JPS61204082A - Cleaning up method of water contaminated with organic halogen compound - Google Patents
Cleaning up method of water contaminated with organic halogen compoundInfo
- Publication number
- JPS61204082A JPS61204082A JP4554285A JP4554285A JPS61204082A JP S61204082 A JPS61204082 A JP S61204082A JP 4554285 A JP4554285 A JP 4554285A JP 4554285 A JP4554285 A JP 4554285A JP S61204082 A JPS61204082 A JP S61204082A
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- Prior art keywords
- compd
- water
- organic halogen
- org
- halogen
- 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.)
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- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は有機ハロゲン化合物で汚染された水の浄化法に
閃する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention is directed to a method for purifying water contaminated with organic halogen compounds.
[従来の技術1
現在、水は上水、下水のいかんにかかわらず多かれ少な
かれ有機ハロゲン化合物で汚染されている。たとえば、
上水道においては、塩素や次亜塩素酸塩などの活性塩素
化合物を用いて水が殺菌されている。しかし、その過程
で、それらの活性塩素化合物により水中の有機物が塩素
化され、トリへロメタンなどの有機塩素化合物が生じて
いる。また、下水道においても、たとえばドライクリー
ニングなど1こ用いられでいるトリクレンやパークレン
が流入したり、都市ゴミなどの焼却により生じた有害な
へロデン化合物が流入したりしている。最近の研究によ
って、これらの有機ハロゲン化合物の中には発ガン性の
強いものが含まれていることが明らかになり、重大な社
会問題となっている。[Prior Art 1] At present, water, whether water or sewage, is contaminated to some extent with organic halogen compounds. for example,
In water supplies, water is sterilized using active chlorine compounds such as chlorine and hypochlorite. However, in the process, organic substances in the water are chlorinated by these active chlorine compounds, producing organic chlorine compounds such as triheromethane. In addition, sewage systems also receive inflows of trichrene and percrene, which are used in dry cleaning, and harmful helodene compounds produced by the incineration of municipal waste. Recent research has revealed that some of these organic halogen compounds are highly carcinogenic, which has become a serious social problem.
そうした水中の有機ハロゲン化合物は、現在、活性炭な
どの吸着剤を用いて吸着除去されているが、吸着量に制
限があると共に、吸着剤の再生工程が複雑であり、その
ために除去率が低く、処理コストが極めて高いことが欠
点となっている。Currently, such organic halogen compounds in water are adsorbed and removed using adsorbents such as activated carbon, but the adsorption amount is limited and the regeneration process of the adsorbent is complicated, resulting in a low removal rate. The disadvantage is that the processing cost is extremely high.
本発明者らは、光化学の研究過程において、波長200
〜300nzの紫外線と過酸化水素を併用するか、また
は波長200nt以下の遠紫外線を照射することにより
、水中のトリハロメタンを酸化分解しうろことを見出し
た。この方法は、トリハロメタンを二酸化炭素と塩化水
素などに分解できるというすぐれた浄化法ではあるが、
飲料水や焼却燃焼排γス洗浄水などの大量の水を処理す
る方法としては、有効な浄化法とはいえな1、% 。In the process of researching photochemistry, the present inventors discovered that wavelengths of 200
We have discovered that trihalomethane in water can be oxidized and decomposed by using a combination of ~300 nz ultraviolet rays and hydrogen peroxide, or by irradiating deep ultraviolet rays with a wavelength of 200 nt or less. Although this method is an excellent purification method that can decompose trihalomethane into carbon dioxide and hydrogen chloride,
1.% is not an effective purification method for treating large amounts of water, such as drinking water or incineration waste gas cleaning water.
また、本発明者らは、各種有機化合物水溶液の放射線化
学反応を研究中に、水の放射線分解によって生ずるOH
ラジカルと水和電子が種々の物質に作用すると、とくに
ORラジカルは有機化合物から水素原子を引き抜いて有
機化合物の酸化分解を促進し、水和電子は有機ハロゲン
化合物を還元的に分解することを見出だした。この放射
線化学的方法も有機ハロゲン化合物含有水の浄化法とし
て応用でき、原子力時代に適した水の浄化法とな9うる
可能性があるが、この方法を実用化するためには大線量
の放射線源が必要となるなどの問題がある。In addition, while researching the radiochemical reactions of various organic compound aqueous solutions, the present inventors discovered that OH produced by radiolysis of water
When radicals and hydrated electrons act on various substances, in particular, OR radicals extract hydrogen atoms from organic compounds and promote the oxidative decomposition of organic compounds, while hydrated electrons reductively decompose organic halogen compounds. It started. This radiochemical method can also be applied to purify water containing organic halogen compounds, and has the potential to become a water purification method suitable for the nuclear age, but in order to put this method into practical use, large doses of radiation are required. There are problems such as the need for a source.
[発明が解決しようとする問題点1
本発明は、きわめで簡単な処理で効率よく水中の有fi
へロデン化合物を無機化分解する方法を提供すること
を目的とする。[Problem to be solved by the invention 1] The present invention efficiently solves the problem of underwater fi
An object of the present invention is to provide a method for mineralizing and decomposing helodenoid compounds.
[問題点を解決するための手段1
本発明は、白金、金、銀、ニッケル、鉛、鉄、銅および
銅を主成分とする合金よりなる群から選ぱれた材料(以
下、特定の金属材料という)により陰極を構成し、電極
間に電流を通しで水中の有機ハロゲン化合物をj!!1
ilf!化分解すること全分解とする有機ハロゲン化合
物汚染水の浄化法に閃する。[Means for Solving the Problems 1] The present invention is based on materials selected from the group consisting of platinum, gold, silver, nickel, lead, iron, copper, and alloys containing copper as main components (hereinafter, specific metal materials). ) constitutes a cathode, and an electric current is passed between the electrodes to remove organic halogen compounds in water. ! 1
ilf! I came up with a method for purifying water contaminated with organic halogen compounds, which involves chemical decomposition or complete decomposition.
[作 用]
本発明における作用原理についでは目下詳細に研究中で
あるが、水中の有機ハロゲン化合物が陰極表面において
還元的に分解されて無機化し、しかも有機ハロゲン化合
物の分解率や生成物の種類が陰極材料の材質によって異
なることからみで、前記特定の金属材料が触媒作用を果
たしているものと推定される。*た前記特定の金属材料
がすぐれた有機ハロゲン化合物の分解効率を示す理由も
未だ明らかではないが、それらの金属材料は有機ハロゲ
ン化合物の吸着量が多く、かつ有機ハロゲン化合物に対
する電背の移動を容易にするという性質を有しており、
そうした性質が重要な役割を果たしているものと考えら
れる。[Function] The working principle of the present invention is currently being studied in detail, but the organic halogen compound in water is reductively decomposed and mineralized on the surface of the cathode, and the decomposition rate of the organic halogen compound and the type of products are unknown. Since this differs depending on the material of the cathode material, it is presumed that the specific metal material has a catalytic effect. *It is still not clear why the above-mentioned specific metal materials exhibit excellent decomposition efficiency of organic halogen compounds, but these metal materials have a large adsorption amount of organic halogen compounds and are highly effective at reducing the transfer of charge back to organic halogen compounds. It has the property of facilitating
It is thought that such properties play an important role.
[実施例]
本発明において、陰極は前記特定の金属材料で構成され
るが、それらの金属材料は少なくとも陰極表面に存在し
ていればよく、必ずしも陰極全体を前記特定の金属材料
で作製するする必要はない。したがって、たとえばプラ
スチック板上に前記金属材料をメッキしたり、金xti
を貼り付けたりする方法などによって被覆したものでも
よく、また金属酸化物などと前記特定の金属材料粉とを
混合成形したものでもよい。[Example] In the present invention, the cathode is composed of the above-mentioned specific metal materials, but it is sufficient that these metal materials are present at least on the surface of the cathode, and the entire cathode is not necessarily made of the above-mentioned specific metal materials. There's no need. Therefore, for example, plating the metal material on a plastic plate or gold xti
It may be coated by pasting or the like, or it may be formed by mixing and molding a metal oxide or the like with the above-mentioned specific metal material powder.
陽極としては、酸化することによって水中に金属イオン
として溶出することが不都合であるばあいには、溶出量
の少ない材料、たとえば白金、ステンレス鋼、炭素など
により構成するのが好ましい。In cases where it is inconvenient for the anode to be eluted as metal ions into water by oxidation, it is preferable to use a material that elutes in a small amount, such as platinum, stainless steel, carbon, etc.
本発明で用いる′N極は、物質的方法や化学的方法によ
るエツチングなどの表面処理をして電力効率を向上させ
ることもできる。The N-electrode used in the present invention can be surface-treated by physical or chemical methods such as etching to improve power efficiency.
電極間に印加する電圧や通電量はと(に限定されないが
、通常0.5〜1ooov 、好ましくは3−30VV
)電圧テ0.1−1000A/m2、好虫L<ハl〜1
00^/ m’2の電流密度で行なうことが好ましい。The voltage and amount of current applied between the electrodes is usually 0.5 to 100V, preferably 3 to 30V, but not limited to
) Voltage Te 0.1-1000A/m2, Insectophile L<Ha l~1
It is preferable to carry out at a current density of 00^/m'2.
また処理時間は電流密度や有機ハロゲン化合物の濃度な
どによって異なるが、通常数秒〜数十時間でよい。Further, the treatment time varies depending on the current density, the concentration of the organic halogen compound, etc., but is usually several seconds to several tens of hours.
本発明の浄化法は、電極を備えたセルなどの容器中に有
機ハロゲン化合物汚染水を通して処理する連続法でもよ
いし、廃水溜などに滞留している被処理水中に電極を浸
漬しで処理するパッチ法でもよい、*た、従来用いられ
ている活性炭処理と併用してもよい。The purification method of the present invention may be a continuous method in which organic halogen compound-contaminated water is passed through a container such as a cell equipped with an electrode, or it may be a continuous method in which the electrode is immersed in the water to be treated accumulated in a wastewater reservoir or the like. A patch method may be used, or it may be used in combination with conventionally used activated carbon treatment.
本発明の方法によるときは種々の有機ハロゲン化合物の
無機化分解処理が可能であるが、とくに有害なりロロホ
ルム、ブロモジクロルメタン、トリクロルエタン、トリ
クレン、パークレン、クロルベンゼン、四塩化炭素、ポ
リ塩化ビフェニル、ペンタクロロ7エノールなどの脂肪
族または芳香族ハロゲン化合物の分解に有効である。こ
れらの有機ハロゲン化合物は本発明の方法によって無害
な化合物に無機化変換される。When using the method of the present invention, it is possible to decompose various organic halogen compounds into minerals, but the most harmful ones are loloform, bromodichloromethane, trichloroethane, trichrene, perchlorene, chlorobenzene, carbon tetrachloride, polychlorinated biphenyls, pentachloro It is effective in decomposing aliphatic or aromatic halogen compounds such as 7-enol. These organic halogen compounds are mineralized into harmless compounds by the method of the present invention.
たとえば、クロロホルムはメタンと塩化水素に還元的に
変換され、トリクレンはエタンと塩化水素に、四塩化炭
素はメタンと塩化水素に、1゜1.1−トリクロルエタ
ンはエタンと塩化水素に、モノクロルベンゼンはベンゼ
ンと塩化水素に、またブロモジクロルメタンはメタンと
塩化水素および臭化水素に変換される。For example, chloroform is reductively converted to methane and hydrogen chloride, trichlene to ethane and hydrogen chloride, carbon tetrachloride to methane and hydrogen chloride, 1°1.1-trichloroethane to ethane and hydrogen chloride, and monochlorobenzene to ethane and hydrogen chloride. is converted to benzene and hydrogen chloride, and bromodichloromethane is converted to methane, hydrogen chloride, and hydrogen bromide.
本発明の浄化法によるときは、陰極材料の種類、有機ハ
ロゲン化合物の種類、濃度、電流密度、反応時間などに
よって異なるが、約70%以上、多くは90%台の分解
率がえられる。When using the purification method of the present invention, a decomposition rate of about 70% or more, often in the 90% range, can be obtained, although it varies depending on the type of cathode material, the type of organic halogen compound, concentration, current density, reaction time, etc.
つぎに本発明の方法を実施例および比較例に基づいて説
明するが、本発明はかかる実施例のみに限定されるもの
ではない。Next, the method of the present invention will be explained based on Examples and Comparative Examples, but the present invention is not limited to these Examples.
実施例1〜8およ1比較例
陽極(極板面積52cz2)材料として5OS−304
のステンレス鋼を用い、陰極(極板面積52ci+2)
材料として第1表に示す金属材料を用い、陽イオン交換
膜で仕切った電解セル中にクロロホルムを6zMの濃度
で含有するクロロホルム水溶液を入れ、これを閉鎖循環
系で240分間通電(電流密度5、フッx io−’^
/z”)L、4329−oンあり’) f> 9 。Examples 1 to 8 and 1 Comparative Example Anode (electrode plate area: 52 cz2) 5OS-304 as material
Using stainless steel, the cathode (electrode plate area 52ci + 2)
Using the metal materials shown in Table 1 as materials, an aqueous chloroform solution containing chloroform at a concentration of 6 zM was placed in an electrolytic cell partitioned with a cation exchange membrane, and this was energized for 240 minutes in a closed circulation system (current density 5, Fu x io-'^
/z") L, 4329-on present') f>9.
ロホルムの分解率を調べた。結果を第1表に示す。The decomposition rate of loform was investigated. The results are shown in Table 1.
E以下余白]
第1表から明らかなごと(、本発明における特定の金属
材料で陰極を構成した実施例1〜8では、クロロホルム
の分解率および生成物の電流効率が比較例(SOS−3
04)に比して数倍以上も大きい。As is clear from Table 1, in Examples 1 to 8 in which the cathode was made of a specific metal material of the present invention, the decomposition rate of chloroform and the current efficiency of the product were lower than those of the comparative example (SOS-3
It is several times larger than 04).
実施例9〜13
被処理化合物としてクロロホルムに代えて第2表に示す
有機ハロゲン化合物を用いたほかは実施例5と同様にし
て処理し、各有機ハロゲン化合物の分解率を実施例1と
同様にして調べた。Examples 9 to 13 The treatment was carried out in the same manner as in Example 5, except that the organic halogen compounds shown in Table 2 were used instead of chloroform as the compound to be treated, and the decomposition rate of each organic halogen compound was the same as in Example 1. I looked it up.
結果を第2表に示す。The results are shown in Table 2.
12表
第2から明らかなごとく、本発明の方法によるときは、
脂肪族、芳香族を問わず種々の有機ハロゲン化合物を高
い効率で分解できる。As is clear from Table 12, when using the method of the present invention,
It can decompose various organic halogen compounds with high efficiency, regardless of whether they are aliphatic or aromatic.
ICリーIC Lee
Claims (1)
成分とする合金よりなる群から選ぱれた材料により陰極
を構成し、電極間に電流を通して水中の有機ハロゲン化
合物を無機化分解することを特徴とする有機ハロゲン化
合物汚染水の浄化法。1 The cathode is made of a material selected from the group consisting of platinum, gold, silver, nickel, lead, iron, copper, and alloys mainly composed of copper, and an electric current is passed between the electrodes to decompose organic halogen compounds in water into inorganic substances. A method for purifying water contaminated with organic halogen compounds.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4554285A JPS61204082A (en) | 1985-03-07 | 1985-03-07 | Cleaning up method of water contaminated with organic halogen compound |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4554285A JPS61204082A (en) | 1985-03-07 | 1985-03-07 | Cleaning up method of water contaminated with organic halogen compound |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS61204082A true JPS61204082A (en) | 1986-09-10 |
JPH051078B2 JPH051078B2 (en) | 1993-01-07 |
Family
ID=12722255
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4554285A Granted JPS61204082A (en) | 1985-03-07 | 1985-03-07 | Cleaning up method of water contaminated with organic halogen compound |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61204082A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2004016911A (en) * | 2002-06-14 | 2004-01-22 | Ohbayashi Corp | Method, apparatus and system for treatment of organic chlorine compound |
JP2006088009A (en) * | 2004-09-22 | 2006-04-06 | Matsushita Electric Ind Co Ltd | Purification method of contamination of soil and ground water |
JP2006130395A (en) * | 2004-11-04 | 2006-05-25 | Taisei Corp | Treatment apparatus of contaminated soil and treatment method of contaminated soil |
EP2300376A1 (en) * | 2008-07-15 | 2011-03-30 | Industrie De Nora S.p.A. | Method for treating industrial wastewaters |
JP2013039270A (en) * | 2011-08-18 | 2013-02-28 | Japan Atomic Energy Agency | Method for dechlorinating chlorinated aliphatic hydrocarbon compound and device for dechlorination |
JP2016040036A (en) * | 2015-10-06 | 2016-03-24 | 国立研究開発法人日本原子力研究開発機構 | Dechlorination method and dechlorination device for chlorinated ethylene |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0027745A1 (en) * | 1979-10-23 | 1981-04-29 | Creconsult Limited | A process for the electrochemical degradation of persistent organic compounds, with harmful or potentially harmful properties |
-
1985
- 1985-03-07 JP JP4554285A patent/JPS61204082A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0027745A1 (en) * | 1979-10-23 | 1981-04-29 | Creconsult Limited | A process for the electrochemical degradation of persistent organic compounds, with harmful or potentially harmful properties |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2004016911A (en) * | 2002-06-14 | 2004-01-22 | Ohbayashi Corp | Method, apparatus and system for treatment of organic chlorine compound |
JP2006088009A (en) * | 2004-09-22 | 2006-04-06 | Matsushita Electric Ind Co Ltd | Purification method of contamination of soil and ground water |
JP2006130395A (en) * | 2004-11-04 | 2006-05-25 | Taisei Corp | Treatment apparatus of contaminated soil and treatment method of contaminated soil |
JP4519605B2 (en) * | 2004-11-04 | 2010-08-04 | 大成建設株式会社 | Contaminated soil treatment apparatus and contaminated soil treatment method |
EP2300376A1 (en) * | 2008-07-15 | 2011-03-30 | Industrie De Nora S.p.A. | Method for treating industrial wastewaters |
JP2011527937A (en) * | 2008-07-15 | 2011-11-10 | インドゥストリエ・デ・ノラ・ソチエタ・ペル・アツィオーニ | Industrial wastewater treatment |
JP2013039270A (en) * | 2011-08-18 | 2013-02-28 | Japan Atomic Energy Agency | Method for dechlorinating chlorinated aliphatic hydrocarbon compound and device for dechlorination |
JP2016040036A (en) * | 2015-10-06 | 2016-03-24 | 国立研究開発法人日本原子力研究開発機構 | Dechlorination method and dechlorination device for chlorinated ethylene |
Also Published As
Publication number | Publication date |
---|---|
JPH051078B2 (en) | 1993-01-07 |
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