JP2000210663A - Method of removing dioxins in waste water - Google Patents
Method of removing dioxins in waste waterInfo
- Publication number
- JP2000210663A JP2000210663A JP11017083A JP1708399A JP2000210663A JP 2000210663 A JP2000210663 A JP 2000210663A JP 11017083 A JP11017083 A JP 11017083A JP 1708399 A JP1708399 A JP 1708399A JP 2000210663 A JP2000210663 A JP 2000210663A
- Authority
- JP
- Japan
- Prior art keywords
- waste water
- dioxins
- tank
- wastewater
- water
- 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- Withdrawn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
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は排水中のダイオキシ
ン類の除去方法に関する。ダイオキシン類は、主にごみ
焼却施設で発生してその排ガス中に含まれ、さらに灰
中、汚水中に移行してくる。本発明は、ごみ焼却施設の
湿式洗煙設備から出る排水や、ごみ最終処分場にある埋
立地浸出水処理設備および各種産業での既設排水処理設
備から出る排水中のダイオキシン類の除去方法に関す
る。The present invention relates to a method for removing dioxins in waste water. Dioxins are mainly generated in refuse incineration facilities and are contained in exhaust gas, and are further transferred to ash and sewage. The present invention relates to a method for removing dioxins from wastewater discharged from a wet smoke cleaning facility of a refuse incineration facility, and effluent discharged from a landfill leachate treatment facility at a landfill waste disposal facility and existing wastewater treatment facilities in various industries.
【0002】[0002]
【従来の技術】現在、排水処理でのダイオキシン類に対
する法的規制はないが、処理技術については、研究・開
発が進められている。「ごみ処理に係るダイオキシン類
発生防止等ガイドライン」には、ダイオキシン類の水へ
の溶解度が小さいことから、ダイオキシン類を削除する
には、SSの除去が有効であり、凝集沈殿法、砂濾
過処理法、生物濾過法等での低減化が確認されてお
り、当面SS濃度が10mg/リットル以下となるよう
排水を維持管理することが必要と記載されているに過ぎ
ない。2. Description of the Related Art At present, there are no legal restrictions on dioxins in wastewater treatment, but research and development are being advanced on treatment technologies. According to the “Guidelines for Prevention of Dioxin Generation Related to Garbage Disposal”, removal of SS is effective in removing dioxins because dioxins have low solubility in water. It has been confirmed that the amount of wastewater has been reduced by the method and the biological filtration method, and it merely states that it is necessary to maintain and control the wastewater so that the SS concentration is 10 mg / liter or less for the time being.
【0003】[0003]
【発明が解決しようとする課題】本発明は、排水中のダ
イオキシン類を可能な限り低濃度まで除去することがで
きる排水中のダイオキシン類の除去方法を提供すること
を目的とする。SUMMARY OF THE INVENTION An object of the present invention is to provide a method for removing dioxins in wastewater, which can remove dioxins in wastewater to the lowest possible concentration.
【0004】[0004]
【課題を解決するための手段】本発明は、ダイオキシン
類の性状が溶解性と粒子状に分けられていることに着目
し、溶解性ダイオキシン類と粒子状ダイオキシン類をそ
れぞれ完全に除去する工程からなる。SUMMARY OF THE INVENTION The present invention focuses on the fact that the properties of dioxins are divided into soluble and particulate forms, and from the step of completely removing soluble dioxins and particulate dioxins, respectively. Become.
【0005】すなわち、本発明による排水中のダイオキ
シン類の除去方法は、ダイオキシン類を含む排水をまず
膜分離処理し、次いで活性炭吸着処理することを特徴と
する方法である。[0005] That is, the method for removing dioxins in wastewater according to the present invention is characterized in that wastewater containing dioxins is first subjected to membrane separation treatment and then to activated carbon adsorption treatment.
【0006】[0006]
【作用】排水中のダイオキシン類は、上述の如く、溶解
性ダイオキシン類と粒子状ダイオキシン類に大別でき
る。ダイオキシン類の水に対する溶解度は極めて低い
が、有機溶媒などに対する溶解度は高いので溶解性ダイ
オキシン類も存在する。一方、粉子状ダイオキシン類
は、有機物質やSS(浮遊物質)に吸着された状態で存
在することがわかっている。溶解性ダイオキシン類は、
活性炭による吸着除去でほとんど100%除去できる
が、活性炭充填層はSSにより閉塞を来たす難点があ
り、その対策として活性炭充填層の逆洗を行う必要があ
る。As described above, dioxins in waste water can be roughly classified into soluble dioxins and particulate dioxins. Although the solubility of dioxins in water is extremely low, the solubility in organic solvents and the like is high, and so there are soluble dioxins. On the other hand, it has been known that powdered dioxins exist in a state of being adsorbed by an organic substance or SS (floating substance). Soluble dioxins are
Almost 100% can be removed by adsorption removal with activated carbon, but there is a problem that the activated carbon packed bed is blocked by SS, and as a countermeasure, it is necessary to backwash the activated carbon packed bed.
【0007】本発明による排水中のダイオキシン類の除
去方法では、活性炭吸着処理の前に、SSをほとんど1
00%除去することができる膜分離処理を行うので、膜
分離処理によりSSに吸着した粒子状ダイオキシン類を
除去することができる。次いで、活性炭吸着処理により
溶解性ダイオキシン類を除去することができる。こうし
て、排水中のダイオキシン類をほぼ100%除去するこ
とができる。In the method for removing dioxins in wastewater according to the present invention, SS is reduced to almost 1 before the activated carbon adsorption treatment.
Since the membrane separation treatment capable of removing 00% is performed, the particulate dioxins adsorbed on the SS by the membrane separation treatment can be removed. Next, soluble dioxins can be removed by activated carbon adsorption treatment. Thus, almost 100% of dioxins in the wastewater can be removed.
【0008】[0008]
【発明の実施の形態】以下、本発明による排水中のダイ
オキシン類の除去方法を2つの例で具体的に説明する。BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the method for removing dioxins in waste water according to the present invention will be specifically described with reference to two examples.
【0009】実施例1 この実施例は、図1に示すように、本発明方法を既設排
水処理設備から出る排水の処理に適用する例である。Embodiment 1 In this embodiment, as shown in FIG. 1, the method of the present invention is applied to the treatment of wastewater discharged from an existing wastewater treatment facility.
【0010】ごみ最終処分場にある埋立地浸出水処理設
備および各種産業での排水は、既設排水処理設備におい
て、排水槽(1) に蓄えられ、次いで薬品混入槽(2) へ送
られてここで凝集剤などが添加された後、凝集沈殿槽
(3) に送られてここで沈殿物が除去される。排水は次い
で中和槽(4) へ送られ、砂濾過塔(5) を通された後、放
流槽(6) に蓄えられ、必要に応じて系外へ放流される
か、または再利用に共される。[0010] Wastewater from landfill leachate treatment facilities and various industries at the final landfill site is stored in the drainage tank (1) in the existing wastewater treatment facility, and then sent to the chemical mixing tank (2) to be discharged there. After the coagulant is added in the coagulation settling tank
Sent to (3) where the sediment is removed. The wastewater is then sent to the neutralization tank (4), passed through the sand filtration tower (5), stored in the discharge tank (6), and discharged to the outside of the system as necessary, or reused. Shared.
【0011】本発明による排水中のダイオキシン類の除
去方法を実施するには、砂濾過塔(5) を通った後の排水
を、まず膜分離装置(7) で処理し、膜透過水を次いで活
性炭吸着塔(8) に通して吸着処理し、この処理水を放流
槽(6) の前流で既設排水処理施設の元のラインへ戻す。In order to carry out the method for removing dioxins in waste water according to the present invention, the waste water after passing through a sand filtration tower (5) is first treated in a membrane separator (7), and the permeated water is then removed. The treated water is passed through the activated carbon adsorption tower (8) for adsorption treatment, and this treated water is returned to the original line of the existing wastewater treatment facility upstream of the discharge tank (6).
【0012】実施例2 この実施例は、図2に示すように、本発明方法をごみ焼
却施設の湿式洗煙設備での排水処理装置から出る排水の
処理に適用する例である。Embodiment 2 In this embodiment, as shown in FIG. 2, the method of the present invention is applied to the treatment of wastewater discharged from a wastewater treatment device in a wet smoke cleaning facility of a refuse incineration facility.
【0013】ごみ焼却施設の焼却炉(11)から出た排煙は
電気集塵器、バグフィルターなどの集塵装置(12)に通さ
れた後、湿式洗煙設備の洗煙塔(13)底部へ送られる。洗
煙塔(13)の上部内には貯水槽(15)、循環ポンプ(16)およ
び冷却器(17)を経て循環する洗浄水がノズル(14)で散水
され、洗煙塔(13)の下部内には、循環ポンプ(18)を経て
循環する洗浄水がノズル(14)で散水されている。排煙は
洗煙塔(13)内を上行する間に湿式洗煙され、次いで処理
ガスはガス再加熱器(19)および煙突(20)を経て系外へ放
散される。The smoke discharged from the incinerator (11) of the refuse incineration facility is passed through a dust collector (12) such as an electric dust collector, a bag filter, etc., and then a smoke tower (13) of a wet smoke cleaning facility. Sent to the bottom. In the upper part of the smoke washing tower (13), washing water circulating through a water storage tank (15), a circulating pump (16) and a cooler (17) is sprinkled with a nozzle (14), and the smoke washing tower (13) is sprayed. In the lower part, washing water circulating through a circulation pump (18) is sprinkled by a nozzle (14). The flue gas is wet-smoke-washed while ascending in the smoke-wash tower (13), and then the processing gas is released outside the system via the gas reheater (19) and the chimney (20).
【0014】洗煙塔(13)の底部から出た洗煙排水は、洗
煙排水処理施設(21)へ送られる。この洗煙排水を本発明
による排水中のダイオキシン類の除去方法で処理するに
は、まず膜分離装置(22)で処理し、膜透過水を次いで活
性炭吸着塔(23)に通して吸着処理し、この処理水を系外
へ放流する。The wastewater from the bottom of the smoke tower (13) is sent to a wastewater treatment facility (21). In order to treat this smoke-washing wastewater by the method for removing dioxins in wastewater according to the present invention, the wastewater is first treated by a membrane separation device (22), and the permeated water is then passed through an activated carbon adsorption tower (23) to be subjected to an adsorption treatment. This treated water is discharged outside the system.
【0015】また、洗煙塔(13)の上部を循環する洗浄水
を本発明による排水中のダイオキシン類の除去方法で処
理するには、まず貯水槽(15)から洗浄水を膜分離装置(2
4)へ送って膜分離処理し、膜透過水を次いで活性炭吸着
塔(25)に通して吸着処理し、この処理水を貯水槽(15)へ
戻す。In order to treat the washing water circulating in the upper part of the smoke washing tower (13) by the method for removing dioxins in waste water according to the present invention, first, the washing water is removed from the water storage tank (15) by a membrane separation device (15). Two
4), membrane separation treatment is carried out, and the permeated water is then passed through an activated carbon adsorption tower (25) for adsorption treatment, and this treated water is returned to the water storage tank (15).
【0016】[0016]
【発明の効果】本発明によれば、活性炭吸着処理の前
に、SSをほとんど100%除去することができる膜分
離処理を行うので、膜分離処理によりSSに吸着した粒
子状ダイオキシン類を除去し、次いで活性炭吸着処理に
より溶解性ダイオキシン類を除去することができ、排水
中のダイオキシン類をほぼ100%除去することができ
る。According to the present invention, before the activated carbon adsorption treatment, a membrane separation treatment capable of removing almost 100% of SS is performed, so that particulate dioxins adsorbed on SS by the membrane separation treatment are removed. Then, soluble dioxins can be removed by activated carbon adsorption treatment, and dioxins in wastewater can be removed by almost 100%.
【0017】また、排水が湿式洗煙設備から出る排水で
ある場合、本発明方法は排ガス中のダイオキシン類除去
処理にもなる。When the waste water is waste water discharged from a wet smoke washing facility, the method of the present invention is also applicable to a process for removing dioxins in exhaust gas.
【図1】本発明方法を既設排水処理設備から出る排水の
処理に適用する例を示すフローシートである。FIG. 1 is a flow sheet showing an example in which the method of the present invention is applied to the treatment of wastewater discharged from an existing wastewater treatment facility.
【図2】本発明方法をごみ焼却施設の湿式洗煙設備での
排水処理装置から出る排水の処理に適用する例フローシ
ートである。FIG. 2 is an example flow sheet in which the method of the present invention is applied to the treatment of wastewater discharged from a wastewater treatment device in a wet smoke cleaning facility of a refuse incineration facility.
5:砂濾過塔 6:放流槽 7,22,24:膜分離装置 8,23,25:活性炭吸着塔 13:洗煙塔 15:貯水槽 5: Sand filtration tower 6: Discharge tank 7, 22, 24: Membrane separation device 8, 23, 25: Activated carbon adsorption tower 13: Smoke washing tower 15: Water storage tank
───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4D006 GA02 KA02 KA03 KA71 KB12 KB13 KB15 KD08 KD19 KE12P KE13P KE15Q PA01 PB08 PB70 PC80 4D024 AA04 AB11 BA02 CA01 DB03 DB05 DB20 DB21 ──────────────────────────────────────────────────続 き Continued on the front page F term (reference) 4D006 GA02 KA02 KA03 KA71 KB12 KB13 KB15 KD08 KD19 KE12P KE13P KE15Q PA01 PB08 PB70 PC80 4D024 AA04 AB11 BA02 CA01 DB03 DB05 DB20 DB21
Claims (3)
処理し、次いで活性炭吸着処理することを特徴とする排
水中のダイオキシン類の除去方法。1. A method for removing dioxins in waste water, comprising first subjecting waste water containing dioxins to membrane separation treatment and then subjecting the waste water to activated carbon adsorption treatment.
出る排水である請求項1記載の方法。2. The method according to claim 1, wherein the wastewater is wastewater discharged from a wet smoke cleaning facility of a refuse incineration plant.
ある請求項1記載の方法。3. The method according to claim 1, wherein the wastewater is wastewater discharged from an existing wastewater treatment facility.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11017083A JP2000210663A (en) | 1999-01-26 | 1999-01-26 | Method of removing dioxins in waste water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11017083A JP2000210663A (en) | 1999-01-26 | 1999-01-26 | Method of removing dioxins in waste water |
Publications (1)
Publication Number | Publication Date |
---|---|
JP2000210663A true JP2000210663A (en) | 2000-08-02 |
Family
ID=11934097
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11017083A Withdrawn JP2000210663A (en) | 1999-01-26 | 1999-01-26 | Method of removing dioxins in waste water |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2000210663A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002219492A (en) * | 2001-01-30 | 2002-08-06 | Kanegafuchi Chem Ind Co Ltd | Method for removing dioxins from waste water |
WO2007007569A1 (en) * | 2005-07-14 | 2007-01-18 | Idemitsu Kosan Co., Ltd. | Method for treatment of water containing hardly-degradable substance |
JP2009220019A (en) * | 2008-03-17 | 2009-10-01 | Metawater Co Ltd | Method and apparatus for treating wastewater |
CN105502552A (en) * | 2014-09-25 | 2016-04-20 | 中国石油化工股份有限公司 | Treatment method for cyclohexanone device waste water |
-
1999
- 1999-01-26 JP JP11017083A patent/JP2000210663A/en not_active Withdrawn
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002219492A (en) * | 2001-01-30 | 2002-08-06 | Kanegafuchi Chem Ind Co Ltd | Method for removing dioxins from waste water |
WO2007007569A1 (en) * | 2005-07-14 | 2007-01-18 | Idemitsu Kosan Co., Ltd. | Method for treatment of water containing hardly-degradable substance |
JP2007021347A (en) * | 2005-07-14 | 2007-02-01 | Idemitsu Kosan Co Ltd | Hardly decomposable substance-containing water treatment method |
JP2009220019A (en) * | 2008-03-17 | 2009-10-01 | Metawater Co Ltd | Method and apparatus for treating wastewater |
CN105502552A (en) * | 2014-09-25 | 2016-04-20 | 中国石油化工股份有限公司 | Treatment method for cyclohexanone device waste water |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
A300 | Withdrawal of application because of no request for examination |
Free format text: JAPANESE INTERMEDIATE CODE: A300 Effective date: 20060404 |