JP3392293B2 - Neutral fly ash treatment method - Google Patents

Neutral fly ash treatment method

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Publication number
JP3392293B2
JP3392293B2 JP15076196A JP15076196A JP3392293B2 JP 3392293 B2 JP3392293 B2 JP 3392293B2 JP 15076196 A JP15076196 A JP 15076196A JP 15076196 A JP15076196 A JP 15076196A JP 3392293 B2 JP3392293 B2 JP 3392293B2
Authority
JP
Japan
Prior art keywords
fly ash
ash
neutral fly
neutral
weight
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
Application number
JP15076196A
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Japanese (ja)
Other versions
JPH09327680A (en
Inventor
幹夫 井手
千嗣 北畠
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.)
Unitika Ltd
Original Assignee
Unitika Ltd
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Filing date
Publication date
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Priority to JP15076196A priority Critical patent/JP3392293B2/en
Publication of JPH09327680A publication Critical patent/JPH09327680A/en
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Publication of JP3392293B2 publication Critical patent/JP3392293B2/en
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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、ゴミ焼却場等の焼
却プラント、溶融プラントから排ガスとともに排出され
る中性飛灰に含まれる重金属の溶出を抑制することので
きる中性飛灰の処理方法に関するものである。
TECHNICAL FIELD The present invention relates to a method for treating neutral fly ash capable of suppressing the elution of heavy metals contained in the neutral fly ash discharged together with the exhaust gas from an incineration plant such as a refuse incinerator or a melting plant. It is about.

【0002】[0002]

【従来の技術】中性飛灰には、身体に有毒な水銀、鉛、
クロム、カドミウム等の重金属が多量に含まれているの
で、これらの重金属の溶出を抑制することが必要であ
る。従来、重金属の溶出を抑制する方法としては、中性
飛灰に水と重金属固定剤であるリン酸化合物とを添加、
混練してpH6〜12の範囲に調整する方法(特開平7
−155725号公報参照)や、中性飛灰に水と水酸化
カルシウム、水酸化ナトリウム等のpH調整剤とを添
加、混練した後に、重金属固定剤を添加、混練する方法
等が行われている。
2. Description of the Prior Art Neutral fly ash contains mercury, lead,
Since heavy metals such as chromium and cadmium are contained in large amounts, it is necessary to suppress the elution of these heavy metals. Conventionally, as a method for suppressing the elution of heavy metals, water and a phosphate compound which is a heavy metal fixing agent are added to neutral fly ash,
Method of kneading to adjust pH to the range of 6 to 12
No. 155725) or water and a pH adjusting agent such as calcium hydroxide or sodium hydroxide to neutral fly ash, and then kneading, followed by addition of a heavy metal fixing agent and kneading. .

【0003】[0003]

【発明が解決しようとする課題】しかし、中性飛灰を水
と重金属固定剤のみで処理する方法では、多量の重金属
固定剤を添加する必要があるという問題点があった。ま
た、中性飛灰を水と水酸化カルシウムや水酸化ナトリウ
ム等のpH調整剤と重金属固定剤とで処理する方法で
は、重金属固定剤の使用量は低減できるが、高価なpH
調整剤を使用することから、ランニングコストが高くな
るという問題点があった。本発明は、低コストで処理す
ることのできる中性飛灰の処理方法を提供することを目
的とするものである。
However, the method of treating neutral fly ash only with water and a heavy metal fixing agent has a problem that it is necessary to add a large amount of heavy metal fixing agent. Further, in the method of treating neutral fly ash with water, a pH adjusting agent such as calcium hydroxide or sodium hydroxide, and a heavy metal fixing agent, the amount of the heavy metal fixing agent can be reduced, but the expensive pH
Since the regulator is used, there is a problem that running cost becomes high. An object of the present invention is to provide a method for treating neutral fly ash that can be treated at low cost.

【0004】[0004]

【課題を解決するための手段】本発明者らは、このよう
な課題を解決するために鋭意検討の結果、pH調整剤と
して焼却灰を用いることにより、従来用いられてきた高
価なpH調整剤や重金属固定剤の使用量を低減すること
ができ、さらに中性飛灰と焼却灰に含まれている重金属
の溶出を同時に抑制することができるという事実を見い
だし、本発明に到達した。すなわち、第1の発明は、中
性飛灰とpH調整剤としての焼却灰とを混練して混練物
のpHが9〜11になるようにpH調整剤としての焼却
灰の量を調整することを特徴とする中性飛灰の処理方法
を要旨とするものである。また、第2の発明は、中性飛
灰とpH調整剤としての焼却灰とを混練して混練物のp
Hが9〜11になるようにpH調整剤としての焼却灰の
量を調整した後、さらにこの混練物と重金属固定剤とを
混練することを特徴とする中性飛灰の処理方法を要旨と
するものである。
Means for Solving the Problems As a result of intensive studies to solve such problems, the present inventors have used an expensive pH adjusting agent which has been conventionally used by using incinerated ash as the pH adjusting agent. The present inventors have found the fact that it is possible to reduce the amount of heavy metal fixing agent used and the amount of heavy metals contained in neutral fly ash and incinerated ash can be suppressed at the same time, and have reached the present invention. That is, the first invention is to knead neutral fly ash and incinerated ash as a pH adjuster to adjust the amount of incinerated ash as a pH adjuster so that the pH of the kneaded product becomes 9 to 11. The gist is a method for treating neutral fly ash, which is characterized by A second aspect of the invention is to knead neutral fly ash and incinerated ash as a pH adjuster to obtain a p
The method for treating neutral fly ash is characterized in that after adjusting the amount of incinerated ash as a pH adjuster so that H becomes 9 to 11, the kneaded product and a heavy metal fixing agent are further kneaded. To do.

【0005】[0005]

【発明の実施の形態】以下、本発明を詳細に説明する。
本発明でいう中性飛灰とは、飛灰を10重量%水溶液と
して6時間振盪させた後の上澄み水のpHが5以上9未
満の範囲に入る飛灰のことであり、このような中性飛灰
としては、例えば、ごみ焼却炉やごみ溶融炉から排ガス
とともに排出する中性飛灰が挙げられる。これらの中性
飛灰には、通常、水銀、鉛、クロム、カドミウム等の重
金属が含まれている。また、本発明でいう焼却灰とは、
ごみ焼却炉底部に残る焼却残査のことであり、この焼却
残査を10重量%水溶液として6時間振盪させた後の上
澄み水のpHは、通常11〜13の範囲を示す。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be described in detail below.
The neutral fly ash referred to in the present invention is fly ash in which the pH of the supernatant water after shaking the fly ash as a 10% by weight aqueous solution for 6 hours falls within the range of 5 or more and less than 9 Examples of the neutral fly ash include neutral fly ash discharged from the refuse incinerator and the refuse melting furnace together with the exhaust gas. These neutral fly ash usually contain heavy metals such as mercury, lead, chromium and cadmium. Further, the incineration ash referred to in the present invention,
It refers to the incineration residue remaining on the bottom of the refuse incinerator, and the pH of the supernatant water after shaking the incineration residue as a 10% by weight aqueous solution for 6 hours usually ranges from 11 to 13.

【0006】本発明においては、中性飛灰とpH調整剤
としての焼却灰とを混練して処理するが、このとき、中
性飛灰に対する焼却灰の量としては、混練後の混練物の
pHが9〜11になるようにすることが必要であり、混
練後の混練物のpHが9未満であると重金属の溶出量が
多くなり、また、11を超えると鉛がアニオンの形態で
溶出することから、重金属固定剤を多量に添加すること
が必要となる。なお、本発明でいう混練物のpHとは、
混練物を10重量%水溶液とし、6時間振盪させた後の
上澄み水のpHのことである。
In the present invention, neutral fly ash and incinerated ash as a pH adjusting agent are kneaded and treated. At this time, the amount of incinerated ash with respect to neutral fly ash is the kneaded product after kneading. It is necessary to adjust the pH to 9 to 11, and if the pH of the kneaded product after kneading is less than 9, the amount of heavy metals eluted will increase, and if it exceeds 11, lead will elute in the form of anions. Therefore, it is necessary to add a large amount of heavy metal fixing agent. The pH of the kneaded material in the present invention means
It is the pH of the supernatant water after the kneaded product was made into a 10 wt% aqueous solution and shaken for 6 hours.

【0007】このときの中性飛灰と焼却灰との混合比と
しては、中性飛灰及び焼却灰の性状は、燃焼物、燃焼時
間、排ガスの処理条件に影響され、また、焼却場により
異なるため、それぞれの灰の成分を分析して決定すべき
である。通常は中性飛灰100重量部に対して、焼却灰
を1〜99重量部の範囲で選択して混合することによ
り、混練後の混練物のpHを9〜11にすることができ
る。
As the mixing ratio of the neutral fly ash and the incinerated ash at this time, the properties of the neutral fly ash and the incinerated ash are influenced by the combustion products, the combustion time, the exhaust gas treatment conditions, and depending on the incineration site. As they differ, the composition of each ash should be analyzed and determined. Usually, the pH of the kneaded product after kneading can be set to 9 to 11 by selecting and mixing the incinerated ash in the range of 1 to 99 parts by weight with respect to 100 parts by weight of the neutral fly ash.

【0008】また、混練するときの水の量としては、特
に限定されるものではないが、中性飛灰と焼却灰の混合
物100重量部に対して、0〜50重量部程度とする
と、混練物の取り扱い性がよいので好ましく、特に好ま
しくは2〜35重量部である。
The amount of water at the time of kneading is not particularly limited, but if it is about 0 to 50 parts by weight with respect to 100 parts by weight of the mixture of neutral fly ash and incineration ash, the kneading is performed. It is preferable because it is easy to handle, and particularly preferably 2 to 35 parts by weight.

【0009】混練方法としては、本発明においては金属
片や不燃物等の異物を含む焼却灰を使用することから、
振動式の混練機を用いて行うことが好ましいが、回転ド
ラム式、二軸混練式等の他の混練機を使用して行うこと
も可能である。また、混練機は、バッチ式のものでも、
連続式のものでも構わない。また、混練時間としては、
特に限定されるものではないが、2〜30分程度とする
と、均一に混練されるので好ましく、特に好ましくは5
〜30分である。
As the kneading method, in the present invention, since incineration ash containing foreign matters such as metal pieces and incombustibles is used,
It is preferable to use a vibration type kneader, but it is also possible to use other kneaders such as a rotary drum type and a twin-screw type. Also, the kneader may be a batch type,
A continuous type may be used. In addition, as the kneading time,
Although it is not particularly limited, it is preferably about 2 to 30 minutes because it is uniformly kneaded, and particularly preferably 5
~ 30 minutes.

【0010】また、本発明の第2発明においては、重金
属の溶出量をさらに抑制するために、上記の混練物と重
金属固定剤とを混練するが、この場合に用いられる重金
属固定剤としては、ジチオカルバミン酸基、チオール
基、ザンテート基、チオウレイド基等を有する水溶性化
合物、硫化ナトリウム、水硫化ナトリウム等の硫黄化合
物、リン酸、次亜リン酸等のリン酸化合物等が挙げら
れ、市販されている各種の重金属固定剤を使用できる。
重金属固定剤の量としては、通常、混練物100重量部
に対して5重量部以下の量で重金属の溶出を十分に抑制
することができる。
Further, in the second aspect of the present invention, in order to further suppress the elution amount of heavy metals, the above kneaded product and the heavy metal fixing agent are kneaded. As the heavy metal fixing agent used in this case, Water-soluble compounds having a dithiocarbamic acid group, a thiol group, a xanthate group, a thioureido group, and the like, sulfur compounds such as sodium sulfide and sodium hydrosulfide, phosphoric acid compounds such as phosphoric acid and hypophosphorous acid, and the like are commercially available. Various heavy metal fixatives can be used.
The amount of the heavy metal fixing agent is usually 5 parts by weight or less with respect to 100 parts by weight of the kneaded product, and the elution of heavy metals can be sufficiently suppressed.

【0011】[0011]

【実施例】次に、本発明を実施例によって具体的に説明
する。なお、実施例中のpHは、試料に対して10倍量
の蒸留水を加え、振盪回数200SPM、振盪幅4c
m、横振りで6時間振盪し、静置後の上澄み水をpH計
で測定したものである。また、重金属の溶出試験は、環
境庁告示13号に準じて行ったものである。
EXAMPLES Next, the present invention will be specifically described with reference to examples. In addition, the pH in the examples was obtained by adding 10 times the amount of distilled water to the sample, shaking frequency 200 SPM, shaking width 4 c.
m was shaken laterally for 6 hours, and the supernatant water after standing was measured with a pH meter. The heavy metal elution test was conducted according to the Environmental Agency Notification No. 13.

【0012】実施例1、2、比較例1〜4 Pb14,200mg/kg、Cd351mg/kgを
含有する都市ごみ焼却場における排ガス処理施設のバグ
フィルターで捕集された中性飛灰(pH7.2)と、消
火、冷却のための灰出し設備で湿潤したPb776mg
/kgを含有する焼却灰とを、10/0(比較例1)、
8/2(実施例1)、6/4(実施例2)、4/6(比
較例2)、2/8(比較例3)、0/10(比較例4)
の割合で混合し、その各混合物100重量部に水を36
重量部、23重量部、10重量部、6重量部、2重量部
添加して、5分間混練した。なお、焼却灰には混練物の
取り扱いに十分な水が含まれていたため、水は添加しな
かった。
Examples 1 and 2, Comparative Examples 1 to 4 Neutral fly ash (pH 7.2) collected by a bag filter of an exhaust gas treatment facility in an municipal solid waste incinerator containing Pb 14, 200 mg / kg and Cd 351 mg / kg. ), And Pb776mg wet in an ashing facility for extinguishing and cooling
10/0 (Comparative Example 1),
8/2 (Example 1), 6/4 (Example 2), 4/6 (Comparative Example 2), 2/8 (Comparative Example 3), 0/10 (Comparative Example 4)
100 parts by weight of each mixture with 36 parts of water.
Parts by weight, 23 parts by weight, 10 parts by weight, 6 parts by weight and 2 parts by weight were added and kneaded for 5 minutes. Since the incinerated ash contained sufficient water for handling the kneaded product, no water was added.

【0013】混練後の混練物のpH及び重金属の溶出試
験の結果を表1及び図1に示す。図1は、中性飛灰と焼
却灰の混合比と、鉛、カドミウムの溶出濃度及び混練物
のpHの関係を示す図であり、縦軸に鉛、カドミウムの
溶出濃度及び混練物のpHを、横軸に中性飛灰と焼却灰
の混合比を示している。
Table 1 and FIG. 1 show the results of the pH of the kneaded product after kneading and the elution test of heavy metals. FIG. 1 is a diagram showing the relationship between the mixing ratio of neutral fly ash and incinerated ash, the elution concentration of lead and cadmium, and the pH of the kneaded product, and the elution concentration of lead and cadmium and the pH of the kneaded product on the vertical axis The horizontal axis shows the mixing ratio of neutral fly ash and incinerated ash.

【0014】[0014]

【表1】 [Table 1]

【0015】表1及び図1からわかるように、混練物の
pHが9〜11となるように中性飛灰と焼却灰とを混練
することにより、鉛、カドミウムの溶出を抑制すること
ができ、鉛及びカドミウムの溶出濃度は「金属等を含む
産業廃棄物に係る判定基準を定める総理府令(昭和48
年2月17日、総理府令第5号)」に定める陸上埋立判
定基準を十分にクリアーしていた(実施例1及び2)。
As can be seen from Table 1 and FIG. 1, the elution of lead and cadmium can be suppressed by kneading the neutral fly ash and the incineration ash so that the pH of the kneaded product becomes 9 to 11. The lead and cadmium elution concentrations are "Prime Minister's Ordinance (Showa 48) which establishes criteria for industrial waste including metals.
February 17, 2014, Prime Minister's Office Ordinance No. 5) "was sufficiently cleared (Examples 1 and 2).

【0016】実施例3、比較例5、6 実施例1と同じ中性飛灰と、実施例1と同じ焼却灰とを
6/4の割合で混合し、混合灰100重量部に対して水
10重量部を添加して5分間混練した(実施例3)。ま
た、比較のため、実施例1と同じ中性飛灰に、中性飛灰
100重量部に対して水36重量部(比較例5)及び中
性飛灰100重量部に対して水34重量部とpH調整剤
として24重量%水酸化ナトリウム15重量部(比較例
6)を添加して5分間混練した。混練後の混練物に重金
属固定剤としてジチオカルバミン酸基を有するユニチカ
社製UML−7200を混練物に対して0〜4重量部添
加し、さらに約5分間混練した。混練後の混練物のpH
及び重金属の溶出試験の結果を表2及び図2に示す。図
2は、重金属固定剤の添加量と、鉛、カドミウムの溶出
濃度との関係を示す図であり、縦軸に鉛、カドミウムの
溶出濃度を、横軸に重金属固定剤の添加量を示してい
る。
Example 3, Comparative Examples 5 and 6 The same neutral fly ash as in Example 1 and the same incinerated ash as in Example 1 were mixed at a ratio of 6/4, and water was added to 100 parts by weight of mixed ash. 10 parts by weight was added and kneading was carried out for 5 minutes (Example 3). For comparison, the same neutral fly ash as in Example 1 was used, with 36 parts by weight of water for 100 parts by weight of neutral fly ash (Comparative Example 5) and 34 parts by weight of water for 100 parts by weight of neutral fly ash. Parts and 15 parts by weight of 24% by weight sodium hydroxide as a pH adjuster (Comparative Example 6) were added and kneaded for 5 minutes. To the kneaded product after kneading, 0 to 4 parts by weight of UML-7200 manufactured by Unitika Ltd. having a dithiocarbamic acid group as a heavy metal fixing agent was added to the kneaded product, and the mixture was further kneaded for about 5 minutes. PH of the kneaded product after kneading
Table 2 and FIG. 2 show the results of the elution test for heavy metals. FIG. 2 is a diagram showing the relationship between the amount of heavy metal fixative added and the elution concentrations of lead and cadmium, where the vertical axis shows the elution concentrations of lead and cadmium and the horizontal axis shows the amount of heavy metal fixative added. There is.

【0017】[0017]

【表2】 [Table 2]

【0018】表2及び図2からわかるように、中性飛灰
を重金属固定剤だけで処理しようとすると(比較例
5)、「金属等を含む産業廃棄物に係る判定基準を定め
る総理府令(昭和48年2月17日、総理府令第5
号)」に定める陸上埋立判定基準をクリアーするために
は、4重量%の重金属固定剤を添加することが必要であ
った。また、pH調整剤として24重量%水酸化ナトリ
ウムと重金属固定剤を併用した処理では(比較例6)、
鉛、カドミウムの溶出濃度は低下し、陸上埋立判定基準
をクリアーした。これに対して、焼却灰を用いて処理す
ると(実施例3)、pH調整剤として24重量%水酸化
ナトリウムを用いて処理した場合よりさらに溶出濃度が
低下し、陸上埋立判定基準を十分にクリアーしていた。
As can be seen from Table 2 and FIG. 2, when attempting to treat neutral fly ash only with a heavy metal fixing agent (Comparative Example 5), “Prime Minister's Ordinance (which defines the criteria for industrial waste containing metals etc. February 17, 1973, Prime Minister's Ordinance No. 5
No. 4), it was necessary to add 4% by weight of a heavy metal fixative in order to clear the landfill landfill judgment standard. Further, in the treatment using 24 wt% sodium hydroxide as a pH adjusting agent and a heavy metal fixing agent together (Comparative Example 6),
The elution concentrations of lead and cadmium decreased and cleared the criteria for landfill landfill. On the other hand, when treated with incinerated ash (Example 3), the elution concentration was lower than when treated with 24 wt% sodium hydroxide as a pH adjuster, and the landfill landfill judgment standard was sufficiently cleared. Was.

【0019】[0019]

【発明の効果】本発明によれば、中性飛灰を、入手が容
易な焼却灰を用いて処理することにより、重金属固定剤
やpH調整剤の使用量を大幅に低減させることができる
ため、低コストで処理することができる。また、本発明
によれば、中性飛灰と焼却灰とに含まれる重金属を同時
に処理することができる。
EFFECTS OF THE INVENTION According to the present invention, by treating neutral fly ash with incineration ash that is easily available, the amount of heavy metal fixing agent and pH adjusting agent used can be greatly reduced. , Can be processed at low cost. Further, according to the present invention, heavy metals contained in neutral fly ash and incinerated ash can be treated at the same time.

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

【図1】中性飛灰と焼却灰の混合比と、混練後の混練物
のpH及び鉛、カドミウムの溶出濃度との関係を示す図
である。
FIG. 1 is a diagram showing a relationship between a mixing ratio of neutral fly ash and incinerated ash, pH of a kneaded product after kneading, and elution concentrations of lead and cadmium.

【図2】重金属固定剤の添加量と、鉛、カドミウムの溶
出濃度との関係を示す図である。
FIG. 2 is a diagram showing the relationship between the amount of a heavy metal fixing agent added and the elution concentrations of lead and cadmium.

───────────────────────────────────────────────────── 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 - 5/00 ─────────────────────────────────────────────────── ─── Continuation of the front page (58) Fields investigated (Int.Cl. 7 , DB name) B09B 3/00-5/00

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 中性飛灰とpH調整剤としての焼却灰と
を混練して混練物のpHが9〜11になるようにpH調
整剤としての焼却灰の量を調整することを特徴とする中
性飛灰の処理方法。
1. An amount of incineration ash as a pH adjuster is adjusted such that neutral fly ash and incinerated ash as a pH adjuster are kneaded so that the pH of the kneaded product becomes 9 to 11. How to treat neutral fly ash.
【請求項2】 中性飛灰とpH調整剤としての焼却灰と
を混練して混練物のpHが9〜11になるようにpH調
整剤としての焼却灰の量を調整した後、さらにこの混合
物と重金属固定剤とを混練することを特徴とする中性飛
灰の処理方法。
2. A neutral fly ash and incinerated ash as a pH adjuster are kneaded to adjust the amount of incinerated ash as a pH adjuster so that the pH of the kneaded product is 9 to 11, and further A method for treating neutral fly ash, which comprises kneading a mixture with a heavy metal fixing agent.
JP15076196A 1996-06-12 1996-06-12 Neutral fly ash treatment method Expired - Lifetime JP3392293B2 (en)

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JP3392293B2 true JP3392293B2 (en) 2003-03-31

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI311494B (en) * 2003-12-23 2009-07-01 Chang Kuen Se Technology for removing heavy metals from fly ash derived from the waste incinerator.
FR3050947B1 (en) * 2016-05-09 2018-06-01 Lab Geodur Gmbh METHOD FOR STABILIZING RESIDUES RESULTING FROM THE COMBUSTION OF WASTE

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