JPH0563632U - Hollow fiber membrane filter - Google Patents

Hollow fiber membrane filter

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Publication number
JPH0563632U
JPH0563632U JP333592U JP333592U JPH0563632U JP H0563632 U JPH0563632 U JP H0563632U JP 333592 U JP333592 U JP 333592U JP 333592 U JP333592 U JP 333592U JP H0563632 U JPH0563632 U JP H0563632U
Authority
JP
Japan
Prior art keywords
hollow fiber
fiber membrane
fiber membranes
membranes
membrane filter
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP333592U
Other languages
Japanese (ja)
Inventor
浩志 小林
晃弘 長野
悦朗 有川
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sanki Engineering Co Ltd
Original Assignee
Sanki Engineering Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sanki Engineering Co Ltd filed Critical Sanki Engineering Co Ltd
Priority to JP333592U priority Critical patent/JPH0563632U/en
Publication of JPH0563632U publication Critical patent/JPH0563632U/en
Pending legal-status Critical Current

Links

Abstract

(57)【要約】 【目的】 本考案は、中空糸膜濾過器に関し、中空糸膜
の表面積を確保して中空糸膜の機能を十分に発揮すると
共に中空糸膜間での被濾過物質の閉塞を防止することを
目的とする。 【構成】 両端又は一端が開口する多数の中空糸膜を一
列にして両端部を型枠で支持固定すると共に、多数の中
空糸膜と連通する濾過液通路を備えた中空糸膜濾過部材
を、所定の間隔で連設すると共に、各濾過液通路を連結
する構成とした。
(57) [Summary] [PROBLEMS] The present invention relates to a hollow fiber membrane filter, which secures the surface area of the hollow fiber membrane so that the function of the hollow fiber membrane is sufficiently exerted and the substance to be filtered between the hollow fiber membranes is The purpose is to prevent blockage. A hollow fiber membrane filtering member having a plurality of hollow fiber membranes having both ends or one end open in a row and having both ends supported and fixed by a mold and having a filtrate passage communicating with the plurality of hollow fiber membranes, The filtration liquid passages are connected at predetermined intervals and are connected to each other.

Description

【考案の詳細な説明】[Detailed description of the device]

【0001】[0001]

【産業上の利用分野】[Industrial applications]

本考案は、中空糸膜濾過器に関するものである。 The present invention relates to a hollow fiber membrane filter.

【0002】[0002]

【従来の技術】[Prior Art]

中空糸膜は、例えば、精密濾過,限外濾過等の透過膜として知られている。 従来、この中空糸膜を用いた濾過装置としては、例えば、実公平3−5097 5号公報等に開示されているものが知られている。 Hollow fiber membranes are known as permeable membranes for, for example, microfiltration and ultrafiltration. Conventionally, as a filtration device using this hollow fiber membrane, for example, one disclosed in Japanese Utility Model Publication No. 3-50975 is known.

【0003】 この種の中空糸膜濾過器では、多数の中空糸膜の両端を接着剤で外筒内に固定 シールし、両端を開口したものが用いられている。 この種の中空糸膜濾過器を用いて原液を精密濾過,限外濾過等の透過膜で濾過 していくと、膜を透過しない物質は、膜表面に集まり(濃度分極という)、やが てゲル状の物質を形成し、膜の濾過速度を低下させる。In this type of hollow fiber membrane filter, a large number of hollow fiber membranes having both ends fixed and sealed in an outer cylinder with an adhesive are used. When the undiluted solution is filtered through a permeable membrane such as microfiltration and ultrafiltration using this type of hollow fiber membrane filter, substances that do not permeate the membrane gather on the membrane surface (called concentration polarization), and eventually. It forms a gel-like substance which reduces the filtration rate of the membrane.

【0004】 通常の膜分離操作では、これらの濃度分極やゲル層の形成を抑え、効率的に濾 過を行う方法としてクロスフイルトレーション(十字流濾過)が行われている。 この方法は、原液を膜の表面上に高速で流し、乱流状態として、膜面での濃度 勾配を少なくし、ゲル層の発達を防止するものである。In a normal membrane separation operation, cross filtration (cross flow filtration) is carried out as a method of suppressing concentration polarization and formation of a gel layer and efficiently performing filtration. In this method, the undiluted solution is caused to flow over the surface of the membrane at a high speed to create a turbulent state to reduce the concentration gradient on the membrane surface and prevent the development of a gel layer.

【0005】 従って、従来の中空糸膜濾過器では、クロスフイルトレーションによって長期 使用を可能としている。Therefore, the conventional hollow fiber membrane filter enables long-term use by cross filtration.

【0006】[0006]

【考案が解決しようとする課題】[Problems to be solved by the device]

然し、従来の中空糸膜濾過器では、多数の中空糸膜が束ねられて固定されてい るため、1本当たりの表面積が有効に使用されていない。 However, in the conventional hollow fiber membrane filter, since many hollow fiber membranes are bundled and fixed, the surface area per one is not used effectively.

【0007】 而も、多数の中空糸膜が束ねられて固定されているため、中空糸膜間に被濾過 物質が閉塞し易いという不具合がある。 又、多数の中空糸膜が束ねられて固定されているため、外圧濾過の場合には、 洗浄用の空気を中空糸膜の内部まで浸透させるために、例えば、実公平3−50 975号公報に開示される如く、エアー導入経路を形成する必要があり、複雑な 構造となっていた。Further, since many hollow fiber membranes are bundled and fixed, there is a problem that the substance to be filtered is easily clogged between the hollow fiber membranes. Further, since a large number of hollow fiber membranes are bundled and fixed, in the case of external pressure filtration, in order to permeate the cleaning air into the hollow fiber membranes, for example, Japanese Utility Model Publication No. 3-50975. As disclosed in 1), it is necessary to form an air introduction path, which results in a complicated structure.

【0008】 更に、多数の中空糸膜が束ねられて固定されているため、クロスフイルトレー ションによって濾過する際に、その高速で流される原液が十分に行き渡り難く、 ゲル層の発達を防止するのに不完全であった。Further, since a large number of hollow fiber membranes are bundled and fixed, it is difficult for the undiluted solution flowing at a high speed to sufficiently spread during filtration by cross-filtration, which prevents the development of a gel layer. Was incomplete.

【0009】 本考案は斯かる従来の問題点を解決するために為されたもので、その目的は、 中空糸膜の表面積を確保して中空糸膜の機能を十分に発揮すると共に中空糸膜間 での被濾過物質の閉塞を防止することを可能とした中空糸膜濾過器を提供するこ とにある。The present invention has been made to solve such conventional problems, and an object thereof is to secure the surface area of the hollow fiber membrane to sufficiently exhibit the function of the hollow fiber membrane and to perform the function of the hollow fiber membrane. Another object of the present invention is to provide a hollow fiber membrane filter capable of preventing the substance to be filtered from clogging in the space.

【0010】[0010]

【課題を解決するための手段】[Means for Solving the Problems]

本考案に係る中空糸膜濾過器は、両端又は一端が開口する多数の中空糸膜を一 列にして両端部を型枠で支持固定すると共に、多数の中空糸膜と連通する濾過液 通路を備えた中空糸膜濾過部材を、所定の間隔で連設すると共に、各濾過液通路 を連結して成るものである。 The hollow fiber membrane filter according to the present invention has a large number of hollow fiber membranes with both ends or one end open in a row, and both ends are supported and fixed by a formwork, and a filtrate passage communicating with the plurality of hollow fiber membranes is provided. The hollow fiber membrane filtering members provided are continuously provided at a predetermined interval, and each filtrate passage is connected.

【0011】[0011]

【作用】[Action]

本考案に於ては、原液が多数の中空糸膜を透過し、中空糸膜濾過部材の濾過液 通路に濾過液が流入し、各濾過液通路を介して集合部へ流出する。 In the present invention, the undiluted solution permeates a large number of hollow fiber membranes, the filtered solution flows into the filtered solution passages of the hollow fiber membrane filtering member, and flows out to the collecting section via the respective filtered solution passages.

【0012】[0012]

【実施例】【Example】

以下、本考案の実施例を図面に基づいて説明する。 図1は本考案の一実施例に係る中空糸膜濾過器を示し、図に於て、10は中空 糸膜濾過部材を表す。 Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 shows a hollow fiber membrane filter according to an embodiment of the present invention. In the figure, 10 denotes a hollow fiber membrane filtering member.

【0013】 この中空糸膜濾過部材10は、端末111,112が開口する多数の中空糸膜 11を一列にして両端部12,13を型枠14,15で挟んで接着剤20で固定 すると共に、型枠14,15の両端部にほぼU字状を為す枠部材16,17を取 り付け、枠部材16,17内に濾過液通路18,19を形成したものである。In this hollow fiber membrane filtering member 10, a large number of hollow fiber membranes 11 having openings 111 and 112 are arranged in a line, and both ends 12 and 13 are sandwiched between molds 14 and 15 and fixed with an adhesive 20. Frame members 16 and 17 having a substantially U shape are attached to both ends of the mold frames 14 and 15, and filtrate passages 18 and 19 are formed in the frame members 16 and 17, respectively.

【0014】 型枠14,15は、図2及び図4に示す如く、額縁形状を為し、横枠部材14 1及び152には、中空糸膜11を一列にして支持固定するための凹部141a 及び152aが形成されている。As shown in FIGS. 2 and 4, the molds 14 and 15 have a frame shape, and the horizontal frame members 141 and 152 have concave portions 141a for supporting and fixing the hollow fiber membranes 11 in a row. And 152a are formed.

【0015】 そして、横枠部材142及び151の内側は、中空糸膜11を一列にして支持 固定するための載置部142a及び151aを形成する。 又、型枠14,15は、図4及び図8に示す如く、縦枠部材143,144及 び153,154に突起部143a,144a及び153a,154aが設けら れている。Inside the horizontal frame members 142 and 151, mounting portions 142a and 151a for supporting and fixing the hollow fiber membranes 11 in a row are formed. As shown in FIGS. 4 and 8, the molds 14 and 15 are provided with protrusions 143a, 144a and 153a, 154a on the vertical frame members 143, 144 and 153, 154, respectively.

【0016】 更に、枠部材16,17は、図3乃至図7に示す如く、型枠14,15の横枠 部材141,142及び151,152に設けた切欠き部141b,142b及 び151b,152bに嵌合するようになっている。Further, as shown in FIGS. 3 to 7, the frame members 16 and 17 include cutouts 141 b, 142 b and 151 b, which are provided in the horizontal frame members 141, 142 and 151, 152 of the form frames 14, 15, respectively. It is adapted to be fitted to 152b.

【0017】 そして、枠部材16には、濾過液通路18,19と連通する濾過液連通路21 が設けられている。 次に、斯して構成された本実施例は、先ず、図4に示す如く、多数の中空糸膜 11を一列に引き揃えて型枠14の凹部141a及び載置部142a上に並べる 。The frame member 16 is provided with a filtrate communication passage 21 that communicates with the filtrate passages 18 and 19. Next, in the present embodiment thus constituted, first, as shown in FIG. 4, a large number of hollow fiber membranes 11 are aligned in a line and arranged on the concave portion 141a and the mounting portion 142a of the form 14.

【0018】 その後、型枠14に型枠15を重ねる。 この際、多数の中空糸膜11は、型枠14,15の横枠部材141,142及 び151,152より突出する長さのものとする。After that, the mold 15 is overlaid on the mold 14. At this time, the large number of hollow fiber membranes 11 have such a length as to project from the lateral frame members 141, 142 and 151, 152 of the molds 14, 15.

【0019】 そして、型枠14,15の横枠部材141,142及び151,152によっ て挟持されている多数の中空糸膜11を、型枠14,15の横枠部材141,1 42及び151,152と共に接着剤20により接着し、固着した後に、多数の 中空糸膜11の上下端部を切断して端末111,112を開口する。The hollow fiber membranes 11 sandwiched by the horizontal frame members 141, 142 and 151, 152 of the molds 14, 15 are attached to the horizontal frame members 141, 142 of the molds 14, 15 and After bonding and fixing with 151 and 152 by the adhesive agent 20, the upper and lower ends of the hollow fiber membranes 11 are cut to open the terminals 111 and 112.

【0020】 その後、図4に示す如く、多数の中空糸膜11の上下端末111,112の部 位に、枠部材16,17を取り付ける。これらも、図5に示す如く、型枠14, 15の横枠部材141,142及び151,152と縦枠部材143,144及 び153,154にと共に接着剤20により固着される。Thereafter, as shown in FIG. 4, frame members 16 and 17 are attached to the positions of the upper and lower terminals 111 and 112 of the large number of hollow fiber membranes 11. As shown in FIG. 5, these are also fixed to the horizontal frame members 141, 142 and 151, 152 of the molds 14, 15 and the vertical frame members 143, 144 and 153, 154 by the adhesive 20.

【0021】 尚、図6に示す如く、枠部材16の下方側に於ては、中空糸膜11は、凹部1 41aと載置面151aで挟持された形で支持固定されている。又、図示しない が、枠部材17の上方側に於ても、中空糸膜11は、凹部152aと載置面14 2aで挟持された形で支持固定されている。As shown in FIG. 6, on the lower side of the frame member 16, the hollow fiber membrane 11 is supported and fixed by being sandwiched between the recessed portion 141a and the mounting surface 151a. Although not shown, the hollow fiber membrane 11 is also supported and fixed above the frame member 17 by being sandwiched between the recess 152a and the mounting surface 142a.

【0022】 以上の手順に従って、順次中空糸膜濾過部材10を形成する。 そして、図1に示す如く、各中空糸膜濾過部材10を、原液が通過するのに支 承のない間隔を保つための所定の長さを有するスペーサ2を介して連結すると共 に、各濾過液連通路21を連結することによって、中空糸膜濾過器1とすること ができる。According to the above procedure, the hollow fiber membrane filtering member 10 is sequentially formed. Then, as shown in FIG. 1, the hollow fiber membrane filtering members 10 are connected to each other through spacers 2 having a predetermined length for keeping an unsupported space for the undiluted solution to pass through, and the respective filtering devices are also connected. The hollow fiber membrane filter 1 can be obtained by connecting the liquid communication passages 21.

【0023】 斯して構成された中空糸膜濾過器1によれば、これを原液を入れた容器中に浸 漬し、濾過液連通路21に連絡する経路を吸引すると、原液が多数の中空糸膜1 1を透過し、中空糸膜濾過部材10の濾過液通路18,19に濾過液が流入し、 濾過液連通路21を介して集合部へ流出する。According to the hollow fiber membrane filter 1 thus configured, when this is immersed in the container containing the stock solution and the path communicating with the filtrate communication passage 21 is sucked, a large number of the stock solution becomes hollow. The filtered liquid permeates the fiber membrane 11, flows into the filtered liquid passages 18 and 19 of the hollow fiber membrane filtering member 10, and flows out to the collecting portion via the filtered liquid communication passage 21.

【0024】 以上の如く構成された本実施例に係る中空糸膜濾過器1によれば、各中空糸膜 濾過部材10が、多数の中空糸膜11を一列に引き揃えて1組の型枠14,15 によって挟持すると共に接着剤20によって固着されているので、各中空糸膜1 1の周囲が全て原液に浸り、中空糸膜11の表面積を十分に確保することが可能 となる。According to the hollow fiber membrane filter 1 according to the present embodiment configured as described above, each hollow fiber membrane filtering member 10 arranges a large number of hollow fiber membranes 11 in a row to form a set of molds. Since the hollow fiber membranes 11 and 14 are sandwiched and fixed by the adhesive 20, the entire circumference of each hollow fiber membrane 11 is immersed in the undiluted solution, and the surface area of the hollow fiber membranes 11 can be sufficiently secured.

【0025】 又、この中空糸膜濾過器1によれば、従来の中空糸膜を用いた中空糸膜濾過器 の如く中空糸膜11が束なっていないので、懸濁物質を含んだ液体に対しても、 閉塞の少ない外圧型中空糸膜モジュールとすることが可能となる。Further, according to this hollow fiber membrane filter 1, since the hollow fiber membranes 11 are not bundled as in a conventional hollow fiber membrane filter using a hollow fiber membrane, a liquid containing a suspended substance is formed. On the other hand, it becomes possible to obtain an external pressure type hollow fiber membrane module with less clogging.

【0026】 而も、中空糸膜11は、接着剤により固着された後に、両端部が切断されるた め、組付時に中空糸膜11が閉塞するという不具合がない。 又、中空糸膜濾過部材10は、同一形状を為す一対の型枠14,15を組み付 けると共に、上下に枠部材16,17を取り付けることによって形成されるため 、構造が簡単で製作が容易である。Furthermore, since both ends of the hollow fiber membrane 11 are cut after being fixed by an adhesive, there is no problem that the hollow fiber membrane 11 is blocked during assembly. Further, the hollow fiber membrane filtering member 10 is formed by assembling a pair of molds 14 and 15 having the same shape and mounting the frame members 16 and 17 on the upper and lower sides, so that the structure is simple and the manufacturing is easy. Is.

【0027】 更に、本実施例では、枠部材17にも濾過液通路19を設けたから、中空糸膜 11を逆洗して再生する時に、系内の圧力が均一となり、効率良く再生処理する ことができる。Further, in this embodiment, since the frame member 17 is also provided with the filtrate passage 19, the pressure in the system becomes uniform when the hollow fiber membrane 11 is backwashed and regenerated, and the regeneration treatment is performed efficiently. You can

【0028】 更に又、本実施例では、従来の中空糸膜を用いた中空糸膜濾過器の如く中空糸 膜11が束なっていないので、再生時に除去されたゲル状の物質が隣接する中空 糸膜に再付着したり隣接する中空糸膜間に閉塞したりする恐れがなく、再生処理 が効率良く行われる。Furthermore, in this embodiment, since the hollow fiber membranes 11 are not bundled as in the conventional hollow fiber membrane filter using the hollow fiber membranes, the gel-like substance removed during regeneration is adjacent to the hollow fiber membrane. There is no risk of reattachment to the fiber membrane or blockage between adjacent hollow fiber membranes, and the regeneration process is performed efficiently.

【0029】 又、本実施例では、中空糸膜濾過部材10は、同一形状を為す一対の型枠14 ,15を組み付けると共に、上下に枠部材16,17を取り付けることによって 形成されるため、強度があり、中空糸膜濾過器1を振動させて使用する場合等に も耐えることが可能となる。Further, in the present embodiment, the hollow fiber membrane filtering member 10 is formed by assembling a pair of molds 14 and 15 having the same shape and mounting the frame members 16 and 17 on the upper and lower sides. Therefore, it is possible to endure even when the hollow fiber membrane filter 1 is vibrated and used.

【0030】 尚、上記実施例では、縦が15〜20cm、横が30〜60cm程度のものと した。但し、横幅を大きくする場合には、中空糸膜11の安定性を高めるために 横方向に押さえを付設することが好ましい。In the above embodiment, the length is about 15 to 20 cm and the width is about 30 to 60 cm. However, when the horizontal width is increased, it is preferable to additionally provide a presser in the horizontal direction in order to enhance the stability of the hollow fiber membrane 11.

【0031】 又、上記実施例では、枠部材16に予め濾過液連通路21を取り付けた場合に ついて説明したが、枠部材16に濾過液連通路21を取り付けるための孔を設け ておき、各中空糸膜濾過部材10を組み付けた後に、濾過液連通路21を取り付 けても良い。In the above embodiment, the case where the filtrate communication passage 21 is attached to the frame member 16 in advance has been described. However, the frame member 16 is provided with a hole for attaching the filtrate communication passage 21, After the hollow fiber membrane filtration member 10 is assembled, the filtrate communication passage 21 may be attached.

【0032】 更に、上記実施例では、枠部材16に濾過液連通路21を取り付けた場合につ いて説明したが、濾過液連通路21は枠部材17に取り付けも、或いは、枠部材 16及び17に取り付けも良い。Further, in the above embodiment, the case where the filtrate communication passage 21 is attached to the frame member 16 has been described, but the filtrate communication passage 21 may be attached to the frame member 17, or alternatively, the frame members 16 and 17 may be attached. It can also be attached to.

【0033】 更に又、上記実施例では、中空糸膜11の両端111及び112を開口した場 合について説明したが、端部111又は112のみを開口しても良い。 又、上記実施例では、多数の中空糸膜11を一列に引き揃えて型枠14の凹部 141a,142aに並べた後に型枠15を重ね、その後に型枠14,15の横 枠部材141,142及び151,152と共に接着剤20により接着したが、 多数の中空糸膜11を予め一列に引き揃えた後、両端部を接着剤で仮止めしてお き、これを型枠14,15で挟持するようにしても良い。Further, in the above embodiment, the case where both ends 111 and 112 of the hollow fiber membrane 11 are opened has been described, but only the end 111 or 112 may be opened. Further, in the above-described embodiment, a large number of hollow fiber membranes 11 are aligned in a row and arranged in the recesses 141a and 142a of the mold 14, and then the mold 15 is overlapped, and then the horizontal frame members 141 of the molds 14 and 15 are formed. Although it was adhered together with 142 and 151, 152 by the adhesive 20, after preliminarily aligning a large number of the hollow fiber membranes 11 in a line, both ends are temporarily fixed with the adhesive, and this is fixed by the molds 14, 15. It may be sandwiched.

【0034】 尚、図9は、型枠14,15の変形例を示すもので、突起部143a,144 aを有する型枠14に突起部145aを設けると共に、突起部153a,154 aを有する型枠15に突起部155aを設け、両者の突起部145aと155a が対向する面に当接することによって、中空糸膜濾過部材10の両側部を閉鎖す るようにしたものである。FIG. 9 shows a modified example of the molds 14 and 15, in which the mold 14 having the protrusions 143a and 144a is provided with the protrusions 145a and the molds having the protrusions 153a and 154a. Protrusions 155a are provided on the frame 15, and both sides of the hollow fiber membrane filtration member 10 are closed by abutting the opposing surfaces of the protrusions 145a and 155a.

【0035】 この場合には、両側部から原液が流入しないため、両側部の中空糸膜11に無 理な力が作用しなくなる。In this case, since the undiluted solution does not flow in from both sides, the hollow fiber membranes 11 on both sides are not subjected to an excessive force.

【0036】[0036]

【考案の効果】[Effect of the device]

以上説明したように本考案によれば、多数の中空糸膜を一列にして両端部を型 枠で支持固定した中空糸膜濾過部材を用いるので、従来の中空糸膜を束ねて形成 される濾過器に比して、中空糸膜の表面積を有効に利用することができると共に 、中空糸膜間での被濾過物質の閉塞を防止することができる。 As described above, according to the present invention, since a hollow fiber membrane filtering member in which a large number of hollow fiber membranes are arranged in a row and both ends are supported and fixed by a frame is used, a filtration formed by bundling conventional hollow fiber membranes is used. The surface area of the hollow fiber membranes can be effectively used as compared with a container, and the substance to be filtered can be prevented from being blocked between the hollow fiber membranes.

【0037】 又、多数の中空糸膜を一列にして両端部を型枠で支持固定した中空糸膜濾過部 材を用いるので、従来の中空糸膜を束ねて形成される濾過器に比して、再生が確 実に行われ、長期間に亘って安定して使用することができる。Further, since a hollow fiber membrane filtering member in which a large number of hollow fiber membranes are arranged in a row and both ends thereof are supported and fixed by a mold is used, compared to a conventional filter formed by bundling hollow fiber membranes. , It can be regenerated properly and can be used stably for a long time.

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

【図1】本考案の一実施例に係る中空糸膜濾過器を示す
斜視図である。
FIG. 1 is a perspective view showing a hollow fiber membrane filter according to an embodiment of the present invention.

【図2】図1に於ける中空糸膜濾過部材の斜視図であ
る。
FIG. 2 is a perspective view of a hollow fiber membrane filtering member in FIG.

【図3】図2の3−3線に沿った縦断面図である。3 is a vertical cross-sectional view taken along line 3-3 of FIG.

【図4】図2に於ける中空糸膜濾過部材の分解斜視図で
ある。
4 is an exploded perspective view of the hollow fiber membrane filtering member in FIG.

【図5】図2の5−5線に沿った断面図である。5 is a cross-sectional view taken along line 5-5 of FIG.

【図6】図2の6−6線に沿った断面図である。6 is a cross-sectional view taken along line 6-6 of FIG.

【図7】図2の7−7線に沿った断面図である。7 is a cross-sectional view taken along line 7-7 of FIG.

【図8】図2の側面図である。FIG. 8 is a side view of FIG.

【図9】図2の型枠の変形例を示す側面図である。9 is a side view showing a modified example of the mold of FIG. 2. FIG.

【符号の説明】[Explanation of symbols]

1 中空糸膜濾過器 10 中空糸膜濾過部材 11 中空糸膜 111,112 中空糸膜11の端部 12,13 両端部 14,15 型枠 18,19 濾過液通路 1 Hollow Fiber Membrane Filter 10 Hollow Fiber Membrane Filtration Member 11 Hollow Fiber Membrane 111, 112 Ends 12, 13 Ends of Hollow Fiber Membrane 14, 15 Form Frame 18, 19 Filtrate Passage

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】 両端又は一端が開口する多数の中空糸膜
を一列にして両端部を型枠で支持固定すると共に、多数
の中空糸膜と連通する濾過液通路を備えた中空糸膜濾過
部材を、所定の間隔で連設すると共に、各濾過液通路を
連結して成ることを特徴とする中空糸膜濾過器。
1. A hollow fiber membrane filtering member having a large number of hollow fiber membranes having both ends or one end open in a row, both ends being supported and fixed by a formwork, and having a filtrate passage communicating with the many hollow fiber membranes. The hollow fiber membrane filter is characterized in that the filter liquids are continuously connected at a predetermined interval, and each filtrate passage is connected.
JP333592U 1992-01-31 1992-01-31 Hollow fiber membrane filter Pending JPH0563632U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP333592U JPH0563632U (en) 1992-01-31 1992-01-31 Hollow fiber membrane filter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP333592U JPH0563632U (en) 1992-01-31 1992-01-31 Hollow fiber membrane filter

Publications (1)

Publication Number Publication Date
JPH0563632U true JPH0563632U (en) 1993-08-24

Family

ID=11554487

Family Applications (1)

Application Number Title Priority Date Filing Date
JP333592U Pending JPH0563632U (en) 1992-01-31 1992-01-31 Hollow fiber membrane filter

Country Status (1)

Country Link
JP (1) JPH0563632U (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009118785A1 (en) * 2008-03-27 2009-10-01 株式会社クボタ Membrane module and membrane cassette
US7615157B2 (en) 1995-08-11 2009-11-10 Zenon Technology Partnership Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes
KR100937376B1 (en) * 1995-08-11 2010-01-20 제논 테크놀로지 파트너쉽 An apparatus for withdrawing permeate from a substrate and a method of treating water using the same
JP2010194434A (en) * 2009-02-24 2010-09-09 Mitsubishi Rayon Eng Co Ltd Hollow fiber membrane module and water treatment apparatus
EP2402070A1 (en) * 2009-02-24 2012-01-04 Mitsubishi Rayon Co., Ltd. Membrane module unit and assembly method, disassembly method, and maintenance method for same, and water-treatment apparatus

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5281078A (en) * 1975-12-29 1977-07-07 Ebara Infilco Co Ltd Permeable membrane module
JPS63258619A (en) * 1987-04-16 1988-10-26 Kawasaki Heavy Ind Ltd Gas permselective membrane module

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5281078A (en) * 1975-12-29 1977-07-07 Ebara Infilco Co Ltd Permeable membrane module
JPS63258619A (en) * 1987-04-16 1988-10-26 Kawasaki Heavy Ind Ltd Gas permselective membrane module

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7615157B2 (en) 1995-08-11 2009-11-10 Zenon Technology Partnership Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes
KR100937376B1 (en) * 1995-08-11 2010-01-20 제논 테크놀로지 파트너쉽 An apparatus for withdrawing permeate from a substrate and a method of treating water using the same
US7708888B2 (en) 1995-08-11 2010-05-04 Zenon Technology Partnership Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes
KR100979435B1 (en) * 1995-08-11 2010-09-02 제논 테크놀로지 파트너쉽 A method of treating water using an apparatus for withdrawing permeate from a substrate, a process for withdrawing filtered permeate from activated sludge at ambient pressure, and a process for withdrawing filtered permeate from a substrate
KR101008697B1 (en) * 1995-08-11 2011-01-17 제논 테크놀로지 파트너쉽 An apparatus for withdrawing permeate from a substrate and a method for treating water using the same
US8075776B2 (en) 1995-08-11 2011-12-13 Zenon Technology Partnership Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes
WO2009118785A1 (en) * 2008-03-27 2009-10-01 株式会社クボタ Membrane module and membrane cassette
JP2010194434A (en) * 2009-02-24 2010-09-09 Mitsubishi Rayon Eng Co Ltd Hollow fiber membrane module and water treatment apparatus
EP2402070A1 (en) * 2009-02-24 2012-01-04 Mitsubishi Rayon Co., Ltd. Membrane module unit and assembly method, disassembly method, and maintenance method for same, and water-treatment apparatus
EP2402070A4 (en) * 2009-02-24 2013-07-10 Mitsubishi Rayon Co Membrane module unit and assembly method, disassembly method, and maintenance method for same, and water-treatment apparatus
US9446970B2 (en) 2009-02-24 2016-09-20 Mitsubishi Rayon Co., Ltd. Membrane module unit and assembly method, disassembly method, and maintenance method for same, and water-treatment apparatus

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