterized in that heavy metals in the molten fly ash are precipitated as hydroxides and the precipitate is recovered.
に導入して槽内の水に懸濁し、この懸濁液に水溶性硫化
物を添加することによって溶融飛灰中の重金属を硫化物
として沈殿させ、沈殿物を回収することを特徴とする溶
融飛灰中の重金属回収方法。2. The heavy fly ash discharged from the melting furnace is introduced into a treatment tank, suspended in water in the tank, and a water-soluble sulfide is added to this suspension to remove heavy metals in the molten fly ash. A method for recovering heavy metals in molten fly ash, which comprises precipitating as sulfide and recovering the precipitate.
に導入して槽内の水に懸濁し、この懸濁液を酸またはア
ルカリの添加によりアルカリ域の適当値にpH調整した
後、懸濁液に水溶性硫化物を添加することによって、溶
融飛灰中の重金属を水酸化物および硫化物として沈殿さ
せ、沈殿物を回収することを特徴とする溶融飛灰中の重
金属回収方法。3. The molten fly ash discharged from the melting furnace is introduced into a treatment tank and suspended in water in the tank, and the pH of the suspension is adjusted to an appropriate value in an alkaline range by adding an acid or an alkali. , A method for recovering heavy metals in molten fly ash, characterized in that heavy metals in the molten fly ash are precipitated as hydroxides and sulfides by adding a water-soluble sulfide to the suspension, and the precipitates are recovered. .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP25353593A JPH07109533A (en) | 1993-10-12 | 1993-10-12 | Method for recovering heavy metals in molten fly ash |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP25353593A JPH07109533A (en) | 1993-10-12 | 1993-10-12 | Method for recovering heavy metals in molten fly ash |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH07109533A true JPH07109533A (en) | 1995-04-25 |
Family
ID=17252725
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP25353593A Pending JPH07109533A (en) | 1993-10-12 | 1993-10-12 | Method for recovering heavy metals in molten fly ash |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH07109533A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2423514A (en) * | 2005-07-01 | 2006-08-30 | Future Ind Services Ltd | A method of treating waste ash |
| JP2008062169A (en) * | 2006-09-07 | 2008-03-21 | Taiheiyo Cement Corp | Processing method and processing system for fine powder containing calcium component and lead component |
| JP2008284522A (en) * | 2007-05-21 | 2008-11-27 | Nippon Steel Engineering Co Ltd | Fly ash treatment method |
| JP2017160496A (en) * | 2016-03-10 | 2017-09-14 | 住友金属鉱山株式会社 | Wastewater treatment method |
| JP2021146249A (en) * | 2020-03-17 | 2021-09-27 | 太平洋セメント株式会社 | Water washing method and water washing system for chlorine-containing powder |
-
1993
- 1993-10-12 JP JP25353593A patent/JPH07109533A/en active Pending
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2423514A (en) * | 2005-07-01 | 2006-08-30 | Future Ind Services Ltd | A method of treating waste ash |
| JP2008062169A (en) * | 2006-09-07 | 2008-03-21 | Taiheiyo Cement Corp | Processing method and processing system for fine powder containing calcium component and lead component |
| JP2008284522A (en) * | 2007-05-21 | 2008-11-27 | Nippon Steel Engineering Co Ltd | Fly ash treatment method |
| JP2017160496A (en) * | 2016-03-10 | 2017-09-14 | 住友金属鉱山株式会社 | Wastewater treatment method |
| JP2021146249A (en) * | 2020-03-17 | 2021-09-27 | 太平洋セメント株式会社 | Water washing method and water washing system for chlorine-containing powder |
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