JPS63143905A - Hollow yarn membrane filter - Google Patents
Hollow yarn membrane filterInfo
- Publication number
- JPS63143905A JPS63143905A JP29204586A JP29204586A JPS63143905A JP S63143905 A JPS63143905 A JP S63143905A JP 29204586 A JP29204586 A JP 29204586A JP 29204586 A JP29204586 A JP 29204586A JP S63143905 A JPS63143905 A JP S63143905A
- Authority
- JP
- Japan
- Prior art keywords
- hollow
- length
- hollow fiber
- membrane filter
- adhesive
- 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
- 239000012528 membrane Substances 0.000 title claims abstract description 31
- 239000000853 adhesive Substances 0.000 claims abstract description 26
- 230000001070 adhesive effect Effects 0.000 claims abstract description 26
- 239000012510 hollow fiber Substances 0.000 claims description 79
- 238000011001 backwashing Methods 0.000 abstract description 22
- 239000007788 liquid Substances 0.000 abstract description 15
- 238000001914 filtration Methods 0.000 abstract description 13
- 239000007787 solid Substances 0.000 abstract description 12
- 238000005452 bending Methods 0.000 abstract description 3
- 238000000034 method Methods 0.000 abstract description 3
- 230000005587 bubbling Effects 0.000 description 10
- 230000000694 effects Effects 0.000 description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 238000005192 partition Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 239000000706 filtrate Substances 0.000 description 2
- 238000005374 membrane filtration Methods 0.000 description 2
- 230000002411 adverse Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 235000021419 vinegar Nutrition 0.000 description 1
- 239000000052 vinegar Substances 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
【発明の詳細な説明】
〔発明の目的〕
(産業上の利用分野)
本発明は各種プラントの水処理装置にあって、被処理液
中の固形部を分離・除去する目的で使用される中空糸膜
フィルタに関する。Detailed Description of the Invention [Objective of the Invention] (Industrial Application Field) The present invention is a hollow water treatment system used for the purpose of separating and removing solid parts in a liquid to be treated, in water treatment equipment of various plants. Regarding thread membrane filters.
(従来の技術)
一般に中空糸はその外径が0.3〜b
その表面に微細な穴を有する中空円筒状の繊維の膜であ
る。そして単位容積内の濾過面積を大きくとることがで
きるとともに、耐圧性に優れているという利点を備えて
いる。そこで中空糸を多数本束ねてその両端を接着剤で
ある樹脂で固めることによりフィルタを形成する。この
中空糸膜フィルタを水処理装置用の濾過装置として使用
する。(Prior Art) Generally, a hollow fiber is a hollow cylindrical fiber membrane having an outer diameter of 0.3 to 0.3 b and minute holes on its surface. It has the advantage of being able to provide a large filtration area within a unit volume and having excellent pressure resistance. Therefore, a filter is formed by bundling a large number of hollow fibers and hardening both ends with resin, which is an adhesive. This hollow fiber membrane filter is used as a filtration device for water treatment equipment.
以下第5図を参照してそのような中空糸l!膜濾過装置
構成を説明する。第5図は中空糸膜濾過装置の断面図で
あり、図中符号1は容器本体である。Referring to FIG. 5 below, such a hollow fiber l! The configuration of the membrane filtration device will be explained. FIG. 5 is a sectional view of the hollow fiber membrane filtration device, and reference numeral 1 in the figure is the container body.
この容器本体1内は仕切板3により上下に二分されてお
り、下部空間を濾過下1aとし、上部空間を処理液室1
bとしている。上記濾過室1a内には中空糸膜フィルタ
、2−が上記仕切板3より垂下されている。上記中空糸
膜フィルタLは支持体4の外周に多数本の中空糸2aを
集束させて、その上端部及び下端部を接着剤充填部6で
固定するとともに、更にその外周から集束固定部材7を
設置して固定した構成となっている。また第1図に示す
¥A置では上記構成をなす中空糸膜フィルタ2−を鉛直
方向に2段連接しており、図中符号8はその際使用され
る接続筒である。上記容器本体1の下端部には濾過室1
aに連通ずる液供給配管10が接続され、一方上端部に
は処理液室1bに連通する処理液排出配管11が接続さ
れている。上記液供□給配管10には開閉弁12が介挿
されており、濃縮液排出配管13が分岐接続されている
。この濃縮液排出配管13には開閉弁14が介挿されて
いる。上記液供給配管10を介してi11過室1a内に
供給された液は、中空糸膜フィルタ、?−を通過する際
に濾過されて各中空糸2aの中空部を介して排出される
。The inside of this container body 1 is divided into upper and lower halves by a partition plate 3, with the lower space serving as the filtration chamber 1a, and the upper space serving as the processing liquid chamber 1a.
b. A hollow fiber membrane filter 2- is suspended from the partition plate 3 in the filtration chamber 1a. The above-mentioned hollow fiber membrane filter L has a large number of hollow fibers 2a bundled around the outer periphery of a support 4, whose upper and lower ends are fixed with an adhesive filling part 6, and a collection fixing member 7 is further fixed from the outer periphery. It has a fixed and installed configuration. Further, at the position A shown in FIG. 1, two hollow fiber membrane filters 2- having the above structure are connected in the vertical direction, and reference numeral 8 in the figure is a connecting tube used in this case. A filtration chamber 1 is provided at the lower end of the container body 1.
A liquid supply pipe 10 communicating with the processing liquid chamber 1b is connected to the upper end thereof, and a processing liquid discharge pipe 11 communicating with the processing liquid chamber 1b is connected to the upper end. An on-off valve 12 is inserted into the liquid supply pipe 10, and a concentrated liquid discharge pipe 13 is branched and connected thereto. An on-off valve 14 is inserted into this concentrated liquid discharge pipe 13. The liquid supplied into the i11 passing chamber 1a through the liquid supply piping 10 is supplied to the hollow fiber membrane filter, ? - when passing through, it is filtered and discharged through the hollow portion of each hollow fiber 2a.
上記構成にあって、通過により中空糸、1賛フイルタ、
2−の前後の差圧が上昇して、これが規定値に達した場
合には、逆洗操作を施して各中空糸2aの表面に付着し
た固形分を洗い落とす操作が行われる。すなわち前記処
理液排出配管11を介して中空糸膜フィルタ、2−の各
中空糸2a内に逆洗用の加圧気体を供給する。それと同
時に中空糸膜フィルタLの下方からバブリング操作を5
!!す。つまり前記容器本体1内にあって中空糸膜フィ
ルタ72−の下方にはバブリング管15が配設されてお
り、このバブリング管15の下面側には気泡孔16が形
成されている。また上記バブリング管15は開閉弁18
を有するエアー供給管17に接続されている。In the above configuration, by passing through a hollow fiber, a single filter,
When the differential pressure before and after 2- increases and reaches a specified value, a backwashing operation is performed to wash off solid matter adhering to the surface of each hollow fiber 2a. That is, pressurized gas for backwashing is supplied into each hollow fiber 2a of the hollow fiber membrane filter 2- through the treatment liquid discharge pipe 11. At the same time, perform bubbling operation from below the hollow fiber membrane filter L.
! ! vinegar. That is, a bubbling pipe 15 is disposed within the container body 1 below the hollow fiber membrane filter 72-, and a bubble hole 16 is formed in the lower surface of the bubbling pipe 15. In addition, the bubbling pipe 15 has an on-off valve 18
It is connected to an air supply pipe 17 having a.
そして上記バブリング管15に上記エアー供給配管17
を介してエアーを供給することにより気泡孔16より気
泡を発生させる。該気泡により中空糸膜フィルタ、?−
をバブリングさせて洗浄効果を高める。尚前記仕切1f
i3の下方位置の容器本体1にはオーバーフロー管1つ
が接続されてあり、該オーバーフロー管19には開閉弁
20か介挿されている。また図中符号21は保護管であ
って、この保護管21によって上述したバブリングの際
の気泡を中空糸膜フィルタL内に効果的に導入するもの
である。Then, the air supply pipe 17 is connected to the bubbling pipe 15.
Air bubbles are generated from the air bubble holes 16 by supplying air through the air bubbles. Hollow fiber membrane filter, due to the air bubbles? −
Bubble to enhance the cleaning effect. In addition, the partition 1f
One overflow pipe is connected to the container body 1 located below i3, and an on-off valve 20 is inserted into the overflow pipe 19. Further, reference numeral 21 in the figure is a protection tube, and this protection tube 21 effectively introduces air bubbles from the above-mentioned bubbling into the hollow fiber membrane filter L.
ところで上述した構成の中空糸膜フィルタ、2−に対し
て逆洗を施す際、両端部の接着剤充填部6によって決定
される両端間の距離(第5図中符号L2示す)に対して
、その間に配置される中空糸2aの長さくし1、上記し
2なる間隔の間で若干弛んでいるのでL2より大きな値
である)をどの程度の余長をもって決定すれば、前述し
たバブリングが効果的になされかつ中空糸2aの破損等
が防止できるかについてはm*されていないのが現状で
ある。従来は5Z程度の余長をもって設定していた。と
ころが、濾過・逆洗を繰返すうちに複数本の中空糸2a
がからみついて屈曲・破損するという事態が発生した。By the way, when performing backwashing on the hollow fiber membrane filter 2- having the above-described structure, with respect to the distance between both ends (indicated by the symbol L2 in FIG. 5) determined by the adhesive filling portions 6 at both ends, How much extra length should be determined for the length of the hollow fibers 2a arranged between them (the length of the hollow fibers 2a is slightly slack between the intervals 1 and 2 as described above, so it is larger than L2) to ensure that the bubbling described above is effective. At present, it has not been determined whether this can be done and damage to the hollow fibers 2a can be prevented. Conventionally, it was set with an extra length of about 5Z. However, as filtration and backwashing were repeated, multiple hollow fibers 2a
A situation occurred in which the parts became tangled, bent, and damaged.
これは中空糸2aが高分子材料からなり、?!!!処理
液の主成分である水とその比巾が殆ど等しい為に、中空
糸2aが舞い上がり屈曲・破損に至ったものと考えられ
る。このような問題を解決する手段としては、前記5X
程度に設定した余長を短くする、あるいは無くすことが
考えられる。しかしながらその様な方法をとった場合に
は以下のような問題が生ずる。This means that the hollow fibers 2a are made of a polymeric material. ! ! ! It is thought that the hollow fibers 2a were thrown up and bent/damaged because their relative widths were almost equal to water, which is the main component of the treatment liquid. As a means to solve such problems, the above-mentioned 5X
It is conceivable to shorten or eliminate the extra length set to a certain degree. However, when such a method is adopted, the following problems occur.
■まず前述したバブリングを行なう際の中空糸2aの揺
動幅が必要以上に制限されて、十分なバブリング効果を
得ることがで、きない。(1) First, the swinging width of the hollow fibers 2a when performing the bubbling described above is restricted more than necessary, making it impossible to obtain a sufficient bubbling effect.
■中空糸膜フィルタ、2−は前述したように?!数本の
中空糸2aがち密に配列された状態で集束されており、
余長を少なくすると、各中空糸28間に被処理液が効果
的に流通せず、よって中空糸膜フィルタ、2−の外周に
位置する中空糸2aのみが濾過に供される結果となる。■Hollow fiber membrane filter, 2- as mentioned above? ! Several hollow fibers 2a are bundled in a dense arrangement,
If the extra length is reduced, the liquid to be treated will not effectively flow between the hollow fibers 28, resulting in only the hollow fibers 2a located on the outer periphery of the hollow fiber membrane filter 2- being subjected to filtration.
これは濾過効率の点からも好ましくなく、又外周に位置
する中空糸2aのみに固形分が付着するという現象が発
生してしまう。This is not preferable from the point of view of filtration efficiency, and also causes a phenomenon in which solid matter adheres only to the hollow fibers 2a located on the outer periphery.
■また逆洗を施した場合に、該逆洗により剥離した固形
分が中空糸2a間に溜ってしまい、剥離した固形分の排
出が効率良く行われないという問題がある。これも結局
上記■と同様に中空糸2aがち密に配設されかつ余長が
少ない為に各中空糸2a間における流通性が悪いことに
よる。(2) Furthermore, when backwashing is performed, there is a problem in that the solids exfoliated by the backwashing accumulate between the hollow fibers 2a, and the exfoliated solids are not efficiently discharged. This is also due to the fact that the hollow fibers 2a are densely arranged and the remaining length is small, resulting in poor flowability between the hollow fibers 2a, as in the above case.
(発明が解決しようとする問題点)
このように従来の中空糸膜フィルタにあってはその余長
をいかに決定するかについての十分な検討がなされてお
らず、その結果種々の問題を引起こしており、本発明は
以下の点に基づいてなされたものでその目的とするとこ
ろは、中空糸の破損を防止するとともに効果的な逆洗を
行なうことを可能とする余長を備えた中空糸膜フィルタ
を提供することにある。(Problems to be Solved by the Invention) As described above, sufficient consideration has not been given to how to determine the extra length of conventional hollow fiber membrane filters, and as a result, various problems have arisen. The present invention has been made based on the following points, and its purpose is to provide a hollow fiber having an extra length that prevents breakage of the hollow fiber and enables effective backwashing. The purpose of the present invention is to provide a membrane filter.
[発明の構成]
(問題点を解決するための手段)
すなわち本発明による中空系膜フィルタは、複数本の中
空糸を集束してその両集束端部が開口するように1妾看
剤を充填して固定し、上記接着剤を充填した接着剤充填
部の外周に集束固定部材を設置して固定して上記両端の
接着剤充填部を所定長さをもって連結する中空糸膜フィ
ルタにおいて、上記間接着剤充填部間の中空糸の長さく
L1)は上記両接着剤充填部間の間隔(L1)に対して
所定の余長(ΔL)を持って配設され、この余長(ΔL
)は以下の条件を満足するものであることを特徴とする
ものである。[Structure of the Invention] (Means for Solving the Problems) That is, the hollow membrane filter according to the present invention collects a plurality of hollow fibers and fills them with a filler so that both bundled ends thereof are open. In the hollow fiber membrane filter in which the adhesive-filled portions at both ends are connected by a predetermined length by installing and fixing a focusing fixing member around the outer periphery of the adhesive-filled portion filled with the adhesive, the indirect The length L1) of the hollow fiber between the adhesive filled parts is arranged with a predetermined extra length (ΔL) with respect to the distance (L1) between the adhesive filled parts, and this extra length (ΔL)
) is characterized by satisfying the following conditions.
0.01≦(ΔL/Ls )≦0.04但し
Ll 二両接着剤充填部間に配設される中空糸の長さ
Ll;両接着剤充填部間の間隔
ΔL ; (Ll−12)
(作用)
中空糸の余長を上記範囲内とすることにより、余長が大
きすぎる為に発生する中空糸のからみつき、それによる
屈曲・破損を無くすとともに、余長が小さ過ぎることに
より発生する逆洗効果の低下等の問題を効果的に解決す
るものである。0.01≦(ΔL/Ls)≦0.04, where Ll Length Ll of the hollow fiber arranged between the two adhesive-filled parts; Distance ΔL between both adhesive-filled parts; (Ll-12) ( Effect) By keeping the extra length of the hollow fibers within the above range, it is possible to eliminate the entanglement of the hollow fibers that occurs due to the extra length, as well as the bending and breakage caused by this, as well as the backwashing that occurs when the extra length is too small. This effectively solves problems such as decreased effectiveness.
(実施例)
以下第1図乃至第4図を参照して本発明の一実施例を説
明する。尚従来と同一部分には同一符号を付して示しそ
の説明は省略する。第1図は中空糸膜フィルタ2−の構
成を示す断面図であり、上端及び下端の各接着剤充填部
6間に若干弛んだ状態で配設される中空糸2aの長ざ(
L1)は、上記各接着剤充填部6間の距lI!1(12
)に対して(△L)なる余長を有しており、この余長(
ΔL)は以下の範囲内に設定されている。0.01≦(
ΔL、′1−1)≦0.04・・・・・・(I>但し
Ll ;両接者剤充填部間に配設される中空糸の長さ
し2 ;両接着剤充頃部間の間隔
ΔL ; (L+ −12>
余長(八L)をこのような範囲内に設定したのは、余長
が大き過ぎることによる弊害、及び余長が小さ過ぎるこ
とによる弊害の両方を効果的に排除する為であり、以下
第3図及び第4図を参照して説明する。(Embodiment) An embodiment of the present invention will be described below with reference to FIGS. 1 to 4. It should be noted that the same parts as in the prior art are denoted by the same reference numerals and the explanation thereof will be omitted. FIG. 1 is a cross-sectional view showing the structure of the hollow fiber membrane filter 2-.
L1) is the distance lI! between each of the adhesive filling portions 6! 1 (12
) has a surplus length of (△L), and this surplus length (
ΔL) is set within the following range. 0.01≦(
ΔL,'1-1)≦0.04...(I>However, Ll; Length 2 of hollow fiber arranged between both adhesive-filled parts; Between both adhesive-filled parts The interval ΔL; (L+ -12>) The reason why the extra length (8L) is set within this range is to effectively eliminate both the negative effects of having too large a surplus length and the negative effects of having a surplus length that is too small. This will be explained below with reference to FIGS. 3 and 4.
第3図は横軸に余長(Δし)の中空糸2aの長さ(L1
)に対する割合をとり(%)、縦軸に中空糸2aの屈曲
部本数(中空糸1000本当り)をとって示した図であ
る。これによると、余長(ΔL)の中空糸2aの長さく
L1)に対する割合が4以下の場合には屈曲部が発生し
た中空糸2aの本数が極めて少ないことがわかる。よっ
て余長(ΔLン割合を4以下にすれば余長が大きいこと
による弊害を効果的に無くすことができる。一方下限値
であるが、これについては第4図を参照して説明する。In Figure 3, the horizontal axis is the length of the hollow fiber 2a (L1) with extra length (Δ).
), and the vertical axis represents the number of bent portions of the hollow fibers 2a (per 1000 hollow fibers). According to this, it can be seen that when the ratio of the extra length (ΔL) to the length L1) of the hollow fibers 2a is 4 or less, the number of hollow fibers 2a in which bent portions have occurred is extremely small. Therefore, if the excess length (ΔL) ratio is set to 4 or less, the adverse effects caused by the large excess length can be effectively eliminated.On the other hand, the lower limit value will be explained with reference to FIG.
第4図は横軸に余長(ΔL)の中空糸2aの長さくし1
)に対する割合をとり(%)、縦軸に逆洗効率(逆洗に
よって剥離した固形分旦/捕)足固形分量、%)をとっ
て示したもので、この第4図から明らかなように余長(
ΔL)の中空糸2aの長さくL1)に対する割合が1以
下になると逆洗効率が急速に悪化しているのがわかる。Figure 4 shows a length comb 1 of the hollow fiber 2a with extra length (ΔL) on the horizontal axis.
), and the vertical axis is the backwashing efficiency (solids removed by backwashing/captured solids, %).As is clear from Figure 4, Extra length (
It can be seen that when the ratio of the hollow fibers 2a (ΔL) to the length L1) becomes 1 or less, the backwashing efficiency deteriorates rapidly.
これは第2図にも示すように、逆洗時にバブリングを行
なう際には中空糸2aがある程度揺動する必要があり、
該揺動により固形分が賑い落とされるからである。さら
に以下のことが観察された。すなわち余長(ΔL)の割
合を1未満とした場合には、中空糸2aの動きが必要以
上に制限されるために、中空糸膜フィルタLの中心部の
中空糸2alllEfflにあっては濾液が流通せず、
よって外周部の中空糸2aのみが濾過に供される結果と
なってしまう。This is because, as shown in Fig. 2, when bubbling is performed during backwashing, the hollow fibers 2a need to swing to some extent.
This is because the solid content is washed away by the shaking. Furthermore, the following was observed. In other words, when the ratio of the surplus length (ΔL) is less than 1, the movement of the hollow fibers 2a is restricted more than necessary, so that the filtrate is Not distributed,
As a result, only the hollow fibers 2a at the outer periphery are subjected to filtration.
これは外周に位置する中空糸2aのみに固形分が付着す
ることから観察することができる。それと同時に1未満
とした場合には、逆洗時に剥離した固形分が中空糸膜フ
イルタ上内に溜ってしまい、効果的に除去できないこと
も確認された。このような理由から余長(ΔL)の中空
糸2aの長さくL1)に対する割合の下限値を1とした
ものである。This can be observed from the fact that the solid content adheres only to the hollow fibers 2a located on the outer periphery. At the same time, it was also confirmed that when the ratio was less than 1, solids separated during backwashing accumulated on the hollow fiber membrane filter and could not be removed effectively. For this reason, the lower limit of the ratio of the extra length (ΔL) to the length L1) of the hollow fiber 2a is set to 1.
以上本実施例によると以下のような効果を奏することが
できる。According to this embodiment, the following effects can be achieved.
■まず逆洗時における中空糸2aの舞い上がり、それに
よってからみつき屈曲あるいは破損するといった事態を
効果的に防止することができる。(1) First, it is possible to effectively prevent the hollow fibers 2a from flying up during backwashing and thereby becoming entangled, bent or damaged.
■次に逆洗時には中空糸2aが適度に揺動するので、効
果的な逆洗が可能となる。(2) Next, during backwashing, the hollow fibers 2a are swayed appropriately, making it possible to perform effective backwashing.
・■また逆洗時に剥離した固形分が中空糸膜フイルタ2
内に溜ってしまうということもない。・■Also, the solid content peeled off during backwashing is transferred to the hollow fiber membrane filter 2.
It doesn't get stuck inside.
■さらに濾過時にあっても中空糸膜フィルタ、?−の中
心部に位置する中空糸2aの回りにも濾液が効果的に流
通するので、外周部のみで濾過が行われるといった事態
を防止することができ、効率のよい濾過を提供すること
ができる。■A hollow fiber membrane filter even during filtration? - Since the filtrate effectively flows around the hollow fibers 2a located in the center of the area, it is possible to prevent a situation where filtration is performed only at the outer periphery, and it is possible to provide efficient filtration. .
[発明の効果コ
以上詳述したように本発明よる中空糸膜フィルタによる
と、中空糸の舞い上がり、それによるからみつき、ざら
には屈曲・破損といった事態を防止することができると
ともに、効果的な逆洗を提供することができる等その効
果は大である。[Effects of the Invention] As detailed above, according to the hollow fiber membrane filter of the present invention, it is possible to prevent hollow fibers from flying up, entanglement, and even bending and breakage, as well as to effectively prevent Its effects are great, such as being able to provide cleansing.
第1図乃至第4図は本発明の一実施例を示す図で、第1
図は中空糸膜フィルタの正面図、第2図は逆洗時の作用
を示す中空糸膜フィルタの正面図、第3図は中空糸の余
長を変化させた場合の屈曲部発生本数の変化を示す特性
図、第4図は中空、2−・・・中空糸摸フィルタ、2a
・・・中空糸、4・・・支持体、6・・・接着剤充填部
、7・・・集束固定部材。
第1図
第2図
1&ΔL/)中空′矛、長LzC’iV?v怜(’10
)ぴ九)
宗長ΔLの中空1(昂L2に註す4害り富
11/。
(Δ1ん)Figures 1 to 4 are diagrams showing one embodiment of the present invention.
The figure is a front view of a hollow fiber membrane filter, Figure 2 is a front view of a hollow fiber membrane filter showing the action during backwashing, and Figure 3 is a change in the number of bent portions when the extra length of the hollow fibers is changed. Characteristic diagram showing Figure 4 is hollow fiber filter, 2-... hollow fiber filter, 2a
... hollow fiber, 4 ... support body, 6 ... adhesive filling part, 7 ... focusing fixing member. Figure 1 Figure 2 1&ΔL/) Hollow spear, long LzC'iV? v Rei ('10
) Pi9) Hollow 1 of Socho ΔL (4 harm wealth noted in L2)
11/. (Δ1n)
Claims (1)
うに接着剤を充填して固定し、上記接着剤を充填した接
着剤充填部の外周に集束固定部材を設置して固定して上
記両端の接着剤充填部を所定長さをもって連結する中空
糸膜フィルタにおいて、上記両接着剤充填部間の中空糸
の長さ(L_1)は上記両接着剤充填部間の間隔(L_
2)に対して所定の余長(ΔL)を持って配設され、こ
の余長(ΔL)は以下の条件を満足するものであること
を特徴とする中空糸膜フィルタ。 0.01≦(ΔL/L_1)≦0.04 但し L_1;両接着剤充填部間に配設される中空糸の長さ L_2;両接着剤充填部間の間隔 ΔL;(L_1−L_2)[Claims] A plurality of hollow fibers are bundled and fixed by being filled with an adhesive so that both bundled ends are open, and a bundle fixing member is provided on the outer periphery of the adhesive-filled part filled with the adhesive. In a hollow fiber membrane filter in which the adhesive-filled parts at both ends are connected with a predetermined length by installing and fixing, the length (L_1) of the hollow fiber between the two adhesive-filled parts is equal to the length (L_1) of the hollow fiber between the two adhesive-filled parts. The interval between (L_
2) A hollow fiber membrane filter, characterized in that it is arranged with a predetermined extra length (ΔL) relative to 2), and this extra length (ΔL) satisfies the following conditions. 0.01≦(ΔL/L_1)≦0.04 However, L_1; Length of hollow fiber arranged between both adhesive-filled parts L_2; Distance ΔL between both adhesive-filled parts; (L_1-L_2)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP29204586A JPS63143905A (en) | 1986-12-08 | 1986-12-08 | Hollow yarn membrane filter |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP29204586A JPS63143905A (en) | 1986-12-08 | 1986-12-08 | Hollow yarn membrane filter |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS63143905A true JPS63143905A (en) | 1988-06-16 |
JPH0579366B2 JPH0579366B2 (en) | 1993-11-02 |
Family
ID=17776822
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP29204586A Granted JPS63143905A (en) | 1986-12-08 | 1986-12-08 | Hollow yarn membrane filter |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS63143905A (en) |
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---|---|---|---|---|
WO1997006880A3 (en) * | 1995-08-11 | 1997-05-01 | Zenon Environmental Inc | Vertical skein of hollow fiber membranes and method of maintaining clean fiber surfaces |
EP1170052A1 (en) * | 1995-08-11 | 2002-01-09 | Zenon Environmental Inc. | System for withdrawing permeate from a multicomponent liquid substrate |
USRE37549E1 (en) * | 1995-08-11 | 2002-02-19 | Zenon Environmental Inc. | Vertical skein of hollow fiber membranes and method of maintaining clean fiber surfaces while filtering a substrate to withdraw a permeate |
JP2005296937A (en) * | 2004-03-17 | 2005-10-27 | Toray Ind Inc | Hollow fiber membrane module and production method therefor |
US7087173B2 (en) | 1995-08-11 | 2006-08-08 | Zenon Environmental Inc. | Inverted cavity aerator for membrane module |
US7160463B2 (en) | 2002-06-18 | 2007-01-09 | U.S. Filter Wastewater Group, Inc. | Methods of minimizing the effect of integrity loss in hollow fibre membrane modules |
JP2007044666A (en) * | 2005-08-12 | 2007-02-22 | Toray Ind Inc | Hollow fiber membrane module |
US7198721B2 (en) | 1998-10-09 | 2007-04-03 | Zenon Technology Partnership | Cyclic aeration system for submerged membrane modules |
WO2007083460A1 (en) * | 2006-01-19 | 2007-07-26 | Toray Industries, Inc. | Hollow-fiber membrane module |
US7361274B2 (en) | 2002-08-21 | 2008-04-22 | Siemens Water Technologies Corp. | Aeration method |
US7537701B2 (en) * | 1995-08-11 | 2009-05-26 | Zenon Technology Partnership | Membrane filtration module with adjustable header spacing |
JP2011167687A (en) * | 2004-03-17 | 2011-09-01 | Toray Ind Inc | Method for producing hollow fiber membrane module |
US8268176B2 (en) | 2003-08-29 | 2012-09-18 | Siemens Industry, Inc. | Backwash |
US8287743B2 (en) | 2007-05-29 | 2012-10-16 | Siemens Industry, Inc. | Membrane cleaning with pulsed airlift pump |
US8293098B2 (en) | 2006-10-24 | 2012-10-23 | Siemens Industry, Inc. | Infiltration/inflow control for membrane bioreactor |
US8318028B2 (en) | 2007-04-02 | 2012-11-27 | Siemens Industry, Inc. | Infiltration/inflow control for membrane bioreactor |
US8377305B2 (en) | 2004-09-15 | 2013-02-19 | Siemens Industry, Inc. | Continuously variable aeration |
US8382981B2 (en) | 2008-07-24 | 2013-02-26 | Siemens Industry, Inc. | Frame system for membrane filtration modules |
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US8956464B2 (en) | 2009-06-11 | 2015-02-17 | Evoqua Water Technologies Llc | Method of cleaning membranes |
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US9533261B2 (en) | 2012-06-28 | 2017-01-03 | Evoqua Water Technologies Llc | Potting method |
US9604166B2 (en) | 2011-09-30 | 2017-03-28 | Evoqua Water Technologies Llc | Manifold arrangement |
US9675938B2 (en) | 2005-04-29 | 2017-06-13 | Evoqua Water Technologies Llc | Chemical clean for membrane filter |
US9764288B2 (en) | 2007-04-04 | 2017-09-19 | Evoqua Water Technologies Llc | Membrane module protection |
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JPS59322A (en) * | 1982-06-23 | 1984-01-05 | Mitsubishi Heavy Ind Ltd | Stirring type granulator |
-
1986
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JPS59322A (en) * | 1982-06-23 | 1984-01-05 | Mitsubishi Heavy Ind Ltd | Stirring type granulator |
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