JP2003094056A - Method and apparatus for treating purified water - Google Patents

Method and apparatus for treating purified water

Info

Publication number
JP2003094056A
JP2003094056A JP2002259957A JP2002259957A JP2003094056A JP 2003094056 A JP2003094056 A JP 2003094056A JP 2002259957 A JP2002259957 A JP 2002259957A JP 2002259957 A JP2002259957 A JP 2002259957A JP 2003094056 A JP2003094056 A JP 2003094056A
Authority
JP
Japan
Prior art keywords
water
tank
activated carbon
treatment tank
liquid
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
Application number
JP2002259957A
Other languages
Japanese (ja)
Inventor
Shiro Inoue
司朗 井上
Naoko Hirata
直子 平田
Tomoki Matsumoto
智樹 松本
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.)
Hitachi Zosen Corp
Original Assignee
Hitachi Zosen Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Hitachi Zosen Corp filed Critical Hitachi Zosen Corp
Priority to JP2002259957A priority Critical patent/JP2003094056A/en
Publication of JP2003094056A publication Critical patent/JP2003094056A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Abstract

PROBLEM TO BE SOLVED: To provide a method and an apparatus for reducing an installation area, facilitating operation management, reducing a facility installation cost and an operation cost, and obtaining a high quality clean water. SOLUTION: Raw water is supplied into a treatment tank 1 built in a granulated activated carbon 2 adhering aerobic microbes to the surface thereof, an organic matter in a liquid inside the tank 1 of the raw water supplied into the treatment tank 1 is adsorbed on the surface of the activated carbon 2, and the organic matter is decomposed by the aerobic microbes. A decomposed organic matter and other suspended matter are filtered and separated by a filtration membrane unit 3 dipped into the liquid inside the tank. When the concentration of the suspended matter in the liquid inside the treatment tank 1 increases, the liquid inside the tank is withdrawn from the treatment tank 1. The withdrawing of the liquid inside the tank from the treatment tank 1 is carried out by lifting the liquid surface by increasing a supplied amount of the raw water into the treatment tank 1, and overflowing those from a water withdrawing port 25 formed at a position located higher than the liquid surface inside the tank at a peripheral wall of the treatment tank 1.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】この発明は、河川水、湖沼
水、池水、地下水等の原水から上水を得るための浄水処
理方法および装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water purification method and apparatus for obtaining clean water from raw water such as river water, lake water, pond water and groundwater.

【0002】[0002]

【従来の技術と発明が解決しようとする課題】従来の一
般的な浄水処理方法は懸濁物の除去と殺菌が主体であ
り、図6に示すように、原水に塩素を注入した後、凝集
沈澱槽において適当な凝集剤を添加することにより凝集
物を生成させてこれを沈殿させ、ついで砂を充填した砂
ろ過槽に導いてろ過し、さらに再度塩素を注入するもの
である。
2. Description of the Related Art The conventional general purification method for water purification is mainly for removing suspended matter and sterilization. As shown in FIG. In this method, a suitable flocculant is added in the settling tank to form a flocculate, which is allowed to settle, then introduced into a sand filter tank filled with sand for filtration, and chlorine is injected again.

【0003】ところが、このような方法では、処理水量
当たりに必要な設備の敷地面積が広大になる上、豊富な
経験に基づく微妙な運転条件の維持管理が不可欠であ
る。すなわち、原水の状態の変動に対応して、凝集沈殿
やろ過の状態を良好に維持するため、薬注条件など多く
の運転パラメータの微妙な調整が必要とされる。
However, in such a method, the site area of equipment required per amount of treated water is vast, and in addition, maintenance of delicate operating conditions based on abundant experience is indispensable. That is, in order to maintain a good state of coagulation and sedimentation and filtration in response to fluctuations in the state of raw water, it is necessary to make delicate adjustments to many operating parameters such as chemical injection conditions.

【0004】さらに、近年、湖沼水、地下水などの水道
原水の水質悪化が著しく、異臭味やトリハロメタン生成
などの問題が生じているが、従来の一般的な浄水処理方
法では、これらの問題に対応できないため、さらに高度
な処理技術が要求され、この要求に応えて種々開発され
ている。現在知られている高度浄水処理方法の一例を図
7に示す。図7において、高度浄水処理方法は、凝集沈
澱槽において原水に適当な凝集剤を添加することにより
凝集物を生成させてこれを沈殿させた後オゾンを吹込
み、ついで砂を充填した砂ろ過槽に導いてろ過し、つい
で再びオゾンを吹込んだ後、粒状活性炭が充填された槽
内に上方から流入させて槽内に下降流を形成することに
より粒状活性炭に有機物等を吸着させ、さらに塩素を注
入するものである。
Furthermore, in recent years, the water quality of tap water such as lake water and groundwater has remarkably deteriorated, and problems such as off-flavor and trihalomethane production have occurred. However, conventional general water purification treatment methods deal with these problems. Therefore, more advanced processing technology is required, and various developments have been made in response to this requirement. FIG. 7 shows an example of the currently known advanced water purification treatment method. In FIG. 7, the advanced water purification method is a sand filter tank in which a coagulant is generated by adding an appropriate coagulant to raw water in a coagulating sedimentation tank to precipitate the coagulant, and then ozone is blown into the coagulated sedimentation tank. After filtering and then blowing ozone again, it is allowed to flow into the tank filled with granular activated carbon from above to form a downward flow in the tank to adsorb organic matter etc. to the granular activated carbon and Is to be injected.

【0005】しかしながら、このような方法は、従来の
一般的な浄水処理方法に比べても非常に複雑な方法とな
っており、上述した一般的な浄水処理方法の有する問題
点(設備の敷地面積が広大となること、および微妙な運
転管理技術が必要であること)に加えて、設備建設費お
よび運転経費が大幅に上昇し、得られる上水のコストの
大幅な高騰を招くという問題が生じる。
However, such a method is very complicated as compared with the conventional general water purification treatment method, and the problems of the above-mentioned general water purification treatment (equipment site area And the need for delicate operation management technology), equipment construction costs and operating costs will rise significantly, and the cost of the resulting water supply will rise significantly. .

【0006】この発明の目的は、上記問題を解決し、設
備の敷地面積が小さく、運転管理が容易で、設備建設費
および運転経費が安く、しかも得られる上水の水質が高
度な浄水処理方法および装置を提供することにある。
An object of the present invention is to solve the above problems, to reduce the site area of the facility, to easily manage the operation, to reduce the facility construction cost and the operating cost, and to obtain a high quality of clean water. And to provide a device.

【0007】[0007]

【課題を解決するための手段と発明の効果】この発明に
よる浄水処理方法は、河川水、湖沼水、池水、地下水等
の原水から上水を得るための浄水処理方法であって、表
面に好気性微生物が付着した粒状活性炭を内蔵している
処理槽中に原水を入れ、処理槽内に入れられた原水であ
る槽内液中の有機物を活性炭表面上に吸着させるととも
に、好気性微生物によりこの有機物を分解し、有機物の
分解物およびその他の懸濁物を槽内液中に浸漬したろ過
膜ユニットによりろ別し、処理槽内の槽内液中における
懸濁物の濃度が高くなったときに、槽内液を処理槽から
抜き出すこととし、槽内液の処理槽からの抜き出しを、
処理槽の周壁における槽内液の液面よりも上方の高さ位
置に水抜き出し口を形成しておくとともに、処理槽内に
への原水の供給量を増大させることによりその液面を上
昇させて、水抜き出し口からオーバーフローさせること
により行うことを特徴とするものである。
[Means for Solving the Problems and Effects of the Invention] The water purification method according to the present invention is a water purification method for obtaining clean water from raw water such as river water, lake water, pond water, groundwater, etc. Raw water is placed in a treatment tank containing granular activated carbon to which aerobic microorganisms are attached, and the organic matter in the tank liquid, which is the raw water placed in the treatment tank, is adsorbed on the surface of the activated carbon. When the organic matter is decomposed and the decomposed matter of organic matter and other suspensions are filtered by the filtration membrane unit immersed in the tank liquid, and the concentration of the suspension in the tank liquid in the treatment tank becomes high. In addition, the solution in the tank is to be extracted from the processing tank, and the solution in the tank is extracted from the processing tank.
A water outlet is formed at a height above the level of the liquid in the tank on the peripheral wall of the processing tank, and the liquid level is raised by increasing the amount of raw water supplied to the processing tank. Then, it is performed by overflowing from the water outlet.

【0008】上記懸濁物とは、難分解不溶性有機物の他
に、ろ過膜ユニットによりろ別されて膜表面から剥離さ
せられた有機物の分解生成物やその他の懸濁物を含む。
[0008] The above-mentioned suspension includes, in addition to the hardly decomposable insoluble organic matter, decomposition products of the organic matter separated by filtration by the filtration membrane unit and peeled off from the membrane surface, and other suspensions.

【0009】この発明の浄水処理方法によれば、1つの
処理槽内において槽内に入れられた原水である槽内液中
の有機物を活性炭表面上に吸着させるとともに、活性炭
表面上に付着した好気性微生物によりこの有機物を分解
し、有機物の分解物およびその他の懸濁物を槽内液中に
浸漬したろ過膜ユニットによりろ別するだけであるの
で、従来の2つの浄水処理方法に比べてプロセス数が少
なくなる。したがって、運転管理が容易になるととも
に、運転費が安価になる。また、トリハロメタン前駆物
質や異臭味原因物質である有機物を好気性微生物により
分解し、この有機物の分解物を槽内液中に浸漬したろ過
膜ユニットによりろ別しているので、トリハロメタンの
生成や異臭味の発生を防止できる。しかも、その他の懸
濁物もろ過膜ユニットによりろ別しているので、浮遊固
形物や細菌も除去される。したがって、高度な上水が得
られる。また、有機物を好気性微生物により分解してい
るので、ろ過膜ユニットに用いる膜としては比較的安価
な精密ろ過膜や限外ろ過膜を使用することができ、設備
費が安くなる。さらに、原水が河川水の場合、原水中の
有機物が稀薄であるので、微生物による分解効率が低下
したり、微生物が生存できなくなることがあるが、有機
物は、表面に好気性微生物が付着した粒状活性炭に吸着
されるので、原水中の有機物が濃縮されることになり、
微生物による分解効率の低下が防止されるとともに、微
生物の生存が保証される。
According to the water purification method of the present invention, in one treatment tank, the organic matter in the in-tank liquid, which is the raw water put in the tank, is adsorbed on the surface of the activated carbon, and the organic matter adhering to the surface of the activated carbon is preferably adsorbed. This organic matter is decomposed by aerobic microorganisms, and the decomposed matter of organic matter and other suspensions are simply filtered by a filtration membrane unit immersed in the liquid in the tank. The number will decrease. Therefore, the operation management becomes easy and the operation cost becomes low. In addition, trihalomethane precursors and organic substances that are substances causing off-flavors are decomposed by aerobic microorganisms, and the decomposed products of these organic substances are filtered by a filtration membrane unit immersed in the liquid in the tank. Occurrence can be prevented. Moreover, since other suspended matters are also filtered out by the filtration membrane unit, suspended solids and bacteria are also removed. Therefore, a high degree of clean water is obtained. Further, since the organic matter is decomposed by aerobic microorganisms, a relatively inexpensive microfiltration membrane or ultrafiltration membrane can be used as the membrane used in the filtration membrane unit, and the equipment cost is reduced. Furthermore, when the raw water is river water, the organic matter in the raw water is dilute, which may reduce the decomposition efficiency by the microorganisms or make it impossible for the microorganisms to survive.However, the organic matter is granular with aerobic microorganisms attached to the surface. Since it is adsorbed by activated carbon, organic matter in raw water will be concentrated,
The degradation of the microbial decomposition efficiency is prevented, and the survival of the microorganism is guaranteed.

【0010】また、処理槽内の槽内液中における懸濁物
の濃度が高くなったときに、槽内液を処理槽から抜き出
すようにすると、ろ過時の膜差圧の上昇を防止すること
ができるとともに、懸濁物による膜の目詰まりが防止さ
れる。さらに、処理槽内の槽内液中における懸濁物の濃
度が高くなったときの槽内液の処理槽からの抜き出し
を、処理槽の周壁における槽内液の液面よりも上方の高
さ位置に水抜き出し口を形成しておくとともに、処理槽
内への原水の供給量を増大させることによりその液面を
上昇させて、水抜き出し口からオーバーフローさせるこ
とにより行うと、抜き出す槽内液中に活性炭が含まれる
のを防止することができる。すなわち、活性炭の比重は
大きいので、活性炭が液面近傍まで浮上することはな
く、その結果活性炭の水抜き出し口からの流出を防止す
ることができる。そして、活性炭の流出が防止できるの
で、有機物の微生物による処理能力および活性炭の吸着
能力を維持するために、活性炭を新たに補充する必要が
なくなって経済的である。ろ過膜ユニットの下方から槽
内液中に曝気していると、活性炭が液面近傍まで上昇す
ることもあるが、この場合には、槽内液の処理槽からの
抜き出し時に曝気量を減らして活性炭が液面近傍まで上
昇しないように調節する。
Further, when the concentration of suspended solids in the tank liquid in the processing tank becomes high, the tank liquid can be withdrawn from the processing tank to prevent an increase in transmembrane pressure during filtration. And the clogging of the membrane due to the suspension is prevented. Further, when the concentration of suspended solids in the bath liquid in the treatment bath becomes high, the withdrawal of the bath liquid from the treatment bath should be performed at a height above the liquid level of the bath liquid on the peripheral wall of the treatment bath. If a water outlet is formed at the position and the liquid level is raised by increasing the amount of raw water supplied to the treatment tank and overflowed from the water outlet, It is possible to prevent activated carbon from being included in the. That is, since the activated carbon has a large specific gravity, the activated carbon does not float to the vicinity of the liquid surface, and as a result, the activated carbon can be prevented from flowing out from the water outlet. Further, since the activated carbon can be prevented from flowing out, it is economical because it is not necessary to newly replenish the activated carbon in order to maintain the treatment ability of the organic matter by the microorganism and the adsorption ability of the activated carbon. If the liquid inside the tank is aerated from below the filtration membrane unit, activated carbon may rise to near the liquid surface.In this case, reduce the amount of aeration when extracting the liquid inside the tank from the treatment tank. Adjust so that activated carbon does not rise near the liquid surface.

【0011】この発明による他の浄水処理方法は、河川
水、湖沼水、池水、地下水等の原水から上水を得るため
の浄水処理方法であって、表面に好気性微生物が付着し
た粒状活性炭を内蔵している処理槽中に原水を入れ、処
理槽内に入れられた原水である槽内液中の有機物を活性
炭表面上に吸着させるとともに、好気性微生物によりこ
の有機物を分解し、有機物の分解物およびその他の懸濁
物を槽内液中に浸漬したろ過膜ユニットによりろ別し、
処理槽内の槽内液中における懸濁物の濃度が高くなった
ときに、槽内液を処理槽から抜き出すこととし、槽内液
の処理槽からの抜き出しを、処理槽の周壁の下端部に形
成された水抜き出し口、および水抜き出し口に接続され
て外側斜め上方にのびかつ活性炭ろ別フィルタを有する
水抜き出し管を通して行うことを特徴とするものであ
る。
Another water purification method according to the present invention is a water purification method for obtaining clean water from raw water such as river water, lake water, pond water, and ground water, in which granular activated carbon having aerobic microorganisms adhered to its surface is used. Raw water is put into the built-in treatment tank, and the organic matter in the tank water, which is the raw water put into the treatment tank, is adsorbed on the activated carbon surface, and this organic matter is decomposed by aerobic microorganisms to decompose the organic matter. Substances and other suspensions are filtered by a filtration membrane unit immersed in the liquid in the tank,
When the concentration of suspended solids in the tank liquid in the processing tank becomes high, the tank liquid is to be withdrawn from the processing tank, and the tank liquid is extracted from the processing tank at the lower end of the peripheral wall of the processing tank. And a water withdrawing pipe connected to the water withdrawing port and extending obliquely outward and having an activated carbon filtering filter.

【0012】上記懸濁物とは、難分解不溶性有機物の他
に、ろ過膜ユニットによりろ別されて膜表面から剥離さ
せられた有機物の分解生成物やその他の懸濁物を含む。
[0012] The above-mentioned suspension includes, in addition to the hardly decomposable insoluble organic matter, decomposition products of the organic matter separated by filtration by the filtration membrane unit and peeled off from the membrane surface, and other suspensions.

【0013】この発明の他の浄水処理方法によれば、1
つの処理槽内において槽内に入れられた原水である槽内
液中の有機物を活性炭表面上に吸着させるとともに、活
性炭表面上に付着した好気性微生物によりこの有機物を
分解し、有機物の分解物およびその他の懸濁物を槽内液
中に浸漬したろ過膜ユニットによりろ別するだけである
ので、従来の2つの浄水処理方法に比べてプロセス数が
少なくなる。したがって、運転管理が容易になるととも
に、運転費が安価になる。また、トリハロメタン前駆物
質や異臭味原因物質である有機物を好気性微生物により
分解し、この有機物の分解物を槽内液中に浸漬したろ過
膜ユニットによりろ別しているので、トリハロメタンの
生成や異臭味の発生を防止できる。しかも、その他の懸
濁物もろ過膜ユニットによりろ別しているので、浮遊固
形物や細菌も除去される。したがって、高度な上水が得
られる。また、有機物を好気性微生物により分解してい
るので、ろ過膜ユニットに用いる膜としては比較的安価
な精密ろ過膜や限外ろ過膜を使用することができ、設備
費が安くなる。さらに、原水が河川水の場合、原水中の
有機物が稀薄であるので、微生物による分解効率が低下
したり、微生物が生存できなくなることがあるが、有機
物は、表面に好気性微生物が付着した粒状活性炭に吸着
されるので、原水中の有機物が濃縮されることになり、
微生物による分解効率の低下が防止されるとともに、微
生物の生存が保証される。
According to another method for purifying water of the present invention, 1
In one treatment tank, the organic matter in the tank liquid, which is the raw water put into the tank, is adsorbed on the activated carbon surface, and the organic matter is decomposed by the aerobic microorganisms adhering to the activated carbon surface. Since the other suspensions are only filtered by the filtration membrane unit immersed in the liquid in the tank, the number of processes is smaller than that of the two conventional water purification treatment methods. Therefore, the operation management becomes easy and the operation cost becomes low. In addition, trihalomethane precursors and organic substances that are substances causing off-flavors are decomposed by aerobic microorganisms, and the decomposed products of these organic substances are filtered by a filtration membrane unit immersed in the liquid in the tank. Occurrence can be prevented. Moreover, since other suspended matters are also filtered out by the filtration membrane unit, suspended solids and bacteria are also removed. Therefore, a high degree of clean water is obtained. Further, since the organic matter is decomposed by aerobic microorganisms, a relatively inexpensive microfiltration membrane or ultrafiltration membrane can be used as the membrane used in the filtration membrane unit, and the equipment cost is reduced. Furthermore, when the raw water is river water, the organic matter in the raw water is dilute, which may reduce the decomposition efficiency by the microorganisms or make it impossible for the microorganisms to survive.However, the organic matter is granular with aerobic microorganisms attached to the surface. Since it is adsorbed by activated carbon, organic matter in raw water will be concentrated,
The degradation of the microbial decomposition efficiency is prevented, and the survival of the microorganism is guaranteed.

【0014】また、処理槽内の槽内液中における懸濁物
の濃度が高くなったときに、槽内液を処理槽から抜き出
すようにすると、ろ過時の膜差圧の上昇を防止すること
ができるとともに、懸濁物による膜の目詰まりが防止さ
れる。さらに、処理槽内の槽内液中における懸濁物の濃
度が高くなったときの槽内液の処理槽からの抜き出し
を、処理槽の周壁の下端部に形成された水抜き出し口、
および水抜き出し口に接続されて外側斜め上方にのびか
つ活性炭ろ別フィルタを有する水抜き出し管を通して行
うと、抜き出す槽内液中に活性炭が含まれるのを防止す
ることができる。すなわち、活性炭がフィルタによりろ
別されるので、活性炭の水抜き出し口からの流出を防止
することができる。そして、活性炭の流出が防止できる
ので、有機物の微生物による処理能力および活性炭の吸
着能力を維持するために、活性炭を新たに補充する必要
がなくなって経済的である。
Further, when the concentration of the suspended matter in the tank liquid in the processing tank becomes high, the tank liquid can be withdrawn from the processing tank to prevent an increase in transmembrane pressure during filtration. And the clogging of the membrane due to the suspension is prevented. Further, when the concentration of suspended matter in the in-tank liquid in the processing tank becomes high, the in-tank liquid is extracted from the processing tank by a water extraction port formed at the lower end of the peripheral wall of the processing tank,
Also, when the water is extracted through a water withdrawing pipe connected to the water withdrawing port and extending obliquely upward to the outside and having an activated carbon filtering filter, it is possible to prevent activated carbon from being contained in the liquid in the tank to be withdrawn. That is, since the activated carbon is filtered by the filter, it is possible to prevent the activated carbon from flowing out of the water outlet. Further, since the activated carbon can be prevented from flowing out, it is economical because it is not necessary to newly replenish the activated carbon in order to maintain the treatment ability of the organic matter by the microorganism and the adsorption ability of the activated carbon.

【0015】上記2つの浄水処理方法において、粒状活
性炭として、粒径0.2〜2mmの石炭原料破砕炭また
は椰子殻原料破砕炭を使用することがある。この場合、
活性炭による膜の目詰まりが防止される。
In the above two water purification methods, crushed coal raw material coal or crushed coconut shell raw material having a particle size of 0.2 to 2 mm may be used as the granular activated carbon. in this case,
The clogging of the membrane due to activated carbon is prevented.

【0016】上記2つの浄水処理方法において、処理槽
中に、さらに表面に好気性微生物が付着した粉状活性炭
を内蔵させておくことがある。粉状活性炭の粒径は20
〜200μm程度である。この場合、粉状活性炭の比表
面積が、粒状活性炭のそれよりも大きくなるので、有機
物の吸着率が向上し、その結果好気性微生物による有機
物の分解効率も向上する。したがって、原水の水質が特
に悪い場合や、得られる上水の水質をさらに高めたい場
合に効果的である。なお、膜の孔径は0.4μm程度で
あるので、粉状活性炭による膜の目詰まりや、粉状活性
炭の膜の通過は防止される。
In the above two water purification treatment methods, a powdery activated carbon having aerobic microorganisms attached to its surface may be incorporated in the treatment tank. The particle size of powdered activated carbon is 20
It is about 200 μm. In this case, since the specific surface area of the powdered activated carbon is larger than that of the granular activated carbon, the adsorption rate of organic matter is improved, and as a result, the decomposition efficiency of organic matter by aerobic microorganisms is also improved. Therefore, it is effective when the quality of raw water is particularly poor or when it is desired to further improve the quality of the obtained clean water. Since the pore size of the membrane is about 0.4 μm, the membrane is prevented from being clogged with the activated carbon powder and the activated carbon powder passing through the membrane.

【0017】上記2つの浄水処理方法において、ろ過膜
ユニットの下方から槽内液中に曝気することが好まし
い。この場合、処理槽内に槽内液の循環流が形成され、
活性炭もこの循環流にのって循環するので、有機物との
接触効率が向上し、活性炭への有機物吸着率も向上す
る。また、好気性微生物への有機物の分解に必要な酸素
供給も効率良く行われる。さらに、循環流にのった活性
炭および気泡により膜表面上の付着物が剥離させられる
ので、膜の目詰まりが防止され、長期間に渡る連続処理
が可能になる。
In the above two water purification methods, it is preferable to aerate the liquid in the tank from below the filtration membrane unit. In this case, a circulating flow of the liquid in the tank is formed in the processing tank,
Since the activated carbon also circulates along this circulation flow, the contact efficiency with the organic matter is improved and the adsorption rate of the organic matter on the activated carbon is also improved. In addition, oxygen is efficiently supplied to the aerobic microorganisms to decompose the organic matter. Further, the activated carbon and air bubbles in the circulating flow separate the deposits on the surface of the film, so that the film is prevented from being clogged and continuous treatment can be performed for a long period of time.

【0018】上記2つの浄水処理方法において、原水を
処理槽に入れる前に、原水中の粗大物および易沈降物を
沈降分離槽で沈降分離しておくことが好ましい。この場
合、粗大物等によりろ過膜ユニットの膜が傷付くことが
防止される。また、上述したように、水抜き出し口から
槽内液を抜き出すさいの水抜き出し口の粗大物等による
詰まりを防止することができる。
In the above two water purification methods, it is preferable that the coarse material and the easily sedimented material in the raw water are separated by sedimentation in the sedimentation tank before the raw water is put into the treatment tank. In this case, it is possible to prevent the membrane of the filtration membrane unit from being damaged by a coarse material or the like. Further, as described above, when the liquid in the tank is drained from the water drain port, it is possible to prevent the water drain port from being clogged with a coarse material or the like.

【0019】この発明による浄水処理装置は、河川水、
湖沼水、池水、地下水等の原水から上水を得るための浄
水処理装置であって、好気性微生物が付着した粒状活性
炭を内蔵する処理槽と、処理槽内に配置されたろ過膜ユ
ニットとを備えており、処理槽の周壁における槽内液の
液面よりも上方の高さ位置に水抜き出し口が形成され、
さらに処理槽内への原水の供給量を増大させることによ
り槽内液の液面を上昇させる液面上昇手段を備えている
ものである。
The water purification apparatus according to the present invention is a river water,
A water purification device for obtaining clean water from raw water such as lake water, pond water, groundwater, etc., comprising a treatment tank containing granular activated carbon to which aerobic microorganisms adhere, and a filtration membrane unit arranged in the treatment tank. It is provided with a water outlet port at a height position above the liquid level of the liquid in the tank on the peripheral wall of the processing tank,
Further, a liquid level raising means for raising the liquid level of the in-tank liquid by increasing the amount of raw water supplied to the processing tank is provided.

【0020】この発明の浄水処理装置は、好気性微生物
が付着した粒状活性炭を内蔵する処理槽と、処理槽内に
配置されたろ過膜ユニットとを備えているだけであるか
ら、設備の敷地面積が、上述した従来の2つの方法を実
施するための装置に比較して小さくて済む。また、設備
建設費および運転費が上述した従来の2つの方法を実施
するための装置に比較して安価になる。
Since the water purification apparatus of the present invention is provided only with a treatment tank containing granular activated carbon to which aerobic microorganisms adhere, and a filtration membrane unit arranged in the treatment tank, the site area of the facility However, it is smaller than an apparatus for performing the above-described two conventional methods. In addition, the facility construction cost and the operating cost are lower than those of the apparatus for performing the two conventional methods described above.

【0021】また、処理槽の周壁における槽内液の液面
よりも上方の高さ位置に水抜き出し口が形成され、さら
に処理槽内への原水の供給量を増大させることにより槽
内液の液面を上昇させる液面上昇手段を備えているか
ら、処理槽内の槽内液中における懸濁物の濃度が高くな
ったときに、液面上昇手段によって処理槽内への原水の
供給量を増大させることにより槽内液の液面を上昇さ
せ、これにより槽内液を水抜き出し口からオーバーフロ
ーさせて抜き出すことができる。しかも、抜き出す槽内
液中に活性炭が含まれるのを防止することができ、浄水
処理方法のところで述べたような作用効果を奏する。
Further, a water outlet is formed at a height position above the liquid surface of the liquid inside the tank on the peripheral wall of the processing tank, and by further increasing the amount of raw water supplied into the processing tank, Since the liquid level raising means for raising the liquid level is provided, the amount of raw water supplied to the processing tank by the liquid level raising means when the concentration of suspended solids in the tank liquid in the processing tank becomes high. Is increased to raise the liquid level of the liquid in the tank, whereby the liquid in the tank can be overflowed and withdrawn from the water outlet. In addition, it is possible to prevent activated carbon from being contained in the liquid in the tank to be extracted, and the same operational effects as described in the water purification method can be obtained.

【0022】上記浄水処理装置において、処理槽の周壁
における水抜き出し口よりも下方の高さ位置に、槽内方
に突出した山形の活性炭流出防止用邪魔板が設けられて
いることがある。この場合、邪魔板の働きにより、活性
炭が液面近傍まで上昇したとしても、活性炭は邪魔板に
当たってそれ以上上昇することはないので、水抜き出し
口からの流出を確実に防止できる。しかも、仮に活性炭
が邪魔板よりも上方まで移動したとしても、曝気装置に
よる上昇流れは、邪魔板により止められるので、活性炭
の比重が大きいことと相俟って、活性炭は邪魔板上に落
下し、その上面に沿って下方に転がり落ちる。
In the above-mentioned water purification apparatus, a mountain-shaped activated carbon outflow preventing baffle projecting inward of the tank may be provided at a height position below the water outlet on the peripheral wall of the processing tank. In this case, even if the activated carbon rises to the vicinity of the liquid surface due to the function of the baffle, the activated carbon does not hit the baffle and further rise, so that the outflow from the water outlet can be reliably prevented. Moreover, even if the activated carbon moves above the baffle plate, the rising flow due to the aeration device is stopped by the baffle plate, so the activated carbon falls on the baffle plate in combination with the large specific gravity of the activated carbon. , Rolling down along its top surface.

【0023】この発明による他の浄水処理装置は、河川
水、湖沼水、池水、地下水等の原水から上水を得るため
の浄水処理装置であって、好気性微生物が付着した粒状
活性炭を内蔵する処理槽と、処理槽内に配置されたろ過
膜ユニットとを備えており、処理槽の周壁の下端部に水
抜き出し口が形成され、水抜き出し口に外側斜め上方に
のびた水抜き出し管が接続され、水抜き出し管に開閉弁
が設けられ、水抜き出し管が着脱自在の活性炭ろ別フィ
ルタを備えているものである。
Another water purification apparatus according to the present invention is a water purification apparatus for obtaining clean water from raw water such as river water, lake water, pond water, and ground water, and contains granular activated carbon to which aerobic microorganisms are attached. It is equipped with a treatment tank and a filtration membrane unit arranged in the treatment tank, and a water outlet is formed at the lower end of the peripheral wall of the treatment tank, and a water outlet pipe extending obliquely upward to the outside is connected to the water outlet. The water extraction pipe is provided with an opening / closing valve, and the water extraction pipe is equipped with a removable activated carbon filter.

【0024】この発明の他の浄水処理装置は、好気性微
生物が付着した粒状活性炭を内蔵する処理槽と、処理槽
内に配置されたろ過膜ユニットとを備えているだけであ
るから、設備の敷地面積が、上述した従来の2つの方法
を実施するための装置に比較して小さくて済む。また、
設備建設費および運転費が上述した従来の2つの方法を
実施するための装置に比較して安価になる。
Since the other water purification apparatus of the present invention is provided only with the treatment tank containing the granular activated carbon to which aerobic microorganisms adhere, and the filtration membrane unit arranged in the treatment tank, The site area is smaller than that of the apparatus for performing the above-described two conventional methods. Also,
Facility construction costs and operating costs are low compared to the devices for carrying out the two conventional methods described above.

【0025】また、処理槽の周壁の下端部に水抜き出し
口が形成され、水抜き出し口に外側斜め上方にのびた水
抜き出し管が接続され、水抜き出し管に開閉弁が設けら
れ、水抜き出し管が着脱自在の活性炭ろ別フィルタを備
えているから、常時は開閉弁を閉じておき、処理槽内の
槽内液中における懸濁物の濃度が高くなったときに開閉
弁を開くと、懸濁物の濃度が高くなった槽内液を、水抜
き出し口から水抜き出し管を経て抜き出すことができ
る。しかも、活性炭がフィルタによりろ別されるので、
抜き出す原水中に活性炭が含まれるのを防止することが
でき、浄水処理方法のところで述べたような作用効果を
奏する。
Further, a water draining port is formed at the lower end of the peripheral wall of the treatment tank, a water draining pipe extending obliquely upward to the outside is connected to the water draining port, and an opening / closing valve is provided in the water draining pipe to remove the water draining pipe. Since it has a removable activated carbon filter, the on-off valve should be closed at all times and opened when the concentration of suspended solids in the liquid inside the processing tank increases. The in-tank liquid with a high concentration can be withdrawn from the water withdrawal port through the water withdrawal pipe. Moreover, since the activated carbon is filtered out by the filter,
It is possible to prevent activated carbon from being contained in the raw water to be extracted, and the same action and effect as described in the water purification method can be obtained.

【0026】上記2つの浄水処理装置において、粒状活
性炭が、粒径0.2〜2mmの石炭原料破砕炭または椰
子殻原料破砕炭であることがある。この場合、浄水処理
方法のところで述べたような作用効果を奏する。
In the above two water purification treatment devices, the granular activated carbon may be coal raw material crushed coal or coconut shell raw material crushed coal having a particle size of 0.2 to 2 mm. In this case, the action and effect as described in the water purification method can be obtained.

【0027】上記2つの浄水処理装置において、処理槽
中に、さらに表面に好気性微生物が付着した粉状活性炭
を内蔵させておくことがある。この場合、浄水処理方法
のところで述べたような作用効果を奏する。
[0027] In the above two water purification treatment apparatuses, powdery activated carbon having aerobic microorganisms attached to the surface may be further incorporated in the treatment tank. In this case, the action and effect as described in the water purification method can be obtained.

【0028】上記2つの浄水処理装置において、さら
に、処理槽内におけるろ過膜ユニットよりも下方の部分
に曝気装置が配置されていることがある。この場合、曝
気装置によりろ過膜ユニットの下方から原水中に曝気す
ると、浄水処理方法のところで述べたような作用効果を
奏する。
In the above two water purification treatment devices, an aeration device may be arranged in a portion below the filtration membrane unit in the treatment tank. In this case, when the raw water is aerated from the lower side of the filtration membrane unit by the aeration device, the action and effect described in the water purification method can be obtained.

【0029】上記2つの浄水処理装置において、ろ過膜
ユニットが、2枚の平膜および両平膜の周縁部間に配置
された額縁状スペーサよりなる平膜モジュールを複数備
えていることがある。この場合、平膜が、精密ろ過膜で
あれば、コストが安くなる。
In the above two water purification treatment devices, the filtration membrane unit may include a plurality of flat membrane modules each including two flat membranes and a frame-shaped spacer arranged between the peripheral portions of both flat membranes. In this case, if the flat membrane is a microfiltration membrane, the cost will be low.

【0030】上記2つの浄水処理装置において、処理槽
の前流側に、原水中の粗大物および易沈降物を沈降分離
沈降させる分離槽を配置しておくことが好ましい。この
場合、原水を処理槽に入れる前に、原水中の粗大物およ
び易沈降物を沈降分離槽で沈降分離させることができ、
浄水処理方法のところで述べたような作用効果を奏す
る。
In each of the above two water purification treatment devices, it is preferable to arrange a separation tank on the upstream side of the treatment tank to settle and separate the coarse material and the easily sedimented material in the raw water. In this case, before putting the raw water into the treatment tank, it is possible to settle and separate the coarse material and easy sediment in the raw water in the settling separation tank,
The action and effect described in the water purification method can be obtained.

【0031】[0031]

【発明の実施の形態】以下、この発明の実施の形態を、
図面を参照して説明する。以下の説明において、全図面
を通じて実質的同一物および同一部分には同一符号を付
して重複する説明を省略する。
BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described below.
A description will be given with reference to the drawings. In the following description, substantially the same parts and the same parts will be denoted by the same reference symbols throughout the drawings, without redundant description.

【0032】図1〜図4はこの発明による浄水処理装置
の第1の実施形態を示す。
1 to 4 show a first embodiment of the water purification apparatus according to the present invention.

【0033】図1において、浄水処理装置は、好気性微
生物が付着した粒状活性炭(2)を内蔵する処理槽(1)と、
処理槽(1)内に配置されたろ過膜ユニット(3)と、処理槽
(1)内におけるろ過膜ユニット(3)よりも下方の部分に配
置された曝気装置(4)と、曝気装置(4)に空気を送り込む
ブロワ(5)と、処理槽(1)内に送り込まれた原水である槽
内液の液面を検出するレベルセンサ(19)と、処理槽(1)
の前流側に配置されかつ原水中の粗大物および易沈降物
を沈降分離させる沈降分離槽(20)と、沈降分離槽(20)か
らのびかつ先端部が処理槽(1)内の底部近傍までのびて
いる原水供給管(6)と、原水を原水供給管(6)を通して沈
降分離槽(20)から処理槽(1)内に送り込むポンプ(7)と、
得られた上水を溜める貯水槽(8)とを備えている。レベ
ルセンサ(19)およびポンプ(7)は図示しない制御器に接
続されており、レベルセンサ(19)、ポンプ(7)および制
御器によって、処理槽(1)内の水位がろ過膜ユニット(3)
の上端より常に上方にあるように原水の供給が制御され
る。
In FIG. 1, the water purification apparatus comprises a treatment tank (1) containing granular activated carbon (2) to which aerobic microorganisms adhere,
The filtration membrane unit (3) arranged in the treatment tank (1) and the treatment tank
The aeration device (4) located below the filtration membrane unit (3) in (1), the blower (5) that sends air to the aeration device (4), and the aeration device (1). Level sensor (19) that detects the level of the liquid in the tank that is the raw water that has been collected, and the processing tank (1)
Settling separation tank (20) that is placed on the upstream side of the tank and that separates coarse and easily settled sediments in raw water, and the tip of the settling separation tank (20) that extends from the settling separation tank (20) near the bottom of the processing tank (1) A raw water supply pipe (6) that extends to the end, and a pump (7) that sends raw water from the sedimentation separation tank (20) into the treatment tank (1) through the raw water supply pipe (6),
A water storage tank (8) for storing the obtained clean water is provided. The level sensor (19) and the pump (7) are connected to a controller (not shown), and the level sensor (19), the pump (7) and the controller cause the water level in the treatment tank (1) to change to the filtration membrane unit (3). )
The raw water supply is controlled so that it is always above the upper end of the.

【0034】処理槽(1)の周壁における槽内液の液面よ
りも上方の高さ位置に水抜き出し口(25)が形成され、水
抜き出し口(25)に水抜き出し管(26)が接続されている。
処理槽(1)の周壁における水抜き出し口(21)よりも下方
の高さ位置に、槽(1)内方に突出した山形の活性炭流出
防止用邪魔板(24)が設けられている。活性炭流出防止用
邪魔板(24)の上端は、槽内液の液面と水抜き出し口(25)
との間の高さ位置にある(図2参照)。また、レベルセ
ンサ(19)とポンプ(7)と制御器とにより、処理槽(1)内へ
の原水の供給量を増大させることにより槽(1)内の槽内
液の液面を上昇させる液面上昇手段が形成されている。
A water drain port (25) is formed at a height position above the liquid level of the liquid in the bath on the peripheral wall of the treatment bath (1), and a water drain pipe (26) is connected to the water drain port (25). Has been done.
A mountain-shaped activated carbon outflow preventing baffle (24) protruding inward of the tank (1) is provided at a height position below the water outlet (21) on the peripheral wall of the processing tank (1). The upper end of the baffle plate (24) for preventing activated carbon outflow is at the liquid level in the tank and the water outlet (25).
It is at a height position between and (see FIG. 2). Further, the level sensor (19), the pump (7), and the controller increase the supply amount of raw water into the treatment tank (1) to raise the liquid level of the liquid in the tank (1). Liquid level raising means is formed.

【0035】活性炭(2)としては、石炭原料の破砕炭ま
たは椰子殻原料の破砕炭が最適であるが、造粒活性炭で
あっても可能である。活性炭(2)の粒度は、0.1〜5
mmの範囲にあるものが好ましく、0.2〜2mmの範
囲内が最適である。さらに、活性炭(2)の平均細孔径が
大きいものほど好ましい。
The activated carbon (2) is most preferably crushed coal of coal raw material or crushed coal of coconut shell raw material, but granulated activated carbon is also possible. The particle size of activated carbon (2) is 0.1-5
Those in the range of mm are preferable, and those in the range of 0.2 to 2 mm are optimal. Further, it is preferable that the activated carbon (2) has a larger average pore diameter.

【0036】ろ過膜ユニット(3)は、図3に示すよう
に、複数の中空状平膜モジュール(13)を備えている。各
平膜モジュール(13)は、図4に示すように、対向状に配
置された2枚の平膜(14)と、両平膜(14)の周縁部間に配
置された額縁状スペーサ(15)とよりなる。各平膜モジュ
ール(13)に、その中空部内と連通するように吸引管(16)
が接続されている。各吸引管(16)は貯水槽(8)からのび
た1つのろ過水管(17)にまとめて接続されている。ろ過
水管(17)の途中には吸引ポンプ(18)が設けられており、
この吸引ポンプ(18)により槽内液が平膜(14)を通過して
平膜モジュール(13)内に吸引されるようになっている。
平膜モジュール(13)の平膜(14)としては、限外ろ過膜や
精密ろ過膜が用いられるが、その中でも比較的吸引抵抗
が小さく、コストの安い精密ろ過膜を用いることが好ま
しい。なお、ろ過膜ユニット(3)には、平膜(14)を用い
た平膜モジュール(13)に代えて、中空糸状膜を用いたキ
ャピラリーモジュールを適用することができる。
The filtration membrane unit (3) comprises a plurality of hollow flat membrane modules (13) as shown in FIG. As shown in FIG. 4, each flat membrane module (13) includes two flat membranes (14) arranged to face each other, and a frame-shaped spacer () disposed between the peripheral portions of both flat membranes (14). 15) and. A suction tube (16) is attached to each flat membrane module (13) so as to communicate with the inside of the hollow part.
Are connected. The suction pipes (16) are collectively connected to one filtered water pipe (17) extending from the water storage tank (8). A suction pump (18) is provided in the middle of the filtered water pipe (17),
By this suction pump (18), the liquid in the tank passes through the flat membrane (14) and is sucked into the flat membrane module (13).
As the flat membrane (14) of the flat membrane module (13), an ultrafiltration membrane or a microfiltration membrane is used, and among them, it is preferable to use a microfiltration membrane having a relatively small suction resistance and a low cost. A capillary module using a hollow fiber membrane can be applied to the filtration membrane unit (3) instead of the flat membrane module (13) using the flat membrane (14).

【0037】次に、上記装置を用いた浄水処理方法につ
いて説明する。
Next, a water purification method using the above apparatus will be described.

【0038】予め、トリハロメタン前駆物質や異臭味原
因物質を含む河川水、湖沼水、池水、地下水等の原水中
の粗大物や易沈降物を、沈降分離槽(20)で沈降分離した
後、この原水をポンプ(7)により処理槽(1)内に供給す
る。このとき、処理槽(1)内の水位がろ過膜ユニット(3)
の上端より常に上方でかつ水抜き出し口(25)よりも下方
にあるように原水の供給が制御される。
[0038] In advance, coarse or easily sedimented raw water such as river water, lake water, pond water, groundwater, etc. containing a trihalomethane precursor or a substance causing off-flavor is settled and separated in a settling separation tank (20). Raw water is supplied into the treatment tank (1) by the pump (7). At this time, the water level in the treatment tank (1) is the filtration membrane unit (3).
The supply of raw water is controlled so that it is always above the upper end of the water and below the water outlet (25).

【0039】そして、ブロワ(5)で曝気装置(4)に空気を
送り込むことによりろ過膜ユニット(3)の下方から槽内
液中に曝気しつつ、吸引ポンプ(18)で吸引する。する
と、槽内液中の有機物が活性炭(2)表面上に吸着させら
れるとともに好気性微生物により分解され、有機物の分
解物、および浮遊固形物、細菌等の懸濁物がろ過膜ユニ
ット(3)の平膜モジュール(13)の平膜(14)によりろ別さ
れ、平膜(14)を通過したろ過水が吸引管(16)およびろ過
水管(17)を通って貯水槽(8)に送られる。なお、原水中
にはウィルスが含まれていることがあり、平膜(14)がウ
イルス除去機能を持たないことと、配水過程での微生物
汚染を避けるため、貯水槽(8)に送る前に、ろ過水管(1
7)内を流れているろ過水に適量の塩素注入を行い、上水
として貯水槽(8)に貯める。
Then, air is sent to the aeration device (4) by the blower (5) to aerate the in-tank liquid from below the filtration membrane unit (3) and suck it by the suction pump (18). Then, the organic matter in the liquid in the tank is adsorbed on the surface of the activated carbon (2) and decomposed by aerobic microorganisms, and the decomposed matter of the organic matter and suspended solids, suspensions such as bacteria are filtered membrane unit (3). The filtered water filtered by the flat membrane (14) of the flat membrane module (13) and passed through the flat membrane (14) is sent to the water tank (8) through the suction pipe (16) and the filtered water pipe (17). To be The raw water may contain viruses, so the flat membrane (14) does not have a virus removal function, and in order to avoid microbial contamination during the water distribution process, before sending it to the water tank (8). , Filtered water pipe (1
7) Inject an appropriate amount of chlorine into the filtered water flowing inside, and store it in the water tank (8) as clean water.

【0040】ろ過膜ユニット(3)の下方から槽内液中に
曝気すると、エアリフト効果により、処理槽(1)内に図
1に矢印で示すような槽内液の循環流が形成される。す
なわち、ろ過膜ユニット(3)の隣接する平膜モジュール
(13)間を槽内液、粒状活性炭(2)および気泡が上昇し、
気泡は水面に達すると大気中に放出され、槽内液および
粒状活性炭(2)はろ過膜ユニット(3)と処理槽(1)の周壁
との間を通って下方に流れてろ過膜ユニット(3)の下側
に至り、再度気泡とともにろ過膜ユニット(3)の隣接す
る平膜モジュール(13)間を上昇する。このとき、ろ過膜
ユニット(3)の下方から槽内液中への曝気により、ろ過
膜ユニット(3)の隣接する平膜モジュール(13)間を上昇
する流れにタービュレンスが与えられる。
When the liquid inside the tank is aerated from below the filtration membrane unit (3), a circulating flow of the liquid inside the tank is formed in the treatment tank (1) due to the air lift effect. That is, the adjacent flat membrane module of the filtration membrane unit (3)
The liquid in the tank, granular activated carbon (2) and bubbles rise between (13),
When the bubbles reach the water surface, they are released into the atmosphere, and the liquid in the tank and the granular activated carbon (2) flow downward between the filtration membrane unit (3) and the peripheral wall of the treatment tank (1) to pass through the filtration membrane unit ( It reaches the lower side of 3) and again rises along with air bubbles between the adjacent flat membrane modules (13) of the filtration membrane unit (3). At this time, turbulence is given to the ascending flow between the flat membrane modules (13) adjacent to each other by the aeration of the inside of the tank liquid from below the filtration membrane unit (3).

【0041】原水中に存在する好ましくない有機物は、
循環する活性炭(2)に吸着され活性炭(2)表面上で濃縮さ
れる。活性炭(2)もこの循環流にのって循環するので、
有機物との接触効率が向上し、活性炭(2)への有機物吸
着率も向上する。また、原水中の濃度のままでは効率よ
く生物処理され難い有機物も、活性炭(2)表面上に濃縮
された状態では、活性炭(2)表面上に付着している微生
物によって容易に効率よく分解される。活性炭(2)に吸
着された有機物は、順次付着微生物によって分解される
ので、飽和吸着による活性炭(2)の性能低下が防止され
る。また、好気性微生物への有機物の分解に必要な酸素
供給も効率良く行われる。
The undesirable organic substances present in the raw water are
It is adsorbed by the circulating activated carbon (2) and concentrated on the surface of the activated carbon (2). Since activated carbon (2) also circulates along this circulation flow,
The contact efficiency with the organic matter is improved, and the organic matter adsorption rate on the activated carbon (2) is also improved. In addition, organic matter that is difficult to be biologically treated efficiently in the concentration of raw water can be easily and efficiently decomposed by microorganisms adhering to the surface of activated carbon (2) when it is concentrated on the surface of activated carbon (2). It The organic matter adsorbed on the activated carbon (2) is sequentially decomposed by the adhering microorganisms, so that the performance deterioration of the activated carbon (2) due to saturated adsorption is prevented. In addition, oxygen is efficiently supplied to the aerobic microorganisms to decompose the organic matter.

【0042】また、ろ過膜ユニット(3)の隣接する平膜
モジュール(13)間を上昇する気泡および活性炭(2)が平
膜(14)を擦ることにより、平膜(14)表面上の付着物が剥
離させられるので、平膜(14)の目詰まりが防止され、長
期間に渡る連続処理が可能になる。
Further, bubbles rising between the adjacent flat sheet membrane modules (13) of the filtration membrane unit (3) and the activated carbon (2) rub the flat sheet membrane (14), so that the surface of the flat sheet membrane (14) is covered. Since the kimono is peeled off, clogging of the flat film (14) is prevented, and continuous treatment for a long period of time becomes possible.

【0043】そして、処理槽(1)内の槽内液中における
懸濁物の濃度が高くなったときに、液面上昇手段によっ
て処理槽(1)内への原水の供給量を増大させることによ
り槽(1)内の槽内液の液面を上昇させると、槽内液を、
水抜き出し口(25)から水抜き出し管(26)を経てオーバー
フローさせて抜き出すことができる。この場合も、抜き
出す槽内液中に活性炭(2)が含まれるのを防止すること
ができる。すなわち、活性炭(2)の比重は大きいので、
活性炭(2)が液面近傍まで浮上することはなく、その結
果活性炭(2)の水抜き出し口(25)からの流出を防止する
ことができる。そして、活性炭(2)の流出が防止できる
ので、有機物の微生物による処理能力および活性炭の吸
着能力を維持するために、活性炭を新たに補充する必要
がなくなって経済的である。ろ過膜ユニット(3)の下方
から槽内液中に曝気していると、活性炭(2)が液面近傍
まで上昇することもあるが、この場合には、槽内液の処
理槽(1)からの抜き出し時に曝気装置(4)による曝気量を
減らして活性炭(2)が液面近傍まで上昇しないように調
節する。
Then, when the concentration of the suspended solids in the liquid in the treatment tank (1) becomes high, the amount of raw water supplied to the treatment tank (1) is increased by the liquid level raising means. By raising the liquid level of the in-tank liquid in the tank (1) by
The water can be extracted by overflowing from the water outlet (25) through the water outlet pipe (26). Also in this case, it is possible to prevent the activated carbon (2) from being contained in the liquid in the tank to be extracted. That is, since the activated carbon (2) has a large specific gravity,
The activated carbon (2) does not float to the vicinity of the liquid surface, and as a result, the activated carbon (2) can be prevented from flowing out of the water outlet (25). Further, since the activated carbon (2) can be prevented from flowing out, it is economical because it is not necessary to newly replenish the activated carbon in order to maintain the treatment ability of the organic matter by the microorganism and the adsorption ability of the activated carbon. If the liquid inside the tank is aerated from below the filtration membrane unit (3), the activated carbon (2) may rise to near the liquid surface.In this case, the tank for treating the liquid inside the tank (1) The amount of aeration by the aeration device (4) is reduced at the time of extraction from the tank so that the activated carbon (2) does not rise to near the liquid surface.

【0044】また、活性炭流出防止用邪魔板(24)の働き
により、活性炭(2)が液面近傍まで上昇したとしても、
活性炭(2)は邪魔板(24)に当たってそれ以上上昇するこ
とはないので、水抜き出し口(25)からの流出を確実に防
止できる。しかも、仮に活性炭(2)が邪魔板(24)よりも
上方まで移動したとしても、曝気装置(4)による水抜き
出し口(25)近傍の上昇流れは、邪魔板(24)により止めら
れるので、活性炭(2)の比重が大きいことと相俟って、
活性炭(2)は邪魔板(24)上に落下し、その上面に沿って
下方に転がり落ちる。
Even if the activated carbon (2) rises to near the liquid surface due to the function of the activated carbon outflow prevention baffle (24),
Since the activated carbon (2) hits the baffle plate (24) and does not rise further, it is possible to reliably prevent the activated carbon (2) from flowing out from the water outlet (25). Moreover, even if the activated carbon (2) moves above the baffle plate (24), the rising flow in the vicinity of the water extraction port (25) by the aeration device (4) is stopped by the baffle plate (24). Coupled with the large specific gravity of activated carbon (2),
The activated carbon (2) falls on the baffle plate (24) and rolls downward along the upper surface thereof.

【0045】図5は、この発明による浄水処理装置の第
2の実施形態を示す。図5において、処理槽(1)の周壁
の下端部に水抜き出し口(30)が形成され、水抜き出し口
(30)に外側斜め上方にのびた水抜き出し管(31)が接続さ
れている。水抜き出し管(31)は途中で下方に曲げられ、
ここに開閉弁(32)が設けられている。また、水抜き出し
管(31)は着脱自在の網状の活性炭ろ別フィルタ(33)を備
えている。ここで、処理槽(1)内の活性炭(2)の粒径を
A、フィルタ(33)の網目の大きさをB、処理槽(1)内の
懸濁物の大きさをC、ろ過膜ユニット(3)の平膜(14)の
細孔径をDとした場合、A>B>C>Dのような関係に
しておく。その他の構成は、図1〜図4に示す装置と同
じである。
FIG. 5 shows a second embodiment of the water purification apparatus according to the present invention. In FIG. 5, the water outlet (30) is formed at the lower end of the peripheral wall of the treatment tank (1),
A water extraction pipe (31) extending obliquely upward to the outside is connected to (30). The drain pipe (31) is bent downwards on the way,
An on-off valve (32) is provided here. Further, the water extraction pipe (31) is provided with a detachable mesh-like activated carbon filter (33). Here, the particle size of the activated carbon (2) in the treatment tank (1) is A, the mesh size of the filter (33) is B, the size of the suspension in the treatment tank (1) is C, and the filtration membrane. When the pore diameter of the flat membrane (14) of the unit (3) is D, the relationship is A>B>C> D. Other configurations are the same as those of the device shown in FIGS.

【0046】次に、上記装置を用いた浄水処理方法につ
いて説明する。
Next, a water purification method using the above apparatus will be described.

【0047】原水を処理して上水を得るまでの操作は、
図1〜図4に示す装置の場合と同様である。常時は開閉
弁(32)は閉じておく。そして、処理槽(1)内の槽内液中
における懸濁物の濃度が高くなったときに、開閉弁(32)
を開くと、懸濁物の濃度が高くなった槽内液を、水抜き
出し口(30)から水抜き出し管(31)を経て抜き出すことが
できる。しかも、活性炭(2)がフィルタ(33)によりろ別
されるので、抜き出す槽内液中に活性炭(2)が含まれる
のを防止することができる。そして、活性炭(2)の流出
が防止できるので、有機物の微生物による処理能力およ
び活性炭の吸着能力を維持するために、活性炭を新たに
補充する必要がなくなって経済的である。フィルタ(33)
によりろ別された活性炭(2)は、自重により水抜き出し
管(31)から処理槽(1)内に戻る。
The procedure for treating raw water to obtain clean water is as follows:
This is similar to the case of the device shown in FIGS. The on-off valve (32) should be closed at all times. Then, when the concentration of the suspended matter in the tank liquid in the processing tank (1) becomes high, the open / close valve (32)
When opened, the in-tank solution having a high concentration of the suspension can be extracted from the water extraction port (30) through the water extraction pipe (31). Moreover, since the activated carbon (2) is filtered by the filter (33), it is possible to prevent the activated carbon (2) from being contained in the liquid in the tank to be extracted. Further, since the activated carbon (2) can be prevented from flowing out, it is economical because it is not necessary to newly replenish the activated carbon in order to maintain the treatment ability of the organic matter by the microorganism and the adsorption ability of the activated carbon. Filter (33)
The activated carbon (2) filtered off by means of the gravity returns from the water extraction pipe (31) into the treatment tank (1).

【0048】上記すべての実施形態においては、処理槽
(1)は、好気性微生物が付着した粒状活性炭(2)を内蔵し
ているが、処理槽(1)は、粒状活性炭(2)に加えて、さら
に粒径20〜200μm程度の粉状活性炭を内蔵してい
ることがある。この場合、粉状活性炭の比表面積が、粒
状活性炭(2)のそれよりも大きくなるので、有機物の吸
着率が向上し、その結果好気性微生物による有機物の分
解効率も向上する。したがって、原水の水質が特に悪い
場合や、得られる上水の水質をさらに高めたい場合に効
果的である。粉状活性炭としては、粒状活性炭(2)と同
様に、石炭原料の破砕炭または椰子殻原料の破砕炭が最
適であるが、造粒活性炭であっても可能である。
In all the above embodiments, the treatment tank
(1) contains granular activated carbon (2) with aerobic microorganisms attached, but the treatment tank (1) is in addition to the granular activated carbon (2), a powdered activated carbon having a particle size of about 20 to 200 μm. May be built in. In this case, since the specific surface area of the powdered activated carbon is larger than that of the granular activated carbon (2), the adsorption rate of organic matter is improved, and as a result, the decomposition efficiency of organic matter by aerobic microorganisms is also improved. Therefore, it is effective when the quality of raw water is particularly poor or when it is desired to further improve the quality of the obtained clean water. As the powdered activated carbon, similarly to the granular activated carbon (2), crushed coal of coal raw material or crushed coal of coconut shell raw material is most suitable, but granulated activated carbon is also possible.

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

【図1】この発明の浄水処理装置の第1の実施形態を示
す構成図である。
FIG. 1 is a configuration diagram showing a first embodiment of a water purification device of the present invention.

【図2】図1のII−II線断面図である。FIG. 2 is a sectional view taken along line II-II in FIG.

【図3】図1の装置のろ過膜ユニットを示す斜視図であ
る。
3 is a perspective view showing a filtration membrane unit of the apparatus of FIG. 1. FIG.

【図4】図1の装置のろ過膜ユニットに組込まれた平膜
モジュールを示す分解斜視図である。
FIG. 4 is an exploded perspective view showing a flat sheet membrane module incorporated in the filtration membrane unit of the apparatus of FIG.

【図5】この発明の浄水処理装置の第2の実施形態を示
す構成図である。
FIG. 5 is a configuration diagram showing a second embodiment of the water purification device of the present invention.

【図6】従来の一般的な浄水処理方法を示すフローシー
トである。
FIG. 6 is a flow sheet showing a conventional general water purification treatment method.

【図7】従来の高度浄水処理方法を示すフローシートで
ある。
FIG. 7 is a flow sheet showing a conventional advanced water purification treatment method.

【符号の説明】[Explanation of symbols]

(1) 処理槽 (2) 粒状活性炭 (3) ろ過膜ユニット (7) ポンプ (19) レベルセンサ (25) 水抜き出し口 (30) 水抜き出し口 (31) 水抜き出し管 (32) 開閉弁 (33) 活性炭ろ別フィルタ (1) Treatment tank (2) Granular activated carbon (3) Filtration membrane unit (7) Pump (19) Level sensor (25) Drainage port (30) Drainage port (31) Drainage pipe (32) Open / close valve (33) Activated carbon filter

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) B01D 35/02 B01D 61/14 61/14 63/08 63/08 C02F 1/52 Z C02F 1/52 3/10 Z 3/10 3/12 S 3/12 B01D 35/02 A (72)発明者 松本 智樹 大阪市此花区西九条5丁目3番28号 日立 造船株式会社内 Fターム(参考) 4D003 AA14 AB02 BA02 CA02 CA03 DA07 DA13 DA16 DA19 DA21 EA14 EA25 FA01 4D006 GA07 HA44 JA02A JA04A JA08A KA01 KA31 KA64 KB13 KB14 KB22 KC02 KC14 KC20 KE02Q MA03 MB02 PA01 PB02 PB22 PC51 4D015 BA19 BB01 CA14 FA15 FA17 FA26 4D028 BB02 BC17 CB01 4D064 AA01 BA02 ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 Identification code FI theme code (reference) B01D 35/02 B01D 61/14 61/14 63/08 63/08 C02F 1/52 Z C02F 1/52 3 / 10 Z 3/10 3/12 S 3/12 B01D 35/02 A (72) Inventor Tomoki Matsumoto 5-3-3 Nishikujo 5-chome, Konohana-ku, Osaka City Hitachi Shipbuilding Co., Ltd. F-term (reference) 4D003 AA14 AB02 BA02 CA02 CA03 DA07 DA13 DA16 DA19 DA21 EA14 EA25 FA01 4D006 GA07 HA44 JA02A JA04A JA08A KA01 KA31 KA64 KB13 KB14 KB22 KC02 KC14 KC20 KE02Q MA03 MB02 PA01 PB02 PB22 PC51 4D015 BA19 BB01 CA14 FA15 FA17 FA26 4D028 BB02 BC17 CB01 4D064 AA01 BA02

Claims (15)

【特許請求の範囲】[Claims] 【請求項1】 河川水、湖沼水、池水、地下水等の原水
から上水を得るための浄水処理方法であって、表面に好
気性微生物が付着した粒状活性炭を内蔵している処理槽
中に原水を入れ、処理槽内に入れられた原水である槽内
液中の有機物を活性炭表面上に吸着させるとともに、好
気性微生物によりこの有機物を分解し、有機物の分解物
およびその他の懸濁物を槽内液中に浸漬したろ過膜ユニ
ットによりろ別し、処理槽内の槽内液中における懸濁物
の濃度が高くなったときに、槽内液を処理槽から抜き出
すこととし、槽内液の処理槽からの抜き出しを、処理槽
の周壁における槽内液の液面よりも上方の高さ位置に水
抜き出し口を形成しておくとともに、処理槽内にへの原
水の供給量を増大させることによりその液面を上昇させ
て、水抜き出し口からオーバーフローさせることにより
行うことを特徴とする浄水処理方法。
1. A water purification method for obtaining clean water from raw water such as river water, lake water, pond water, groundwater, etc., in a treatment tank containing granular activated carbon having aerobic microorganisms attached to its surface. Raw water is added, and the organic matter in the tank liquid that is the raw water put in the treatment tank is adsorbed on the surface of activated carbon, and this organic matter is decomposed by aerobic microorganisms to decompose organic matter and other suspended matter. When the concentration of suspended solids in the in-tank liquid in the treatment tank becomes high, the in-tank liquid is extracted from the treatment tank by filtration using a filtration membrane unit immersed in the in-tank liquid. The water withdrawal port is formed in the peripheral wall of the treatment tank at a height position above the liquid level of the liquid inside the treatment tank, and the amount of raw water supplied to the treatment tank is increased. By raising the liquid level, The method for purifying water is characterized in that it is carried out by overflowing the water.
【請求項2】 河川水、湖沼水、池水、地下水等の原水
から上水を得るための浄水処理方法であって、表面に好
気性微生物が付着した粒状活性炭を内蔵している処理槽
中に原水を入れ、処理槽内に入れられた原水である槽内
液中の有機物を活性炭表面上に吸着させるとともに、好
気性微生物によりこの有機物を分解し、有機物の分解物
およびその他の懸濁物を槽内液中に浸漬したろ過膜ユニ
ットによりろ別し、処理槽内の槽内液中における懸濁物
の濃度が高くなったときに、槽内液を処理槽から抜き出
すこととし、槽内液の処理槽からの抜き出しを、処理槽
の周壁の下端部に形成された水抜き出し口、および水抜
き出し口に接続されて外側斜め上方にのびかつ活性炭ろ
別フィルタを有する水抜き出し管を通して行うことを特
徴とする浄水処理方法。
2. A water purification method for obtaining clean water from raw water such as river water, lake water, pond water, groundwater, etc., in a treatment tank containing granular activated carbon having aerobic microorganisms attached to its surface. Raw water is added, and the organic matter in the tank liquid that is the raw water put in the treatment tank is adsorbed on the surface of activated carbon, and this organic matter is decomposed by aerobic microorganisms to decompose organic matter and other suspended matter. When the concentration of suspended solids in the in-tank liquid in the treatment tank becomes high, the in-tank liquid is extracted from the treatment tank by filtration using a filtration membrane unit immersed in the in-tank liquid. The removal from the treatment tank is performed through a water withdrawal port formed at the lower end of the peripheral wall of the treatment tank, and a water withdrawal pipe connected to the water withdrawal port and extending obliquely outward and having an activated carbon filter. Characteristic water purification method Law.
【請求項3】 粒状活性炭として、粒径0.2〜2mm
の石炭原料破砕炭または椰子殻原料破砕炭を使用するこ
とを特徴とする請求項1または2記載の浄水処理方法。
3. The granular activated carbon has a particle size of 0.2 to 2 mm.
3. The purified water treatment method according to claim 1, wherein the crushed coal raw material coal or the coconut shell raw material crushed coal is used.
【請求項4】 処理槽中に、さらに表面に好気性微生物
が付着した粉状活性炭を内蔵させておくことを特徴とす
る請求項1〜3のうちのいずれかに記載の浄水処理方
法。
4. The purified water treatment method according to claim 1, further comprising a powdery activated carbon having aerobic microorganisms attached to its surface in the treatment tank.
【請求項5】 ろ過膜ユニットの下方から槽内液中に曝
気することを特徴とする請求項1〜4のうちのいずれか
に記載の浄水処理方法。
5. The purified water treatment method according to claim 1, wherein the inside of the tank is aerated from below the filtration membrane unit.
【請求項6】 原水を処理槽に入れる前に、原水中の粗
大物および易沈降物を沈降分離槽で沈降分離しておくこ
とを特徴とする請求項1〜5のうちのいずれかに記載の
浄水処理方法。
6. The method according to any one of claims 1 to 5, wherein before the raw water is put into the treatment tank, the coarse material and the easily sedimented material in the raw water are settled and separated in the settling separation tank. Water purification method.
【請求項7】 河川水、湖沼水、池水、地下水等の原水
から上水を得るための浄水処理装置であって、好気性微
生物が付着した粒状活性炭を内蔵する処理槽と、処理槽
内に配置されたろ過膜ユニットとを備えており、処理槽
の周壁における槽内液の液面よりも上方の高さ位置に水
抜き出し口が形成され、さらに処理槽内への原水の供給
量を増大させることにより槽内液の液面を上昇させる液
面上昇手段を備えている浄水処理装置。
7. A water purification device for obtaining clean water from raw water such as river water, lake water, pond water, groundwater, etc., which comprises a treatment tank containing granular activated carbon to which aerobic microorganisms adhere, and a treatment tank in the treatment tank. Equipped with a filtration membrane unit arranged, a water outlet is formed at a height above the liquid level of the in-tank liquid on the peripheral wall of the processing tank, further increasing the amount of raw water supplied into the processing tank. A water purification apparatus equipped with a liquid level raising means for raising the liquid level of the liquid in the tank by making it.
【請求項8】 処理槽の周壁における水抜き出し口より
も下方の高さ位置に、槽内方に突出した山形の活性炭流
出防止用邪魔板が設けられている請求項7記載の浄水処
理装置。
8. The water purifying apparatus according to claim 7, wherein a mountain-shaped activated carbon outflow preventing baffle projecting inward of the tank is provided at a height position below the water outlet on the peripheral wall of the processing tank.
【請求項9】 河川水、湖沼水、池水、地下水等の原水
から上水を得るための浄水処理装置であって、好気性微
生物が付着した粒状活性炭を内蔵する処理槽と、処理槽
内に配置されたろ過膜ユニットとを備えており、処理槽
の周壁の下端部に水抜き出し口が形成され、水抜き出し
口に外側斜め上方にのびた水抜き出し管が接続され、水
抜き出し管に開閉弁が設けられ、水抜き出し管が着脱自
在の活性炭ろ別フィルタを備えている浄水処理装置。
9. A water treatment apparatus for obtaining clean water from raw water such as river water, lake water, pond water, groundwater, etc., which comprises a treatment tank containing granular activated carbon to which aerobic microorganisms adhere, and a treatment tank in the treatment tank. It is equipped with a filtration membrane unit, and a water outlet is formed at the lower end of the peripheral wall of the treatment tank.The water outlet is connected to a water outlet pipe extending obliquely upward to the outside, and an opening / closing valve is attached to the water outlet pipe. A water purification device that is equipped with an activated carbon filter that has a water extraction tube that is removable.
【請求項10】 粒状活性炭が、粒径0.2〜2mmの
石炭原料破砕炭または椰子殻原料破砕炭である請求項7
〜9のうちのいずれかに記載の浄水処理装置。
10. The granular activated carbon is crushed coal raw material coal or coconut shell raw material crushed coal having a particle size of 0.2 to 2 mm.
The water purification apparatus according to any one of 1 to 9.
【請求項11】 処理槽中に、さらに表面に好気性微生
物が付着した粉状活性炭を内蔵させておく請求項7〜1
0のうちのいずれかに記載の浄水処理装置。
11. The treatment tank is further provided with powdered activated carbon having aerobic microorganisms attached to the surface thereof.
The water purification device according to any one of 0.
【請求項12】 さらに、処理槽内におけるろ過膜ユニ
ットよりも下方の部分に曝気装置が配置されている請求
項7〜11のうちのいずれかに記載の浄水処理装置。
12. The water purification apparatus according to any one of claims 7 to 11, wherein an aeration device is arranged in a portion below the filtration membrane unit in the treatment tank.
【請求項13】 ろ過膜ユニットが、2枚の平膜および
両平膜の周縁部間に配置された額縁状スペーサよりなる
平膜モジュールを複数備えている請求項7〜12のうち
のいずれかに記載の浄水処理装置。
13. The filtration membrane unit includes a plurality of flat membrane modules each including two flat membranes and a frame-shaped spacer arranged between peripheral portions of both flat membranes. The water purification device described in.
【請求項14】 平膜が、精密ろ過膜である請求項13
記載の浄水処理装置。
14. The flat membrane is a microfiltration membrane.
The described water purification device.
【請求項15】 処理槽の前流側に、原水中の粗大物お
よび易沈降物を沈降分離させる分離槽を配置しておくこ
とを特徴とする請求項7〜14のうちのいずれかに記載
の浄水処理装置。
15. The separation tank for settling and separating a coarse material and a readily sedimentable material in raw water is disposed on the upstream side of the treatment tank, according to any one of claims 7 to 14. Water purification equipment.
JP2002259957A 1996-07-11 2002-09-05 Method and apparatus for treating purified water Pending JP2003094056A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2002259957A JP2003094056A (en) 1996-07-11 2002-09-05 Method and apparatus for treating purified water

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
JP18228496 1996-07-11
JP8-182284 1996-07-11
JP7108997 1997-03-25
JP9-71089 1997-03-25
JP2002259957A JP2003094056A (en) 1996-07-11 2002-09-05 Method and apparatus for treating purified water

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP15695997A Division JP3491125B2 (en) 1996-07-11 1997-06-13 Water treatment equipment

Publications (1)

Publication Number Publication Date
JP2003094056A true JP2003094056A (en) 2003-04-02

Family

ID=27300537

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2002259957A Pending JP2003094056A (en) 1996-07-11 2002-09-05 Method and apparatus for treating purified water

Country Status (1)

Country Link
JP (1) JP2003094056A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100393396C (en) * 2003-10-06 2008-06-11 月岛机械株式会社 Filtration unit, installation method for a filtration unit and filtration apparatus
CN112744982A (en) * 2020-12-25 2021-05-04 西华师范大学 Water treatment system based on reverse osmosis technology and treatment method thereof

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100393396C (en) * 2003-10-06 2008-06-11 月岛机械株式会社 Filtration unit, installation method for a filtration unit and filtration apparatus
US7449117B2 (en) 2003-10-06 2008-11-11 Tsukishima Kikai Co., Ltd. Filtration unit, installation method for a filtration unit and filtration apparatus
CN112744982A (en) * 2020-12-25 2021-05-04 西华师范大学 Water treatment system based on reverse osmosis technology and treatment method thereof
CN112744982B (en) * 2020-12-25 2022-10-18 西华师范大学 Water treatment system based on reverse osmosis technology and treatment method thereof

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