JPS6313777Y2 - - Google Patents
Info
- Publication number
- JPS6313777Y2 JPS6313777Y2 JP1980172858U JP17285880U JPS6313777Y2 JP S6313777 Y2 JPS6313777 Y2 JP S6313777Y2 JP 1980172858 U JP1980172858 U JP 1980172858U JP 17285880 U JP17285880 U JP 17285880U JP S6313777 Y2 JPS6313777 Y2 JP S6313777Y2
- Authority
- JP
- Japan
- Prior art keywords
- filtration element
- filtration
- stock solution
- foreign matter
- scraper
- 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.)
- Expired
Links
- 238000001914 filtration Methods 0.000 claims description 44
- 239000011550 stock solution Substances 0.000 claims description 31
- 239000007787 solid Substances 0.000 claims description 20
- 239000000706 filtrate Substances 0.000 claims description 8
- 239000000243 solution Substances 0.000 claims description 8
- 239000007788 liquid Substances 0.000 claims description 5
- 238000004891 communication Methods 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000003780 insertion Methods 0.000 description 2
- 230000037431 insertion Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 230000002093 peripheral effect Effects 0.000 description 2
- 229910001369 Brass Inorganic materials 0.000 description 1
- 239000004809 Teflon Substances 0.000 description 1
- 229920006362 Teflon® Polymers 0.000 description 1
- 239000010951 brass Substances 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 239000008235 industrial water Substances 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
Description
【考案の詳細な説明】
本考案は工業用水、工業排液、下水、海水、原
油等濾過を必要とする液体(原液)中からゴミ、
土砂等の固形異物を取除くために使用され、且つ
堅型円筒状の濾過槽内に円筒状の濾過エレメント
を配し、濾過エレメントで濾過された濾液を濾過
エレメント内から外部に取り出せるように構成し
たストレーナの改良に関する。[Detailed description of the invention] This invention removes garbage from liquids (undiluted solutions) that require filtration, such as industrial water, industrial wastewater, sewage, seawater, and crude oil.
It is used to remove solid foreign matter such as earth and sand, and has a cylindrical filtration element placed inside a rigid cylindrical filtration tank, and is configured so that the filtrate filtered by the filtration element can be taken out from inside the filtration element. Regarding improvement of strainer.
この種ストレーナとしては本考案の考案者が開
発したものが公知である(実開昭55−95812号公
報)。このストレーナは濾過槽と濾過エレメント
との間に形成される原液流動室を仕切部材(スク
レーパを仕切部材として使用している実施例もあ
る。)で二分し、原液が原液流動室で1円運動を
行う間に濾過エレメント内に流入しうるように構
成したものである。従つてこの従来例によれば、
原液の円運動によるサイクロン現象により、原液
中の固形異物は遠心分離されると共に残りの固形
異物も濾過エレメントにより分離される。又濾過
エレメントの表面は原液の円運動流により洗わ
れ、固形異物が固着するのを防ぎ、スクレーパに
よる固形異物の掻き落としを容易にし、濾過エレ
メントの濾過性能をある程度良好な状態に保つこ
とができる。 A strainer of this type developed by the inventor of the present invention is known (Japanese Utility Model Application No. 55-95812). This strainer divides the liquid flow chamber formed between the filtration tank and the filtration element into two with a partition member (some examples use a scraper as a partition member), and the liquid moves in a circular motion in the liquid flow chamber. The structure is such that it can flow into the filtration element during the process. Therefore, according to this conventional example,
Due to the cyclone effect caused by the circular motion of the stock solution, solid foreign matter in the stock solution is centrifuged and the remaining solid foreign matter is also separated by the filter element. In addition, the surface of the filtration element is washed by the circular flow of the undiluted solution, preventing solid foreign matter from sticking to it, making it easier to scrape off the solid foreign matter with a scraper, and maintaining the filtration performance of the filtration element in a somewhat good state. .
しかし上記従来例においては、原液流動室を2
分する仕切部材により、原液の円運動が1円周内
に制限されるため、原液の強力な施回運動を期待
することができない。その結果、上記サイクロン
現象による固形異物の遠心分離及び原液流動によ
る濾過エレメント表面の洗浄において今1つの性
能に劣るという問題があつた。 However, in the above conventional example, two stock solution flow chambers are used.
Since the dividing member restricts the circular motion of the stock solution within one circumference, it is not possible to expect a strong swirling motion of the stock solution. As a result, there was a problem that the performance was inferior in terms of centrifugal separation of solid foreign matter by the cyclone phenomenon and cleaning of the surface of the filtration element by flowing the stock solution.
本考案は上記従来例の問題点を解決し、一層性
能のすぐれたストレーナを提供することを目的と
する。 It is an object of the present invention to solve the problems of the prior art described above and to provide a strainer with even better performance.
以下本考案を図面に示す実施例に基き具体的に
説明する。1は円筒状に形成した堅型の濾過槽
で、その側周壁2の上端近くに原液流入室3aを
設けると共に底板4の中央に濾液流出口5aを設
ける。原液流入口3aには濾過槽1の内周面の接
線方向を向く原液流入管3を接続し、原液が濾過
槽内で渦巻運動を行うように構成している。濾液
流出口5aには濾液を装置外に取出すための流出
管5を接続する。又濾過槽1の下方に異物貯留タ
ンク6を連設し、前記底板4の所定位置に穿設し
た連通孔7を通して、濾過槽1と濾過エレメント
8との間に形成される原液流動室9と異物貯留タ
ンク6とを連通する。10は異物貯留タンク6の
下端に設けた異物排出管で、適時開口し異物を排
出する。 The present invention will be explained in detail below based on embodiments shown in the drawings. Reference numeral 1 denotes a cylindrical, rigid filtration tank, in which a stock solution inflow chamber 3a is provided near the upper end of the side peripheral wall 2, and a filtrate outlet 5a is provided in the center of the bottom plate 4. The stock solution inlet 3a is connected to a stock solution inflow pipe 3 that faces in the tangential direction of the inner circumferential surface of the filtration tank 1, so that the stock solution moves in a spiral motion within the filtration tank. An outflow pipe 5 for taking out the filtrate out of the apparatus is connected to the filtrate outflow port 5a. Further, a foreign matter storage tank 6 is connected to the lower part of the filtration tank 1, and a stock solution flow chamber 9 formed between the filtration tank 1 and the filtration element 8 is connected through a communication hole 7 bored at a predetermined position in the bottom plate 4. It communicates with the foreign matter storage tank 6. Reference numeral 10 denotes a foreign matter discharge pipe provided at the lower end of the foreign matter storage tank 6, which is opened at appropriate times to discharge foreign matter.
前記濾過エレメント8は有頂無底円筒形状に形
成され、濾過槽1内に回転可能に配設される。こ
の濾過エレメント8の濾過部11は、例えば断面
三角状のウエツジワイヤー12を円筒状に捲装し
て構成することができ、ここで固形異物の通過を
阻止する。前記ウエツジワイヤー12の相隣接す
る部分間には隙間が形成され、この隙間を濾液の
みが通過するようにしてある。前記濾過部11は
この外、多孔筒などによつても構成しうることは
勿論である。 The filtration element 8 is formed into a cylindrical shape with a top and bottom, and is rotatably disposed within the filtration tank 1 . The filtration part 11 of the filtration element 8 can be constructed by, for example, wrapping a wedge wire 12 having a triangular cross section into a cylindrical shape, and prevents solid foreign matter from passing through. A gap is formed between adjacent portions of the wedge wire 12, and only the filtrate passes through this gap. It goes without saying that the filter section 11 can also be constructed of a porous tube or the like.
前記濾過エレメント8はその下端開口縁13が
底板4に水封状態に接触し、濾過槽1の頂板14
を貫いて配設される回転軸15の回転に伴つて回
転する。この回転軸15はモータ16で回転させ
ると好適であるが、手動によつて回転させてもよ
い。濾過エレメント8の回転方向は原液の流動方
向と同方向に設定できる外、逆方向に設定しても
よい。更に濾過エレメント8を固定構造とし、後
記スクレーパ18が濾過エレメント8に接触しつ
つ、その周囲を回動するように構成することも可
能である。 The filtration element 8 has its lower opening edge 13 in contact with the bottom plate 4 in a water-sealing state, and the top plate 14 of the filtration tank 1
It rotates with the rotation of a rotating shaft 15 disposed through the shaft. This rotating shaft 15 is preferably rotated by a motor 16, but may also be rotated manually. The rotation direction of the filter element 8 can be set in the same direction as the flow direction of the stock solution, or may be set in the opposite direction. Furthermore, it is also possible to configure the filtration element 8 to have a fixed structure so that the scraper 18 described later contacts the filtration element 8 and rotates around it.
18は濾過エレメント8に接触して固形異物を
分離するスクレーパである。このスクレーパ18
としてはナイフエツジ状に形成したテフロン(登
録商標)製棒状体、同様の形状の黄銅製棒状体な
どを使用し、濾過エレメント8の濾過部11に付
着する固形異物を掻き取りうるように構成するこ
とができる。又スクレーパ18としてブラシ状の
ものを使用し、前記濾過部11に付着する固形異
物を擦り取りうるように構成してもよい。19は
スクレーパ支持部材で、比較的細い堅杆で構成さ
れる主柱部20、スクレーパ挿着部21及び両者
20,21を連結する連結部22,22より成
り、スクレーパ挿着部21にスクレーパ18を着
脱自在に挿着することができる。主柱部20はそ
の上下端を頂板14及び底板4にネジ手段などに
より固定され、前記原液流動室9の適所に配され
る。スクレーパ支持部材19は原液の渦巻運動に
重大な支障を与えないように形成され、且つその
配設位置が定められている。図示する例におい
て、スクレーパ支持部材19の主柱部20とスク
レーパ挿着部21との間隔を置いて並設し、両者
間を原液が流動しうるように構成し、又スクレー
パ支持部材19を第2図に示す如く配したのは、
上記要請に応えるために外ならない。又図示する
例においてはスクレーパ18を前記連通孔7の近
傍に配してあり、スクレーパ18により掻き落さ
れた固形異物が連通孔7を通じて、異物貯留タン
ク6に導かれ易いように構成している。尚、23
は連通孔7の後方に立設したガイド板である。 18 is a scraper that comes into contact with the filter element 8 to separate solid foreign matter. This scraper 18
For example, a Teflon (registered trademark) rod shaped like a knife edge or a similarly shaped brass rod can be used to scrape off solid foreign matter adhering to the filtration part 11 of the filtration element 8. I can do it. Alternatively, a brush-like object may be used as the scraper 18 to scrape off solid foreign matter adhering to the filter section 11. Reference numeral 19 denotes a scraper support member, which is composed of a main column portion 20 made of a relatively thin hard rod, a scraper insertion portion 21, and connecting portions 22, 22 that connect both 20 and 21. can be removably inserted. The main column part 20 has its upper and lower ends fixed to the top plate 14 and the bottom plate 4 by screw means or the like, and is arranged at an appropriate position in the stock solution flow chamber 9. The scraper support member 19 is formed and positioned so as not to seriously impede the swirling motion of the stock solution. In the illustrated example, the main column part 20 and the scraper insertion part 21 of the scraper support member 19 are arranged side by side with a gap between them, so that the stock solution can flow between them, and the scraper support member 19 is The arrangement as shown in Figure 2 is as follows.
We have no choice but to respond to the above request. In the illustrated example, a scraper 18 is disposed near the communication hole 7, so that solid foreign matter scraped off by the scraper 18 is easily guided to the foreign matter storage tank 6 through the communication hole 7. . In addition, 23
is a guide plate erected at the rear of the communication hole 7.
次に本考案の作用を上記実施例を基き説明す
る。原液aは流入口3aより原液流動室9内に流
入し、ここで濾過槽1の内周面に沿つて渦巻運動
しつつ斜下方向に向け流動する。この渦巻運動
は、スクレーパ18及びスクレーパ支持部材19
により若干阻止される傾向にはあるが、概ねスム
ースに行われ、原液aは濾過エレメント8の周囲
を渦状に回りつつ、順次濾過エレメント8内に流
入する。 Next, the operation of the present invention will be explained based on the above embodiment. The stock solution a flows into the stock solution flow chamber 9 through the inlet port 3a, where it flows diagonally downward while swirling along the inner peripheral surface of the filtration tank 1. This spiral motion is caused by the scraper 18 and the scraper support member 19.
Although there is a tendency to be somewhat blocked by this, the process is generally smooth, and the stock solution a sequentially flows into the filtration element 8 while circulating in a spiral around the filtration element 8.
原液中の大部分の固形異物bは、原液の過巻運
動に起因するサイクロン現象により遠心分離さ
れ、原液流動室9の外周部を旋回しつつ降下した
後、ガイド板23に把えられて異物貯留タンク6
に送られる。 Most of the solid foreign matter b in the stock solution is centrifuged by the cyclone phenomenon caused by the overwinding movement of the stock solution, and after descending while swirling around the outer periphery of the stock solution flow chamber 9, the foreign matter is grasped by the guide plate 23. Storage tank 6
sent to.
遠心分離されない固形異物bは、原液aと共に
濾過エレメント8に送られるが、その濾過部11
に付着することにより分離される。濾過エレメン
ト8に付着した大部分の固形異物bは、スクレー
パ18で掻き落され、最終的には異物貯留槽6に
導かれる。又濾過エレメント8に付着した一部の
固形異物bは、原液の渦巻流による強い洗浄作用
を受けて、スクレーパ18で分離される前に、濾
過エレメント8より分離せしめられる。 The solid foreign matter b that is not centrifuged is sent to the filtration element 8 together with the stock solution a;
It is separated by adhering to. Most of the solid foreign matter b adhering to the filter element 8 is scraped off by the scraper 18 and finally led to the foreign matter storage tank 6. Further, some of the solid foreign matter b adhering to the filter element 8 is subjected to a strong cleaning action by the swirling flow of the stock solution, and is separated from the filter element 8 before being separated by the scraper 18.
他方濾過エレメント8内に流入した原液aはこ
こで濾過され、濾液cとなり、流出管5を通じて
外部に取り出される。 On the other hand, the stock solution a that has flowed into the filter element 8 is filtered here to become a filtrate c, which is taken out to the outside through the outflow pipe 5.
本考案のストレーナは上記の如き構成、作用を
有するので次のような効果を奏することができ
る。 Since the strainer of the present invention has the above-described structure and function, it can produce the following effects.
原液流動室において原液が渦巻運動し、且つ
この渦巻運動がスクレーパ及びスクレーパ支持
部材(比較的細い竪杆で主構成され、原液の渦
巻運動に対する抵抗を必要最少限にしている。)
により阻止されない構成となつているため、実
開昭55−95812号公報記載のストレーナに比較
し、原液には強烈なサイクロン現象が生じる。
この結果、濾過エレメントに達する固形異物の
量を減少させ、遠心分離される固形異物を増大
させることができる。従つて濾過エレメントの
負担が軽くなり、濾過効率を上げることができ
る。 In the stock solution flow chamber, the stock solution swirls, and this swirling motion causes a scraper and a scraper support member (mainly composed of a relatively thin vertical rod, minimizing resistance to the swirling motion of the stock solution).
Since the strainer is not blocked by the strainer, a strong cyclone phenomenon occurs in the stock solution compared to the strainer described in Japanese Utility Model Application Publication No. 55-95812.
As a result, the amount of solid foreign matter that reaches the filter element can be reduced, and the amount of solid foreign matter that can be centrifuged can be increased. Therefore, the load on the filtration element is reduced, and filtration efficiency can be increased.
原液の渦巻運動は実開昭55−95812号公報記
載のストレーナの原液を円運動に比較し、強烈
であるため、濾過エレメント表面の洗浄能力も
数段優れている。従つて、濾過エレメントに付
着した固形異物を積極的に剥離することができ
ると共に、スクレーパによる掻き落とし作業を
容易にする。 The swirling motion of the undiluted solution is more intense than the circular motion of the undiluted solution in the strainer described in Japanese Utility Model Application No. 55-95812, so the ability to clean the surface of the filtration element is much superior. Therefore, the solid foreign matter adhering to the filter element can be actively peeled off, and the scraping operation with the scraper is facilitated.
及びに述べた如く、濾過エレメントに付
着する固形異物の量を減少させることができる
ので、その減少分に比例して、濾液の質を高め
ることができる。 As described in and, since the amount of solid foreign matter adhering to the filter element can be reduced, the quality of the filtrate can be improved in proportion to the reduction.
図面は本考案の実施例を示し、第1図は本考案
の原理を示す斜視図、第2図は第1図の概略平面
図である。
1……濾過槽、3……原液流入管、8……濾過
エレメント、9……原液流動室、18……スクレ
ーパ、19……スクレーパ支持部材。
The drawings show an embodiment of the present invention, and FIG. 1 is a perspective view showing the principle of the present invention, and FIG. 2 is a schematic plan view of FIG. 1. DESCRIPTION OF SYMBOLS 1... Filter tank, 3... Stock solution inflow pipe, 8... Filtration element, 9... Stock solution flow chamber, 18... Scraper, 19... Scraper support member.
Claims (1)
トを配し、濾過エレメントで濾過された濾液を濾
過エレメント内から外部に取り出せるように構成
したストレーナにおいて、濾過槽と濾過エレメン
トとの間に形成される原液流動室の上部にその接
線方向に原液流入管を接続し、原液が渦巻運動を
行うように構成すると共に、原液流動室内に配さ
れ且つ濾過エレメントに相対回転可能に接触して
固形異物を分離するスクレーパを、原液の渦巻運
動に重大な支障を与えないように比較的細い堅杆
で主形成されたスクレーパ支持部材に取付けたこ
とを特徴とするストレーナ。 A strainer formed between the filtration tank and the filtration element in a strainer configured such that a cylindrical filtration element is arranged in a rigid cylindrical filtration tank and the filtrate filtered by the filtration element can be taken out from inside the filtration element. A undiluted solution inflow pipe is connected to the upper part of the undiluted solution flow chamber in the tangential direction thereof, so that the undiluted solution moves in a spiral motion, and the filtration element is disposed within the undiluted solution flow chamber and is relatively rotatably in contact with the filtration element to remove solid foreign matter. A strainer characterized in that a scraper for separating liquid is attached to a scraper support member mainly formed of a relatively thin rod so as not to seriously impede the swirling motion of the stock solution.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1980172858U JPS6313777Y2 (en) | 1980-12-02 | 1980-12-02 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1980172858U JPS6313777Y2 (en) | 1980-12-02 | 1980-12-02 |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5795214U JPS5795214U (en) | 1982-06-11 |
JPS6313777Y2 true JPS6313777Y2 (en) | 1988-04-19 |
Family
ID=29531138
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1980172858U Expired JPS6313777Y2 (en) | 1980-12-02 | 1980-12-02 |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6313777Y2 (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5927807U (en) * | 1982-08-14 | 1984-02-21 | 花井 安五郎 | Dual strainer |
JPH0326889Y2 (en) * | 1987-03-17 | 1991-06-11 | ||
JPH0454803Y2 (en) * | 1988-03-14 | 1992-12-22 | ||
JPH0698754A (en) * | 1992-09-24 | 1994-04-12 | Able Kk | Filter and method for cell culture |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4927970A (en) * | 1972-05-26 | 1974-03-12 |
-
1980
- 1980-12-02 JP JP1980172858U patent/JPS6313777Y2/ja not_active Expired
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4927970A (en) * | 1972-05-26 | 1974-03-12 |
Also Published As
Publication number | Publication date |
---|---|
JPS5795214U (en) | 1982-06-11 |
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