JPS6020077B2 - Method for treating sludge containing calcium fluoride - Google Patents

Method for treating sludge containing calcium fluoride

Info

Publication number
JPS6020077B2
JPS6020077B2 JP6110877A JP6110877A JPS6020077B2 JP S6020077 B2 JPS6020077 B2 JP S6020077B2 JP 6110877 A JP6110877 A JP 6110877A JP 6110877 A JP6110877 A JP 6110877A JP S6020077 B2 JPS6020077 B2 JP S6020077B2
Authority
JP
Japan
Prior art keywords
sludge
calcium fluoride
containing calcium
sludge containing
chromium
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
JP6110877A
Other languages
Japanese (ja)
Other versions
JPS53146464A (en
Inventor
千秋 前小屋
耕二 大谷
文雄 水庭
真次 小森
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.)
Hitachi Ltd
Mitsubishi Power Ltd
Original Assignee
Babcock Hitachi KK
Hitachi Ltd
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 Babcock Hitachi KK, Hitachi Ltd filed Critical Babcock Hitachi KK
Priority to JP6110877A priority Critical patent/JPS6020077B2/en
Publication of JPS53146464A publication Critical patent/JPS53146464A/en
Publication of JPS6020077B2 publication Critical patent/JPS6020077B2/en
Expired legal-status Critical Current

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  • Treatment Of Sludge (AREA)

Description

【発明の詳細な説明】 本発明は廃棄物処理方法に係り、特にフッ化カルシウム
を含有するスラツジの無害化処理方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a waste treatment method, and particularly to a method for detoxifying sludge containing calcium fluoride.

半導体製造プロセスやメッキ作業等においてフッ素化合
物を用いた処理を行うが、処理後の廃水にはフッ素を始
め、クロム、亜鉛等の有害物質が含有されている。
Fluorine compounds are used in semiconductor manufacturing processes and plating operations, but the wastewater after treatment contains fluorine as well as harmful substances such as chromium and zinc.

これを無害化するため、通常消石灰あるいは石灰石等の
カルシウムを加えてフッ素をフッ化カルシウムに、クロ
ムや亜鉛等の重金属を水酸化物として、これを沈殿分離
することにより無害な排水として放流する。生成した沈
殿物(スラッジ)にはフツ化カルシウムや夫反応のカル
シウム塩の他、種々の成分の水酸化物が含有するため、
有効な再生利用が難かしく、また、水分を70%前後含
有する泥状物であるので屋外投棄が困難で、現状ではビ
ットを堀り保管しているが、排出量の増加により処理が
困難になつきた。このフツ化カルシウムを含むスラツジ
の無害化処理法として高温焼成処理がある。これは上記
スラツジを1000qo以上で焼成するもので、スラッ
ジ量を大中に低減することができるとともに、暁給体か
らのフッ素やクロム等の有害物質の水への溶解量(溶出
)を原スラッジに比較して大中に低下させることができ
る。しかし、上記方法で競結した競結体からは処理条件
によって、六価クロムが溶出することがある。このため
、スラッジに粘土などの添加物を混合して焼成し、クロ
ムをスピネル構造(M○・Cr203)として安定化し
ている。この方法はスラッジに10%以上の添加物を混
合するため、焼結体の量が増大するという欠点がある。
本発明の目的は、フツ化カルシウムを含有するスラッジ
を焼成処理する際、少量の添加物を加えることにより、
無害な焼結体を得ることにある。本発明は、フッ化カル
シウムを含有するスラッジに硫酸ヒドロキシルアミンよ
りなる還元剤を混合して1000〜1200午○で焼成
することにより、競鯖体からの六価クロムの港出を低下
させる焼結方法を提供することにある。すなわち、実験
によるとフツ化カルシウム含有スラッジを1050〜1
100つ○で焼成すると良好な競結体を得ることができ
るが、この際、スラツジ中の鉄の濃度が大きくなると、
暁縞体からの六価クロムの溶出が増大することが明らか
になった。
In order to render this waste harmless, calcium such as slaked lime or limestone is usually added, fluorine is converted into calcium fluoride, and heavy metals such as chromium and zinc are converted into hydroxides, which are precipitated and separated to be discharged as harmless wastewater. The generated precipitate (sludge) contains calcium fluoride and calcium salts from the reaction, as well as hydroxides of various components.
It is difficult to recycle effectively, and since it is a slurry containing around 70% water, it is difficult to dump it outdoors.Currently, the bits are dug up and stored, but the increasing amount of waste makes it difficult to dispose of them. I got used to it. A high-temperature firing process is a method for detoxifying sludge containing calcium fluoride. This method involves burning the above sludge at a pressure of 1,000 qo or more, which makes it possible to reduce the amount of sludge to a large extent, and also to reduce the amount of harmful substances such as fluorine and chromium dissolved in water (elution) from the raw sludge from the feeder. It can be lowered to large compared to . However, depending on the processing conditions, hexavalent chromium may be eluted from the aggregates formed by the above method. For this reason, additives such as clay are mixed with the sludge and fired to stabilize the chromium as a spinel structure (M○・Cr203). This method has the disadvantage that the amount of sintered bodies increases because 10% or more of additives are mixed into the sludge.
The purpose of the present invention is to add a small amount of additives when calcining sludge containing calcium fluoride.
The objective is to obtain a harmless sintered body. The present invention is a sintering method that reduces the release of hexavalent chromium from competitive mackerel by mixing a reducing agent made of hydroxylamine sulfate with sludge containing calcium fluoride and firing it for 1,000 to 1,200 hours. The purpose is to provide a method. That is, according to experiments, the sludge containing calcium fluoride was
A good composite can be obtained by firing with 100 pieces, but at this time, if the concentration of iron in the sludge increases,
It was revealed that the elution of hexavalent chromium from the dawn stripes increased.

これは、スラツジを加熱すると、スラツジ中の鉄はFe
203となるが、105000以上になると次の反応に
より、餌e203→がe304十(0) 鉄の酸化物としては極めて安定なFe304と化学的に
活性な酸素が生成する。
This means that when the sludge is heated, the iron in the sludge becomes Fe.
203, but when it reaches 105,000 or more, the following reaction produces Fe304, which is extremely stable as an iron oxide, and chemically active oxygen.

さらにこの酸素がスラッジ中のクロムと次のような反応
により、Cr203十3(0)一本の3 六価クロムを生成するものと考えられる。
Furthermore, it is thought that this oxygen reacts with chromium in the sludge in the following manner to produce one Cr2033(0) 36-valent chromium.

ここで、スラッジ中の鉄を比較的低温でFe304とし
て存在させるため、スラツジと鉄の還元剤である硫酸ヒ
ドロキシルアミンを混合すると、スラツジ中の鉄はFe
(OH)2として保持され、これを加熱するとFe20
3を経ないでFe304が生成され、1050qo以上
でも酸素の発生が起らないので、六価クロムも生成され
ない。
Here, in order to make the iron in the sludge exist as Fe304 at a relatively low temperature, when the sludge and hydroxylamine sulfate, which is a reducing agent for iron, are mixed, the iron in the sludge becomes Fe304.
It is retained as (OH)2, and when heated, Fe20
Fe304 is generated without passing through 3, and no oxygen is generated even at 1050 qo or more, so hexavalent chromium is not generated either.

以下実施例を用いて説明する。フッ化カルシウムを含有
する水分70%のスラッジA(水分を除いたときの主な
成分は、フッ化カルシウム20%、酸化マグネシウム2
0%、リン酸カルシウム15%、酸化カルシウム10%
)と、このスラツジに5%の水酸化第二鉄を混合したも
のB、さらに、Bのスラッジに硫酸ヒドロキシルアミン
を3%混合したものCを、焼成温度を1000〜110
0℃の範囲にて焼成したときの溶出量の変化を図に示す
This will be explained below using examples. Sludge A containing calcium fluoride with 70% water content (after removing water, the main components are 20% calcium fluoride, 22% magnesium oxide)
0%, calcium phosphate 15%, calcium oxide 10%
), this sludge mixed with 5% ferric hydroxide B, and the sludge B mixed with 3% hydroxylamine sulfate C were heated at a firing temperature of 1000 to 110°C.
The figure shows the change in elution amount when firing in the range of 0°C.

ここで六価クロムの溶出量は焼結体10夕を純水100
の上中で6時間かくはんした後の炉液中の濃度である。
試料Aではいずれの焼成温度でも六価クロムの溶出量は
少なく問題はない。
Here, the elution amount of hexavalent chromium is 10 times the sintered body and 100 times the pure water.
This is the concentration in the furnace solution after stirring for 6 hours in the upper part of the furnace.
In sample A, the amount of hexavalent chromium eluted is small at any firing temperature, and there is no problem.

試料BではFe(OH)3を5%添加したために、焼成
温度が1050℃付近で六価クロムが4ppm前後と有
害な産業廃棄物に係る判定基準の1.5ppmを大中に
越えている。さらに試料Cでは、硫酸ヒドロキシルアミ
ンを3%添加することにより、焼成温度が1050二0
付近でもlppm以下となり、規準値を満足しており、
硫酸ヒドロキシルアミンがクロムの溶出を低下させる効
果があることがわかる。本発明によればフツ化カルシウ
ムを含有するスラッジを焼成する際、暁縞体からの六価
クロムの溶出を防止するため、従来法では粘土などの添
加物を10%以上混合していたものを、少量の添加物を
混合することにより、良質な暁鯖体を得ることが可能に
なった。
In sample B, since 5% of Fe(OH)3 was added, the hexavalent chromium content was around 4 ppm at a firing temperature of around 1050°C, significantly exceeding the 1.5 ppm criterion for hazardous industrial waste. Furthermore, in sample C, by adding 3% hydroxylamine sulfate, the firing temperature was increased to 105020.
Even in the vicinity, it is below lppm, satisfying the standard value,
It can be seen that hydroxylamine sulfate is effective in reducing chromium elution. According to the present invention, when calcining sludge containing calcium fluoride, in order to prevent the elution of hexavalent chromium from the dawn stripes, additives such as clay are mixed in at least 10% in the conventional method. By mixing small amounts of additives, it became possible to obtain high quality Akatsuki mackerel.

【図面の簡単な説明】[Brief explanation of the drawing]

焼成温度と六価クロムの関係を示す図。 A diagram showing the relationship between firing temperature and hexavalent chromium.

Claims (1)

【特許請求の範囲】[Claims] 1 フツ化カルシウムとクロムと3価の鉄とを含有する
スラツジを高温処理する際、上記スラツジに硫酸ヒドロ
キシルアミンを添加して鉄を2価に保持したのち、10
00〜1200℃で焼成することを特徴とするフツ化カ
ルシウム含有スラツジの処理方法。
1 When sludge containing calcium fluoride, chromium, and trivalent iron is treated at high temperature, hydroxylamine sulfate is added to the sludge to keep the iron divalent, and then 10
A method for treating sludge containing calcium fluoride, which comprises firing at a temperature of 00 to 1200°C.
JP6110877A 1977-05-27 1977-05-27 Method for treating sludge containing calcium fluoride Expired JPS6020077B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6110877A JPS6020077B2 (en) 1977-05-27 1977-05-27 Method for treating sludge containing calcium fluoride

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6110877A JPS6020077B2 (en) 1977-05-27 1977-05-27 Method for treating sludge containing calcium fluoride

Publications (2)

Publication Number Publication Date
JPS53146464A JPS53146464A (en) 1978-12-20
JPS6020077B2 true JPS6020077B2 (en) 1985-05-20

Family

ID=13161544

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6110877A Expired JPS6020077B2 (en) 1977-05-27 1977-05-27 Method for treating sludge containing calcium fluoride

Country Status (1)

Country Link
JP (1) JPS6020077B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6261205B2 (en) * 1984-01-30 1987-12-21 Mitsubishi Chem Ind

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6261205B2 (en) * 1984-01-30 1987-12-21 Mitsubishi Chem Ind

Also Published As

Publication number Publication date
JPS53146464A (en) 1978-12-20

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