JPS6043193B2 - Method for detoxifying industrial waste containing hazardous substances - Google Patents

Method for detoxifying industrial waste containing hazardous substances

Info

Publication number
JPS6043193B2
JPS6043193B2 JP56135447A JP13544781A JPS6043193B2 JP S6043193 B2 JPS6043193 B2 JP S6043193B2 JP 56135447 A JP56135447 A JP 56135447A JP 13544781 A JP13544781 A JP 13544781A JP S6043193 B2 JPS6043193 B2 JP S6043193B2
Authority
JP
Japan
Prior art keywords
industrial waste
waste
hazardous substances
calcium
aqueous solution
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
Application number
JP56135447A
Other languages
Japanese (ja)
Other versions
JPS5836690A (en
Inventor
英明 高木
政男 出山
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.)
Adeka Corp
Original Assignee
Asahi Denka Kogyo KK
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 Asahi Denka Kogyo KK filed Critical Asahi Denka Kogyo KK
Priority to JP56135447A priority Critical patent/JPS6043193B2/en
Publication of JPS5836690A publication Critical patent/JPS5836690A/en
Publication of JPS6043193B2 publication Critical patent/JPS6043193B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は有害物質を含有する産業廃棄物または汚染土壌
の無害化方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for detoxifying industrial waste or contaminated soil containing harmful substances.

重金属等の有害物質を含有する、金属くす、ガラスくず
、陶磁器くず、鉱さい、汚泥、ばいじん、もえがら等の
産業廃棄物及び汚染土壌は近年各事業所等から大量に発
生し、その処理は公害対策上極めて重大な課題である。
In recent years, large amounts of industrial waste and contaminated soil, such as metal scraps, glass scraps, ceramic scraps, slag, sludge, soot, and rice husks, which contain hazardous substances such as heavy metals, have been generated from various business establishments, etc., and their disposal is a pollution-related issue. This is an extremely important issue in terms of countermeasures.

大量の産業廃棄物は埋立、海洋投棄等により最終処分が
なされるが、いずれの場合にも廃棄物中に含まれる有害
物質が溶出しないような無害化処理を行なわねばならず
、「有害な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号月等により有
害物質の判定基準が定められている。しかるに、有害物
質を含有する大量の産業廃棄物について溶出防止処理を
行ない、上記判定基準をクリアすることは作業性、経済
性の面でかなり困難を伴なうものであつた。
A large amount of industrial waste is finally disposed of by landfilling, ocean dumping, etc., but in either case, it is necessary to detoxify the waste so that the harmful substances contained in the waste do not leach out. Criteria for determining hazardous substances are established by the Prime Minister's Office Ordinance (February 17, 1971, Prime Minister's Office Ordinance No. 5, etc.) that establishes criteria for determining waste. It was quite difficult in terms of workability and economy to carry out elution prevention treatment and clear the above criteria.

等に有害物質として鉛(Pb)、カドミウム(Cd)、
亜鉛(Zn)、銅(Cu)、6価クロム(Cr’゛)、
水銀(Hg)、アルキル水銀、ヒ素(As)等の重金属
やシアン(CN)を含有する廃棄物、あるいはさらにこ
れにフッ素(F)を含有する廃棄物を完全に無害化処理
することは非常に困難とされていた。本発明者らは有害
物質を含有する大量の産業廃棄物の溶出防止無害化方法
について種々の検討を行なつた結果、ある特定の化合物
水溶液で廃棄物を処理することにより、大量の被処理物
質を効率よく無害化しうることを見い出し本発明を完成
した。
Lead (Pb), cadmium (Cd), etc. are harmful substances.
Zinc (Zn), copper (Cu), hexavalent chromium (Cr'゛),
It is extremely difficult to completely detoxify waste containing heavy metals such as mercury (Hg), alkyl mercury, arsenic (As), cyanide (CN), or even fluorine (F). It was considered difficult. The present inventors have conducted various studies on methods for preventing the elution of large amounts of industrial waste containing hazardous substances and making them harmless. As a result, we have found that by treating waste with an aqueous solution of a specific compound, a large amount of the substances to be treated can be removed. The present invention has been completed based on the discovery that it is possible to efficiently render the molecule harmless.

すなわち、本発明の無害化方法は有害物質として有害金
属及びフッ素を含有する産業廃棄物または汚染土壌を塩
化鉄または硫酸鉄、イオウ含有化合物、及びカルシウム
化合物を含む水溶液で処理することを特徴とする。
That is, the detoxification method of the present invention is characterized by treating industrial waste or contaminated soil containing toxic metals and fluorine as hazardous substances with an aqueous solution containing iron chloride or iron sulfate, a sulfur-containing compound, and a calcium compound. .

ここで、産業廃棄物または汚染土壌に含まれる・有害物
質としては鉛(Pb)、カドミウム(Cd)、亜鉛(Z
n)、銅(Cu)、6価クロム(Cr6*)、水銀(H
g)、アルキル水銀、ヒ素(As)等の金属類、シアン
(CN)、PCB、有機塩素等があり、これらの有害物
質は塩化鉄または硫酸鉄、及びイオン含有化合物を含む
水溶液で溶出防止処理されて無害化され、有害物質とし
てさらにフッ素(F)が含まれている場合には塩化鉄ま
たは硫酸鉄、イオウ含有化合物、及びカルシウム含有化
合物を含む水溶液て溶出防止処理されて無害化される。
Here, the harmful substances contained in industrial waste or contaminated soil include lead (Pb), cadmium (Cd), and zinc (Z).
n), copper (Cu), hexavalent chromium (Cr6*), mercury (H
g), alkyl mercury, metals such as arsenic (As), cyanide (CN), PCB, organic chlorine, etc. These harmful substances are treated to prevent elution with an aqueous solution containing iron chloride or iron sulfate, and ion-containing compounds. If fluorine (F) is further included as a harmful substance, it is rendered harmless by being treated to prevent elution with an aqueous solution containing iron chloride or iron sulfate, a sulfur-containing compound, and a calcium-containing compound.

該産業廃棄物の種類は、金属くず、ガラスくず、陶磁器
くず、鉱さい、汚泥、ばいじん、もえがら、汚染土壌等
、粉状、粒状破砕物、スラリー等の形状であればよく、
このような形状でないものは粉砕、破砕等の前処理を行
なつて本発明の無害化方法を適用することができる。本
発明の処理液は、塩化鉄または硫酸鉄、イオウ化合物及
びカルシウム化合物が含まれる水溶液である。
The types of industrial waste may be in the form of metal scraps, glass scraps, ceramic scraps, slag, sludge, soot, dust, rice husks, contaminated soil, powder, crushed granules, slurry, etc.
If the shape is not such, the detoxification method of the present invention can be applied after pretreatment such as crushing or crushing. The treatment liquid of the present invention is an aqueous solution containing iron chloride or iron sulfate, a sulfur compound, and a calcium compound.

塩化鉄としては塩化第一鉄が好ましいが、少量の塩化第
二鉄等が混在していてもよい。
As the iron chloride, ferrous chloride is preferable, but a small amount of ferric chloride or the like may be mixed.

このような塩化鉄を含む水溶液としては、アルミエッチ
ング廃液等を使用することができる。硫酸鉄としては硫
酸第一鉄を用いるのがよい。イオウ化合物としては硫化
ソーダ、NaHSOJl粉末イオウ、チオ尿素等を用い
ることができるが、特に硫化ソーダを用いるのが好まし
い。
As such an aqueous solution containing iron chloride, aluminum etching waste liquid or the like can be used. As the iron sulfate, ferrous sulfate is preferably used. As the sulfur compound, sodium sulfide, NaHSOJl powdered sulfur, thiourea, etc. can be used, but it is particularly preferable to use sodium sulfide.

カルシウム化合物としては塩化カルシウム、酸化カルシ
ウム、水酸化カルシウム、セメント等を用いることがで
きるが、特に塩化カルシウムを用いるのが好ましい。上
記塩化鉄液または硫酸鉄液は20%水溶液換算で廃棄物
に対して2〜25%(重量%、以下同じ)、好ましくは
5〜20%、イオウ化合物は0.1〜5%好ましくは0
.2〜2%、カルシウム化合物は0.1〜5%好ましく
は0.1〜2%となるように配合して水溶液を調製、使
用することができる。
As the calcium compound, calcium chloride, calcium oxide, calcium hydroxide, cement, etc. can be used, but it is particularly preferable to use calcium chloride. The above-mentioned iron chloride solution or iron sulfate solution is 2 to 25% (wt%, same hereinafter), preferably 5 to 20%, based on the waste in terms of 20% aqueous solution, and the sulfur compound is 0.1 to 5%, preferably 0.
.. An aqueous solution can be prepared and used by blending the calcium compound in an amount of 2 to 2%, preferably 0.1 to 5%, and preferably 0.1 to 2%.

廃棄物の処理方法は廃棄物の形態、量、処理装置、処理
時間等に応じて適当な方法を選択することができ、例え
ばダストをペレタイザーに積み、本発明の水溶液を吹き
つけ造粒する方法をとることができる。結局、処理方法
は廃棄物と水溶液が充分接触できるような方法であれば
よい。
An appropriate method for processing waste can be selected depending on the form and amount of waste, processing equipment, processing time, etc. For example, a method in which dust is piled up in a pelletizer and granulated by spraying the aqueous solution of the present invention. can be taken. Ultimately, the treatment method may be any method that allows sufficient contact between the waste and the aqueous solution.

本発明の無害化処理方法は常温、常圧で実施し−て十分
効果的であるが、所望によつては加温、加圧等の条件を
加えてもよい。
Although the detoxification treatment method of the present invention is sufficiently effective when carried out at normal temperature and normal pressure, conditions such as heating and pressurization may be added as desired.

本発明の無害化処理方法は処理4日後の廃棄物のPHを
6.5〜9.5好ましくは7.0〜9.0にコントロー
ルして行なうのがよく、すなわち中性及び弱アルカリ性
付近で行なうのが好ましい。
The detoxification treatment method of the present invention is preferably carried out by controlling the pH of the waste after 4 days of treatment to 6.5 to 9.5, preferably 7.0 to 9.0, that is, around neutral and weak alkalinity. It is preferable to do so.

PHのコントロールは力性ソーダ、消石灰、セメント等
で行なえばよい。廃棄物は、処理により、ペレット化、
コンクリート固化、スラリー化等最終処分に適した形態
に変換することができる。本発明の産業廃棄物の無害化
方法は有害物質を含有する大量の廃棄物を一段の処理で
溶出防止無害化することができる、作業性、経済性の優
れた”方法である。さらに、有害物質として鉛(Pb)
、カドミウム(Cd)、亜鉛(Zn)、銅(Cu)、6
価クロム(Cr6つ、水銀(Hg)、アルキル化水銀、
ヒ素(,As)、シアン(CN)、PCBl有機塩素等
、さらにフッ素(F)等を含有するような廃棄物を処理
して、すべての有害物質を政令で規定された判定基準以
下に無害化することができる。
PH may be controlled using hydric soda, slaked lime, cement, etc. Waste is processed into pellets,
It can be converted into a form suitable for final disposal, such as concrete solidification or slurry. The method for detoxifying industrial waste of the present invention is a method with excellent workability and economy, which can prevent the elution of a large amount of waste containing hazardous substances and detoxify it in one step. Lead (Pb) as a substance
, cadmium (Cd), zinc (Zn), copper (Cu), 6
Valent chromium (6 Cr, mercury (Hg), alkylated mercury,
We treat waste that contains arsenic (, As), cyanide (CN), PCBl organic chlorine, etc., and fluorine (F), etc., and make all hazardous substances harmless below the criteria specified by government ordinance. can do.

また、本法によれば多種多様な形態の廃棄物を容易に無
害化することができ、その利用範囲は大である。
Moreover, according to this method, a wide variety of wastes can be easily rendered harmless, and its application range is wide.

次に本発明の実施例を挙げる。Next, examples of the present invention will be described.

実施例1 産業廃棄物として焙焼炉から発生したダストを5トン/
時間の害合でペレタイザー上に導入した。
Example 1 5 tons of dust generated from a roasting furnace as industrial waste
Due to time constraints, it was introduced onto the pelletizer.

この上から、塩化第1鉄20%、塩化カルシウム1%混
合液と4%硫化ソーダ液の水溶液を別々のノズルより吹
き付け溶出防止処理を行なつた。使用量は20%塩化第
1鉄液750k9/時間、硫化ソーダ40k9/時間、
塩化カルシウム42.5k9/時間であつた。上記ダス
トの処理前の成分分析、及び処理後の溶出液の分析結果
を後記第1表に示す。
On top of this, an aqueous solution of 20% ferrous chloride, 1% calcium chloride, and 4% sodium sulfide solution was sprayed from separate nozzles to prevent elution. The usage amount is 20% ferrous chloride liquid 750k9/hour, soda sulfide 40k9/hour,
Calcium chloride was 42.5k9/hour. The results of component analysis of the dust before treatment and analysis of the eluate after treatment are shown in Table 1 below.

溶出液の分析は以下に示す方法で行なつた。The eluate was analyzed by the method shown below.

試料液の作成;試料液の作成は、次のとおり試料と溶媒
とを混合し作成する。
Preparation of sample liquid: The sample liquid is prepared by mixing the sample and solvent as follows.

1溶媒の水素イオン濃度指数 溶媒は海洋投入処分又は海面埋立処分の場合は、海水の
PHを考慮した水素イオン濃度指数7.8〜8.3にし
、陸上埋立処分の場合は水素イオン濃度指数5.8〜6
.3になるように純水に水酸化ナトリウム又は塩酸を加
えて作成する。
1 Hydrogen ion concentration index of the solvent If the solvent is to be disposed of in the ocean or in a sea-surface landfill, the hydrogen ion concentration index should be 7.8 to 8.3, taking into account the pH of the seawater, and in the case of land landfill disposal, the hydrogen ion concentration index should be 5. .8~6
.. 3 by adding sodium hydroxide or hydrochloric acid to pure water.

2試料と溶媒の割合 試料と溶媒の割合は、下表のとおり定められている。2 Ratio of sample and solvent The ratio of sample to solvent is determined as shown in the table below.

この表に示すように試料と溶媒の重量体積比は10%の
場合と、混合液中の固型分が3%にする場合とがある。
固型分で定めているのは、汚でい等含水しやすい廃棄物
を含水率について処分基準がない海洋投入処分または海
面埋立処分する場合に、判定試験に当つて、意識的に含
水させ、事実上試料の量を減少させて、溶出する有害物
質の濃度を減少させるような抜け道を防ぐためである。
溶出の操作; 試料流を常温(おおむね2(代))、常圧(おおむね1
気圧)で振とう機(振とう回数毎分200往復、振とう
幅4〜5c!n)用いて、6時間連続振とうする。
As shown in this table, the weight/volume ratio of the sample to the solvent is sometimes 10%, and sometimes the solid content in the mixed liquid is 3%.
The solid content is determined by intentionally adding water during the judgment test when disposing of waste that easily contains water, such as dirty sewage, into the ocean or in a sea-surface landfill for which there are no disposal standards regarding water content. This is to prevent a loophole that would effectively reduce the amount of sample and thus reduce the concentration of harmful substances eluted.
Elution operation: Keep the sample flow at room temperature (approximately 2) and normal pressure (approximately 1)
Shake continuously for 6 hours using a shaker (shaking frequency: 200 reciprocations per minute, shaking width: 4-5c!n) at atmospheric pressure).

検液の作成: 溶出の操作を行つ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ベーパーを用いてろ過した
後の溶液(ろ過が著しく困難な場合は、毎分30(4)
回転で2紛間遠心分離した後上澄・み液)を検液とする
Preparation of test solution: Filter the sample solution obtained by elution using a glass fiber filter vapor with a pore size of 1 micron (if filtration is extremely difficult, filter the solution at a rate of 30 (4) per minute).
After centrifuging the two powders by rotation, use the supernatant/filtrate as the test solution.

比較例1 塩化カルシウム溶液を用いない他は、実施例1と同様に
して同じ産業廃棄物の処理を行なつた。
Comparative Example 1 The same industrial waste was treated in the same manner as in Example 1, except that the calcium chloride solution was not used.

処理後の溶出液の分析結果を第1表に示した。実施例2
産業廃棄物として、蛍光灯製造工程から発生した、水銀
含有ガラス屑をセメント用ロールミキサーに1トン(t
)投入し、混合しながら4%硫化ソーダ液50kgを加
えた後、20%塩化第一鉄液100kgを加える。
The analysis results of the eluate after treatment are shown in Table 1. Example 2
As industrial waste, 1 ton (t) of mercury-containing glass waste generated from the fluorescent lamp manufacturing process was put into a cement roll mixer.
), add 50 kg of 4% sodium sulfide solution while mixing, and then add 100 kg of 20% ferrous chloride solution.

更にセメントを100k9加え、充分に混合した。上記
ガラス屑の成分分析及び処理後の溶出液の分析結果を後
記第2表に示す。
Furthermore, 100k9 of cement was added and mixed thoroughly. The results of the component analysis of the glass waste and the analysis of the eluate after treatment are shown in Table 2 below.

比較例2 セメントを用いない他は、実施例2と同様にして同じ産
業廃棄物の処理を行なつた。
Comparative Example 2 The same industrial waste was treated in the same manner as in Example 2, except that cement was not used.

処理後の溶出液の分析結果を第2表に示した。ノ実施例
3 実施例1で用いたと同じ産業廃棄物の上に、硫酸第1鉄
24%溶液、水酸化カルシウム5%水分散液、硫化ソー
ダ4%溶液を3つの別々のノズルにより吹き付け、溶出
防止処理を行なつた。
The analysis results of the eluate after treatment are shown in Table 2. Example 3 A 24% ferrous sulfate solution, a 5% calcium hydroxide aqueous dispersion, and a 4% sodium sulfide solution were sprayed onto the same industrial waste as used in Example 1 using three separate nozzles for elution. Preventive treatment was carried out.

使用量は24%硫酸第1鉄溶液750kg/時間、硫化
ソーダ40kg/時間、水酸化カルシウム水分散液15
0kg/時間であつた。上記処理後の溶出液の分析結果
を第1表に示した。
The amount used is 750 kg/hour of 24% ferrous sulfate solution, 40 kg/hour of sodium sulfide, and 15 kg/hour of calcium hydroxide aqueous dispersion.
It was 0 kg/hour. The analysis results of the eluate after the above treatment are shown in Table 1.

Claims (1)

【特許請求の範囲】[Claims] 1 有害物質として有害金属及びフッ素を含有する産業
廃棄物または汚染土壌を塩化鉄または硫酸鉄、イオウ化
合物及びカルシウムを含む水溶液で処理することを特徴
とする産業廃棄物または汚染土壌の無害化方法。
1. A method for detoxifying industrial waste or contaminated soil, which comprises treating industrial waste or contaminated soil containing toxic metals and fluorine as hazardous substances with an aqueous solution containing iron chloride or iron sulfate, a sulfur compound, and calcium.
JP56135447A 1981-08-31 1981-08-31 Method for detoxifying industrial waste containing hazardous substances Expired JPS6043193B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56135447A JPS6043193B2 (en) 1981-08-31 1981-08-31 Method for detoxifying industrial waste containing hazardous substances

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56135447A JPS6043193B2 (en) 1981-08-31 1981-08-31 Method for detoxifying industrial waste containing hazardous substances

Publications (2)

Publication Number Publication Date
JPS5836690A JPS5836690A (en) 1983-03-03
JPS6043193B2 true JPS6043193B2 (en) 1985-09-26

Family

ID=15151924

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56135447A Expired JPS6043193B2 (en) 1981-08-31 1981-08-31 Method for detoxifying industrial waste containing hazardous substances

Country Status (1)

Country Link
JP (1) JPS6043193B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62132579A (en) * 1985-12-06 1987-06-15 Sanyo Mokuzai Boufu Kk Treatment for making waste non-polluting

Also Published As

Publication number Publication date
JPS5836690A (en) 1983-03-03

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