JP2765170B2 - Treatment of wastewater containing fungicides - Google Patents

Treatment of wastewater containing fungicides

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Publication number
JP2765170B2
JP2765170B2 JP2069995A JP6999590A JP2765170B2 JP 2765170 B2 JP2765170 B2 JP 2765170B2 JP 2069995 A JP2069995 A JP 2069995A JP 6999590 A JP6999590 A JP 6999590A JP 2765170 B2 JP2765170 B2 JP 2765170B2
Authority
JP
Japan
Prior art keywords
wastewater
absorbance
activated carbon
nitrification
denitrification
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 - Lifetime
Application number
JP2069995A
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Japanese (ja)
Other versions
JPH03270795A (en
Inventor
佐藤  進
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.)
Sumitomo Heavy Industries Ltd
Original Assignee
Sumitomo Heavy Industries Ltd
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Priority to JP2069995A priority Critical patent/JP2765170B2/en
Publication of JPH03270795A publication Critical patent/JPH03270795A/en
Application granted granted Critical
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Description

【発明の詳細な説明】 [産業上の利用分野] この発明は、航空機から排出されるトイレ排水のよう
に殺菌剤を多量に含む排水の生物処理法に改良を施した
ものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention is an improvement in a biological treatment method for wastewater containing a large amount of a disinfectant, such as toilet wastewater discharged from an aircraft.

[従来の技術] 殺菌剤を多量に含む排水、例えば、航空機内で循環使
用されたし尿性排水の処理法としては、大別して、生物
処理方式と凝集沈殿法による化学処理方式とが知られて
いる。
[Prior Art] As a method of treating wastewater containing a large amount of a bactericide, for example, human wastewater circulated and used in an aircraft, a biological treatment method and a chemical treatment method by a coagulation sedimentation method are known. I have.

ところで、航空機排水には衛生上の観点から多量の臭
素系殺菌剤が添加されているため、生物処理法によって
排水処理を行う場合、その過程において、排水中に含ま
れる多量の殺菌剤による有機物阻害が懸念されたが、有
機物除去については支障なく処理できることが確認され
ている。これは有機物(BOD)分解菌が殺菌剤に馴養し
耐性を得たためとみられる。
By the way, since a large amount of bromine-based germicides are added to aircraft effluent from a sanitary point of view, when performing wastewater treatment by a biological treatment method, in the process, a large amount of germicides contained in the effluents inhibit organic matter. However, it has been confirmed that the removal of organic substances can be performed without any problem. This is considered to be because organic matter (BOD) degrading bacteria acclimated to the fungicide and gained resistance.

しかしながら、生物処理法によって有機物除去のほか
に硝化・脱窒を行う場合には、有機物除去は十分に可能
であっても、殺菌剤が硝化菌に阻害を与え、硝化阻害を
生起して安定した窒素除去がなされないという問題点が
ある。
However, in the case of performing nitrification and denitrification in addition to organic matter removal by the biological treatment method, even if organic matter removal is sufficiently possible, the bactericide inhibits nitrifying bacteria, causing nitrification inhibition and becoming stable. There is a problem that nitrogen is not removed.

[この発明が解決しようとする課題] この発明は、上記問題点を解決することを課題として
なされたものであって、臭素系殺菌剤のような有色殺菌
剤を含む排水を生物処理法によって硝化・脱窒処理を行
うに当たり、その前段階又は処理の過程において、排水
中に含まれる多量の殺菌剤を活性炭により吸着除去して
硝化阻害を改善し、安定した窒素除去を可能ならしめる
手段を提供することを目的とするものである。
[Problems to be Solved by the Invention] The present invention has been made to solve the above problems, and nitrates wastewater containing a colored disinfectant such as a bromine-based disinfectant by a biological treatment method.・ In the denitrification process, in the previous stage or in the process, a large amount of disinfectant contained in the wastewater is removed by adsorption with activated carbon to improve nitrification inhibition and provide a means to enable stable nitrogen removal. It is intended to do so.

[課題を解決するための手段] この発明は、前記課題を解決するための手段を提供す
るものであって、多量の有色殺菌剤を含む排水を生物処
理法によって硝化・脱窒処理を行うに当たり、吸光光度
計により当該殺菌剤特有の吸光度最大吸収波長における
排水の吸光度を測定し、該吸光度が1.5を超える場合、
排水中に粉末状活性炭を添加すること及び添加後の吸光
度を0.5〜1.5の範囲内とすることを特徴とし、例えば、
ブルーの色彩を有し臭素を含むメチレンブルーを主体と
する多量の殺菌剤を含む航空機のし尿系排水を生物処理
法によって硝化・脱窒処理を行うに当たっては、当該殺
菌剤特有の吸光度最大吸収波長である波長662nmにおけ
る排水の吸光度を測定し、該吸光度が1.5を超える場
合、排水中に粉末状活性炭を添加し、添加後の吸光度を
0.5〜1.5の範囲内とすればよい。
[Means for Solving the Problems] The present invention provides means for solving the above-mentioned problems. In the present invention, wastewater containing a large amount of a colored germicide is subjected to nitrification and denitrification by a biological treatment method. By measuring the absorbance of the wastewater at the absorbance maximum absorption wavelength specific to the bactericide with an absorptiometer, if the absorbance exceeds 1.5,
It is characterized in that the powdered activated carbon is added to the wastewater and the absorbance after the addition is in the range of 0.5 to 1.5, for example,
In performing nitrification and denitrification treatment of human sewage wastewater containing a large amount of disinfectant mainly composed of methylene blue containing bromine and containing bromine by biological treatment, the absorbance maximum absorption wavelength specific to the disinfectant is used. The absorbance of the wastewater at a certain wavelength 662 nm is measured, and when the absorbance exceeds 1.5, powdered activated carbon is added to the wastewater, and the absorbance after the addition is measured.
It may be in the range of 0.5 to 1.5.

また、粉末状活性炭はスラリー状として添加するを可
とし、その添加位置は、硝化・脱窒工程の前段において
添加しても、硝化・脱窒工程において添加してもよい。
The powdered activated carbon may be added in the form of slurry, and may be added at a stage prior to the nitrification / denitrification step or at the nitrification / denitrification step.

[作用] 本発明によれば、多量の殺菌剤なかんづく有色殺菌剤
を含む排水を生物処理法によって硝化・脱窒処理を行う
に当たり、当該殺菌剤特有の吸光度最大吸収波長におけ
る排水の吸光度を測定し、該吸光度が1.5を超える場合
は、殺菌剤過多による硝化阻害を除去するため、排水中
に粉末状活性炭を添加し、過剰殺菌剤を活性炭により吸
着除去することによって、硝化阻害要因を排除すること
ができる。硝化阻害を排除するためには、活性炭添加後
の吸光度を、0.5〜1.5の範囲内とするのが好ましい。
[Action] According to the present invention, in performing nitrification and denitrification treatment of wastewater containing a large amount of a fungicide, particularly a colored fungicide, by biological treatment, the absorbance of the wastewater at the absorbance maximum absorption wavelength specific to the fungicide is measured. If the absorbance exceeds 1.5, powdery activated carbon is added to the wastewater in order to remove nitrification inhibition due to excess bactericide, and the excess bactericide is adsorbed and removed by activated carbon to eliminate the nitrification inhibition factor. Can be. In order to eliminate nitrification inhibition, the absorbance after the addition of activated carbon is preferably in the range of 0.5 to 1.5.

長時間飛行した航空機のし尿系排水の処理について説
明すると、航空機排水は、衛生上の観点から、ブルーの
色彩を有し臭素を含むメチレンブルーを主体とする多量
の殺菌剤を含んでいるが、この排水を生物処理法によっ
て硝化・脱窒処理する場合には、当該殺菌剤特有の吸光
度最大吸収波長である波長662nmにおける排水の吸光度
を測定し、該吸光度が1.5を超える場合、排水中に粉末
状活性炭を添加し、添加後の吸光度を0.5〜1.5の範囲内
とすれば、硝化阻害要因となる過剰殺菌剤は活性炭によ
り吸着除去され、硝化阻害を生起することなく、硝化・
脱窒処理を行うことができる。
Explaining the treatment of human wastewater from a long-flighted aircraft, aircraft wastewater contains, from a sanitary point of view, a large amount of a disinfectant mainly composed of methylene blue having a blue color and containing bromine. When the wastewater is subjected to nitrification and denitrification by a biological treatment method, the absorbance of the wastewater at a wavelength of 662 nm, which is the maximum absorbance wavelength specific to the bactericide, is measured. If activated carbon is added and the absorbance after the addition is within the range of 0.5 to 1.5, the excess bactericide which becomes a nitrification inhibiting factor is adsorbed and removed by activated carbon, and without causing nitrification inhibition, nitrification
A denitrification treatment can be performed.

[実施例] 航空機排水を例にとって説明すると、殺菌剤として
は、ブルーの色素を有し臭素を含んだメチレンブルーを
主体とする殺菌剤が用いられ、排水中にはBr濃度で通常
2mg/程度含まれている。このBr濃度であれば、BOD分
解菌も消化菌も1週間程度で馴養される。
[Examples] Explaining the case of aircraft drainage as an example, as a disinfectant, a disinfectant mainly composed of methylene blue containing a blue pigment and containing bromine is used.
Contains 2mg / about. With this Br concentration, both BOD degrading bacteria and digestive bacteria are acclimated in about one week.

しかしながら、航空機排水における殺菌剤の使用量
は、航空機各社でその使用マニュアルにバラツキがあ
り、計算上、最小値と最大値では100倍程度の殺菌剤濃
度差となり得る。
However, the usage amount of the disinfectant in the aircraft drainage varies depending on the use manual of each aircraft company, and the difference between the minimum value and the maximum value of the disinfectant concentration can be calculated by about 100 times.

(1) 実験例 そこで、Br濃度を前記通常値(2mg/)の5倍(10mg
/)とした場合の処理水中に含まれるNH4 +−Nの増加
状況を実験例として第2図に示す。
(1) Experimental example Therefore, the Br concentration was set to 5 times (10 mg) the normal value (2 mg /).
FIG. 2 shows an experimental example of an increase in NH 4 + -N contained in the treated water in the case of (/).

この実験例によれば、経過日数3日目にBr濃度を通
常値(2mg/)の5倍(10mg/)とした場合、処理水
のNH4 +−N濃度は急上昇し明らかに硝化阻害を引き起こ
すことが分かる。
According to this experimental example, when the Br concentration was set to 5 times (10 mg /) of the normal value (2 mg /) on the third day after the lapse of days, the NH 4 + -N concentration of the treated water rapidly increased, and the nitrification inhibition was apparently suppressed. It turns out to cause.

この場合添加5日後(経過日数8日目)には以前のNH
4 +−N濃度となるため、硝化菌は高濃度の殺菌剤にも馴
養し耐性を得ることが分かる。
In this case, 5 days after the addition (8 days after the addition), the previous NH was added.
Since the concentration becomes 4 + -N, it can be seen that nitrifying bacteria acclimate to a high concentration of a bactericide and obtain resistance.

しかしながら、Br濃度が変動する場合には、硝化菌の
馴養は期待できず、処理水のNH4 +−N濃度は高い値とな
る。
However, when the Br concentration fluctuates, acclimation of nitrifying bacteria cannot be expected, and the NH 4 + -N concentration of the treated water becomes a high value.

(2) 実験例 次に、殺菌剤による硝化反応への悪影響を実験例と
して第3図に示す。
(2) Experimental Example Next, FIG. 3 shows an adverse effect of the germicide on the nitrification reaction as an experimental example.

試験条件として N−VOL:0.1kg/m3・日 基質:(NH42CO3 種汚泥:殺菌剤通常濃度(Br:2mg/)で馴養 上記試験条件により、殺菌剤に馴養した活性汚泥を使
用し、殺菌剤による硝化速度への影響を測定した結果、
NH4 +−NおよびNOx-−N濃度を縦軸に、経過時間を横軸
にとると第3図のとおりとであった。
As test conditions N-VOL: 0.1 kg / m 3 · day Substrate: (NH 4 ) 2 CO 3 type sludge: disinfectant acclimated at normal concentration (Br: 2 mg /) Activated sludge acclimated to disinfectant under the above test conditions As a result of measuring the effect on the nitrification rate by the bactericide,
FIG. 3 shows the NH 4 + -N and NOx -- N concentrations on the vertical axis and the elapsed time on the horizontal axis.

第3図により明らかなように、殺菌剤の濃度(Br濃度
を指標として)が通常値(2mg/)の3倍となると硝化
速度は3/4に、また、5倍となると硝化速度は1/2に遅速
し、殺菌剤による硝化障害が生ずることが判明した。
As is clear from FIG. 3, when the concentration of the fungicide (using the Br concentration as an index) becomes three times the normal value (2 mg /), the nitrification rate becomes 3/4, and when the concentration becomes five times, the nitrification rate becomes one. It was found that the rate was slowed down to / 2, and nitrification damage by fungicides occurred.

(3) 実験例 ところが、硝化・脱窒工程またはその前段において排
水中に粉末状活性炭を添加すると、殺菌剤は活性炭によ
く吸着され前記ブルーの色素は脱色される。
(3) Experimental example However, when powdered activated carbon is added to the wastewater in the nitrification / denitrification step or in the preceding stage, the disinfectant is well adsorbed by the activated carbon and the blue pigment is decolorized.

実験例として、殺菌剤を通常値の5倍(10mg/)
に増量した航空機排水を用い、第3図と同一試験条件で
粉末活性炭200mg/を添加したところ、第4図に示すよ
うに、通常値に近い処理結果が得られることが判明し
た。
As an experimental example, the disinfectant is 5 times the normal value (10mg /)
When 200 mg / powder of activated carbon powder was added under the same test conditions as in FIG. 3 using the increased amount of aircraft wastewater, it was found that a treatment result close to the normal value was obtained as shown in FIG.

(4) 実験例 排水中の有色殺菌剤含有量は、当該殺菌剤特有の吸光
度最大吸収波長における排水の吸光度を測定することに
よってその多寡を知ることができる。
(4) Experimental Example The content of the colored fungicide in the wastewater can be known by measuring the absorbance of the wastewater at the absorbance maximum absorption wavelength specific to the fungicide.

一例として、ブルーの色素を有し臭素を含んだメチレ
ンブルーを主体とする殺菌剤の吸収度波長スキャンを第
5図に示す。すなわち、波長662nmに最大吸収があり、
この波長で活性炭添加量をコントロールできることが分
かる。
As an example, FIG. 5 shows an absorbance wavelength scan of a bactericide mainly containing methylene blue containing a blue pigment and containing bromine. That is, there is a maximum absorption at a wavelength of 662 nm,
It can be seen that the amount of activated carbon can be controlled at this wavelength.

前記実験例において、波長662nmで排水の吸光
度を測定したとき、吸光度が1.5を超えると硝化阻害が
生じ、吸光度を0.5〜1.5好ましくは1.0以下とすれば、
硝化阻害が除去されることが確認された。
In the experimental example, when measuring the absorbance of the wastewater at a wavelength of 662 nm, nitrification inhibition occurs when the absorbance exceeds 1.5, if the absorbance is 0.5 to 1.5, preferably 1.0 or less,
It was confirmed that nitrification inhibition was eliminated.

[実施例] 第1図は、本発明方法を示す工程図であって、Aは粉
末活性炭を硝化・脱窒工程の前段において添加する例、
Bは硝化・脱窒工程において添加する例、Cは硝化・脱
窒工程の前段と硝化・脱窒工程の双方において添加する
例を示す。
[Example] FIG. 1 is a process chart showing the method of the present invention, wherein A is an example in which powdered activated carbon is added at a stage prior to the nitrification / denitrification step
B shows an example of addition in the nitrification / denitrification step, and C shows an example of addition in both the former stage of the nitrification / denitrification step and the nitrification / denitrification step.

まず第1図Aに示す工程について説明すると、図中、
1は原水調整槽、2は活性炭反応槽、3は硝化・脱窒
槽、4は沈殿分離槽、5は粉末活性炭スラリー化槽、6
は吸光光度計、7はシーケンサを示し、航空機排水等多
量の有色殺菌剤を含む排水は原水調整槽1から活性炭反
応槽2を経て硝化・脱窒槽3に送られる。
First, the process shown in FIG. 1A will be described.
1 is a raw water adjustment tank, 2 is an activated carbon reaction tank, 3 is a nitrification / denitrification tank, 4 is a sedimentation separation tank, 5 is a powdered activated carbon slurry tank, 6
Reference numeral 7 denotes an absorptiometer, 7 denotes a sequencer, and wastewater containing a large amount of a colored sterilizing agent such as aircraft wastewater is sent from a raw water regulating tank 1 to a nitrification / denitrification tank 3 via an activated carbon reaction tank 2.

粉末活性炭aはスラリー化槽5において水分と混合撹
拌されスラリー化された後、必要に応じポンプPによっ
て活性炭反応槽2に送られる。なお図中Mはモータ,Bは
ブロワを示す。
The powdered activated carbon a is mixed and stirred with water in the slurrying tank 5 to be slurried, and then sent to the activated carbon reaction tank 2 by the pump P as necessary. In the drawing, M indicates a motor, and B indicates a blower.

吸光光度計6は、測定管6aを介して例えば波長662nm
における原水調整槽1内に滞留する排水の吸光度を測定
し、一方、測定管6bを介して活性炭反応槽2内の排水の
吸光度を測定する。
The absorptiometer 6 is, for example, at a wavelength of 662 nm via a measuring tube 6a.
The absorbance of the wastewater retained in the raw water adjusting tank 1 in the above is measured, while the absorbance of the wastewater in the activated carbon reaction tank 2 is measured via the measuring pipe 6b.

そして、原水調整槽1内に滞留する排水の吸光度が1.
5を超える場合には、シーケンサ7を介してポンプPを
駆動し、スラリー化槽5でスラリー化された粉末活性炭
aを活性炭反応槽2に送り込み、活性炭反応槽2内の排
水の吸光度を0.5〜1.5の範囲内、好ましくは1.0以下に
保つようコントロールされる。
Then, the absorbance of the waste water staying in the raw water adjusting tank 1 is 1.
If it exceeds 5, the pump P is driven via the sequencer 7 and the powdered activated carbon a slurried in the slurrying tank 5 is sent to the activated carbon reaction tank 2 and the absorbance of the wastewater in the activated carbon reaction tank 2 is reduced to 0.5 to 0.5. It is controlled within the range of 1.5, preferably 1.0 or less.

その結果、硝化・脱窒槽3に流入する排水中の殺菌剤
は、硝化阻害を生起しない程度にまで活性炭により吸着
除去され、硝化・脱窒反応条件を良好に保つことができ
る。
As a result, the disinfectant in the wastewater flowing into the nitrification / denitrification tank 3 is adsorbed and removed by activated carbon to such an extent that nitrification is not inhibited, and the nitrification / denitrification reaction conditions can be kept good.

第1図Bに示す工程は、活性炭反応槽2を省略し、ス
ラリー化槽5でスラリー化された粉末活性炭aを直接硝
化・脱窒槽3に送り込むようにし、測定管6bを介して該
硝化・脱窒槽3内の排水の吸光度を測定し、その吸光度
を0.5〜1.5の範囲内に保つようにしたものであって、排
水中の殺菌剤の量が多量とはいえ比較的少ない場合に適
している。
In the step shown in FIG. 1B, the activated carbon reaction tank 2 is omitted and the powdered activated carbon a slurried in the slurrying tank 5 is directly sent to the nitrification / denitrification tank 3, and the nitrification / denitrification is performed via the measuring pipe 6b. The absorbance of the wastewater in the denitrification tank 3 is measured, and the absorbance is kept in the range of 0.5 to 1.5, which is suitable when the amount of the disinfectant in the wastewater is relatively small although the amount is large. I have.

第1図Cに示す工程は、吸光光度計6およびシーケン
サ7を省略し、スラリー化槽5でスラリー化された粉末
活性炭aを常に活性炭反応槽2および硝化・脱窒槽3に
添加するようにしたものであって、排水中に含まれる殺
菌剤の量が既知である場合に適している。
In the step shown in FIG. 1C, the absorptiometer 6 and the sequencer 7 are omitted, and the powdered activated carbon a slurried in the slurrying tank 5 is always added to the activated carbon reaction tank 2 and the nitrification / denitrification tank 3. And is suitable when the amount of germicide contained in the wastewater is known.

[効果] 本発明によれば、多量の有色殺菌剤を含む排水を生物
処理法によって硝化・脱窒処理を行うに当たり、吸光光
度計により当該殺菌剤特有の吸光度最大吸収波長におけ
る排水の吸光度を測定し、該吸光度が1.5を超える場
合、排水中に粉末状活性炭を添加し、添加後の吸光度を
0.5〜1.5の範囲内とすることによって、硝化阻害を除去
することができる。
[Effects] According to the present invention, in performing nitrification / denitrification treatment of wastewater containing a large amount of a colored germicide by a biological treatment method, the absorbance of the effluent at the absorbance maximum absorption wavelength specific to the germicide is measured by an absorptiometer. If the absorbance exceeds 1.5, add powdered activated carbon to the wastewater and adjust the absorbance after the addition.
By setting it in the range of 0.5 to 1.5, nitrification inhibition can be eliminated.

また、粉末状活性炭をスラリー状として添加すること
によって排水中にほぼ均一に添加することができ、その
添加位置は、殺菌剤の含有量の多寡によって適当に選択
することができる。
In addition, by adding powdered activated carbon as a slurry, it can be added almost uniformly to wastewater, and the addition position can be appropriately selected depending on the content of the fungicide.

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

第1図A,B,Cは本発明方法の工程を示す説明図、第2図
ないし第5図は実験例を示すグラフ図である。 1:原水調整槽、2:活性炭反応槽 3:硝化・脱窒槽、4:沈殿分離槽 5:粉末活性炭スラリー化槽 6:吸光光度計、7:シーケンサ P:ポンプ、M:モータ、B:ブロワ
FIGS. 1A, 1B and 1C are explanatory views showing the steps of the method of the present invention, and FIGS. 2 to 5 are graphs showing experimental examples. 1: Raw water adjustment tank, 2: Activated carbon reaction tank 3: Nitrification / denitrification tank, 4: Sedimentation separation tank 5: Activated carbon powder slurry tank 6: Spectrophotometer, 7: Sequencer P: Pump, M: Motor, B: Blower

Claims (6)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】多量の有色殺菌剤を含む排水を生物処理法
によって硝化・脱窒処理を行うに当たり、吸光光度計に
より当該殺菌剤特有の吸光度最大吸収波長における排水
の吸光度を測定し、該吸光度が1.5を超える場合、排水
中に粉末状活性炭を添加することを特徴とする排水の処
理法。
When a wastewater containing a large amount of a colored fungicide is subjected to nitrification and denitrification by a biological treatment method, the absorbance of the wastewater at an absorption maximum wavelength unique to the fungicide is measured by an absorptiometer. The method for treating wastewater, wherein powdered activated carbon is added to the wastewater when the value exceeds 1.5.
【請求項2】多量の有色殺菌剤を含む排水を生物処理法
によって硝化・脱窒処理を行うに当たり、吸光光度計に
より当該殺菌剤特有の吸光度最大吸収波長における排水
の吸光度を測定し、該吸光度が1.5を超える場合、排水
中に粉末状活性炭を添加し、添加後の吸光度を0.5〜1.5
の範囲内とすることを特徴とする排水の処理法。
2. A wastewater containing a large amount of a colored germicide is subjected to nitrification and denitrification by a biological treatment method, and the absorbance of the effluent at the maximum absorption wavelength specific to the germicide is measured by an absorptiometer. If the value exceeds 1.5, add powdered activated carbon to the wastewater and adjust the absorbance after addition to 0.5 to 1.5.
A method for treating wastewater, characterized by being within the range of.
【請求項3】ブルーの色彩を有し臭素を含むメチレンブ
ルーを主体とする多量の殺菌剤を含む航空機のし尿系排
水を生物処理法によって硝化・脱窒処理を行うに当た
り、吸光光度計により当該殺菌剤特有の吸光度最大吸収
波長である662nmにおける排水の吸光度を測定し、該吸
光度が1.5を超える場合、排水中に粉末状活性炭を添加
し、添加後の吸光度を0.5〜1.5の範囲内とすることを特
徴とする排水の処理法。
3. Nitrogen and denitrification treatment of an aircraft wastewater containing a large amount of a disinfectant mainly composed of methylene blue containing bromine and containing bromine by a biological treatment method. Measure the absorbance of the wastewater at 662 nm, which is the maximum absorbance wavelength of the agent, and if the absorbance exceeds 1.5, add powdered activated carbon to the wastewater and keep the absorbance after addition within the range of 0.5 to 1.5. A method for treating wastewater, characterized in that:
【請求項4】粉末状活性炭を、スラリー状として添加す
る請求項1)乃至3)記載の排水の処理法。
4. The method for treating wastewater according to claim 1, wherein the activated carbon powder is added as a slurry.
【請求項5】活性炭を硝化・脱窒工程の前段において添
加する請求項1)乃至4)記載の排水の処理法。
5. The method for treating wastewater according to claim 1, wherein the activated carbon is added before the nitrification / denitrification step.
【請求項6】活性炭を硝化・脱窒工程において添加する
請求項1)乃至4)記載の排水の処理法。
6. The method for treating wastewater according to claim 1, wherein the activated carbon is added in the nitrification / denitrification step.
JP2069995A 1990-03-20 1990-03-20 Treatment of wastewater containing fungicides Expired - Lifetime JP2765170B2 (en)

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Application Number Priority Date Filing Date Title
JP2069995A JP2765170B2 (en) 1990-03-20 1990-03-20 Treatment of wastewater containing fungicides

Publications (2)

Publication Number Publication Date
JPH03270795A JPH03270795A (en) 1991-12-02
JP2765170B2 true JP2765170B2 (en) 1998-06-11

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20110125211A (en) * 2009-01-29 2011-11-18 베오리아 워터 솔류션즈 앤드 테크놀로지즈 서포트 Method for treating water by ballasted flocculation and settlement, including pre-contacting the water with an adsorbent

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004298763A (en) * 2003-03-31 2004-10-28 Nippon Steel Chem Co Ltd Method and apparatus for removing nitrate nitrogen
CN103387281A (en) * 2012-05-10 2013-11-13 天津恒英科技有限公司 Acetic acid mixed solution as sewage denitrification carbon source additive
CN105668809B (en) * 2016-04-07 2018-07-10 福建省海岛之星水产有限公司 A kind of abalone culture water purification method

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Publication number Priority date Publication date Assignee Title
JPS5264148A (en) * 1975-11-21 1977-05-27 Sanki Eng Co Ltd Method of denitrifying organic waste water containing ammonia nitrogen
JPS61185394A (en) * 1985-02-12 1986-08-19 Mitsubishi Kakoki Kaisha Ltd Treatment of organic high concentration waste solution
JPS61197097A (en) * 1985-02-25 1986-09-01 Mitsubishi Kakoki Kaisha Ltd Method for denitrifying waste water

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20110125211A (en) * 2009-01-29 2011-11-18 베오리아 워터 솔류션즈 앤드 테크놀로지즈 서포트 Method for treating water by ballasted flocculation and settlement, including pre-contacting the water with an adsorbent
KR101671444B1 (en) * 2009-01-29 2016-11-01 베오리아 워터 솔류션즈 앤드 테크놀로지즈 서포트 Method for treating water by ballasted flocculation and settlement, including pre-contacting the water with an adsorbent

Also Published As

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