JPH10174986A - Septic tank - Google Patents

Septic tank

Info

Publication number
JPH10174986A
JPH10174986A JP34030096A JP34030096A JPH10174986A JP H10174986 A JPH10174986 A JP H10174986A JP 34030096 A JP34030096 A JP 34030096A JP 34030096 A JP34030096 A JP 34030096A JP H10174986 A JPH10174986 A JP H10174986A
Authority
JP
Japan
Prior art keywords
hollow fiber
fiber membrane
membranes
septic tank
membrane
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
JP34030096A
Other languages
Japanese (ja)
Inventor
Hiroshi Kano
広志 加納
Yoshitsugu Masuguchi
義次 増口
Takayoshi Nakaoka
敬善 中岡
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.)
Panasonic Electric Works Co Ltd
Original Assignee
Matsushita Electric Works 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 Matsushita Electric Works Ltd filed Critical Matsushita Electric Works Ltd
Priority to JP34030096A priority Critical patent/JPH10174986A/en
Publication of JPH10174986A publication Critical patent/JPH10174986A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To hold uniformly without reducing a rotary flow velocity, to wash efficiently, to prevent clogging, and to improve a filtration-purification capacity by stretching hollow fiber membranes set in a purification tank horizontally. SOLUTION: An aerobic tank body 2 in which hollow fiber membranes 1 are set is installed in a purification tank. The membranes 1 are stretched horizontally by a tension means 3 comprising a spring 6. A diffusion pipe 4 is installed below the membranes 1. The membranes 1 are arranged vertically in parallel at distance from each other. Each membrane 1 is aerated by air ejected from the pipe 4, an ascending agitation flow is generated by water to be treated, and cake layers adherent to the membranes 1 are peeled off to wash the membranes 1. Since the membranes 1 are stretched horizontally, they are prevented from slackening to a vertical sludge rotary flow. Accordingly, the pressure loss of rotary flow sludge and the decrease in a rotary flow velocity can be prevented.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、中空糸膜が内装さ
れた好気槽体を有し、該好気槽体内で固液分離する膜分
離式の浄化槽に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a membrane separation type septic tank having an aerobic tank in which a hollow fiber membrane is provided, and performing solid-liquid separation in the aerobic tank.

【0002】[0002]

【従来の技術】従来から、図7に示す如く、中空糸膜1
が内装された好気槽体2を有する浄化槽は知られてい
る。この場合、中空糸膜1は略垂直となり相互に間隔を
あけて三枚並設された状態で好気槽体2に内装されてお
り、図8に示す如く、各中空糸膜1はその両側端に配設
される支持枠5間に架設支持されている。該支持枠5は
好気槽体2内に立設固定されており、各中空糸膜1は同
好気槽体2内に動かないように固定される。又、図示し
ないが、好気槽体2内の中空糸膜1の下方には散気管が
配設されており、該散気管から噴出する空気によって同
好気槽体2内に好気状態が形成される。
2. Description of the Related Art Conventionally, as shown in FIG.
A septic tank having an aerobic tank body 2 in which is installed is known. In this case, the hollow fiber membranes 1 are substantially vertical and are housed in the aerobic tank body 2 in a state where three hollow fiber membranes are arranged side by side with an interval therebetween. As shown in FIG. It is erected and supported between support frames 5 disposed at the ends. The support frame 5 is fixed upright in the aerobic tank 2, and each hollow fiber membrane 1 is fixed in the aerobic tank 2 so as not to move. Although not shown, an air diffusion tube is provided below the hollow fiber membrane 1 in the aerobic tank body 2, and an aerobic state is formed in the aerobic tank body 2 by air ejected from the air diffusion pipe. Is done.

【0003】したがって、該浄化槽においては、好気槽
体2内で、散気管から噴出される空気によって該好気槽
体2内に好気状態が形成され、該好気状態において被処
理水の活性汚泥処理が行われる。すなわち、各中空糸膜
1にて被処理水が固液分離され、この固液分離におい
て、活性汚泥が好気槽体2内に保持される一方、濾過さ
れた膜透過液は処理水として該好気槽体2から送出さ
れ、同活性汚泥によって被処理水が好気的に生物学的処
理される。又、散気管から噴出される下方からの空気に
よって各中空糸膜1は曝気され、これにより、被処理水
に上昇攪拌流が発生し、同各中空糸膜1の濾過膜の膜面
に付着したケーキ層が剥離されて膜洗浄が行われる。
Therefore, in the septic tank, an aerobic state is formed in the aerobic tank body 2 by the air blown out from the diffuser pipe in the aerobic tank body 2, and in the aerobic state, the water to be treated is formed. Activated sludge treatment is performed. That is, the water to be treated is solid-liquid separated in each hollow fiber membrane 1, and in this solid-liquid separation, activated sludge is held in the aerobic tank body 2, while the filtered membrane permeate is treated as treated water. The water to be treated is sent out from the aerobic tank 2 and is aerobically biologically treated by the activated sludge. Further, each hollow fiber membrane 1 is aerated by the air blown from the air diffuser from below, whereby an ascending flow is generated in the water to be treated and adheres to the membrane surface of the filtration membrane of each hollow fiber membrane 1. The cake layer thus removed is peeled off and the film is washed.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、上記従
来の技術においては、散気管から噴出される空気によっ
て各中空糸膜1が曝気される際に、該中空糸膜1はエア
ーレイションによる外力によって伸びてしまい、これに
より、同中空糸膜1の中程部分に弛みが発生して該中程
部分付近を回流する汚泥に対する圧力損失が増大し、該
汚泥の回流が不均一となってしまうという問題があっ
た。又、該不均一な回流によって、中空糸膜1の中程部
分付近における流速が低下し、洗浄能力が落ちると共に
同中空糸膜1の膜閉塞につながるという問題もあった。
However, in the above-mentioned prior art, when each hollow fiber membrane 1 is aerated by air blown out from a diffuser, the hollow fiber membrane 1 is stretched by an external force due to air ration. As a result, the hollow fiber membrane 1 is slackened in the middle part thereof, and the pressure loss of the sludge circulating near the middle part increases, and the circulation of the sludge becomes uneven. was there. In addition, there is a problem that the non-uniform circulating flow reduces the flow velocity in the vicinity of the middle part of the hollow fiber membrane 1, lowers the cleaning ability, and leads to blockage of the hollow fiber membrane 1.

【0005】本発明は、上記従来の技術における問題を
悉く解決するために発明されたもので、すなわち、その
課題は、回流速度が低下することなく均一に保持され、
中空糸膜が効率良く洗浄されその閉塞も防止されて、濾
過浄化能力の高い浄化槽を提供することである。
[0005] The present invention has been made in order to solve all the problems in the above-mentioned conventional technology, that is, the problem is that the circulating speed is kept uniform without lowering,
An object of the present invention is to provide a septic tank having a high filtration and purification ability, in which the hollow fiber membrane is efficiently washed and its clogging is prevented.

【0006】[0006]

【課題を解決するための手段】本発明の請求項1記載の
浄化槽は、中空糸膜が内装された好気槽体を有する浄化
槽であって、中空糸膜を略水平方向に引っ張るテンショ
ン手段を具備してなるものである。したがって、この場
合、中空糸膜がテンション手段により略水平方向に引っ
張られて常に伸張された状態に保持されるので、上下方
向の汚泥の回流に対しても同中空糸膜には弛みが発生せ
ず、同回流する汚泥に対する圧力損失の増大が防止さ
れ、該汚泥の回流速度は低下することなく均一に保持さ
れる。これにより、中空糸膜は効率良く洗浄されて閉塞
することもなく、濾過浄化能力が高く維持される。
According to a first aspect of the present invention, there is provided a septic tank having an aerobic tank in which a hollow fiber membrane is provided, and a tension means for pulling the hollow fiber membrane in a substantially horizontal direction. It is provided. Therefore, in this case, the hollow fiber membrane is pulled in a substantially horizontal direction by the tension means and is always kept in an extended state, so that the hollow fiber membrane is slackened even with respect to the vertical circulation of sludge. Therefore, an increase in pressure loss with respect to the sludge flowing at the same time is prevented, and the circulation speed of the sludge is maintained uniformly without decreasing. As a result, the hollow fiber membrane is efficiently washed without clogging, and the filtration and purification ability is maintained at a high level.

【0007】本発明の請求項2記載の浄化槽は、上記請
求項1記載の浄化槽において、好気槽体内の中空糸膜の
下方に散気管が配設されていることを特徴とする。した
がって、この場合は特に、散気管から噴出される下方か
らの空気によって中空糸膜が曝気され、被処理水には上
昇攪拌流が発生して、同中空糸膜の濾過膜の膜面に付着
したケーキ層は効果的に剥離され、より効率的な膜洗浄
が行われる。
A septic tank according to a second aspect of the present invention is the septic tank according to the first aspect, wherein an air diffuser is provided below the hollow fiber membrane in the aerobic tank. Therefore, in this case, in particular, the hollow fiber membrane is aerated by the air blown out from the air diffuser from below, and ascending flow is generated in the water to be treated, and adheres to the surface of the filtration membrane of the hollow fiber membrane. The cake layer thus removed is effectively peeled off, and more efficient film cleaning is performed.

【0008】本発明の請求項3記載の浄化槽は、上記請
求項2記載の浄化槽において、中空糸膜が略垂直となり
相互に間隔をあけて複数枚並設された状態で好気槽体に
内装されていることを特徴とする。したがって、この場
合は特に、中空糸膜が複数枚並設されることによって濾
過洗浄能力が向上するのはもちろんのこと、略垂直とな
る各中空糸膜間の間隔を攪拌流がスムーズに上昇して、
汚泥の回流速度が高められると共に膜洗浄能力も向上さ
れる。
According to a third aspect of the present invention, there is provided the septic tank according to the second aspect, wherein a plurality of hollow fiber membranes are arranged substantially vertically and are arranged side by side at intervals from each other. It is characterized by having been done. Therefore, in this case, in particular, not only the filtration and washing performance is improved by the plurality of hollow fiber membranes being arranged in parallel, but also the agitated flow smoothly rises between the substantially vertical intervals between the hollow fiber membranes. hand,
The sludge circulation speed is increased and the membrane cleaning ability is also improved.

【0009】本発明の請求項4記載の浄化槽は、上記請
求項1〜3のいずれか一つの請求項記載の浄化槽におい
て、中空糸膜をその両側端に配設される支持枠間に架設
支持して該支持枠を側方へ引っ張るテンション手段とな
したことを特徴とする。したがって、この場合は特に、
中空糸膜がその両側端に配設される支持枠間に架設支持
されているので、該支持枠がテンション手段によって側
方へ引っ張られることにより、同中空糸膜は全体が均等
に略水平方向に引っ張られてその弛み変形が確実に防止
される。
A septic tank according to a fourth aspect of the present invention is the septic tank according to any one of the first to third aspects, wherein the hollow fiber membrane is supported between the supporting frames provided at both ends thereof. And a tension means for pulling the support frame to the side. Therefore, especially in this case,
Since the hollow fiber membrane is erected and supported between the support frames disposed at both ends thereof, the support frame is pulled to the side by the tension means, so that the entire hollow fiber membrane is substantially uniformly in the substantially horizontal direction. And the slack deformation is reliably prevented.

【0010】本発明の請求項5記載の浄化槽は、上記請
求項4記載の浄化槽において、中空糸膜が相互に間隔を
あけて複数枚並設された状態で好気槽体に内装されてお
り、隣接する中空糸膜間で支持枠を相互に結合一体化し
たことを特徴とする。したがって、この場合は特に、中
空糸膜が複数枚並設されることによって濾過洗浄能力が
向上するのはもちろんのこと、各中空糸膜を架設支持す
るその両側端の支持枠が隣接するもの相互で結合一体化
されるため、テンション手段による引っ張り力が同結合
一体化された支持枠を介して各中空糸膜に均等に作用
し、複数枚の同中空糸膜の弛み変形が効率良く確実に防
止される。
The septic tank according to a fifth aspect of the present invention is the septic tank according to the fourth aspect, wherein a plurality of hollow fiber membranes are arranged in parallel in the aerobic tank at intervals. In addition, the support frames are mutually connected and integrated between adjacent hollow fiber membranes. Therefore, in this case, in particular, not only the filtration and washing ability is improved by arranging a plurality of hollow fiber membranes side by side, but also the supporting frames at both side ends for supporting and supporting each hollow fiber membrane are mutually adjacent. , The tensile force by the tension means acts uniformly on each hollow fiber membrane via the support frame integrated with the same, and the slack deformation of a plurality of the hollow fiber membranes can be efficiently and reliably performed. Is prevented.

【0011】本発明の請求項6記載の浄化槽は、上記請
求項1〜5のいずれか一つの請求項記載の浄化槽におい
て、スプリングにより引っ張るテンション手段であるこ
とを特徴とする。したがって、この場合は特に、スプリ
ングにより中空糸膜が弾性的に引っ張られて保持される
ので、該中空糸膜に加わる汚泥回流時の衝撃は吸収され
てその破損が防止される。
According to a sixth aspect of the present invention, there is provided a septic tank according to any one of the first to fifth aspects, wherein the septic tank is a tension means for pulling by a spring. Therefore, in this case, in particular, the hollow fiber membrane is elastically pulled and held by the spring, so that the shock applied to the hollow fiber membrane when the sludge is circulated is absorbed and its breakage is prevented.

【0012】本発明の請求項7記載の浄化槽は、上記請
求項1〜5のいずれか一つの請求項記載の浄化槽におい
て、錘体により引っ張るテンション手段であることを特
徴とする。したがって、この場合は特に、錘体による引
っ張り力が変化しないので、中空糸膜は一定の引っ張り
力でもって伸張された状態に確保される。
A septic tank according to a seventh aspect of the present invention is the septic tank according to any one of the first to fifth aspects, characterized in that the septic tank is tension means for pulling by a weight. Therefore, in this case, in particular, since the tensile force of the weight body does not change, the hollow fiber membrane is secured in a stretched state with a constant tensile force.

【0013】[0013]

【発明の実施の形態】図1〜3は、本発明の請求項1〜
6に対応する一実施形態を示し、該実施形態の浄化槽
は、中空糸膜1が内装された好気槽体2を有する浄化槽
であって、中空糸膜1を略水平方向に引っ張るテンショ
ン手段3を具備している。該実施形態の浄化槽において
は、好気槽体2内の中空糸膜1の下方に散気管4が配設
されており、同中空糸膜1は略垂直となり相互に間隔を
あけて複数枚並設された状態で好気槽体2に内装されて
いる。又、中空糸膜1はその両側端に配設される支持枠
5間に架設支持されており、該支持枠5を側方へ引っ張
るテンション手段3となっている。又、この場合、隣接
する中空糸膜1間で支持枠5は相互に結合一体化されて
おり、テンション手段3がスプリング6により引っ張る
ものである。
1 to 3 show the first embodiment of the present invention.
6 shows an embodiment corresponding to FIG. 6, a septic tank having an aerobic tank body 2 in which a hollow fiber membrane 1 is provided, and a tension means 3 for pulling the hollow fiber membrane 1 in a substantially horizontal direction. Is provided. In the septic tank of this embodiment, an air diffuser 4 is provided below the hollow fiber membrane 1 in the aerobic tank body 2, and the hollow fiber membranes 1 are substantially vertical and a plurality of hollow fiber membranes 1 are arranged at intervals from one another. It is installed in the aerobic tank body 2 in the installed state. The hollow fiber membrane 1 is supported by being supported between support frames 5 provided on both side ends thereof, and serves as tension means 3 for pulling the support frame 5 to the side. In this case, the supporting frames 5 are mutually connected and integrated between the adjacent hollow fiber membranes 1, and the tension means 3 is pulled by the spring 6.

【0014】中空糸膜1としては、種々のものを使用す
ることができ、例えば、セルロース系、ポリオレフィン
系、ポリビニルアルコール系、PMMA系、ポリスルホ
ン系等の各種材質でなるものを使用することができる。
ただし、編地への加工のし易さ等を考えると、ポリエチ
レン系等の強伸度の高い材質のものを使用することが好
ましい。なお、濾過膜として使用可能なものであれば、
その孔径、空孔率、膜厚、外径等には特に制限はない。
As the hollow fiber membrane 1, various materials can be used. For example, those made of various materials such as cellulose, polyolefin, polyvinyl alcohol, PMMA, and polysulfone can be used. .
However, considering the ease of processing into a knitted fabric, it is preferable to use a material having a high elongation such as polyethylene. In addition, if it can be used as a filtration membrane,
The pore diameter, porosity, film thickness, outer diameter, etc. are not particularly limited.

【0015】中空糸膜1は横長の長方形状で、その両側
端には支持枠5が結合固着されており、該両側の支持枠
5によって略垂直となるように支持される。支持枠5は
金属や合成樹脂のように強度の高い材質でなり、金属で
ある場合には防錆処理が施される。又、中空糸膜1は相
互に間隔をあけて三枚並設されているが、その並設枚
数、間隔寸法等は濾過処理能力に応じて適宜に設定され
る。各中空糸膜1間において隣接する支持枠5は相互
に、接着或いは固着具等の適宜結合手段によって結合一
体化されている。
The hollow fiber membrane 1 has a horizontally long rectangular shape, and has support frames 5 fixedly attached to both ends thereof, and is supported by the support frames 5 on both sides so as to be substantially vertical. The support frame 5 is made of a high-strength material such as a metal or a synthetic resin. Further, three hollow fiber membranes 1 are arranged side by side with an interval therebetween, and the number of the arranged side panels, the dimension of the interval, and the like are appropriately set according to the filtration capacity. The support frames 5 adjacent to each other between the hollow fiber membranes 1 are integrally connected to each other by an appropriate connecting means such as an adhesive or a fixing tool.

【0016】結合一体化された三本の支持枠5のうち、
最も外側に位置する両側の支持枠5の外面にはガイドロ
ーラ7が配設固定されている。この場合、ガイドローラ
7は上下に二個づつ対向配置されて一組が構成され、該
一組のガイドローラ7が一つの支持枠5の外面の上部、
中部、下部に三組配設されている。又、中空糸膜1の両
側端の支持枠5においても同様にガイドローラ7は配設
固定されるので、同ガイドローラ7は四隅に位置する各
支持枠5に各々三組づつ配設固定されることになる。
Of the three support frames 5 integrated and integrated,
Guide rollers 7 are disposed and fixed to the outer surfaces of the outermost support frames 5 located on both sides. In this case, two sets of the guide rollers 7 are arranged facing each other in the upper and lower directions to form a set, and the set of the guide rollers 7 is formed on the upper portion of the outer surface of one support frame 5.
There are three sets in the middle and lower part. Similarly, the guide rollers 7 are disposed and fixed also on the support frames 5 on both side ends of the hollow fiber membrane 1, so that three sets of the guide rollers 7 are disposed and fixed on the support frames 5 located at the four corners. Will be.

【0017】好気槽体2の相対向する内壁面には各々、
その両側において上部、中部、下部に支持レール8が杆
状に突設されている。この場合、各支持レール8は上記
ガイドローラ7の各組に対応する位置に配設されてい
て、図2に詳細に示す如く、同支持レール8に各組の上
下のガイドローラ7が転動自在に係合されることによっ
て、支持枠5を介し一体化された三枚の中空糸膜1がま
とめて略垂直に架設支持される。又、中空糸膜1の両側
において、結合一体化された支持枠5が略水平方向にス
ライド自在となるように支持されている。
On the opposed inner wall surfaces of the aerobic tank 2,
On both sides, support rails 8 are provided at upper, middle and lower portions in a rod-like manner. In this case, each support rail 8 is disposed at a position corresponding to each set of the guide rollers 7, and the upper and lower guide rollers 7 of each set roll on the support rail 8, as shown in detail in FIG. By being freely engaged, the three hollow fiber membranes 1 integrated via the support frame 5 are collectively supported substantially vertically. Further, on both sides of the hollow fiber membrane 1, a support frame 5 integrated and integrated is supported so as to be slidable in a substantially horizontal direction.

【0018】結合一体化された支持枠5の上下方向にお
ける中部と好気槽体2の内壁面との間には、両者を結合
するスプリング6が水平方向に三つ各支持枠5ごとに介
在配設されており、該三つのスプリング6がテンション
手段3として、三枚の中空糸膜1を略水平方向に引っ張
るものである。この場合、中空糸膜1の両側に同スプリ
ング6によるテンション手段3が同様に配設されてい
て、各中空糸膜1は両側方へ均等に引っ張られる。又、
各スプリング6による引っ張り力の初期値は4kgで、片
側のテンション手段3としては計12kgとなり、該12kgの
引っ張り力によって両側から引っ張られることになる。
なお、この引っ張り力は、中空糸膜1の材質、並設枚数
等に応じて適宜変更設定される。
Between the vertically central portion of the integrated support frame 5 and the inner wall surface of the aerobic tank 2, springs 6 connecting the two are interposed in the horizontal direction for each of the three support frames 5. The three springs 6 serve as tensioning means 3 for pulling the three hollow fiber membranes 1 in a substantially horizontal direction. In this case, tension means 3 by the same spring 6 are similarly arranged on both sides of the hollow fiber membrane 1, and each hollow fiber membrane 1 is equally pulled to both sides. or,
The initial value of the tension force by each spring 6 is 4 kg, and the tension means 3 on one side is 12 kg in total, and the tension means 3 is pulled from both sides by the tension force of 12 kg.
Note that the pulling force is appropriately changed and set according to the material of the hollow fiber membrane 1, the number of juxtaposed fibers, and the like.

【0019】又、並設された中空糸膜1の両外側には、
該中空糸膜1と略平行に回流仕切板2aが配設固定されて
おり、該両側の回流仕切板2aの内側において好気槽体2
内の下部に散気管4が配設されている。この場合、散気
管4から噴出される下方からの空気によって、同両側の
回流仕切板2aの間のスペースにおいて上昇攪拌流が発生
し、同回流仕切板2aの両外側のスペースにおいては下降
流となって、好気槽体2内に汚泥を含む被処理水の回流
が形成される。
On both outer sides of the hollow fiber membranes 1 arranged side by side,
A circulation partition 2a is disposed and fixed substantially parallel to the hollow fiber membrane 1, and the aerobic tank body 2 is provided inside the circulation divider 2a on both sides.
An air diffuser 4 is provided at a lower part of the inside. In this case, an upward stirring flow is generated in the space between the circulating partition plates 2a on both sides by the air blown from the diffuser pipe 4 from below, and a downward flow is generated in the space on both outer sides of the circulating partition plate 2a. As a result, circulating water to be treated containing sludge is formed in the aerobic tank 2.

【0020】それ故に、該実施形態の浄化槽において
は、好気槽体2内で、散気管4から噴出される空気によ
って該好気槽体2内に好気状態が形成され、該好気状態
において被処理水の活性汚泥処理が行われる。すなわ
ち、各中空糸膜1にて被処理水が固液分離され、この固
液分離において、活性汚泥が好気槽体2内に保持される
一方、濾過された膜透過液は処理水として該好気槽体2
から送出され、同活性汚泥によって被処理水が好気的に
生物学的処理される。又、散気管4から噴出される下方
からの空気によって各中空糸膜1は曝気され、これによ
り、被処理水に上昇攪拌流が発生し、同各中空糸膜1の
濾過膜の膜面に付着したケーキ層が剥離されて膜洗浄が
行われる。
Therefore, in the septic tank according to this embodiment, the aerobic state is formed in the aerobic tank body 2 by the air blown out from the diffuser pipe 4 in the aerobic tank body 2. Activated sludge treatment of the water to be treated is performed. That is, the water to be treated is solid-liquid separated in each hollow fiber membrane 1, and in this solid-liquid separation, activated sludge is held in the aerobic tank body 2, while the filtered membrane permeate is treated as treated water. Aerobic tank 2
And the treated water is aerobically biologically treated by the activated sludge. Further, each hollow fiber membrane 1 is aerated by the air blown from the air diffuser 4 from below, whereby a rising agitated flow is generated in the water to be treated, and the surface of the filtration membrane of each hollow fiber membrane 1 is formed. The attached cake layer is peeled off, and the film is washed.

【0021】上記好気槽体2から送出される処理水は、
図3に示す如く、連通管9を通じて処理水貯留用の貯留
槽体10へと送られ、次いで、放流ポンプ11によって同貯
留槽体10から汲み上げられ、放流管12を通じて消毒槽体
13へと送られ、この後に、浄化槽外へと放流される。
又、該浄化槽においては、二つの流量調整槽体14が排水
流入側に配設されており、該二つの流量調整槽体14に流
入する排水の流入量を調整した後に、移送ポンプ15で汚
泥移送管16を通じて好気槽体2へと移送するようになっ
ている。そして、二つの流量調整槽体14及び好気槽体2
の水位を、各々に設けた水位検知部17で検知し、検知さ
れた水位に応じて移送ポンプ15及び放流ポンプ11の動作
を制御する制御部18を設けている。この場合、流量調整
槽体14及び好気槽体2における検知すべき水位L1、L
2は、各々予め設定されている。
The treated water sent out from the aerobic tank 2 is
As shown in FIG. 3, the treated water is sent to a storage tank body 10 for storing treated water through a communication pipe 9, then pumped up from the storage tank body 10 by a discharge pump 11, and then disinfected by a discharge pipe 12.
It is sent to 13, after which it is discharged outside the septic tank.
Further, in the septic tank, two flow control tank bodies 14 are disposed on the drain inflow side, and after adjusting the inflow amount of the wastewater flowing into the two flow control tank bodies 14, the sludge is transferred by the transfer pump 15. The air is transferred to the aerobic tank 2 through the transfer pipe 16. Then, the two flow control tanks 14 and the aerobic tank 2
The water level is detected by a water level detection unit 17 provided in each of them, and a control unit 18 that controls the operations of the transfer pump 15 and the discharge pump 11 according to the detected water level is provided. In this case, the water levels L1, L to be detected in the flow rate adjusting tank 14 and the aerobic tank 2
2 is set in advance.

【0022】したがって、該実施形態の浄化槽において
は、中空糸膜1がテンション手段3により略水平方向に
引っ張られて常に伸張された状態に保持されるので、上
下方向の汚泥の回流に対しても同中空糸膜1には弛みが
発生せず、同回流する汚泥に対する圧力損失の増大が防
止されて、該汚泥の回流速度は低下することなく均一に
保持される。これにより、中空糸膜1は効率良く洗浄さ
れて閉塞することもなく、濾過浄化能力が高く維持され
る。すなわち、図1(a)に示す如く、好気槽体2内部
の中程部分(二点鎖線で囲んだ部分)において、中空糸
膜1に弛みが発生せず、回流する汚泥に対する圧力損失
が増大せず、該汚泥の回流速度の低下が防止されるもの
である。
Therefore, in the septic tank of this embodiment, since the hollow fiber membrane 1 is pulled in the substantially horizontal direction by the tension means 3 and is always kept in an expanded state, the hollow fiber membrane 1 is also protected against the vertical flow of sludge. The hollow fiber membrane 1 is not slackened, the pressure loss of the sludge flowing at the same time is prevented from increasing, and the circulation speed of the sludge is kept uniform without decreasing. As a result, the hollow fiber membrane 1 is efficiently washed without clogging, and the filtration and purification ability is maintained at a high level. That is, as shown in FIG. 1A, in the middle part of the aerobic tank body 2 (the part surrounded by the two-dot chain line), the hollow fiber membrane 1 does not loosen, and the pressure loss to the circulating sludge is reduced. The sludge does not increase, and a decrease in the circulation speed of the sludge is prevented.

【0023】又、該実施形態の浄化槽においては、散気
管4から噴出される下方からの空気によって中空糸膜1
が曝気され、被処理水には上昇攪拌流が発生して、同中
空糸膜1の濾過膜の膜面に付着したケーキ層は効果的に
剥離され、より効率的な膜洗浄が行われる。しかも、こ
の場合に、中空糸膜1が略垂直となり相互に間隔をあけ
て複数枚並設されているので、濾過洗浄能力が向上され
ているのはもちろんのこと、略垂直となる各中空糸膜1
間の間隔を攪拌流がスムーズに上昇して、汚泥の回流速
度が高められると共に膜洗浄能力も向上されている。
Further, in the septic tank of this embodiment, the hollow fiber membrane 1 is blown by air blown from the air diffuser 4 from below.
Is aerated, a rising stirring flow is generated in the water to be treated, and the cake layer attached to the membrane surface of the filtration membrane of the hollow fiber membrane 1 is effectively peeled off, and more efficient membrane washing is performed. In addition, in this case, since the hollow fiber membranes 1 are substantially vertical and a plurality of hollow fiber membranes are arranged side by side with an interval therebetween, not only the filtration and washing performance is improved, but also the hollow fiber Membrane 1
The agitated flow smoothly rises in the interval between the sludges, thereby increasing the circulation speed of the sludge and improving the membrane cleaning ability.

【0024】又、該実施形態の浄化槽においては、中空
糸膜1がその両側端に配設される支持枠5間に架設支持
されているので、該支持枠5がテンション手段3によっ
て側方へ引っ張られることにより、同中空糸膜1は全体
が均等に略水平方向に引っ張られてその弛み変形が確実
に防止される。しかも、この場合に、中空糸膜1が相互
に間隔をあけて複数枚並設され、各中空糸膜1を架設支
持するその両側端の支持枠5が隣接するもの相互で結合
一体化されているので、テンション手段3による引っ張
り力が同結合一体化された支持枠5を介して各中空糸膜
1に均等に作用し、複数枚の同中空糸膜1の弛み変形が
効率良く確実に防止される。又、スプリングにより引っ
張るテンション手段3であるので、中空糸膜1が弾性的
に引っ張られて保持され、該中空糸膜1に加わる汚泥回
流時の衝撃は吸収されてその破損が防止される。
In the septic tank of this embodiment, since the hollow fiber membrane 1 is supported between the supporting frames 5 disposed on both side ends thereof, the supporting frame 5 is laterally moved by the tension means 3. By being pulled, the entire hollow fiber membrane 1 is evenly pulled substantially in the horizontal direction, and the loosening deformation is reliably prevented. Moreover, in this case, a plurality of hollow fiber membranes 1 are juxtaposed at a distance from each other, and support frames 5 on both side ends for supporting and supporting each hollow fiber membrane 1 are connected and integrated with each other. Therefore, the tensile force of the tension means 3 uniformly acts on each hollow fiber membrane 1 via the support frame 5 integrated and integrated, and the slack deformation of the plurality of hollow fiber membranes 1 is efficiently and reliably prevented. Is done. Further, since the tension means 3 is pulled by a spring, the hollow fiber membrane 1 is elastically pulled and held, and the shock applied to the hollow fiber membrane 1 at the time of sludge circulation is absorbed to prevent breakage.

【0025】図4、5は、本発明の請求項1〜5、7に
対応する別の実施形態を示し、該実施形態の浄化槽にお
いては、テンション手段3が錘体19により引っ張るもの
である。この場合、図5に詳細に示す如く、錘体19を吊
下支持する索状体20の中程が支持ローラ21に巻掛けら
れ、該索状体20の先端が支持枠5の略中央に連結されて
おり、同支持ローラ21は好気槽体2の内壁面に突設され
る支持杆体22の先端部分に回動自在に取り付けられてい
る。又、同錘体19、索状体20、支持ローラ21等でなるテ
ンション手段3は中空糸膜1の両側に同様に配設されて
おり、各中空糸膜1は両側方へ均等に引っ張られる。
FIGS. 4 and 5 show another embodiment corresponding to claims 1 to 5 and 7 of the present invention. In the septic tank of this embodiment, the tension means 3 is pulled by a weight 19. In this case, as shown in detail in FIG. 5, the middle of the cord 20 that suspends and supports the weight 19 is wound around the support roller 21, and the tip of the cord 20 is substantially at the center of the support frame 5. The supporting roller 21 is rotatably attached to a tip end of a supporting rod 22 protruding from an inner wall surface of the aerobic tank 2. Further, the tension means 3 including the same weight 19, the cord-like body 20, the support roller 21 and the like are similarly arranged on both sides of the hollow fiber membrane 1, and each hollow fiber membrane 1 is equally pulled to both sides. .

【0026】したがって、該実施形態の浄化槽において
は、特に、錘体19による引っ張り力が変化しないので、
各中空糸膜1は一定の引っ張り力でもって伸張された状
態に確保される。なお、それ以外は上記実施形態と同様
に構成されており、上記実施形態におけると同様の作用
効果が奏される。
Therefore, in the septic tank of this embodiment, in particular, since the pulling force of the weight 19 does not change,
Each hollow fiber membrane 1 is secured in a stretched state with a constant tensile force. The other configuration is the same as that of the above embodiment, and the same operation and effect as those of the above embodiment can be obtained.

【0027】図6は、本発明の請求項1〜5、7に対応
する更に別の実施形態を示し、該実施形態の浄化槽にお
いては、錘体19、索状体20、支持ローラ21等でなるテン
ション手段3が中空糸膜1の片側だけに設けられてい
る。なお、それ以外は上記実施形態と同様に構成されて
おり、上記実施形態におけると同様の作用効果が奏され
る。
FIG. 6 shows still another embodiment corresponding to claims 1 to 5 and 7 of the present invention. In the septic tank of this embodiment, a weight 19, a cord 20 and a support roller 21 are used. Is provided on only one side of the hollow fiber membrane 1. The other configuration is the same as that of the above embodiment, and the same operation and effect as those of the above embodiment can be obtained.

【0028】[0028]

【発明の効果】上述の如く、本発明の請求項1記載の浄
化槽においては、中空糸膜が略水平方向に引っ張られて
伸張された状態に保持されるので、該中空糸膜には弛み
が発生せず、回流する汚泥に対する圧力損失の増大が防
止され、該汚泥の回流速度は低下することなく均一に保
持され、これにより、中空糸膜は効率良く洗浄されて閉
塞することもなく、濾過浄化能力が高く維持される。
As described above, in the septic tank according to the first aspect of the present invention, the hollow fiber membrane is held in a stretched state by being pulled in a substantially horizontal direction. No increase in pressure loss to the circulating sludge is prevented, and the circulating speed of the sludge is maintained uniformly without lowering, whereby the hollow fiber membrane is efficiently washed and clogged without filtration. Purification capacity is kept high.

【0029】又、本発明の請求項2記載の浄化槽におい
ては、特に、散気管から噴出される下方からの空気によ
って中空糸膜が曝気され、被処理水には上昇攪拌流が発
生して、同中空糸膜の濾過膜の膜面に付着したケーキ層
は効果的に剥離され、より効率的な膜洗浄が行われる。
Further, in the septic tank according to the second aspect of the present invention, the hollow fiber membrane is aerated by air from below which is blown out from the air diffuser, and an ascending flow is generated in the water to be treated. The cake layer adhering to the membrane surface of the filtration membrane of the hollow fiber membrane is effectively peeled off, and more efficient membrane cleaning is performed.

【0030】又、本発明の請求項3記載の浄化槽におい
ては、特に、中空糸膜が複数枚並設されることによって
濾過洗浄能力が向上するのはもちろんのこと、略垂直と
なる各中空糸膜間の間隔を攪拌流がスムーズに上昇し
て、汚泥の回流速度が高められると共に膜洗浄能力も向
上される。
In the septic tank according to the third aspect of the present invention, in particular, not only the hollow fiber membranes are arranged in parallel to improve the filtration / cleaning ability but also each of the hollow fibers which are substantially vertical. The agitated flow smoothly rises between the membranes, thereby increasing the sludge circulation speed and improving the membrane cleaning ability.

【0031】又、本発明の請求項4記載の浄化槽におい
ては、特に、中空糸膜がその両側端に配設される支持枠
間に架設支持されているので、該支持枠がテンション手
段によって側方へ引っ張られることにより、同中空糸膜
は全体が均等に略水平方向に引っ張られてその弛み変形
が確実に防止される。
Further, in the septic tank according to the fourth aspect of the present invention, since the hollow fiber membrane is particularly supported between the supporting frames provided at both ends thereof, the supporting frame is supported by the tension means. By being pulled in the direction, the hollow fiber membrane is pulled evenly in the substantially horizontal direction as a whole, so that the slack deformation is reliably prevented.

【0032】又、本発明の請求項5記載の浄化槽におい
ては、特に、中空糸膜が複数枚並設されることによって
濾過洗浄能力が向上するのはもちろんのこと、隣接する
中空糸膜間で支持枠が相互に結合一体化されるため、テ
ンション手段による引っ張り力が同結合一体化された支
持枠を介して各中空糸膜に均等に作用し、複数枚の同中
空糸膜の弛み変形が効率良く確実に防止される。
In the septic tank according to the fifth aspect of the present invention, in particular, the filtration and washing ability is improved by providing a plurality of hollow fiber membranes in parallel, and the hollow fiber membranes between adjacent hollow fiber membranes can be improved. Since the support frames are combined and integrated with each other, the tensile force by the tension means acts evenly on each hollow fiber membrane through the support frame integrated and integrated with the same, and the slack deformation of a plurality of the hollow fiber membranes is prevented. It is prevented efficiently and reliably.

【0033】又、本発明の請求項6記載の浄化槽におい
ては、特に、スプリングにより中空糸膜が弾性的に引っ
張られて保持されるので、該中空糸膜に加わる汚泥回流
時の衝撃は吸収されてその破損が防止される。
In the septic tank according to claim 6 of the present invention, the hollow fiber membrane is particularly elastically pulled and held by the spring, so that the shock applied to the hollow fiber membrane during the circulation of sludge is absorbed. Damage is prevented.

【0034】又、本発明の請求項7記載の浄化槽におい
ては、特に、錘体による引っ張り力が変化しないので、
中空糸膜は一定の引っ張り力でもって伸張された状態に
確保される。
In the septic tank according to claim 7 of the present invention, in particular, since the pulling force of the weight does not change,
The hollow fiber membrane is secured in a stretched state with a certain tensile force.

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

【図1】本発明の一実施形態である浄化槽における好気
槽体内部構造を示し、(a)はその平面図、(b)はそ
の正面図。
1A and 1B show an internal structure of an aerobic tank in a septic tank according to an embodiment of the present invention, wherein FIG. 1A is a plan view and FIG.

【図2】同好気槽体内の要部構造を示し、(a)はその
拡大側面図、(b)はその拡大正面図。
FIGS. 2A and 2B show an essential part structure in the aerobic tank body, wherein FIG. 2A is an enlarged side view thereof, and FIG.

【図3】同浄化槽全体の内部構造を示す概略側面図。FIG. 3 is a schematic side view showing the internal structure of the entire septic tank.

【図4】本発明の別の実施形態である浄化槽における好
気槽体内部構造を示し、(a)はその平面図、(b)は
その正面図。
4A and 4B show an internal structure of an aerobic tank body in a septic tank according to another embodiment of the present invention, wherein FIG. 4A is a plan view and FIG.

【図5】同好気槽体内の要部構造を示し、(a)はその
拡大側面図、(b)はその拡大正面図。
FIGS. 5A and 5B show an essential part structure in the aerobic tank body, FIG. 5A is an enlarged side view thereof, and FIG. 5B is an enlarged front view thereof.

【図6】本発明の更に別の実施形態である浄化槽におけ
る好気槽体内部構造を示す正面図。
FIG. 6 is a front view showing the internal structure of an aerobic tank in a septic tank according to still another embodiment of the present invention.

【図7】従来例である浄化槽における好気槽体内部構造
を示す概略平面図。
FIG. 7 is a schematic plan view showing an internal structure of an aerobic tank in a conventional septic tank.

【図8】同従来例である浄化槽における中空糸膜を示
し、(a)はその平面図、(b)はその正面図。
8A and 8B show a hollow fiber membrane in a septic tank according to the conventional example, wherein FIG. 8A is a plan view and FIG. 8B is a front view.

【符号の説明】[Explanation of symbols]

1 中空糸膜 2 好気槽体 3 テンション手段 4 散気管 5 支持枠 6 スプリング 19 錘体 DESCRIPTION OF SYMBOLS 1 Hollow fiber membrane 2 Aerobic tank 3 Tension means 4 Air diffuser 5 Support frame 6 Spring 19 Weight

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 中空糸膜が内装された好気槽体を有する
浄化槽であって、中空糸膜を略水平方向に引っ張るテン
ション手段を具備してなる浄化槽。
1. A septic tank having an aerobic tank body in which a hollow fiber membrane is provided, wherein the septic tank includes tension means for pulling the hollow fiber membrane in a substantially horizontal direction.
【請求項2】 好気槽体内の中空糸膜の下方に散気管が
配設されていることを特徴とする請求項1記載の浄化
槽。
2. The septic tank according to claim 1, wherein an air diffuser is disposed below the hollow fiber membrane in the aerobic tank.
【請求項3】 中空糸膜が略垂直となり相互に間隔をあ
けて複数枚並設された状態で好気槽体に内装されている
ことを特徴とする請求項2記載の浄化槽。
3. The septic tank according to claim 2, wherein the hollow fiber membranes are substantially vertical and are installed in the aerobic tank body in a state where a plurality of hollow fiber membranes are juxtaposed at intervals.
【請求項4】 中空糸膜をその両側端に配設される支持
枠間に架設支持して該支持枠を側方へ引っ張るテンショ
ン手段となしたことを特徴とする請求項1〜3のいずれ
か一つの請求項記載の浄化槽。
4. A tensioning means for supporting a hollow fiber membrane between supporting frames provided on both side ends thereof and pulling the supporting frame to the side. A septic tank according to any one of the preceding claims.
【請求項5】 中空糸膜が相互に間隔をあけて複数枚並
設された状態で好気槽体に内装されており、隣接する中
空糸膜間で支持枠を相互に結合一体化したことを特徴と
する請求項4記載の浄化槽。
5. A plurality of hollow fiber membranes are installed in an aerobic tank with a plurality of hollow fiber membranes arranged side by side at an interval from each other, and a supporting frame is mutually connected and integrated between adjacent hollow fiber membranes. The septic tank according to claim 4, characterized in that:
【請求項6】 スプリングにより引っ張るテンション手
段であることを特徴とする請求項1〜5のいずれか一つ
の請求項記載の浄化槽。
6. A septic tank according to claim 1, wherein said septic tank is tension means for pulling by a spring.
【請求項7】 錘体により引っ張るテンション手段であ
ることを特徴とする請求項1〜5のいずれか一つの請求
項記載の浄化槽。
7. The septic tank according to any one of claims 1 to 5, wherein the septic tank is tension means for pulling by a weight.
JP34030096A 1996-12-20 1996-12-20 Septic tank Pending JPH10174986A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP34030096A JPH10174986A (en) 1996-12-20 1996-12-20 Septic tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP34030096A JPH10174986A (en) 1996-12-20 1996-12-20 Septic tank

Publications (1)

Publication Number Publication Date
JPH10174986A true JPH10174986A (en) 1998-06-30

Family

ID=18335632

Family Applications (1)

Application Number Title Priority Date Filing Date
JP34030096A Pending JPH10174986A (en) 1996-12-20 1996-12-20 Septic tank

Country Status (1)

Country Link
JP (1) JPH10174986A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6863817B2 (en) 2002-12-05 2005-03-08 Zenon Environmental Inc. Membrane bioreactor, process and aerator
WO2016019272A1 (en) * 2014-07-31 2016-02-04 Clark Technology, LLC Single-stage water treatment system
CN109569302A (en) * 2018-12-17 2019-04-05 合肥信达膜科技有限公司 A kind of internal pressure ultrafiltration membrane elements
US10266440B2 (en) 2016-07-01 2019-04-23 Abdolreza Assadi Anaerobic digestion system and method

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6863817B2 (en) 2002-12-05 2005-03-08 Zenon Environmental Inc. Membrane bioreactor, process and aerator
US7022236B2 (en) 2002-12-05 2006-04-04 Zenon Environmental Inc. Membrane bioreactor, process and aerator
WO2016019272A1 (en) * 2014-07-31 2016-02-04 Clark Technology, LLC Single-stage water treatment system
US10266440B2 (en) 2016-07-01 2019-04-23 Abdolreza Assadi Anaerobic digestion system and method
US11691903B2 (en) 2016-07-01 2023-07-04 Abdolreza Assadi Anaerobic digestion system
CN109569302A (en) * 2018-12-17 2019-04-05 合肥信达膜科技有限公司 A kind of internal pressure ultrafiltration membrane elements

Similar Documents

Publication Publication Date Title
JP2541595B2 (en) Method and apparatus for performing microbubble aeration over a large area of liquid
US20090218299A1 (en) Inverted aerated immersed screen, screen assembly and operating process
JP7103728B2 (en) Operation method of membrane separation device and wastewater treatment equipment
JPH10174986A (en) Septic tank
JPH0716589B2 (en) Hollow fiber membrane filtration device
KR100544383B1 (en) Hollow Fiber Membrane Module Combined with Air Diffuser
JP4188226B2 (en) Filtration device and filtration method using the filtration device
JP2000107791A (en) Apparatus for treating activated sludge
JP2000210542A (en) Method and apparatus for washing membrane unit in waste water treatment equipment
JPH0975970A (en) Dipping type membrane separation device using hollow fiber membrane
JP2001286881A (en) Water treating device and water treating system provided with the water treating device
JP2001286888A (en) Water treating device and water treating system having the same
JP2904102B2 (en) Sewage septic tank
JP3054821B2 (en) Aerobic filter bed tank for sewage purification tank
JP2000051885A (en) Activated sludge treatment apparatus
JP3024638B2 (en) Sewage treatment tank treatment method
JP3897419B2 (en) Filtration method and filtration apparatus using hollow fiber membrane module
JP3072287B2 (en) Operation method of aerobic filter bed tank for sewage purification tank
JPH06114242A (en) Sheet-like hollow fiber membrane
JP2000037698A (en) Method and apparatus for biological treatment of sewage
JPH04247287A (en) Hollow fiber filter module
JPH06142463A (en) Flat type hollow yarn membrane module
JPH0615286A (en) Contact oxidation apparatus
JP3450877B2 (en) Aerobic filter bed processing device with membrane module
JP2004105800A (en) Membrane separation device, membrane-separation activated sludge treatment apparatus, and treatment method