JP3176162B2 - Treatment method for heavy metal-containing materials - Google Patents

Treatment method for heavy metal-containing materials

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Publication number
JP3176162B2
JP3176162B2 JP03345893A JP3345893A JP3176162B2 JP 3176162 B2 JP3176162 B2 JP 3176162B2 JP 03345893 A JP03345893 A JP 03345893A JP 3345893 A JP3345893 A JP 3345893A JP 3176162 B2 JP3176162 B2 JP 3176162B2
Authority
JP
Japan
Prior art keywords
heavy metal
ash
ferrite
mixture
treatment method
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
Application number
JP03345893A
Other languages
Japanese (ja)
Other versions
JPH06246255A (en
Inventor
誠 北野
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.)
Nippon Steel Corp
Original Assignee
Nippon Steel 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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP03345893A priority Critical patent/JP3176162B2/en
Publication of JPH06246255A publication Critical patent/JPH06246255A/en
Application granted granted Critical
Publication of JP3176162B2 publication Critical patent/JP3176162B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Fire-Extinguishing Compositions (AREA)
  • Processing Of Solid Wastes (AREA)

Description

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

【0001】[0001]

【産業上の利用分野】この発明は、都市ごみ,産業廃棄
物などの固型廃棄物の焼却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及びその他産業で発
生する重金属含有廃棄物の処理方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to incinerated ash discharged from incineration of solid waste such as municipal waste and industrial waste, heavy metal-containing ash such as exhaust gas dust ash, and heavy metal-containing ash generated in other industries. The present invention relates to a method for treating waste.

【0002】[0002]

【従来の技術】都市ごみや産業廃棄物排出量の増加と焼
却率の増加に伴い、焼却廃棄物である焼却灰や灰ガス集
塵灰の発生量が増え、その中に含まれる重金属が新しい
環境汚染源として注目を集めている。これら灰廃棄物の
うち、特に排ガス集塵灰は、水銀,亜鉛,鉛等の低沸点
重金属を多く含有し、これらが環境に放出された場合、
雨水等に溶解し溶出するため、その防止技術が開発され
てきた。
2. Description of the Related Art With an increase in the amount of municipal solid waste and industrial waste and an increase in the incineration rate, the amount of incinerated ash and ash gas dust ashes, which are incinerated waste, has increased, and heavy metals contained therein have become new. It is attracting attention as a source of environmental pollution. Among these ash wastes, exhaust gas dust ash, in particular, contains a large amount of low-boiling heavy metals such as mercury, zinc, and lead, and when these are released to the environment,
In order to dissolve and elute in rainwater and the like, prevention techniques have been developed.

【0003】例えば、特公昭61−47154号公報に
は、重金属を含有する廃棄物灰に、鉄塩の存在の下でア
ルカリ成分を加えて混合し、この混合物を造粒あるいは
静置状態で300℃以下に保持することによって、重金
属を鉄塩との混合水酸化物として固定することが開示さ
れている。
[0003] For example, Japanese Patent Publication No. 61-47154 discloses a waste ash containing a heavy metal to which an alkali component is added in the presence of an iron salt and mixed, and the mixture is granulated or allowed to stand for 300 minutes. It is disclosed that the heavy metal is fixed as a mixed hydroxide with an iron salt by keeping the temperature at not more than ° C.

【0004】これによって、灰中の重金属は相当割合固
定されて、安全な投棄が可能になるという利点があると
している。
[0004] It is said that this has the advantage that the heavy metals in the ash are fixed to a considerable extent, enabling safe dumping.

【0005】しかしながら、この重金属の固定法は、ア
ルカリを灰に直接添加して混合するものであるので、該
処理のために高価なアルカリが必要であり、また、混合
が不充分であると部分的にpHが高くなり、pHが1
1.5超になると重金属が固定できなくなり、固定化の
効率が低下し、しかも、常温付近では2日間の処理時間
を要し、処理時間の長期化又は処理設備が膨大になると
いう欠点がある。
However, this method of fixing heavy metals involves directly adding an alkali to the ash and mixing the ash. Therefore, an expensive alkali is required for the treatment, and if the mixing is not sufficient, some alkalis are required. PH rises to pH 1
If it exceeds 1.5, heavy metals cannot be fixed, the efficiency of fixing decreases, and a processing time of about two days is required at around normal temperature, resulting in a drawback that the processing time is lengthened or the processing equipment becomes enormous. .

【0006】[0006]

【発明が解決しようとする課題】本発明が解決すべき課
題は、重金属を含有する廃棄物を鉄塩の存在下で炭酸ガ
スを用いて効率よく固定化する手段を提供することにあ
る。
SUMMARY OF THE INVENTION An object of the present invention is to provide a means for efficiently fixing heavy metal-containing waste using carbon dioxide in the presence of an iron salt.

【0007】[0007]

【課題を解決するための手段】前記の課題を解決するた
めに、本発明は、重金属含有物に水、2価鉄を加え、そ
の後該混合物中に燃焼排ガスを添加しながら加熱・撹拌
し、該混合物のpHを7.0〜11.5かつ温度を30
〜99℃にしてフェライトを生成させ、前記重金属含有
物中の重金属をフェライト中に固定化することを特徴と
する。
In order to solve the above problems SUMMARY OF THE INVENTION The present invention is, water containing heavy metals was divalent iron was added, followed the addition while heating and stirring the flue gases in the mixture
The pH of the mixture is 7.0 to 11.5 and the temperature is 30.
~ 99 ° C to produce ferrite, containing heavy metal
The method is characterized in that heavy metals in a product are fixed in ferrite .

【0008】フェライトとは、Mを重金属として表した
とき、化学式でMFe2 4 として示されるもので、本
発明におけるアッシュフェライト化処理とは、混合物中
の2価鉄がフェライトと言われる鉄酸化物の結晶格子を
形成して行く過程で、重金属が本来鉄の原子が占めるべ
き位置に鉄の代わりに取り込まれて固定化される処理を
意味する。
[0008] Ferrite is a compound represented by the chemical formula MFe 2 O 4 when M is represented as a heavy metal, and the ash ferrite-forming treatment in the present invention means that ferrous iron in a mixture is a ferrous oxide called ferrite. In the process of forming the crystal lattice of an object, it means a process in which heavy metal is taken in place of iron at the position where iron atoms should occupy and is fixed.

【0009】その反応式は、次のように表される。The reaction formula is represented as follows.

【0010】 中和反応:M2++2Fe2++6OH- →MFe2 (OH)6 (1) 酸化反応:MFe2 (OH)6 +1/2O2 →MFe2 4 +3H2 O(2) 上記反応式において、pHが7.0より小さいと、
(1)式の反応におけるOH- が不足してフェライト化
反応は進まない。また、混合物を攪拌しない場合には
(2)式におけるO2 が不足して、反応が進まない。
[0010] Neutralization reaction: M 2+ + 2Fe 2+ + 6OH → MFe 2 (OH) 6 (1) Oxidation reaction: MFe 2 (OH) 6 + / O 2 → MFe 2 O 4 + 3H 2 O (2) In the reaction formula, if the pH is less than 7.0,
(1) OH in the reaction of the formula - ferrite reaction does not proceed in short supply. When the mixture is not stirred, the reaction does not proceed because O 2 in the formula (2) is insufficient.

【0011】また、フェライト化反応では、混合物のp
Hを11.5以下にしなければ、重金属は可溶性イオン
の形態をとり、フェライトの中に取り込まれない。その
ため、混合物のpHが11.5を超える場合には、酸を
加えてpHを調整する必要がある。また、温度は30〜
99℃の範囲が好ましい。加熱温度の上限は、上記酸化
反応(2)式における酸素の水への溶解度が100℃以
上では殆ど零に近くなり、酸化反応が進まないため10
0℃未満にする必要がある。
In the ferrite-forming reaction, p
If H is not less than 11.5, the heavy metals will take the form of soluble ions and will not be incorporated into the ferrite. Therefore, when the pH of the mixture exceeds 11.5, it is necessary to adjust the pH by adding an acid. The temperature is 30 ~
A range of 99 ° C. is preferred. The upper limit of the heating temperature is almost zero when the solubility of oxygen in water in the above-mentioned oxidation reaction (2) is 100 ° C. or more.
It must be below 0 ° C.

【0012】本発明は、このpH調整用の酸として、排
ガス中の炭酸ガスを用いるものである。
In the present invention, carbon dioxide in exhaust gas is used as the acid for pH adjustment.

【0013】[0013]

【作用】重金属含有物と2価鉄と水との混合物中に炭酸
ガスを添加しながら攪拌・加熱することで、重金属は水
側へ溶出した後、炭酸ガスが水に溶解することでpHが
低下し、pHが7.0以上、11.5以下の状態で2価
鉄がフェライトと呼ばれる鉄酸化物の結晶格子を形成す
る過程で、重金属はこの結晶格子中に取り込まれて固定
化される。
[Function] By stirring and heating while adding carbon dioxide to a mixture of a heavy metal-containing substance, ferrous iron and water, the heavy metal elutes to the water side, and the pH is dissolved by dissolving the carbon dioxide in water. During the process in which ferrous iron forms a crystal lattice of iron oxide called ferrite at a pH of 7.0 or more and 11.5 or less, heavy metals are incorporated into the crystal lattice and fixed. .

【0014】[0014]

【実施例】本実施例は、処理灰と2価鉄と炭酸ガスとの
混合をリアクター内で行なう例を示す。
EXAMPLE 1 This example shows an example in which treated ash, ferrous iron and carbon dioxide are mixed in a reactor.

【0015】図1は、使用した処理設備の概要を示す。FIG. 1 shows an outline of the processing equipment used.

【0016】同図において、1は廃棄灰を処理するため
のリアクターであり、2は2価硫酸鉄を水溶液の状態で
収納したタンクであり、3はリアクター1に炭酸ガスを
含む排ガスを導入するための導入口、4は排気ファンを
示す。5はリアクター1を加熱するための加熱装置、6
はリアクター1内の攪拌機であって、外部のモータ7に
よって回転される。8は処理済灰の排出口である。9は
飛灰を集塵する集塵機、10は飛灰ホッパー、11は除
塵後の煙道、12は煙突を示す。
In FIG. 1, reference numeral 1 denotes a reactor for treating waste ash, 2 denotes a tank containing divalent iron sulfate in an aqueous solution state, and 3 denotes an exhaust gas containing carbon dioxide gas introduced into the reactor 1. And an inlet 4 for the exhaust fan. 5 is a heating device for heating the reactor 1, 6
Is a stirrer in the reactor 1 and is rotated by an external motor 7. Reference numeral 8 denotes a discharge port of the treated ash. 9 denotes a dust collector for collecting fly ash, 10 denotes a fly ash hopper, 11 denotes a flue after dust removal, and 12 denotes a chimney.

【0017】同図において、飛灰ホッパーから表2に示
す重金属を含有する集塵設備からの灰を1トン、リアク
ター1に導入した。この重金属含有灰に対し、タンク2
からの20%硫酸鉄(II)水溶液と重量比で15%にな
るように混合し、その後、この攪拌混合物に対して混合
物乾物重量1kg当たり10リットル/minの割合
で、煙道ダクトから炭酸ガス10%を含む排ガスを導入
し、混合物の温度を70℃に維持すると共に、攪拌機6
による攪拌を継続した。表1はこの処理を1時間継続し
た後の、かかる処理においての環境庁告示13号法に準
拠した溶出試験結果を示す。全ての重金属において、海
洋投棄基準以下であり、優れた結果を示した。
In the figure, 1 ton of ash from a dust collecting facility containing heavy metals shown in Table 2 was introduced into the reactor 1 from a fly ash hopper. Tank 2 for this heavy metal-containing ash
From the flue duct at a rate of 10 liters / min per 1 kg of dry matter of the mixture with respect to this stirred mixture. An exhaust gas containing 10% was introduced, the temperature of the mixture was maintained at 70 ° C., and a stirrer 6 was used.
Stirring was continued. Table 1 shows the results of the dissolution test based on the Law No. 13 of the Notification of the Environment Agency after the treatment was continued for one hour. All heavy metals were below the marine dumping standard and showed excellent results.

【0018】図2は、温度を70℃に維持して、所定時
間処理後の混合物のpHと鉛の溶出量の関係を示すもの
で、pHが7と11.5の範囲内で鉛は略完全に固定化
しているのが判る。また、pHが7未満、及び11.5
を超えたところで、溶出量は極端に増大することが判
る。
FIG. 2 shows the relationship between the pH of the mixture after the treatment for a predetermined time and the amount of lead eluted while maintaining the temperature at 70 ° C. When the pH is in the range of 7 and 11.5, lead is substantially eliminated. You can see that it is completely fixed. In addition, the pH is less than 7, and 11.5
It can be seen that the elution amount is extremely increased when the value exceeds.

【0019】[0019]

【表1】 [Table 1]

【表2】 [Table 2]

【0020】[0020]

【発明の効果】本発明により、以下の効果を奏すること
ができる。
According to the present invention, the following effects can be obtained.

【0021】(1)フェライト化反応において、pH調
整用の酸として排ガス中の炭酸ガスを用いることで、処
理コストを大幅に低減できる。
(1) In the ferrite-forming reaction, the use of carbon dioxide gas in the exhaust gas as the acid for adjusting the pH can greatly reduce the processing cost.

【0022】(2)pH調整時の中和反応が緩やかに進
行するため、反応熱の発生も緩やかとなり、塩化水素や
水素等鉱酸を用いる場合に発生する有毒ガスが発生しな
い。
(2) Since the neutralization reaction at the time of pH adjustment proceeds slowly, the heat of reaction also becomes moderate, and no toxic gas is generated when a mineral acid such as hydrogen chloride or hydrogen is used.

【0023】(3)排ガスの温度が150〜200℃で
あり、フェライト化に必要な熱源として使えるため、省
エネルギー的である。
(3) Since the temperature of the exhaust gas is 150 to 200 ° C. and can be used as a heat source required for ferrite formation, energy is saved.

【0024】(4)炭酸ガスを使い固定するため、煙突
から発生する炭酸ガスを低減できる。
(4) Since carbon dioxide is used and fixed, carbon dioxide generated from the chimney can be reduced.

【図面の簡単な説明】[Brief description of the drawings]

【図1】 本発明に適用できる処理設備の概要を示す。FIG. 1 shows an outline of a processing facility applicable to the present invention.

【図2】 処理物中のpHを変化させたときの灰中の鉛
の溶出量を示す。
FIG. 2 shows the elution amount of lead in ash when the pH in the treated material is changed.

【符号の説明】[Explanation of symbols]

1 リアクター 2 硫酸鉄タンク 3 排ガス導入口 4 排気ファン 5 加熱装置 6 攪拌機 7 モータ 8 灰排出口 9 集塵機 10 飛灰ホッパー 11 煙道 12 煙突 REFERENCE SIGNS LIST 1 reactor 2 iron sulfate tank 3 exhaust gas inlet 4 exhaust fan 5 heating device 6 stirrer 7 motor 8 ash outlet 9 dust collector 10 fly ash hopper 11 stack 12 chimney

フロントページの続き (58)調査した分野(Int.Cl.7,DB名) B09B 3/00 A62D 3/00 C02F 1/62 Continuation of front page (58) Field surveyed (Int. Cl. 7 , DB name) B09B 3/00 A62D 3/00 C02F 1/62

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】重金属含有物に水、2価鉄を加え、その後
該混合物中に燃焼排ガスを添加しながら加熱・撹拌し、
該混合物のpHを7.0〜11.5かつ温度を30〜9
9℃にしてフェライトを生成させ、前記重金属含有物中
の重金属をフェライト中に固定化することを特徴とする
重金属含有物の処理方法。
1. A water heavy metal inclusions, the divalent iron is added, followed by heating and stirring while adding the combustion exhaust gas in the mixture,
The pH of the mixture is 7.0-11.5 and the temperature is 30-9.
9 ° C. to produce ferrite,
A method for treating a heavy metal-containing material, wherein the heavy metal is fixed in ferrite .
JP03345893A 1993-02-23 1993-02-23 Treatment method for heavy metal-containing materials Expired - Fee Related JP3176162B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP03345893A JP3176162B2 (en) 1993-02-23 1993-02-23 Treatment method for heavy metal-containing materials

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP03345893A JP3176162B2 (en) 1993-02-23 1993-02-23 Treatment method for heavy metal-containing materials

Publications (2)

Publication Number Publication Date
JPH06246255A JPH06246255A (en) 1994-09-06
JP3176162B2 true JP3176162B2 (en) 2001-06-11

Family

ID=12387103

Family Applications (1)

Application Number Title Priority Date Filing Date
JP03345893A Expired - Fee Related JP3176162B2 (en) 1993-02-23 1993-02-23 Treatment method for heavy metal-containing materials

Country Status (1)

Country Link
JP (1) JP3176162B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009195791A (en) * 2008-02-20 2009-09-03 Oji Paper Co Ltd Treatment method of incineration ash

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53102273A (en) * 1977-02-17 1978-09-06 Sakai Chem Ind Co Ltd Treating method for powdery substance containing chromium

Also Published As

Publication number Publication date
JPH06246255A (en) 1994-09-06

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