JP2002346344A - Immersed filtration apparatus - Google Patents
Immersed filtration apparatusInfo
- Publication number
- JP2002346344A JP2002346344A JP2001153895A JP2001153895A JP2002346344A JP 2002346344 A JP2002346344 A JP 2002346344A JP 2001153895 A JP2001153895 A JP 2001153895A JP 2001153895 A JP2001153895 A JP 2001153895A JP 2002346344 A JP2002346344 A JP 2002346344A
- Authority
- JP
- Japan
- Prior art keywords
- hollow fiber
- fiber membrane
- bundle
- cartridge
- air
- 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.)
- Granted
Links
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、浸漬用濾過装置に
関する。更に詳しくは、槽やタンクに中空糸膜を浸漬
し、し尿、下水、生活排水水、又は工場排水等の浄化処
理に於いて固液分離を行う浸漬型膜濾過装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a filter for immersion. More specifically, the present invention relates to an immersion type membrane filtration device in which a hollow fiber membrane is immersed in a tank or a tank to perform solid-liquid separation in purification treatment of human waste, sewage, domestic wastewater, industrial wastewater, or the like.
【0002】[0002]
【従来の技術】従来の槽やタンクに中空糸膜を浸漬し、
中空糸膜下部に散気管を設け、散気管より噴出空気で中
空糸膜に付着した不純物を剥離させる浸漬用濾過装置の
例としては、特開昭61−107905号公報に示すよ
うな、複数の中空糸膜(上部は接着固定し、下部フリー
端)の下部が開放され、中空糸膜より長い外壁内に収容
され、その下に散気管を設けエアーバブリングを行い、
中空糸膜を振動させ中空糸膜面に付着した不純物を剥離
させ洗浄する濾過装置が記載されている。しかしなが
ら、中空糸膜の下部はフリー端であるため、濾過中にエ
アーバブリングを行う場合、空気流量が多くなると中空
糸膜が浮上したり、中空糸膜同士がからみあったりし、
洗浄が十分に行われないことがある。特にカートリッジ
の直径が大きくなるとこの現象が顕著であり、長期間に
わたって濾過運転を行う場合に支障を来すことがある。2. Description of the Related Art A hollow fiber membrane is immersed in a conventional tank or tank,
An example of an immersion filtration device that provides an air diffuser tube below the hollow fiber membrane and removes impurities adhering to the hollow fiber membrane with air ejected from the air diffuser tube is disclosed in Japanese Patent Application Laid-Open No. 61-107905. The lower part of the hollow fiber membrane (the upper part is adhesively fixed and the lower free end) is opened, housed in the outer wall longer than the hollow fiber membrane, and a diffuser tube is provided below it to perform air bubbling,
A filtration device for vibrating a hollow fiber membrane to remove impurities adhered to the surface of the hollow fiber membrane and washing the same is described. However, since the lower end of the hollow fiber membrane is a free end, when performing air bubbling during filtration, when the air flow rate increases, the hollow fiber membrane floats up or the hollow fiber membranes are entangled with each other,
Cleaning may not be sufficient. In particular, this phenomenon is remarkable when the diameter of the cartridge is large, which may hinder a long-term filtration operation.
【0003】[0003]
【発明が解決しようとする課題】本発明は、中空糸膜の
外表面に堆積した懸濁物を剥離しやすくするとともに、
剥離した懸濁物を中空糸膜カートリッジの外に容易に排
出でき、中空糸膜上下端部への不純物の堆積を防止する
ことが出来る浸漬用濾過装置を提供することを目的とす
るものである。DISCLOSURE OF THE INVENTION The present invention makes it easy to peel off a suspension deposited on the outer surface of a hollow fiber membrane,
It is an object of the present invention to provide an immersion filtration device capable of easily discharging a peeled suspension out of a hollow fiber membrane cartridge and preventing the accumulation of impurities on the upper and lower ends of the hollow fiber membrane. .
【0004】[0004]
【課題を解決するための手段】本発明者らは、上記課題
を解決するために鋭意研究を重ねた結果、浸漬用濾過装
置として、散気管から噴出させた空気を中空糸膜接着固
定下部端部より中空糸膜束内に分散導入し、その時のエ
アードラフト効果により、原水を下接着固定部上の中空
糸膜束外周の外壁開口部より導入し、濃縮液及びエアー
を外壁上端と上接着固定部の間の外壁開放部より放出す
ることにより、その目的に適合し、この知見に基づいて
本発明をなすに至った。Means for Solving the Problems The inventors of the present invention have conducted intensive studies to solve the above-mentioned problems, and as a result, as an immersion filter, air blown out of a diffuser tube is fixed to a lower end of a hollow fiber membrane. The raw water is introduced from the outer wall opening of the outer periphery of the hollow fiber membrane bundle on the lower adhesive fixing part, and the concentrated liquid and air are adhered to the upper end of the outer wall by the air draft effect at that time. The release from the open portion of the outer wall between the fixing portions is suitable for the purpose, and the present invention has been accomplished based on this finding.
【0005】すなわち、本発明は下記の通りである。 1) 垂直に懸垂された中空糸膜下部に設置された散気
管からの噴出空気により中空糸膜面を洗浄しつつ原液を
濾過処理する浸漬用膜分離装置において、中空糸膜上下
端部が接着固定され、下接着固定部は中空糸束内部に空
気を導入出来る構造を有し、上下接着固定部が2本以上
の棒又はパイプで連結固定され、中空糸膜が実質的に露
出している中空糸膜カートリッジを用い、該中空糸膜カ
ートリッジの中空糸膜束外周側面が、中空糸膜束長より
短い、上下が開放された外壁内に、外壁上端と上接着固
定部の間及び外壁下端と下接着固定部の間で中空糸膜束
が露出するように収納されていることを特徴とする浸漬
用濾過装置。That is, the present invention is as follows. 1) The upper and lower ends of a hollow fiber membrane are bonded in a immersion membrane separation device that filters the stock solution while washing the surface of the hollow fiber membrane with air blown out from a diffuser installed below the vertically suspended hollow fiber membrane. It is fixed, the lower adhesive fixing part has a structure capable of introducing air into the hollow fiber bundle, the upper and lower adhesive fixing parts are connected and fixed by two or more rods or pipes, and the hollow fiber membrane is substantially exposed. A hollow fiber membrane cartridge is used, and the outer peripheral side surface of the hollow fiber membrane bundle of the hollow fiber membrane cartridge is shorter than the length of the hollow fiber membrane bundle. A hollow fiber membrane bundle is housed so as to be exposed between the lower adhesive fixing portion and the lower adhesive fixing portion.
【0006】[0006]
【発明の実施の形態】本発明について、以下図により浸
漬濾過装置の実施の形態の一例を具体的に説明する。図
1は本発明に係る浸漬用濾過装置の一実施態様を示す断
面説明図、図2は中空糸膜下接着固定部の構成を説明す
るための要部拡大図である。図1において、本発明で
は、束ねられた中空糸膜3の上部はカートリッジヘッド
2内に一体的に結合され、接着固定されている。カート
リッジヘッド2側の中空糸膜3は端部が開口されてい
る。また、束ねられた中空糸膜3の下部はスカート4内
に一体的に接着固定され、スカート4側の中空糸膜3の
端部は封止されている。スカート4は、図2に例示する
ように、散気管より放出された空気を中空糸膜束内部に
導入し、各中空糸膜外周面に効果的に接触させるため複
数の貫通穴4bが形成されている。BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a perspective view showing an embodiment of an immersion filtration apparatus according to the present invention. FIG. 1 is an explanatory cross-sectional view showing an embodiment of a filter device for immersion according to the present invention, and FIG. In FIG. 1, in the present invention, the upper portion of the bundled hollow fiber membranes 3 is integrally connected to the inside of the cartridge head 2 and is adhesively fixed. The hollow fiber membrane 3 on the side of the cartridge head 2 has an open end. Further, the lower portion of the bundled hollow fiber membranes 3 is integrally bonded and fixed inside the skirt 4, and the end of the hollow fiber membrane 3 on the skirt 4 side is sealed. As illustrated in FIG. 2, the skirt 4 is formed with a plurality of through holes 4b for introducing air released from the air diffuser tube into the inside of the hollow fiber membrane bundle and effectively contacting the outer peripheral surface of each hollow fiber membrane. ing.
【0007】本発明に用いられる中空糸膜3としては、
孔径の点から、限外濾過膜、及び精密濾過膜が好まし
い。カートリッジヘッド2は、中空糸膜カートリッジを
漬浸型濾過装置に懸垂する際の固定部となり、また、原
水と濾水を分離するシール部となるため、カートリッジ
ヘッド2は懸垂、固定、シール機能を併せ持った形状と
なる。例えば、外周部に段差を設けたり、溝を設けた
り、径方向外側に突き出したツバ部を設けたりしてもよ
い。また、カートリッジヘッド2の径方向の断面形状
は、円形のほか、四角形、六角形、楕円形等であっても
よいが、カートリッジヘッド2と接着固定部とのシール
性や濾過タンクの製作の容易さから円形が好ましい。The hollow fiber membrane 3 used in the present invention includes:
Ultrafiltration membranes and microfiltration membranes are preferred in terms of pore size. The cartridge head 2 serves as a fixing portion when suspending the hollow fiber membrane cartridge in the immersion type filtration device, and also serves as a seal portion for separating raw water and filtered water. Therefore, the cartridge head 2 has a suspending, fixing, and sealing function. It has a combined shape. For example, a step may be provided on the outer peripheral portion, a groove may be provided, or a flange portion protruding radially outward may be provided. The radial cross section of the cartridge head 2 may be square, hexagonal, elliptical, or the like, in addition to the circular shape. However, the sealing property between the cartridge head 2 and the adhesive fixing portion and the ease of manufacturing the filtration tank are easy. Therefore, a circle is preferable.
【0008】本発明のスカート側の接着固定層4a(下
接着固定部)に設けられた貫通穴4bは、接着固定層自
体に開けられた穴で、貫通穴の大きさとしては、相当直
径2mm〜30mmの範囲が好ましい。ここで相当直径
は4×(流路断面積)/(周囲辺長)と定義される。貫
通穴の形状としては、三角形、四角形、六角形等の多角
形、円形、楕円形、扇型、C字型、又は星形等が挙げら
れる。また、貫通穴の数は、カートリッジの断面積や糸
の本数にもよるが、2〜300個が好ましい。貫通穴の
位置は、ある接着固定断面について見れば、例えば多重
円と放射状線との交点、格子の交点、又は、多数の正三
角形の頂点の位置などに、接着固定断面上に分散するよ
うに設けることが好ましく、特に中空糸膜束の中心部に
多く設けることが好ましい。The through hole 4b provided in the adhesive fixing layer 4a (lower adhesive fixing portion) on the skirt side of the present invention is a hole formed in the adhesive fixing layer itself, and the size of the through hole is an equivalent diameter of 2 mm. A range of 3030 mm is preferred. Here, the equivalent diameter is defined as 4 × (cross-sectional area of flow path) / (peripheral side length). Examples of the shape of the through hole include a polygon such as a triangle, a square, and a hexagon, a circle, an ellipse, a sector, a C-shape, and a star. The number of through holes depends on the cross-sectional area of the cartridge and the number of threads, but is preferably 2 to 300. The positions of the through holes are distributed on the adhesive fixing cross section at a certain adhesive fixing cross section, for example, at the intersection of the multiple circle and the radial line, the intersection of the lattice, or the position of the vertices of many equilateral triangles. It is preferably provided, particularly preferably a large amount at the center of the hollow fiber membrane bundle.
【0009】本発明では、スカート4は、好ましくは中
空糸膜3の端部より突き出して中空糸膜束と接着固定さ
れ、接着固定層とスカートで囲まれた空気室4cを形成
する。スカート4の中空糸膜端面から突き出した長さ
は、カートリッジの直径、供給される気体量や、貫通穴
の直径と数によるが、気体の散逸を防ぐためには5mm
〜200mmであることが好ましい。スカート4の径方
向の断面形状は、円形のほか、四角形、六角形、楕円形
等であってもよいが、濾過タンクにカートリッジを装着
する場合は、カートリッジヘッドの形状と同じ形状にす
ることが好ましく、特に円形が好ましい。In the present invention, the skirt 4 preferably protrudes from the end of the hollow fiber membrane 3 and is adhered and fixed to the hollow fiber membrane bundle to form an air chamber 4c surrounded by the adhesive fixing layer and the skirt. The length of the skirt 4 protruding from the end face of the hollow fiber membrane depends on the diameter of the cartridge, the amount of supplied gas, and the diameter and number of through holes.
Preferably it is ~ 200 mm. The cross-sectional shape of the skirt 4 in the radial direction may be a circle, a square, a hexagon, an ellipse, or the like, in addition to a circle. However, when a cartridge is mounted on the filtration tank, the same shape as the cartridge head may be used. Preferred, especially circular.
【0010】カートリッジヘッド2接着固定層(上接着
固定部)とスカート4接着固定層(下接着固定部)は、
横方向への曲げやねじりを抑制するため2本以上の棒又
はパイプで連結固定されている。連結固定用の棒又はパ
イプの大きさとしては、相当直径2mm〜30mmの範
囲が好ましい。ここで相当直径は4×(断面積)/(周
囲辺長)と定義される。連結固定用の棒又はパイプの形
状としては、三角形、四角形、六角形等の多角形、円
形、楕円形、扇型、C字型、又は星形等が挙げられる。
特に、円形の形状のものが好ましい。また、その数は、
カートリッジの断面積や糸の本数にもよるが、2〜30
個が好ましく、位置は特に限定されないが、エアーバブ
リング時に下からの力を均一に受けられる様に配置され
ることが好ましい。例えば、糸束の外周部に等間隔に配
置したり、糸束中に分散して配置する事が好ましい。The cartridge head 2 adhesive fixing layer (upper adhesive fixing portion) and the skirt 4 adhesive fixing layer (lower adhesive fixing portion)
It is connected and fixed by two or more rods or pipes to suppress bending and twisting in the lateral direction. The size of the connecting rod or pipe is preferably in the range of an equivalent diameter of 2 mm to 30 mm. Here, the equivalent diameter is defined as 4 × (cross-sectional area) / (peripheral side length). Examples of the shape of the connecting or fixing rod or pipe include a polygon such as a triangle, a square, and a hexagon, a circle, an ellipse, a sector, a C-shape, and a star.
In particular, those having a circular shape are preferable. The number is
Depending on the cross-sectional area of the cartridge and the number of yarns, 2-30
The number is preferably, and the position is not particularly limited. However, it is preferable that the members are arranged so that a force from below can be uniformly received during air bubbling. For example, it is preferable to arrange them at equal intervals on the outer periphery of the yarn bundle or to disperse them in the yarn bundle.
【0011】本発明に使用される外壁7は中空糸膜カー
トリッジで露出している中空糸膜より短い。長さとして
は中空糸膜カートリッジで露出している中空糸膜長より
1〜30cm短い長さが好ましく、2〜10cm短い長
さがより好ましい。また、外壁はスカート4の相当直径
の1.1〜3倍が好ましく、1.2〜2倍がより好まし
い。ここで相当直径は4×(断面積)/(周囲辺長)と
定義される。外壁7の断面形状は、円形のほか、四角
形、六角形、楕円形等であってもよいが、中空糸膜カー
トリッジと同じ形状が好ましい。The outer wall 7 used in the present invention is shorter than the hollow fiber membrane exposed in the hollow fiber membrane cartridge. The length is preferably 1 to 30 cm shorter than the length of the hollow fiber membrane exposed in the hollow fiber membrane cartridge, and more preferably 2 to 10 cm shorter. The outer wall is preferably 1.1 to 3 times the equivalent diameter of the skirt 4, more preferably 1.2 to 2 times. Here, the equivalent diameter is defined as 4 × (cross-sectional area) / (peripheral side length). The cross-sectional shape of the outer wall 7 may be circular, square, hexagonal, elliptical, or the like, but is preferably the same shape as the hollow fiber membrane cartridge.
【0012】また、中空糸膜カートリッジは、中空糸膜
束外周側面が、中空糸膜束長より短い、上下が開放され
た外壁内に、外壁上端と上接着固定部の間及び外壁下端
と下接着固定部の間で中空糸膜束が露出するように収納
されている。また、外壁7は例えばヘッダー配管8や散
気管等により固定される。In the hollow fiber membrane cartridge, the outer peripheral side surface of the hollow fiber membrane bundle is shorter than the length of the hollow fiber membrane bundle, and is provided in an open outer wall between the upper end of the outer wall and the upper adhesive fixing portion and the lower end of the outer wall. The hollow fiber membrane bundle is housed so as to be exposed between the adhesive fixing portions. The outer wall 7 is fixed by, for example, a header pipe 8 or a diffuser pipe.
【0013】[0013]
【実施例1】以下、本発明に係る中空糸膜カートリッジ
を処理水ヘッダー配管に懸垂、固定した浸漬型濾過装置
での運転実施例(図1)を説明する。図1において、中
空糸膜はカートリッジヘッド2により、処理水ヘッダー
配管8に、ガスケットを介してクランプにより懸垂し、
固定されている。上記構成において、浸漬型濾過装置に
よる濾過運転時には、ポンプ(図示せず)により漬浸タ
ンク1上部に設けられた供給水入口10から、原水が浸
漬タンク1に供給される。Embodiment 1 Hereinafter, an embodiment (FIG. 1) of operating a submerged filtration device in which a hollow fiber membrane cartridge according to the present invention is suspended and fixed to a treated water header pipe will be described. In FIG. 1, the hollow fiber membrane is suspended by a cartridge head 2 on a treated water header pipe 8 via a gasket by a clamp,
Fixed. In the above configuration, during a filtration operation by the immersion type filtration device, raw water is supplied to the immersion tank 1 from a supply water inlet 10 provided above the immersion tank 1 by a pump (not shown).
【0014】中空糸膜へのエアーバブリングは、浸漬タ
ンク1に原水を満たした状態で、下部に設けられた散気
管6から浸漬タンク2の内部に気泡状となって流入し、
スカート4に集められ、接着固定層4aの貫通穴4bを
通過して各中空糸膜3内部の外周側面に導かれることに
より行われる。この時に各中空糸膜束内の水を攪拌する
と共に各中空糸膜3を振動させて中空糸膜3の表面に付
着している懸濁物を剥離する。中空糸膜3を振動させた
空気及び剥離した不純物を含む濃縮原水はカートリッジ
ヘッド側の外壁開口部より、浸漬タンク1に排出され
る。The air bubbling of the hollow fiber membrane is carried out in a state of being filled with raw water in the immersion tank 1 from the diffuser pipe 6 provided at the lower part in the form of bubbles into the immersion tank 2.
It is collected by the skirt 4, passed through the through hole 4 b of the adhesive fixing layer 4 a, and guided to the outer peripheral side surface inside each hollow fiber membrane 3. At this time, the water in each bundle of the hollow fiber membranes is stirred and the respective hollow fiber membranes 3 are vibrated to separate the suspension adhered to the surface of the hollow fiber membranes 3. The air which vibrated the hollow fiber membrane 3 and the concentrated raw water containing the separated impurities are discharged into the immersion tank 1 from the outer wall opening on the cartridge head side.
【0015】浸漬タンク1の原水は中空糸膜内のエアー
バブリングによるエアードラフトにより、スカート4と
外壁7下端の開口部より各中空糸膜3に導かれる。各中
空糸膜3の外周部近傍の原水は、中空糸膜3の外部から
内部に陰圧濾過され、その濾水は中空糸膜3の開口され
た上端部から処理水ヘッダー配管8に導かれる。処理水
ヘッダー配管内の濾水は、浸漬タンク1に設けられた処
理水出口から漬浸タンク1の外部に排出される。The raw water in the immersion tank 1 is guided to each hollow fiber membrane 3 from the opening at the lower end of the skirt 4 and the outer wall 7 by air draft by air bubbling in the hollow fiber membrane. Raw water near the outer periphery of each hollow fiber membrane 3 is negatively filtered from the outside to the inside of the hollow fiber membrane 3, and the filtered water is guided to the treated water header pipe 8 from the open upper end of the hollow fiber membrane 3. . The filtrate in the treated water header pipe is discharged from the treated water outlet provided in the immersion tank 1 to the outside of the immersion tank 1.
【0016】上記濾過装置において、原水として合成下
水を供給し、浸漬タンク内の活性汚泥濃度(MLSS)
を8000〜12000mg/Lに維持し、1m3膜面
積当たり1Nm3/hrのエアーバブリングを実施、5
0KPa陰圧濾過運転では、Flux1m/dayで1
ヶ月間安定して運転できた。なお、用いた合成下水の組
成は以下の通りである。 ヘプトン 0.35 (g/L) 肉エキス 0.23 尿素 0.05 NaCl 0.05 KCl 0.015 CaCl2 0.015 MgS04 0.012 K2HPO4 0.935 KH2PO4 0.117 水道水In the above filtration apparatus, synthetic sewage is supplied as raw water, and the activated sludge concentration (MLSS) in the immersion tank is supplied.
Was maintained at 8000 to 12000 mg / L, and air bubbling of 1 Nm 3 / hr per 1 m 3 of membrane area was performed.
In the 0 KPa negative pressure filtration operation, the flux is 1 m / day at 1 m / day.
I was able to drive stably for months. The composition of the synthetic sewage used was as follows. Heptonic 0.35 (g / L) meat extract 0.23 Urea 0.05 NaCl 0.05 KCl 0.015 CaCl 2 0.015 MgS0 4 0.012 K 2 HPO 4 0.935 KH 2 PO 4 0.117 Tap water
【0017】[0017]
【発明の効果】本発明の濾過装置はエアーバブリングに
より各中空糸膜を振動させ、中空糸膜の外表面に堆積し
た懸濁物を剥離しやすくするとともに、エアーバブリン
グによるエアードラフトにより中空糸膜に原水を導入
し、且つ、剥離した懸濁物を中空糸膜カートリッジの外
に容易に排出できる。更に、中空糸膜下端部は原水流入
により、中空糸膜上端部は空気及び濃縮水の排出により
不純物の堆積を防止できる。According to the filtration apparatus of the present invention, each hollow fiber membrane is vibrated by air bubbling to facilitate separation of suspended matter deposited on the outer surface of the hollow fiber membrane, and hollow fiber membrane is formed by air draft by air bubbling. And the separated suspension can be easily discharged out of the hollow fiber membrane cartridge. Further, the lower end of the hollow fiber membrane can prevent the accumulation of impurities by inflow of raw water, and the upper end of the hollow fiber membrane can prevent accumulation of impurities by discharging air and concentrated water.
【図1】本発明に係る浸漬用濾過装置の実施形態の一例
を示す断面説明図である。FIG. 1 is an explanatory sectional view showing an example of an embodiment of a filter device for immersion according to the present invention.
【図2】図1の中空糸膜の下部スカート部の構成を示す
要部拡大図である。FIG. 2 is an enlarged view of a main part showing a configuration of a lower skirt portion of the hollow fiber membrane of FIG.
1 浸漬タンク 2 カートリッジヘッド 3 中空糸膜 4 スカート 4a 接着層 4b 貫通孔 4c 空気室 5 SUSパイプ 6 散気管 7 外壁 8 ヘッダー配管 9 サポートパイプ 10 供給水入口 DESCRIPTION OF SYMBOLS 1 Immersion tank 2 Cartridge head 3 Hollow fiber membrane 4 Skirt 4a Adhesive layer 4b Through hole 4c Air chamber 5 SUS pipe 6 Air diffuser 7 Outer wall 8 Header piping 9 Support pipe 10 Supply water inlet
Claims (1)
れた散気管からの噴出空気により中空糸膜面を洗浄しつ
つ原液を濾過処理する浸漬用膜分離装置において、中空
糸膜上下端部が接着固定され、下接着固定部は中空糸束
内部に空気を導入出来る構造を有し、上下接着固定部が
2本以上の棒又はパイプで連結固定され、中空糸膜が実
質的に露出している中空糸膜カートリッジを用い、該中
空糸膜カートリッジの中空糸膜束外周側面が、中空糸膜
束長より短い、上下が開放された外壁内に、外壁上端と
上接着固定部の間及び外壁下端と下接着固定部の間で中
空糸膜束が露出するように収納されていることを特徴と
する浸漬用濾過装置。1. An immersion membrane separation apparatus for filtering a stock solution while washing the surface of a hollow fiber membrane with air blown out from an air diffuser provided below a vertically suspended hollow fiber membrane. The lower adhesive fixing part has a structure that can introduce air into the hollow fiber bundle, the upper and lower adhesive fixing parts are connected and fixed by two or more rods or pipes, and the hollow fiber membrane is substantially exposed. The hollow fiber membrane cartridge has a hollow fiber membrane cartridge, and the outer peripheral side surface of the hollow fiber membrane bundle is shorter than the length of the hollow fiber membrane bundle. And a dipping filter device wherein the hollow fiber membrane bundle is housed between the lower end of the outer wall and the lower adhesive fixing portion so as to be exposed.
Priority Applications (1)
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JP2001153895A JP4753270B2 (en) | 2001-05-23 | 2001-05-23 | Immersion filtration device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001153895A JP4753270B2 (en) | 2001-05-23 | 2001-05-23 | Immersion filtration device |
Publications (3)
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JP2002346344A true JP2002346344A (en) | 2002-12-03 |
JP2002346344A5 JP2002346344A5 (en) | 2008-05-15 |
JP4753270B2 JP4753270B2 (en) | 2011-08-24 |
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JP2001153895A Expired - Fee Related JP4753270B2 (en) | 2001-05-23 | 2001-05-23 | Immersion filtration device |
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006272049A (en) * | 2005-03-28 | 2006-10-12 | Toray Ind Inc | Hollow fiber membrane module |
JP2007044666A (en) * | 2005-08-12 | 2007-02-22 | Toray Ind Inc | Hollow fiber membrane module |
WO2007083460A1 (en) | 2006-01-19 | 2007-07-26 | Toray Industries, Inc. | Hollow-fiber membrane module |
JP2008188562A (en) * | 2007-02-07 | 2008-08-21 | Mitsubishi Rayon Eng Co Ltd | Membrane separation apparatus |
JP2009066510A (en) * | 2007-09-12 | 2009-04-02 | Panasonic Electric Works Co Ltd | Filtration apparatus |
WO2010001680A1 (en) | 2008-07-01 | 2010-01-07 | 東レ株式会社 | Submerged hollow fiber membrane module |
JP7105431B2 (en) | 2017-01-26 | 2022-07-25 | オルガノ株式会社 | Method and apparatus for treating wastewater containing organic matter |
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JPH10128327A (en) * | 1996-10-31 | 1998-05-19 | Best Kogyo Kk | Drainage treatment apparatus |
JPH10249171A (en) * | 1997-03-18 | 1998-09-22 | Kanegafuchi Chem Ind Co Ltd | Hollow yarn membrane module |
JPH11207152A (en) * | 1998-01-26 | 1999-08-03 | Hitachi Ltd | Hollow yarn membrane module |
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JPH06254582A (en) * | 1993-03-01 | 1994-09-13 | Toto Ltd | Membrane device for septic tank |
JPH10128327A (en) * | 1996-10-31 | 1998-05-19 | Best Kogyo Kk | Drainage treatment apparatus |
JPH10249171A (en) * | 1997-03-18 | 1998-09-22 | Kanegafuchi Chem Ind Co Ltd | Hollow yarn membrane module |
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Publication number | Priority date | Publication date | Assignee | Title |
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JP2006272049A (en) * | 2005-03-28 | 2006-10-12 | Toray Ind Inc | Hollow fiber membrane module |
JP2007044666A (en) * | 2005-08-12 | 2007-02-22 | Toray Ind Inc | Hollow fiber membrane module |
WO2007083460A1 (en) | 2006-01-19 | 2007-07-26 | Toray Industries, Inc. | Hollow-fiber membrane module |
JP2008188562A (en) * | 2007-02-07 | 2008-08-21 | Mitsubishi Rayon Eng Co Ltd | Membrane separation apparatus |
JP2009066510A (en) * | 2007-09-12 | 2009-04-02 | Panasonic Electric Works Co Ltd | Filtration apparatus |
WO2010001680A1 (en) | 2008-07-01 | 2010-01-07 | 東レ株式会社 | Submerged hollow fiber membrane module |
JP7105431B2 (en) | 2017-01-26 | 2022-07-25 | オルガノ株式会社 | Method and apparatus for treating wastewater containing organic matter |
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