JPH10286597A - Method for wastewater purification treatment - Google Patents
Method for wastewater purification treatmentInfo
- Publication number
- JPH10286597A JPH10286597A JP9114282A JP11428297A JPH10286597A JP H10286597 A JPH10286597 A JP H10286597A JP 9114282 A JP9114282 A JP 9114282A JP 11428297 A JP11428297 A JP 11428297A JP H10286597 A JPH10286597 A JP H10286597A
- Authority
- JP
- Japan
- Prior art keywords
- dioxins
- wastewater
- water
- microfiltration membrane
- stirring
- 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.)
- Withdrawn
Links
Landscapes
- Physical Water Treatments (AREA)
- Removal Of Specific Substances (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、ごみ焼却炉や産業
廃棄物焼却炉の排水処理や埋立地の排水処理に適用され
る、ダイオキシン類を含有する排水の浄化処理方法に関
する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for purifying wastewater containing dioxins, which is applied to wastewater treatment of waste incinerators and industrial waste incinerators and wastewater treatment of landfills.
【0002】[0002]
【従来の技術】これまで、排ガス中のダイオキシン類は
重要視され、国内外でも規制やガイドラインが設けられ
て排ガス処理設備の改善が行なわれてきたが、排水中の
ダイオキシン類についても今後、規制が設けられていく
のではないかと推測される。特に、廃棄物焼却工程にお
いてはダイオキシン類が発生しやすく、燃焼技術での発
生抑制や排ガス処理技術による捕集・除去が広く行われ
るようになった。2. Description of the Related Art Dioxins in exhaust gas have been regarded as important, and regulations and guidelines have been established in Japan and overseas to improve exhaust gas treatment equipment. Dioxins in wastewater will be regulated in the future. It is presumed that is provided. In particular, in the waste incineration process, dioxins are easily generated, and the suppression of generation by combustion technology and the collection and removal by exhaust gas treatment technology have been widely performed.
【0003】[0003]
【発明が解決しようとする課題】そして廃棄物焼却炉で
生成された排ガスの処理方法には乾式法、半乾式法、湿
式洗浄法等が存在するが、湿式洗浄方法{中和剤として
苛性ソーダ(NaOH)や炭酸カルシウム(CaC
O3)を用いる}を採用すると、排ガス中のダイオキシ
ン類が洗浄液中に懸濁し、廃液がダイオキシン類で汚染
されてしまう。そしてこのようなダイオキシン類が含有
された排水の処理技術は、未だ規制が存在しないため
に、十分に研究された有効な設備として実用化されてい
ない。The exhaust gas generated in a waste incinerator can be treated by a dry method, a semi-dry method, a wet cleaning method, or the like. The wet cleaning method {caustic soda (neutralizing agent) NaOH) and calcium carbonate (CaC)
If the method using O 3 ) is adopted, dioxins in the exhaust gas are suspended in the cleaning solution, and the waste liquid is contaminated with dioxins. Such a wastewater treatment technology containing dioxins has not yet been put into practical use as a well-studied effective facility because there is no regulation yet.
【0004】本発明はかかる従来技術の課題に鑑み、ダ
イオキシン類を含有する排水から微量のダイオキシン類
までも効果的に捕集・除去することが出来る排水浄化方
法を提供する事にある。SUMMARY OF THE INVENTION In view of the above-mentioned problems of the prior art, an object of the present invention is to provide a wastewater purification method capable of effectively collecting and removing even a small amount of dioxins from wastewater containing dioxins.
【0005】[0005]
【課題を解決するための手段】本発明に至った経過を順
を追って説明する。さて前記湿式洗浄法等より得られる
排水中のダイオキシン類の殆どは、サブミクロンサイズ
の微粒子であり、一部は懸濁物に吸着されて存在する。
このため、排水中のダイオキシン類を処理するには、微
粒子状もしくは懸濁物質を捕集・除去する必要がある。
そこで本発明はダイオキシン類を含む排水(原水)を、
まず凝集沈殿して懸濁物及びダイオキシン類を吸着した
粒子の大きい懸濁物を沈殿除去する凝集沈殿工程を設け
る点を第1の特徴としている。The process leading to the present invention will be described step by step. Almost all dioxins in wastewater obtained by the wet washing method and the like are submicron-sized fine particles, and a part of the dioxins is present by being adsorbed to a suspension.
Therefore, in order to treat dioxins in wastewater, it is necessary to collect and remove particulate or suspended substances.
Therefore, the present invention provides wastewater (raw water) containing dioxins,
The first feature is that a coagulation sedimentation step of first coagulating and sedimenting to remove a suspension and a large suspension of particles adsorbing dioxins is provided.
【0006】又、ダイオキシン類そのものは有機系化合
物であり、極微量で有害性を示す為に、極微量リークし
てくるダイオキシン類は完全に排水側から除去しなけれ
ばならない。そこで本発明は、第2の特徴として、前記
沈殿除去後の排水を精密濾過膜を通す事により、ダイオ
キシン類を吸着した粒子の小さい懸濁物やダイオキシン
類粒子を前記排水より濾過する工程を設ける。更に本発
明は、前記精密濾過膜を通過したダイオキシン類を除去
するため、過酸化水素水(H2O2)を添加して攪拌混合
した後若しくは攪拌混合しながら、紫外線(UV)を照
射して分解する工程を設ける点を第3の特徴としてい
る。[0006] Further, dioxins themselves are organic compounds, and since they are harmful in a very small amount, dioxins leaking in a very small amount must be completely removed from the drain side. Therefore, the present invention provides, as a second feature, a step of filtering a small suspension of dioxin-adsorbed particles or dioxin particles from the wastewater by passing the wastewater after the precipitation removal through a microfiltration membrane. . Further, in the present invention, in order to remove dioxins that have passed through the microfiltration membrane, ultraviolet light (UV) is irradiated after or with stirring and mixing with hydrogen peroxide solution (H 2 O 2 ). The third feature is that a step of disassembly is provided.
【0007】即ち、本発明はダイオキシン類を含有する
排水を浄化する方法において、ダイオキシン類を含有す
る原水を凝集沈殿させたのち、精密濾過膜を通して濾過
し、次に、該濾過膜を通過した排水中に過酸化水素水を
添加して攪拌混合した後若しくは攪拌混合しながら紫外
線を照射することにより、排水中に含有する微量のダイ
オキシン類までも効果的に捕集除去出来る浄化方法を提
案する。That is, the present invention relates to a method for purifying wastewater containing dioxins, wherein the raw water containing dioxins is coagulated and settled, filtered through a microfiltration membrane, and then discharged through the filtration membrane. We propose a purification method capable of effectively collecting and removing even trace amounts of dioxins contained in wastewater by irradiating ultraviolet rays after adding or stirring and mixing aqueous hydrogen peroxide into the wastewater.
【0008】[0008]
【作用】前記湿式洗浄法等より得られる排水中に含有す
るダイオキシン類は微粒子で存在し、懸濁物に付着して
存在するものもある。又、超微粒子で存在するものもあ
り、排水中からこれらダイオキシン類を捕集・除去する
には各々性状に適合した処理方法が必要である。そのた
め、前記解決手段の項で示した手順で捕集・除去を行な
うことにより本発明が円滑に達成し得るが、その手順は
次の通りである。The dioxins contained in the waste water obtained by the wet washing method or the like are present as fine particles, and some dioxins are present in a suspension. Some of them are present as ultra-fine particles. To collect and remove these dioxins from the wastewater, a treatment method suitable for each property is required. Therefore, the present invention can be achieved smoothly by performing collection and removal according to the procedure described in the section of the above-mentioned solution means, but the procedure is as follows.
【0009】(1)ダイオキシン類を含む排水(原水)
の凝集沈殿工程 かかる工程により、ダイオキシン類を吸着した粒子の大
きい懸濁物が沈殿除去される。 (2)精密濾過工程 かかる工程により、ダイオキシン類を吸着した粒子の小
さい懸濁物やダイオキシン類粒子が濾過される。 (3)過酸化水素水の添加と攪拌混合/UV照射工程 前記精密濾過膜を通過した、より超微粒子のダイオキシ
ン類を過酸化水素水と反応させ、酸化分解し、無害化す
る。攪拌混合とUV照射はそのときの反応を加速させる
働きをする。(1) Wastewater containing dioxins (raw water)
Agglomerated sedimentation step By this step, a large suspension of particles adsorbing dioxins is precipitated and removed. (2) Microfiltration step By this step, a small suspension of dioxin-adsorbed particles and dioxin particles are filtered. (3) Addition of Hydrogen Peroxide Water and Stir Mixing / UV Irradiation Step Dioxins of more ultrafine particles that have passed through the microfiltration membrane are reacted with hydrogen peroxide water, oxidatively decomposed, and rendered harmless. Stirring and UV irradiation serve to accelerate the reaction at that time.
【0010】[0010]
【発明の実施の形態】以下、図面を参照して本発明の好
適な実施形態を例示的に詳しく説明する。但しこの実施
形態に記載されている構成部品の寸法、材質、形状、そ
の相対的配置等は特に特定的な記載がないかぎりは、こ
の発明の範囲をそれに限定する趣旨ではなく、単なる説
明例にすぎない。図1に本発明の実施形態としての排水
処理概略構成図を示す。ここで、W1 はダイオキシン類
を含む排水(原水)、W2 は本実施形態により処理後の
浄化水、は、1は凝集沈殿槽で例えば凝集沈殿剤として
硫酸アルミ(Al2(SO4)3 )等が投入される、2は
精密濾過膜(MF膜)20を有する濾過槽、3は紫外線
(UV)照射水路若しくは紫外線照射槽で、前記濾過槽
2通過後の排水に過酸化水素水(H2O2)を添加後、攪
拌混合機40により攪拌混合しながら紫外線照射ランプ
30により紫外線照射を行なう。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Preferred embodiments of the present invention will now be described in detail with reference to the drawings. However, the dimensions, materials, shapes, relative arrangements, and the like of the components described in this embodiment are not intended to limit the scope of the present invention unless otherwise specified, and are merely illustrative examples. Only. FIG. 1 shows a schematic configuration diagram of a wastewater treatment as an embodiment of the present invention. Here, W 1 is waste water (raw water) containing dioxins, W 2 is purified water treated according to the present embodiment, 1 is a coagulation sedimentation tank, for example, aluminum sulfate (Al 2 (SO 4 )) as a coagulation precipitant 3 ) a filtration tank 2 having a microfiltration membrane (MF membrane) 20; 3 an ultraviolet (UV) irradiation channel or an ultraviolet irradiation tank; After adding (H 2 O 2 ), ultraviolet irradiation is performed by the ultraviolet irradiation lamp 30 while stirring and mixing by the stirring mixer 40.
【0011】次にかかる実施形態の作用を説明する。先
ず、ダイオキシン類を含む排水(原水)W1 を凝集沈殿
槽1に導入して、粒子の大きい懸濁物を沈殿除去する。
沈殿した懸濁物は、不図示の汚泥処理槽内で接触爆気や
活性汚泥法等の所定の汚泥処理をした後、不図示の脱水
機により脱水処理する。つぎに、沈殿除去された排水は
濾過槽2内で精密濾過膜(MF膜)20を通すことによ
り、より小さい粒子の懸濁物とダイオキシン類を濾過・
除去する。更に、精密濾過膜20を通過した排水中に過
酸化水素水(H2O2)を添加した後、前記UV照射水路
3中で攪拌混合機40により攪拌混合しながら、ダイオ
キシン類を酸化分解する。Next, the operation of the embodiment will be described. First, waste water containing dioxins (raw water) W 1 is introduced into the coagulating sedimentation tank 1, precipitating and removing large suspension particles.
The precipitated suspension is subjected to a predetermined sludge treatment such as a contact explosion or activated sludge method in a sludge treatment tank (not shown), and then subjected to a dehydration treatment by a dehydrator (not shown). Next, the sediment-removed wastewater is passed through a microfiltration membrane (MF membrane) 20 in the filtration tank 2 to filter a suspension of smaller particles and dioxins.
Remove. Further, after adding aqueous hydrogen peroxide (H 2 O 2 ) to the wastewater that has passed through the microfiltration membrane 20, the dioxins are oxidatively decomposed while being stirred and mixed by the stirring mixer 40 in the UV irradiation water channel 3. .
【0012】この酸化分解を加速するため前記UV照射
水路3で紫外線ランプ30により紫外線を照射しながら
酸化分解を行ない、これによりダイオキシン類が除かれ
た処理後の浄化水W2 として放流することが出来る。
尚、紫外線照射と攪拌混合は同時に行なう必要はなく、
図2に示すように、紫外線照射槽3’の前段側に攪拌混
合槽4を設け、過酸化水素水(H2O2)を添加しながら
攪拌混合した後、前記紫外線照射槽3’で紫外線ランプ
30により紫外線を照射しながら酸化分解を行なうよう
に構成してもよい。[0012] subjected to oxidative decomposition while irradiating ultraviolet rays UV lamp 30 in the UV irradiation waterway 3 to accelerate the oxidative decomposition, it may thereby discharged as clean water W 2 after treatment dioxins are removed I can do it.
It is not necessary to perform the ultraviolet irradiation and the stirring and mixing at the same time,
As shown in FIG. 2, a stirring / mixing tank 4 is provided in front of the ultraviolet irradiation tank 3 ', and after stirring and mixing while adding hydrogen peroxide solution (H 2 O 2 ), the ultraviolet irradiation tank 3' The oxidative decomposition may be performed while irradiating the lamp 30 with ultraviolet rays.
【0013】[0013]
【実施例】図1の装置を用いて下記のように本発明の効
果を確認した。ダイオキシン類(ジベンゾジオモシンと
ジベンゾフランの総計)濃度が4.5mg/lの廃棄物焼却
炉洗煙排水(原水)図1の排水処理システムで処理し
た。まず原水を凝集沈殿槽に投入し、硫酸アルミニウム
(硫酸バンド)で凝集沈殿したのち、濾過槽に導入して
精密濾過膜(MF膜)を通して固液分離した。EXAMPLES The effects of the present invention were confirmed as follows using the apparatus shown in FIG. Waste incinerator smoke washing wastewater (raw water) having a dioxin concentration (total of dibenzodiomosine and dibenzofuran) of 4.5 mg / l was treated by the wastewater treatment system shown in FIG. First, raw water was put into a coagulation sedimentation tank, coagulated and precipitated with aluminum sulfate (sulfuric acid band), then introduced into a filtration tank, and subjected to solid-liquid separation through a microfiltration membrane (MF membrane).
【0014】つぎに精密濾過膜(MF膜)を通過した後
の処理水中に過酸化水素水1ppmを添加したのち、攪
拌混合させながら、紫外線ランプ(UVランプ)を設置
した水路3を通した。その結果、最終処理中のダイオキ
シン類濃度は0.01mg/l以下まで低減することが出来
た。Next, 1 ppm of hydrogen peroxide solution was added to the treated water after passing through the microfiltration membrane (MF membrane), and the mixture was passed through a water channel 3 provided with an ultraviolet lamp (UV lamp) while stirring and mixing. As a result, the concentration of dioxins during the final treatment could be reduced to 0.01 mg / l or less.
【0015】[0015]
【発明の効果】以上記載のごとく本発明によれば、ダイ
オキシン類を含む排水から微量のダイオキシン類まで効
率的に捕集・除去することが出来、これによりダイオキ
シン類や懸濁物を含まない浄化水を得ることができる。As described above, according to the present invention, it is possible to efficiently collect and remove trace amounts of dioxins from wastewater containing dioxins, and thereby purify without dioxins and suspended matter. You can get water.
【図1】本発明の実施形態としての排水処理概略構成図
を示す。FIG. 1 shows a schematic configuration diagram of a wastewater treatment as an embodiment of the present invention.
【図2】図1の変形例に係る排水処理概略構成図を示
す。FIG. 2 shows a schematic configuration diagram of a wastewater treatment according to a modification of FIG.
1 凝集沈殿槽 2 濾過槽 3 紫外線(UV)照射水路 3’ 紫外線照射槽 4 攪拌混合槽 20 精密濾過膜(MF膜) 30 紫外線照射ランプ 40 攪拌混合機 DESCRIPTION OF SYMBOLS 1 Coagulation sedimentation tank 2 Filtration tank 3 Ultraviolet (UV) irradiation water path 3 'Ultraviolet irradiation tank 4 Stir-mixing tank 20 Microfiltration membrane (MF membrane) 30 Ultraviolet irradiation lamp 40 Stir-mixer
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI C02F 9/00 504 C02F 9/00 504D 1/32 ZAB 1/32 ZAB 1/44 1/44 F 1/52 1/52 K 1/58 1/58 A 1/72 1/72 Z 101 101 ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 6 Identification code FI C02F 9/00 504 C02F 9/00 504D 1/32 ZAB 1/32 ZAB 1/44 1/44 F 1/52 1/52 K 1/58 1/58 A 1/72 1/72 Z 101 101
Claims (1)
法において、 ダイオキシン類を含有する原水を凝集沈殿させたのち、
精密濾過膜を通して濾過し、つぎに、該濾過膜を通過し
た排水中に過酸化水素水を添加して攪拌混合した後若し
くは攪拌混合しながら紫外線を照射することを特徴とす
る排水浄化処理方法。1. A method for purifying wastewater containing dioxins, comprising coagulating and sedimenting raw water containing dioxins.
A method for purifying waste water, comprising filtering through a microfiltration membrane, and then irradiating with ultraviolet light after stirring or mixing with hydrogen peroxide water added to the waste water passing through the filtration membrane.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9114282A JPH10286597A (en) | 1997-04-16 | 1997-04-16 | Method for wastewater purification treatment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9114282A JPH10286597A (en) | 1997-04-16 | 1997-04-16 | Method for wastewater purification treatment |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH10286597A true JPH10286597A (en) | 1998-10-27 |
Family
ID=14633943
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9114282A Withdrawn JPH10286597A (en) | 1997-04-16 | 1997-04-16 | Method for wastewater purification treatment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH10286597A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001129569A (en) * | 1999-11-05 | 2001-05-15 | Mitsubishi Heavy Ind Ltd | Method and apparatus for treating harmful substance |
CN103641221A (en) * | 2013-11-30 | 2014-03-19 | 常熟市华宇针织印染有限公司 | Method for preparing coagulating and decolorizing agent for printing and dyeing wastewater treatment |
-
1997
- 1997-04-16 JP JP9114282A patent/JPH10286597A/en not_active Withdrawn
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001129569A (en) * | 1999-11-05 | 2001-05-15 | Mitsubishi Heavy Ind Ltd | Method and apparatus for treating harmful substance |
CN103641221A (en) * | 2013-11-30 | 2014-03-19 | 常熟市华宇针织印染有限公司 | Method for preparing coagulating and decolorizing agent for printing and dyeing wastewater treatment |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP3883445B2 (en) | Sewage treatment equipment | |
WO2005070833A1 (en) | Method for treating raw water containing hardly decomposable substance | |
JP2000288560A (en) | Water purifying treatment apparatus and method | |
KR100446042B1 (en) | Industrial wastewater reusing system using combination froth separation process, hollow fiber filter process and advanced oxidation process | |
JP3537312B2 (en) | Method for decomposing and removing organic chlorine compounds such as dioxins in sludge | |
JPH10305287A (en) | Ozone catalytic reactor | |
JPH10286597A (en) | Method for wastewater purification treatment | |
JPH10337579A (en) | Method and apparatus for treatment of wastewater | |
JP2000102794A (en) | Treatment of harmful material and device therefor | |
WO1994011307A1 (en) | Ozone treatment of landfill waste-water | |
JP4401251B2 (en) | General waste incineration wastewater treatment method | |
JP3400942B2 (en) | Method and apparatus for decomposing organic chlorine compounds such as dioxins in landfill leachate | |
JP3654579B2 (en) | Wastewater purification method | |
JP2003266090A (en) | Wastewater treatment method | |
JP2000185289A (en) | Waste water treatment method and apparatus | |
JP2008043879A (en) | Contaminated soil-cleaning system by washing | |
JP3418550B2 (en) | Method and equipment for decomposing and removing dioxins in sewage | |
JP2003103271A (en) | Treatment method for dioxins in wastewater | |
JP2002239597A (en) | Method for treating wastewater containing dioxins | |
KR100461894B1 (en) | Sewage and waste water disposal plant | |
KR100385847B1 (en) | A treatment system fo sewage of food | |
JP2005254159A (en) | Waste water treatment system and waste gas treatment system using the same | |
JP3323099B2 (en) | Method for removing dioxins from sludge | |
JP2004188340A (en) | Method for treating liquid containing dioxins | |
JPH11300347A (en) | Method for decomposing organochlorine compounds such as dioxins in landfill leachate |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A300 | Application deemed to be withdrawn because no request for examination was validly filed |
Free format text: JAPANESE INTERMEDIATE CODE: A300 Effective date: 20040706 |