JP3418550B2 - Method and equipment for decomposing and removing dioxins in sewage - Google Patents

Method and equipment for decomposing and removing dioxins in sewage

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Publication number
JP3418550B2
JP3418550B2 JP11979198A JP11979198A JP3418550B2 JP 3418550 B2 JP3418550 B2 JP 3418550B2 JP 11979198 A JP11979198 A JP 11979198A JP 11979198 A JP11979198 A JP 11979198A JP 3418550 B2 JP3418550 B2 JP 3418550B2
Authority
JP
Japan
Prior art keywords
sludge
dioxin
dioxins
treatment
extract
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
Application number
JP11979198A
Other languages
Japanese (ja)
Other versions
JPH11309486A (en
Inventor
正器 高比良
安雄 堀井
浩一 中河
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kubota Corp
Original Assignee
Kubota Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Kubota Corp filed Critical Kubota Corp
Priority to JP11979198A priority Critical patent/JP3418550B2/en
Publication of JPH11309486A publication Critical patent/JPH11309486A/en
Application granted granted Critical
Publication of JP3418550B2 publication Critical patent/JP3418550B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Removal Of Specific Substances (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)
  • Treatment Of Sludge (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Activated Sludge Processes (AREA)
  • Physical Water Treatments (AREA)

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、廃棄物最終処分場
の浸出水などの汚水中のダイオキシン類の分解除去方法
および分解除去設備に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and apparatus for decomposing and removing dioxins in wastewater such as leachate at a final waste disposal site.

【0002】[0002]

【従来の技術】一般廃棄物や産業廃棄物を埋立てた廃棄
物最終処分場の浸出水など、ダイオキシン類(PCDD
s,PCDFs)を含んだ汚水を浄化するフローは、た
とえば図2に示したようなものである。
2. Description of the Related Art Dioxins (PCDD), such as leachate from the final landfill of landfills of general waste and industrial waste
s, PCDFs) for purifying the waste water is, for example, as shown in FIG.

【0003】すなわち、汚水を凝沈処理1してカルシウ
ム並びにマンガンなどの重金属類を除去し、生物処理2
してBOD物質やT−Nを分解し、凝沈処理3してCO
D物質や浮遊物質やT−Pなどを除去し、砂濾過4して
微細な浮遊物質を除去し、その後に、オゾン・紫外線処
理5して、残存するダイオキシン類の他、COD物質や
色度成分などを分解し、活性炭処理6を経て放流してい
る。
That is, wastewater is subjected to coagulation treatment 1 to remove heavy metals such as calcium and manganese, and biological treatment 2
Then, the BOD substance and TN are decomposed, and the coagulation treatment 3 is performed to CO.
D substances, suspended substances, TP, etc. are removed, sand filtration 4 is used to remove fine suspended substances, and then ozone / ultraviolet treatment 5 is carried out, in addition to residual dioxins, COD substances and chromaticity. The components are decomposed, and the product is discharged after being treated with activated carbon 6.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、上記し
たように砂濾過4の後の砂濾過処理水4aをオゾン・紫
外線処理5しても、ダイオキシン類(PCDDs,PC
DFs)は生物処理2やその前後の凝沈処理1,3にお
いて微生物中あるいはSSに蓄積される形でほとんど
(99%以上)除去されているため、オゾン・紫外線に
よる分解効果は小さく、各処理で発生する汚泥中に含ま
れて排出されてしまう。
However, even if the sand filtration treated water 4a after the sand filtration 4 is subjected to the ozone / ultraviolet treatment 5 as described above, dioxins (PCDDs, PCDDs) can be obtained.
Most (99% or more) of DFs) are removed in the form of being accumulated in microorganisms or SS in biological treatment 2 and coagulation treatments 1 and 3 before and after it, so the decomposition effect by ozone and ultraviolet rays is small, and each treatment It is included in the sludge generated in and discharged.

【0005】また、砂濾過処理水4aであっても、S
S,フミン質等のCOD,Caイオン,NH4 −N,C
イオンなどが残存しており、これらが、紫外線の照
射効率を低下させたり、オゾン・紫外線より発生するO
Hラジカルのスカベンジャーとして働き、ダイオキシン
類の分解を阻害する。
Even if the sand-filtered water 4a is S
S, COD such as humic substances, Ca ions, NH 4 —N, C
l Ions, etc. remain, and these reduce the irradiation efficiency of ultraviolet rays and generate O from ozone and ultraviolet rays.
It acts as a scavenger for H radicals and inhibits the decomposition of dioxins.

【0006】本発明は上記問題を解決するもので、汚水
中のダイオキシン類を分解除去できる分解除去方法およ
び分解除去設備を提供することを目的とするものであ
る。
The present invention solves the above problems, and an object of the present invention is to provide a decomposition removal method and a decomposition removal equipment capable of decomposing and removing dioxins in wastewater.

【0007】[0007]

【課題を解決するための手段】上記課題を解決するため
に、本発明の汚水中のダイオキシン類の分解除去方法
は、ダイオキシン類を含んだ汚水を生物処理と凝沈処理
の少なくとも一方を行う汚水処理工程において処理し、
浄化された処理水を得るとともに、前記生物処理や凝沈
処理で発生したダイオキシン類を含んだ汚泥を清水で洗
浄し、洗浄した汚泥にダイオキシン抽出液を混合して汚
泥中のダイオキシン類をダイオキシン抽出液中に抽出
し、このダイオキシン抽出液を汚泥より分離し、濾過し
た後にオゾン・紫外線処理することによってダイオキシ
ン類を分解除去するようにしたものである。
In order to solve the above problems, the method for decomposing and removing dioxins in wastewater according to the present invention is a wastewater containing at least one of biological treatment and coagulation treatment of wastewater containing dioxins. Processing in the processing step,
In addition to obtaining purified treated water, sludge containing dioxins generated by the biological treatment or coagulation treatment is washed with fresh water, and the washed sludge is mixed with a dioxin extract solution to extract dioxin in the sludge. The dioxin is extracted in a liquid, the dioxin extract is separated from the sludge, filtered, and then treated with ozone and ultraviolet rays to decompose and remove dioxins.

【0008】また本発明の汚水中のダイオキシン類の分
解除去設備は、汚水を浄化する生物処理装置と凝集沈殿
処理装置の少なくとも一方を備えるとともに、生物処理
装置や凝集沈殿処理装置で発生した汚泥を処理する汚泥
処理装置を備え、前記汚泥処理装置は、清水供給手段を
有し、汚泥を洗浄する汚泥洗浄槽と、ダイオキシン抽出
液供給手段を有し、前記汚泥洗浄槽より移送される汚泥
中のダイオキシン類を抽出するダイオキシン抽出槽と、
前記ダイオキシン抽出槽より移送されるダイオキシン抽
出液を濾過する濾過手段と、オゾン供給手段および紫外
線照射手段を有し、前記濾過手段より移送されるダイオ
キシン抽出液中のダイオキシン類を分解するダイオキシ
ン分解塔とを備えた構成としたものである。
The facility for decomposing and removing dioxins in sewage of the present invention is equipped with at least one of a biological treatment device for purifying sewage and a coagulation sedimentation treatment device, and is capable of removing sludge generated in the biological treatment device or the coagulation sedimentation treatment device. A sludge treatment device for processing, the sludge treatment device has a fresh water supply means, a sludge cleaning tank for cleaning the sludge, and a dioxin extract supply means, in the sludge transferred from the sludge cleaning tank A dioxin extraction tank for extracting dioxins,
A dioxin decomposition tower having a filtering means for filtering the dioxin extract transferred from the dioxin extraction tank, an ozone supply means, and an ultraviolet irradiation means, for decomposing dioxins in the dioxin extract transferred from the filtering means; Is provided with.

【0009】ダイオキシン抽出液としては、アセトン、
アセトニトリル、ベンゼン、DMSO、クロロベンゼ
ン、o−ジクロロベンゼン、LAS(直鎖アルキルベン
ゼンスルホン酸ナトリウム)などを使用できる。
As the dioxin extract, acetone,
Acetonitrile, benzene, DMSO, chlorobenzene, o-dichlorobenzene, LAS (sodium linear alkylbenzene sulfonate) and the like can be used.

【0010】上記した構成によれば、汚泥を清水で洗浄
することで、汚泥の表面の水分を清水で置換して、オゾ
ン・紫外線処理の阻害要因となるSS,フミン質等のC
OD,Caイオン,NH4 −N,Cl イオンなどのス
カベンジャーの濃度を低下させることができ、このよう
な汚泥よりダイオキシン類を抽出したダイオキシン抽出
液を濾過したうえでオゾン・紫外線処理するので、ダイ
オキシン類を効率よく分解除去できる。
According to the above construction, by cleaning the sludge with fresh water, the water on the surface of the sludge is replaced with fresh water, and C such as SS and humic substances which become an obstructive factor for ozone / ultraviolet treatment.
OD, Ca ion, NH 4 -N, Cl It is possible to reduce the concentration of scavengers such as ions, and the dioxin extract solution obtained by extracting dioxin from such sludge is filtered and then treated with ozone and ultraviolet rays, so that dioxins can be efficiently decomposed and removed.

【0011】[0011]

【発明の実施の形態】以下、本発明の一実施形態を図面
を参照しながら説明する。図1は、廃棄物最終処分場の
浸出水処理プラントなど、ダイオキシン類(PCDD
s,PCDFs)を含んだ汚水を処理する汚水処理プラ
ントの概略全体構成を示し、汚水が順次流入する調整槽
11、カルシウム除去設備12,生物処理設備13,凝
集沈殿処理設備14,砂濾過塔15,活性炭吸着塔16
を備えている。
BEST MODE FOR CARRYING OUT THE INVENTION An embodiment of the present invention will be described below with reference to the drawings. Figure 1 shows dioxins (PCDDs) such as leachate treatment plants at final waste disposal sites.
s, PCDFs) showing a schematic overall structure of a sewage treatment plant for treating sewage, including a regulating tank 11 into which sewage sequentially flows, a calcium removal facility 12, a biological treatment facility 13, a coagulation sedimentation facility 14, a sand filtration tower 15. , Activated carbon adsorption tower 16
Is equipped with.

【0012】また、カルシウム除去設備12,生物処理
設備13,凝集沈殿処理設備14で発生した汚泥を処理
するための汚泥洗浄槽17,18,ダイオキシン抽出槽
19,濾過装置20,ダイオキシン分解装置21,2
2,汚泥脱水機23を備えている。
[0012] Further, sludge cleaning tanks 17 and 18 for treating sludge generated in the calcium removal equipment 12, the biological treatment equipment 13, and the coagulation sedimentation equipment 14, a dioxin extraction tank 19, a filtration device 20, a dioxin decomposition device 21, Two
2. The sludge dehydrator 23 is provided.

【0013】汚泥洗浄槽17,18は、清水供給手段1
7a,18a,攪拌手段17b,18bを備えた混合槽
17c,18cと沈殿槽17d,18dとで構成されて
いる。ダイオキシン抽出槽19はダイオキシン抽出液供
給手段19aを有し、かつ内容物を振とう可能であり、
ダイオキシン分解装置21,22はそれぞれ、上向きに
通液される円筒状の槽21a,22aの軸心位置に紫外
線ランプ21b,22bを配置し、槽内下部にオゾン供
給管21c,22cを配置している。汚泥脱水機23は
流入部に脱水助剤供給手段23aを有している。
The sludge cleaning tanks 17 and 18 are the fresh water supply means 1
7a and 18a, mixing tanks 17c and 18c equipped with stirring means 17b and 18b, and precipitation tanks 17d and 18d. The dioxin extraction tank 19 has a dioxin extract supply means 19a and is capable of shaking the contents,
The dioxin decomposers 21 and 22 have ultraviolet lamps 21b and 22b arranged at the axial center positions of the cylindrical tanks 21a and 22a, respectively, which are passed upward, and ozone supply pipes 21c and 22c arranged at the lower part of the tank. There is. The sludge dewatering machine 23 has a dewatering auxiliary agent supply means 23a at the inflow portion.

【0014】上記した処理プラントにおける汚水の処理
を説明する。汚水10を調整槽11で水質および流量調
整し、カルシウム除去設備12でNa2 CO3 凝集剤に
よってカルシウムやマンガンなどの重金属類を凝集沈殿
させ、生物処理設備13でBOD物質やT−Nを分解
し、凝集沈殿処理設備14で凝集剤によってCOD物質
や浮遊物質やT−Pなどを凝集沈殿させ、残存するS
S,T−N,フミン質等のCOD物質や色度成分などを
砂濾過塔15,活性炭吸着塔16で除去し、処理水24
として放流する。
The treatment of wastewater in the above treatment plant will be described. The water quality and flow rate of the sewage 10 are adjusted in the adjusting tank 11, heavy metals such as calcium and manganese are aggregated and precipitated by the Na 2 CO 3 aggregating agent in the calcium removal facility 12, and the BOD substance and TN are decomposed in the biological treatment facility 13. Then, in the coagulation-sedimentation treatment facility 14, the COD substance, the suspended matter, T-P, etc. are coagulated and precipitated by the coagulant, and the remaining S
COD substances such as S, TN, humic substances and chromaticity components are removed by the sand filtration tower 15 and the activated carbon adsorption tower 16, and treated water 24
To be released as.

【0015】カルシウム除去設備12と生物処理設備1
3と凝集沈殿処理設備14で発生した汚泥25はダイオ
キシン類を含んでいるので、汚泥洗浄槽17の混合槽1
7cに移送して、清水供給手段17aより供給される清
水中、攪拌手段17bで攪拌しながら洗浄した後に沈殿
槽17dに移送して沈降分離させ、次に、汚泥洗浄槽1
8の混合槽18cに移送して同様に洗浄した後に沈殿槽
18dに移送して沈降分離させる。洗浄は、汚泥25よ
り分離される分離水中に含まれるCaイオン,NH4
N,Cl イオンなどが10分の1以下程度になるま
で、必要に応じて複数回行う。
Calcium removal facility 12 and biological treatment facility 1
3 and the sludge 25 generated in the coagulation sedimentation treatment facility 14 contain dioxins, the mixing tank 1 of the sludge cleaning tank 17
7c, and in the clean water supplied from the fresh water supply means 17a, while stirring and washing with the stirring means 17b, it is transferred to the settling tank 17d for sedimentation separation, and then the sludge cleaning tank 1
Then, it is transferred to the mixing tank 18c of No. 8 and washed in the same manner, and then transferred to the precipitation tank 18d for sedimentation separation. For cleaning, Ca ions and NH 4 − contained in the separated water separated from the sludge 25
N, Cl It is performed plural times as necessary until the amount of ions and the like is reduced to about 1/10 or less.

【0016】そして、沈殿槽18dより洗浄汚泥26を
取り出してダイオキシン抽出槽19に移送し、ダイオキ
シン抽出液供給手段19aよりDMSOなどのダイオキ
シン抽出液を注入して1時間以上振とうし、洗浄汚泥2
6中のダイオキシン類をダイオキシン抽出液中に抽出す
る。
Then, the cleaning sludge 26 is taken out from the settling tank 18d and transferred to the dioxin extraction tank 19, and the dioxin extraction solution such as DMSO is injected from the dioxin extract supply means 19a and shaken for 1 hour or more to wash the sludge 2
The dioxins in 6 are extracted into the dioxin extract.

【0017】次に、ダイオキシン類を抽出したダイオキ
シン抽出液27を取り出し、濾過装置20で濾過した後
に、ダイオキシン分解装置21,22に順次通液し、各
装置の槽21a(22a)の内部において、オゾン供給
管21c(22c)を通じて供給されるオゾンと紫外線
ランプ21b(22b)より照射される紫外線とから発
生するOHラジカルを作用させ、ダイオキシン類を分解
する。
Next, the dioxin extract liquid 27 from which dioxins have been extracted is taken out, filtered by the filter device 20, and then passed through the dioxin decomposing devices 21, 22 in order, and inside the tank 21a (22a) of each device, OH radicals generated from ozone supplied through the ozone supply pipe 21c (22c) and the ultraviolet light emitted from the ultraviolet lamp 21b (22b) act to decompose dioxins.

【0018】ダイオキシン抽出槽19内に残留した汚泥
28は、脱水助剤供給手段23aより脱水助剤を添加し
たうえで汚泥脱水機23において脱水し、脱水ケーキ2
9はケーキホッパー(図示せず)に投入した後に適宜搬
出して、焼却・溶融処分する。
The sludge 28 remaining in the dioxin extraction tank 19 is dehydrated in the sludge dehydrator 23 after adding a dehydration aid from the dehydration aid supply means 23a, and the dehydrated cake 2
9 is put into a cake hopper (not shown), then appropriately carried out, and incinerated and melted and disposed.

【0019】汚泥脱水機23における脱離液30と、汚
泥洗浄槽17,18で発生した洗浄排水31,32と、
ダイオキシン分解装置22より流出するダイオキシン抽
出廃液33とは、調整槽11へ返送して一連の汚水処理
を行う。
The desorbed liquid 30 in the sludge dewatering machine 23, the cleaning drainages 31 and 32 generated in the sludge cleaning tanks 17 and 18,
The dioxin extraction waste liquid 33 flowing out from the dioxin decomposition device 22 is returned to the adjusting tank 11 and a series of wastewater treatment is performed.

【0020】このようにして、汚泥25を清水中で洗浄
するようにしたことにより、汚泥25の濃縮度が高まっ
てダイオキシン類抽出効率がよくなるとともに、汚泥2
5の表面の分離水が清水で置換されて、ダイオキシン分
解装置21,22へ通液されるダイオキシン抽出液27
中のSS,フミン質等のCOD,Caイオン,NH4
N,Cl イオンなどの濃度が低下する。
By cleaning the sludge 25 in clear water in this manner, the concentration of the sludge 25 is increased and the dioxins extraction efficiency is improved, and the sludge 2
The separated water on the surface of No. 5 is replaced with fresh water, and the dioxin extract liquid 27 is passed through the dioxin decomposers 21 and 22.
CO, such as SS and humic substances, Ca ions, NH 4
N, Cl The concentration of ions etc. decreases.

【0021】これらの結果、紫外線照射効率が高く、ス
カベンジャーによる無駄なオゾン消費が少ない状態にお
いて、ダイオキシン抽出液27中に抽出されたダイオキ
シン類を効率よく分解除去できる。しかも、脱水ケーキ
29はCl含有量が少ないので、焼却・溶融時における
ダイオキシンの発生量は少ない。
As a result, it is possible to efficiently decompose and remove the dioxins extracted in the dioxin extraction liquid 27 in a state where the ultraviolet irradiation efficiency is high and the wasteful ozone consumption by the scavenger is small. Moreover, since the dehydrated cake 29 has a low Cl content, the amount of dioxin generated during incineration / melting is small.

【0022】ダイオキシン抽出液としては、上記したD
MSOの他に、LAS(直鎖アルキルベンゼンスルホン
酸ナトリウム)、ベンゼン、アセトン、クロロベンゼ
ン、アセトニトリル、o−ジクロロベンゼンなどを使用
できる。たとえば、2w/v%濃度の汚泥(乾燥ベー
ス)に対して、DMSOの場合は10〜20w/v%濃
度のものを汚泥量と等容量以上添加し、ベンゼン(ある
いはアセトン、クロロベンゼン、アセトニトリル、o−
ジクロロベンゼン)の場合は20w/v%濃度のものを
汚泥量と等容量以上添加する。
As the dioxin extract, the above-mentioned D
In addition to MSO, LAS (sodium linear alkylbenzene sulfonate), benzene, acetone, chlorobenzene, acetonitrile, o-dichlorobenzene and the like can be used. For example, in the case of DMSO, the concentration of 10 to 20 w / v% DMSO is added to a sludge of 2 w / v% concentration (dry basis) in an amount equal to or more than the amount of sludge, and benzene (or acetone, chlorobenzene, acetonitrile, o −
In the case of (dichlorobenzene), 20 w / v% concentration is added in an amount equal to or more than the sludge amount.

【0023】清水としては、汚水処理工程で得られる処
理水24を使用するのが好都合である。なお、上記した
実施形態は、汚水の性状に基いて適宜変更可能である。
たとえば、汚水処理工程において、カルシウム除去処理
と生物処理とを行って凝集沈殿処理を省略するか、ある
いは生物処理と凝集沈殿処理とを行ってカルシウム除去
処理を省略してもよいし、キレート処理、イオン交換処
理などを加えてもよい。また、汚泥処理工程において、
汚泥の濃縮工程などを加えてもよいし、脱水ケーキを埋
立処分してもよい。
As the fresh water, it is convenient to use the treated water 24 obtained in the sewage treatment step. In addition, the above-described embodiment can be appropriately changed based on the property of sewage.
For example, in the sewage treatment step, calcium removal treatment and biological treatment may be performed to omit the coagulation-sedimentation treatment, or biological treatment and coagulation-sedimentation treatment may be performed to omit the calcium removal treatment, or a chelate treatment, Ion exchange treatment or the like may be added. In the sludge treatment process,
A sludge concentration step may be added, or the dehydrated cake may be landfilled.

【0024】[0024]

【発明の効果】以上のように本発明によれば、ダイオキ
シン類の抽出前に汚泥を清水で洗浄することにより、オ
ゾン・紫外線処理の阻害要因となるNH4 −N,Cl
イオン,Caイオンなどの濃度を低減して、高い紫外線
照射効率を実現できるとともに、無駄なオゾン消費を低
減することができ、ダイオキシン類を効率よく分解除去
できる。また、汚泥に残留するCl分が少なくなるの
で、汚泥を焼却・溶融処分する際のダイオキシンの発生
を低減できる。
As described above, according to the present invention, by washing sludge with fresh water before extraction of dioxins, NH 4 -N, Cl, which becomes an obstructive factor for ozone / ultraviolet treatment, can be obtained.
It is possible to reduce the concentration of ions, Ca ions, etc., to achieve high ultraviolet irradiation efficiency, reduce unnecessary ozone consumption, and efficiently decompose and remove dioxins. In addition, since the Cl content remaining in the sludge is reduced, it is possible to reduce the generation of dioxins when the sludge is incinerated or melted and disposed.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の一実施形態において汚水中のダイオキ
シン類を分解除去する汚水処理プラントの概略全体構成
図である。
FIG. 1 is a schematic overall configuration diagram of a wastewater treatment plant for decomposing and removing dioxins in wastewater in an embodiment of the present invention.

【図2】従来の汚水処理方法を示したフローチャートで
ある。
FIG. 2 is a flowchart showing a conventional wastewater treatment method.

【符号の説明】[Explanation of symbols]

10 汚水 12 カルシウム除去設備 13 生物処理設備 14 凝集沈殿処理設備 17,18 汚泥洗浄槽 19 ダイオキシン抽出槽 19a ダイオキシン抽出液供給手段 20 濾過装置 21,22 ダイオキシン分解装置 24 処理水 25 汚泥 26 洗浄汚泥 27 ダイオキシン抽出液 10 dirty water 12 Calcium removal equipment 13 Biological treatment equipment 14 Coagulation sedimentation treatment equipment 17,18 Sludge cleaning tank 19 Dioxin extraction tank 19a Dioxin extract supply means 20 Filtration device 21,22 Dioxin decomposition device 24 Treated water 25 sludge 26 Washing sludge 27 Dioxin extract

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI C02F 11/00 ZAB C02F 11/00 ZABC (56)参考文献 特開 平11−309499(JP,A) 特開 平11−33570(JP,A) 特開 平11−5099(JP,A) 特開 平10−296299(JP,A) 特開 平7−108285(JP,A) (58)調査した分野(Int.Cl.7,DB名) C02F 1/00 - 1/78 C02F 3/00 - 3/34 101 C02F 11/00 - 11/20 ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 Identification code FI C02F 11/00 ZAB C02F 11/00 ZABC (56) References JP-A-11-309499 (JP, A) JP-A-11-33570 (JP, A) JP-A-11-5099 (JP, A) JP-A-10-296299 (JP, A) JP-A-7-108285 (JP, A) (58) Fields investigated (Int. Cl. 7) , DB name) C02F 1/00-1/78 C02F 3/00-3/34 101 C02F 11/00-11/20

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 ダイオキシン類を含んだ汚水を生物処理
と凝沈処理の少なくとも一方を行う汚水処理工程におい
て処理し、浄化された処理水を得るとともに、前記生物
処理や凝沈処理で発生したダイオキシン類を含んだ汚泥
を清水で洗浄し、洗浄した汚泥にダイオキシン抽出液を
混合して汚泥中のダイオキシン類をダイオキシン抽出液
中に抽出し、このダイオキシン抽出液を汚泥より分離
し、濾過した後にオゾン・紫外線処理することによって
ダイオキシン類を分解除去することを特徴とする汚水中
のダイオキシン類の分解除去方法。
1. A sewage containing dioxins is treated in a sewage treatment step in which at least one of biological treatment and coagulation treatment is performed to obtain purified treated water, and dioxin generated by the biological treatment or coagulation treatment. The sludge containing the substances is washed with fresh water, the dioxin extract is mixed with the washed sludge to extract the dioxins in the sludge into the dioxin extract, and the dioxin extract is separated from the sludge, filtered and then ozone. A method for decomposing and removing dioxins in wastewater, which comprises decomposing and removing dioxins by treating with ultraviolet light.
【請求項2】 汚水を浄化する生物処理装置と凝集沈殿
処理装置の少なくとも一方を備えるとともに、生物処理
装置や凝集沈殿処理装置で発生した汚泥を処理する汚泥
処理装置を備え、前記汚泥処理装置は、清水供給手段を
有し、汚泥を洗浄する汚泥洗浄槽と、ダイオキシン抽出
液供給手段を有し、前記汚泥洗浄槽より移送される汚泥
中のダイオキシン類を抽出するダイオキシン抽出槽と、
前記ダイオキシン抽出槽より移送されるダイオキシン抽
出液を濾過する濾過手段と、オゾン供給手段および紫外
線照射手段を有し、前記濾過手段より移送されるダイオ
キシン抽出液中のダイオキシン類を分解するダイオキシ
ン分解塔とを備えたことを特徴とする汚水中のダイオキ
シン類の分解除去設備。
2. A biological treatment device for purifying sewage and / or a coagulation sedimentation treatment device, and a sludge treatment device for treating sludge generated in the biological treatment device or the coagulation sedimentation treatment device. , Having a fresh water supply means, a sludge cleaning tank for cleaning sludge, and a dioxin extract supply means, a dioxin extraction tank for extracting dioxins in the sludge transferred from the sludge cleaning tank,
A dioxin decomposition tower having a filtering means for filtering the dioxin extract transferred from the dioxin extraction tank, an ozone supply means, and an ultraviolet irradiation means, for decomposing dioxins in the dioxin extract transferred from the filtering means; A facility for decomposing and removing dioxins in sewage characterized by being equipped with.
JP11979198A 1998-04-30 1998-04-30 Method and equipment for decomposing and removing dioxins in sewage Expired - Fee Related JP3418550B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11979198A JP3418550B2 (en) 1998-04-30 1998-04-30 Method and equipment for decomposing and removing dioxins in sewage

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11979198A JP3418550B2 (en) 1998-04-30 1998-04-30 Method and equipment for decomposing and removing dioxins in sewage

Publications (2)

Publication Number Publication Date
JPH11309486A JPH11309486A (en) 1999-11-09
JP3418550B2 true JP3418550B2 (en) 2003-06-23

Family

ID=14770322

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11979198A Expired - Fee Related JP3418550B2 (en) 1998-04-30 1998-04-30 Method and equipment for decomposing and removing dioxins in sewage

Country Status (1)

Country Link
JP (1) JP3418550B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3795268B2 (en) * 1999-08-17 2006-07-12 アタカ工業株式会社 Method and apparatus for treating wastewater containing organochlorine compounds

Also Published As

Publication number Publication date
JPH11309486A (en) 1999-11-09

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