JPH0790228B2 - Treatment method for fluorine-containing wastewater - Google Patents
Treatment method for fluorine-containing wastewaterInfo
- Publication number
- JPH0790228B2 JPH0790228B2 JP61180027A JP18002786A JPH0790228B2 JP H0790228 B2 JPH0790228 B2 JP H0790228B2 JP 61180027 A JP61180027 A JP 61180027A JP 18002786 A JP18002786 A JP 18002786A JP H0790228 B2 JPH0790228 B2 JP H0790228B2
- Authority
- JP
- Japan
- Prior art keywords
- fluorine
- wastewater
- concentration
- aluminum
- ppm
- 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
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Description
【発明の詳細な説明】 [産業上の利用分野] 本発明はフッ素含有排水の処理方法に関し、詳しくはフ
ッ素を高濃度で含み、かつホウ素が共存する排水の処理
方法に関する。TECHNICAL FIELD The present invention relates to a method for treating fluorine-containing wastewater, and more particularly to a method for treating wastewater containing fluorine in a high concentration and containing boron.
[従来の技術] フッ素含有排水としては、たとえば石炭燃焼排ガスをカ
ルシウム化合物などを含む吸収液で処理する排煙脱硫装
置から排出される排水等がある。[Prior Art] Examples of fluorine-containing wastewater include wastewater discharged from a flue gas desulfurization apparatus that treats coal combustion exhaust gas with an absorbent containing a calcium compound or the like.
通常、排水中においてフッ素は溶解度が小さく、カルシ
ウムと反応させてフッ化カルシウムを生成させることに
よって除去することができる。しかしながら、排水中に
ホウ素も含まれていると、フッ素と反応してフルオロホ
ウ酸等のホウフッ化物が生成するため、通常の方法では
除去することが困難である。Usually, fluorine has a low solubility in waste water and can be removed by reacting with calcium to produce calcium fluoride. However, if the wastewater also contains boron, it reacts with fluorine to form a borofluoride such as fluoroboric acid, so that it is difficult to remove it by an ordinary method.
そこで、フッ素含有排水の処理にあたり、アルミニウム
化合物を添加する方法が提案されている(Gypsum & Li
me、No.133,1974年)。ここで、アルミニウム化合物と
しては硫酸アルミニウム(硫酸バン土)やポリ塩化アル
ミニウム(PAC)が使用されている。通常のフッ素含有
排水はフッ素濃度300ppm以下であり、ホウ素濃度も15pp
m以下であるため、これらアルミニウム化合物を用いる
排水処理法によって一応の成果を挙げている。Therefore, a method of adding an aluminum compound to the treatment of fluorine-containing wastewater has been proposed (Gypsum & Li
me, No.133, 1974). Here, as the aluminum compound, aluminum sulfate (van sulfate earth) or polyaluminum chloride (PAC) is used. Normal fluorine-containing wastewater has a fluorine concentration of 300 ppm or less and a boron concentration of 15 pp
Since it is less than m, the wastewater treatment method using these aluminum compounds has achieved some results.
[発明が解決しようとする問題点] しかしながら、本発明者らの研究により、排水中のフッ
素およびホウ素のいずれか一方の濃度が通常の値よりも
高い場合、特にホウ素濃度が高くなると、フッ素の除去
が困難となり、硫酸バン土やPACの添加量の大巾な増加
を必要とし、フッ素やホウ素の濃度がさらに高くなる
と、これらアルミニウム化合物を使用しても安定した処
理を行うことが出来なくなることを知見した。[Problems to be Solved by the Invention] However, studies by the present inventors have revealed that when the concentration of either fluorine or boron in the wastewater is higher than a normal value, especially when the concentration of boron is high, It becomes difficult to remove it, and it is necessary to drastically increase the addition amount of vanadium sulfate and PAC. If the concentration of fluorine or boron becomes higher, stable treatment cannot be performed even if these aluminum compounds are used. I found out.
排水処理のために用いる硫酸バン土やPACの添加量が増
加することは、単に処理コストを高くするだけでなく、
下流側でのNaOH等の使用量増加につながり、さらにはス
ラッジ量が増加することになり、新たな公害問題の発生
が避けられない。また、硫酸バン土使用量の増加は処理
水中の硫酸イオン濃度の増加をもたらし、石膏スケーリ
ングの発生という問題点がある。さらに、硫酸バン土や
PACの使用は凝集剤であることから水酸化アルミニウム
等の沈着やスケーリングの発生を伴うため、安定した排
水処理を行えないという重大な欠点がある。Increasing the amount of van sulphate soil and PAC used for wastewater treatment not only increases the treatment cost, but also
This leads to an increase in the amount of NaOH, etc. used on the downstream side, which in turn increases the amount of sludge, which inevitably causes new pollution problems. In addition, an increase in the amount of van sulphate soil used causes an increase in the concentration of sulfate ions in the treated water, which causes the problem of gypsum scaling. In addition,
Since the use of PAC is a coagulant, it is accompanied by the deposition of aluminum hydroxide and the like and scaling, which has a serious drawback that stable wastewater treatment cannot be performed.
一般に、排水量はフッ素やホウ素の濃度によって決めら
れるものではなく、液中の塩素イオン濃度やシール水
量、洗浄水量等の排煙脱硫装置系の水バランスにより決
められるものである。Generally, the amount of wastewater is not determined by the concentration of fluorine or boron, but is determined by the water balance of the flue gas desulfurization system such as the concentration of chlorine ions in the liquid, the amount of sealing water, the amount of washing water, etc.
しかし、排水規制の強化,工業用水の使用制限の強化等
の実情から、排水量の低減が強く望まれている。そのた
め、処理水の塩素イオン濃度についての対策や洗浄方法
の改良等が行われており、排水量を低減するための試み
がなされつつある。However, due to actual conditions such as tightening of regulations on wastewater and tightening of restrictions on use of industrial water, reduction of wastewater is strongly desired. Therefore, countermeasures for the chlorine ion concentration of the treated water, improvement of the cleaning method, and the like are being carried out, and attempts are being made to reduce the amount of wastewater.
燃料である石炭は、そほ産地等により組成が変化するた
め、石炭燃焼排ガスを処理したときに排出される排水中
のフッ素やホウ素の濃度も様々に変化する。排水中にお
けるこれら成分の濃度変化、特に通常よりも高濃度とな
った場合、前記した従来技術で対応することは技術的に
困難であるばかりでなく、経済的にも不利である。Since the composition of coal, which is a fuel, changes depending on the production site of Soho, the concentrations of fluorine and boron in the wastewater discharged when the coal combustion exhaust gas is treated also change variously. When the concentration of these components in the waste water changes, especially when the concentration is higher than usual, it is not only technically difficult to cope with the above-mentioned conventional techniques, but also economically disadvantageous.
なお、フッ素を高濃度に含有する排水の処理を容易にす
るために、希釈して排水量を増加することは、前記した
排水規制の立場から実現性が困難である。It is difficult to dilute and increase the amount of wastewater in order to facilitate the treatment of wastewater containing a high concentration of fluorine from the standpoint of the above-mentioned wastewater regulation.
[問題点を解決するための手段] 本発明は上記のような背景のもとに完成されたものであ
る。[Means for Solving Problems] The present invention has been completed based on the above background.
すなわち本発明は、石炭燃焼排ガスをカルシウム化合物
を含む吸収液で処理して得られ、フッ素濃度が500ppm以
上であり、かつホウ素を含む排水にカルシウム化合物を
加えてpH調整後、アルミニウム濃度が300〜600ppmとな
るように塩化アルミニウムを添加して反応を行い、次い
てカルシウム化合物を含む溶液で処理することを特徴と
するフッ素含有排水の処理方法を提供するものである。That is, the present invention is obtained by treating coal combustion exhaust gas with an absorbing solution containing a calcium compound, the fluorine concentration is 500 ppm or more, and after adjusting the pH by adding the calcium compound to the wastewater containing boron, the aluminum concentration is 300 ~. The present invention provides a method for treating fluorine-containing wastewater, which comprises adding aluminum chloride to 600 ppm to cause a reaction, and then treating with a solution containing a calcium compound.
本発明の対象となる排水は、上記の如くフッ素を高濃度
に含み、かつホウ素を含有するものである。このような
排水として、たとえば石炭燃焼排ガスを適当な吸収剤、
たとえばカルシウム化合物を含有する吸収液で処理する
排煙脱硫装置から排出される排水などを挙げることがで
きる。The wastewater to be the subject of the present invention contains fluorine at a high concentration and also contains boron as described above. As such wastewater, for example, coal combustion exhaust gas, a suitable absorbent,
For example, waste water discharged from a flue gas desulfurization apparatus that is treated with an absorbent containing a calcium compound can be used.
本発明の方法は、フッ素濃度500ppm以上、通常は500〜3
000ppm程度であり、かつ40ppm以上、通常は40〜300ppm
程度のホウ素を含有する排水に対して好適に適用するこ
とができる。The method of the present invention has a fluorine concentration of 500 ppm or more, usually 500 to 3
000ppm or so and 40ppm or more, usually 40-300ppm
It can be preferably applied to wastewater containing a certain amount of boron.
塩化アルミニウムは、上記排水のpH調整後に加えられ、
その使用量は、上記排水中のフッ素を除去しうる量でよ
いが、通常はアルミニウム濃度が300〜600ppmとなるよ
うに用い、その形態は粉状,液状など任意であるが、水
溶液が取扱上最も好ましい。Aluminum chloride is added after adjusting the pH of the wastewater,
The amount used may be an amount capable of removing the fluorine in the wastewater, but it is usually used so that the aluminum concentration is 300 to 600 ppm, and its form is arbitrary such as powdery or liquid, but an aqueous solution is easy to handle. Most preferred.
塩化アルミニウムを添加すると、排水中のフッ素、たと
えばホウ素と結合してフルオロホウ酸などのホウフッ化
物として存在するフッ素は分解し、さらに共沈凝集効果
により系外に除去することができる。排水中のホウフッ
化物の分解には、アルミニウムイオンの存在が必要であ
る。硫酸バン土やPACは凝集剤としての作用が強く発現
するため、液中にアルミニウムイオンとして溶解し難い
が、塩化アルミニウムは容易に解離してアルミニウムイ
オンを形成する。さらに、塩素イオンの増加から溶解カ
ルシウム濃度が増加するため、溶解度積からフッ素除去
効果のあるフッ化カルシウムの生成が促進され、フッ素
の除去率が向上する。そのため、少ない添加量で効率よ
くフッ素を除去することができる。When aluminum chloride is added, fluorine in the waste water, for example, fluorine that is present as borofluoride such as fluoroboric acid by combining with boron is decomposed and can be removed to the outside of the system by a coprecipitation agglomeration effect. The presence of aluminum ions is required for the decomposition of borofluorides in waste water. Bansulfate and PAC strongly act as a flocculant, and are difficult to dissolve as aluminum ions in the liquid, but aluminum chloride easily dissociates to form aluminum ions. Furthermore, since the concentration of dissolved calcium increases due to an increase in chlorine ions, the production of calcium fluoride having a fluorine removing effect is promoted from the solubility product, and the removal rate of fluorine improves. Therefore, fluorine can be efficiently removed with a small addition amount.
なお、必要に応じてpH調整のために塩酸を添加してもよ
い。また、塩化アルミニウムによる反応後にカルシウム
化合物を含む溶液で処理してフッ化カルシウムとしてフ
ッ素を除去する。If necessary, hydrochloric acid may be added to adjust the pH. Further, after the reaction with aluminum chloride, it is treated with a solution containing a calcium compound to remove fluorine as calcium fluoride.
[発明の効果] 本発明によれば、ホウ素と共に高濃度のフッ素を含有す
る排水を効率よく処理することができる。特に、排水量
の低減という要請を満足しつつ排水中のフッ素処理を行
うことができる。しかも、塩化アルミニウムを選択、使
用したことにより、従来の硫酸イオンに起因する石膏ス
ケールの発生がなく、石膏スラッジの生成がなく、安定
した状態で排水処理を行うことが可能となった。また、
塩化アルミニウムは凝集剤として作用が小さいため、配
管,タンク類への沈着やスケーリングの進行発生が極め
て小さい。[Effects of the Invention] According to the present invention, wastewater containing a high concentration of fluorine together with boron can be efficiently treated. In particular, it is possible to perform the fluorine treatment in the waste water while satisfying the request for reducing the waste water amount. Moreover, by selecting and using aluminum chloride, it has become possible to perform wastewater treatment in a stable state without the generation of gypsum scale due to conventional sulfate ions and the generation of gypsum sludge. Also,
Since aluminum chloride has a small effect as a coagulant, the occurrence of deposition and scaling on pipes and tanks is extremely small.
[実施例] 次に、本発明を実施例により説明する。EXAMPLES Next, the present invention will be described with reference to examples.
実施例および比較例 石炭燃焼排ガスを処理する排煙脱硫装置からの排水(フ
ッ素濃度1400ppm,ホウ酸濃度150ppm,アルミニウム濃度5
0ppm)を3m3/hrで流し、第1図に示すフッ素処理工程に
おいて添加アルミニウム剤としてPAC,硫酸バン土または
塩化アルミニウムを用いてフッ素の除去性能とアルミニ
ウムフロックの付着やスケーリング状況について評価し
た。結果を第2図に示す。Examples and Comparative Examples Wastewater from a flue gas desulfurization unit for treating coal combustion exhaust gas (fluorine concentration 1400ppm, boric acid concentration 150ppm, aluminum concentration 5
(0 ppm) at a flow rate of 3 m 3 / hr, and in the fluorine treatment step shown in FIG. 1, PAC, vanadium sulfate, or aluminum chloride was used as an additive aluminum agent to evaluate the fluorine removal performance and the adhesion and scaling of aluminum flocs. Results are shown in FIG.
図から明らかなように、フッ素除去効率は塩化アルミニ
ウムを用いた場合が最も高く、スケーリング等の発生量
は塩化アルミニウムの場合が最も少なかった。As is clear from the figure, the fluorine removal efficiency was highest when aluminum chloride was used, and the amount of scaling and the like was lowest when aluminum chloride was used.
第1図は排水のフッ素処理工程の1例を示す説明図、第
2図は各種アルミニウム剤の使用による排水処理の結果
を示すグラフである。FIG. 1 is an explanatory view showing an example of the fluorine treatment process of waste water, and FIG. 2 is a graph showing the results of waste water treatment by using various aluminum agents.
Claims (2)
吸収液で処理して得られ、フッ素濃度が500ppm以上であ
り、かつホウ素を含む排水にカルシウム化合物を加えて
pH調整後、アルミニウム濃度が300〜600ppmとなるよう
に塩化アルミニウムを添加して反応を行い、次いでカル
シウム化合物を含む溶液で処理することを特徴とするフ
ッ素含有排水の処理方法。1. A coal flue gas obtained by treating a coal combustion exhaust gas with an absorption liquid containing a calcium compound, having a fluorine concentration of 500 ppm or more, and adding a calcium compound to wastewater containing boron.
After the pH is adjusted, aluminum chloride is added so that the aluminum concentration becomes 300 to 600 ppm, the reaction is carried out, and then the solution is treated with a solution containing a calcium compound.
つホウ素濃度40ppm以上のものであ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 waste water has a fluorine concentration of 500 ppm or more and a boron concentration of 40 ppm or more.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61180027A JPH0790228B2 (en) | 1986-08-01 | 1986-08-01 | Treatment method for fluorine-containing wastewater |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61180027A JPH0790228B2 (en) | 1986-08-01 | 1986-08-01 | Treatment method for fluorine-containing wastewater |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP7016390A Division JP2596908B2 (en) | 1995-01-09 | 1995-01-09 | Treatment method for fluorine-containing wastewater |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6339694A JPS6339694A (en) | 1988-02-20 |
JPH0790228B2 true JPH0790228B2 (en) | 1995-10-04 |
Family
ID=16076187
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61180027A Expired - Lifetime JPH0790228B2 (en) | 1986-08-01 | 1986-08-01 | Treatment method for fluorine-containing wastewater |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0790228B2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2011118808A1 (en) | 2010-03-26 | 2011-09-29 | 千代田化工建設株式会社 | Treatment method of wastewater containing persistent substances |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5310553A (en) * | 1976-07-15 | 1978-01-31 | Kurita Water Ind Ltd | Mehtod of treating waste water containing fluorine and boron |
-
1986
- 1986-08-01 JP JP61180027A patent/JPH0790228B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPS6339694A (en) | 1988-02-20 |
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