JP2004066061A - Water treatment method and equipment therefor - Google Patents

Water treatment method and equipment therefor Download PDF

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Publication number
JP2004066061A
JP2004066061A JP2002226505A JP2002226505A JP2004066061A JP 2004066061 A JP2004066061 A JP 2004066061A JP 2002226505 A JP2002226505 A JP 2002226505A JP 2002226505 A JP2002226505 A JP 2002226505A JP 2004066061 A JP2004066061 A JP 2004066061A
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Japan
Prior art keywords
membrane
sterilization
water treatment
water
wastewater
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JP2002226505A
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Japanese (ja)
Inventor
Komei Kadokawa
角川  功明
Nobudai Yamato
大和  信大
Nobuyuki Motoyama
本山  信行
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Fuji Electric Co Ltd
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Fuji Electric Holdings Ltd
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Publication date
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Priority to JP2002226505A priority Critical patent/JP2004066061A/en
Publication of JP2004066061A publication Critical patent/JP2004066061A/en
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a water treatment method and equipment using membrane filtration which surely kills pathogenic protozoa contained in physically washed wastewater to prevent the pathogenic protozoa from being redischarged into raw water. <P>SOLUTION: The physically washed wastewater is temporarily held in a sterilization apparatus provided outside the membrane module. Ozone, ultraviolet rays, or the like are used as a means for sterilization. The sterilization is performed by means of an ozone generator, a waste ozone treatment apparatus, or a UV (ultraviolet ray) lamp. <P>COPYRIGHT: (C)2004,JPO

Description

【0001】
【発明の属する技術分野】
本発明は、膜を用いた水処理方法および装置で、特に物理洗浄排水に含まれる病原性原虫の殺菌する方法を備えた膜を用いた水処理方法および装置に関する。
【0002】
【従来の技術】
汚濁物質を含んだ原水の処理方法として、膜ろ過を用いた水処理方法がその信頼性、自動運転などの利点から簡易水道を中心に広く利用されている。しかしながら、膜ろ過を用いた水処理装置では、長時間の運転によってファウリングが起こるため、ろ過性能が低下することが課題となっている。これらの原因による膜ろ過性能の低下は膜を洗浄することによって回復することができる。
【0003】
膜の洗浄方法の一つに、物理洗浄がある。物理洗浄には、膜ろ過水を逆流させる逆圧水洗浄(逆洗)や、膜の一次側での水流によるフラッシングや、空気により膜を振動させるエアースクラビングなどがあり、物理的な作用によって付着物質を取り除くもので、自動運転においては、予め定めた条件により洗浄が実施されている。
【0004】
【発明が解決しようとする課題】
図3に従来の膜ろ過装置の代表例としての構成図を示す。
この図において、まず原水1は、原水タンク2に流入し、運転ポンプ3により膜モジュール4に供給されて、膜ろ過水5が得られる。膜ろ過水5は、ろ過水タンク6に一定量貯留され、一部は物理洗浄に使用され、残りは処理水7となる。この際に、原水に含まれる固形の不純物などが膜モジュールの主として原水側に捕捉されるために、膜の両側の差圧が上昇するので、所定の条件を満たした場合に物理洗浄が行われる。この物理洗浄は、所定時間毎に逆洗ポンプ8を用いた逆洗と、エアーコンプレッサー9を用いたエアースクラビングとがなされ、その洗浄排水は、次工程のフラッシングにより排水ライン10により排水される。ここで、前記の物理洗浄排水は、膜で補足した固形の不純物などを取り除き排水しているだけなので、後工程の排水処理の有無やその排水処理方法によっては、物理洗浄排水中に含まれる病原性原虫を不活化することなく原水中に再放流される可能性があり、これが大きな課題となっている。
【0005】
また、逆洗水として、次亜塩素酸ナトリウム含有水やオゾン水を用いる方法も行われているが、これらの方法においても、病原性原虫の不活化を目的としているわけではないため、薬品と病原性原虫の間に十分な反応時間を取るような装置とはなっていない。
本発明の目的は、上記のような物理洗浄排水中に含まれる病原性原虫を確実に不活化し、病原性原虫の原水中への再放流を防止した膜ろ過を用いた水処理方法および装置を提供することにある。
【0006】
【課題を解決するための手段】
上記の目的を達成するために、本発明においては、膜ろ過性能を回復するための物理洗浄後の排水を殺菌処理し、膜に補足された病原性原虫を不活化することとする。
この際に、物理洗浄排水を膜モジュールの外に設置した殺菌処理手段内に一旦貯留し、殺菌処理することとし、殺菌の処理手段には、オゾン、紫外線や、過酸化水素、熱水、超音波を用いることとする。
【0007】
また、膜ろ過性能を回復するための物理洗浄後の排水を殺菌処理する設備を備え、膜に補足された病原性原虫を不活化することとする。
物理洗浄排水を膜モジュールの外に設置した殺菌処理装置内に一旦貯留し、殺菌処理をすることとする。
具体的には、物理洗浄排水を膜モジュールの外に設置した殺菌処理装置内に一旦貯留し、少なくともオゾン発生器、排オゾン処理装置を備えて、殺菌処理をオゾンで行うこととする。
【0008】
さらに、物理洗浄排水を膜モジュールの外に設置した殺菌処理装置内に一旦貯留し、少なくともUV(紫外線)ランプを備えて、殺菌処理を紫外線で行うこととする。
【0009】
【発明の実施の形態】
以下に本発明の2つの実施例を図面を参照しながら説明する。
〔実施例1〕
図1に、本発明の実施例1に係る水処理装置の構成図を示す。図1は殺菌処理装置としてオゾンを利用した場合の膜ろ過装置である。
【0010】
この図と図3の従来の膜ろ過装置との構成上の差は、殺菌用のオゾン発生器11、排オゾン処理装置13、洗浄排水殺菌装置14を追加したことである。
この図において、原水タンク2に流入した原水1を運転ポンプ3により膜モジュール4に供給することにより、膜ろ過水5が得られる。膜ろ過水5は、ろ過水タンク6に一定量貯留され、一部は物理洗浄に使用され、残りは処理水7となる。ろ過30分後毎に逆洗ポンプ8を用いた逆洗およびエアーコンプレッサー9を用いたエアースクラビングの物理洗浄がなされるが、この物理洗浄による排水は、その中に含まれる病原性原虫に対して殺菌処理を実施する。
【0011】
本発明においては、この殺菌処理を効率的に実施するために、物理洗浄による排水を一旦洗浄排水殺菌装置14へ流入貯留して、オゾン発生器11よりオゾンガス12をこの洗浄排水殺菌装置14へ供給して、物理洗浄排水のオゾンで処理を行う。
この際に、オゾン処理におけるCT値(水中の溶存オゾン濃度×殺菌処理の保持時間)は、対象水質・水温により定まる殺菌に必要な値に選定される。本発明者らの実験結果からは、基本的には殺菌に必要とされるオゾンのCT値は、水温20℃ではCT値=6mg/L・min以上となるように供給するのがよく、例えば保持時間を6分とすると、洗浄排水殺菌装置14内に貯留された洗浄排水中の溶存オゾン濃度が1mg/L以上となるようにオゾンガス濃度を予め実験により求めておき供給する。溶存オゾン濃度および保持時間は特に限定されず、あくまでもCT値を基準に供給すればよい。また、水温が低い場合はCT値を大きく(例えば水温10度低下で4倍)、水温が低い場合はCT値を小さく(例えば水温10度上昇で1/4倍)して供給する。
【0012】
洗浄排水殺菌装置14の構造は,液体をオゾン処理できるものなら特に限定されず、散気管を用いた反応塔タイプやスタティックミキサーなどを用いた循環タイプのものなどを用いることができる。
オゾン処理後に未反応のオゾンガスは、排オゾン処理設備13にて処理される。殺菌処理された洗浄排水は排水ライン10より装置外へと排水される。ここで、殺菌処理工程は各ろ過毎に実施しても、何回かのろ過における洗浄排水をまとめて実施してもよい。また、殺菌処理工程は膜ろ過の運転におけるサイクルとは切り離されており、膜ろ過装置がろ過中に殺菌処理を実施していても問題ないことは明らかである。
【0013】
なお、本発明に使用される膜モジュールには、中空糸状、スパイラル状、チューブラ状、平膜状、浸漬状等の各種の膜モジュールが用いられ、また膜の孔径についても各種のものが問題なく用いることができる。
〔実施例2〕
図2に、本発明の実施例2に係る水処理装置の構成図を示す。図2は殺菌処理装置として紫外線を利用した場合の膜ろ過装置である。
【0014】
この図と図3の従来の膜ろ過装置との構成上の差は、洗浄排水殺菌装置14とUV(紫外線)ランプ15を追加したことである。
この図において、原水タンク2に流入した原水1を運転ポンプ3により膜モジュール4に供給することにより、膜ろ過水5が得られる。膜ろ過水5は、ろ過水タンク6に一定量貯留され、一部は物理洗浄に使用され、残りは処理水7となる。ろ過30分後毎に逆洗ポンプ8を用いた逆洗およびエアーコンプレッサー9を用いたエアースクラビングの物理洗浄がなされるが、この物理洗浄による排水は、その中に含まれる病原性原虫に対して殺菌処理を実施する。
【0015】
本発明においては、この殺菌処理を効率的に実施するために、物理洗浄による排水を一旦洗浄排水殺菌装置14へ流入貯留して、UVランプ15より紫外線をこの洗浄排水殺菌装置14へ照射して、物理洗浄排水の紫外線で処理を行う。
この際に、紫外線処理におけるIT値(紫外線照射量×殺菌処理の保持時間)は、対象水質定まる殺菌に必要な値に選定される。本発明者らの実験結果からは、基本的には殺菌に必要とされる紫外線量のIT値は、IT値=1mW・sec/cm2 以上となるように照射するのがよく、紫外線量および保持時間は特に限定されず、あくまでもIT値を基準に照射すればよい。
【0016】
なお、殺菌処理された洗浄排水は排水ライン10より装置外へと排水される。ここで、殺菌処理工程は各ろ過毎に実施しても、何回かのろ過における洗浄排水をまとめて実施してもよい。また、殺菌処理工程は膜ろ過の運転におけるサイクルとは切り離されており、膜ろ過装置がろ過中に殺菌処理を実施していても問題ないことは明らかである。
【0017】
殺菌処理された洗浄排水は排水ライン10より装置外へと排水される。ここで、殺菌処理工程は各ろ過毎に実施しても、何回かのろ過における洗浄排水をまとめて実施してもよい。また、殺菌処理工程は膜ろ過の運転におけるサイクルとは切り離されており、膜ろ過装置がろ過中に殺菌処理を実施していても問題ないことは明らかである。
【0018】
なお、本発明に使用される膜モジュールには、中空糸状、スパイラル状、チューブラ状、平膜状、浸漬状等の各種の膜モジュールが用いられ、また膜の孔径についても各種のものが問題なく用いることができる。
実施例1、2で示した殺菌処理方法以外にも、過酸化水素、熱水、超音波を用いた方法およびそれらを組み合わせた方法においても、殺菌処理で同様の効果が得られることは明らかである。また、それぞれの方法に関しても各種原水に対して予め実験をし、殺菌条件を確定した上で実施することが望ましい。
【0019】
【発明の効果】
上述のように、物理洗浄排水を殺菌処理し、膜に補足された病原性原虫を不活化するために、物理洗浄排水を膜モジュールの外に設置した殺菌処理装置内に一旦貯留し、殺菌処理の手段としてオゾン、紫外線などを用い、オゾン発生器、排オゾン処理装置、またはUV(紫外線)ランプを備えて、殺菌処理を行う。この結果、病原性原虫の原水への再放流を防止できる。
【図面の簡単な説明】
【図1】本発明の実施例1に係るオゾン処理による膜利用水処理装置の構成図
【図2】本発明の実施例2に係る紫外線処理による膜利用水処理装置の構成図
【図3】従来の膜を利用した水処理装置の構成図
【符号の説明】
1:        原水
2:        原水タンク
3:        運転ポンプ
4:        膜モジュール
5:        膜ろ過水
6:        ろ過水タンク
7:        処理水
8:        逆洗ポンプ
9:        エアーコンプレッサー
10:        排水ライン
11:        オゾン発生器
12:        オゾンガス
13:        排オゾン処理装置
14:        洗浄排水殺菌装置
15:        UV(紫外線)ランプ
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a water treatment method and apparatus using a membrane, and more particularly to a water treatment method and apparatus using a membrane provided with a method for disinfecting pathogenic protozoa contained in physical washing wastewater.
[0002]
[Prior art]
As a method for treating raw water containing pollutants, a water treatment method using membrane filtration is widely used mainly for simple water supply, because of its advantages such as reliability and automatic operation. However, in a water treatment apparatus using membrane filtration, fouling occurs due to long-term operation, and thus, a problem is that filtration performance is reduced. The decrease in membrane filtration performance due to these causes can be recovered by washing the membrane.
[0003]
One of the methods for cleaning a film is physical cleaning. Physical cleaning includes back pressure water washing (backwashing) in which membrane filtered water flows backward, flushing by water flow on the primary side of the membrane, and air scrubbing in which the membrane is vibrated by air. The substance is removed, and in automatic operation, cleaning is performed under predetermined conditions.
[0004]
[Problems to be solved by the invention]
FIG. 3 shows a configuration diagram as a typical example of a conventional membrane filtration device.
In this figure, first, raw water 1 flows into a raw water tank 2 and is supplied to a membrane module 4 by an operation pump 3 to obtain membrane filtered water 5. The membrane filtered water 5 is stored in a fixed amount in a filtered water tank 6, a part of which is used for physical cleaning, and the rest is treated water 7. At this time, since solid impurities and the like contained in the raw water are trapped mainly on the raw water side of the membrane module, the differential pressure on both sides of the membrane increases, so that physical cleaning is performed when a predetermined condition is satisfied. . In this physical cleaning, backwashing using a backwash pump 8 and air scrubbing using an air compressor 9 are performed at predetermined time intervals, and the washing wastewater is drained by a drainage line 10 by flushing in the next step. Here, since the physical washing wastewater is only drained after removing solid impurities and the like captured by the membrane, depending on whether or not there is a wastewater treatment in a post-process and the method of the wastewater treatment, the pathogen contained in the physical washing wastewater is removed. The protozoa may be re-discharged into raw water without inactivating them, which is a major issue.
[0005]
In addition, as the backwash water, a method using sodium hypochlorite-containing water or ozone water is also performed.However, since these methods are not intended to inactivate the pathogenic protozoa, they are used with chemicals. The device is not designed to allow sufficient reaction time between pathogenic protozoa.
An object of the present invention is to provide a method and apparatus for water treatment using membrane filtration in which pathogenic protozoa contained in physical washing wastewater as described above are surely inactivated and re-discharge of pathogenic protozoa into raw water is prevented. Is to provide.
[0006]
[Means for Solving the Problems]
In order to achieve the above object, in the present invention, wastewater after physical washing for restoring membrane filtration performance is sterilized to inactivate pathogenic protozoa captured in the membrane.
At this time, the physical cleaning wastewater is temporarily stored in the sterilization processing means installed outside the membrane module and sterilized, and the sterilization processing means includes ozone, ultraviolet rays, hydrogen peroxide, hot water, A sound wave is used.
[0007]
In addition, equipment for sterilizing wastewater after physical washing for restoring membrane filtration performance will be provided to inactivate pathogenic protozoa trapped in the membrane.
The physical cleaning wastewater is temporarily stored in a sterilization apparatus installed outside the membrane module, and sterilized.
Specifically, the physical cleaning wastewater is temporarily stored in a sterilization treatment device installed outside the membrane module, and at least an ozone generator and a waste ozone treatment device are provided to perform the sterilization treatment with ozone.
[0008]
Further, the physical cleaning wastewater is temporarily stored in a sterilization treatment device installed outside the membrane module, and at least a UV (ultraviolet) lamp is provided to perform the sterilization treatment with ultraviolet rays.
[0009]
BEST MODE FOR CARRYING OUT THE INVENTION
Hereinafter, two embodiments of the present invention will be described with reference to the drawings.
[Example 1]
FIG. 1 shows a configuration diagram of a water treatment apparatus according to Embodiment 1 of the present invention. FIG. 1 shows a membrane filtration device using ozone as a sterilization treatment device.
[0010]
The difference between this figure and the conventional membrane filtration apparatus of FIG. 3 is that an ozone generator 11 for sterilization, a waste ozone treatment device 13, and a cleaning wastewater sterilization device 14 are added.
In this figure, by supplying raw water 1 flowing into a raw water tank 2 to a membrane module 4 by an operation pump 3, membrane filtered water 5 is obtained. The membrane filtered water 5 is stored in a fixed amount in a filtered water tank 6, a part of which is used for physical cleaning, and the rest is treated water 7. Every 30 minutes after the filtration, physical washing of the backwashing using the backwashing pump 8 and the air scrubbing using the air compressor 9 is performed, and the wastewater from the physical washing removes the pathogenic protozoa contained therein. Perform sterilization treatment.
[0011]
In the present invention, in order to carry out this sterilization treatment efficiently, wastewater by physical cleaning is once flowed into the cleaning wastewater sterilization apparatus 14 and stored, and ozone gas 12 is supplied from the ozone generator 11 to the cleaning wastewater sterilization apparatus 14. Then, treatment is performed with ozone of the physical cleaning wastewater.
At this time, the CT value (dissolved ozone concentration in water × retention time of sterilization treatment) in the ozone treatment is selected as a value necessary for sterilization determined by the target water quality and water temperature. From the experimental results of the present inventors, it is preferable that the CT value of ozone required for sterilization be supplied so that the CT value is 6 mg / L · min or more at a water temperature of 20 ° C. Assuming that the holding time is 6 minutes, the ozone gas concentration is determined in advance by experiments so that the dissolved ozone concentration in the washing wastewater stored in the washing wastewater sterilizing apparatus 14 becomes 1 mg / L or more, and supplied. The dissolved ozone concentration and the holding time are not particularly limited, and may be supplied based on the CT value. When the water temperature is low, the CT value is increased (for example, 4 times when the water temperature drops by 10 degrees), and when the water temperature is low, the CT value is decreased (for example, 1/4 times when the water temperature rises by 10 degrees).
[0012]
The structure of the washing and draining sterilizer 14 is not particularly limited as long as it can ozone-treat the liquid, and a reaction tower type using a diffuser or a circulation type using a static mixer can be used.
The unreacted ozone gas after the ozone treatment is treated in the waste ozone treatment equipment 13. The cleaning wastewater subjected to the sterilization treatment is discharged from the drainage line 10 to the outside of the apparatus. Here, the sterilization process may be performed for each filtration, or may be performed for cleaning drainage in several filtrations. Further, the sterilization process is separated from the cycle in the operation of membrane filtration, and it is clear that there is no problem even if the membrane filtration device performs the sterilization process during filtration.
[0013]
As the membrane module used in the present invention, various types of membrane modules such as hollow fiber, spiral, tubular, flat membrane, and immersion are used. Can be used.
[Example 2]
FIG. 2 shows a configuration diagram of a water treatment apparatus according to Embodiment 2 of the present invention. FIG. 2 shows a membrane filtration device using ultraviolet light as a sterilization treatment device.
[0014]
The difference between this figure and the conventional membrane filtration apparatus shown in FIG. 3 is that a washing and drainage sterilizer 14 and a UV (ultraviolet) lamp 15 are added.
In this figure, by supplying raw water 1 flowing into a raw water tank 2 to a membrane module 4 by an operation pump 3, membrane filtered water 5 is obtained. The membrane filtered water 5 is stored in a fixed amount in a filtered water tank 6, a part of which is used for physical cleaning, and the rest is treated water 7. Every 30 minutes after the filtration, physical washing of the backwashing using the backwashing pump 8 and the air scrubbing using the air compressor 9 is performed, and the wastewater from the physical washing removes the pathogenic protozoa contained therein. Perform sterilization treatment.
[0015]
In the present invention, in order to efficiently carry out this sterilization treatment, wastewater by physical cleaning is once flowed into and stored in the cleaning and wastewater sterilizing apparatus 14, and ultraviolet rays are irradiated from the UV lamp 15 to the cleaning and wastewater sterilizing apparatus 14. The treatment is performed with ultraviolet light from the physical cleaning wastewater.
At this time, the IT value (ultraviolet irradiation amount × retention time of sterilization treatment) in the ultraviolet treatment is selected as a value necessary for sterilization that determines the target water quality. From the experimental results of the present inventors, it is preferable that the irradiation is performed so that the IT value of the amount of ultraviolet light required for sterilization basically becomes IT value = 1 mW · sec / cm 2 or more. The holding time is not particularly limited, and irradiation may be performed based on the IT value.
[0016]
The sterilized washing wastewater is drained from the drainage line 10 to the outside of the apparatus. Here, the sterilization process may be performed for each filtration, or may be performed for cleaning drainage in several filtrations. Further, the sterilization process is separated from the cycle in the operation of membrane filtration, and it is clear that there is no problem even if the membrane filtration device performs the sterilization process during filtration.
[0017]
The cleaning wastewater subjected to the sterilization treatment is discharged from the drainage line 10 to the outside of the apparatus. Here, the sterilization process may be performed for each filtration, or may be performed for cleaning drainage in several filtrations. Further, the sterilization process is separated from the cycle in the operation of membrane filtration, and it is clear that there is no problem even if the membrane filtration device performs the sterilization process during filtration.
[0018]
The membrane module used in the present invention includes various types of membrane modules, such as hollow fiber, spiral, tubular, flat membrane, and immersion membranes. Can be used.
In addition to the sterilization treatment methods shown in Examples 1 and 2, it is apparent that the same effect can be obtained by the sterilization treatment in the method using hydrogen peroxide, hot water, ultrasonic waves, and the method combining them. is there. In addition, it is preferable that each method be performed after conducting experiments on various raw waters in advance and determining sterilization conditions.
[0019]
【The invention's effect】
As described above, in order to sterilize the physical cleaning wastewater and inactivate the pathogenic protozoa captured by the membrane, the physical cleaning wastewater is temporarily stored in a sterilization processing device installed outside the membrane module, and sterilized. The sterilization process is performed by using an ozone generator, an ultraviolet ray, or the like, and using an ozone generator, a waste ozone treatment device, or a UV (ultraviolet) lamp. As a result, re-discharge of the pathogenic protozoa to the raw water can be prevented.
[Brief description of the drawings]
FIG. 1 is a configuration diagram of a membrane-based water treatment apparatus using ozone treatment according to Embodiment 1 of the present invention. FIG. 2 is a configuration diagram of a membrane-based water treatment apparatus using ultraviolet treatment according to Embodiment 2 of the present invention. Configuration diagram of a conventional water treatment device using a membrane [Explanation of symbols]
1: Raw water 2: Raw water tank 3: Operation pump 4: Membrane module 5: Membrane filtration water 6: Filtration water tank 7: Treated water 8: Backwash pump 9: Air compressor 10: Drain line 11: Ozone generator 12: Ozone gas 13: Wastewater ozone treatment device 14: Cleaning wastewater sterilization device 15: UV (ultraviolet) lamp

Claims (8)

膜を用いた水処理方法において、膜ろ過性能を回復するための物理洗浄後の排水を殺菌処理し、膜に補足された病原性原虫を不活化することを特徴とした膜を用いた水処理方法。In a water treatment method using a membrane, water treatment using a membrane characterized by sterilizing wastewater after physical washing to restore membrane filtration performance and inactivating pathogenic protozoa captured by the membrane. Method. 請求項1に記載の膜を用いた水処理方法において、物理洗浄排水を膜モジュールの外に設置した殺菌処理手段内に一旦貯留し、殺菌処理することを特徴とした膜を用いた水処理方法。The water treatment method using a membrane according to claim 1, wherein the physical cleaning wastewater is temporarily stored in a sterilization treatment means installed outside the membrane module, and sterilized. . 請求項1または2に記載の膜を用いた水処理方法において、殺菌処理において、殺菌処理をオゾン、紫外線を用いることを特徴とした膜を用いた水処理方法。The water treatment method using a membrane according to claim 1 or 2, wherein the sterilization treatment uses ozone and ultraviolet rays in the sterilization treatment. 請求項1または2に記載の膜を用いた水処理方法において、殺菌処理において、殺菌処理を過酸化水素、熱水、超音波を用いることを特徴とした膜を用いた水処理方法。The water treatment method using a membrane according to claim 1 or 2, wherein the sterilization treatment uses hydrogen peroxide, hot water, or ultrasonic waves in the sterilization treatment. 膜を用いた水処理装置において、膜ろ過性能を回復するための物理洗浄後の排水を殺菌処理する設備を備え、膜に補足された病原性原虫を不活化することを特徴とした膜を用いた水処理装置。A water treatment system using a membrane is equipped with a facility that sterilizes wastewater after physical washing to restore membrane filtration performance, and uses a membrane characterized by inactivating pathogenic protozoa captured in the membrane. Water treatment equipment. 請求項5に記載の膜を用いた水処理装置において、物理洗浄排水を膜モジュールの外に設置した殺菌処理装置内に一旦貯留し、殺菌処理することを特徴とした膜を用いた水処理装置。The water treatment apparatus using a membrane according to claim 5, wherein the physical cleaning wastewater is temporarily stored in a sterilization apparatus installed outside the membrane module, and sterilized. . 請求項5または6に記載の膜を用いた水処理装置において、物理洗浄排水を膜モジュールの外に設置した殺菌処理装置内に一旦貯留し、少なくともオゾン発生器、排オゾン処理装置を備えて、殺菌処理をオゾンで行うことを特徴とした膜を用いた水処理方法。The water treatment apparatus using the membrane according to claim 5 or 6, wherein the physical cleaning wastewater is temporarily stored in a sterilization treatment apparatus installed outside the membrane module, and at least an ozone generator and a waste ozone treatment apparatus are provided. A water treatment method using a membrane, wherein the sterilization treatment is performed with ozone. 請求項5または6に記載の膜を用いた水処理装置において、物理洗浄排水を膜モジュールの外に設置した殺菌処理装置内に一旦貯留し、少なくともUV(紫外線)ランプを備えて、殺菌処理を紫外線で行うことを特徴とした膜を用いた水処理方法。The water treatment apparatus using a membrane according to claim 5 or 6, wherein the physical cleaning wastewater is temporarily stored in a sterilization apparatus installed outside the membrane module, and is provided with at least a UV (ultraviolet) lamp to perform sterilization processing. A water treatment method using a film, which is performed using ultraviolet light.
JP2002226505A 2002-08-02 2002-08-02 Water treatment method and equipment therefor Withdrawn JP2004066061A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8137542B2 (en) 2007-12-27 2012-03-20 Kabushiki Kaisha Toshiba Water treatment system
KR101320995B1 (en) 2011-08-22 2013-10-22 (주)씨엠엔텍 In-line ultraviolet reactor for water and wastewater treatment using ultrasonic energy
KR101899996B1 (en) * 2018-02-22 2018-09-18 주식회사 워터솔루션텍 Non-point pollution source treatment system

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8137542B2 (en) 2007-12-27 2012-03-20 Kabushiki Kaisha Toshiba Water treatment system
KR101320995B1 (en) 2011-08-22 2013-10-22 (주)씨엠엔텍 In-line ultraviolet reactor for water and wastewater treatment using ultrasonic energy
KR101899996B1 (en) * 2018-02-22 2018-09-18 주식회사 워터솔루션텍 Non-point pollution source treatment system

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