JPH10109095A - Water purifying treatment device - Google Patents

Water purifying treatment device

Info

Publication number
JPH10109095A
JPH10109095A JP8263114A JP26311496A JPH10109095A JP H10109095 A JPH10109095 A JP H10109095A JP 8263114 A JP8263114 A JP 8263114A JP 26311496 A JP26311496 A JP 26311496A JP H10109095 A JPH10109095 A JP H10109095A
Authority
JP
Japan
Prior art keywords
water
filter layer
membrane module
valve
treated water
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
JP8263114A
Other languages
Japanese (ja)
Inventor
Kazunari Katagiri
一成 片桐
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.)
JFE Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan 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 NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP8263114A priority Critical patent/JPH10109095A/en
Publication of JPH10109095A publication Critical patent/JPH10109095A/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

Landscapes

  • Filtration Of Liquid (AREA)
  • Water Treatment By Sorption (AREA)
  • Biological Treatment Of Waste Water (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PROBLEM TO BE SOLVED: To constitute the device of two filtering parts in a filter tower and to reduce a required installation area by providing a filter layer packed active coal in an upward counter flow type filter tower, and arranging an immersed type membrane module at the upper side of the filter layer. SOLUTION: At the water purifying treatment, the raw water after an aggregation and precipitation treatment is introduced into the filter tower 10, and is passed through the filter layer 11 packed the active coal. At this time, chemical substance such as ammonia is adsorbed and organic matters are decomposed and removed with microorganisms stuck to the surface of the active coal. Next, the water is sucked with a suction pump 15, transmitted a hollow fiber membrane of the membrane module 12, passed a treated water flow-out pipe 13 and is temporarily stored in a treated water tank 16. At the time of regeneration, the suction pump 15 is stopped and a valve 14 is closed, and then a blower 20 is driven and air is blown into the filter layer 11 from a diffusion pipe 19. A valve 22 is opened and a backwashing pump 17 is driven, and then a valve 23 is opened and the treated water is introduced into the filtering tower 10, and next a valve 18 is opened and the treated water is fed into the hollow fiber membrane in the membrane module 12 to wash it.

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】本発明は上水道の浄水処理装
置に関する。
The present invention relates to a water purification system for water supply.

【0002】[0002]

【従来の技術】上水道の浄水処理においては、従来か
ら、取水した河川水や湖沼水などに凝集剤を添加して懸
濁物を凝集沈澱させて除去した後、塩素処理を行う操作
が行われていたが、近年、特に、大都会近郊における上
水道の浄水処理においては、水源の水質の悪化に伴っ
て、高度処理システムによる処理が行われるようになっ
てきた。この高度処理は、凝集沈澱処理と、生物活性炭
濾過あるいは通常の生物膜濾過による処理、およびオゾ
ン処理の組み合わせによるものである。
2. Description of the Related Art Conventionally, in water purification treatment of waterworks, an operation of adding a flocculant to river water, lake water, or the like that has been withdrawn to coagulate and precipitate a suspended matter, and then performing a chlorine treatment. However, in recent years, in particular, in water purification treatment of waterworks in the suburbs of large cities, treatment by an advanced treatment system has been performed along with deterioration of water quality of a water source. This advanced treatment is based on a combination of coagulation precipitation treatment, treatment with biological activated carbon filtration or ordinary biofilm filtration, and ozone treatment.

【0003】ところで、高度処理システムにおいて選択
される処理方法の一つである生物活性炭濾過は、各種成
分を吸着する処理と有機物を生物学的に分解する処理を
同時に行わせる処理方法であって、有機物の分解は充填
された活性炭の表面に原水を通水している間に着生する
微生物の働きによって行われる。このため、生物活性炭
濾過で行った場合には、各種成分が吸着されるだけでな
く、有機物の分解・除去も行われる。
[0003] Biological activated carbon filtration, which is one of the treatment methods selected in an advanced treatment system, is a treatment method in which a treatment for adsorbing various components and a treatment for biologically decomposing organic substances are simultaneously performed. The decomposition of organic matter is carried out by the action of microorganisms that grow while passing raw water through the surface of the filled activated carbon. Therefore, when the filtration is performed by biological activated carbon, not only various components are adsorbed, but also decomposition and removal of organic substances are performed.

【0004】図2は従来の高度処理システムによる浄水
処理装置に係る構成の一例を示す図である。この装置
は、第1の濾過装置である濾過塔30と、砂濾過方式あ
るいは分離膜を用いる方式による第2の濾過装置40よ
りなり、この濾過塔30内には粒状活性炭が充填された
濾層31が設けられている。図中、32は浄水操作を停
止して濾過塔30を洗浄する際に濾層32を流動させる
空気を吹き込むための散気管であり、33は散気管32
へ空気を送るブロアーである。
FIG. 2 is a diagram showing an example of a configuration relating to a water purification apparatus using a conventional advanced treatment system. This apparatus comprises a filtration tower 30 as a first filtration apparatus and a second filtration apparatus 40 by a sand filtration method or a method using a separation membrane, and a filtration layer filled with granular activated carbon in the filtration tower 30. 31 are provided. In the drawing, reference numeral 32 denotes an air diffuser for blowing air for flowing the filter layer 32 when the water purification operation is stopped and the filtration tower 30 is washed, and 33 denotes an air diffuser 32.
It is a blower that sends air to

【0005】この装置で浄水処理を行う場合、凝集沈澱
処理された原水が濾過塔30へ供給され、この原水は濾
層31を通過する間に浄化され、処理水となって排出さ
れる。ここで、この処理水の中には、濾層31で繁殖し
た原生動物や後生動物などの生物が混入してくるので、
処理水を第2の濾過装置40へ送って濾過した後、浄水
池へ送水する。
When water purification treatment is performed by this apparatus, raw water subjected to coagulation and sedimentation is supplied to a filtration tower 30, and this raw water is purified while passing through a filtration layer 31, and is discharged as treated water. Here, organisms such as protozoa and metazoans that have propagated in the filter layer 31 are mixed into the treated water.
After sending the treated water to the second filtration device 40 for filtration, the treated water is sent to a water purification tank.

【0006】[0006]

【発明が解決しようとする課題】しかし、上記従来の浄
水処理装置においては、原水を浄化する濾過塔30の他
に第2の濾過装置40を独立させて列設しなければなら
ないので、広い設置スペースが必要であり、その狭小化
が望まれている。
However, in the above-mentioned conventional water purification apparatus, the second filtration device 40 must be arranged independently in addition to the filtration tower 30 for purifying raw water. Space is required, and a reduction in space is desired.

【0007】本発明は、設置スペースの所要面積が小さ
い浄水処理装置を提供することを目的とする。
[0007] It is an object of the present invention to provide a water purification treatment apparatus requiring a small installation space.

【0008】[0008]

【課題を解決するための手段】上記の目的を達成するた
めに、本発明に係る浄水処理装置は、上向流式の濾過塔
内に活性炭が充填された濾層が設けられ、この濾層の上
方に浸漬型の膜モジュールが配設されていることを特徴
としている。
In order to achieve the above object, a water treatment apparatus according to the present invention is provided with a filter bed filled with activated carbon in an upflow type filtration tower. Is characterized in that a immersion type membrane module is disposed above the above.

【0009】[0009]

【発明の実施の形態】図1は本発明の浄水処理装置に係
る一例の構成を示す図である。図1において、10は上
向流式の濾過塔であり、この濾過塔10内には粒状活性
炭が充填された濾層11が設けられている。そして、こ
の濾層11の上方には浸漬型の膜モジュール12が配置
されている。この膜モジュール12は原水中に浸漬され
る。膜モジュール12は多数本の中空糸膜よりなるもの
であって、原水を中空糸膜の外側から内側へ向かって透
過させる構造になっており、その二次側は処理水流出管
13に接続されている。また、膜モジュール12による
濾過を行う際には、中空糸膜の外側から内側へ処理水を
透過させるための差圧を発生させる必要があるが、この
装置においては、処理水流出管13に連結された吸引ポ
ンプ15によって処理水を吸引する方式になっている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 is a diagram showing an example of the configuration of a water purification apparatus according to the present invention. In FIG. 1, reference numeral 10 denotes an upward-flow filtration tower, in which a filtration layer 11 filled with granular activated carbon is provided. Then, a immersion type membrane module 12 is disposed above the filter layer 11. This membrane module 12 is immersed in raw water. The membrane module 12 is composed of a number of hollow fiber membranes, and has a structure in which raw water permeates from the outside to the inside of the hollow fiber membrane, and the secondary side thereof is connected to the treated water outflow pipe 13. ing. Further, when performing filtration by the membrane module 12, it is necessary to generate a differential pressure for allowing treated water to permeate from the outside to the inside of the hollow fiber membrane. In this system, the treated water is sucked by the suction pump 15 that has been used.

【0010】図中、16は処理水を一時貯留させるため
の処理水槽であり、17は膜モジュール12を逆洗する
ためのポンプである。また、19は浄水操作を停止して
濾過塔10を洗浄する際に濾層11を流動させる空気を
吹き込むための散気管であり、20は散気管19へ空気
を送るブロアーである。そして、21は濾過塔10を洗
浄した際に発生する洗浄排水を排出するためのトラフで
ある。
In FIG. 1, reference numeral 16 denotes a treatment water tank for temporarily storing treated water, and reference numeral 17 denotes a pump for back washing the membrane module 12. Reference numeral 19 denotes an air diffuser for blowing air for flowing the filter layer 11 when the water purification operation is stopped and the filtration tower 10 is washed, and reference numeral 20 denotes a blower for sending air to the air diffuser 19. Reference numeral 21 denotes a trough for discharging washing wastewater generated when the filtration tower 10 is washed.

【0011】上記の構成による装置による浄水処理は次
のように行われる。凝集沈澱処理がなされた原水が濾過
塔10の下部に導入され、上昇して濾層11を通過す
る。濾層11には粒状の活性炭が充填されており、この
活性炭の表面には過去の通水中に繁殖した微生物が着生
しているので、濾層11内においては、アンモニアや界
面活性剤などの化学物質が吸着されると共に、有機物の
分解・除去も行われる。濾層11を通過した水はポンプ
15によって吸引されている膜モジュール12の中空糸
膜を透過し、処理水流出管13を経由して処理水槽に一
時貯留される。
[0011] The water purification treatment by the apparatus having the above configuration is performed as follows. The raw water subjected to the coagulation and sedimentation treatment is introduced into the lower part of the filtration tower 10 and rises and passes through the filtration layer 11. The filter layer 11 is filled with granular activated carbon, and on the surface of the activated carbon, microorganisms that have propagated in the past water have settled. The chemical substances are adsorbed and the organic substances are decomposed and removed. The water that has passed through the filter layer 11 passes through the hollow fiber membrane of the membrane module 12 that is sucked by the pump 15 and is temporarily stored in the treated water tank via the treated water outflow pipe 13.

【0012】このような濾過操作を長時間継続している
と、活性炭が充填されている濾層11内に懸濁物か捕捉
さて付着し、また、膜モジュール12の中空糸膜の外面
にも濾層11から漏出した生物や懸濁物か付着し、それ
らの付着量がある限度を超えると、濾過抵抗が大きくな
って所定の濾過速度を維持することができなくなる。こ
のため、上記のような状態になった場合には、原水の供
給を停止し、両者の洗浄を同時に並行して行う。
If such a filtration operation is continued for a long time, the suspended matter is trapped and adhered in the filter layer 11 filled with the activated carbon, and also on the outer surface of the hollow fiber membrane of the membrane module 12. If the organisms or suspended matter leaked from the filter layer 11 adhere to the filter, and if the amount of the adhered substance exceeds a certain limit, the filtration resistance increases and the predetermined filtration rate cannot be maintained. For this reason, when it becomes the above-mentioned state, the supply of the raw water is stopped, and both of them are washed at the same time.

【0013】まず、濾層11を洗浄するために、吸引ポ
ンプ15を停止し、弁14を閉にした後、ブロアー20
を起動して散気管19から濾層11内へ空気を吹き込
む。また、弁22を開にし、逆洗用ポンプ17を起動し
た後、弁23を開にして一時貯留されている処理水を洗
浄水として濾過塔10の底部へ導入する。次いで、膜モ
ジュール12を洗浄するために、弁18を開にして一時
貯留されている処理水を洗浄水として膜モジュール12
の中空糸膜の中へ送り込む。
First, in order to wash the filter layer 11, the suction pump 15 is stopped and the valve 14 is closed.
Is started to blow air from the air diffuser 19 into the filter layer 11. After the valve 22 is opened and the backwashing pump 17 is started, the valve 23 is opened and the temporarily stored treated water is introduced into the bottom of the filtration tower 10 as washing water. Next, in order to wash the membrane module 12, the valve 18 is opened and the temporarily stored treated water is used as washing water to clean the membrane module 12.
Into the hollow fiber membrane.

【0014】濾層11においては、吹き込まれた空気に
よって活性炭が流動し、その付着物が剥離する。また、
膜モジュール12においては、洗浄水の導入によって中
空糸膜内の水が外側に逆流し、散気管19から吹き込ま
れる空気によって中空糸膜のエアスクラビングが行われ
るので、中空糸膜の付着物が剥離する。濾層11の活性
炭および膜モジュール12の中空糸膜から剥離した付着
物によって汚染された水は洗浄排水用トラフ21を溢流
して排出し、浄水池へ送られる。
In the filter layer 11, the activated carbon flows by the blown air, and the deposits are separated. Also,
In the membrane module 12, the water in the hollow fiber membrane flows backward by the introduction of the washing water, and air scrubbing of the hollow fiber membrane is performed by the air blown from the diffuser pipe 19. I do. The water contaminated by the activated carbon of the filter layer 11 and the deposits separated from the hollow fiber membrane of the membrane module 12 overflows the washing / draining trough 21 and is discharged therefrom, and sent to a water purification tank.

【0015】そして、濾層11の活性炭および膜モジュ
ール12の中空糸膜が清浄になった時点で、ブロアー2
0および逆洗用ポンプ17を停止し、各弁を濾過操作時
の状態に戻した後、原水の供給を開始し、吸引ポンプ1
5を起動して濾過操作に移行する。
When the activated carbon of the filter layer 11 and the hollow fiber membrane of the membrane module 12 have been cleaned, the blower 2
0, the backwash pump 17 is stopped, and each valve is returned to the state at the time of the filtration operation.
5 is started and it shifts to a filtration operation.

【0016】このように、本発明に係る上記の装置は、
濾過塔10内に濾層11と膜モジュール12を備えてお
り、一つの装置内に二つの機能が収められているので、
所要設置面積が小さく、狭小な場所にも設置することが
できると言う利点を有する外に、濾過塔10および膜モ
ジュール12を洗浄する際に必要な空気の使用量が少量
でよいと言う利点をも有する。
As described above, the above device according to the present invention comprises:
Since a filtration layer 10 and a membrane module 12 are provided in a filtration tower 10 and two functions are contained in one apparatus,
In addition to having the advantage that the required installation area is small and that it can be installed even in a small place, it also has the advantage that the amount of air required for cleaning the filtration tower 10 and the membrane module 12 can be small. Also have.

【0017】すなわち、第2の濾過装置が別途に設置さ
れている従来の浄水処理装置において、第2の濾過装置
を洗浄する際には、洗浄水と共に底部から吹き込む空気
が必要であるが、本発明に係る上記の装置の装置におい
ては、濾層11の上に膜モジュール12が配置されてい
るので、散気管19から吹き込んで濾層11を流動させ
た空気が、その上方において、再び、膜モジュール12
をエアスクラビングするための空気として利用されるの
で、膜モジュール12の洗浄に要する分の空気量が節減
される。
That is, in the conventional water treatment apparatus in which the second filtration device is separately installed, when the second filtration device is washed, air blown from the bottom together with the washing water is required. In the apparatus of the above-described apparatus according to the present invention, since the membrane module 12 is disposed on the filter layer 11, the air blown from the diffuser pipe 19 to flow the filter layer 11 flows again above the filter layer. Module 12
Is used as air for air scrubbing, so that the amount of air required for cleaning the membrane module 12 is reduced.

【0018】なお、膜モジュール12に用いる膜は、必
ずしも、中空糸膜でなくてもよく、平膜などを用いるこ
ともできる。
The membrane used for the membrane module 12 is not necessarily a hollow fiber membrane, but may be a flat membrane or the like.

【0019】また、膜モジュール12による濾過に際
し、膜の内側と外側の間に差圧を発生させる方式は、上
記のような吸引式でも、水位差利用式であってもよい。
The method of generating a pressure difference between the inside and the outside of the membrane during filtration by the membrane module 12 may be the above-mentioned suction type or the type utilizing a difference in water level.

【0020】[0020]

【発明の効果】本発明においては、上向流式の濾過塔内
に濾層が設けられると共に、この濾層の上方に浸漬型の
膜モジュールが配設され、濾過塔内に二つの濾過部を有
する構成になっているので、所要設置面積が小さく、狭
小な場所にも設置することができる。
According to the present invention, a filter layer is provided in an upward-flow type filtration tower, and a immersion type membrane module is disposed above the filter layer. , The required installation area is small, and it can be installed in a small place.

【0021】さらに、濾過塔内には濾層と膜モジュール
が上下に配置されており、この両者を同じ塔内で同時に
洗浄することができるので、濾層を洗浄するために吹き
込んだ空気を膜モジュールの洗浄にも利用することがで
き、ブロアーの小型化されると共に、動力が節減され
る。
Further, a filter layer and a membrane module are arranged vertically in the filter tower, and both can be washed simultaneously in the same tower. Therefore, air blown for washing the filter layer is removed by the membrane. It can also be used for cleaning the module, reducing the size of the blower and saving power.

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

【図1】本発明の浄水処理装置に係る一例の構成を示す
図である。
FIG. 1 is a diagram showing a configuration of an example of a water purification apparatus according to the present invention.

【図2】従来の高度処理システムによる浄水処理装置に
係る構成の一例を示す図である。
FIG. 2 is a diagram showing an example of a configuration relating to a water purification treatment device using a conventional advanced treatment system.

【符号の説明】[Explanation of symbols]

10 濾過塔 11 濾層 12 膜モジュール 13 処理水流出管 15 吸引ポンプ 16 処理水槽 17 逆洗用ポンプ 19 散気管 20 ブロアー 21 洗浄排水用のトラフ DESCRIPTION OF SYMBOLS 10 Filtration tower 11 Filtration layer 12 Membrane module 13 Treated water outflow pipe 15 Suction pump 16 Treatment water tank 17 Backwash pump 19 Air diffuser 20 Blower 21 Trough for washing and drainage

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI C02F 9/00 502 C02F 9/00 502E 504B 504 B01D 23/14 ──────────────────────────────────────────────────の Continuation of front page (51) Int.Cl. 6 Identification code FI C02F 9/00 502 C02F 9/00 502E 504B 504 B01D 23/14

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 上水道の浄水処理装置において、上向流
式の濾過塔内に活性炭が充填された濾層が設けられ、こ
の濾層の上方に浸漬型の膜モジュールが配設されている
ことを特徴とする浄水処理装置。
1. A water purification system for a water supply system, wherein a filter layer filled with activated carbon is provided in an upward flow type filtration tower, and a immersion type membrane module is disposed above the filter layer. A water purification treatment device characterized by the above-mentioned.
JP8263114A 1996-10-03 1996-10-03 Water purifying treatment device Pending JPH10109095A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8263114A JPH10109095A (en) 1996-10-03 1996-10-03 Water purifying treatment device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8263114A JPH10109095A (en) 1996-10-03 1996-10-03 Water purifying treatment device

Publications (1)

Publication Number Publication Date
JPH10109095A true JPH10109095A (en) 1998-04-28

Family

ID=17385031

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8263114A Pending JPH10109095A (en) 1996-10-03 1996-10-03 Water purifying treatment device

Country Status (1)

Country Link
JP (1) JPH10109095A (en)

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002001375A (en) * 2000-06-26 2002-01-08 Aoki Denki Kogyo Kk Waste water treating apparatus
JP2002292254A (en) * 2001-03-29 2002-10-08 Yuasa Corp Dip type membrane filtration apparatus
JP2002336660A (en) * 2001-05-18 2002-11-26 Yuasa Corp Immersion type membrane filtration equipment and immersion type membrane filtration method
JP2003513785A (en) * 1999-11-18 2003-04-15 ゼノン、エンバイロンメンタル、インコーポレーテッド Immersion type membrane filtration system and overflow treatment method
JP2004000983A (en) * 2003-06-20 2004-01-08 Aoki Denki Kogyo Kk Waste water treatment apparatus
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JP2003513785A (en) * 1999-11-18 2003-04-15 ゼノン、エンバイロンメンタル、インコーポレーテッド Immersion type membrane filtration system and overflow treatment method
JP2002001375A (en) * 2000-06-26 2002-01-08 Aoki Denki Kogyo Kk Waste water treating apparatus
JP2002292254A (en) * 2001-03-29 2002-10-08 Yuasa Corp Dip type membrane filtration apparatus
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JP2004000983A (en) * 2003-06-20 2004-01-08 Aoki Denki Kogyo Kk Waste water treatment apparatus
JP2005095818A (en) * 2003-09-26 2005-04-14 Sanki Eng Co Ltd Water purification method and water purification system
JP2005169288A (en) * 2003-12-11 2005-06-30 Kokudo Sogo Kensetsu Kk Automatic water cleaning device and water cleaning method
JP2005279408A (en) * 2004-03-29 2005-10-13 Hanshin Water Supply Authority Media and membrane filtration combined filter equipment
JP4672993B2 (en) * 2004-03-29 2011-04-20 阪神水道企業団 Media and membrane filtration combined filtration equipment
JP2006116376A (en) * 2004-10-19 2006-05-11 Chubu Electric Power Co Inc Waste water treatment system
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US7875181B2 (en) 2005-07-06 2011-01-25 Glowtec Bio Pte Ltd Water treatment process
KR100912268B1 (en) 2008-12-15 2009-08-17 유네코개발 주식회사 Water purification apparatus using adsorption and filtration of biological activated carbon and cleansing method thereof
KR101109762B1 (en) * 2009-06-29 2012-02-15 유림엔마텍(주) water treatment method and the apparatus for purified water using natural water
CN103803667A (en) * 2014-02-28 2014-05-21 环境保护部南京环境科学研究所 Two-stage desert sand filter and wastewater treatment method thereof
WO2021176772A1 (en) * 2020-03-02 2021-09-10 日立造船株式会社 Water purification system and water purification method
JP2021137678A (en) * 2020-03-02 2021-09-16 日立造船株式会社 Water purification system and water purification method
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