JP4147381B2 - Method and apparatus for treating peroxide-containing wastewater - Google Patents

Method and apparatus for treating peroxide-containing wastewater Download PDF

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Publication number
JP4147381B2
JP4147381B2 JP2002169776A JP2002169776A JP4147381B2 JP 4147381 B2 JP4147381 B2 JP 4147381B2 JP 2002169776 A JP2002169776 A JP 2002169776A JP 2002169776 A JP2002169776 A JP 2002169776A JP 4147381 B2 JP4147381 B2 JP 4147381B2
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Japan
Prior art keywords
peroxide
anaerobic
wastewater
treatment
containing wastewater
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JP2002169776A
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Japanese (ja)
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JP2004009017A (en
Inventor
護 水口
武 宮本
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Shinko Pantec Co Ltd
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Kobelco Eco Solutions Co Ltd
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    • Y02W10/12

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  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、過酸化物含有排水の処理方法とその装置、さらに詳しくは、過酸化水素や過酢酸等の過酸化物を含有する排水を処理する方法とその装置に関する。
【0002】
【従来の技術】
近年、食品工場等においては、飲料水や食品の生産に際して滅菌処理を厳格に行う観点から、過酸化水素や過酢酸等の過酸化物が用いられている。このような過酸化水素等の過酸化物は、具体的には、たとえば飲料水を収容するペットボトルの蓋を殺菌するための洗浄に使用される。
【0003】
このような排水中においては、上記のような過酸化物以外に有機物が含まれている場合があり、その場合には一般の排水中の有機物と同様に微生物を用いて生物処理を行うことが望ましい。また、過酸化物として過酢酸を用いる場合には、その過酢酸は添加後には酢酸に変化するが、その酢酸も有機物であるため、生物処理を行うのが望ましい。
【0004】
ところが、過酸化水素や過酢酸等には殺菌作用があるため、結果として微生物に対して阻害性を持つこととなり、従って上記のような過酸化物を含有する排水をそのまま生物処理すると、微生物が死滅し、生物処理の実効が図られないこととなる。
【0005】
そこで、上記のような過酸化物は事前に分解しておく必要があり、その手段として、従来ではたとえば重亜硫酸ナトリウム、チオ硫酸ナトリウムや鉄化合物等の還元剤を用いる方法や、活性炭等の触媒を用いる方法が採用されている。
【0006】
【発明が解決しようとする課題】
しかし、還元剤を用いる方法では、還元剤自体が比較的高価なものであるため、全体の処理コストも高くなり、しかも還元剤を添加する分、後段の汚泥量も増加するという問題点がある。
【0007】
また活性炭を用いる方法は、還元剤を用いる方法に比べるとコストは低減できるが、触媒としての活性炭を担持させるための装置が別途必要となる。また、過酸化物が分解される反応が生ずる際に、活性炭が発泡して流出するおそれがある。
【0008】
本発明は、このような従来の問題点を解決するためになされたもので、還元剤や触媒等を別途必要とせずに排水中の過酸化物を分解して生物処理するのを可能とすることを課題とするものである。
【0009】
【課題を解決するための手段】
本発明は、このような課題を解決するために、過酸化水素や過酢酸等の過酸化物を含有する過酸化物含有排水の処理方法とその装置としてなされたもので、過酸化物含有排水の処理方法としての特徴は、生物処理すべき排水を上向流式の嫌気処理設備で嫌気処理した後、その嫌気処理水を過酸化物含有排水と混合して過酸化物含有排水中の過酸化物を分解することである。
【0010】
た、過酸化物含有排水の処理装置としての特徴は、生物処理すべき排水を嫌気処理するための上向流式の嫌気処理設備2と、該上向流式の嫌気処理設備2で処理された嫌気処理水を過酸化物含有排水と混合するための混合槽4とを具備させたことである。
【0011】
この混合槽4の後段には、好気処理設備5を設けて、過酸化物含有排水中の過酸化物を分解した後の嫌気処理水と過酸化物含有排水との混合排水を好気的に生物処理するのが望ましい。
【0012】
【発明の実施の形態】
以下、本発明の実施形態について、図面に従って説明する。
【0013】
(実施形態1)
図1は、一実施形態としての過酸化物含有排水の処理装置の概略ブロック図を示す。
【0014】
本実施形態の過酸化物含有排水の処理装置は、同図に示すように、食品工場排水貯留槽1と、嫌気処理設備2と、過酸化物含有排水貯留槽3と、混合槽4と、好気処理設備5とからなる。
【0015】
食品工場排水貯留槽1は、食品工場から排出される排水であって、製品化に至らない飲料,食品の不要物、その他の液状物である一般の排水を食品工場から供給して貯留するためのものである。
【0016】
嫌気処理設備2は、前記食品工場排水貯留槽1からの排水を嫌気処理するためのものであり、たとえばメタン発酵菌等で前記排水中の有機物等を分解して処理するものである。
【0017】
このような嫌気処理設備2としては、たとえば上向流式嫌気処理設備(UASB)が用いられる。この嫌気処理設備2には、メタン発酵菌の菌体グラニュールが充填される反応槽(図示せず)が具備され、その反応槽の底部から前記食品工場排水貯留槽1からの排水が供給されることになる。
【0018】
過酸化物含有排水貯留槽3は、食品工場において、過酸化水素を含む洗浄,殺菌用の洗浄水を用いて容器やその蓋類の洗浄を行った後の排水を貯留するためのものである。その排水には、生物阻害成分としての過酸化物が含有されている。
【0019】
混合槽4は、前記嫌気処理設備2で嫌気処理された嫌気処理水と、前記過酸化物含有排水貯留槽3からの過酸化物含有排水を混合するための槽であり、この混合槽4内で過酸化物含有排水中の過酸化物である過酸化水素が嫌気処理水によって分解されることとなる。
【0020】
好気処理設備5は、前記混合槽4で過酸化物が分解された混合排水を好気的に生物処理するためのもので、たとえば活性汚泥法等が採用される。
【0021】
活性汚泥法による好気処理設備5には、図示しないが、生物処理槽、沈殿槽等が具備されており、生物処理槽には必要に応じて担体が充填される。
【0022】
上述のような構成からなる過酸化物含有排水の処理装置を用いて、食品工場から排出される過酸化物含有排水を処理する処理方法の実施形態について説明する。
【0023】
先ず、食品工場から排出される一般の排水を食品工場排水貯留槽1に貯留し、その食品工場排水貯留槽1から排水を嫌気処理設備2に供給する。この嫌気処理設備2における反応槽中のメタン発酵菌の菌体グラニュールによって、排水中の有機物等が分解され、嫌気処理される。
【0024】
次に、嫌気処理設備2で嫌気処理された嫌気処理水は、前記混合槽4へ供給される。一方、この混合槽4へは、前記過酸化物含有排水貯留槽3から過酸化物含有排水が供給される。
【0025】
そして、混合槽4内で嫌気処理水と過酸化物含有排水とが混合され、過酸化物含有排水中の過酸化水素が嫌気処理水によって分解される。
【0026】
過酸化水素が嫌気処理水によって分解される作用は必ずしも明確ではないが、嫌気処理水が有する還元力によって分解されるものと認められる。そして、メタン発酵の場合の具体的な作用は、一応次のように推定される。
【0027】
生物処理においては、有機物の分解に関して電子の授受が行われ、すなわち酸化,還元反応が逐次行われて反応が進行する。
【0028】
生物処理に用いられる微生物が生存するためにはATP等の高エネルギー化合物が必要であるが、このような高エネルギー化合物を生成するために必要なエネルギーは有機物の酸化によって得られる。その際、電子が放出されることとなるので、電子受容体が必要となる。
【0029】
嫌気性排水処理においては、溶存酸素がなく、また効率のよい電子受容体(酸化ステップにより放出された電子を受けとるもの)がないので、メタン菌により放出された電子の受け取りに、炭酸ガスが利用される。
換言すれば、炭酸ガスは水素によって還元され、その結果メタンが生成するのである。
【0030】
また硫酸塩が存在している場合には、水素、有機物により還元され、硫化水素を生成する反応が進行する。このような反応の進行を考慮すると、嫌気処理水は高い還元力を持った水であるといえる。
【0031】
このようにして混合槽4で過酸化水素が分解された混合排水は、好気処理設備5に供給される。混合排水は、好気処理設備5の生物処理槽、沈殿槽へ順次供給され、好気的に生物処理される。
【0032】
食品工場からの排水中の有機物は、前記嫌気処理設備2による嫌気処理のみでは完全には分解処理されないが、その後の好気処理設備5でさらに分解処理されるので、排水中のBODも低減することができるのである。
【0033】
以上のように、本実施形態では、食品工場から排出される一般の排水を嫌気処理し、その嫌気処理後の嫌気処理水の還元力を利用して過酸化物含有排水中の生物阻害成分である過酸化水素を分解することができた。
【0034】
従って、従来のような還元剤や触媒等を別途準備することなく、食品工場からの一般の排水処理システムをそのまま利用して過酸化物含有排水の処理を行うことが可能となった。
【0035】
(実施形態2)
本実施形態の過酸化物含有排水の処理装置は、図2に示すように、嫌気処理設備2と、混合槽4と、好気処理設備5とが具備されており、実施形態1のように食品工場排水貯留槽1と過酸化物含有排水貯留槽3とは具備されていない。
【0036】
すなわち、本実施形態では、食品工場から排出される排水が、直接嫌気処理設備2に供給され、また食品工場において、洗浄,殺菌用の洗浄水として使用された後の過酸化物含有排水は、直接混合槽4へ供給される。
【0037】
ただし、食品工場からの排水が嫌気処理設備2に供給されてメタン発酵菌の菌体グラニュールによって嫌気処理される点、嫌気処理後の嫌気処理水が混合槽4内で過酸化物含有排水と混合され、過酸化物含有排水中の過酸化水素が嫌気処理水によって分解される点、過酸化物が分解された混合排水が好気処理設備5で好気処理される点は上記実施形態1と同じである。
【0038】
本実施形態においても、上記実施形態1と同様に食品工場から排出される一般の排水を嫌気処理した後、その嫌気処理水の還元力を利用して過酸化物含有排水中の過酸化水素を分解することができる。
【0039】
(その他の実施形態)
尚、上記実施形態では、混合槽4の後段に好気処理設備5を設けたため、嫌気処理設備2で十分に分解できなかった有機物を好適に分解することができ、また過酸化物含有排水中の有機物等も分解できるという好ましい効果が得られたが、このような好気処理設備5を設けることは本発明に必須の条件ではない。
【0040】
また、該実施形態では、嫌気処理設備2の後段に混合槽4を設け、その混合槽4に過酸化物含有排水を供給して該過酸化物含有排水と嫌気処理水とを混合するようにしたが、混合槽4を設けることは本発明に必須の条件ではない。たとえば、嫌気処理設備2の後方のラインに直接過酸化物含有排水を供給して嫌気処理水と混合することも可能である。要は、過酸化物含有排水と嫌気処理水とが混合されればよいのである。
【0041】
さらに、該実施形態では、過酸化水素を含有する排水を適用する場合について説明したが、過酢酸を含有する排水に本発明を適用することも可能である。要は、これらの過酸化物を含有する排水であれば本発明を適用することが可能である。
さらに上記実施形態では、食品工場排水に過酸化物含有排水を混合する場合について説明したが、本発明を適用する排水の種類も該実施形態の食品工場排水に限定されるものではなく、他の種類の排水に適用することも可能である。
【0043】
【実施例】
(実施例1)
本実施例では、生物阻害成分である過酸化水素を含有した過酸化水素含有排水と嫌気処理水とを1:1に混合し、攪拌して所定時間経過後の過酸化水素の濃度を測定した。
【0044】
過酸化水素含有排水の250mlを容器に入れ、pHを中性に調製した後、嫌気処理水250mlを添加して攪拌し、所定時間経過後の過酸化水素の濃度を測定した。
【0045】
嫌気処理水としては、サンプリングから2日経過後のもの、3日経過後のもの、及び4日経過後のものの3種類を準備した。試験結果を図3に示す。
【0046】
図3からも明らかなように、3種類のいずれのサンプルも混合した直後は過酸化水素の濃度は1000mg/l前後であったが、90分経過後には約6mg/lまで低下した。
【0047】
(実施例2)
本実施例では、上記実施例1で過酸化水素を分解した嫌気処理水の活性汚泥回分試験を行った。これは、過酸化水素分解処理後の嫌気処理水の生物分解性を確認するために行うものである。
【0048】
嫌気処理水によって過酸化水素を分解した処理水に、必要量の窒素、リンを添加し、汚泥を添加して、処理水のTOCを測定した。
その結果を図4に示す。
【0049】
図4からも明らかなように、経過時間とともに嫌気処理水のTOCは低下し、24時間経過後にはTOC除去率は72%となった。これにより、上記実施例1の嫌気処理水の生物分解は可能であることが確認できた。
【0050】
【発明の効果】
以上のように、本発明は、生物処理すべき排水を嫌気処理した後、その嫌気処理水を過酸化物含有排水と混合して過酸化物含有排水中の過酸化水素等の生物阻害成分を分解するものであるため、従来のような還元剤や触媒等を別途準備することなく、一般の排水処理システムをそのまま利用して過酸化物含有排水の処理を行うことが可能になるという効果がある。
【0051】
従って、過酸化物含有排水を処理するための処理コストも、還元剤や触媒を用いる従来の方法等に比べて低減することができるという効果がある。
【0052】
また、従来のように薬品由来の汚泥量が増加することもない。
【0053】
さらに、嫌気処理水を過酸化物含有排水とを混合した後、その混合排水を好気処理した場合には、嫌気処理のみで分解しきれない有機物を好適に分解することができるという効果がある。
【図面の簡単な説明】
【図1】一実施形態としての過酸化物含有排水の処理装置の概略ブロック図。
【図2】他実施形態としての過酸化物含有排水の処理装置の概略ブロック図。
【図3】嫌気処理水の添加による過酸化物含有排水中の酸化剤濃度の推移を示すグラフ。
【図4】活性汚泥回文試験結果のグラフ。
【符号の説明】
2…嫌気処理設備 4…混合槽
5…好気処理設備
[0001]
BACKGROUND OF THE INVENTION
The present invention, the processing method of the peroxide-containing wastewater and apparatus, and more particularly to a method and an apparatus for processing waste water you containing a peroxide such as hydrogen peroxide or peracetic acid.
[0002]
[Prior art]
In recent years, in food factories and the like, peroxides such as hydrogen peroxide and peracetic acid have been used from the viewpoint of strict sterilization when producing drinking water and food. Specifically, such a peroxide such as hydrogen peroxide is used for cleaning for sterilizing a lid of a plastic bottle containing drinking water, for example.
[0003]
In such wastewater, organic substances may be contained in addition to the above-described peroxides. In such cases, biological treatment may be performed using microorganisms in the same manner as organic substances in general wastewater. desirable. Further, when peracetic acid is used as the peroxide, the peracetic acid changes to acetic acid after the addition, but since the acetic acid is also an organic substance, it is desirable to perform biological treatment.
[0004]
However, since hydrogen peroxide, peracetic acid, and the like have a bactericidal action, they have an inhibitory effect on microorganisms. Therefore, when wastewater containing peroxide as described above is biologically treated as it is, It will die and the biological treatment will not be effective.
[0005]
Therefore, it is necessary to decompose the peroxide as described above in advance. As the means, conventionally, for example, a method using a reducing agent such as sodium bisulfite, sodium thiosulfate or an iron compound, or a catalyst such as activated carbon is used. The method using is adopted.
[0006]
[Problems to be solved by the invention]
However, in the method using a reducing agent, since the reducing agent itself is relatively expensive, there is a problem in that the entire treatment cost is increased, and the amount of sludge in the subsequent stage is increased by the amount of addition of the reducing agent. .
[0007]
In addition, the method using activated carbon can reduce the cost as compared with the method using a reducing agent, but requires a separate apparatus for supporting activated carbon as a catalyst. Moreover, when the reaction in which the peroxide is decomposed occurs, the activated carbon may foam and flow out.
[0008]
The present invention has been made to solve such a conventional problem, and enables biological treatment by decomposing peroxide in wastewater without requiring a reducing agent, a catalyst, or the like. This is a problem.
[0009]
[Means for Solving the Problems]
The present invention, in order to solve such problems, has been made as a processing method and apparatus for you containing a peroxide such as hydrogen peroxide or peracetic acid peroxide-containing wastewater, containing peroxide The characteristic of the wastewater treatment method is that the wastewater to be biologically treated is anaerobically treated with an upflow type anaerobic treatment facility, and then the anaerobic treated water is mixed with the peroxide-containing wastewater. It is to decompose the peroxide.
[0010]
Also, features of the apparatus of peroxide-containing wastewater is treated wastewater to be biological treatment with anaerobic treatment facility second upflow for anaerobic treatment, anaerobic treatment equipment 2 of the upflow And a mixing tank 4 for mixing the anaerobic treated water with the peroxide-containing waste water.
[0011]
An aerobic treatment facility 5 is provided at the subsequent stage of the mixing tank 4, and the mixed waste water of the anaerobic treated water and the peroxide-containing waste water after decomposing the peroxide in the peroxide-containing waste water is aerobic. It is desirable to be biologically treated.
[0012]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
[0013]
(Embodiment 1)
FIG. 1: shows the schematic block diagram of the processing apparatus of the peroxide containing waste_water | drain as one Embodiment.
[0014]
The peroxide-containing wastewater treatment apparatus of the present embodiment, as shown in the figure, is a food factory wastewater storage tank 1, an anaerobic treatment facility 2, a peroxide-containing wastewater storage tank 3, a mixing tank 4, An aerobic treatment facility 5.
[0015]
The food factory wastewater storage tank 1 is a wastewater discharged from a food factory, and is used to supply and store general wastewater, which is a beverage, an unnecessary food product, and other liquid materials that cannot be commercialized, from the food factory. belongs to.
[0016]
The anaerobic treatment facility 2 is for treating the wastewater from the food factory wastewater storage tank 1 by anaerobic treatment. For example, the anaerobic treatment facility 2 decomposes and treats organic matter in the wastewater with methane fermentation bacteria or the like.
[0017]
As such anaerobic treatment equipment 2, for example, an upflow anaerobic treatment equipment (UASB) is used. The anaerobic treatment facility 2 is provided with a reaction tank (not shown) filled with cell granules of methane fermentation bacteria, and the waste water from the food factory waste water storage tank 1 is supplied from the bottom of the reaction tank. Will be.
[0018]
The peroxide-containing waste water storage tank 3 is for storing waste water after washing containers and their lids using cleaning water for cleaning and sterilization containing hydrogen peroxide in a food factory. . The wastewater contains peroxide as a biological inhibitory component.
[0019]
The mixing tank 4 is a tank for mixing the anaerobic treated water that has been anaerobically treated by the anaerobic treatment equipment 2 and the peroxide-containing waste water from the peroxide-containing waste water storage tank 3. Thus, hydrogen peroxide, which is a peroxide in the peroxide-containing wastewater, is decomposed by the anaerobic treated water.
[0020]
The aerobic treatment facility 5 is for aerobically biologically treating the mixed waste water in which the peroxide is decomposed in the mixing tank 4, and for example, an activated sludge method is employed.
[0021]
Although not shown, the aerobic treatment facility 5 by the activated sludge method is provided with a biological treatment tank, a sedimentation tank, and the like, and the biological treatment tank is filled with a carrier as necessary.
[0022]
Embodiment of the processing method which processes the peroxide containing waste_water | drain discharged | emitted from a food factory using the processing apparatus of the peroxide containing waste water which consists of the above structures is demonstrated.
[0023]
First, the general waste water discharged from the food factory is stored in the food factory waste water storage tank 1, and the waste water is supplied from the food factory waste water storage tank 1 to the anaerobic treatment facility 2. The organic matter in the waste water is decomposed and anaerobically treated by the cell granules of the methane fermentation bacteria in the reaction tank in the anaerobic treatment facility 2.
[0024]
Next, the anaerobic treated water that has been anaerobically treated by the anaerobic treatment facility 2 is supplied to the mixing tank 4. On the other hand, the peroxide-containing waste water is supplied from the peroxide-containing waste water storage tank 3 to the mixing tank 4.
[0025]
Then, the anaerobic treated water and the peroxide-containing waste water are mixed in the mixing tank 4, and the hydrogen peroxide in the peroxide-containing waste water is decomposed by the anaerobic treated water.
[0026]
The action of hydrogen peroxide being decomposed by the anaerobic treated water is not necessarily clear, but it is recognized that it is decomposed by the reducing power of the anaerobic treated water. And the concrete effect | action in the case of methane fermentation is estimated as follows once.
[0027]
In biological treatment, electrons are exchanged with respect to the decomposition of organic substances, that is, oxidation and reduction reactions are sequentially performed and the reaction proceeds.
[0028]
A high-energy compound such as ATP is necessary for the microorganisms used in biological treatment to survive, but the energy necessary to produce such a high-energy compound is obtained by oxidation of organic matter. At that time, electrons are emitted, so an electron acceptor is required.
[0029]
In anaerobic wastewater treatment, there is no dissolved oxygen and there is no efficient electron acceptor (the one that receives the electrons released by the oxidation step), so carbon dioxide is used to receive the electrons released by methane bacteria. Is done.
In other words, carbon dioxide is reduced by hydrogen, resulting in the production of methane.
[0030]
In addition, when sulfate is present, the reaction is reduced by hydrogen and organic matter to generate hydrogen sulfide. Considering the progress of such a reaction, it can be said that the anaerobic treated water is water having a high reducing power.
[0031]
The mixed waste water in which hydrogen peroxide is decomposed in the mixing tank 4 in this way is supplied to the aerobic treatment facility 5. The mixed waste water is sequentially supplied to the biological treatment tank and the sedimentation tank of the aerobic treatment facility 5 and is aerobically biologically treated.
[0032]
The organic matter in the wastewater from the food factory is not completely decomposed only by the anaerobic treatment by the anaerobic treatment equipment 2, but is further decomposed by the subsequent aerobic treatment equipment 5, so that the BOD in the wastewater is also reduced. It can be done.
[0033]
As described above, in this embodiment, the general wastewater discharged from the food factory is anaerobically treated, and the bioinhibitory component in the peroxide-containing wastewater is utilized by utilizing the reducing power of the anaerobic treated water after the anaerobic treatment. Some hydrogen peroxide could be decomposed.
[0034]
Therefore, it becomes possible to treat peroxide-containing wastewater by directly using a general wastewater treatment system from a food factory without separately preparing a reducing agent, a catalyst and the like as in the past.
[0035]
(Embodiment 2)
As shown in FIG. 2, the peroxide-containing wastewater treatment apparatus according to the present embodiment includes an anaerobic treatment facility 2, a mixing tank 4, and an aerobic treatment facility 5. The food factory wastewater storage tank 1 and the peroxide-containing wastewater storage tank 3 are not provided.
[0036]
That is, in this embodiment, the wastewater discharged from the food factory is directly supplied to the anaerobic treatment facility 2, and the peroxide-containing wastewater after being used as cleaning water for cleaning and sterilization in the food factory is Directly supplied to the mixing tank 4.
[0037]
However, the wastewater from the food factory is supplied to the anaerobic treatment facility 2 and anaerobically treated by the cell granules of the methane fermentation bacteria, and the anaerobic treated water after the anaerobic treatment is mixed with the peroxide-containing wastewater in the mixing tank 4. Embodiment 1 is that the hydrogen peroxide in the peroxide-containing wastewater mixed is decomposed by the anaerobic treated water, and the mixed wastewater in which the peroxide is decomposed is aerobically treated in the aerobic treatment equipment 5. Is the same.
[0038]
Also in the present embodiment, after the general waste water discharged from the food factory is anaerobically treated as in the first embodiment, the hydrogen peroxide in the peroxide-containing waste water is reduced using the reducing power of the anaerobic treated water. Can be disassembled.
[0039]
(Other embodiments)
In the above embodiment, since the aerobic treatment equipment 5 is provided in the subsequent stage of the mixing tank 4, organic substances that could not be sufficiently decomposed by the anaerobic treatment equipment 2 can be suitably decomposed, and in the peroxide-containing waste water. However, the provision of such aerobic treatment equipment 5 is not an essential condition for the present invention.
[0040]
Moreover, in this embodiment, the mixing tank 4 is provided in the back | latter stage of the anaerobic treatment equipment 2, and the peroxide containing waste water is supplied to the mixing tank 4, and this peroxide containing waste water and anaerobic treated water are mixed. However, the provision of the mixing tank 4 is not an essential condition for the present invention. For example, it is also possible to supply the peroxide-containing wastewater directly to the line behind the anaerobic treatment facility 2 and mix it with the anaerobic treated water. In short, the peroxide-containing waste water and the anaerobic treated water may be mixed.
[0041]
Furthermore, in this embodiment, although the case where the waste_water | drain containing hydrogen peroxide was applied was demonstrated, it is also possible to apply this invention to the waste_water | drain containing peracetic acid. In short, the present invention can be applied to any wastewater containing these peroxides.
Furthermore, in the above-described embodiment, the case where the peroxide-containing wastewater is mixed with the food factory wastewater is described, but the type of wastewater to which the present invention is applied is not limited to the food factory wastewater of the embodiment, It can also be applied to various types of wastewater.
[0043]
【Example】
(Example 1)
In this example, the hydrogen peroxide-containing wastewater containing hydrogen peroxide, which is a biological inhibitory component, and anaerobic treated water were mixed at a ratio of 1: 1, and the concentration of hydrogen peroxide after a predetermined time was measured by stirring. .
[0044]
After 250 ml of hydrogen peroxide-containing wastewater was put in a container and the pH was adjusted to neutral, 250 ml of anaerobic water was added and stirred, and the concentration of hydrogen peroxide after a predetermined time was measured.
[0045]
Three types of anaerobic treated water were prepared: one after 2 days from sampling, one after 3 days, and one after 4 days. The test results are shown in FIG.
[0046]
As is apparent from FIG. 3, the concentration of hydrogen peroxide was about 1000 mg / l immediately after mixing all three types of samples, but it decreased to about 6 mg / l after 90 minutes.
[0047]
(Example 2)
In this example, an activated sludge batch test of anaerobic treated water obtained by decomposing hydrogen peroxide in Example 1 was performed. This is performed in order to confirm the biodegradability of the anaerobic treated water after the hydrogen peroxide decomposition treatment.
[0048]
Necessary amounts of nitrogen and phosphorus were added to treated water obtained by decomposing hydrogen peroxide with anaerobic treated water, sludge was added, and the TOC of the treated water was measured.
The result is shown in FIG.
[0049]
As is clear from FIG. 4, the TOC of anaerobic treated water decreased with the passage of time, and the TOC removal rate became 72% after 24 hours. Thereby, it was confirmed that biodegradation of the anaerobic treated water of Example 1 was possible.
[0050]
【The invention's effect】
As described above, according to the present invention, after anaerobic treatment of wastewater to be biologically treated, the anaerobic treated water is mixed with peroxide-containing wastewater to remove bioinhibitory components such as hydrogen peroxide in the peroxide-containing wastewater. Since it decomposes, there is an effect that it is possible to treat peroxide-containing wastewater by using a general wastewater treatment system as it is without separately preparing a conventional reducing agent or catalyst. is there.
[0051]
Therefore, there is an effect that the treatment cost for treating the peroxide-containing waste water can be reduced as compared with the conventional method using a reducing agent or a catalyst.
[0052]
Moreover, the amount of sludge derived from chemicals does not increase as in the prior art.
[0053]
Furthermore, after anaerobic treated water is mixed with peroxide-containing wastewater, when the mixed wastewater is aerobically treated, there is an effect that organic substances that cannot be decomposed only by anaerobic treatment can be suitably decomposed. .
[Brief description of the drawings]
FIG. 1 is a schematic block diagram of an apparatus for treating peroxide-containing wastewater as one embodiment.
FIG. 2 is a schematic block diagram of a treatment apparatus for peroxide-containing wastewater as another embodiment.
FIG. 3 is a graph showing the transition of the oxidant concentration in peroxide-containing wastewater by the addition of anaerobic treated water.
FIG. 4 is a graph of the activated sludge circulation test result.
[Explanation of symbols]
2 ... Anaerobic treatment equipment 4 ... Mixing tank 5 ... Aerobic treatment equipment

Claims (5)

生物処理すべき排水を上向流式の嫌気処理設備で嫌気処理した後、その嫌気処理水を過酸化物含有排水と混合して過酸化物含有排水中の過酸化物を分解することを特徴とする過酸化物含有排水の処理方法。The wastewater to be biologically treated is anaerobically treated with an upflow anaerobic treatment facility, and then the anaerobic treated water is mixed with the peroxide-containing wastewater to decompose the peroxide in the peroxide-containing wastewater. processing method of peroxide-containing wastewater shall be the. 過酸化物含有排水中の過酸化物を分解した後、嫌気処理水と過酸化物含有排水との混合排水を生物処理する請求項1記載の過酸化物含有排水の処理方法。After decomposing the peroxide in the peroxide-containing wastewater treatment method of peroxide-containing wastewater according to claim 1, wherein the biological treatment of mixed waste water with anaerobic treatment water and peroxide-containing wastewater. 混合排水の生物処理が好気的生物処理である請求項2記載の過酸化物含有排水の処理方法。Biological treatment of mixed wastewater Ru aerobic biological treatment der Motomeko 2 processing method of peroxide-containing wastewater as claimed. 生物処理すべき排水を嫌気処理するための上向流式の嫌気処理設備(2)と、該上向流式の嫌気処理設備(2)で処理された嫌気処理水を過酸化物含有排水と混合するための混合槽(4)とを具備したことを特徴とする過酸化物含有排水の処理装置。Anaerobic treatment facility upflow for anaerobic treatment of waste water to be biological treatment (2), and peroxide-containing wastewater the treated anaerobically treated water by anaerobic treatment facility of the upflow (2) mixing tank (4) and peroxide-containing wastewater treatment apparatus characterized by comprising the for mixing. 生物処理すべき排水を嫌気処理するための上向流式の嫌気処理設備(2)と、該上向流式の嫌気処理設備(2)で処理された嫌気処理水を過酸化物含有排水と混合するための混合槽(4)と、該混合槽(4)で混合されて過酸化物が分解された前記嫌気処理水と過酸化物含有排水との混合排水を好気処理するための好気処理設備(5)とを具備したことを特徴とする過酸化物含有排水の処理装置。Anaerobic treatment facility upflow for anaerobic treatment of waste water to be biological treatment (2), and peroxide-containing wastewater the treated anaerobically treated water by anaerobic treatment facility of the upflow (2) A mixing tank (4) for mixing, and a favorable condition for aerobic treatment of the mixed waste water of the anaerobic treated water mixed with the mixing tank (4) and the peroxide decomposed and the peroxide-containing waste water. air treatment facility (5) and the peroxide-containing wastewater treatment apparatus you characterized by comprising a.
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