JPH11169612A - Water filtration device and removing method of pathogenic microorganism in water - Google Patents

Water filtration device and removing method of pathogenic microorganism in water

Info

Publication number
JPH11169612A
JPH11169612A JP9338360A JP33836097A JPH11169612A JP H11169612 A JPH11169612 A JP H11169612A JP 9338360 A JP9338360 A JP 9338360A JP 33836097 A JP33836097 A JP 33836097A JP H11169612 A JPH11169612 A JP H11169612A
Authority
JP
Japan
Prior art keywords
water
treated
cylindrical filter
filtration device
filtration
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.)
Granted
Application number
JP9338360A
Other languages
Japanese (ja)
Other versions
JP3813338B2 (en
Inventor
Satoshi Yo
敏 楊
Fudeko Tsunoda
ふで子 角田
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.)
Organo Corp
Original Assignee
Organo Corp
Japan Organo Co Ltd
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 Organo Corp, Japan Organo Co Ltd filed Critical Organo Corp
Priority to JP33836097A priority Critical patent/JP3813338B2/en
Publication of JPH11169612A publication Critical patent/JPH11169612A/en
Application granted granted Critical
Publication of JP3813338B2 publication Critical patent/JP3813338B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)
  • Physical Water Treatments (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)
  • Filtration Of Liquid (AREA)
  • Catalysts (AREA)

Abstract

PROBLEM TO BE SOLVED: To obtain a water filtration device for removing and inactivating a pathogenic microorganism by equipping an ultraviolet ray irradiation means in the inside space of a cylindrical filter body composed of a porous inorganic membrane and providing a treating water feed passage for supplying a water to be treated to the inside space of the filter body and a treated water discharged passage for discharging the resultant filtrate. SOLUTION: The water filtration device 1 is constituted so that an ultraviolet ray irradiation means is provided in the inside space of the cylindrical filter body 2 composed of the porous inorganic membrane. And the treating water feed passage 5 for supplying the water to be treated to the inside space of the cylindrical filter body 2 is provided to capture the pathogenic microorganism in the supplied water on the inner peripheral surface of the cylindrical filter body 2. The filtrate removed in the pathogenic microorganism flows-out from the outer peripheral surface of the cylindrical filter body 2 to be discharged from the treated water discharged passage 6. At this time, the pathogenic microorganism captured on the inner peripheral surface of the cylindrical filter body 2 is inactivated by the ultraviolet lamp 3. When the porous inorganic membrane is clogged, the treated filtrate is made to flow-in from the treated water discharge passage 7 to back-wash and discharged from a bask-washing waste water discharge passage 7.

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】本発明は、各種の水の濾過に
用いられる濾過装置に関し、特に水道水、各種飲料水、
自動販売機用水および医療用水や医薬品製造用水などの
無菌水更には半導体装置分野等で用いられる超純水を製
造するために有用な水濾過装置および該装置を用いた水
中の病原性微生物の除去方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a filtration device used for filtering various kinds of water, and particularly to tap water, various kinds of drinking water,
Water filtration equipment useful for producing aseptic water such as water for vending machines, medical water and pharmaceutical production, and also ultrapure water used in the field of semiconductor devices, etc., and removal of pathogenic microorganisms in water using the device. It is about the method.

【0002】[0002]

【従来の技術】飲用に供する水は、安全のために消毒
し、各種の病原性微生物を不活化させなければならな
い。一般的には、塩素消毒により細菌類の不活化を行っ
ている。塩素消毒は、大腸菌や一般細菌などの細菌類の
消毒には非常に有効で、低濃度の塩素で充分殺菌するこ
とができる。しかし、近年集団感染症状を起こすことで
注目されているクリプトスポリジウムなどのような耐塩
素性の病原性微生物を不活化するには、塩素濃度を極め
て高くする必要があり、飲用水の処理としては不向きで
ある。
2. Description of the Related Art Water for drinking must be disinfected for safety and inactivated various pathogenic microorganisms. Generally, bacteria are inactivated by chlorination. Chlorine disinfection is very effective for disinfecting bacteria such as Escherichia coli and general bacteria, and can be sufficiently sterilized with a low concentration of chlorine. However, in order to inactivate chlorine-resistant pathogenic microorganisms such as Cryptosporidium, which has recently attracted attention due to the outbreak of outbreaks, it is necessary to make the chlorine concentration extremely high. Not suitable.

【0003】クリプトスポリジウムなどの耐塩素性病原
体を不活化する場合には、塩素に比べてオゾンや紫外線
などによる消毒の方がより効果的であるが、それでも非
常にコストがかかる。例えば、オゾンでクリプトスポリ
ジウムを不活化する場合、CT値(濃度×消毒時間)1
0mg/L−minぐらいでやっと99%の除去率にな
る。この後さらに凝集沈澱および砂濾過によりさらに除
去率が上昇する。また、細菌や原虫類のサイズは比較的
大きいため(菌の場合、1μm前後、クリプトスポリジ
ウムの場合、3〜5μm前後)、コストを無視すれば、
精密濾過、限外濾過などの膜処理の手段は、非常に高い
病原性微生物の除去率が期待できる。
When inactivating chlorine-resistant pathogens such as Cryptosporidium, disinfection with ozone or ultraviolet rays is more effective than chlorine, but it is still very costly. For example, when Cryptosporidium is inactivated by ozone, the CT value (concentration × disinfection time) 1
At about 0 mg / L-min, the removal rate is only 99%. Thereafter, the removal rate further increases due to coagulation sedimentation and sand filtration. In addition, since the size of bacteria and protozoa is relatively large (about 1 μm for bacteria and about 3 to 5 μm for cryptosporidium), if costs are ignored,
Means for membrane treatment such as microfiltration and ultrafiltration can be expected to have a very high removal rate of pathogenic microorganisms.

【0004】一方、従来の消毒方法に比べて処理コスト
を大幅に低減できる水処理装置が提案されている(WO
96/05141)。この装置は、予め砂濾過器によっ
て濾過された濾過水を膜で仕切られた容器の中に流入さ
せ、水中の微生物を膜面でトラップしながら紫外線照射
し、トラップした微生物を不活化させる水処理装置であ
る。また、トラップして不活化した微生物を一定の間隔
の逆洗により膜面から洗い落とし、次の全く同じ装置の
なかでもう一回不活化処理を行う。この水処理装置の場
合、膜面で捕捉した微生物に対して不活化処理を行うた
め、紫外線の利用率が非常に高くなり、処理コストを低
減できる。
[0004] On the other hand, there has been proposed a water treatment apparatus capable of greatly reducing the treatment cost as compared with the conventional disinfection method (WO).
96/05141). This water treatment system injects filtered water that has been filtered by a sand filter in advance into a container partitioned by a membrane, irradiates the ultraviolet rays while trapping microorganisms in the water on the membrane surface, and inactivates the trapped microorganisms. Device. Further, the microorganisms trapped and inactivated are washed off from the membrane surface by backwashing at regular intervals, and the inactivation treatment is performed once again in the next identical apparatus. In the case of this water treatment apparatus, since the microorganisms captured on the membrane surface are inactivated, the utilization rate of ultraviolet rays becomes extremely high, and the treatment cost can be reduced.

【0005】[0005]

【発明が解決しようとする課題】WO96/05141
の水処理装置は、非常に有効なものであるが、平膜を使
用しているため単位容積当たりの有効濾過面積が小さ
く、かつ膜面以外への紫外線照射光は有効に利用できな
い等の欠点がある。さらに逆洗水が最終的に処理水に合
流するため、末端処理水は紫外線により完全に不活化で
きなかった微生物によりコンタミするおそれもある。
[Problems to be Solved by the Invention] WO96 / 05141
Is very effective, but the use of flat membranes results in a small effective filtration area per unit volume, and the ultraviolet irradiation light on the surface other than the membrane surface cannot be used effectively. There is. Furthermore, since the backwash water finally joins the treated water, the end treated water may be contaminated by microorganisms that could not be completely inactivated by ultraviolet rays.

【0006】本発明が解決しようとする課題は、病原性
微生物を除去し効率的に不活化する水濾過装置および水
中の病原性微生物を除去する方法を提供することであ
る。
[0006] The problem to be solved by the present invention is to provide a water filtration device for removing pathogenic microorganisms and inactivating them efficiently and a method for removing pathogenic microorganisms in water.

【0007】[0007]

【課題を解決するための手段】上記課題を解決するため
の請求項1に係る本発明は、多孔質無機膜からなる筒状
濾過体の内部空間に紫外線照射手段を設けた濾過ユニッ
トを容器内に配置した濾過装置であって、該筒状濾過体
の内部空間に被処理水を供給する被処理水供給流路と、
筒状濾過体の外周面から得られた濾過水を排出する処理
水排出流路とを有することを特徴とする水濾過装置に関
するものである。
According to a first aspect of the present invention, there is provided a filter unit having an ultraviolet irradiation means provided in an inner space of a cylindrical filter made of a porous inorganic membrane. A treated water supply flow path for supplying treated water to the internal space of the cylindrical filter body,
The present invention relates to a water filtration device having a treated water discharge channel for discharging filtered water obtained from the outer peripheral surface of a cylindrical filter.

【0008】上記課題を解決するための請求項2に係る
本発明は、前記濾過ユニットを複数個容器内に並列に配
置したことを特徴とする請求項1に記載の水濾過装置に
関するものである。
According to a second aspect of the present invention, there is provided a water filtration apparatus according to the first aspect, wherein a plurality of the filtration units are arranged in parallel in a container. .

【0009】上記課題を解決するための請求項3に係る
本発明は、前記筒状濾過体の内周面の表面が二酸化チタ
ンでコーティングされていることを特徴とする請求項1
または請求項2に記載の水濾過装置に関するものであ
る。
The present invention according to claim 3 for solving the above-mentioned problem is characterized in that the surface of the inner peripheral surface of the cylindrical filter is coated with titanium dioxide.
Alternatively, the present invention relates to a water filtration device according to claim 2.

【0010】上記課題を解決するための請求項4に係る
本発明は、前記筒状濾過体が、焼結金属からなる多孔質
無機膜であることを特徴とする請求項1ないし請求項3
のいずれか1項に記載の水濾過装置に関するものであ
る。
The present invention according to claim 4 for solving the above-mentioned problem is characterized in that the cylindrical filter is a porous inorganic membrane made of a sintered metal.
A water filtration device according to any one of the above.

【0011】上記課題を解決するための請求項5に係る
本発明は、請求項1ないし請求項4のいずれか1項に記
載の水濾過装置の被処理水供給流路から被処理水を供給
し、筒状濾過体の内面で被処理水中の病原性微生物を捕
捉するとともに捕捉された病原性微生物を濾過ユニット
内の紫外線照射手段で不活化し、筒状濾過体の外周面か
ら濾過水を得ることを特徴とする水中の病原性微生物の
除去方法に関するものである。
According to a fifth aspect of the present invention, there is provided a water filtration apparatus for supplying treated water from a treated water supply passage of a water filtration device according to any one of claims 1 to 4. Then, the pathogenic microorganisms in the water to be treated are captured on the inner surface of the cylindrical filter, and the captured pathogenic microorganisms are inactivated by the ultraviolet irradiation means in the filtration unit, and the filtered water is discharged from the outer peripheral surface of the cylindrical filter. And a method for removing pathogenic microorganisms in water.

【0012】上記課題を解決するための請求項6に係る
本発明は、請求項1ないし請求項4のいずれか1項に記
載の水濾過装置を用いて被処理水中の病原性微生物を除
去し、一定時間毎に被処理水の濾過を停止し、筒状濾過
体の外周面から内周面に向けて濾過水を供給して逆洗
し、筒状濾過体の内面に捕捉された病原性微生物を洗い
落とし、系外に排出することを特徴とする水中の病原性
微生物の除去方法に関するものである。
According to a sixth aspect of the present invention, there is provided a water filtration apparatus for removing pathogenic microorganisms in water to be treated by using the water filtration apparatus according to any one of the first to fourth aspects. , The filtration of the water to be treated is stopped at regular intervals, the filtered water is supplied from the outer peripheral surface to the inner peripheral surface of the cylindrical filter to backwash, and the pathogenicity trapped on the inner surface of the cylindrical filter is The present invention relates to a method for removing pathogenic microorganisms in water, which is characterized by washing off microorganisms and discharging them out of the system.

【0013】上記課題を解決するための請求項7に係る
本発明は、請求項1ないし請求項4のいずれか1項に記
載の水濾過装置を2系列以上並列に設置し、各水濾過装
置の逆洗のタイミングをずらし、逆洗の必要が生じた水
濾過装置の逆洗用水として濾過処理中の他の水濾過装置
の濾過水を使用することを特徴とする請求項6に記載の
水中の病原性微生物の除去方法に係るものである。
According to a seventh aspect of the present invention, there is provided a water filtration apparatus comprising: a plurality of water filtration devices according to any one of the first to fourth aspects; 7. The underwater according to claim 6, wherein the timing of the backwashing is shifted, and the filtered water of another water filtering device during the filtration process is used as the backwashing water of the water filtering device in which the backwashing is required. And a method for removing pathogenic microorganisms.

【0014】[0014]

【発明の実施の形態】本発明装置で処理するための被処
理水としては、多孔質無機膜からなる筒状濾過体の濾過
寿命を延ばすために、凝集沈澱や濾過等の公知の方法で
予め除濁されたものが好ましい。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The water to be treated by the apparatus of the present invention is prepared in advance by a known method such as coagulation sedimentation or filtration in order to prolong the filtration life of a cylindrical filter made of a porous inorganic membrane. Those that are turbid are preferred.

【0015】本発明装置の、濾過手段としての膜は、例
えば断面が円形や三角形等の多角形状をなした筒状に形
成された多孔質無機膜である。ただし、制作が容易で強
度的にも優れており、かつデッドスペースが生じないと
いう点で、特に円筒状のものが好ましい。多孔質無機膜
の材質は特に限定されるものではないが、例えば、ステ
ンレス粉末等の金属で焼結した焼結金属、アルミナ粒子
で固めたセラミックス等を挙げることができる。無機膜
である理由は、高い流束に耐えられることと、紫外線照
射に耐えられること、すなわち紫外線照射によって膜材
質が劣化することがないことである。また、多孔質無機
膜のポアサイズは、1〜2μmが好ましい。ポアサイズ
が1μmより小さいと、濾過抵抗が大きくなり、高い濾
過流束が得られらくなる。また、2μmより大きくなる
と、クリプトスポリジウム等の病原性微生物が漏れる恐
れがある。
The membrane as the filtering means of the apparatus of the present invention is, for example, a porous inorganic membrane formed in a cylindrical shape having a polygonal shape such as a circular or triangular cross section. However, in view of easy production, excellent strength, and no dead space, a cylindrical shape is particularly preferable. The material of the porous inorganic film is not particularly limited, and examples thereof include a sintered metal sintered with a metal such as a stainless steel powder and a ceramic solidified with alumina particles. The reason that the inorganic film is used is that it can withstand a high flux and that it can withstand ultraviolet irradiation, that is, the film material does not deteriorate due to ultraviolet irradiation. The pore size of the porous inorganic membrane is preferably from 1 to 2 μm. If the pore size is smaller than 1 μm, the filtration resistance increases, and it becomes difficult to obtain a high filtration flux. If it is larger than 2 μm, pathogenic microorganisms such as cryptosporidium may leak.

【0016】本発明装置は、筒状濾過体の内部空間に被
処理水を供給し、筒状濾過体の内周面で病原性微生物を
捕捉するものである。捕捉した病原性微生物を、筒状濾
過体の内部空間内に設けた紫外線照射手段から照射され
た紫外線により不活化するものである。従って、紫外線
は360度に渡って、膜面まで照射されるので、従来の
平膜を使用した場合に比べ、2倍以上の紫外線利用率が
得られる。つまり単位膜面積当たりの紫外線照射強度を
同じくすれば、従来の半分の紫外線ランプ数ですむ。本
発明装置によってクリプトスポリジウム等の病原性微生
物を不活化することを目的とする場合、紫外線ランプと
しては波長254nm付近の紫外線を照射するこのとで
きる低圧水銀ランプを用いるのが好ましく、紫外線ラン
プの出力は、100mW・秒/cm2〜1000mW・
秒/cm2程度でよい。
The apparatus of the present invention supplies water to be treated to the internal space of a cylindrical filter, and captures pathogenic microorganisms on the inner peripheral surface of the cylindrical filter. The captured pathogenic microorganisms are inactivated by ultraviolet rays emitted from ultraviolet irradiation means provided in the internal space of the cylindrical filter. Therefore, since the ultraviolet rays are irradiated to the film surface over 360 degrees, the utilization rate of the ultraviolet rays is twice or more as compared with the case where the conventional flat film is used. In other words, if the UV irradiation intensity per unit film area is the same, the number of UV lamps is half that of the conventional one. When it is intended to inactivate pathogenic microorganisms such as Cryptosporidium by the apparatus of the present invention, it is preferable to use a low-pressure mercury lamp capable of irradiating ultraviolet rays having a wavelength of about 254 nm as an ultraviolet lamp, Is 100 mW · s / cm 2 to 1000 mW ·
Seconds / cm 2 may be sufficient.

【0017】なお、本発明の水濾過装置は上記のような
病原性微生物の不活化の他に、例えば被処理水中の有機
物を紫外線照射によって酸化分解する目的に使用するこ
とができ、このような場合は紫外線ランプとして波長1
85nm付近の紫外線を照射することのできる低圧水銀
ランプを用いるのが好ましい。ただし、紫外線ランプと
してはこれらに限定されるものではなく、目的に応じて
種々の波長のものを使用することができる。
The water filtration apparatus of the present invention can be used for the purpose of oxidatively decomposing organic substances in the water to be treated, for example, by irradiating ultraviolet rays, in addition to inactivating pathogenic microorganisms as described above. In case of UV lamp 1
It is preferable to use a low-pressure mercury lamp capable of irradiating an ultraviolet ray having a wavelength of about 85 nm. However, the UV lamp is not limited to these, and various wavelengths can be used according to the purpose.

【0018】本発明装置に用いる、筒状濾過体の内周面
の表面を二酸化チタンでコーティングすることにより、
光触媒作用により、紫外線による殺菌効果あるいは酸化
効果が向上するので、好ましい。
The surface of the inner peripheral surface of the cylindrical filter used in the device of the present invention is coated with titanium dioxide,
The photocatalytic action is preferable because the bactericidal effect or the oxidizing effect by ultraviolet rays is improved.

【0019】本発明装置では、紫外線の照射により捕捉
された病原性微生物を不活化しているため、この時同時
に被処理水中に含まれる有機物が酸化されて副生物が生
成し、飲用に好ましくない副生物が極めて微量ではある
が生成する虞れがある。そのため、本発明装置から得ら
れる濾過水を、活性炭で処理して副生物を吸着、除去す
ることが好ましい。
In the apparatus of the present invention, since the pathogenic microorganisms captured by the irradiation of ultraviolet rays are inactivated, organic substances contained in the water to be treated are simultaneously oxidized to produce by-products, which is undesirable for drinking. There is a possibility that by-products are produced although they are very small. Therefore, it is preferable to treat filtered water obtained from the apparatus of the present invention with activated carbon to adsorb and remove by-products.

【0020】本発明処理装置の多孔質無機膜の透過速度
は被処理水の水質および濾過圧等にもよるが、一般的に
は20〜200m3/m2/hで行うとよい。濾過継続時
間は、5〜30min程度が適切であり、それ以上にな
ると膜の目詰まりが発生しやすくなるし、また濾過継続
時間が短くなると水の回収率が少なくなるので好ましく
ない。
The permeation speed of the porous inorganic membrane of the treatment apparatus of the present invention depends on the quality of the water to be treated, the filtration pressure, etc., but is generally preferably 20 to 200 m 3 / m 2 / h. The duration of filtration is suitably about 5 to 30 min. If the duration is longer than this, clogging of the membrane is likely to occur, and if the duration of filtration is shorter, the recovery rate of water is reduced, which is not preferable.

【0021】図1により本発明の水濾過装置の一実施形
態を説明する。
Referring to FIG. 1, one embodiment of the water filtration device of the present invention will be described.

【0022】本発明の水濾過装置1は、多孔質無機膜か
らなる例えば円筒状の筒状濾過体2の内部空間の略中心
に紫外線照射手段としての紫外線ランプ3を例えば円筒
状の容器4内に設けたものである。筒状濾過体2の内部
空間に被処理水を供給する被処理水供給流路5が設けら
れ、水中の病原性微生物は、筒状濾過体2の内周面上に
捕捉され、病原性微生物が除去された濾過水が筒状濾過
体2の外周面から流出し、処理水排出流路6から排出さ
れる。この時、筒状濾過体2の内部に流入した被処理水
中の病原性微生物および筒状濾過体2の内周面上に捕捉
された病原性微生物は、紫外線ランプ3から照射された
紫外線によって不活化される。
In the water filtration device 1 of the present invention, an ultraviolet lamp 3 as an ultraviolet irradiation means is provided in a substantially cylindrical container 4 at substantially the center of the internal space of, for example, a cylindrical tubular filter 2 made of a porous inorganic membrane. It is provided in. A treated water supply flow path 5 for supplying treated water is provided in the internal space of the cylindrical filter 2, and the pathogenic microorganisms in the water are captured on the inner peripheral surface of the cylindrical filter 2, and the pathogenic microorganisms are captured. The filtered water from which the water has been removed flows out from the outer peripheral surface of the cylindrical filter body 2 and is discharged from the treated water discharge channel 6. At this time, the pathogenic microorganisms in the water to be treated and the pathogenic microorganisms trapped on the inner peripheral surface of the cylindrical filter 2 that have flowed into the cylindrical filter 2 are improperly irradiated by the ultraviolet light emitted from the ultraviolet lamp 3. Be activated.

【0023】一定時間、濾過を継続すると多孔質無機膜
が目詰まりするので、濾過処理を停止し、処理水排出流
路6から該水濾過装置1によって処理済みの濾過水を流
入させて、逆洗し、逆洗排水排出流路7から逆洗排水を
系外へ排出する。なお、本例では上記逆洗の際に排出さ
れる逆洗排水を逆洗排水排出流路7から排出するように
したが、後述の実施形態に示すごとく逆洗排水排出流路
7を設けず、逆洗排水を被処理水供給流路5から排出す
るようにしてもよい。
If the filtration is continued for a certain period of time, the porous inorganic membrane is clogged. Therefore, the filtration process is stopped, and the filtered water treated by the water filtration device 1 is caused to flow from the treated water discharge channel 6 to reverse. After washing, the backwash wastewater is discharged from the backwash wastewater discharge channel 7 to the outside of the system. In this example, the backwash drainage discharged at the time of the backwash is discharged from the backwash drain discharge channel 7, but the backwash drain discharge channel 7 is not provided as shown in an embodiment described later. Alternatively, the backwash wastewater may be discharged from the treated water supply flow path 5.

【0024】上述のごとく、逆洗に使用する水は水濾過
装置1で予め処理されて病原性微生物が除去された濾過
水を使用するとともに、濾過処理の停止時に水濾過装置
1の内部に残留している被処理水中の病原性微生物も紫
外線ランプ3からの紫外線照射によって不活化されてい
るので、逆洗によって上記水濾過装置1から排出される
逆洗排水中には病原性微生物が含まれておらず、したが
って、逆洗排水はなんらの殺菌処理を施すことなく系外
に放流することができる。
As described above, the water used for backwashing is filtered water which has been treated in advance in the water filtration device 1 and from which pathogenic microorganisms have been removed, and which remains inside the water filtration device 1 when the filtration process is stopped. Since the pathogenic microorganisms in the water to be treated are also inactivated by the irradiation of ultraviolet rays from the ultraviolet lamp 3, the backwash wastewater discharged from the water filtration device 1 by backwashing contains pathogenic microorganisms. Therefore, the backwash wastewater can be discharged out of the system without performing any sterilization treatment.

【0025】なお、筒状濾過体の内部空間に紫外線ラン
プを有しない濾過ユニットを備えた水濾過装置を用い
て、病原性微生物を含む被処理水を処理することも考え
られるが、この場合は筒状濾過体の内周面上に捕捉され
た活性を有する病原性微生物が膜面から除去されて逆洗
排水中に混入するため、逆洗排水を殺菌(不活化)処理
してからでないと放流できないので、逆洗排水の殺菌処
理装置が新たに必要となるとともに処理工程も煩雑とな
る。
It is also conceivable to treat the water to be treated containing pathogenic microorganisms by using a water filtration device provided with a filtration unit having no ultraviolet lamp in the internal space of the cylindrical filtration body. Since pathogenic microorganisms having activity trapped on the inner peripheral surface of the cylindrical filter are removed from the membrane surface and mixed into the backwash wastewater, the backwash wastewater must be sterilized (inactivated). Since it cannot be discharged, a new sterilization apparatus for backwash wastewater is required, and the processing steps become complicated.

【0026】図2により、本発明の水濾過装置を水中の
病原性微生物の除去に適用した場合の水の処理方法の一
実施形態を説明する。
Referring to FIG. 2, one embodiment of a water treatment method when the water filtration device of the present invention is applied to the removal of pathogenic microorganisms in water will be described.

【0027】図2において、まずバルブ8,10を開放
し、バルブ9を閉じておく。被処理水を被処理水供給流
路5から水濾過装置1に供給し、病原性微生物を筒状濾
過体(不図示)の内周面上に捕捉する。捕捉された病原
性微生物は、濾過ユニット内部に収容された紫外線ラン
プ(不図示)から照射された紫外線により不活化され
る。濾過された濾過水は、処理水排出流路6を経て、処
理水貯槽11に溜まる。筒状濾過体2の目詰まりを解消
するために、一定時間毎に逆洗処理を行う必要がある。
逆洗処理を行うには、まずバルブ8,10を閉じ、バル
ブ9を開放し、処理水貯槽11内に貯留されている濾過
水を逆洗用水として逆洗水ポンプ12で処理水排出流路
6を経て、供給する。逆洗用水は、筒状濾過体の外周面
から浸透し、内周面に捕捉された懸濁物質や病原性微生
物の不活化されたものを剥離して、逆洗水排出流路7か
ら排出され、バルブ9を経て、逆洗排水槽13に流入す
る。前述のごとく、逆洗排水中には活性を有する病原性
微生物は含まれていないので、逆洗排水は、排水として
そのまま放流してもよく、また被処理水(原水)に返送
してもよい。
In FIG. 2, first, the valves 8, 10 are opened, and the valve 9 is closed. The to-be-treated water is supplied to the water filtration device 1 from the to-be-treated water supply flow path 5, and the pathogenic microorganisms are captured on the inner peripheral surface of a cylindrical filter (not shown). The captured pathogenic microorganisms are inactivated by ultraviolet rays emitted from an ultraviolet lamp (not shown) housed inside the filtration unit. The filtered water passes through the treated water discharge channel 6 and accumulates in the treated water storage tank 11. In order to eliminate clogging of the tubular filter 2, it is necessary to perform a backwashing process at regular intervals.
To perform the backwashing process, first, the valves 8 and 10 are closed, the valve 9 is opened, and the filtered water stored in the treated water storage tank 11 is used as backwashing water by the backwashing water pump 12 and the treated water discharge flow path. Supply via 6 The backwash water penetrates from the outer peripheral surface of the cylindrical filter, peels off suspended substances and inactivated pathogenic microorganisms trapped on the inner peripheral surface, and is discharged from the backwash water discharge channel 7. Then, it flows into the backwash drainage tank 13 via the valve 9. As described above, since active pathogenic microorganisms are not contained in the backwash wastewater, the backwash wastewater may be discharged as wastewater as it is, or may be returned to the water to be treated (raw water). .

【0028】図3により、本発明の水中の病原性微生物
の除去方法の他の実施形態を示す。図3は、水濾過装置
を2系列並列に設け、逆洗による濾過処理の中断時間を
なくすための装置例のフロー図である。
FIG. 3 shows another embodiment of the method for removing pathogenic microorganisms in water according to the present invention. FIG. 3 is a flow chart of an example of an apparatus for providing two water filtration devices in parallel and eliminating an interruption time of a filtration process by backwashing.

【0029】本実施形態例の装置においては、2系列の
水濾過装置1および1’を、両者が同時に逆洗操作に入
ることのないように互いに運転間隔をずらして運転す
る。まず、2系列同時に濾過処理を行っている段階で
は、バルブ8およびバルブ8’を開放し、バルブ9、
9’およびバルブ14、14’を閉じた状態でポンプ1
5により2系列の水濾過装置1、1’に被処理水供給流
路5、5’を介して被処理水を供給する。被処理水は、
筒状濾過体(不図示)の内部空間に供給され、筒状濾過
体の内周面上で病原性微生物が捕捉され、透過した処理
水(濾過水)が処理水排出流路6、6’およびバルブ1
0、10’を経て、処理水貯槽11に溜まる。一定時間
濾過操作を行って、例えば水濾過装置1が逆洗時期に達
したら、別系統の水濾過装置1’で濾過操作を行ってい
る間に、水濾過装置1の逆洗操作を行う。まず、バルブ
9およびバルブ14を開放し、バルブ10およびバルブ
14’を閉じる。ついで逆洗ポンプ12を稼働し、処理
水貯槽11内の濾過水を逆洗用水としてバルブ14およ
び処理水排出流路6を経て、水濾過装置1に供給する。
筒状濾過体の内周面上に捕捉された病原性微生物は、逆
洗用水により洗い流され逆洗排水排出流路7およびバル
ブ9を経て、系外に放出される。
In the apparatus of the present embodiment, the two-line water filtration devices 1 and 1 'are operated at an interval different from each other so that they do not simultaneously enter the backwashing operation. First, at the stage where the filtration process is performed simultaneously for two lines, the valve 8 and the valve 8 'are opened, and the valve 9,
Pump 1 with 9 'and valves 14, 14' closed
5, the water to be treated is supplied to the two series of water filtration devices 1, 1 'through the water supply flow paths 5, 5'. The water to be treated is
The treated water (filtrated water) is supplied to the internal space of the cylindrical filter (not shown), the pathogenic microorganisms are captured on the inner peripheral surface of the cylindrical filter, and the permeated treated water (filtrated water) is treated water discharge channels 6, 6 '. And valve 1
After passing through 0 and 10 ′, the water accumulates in the treated water storage tank 11. When the filtration operation is performed for a certain period of time and, for example, the water filtration device 1 reaches a backwashing time, the backwash operation of the water filtration device 1 is performed while the filtration operation is performed by the water filtration device 1 ′ of another system. First, the valves 9 and 14 are opened, and the valves 10 and 14 'are closed. Then, the backwash pump 12 is operated, and the filtered water in the treated water storage tank 11 is supplied to the water filtration device 1 through the valve 14 and the treated water discharge channel 6 as backwash water.
The pathogenic microorganisms trapped on the inner peripheral surface of the cylindrical filter are washed away by the backwash water and discharged out of the system via the backwash drainage discharge channel 7 and the valve 9.

【0030】水濾過装置1の逆洗操作が終了したら、再
び水濾過装置1および1’により濾過処理を継続すれば
よい。このような濾過操作を行っている間に、別系統の
水濾過装置1’が逆洗の時期に達した場合は、上記と同
様にして水濾過装置1’の逆洗操作を行えばよい。別系
統の水濾過装置1’の逆洗操作は、水濾過装置1の逆洗
操作と同様であるので、説明を省略する。
After the back washing operation of the water filtration device 1 is completed, the filtration process may be continued by the water filtration devices 1 and 1 'again. If the water filtration device 1 'of another system reaches the time of backwashing while performing such a filtration operation, the backwash operation of the water filtration device 1' may be performed in the same manner as described above. The backwashing operation of the water filtration device 1 ′ of another system is the same as the backwashing operation of the water filtration device 1, and thus the description is omitted.

【0031】図3に示した実施形態のように、水濾過装
置を2系列もしくはそれ以上並列に設置することによ
り、連続して濾過操作を行いながら逆洗操作を行うこと
ができ、処理効率が向上する。
By installing two or more water filtration devices in parallel as in the embodiment shown in FIG. 3, the backwashing operation can be performed while performing the filtration operation continuously, and the processing efficiency is improved. improves.

【0032】図4に本発明の水濾過装置の他の実施形態
の一例を示す。なお、図4において矢印は水の流れを示
している。
FIG. 4 shows an example of another embodiment of the water filtration device of the present invention. In FIG. 4, arrows indicate the flow of water.

【0033】本実施形態では、筒状濾過体2の内部に紫
外線ランプ3を設けた濾過ユニットを円筒状の容器4内
に複数並列に設けた例であり、大量の被処理水を濾過す
る場合に好適に用いられる。濾過ユニットを複数並列に
設ける場合には、各ユニットの筒状濾過体2を軸方向に
向けた状態で各筒状濾過体2の両端部を仕切り板15,
15’で保持すると共に各筒状濾過体2の両端開口部
を、容器4の両端に形成された被処理水室16を介して
被処理水供給流路5に連通させ、また、両仕切板15,
15’間に、各筒状濾過体2が収容された濾過水室17
を形成すると共に、該濾過水室17を処理水排出流路5
に連通させ、被処理水が被処理水室16を介して筒状濾
過体2の内部に供給され、濾過水は濾過水室17に集水
されて処理水排出流路6から排出されるようにすればよ
い。また、本例では、図1に示した装置と異なり逆洗排
水排出流路を設けておらず、したがって、逆洗排水は被
処理水供給流路5から排出すればよい。
This embodiment is an example in which a plurality of filtration units each having an ultraviolet lamp 3 provided inside a cylindrical filter body 2 are provided in parallel in a cylindrical container 4, and a large amount of water to be treated is filtered. It is preferably used. When a plurality of filtration units are provided in parallel, both ends of each tubular filter 2 are partitioned by partition plates 15 with the tubular filter 2 of each unit oriented in the axial direction.
15 ', and both ends of each cylindrical filter 2 are communicated with the treated water supply flow path 5 through the treated water chambers 16 formed at both ends of the container 4; 15,
15 ′, a filtered water chamber 17 in which each cylindrical filter body 2 is accommodated.
And the filtered water chamber 17 is connected to the treated water discharge flow path 5.
The treated water is supplied to the inside of the cylindrical filter body 2 through the treated water chamber 16, and the filtered water is collected in the filtered water chamber 17 and discharged from the treated water discharge channel 6. What should I do? Further, in this example, unlike the apparatus shown in FIG. 1, a backwash drain discharge channel is not provided. Therefore, the backwash drain may be discharged from the treated water supply channel 5.

【0034】なお、複数の濾過ユニットを同一容器内に
収容してなる濾過装置の構造は、図4に示した実施形態
のものに限定されるものではなく、要は、被処理水供給
流路5から供給される被処理水を各筒状濾過体の内部空
間に導入し、また、各筒状濾過体の外側に得られる濾過
水を濾過水室に集水して容器外に流出させる構造であれ
ばいかなる構造であってもよい。
The structure of the filtration device in which a plurality of filtration units are housed in the same container is not limited to that of the embodiment shown in FIG. 5. A structure in which the water to be treated supplied from 5 is introduced into the internal space of each cylindrical filter, and the filtered water obtained outside each cylindrical filter is collected in a filtered water chamber and discharged out of the vessel. Any structure may be used.

【0035】また、図4では、濾過ユニットを容器4内
に水平に配設した横型の水濾過装置の例を示したが、濾
過ユニットを容器内に垂直に配設して縦型の水濾過装置
としてもよい。
FIG. 4 shows an example of a horizontal water filtration apparatus in which a filtration unit is horizontally disposed in a container 4, but a vertical water filtration apparatus in which a filtration unit is vertically disposed in a container. It may be a device.

【0036】[0036]

【実施例】実施例1 浄水場の砂濾過水に1リットル当たり10個のクリプト
スポリジウムのオーシストを添加した後、図2に示した
ような病原性微生物除去装置に濾過圧1.5kg/cm
2、濾過速度20m3/m2/hの条件下で濾過した。筒
状濾過体としてステンレス製焼結金属フィルターからな
る円筒状(外径:15cm、厚さ:3mm)の多孔質無
機膜(公称濾過孔径:2μm)を使用した。
EXAMPLE 1 After adding 10 oocysts of Cryptosporidium per liter to sand filtered water of a water purification plant, the filtration pressure was set at 1.5 kg / cm in a device for removing pathogenic microorganisms as shown in FIG.
2. Filtration was performed under the conditions of a filtration speed of 20 m 3 / m 2 / h. A cylindrical (outer diameter: 15 cm, thickness: 3 mm) porous inorganic membrane (nominal filtration hole diameter: 2 μm) made of a stainless steel sintered metal filter was used as the cylindrical filter.

【0037】使用した水濾過装置の筒状濾過体の内部に
は、ほぼ中心に主波長が254nmの2本の低圧水銀ラ
ンプ(紫外線ランプ)が設置されており、濾過面積当た
り500mW・秒/cm2の紫外線強度で紫外線を照射
した。濾過継続時間を6分とし、その後1分間逆洗し
た。逆洗水量は、濾過水量の2%とした。濾過水および
逆洗排水をサンプリングし、クリプトスポリジウムの測
定を行った。結果を表1に示す。なお、蛍光発光検体数
とは、生存検体および死滅検体を含む全ての検体数であ
る。
Inside the cylindrical filter of the water filter used, two low-pressure mercury lamps (ultraviolet lamps) having a main wavelength of 254 nm are installed at substantially the center, and 500 mW · sec / cm per filtration area. Ultraviolet light was irradiated at an ultraviolet intensity of 2 . The duration of filtration was set to 6 minutes, and then backwashed for 1 minute. The backwash water amount was 2% of the filtered water amount. Filtration water and backwash wastewater were sampled and Cryptosporidium was measured. Table 1 shows the results. Note that the number of fluorescent light-emitting specimens is the total number of specimens including viable specimens and dead specimens.

【0038】[0038]

【表1】 [Table 1]

【0039】表1に示した結果から明らかなように、本
願発明装置により、被処理水中に含まれたクリプトスポ
リジウムのオーシストは、筒状濾過体により捕捉され、
濾過水中にはほとんど含まれていない。捕捉されたクリ
プトスポリジウムのオーシストは逆洗排水中に含まれて
いるが、ほぼ完全に紫外線により不活化されており、そ
のまま放流しても問題ないことが分かる。
As is evident from the results shown in Table 1, the oocysts of Cryptosporidium contained in the water to be treated are captured by the cylindrical filter by the apparatus of the present invention.
It is hardly contained in filtered water. Although the captured oocysts of Cryptosporidium are contained in the backwash wastewater, they are almost completely inactivated by ultraviolet light, and it can be seen that there is no problem if the oocysts are discharged as they are.

【0040】[0040]

【発明の効果】請求項1、請求項5および請求項6に記
載された本発明は、多孔質無機膜により水中のクリプト
スポリジウム等の病原性微生物を容易に除去でき、また
筒状濾過体の内部空間に設けた紫外線照射手段により捕
捉した病原性微生物を効率的に不活化することができ、
さらに濾過膜が多孔質無機膜であるため紫外線照射によ
って膜が劣化することがない。
According to the first, fifth and sixth aspects of the present invention, the porous inorganic membrane can easily remove pathogenic microorganisms such as Cryptosporidium in water. Pathogenic microorganisms captured by ultraviolet irradiation means provided in the internal space can be inactivated efficiently,
Further, since the filtration membrane is a porous inorganic membrane, the membrane is not deteriorated by ultraviolet irradiation.

【0041】請求項2に記載された本発明は、濾過ユニ
ットを複数個容器内に並列に配置したことにより、同一
容量の容器であれば濾過膜面積を増やすことができ、同
一の濾過膜面積であれば水濾過装置全体の大きさを小さ
くすることができるので、大量の水を処理する場合に極
めて有利である。
According to the second aspect of the present invention, by arranging a plurality of filtration units in parallel in a vessel, the filtration membrane area can be increased if the vessels have the same capacity, and the same filtration membrane area can be obtained. In this case, the size of the entire water filtration device can be reduced, which is extremely advantageous when treating a large amount of water.

【0042】請求項3に記載された本発明は、多孔質無
機膜の内面を二酸化チタンでコーティングしたため、捕
捉した病原性微生物の不活化あるいは被処理水中の有機
物の酸化をより効率的に行うことができる。
According to the third aspect of the present invention, since the inner surface of the porous inorganic film is coated with titanium dioxide, the inactivated captured pathogenic microorganisms or the oxidation of organic substances in the water to be treated can be performed more efficiently. Can be.

【0043】請求項4に記載された本発明は、多孔質無
機膜を焼結金属とすることにより、膜強度が向上し、濾
過圧を高められるので、より大量の水を短時間で処理す
ることができる。
According to the fourth aspect of the present invention, since the porous inorganic membrane is made of a sintered metal, the membrane strength is improved and the filtration pressure is increased, so that a larger amount of water can be treated in a short time. be able to.

【0044】請求項7に記載された本発明は、水濾過装
置を2系列以上並列に設置したため、連続して病原性微
生物の除去操作を行うことができ、逆洗操作に伴うロス
がない。
According to the seventh aspect of the present invention, since two or more water filtration devices are installed in parallel, the operation of removing pathogenic microorganisms can be performed continuously, and there is no loss associated with the backwashing operation.

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

【図1】本発明の水濾過装置の一実施形態を示す断面模
式図。
FIG. 1 is a schematic sectional view showing one embodiment of a water filtration device of the present invention.

【図2】本発明の水濾過装置を用いた、水処理方法の一
実施形態を示すフロー図。
FIG. 2 is a flowchart showing one embodiment of a water treatment method using the water filtration device of the present invention.

【図3】本発明の水濾過除去装置を用いた、水処理方法
の他の実施形態を示すフロー図。
FIG. 3 is a flowchart showing another embodiment of the water treatment method using the water filtration / removal device of the present invention.

【図4】本発明の水濾過装置の他の実施形態を示す断面
模式図。
FIG. 4 is a schematic sectional view showing another embodiment of the water filtration device of the present invention.

【符号の説明】[Explanation of symbols]

1,1’ 水濾過装置 2 筒状濾過体 3 紫外線ランプ 4 容器 5,5’ 被処理水供給流路 6,6’ 処理水排出流路 7,7’ 逆洗排水排出流路 8,9,10,14,8’,9’,10’,14’ バ
ルブ 11 処理水貯槽 12,14 ポンプ 15 仕切り板 16 被処理水室 17 濾過水室
1, 1 'water filtration device 2 cylindrical filter body 3 ultraviolet lamp 4 container 5, 5' treated water supply flow path 6, 6 'treated water discharge flow path 7, 7' backwash drain discharge flow path 8, 9, 10, 14, 8 ', 9', 10 ', 14' Valve 11 Treated water storage tank 12, 14 Pump 15 Partition plate 16 Treated water chamber 17 Filtration water chamber

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI C02F 1/32 C02F 1/72 101 1/72 101 B01D 29/10 520B 530A 29/38 510C 520A ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 6 Identification code FI C02F 1/32 C02F 1/72 101 1/72 101 B01D 29/10 520B 530A 29/38 510C 520A

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 多孔質無機膜からなる筒状濾過体の内部
空間に紫外線照射手段を設けた濾過ユニットを容器内に
配置した濾過装置であって、該筒状濾過体の内部空間に
被処理水を供給する被処理水供給流路と、筒状濾過体の
外周面から得られた濾過水を排出する処理水排出流路と
を有することを特徴とする水濾過装置。
1. A filtration device in which a filtration unit provided with an ultraviolet irradiation means is provided in a container in an inner space of a cylindrical filter made of a porous inorganic membrane. A water filtration device comprising: a treated water supply flow path for supplying water; and a treated water discharge flow path for discharging filtered water obtained from an outer peripheral surface of a cylindrical filter.
【請求項2】 前記濾過ユニットを複数個容器内に並列
に配置したことを特徴とする請求項1に記載の水濾過装
置。
2. The water filtration device according to claim 1, wherein a plurality of the filtration units are arranged in a container in parallel.
【請求項3】 前記筒状濾過体の内周面の表面が二酸化
チタンでコーティングされていることを特徴とする請求
項1または請求項2に記載の水濾過装置。
3. The water filtration device according to claim 1, wherein an inner peripheral surface of the cylindrical filter is coated with titanium dioxide.
【請求項4】 前記筒状濾過体が、焼結金属からなる多
孔質無機膜であることを特徴とする請求項1ないし請求
項3のいずれか1項に記載の水濾過装置。
4. The water filtration device according to claim 1, wherein the cylindrical filter is a porous inorganic membrane made of a sintered metal.
【請求項5】 請求項1ないし請求項4のいずれか1項
に記載の水濾過装置の被処理水供給流路から被処理水を
供給し、筒状濾過体の内面で被処理水中の病原性微生物
を捕捉するとともに捕捉された病原性微生物を濾過ユニ
ット内の紫外線照射手段で不活化し、筒状濾過体の外周
面から濾過水を得ることを特徴とする水中の病原性微生
物の除去方法。
5. The water to be treated is supplied from the treated water supply flow path of the water filtration device according to any one of claims 1 to 4, and the pathogen in the treated water is formed on the inner surface of the cylindrical filter. A method for removing pathogenic microorganisms in water, comprising capturing the pathogenic microorganisms, inactivating the captured pathogenic microorganisms by means of ultraviolet irradiation in a filtration unit, and obtaining filtered water from the outer peripheral surface of the cylindrical filter. .
【請求項6】 請求項1ないし請求項4のいずれか1項
に記載の水濾過装置を用いて被処理水中の病原性微生物
を除去し、一定時間毎に被処理水の濾過を停止し、筒状
濾過体の外周面から内周面に向けて濾過水を供給して逆
洗し、筒状濾過体の内面に捕捉された病原性微生物を洗
い落とし、系外に排出することを特徴とする水中の病原
性微生物の除去方法。
6. A method for removing the pathogenic microorganisms in the water to be treated using the water filtration device according to any one of claims 1 to 4, and stopping the filtration of the water to be treated at regular intervals, It is characterized by supplying filtered water from the outer peripheral surface to the inner peripheral surface of the cylindrical filter and backwashing, washing off pathogenic microorganisms trapped on the inner surface of the cylindrical filter, and discharging the same out of the system. A method for removing pathogenic microorganisms in water.
【請求項7】 請求項1ないし請求項4のいずれか1項
に記載の水濾過装置を2系列以上並列に設置し、各水濾
過装置の逆洗のタイミングをずらし、逆洗の必要が生じ
た水濾過装置の逆洗用水として濾過処理中の他の水濾過
装置の濾過水を使用することを特徴とする請求項6に記
載の水中の病原性微生物の除去方法。
7. The water filtration device according to claim 1 is installed in two or more lines in parallel, and the timing of backwashing of each water filtration device is shifted, so that the necessity of backwashing arises. The method for removing pathogenic microorganisms in water according to claim 6, wherein filtered water of another water filtration device being filtered is used as backwashing water of the water filtration device.
JP33836097A 1997-12-09 1997-12-09 Water filtration apparatus and method for removing pathogenic microorganisms in water Expired - Fee Related JP3813338B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33836097A JP3813338B2 (en) 1997-12-09 1997-12-09 Water filtration apparatus and method for removing pathogenic microorganisms in water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33836097A JP3813338B2 (en) 1997-12-09 1997-12-09 Water filtration apparatus and method for removing pathogenic microorganisms in water

Publications (2)

Publication Number Publication Date
JPH11169612A true JPH11169612A (en) 1999-06-29
JP3813338B2 JP3813338B2 (en) 2006-08-23

Family

ID=18317428

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33836097A Expired - Fee Related JP3813338B2 (en) 1997-12-09 1997-12-09 Water filtration apparatus and method for removing pathogenic microorganisms in water

Country Status (1)

Country Link
JP (1) JP3813338B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005110928A1 (en) * 2004-05-19 2005-11-24 Organo Corporation Production method of ballast water for vessel, production system of ballast water for vessel and use
CN113015690A (en) * 2018-12-07 2021-06-22 三星电子株式会社 Water purifier and control method thereof

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005110928A1 (en) * 2004-05-19 2005-11-24 Organo Corporation Production method of ballast water for vessel, production system of ballast water for vessel and use
CN113015690A (en) * 2018-12-07 2021-06-22 三星电子株式会社 Water purifier and control method thereof
CN113015690B (en) * 2018-12-07 2024-03-08 三星电子株式会社 Water purifier and control method thereof

Also Published As

Publication number Publication date
JP3813338B2 (en) 2006-08-23

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