JPH01307488A - Treatment of trihalomethane in waste water - Google Patents
Treatment of trihalomethane in waste waterInfo
- Publication number
- JPH01307488A JPH01307488A JP13773688A JP13773688A JPH01307488A JP H01307488 A JPH01307488 A JP H01307488A JP 13773688 A JP13773688 A JP 13773688A JP 13773688 A JP13773688 A JP 13773688A JP H01307488 A JPH01307488 A JP H01307488A
- Authority
- JP
- Japan
- Prior art keywords
- trihalomethane
- water
- activated carbon
- waste water
- aerated
- 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
- 239000002351 wastewater Substances 0.000 title claims abstract description 24
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 32
- 239000007921 spray Substances 0.000 claims abstract description 14
- 238000000034 method Methods 0.000 claims description 12
- 238000005273 aeration Methods 0.000 claims description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 32
- 238000001914 filtration Methods 0.000 abstract description 3
- 239000007788 liquid Substances 0.000 description 8
- 238000011084 recovery Methods 0.000 description 7
- XSTXAVWGXDQKEL-UHFFFAOYSA-N Trichloroethylene Chemical group ClC=C(Cl)Cl XSTXAVWGXDQKEL-UHFFFAOYSA-N 0.000 description 6
- 230000000694 effects Effects 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 238000007599 discharging Methods 0.000 description 3
- 230000001105 regulatory effect Effects 0.000 description 3
- 238000011109 contamination Methods 0.000 description 2
- 238000011002 quantification Methods 0.000 description 2
- SCYULBFZEHDVBN-UHFFFAOYSA-N 1,1-Dichloroethane Chemical compound CC(Cl)Cl SCYULBFZEHDVBN-UHFFFAOYSA-N 0.000 description 1
- 239000012494 Quartz wool Substances 0.000 description 1
- 239000002519 antifouling agent Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
Landscapes
- Physical Water Treatments (AREA)
- Water Treatment By Sorption (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本参すは排水中のトリハロメタンの処理方法トリクロロ
エチレン及び1イ1,1)リクロロエタン等のトリハロ
メタンの回収装置に設置されている水分離器から発生ず
る微量に言まれだ排水中のトリハロメタンを除去する、
排水中のトリハロメタンの処理方法に関する・
〔従来の技術〕
最近におりて、トリハロメタンとその化合物の地下汚染
防止が一段と強化され、七〇殊去技術を必要としている
。Detailed Description of the Invention [Field of Industrial Application] This article describes a method for treating trihalomethane in wastewater from a water separator installed in a recovery device for trihalomethane such as trichlorethylene and 1-1,1) dichloroethane. Removes trihalomethane from wastewater, which is said to occur in very small amounts.
Concerning methods for treating trihalomethanes in wastewater [Prior technology] Recently, prevention of underground contamination of trihalomethanes and their compounds has been further strengthened, and 70 special removal techniques are required.
特に問題となるのは、1収装置の水離器から微量のトリ
ハロメタンが排水され、例えばトリクロロエチレンの場
合、換度として500〜1,000Ppm程度水中に混
入している状態から規制値の1/10以下の目標、例え
ば公共用水域への排出を行なう場合はトリクロロエチレ
ン0.031)I)m以下% 1 。A particular problem is that trace amounts of trihalomethane are discharged from the water separator of the 1-collection equipment. For example, in the case of trichlorethylene, the concentration ranges from 500 to 1,000 Ppm, which is 1/10 of the regulatory value. The following targets, for example, when discharging into public waters, trichlorethylene 0.031) I) m% 1 or less.
1、lトリクロロエチンo、sppm以下に処理する仁
とが地下汚染対策上必要とされている。1.L trichloroethine is required to be treated to less than 1,000 sppm as a countermeasure against underground contamination.
従来、水中に溶解している微量のトリハロメタンを除去
するには、主として気液接触法のエアレージ1ンによる
曝気のみで処理されている。Conventionally, in order to remove trace amounts of trihalomethane dissolved in water, only aeration using an aeration tank of the gas-liquid contact method has been used.
上述した従来の方法は、主としてエアレージ璽ン4気に
よる気液接触法を行なっていたために、規制値基準のl
/l O以下の一度に抑えるためには大容量の空気流量
を必要とし、そのため大型のファンを使用しなければな
らず、小型でコンパクトな曝気槽に対しては大きな負荷
がかかるという欠点を有している・
また、気液接触法に伴って発生するガスはミス) (m
ist )を伴ない、湿気を含んだガスが直接排気口を
通ってトリハロメタン回収装置に戻入されるため、回収
装置の運転状況に支障が生じ易いという欠点がある◎
本発明の目的は上述した欠点を除去し、排水中のトリハ
ロメタンを短時間で効率よく除去しうる排水中のトリハ
ロメタンの処理方法を提供することにある。The above-mentioned conventional method mainly uses a gas-liquid contact method using an airage tank, so it does not meet the regulatory value standard.
/l O or less at once requires a large air flow rate, which requires the use of a large fan, which has the disadvantage of placing a large load on a small and compact aeration tank. In addition, the gas generated with the gas-liquid contact method is a mistake) (m
ist), and the humid gas is directly returned to the trihalomethane recovery equipment through the exhaust port, which has the drawback that the operation status of the recovery equipment is likely to be disturbed. The purpose of the present invention is to solve the above-mentioned drawbacks. It is an object of the present invention to provide a method for treating trihalomethane in wastewater, which can remove trihalomethane in wastewater efficiently in a short time.
本発明の排水中のトリハロメタンの処理方法は、トリハ
ロメタンを含有する排水を貯溜槽で循環可能とするスプ
レーノズルで曝気処理を施したのちこれを活性炭処理し
かつ前記4気処理によって発生するガスを除湿したうえ
排水する手段を備えて構成される。The method for treating trihalomethane in wastewater of the present invention involves performing aeration treatment using a spray nozzle that allows the wastewater containing trihalomethane to be circulated in a storage tank, then treating it with activated carbon, and dehumidifying the gas generated by the four-gas treatment. Furthermore, it is constructed with means for draining water.
次に、図面を参照して本発明の詳細な説明する。 Next, the present invention will be described in detail with reference to the drawings.
第1図は本発明の一実施例の横断面図である。FIG. 1 is a cross-sectional view of one embodiment of the present invention.
第1図の実施例は、トリハロメタンを富んだ水をた
受ける原水人口1.原水人口1から受的水が溜められる
貯溜fi2.貯溜槽2の原水を循環するとともに強制的
に押し出すポンプ3.貯溜槽2の内部の気液の接触面積
を大きくするために一定間隔で取付けたスプレーノズル
4.スプレーノズル4である程度トリハロメタンが除去
された水をオーバフロー状態で排水する水出口5.活性
炭処理槽6、活性炭処理槽6を構成する活性炭槽7およ
び濾過材8.活性炭処理漕6で浄化した原水を峨9出す
バルブ9.水出口10.スプレーノズル4から出る噴霧
状の湿気を取除く除湿器11.排水塔12、・電動7ア
ン13を備えて構成される0次に、第1図の実施例の動
作について説明する・第1図の実施例による排水中のト
リハロメタンの処理方法の要点は、スプレーノズルを用
いた気液接触法を行なうことにより、エアレージlンの
ように大容量の空気流量を必要とせずして同等の性能が
得られ、さらに、処理の確実性を勘案して活性炭処理を
行なうことによシ、はぼ完全に排水中のトリハロメタン
が吸着され、例えば、トリクロロエチレンの場合、常に
定量限界値以下(0,001ppmで規制基準値の1/
300)まで除去出来る能率的な機能を提供するもので
ある。The embodiment of FIG. 1 has a raw water population of 1. Reservoir fi2 where passive water is stored from raw water population 1. Pump 3 that circulates the raw water in the storage tank 2 and forcibly pushes it out. 4. Spray nozzles installed at regular intervals to increase the contact area of gas and liquid inside the storage tank 2. 5. A water outlet for draining the water from which trihalomethane has been removed to some extent by the spray nozzle 4 in an overflow state. Activated carbon treatment tank 6, activated carbon tank 7 that constitutes the activated carbon treatment tank 6, and filter material 8. A valve 9 that discharges the raw water purified by the activated carbon treatment tank 6. Water outlet 10. Dehumidifier 11 that removes the sprayed moisture coming out of the spray nozzle 4. Next, the operation of the embodiment shown in FIG. 1 will be explained. The main points of the method for treating trihalomethane in waste water according to the embodiment shown in FIG. By using a gas-liquid contact method using a nozzle, it is possible to obtain the same performance as an airage system without requiring a large air flow rate. By doing this, trihalomethane in wastewater is almost completely adsorbed, and for example, in the case of trichlorethylene, it is always below the quantification limit (0,001 ppm, 1/1/2 of the regulatory standard value).
This provides an efficient function that can remove up to 300).
また、排水ダクトに除湿器を設置することにより、気液
接触を行う際にスプレーノズルから出る噴霧状の湿気を
取除く乙とができ、ガスのみが排気口を通って回収装置
に戻入されるため、トリハロメタンの回収装置の正常な
運転が確保されることを実現したものである。In addition, by installing a dehumidifier in the drainage duct, it is possible to remove the atomized moisture emitted from the spray nozzle during gas-liquid contact, and only the gas is returned to the recovery device through the exhaust port. Therefore, the normal operation of the trihalomethane recovery equipment is ensured.
第1図の実施例において、トリハロメタンを含んだ排水
が原水人口1から貯溜槽2に櫨められる・ポンプ3は貯
溜槽2の排水を循環するとともに排水を強制的に押し出
す。In the embodiment shown in FIG. 1, wastewater containing trihalomethane is pumped from raw water 1 to a storage tank 2. A pump 3 circulates the wastewater in the storage tank 2 and forcibly pushes out the wastewater.
スプレーノズル4は気液の接触面積を大きくするために
一定間隔で取付けてられ、このスプレーノズル4である
4度トリハロメタンが除去された排水はオーバーフロー
形式で水出口5から排水される。The spray nozzles 4 are installed at regular intervals to increase the contact area of gas and liquid, and the waste water from which the 4-degree trihalomethane has been removed is discharged from the water outlet 5 in an overflow format.
活性炭処理槽6は、水出口5から出る水を活性炭層7で
濾過することによって微量のトリハロメタンをほぼ完全
に吸着せしめる。The activated carbon treatment tank 6 filters the water coming out of the water outlet 5 through an activated carbon layer 7, thereby almost completely adsorbing trace amounts of trihalomethane.
濾過材8は、トリハロメタンを完全に除去した水をパル
プ9を開にして排出し活性炭の混入を防止するために濾
過させる部材で、材質としてはグラスクール、石英ウー
ル等の耐尋剤性のものが利用される。The filtering material 8 is a member that drains the water from which trihalomethane has been completely removed by opening the pulp 9 and filtering it to prevent the mixture of activated carbon, and is made of a material that is resistant to antifouling agents such as glass core or quartz wool. is used.
トリハロメタンを活性炭層7によって完全に吸着除去し
た水は水出口11から排出される◎除湿器11は、スプ
レーノズル4から出る噴霧状の水が排気塔12の排気口
へ混入することを防止する役目をはたす。排水中のトリ
ハロメタンはスプレーノズル4から噴霧されると液相が
ら気相に揮散され、排気塔12からガス状となって電動
ファン13で強制的に排出される。また排出されたトリ
ハロメタン、例えばトリクロロエチレンのガスについて
は回収装置に戻入され回収される〇このようにして、ト
リハロメタンを官有する排水を貯溜槽で循環可能とする
スプレーノズルを利用して曝気処理を施したのちこれを
活用次処理しかつ前記曝気処理によって発生するガスを
防湿したうえ排出することによ)、排水中のトリハロメ
タンを短時間かつ効率的に処理することができる〇〔発
明の効果〕
以上説明したように木兄I!#1は、スプレーノズルに
よる曝気処理と、引続く活性炭処理を併用しかつ曝気処
理によって発生するガスを除去して排出することによ)
、排水中のトリハロメタンに対して短時間で著しく除去
効率の尚い処理が行なえるという効果がある。The water from which trihalomethane has been completely adsorbed and removed by the activated carbon layer 7 is discharged from the water outlet 11 ◎The dehumidifier 11 serves to prevent water in the form of atomized water emitted from the spray nozzle 4 from entering the exhaust port of the exhaust tower 12. to play. When the trihalomethane in the waste water is sprayed from the spray nozzle 4, the liquid phase is volatilized into the gas phase, and the gaseous state is forcibly discharged from the exhaust tower 12 by the electric fan 13. In addition, the discharged trihalomethane gas, such as trichlorethylene gas, is returned to the recovery device and recovered. In this way, aeration treatment is performed using a spray nozzle that allows the wastewater containing trihalomethane to be circulated in the storage tank. By utilizing this and discharging the gas generated by the aeration treatment after moisture-proofing), trihalomethane in wastewater can be treated quickly and efficiently.〇 [Effects of the Invention] As explained above. As you did, Ki-nii I! #1 is by using a combination of aeration treatment using a spray nozzle and subsequent activated carbon treatment, and removing and discharging the gas generated by the aeration treatment)
This method has the effect that trihalomethane in wastewater can be treated in a short period of time with extremely high removal efficiency.
例えば、人口濃度のトリクロロエチレン500〜1.0
00 ppmが出口濃度0.01ppm(定量限界)以
下となり、はぼ100チの除去効果があった@また、従
来気液接触で発生するガスを、排気口からトリハロメタ
ン回収装置へ戻入する際問題となっていたミストの発生
による湿気についても除湿器によって解決できるという
効果がある。For example, the population concentration of trichlorethylene is 500 to 1.0
00 ppm was below the outlet concentration of 0.01 ppm (quantification limit), and the removal effect was approximately 100 ppm.@Also, there was a problem when the gas generated by conventional gas-liquid contact was returned to the trihalomethane recovery device from the exhaust port. The dehumidifier has the effect of solving the problem of moisture caused by the generation of mist.
第1図は本−日の一実施例にかかわる横断面図である。
l・・・・・・原水入口、2・・・・・・貯溜槽、3・
・団・ポンプ、4・・・・・・スプレーノズル、5・旧
・・水出口、6・旧・・活性炭処理槽、7・・・・・・
活性炭層、8・・・・・・濾過材、9・・・・・・パル
プ、10・・・・・・水出口、11・・・・・・除湿器
、12・・・・・・排水塔、13・・・・・・1動ファ
ン。
代理人 弁理士 内 原 晋FIG. 1 is a cross-sectional view of today's embodiment. l...Raw water inlet, 2...Storage tank, 3.
・Group: Pump, 4: Spray nozzle, 5: Old: Water outlet, 6: Old: Activated carbon treatment tank, 7:...
Activated carbon layer, 8... Filter material, 9... Pulp, 10... Water outlet, 11... Dehumidifier, 12... Drainage Tower, 13...1 moving fan. Agent Patent Attorney Susumu Uchihara
Claims (1)
るスプレーノズルで曝気処理を施したのちこれを活性炭
処理しかつ前記曝気処理によって発生するガスを除湿し
たうえ排出する手段を備えて成ることを特徴とする排水
中のトリハロメタンの処理方法。The waste water containing trihalomethane is aerated using a spray nozzle that can be circulated in a storage tank, and then treated with activated carbon, and the wastewater generated by the aeration is dehumidified and then discharged. A method for treating trihalomethanes in wastewater.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13773688A JPH01307488A (en) | 1988-06-03 | 1988-06-03 | Treatment of trihalomethane in waste water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13773688A JPH01307488A (en) | 1988-06-03 | 1988-06-03 | Treatment of trihalomethane in waste water |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH01307488A true JPH01307488A (en) | 1989-12-12 |
Family
ID=15205628
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP13773688A Pending JPH01307488A (en) | 1988-06-03 | 1988-06-03 | Treatment of trihalomethane in waste water |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01307488A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH09187795A (en) * | 1995-12-29 | 1997-07-22 | Seiken Clean:Kk | Removing method for trihalomethane contained in water |
-
1988
- 1988-06-03 JP JP13773688A patent/JPH01307488A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH09187795A (en) * | 1995-12-29 | 1997-07-22 | Seiken Clean:Kk | Removing method for trihalomethane contained in water |
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