JPH10113510A - Filter - Google Patents

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Publication number
JPH10113510A
JPH10113510A JP8266047A JP26604796A JPH10113510A JP H10113510 A JPH10113510 A JP H10113510A JP 8266047 A JP8266047 A JP 8266047A JP 26604796 A JP26604796 A JP 26604796A JP H10113510 A JPH10113510 A JP H10113510A
Authority
JP
Japan
Prior art keywords
water
projections
water passage
supply port
hard
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
JP8266047A
Other languages
Japanese (ja)
Inventor
Kazutoshi Kaihara
和年 貝原
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.)
Koyo Giken KK
Original Assignee
Koyo Giken KK
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 Koyo Giken KK filed Critical Koyo Giken KK
Priority to JP8266047A priority Critical patent/JPH10113510A/en
Publication of JPH10113510A publication Critical patent/JPH10113510A/en
Pending legal-status Critical Current

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  • Filtration Of Liquid (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide an apparatus which removes solid components contained in raw water efficiently. SOLUTION: In a cylindrical container having a raw water supply port 2 and a treated water discharge outlet 3, numbers of rigid plates 4 are laminated to form water passage spaces 9 between the plates 4. In the space 9, a large number of projections 8 are formed on the surface of each rigid plate 4 to make each projection interval 8, and each space 9 is formed to be wide on the port 2 side, to be narrowed toward the outlet 3, and to meander.

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、上水、中水、下水
中に含まれる固形分を取り除く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 for removing solids contained in tap water, intermediate water, and sewage.

【0002】[0002]

【従来の技術】源水供給口と処理水放出口とを備える筒
状の容器内に、多数の硬質板を相互の間に通水間隔を存
して多数積層して成る濾過装置は知られている(特公平
7−61405号公報)。
2. Description of the Related Art There is known a filter device comprising a large number of hard plates stacked in a cylindrical container having a source water supply port and a treated water discharge port with a water gap therebetween. (Japanese Patent Publication No. 7-61405).

【0003】[0003]

【発明が解決しようとする課題】従来この主装置は、表
面を粗面(表面粗さ1μから100μ位の表面粗さのも
のを適宜選択)とした硬質板の多数を積層し、各硬質板
間に通水間隔を形成し、硬質板間を通過するとき固形分
を取り除いている。
Conventionally, this main apparatus has a structure in which a large number of hard plates having a rough surface (a surface roughness of approximately 1 μm to 100 μm is appropriately selected) are laminated, and each hard plate is laminated. A water gap is formed between the plates to remove solids when passing between the hard plates.

【0004】しかし、源水に含まれる固形分の大きさは
一定しない。したがって、きわめて細かな粒子(固形
分)まで取除こうとすると、表面粗さをきわめて細かく
した硬質板を使用しなければならず、これによれば直ぐ
目詰まりして頻繁に固形分を洗い流す所謂逆洗を行なわ
なければならず、作業能率がきわめて悪いという不具合
を生じ、また表面粗さの粗い硬質板を使用すれば、細か
な粒子を取除くことが出来なくなると言う不具合を生ず
る。
[0004] However, the size of the solid content contained in the source water is not constant. Therefore, in order to remove very fine particles (solid content), a hard plate having a very fine surface roughness must be used. Backwashing must be performed, resulting in a problem that the working efficiency is extremely poor, and a problem that it is impossible to remove fine particles if a hard plate having a rough surface is used.

【0005】しかも、長期間の使用で、硬質板間に固形
分が付着し、濾過機能が下がった場合、処理水放出口か
ら圧力水を注入して固形分を洗い流す(逆洗)作業を行
う場合も、単に硬質板の表面を粗面としただけのもので
は、充分に洗い流すことが難しいという不具合がある。
[0005] In addition, when solids adhere between the hard plates due to long-term use and the filtering function is lowered, pressure water is injected from the treated water discharge port to wash out the solids (backwashing). Also in this case, there is a problem that it is difficult to sufficiently wash out the hard plate simply by making the surface of the hard plate rough.

【0006】本発明はかかる不具合のない濾過装置を提
供することを課題とする。
[0006] It is an object of the present invention to provide a filtration device free from such a problem.

【0007】[0007]

【課題を解決するための手段】本願の請求項1記載の発
明は、源水供給口と処理水放出口とを備える筒状の容器
内に、多数の硬質板を積層して相互の間に通水間隔を形
成して成る濾過装置において、各硬質板の表面に多数の
突起を設けて各突起間に前記通水間隔を形成し、各通水
間隔は源水供給口側で広く処理水放出口側に至るに従い
漸次狭くすると共に、前記突起によって蛇行する通水間
隔が形成されるようにしたことを特徴とし、かかる構成
を備えることで、各通水間隔に源水を供給するとき、源
水供給口に近い突起の裏側の流れが澱むところ粒子の大
きい固形分が付着残存し、源水供給口から離れた突起の
裏側の流れが澱むところに細かい粒子が付着して、源水
に含まれる固形分を取除くことができる。
According to the first aspect of the present invention, a large number of hard plates are laminated in a cylindrical container having a source water supply port and a treated water discharge port. In a filtration device having a water passage interval, a number of projections are provided on the surface of each hard plate to form the water passage interval between the projections, and each water passage interval is wide at the source water supply port side. With gradually narrowing as it reaches the discharge port side, it is characterized in that a meandering water passage interval is formed by the protrusion, by providing such a configuration, when supplying source water to each water passage interval, When the flow on the back side of the protrusion near the source water supply port stagnates, large solids of particles adhere and remain, and fine particles adhere on the place where the flow on the back side of the protrusion distant from the source water supply port stagnates. The solids content can be removed.

【0008】本願の請求項2記載の発明は、請求項1記
載の発明において、硬質板を円板に構成すると共に、該
硬質板の中心位置に、容器の処理水放出口と連なる多孔
質パイプからなる通水管を設け、硬質板の周囲に源水供
給口からの源水を供給するようにしたことを特徴とし、
かかる構成を備えることで、源水供給口に近く、固形分
を多く含む源水が流れる部分の通水間隔が占める面積を
大きく取ることができる。
According to a second aspect of the present invention, in the first aspect of the present invention, the hard plate is formed into a circular plate, and a porous pipe connected to the treated water discharge port of the container is provided at the center of the hard plate. It is characterized by providing a water pipe consisting of, and supplying the source water from the source water supply port around the hard plate,
By providing such a configuration, it is possible to increase the area occupied by the water flow interval in a portion close to the source water supply port and in which the source water containing a large amount of solids flows.

【0009】[0009]

【発明の実施の形態】本発明実施の形態を図に示すもの
に付き説明する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described with reference to the drawings.

【0010】図面で1は、源水供給口2と処理水放出口
3とを備える筒状の容器、4は該容器1内に積層して収
容したガラス板等からなる硬質板を示す。
In the drawings, reference numeral 1 denotes a cylindrical container provided with a source water supply port 2 and a treated water discharge port 3, and reference numeral 4 denotes a hard plate made of a glass plate or the like housed in the container 1 stacked.

【0011】図示する実施の形態では、該容器1は、そ
の一端が閉じられ多端に開口1aを備える円筒型に構成
し、該容器1の外周に源水供給口2を備えてなり、該容
器1の一端を閉塞した端板の中央部に前記処理水放出口
3を設け、且つ該容器1の中央には、該源水供給口2に
連通する多孔質パイプ5を設け、該多孔質パイプ5に、
中心部に透孔4aを備えた円板型の前記硬質板4を、そ
の透孔4aで嵌合させて該容器1内に収容させた。
In the embodiment shown in the drawings, the container 1 is formed in a cylindrical shape having one end closed and an opening 1a at one end, and a source water supply port 2 provided on the outer periphery of the container 1. The treatment water discharge port 3 is provided at the center of an end plate having one end closed, and a porous pipe 5 communicating with the source water supply port 2 is provided at the center of the container 1. 5,
The disk-shaped hard plate 4 having a through hole 4a at the center was fitted in the through hole 4a and housed in the container 1.

【0012】6は該容器1の開口1aを閉じる蓋体を示
し、該蓋体6は基板6aとその内側に設けたゴムその他
の弾性体6bからなり、該弾性体6bは該容器1内に嵌
まり込み、その端面が容器1内に収容した硬質板4に当
たるようにした。
Reference numeral 6 denotes a lid for closing the opening 1a of the container 1. The lid 6 is composed of a substrate 6a and a rubber or other elastic body 6b provided inside the substrate 6a. It was fitted so that its end face hit the hard plate 4 housed in the container 1.

【0013】そして蓋体6は複数本の螺杆7で容器1に
締付けられるようにし、該螺杆7で蓋体6を締付けると
き、積層した硬質板4を弾性体6bで押して硬質板4同
志が圧接するようにした。
The lid 6 is fastened to the container 1 with a plurality of screw rods 7. When the lid 6 is tightened with the screw rod 7, the laminated hard plate 4 is pressed by the elastic body 6b to press the hard plates 4 together. I did it.

【0014】なお、弾性体6bの内端には、前記多孔質
パイプ5の一端が嵌入する凹部6cを設け、前記螺杆7
の締付けで、硬質板4同志を圧接させるとき、該多孔質
パイプ5によって邪魔されることなく蓋体6が移動でき
るようにした。
The elastic body 6b has an inner end provided with a recess 6c into which one end of the porous pipe 5 is fitted.
When the hard plates 4 are pressed against each other by the tightening, the lid 6 can be moved without being disturbed by the porous pipe 5.

【0015】各硬質板4の1側面には、各硬質板4の表
面に多数の突起8を設けて、各突起間8に通水間隔9を
形成し、各通水間隔9は源水供給口2側で広く処理水放
出口3側に至るに従い漸次狭くすると共に、通水間隔9
は該突起8によって蛇行するように形成させた。
On one side surface of each hard plate 4, a number of projections 8 are provided on the surface of each hard plate 4, and a water passage 9 is formed between the projections 8, and each water passage 9 is provided with a source water supply. At the mouth 2 side, the width gradually becomes narrower toward the treated water discharge port 3 side, and the water passage interval 9
Was formed so as to meander by the projections 8.

【0016】図示すものは、直径10cmの耐熱性の円
板型ガラスからなる硬質板4の一側面に、高さ20μの
多数の突起8を内外6段に環状に配設して、この硬質板
4を積層したとき、これら突起8間に前記通水間隔9を
形成した。
In the figure, a large number of protrusions 8 having a height of 20 μ are provided in a ring shape in six steps on the inner side and outer side on one side surface of a hard plate 4 made of heat-resistant disc-shaped glass having a diameter of 10 cm. When the plates 4 were stacked, the water gap 9 was formed between the projections 8.

【0017】これを更に説明すると、最外周に位置する
環状部分は、平均幅約4mmの突起8の多数をこれらの
間に平均幅約6mmの間隔を存して環状に配置して比較
的広い通水間隔9を形成し、その内側に位置する環状部
分は、平均幅4mmの突起8をそれらの間に平均幅約4
mmの間隔を存して多数配置して最外周に位置する環状
部分よりは狭い通水間隔9を形成し、更に内側に位置す
る環状部分は、平均幅約4mmの突起8をそれらの間に
平均幅約3.5mmの間隔を存して多数配置して更に狭
い通水間隔9を形成し、更にその内側に位置する環状部
分は、平均幅約4mmの突起8をそれらの間に平均幅約
3.5mmの間隔を存して多数配置し、更にその内側に
位置する環状部分は、平均幅約3mmの突起8をそれら
の間に平均幅約2.5mmの間隔を存して多数置して更
に狭い通水間隔9を形成し、最内周に位置する環状部分
は、平均幅約3mmの突起8をそれらの間に平均幅約
1.5mmの間隔を存して多数配置して最も狭い通水間
隔9を形成した。
To explain this further, the annular portion located at the outermost periphery is relatively wide by arranging a large number of projections 8 having an average width of about 4 mm in an annular shape with an interval of an average width of about 6 mm therebetween. An annular portion which forms a water passage space 9 and which is located inside has a projection 8 having an average width of 4 mm and an average width of about 4 mm therebetween.
A large number of holes are arranged at intervals of 1 mm to form a water passage space 9 that is narrower than the annular portion located at the outermost periphery, and the annular portion located further inside has a projection 8 with an average width of about 4 mm Numerous arrangements having an average width of about 3.5 mm are provided to form a narrower water passage space 9, and further, an annular portion located on the inside thereof has a projection 8 having an average width of about 4 mm between them. A large number of protrusions 8 are arranged at intervals of about 3.5 mm, and a plurality of protrusions 8 having an average width of about 3 mm are arranged at intervals of about 2.5 mm between them. Then, a narrower water passage space 9 is formed, and the annular portion located at the innermost periphery is formed by arranging a large number of protrusions 8 having an average width of about 3 mm with an average width of about 1.5 mm between them. The narrowest water passage 9 was formed.

【0018】なお、各環状に配した突起8は、その外周
に位置する突起8と重ならないように配置することで、
各突起8間に形成される通水間隔9が蛇行するように
し、環状に配した各突起8間(半径方向)には2mm程
度の間隔10を設けた。
The annularly arranged projections 8 are arranged so as not to overlap with the projections 8 located on the outer periphery thereof.
The water gap 9 formed between the projections 8 was meandered, and a gap 10 of about 2 mm was provided between the annularly arranged projections 8 (in the radial direction).

【0019】なお、この実施の形態ではガラス製の硬質
板4の表面の突起に相当する部分をマスキングした後、
エッチング液に漬けエッチング処理することで、前記し
た高さ20μ程度の高さの突起8の無数を硬質板4の一
側に形成した。
In this embodiment, after a portion corresponding to the projection on the surface of the hard plate 4 made of glass is masked,
By immersing in an etching solution and performing an etching process, innumerable projections 8 having a height of about 20 μ were formed on one side of the hard plate 4.

【0020】本濾過装置を用いて、固形物として活性炭
の粉末(50μ乃至1μの粒子を含む)を水に溶かした
ものを濾過したところ、真黒であった水が無色透明とな
った。このことは、極めて微細な活性炭の粉末まで本濾
過装置で取除かれたものと思われる。なお、このときの
注入速度は、0.2lh/cm2 であった。
Using this filtration apparatus, a solution obtained by dissolving activated carbon powder (including 50 μm to 1 μm particles) in water as a solid was filtered, and the black water became colorless and transparent. This seems to be because very fine activated carbon powder was removed by the present filtration device. The injection speed at this time was 0.2 lh / cm 2 .

【0021】そして、濾過した後の硬質板4を取出し
て、観察したところ、活性炭の粒子が、各突起8,8間
に形成される一部の通水間隔9並びに各突起8の裏側に
付着していることが確認され、顕微鏡で見たところ、各
突起8,8間に形成される通水間隔9に詰まった粒子程
大きく、また、外周に近い位置にある突起8の裏側に付
着した粒子程大きいことが確認された。これは、大きい
粒子程、源水供給口2に近い部分で通水間隔9間に詰ま
り、また重量のある大粒の粒子ほど早く突起8の裏側の
流れが澱む部分に滞積分離されたものと思われる。
The hard plate 4 after the filtration was taken out and observed. As a result, the activated carbon particles adhered to a part of the water gap 9 formed between the projections 8 and the back side of each projection 8. It was confirmed that the particles clogged in the water gap 9 formed between the projections 8 and 8 were larger and adhered to the back side of the projections 8 near the outer periphery. It was confirmed that the particles were larger. This is because the larger the particles, the closer to the source water supply port 2 becomes clogged between the water passage intervals 9, and the larger the heavier particles, the faster they accumulate and separate in the portion where the flow behind the projections 8 stagnates. Seem.

【0022】なお、本装置は長期の使用によって、固形
分が通水間隔9に滞積し濾過能力が低下する。このとき
は、前記螺杆7による締め付けを解いた後、処理水放出
口3から圧力水を注入することで、該通水間隔9に滞積
する固形分を洗い流す(逆洗する)ことが出来る。11
は容器1に設けた洗浄水の出口を示す。
In this device, the solid content is accumulated in the water passage interval 9 due to long-term use, and the filtration capacity is reduced. At this time, after the tightening by the screw 7 is released, by injecting the pressurized water from the treated water discharge port 3, it is possible to wash out (backwash) the solids accumulated in the water passage interval 9. 11
Denotes an outlet of the washing water provided in the container 1.

【0023】そして、逆洗するときは、通水間隔9が下
流程通水間隔9の幅が広いため、付着した固形分の洗い
流しが行い易いことも分った。
In backwashing, it was also found that the width of the water passage 9 was wider as the water passage 9 was downstream, so that the attached solids could be easily washed away.

【0024】なお、上述の硬質板4の直径は実験装置の
大きさを現すもので、この直径は処理する源水の量等に
応じて変えられるものであること申すまでもない。
The diameter of the hard plate 4 represents the size of the experimental apparatus, and it goes without saying that the diameter can be changed according to the amount of source water to be treated.

【0025】なお、上述の実施の形態では、硬質板4を
円板型とし、その外周から源水を供給し、硬質板4の中
心部に設けた多孔質パイプ5を介して処理水を取出すよ
うにしたが、これは、例えば方形の硬質板4の一側から
他側に向かって源水を流すようにし、各硬質板4の側面
に無数の突起によって形成した各通水間隔を、源水供給
口側で広く処理水放出口側に至るに従い漸次狭くするこ
とでも同様の濾過を行うことができる。
In the above-described embodiment, the hard plate 4 is formed in a disk shape, the source water is supplied from the outer periphery thereof, and the treated water is taken out through the porous pipe 5 provided at the center of the hard plate 4. However, this is because, for example, the source water flows from one side of the rectangular hard plate 4 toward the other side, and the water passage intervals formed by the countless projections on the side surface of each hard plate 4 The same filtration can be performed by gradually narrowing the water supply port side gradually toward the treated water discharge port side.

【0026】なお、この濾過装置は、図4に示す上水処
理装置において、河川から着水井Aに導かれて固形物を
沈殿分離した後の上水を混合槽Bに導いて該混合槽B内
に活性炭を投入した後の水をポンプPで本装置Cに導け
ば、固形物と共に活性炭を回収することができて、該活
性炭を再使用することが出来る。
The filtering device is the same as the tap water treatment device shown in FIG. 4 except that the tap water from the river to the landing well A where the solids are precipitated and separated is led to the mixing tank B, If the water after the activated carbon is introduced into the apparatus is guided to the device C by the pump P, the activated carbon can be recovered together with the solid matter, and the activated carbon can be reused.

【0027】因みに、従来の上水処理装置では、活性炭
を取除くために、凝集剤を混合槽B内にいれて、取除い
ていたため活性炭が凝集剤で固められ再使用することは
不可能であった。
In the conventional water treatment apparatus, the flocculant was put into the mixing tank B to remove the activated carbon and was removed. Therefore, the activated carbon was solidified with the flocculant and could not be reused. there were.

【0028】また、図5に示す下水処理装置において、
曝気槽Dで曝気処理した後の上水を本装置Cに導けば、
上水に含まれるきわめて微細な固形物を取除くことがで
きる。なお本装置Cを通過した上水は、その後必要な処
理を施された後河川等に放流される。
In the sewage treatment apparatus shown in FIG.
If the clean water after aeration treatment in the aeration tank D is led to the device C,
Very fine solids contained in tap water can be removed. After passing through the device C, the clean water is discharged to a river or the like after necessary treatment.

【0029】また、図6に示す中水処理装置において、
排水をスクリーン型のごみ除去装置Eで、挟雑物を除去
した後の排水を本装置Cに導けば、これに含まれる微細
な挟雑物(固形分)を取り除くことができる。なお、そ
の後該排水を処理槽Fで塩素消毒その他の処理をすれば
中水として使用出来る。なお、図6でGは中水を溜める
溜めのタンク、Hは上水タンクを示す。
In the intermediate water treatment apparatus shown in FIG.
If the wastewater is removed by a screen-type waste removal apparatus E to remove the contaminants, and the wastewater is guided to the apparatus C, fine contaminants (solid content) contained therein can be removed. After that, if the waste water is subjected to chlorine disinfection or other treatment in the treatment tank F, it can be used as intermediate water. In FIG. 6, G indicates a storage tank for storing the middle water, and H indicates a clean water tank.

【0030】なお、上述する実施の形態では、硬質板4
の一側のみに、突起8を設け他側は平坦面としたが、こ
れは両側に突起8を設けても良いこと申すまでもない。
In the above embodiment, the hard plate 4
The projections 8 are provided only on one side and the other side is a flat surface, but it goes without saying that the projections 8 may be provided on both sides.

【0031】また、上記実施の形態では、通水間隔9の
幅のみを変化させ、突起8の高さは一定としたが、突起
8の高さを水供給口2側即ち外周で高く処理水放出口3
側で低くすれば、より良好な濾過処理を行うことが出来
る。
In the above embodiment, only the width of the water passage space 9 is changed and the height of the projections 8 is kept constant. However, the height of the projections 8 is increased on the water supply port 2 side, that is, on the outer periphery. Outlet 3
If it is set lower on the side, better filtration can be performed.

【0032】[0032]

【発明の効果】 本願の請求項1記載の発明によるとき
は、各通水間隔に源水を供給するとき、源水供給口に近
い突起の裏側の流れが澱むところに粒子の大きい固形分
が付着残存し、源水供給口から離れた突起の裏側の流れ
が澱むところに細かい粒子が付着して、源水に含まれる
固形分を取除くことができ、しかも逆洗するときは、通
水間隔9が下流程広いため、付着した固形分の洗い流し
が行い易い。
According to the first aspect of the present invention, when the source water is supplied to each of the water passage intervals, a large solid content of particles is formed where the flow behind the protrusion near the source water supply port stagnates. Fine particles adhere to the place where the flow remains behind the protrusions remote from the source water supply port, and the solid content contained in the source water can be removed. Since the interval 9 is wider toward the downstream, it is easy to wash away the attached solids.

【0033】本願の請求項2記載の発明は、請求項1記
載の発明において、源水供給口に近く、固形分を多く含
む源水が流れる部分の通水間隔の面積を大きく取ること
ができて、より目詰まりし難くい濾過装置が得られる。
According to the invention of claim 2 of the present application, in the invention of claim 1, the area of the water flow interval near the source water supply port and where the source water containing a large amount of solids flows can be made large. As a result, a filter device that is less likely to be clogged can be obtained.

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

【図1】 本装置の截断側面図FIG. 1 is a cutaway side view of the apparatus.

【図2】 図1のA−A線截断面図FIG. 2 is a sectional view taken along line AA of FIG. 1;

【図3】 図2のB−B線截断面図FIG. 3 is a sectional view taken along line BB of FIG. 2;

【図4】 本装置を応用したシステムの一例を示す図FIG. 4 is a diagram showing an example of a system to which the present apparatus is applied.

【図5】 本装置を応用したシステムの他の例を示す図FIG. 5 is a diagram showing another example of a system to which the present apparatus is applied.

【図6】 更に本装置を応用したシステムの他の例を示
す図
FIG. 6 is a diagram showing another example of a system to which the present apparatus is further applied.

【符号の説明】[Explanation of symbols]

1 容器 2 源水供給口 3 処
理水放出口 4 硬質板 5 多孔質パイプ 6 蓋
体 8 突起 9 通水間隔
DESCRIPTION OF SYMBOLS 1 Container 2 Source water supply port 3 Treated water discharge port 4 Hard plate 5 Porous pipe 6 Lid 8 Projection 9 Water passage interval

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 源水供給口と処理水放出口とを備える筒
状の容器内に、多数の硬質板を積層して相互の間に通水
間隔を形成して成る濾過装置において、各硬質板の表面
に多数の突起を設けて各突起間に前記通水間隔を形成
し、各通水間隔は源水供給口側で広く処理水放出口側に
至るに従い漸次狭くすると共に、前記突起によって蛇行
する通水間隔が形成されるようにしたことを特徴とする
濾過装置。
1. A filter device comprising a plurality of hard plates laminated in a cylindrical container having a source water supply port and a treated water discharge port to form a water passage space therebetween. A large number of projections are provided on the surface of the plate to form the water passage intervals between the projections, and the water passage intervals are gradually widened on the source water supply port side and gradually reduced toward the treated water discharge port side. A filtering device, wherein a meandering water passage interval is formed.
【請求項2】 前記硬質板を円板に構成すると共に、該
硬質板の中心位置に設けた透孔に、容器の処理水放出口
と連なる多孔質パイプからなる通水管を挿通して、容器
内に多数の硬質板を積層した状態で取り付け、該硬質板
の周囲から源水を供給するようにしたことを特徴とする
請求項1記載の濾過装置。
2. The container according to claim 1, wherein said hard plate is formed as a circular plate, and a water pipe formed of a porous pipe connected to a treated water discharge port of the container is inserted into a through hole provided at a center position of said hard plate. 2. The filtering device according to claim 1, wherein a number of hard plates are mounted in a stacked state, and the source water is supplied from around the hard plates.
JP8266047A 1996-10-07 1996-10-07 Filter Pending JPH10113510A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8266047A JPH10113510A (en) 1996-10-07 1996-10-07 Filter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8266047A JPH10113510A (en) 1996-10-07 1996-10-07 Filter

Publications (1)

Publication Number Publication Date
JPH10113510A true JPH10113510A (en) 1998-05-06

Family

ID=17425662

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8266047A Pending JPH10113510A (en) 1996-10-07 1996-10-07 Filter

Country Status (1)

Country Link
JP (1) JPH10113510A (en)

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