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JPH11244877A - Sewage septic tank with built-in membrane separation vessel - Google Patents

Sewage septic tank with built-in membrane separation vessel

Info

Publication number
JPH11244877A
JPH11244877A JP5496598A JP5496598A JPH11244877A JP H11244877 A JPH11244877 A JP H11244877A JP 5496598 A JP5496598 A JP 5496598A JP 5496598 A JP5496598 A JP 5496598A JP H11244877 A JPH11244877 A JP H11244877A
Authority
JP
Japan
Prior art keywords
tank
sewage
membrane
membrane separation
vessel
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
JP5496598A
Other languages
Japanese (ja)
Inventor
Hideaki Tsukahara
秀明 塚原
Toshimasa Umehara
敏正 梅原
Yasuhiro Ishii
康弘 石井
Satoshi Arai
聡 荒井
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.)
Resonac Corp
Original Assignee
Hitachi Chemical 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 Hitachi Chemical Co Ltd filed Critical Hitachi Chemical Co Ltd
Priority to JP5496598A priority Critical patent/JPH11244877A/en
Publication of JPH11244877A publication Critical patent/JPH11244877A/en
Pending legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)
  • Treatment Of Biological Wastes In General (AREA)

Abstract

PROBLEM TO BE SOLVED: To enable the removal of ammoniacal nitrogen, nitrate nitrogen, etc., in addition to the decrease of BOD by providing a sewage septic tank having at least intermittent aerator with a membrane sepn. vessel separated from this intermittent aerator and providing the septic tank with an air diffusion pipe for applying air bubbles to the membrane in this membrane sepn. vessel from below the membrane at all times. SOLUTION: The sewage flowing in from an inflow port 9 is subjected to the removal of the extraneous matter and coarse solids, etc., in the sewage by an aeration type screen and is admitted into a flow rate regulation vessel 11. Next, the sewage is advected to a metering measure 13 and is subjected to flow rate regulation and thereafter, the small extraneous matter and coarse solids, etc., in the sewage are removed by a fine mesh screen 14 and is then admitted into the intermittent aerator 5. The sewage is mixed with the liquid mixture flowing in from the membrane sepn. vessel 6 therein to repeat aeration and agitation and the oxygen is supplied from the air diffusion pipe 3, etc., by which the decrease of the BOD in the raw water and the nitrification of the ammonia nitrogen and nitrate nitrogen are effected. The sewage flowing over to the membrane sepn. vessel 6 from the intermittent aerator 5 is subjected to permeation filtration with the membrane 1 and is released to the outside of the system.

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、汚水浄化槽、特に
その汚水処理工程の一部として使用される間欠ばっ気槽
および膜分離槽を有する膜分離槽内蔵型汚水浄化槽に関
する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a sewage treatment tank, and more particularly to a sewage treatment tank with a built-in membrane separation tank having an intermittent aeration tank and a membrane separation tank used as a part of the sewage treatment process.

【0002】[0002]

【従来の技術】従来の汚水浄化槽について図4を用いて
説明すると、膜1を用いた汚水浄化槽は連続的にばっ気
を行う槽内(以下ばっ気槽2という)に膜1が設置され
ている。該膜1の設置場所は散気管3の上方となってお
り、散気管からの好気性生物処理及び、膜の洗浄が行わ
れ膜の目詰まりを防いでいる。流入口4から流入した水
は、該ばっ気槽内で生物化学的酸素要求量(以下BOD
という)を低減し膜によって浮遊物質(以下SSとい
う)の濾過を行う。
2. Description of the Related Art A conventional sewage purifying tank will be described with reference to FIG. 4. A sewage purifying tank using a membrane 1 has a membrane 1 installed in a tank which continuously aerates (hereinafter referred to as an aeration tank 2). I have. The installation location of the membrane 1 is above the air diffuser 3, and aerobic biological treatment from the air diffuser and washing of the membrane are performed to prevent clogging of the membrane. Water flowing from the inflow port 4 is subjected to biochemical oxygen demand (hereinafter referred to as BOD) in the aeration tank.
) And the suspended substance (hereinafter referred to as SS) is filtered by the membrane.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、ばっ気
槽2においてBODは低減できるがアンモニア性窒素,
硝酸性窒素及び亜硝酸性窒素などの除去はできない。
However, in the aeration tank 2, the BOD can be reduced, but the ammonia nitrogen,
Nitrate nitrogen and nitrite nitrogen cannot be removed.

【0004】本発明は、以上のような課題に鑑み、BO
Dの低減の他にアンモニア性窒素、硝酸性窒素及び亜硝
酸性窒素などの除去を行い且つ安定した処理水質および
適正な放流水量を得る膜分離槽内蔵型汚水浄化槽を提供
することを目的とする。
[0004] In view of the above problems, the present invention provides a BO
An object of the present invention is to provide a sewage purification tank with a built-in membrane separation tank that removes ammonia nitrogen, nitrate nitrogen, nitrite nitrogen, etc. in addition to reducing D, and obtains a stable treated water quality and an appropriate amount of discharged water. .

【0005】[0005]

【課題を解決するための手段】本発明は、図1に示すよ
うに、少なくとも間欠ばっ気槽5を有する汚水浄化槽で
あって、前記間欠ばっ気槽5とは分離した膜分離槽6を
設けると共に、該膜分離槽6内の膜1の下方より常時気
泡を当てる散気管3を設けたことを特徴とする。
The present invention, as shown in FIG. 1, is a sewage purification tank having at least an intermittent aeration tank 5, in which a membrane separation tank 6 separated from the intermittent aeration tank 5 is provided. In addition, an air diffuser 3 for constantly applying air bubbles from below the membrane 1 in the membrane separation tank 6 is provided.

【0006】本発明では、ばっ気槽を間欠ばっ気槽5と
することによってBODの低減の他にアンモニア性窒
素、硝酸性窒素及び亜硝酸性窒素などの除去を行うこと
を可能としたものである。しかしながら、ばっ気槽を単
純に間欠ばっ気槽5に変更すればアンモニア性窒素、硝
酸性窒素及び亜硝酸性窒素などの除去は可能となるもの
の、ばっ気停止時においては膜1の洗浄が不可能となる
ため膜1が目詰まりし適正な放流水量が得られなくな
る、もしくは、適正な処理水量を得るために膜を大きく
する必要がある。そこで本発明では、更に、間欠ばっ気
槽5と膜分離槽6を仕切板7で分離させ、膜分離槽6の
底部に散気管3を設けて常時空気を送ることによって、
膜1の目詰まりを防止し、且つ膜1を大きくする必要も
なくしたものである。
In the present invention, the intermittent aeration tank 5 is used as the aeration tank to reduce BOD and to remove ammonia nitrogen, nitrate nitrogen, nitrite nitrogen and the like. is there. However, if the aeration tank is simply changed to the intermittent aeration tank 5, it is possible to remove ammonia nitrogen, nitrate nitrogen, nitrite nitrogen, etc., but when the aeration is stopped, cleaning of the membrane 1 is not possible. Since it becomes possible, the membrane 1 is clogged and an appropriate amount of discharged water cannot be obtained, or the membrane needs to be enlarged in order to obtain an appropriate amount of treated water. Therefore, in the present invention, the intermittent aeration tank 5 and the membrane separation tank 6 are further separated by a partition plate 7, and the air diffuser 3 is provided at the bottom of the membrane separation tank 6 to constantly send air.
This prevents clogging of the film 1 and eliminates the need to increase the size of the film 1.

【0007】[0007]

【発明の実施の形態】次に本発明の実施形態について説
明する。図1において、5は間欠ばっ気槽であり、この
間欠ばっ気槽5と膜分離槽6を仕切板7で分離させる。
膜分離槽6の底部には、散気管3を設けて常時空気を送
るよう構成されている。8は水中撹拌機、16は混合液
移送ポンプである。
Next, an embodiment of the present invention will be described. In FIG. 1, reference numeral 5 denotes an intermittent aeration tank, and the intermittent aeration tank 5 and the membrane separation tank 6 are separated by a partition plate 7.
A diffuser 3 is provided at the bottom of the membrane separation tank 6 so that air is always sent. 8 is a submersible agitator, and 16 is a mixed liquid transfer pump.

【0008】本発明における間欠ばっ気槽5とは、汚水
を浄化する方法の1つとして古くから行われておりその
仕組について、図1を用いて説明すると、図1において
原水は流入口4より間欠ばっ気槽5内に流入する。その
原水は固液分離処理を行った一次処理または固液分離処
理及び好気性生物処理を行った二次処理水である。
The intermittent aeration tank 5 in the present invention has been used for a long time as one of the methods for purifying sewage, and the mechanism thereof will be described with reference to FIG. 1. In FIG. It flows into the intermittent aeration tank 5. The raw water is a primary treatment that has undergone a solid-liquid separation treatment or a secondary treatment water that has undergone a solid-liquid separation treatment and an aerobic biological treatment.

【0009】流入した原水は槽内において、膜分離槽6
から流入する混合液(好気性生物処理を終えた汚水)と
混合され、ばっ気と撹拌が繰り返され、ばっ気時には、
膜の中心から離れた位置にあるブロワ、エアコンプレッ
サ等に接続された散気筒、散気管3、ディフューザ等か
ら酸素(空気中の酸素)が供給されることにより、原水
中のBODの低減と、アンモニア性窒素と有機性窒素の
硝化が行われ、撹拌時には、間欠ばっ気槽の長手方向中
央垂直断面部の底部付近に設置された水中撹拌機8によ
り長手方向に水流が生じ、槽内の活性汚泥が十分に撹拌
され、ばっ気時に生成した硝酸性窒素と亜硝酸性窒素の
脱窒素が行われると共にBODの低減が行われる。
The raw water that has flowed into the tank is supplied to a membrane separation tank 6.
Mixed with the mixed liquid (sewage water that has undergone aerobic biological treatment), and aeration and agitation are repeated.
Oxygen (oxygen in the air) is supplied from a diffuser, diffuser 3, diffuser, etc. connected to a blower, air compressor, etc., at a position away from the center of the membrane, thereby reducing BOD in raw water, The nitrification of ammoniacal nitrogen and organic nitrogen is carried out, and at the time of stirring, a water flow is generated in the longitudinal direction by a submerged stirrer 8 installed near the bottom of the longitudinally central vertical section of the intermittent aeration tank, and the activity in the tank is increased. Sludge is sufficiently agitated, and nitrate nitrogen and nitrite nitrogen generated during aeration are denitrified and BOD is reduced.

【0010】次に膜分離槽6について一例を示すと、図
1に示すように原水(一次処理水又は二次処理水を更に
好気性生物処理や濾過等を行った三次処理水)を膜1に
通すことによって原水に含まれるSS(浮遊物質)を除
去することができる。膜1は散気管3の上方に設置さ
れ、散気管3からの気泡によって常時その表面を洗浄さ
れ、目詰まりの発生を防止している。
Next, an example of the membrane separation tank 6 will be described. As shown in FIG. 1, raw water (tertiary treated water obtained by further performing aerobic biological treatment or filtration of primary treated water or secondary treated water) is applied to the membrane 1 as shown in FIG. To remove SS (suspended matter) contained in the raw water. The membrane 1 is installed above the air diffuser 3, and its surface is constantly cleaned by bubbles from the air diffuser 3 to prevent clogging.

【0011】本発明で用いる間欠ばっ気槽と分離した膜
分離槽6とは、図1に示すように、槽内を仕切板7で仕
切ることにより分離したもの、または図2のように槽本
体を独立(間欠ばっ気槽5と膜分離槽6を独立)させ、
移流管21にて接続したものである。
The intermittent aeration tank and the separated membrane separation tank 6 used in the present invention are separated by partitioning the inside of the tank with a partition plate 7 as shown in FIG. 1, or the tank body as shown in FIG. Independently (intermittent aeration tank 5 and membrane separation tank 6 are independent),
It is connected by the advection tube 21.

【0012】次に、本発明のより具体的な実施例につい
て図3に沿って説明する。図3は図1に示した本発明の
排水処理装置を組込んだ汚水浄化槽全体の一実施例であ
る。
Next, a more specific embodiment of the present invention will be described with reference to FIG. FIG. 3 shows an embodiment of the entire sewage purification tank incorporating the wastewater treatment apparatus of the present invention shown in FIG.

【0013】流入口9から流入した汚水はばっ気型スク
リーン(図示省略)により汚水中の夾雑物および粗大な
固形物などを除去され、流量調整槽11に流入する。な
お、ばっ気型スクリーンは荒目スクリーンを代わりに使
用してもよい。
The sewage flowing from the inlet 9 is subjected to an aeration screen (not shown) to remove impurities and coarse solids in the sewage, and flows into the flow control tank 11. Note that the aerated screen may use a coarse screen instead.

【0014】流量調整槽に流入した汚水は流量調整ポン
プ12により計量マス13に移流され、計画汚水量に流
量調整された後、微細目スクリーン14で汚水中の小さ
な夾雑物および固形物などを除去後、間欠ばっ気槽5に
流入する。なお、微細目スクリーンで除去された汚水中
の小さな夾雑物および固形物などは汚泥貯留槽15に貯
留される。
The sewage flowing into the flow control tank is transferred to the measuring mass 13 by the flow control pump 12 and adjusted to the planned sewage amount. Then, the fine screen 14 removes small impurities and solids in the sewage. Thereafter, it flows into the intermittent aeration tank 5. The small contaminants and solids in the sewage removed by the fine screen are stored in the sludge storage tank 15.

【0015】間欠ばっ気槽5に流入した原水は槽内にお
いて、膜分離槽6から流入する混合液と混合され、ばっ
気と撹拌が繰り返され、ばっ気時には、槽の中心から離
れた位置にあるブロワ、エアコンプレッサ等に接続され
た散気筒、散気管3、ディフューザ等から酸素が供給さ
れることにより、原水中のBODの低減と、アンモニア
性窒素と有機性窒素の硝化が行われ、撹拌時には、間欠
ばっ気槽の長手方向中央垂直断面部の底部付近に設置さ
れた水中撹拌機8により長手方向に水流が生じ、槽内の
活性汚泥が十分に撹拌され、ばっ気時に生成した硝酸性
窒素と亜硝酸性窒素の脱窒素が行われると共にBODの
低減が行われる。
The raw water flowing into the intermittent aeration tank 5 is mixed with the mixed solution flowing from the membrane separation tank 6 in the tank, and is repeatedly aerated and agitated. Oxygen is supplied from a diffuser, diffuser 3, diffuser, etc. connected to a blower, air compressor, etc., thereby reducing BOD in raw water and nitrifying ammoniacal nitrogen and organic nitrogen. Occasionally, a water flow is generated in the longitudinal direction by a submersible agitator 8 installed near the bottom of the longitudinally central vertical section of the intermittent aeration tank, and the activated sludge in the tank is sufficiently stirred, and the nitric acid generated during aeration is generated. The denitrification of nitrogen and nitrite nitrogen is performed, and the BOD is reduced.

【0016】間欠ばっ気槽5から膜分離槽6に越流した
汚水は、膜1により浸透濾過し、ポンプ(図示省略)に
より消毒筒17へ移流し、消毒後、放流ポンプ槽18に
流出し、放流ポンプ19を稼働させることにより系外に
放流される。ここで、膜分離槽6は散気管3によって常
時空気を送られ、気泡により洗浄される。また、膜分離
槽6内の混合液は混合液移送ポンプ16等により間欠ば
っ気槽に返送され、前述した脱窒を行う。更に、汚泥返
送用ポンプ20などを定期的に作動させ、汚泥貯留槽1
5に返送汚泥を移送し、間欠ばっ気槽内の汚泥濃度を制
御する。
The sewage flowing from the intermittent aeration tank 5 to the membrane separation tank 6 is permeated and filtered by the membrane 1, transferred to a disinfecting cylinder 17 by a pump (not shown), and discharged to a discharge pump tank 18 after disinfection. , And is discharged out of the system by operating the discharge pump 19. Here, the membrane separation tank 6 is constantly supplied with air by the air diffuser 3 and is washed by air bubbles. The mixed liquid in the membrane separation tank 6 is returned to the intermittent aeration tank by the mixed liquid transfer pump 16 or the like, and performs the above-described denitrification. Further, the sludge return pump 20 and the like are periodically operated to activate the sludge storage tank 1.
The returned sludge is transferred to 5, and the sludge concentration in the intermittent aeration tank is controlled.

【0017】[0017]

【発明の効果】本発明により、安定した処理性能および
良好な放流水質を得る膜分離槽内蔵型汚水浄化槽が提供
される。すなわち、間欠ばっ気槽によってBODの低減
の他にアンモニア性窒素、硝酸性窒素及び亜硝酸性窒素
などの除去が行われ、膜分離槽によってSSの除去が行
われる。更に間欠ばっ気槽と分離した膜分離槽の底部に
散気管を設けて常時空気を送ることによって、膜の目詰
まりを防止し且つ膜を大きくする必要もなくなる。
According to the present invention, there is provided a sewage purifying tank with a built-in membrane separation tank capable of obtaining a stable treatment performance and good discharge water quality. That is, in addition to the reduction of BOD, the removal of ammonia nitrogen, nitrate nitrogen, nitrite nitrogen and the like is performed by the intermittent aeration tank, and the removal of SS is performed by the membrane separation tank. Further, by providing an air diffuser at the bottom of the membrane separation tank separated from the intermittent aeration tank and constantly sending air, it is possible to prevent clogging of the membrane and eliminate the need to increase the size of the membrane.

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

【図1】本発明の一実施例である膜分離槽内蔵汚水浄化
槽の部分的な概略図である。
FIG. 1 is a partial schematic view of a sewage purification tank with a built-in membrane separation tank according to one embodiment of the present invention.

【図2】本発明の一実施例である膜分離槽内蔵型汚水浄
化槽の部分的な概略図である。
FIG. 2 is a partial schematic view of a sewage purification tank with a built-in membrane separation tank according to one embodiment of the present invention.

【図3】本発明の一実施例である間欠ばっ気槽、膜分離
槽を含む排水処理装置の概略図である。
FIG. 3 is a schematic diagram of a wastewater treatment apparatus including an intermittent aeration tank and a membrane separation tank according to one embodiment of the present invention.

【図4】従来の技術の一例である膜分離槽内蔵型汚水浄
化槽の部分的な概略図である。
FIG. 4 is a partial schematic view of a sewage purification tank with a built-in membrane separation tank, which is an example of a conventional technique.

【符号の説明】[Explanation of symbols]

1…膜、2…ばっ気槽、3…散気管、4…流入口、5…
間欠ばっ気槽、6…膜分離槽、7…仕切板、8…水中撹
拌機、9…流入口、11…流量調整槽、12…流量調整
ポンプ、13…計量マス、14…微細目スクリーン、1
5…汚泥貯留槽、16…混合液移送ポンプ、17…消毒
筒、18…放流ポンプ槽、19…放流ポンプ、20…汚
泥返送用ポンプ、21…移流管。
DESCRIPTION OF SYMBOLS 1 ... Membrane, 2 ... Aeration tank, 3 ... Aerator, 4 ... Inlet, 5 ...
Intermittent aeration tank, 6: membrane separation tank, 7: partition plate, 8: underwater stirrer, 9: inflow port, 11: flow control tank, 12: flow control pump, 13: measuring mass, 14: fine mesh screen, 1
5: Sludge storage tank, 16: Mixed liquid transfer pump, 17: Disinfection cylinder, 18: Discharge pump tank, 19: Discharge pump, 20: Sludge return pump, 21: Transfer pipe.

フロントページの続き (72)発明者 荒井 聡 茨城県下館市大字下江連1250番地 日立化 成工業株式会社結城工場内Continued on the front page (72) Inventor Satoshi Arai 1250 Shimoe-ren, Shimodate-shi, Ibaraki Pref.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】少なくとも間欠ばっ気槽を有する汚水浄化
槽であって、前記間欠ばっ気槽とは分離した膜分離槽を
設けると共に、該膜分離槽内の膜の下方より常時気泡を
当てる散気管を設けたことを特徴とする膜分離槽内蔵型
汚水浄化槽。
1. A sewage purifying tank having at least an intermittent aeration tank, comprising a membrane separation tank separate from the intermittent aeration tank, and an air diffuser pipe constantly blowing air bubbles from below the membrane in the membrane separation tank. A sewage treatment tank with a built-in membrane separation tank, which is provided with:
【請求項2】間欠ばっ気槽と分離した膜分離槽は、槽内
を仕切板で仕切ることにより分離したものであることを
特徴とする請求項1記載の膜分離槽内蔵型汚水浄化槽。
2. The sewage purification tank with a built-in membrane separation tank according to claim 1, wherein the membrane separation tank separated from the intermittent aeration tank is separated by partitioning the inside of the tank with a partition plate.
【請求項3】間欠ばっ気槽と分離した膜分離槽は、槽本
体を独立させたものであることを特徴とする請求項1記
載の膜分離槽内蔵型汚水浄化槽。
3. The sewage purification tank with built-in membrane separation tank according to claim 1, wherein the membrane separation tank separated from the intermittent aeration tank has a tank main body made independent.
JP5496598A 1998-03-06 1998-03-06 Sewage septic tank with built-in membrane separation vessel Pending JPH11244877A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5496598A JPH11244877A (en) 1998-03-06 1998-03-06 Sewage septic tank with built-in membrane separation vessel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5496598A JPH11244877A (en) 1998-03-06 1998-03-06 Sewage septic tank with built-in membrane separation vessel

Publications (1)

Publication Number Publication Date
JPH11244877A true JPH11244877A (en) 1999-09-14

Family

ID=12985383

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5496598A Pending JPH11244877A (en) 1998-03-06 1998-03-06 Sewage septic tank with built-in membrane separation vessel

Country Status (1)

Country Link
JP (1) JPH11244877A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6863817B2 (en) 2002-12-05 2005-03-08 Zenon Environmental Inc. Membrane bioreactor, process and aerator
WO2009112618A1 (en) * 2008-03-12 2009-09-17 Universisdad De Alicante Compact system for treating household waste water
WO2020015458A1 (en) * 2018-07-17 2020-01-23 厦门理工学院 Treatment method for waste water from livestock and poultry
WO2020015435A1 (en) * 2018-07-17 2020-01-23 厦门理工学院 Method for treating domestic wastewater
US11286186B2 (en) 2018-07-17 2022-03-29 Xiamen University Of Technology Method for treating dye wastewater
US11485656B2 (en) 2018-07-17 2022-11-01 Xiamen University Of Technology Method for treating heavy metal wastewater

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6863817B2 (en) 2002-12-05 2005-03-08 Zenon Environmental Inc. Membrane bioreactor, process and aerator
US7022236B2 (en) 2002-12-05 2006-04-04 Zenon Environmental Inc. Membrane bioreactor, process and aerator
WO2009112618A1 (en) * 2008-03-12 2009-09-17 Universisdad De Alicante Compact system for treating household waste water
ES2330824A1 (en) * 2008-03-12 2009-12-15 Universidad De Alicante Compact system for treating household waste water
ES2330824B2 (en) * 2008-03-12 2011-05-17 Universidad De Alicante COMPACT SYSTEM FOR TREATMENT OF RESIDUAL WATERS OF DOMESTIC ORIGIN.
WO2020015458A1 (en) * 2018-07-17 2020-01-23 厦门理工学院 Treatment method for waste water from livestock and poultry
WO2020015435A1 (en) * 2018-07-17 2020-01-23 厦门理工学院 Method for treating domestic wastewater
US11286186B2 (en) 2018-07-17 2022-03-29 Xiamen University Of Technology Method for treating dye wastewater
US11352278B2 (en) 2018-07-17 2022-06-07 Xiamen University Of Technology Method for treating domestic sewage
US11485656B2 (en) 2018-07-17 2022-11-01 Xiamen University Of Technology Method for treating heavy metal wastewater

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