JP3237465B2 - Method for determining required amount of liquid chelating agent for fly ash treatment - Google Patents
Method for determining required amount of liquid chelating agent for fly ash treatmentInfo
- Publication number
- JP3237465B2 JP3237465B2 JP12240395A JP12240395A JP3237465B2 JP 3237465 B2 JP3237465 B2 JP 3237465B2 JP 12240395 A JP12240395 A JP 12240395A JP 12240395 A JP12240395 A JP 12240395A JP 3237465 B2 JP3237465 B2 JP 3237465B2
- Authority
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- Japan
- Prior art keywords
- chelating agent
- fly ash
- liquid
- liquid chelating
- required amount
- 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.)
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Description
【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION
【0001】[0001]
【産業上の利用分野】本発明は、飛灰に液体キレート剤
を添加して処理するに当り、飛灰からの重金属の溶出を
防止するに必要な液体キレート剤の添加量を簡便な方法
で決定する方法に関する。BACKGROUND OF THE INVENTION The present invention relates to a method for adding a liquid chelating agent to fly ash and treating the amount of the liquid chelating agent necessary for preventing the elution of heavy metals from the fly ash. How to decide.
【0002】[0002]
【従来の技術】飛灰(煤塵)は、作業環境を悪化させ作
業員の健康上の問題を引き起こす可能性があることか
ら、法律(廃棄物処理法)で指定された下記〜の廃
棄物処理法に従って処理することが義務付けられてい
る。2. Description of the Related Art Fly ash (dust) may degrade the working environment and cause health problems for workers. Therefore, the following waste treatment specified by law (Waste Disposal Law) It is obliged to process according to law.
【0003】 薬剤処理法 溶融固化法 セメント固化法 酸、その他の溶媒による安定化法 上記処理法のうち、薬剤処理法による処理においては、
飛灰中の重金属の溶出を防止する目的で液体キレート剤
を使用する場合がある。Chemical treatment method Melt solidification method Cement solidification method Stabilization method with acid and other solvents Among the treatment methods described above, in the treatment by the chemical treatment method,
Liquid chelating agents may be used for the purpose of preventing the elution of heavy metals in fly ash.
【0004】この液体キレート剤としては、ジエチルジ
チオカルバミン酸及びその塩、エチレンビスジチオカル
バミン酸等の脂肪族ポリジチオカルバミン酸及びその
塩、ポリアミンにジチオカルボキシル基をN置換基とし
て導入したポリアミン誘導体、ポリエチレンイミンにジ
チオカルボキシル基をN置換基として導入したポリエチ
レンイミン誘導体、チオール等の硫黄化合物が知られて
いる。Examples of the liquid chelating agent include diethyldithiocarbamic acid and salts thereof, aliphatic polydithiocarbamic acids such as ethylenebisdithiocarbamic acid and salts thereof, polyamine derivatives obtained by introducing a dithiocarboxyl group into a polyamine as an N substituent, and polyethyleneimine. Sulfur compounds such as polyethyleneimine derivatives and thiols having a dithiocarboxyl group introduced as an N substituent are known.
【0005】これらの液体キレート剤の必要添加量を決
定するには、机上試験にて飛灰に液体キレート剤を加え
て前処理を施し、更に法律の定める方法(環境庁告示1
3号法)で重金属の溶出試験(溶出濃度の測定)を行っ
て効果を判定し、決定するのが一般的である。[0005] In order to determine the required amount of the liquid chelating agent, a fly ash is pretreated by adding a liquid chelating agent to the fly ash in a desk test, and further, a method specified by law (Notification 1 of the Environment Agency).
In general, the effect is determined by performing a dissolution test (measurement of dissolution concentration) of heavy metals according to No. 3 method).
【0006】一方、飛灰の成分ないし性状は、その焼却
方式、集塵方式、有害ガス除去方式、更には焼却物の種
類により大きく変動する。On the other hand, the components or properties of fly ash vary greatly depending on its incineration system, dust collection system, harmful gas removal system, and the type of incineration.
【0007】[0007]
【発明が解決しようとする課題】しかしながら、環境庁
告示13号法により重金属の溶出量を分析する上記従来
の方法では、評価に時間がかかるため、飛灰の性状が変
動する毎に上述の試験を行うことは容易ではない。この
ため、従来においては、現場における飛灰の性状の変動
に合わせた適正な薬剤処理を行うことが困難であった。However, in the above-mentioned conventional method of analyzing the elution amount of heavy metals according to the Environment Agency Notification No. 13 method, it takes a long time to evaluate, and the above-mentioned test is performed every time the properties of fly ash change. It is not easy to do. For this reason, conventionally, it has been difficult to perform appropriate chemical treatment in accordance with fluctuations in the properties of fly ash at the site.
【0008】本発明は上記従来の問題点を解決し、飛灰
の薬剤処理における液体キレート剤の必要添加量を簡便
な操作で容易かつ迅速に求めることができ、これにより
適正な薬剤処理を行うことを可能とする飛灰処理用液体
キレート剤の必要添加量決定方法を提供することを目的
とする。The present invention solves the above-mentioned conventional problems, and enables the required amount of a liquid chelating agent to be added easily and quickly in a chemical treatment of fly ash by a simple operation, thereby performing an appropriate chemical treatment. It is an object of the present invention to provide a method for determining a required addition amount of a liquid chelating agent for fly ash treatment that enables the above.
【0009】[0009]
【課題を解決するための手段】請求項1の飛灰処理用液
体キレート剤の必要添加量決定方法は、飛灰及び液体キ
レート剤を水に混合して得られた溶液の酸化還元電位
(ORP)を測定し、この測定値から液体キレート剤の
必要添加量を決定することを特徴とする。According to a first aspect of the present invention, there is provided a method for determining a required amount of a liquid chelating agent for treating fly ash, the method comprising: mixing a fly ash and a liquid chelating agent with water; ) Is measured, and the required addition amount of the liquid chelating agent is determined from the measured value.
【0010】請求項2の飛灰処理用液体キレート剤の必
要添加量決定方法は、飛灰及び液体キレート剤を水に混
合して得られた溶液のORP及びpHを測定し、これら
の測定値から液体キレート剤の必要添加量を決定するこ
とを特徴とする。According to a second aspect of the present invention, there is provided a method for determining a required amount of a liquid chelating agent for treating fly ash, comprising measuring the ORP and pH of a solution obtained by mixing the fly ash and the liquid chelating agent with water, and measuring these measured values. The required amount of the liquid chelating agent to be added is determined from the above formula.
【0011】請求項3の飛灰処理用液体キレート剤の必
要添加量決定方法は、請求項1又は2の方法において、
水と飛灰との混合割合を固液比(L/S)で10〜10
00とすることを特徴とする。The method for determining the required amount of the liquid chelating agent for fly ash treatment according to claim 3 is the method according to claim 1 or 2,
The mixing ratio of water and fly ash is 10 to 10 in solid-liquid ratio (L / S).
00 is set.
【0012】以下に本発明の飛灰処理用液体キレート剤
の必要添加量決定方法について詳細に説明する。The method for determining the required amount of the liquid chelating agent for fly ash treatment of the present invention will be described in detail below.
【0013】本発明の方法は、具体的には次のような方
法で実施することができる。The method of the present invention can be specifically carried out by the following method.
【0014】[I] キレート剤で処理した飛灰につい
て環境庁告示13号法試験に従って試験液を調製し、濾
過を行う前の溶液(スラリー)のORP、或いは、OR
PとpHを測定し、キレート剤が重金属を安定化する条
件の値と照合してキレート剤の効果を速やかに判断し、
キレート剤の必要添加量を決定する。[I] A fly ash treated with a chelating agent is used to prepare a test solution in accordance with the test method of the Environment Agency Notification No. 13, and the ORP or OR of the solution (slurry) before the filtration is performed.
P and pH are measured, and the effect of the chelating agent is quickly determined by comparing with the value of the condition under which the chelating agent stabilizes the heavy metal.
Determine the required amount of chelating agent to be added.
【0015】[II] 飛灰原灰を固液比(L/S)=1
0〜1000で水(好ましくは純水)に溶解し、溶液の
ORP、或いは、ORPとpHを測定し、この値がキレ
ート剤が重金属を安定化する条件の値になるまでキレー
ト剤を滴下し、キレート剤の必要添加量を速やかに決定
する。[II] Fly ash raw ash solid-liquid ratio (L / S) = 1
Dissolve in water (preferably pure water) at 0 to 1000, measure the ORP of the solution, or the ORP and pH, and add the chelating agent dropwise until the value reaches the value of the condition under which the chelating agent stabilizes heavy metals. The required amount of the chelating agent is determined promptly.
【0016】ここで、キレート剤が重金属を安定化する
条件とは、後掲の作用の項及び実施例1,2より明らか
なように、次のような条件とすることができる。Here, the conditions under which the chelating agent stabilizes the heavy metal can be the following conditions, as apparent from the operation section described later and Examples 1 and 2.
【0017】[0017]
【表1】 [Table 1]
【0018】簡便かつ確実な方法としては、ORPが−
120〜−150mV或いはそれ以下となるようにキレ
ート剤の必要添加量を決定する方法が挙げられる。As a simple and reliable method, ORP is-
There is a method of determining the necessary amount of the chelating agent to be 120 to -150 mV or less.
【0019】[0019]
【作用】本発明者らは、後述の実施例1,2に示す如
く、液体キレート剤が飛灰中の重金属を安定化するため
の条件は、被処理飛灰及び液体キレート剤を水に溶解し
たときのORP、或いは、pHとORPによって決まる
ことを見出した。According to the present invention, as shown in Examples 1 and 2 below, the conditions for the liquid chelating agent to stabilize the heavy metal in the fly ash are as follows: the fly ash to be treated and the liquid chelating agent are dissolved in water. It was found that it depends on the ORP, or pH and ORP.
【0020】即ち、実施例1の結果より明らかなよう
に、例えば、被処理飛灰を水に溶解させキレート剤を添
加したときのpH、又は、キレート剤で処理した被処理
飛灰を水に添加したときのpHが12.4でORPが−
120〜−150mV又はそれ以下の場合、或いは、当
該pHが8.0の場合、或いは、pHが4.0でORP
が120〜150mV又はそれ以下の場合において、重
金属であるPbを安定化することができる。That is, as is clear from the results of Example 1, for example, the pH at the time of dissolving the fly ash to be treated in water and adding a chelating agent, or the fly ash treated with the chelating agent is added to water. PH when added is 12.4 and ORP is-
ORP at 120 to -150 mV or lower, or when the pH is 8.0, or when the pH is 4.0
Is 120 to 150 mV or less, Pb which is a heavy metal can be stabilized.
【0021】また、被処理飛灰を水に溶解させキレート
剤を添加したときのpH、又は、キレート剤で処理した
被処理飛灰を水に添加したときのpHが12.4又は
8.0の場合、或いは、当該pHが4.0でORPが1
20〜150mV又はそれ以下の場合において、重金属
であるCdを安定化することができる。The pH when the fly ash to be treated is dissolved in water and a chelating agent is added, or when the fly ash to be treated with the chelating agent is added to water, the pH is 12.4 or 8.0. Or the pH is 4.0 and the ORP is 1
In the case of 20 to 150 mV or less, Cd which is a heavy metal can be stabilized.
【0022】更に、実施例2の各種飛灰の環境庁告示1
3号法試験の溶出液の分析からも、キレート剤の種類や
添加量によらず、様々な飛灰に対して、pHが11.7
〜12.5においてORPが−120〜−150mV或
いはそれ以下のとき、Pbを安定化できることがわか
る。換言すると、溶出液のORPを−120〜−150
mV或いはそれ以下にするようにキレート剤を添加すれ
ば、Pbを安定化できる。Furthermore, the notification 1 of the Environment Agency of various fly ash of Example 2
From the analysis of the eluate in the No. 3 test, the pH was 11.7 for various fly ash irrespective of the type and amount of the chelating agent.
It can be seen that Pb can be stabilized when the ORP is -120 to -150 mV or lower at ~ 12.5. In other words, the ORP of the eluate is -120 to -150.
Pb can be stabilized by adding a chelating agent so as to have a mV or less.
【0023】[0023]
【実施例】以下に実施例を挙げて本発明をより具体的に
説明する。The present invention will be described more specifically with reference to the following examples.
【0024】なお、以下の実施例において用いた液体キ
レート剤は、キレート剤A,Bがジチオカルバミン酸系
化合物、キレート剤Cがイミン系化合物である。In the liquid chelating agents used in the following examples, chelating agents A and B are dithiocarbamic acid compounds, and chelating agent C is an imine compound.
【0025】実施例1 供試飛灰の分析 ゴミ種:都市ゴミ,炉型式:ストーカ炉,排ガス処理方
式:乾式,集塵方式:EP(電気集塵)で発生した飛灰
の成分分析及び環境庁告示13号法試験を行い、結果を
表2,3に示した。Example 1 Analysis of test fly ash Refuse type: municipal waste, furnace type: stoker furnace, exhaust gas treatment method: dry type, dust collection method: analysis of components of fly ash generated by EP (electric dust collection) and Environment Agency Test No. 13 was conducted, and the results are shown in Tables 2 and 3.
【0026】[0026]
【表2】 [Table 2]
【0027】[0027]
【表3】 [Table 3]
【0028】 飛灰の処理 500mlのポリビーカーに上記供試飛灰70g,純水
21g(固液比(L/S):0.3)及び液体キレート
剤Aを飛灰に対して4重量%入れ、スパーテルで約5分
間混練して処理灰を作成した。Treatment of Fly Ash 70 g of the test fly ash, 21 g of pure water (solid-liquid ratio (L / S): 0.3) and liquid chelating agent A were put into a 500 ml polybeaker at 4% by weight based on the fly ash. The mixture was kneaded with a spatula for about 5 minutes to prepare a treated ash.
【0029】 重金属の安定化(溶出防止)効果の確
認 1リットルのガラスビーカーに純水700g及び上記処
理灰70gを入れて蓋をした(固液比(L/S):1
3.3)。ビーカー内の溶液をスターラー撹拌し、同時
に空気(0.7リットル/分)で溶液を曝気しながら、
pHコントローラにより30重量%硝酸又は48重量%
水酸化ナトリウム水溶液を添加して所定のpHに調整し
た。Confirmation of Stabilization (Prevention of Elution) Effect of Heavy Metals 700 g of pure water and 70 g of the above treated ash were put into a 1-liter glass beaker, and the lid was closed (solid-liquid ratio (L / S): 1).
3.3). While stirring the solution in the beaker and simultaneously aerating the solution with air (0.7 L / min),
30% by weight nitric acid or 48% by weight by pH controller
The pH was adjusted to a predetermined value by adding an aqueous sodium hydroxide solution.
【0030】撹拌開始後、経時的にビーカー内の溶液を
固形物と共に50mlずつサンプリングし、ただちにO
RPメーターでORPを測定した。その後、0.45μ
mのメンブレンフィルターで吸引濾過して濾液中のP
b,Cd濃度を原子吸光分光光度計で測定した。After the stirring was started, 50 ml of the solution in the beaker was sampled together with the solid matter over time, and immediately
ORP was measured with an RP meter. Then, 0.45μ
Suction filtration with a membrane filter of m
b, Cd concentrations were measured with an atomic absorption spectrophotometer.
【0031】 結果 溶液のpH,ORP及びPb溶出濃度の関係を図1に、
また、溶液のpH,ORP及びCd溶出濃度の関係を図
2に示す。Results FIG. 1 shows the relationship among the pH, ORP, and Pb elution concentration of the solution.
FIG. 2 shows the relationship among the pH, ORP, and Cd elution concentration of the solution.
【0032】 考察 図1,2より、以下の通り結論づけることができる。Discussion From FIGS. 1 and 2, the following can be concluded.
【0033】Pbについて (a) 溶液がpH12.4の時はORPが−120〜
−150mV或いはそれ以下で安定 (b) 溶液がpH8.0の時は安定 (c) 溶液がpH4.0の時はORPが150〜20
0mV或いはそれ以下で安定Cdについて (d) 溶液がpH12.4,pH8.0の時は安定 (e) 溶液がpH4.0の時はORPが120〜15
0mV或いはそれ以下で安定 この結果から、Pbについては上記(a)〜(c)の条
件を満たすようにキレート剤の必要添加量を決定し、ま
た、Cdについては上記(d),(e)の条件を満たす
ようにキレート剤の必要添加量を決定すれば良いことが
わかる。 Regarding Pb (a) When the solution has a pH of 12.4, the ORP is from -120 to
Stable at -150 mV or less (b) Stable when the solution is at pH 8.0 (c) ORP is 150 to 20 when the solution is at pH 4.0
Stable Cd at 0 mV or less (d) Stable when the solution is at pH 12.4 and pH 8.0 (e) When the solution is at pH 4.0, the ORP is 120 to 15
Stable at 0 mV or less From these results, the necessary amount of the chelating agent to be added is determined for Pb so as to satisfy the above conditions (a) to (c). It can be understood that the necessary amount of the chelating agent should be determined so as to satisfy the condition (1).
【0034】実施例2 都市ゴミA〜Kの焼却工程で排出された飛灰A〜Kにキ
レート剤A〜Cを表4,5に示す割合で添加して環境庁
告示13号法試験におけるPb濃度とORP,pHとの
関係を調べ、結果を表4,5に示した。Example 2 Chelating agents A to C were added to fly ash A to K discharged in the incineration process of municipal waste A to K at the ratios shown in Tables 4 and 5, and Pb in a test of method No. 13 notified by the Environment Agency. The relationship between the concentration, ORP and pH was examined, and the results are shown in Tables 4 and 5.
【0035】また、表4,5の結果から、ORPとPb
濃度(対数換算値)との関係をグラフ化したものを図3
に示す。Also, from the results of Tables 4 and 5, ORP and Pb
Fig. 3 shows a graph of the relationship with the concentration (logarithmic conversion value).
Shown in
【0036】表4,5及び図3より、Pbの安定化効果
(Pb溶出濃度が0.3mg/l以下になる時)が発揮
されるのは、キレート剤の種類や添加量によらず、溶出
液(pH11.0〜12.5の範囲)のORPが−12
0〜−150mV或いはそれ以下になる時であり、従っ
て、ORPが−120〜−150mV或いはそれ以下と
なるようにキレート剤の添加量を決定すれば良いことが
わかる。According to Tables 4 and 5 and FIG. 3, the stabilizing effect of Pb (when the Pb elution concentration is 0.3 mg / l or less) is exhibited regardless of the type and amount of the chelating agent. ORP of eluate (pH 11.0 to 12.5) is -12
This is the time when it becomes 0 to -150 mV or less, and therefore, it can be seen that the addition amount of the chelating agent should be determined so that the ORP becomes -120 to -150 mV or less.
【0037】[0037]
【表4】 [Table 4]
【0038】[0038]
【表5】 [Table 5]
【0039】[0039]
【発明の効果】以上詳述した通り、本発明の飛灰処理用
液体キレート剤の必要添加量決定方法によれば、飛灰及
び液体キレート剤を水に混合して得られる溶液のOR
P、或いは、pHとORPを測定するという極めて簡便
な操作により、飛灰中の重金属の安定化に必要なキレー
ト剤の添加量を決定することができる。従って、本発明
によれば、飛灰の性状の変動に迅速に対応した適正な薬
剤処理を容易に行うことができる。As described above in detail, according to the method for determining the required amount of the liquid chelating agent for fly ash treatment according to the present invention, the OR of the solution obtained by mixing the fly ash and the liquid chelating agent with water is obtained.
By an extremely simple operation of measuring P, or pH and ORP, the amount of the chelating agent necessary for stabilizing heavy metals in fly ash can be determined. Therefore, according to the present invention, it is possible to easily perform appropriate chemical treatment that quickly responds to fluctuations in the properties of fly ash.
【図1】実施例1の結果(Pd溶出濃度)を示すグラフ
である。FIG. 1 is a graph showing the results (Pd elution concentration) of Example 1.
【図2】実施例1の結果(Cd溶出濃度)を示すグラフ
である。FIG. 2 is a graph showing the results (Cd elution concentration) of Example 1.
【図3】実施例2の結果を示すグラフである。FIG. 3 is a graph showing the results of Example 2.
Claims (3)
得られた溶液の酸化還元電位を測定し、この測定値から
液体キレート剤の必要添加量を決定することを特徴とす
る飛灰処理用液体キレート剤の必要添加量決定方法。1. A fly ash characterized by measuring the oxidation-reduction potential of a solution obtained by mixing a fly ash and a liquid chelating agent with water, and determining the required addition amount of the liquid chelating agent from the measured value. A method for determining the required amount of a liquid chelating agent for treatment.
得られた溶液の酸化還元電位及びpHを測定し、これら
の測定値から液体キレート剤の必要添加量を決定するこ
とを特徴とする飛灰処理用液体キレート剤の必要添加量
決定方法。2. The method according to claim 1, wherein the redox potential and the pH of a solution obtained by mixing the fly ash and the liquid chelating agent with water are measured, and the required addition amount of the liquid chelating agent is determined from the measured values. To determine the required amount of added liquid chelating agent for fly ash treatment.
灰との混合割合を固液比(L/S)で10〜1000と
することを特徴とする飛灰処理用液体キレート剤の必要
添加量決定方法。3. The method according to claim 1, wherein the mixing ratio of water and fly ash is 10 to 1000 in terms of a solid-liquid ratio (L / S). How to determine the required amount.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12240395A JP3237465B2 (en) | 1995-05-22 | 1995-05-22 | Method for determining required amount of liquid chelating agent for fly ash treatment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12240395A JP3237465B2 (en) | 1995-05-22 | 1995-05-22 | Method for determining required amount of liquid chelating agent for fly ash treatment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH08309312A JPH08309312A (en) | 1996-11-26 |
| JP3237465B2 true JP3237465B2 (en) | 2001-12-10 |
Family
ID=14834939
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12240395A Expired - Lifetime JP3237465B2 (en) | 1995-05-22 | 1995-05-22 | Method for determining required amount of liquid chelating agent for fly ash treatment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3237465B2 (en) |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4543502B2 (en) * | 2000-06-01 | 2010-09-15 | 栗田工業株式会社 | Determination method of required addition amount of chelating heavy metal scavenger, chemical injection control method and chemical injection control device |
| JP4665347B2 (en) * | 2001-06-26 | 2011-04-06 | 日立造船株式会社 | Method for stabilizing lead in fly ash |
| JP4599913B2 (en) * | 2004-05-17 | 2010-12-15 | 東ソー株式会社 | Method for determining required addition amount of heavy metal treating agent and apparatus used therefor |
| JP7075860B2 (en) * | 2018-09-27 | 2022-05-26 | 株式会社タクマ | Fly ash processing equipment and processing method |
| JP7105203B2 (en) * | 2019-01-22 | 2022-07-22 | 鹿島建設株式会社 | Method for insolubilizing heavy metals |
| JP7261703B2 (en) * | 2019-08-30 | 2023-04-20 | 日立造船株式会社 | Method for treating heavy metal-containing ash |
| JP7438855B2 (en) * | 2020-06-05 | 2024-02-27 | 清水建設株式会社 | Processing method and equipment for substances containing heavy metals |
-
1995
- 1995-05-22 JP JP12240395A patent/JP3237465B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH08309312A (en) | 1996-11-26 |
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