JPH07303895A - Water treatment apparatus - Google Patents
Water treatment apparatusInfo
- Publication number
- JPH07303895A JPH07303895A JP6100319A JP10031994A JPH07303895A JP H07303895 A JPH07303895 A JP H07303895A JP 6100319 A JP6100319 A JP 6100319A JP 10031994 A JP10031994 A JP 10031994A JP H07303895 A JPH07303895 A JP H07303895A
- Authority
- JP
- Japan
- Prior art keywords
- water
- treated
- flow path
- tank
- solid
- 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
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Activated Sludge Processes (AREA)
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、有機性廃水などの被処
理水の生物処理と固液分離とを行う水処理装置に関す
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water treatment apparatus for biological treatment of water to be treated such as organic wastewater and solid-liquid separation.
【0002】[0002]
【従来の技術】従来、有機性廃水などの被処理水の生物
処理を行う装置として、比較的深い下向流路と上向流路
とを形成し、この下向流路と上向流路とにわたって被処
理水を循環流動させる循環手段と、下向流路内を下降す
る被処理水に曝気空気を供給する曝気手段とを備えた深
層反応槽が知られている。このような深層反応槽におい
ては、槽内に被処理水を導入して、循環手段により循環
流動させつつ、槽内のDOが硝化・脱窒に適した条件に
なるように曝気空気を吹き込む状態において、槽内の活
性汚泥により被処理水を生物学的に硝化・脱窒してい
る。そして、このようにして硝化・脱窒された槽内の混
合液から活性汚泥を分離するために、浸漬型膜分離装置
などにより固液分離を行っている。2. Description of the Related Art Conventionally, as a device for biological treatment of water to be treated such as organic wastewater, a relatively deep downward flow path and upward flow path are formed, and the downward flow path and the upward flow path are formed. There is known a deep reaction tank provided with a circulation means for circulating and flowing the water to be treated and an aeration means for supplying aeration air to the water to be treated which descends in the downward flow path. In such a deep-layer reaction tank, the aeration air is blown in such a manner that the water to be treated is introduced into the tank and circulated and flowed by the circulation means while the DO in the tank is in a condition suitable for nitrification / denitrification. In the above, the treated water is biologically nitrified and denitrified by the activated sludge in the tank. Then, in order to separate the activated sludge from the mixed liquid in the tank thus nitrified and denitrified, solid-liquid separation is performed by an immersion type membrane separation device or the like.
【0003】[0003]
【発明が解決しようとする課題】しかしながら、上記し
た浸漬型膜分離装置により固液分離を行う場合、膜分離
装置用の膜原水槽を設置するのが従来の技術であり、そ
のため、装置や処理が複雑になるという問題がある。However, when solid-liquid separation is carried out by the above-mentioned immersion type membrane separation apparatus, it is a conventional technique to install a membrane raw water tank for the membrane separation apparatus, and therefore, the apparatus and treatment are performed. Is complicated.
【0004】本発明は上記問題を解決するもので、被処
理水の生物処理と固液分離とを行うことができる簡略な
構成の水処理装置を提供することを目的とするものであ
る。The present invention solves the above problems, and an object of the present invention is to provide a water treatment apparatus having a simple structure capable of performing biological treatment and solid-liquid separation of treated water.
【0005】[0005]
【課題を解決するための手段】上記問題を解決するため
に、本発明の水処理装置は、被処理水を循環流動させる
下向流路と上向流路とを形成し、下向流路内を下降する
被処理水に曝気空気を供給する曝気手段を設けた深層反
応槽に、上向流路内に位置して槽内の被処理水を固液分
離する浸漬型膜分離装置を設けたものである。In order to solve the above problems, the water treatment apparatus of the present invention forms a downward flow passage and an upward flow passage for circulating the water to be treated, and the downward flow passage is formed. A deep-layer reaction tank equipped with aeration means for supplying aeration air to the water to be treated that descends inside is provided with an immersion type membrane separation device located in the upward flow path for solid-liquid separation of the water to be treated in the tank. It is a thing.
【0006】[0006]
【作用】上記構成により、深層反応槽内を循環流動させ
る状態において、被処理水の生物処理と固液分離を行う
ことができる。このとき、下向流路内を下降する被処理
水に曝気手段より曝気空気を供給するようにしたため、
曝気空気は被処理水に巻き込まれて下向流路内を下降し
た後に上向流路内を上昇することになり、下降する曝気
空気中の酸素が被処理水に十分溶解するとともに、上昇
する曝気空気の気泡によって浸漬型膜分離装置の分離膜
表面が洗浄される。With the above structure, biological treatment and solid-liquid separation of the water to be treated can be performed in a state of circulating and flowing in the deep reaction tank. At this time, since aeration air is supplied from the aeration means to the water to be treated descending in the downward flow path,
The aerated air is entrained in the water to be treated and descends in the downward flow path, and then rises in the upward flow path, and the oxygen in the descending aerated air is sufficiently dissolved in the water to be treated and rises. The surface of the separation membrane of the immersion type membrane separation device is washed by the bubbles of the aerated air.
【0007】[0007]
【実施例】以下、本発明の実施例を図面を参照しながら
説明する。図1は本発明の一実施例の水処理装置の全体
構成を示し、1は深層反応槽であって、下向流路2と上
向流路3とで構成されている。上向流路3の外周側には
越流堰4を介してポンプ槽5が設けられていて、このポ
ンプ槽5に、被処理水供給管6より被処理水が供給され
るとともに、上向流路3内の被処理水が越流堰4より越
流するようになっている。Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 shows the overall structure of a water treatment apparatus according to an embodiment of the present invention, in which a deep-layer reaction tank 1 is composed of a downward flow path 2 and an upward flow path 3. A pump tank 5 is provided on the outer peripheral side of the upward flow path 3 via an overflow weir 4, and the water to be treated is supplied to the pump tank 5 from a treated water supply pipe 6 and is directed upward. The water to be treated in the flow path 3 overflows from the overflow weir 4.
【0008】ポンプ槽5は、攪拌ポンプ7などの攪拌手
段を備えた循環管8を介して下向流路2の頂部に連通し
ていて、これにより、ポンプ槽5内の被処理水が攪拌ポ
ンプ7により下向流路2の頂部へ揚水され、下向流路
2、上向流路3を経てポンプ槽5に至る循環路において
循環流動するようになっている。下向流路2の頂部に
は、下向流路2内を下降する被処理水に曝気空気を供給
するエゼクタ9などの曝気手段が設けられている。The pump tank 5 is communicated with the top of the downward flow path 2 through a circulation pipe 8 equipped with a stirring means such as a stirring pump 7, whereby the water to be treated in the pump tank 5 is stirred. The pump 7 pumps water to the top of the downward flow passage 2, and circulates and flows in the circulation passage extending from the downward flow passage 2 and the upward flow passage 3 to the pump tank 5. At the top of the downward flow passage 2, an aeration means such as an ejector 9 for supplying aerated air to the water to be treated that descends in the downward flow passage 2 is provided.
【0009】上向流路3内における上部には、槽内の被
処理水を固液分離する浸漬型膜分離装置10が設けられ
ている。浸漬型膜分離装置10は、管状セラミック分離
膜や濾過膜を配置した平板型分離膜などの膜エレメント
を複数個連結して構成されている。膜分離装置10に
は、透過側に連通して、吸引ポンプ11などの吸引手段
を備えた吸引管12が設けられている。An immersion type membrane separation device 10 for solid-liquid separating the water to be treated in the tank is provided in the upper part of the upward flow path 3. The submerged membrane separation apparatus 10 is configured by connecting a plurality of membrane elements such as a tubular ceramic separation membrane or a flat plate-type separation membrane having a filtration membrane. The membrane separation device 10 is provided with a suction tube 12 that is connected to the permeate side and that is equipped with suction means such as a suction pump 11.
【0010】深層反応槽1の外部には、浸漬型膜分離装
置10により取り出された透過水を貯留する二次処理水
槽13が配置されており、二次処理水槽13には移送ポ
ンプ14が設けられている。A secondary treated water tank 13 for storing permeated water taken out by the submerged membrane separation apparatus 10 is arranged outside the deep reaction tank 1, and a transfer pump 14 is provided in the secondary treated water tank 13. Has been.
【0011】以下、上記構成における作用を説明する。
攪拌ポンプ7、エゼクタ9、吸引ポンプ11を駆動する
状態において、被処理水供給管6よりポンプ槽5に被処
理水を導入すると、被処理水は、ポンプ槽5より下向流
路2の頂部へ揚水されて下向流路2内を下降し、次いで
上向流路3内を上昇して、越流堰4よりポンプ槽5へ流
入する循環経路で、深層反応槽内の被処理水とともに循
環流動する。The operation of the above structure will be described below.
When the agitating pump 7, the ejector 9, and the suction pump 11 are driven, when the treated water is introduced from the treated water supply pipe 6 into the pump tank 5, the treated water flows from the pump tank 5 to the top of the downward flow path 2. The water is pumped up to the inside of the downward flow path 2, then descends in the upward flow path 3, and then rises in the upward flow path 3 to flow into the pump tank 5 from the overflow weir 4, together with the water to be treated in the deep reaction tank. Circulate and flow.
【0012】このとき、循環流動する被処理水に、下向
流路2の頂部においてエゼクタ9より硝化・脱窒に適し
たDOとなる曝気空気が供給され、この曝気空気は被処
理水が下向流路2内を下降するときの攪拌と水深とによ
り被処理水中に十分溶解される。At this time, aeration air serving as DO suitable for nitrification and denitrification is supplied from the ejector 9 to the circulating water to be treated water at the top of the downward flow path 2. It is sufficiently dissolved in the water to be treated due to the stirring and the water depth when descending in the counter flow passage 2.
【0013】被処理水は、このようにして循環流動され
つつ曝気空気が供給される状態において、槽内の活性汚
泥により生物学的に硝化・脱窒されるとともに、膜分離
装置10によって固液分離され、膜分離装置10の分離
膜を透過した透過水は吸引管12を通じて二次処理水槽
13に送られる。なお、膜分離装置10は、被処理水循
環流や曝気空気の気泡流により分離膜表面が洗浄され、
付着物の堆積が防止される。The water to be treated is biologically nitrified and denitrified by the activated sludge in the tank in the state where the aerated air is supplied while being circulated and flown in this manner, and the solid water is liquefied by the membrane separation device 10. The permeated water that has been separated and has passed through the separation membrane of the membrane separation device 10 is sent to the secondary treatment water tank 13 through the suction pipe 12. In the membrane separation device 10, the surface of the separation membrane is washed by a circulating flow of water to be treated or a bubble flow of aerated air,
Accumulation of deposits is prevented.
【0014】[0014]
【発明の効果】以上のように本発明によれば、被処理水
を循環流動させつつ効果的に曝気空気を供給するように
した深層反応槽の内部に浸漬型膜分離装置を設けたこと
により、単一の槽内において、被処理水の生物処理と固
液分離を好適に行うことができる。As described above, according to the present invention, the immersion type membrane separation device is provided inside the deep-layer reaction tank in which the aerated air is effectively supplied while circulating the water to be treated. The biological treatment and solid-liquid separation of the water to be treated can be suitably performed in a single tank.
【図1】本発明の一実施例の水処理装置の全体構成を示
した説明図である。FIG. 1 is an explanatory diagram showing an overall configuration of a water treatment device according to an embodiment of the present invention.
1 深層反応槽 2 下向流路 3 上向流路 9 エゼクタ(曝気手段) 10 浸漬型膜分離装置 1 Deep reaction tank 2 Downward flow path 3 Upward flow path 9 Ejector (aeration means) 10 Immersion type membrane separation device
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C02F 9/00 503 C 504 A ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI Technical display location C02F 9/00 503 C 504 A
Claims (1)
向流路とを形成し、下向流路内を下降する被処理水に曝
気空気を供給する曝気手段を設けた深層反応槽に、上向
流路内に位置して槽内の被処理水を固液分離する浸漬型
膜分離装置を設けたことを特徴とする水処理装置。1. A deep-layer reaction which forms an downward flow path and an upward flow path for circulating the water to be treated and which is provided with aeration means for supplying aeration air to the water to be treated descending in the downward flow passage. A water treatment device, characterized in that the tank is provided with an immersion type membrane separation device which is located in the upward flow path and performs solid-liquid separation of the water to be treated in the tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6100319A JPH07303895A (en) | 1994-05-16 | 1994-05-16 | Water treatment apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6100319A JPH07303895A (en) | 1994-05-16 | 1994-05-16 | Water treatment apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH07303895A true JPH07303895A (en) | 1995-11-21 |
Family
ID=14270873
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6100319A Pending JPH07303895A (en) | 1994-05-16 | 1994-05-16 | Water treatment apparatus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH07303895A (en) |
Cited By (21)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1115474A4 (en) * | 1998-09-25 | 2005-03-30 | Us Filter Wastewater Group Inc | Apparatus and method for cleaning membrane filtration modules |
KR100506586B1 (en) * | 1998-12-31 | 2005-09-26 | 한솔제지주식회사 | Chemically Advanced Oxidation of Refractory High Concentration Organic Wastewater |
US7361274B2 (en) | 2002-08-21 | 2008-04-22 | Siemens Water Technologies Corp. | Aeration method |
KR100832673B1 (en) * | 1998-09-25 | 2008-05-27 | 유.에스. 필터 웨이스트워터 그룹, 인크. | Filtration system, membrane module and method for cleaning the module |
US20100326897A1 (en) * | 1995-08-11 | 2010-12-30 | Mailvaganam Mahendran | Membrane filtration module with adjustable header spacing |
US8840783B2 (en) | 2007-05-29 | 2014-09-23 | Evoqua Water Technologies Llc | Water treatment membrane cleaning with pulsed airlift pump |
US8858796B2 (en) | 2005-08-22 | 2014-10-14 | Evoqua Water Technologies Llc | Assembly for water filtration using a tube manifold to minimise backwash |
US8956464B2 (en) | 2009-06-11 | 2015-02-17 | Evoqua Water Technologies Llc | Method of cleaning membranes |
US9022224B2 (en) | 2010-09-24 | 2015-05-05 | Evoqua Water Technologies Llc | Fluid control manifold for membrane filtration system |
US9023206B2 (en) | 2008-07-24 | 2015-05-05 | Evoqua Water Technologies Llc | Frame system for membrane filtration modules |
US9533261B2 (en) | 2012-06-28 | 2017-01-03 | Evoqua Water Technologies Llc | Potting method |
US9604166B2 (en) | 2011-09-30 | 2017-03-28 | Evoqua Water Technologies Llc | Manifold arrangement |
US9675938B2 (en) | 2005-04-29 | 2017-06-13 | Evoqua Water Technologies Llc | Chemical clean for membrane filter |
US9764288B2 (en) | 2007-04-04 | 2017-09-19 | Evoqua Water Technologies Llc | Membrane module protection |
US9764289B2 (en) | 2012-09-26 | 2017-09-19 | Evoqua Water Technologies Llc | Membrane securement device |
US9815027B2 (en) | 2012-09-27 | 2017-11-14 | Evoqua Water Technologies Llc | Gas scouring apparatus for immersed membranes |
US9914097B2 (en) | 2010-04-30 | 2018-03-13 | Evoqua Water Technologies Llc | Fluid flow distribution device |
US9925499B2 (en) | 2011-09-30 | 2018-03-27 | Evoqua Water Technologies Llc | Isolation valve with seal for end cap of a filtration system |
US9962865B2 (en) | 2012-09-26 | 2018-05-08 | Evoqua Water Technologies Llc | Membrane potting methods |
US10322375B2 (en) | 2015-07-14 | 2019-06-18 | Evoqua Water Technologies Llc | Aeration device for filtration system |
US10427102B2 (en) | 2013-10-02 | 2019-10-01 | Evoqua Water Technologies Llc | Method and device for repairing a membrane filtration module |
-
1994
- 1994-05-16 JP JP6100319A patent/JPH07303895A/en active Pending
Cited By (31)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20100326897A1 (en) * | 1995-08-11 | 2010-12-30 | Mailvaganam Mahendran | Membrane filtration module with adjustable header spacing |
US8852438B2 (en) | 1995-08-11 | 2014-10-07 | Zenon Technology Partnership | Membrane filtration module with adjustable header spacing |
EP1115474A4 (en) * | 1998-09-25 | 2005-03-30 | Us Filter Wastewater Group Inc | Apparatus and method for cleaning membrane filtration modules |
KR100832673B1 (en) * | 1998-09-25 | 2008-05-27 | 유.에스. 필터 웨이스트워터 그룹, 인크. | Filtration system, membrane module and method for cleaning the module |
KR100506586B1 (en) * | 1998-12-31 | 2005-09-26 | 한솔제지주식회사 | Chemically Advanced Oxidation of Refractory High Concentration Organic Wastewater |
US7361274B2 (en) | 2002-08-21 | 2008-04-22 | Siemens Water Technologies Corp. | Aeration method |
US9675938B2 (en) | 2005-04-29 | 2017-06-13 | Evoqua Water Technologies Llc | Chemical clean for membrane filter |
US8858796B2 (en) | 2005-08-22 | 2014-10-14 | Evoqua Water Technologies Llc | Assembly for water filtration using a tube manifold to minimise backwash |
US8894858B1 (en) | 2005-08-22 | 2014-11-25 | Evoqua Water Technologies Llc | Method and assembly for water filtration using a tube manifold to minimize backwash |
US9764288B2 (en) | 2007-04-04 | 2017-09-19 | Evoqua Water Technologies Llc | Membrane module protection |
US9573824B2 (en) | 2007-05-29 | 2017-02-21 | Evoqua Water Technologies Llc | Membrane cleaning with pulsed airlift pump |
US8840783B2 (en) | 2007-05-29 | 2014-09-23 | Evoqua Water Technologies Llc | Water treatment membrane cleaning with pulsed airlift pump |
US9206057B2 (en) | 2007-05-29 | 2015-12-08 | Evoqua Water Technologies Llc | Membrane cleaning with pulsed airlift pump |
US10507431B2 (en) | 2007-05-29 | 2019-12-17 | Evoqua Water Technologies Llc | Membrane cleaning with pulsed airlift pump |
US9023206B2 (en) | 2008-07-24 | 2015-05-05 | Evoqua Water Technologies Llc | Frame system for membrane filtration modules |
US8956464B2 (en) | 2009-06-11 | 2015-02-17 | Evoqua Water Technologies Llc | Method of cleaning membranes |
US10441920B2 (en) | 2010-04-30 | 2019-10-15 | Evoqua Water Technologies Llc | Fluid flow distribution device |
US9914097B2 (en) | 2010-04-30 | 2018-03-13 | Evoqua Water Technologies Llc | Fluid flow distribution device |
US9630147B2 (en) | 2010-09-24 | 2017-04-25 | Evoqua Water Technologies Llc | Fluid control manifold for membrane filtration system |
US9022224B2 (en) | 2010-09-24 | 2015-05-05 | Evoqua Water Technologies Llc | Fluid control manifold for membrane filtration system |
US9604166B2 (en) | 2011-09-30 | 2017-03-28 | Evoqua Water Technologies Llc | Manifold arrangement |
US9925499B2 (en) | 2011-09-30 | 2018-03-27 | Evoqua Water Technologies Llc | Isolation valve with seal for end cap of a filtration system |
US10391432B2 (en) | 2011-09-30 | 2019-08-27 | Evoqua Water Technologies Llc | Manifold arrangement |
US11065569B2 (en) | 2011-09-30 | 2021-07-20 | Rohm And Haas Electronic Materials Singapore Pte. Ltd. | Manifold arrangement |
US9533261B2 (en) | 2012-06-28 | 2017-01-03 | Evoqua Water Technologies Llc | Potting method |
US9764289B2 (en) | 2012-09-26 | 2017-09-19 | Evoqua Water Technologies Llc | Membrane securement device |
US9962865B2 (en) | 2012-09-26 | 2018-05-08 | Evoqua Water Technologies Llc | Membrane potting methods |
US9815027B2 (en) | 2012-09-27 | 2017-11-14 | Evoqua Water Technologies Llc | Gas scouring apparatus for immersed membranes |
US10427102B2 (en) | 2013-10-02 | 2019-10-01 | Evoqua Water Technologies Llc | Method and device for repairing a membrane filtration module |
US11173453B2 (en) | 2013-10-02 | 2021-11-16 | Rohm And Haas Electronic Materials Singapores | Method and device for repairing a membrane filtration module |
US10322375B2 (en) | 2015-07-14 | 2019-06-18 | Evoqua Water Technologies Llc | Aeration device for filtration system |
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