JPH0221311B2 - - Google Patents
Info
- Publication number
- JPH0221311B2 JPH0221311B2 JP57184998A JP18499882A JPH0221311B2 JP H0221311 B2 JPH0221311 B2 JP H0221311B2 JP 57184998 A JP57184998 A JP 57184998A JP 18499882 A JP18499882 A JP 18499882A JP H0221311 B2 JPH0221311 B2 JP H0221311B2
- Authority
- JP
- Japan
- Prior art keywords
- aqueous solution
- incinerator
- ash
- incinerator dust
- dust ash
- 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 - Lifetime
Links
Landscapes
- Processing Of Solid Wastes (AREA)
Description
<産業上の利用分野>
本発明は焼却炉集塵灰等の処理方法に関する。
都市ゴミや産業廃棄物更には汚泥の類等の各種
廃棄物類を焼却処理すると、焼却炉から飛散して
例えば電気集塵装置等で捕獲される焼却炉集塵灰
や、焼却炉中に残存する焼却灰が二次的に発生す
る。これらの焼却炉集塵灰等は、そのまま埋立等
で処分すると、該焼却炉集塵灰等に含まれること
のあるCd、Pb、Hg、Cr6+等の有害な重金属類が
溶出して、重大な二次公害を引き起こす恐れがあ
る。
本発明は、上記のような焼却炉集塵灰等に特定
の可溶性硫化物の水溶液又は水分散液と酸性水溶
液とを所定条件下に混練して該焼却炉集塵灰等に
含まれる有害物質を無害化する処理方法に関する
ものである。
<従来の技術、その問題点>
従来一般に、焼却炉集塵灰等にセメント又はア
スフアルト等を混練したり、或いはケイ酸類を加
えて焼結したりする処理方法が行なわれている。
ところが、これらの従来法には、前述の如き有
害な重金属類の溶出防止が不充分であるという基
本的欠陥に加え、セメントやアスフアルト等を多
量に混練する必要があるために埋立処分量が増加
するという問題点や、ケイ酸類を混合して高温焼
結するために非経済的であるという問題点があ
る。
ところで、既に本出願人は、製鋼ダストの処理
方法として、製鋼ダストに可溶性硫化物を添加混
練する方法、及びこれと共にアルカリ性物質を添
加混練する方法、更にはこれらを添加混練後に養
生する方法を提案している(特開昭54−118304)。
ところが、この従来法を焼却炉集塵灰等の処理
に用いると、相応にして効果は認められるもの
の、可溶性硫化物だけを添加混練する方法では前
述の如き有害な重金属類の溶出をほぼ完全に防止
する迄には至らず、また該可溶性硫化物とアルカ
リ性物質とを添加混練する方法ではPH10〜11以上
になつてしまうために該PHによる弊害が大きく、
更に養性する方法ではそれだけ手間がかかるとい
う問題点がある。
<発明が解決しようとする問題点、その解決手段
>
本発明は、叙上の如き従来の問題点を解決し
て、簡易且つ経済的に前述の如き有害な重金属類
の溶出をほぼ完全に防止することができる、焼却
炉集塵灰等の処理方法を提供するものである。
しかして本発明は、
焼却炉集塵灰等に、Na2Sn、K2So,CaSp、
(NH4)2Sq、NaHS、KHS、Ca(HS)2又は
(NH4)HS[但し、m、n、p、qはいずれも1
〜5の整数]から選ばれるアルカリ性で還元機能
を有する可溶性硫化物の水溶液又は水分散液と、
酸性水溶液とを添加混練して、PH8.0〜9.5に調整
することを特徴とする焼却炉集塵灰等の処理方法
に係わる。
本発明で使用される可溶性硫化物は、アルカリ
性で還元機能を有し、前述の範疇にある、アルカ
リ金属、アルカリ土類金属又はアンモニウムのモ
ノ若しくはポリ硫化物又は硫化水素物である。
焼却炉集塵灰等にかかる可溶性硫化物の水溶液
又は水分散液を添加混練すると、次式(可溶性硫
化物としてCaS4を使用する場合):
CaS4+O2+H2O→CaS2O3+H2S+S
にしたがつて発生するH2Sにより、焼却炉集塵灰
等に含まれることのある重金属(M=Cd、Pb、
Hg等)が次式:
H2S+M2+→MS↓+2H+
の如く金属硫化物(MS)となつて安定化し、ま
た6価クロムは次式:
CrO4 2-+4H2S→Cr3++4H2O+4S
CrO4 2-+4CaS2O3→Cr3++4CaSO4+4S
にしたがつて3価のクロムに還元されるととも
に、該3価のクロムがこの系のアルカリ性によつ
て水酸化物に変換されることにより安定化するも
のと考えられる。
本発明では、焼却炉集塵灰等に可溶性硫化物の
水溶液又は水分散液と、酸性水溶液とを添加混練
して、PH8.0〜9.5に調整する。焼却炉集塵灰等に
可溶性硫化物の水溶液又は水分散液を添加混練す
るだけでも、重金属類の溶出をある程度防止する
ことができるが、これと共に酸性水溶液を添加混
練してPH8.0〜9.5に調整すると、重金属類の溶出
をほぼ完全に防止することができる。かかる酸性
水溶液としては、同時にそれ自体の廃液処理をも
行なうために、2価の鉄イオンを含む鉄鋼酸洗廃
液を用いるのが有利である。
以下、本発明の構成及び効果をより具体的にす
るため、実施例等を挙げるが、本発明が該実施例
に限定されるというものではない。
<実施例>
第1表記載の成分組成の焼却炉集塵灰を処理対
象として、該焼却炉集塵灰100gに、第2表記載
の如く可溶性硫化物の水溶液と酸性水溶液とを添
加混練した後、PHと、Cd、Pb、Cr6+並びにT−
Hg(全水銀)の溶出量を測定した。結果を第2表
に示した。
尚、可溶性硫化物の水溶液としてはCaS4の27.5
重量%水溶液を使用した。また酸性水溶液として
は鉄鋼酸洗後の塩酸廃液であつて、FeCl2を24重
量%及び遊離HClを3重量%含有する塩酸廃液を
10ml使用した。そして溶出量の測定は環境庁告示
第13号(昭52.3.14改正・同第4号)にしたがつ
て行なつた。
<Industrial Application Field> The present invention relates to a method for treating incinerator dust ash, etc. When various types of waste such as municipal garbage, industrial waste, and even sludge are incinerated, incinerator dust ash, which is scattered from the incinerator and captured by an electrostatic precipitator, and remains in the incinerator. Incineration ash is generated secondary. If these incinerator dust ash, etc. are disposed of in a landfill, etc., harmful heavy metals such as Cd, Pb, Hg, Cr 6+ , etc. that may be contained in the incinerator dust ash, etc. will be eluted. There is a risk of causing serious secondary pollution. The present invention involves mixing an aqueous solution or aqueous dispersion of a specific soluble sulfide with an acidic aqueous solution under predetermined conditions in the incinerator ash, etc. to remove harmful substances contained in the incinerator ash, etc. The present invention relates to a treatment method for rendering harmless. <Prior art and its problems> Conventionally, a treatment method has generally been used in which incinerator dust ash is mixed with cement or asphalt, or silicic acid is added thereto and sintered. However, these conventional methods have the basic flaw that they do not sufficiently prevent the elution of harmful heavy metals as mentioned above, and the amount of waste disposed of in landfills has increased due to the need to mix large amounts of cement, asphalt, etc. There are also problems in that it is uneconomical because silicic acids are mixed and sintered at high temperatures. By the way, the present applicant has already proposed a method of adding and kneading soluble sulfide to steelmaking dust, a method of adding and kneading an alkaline substance together with this, and a method of curing these after addition and kneading, as methods for treating steelmaking dust. (Japanese Patent Application Laid-Open No. 118304, 1972). However, when this conventional method is used to treat incinerator dust ash, etc., although it is reasonably effective, the method of adding and kneading only soluble sulfides almost completely prevents the elution of harmful heavy metals as mentioned above. It cannot be prevented, and the method of adding and kneading the soluble sulfide and alkaline substance results in a pH of 10 to 11 or higher, so the adverse effects of the PH are significant.
Furthermore, there is a problem in that the method of cultivating the food requires more effort. <Problems to be Solved by the Invention and Means for Solving the Problems> The present invention solves the conventional problems as described above, and almost completely prevents the elution of harmful heavy metals as described above in a simple and economical manner. The present invention provides a method for processing incinerator dust ash, etc., which can Therefore, the present invention provides incinerator dust collection ash, etc. with Na 2 S n , K 2 So , CaS p ,
(NH 4 ) 2 S q , NaHS, KHS, Ca(HS) 2 or (NH 4 )HS [However, m, n, p, q are all 1
an aqueous solution or dispersion of an alkaline soluble sulfide having a reducing function selected from [an integer of ~5];
The present invention relates to a method for treating incinerator dust ash, etc., which is characterized by adjusting the pH to 8.0 to 9.5 by adding and kneading with an acidic aqueous solution. The soluble sulfides used in the present invention are mono- or polysulfides or hydrogen sulfides of alkali metals, alkaline earth metals or ammonium, which are alkaline and have a reducing function and are in the categories mentioned above. When an aqueous solution or aqueous dispersion of soluble sulfide from incinerator dust ash is added and kneaded, the following formula (when CaS 4 is used as the soluble sulfide): CaS 4 +O 2 +H 2 O→CaS 2 O 3 +H 2 S + S The H 2 S generated as a result of the reaction removes heavy metals (M = Cd, Pb,
Hg, etc.) becomes a metal sulfide (MS) and stabilizes as shown in the following formula: H 2 S + M 2+ →MS↓+2H + , and hexavalent chromium becomes stable as shown in the following formula: CrO 4 2- +4H 2 S→Cr 3+ +4H 2 O+4S CrO 4 2- +4CaS 2 O 3 →Cr 3+ +4CaSO 4 +4S is reduced to trivalent chromium, and the trivalent chromium is converted to hydroxide due to the alkalinity of this system. It is thought that this will stabilize the temperature. In the present invention, an aqueous solution or aqueous dispersion of a soluble sulfide and an acidic aqueous solution are added and kneaded to incinerator dust collection ash, etc., and the pH is adjusted to 8.0 to 9.5. Simply adding and kneading an aqueous solution or aqueous dispersion of soluble sulfide to incinerator dust ash, etc. can prevent the elution of heavy metals to some extent, but adding and kneading an acidic aqueous solution together with this can prevent the pH from 8.0 to 9.5. When adjusted to , it is possible to almost completely prevent the elution of heavy metals. As such an acidic aqueous solution, it is advantageous to use a steel pickling waste solution containing divalent iron ions in order to simultaneously treat the waste solution itself. Examples will be given below to make the structure and effects of the present invention more specific, but the present invention is not limited to these Examples. <Example> Incinerator dust collection ash having the composition shown in Table 1 was treated, and an aqueous solution of a soluble sulfide and an acidic aqueous solution as shown in Table 2 were added and kneaded to 100 g of the incinerator dust collection ash. After that, PH, Cd, Pb, Cr 6+ and T−
The amount of Hg (total mercury) eluted was measured. The results are shown in Table 2. In addition, as an aqueous solution of soluble sulfide, 27.5 of CaS 4
A wt% aqueous solution was used. In addition, as the acidic aqueous solution, we used hydrochloric acid waste solution after steel pickling, which contains 24% by weight of FeCl 2 and 3% by weight of free HCl.
I used 10ml. The amount of elution was measured in accordance with the Environment Agency Notification No. 13 (revised March 14, 1980, No. 4).
【表】【table】
【表】
<発明の効果>
第2表の結果からも明らかなように、以上説明
した本発明には、簡易且つ経済的な手段で焼却炉
集塵灰等からの有害な重金属類の溶出をほぼ完全
に防止することができるという効果がある。[Table] <Effects of the Invention> As is clear from the results in Table 2, the present invention described above has the ability to prevent the elution of harmful heavy metals from incinerator dust ash, etc. by simple and economical means. The effect is that it can be almost completely prevented.
Claims (1)
(NH4)2Sq、NaHS、KHS、Ca(HS)2又は
(NH4)HS[但し、m、n、p、qはいずれも1
〜5の整数]から選ばれるアルカリ性で還元機能
を有する可溶性硫化物の水溶液又は水分散液と、
酸性水溶液とを添加混練して、PH8.0〜9.5に調整
することを特徴とする焼却炉集塵灰等の処理方
法。 2 酸性水溶液が鉄鋼酸洗廃液である特許請求の
範囲第1項記載の焼却炉集塵灰等の処理方法。[Claims] 1. Na 2 S n , K 2 S o , CaS p , etc. in incinerator dust ash, etc.
(NH 4 ) 2 S q , NaHS, KHS, Ca(HS) 2 or (NH 4 )HS [However, m, n, p, q are all 1
an aqueous solution or dispersion of an alkaline soluble sulfide having a reducing function selected from [an integer of ~5];
A method for treating incinerator dust ash, etc., which comprises adding and kneading an acidic aqueous solution to adjust the pH to 8.0 to 9.5. 2. The method for treating incinerator dust ash, etc. according to claim 1, wherein the acidic aqueous solution is a steel pickling waste liquid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57184998A JPS5973091A (en) | 1982-10-20 | 1982-10-20 | Treatment of ash generated in incinerator from collected dust etc. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57184998A JPS5973091A (en) | 1982-10-20 | 1982-10-20 | Treatment of ash generated in incinerator from collected dust etc. |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5973091A JPS5973091A (en) | 1984-04-25 |
| JPH0221311B2 true JPH0221311B2 (en) | 1990-05-14 |
Family
ID=16162989
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57184998A Granted JPS5973091A (en) | 1982-10-20 | 1982-10-20 | Treatment of ash generated in incinerator from collected dust etc. |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5973091A (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63111990A (en) * | 1986-10-29 | 1988-05-17 | Nkk Corp | Treatment for stabilizing heavy metals in flying cinder of refuse incineration |
| JPH026889A (en) * | 1988-06-27 | 1990-01-11 | Hitachi Zosen Corp | Treatment for making fly ash harmless |
| JP2736097B2 (en) * | 1989-02-01 | 1998-04-02 | 甲陽化成株式会社 | Detoxification method of industrial waste containing hazardous heavy metals |
| FR2694710B1 (en) * | 1992-08-14 | 1994-11-04 | Secomi | Process for neutralizing heavy metals contained in waste incineration residues. |
| JP4043411B2 (en) * | 2003-06-30 | 2008-02-06 | 株式会社クボタ | Method and apparatus for insolubilizing ash containing heavy metals |
| JP2016022406A (en) * | 2014-07-17 | 2016-02-08 | 株式会社ワールド・リンク | Method for treating heavy metal-contaminated water |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS581637B2 (en) * | 1978-03-08 | 1983-01-12 | 大同特殊鋼株式会社 | Processing method for steelmaking dust |
| JPS595358B2 (en) * | 1981-10-19 | 1984-02-03 | 日本流通株式会社 | Methods and agents for detoxifying industrial waste containing hazardous substances such as heavy metals |
-
1982
- 1982-10-20 JP JP57184998A patent/JPS5973091A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5973091A (en) | 1984-04-25 |
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