JPH1043516A - Filter device for separation of solid from liquid, such as sewage and waste water - Google Patents
Filter device for separation of solid from liquid, such as sewage and waste waterInfo
- Publication number
- JPH1043516A JPH1043516A JP8224495A JP22449596A JPH1043516A JP H1043516 A JPH1043516 A JP H1043516A JP 8224495 A JP8224495 A JP 8224495A JP 22449596 A JP22449596 A JP 22449596A JP H1043516 A JPH1043516 A JP H1043516A
- Authority
- JP
- Japan
- Prior art keywords
- sewage
- wires
- waste water
- peripheral wall
- solid
- 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
Landscapes
- Filtration Of Liquid (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、浄化槽などの内部
に設置して、汚水や廃水等の固液を分離するための濾過
装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a filter installed in a septic tank or the like for separating solid and liquid such as wastewater and wastewater.
【0002】[0002]
【従来の技術】従来、汚水や廃水中に浮遊するスラッヂ
を除くために、濾過する方法、遠心力により分離する方
法、加圧して浮上させる方法、凝集剤を添加して固める
方法等が採用されている。2. Description of the Related Art Conventionally, in order to remove sludge floating in sewage or wastewater, a method of filtering, a method of separating by centrifugal force, a method of floating by applying pressure, a method of adding a flocculant, and solidifying are adopted. ing.
【0003】このうち、濾過する方法では、一般的に濾
過膜などが使用されることが多い。しかしながら、濾過
膜は一枚だけでは効果が少ないので多数枚を積層する必
要があるが、そのように濾過膜を何枚も積層した構造の
ものは製造が面倒であった。また、濾過材としては、こ
の他、布、砂、セラミック、多孔体等の各種の素材が使
用されているが、このような濾過材は、長期間使用する
ことにより目詰まりが生じやすく、そのような場合に逆
洗再使用が困難であるという問題があった。[0003] Of these, in the method of filtration, a filtration membrane or the like is generally used in many cases. However, since only one filter membrane has little effect, it is necessary to laminate a large number of filter membranes. However, such a structure in which a plurality of filter membranes are laminated has been troublesome to manufacture. In addition, various materials such as cloth, sand, ceramics, and porous materials are used as the filtering material. However, such a filtering material is likely to be clogged by being used for a long period of time. In such a case, there is a problem that backwashing and reuse are difficult.
【0004】[0004]
【発明が解決しようとする課題】そこで本発明は、十分
な濾過性能を有してしかも製造が容易で、また、長期間
の使用により目詰まりが生じた場合に逆洗再使用が容易
な汚水、廃水等の固液分離用濾過装置の提供を目的とす
る。SUMMARY OF THE INVENTION Accordingly, the present invention provides a sewage system which has sufficient filtration performance, is easy to manufacture, and is easy to backwash and reuse when clogging occurs due to long-term use. And a filtration device for solid-liquid separation of waste water and the like.
【0005】[0005]
【課題を解決するための手段】上記の目的は本発明によ
って、すなわち、多数の線条1を縦方向又は横方向に密
に並列するとともに、それら並列した線条1の所要位置
に別の線条2、フィルム又は接着剤付き部材等を向きが
異なるように配置して、その線条2、フィルム又は接着
剤付き部材等を上記の線条1に対し融着又は接着等の手
段により一体的に固着することによりスダレ状の膜板3
を形成し、その膜板3を筒状に巻いて膜板3が重層した
構造の周壁部7を有する筒状濾過部材6を構成し、汚水
や廃水がその周壁部7を通過して筒状濾過部材6の内外
に流通するようになした汚水、廃水等の固液分離用濾過
装置によって達成することができる。SUMMARY OF THE INVENTION The above object is achieved by the present invention, i.e., by arranging a large number of filaments 1 closely in the vertical or horizontal direction, and by providing another line at a required position of the parallel filaments. The line 2, the film or the member with the adhesive, etc. are arranged in different directions, and the line 2, the film, the member with the adhesive, etc. are integrated with the above-mentioned line 1 by means such as fusion or adhesion. The film plate 3 in the form of a drip is fixed to the
Is formed, and the membrane plate 3 is wound into a cylindrical shape to constitute a cylindrical filter member 6 having a peripheral wall portion 7 having a structure in which the membrane plate 3 is layered, and sewage and wastewater pass through the peripheral wall portion 7 to form a cylindrical filter member. This can be achieved by a filtration device for solid-liquid separation of sewage, wastewater, etc., which is made to flow in and out of the filtration member 6.
【0006】なお、スダレ状態の膜板3は、太さのそれ
ぞれ異なる線条1をその太さ順に並べて構成することが
可能である。[0006] The film plate 3 in the slender state can be formed by arranging the filaments 1 having different thicknesses in the order of the thickness.
【0007】[0007]
【実施例】以下、図面に基づき本発明の実施例について
説明する。まず、図1は本発明の濾過装置の構成要素で
ある膜板3を示したものである。この膜板3は、ポリプ
ロピレン等の熱可塑性プラスチック製のそれぞれ太さが
異なる多数の線条1を縦方向に且つ太さの順に密に並列
させるとともに、それらの並列した線条1の縦方向にお
ける複数箇所に一定間隔で別の同様に熱可塑性プラスチ
ック製の線条2を横方向に配置して、その線条2を上記
の線条1に融着して一体的に固着した構造になってお
り、全体的にスダレ状を呈している。なお、線条2の代
わりにフィルム又は接着剤付き部材等を使用することも
可能である。また、その線条2、フィルム又は接着剤付
き部材等は、融着の代わりに接着等の他の手段により固
着することも可能である。なお、線条1,2は上記のプ
ラスチックの他に、金属繊維、炭素繊維、セラミックや
ガラス繊維なども使用可能である。Embodiments of the present invention will be described below with reference to the drawings. First, FIG. 1 shows a membrane plate 3 which is a component of the filtration device of the present invention. This membrane plate 3 has a large number of filaments 1 made of a thermoplastic plastic such as polypropylene, each having a different thickness, which are densely arranged in the longitudinal direction and in the order of the thickness, and in the longitudinal direction of the parallel filaments 1. Another similar thermoplastic filament 2 is arranged laterally at a certain interval at a plurality of locations, and the filament 2 is fused to the above-mentioned filament 1 to be integrally fixed. And has a sloping shape as a whole. In addition, it is also possible to use a film or a member with an adhesive instead of the filament 2. Further, the wire 2, the film, the member with an adhesive, and the like can be fixed by other means such as adhesion instead of fusion. The filaments 1 and 2 may be made of metal fibers, carbon fibers, ceramics, glass fibers, or the like, in addition to the above-mentioned plastics.
【0008】上記の膜板3は、図3に示すように、金網
を筒状にした中芯4の周囲に複数回巻き付けて筒状とな
してからその周囲に固定リング5を嵌めてカートリッジ
式の筒状濾過部材6を構成している。すなわち、筒状濾
過部材6はその周壁部7が膜板3による重層構造となっ
ている。この筒状濾過部材6は、太い線条が外側に、細
い線条が内側になるように巻かれている。なお、中芯4
は筒状で隙間を有する構造のものなら金網以外でも構わ
ない。As shown in FIG. 3, the above-mentioned membrane plate 3 is wound around the core 4 made of a cylindrical wire mesh a plurality of times to form a tubular shape, and a fixing ring 5 is fitted around the tubular shape. Of the cylindrical filtration member 6. That is, the cylindrical filter member 6 has a multilayer structure in which the peripheral wall portion 7 is formed by the membrane plate 3. The tubular filtration member 6 is wound such that a thick line is on the outside and a thin line is on the inside. The core 4
May be anything other than a wire mesh as long as it has a cylindrical structure with a gap.
【0009】図2及び図3は装置の全体構造を示したも
のである。上記の筒状濾過部材6は両端にそれぞれ取付
用アダプタ8,9を嵌着して、ケース10の内部に着脱
自在に装着されている。すなわち、ケース10の両側の
側壁にそれぞれ設けた開口部11,12に取付用アダプ
タ8,9が螺着している。ケース10には汚水や廃水の
原液15の出入り口13,14が開設されている。ケー
ス10に入った原液15は、筒状濾過部材6の周壁部7
を通過してその内部に入る。そして、周壁部7を通過す
るときに濾過され、その濾過液16は筒状濾過部材6の
内部を流れて一端又は両端から流出するようになってい
る。FIGS. 2 and 3 show the entire structure of the apparatus. The tubular filtering member 6 has attachment adapters 8 and 9 fitted to both ends thereof, and is detachably mounted inside the case 10. That is, the mounting adapters 8 and 9 are screwed into the openings 11 and 12 provided on the side walls on both sides of the case 10, respectively. The case 10 is provided with entrances 13 and 14 for an undiluted solution 15 of sewage and wastewater. The undiluted solution 15 that has entered the case 10 is removed from the peripheral wall 7 of the cylindrical filtration member 6.
Through to get inside. Then, the filtrate 16 is filtered when passing through the peripheral wall portion 7, and the filtrate 16 flows inside the cylindrical filter member 6 and flows out from one end or both ends.
【0010】上記の実施例では、膜板3から筒状濾過部
材6を形成する場合に、太い線条が外側になるような巻
き方をしているが、太い線条が内側になって細い線条が
外側になるような巻き方も可能である。そのように逆向
きに巻いた場合は、筒状濾過部材6の内側へ原液15を
入れて、濾過液16を筒状濾過部材6の外側のケース1
0内へ流出させる。In the above embodiment, when the cylindrical filtering member 6 is formed from the membrane plate 3, the winding is performed such that the thick line is on the outside, but the thick line is on the inside and is thin. A winding method in which the filament is on the outside is also possible. In the case of such a reverse winding, the undiluted solution 15 is put into the inside of the cylindrical filtration member 6, and the filtrate 16 is poured into the case 1 outside the cylindrical filtration member 6.
Discharge into 0.
【0011】[0011]
【発明の効果】本発明の汚水、廃水等の固液分離用濾過
装置は上記の通りであり、1枚のスダレ状の膜板3を筒
状に巻くことによって膜板3が重層した構造の周壁部7
を有する筒状濾過部材6を構成するので、その周壁部7
を汚水や廃水の原液15が通過するときに十分に濾過す
ることができる。しかも、従来のように濾過膜を何枚も
積層するという面倒がなく、膜板3を巻くだけで筒状濾
過部材6を容易に製造できるという利点がある。また、
筒状濾過部材6を構成するのはスダレ状の膜板3で空隙
が規則的に配列しているので、目詰まりが生じた場合に
濾過液16を逆流させてスラッヂを取り除くという逆洗
再使用が容易である。特に筒状濾過部材6の内部にスラ
ッヂが詰まっても筒状濾過部材6を展開することによっ
てその内部のスラッヂも容易に除去できるという利点が
ある。そして、その筒状濾過部材6はカートリッジ式な
ので性能が低下した場合に簡単に交換できるという利便
性がある。また、請求項2記載のように、太さのそれぞ
れ異なる線条をその太さの順に並べてスダレ状の膜板3
を形成すれは、それを巻いて筒状濾過部材6を構成した
ときに、その周壁部7の断面が、内外方向に太い線条の
層からより細い線条の層へと順に変化する重層構造とな
るので、濾過部材として最適な構造となる。The filtration apparatus for solid-liquid separation of sewage, waste water and the like according to the present invention is as described above, and has a structure in which the membrane plate 3 is layered by winding a single drip-like membrane plate 3 into a cylindrical shape. Surrounding wall 7
, The peripheral wall 7
Can be sufficiently filtered when the undiluted solution 15 of wastewater or wastewater passes. In addition, there is an advantage that the tubular filtration member 6 can be easily manufactured simply by winding the membrane plate 3 without the trouble of laminating a number of filtration membranes as in the related art. Also,
Since the cylindrical filter member 6 is composed of the sloping membrane plate 3 and the voids are regularly arranged, when the clogging occurs, the backflow of the filtrate 16 to remove the sludge by backflow of the filtrate 16 is performed. Is easy. In particular, there is an advantage that even if a sludge is clogged in the cylindrical filter member 6, the sludge inside the cylindrical filter member 6 can be easily removed by expanding the cylindrical filter member. And since the cylindrical filtration member 6 is a cartridge type, it has the convenience that it can be easily replaced when its performance is reduced. Further, as in claim 2, the filaments having different thicknesses are arranged in the order of the thicknesses, and the film plate 3 in the form of a sludge is formed.
Is formed in a multilayer structure in which, when the cylindrical filter member 6 is formed by winding it, the cross section of the peripheral wall portion 7 changes in order from the thick line to the thin line in the inward and outward directions. Therefore, the structure becomes optimal as a filtering member.
【図1】膜板の平面図である。FIG. 1 is a plan view of a membrane plate.
【図2】装置全体の断面図である。FIG. 2 is a sectional view of the entire apparatus.
【図3】図2のA−A線断面図である。FIG. 3 is a sectional view taken along line AA of FIG. 2;
1 線条 2 線条 3 膜板 4 中芯 5 固定リング 6 筒状濾過部材 7 周壁部 8 取付用アダプタ 9 取付用アダプタ 10 ケース 11 開口部 12 開口部 13 出入り口 14 出入り口 15 汚水や廃水の原液 16 濾過液 DESCRIPTION OF SYMBOLS 1 Filament 2 Filament 3 Membrane plate 4 Core 5 Fixing ring 6 Cylindrical filter member 7 Peripheral wall 8 Mounting adapter 9 Mounting adapter 10 Case 11 Opening 12 Opening 13 Doorway 14 Doorway 15 Undiluted solution of waste water and waste water 16 Filtrate
Claims (2)
並列するとともに、それら並列した線条1の所要位置に
別の線条2、フィルム又は接着剤付き部材等を向きが異
なるように配置して、その線条2、フィルム又は接着剤
付き部材等を上記の線条1に対し融着又は接着等の手段
により一体的に固着することによりスダレ状の膜板3を
形成し、その膜板3を筒状に巻いて膜板3が重層した構
造の周壁部7を有する筒状濾過部材6を構成し、汚水や
廃水がその周壁部7を通過して筒状濾過部材6の内外に
流通するようになした汚水、廃水等の固液分離用濾過装
置。1. A large number of filaments 1 are closely arranged in the vertical or horizontal direction, and another filament 2, a film or a member with an adhesive is placed at a required position of the parallel filaments 1 in different directions. And the filament 2, the film or the member with adhesive are integrally fixed to the filament 1 by means such as fusion or adhesion to form a splayed membrane plate 3. The membrane plate 3 is wound into a cylindrical shape to constitute a cylindrical filter member 6 having a peripheral wall portion 7 having a structure in which the membrane plate 3 is layered, and sewage and wastewater pass through the peripheral wall portion 7 to form a cylindrical filter member 6. Filtration device for solid-liquid separation of sewage, wastewater, etc., which is circulated inside and outside.
順に並べてスダレ状の膜板3を形成した請求項1記載の
汚水、廃水等の固液分離用濾過装置。2. The filter for solid-liquid separation of sewage, waste water, etc. according to claim 1, wherein the filaments 1 having different thicknesses are arranged in the order of the thickness to form a slender membrane plate 3.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22449596A JP3218366B2 (en) | 1996-08-07 | 1996-08-07 | Filtration equipment for solid-liquid separation of sewage, wastewater, etc. |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22449596A JP3218366B2 (en) | 1996-08-07 | 1996-08-07 | Filtration equipment for solid-liquid separation of sewage, wastewater, etc. |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH1043516A true JPH1043516A (en) | 1998-02-17 |
JP3218366B2 JP3218366B2 (en) | 2001-10-15 |
Family
ID=16814699
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP22449596A Expired - Fee Related JP3218366B2 (en) | 1996-08-07 | 1996-08-07 | Filtration equipment for solid-liquid separation of sewage, wastewater, etc. |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3218366B2 (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007325994A (en) * | 2006-06-06 | 2007-12-20 | Kurita Water Ind Ltd | Filtering device |
CN102553318A (en) * | 2012-02-04 | 2012-07-11 | 侯明玉 | Clamping ring type centrifugal filtration and centripetal slag removal filter press |
CN105709482A (en) * | 2016-02-23 | 2016-06-29 | 哈尔滨恒通排水设备制造股份有限公司 | Straight-pushed solid-liquid separation device |
JP2016173195A (en) * | 2015-03-17 | 2016-09-29 | ゼネラルヒートポンプ工業株式会社 | Heat source water supply mechanism |
-
1996
- 1996-08-07 JP JP22449596A patent/JP3218366B2/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007325994A (en) * | 2006-06-06 | 2007-12-20 | Kurita Water Ind Ltd | Filtering device |
CN102553318A (en) * | 2012-02-04 | 2012-07-11 | 侯明玉 | Clamping ring type centrifugal filtration and centripetal slag removal filter press |
JP2016173195A (en) * | 2015-03-17 | 2016-09-29 | ゼネラルヒートポンプ工業株式会社 | Heat source water supply mechanism |
CN105709482A (en) * | 2016-02-23 | 2016-06-29 | 哈尔滨恒通排水设备制造股份有限公司 | Straight-pushed solid-liquid separation device |
Also Published As
Publication number | Publication date |
---|---|
JP3218366B2 (en) | 2001-10-15 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR100613118B1 (en) | Solid-liquid separation filter such as sewage and wastewater | |
JP4809345B2 (en) | Integrated permeable channel membrane | |
KR101912869B1 (en) | Integrated uf-sediment filter for water purification | |
JPH09141063A (en) | Hollow fiber membrane module | |
JP3218366B2 (en) | Filtration equipment for solid-liquid separation of sewage, wastewater, etc. | |
JPH10230145A (en) | Spiral membrane element | |
JP2000271457A (en) | Operation of spiral type membrane element and spiral type membrane module and spiral type membrane module | |
JPS6274408A (en) | Filter cartridge utilizing hollow yarn | |
JP4270644B2 (en) | Operating method and cleaning method of spiral membrane element and spiral membrane module | |
JPH1176764A (en) | Hollow yarn membrane module and its production | |
JP4454091B2 (en) | Spiral membrane module and spiral membrane element loading method | |
JP4107724B2 (en) | Spiral membrane element | |
JPH10230140A (en) | Spiral membrane element | |
JP4882173B2 (en) | Hollow fiber membrane module | |
JP2004081942A (en) | Filtering method using ceramic membrane module | |
JPH1015319A (en) | Filter material for solid-liquid separation of sewage and waste water or the like | |
JP2951189B2 (en) | Hollow fiber membrane module | |
KR20010086098A (en) | Purifying device for liquid | |
KR101361156B1 (en) | Laminated disk filter and filter unit using the same | |
JP2003144862A (en) | Method for manufacturing element assembly and element assembly | |
JPH10180053A (en) | Spiral type membrane element | |
GB2351677A (en) | Edge filter with filament wound around cage | |
JPH06277463A (en) | Membrane separation device | |
JPH11137974A (en) | Spiral membrane element | |
JP2000271456A (en) | Spiral type membrane element and method for operating and washing spiral type membrane module |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090810 Year of fee payment: 8 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20100810 Year of fee payment: 9 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20100810 Year of fee payment: 9 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20110810 Year of fee payment: 10 |
|
LAPS | Cancellation because of no payment of annual fees |