JPH0757348B2 - Method for treating fluorine in wastewater - Google Patents
Method for treating fluorine in wastewaterInfo
- Publication number
- JPH0757348B2 JPH0757348B2 JP34474292A JP34474292A JPH0757348B2 JP H0757348 B2 JPH0757348 B2 JP H0757348B2 JP 34474292 A JP34474292 A JP 34474292A JP 34474292 A JP34474292 A JP 34474292A JP H0757348 B2 JPH0757348 B2 JP H0757348B2
- Authority
- JP
- Japan
- Prior art keywords
- fluorine
- wastewater
- mixed solution
- cryolite
- waste water
- 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 - Fee Related
Links
Landscapes
- Removal Of Specific Substances (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、廃水中のフッ素を処理
する方法に関する。FIELD OF THE INVENTION The present invention relates to a method for treating fluorine in waste water.
【0002】[0002]
【従来の技術】従来、この種の廃水中のフッ素を処理す
る方法としては、フッ素を含有する廃水中に、予め混合
したアルミニウムとナトリウムの可溶性塩類の混合液を
反応当量程度添加して、氷晶石(oryolite:N
a3AlF6)を生成させた後、氷晶石を分離除去し、残
留フッ素を含有する廃水中でフッ化カルシウム(cal
oium fluoride:CaF2)を生成せしめ
る方法が知られている(特願平3−35004号,特願
平3−35005号参照)。2. Description of the Related Art Conventionally, as a method of treating fluorine in waste water of this type, a mixed solution of aluminum and sodium soluble salts, which has been mixed in advance, is added to a waste water containing fluorine in a reaction equivalent amount and iced. Orylite: N
a 3 AlF 6 ), the cryolite is separated and removed, and calcium fluoride (cal) is added in the waste water containing residual fluorine.
There is known a method for producing oium fluoride: CaF 2 (see Japanese Patent Application Nos. 3-35004 and 3-35005).
【0003】上述した従来例においては、添加するアル
ミニウムとナトリウムの可溶性塩類混合液の添加量は、
中和適定法などにより廃水中のフッ素濃度を測定し、そ
の結果をもとに決定していた(以降、この方法を氷晶石
法という)。In the above-mentioned conventional example, the addition amount of the soluble salt mixture of aluminum and sodium to be added is
The concentration of fluorine in the wastewater was measured by the neutralization titration method, and the result was used for determination (hereinafter, this method is called cryolite method).
【0004】[0004]
【発明が解決しようとする課題】従来の氷晶石法では、
氷晶石生成に必要な薬剤の添加量は、廃水中のフッ素濃
度を測定し、その結果をもとに決定していたため、薬剤
添加量の決定操作が煩雑であるという欠点があった。[Problems to be Solved by the Invention] In the conventional cryolite method,
The addition amount of the chemical agent necessary for the production of cryolite was determined based on the result of measuring the fluorine concentration in the waste water, and thus the operation of determining the addition amount of the chemical agent was complicated.
【0005】本発明の目的は、薬剤添加量の決定操作を
容易にした氷晶石生成によるフッ素処理方法を提供する
ことにある。An object of the present invention is to provide a method for fluorine treatment by producing cryolite, which facilitates the operation of determining the amount of added chemicals.
【0006】[0006]
【課題を解決するための手段】上記目的を達成するた
め、本発明による廃水中のフッ素を処理する方法におい
ては、フッ素を含有する廃水中に反応当量程度のアルミ
ニウムとナトリウムの可溶性塩類の混合液を添加し、廃
水中に分離可能な氷晶石を生成させる廃水中のフッ素を
処理する方法であって、氷晶石の生成に必要な前記混合
液の反応当量の決定は、廃水中の電気伝導度の変化を検
知しつつ行うものである。In order to achieve the above object, in the method for treating fluorine in waste water according to the present invention, a mixed solution of aluminum and sodium soluble salts in the waste water containing fluorine in a reaction equivalent amount. Is a method of treating fluorine in wastewater to form separable cryolite in the wastewater, wherein the reaction equivalence of the mixed solution necessary for the production of cryolite is determined by It is performed while detecting the change in conductivity.
【0007】また、アルミニウムとナトリウムの可溶性
塩類の混合液を徐々に添加し、電気伝導度の極小点を検
出した時点で前記混合液の添加を終了するものである。Further, a mixed solution of soluble salts of aluminum and sodium is gradually added, and the addition of the mixed solution is terminated when the minimum point of electric conductivity is detected.
【0008】[0008]
【作用】フッ素を含有する廃水中で氷晶石を生成する
際、添加するアルミニウムとナトリウムは、反応当量程
度にする必要がある。フッ素を含有する廃水中の電気伝
導度をpH計で測定しながら、アルミニウムとナトリウ
ム可溶性塩類の混合溶液を徐々に添加していくと、氷晶
石の生成に伴い、溶液中のpHは徐々に低下し、反応当
量の可溶性塩類の混合液を添加した時点でpHが極小と
なる。また、残存フッ素イオン濃度も同様に推移し、p
Hが極小となる点で最低となる。すなわち、反応槽中の
電気伝導度の変化をpH計を用いて測定し、pHが極小
となる点を検出することにより、アルミニウムとナトリ
ウム可溶性塩類の混合液の添加量を決定する。[Function] When producing cryolite in waste water containing fluorine, aluminum and sodium to be added must be in a reaction equivalent amount. When the mixed solution of aluminum and sodium-soluble salts was gradually added while measuring the electrical conductivity of waste water containing fluorine with a pH meter, the pH of the solution gradually increased with the formation of cryolite. The pH becomes minimal and the pH becomes a minimum when the reaction solution of the mixed solution of soluble salts is added. In addition, the residual fluorine ion concentration also changes, and p
It is the lowest at the point where H becomes a minimum. That is, the amount of addition of the mixed solution of aluminum and sodium-soluble salts is determined by measuring the change in the electric conductivity in the reaction tank using a pH meter and detecting the point where the pH becomes a minimum.
【0009】[0009]
【実施例】以下、本発明の実施例について説明する。図
1は本発明の全体フロー図、図2は薬剤添加量とpHと
の関係を示す図である。EXAMPLES Examples of the present invention will be described below. FIG. 1 is an overall flow chart of the present invention, and FIG. 2 is a diagram showing a relationship between a drug addition amount and pH.
【0010】本実施例においては、フッ化アンモニウム
とフッ酸を含有するフッ素イオン濃度50,000mg
/l,pH6.3のフッ素含有廃水1を1000ml反
応槽2に注入し、フッ素含有廃水1を反応槽2中で緩や
かに撹拌しながら、Na,Al混合溶液供給装置3から
ポリ塩化アルミニウム(工業用Al2O3 10%)と塩
化ナトリウム溶液(Naとして98.3g/l)を30
0:480の割合に混合した溶液をフッ素含有廃水1中
に徐々に添加しつつ、そのフッ素含有廃水1中の電気伝
導度をpH計4で測定した。混合溶液のpHは3.5で
あった。混合溶液の添加に伴い、反応槽1におけるフッ
素含有廃水1中のpHが徐々に低下し、pH3.7で極
小となった。反応槽2におけるフッ素含有廃水1中のp
hが極小となったことをピーク検出器5を用いて検出
し、その検出信号に基づいて制御器6によりNa,Al
混合溶液供給装置3の駆動を停止し、混合溶液の廃水1
への添加を停止した。このpHが極小となった時の混合
溶液添加量は、廃水1中の含有フッ素に対して氷晶石を
生成する反応当量である。また、沈澱した氷晶石を分離
除去し、反応槽2内の溶液中に残存するフッ素濃度をJ
IS K0102により測定した。測定の結果、残存フ
ッ素濃度は150mg/lであった。In this embodiment, the concentration of fluorine ion containing ammonium fluoride and hydrofluoric acid is 50,000 mg.
/ L, fluorine-containing wastewater 1 having a pH of 6.3 is injected into the reaction tank 2 of 1000 ml, and the fluorine-containing wastewater 1 is gently stirred in the reaction tank 2 while the Na / Al mixed solution supply device 3 supplies polyaluminum chloride Al 2 O 3 10%) and sodium chloride solution (98.3 g / l as Na) for 30
While the solution mixed at a ratio of 0: 480 was gradually added to the fluorine-containing wastewater 1, the electrical conductivity of the fluorine-containing wastewater 1 was measured with a pH meter 4. The pH of the mixed solution was 3.5. With the addition of the mixed solution, the pH of the fluorine-containing wastewater 1 in the reaction tank 1 gradually decreased, and became the minimum at pH 3.7. P in the fluorine-containing wastewater 1 in the reaction tank 2
The peak detector 5 is used to detect that h is minimized, and the controller 6 controls the Na and Al based on the detection signal.
The driving of the mixed solution supply device 3 is stopped, and the mixed solution waste water 1
Was stopped. The amount of the mixed solution added when the pH becomes the minimum is the reaction equivalent amount for producing cryolite with respect to the fluorine contained in the wastewater 1. The precipitated cryolite was separated and removed, and the concentration of fluorine remaining in the solution in the reaction tank 2 was adjusted to J
It was measured according to IS K0102. As a result of the measurement, the residual fluorine concentration was 150 mg / l.
【0011】[0011]
【発明の効果】以上のように本発明によれば、フッ素含
有廃水に対して処理反応槽中の電気伝導度変化を利用し
て、反応当量程度のアルミニウムとナトリウムの可溶性
塩類の混合液を添加して氷晶石を生成させるため、氷晶
石を生成する段階での薬剤量の決定が非常に容易とな
り、また複雑な制御装置を必要としないという利点があ
る。As described above, according to the present invention, a mixture of aluminum and sodium soluble salts in a reaction equivalent amount is added to the fluorine-containing wastewater by utilizing the change in electric conductivity in the treatment reactor. Since the cryolite is produced by the above method, it is very easy to determine the amount of the drug at the stage of producing the cryolite, and there is an advantage that a complicated control device is not required.
【図1】本発明の全体フローを表した図である。FIG. 1 is a diagram showing an overall flow of the present invention.
【図2】薬剤添加量とpHとの関係を表した図である。FIG. 2 is a diagram showing a relationship between a drug addition amount and pH.
1 フッ素含有廃水 2 反応槽 3 Na,Al混合溶液供給装置 4 pH計 5 ピーク検出器 6 制御器 1 Fluorine-containing wastewater 2 Reaction tank 3 Na / Al mixed solution supply device 4 pH meter 5 Peak detector 6 Controller
Claims (2)
のアルミニウムとナトリウムの可溶性塩類の混合液を添
加し、廃水中に分離可能な氷晶石を生成させる廃水中の
フッ素を処理する方法であって、 氷晶石の生成に必要な前記混合液の反応当量の決定は、
廃水中の電気伝導度の変化を検知しつつ行うものである
ことを特徴とする廃水中のフッ素を処理する方法。1. A method of treating fluorine in waste water, which comprises adding a mixture of soluble salts of aluminum and sodium in a reaction equivalent amount to waste water containing fluorine, and producing separable cryolite in the waste water. Therefore, the determination of the reaction equivalent of the mixed solution necessary for the production of cryolite is
A method for treating fluorine in wastewater, which is performed while detecting a change in electrical conductivity in the wastewater.
の混合液を徐々に添加し、電気伝導度の極小点を検出し
た時点で前記混合液の添加を終了することを特徴とする
請求項1に記載の廃水中のフッ素を処理する方法。2. The method according to claim 1, wherein a mixed solution of soluble salts of aluminum and sodium is gradually added, and the addition of the mixed solution is terminated when the minimum point of electrical conductivity is detected. Method for treating fluorine in wastewater.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP34474292A JPH0757348B2 (en) | 1992-12-24 | 1992-12-24 | Method for treating fluorine in wastewater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP34474292A JPH0757348B2 (en) | 1992-12-24 | 1992-12-24 | Method for treating fluorine in wastewater |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH06190372A JPH06190372A (en) | 1994-07-12 |
| JPH0757348B2 true JPH0757348B2 (en) | 1995-06-21 |
Family
ID=18371630
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP34474292A Expired - Fee Related JPH0757348B2 (en) | 1992-12-24 | 1992-12-24 | Method for treating fluorine in wastewater |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0757348B2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20010097375A (en) * | 2000-04-21 | 2001-11-08 | 이희창 | The method for making goods to use instead for cryolite |
| JP4599307B2 (en) * | 2006-01-30 | 2010-12-15 | 森田化学工業株式会社 | Method for recovering fluorine compounds from fluorine-containing waste liquid |
| CN117105361B (en) * | 2023-08-21 | 2025-10-31 | 北京翰祺环境技术股份有限公司 | Treatment method, device and computer readable medium for controlling fluorine-containing wastewater |
-
1992
- 1992-12-24 JP JP34474292A patent/JPH0757348B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH06190372A (en) | 1994-07-12 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4207157A (en) | Method for controlling halogen ion concentration in a photographic processing solution | |
| Lingane | A study of the lanthanum fluoride membrane electrode for end point detection in titrations of fluoride with thorium, lanthanum, and calcium | |
| US4030548A (en) | Economically dissolving barium sulfate scale with a chelating agent | |
| Elofson et al. | Application of the dropping mercury electrode to diazo chemistry | |
| US3700450A (en) | Regeneration of bleach-fix solutions used in photographic processing | |
| Ferguson et al. | A model for aluminum phosphate precipitation | |
| US3634088A (en) | Regeneration of blix solutions used in photographic processing | |
| JPH0757348B2 (en) | Method for treating fluorine in wastewater | |
| Erwin et al. | The crystallization and dissolution of sodium urate | |
| JP2530711B2 (en) | Method and apparatus for simultaneous quantitative analysis of free acid and ferric ion in solution | |
| Dubravčić | Determination of iodine in common salt by the catalytic reduction of ceric ions | |
| JPH0144118B2 (en) | ||
| TWI885977B (en) | pH value controlled cryolite crystallization method for removing fluoride | |
| JPH1076278A (en) | Apparatus for controlling addition of phosphorus removing agent | |
| Forsman | Coulometric titration of penicillins and penicillamine with mercury (II) | |
| WO2016157452A1 (en) | Method for treating wastewater, and system for treating wastewater | |
| Briggs et al. | The physical chemistry of dyeing | |
| Sekerka et al. | Simultaneous determination of total, non-carbonate and carbonate water hardnesses by direct potentiometry | |
| JPH09314123A (en) | Apparatus for controlling addition of phosphorus removing agent | |
| Johannesson | Determination of microgram quantities of free iodine using o-tolidine reagent | |
| Radić et al. | Kinetic-potentiometric determination of aluminium in acidic solution using a fluoride ion-selective electrode | |
| JP2522536B2 (en) | Method and apparatus for simultaneous quantitative analysis of free acid and iron ion in solution | |
| JPH0635968B2 (en) | Method for continuous flow analysis of colloidal charge | |
| Eliezer et al. | Potentiometric study of mixed cadmium halide complexes in aqueous solution | |
| Calokerinos et al. | Indirect potentiometric determination of sulphide with a cadmium ion-selective electrode |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |