JPS60261590A - Treatment of waste water containing chlorinated hydrocarbon - Google Patents
Treatment of waste water containing chlorinated hydrocarbonInfo
- Publication number
- JPS60261590A JPS60261590A JP11870484A JP11870484A JPS60261590A JP S60261590 A JPS60261590 A JP S60261590A JP 11870484 A JP11870484 A JP 11870484A JP 11870484 A JP11870484 A JP 11870484A JP S60261590 A JPS60261590 A JP S60261590A
- Authority
- JP
- Japan
- Prior art keywords
- chlorinated hydrocarbons
- waste water
- treatment
- wastewater
- treated
- 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.)
- Pending
Links
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、塩素化炭化水素を含有する廃水の処理方法に
関する。DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a method for treating wastewater containing chlorinated hydrocarbons.
従来の扶′jおよび発明が角・′シようとする間■怠塩
素化炭化水素は洗浄剤、抽出剤、希釈剤、反応溶剤等と
して広範囲の分野において使用され、特に金属脱脂洗浄
の分野において多量に使用されているが、このような塩
素化炭化水素を含んだ廃水の処理問題は公害問題として
把握されるようになり、環境保全や保健衛生等の面から
厳しく規制されでいる。While the conventional aids and inventions are trying to overcome this problem, lazily chlorinated hydrocarbons are used in a wide range of fields as cleaning agents, extractants, diluents, reaction solvents, etc., especially in the field of metal degreasing and cleaning. Although they are used in large quantities, the problem of processing wastewater containing such chlorinated hydrocarbons has come to be understood as a pollution problem, and is strictly regulated from the standpoint of environmental conservation and health and hygiene.
廃水中に含まれる塩素化炭化水素を除去する方法として
は、曝気方式または活性炭に吸着させる方式等が従来か
ら採用されているが、両方式とも莫大な設備投資を必要
とし、特に前者は大気汚染によって別の公害問題を誘発
し、また後者は多量の比較的高価な活性炭を必要とする
ばかりでなく、付随的にその再生処理問題を発生する等
の難点がある。Conventional methods for removing chlorinated hydrocarbons contained in wastewater include aeration methods and activated carbon adsorption methods, but both methods require huge capital investment, and the former in particular causes air pollution. However, the latter method not only requires a large amount of relatively expensive activated carbon, but also has problems in its recycling process.
本発明は、このような欠点を低コストで簡単な方法によ
って解消し、廃水中に含まれる塩素化炭化水素、例えば
、トリクロロエチレン、テトラクロロエチレン、1,1
.1−トリクロロエタン等を効率よく除去する方法を提
供するものである。The present invention overcomes these drawbacks by a simple method at low cost, and eliminates chlorinated hydrocarbons contained in wastewater, such as trichlorethylene, tetrachlorethylene, 1,1
.. The present invention provides a method for efficiently removing 1-trichloroethane and the like.
問題点を解決するための手段
即ち、本発明の要旨は、塩素化炭化水素含有廃水を過酸
化物と周期律表第8族元素の化合物(以下、単に金属化
合物という)の共存下に処理することを特徴とする塩素
化炭化水素含有廃水の処理方法に存する。A means for solving the problem, that is, the gist of the present invention is to treat wastewater containing chlorinated hydrocarbons in the coexistence of peroxide and a compound of a group 8 element of the periodic table (hereinafter simply referred to as a metal compound). A method for treating wastewater containing chlorinated hydrocarbons is provided.
本発明に使用する過酸化物としては、過酸化水素が一般
的である。Hydrogen peroxide is generally used as the peroxide in the present invention.
また、本発明に使用する好ましい金属化合物としては、
硫酸第1鉄、硫酸第2鉄、塩化第1鉄、塩化第2鉄等の
鉄化合物か例示される。Further, preferable metal compounds used in the present invention include:
Examples include iron compounds such as ferrous sulfate, ferric sulfate, ferrous chloride, and ferric chloride.
過酸化物および金属化合物の使用量は、これらの処理剤
の種類、廃水中に含まれる塩素化炭化水素の種類や量、
廃水の性状等に応じて適宜選定すればよく、特に限定的
ではないが、例えば、通常は塩素化炭化水素約1〜11
00ppm含有する廃水約1lに対して過酸化物的0.
1〜30mol、金属酸化物的0.1〜30mol使用
する。The amount of peroxides and metal compounds used depends on the type of these treatment agents, the type and amount of chlorinated hydrocarbons contained in the wastewater,
It may be selected as appropriate depending on the properties of the wastewater, etc., and is not particularly limited, but for example, usually chlorinated hydrocarbon
per liter of wastewater containing 0.00 ppm peroxide.
Use 1 to 30 mol, and 0.1 to 30 mol for metal oxide.
処理温度は通常的40〜50℃であるか、これに限定さ
れるものではない。The processing temperature is typically 40 to 50°C, but is not limited thereto.
処理操作は静置法によっておこなってもよいか、攪拌す
ることによって処理効率か高められる。The processing operation may be carried out by a static method, or the processing efficiency can be increased by stirring.
本発明方法によって処理された廃水中の塩素化炭素水素
の濃度は約3〜14ppbであり、環境保全上全く問題
はない。The concentration of chlorinated carbon hydrogen in wastewater treated by the method of the present invention is about 3 to 14 ppb, which poses no problem in terms of environmental protection.
処理後の廃水は通常酸性であるのでアルカリ処理し、ろ
過後、排水するか、再使用に供する。Since treated wastewater is usually acidic, it is treated with alkali, filtered, and then either drained or reused.
なお、以上の処理に付された排水のTOC、COD、B
OD等を調整するために、所望により処理廃水をさらに
凝集剤処理に付してもよい。In addition, TOC, COD, B of the wastewater subjected to the above treatment
In order to adjust the OD and the like, the treated wastewater may be further treated with a flocculant, if desired.
この目的に使用される好適な凝集剤としては、特開昭5
8−216705号公報に開示されている水処理用析出
疑集剤が例示される。Suitable flocculants used for this purpose include JP-A No. 5
An example is the precipitation dispersing agent for water treatment disclosed in Japanese Patent No. 8-216705.
このような凝集剤処理によって廃水のTOC、COD、
およびBODはそれぞれ、例えば、約5〜2S、約5〜
20、および約5〜10に調整することかできる。Through such flocculant treatment, wastewater TOC, COD,
and BOD are, for example, about 5-2S and about 5-2S, respectively.
20, and can be adjusted to about 5-10.
以下、本発明を実施例によって説明する。Hereinafter, the present invention will be explained by examples.
実施例
トリクロロエチレン78ppmの原水100mlに35
%H2O21mlおよび10%硫酸第2鉄水溶液1ml
を加え、約45℃で約60分間処理した後(pH2)、
水酸化ナトリウム水溶液を用いて中和し、濾過処理に付
し、ろ液中のトリクロロエチレンの濃度を、厚生省環境
衛生局還水第15の方法によって測定したところ、16
ppbであった。Example 35 to 100 ml of raw water containing 78 ppm of trichlorethylene
21 ml of %H2O and 1 ml of 10% ferric sulfate aqueous solution
was added and treated at about 45°C for about 60 minutes (pH 2),
It was neutralized using an aqueous sodium hydroxide solution and subjected to filtration treatment, and the concentration of trichlorethylene in the filtrate was measured according to method No. 15 of Kansei Water, Environmental Sanitation Bureau, Ministry of Health and Welfare.
It was ppb.
この処理液をさらに凝集剤(ムラタ産業株式会社製[サ
ブロCDを用して処理したところ、トリクロロエチレン
の濃度は14ppm、CODは21ppmであった。When this treatment solution was further treated using a flocculant (Saburo CD manufactured by Murata Sangyo Co., Ltd.), the concentration of trichlorethylene was 14 ppm and the COD was 21 ppm.
実施例2
トリクロロエチレン520ppmの原水100mlを実
施例1に準拠してH2O2と硫酸第2鉄を用いて処理し
たところ、トリクロロエチレンの濃度は10ppbとな
った。Example 2 When 100 ml of raw water containing 520 ppm of trichlorethylene was treated with H2O2 and ferric sulfate according to Example 1, the concentration of trichlorethylene was 10 ppb.
発明の効果
本発明方法によって、廃水中の塩素化炭化水素を効率よ
く除去することかでと、その濃度は約5〜14ppbま
で低減される。Effects of the Invention By the method of the present invention, chlorinated hydrocarbons in wastewater are efficiently removed and their concentration is reduced to about 5-14 ppb.
Claims (1)
族元素の化合物の共存下で処理することを特徴とする塩
素化炭化水素含有廃水の処理方法。 2、所望により、処理廃水をさらに凝集剤で処理する第
1項記載の方法。[Claims] 1. Treating chlorinated hydrocarbon-containing wastewater with peroxide and No. 8 of the periodic table.
A method for treating wastewater containing chlorinated hydrocarbons, characterized in that the treatment is carried out in the coexistence of a group element compound. 2. The method according to item 1, wherein the treated wastewater is further treated with a flocculant, if desired.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11870484A JPS60261590A (en) | 1984-06-08 | 1984-06-08 | Treatment of waste water containing chlorinated hydrocarbon |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11870484A JPS60261590A (en) | 1984-06-08 | 1984-06-08 | Treatment of waste water containing chlorinated hydrocarbon |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS60261590A true JPS60261590A (en) | 1985-12-24 |
Family
ID=14743067
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11870484A Pending JPS60261590A (en) | 1984-06-08 | 1984-06-08 | Treatment of waste water containing chlorinated hydrocarbon |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60261590A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5611928A (en) * | 1992-12-04 | 1997-03-18 | Kemira Oy | Process for treating waste water |
US6497795B1 (en) | 1998-12-16 | 2002-12-24 | Canon Kabushiki Kaisha | Method and apparatus for decomposing gaseous aliphatic hydrocarbon halide compound |
US6616815B2 (en) | 1998-06-22 | 2003-09-09 | Canon Kabushiki Kaisha | Method of decomposing halogenated aliphatic hydrocarbon compounds or aromatic compounds and apparatus to be used for the same as well as method of clarifying exhaust gas and apparatus to be used for the same |
US6716399B2 (en) | 1998-11-30 | 2004-04-06 | Canon Kabushiki Kaisha | Apparatus for decomposing halogenated aliphatic hydrocarbon compounds or aromatic compounds |
US7018514B2 (en) | 2001-11-12 | 2006-03-28 | Canon Kabushiki Kaisha | Method and apparatus for processing substances to be decomposed |
US7163615B2 (en) | 2001-11-12 | 2007-01-16 | Canon Kabushiki Kaisha | Method of treating substance to be degraded and its apparatus |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS51144060A (en) * | 1975-06-06 | 1976-12-10 | Toagosei Chem Ind Co Ltd | Method of treating waste water |
JPS5447357A (en) * | 1977-09-22 | 1979-04-13 | Toa Gosei Chem Ind | Waste water disposal method |
-
1984
- 1984-06-08 JP JP11870484A patent/JPS60261590A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS51144060A (en) * | 1975-06-06 | 1976-12-10 | Toagosei Chem Ind Co Ltd | Method of treating waste water |
JPS5447357A (en) * | 1977-09-22 | 1979-04-13 | Toa Gosei Chem Ind | Waste water disposal method |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5611928A (en) * | 1992-12-04 | 1997-03-18 | Kemira Oy | Process for treating waste water |
US6616815B2 (en) | 1998-06-22 | 2003-09-09 | Canon Kabushiki Kaisha | Method of decomposing halogenated aliphatic hydrocarbon compounds or aromatic compounds and apparatus to be used for the same as well as method of clarifying exhaust gas and apparatus to be used for the same |
US6716399B2 (en) | 1998-11-30 | 2004-04-06 | Canon Kabushiki Kaisha | Apparatus for decomposing halogenated aliphatic hydrocarbon compounds or aromatic compounds |
US6497795B1 (en) | 1998-12-16 | 2002-12-24 | Canon Kabushiki Kaisha | Method and apparatus for decomposing gaseous aliphatic hydrocarbon halide compound |
US7163665B2 (en) | 1998-12-16 | 2007-01-16 | Canon Kabushiki Kaisha | Apparatus for decomposing gaseous aliphatic hydrocarbon halide compounds |
US7018514B2 (en) | 2001-11-12 | 2006-03-28 | Canon Kabushiki Kaisha | Method and apparatus for processing substances to be decomposed |
US7163615B2 (en) | 2001-11-12 | 2007-01-16 | Canon Kabushiki Kaisha | Method of treating substance to be degraded and its apparatus |
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