JPH062275B2 - Method of detoxifying fly ash - Google Patents
Method of detoxifying fly ashInfo
- Publication number
- JPH062275B2 JPH062275B2 JP62113836A JP11383687A JPH062275B2 JP H062275 B2 JPH062275 B2 JP H062275B2 JP 62113836 A JP62113836 A JP 62113836A JP 11383687 A JP11383687 A JP 11383687A JP H062275 B2 JPH062275 B2 JP H062275B2
- Authority
- JP
- Japan
- Prior art keywords
- fly ash
- ash
- water
- mixer
- detoxifying
- 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
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- Processing Of Solid Wastes (AREA)
Description
【発明の詳細な説明】 産業上の利用分野 この発明は、都市ごみや産業廃棄物などの焼却プラント
から排ガスとともに排出される灰分、たとえば電気集塵
機で収集された灰分であるEP灰や、バグフィルタで収
集された灰分等(この明細書全体を通してこの種の灰分
を「飛灰」と称する。)を無害化する処理方法に関する
ものである。Description: TECHNICAL FIELD The present invention relates to ash discharged together with exhaust gas from an incinerator plant such as municipal waste and industrial waste, for example, EP ash which is ash collected by an electric dust collector, and a bag filter. The present invention relates to a treatment method for detoxifying the ash and the like collected in (the ash of this type is referred to as "fly ash" throughout this specification).
従来技術およびその問題点 この種の飛灰の中には人体に有害な重金属類の塩化物が
多量に含まれており、特にカドミウム、鉛、水銀の含有
量は、「有害な産業廃棄物に係る判定基準を定める総理
府令」に定められた溶出基準値を超える傾向がある。Conventional technology and its problems This type of fly ash contains a large amount of chlorides of heavy metals that are harmful to the human body. Especially, the content of cadmium, lead, and mercury is " It tends to exceed the elution standard value defined by the Prime Minister's Ordinance that establishes such criteria.
そのため、最近では、添付第3図(イ)(ロ)に示すよ
うに、EP灰にセメントと水を添加混合してEP灰を固
化する方法や、EP灰に含まれる重金属類を酸によって
抽出する方法によって、EP灰を無害化処理する例が多
くなってきた。Therefore, recently, as shown in the attached Fig. 3 (a) and (b), cement and water are added to and mixed with EP ash to solidify EP ash, and heavy metals contained in EP ash are extracted with acid. The method of detoxifying the EP ash has been increasing in many cases.
しかしながら、これらの処理方法では、添加するセメン
トや抽出した重金属類を固定するための薬剤のコストが
多大なものとなり、さらにこの処理設備の運転維持管理
がはなはだ面倒なものであった。However, in these treatment methods, the cost of chemicals for fixing the cement to be added and the extracted heavy metals becomes enormous, and the operation and maintenance of this treatment equipment is very troublesome.
この発明は、上記の如き実情に鑑み、必要最小限の薬剤
コストによってかつ簡略な運転維持管理によって実施す
ることができる飛灰の無害化処理方法を提供することを
目的とする。In view of the above situation, an object of the present invention is to provide a fly ash detoxification treatment method which can be carried out with a minimum necessary chemical cost and with simple operation and maintenance.
問題点の解決手段 この発明による飛灰の無害化処理方法は、飛灰に所要量
の水および必要に応じて所要量のpH調整剤を添加して飛
灰を振動式混合機を用いて加湿混練しながら、キレート
化剤さらに鉄塩を所要量ずつ添加することを特徴とす
る。Solution to Problem A method for detoxifying fly ash according to the present invention is to add a required amount of water and, if necessary, a required amount of a pH adjuster to the fly ash to humidify the fly ash using a vibration mixer. It is characterized in that a chelating agent and an iron salt are added in required amounts while kneading.
この発明の好ましい実施態様においては、最終的に得ら
れるスラッジの含水率は湿り基準で15〜50%になさ
れる。In a preferred embodiment of the present invention, the final sludge has a water content of 15-50% on a wet basis.
一般に飛灰はpH12程度のアルカリ性を示すことが多い
ので、必要に応じてこれに塩酸等の酸を酸化してそのpH
を調整する。飛灰の加湿混練においてキレート化剤の添
加前のpHは3〜10になされ、本処理終了後のpHは9〜
10になされる。In general, fly ash is often alkaline with a pH of about 12, so if necessary, oxidize an acid such as hydrochloric acid to adjust its pH.
Adjust. In humidified kneading of fly ash, the pH before addition of the chelating agent is adjusted to 3 to 10, and the pH after completion of this treatment is 9 to
Be done at 10.
飛灰の加湿混練時に添加するpH調整剤の量は、飛灰のサ
ンプルを用いた自動滴定によって予め設定しておくこと
ができる。The amount of the pH adjusting agent added during the humidification and kneading of fly ash can be set in advance by automatic titration using a fly ash sample.
キレート化剤および鉄塩の添加量は、飛灰の性状に応じ
て適宜設定される。キレート化剤としては、市販の重金
属固定剤が用いられる。なお、この場合、上記鉄塩は重
金属類のキレート化物の凝集の核となって反応を促進さ
せる。The addition amount of the chelating agent and the iron salt is appropriately set according to the properties of the fly ash. A commercially available heavy metal fixing agent is used as the chelating agent. In this case, the iron salt serves as a nucleus for the agglomeration of the chelate of heavy metals to accelerate the reaction.
飛灰の混練手段としては、好ましくは振動式混合機が用
いられる。As a kneading means for fly ash, a vibration type mixer is preferably used.
振動式混合機を用いることにより、つぎのような効果が
奏される。The following effects can be obtained by using the vibration mixer.
飛灰の加湿混練時に飛灰に付与される加振力によっ
て、水分が飛灰に均質に行き亘る。そのため添加される
べき水の量を必要最小限に抑えることができ、また全体
に均質な反応を実施することができる。Moisture is evenly spread over the fly ash by vibrating force applied to the fly ash during the humidification and kneading of the fly ash. Therefore, the amount of water to be added can be minimized and a homogeneous reaction can be carried out throughout.
上述のように水の量が抑えられるので、最終的に得ら
れる無害化スラッジの含水率も低く抑えることができ
る。したがってスラッジに脱水等の後処理を施す必要が
なく、よって廃水を生じることもない。Since the amount of water is suppressed as described above, the water content of the detoxified sludge finally obtained can also be suppressed to be low. Therefore, it is not necessary to subject the sludge to a post-treatment such as dehydration, so that waste water is not generated.
振動式混合機の機構上、飛灰と混合機の内部構造部分
との相対的な速度差は非常に小さい。したがって内部構
造部分の摩耗は極めて少ない。Due to the mechanism of the vibration mixer, the relative speed difference between the fly ash and the internal structure of the mixer is very small. Therefore, wear of the internal structure portion is extremely small.
振動式混合機の一例を第1図および第2図に示す。すな
わち、横倒円胴状の混合機本体(1)はスプリング(2)によ
って床(3)上に指示されており、同本体(1)はたとえば加
振モータなどの手段によって振動せしめられるようにな
っている。本体(1)の内部には混合媒体(4)が多数入れて
ある。本体(1)の一端頂部には供給口(5)が、また他端底
部には排出口(6)がそれぞれ設けられている。こうして
振動式混合機(7)が構成されている。An example of the vibration mixer is shown in FIGS. 1 and 2. That is, the mixer body (1) in the shape of an inverted cylinder is directed on the floor (3) by the spring (2), and the body (1) is made to vibrate by means such as a vibration motor. Has become. A large number of mixed media (4) are placed inside the main body (1). A supply port (5) is provided at the top of one end of the main body (1), and a discharge port (6) is provided at the bottom of the other end. Thus, the vibration mixer (7) is constructed.
振動する本体(1)内に供給口(5)から供給された飛灰は、
混合媒体(4)によってよく混合される。ここへ水および
薬剤を添加すると、飛灰は効果的に加湿混練され、これ
らとよく反応する。Fly ash supplied from the supply port (5) in the vibrating body (1)
It is well mixed by the mixing medium (4). When water and chemicals are added thereto, the fly ash is effectively humidified and kneaded, and reacts well with them.
発明の効果 この発明による方法は以上のとおり構成されているの
で、従来技術による方法に比べて、使用される薬剤のコ
ストを必要最小限に抑えることができる上に、運転維持
管理を大幅に簡略化することができる。EFFECTS OF THE INVENTION Since the method according to the present invention is configured as described above, compared to the method according to the prior art, the cost of chemicals used can be kept to a necessary minimum, and operation and maintenance can be greatly simplified. Can be converted.
実施例 つぎに、この発明の実施例について図面を基に具体的に
説明する。Embodiment Next, an embodiment of the present invention will be specifically described with reference to the drawings.
第1図および第2図において、振動式混合機(7)を約6
Gの加速度で振動させておく。ホッパ(8)からフィーダ
(9)を経て振動式混合機(7)の供給口(5)に6kgのEP灰
を供給した。ついで、供給口(6)へ1160mlの水と2
40mlの35%塩酸とを添加し、さらに60mlの10%
キレート水溶液(ミヨシ油脂株式会社製の重金属固定
剤、商品名「エポフロックL−1」)を添加し、混練を
10分間続けた。つぎに、170mlの1%塩化第2鉄水
溶液を添加して混練を15分間続けた。こうして最終的
に得られた無害化スラッジを排出口(6)から取出した。In FIG. 1 and FIG. 2, the vibration type mixer (7) has about 6
Vibrate with G acceleration. Feeder from hopper (8)
6 kg of EP ash was supplied to the supply port (5) of the vibration type mixer (7) via (9). Then add 1160 ml of water and 2 to the inlet (6)
Add 40 ml of 35% hydrochloric acid and add another 60 ml of 10%
A chelate aqueous solution (heavy metal fixing agent manufactured by Miyoshi Yushi Co., Ltd., trade name "Epofloc L-1") was added, and kneading was continued for 10 minutes. Then, 170 ml of 1% ferric chloride aqueous solution was added and kneading was continued for 15 minutes. The detoxified sludge finally obtained in this way was taken out from the discharge port (6).
混練中はEP灰には水分が均質に行き亘り、スラリーが
形成され、良好な反応条件が得られたことが観察され
た。It was observed that during the kneading, the EP ash was uniformly distributed with water, a slurry was formed, and good reaction conditions were obtained.
最終的に得られたスラッジは粘土状をなしていた。これ
の嵩比重を計測したところ、1.67であり、処理前の嵩比
重0.33に比べて約1/5に減容した。The sludge finally obtained was in the form of clay. The bulk specific gravity of this was measured to be 1.67, which was about 1/5 the volume specific gravity of 0.33 before treatment.
またこのスラッジのpHおよび含水率をそれぞれ測定し、
さらに下記に示すように「産業廃棄物に含まれる金属等
の検定方法(昭和48年2月17日、環告13)」に定
める方法に従い、重金属類の溶出試験を行なったとこ
ろ、得られた測定値はいずれも表1に示すように、「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、総令5)」に定める基準値に
充分に合格するものであった。Also, measure the pH and water content of this sludge,
Further, as shown below, the elution test of heavy metals was carried out according to the method specified in “Testing method for metals contained in industrial waste (February 17, 1973, Announcement 13)”. As shown in Table 1, all of the measured values passed the standard values stipulated in the “Prime Minister's Ordinance (February 17, 1973, General Ordinance 5) that establishes criteria for industrial waste containing metals etc.” It was something to do.
重金属類の溶出試験方法 有姿のスラッジと純水(pH=6.3)とを重量体積比10
%の割合で混合し、得られた混合液(500ml以上)を
常温常圧にて6時間連続振とうした。こうして得られた
試料液を孔径1ミクロンのグラスファイバーフィルター
ペーパーにて濾過し、この濾液中の全水銀、カドミウム
および鉛をいずれも原子吸光光度法によって定量分析し
た。Dissolution test method for heavy metals 10% by weight of pure sludge and pure water (pH = 6.3)
%, And the resulting mixed liquid (500 ml or more) was continuously shaken at room temperature and atmospheric pressure for 6 hours. The sample solution thus obtained was filtered through a glass fiber filter paper having a pore size of 1 micron, and total mercury, cadmium and lead in this filtrate were quantitatively analyzed by an atomic absorption spectrophotometry.
第1図はこの発明の実施例を示す振動式混合機の側面
図、第2図は第1図中のII−II線に沿う断面図、第3図
(イ)(ロ)は従来技術による方法を示すフローシー
ト、同図(ハ)はこの発明による方法を示すフローシー
トである。FIG. 1 is a side view of a vibrating mixer showing an embodiment of the present invention, FIG. 2 is a sectional view taken along the line II-II in FIG. 1, and FIGS. A flow sheet showing the method, and FIG. 6C is a flow sheet showing the method according to the present invention.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 漁野 裕史 大阪府堺市大豆塚町1丁目27番地 (56)参考文献 特開 昭57−87881(JP,A) 特開 昭54−37069(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Hiroshi Ukino 1-27, Soyozuka-cho, Sakai City, Osaka Prefecture (56) Reference JP-A-57-87881 (JP, A) JP-A-54-37069 (JP) , A)
Claims (4)
量のpH調整剤を添加して飛灰を振動式混合機を用いて加
湿混練しながら、キレート化剤さらに鉄塩を所要量ずつ
添加することを特徴とする、飛灰の無害化処理方法。1. A chelating agent and an iron salt are required while a fly ash is added with a required amount of water and, if necessary, a required amount of a pH adjusting agent, to moisten and knead the fly ash using a vibration mixer. A method for detoxifying fly ash, which is characterized by adding each in a quantity.
基準で15〜50%にする、特許請求の範囲第1項記載
の方法。2. The method according to claim 1, wherein the sludge finally obtained has a water content of 15 to 50% on a wet basis.
請求の範囲第1または2項記載の方法。3. The method according to claim 1 or 2, wherein the pH of the fly ash during kneading is 3 to 10.
によって予め設定しておく、特許請求の範囲第1〜3項
のうち1項記載の方法。4. The method according to claim 1, wherein the amount of the pH adjusting agent is preset by automatic titration of a fly ash sample.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62113836A JPH062275B2 (en) | 1987-05-11 | 1987-05-11 | Method of detoxifying fly ash |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62113836A JPH062275B2 (en) | 1987-05-11 | 1987-05-11 | Method of detoxifying fly ash |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63278589A JPS63278589A (en) | 1988-11-16 |
| JPH062275B2 true JPH062275B2 (en) | 1994-01-12 |
Family
ID=14622264
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62113836A Expired - Lifetime JPH062275B2 (en) | 1987-05-11 | 1987-05-11 | Method of detoxifying fly ash |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH062275B2 (en) |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH062276B2 (en) * | 1988-02-29 | 1994-01-12 | 日本鋼管株式会社 | Treatment method of fly ash containing alkali |
| JPH01218673A (en) * | 1988-02-29 | 1989-08-31 | Nkk Corp | Method for treating fly ash |
| JP2920717B2 (en) * | 1992-07-01 | 1999-07-19 | 日立造船株式会社 | Ash treatment method with reduced hydrogen generation |
| JPH11236548A (en) * | 1998-02-19 | 1999-08-31 | Miyoshi Oil & Fat Co Ltd | Metal collecting agent composition and metal collecting method |
| JP4756415B2 (en) * | 2001-08-03 | 2011-08-24 | 三井造船株式会社 | Gas processing method |
| JP7075860B2 (en) * | 2018-09-27 | 2022-05-26 | 株式会社タクマ | Fly ash processing equipment and processing method |
| JP7304029B2 (en) * | 2019-03-01 | 2023-07-06 | 太平洋マテリアル株式会社 | Method for preventing elution of heavy metals from incinerated ash |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS52111260A (en) * | 1976-03-15 | 1977-09-17 | Kuraray Co Ltd | Treating method for sludge containing heavy metals |
| JPS5320948A (en) * | 1976-08-11 | 1978-02-25 | Seiko Instr & Electronics Ltd | Liquid crystal display device |
| JPS5437069A (en) * | 1977-08-30 | 1979-03-19 | Ogasawara Tetsunori | Method of treating industrial wastes |
| JPS5787881A (en) * | 1980-11-21 | 1982-06-01 | Maeda Sekkei Kk | Treatment of incineration refuse |
| JPS6011254A (en) * | 1983-06-29 | 1985-01-21 | 大同特殊鋼株式会社 | Processing method for steelmaking dust |
| JPS61216720A (en) * | 1985-03-22 | 1986-09-26 | Kanemi Abe | Vibration kneading apparatus |
-
1987
- 1987-05-11 JP JP62113836A patent/JPH062275B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63278589A (en) | 1988-11-16 |
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