JP2011104502A - Immersed flat membrane element - Google Patents

Immersed flat membrane element Download PDF

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JP2011104502A
JP2011104502A JP2009261169A JP2009261169A JP2011104502A JP 2011104502 A JP2011104502 A JP 2011104502A JP 2009261169 A JP2009261169 A JP 2009261169A JP 2009261169 A JP2009261169 A JP 2009261169A JP 2011104502 A JP2011104502 A JP 2011104502A
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flat membrane
support plate
membrane element
end portion
long distance
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Kotaro Kitamura
光太郎 北村
Minoru Morita
穣 森田
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Hitachi Plant Technologies Ltd
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Hitachi Plant Technologies Ltd
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Priority to JP2009261169A priority Critical patent/JP2011104502A/en
Priority to PCT/JP2010/067409 priority patent/WO2011058835A1/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D63/00Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/08Flat membrane modules
    • B01D63/082Flat membrane modules comprising a stack of flat membranes
    • B01D63/0821Membrane plate arrangements for submerged operation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D63/00Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/08Flat membrane modules
    • B01D63/082Flat membrane modules comprising a stack of flat membranes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D69/00Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/06Flat membranes
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/12Activated sludge processes
    • C02F3/1236Particular type of activated sludge installations
    • C02F3/1268Membrane bioreactor systems
    • C02F3/1273Submerged membrane bioreactors
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2315/00Details relating to the membrane module operation
    • B01D2315/06Submerged-type; Immersion type
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/16Regeneration of sorbents, filters
    • 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

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Microbiology (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide an immersed flat membrane element capable of preventing bubbles passing through a space between adjoining flat membrane elements from converging to the central part thereof to enhance the efficiency of cleaning its membrane face. <P>SOLUTION: The flat membrane elements 10 of an immersed flat-membrane filtration apparatus wherein a plurality of flat membrane elements 10 each comprising a pair of adjoining filtration membranes disposed to face each other are vertically immersed in water to be treated present in its treatment tank, and an aeration means is disposed below the plurality of flat membrane elements 10, with the flat membrane elements 10 each constituted of a base frame 12 equipped with a support plate 14 having a water collection groove 16 and with a water collection section 18 disposed on the side face of the support plate 14, and of a pair of filtration membranes 22 each disposed on either main-faces of the support plate 14 respectively, is characterized in that the vertical distances each connecting the upper end 14a and the lower end 14b of the support plate 14 are made to vary in the horizontal direction to provide a long-distance section B and a short-distance section A. <P>COPYRIGHT: (C)2011,JPO&INPIT

Description

本発明は、浸漬平膜濾過装置に係り、特に当該装置において濾過膜として使用される浸漬平膜エレメントに関する。   The present invention relates to an immersion flat membrane filtration device, and more particularly to an immersion flat membrane element used as a filtration membrane in the device.

浸漬平膜濾過装置は、産業排水系の凝集汚泥処理や下水等の活性汚泥処理に用いられる。浸漬平膜濾過装置では図13に示すように、並列配置された複数の平膜エレメント1を処理槽2内に浸漬させた状態で配置され、各平膜エレメント1の内部から被処理水を吸引することによって濾過水が得られる。   The submerged flat membrane filtration apparatus is used for activated sludge treatment such as coagulation sludge treatment for industrial drainage and sewage. In the submerged flat membrane filtration apparatus, as shown in FIG. 13, a plurality of flat membrane elements 1 arranged in parallel are arranged so as to be immersed in the treatment tank 2, and water to be treated is sucked from the inside of each flat membrane element 1. By doing so, filtered water is obtained.

このような配置形態にある平膜エレメント1の下方には、散気手段3が配置されている。散気手段3による散気は、平膜エレメント1における濾膜面の洗浄、処理槽2内の攪拌、および処理槽2内の微生物に対する酸素供給等といった目的を持って成される。このような目的の中で、被処理水の濾過に対して直接的に関係するのが膜面の洗浄である。しかしながら、従来の浸漬平膜濾過装置では、処理槽2内に活性汚泥などの固形物が高濃度で存在する場合、被処理水の粘度が増加するため、散気手段3によって発生する気泡の大きさに均一性がなくなると共に気泡の偏りが生じ、効果的な膜面洗浄が成されなくなり、被処理水の濾過効率が低下するという問題があった。   Aeration means 3 is arranged below flat membrane element 1 in such an arrangement. The air diffused by the air diffuser 3 is formed for the purpose of cleaning the membrane surface of the flat membrane element 1, stirring in the processing tank 2, supplying oxygen to the microorganisms in the processing tank 2, and the like. Among these purposes, the membrane surface cleaning is directly related to the filtration of the water to be treated. However, in the conventional submerged flat membrane filtration apparatus, when the solid matter such as activated sludge is present in the treatment tank 2 at a high concentration, the viscosity of the water to be treated increases. In addition, there is a problem that the uniformity of the thickness is lost and bubbles are unevenly distributed, so that effective membrane surface cleaning is not performed and the filtration efficiency of the water to be treated is lowered.

このような問題に対しては、様々な技術が提案されており、例えば特許文献1では、平膜エレメントの上部に生ずるエア溜まりを解消するために、平膜エレメントの上部左右から、処理水と共にエアを吸引し、エア溜まりの発生を防止することで、散気による洗浄効率の向上を図っている。   Various techniques have been proposed for such a problem. For example, in Patent Document 1, in order to eliminate an air pool generated in the upper part of the flat membrane element, from the upper left and right of the flat membrane element, along with the treated water. By sucking air and preventing the occurrence of air accumulation, the cleaning efficiency is improved by aeration.

また特許文献2では、平膜エレメントと散気管の間に、散気された気泡を分散させる分散板を配置して、平膜エレメントに供給される気泡の小径化、および分散を図っている。   Moreover, in patent document 2, the dispersion plate which disperse | distributes the air bubble diffused is arrange | positioned between a flat membrane element and a diffuser tube, and diameter reduction and dispersion | distribution of the bubble supplied to a flat membrane element are aimed at.

さらに特許文献3では、並列配置される平膜エレメントの枠部下端部の厚みを膜面より狭小化すると共にその配置位置によって間隔を変えることにより、平膜エレメントの下部に形成したエアベッドから膜面に供給されるエアを均等分散させることを特徴としている。   Further, in Patent Document 3, the thickness of the lower end portion of the frame portion of the flat membrane elements arranged in parallel is narrowed from the membrane surface, and the interval is changed depending on the arrangement position, whereby the membrane is removed from the air bed formed in the lower portion of the flat membrane element. The air supplied to the surface is uniformly dispersed.

特開2000−237551号公報JP 2000-237551 A 特開2001−162141号公報JP 2001-162141 A 特開2006−43631号公報JP 2006-43631 A

上記特許文献に開示されているような種々の工夫が成されたとしても、隣接する平膜エレメント間に流れ込んだ気泡は、平膜エレメントの中央に集中し、気泡が粗大化して上昇速度を加速させるという現象が生ずることが確認されている。このような現象が生じた場合、平膜エレメントの端部、すなわち膜面の左右部には、気泡の流れが生じないこととなり、膜面の洗浄効率および被処理水の濾過効率が共に低下することとなる。   Even if various ideas as disclosed in the above patent document are made, the bubbles flowing between the adjacent flat membrane elements are concentrated in the center of the flat membrane elements, and the bubbles are coarsened to accelerate the rising speed. It has been confirmed that this phenomenon occurs. When such a phenomenon occurs, the flow of bubbles does not occur at the ends of the flat membrane element, that is, the left and right sides of the membrane surface, and both the membrane surface cleaning efficiency and the filtration efficiency of the water to be treated are reduced. It will be.

そこで本発明では、隣接する平膜エレメント間を通過する気泡の中央集中化を抑制し、膜面の洗浄効率、被処理水の濾過効率の向上を図ることのできる浸漬平膜エレメントを提供することを目的とする。   Accordingly, the present invention provides an immersion flat membrane element that can suppress central concentration of bubbles passing between adjacent flat membrane elements and can improve the cleaning efficiency of the membrane surface and the filtration efficiency of water to be treated. With the goal.

上記目的を達成するための浸漬平膜エレメントは、処理槽内の被処理水中に、濾膜面を対向させて隣接配置された複数の平膜エレメントを垂直に浸漬させ、前記複数の平膜エレメントの下方に散気手段を配置した浸漬平膜濾過装置の平膜エレメントであって、集水溝を有する支持板と当該支持板の側面に配置される集水部とを有するベースフレームと、前記支持板の両主面に配置される濾膜を備え、前記支持板の上端部と下端部とを結ぶ垂直距離に、水平方向における変化を持たせ、長距離部と短距離部を設けたことを特徴とする。   In order to achieve the above object, an immersion flat membrane element comprises a plurality of flat membrane elements vertically immersed in water to be treated in a treatment tank, with a plurality of flat membrane elements arranged adjacent to each other with their membrane surfaces facing each other. A flat membrane element of a submerged flat membrane filtration apparatus having a diffuser disposed below, a base frame having a support plate having a water collecting groove and a water collecting portion arranged on a side surface of the support plate, Provided with filter membranes arranged on both main surfaces of the support plate, the vertical distance connecting the upper end portion and the lower end portion of the support plate was changed in the horizontal direction, and a long distance portion and a short distance portion were provided. It is characterized by.

また、上記のような特徴を有する浸漬平膜エレメントにおいて前記支持板の上端部および下端部のうちの少なくとも一方は、前記長距離部と前記短距離部とを結ぶ直線部を有すると良い。   Moreover, in the submerged flat membrane element having the above-described characteristics, at least one of the upper end portion and the lower end portion of the support plate may have a linear portion connecting the long distance portion and the short distance portion.

また、上記のような特徴を有する浸漬平膜エレメントでは、前記支持板の上端部および下端部のうちの少なくとも一方は、前記長距離部と前記短距離部とを結ぶ曲線部を有するものとしても良い。   In the submerged flat membrane element having the above-described features, at least one of the upper end portion and the lower end portion of the support plate may have a curved portion connecting the long distance portion and the short distance portion. good.

また、上記のような特徴を有する浸漬平膜エレメントでは、前記長距離部は、前記支持板における水平方向中央部に設けられ、前記短距離部は、前記支持板における水平方向両端部に設けられるようにすると良い。
さらに、上記のような特徴を有する浸漬平膜エレメントにおいて前記長距離部と前記短距離部は、1つの前記支持板に対して複数設けるようにしても良い。
Further, in the submerged flat membrane element having the above-described characteristics, the long distance portion is provided at a horizontal central portion of the support plate, and the short distance portion is provided at both horizontal ends of the support plate. It is good to do so.
Furthermore, in the submerged flat membrane element having the above-described characteristics, a plurality of the long distance portions and the short distance portions may be provided for one support plate.

上記のような特徴を有する浸漬平膜エレメントによれば、隣接する平膜エレメント間を通過する気泡の中央集中化を抑制し、膜面の洗浄効率の向上、および被処理水の濾過効率の向上を図ることができる。また、膜面の効果的な洗浄により、不可逆的な膜閉塞(膜面に対する汚泥の固着)を抑制することができるため、薬品洗浄の頻度を少なくすることができ、膜寿命の延命化を図ることもできる。   According to the submerged flat membrane element having the above-described characteristics, the central concentration of bubbles passing between adjacent flat membrane elements is suppressed, the membrane surface cleaning efficiency is improved, and the treatment water filtration efficiency is improved. Can be achieved. In addition, irreversible membrane clogging (sludge sticking to the membrane surface) can be suppressed by effective cleaning of the membrane surface, so that the frequency of chemical cleaning can be reduced and the membrane life can be extended. You can also.

第1の実施形態に係る浸漬平膜エレメントの構成を示す部分分解斜視図である。It is a partial exploded perspective view which shows the structure of the immersion flat membrane element which concerns on 1st Embodiment. 第1の実施形態に係る浸漬平膜エレメントを複数組み合わせた平膜ユニットの構成を示す斜視図である。It is a perspective view showing composition of a flat membrane unit which combined a plurality of immersion flat membrane elements concerning a 1st embodiment. 従来の浸漬平膜ユニットに生ずる被処理水の流れの速度分布と、気泡の偏りを説明するための図である。It is a figure for demonstrating the velocity distribution of the flow of the to-be-processed water which arises in the conventional immersion flat membrane unit, and the bias | inclination of a bubble. 実施形態に係る浸漬平膜ユニットに生ずる被処理水の流れの速度分布と、気泡の分散化を説明するための図である。It is a figure for demonstrating the velocity distribution of the flow of the to-be-processed water which arises in the immersion flat membrane unit which concerns on embodiment, and dispersion | distribution of a bubble. 第1の実施形態に係る浸漬平膜エレメントの第1の変形例を示す図である。It is a figure which shows the 1st modification of the immersion flat membrane element which concerns on 1st Embodiment. 第1の実施形態に係る浸漬平膜エレメントの第2の変形例を示す図である。It is a figure which shows the 2nd modification of the immersion flat membrane element which concerns on 1st Embodiment. 第2の実施形態に係る浸漬平膜エレメントの構成を示す平面図である。It is a top view which shows the structure of the immersion flat membrane element which concerns on 2nd Embodiment. 第2の実施形態に係る浸漬平膜エレメントの第1の変形例を示す図である。It is a figure which shows the 1st modification of the immersion flat membrane element which concerns on 2nd Embodiment. 第3の実施形態に係る浸漬平膜エレメントの構成を示す平面図である。It is a top view which shows the structure of the immersion flat membrane element which concerns on 3rd Embodiment. 第3の実施形態に係る浸漬平膜エレメントの第1の変形例を示す図である。It is a figure which shows the 1st modification of the immersion flat membrane element which concerns on 3rd Embodiment. 第4の実施形態に係る浸漬平膜エレメントの構成を示す平面図である。It is a top view which shows the structure of the immersion flat membrane element which concerns on 4th Embodiment. 支持板の上端部側にも凸部を設けて長距離部を構成した浸漬平膜エレメントの例を示す図である。It is a figure which shows the example of the immersion flat membrane element which provided the convex part also in the upper end part side of the support plate, and comprised the long distance part. 浸漬平膜エレメントを用いた浸漬平膜濾過装置の構成を示す図である。It is a figure which shows the structure of the immersion flat membrane filtration apparatus using an immersion flat membrane element.

以下、本発明の浸漬平膜エレメントに係る実施の形態について、図面を参照しつつ詳細に説明する。まず、図1を参照して、本発明の浸漬平膜エレメント(以下、単に平膜エレメント10と称す)に係る第1の実施形態について説明する。   Hereinafter, embodiments of the immersed flat membrane element of the present invention will be described in detail with reference to the drawings. First, with reference to FIG. 1, 1st Embodiment which concerns on the immersion flat membrane element (henceforth only the flat membrane element 10) of this invention is described.

本実施形態に係る平膜エレメント10は、ベースフレーム12と、このベースフレーム12に貼付される濾膜22とを基本として構成される。また、本実施形態に係る平膜エレメント10のベースフレーム12は、支持板14と集水部18を有する。   The flat membrane element 10 according to the present embodiment is configured based on a base frame 12 and a filter membrane 22 attached to the base frame 12. In addition, the base frame 12 of the flat membrane element 10 according to the present embodiment includes a support plate 14 and a water collecting portion 18.

本実施形態に係る支持板14は、支持板14の上端部14aと下端部14bとを結ぶ垂直距離に、水平方向(配置形態上)における変化を持たせている。すなわち、支持板14の上端部14aと下端部14bを平行に形成していないのである。具体的には、支持板14の水平方向中央部近傍に、垂直距離を長距離とする長距離部Bを配置し、両端部に、長距離部Bよりも垂直距離を短くした短距離部Aを配置している。   In the support plate 14 according to the present embodiment, the vertical distance connecting the upper end portion 14a and the lower end portion 14b of the support plate 14 is changed in the horizontal direction (on the arrangement form). That is, the upper end portion 14a and the lower end portion 14b of the support plate 14 are not formed in parallel. Specifically, a long distance portion B having a long vertical distance is disposed in the vicinity of the horizontal central portion of the support plate 14, and a short distance portion A having a vertical distance shorter than the long distance portion B at both ends. Is arranged.

本実施形態に係る平膜エレメント10では図1に示すように、支持板14の下端部14bを下に凸状に形成することで、長距離部Bと短距離部Aを形成し、長距離部Bと短距離部Aとを直線で結ぶように支持板14の下端部14bの外形を形成している。このため、支持板14の下端部14bは、下に凸な台形状となる。   In the flat membrane element 10 according to the present embodiment, as shown in FIG. 1, the lower end portion 14 b of the support plate 14 is formed in a convex shape downward, thereby forming the long distance portion B and the short distance portion A. The outer shape of the lower end portion 14b of the support plate 14 is formed so as to connect the portion B and the short distance portion A with a straight line. For this reason, the lower end part 14b of the support plate 14 becomes a trapezoid shape convex downward.

このような外形形状を有する支持板14の主面(板面)には、複数の集水溝16が形成されている。集水溝16は支持板14の両主面に形成され、いずれか一方の端部を、詳細を後述する集水部18に接続することで、詳細を後述する濾膜22を介して主面に接する被処理水を、集水部18へと導くことが可能となる。   A plurality of water collecting grooves 16 are formed on the main surface (plate surface) of the support plate 14 having such an outer shape. The water collecting grooves 16 are formed on both main surfaces of the support plate 14, and one of the end portions is connected to a water collecting portion 18, which will be described in detail later, so that the main surface passes through a filter membrane 22, which will be described in detail later. It is possible to guide the water to be treated in contact with the water collecting section 18.

集水部18は、支持板14の両側面に配置される流水路である。集水部18には吸引口20が設けられ、吸引口20に負圧が印加されることにより、支持板14に形成された集水溝16より吸引された被処理水が、集水部18内部に流れ込み、吸引口20を介して外部へ送水される。集水部18は、支持板14よりも厚みを厚く形成され、集水部18の厚み方向中央部に、支持板14が配置されるように構成されている。このような構成とすることにより、平膜エレメント10を隣接配置した際に、隣り合う平膜エレメント10の支持板14間に隙間を形成することができ、気泡の通過する流路が確保できると共に、詳細を後述する濾膜22同士の接触による濾膜22の破損を防止することができる。なお、濾膜22は、支持板14の両主面に貼付され、被処理水を濾過する役割を担う。   The water collecting portion 18 is a water channel arranged on both side surfaces of the support plate 14. The water collecting portion 18 is provided with a suction port 20, and when negative pressure is applied to the suction port 20, the water to be treated sucked from the water collecting groove 16 formed in the support plate 14 is collected in the water collecting portion 18. It flows into the inside and is fed to the outside through the suction port 20. The water collecting portion 18 is formed to be thicker than the support plate 14, and is configured such that the support plate 14 is disposed at the central portion in the thickness direction of the water collecting portion 18. By adopting such a configuration, when the flat membrane elements 10 are arranged adjacent to each other, a gap can be formed between the support plates 14 of the adjacent flat membrane elements 10, and a flow path through which bubbles pass can be secured. Further, it is possible to prevent damage to the filter membrane 22 due to contact between the filter membranes 22 described later in detail. In addition, the filter membrane 22 is affixed on both main surfaces of the support plate 14, and bears the role which filters to-be-processed water.

図2は、本実施形態に係る平膜エレメント10を複数、隣接配置して構成される平膜ユニット50である。平膜ユニット50は、複数の平膜エレメント10における濾膜22の膜面を対向させ、集水部18を重ね合わせるように配置して構成される。   FIG. 2 shows a flat membrane unit 50 configured by arranging a plurality of flat membrane elements 10 according to this embodiment adjacent to each other. The flat membrane unit 50 is configured such that the membrane surfaces of the filtration membranes 22 in the plurality of flat membrane elements 10 are opposed to each other and the water collecting portions 18 are overlapped.

このように配置された平膜エレメント10では、隣接配置された平膜エレメント10の濾膜22間をエアが通過することにより、隣り合う平膜エレメント10の膜面間に位置する被処理水には、エアリフトの作用による上昇流が生ずることとなる。   In the flat membrane element 10 arranged in this way, the air passes between the filter membranes 22 of the adjacent flat membrane elements 10, so that the treated water located between the membrane surfaces of the adjacent flat membrane elements 10 is treated. As a result, an upward flow is generated by the action of the air lift.

この際、濾膜22の両端側には集水部18が配置されるため、従来の平膜エレメントでは図3(A)に示すように、濾膜上を流れる被処理水の流速は、集水部近傍よりも濾膜中央部の方が抵抗が少なくなるため、濾膜中央部の流れが速くなる。   At this time, since the water collecting portions 18 are arranged at both ends of the filter membrane 22, the flow rate of the water to be treated flowing on the filter membrane is collected in the conventional flat membrane element as shown in FIG. Since the resistance in the central part of the membrane is less than that in the vicinity of the water part, the flow in the central part of the membrane is faster.

隣接する平膜エレメントの濾膜間に、このような速度分布を有する上昇流が生ずると、流速の高低に基づく圧力差が生ずることとなる。濾膜間に、このような圧力差が生ずると、圧力の低い部分、すなわち流速の早い中央部へ気泡が集中し易くなる。そして、中央部に集中した気泡は合一により粗大化し、上昇速度が加速することでさらなる流速の偏りを生み出すこととなり、濾膜の洗浄効率の低下、具体的には、濾膜端部側の洗浄効率の低下を招くこととなる(図3(B)参照)。また、粗大化して中央に集中した気泡は、平膜エレメントを歪ませて、隣接配置した平膜エレメント間の接触、破損を生じさせる要因にもなる。   When an upward flow having such a velocity distribution is generated between the filter membranes of adjacent flat membrane elements, a pressure difference based on the flow rate is generated. When such a pressure difference occurs between the filter membranes, bubbles tend to concentrate in a low pressure portion, that is, a central portion where the flow velocity is high. And the bubbles concentrated in the central part are coarsened by coalescence, and the rising speed is accelerated, resulting in a further deviation of the flow velocity, resulting in a decrease in the cleaning efficiency of the filter membrane, specifically, on the filter membrane end side. The cleaning efficiency is reduced (see FIG. 3B). Further, the air bubbles which are coarsened and concentrated in the center cause distortion of the flat membrane element, which may cause contact and breakage between adjacent flat membrane elements.

これに対して上述したような特徴を有する本実施形態に係る平膜エレメント10では、集水部18を配置した両端部よりも支持板の中央部の長さを長くしている。上述のような図3(A)に見られる流速分布は、隣接配置された平膜エレメント10における濾膜22の膜面間においても生ずるため、支持板14の対向領域が長いほど、被処理水の受ける抵抗が大きくなり、エアリフトによって生ずる上昇流の速度が加速することを抑制する。そして図4(A)に示すように、本実施形態の平膜エレメント10では、支持板14の長距離部Bにおける対向領域(B−B断面)は、短距離部Aの対向領域(A−A断面)に比べて垂直距離が長い。このため、長距離部Bである支持板14の中央部では、エアリフトによって生ずる上昇流の加速化が生じにくく、圧力差によって生ずる気泡の集中肥大を避けることができる。このため、図4(B)に示すように、気泡を分散させることができる。   In contrast, in the flat membrane element 10 according to the present embodiment having the above-described features, the length of the central portion of the support plate is made longer than both end portions where the water collecting portions 18 are arranged. The flow velocity distribution shown in FIG. 3A as described above also occurs between the membrane surfaces of the filter membranes 22 in the flat membrane elements 10 arranged adjacent to each other. The resistance received by the air increases, and the speed of the upward flow generated by the air lift is prevented from accelerating. As shown in FIG. 4 (A), in the flat membrane element 10 of the present embodiment, the facing region (BB cross section) in the long distance portion B of the support plate 14 is the facing region (A-) of the short distance portion A. The vertical distance is longer than (A cross section). For this reason, in the center part of the support plate 14 which is the long distance part B, acceleration of the upward flow caused by the air lift is unlikely to occur, and the concentrated enlargement of bubbles caused by the pressure difference can be avoided. For this reason, as shown in FIG. 4B, the bubbles can be dispersed.

これにより、濾膜22の洗浄効果の向上、すなわち濾膜22の洗浄率の偏りの防止、および濾膜22の効果的な洗浄による被処理水の濾過効率の向上を図ることが可能となる。また、支持板14を樹脂により構成する平膜エレメント10の歪みを抑制し、濾膜22の接触による破損等も防止することができる。さらに、洗浄効果の向上を図ることができるため、濾膜22の不可逆的な膜閉塞を抑制することができる。これにより、薬品洗浄の頻度を減らすことができ、濾膜寿命の延命化を図ることもできる。   Thereby, it is possible to improve the cleaning effect of the filter membrane 22, that is, to prevent the unevenness of the cleaning rate of the filter membrane 22 and to improve the filtration efficiency of the water to be treated by the effective cleaning of the filter membrane 22. Moreover, the distortion of the flat membrane element 10 which comprises the support plate 14 by resin can be suppressed, and the damage by the contact of the filter membrane 22 etc. can also be prevented. Furthermore, since the cleaning effect can be improved, irreversible membrane blockage of the filter membrane 22 can be suppressed. Thereby, the frequency of chemical cleaning can be reduced, and the life of the membrane can be extended.

図5は、本実施形態に係る平膜エレメント10の第1の変形例である。図1に示す実施形態では、長距離部Bと短距離部Aとを直線で結ぶ形態とし、支持板14の下端部14bに台形形状を形成していた。これに対して図5に示す変形例では、長距離部Bと短距離部Aを曲線で結ぶように、支持板14の下端部14bを形成した。このため、本実施例に係る平膜エレメント10aでは、支持板14の下端部14bの形状が円弧状を成すこととなる。   FIG. 5 is a first modification of the flat membrane element 10 according to the present embodiment. In the embodiment shown in FIG. 1, the long distance portion B and the short distance portion A are connected by a straight line, and the trapezoidal shape is formed on the lower end portion 14 b of the support plate 14. On the other hand, in the modification shown in FIG. 5, the lower end portion 14b of the support plate 14 is formed so as to connect the long distance portion B and the short distance portion A with a curve. For this reason, in the flat membrane element 10a which concerns on a present Example, the shape of the lower end part 14b of the support plate 14 will comprise circular arc shape.

支持板14の形状をこのようなものとした場合であっても、支持板14の上端部14aと下端部14bとを結ぶ垂直距離に、長距離部Bと短距離部Aを有する構造となるため、上記実施形態に係る平膜エレメント10と同様な効果を得ることができる。   Even when the shape of the support plate 14 is such, the structure having the long distance portion B and the short distance portion A at the vertical distance connecting the upper end portion 14a and the lower end portion 14b of the support plate 14 is obtained. Therefore, the same effect as the flat membrane element 10 according to the above embodiment can be obtained.

図6は、本実施形態に係る平膜エレメント10の第2の変形例である。図5に示した第1の変形例では、支持板14の下端部14b全体を円弧状に形成している。これに対して本変形例に係る平膜エレメント10bでは、長距離部Bを構成する領域(長距離部領域)に直線部を残しつつ、長距離部Bと短距離部Aを結ぶ辺を曲線により構成している。   FIG. 6 is a second modification of the flat membrane element 10 according to the present embodiment. In the first modification shown in FIG. 5, the entire lower end portion 14b of the support plate 14 is formed in an arc shape. On the other hand, in the flat membrane element 10b according to this modified example, the side connecting the long distance part B and the short distance part A is curved while leaving the straight part in the area (long distance part area) constituting the long distance part B. It is constituted by.

支持板14の形状をこのようなものとした場合であっても、支持板14の上端部14aと下端部14bとを結ぶ垂直距離に、長距離部Bと短距離部Aを有する構造となるため、上記実施形態に係る平膜エレメント10と同様な効果を得ることができる。   Even when the shape of the support plate 14 is such, the structure having the long distance portion B and the short distance portion A at the vertical distance connecting the upper end portion 14a and the lower end portion 14b of the support plate 14 is obtained. Therefore, the same effect as the flat membrane element 10 according to the above embodiment can be obtained.

次に、本発明の浸漬平膜エレメントに係る第2の実施形態について、図7を参照して説明する。本実施形態に係る平膜エレメント110は、その殆どの形態を上述した第1の実施形態に係る平膜エレメント10と同一とする。よって、その機能を同一とする箇所には、図面に同一符号を付して、詳細な説明は省略するものとする。   Next, 2nd Embodiment which concerns on the immersion flat membrane element of this invention is described with reference to FIG. The flat membrane element 110 according to the present embodiment has the same configuration as that of the flat membrane element 10 according to the first embodiment described above. Therefore, portions having the same function are denoted by the same reference numerals in the drawings, and detailed description thereof is omitted.

本実施形態に係る平膜エレメント110は、上述した第1の実施形態に係る平膜エレメント10に比べ、支持板14における短距離部Aの形成領域(短距離部領域)を広げ、長距離部Bの形成領域(長距離部領域)を狭めた点を特徴とする。このような形態的特徴を有する平膜エレメント110によれば、濾膜22の両端側(左右側)に位置する短距離部Aの領域を広げたことにより、当該部分に生ずる上昇流の加速度を向上させることができる。このため、気泡の中央集中化が促進されるような粘性の高い被処理水であっても、気泡の中央集中化を効果的に抑制することが可能となる。
なお、その他の構成、作用、効果については、上述した第1の実施形態に係る平膜エレメント10と同様である。
Compared with the flat membrane element 10 according to the first embodiment described above, the flat membrane element 110 according to the present embodiment expands the formation region (short distance portion region) of the short distance portion A in the support plate 14 and increases the long distance portion. It is characterized in that the formation region (long distance portion region) of B is narrowed. According to the flat membrane element 110 having such morphological characteristics, the area of the short-distance portion A located on both ends (left and right sides) of the filter membrane 22 is widened, so that the acceleration of the upward flow generated in the portion is increased. Can be improved. For this reason, even if it is the to-be-processed water with high viscosity which promotes the central concentration of a bubble, it becomes possible to suppress the central concentration of a bubble effectively.
In addition, about another structure, an effect | action, and an effect, it is the same as that of the flat membrane element 10 which concerns on 1st Embodiment mentioned above.

図8は、本実施形態に係る平膜エレメント110の変形例である。本変形例は、上述した第1の実施形態における第1の変形例と同様に、長距離部Bと短距離部Aを曲線で結び、支持板14の下端部14bの形状を円弧状としている。なお、本変形例では、短距離部Aの領域を広く確保しているため、円弧状の下端部14bの両端側に、直線部が設けられることとなる。
支持板14の形状をこのようなものとした場合であっても、上記第2の実施形態に係る平膜エレメント110と同様な効果を得ることができる。
FIG. 8 is a modification of the flat membrane element 110 according to the present embodiment. In the present modification, similarly to the first modification in the first embodiment described above, the long distance portion B and the short distance portion A are connected by a curve, and the shape of the lower end portion 14b of the support plate 14 is an arc shape. . In addition, in this modification, since the area | region of the short distance part A is ensured widely, a linear part will be provided in the both ends side of the circular arc-shaped lower end part 14b.
Even when the shape of the support plate 14 is such, the same effect as the flat membrane element 110 according to the second embodiment can be obtained.

次に、本発明の浸漬平膜エレメントに係る第3の実施形態について、図9を参照して説明する。本実施形態に係る平膜エレメント210も、その殆どの形態を上述した第1、第2の実施形態に係る平膜エレメント10,110と同一としている。よって、その機能を同一とする箇所には、図面に同一符号を付して、詳細な説明は省略するものとする。   Next, 3rd Embodiment which concerns on the immersion flat membrane element of this invention is described with reference to FIG. The flat membrane element 210 according to this embodiment is almost the same as the flat membrane elements 10 and 110 according to the first and second embodiments described above. Therefore, portions having the same function are denoted by the same reference numerals in the drawings, and detailed description thereof is omitted.

本実施形態に係る平膜エレメント210は、支持板14に形成する長距離部Bを一点とし、両端部に位置する短距離部Aに向けて伸びる直線に沿って支持板14の下部形状を定めている。このため、本実施形態に係る平膜エレメント210における支持板14の下端部14bの形状は、下に凸な三角形となる。このような端部形状を有する支持板14を備える平膜エレメント210では、より粘度の高い被処理水であっても、気泡の分散化を図ることができる。   The flat membrane element 210 according to the present embodiment defines the lower shape of the support plate 14 along a straight line extending toward the short distance portion A located at both ends with the long distance portion B formed on the support plate 14 as one point. ing. For this reason, the shape of the lower end part 14b of the support plate 14 in the flat membrane element 210 which concerns on this embodiment becomes a triangle convex downward. In the flat membrane element 210 provided with the support plate 14 having such an end shape, it is possible to disperse the bubbles even if the water to be treated has a higher viscosity.

図10は、本実施形態に係る平膜エレメント210の変形例である。本変形例は、上述した第1の実施形態における第1の変形例と同様に、長距離部Bと短距離部Aを曲線で結んでいるが、本変形例に係る平膜エレメント210aでは、円弧部を上に向けるようにして辺を形成しているため、1点とした長距離部Bが鋭角に張り出す形状となっている。支持板14の形状をこのようなものとした場合であっても、上記第3の実施形態に係る平膜エレメント210と同様な効果を得ることができる。   FIG. 10 is a modification of the flat membrane element 210 according to the present embodiment. In this modified example, the long distance portion B and the short distance portion A are connected by a curve, similarly to the first modified example in the first embodiment described above, but in the flat membrane element 210a according to the modified example, Since the sides are formed so that the arc portion faces upward, the long distance portion B, which is one point, has a shape that projects at an acute angle. Even when the shape of the support plate 14 is as described above, the same effect as that of the flat membrane element 210 according to the third embodiment can be obtained.

次に、本発明の浸漬平膜エレメントに係る第4の実施形態について、図11を参照して説明する。本実施形態に係る平膜エレメント310も、その殆どの形態を上述した第1、第2、および第3の実施形態に係る平膜エレメント10,110,210と同一としている。よって、その機能を同一とする箇所には、図面に同一符号を付して、詳細な説明は省略するものとする。   Next, a fourth embodiment according to the immersed flat membrane element of the present invention will be described with reference to FIG. The flat membrane element 310 according to the present embodiment is almost the same as the flat membrane elements 10, 110, and 210 according to the first, second, and third embodiments described above. Therefore, portions having the same function are denoted by the same reference numerals in the drawings, and detailed description thereof is omitted.

本実施形態に係る平膜エレメント310は図11に示すように、1つの支持板14に対して、複数(図11においては2箇所)の長距離部Bおよび複数(図11においては3箇所)の短距離部Aを備える構成としている。
このような形態とした場合であっても、上述した各実施形態に係る平膜エレメントと同様に、上昇する気泡の分散化を図ることができる。
As shown in FIG. 11, the flat membrane element 310 according to the present embodiment has a plurality of (two places in FIG. 11) long distance portions B and a plurality (three places in FIG. 11) with respect to one support plate 14. The short distance portion A is provided.
Even if it is a case where it is set as such a form, dispersion | distribution of the rising bubble can be aimed at similarly to the flat membrane element which concerns on each embodiment mentioned above.

また、上記実施形態ではいずれも、支持板14の下端部14bの形状のみを変化させ、支持板14の下端部14bに凸部を形成するように示した。しかしながら、長距離部Bの形成は支持板14の上端部14aを利用して行うようにしても良い。例えば第1の実施形態に係る平膜エレメント10の上端部14aを変形させると、図12に示すような形態となり、支持板14の下端部14bに加え上端部14aにも凸状の台形を備えた形態となる。このような形態の支持板14を備える平膜エレメント10cによれば、抵抗となる長距離部Bの長さをより長くすることができる。よって、気泡が中央へ集中し、肥大化することの抑制効果を向上させることができる。   In the above embodiments, only the shape of the lower end portion 14b of the support plate 14 is changed, and a convex portion is formed on the lower end portion 14b of the support plate 14. However, the long distance portion B may be formed by using the upper end portion 14a of the support plate 14. For example, when the upper end portion 14a of the flat membrane element 10 according to the first embodiment is deformed, the form shown in FIG. 12 is obtained, and the upper end portion 14a has a convex trapezoid in addition to the lower end portion 14b of the support plate 14. It becomes a form. According to the flat membrane element 10c provided with the support plate 14 of such a form, the length of the long distance part B used as resistance can be made longer. Therefore, the inhibitory effect of bubbles concentrating to the center and enlarging can be improved.

10………平膜エレメント、12………ベースフレーム、14………支持板、14a………上端部、14b………下端部、16………集水溝、18………集水部、20………吸引口、22………濾膜、50………平膜ユニット。 10 ......... Flat membrane element, 12 ......... Base frame, 14 ......... Support plate, 14a ......... Upper end, 14b ......... Lower end, 16 ......... Water collecting groove, 18 ......... Water collecting Part, 20 ......... suction port, 22 ...... filter membrane, 50 ...... flat membrane unit.

Claims (5)

処理槽内の被処理水中に、濾膜面を対向させて隣接配置された複数の平膜エレメントを垂直に浸漬させ、前記複数の平膜エレメントの下方に散気手段を配置した浸漬平膜濾過装置の平膜エレメントであって、
集水溝を有する支持板と当該支持板の側面に配置される集水部とを有するベースフレームと、
前記支持板の両主面に配置される濾膜を備え、
前記支持板の上端部と下端部とを結ぶ垂直距離に、水平方向における変化を持たせ、長距離部と短距離部を設けたことを特徴とする浸漬平膜エレメント。
Submerged flat membrane filtration in which a plurality of flat membrane elements arranged adjacent to each other with the membrane surface facing each other are vertically immersed in the water to be treated in the treatment tank, and a diffuser is disposed below the plurality of flat membrane elements. A flat membrane element of the device,
A base frame having a support plate having a water collecting groove and a water collecting portion disposed on a side surface of the support plate;
Comprising a filter membrane disposed on both main surfaces of the support plate;
An immersion flat membrane element characterized in that a vertical distance connecting the upper end portion and the lower end portion of the support plate is changed in the horizontal direction to provide a long distance portion and a short distance portion.
前記支持板の上端部および下端部のうちの少なくとも一方は、前記長距離部と前記短距離部とを結ぶ直線部を有することを特徴とする請求項1に記載の浸漬平膜エレメント。   2. The immersed flat membrane element according to claim 1, wherein at least one of an upper end portion and a lower end portion of the support plate has a straight portion connecting the long distance portion and the short distance portion. 前記支持板の上端部および下端部のうちの少なくとも一方は、前記長距離部と前記短距離部とを結ぶ曲線部を有することを特徴とする請求項1に記載の浸漬平膜エレメント。   2. The immersed flat membrane element according to claim 1, wherein at least one of an upper end portion and a lower end portion of the support plate has a curved portion connecting the long distance portion and the short distance portion. 前記長距離部は、前記支持板における水平方向中央部に設けられ、
前記短距離部は、前記支持板における水平方向両端部に設けられることを特徴とする請求項1乃至請求項3のいずれか1項に記載の浸漬平膜エレメント。
The long distance portion is provided in a horizontal central portion of the support plate,
4. The submerged flat membrane element according to claim 1, wherein the short distance portion is provided at both ends in the horizontal direction of the support plate. 5.
前記長距離部と前記短距離部は、1つの前記支持板に対して複数設けられることを特徴とする請求項1乃至請求項3のいずれか1項に記載の浸漬平膜エレメント。   4. The submerged flat membrane element according to claim 1, wherein a plurality of the long distance portions and the short distance portions are provided with respect to one of the support plates. 5.
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