JP5390499B2 - Hollow fiber membrane module and water treatment apparatus using the same - Google Patents

Hollow fiber membrane module and water treatment apparatus using the same Download PDF

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JP5390499B2
JP5390499B2 JP2010261908A JP2010261908A JP5390499B2 JP 5390499 B2 JP5390499 B2 JP 5390499B2 JP 2010261908 A JP2010261908 A JP 2010261908A JP 2010261908 A JP2010261908 A JP 2010261908A JP 5390499 B2 JP5390499 B2 JP 5390499B2
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hollow fiber
fiber membrane
air
fixing portion
water
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JP2011062696A (en
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進 長谷川
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Shinko Pantec Co Ltd
Asahi Kasei Chemicals Corp
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Asahi Kasei Chemicals Corp
Kobelco Eco Solutions Co Ltd
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本発明は、河川水などの浄水処理、あるいは下水、工業廃水などの膜分離活性汚泥法による汚水浄化処理などに用いられる外圧型の中空糸膜モジュール及び水処理装置に関するものである。   The present invention relates to an external pressure type hollow fiber membrane module and a water treatment device used for water purification treatment of river water or the like, or sewage purification treatment by a membrane separation activated sludge method such as sewage and industrial wastewater.

近年、膜分離活性汚泥法による汚水浄化処理において、生物反応槽内の好気性処理された被処理水(活性汚泥混合液)中に、中空糸膜を上下方向に延びるように保持して起立姿勢にて浸漬されて、中空糸膜内部を吸引することにより被処理水の膜ろ過による固液分離を行って透過水を得る外圧型の中空糸膜モジュールが用いられるようになってきている。   In recent years, in a sewage purification process using a membrane-separated activated sludge method, the hollow fiber membrane is held so as to extend vertically in the aerobic treated water (activated sludge mixed liquid) in the biological reaction tank. An external pressure type hollow fiber membrane module is obtained which is soaked in and is subjected to solid-liquid separation by membrane filtration of water to be treated by sucking the inside of the hollow fiber membrane to obtain permeated water.

そして、この種の中空糸膜モジュールとして、特開2003−326140号公報記載のものが知られている。図7はこの従来の中空糸膜モジュールの概念図であり、一部を断面図で示している。この従来の中空糸膜モジュール70は、図7に示すように、上部固定部72及び下部固定部74を有し、2つの固定部72,74は、支持棒76により連結支持されている。   And as this kind of hollow fiber membrane module, the thing of Unexamined-Japanese-Patent No. 2003-326140 is known. FIG. 7 is a conceptual diagram of this conventional hollow fiber membrane module, and a part thereof is shown in a sectional view. As shown in FIG. 7, the conventional hollow fiber membrane module 70 includes an upper fixing portion 72 and a lower fixing portion 74, and the two fixing portions 72 and 74 are connected and supported by a support rod 76.

上部固定部72は、複数本の中空糸膜の両端を接着した中空糸膜束78の複数を、支持棒76を中心として、その周囲に二重に配置し、支持棒76の両端と共に接着剤80で一体化した構成となっている。中空糸膜束78の上端面は開口されている。そして、上部固定部72はこれと一体となったキャップ73を有しており、このキャップ73は、内部に透過液の集液室75を有し、透過液の集液室75は透過液出口(又は逆圧洗浄水入口)82に繋がっている。一方、中空糸膜束78の下部固定部74側の下端面は、接着剤80により封止されている。   The upper fixing portion 72 is formed by arranging a plurality of hollow fiber membrane bundles 78 in which both ends of a plurality of hollow fiber membranes are bonded around the support rod 76 around the support rod 76. 80 is an integrated configuration. The upper end surface of the hollow fiber membrane bundle 78 is opened. The upper fixing portion 72 has a cap 73 integrated therewith. The cap 73 has a permeate collection chamber 75 therein, and the permeate collection chamber 75 is a permeate outlet. (Or back pressure washing water inlet) 82. On the other hand, the lower end surface of the hollow fiber membrane bundle 78 on the lower fixing portion 74 side is sealed with an adhesive 80.

下部固定部74は、空気供給管84と、複数の空気噴出孔86を有している。空気噴出孔86は、中空糸膜束78同士の間隙や外周に設けられている。このように下部固定部74に設けられた空気の噴出孔86により、中空糸膜束78のエアスクラビングによる洗浄がなされるようになっている。   The lower fixing portion 74 has an air supply pipe 84 and a plurality of air ejection holes 86. The air ejection holes 86 are provided in the gap or the outer periphery of the hollow fiber membrane bundles 78. In this manner, the hollow fiber membrane bundle 78 is cleaned by air scrubbing through the air ejection holes 86 provided in the lower fixing portion 74.

このように構成される中空糸膜モジュール70は、生物反応槽内の被処理水中に、中空糸膜を上下方向に延びるように保持して起立姿勢にて浸漬されて使用される。そして、ろ過運転時には、透過水出口82に連通する吸引ポンプによるろ過を行う。被処理水は、中空糸膜束78を構成する中空糸膜の外表面から内部空間に流入してろ過され、得られた透過水は中空糸膜内を通って、中空糸膜束78の上端面側から排出され、集液室75に流入した後、透過水出口82から排出される。   The hollow fiber membrane module 70 configured as described above is used by being immersed in a standing posture while holding the hollow fiber membrane in the biological water in the biological reaction tank so as to extend in the vertical direction. And at the time of filtration operation, it filters by the suction pump connected to the permeate outlet 82. Water to be treated flows from the outer surface of the hollow fiber membrane constituting the hollow fiber membrane bundle 78 into the internal space and is filtered, and the permeated water obtained passes through the hollow fiber membrane and passes over the hollow fiber membrane bundle 78. After being discharged from the end face side and flowing into the liquid collection chamber 75, it is discharged from the permeate outlet 82.

ろ過運転を長時間継続して行ったとき、中空糸膜の表面に懸濁物質が付着して濾過性能が低下して行くため、下部固定部74に設けられた空気供給管84と空気噴出孔86を用い、必要に応じて、あるいはろ過運転中、常時、エアスクラビングを行って、膜面に付着した懸濁物質(付着物)を取り除くようにしている。   When the filtration operation is continued for a long time, the suspended substance adheres to the surface of the hollow fiber membrane and the filtration performance deteriorates. Therefore, the air supply pipe 84 and the air ejection hole provided in the lower fixing portion 74 No. 86 is used to remove suspended substances (deposits) adhering to the membrane surface by performing air scrubbing as needed or during filtration operation at all times.

特開2003−326140号公報(図1、図2)JP 2003-326140 A (FIGS. 1 and 2)

しかし前述した従来の中空糸膜モジュール70では、下部固定部74に設けられた空気供給管84と空気噴出孔86とによるエアスクラビングを行っても、使用時間の経過とともに髪の毛などの繊維状の夾雑物が、上部固定部72より露出した各中空糸膜束78根元付近に付着したり絡み付いたりして、夾雑物の堆積が起こり易く、夾雑物の堆積による有効膜面積の減少によって透過水量が減少することから、この点において改善すべき余地があった。   However, in the above-described conventional hollow fiber membrane module 70, even if air scrubbing is performed by the air supply pipe 84 and the air ejection hole 86 provided in the lower fixing portion 74, fibrous contamination such as hair is increased over time. The matter adheres to or entangles with the roots of the hollow fiber membrane bundles 78 exposed from the upper fixing portion 72, and the accumulation of contaminants is likely to occur. The amount of permeated water is reduced by reducing the effective membrane area due to the accumulation of contaminants. So there was room for improvement in this regard.

そこで、本発明の課題は、中空糸膜の上端部が固定される上側固定部と、前記中空糸膜の下端部が固定される下側固定部とを備え、各中空糸膜を上下方向に延びるように保持して被処理水中に浸漬される中空糸膜モジュールにおいて、上側固定部より露出した各中空糸膜根元付近での夾雑物の堆積が起こり難く、長期間安定してろ過性能を発揮することができる中空糸膜モジュールを提供することにある。また、長期間にわたって安定して水処理が可能な水処理装置を提供することにある。   Then, the subject of this invention is equipped with the upper side fixing | fixed part to which the upper end part of a hollow fiber membrane is fixed, and the lower side fixing | fixed part to which the lower end part of the said hollow fiber membrane is fixed, and each hollow fiber membrane is made into an up-down direction. In hollow fiber membrane modules that are held so as to be stretched and immersed in the water to be treated, it is difficult for sediment to accumulate near the base of each hollow fiber membrane exposed from the upper fixed part, and stable filtration performance is demonstrated over a long period of time. An object of the present invention is to provide a hollow fiber membrane module that can be used. Another object of the present invention is to provide a water treatment apparatus capable of stably treating water over a long period of time.

前記の課題を解決するため、本願発明では、次の技術的手段を講じている。   In order to solve the above problems, the present invention takes the following technical means.

1の発明は、中空糸膜の上端部が中空糸膜端を開口した状態にて固定される上側固定部と、前記中空糸膜の下端部が中空糸膜端を封止した状態にて固定され、エアスクラビング用の空気導入孔を複数有する下側固定部とを備え、各中空糸膜を上下方向に延びるように保持して被処理水中に浸漬される中空糸膜モジュールにおいて、複数本の中空糸膜が上端部で結合された複数の中空糸膜束を、前記上側固定部の径方向中心を中心とする放射線上に配置して該上側固定部に固定していることを特徴とする中空糸膜モジュールである。 According to a first aspect of the present invention, an upper fixing portion that is fixed in a state in which an upper end portion of the hollow fiber membrane is opened at the end of the hollow fiber membrane, and a lower end portion of the hollow fiber membrane that is sealed at the end of the hollow fiber membrane. A plurality of hollow fiber membrane modules that are fixed and have a lower fixing portion having a plurality of air introduction holes for air scrubbing and that are each immersed in the water to be treated while holding each hollow fiber membrane extending in the vertical direction. A plurality of hollow fiber membrane bundles, in which the hollow fiber membranes are joined at the upper end, are arranged on the radiation centered on the radial center of the upper fixing portion and fixed to the upper fixing portion. This is a hollow fiber membrane module.

2の発明は、第1の発明の中空糸膜モジュールを備えていることを特徴とする水処理装置である。 The second invention is a water treatment apparatus comprising the hollow fiber membrane module of the first invention .

第1の発明の中空糸膜モジュールは、複数本の中空糸膜が上端部で結合された複数の中空糸膜束を、上側固定部の径方向中心を中心とする放射線上に配置して該上側固定部に固定している。したがって、エアスクラビング用の上昇気泡、並びに上昇気泡による被処理水の上昇流は、中空糸膜表面の夾雑物を剥離しながら上昇して上側固定部に近づき、放射線上に配置されている互いに向い合う中空糸膜束列同士の間の領域に導かれ、中心より半径方向外側へ行くに従って広くなる前記領域を流れが妨げられることなく半径方向外側へ流れて上側固定部の外方へ導かれる。これにより、上側固定部より露出した各中空糸膜束根元付近での夾雑物の堆積を起こり難くすることができるので、有効膜面積の減少を防止して長期間安定してろ過性能を発揮することができる。 A hollow fiber membrane module according to a first aspect of the present invention includes a plurality of hollow fiber membrane bundles in which a plurality of hollow fiber membranes are joined at an upper end portion, arranged on a radiation centered on the radial center of the upper fixed portion. It is fixed to the upper fixed part. Therefore, the rising bubbles for air scrubbing and the rising flow of the water to be treated due to the rising bubbles rise while peeling impurities on the surface of the hollow fiber membrane, approach the upper fixing portion, and face each other arranged on the radiation. It is guided to the region between the matching hollow fiber membrane bundle rows, flows in the region that becomes wider as it goes outward in the radial direction from the center, and flows to the outer side in the radial direction without being blocked. As a result, it is possible to prevent the accumulation of impurities in the vicinity of the roots of the hollow fiber membrane bundles exposed from the upper fixing part, so that the effective membrane area is prevented from decreasing and the filtration performance is stably demonstrated for a long period of time. be able to.

第2の発明の水処理装置によれば、前記の中空糸膜モジュールを備えたものであるから、従来に比べて膜モジュール洗浄の間隔を延ばすことができて、長期間にわたって安定して水処理が可能である。 According to the water treatment apparatus of the second aspect of the invention , since the hollow fiber membrane module is provided, the interval between membrane module washing can be extended compared to the conventional case, and the water treatment can be performed stably over a long period of time. Is possible.

本発明の中空糸膜モジュールの一実施形態の構成を示す断面図である。It is sectional drawing which shows the structure of one Embodiment of the hollow fiber membrane module of this invention. 図1における上側固定部に固定された中空糸膜束の配置を示す平面図である。It is a top view which shows arrangement | positioning of the hollow fiber membrane bundle fixed to the upper side fixing | fixed part in FIG. 図1における下側固定部に設けられた空気導入孔の配置を示す平面図である。It is a top view which shows arrangement | positioning of the air introduction hole provided in the lower side fixing | fixed part in FIG. 本発明の中空糸膜モジュールの別の実施形態の構成を示す断面図である。It is sectional drawing which shows the structure of another embodiment of the hollow fiber membrane module of this invention. 本発明の水処理装置の一実施形態を示す構成説明図である。It is composition explanatory drawing which shows one Embodiment of the water treatment apparatus of this invention. 本発明の水処理装置の別の実施形態を示す構成説明図である。It is a structure explanatory view showing another embodiment of the water treatment equipment of the present invention. 従来の中空糸膜モジュールの概念図である。It is a conceptual diagram of the conventional hollow fiber membrane module.

以下、図面に基づき本発明の実施形態について説明する。図1は本発明の中空糸膜モジュールの一実施形態の構成を示す断面図、図2は図1における上側固定部に固定された中空糸膜束の配置を示す平面図、図3は図1における下側固定部に設けられた空気導入孔の配置を示す平面図である。   Hereinafter, embodiments of the present invention will be described with reference to the drawings. FIG. 1 is a cross-sectional view showing the configuration of an embodiment of the hollow fiber membrane module of the present invention, FIG. 2 is a plan view showing the arrangement of hollow fiber membrane bundles fixed to the upper fixing part in FIG. 1, and FIG. It is a top view which shows arrangement | positioning of the air introduction hole provided in the lower side fixing | fixed part in FIG.

図1に示すように、中空糸膜モジュール10は、下側固定部20と、下側固定部20の上方に所定間隔をあけて位置される上側固定部30と、下側固定部20と上側固定部30とをそれらの間隔を保持して支持する上下方向に延びる複数本の支持部材(図示省略)と、下端部がその膜端を封止した状態で下側固定部20に固定され、上端部がその膜端を開口した状態で上側固定部30に固定された多数本の中空糸膜11とにより構成されている。上下方向に延びる多数本の中空糸膜11は、上側固定部30の側において、所定数でなる複数本を上端部で束ねて接着結合した複数の中空糸膜束12に形成されており、これら複数の中空糸膜束12が上側固定部30に固定されている。   As shown in FIG. 1, the hollow fiber membrane module 10 includes a lower fixing portion 20, an upper fixing portion 30 positioned above the lower fixing portion 20 with a predetermined interval, a lower fixing portion 20 and an upper side. A plurality of support members (not shown) extending in the vertical direction to support the fixing portion 30 while maintaining their spacing, and the lower end portion is fixed to the lower fixing portion 20 with its membrane end sealed, The upper end portion is constituted by a plurality of hollow fiber membranes 11 fixed to the upper fixing portion 30 with the membrane end opened. A plurality of hollow fiber membranes 11 extending in the vertical direction are formed into a plurality of hollow fiber membrane bundles 12 on the upper fixing portion 30 side, in which a predetermined number of hollow fiber membranes 11 are bundled and bonded together at the upper end. A plurality of hollow fiber membrane bundles 12 are fixed to the upper fixing portion 30.

上側固定部30は、円筒体31と、透過水出口32aを有して円筒体上側に取り付けられる円形上板32と、膜束貫通孔を有して円筒体下側に取り付けられる円形下板33とにより構成されている。上側固定部30の内側には、複数の中空糸膜束12が、図2に示すように、上側固定部30の径方向中心を中心とする放射線上、本実施形態では径方向中心位置を含めて8本の放射線L1〜L8上に配置されて上側固定部30に固定されている。12aは複数の中空糸膜束12が接着剤にて結合された中空糸膜束結合部分、34は上側固定部30に中空糸膜束12を固定する接着剤部分である。上側固定部30の組立てにあたり、円形下板33の各膜束貫通孔に中空糸膜束12をそれぞれ通してから、中空糸膜束12の間を接着剤で埋めるようにして円筒体31に中空糸膜束12を接着固定し、しかる後、円形下板33が円筒体31に取り付けられるようになっている。   The upper fixing portion 30 includes a cylindrical body 31, a circular upper plate 32 having a permeate outlet 32a and attached to the upper side of the cylindrical body, and a circular lower plate 33 having a membrane bundle through hole and attached to the lower side of the cylindrical body. It is comprised by. As shown in FIG. 2, a plurality of hollow fiber membrane bundles 12 are included inside the upper fixing portion 30 in terms of radiation centering on the radial center of the upper fixing portion 30, in this embodiment, including the radial center position. Are arranged on the eight radiations L <b> 1 to L <b> 8 and fixed to the upper fixing part 30. Reference numeral 12 a denotes a hollow fiber membrane bundle binding portion in which a plurality of hollow fiber membrane bundles 12 are bonded with an adhesive, and 34 denotes an adhesive portion that fixes the hollow fiber membrane bundle 12 to the upper fixing portion 30. When assembling the upper fixing portion 30, the hollow fiber membrane bundle 12 is passed through the respective membrane bundle through holes of the circular lower plate 33, and then the hollow space between the hollow fiber membrane bundles 12 is filled with an adhesive so as to be hollow in the cylindrical body 31. The thread membrane bundle 12 is bonded and fixed, and then the circular lower plate 33 is attached to the cylindrical body 31.

そして、上側固定部30内の上部には、集水室35が形成されており、透過水の集水室35は、各中空糸膜束12を構成する中空糸膜11の上端部の開口に連通しており、円形上板32の下側面、円筒体31の内壁面、中空糸膜束12の上端面及び接着剤部分34により画成されている。この集水室35に繋がる透過水出口32aには、生物反応槽の外部に設置された吸引ポンプからの配管が接続される。   A water collection chamber 35 is formed in the upper portion of the upper fixing portion 30, and the permeated water collection chamber 35 is formed in the opening at the upper end of the hollow fiber membrane 11 constituting each hollow fiber membrane bundle 12. It communicates and is defined by the lower surface of the circular upper plate 32, the inner wall surface of the cylindrical body 31, the upper end surface of the hollow fiber membrane bundle 12, and the adhesive portion 34. A pipe from a suction pump installed outside the biological reaction tank is connected to the permeate outlet 32 a connected to the water collection chamber 35.

また、下側固定部20は、上側固定部30の円筒体31と同一寸法の内径を持つ円筒体21と、エアスクラビング用の本実施形態では8個の空気導入孔23を有して円筒体21内の上部に取り付けられた円板状をなすエアスクラビング用気泡放出部材(以下、単に気泡放出部材という)22とにより構成されている。   Further, the lower fixing portion 20 has a cylindrical body 21 having the same inner diameter as the cylindrical body 31 of the upper fixing portion 30 and eight air introduction holes 23 in the present embodiment for air scrubbing. The air scrubbing bubble releasing member 22 (hereinafter simply referred to as a bubble releasing member) 22 is formed in a disk shape attached to the upper portion of the inside 21.

前記8個の空気導入孔23は、気泡放出部材22において、図3に示すように、上側固定部30における放射線L1〜L8とは位相を角度22.5°だけずらせた放射線L1’〜L8’上であって、径方向中心より所定距離の位置にそれぞれ設けられている。すなわち、空気導入孔23は、上側固定部30における放射線L1〜L8上に配置された互いに向い合う中空糸膜束12列同士の間の位置に対応する下側固定部20における位置に設けられている。なお、図3に示す例とは違って、前記位置に、それぞれ、空気導入孔23を複数個設けるようにしてもよい(図3に示す例では前記位置にそれぞれ1個設けてある)。   As shown in FIG. 3, the eight air introduction holes 23 in the bubble discharge member 22 are radiations L1 ′ to L8 ′ whose phases are shifted from the radiations L1 to L8 in the upper fixing part 30 by an angle of 22.5 °. They are provided at a predetermined distance from the center in the radial direction. That is, the air introduction hole 23 is provided at a position in the lower fixing portion 20 corresponding to a position between the 12 rows of mutually facing hollow fiber membrane bundles arranged on the radiations L1 to L8 in the upper fixing portion 30. Yes. Unlike the example shown in FIG. 3, a plurality of air introduction holes 23 may be provided at each of the positions (one in each of the positions shown in FIG. 3).

この気泡放出部材22の上面には、その空気導入孔23以外の部分に、ほぼ均一に分布させて、中空糸膜束12を形成する中空糸膜11の下端部が中空糸膜端を封止した状態で接着固定されている。また、円筒体21の下端側には、生物反応槽の外部に設置されたブロワからのエアスクラビング用空気供給管25の先端部分が位置されている。このエアスクラビング用空気供給管25より円筒体21内へ空気を圧入し、気泡放出部材22下側の空気溜まり24からの空気を空気導入孔23より気泡として、被処理水中に放出させるようにしている。そして、この気泡の中空糸膜11への衝突、並びに上昇気泡による被処理水の上昇流によって中空糸膜表面の付着物の除去を行うようにしている。   On the upper surface of the bubble releasing member 22, the lower end portion of the hollow fiber membrane 11 forming the hollow fiber membrane bundle 12 is distributed almost uniformly in the portion other than the air introduction hole 23 to seal the end of the hollow fiber membrane. In this state, the adhesive is fixed. Further, a tip portion of an air scrubbing air supply pipe 25 from a blower installed outside the biological reaction tank is positioned on the lower end side of the cylindrical body 21. Air is pressed into the cylindrical body 21 from the air scrubbing air supply pipe 25 so that air from the air reservoir 24 below the bubble release member 22 is discharged as bubbles from the air introduction hole 23 into the water to be treated. Yes. Then, the deposits on the surface of the hollow fiber membrane are removed by the collision of the bubbles with the hollow fiber membrane 11 and the upward flow of the water to be treated by the rising bubbles.

このように、本実施形態による中空糸膜モジュール10は、複数本の中空糸膜11が上端部で結合された複数の中空糸膜束12を、上側固定部30の径方向中心を中心とする放射線上に配置して該上側固定部30(円筒体31)に固定している。したがって、エアスクラビング用の上昇気泡、並び上昇気泡による被処理水の上昇流は、中空糸膜表面の夾雑物や汚泥を剥離しながら上昇して上側固定部30に近づき、放射線L1〜L8上に配置されている互いに向い合う中空糸膜束列同士の間の領域に導かれ、中心より半径方向外側へ行くに従って広くなる前記領域を流れが妨げられることなく半径方向外側へ流れて上側固定部30の外方へ導かれる。これにより、上側固定部30より露出した各中空糸膜束12根元付近での夾雑物や汚泥の堆積を起こり難くすることができるので、有効膜面積の減少を防止して長期間安定してろ過性能を発揮することができる。   Thus, the hollow fiber membrane module 10 according to the present embodiment has a plurality of hollow fiber membrane bundles 12 in which a plurality of hollow fiber membranes 11 are coupled at the upper end as a center in the radial direction of the upper fixing portion 30. It arrange | positions on a radiation and it fixes to this upper side fixing | fixed part 30 (cylindrical body 31). Therefore, ascending bubbles for air scrubbing, and the rising flow of the water to be treated due to the rising bubbles rise while peeling foreign matter and sludge on the surface of the hollow fiber membrane, approach the upper fixing part 30, and on the radiations L1 to L8 The upper fixing portion 30 is guided to the region between the arranged hollow fiber membrane bundle rows that are arranged and flows radially outward without being blocked in the region that becomes wider radially outward from the center. To the outside. As a result, it is possible to prevent accumulation of contaminants and sludge in the vicinity of the roots of the hollow fiber membrane bundles 12 exposed from the upper fixing portion 30, so that the effective membrane area can be prevented from decreasing and filtered stably for a long period of time. Performance can be demonstrated.

この場合、図3に示すように、下側固定部20の空気導入孔23を、上側固定部30における放射線L1〜L8上に配置された互いに向い合う中空糸膜束列同士の間の位置に対応する下側固定部20における位置に設けていることにより、上昇気泡並びに上昇気泡による被処理水の上昇流を、上側固定部30に固定されている互いに向い合う中空糸膜束列同士の間の領域に確実に導くことができる。   In this case, as shown in FIG. 3, the air introduction hole 23 of the lower fixing portion 20 is positioned at a position between the mutually facing hollow fiber membrane bundle rows arranged on the radiations L1 to L8 in the upper fixing portion 30. By providing at the position in the corresponding lower fixing part 20, the rising flow of the rising water and the treated water due to the rising bubble between the hollow fiber membrane bundle rows facing each other fixed to the upper fixing part 30. It is possible to reliably lead to the area.

図4は本発明の中空糸膜モジュールの別の実施形態の構成を示す断面図である。ここで、上側固定部30’が水流方向変換部材(逆円錐形下板36)を備えている点以外は、前記図1〜図3に示される中空糸膜モジュールと同一構成なので、両者の共通する部分には同一の符合を付して説明を省略する。   FIG. 4 is a cross-sectional view showing the configuration of another embodiment of the hollow fiber membrane module of the present invention. Here, since it is the same structure as the hollow fiber membrane module shown by the said FIGS. 1-3 except that the upper side fixing | fixed part 30 'is equipped with the water flow direction change member (inverse conical lower board 36), both are common The same reference numerals are given to the parts to be described, and the description is omitted.

図4に示すように、上側固定部30’は、膜束貫通孔を有して円筒体31下側に取り付けられた逆円錐形下板36を備えている。この逆円錐形下板36は、中心部から外周部へ向かう上向き傾斜面を有しており、エアスクラビング用の上昇気泡並びに上昇気泡による被処理水の上昇流を外方へ導く水流方向変換部材を構成している。   As shown in FIG. 4, the upper fixing portion 30 ′ includes an inverted conical lower plate 36 having a membrane bundle through hole and attached to the lower side of the cylindrical body 31. The inverted conical lower plate 36 has an upward inclined surface from the center portion toward the outer peripheral portion, and a water flow direction changing member that guides the rising flow for air scrubbing and the upward flow of the water to be treated by the rising bubble to the outside. Is configured.

このように、本実施形態による中空糸膜モジュール10’は、中空糸膜束12を放射線上に配置して固定している上側固定部30が、その下面側に水流方向変換部材としての逆円錐形下板36を有する構成としている。したがって、上昇気泡並びに上昇気泡による被処理水の上昇流は、上側固定部30に近づき、放射線上に配置されている互いに向い合う中空糸膜束列同士の間の領域に導かれて上側固定部30に達した後、逆円錐形下板36によって、確実に前記領域を半径方向外側へ流れて上側固定部30の外方へ導かれる。これにより、上側固定部30より露出した各中空糸膜束12根元付近での夾雑物や汚泥の堆積をより確実に起こり難くすることができる。   As described above, in the hollow fiber membrane module 10 ′ according to the present embodiment, the upper fixing portion 30 that fixes the hollow fiber membrane bundle 12 by placing it on the radiation has an inverted cone as a water flow direction changing member on the lower surface side. The lower plate 36 is provided. Accordingly, the rising bubbles and the rising flow of the water to be treated due to the rising bubbles approach the upper fixing portion 30 and are guided to the region between the mutually facing hollow fiber membrane bundle rows arranged on the radiation. After reaching 30, the inverted conical lower plate 36 ensures that the region flows radially outward and is guided out of the upper fixing portion 30. Thereby, accumulation of impurities and sludge near the roots of the hollow fiber membrane bundles 12 exposed from the upper fixing portion 30 can be more reliably prevented.

なお、水流方向変換部材として逆円錐形形状をなす板部材を用いたが、逆円錐台形形状をなす板部材でもよい。   Although the plate member having an inverted conical shape is used as the water flow direction changing member, a plate member having an inverted frustoconical shape may be used.

図5は本発明の水処理装置の一実施形態を示す構成説明図である。   FIG. 5 is a configuration explanatory view showing an embodiment of the water treatment apparatus of the present invention.

この水処理装置40は、本実施形態では被処理水である河川水の浄水処理を行うものである。図5に示すように、水処理装置40は、被処理水供給ライン41からの被処理水(河川水)が供給される被処理水槽42と、この被処理水槽42内の被処理水中に浸漬させて配置された複数の中空糸膜モジュール10’(前記図4に示す構成の中空糸膜モジュール)と、これらの中空糸膜モジュール10’に接続され、吸引ポンプ43aを有して該吸引ポンプ43aによって中空糸膜内部を吸引することにより被処理水の膜ろ過による固液分離を行って透過水を取り出すための透過水取出しライン43と、ブロワ44aを有して中空糸膜モジュール10’にエアスクラビング用空気を供給するためのエアスクラビング用空気供給ライン44と、被処理水槽42内の汚泥を排出するための汚泥排出ライン45とを備えている。   In this embodiment, the water treatment apparatus 40 performs water purification treatment of river water that is to-be-treated water. As shown in FIG. 5, the water treatment device 40 is immersed in the for-treatment water tank 42 to which the for-treatment water (river water) is supplied from the for-treatment water supply line 41 and the for-treatment water in the for-treatment water tank 42. A plurality of hollow fiber membrane modules 10 ′ (hollow fiber membrane modules having the configuration shown in FIG. 4) arranged in this manner, and connected to these hollow fiber membrane modules 10 ′ and having a suction pump 43a, the suction pump A hollow fiber membrane module 10 'having a permeate water extraction line 43 for performing solid-liquid separation by membrane filtration of the water to be treated by suctioning the inside of the hollow fiber membrane by 43a and taking out permeate water, and a blower 44a. An air scrubbing air supply line 44 for supplying air scrubbing air and a sludge discharge line 45 for discharging sludge in the water tank 42 to be treated are provided.

図5において、43bは各中空糸膜モジュール10’の透過水出口32aに接続された集水管、43cは各集水管43bに連通する集水ヘッダー管、43dは透過水取出し管である。集水管43b、集水ヘッダー管43c、透過水取出し管43d及び吸引ポンプ43aは、透過水取出しライン43を構成している。また、44bはブロワ44aによって加圧された空気を供給する空気供給管、25は空気供給管44bから分岐し、その先端部分が各中空糸膜モジュール10’の円筒体21の下端側に位置されるエアスクラビング用空気供給管(図1,図4参照)である。ブロワ44a、空気供給管44b及びエアスクラビング用空気供給管25は、エアスクラビング用空気供給ライン44を構成している。各中空糸膜モジュール10’は、その上側固定部30’の逆円錐形下板36が水面より下方に位置するように設置されている(図5では膜モジュール全体が完全に浸漬されて設置されている)。   In FIG. 5, 43b is a water collection pipe connected to the permeate outlet 32a of each hollow fiber membrane module 10 ', 43c is a water collection header pipe communicating with each water collection pipe 43b, and 43d is a permeate take-out pipe. The water collection pipe 43b, the water collection header pipe 43c, the permeate water take-out pipe 43d, and the suction pump 43a constitute a permeate water take-out line 43. 44b is an air supply pipe for supplying air pressurized by the blower 44a, 25 is branched from the air supply pipe 44b, and the tip portion thereof is positioned on the lower end side of the cylindrical body 21 of each hollow fiber membrane module 10 ′. An air scrubbing air supply pipe (see FIGS. 1 and 4). The blower 44 a, the air supply pipe 44 b, and the air scrubbing air supply pipe 25 constitute an air scrubbing air supply line 44. Each hollow fiber membrane module 10 'is installed such that the inverted conical lower plate 36 of the upper fixing portion 30' is located below the water surface (in FIG. 5, the entire membrane module is completely immersed). ing).

このように構成される水処理装置40によれば、前述した中空糸膜モジュール10’を備えたものであるから、従来に比べて膜モジュール洗浄の間隔を延ばすことができて、長期間にわたって安定して浄水処理を行うことができる。   According to the water treatment apparatus 40 configured as described above, since the above-described hollow fiber membrane module 10 'is provided, the interval between membrane module cleaning can be extended compared to the conventional case, and stable for a long period of time. Water purification treatment can be performed.

図6は本発明の水処理装置の別の実施形態を示す構成説明図である。   FIG. 6 is a configuration explanatory view showing another embodiment of the water treatment apparatus of the present invention.

この水処理装置50は、本実施形態では下水、廃水などの有機性物質を含有する被処理水の汚水浄化処理を膜分離活性汚泥法によって行うものである。図6に示すように、水処理装置50は、被処理水供給ライン51からの一次処理水が供給される被処理水槽としての生物反応槽52と、この生物反応槽52内の被処理水(活性汚泥混合液)中に浸漬させて配置された複数の中空糸膜モジュール10’(前記図4に示す構成の中空糸膜モジュール)と、これらの中空糸膜モジュール10’に接続され、吸引ポンプ53aを有して該吸引ポンプ53aによって中空糸膜内部を吸引することにより被処理水の膜ろ過による固液分離を行って透過水を取り出すための透過水取出しライン53とを備えている。さらに、水処理装置50は、ブロワ54aを有して中空糸膜モジュール10’にエアスクラビング用空気を供給するためのエアスクラビング用空気供給ライン54と、生物反応槽52内における中空糸膜モジュール10’の下方に配置された散気装置56と、生物反応槽52内の汚泥を排出するための汚泥排出ライン55とを備えている。   In this embodiment, the water treatment apparatus 50 performs sewage purification treatment of water to be treated containing organic substances such as sewage and wastewater by a membrane separation activated sludge method. As shown in FIG. 6, the water treatment device 50 includes a biological reaction tank 52 as a water tank to be treated to which primary treated water is supplied from a water supply line 51 to be treated, and water to be treated in the biological reaction tank 52 ( A plurality of hollow fiber membrane modules 10 ′ (hollow fiber membrane modules having the structure shown in FIG. 4) arranged soaked in the activated sludge mixed solution), and suction pumps connected to these hollow fiber membrane modules 10 ′. And a permeated water take-out line 53 for taking out permeated water by performing solid-liquid separation by membrane filtration of water to be treated by suctioning the inside of the hollow fiber membrane by the suction pump 53a. Further, the water treatment device 50 has a blower 54 a and an air scrubbing air supply line 54 for supplying air scrubbing air to the hollow fiber membrane module 10 ′, and the hollow fiber membrane module 10 in the biological reaction tank 52. An air diffuser 56 disposed below 'and a sludge discharge line 55 for discharging sludge in the biological reaction tank 52 are provided.

前記透過水取出しライン53は、集水管53b、集水ヘッダー管53c、透過水取出し管53d及び吸引ポンプ53aにより構成されている。エアスクラビング用空気供給ライン54は、ブロワ54a、空気供給管54b及びエアスクラビング用空気供給管25により構成されている。散気装置56は、この実施形態ではブロワ54aからの加圧された空気が空気供給管54bより分岐した配管を介して供給される。散気装置56は、その散気孔から散気する気泡(空気)によって酸素供給を行って活性汚泥処理(好気性処理)を行うとともに、上昇気泡のエアリフト作用によって生起する上昇流を中空糸膜モジュール10’の膜面に作用させ、膜面洗浄をも行うためのものである。各中空糸膜モジュール10’は、その上側固定部30’の逆円錐形下板36が水面より下方に位置するように設置されている(図6では膜モジュール全体が完全に浸漬されて設置されている)。   The permeated water extraction line 53 includes a water collection pipe 53b, a water collection header pipe 53c, a permeated water extraction pipe 53d, and a suction pump 53a. The air scrubbing air supply line 54 includes a blower 54 a, an air supply pipe 54 b, and an air scrubbing air supply pipe 25. In this embodiment, the air diffuser 56 is supplied with the pressurized air from the blower 54a via a pipe branched from the air supply pipe 54b. The air diffuser 56 performs activated sludge treatment (aerobic treatment) by supplying oxygen with air bubbles (air) diffused from the air diffuser holes, and generates an upward flow generated by the air lift action of the air bubbles to the hollow fiber membrane module. It is for acting on the film surface of 10 'and also performing film surface cleaning. Each hollow fiber membrane module 10 'is installed such that the inverted conical lower plate 36 of the upper fixing portion 30' is positioned below the water surface (in FIG. 6, the entire membrane module is completely immersed). ing).

このように構成される水処理装置50によれば、前述した中空糸膜モジュール10’を備えたものであるから、従来に比べて膜モジュール洗浄の間隔を延ばすことができて、長期間にわたって安定して膜分離活性汚泥法による汚水浄化処理を行うことができる。   According to the water treatment device 50 configured as described above, since the hollow fiber membrane module 10 ′ described above is provided, the interval between membrane module cleaning can be extended as compared with the conventional case, and stable for a long period of time. Thus, the sewage purification treatment by the membrane separation activated sludge method can be performed.

10,10’…中空糸膜モジュール
11…中空糸膜
12…中空糸膜束
12a…中空糸膜束結合部分
20…下側固定部
21…円筒体
22…エアスクラビング用気泡放出部材
23…空気導入孔
24…空気溜まり
25…エアスクラビング用空気供給管
30,30’…上側固定部
31…円筒体
32…円形上板
32a…透過水出口
33…円形下板
34…接着剤部分
35…集水室
36…逆円錐形下板
40…水処理装置
42…被処理水槽
43…透過水取出しライン
44…エアスクラビング用空気供給ライン
50…水処理装置
52…生物反応槽
53…透過水取出しライン
54…エアスクラビング用空気供給ライン
56…散気装置
DESCRIPTION OF SYMBOLS 10,10 '... Hollow fiber membrane module 11 ... Hollow fiber membrane 12 ... Hollow fiber membrane bundle 12a ... Hollow fiber membrane bundle coupling | bond part 20 ... Lower side fixing | fixed part 21 ... Cylinder 22 ... Bubble release member for air scrubbing 23 ... Air introduction Hole 24 ... Air reservoir 25 ... Air scrubbing air supply pipe 30, 30 '... Upper fixing part 31 ... Cylindrical body 32 ... Circular upper plate 32a ... Permeate outlet 33 ... Circular lower plate 34 ... Adhesive part 35 ... Water collecting chamber 36 ... Reverse conical lower plate 40 ... Water treatment device 42 ... Water tank 43 ... Permeate take-out line 44 ... Air scrubbing air supply line 50 ... Water treatment device 52 ... Biological reaction tank 53 ... Permeate take-out line 54 ... Air Scrubbing air supply line 56 ... Air diffuser

Claims (3)

中空糸膜の上端部が中空糸膜端を開口した状態にて固定される上側固定部と、前記中空糸膜の下端部が中空糸膜端を封止した状態にて固定され、エアスクラビング用の空気導入孔を複数有する下側固定部とを備え、各中空糸膜を上下方向に延びるように保持して被処理水中に浸漬される中空糸膜モジュールにおいて、複数本の中空糸膜が上端部で結合された複数の中空糸膜束を、前記上側固定部の径方向中心を中心とする放射線上に配置して該上側固定部に固定し、
前記空気導入孔は、前記上側固定部における前記中空糸膜束の列同士の間の位置に対応する前記下側固定部における位置に設けられ、
前記上側固定部は、前記上側固定部の径方向中心部から外周部へ向かって上向きに傾斜する上向き傾斜面を有していることを特徴とする中空糸膜モジュール。
An upper fixing portion that is fixed with the upper end portion of the hollow fiber membrane being opened at the end of the hollow fiber membrane, and a lower end portion of the hollow fiber membrane that is fixed with the end of the hollow fiber membrane being sealed, for air scrubbing A hollow fixing module having a plurality of air-introducing holes, and holding the hollow fiber membranes so as to extend in the vertical direction and immersing them in the water to be treated. A plurality of bundles of hollow fiber membranes bonded at the portion are arranged on the radiation centered on the radial center of the upper fixing portion and fixed to the upper fixing portion;
The air introduction hole is provided at a position in the lower fixing portion corresponding to a position between the rows of the hollow fiber membrane bundles in the upper fixing portion,
The hollow fiber membrane module, wherein the upper fixing portion has an upward inclined surface that is inclined upward from a radial center portion of the upper fixing portion toward an outer peripheral portion.
請求項1に記載の中空糸膜モジュールを備えていることを特徴とする水処理装置。   A water treatment apparatus comprising the hollow fiber membrane module according to claim 1. 前記下側固定部に前記エアスクラビング用の空気を供給するブロワと、
前記中空糸膜モジュールの下方に配置されるとともに、前記ブロワから空気が供給される散気装置と、
を備える請求項2に記載の水処理装置。
A blower for supplying the air scrubbing air to the lower fixed portion;
An air diffuser disposed below the hollow fiber membrane module and supplied with air from the blower,
The water treatment apparatus of Claim 2 provided with.
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