JP2002028652A - Membrane separator - Google Patents

Membrane separator

Info

Publication number
JP2002028652A
JP2002028652A JP2000217955A JP2000217955A JP2002028652A JP 2002028652 A JP2002028652 A JP 2002028652A JP 2000217955 A JP2000217955 A JP 2000217955A JP 2000217955 A JP2000217955 A JP 2000217955A JP 2002028652 A JP2002028652 A JP 2002028652A
Authority
JP
Japan
Prior art keywords
membrane
filtration
immersion
tank
filtration membrane
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
JP2000217955A
Other languages
Japanese (ja)
Inventor
Tatsuhiko Suzuki
辰彦 鈴木
Hironobu Teramoto
裕宣 寺本
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Maezawa Industries Inc
Original Assignee
Maezawa Industries Inc
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 Maezawa Industries Inc filed Critical Maezawa Industries Inc
Priority to JP2000217955A priority Critical patent/JP2002028652A/en
Publication of JP2002028652A publication Critical patent/JP2002028652A/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

  • Separation Using Semi-Permeable Membranes (AREA)
  • Activated Sludge Processes (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a membrane separator which is capable of efficiently carrying out separation of solid from liquid and allows the easy application to a circular sedimentation basin disposed at existing drinking water treatment equipments. SOLUTION: Immersion type filter membranes 14 are radially installed in a state rotatable around a supporting shaft 12 erected at the center of a filtration treatment chamber 11 of a circular sedimentation basin type at the circumference of this supporting shaft 12.

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、膜分離装置に関
し、特に、既設の円形沈殿池を膜分離用のろ過処理槽に
利用して効果的な膜分離を行うことができる膜分離装置
に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a membrane separation device, and more particularly to a membrane separation device capable of performing effective membrane separation by using an existing circular sedimentation tank as a filtration tank for membrane separation.

【0002】[0002]

【従来の技術】各種浄水設備における最終沈殿池では、
活性汚泥のバルキング等による沈降性の悪化によって処
理性が低下し、処理水質が著しく損なわれる現象が生じ
ることがある。このため、沈殿池等の日常の維持管理性
が問題となっており、安定した処理が行える膜分離に移
行しつつある。
2. Description of the Related Art In a final sedimentation basin in various water purification facilities,
Degradation of settling properties due to bulking or the like of activated sludge lowers the processability and may cause a phenomenon that the quality of treated water is significantly impaired. For this reason, daily maintainability of the sedimentation basin and the like has become a problem, and the transition to membrane separation that enables stable processing has been started.

【0003】[0003]

【発明が解決しようとする課題】しかし、既設の浄水設
備に膜分離装置を設置するためには、既設の最終沈殿池
を取り壊して新たに膜分離用のろ過処理槽を建設しなけ
ればならず、多大な費用と時間とを必要としていた。
However, in order to install a membrane separation apparatus in an existing water purification facility, the existing final sedimentation basin must be demolished and a new filtration tank for membrane separation must be constructed. A great deal of money and time.

【0004】そこで本発明は、固液分離を効率よく行え
るとともに、既設の浄水設備に最終沈殿池等として設け
られている円形沈殿池の構造物や機器を利用して形成す
ること可能な膜分離装置を提供することを目的としてい
る。
Accordingly, the present invention provides a membrane separation system capable of efficiently performing solid-liquid separation and forming the same using the structure and equipment of a circular sedimentation basin provided as a final sedimentation basin in an existing water purification facility. It is intended to provide a device.

【0005】[0005]

【課題を解決するための手段】上記目的を達成するた
め、本発明の膜分離装置は、円形沈殿池型のろ過処理槽
の中央に立設した支軸の周囲に、該支軸を中心として回
転可能な状態で放射状に浸漬型ろ過膜を設置したことを
特徴としている。
In order to achieve the above object, a membrane separation apparatus according to the present invention is provided around a support shaft erected at the center of a filtration tank of a circular sedimentation tank type. It is characterized in that a submerged filtration membrane is installed radially in a rotatable state.

【0006】より具体的な構造としては、円形沈殿池型
のろ過処理槽の中央に立設した支軸と、該支軸から放射
状に設けられた複数のろ過膜支持部材と、該支持部材に
より支持されてろ過処理槽内に放射状に設置された浸漬
型ろ過膜と、前記ろ過膜支持部材に沿うように設けられ
て前記支軸部で集合する膜処理水吸引管と、該膜処理水
吸引管が集合した吸引主管にスイベルジョイントを介し
て接続した膜処理水吸引ポンプと、前記ろ過膜支持部材
を支軸を中心にして回転させる駆動手段と、前記浸漬型
ろ過膜のエアスクラビングを行うための散気手段とを備
えていることを特徴とし、さらに、前記ろ過処理槽に隣
接して前記浸漬型ろ過膜の薬液洗浄を行うための薬液洗
浄槽を設けたことを特徴としている。
As a more specific structure, a support shaft erected at the center of a filtration tank of a circular sedimentation tank type, a plurality of filter membrane support members provided radially from the support shaft, and the support member An immersion-type filtration membrane that is supported and installed radially in a filtration tank, a membrane-treated water suction pipe that is provided along the filtration-membrane support member, and that gathers at the spindle portion; A membrane-treated water suction pump connected to a main suction pipe through a swivel joint, a driving means for rotating the filtration membrane support member about a support shaft, and air scrubbing of the immersion filtration membrane. And a chemical cleaning tank for cleaning the immersion-type filtration membrane with a chemical solution is provided adjacent to the filtration treatment tank.

【0007】[0007]

【発明の実施の形態】図1及び図2は、本発明の膜分離
装置の一形態例を示すもので、図1は縦断面図、図2は
平面図である。この膜分離装置は、既設の円形沈殿池を
改造して形成したものであって、円形沈殿池を利用した
ろ過処理槽11の中央に設けられた支軸12と、該支軸
12から放射状に等角度間隔で設けられた複数のろ過膜
支持部材13と、該支持部材13により支持されてろ過
処理槽11内に放射状に設置された浸漬型ろ過膜(浸漬
型膜モジュール)14と、前記ろ過膜支持部材13に沿
うように設けられて前記支軸部で集合する膜処理水吸引
管15と、該膜処理水吸引管15が集合した吸引主管1
6にスイベルジョイント17を介して接続した膜処理水
吸引ポンプ18と、前記ろ過膜支持部材13を支軸12
を中心にして回転させる駆動手段である減速機19と、
前記浸漬型ろ過膜14のエアスクラビングを行うための
散気手段である散気管20及びブロワ21と、浸漬型ろ
過膜14の薬液洗浄を行うための薬液洗浄槽22とによ
り形成されている。
1 and 2 show an embodiment of a membrane separation apparatus according to the present invention. FIG. 1 is a longitudinal sectional view and FIG. 2 is a plan view. This membrane separation device is formed by modifying an existing circular sedimentation basin, and includes a support shaft 12 provided at the center of a filtration tank 11 using the circular sedimentation basin, and a radial shaft from the support shaft 12. A plurality of filtration membrane support members 13 provided at equal angular intervals, a submerged filtration membrane (submerged membrane module) 14 supported by the support members 13 and radially installed in the filtration tank 11; A membrane-treated water suction pipe 15 provided along the membrane support member 13 and gathering at the support shaft; and a suction main pipe 1 on which the membrane-treated water suction pipe 15 is gathered
6 and a membrane treated water suction pump 18 connected via a swivel joint 17 to the filtration membrane support member 13.
A speed reducer 19 which is a driving means for rotating around
The immersion filter membrane 14 is formed by an air diffuser 20 and a blower 21 which are air diffusers for performing air scrubbing of the immersion filter membrane 14, and a chemical cleaning tank 22 for cleaning the immersion filter membrane 14 with a chemical.

【0008】また、ろ過処理槽11は、上部中央に原水
流入経路23を有するとともに、底部中央に汚泥(濃縮
水)引抜き経路24を有している。これらの経路23,
24は、円形沈殿池に設けられていたものをそのまま利
用することができ、さらに、前記支軸12や減速機19
も、支軸下端を支持する軸受部材25や支軸上部を支持
するとともに減速機19を設置するデッキ26を含め
て、円形沈殿池に設けられている汚泥掻寄機のものを利
用することが可能である。
The filtration tank 11 has a raw water inflow path 23 at the upper center and a sludge (concentrated water) extraction path 24 at the bottom center. These routes 23,
As for 24, what was provided in the circular sedimentation basin can be used as it is.
Also, it is possible to use the sludge scraper provided in the circular sedimentation pond, including the bearing member 25 supporting the lower end of the support shaft and the deck 26 supporting the upper portion of the support shaft and installing the speed reducer 19. It is possible.

【0009】ろ過膜支持部材13は、上部支持材13a
と下部支持材13bとで浸漬型ろ過膜14の上部及び下
部をそれぞれ支持するものであり、適宜な支持構造、例
えば嵌合構造等によって浸漬型ろ過膜14を着脱可能に
支持するようにしている。一方の浸漬型ろ過膜14は、
適宜なフレーム等を使用してユニット化されており、ろ
過膜支持部材13への着脱が容易に行えるように形成さ
れている。このとき、使用するろ過膜が平膜の場合は、
膜面が周方向に向くようにして取付けておくことが望ま
しい。
[0009] The filtration membrane support member 13 includes an upper support member 13a.
The lower and upper support members 13b support the upper and lower portions of the immersion type filtration membrane 14, respectively. The immersion type filtration membrane 14 is detachably supported by an appropriate support structure, for example, a fitting structure or the like. . One immersion type filtration membrane 14 is
It is formed into a unit using an appropriate frame or the like, and is formed so that it can be easily attached to and detached from the filtration membrane support member 13. At this time, if the filtration membrane used is a flat membrane,
It is desirable that the film be attached so that the film surface faces in the circumferential direction.

【0010】また、前記膜処理水吸引管15は、ろ過膜
側が浸漬型ろ過膜14に対して着脱可能に取付けられて
おり、支軸側が支軸12内に挿入された吸引主管16に
直接あるいは適当に集合した後に接続されている。さら
に、前記薬液洗浄槽22の部分には、ろ過膜支持部材1
3と薬液洗浄槽22とに浸漬型ろ過膜14を移送するた
めの適宜な搬送手段、例えばクレーン27が設けられて
いる。
The membrane-treated water suction pipe 15 has a filtration membrane side removably attached to the immersion filtration membrane 14, and a spindle side directly or directly attached to a suction main pipe 16 inserted into the spindle 12. They are connected after being assembled appropriately. Further, a part of the chemical solution washing tank 22 is provided with the filtration membrane support member 1.
Appropriate transport means, for example, a crane 27, for transferring the immersion type filtration membrane 14 to the chemical solution washing tank 22 and the chemical solution washing tank 22 are provided.

【0011】このように形成した膜分離装置は、例え
ば、最終沈殿池として用いる場合は、活性汚泥法等によ
る処理を行った処理水を原水流入経路23から流入させ
ながら、膜処理水吸引ポンプ18を作動させて浸漬型ろ
過膜14から膜処理水を吸引することによって固液分離
を行う。このとき、減速機19を作動させて連続的ある
いは間欠的に浸漬型ろ過膜14を回転させることによ
り、ろ過膜に剪断力を与えて膜面への汚泥の付着を抑制
することができる。
When the membrane separation apparatus thus formed is used as, for example, a final sedimentation basin, the treated water treated by the activated sludge method or the like flows in from the raw water inflow path 23 while the membrane treated water suction pump 18 is used. Is operated to suck the membrane-treated water from the immersion-type filtration membrane 14, thereby performing solid-liquid separation. At this time, by operating the speed reducer 19 and rotating the immersion type filtration membrane 14 continuously or intermittently, a shearing force is applied to the filtration membrane, and the adhesion of sludge to the membrane surface can be suppressed.

【0012】また、ブロワ21を連続的あるいは間欠的
に作動させることにより、散気管20の上方に位置した
浸漬型ろ過膜14に対してエアスクラビング洗浄を行う
ことができる。このエアスクラビング洗浄は、浸漬型ろ
過膜14を所定位置に回転させることにより、浸漬型ろ
過膜14の設置数に関係なく一箇所の散気管20で全て
の浸漬型ろ過膜14に対してそれぞれ行うことが可能な
ため、散気管20及びブロワ21をろ過処理槽11内に
一箇所だけ設ければ十分であり、これらに要する設備費
やランニングコストの削減が図れる。なお、散気管20
は、必要に応じて複数箇所に設けることもできる。
By operating the blower 21 continuously or intermittently, air scrubbing and cleaning can be performed on the immersion type filtration membrane 14 located above the air diffuser 20. This air scrubbing cleaning is performed on all of the immersion filtration membranes 14 by rotating the immersion filtration membrane 14 at a predetermined position, regardless of the number of immersion filtration membranes 14 installed, with one diffuser 20. Therefore, it is sufficient to provide only one diffuser tube 20 and blower 21 in the filtration tank 11, and it is possible to reduce equipment costs and running costs required for these. The air diffuser 20
May be provided at a plurality of locations as needed.

【0013】浸漬型ろ過膜14の薬液洗浄を行う場合
は、対象となる浸漬型ろ過膜14を前記クレーン27の
部分に止めてろ過膜支持部材13から取外し、クレーン
27で薬液洗浄槽22に移送して行えばよい。このと
き、該浸漬型ろ過膜14に接続する膜処理水吸引管15
を弁等で塞いでおくことにより、薬液洗浄中も、他の浸
漬型ろ過膜14によるろ過処理を継続して行うことがで
きる。さらに、予備の浸漬型ろ過膜14を用意してお
き、各ろ過膜を順次交換しながら薬液洗浄を行うように
することもできる。
When the chemical cleaning of the immersion type filtration membrane 14 is performed, the immersion type filtration membrane 14 to be targeted is stopped at the crane 27 and removed from the filtration membrane support member 13 and transferred to the chemical cleaning tank 22 by the crane 27. And do it. At this time, a membrane-treated water suction pipe 15 connected to the immersion type filtration membrane 14 is used.
Is closed by a valve or the like, so that the filtration process by another immersion-type filtration membrane 14 can be continuously performed even during the cleaning of the chemical solution. Further, it is also possible to prepare a preliminary immersion type filtration membrane 14 and perform the chemical cleaning while sequentially replacing each filtration membrane.

【0014】なお、運転は、通常の一般的な膜分離装置
と同様にして行うことができ、エアスクラビングや薬液
洗浄も同じようにして行えばよい。また、浸漬型ろ過膜
の設置数や支持構造、その他各部の構造は、利用する円
形沈殿池の大きさや形式、分離膜の種類等に応じて適当
に設計することができる。さらに、同様の構造の膜分離
装置を新設した場合でも、膜面への汚泥付着の抑制や散
気手段の削減等の作用効果は同様に得ることができる。
The operation can be carried out in the same manner as in a general membrane separation apparatus, and the air scrubbing and chemical cleaning may be carried out in the same manner. Further, the number of immersion type filtration membranes, the supporting structure, and the structure of each part can be appropriately designed according to the size and type of the circular sedimentation basin to be used, the type of separation membrane, and the like. Furthermore, even when a membrane separation device having a similar structure is newly installed, the same effect as that of the prevention of sludge adhesion to the membrane surface and the reduction of air diffusion means can be obtained.

【0015】[0015]

【発明の効果】以上説明したように、本発明の膜分離装
置によれば、最終沈殿池等に使用していた円形沈殿池を
膜分離用のろ過処理槽に利用するとともに、既設の構造
物や機器を利用して膜分離装置を形成することができ、
維持管理が容易で、しかも、安定した固液分離を行える
膜分離への転換を低コストで行うことができる。さら
に、汚泥掻寄機用の減速機を利用して浸漬型ろ過膜を回
転させることにより、膜面への汚泥の付着を抑制して効
率的な運転を安定した状態で継続できる。また、エアス
クラビングを行うための散気手段も一箇所だけ設置すれ
ばよいため、これらのコスト削減も図れる。
As described above, according to the membrane separation apparatus of the present invention, the circular sedimentation basin used for the final sedimentation basin and the like is used for the filtration treatment tank for membrane separation, and the existing structure is used. Can be used to form a membrane separation device,
It is easy to maintain and control, and the conversion to membrane separation that can perform stable solid-liquid separation can be performed at low cost. Furthermore, by rotating the immersion type filtration membrane using a reduction device for a sludge scraper, it is possible to suppress the adhesion of sludge to the membrane surface and to continue an efficient operation in a stable state. In addition, since only one air diffusion means for performing the air scrubbing needs to be provided, the cost can be reduced.

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

【図1】 本発明の膜分離装置の一形態例を示す縦断面
図である。
FIG. 1 is a longitudinal sectional view showing one embodiment of a membrane separation device of the present invention.

【図2】 同じく平面図である。FIG. 2 is a plan view of the same.

【符号の説明】[Explanation of symbols]

11…ろ過処理槽、12…支軸、13…ろ過膜支持部
材、14…浸漬型ろ過膜、15…膜処理水吸引管、16
…吸引主管、17…スイベルジョイント、18…膜処理
水吸引ポンプ、19…減速機、20…散気管、21…ブ
ロワ、22…薬液洗浄槽、23…原水流入経路、24…
汚泥(濃縮水)引抜き経路、25…軸受部材、26…デ
ッキ、27…クレーン
11 ... filtration treatment tank, 12 ... spindle, 13 ... filtration membrane support member, 14 ... immersion filtration membrane, 15 ... membrane treated water suction pipe, 16
... suction main pipe, 17 ... swivel joint, 18 ... membrane treatment water suction pump, 19 ... reducer, 20 ... diffuser pipe, 21 ... blower, 22 ... chemical cleaning tank, 23 ... raw water inflow path, 24 ...
Sludge (concentrated water) extraction path, 25 ... bearing member, 26 ... deck, 27 ... crane

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 円形沈殿池型のろ過処理槽の中央に立設
した支軸の周囲に、該支軸を中心として回転可能な状態
で放射状に浸漬型ろ過膜を設置したことを特徴とする円
形沈殿池型膜分離装置。
An immersion type filtration membrane is installed radially around a support shaft erected in the center of a filtration tank of a circular sedimentation tank type so as to be rotatable around the support shaft. Circular sedimentation tank type membrane separation device.
【請求項2】 円形沈殿池型のろ過処理槽の中央に立設
した支軸と、該支軸から放射状に設けられた複数のろ過
膜支持部材と、該支持部材により支持されてろ過処理槽
内に放射状に設置された浸漬型ろ過膜と、前記ろ過膜支
持部材に沿うように設けられて前記支軸部で集合する膜
処理水吸引管と、該膜処理水吸引管が集合した吸引主管
にスイベルジョイントを介して接続した膜処理水吸引ポ
ンプと、前記ろ過膜支持部材を支軸を中心にして回転さ
せる駆動手段と、前記浸漬型ろ過膜のエアスクラビング
を行うための散気手段とを備えていることを特徴とする
膜分離装置。
2. A support shaft erected in the center of a circular sedimentation tank type filtration treatment tank, a plurality of filtration membrane support members provided radially from the support shaft, and a filtration treatment tank supported by the support member. A immersion-type filtration membrane radially installed in the inside, a membrane-treated water suction pipe provided along the filtration membrane support member and gathering at the spindle, and a suction main pipe with the membrane-treated water suction pipe gathered A membrane-treated water suction pump connected via a swivel joint, a driving unit for rotating the filtration membrane support member about a support shaft, and an air diffusion unit for performing air scrubbing of the immersion filtration membrane. A membrane separation device, comprising:
【請求項3】 前記ろ過処理槽に隣接して前記浸漬型ろ
過膜の薬液洗浄を行うための薬液洗浄槽が設けられてい
ることを特徴とする請求項2記載の膜分離装置。
3. The membrane separation device according to claim 2, wherein a chemical cleaning tank for cleaning the immersion type filtration membrane with a chemical is provided adjacent to the filtration tank.
JP2000217955A 2000-07-18 2000-07-18 Membrane separator Pending JP2002028652A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000217955A JP2002028652A (en) 2000-07-18 2000-07-18 Membrane separator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000217955A JP2002028652A (en) 2000-07-18 2000-07-18 Membrane separator

Publications (1)

Publication Number Publication Date
JP2002028652A true JP2002028652A (en) 2002-01-29

Family

ID=18712984

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000217955A Pending JP2002028652A (en) 2000-07-18 2000-07-18 Membrane separator

Country Status (1)

Country Link
JP (1) JP2002028652A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004188255A (en) * 2002-12-09 2004-07-08 Hitachi Kiden Kogyo Ltd Oxidation ditch
JP2005246310A (en) * 2004-03-05 2005-09-15 Ngk Insulators Ltd Membrane separation activated sludge process
JP2010137216A (en) * 2008-11-11 2010-06-24 Kobelco Eco-Solutions Co Ltd Membrane separation activated sludge treatment apparatus and membrane separation activated sludge treatment method
CN109748467A (en) * 2019-03-11 2019-05-14 秦皇岛市第一医院 A kind of Hospital Sewage Treatment reclaimer with efficient sterilization function
CN110627164A (en) * 2019-09-05 2019-12-31 上海申欣环保实业有限公司 Solid-liquid separation device

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004188255A (en) * 2002-12-09 2004-07-08 Hitachi Kiden Kogyo Ltd Oxidation ditch
JP2005246310A (en) * 2004-03-05 2005-09-15 Ngk Insulators Ltd Membrane separation activated sludge process
JP4500069B2 (en) * 2004-03-05 2010-07-14 メタウォーター株式会社 Membrane separation activated sludge method
JP2010137216A (en) * 2008-11-11 2010-06-24 Kobelco Eco-Solutions Co Ltd Membrane separation activated sludge treatment apparatus and membrane separation activated sludge treatment method
CN109748467A (en) * 2019-03-11 2019-05-14 秦皇岛市第一医院 A kind of Hospital Sewage Treatment reclaimer with efficient sterilization function
CN110627164A (en) * 2019-09-05 2019-12-31 上海申欣环保实业有限公司 Solid-liquid separation device

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