JP2014014736A - Membrane module and method of producing membrane module, and membrane unit - Google Patents

Membrane module and method of producing membrane module, and membrane unit Download PDF

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JP2014014736A
JP2014014736A JP2012151973A JP2012151973A JP2014014736A JP 2014014736 A JP2014014736 A JP 2014014736A JP 2012151973 A JP2012151973 A JP 2012151973A JP 2012151973 A JP2012151973 A JP 2012151973A JP 2014014736 A JP2014014736 A JP 2014014736A
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membrane
water collecting
membrane module
water
ceramic
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JP5970988B2 (en
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Takayuki Ugajin
孝行 宇賀神
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Meidensha Corp
Meidensha Electric Manufacturing Co Ltd
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    • 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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water desalination
    • Y02A20/131Reverse-osmosis

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Abstract

PROBLEM TO BE SOLVED: To obtain a membrane module and a membrane unit which are excellent in durability and chemical resistance.SOLUTION: A membrane module 1 includes ceramic membranes 2 and water collecting parts 3. The ceramic membrane 2 is a plate-shaped filter member, and the ceramic membranes 2 are juxtaposed so that the principal surfaces 2a thereof face each other with a distance therebetween. The water collecting parts 3 are provided at the ends on the side surface 2c sides of the ceramic membranes 2 to support the ceramic membranes 2. In the water collecting part 3, a water collecting passage 3c is formed by penetrating the water collecting part 3 along the longitudinal direction of the side surface 2c of the ceramic membrane 2. The water collecting passage 3c is formed by communicating with a flow passage of each ceramic membrane 2, and treated water filtered by the ceramic membranes 2 passes through the flow passages to be collected in the water collecting passage 3c. The water collecting part 3 is formed by molding.

Description

本発明は、浄水や産業廃水などを処理する膜モジュール及び膜モジュールの製造方法並びに膜ユニットに関する。   The present invention relates to a membrane module for treating purified water, industrial wastewater, and the like, a method for manufacturing the membrane module, and a membrane unit.

膜分離技術は、従来から海水淡水化、浄水処理、ガス分離、血液浄化等で使用されてきたが、最近では環境保全の観点から、廃水処理にも膜分離技術を適用しようとする研究が進められている。   Membrane separation technology has been used for seawater desalination, water purification, gas separation, blood purification, etc., but recently, from the viewpoint of environmental conservation, research to apply membrane separation technology to wastewater treatment has been promoted. It has been.

従来、浄水処理、下排水処理、あるいは産業廃水の処理等、濁度の高い被処理水の固液分離を行う方法として、砂濾過や重力沈殿等が行われている。しかしながら、これら方法による固液分離は、得られる処理水の水質が不充分となるおそれがあることや、固液分離のために広大な用地を必要とするといった課題を有している。   Conventionally, sand filtration, gravity precipitation, and the like have been performed as methods for solid-liquid separation of water to be treated with high turbidity, such as water purification treatment, sewage treatment, or industrial wastewater treatment. However, solid-liquid separation by these methods has problems that the quality of the treated water obtained may be insufficient and that a vast site is required for solid-liquid separation.

この課題を解決する方法として、近年精密濾過膜、限外濾過膜等の分離膜を配設した膜モジュールを用いて被処理水の固液分離を行う方法が種々検討されている。分離膜を用いて被処理水の濾過処理を行うと、水質の高い処理水を得ることができる。   As a method for solving this problem, various methods for solid-liquid separation of water to be treated using a membrane module provided with a separation membrane such as a microfiltration membrane and an ultrafiltration membrane have been recently studied. When water to be treated is filtered using a separation membrane, treated water with high water quality can be obtained.

膜モジュールは、セラミック膜などの濾過部材と、この濾過部材を保持する集水部を有する(例えば、特許文献1〜4)。集水部は、濾過部材に形成された流路と連通する集水路が形成され、濾過膜で濾過された処理水は、濾過部材の流路及び集水部の集水路を介して系外に排出される。   The membrane module has a filtration member such as a ceramic membrane and a water collecting part that holds the filtration member (for example, Patent Documents 1 to 4). The water collecting part is formed with a water collecting passage communicating with the flow path formed in the filtration member, and the treated water filtered by the filtration membrane is discharged outside the system through the flow path of the filtering member and the water collecting passage of the water collecting part. Discharged.

特開2006−15233号公報JP 2006-15233 A 国際公開第2010/015374号International Publication No. 2010/015374 特開2005−125198号公報JP 2005-125198 A 特開平10−57775号公報Japanese Patent Laid-Open No. 10-57775

しかしながら、特許文献1の膜モジュールの集水部のように、濾過水の取出口をセラミック膜が設けられる面と対向する面に設けると、膜モジュールを多段に積重するときに各取出口に配管接続のコネクタが必要となるなど、膜モジュールのコストが高くなるおそれや組立工程が煩雑になるおそれが生じる。また、セラミック膜を固定するヘッダ部と、取出口が形成されたカバーとにより集水部を形成すると、ヘッダ部とカバーとが対面接合のため、接合強度が弱くなるおそれがある。   However, when the filtered water outlet is provided on the surface opposite to the surface on which the ceramic membrane is provided, as in the water collecting part of the membrane module of Patent Document 1, each outlet is provided when the membrane modules are stacked in multiple stages. There is a risk that the cost of the membrane module may be increased and the assembly process may be complicated, such as the need for a connector for pipe connection. Moreover, if the water collecting part is formed by the header part for fixing the ceramic membrane and the cover on which the outlet is formed, the joining part may be weakened because the header part and the cover are face-to-face joined.

特許文献2の膜モジュールの集水部は、セラミック膜を保持したフレームの開口部をカバープレートで閉塞して集水部を形成しているので、フレーム及びカバープレートの強度によっては膜モジュールを積重したときに膜モジュールの長期信頼性が低下するおそれが生じる。また、個々のセラミック膜を切り欠を有する仕切板で仕切ると、逆圧を作用させてセラミック膜を洗浄する際に、各セラミック膜への圧力伝達が十分に作用せず、洗浄効果が期待できなくなるおそれがある。また、セラミック膜の保持部は平板状ではなく複雑な形状であり、保持部を樹脂で形成する際にセラミック膜の開口部への樹脂の侵入を防止するシール部材を配置することが煩雑となる。例えば、仕切板と個別集水室を形成するための型部材を用いる場合、この型部材の先端部分と開口部が形成されたセラミック膜の側面との間にシール部材を設ける必要があり、シール機能が低下するおそれがある。   The water collecting part of the membrane module of Patent Document 2 forms the water collecting part by closing the opening of the frame holding the ceramic membrane with the cover plate. Therefore, depending on the strength of the frame and the cover plate, the membrane module is loaded. When it overlaps, there exists a possibility that the long-term reliability of a membrane module may fall. In addition, when individual ceramic membranes are partitioned by a partition plate having a notch, when cleaning the ceramic membranes by applying back pressure, the pressure transmission to each ceramic membrane does not act sufficiently, and a cleaning effect can be expected. There is a risk of disappearing. In addition, the holding portion of the ceramic film is not flat and has a complicated shape, and it becomes complicated to arrange a sealing member that prevents the resin from entering the opening of the ceramic film when the holding portion is formed of resin. . For example, when using a mold member for forming a partition plate and an individual water collection chamber, it is necessary to provide a seal member between the tip portion of the mold member and the side surface of the ceramic membrane in which the opening is formed. Function may be degraded.

つまり、集水部を複数の部材を接着剤で接合して形成する場合、接着部の接着不良はリーク発生の原因となるおそれがある。また、膜モジュールの長期信頼性を向上させるために、集水部の耐久性や耐薬品性の向上が求められている。   That is, when the water collecting part is formed by joining a plurality of members with an adhesive, poor adhesion of the adhesive part may cause leakage. Moreover, in order to improve the long-term reliability of a membrane module, improvement of durability and chemical resistance of a water collection part is calculated | required.

上記事情に鑑み、本発明は、膜モジュールの集水部の耐久性及び耐薬品性の向上に寄与する技術の提供を目的としている。   In view of the above circumstances, an object of the present invention is to provide a technique that contributes to an improvement in durability and chemical resistance of a water collecting portion of a membrane module.

上記目的を達成する本発明の膜モジュールは、外表面に濾過膜を有し、この濾過膜で処理された処理水が流通する流路が形成された濾過部材と、この濾過部材を保持するとともに濾過部材の流路と連通する集水路が形成された集水部とを有する膜モジュールであって、集水部を一体に形成すること、及び集水路を集水部の積重方向に貫通して形成することを特徴としている。   The membrane module of the present invention that achieves the above object has a filtration membrane on the outer surface, a filtration member in which a flow path through which treated water treated with this filtration membrane flows is formed, and holds this filtration member A membrane module having a water collecting portion formed with a water collecting passage communicating with the flow path of the filtration member, and forming the water collecting portion integrally, and penetrating the water collecting passage in the stacking direction of the water collecting portion. It is characterized by forming.

また、上記目的を達成する本発明の膜ユニットは、この膜モジュールを積重して構成されることを特徴としている。   In addition, the membrane unit of the present invention that achieves the above object is characterized by being configured by stacking the membrane modules.

また、上記目的を達成する本発明の膜モジュール製造方法は、この膜モジュールの集水部をモールドにより形成することを特徴としている。   Moreover, the membrane module manufacturing method of the present invention that achieves the above object is characterized in that the water collecting portion of the membrane module is formed by molding.

以上の発明によれば、膜モジュールの集水部の耐久性及び耐薬品性の向上に貢献することができる。   According to the above invention, it can contribute to the improvement of durability and chemical resistance of the water collecting part of the membrane module.

本発明の実施形態に係る膜モジュールを示す図であり、(a)上面図、(b)側面図、(c)正面図である。It is a figure which shows the membrane module which concerns on embodiment of this invention, (a) Top view, (b) Side view, (c) Front view. 本発明の実施形態に係る膜モジュールの集水部を示す図であり、(a)A−A断面図、(b)側面図である。It is a figure which shows the water collection part of the membrane module which concerns on embodiment of this invention, (a) AA sectional drawing, (b) It is a side view. 本発明の実施形態に係る膜モジュールの集水部を示す図であり、(a)B−B断面図、(b)上面図である。It is a figure which shows the water collection part of the membrane module which concerns on embodiment of this invention, (a) BB sectional drawing, (b) Top view. 本発明の実施形態に係る膜モジュールの集水部のOリング装着部位を示す図である。It is a figure which shows the O-ring mounting site | part of the water collection part of the membrane module which concerns on embodiment of this invention. 本発明の実施形態に係る膜ユニットを示す図であり、(a)正面図、(b)側面図、(c)膜モジュールを2列設けた場合の正面図である。It is a figure which shows the membrane unit which concerns on embodiment of this invention, (a) Front view, (b) Side view, (c) It is a front view at the time of providing two rows of membrane modules. 本発明の実施形態に係る膜ユニットを示す図であり、(a)上面図、(b)側面図である。It is a figure which shows the membrane unit which concerns on embodiment of this invention, (a) Top view, (b) Side view. 本発明の実施形態に係る膜モジュールの製造方法を説明する説明図であり、(a)セラミック膜を固定した金型及び治具フレームを示す図、(b)セラミック膜を固定した金型の詳細を示す拡大断面図、(c)セラミック膜を固定した金型に樹脂を注型する工程を説明する説明図、(d)注型後に中子を除去する工程を説明する説明図である。It is explanatory drawing explaining the manufacturing method of the membrane module which concerns on embodiment of this invention, (a) The figure which shows the metal mold | die and jig | tool frame which fixed the ceramic membrane, (b) The detail of the metal mold | die which fixed the ceramic membrane. (C) It is explanatory drawing explaining the process of casting resin to the metal mold | die which fixed the ceramic film, (d) It is explanatory drawing explaining the process of removing a core after casting.

本発明の実施形態に係る膜モジュール及び膜モジュールの製造方法並びに膜ユニットについて図を参照して詳細に説明する。   A membrane module, a membrane module manufacturing method, and a membrane unit according to an embodiment of the present invention will be described in detail with reference to the drawings.

[膜モジュール]
図1は、本発明の実施形態に係る膜モジュールを示す図である。図1に示すように、本発明の実施形態に係る膜モジュール1は、セラミック膜2と集水部3を備える。
[Membrane module]
FIG. 1 is a view showing a membrane module according to an embodiment of the present invention. As shown in FIG. 1, a membrane module 1 according to an embodiment of the present invention includes a ceramic membrane 2 and a water collection unit 3.

セラミック膜2は板状の濾過部材である。各セラミック膜2は、セラミック膜2の主面2aが離間して向かい合うように並設される。セラミック膜2の1対の主面2aには、濾過膜が設けられる。セラミック膜2の内部には、この濾過膜を透過した処理水が流通する流路(図示せず)が形成される。図2(a)に示すように、流路の開口部2bはセラミック膜2の側面2cに形成される。なお、膜モジュール1では、流路の開口部2bは、セラミック膜2の両側端面に形成されるが、流路の開口部は、セラミック膜2の少なくとも1側面に設ければよい。   The ceramic membrane 2 is a plate-shaped filtration member. The ceramic films 2 are arranged side by side so that the main surfaces 2a of the ceramic films 2 are spaced apart from each other. A filter membrane is provided on the pair of main surfaces 2 a of the ceramic membrane 2. Inside the ceramic membrane 2, a flow path (not shown) is formed through which treated water that has passed through the filtration membrane flows. As shown in FIG. 2 (a), the opening 2 b of the flow path is formed on the side surface 2 c of the ceramic film 2. In the membrane module 1, the opening 2 b of the flow path is formed on both end surfaces of the ceramic film 2, but the opening of the flow path may be provided on at least one side surface of the ceramic film 2.

集水部3は、セラミック膜2の側面2c側の端部にそれぞれ設けられ、セラミック膜2を保持する。図2(a),(b)に示すように、集水部3の上面には位置決め用の凸部3aが形成され、集水部3の下面には位置決め用の凹部3bが形成される。膜モジュール1を積重する場合、上下に隣接する膜モジュール1の集水部3の凸部3aと凹部3bとが嵌合することで、各膜モジュール1の位置決めが行われる。   The water collecting portions 3 are respectively provided at the end portions on the side surface 2 c side of the ceramic membrane 2 and hold the ceramic membrane 2. As shown in FIGS. 2A and 2B, a positioning convex portion 3 a is formed on the upper surface of the water collecting portion 3, and a positioning concave portion 3 b is formed on the lower surface of the water collecting portion 3. When the membrane modules 1 are stacked, the membrane modules 1 are positioned by fitting the convex portions 3a and the concave portions 3b of the water collecting portions 3 of the membrane modules 1 adjacent to each other in the vertical direction.

図3(a)に示すように、集水部3にはセラミック膜2の側面2cの長手方向に沿うように集水路3cが形成される。この集水路3cは、集水部3を貫通して形成される。図3(b)に示すように、集水路3cは各セラミック膜2の流路2dと連通して形成され、セラミック膜2で濾過された処理水は流路2dを通り、集水路3cに集められる。また、この集水路3cの開口部が形成される集水部3の両端面3d,3dには、集水路3cを囲むように溝部3eが形成される。図4に示すように、膜モジュール1を積重する場合、この溝部3eにOリング4を設けて膜モジュール1を積重することで、積重した膜モジュール1間の水密性が確保される。なお、図3(a)に示すように、集水部3のセラミック膜2を固定する面の対面には溝3fが形成され、この溝3fは、膜モジュール1の積重作業時など膜モジュール1を移動する際の取っ手として用いられる。   As shown in FIG. 3A, a water collection channel 3 c is formed in the water collection unit 3 along the longitudinal direction of the side surface 2 c of the ceramic membrane 2. The water collection channel 3 c is formed through the water collection unit 3. As shown in FIG. 3 (b), the water collection channel 3c is formed in communication with the flow channel 2d of each ceramic membrane 2, and the treated water filtered by the ceramic membrane 2 passes through the flow channel 2d and is collected in the water collection channel 3c. It is done. Moreover, the groove part 3e is formed in the both end surfaces 3d and 3d of the water collection part 3 in which the opening part of this water collection path 3c is formed so that the water collection path 3c may be enclosed. As shown in FIG. 4, when stacking the membrane modules 1, the water tightness between the stacked membrane modules 1 is ensured by providing the O-ring 4 in the groove 3 e and stacking the membrane modules 1. . As shown in FIG. 3 (a), a groove 3f is formed on the surface of the water collecting portion 3 on which the ceramic membrane 2 is fixed, and this groove 3f is formed in the membrane module during stacking work of the membrane module 1 or the like. Used as a handle when moving 1.

集水部3は、例えば、モールドにより形成される。モールドに用いられる材料は、金属、セラミックなどの無機材料及び樹脂などの有機材料から耐久性及び耐薬品性などの条件に基づいて選択される。モールドに用いられる樹脂としては、熱硬化性樹脂、熱可塑性樹脂、二液硬化型樹脂、紫外線硬化型樹脂などがある。これらの樹脂から、耐久性を含め被処理液の性状に対して適する材料が選定される。より具体的には、熱硬化樹脂として、エポキシ樹脂、メラミン樹脂、フェノール樹脂などがあり、熱可塑性樹脂として、塩化ビニル樹脂、ABS樹脂、フッ素樹脂、ポリエチレン、ポリプロピレン、ポリスチレンなどがある。さらには、二液硬化型樹脂として、ウレタン系樹脂などがある。そして、ウレタン系樹脂として硬質ウレタン樹脂を用いると、常温での作業が可能であるので作業性が高く、耐久性及び耐薬品性に優れた集水部3を形成することができる。この硬質ウレタン樹脂としては、水和アルミナ含有ポリエステルポリオール型ウレタン樹脂などが例示される。   The water collection part 3 is formed by a mold, for example. The material used for the mold is selected based on conditions such as durability and chemical resistance from inorganic materials such as metals and ceramics and organic materials such as resins. Examples of the resin used for the mold include a thermosetting resin, a thermoplastic resin, a two-component curable resin, and an ultraviolet curable resin. From these resins, materials suitable for the properties of the liquid to be treated including durability are selected. More specifically, examples of the thermosetting resin include an epoxy resin, a melamine resin, and a phenol resin, and examples of the thermoplastic resin include a vinyl chloride resin, an ABS resin, a fluororesin, polyethylene, polypropylene, and polystyrene. Furthermore, examples of the two-component curable resin include a urethane-based resin. If a hard urethane resin is used as the urethane-based resin, it is possible to work at room temperature, so that the water collection section 3 having high workability and excellent durability and chemical resistance can be formed. Examples of the hard urethane resin include a hydrated alumina-containing polyester polyol type urethane resin.

図5(a),(b)に示すように、膜ユニット6は、架台5上に複数の膜モジュール1を積重して構成される。複数の膜モジュール1は、上下に隣り合う集水部3の凸部3aと凹部3bを嵌合させて膜モジュール1の位置決めを行うとともに、各膜モジュール1の集水部3同士がOリング(図示せず)を介して積重される。積重された膜モジュール1の上下には、膜モジュール固定部材7,7が設けられ、モジュール固定部材7,7をボルト8で締結することで、積重された膜モジュール1が固定される。このように膜モジュール1を積重すると、各膜モジュール1の集水路3c(図示せず)が連通し一つの流路が形成される。膜ユニット6の上端面には、この流路を流通する処理水を排出する濾過水排出口9が設けられる。また、膜ユニット6の上端面にはアイボルト10が設けられ、被処理液中に膜ユニット6を出し入れする際に膜ユニット6を吊下げる。   As shown in FIGS. 5A and 5B, the membrane unit 6 is configured by stacking a plurality of membrane modules 1 on a gantry 5. The plurality of membrane modules 1 are positioned by fitting the convex portions 3a and the concave portions 3b of the water collecting portions 3 adjacent to each other vertically, and the water collecting portions 3 of each membrane module 1 are O-rings ( (Not shown). Membrane module fixing members 7 and 7 are provided above and below the stacked membrane modules 1, and the stacked membrane modules 1 are fixed by fastening the module fixing members 7 and 7 with bolts 8. When the membrane modules 1 are stacked in this way, the water collecting passages 3c (not shown) of the membrane modules 1 communicate with each other to form one flow path. At the upper end surface of the membrane unit 6, a filtered water discharge port 9 for discharging treated water flowing through this flow path is provided. Further, an eyebolt 10 is provided on the upper end surface of the membrane unit 6, and the membrane unit 6 is suspended when the membrane unit 6 is taken in and out of the liquid to be treated.

なお、架台5内部には、図示省略の散気装置などが配置され、散気装置からの気泡により生じる上向流で被処理水が膜モジュール1に導入される。また、図6に示すように、各膜モジュール1の最も外側に位置するセラミック膜2の主面2aに対向して側板11が設けられる。側板11の両側端部にはクップ部11aが設けられ、このクップ部11aをボルト8に係合して膜ユニット6に側板11が設けられる。側板11は断面(D−D断面)コ字状であり、上下に隣り合う側板11同士が係合して側板11が所定の位置に固定される。   An aeration device (not shown) or the like is disposed inside the gantry 5, and the water to be treated is introduced into the membrane module 1 by upward flow generated by bubbles from the aeration device. Further, as shown in FIG. 6, a side plate 11 is provided to face the main surface 2 a of the ceramic membrane 2 located on the outermost side of each membrane module 1. Cup portions 11 a are provided at both side ends of the side plate 11, and the side plates 11 are provided on the membrane unit 6 by engaging the cup portions 11 a with the bolts 8. The side plate 11 has a U-shaped cross section (DD cross section), and the side plates 11 adjacent to each other in the vertical direction are engaged with each other to fix the side plate 11 at a predetermined position.

[膜モジュールの製造方法]
図7を参照して、本発明の実施形態に係る膜モジュール1の製造方法について説明する。
[Membrane module manufacturing method]
With reference to FIG. 7, the manufacturing method of the membrane module 1 which concerns on embodiment of this invention is demonstrated.

図7(a)に示すように、セラミック膜2は、注型用の金型12Aと金型12Bの間に設けられ、このセラミック膜2を固定した金型12Aと金型12Bが治具フレーム13,13で固定される。このとき、治具フレーム13,13間には膜間隔保持治具14が設けられ、各セラミック膜2が所定の間隔をあけて並設される。   As shown in FIG. 7A, the ceramic film 2 is provided between the casting mold 12A and the mold 12B, and the mold 12A and the mold 12B to which the ceramic film 2 is fixed serve as a jig frame. 13 and 13 are fixed. At this time, a film interval holding jig 14 is provided between the jig frames 13 and 13, and the ceramic films 2 are arranged in parallel at a predetermined interval.

図7(b)に示すように、金型12A(及び金型12B)は、中子15a,15bとこの中子15a,15bを保持する外枠16,17から構成される。中子15a,15bには、予め離型剤が塗布される。中子15aには、セラミック膜2の開口部が形成された側面2cが、樹脂侵入防止のためのシール材18を介して貼着される。そして、中子15aのシール材18が貼着された面の反対側の面に中子15bが設けられ、この中子15a,15bが外枠16に固定される。外枠16は一対の開口部を有し、一方の開口部はセラミック膜2が延出し、他方の開口部は外枠17で閉塞される。   As shown in FIG. 7B, the mold 12A (and the mold 12B) includes cores 15a and 15b and outer frames 16 and 17 that hold the cores 15a and 15b. A release agent is applied to the cores 15a and 15b in advance. A side surface 2c in which an opening of the ceramic film 2 is formed is attached to the core 15a via a sealing material 18 for preventing resin intrusion. A core 15 b is provided on the surface of the core 15 a opposite to the surface to which the sealing material 18 is attached, and the cores 15 a and 15 b are fixed to the outer frame 16. The outer frame 16 has a pair of openings, the ceramic film 2 extends from one opening, and the other opening is closed by the outer frame 17.

図7(c)に示すように、シール材18の貼着面を上にして治具フレーム13を立設し、中子15a,15bを固定した外枠16と外枠17で形成される空間部19(図7(b)の図に斜線で示す)に樹脂を注入する。注入された樹脂が固化してセラミック膜2を一体に固定した集水部3が形成される。最後に、図7(d)に示すように、樹脂から中子15b、中子15aの順に除去して集水部3に集水路3cを形成し、その後、外枠16,17を外す。   As shown in FIG. 7C, a space formed by the outer frame 16 and the outer frame 17 in which the jig frame 13 is erected with the sticking surface of the sealing material 18 facing up and the cores 15a and 15b are fixed. Resin is injected into the portion 19 (indicated by hatching in FIG. 7B). The injected resin is solidified to form a water collecting portion 3 in which the ceramic membrane 2 is fixed integrally. Finally, as shown in FIG. 7 (d), the core 15 b and the core 15 a are removed from the resin in this order to form the water collection passage 3 c in the water collection section 3, and then the outer frames 16 and 17 are removed.

以上のように、本発明の膜モジュール及び膜ユニットによれば、濾過部材を保持しこの濾過部材に形成された流路と連通する集水路を有する集水部を一体に形成することで、集水部の耐久性及び耐薬品性が向上する。また、集水部を一体形成することで、集水部の水密性が向上し、集水部を積重したときの耐久性が向上する。   As described above, according to the membrane module and the membrane unit of the present invention, the water collecting part that holds the filtering member and has the water collecting channel that communicates with the flow path formed in the filtering member is integrally formed. The durability and chemical resistance of the water part are improved. Moreover, the water-tightness of a water collection part improves by forming a water collection part integrally, and durability when a water collection part is piled up improves.

また、集水部をモールドで形成すると、接着剤を用いることなく集水部を形成することができ、集水部の水密性及び耐薬品性が向上する。特に、モールド樹脂として耐薬品性に優れる樹脂を用いると、集水部の耐薬品性がさらに向上し、膜モジュール及び膜ユニットの長期信頼性が向上する。また、集水部をモールドで形成することで、濾過部材と集水部の一体化と同時に集水部に集水路を形成することができるので、膜モジュールの生産性が向上する。   Further, when the water collecting part is formed by a mold, the water collecting part can be formed without using an adhesive, and the water tightness and chemical resistance of the water collecting part are improved. In particular, when a resin having excellent chemical resistance is used as the mold resin, the chemical resistance of the water collecting portion is further improved, and the long-term reliability of the membrane module and the membrane unit is improved. In addition, by forming the water collecting part with a mold, a water collecting channel can be formed in the water collecting part simultaneously with the integration of the filtration member and the water collecting part, so that the productivity of the membrane module is improved.

また、集水部が上下に開口していることから、注型時に中子を容易に除去することができ、膜モジュール及び膜ユニットの生産性が向上する。このように集水部を形成することで、Oリングなどの封止材を介して集水部を積重するだけで、積重された集水部間の水密特性を良好に保つことができ、膜ユニットの生産性が向上する。   Moreover, since the water collection part is opened up and down, a core can be easily removed at the time of casting, and the productivity of a membrane module and a membrane unit improves. By forming the water collecting portion in this way, it is possible to maintain good watertight characteristics between the stacked water collecting portions only by stacking the water collecting portions through a sealing material such as an O-ring. The productivity of the membrane unit is improved.

また、本発明の膜モジュール製造方法によれば、集水路が一体に形成された集水部を得ることができるので、膜モジュールの耐久性や耐薬品性が向上する。さらに、集水部への濾過部材の固定と集水部の集水路の形成を同時に行うので、膜モジュールの生産性が向上する。   In addition, according to the membrane module manufacturing method of the present invention, a water collecting part in which a water collecting channel is integrally formed can be obtained, so that the durability and chemical resistance of the membrane module are improved. Furthermore, since the filtration member is fixed to the water collecting portion and the water collecting passage of the water collecting portion is simultaneously formed, the productivity of the membrane module is improved.

なお、本発明の膜モジュール及び膜モジュールの製造方法並びに膜ユニットは、記載された実施形態に限定されるものではなく、その特徴を損なわない範囲で適宜設計変更が可能であり、そのように設計変更された形態も本発明の技術範囲に属する。   The membrane module, the method for manufacturing the membrane module, and the membrane unit of the present invention are not limited to the described embodiments, and can be appropriately modified within a range that does not impair the characteristics thereof. Modified forms also belong to the technical scope of the present invention.

例えば、膜モジュールを構成する濾過部材は、セラミック膜に限定されるものではなく、有機中空糸膜、有機平膜、無機平膜、無機単管膜などを用いることができる。この濾過部材の材質としては、セルロース、ポリオレフィン、ポリスルホン、PVDF(ポリビニリデンフロライド)、PTFE(ポリ四フッ化エチレン)などが例示される。   For example, the filtration member constituting the membrane module is not limited to a ceramic membrane, and an organic hollow fiber membrane, an organic flat membrane, an inorganic flat membrane, an inorganic single tube membrane, or the like can be used. Examples of the material of the filter member include cellulose, polyolefin, polysulfone, PVDF (polyvinylidene fluoride), PTFE (polytetrafluoroethylene), and the like.

また、濾過部材に設けられる分離膜の孔径は、固液分離の対象となる物質の粒径に応じて選択される。例えば、活性汚泥の固液分離に用いるならば、0.5μm以下の孔径を有する濾過膜が用いられ、また、浄水の濾過のように、除菌が必要な場合は0.1μm以下の孔径を有する濾過膜が用いられる。   Moreover, the pore diameter of the separation membrane provided in the filtration member is selected according to the particle diameter of the substance to be subjected to solid-liquid separation. For example, if it is used for solid-liquid separation of activated sludge, a filtration membrane having a pore size of 0.5 μm or less is used, and if sterilization is required, such as filtration of purified water, a pore size of 0.1 μm or less is used. A filtration membrane is used.

また、膜ユニットを構成する膜モジュールの数は、被処理水の処理量や被処理水の水深により適宜必要な数の膜モジュールが用いられる。また、図5(c)に示すように、架台5上に積重した膜モジュール1を並設して膜ユニット6aを構成することもできる。   Moreover, the number of membrane modules which comprise a membrane unit uses a required number of membrane modules suitably according to the processing amount of to-be-processed water, and the water depth of to-be-processed water. Moreover, as shown in FIG.5 (c), the membrane unit 6a can also be comprised by arranging the membrane module 1 piled up on the mount frame 5 in parallel.

1…膜モジュール
2…セラミック膜(濾過部材)
2a…主面、2b…開口部、2c…側面、2d…流路
3…集水部
3a…凸部、3b…凹部、3c…集水路、3d…端面、3e…溝部、3f…溝部
4…Oリング
5…架台
6,6a…膜ユニット
7…膜モジュール固定部材
8…ボルト
9…濾過水排出口
10…アイボルト
11…側板
11a…クップ部
12A,12B…金型
13…治具フレーム
14…膜間隔保持治具
15a,15b…中子
16,17…外枠
18…シール材
19…空間部
DESCRIPTION OF SYMBOLS 1 ... Membrane module 2 ... Ceramic membrane (filtration member)
2a ... Main surface, 2b ... Opening part, 2c ... Side, 2d ... Flow path 3 ... Water collecting part 3a ... Convex part, 3b ... Concave part, 3c ... Water collecting channel, 3d ... End face, 3e ... Groove part, 3f ... Groove part 4 ... O-ring 5 ... frame 6, 6a ... membrane unit 7 ... membrane module fixing member 8 ... bolt 9 ... filtered water discharge port 10 ... eye bolt 11 ... side plate 11a ... cup part 12A, 12B ... mold 13 ... jig frame 14 ... membrane Spacing holding jigs 15a, 15b ... cores 16, 17 ... outer frame 18 ... sealing material 19 ... space

Claims (8)

外表面に設けられる濾過膜と当該濾過膜で濾過された処理液が流通する流路を有する濾過部材と、
一対の端面に開口部を有する集水路が形成され、当該端面間の一側面に前記集水路と前記流路を連通させて前記濾過部材が一体に設けられる集水部と、
を有する
ことを特徴とする膜モジュール。
A filtration member having a filtration membrane provided on the outer surface and a flow path through which a treatment liquid filtered by the filtration membrane flows;
A water collecting channel having an opening at a pair of end surfaces, and a water collecting unit in which the water collecting channel and the flow path communicate with each other on one side surface between the end surfaces, and the filtration member is provided integrally.
A membrane module comprising:
前記集水部を、モールドで形成する
ことを特徴とする請求項1に記載の膜モジュール。
The membrane module according to claim 1, wherein the water collecting part is formed by a mold.
前記集水部を、樹脂で形成する
ことを特徴とする請求項2に記載の膜モジュール。
The membrane module according to claim 2, wherein the water collecting portion is formed of a resin.
前記樹脂は、耐薬品性を有する
ことを特徴とする請求項3に記載の膜モジュール。
The membrane module according to claim 3, wherein the resin has chemical resistance.
前記樹脂は、硬質ウレタン樹脂である
ことを特徴とする請求項4に記載の膜モジュール。
The membrane module according to claim 4, wherein the resin is a hard urethane resin.
前記樹脂は、水和アルミナ含有ポリエステルポリオール型ウレタン樹脂である
ことを特徴とする請求項5に記載の膜モジュール。
6. The membrane module according to claim 5, wherein the resin is a hydrated alumina-containing polyester polyol type urethane resin.
請求項1から6のいずれか1項に記載の膜モジュールを、当該膜モジュールの集水路の開口部が形成される端面を対向させて積重する
ことを特徴とする膜ユニット。
A membrane unit, wherein the membrane module according to any one of claims 1 to 6 is stacked with an end face where an opening of a water collecting channel of the membrane module is formed facing each other.
外表面に設けられる濾過膜と当該濾過膜で濾過された処理液が流通する流路を有する濾過部材を備える膜モジュールの製造方法であって、
前記濾過部材の流路の開口部が形成された面に、シール材を介して中子を設け、
当該中子の外周をモールドし、
前記中子及び前記シール材を除去する
ことを特徴とする膜モジュール製造方法。
A method for producing a membrane module comprising a filtration membrane provided on an outer surface and a filtration member having a flow path through which a treatment liquid filtered by the filtration membrane flows,
A core is provided via a sealing material on the surface where the opening of the flow path of the filtering member is formed,
Mold the outer periphery of the core,
A method for manufacturing a membrane module, wherein the core and the sealing material are removed.
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2016041956A1 (en) * 2014-09-15 2016-03-24 Nanostone Water Gmbh Filter device
WO2016044304A3 (en) * 2014-09-15 2016-05-06 Nanostone Water Inc. Tower filtration module assembly and related methods
KR101905023B1 (en) * 2016-07-07 2018-10-08 주식회사 퓨어엔비텍 Ceramic membranes module
CN115884825A (en) * 2020-08-21 2023-03-31 株式会社明电舍 Flat ceramic membrane

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63240916A (en) * 1987-03-26 1988-10-06 Tsukishima Kikai Co Ltd Gas separating membrane module of hollow yarn
JPH0796149A (en) * 1993-08-05 1995-04-11 Mitsubishi Rayon Co Ltd Hollow-fiber membrane module and its production
JPH07236817A (en) * 1994-02-28 1995-09-12 Mitsubishi Rayon Co Ltd Hollow yarn membrane module
JP2005342690A (en) * 2004-06-07 2005-12-15 Asahi Kasei Chemicals Corp Hollow fiber membrane cartridge
JP2010279878A (en) * 2009-06-03 2010-12-16 Mitsubishi Rayon Co Ltd Method of manufacturing hollow fiber membrane module
JP2011031174A (en) * 2009-07-31 2011-02-17 Sumitomo Electric Fine Polymer Inc Separating membrane module and filter equipped with separating membrane module
WO2011148768A1 (en) * 2010-05-26 2011-12-01 株式会社明電舎 Filtration membrane module

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63240916A (en) * 1987-03-26 1988-10-06 Tsukishima Kikai Co Ltd Gas separating membrane module of hollow yarn
JPH0796149A (en) * 1993-08-05 1995-04-11 Mitsubishi Rayon Co Ltd Hollow-fiber membrane module and its production
JPH07236817A (en) * 1994-02-28 1995-09-12 Mitsubishi Rayon Co Ltd Hollow yarn membrane module
JP2005342690A (en) * 2004-06-07 2005-12-15 Asahi Kasei Chemicals Corp Hollow fiber membrane cartridge
JP2010279878A (en) * 2009-06-03 2010-12-16 Mitsubishi Rayon Co Ltd Method of manufacturing hollow fiber membrane module
JP2011031174A (en) * 2009-07-31 2011-02-17 Sumitomo Electric Fine Polymer Inc Separating membrane module and filter equipped with separating membrane module
WO2011148768A1 (en) * 2010-05-26 2011-12-01 株式会社明電舎 Filtration membrane module

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2016041956A1 (en) * 2014-09-15 2016-03-24 Nanostone Water Gmbh Filter device
WO2016044304A3 (en) * 2014-09-15 2016-05-06 Nanostone Water Inc. Tower filtration module assembly and related methods
CN107106987A (en) * 2014-09-15 2017-08-29 纳诺斯通水务公司 Tower filtering module component and correlation technique
US10427105B2 (en) 2014-09-15 2019-10-01 Nanostone Water Inc. Filter device
KR101905023B1 (en) * 2016-07-07 2018-10-08 주식회사 퓨어엔비텍 Ceramic membranes module
CN115884825A (en) * 2020-08-21 2023-03-31 株式会社明电舍 Flat ceramic membrane
CN115884825B (en) * 2020-08-21 2023-11-14 株式会社明电舍 Flat ceramic membrane

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